Zero discharge method of salt-containing wastewater
A salty wastewater, zero-discharge technology, applied in chemical instruments and methods, water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of low recycling rate, long process route and high energy consumption
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Embodiment 1
[0027] Raw material water source: Salt production wastewater from a certain enterprise, the amount of wastewater produced is 5m 3 / d. pH value 5.5, CODcr240mg / L, SS 80mg / L, Ca 2+ 1200 mg / L, Mg 2+ 1350mg / L, TDS230000mg / L.
[0028] Pretreatment: After the raw material water is treated through physical, chemical and oxidation processes, the SS is reduced to below 20 mg / L, and the CODcr is reduced to below 50 mg / L.
[0029] Preheating adjustment: the feed water in step (1) is stirred and mixed by air; it is preheated to 58-62°C by heat exchange with the waste flue gas at 80°C in the plant through a tubular heat exchanger.
[0030] Vaporization separation: the feed water in step (2) is heated by heat exchange with the waste flue gas at 80°C in the plant through a tubular heat exchanger, and the temperature is controlled at 65°C; then pervaporation is carried out through the SY-PVLCS-II membrane module Separation of vaporized water to achieve concentration reduction of feed wate...
Embodiment 2
[0036] Source of raw water: high-concentration saline wastewater produced by an enterprise, the amount of wastewater produced is 30m 3 / week. pH value 7.8, CODcr2100mg / L, turbidity 2NUT, TDS210000mg / L.
[0037] Raw material water pretreatment: After physical, chemical and oxidation treatment, CODcr is reduced to below 200 mg / L.
[0038] Preheating adjustment: the feed water in step (1) is preheated to 60-65°C by heat exchange with the 85°C waste hot water generated by the heat exchange and condensation of steam in the plant through a tubular heat exchanger; it is stirred and mixed by a mixer.
[0039] Vaporization separation: the raw material water in step (2) is heated by a metal heater, the temperature is controlled at 68°C, and then the vaporized water is separated by pervaporation through the SY-PVLCS-I type membrane module, so as to realize the concentration and weight loss of the feed water.
[0040] Condensation recovery: the vaporized water separated in step (3) is h...
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