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June2011311ModernChemicalIndustry20116266071、、CODCr、NH3-N、CAST、、BAF《》DB21/1627—2008。CASTBAFTU992.3A0253-43202011S1-0366-02ProjectdesignfortreatmentofsuperheavyoilrefinerywastewaterbybiologicalprocessCAIYu-yingEastChinaBranchofChinaPetroleumEngineeringConstructionCorporationQingdao266071ChinaAbstractHeavyoilandsuperheavyoilrefinerywastewaterfromLiaohePetrochemicalCompanyischaracterizedbyhighdegreeofemulsificationandhighconcentrationofoilCODCrammonianitrogenandsuspendedsolids.TheprojectdesignofbiochemicaltreatmentprocesswithprimaryhydrolysisacidificationCASTsecondaryhydrolysisacidificationandbiologicalaeratedfiltersBAFasitscoreisproposedbythispaper.TheeffluentaftertreatmentcouldreachtothefirstlevelofintegratedwastewaterdischargestandardinLiaoningprovinceDB21/1627—2008.KeywordsheavyoilrefinerywastewaterhydrolysisacidificationCASTBAFbiochemicaltreatmentprocess2011-04-291966-0532-80950429caiyuying@cnpccec.cn。、1。2。4、、3“”、、4-5。、、COD、、、《》DB21/1627—2008。11.1600m3/h。1.21。1pHCODCrSS6~9≤150050~100≤20≤80≤30≤806~95070350.50.2pHmg/L。22.12COD、BOD、NH3-N。“+CAST++BAF”。1CODCr。CAST。·663·DOI:10.16606/j.cnki.issn0253-4320.2011.s1.102201162CASTCAST。1、。“-”、、。CAST5、、、、。3CASTB/C。CASTNOx-NCAST。4BAFB/C。BAF。BAFBOD、S2-BAFNH3-N。2.22。2CODCrSS/mg·L-11500150100/mg·L-11200150100/%2000CAST/mg·L-11443060/%888040/mg·L-11153060/%2000/mg·L-157.69.036/%507040/mg·L-15010202.31“+CAST”“+BAF”、。2CAST、。3-。33.11V=2500m3415h、、。2CAST8L×B×H=48m×16.4m×6.0m。、、、、。314L×B×H=7.0m×9.0m×7.0m2P=3.75kW4h。4BAFL×B×H=7.0m×9.0m×7.0m12。1140m3161m3380m2136800.25~0.40m31380m2。、、BAF。3.2。pH7.5~8.515~25g/L。CAST。DO1~2mg/LSVI=100~140MLSS=3500~5000mg/LR=30%~50%10g/L38h5h1h1h1h。pH7.5~8.515~25g/L。369·763·20116BOPPMFRMFR、、。BOPPF280SOMFR2.5~3.5g/10min。F280BOPP。1BOPPF300SPHF030GS28CF280MFR/g·10min-1GB/T36823.03.22.22.8/MPaGB/T104031303533/MPaGB/T93411258131015171384/J·m-1GB/T1843323338332.22.2.1BOPPBOPP。MW、MWD。PPPPBOPP。“”。“”BOPPBOPP。BOPP“”。2.2.2BOPPMFRPP。2BOPPF280F2801。櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆櫆367BAF1.54m/hCOD1.23kgCOD/m3·dNH3-N0.25kgNH3-N/m3·d6∶12~3d。--。60m3/m2·h5min60m3/m2·h30m3/m2·h5~8min30m3/m2·h5min。420081251、33CAST/%CODCr/mg·L-11134659.3SS/mg·L-11001882.0/mg·L-12.81.642.9/mg·L-10.040.0175.0S2-/mg·L-10.6400.01398.0/mg·L-112375.0《》DB21/1627—2008。。CAST、。1.J.200611610-14.2.J.20072441-4.3.A//C2007.4.-J.200727166-68.5.J.200121514-16.■·963·
本文标题:超稠油炼制污水生化处理工程设计蔡玉颖
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