CN101864072A - Synthetizing method of water reducer macromer methoxyl-polyethyleneglycol allylether - Google Patents
Synthetizing method of water reducer macromer methoxyl-polyethyleneglycol allylether Download PDFInfo
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- CN101864072A CN101864072A CN201010213686.4A CN201010213686A CN101864072A CN 101864072 A CN101864072 A CN 101864072A CN 201010213686 A CN201010213686 A CN 201010213686A CN 101864072 A CN101864072 A CN 101864072A
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- ethylene glycol
- methoxy poly
- allyl ethers
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Abstract
The invention relates to a synthetizing method of water reducer macromer methoxyl-polyethyleneglycol allylether. The methoxyl-polyethyleneglycol allylether is synthetized by condensing methoxyl-polyethyleneglycol and allylhalide in NaOH or KOH. The raw materials used by the synthetizing method are cheap and available allyl chloride; the synthetizing method has simple process and low cost and is suitable for the industrial production of the water reducer macromer methoxyl-polyethyleneglycol allyl ether compound, and the prepared water reducer macromer has the advantages of high blocking rate and does not contain a polymerization inhibitor.
Description
Technical field
The present invention relates to a kind of synthetic method of water reducer macromer, especially be particularly related to a kind of synthetic method of water reducer macromer methoxyl-polyethyleneglycol allyl ethers, belong to end capped synthesis technical field in the organic chemistry.
Background technology
The allyl ethers structure has isomerization, in conjunction with performances such as oxygen and polymerizations, is usually used in polymer monomer or fields such as linking agent and water reducer, is the important organic compound of a class.One end of its molecular structure of methoxy poly (ethylene glycol) allyl ethers has polymerisable double bonds, is a kind of surface-active macromonomer of novel polycarboxylic acids dehydragent.
Poly carboxylic acid series water reducer has experienced continuous development and the improvement in twenties years, and it is more superior that the high performance water reducer of this class and former water reducer are compared performance.Add its production and use the characteristics that go up the tool environmental protection, generally acknowledge that generally poly carboxylic acid series water reducer is a water reducer of new generation.The molecular weight of this class water reducer macromer is generally less than 5000, its principal feature is to have that volume is few, water-reducing rate greatly, do not emanate, bleeding, concrete are not spoilt characteristics such as degree of falling property retention is good.
The big monomeric synthetic side of traditional poly carboxylic acid series water reducer gets with poly glycol monomethyl ether and vinylformic acid (methacrylic acid) esterification, in esterification process, add noxious solvent usually, make the band aqua as benzene, toluene or hexanaphthene equal solvent, also need add a certain amount of stopper simultaneously.Synthetic middle radical polymerization has bigger influence to next step water reducer in the adding of stopper.And the synthetic method of water reducer macromer methoxyl-polyethyleneglycol allyl ethers is still appeared in the newspapers at the end, does not particularly add more last the appearing in the newspapers of synthetic method of solvent and stopper when the big monomer of preparation poly carboxylic acid series water reducer.
Summary of the invention
It is reasonable to the purpose of this invention is to provide a kind of technology, product end-blocking rate height, have the synthetic method of the water reducer macromer methoxyl-polyethyleneglycol allyl ethers of better use properties, the inventive method is environmentally friendly, does not add stopper when the big monomer of synthesizing polycarboxylic acid dehydragent.
The present invention is by the following technical solutions:
A kind of synthetic method of water reducer macromer methoxyl-polyethyleneglycol allyl ethers may further comprise the steps:
1) methoxy poly (ethylene glycol) and N
aOH or KOH mix the back and stir intensification, under vacuum condition, keep for 80-150 ℃, make methoxy poly (ethylene glycol) sodium or methoxy poly (ethylene glycol) potassium;
2) methoxy poly (ethylene glycol) sodium that makes or methoxy poly (ethylene glycol) potassium cooling back drip chloro propylene are warming up to 70-85 ℃ of reaction after dropwising;
3) with step 2) cooling of gained reaction product, add dissolution with solvents, and wash with the saturated solution of sodium-chlor or Repone K, upper strata liquid is got in phase-splitting, and underpressure distillation removes solvent, gets the methoxy poly (ethylene glycol) allyl ethers.
The inventive method is a raw material with methoxy poly (ethylene glycol) and propenyl chloride, at N
aOH or KOH exist down, methoxy poly (ethylene glycol) and propenyl chloride condensation and make the methoxy poly (ethylene glycol) allyl ethers.With N
aOH is an example, and the reaction equation of the inventive method is:
(1) preparation of sodium alkoxide
CH
3O(CH
2CH
2O)
nH+N
aOH→CH
3O(CH
2CH
2O)
nN
a+H
2O
(2) preparation of allyl ether
CH
3O(CH
2CH
2O)
nN
a+CH
2＝CHCH
2CL→CH
3O(CH
2CH
2O)
nCH
2CH＝CH
2+N
aCL
The structural formula of described water reducer macromer methoxyl-polyethyleneglycol allyl ethers can be expressed as:
CH
3O(CH
2CH
2O)
nCH
2CH＝CH
2
N=17-110 in the formula.
The polymerization degree of described methoxy poly (ethylene glycol) is 17-110.
In the described step 1), methoxy poly (ethylene glycol) and N
aThe mol ratio of OH or KOH is 1.0: 1.0-5.0.
In the described step 1), the temperature of reaction of preparation sodium alkoxide is 80-150 ℃, preferred 110-120 ℃.
In the described step 1), the reaction of preparation sodium alkoxide is held time and is 30-120min.
In the described step 1), the vacuum tightness during the preparation sodium alkoxide is-0.09Mpa---0.098Mpa.
Described step 2) in, the mol ratio of propenyl chloride and methoxy poly (ethylene glycol) is 1.0: 1.0-5.0.
Described step 2) in, the time of drip chloro propylene is controlled to be 45-90min, and dropping temperature is controlled to be 50-60 ℃.
Described step 2) in, the propenyl chloride temperature of reaction is controlled to be 70-85 ℃, preferred 80-85 ℃.
Described step 2) in, the propenyl chloride reaction times is 180-400min.
In the described step 3), add solvent to remove sodium-chlor or the Repone K that dereaction generates.Described solvent is glycol dimethyl ether, diethylene glycol dimethyl ether or triethylene glycol dme etc., and washs with the saturated solution of sodium-chlor or Repone K, to remove the salt that dereaction generates.Upper organic phase is got in phase-splitting, and underpressure distillation removes solvent can get the methoxy poly (ethylene glycol) allyl ethers.。
The inventive method compared with prior art has following beneficial effect:
1, adopt the propenyl chloride end-blocking to prepare water reducer macromer, raw material cheaply is easy to get, and technology is simple, can effectively reduce the cost of water reducer macromer.
2 and traditional esterification technique compare, do not adopt noxious solvent to make the band aqua, production method is environmentally friendly.
3, the methoxy poly (ethylene glycol) allyl ethers water reducer macromer of the inventive method preparation has end-blocking rate height, does not contain the advantage of stopper, is applicable to the synthetic field of high-performance polycarboxylic acids dehydragent.
Describe the present invention below in conjunction with embodiment.Scope of the present invention is not exceeded with embodiment, but is limited by the scope of claim.
Embodiment
Embodiment 1
In the four-hole boiling flask of 2000ml, drop into 1200g methoxy poly (ethylene glycol) (polymerization degree is 22), 48g solid N
aOH stirs and heats up.Controlled temperature 110-120 ℃, vacuum tightness-0.09Mpa---0.098Mpa, reaction 30-120min.Be cooled to then 50-60 ℃ stand-by.Adding 91.8g propenyl chloride is controlled in the 60min and dropwises in constant pressure funnel.Be warming up to 80-85 ℃ of reaction 180-400min then, be cooled to 50-60 ℃, add the diethylene glycol dimethyl ether dissolving, with the saturated solution washing of sodium-chlor, upper solution is got in phase-splitting, last underpressure distillation desolventizing and moisture content.Get the methoxy poly (ethylene glycol) allyl ethers, record the little what 2mgKOH/g of hydroxyl value, end-blocking rate＞98%.
Embodiment 2
In the four-hole boiling flask of 2000ml, drop into 1200g methoxy poly (ethylene glycol) (polymerization degree is 26.5), 60g part N
aOH stirs and heats up.Controlled temperature 80-150 ℃, vacuum tightness-0.09Mpa---0.098Mpa, reaction 30-120min.Be cooled to then 50-60 ℃ stand-by.Adding 114.7g propenyl chloride is controlled in the 60min and dropwises in constant pressure funnel.Be warming up to 80-85 ℃ of reaction 180-400min then, be cooled to 50-60 ℃, add the diethylene glycol dimethyl ether dissolving, with the saturated solution washing of sodium-chlor, upper solution is got in phase-splitting, last underpressure distillation desolventizing and moisture content.Get the methoxy poly (ethylene glycol) allyl ethers, record the little what 2mgKOH/g of hydroxyl value, end-blocking rate＞98%.
Embodiment 3
In the four-hole boiling flask of 2000ml, drop into 1200g part methoxy poly (ethylene glycol) (polymerization degree is 33.3), 64g part N
aOH stirs and heats up.Controlled temperature 80-150 ℃, vacuum tightness-0.09Mpa---0.098Mpa, reaction 30-120min.Be cooled to then 50-60 ℃ stand-by.Adding 122.4g propenyl chloride is controlled in the 60min and dropwises in constant pressure funnel.Be warming up to 70-80 ℃ of reaction 180-400min then, be cooled to 50-60 ℃, add the glycol dimethyl ether dissolving, with the saturated solution washing of sodium-chlor, upper solution is got in phase-splitting, last underpressure distillation desolventizing and moisture content.Get the methoxy poly (ethylene glycol) allyl ethers, record the little what 2mgKOH/g of hydroxyl value, end-blocking rate＞98%.
Claims (9)
1. the synthetic method of a water reducer macromer methoxyl-polyethyleneglycol allyl ethers may further comprise the steps:
1) methoxy poly (ethylene glycol) and N
aOH or KOH mix the back and stir intensification, under vacuum condition, keep for 80-150 ℃, make methoxy poly (ethylene glycol) sodium or methoxy poly (ethylene glycol) potassium;
2) methoxy poly (ethylene glycol) sodium that makes or methoxy poly (ethylene glycol) potassium cooling back drip chloro propylene are warming up to 70-85 ℃ of reaction after dropwising;
3) with step 2) cooling of gained reaction product, add dissolution with solvents, and wash with the saturated solution of sodium-chlor or Repone K, upper strata liquid is got in phase-splitting, and underpressure distillation removes solvent, gets the methoxy poly (ethylene glycol) allyl ethers.
2. the synthetic method of methoxy poly (ethylene glycol) allyl ethers according to claim 1, the polymerization degree that it is characterized in that described methoxy poly (ethylene glycol) is 17-110.
3. the synthetic method of methoxy poly (ethylene glycol) allyl ethers according to claim 1 is characterized in that in the described step 1) methoxy poly (ethylene glycol) and N
aThe mol ratio of OH or KOH is 1.0: 1.0-5.0.
4. the synthetic method of methoxy poly (ethylene glycol) allyl ethers according to claim 1 is characterized in that in the described step 1), and the reaction of preparation sodium alkoxide is held time and is 30-120min.
5. the synthetic method of methoxy poly (ethylene glycol) allyl ethers according to claim 1 is characterized in that in the described step 1), and vacuum tightness is-0.09Mpa---0.098Mpa during the preparation sodium alkoxide.
6. the synthetic method of methoxy poly (ethylene glycol) allyl ethers according to claim 1 is characterized in that described step 2) in, the mol ratio of propenyl chloride and methoxy poly (ethylene glycol) is 1.0: 1.0-5.0.
7. the synthetic method of methoxy poly (ethylene glycol) allyl ethers according to claim 1 is characterized in that described step 2) in, the time of drip chloro propylene is controlled to be 45-90min, and dropping temperature is controlled to be 50-60 ℃.
8. the synthetic method of methoxy poly (ethylene glycol) allyl ethers according to claim 1 is characterized in that described step 2) in, the propenyl chloride reaction times is 180-400min.
9. the synthetic method of methoxy poly (ethylene glycol) allyl ethers according to claim 1 is characterized in that in the described step 3), and solvent is glycol dimethyl ether, diethylene glycol dimethyl ether or triethylene glycol dme.
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| CN104230202A (en) * | 2014-09-02 | 2014-12-24 | 科之杰新材料集团有限公司 | Methoxy-terminated straight-chain olefins polyether monomer for concrete water reducing agent and preparation method of methoxy-terminated straight-chain olefins polyether monomer |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050158506A1 (en) * | 2002-02-18 | 2005-07-21 | Fuji Photo Film Co., Ltd. | Nanoparticle, method of producing nanoparticle and magnetic recording medium |
| CN101450984A (en) * | 2008-08-13 | 2009-06-10 | 大连市铭源全科技开发有限公司 | Most simple method for producing concrete polycarboxylate high performance dehydragent |
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Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050158506A1 (en) * | 2002-02-18 | 2005-07-21 | Fuji Photo Film Co., Ltd. | Nanoparticle, method of producing nanoparticle and magnetic recording medium |
| CN101450984A (en) * | 2008-08-13 | 2009-06-10 | 大连市铭源全科技开发有限公司 | Most simple method for producing concrete polycarboxylate high performance dehydragent |
Non-Patent Citations (1)
| Title |
|---|
| 《"全国特种混凝土技术及工程应用"学术交流会暨2008年混凝土质量专业委员会年会论文集》 20080930 姜艳等 甲氧基聚乙二醇稀丙基封端聚醚的制备及其在水泥减水剂中的应用 , 2 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104230202A (en) * | 2014-09-02 | 2014-12-24 | 科之杰新材料集团有限公司 | Methoxy-terminated straight-chain olefins polyether monomer for concrete water reducing agent and preparation method of methoxy-terminated straight-chain olefins polyether monomer |
| CN104230202B (en) * | 2014-09-02 | 2016-03-09 | 科之杰新材料集团有限公司 | A kind of cement water reducing agent methoxy group normal olefine polyether monomer and preparation method thereof |
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Address after: 214262 Jiangsu province Zhoutie town Yixing City Patentee after: Jiangsu Tianyin Chemical Co.,Ltd. Patentee after: JIANGSU DYNAMIC CHEMICAL Co.,Ltd. Address before: 214262 Jiangsu province Zhoutie town Yixing City Patentee before: Jiangsu Tianyin Chemical Co.,Ltd. Patentee before: DENA NANJING CHEMICAL CO.,LTD. |
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Effective date of registration: 20220920 Address after: No. 109, Yi South Road, High-tech Zone, Maoming City, Guangdong Province, 525030 Patentee after: Dana New Materials (Maoming) Co.,Ltd. Address before: 214262 Jiangsu province Zhoutie town Yixing City Patentee before: Jiangsu Tianyin Chemical Co.,Ltd. Patentee before: JIANGSU DYNAMIC CHEMICAL Co.,Ltd. |