CN105130814B - A kind of method that pyrovinic acid catalysis prepares diethyl sebacate - Google Patents

A kind of method that pyrovinic acid catalysis prepares diethyl sebacate Download PDF

Info

Publication number
CN105130814B
CN105130814B CN201510462151.3A CN201510462151A CN105130814B CN 105130814 B CN105130814 B CN 105130814B CN 201510462151 A CN201510462151 A CN 201510462151A CN 105130814 B CN105130814 B CN 105130814B
Authority
CN
China
Prior art keywords
acid
diethyl sebacate
pyrovinic
ethyl alcohol
absolute ethyl
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.)
Active
Application number
CN201510462151.3A
Other languages
Chinese (zh)
Other versions
CN105130814A (en
Inventor
李敢
王德堂
刘颖
田华
夏先伟
王金兴
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xuzhou Currency Magnetoelectricity Co., Ltd.
Original Assignee
Xuzhou College of Industrial Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Xuzhou College of Industrial Technology filed Critical Xuzhou College of Industrial Technology
Priority to CN201510462151.3A priority Critical patent/CN105130814B/en
Publication of CN105130814A publication Critical patent/CN105130814A/en
Application granted granted Critical
Publication of CN105130814B publication Critical patent/CN105130814B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/08Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds

Abstract

The invention discloses the method that a kind of method that pyrovinic acid catalysis prepares diethyl sebacate, category catalyze and synthesize diethyl sebacate.Be raw material with decanedioic acid and absolute ethyl alcohol, catalyst made with pyrovinic acid, hexamethylene makees water entrainer, after reaction terminates, product is neutralized, washing, distillation, purifying, obtain diethyl sebacate.Using hexamethylene as water entrainer, reaction time is short, pyrovinic acid is degradable, product needs not move through vacuum distillation and can obtain the good product of outward appearance, and soda acid consumption is few, the advantages of pollution-free, reaction 1h product yields are more than 94%, low production cost, is a kind of method of efficient, environment-friendly synthesis of sebacic acid diethylester, can realize large-scale industrial production.

Description

A kind of method that pyrovinic acid catalysis prepares diethyl sebacate
Technical field
The present invention relates to the preparation method of diethyl sebacate, particularly a kind of pyrovinic acid catalysis prepares decanedioic acid diethyl The method of ester.
Background technology
Diethyl sebacate also known as sebum acetoacetic ester, sebum diethyl phthalate is colourless to flaxen liquid, there is grape Wine, fruit, the fragrance of muskmelon, can be miscible with the organic matter such as ethanol, ether, oils, is mainly used in preparing the edible perfume (or spice) such as grape, pears Essence and daily chemical essence, can also be commonly used in the middle of plasticizer or organic synthesis as organic solvent, in light, electrochemical sensor Body.Increasingly perfect with people's environmental consciousness and environmental regulation, Development and Production diethyl sebacate has fabulous development Prospect.
Diethyl sebacate is typically with decanedioic acid and absolute ethyl alcohol as raw material, in the presence of catalyst, certain Synthesize under process conditions.Domestic useful p-methyl benzenesulfonic acid, ion exchange resin, solid acid, niter cake, chlorination at present The catalysis such as iron, heteropoly acid prepare the report of diethyl sebacate, but it is long to there is the reaction time in various degree, and ethanol consumption is big and one Secondary addition, temperature is raised too soon, and ethanol has neither part nor lot in reaction and just taken out of with by solvent, and catalyst preparation is complicated, high cost, and product is needed Want vacuum distillation, consume mass energy, dangerous, industrializing implementation difficulty is big, the shortcomings of the three wastes are not effectively addressed.
The content of the invention
It is existing to overcome it is an object of the invention to provide a kind of method that pyrovinic acid catalysis prepares diethyl sebacate The deficiency of preparation method, takes following several ways and obtains good effect:Absolute ethyl alcohol is added at twice, shortens esterification Reaction time;The pyrovinic acid separated after reaction has two kinds of purposes:First, can be to reclaim for esterification next time, In the industrial production, it is capable of achieving to recycle;2nd, it is to extract the decanedioic acid for not participating in reaction completely for neutralizing alkali lye, obtains Wet decanedioic acid;The complexity of operation is reduced, energy resource consumption is reduced, environmental pollution is reduced significantly, and reduction is produced into This;By the way of activated carbon purification, reduce because of vacuum distillation(Need high temperature, high pressure)Caused by high energy consumption, yield is low, The presence of unsafe factor, easy to operate, activated carbon can be reused, and energy consumption is low, low cost;Pyrovinic acid is a kind of catalysis The active strong, homogeneous catalyst of small toxicity high, acid, it is small to equipment corrosion, biodegradable, environmentally friendly, uses Amount is small, reusable multiple, low production cost.
Technical scheme is as follows:It is raw material with decanedioic acid and absolute ethyl alcohol, catalyst, hexamethylene is made with pyrovinic acid Alkane does water entrainer, and after reaction terminates, product is neutralized, washing, distillation, and purifying obtains diethyl sebacate.
Catalyst is made with pyrovinic acid, the present invention is comprised the following steps:
1)Hexamethylene, nothing are added in the three neck round bottom flask of electric blender, thermometer, condenser pipe, water knockout drum is had Water-ethanol I and pyrovinic acid, stirring is lower to add decanedioic acid, rotating speed to control in 450~500r/min.
2)Esterification:It is heated to reflux to temperature to 84 DEG C, is cooled to 50 DEG C, add absolute ethyl alcohol II, continuation is heated back 84 DEG C are flow to, the water for producing reaction is separated from water knockout drum, treats that three neck round bottom flask is cooled to 50 DEG C, carries out next step;At this In step, the method for employing secondary addition absolute ethyl alcohol, the purpose of do so is conducive to improving the conversion ratio of decanedioic acid, increases Plus the yield of purpose product diethyl sebacate.
3)Stand, point sub-cloud pyrovinic acid obtains feed liquid I.
4)To the sodium hydrate aqueous solution that mass percent is 3~5% is added in feed liquid I, stir and neutralize and be unreacted Decanedioic acid, removes buck layer, obtains feed liquid II;Buck layer step 3)In pyrovinic acid be neutralized to pH=3~4, be filtrated to get Decanedioic acid;Without drying, can directly bottle, the esterification experiment of diethyl sebacate is prepared for laboratory next time;In industry In production, the unreacted decanedioic acid that can also obtain the step is added directly into reactor, realizes the circulation of production technology, drop Low cost of material.
5)Feed liquid II is washed with water to neutrality, and is separated;Separation method is different with the density of water phase according to organic phase, Separated using separatory funnel.
6)By step 5)The organic phase isolated is put into one and new has electric blender, thermometer, three mouthfuls of condenser pipe In round-bottomed flask, air-distillation is carried out below 140 DEG C and removes hexamethylene and water, obtain liquid diethyl sebacate.
7)By step 6)The liquid diethyl sebacate for obtaining is cooled to 90 DEG C, adds activated carbon, stirring, at 80~90 DEG C Insulation 10min, heat filter, obtains diethyl sebacate.
Described absolute ethyl alcohol I and the weight ratio of absolute ethyl alcohol II are 4:1.
Described decanedioic acid and absolute ethyl alcohol mol ratio are 1:6.
The consumption of described catalyst pyrovinic acid is the 3~7% of decanedioic acid weight.
The consumption of hexamethylene is 0.7~1.2 times of decanedioic acid weight.
The consumption of described activated carbon is the 0.5~1% of decanedioic acid weight.
Described decanedioic acid, absolute ethyl alcohol, pyrovinic acid, hexamethylene are 99.5% analysis net product;Activated carbon is medicinal.
The equation of the reaction is as follows:
The beneficial effects of the invention are as follows:
Take following several ways:First, absolute ethyl alcohol is added at twice, shortens reaction time of esterification;2nd, divide after reacting Separating out the pyrovinic acid for coming has two kinds of purposes:1st, can be to reclaim for esterification next time, in the industrial production, be capable of achieving Recycle;2nd, it is to extract the decanedioic acid for not participating in reaction completely for neutralizing alkali lye, obtains wet decanedioic acid;Reduce operation Complexity, reduce energy resource consumption, environmental pollution is reduced significantly, reduce production cost;The side purified using activated carbon Formula, reduces because of vacuum distillation(Need high temperature, high pressure)Caused by high energy consumption, yield is low, the presence of unsafe factor, operation Simplicity, energy consumption is low, low cost;Pyrovinic acid is that a kind of catalysis activity is high, the acid strong, homogeneous catalyst of small toxicity, and its pair sets Standby corrosivity is small, and biodegradable, usage amount is small, reusable multiple, reduces production cost.Using hexamethylene as band water Agent, reaction condition is gentle, and the reaction time is short, and convenient post-treatment, the advantages of unreacted decanedioic acid is recycled recycling, produces Product yield can realize large-scale industrial production more than 94%.
Brief description of the drawings
Fig. 1 is present invention process flow chart.
Specific embodiment
With reference to case study on implementation the scheme and effect that the present invention is furture elucidated.
Embodiment 1
The decanedioic acid of selection, absolute ethyl alcohol, pyrovinic acid, hexamethylene are 99.5% analysis net product;Activated carbon is medicinal;
Added in the three neck round bottom flask of electric blender, thermometer, condenser pipe, water knockout drum is had hexamethylene 50mL, The 44.22g of absolute ethyl alcohol I and pyrovinic acid 2g, stirring is lower to add decanedioic acid 40.45g, rotating speed to control in 450r/min, heat back Stream, the water for producing reaction is separated from water knockout drum, and heating is stopped to 84 DEG C, is cooled to 50 DEG C, and the 11.06g of absolute ethyl alcohol II continues It is heated to reflux stopping heating to 84 DEG C, always flow back 1h, is cooled to 50 DEG C, stands a point demethyl sulfonic acid, obtains feed liquid I, feed liquid I adds Enter the sodium hydrate aqueous solution stirring that mass fraction is 5% and neutralize unreacted decanedioic acid, remove buck layer, obtain feed liquid II; The pyrovinic acid that the experiment of buck layer is separated is neutralized to pH=3.0, is filtrated to get decanedioic acid;During feed liquid II is washed with water to Property, the organic phase isolated first carries out air-distillation, is cooled to 90 DEG C or so, addition activated carbon 0.25g, stirring, on 87 DEG C of left sides Right insulation 10min, heat filter, obtains diethyl sebacate, is computed obtaining:Yield is 94.64%.
Embodiment 2
The decanedioic acid of selection, absolute ethyl alcohol, pyrovinic acid, hexamethylene are 99.5% analysis net product;Activated carbon is medicinal;
Hexamethylene 50mL, absolute ethyl alcohol I are added in the flask of electric blender, thermometer, condenser pipe, water knockout drum is had 44.22g and fresh pyrovinic acid 0.3g and recovery pyrovinic acid 1.7g, stirring is lower to add decanedioic acid 40.45g, rotating speed control In 450r/min, it is heated to reflux, the water for producing reaction is separated from water knockout drum, heating is stopped to 84 DEG C, is cooled to 50 DEG C, it is anhydrous The 11.06g of ethanol II, continues to be heated to reflux to 84 DEG C to stop heating, and always flow back 1h, is cooled to 50 DEG C, stands a point demethyl sulfonic acid, Feed liquid I is obtained, feed liquid I adds the sodium hydrate aqueous solution stirring that mass fraction is 5% to neutralize unreacted decanedioic acid, except lixiviating Water layer, obtains feed liquid II;The pyrovinic acid that the experiment of buck layer is separated is neutralized to pH=3.5, is filtrated to get decanedioic acid;Material Liquid II is washed with water to neutrality, and the organic phase isolated first carries out air-distillation, is cooled to 90 DEG C, adds activated carbon 0.25g, stirs Mix, 10min is incubated at 85 DEG C or so, heat filter obtains diethyl sebacate, is computed obtaining:Yield is 94.55%.
Embodiment 3
The decanedioic acid of selection, absolute ethyl alcohol, pyrovinic acid, hexamethylene are 99.5% analysis net product;Activated carbon is medicinal;
Hexamethylene 50mL, absolute ethyl alcohol are added in the flask of electric blender, thermometer, condenser pipe, water knockout drum is had 44.22g and pyrovinic acid 2g, stirring is lower to add decanedioic acid 39g, reclaims decanedioic acid 3.0g(Weight in wet base), rotating speed control is in 450r/ Min, is heated to reflux, and the water for producing reaction is separated from water knockout drum, and heating is stopped to 84 DEG C, is cooled to 50 DEG C, absolute ethyl alcohol 11.06g, continues to be heated to reflux to 84 DEG C to stop heating, and always flow back 1h, is cooled to 50 DEG C, stands a point demethyl sulfonic acid, is expected Liquid I, feed liquid I adds the sodium hydrate aqueous solution stirring that mass fraction is 5% to neutralize unreacted decanedioic acid, removes buck layer, Obtain feed liquid II;The pyrovinic acid that the experiment of buck layer is separated is neutralized to pH=4.0, is filtrated to get decanedioic acid;Feed liquid II is used Water washing to neutrality, the organic phase isolated first carries out air-distillation, is cooled to 90 DEG C, adds activated carbon 0.25g, stirs, 85 DEG C or so insulation 10min, heat filter obtains diethyl sebacate, is computed obtaining:Yield 94.48%.
Embodiment 4
The decanedioic acid of selection, absolute ethyl alcohol, pyrovinic acid, hexamethylene are 99.5% analysis net product;Activated carbon is medicinal;
Added in the flask of electric blender, thermometer, condenser pipe, water knockout drum is had and reclaim hexamethylene 50mL, anhydrous Ethanol 44.22g and pyrovinic acid 2g, stirring is lower to add decanedioic acid 39g, reclaims decanedioic acid 3.0g(Weight in wet base), rotating speed control exist 450r/min, is heated to reflux, and the water for producing reaction is separated from water knockout drum, and heating is stopped to 84 DEG C, is cooled to 50 DEG C, anhydrous second Alcohol 11.06g, continues to be heated to reflux to 84 DEG C to stop heating, and always flow back 1h, is cooled to 50 DEG C, stands a point demethyl sulfonic acid, expects To feed liquid I, the addition mass fraction of feed liquid I is the 5% sodium hydrate aqueous solution stirring unreacted decanedioic acid of neutralization, removes buck Layer, obtains feed liquid II;The pyrovinic acid that the experiment of buck layer is separated is neutralized to pH=3.7, is filtrated to get decanedioic acid;Feed liquid II is washed with water to neutrality, and the organic phase isolated first carries out air-distillation, is cooled to 90 DEG C, adds activated carbon 0.25g, stirs Mix, 10min is incubated at 83 DEG C or so, heat filter obtains diethyl sebacate, is computed obtaining:Yield is 94.52%.

Claims (1)

1. a kind of method that pyrovinic acid catalysis prepares diethyl sebacate, it is characterised in that:Catalyst is made with pyrovinic acid, is pressed It is prepared by following steps:
1)Hexamethylene, anhydrous second are added in the three neck round bottom flask of electric blender, thermometer, condenser pipe, water knockout drum is had Alcohol I and pyrovinic acid, stirring is lower to add decanedioic acid, rotating speed to control in 450~500r/min;
2)Esterification:Be heated to reflux to temperature to 84 DEG C, be cooled to 50 DEG C, add absolute ethyl alcohol II, continue to be heated to reflux to 84 DEG C, the water for producing reaction is separated from water knockout drum, treats that three neck round bottom flask is cooled to 50 DEG C, carries out next step;
3)Stand, point sub-cloud pyrovinic acid obtains feed liquid I;
4)To the sodium hydrate aqueous solution that mass percent is 3~5% is added in feed liquid I, the unreacted last of the ten Heavenly stems two is stirred and neutralized Acid, removes buck layer, obtains feed liquid II;Buck layer step 3)In pyrovinic acid be neutralized to pH=3~4, be filtrated to get the last of the ten Heavenly stems two Acid;
5)Feed liquid II is washed with water to neutrality, and is separated;
6)By step 5)The organic phase isolated be put into it is another have an electric blender, thermometer, three mouthfuls of round bottoms of condenser pipe burn In bottle, air-distillation is carried out below 140 DEG C and removes hexamethylene and water, obtain liquid diethyl sebacate;
7)By step 6)The liquid diethyl sebacate for obtaining is cooled to 90 DEG C, adds activated carbon, stirring, in 80~90 DEG C of insulations 10min, heat filter, obtains filtrate, i.e.,:Diethyl sebacate;
Described absolute ethyl alcohol I and the weight ratio of absolute ethyl alcohol II are 4:1;
Described decanedioic acid and absolute ethyl alcohol mol ratio are 1:6;
The consumption of described catalyst pyrovinic acid is the 3~7% of decanedioic acid weight;
The consumption of hexamethylene is 0.7~1.2 times of decanedioic acid weight;
The consumption of described activated carbon is the 0.5~1% of decanedioic acid weight;
Described decanedioic acid, absolute ethyl alcohol, pyrovinic acid, hexamethylene are 99.5% analysis net product;Activated carbon is medicinal.
CN201510462151.3A 2015-07-31 2015-07-31 A kind of method that pyrovinic acid catalysis prepares diethyl sebacate Active CN105130814B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510462151.3A CN105130814B (en) 2015-07-31 2015-07-31 A kind of method that pyrovinic acid catalysis prepares diethyl sebacate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510462151.3A CN105130814B (en) 2015-07-31 2015-07-31 A kind of method that pyrovinic acid catalysis prepares diethyl sebacate

Publications (2)

Publication Number Publication Date
CN105130814A CN105130814A (en) 2015-12-09
CN105130814B true CN105130814B (en) 2017-05-31

Family

ID=54716451

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510462151.3A Active CN105130814B (en) 2015-07-31 2015-07-31 A kind of method that pyrovinic acid catalysis prepares diethyl sebacate

Country Status (1)

Country Link
CN (1) CN105130814B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107827745B (en) * 2017-11-17 2020-11-03 徐州工业职业技术学院 Low-temperature homogeneous green method for synthesizing prolifene
CN110632231B (en) * 2019-10-12 2022-04-15 首都医科大学附属北京天坛医院 Metabolic marker of glioblastoma in urine and use thereof in early diagnosis

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103254073B (en) * 2013-05-14 2015-04-15 常州大学 Preparation method of high-purity (bi)pentaerythritol crylic acid non-complete esterification product
CN104592015A (en) * 2013-10-31 2015-05-06 青岛旺裕橡胶制品有限公司 Preparation method of rubber plasticizer dioctyl sebacate
CN103664597A (en) * 2013-11-27 2014-03-26 浙江海利业科技有限公司 Novel synthesis technology of adipic acid (2-propyl heptyl) ester

Also Published As

Publication number Publication date
CN105130814A (en) 2015-12-09

Similar Documents

Publication Publication Date Title
CN103613501B (en) Method with macropore strong acid cation exchanger resin for catalyst preparing tributyl citrate
CN105562041A (en) Preparation method of solid alkali catalyst and reaction method for catalytic synthesis of ionone fragrance intermediate by solid alkali catalyst
CN104151164A (en) Method for preparing methyl chloroacetate
CN105130814B (en) A kind of method that pyrovinic acid catalysis prepares diethyl sebacate
CN104844493A (en) Dicumyl peroxide (DCP) and propylene oxied (CHPPO) coproduction method
CN104119230A (en) Synthesis method and application of long-chain methyl p-hydroxybenzoate
CN104311413A (en) Method for synthesis of ferulic acid ester by solid acid catalysis
CN102614919B (en) Sulfonated cross-linked chitosan resin type solid acid catalyst and preparation method thereof
CN102531899B (en) Method for catalytic synthesis of tributyl citrate by utilizing immobilized p-toluenesulfonic acid
CN103848739A (en) Production method of high-purity dimethyl fumarate
CN102872911B (en) Fatty acid preparation method
CN104624242B (en) A kind of biodiesel synthesis acidic ion liquid immobilized AlCl_3 catalyst and preparation method thereof
CN103319312A (en) Joint production process of antioxidant 264 and 6-tertiary butyl m-cresol
CN102627528A (en) Method for synthesis of terpineol by supersonic wave assistance
CN102351695A (en) High-selectivity synthesis method of ethyl alpha-bromoacetate
CN103833541A (en) Novel synthesis method of 2-methyl-1,4-naphthoquinone
CN101412739B (en) Production process of beta-glucose pentaacetate
CN105749967A (en) Method for preparing tributyl citrate in presence of bamboo-charcoal-based solid sulfonic acid catalyst
CN106478402A (en) The method that ethanol acid crystal is prepared by methyl glycollate
CN103965041A (en) Method for preparing 2-(4-benzyloxy phenyl)ethanol fatty acid ester
CN103030557B (en) Method for generating phenylacetate by acetophenone in one step
CN105566115B (en) A kind of synthetic method of 3,4,5-tri-methoxybenzoates
CN105732375B (en) A kind of method that gallic acid synthesizes 3,4,5-tri-methoxybenzoate
CN103467420A (en) Preparation method for 3-O-alkyl ascorbic acid
CN109627168A (en) A kind of preparation method of tributyl citrate

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CB03 Change of inventor or designer information
CB03 Change of inventor or designer information

Inventor after: Li Gan

Inventor after: Gao Kun

Inventor after: Wang Detang

Inventor after: Liu Ying

Inventor after: Tian Hua

Inventor after: Xia Xianwei

Inventor after: Wang Jinxing

Inventor before: Li Gan

Inventor before: Wang Detang

Inventor before: Liu Ying

Inventor before: Tian Hua

Inventor before: Xia Xianwei

Inventor before: Wang Jinxing

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20171114

Address after: 221000 Qingshan Industrial Park, Qingshan Town, Jiawang District, Xuzhou, Jiangsu

Patentee after: Xuzhou Currency Magnetoelectricity Co., Ltd.

Address before: 221000 Jiangsu Province, Gulou District of Xuzhou City Xiang Wang Road No. 1

Patentee before: Xuzhou Institute of Industry Technology