CN1872835A - Method for preparing lignocaine ethyl ester caproic acid by catalyzing cation exchange resin in type of sulfonic acid - Google Patents
Method for preparing lignocaine ethyl ester caproic acid by catalyzing cation exchange resin in type of sulfonic acid Download PDFInfo
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- CN1872835A CN1872835A CN 200610014476 CN200610014476A CN1872835A CN 1872835 A CN1872835 A CN 1872835A CN 200610014476 CN200610014476 CN 200610014476 CN 200610014476 A CN200610014476 A CN 200610014476A CN 1872835 A CN1872835 A CN 1872835A
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Abstract
This invention provides a method for preparing diethylaminoethyl hexanoate with sulfonic acid-type cation exchanger resin as the catalyst. The method comprises: (1) selecting n-hexanoic acid and diethylaminoethanol as the raw materials at a mol. ratio of (1.1-1.3):1,0; (2) selecting crosslinked polystyrene sulfonic acid-typed cation exchange resin as the catalyst for esterification; (3) adding the raw materials to a reactor, stirring, heating to refluxing, and removing water in the water segregator below the refluxing condenser till no water is formed; (4) separating the resin, removing the solvent, and distilling to obtain the final product. The method has such advantages as high product yield (90-93%), high product purity (95-96%), simple operation, no corrosion, low raw material consumption, and high profit. After application, the crops yield can be increased by 10-50%, and even 50-80% for capsicum, tomato, etc.
Description
Technical field
The present invention relates to a kind ofly, particularly a kind ofly promote that crop grows, the method for caproic acid lignocaine ethyl ester is produced in the sulfonic acid ion exchange resin catalysis that is used for multiple kinds of crops such as vegetables, fruit, cotton, paddy rice disease-resistant, volume increase with chemical process synthetic a kind of agricultural plant hormone.
Background technology
According to reports, caproic acid lignocaine ethyl ester synthetic method majority is caproic acid and diethylaminoethanol direct esterification, makes catalyzer with the vitriol oil.Used titanium dioxide of ZL-92112507.0 bibliographical information or heteropolyacid are made catalyzer.The vitriol oil is classical esterifying catalyst, and its shortcoming is that yield is not high, generally is 80～85%.This reaction reduces activity because of sulfuric acid and diethylaminoethanol salify, and heteropolyacid is manufactured trouble, and price is also somewhat expensive.Japanese Patent is flat-introduce method in the 1-290606 document with caproyl chloride and diethylaminoethanol prepared in reaction ester, use the chloroform give solvent, and yield is up to 98%.But the preparation caproyl chloride need react with the sulfur oxychloride of caproic acid and 2～3 times (moles), and its shortcoming is that raw material consumption is more, produces a large amount of sulfurous gas and hydrogenchloride, certainly will bring contaminate environment, increases disposal of three wastes cost.
Summary of the invention
For solving the problem that exists in the above-mentioned technology, the purpose of this invention is to provide a kind of sulfonic acid ion exchange resin catalysis and produce the method for caproic acid lignocaine ethyl ester, this method can improve reaction yield, can avoid making the trouble of heteropolyacid and the high flow rate of chloride method, the problem of many three wastes again.
For achieving the above object, the technical solution used in the present invention provides the method that the caproic acid lignocaine ethyl ester is produced in a kind of sulfonic acid ion exchange resin catalysis, and this method comprises the steps:
1., select raw material
Reaction raw materials is n-caproic acid and diethylaminoethanol, and its material molar ratio is 1.1～1.3: 1.0;
2., the esterification reaction formula is:
The catalyzer that above-mentioned reaction is adopted is a crosslinked polystyrene sulfonic acid type Zeo-karb, this resin is through pre-treatment, make it convert Hydrogen to after drop anhydrate wherein a part of natural air drying (not moisture), another part is wet preserves (moisture in the resin), and then tests its catalytic effect respectively; The addition of catalyst system therefor is 0.1～5% (weight ratio) of described diethylaminoethanol (standard substance);
3., reaction raw materials dropped into reaction flask after, stir, be heated to backflow, the moisture that reflux exchanger is produced in the water trap of dress is down told at any time, when regeneration water not (about 4 hours), reaction is promptly accused and is finished, and tells resin, slough solvent, rectifying promptly draws product.
The solvent of described esterification is selected a kind of of benzene, toluene or dimethylbenzene for use.
0.5～2% (weight ratio) of the preferably described diethylaminoethanol of the addition of catalyzer (standard substance).
Effect of the present invention is to adopt this method to make the product yield of gained reach 90～93%, and purity reaches 95～96%.Operating procedure is simple, and non-corrosiveness reduces the consumption and the three waste discharge of material simultaneously, can improve economic return.The crop yield amplitude that is applied can reach 10～50%, as is used for can increasing production 50～80% on the crops such as capsicum, tomato.
Embodiment
The method that the caproic acid lignocaine ethyl ester is produced in sulfonic acid ion exchange resin catalysis of the present invention is illustrated by the following example.
The method of caproic acid lignocaine ethyl ester is produced in sulfonic acid ion exchange resin catalysis of the present invention, and this method comprises the steps:
1., select raw material
Reaction raw materials is n-caproic acid and diethylaminoethanol, and its material molar ratio is 1.1～1.3: 1.0.
2., the esterification reaction formula is:
The catalyzer that above-mentioned reaction is adopted is a crosslinked polystyrene sulfonic acid type Zeo-karb, this resin is through pre-treatment, make it convert Hydrogen to after drop anhydrate wherein a part of natural air drying (not moisture), another part is wet preserves (moisture in the resin), and then tests its catalytic effect respectively; The addition of catalyst system therefor is 0.1～5% (weight ratio) of described diethylaminoethanol (standard substance), 0.5～2% (weight ratio) of preferably described diethylaminoethanol (standard substance), catalyzer are that crosslinked polystyrene sulfonic acid type Zeo-karb is used homemade trade mark strong acid-1 resin of following embodiment.
3., reaction raw materials dropped into reaction flask after, stir, be heated to backflow, the moisture that reflux exchanger is produced in the water trap of dress is down told at any time, when regeneration water not (about 4 hours), reaction is promptly accused and is finished, and tells resin, slough solvent, rectifying promptly draws product.
The solvent of described esterification is selected a kind of of benzene, toluene or dimethylbenzene for use.
Embodiment 1:
The 100ml four-hole bottle is equipped with agitator, be furnished with water trap under the reflux exchanger, drop into caproic acid 23.6g, diethylaminoethanol 21.06g, toluene 30ml, homemade trade mark strong acid-1 resin (Hydrogen, air-dry) 0.4g about 1.9%, slowly be heated to backflow, keep refluxing 4～10 hours.When water trap no longer divided water outlet, reaction promptly came to an end.Tell resin, slough solvent, 88～90 ℃/1mmHg caproic acid lignocaine ethyl ester product is collected in rectifying, obtains the caproic acid lignocaine ethyl ester of 37.5g colourless oil liquid, and stratographic analysis purity is 96%.
Embodiment 2:
Experimental installation and operation be with embodiment 1, and catalyzer is about 1.9% with Hydrogen wet resin 0.8g, product caproic acid lignocaine ethyl ester 36.7g, purity is 95%.
Embodiment 3:
Laboratory apparatus and operation are with embodiment 1, and the catalyzer vitriol oil gets caproic acid lignocaine ethyl ester product 34.6g, and purity is 95%.
Embodiment 4:
Laboratory apparatus and operation are with embodiment 1, and catalyzer 90% sulfuric acid gets caproic acid lignocaine ethyl ester product 34.5g, and purity is 93%.
Embodiment 5:
Instrument and operation are with embodiment 1, and solvent is chosen as benzene, get caproic acid lignocaine ethyl ester product 37.2g, and purity is 95%.
Embodiment 6:
Instrument and operation are with embodiment 1, and solvent is chosen as dimethylbenzene, get caproic acid lignocaine ethyl ester product 37.0g, and purity is 95%.
Embodiment 7:
100 liters of enamel reaction stills are furnished with agitator, reflux exchanger, water trap.Drop into n-caproic acid 23.6Kg, diethylaminoethanol 21.1Kg, toluene 30L, strong acid-1 resin 0.5Kg in the still, be heated to backflow, tell moisture at any time.When reaction when no longer including water and form, continue reaction 1h, tell resin, slough solvent, rectification under vacuum, product 38Kg, purity is 94.7%.
Embodiment 8:
Caproic acid lignocaine ethyl ester 10g, citric acid 10g puts into the 100ml beaker, is placed on to be heated with stirring on the electric heater to melt.Move to outside the well heater, continue to stir, the cooling back cured shape white powder.Promptly get caproic acid lignocaine ethyl ester Citrate trianion.
Comparative example:
Instrument and operation do not add catalyzer with embodiment 1, get caproic acid lignocaine ethyl ester product 29.2g, and purity is 90%.
The ester of above-mentioned generation can be made Citrate trianion at any time, and salt extraction process is an ester disalt (weight ratio)=1: 1～1: 1.5.
Embodiment 1～4 and comparative example result gather as following table
| Numbering | Catalyzer | Output (g) | Purity % | Yield % |
| 1 | Strong resin (doing) | 37.5 | 96 | 93 |
| 2 | Strong resin (wetting) | 36.7 | 95 | 90 |
| 3 | The vitriol oil | 34.6 | 95 | 84.9 |
| 4 | 90% sulfuric acid | 34.5 | 93 | 82.9 |
| 5 | Do not have | 29.2 | 90 | 68 |
Claims (3)
1, the method for caproic acid lignocaine ethyl ester is produced in a kind of sulfonic acid ion exchange resin catalysis, and this method comprises the steps:
1., select raw material
Reaction raw materials is n-caproic acid and diethylaminoethanol, and its material molar ratio is 1.1～1.3: 1.0;
2., the esterification reaction formula is:
The catalyzer that above-mentioned reaction is adopted is a crosslinked polystyrene sulfonic acid type Zeo-karb, this resin is through pre-treatment, make it convert Hydrogen to after drop anhydrate wherein a part of natural air drying (not moisture), another part is wet preserves (moisture in the resin), and then tests its catalytic effect respectively; The addition of catalyst system therefor is 0.1～5% (weight ratio) of described diethylaminoethanol (standard substance);
3., reaction raw materials dropped into reaction flask after, stir, be heated to backflow, the moisture that reflux exchanger is produced in the water trap of dress is down told at any time, when regeneration water not (about 4 hours), reaction is promptly accused and is finished, and tells resin, slough solvent, rectifying promptly draws product.
2, according to the described method of claim, it is characterized in that: the solvent of described esterification is selected a kind of of benzene, toluene or dimethylbenzene for use.
3, according to the described method of claim, it is characterized in that: 0.5～2% (weight ratio) of the preferably described diethylaminoethanol of the addition of described catalyzer (standard substance).
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2006100144766A CN100393695C (en) | 2006-06-29 | 2006-06-29 | Method for preparing lignocaine ethyl ester caproic acid by catalyzing cation exchange resin in type of sulfonic acid |
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| CNB2006100144766A CN100393695C (en) | 2006-06-29 | 2006-06-29 | Method for preparing lignocaine ethyl ester caproic acid by catalyzing cation exchange resin in type of sulfonic acid |
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| CN1872835A true CN1872835A (en) | 2006-12-06 |
| CN100393695C CN100393695C (en) | 2008-06-11 |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103420832A (en) * | 2013-09-04 | 2013-12-04 | 天宁香料（江苏）有限公司 | Preparing method of cis-3-Hexenyl caproate |
| CN104607252A (en) * | 2014-12-17 | 2015-05-13 | 烟台大学 | Load type polystyrene sulfonic acid resin catalyst and preparation method thereof |
| CN105013510B (en) * | 2015-06-10 | 2017-09-05 | 仲恺农业工程学院 | Solid catalyst for synthesizing plant growth regulator DA-6 |
| CN114478272A (en) * | 2021-12-29 | 2022-05-13 | 西安近代化学研究所 | N, N-diethylaminoethanol isooctanoate and preparation method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE590370A (en) * | 1959-04-29 | 1900-01-01 |
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2006
- 2006-06-29 CN CNB2006100144766A patent/CN100393695C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103420832A (en) * | 2013-09-04 | 2013-12-04 | 天宁香料（江苏）有限公司 | Preparing method of cis-3-Hexenyl caproate |
| CN104607252A (en) * | 2014-12-17 | 2015-05-13 | 烟台大学 | Load type polystyrene sulfonic acid resin catalyst and preparation method thereof |
| CN104607252B (en) * | 2014-12-17 | 2016-09-14 | 烟台大学 | A kind of support type polystyrene sulfonic acid resin catalyst and preparation method thereof |
| CN105013510B (en) * | 2015-06-10 | 2017-09-05 | 仲恺农业工程学院 | Solid catalyst for synthesizing plant growth regulator DA-6 |
| CN114478272A (en) * | 2021-12-29 | 2022-05-13 | 西安近代化学研究所 | N, N-diethylaminoethanol isooctanoate and preparation method thereof |
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