CN113699196A - Anhydrous enzymatic method catalytic synthesis method of sucrose-6-acetate - Google Patents

Anhydrous enzymatic method catalytic synthesis method of sucrose-6-acetate Download PDF

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Publication number
CN113699196A
CN113699196A CN202110942046.5A CN202110942046A CN113699196A CN 113699196 A CN113699196 A CN 113699196A CN 202110942046 A CN202110942046 A CN 202110942046A CN 113699196 A CN113699196 A CN 113699196A
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sucrose
reaction kettle
pumping
molecular sieve
reaction
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CN202110942046.5A
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Inventor
祁飞
戴永辉
朱岁繁
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Anhui Jinhe Industrial Co Ltd
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Anhui Jinhe Industrial Co Ltd
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Priority to CN202110942046.5A priority Critical patent/CN113699196A/en
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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/12Disaccharides

Abstract

A method for synthesizing sucrose-6-acetate by anhydrous enzyme catalysis comprises the following steps: drying the molecular sieve for 8-24 h at the drying temperature of 120-300 ℃ by using water; pumping the tertiary amyl alcohol into a reaction kettle, pumping dimethyl sulfoxide into the reaction kettle, and uniformly stirring, wherein the volume ratio of the tertiary amyl alcohol to the dimethyl sulfoxide is 4: 1; adding sucrose into a reaction kettle, starting stirring to completely dissolve the sucrose, pumping vinyl acetate into the reaction kettle, uniformly stirring, controlling the concentration of the sucrose to be 0.03-0.12 mmoL/mL, and controlling the molar ratio of the sucrose to the vinyl acetate to be 1: 5-1: 20; adding molecular sieve at the bottom of the organic resin column, adding lipase into the column, and finally adding the molecular sieve. And (3) carrying out heat preservation reaction at 30 ℃, and pumping the medium in the reaction kettle into the organic resin column at the pump speed of 20 m/L for self-circulation reaction for 8-24 hours. The method has the advantages of simple operation, high efficiency, high conversion rate and low cost.

Description

Anhydrous enzymatic method catalytic synthesis method of sucrose-6-acetate
Technical Field
The invention relates to a method for synthesizing sucrose-6-acetate by catalysis of an anhydrous enzyme method.
Background
Sucralose is a fresh sweetener, which is a novel sweetener developed by the company of England and university of London and applied for patent in 1976, and is the only functional sweetener using sucrose as raw material. The sucralose has the effect of desalting sour and salty tastes, has the effect of covering up unpleasant tastes such as astringent taste, bitter taste, alcoholic taste and the like, has the synergistic effect on the spicy taste and the milk taste, and has a very wide application range. Therefore, the product is the most ideal intense sweetener at present, can be eaten by children, teenagers, adolescents, middle-aged people, old people and patients with various diseases, and has no any nutritional doubt. The method for synthesizing sucrose-6-acetate is mainly a traditional chemical method, such as acetic anhydride esterification, organometallic synthesis, orthoester method, etc., and there are reports about enzymatic synthesis. The chemical synthesis reaction conditions of sucrose ester are generally harsh, the synthesized product has dark color, and by-products are easily generated due to poor selectivity.
Disclosure of Invention
The technical problem to be solved by the invention is to provide a method for synthesizing sucrose-6-acetate by catalysis in an anhydrous enzyme method, which has the advantages of simple operation, high efficiency, high conversion rate and low cost.
In order to solve the technical problem, the invention provides a method for synthesizing sucrose-6-acetate by catalysis in an anhydrous enzyme method, which comprises the following steps:
(1) pretreatment of a molecular sieve: drying the 4A molecular sieve in a drying oven at the drying temperature of 120-300 ℃ for 8-24 h;
(2) preparing a mixed organic solution: pumping the tertiary amyl alcohol into a reaction kettle, pumping dimethyl sulfoxide into the reaction kettle, and uniformly stirring, wherein the volume ratio of the tertiary amyl alcohol to the dimethyl sulfoxide is 4: 1;
(3) adding sucrose into a reaction kettle, starting stirring to completely dissolve the sucrose, pumping vinyl acetate into the reaction kettle, uniformly stirring, controlling the concentration of the sucrose to be 0.03-0.12 mmoL/mL, and controlling the molar ratio of the sucrose to the vinyl acetate to be 1: 5-1: 20;
(4) adding part of the 4A molecular sieve after high-temperature drying at the bottom of the organic resin column, then putting lipase into the column, and finally adding part of the 4A molecular sieve. And (3) carrying out heat preservation reaction at 30 ℃, and pumping the medium in the reaction kettle into the organic resin column at the pump speed of 20 m/L for self-circulation reaction for 8-24 hours.
The principle and the advantages of the invention are as follows: compared with the prior art, the method has the advantages that lipase can be combined with vinyl acetate into an intermediate compound, can efficiently and specifically act on hydroxyl at the 6 th position of sucrose to perform transesterification, and simultaneously, the molecular sieve and the medium subjected to high-temperature treatment are utilized to fully remove moisture in a reagent machine and a closed space in a reciprocating circulation mode in an organic resin column, so that the balance is effectively moved towards the direction of a product. The method has simple experimental process, avoids the generation of byproducts and the low-efficiency transesterification reaction with poor selectivity. The organic resin column is filled with molecular sieve sucrose-6-acetate, and has the advantages of mild reaction conditions, strong catalytic selectivity, good product safety and the like.
Detailed Description
The first embodiment is as follows:
a method for synthesizing sucrose-6-acetate by anhydrous enzyme catalysis comprises the following steps:
(1) pretreatment of a molecular sieve: drying moisture of 600kg of 4A molecular sieve in a reactor vacuum drying oven at the drying temperature of 300 ℃ for 15 h;
(2) preparing a mixed organic solution: pumping the tert-amyl alcohol obtained by carrying out the high-speed transformation at 4.8m into the reaction kettle, and pumping the dimethyl sulfoxide obtained by carrying out the high-speed transformation at 1.2m into the reaction kettle and uniformly stirring;
(3) adding 123kg (0.06 mol/L) of sucrose into the reaction kettle, starting stirring to completely dissolve the sucrose, pumping 310kg (0.6 mol/L) of vinyl acetate, and uniformly stirring;
(4) after 10m of cultivation, 250kg of the 4A molecular sieve after high-temperature drying is added to the bottom of the organic resin column, 480kg of lipase is then added to the column, and finally 250kg of the 4A molecular sieve is added. And (3) carrying out heat preservation reaction at 30 ℃, and pumping the medium in the reaction kettle into the organic resin column at the pump speed of 20 m/L for self-circulation reaction for 9 hours.
A portion of the supernatant was taken and filtered through a 0.22 um filter into a liquid phase vial. HPLC quantitative analysis was carried out, and the conversion was 97.7% as a result of HPLC.
Example two:
a method for synthesizing sucrose-6-acetate by anhydrous enzyme catalysis comprises the following steps:
(1) pretreatment of a molecular sieve: drying 500kg of 4A molecular sieve in a reactor vacuum drying oven for 24 hours at the drying temperature of 120 ℃;
(2) preparing a mixed organic solution: pumping the tert-amyl alcohol obtained by carrying out the high-speed transformation at 4.8m into the reaction kettle, and pumping the dimethyl sulfoxide obtained by carrying out the high-speed transformation at 1.2m into the reaction kettle and uniformly stirring;
(3) adding 123kg (0.06 mol/L) of sucrose into the reaction kettle, starting stirring to completely dissolve the sucrose, pumping 310kg (0.6 mol/L) of vinyl acetate, and uniformly stirring;
(4) after 10m of cultivation, 250kg of the 4A molecular sieve after high-temperature drying is added to the bottom of the organic resin column, 480kg of lipase is then added to the column, and finally 250kg of the 4A molecular sieve is added. And (3) carrying out heat preservation reaction at 30 ℃, and pumping the medium in the reaction kettle into the organic resin column at the pump speed of 20 m/L for self-circulation reaction for 9 hours.
A portion of the supernatant was taken and filtered through a 0.22 um filter into a liquid phase vial. HPLC quantitative analysis was carried out, and the conversion was 94.1% as a result of HPLC.

Claims (1)

1. A method for synthesizing sucrose-6-acetate by anhydrous enzyme catalysis is characterized by comprising the following steps:
(1) pretreatment of a molecular sieve: drying the 4A molecular sieve in a drying oven at the drying temperature of 120-300 ℃ for 8-24 h;
(2) preparing a mixed organic solution: pumping the tertiary amyl alcohol into a reaction kettle, pumping dimethyl sulfoxide into the reaction kettle, and uniformly stirring, wherein the volume ratio of the tertiary amyl alcohol to the dimethyl sulfoxide is 4: 1;
(3) adding sucrose into a reaction kettle, starting stirring to completely dissolve the sucrose, pumping vinyl acetate into the reaction kettle, uniformly stirring, controlling the concentration of the sucrose to be 0.03-0.12 mmoL/mL, and controlling the molar ratio of the sucrose to the vinyl acetate to be 1: 5-1: 20;
(4) adding the high-temperature dried part of the 4A molecular sieve at the bottom of the organic resin column, then putting lipase into the column, finally adding the part of the 4A molecular sieve, carrying out heat preservation reaction at 30 ℃, and driving the medium in the reaction kettle into the organic resin column at the pump speed of 20m for self-circulation reaction for 8-24 hours.
CN202110942046.5A 2021-08-17 2021-08-17 Anhydrous enzymatic method catalytic synthesis method of sucrose-6-acetate Pending CN113699196A (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4980463A (en) * 1989-07-18 1990-12-25 Noramco, Inc. Sucrose-6-ester chlorination
US20080163867A1 (en) * 2005-02-22 2008-07-10 Molecular Separation Process in Various Steps of Process for Production of Chlorinated Sugars, Their Precursors and Derivatives
CN101759728A (en) * 2010-01-08 2010-06-30 江苏巨邦制药有限公司 Method for preparing and refining sucralose
CN101886100A (en) * 2010-07-12 2010-11-17 江南大学 Method for preparing sucrose-6-acetic ester by enzymatic method
CN102181494A (en) * 2011-03-21 2011-09-14 盐城捷康三氯蔗糖制造有限公司 Synthesis of sucrose-6-fatty acid ester through selective catalysis of immobilized aspergillus oryzae lipase
CN112029754A (en) * 2020-08-13 2020-12-04 浙江工业大学 Imprinted lipase and application thereof in synthesis of sucrose-6-ethyl ester

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4980463A (en) * 1989-07-18 1990-12-25 Noramco, Inc. Sucrose-6-ester chlorination
US20080163867A1 (en) * 2005-02-22 2008-07-10 Molecular Separation Process in Various Steps of Process for Production of Chlorinated Sugars, Their Precursors and Derivatives
CN101759728A (en) * 2010-01-08 2010-06-30 江苏巨邦制药有限公司 Method for preparing and refining sucralose
CN101886100A (en) * 2010-07-12 2010-11-17 江南大学 Method for preparing sucrose-6-acetic ester by enzymatic method
CN102181494A (en) * 2011-03-21 2011-09-14 盐城捷康三氯蔗糖制造有限公司 Synthesis of sucrose-6-fatty acid ester through selective catalysis of immobilized aspergillus oryzae lipase
CN112029754A (en) * 2020-08-13 2020-12-04 浙江工业大学 Imprinted lipase and application thereof in synthesis of sucrose-6-ethyl ester

Non-Patent Citations (5)

* Cited by examiner, † Cited by third party
Title
季祥等: "生物质能源及废物利用新技术", 31 December 2012, 吉林大学出版社, pages: 67 - 68 *
李明华;孟秀梅;吴金山;朱国廷;: "离子液体介质中脂肪酶催化合成蔗糖-6-乙酯工艺优化", 中国食品添加剂, no. 11, pages 207 - 48 *
杨绪娥;郑璞;孙志浩;倪晔;: "Lipozyme TL 100L的固定化及其催化合成蔗糖-6-乙酯", 化工进展, no. 11, pages 2517 - 2522 *
王勍等: "非水介质中脂肪酶催化合成蔗糖-6-乙酸酯", 食品与发酵工业, vol. 36, no. 12, pages 4 *
马玲芝;钱俊青;: "离子交换树脂固定化脂肪酶催化合成蔗糖乙酯", 浙江工业大学学报, pages 21 - 24 *

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