CN1528772A - Method for preparing sucrose-6-ethyl ester - Google Patents
Method for preparing sucrose-6-ethyl ester Download PDFInfo
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- CN1528772A CN1528772A CNA2003101060270A CN200310106027A CN1528772A CN 1528772 A CN1528772 A CN 1528772A CN A2003101060270 A CNA2003101060270 A CN A2003101060270A CN 200310106027 A CN200310106027 A CN 200310106027A CN 1528772 A CN1528772 A CN 1528772A
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Abstract
The invention relates to a chemical products preparing method, especially a modified method to prepare a key intermediate sucrose-6-ethyl ester preparing food sweetener sucralose. Its concrete technical flow: (1) add sucrose to formyl compound-containing organic solvent, heat to 70-100 deg.C to dissolve, then cool to below 70 deg.C, add in nonpolar organic solvent and dibutyl tin dioxide to make reflux water reaction for 3-6 hours at 70-100 deg.C; (2) cool the above reacting substances to below 20 deg.C, then drip acetic anhydride to react for 3-10 hours; (3) add a proper amount of water to the above reacting solution, extract by nonpolar organic solvent, and then make reflux water reaction by nonpolar organic solvent to obtain sucrose-6-ethyl ester solution.
Description
Technical field
The present invention relates to chemical products preparation method, particularly a kind of preparation method of key intermediate sucrose-6-ethyl ester of improved preparation sweetening agent Sucralose.
Background technology
Sucralose is a kind of functional type sweeting agent, and it has represented the last word of sweeting agent development, and it is that 4,1 ', 6 ' three hydroxyls are formed by three chlorine atoms replacements in the sucrose molecules; And 8 hydroxyls are arranged in the sucrose molecules, and be respectively three primary carbon hydroxyls (6,1 ', 6 ') and five secondary carbon hydroxyls (2,3,4,3 ', 4 '), Sucralose be prepared and 6-position hydroxyl must be protected.
Utilize Dibutyltin oxide to carry out the existing various kinds of document report of selective esterification reaction, as: J.Org.Chem., 33,2684 (1968) and Tetrahedron, described in detail in 41,643 (1985) Dibutyltin oxide and hydroxy-containing compounds effect then with acid anhydrides generation transesterification reaction type, process and mechanism.Navia etc. disclose the preparation method of sucrose-6-ethyl ester in US4950746, process is: (1) sucrose, Dibutyltin oxide and methanol eddy reaction, concentrate 1, two (the 6-oxygen-sucrose)-1,1,3 of 3-, 3-tetrabutyl tindioxide (DBSS); (2) DBSS and diacetyl oxide are reacted in DMF, obtain sucrose-6-ethyl ester, content 63.4% through a series of processing then; The shortcoming of this method is that sucrose-6-ethyl ester content is too low, and many difficulties are arranged when being used for one-step chlorination reaction down.David etc. disclose the preparation method of sucrose-6-ethyl ester in US5023329, process is: (1) sucrose, Dibutyltin oxide, DMF and hexanaphthene refluxed 5 hours in 100 ± 1 ℃; (2) be chilled to-4 ℃ and drip diacetyl oxides, top temperature is no more than-1 ℃, spends the night in room temperature reaction after dripping diacetyl oxide; (3) add suitable quantity of water, with hexanaphthene extraction three times, concentrate a viscous material; (4) this viscous material is dissolved in methyl alcohol and obtains sucrose-6-ethyl ester through a series of processes processing, yield 55.3%, content 90.2%, this method shortcoming is that yield is not high, content is still on the low side.
Summary of the invention
In order to overcome the deficiencies in the prior art, the invention provides the preparation method of the higher sucrose-6-ethyl ester of a kind of yield and purity.
The technical solution adopted for the present invention to solve the technical problems is: a kind of preparation method of sucrose-6-ethyl ester, comprising the following steps: that (1) adds sucrose contains in the N-carbamoyl compound organic solvent, be heated to 70~100 ℃ of dissolvings, be cooled to then below 70 ℃, add non-polar organic solvent and Dibutyltin oxide backflow band water reaction 3~6 hours, 70~100 ℃ of the band water temperature of reaction that refluxes; (2) above-mentioned reactant is chilled to below 20 ℃, then to wherein being added dropwise to acetic anhydride 3~10 hours; (3) in above-mentioned reaction solution, add suitable quantity of water, with non-polar organic solvent extraction, and then with non-polar organic solvent reflux band water react sucrose-6-ethyl ester solution.
Further: according to the reaction requirement; the mol ratio of sucrose and Dibutyltin oxide, diacetyl oxide is 1: 0.9-1.1: 0.9-1.1; sucrose is 1 with the weight ratio that contains N-carbamoyl compound organic solvent, non-polar organic solvent: 2-10: 0.5-5, the weight ratio of sucrose and water is 1: 0.2-0.6.
Again further: containing N-carbamoyl compound organic solvent is N, dinethylformamide, N, N-diethylformamide, N, N-dipropyl methane amide; Non-polar organic solvent is hexane, hexanaphthene, benzene, ethyl acetate.
Again further: it is 85~95 ℃ that sucrose is added the heating for dissolving temperature that contains in the N-carbamoyl compound organic solvent; the time that adds the reaction of non-polar organic solvent and Dibutyltin oxide backflow band water then is 4~6 hours; the temperature that the band water that refluxes reacts is 85~95 ℃; the too high meeting of temperature of reaction is decomposed reactant; temperature is too low, and reaction becomes slow.
Again further: the temperature that is added dropwise to diacetyl oxide is 0~10 ℃, and the reaction times is 6~10 hours.
Further: what the band water reaction that refluxes was at last used is hexanaphthene or benzene.
The advantage of this invention is: simple to operate, purity height, its solution do not need separation can be directly used in down the one-step chlorination reaction.
Embodiment
Further specify the present invention below by embodiment:
Embodiment 1, a 1000ml four-hole round-bottomed flask, mechanical stirring is housed, thermometer and having in the prolong of water trap adds 150 gram (0.438mol) sucrose and 600mlDMF solution (N, dinethylformamide), be heated to 90~95 ℃ of dissolvings, be chilled to 60 ℃ and add 112.5 gram (0.450mol) Dibutyltin oxide and 150ml hexanaphthenes, be heated to 90~95 ℃, regulating ring hexane amount makes its reflux water-dividing; Reaction in 5 hours finishes, and is chilled to 5 ℃ and is added dropwise to 47.3 gram (0.463mol) diacetyl oxides, and drip off half an hour, is warming up to room temperature, continues to stir 6~8 hours; Add 50ml water, stir half hour, respectively with 200ml hexanaphthene extraction three times; Add again in the 200ml hexanaphthene reaction solution, reflux dewatering 5 hours steams at last and removes hexanaphthene, is cooled to room temperature and gets sucrose-6-ethyl ester DMF solution, high pressure liquid chromatographic analysis shows that sucrose-6-ethyl ester purity is 95% in the solution, and this solution can be directly used in down the one-step chlorination reaction.
Embodiment 2,100 liters of enamel reaction stills, mechanical stirring is housed, thermometer and the prolong that has water trap, add 15 kilograms of (43.8mol) sucrose and 60 liters of DMF solution, be heated to 80~90 ℃ of dissolvings, be chilled to 60 ℃ and add 11.25 kilograms of (45.0mol) Dibutyltin oxides and 15 liters of hexanaphthenes, be heated to 90~95 ℃, regulating ring hexane amount makes its reflux water-dividing; Reaction in 5 hours finishes, and is chilled to 5 ℃ and is added dropwise to 4.73 kilograms of (46.3mol) diacetyl oxides, and drip off half an hour, is warming up to room temperature, continues to stir 8 hours; Add 5 premium on currency, stir half hour, respectively with 20 liters of hexanaphthene extractions three times; Add again in 20 liters of hexanaphthene reaction solutions, reflux dewatering 5 hours steams at last and removes hexanaphthene, is cooled to room temperature and gets sucrose-6-ethyl ester DMF solution, high pressure liquid chromatographic analysis shows that sucrose-6-ethyl ester purity is 94.5% in the solution, and this solution can be directly used in down the one-step chlorination reaction.
Claims (6)
1, a kind of preparation method of sucrose-6-ethyl ester is characterized in that comprising the following steps:
(1) the sucrose adding is contained in the N-carbamoyl compound organic solvent, be heated to 70~100 ℃ of dissolvings, be cooled to then below 70 ℃, add non-polar organic solvent and Dibutyltin oxide backflow band water reaction 3~6 hours, 70~100 ℃ of backflow band water temperature of reaction;
(2) above-mentioned reactant is chilled to below 20 ℃, then to wherein being added dropwise to acetic anhydride 3~10 hours;
(3) in above-mentioned reaction solution, add suitable quantity of water, with non-polar organic solvent extraction, and then with non-polar organic solvent reflux band water react sucrose-6-ethyl ester solution.
2, the preparation method of sucrose-6-ethyl ester according to claim 1; it is characterized in that: the mol ratio of described sucrose and Dibutyltin oxide, diacetyl oxide is 1: 0.9-1.1: 0.9-1.1; sucrose is 1 with the weight ratio that contains N-carbamoyl compound organic solvent, non-polar organic solvent: 2-10: 0.5-5, the weight ratio of sucrose and water is 1: 0.2-0.6.
3, the preparation method of sucrose-6-ethyl ester according to claim 1 is characterized in that: the described N-of containing carbamoyl compound organic solvent is N, dinethylformamide, N, N-diethylformamide, N, N-dipropyl methane amide; Non-polar organic solvent is hexane, hexanaphthene, benzene, ethyl acetate.
4, the preparation method of sucrose-6-ethyl ester according to claim 1; it is characterized in that: the described heating for dissolving temperature that the sucrose adding is contained in the N-carbamoyl compound organic solvent is 85~95 ℃; the time that adds the reaction of non-polar organic solvent and Dibutyltin oxide backflow band water then is 4~6 hours, and the temperature that the band water that refluxes reacts is 85~95 ℃.
5, the preparation method of sucrose-6-ethyl ester according to claim 1 is characterized in that: the described temperature that is added dropwise to diacetyl oxide is 0~10 ℃, and the reaction times is 6~10 hours.
6, the preparation method of sucrose-6-ethyl ester according to claim 1 is characterized in that: what described last backflow band water reaction was used is hexanaphthene or benzene.
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Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008116359A1 (en) * | 2007-03-27 | 2008-10-02 | Suzhou Kaiyuan Minsheng Chemicals Technology Co., Ltd. | Method for preparing sucrose-6-ester |
CN102167712A (en) * | 2010-12-24 | 2011-08-31 | 李罡 | Synthetic method for sucralose |
CN101245085B (en) * | 2007-12-19 | 2012-02-01 | 上海同辰生物科技有限公司 | Technique for synthesizing and purifying sucrose trichloride |
CN102618601A (en) * | 2012-04-17 | 2012-08-01 | 广西大学 | Method for preparing sucrose-6-ethyl ester by using biological fermentation and immobilized enzyme methods |
CN103130843A (en) * | 2013-01-21 | 2013-06-05 | 溧阳维信生物科技有限公司 | Method of recycling and reusing of dibutyltin oxide in process of cane sugars manufacturing cane suger-6-ethyl ester |
CN104945454A (en) * | 2015-02-02 | 2015-09-30 | 李玉山 | Preparation method of pure micronized diosmin |
CN105601689A (en) * | 2016-03-04 | 2016-05-25 | 李云军 | Cane sugar stanizing method |
CN105646605A (en) * | 2016-03-04 | 2016-06-08 | 李云军 | Esterification method of cane sugar |
CN106946956A (en) * | 2017-03-16 | 2017-07-14 | 浙江新和成股份有限公司 | A kind of recrystallization method of acetic acid esters of sucrose 6 and its application |
CN109438533A (en) * | 2018-12-10 | 2019-03-08 | 安徽金禾实业股份有限公司 | A kind of method of Sucralose production high temperature continuous acylation |
CN109575090A (en) * | 2018-12-10 | 2019-04-05 | 安徽金禾实业股份有限公司 | A kind of preparation method of cane sugar-6-acetic ester |
CN109734755A (en) * | 2018-12-28 | 2019-05-10 | 山东三和维信生物科技有限公司 | A kind of Sucralose crystallization processes |
WO2022051988A1 (en) * | 2020-09-10 | 2022-03-17 | 安徽金禾实业股份有限公司 | Method for preparing sucrose-6-ester |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5023329A (en) * | 1990-04-23 | 1991-06-11 | Noramco, Inc. | Sucrose-6-ester production process |
GB2365424B (en) * | 2000-07-31 | 2002-06-26 | Tate & Lyle Plc | An improved method for the synthesis of sucrose-6-esters |
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2003
- 2003-10-01 CN CNB2003101060270A patent/CN1295237C/en not_active Expired - Fee Related
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008116359A1 (en) * | 2007-03-27 | 2008-10-02 | Suzhou Kaiyuan Minsheng Chemicals Technology Co., Ltd. | Method for preparing sucrose-6-ester |
CN101274949B (en) * | 2007-03-27 | 2010-12-29 | 苏州开元民生科技股份有限公司 | Preparation for sucrose-6-ester |
CN101245085B (en) * | 2007-12-19 | 2012-02-01 | 上海同辰生物科技有限公司 | Technique for synthesizing and purifying sucrose trichloride |
CN102167712A (en) * | 2010-12-24 | 2011-08-31 | 李罡 | Synthetic method for sucralose |
CN102167712B (en) * | 2010-12-24 | 2013-10-16 | 李罡 | Synthetic method for sucralose |
CN102618601A (en) * | 2012-04-17 | 2012-08-01 | 广西大学 | Method for preparing sucrose-6-ethyl ester by using biological fermentation and immobilized enzyme methods |
CN102618601B (en) * | 2012-04-17 | 2013-10-16 | 广西大学 | Method for preparing sucrose-6-ethyl ester by using biological fermentation and immobilized enzyme methods |
CN103130843A (en) * | 2013-01-21 | 2013-06-05 | 溧阳维信生物科技有限公司 | Method of recycling and reusing of dibutyltin oxide in process of cane sugars manufacturing cane suger-6-ethyl ester |
CN104945454A (en) * | 2015-02-02 | 2015-09-30 | 李玉山 | Preparation method of pure micronized diosmin |
CN105601689A (en) * | 2016-03-04 | 2016-05-25 | 李云军 | Cane sugar stanizing method |
CN105646605A (en) * | 2016-03-04 | 2016-06-08 | 李云军 | Esterification method of cane sugar |
CN106946956A (en) * | 2017-03-16 | 2017-07-14 | 浙江新和成股份有限公司 | A kind of recrystallization method of acetic acid esters of sucrose 6 and its application |
CN109438533A (en) * | 2018-12-10 | 2019-03-08 | 安徽金禾实业股份有限公司 | A kind of method of Sucralose production high temperature continuous acylation |
CN109575090A (en) * | 2018-12-10 | 2019-04-05 | 安徽金禾实业股份有限公司 | A kind of preparation method of cane sugar-6-acetic ester |
CN109734755A (en) * | 2018-12-28 | 2019-05-10 | 山东三和维信生物科技有限公司 | A kind of Sucralose crystallization processes |
WO2022051988A1 (en) * | 2020-09-10 | 2022-03-17 | 安徽金禾实业股份有限公司 | Method for preparing sucrose-6-ester |
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