Treatment method for high concentration organic waste liquid in sucralose production
A technology of organic waste liquid and sucralose, which is applied in biological water/sewage treatment, sedimentation treatment, water/sewage treatment, etc., can solve the problems of many reagents required for treatment, high energy consumption in the treatment process, and low combustion value of organic matter. , to meet the needs of environmental protection, simple equipment and reagents, and achieve the effect of degradation
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Embodiment 1
[0030] In this embodiment, a method for treating high-concentration organic waste liquid in the production of sucralose, the steps are as follows:
[0031] (1) Place 50t of high-concentration organic waste liquid collected in a spherical concentrator for primary concentration. The concentration temperature is 85°C and the vacuum degree is -0.09MPa. After completion, 24t fraction A and 26t fraction A are obtained; fraction A is directly used for production;
[0032] (2) Place the above-mentioned distillation bottom A in a concentrator for secondary concentration. The concentration temperature is 120°C and the vacuum degree is -0.09MPa. The concentration ratio accounts for 35% of the total volume of the distillation bottom A. 5t, to obtain 9.6t fraction B and 8t distillation bottom B;
[0033] (3) Add 1.5t of sodium hydroxide three times to the above-mentioned distillation bottom B, reflux at 100°C for 3 hours, and perform three-stage concentration after completion. The concent...
Embodiment 2
[0045]In this embodiment, a method for treating high-concentration organic waste liquid in the production of sucralose, the steps are as follows:
[0046] (1) Place the collected 50t of high-concentration organic waste liquid in a horizontal concentrator for primary concentration. The concentration temperature is 90°C and the vacuum degree is -0.092MPa. The concentration ratio accounts for 45% of the total volume of the organic waste liquid. After the concentration is completed, 22.5t fraction A and 27.5t fraction A are obtained; fraction A is directly used for production;
[0047] (2) Place the above-mentioned distillation bottom A in a concentrator for secondary concentration. The concentration temperature is 130°C and the vacuum degree is -0.092MPa. The concentration ratio accounts for 40% of the total volume of the distillation bottom A. 5.1t, to obtain 11t fraction B and 8.2t distillation bottoms B;
[0048] (3) Add 1.7t of potassium hydroxide three times to the above di...
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