aspen设计萃取精馏塔系统补充萃取剂量无法计算? 萃取 精馏塔 T-102错误如下***SEVERE ERROR THE FOLLOWING STAGES DRIED UP (VAPOR OR LIQUID FLOW APPROACHES 0): 85 A LIMIT OF 0.10000E-04 * SUM OF FEEDS WAS IMPOSED ON THE FLOW RATES OR A LIMIT OF 0.10000E-04 WAS IMPOSED ON THE STAGE V/L OR L/V RATIO. 溶剂解吸塔T-103错误如下 ***SEVERE ERROR COMPONENT BALANCE EQUATION FAILED TO CONVERGE. ***SEVERE ERROR THE FOLLOWING STAGES DRIED UP (VAPOR OR LIQUID FLOW APPROACHES 0): 7 8 9 A LIMIT OF 0.10000E-04 * SUM OF FEEDS WAS IMPOSED ON THE FLOW RATES OR A LIMIT OF 0.10000E-04 WAS IMPOSED ON THE STAGE V/L OR L/V RATIO. ** ERROR BLOCK T-103 IS NOT IN MASS BALANCE: MASS INLET FLOW = 0.15998998E+02, MASS OUTLET FLOW = 0.15241218E+02 RELATIVE DIFFERENCE = 0.49719096E-01 查看更多2个回答 . 5人已关注