CN106008780A - Method for preparing shock-resistant vinyl chloride copolymer resin - Google Patents
Method for preparing shock-resistant vinyl chloride copolymer resin Download PDFInfo
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- CN106008780A CN106008780A CN201610412735.4A CN201610412735A CN106008780A CN 106008780 A CN106008780 A CN 106008780A CN 201610412735 A CN201610412735 A CN 201610412735A CN 106008780 A CN106008780 A CN 106008780A
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- vinyl chloride
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F214/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen
- C08F214/02—Monomers containing chlorine
- C08F214/04—Monomers containing two carbon atoms
- C08F214/06—Vinyl chloride
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/12—Polymerisation in non-solvents
- C08F2/16—Aqueous medium
- C08F2/20—Aqueous medium with the aid of macromolecular dispersing agents
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/38—Polymerisation using regulators, e.g. chain terminating agents, e.g. telomerisation
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- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
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- Graft Or Block Polymers (AREA)
Abstract
The invention discloses a method for preparing shock-resistant vinyl chloride copolymer resin. A polymerization method is optimized by optimizing a polymerization monomer formula, a dispersing agent formula, polymerization reaction temperature and time, the charging mode and other factors influencing a polymerization reaction. A product processed through the vinyl chloride copolymer resin prepared through the method has excellent processability, barrier performance, fire resistance and shock resistance, is widely applied to the fields of the industries of buildings, packages, cars, food and the like, and has wide market prospects.
Description
The present invention is application number: 2014108369832, the applying date: 2014-12-29, denomination of invention:
The divisional application of the vinyl chloride copolymer resin planting resistance to impact and preparation method thereof.
Technical field
The present invention relates to a kind of vinyl chloride copolymer resin and preparation method thereof, particularly relate to a kind of resistance to impact
The copolymer resin of vinyl chloride, vinylidene chloride, acrylate and maleic anhydride and preparation method thereof.
Background technology
Though polrvinyl chloride prepared at laboratory the most as far back as 1835, but because of poor heat stability, processing should
With never breaking through.Arrived eighties of last century end of the twenties, occur in that of both break through: one is plasticising,
Goodrich companies in 1933 have delivered the patent adding plasticizer;Another is copolymerization, and PVC is served structure
Improve, be conducive to processing.The chloroethylene copolymer species produced in the world at present not less than dozens, kind board
Number more.Poor due to the processing type of polrvinyl chloride, impact strength, dissolubility etc., can not meet some special
Different purposes, the therefore new polrvinyl chloride kind of development.
VDC-VC copolymer resins from 1936 come out since, U.S. DOW, Japan Wu Yu, the Northeast electrification,
Company's competitively Development and Production such as East Asia synthesis go out VDC-VC suspension copolymer resin.Domestic open from the eighties in 20th century
Begin to study synthesis technique and the performance of VDC-VC copolymer resins, have accumulated certain theoretical basis and technology.Work
Use free radical to suspend in industry and emulsion is polymerized VDC-VC polymer processed, mainly with VDC as main monomer, by
React to monomer chain tra nsfer etc. in existing, cause the formation of unstable structure in polymer chain, the heat of polymer
Less stable, affects processing characteristics.
US4983311A describes a kind of vinyl chloride copolymer, hydroxyl and two groups of carboxylic acid group by all mixing
Liquid polymerization is simultaneously introduced in polymer adhesive.In being preferable to carry out one, vinyl chloride, glycerol monoallyl
Ether, acetone, benzoyl peroxide first phthalein are added by fed-batch mode, and maleic acid, vinylidene chloride and methanol are logical
Cross quantitative feeding mode to add.But owing to employing multi-solvents, the dependence to solvent causes environmental problem
And add the cost of production.
US5912082A disclose a kind of to vinyl chloride or vinyl chloride and other mixture of vinyl monomer with contain
Carboxylic monomer is polymerized, thus the method obtaining vinyl chloride copolymer.Hydroxyl monomer is by dihydroxy
Base or polyhydroxy-alcohol part allylation obtain.This copolymer is prepared by suspension polymerization, hydroxyl
There is the character substantially changing polymer, plasticizer absorption rate substantially increases and drying time significantly reduces.
It addition, hydroxyl becomes the reflecting point of post-polymerization due to its polarity and activity.But owing to carboxylic monomer enters
Having arrived polrvinyl chloride main chain, resin heat stability in the course of processing is inadequate, easily decomposes and makes goods variable color.
CN101386661A discloses the preparation method of a kind of polychloroethylene with high polymerization degree, vinyl chloride main monomer with
Diallyl fumarate, DAIP and/or diallyl maleate comonomer use and suspend
Copolymerization process obtains high polymerization degree vinyl chloride copolymer resin, employs the compound system of chain extender/chain-transferring agent
Shorten the response time, solve polymeric reaction temperature difficulty control problem, and improve the processability of goods,
Improve its mechanical property.But the method is faced with the difficult separation and recycling of monomer and resin, and cost produces
Higher.
CN103265658A discloses the synthetic method of a kind of heat resistant type chloroethylene copolymer resin, uses emulsion to gather
Conjunction method is by Vinyl Chloride Monomer and second comonomer or second comonomer and Third monomer, poly-under anaerobic airtight condition
Closing reaction, polymerization temperature is 45-65 DEG C, when reaction temperature reaches set temperature value, starts to add initiator
And, prepare copolymer emulsion, this LS is dried and i.e. prepares polyvinyl chloride copolymer.But the method is adopted
The resin prepared with emulsion polymerization way is difficult to obtain controlled grain diameter and porosity, and molecular weight
Distribution width.
Summary of the invention
Not enough for prior art, the present invention provides a kind of with vinyl chloride as main monomer, vinylidene chloride, propylene
Acid esters and maleic anhydride monomer carry out resistance to impact vinyl chloride copolymer resin and the preparation thereof of modification by copolymerization
Method.
To achieve the above object of the invention, the present invention provides the preparation of a kind of resistance to impact vinyl chloride copolymer resin
Method, described copolymer resin is made up by suspension polymerisation of the raw material of following parts by weight: mix monomer 100
Part, dispersant 0.1-1 part, initiator 0.05-0.3 part, pH adjusting agent 0.1-2 part, chain-transferring agent 0.05-0.2
Part and deionized water 100-300 part;
Described mix monomer consists of the following components in percentage by weight: vinyl chloride 60-90%, vinylidene chloride
5-30%, acrylate 1-10% and maleic anhydride (MA) 1-5%;
Described dispersant is hydroxypropyl methyl cellulose and/or polyvinyl alcohol (PVA);
Described initiator is azo compound or persulfate;
Described pH adjusting agent is hydrophosphate or bicarbonate;
Described chain-transferring agent is aliphatic mercaptan;
Described preparation method comprises the steps:
(1) under the protection of noble gas, Vinyl Chloride Monomer, dispersant, part initiator, pH are adjusted
Joint agent and deionized water join reactor, pre-dispersed 20-30min under room temperature;
(2) heat up and control at reaction temperature 30-70 DEG C react 15-45min, then add vinylidene chloride and
Crylic acid ester mixture monomer;
(3) after completing monomer interpolation, add residue initiator, control to react at reaction temperature 30-70 DEG C
15-30min;
(4) reactor temperature is warming up to 40-80 DEG C, drips maleic anhydride monomer;
(5) when polymerization pressure declines 0.1-0.3MPa, add chain-transferring agent, stop stirring, reduce
Reaction temperature, residual gas in releasing reactor, discharging;
(6) discharging is through filtering, washing and dried, obtains vinyl chloride copolymer resin;
Described acrylate is selected from acrylic acid methyl ester., ethyl acrylate, n-butyl acrylate and acrylic acid-2-ethyl
One or more in own ester;
Described dispersant consists of the following components in percentage by weight: polyvinyl alcohol (PVA) 20-80% and hydroxyl
Propyl methocel 20-80%.
The present invention is by aggregation Monomer Formations, dispersant formulation, polymeric reaction temperature and time, charging
Modes etc. affect the factor of polyreaction, optimize polymerization, are obtained by the preparation method of the present invention
Vinyl chloride copolymer resin product, has relatively high resin particle diameter, owing to introducing vinylidene chloride, no in polymerization
Satisfied fatty acid and maleic anhydride so that the flexibility of molecule segment in whole molecular structure, can be strengthened,
The property that resin is excellent can be given, as reduce resin melt temperature, improve resin heat stability,
Strengthen the impact resistance of goods, be widely used in the fields such as building, packaging, automobile, food service industry, have relatively
Good market prospect.Compared with prior art, the method have the advantages that
1, by introducing vinylidene chloride, unsaturated fatty acid and maleic anhydride on polrvinyl chloride main chain,
Optimizing the chain structure of main chain, the intensity of vinyl chloride copolymer resin particle is higher, the most broken, uses the longevity
Life is long, and its fabricated product has excellent impact resistance, the transparency, barrier and anti-flammability;
2, by adjusting, improving dispersant dosage and coupling, bulky grain and little granule, holding can be eliminated
Particle diameter compares concentration, and grain form is regular, fine and close, has relatively low porosity and relatively high apparent density, particle diameter
Resin ratio between 0.2-0.25mm is more than 85%, and apparent density is at 0.55-0.75g/ml.
3, introduce different monomers at different polymerization stages, be conducive to effectively controlling polymerization rate, copolymer
Composition and the molecular weight of copolymer, form the relatively uniform vinyl chloride copolymer of composition;
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is further described, but does not limit the invention to this
A little detailed description of the invention.One skilled in the art would recognize that and present invention encompasses Claims scope
Interior potentially included all alternatives, improvement project and equivalents.
Embodiment 1
Under the protection of noble gas, in 10L rustless steel autoclave add 6L high purity deionized water,
2688g Vinyl Chloride Monomer, 18g sodium peroxydisulfate, 28g sodium bicarbonate and 185g hydroxypropyl methyl cellulose (hydroxyl
Propyl group content is 6.3mol%), it is stirred at room temperature pre-dispersed 25min, heats up and control reaction temperature 55 DEG C
Lower reaction 30min, then adds 148g vinylidene chloride monomer and 93g n-butyl acrylate monomer, completes list
After body adds, then add 2g sodium peroxydisulfate and control to react at reaction temperature 55 DEG C 20min, then dripping 60g
Maleic anhydride monomer, heats up and controls reaction temperature 60 DEG C, when polymerization pressure declines 0.2MPa
Time, add 18g n-dodecyl mercaptan and stop stirring, reducing residue in reaction temperature, releasing reactor
Gas, discharging and through filter, washing and dried, obtain 2535g vinyl chloride copolymer resin.Through unit
Element analysis, nuclear-magnetism, infrared analysis confirm vinyl chloride construction unit shared mole hundred in vinyl chloride copolymer resin
Dividing content is 89.2%;Molar content shared by vinylidene chloride construction unit is 5.2%;N-butyl acrylate
Molar content shared by construction unit is 3.4%;Molar content shared by maleic anhydride construction unit
It is 2.2%.
Polymer data: resin particle diameter 213 μm that Coulter particle size analyzer measures;AutoPore-IV
The resin apparent density that-9510 mercury injection apparatuses measure is 0.68g/cm3, porosity is 55%, is specifically shown in Table 1.
Mechanical properties of polymer: hot strength (GB/T1040-2006) is 67.3MPa, shock strength (GB/T
1843-1996) it is 28.3KJ/m2, specifically it is shown in Table 1.
Embodiment 2
Under the protection of noble gas, in 10L rustless steel autoclave add 6L high purity deionized water,
2412g Vinyl Chloride Monomer, 16g sodium peroxydisulfate, 28g sodium bicarbonate and 185g hydroxypropyl methyl cellulose (hydroxyl
Propyl group content is 6.3mol%), it is stirred at room temperature pre-dispersed 25min, heats up and control reaction temperature 55 DEG C
Lower reaction 30min, then adds 296g vinylidene chloride monomer and 242g n-butyl acrylate monomer, completes list
After body adds, then add 4g sodium peroxydisulfate and control to react at reaction temperature 55 DEG C 20min, then dripping 60g
Maleic anhydride monomer, heats up and controls reaction temperature 60 DEG C, when polymerization pressure declines 0.2MPa
Time, add 18g n-dodecyl mercaptan and stop stirring, reducing residue in reaction temperature, releasing reactor
Gas, discharging and through filter, washing and dried, obtain 2619g vinyl chloride copolymer resin.Through unit
Element analysis, nuclear-magnetism, infrared analysis confirm vinyl chloride construction unit shared mole hundred in vinyl chloride copolymer resin
Dividing content is 78.4%;Molar content shared by vinylidene chloride construction unit is 10.5%;N-butyl acrylate
Molar content shared by construction unit is 9.0%;Molar content shared by maleic anhydride construction unit
It is 2.1%.
Polymer data: resin particle diameter 223 μm that Coulter particle size analyzer measures;AutoPore-IV
The resin apparent density that-9510 mercury injection apparatuses measure is 0.62g/cm3, porosity is 49%, is specifically shown in Table 1.
Mechanical properties of polymer: hot strength (GB/T1040-2006) is 65.3MPa, shock strength (GB/T
1843-1996) it is 31.4KJ/m2, specifically it is shown in Table 1.
Embodiment 3
Under the protection of noble gas, in 10L rustless steel autoclave add 6L high purity deionized water,
2088g Vinyl Chloride Monomer, 14g sodium peroxydisulfate, 28g sodium bicarbonate and 185g hydroxypropyl methyl cellulose (hydroxyl
Propyl group content is 6.3mol%), it is stirred at room temperature pre-dispersed 25min, heats up and control reaction temperature 55 DEG C
Lower reaction 30min, then adds 603g vinylidene chloride monomer and 153g n-butyl acrylate monomer, completes list
After body adds, then add 6g sodium peroxydisulfate and control to react at reaction temperature 55 DEG C 20min, then dripping 146g
Maleic anhydride monomer, heats up and controls reaction temperature 60 DEG C, when polymerization pressure declines 0.2MPa
Time, add 18g n-dodecyl mercaptan and stop stirring, reducing residue in reaction temperature, releasing reactor
Gas, discharging and through filter, washing and dried, obtain 2608g vinyl chloride copolymer resin.Through unit
Element analysis, nuclear-magnetism, infrared analysis confirm vinyl chloride construction unit shared mole hundred in vinyl chloride copolymer resin
Dividing content is 68.8%;Molar content shared by vinylidene chloride construction unit is 20.4%;N-butyl acrylate
Molar content shared by construction unit is 5.5%;Molar content shared by maleic anhydride construction unit
It is 5.3%, is specifically shown in Table 1.
Polymer data: resin particle diameter 234 μm that Coulter particle size analyzer measures;AutoPore-IV
The resin apparent density that-9510 mercury injection apparatuses measure is 0.58g/cm3, porosity is 45%, is specifically shown in Table 1.
Mechanical properties of polymer: hot strength (GB/T1040-2006) is 59.7MPa, shock strength (GB/T
1843-1996) it is 34.8KJ/m2, specifically it is shown in Table 1.
Embodiment 4
Under the protection of noble gas, in 10L rustless steel autoclave add 6L high purity deionized water,
1804g Vinyl Chloride Monomer, 12g sodium peroxydisulfate, 28g sodium bicarbonate and 185g hydroxypropyl methyl cellulose (hydroxyl
Propyl group content is 6.3mol%), it is stirred at room temperature pre-dispersed 25min, heats up and control reaction temperature 55 DEG C
Lower reaction 30min, then adds 743g vinylidene chloride monomer and 303g n-butyl acrylate monomer, completes list
After body adds, then add 8g sodium peroxydisulfate and control to react at reaction temperature 55 DEG C 20min, then dripping 152g
Maleic anhydride monomer, heats up and controls reaction temperature 60 DEG C, when polymerization pressure declines 0.2MPa
Time, add 18g n-dodecyl mercaptan and stop stirring, reducing residue in reaction temperature, releasing reactor
Gas, discharging and through filter, washing and dried, obtain 2643g vinyl chloride copolymer resin.Through unit
Element analysis, nuclear-magnetism, infrared analysis confirm vinyl chloride construction unit shared mole hundred in vinyl chloride copolymer resin
Dividing content is 58.0%;Molar content shared by vinylidene chloride construction unit is 25.6%;N-butyl acrylate
Molar content shared by construction unit is 10.9%;Molar content shared by maleic anhydride construction unit
It is 5.5%.
Polymer data: resin particle diameter 252 μm that Coulter particle size analyzer measures;AutoPore-IV
The resin apparent density that-9510 mercury injection apparatuses measure is 0.56g/cm3, porosity is 42%, is specifically shown in Table 1.
Mechanical properties of polymer: hot strength (GB/T1040-2006) is 58.7MPa, shock strength (GB/T
1843-1996) it is 35.2KJ/m2, specifically it is shown in Table 1.
Embodiment 5
Under the protection of noble gas, in 10L rustless steel autoclave add 6L high purity deionized water,
2408g Vinyl Chloride Monomer, 12g sodium peroxydisulfate, 28g sodium bicarbonate, 125g hydroxypropyl methyl cellulose (hydroxyl
Propyl group content is 6.3mol%) and 60g polyvinyl alcohol (alcoholysis degree is 65%), it is stirred at room temperature pre-dispersed
25min, heats up and controls to react at reaction temperature 55 DEG C 30min, then adding 296g vinylidene chloride monomer
With 242g n-butyl acrylate monomer, after completing monomer interpolation, then add 4g sodium peroxydisulfate and control reaction
React 20min, then dropping 60g maleic anhydride monomer at temperature 55 DEG C, heat up and control reaction temperature
Spend 60 DEG C, when polymerization pressure declines 0.2MPa, add 18g n-dodecyl mercaptan and stop stirring,
Reduce reaction temperature, residual gas in releasing reactor, discharging and through filter, washing and dried,
To 2635g vinyl chloride copolymer resin.Vinyl chloride copolymer is confirmed through elementary analysis, nuclear-magnetism, infrared analysis
In resin, molar content shared by vinyl chloride construction unit is 77.9%;Shared mole of vinylidene chloride construction unit
Percentage composition is 11.0%;Molar content shared by n-butyl acrylate construction unit is 8.9%;Maleic
Molar content shared by dicarboxylic anhydride construction unit is 2.2%.
Polymer data: resin particle diameter 219 μm that Coulter particle size analyzer measures;AutoPore-IV
The resin apparent density that-9510 mercury injection apparatuses measure is 0.65g/cm3, porosity is 47%, is specifically shown in Table 1.
Mechanical properties of polymer: hot strength (GB/T1040-2006) is 66.1MPa, shock strength (GB/T
1843-1996) it is 32.4KJ/m2, specifically it is shown in Table 1.
Embodiment 6
Under the protection of noble gas, in 10L rustless steel autoclave add 6L high purity deionized water,
2415g Vinyl Chloride Monomer, 12g sodium peroxydisulfate, 28g sodium bicarbonate, 95g hydroxypropyl methyl cellulose (hydroxyl
Propyl group content is 6.3mol%) and 90g polyvinyl alcohol (alcoholysis degree is 65%), it is stirred at room temperature pre-dispersed
25min, heats up and controls to react at reaction temperature 55 DEG C 30min, then adding 296g vinylidene chloride monomer
With 242g n-butyl acrylate monomer, after completing monomer interpolation, then add 4g sodium peroxydisulfate and control reaction
React 20min, then dropping 60g maleic anhydride monomer at temperature 55 DEG C, heat up and control reaction temperature
Spend 60 DEG C, when polymerization pressure declines 0.2MPa, add 18g n-dodecyl mercaptan and stop stirring,
Reduce reaction temperature, residual gas in releasing reactor, discharging and through filter, washing and dried,
To 2642g vinyl chloride copolymer resin.Vinyl chloride copolymer is confirmed through elementary analysis, nuclear-magnetism, infrared analysis
In resin, molar content shared by vinyl chloride construction unit is 78.0%;Shared mole of vinylidene chloride construction unit
Percentage composition is 10.8%;Molar content shared by n-butyl acrylate construction unit is 9.0%;Maleic
Molar content shared by dicarboxylic anhydride construction unit is 2.2%.
Polymer data: resin particle diameter 216 μm that Coulter particle size analyzer measures;AutoPore-IV
The resin apparent density that-9510 mercury injection apparatuses measure is 0.73g/cm3, porosity is 44%, is specifically shown in Table 1.
Mechanical properties of polymer: hot strength (GB/T1040-2006) is 66.8MPa, shock strength (GB/T
1843-1996) it is 34.5KJ/m2, specifically it is shown in Table 1.
Embodiment 7
Under the protection of noble gas, in 10L rustless steel autoclave add 6L high purity deionized water,
2407g Vinyl Chloride Monomer, 12g sodium peroxydisulfate, 28g sodium bicarbonate, 60g hydroxypropyl methyl cellulose (hydroxyl
Propyl group content is 6.3mol%) and 125g polyvinyl alcohol (alcoholysis degree is 65%), it is stirred at room temperature pre-point
Dissipate 25min, heat up and control to react at reaction temperature 55 DEG C 30min, then adding 296g vinylidene chloride list
Body and 242g n-butyl acrylate monomer, after completing monomer interpolation, then add 4g sodium peroxydisulfate and control anti-
Answer reaction 20min at temperature 55 DEG C, then dropping 60g maleic anhydride monomer, heat up and control reaction
Temperature 60 C, when polymerization pressure declines 0.2MPa, adds 18g n-dodecyl mercaptan and stops stirring
Mix, reduce reaction temperature, residual gas in releasing reactor, discharging and through filter, washing and dried,
Obtain 2624g vinyl chloride copolymer resin.Chloroethylene copolymer is confirmed through elementary analysis, nuclear-magnetism, infrared analysis
In resin, molar content shared by vinyl chloride construction unit is 77.8%;Rub shared by vinylidene chloride construction unit
Your percentage composition is 11.0%;Molar content shared by n-butyl acrylate construction unit is 9.1%;Along fourth
Molar content shared by enedioic acid acid anhydride construction unit is 2.1%.
Polymer data: resin particle diameter 217 μm that Coulter particle size analyzer measures;AutoPore-IV
The resin apparent density that-9510 mercury injection apparatuses measure is 0.68g/cm3, porosity is 46%, is specifically shown in Table 1.
Mechanical properties of polymer: hot strength (GB/T1040-2006) is 65.9MPa, shock strength (GB/T
1843-1996) it is 31.0KJ/m2, specifically it is shown in Table 1.
Embodiment 8
Under the protection of noble gas, in 10L rustless steel autoclave add 6L high purity deionized water,
2395g Vinyl Chloride Monomer, 12g sodium peroxydisulfate, 28g 2,2'-Azobis(2,4-dimethylvaleronitrile), 60g hydroxypropyl methyl cellulose
(hydroxypropyl content is 6.3mol%) and 125g polyvinyl alcohol (alcoholysis degree is 65%), be stirred at room temperature
Pre-dispersed 25min, heats up and controls to react at reaction temperature 55 DEG C 30min, then adding the inclined chloroethene of 296g
Alkene monomer and 241g acrylic acid-2-ethyl caproite monomer, after completing monomer interpolation, then it is different to add 4g azo two
Heptonitrile also controls to react at reaction temperature 55 DEG C 20min, then dropping 60g maleic anhydride monomer, rises
Temperature also controls reaction temperature 60 DEG C, when polymerization pressure declines 0.2MPa, adds 18g dodecyl
Mercaptan also stops stirring, reduces reaction temperature, residual gas in releasing reactor, discharging through filtering, washing
Wash and dried, obtain 2648g vinyl chloride copolymer resin.Through elementary analysis, nuclear-magnetism, infrared analysis
Confirm that in vinyl chloride copolymer resin, molar content shared by vinyl chloride construction unit is 78.1%;Vinylidene chloride
Molar content shared by construction unit is 10.9%;Molar content shared by n-butyl acrylate construction unit
It is 9.0%;Molar content shared by maleic anhydride construction unit is 2.0%.
Polymer data: resin particle diameter 235 μm that Coulter particle size analyzer measures;AutoPore-IV
The resin apparent density that-9510 mercury injection apparatuses measure is 0.75g/cm3, porosity is 42%, is specifically shown in Table 1.
Mechanical properties of polymer: hot strength (GB/T1040-2006) is 63.2MPa, shock strength (GB/T
1843-1996) it is 38.7KJ/m2, specifically it is shown in Table 1.
Table 1: vinyl chloride copolymer resin Performance comparision prepared by embodiment 1-8
Knowable to table 1 data, the present invention is by introducing vinylidene chloride, unsaturated lipid on polrvinyl chloride main chain
Fat acid and maleic anhydride, and adjust whole, improve dispersant dosage and vinyl chloride that coupling prepares altogether
Copolymer resin, grain form is regular, fine and close, has relatively low porosity and relatively high apparent density, and it processes system
Product possess excellent tensile property and erosion-resisting characteristics.
Claims (1)
1. the preparation method of the vinyl chloride copolymer resin of a resistance to impact, it is characterised in that
Described copolymer resin is made up by suspension polymerisation of the raw material of following parts by weight: mix monomer 100 parts,
Dispersant 0.1-1 part, initiator 0.05-0.3 part, pH adjusting agent 0.1-2 part, chain-transferring agent 0.05-0.2 part
With deionized water 100-300 part;
Described mix monomer consists of the following components in percentage by weight: vinyl chloride 60-90%, vinylidene chloride
5-30%, acrylate 1-10% and maleic anhydride (MA) 1-5%;
Described dispersant is hydroxypropyl methyl cellulose and/or polyvinyl alcohol (PVA);
Described initiator is azo compound or persulfate;
Described pH adjusting agent is hydrophosphate or bicarbonate;
Described chain-transferring agent is aliphatic mercaptan;
Described method comprises the steps:
(1) under the protection of noble gas, by Vinyl Chloride Monomer, dispersant, part initiator, pH regulator
Agent and deionized water join reactor, pre-dispersed 20-30min under room temperature;
(2) heat up and control to react at reaction temperature 30-70 DEG C 15-45min, then adding vinylidene chloride and third
Olefin(e) acid ester mix monomer;
(3) after completing monomer interpolation, add residue initiator, control to react at reaction temperature 30-70 DEG C
15-30min;
(4) reactor temperature is warming up to 40-80 DEG C, drips maleic anhydride monomer;
(5) when polymerization pressure declines 0.1-0.3MPa, add chain-transferring agent, stop stirring, reduce
Reaction temperature, residual gas in releasing reactor, discharging;
(6) discharging is through filtering, washing and dried, obtains vinyl chloride copolymer resin;
Described acrylate is selected from acrylic acid methyl ester., ethyl acrylate, n-butyl acrylate and acrylic acid-2-ethyl
One or more in own ester;
Described dispersant consists of the following components in percentage by weight: polyvinyl alcohol (PVA) 20-80% and hydroxypropyl
Ylmethyl cellulose 20-80%.
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CN201610412284.4A Expired - Fee Related CN105859943B (en) | 2014-12-29 | 2014-12-29 | A kind of preparation method of the vinyl chloride copolymer resin of impact resistance |
CN201610412730.1A Expired - Fee Related CN105924559B (en) | 2014-12-29 | 2014-12-29 | A kind of preparation method of the vinyl chloride copolymer resin of impact resistance |
CN201410836983.2A Expired - Fee Related CN104448092B (en) | 2014-12-29 | 2014-12-29 | Preparation method of impact-resistant chloroethylene copolymer resin |
CN201610414680.0A Active CN105968246B (en) | 2014-12-29 | 2014-12-29 | A kind of preparation method of the vinyl chloride copolymer resin of impact resistance |
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CN108084318A (en) * | 2017-12-28 | 2018-05-29 | 宁波俐辰新能源有限公司 | A kind of nuisanceless flame-resistant high-temperature-resistant polyvinyl chloride and its manufacturing method |
KR102251268B1 (en) | 2018-04-30 | 2021-05-12 | 주식회사 엘지화학 | Vinyl chloride polymer and preparation method thereof |
CN109369839B (en) * | 2018-09-21 | 2020-12-29 | 无锡洪汇新材料科技股份有限公司 | Self-crosslinking vinyl chloride copolymer emulsion and preparation method thereof |
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- 2014-12-29 CN CN201610412284.4A patent/CN105859943B/en not_active Expired - Fee Related
- 2014-12-29 CN CN201610412730.1A patent/CN105924559B/en not_active Expired - Fee Related
- 2014-12-29 CN CN201410836983.2A patent/CN104448092B/en not_active Expired - Fee Related
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CN101314627A (en) * | 2008-06-04 | 2008-12-03 | 中国农业大学 | Film-forming agent for seed clothing sheet and preparation method thereof |
CN101367898A (en) * | 2008-08-27 | 2009-02-18 | 浙江巨化股份有限公司电化厂 | PVDC copolymerization emulsion, preparation and uses thereof |
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CN105859943B (en) | 2017-12-19 |
CN105924559B (en) | 2017-12-08 |
CN105924559A (en) | 2016-09-07 |
CN104448092B (en) | 2017-02-22 |
CN105859943A (en) | 2016-08-17 |
CN106008780B (en) | 2017-11-17 |
CN104448092A (en) | 2015-03-25 |
CN105968246A (en) | 2016-09-28 |
CN105968246B (en) | 2018-03-20 |
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