Method for purifying deoxyribose

A deoxyribose and supercritical fluid technology, applied in the directions of deoxy/unsaturated sugar, chemical instruments and methods, sugar derivatives, etc., can solve the problems of unsatisfactory product purity, poor control of cooling temperature, low yield, etc. , to achieve the effect of improving crystallization safety, easy control of operating parameters, and fast dissolution

Inactive Publication Date: 2018-08-24
NANTONG DISONG TEXTILE CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the equipment for large-scale production of deoxyribose at home and abroad is a general enamel reaction kettle. The mature process is roughly as follows: that is, take dehydroacetic acid and sodium hydroxide for neutralization reaction, and then cool and crystallize through the enamel kettle, dehydrate, dry, Finished products are obtained through packaging and other ...

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  • Method for purifying deoxyribose

Examples

Experimental program
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Effect test

Embodiment 1

[0020] (1) Use the raw material pump to spray the neutralized deoxyribose solution A containing impurities at 90° C. from the top of the extraction column E, and at the same time pass the supercritical fluid CO at the bottom of the extraction column E. 2 C, control the temperature of the supercritical fluid to be 33°C, the pressure to be 9Mpa, and the flow rate to be 15m 3 / min, so that deoxyribose dissolves in supercritical fluid CO 2 C;

[0021] (2) High pressure supercritical fluid CO containing dissolved deoxyribose 2 B is depressurized to lower than the supercritical fluid CO through the throttle valve D 2 Enter the separation kettle F below the critical pressure; supercritical fluid CO 2 The solubility drops sharply to separate out the solute, which is separated into two parts, the deoxyribose solution H and the supercritical fluid gas, the former is the process product, which is regularly discharged from the bottom of the separation kettle F, and the latter is the ci...

Embodiment 2

[0024] (1) Use the raw material pump to spray the neutralized deoxyribose solution A containing impurities at 90° C. from the top of the extraction column E, and at the same time pass the supercritical fluid CO at the bottom of the extraction column E. 2 C, control the temperature of the supercritical fluid to be 34°C, the pressure to be 10Mpa, and the flow rate to be 17m 3 / min, so that deoxyribose dissolves in supercritical fluid CO 2 C;

[0025] (2) High pressure supercritical fluid CO containing dissolved deoxyribose 2 B is depressurized to lower than the supercritical fluid CO through the throttle valve D 2 Enter the separation kettle F below the critical pressure; supercritical fluid CO 2 The solubility drops sharply to separate out the solute, which is separated into two parts, the deoxyribose solution H and the supercritical fluid gas, the former is the process product, which is regularly discharged from the bottom of the separation kettle F, and the latter is the c...

Embodiment 3

[0028] (1) Use the raw material pump to spray the neutralized deoxyribose solution A containing impurities at 90° C. from the top of the extraction column E, and at the same time pass the supercritical fluid CO at the bottom of the extraction column E. 2 C, control the temperature of the supercritical fluid to be 36°C, the pressure to be 11Mpa, and the flow rate to be 20m 3 / min, so that deoxyribose dissolves in supercritical fluid CO 2 C;

[0029] (2) High pressure supercritical fluid CO containing dissolved deoxyribose 2 B is depressurized to lower than the supercritical fluid CO through the throttle valve D 2 Enter the separation kettle F below the critical pressure; supercritical fluid CO 2 The solubility drops sharply to separate out the solute, which is separated into two parts, the deoxyribose solution H and the supercritical fluid gas, the former is the process product, which is regularly discharged from the bottom of the separation kettle F, and the latter is the c...

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Abstract

The invention discloses a technology for purifying deoxyribose through supercritical fluid crystallization. The technology comprises the steps as follows: (1) spraying a neutralized 90 DEG C deoxyribose liquor containing impurities from the top of an extraction tower through a raw material pump, meanwhile, introducing a supercritical fluid into the bottom of the extraction tower, and controlling the temperature of the supercritical fluid at 33-36 DEG C, the pressure at 9-11 Mpa and the flow at 15-20 m<3>/min; (2) reducing the pressure of the high-pressure supercritical fluid containing dissolved deoxyribose to the pressure lower than supercritical flow critical pressure through a throttle valve to allow the supercritical fluid to enter a separation kettle; (3) after extracting the deoxyribose, performing dehydration and drying processes sequentially on a product. The technology is simple, the equipment structure is compact, meanwhile, crystals form a crystal layer on a heat transfer surface instead of suspending in a liquid in the technological process, so that blockage of equipment and pipelines is avoided, and production faults are reduced. The product produced with the technology has high purity, bright and white appearance, good bioactivity and uniform grain size.

Description

technical field [0001] The present invention relates to a method for purifying deoxyribose, in particular to a method for purifying deoxyribose by supercritical fluid. Background technique [0002] Deoxyribose is a food preservative and preservative. This product has a strong antibacterial effect on yeast, spoilage bacteria and mold in food, and is widely used in the preservation and preservation of meat, fish, vegetables, fruits, beverages, cakes, etc. spectrum bacteriostatic agents. At present, the equipment for large-scale production of deoxyribose at home and abroad is a general enamel reaction kettle. The process of its mature process is roughly as follows: that is, dehydroacetic acid is neutralized with sodium hydroxide, and then the enamel kettle is cooled for crystallization, dehydration, drying, Packaging and other processes are used to obtain finished products. However, because the cooling temperature of the enamel kettle is not well controlled, it is easy to mak...

Claims

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Application Information

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IPC IPC(8): C07H1/06C07H3/08
CPCC07H1/06C07H3/08Y02P20/54
Inventor 范雪萍
Owner NANTONG DISONG TEXTILE CO LTD
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