环境工程专业英语Ananaerobichydrogenfermentationsystemwithathermophilicflow-throughreactor(55oC)forhydrogenproductionandaboilingretentionvessel(100oC)forcontinuousheattreatment,(HRTs),mercialhydrogenisalmostproducedfromsteamreformingofnaturalgasesandgasificationofcoal,buttheserequirehigh-energyinputsobtainedfromnon-,,,,andthetemperaturesoftheinjector,detector,andcolumnwere80,90,and50oC,-fromboththeflow-throughandtheretentionreactor,andtheproperties,includingpH,alkalinity,COD,VSS,VS,andTS,ofordingtotheStandard.(1)and(2)respectively.[(massSCOD/d)effluent−(massSCOD/d)influent]/[(massPCOD/d)influent−(massPCOD/d)effluent](1)[(massVFA/d)effluen−(massVFA/d)influent]/[(massSCOD/d)effluen−(massSCOD/d)influent](2)HydrogenProductionHydrolysisandVSReductionVFAProductionandHydrogenYieldResultsandDiscussionHydrogenProductionHydrogenProductionthehydrogenproductionratewasquicklyincreasedandapproachedtosteadystatewithinthe10thdayoftheoperationat1dayHRT,aproperHRTisalsoveryimportanttoobtainhigherhydrogenproduct
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