CN112142967A - Synthesis method of polycaprolactone polyol - Google Patents

Synthesis method of polycaprolactone polyol Download PDF

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Publication number
CN112142967A
CN112142967A CN202010879970.9A CN202010879970A CN112142967A CN 112142967 A CN112142967 A CN 112142967A CN 202010879970 A CN202010879970 A CN 202010879970A CN 112142967 A CN112142967 A CN 112142967A
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catalyst
acid
polycaprolactone polyol
polyol
poly
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谢传欣
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Qingdao University of Science and Technology
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Qingdao University of Science and Technology
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/78Preparation processes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/02Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
    • C08G63/06Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids
    • C08G63/08Lactones or lactides

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyesters Or Polycarbonates (AREA)

Abstract

The invention provides a method for synthesizing polycaprolactone polyol, which comprises the following steps of mixing poly-6-hydroxyhexanoate with polyol, a first catalyst and a solvent at 300 ℃ for transesterification reaction for 1-20h, adding a second catalyst at 300 ℃ of 250 ℃ and 0.0005-0.1MPa for molecular weight modulation for 1-5h, distilling the solvent after the reaction is finished, and finally obtaining the polycaprolactone polyol: the cost is lower, the yield of polycaprolactone polyol is improved, the whole reaction risk is low, and the method is environment-friendly and pollution-free.

Description

Synthesis method of polycaprolactone polyol
Technical Field
The invention belongs to the chemical industry, and particularly relates to a synthetic method of polycaprolactone polyol.
Background
Polycaprolactone Polyol (PCL) is an aliphatic linear polyester, is very soft and has extremely high stretchability, and PCL having a molecular weight of several thousand or less has a wide range of applications and a wide range of applications in resin modification, paints, adhesives, polyurethane artificial leathers, leather finishing agents, and the like, and is a very useful organic material. At present, caprolactone monomers are used as raw materials for preparing polycaprolactone polyol, different catalysts and initiators are used for researching the production process of polycaprolactone polyol, and the best materials and methods are selected, for example, patents CN108424512A, CN108912316A and CN109054001A are provided, but only holy petrochemical seeds and Hunan polymer seeds can industrially produce caprolactone at home, the holy petrochemical seeds are 200t/a, the Hunan polymer seeds are few, and only Swedish Basito (PERSTORP) is produced at home and can be 15000t/a abroad, and other three large enterprises are also producing caprolactone, so that the home price of caprolactone is always high, the production of polycaprolactone polyol has the problem of high raw material price, and the production of polycaprolactone polyol applied in different aspects needs to be controlled, and the reaction can be controlled according to the monomer purity, the initiator proportion, the amount of the catalysts, the reaction time and the like, The reaction temperature and the like are controlled in various aspects, and the experimental conditions are harsh.
Disclosure of Invention
In order to solve the above problems, the present invention provides a specific experimental scheme: firstly, mixing the poly 6-hydroxy caproate with polyhydric alcohol, a first catalyst and a solvent at the temperature of 220-300 ℃ for transesterification reaction for 1-20h, then adding a second catalyst at the temperature of 250-300 ℃ under the absolute pressure of 0.0005-0.1Mpa for molecular weight modulation for 1-5h, and distilling the solvent after the reaction is finished to finally obtain the polycaprolactone polyhydric alcohol.
The polyalcohol used for ester exchange is one or more selected from ethylene glycol, 1, 3-propylene glycol, 1, 2-propylene glycol, 1, 4-butanediol, 1, 5-pentanediol, 1, 6-hexanediol, glycerol, 1, 4-cyclohexanediol, and 1, 4-cyclohexanedimethanol.
The amount of the polyhydric alcohol is 50-300% of the poly-6-hydroxycaproic acid.
The first catalyst is selected from one or more of concentrated sulfuric acid, sulfonic acid, strong acid cation exchange resin, zirconium sulfate, tin sulfate, zirconium oxide, zirconium tungstate, formic acid, acetic acid, propionic acid and p-toluenesulfonic acid.
The first catalyst is 0.005-5% of poly-6-hydroxycaproic acid.
The solvent is one or more selected from THF, acetone, DMSO, DMF, and chloroform, and the amount of the solvent is 0-200% of that of the poly-6-hydroxycaproic acid.
The ester exchange reaction temperature is 220-300 ℃, and the reaction time is 1-20 h.
The second catalyst is selected from one or more of cobalt acetate, ethylene glycol antimony, manganese, zinc, calcium, cobalt and lead acetate, amorphous aluminum silicate and ZSM-5 type molecular sieve, and the dosage of the second catalyst is 0.005-5% of that of the 6-hydroxycaproic acid.
The invention has the beneficial effects that:
compared with most of polycaprolactone polyol products on the market, the technology has lower cost, solves the problem of cost of a route which depends on caprolactone as a raw material, provides a new technical route for the diversified production of the polycaprolactone polyol, improves the yield of the polycaprolactone polyol, has small risk of the whole reaction, is environment-friendly and has no pollution.
Detailed Description
The invention is further described below with reference to examples. The scope of the invention is not limited thereto.
Example 1
30g of polycaprolactone, 20g of ethylene glycol, 0.5g of formic acid and 20g of THF are mixed and added into a 250ml round-bottom flask, the flask is placed in a heat collection type constant temperature heating magnetic stirring instrument for reaction at 250 ℃ for 3h, then 0.5g of ethylene glycol antimony is added for reaction at 255 ℃ and absolute pressure of 0.05Mpa for 1h, and after the reaction is finished, redundant solvent is distilled and removed to obtain 28.9g of polycaprolactone polyol, wherein the yield is 96.3%.
Examples 2 to 5
The quality of polycaprolactone is the same as that of example 1, and is different from that of example 1 in the following table 1.
Examples 6 to 10
The mass of polycaprolactone was 40g, which is otherwise different from example 1 and is specified in Table 1.
Examples 11 to 15
The mass of polycaprolactone was 50g, which is different from example 1 and is shown in Table 1.
The experimental data for examples 1-15 are detailed in Table 1.
Table 1 summary of experimental data of examples
Figure BDA0002653829390000021
Figure BDA0002653829390000031
As can be seen from the table, the yield of polycaprolactone polyol was over 95%.

Claims (7)

1. A synthesis method of polycaprolactone polyol is characterized in that poly-6-hydroxyhexanoate is firstly mixed with polyol, a first catalyst and a solvent at the temperature of 220 ℃ and 300 ℃ for transesterification reaction for 1-20h, then a second catalyst is added for molecular weight modulation at the temperature of 250 ℃ and 300 ℃ and the absolute pressure of 0.0005-0.1Mpa for 1-5h, and the solvent is distilled after the reaction is finished, so that the polycaprolactone polyol is finally obtained.
2. The method for synthesizing polycaprolactone polyol according to claim 1, wherein the polyol used for the transesterification is one or more selected from ethylene glycol, 1, 3-propanediol, 1, 2-propanediol, 1, 4-butanediol, 1, 5-pentanediol, 1, 6-hexanediol, glycerol, 1, 4-cyclohexanediol, and 1, 4-cyclohexanedimethanol.
3. The method of claim 1, wherein the polyol is present in an amount of 50% to 300% of the poly-6-hydroxycaproic acid.
4. The method for synthesizing polycaprolactone polyol according to claim 1, wherein the first catalyst is one or more selected from concentrated sulfuric acid, sulfonic acid, strongly acidic cation exchange resin, zirconium sulfate, tin sulfate, zirconium oxide, zirconium tungstate, formic acid, acetic acid, propionic acid and p-toluenesulfonic acid.
5. The method of claim 1, wherein the first catalyst is present in an amount of 0.005% to 5% of the poly-6-hydroxycaproic acid.
6. The method for synthesizing polycaprolactone polyol according to claim 1, wherein the solvent is one or more selected from THF, acetone, DMSO, DMF and chloroform, and the amount is 0-200% of poly-6-hydroxycaproic acid.
7. The method for synthesizing polycaprolactone polyol according to claim 1, wherein the second catalyst is one or more selected from cobalt acetate, ethylene glycol antimony, manganese, zinc, calcium, cobalt, lead acetate, amorphous aluminum silicate, and ZSM-5 type molecular sieve, and the amount of the second catalyst is 0.005% -5% of 6-hydroxycaproic acid.
CN202010879970.9A 2020-08-27 2020-08-27 Synthesis method of polycaprolactone polyol Pending CN112142967A (en)

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CN112142967A true CN112142967A (en) 2020-12-29

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114044886A (en) * 2021-12-01 2022-02-15 青岛科技大学 Production method of polycaprolactone

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1397577A (en) * 2002-08-23 2003-02-19 清华大学 Process for synthesizing polyurethane elastomer containing poly-beta-hydroxybutyrate block
CN101450989A (en) * 2008-12-19 2009-06-10 东华大学 Method for synthesizing poly hydroxy fatty acid ester block copolymers in situ

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1397577A (en) * 2002-08-23 2003-02-19 清华大学 Process for synthesizing polyurethane elastomer containing poly-beta-hydroxybutyrate block
CN101450989A (en) * 2008-12-19 2009-06-10 东华大学 Method for synthesizing poly hydroxy fatty acid ester block copolymers in situ

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114044886A (en) * 2021-12-01 2022-02-15 青岛科技大学 Production method of polycaprolactone
CN114044886B (en) * 2021-12-01 2023-08-29 青岛科技大学 Production method of polycaprolactone

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