A treatment method for phosphorus-containing waste produced in the production process of glufosinate-ammonium
A production process and treatment method technology, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problems of high chloride ion content and low effective solid product content, and achieve Improve the removal rate and avoid the effect of escape
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Embodiment 1
[0077] Take by weighing the phosphorus-containing waste material 150g that produces in the pasty glufosinate-ammonium production process, wherein the content of COD is 85.5wt%, and total phosphorus content is 13.4wt%, and chloride content is 9.3wt%, and ammonia nitrogen content is 5.6wt%, The ammonium salt of glufosinate-ammonium is 1.15wt%, and the pH value is 1.5. In the phosphorus-containing waste material, adding concentration is 225g of 30wt% sodium hydroxide aqueous solution, after stirring and dissolving, measure the pH value of the phosphorus-containing waste material to be 13.5, and the above-mentioned phosphorus-containing waste material adjusted to the pH value is heated to 104° C. for reflux alkaline hydrolysis for 3 Hour. After the alkali hydrolysis is finished, the mixed solution is concentrated, concentrated at normal pressure to a terminal temperature of 115°C, crystallized and filtered, and sodium chloride is recovered. The filtrate enters the high-temperatur...
Embodiment 2
[0079] Take by weighing the phosphorus-containing waste material 150g that produces in the liquid glufosinate-ammonium production process, wherein the content of COD is 65.5wt%, and total phosphorus content is 7.71wt%, and chloride root content is 5.68wt%, and ammonia nitrogen content is 0.2wt%, The content of glufosinate-ammonium hydrochloride is 0.85wt%, and the pH value is 0. Adding concentration is 116g of sodium hydroxide aqueous solution of 30wt% in waste material, after stirring and dissolving, measure the pH value of phosphorus-containing waste material to be 13, the above-mentioned phosphorus-containing waste material adjusted pH value is heated to 102 ℃ of reflux alkaline hydrolysis for 2 hours. After the alkali hydrolysis is finished, the mixed solution is concentrated, concentrated at normal pressure to the end point temperature of 116°C, crystallized and filtered, and sodium chloride is recovered. The filtrate enters the high-temperature oxidation furnace for spra...
Embodiment 3
[0081] Take by weighing the phosphorus-containing waste material 150g that produces in the liquid glufosinate-ammonium production process, wherein the content of COD is 65.5wt%, and total phosphorus content is 7.71wt%, and chloride root content is 5.68wt%, and ammonia nitrogen content is 0.2wt%, The content of glufosinate-ammonium hydrochloride is 0.85wt%, and the pH value is 0. Adding concentration is 158g of aqueous sodium hydroxide solution of 30wt% in waste material, after stirring and dissolving, measure the pH value of phosphorus-containing waste material to be 14, the above-mentioned phosphorus-containing waste material adjusted pH value is heated to 102 ℃ of reflux alkaline hydrolysis for 2 hours. After the alkali hydrolysis is finished, the mixed solution is concentrated, concentrated at normal pressure to the end point temperature of 116°C, crystallized and filtered, and sodium chloride is recovered. The filtrate enters the high-temperature oxidation furnace for spra...
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