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年產(chǎn)10萬噸丙烯腈生產(chǎn)流程概念設計-資料下載頁

2025-06-07 00:55本頁面
  

【正文】 + + + + + + + + + + + + + + + + + + ++ + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + ++ + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + +TABLE OF CONTENTSRUN CONTROL SECTION.................................... 1RUN CONTROL INFORMATION........................... 119
DESCRIPTION....................................... 1FLOWSHEET SECTION...................................... 2FLOWSHEET CONNECTIVITY BY STREAMS................. 2FLOWSHEET CONNECTIVITY BY BLOCKS.................. 2CONVERGENCE STATUS SUMMARY........................ 2CONVERGENCE BLOCK: $OLVER01...................... 2COMPUTATIONAL SEQUENCE............................ 4OVERALL FLOWSHEET BALANCE......................... 4PHYSICAL PROPERTIES SECTION............................ 6COMPONENTS........................................ 6UOS BLOCK SECTION.................................... 7BLOCK: E101BLOCK: E102BLOCK: E103BLOCK: E104BLOCK: E105BLOCK: F101BLOCK: F102BLOCK: P101BLOCK: R101BLOCK: T101BLOCK: T102MODEL: HEATER.................... 7MODEL: HEATER.................... 7MODEL: HEATER.................... 8MODEL: HEATER.................... 9MODEL: HEATER.................... 10MODEL: FLASH2.................... 11MODEL: FLASH2.................... 12MODEL: PUMP...................... 13MODEL: RSTOIC.................... 14MODEL: DISTL..................... 16MODEL: DISTL..................... 17STREAM SECTION......................................... 191 10 11 12 13..................................... 1914 15 16 17 18.................................... 212 3 4 5 6......................................... 237 8 9............................................. 25TABLE OF CONTENTSPROBLEM STATUS SECTION................................. 27BLOCK STATUS...................................... 27RUN CONTROL SECTIONRUN CONTROL INFORMATIONTHIS COPY OF ASPEN PLUS LICENSED TO CompanyTYPE OF RUN: EDITINPUT FILE NAME: INPUT PROBLEM DATA FILE NAME : _0040wxs VERSION NO. 1OUTPUT PROBLEM DATA FILE NAME: _2017toi VERSION NO. 1LOCATED IN:PDF SIZE USED FOR INPUT TRANSLATION:NUMBER OF FILE RECORDS (PSIZE) =0NUMBER OF INCORE RECORDSPSIZE NEEDED FOR SIMULATIONCALLING PROGRAM NAME:= 2561=apmain20
LOCATED IN:C:\PROGRA~1\ASPENT~1\ASPENP~\Engine\xeqSIMULATION REQUESTED FOR ENTIRE FLOWSHEETDESCRIPTIONGENERAL SIMULATION WITH METRIC UNITS : C, BAR, KG/HR, KMOL/HR,MMKCAL/HR, CUM/HR. PROPERTY METHOD: NONE FLOW BASIS FOR INPUT:MOLE STREAM REPORT COMPOSITION: MOLE FLOWFLOWSHEET SECTIONFLOWSHEET CONNECTIVITY BY STREAMSSTREAMSOURCEDESTSTREAMSOURCEDEST1E101E103F1012E102E104F10237R101F101F102P101T101T102E101E1038E104F101F102T101T102E105E102101113151649121417185P101F101E105T101T102R101R101R1016FLOWSHEET CONNECTIVITY BY BLOCKSBLOCKR101E104F101F102P101T101T102E105E101E102E103INLETSOUTLETS4 6 57788 141012131517110 911 121314 1517 161842536CONVERGENCE STATUS SUMMARYTEAR STREAM SUMMARY===================STREAMIDMAXIMUMERRORMAXIMUMERR/TOLVARIABLECONVTOLERANCEIDSTAT BLOCK21
14 PROPA01MOLEFLOW $OLVER01 = CONVERGED* = NOT CONVERGEDCONVERGENCE BLOCK: $OLVER01Tear Stream : 14Tolerance used: Trace molefrac: MAXIT= 30 WAIT 1 ITERATIONS BEFORE ACCELERATINGQMAX = +00 QMIN = FLOWSHEET SECTIONCONVERGENCE BLOCK: $OLVER01 (CONTINUED)METHOD: WEGSTEINSTATUS: CONVERGEDTOTAL NUMBER OF ITERATIONS:59NUMBER OF ITERATIONS ON LAST OUTER LOOP:0*** FINAL VALUES ***VARIABLEVALUEPREV VALUEERR/TOLTOTAL MOLEFLOW KMOL/HRAMMON01MOLEFLOW KMOL/HROXYGE01MOLEFLOW KMOL/HRACRYL01MOLEFLOW KMOL/HRACETO01MOLEFLOW KMOL/HRHYDRO01MOLEFLOW KMOL/HRWATER MOLEFLOW KMOL/HRCARBO01MOLEFLOW KMOL/HRCARBO02MOLEFLOW KMOL/HRPROPA01MOLEFLOW KMOL/HRPRESSUREBARMASS ENTHALPYKCAL/KG*** ITERATION HISTORY ***FLOWSHEET SECTIONCONVERGENCE BLOCK: $OLVER01 (CONTINUED)TEAR STREAMS:ITERATION MAXERR/TOL STREAM ID VARIABLE 123452675.2020.1924.1268.1414141414ACETO01MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWWATER MOLEFLOWACETO01MOLEFLOW22
671933.141414141414141414141414141414141414141414141414CARBO02MOLEFLOWACETO01MOLEFLOWACRYL01MOLEFLOWACRYL01MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWACRYL01MOLEFLOWCARBO02MOLEFLOWCARBO02MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWACRYL01MOLEFLOWCARBO02MOLEFLOWACETO01MOLEFLOWACRYL01MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWACETO01MOLEFLOWOXYGE01MOLEFLOWPROPA01MOLEFLOW891011121314151617181920212223242526272829COMPUTATIONAL SEQUENCESEQUENCE USED WAS:E102 E103 E101 R101 E104$OLVER01 F101 F102 P101 T101(RETURN $OLVER01)T102 E105OVERALL FLOWSHEET BALANCEFLOWSHEET SECTIONOVERALL FLOWSHEET BALANCE (CONTINUED)*** MASS AND ENERGY BALANCE ***INOUTGENERATION RELATIVE DIFF.CONVENTIONAL COMPONENTS(KMOL/HR )AMMON01
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