国内外干式厌氧发酵技术与工程现状梁芳

[e-mail]梁芳1，包先斌1，王海洋1，陈祥21．3100512．310058、。、。TK6S216．4A1000－1166201303－0044－07CurrentSituationofDryAnaerobicFermentationTechnologyandtheProjectsinDomestic＆Abroad/LINAGFang1BAOXian-bin1WANGHai-yang1CHENXiang2/1．ZheJiangDunAnArtificialEnvironmentCo．Ltd．Hangzhou310051China2．CollegeofBiosystemsEngineeringandFoodScienceZhejiangUniversityHangzhou310058ChinaAbstractThedryanaerobicfermentationtechnologyhasahistoryofmorethandecadeinChinabutithasnolarge-scaleindustrializedprojects．ThispapermainlyoutlinedthecurrenttechnologiesandprojectsinChinaandtheirprogresses．Thematuredtechnologiesandrealengineeringcasesinforeigncountrywereanalized．And4kindsofengineeringtechniqueswerecomparedandsummaried．Allaretoprovidereferencefordevelopingdryanaerobicfermentationtechnologyinourcountry．Keywordsdryanaerobicfermentationforeigntechnologyproject20%～40%1。20108.47。201070．6%5。、1．2217．8%2～3。4。。34400。180。1。、、、、、130%～40%20%～40%20%～40%、44ChinaBiogas2013313、5～6。。、。、。7。1．2．3．4．5．6．7．8．9．10．11．12．13．14．①～⑧1“”“”188。2BIOFerm、Valogra、Kompogas。2．1德国车库型工艺BIOFermBEKON9～10。BIOFermViessmann1917BIOFerm。BIOFerm25%～35%28。。、、、。Wisconsin-Osh-kosh。2BIOFerm3BIOFerm。2BIOFrem54ChinaBiogas20133133BIOFremBEKON1、2。60%、3、。BEKON4pH56。。4。2．2法国Valorga工艺ValorgaInternationalS．A．S．11URBASERSA。19815。7、18。231228160。、。55%～58%30158．5。4BEKON5。37℃54℃316m22m64ChinaBiogas201331320～305200。1。55%～58%40%。158．5m365%35%2000～3000ppm200ppm。4MW。5ValorgaValorga2．3比利时Dranco工艺DrancoDryAnaerobicCompostingOrganicWasteSystems12。Dranco、SordisepDranco-farm。Dranco/SordisepDrancoDranco-farm、。10～20kgCOD·m－3d－148℃～57℃35℃～40℃15～30d100～200Nm3·t－1220～440kWh·t－1。15%～40%。Dranco-Sep5%～20%。6DrancoDranco、。6DrancoDranco74ChinaBiogas2013313、、、。1424Dranco3000t·a－1180000t·a－1。Brecht、70000t·a－1。2．4瑞典Kompogas工艺Kompogas13HCF。1415～18d。TS30%～45%VS55%～75%ofTS＜40mmpH4．5～7＜4g·kg－1C/N＞18。55°C。。7Kompogas。7Kompogas2．5德国林德BRV工艺LindeBRV14Kompogas8。。20%45%。BRVKompogas。84ChinaBiogas20133138BRV32。2Valorga1．、。2．。3．55%～58%。4．30d。5．。1．。。2．、。Dranco1．10～20kgCOD·m－3d－1。2．50℃～58℃35℃。3．15～30d。4．。1．。2．。3．。Bioferm1．。2．50～300ppm。3．。4．。1．。2．。3．。4．。5．。Kompogas1．。2．15～30t·d－160t·d－1。3．5～8cm15～18d。1．。2．。。490%ValorgaDranco。。、、。。、、。6094ChinaBiogas20133133。。。。、、。Z3、。1．J．20073541089－1091．2．J．2009266137－138．3．J．201230341－44．4．J．200826530－32．5．J．201129551－54．6．J．200927143－46．7．J．2011147－48．8．J．2001332103－106．9．J．200826436－37．10．J．20065櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵櫵36－38．491．J．201028510－14．2．J．20102831－5．3．J．20011933－8．4．J．2007134586－585．5．D．2009．6．D．2008．7．J．200824276－7996．8〗．J．20082410100－104．9．J．2012131．10LutzP．NewBEKONBiogastechnologyfordryfermenta-tioninbatchprocessJ．BEKONEnergyTechnologiesGmbH＆CoKG2010203－06．11FruteaudeLaclosHDesboisSSaint－JolyC．Anaero-bicdigestionofmunicipalsolidorganicwasteValorgafull－scaleplantinTilburgTheNetherlandsJ．Waterscienceandtechnology1997366457－462．12DeBaereL．TheDRANCOtechnologyauniquedigestiontechnologyforsolidorganicwasteJ．OrganicWasteSystemsOWSPub2010475－77．13WellingerAWyderKMetzlerAE．Kompogas－anewsystemfortheanaerobictreatmentofsourceseparatedwasteJ．WaterScienceTechnology1993272153－158．14FrickeKSantenHWallmannR．Comparisonofselect-edaerobicandanaerobicproceduresforMSWtreatmentJ．Wastemanagement2005258799－810．06ChinaBiogas2013313