换热器设计外文翻译原稿(8)

发布时间:2021-06-11

234J.Guo,M.Xu/AppliedThermalEngineering36(2012)227e235

Table5

TheParetofrontobtainedbymulti-objectiveoptimizationdesignwith xedheatload.

do(m)

Multi-objective

0.0220.0220.0220.0220.0220.022

n283283283283283283

Bs1.001.001.001.000.950.91

q(rad)

2.3622.3492.3202.2992.2952.294

Tc,o(K)69.1469.2669.5369.7169.8670.00

Ko(W/m2K)1260.51263.11268.61272.51276.61280.2

C*0.4230.4220.4200.4190.4180.417

W(W)260.2260.2260.2260.3265.0270.2

0.6960.6970.7000.7030.7040.706

G*DT0.5050.5040.5030.5020.5010.500

G*DP1.581.581.581.581.611.64

ÂÂÂÂÂÂ1010À410À410À410À410À4

G*0.50520.50450.50290.50190.50100.5002

*Fig.10.TheParetofrontforheatexchangerwith xedheattransferarea:(a)G*DTversusGDP;(b)thepumpingpowerversustheexchangereffectiveness.

solutionsareavailableforthemulti-objectiveoptimization

approach,therefore,itprovidesmorealternativesforheatexchangerdesignthanthesingle-objectiveoptimizationapproach.4.Concludingremarks

Accordingtotheentransydissipationtheory,theentransydissipationcanbeusedtodescribetheirreversibilitiesinducedbyheatconductionand uidfriction,whilesuchirreversibilitiesarethemainfactorstodeterioratetheperformanceofheatexchanger.Therefore,inthepresentwork,basedontheentransydissipationtheoryandgeneticalgorithm,twooptimizationapproachesforheatexchangerdesignareproposed.Firstly,asingle-objectiveoptimizationapproachisformulated,wherethetotalentransydissipationnumberistakenastheobjectivefunction.Whentheheatloadis xed,thesingle-objectiveoptimizationdesigncansigni cantlyimprovetheperformanceofheatexchanger.However,forthe xedheattransferareacase,theimprovementofexchangereffectivenessthroughtheoptimizationprocessisattheexpenseoftheincreaseofthepumpingpower.Inordertoaddressthisproblem,themulti-objectiveoptimizationdesignofheatexchangerisestablished,wheretheentransydissipationnumbersrelatedtoheatconductionand uidfriction,respectively,aretakenastwoseparateobjectives.Incomparisonwiththesingle-objectiveoptimizationapproach,themulti-objectiveoptimiza-tiondesignofheatexchangercanachievethesameexchangereffectivenesswithlessconsumptionofpumpingpower.Further-more,themulti-objectiveoptimizationleadstothenon-uniqueoptimalsolutionswhichprovidemore exibilityfortheheatexchangerdesign.Acknowledgements

TheSupportofourresearchprogrambyNationalBasicResearchProgramofChina(ProjectNo.2007CB206900)isgreatlyappreciated.

References

[1]M.Yilmaz,O.N.Sara,S.Karsli,Performanceevaluationcriteriaforheat

exchangersbasedonsecondlawanalysis,exergy,AnInternationalJournal1(2001)278e294.

[2]I.Prigogine,IntroductiontoThermodynamicsofIrreversibleProcesses,Wiley,

NewYork,1967.

[3]A.Bejan,EntropyGenerationThroughHeatandFluidFlow,Wiley,NewYork,

1982.

[4]A.Bejan,EntropyGenerationMinimization,CRCPress,Florida,1996.

[5]V.Bertola,E.Cafaro,Acriticalanalysisoftheminimumentropyproduction

theoremanditsapplicationtoheatand uid ow,InternationalJournalof

3

HeatandMassTransfer51(2008)1907e1912.

[6]J.E.Hesselgreaves,Rationalisationofsecondlawanalysisofheatexchangers,

InternationalJournalofHeatandMassTransfer43(2000)4159e4204.

[7]Z.Y.Guo,X.G.Cheng,Z.Z.Xia,Leastdissipationinprincipleofheattransport

potentialcapacityanditsapplicationinheatconductionoptimization,ChineseScienceBulletin48(2003)406e410.

[8]Z.Y.Guo,H.Y.Zhu,X.G.Liang,EntransyeAphysicalquantitydescribingheat

transferability,InternationalJournalofHeatandMassTransfer50(2007)2545e2556.

[9]G.Z.Han,Z.Y.Guo,Physicalmechanismofheatconductionabilitydissipation

anditsanalyticalexpression,ProceedingoftheCSEE27(2007)98e102(inChinese).

[10]S.P.Wang,Q.L.Chen,B.J.Zhang,Anequationofentransytransferandits

application,ChineseScienceBulletin54(2009)3572e3578.

[11]Q.Chen,J.X.Ren,Generalizedthermalresistanceforconvectiveheattransfer

anditsrelationtoentransydissipation,ChineseScienceBulletin53(2008)3753e3761.

[12]Q.Chen,M.Wang,N.Pan,Z.Y.Guo,Optimizationprinciplesforconvective

heattransfer,Energy34(9)(2009)1199e1206.

[13]S.J.Xia,L.G.Chen,F.R.Sun,Optimizationforentransydissipationminimization

inheatexchanger,ChineseScienceBulletin54(2009)3587e3595.

[14]J.F.Guo,M.T.Xu,L.Cheng,Principleofequipartitionofentransydissipationforheat

exchangerdesign,ScienceChinaTechnologicalSciences53(2010)1309e1314.[15]X.B.Liu,J.A.Meng,Z.Y.Guo,Entropygenerationextremumandentransy

dissipationextremumforheatexchangeroptimization,ChineseScienceBulletin54(2009)943e947.

[16]J.F.Guo,M.T.Xu,L.Cheng,Thein uenceofviscousheatingontheentransyin

two- uidheatexchangers,ScienceChinaTechnologicalSciences54(5)(2011)1267e1274.

[17]J.Wu,X.G.Liang,Applicationofentransydissipationextremumprinciplein

radiativeheattransferoptimization,ScienceChinaTechnologicalSciences51(2008)1306e1314.

[18]X.B.Liu,M.Wang,J.Meng,E.Ben-Naim,Z.Y.Guo,Minimumentransydissi-pationprincipleforoptimizationoftransportnetworks,InternationalJournalofNonlinearSciencesandNumericalSimulation11(2)(2010)113e120.

换热器设计外文翻译原稿(8).doc 将本文的Word文档下载到电脑

精彩图片

热门精选

大家正在看

× 游客快捷下载通道(下载后可以自由复制和排版)

限时特价:7 元/份 原价:20元

支付方式:

开通VIP包月会员 特价:29元/月

注:下载文档有可能“只有目录或者内容不全”等情况,请下载之前注意辨别,如果您已付费且无法下载或内容有问题,请联系我们协助你处理。
微信:fanwen365 QQ:370150219