Separating, purifying and recycling method of amine substances in sucralose wastewater
A technology for sucralose and amine substances, which is applied in the preparation/separation of ammonia, chemical instruments and methods, purification/separation of amino compounds, etc., can solve the problems of high COD value and poor biodegradability of sucralose wastewater, and achieves Effects of reduced toxicity, improved biodegradability, and lower costs
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Embodiment 1
[0018] 2000g of sucralose production wastewater with a COD of 90000mg / L, wherein the concentration of ammonium chloride is 3.65%, the concentration of dimethylamine hydrochloride is 6.64%, the concentration of tert-butylamine hydrochloride is 3.51%, and the concentration of N,N-dimethylformamide 0.88%, the concentration of sucralose is 0.49%, the concentration of sucralose-6-ethyl ester is 0.03%, and it also contains a small amount of sucralose, tetrachlorosucrose, sucralose-6-ethyl ester, sucralose-6-ethyl Chlorinated by-products such as esters are first evaporated by thin film evaporation method to obtain 1100g evaporation condensate and 900g concentrate, the COD of the condensate is 5000mg / L, the pollutant is N,N-dimethylformamide, the concentration is 1.58%, It can be directly used as process water in the sucralose synthesis section; the main pollutants of the evaporative condensate are ammonium chloride, dimethylamine hydrochloride, tert-butylamine hydrochloride, three amm...
Embodiment 2
[0020] 1350g of sucralose wastewater was evaporated and concentrated, COD was 198000mg / L, ammonium chloride concentration was 13.0%, dimethylamine hydrochloride concentration was 17.4%, tert-butylamine hydrochloride concentration was 9.2%, and 850g sodium hydroxide saturated solution was added dropwise. Slowly raise the temperature to 95° C. to volatilize the amines in the concentrated solution evenly, and absorb it with 1000 g of pure water to obtain a mixed aqueous solution of amines. Add the aqueous solution to a simulated moving bed chromatography separation system to obtain ammonia solutions, dimethylamine solutions and tert-butylamine solutions with concentrations of 1.8%, 5.1%, and 2.9%, respectively, which can be used as amine solutions in the sucralose synthesis section after proper concentration. First cool down to 5°C to precipitate sodium chloride crystals, filter to obtain 166g sodium chloride crystals, dilute the filtrate with 3 times of tap water, inoculate aerob...
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