高海拔城市污水处理厂表曝机供气量计算

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〔〕、、,。,,。〔〕;;;;:X703.1:B:1004-4345(2015)04-0062-03CalculationonAirSupplyQuantityofSurfaceAeratorforSewageTreatmentPlantofHigh-altitudeCityLIUYi(ChinaNerinEngineeringCo.,Ltd.,Nanchang,Jiangxi330031,China)AbstractDuetolowairtemperatureandairpressure,lowconcentrationofsaturateddissolvedoxygeninwaterandlowoxygencontentinair,calculationonairsupplyquantityofsewagetreatmentplanthasacertainparticularityinhigh-altitudearea.Incombinationwithdesignpracticeofoxidationditchprocessinsewagetreatmentplantofahigh-altitudecity,thepapersummarizescalculationmethodofairsupplyquantityofsurfaceaeratorinhigh-altitudeareaandputsforwardcalculationpointsandsomeproblemsneedstobepaid.Keywordshigh-altitudearea;oxidationditch;surfaceaerator;oxygentransferrate;calculationonairsupplyquantity(,330031):2014-08-01:(1979—),,。,。,,(),,,,,。1。,,(DO),();,,。,,,。,、,4:;,;;、、。:1)。,,,;2)。,,,、;3)。。364201584。,,,,。、K,、、。2,,,,KLa[1]。(kgO2/h)1、20℃,DO,(StandardOxygenRate),SOR。,;;DO,2mg/L。、KLa,。(ActualOxygenRate),AOR。,,,。N0SOR,NAOR,[1]:N=αN0βCSW-C0Cs×1.024(T-20)(1):αKLawKLa,KLaw/KLa,0.8~0.85;β,0.9~0.97;CSW(mg/L),T,Pa;C0DO,2mg/L;Cs,9.17mg/L;T,5~30℃;1.024。3、、,。3.1,,,KLa;。KLa[2]:KLa(T)=KLa(20)×1.024(T-20)(2):KLa(T)KLa(20)T℃20℃;T,℃。,,,Cs。,Cs。,[3]:Cs(760,T)=477.8T+32.26(3):Cs(760,T),T℃Cs,mg/L;T,℃。1()。1[4],KLa,,SOR;Cs,,SOR。,。,DO2mg/L,SOR,。3.2,Cs,,。CsP:CSW(P,T)=Cs(760,T)×θ=Cs(760,T)Pa1.013(4):CSW(P,T)Pa,T℃Cs,mg/L;Cs(760,T),T℃T/℃Cs/(mg/L)T/℃Cs/(mg/L)T/℃Cs/(mg/L)01234567891014.6214.2313.8413.4813.1312.8012.4812.1711.8711.5911.33111213141516171819202111.0810.8310.6010.3710.159.959.749.549.359.178.992223242526272829308.838.638.538.388.228.077.927.777.6363··36Cs,mg/L;θ;Pa,105Pa;T,℃。,,,:Pa=1.013×e(-g×M×hR×(273.15+T)×1000)(5):Pa,105Pa;g,m/s2;M,28.95;R,8.314J/(K·mol);T,℃。3.3,AOR(1)SOR,,,,。1、20℃,1.22kg/m3(20℃),21%,0.256kg/m3;,,,21%,。,:ρ=Pa×MR×(273.15+T)(6):ρ,kg/m3;Pa,105Pa;M,28.95;R,0.082L·atm/(K·mol);T,℃。(),,。,3000m0m69%,。(1)SORδ,,,,。4,。2200~2600m,2240m,10.5~22.8℃,24.8℃,25℃,20℃。,ATV(AOR)1180kgO2/h,SOR(、):1),(5)0.78×105Pa;2),(3)(4)CSW7.06mg/L;3)AOR1180kgO2/h,(1),α0.8,β0.9,SOR3107kgO2/h。4),(6)0.924kg/m3,1.22kg/m3,75.7%。5)3SOR3107kgO2/h,75.7%,4104kgO2/h,。,0m,,2200kgO2/h,,。5,、,。,,、、。,。[1].:[M].2.:,2004.[2],,.:[M].2.:,2000.[3].[J].,2012,38(2):41-45.[4].[J].,1999,12(2):54-55.64··

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