************************************************************************* ** ** ** OUTPUT FOR STREAM 1 ** ** ** ************************************************************************* STREAM NAME : VAPORIZING HC USER REF.NO. 1 MODE: 1 DIRECTION 1 UNITS SI gravity 9.810000E+00 [m/s^2] MASS FLOW 2.000000E+02 [kg/s] P INLET 1.252928E+06 [Pa] P OUTLET 1.200000E+06 [Pa] dP 5.292830E+04 [Pa] H INLET 6.175910E+05 [J/kg] POT.energy_in 2.049505E+02 [J/kg] KIN.energy_in 5.384611E+00 [J/kg] H OUTLET 7.229661E+05 [J/kg] POT.energy_out 1.569600E+02 [J/kg] KIN.energy_out 3.826951E+01 [J/kg] Q_transf 2.107200E+07 [W] HT-bal.ERROR = -2.524179E-01 [W] LAST INT. STEP 2.000000E+01 [s] Name Q_transf Q_total K_fric_Up K_fric_Dn Press H_mix Veloc T_abs T_degC WtFr_vap [W] [W] [-] [-] [Pa] [J/kg] [m/s] [K] [degC] [-] row08_in 0.00000E+00 0.00000E+00 8.94223E-01 8.94223E-01 1.25293E+06 6.17591E+05 3.28165E+00 5.57080E+02 2.83930E+02 0.00000E+00 row08_out 4.00804E+05 4.00804E+05 8.94223E-01 8.94223E-01 1.24850E+06 6.19597E+05 3.28500E+00 5.57870E+02 2.84720E+02 0.00000E+00 row07_out 5.24530E+05 9.25334E+05 8.94223E-01 8.88564E-01 1.24407E+06 6.22222E+05 3.28897E+00 5.58815E+02 2.85665E+02 0.00000E+00 row06_out 6.92006E+05 1.61734E+06 8.88564E-01 8.88564E-01 1.23966E+06 6.25684E+05 3.29259E+00 5.59711E+02 2.86561E+02 0.00000E+00 row05_out 9.21300E+05 2.53864E+06 8.88564E-01 8.88564E-01 1.23524E+06 6.30293E+05 3.29762E+00 5.60950E+02 2.87800E+02 0.00000E+00 row04_out 1.29621E+06 3.83485E+06 8.88564E-01 8.88564E-01 1.22689E+06 6.36771E+05 4.63667E+00 5.61409E+02 2.88259E+02 3.02732E-02 row03_out 5.71321E+05 4.40617E+06 7.49643E-01 7.49643E-01 1.22630E+06 6.39634E+05 3.59082E+00 5.61671E+02 2.88521E+02 4.28720E-02 row02_out 6.94634E+05 5.10081E+06 7.49643E-01 7.49643E-01 1.22260E+06 6.43108E+05 4.12951E+00 5.61702E+02 2.88552E+02 6.02320E-02 row01_out 1.06558E+06 6.16638E+06 7.49643E-01 9.79883E-01 1.21772E+06 6.48435E+05 4.94574E+00 5.61533E+02 2.88383E+02 8.63493E-02 X-OVR_out 3.77989E-03 6.16638E+06 9.79883E-01 7.49643E-01 1.21660E+06 6.48455E+05 4.97463E+00 5.61476E+02 2.88326E+02 8.72026E-02 R_tb1_out 2.09022E+06 8.25660E+06 7.49643E-01 7.49643E-01 1.24427E+06 6.59037E+05 5.70658E+00 5.63054E+02 2.89904E+02 1.13305E-01 R_tb2_out 2.09108E+06 1.03477E+07 7.49643E-01 7.49643E-01 1.20720E+06 6.69342E+05 7.91660E+00 5.61197E+02 2.88047E+02 1.80695E-01 R_tb3_out 2.68834E+06 1.30360E+07 7.20188E-01 7.20188E-01 1.22959E+06 6.82936E+05 5.28625E+00 5.62488E+02 2.89338E+02 2.22475E-01 R_tb4_out 2.67697E+06 1.57130E+07 7.20188E-01 7.20188E-01 1.20733E+06 6.96178E+05 6.62276E+00 5.61442E+02 2.88292E+02 2.91987E-01 R_tb5_out 2.67884E+06 1.83918E+07 7.20188E-01 7.20188E-01 1.21770E+06 7.09701E+05 7.46116E+00 5.62085E+02 2.88935E+02 3.41169E-01 R_tb6_out 2.68017E+06 2.10720E+07 7.20188E-01 0.00000E+00 1.20000E+06 7.22966E+05 8.74866E+00 5.61235E+02 2.88085E+02 4.06501E-01 Name Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap MW_vap Z_vap [J/kg/K] [W/m/K] [Pa*s] [kg/m^3] [N/m] [J/kg/K] [W/m/K] [Pa*s] [kg/kmol] [-] row08_in 3.03335E+03 1.08089E-01 1.00298E-04 5.91102E+02 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 row08_out 3.03162E+03 1.07875E-01 1.00210E-04 5.90499E+02 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 row07_out 3.02970E+03 1.07616E-01 1.00075E-04 5.89785E+02 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 row06_out 3.02771E+03 1.07360E-01 9.98160E-05 5.89139E+02 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 row05_out 3.02531E+03 1.07007E-01 9.94810E-05 5.88238E+02 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 row04_out 3.02261E+03 1.06248E-01 9.95463E-05 5.89101E+02 0.00000E+00 2.33913E+03 3.71521E-02 1.08805E-05 1.16118E+02 7.50268E-01 row03_out 3.02203E+03 1.05914E-01 9.95748E-05 5.89405E+02 0.00000E+00 2.33548E+03 3.71713E-02 1.08920E-05 1.16167E+02 7.50667E-01 row02_out 3.02017E+03 1.05710E-01 9.96320E-05 5.89785E+02 0.00000E+00 2.33214E+03 3.71701E-02 1.08968E-05 1.16216E+02 7.51288E-01 row01_out 3.01659E+03 1.05701E-01 9.97117E-05 5.90105E+02 0.00000E+00 2.32994E+03 3.71514E-02 1.08903E-05 1.16263E+02 7.52020E-01 X-OVR_out 3.01633E+03 1.05717E-01 9.97208E-05 5.90151E+02 0.00000E+00 2.32971E+03 3.71461E-02 1.08888E-05 1.16265E+02 7.52096E-01 R_tb1_out 3.01781E+03 1.05149E-01 9.95746E-05 5.89277E+02 0.00000E+00 2.33306E+03 3.72830E-02 1.09276E-05 1.16309E+02 7.51003E-01 R_tb2_out 3.00561E+03 1.05616E-01 9.98528E-05 5.90987E+02 0.00000E+00 2.32687E+03 3.71102E-02 1.08985E-05 1.16402E+02 7.53290E-01 R_tb3_out 3.00500E+03 1.05127E-01 9.97227E-05 5.90341E+02 0.00000E+00 2.33033E+03 3.72200E-02 1.09327E-05 1.16460E+02 7.52289E-01 R_tb4_out 2.99486E+03 1.05325E-01 9.99032E-05 5.91554E+02 0.00000E+00 2.32647E+03 3.71192E-02 1.09311E-05 1.16556E+02 7.53796E-01 R_tb5_out 2.99162E+03 1.05046E-01 9.98706E-05 5.91402E+02 0.00000E+00 2.32794E+03 3.71717E-02 1.09469E-05 1.16622E+02 7.53499E-01 R_tb6_out 2.98233E+03 1.05235E-01 1.00071E-04 5.92521E+02 0.00000E+00 2.32458E+03 3.70933E-02 1.09473E-05 1.16704E+02 7.54854E-01 Name Dens_mix V_sonic Cv_vap kappa elevation V_flow A_flow D_hydr dP_accel dP_grav [kg/m^3] [m/s] [J/kg/K] [-] [m] [m^3] [m^2] [m] [Pa] [Pa] row08_in 5.91102E+02 0.00000E+00 0.00000E+00 0.00000E+00 2.08920E+01 7.46470E-01 1.03104E-01 1.28100E-01 0.00000E+00 0.00000E+00 row08_out 5.90499E+02 0.00000E+00 0.00000E+00 0.00000E+00 2.06720E+01 7.46470E-01 1.03104E-01 1.28100E-01 6.49899E+00 -1.27507E+03 row07_out 5.89785E+02 0.00000E+00 0.00000E+00 0.00000E+00 2.04520E+01 7.46470E-01 1.03104E-01 1.28100E-01 7.71012E+00 -1.27364E+03 row06_out 5.89139E+02 0.00000E+00 0.00000E+00 0.00000E+00 2.02320E+01 7.46470E-01 1.03104E-01 1.28100E-01 7.00437E+00 -1.27218E+03 row05_out 5.88238E+02 0.00000E+00 0.00000E+00 0.00000E+00 2.00120E+01 7.46470E-01 1.03104E-01 1.28100E-01 9.77319E+00 -1.27051E+03 row04_out 4.18358E+02 2.03637E+02 2.26753E+03 1.03158E+00 1.97920E+01 7.46470E-01 1.03104E-01 1.28100E-01 2.59747E+03 -1.08622E+03 row03_out 3.73288E+02 2.03645E+02 2.26391E+03 1.03161E+00 1.95280E+01 1.08027E+00 1.49208E-01 1.54100E-01 -4.18098E+03 -1.02512E+03 row02_out 3.24593E+02 2.03611E+02 2.26059E+03 1.03165E+00 1.92640E+01 1.08027E+00 1.49208E-01 1.54100E-01 7.22067E+02 -9.03700E+02 row01_out 2.71023E+02 2.03541E+02 2.25843E+03 1.03167E+00 1.90000E+01 1.08027E+00 1.49208E-01 1.54100E-01 1.09409E+03 -7.71275E+02 X-OVR_out 2.69449E+02 2.03529E+02 2.25820E+03 1.03167E+00 1.69500E+01 2.39000E+00 1.49208E-01 1.54100E-01 3.87237E+01 -5.43458E+03 R_tb1_out 2.34889E+02 2.03770E+02 2.26157E+03 1.03161E+00 3.20000E+00 2.09040E+00 1.49208E-01 1.54100E-01 9.81105E+02 -3.40144E+04 R_tb2_out 1.69317E+02 2.03359E+02 2.25544E+03 1.03167E+00 1.69500E+01 2.09040E+00 1.49208E-01 1.54100E-01 2.96233E+03 2.72611E+04 R_tb3_out 1.47425E+02 2.03535E+02 2.25894E+03 1.03160E+00 3.20000E+00 3.54409E+00 2.56632E-01 2.02100E-01 -6.49177E+03 -2.13622E+04 R_tb4_out 1.17674E+02 2.03265E+02 2.25514E+03 1.03163E+00 1.69500E+01 3.54409E+00 2.56632E-01 2.02100E-01 1.04157E+03 1.78793E+04 R_tb5_out 1.04451E+02 2.03320E+02 2.25665E+03 1.03159E+00 3.20000E+00 3.54409E+00 2.56632E-01 2.02100E-01 6.53392E+02 -1.49809E+04 R_tb6_out 8.90795E+01 2.03097E+02 2.25333E+03 1.03162E+00 1.60000E+01 3.54409E+00 2.56632E-01 2.02100E-01 1.00338E+03 1.21506E+04 Name dPfric_up dPfric_dn M_flux Re_liq Re_vap Pr_liq Pr_vap HoldUpSum H-Up,TimC dT/dH [Pa] [Pa] [kg/m^2/s] [-] [-] [-] [-] [s] [s] [kg*K/J] row08_in 0.00000E+00 2.84618E+03 1.93979E+03 2.47750E+06 0.00000E+00 2.81469E+00 0.00000E+00 0.00000E+00 0.00000E+00 3.94787E-04 row08_out 2.84909E+03 2.84909E+03 1.93979E+03 2.47966E+06 0.00000E+00 2.81622E+00 0.00000E+00 2.20507E+00 2.20507E+00 3.94055E-04 row07_out 2.85253E+03 2.83448E+03 1.93979E+03 2.48300E+06 0.00000E+00 2.81740E+00 0.00000E+00 4.40769E+00 2.20262E+00 2.97551E-04 row06_out 2.83759E+03 2.83759E+03 1.93979E+03 2.48945E+06 0.00000E+00 2.81496E+00 0.00000E+00 6.60777E+00 2.20008E+00 3.01309E-04 row05_out 2.84194E+03 2.84194E+03 1.93979E+03 2.49783E+06 0.00000E+00 2.81253E+00 0.00000E+00 8.80496E+00 2.19719E+00 3.05078E-04 row04_out 3.99594E+03 3.99594E+03 1.93979E+03 2.49620E+06 2.28378E+07 2.83195E+00 6.85047E-01 1.06834E+01 1.87849E+00 9.94055E-05 row03_out 1.80408E+03 1.80408E+03 1.34041E+03 2.07439E+06 1.89642E+07 2.84114E+00 6.84343E-01 1.24723E+01 2.13798E+00 9.94013E-05 row02_out 2.07473E+03 2.07473E+03 1.34041E+03 2.07320E+06 1.89558E+07 2.84651E+00 6.83691E-01 1.43571E+01 1.88475E+00 1.54605E-05 row01_out 2.48481E+03 3.24798E+03 1.34041E+03 2.07154E+06 1.89671E+07 2.84566E+00 6.82982E-01 1.59656E+01 1.60857E+00 1.54523E-05 X-OVR_out 3.26696E+03 2.49933E+03 1.34041E+03 2.07136E+06 1.89697E+07 2.84524E+00 6.82918E-01 1.91949E+01 3.22932E+00 1.54504E-05 R_tb1_out 2.86707E+03 2.86707E+03 1.34041E+03 2.07440E+06 1.89024E+07 2.85783E+00 6.83814E-01 2.18306E+01 2.63567E+00 8.38668E-06 R_tb2_out 3.97741E+03 3.97741E+03 1.34041E+03 2.06862E+06 1.89528E+07 2.84161E+00 6.83356E-01 2.39430E+01 2.11238E+00 8.82922E-06 R_tb3_out 1.48348E+03 1.48348E+03 7.79326E+02 1.57940E+06 1.44065E+07 2.85052E+00 6.84493E-01 2.61214E+01 2.80640E+00 8.56187E-06 R_tb4_out 1.85855E+03 1.85855E+03 7.79326E+02 1.57654E+06 1.44086E+07 2.84070E+00 6.85114E-01 2.84703E+01 2.34884E+00 8.82766E-06 R_tb5_out 2.09383E+03 2.09383E+03 7.79326E+02 1.57706E+06 1.43877E+07 2.84423E+00 6.85570E-01 3.04383E+01 1.96808E+00 6.31370E-06 R_tb6_out 2.45514E+03 0.00000E+00 7.79326E+02 1.57390E+06 1.43872E+07 2.83600E+00 6.86052E-01 3.21531E+01 1.71472E+00 5.99939E-06 Name WK_fric_up WK_fric_dn . . . . . . . . [W] [W] . . . . . . . . row08_in 0.00000E+00 9.63009E+02 row08_out 9.64976E+02 9.64976E+02 row07_out 9.67312E+02 9.61191E+02 row06_out 9.63303E+02 9.63303E+02 row05_out 9.66253E+02 9.66253E+02 row04_out 1.91030E+03 1.91030E+03 row03_out 9.66590E+02 9.66590E+02 row02_out 1.27836E+03 1.27836E+03 row01_out 1.83366E+03 2.39683E+03 X-OVR_out 2.42491E+03 1.85514E+03 R_tb1_out 2.44121E+03 2.44121E+03 R_tb2_out 4.69820E+03 4.69820E+03 R_tb3_out 2.01253E+03 2.01253E+03 R_tb4_out 3.15881E+03 3.15881E+03 R_tb5_out 4.00921E+03 4.00921E+03 R_tb6_out 5.51225E+03 0.00000E+00 Name 1st_IerrP 1st_TerrP Lst_IerrP Lst_TerrP 1st_IerrH 1st_TerrH Lst_IerrH Lst_TerrH . . row08_in 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row08_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row07_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row06_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row05_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row04_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row03_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row02_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row01_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 X-OVR_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 R_tb1_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 R_tb2_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 R_tb3_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 R_tb4_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 R_tb5_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 R_tb6_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 ************************************************************************* ** ** ** OUTPUT FOR STREAM 2 ** ** ** ************************************************************************* STREAM NAME : Cooled fl-gas USER REF.NO. 2 MODE: 1 DIRECTION 1 UNITS SI gravity 9.810000E+00 [m/s^2] MASS FLOW 1.104960E+01 [kg/s] P INLET 1.014129E+05 [Pa] P OUTLET 1.013250E+05 [Pa] dP 8.786761E+01 [Pa] H INLET 2.376892E+06 [J/kg] POT.energy_in 2.943000E+01 [J/kg] KIN.energy_in 2.879664E+00 [J/kg] H OUTLET 4.394482E+05 [J/kg] POT.energy_out 2.049505E+02 [J/kg] KIN.energy_out 8.642717E+00 [J/kg] Q_transf -2.140597E+07 [W] HT-bal.ERROR = 4.097595E+00 [W] LAST INT. STEP 2.000000E+01 [s] Name Q_transf Q_total K_fric_Up K_fric_Dn Press H_mix Veloc T_abs T_degC WtFr_vap [W] [W] [-] [-] [Pa] [J/kg] [m/s] [K] [degC] [-] radiant_i 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.01413E+05 2.37689E+06 2.39986E+00 2.07853E+03 1.80538E+03 1.00000E+00 radiant_o -1.52046E+07 -1.52046E+07 0.00000E+00 0.00000E+00 1.01379E+05 1.00072E+06 1.27511E+00 1.10401E+03 8.30858E+02 1.00000E+00 row01_out -1.08470E+06 -1.62893E+07 0.00000E+00 2.38500E-01 1.01361E+05 9.02519E+05 6.53402E+00 1.03090E+03 7.57755E+02 1.00000E+00 row02_out -6.94634E+05 -1.69839E+07 2.38500E-01 2.38500E-01 1.01358E+05 8.39654E+05 6.23761E+00 9.84105E+02 7.10955E+02 1.00000E+00 row03_out -5.71321E+05 -1.75552E+07 2.38500E-01 5.50000E-01 1.01354E+05 7.87947E+05 5.99384E+00 9.45612E+02 6.72462E+02 1.00000E+00 row04_out -1.31212E+06 -1.88673E+07 5.50000E-01 5.50000E-01 1.01348E+05 6.69201E+05 5.38183E+00 8.55012E+02 5.81862E+02 1.00000E+00 row05_out -9.21300E+05 -1.97886E+07 5.50000E-01 5.50000E-01 1.01342E+05 5.85822E+05 4.93749E+00 7.84373E+02 5.11223E+02 1.00000E+00 row06_out -6.92005E+05 -2.04806E+07 5.50000E-01 5.50000E-01 1.01336E+05 5.23195E+05 4.60375E+00 7.31314E+02 4.58164E+02 1.00000E+00 row07_out -5.24529E+05 -2.10052E+07 5.50000E-01 5.50000E-01 1.01331E+05 4.75723E+05 4.35082E+00 6.91096E+02 4.17946E+02 1.00000E+00 row08_out -4.00804E+05 -2.14060E+07 5.50000E-01 0.00000E+00 1.01325E+05 4.39449E+05 4.15758E+00 6.60364E+02 3.87214E+02 1.00000E+00 Name Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap MW_vap Z_vap [J/kg/K] [W/m/K] [Pa*s] [kg/m^3] [N/m] [J/kg/K] [W/m/K] [Pa*s] [kg/kmol] [-] radiant_i 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.46532E+03 4.60538E-02 4.04322E-05 2.77500E+01 1.00000E+00 radiant_o 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.31917E+03 3.50781E-02 2.87705E-05 2.77500E+01 1.00000E+00 row01_out 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.30297E+03 3.41034E-02 2.77349E-05 2.77500E+01 1.00000E+00 row02_out 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.29259E+03 3.34794E-02 2.70719E-05 2.77500E+01 1.00000E+00 row03_out 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.28406E+03 3.29662E-02 2.65266E-05 2.77500E+01 1.00000E+00 row04_out 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.26286E+03 3.17582E-02 2.52430E-05 2.77500E+01 1.00000E+00 row05_out 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.24285E+03 3.08163E-02 2.42423E-05 2.77500E+01 1.00000E+00 row06_out 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.22781E+03 3.01089E-02 2.34907E-05 2.77500E+01 1.00000E+00 row07_out 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.21642E+03 2.95726E-02 2.29209E-05 2.77500E+01 1.00000E+00 row08_out 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.20771E+03 2.91628E-02 2.24855E-05 2.77500E+01 1.00000E+00 Name Dens_mix V_sonic Cv_vap kappa elevation V_flow A_flow D_hydr dP_accel dP_grav [kg/m^3] [m/s] [J/kg/K] [-] [m] [m^3] [m^2] [m] [Pa] [Pa] radiant_i 1.62843E-01 8.84779E+02 1.16570E+03 1.25703E+00 3.00000E+00 0.00000E+00 2.82743E+01 2.00000E+00 0.00000E+00 0.00000E+00 radiant_o 3.06483E-01 6.54208E+02 1.01956E+03 1.29387E+00 1.80000E+01 4.09973E+02 2.82743E+01 2.00000E+00 -4.39552E-01 3.45307E+01 row01_out 3.28160E-01 6.33336E+02 1.00335E+03 1.29862E+00 1.92640E+01 1.92045E+00 5.15324E+00 1.68300E-01 1.35119E+01 3.93474E+00 row02_out 3.43754E-01 6.19536E+02 9.92977E+02 1.30174E+00 1.95280E+01 1.92045E+00 5.15324E+00 1.68300E-01 -6.35563E-01 8.70075E-01 row03_out 3.57735E-01 6.07908E+02 9.84444E+02 1.30435E+00 1.97920E+01 1.92045E+00 5.15324E+00 1.68300E-01 -5.22694E-01 9.08372E-01 row04_out 3.95618E-01 5.79535E+02 9.63243E+02 1.31105E+00 2.00120E+01 1.95430E+00 5.18968E+00 1.41300E-01 -1.39330E+00 8.12943E-01 row05_out 4.31221E-01 5.56475E+02 9.43228E+02 1.31765E+00 2.02320E+01 1.95430E+00 5.18968E+00 1.41300E-01 -9.46070E-01 8.92242E-01 row06_out 4.62481E-01 5.38372E+02 9.28195E+02 1.32280E+00 2.04520E+01 1.95430E+00 5.18968E+00 1.41300E-01 -7.10563E-01 9.64393E-01 row07_out 4.89367E-01 5.24152E+02 9.16800E+02 1.32681E+00 2.06720E+01 1.95430E+00 5.18968E+00 1.41300E-01 -5.38540E-01 1.02714E+00 row08_out 5.12113E-01 5.12970E+02 9.08092E+02 1.32994E+00 2.08920E+01 1.95430E+00 5.18968E+00 1.41300E-01 -4.11448E-01 1.08070E+00 Name dPfric_up dPfric_dn M_flux Re_liq Re_vap Pr_liq Pr_vap HoldUpSum H-Up,TimC dT/dH [Pa] [Pa] [kg/m^2/s] [-] [-] [-] [-] [s] [s] [kg*K/J] radiant_i 0.00000E+00 0.00000E+00 3.90800E-01 0.00000E+00 1.93311E+04 0.00000E+00 1.28645E+00 0.00000E+00 0.00000E+00 6.87691E-04 radiant_o 0.00000E+00 0.00000E+00 3.90800E-01 0.00000E+00 2.71667E+04 0.00000E+00 1.08196E+00 8.70669E+00 8.70669E+00 7.44443E-04 row01_out 0.00000E+00 1.67072E+00 2.14420E+00 0.00000E+00 1.30114E+04 0.00000E+00 1.05965E+00 8.88134E+00 5.51514E-02 7.44443E-04 row02_out 1.59493E+00 1.59493E+00 2.14420E+00 0.00000E+00 1.33301E+04 0.00000E+00 1.04521E+00 8.93973E+00 5.83903E-02 7.44443E-04 row03_out 1.53260E+00 3.53430E+00 2.14420E+00 0.00000E+00 1.36041E+04 0.00000E+00 1.03323E+00 9.00069E+00 6.09603E-02 7.44443E-04 row04_out 3.15114E+00 3.15114E+00 2.12915E+00 0.00000E+00 1.19181E+04 0.00000E+00 1.00379E+00 9.06709E+00 6.66213E-02 8.47209E-04 row05_out 2.89097E+00 2.89097E+00 2.12915E+00 0.00000E+00 1.24101E+04 0.00000E+00 9.77713E-01 9.14021E+00 7.31199E-02 8.47209E-04 row06_out 2.69557E+00 2.69557E+00 2.12915E+00 0.00000E+00 1.28072E+04 0.00000E+00 9.57929E-01 9.21925E+00 7.90328E-02 8.47209E-04 row07_out 2.54747E+00 2.54747E+00 2.12915E+00 0.00000E+00 1.31255E+04 0.00000E+00 9.42811E-01 9.30342E+00 8.41748E-02 8.47209E-04 row08_out 2.43433E+00 0.00000E+00 2.12915E+00 0.00000E+00 1.33797E+04 0.00000E+00 9.31185E-01 9.39198E+00 8.85639E-02 8.47209E-04 Name WK_fric_up WK_fric_dn . . . . . . . . [W] [W] . . . . . . . . radiant_i 0.00000E+00 0.00000E+00 radiant_o 0.00000E+00 0.00000E+00 row01_out 0.00000E+00 5.62556E+01 row02_out 5.12674E+01 5.12674E+01 row03_out 4.73385E+01 1.09166E+02 row04_out 8.80114E+01 8.80114E+01 row05_out 7.40783E+01 7.40783E+01 row06_out 6.44026E+01 6.44027E+01 row07_out 5.75203E+01 5.75204E+01 row08_out 5.25242E+01 0.00000E+00 Name 1st_IerrP 1st_TerrP Lst_IerrP Lst_TerrP 1st_IerrH 1st_TerrH Lst_IerrH Lst_TerrH . . radiant_i 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 radiant_o 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row01_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row02_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row03_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row04_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row05_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row06_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row07_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 row08_out 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 ************************************************************************* ** ** ** OUTPUT FOR STREAM 3 ** ** ** ************************************************************************* STREAM NAME : Ambient air USER REF.NO. 3 MODE: 1 DIRECTION 1 UNITS SI gravity 9.810000E+00 [m/s^2] MASS FLOW 1.000000E+03 [kg/s] P INLET 1.013250E+05 [Pa] P OUTLET 1.013250E+05 [Pa] dP 9.157520E-08 [Pa] H INLET 1.597040E+04 [J/kg] POT.energy_in 0.000000E+00 [J/kg] KIN.energy_in 3.352838E-05 [J/kg] H OUTLET 1.630597E+04 [J/kg] POT.energy_out 0.000000E+00 [J/kg] KIN.energy_out 3.360342E-05 [J/kg] Q_transf 3.355657E+05 [W] HT-bal.ERROR = -1.942233E-02 [W] LAST INT. STEP 2.000000E+01 [s] Name Q_transf Q_total K_fric_Up K_fric_Dn Press H_mix Veloc T_abs T_degC WtFr_vap [W] [W] [-] [-] [Pa] [J/kg] [m/s] [K] [degC] [-] upstream 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.01325E+05 1.59704E+04 8.18882E-03 2.88506E+02 1.53562E+01 1.00000E+00 dwnstream 3.35566E+05 3.35566E+05 0.00000E+00 0.00000E+00 1.01325E+05 1.63060E+04 8.19798E-03 2.88829E+02 1.56788E+01 1.00000E+00 Name Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap MW_vap Z_vap [J/kg/K] [W/m/K] [Pa*s] [kg/m^3] [N/m] [J/kg/K] [W/m/K] [Pa*s] [kg/kmol] [-] upstream 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.02307E+03 2.41536E-02 1.71537E-05 2.89100E+01 1.00000E+00 dwnstream 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 0.00000E+00 1.02314E+03 2.41568E-02 1.71549E-05 2.89100E+01 1.00000E+00 Name Dens_mix V_sonic Cv_vap kappa elevation V_flow A_flow D_hydr dP_accel dP_grav [kg/m^3] [m/s] [J/kg/K] [-] [m] [m^3] [m^2] [m] [Pa] [Pa] upstream 1.22118E+00 3.39733E+02 7.35475E+02 1.39103E+00 0.00000E+00 0.00000E+00 1.00000E+05 1.00000E+03 0.00000E+00 0.00000E+00 dwnstream 1.21981E+00 3.39919E+02 7.35540E+02 1.39100E+00 0.00000E+00 1.00000E+03 1.00000E+05 1.00000E+03 9.15821E-08 0.00000E+00 Name dPfric_up dPfric_dn M_flux Re_liq Re_vap Pr_liq Pr_vap HoldUpSum H-Up,TimC dT/dH [Pa] [Pa] [kg/m^2/s] [-] [-] [-] [-] [s] [s] [kg*K/J] upstream 0.00000E+00 0.00000E+00 1.00000E-02 0.00000E+00 5.82963E+05 0.00000E+00 7.26580E-01 0.00000E+00 0.00000E+00 9.61538E-04 dwnstream 0.00000E+00 0.00000E+00 1.00000E-02 0.00000E+00 5.82925E+05 0.00000E+00 7.26577E-01 1.22050E+00 1.22050E+00 9.61538E-04 Name WK_fric_up WK_fric_dn . . . . . . . . [W] [W] . . . . . . . . upstream 0.00000E+00 0.00000E+00 dwnstream 0.00000E+00 0.00000E+00 Name 1st_IerrP 1st_TerrP Lst_IerrP Lst_TerrP 1st_IerrH 1st_TerrH Lst_IerrH Lst_TerrH . . upstream 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 dwnstream 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 0 0.00000E+00 ====================================================== ** ** ** WALL OUTPUT ** ** ** ====================================================== Wall number: 1 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st001i 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 1.7397E+05 1.7397E+05 1.7397E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.5981E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.6953E+02 5.6953E+02 1 inner surf 1.0052E+01 1.2818E-01 3.5624E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.6713E+02 5.6713E+02 2 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 1.5702E+04 1.5702E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 1.7307E+04 1.7307E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1820E+03 2.7952E-02 2.1199E-05 inner surf 3.0284E+03 1.0683E-01 9.9436E-05 5.8775E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 8.9641E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8187E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 1.7397E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.6953E+02 2.9638E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.6713E+02 2.9398E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 2 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st001o 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 2.2684E+05 2.2684E+05 2.2684E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.6180E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.7411E+02 5.7411E+02 3 inner surf 1.0052E+01 1.2818E-01 3.5578E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7098E+02 5.7098E+02 4 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 2.0474E+04 2.0474E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 2.2567E+04 2.2567E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1833E+03 2.8013E-02 2.1264E-05 inner surf 3.0277E+03 1.0690E-01 9.9463E-05 5.8793E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 8.9818E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8172E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 2.2684E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.7411E+02 3.0096E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.7098E+02 2.9783E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 3 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st002i 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 2.2684E+05 2.2684E+05 2.2684E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.6180E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.7411E+02 5.7411E+02 5 inner surf 1.0052E+01 1.2818E-01 3.5578E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7098E+02 5.7098E+02 6 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 2.0474E+04 2.0474E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 2.2567E+04 2.2567E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1833E+03 2.8013E-02 2.1264E-05 inner surf 3.0277E+03 1.0690E-01 9.9463E-05 5.8793E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 8.9818E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8172E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 2.2684E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.7411E+02 3.0096E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.7098E+02 2.9783E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 4 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st002o 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 2.9769E+05 2.9769E+05 2.9769E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.6432E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.8014E+02 5.8014E+02 7 inner surf 1.0052E+01 1.2818E-01 3.5528E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7604E+02 5.7604E+02 8 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 2.6870E+04 2.6870E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 2.9616E+04 2.9616E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1850E+03 2.8093E-02 2.1349E-05 inner surf 3.0270E+03 1.0696E-01 9.9491E-05 5.8810E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0051E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8156E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 2.9769E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.8014E+02 3.0699E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.7604E+02 3.0289E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 5 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st003i 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 2.9769E+05 2.9769E+05 2.9769E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.6432E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.8014E+02 5.8014E+02 9 inner surf 1.0052E+01 1.2818E-01 3.5528E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7604E+02 5.7604E+02 10 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 2.6870E+04 2.6870E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 2.9616E+04 2.9616E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1850E+03 2.8093E-02 2.1349E-05 inner surf 3.0270E+03 1.0696E-01 9.9491E-05 5.8810E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0051E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8156E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 2.9769E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.8014E+02 3.0699E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.7604E+02 3.0289E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 6 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st003o 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 3.9431E+05 3.9431E+05 3.9431E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.6752E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.8797E+02 5.8797E+02 11 inner surf 1.0052E+01 1.2818E-01 3.5493E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.8253E+02 5.8253E+02 12 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.5591E+04 3.5591E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 3.9228E+04 3.9228E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1872E+03 2.8198E-02 2.1460E-05 inner surf 3.0263E+03 1.0703E-01 9.9518E-05 5.8828E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0352E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8141E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 3.9431E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.8797E+02 3.1482E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.8253E+02 3.0938E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 7 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st004i 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 3.9431E+05 3.9431E+05 3.9431E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.6752E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.8797E+02 5.8797E+02 13 inner surf 1.0052E+01 1.2818E-01 3.5493E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.8253E+02 5.8253E+02 14 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.5591E+04 3.5591E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 3.9228E+04 3.9228E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1872E+03 2.8198E-02 2.1460E-05 inner surf 3.0263E+03 1.0703E-01 9.9518E-05 5.8828E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0352E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8141E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 3.9431E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.8797E+02 3.1482E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.8253E+02 3.0938E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 8 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st004o 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 5.2699E+05 5.2699E+05 5.2699E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.7158E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.9874E+02 5.9874E+02 15 inner surf 1.0052E+01 1.2818E-01 3.5443E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.9147E+02 5.9147E+02 16 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 4.7566E+04 4.7566E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 5.2427E+04 5.2427E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1902E+03 2.8341E-02 2.1612E-05 inner surf 3.0257E+03 1.0709E-01 9.9546E-05 5.8846E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0766E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8125E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 5.2699E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.9874E+02 3.2559E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.9147E+02 3.1832E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 9 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st005i 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 5.2699E+05 5.2699E+05 5.2699E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.7158E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.9874E+02 5.9874E+02 17 inner surf 1.0052E+01 1.2818E-01 3.5443E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.9147E+02 5.9147E+02 18 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 4.7566E+04 4.7566E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 5.2427E+04 5.2427E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1902E+03 2.8341E-02 2.1612E-05 inner surf 3.0257E+03 1.0709E-01 9.9546E-05 5.8846E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0766E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8125E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 5.2699E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.9874E+02 3.2559E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 5.9147E+02 3.1832E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 10 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 5" PT st005o 7.0645E-02 1.2855E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.3788E-05 7.6922E+05 7.6922E+05 7.6922E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.1079E+01 1.4129E-01 1.9508E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 6.1658E+02 6.1658E+02 19 inner surf 1.0052E+01 1.2818E-01 3.5410E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 6.0598E+02 6.0598E+02 20 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 6.9431E+04 6.9431E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 7.0716E-02CS inner surf 7.6526E+04 7.6526E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1953E+03 2.8579E-02 2.1865E-05 inner surf 3.0226E+03 1.0625E-01 9.9546E-05 5.8910E+02 0.0000E+00 2.3391E+03 3.7152E-02 1.0881E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.1450E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8022E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 6.5500E-03 7.6922E+05 1.3788E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.1658E+02 3.4343E+02 8.6474E+02 4.0816E+05 3.8755E+00 2 1 6.0598E+02 3.3283E+02 3.1316E+02 1.4781E+05 2.0379E+00 ****************************************** Wall number: 11 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st006i 8.4135E-02 1.5309E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.2511E-05 2.7191E+05 2.7191E+05 2.7191E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.3195E+01 1.6829E-01 5.6240E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.7920E+02 5.7920E+02 21 inner surf 1.2080E+01 1.5405E-01 2.9464E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7580E+02 5.7580E+02 22 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 2.0607E+04 2.0607E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 2.2509E+04 2.2509E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1847E+03 2.8081E-02 2.1336E-05 inner surf 3.0226E+03 1.0625E-01 9.9546E-05 5.8910E+02 0.0000E+00 2.3391E+03 3.7152E-02 1.0881E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0015E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 2.8022E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 2.7191E+05 1.2511E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.7920E+02 3.0605E+02 4.0657E+02 1.9190E+05 2.4008E+00 2 1 5.7580E+02 3.0265E+02 4.0657E+02 1.9190E+05 2.4008E+00 ****************************************** Wall number: 12 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st006o 8.4135E-02 1.5309E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.2511E-05 2.9941E+05 2.9941E+05 2.9941E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.3195E+01 1.6829E-01 5.6517E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 5.8261E+02 5.8261E+02 23 inner surf 1.2080E+01 1.5405E-01 2.5403E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7886E+02 5.7886E+02 24 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 2.2691E+04 2.2691E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 2.4786E+04 2.4786E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1857E+03 2.8126E-02 2.1384E-05 inner surf 3.0220E+03 1.0591E-01 9.9575E-05 5.8941E+02 0.0000E+00 2.3355E+03 3.7171E-02 1.0892E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0146E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 2.9941E+05 1.2511E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.8261E+02 3.0946E+02 4.0657E+02 1.9190E+05 2.4008E+00 2 1 5.7886E+02 3.0571E+02 4.0657E+02 1.9190E+05 2.4008E+00 ****************************************** Wall number: 13 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st007i 8.4135E-02 1.5309E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.2511E-05 3.2837E+05 3.2837E+05 3.2837E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.3195E+01 1.6829E-01 6.2297E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.7000E+00 5.9928E+02 5.7549E+02 25 inner surf 1.2080E+01 1.5405E-01 2.5403E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7302E+02 5.9255E+02 26 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 2.4886E+04 4.0755E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 2.7183E+04 4.4517E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1863E+03 2.8153E-02 2.1413E-05 inner surf 3.0220E+03 1.0591E-01 9.9575E-05 5.8941E+02 0.0000E+00 2.3355E+03 3.7171E-02 1.0892E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0224E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 3.2837E+05 1.2511E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.8463E+02 3.1148E+02 4.0657E+02 1.9190E+05 2.4008E+00 2 1 5.8053E+02 3.0738E+02 4.0657E+02 1.9190E+05 2.4008E+00 ****************************************** Wall number: 14 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st007o 8.4135E-02 1.5309E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.2511E-05 3.6627E+05 3.6627E+05 3.6627E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.3195E+01 1.6829E-01 6.2575E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.7000E+00 6.0363E+02 5.7711E+02 27 inner surf 1.2080E+01 1.5405E-01 2.5424E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7435E+02 5.9612E+02 28 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 2.7758E+04 4.5452E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.0320E+04 4.9648E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1870E+03 2.8189E-02 2.1451E-05 inner surf 3.0202E+03 1.0571E-01 9.9632E-05 5.8979E+02 0.0000E+00 2.3321E+03 3.7170E-02 1.0897E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0327E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 3.6627E+05 1.2511E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.8731E+02 3.1416E+02 4.0657E+02 1.9190E+05 2.4008E+00 2 1 5.8272E+02 3.0957E+02 4.0657E+02 1.9190E+05 2.4008E+00 ****************************************** Wall number: 15 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st008i 8.4135E-02 1.5309E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.2511E-05 4.4670E+05 4.4670E+05 4.4670E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.3195E+01 1.6829E-01 7.7296E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.9000E+00 6.1768E+02 5.7867E+02 29 inner surf 1.2080E+01 1.5405E-01 2.5424E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7564E+02 6.0766E+02 30 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.3854E+04 6.0687E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.6979E+04 6.6289E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1886E+03 2.8264E-02 2.1530E-05 inner surf 3.0202E+03 1.0571E-01 9.9632E-05 5.8979E+02 0.0000E+00 2.3321E+03 3.7170E-02 1.0897E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0543E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 4.4670E+05 1.2511E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.9293E+02 3.1978E+02 4.0657E+02 1.9190E+05 2.4008E+00 2 1 5.8734E+02 3.1419E+02 4.0657E+02 1.9190E+05 2.4008E+00 ****************************************** Wall number: 16 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st008o 8.4135E-02 1.5309E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 1.2511E-05 6.1888E+05 6.1888E+05 6.1888E+05 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.3195E+01 1.6829E-01 9.3942E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.9000E+00 6.3813E+02 5.8516E+02 31 inner surf 1.2080E+01 1.5405E-01 2.5500E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.8093E+02 6.2440E+02 32 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 4.6902E+04 8.3155E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 5.1232E+04 9.0830E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1919E+03 2.8421E-02 2.1697E-05 inner surf 3.0166E+03 1.0570E-01 9.9712E-05 5.9011E+02 0.0000E+00 2.3299E+03 3.7151E-02 1.0890E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0997E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 6.1888E+05 1.2511E-05 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.0474E+02 3.3159E+02 4.0657E+02 1.9190E+05 2.4008E+00 2 1 5.9699E+02 3.2384E+02 4.0657E+02 1.9190E+05 2.4008E+00 ****************************************** Wall number: 17 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st009i 8.4135E-02 2.0000E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 8.2539E-06 1.2840E-04 0.0000E+00 2.0778E-03 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 2.0000E+01 1.6829E-01 0.0000E+00 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 0.0000E+00 0.0000E+00 33 inner surf 1.8310E+01 1.5405E-01 2.5500E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 0.0000E+00 0.0000E+00 34 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 1.1348E-04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 inner surf 3.0166E+03 1.0570E-01 9.9712E-05 5.9011E+02 0.0000E+00 2.3299E+03 3.7151E-02 1.0890E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 1.2840E-04 8.2539E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.6153E+02 2.8838E+02 5.3115E+02 2.5070E+05 2.0693E+00 2 1 5.6153E+02 2.8838E+02 5.3115E+02 2.5070E+05 2.0693E+00 ****************************************** Wall number: 18 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st009o 8.4135E-02 2.0000E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 8.2539E-06 2.1406E-04 0.0000E+00 1.7021E-03 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 2.0000E+01 1.6829E-01 0.0000E+00 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 0.0000E+00 0.0000E+00 35 inner surf 1.8310E+01 1.5405E-01 2.5504E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 0.0000E+00 0.0000E+00 36 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 9.2958E-05 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 inner surf 3.0163E+03 1.0572E-01 9.9721E-05 5.9015E+02 0.0000E+00 2.3297E+03 3.7146E-02 1.0889E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 2.1406E-04 8.2539E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.6148E+02 2.8833E+02 5.3115E+02 2.5070E+05 2.0693E+00 2 1 5.6148E+02 2.8833E+02 5.3115E+02 2.5070E+05 2.0693E+00 ****************************************** Wall number: 19 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st010i 8.4135E-02 2.9614E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 5.5743E-06 1.0466E+06 1.0466E+06 1.0466E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 2.9614E+01 1.6829E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.3198E+02 5.7588E+02 37 inner surf 2.7111E+01 1.5405E-01 2.5504E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7330E+02 6.1934E+02 38 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.5342E+04 7.6545E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.8604E+04 8.3611E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1889E+03 2.8278E-02 2.1546E-05 inner surf 3.0163E+03 1.0572E-01 9.9721E-05 5.9015E+02 0.0000E+00 2.3297E+03 3.7146E-02 1.0889E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0585E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 1.0466E+06 5.5743E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.9403E+02 3.2088E+02 7.8647E+02 3.7121E+05 2.0693E+00 2 1 5.8819E+02 3.1504E+02 7.8647E+02 3.7121E+05 2.0693E+00 ****************************************** Wall number: 20 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st010o 8.4135E-02 2.9614E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 5.5743E-06 1.0436E+06 1.0436E+06 1.0436E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 2.9614E+01 1.6829E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.3331E+02 5.7741E+02 39 inner surf 2.7111E+01 1.5405E-01 2.5544E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7483E+02 6.2071E+02 40 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.5240E+04 7.6330E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.8493E+04 8.3376E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1893E+03 2.8298E-02 2.1566E-05 inner surf 3.0178E+03 1.0515E-01 9.9575E-05 5.8928E+02 0.0000E+00 2.3331E+03 3.7283E-02 1.0928E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0642E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 1.0436E+06 5.5743E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.9549E+02 3.2234E+02 7.8647E+02 3.7121E+05 2.0693E+00 2 1 5.8967E+02 3.1652E+02 7.8647E+02 3.7121E+05 2.0693E+00 ****************************************** Wall number: 21 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st011i 8.4135E-02 2.9614E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 5.5743E-06 1.0436E+06 1.0436E+06 1.0436E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 2.9614E+01 1.6829E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.3331E+02 5.7741E+02 41 inner surf 2.7111E+01 1.5405E-01 2.5544E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7483E+02 6.2071E+02 42 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.5240E+04 7.6330E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.8493E+04 8.3376E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1893E+03 2.8298E-02 2.1566E-05 inner surf 3.0178E+03 1.0515E-01 9.9575E-05 5.8928E+02 0.0000E+00 2.3331E+03 3.7283E-02 1.0928E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0642E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 1.0436E+06 5.5743E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.9549E+02 3.2234E+02 7.8647E+02 3.7121E+05 2.0693E+00 2 1 5.8967E+02 3.1652E+02 7.8647E+02 3.7121E+05 2.0693E+00 ****************************************** Wall number: 22 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 6" PT st011o 8.4135E-02 2.9614E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 5.5743E-06 1.0475E+06 1.0475E+06 1.0475E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 2.9614E+01 1.6829E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.3142E+02 5.7554E+02 43 inner surf 2.7111E+01 1.5405E-01 2.5793E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7295E+02 6.1877E+02 44 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.5371E+04 7.6636E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.8636E+04 8.3711E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1888E+03 2.8273E-02 2.1540E-05 inner surf 3.0056E+03 1.0562E-01 9.9853E-05 5.9099E+02 0.0000E+00 2.3269E+03 3.7110E-02 1.0899E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0569E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 7.1100E-03 1.0475E+06 5.5743E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.9361E+02 3.2046E+02 7.8647E+02 3.7121E+05 2.0693E+00 2 1 5.8777E+02 3.1462E+02 7.8647E+02 3.7121E+05 2.0693E+00 ****************************************** Wall number: 23 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 8" PT st012i 1.0954E-01 3.8576E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 4.8974E-06 1.3514E+06 1.3514E+06 1.3514E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.8576E+01 2.1908E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.4110E+02 5.7779E+02 45 inner surf 3.5695E+01 2.0272E-01 1.9600E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7484E+02 6.2692E+02 46 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.5032E+04 7.5065E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.7860E+04 8.1123E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1902E+03 2.8338E-02 2.1609E-05 inner surf 3.0056E+03 1.0562E-01 9.9853E-05 5.9099E+02 0.0000E+00 2.3269E+03 3.7110E-02 1.0899E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0757E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 8.1800E-03 1.3514E+06 4.8974E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 5.9849E+02 3.2534E+02 1.1847E+03 5.5918E+05 2.7385E+00 2 1 5.9187E+02 3.1872E+02 1.1847E+03 5.5918E+05 2.7385E+00 ****************************************** Wall number: 24 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 8" PT st012o 1.0954E-01 3.8576E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 4.8974E-06 1.3369E+06 1.3369E+06 1.3369E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.8576E+01 2.1908E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.5040E+02 5.8100E+02 47 inner surf 3.5695E+01 2.0272E-01 1.5847E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7807E+02 6.3650E+02 48 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.4657E+04 7.3559E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.7454E+04 7.9495E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1917E+03 2.8410E-02 2.1686E-05 inner surf 3.0050E+03 1.0513E-01 9.9723E-05 5.9034E+02 0.0000E+00 2.3303E+03 3.7220E-02 1.0933E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0965E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 8.1800E-03 1.3369E+06 4.8974E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.0391E+02 3.3076E+02 1.1847E+03 5.5918E+05 2.7385E+00 2 1 5.9736E+02 3.2421E+02 1.1847E+03 5.5918E+05 2.7385E+00 ****************************************** Wall number: 25 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 8" PT st013i 1.0954E-01 3.8576E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 4.8974E-06 1.3369E+06 1.3369E+06 1.3369E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.8576E+01 2.1908E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.5040E+02 5.8100E+02 49 inner surf 3.5695E+01 2.0272E-01 1.5847E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7807E+02 6.3650E+02 50 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.4657E+04 7.3559E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.7454E+04 7.9495E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1917E+03 2.8410E-02 2.1686E-05 inner surf 3.0050E+03 1.0513E-01 9.9723E-05 5.9034E+02 0.0000E+00 2.3303E+03 3.7220E-02 1.0933E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0965E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 8.1800E-03 1.3369E+06 4.8974E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.0391E+02 3.3076E+02 1.1847E+03 5.5918E+05 2.7385E+00 2 1 5.9736E+02 3.2421E+02 1.1847E+03 5.5918E+05 2.7385E+00 ****************************************** Wall number: 26 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 8" PT st013o 1.0954E-01 3.8576E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 4.8974E-06 1.3400E+06 1.3400E+06 1.3400E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.8576E+01 2.1908E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.4914E+02 5.7990E+02 51 inner surf 3.5695E+01 2.0272E-01 1.5990E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7696E+02 6.3521E+02 52 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.4738E+04 7.3762E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.7541E+04 7.9715E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1914E+03 2.8395E-02 2.1669E-05 inner surf 2.9949E+03 1.0532E-01 9.9903E-05 5.9155E+02 0.0000E+00 2.3265E+03 3.7119E-02 1.0931E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0920E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 8.1800E-03 1.3400E+06 4.8974E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.0274E+02 3.2959E+02 1.1847E+03 5.5918E+05 2.7385E+00 2 1 5.9618E+02 3.2303E+02 1.1847E+03 5.5918E+05 2.7385E+00 ****************************************** Wall number: 27 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 8" PT st014i 1.0954E-01 3.8576E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 4.8974E-06 1.3400E+06 1.3400E+06 1.3400E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.8576E+01 2.1908E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.4914E+02 5.7990E+02 53 inner surf 3.5695E+01 2.0272E-01 1.5990E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7696E+02 6.3521E+02 54 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.4738E+04 7.3762E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.7541E+04 7.9715E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1914E+03 2.8395E-02 2.1669E-05 inner surf 2.9949E+03 1.0532E-01 9.9903E-05 5.9155E+02 0.0000E+00 2.3265E+03 3.7119E-02 1.0931E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0920E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 8.1800E-03 1.3400E+06 4.8974E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.0274E+02 3.2959E+02 1.1847E+03 5.5918E+05 2.7385E+00 2 1 5.9618E+02 3.2303E+02 1.1847E+03 5.5918E+05 2.7385E+00 ****************************************** Wall number: 28 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 8" PT st014o 1.0954E-01 3.8576E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 4.8974E-06 1.3388E+06 1.3388E+06 1.3388E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.8576E+01 2.1908E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.4943E+02 5.8046E+02 55 inner surf 3.5695E+01 2.0272E-01 1.6087E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7753E+02 6.3550E+02 56 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.4705E+04 7.3715E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.7506E+04 7.9664E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1915E+03 2.8401E-02 2.1676E-05 inner surf 2.9916E+03 1.0505E-01 9.9871E-05 5.9140E+02 0.0000E+00 2.3279E+03 3.7172E-02 1.0947E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0938E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 8.1800E-03 1.3388E+06 4.8974E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.0321E+02 3.3006E+02 1.1847E+03 5.5918E+05 2.7385E+00 2 1 5.9665E+02 3.2350E+02 1.1847E+03 5.5918E+05 2.7385E+00 ****************************************** Wall number: 29 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 8" PT st015i 1.0954E-01 3.8576E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 4.8974E-06 1.3388E+06 1.3388E+06 1.3388E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.8576E+01 2.1908E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.4943E+02 5.8046E+02 57 inner surf 3.5695E+01 2.0272E-01 1.6087E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7753E+02 6.3550E+02 58 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.4705E+04 7.3715E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.7506E+04 7.9664E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1915E+03 2.8401E-02 2.1676E-05 inner surf 2.9916E+03 1.0505E-01 9.9871E-05 5.9140E+02 0.0000E+00 2.3279E+03 3.7172E-02 1.0947E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0938E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 8.1800E-03 1.3388E+06 4.8974E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.0321E+02 3.3006E+02 1.1847E+03 5.5918E+05 2.7385E+00 2 1 5.9665E+02 3.2350E+02 1.1847E+03 5.5918E+05 2.7385E+00 ****************************************** Wall number: 30 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] 8" PT st015o 1.0954E-01 3.8576E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 4.8974E-06 1.3414E+06 1.3414E+06 1.3414E+06 1.0000E-04 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.8576E+01 2.1908E-01 6.9300E+01 0.0000E+00 5.0000E-05 9.0000E-01 2.3400E+00 6.4838E+02 5.7955E+02 59 inner surf 3.5695E+01 2.0272E-01 1.6220E+03 3.0000E-04 5.0000E-05 9.0000E-01 1.0000E+00 5.7662E+02 6.3442E+02 60 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf 3.4772E+04 7.3886E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf 3.7578E+04 7.9849E+04 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.1912E+03 2.8388E-02 2.1662E-05 inner surf 2.9823E+03 1.0523E-01 1.0007E-04 5.9252E+02 0.0000E+00 2.3246E+03 3.7093E-02 1.0947E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 9.0901E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 CS_tube 1 CS 8.1800E-03 1.3414E+06 4.8974E-06 4.5000E+01 4.5000E+01 0 0 4.7200E+02 4.7200E+02 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 6.0225E+02 3.2910E+02 1.1847E+03 5.5918E+05 2.7385E+00 2 1 5.9568E+02 3.2253E+02 1.1847E+03 5.5918E+05 2.7385E+00 ****************************************** Wall number: 31 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] SHIELD-REFR 175 mm t 3.3255E+00 3.0350E+02 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 2.2770E-03 -2.2043E+05 -2.2062E+05 -2.1904E+05 1.0000E-02 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 3.0350E+02 6.6510E+00 1.5000E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 3.3715E+02 3.3715E+02 61 inner surf 2.8753E+02 6.3000E+00 7.0000E+01 3.3330E-01 5.0000E-05 9.0000E-01 1.0000E+00 8.3807E+02 8.3807E+02 62 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf -7.2693E+02 -7.2484E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf -7.6181E+02 -7.6511E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.0328E+03 2.4641E-02 1.7324E-05 inner surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.2584E+03 3.1548E-02 2.5019E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 7.2614E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 9.9798E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 REFRACTORY 1 LHV123 1.7500E-01 -2.2043E+05 2.2770E-03 2.2500E-01 2.9527E-01 0 0 1.0000E+03 1.0000E+03 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 3.3729E+02 6.4141E+01 5.4301E+04 5.4301E+07 1.2125E+05 2 1 8.3922E+02 5.6607E+02 5.4301E+04 5.4301E+07 1.2125E+05 ****************************************** Wall number: 32 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] HEARTH-ARCH 225 mm t 0.0000E+00 8.8446E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 9.0975E-03 -7.9911E+04 -7.9911E+04 -7.9900E+04 1.0000E-02 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 8.8446E+01 6.6510E+00 1.2000E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 3.6412E+02 3.6412E+02 63 inner surf 8.8446E+01 6.6510E+00 7.0000E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 1.0911E+03 1.0911E+03 64 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf -9.0351E+02 -9.0349E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf -9.0337E+02 -9.0349E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.0382E+03 2.4910E-02 1.7418E-05 inner surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.3163E+03 3.4906E-02 2.8588E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 7.2597E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 1.0780E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 REFRACTORY 1 LHV123 2.2500E-01 -7.9911E+04 9.0975E-03 2.2876E-01 3.3034E-01 0 0 1.0000E+03 1.0000E+03 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 3.6412E+02 9.0971E+01 2.0895E+04 2.0895E+07 2.0038E+05 2 1 1.0911E+03 8.1795E+02 2.0895E+04 2.0895E+07 2.0038E+05 ****************************************** Wall number: 33 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] SHOCK-ROWS 150 mm t 0.0000E+00 1.6200E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 3.3745E-02 -1.9121E+04 -1.9121E+04 -1.9120E+04 1.0000E-02 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.6200E+01 6.6510E+00 1.5000E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 3.6752E+02 3.6752E+02 65 inner surf 1.6200E+01 6.6510E+00 6.5000E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 1.0127E+03 1.0127E+03 66 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf -1.1803E+03 -1.1803E+03 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf -1.1802E+03 -1.1803E+03 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.0389E+03 2.4944E-02 1.7430E-05 inner surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.2989E+03 3.3861E-02 2.7478E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 7.2595E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 1.0541E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 REFRACTORY 1 LHV123 1.5000E-01 -1.9121E+04 3.3745E-02 2.2923E-01 3.1950E-01 0 0 1.0000E+03 1.0000E+03 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 3.6752E+02 9.4367E+01 2.5515E+03 2.5515E+06 9.1470E+04 2 1 1.0127E+03 7.3960E+02 2.5515E+03 2.5515E+06 9.1470E+04 ****************************************** Wall number: 34 WALL DATA RadOut Aout_ACT HeatFlxFxd TimeStep Wall Name [m] [m^2] [W] [s] FIN - TUBES 150 mm t 0.0000E+00 1.8500E+01 0.0000E+00 2.0000E+01 Rtotal Qwall_cnd Qsurf_out Qsurf_in Tolerance Conv Prt [W/K] [W] [W] [W] [-] T/F T/F 3.1082E-02 -1.5910E+04 -1.5910E+04 -1.5909E+04 1.0000E-02 T F SURFACE DATA Surface Name HX-Area[m2] Char Lth[m] U_c[W/m2K] R_f[Km2/W] Rghn_Abs[m] Emiss PeakToAv T_CloToProc T_FarFrPrc SolidNode outer surf 1.8500E+01 6.6510E+00 1.5000E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 3.4616E+02 3.4616E+02 67 inner surf 1.8500E+01 6.6510E+00 6.0000E+01 0.0000E+00 5.0000E-05 9.0000E-01 1.0000E+00 8.4068E+02 8.4068E+02 68 Surface Name Avg_Flux Max_Flux Loc. x y z Orient x y z ExtSurfVol ES-Material outer surf -8.6001E+02 -8.6000E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none inner surf -8.5995E+02 -8.6000E+02 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 none Surface Name FILM Cp_liq K_liq u_liq Dens_liq Srft_liq Cp_vap K_vap u_vap outer surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.0346E+03 2.4730E-02 1.7356E-05 inner surf 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 0.0000E+00 1.2588E+03 3.1567E-02 2.5040E-05 Surface Name FILM PR_film_lq Pr_film_vp PF TF PL TL HF TF HL TL outer surf 0.0000E+00 7.2608E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 inner surf 0.0000E+00 9.9852E-01 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 0 0.0000E+00 Layer Name id Mat'l Name Thickn HeatFlow Resist Cond1 Cond2 E1 E2 SpecHeat1 SpecHeat2 E1 E2 REFRACTORY 1 LHV123 1.5000E-01 -1.5910E+04 3.1082E-02 2.2624E-01 2.9548E-01 0 0 1.0000E+03 1.0000E+03 0 0 Solid Node Name Mode Tabs_K T_Celsius TotMass TotCapacit TimeConst 1 1 3.4616E+02 7.3013E+01 2.9138E+03 2.9138E+06 9.7551E+04 2 1 8.4068E+02 5.6753E+02 2.9138E+03 2.9138E+06 9.7551E+04 ****************************************** ******************************************************************* ** ** ** HEAT TRANSFER DETAILED OUTPUT ** ** ** ******************************************************************* ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 1 ================================ type = CONFRC name = Area01 A_node, Tfl_node, Htarget: 1 26 26 HEAT TRANSFER COEFFICIENT: 1.59809E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.6952873372426200E+02 Gas Temperature [K] 6.6036353994616024E+02 Gas Conductivity [W/m/K] 2.9162847199282138E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.338E+04 ______Pr_ = 9.312E-01 _____C1a_ = ______Re_^(-0.35) 3.595E-02 = 1.338E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 8.988E-03 = 0.25 / 1.338E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.805E+01 = 1.800E-01 * 2.916E-02 / 1.413E-01 * 1.338E+04^0.65 * 9.312E-01^0.33 * ( 6.604E+02 / 5.779E+02 )^0.25 hc = 3.179E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.805E+01 = 1.0 / ( 1.0 / ( 1.805E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.520E+01 = SQRT[ 2 * 1.805E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.766E-01 = tanh( 2.520E+01 * 2.615E-02 )/( 2.520E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.695E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.838E-01 = 1.0 - (1.0 / cosh( 2.520E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 5.862E+02 = 5.695E+02 + 1.838E-01 * ( 6.604E+02 - 5.695E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 5.779E+02 = 0.5 * ( 5.695E+02 + 5.862E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 5.862E+02 = 5.695E+02 + 1.000E+00 * 1.838E-01 * ( 6.604E+02 - 5.695E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.598E+01 = ( 8.766E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.805E+01 [W/(m^2.K)] ( 2.815E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.729E+02 = ( 8.766E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.805E+01 [W/(m^2.K)] ( 3.045E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.729E+02 * ( 6.604E+02 - 5.695E+02) = 1.740E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 3 ================================ type = CONFRC name = Area03 A_node, Tfl_node, Htarget: 3 25 26 HEAT TRANSFER COEFFICIENT: 1.61796E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.7411048170341019E+02 Gas Temperature [K] 6.9109572048026064E+02 Gas Conductivity [W/m/K] 2.9572609606403476E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.313E+04 ______Pr_ = 9.428E-01 _____C1a_ = ______Re_^(-0.35) 3.620E-02 = 1.313E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 9.049E-03 = 0.25 / 1.313E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.830E+01 = 1.800E-01 * 2.957E-02 / 1.413E-01 * 1.313E+04^0.65 * 9.428E-01^0.33 * ( 6.911E+02 / 5.850E+02 )^0.25 hc = 3.224E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.830E+01 = 1.0 / ( 1.0 / ( 1.830E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.538E+01 = SQRT[ 2 * 1.830E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.752E-01 = tanh( 2.538E+01 * 2.615E-02 )/( 2.538E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.741E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.859E-01 = 1.0 - (1.0 / cosh( 2.538E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 5.959E+02 = 5.741E+02 + 1.859E-01 * ( 6.911E+02 - 5.741E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 5.850E+02 = 0.5 * ( 5.741E+02 + 5.959E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 5.959E+02 = 5.741E+02 + 1.000E+00 * 1.859E-01 * ( 6.911E+02 - 5.741E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.618E+01 = ( 8.752E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.830E+01 [W/(m^2.K)] ( 2.850E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.750E+02 = ( 8.752E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.830E+01 [W/(m^2.K)] ( 3.082E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.750E+02 * ( 6.911E+02 - 5.741E+02) = 2.268E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 5 ================================ type = CONFRC name = Area05 A_node, Tfl_node, Htarget: 5 25 25 HEAT TRANSFER COEFFICIENT: 1.61796E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.7411048170341030E+02 Gas Temperature [K] 6.9109572048026064E+02 Gas Conductivity [W/m/K] 2.9572609606403476E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.313E+04 ______Pr_ = 9.428E-01 _____C1a_ = ______Re_^(-0.35) 3.620E-02 = 1.313E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 9.049E-03 = 0.25 / 1.313E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.830E+01 = 1.800E-01 * 2.957E-02 / 1.413E-01 * 1.313E+04^0.65 * 9.428E-01^0.33 * ( 6.911E+02 / 5.850E+02 )^0.25 hc = 3.224E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.830E+01 = 1.0 / ( 1.0 / ( 1.830E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.538E+01 = SQRT[ 2 * 1.830E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.752E-01 = tanh( 2.538E+01 * 2.615E-02 )/( 2.538E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.741E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.859E-01 = 1.0 - (1.0 / cosh( 2.538E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 5.959E+02 = 5.741E+02 + 1.859E-01 * ( 6.911E+02 - 5.741E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 5.850E+02 = 0.5 * ( 5.741E+02 + 5.959E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 5.959E+02 = 5.741E+02 + 1.000E+00 * 1.859E-01 * ( 6.911E+02 - 5.741E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.618E+01 = ( 8.752E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.830E+01 [W/(m^2.K)] ( 2.850E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.750E+02 = ( 8.752E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.830E+01 [W/(m^2.K)] ( 3.082E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.750E+02 * ( 6.911E+02 - 5.741E+02) = 2.268E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 7 ================================ type = CONFRC name = Area07 A_node, Tfl_node, Htarget: 7 24 25 HEAT TRANSFER COEFFICIENT: 1.64315E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.8014008234751873E+02 Gas Temperature [K] 7.3131405439364971E+02 Gas Conductivity [W/m/K] 3.0108854058581998E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.281E+04 ______Pr_ = 9.579E-01 _____C1a_ = ______Re_^(-0.35) 3.651E-02 = 1.281E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 9.127E-03 = 0.25 / 1.281E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.862E+01 = 1.800E-01 * 3.011E-02 / 1.413E-01 * 1.281E+04^0.65 * 9.579E-01^0.33 * ( 7.313E+02 / 5.944E+02 )^0.25 hc = 3.280E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.862E+01 = 1.0 / ( 1.0 / ( 1.862E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.560E+01 = SQRT[ 2 * 1.862E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.733E-01 = tanh( 2.560E+01 * 2.615E-02 )/( 2.560E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.801E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.887E-01 = 1.0 - (1.0 / cosh( 2.560E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 6.087E+02 = 5.801E+02 + 1.887E-01 * ( 7.313E+02 - 5.801E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 5.944E+02 = 0.5 * ( 5.801E+02 + 6.087E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 6.087E+02 = 5.801E+02 + 1.000E+00 * 1.887E-01 * ( 7.313E+02 - 5.801E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.643E+01 = ( 8.733E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.862E+01 [W/(m^2.K)] ( 2.894E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.777E+02 = ( 8.733E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.862E+01 [W/(m^2.K)] ( 3.130E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.777E+02 * ( 7.313E+02 - 5.801E+02) = 2.977E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 9 ================================ type = CONFRC name = Area09 A_node, Tfl_node, Htarget: 9 24 24 HEAT TRANSFER COEFFICIENT: 1.64315E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.8014008234751873E+02 Gas Temperature [K] 7.3131405439364971E+02 Gas Conductivity [W/m/K] 3.0108854058581998E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.281E+04 ______Pr_ = 9.579E-01 _____C1a_ = ______Re_^(-0.35) 3.651E-02 = 1.281E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 9.127E-03 = 0.25 / 1.281E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.862E+01 = 1.800E-01 * 3.011E-02 / 1.413E-01 * 1.281E+04^0.65 * 9.579E-01^0.33 * ( 7.313E+02 / 5.944E+02 )^0.25 hc = 3.280E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.862E+01 = 1.0 / ( 1.0 / ( 1.862E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.560E+01 = SQRT[ 2 * 1.862E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.733E-01 = tanh( 2.560E+01 * 2.615E-02 )/( 2.560E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.801E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.887E-01 = 1.0 - (1.0 / cosh( 2.560E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 6.087E+02 = 5.801E+02 + 1.887E-01 * ( 7.313E+02 - 5.801E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 5.944E+02 = 0.5 * ( 5.801E+02 + 6.087E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 6.087E+02 = 5.801E+02 + 1.000E+00 * 1.887E-01 * ( 7.313E+02 - 5.801E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.643E+01 = ( 8.733E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.862E+01 [W/(m^2.K)] ( 2.894E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.777E+02 = ( 8.733E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.862E+01 [W/(m^2.K)] ( 3.130E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.777E+02 * ( 7.313E+02 - 5.801E+02) = 2.977E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 11 ================================ type = CONFRC name = Area11 A_node, Tfl_node, Htarget: 11 23 24 HEAT TRANSFER COEFFICIENT: 1.67523E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.8796844655743041E+02 Gas Temperature [K] 7.8437292941047360E+02 Gas Conductivity [W/m/K] 3.0816305725472982E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.241E+04 ______Pr_ = 9.777E-01 _____C1a_ = ______Re_^(-0.35) 3.691E-02 = 1.241E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 9.228E-03 = 0.25 / 1.241E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.904E+01 = 1.800E-01 * 3.082E-02 / 1.413E-01 * 1.241E+04^0.65 * 9.777E-01^0.33 * ( 7.844E+02 / 6.068E+02 )^0.25 hc = 3.353E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.904E+01 = 1.0 / ( 1.0 / ( 1.904E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.588E+01 = SQRT[ 2 * 1.904E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.709E-01 = tanh( 2.588E+01 * 2.615E-02 )/( 2.588E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.880E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.922E-01 = 1.0 - (1.0 / cosh( 2.588E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 6.257E+02 = 5.880E+02 + 1.922E-01 * ( 7.844E+02 - 5.880E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 6.068E+02 = 0.5 * ( 5.880E+02 + 6.257E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 6.257E+02 = 5.880E+02 + 1.000E+00 * 1.922E-01 * ( 7.844E+02 - 5.880E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.675E+01 = ( 8.709E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.904E+01 [W/(m^2.K)] ( 2.950E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.812E+02 = ( 8.709E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.904E+01 [W/(m^2.K)] ( 3.191E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.812E+02 * ( 7.844E+02 - 5.880E+02) = 3.943E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 13 ================================ type = CONFRC name = Area13 A_node, Tfl_node, Htarget: 13 23 23 HEAT TRANSFER COEFFICIENT: 1.67523E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.8796844655743041E+02 Gas Temperature [K] 7.8437292941047360E+02 Gas Conductivity [W/m/K] 3.0816305725472982E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.241E+04 ______Pr_ = 9.777E-01 _____C1a_ = ______Re_^(-0.35) 3.691E-02 = 1.241E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 9.228E-03 = 0.25 / 1.241E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.904E+01 = 1.800E-01 * 3.082E-02 / 1.413E-01 * 1.241E+04^0.65 * 9.777E-01^0.33 * ( 7.844E+02 / 6.068E+02 )^0.25 hc = 3.353E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.904E+01 = 1.0 / ( 1.0 / ( 1.904E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.588E+01 = SQRT[ 2 * 1.904E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.709E-01 = tanh( 2.588E+01 * 2.615E-02 )/( 2.588E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.880E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.922E-01 = 1.0 - (1.0 / cosh( 2.588E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 6.257E+02 = 5.880E+02 + 1.922E-01 * ( 7.844E+02 - 5.880E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 6.068E+02 = 0.5 * ( 5.880E+02 + 6.257E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 6.257E+02 = 5.880E+02 + 1.000E+00 * 1.922E-01 * ( 7.844E+02 - 5.880E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.675E+01 = ( 8.709E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.904E+01 [W/(m^2.K)] ( 2.950E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.812E+02 = ( 8.709E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.904E+01 [W/(m^2.K)] ( 3.191E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.812E+02 * ( 7.844E+02 - 5.880E+02) = 3.943E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 15 ================================ type = CONFRC name = Area15 A_node, Tfl_node, Htarget: 15 22 23 HEAT TRANSFER COEFFICIENT: 1.71584E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.9873606566489309E+02 Gas Temperature [K] 8.5501194116300530E+02 Gas Conductivity [W/m/K] 3.1758159215506739E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.192E+04 ______Pr_ = 1.004E+00 _____C1a_ = ______Re_^(-0.35) 3.744E-02 = 1.192E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 9.360E-03 = 0.25 / 1.192E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.956E+01 = 1.800E-01 * 3.176E-02 / 1.413E-01 * 1.192E+04^0.65 * 1.004E+00^0.33 * ( 8.550E+02 / 6.239E+02 )^0.25 hc = 3.445E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.956E+01 = 1.0 / ( 1.0 / ( 1.956E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.623E+01 = SQRT[ 2 * 1.956E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.679E-01 = tanh( 2.623E+01 * 2.615E-02 )/( 2.623E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.987E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.966E-01 = 1.0 - (1.0 / cosh( 2.623E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 6.491E+02 = 5.987E+02 + 1.966E-01 * ( 8.550E+02 - 5.987E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 6.239E+02 = 0.5 * ( 5.987E+02 + 6.491E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 6.491E+02 = 5.987E+02 + 1.000E+00 * 1.966E-01 * ( 8.550E+02 - 5.987E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.716E+01 = ( 8.679E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.956E+01 [W/(m^2.K)] ( 3.022E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.856E+02 = ( 8.679E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.956E+01 [W/(m^2.K)] ( 3.269E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.856E+02 * ( 8.550E+02 - 5.987E+02) = 5.270E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 17 ================================ type = CONFRC name = Area17 A_node, Tfl_node, Htarget: 17 22 22 HEAT TRANSFER COEFFICIENT: 1.71584E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 5.9873606566489286E+02 Gas Temperature [K] 8.5501194116300530E+02 Gas Conductivity [W/m/K] 3.1758159215506739E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.192E+04 ______Pr_ = 1.004E+00 _____C1a_ = ______Re_^(-0.35) 3.744E-02 = 1.192E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 9.360E-03 = 0.25 / 1.192E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 1.956E+01 = 1.800E-01 * 3.176E-02 / 1.413E-01 * 1.192E+04^0.65 * 1.004E+00^0.33 * ( 8.550E+02 / 6.239E+02 )^0.25 hc = 3.445E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 1.956E+01 = 1.0 / ( 1.0 / ( 1.956E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.623E+01 = SQRT[ 2 * 1.956E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.679E-01 = tanh( 2.623E+01 * 2.615E-02 )/( 2.623E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 5.987E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 1.966E-01 = 1.0 - (1.0 / cosh( 2.623E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 6.491E+02 = 5.987E+02 + 1.966E-01 * ( 8.550E+02 - 5.987E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 6.239E+02 = 0.5 * ( 5.987E+02 + 6.491E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 6.491E+02 = 5.987E+02 + 1.000E+00 * 1.966E-01 * ( 8.550E+02 - 5.987E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.716E+01 = ( 8.679E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 1.956E+01 [W/(m^2.K)] ( 3.022E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 1.856E+02 = ( 8.679E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 1.956E+01 [W/(m^2.K)] ( 3.269E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 1.856E+02 * ( 8.550E+02 - 5.987E+02) = 5.270E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 19 ================================ type = CONFRC name = Area19 A_node, Tfl_node, Htarget: 19 21 22 HEAT TRANSFER COEFFICIENT: 1.95076E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] ESCOA TURB-X HF HEAT TRANSFER COEFFICIENT CALCULATION Bundle layout: STAGRD 1976 correlation Tube OD [m] 0.1412900000000000 Tube pitch [m] 0.2540000000000000 Row pitch [m] 0.2199700000000000 Fin height [m] 2.5399999999999999E-02 Fin thickness [m] 1.5000000000000000E-03 Nr of fins per meter [1/m] 1.5747999999999999E+02 Serration width [m] 8.0000000000000002E-03 Solid fin base height [m] 5.0000000000000001E-03 Nr of tube ROWS [-] 6 Nr of tubes/ROW [-] 8 Avg. Tube Temperature [K] 6.1658370819384402E+02 Gas Temperature [K] 9.4561236674242616E+02 Gas Conductivity [W/m/K] 3.2966164889899015E-02 H_radiant [W/m2/K] 0.0000000000000000E+000 Fin side fouling [K*m2/W] 0.0000000000000000E+000 A_bare / unit of L ______Ab_ = pi * ______OD_ 4.439E-01 = pi * 1.413E-01 outside diameter of fins _____ODf_ = ______OD_ + 2.0 * ______hf_ 1.921E-01 = 1.413E-01 + 2.0 * 2.540E-02 space between fins ______sf_ = 1.0 / _______nf_ - ______tf_ 4.850E-03 = 1.0 / 1.575E+02 - 1.500E-03 uncut fin height (solid lower part of fin) = 5.000E-03 [m] cut depth fin (height serrated part of fin) ____hser_ = ______hf_ - ____base_ 2.040E-02 = 2.540E-02 - 5.000E-03 diameter over top solid part fin (base cfin) _____ODb_ = ______OD_ + 2 * ____base_ 1.513E-01 = 1.413E-01 + 2 * 5.000E-03 number of serrations on circumference over top of solid part fin base diameter ____nser_ = pi * _____ODb_ / ______ws_ 5.941E+01 = pi * 1.513E-01 / 8.000E-03 Fin volume per unit of length ____VolF_ = ______nf_ * ______tf_ * ( pi/4 * ( _OD_base_^2 - ______OD_^2) + ( ______ws_ * ____hser_ ) * ____nser_ ) 2.833E-03 = 1.575E+02 * 1.500E-03 * ( pi/4 * ( 2.289E-02 - 1.996E-02 ) + ( 8.000E-03 * 2.040E-02 ) * 5.941E+01 ) A_prime (without fins) / unit of L _____Apo_ = pi * ______OD_ * (1.0 - ______nf_ * ______tf_) 3.390E-01 = pi * 1.413E-01 * (1.0 - 1.575E+02 * 1.500E-03) A_finned / unit of L _____Afo_ = ______nf_ * ( pi * 2.0 * ____base_ * ( ______OD_ + ____base_ ) + ____nser_ * ( 2.0 * ( ______ws_ + ______tf_ ) * ____hser_ + ______tf_ * ______ws_ ) ) 4.462E+00 = 1.575E+02 * ( pi * 2.0 * 5.000E-03 * ( 1.413E-01 + 5.000E-03 ) + 5.941E+01 * ( 2.0 * ( 8.000E-03 + 1.500E-03 ) * 2.040E-02 + 1.500E-03 * 8.000E-03 ) ) A_prime + A_finned / unit of L ______Ao_ = _____Apo_ + _____Afo_ 4.801E+00 = 3.390E-01 + 4.462E+00 _______b_ = ______hf_ + ______tf_ / 2.0 2.615E-02 = 2.540E-02 + 1.500E-03 / 2.0 ______Re_ = 1.360E+04 ______Pr_ = 1.033E+00 _____C1a_ = ______Re_^(-0.35) 3.575E-02 = 1.360E+04^(-0.35) C1b = 0.25 ______C1_ = 0.25 / ______Re_^0.35 (= C1a * C1b) 8.936E-03 = 0.25 / 1.360E+04^0.35 ______C3_ = 0.55 + 0.45 * exp(-0.35 * ______hf_ / ______sf_ ) 6.220E-01 = 0.55 + 0.45 * exp(-0.35 * 2.540E-02 / 4.850E-03 ) ______C5_ = 0.7 + (0.7-0.8*exp(-0.15 * _NR_ * _NR_) ) * (exp(-1.0 * ______Pl_ / ______Pt_) ) 9.929E-01 = 0.7 + (0.7-0.8*exp(-0.15 * 6 * 6) ) * (exp(-1.0 * 2.200E-01 / 2.540E-01) ) j = C1*C3*C5* [(df/OD)^0.5] * film_temp._correction j = C1a * FAC1 * film_temp._correction FAC1 contains constant and/or geometric info only. ____FAC1_ = _____C1b_ * ______C3_ * ______C5_ * SQRT( _____ODf_ / ______OD_ ) 1.800E-01 = 2.500E-01 * 6.220E-01 * 9.929E-01 * SQRT( 1.921E-01 / 1.413E-01 ) ______hc_ = ____FAC1_ * _______K_ / ______OD_ * ______Re_^0.65 * ______Pr_^0.33 * ( ______Tg_ / ______Ts_ )^0.25 (MODIFIED) 2.265E+01 = 1.800E-01 * 3.297E-02 / 1.413E-01 * 1.360E+04^0.65 * 1.033E+00^0.33 * ( 9.456E+02 / 6.531E+02 )^0.25 hc = 3.989E+00 Btu/hr/sqft/F ______ho_ = 1.0 / ( 1.0 / ( ______hc_ + ______hr_ ) + _____Rfo_ ) 2.265E+01 = 1.0 / ( 1.0 / ( 2.265E+01 + 0.000E+00 ) + 0.000E+00 ) _______b_ = ______hf_ + ______tf_ / 2.0 = 2.615E-02 _______m_ = SQRT[ 2 * ______ho_ * ( ______tf_ + ______ws_ ) / ( ______kf_ * ______tf_ * ______ws_ )] 2.823E+01 = SQRT[ 2 * 2.265E+01 * ( 1.500E-03 + 8.000E-03 ) / ( 4.500E+01 * 1.500E-03 * 8.000E-03 ) ] _______e_ = tanh( _______m_ * _______b_ )/( _______m_ * _______b_ ) 8.508E-01 = tanh( 2.823E+01 * 2.615E-02 )/( 2.823E+01 * 2.615E-02 ) FIN TIP TEMPERATURE CALCULATION __PkToAv_ = 1.000E+00 _____Ttm_ = 6.166E+02 _____eta_ = 1.0 - (1.0 / cosh( _______m_ * _______b_ )) 2.218E-01 = 1.0 - (1.0 / cosh( 2.823E+01 * 2.615E-02 )) _____Tft_ = ______Tt_ + _____eta_ * ( ______Tg_ - ______Tt_ ) 6.896E+02 = 6.166E+02 + 2.218E-01 * ( 9.456E+02 - 6.166E+02 ) ______Ts_ = 0.5 * ( ______Tt_ + _____Tft_ ) 6.531E+02 = 0.5 * ( 6.166E+02 + 6.896E+02 ) ____Tftm_ = _____Ttm_ + __PkToAv_ * _____eta_ * ( ______Tg_ - ______Tt_ ) 6.896E+02 = 6.166E+02 + 1.000E+00 * 2.218E-01 * ( 9.456E+02 - 6.166E+02 ) ____Xrat_ = ( _____Afo_ + _____Apo_ ) / ______Ab_ 1.082E+01 = ( 4.462E+00 + 3.390E-01 ) / 4.439E-01 ______he_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ao_ * ______ho_ 1.951E+01 = ( 8.508E-01 * 4.462E+00 + 3.390E-01 ) / 4.801E+00 * 2.265E+01 [W/(m^2.K)] ( 3.436E+00 Btu/hr/sqft/F ) _he_bare_ = ( _______e_ * _____Afo_ + _____Apo_ ) / ______Ab_ * ______ho_ 2.110E+02 = ( 8.508E-01 * 4.462E+00 + 3.390E-01 ) / 4.439E-01 * 2.265E+01 [W/(m^2.K)] ( 3.716E+01 Btu/hr/sqft/F ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.108E+01 * 2.110E+02 * ( 9.456E+02 - 6.166E+02) = 7.692E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 21 ================================ type = CONFRC name = Area21 A_node, Tfl_node, Htarget: 21 21 21 HEAT TRANSFER COEFFICIENT: 5.62402E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES FISHENDN VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.297E-02 6.000E-01 3.000E-01 / 9.456E+02 \ 0.000E+00 H_VAP = 1.500E+01 + 6.900E-01 x ---------- x 1.360E+04 x 1.033E+00 x ( --------- ) = 5.624E+01 1.683E-01 \ 5.792E+02 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 5.624E+01 = 1.0 / ( 1.0 / 5.624E+01 + 0.000E+00 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.320E+01 * 5.624E+01 * ( 9.456E+02 - 5.792E+02) = 2.719E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 23 ================================ type = CONFRC name = Area23 A_node, Tfl_node, Htarget: 23 20 21 HEAT TRANSFER COEFFICIENT: 5.65172E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES FISHENDN VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.348E-02 6.000E-01 3.000E-01 / 9.841E+02 \ 0.000E+00 H_VAP = 1.500E+01 + 6.900E-01 x ---------- x 1.333E+04 x 1.045E+00 x ( --------- ) = 5.652E+01 1.683E-01 \ 5.826E+02 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 5.652E+01 = 1.0 / ( 1.0 / 5.652E+01 + 0.000E+00 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.320E+01 * 5.652E+01 * ( 9.841E+02 - 5.826E+02) = 2.994E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 25 ================================ type = CONFRC name = Area25 A_node, Tfl_node, Htarget: 25 20 20 HEAT TRANSFER COEFFICIENT: 6.22969E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES FISHENDN VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.348E-02 6.000E-01 3.000E-01 / 9.841E+02 \ 0.000E+00 H_VAP = 2.800E+01 + 5.700E-01 x ---------- x 1.333E+04 x 1.045E+00 x ( --------- ) = 6.230E+01 1.683E-01 \ 5.846E+02 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 6.230E+01 = 1.0 / ( 1.0 / 6.230E+01 + 0.000E+00 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.320E+01 * 6.230E+01 * ( 9.841E+02 - 5.846E+02) = 3.284E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 27 ================================ type = CONFRC name = Area27 A_node, Tfl_node, Htarget: 27 19 20 HEAT TRANSFER COEFFICIENT: 6.25746E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES FISHENDN VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.410E-02 6.000E-01 3.000E-01 / 1.031E+03 \ 0.000E+00 H_VAP = 2.800E+01 + 5.700E-01 x ---------- x 1.301E+04 x 1.060E+00 x ( --------- ) = 6.257E+01 1.683E-01 \ 5.873E+02 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 6.257E+01 = 1.0 / ( 1.0 / 6.257E+01 + 0.000E+00 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.320E+01 * 6.257E+01 * ( 1.031E+03 - 5.873E+02) = 3.663E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 29 ================================ type = CONFRC name = Area29 A_node, Tfl_node, Htarget: 29 19 19 HEAT TRANSFER COEFFICIENT: 7.72958E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES FISHENDN VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.410E-02 6.000E-01 3.000E-01 / 1.031E+03 \ 0.000E+00 H_VAP = 5.000E+01 + 4.500E-01 x ---------- x 1.301E+04 x 1.060E+00 x ( --------- ) = 7.730E+01 1.683E-01 \ 5.929E+02 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 7.730E+01 = 1.0 / ( 1.0 / 7.730E+01 + 0.000E+00 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.320E+01 * 7.730E+01 * ( 1.031E+03 - 5.929E+02) = 4.467E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 31 ================================ type = CONFRC name = Area31 A_node, Tfl_node, Htarget: 31 18 19 HEAT TRANSFER COEFFICIENT: 9.39417E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES FISHENDN VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.508E-02 6.000E-01 3.000E-01 / 1.104E+03 \ 0.000E+00 H_VAP = 5.000E+01 + 4.500E-01 x ---------- x 2.717E+04 x 1.082E+00 x ( --------- ) = 9.394E+01 1.683E-01 \ 6.047E+02 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 9.394E+01 = 1.0 / ( 1.0 / 9.394E+01 + 0.000E+00 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.320E+01 * 9.394E+01 * ( 1.104E+03 - 6.047E+02) = 6.189E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 37 ================================ type = CONFRC name = Area37 A_node, Tfl_node, Htarget: 37 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.961E+01 * 6.930E+01 * ( 1.104E+03 - 5.940E+02) = 1.047E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 39 ================================ type = CONFRC name = Area39 A_node, Tfl_node, Htarget: 39 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.961E+01 * 6.930E+01 * ( 1.104E+03 - 5.955E+02) = 1.044E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 41 ================================ type = CONFRC name = Area41 A_node, Tfl_node, Htarget: 41 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.961E+01 * 6.930E+01 * ( 1.104E+03 - 5.955E+02) = 1.044E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 43 ================================ type = CONFRC name = Area43 A_node, Tfl_node, Htarget: 43 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.961E+01 * 6.930E+01 * ( 1.104E+03 - 5.936E+02) = 1.047E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 45 ================================ type = CONFRC name = Area45 A_node, Tfl_node, Htarget: 45 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.858E+01 * 6.930E+01 * ( 1.104E+03 - 5.985E+02) = 1.351E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 47 ================================ type = CONFRC name = Area47 A_node, Tfl_node, Htarget: 47 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.858E+01 * 6.930E+01 * ( 1.104E+03 - 6.039E+02) = 1.337E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 49 ================================ type = CONFRC name = Area49 A_node, Tfl_node, Htarget: 49 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.858E+01 * 6.930E+01 * ( 1.104E+03 - 6.039E+02) = 1.337E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 51 ================================ type = CONFRC name = Area51 A_node, Tfl_node, Htarget: 51 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.858E+01 * 6.930E+01 * ( 1.104E+03 - 6.027E+02) = 1.340E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 53 ================================ type = CONFRC name = Area53 A_node, Tfl_node, Htarget: 53 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.858E+01 * 6.930E+01 * ( 1.104E+03 - 6.027E+02) = 1.340E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 55 ================================ type = CONFRC name = Area55 A_node, Tfl_node, Htarget: 55 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.858E+01 * 6.930E+01 * ( 1.104E+03 - 6.032E+02) = 1.339E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 57 ================================ type = CONFRC name = Area57 A_node, Tfl_node, Htarget: 57 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.858E+01 * 6.930E+01 * ( 1.104E+03 - 6.032E+02) = 1.339E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 59 ================================ type = CONFRC name = Area59 A_node, Tfl_node, Htarget: 59 18 18 HEAT TRANSFER COEFFICIENT: 6.93000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.930E+01 = 1.0 / (1.0 / 6.930E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.858E+01 * 6.930E+01 * ( 1.104E+03 - 6.022E+02) = 1.341E+06 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 2 ================================ type = CONFRC name = ts1_in A_node, Tfl_node, Htarget: 2 1 2 HEAT TRANSFER COEFFICIENT: 3.56235E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.081E-01 8.000E-01 3.300E-01 / 1.003E-04 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.477E+06 x 2.815E+00 x ( --------- ) = 3.562E+03 1.282E-01 \ 9.944E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.722E+03 = 1.0 / ( 1.0 / 3.562E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.722E+03 * ( 5.571E+02 - 5.671E+02) = -1.740E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 4 ================================ type = CONFRC name = ts1_out A_node, Tfl_node, Htarget: 4 2 2 HEAT TRANSFER COEFFICIENT: 3.55784E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.079E-01 8.000E-01 3.300E-01 / 1.002E-04 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.480E+06 x 2.816E+00 x ( --------- ) = 3.558E+03 1.282E-01 \ 9.946E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.721E+03 = 1.0 / ( 1.0 / 3.558E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.721E+03 * ( 5.579E+02 - 5.710E+02) = -2.268E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 6 ================================ type = CONFRC name = ts2_in A_node, Tfl_node, Htarget: 6 2 3 HEAT TRANSFER COEFFICIENT: 3.55784E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.079E-01 8.000E-01 3.300E-01 / 1.002E-04 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.480E+06 x 2.816E+00 x ( --------- ) = 3.558E+03 1.282E-01 \ 9.946E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.721E+03 = 1.0 / ( 1.0 / 3.558E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.721E+03 * ( 5.579E+02 - 5.710E+02) = -2.268E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 8 ================================ type = CONFRC name = ts2_out A_node, Tfl_node, Htarget: 8 3 3 HEAT TRANSFER COEFFICIENT: 3.55282E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.076E-01 8.000E-01 3.300E-01 / 1.001E-04 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.483E+06 x 2.817E+00 x ( --------- ) = 3.553E+03 1.282E-01 \ 9.949E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.720E+03 = 1.0 / ( 1.0 / 3.553E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.720E+03 * ( 5.588E+02 - 5.760E+02) = -2.977E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 10 ================================ type = CONFRC name = ts3_in A_node, Tfl_node, Htarget: 10 3 4 HEAT TRANSFER COEFFICIENT: 3.55282E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.076E-01 8.000E-01 3.300E-01 / 1.001E-04 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.483E+06 x 2.817E+00 x ( --------- ) = 3.553E+03 1.282E-01 \ 9.949E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.720E+03 = 1.0 / ( 1.0 / 3.553E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.720E+03 * ( 5.588E+02 - 5.760E+02) = -2.977E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 12 ================================ type = CONFRC name = ts3_out A_node, Tfl_node, Htarget: 12 4 4 HEAT TRANSFER COEFFICIENT: 3.54927E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.074E-01 8.000E-01 3.300E-01 / 9.982E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.489E+06 x 2.815E+00 x ( --------- ) = 3.549E+03 1.282E-01 \ 9.952E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.719E+03 = 1.0 / ( 1.0 / 3.549E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.719E+03 * ( 5.597E+02 - 5.825E+02) = -3.943E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 14 ================================ type = CONFRC name = ts4_in A_node, Tfl_node, Htarget: 14 4 5 HEAT TRANSFER COEFFICIENT: 3.54927E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.074E-01 8.000E-01 3.300E-01 / 9.982E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.489E+06 x 2.815E+00 x ( --------- ) = 3.549E+03 1.282E-01 \ 9.952E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.719E+03 = 1.0 / ( 1.0 / 3.549E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.719E+03 * ( 5.597E+02 - 5.825E+02) = -3.943E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 16 ================================ type = CONFRC name = ts4_out A_node, Tfl_node, Htarget: 16 5 5 HEAT TRANSFER COEFFICIENT: 3.54432E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.070E-01 8.000E-01 3.300E-01 / 9.948E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.498E+06 x 2.813E+00 x ( --------- ) = 3.544E+03 1.282E-01 \ 9.955E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.718E+03 = 1.0 / ( 1.0 / 3.544E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.718E+03 * ( 5.610E+02 - 5.915E+02) = -5.270E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 18 ================================ type = CONFRC name = ts5_in A_node, Tfl_node, Htarget: 18 5 6 HEAT TRANSFER COEFFICIENT: 3.54432E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.070E-01 8.000E-01 3.300E-01 / 9.948E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.498E+06 x 2.813E+00 x ( --------- ) = 3.544E+03 1.282E-01 \ 9.955E-05 / U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.718E+03 = 1.0 / ( 1.0 / 3.544E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.718E+03 * ( 5.610E+02 - 5.915E+02) = -5.270E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 20 ================================ type = CONFRC name = ts5_out A_node, Tfl_node, Htarget: 20 6 6 HEAT TRANSFER COEFFICIENT: 3.54101E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.062E-01 8.000E-01 3.300E-01 / 9.955E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.496E+06 x 2.832E+00 x ( --------- ) = 3.526E+03 1.282E-01 \ 9.955E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.715E-02 8.000E-01 4.000E-01 / 5.614E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 2.284E+07 x 6.850E-01 x ( --------- ) = 3.882E+03 1.282E-01 \ 6.060E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.030273 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 3.027E-02 + 0.000E+00 * 9.165E-04 + 0.000E+00 * 2.774E-05 ) x 3.526E+03 + ( 0.000E+00 + 1.000E+00 * 3.027E-02 + 0.000E+00 * 9.165E-04 + 0.000E+00 * 2.774E-05 ) x 3.882E+03 = 3.541E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.717E+03 = 1.0 / ( 1.0 / 3.541E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.005E+01 * 1.717E+03 * ( 5.614E+02 - 6.060E+02) = -7.692E+05 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 22 ================================ type = CONFRC name = ts6_in A_node, Tfl_node, Htarget: 22 6 7 HEAT TRANSFER COEFFICIENT: 2.94636E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.062E-01 8.000E-01 3.300E-01 / 9.955E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.496E+06 x 2.832E+00 x ( --------- ) = 2.934E+03 1.540E-01 \ 9.955E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.715E-02 8.000E-01 4.000E-01 / 5.614E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 2.284E+07 x 6.850E-01 x ( --------- ) = 3.313E+03 1.540E-01 \ 5.758E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.030273 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 3.027E-02 + 0.000E+00 * 9.165E-04 + 0.000E+00 * 2.774E-05 ) x 2.934E+03 + ( 0.000E+00 + 1.000E+00 * 3.027E-02 + 0.000E+00 * 9.165E-04 + 0.000E+00 * 2.774E-05 ) x 3.313E+03 = 2.946E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.564E+03 = 1.0 / ( 1.0 / 2.946E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.208E+01 * 1.564E+03 * ( 5.614E+02 - 5.758E+02) = -2.719E+05 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 24 ================================ type = CONFRC name = ts6_out A_node, Tfl_node, Htarget: 24 7 7 HEAT TRANSFER COEFFICIENT: 2.54033E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.059E-01 8.000E-01 3.300E-01 / 9.957E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.074E+06 x 2.841E+00 x ( --------- ) = 2.525E+03 1.540E-01 \ 9.957E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.717E-02 8.000E-01 4.000E-01 / 5.617E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.896E+07 x 6.843E-01 x ( --------- ) = 2.849E+03 1.540E-01 \ 5.789E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.042872 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 4.287E-02 + 0.000E+00 * 1.838E-03 + 0.000E+00 * 7.880E-05 ) x 2.525E+03 + ( 0.000E+00 + 1.000E+00 * 4.287E-02 + 0.000E+00 * 1.838E-03 + 0.000E+00 * 7.880E-05 ) x 2.849E+03 = 2.540E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.442E+03 = 1.0 / ( 1.0 / 2.540E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.208E+01 * 1.442E+03 * ( 5.617E+02 - 5.789E+02) = -2.994E+05 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 26 ================================ type = CONFRC name = ts7_in A_node, Tfl_node, Htarget: 26 7 8 HEAT TRANSFER COEFFICIENT: 2.54033E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.059E-01 8.000E-01 3.300E-01 / 9.957E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.074E+06 x 2.841E+00 x ( --------- ) = 2.525E+03 1.540E-01 \ 9.957E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.717E-02 8.000E-01 4.000E-01 / 5.617E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.896E+07 x 6.843E-01 x ( --------- ) = 2.845E+03 1.540E-01 \ 5.805E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.042872 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 4.287E-02 + 0.000E+00 * 1.838E-03 + 0.000E+00 * 7.880E-05 ) x 2.525E+03 + ( 0.000E+00 + 1.000E+00 * 4.287E-02 + 0.000E+00 * 1.838E-03 + 0.000E+00 * 7.880E-05 ) x 2.845E+03 = 2.540E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.442E+03 = 1.0 / ( 1.0 / 2.540E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.208E+01 * 1.442E+03 * ( 5.617E+02 - 5.805E+02) = -3.284E+05 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 28 ================================ type = CONFRC name = ts7_out A_node, Tfl_node, Htarget: 28 8 8 HEAT TRANSFER COEFFICIENT: 2.54239E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.057E-01 8.000E-01 3.300E-01 / 9.963E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.073E+06 x 2.847E+00 x ( --------- ) = 2.520E+03 1.540E-01 \ 9.963E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.717E-02 8.000E-01 4.000E-01 / 5.617E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.896E+07 x 6.837E-01 x ( --------- ) = 2.837E+03 1.540E-01 \ 5.827E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.060232 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 6.023E-02 + 0.000E+00 * 3.628E-03 + 0.000E+00 * 2.185E-04 ) x 2.520E+03 + ( 0.000E+00 + 1.000E+00 * 6.023E-02 + 0.000E+00 * 3.628E-03 + 0.000E+00 * 2.185E-04 ) x 2.837E+03 = 2.542E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.442E+03 = 1.0 / ( 1.0 / 2.542E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.208E+01 * 1.442E+03 * ( 5.617E+02 - 5.827E+02) = -3.663E+05 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 30 ================================ type = CONFRC name = ts8_in A_node, Tfl_node, Htarget: 30 8 9 HEAT TRANSFER COEFFICIENT: 2.54239E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.057E-01 8.000E-01 3.300E-01 / 9.963E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.073E+06 x 2.847E+00 x ( --------- ) = 2.520E+03 1.540E-01 \ 9.963E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.717E-02 8.000E-01 4.000E-01 / 5.617E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.896E+07 x 6.837E-01 x ( --------- ) = 2.826E+03 1.540E-01 \ 5.873E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.060232 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 6.023E-02 + 0.000E+00 * 3.628E-03 + 0.000E+00 * 2.185E-04 ) x 2.520E+03 + ( 0.000E+00 + 1.000E+00 * 6.023E-02 + 0.000E+00 * 3.628E-03 + 0.000E+00 * 2.185E-04 ) x 2.826E+03 = 2.542E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.442E+03 = 1.0 / ( 1.0 / 2.542E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.208E+01 * 1.442E+03 * ( 5.617E+02 - 5.873E+02) = -4.467E+05 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 32 ================================ type = CONFRC name = ts8_out A_node, Tfl_node, Htarget: 32 9 9 HEAT TRANSFER COEFFICIENT: 2.55004E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.057E-01 8.000E-01 3.300E-01 / 9.971E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.072E+06 x 2.846E+00 x ( --------- ) = 2.518E+03 1.540E-01 \ 9.971E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.715E-02 8.000E-01 4.000E-01 / 5.615E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.897E+07 x 6.830E-01 x ( --------- ) = 2.802E+03 1.540E-01 \ 5.970E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.086349 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 8.635E-02 + 0.000E+00 * 7.456E-03 + 0.000E+00 * 6.438E-04 ) x 2.518E+03 + ( 0.000E+00 + 1.000E+00 * 8.635E-02 + 0.000E+00 * 7.456E-03 + 0.000E+00 * 6.438E-04 ) x 2.802E+03 = 2.550E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.445E+03 = 1.0 / ( 1.0 / 2.550E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.208E+01 * 1.445E+03 * ( 5.615E+02 - 5.970E+02) = -6.189E+05 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 34 ================================ type = CONFRC name = XO_9in A_node, Tfl_node, Htarget: 34 9 10 HEAT TRANSFER COEFFICIENT: 2.55004E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.057E-01 8.000E-01 3.300E-01 / 9.971E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.072E+06 x 2.846E+00 x ( --------- ) = 2.518E+03 1.540E-01 \ 9.971E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.715E-02 8.000E-01 4.000E-01 / 5.615E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.897E+07 x 6.830E-01 x ( --------- ) = 2.889E+03 1.540E-01 \ 5.615E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.086349 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 8.635E-02 + 0.000E+00 * 7.456E-03 + 0.000E+00 * 6.438E-04 ) x 2.518E+03 + ( 0.000E+00 + 1.000E+00 * 8.635E-02 + 0.000E+00 * 7.456E-03 + 0.000E+00 * 6.438E-04 ) x 2.889E+03 = 2.550E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.445E+03 = 1.0 / ( 1.0 / 2.550E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.831E+01 * 1.445E+03 * ( 5.615E+02 - 5.615E+02) = -4.833E-04 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 36 ================================ type = CONFRC name = XO_9out A_node, Tfl_node, Htarget: 36 10 10 HEAT TRANSFER COEFFICIENT: 2.55040E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.057E-01 8.000E-01 3.300E-01 / 9.972E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.071E+06 x 2.845E+00 x ( --------- ) = 2.518E+03 1.540E-01 \ 9.972E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.715E-02 8.000E-01 4.000E-01 / 5.615E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.897E+07 x 6.829E-01 x ( --------- ) = 2.888E+03 1.540E-01 \ 5.615E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.087203 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 8.720E-02 + 0.000E+00 * 7.604E-03 + 0.000E+00 * 6.631E-04 ) x 2.518E+03 + ( 0.000E+00 + 1.000E+00 * 8.720E-02 + 0.000E+00 * 7.604E-03 + 0.000E+00 * 6.631E-04 ) x 2.888E+03 = 2.550E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.445E+03 = 1.0 / ( 1.0 / 2.550E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.831E+01 * 1.445E+03 * ( 5.615E+02 - 5.615E+02) = -3.925E-04 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 38 ================================ type = CONFRC name = ts10_in A_node, Tfl_node, Htarget: 38 10 11 HEAT TRANSFER COEFFICIENT: 2.55040E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.057E-01 8.000E-01 3.300E-01 / 9.972E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.071E+06 x 2.845E+00 x ( --------- ) = 2.518E+03 1.540E-01 \ 9.972E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.715E-02 8.000E-01 4.000E-01 / 5.615E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.897E+07 x 6.829E-01 x ( --------- ) = 2.822E+03 1.540E-01 \ 5.882E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.087203 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 8.720E-02 + 0.000E+00 * 7.604E-03 + 0.000E+00 * 6.631E-04 ) x 2.518E+03 + ( 0.000E+00 + 1.000E+00 * 8.720E-02 + 0.000E+00 * 7.604E-03 + 0.000E+00 * 6.631E-04 ) x 2.822E+03 = 2.550E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.445E+03 = 1.0 / ( 1.0 / 2.550E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.711E+01 * 1.445E+03 * ( 5.615E+02 - 5.882E+02) = -1.047E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 40 ================================ type = CONFRC name = ts10_out A_node, Tfl_node, Htarget: 40 11 11 HEAT TRANSFER COEFFICIENT: 2.55437E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.051E-01 8.000E-01 3.300E-01 / 9.957E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.074E+06 x 2.858E+00 x ( --------- ) = 2.511E+03 1.540E-01 \ 9.957E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.728E-02 8.000E-01 4.000E-01 / 5.631E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.890E+07 x 6.838E-01 x ( --------- ) = 2.826E+03 1.540E-01 \ 5.897E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.113305 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 1.133E-01 + 0.000E+00 * 1.284E-02 + 0.000E+00 * 1.455E-03 ) x 2.511E+03 + ( 0.000E+00 + 1.000E+00 * 1.133E-01 + 0.000E+00 * 1.284E-02 + 0.000E+00 * 1.455E-03 ) x 2.826E+03 = 2.554E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.446E+03 = 1.0 / ( 1.0 / 2.554E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.711E+01 * 1.446E+03 * ( 5.631E+02 - 5.897E+02) = -1.044E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 42 ================================ type = CONFRC name = ts11_in A_node, Tfl_node, Htarget: 42 11 12 HEAT TRANSFER COEFFICIENT: 2.55437E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.051E-01 8.000E-01 3.300E-01 / 9.957E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.074E+06 x 2.858E+00 x ( --------- ) = 2.511E+03 1.540E-01 \ 9.957E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.728E-02 8.000E-01 4.000E-01 / 5.631E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.890E+07 x 6.838E-01 x ( --------- ) = 2.826E+03 1.540E-01 \ 5.897E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.113305 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 1.133E-01 + 0.000E+00 * 1.284E-02 + 0.000E+00 * 1.455E-03 ) x 2.511E+03 + ( 0.000E+00 + 1.000E+00 * 1.133E-01 + 0.000E+00 * 1.284E-02 + 0.000E+00 * 1.455E-03 ) x 2.826E+03 = 2.554E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.446E+03 = 1.0 / ( 1.0 / 2.554E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.711E+01 * 1.446E+03 * ( 5.631E+02 - 5.897E+02) = -1.044E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 44 ================================ type = CONFRC name = ts11_out A_node, Tfl_node, Htarget: 44 12 12 HEAT TRANSFER COEFFICIENT: 2.57926E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.056E-01 8.000E-01 3.300E-01 / 9.985E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.069E+06 x 2.842E+00 x ( --------- ) = 2.512E+03 1.540E-01 \ 9.985E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.711E-02 8.000E-01 4.000E-01 / 5.612E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.895E+07 x 6.834E-01 x ( --------- ) = 2.818E+03 1.540E-01 \ 5.878E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.180695 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 1.807E-01 + 0.000E+00 * 3.265E-02 + 0.000E+00 * 5.900E-03 ) x 2.512E+03 + ( 0.000E+00 + 1.000E+00 * 1.807E-01 + 0.000E+00 * 3.265E-02 + 0.000E+00 * 5.900E-03 ) x 2.818E+03 = 2.579E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.454E+03 = 1.0 / ( 1.0 / 2.579E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.711E+01 * 1.454E+03 * ( 5.612E+02 - 5.878E+02) = -1.047E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 46 ================================ type = CONFRC name = ts12_in A_node, Tfl_node, Htarget: 46 12 13 HEAT TRANSFER COEFFICIENT: 1.96002E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.056E-01 8.000E-01 3.300E-01 / 9.985E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 2.069E+06 x 2.842E+00 x ( --------- ) = 1.909E+03 2.027E-01 \ 9.985E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.711E-02 8.000E-01 4.000E-01 / 5.612E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.895E+07 x 6.834E-01 x ( --------- ) = 2.134E+03 2.027E-01 \ 5.919E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.180695 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 1.807E-01 + 0.000E+00 * 3.265E-02 + 0.000E+00 * 5.900E-03 ) x 1.909E+03 + ( 0.000E+00 + 1.000E+00 * 1.807E-01 + 0.000E+00 * 3.265E-02 + 0.000E+00 * 5.900E-03 ) x 2.134E+03 = 1.960E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.234E+03 = 1.0 / ( 1.0 / 1.960E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.570E+01 * 1.234E+03 * ( 5.612E+02 - 5.919E+02) = -1.351E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 48 ================================ type = CONFRC name = ts12_out A_node, Tfl_node, Htarget: 48 13 13 HEAT TRANSFER COEFFICIENT: 1.58471E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.051E-01 8.000E-01 3.300E-01 / 9.972E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 1.579E+06 x 2.851E+00 x ( --------- ) = 1.533E+03 2.027E-01 \ 9.972E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.722E-02 8.000E-01 4.000E-01 / 5.625E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.441E+07 x 6.845E-01 x ( --------- ) = 1.714E+03 2.027E-01 \ 5.974E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.222475 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 2.225E-01 + 0.000E+00 * 4.950E-02 + 0.000E+00 * 1.101E-02 ) x 1.533E+03 + ( 0.000E+00 + 1.000E+00 * 2.225E-01 + 0.000E+00 * 4.950E-02 + 0.000E+00 * 1.101E-02 ) x 1.714E+03 = 1.585E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.074E+03 = 1.0 / ( 1.0 / 1.585E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.570E+01 * 1.074E+03 * ( 5.625E+02 - 5.974E+02) = -1.337E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 50 ================================ type = CONFRC name = ts13_in A_node, Tfl_node, Htarget: 50 13 14 HEAT TRANSFER COEFFICIENT: 1.58471E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.051E-01 8.000E-01 3.300E-01 / 9.972E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 1.579E+06 x 2.851E+00 x ( --------- ) = 1.533E+03 2.027E-01 \ 9.972E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.722E-02 8.000E-01 4.000E-01 / 5.625E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.441E+07 x 6.845E-01 x ( --------- ) = 1.714E+03 2.027E-01 \ 5.974E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.222475 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 2.225E-01 + 0.000E+00 * 4.950E-02 + 0.000E+00 * 1.101E-02 ) x 1.533E+03 + ( 0.000E+00 + 1.000E+00 * 2.225E-01 + 0.000E+00 * 4.950E-02 + 0.000E+00 * 1.101E-02 ) x 1.714E+03 = 1.585E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.074E+03 = 1.0 / ( 1.0 / 1.585E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.570E+01 * 1.074E+03 * ( 5.625E+02 - 5.974E+02) = -1.337E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 52 ================================ type = CONFRC name = ts13_out A_node, Tfl_node, Htarget: 52 14 14 HEAT TRANSFER COEFFICIENT: 1.59904E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.053E-01 8.000E-01 3.300E-01 / 9.990E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 1.577E+06 x 2.841E+00 x ( --------- ) = 1.532E+03 2.027E-01 \ 9.990E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.712E-02 8.000E-01 4.000E-01 / 5.614E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.441E+07 x 6.851E-01 x ( --------- ) = 1.710E+03 2.027E-01 \ 5.962E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.291987 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 2.920E-01 + 0.000E+00 * 8.526E-02 + 0.000E+00 * 2.489E-02 ) x 1.532E+03 + ( 0.000E+00 + 1.000E+00 * 2.920E-01 + 0.000E+00 * 8.526E-02 + 0.000E+00 * 2.489E-02 ) x 1.710E+03 = 1.599E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.081E+03 = 1.0 / ( 1.0 / 1.599E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.570E+01 * 1.081E+03 * ( 5.614E+02 - 5.962E+02) = -1.340E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 54 ================================ type = CONFRC name = ts14_in A_node, Tfl_node, Htarget: 54 14 15 HEAT TRANSFER COEFFICIENT: 1.59904E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.053E-01 8.000E-01 3.300E-01 / 9.990E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 1.577E+06 x 2.841E+00 x ( --------- ) = 1.532E+03 2.027E-01 \ 9.990E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.712E-02 8.000E-01 4.000E-01 / 5.614E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.441E+07 x 6.851E-01 x ( --------- ) = 1.710E+03 2.027E-01 \ 5.962E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.291987 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 2.920E-01 + 0.000E+00 * 8.526E-02 + 0.000E+00 * 2.489E-02 ) x 1.532E+03 + ( 0.000E+00 + 1.000E+00 * 2.920E-01 + 0.000E+00 * 8.526E-02 + 0.000E+00 * 2.489E-02 ) x 1.710E+03 = 1.599E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.081E+03 = 1.0 / ( 1.0 / 1.599E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.570E+01 * 1.081E+03 * ( 5.614E+02 - 5.962E+02) = -1.340E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 56 ================================ type = CONFRC name = ts14_out A_node, Tfl_node, Htarget: 56 15 15 HEAT TRANSFER COEFFICIENT: 1.60871E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.050E-01 8.000E-01 3.300E-01 / 9.987E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 1.577E+06 x 2.844E+00 x ( --------- ) = 1.529E+03 2.027E-01 \ 9.987E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.717E-02 8.000E-01 4.000E-01 / 5.621E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.439E+07 x 6.856E-01 x ( --------- ) = 1.712E+03 2.027E-01 \ 5.967E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.341169 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 3.412E-01 + 0.000E+00 * 1.164E-01 + 0.000E+00 * 3.971E-02 ) x 1.529E+03 + ( 0.000E+00 + 1.000E+00 * 3.412E-01 + 0.000E+00 * 1.164E-01 + 0.000E+00 * 3.971E-02 ) x 1.712E+03 = 1.609E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.085E+03 = 1.0 / ( 1.0 / 1.609E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.570E+01 * 1.085E+03 * ( 5.621E+02 - 5.967E+02) = -1.339E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 58 ================================ type = CONFRC name = ts15_in A_node, Tfl_node, Htarget: 58 15 16 HEAT TRANSFER COEFFICIENT: 1.60871E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.050E-01 8.000E-01 3.300E-01 / 9.987E-05 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 1.577E+06 x 2.844E+00 x ( --------- ) = 1.529E+03 2.027E-01 \ 9.987E-05 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.717E-02 8.000E-01 4.000E-01 / 5.621E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.439E+07 x 6.856E-01 x ( --------- ) = 1.712E+03 2.027E-01 \ 5.967E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.341169 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 3.412E-01 + 0.000E+00 * 1.164E-01 + 0.000E+00 * 3.971E-02 ) x 1.529E+03 + ( 0.000E+00 + 1.000E+00 * 3.412E-01 + 0.000E+00 * 1.164E-01 + 0.000E+00 * 3.971E-02 ) x 1.712E+03 = 1.609E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.085E+03 = 1.0 / ( 1.0 / 1.609E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.570E+01 * 1.085E+03 * ( 5.621E+02 - 5.967E+02) = -1.339E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 60 ================================ type = CONFRC name = ts15_out A_node, Tfl_node, Htarget: 60 16 16 HEAT TRANSFER COEFFICIENT: 1.62203E+03 [W/m2K], FOULING RESISTANCE: 3.00000E-04 [K.m2/W] METHOD: ADAMS CORRELATION WITH PARAMETERS; EMULATES API-530 LIQUID HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------ K_liq_bulk ____CL___ ____DL___ / ___u_bulk \ ____EL___ H_LIQ = ____AL___ + ____BL___ x ---------- x ___Re_liq x ___Pr_liq x ( --------- ) L_charact \ ___u_film / 1.052E-01 8.000E-01 3.300E-01 / 1.001E-04 \ 1.400E-01 H_LIQ = 0.000E+00 + 2.300E-02 x ---------- x 1.574E+06 x 2.836E+00 x ( --------- ) = 1.527E+03 2.027E-01 \ 1.001E-04 / VAPOR HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- K_vap_bulk ____CV___ ____DV___ / ___T_bulk \ ____EV___ H_VAP = ____AV___ + ____BV___ x ---------- x ___Re_vap x ___Pr_vap x ( --------- ) L_charact \ ___T_film / 3.709E-02 8.000E-01 4.000E-01 / 5.612E+02 \ 5.000E-01 H_VAP = 0.000E+00 + 2.100E-02 x ---------- x 1.439E+07 x 6.861E-01 x ( --------- ) = 1.708E+03 2.027E-01 \ 5.957E+02 / MIXED HEAT TRANSFER COEFFICIENT ------------------------------------------------------------------------- VAPOR FRACTION: 0.406501 H_MIX = ( ____L0___ + ____L1___ * ____vapfr + ____L2___ * __vapfr^2 + ____L3___ * __vapfr^3 ) * H_LIQ + + ( ____V0___ + ____V1___ * ____vapfr + ____V2___ * __vapfr^2 + ____V3___ * __vapfr^3 ) * H_VAP H_MIX = ( 1.000E+00 +-1.000E+00 * 4.065E-01 + 0.000E+00 * 1.652E-01 + 0.000E+00 * 6.717E-02 ) x 1.527E+03 + ( 0.000E+00 + 1.000E+00 * 4.065E-01 + 0.000E+00 * 1.652E-01 + 0.000E+00 * 6.717E-02 ) x 1.708E+03 = 1.622E+03 [W/m2/K] U_eff_bare = 1.0 / ( 1.0 / _U_adams_ + __R_foul_ ) 1.091E+03 = 1.0 / ( 1.0 / 1.622E+03 + 3.000E-04 ) [W/(m^2.K)] HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.570E+01 * 1.091E+03 * ( 5.612E+02 - 5.957E+02) = -1.341E+06 Watt ######## Pr_vap < 0.7=min. ######### ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 62 ================================ type = CONFRC name = Area62 A_node, Tfl_node, Htarget: 62 18 18 HEAT TRANSFER COEFFICIENT: 7.00000E+01 [W/m2K], FOULING RESISTANCE: 3.33300E-01 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 2.877E+00 = 1.0 / (1.0 / 7.000E+01 + 3.333E-01 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 2.875E+02 * 2.877E+00 * ( 1.104E+03 - 8.392E+02) = 2.190E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 64 ================================ type = CONFRC name = Area64 A_node, Tfl_node, Htarget: 64 18 18 HEAT TRANSFER COEFFICIENT: 7.00000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 7.000E+01 = 1.0 / (1.0 / 7.000E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 8.845E+01 * 7.000E+01 * ( 1.104E+03 - 1.091E+03) = 7.990E+04 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 66 ================================ type = CONFRC name = Area66 A_node, Tfl_node, Htarget: 66 19 19 HEAT TRANSFER COEFFICIENT: 6.50000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.500E+01 = 1.0 / (1.0 / 6.500E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.620E+01 * 6.500E+01 * ( 1.031E+03 - 1.013E+03) = 1.912E+04 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 68 ================================ type = CONFRC name = Area68 A_node, Tfl_node, Htarget: 68 22 22 HEAT TRANSFER COEFFICIENT: 6.00000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 6.000E+01 = 1.0 / (1.0 / 6.000E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.850E+01 * 6.000E+01 * ( 8.550E+02 - 8.407E+02) = 1.591E+04 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 61 ================================ type = CONFRC name = Area62 A_node, Tfl_node, Htarget: 61 28 28 HEAT TRANSFER COEFFICIENT: 1.50000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 1.500E+01 = 1.0 / (1.0 / 1.500E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 3.035E+02 * 1.500E+01 * ( 2.888E+02 - 3.373E+02) = -2.206E+05 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 63 ================================ type = CONFRC name = Area62 A_node, Tfl_node, Htarget: 63 28 28 HEAT TRANSFER COEFFICIENT: 1.20000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 1.200E+01 = 1.0 / (1.0 / 1.200E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 8.845E+01 * 1.200E+01 * ( 2.888E+02 - 3.641E+02) = -7.991E+04 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 65 ================================ type = CONFRC name = Area62 A_node, Tfl_node, Htarget: 65 28 28 HEAT TRANSFER COEFFICIENT: 1.50000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 1.500E+01 = 1.0 / (1.0 / 1.500E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.620E+01 * 1.500E+01 * ( 2.888E+02 - 3.675E+02) = -1.912E+04 Watt ====================== CONVECTIVE HT EXCH COEFF CALC OF SURFACE NR: 67 ================================ type = CONFRC name = Area62 A_node, Tfl_node, Htarget: 67 28 28 HEAT TRANSFER COEFFICIENT: 1.50000E+01 [W/m2K], FOULING RESISTANCE: 0.00000E+00 [K.m2/W] METHOD: CONSTANT VALUE U_eff_bare = 1.0 / (1.0 / _U_const_ + __R_foul_ ) 1.500E+01 = 1.0 / (1.0 / 1.500E+01 + 0.000E+00 ) HEAT TRANSFERRED = ___AREA__ * U_eff_bare * ( __TFLUID_ - __TWALL__) Q = 1.850E+01 * 1.500E+01 * ( 2.888E+02 - 3.462E+02) = -1.591E+04 Watt