毕业设计餐厨垃圾厌氧的外文文献.docx
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毕业设计餐厨垃圾厌氧的外文文献
Solidstateanaerobicco-digestionofyardwasteandfoodwasteforbiogasproduction
DanBrown,YeboLi﹡
DepartmentofFood,Agricultural,andBiologicalEngineering,TheOhioStateUniversity/OhioAgriculturalResearchandDevelopmentCenter,1680MadisonAve.,Wooster,OH44691-4096,UnitedStates
HIGHLIGHTS
▲Solidstateanaerobicdigestion(SS-AD)offoodwasteandyardwaste.
▲Thehighestmethaneyieldswereobtainedatfeedstock/effluent(F/E)ratio1.
▲IncreasingF/Eratiofrom1to2and3causeddecreasesinmethaneyield.
▲TheADwasupsetatF/Eratio3exceptyardwasteonly.
ABSTRACT
FoodandyardwastesareavailableyearroundatlowcostandhavethepotentialtocomplementeachotherforSS-AD.Thegoalofthisstudywastodetermineoptimalfeedstock/effluent(F/E)andfoodwaste/yardwastemixingratiosforoptimalbiogasproduction.Co-digestionofyardandfoodwastewascarriedoutatF/Eratiosof1,2,and3.ForeachF/Eratio,foodwastepercentagesof0%,10%,and20%,basedondryvolatilesolids,wereevaluated.Resultsshowedincreasedmethaneyieldsandvolumetricproductivitiesasthepercentageoffoodwastewasincreasedto10%and20%ofthesubstrateatF/Eratiosof2and1,respectively.Thisstudyshowedthatco-digestionoffoodwastewithyardwasteatspecificratioscanimprovedigesteroperatingcharacteristicsandendperformancemetricsoverSS-ADofyardwastealone.
2012ElsevierLtd.Allrightsreserved.
Keywords:
Solid-stateanaerobicdigestion,Biogas,Municipalsolidwaste,Foodwaste,Co-digestion
1.Introduction
Solid-stateanaerobicdigestion(SS-AD)hasbeensuccessfullyusedtoconvertvariouslignocellulosicbiomassfeedstockstobiogas(Lietal.,2011a).SS-ADhasbeenthedominantADsysteminstalledinEuropesincetheearly1990sforthetreatmentofmunicipalsolidwaste(MSW),andtypicallyoperatesat15–50%totalsolids(TS)content(Lietal.,2011b;BaereandMattheeuws,2008;Guendouzetal.,2010).SS-ADprovidesmanybenefitsoverliquidADindigestinglignocellulosicbiomasssuchastreatingmoreorganicsolidsinthesamesizedigesterandproducingacompost-likefinishedorganicmaterialthatiseasiertohandleandcanbeappliedtoagriculturallandforfertilizer(Martinetal.,2003a;Lietal.,2011b).TheSS-ADsystemalsofeaturesfewermovingpartsandlowerenergyinputsneededforheatingandmixing(Lietal.,2011a),andithasagreateracceptanceofinputscontainingglass,plastics,andgrit.Furthermore,SS-ADcanovercomeothercommonproblemsexistingintheliquidADprocesssuchasfloatingandstratificationoffats,fibers,andplastics(Chanakyaetal.,1999).
Thestart-upperiodofanSS-ADsystemisconsideredthemostcriticalphaseinbatchdigestion.Thefeedstock/effluent(F/E)ratio,anoperatingparameterthatmeasurestheamountofsubstratetotheamountofinoculumonadryvolatilesolids(VS)basis,hasbeenshowntobeacriticalfactoraffectingtheperformanceofSS-AD(Lietal.,2011b).SS-ADmayrequireupto50%ofdigestedresidueforarapidstartup,whichdecreasesreactorutilizationefficiency(Martinetal.,2003b;Rapportetal.,2008;Lietal.,2011b).Ahighlyconcentratedandactiveinoculumsourceisimportanttoreducedigestiontime,improvedigesterefficacy,andincreaseTSinthefinishedproduct(Forster-Carneiroetal.,2008).
Co-digestionofmixedsubstratesoffersmanyadvantages,includingecological,technological,andeconomicbenefits,comparedtodigestingasinglesubstrate(Rughoonundunetal.,2012).However,combiningtwoormoredifferenttypesoffeedstocksrequirescarefulselectiontoimprovetheefficiencyofanaerobicdigestion(álvarezetal.,2010).Thepurposeofco-digestionistobalancenutrients(C/Nratioandmacro-andmicronutrients)anddiluteinhibitors/toxiccompoundstoenhancemethaneproduction(Hartmannetal.,2004;Sosnowskietal.,2003).
XuandLi(2012)foundthatanF/Eratioof2achievedhigheraccumulativemethaneyieldsthanathigherF/Eratiosof4and6forthesamedogfoodtocornstoverratio.Thestudyalsofoundthatco-digestionimprovedmethaneyieldcomparedwithusingcornstoverordogfoodasthesolesubstrateduetoimprovementsinreactorcharacteristics.Thestudyalsoconcludedthatco-digestionofdogfoodwithcornstoverreducedstart-uptimeandvolatilefattyacid(VFA)accumulationinSS-AD.AstudybyEl-MashadandZhang(2010)foundthatinclusionoffoodwaste,atratesofupto60%offeedstockVS,withdairymanureresultedinhigherbiogasyieldsandproductionratesascomparedtothedigestionofdairymanurealone.Panichnumsinetal.(2010)examinedthepotentialofco-digestionofcassavapulpwithpigmanureusingasemi-continuouslyfed,stirredtankreactor.ThestudyfoundamaximummethaneyieldandVSremovalof306L/kgVSaddedand61%,respectfull