CN1696174A - Method for preparing polyether glycol - Google Patents
Method for preparing polyether glycol Download PDFInfo
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- CN1696174A CN1696174A CN 200510046581 CN200510046581A CN1696174A CN 1696174 A CN1696174 A CN 1696174A CN 200510046581 CN200510046581 CN 200510046581 CN 200510046581 A CN200510046581 A CN 200510046581A CN 1696174 A CN1696174 A CN 1696174A
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Abstract
A process for preparing polyether polyol features that the natural oil and/or natural carboxylic acid and the epoxide proportionally take part in loop-opening polymerization reaction under the action of catalyst.
Description
One, technical field
The present invention relates to a kind ofly under catalyst action, preparation contains carboxylate group's the method for polyether glycol.Be used to make polyurethane material etc.
Two, background technology
Utilize the main method of natural fats and oils to have in the urethane resin at present:
(1) natural fats and oils is done the alcoholysis agent with polyols such as glycerol, carries out alcoholysis, add catalyzer and can promote alcoholysis at about 200～220 ℃, directly utilize after the alcoholysis or again with epoxide reaction.(the 233rd page of " polyurethane foamed material " third edition, in January, 2005, Chemical Industry Press)
(2) with natural fats and oils under appropriate condition, through a series of chemical reaction such as hydrolysis, saponification, hydrogenation, epoxidation and amination reaction, be translated into a kind of raw material of urethane.(the 233rd page of " polyurethane foamed material " third edition, in January, 2005, Chemical Industry Press)
Above technology more complicated.
Three, summary of the invention
The purpose of this invention is to provide a kind of novel method of utilizing natural materials system polyether glycol.
The inventive method is under catalyst action, is initiator with natural fats and oils and/or natural carboxylic acid and polyvalent alcohol directly, and with epoxide ring-opening polymerization, preparation contains carboxylate group's polyether glycol.Wherein each material consumption is (in a mass parts): polyvalent alcohol: natural grease and/or natural carboxylic acid: epoxide=1: 0.05～9.5: 0.22～10.5, catalyst levels are 0.1～1.2% of above-mentioned material sum.Temperature of reaction is 90～160 ℃, and reaction pressure is＜1MPa that the reaction times is＜12 hours.
Used natural fats and oils can be one or more in vegetables oil and fat, animal oil and the fat, and the natural carboxylic acid comprises one or more in natural acid and the rosin.
Used polyvalent alcohol can be to contain two above oxy-compound, or contains the polymkeric substance of two above oxy-compound and epoxide, or other contains the polymkeric substance of active hydride and epoxide, or above-mentioned two or more mixture.It is wherein commonly used that to contain two above oxy-compound can be in glycol ether, glycerol, tetramethylolmethane, sorbyl alcohol, the sucrose etc. one or more.Other active hydrogen-contg compound can be that hydroxyl is tetramethylolmethane and the ethylene oxide polymer of 340mgkoH/g, hydroxyl is glycerine and the epoxypropane polymer of 450mgkoH/g, and hydroxyl is one or more in the quadrol of 770mgkoH/g and epoxypropane polymer etc.
Used epoxide is one or more in propylene oxide, oxyethane, the butylene oxide ring.
Catalyst system therefor is the catalyzer of catalysis epoxidation thing ring-opening polymerization, can be mineral alkali and/or organic bases, as potassium hydroxide, sodium hydroxide, dimethylamine etc., also comprise they are suitably mixed the catalyzer that uses, when being catalyzer with highly basic such as potassium hydroxide, sodium hydroxide, in the product needed and the time, neutralizing agent is a lipid acid, as oleic acid, acetic acid etc.
Its preparation method is: drop into initiator polyvalent alcohol 1 mass parts in reactor, natural fats and oils and/or natural carboxylic acid's 0.05～9.5 mass parts, catalyzer is initiator and advance 0.1%～1.2% of epoxide quality sum, behind nitrogen replacement, advance epoxide 0.22～10.5 mass parts in 90～160 ℃, optimal reaction temperature is 100～140 ℃, reaction pressure＜1MPa, optimum response pressure＜0.4Mpa, the reaction times is＜12 hours.Advanced epoxide through slaking (insulation reaction) 1～3 hour, added neutralizing agent in case of necessity, stirring gets product.
The inventive method technology is simple.
Four, embodiment
Embodiment 1: drop into glycerine 1 mass parts in reactor, Oleum Cocois 1.66 mass parts, dimethylamine 0.06 mass parts, with nitrogen with after the reactor displacement, be warmed up to 100 ℃ and begin into propylene oxide 2.65 mass parts, control reaction temperature is at 100～140 ℃, and pressure＜0.6MPa has advanced propylene oxide after neutralization gets product.Product appearance: pale brown look paste, hydroxyl value: 392mgKOH/g, water:＜0.2%.
Embodiment 2: drop into glycerine 0.17 mass parts in reactor, sorbyl alcohol 0.83 mass parts, plam oil 0.11 mass parts, potassium hydroxide 0.005 mass parts, behind nitrogen replacement, advance propylene oxide 0.64 mass parts in 100～140 ℃, control pressure＜0.4MPa has advanced material and has got product through the slaking neutralization.Product appearance: pale brown look liquid, hydroxyl value: 717mgKOH/g, acid number:＜0.2mgKOH/g, water:＜0.2%.
Embodiment 3: dropping into the tetramethylolmethane polyethers in reactor (is tetramethylolmethane and ethylene oxide polymer, hydroxyl value 340mgKOH/g) 1 mass parts, oleic acid 0.23 mass parts, sodium hydroxide 0.005 mass parts, behind nitrogen replacement, advance oxyethane 1.05 mass parts in 100～150 ℃, control pressure＜0.4MPa has advanced material and has got product through slaking.The pale brown look liquid of product appearance, hydroxyl value: 168mgKOH/g, acid number:＜0.2mgKOH/g, water:＜0.2%.
Embodiment 4: drop into sorbyl alcohol 1 mass parts, rosin 0.82 mass parts, soybean oil 0.82 mass parts in reactor, potassium hydroxide 0.0085 mass parts, advance propylene oxide 1.135 mass parts in 100～150 ℃ behind nitrogen replacement, control pressure＜0.4MPa has advanced the material slaking and has promptly got product.Product appearance: brown liquid, hydroxyl value: 501mgKOH/g, acid number:＜0.2mgKOH/g, water:＜0.2%.
Embodiment 5: drop into sorbyl alcohol 1 mass parts, Oleum Cocois 9.5 mass parts, potassium hydroxide 0.03 mass parts in reactor, dimethylamine 0.22 mass parts, advance oxyethane 10.5 mass parts in 100～140 ℃ behind nitrogen replacement, control pressure＜1MPa has advanced material and has got product through the slaking neutralization.Product appearance: brown liquid, hydroxyl value: 142mgKOH/g, acid number:＜0.2mgKOH/g, water:＜0.2%.
Embodiment 6: dropping into the tetramethylolmethane polyethers in reactor (is tetramethylolmethane and ethylene oxide polymer, hydroxyl value: 266mgkoH/g) 0.91 mass parts, trolamine 0.09 mass parts, plam oil 0.05 mass parts, potassium hydroxide 0.00127 mass parts, advance propylene oxide 0.22 mass parts in 100～140 ℃ behind nitrogen replacement, control reaction pressure＜0.3MPa has advanced material and has neutralized through slaking and get product.Product appearance: brown liquid, hydroxyl value: 285mgKOH/g, acid number:＜0.2mgKOH/g, water:＜0.2%.
Claims (9)
1, a kind of preparation method of polyether glycol is characterized in that: under catalyst action, be initiator with natural fats and oils and/or natural carboxylic acid and polyvalent alcohol directly, with epoxide ring-opening polymerization, preparation contains carboxylate group's polyether glycol; Wherein each material consumption is counted with mass parts: polyvalent alcohol: natural grease and/or natural carboxylic acid: epoxide=1: 0.05～9.5: 0.22～10.5, catalyst levels are 0.1～1.2% of above-mentioned material sum.Temperature of reaction is 90～160 ℃, and reaction pressure is＜1MPa that the reaction times is＜12 hours.
2, method according to claim 1 is characterized in that described natural fats and oils comprises vegetables oil and fat, animal oil and fat, and the natural carboxylic acid comprises natural acid and rosin.
3, method according to claim 1, it is characterized in that described polyvalent alcohol can be to contain two above oxy-compound, or contain the polymkeric substance of two above oxy-compound and epoxide, or other contains the polymkeric substance of active hydride and epoxide, or above-mentioned two or more mixture.
4, method according to claim 3, two the above oxy-compound that contain that it is characterized in that using always can be in glycol ether, glycerol, tetramethylolmethane, sorbyl alcohol, the sucrose one or more; Other active hydrogen-contg compound can be that hydroxyl is tetramethylolmethane and the ethylene oxide polymer of 340mgkoH/g, hydroxyl is glycerine and the epoxypropane polymer of 450mgkoH/g, and hydroxyl is the quadrol of 770mgkoH/g and in the epoxypropane polymer one or more.
5, method according to claim 1 is characterized in that described epoxide is propylene oxide, oxyethane, butylene oxide ring.
6, method according to claim 1 is characterized in that described catalyzer is the catalyzer of catalysis epoxidation thing ring-opening polymerization polymer, as potassium hydroxide, sodium hydroxide, dimethylamine, also comprises they are suitably mixed the catalyzer that uses.
7, method according to claim 6 is characterized in that making catalyzer when highly basic such as adopting potassium hydroxide, sodium hydroxide, in the product needed and the time, used neutralizing agent is a lipid acid.
8, method according to claim 1, it is characterized in that being in reactor, dropping into initiator polyvalent alcohol 1 mass parts, natural grease and/or natural carboxylic acid's 0.05～9.5 mass parts, catalyzer is initiator and advance 0.1%～1.2% of epoxide quality sum, behind nitrogen replacement, advance epoxide 0.22～10.5 mass parts in 90～160 ℃, temperature of reaction is 100～140 ℃, reaction pressure＜1MPa, advanced epoxide through slaking, add neutralizing agent in case of necessity, neutralization is stirred and is promptly got product.
9, method according to claim 8 is characterized in that being that reaction pressure is＜0.4Mpa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100465813A CN1320029C (en) | 2005-05-31 | 2005-05-31 | Method for preparing polyether glycol |
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| CNB2005100465813A CN1320029C (en) | 2005-05-31 | 2005-05-31 | Method for preparing polyether glycol |
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| CN1696174A true CN1696174A (en) | 2005-11-16 |
| CN1320029C CN1320029C (en) | 2007-06-06 |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102304223A (en) * | 2011-07-14 | 2012-01-04 | 广州朗腾聚氨酯有限公司 | Plant oil polyether glycol and preparation method thereof |
| CN102336901A (en) * | 2011-08-03 | 2012-02-01 | 句容宁武新材料发展有限公司 | Method for preparing polyurethane polyether polyol by waste oil |
| US8865945B2 (en) | 2007-08-16 | 2014-10-21 | Bayer Materialscience Ag | Process for the preparation of polyols |
| CN104497298A (en) * | 2015-01-16 | 2015-04-08 | 江苏长华聚氨酯科技有限公司 | Method for preparing polyether polyol with low degree of unsaturation, high molecular weight and high activity |
| CN110387033A (en) * | 2018-04-17 | 2019-10-29 | 高春青 | It is a kind of for synthesizing the bio-based resin and preparation method thereof of sustained and controlled release chemical fertilizer polymer capsule |
| CN111171964A (en) * | 2020-01-10 | 2020-05-19 | 佛山市三水伯马絮凝剂厂 | Vegetable oil polyalcohol and preparation method thereof |
| CN115246920A (en) * | 2021-09-16 | 2022-10-28 | 佳化化学科技发展（上海）有限公司 | Open-cell polyurethane rigid foam and preparation method and application thereof |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IS4687A (en) * | 1998-03-13 | 1998-04-06 | Shell Internationale Research Maatschappij B.V. | Process for the production of odorless polyether polyols |
| DE10008635A1 (en) * | 2000-02-24 | 2001-09-06 | Basf Ag | Process for the preparation of polyether polyols |
| DE60110587T2 (en) * | 2000-05-15 | 2006-01-19 | Shell Internationale Research Maatschappij B.V. | PROCESS FOR PREPARING POLYEHTER POLYOLS |
| DE10108484A1 (en) * | 2001-02-22 | 2002-09-05 | Bayer Ag | Improved process for the production of polyether polyols |
| CN1294178C (en) * | 2003-07-09 | 2007-01-10 | 中国石油化工股份有限公司 | Process for producing polyether polyols with low degree of unsaturation |
-
2005
- 2005-05-31 CN CNB2005100465813A patent/CN1320029C/en active Active
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8865945B2 (en) | 2007-08-16 | 2014-10-21 | Bayer Materialscience Ag | Process for the preparation of polyols |
| CN101367926B (en) * | 2007-08-16 | 2015-09-16 | 拜耳材料科技股份有限公司 | Prepare the method for polyvalent alcohol |
| CN102304223A (en) * | 2011-07-14 | 2012-01-04 | 广州朗腾聚氨酯有限公司 | Plant oil polyether glycol and preparation method thereof |
| CN102336901A (en) * | 2011-08-03 | 2012-02-01 | 句容宁武新材料发展有限公司 | Method for preparing polyurethane polyether polyol by waste oil |
| CN104497298A (en) * | 2015-01-16 | 2015-04-08 | 江苏长华聚氨酯科技有限公司 | Method for preparing polyether polyol with low degree of unsaturation, high molecular weight and high activity |
| CN104497298B (en) * | 2015-01-16 | 2017-02-22 | 江苏长华聚氨酯科技有限公司 | Method for preparing polyether polyol with low degree of unsaturation, high molecular weight and high activity |
| CN110387033A (en) * | 2018-04-17 | 2019-10-29 | 高春青 | It is a kind of for synthesizing the bio-based resin and preparation method thereof of sustained and controlled release chemical fertilizer polymer capsule |
| CN111171964A (en) * | 2020-01-10 | 2020-05-19 | 佛山市三水伯马絮凝剂厂 | Vegetable oil polyalcohol and preparation method thereof |
| CN115246920A (en) * | 2021-09-16 | 2022-10-28 | 佳化化学科技发展（上海）有限公司 | Open-cell polyurethane rigid foam and preparation method and application thereof |
| CN115246920B (en) * | 2021-09-16 | 2024-09-10 | 佳化化学科技发展（上海）有限公司 | Open-cell polyurethane rigid foam and preparation method and application thereof |
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| Publication number | Publication date |
|---|---|
| CN1320029C (en) | 2007-06-06 |
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Owner name: JIAHUA CHEMICALS INC. Free format text: FORMER NAME: JIAHUA POLYURETHANE CO., LTD., FUSHUN |
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Address after: Hebei Xiang Dong Gou Cun 113123 Fushun City Shuncheng District in Liaoning Province Patentee after: Jiahua Chemicals Inc. Address before: Hebei Xiang Dong Gou Cun 113123 Fushun City Shuncheng District in Liaoning Province Patentee before: Jiahua Polyurethane Co., Ltd., Fushun |
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Effective date of registration: 20210709 Address after: 113000 No.3, Qilong East Street, Dongzhou District, Fushun City, Liaoning Province Patentee after: JIAHUA CHEMICAL (FUSHUN) NEW MATERIALS Co.,Ltd. Address before: Hebei Xiang Dong Gou Cun 113123 Fushun City Shuncheng District in Liaoning Province Patentee before: JIAHUA CHEMICALS Inc. |
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