制药过程的溶媒回收技术

1、原料液3101LI3101PFIC水、碱PPLIC310431053102TIPILI31053106LIP3107LITI3104TI31083103TI3107TIFIC3105FI3108LP轻相去去苯胺系统FI3107原料液碱、水3103FILP3103LI3106TI甲醇系统FICPPTITILI23456789101112131415161718192021222324125T1CON1-2REB1CON1-1F123456789101112131415161718192021222324125T2EPDCON2-2REB2E-NSS1Liquid30.000150.000138.

2、3890.7580.0050.237Stream NameStream DescriptionPhaseTemperaturePressureFlowrateComposition H2O CL2M METHANOLCKPAKG-MOL/HRCKPAKG-MOL/HRS2Liquid40.477102.0001.8120.0000.4380.562CKPAKG-MOL/HRS3Liquid30.000102.0001.8120.0000.4380.562CKPAKG-MOL/HRS4Liquid84.753117.000148.7730.7800.0000.220CKPAKG-MOL/HRS5

3、Liquid25.806102.00012.1930.9100.0070.083CKPAKG-MOL/HRS6Liquid25.806102.0000.7210.0110.9800.009CKPAKG-MOL/HRH2OLiquid25.000133.00011.1021.0000.0000.000CKPAKG-MOL/HRS7Liquid64.699102.00032.7750.0000.0001.000CKPAKG-MOL/HRS8Liquid104.066117.000115.9981.0000.0000.000CKPAKG-MOL/HRPDLiquid36.000102.00032.7

4、750.0000.0001.000CKPAKG-MOL/HRS10Mixed86.464150.000138.3890.7580.0050.237CKPAKG-MOL/HRNSLiquid110.000143.292111.0191.0000.0000.000CKPAKG-MOL/HRS12Liquid35.530143.292111.0191.0000.0000.000Hx NameDutyHx Hot Prod TempHx Cold Prod TempHx Utility Temp InHx Utility Temp OutHx Utility Flow RateHx UHx AreaM*KCAL/HRCCCCkg-mol/hrKW/K/M2M2REB10.2352143.984.8143.9n/a25.60.3513.0CON1-10.230740.525.015.025.01280.50.3529.7CON1-20.000430.030.025.030.04.50.230.3REB20.8525133.8104.1133.8n/a91.60.4771.5E-NS0.149286.535.5n/an/an/a0.3540.0CON2-