Treatment method for high salt content and high COD alkaline residue neutralization water
A technology of alkali slag and content, applied in chemical instruments and methods, natural water treatment, extracted water/sewage treatment, etc., can solve the problems of high effluent COD and ineffective treatment of effluent, and achieve improved standard discharge, easy biochemical treatment, The effect of reducing solubility
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Embodiment 1
[0019] A stream of alkali washing gasoline alkali slag wastewater, after neutralization and recovery of phenols, the COD of alkali slag neutralized water is 5.22×10 4 mg / L, the total salt content is 9.13×10 4 mg / L, pH<2. Using the method of the present invention, firstly, the temperature of the alkali slag neutralizing water is lowered from room temperature 20°C to -1°C. Since the concentration of the alkali slag wastewater is relatively high, the crude kerosene agent can be used for multi-stage extraction. Organic amine extractants can be used. Adopt C8 trialkyl tertiary amine single-stage extraction (i.e. 1st-stage extraction) and gas oil 7-stage cross-flow extraction respectively, the ratio of water to water is 4, and the waste extractant after using trialkyl tertiary amine extraction needs to use 20% NaOH solution regeneration.
[0020] After treatment, the total salt content of the alkali slag neutralized water was reduced to 4.23×10 4 mg / L, the total salt removal rat...
Embodiment 2
[0022] A stream of alkali washing diesel oil alkali slag wastewater, after neutralization and recovery of naphthenic acid, the COD of alkali slag neutralized water is 9.42×10 3 mg / L, the total salt content is 1.63×10 5 mg / L, pH3~4. When using the method of the present invention, since the concentration of the alkali slag wastewater is low, an organic amine extractant is selected, and the pH of the alkali slag neutralization water needs to be adjusted to below 2. The temperature of the wastewater is lowered from room temperature 20°C to 1°C, using C9 trialkyl tertiary amine for single-stage extraction, the ratio of water to water is 4, and the waste extractant after use is regenerated with 20% NaOH solution.
[0023] After the above treatment, the total salt content of the alkali slag neutralized water was reduced to 4.61×10 4 mg / L, the removal rate of total salt was 71.7%, and after single-stage extraction with trialkyl tertiary amine, the COD was reduced to 2.21×10 3 mg / L,...
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