CN100355792C - Method for synthesizing homopolymer and copolymers in alcohol-water system - Google Patents
Method for synthesizing homopolymer and copolymers in alcohol-water system Download PDFInfo
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Abstract
The present invention belongs to the synthetic field of high molecular polymers, which relates to a synthetic method for homopolymers and copolymers in an alcohol-water system. A mixture of C1-C3 alcohol and water is adopted as a reaction medium. Under the action of emulsifying agents, auxiliary emulsifying agents, initiating agents, an amount of stabilizing agents and plasticizing agents, a polymer monomer or a mixed monomer is synthesized into homopolymers and copolymers in a reaction kettle at the temperature of 30 to 80 DEG C through the steps of raw material mixing, alcohol addition, polymerization reaction and separation. The method synthesizes the advantages of suspension polymerization and emulsion polymerization by high molecular synthesis and is suitable for preparing polymer powder and polymer emulsions. The auxiliary agents have few use kinds and dosages, and product quality is good. The synthetic method uses the action of low molecular weight alcohol to efficiently control product performance by changing the concentration of reaction materials, the ratio of alcohol/water, reaction temperature and reaction time. Reaction processes are easy to control. The synthetic method has especially and obviously effects on preventing implosion and increases the safety and the reliability of production.
Description
Technical field
The present invention relates to the synthetic field of high molecular polymer, the synthetic method of particularly a kind of homopolymerization and multipolymer.
Background technology
Synthetic main at present the adopt suspension polymerization and the emulsion polymerization of vinylidene chloride homopolymerization and multipolymer, suspension polymerization generally is used to produce Powdered vinylidene chloride homopolymerization and multipolymer, vinylidene chloride homopolymerization of letex polymerization production emulsus and multipolymer.In patent 02141005.4 (application number), describe the method for the synthetic vinylidene chloride polymer of a kind of suspension polymerization, still belonged to the extension of conventional suspension polymerization method.It has described the synthetic method and the technology of a kind of vinylbenzene, divinyl, vinylchlorid, vinyl acetate, vinylidene chloride, (methyl) alkyl acrylate, (methyl) vinylformic acid, (methyl) vinyl cyanide and (methyl) acrylamide homopolymerization and multipolymer, wherein still use water as solvent, auxiliary agents such as emulsifying agent and dispersion agent have been used, adopt seed to control the size and the distribution of particle, therefore also the method for its use can be belonged to emulsion polymerisation process.DEA2332637 has also announced a kind of emulsion polymerisation process of the butadienecopolymer more than 115 ℃, but hot conditions can influence performance such as molecular weight distribution, the particle size distribution etc. of product.Adopt to suspend and the main drawback of emulsion polymerisation process is relatively stricter to the requirement of operational condition, bad if condition is controlled, be easy to generate implode, influence the molecular weight of quality and performance, particularly product of product and the distribution of size of particles.In ZL97121466.2, utilize new technology and technology, as if obtained result preferably.But technology, equipment is relative complex again.In patent EPA0486262, EPA0608567 and DEA4442577, described corresponding suspension polymerization and emulsion polymerization technique,, be difficult to be applied to large-scale commercial production owing to technology, equipment.
Summary of the invention
The object of the present invention is to provide that a kind of quality product and production process are controlled easily, temperature of reaction is low and equipment is simple and is easy to the synthetic method of homopolymerization and multipolymer in the alcohol-water system of large-scale commercial production.
The technical solution adopted for the present invention to solve the technical problems is: the synthetic method of homopolymerization and multipolymer in a kind of alcohol-water system is provided, and is to adopt C
1-C
3Alcohol and the mixture of water be as reaction medium, and under emulsifying agent and assistant for emulsifying agent, initiator and an amount of stablizer and softening agent effect, polymer monomer or mix monomer synthesize homopolymerization or multipolymer in reactor, and comprise the steps:
A, raw material mix: with the emulsifying agent of the water of the polymer monomer of 10%～80% quality or mix monomer, 19%～89% quality, 0.5%～5% quality with the initiator of assistant for emulsifying agent, 0.2%～3% quality and an amount of stablizer and softening agent stirring and emulsifying fast in mixing tank;
B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still by the valve switching, and adding is 5%～60% C in the water mass percent under stirring fast in reactor
1-C
3Alcohol;
C, polyreaction: behind rare gas element such as nitrogen purging, be heated to 30 ℃～80 ℃ reactions 1～3 hour in the reactor;
D, separation: reaction product enters carries out in the pure water separator separating of polymerisate and alcohol and unreacted monomer, the alcohol water separator is common separation column or flashing tower, alcohol and unreacted monomer distillate from the top, return the reactor recycling through recycle pump, product is milk sap or suspension, and suspension can get polymer powder after centrifugal, washing, drying.
Wherein, described polymer monomer is the one or more kinds of mixtures in vinylidene chloride, vinylbenzene, divinyl, vinylchlorid, vinyl acetate, alkyl acrylate, alkyl methacrylate, vinylformic acid, methacrylic acid, vinyl cyanide, methacrylonitrile, acryloyl and the Methacrylamide, and the mass content of principal monomer accounts for the 50%-100% of polymer monomer total amount in the mixed with polymers monomer.Described emulsifying agent is an anion surfactant, comprises the one or more kinds of mixtures in dodecyl sulfate, dodecylbenzene sulfonate and the dodecyl polyoxyethylene ether sulfate; Assistant for emulsifying agent is C
14-C
22Alkanol.Described C
1-C
3Alcohol is the one or more kinds of mixtures in propyl alcohol, Virahol, ethanol and the methyl alcohol.
The controlled polymerization reaction product polymerization degree of the present invention and and the principle of molecular weight aspect be: the mixture that adopts low-molecular-weight alcohol and water is as polymerization reaction medium, different with water as the reaction system of solvent, by in the emulsion of reactant and water, adding low-molecular-weight alcohol, owing to low-molecular-weight alcohol can not with former emulsion further emulsification formation alcohol, water, reactant emulsification system, the adding of alcohol has destroyed the continuity of former emulsion, can play iris action, stop excessively carrying out of polyreaction, prevent implode thereby reach, the effect of control molecular weight of product.Major equipment comprises mixing tank, the reactor more than, a pure water separator of cover and a recycle pump in the inventive method, switches by valve and can realize polymkeric substance intermittence or semi-continuous production.
The invention has the advantages that:
1, utilizes C
1-C
3The effect of low-molecular-weight alcohol, just can control product property by changing reactant concn, alcohol/water effectively than, temperature of reaction and time, operating procedure is simple, and reaction process is easy to control, particularly very obvious for preventing the implode effect, improved the security and the reliability of producing.
2, suitability of the present invention is wide, can be used for improving comprising synthetic vinylidene chloride, vinylbenzene, divinyl, vinylchlorid, vinyl acetate, (methyl) alkyl acrylate, (methyl) vinylformic acid, (methyl) vinyl cyanide and (methyl) acrylamide homopolymerization and the nearly all suspension polymerization of multipolymer and the production technique of emulsion polymerization systems.
3, employed C in the reaction process
1-C
3Low-molecular-weight alcohol can separate in pure water separator and recycles in the final stage of reaction, when temperature of reaction reaches more than 60 ℃, can utilize the coronite separation of residual heat of reaction limit during separation, and the sepn process energy consumption is lower.
4, the present invention combines the advantage of Polymer Synthesizing suspension polymerization and letex polymerization, both has been applicable to the production polymer powder, also is suitable for producing polymer emulsion, and auxiliary agent use kind and consumption are few, good product quality.
5, in the technology involved in the present invention, adopt a plurality of reactor parallel operations, the switching by the reactor input and output material can realize serialization production.
The invention will be further described below in conjunction with embodiment and accompanying drawing.
Description of drawings
Accompanying drawing 1: the synthesis process flow diagram of homopolymerization and multipolymer in the alcohol-water system.
Among the figure: 1, reactor, 2, mixing tank, 3, pure water separator, 4, recycle pump.
Embodiment
Embodiment 1.a, raw material mix: the mix monomer double centner of vinylidene chloride mass content 80%, vinylchlorid mass content 20% is mixed with double centner water, form the mixed system of total monomer quality mark 50%, the sodium lauryl sulphate, 1% cetyl alcohol, 1% ammonium persulphate and the S-WAT that add quality 2% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the ethanol of water quality 5% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 2 hours in the reactor (1) at 50 ℃.D, separation: reaction product gets vinylidene chloride, vinyl chloride copolymer emulsion after pure water separator (3) is isolated ethanol and unreacted monomer, yield 98%, molecular weight of copolymer 320,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, ethanol and unreacted monomer distillate from the top, return reactor (1) recycling through recycle pump (4).
Embodiment 2.a, raw material mix: the mix monomer double centner of vinylidene chloride mass content 90%, vinylchlorid mass content 10% is mixed with double centner water, form the mixed system of total monomer quality mark 50%, the sodium lauryl sulphate, 1% cetyl alcohol, 1% ammonium persulphate and the S-WAT that add quality 2% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the ethanol of water quality 20% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 2 hours in the reactor (1) at 80 ℃.D, separation: reaction product gets vinylidene chloride, vinyl chloride copolymer suspension after pure water separator (3) is isolated ethanol and unreacted monomer, get copolymer powder after the centrifugation, yield 97%, molecular weight of copolymer 280,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, and ethanol and unreacted monomer distillate from the top, returns reactor (1) recycling through recycle pump (4).
Embodiment 3.a, raw material mix: the mix monomer double centner of vinylidene chloride mass content 80%, vinylbenzene mass content 20% is mixed with 233 kg water, form the mixed system of total monomer quality mark 30%, the sodium lauryl sulphate, 2% cetyl alcohol, 0.2% ammonium persulphate and the S-WAT that add quality 1% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the methyl alcohol of water quality 5% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 3 hours in the reactor (1) at 50 ℃.D, separation: reaction product gets vinylidene chloride, styrol copolymer emulsion after pure water separator (3) is isolated methyl alcohol and unreacted monomer, yield 98%, molecular weight of copolymer 310,000, no implode phenomenon in the reaction, alcohol water separator (3) is common flashing tower, methyl alcohol and unreacted monomer distillate from the top, return reactor (1) recycling through recycle pump (4).
Embodiment 4.a, raw material mix: the mix monomer double centner of vinylidene chloride mass content 90%, vinylbenzene mass content 10% is mixed with double centner water, form the mixed system of total monomer quality mark 50%, the sodium lauryl sulphate, 1% cetyl alcohol, 1% ammonium persulphate and the S-WAT that add quality 2% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the ethanol of water quality 40% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 3 hours in the reactor (1) at 70 ℃.D, separation: reaction product gets vinylidene chloride, styrol copolymer emulsion after pure water separator (3) is isolated ethanol and unreacted monomer, yield 98%, molecular weight of copolymer 360,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, ethanol and unreacted monomer distillate from the top, return reactor (1) recycling through recycle pump (4).
Embodiment 5.a, raw material mix: 107 kilograms of the mix monomers of vinylidene chloride mass content 80%, vinylchlorid mass content 20% are mixed with 893 kg water, form the mixed system of total monomer quality mark 10.7%, the sodium lauryl sulphate, 0.2% cetyl alcohol, 3% ammonium persulphate and the S-WAT that add quality 0.3% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the propyl alcohol of water quality 20% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 1 hour in the reactor (1) at 80 ℃.D, separation: reaction product gets vinylidene chloride, vinyl chloride copolymer emulsion after pure water separator (3) is isolated propyl alcohol and unreacted monomer, yield 98%, molecular weight of copolymer 250,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, propyl alcohol and unreacted monomer distillate from the top, return reactor (1) recycling through recycle pump (4).
Embodiment 6.a, raw material mix: the mix monomer double centner of vinylidene chloride mass content 60%, methyl methacrylate mass content 40% is mixed with double centner water, form the mixed system of total monomer quality mark 50%, the sodium lauryl sulphate, 2% cetyl alcohol, 1% ammonium persulphate and the S-WAT that add quality 3% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the ethanol of water quality 5% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 2 hours in the reactor (1) at 50 ℃.D, separation: reaction product gets vinylidene chloride, methylmethacrylate copolymer emulsion after pure water separator (3) is isolated ethanol and unreacted monomer, yield 98%, molecular weight of copolymer 320,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, ethanol and unreacted monomer distillate from the top, return reactor (1) recycling through recycle pump (4).
Embodiment 7.a, raw material mix: the mix monomer double centner of vinylidene chloride mass content 90%, methyl methacrylate mass content 10% is mixed with 25 kg water, form the mixed system of total monomer quality mark 80%, the sodium lauryl sulphate, 2% cetyl alcohol, 1% ammonium persulphate and the S-WAT that add quality 2% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the methyl alcohol of water quality 30% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 2 hours in the reactor (1) at 80 ℃.D, separation: reaction product gets vinylidene chloride, methylmethacrylate copolymer suspension after pure water separator (3) is isolated methyl alcohol and unreacted monomer, get copolymer powder after the centrifugation, yield 98%, molecular weight of copolymer 270,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, and methyl alcohol and unreacted monomer distillate from the top, and the methyl alcohol of separating returns reactor (1) recycling through recycle pump (4).
Embodiment 8.a, raw material mix: 120 kilograms of the mix monomers of vinylidene chloride mass content 50%, vinyl cyanide mass content 50% are mixed with 80 kg water, form the mixed system of total monomer quality mark 60%, the Sodium dodecylbenzene sulfonate, 1% cetyl alcohol, 1% ammonium persulphate and the S-WAT that add quality 1% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the Virahol of water quality 10% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 3 hours in the reactor (1) at 30 ℃.D, separation: reaction product gets vinylidene chloride, acrylonitrile copolymer emulsion after pure water separator (3) is isolated Virahol and unreacted monomer, get copolymer powder after the centrifugation, yield 98%, molecular weight of copolymer 300,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, and Virahol and unreacted monomer distillate from the top, returns reactor (1) recycling through recycle pump (4).
Embodiment 9.a, raw material mix: vinylidene chloride mass content 100% monomer double centner is mixed with 150 kg water, form the mixed system of total monomer quality mark 40%, add the Sodium dodecylbenzene sulfonate of quality 2% and sodium dodecyl sulfate mixture, 1% cetyl alcohol, 2% ammonium persulphate and S-WAT as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the methyl alcohol of water quality 60% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 3 hours in the reactor (1) at 70 ℃.D, separation: reaction product gets vinylidene chloride homopolymer suspension after pure water separator (3) is isolated methyl alcohol and unreacted monomer, get copolymer powder after the centrifugation, yield 98%, molecular weight of copolymer 220,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, and methyl alcohol and unreacted monomer distillate from the top, returns reactor (1) recycling through recycle pump (4).
Embodiment 10.a, raw material mix: 120 kilograms of the mix monomers of vinylidene chloride mass content 80%, vinyl cyanide mass content 10% and acrylamide mass content 10% are mixed with 80 kg water, form the mixed system of total monomer quality mark 60%, the dodecyl polyethenoxy ether sodium sulfate, 1% cetyl alcohol, 1% ammonium persulphate and the S-WAT that add quality 1% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the ethanol of water quality 40% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 2 hours in the reactor (1) at 70 ℃.D, separation: reaction product gets vinylidene chloride, vinyl cyanide and acrylamide copolymer suspension after pure water separator (3) is isolated ethanol and unreacted monomer, get copolymer powder after the centrifugation, yield 97%, molecular weight of copolymer 170,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, and ethanol and unreacted monomer distillate from the top, returns reactor (1) recycling through recycle pump (4).
Embodiment 11.a, raw material mix: 120 kilograms of the mix monomers of vinylidene chloride mass content 80% and divinyl mass content 20% are mixed with 80 kg water, form the mixed system of total monomer quality mark 60%, the sodium lauryl sulphate, 2% V-1326,1% ammonium persulphate and the S-WAT that add quality 3% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is in the propyl alcohol of water quality 10% under stirring fast in reactor.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 1 hour in the reactor (1) at 80 ℃.D, separation: reaction product gets vinylidene chloride and butadienecopolymer emulsion after pure water separator (3) is isolated propyl alcohol and unreacted monomer, yield 98%, molecular weight of copolymer 330,000, no implode phenomenon in the reaction, alcohol water separator (3) is common flashing tower, propyl alcohol and unreacted monomer distillate from the top, return reactor (1) recycling through recycle pump (4).
Embodiment 12.a, raw material mix: the mix monomer double centner of vinylidene chloride mass content 80% and vinyl acetate mass content 20% is mixed with double centner water, form the mixed system of total monomer quality mark 50%, the sodium lauryl sulphate, 1% cetyl alcohol, 3% ammonium persulphate and the S-WAT that add quality 2% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, add alcohol: above-mentioned mixing raw material is switched by valve send into chuck reacting by heating still (1), add propyl alcohol under in reactor, stirring fast: the alcohol mixture of ethanol=1: 1 (volume) in water quality 50%.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 3 hours in the reactor (1) at 50 ℃.D, separation: reaction product gets vinylidene chloride and butadienecopolymer suspension after pure water separator (3) is isolated alcohol mixture and unreacted monomer, get copolymer powder after the centrifugation, yield 98%, molecular weight of copolymer 280,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, and alcohol mixture and unreacted monomer distillate from the top, returns reactor (1) recycling through recycle pump (4).
Embodiment 13.a, raw material mix: the mix monomer double centner of vinylbenzene mass content 90% and methacrylic ester mass content 10% is mixed with double centner water, form the mixed system of total monomer quality mark 50%, the sodium lauryl sulphate, 1% cetyl alcohol, 0.5% ammonium persulphate and the S-WAT that add quality 3% be as initiator and an amount of stablizer and softening agent, quick stirring and emulsifying in mixing tank (2).B, add alcohol: above-mentioned mixing raw material is switched by valve send into chuck reacting by heating still (1), add methyl alcohol under in reactor, stirring fast: the alcohol mixture of ethanol=1: 1 (volume) in water quality 50%.C, polyreaction: behind rare gas element such as nitrogen purging, reacted 2 hours in the reactor (1) at 70 ℃.D, separation: reaction product gets vinylbenzene and methacrylic ester copolymer emulsion after pure water separator (3) is isolated alcohol mixture and unreacted monomer, yield 97%, molecular weight of copolymer 280,000, no implode phenomenon in the reaction, alcohol water separator (3) is common separation column, alcohol mixture and unreacted monomer distillate from the top, return reactor (1) recycling through recycle pump (4).
Claims (6)
1, the synthetic method of homopolymerization and multipolymer in a kind of alcohol-water system is characterized in that adopting C
1-C
3Alcohol and the mixture of water be as reaction medium, and under emulsifying agent and assistant for emulsifying agent, initiator and an amount of stablizer and softening agent effect, polymer monomer or mix monomer synthesize homopolymerization or multipolymer in reactor (1), and comprise the steps:
A, raw material mix: with the emulsifying agent of the water of the polymer monomer of 10%～80% quality or mix monomer, 19%～89% quality, 0.5%～5% quality with the initiator of assistant for emulsifying agent, 0.2%～3% quality and an amount of stablizer and softening agent stirring and emulsifying fast in mixing tank (2);
B, interpolation alcohol: above-mentioned mixing raw material is sent into chuck reacting by heating still (1) by the valve switching, and adding is 5%～60% C in the water mass percent under stirring fast in reactor (1)
1-C
3Alcohol;
C, polyreaction: after inert nitrogen gas purges, be heated to 30 ℃～80 ℃ reactions 1～3 hour in the reactor (1);
D, separation: reaction product enters carries out in the pure water separator (3) separating of polymerisate and alcohol, alcohol water separator (3) is common separation column, alcohol distillates from the top, and the alcohol of separating returns the reactor recycling through recycle pump (4), and product is milk sap or suspension.
2, the synthetic method of homopolymerization and multipolymer in the alcohol-water system according to claim 1 is characterized in that polymer monomer is the one or more kinds of mixtures in vinylidene chloride, vinylbenzene, divinyl, vinylchlorid, vinyl acetate, alkyl acrylate, alkyl methacrylate, vinylformic acid, methacrylic acid, vinyl cyanide, methacrylonitrile, acryloyl and the Methacrylamide.
3, the synthetic method of homopolymerization and multipolymer in the alcohol-water system according to claim 1 and 2 is characterized in that the mass content of principal monomer in the mixed with polymers monomer accounts for the 80%-100% of polymer monomer total amount.
4, the synthetic method of homopolymerization and multipolymer in the alcohol-water system according to claim 1 is characterized in that emulsifying agent is an anion surfactant.
5, the synthetic method of homopolymerization and multipolymer in the alcohol-water system according to claim 1 is characterized in that C
1-C
3Alcohol is the one or more kinds of mixtures in propyl alcohol, Virahol, ethanol and the methyl alcohol.
6, the synthetic method of homopolymerization and multipolymer in the alcohol-water system according to claim 4 is characterized in that emulsifying agent is the one or more kinds of mixtures in dodecyl sulfate, dodecylbenzene sulfonate and the dodecyl polyoxyethylene ether sulfate.
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN88102269A (en) * | 1987-04-14 | 1988-12-14 | 阿托化学公司 | Process for preparing aqueous emulsion of polyvinyl chloride in form of latex of monodisperse particles |
| US5420215A (en) * | 1992-12-28 | 1995-05-30 | Shin-Etsu Chemical Co., Ltd. | Process for producing vinyl chloride-based polymer |
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Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN88102269A (en) * | 1987-04-14 | 1988-12-14 | 阿托化学公司 | Process for preparing aqueous emulsion of polyvinyl chloride in form of latex of monodisperse particles |
| US5420215A (en) * | 1992-12-28 | 1995-05-30 | Shin-Etsu Chemical Co., Ltd. | Process for producing vinyl chloride-based polymer |
Non-Patent Citations (1)
| Title |
|---|
| 单分散聚合物微球的合成 顾尧，李春生，刘长欣，徐学平.《山东建材学院学报》，第12卷第3期 1998 * |
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