CN106831654B - A method of cleaning synthesizing epoxy soybean oil - Google Patents
A method of cleaning synthesizing epoxy soybean oil Download PDFInfo
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- CN106831654B CN106831654B CN201710083443.5A CN201710083443A CN106831654B CN 106831654 B CN106831654 B CN 106831654B CN 201710083443 A CN201710083443 A CN 201710083443A CN 106831654 B CN106831654 B CN 106831654B
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- soybean oil
- composite mixed
- cleaning
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- synthesizing epoxy
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/02—Synthesis of the oxirane ring
- C07D301/03—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds
- C07D301/12—Synthesis of the oxirane ring by oxidation of unsaturated compounds, or of mixtures of unsaturated and saturated compounds with hydrogen peroxide or inorganic peroxides or peracids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/0234—Nitrogen-, phosphorus-, arsenic- or antimony-containing compounds
- B01J31/0235—Nitrogen containing compounds
- B01J31/0239—Quaternary ammonium compounds
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/26—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24
- B01J31/38—Catalysts comprising hydrides, coordination complexes or organic compounds containing in addition, inorganic metal compounds not provided for in groups B01J31/02 - B01J31/24 of titanium, zirconium or hafnium
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/38—Compounds containing oxirane rings with hydrocarbon radicals, substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals
- C07D303/40—Compounds containing oxirane rings with hydrocarbon radicals, substituted by carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals by ester radicals
- C07D303/42—Acyclic compounds having a chain of seven or more carbon atoms, e.g. epoxidised fats
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
- B01J2231/70—Oxidation reactions, e.g. epoxidation, (di)hydroxylation, dehydrogenation and analogues
- B01J2231/72—Epoxidation
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- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
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Abstract
The present invention relates to a kind of methods for cleaning synthesizing epoxy soybean oil, and using composite mixed phosphotungstate as catalyst, hydrogen peroxide is oxidant, and under the conditions of no carboxylic acid, soybean oil epoxidation is prepared epoxidized soybean oil, the structural formula of the composite mixed phosphotungstate are as follows:, wherein R=- C16H33Or-C18H37, x=0.6~2.0.The advantage of the invention is that related composite mixed phosphotungstate has excellent catalytic properties the epoxidation reaction of soybean oil, epoxidation reaction carries out under the conditions of no carboxylic acid, reaction process cleaning, efficient, the epoxide number height of product.
Description
Technical field
The present invention relates to a kind of method of synthesizing epoxy soybean oil, in particular to a kind of side for cleaning synthesizing epoxy soybean oil
Method.
Background technique
Epoxidized soybean oil is a kind of non-toxic, environmental friendly plastic additive, has very excellent plasticising and heat stabilization, extensively
It is general to be applied to the fields such as plastics, coating and rubber.Epoxidized soybean oil is with nontoxic, compatibility is good, biodegradable and mobility
The features such as low, can be used for medical treatment, food packaging, daily necessities and toy for children etc. to the higher field of security requirement.
Currently, it is carboxylic acid catalysis epoxidation method that the method for industrially prepared epoxidized soybean oil, which is mainly,.This method is with peroxidating
Hydrogen is that oxygen source, formic acid or acetic acid are active oxygen carrier, and sulfuric acid or solid acid are catalyst, and it is big that soybean oil epoxidation is prepared epoxy
Soya-bean oil.This method needs to add a large amount of formic acid or acetic acid in the reaction system, and after epoxidation reaction, product need to use a large amount of water
Acid is removed, a large amount of acidic industrial effluent is generated, causes serious environmental pollution.In addition, under acidic environment, epoxy soybean
Open loop side reaction easily occurs for the epoxy group of oil, it is difficult to obtain the epoxidized soybean oil of epoxide number higher (< 6.5%).Therefore, it realizes
The cleaning synthesis of epoxidized soybean oil, to solve the problems, such as discharge of wastewater, causes the extensive concern of researcher under the conditions of no carboxylic acid.Li Kun
For orchids etc. using phospho heteropoly tungstate as phase transfer catalyst, 1,2- dichloroethanes is solvent, and epoxy is prepared in neutral conditions
The epoxidized soybean oil (Li Kunlan etc., applied chemistry, 2007,10,1177-1181) of value about 6%.Shi Saiquan etc. is with peroxide phosphorus tungsten
Heteropoly acid quaternary ammonium salt is catalyst, and the epoxidized soybean oil that epoxide number is 6.28% is obtained under the conditions of no carboxylic acid
(CN101235021；Shi Saiquan, Master's thesis, Southern Yangtze University, 2008).Zhu is superfine using phosphotungstic acid quaternary as catalyst, in nothing
Epoxidized soybean oil is catalyzed and synthesized under the conditions of carboxylic acid, the epoxide number of product is that Zhu 6%(is superfine, bonding, 2016,8,39-42).
Realize that the key technology without carboxylic acid Clean Synthesis of Epoxidized Soybean Oil is the exploitation of effective catalyst, it is existing
Technical solution mainly uses single type quaternary ammonium cation doping phosphorus heteropoly tungstic acid as catalyst, it is difficult to which obtaining epoxide number is more than
6.5% high-quality epoxidized soybean oil, and it is lower to be catalyzed reaction efficiency.Therefore, there is the epoxidation of excellent catalytic performance to urge for exploitation
Agent is still those skilled in the art's technology in the urgent need to address to realize the cleaning of epoxidized soybean oil, efficiently synthesize
Problem.
Summary of the invention
The purpose of the present invention is to provide a kind of efficient, cleaning synthesizing epoxy soybean oil methods.
The present invention provides a kind of methods for cleaning synthesizing epoxy soybean oil: using composite mixed phosphotungstate as catalyst,
Hydrogen peroxide is oxidant, and under the conditions of no carboxylic acid, soybean oil epoxidation is prepared epoxidized soybean oil, the composite mixed phosphorus tungsten
The structural formula of hydrochlorate are as follows:
Wherein, R=- C16H33Or-C18H37, x=0.6 ~ 2.0.
Further, the preparation method of the composite mixed phosphotungstate: the cetyl three of 0.6~2.0 mmol is weighed
Ammonio methacrylate or the phosphotungstic acid of octadecyltrimethylammonium chloride, the titanium sulfate of 0.25~0.6 mmol and 1 mmol difference are molten
Solution is in 20 ml deionized waters；After being completely dissolved, under conditions of room temperature and lasting stirring, first by cetyl trimethyl chlorine
Change ammonium or octadecyltrimethylammonium chloride solution to be slowly added dropwise into Salkowski's solution, is further continued for titanium sulfate is slowly added dropwise molten
Liquid increasingly generates white precipitate；After dripping, continue to stir 0.5 h, then still aging 1 h.White precipitate is separated by filtration
Afterwards, dry, the composite mixed phosphotungstate of quaternary ammonium, titanium can be obtained.
Further, the mass ratio of the composite mixed phosphotungstate and soybean oil is 1~10:100.
Further, the concentration of the hydrogen peroxide is 20~40%, and the mass ratio of hydrogen peroxide and soybean oil is 1~2:
1。
Further, the reaction temperature is 40~90 DEG C.
Further, the reaction time is 1.5~9 hours.
Technical solution according to the present invention has the advantage that the composite mixed phosphotungstate of the quaternary ammonium of fabricated in situ, titanium
Have both the phase-transfer catalysis in phosphotungstic acid quaternary activated centre, it may have the high catalytic activity in phosphotungstic acid titanium activated centre,
And two kinds of activated centres show good synergistic effect, have composite mixed phosphotungstate to the epoxidation reaction of soybean oil
Excellent catalytic performance；Reaction carries out under the conditions of no carboxylic acid, synthesis process cleaning, efficient, the epoxide number height of product.
Specific embodiment
Specific embodiments of the present invention will be described in further detail below.For those of skill in the art
For member, from detailed description of the invention, above and other objects, features and advantages of the invention be will be evident.
Embodiment 1:
The preparation of catalyst: 1.2 mmol hexadecyltrimethylammonium chlorides, 0.45 mmol titanium sulfate and 1 are weighed
Mmol phosphotungstic acid is dissolved in respectively in 20 ml deionized waters；After being completely dissolved, under conditions of room temperature and lasting stirring, first will
Hexadecyltrimethylammonium chloride solution is slowly added dropwise into Salkowski's solution, is further continued for that titanium sulfate solution is slowly added dropwise, gradually
Generate white precipitate；After dripping, continue to stir 0.5 h, then still aging 1 h.After white precipitate is separated by filtration, do
Dry, it is [(C that molecular formula, which can be obtained,16H33)N(CH3)3]1.2Ti0.45PW12O40Composite mixed phosphotungstate.
Embodiment 2:
The preparation of catalyst: the additional amount of hexadecyltrimethylammonium chloride is only changed to by preparation process with embodiment 1
0.6 mmol, the additional amount of titanium sulfate are changed to 0.6 mmol, and it is [(C that molecular formula, which can be obtained,16H33)N(CH3)3]0.6Ti0.6PW12O40
Composite mixed phosphotungstate.
Embodiment 3:
The preparation of catalyst: hexadecyltrimethylammonium chloride is only changed to 2 mmol, sulphur with embodiment 1 by preparation process
The additional amount of sour titanium is changed to 0.25 mmol, and it is [(C that molecular formula, which can be obtained,16H33)N(CH3)3]2Ti0.25PW12O40It is composite mixed
Phosphotungstate.
Embodiment 4:
The preparation of catalyst: hexadecyltrimethylammonium chloride is only changed to octadecyl three with embodiment 1 by preparation process
Ammonio methacrylate, it is [(C that molecular formula, which can be obtained,18H37)N(CH3)3]1.2Ti0.45PW12O40Composite mixed phosphotungstate.
Embodiment 5:
[(the C prepared in 10 g soybean oils and 0.3 g embodiment 1 is added in the reactor16H33)N(CH3)3]1.2Ti0.45PW12O40Catalyst opens stirring, is warming up to 60 DEG C, and the hydrogen peroxide that 10 g concentration are 30% is slowly added to dropwise
In reaction system, react 3 hours.After reaction, by reaction system stratification, gained oil is mutually removed water through vacuum distillation to obtain the final product
Epoxidized soybean oil.The epoxide number of product is detected by GB/T 1677-2008, epoxide number 6.71%.
Embodiment 6:
Using reaction condition and detection method same as Example 5, only catalyst is changed to prepare in embodiment 2
[(C16H33)N(CH3)3]0.6Ti0.6PW12O40, the epoxide number of product is 6.62%.
Embodiment 7:
Using reaction condition and detection method same as Example 5, only catalyst is changed to prepare in embodiment 3
[(C16H33)N(CH3)3]2Ti0.25PW12O40, the epoxide number of product is 6.53%.
Embodiment 8:
Using reaction condition and detection method same as Example 5, only catalyst is changed to prepare in embodiment 4
[(C18H37)N(CH3)3]1.2Ti0.45PW12O40, the epoxide number of product is 6.65%.
Embodiment 9:
Using reaction condition and detection method same as Example 5, the dosage of catalyst is only changed to 0.1g, when reaction
Between be changed to 9 hours, the epoxide number of product is 6.51%.
Embodiment 10:
Using reaction condition and detection method same as Example 5, the dosage of catalyst is only changed to 1 g, when reaction
Between be changed to 1.5 hours, the epoxide number of product is 6.56%.
Embodiment 11:
Using reaction condition and detection method same as Example 5, it is 20% that hydrogen peroxide, which is only changed to 15 g concentration,
Reaction temperature is changed to 90 DEG C, and the epoxide number of product is 6.73%.
Embodiment 12:
Using reaction condition and detection method same as Example 5, it is 40% that hydrogen peroxide, which is only changed to 10 g concentration,
Reaction temperature is changed to 40 DEG C, and the epoxide number of product is 6.67%.
Comparative example 1:
Using reaction condition and detection method same as Example 5, catalyst is only changed to [(C16H33)N(CH3)3]3PW12O40, the epoxide number of product is 5.56%.
Comparative example 2:
Using reaction condition and detection method same as Example 5, catalyst is only changed to Ti0.75PW12O40, product
Epoxide number is 4.75%.
According to embodiment 5-12, comparative example 1 and comparative example 2 as a result, quaternary ammonium of the present invention, the composite mixed phosphorus tungsten of titanium
Hydrochlorate has very excellent catalytic performance to the reaction of no carboxylic acid Clean Synthesis of Epoxidized Soybean Oil, and catalytic performance is excellent
Phosphotungstate is adulterated in traditional single type quaternary ammonium cation or titanium ion.It is with composite mixed phosphotungstate provided by the invention
Catalyst is, it can be achieved that the cleaning of high-quality epoxidized soybean oil (epoxide number >=6.5%), efficiently synthesize.
It should be appreciated that although the present invention has carried out clear explanation by above embodiments, without departing substantially from the present invention
Spirit and its essence in the case where, person of ordinary skill in the field make in accordance with the present invention it is various it is corresponding variation and
Amendment, but these corresponding variations and modifications all should belong to scope of protection of the claims of the invention.
Claims (5)
1. a kind of method for cleaning synthesizing epoxy soybean oil, which is characterized in that using composite mixed phosphotungstate as catalyst, peroxide
Change hydrogen is that soybean oil epoxidation is prepared epoxidized soybean oil, the composite mixed phosphotungstate under the conditions of no carboxylic acid by oxidant
Structural formula are as follows:
Wherein, R=- C16H33Or-C18H37, x=0.6~2.0.
2. the method for synthesizing epoxy soybean oil according to claim 1, which is characterized in that the composite mixed phosphotungstate
Mass ratio with soybean oil is 1~10:100.
3. the method for synthesizing epoxy soybean oil according to claim 1, which is characterized in that the concentration of the hydrogen peroxide is
20~40%, the mass ratio of hydrogen peroxide and soybean oil is 1~2:1.
4. the method for synthesizing epoxy soybean oil according to claim 1, which is characterized in that the reaction temperature is 40~90
℃。
5. the method for synthesizing epoxy soybean oil according to claim 1, which is characterized in that the reaction time is 1.5~9
Hour.
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| CN111511845B (en) | 2017-12-22 | 2022-10-11 | 汉高股份有限及两合公司 | Primer coating and articles coated therewith |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20130244867A1 (en) * | 2009-05-19 | 2013-09-19 | Bayer Materialscience Ag | Catalyst for producing n-substituted carbamates, and the preparation and application of the same |
| CN104292187A (en) * | 2014-10-10 | 2015-01-21 | 南京工业大学 | Method for preparing high-quality epoxidized soybean oil |
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2017
- 2017-02-16 CN CN201710083443.5A patent/CN106831654B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20130244867A1 (en) * | 2009-05-19 | 2013-09-19 | Bayer Materialscience Ag | Catalyst for producing n-substituted carbamates, and the preparation and application of the same |
| CN104292187A (en) * | 2014-10-10 | 2015-01-21 | 南京工业大学 | Method for preparing high-quality epoxidized soybean oil |
Non-Patent Citations (1)
| Title |
|---|
| 过渡金属磷钨酸盐在醇氧化反应中的催化作用研究;田伟;《中国优秀硕士学位论文全文数据库 工程科技I辑》;20120715(第7期);第B014-326页，尤其是中文摘要，正文第1-2页第1.1.1-1.1.2节、第6页第1.2.1节及第9-10页第2节 |
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