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氯苯废水中苯和氯苯的回收119471619955122500700740501997ISO90011243135RT40204010NARD420kt/a200441.289FeIII20004000mg/L5001000mg/L100800mg/LFeIII4/GB8978-1996212GB8978-199631234544.112000m3/a1.37m3/h1.5m3/h4.211/mg·L-110008004.3GB8978-199622GB8978-1996/mg·L-10.10.20.50.20.41.04.44.4.180.11.865g·L-12569.25101.3kPa91.16%8.84%1320.049g/100gH2O3090.271.628.4%4.4.2952.44m10.7m220t4.4.311123415627pH69804.4.4ASPENPLUS22133255.1ASPENPLUS0.018kmol/s380K130kPaVsVs0.0188.314380/1300.4374m3/sDu14.3Vs4Vsm3/sum/su0.6m/sD0.964mD1m5.2+HNPHETPNPNT/AspanNT1170NP11/0.716HETP0.5mH160.58m866.195330t84.2733024%95h/m550.13m/Kg2731.033=××××t9.1433024%95h/m550.13m/Kg1462.033=××××t14.033024%95h/m550.13m/Kg00137.033=××××2400/t2750/t4500/t10.85/6.2712AspenPlus38AspenPlus[1][]J.M...1994[2]..1990[3]..1989[4]ASPLENPLUSMANUL.[5]..1990[6]RichardTurton,RichardC.Bailie,WallaceB.Whiting,JosephA.Shaeiwitz.Analysis,Synthesis,andDesignofChemicalProcesses.AmericaPrenticeHall[7]..20007[8]..2001[9]..19981ASPANPLUS2ASPANPLUSSubstreamMIXEDMoleFlowkmol/sec123CALCI-01.00000191181681.000001911816812.94632197E-33BENZE-01.0000132468036.0000132468036.0000132468036CHLOR-01.0000049213668.0000049213668.0000049213668M-DIC-013.53110125E-083.53110125E-085.3389562E-11WATER.208827332.208827332.00299561463MassFlowkg/secCALCI-01.000212179929.0002121799293.2699283E-31BENZE-01.00103475605.00103475605.00103475605CHLOR-01.000553941173.000553941173.000553941173M-DIC-01.00000519083041.000005190830417.84843433E-09WATER3.762082853.76208285.0539668363TotalFlowkmol/sec.208847447.208847447.00301378285TotalFlowkg/sec3.763888923.76388892.0555555414TotalFlowcum/sec.00378892731.00396665728.0782389949TemperatureK298.15343.15377.806009PressureN/sqm120000120000120000VaporFrac001LiquidFrac110SolidFrac000EnthalpyJ/kmol-285657104-282415791-237254123EnthalpyJ/kg-15850296.9-15670445.7-12870586.6EnthalpyWatt-59658756.8-58981817-715032.409EntropyJ/kmol-K-162681.609-152606.928-38126.0206EntropyJ/kg-K-9026.73789-8467.72259-2068.26438Densitykmol/cum55.120468152.6507415.0385202143Densitykg/cum993.391694948.881806.710074835AverageMW18.022192618.022192618.4338236SubstreamMIXEDMoleFlowkmol/sec456CALCI-012.94632197E-33.000001911816810BENZE-01.00001324680363.32163039E-270CHLOR-01.00000492136681.52929811E-230M-DIC-015.3389562E-113.52576229E-080WATER.00299561463.205831717.0462570296MassFlowkg/secCALCI-013.2699283E-31.0002121799290BENZE-01.001034756052.59464641E-250CHLOR-01.0005539411731.72135348E-210M-DIC-017.84843433E-09.000005182981980WATER.05396683633.70811601.83333334TotalFlowkmol/sec.00301378285.205833664.0462570296TotalFlowkg/sec.05555554143.70833338.83333334TotalFlowcum/sec.000363556212.004084862131.30516958TemperatureK323.15382.494248376.15PressureN/sqm120000140000110000VaporFrac.0047427094101LiquidFrac.99525729110SolidFrac000EnthalpyJ/kmol-281758014-279397387-239241087EnthalpyJ/kg-15284838.4-15508149.3-13279898.3EnthalpyWatt-849157.47-57509387.8-11066582EntropyJ/kmol-K-156991.67-144238.135-37289.9567EntropyJ/kg-K-8516.50065-8006.03957-2069.90714Densitykmol/cum8.2897300450.3893785.0354413941Densitykg/cum152.811421907.823387.638486638AverageMW18.433823618.016165618.01528SubstreamMIXEDMoleFlowkmol/sec6789CALCI-010000BENZE-010000CHLOR-010000M-DIC-010000WATER.0462570296.0462570296.0462570296.0462570296MassFlowkg/secCALCI-010000BENZE-010000CHLOR-010000M-DIC-010000WATER.83333334.83333334.83333334.83333334TotalFlowkmol/sec.0462570296.0462570296.0462570296.0462570296TotalFlowkg/sec.83333334.83333334.83333334.83333334TotalFlowcum/sec1.30516958.835304525.000838773235.000873855492TemperatureK376.15375.487938298.15338.581283PressureN/sqm110000110000101300101300VaporFrac1.64089753500LiquidFrac0.35910246511SolidFrac0000EnthalpyJ/kmol-239241087-253875399-285682722-282783162EnthalpyJ/kg-13279898.3-14092226.1-15857800.8-15696850.8EnthalpyWatt-11066582-11743521.9-13214834.1-13080709.1EntropyJ/kmol-K-37289.9567-76264.0243-162687.738-153614.464EntropyJ/kg-K-2069.90714-4233.29664-9030.54175-8526.89848Densitykmol/cum.0354413941.05537744455.148433152.9344154Densitykg/cum.638486638.99764016993.514463953.628315AverageMW18.0152818.0152818.0152818.01528B11627SubstreamMIXEDMoleFlowkmol/secCALCI-01.00000191181681kmol/sec0kmol/sec.00000191181681kmol/sec0kmol/secBENZE-01.0000132468036kmol/sec0kmol/sec.0000132468036kmol/sec0kmol/secCHLOR-01.0000049213668kmol/sec0kmol/sec.0000049213668kmol/sec0kmol/secM-DIC-013.53110125E-08kmol/sec0kmol/sec3.53110125E-08kmol/sec0kmol/secWATER.208827332kmol/sec.0462570296kmol/sec.208827332kmol/sec.0462570296kmol/secMassFlowkg/secCALCI-01.000212179929kg/sec0kg/sec.000212179929kg/sec0kg/secBENZE-01.00103475605kg/sec0kg/sec.00103475605kg/sec0kg/secCHLOR-01.000553941173kg/sec0kg/sec.000553941173kg/sec0kg/secM-DIC-01.00000519083041kg/sec0kg/sec.00000519083041kg/sec0kg/secWATER3.76208285kg/sec.83333334kg/sec3.76208285kg/sec.83333334kg/secTotalFlowkmol/sec.208847447kmol/sec.0462570296kmol/sec.208847447kmol/sec.0462570296kmol/secTotalFlowkg/sec3.76388892kg/sec.83333334kg/sec3.76388892kg/sec.83333334kg/secTotalFlowcu
本文标题:氯苯废水中苯和氯苯的回收
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