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Process for preparing ascorbic acid ester

An ascorbic acid and process technology, applied in the field of preparation of ascorbic acid esters, can solve problems such as increased post-processing difficulty, reduced product yield, and difficulty in suction filtration, and can avoid excessive drying time, reduce the content of impurities, and avoid the reduction of purity. Effect

Active Publication Date: 2011-02-16
HONGFENG CHEM GUAN COUNTY HEBEI PROV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of this method are firstly that the feed liquid is a viscous liquid, which is not easy to remove, and the loss is large, it is difficult to wash the filter cake with water, it is difficult to filter, and it is easy to emulsify, it is difficult to dry after acid washing, and the water is not easy to remove
[0004] Chinese patent CN 1,478,775A records: add ascorbic acid into the reaction bottle of tetrahydrofuran and water, drop into isopalmitoyl chloride and sodium hydroxide solution, keep the pH value of 6-8 in the reaction, after the reaction, add ethyl acetate to stir and extract the reactant, This method needs to keep the pH of the reaction solution at 6-8. When the pH value of the reaction solution is lower than 6, ethyl acetate is added, and the organic phase and the water phase are not easy to separate, resulting in greater product loss and impurities in the water phase. removal, leading to a decrease in product purity
This method is more complicated, and repeated operations will reduce the product yield. A large amount of diethyl ketone is used, and the production cost is high. Diethyl ketone and water are very miscible. Simply using this solvent for extraction will easily lead to solvent and viscous mixture. Miscible, not easy to separate, resulting in a decrease in yield
In addition, acid is artificially added during the isomerization process, which increases the difficulty of post-processing
The target product and palmitic acid are easily soluble in diethyl ketone, so it is not easy to separate in the end

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] ①Put 648.0g of palmitic acid into the reaction kettle, slowly add 3.2kg of 95% concentrated sulfuric acid and stir until it is molten (about 20min), then add 300.0g of ascorbic acid, and continue to stir and react for 18h at 20°C to 25°C;

[0035] ②Reduce the temperature of the reaction mixture in step ① to 5°C, slowly add 1.4kg of water at 0°C to 4°C until the temperature of the mixture no longer rises, then add 2.8kg of room temperature water to dilute the mixture, then add 3.1kg of acetone and 7.7kg For the mixed solution of chloroform, heat up to 30°C, stir and extract for 20 minutes; separate and remove the aqueous phase;

[0036] ③Add water at 25°C to the mixed liquid phase of chloroform and acetone obtained in step ②, the amount of water added each time is 4.2kg, stir and wash until the pH value is 6.5; separate and remove the water phase; wash to hydrolyze the sulfuric acid ester and remove sulfuric acid and water-soluble sex impurities;

[0037] ④The mixed org...

Embodiment 2

[0040] ①Put 3.15kg of sodium palmitate into the reactor, slowly add 37.8kg of 95% concentrated sulfuric acid and stir until molten (about 20min), then add 2.1kg of sodium ascorbate, and continue to stir and react for 24h at 20°C to 25°C;

[0041] ②Reduce the temperature of the reaction mixture in step ① to 15°C, slowly add 29.5kg of water at 0°C to 4°C until the temperature of the mixture no longer rises, then add 56.6kg of room temperature water to dilute the mixture, then add 77.5kg of methyl ethyl ketone and 309.5 kg of dichloroethane mixture, heated to 35°C, stirred and extracted for 30 minutes; separated and removed the water phase;

[0042] ③ Add water at 30°C to the mixed liquid phase of butanone and dichloroethane obtained in step ②, stir and wash until the pH value is 7.0; separate and remove the water phase; wash to hydrolyze the sulfuric acid ester and remove sulfuric acid and water-soluble impurities;

[0043] ④The mixed organic phase obtained in step ③ was subject...

Embodiment 3

[0046] ①Put 3kg of cinnamic acid into the reaction kettle, slowly add 30kg of 98% concentrated sulfuric acid and stir until it reaches a molten state (about 20min), then add 3kg of ascorbic acid, and continue to stir and react for 22h at 20°C to 25°C;

[0047] ② Cool down the reaction mixture in step ① to 25°C, slowly add 150kg of water until the temperature of the mixture no longer rises, then add 210kg of room temperature water to dilute the mixture, then add a mixed solution of 39.6kg of butyraldehyde and 356.4kg of tribromomethane, Heat up to 50°C, stir and extract for 40 minutes; separate and remove the water phase;

[0048] ③Add 35°C water to the mixed liquid phase of butyraldehyde and tribromomethane obtained in step ②, stir and wash until the pH value is 5.5; separate and remove the water phase; wash to hydrolyze the sulfuric acid ester and remove sulfuric acid and water-soluble impurities;

[0049] ④The mixed organic phase obtained in step ③ was subjected to vacuum di...

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PUM

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Abstract

The invention provides a process for preparing an ascorbic acid ester. Ascorbic acid and fatty acid are used as raw materials. The process comprises the following steps of: cooling the reacted mixture after sulfuric acid catalytic synthesis, adding water into the mixture, extracting the mixture by using mixed solution of aliphatic monoaldehyde and halogenated hydrocarbon, washing the extract by using water, evaporating the extract to obtain a coarse product, re-crystallizing the coarse product by using the halogenated hydrocarbon, and filtering, washing and drying the re-crystallized product to obtain high-purity ascorbic acid-6-fatty acid ester. The process is operated in the same reaction kettle, and the extracting process is in a liquid-liquid form so as to avoid the defects of difficult filtering and drying and difficult moisture removal in the prior art; the extracting solution well dissolves the esterification product and is easily separated from the water, the byproduct is little, and particularly the disadvantages that the purity of a target product is reduced and the quality becomes poor due to emulsification during acid washing in the prior art are avoided; and the coarse product is re-crystallized by using the halogenated hydrocarbon so as to effectively remove a little amount of residual fatty acid which is not totally extracted. The yield of the fatty acid ester product of the ascorbic acid ester produced by the process is over 70 percent, and the purity is over 98 percent.

Description

technical field [0001] The invention relates to a preparation process of ascorbic acid ester, in particular to a preparation process of saturated fatty acid and unsaturated fatty acid ascorbic acid ester. Background technique [0002] There are many methods for synthesizing ascorbic acid fatty acid ester production technology, such as U.S. Patent No. 4,151,178 records: add sulfuric acid, ascorbic acid, and dodecanoic acid in the reaction bottle in turn until all the dodecanoic acid is completely reacted, and the reaction solution is first extracted with a large amount of ether, divided layer, the ether phase was washed with brine, and then the ether was evaporated, and the insoluble solid was repeatedly washed with petroleum ether, and dried in vacuo to obtain the product. Recrystallization is carried out with diethyl ether and petroleum ether. In this method, a large amount of volatile, inflammable and explosive diethyl ether needs to be used, and the crude product is repea...

Claims

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Application Information

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IPC IPC(8): C07D307/62
Inventor 裴双秀梁志勇
Owner HONGFENG CHEM GUAN COUNTY HEBEI PROV
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