CN107603230A - Silicon rubber prepared using organosilicon low boiling hydrolysate and preparation method thereof - Google Patents

Silicon rubber prepared using organosilicon low boiling hydrolysate and preparation method thereof Download PDF

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Publication number
CN107603230A
CN107603230A CN201710742448.4A CN201710742448A CN107603230A CN 107603230 A CN107603230 A CN 107603230A CN 201710742448 A CN201710742448 A CN 201710742448A CN 107603230 A CN107603230 A CN 107603230A
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hydrolysate
low boiling
silicon rubber
prepared
organosilicon
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CN201710742448.4A
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CN107603230B (en
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王安营
伊港
毛宁
张振玉
宋超
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SHANDONG DONGYUE SILICON MATERIAL CO Ltd
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SHANDONG DONGYUE SILICON MATERIAL CO Ltd
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Abstract

The invention belongs to silicon rubber preparing technical field, and in particular to a kind of silicon rubber prepared using organosilicon low boiling hydrolysate and preparation method thereof.The silicon rubber prepared using organosilicon low boiling hydrolysate is made up of the raw material of following parts by weight:100 parts of vinyl polysiloxane, 20 60 parts of nano-calcium carbonate, 30 60 parts of organosilicon low boiling hydrolysate, the addition of platinum catalyst are 1 6ppm of raw material gross mass, and the addition of inhibitor is 0.1 6ppm of raw material gross mass.The invention provides a kind of method that no catalyst, low energy consumption utilize organic silicon low-boiling-point substance, under conditions of silicon rubber aging speed is not influenceed, strengthen the mechanical property of silicon rubber, substantially reduce the production cost of silicon rubber.

Description

Silicon rubber prepared using organosilicon low boiling hydrolysate and preparation method thereof
Technical field
The invention belongs to silicon rubber preparing technical field, and in particular to a kind of silicon prepared using organosilicon low boiling hydrolysate Rubber and preparation method thereof.
Background technology
Drastically expand along with domestic methylchlorosilane is production-scale, the yield of its accessory substance organic silicon low-boiling-point substance is also fast Speed increase.The quantity in stock of organic silicon low-boiling-point substance increased dramatically carrys out enormous pressure to environment and safety belt.
During using direct synthesis methylchlorosilane, except target product Me2SiCL2Outside, the organosilicon of meeting by-product about 2% is low Boil thing.Organic silicon low-boiling-point substance refers to silane mixture of the boiling point below 40 DEG C, mainly contains tetramethylsilane (molecular formula:Si (CH3)4), trichlorosilane (molecular formula:SiHCl3), dimethyl dichlorosilane (DMCS) (CH3Cl2SiH), chlorodimethyl silane (molecular formula: Si(CH3)2) and some alkane HCl.Because each component boiling point approaches, it is used it is difficult to separate.
Sun Feng exists《Organic silicon low-boiling-point substance progress》In point out:Organic silicon low-boiling-point substance processing method has two kinds, first, essence Method of purification is evaporated, by chemically or physically acting on, changes iso-amylene and Me2SiHCl boiling-point difference is away from purifying Me2SiMe2SiHCl, The major defect of this technology is to separate these low-boiling-point substance components to need very high fractionating column at present, and energy consumption is very big, and only purifies A kind of important component.Second, redistribution procedure, the principle that redistribution procedure prepares single silane is to utilize being the richest in organic silicon low-boiling-point substance The displacement that Si-Cl and Si-Me occurs with rich chlorine component in methylchlorosilane under high temperature and Louis acid catalysis for base component is reacted, And high-boiling components are made to be cracked into single silane;Disproportionated reaction occurs between the single silane and low-boiling-point substance of cracking, changes into valuable silicon Alkane monomer, such as Me2SiCl2、Me3SiCl, the current major defect of the technique are to need to consume many catalyst, these catalyst It is cleaved product to be covered, recycling rate of waterused is very low, and often completes redistribution reaction under higher temperature, pressure.
The content of the invention
It is an object of the invention to provide a kind of silicon rubber prepared using organosilicon low boiling hydrolysate, both can effectively solve the problem that The Utilizing question of organic silicon low-boiling-point substance, and energy consumption is low, it is not necessary to spent catalyst, can hydrolysis, avoids height at room temperature Temperature and high pressure, and can strengthen the mechanical property of silicon rubber, substantially reduce the production cost of silicon rubber;Present invention simultaneously provides The preparation method of the silicon rubber prepared using organosilicon low boiling hydrolysate, it is scientific and reasonable, simple and easy.
The silicon rubber of the present invention prepared using organosilicon low boiling hydrolysate, by the raw material system of following parts by weight Into:
100 parts of vinyl polysiloxane
Nano-calcium carbonate 20-60 parts
Organosilicon low boiling hydrolysate 30-60 parts,
The addition of platinum catalyst is the 1-6ppm of raw material gross mass, and the addition of inhibitor is raw material gross mass 0.1-6ppm。
The silicon rubber of the present invention prepared using organosilicon low boiling hydrolysate, preferably by the raw material of following parts by weight It is made:
100 parts of vinyl polysiloxane
20 parts of nano-calcium carbonate
30 parts of organosilicon low boiling hydrolysate,
The addition of platinum catalyst is the 1-6ppm of raw material gross mass, and the addition of inhibitor is raw material gross mass 0.1-6ppm。
Described vinyl polysiloxane is one or both of methyl vinyl silicone rubber or vinyl silicone oil, is Commercially available prod.
The preparation method of described organosilicon low boiling hydrolysate is to take organic silicon low-boiling-point substance to be put into 1000mL beakers, Xiang Qi Excessive water is added, after hydrolysis, by the white flock powder of generation and the mixed liquor of water, with Bush's funnel separating and filtering, 100-150 DEG C oven for drying is put into, continued to employ.
Described inhibitor is 1- acetenyl -1- cyclohexanol.
The aobvious alkalescence of nano-calcium carbonate, the acidity of organosilicon low boiling hydrolysate can be neutralized, keep the neutrality of silicon rubber, energy Enough delaying aging speeds.
Described platinum catalyst, inhibitor are commercially available prod.
The preparation method of the silicon rubber of the present invention prepared using organosilicon low boiling hydrolysate, step are as follows:
(1) vinyl polysiloxane is added in mill;
(2) then, add the ground organosilicon low boiling hydrolysate of drying and nano-calcium carbonate be kneaded uniformly, then add Enter platinum catalyst, inhibitor mixing uniformly, discharging, make semisolid elastomeric compound, place;Can hydrolyze organosilicon low boiling The acidity of thing and the alkalescence of nano-calcium carbonate, neutralization reaction is thorough, silicone rubber products is turned into neutrality, after not influenceing silicon rubber Service life or do not change the aging speed of silicon rubber;
(3) vulcanization tabletting and test are finally carried out in 150 DEG C on vulcanizing press;
Described vinyl polysiloxane is methyl vinyl silicone rubber.
The temperature of mill described in step (1) is 40 DEG C.
The particle diameter of grinding described in step (2) is 0.01-10 μm.
Standing time described in step (2) is 12h.
The preparation method of the silicon rubber of the present invention prepared using organosilicon low boiling hydrolysate, step are as follows:
(1) vinyl polysiloxane is added in the stirred tank of planetary mixer at room temperature;
(2) add and dry ground organosilicon low boiling hydrolysate and nano-calcium carbonate, be uniformly mixed, add platinum Au catalyst, inhibitor, are uniformly mixed, and discharge, and place;The acidity and nano-calcium carbonate of organosilicon low boiling hydrolysate can be made The alkalescence of calcium, neutralization reaction is thorough, silicone rubber products is turned into neutrality, does not influence the later service life of silicon rubber or do not change The aging speed of silicon rubber;
(3) natural levelling in mould is finally poured into carry out vulcanizing tabletting and test in 150 DEG C;
Described vinyl polysiloxane is vinyl silicone oil.
The particle diameter of grinding described in step (2) is 0.01-10 μm, standing time 12h.
The present invention need not add crosslinking agent, because containing the Si -- H bond that can be crosslinked in organosilicon low boiling hydrolysate.
The cross-linking agent that white is obtained after organic silicon low-boiling-point substance is hydrolyzed is separated, the white cross-linking agent density very little, Present powdered, therefore, may be used as the filler of silicon rubber, the production cost of silicon rubber can be substantially reduced, improve silicon rubber Mechanical property, solve the Utilizing question of organic silicon low-boiling-point substance, in machine silicon low-boiling-point substance, most of chlorosilane such as trichlorosilane (SiHCl3), dimethyl dichlorosilane (DMCS) (CH3Cl2SiH), the chlorosilane of diformazan one (Si (CH3)2HCl) can be hydrolyzed, after hydrolysis Cross-linking agent can be easily separated, safe, energy consumption is low, and does not need spent catalyst, at room temperature can hydrolyze, avoid High-temperature and high pressure.At present, organosilicon low boiling hydrolyses applying is used as filler, had not been reported into silicon rubber.
The present invention compared with prior art, has the advantages that:
1st, a kind of no catalyst is provided, the method that low energy consumption utilizes organic silicon low-boiling-point substance.
2nd, under conditions of silicon rubber aging speed is not influenceed, strengthen the mechanical property of silicon rubber, substantially reduce silicon rubber Production cost.
Embodiment
The present invention is described further with reference to embodiments.
Embodiment 1
It is prepared by organosilicon low boiling hydrolysate:500g organic silicon low-boiling-point substances are taken to be put into 1000mL beakers, it is excessive to its addition Water, the chlorosilane that at this moment organic silicon low-boiling-point substance contains include trichlorosilane, dimethyl dichlorosilane (DMCS), chlorodimethyl silane hydrolysis Afterwards, further crosslinking, forms the white flock powder of density very little, and the white flock powder is mainly to be obtained after Si-Cl is hydrolyzed Si-OH, Si-OH continue what is be cross-linked to form under sour environment, by the white flock powder of generation and the mixed liquor of water, use Bush Funnel separating and filtering, 100 DEG C are put into oven for drying, continue to employ.
It is 40 DEG C by mill temperature setting, 90 parts of methyl vinyl silicone rubbers is added in mill, add 10 Part vinyl silicone oil, adds 60 parts ground of organosilicon low boiling hydrolysate of drying and 60 parts of nano-calcium carbonate be kneaded Even, the addition of platinum catalyst is the 1ppm of raw material gross mass, and the addition of inhibitor is the 0.1ppm of raw material gross mass, is mixed Refining is uniform, discharging, makes semisolid elastomeric compound, places 12h, can make the acidity and nano-calcium carbonate of organosilicon low boiling hydrolysate The alkalescence of calcium, neutralization reaction is thorough, silicone rubber products is turned into neutrality, does not influence the later service life of silicon rubber or do not change The aging speed of silicon rubber, finally carry out vulcanizing tabletting and test in 150 DEG C on vulcanizing press.
Embodiment 2
It is prepared by organosilicon low boiling hydrolysate:500g organic silicon low-boiling-point substances are taken to be put into 1000mL beakers, it is excessive to its addition Water, the chlorosilane that at this moment organic silicon low-boiling-point substance contains include trichlorosilane, dimethyl dichlorosilane (DMCS), chlorodimethyl silane hydrolysis Afterwards, further crosslinking, forms the white flock powder of density very little, and the white flock powder is mainly to be obtained after Si-Cl is hydrolyzed Si-OH, Si-OH continue what is be cross-linked to form under sour environment, by the white flock powder of generation and the mixed liquor of water, use Bush Funnel separating and filtering, 150 DEG C are put into oven for drying, continue to employ.
It is 40 DEG C by mill temperature setting, 100 parts of methyl vinyl silicone rubbers is added in mill;Then, add Enter to dry 30 parts of ground organosilicon low boiling hydrolysate and 20 parts of nano-calcium carbonate be kneaded uniformly, platinum catalyst adds Enter the 6ppm that amount is raw material gross mass, the addition of inhibitor is the 1ppm of raw material gross mass, is kneaded uniformly, discharging, makes half The elastomeric compound of solid, 12h is placed, the acidity of organosilicon low boiling hydrolysate and the alkalescence of nano-calcium carbonate, neutralization reaction can be made Thoroughly, silicone rubber products is turned into neutrality, do not influence the later service life of silicon rubber or do not change the aging speed of silicon rubber, Finally carry out vulcanizing tabletting and test in 150 DEG C on vulcanizing press.
Embodiment 3
It is prepared by organosilicon low boiling hydrolysate:500g organic silicon low-boiling-point substances are taken to be put into 1000mL beakers, it is excessive to its addition Water, the chlorosilane that at this moment organic silicon low-boiling-point substance contains include trichlorosilane, dimethyl dichlorosilane (DMCS), chlorodimethyl silane hydrolysis Afterwards, further crosslinking, forms the white flock powder of density very little, and the white flock powder is mainly to be obtained after Si-Cl is hydrolyzed Si-OH, Si-OH continue what is be cross-linked to form under sour environment, by the white flock powder of generation and the mixed liquor of water, use Bush Funnel separating and filtering, 120 DEG C are put into oven for drying, continue to employ.
100 parts of vinyl silicone oils are added in the stirred tank of planetary mixer at room temperature, addition drying is ground to be had 40 parts of 45 parts of machine silicon low boiling hydrolysate and nano-calcium carbonate, are uniformly mixed, the addition of platinum catalyst is the total matter of raw material The 1ppm of amount, the addition of inhibitor are the 6ppm of raw material gross mass, are uniformly mixed, discharge, place 12h, can make to have The acidity of machine silicon low boiling hydrolysate and the alkalescence of nano-calcium carbonate, neutralization reaction is thorough, silicone rubber products is turned into neutrality, not shadow Ring the later service life of silicon rubber or do not change the aging speed of silicon rubber, finally pour into mould natural levelling in 150 DEG C Carry out vulcanizing tabletting and test.
The tensile strength of product test sample and elongation at break are tested according to GB/T528-1998 made from embodiment 1-3, Tearing strength is tested according to GB/T529-1999, and hardness is tested according to GB/T531-1999.Test result is shown in Table 1.
Product test result made from the embodiment 1-3 of table 1

Claims (10)

1. a kind of silicon rubber prepared using organosilicon low boiling hydrolysate, it is characterised in that by the raw material system of following parts by weight Into:
100 parts of vinyl polysiloxane
Nano-calcium carbonate 20-60 parts
Organosilicon low boiling hydrolysate 30-60 parts,
The addition of platinum catalyst is the 1-6ppm of raw material gross mass, and the addition of inhibitor is the 0.1- of raw material gross mass 6ppm。
2. the silicon rubber according to claim 1 prepared using organosilicon low boiling hydrolysate, it is characterised in that described second Alkenyl polysiloxanes is one or both of methyl vinyl silicone rubber or vinyl silicone oil.
3. the silicon rubber according to claim 1 prepared using organosilicon low boiling hydrolysate, it is characterised in that described has The preparation method of machine silicon low boiling hydrolysate is to take organic silicon low-boiling-point substance to be put into 1000mL beakers, and excessive water, hydrolysis are added to it Afterwards, by the white flock powder of generation and the mixed liquor of water, with Bush's funnel separating and filtering, 100-150 DEG C is put into oven for drying, Continue to employ.
4. the silicon rubber according to claim 1 prepared using organosilicon low boiling hydrolysate, it is characterised in that described suppression Preparation is 1- acetenyl -1- cyclohexanol.
5. a kind of preparation method of any described silicon rubber prepared using organosilicon low boiling hydrolysate of claim 1-4, its It is characterised by that step is as follows:
(1) vinyl polysiloxane is added in mill;
(2) then, add the ground organosilicon low boiling hydrolysate of drying and nano-calcium carbonate be kneaded uniformly, add platinum Au catalyst, inhibitor are kneaded uniformly, discharging, make semisolid elastomeric compound, are placed;
(3) vulcanization tabletting and test are finally carried out in 150 DEG C on vulcanizing press;
Described vinyl polysiloxane is methyl vinyl silicone rubber.
6. the preparation method of the silicon rubber according to claim 5 prepared using organosilicon low boiling hydrolysate, its feature are existed The temperature of mill described in step (1) is 40 DEG C.
7. the preparation method of the silicon rubber according to claim 5 prepared using organosilicon low boiling hydrolysate, its feature are existed The particle diameter of grinding described in step (2) is 0.01-10 μm.
8. the preparation method of the silicon rubber according to claim 5 prepared using organosilicon low boiling hydrolysate, its feature are existed Standing time described in step (2) is 12h.
9. a kind of preparation method of any described silicon rubber prepared using organosilicon low boiling hydrolysate of claim 1-4, its It is characterised by that step is as follows:
(1) vinyl polysiloxane is added in the stirred tank of planetary mixer at room temperature;
(2) add and dry ground organosilicon low boiling hydrolysate and nano-calcium carbonate, be uniformly mixed, add platinum and urge Agent, inhibitor, are uniformly mixed, and discharge, and place;
(3) natural levelling in mould is finally poured into carry out vulcanizing tabletting and test in 150 DEG C;
Described vinyl polysiloxane is vinyl silicone oil.
10. the preparation method of the silicon rubber according to claim 9 prepared using organosilicon low boiling hydrolysate, its feature are existed The particle diameter of grinding described in step (2) is 0.01-10 μm, standing time 12h.
CN201710742448.4A 2017-08-25 2017-08-25 Silicone rubber prepared by using organosilicon low-boiling hydrolysate and preparation method thereof Active CN107603230B (en)

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