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36121.2.42100817%~22%4%~10%2%11t3.5t15%~20%F60%1200℃[1]20%40%50%70%90%140%2211.10~1.221.01~1.06H2SO4/%17~201.4~2.5FeSO4/%5~80.2~0.8Ti(SO4)2/%1~20~0.5(Al2(SO4)3)/%1.5~2.50.1~0.22/t/d3020201850930195922.1CaCO3MgCO3+2H2SO45CaSO4A+MgSO4+2H2O+CO2BH2SO42%20~40m/hCaSO4CO2CO2pH4~5pH7.5pH7.50.005mg/L0.0005mg/L0.0005mg/L6CDDDDDDDCDDCDDDDDDDCDD2002-07-0237372003101ChemicalProductionandTechnology0.01mg/L0.01mg/L0.05mg/L0.1mg/L1mg/L5mg/L1.9mg/LKMnO42.2CaO+H2O=CaOH2CaOH2+H2SO4=CaSO4+2H2O1pH4CaOH2pH7CODpH6~9COD100×10-670mg/L[2]315%~20%1..2..,1999.195291~293[]1966,()5000400kt50kt30%()(4~5min)150kt6kt4kt3kt()EEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEEE!
本文标题:硫酸法生产钛白的废酸治理
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