A2OMBBR组合工艺处理工业园区污水何丹

整理文档很辛苦,赏杯茶钱您下走!

免费阅读已结束,点击下载阅读编辑剩下 ...

阅读已结束,您可以下载文档离线阅读编辑

资源描述

A2O+MBBR330039A2O+MBBR、、、6h3hA2O12h3h、3h、6hMBBR12h4.2h30min15℃A2O+MBBRCODCr、BOD5、SS、NH3-NTN88%、93.3%、95%、84%71.4%《》GB18918-2002B。A2OMBBR0。。MBBRKaldnesMi-jecpteknogiSINTEF。MBBRMBBR1-3、4-5、6-7、8、9、10。A2O+MBBRA2O+MBBR。1MBBR1.1MBBRMBBR、。。1.2MBBRMBBRCNP。1.3MBBRMBBR1、20-40%。2MBBR、。3MBBR。4。5。1.4MBBRMBBRA/O+MBBR2、22UASB+MBBRABR/MBBRMBBR+FentonA2O+MBBR、2、MBBRCOD、NH3-NTN。22.1、、、、、、。1。2920156DOI:10.14127/j.cnki.jiangxihuagong.2015.06.0241mg/LpHpHCODBOD5NH3-NSSTN6~9≤500≤300≤50≤400≤70TP≤830.51.00.52.2++++A2O+MBBR++1。12.3A2OA2O、、MB-BRMBBR。2.4A2O+MBBR2。21Vmax=0.74m/s26h36h43h56h6A2/OT=15℃12h3h3h6h14d7MBBRT=15℃12h16d84.2h930min2.5A2O+MBBR3。3CODCrBOD5SSNH3-NTNmg/L%mg/L%mg/L%mg/L%mg/L%+500—300—400—50—70—30040195356085451063102806.71807.760—401163—A2O+MBBR+≤6079≤2089≤2067≤880≤2068GB18918-2002B60882093.320958842071.42A2O+MBBRCODCr、BOD5、SS、NH3-NTN88%、93.3%、95%、84%71.4%《》GB18918-2002B。3A2O+MBBR、6h3hA2/O12h3h、3h、6hMBBR12h4.2h30min15℃CODCr、BOD5、SS、NH3-NTN88%、93.3%、95%、84%71.4%《》GB18918-2002B。1.39201512A2O+MBBRJ.200319256-57.2.MBBRJ.201142356-57.3.MBBRA/OJ.20071719-23.4.ABR/MBBRJ.2007231991-93.5.MBBRJ.2009251472-74.6.—MBBRFentonJ.2008281245-48.7.MBBRJ.200730366-68.8.A/O-MBBRJ.2010313274-277.9.A/O+MBBRJ.20103612122-126.10.A2O+MBBRJ.201329122-25.CombinedProcessofA2OandMBBRforTreatmentofIndustrialParkWastewaterHEDanTIANMing-mingWULi-fangZHANGZhi-jieJiangxiAcademyofEnvironmentalSciencesJiangxiNanchang330039AbstractThispapermainlyintroducestechnicsprocesstechnicsparameterandtreatmenteffectetcofcombinedprocessofA2OandMBBRusedoneindustrialparksewagetreatmentplantfortreatmentofcomprehensiveindustrialwastewater.TheresultsshowedthattheremovalefficiencyofCODCrreached88%theremovalefficiencyofBOD5reached93.3%there-movalefficiencyofSSreached95%theremovalefficiencyofNH3-Nreached84%andtheremovalefficiencyofTNreached71.4%whenHRTofretentionpoolaccidentpoolandacidhydrolyticpoolwas6hHRTofprecipitationpoolwas6hHRTofA2Opoolwas12hanaerobic3hanoxic3haerobic6hHRTofMBBRpoolwas12hHRTofsecondarysedi-mentationpoolwas4.2hHRTofsludgepoolwas30minthetemperatureofthewaterwas15℃dischargedwastewatercouldmeetthefirstgradeBrequirementsof<Pollutantdischargestandardofurbansewagetreatmentplant>GB18918-2002.KeyWordsA2OMBBRIndustrialParkWastewater4920156

1 / 3
下载文档,编辑使用

©2015-2020 m.777doc.com 三七文档.

备案号:鲁ICP备2024069028号-1 客服联系 QQ:2149211541

×
保存成功