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ResearchStatusOfTheTreatmentTechnologyOfBreweryWastewaterEnvironmentalengineeringJiaGuiyunPoint
IntroductionTheusualprocessCasesofengineeringprojectBackgroundSourceCharacteristicdischargestandard1IntroductionbrewerywastewaterBackgroundProducing1tbeerwillconsume10~30m3freshwateranddischarge10~20m3wastewater.Theconcentrationoforganicmatteristhousandstimesmorethanthelifewastewater.Withtheimprovementofbreweryindustry,theproductionhadreached30millionperyearinChina,morethantheU.S.Alongwiththeexpansionofthescaleofthebreweryfactories,thedischargeofbrewerywastewaterisalsoincreasing.60%Source-Wastewatercomefrom?10%30%Theprocessofbrewing,suchasCrushingandseparatingprocessofmalt,etcRawmaterialofwheatcleaning,maltcultivationandthewashingwater(oldbottleswashing,Filterwashingandsoon.)domesticsewageandothersdeepLargeemissionGoodbiodegradabilityBODchromaticitysolidOrganicmattersuspendedprocessEntertextCODLargeemission,varyfromtheproductionprocessandlevels.Ahighconcentrationofororganicmatter(BOD5/COD)andsuspendedsolid(SS);Chromaticitydeep.Goodbiodegradability.CharacteristicIndustrialStandardCODBOD5SSNH3-NTPpHWasteemissionsperunitofproduct(kg/t)0.560.140.490.1050.0216~9standardvalue(mg/L)8020701536~9Table1.EmissionstandardofBreweryWastewater2TheusualprocessTreatmentofbrewerywastewater
AdsorptionBiodegradation(A-B)SequencingBatchReactor
(SBR)CyclicActivatedSludgeTechnology(CAST)BiologicalAeratedFilter
rotating
disc
bio-filterbiologicalcontactoxidationprocessUpflowAnaerobicSludgeBed(UASB)internalcirculation(IC)UBF(AF+UASB)Threetypes:Activatedsludgebiomembraneprocessanaerobicbiotreatment
AdsorptionBiodegradation(A-B)----case1SequencingBatchReactor
(SBR)CyclicActivatedSludgeTechnology(CAST)---case3BiologicalAeratedFilter----case4
rotating
disc
bio-filterbiologicalcontactoxidationprocessbiologicalcontactoxidationprocessUpflowAnaerobicSludgeBed(UASB)----case4internalcirculation(IC)----case2UBF(AF+UASB)UBF(AF+UASB)Threetypes:Activatedsludgebiomembraneprocessanaerobicbiotreatment3CasesofengineeringprojectCASES
OneTwoThreeFourICCASTA-BUASBCASES
OneTwoThreeFourICCASTA-BUASBCase1:camefromPEARLRIVERAdsorptionBiodegradationHignoftheremovalrateofCOD,BOD5Quantityofwastewatereffluent:8000~9000m3/dCODcrBOD5SSpHInlet(mg/L)≤2000≤1000≤5004.5~10Outlet(mg/L)≤110≤50≤706~9%≥99≥95≥86-Case1:camefromPEARLRIVERAdsorptionBiodegradationinflowrotary
screenregulatingpoolLiftpumpoutletsludgethickenersludgepressingexcesssludgeclean
water
basinsludgerecycleA
-aeration-tankA-
sedimentation
basinB
-
sedimentation
basinB1
-aeration-tankB2
-aeration-tankCASES
OneTwoThreeFourICCASTA-BUASBCASES
OneTwoThreeFourICCASTA-BUASBCase2:Foster`s
IC-CIRCOX
ShanghaiFostinflowInletwellrotary
sievepumpCIRCOXICinclined-tube
sedimentationtankpumpPreacidificationtankoutletpumppumppumpmethaneflocculantsludgeacid-base
nutritional
agentsCase2:Foster`s
IC-CIRCOX
Fornitrogen-containinganddegradation-resistantcompound.LittlesurplussludgeLessoccupiedareaCODcrBOD5SSNH3-NpHInlet(mg/L)1000-3000600-1875100-60012~454~10Outlet(mg/L)50-10≤3010-1005~156~9%95-99≥9590-9867-CASES
OneTwoThreeFourICCASTA-BUASBCASES
OneTwoThreeFourICCASTA-BUASBCODBODSSInlet(mg/L)1390-2250672-1150425-762Outlet(mg/L)25-8621-2552-64%96-9897-9888-92Case3:CASTMEIXUEBEERIntermittentoperationMediumconcentrationorganicwastewaterNo
SludgebulkingCase3:CASTMEIXUEBEERinflowGrillewellWaterregulatingpoolLiftpumpCASTsludgethickenersludgepressingsupernatantexcesssludgeWateroutletoutward
transportsludgerecycle
air
blowerCASES
OneTwoThreeFourICCASTA-BUASBCASES
OneTwoThreeFourICCASTA-BUASBWorkunderthelowtemperaturesmalloccupationareaSimplestructure,savethecostCase4:UASB+QINGDAOBEERCODcrBOD5SSNH3-NpHInlet(mg/L)1300-2000-300-80012~456~9Outlet(mg/L)70-150-40-1004.966.5~8.5%80--67-Case4:UASB+QINGDAOBEERBrewerywastewaterGrillewellregulatingpoolprimary
clarificationAerationtank
UASBsludgeSludgethickenersludgemicrostrainerclarificationsludgepressingtransportmethane处理路线主要参数主要构筑物进水水质(mg/L)处理要求(mg/L)项目所在地A-BQ=8000~9000m3/d调节池、AB段曝气池、沉淀池、污泥处理BOD5=1000COD=2000-珠江啤酒厂CASTQ=1000m3/d格栅、集水调节池、CAST反应池、滗水器、曝气鼓风系统、污泥系统BOD5,672~1150COD,1390~2250CODc
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