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200296ChemicalProductionandTechnology1221.,3240042.324004--OO-35OO-16051t9t/149t/tC2H5O2ClPS112PSClCOD[2]2.1(1)2.2H2SpH6~71[1]80P/mg/L2611.0261/mg/L130001.013000CODcr/mg/L336320016.8Cl-/mg/L19750--pH7.86~9-9:::::::9::9:::::::9::2001-04-242002-09-1936C2H5O2PSCl+4H2O#2C2H5OH+H3PO4+H2S0+Cl-2H3PO4+2CaOH2#2CaHPO42H2O433.112pH2.52.52.53.03.03.03.5/%99.499.399.399.399.299.499.2pH3.521min2pH9.73.21312345/mg/L1136560368190170/h6122436/g/L1.312.242.943.493.9236h2412345/mg/L1221772624485473/h6122436/g/L4.626.077.208.108.833AO6hCOD3338294109.724hCOD9997%28.30.6945536%/kg/kg/kWh/tPAM/kg/kg2.742.13.561.400.0020.002/0.500.10.550.4010.010.0/1.370.211.960.560.020.02-1.0/t3.14/t512200296ChemicalProductionandTechnologyAO33.14/t6/t41..2.-.1997(4)[]196319851037;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;;(morpholine,C4H9NO)14-Willgerodt(1)N--N-(OTOS)N--2-(NOBS)44'-(DTDM)44'-(2)NN'-N-A(3)NN'-N-(4)(5)(6)NN'-2-(N-)(7)N-Formex(8)CO2H2SHCN(DEG)(DCEE)(DCEE)(DGA)(DEA)(BCME)(EO)(1)(DEG)H2240℃1.7MPa(DGA)3(2)(DCEE)10.65MPa50℃24hNH3280~420℃0.15MPa(3)(DGA)CuNiCrH2NH3150~250℃6.5~22.5MPaPSrSiAl280~420℃0.15MPa(4)(DEA)1889150℃(5)(BCME)(3.5MPa)NiHCN(6)(EO)250~500℃NHCON-C-(7)CuNiCoMoRhRu20()
本文标题:乙基氯化物生产废水的处理研究
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