Energy-saving evaporation treatment process of high-salinity wastewater
A high-salt wastewater treatment technology, applied in the direction of heating water/sewage treatment, adsorption water/sewage treatment, water/sewage multi-stage treatment, etc., can solve the problems of high impurity content, difficult to meet the waste water standard, difficult to effectively use, etc. Achieve the effect of reducing impurity content, short treatment process and remarkable energy saving effect
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Embodiment 1
[0045] Example 1 Taking the wastewater containing ammonium chloride produced during the production of potassium dihydrogen phosphate as an example, the specific treatment process is as follows:
[0046] ① Evaporation system: 500kg of ammonium chloride wastewater with 10% ammonium chloride concentration treated by the sewage treatment system is passed into the raw material tank, and then sent to the primary preheater and secondary preheater for grading preheating , After preheating, it is transported to the evaporator and heated and evaporated at 30°C to obtain the ammonium chloride evaporation liquid with a concentration of 25%;
[0047] ②Concentration system: the ammonium chloride evaporation liquid enters the first storage tank and is stored after removing impurities from the adsorption layer. The adsorption layer is supported by the upper and lower grid plates. The weight of activated coal gangue in the adsorption layer is 5kg. After storage, the ammonium chloride is evaporated ...
Embodiment 2
[0053] Example 2 Taking the sodium chloride-containing wastewater produced during the production of epoxy resin as an example, the specific treatment process is as follows:
[0054] ① Evaporation system: 1t of sodium chloride wastewater with a sodium chloride concentration of 18% that has been treated by the sewage treatment system is passed into the raw material tank, and then sent to the primary preheater and secondary preheater for grading preheating , After preheating, it is transported to the evaporator and heated and evaporated at 100°C to obtain a 35% sodium chloride evaporation liquid;
[0055] ②Concentration system: the sodium chloride evaporation liquid enters the first storage tank and is stored after removing impurities from the adsorption layer. The adsorption layer is supported by the upper and lower grid plates. The weight of activated coal gangue in the adsorption layer is 20kg, and the sodium chloride after storage is evaporated The liquid is transported to the hig...
Embodiment 3
[0061] Example 3 Taking the waste water containing calcium chloride produced during the production of sodium dichloroisocyanurate as an example, the specific treatment process is as follows:
[0062] ① Evaporation system: 2t of calcium chloride wastewater with a calcium chloride concentration of 14% that has been treated by the sewage treatment system is passed into the raw material tank, and then sent to the primary preheater and secondary preheater for grading preheating , After preheating, it is transported to the evaporator and heated and evaporated at 65°C to obtain a calcium chloride evaporation liquid with a concentration of 30%;
[0063] ②Concentration system: Calcium chloride evaporation liquid enters the first storage tank and is stored after removal of impurities by the adsorption layer. The adsorption layer is supported by the upper and lower grid plates. The weight of activated coal gangue in the adsorption layer is 30kg, and the stored calcium chloride evaporates The ...
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