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188宝金博页面版: 工业流化床乙烯共聚合生产过程中牌号切换的最优化研究 study on optimal strategy of grade transition in industrial fluidized bed ga

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内容提示: Chi ㈣JChvm .Eng,i i ( 1j 1—8( 2003)St udyonO pti m al Strategyof G rade Transi ti oni n Industri alFl ui di zed Bed G as.Phase Pol yet hyl eneProduct i on ProcessW AN GJ i ngdai ( t靖岱) andYAN GYongrong( 阳水荣) +D epartm ent of ohem |calEngi neerl ng,Zhej i angU nl versi %y,H angzhou 310027,Chi na了&{万禽AbstractD roduct i on D rocessby theopti m i zati onof operat i ag vari abl es,such晒pol ym eri zatl on t铀pera札re,the rati o ofhydrogeato ethyl ene,the rari o of co- m onom erreel %fl ow ( M FR) .ui nduded i n"o...

文档格式:PDF | 页数:8 | 浏览次数:8 | 上传日期:2015-02-15 12:57:12 | 文档星级:
Chi ㈣JChvm .Eng,i i ( 1j 1—8( 2003)St udyonO pti m al Strategyof G rade Transi ti oni n Industri alFl ui di zed Bed G as.Phase Pol yet hyl eneProduct i on ProcessW AN GJ i ngdai ( t靖岱) andYAN GYongrong( 阳水荣) +D epartm ent of ohem |calEngi neerl ng,Zhej i angU nl versi %y,H angzhou 310027,Chi na了&{万禽AbstractD roduct i on D rocessby theopti m i zati onof operat i ag vari abl es,such晒pol ym eri zatl on t铀pera札re,the rati o ofhydrogeato ethyl ene,the rari o of co- m onom erreel %fl ow ( M FR) .ui nduded i n"obeobj ecti vef unctl oq,[ or rcstral ni ngthesharp edl ustm cntand narrow i ngthe di stri buti on of m ol ecul ar w ei ghtof the resi nbed l evel 时e decreased i n orderThi s。D tl m l zati onprobl emi s sol ved by an al gori thmof sequenti al quadrati c program m i ng( SQ P) i n M ATLABThere bconsi derabl e di f i ef ence betw een the forw ard transi ti on and reversetransi ti onofgradew i t h regardto theoD erat i ngvari abl es due to thenon- l i neari ty of thesystem .The gradetransi ti on m odelti Ineyi el d( STY) process w i t h the so- cal l ed condensed m odelm ul ti .producttheopti m al gradetransi ti on roodel .A曲quenti al transi ti onof si x com m erel alanopti m al m ul ti - product operati on.Keyw ordspol ym er,conti nuous pol ym eri zati on,gradetransi ti on,m ul ti —product operati on,tw o- l evel opti m i zati onA m odelof grade transi ti on hpresent edThequant i t y of off-speci fi cati on productfor a com m erci al i zed fl ui di zed bed gab- phase poLyet hyLeneandthe ti m e of gradetransi ti on can be m i ni m l 20dto ethyf exxe,f eed rate of catal yst,andbed l evelAnewperf orm ance i ndext the rati oolof operat i onvari abl esi s recon2rnended thatItcatal ystf eedrate andto reduce the gradetransi ti on ti m e and the quant i t y of off-speci fi cati on producti s ext endedto ahi gh spaceoperat i on.I n theend,al l opti m i zati on strategyfortransi ti on i s propodedw i t h tw o- l evelopti m i zati onof the obj ecti ve f unct i onJ ( z,u) onthe basi s ofpol yet hyl enegradesi s l l l ustrated for1 I N TRoD U CTI oNToday pl asti c pol ym ersO U S ki nds ofproducts.sucha8partsfor cars、dl i ferentki nds ofbottl es,fi l m s and fram esances.Each usage requi res di fi erent pol ym ers w i thsom edesi gnated speci fi cati ons.Inorder to m eet thesedem ands,pol ym et com pani es often have toproducevari ousgradesof apol ym er.Therefore m any typesofpol yethyl eneshoul d beproducedi n asystemw i thor severalreactors.Thi s i nvol vescess operati onthat i s cal l edgrade transi ti on.The fre-quencyandm agni tudeofgradetransi ti ons D.reusual l ydeterm i nedbyboth thepri ceand m arket dem ands forpol ym ers,G rude transi ti on l eadsoff-specti fi cati on pol ym ers to beproducedsi ncegradechangeover w oul d be m ade som eti m eseverya fewdaysand the transi ti on ti m eof pol ym etphase pol yethyl ene reactor i s general l y from10 to 30hours.Iti svery i m portantcom panytoperformagood gradetransi ti onopera-ti on ai m ed atproduci ng l ess off-specti fi cati on po妒m etand/or reduci ngof the ti m e of grade transi ti onsi nce the m arketspecti fl cati on pol ym ers D i e qui tedi 船rentl l |.Si ncl ai rhas outl i ned som epracti cm aspectsthegrade transi ti on probl em l Ⅲ.Ray m adedynam i csi reul ati ous offor t w o fl ui di zed.bed reactors,and theydeterm i nedthatthecatal ystfeedrate,hydrogenfeedrate,andbl eed fl ow rate are i m portantarew i del yused asvari -f or el ectri c appl i -ouea speci alpro-t o a97reatdesl ofi 12 an i ndustri algasforapol ym er-produci ngpri cesofon-specti ti cati on and off-ofRam anathan andgradetransi ti onvari abl es foraccom ,pl i shi ng rapi dstone for opti m alsol vi ngl em .M cAul eyandM acG regorfi rst obtai nedopti m algradetransi ti on strategi esl ene reactort5J .0hshi m atransi ti ons LSJ.gradetransi ti on strategy[ 4J.a dynam i c m odel - basedAndi t w asam i l e—Byopti m i zati on prob—i nal so conductedal oop and gas· phaseagas phase pol yethy—opti m algrade-transi ti on strategi espol ypropyl enereactorby usi ng dynam i c progranl m i ngaftersi l npl i fyi ngthe correl ati on m odel s ofpol ypropy-l ene resi nspeci fi cati on ofAl thoughcorrel ati on m odel s w i th the vari ati on of m el ti ndex(M I),densi ty, tem peraturesandgasCO ncentra-ti ons i n the reactor m ake opti m i zati on to be sol vedeasi l y, M cAul ey andM acG regorD] 、O hshi m a[ 6J di dnotful l y characteri ze other speci ti cati ons ofsuch as m ol ecul arw ei ght di stri buti on( M W D) De.bri nge£alsi m ul ated grade-transi ti on operati ons forvari ous ki nds of pol ym eri zati on process by usi ng thedynam i csi m ul ati onpackage“ PO LYRED ” 川TakedaandRay al so si m ul ated the opti m al grade-transi ti onstrategi estots w i th bi m odal products by usi ng“ PO LYRED ” ( slH ow ever,them ethods adopted i nRefs.『7, 81to obtsi ntheopti m alInthi s study, several i m provem ents ou the basi sofM cAul eyandM acGregor’ s grade transi ti on m odel [5】are m ade to obtai n theopti m um profi l es for gradetransi ti oneffecti vel y.Fi rst( M FR) i s consi dered i n t heopti m al grade transi ti onm odel because M FRdi rectl y refl ects the di stri buti oni nm ei ti ndex anddeusi ty[ Slapol ym er,form ul ti stageol 胡npol ym eri zati on reac-sol uti on areti m e.consum i ng.ofal l ,m el tfl ow rati oRecei ved2002· 02- 11,accepted 2002- 11- 08.Tow homcorrespondenceshoul d be addre"ed.E-m ai l :yryangO m ai l .hz.羁j .cn’ 万方数据

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