改良UCT分段进水脱氮除磷工艺性能及物料平衡.docx

改良UCT分段进水脱氮除磷工艺性能及物料平衡改良UCT分段进水脱氮除磷工艺性能及物料平衡摘要：采用改良UCT分段进水试验装置研究了该工艺处理实际生活废水的脱氮除磷性能,建立了该系统碳(COD)、氮、磷的物料衡算公式,并以稳态条件下试验数据为基础分析评价了各指标的物料分布情况.结果表明,工艺出水水质稳定,抗冲击负荷能力较强,平均出水COD、总氮、总磷含量分别为43.5、8.51、0.29mg·L~(-1),满足国家城镇生活污水一级A排放标准.此外,根据建立的物料衡算公式及工艺各反应区污染物指标的转化途径分析发现,高达67.1%的'反硝化脱氮作用(包括缺氧反硝化和好氧同步硝化反硝化)是该工艺深度脱氮的根本原因;系统反硝化和释磷过程利用的COD占总去除量的62.1%,体现了该工艺充分利用原水碳源的优势;氮素和COD的平衡率均高达99.8%,证明了所建立的公式的有效性.系统对磷的去除主要依赖于排放的剩余污泥,占总量的71.7%.Abstract：TheremovalofwastewaternutrientsinthemodifiedUCTstepfeedprocesswasinvestigatedwhentreatingmunicipalwastewater.Basedonexperimentaldataundersteady-stateconditions,theequationsforcalculatingmaterialbalancesofCOD,nitrogenandphosphatewereestablished.Thesethreematerialdistributionsinthesystemwerealsoevaluated.Theresultsindicatedthatwithstableeffluentqualityandgoodcapacityofresistancetoshockload,theeffluentconcentrationsofCOD,TNandTPwere43.5,8.51,0.29mg·L~(-1)onaverage,respectively,whichthefirstlevelAdischargestandardofpollutantsformunicipalwastewatertreatmentplantwasmet.Furthermore,accordingtocalculationequationsandtransformationpathwaysofnutrients,itwasfoundthatapproximately67.1%ofnitrogenwassuccessfullyremovedduringthedenitrificationprocess,includinganoxicdenitrificationprocessandsimultaneousnitrificationanddenitrification(SND)process,whichgreatlycontributedtohighnitrogenremovalefficiency.CODconsumedinthedenitrificationandphosphatereleaseprocessaccountedfor62.1%,whichembodiedtheadvantageofsufficientutilizationofinfluentcarbonsources.BothnitrogenandCODbalanceratioswereashighas99.8%,whichconfirmedthevalidityofequationsestablished.Phosphateremovalwasmainlyachievedbythedischargeofexcesssludge,accountingfor71.7%ofthetotal.作者：葛士建[1]彭永臻[1]张亮[2]王希明[1]王淑莹[1]Author：GEShijian[1]  PENGYongzhen[1]  ZHANGLiang[2]  WANGXiming[1]  WANGShuying[1]作者单位：北京工业大学北京市水质科学与水环境恢复重点实验室,北京,100124哈尔滨工业大学城市水资源与水环境国家重点实验室,黑龙江,哈尔滨,150090期刊：化工学报 ISTICEIPKUJournal：CIESCJOURNAL年，卷(期)：2010, 61(4)分类号：X703.1关键词：分段进水  脱氮除磷