Oxidation treatment device and method for AK sugar crystallization waste liquid
A technology for oxidation treatment and waste liquid, applied in the direction of oxidized water/sewage treatment, chemical instruments and methods, feeding devices, etc., can solve the problems of low purity of potassium salt crude products, unresolved organic impurities, multiple secondary pollution, etc. , to achieve the effect of increasing yield, reducing production cost and reducing pollution
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Embodiment 1
[0029] The primary crystallization waste liquid (potassium carbonate 10%, potassium sulfamate 2%, potassium sulfate 2.5%, potassium hydroxide 5%, acesulfame potassium 2.5%) 100mL and hydrogen peroxide (concentration of 50% %) 30mL were pumped into the fast mixer (40°C) for mixing (a lot of air bubbles and heat generated after mixing), and then entered the top of the tower reactor, as the reaction progressed, a lot of gas and heat generated, the tower The temperature in the reactor naturally rises to 90°C, and after 20 minutes of reaction, it drops to room temperature. The solution changes from dark brown before the reaction to a bright yellow transparent solution (potassium salt solution) 130mL (almost no organic components detected by gas chromatography), and enters the solution Storage tank spare.
[0030] Take 130mL of the bright yellow transparent solution obtained in Example 1, and add dropwise to 500mL of the dichloromethane solution after sulfonation and cyclization hyd...
Embodiment 2
[0032] The primary crystallization waste liquid (potassium carbonate 15%, potassium sulfamate 5%, potassium sulfate 3%, potassium hydroxide 8%, acesulfame potassium 1%) 500mL produced in the AK sugar production process was mixed with hydrogen peroxide (concentration is 50 %) 50mL were pumped into the fast mixer (80°C) for mixing (a lot of air bubbles and heat generated after mixing), and then entered the top of the tower reactor, as the reaction progressed, a lot of gas and heat generated, the tower The temperature in the reactor naturally rises to 100°C, reacts for 60 minutes and then drops to room temperature. The solution changes from dark brown before the reaction to a bright yellow transparent solution (potassium salt solution) 550mL (almost no organic components detected by gas chromatography), and enters the solution Storage tank spare.
Embodiment 3
[0034]The primary crystallization waste liquid (potassium carbonate 20%, potassium sulfamate 1%, potassium sulfate 1%, potassium hydroxide 2%, acesulfame potassium 5%) 1000mL produced in the AK sugar production process was mixed with hydrogen peroxide (concentration is 50 %) 200mL were pumped into the fast mixer (10°C) for mixing (a lot of air bubbles and heat generated after mixing), and then entered the top of the tower reactor, as the reaction progressed, a lot of gas and heat generated, the tower The temperature in the reactor naturally rises to 90°C, and after 20 minutes of reaction, it drops to room temperature. The solution changes from dark brown before the reaction to a bright yellow transparent solution (potassium salt solution) 1200mL (almost no organic components detected by gas chromatography), and enters the solution Storage tank spare.
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