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34220113JOURNALOFAGRICULTURALUNIVERSITYOFHEBEI Vol.34No.2Mar.2011:1000-1573(2011)02-0124-07路金喜1, 马恒泽1, 王德宏2, 李宏伟1, 王彦惠1, 陈 丽1*(1.,071001;2.,071001):1。:,,,,。,。 :;;;;:TU992.3:AAtreatmentprocessofthesewageeco-situpurificationandreuseforcitiesandtownssewageLUJin-xi1,MAHeng-ze1,WANGDe-hong2,LIHong-wei1,WANGYan-hui1,CHENLi1(1.CollegeofUrbanConstruction,AgriculturalUniversityofHebei,Baoding071001,China;2.BaodingYidaEnvironmentEngineeringTechnologyLimitedCompany,Baoding071001,China)Abstract:Atreatmentprocessofthesewageeco-situpurificationandreuseforcitiesandtownssewageisputforward.Theexperimentdemonstratesthatthistreatmentprocess,whichcom-binestheanaerobicbiochemicaltechnologyandartificialwetlandtechnology,cannotonlyin-creasebiodegradationrateremarkably,butalsoimprovethequalityofsewagepurificationsig-nificantly.Inaddition,thisprocesscanbeusedforreclaimedwaterandthereforebeautifyeco-logicalenvironmentandlandscapeofthehousingestate.Comparedwiththeprocessofcentral-izedtreatment,thiseco-situpurificationandreusetreatmentprocessofthesewageismoree-conomicalandsuitable.Keywords:granularsludge;constructedwetlands;sewage;landinfiltration;organism ,,、,。、,1t1000~1500,0.8~1.0,,10t,1.0~1.5,*:2010-09-20:(2006-259).:(1957-),,,. 2 :3000~5000[1],,,。,1。,1。,、,。2060,70;,400;80%[2-3]。,1。,,、,《》、《》,。,、。,,、、,、[4-5]。1 工艺流程设计1.1 (1)、,,。,、,、、、。(2),,,,,,,。(3),,“”。(4),,,,,。1.2 、,1。1。1,①;②;③;④;⑤;⑥;⑦;⑧;⑨;⑩;11;12;13;14;15;16;17;18;19;20;21;22;23;24;25;26;27;28。1 Fig.1 Thediagramofthetreatmentprocessofthesewageeco-situpurificationandreuseforcitiesandtownssewage4:、,、、3,、,;3,3;。。、,、、,。125 34,,,,,,,,,,,,,,3,,,,,,,。。,,,,,、、、,、。,,,,,,,,,,,,,,,。,。,。,,,。2 结果与分析,:3m3,65m2,75m2,。60d,。1,23,3。2.1 ,,15~36℃,、。2.2 HRT2.5、5.5、8.5、11.5h,44、20、13、9.6cm/d,3,HRTCOD、SS、NH3-N,1。1,COD、SS、NH3-N,HRT。NH3-NHRT5.5h,,HRT5.5hNH3-N;COD、SSHRT5.5h,。,5.5h,20cm/d。1 、Table1 Indexesremovalofdifferentoperatingtemperatureandhydraulicretentiontime15~25℃/%Operatingtemperature15~25℃eachindexremovalrate26~36℃/%Operatingtemperature26~36℃eachindexremovalrate/hTime IndexCODSSNH3-N/hTime IndexCODSSNH3-N2.58497712.58898765.58998755.59499.5838.59299.5798.59599.88611.59399.98411.59699.990126 2 :2.3 COD,COD2。2,,COD,3~4℃,COD2~3%,32~36℃COD78%~83%,。[8],COD。24~36℃,。2,COD250~320mg/L16~39mg/L。2 CODTable2 CODIndexdataofeachtestsamplemouth/℃Temperature Dataofeachtestsamplemouth1/(mg·L-1)Dataofsamplemouth12/(mg·L-1)Dataofsamplemouth22/%Removalrateofsamplemouth23/(mg·L-1)Dataofsamplemouth33%Removalrateofsamplemouth315~19250~30080~8468~7230~3962~6520~23280~31081~8769~7429~3763~6724~27270~32074~7972~7723~2666~7128~31258~31262~6975~8017~2267~7432~36275~31854~6578~8316~1971~772.4 NH3-N、TNTPNH3-N、TNTP3、4、5。3、4、5,,,,,。2.5%~8%,,。0.2%~5.1%,,,,[9-10]。NH3-N、TNTP,NH3-N、TNTP。NH3-N、TN。,。TP,,,、,。3 NH3-NTable3 NH3-Nindexdataofeachtestsamplemouth/℃Tempeature Dataofeachtestsamplemouth1/(mg·L-1)Dataofsamplemouth12/(mg·L-1)Dataofsamplemouth23/(mg·L-1)Dataofsamplemouth33/%Removalrateofsamplemouth315~1916~2318~254.0~8.071~7520~2318~2521~276.0~7.074~7824~2716~2518~284.5~6.076~8028~3116~2518~284.0~5.078~8332~3616~2518~282.2~4.080~87127 344 TNTable4 TNIndexdataofeachtestsamplemouth/℃Temperature Dataofeachtestsamplemouth1/(mg·L-1)Dataofsamplemouth12/(mg·L-1)Dataofsamplemouth22/%Removalrateofsamplemouth23/(mg·L-1)Dataofsamplemouth33%Removalrateofsamplemouth315~1918~2918~282.5~5.74.9~7.674~7620~2320~3820~363.0~6.35.0~7.676~7824~2721~3921~373.8~6.94.5~6.779~8228~3121~3921~364.5~7.84.0~5.581~8532~3622~3922~364.8~8.03.1~5.082~865 TPTable5 TPIndexdataofeachtestsamplemouth/℃Temperature Dataofeachtestsamplemouth1/(mg·L-1)Dataofsamplemouth12/(mg·L-1)Dataofsamplemouth22/%Removalrateofsamplemouth23/(mg·L-1)Dataofsamplemouth33%Removalrateofsamplemouth315~194.0~5.54.0~5.40.2~2.00.47~0.6588~9120~234.2~6.04.1~5.80.8~2.90.45~0.5889~9224~274.7~6.34.6~6.11.7~3.50.43~0.5690~9328~314.8~8.04.7~7.62.8~4.60.42~0.5691~9432~364.8~6.44.7~6.13.0~5.10.32~0.5790~952.5 SSSS6。6,,85%~96%。,,。SS,,SS130~180mg/L1.2~3.5mg/L。6 SSTable6 SSIndexdataofeachtestsamplemouth/℃Temperature Dataofeachtestsamplemouth1/(mg·L-1)Dataofsamplemouth12/(mg·L-1)Dataofsamplemouth22/%Removalrateofsamplemouth23/(mg·L-1)Dataofsamplemouth33%Removalrateofsamplemouth315~19140~18018.4~25.585~912.0~3.585~6920~23135~17016~2392~941.8~2.589~9224~27130~18012~1793~951.2~1.991~9328~31130~18012~1793~961.2~1.892~9532~36135~18013~1794~961.2~1.793~953 城镇生活小区污水生态处理回用可行性分析3.1 ,、,,,,,,。,,、,、、、、128 2 :,;,。,[9,11]。3.2 ,,。7,7,、,,,,,,39%~42%;,,,21%~26%。。7 Table7 IninvestmentoperationcosttownsewageecologicaltreatmenttechnologycomparewithconventionaltechnologyTreatmentmodeSewagreuseinvestmentSwerageandwaterrecoverynetworkinvestmentSewagereuseunningcosts2500~35002500~40001.4~2.71800~2800180~3500.3~0.73.3 ,1,。,201050%,30%[10,13]。,,、、、。,,。。,。,35,,。,。,,、,,。4 结论,,;、,。,,,、;,,,,。:[1] .[J].,2006(6):19-22.[2] DavidSteer,LauchlanFraser,JamesBoddy.Efficiencyofsmallconstructedwetlandsforsubsurfacetreat-mentofsingle-familydomesticeffluent[J].EcologicalEngineering,2002(18):429-440.[3] KeithRHench,GaryKBissonnette,Alan
本文标题:城镇生活小区污水生态原位净化回用处理工艺研究
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