2019年第十三届全国大学生化工设计竞赛安徽工业大学作品扬子石化年产10万吨醋酸乙烯酯项目设计.docx

《2019年第十三届全国大学生化工设计竞赛安徽工业大学作品扬子石化年产10万吨醋酸乙烯酯项目设计.docx》由会员分享，可在线阅读，更多相关《2019年第十三届全国大学生化工设计竞赛安徽工业大学作品扬子石化年产10万吨醋酸乙烯酯项目设计.docx（186页珍藏版）》请在淘文阁 - 分享文档赚钱的网站上搜索。

1、OL ML ILErr/TolBlock: QIModel: FSPLITBlock: E0101Model: HEATERMATIONTHERE ARE HENRY COMPONENTS DEFINED IN THIS CASE, THE BINARY DATABANK WILL BE SEARCHED AUTOMATICALLY FOR ANY AVAILABLE HENRY CONSTANTS.THE PAIR PARAMETERS FOR ELECNRTL OPTION SET HAS BEEN RETRIEVED FROM DATABANK ENRTL-RK.* WARNING IN

2、 THE STREAM PARAGRAPH WHICH BEGINS ON LINE 518STREAM NAME: 0302STREAM 0302 NOT IN CHARGE BALANCE.ION MOLE FLOWS ADJUSTED TO MAINTAIN AN AVERAGE CHARGE BALANCE.CATIONS SCALED BY A FACTOR OF (0.987850), ANDANIONS BY A FACTOR OF (1.01245).* WARNING IN THE STREAM PARAGRAPH WHICH BEGINS ON LINE 539STREAM

3、 NAME: 0325STREAM 0325 NOT IN CHARGE BALANCE.ION MOLE FLOWS ADJUSTED TO MAINTAIN AN AVERAGE CHARGE BALANCE.CATIONS SCALED BY A FACTOR OF (0.761985), ANDANIONS BY A FACTOR OF (1.45425).* WARNING IN THE STREAM PARAGRAPH WHICH BEGINS ON LINE 549STREAM NAME: 0327STREAM 0327 NOT IN CHARGE BALANCE.ION MOL

4、E FLOWS ADJUSTED TO MAINTAIN AN AVERAGE CHARGE BALANCE.CATIONS SCALED BY A FACTOR OF (0.761981), ANDANIONS BY A FACTOR OF (1.45427).* WARNING IN THE STREAM PARAGRAPH WHICH BEGINS ON LINE 559STREAM NAME: 0333STREAM 0333 NOT IN CHARGE BALANCE.ION MOLE FLOWS ADJUSTED TO MAINTAIN AN AVERAGE CHARGE BALAN

5、CE.CATIONS SCALED BY A FACTOR OF (0.535319E+12), ANDANIONS BY A FACTOR OF (0.500000).* WARNING WHILE CHECKING INPUT SPECIFICATIONSINCONSISTENT PROPERTIES DETECTED FOR 8 STREAMSSOURCE BLOCKPROPERTIES STREAMDESTINATION BLOCKPROPERTIEST0302NRTL-RK0304E0305ELECNRTLT0301ELECNRTL0302T0302NRTL-RKP0310ELECN

6、RTL0313T0304NRTL-HOCT0304NRTL-HOC0315V0310ELECNRTLP0317ELECNRTL0325T0306NRTL-HOCT0302NRTL-RK0303M03ELECNRTLT0306NRTL-HOC0327T0307ELECNRTLT0304NRTL-HOC0314V0307ELECNRTLFlowsheet Analysis:Block SOLVEROl (Method: BROYDEN ) has been defined to converge streams: 01130209Block SOLVER02 (Method: BROYDEN )

7、has been defined to converge streams: 03380333COMPUTATION ORDER FOR THE FLOWSHEET:AIR 1000 RI MP R2 HP LP COOLSOLVEROl R0101 T0101 T0102 C0104 V0104 M01 E0107 P0103I T0103 V0201 T0301 E0306 V0303 P0306 T0303 V0305 P0310I T0304 V0307 T0302 E0305 V0102 T0202 V0202 E0201 T0201I E0202 V0203 V0101 V0204

8、E0204 V0205 F0201 E0205 E0206I M0201 E0207 M0202 M02 V03 QI E0101 V0103 C0101 E0102I C0102 E0103 C0103 E0104(RETURN SOLVEROl)P0313 T0305 E0313 V0309 V0310 P0317 T0306 E0208SOLVER02 T0307 C0301 E0316 P0318 E0317 V0313 E0318 V0312(RETURN SOLVER02)M03 -Calculations begin .Utility AIRModel: GENERALUtili

9、ty 1000Model: GENERALUtility RIModel: GENERALUtility HPModel: GENERALUtility LPModel: GENERALUtility COOLModel: GENERALUtility R2Model: GENERAL Beginning Convergence Loop SOLVEROl Method: BROYDEN Converging tear streams: 01130209Block: R0101Model: RSTOICBlock: T0101Model: RADFRACConvergence iteratio

10、ns:OLMLILErr/Tol11103570.221102765.331102446.041101275.951101507.061101734.971102282.781101966.591101622.7101101956.9111102139.9121102164.8131101643.1141102965.9151102205.316181372.6171102231.1181102166.9191102658.8201102248.1211101882.6221102586.923172680.22415640.41251103294.3261102606.1271102353.

11、1281103384.52911010315.301105082.6311103303.8321104638.133161211.0341103436.6351103724.0361105204.6371102859.6381102198.2391102704.140171623.4411101199.642110902.1043161101.44416579.07451101398.14614784.8547181456.74815630.614916243.965012165.245112156.095212112.29531226.861541266,36455126.756056122

12、.136057123.430958110.94779Block: T0102Model: RADFRACConvergence iterations:OLMLILErr/Tol111016246.2195692.83162744.9414640.62513335.99612230.5271288.18289101112131415161252.6321228.4961213.8711112.0611110.843115.6307123.0206121.227712062033Block: C0104Model: COMPRBlock: V0104Model: FSPLITBlock: MOIM

13、odel: MIXERBlock: E0107Model: HEATERBlock: P0103Model: PUMPBlock: T0103Model: RADFRACConvergence iterations:OL ML IL Err/Tol12345678910111213142319.6121501.612561.3812800.0612344.6812111.8611107.021181.8751116.229115.1831114.0120112.354311025852Block: V0201Model: MIXERBlock: T0301Model: RADFRACConve

14、rgence iterations:OL ML IL Err/Tol113849.73212389.9631356.02641214.4715125.70016121.32507120.69716Block: E0306Model: HEATERBlock: V0303Model: DECANTERBlock: P0306Model: PUMPBlock: T0303Model: RADFRACConvergence iterations:OLMLILErr/Tol111182.86212106.4731228.5754128.75055122.73896120.84052Block: V03

15、05Model:DECANTERBlock: P0310Model:PUMPBlock: T0304Model:RADFRACConvergence iterations:OLMLILErr/Tol11101025.32152481.73151945.74141422.65141517.0613899.767110387.92813863.989142396.5101104104.811141846.412141454.9131101345.31416704.431517657.4116141994.2171104393.8181100.68614191101014.3201101432.92

16、1110849.772213441.8923131125.724163255.225161008.426110804.602712862.7128151728.729141969.93014732.653113522.133213308.593312101.74341254.808351271.905361227.79837119.280338128.137339122.422740120.86747Block: V0307Model: FLASH2Block: T0302Model: RADFRACConvergence iterations:OLMLILErr/Tol114314.8721

17、462.86331410.4034133.30435140.52271Block: E0305 Model: HEATERBlock: V0102 Model: MIXERModel: HEATERBlock: V0203Model: FLASH2Block: V0101Model: MIXERBlock: T0202 Model: RADFRACConvergence iterations:OLMLILErr/Tol11135.5572588.14403350.61988Block: V0202Model: MIXERBlock: E0201Model:HEATERBlock: T0201M

18、odel: RADFRACConvergence iterations:OLMLILErr/Tol1152625.62131516.83131160.54132098.9513960.47613671.87712526.10812203.2891299.925101268,892111248,073121217.73913115.721814123.454115121.466316122.658017122.450518110.80030Block: E0202Block: V0204 Model: MIXERBlock: E0204Model: HEATERBlock: V0205Model

19、: FLASH2Block: F0201Model: RSTOICBlock: E0205Model: HEATXBlock: E0206Model: HEATERBlock: M0201Model: COMPRBlock: E0207Model: HEATERBlock: M0202Model: COMPRBlock: M02Model: MIXERBlock: V03Model: FSPLITBlock: QIModel: FSPLITBlock: E0101Model: HEATERBlock: V0103Model: MIXERBlock: C0101Model: COMPRBlock

20、: E0102Model: HEATERBlock: C0102Model: COMPRBlock: E0103Model: HEATERBlock: C0103Model: COMPRBlock: E0104Model: HEATERIteration 102090.86542E+02 Loop SOLVEROl Method: BROYDEN Converging tear streams: 0113 17 vars not converged, Max Err/TolBlock: R0101 Model: RSTOICBlock: T0101 Model: RADFRACOLML1 12

21、 13 1Block: C0104印ock: V0104Block: MOIBlock: E0107Block: P0103Block: T0103IL Err/Tol12.459711.035410.41902Model: COMPRModel: FSPLITModel: MIXERModel: HEATERModel: PUMPModel: RADFRACConvergence iterations:OLMLILErr/Tol11377.839212204.223126.10894110.96958Block: T0102Model: RADFRACConvergence iteratio

22、ns:Convergence iterations:OL ML ILErr/Tol1110.23263Block: V0201Model: MIXERBlock: T0301Model: RADFRACConvergence iterations:OL ML ILErr/Tol1110.25075Block: E0306 Model: HEATERBlock: V0303 Model: DECANTERBlock: P0306Model: PUMPBlock: T0303Model: RADFRACBlock: V0305Model: DECANTERBlock: P0310Model: PU

23、MPBlock: T0304Model: RADFRACConvergence iterations:OLMLILErr/Tol1121.74852120.92099Block: V0307Model: FLASH2Block: T0302Model: RADFRACConvergence iterations:OLMLILErr/Tol1126.73892126.423731217.4594118.51735123.61746120.95488Convergence iterations:OL ML1121Block: E0305Block: V0102Block: T0202ILErr/T

24、ol62.016630,26793Model: HEATERModel: MIXERModel: RADFRACConvergence iterations:OL ML IL Err/Tol1475.1981233242.713820,99425E-01Block: V0202Model: MIXERBlock: E0201Model: HEATERBlock: T0201Model: RADFRACConvergence iterations:OL ML IL Err/Tol1 110,86763Block: E0202Model: HEATERBlock: V0203Model: FLAS

25、H2Block: V0101Model: MIXERBlock: V0204Model: MIXERBlock: E0204Model: HEATERBlock: V0205Model: FLASH2Block: F0201Model: RSTOICBlock: E0205Model: HEATXBlock: E0206Model: HEATERBlock: M0201Model: COMPRBlock: E0207Model: HEATERBlock: M0202Model: COMPRBlock: M02Model: MIXERBlock: V03Model: FSPLITBlock: Q

26、IModel: FSPLITBlock: E0101Model: HEATERBlock: V0103Model: MIXERBlock: C0101Model: COMPRBlock: E0102Model: HEATERBlock: C0102Model: COMPRBlock: E0103Model: HEATERBlock: C0103Model: COMPRBlock: E0104Model: HEATER Loop $OLVER01 Method: BROYDEN Iteration 2Converging tear streams: 0113020914 vars not con

27、verged, Max Err/Tol -0.79895E+02Block: R0101Model: RSTOICBlock: T0101Model: RADFRACConvergence iterations:OL ML IL Err/Tol1110.33704Block: T0102Model: RADFRACConvergence iterations:OL ML IL Err/Tol1110.99157Block: C0104Model: COMPRBlock: V0104Model: FSPLITBlock: M01Model: MIXERBlock: E0107Model: HEA

28、TERBlock: P0103Model: PUMPBlock: T0103Model: RADFRACConvergence iterations:OL1ML1ILErr/Tol10.70691Block: V0201Model: MIXERBlock: T0301Model: RADFRACConvergence iterations:OL ML ILErr/Tol1110.78448EBlock: E0306Model: HEATERBlock: V0303Model: DECANTERBlock: P0306Model: PUMPBlock: T0303Model: RADFRACCo

29、nvergence iterations:OL ML ILErr/Tol1110.27742Block: V0305Model: DECANTERBlock: P0310Model: PUMPBlock: T0304Model: RADFRACConvergence iterations:OL ML ILErr/Tol1123.88532123.70023128.36154121.66685121.92086121.07787110.35494Block: V0307Model: FLASH2Convergence iterations:OL1ML1ILErr/Tol40.15398Block

30、: E0305Model: HEATERBlock: V0102Model: MIXERBlock: T0202Model: RADFRACConvergence iterations:OLMLILErr/Tol1473.80092341.92913220.39656E-01Block: V0202Model: MIXERBlock: E0201Model: HEATERBlock: T0201Model: RADFRACConvergence iterations:OL ML ILErr/Tol1110.22538Block: E0202Model: HEATERBlock: V0203Mo

31、del: FLASH2Block: V0101Model: MIXERBlock: V0204Model: MIXERBlock: E0204Model: HEATERBlock: V0205Model: FLASH2Block: F0201Model: RSTOICBlock: E0205Model: HEATXBlock: M0201 Model: COMPRBlock: E0207Model: HEATERBlock: M0202Model: COMPRBlock: M02Model: MIXERBlock: V03Model: FSPLITBlock: QIModel: FSPLITB

32、lock: E0101Model: HEATERBlock: V0103Model: MIXERBlock: C0101Model: COMPRBlock: E0102Model: HEATERBlock: C0102Model: COMPRBlock: E0103Model: HEATERBlock: C0103Model: COMPRBlock: E0104Model: HEATER Loop $OLVER01 Method: BROYDEN Iteration 3 Converging tear streams: 0113020914 vars not converged, Max Er

33、r/Tol -0.16477E+02Block: R0101Model: RSTOICBlock: T0101Model: RADFRACConvergence iterations:OLMLILErr/Tol1111.83412134.86893110.59182E-01Convergence iterations:OL1ML1ILErr/Tol10,97355Block: C0104Model: COMPRBlock: V0104Model: FSPLITBlock: MOIModel: MIXERBlock: E0107Model: HEATERBlock: P0103Model: PU

34、MPBlock: T0103Model: RADFRACConvergence iterations:OLMLILErr/Tol1110,58449E-01Block: V0201Model: MIXERBlock: T0301Model: RADFRACConvergence iterations:OLMLILErr/Tol1110.19292E-01Block: E0306Model: HEATERBlock: V0303Model: DECANTERBlock: P0306Model: PUMPBlock: T0303Model: RADFRACConvergence iteration

35、s:OLMLILErr/Tol1110.14762Block: V0305Model: DECANTERBlock: T0304 Model: RADFRACBlock: V0307Model: FLASH2Block: T0302Model: RADFRACConvergence iterations:OLMLILErr/Tol1121.70292111.60243124.07594122.26775120.82274Convergence iterations:OL ML1 1Block: E0305Block: V0102Block: T0202ILErr/Tol40,36134Mode

36、l: HEATERModel: MIXERModel: RADFRACConvergence iterations:OL ML14Block: V0202Block: E0201Block: T0201ILErr/Tol60.55187Model: MIXERModel: HEATERModel: RADFRACConvergence iterations:OL ML ILErr/Tol1110.22507Block: E0202Model: HEATERBlock: V0203Model: FLASH2Block: E0204Model: HEATERBlock: V0205Model: F

37、LASH2Block: F0201Model: RSTOICBlock: E0205Model: HEATXBlock: E0206Model: HEATERBlock: M0201Model: COMPRBlock: E0207Model: HEATERBlock: M0202Model: COMPRBlock: M02Model: MIXERBlock: V03Model: FSPLITBlock: QIModel: FSPLITBlock: E0101Model: HEATERBlock: V0103Model: MIXERBlock: C0101Model: COMPRBlock: E

38、0102Model: HEATERBlock: C0102Model: COMPRBlock: E0103Model: HEATERBlock: C0103Model: COMPRBlock: E0104Model: HEATERIteration 40209 -0.49458E+01 Loop $OLVER01 Method: BROYDEN Converging tear streams: 01135 vars not converged, Max Err/TolBlock: R0101 Model: RSTOICBlock: T0101 Model: RADFRACConvergence

39、 iterations:OLMLILErr/Tol1111.84862124.79913110.10454E-01Block: T0102Model:RADFRACConvergence iterations:OL ML1 1Block: C0104Block: V0104Block: MOIBlock: E0107Block: P0103Block: T0103ILErr/Tol10,58221Model: COMPRModel: FSPLITModel: MIXERModel: HEATERModel: PUMPModel: RADFRACConvergence iterations:OL ML ILErr/Tol1110.79474E-01Block: V0201Model: MIXERBlock: T0301Model: RADFRACConve