CN103319342A - Method for synthesizing ethyl oleate - Google Patents
Method for synthesizing ethyl oleate Download PDFInfo
- Publication number
- CN103319342A CN103319342A CN2013102705888A CN201310270588A CN103319342A CN 103319342 A CN103319342 A CN 103319342A CN 2013102705888 A CN2013102705888 A CN 2013102705888A CN 201310270588 A CN201310270588 A CN 201310270588A CN 103319342 A CN103319342 A CN 103319342A
- Authority
- CN
- China
- Prior art keywords
- ethyl oleate
- solid
- sio
- oleic acid
- esterification
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention discloses a method for synthesizing ethyl oleate. The method is characterized by comprising the following steps: carrying out an esterification reaction between oleic acid and ethanol in the presence of an H2SO4/SiO2 immobilized catalyst, filtering the reaction solution, and purifying or distilling the filtrate through column chromatography to obtain colorless or faint yellow clarified liquid ethyl oleate, wherein the molar ratio of oleic acid to ethanol is 1: (1.5-5); and the molar ratio of the catalyst to oleic acid is 1: (10-50). Compared with the prior art, the method has the advantages that the method is simple in process, convenient to operate, low in production cost, high in yield and mild in reaction conditions, the consumption of raw materials is further reduced, the yield can be improved to be over 95 percent, and the production cost is obviously reduced; and moreover, the catalyst can be recycled, the environment is not polluted, and the method is an ethyl oleate synthesizing method which is environment-friendly, economic and high-efficiency and has a good application prospect.
Description
Technical field
The present invention relates to the organic chemical synthesis technical field, specifically a kind of synthetic method of ethyl oleate.
Background technology
Ethyl oleate is the pale yellow oily liquid body, mainly as tensio-active agent, lubricant, permeate agent, solubility promoter, essence, water repellent agent and the agent of resin malleableize, also as spices.As raw material take oleic acid and ethanol for the synthetic most typical method of ethyl oleate, use sulfuric acid to carry out reflux 10h as catalyzer, being neutralized to pH with sodium methylate after the cooling is 8 ~ 9, then washes with water to neutrality, and at last, filtration dry with Calcium Chloride Powder Anhydrous makes.(Xu Kexun. meticulous Organic Chemicals and intermediate handbook. Beijing: Chemical Industry Press 1998,4:1 ~ 350).The method shortcoming is that the reaction times is oversize, and the product postprocessing working procedures is longer simultaneously, and industrial cost is higher.
Another kind of method commonly used is to adopt pickling process to prepare the carried phospho-tungstic acid mesoporous carbon as catalyzer (Tan Xiaoyu, Yang Lina, Liu Jing, Xu Junbo, the carried phospho-tungstic acid mesoporous carbon catalyzes and synthesizes the research of ethyl oleate. charcoal element, 2011,1 (145): 25 ~ 28).The method temperature of reaction is 110 ℃, and the phospho-wolframic acid charge capacity is 30%, reaction times 4h, and, the oleic acid ester rate is 89.34%.Although this method shortened to some extent than traditional preparation method's reaction times, temperature of reaction is higher, and the reaction times is also longer, and the preparation cost of catalyzer is higher and cannot reclaim and reuse.
In sum, the ethyl oleate of prior art preparation, synthesis technique is complicated, and environmental pollution is large, the widespread use that has seriously restricted.Therefore, be necessary to seek a kind of system milder, more economical, green ethyl oleate synthetic method, this is significant for ethyl oleate application aborning.
Summary of the invention
The synthetic method that a kind of ethyl oleate of providing for the deficiencies in the prior art is provided, recover the oil acid and ethanol are at H
2SO
4/ SiO
2Carry out esterification under the solid-carrying type catalyzer, the reaction system of synthetic oil acetoacetic ester is gentle, easy and simple to handle, raw materials consumption reduces, productive rate can be brought up to more than 95%, and production cost obviously reduces, and the catalyzer aftertreatment simply can be recycled, free from environmental pollution, be a kind of environmental protection and economical and efficient and very promising ethyl oleate synthetic method.
The concrete technical scheme that realizes the object of the invention is: a kind of synthetic method of ethyl oleate, be characterized in the method with oleic acid and ethanol at H
2SO
4/ SiO
2Carry out esterification under the solid-carrying type catalyzer, then reacting liquid filtering is removed catalyzer, filtrate is purified that colourless or faint yellow clarified liq is ethyl oleate, and concrete synthesis step is as follows:
The preparation of a, solid acid catalyst
With SiO
2Solid and anhydrous methyl ether and concentration be 98% sulfuric acid by weight volume ratio be after 2g:4ml:1ml mixes, dry 4 ~ 5h under 130 ~ 140 ℃ of temperature, the fine powder that obtains light brown is H
2SO
4/ SiO
2The solid-carrying type catalyzer;
B, esterification
Oleic acid is mixed for 1:1.5 ~ 5 in molar ratio with ethanol, then at the H of above-mentioned preparation
2SO
4/ SiO
2Carry out 1 ~ 5 hour esterification under the solid-carrying type catalyzer, its temperature of reaction is 50 ~ 110 ℃; Described H
2SO
4/ SiO
2The mol ratio of solid-carrying type catalyzer and oleic acid is 1:10 ~ 50;
C, purification
Leach catalyzer in the reaction solution with above-mentioned esterification, filtrate is purified through silica gel column chromatography or underpressure distillation, and obtaining colourless or light yellow transparent oily liquid is ethyl oleate.
It is simple, easy to operate that the present invention compared with prior art has technique, reaction conditions is gentle, productive rate can be brought up to more than 95%, further reducing raw materials consumption reduces, production cost obviously reduces, and catalyzer can be recycled, and is free from environmental pollution, is the synthetic method of a kind of environmental protection and economical and efficient and very promising ethyl oleate.
Description of drawings
Fig. 1 is infrared spectrogram of the present invention.
Embodiment
Below will the present invention is further elaborated by specific embodiment:
The preparation of a, solid acid catalyst
Take by weighing SiO
2It is 98% sulfuric acid that solid 10.0g and 20.0ml anhydrous diethyl ether mix rear slow dropping 5ml concentration, need stir during dropping, after dripping with its ventilation, be positioned in the baking oven dry after allowing methyl ether volatilize, oven temperature is arranged on 135 ℃, and be 4h time of drying, and the fine powder that makes light brown is H
2SO
4/ SiO
2The solid-carrying type catalyzer, stand-by.
B, esterification
H with 1.00ml oleic acid and 0.55ml ethanol and the above-mentioned preparation of 0.013g
2SO
4/ SiO
2The solid-carrying type catalyzer mixes, and under agitation carries out esterification, and its temperature of reaction is 90 ℃, and the reaction times is 2.5 hours.
C, purification
With the reacting liquid filtering of above-mentioned esterification, the catalyzer that leaches can be recycled, and filtrate is purified through silica gel column chromatography, makes the ethyl oleate 0.981g of achromaticity and clarification liquid, and its productive rate is 91.4%, records refractive index n
20 D=1.4532.
Nuclear-magnetism spectrum test data is as follows:
1H-NMR (500MHz, CDCl
3): δ (ppm) 5.34 (m, 2H), 4.12 (q, J=7.2Hz, 2H), 2.28 (t, J=7.5Hz, 2H), 1.62 (m, 2H), 1.24-1.31 (m, 24H), 0.89 (t, J=6.0Hz, 3H).
To above-mentioned products therefrom ethyl oleate after testing, can confirm as pure target product after analyzing.
Embodiment 2
The preparation of a, solid acid catalyst
Take by weighing SiO
2It is 98% sulfuric acid that solid 10.0g and 20.0ml anhydrous diethyl ether mix rear slow dropping 5ml concentration, need stir during dropping, after dripping with its ventilation, be positioned in the baking oven dry after allowing methyl ether volatilize, oven temperature is arranged on 140 ℃, and be 3.5h time of drying, and the fine powder that makes light brown is H
2SO
4/ SiO
2The solid-carrying type catalyzer, stand-by.
B, esterification
H with 50.0ml oleic acid and 20.0ml ethanol and the above-mentioned preparation of 1.9g
2SO
4/ SiO
2The solid-carrying type catalyzer mixes, and under agitation carries out esterification, and its temperature of reaction is 110 ℃, and the reaction times is 1.5 hours.
C, purification
Filter reaction system after esterification finishes, filtrate obtains faint yellow clarified liq ethyl oleate 46.7g through underpressure distillation.(bp:205~208 ℃/7mmHg) the ethyl oleate theoretical yield is 49.0g, and the productive rate that historical facts or anecdotes is tested middle ethyl oleate is 95.3%, records sample refractive index n
20 D=1.4538.
More than just the present invention is further illustrated, is not to limit this patent, all for the present invention's equivalence enforcement, all should be contained within the claim scope of this patent.
Claims (1)
1. the synthetic method of an ethyl oleate, it is characterized in that the method with oleic acid and ethanol at H
2SO
4/ SiO
2Carry out esterification under the solid-carrying type catalyzer, then with reacting liquid filtering, filtrate is through purifying to such an extent that faint yellow clarified liq is ethyl oleate, and concrete synthesis step is as follows:
The preparation of a, solid acid catalyst
With SiO
2Solid and anhydrous diethyl ether and concentration be 98% sulfuric acid by weight volume ratio be after 2g:4ml:1ml mixes, dry 4 ~ 5h under 130 ~ 140 ℃ of temperature, the fine powder that obtains light brown is H
2SO
4/ SiO
2The solid-carrying type catalyzer;
B, esterification
Oleic acid is mixed for 1:1.5 ~ 5 in molar ratio with ethanol, then at the H of above-mentioned preparation
2SO
4/ SiO
2Carry out 1 ~ 5 hour esterification under the solid-carrying type catalyzer, its reaction oil bath temperature is 50 ~ 110 ℃; Described H
2SO
4/ SiO
2The mol ratio of solid-carrying type catalyzer and oleic acid is 1:10 ~ 50;
C, purification
Leach catalyzer in the reaction solution with above-mentioned esterification, filtrate is purified through silica gel column chromatography or underpressure distillation, and obtaining colourless or light yellow transparent oily liquid is ethyl oleate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2013102705888A CN103319342A (en) | 2013-07-01 | 2013-07-01 | Method for synthesizing ethyl oleate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2013102705888A CN103319342A (en) | 2013-07-01 | 2013-07-01 | Method for synthesizing ethyl oleate |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103319342A true CN103319342A (en) | 2013-09-25 |
Family
ID=49188438
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2013102705888A Pending CN103319342A (en) | 2013-07-01 | 2013-07-01 | Method for synthesizing ethyl oleate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103319342A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109942783A (en) * | 2019-02-22 | 2019-06-28 | 上海稻畑精细化工有限公司 | A kind of high stability polyurethane curing agent and its preparation process |
CN110668944A (en) * | 2019-04-19 | 2020-01-10 | 江西阿尔法高科药业有限公司 | Refining method of ethyl oleate |
CN115322090A (en) * | 2022-07-16 | 2022-11-11 | 江西益普生药业有限公司 | Method for preparing ethyl oleate |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101735288A (en) * | 2010-01-18 | 2010-06-16 | 华东师范大学 | Method for complete acetylization of saccharides in presence of solid acid catalyst |
-
2013
- 2013-07-01 CN CN2013102705888A patent/CN103319342A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101735288A (en) * | 2010-01-18 | 2010-06-16 | 华东师范大学 | Method for complete acetylization of saccharides in presence of solid acid catalyst |
Non-Patent Citations (1)
Title |
---|
KENNETH M. DOLL ET AL.: "Surface Tension Studies of Alkyl Esters and Epoxidized Alkyl Esters Relevant to Oleochemically Based Fuel Additives", 《ENERGY & FUELS》 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109942783A (en) * | 2019-02-22 | 2019-06-28 | 上海稻畑精细化工有限公司 | A kind of high stability polyurethane curing agent and its preparation process |
CN110668944A (en) * | 2019-04-19 | 2020-01-10 | 江西阿尔法高科药业有限公司 | Refining method of ethyl oleate |
CN115322090A (en) * | 2022-07-16 | 2022-11-11 | 江西益普生药业有限公司 | Method for preparing ethyl oleate |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103319341A (en) | Method for synthesizing methyl oleate | |
KR101125853B1 (en) | Process for preparing of n-methyl pyrrolidone | |
CN107674044B (en) | Method for synthesizing carbamate by using carbon dioxide, amine and aryl diazo acetate | |
CN103319342A (en) | Method for synthesizing ethyl oleate | |
CN103450018A (en) | Preparation method of ethyl acetoacetate | |
CN102796047A (en) | Method for preparing 1,2-dimethylimidazole | |
CN113264843B (en) | Synthetic method of 3-aminobicyclo [1.1.1] pentane-1-carboxylic ester derivative | |
CN104262081B (en) | A kind ofly full chloro-1,3-butadiene gas phase is utilized to prepare the method for perchloro-ethane | |
CN103497157B (en) | 2-imidazolidone synthesis method | |
CN103724203A (en) | Preparation method of o-methyl hydroxyphenylacetate | |
CN103214328A (en) | Synthesis method for alpha-bromo-aromatic ketone compounds | |
CN103193660B (en) | Synthetic method of 4-alkoxy phenylamine compound | |
CN86107090A (en) | The preparation method of Clausenamide | |
CN108250056B (en) | Catalytic synthesis method of benzaldehyde | |
CN103755631B (en) | The direct aromatize technique of pyridine derivate | |
CN101602681A (en) | The preparation method of β-enamine ketone, ester derivative | |
CN109422631B (en) | Synthetic method of indanone compound | |
CN105541611A (en) | Method for preparing aceto acetoxy ethyl methacrylate | |
CN101486696B (en) | Preparation of 2,5-dimethyl furan-3,4-dicarboxylic acid | |
CN107141212B (en) | Preparation method of 2-chloro-4' -fluoroacetophenone | |
CN102731293A (en) | Method for synthesizing oleoyl chloride by triphosgene | |
CN101486694A (en) | Preparation method of 2,5-dimethyl furan-3,4-dicarboxylate | |
CN102586798B (en) | Method for synthesizing 2-(N-benzyl)methyl acetamido methylpropionate | |
CN104557604B (en) | Synthetic method for 5-acetylsalicylamide | |
CN103524337A (en) | Preparation method of butyl levulinate by use of biomass based furfuryl alcohol |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20130925 |