CN110760047B - Bis-secondary amine containing siloxane group and preparation method and application thereof - Google Patents

Bis-secondary amine containing siloxane group and preparation method and application thereof Download PDF

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CN110760047B
CN110760047B CN201810831487.6A CN201810831487A CN110760047B CN 110760047 B CN110760047 B CN 110760047B CN 201810831487 A CN201810831487 A CN 201810831487A CN 110760047 B CN110760047 B CN 110760047B
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杜秀才
刘赵兴
任树杰
陈杰
方璞
吴鹏超
姜庆梅
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Wanhua Chemical Group Co Ltd
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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Abstract

The invention discloses a bis-secondary amine containing siloxane groups, and a preparation method and application thereof, wherein the bis-secondary amine containing siloxane groups is obtained by one or more than one primary diamine and siloxane containing unsaturated double bonds through Michael addition reaction. The component B of the spray polyurea is prepared by mixing the secondary diamine and the auxiliary agent thereof, and the polyurea material is prepared by mixing and spraying the component A and the component B according to the volume ratio of 1:1, wherein the component A is an isocyanate prepolymer generated by the reaction of polyether polyol and isocyanate. Two active hydrogens of the secondary diamine can react with isocyanate to generate linear polyurea, and siloxane groups can be hydrolyzed to generate Si-O-Si crosslinking points, so that the crosslinking speed of amine and isocyanate is reduced, and the mechanical property of the polyurea material is improved.

Description

Bis-secondary amine containing siloxane group and preparation method and application thereof
Technical Field
The invention relates to the technical field of spray polyurea elastomers, in particular to secondary diamine containing siloxane groups and a preparation method thereof, and a spray polyurea elastomer which is prepared by taking the secondary diamine as a raw material and is moisture-cured and a preparation method thereof.
Background
The spray polyurea elastomer is a novel multifunctional material which is widely applied to the fields of water resistance and corrosion resistance and has excellent waterproof performance, corrosion resistance and wear resistance, overcomes the defects of non-aging resistance, non-exposure, low strength, poor puncture resistance, high requirement on construction environment, slow curing, low construction efficiency and the like of traditional waterproof materials such as asphalt coiled materials, single/double-component polyurethane waterproof coatings, acrylate emulsion waterproof coatings and the like, does not contain a solvent in a raw material system, meets the current environmental protection requirement, and can continuously spray a base material surface with the thickness of more than ten millimeters without sagging.
The spray polyurea technology is introduced from abroad into China, is rapidly developed, is successfully applied to a series of national key projects such as waterproof projects of Jingjin high-speed iron and Jinghu high-speed iron, waterproof and wear-resistant projects of national theater artificial lakes and stands of Beijing Olympic stadiums, and the like, and obtains high evaluation of a construction party and a project party, but the spray polyurea elastomer slowly shows a series of defects along with the passage of time, such as general weather resistance, chemical medium resistance and ultraviolet resistance, low adhesive force to a base material, and polyurea falls off from the surface of the base material after water vapor enters gaps between the base material and the polyurea, and the polyurea has poor toughness, cannot meet the requirements of special environments, and is limited in application and development.
U.S. Pat. No. 5162388 discloses an aliphatic spray polyurea elastomer, which uses alicyclic diamine as a chain extender to improve the physical properties and operational properties of the spray polyurea elastomer, and can improve the performance disadvantage of the traditional spray polyurea with poor ultraviolet aging resistance, but the alicyclic diamine has a fast reaction speed, the viscosity of the mixed raw material is rapidly increased, the wettability to the base material is poor, and finally the adhesion of the polyurea to the base material is poor.
Chinese patent publication CN1817989A discloses a spray polyurea high-strength elastic waterproof coating and a construction method thereof, wherein a component A is a semi-prepolymer synthesized by liquefied diphenyl diisocyanate and/or MDI and polyether polyol, a component B is a combination of amine-terminated polyether, amine chain extender, various fillers and auxiliaries, the tensile strength of the spray polyurea system is 13MPa, the elongation at break is 400%, the tear strength is 49kN/m, and the spray polyurea system has better mechanical properties, but the spray polyurea system is also delaminated from a base material at the later stage.
Chinese patent publication CN105694702A discloses a single-component moisture-curing organosilicon-modified polyurethane waterproof coating, which is prepared by using monohydroxy polydimethylsiloxane and diisocyanate as raw materials, and then dispersing the raw materials with other fillers and auxiliaries at a high speed at room temperature to obtain the single-component moisture-curing organosilicon-modified polyurethane waterproof coating.
The organic silicon has better high and low temperature resistance, weather resistance, oxidation resistance stability and corrosion resistance, so that the organic silicon modified polyurea material can effectively improve the adhesive force, weather resistance and high and low temperature resistance of the polyurea material. At present, the method for introducing organic silicon into polyurea is mainly to physically mix the organic silicon with other diamine in a component B and then spray the mixture, the reaction speed of the A/B mixed component sprayed by the method is too fast, the A/B mixed component is difficult to effectively infiltrate into a base material, the adhesive force is poor, and cross-linking points in the system are carbamido, so that the later-period toughness of the polyurea material is poor.
Disclosure of Invention
In order to overcome the disadvantages and shortcomings of the prior art, the present invention provides a bis-secondary amine containing a siloxane group and a method for preparing the same. Two active hydrogens of the secondary diamine can react with isocyanate to generate linear polyurea, and siloxane groups can be hydrolyzed to generate Si-O-Si crosslinking points, so that the crosslinking speed of amine and isocyanate is reduced, and the mechanical property of the polyurea material is improved.
The invention also aims to provide the application of the bis-secondary amine containing siloxane groups in preparing spray polyurea, which is used as a raw material of the component B to prepare a moisture-cured spray polyurea material.
The invention further aims to provide a moisture-curing spray polyurea elastomer and a preparation method thereof, wherein the curing speed is lower than that of the traditional polyurea, the mixing viscosity of A, B components is lower, A, B components have sufficient time to infiltrate into pores of a base material after being mixed, the infiltration on the base material is better, and the introduction of siloxane improves the adhesive force of the polyurea material to the base material. The novel polyurea material takes-Si-O-Si-as a crosslinking point, so that the toughness of the polyurea material can be obviously improved, and the thermal-oxidative aging resistance of the polyurea material is improved. The moisture-curing spray polyurea material is particularly suitable for the fields of high-speed rail waterproofing and the like.
In order to achieve the above purpose, the technical scheme of the invention is as follows:
a bis-secondary amine containing siloxane groups having the general formula:
(R3O)3SiR2NHR1NHR2Si(OR3)3
(I)
in the formula, R1An ether group selected from C1-C10 alkylene, C3-16 cycloalkylene or C3-C16, preferably C3-12 cycloalkylene, C3-C12 ether; further preferred is R1Comprises the following steps:
Figure BDA0001743597260000031
Figure BDA0001743597260000032
Figure BDA0001743597260000041
R2is selected from C2-C7 alkylene, preferably C2-C3 alkylene;
R3selected from C1-C10 alkyl groups, preferably C1-C2 alkyl groups.
The bis-secondary amine containing siloxane groups is prepared by dripping siloxane containing unsaturated double bonds into one or more than one primary diamine system and carrying out Michael addition reaction at a certain temperature.
Preferably, the method for preparing the above-mentioned siloxane group-containing bis-secondary amine comprises the following steps:
adding one or more than one primary diamine into a reaction kettle provided with a stirrer, a thermometer and an inert gas pipeline, adding a catalyst, stirring at a certain temperature, dropwise adding siloxane containing unsaturated double bonds into the reaction kettle, and continuously reacting under the protection of inert gas to obtain the secondary diamine containing siloxane branched chains. The reaction equation is shown In (IV).
H2N-R1-NH2+2H2C=CH-R4-SiOR3)3→(R3O)3SiR2HN-R1-NHR2Si(OR3)3
(IV)
Among them, the inert protective gas used in the step of preparing the siloxane group-containing bis-secondary amine may be nitrogen, argon, or the like, and nitrogen is preferable in this method.
Wherein the primary diamine used in the step of preparing the siloxane group-containing secondary diamine has the following structure (II):
H2N-R1-NH2
(II)
in the above formula, R1Is composed of
Figure BDA0001743597260000051
Figure BDA0001743597260000052
Figure BDA0001743597260000053
Wherein the unsaturated double bond-containing siloxane used in the step of preparing the bis-secondary amine containing a siloxane group has a structure described by the general formula (III):
CH2=CH-R4-Si(OR3)3
(III)
R4selected from C0-C5 alkylene, preferably C0-C1;
R3selected from C1-C10 alkyl groups, preferably C1-C2. (ii) a
Further, the molar ratio of the unsaturated double bond-containing siloxane to the primary diamine used in the step of preparing the secondary diamine containing a siloxane group is 2.0 to 2.1:1, preferably 2.0 to 2.05: 1.
further, the catalyst used in the step of preparing the siloxane group-containing bis-secondary amine is a basic catalyst such as metallic sodium, sodium ethoxide, sodium hydride, sodium amide, tetraalkylammonium hydroxide, etc., and tetraalkylammonium hydroxide is more preferable.
Further, the catalyst used in the step of preparing the secondary diamine containing a siloxane group is used in an amount of 0.1 to 1% by weight, preferably 0.4 to 0.8% by weight, based on the total amount of the unsaturated double bond-containing siloxane and the primary diamine.
Further, the reaction temperature in the step of preparing the bis-secondary amine containing a siloxane group is 60 ℃ to 90 ℃, preferably 70 ℃ to 80 ℃, and the reaction time is 2 to 4 hours, preferably 3 to 4 hours.
The specific synthetic procedure for the bis-secondary amine containing a siloxane group can be carried out as follows:
in a container equipped with a stirrer, a thermometer and N2Adding one or more than one primary diamine and a catalyst into a reaction kettle of a gas pipeline in a precisely metered manner, accurately weighing the siloxane containing the unsaturated double bond at the temperature of 60-90 ℃, preferably 70-80 ℃, according to the molar ratio of the siloxane containing the unsaturated double bond to the primary diamine of 2.0-2.1:1, preferably 2.0-2.05:1, slowly dripping the siloxane into the reaction kettle, and reacting for 2-4h, preferably 3-4h under the protection of nitrogen to obtain the secondary diamine containing the siloxane group.
Further, the bis-secondary amine containing siloxane groups obtained as described above is mainly used in the B component for preparing moisture-curable spray polyurea. The component B of the spray polyurea is prepared by mixing the secondary diamine and other auxiliary agents, and the moisture-curing spray polyurea elastomer is obtained by mixing and spraying the component A which is an isocyanate prepolymer generated by the reaction of polyol and isocyanate according to the volume ratio of the component A/B of 1: 1.
A moisture-curing spray polyurea elastomer comprises the following formula system:
the component A comprises:
the mass ratio/part is preferable
Isocyanate prepolymer 70-12088-
Diluent 0-305-15
The component B comprises:
Figure BDA0001743597260000061
preferably, the isocyanate prepolymer in the component A is synthesized by reacting polyether polyol and isocyanate, and the-NCO content of the isocyanate prepolymer is 12-20%.
Further, the molecular weight of the polyether polyol in the component A is 200-10000, preferably 400-1000, and the polyether polyol prepared by the ring-opening reaction of dipropylene glycol serving as an initiator and propylene oxide is preferred.
Further, the catalyst required during the synthesis of the isocyanate prepolymer described in the a component is an organotin-based catalyst, preferably dibutyltin dilaurate, and is added in an amount of 0.1% by weight to 0.8% by weight, preferably 0.1% by weight to 0.6% by weight, based on the total amount of the polyether polyol and the isocyanate.
Further, the diluent in the a component is selected from Propylene Carbonate (PC), dioctyl phthalate (DOP) or dibutyl phthalate (DBP), preferably dibutyl phthalate.
Further, the A component in the spray polyurea formula system is one or more of toluene diisocyanate, diphenylmethane diisocyanate, 4 '-dicyclohexylmethane diisocyanate or isophorone diisocyanate, and preferably one or two of 4,4' -dicyclohexylmethane diisocyanate, isophorone diisocyanate and the like.
Wherein, the bis-secondary amine in the component B in the moisture-curing spray polyurea formula is the bis-secondary amine containing siloxane groups synthesized in the invention.
Wherein the dispersant in the B component in the moisture-curing spray polyurea formulation is a fatty acid derivative, such as: one or two of Tego Dispers610, Dispers 630.
Wherein the defoaming agent in the component B in the moisture-curing spray polyurea formula is an organic silicon defoaming agent. Preferably a mixture of one or more of Tego Foamex N, Airex900, Airex 930, Airex 940, Airex 950.
Further, the preparation method of the moisture-curing spray polyurea elastomer comprises the following steps:
preparation of component A:
adding accurately metered polyether polyol into a reaction kettle, vacuumizing and dehydrating for 1-5 hours, preferably 2-3 hours at 80-150 ℃, preferably 90-130 ℃, sampling and measuring the water content, stopping dehydrating when the water content reaches below 0.08 wt%, cooling to 30-80 ℃, preferably 50-70 ℃, maintaining the temperature range, optionally adding a diluent and an organic tin catalyst, dropwise adding accurately metered diisocyanate into the kettle while stirring, continuously reacting for 1-5 hours, preferably 2-4 hours at 70-110 ℃, preferably 80-100 ℃, reducing the temperature after defoaming, obtaining a component A with the NCO content of 12-20 wt%, and cooling and discharging.
Preparation of the component B:
in a container equipped with a stirrer, a thermometer and N2Adding one or more than one primary diamine and catalyst in a reaction kettle of a gas pipeline, dropwise adding siloxane containing unsaturated double bonds in an accurately metered amount under stirring at 60-90 ℃, preferably 70-80 ℃, reacting for 2-4h, preferably 3-4h under the protection of nitrogen to obtain the secondary diamine containing siloxane branched chains. Pouring the secondary diamine, the fumed silica, the dispersing agent and the defoaming agent into a stirring kettle according to a certain ratio, heating to 50-100 ℃, preferably 60-90 ℃, stirring for 30-50min at the rotation speed of 400-1200r/min, preferably 500-1000r/min to obtain a component B;
mixing the component A and the component B according to a volume ratio of 1:1, mixing and spraying to obtain the polyurea elastomer.
In the present invention, the term "optionally added" means addition or non-addition.
The invention has the following beneficial effects:
(1) the moisture-cured spray polyurea elastomer has excellent thermal-oxidative aging resistance.
(2) The moisture-cured spray polyurea elastomer has a slower curing speed than the conventional polyurea and a lower A, B component mixing viscosity.
(3) The moisture-cured spray polyurea elastomer disclosed by the invention has excellent adhesion performance of a cured material to a base material.
(4) The material after being cured has better toughness.
Description of the drawings: FIG. 1 is a NMR spectrum of a bis-secondary amine containing a siloxane group prepared in example 1.
FIG. 2 is a NMR spectrum of a bis-secondary amine containing a siloxane group prepared in example 2.
FIG. 3 is a NMR spectrum of a bis-secondary amine containing siloxane groups prepared in example 3.
FIG. 4 is a NMR spectrum of a bis-secondary amine containing a siloxane group prepared in example 4.
Detailed Description
The present invention is further illustrated by the following specific examples, which are intended to be illustrative only and not to limit the scope of the invention.
The NMR spectra in the examples were obtained from Bruker AVANCE III 400MHz test.
The raw materials and sources are detailed in table 1.
TABLE 1 raw materials and sources
Chemical name Manufacturer of the product
IPDA Wanhua Chemical Group Co., Ltd.
HMDA Wanhua Chemical Group Co., Ltd.
Polyetheramine D230 Henscman chemistry
Vinyl trimethoxy silane Nanjing Union Silicon Chemical Co.,Ltd.
Vinyl triethoxy silane Nanjing Union Silicon Chemical Co.,Ltd.
Fumed silica Jiangsu Hao energy chemical industry Co., Ltd
HMDI Wanhua Chemical Group Co., Ltd.
IPDI Wanhua Chemical Group Co., Ltd.
HDI Wanhua Chemical Group Co., Ltd.
Polyether polyols Optimization chemistry
Dibutyl phthalate SHANGHAI MACKLIN BIOCHEMICAL Co.,Ltd.
1, 3-Cyclohexanediamine Basf-Fr
1, 3-propanediamine SHANGHAI MACKLIN BIOCHEMICAL Co.,Ltd.
Tego Dispers 610 Winning wound
Tego Airex900 Winning wound
Diethyltoluene diamine (DETDA) Jiangsu Vico Teri chemical Co., Ltd
Chain extender clearlink-1000 Dorf KATAL
Example 1
A method of preparing a moisture-curable spray polyurea elastomer comprising:
preparation of component A:
40 parts of polyoxypropylene glycol (N210, Mn 1000) was charged into a reaction vessel, dehydrated at 110 ℃ under a vacuum of 0.09MPa for 3 hours, and then cooled to 60 ℃. Adding 48 parts of isophorone diisocyanate into a reaction kettle with a stirrer and nitrogen protection, adding 5 parts of dibutyl phthalate and 0.1 part of dibutyltin dilaurate, slowly dripping dehydrated polyoxypropylene glycol into the reaction kettle, heating a reaction system to 90 ℃ after dripping is finished, carrying out heat preservation reaction for 3 hours, defoaming, and cooling to obtain an isocyanate prepolymer A component with 15.9% of-NCO content;
preparation of the component B:
in a container equipped with a stirrer, a thermometer and N2Adding 30 parts of isophorone diamine and 0.39 part of tetraalkylammonium hydroxide into a reaction kettle of a gas pipeline, then dropwise adding 67.2 parts of vinyltriethoxysilane into the reaction kettle under stirring at 80 ℃, and continuing to react for 4 hours under the protection of nitrogen after dropwise adding to obtain the bis-secondary amine containing siloxane branches (groups) (the nuclear magnetism characterization result is shown in figure 1, the peak value at the chemical shift delta of 125-140 ppm is reduced, and the Markel addition reaction between double bonds in vinyl siloxane and hydrogen atoms on amino groups is proved to be generated, so that the bis-secondary amine containing siloxane groups is generated). Then 0.5 part of fumed silica, 0.2 part of dispersant Tego Dispers610 and 0.4 part of defoamer Airex900 are poured into a stirring kettle, the temperature is raised to 60 ℃, the stirring is carried out for 30min, and the rotating speed is 1000r/min, so as to obtain a component B;
mixing the component A and the component B according to the volume ratio of 1:1, mixing and spraying to obtain the moisture-cured spraying polyurea elastomer.
Example 2
A method of preparing a moisture-curable spray polyurea elastomer comprising:
preparation of component A:
51.25 parts of polyoxypropylene glycol (N204, Mn. RTM.400) was charged into a reaction vessel, dehydrated at 110 ℃ under a vacuum of 0.09MPa for 3 hours, and then cooled to 60 ℃. Adding 59 parts of hexamethylene diisocyanate into a reaction kettle with a stirrer and nitrogen protection, adding 15 parts of dibutyl phthalate and 0.66 part of dibutyltin dilaurate, slowly dripping dehydrated polyoxypropylene glycol into the reaction kettle, heating a reaction system to 90 ℃ after dripping is finished, carrying out heat preservation reaction for 3 hours, defoaming and cooling to obtain an isocyanate prepolymer A component with 15% of-NCO content;
preparation of the component B:
in a container equipped with a stirrer, a thermometer and N2Adding 46.75 parts of diaminodicyclohexyl methane and 1.12 parts of tetraalkylammonium hydroxide into a reaction kettle of a gas pipeline, then dropwise adding 66 parts of vinyltrimethoxysilane into the reaction kettle under stirring at 80 ℃, and continuing to react for 4 hours under the protection of nitrogen after dropwise adding to obtain the bis-secondary amine containing siloxane branches (a nuclear magnetism characterization result is shown in figure 2, the peak value at the chemical shift delta of 125-140 ppm is reduced, and the Markel addition reaction between double bonds in vinyl siloxane and hydrogen atoms on amine groups is proved to generate the bis-secondary amine containing siloxane groups). Then 0.8 part of fumed silica, 0.6 part of dispersant Tego Dispers610 and 0.7 part of defoamer Airex900 are poured into a stirring kettle, the temperature is raised to 60 ℃, the stirring is carried out for 50min, and the rotating speed is 500r/min, so as to obtain a component B;
mixing the component A and the component B according to the volume ratio of 1:1, mixing and spraying to obtain the moisture-cured spraying polyurea elastomer.
Example 3
A method of preparing a moisture-curable spray polyurea elastomer comprising:
preparation of component A:
37.2 parts of polyoxypropylene glycol (N210, Mn 1000) was charged into a reaction vessel, dehydrated at 110 ℃ under a vacuum of 0.09MPa for 3 hours, and then cooled to 60 ℃. Adding 62.8 parts of dicyclohexylmethane diisocyanate into a reaction kettle with a stirrer and nitrogen protection, adding 10 parts of dibutyl phthalate and 0.4 part of dibutyltin dilaurate, slowly dripping dehydrated polyoxypropylene glycol into the reaction kettle, heating a reaction system to 90 ℃ after dripping is finished, carrying out heat preservation reaction for 3 hours, and cooling after defoaming to obtain an isocyanate prepolymer A component with 15.4% of-NCO content;
preparation of the component B:
in a container equipped with a stirrer, a thermometer and N 215 parts of 1, 3-propanediamine and 0.64 part of tetraalkylammonium hydroxide were added to a gas-line reactor at 80 ℃ CUnder stirring, 77.05 parts of vinyltriethoxysilane is dropwise added into a reaction kettle, and after dropwise addition, reaction is continued for 4 hours under the protection of nitrogen to obtain the bis-secondary amine containing siloxane branches (shown in figure 3 as a nuclear magnetic characterization result, the peak value at the chemical shift delta of 125-140 ppm is reduced, and the result proves that the double bonds in the vinyl siloxane and the hydrogen atoms on the amino groups undergo a Markel addition reaction to generate the bis-secondary amine containing siloxane groups). Then 0.6 part of fumed silica, 0.4 part of dispersant Tego Dispers610 and 0.6 part of defoamer Airex900 are poured into a stirring kettle, the temperature is raised to 60 ℃, the stirring is carried out for 40min, and the rotating speed is 800r/min, so as to obtain a component B;
mixing the component A and the component B according to the volume ratio of 1:1, mixing and spraying to obtain the moisture-cured spraying polyurea elastomer.
Example 4
A method of preparing a moisture-curable spray polyurea elastomer comprising:
preparation of component A:
32 parts of polyoxypropylene glycol (N204, Mn. RTM. 400) was charged into a reaction vessel, dehydrated at 110 ℃ under a vacuum of 0.09MPa for 3 hours, and then cooled to 60 ℃. Adding 58.4 parts of isophorone diisocyanate into a reaction kettle with a stirrer and nitrogen protection, adding 10 parts of dibutyl phthalate and 0.36 part of dibutyltin dilaurate, slowly dripping dehydrated polyoxypropylene glycol into the reaction kettle, heating a reaction system to 90 ℃ after dripping is finished, carrying out heat preservation reaction for 3 hours, defoaming, and cooling to obtain an isocyanate prepolymer A component with 15.3% of-NCO content;
preparation of the component B:
in a container equipped with a stirrer, a thermometer and N2Adding 42 parts of polyetheramine D230 and 0.67 part of tetraalkylammonium hydroxide into a reaction kettle of a gas pipeline, then dropwise adding 54.16 parts of vinyltrimethoxysilane into the reaction kettle while stirring at 80 ℃, and continuing to react for 4 hours under the protection of nitrogen after dropwise adding to obtain bis-secondary amine containing siloxane branched chains (shown in figure 4 as a nuclear magnetic characterization result, the peak value at the chemical shift delta of 125-140 ppm is reduced, which proves that the double bonds in the vinyl siloxane and the hydrogen atoms on the amino groups have the Markel addition reactionA bis-secondary amine containing a siloxane group is generated). Then 0.6 part of fumed silica, 0.4 part of dispersant Tego Dispers610 and 0.5 part of defoamer Airex900 are poured into a stirring kettle, the temperature is raised to 60 ℃, the stirring is carried out for 30min, and the rotating speed is 1000r/min, so as to obtain the component B.
Mixing the component A and the component B according to the volume ratio of 1:1, mixing and spraying to obtain the moisture-cured spraying polyurea elastomer.
Comparative example:
preparation of component A:
32 parts of polyoxypropylene glycol (N204) was charged into a reaction vessel, dehydrated at 110 ℃ under a vacuum of 0.09MPa for 3 hours, and then cooled to 60 ℃. Adding 58.4 parts of isophorone diisocyanate and 0.54 part of dibutyltin dilaurate into a reaction kettle with a stirrer and nitrogen protection, slowly dripping dehydrated polyoxypropylene glycol into the reaction kettle, heating a reaction system to 90 ℃ after dripping is finished, carrying out heat preservation reaction for 3 hours, and cooling after defoaming to obtain an isocyanate prepolymer A component with 17% of-NCO content;
preparation of the component B:
in a container equipped with a stirrer, a thermometer and N2Adding 36 parts of polyetheramine D2000, 16.18 parts of diethyltoluenediamine, 18 parts of clearlink-1000, 0.8 part of fumed silica, 0.5 part of dispersant Tego Dispers610 and 0.7 part of defoamer Airex900 into a reaction kettle of an air pipeline, pouring into a stirring kettle, heating to 60 ℃, stirring for 30min at the rotating speed of 1000r/min, and obtaining a component B;
mixing the component A and the component B according to the volume ratio of 1:1, mixing and spraying to obtain the traditional spraying polyurea elastomer.
The spray polyurea elastomer prepared respectively in the above embodiments is cured for three days in an indoor environment with 23 ℃ and 50% relative humidity, cured for 4 days in a common oven with 50 ℃ to prepare cured sample strips, the sample strips are tested according to corresponding national standards and standards, and then are subjected to thermal oxidation aging for 300 hours at 90 ℃, and then are subjected to performance test and comparison, wherein the test standards are as follows:
the results of the gel time (GB-T12007.7-1989), tensile strength (GB/T528-.
TABLE 2 comparison of spray polyurea elastomer Properties
Figure BDA0001743597260000141
As can be seen from Table 2, compared with the traditional spray polyurea elastomer, the moisture-cured spray polyurea elastomer provided by the invention has longer gel time, better low-temperature resistance, wear resistance, adhesive force and thermal-oxidative aging resistance, and obviously overcomes the defects of poor adhesive force, poor low-temperature resistance and the like of the traditional polyurea, so that the moisture-cured spray polyurea elastomer system provided by the invention has wider application prospect.

Claims (24)

1. Use of a siloxane group-containing bis-secondary amine having the general formula of formula (I):
(R3O)3SiR2NHR1NHR2Si(OR3)3 (I)
in the formula, R1Selected from C3-C10 alkylene, C3-16 cycloalkylene or C3-C16 ether, R2Alkylene selected from C2-C7; r3Selected from C1-C10 alkyl groups.
2. Use according to claim 1, characterized in that, in formula (I), R1Is selected from C3-12 cycloalkylene, C3-C12 ether group; r2Alkylene selected from C2-C3; r3Selected from C1-C2 alkyl groups.
3. Use according to claim 1, characterized in that, in formula (I), R1Comprises the following steps:
Figure FDA0003511776930000011
Figure FDA0003511776930000012
4. use according to any one of claims 1 to 3, the method for preparing a bis-secondary amine containing siloxane groups comprising the following steps: siloxane containing unsaturated double bonds and one or more than one primary diamine are subjected to Michael addition reaction to obtain secondary diamine containing siloxane groups; wherein the primary diamine has a structure described by a general formula (II):
H2N-R1-NH2 (II)
wherein R is1Selected from C3-C10 alkylene, C3-16 cycloalkylene or C3-C16 ether, the unsaturated double bond-containing siloxane has a structure described by the general formula (III):
CH2=CH-R4-Si(OR3)3 (III)
wherein R is4Selected from C0-C5 alkylene; r3Selected from C1-C10 alkyl.
5. Use according to claim 4, characterized in that in formula (II), R1Is selected from C3-12 cycloalkylene, C3-C12 ether group; in the general formula (III), R4Selected from C0-C1 alkylene; r3Selected from C1-C2 alkyl.
6. Use according to claim 4, characterized in that in formula (II), R1Is composed of
Figure FDA0003511776930000021
7. Use according to claim 4, wherein the Michael addition reaction is carried out under an inert gas blanket.
8. Use according to claim 7, characterized in that the inert protective gas is nitrogen, argon.
9. Use according to claim 4, characterized in that the molar ratio of the unsaturated double bond-containing siloxane to the primary diamine is from 2.0 to 2.1:1, the reaction temperature is 60-90 ℃, and the reaction time is 2-4 h.
10. Use according to claim 9, characterized in that the molar ratio of the unsaturated double bond-containing siloxane to the primary diamine is from 2.0 to 2.05: 1; the reaction temperature is 70-80 ℃, and the reaction time is 3-4 h.
11. Use according to claim 4, wherein the Michael addition reaction is carried out under catalysis of a basic compound in an amount of 0.1 wt% to 1 wt%, based on the total amount of the unsaturated double bond-containing siloxane and the primary diamine.
12. Use according to claim 11, characterized in that the basic compound is sodium metal, sodium ethoxide, sodium hydride, sodium amide or tetraalkylammonium hydroxide in an amount of 0.4% to 0.8% by weight, based on the total amount of the unsaturated double bond-containing siloxane and the diprimary amine.
13. Use according to claim 12, characterized in that the basic compound is tetraalkylammonium hydroxide.
14. Use according to claim 1, characterized in that: mixing diamine containing siloxane group and assistant to prepare component B of spray polyurea, and mixing and spraying component A containing isocyanate prepolymer generated by reaction of polyol and isocyanate to obtain the moisture-cured spray polyurea elastomer.
15. Use according to claim 14, characterized in that: and carrying out mixed spraying according to the volume ratio of the A \ B components of 1: 1.
16. Use according to claim 14, characterized in that: the formulation of the moisture-curable spray polyurea elastomer comprises:
the component A comprises:
mass ratio per part
Isocyanate prepolymer 70-120
0-30 of diluent
The component B comprises:
Figure FDA0003511776930000031
17. use according to claim 16, characterized in that: the formulation of the moisture-curable spray polyurea elastomer comprises:
the component A comprises:
mass ratio per part
Isocyanate prepolymer 88-110
Diluent 5-15
The component B comprises:
Figure FDA0003511776930000041
18. use according to any one of claims 14 to 17, characterized in that: the NCO content of the isocyanate prepolymer is 12-20 wt%; the polyol has a number average molecular weight of 200-10000.
19. Use according to claim 18, characterized in that: the polyol is a 400-1000 polyether polyol.
20. Use according to claim 16 or 17, characterized in that: the diluent is selected from one or more of propylene carbonate, dioctyl phthalate and dibutyl phthalate; the dispersing agent is a fatty acid derivative.
21. Use according to claim 20, characterized in that: the diluent is dibutyl phthalate; the dispersing agent is one or two of Tego Dispers610 and Dispers 630.
22. A method for preparing a moisture-curable spray polyurea elastomer, comprising the steps of:
(1) preparation of component A:
adding polyalcohol into a reaction kettle for dehydration, sampling to determine the water content, stopping dehydration when the water content reaches below 0.08 wt%, optionally adding a diluent within the temperature range of 30-80 ℃, dropwise adding diisocyanate into the kettle while stirring, continuously reacting for 1-5 hours within the temperature range of 70-110 ℃ after dropwise adding, defoaming, cooling to obtain a component A, and cooling and discharging;
(2) preparation of the component B:
pouring secondary diamine containing siloxane groups, fumed silica, a dispersing agent and a defoaming agent into a stirring kettle, heating to 50-100 ℃, stirring for 30-50min at the rotation speed of 400-1200r/min to obtain a component B;
(3) mixing the component A and the component B according to a volume ratio of 1:1, mixing and spraying to obtain the polyurea elastomer;
the siloxane group-containing bis-secondary amine is selected from the siloxane group-containing bis-secondary amines of any of claims 1-21.
23. The preparation method according to claim 22, wherein in the step (1), vacuum dehydration is performed for 1 to 5 hours at a temperature of between 80 and 150 ℃, a diluent is optionally added within a temperature range of between 50 and 70 ℃, then diisocyanate is dropwise added into the kettle while stirring, and after the dropwise addition is completed, the reaction is continued for 2 to 4 hours at a temperature range of between 80 and 100 ℃; in the step (2), the temperature is raised to 60-90 ℃, the stirring is carried out for 30-50min, and the rotating speed is 500-.
24. The method according to claim 23, wherein the dehydration is carried out at 90 ℃ to 130 ℃ under vacuum for 2 to 3 hours in the step (1).
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