CN115850642A - Preparation method of high-performance polyurethane elastomer - Google Patents

Preparation method of high-performance polyurethane elastomer Download PDF

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CN115850642A
CN115850642A CN202211546196.5A CN202211546196A CN115850642A CN 115850642 A CN115850642 A CN 115850642A CN 202211546196 A CN202211546196 A CN 202211546196A CN 115850642 A CN115850642 A CN 115850642A
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polyurethane elastomer
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performance polyurethane
chain extender
reaction system
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项赛飞
应建波
费正东
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Ningbo Polytec New Materials Technology Co ltd
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Abstract

The invention belongs to the technical field of high polymer materials, and particularly relates to a preparation method of a high-performance polyurethane elastomer. The preparation method of the high-performance polyurethane elastomer comprises the following steps: (1) Mixing and heating polymer polyol and polyisocyanate to carry out prepolymerization reaction; (2) Adding a catalyst and a chain extender into the reaction system in the step (1) for heating reaction; (3) Adding bridged siloxane into the reaction system in the step (2), and uniformly stirring to obtain a material to be mixed; (4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer. The polyurethane elastomer prepared by adding the reinforcing modifier bridging siloxane into a reaction system for synthesizing polyurethane has excellent mechanical property, hydrolysis resistance and oil resistance.

Description

Preparation method of high-performance polyurethane elastomer
Technical Field
The invention belongs to the technical field of high polymer materials, and particularly relates to a preparation method of a high-performance polyurethane elastomer.
Background
The polyurethane elastomer has excellent comprehensive properties such as high strength, high toughness, wear resistance, oil resistance and the like, has good processing performance, and is widely applied to various fields of national life such as cables, sealing elements, transmission belts, steel rolling rubber rollers and the like. With the development of science and technology, the application field of polyurethane elastomers is continuously expanded, and products in practical application have higher requirements on the performance of the polyurethane elastomers.
Currently, inorganic filler loading is the primary method of polyurethane elastomer reinforcement. The inorganic filler generally has the advantages of high strength, high rigidity, heat resistance, low price and the like, and when the inorganic filler is added into the polyurethane elastomer to prepare the composite material, the cost can be reduced, and the mechanical property, the heat resistance and the like of the material can be improved. Common inorganic fillers include: nano particles (Nano SiO) 2 Nano TiO 2 2 Nano CaCO, nano-grade CaCO 3 ) Layered silicate clay minerals (montmorillonite and attapulgite), short fibers (carbon fibers and glass fibers), carbon nanotubes and the like. However, the compatibility of the inorganic filler and polyurethane is poor, the inorganic filler is difficult to uniformly distribute in the system, and the surface modification needs to be carried out on the filler so as to improve the two-phase interface and improve the dispersion uniformity and stability. If the surface treatment cannot be performed efficiently, the material properties will be deteriorated.
Crosslinking technology is also an effective way to improve the performance of polyurethane elastomers. Chinese patent application document (publication No. CN 114369220A) discloses a thermoplastic polyurethane elastomer nano composite material and a preparation method thereof, and reactive nano silicon dioxide introduced in the polymerization process of a thermoplastic polyurethane elastomer is expected to solve the problem that the toughness of TPU cannot be maintained while the strength and the wear resistance of TPU are improved in the prior art. However, the reactive nano-silica is used as an inorganic particle, the number of active groups on the surface which can participate in the reaction is limited, the chemical bonding capability with the polyurethane elastomer is weak, and the mechanical property of the obtained composite material is poor.
Disclosure of Invention
The present invention has been made in view of the above problems, and an object of the present invention is to provide a method for producing a high-performance polyurethane elastomer which can provide a polyurethane elastomer having good mechanical properties and excellent hydrolysis resistance and oil resistance.
The preparation method of the high-performance polyurethane elastomer in the technical scheme of the invention comprises the following steps:
(1) Mixing and heating polymer polyol and polyisocyanate to carry out prepolymerization reaction;
(2) Adding a catalyst and a chain extender into the reaction system in the step (1) for heating reaction;
(3) Adding bridged siloxane into the reaction system in the step (2), and uniformly stirring to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer.
Adding a reinforcing modifier bridging siloxane into a reaction system for synthesizing polyurethane, pre-embedding the reinforcing modifier bridging siloxane in a polyurethane elastomer, and hydrolyzing the bridging siloxane embedded in the elastomer in a moist-heat environment and performing mutual polycondensation in the process of heating and forming the elastomer so as to form a cross-linked network structure in the process of forming the elastomer and improve the mechanical property of the polyurethane elastomer.
Further, the polymer polyol is one or two of polyester polyol and polyether polyol. Preferably, the polyester polyol includes, but is not limited to, any one of polyethylene adipate, polybutylene adipate, or polybutylene adipate, and the polyether polyol includes, but is not limited to, any one of polytetrahydrofuran glycol or polypropylene glycol.
Further, the polyisocyanate is one or more of Toluene Diisocyanate (TDI), diphenylmethane diisocyanate (MDI), isophorone diisocyanate (IPDI), hexamethylene Diisocyanate (HDI).
Further, the chain extender is one or two of diamine chain extender and alcohol chain extender, preferably, the diamine chain extender includes but is not limited to 3,3 '-dichloro-4,4' -diaminodiphenylmethane (MOCA), and any one of dimethylthiotoluenediamine (DMTDA), and the alcohol chain extender includes but is not limited to any one of 1,4-Butanediol (BDO), ethylene Glycol (EG), and Trimethylolpropane (TMP).
Further, the catalyst is one or more of stannous octoate, dibutyltin dioctoate and dibutyltin laurate.
Further, the bridging siloxane is one or more of bis (3-triethoxysilylpropyl) amine (BTESPA), bis- (3- (triethoxysilyl) propyl) -disulfide (TSDS), 1,2-bis (triethoxysilyl) ethane (BTESE).
The structural formula of bis (3-triethoxysilylpropyl) amine is as follows:
Figure BDA0003980034220000021
the structural formula of bis- (3- (triethoxysilane) propyl) -disulfide is as follows:
Figure BDA0003980034220000022
1,2-bis (triethoxysilyl) ethane has the following structural formula:
Figure BDA0003980034220000031
further, the weight parts of the raw materials are as follows: 45-70 parts of polymer polyol, 15-30 parts of polyisocyanate, 3-8 parts of chain extender, 0.05-0.1 part of catalyst and 0.5-3.0 parts of reinforcing modifier bridging siloxane.
Further, adding a catalyst, a chain extender and a mineral filler into the reaction system of the step (1) and heating for reaction together.
Further, the mineral filler is one of calcium carbonate, talcum powder, titanium dioxide, silicon dioxide and montmorillonite.
Furthermore, the weight portion of the mineral filler is more than 0 portion and less than or equal to 10 portions.
Further, the temperature of the prepolymerization reaction in the step (1) is 20-80 ℃, and the time is 1-4 h.
Further, the heating reaction in the step (2) is carried out at the temperature of 20-80 ℃ for 1-4 h.
Further, in the step (3), the bridging siloxane is diluted by an organic solvent before being added into the reaction system, and the mass ratio of the bridging siloxane to the organic solvent is 1:5-10.
Further, the organic solvent is one or more of ethanol, acetone, tetrahydrofuran, N-methylpyrrolidone and dimethyl sulfoxide.
A high-performance polyurethane elastomer is prepared by the preparation method of the high-performance polyurethane elastomer.
Compared with the prior art, the technical scheme of the invention has the following beneficial effects:
(1) The reinforcing modifier bridged siloxane is added into a reaction system for synthesizing polyurethane, and the prepared polyurethane elastomer has excellent mechanical property, hydrolysis resistance and oil resistance;
(2) The bridged siloxane is hydrolyzed and mutually condensed in the elastomer heating and forming process to form a cross-linked network structure in the elastomer forming process, so that the mechanical property of the polyurethane elastomer is improved;
(3) The bridging siloxane adopted by the invention is further one or more of bis (3-triethoxysilylpropyl) amine, bis- (3- (triethoxysilylpropyl) -disulfide and 1,2-bis (triethoxysilyl) ethane, the siloxane with the structure has the advantages of mild polycondensation reaction conditions, stable product structure and good mechanical property, and can simultaneously improve the mechanical property, hydrolysis resistance and oil resistance of the polyurethane elastomer;
(4) The preparation method has the advantages of simple process, low cost, environmental friendliness and remarkable effect.
Detailed Description
The technical solutions of the present invention are further described and illustrated below by specific examples, it should be understood that the specific examples described herein are only for the purpose of facilitating understanding of the present invention, and are not intended to be specific limitations of the present invention. The raw materials used in the examples of the present invention are those commonly used in the art, and the methods used in the examples are those conventional in the art, unless otherwise specified.
Example 1
The preparation method of the high-performance polyurethane elastomer comprises the following steps:
(1) Uniformly mixing 45 parts of polyethylene glycol adipate and 30 parts of toluene diisocyanate at 25 ℃, and reacting for 4 hours;
(2) Adding 0.1 part of catalyst stannous octoate, 3.0 parts of chain extender 3,3 '-dichloro-4,4' -diaminodiphenylmethane and 6.9 parts of calcium carbonate into the reaction system in the step (1), and uniformly stirring at 25 ℃ for reacting for 4 hours;
(3) Dissolving 2.0 parts of bis (3-triethoxysilylpropyl) amine in 13.0 parts of ethanol, adding into the reaction system in the step (2), and uniformly stirring to remove the solvent to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
Example 2
The preparation method of the high-performance polyurethane elastomer of the embodiment comprises the following steps:
(1) Uniformly mixing 50 parts of polytetrahydrofuran diol and 30 parts of hexamethylene diisocyanate at 80 ℃ and reacting for 1 hour;
(2) Adding 0.05 part of catalyst dibutyltin laurate, 3.0 parts of chain extender glycol and 5.0 parts of silicon dioxide into the reaction system in the step (1), and uniformly stirring at 80 ℃ for reacting for 1h;
(3) Dissolving 1.5 parts of bis (3-triethoxysilylpropyl) amine in 10.5 parts of ethanol, adding into the reaction system in the step (2), uniformly stirring, and removing the solvent to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
Example 3
The preparation method of the high-performance polyurethane elastomer comprises the following steps:
(1) Uniformly mixing 45 parts of polypropylene glycol and 30 parts of toluene diisocyanate at 25 ℃, and reacting for 4 hours;
(2) Adding 0.1 part of catalyst stannous octoate, 8.0 parts of chain extender trimethylolpropane and 5.0 parts of montmorillonite into the reaction system in the step (1), and uniformly stirring at 80 ℃ to react for 1 hour;
(3) Dissolving 1.0 part of bis (3-triethoxysilylpropyl) amine in 9.0 parts of ethanol, adding into the reaction system in the step (2), uniformly stirring, and removing the solvent to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
Example 4
The preparation method of the high-performance polyurethane elastomer comprises the following steps:
(1) Uniformly mixing 70 parts of polybutylene adipate and 15 parts of diphenylmethane diisocyanate at 80 ℃, and reacting for 1 hour;
(2) Adding 0.05 part of catalyst stannous octoate, 8.0 parts of chain extender dimethylthiotoluenediamine and 1.95 parts of talcum powder into the reaction system in the step (1), and stirring uniformly at 80 ℃ for reacting for 1h;
(3) Dissolving 2.0 parts of bis- (3- (triethoxysilane) propyl) -disulfide in 13.0 parts of ethanol, adding into the reaction system in the step (2), uniformly stirring, and removing the solvent to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
Example 5
The preparation method of the high-performance polyurethane elastomer comprises the following steps:
(1) Uniformly mixing 55 parts of polyethylene glycol adipate and 25 parts of isophorone diisocyanate at 60 ℃, and reacting for 2 hours;
(2) Adding 0.1 part of catalyst dibutyltin dioctoate, 5.0 parts of chain extender 1,4-butanediol and 5.0 parts of titanium dioxide into the reaction system in the step (1), and uniformly stirring at 60 ℃ for reacting for 2 hours;
(3) Dissolving 2.0 parts of 1,2-bis (triethoxysilyl) ethane in 13.0 parts of ethanol, adding into the reaction system in the step (2), uniformly stirring, and removing the solvent to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
Example 6
This example differs from example 1 only in that bis (3-triethoxysilylpropyl) amine was added in an amount of 0.1 part in step (3).
Example 7
This example differs from example 1 only in that bis (3-triethoxysilylpropyl) amine was added in an amount of 5.0 parts in step (3).
Comparative example 1
The preparation method of the comparative example polyurethane elastomer comprises the following steps:
(1) Uniformly mixing 45 parts of polyethylene glycol adipate and 30 parts of toluene diisocyanate at 25 ℃, and reacting for 4 hours;
(2) Adding 0.1 part of catalyst stannous octoate, 3.0 parts of chain extender 3,3 '-dichloro-4,4' -diaminodiphenylmethane and 6.9 parts of calcium carbonate into the reaction system in the step (1), and uniformly stirring at 25 ℃ for reacting for 4 hours;
(3) Dissolving 2.0 parts of reactive silica in 13.0 parts of ethanol, adding the mixture into the reaction system in the step (2), and uniformly stirring to remove the solvent to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
Comparative example 2
The preparation method of the polyurethane elastomer of the comparative example comprises the following steps:
(1) Uniformly mixing 45 parts of polyethylene glycol adipate and 30 parts of toluene diisocyanate at 25 ℃, and reacting for 4 hours;
(2) Adding 0.1 part of catalyst stannous octoate, 3.0 parts of chain extender 3,3 '-dichloro-4,4' -diaminodiphenylmethane and 6.9 parts of calcium carbonate into the reaction system in the step (1), and uniformly stirring at 25 ℃ for reacting for 4 hours;
(3) Dissolving 2.0 parts of silane coupling agent KH-550 in 13.0 parts of ethanol, adding into the reaction system in the step (2), uniformly stirring, and removing the solvent to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
Comparative example 3
The preparation method of the polyurethane elastomer of the comparative example comprises the following steps:
(1) Uniformly mixing 45 parts of polyethylene glycol adipate and 30 parts of toluene diisocyanate at 25 ℃, and reacting for 4 hours;
(2) Adding 0.1 part of catalyst stannous octoate, 3.0 parts of chain extender 3,3 '-dichloro-4,4' -diaminodiphenylmethane and 6.9 parts of calcium carbonate into the reaction system in the step (1), and uniformly stirring at 25 ℃ for reacting for 4 hours;
(3) Dissolving 2.0 parts of tetraethoxysilane in 40 parts of ammonia water (27%), adding into the reaction system in the step (2), and heating and stirring at 40 ℃ for 1h to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
Comparative example 4
The preparation method of the polyurethane elastomer of the comparative example comprises the following steps:
(1) Uniformly mixing 45 parts of polyethylene glycol adipate and 30 parts of toluene diisocyanate at 25 ℃, and reacting for 4 hours;
(2) Adding 0.1 part of stannous octoate catalyst, 3.0 parts of chain extender 3,3 '-dichloro-4,4' -diaminodiphenylmethane and 6.9 parts of calcium carbonate into the reaction system in the step (1), uniformly stirring at 25 ℃ for reacting for 4 hours, and removing the solvent to obtain a material to be mixed;
(3) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer, wherein the temperature range of each section of the extruder is 160-220 ℃.
The polyurethane elastomers obtained in the above examples and comparative examples were tested for mechanical properties, water resistance and oil resistance, the water resistance was determined by testing the tensile strength and the elongation at break after being left at 80 ℃ for 168 hours, the oil resistance was determined by testing the tensile strength and the elongation at break after being left at 100 ℃ for 168 hours, and the property data are shown in table 1.
TABLE 1 polyurethane elastomer Properties data Table
Figure BDA0003980034220000071
Figure BDA0003980034220000081
As can be seen from the data in table 1, the polyurethane elastomer obtained in the present application has excellent mechanical properties, hydrolysis resistance and oil resistance. Example 6 when the amount of the bridged siloxane used is too small, the cross-linked network structure formed in the elastomer molding process is small, and the mechanical strength of the obtained polyurethane elastomer is poor; example 7 when the amount of the bridged siloxane is too large, a crosslinked network structure is formed in the elastomer molding process, and the obtained polyurethane elastomer has high mechanical strength, low elongation at break and poor elasticity; comparative examples 1 to 4 were obtained with or without modification with other types of silicon compounds, and the polyurethane elastomers obtained were inferior in mechanical properties, hydrolysis resistance and oil resistance.
Finally, it should be noted that the specific examples described herein are merely illustrative of the spirit of the invention and do not limit the embodiments of the invention. Various modifications, additions and substitutions for the embodiments described herein will occur to those skilled in the art, and all such embodiments are neither required nor possible. While the invention has been described with respect to specific embodiments, it will be appreciated that various changes and modifications may be made without departing from the spirit and scope of the invention, as defined by the appended claims.

Claims (10)

1. A preparation method of a high-performance polyurethane elastomer is characterized by comprising the following steps:
(1) Mixing and heating polymer polyol and polyisocyanate to carry out prepolymerization reaction;
(2) Adding a catalyst and a chain extender into the reaction system in the step (1) for heating reaction;
(3) Adding bridged siloxane into the reaction system in the step (2), and uniformly stirring to obtain a material to be mixed;
(4) And extruding and granulating the materials to be mixed to obtain the high-performance polyurethane elastomer.
2. The method for preparing high-performance polyurethane elastomer according to claim 1, wherein the polymer polyol is one or both of polyester polyol and polyether polyol.
3. The method for preparing high-performance polyurethane elastomer according to claim 1, wherein the polyisocyanate is one or more of toluene diisocyanate, diphenylmethane diisocyanate, isophorone diisocyanate, and hexamethylene diisocyanate.
4. The method for preparing a high-performance polyurethane elastomer according to claim 1, wherein the chain extender is one or both of a diamine chain extender and an alcohol chain extender.
5. The method for preparing the high-performance polyurethane elastomer according to claim 1, wherein the catalyst is one or more of stannous octoate, dibutyltin dioctoate and dibutyltin laurate.
6. The method of claim 1, wherein the bridging siloxane is one or more of bis (3-triethoxysilylpropyl) amine, bis- (3- (triethoxysilyl) propyl) -disulfide, 1,2-bis (triethoxysilyl) ethane.
7. The preparation method of the high-performance polyurethane elastomer according to claim 1, wherein the weight parts of the raw materials are as follows: 45-70 parts of polymer polyol, 15-30 parts of polyisocyanate, 3-8 parts of chain extender, 0.05-0.1 part of catalyst and 0.5-3.0 parts of bridging siloxane.
8. The method for preparing a high-performance polyurethane elastomer according to claim 1, wherein the prepolymerization reaction in the step (1) is carried out at a temperature of 20 to 80 ℃ for 1 to 4 hours.
9. The method for preparing high-performance polyurethane elastomer according to claim 1, wherein the heating reaction in step (2) is carried out at a temperature of 20 to 80 ℃ for 1 to 4 hours.
10. A high-performance polyurethane elastomer obtained by the production method according to claim 1.
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