Method for treating meta ethylene chloride saponification waste water
A technology for vinylidene chloride and saponification wastewater, applied in the field of vinylidene chloride saponification wastewater treatment and recovery of vinylidene chloride and salt, can solve the problems of lack of simultaneous removal of chlorine, lack of, lack of removal of chloric acid radicals, etc., and achieve significant economic benefits , low processing cost, cheap and easy-to-obtain materials
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Embodiment 1
[0059] After the vinylidene chloride saponification wastewater is collected, it is introduced into the stripping unit, and steam is introduced to recover vinylidene chloride; the effluent from the stripping unit is introduced into the neutralization tank, and hydrochloric acid is added to adjust the pH value; the wastewater is introduced into the fluidized bed dechlorination reactor, and the As a reducing agent, two-stage or multi-stage dechlorination reactors can be used to increase the removal rate of chlorate and chlorinated alkanes; the waste water after dechlorination treatment is introduced into the coagulation reactor, and alkali is first added to neutralize to neutral to alkali After the coagulation reaction, the wastewater is introduced into the clarification tank, and the clarified wastewater is introduced into the subsequent process for electrolytic recovery of salt.
[0060] Saponification wastewater quality: vinylidene chloride 0.2%; sodium chlorate 552mg / l; sodium...
Embodiment 2
[0071] According to the step described in embodiment 1, concrete processing conditions are as follows:
[0072] Saponification wastewater quality: vinylidene chloride 4150mg / l; sodium chlorate 1200mg / l; sodium hypochlorite 1500mg / l; trichloroethane 100mg / l; dichloromethane 360mg / l; salt concentration 17%; iron ion concentration 330mg / l; Sulfate concentration 80mg / l.
[0073] Stripping operating conditions: 88°C.
[0074] Stripping and water neutralization conditions: pH5.0.
[0075] Reductant: cast iron powder, the dosage is 1.7kg per ton of waste water.
[0076] Reductive dechlorination operating conditions: temperature 55°C; pressure at atmospheric pressure, residence time 75min.
[0077] Neutralization and coagulation unit operating conditions: caustic neutralization, pH 10.2; 45°C.
[0078] Chemical precipitant: barium chloride, the dosage is 50g per ton of waste water.
[0079] Coagulant aid: polyacrylic acid, the dosage is 20g per ton of waste water.
[0080] Coagu...
Embodiment 3
[0083] According to the step described in embodiment 1, concrete processing conditions are as follows:
[0084] Saponification wastewater quality: vinylidene chloride 5000mg / l; sodium chlorate 650mg / l; sodium hypochlorite 1820mg / l; trichloroethane 121mg / l; dichloromethane 720mg / l; salt concentration 22%; iron ion concentration 500mg / l; Sulfate concentration 170mg / l.
[0085] Stripping operating conditions: 95°C.
[0086] Stripping and water neutralization conditions: pH3.2.
[0087] Reducing agent: metal iron powder, the dosage is 2.6kg per ton of waste water.
[0088] Reductive dechlorination operating conditions: the temperature is 72°C; the pressure is atmospheric pressure, and the residence time is 110min.
[0089] Neutralization and coagulation unit operating conditions: caustic neutralization, pH9.0; 67°C.
[0090] Chemical precipitant: barium chloride, the dosage is 360g per ton of waste water.
[0091] Coagulant aid: polyacrylic acid amide, the dosage is 8.0g per ...
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