Method for treating sucralose primary mother liquor

A technology for sucralose and processing methods, applied in chemical instruments and methods, sugar derivatives, sugar derivatives, etc., can solve problems affecting product quality, abnormal taste of sugar water, poor extraction and removal of impurities, etc., and improve the extraction effect , Improve product quality, improve the effect of product yield

Inactive Publication Date: 2021-03-12
ANHUI JINGHE IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In the process of sucralose production, the treatment of the mother liquor from the centrifugation of the baking bag has always been the first-class problem affecting the product quality. The mother liquor contains a large amount of acetate, water-soluble impurities, and ester-soluble impurities. In the prior art, the primary mother liquor is mostly mixed with batches of sugar water. Treated together, the acetic acid content of the treated sugar water is high, up to 1000PPM, and the effect of extraction and removal of impurities is not good, and the sugar water has a slight odor, which affects market sales

Method used

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  • Method for treating sucralose primary mother liquor
  • Method for treating sucralose primary mother liquor

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] (1) Pump the primary mother liquor (sugar water concentration 28%, acetic acid content 480PPM) from the drying section into the upper part of the extraction tower at 2000L / h, pump butyl acetate from the bottom of the extraction tower at 1000L / h, and the primary mother liquor Carry out counter-current extraction with butyl acetate in the extraction tower, and the butyl acetate phase coming out from the top of the tower after extraction enters the water washing tower at 1000L / h;

[0022] (2) Add pure water to the water washing tower at 600L / h for washing. The washed butyl acetate enters the concentration tank for concentration, and the temperature in the concentration tank is controlled at 45°C. The concentrated butyl acetate phase enters the butyl acetate tank and The phase (waste residue) goes to the sewage station, and the heavy phase after washing goes to the waste water degreasing kettle, and after removing butyl acetate in the water, it is sent to the thickening and ...

Embodiment 2

[0026] (1) Pump the primary mother liquor (sugar water concentration 29%, acetic acid content 500PPM) from the drying section into the upper part of the extraction tower at 2000L / h, pump butyl acetate from the bottom of the extraction tower at 1000L / h, and the primary mother liquor Carry out counter-current extraction with butyl acetate in the extraction tower, and the butyl acetate phase coming out from the top of the tower after extraction enters the water washing tower at 800L / h;

[0027] (2) Add pure water to the water washing tower at 500L / h for washing. The washed butyl acetate enters the concentration tank for concentration, and the temperature in the concentration tank is controlled at 48°C. The concentrated butyl acetate phase enters the butyl acetate tank and The phase (waste residue) goes to the sewage station, and the heavy phase after washing goes to the waste water degreasing kettle, and after removing butyl acetate in the water, it is sent to the thickening and d...

Embodiment 3

[0031] (1) Pump the primary mother liquor (concentration of sugar water 30% and acetic acid content of 520PPM) from the drying section into the upper part of the extraction tower at 2000L / h, pump butyl acetate from the bottom of the extraction tower at 1100L / h, and the primary mother liquor Carry out counter-current extraction with butyl acetate in the extraction tower, and the butyl acetate phase coming out from the top of the tower after extraction enters the water washing tower at 900L / h;

[0032] (2) Add pure water to the water washing tower at 550L / h for washing, and the washed butyl acetate enters the concentration tank to concentrate, control the temperature in the concentration tank to 42°C, the concentrated butyl acetate phase enters the butyl acetate tank, and The phase (waste residue) goes to the sewage station, and the heavy phase after washing goes to the waste water degreasing kettle, and after removing butyl acetate in the water, it is sent to the thickening and ...

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Abstract

The invention relates to a method for treating sucralose primary mother liquor, which is characterized by comprising the following steps: (1) pumping primary mother liquor and butyl acetate into an extraction tower according to a volume ratio of 2-3:1 for countercurrent extraction, and enabling a heavy phase to enter a degreasing kettle; (2) feeding the light phase to enter a water washing tower,adding pure water, feeding butyl acetate after water washing to enter a concentration kettle for concentration, controlling the temperature to be 40-50 DEG C, feeding the light phase to enter a butylacetate tank and the heavy phase to enter a sewage station, and feeding the washed heavy phase to enter a wastewater degreasing kettle; (3) controlling the temperature in the degreasing kettle to be 40-50 DEG C, enabling the light phase to enter a butyl acetate tank, pumping the heavy phase into a decolorizing kettle, and adding activated carbon which accounts for 0.2-0.5% of the mass of the sugarliquid into the decolorizing kettle for decolorization at 45-55 DEG C for 40-80 minutes; and (4) subsequently filtering and primarily concentrating the sugar liquid by controlling the pressure to be0.085-0.095 MPa and the temperature to be 45-55 DEG C, crystallizing the concentrated material until the sugar degree of the mother liquor is 30%, discharging and centrifuging the mother liquid, putting the centrifuged mother liquor into a sugar dissolving kettle, and pumping into a sugar liquid tank in batches. The method has the advantages that the sugar degree is reduced to 25% and the acetic acid content is reduced to 100 PPM from that the sugar degree of the primary mother liquor is 30% and the acetic acid content is 500 PPM.

Description

technical field [0001] The invention belongs to the technical field of sucralose production, and relates to a method and device for treating primary sucralose mother liquor. Background technique [0002] As a new type of sweet food additive, sucralose has more advantages than sucrose, saccharin, AK sugar, aspartame, stevioside, etc. It has high safety and stable performance, and is a new type of high-quality , non-nutritional high-efficiency sweetener, is the best ideal sweet substitute for food for obesity, cardiovascular disease and diabetes patients; it also belongs to the field of fine chemical products, and is a branch product of food additives. It is not only widely used in health food and medicine, but also widely used in more than 300 kinds of processed products such as baked food, beverage, chewing coffee, dairy products, frozen snacks, ice cream, pudding, jelly, jam, syrup, etc. , has been widely accepted by the market and has become one of the most popular high-i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07H1/06C07H5/02
CPCC07H1/06C07H5/02
Inventor 夏家信肖世东王东耿庆保
Owner ANHUI JINGHE IND
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