aspen 模拟换热器出现如下问题,是什么原因? 各位大侠,我在用aspen 模拟 换热器 出现如下问题,是什么原因? 条件如下: 冷近 冷出 热进 热出 Temperature C 109.40 -176.10 179.20 174.00 Pressure bar 80.00 71.48 10.00 6.00 Vapor Frac 0.00 0.00 0.13 1.00 Mass Flow kg/hr 143728.82 143728.82 28306400.00 28306400.00 Volume Flow cum/hr 158.32 122.72 739158.15 9423890.00 Enthalpy MMkcal/hr -536.46 -13062.35 -101290.00 -88762.69 CO 0.00 0.00 1566.43 1566.43 CO2 0.00 0.00 1918.49 1918.49 H2 0.00 0.00 1348.90 1348.90 CH4 0.00 0.00 0.00 0.00 N2 0.00 0.00 7.07 7.07 AR 0.00 0.00 4.52 4.52 H2S 0.00 0.00 18.49 18.49 COS 0.00 0.00 1.76 1.76 H3N 1.33 1.33 170.89 170.89 CL 0.00 0.00 4.18 4.18 O2 0.00 0.00 0.00 0.00 H2O 7976.90 7976.90 1563730.00 1563730.00 结果: Block: B1 Model: HEATX * WARNING CALCULATED SHELLSIDE DELTA-P > THAN MAXIMUM ALLOWABLE DELTA-P MAXIMUM DELTA-P USED IN CALCULATIONS * WARNING CALCULATED TUBESIDE DELTA-P > THAN MAXIMUM ALLOWABLE DELTA-P MAXIMUM DELTA-P USED IN CALCULATIONS ** ERROR SPECIFIED CONDITION IS IN THE ONE PHASE REGION. FAILED TO FIND REASONABLE TEMPERATURE TO SATISFY SPECIFIED ENTHALPY; POSSIBLE ERROR WITH ENTHALPY VALUE. FLASH FAILED FOR COLD STREAM DURING ENERGY BALANCE CALCULATION ** ERROR FLASH CALCULATION HAS DRIVEN THE TEMPERATURE DOWN TO THE LOWER LIMIT OF 97.0634 DEGREES K., BUT ENTHALPY BALANCE IS STILL NOT SATISFIED. HEAT DUTY SPECIFICATIONS MAY BE INFEASIBLE. FLASH FAILED FOR HOT STREAM DURING ENERGY BALANCE CALCULATION查看更多2个回答 . 2人已关注