CN101862678A - Method for preparing tungstosilicic acid-supported catalyst for use in preparation of menthyl lactate - Google Patents
Method for preparing tungstosilicic acid-supported catalyst for use in preparation of menthyl lactate Download PDFInfo
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- CN101862678A CN101862678A CN201010210779A CN201010210779A CN101862678A CN 101862678 A CN101862678 A CN 101862678A CN 201010210779 A CN201010210779 A CN 201010210779A CN 201010210779 A CN201010210779 A CN 201010210779A CN 101862678 A CN101862678 A CN 101862678A
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Abstract
The invention relates to a tungstosilicic acid-supported catalyst for the esterification of lactic acid and menthol, which comprises the following components: silicotungstic acid H2SiW12O40.xH2O with a Keggin structure, which accounting for 5 to 50 mass percent of the total mass of the catalyst; and a catalyst carrier, which is attapulgite. Under optimized conditions, the menthyl lactate yield is up to over 80 percent. The tungstosilicic acid-supported catalyst of the invention has the advantages of high activity, easy separation, repeated use and the like. The menthyl lactate is widely used as a freshener for spices, oral care and cosmetics.
Description
Technical field
The present invention relates to the method for making and the application of a kind of menthol and lactic acid catalyst for esterification reaction, its esterification products menthyl lactate (ML) is widely used in the freshener of spices, MC and cosmetics.
Background technology
Menthyl lactate (ML) is the ester that menthol and lactic acid are arranged, and is widely used in the freshener of spices, MC and cosmetics.In recent years there has been the people to propose that menthyl lactate is used for treatment of cancer since or as diagnostic reagent (U.S. Patent Application Publication 2005/0054651).
Menthol has three chiral centres, and lactic acid has a chiral centre, so ML has four chiral centres, has 16 kinds of possible stereoisomers accordingly, the ML (See Figure) that the modal l-of being menthol and L (+)-the lactic acid reaction obtains
The simplest ML synthetic method is exactly lactic acid and menthol direct esterification, and still, the details of this reaction is reported seldom.Before more than 100 year, people such as McKenzie (J.Chem.Soc.87 (1905) 1016) described a kind of " passing through chlorine-hydride method ", mainly prepared l-menthyl-dl-lactate by l-menthol and dl-lactic acid by esterification.Course of reaction comprises in the ethereal solution that contains l-menthol and excessive dl-lactic acid and feeds hydrogen chloride gas, uses this ether of aqueous sodium carbonate and water washing then mutually, and is dry again, concentrate and distillation.But this method is not used for synthetic ML, but after attempting to obtain ML by esterification, hydrolysis ML obtains high menthol of optical selective or lactic acid, is a kind of exploration of optical resolution.
People such as Kuhn (U.S. Patent number 5783725) have described the acid-catalyzed esterification reaction of L-(+)-lactic acid and l-menthol.The acid of being advised is sulfuric acid, phosphoric acid, methanesulfonic acid, p-methyl benzenesulfonic acid, acid clay and acid-exchange resin.After the post processing, the purity of ML can arrive 97-98%.This patent does not provide the details of synthetic reaction, does not provide the productive rate of the ML of acquisition yet.
People such as L.Horner (Liebigs Ann.Chem. (1979) 1232) have also described the method for the synthetic ML of direct esterification.Roughly be in the presence of chloroform and strong-acid ion exchange resin, with L (+)-lactic acid and L-menthol reaction, post processing comprises peroxidating aluminium post and distillation except that desolvating, and after the fractionation, the productive rate of ML can reach 35%.
(Guangdong Industry Technical College journal, Vol.5, No.1 (2006) socialize, use the mixed solution of a kind of zirconium oxychloride and sodium metasilicate, behind ammonia precipitation process, soak with sulfuric acid again, the catalyst that obtained in 3 hours in 400 ℃ of roastings then, the ML productive rate can reach more than 70%.
Replace the esterification traditional catalyst with solid catalyst and become important catalyticing research field.Heterogeneous catalysis is easy to separate with product, can also become the basis of fixed-bed catalytic.Solid acid is applied in fields such as alkylation, esterification, etherificates as a kind of eco-friendly heterogeneous catalysis, attapulgite (Attapulgite) be a kind of tool chain layer structure contain Shuifu County's magnesium silicate clay mineral.Compression strength height, specific area are big, are mainly used in molecular sieve etc. in chemical industry.Heteropoly acid (HPA) is a kind of general name of being made up of by the oxygen atom ligand bridging with a fixed structure central atom caryogamy position atom that contains oxygen multielement acid.As a kind of novel catalysis material, heteropoly acid has strong and Bronsted acid and " accurate liquid phase " characteristic homogeneous have effective catalytic action to reactions such as dehydration, esterification, etherificates.What be used as esterification catalyst mainly is 12 serial heteropoly acids, and commonly used is that phosphotungstic acid, silico-tungstic acid, phosphomolybdic acid and tungsten germanic acid etc. are several.
In the polar reaction system, be difficult to as the shortcoming that solid acid uses, price is expensive in order to overcome heteropoly acid, usually with loaded by heteropoly acid on suitable carriers, increase the surface area of catalyst.Have with loaded by heteropoly acid on silica gel the catalysis Synthesis of Butyl Acetate (osmanthus etc. of becoming a common practice, Zhongnan College of Nationalities's journal (natural science edition) .20 (2), 2001:68-72); Have with loaded by heteropoly acid on active carbon the reaction of catalysis acetate and n-butanol (Schwegler M.A. etc., Appl Catal[A], 80,1992:41-57; On H β Zeolites Zeolites, catalysis synthesizes n-butyl acetate, isobutyl acetate, ethyl acetate and n-butyl lactate and has obtained effect (Chinese patent 200710118426.7) preferably Du Yingchun with loaded by heteropoly acid.People such as Qian Yunhua load on the attapulgite catalysis with solid super-strong acid and have synthesized propylben obtain a good result (food industry science and technology, 2007 (11): 189-191)
The catalyst of the synthetic usefulness of the ML that provides from document as seen, main catalyst is the various acidic materials that comprise solid acid, also useful transistion metal compound etc.
The present invention will provide a kind of catalytic efficiency height, productive rate height, reusable solid acid catalyst, use for ML is synthetic.
Summary of the invention
Under the silico-tungstic acid catalysis that is carried on the attapulgite, menthol and lactic acid esterification obtain menthyl lactate (ML).
The used menthol of the present invention can be arbitrary stereochemical structure of menthol; Consider all stereoisomers that on market, can directly buy menthol, comprise l-menthol, d-menthol, dl-menthol or the like; Their lactate all provides excellent physiological cooling performance.
Lactic acid also has a chiral centre, and it has two kinds of possible stereoisomers, L-(+)-lactic acid and D-(-)-lactic acid. and lactic acid provides (for example 85%wt) with the form of fortified aqueous usually.The present invention can use arbitrary stereoisomer of lactic acid.
The inventor finds, in the polar reaction system, the solid silicon heteropoly tungstic acid catalyzer that adopts immersion process for preparing to be carried on the attapulgite can catalytic esterification, and reaction efficiency height, productive rate are also high, so decision is applied to the synthesizing lactic acid menthol ester with this catalyst.
The preparation method of silico-tungstic acid loaded catalyst that the present invention is used for catalysis lactic acid and menthol esterification reaction is as follows: with Keggin structure silico-tungstic acid (H
3SiW
12O
40-xH
2O) be dissolved in the deionized water, the attapulgite of anticipating mixed obtaining suspension with above-mentioned solution, steeping medium is a deionized water, the solid-to-liquid ratio of immersion solvent volume and carrier is 1～10mL/g, at room temperature stirred 30 minutes, left standstill 1 hour, 6～12 times repeatedly; Heat drying then 100-110 ℃ of drying 1～4 hour, obtained catalyst in 1～4 hour in 180～240 ℃ of calcination activations again.Optimum condition is solid-to-liquid ratio 3～8mL/g, stirs, leaves standstill repetition 8～10 times, and catalyst suspension is 100～110 ℃ of dryings 2～3 hours, again in 200～220 ℃ of roastings 2～3 hours.
The preliminary treatment of attapulgite: use after 1～4 hour in 150～250 ℃ of following roastings.Preferred condition is 180～220 ℃ of following roastings 2～3 hours.
Typical esterification reaction process:
In the there-necked flask that agitator, thermometer, water knockout drum and reflux condenser are housed, add lactic acid, menthol (mol ratio is: lactic acid: menthol=1.5～1: 1～1.4), catalyst and band aqua heptane.Turn on agitator, heating, cessation reaction after 2～6 hours is reacted in timing when refluxing beginning, is cooled to room temperature.Incline and liquid layer (catalyst can be reused).Through distillation, go out band aqua heptane, with water: ethanol=mixed solvent carried out crystallization in 10: 1, obtained menthyl lactate.In this esterification, catalyst amount is 1～10%, preferred 3～6%.
Silico-tungstic acid loaded catalyst of the present invention is mainly used in the esterification between lactic acid and the menthol.
The used raw material of the present invention comprises: Keggin structure silico-tungstic acid (H
3SiW
12O
40-xH
2O), attapulgite (purity＞95%), deionized water, heptane, lactic acid (purity 〉=85%) and menthol.
Specific embodiment
Embodiment 1
5% SiW
12/ attapulgite Preparation of catalysts
Take by weighing Keggin structure silico-tungstic acid (H
3SiW
12O
40-xH
2O) 1g is dissolved in the deionized water, takes by weighing at 4 hours attapulgite 19g of 150 ℃ of following roastings to mix with silico-tungstic acid solution, and steeping medium is a deionized water, the solid-to-liquid ratio ratio of carrier quality (the steeping medium volume with) 1mL/g.Stirred 30 minutes under the room temperature, left standstill 1 hour, repeat 6 times; Heat drying was warming up to 100 ℃ in 5～6 hours then, was incubated 1 hour, in 180 ℃ of following roastings 4 hours, obtained 5% SiW again
12/ attapulgite catalyst.
Embodiment 2
10% SiW
12/ attapulgite Preparation of catalysts
Take by weighing Keggin structure silico-tungstic acid (H
3SiW
12O
40-xH
2O) 2g is dissolved in the deionized water, takes by weighing at 3 hours attapulgite 28g of 200 ℃ of following roastings to mix with silico-tungstic acid solution, and steeping medium is a deionized water, the solid-to-liquid ratio ratio of carrier quality (the steeping medium volume with) 3mL/g.Stirred 30 minutes under the room temperature, left standstill 1 hour, repeat 7 times; Heat drying was warming up to 100 ℃ in 5～6 hours then, was incubated 2 hours, in 190 ℃ of following roastings 3 hours, obtained 10% SiW again
12/ attapulgite catalyst.
Embodiment 3
20% SiW
12/ attapulgite Preparation of catalysts
Take by weighing Keggin structure silico-tungstic acid (H
3SiW
12O
40-xH
2O) 4g is dissolved in the deionized water, takes by weighing at 2 hours attapulgite 16g of 220 ℃ of following roastings to mix with silico-tungstic acid solution, and steeping medium is a deionized water, the solid-to-liquid ratio ratio of carrier quality (the steeping medium volume with) 5mL/g.Stirred 30 minutes under the room temperature, left standstill 1 hour, repeat 8 times; Heat drying was warming up to 100 ℃ in 5～6 hours then, was incubated 3 hours, in 200 ℃ of following roastings 2 hours, obtained 20% SiW again
12/ attapulgite catalyst.
Embodiment 4
30% SiW
12/ attapulgite Preparation of catalysts
Take by weighing Keggin structure silico-tungstic acid (H
3SiW
12O
40-xH
2O) 6g is dissolved in the deionized water, takes by weighing at 2 hours attapulgite 14g of 235 ℃ of following roastings to mix with silico-tungstic acid solution, and steeping medium is a deionized water, the solid-to-liquid ratio ratio of carrier quality (the steeping medium volume with) 8mL/g.Stirred 30 minutes under the room temperature, left standstill 1 hour, repeat 10 times; Heat drying was warming up to 100 ℃ in 5～6 hours then, was incubated 4 hours, in 220 ℃ of following roastings 1.5 hours, obtained 30%SiW again
12/ attapulgite catalyst.
Embodiment 5
50% SiW
12/ attapulgite Preparation of catalysts
Take by weighing Keggin structure silico-tungstic acid (H
3SiW
12O
40-xH
2O) 10g is dissolved in the deionized water, takes by weighing at 1 hour attapulgite 10g of 250 ℃ of following roastings to mix with silico-tungstic acid solution, and steeping medium is a deionized water, the solid-to-liquid ratio ratio of carrier quality (the steeping medium volume with) 10mL/g.Stirred 30 minutes under the room temperature, left standstill 1 hour, repeat 12 times; Heat drying was warming up to 100 ℃ in 5～6 hours then, was incubated 4 hours, in 240 ℃ of following roastings 1 hour, obtained 50%SiW again
12/ attapulgite catalyst.
Embodiment 6-10
Present embodiment is intended to investigate the prepared catalyst lactic acid of embodiment 1～5 and the effect of menthol esterification reaction.
In the there-necked flask that agitator, thermometer, water knockout drum and reflux condenser are housed, add lactic acid: menthol=1: 1.3, the catalyst 5% of embodiment 1～5 (accounting for reactant weight) and band aqua heptane (80～85g).Turn on agitator, heating, cessation reaction after 4 hours is reacted in timing when refluxing beginning, is cooled to room temperature.Inclining liquid layer, (catalyst can be reused).Through distillation, remove band aqua heptane, with water: ethanol=1; 10 mixed solvents carry out crystallization, obtain menthyl lactate, purity 〉=98%.
Embodiment 11-17
Present embodiment is intended to investigate the influence to catalysis lactic acid and menthol esterification reaction of catalyst amount of the present invention and change in reaction conditions.
In the there-necked flask that agitator, thermometer, water knockout drum and reflux condenser are housed, add lactic acid: menthol=1.5～1: 1～1.4,30% SiW
12/ attapulgite catalyst (1～10%) and band aqua heptane (80～85g).Turn on agitator, heating, cessation reaction after 2～6 hours is reacted in timing when refluxing beginning, is cooled to room temperature.Inclining liquid layer, (catalyst can be reused).Through distillation, remove band aqua heptane, with water: ethanol=mixed solvent carried out crystallization in 1: 10, obtained menthyl lactate, purity 〉=98%.
| Embodiment | Lactic acid (85%) (g) | Menthol (g) | Menthyl lactate output (g) | Menthyl lactate productive rate * (%) | Remarks |
| ??11 | ??160 | ??156 | ??156.0 | ??68.4 | ??1.5∶1 |
| ??12 | ??127 | ??156 | ??161.7 | ??70.9 | ??1.2∶1 |
| ??13 | ??160 | ??234 | ??165.5 | ??72.6 | ??1∶1 |
| ??14 | ??160 | ??258 | ??176.7 | ??77.5 | ??1∶1.1 |
| ??15 | ??160 | ??281 | ??182.9 | ??80.2 | ??1∶1.2 |
| ??16 | ??160 | ??304 | ??185.4 | ??81.3 | ??1∶1.3 |
| ??17 | ??160 | ??328 | ??186.5 | ??81.8 | ??1∶1.4 |
Claims (3)
1. silico-tungstic acid loaded catalyst that is used for catalysis lactic acid and menthol esterification reaction; Be Keggin structure silico-tungstic acid concrete the composition, and its content accounts for 5～50% mass fractions of catalyst total amount, is preferably 30～40%; Carrier is an attapulgite.
2. the preparation that is used for the silico-tungstic acid loaded catalyst of lactic acid and menthol esterification reaction according to claim 1 comprises the steps:
With Keggin structure silico-tungstic acid (H
3SiW
12O
40XH
2O) be dissolved in the deionized water, the attapulgite of anticipating mixed obtaining suspension with above-mentioned solution, steeping medium is a deionized water, the solid-to-liquid ratio of immersion solvent volume and carrier is 1～10mL/g, at room temperature stirred 30 minutes, left standstill 1 hour, 6～12 times repeatedly; Heat drying then 100～110 ℃ of dryings 1～4 hour, obtained catalyst in 1～4 hour in 180～240 ℃ of calcination activations again; Optimum condition is solid-to-liquid ratio 3～8mL/g, stirs, leaves standstill repetition 8～10 times, and catalyst suspension is 100～110 ℃ of dryings 2～3 hours, again in 200～220 ℃ of roastings 2～3 hours;
The preliminary treatment of attapulgite: use after 1～4 hour in 150～250 ℃ of following roastings, preferred condition is 180～220 ℃ of following roastings 2～3 hours.
3. one kind with the described lactic acid of claim 1 and menthol esterification reaction, typical esterification reaction process: in the there-necked flask that agitator, thermometer, water knockout drum and reflux condenser are housed, add lactic acid, menthol (mol ratio is: lactic acid: menthol=1.5～1: 1～1.4), catalyst and band aqua heptane; Turn on agitator, heating, cessation reaction after 2～6 hours is reacted in timing when refluxing beginning, is cooled to room temperature, and inclining liquid layer (catalyst can be reused); Through distillation, go out band aqua heptane, with water: ethanol=mixed solvent carried out crystallization in 10: 1, obtained menthyl lactate;
In this esterification, catalyst amount is 1～10%, preferred 3～6%; Reaction time is preferably 3～4 hours.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102078824A (en) * | 2010-12-06 | 2011-06-01 | 浙江树人大学 | 4-dimethylaminopyridine supported catalyst used for preparation of menthol ester lactate |
| CN102744057A (en) * | 2011-04-20 | 2012-10-24 | 中国石油化工股份有限公司 | Preparation method of silicotungstic heteropoly acid loaded catalyst |
| CN103951561A (en) * | 2014-05-06 | 2014-07-30 | 杭州师范大学 | Method for preparing L-menthyl glyoxylate-hydrate through catalysis of heteropoly acid |
| CN105618140A (en) * | 2016-03-24 | 2016-06-01 | 广西新天德能源有限公司 | Solid supported catalyst of butyl acetate and preparation method of solid supported catalyst |
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| CN101618349A (en) * | 2009-07-06 | 2010-01-06 | 江南大学 | Preparation method of heteropoly acid catalysts by taking organic modified concave-convex soil as carrier |
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| CN101293210A (en) * | 2007-04-25 | 2008-10-29 | 中国科学院大连化学物理研究所 | Composite catalyst for preparing sec-butyl acetate with direct esterification of ethyl ester and butylene |
| CN101618349A (en) * | 2009-07-06 | 2010-01-06 | 江南大学 | Preparation method of heteropoly acid catalysts by taking organic modified concave-convex soil as carrier |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102078824A (en) * | 2010-12-06 | 2011-06-01 | 浙江树人大学 | 4-dimethylaminopyridine supported catalyst used for preparation of menthol ester lactate |
| CN102744057A (en) * | 2011-04-20 | 2012-10-24 | 中国石油化工股份有限公司 | Preparation method of silicotungstic heteropoly acid loaded catalyst |
| CN102744057B (en) * | 2011-04-20 | 2015-01-07 | 中国石油化工股份有限公司 | Preparation method of silicotungstic heteropoly acid loaded catalyst |
| CN103951561A (en) * | 2014-05-06 | 2014-07-30 | 杭州师范大学 | Method for preparing L-menthyl glyoxylate-hydrate through catalysis of heteropoly acid |
| CN103951561B (en) * | 2014-05-06 | 2016-06-08 | 杭州师范大学 | A kind of heteropoly acid catalysis prepares the method for MENTHOL glyoxylic ester monohydrate |
| CN105618140A (en) * | 2016-03-24 | 2016-06-01 | 广西新天德能源有限公司 | Solid supported catalyst of butyl acetate and preparation method of solid supported catalyst |
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