CN1453285A - Synthesis of sucrose-6-acetate - Google Patents
Synthesis of sucrose-6-acetate Download PDFInfo
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- CN1453285A CN1453285A CN 03126656 CN03126656A CN1453285A CN 1453285 A CN1453285 A CN 1453285A CN 03126656 CN03126656 CN 03126656 CN 03126656 A CN03126656 A CN 03126656A CN 1453285 A CN1453285 A CN 1453285A
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- acid catalyst
- solid acid
- synthetic method
- sucrose
- acetate
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Abstract
The present invention discloses the synthesis of sucrose-6-acetate. Sucrose material is mixed with N, N-dimethyl formamide solution, made to produce ester exchange reaction with ethyl acetate under the action of solid sulfate catalyst, which may be adsorbed on polymer carrier, to produce sucrose-6-acetate. Sucrose-6-acetate is the key intermediate for synthesizing trichlorosucrose as sweetening agent. The present invention has the advantages of simple technological process, high product purity, low production cost, etc. and is suitable for industrial production.
Description
Affiliated technical field
The present invention relates to a kind of key intermediate of synthetic sweetener Sucralose---the synthetic method of cane sugar-6-acetic ester.
Background technology
Sucralose, chemical name 4,1 ', 6 '-three chloro-4,1 ', 6 '-three deoxidation sucralose, its structural formula is:
The sugariness of Sucralose is 600 times of sucrose, is used as sweetening agent by more than 20 state approvals.
The preparation method of Sucralose has single radical protection method and full radical protection method two big classes substantially.Full radical protection method (as U.S. Pat 4801700, US4783526, US4362869 record) complex process does not have suitability for industrialized production to be worth; Usually concerning glucide, it is more more active that the hydroxyl on 6 is gone up hydroxyl than other positions, therefore, want to make other hydroxyls to react, and 6 hydroxyls remains unchanged, and just need carry out radical protection to 6 hydroxyls, and this is single basic starting point of protecting consideration.Therefore the core of single radical protection method is the preparation of cane sugar-6-acetic ester.The structural formula of cane sugar-6-acetic ester is:
The synthetic method of cane sugar-6-acetic ester mainly contains two kinds: the ethyl acetate method is (as U.S. Pat 4,889,928,5,449,772 the record) and the Dibutyltin oxide method (as U.S. Pat 5,023,329,4,950,746 records), these synthetic methods have certain advance, but also have certain limitation, as complex process, production cost height.
Summary of the invention
The object of the present invention is to provide a kind of new cane sugar-6-acetic ester synthetic method, this method technology is simple, production cost is low.
The synthetic method of a kind of cane sugar-6-acetic ester provided by the invention, this method is raw material with sucrose, add N, dinethylformamide solution, at solid acid catalyst or be adsorbed under the solid acid catalyst effect on the polymer carrier and ethyl acetate generation transesterification reaction, generate cane sugar-6-acetic ester.
Solid acid catalyst is also referred to as Lewies acid in organic chemistry, as ferric sulfate, and cerous sulfate, zinc chloride, iron(ic) chloride, zirconium chloride is usually used in esterification, transesterification reaction, the catalyzer of aldol (ketone) condensation reaction.Industrial, also this class catalyzer is adsorbed on polymer carrier such as the silica gel sometimes, make active higher loaded catalyst.The solid acid catalyst that the present invention selects for use is vitriol or hydrosulfate solid acid catalyst, and wherein the vitriol solid acid catalyst is selected cerous sulfate, copper sulfate or titanium sulfate for use; The hydrosulfate solid acid catalyst is selected sodium pyrosulfate for use.Preferably sulfuric acid cerium of the present invention and cerous sulfate-silica gel are as above-mentioned catalyst for reaction.When making catalyzer with cerous sulfate and cerous sulfate-silica gel, the selectivity height can obtain the cane sugar-6-acetic ester of higher degree, and product yield also can be up to more than 80%.
Compare with the synthetic method of existing cane sugar-6-acetic ester, the present invention has advantages such as technology is simple, product purity is high, production cost is low, is fit to very much suitability for industrialized production.
The present invention is further illustrated below in conjunction with embodiment.
Embodiment 1
The preparation of loading type cerous sulfate-silica-gel catalyst
In the 100ml round-bottomed flask, add 6.2g Ce (SO
4)
24H
2O, add water 20ml dissolving after, add 230～400 purpose silica gel 4.8g again, on Rotary Evaporators, be heated to 110 ℃ of vacuum (200Pa) dry 3 hours, obtain about 9.5 gram cerous sulfate-silica gel (1: 1) catalyzer.
Embodiment 2
In the 1000ml three-necked bottle, add sucrose 50g and N, dinethylformamide (DMF) 250ml, 2g anhydrous ceric sulfate and 50ml ethyl acetate, be heated to 80 ℃ and stirring reaction 4 hours, and be chilled to 10 ℃, the filtered and recycled cerous sulfate, steam earlier the unreacted ethyl acetate at normal temperatures, decompression steams whole DMF again.Get syrup 55g, detect with HPLC, the content of cane sugar-6-acetic ester is 79.3%.
Embodiment 3
In the 1000ml three-necked bottle, add sucrose 50g and N, dinethylformamide (DMF) 250ml, cerous sulfate-silica gel (1: 1) 5g, ethyl acetate 100ml was heated to 80 ℃ and stirring reaction 4 hours, was chilled to 5 ℃, filtering recovering catalyst, steam earlier the unreacted ethyl acetate at normal temperatures, decompression steams whole DMF again, gets syrup 56g, HPLC detects, and the content of cane sugar-6-acetic ester is 85.7%.
Claims (7)
1, a kind of synthetic method of cane sugar-6-acetic ester, it is characterized in that with sucrose being raw material, add N, dinethylformamide solution, at solid acid catalyst or be adsorbed under the solid acid catalyst effect on the polymer carrier and ethyl acetate generation transesterification reaction, generate cane sugar-6-acetic ester.
2, synthetic method according to claim 1 is characterized in that described solid acid catalyst is vitriol or hydrosulfate solid acid catalyst.
3, synthetic method according to claim 2 is characterized in that described vitriol solid acid catalyst is cerous sulfate, copper sulfate or titanium sulfate.
4, synthetic method according to claim 2 is characterized in that described hydrosulfate solid acid catalyst is a sodium pyrosulfate.
5, synthetic method according to claim 1 is characterized in that described polymer carrier is a silica gel.
6, synthetic method according to claim 3 is characterized in that described vitriol solid acid catalyst is a cerous sulfate.
7, synthetic method according to claim 2 is characterized in that the described vitriol that is adsorbed on the polymer carrier is cerous sulfate-silica gel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031266568A CN1176095C (en) | 2003-05-23 | 2003-05-23 | Synthesis of sucrose-6-acetate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031266568A CN1176095C (en) | 2003-05-23 | 2003-05-23 | Synthesis of sucrose-6-acetate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1453285A true CN1453285A (en) | 2003-11-05 |
| CN1176095C CN1176095C (en) | 2004-11-17 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB031266568A Expired - Lifetime CN1176095C (en) | 2003-05-23 | 2003-05-23 | Synthesis of sucrose-6-acetate |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102007053947A1 (en) | 2007-04-25 | 2008-10-30 | Shenzhen New Trend Industrial Development Co., Ltd., Shenzhen | Process for the synthesis of sucrose-6-acetic acid ester |
| CN100436467C (en) * | 2007-04-18 | 2008-11-26 | 江苏强盛化工有限公司 | Preparation method of saccharose-6-acetic acid esters |
| CN100480252C (en) * | 2006-10-13 | 2009-04-22 | 恩滋药业(南京)有限公司 | Sucrose derivative and preparing method thereofr, and method for synthesizing trichloro sucrose utilizing same |
| CN101886100A (en) * | 2010-07-12 | 2010-11-17 | 江南大学 | Method for preparing sucrose-6-acetic ester by enzymatic method |
| CN104356175A (en) * | 2014-11-24 | 2015-02-18 | 苏州乔纳森新材料科技有限公司 | Method for preparing sucralose-6-acetate |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100420697C (en) * | 2006-08-30 | 2008-09-24 | 河北苏科瑞科技有限公司 | Method of preparing trichloro sucrose-6-organic acid ester |
-
2003
- 2003-05-23 CN CNB031266568A patent/CN1176095C/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100480252C (en) * | 2006-10-13 | 2009-04-22 | 恩滋药业(南京)有限公司 | Sucrose derivative and preparing method thereofr, and method for synthesizing trichloro sucrose utilizing same |
| CN100436467C (en) * | 2007-04-18 | 2008-11-26 | 江苏强盛化工有限公司 | Preparation method of saccharose-6-acetic acid esters |
| DE102007053947A1 (en) | 2007-04-25 | 2008-10-30 | Shenzhen New Trend Industrial Development Co., Ltd., Shenzhen | Process for the synthesis of sucrose-6-acetic acid ester |
| CN101293902B (en) * | 2007-04-25 | 2011-05-11 | 吉安市新琪安科技有限公司 | Process for synthesizing sucrose-6- ethyl ester |
| US8609834B2 (en) | 2007-04-25 | 2013-12-17 | Shenzhen New Trend Industrial Development Co. Ltd. | Method for synthesizing sucrose-6-acetic ester |
| CN101886100A (en) * | 2010-07-12 | 2010-11-17 | 江南大学 | Method for preparing sucrose-6-acetic ester by enzymatic method |
| CN101886100B (en) * | 2010-07-12 | 2012-08-08 | 江南大学 | Method for preparing sucrose-6-acetic ester by enzymatic method |
| CN104356175A (en) * | 2014-11-24 | 2015-02-18 | 苏州乔纳森新材料科技有限公司 | Method for preparing sucralose-6-acetate |
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| Publication number | Publication date |
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| CN1176095C (en) | 2004-11-17 |
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Owner name: GUANGDONG GUANG YE QING YI FOOD TECHNOLOGY CO., L Free format text: FORMER OWNER: GUANGDONG PROV. INST. OF FOOD INDUSTRY Effective date: 20080118 |
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Effective date of registration: 20080118 Address after: Guangzhou, Guangdong Province, Panyu District City, South Village, new base village industrial zone, 303 Jin Xin Avenue Patentee after: GUANGDONG GUANGYE QINGYI FOOD TECHNOLOGY CO.,LTD. Address before: No. 146, Xingang East Road, Guangdong, Guangzhou Patentee before: Guangdong Food Industry Institute Co.,Ltd. |
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Granted publication date: 20041117 |
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