CN1982345A - Dextrin for producing PVC gloves and its production - Google Patents
Dextrin for producing PVC gloves and its production Download PDFInfo
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- CN1982345A CN1982345A CN 200510047982 CN200510047982A CN1982345A CN 1982345 A CN1982345 A CN 1982345A CN 200510047982 CN200510047982 CN 200510047982 CN 200510047982 A CN200510047982 A CN 200510047982A CN 1982345 A CN1982345 A CN 1982345A
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Abstract
A paste resin for producing PVC gloves and its production are disclosed. The process is carried out by making chlorethylene monomer under emulsifier system-surface activator protection, dispersing materials into water to become 1-2mum fine grain by disperser, polymerization reacting at 40-60degree under action of composite initiating agent to generate polymer latex with average grain diameter 1-2mum, and spray drying by latex to obtain the final product. It is stable, has no fluid, and has proper yield value and better tensile strength.
Description
Technical field
The invention belongs to the macromolecule chemical industry technical field, specifically a kind of paste resin that is used for production (pickling process) PVC gloves for preparing by the microsuspension method and preparation method thereof.
Background technology
Present domestic pvc resin paste grade product has multiple production method, and wherein main method has letex polymerization and microsuspension.The paste rosin products trade mark of its production is numerous, is mainly used in coating, foaming, slush moulding, dips in and mould and complete processing such as rotation-formed, produces goods such as leatheroid, flooring laminate, wallpaper, flame-retardant conveyor belt and toy.
The PVC gloves of dip forming are used for the labour protection of medical worker and other industries, because traditional emgloves white man skin produces anaphylaxis, thereby the PVC gloves are exported states such as the U.S., Europe and Australia in a large number.China PVC gloves have 80% outlet approximately, produce required PVC paste resin and account for 50% of China's paste resin total quantity consumed, and the manufacturing enterprise of China uses the import pvc resin paste grade to be raw material always.Numerous domestic is stuck with paste in the resin trade mark does not still have the resin dedicated of suitable for producing gloves.The present invention provides the resin dedicated of substituting import one products production PVC gloves for the sector.
Summary of the invention
Purpose of the present invention provides a kind of microsuspension by vinylchlorid, the primary particle median size that makes product be 1.0 μ m～2.0 μ m dispersion type polyvinyl chloride homopolymer (paste resin) be used to paste resin of producing by the PVC gloves and preparation method thereof
The object of the present invention is achieved like this: its technical scheme comprises following monomeric chemical ingredients composition and prescription thereof:
Vinyl chloride monomer 100% (wt), account for monomer weight 0.5%～0.8% emulsifying agent, account for the Fatty Alcohol(C12-C14 and C12-C18) of monomer weight 0.9%～1.1%, account for the oil soluble composite initiator of monomer weight 0.007%～0.010%;
Emulsifying agent is one or more arbitrary proportion blended aniorfic surfactant, and this anion surfactant is hard soap, long chain alkyl sulfates, aromatic sulfonate, sodium laurylsulfate, hexadecanol sodium sulfate, sodium lauryl sulfate, Sodium dodecylbenzene sulfonate, tetradecyl benzene sulfonic acid sodium salt:
The oil soluble composite initiator is one or both azo classes and the combining of one or more peroxide initiators, and wherein the azo class is Diisopropyl azodicarboxylate, 2,2'-Azobis(2,4-dimethylvaleronitrile); Superoxide is dicyclohexyl peroxydicarbonate, di-isopropyl peroxydicarbonate, peroxy dicarbonate hexichol oxygen ethyl ester and ethoxyethyl peroxy dicarbonate.
The present invention comprises that also the Fatty Alcohol(C12-C14 and C12-C18) that adds to some extent makes the more stable high fatty alcohol or the higher fatty acid of dispersion liquid of microsuspension for one or more.
The present invention also includes and adds an amount of oxidative ethane or epoxypropane polymer as the viscosity modifier ring.
Preparation method of the present invention is: scope is got vinyl chloride monomer, pure water, emulsifying agent and initiator after dispersion machine disperses according to the above ratio, make it to form fine droplets, under the effect of oil-soluble initiator,, generate polyvinyl chloride homopolymer-latex in 40～60 ℃ of reactions 10～30 hours.Operations such as latex is spray-dried, cloth bag filtration, pulverizing, packing make pvc resin paste grade.
Emulsifying agent generally uses aniorfic surfactant.Anion surfactant such as hard soap, long chain alkyl sulfates, aromatic sulfonate, sodium laurylsulfate, hexadecanol sodium sulfate, Sodium dodecylbenzene sulfonate, tetradecyl benzene sulfonic acid sodium salt etc.Its consumption is 0.4%～1.2% (wt) of monomer consumption.Higher alcohols that uses in the emulsification system or higher fatty acid etc. are as dispersion aids, its purpose is to reduce the interfacial tension of vinylchlorid and water, make tiny dispersant liquid drop in polymerization process, keep the stability of drop effectively, do not take place to assemble and layering, behind the latex that forms polymkeric substance, can make it keep stable again.But the stabilising effect of the dispersion liquid of carbonatoms below 8 is not good, should select carbonatoms more than 8, and consumption is 0.6%～1.5% (wt) of monomer consumption, preferably select 0.9%～1.2% for use.
Initiator generally uses azo class and peroxide azo class that Diisopropyl azodicarboxylate, 2,2'-Azobis(2,4-dimethylvaleronitrile) etc. are arranged usually; Superoxide is dicyclohexyl peroxydicarbonate, di-isopropyl peroxydicarbonate, peroxy dicarbonate hexichol oxygen ethyl ester and ethoxyethyl peroxy dicarbonate, the positive caproyl superoxide of 3.3.5-trimethylammonium etc.; consumption is 0.005%～0.012% (wt) of monomer usage quantity, preferred 0.006%～0.01%.Initiator system can use wherein two kinds compound.
The selected polymerization temperature of the present invention is advisable with 40～50 ℃.
Composite initiator of the present invention is composited by a kind of azo class and a kind of peroxide.
Emulsifier system of the present invention is made up of a kind of aniorfic surfactant and a kind of Fatty Alcohol(C12-C14 and C12-C18).
The reaction system material dispersed time of the present invention is 40～60min.
The present invention and additive method are compared, and have following characteristics:
1. adopt composite initiator system to make the speed of response held stationary;
2. the adding of dispersion stabilizer is guaranteed to stir down dispersion liquid and still can be kept stable;
3. polymerization latex good stability;
4. gained paste stable resin is good;
The viscosity stability of plastisol is good, through the time change little.
To be described in further detail invention by example below, but following example only is the present invention's example wherein, the rights protection scope of not representing the present invention and being limited, the scope of the present invention is as the criterion with claims.
Embodiment
Experiment is at volume 48m
3Have in the stainless steel cauldron of grid agitator and carry out.Reaction mixture (emulsifying agent, dispersion aids, initiator, pure water, vinylchlorid) enters dispersion tank, and it is reinforced through dispersion machine in setting-up time while disperseing in polymeric kettle, the reinforced back of finishing makes the still internal pressure increase 0.1MPa on former pressure-based to the polymeric kettle inflated with nitrogen, and begins the polymerization that heats up.Polymerization finishes the unreacted residual nitrogen ethene in back and is recovered to the vinylchlorid gas holder, and reactant (latex) is delivered to the blowing jar.
Latex obtains paste resin of the present invention, its median size 0.5～2 μ m with the spray-dryer drying after pulverize.Mean polymerisation degree 1700～1800.Stick with paste viscosity 500～3000mpa.s.
Embodiment 1
Vinylchlorid 95 (part), pure water 100 (part), 2,2'-Azobis(2,4-dimethylvaleronitrile) 0.0078 (part), C
12～26Fatty Alcohol(C12-C14 and C12-C18) 0.9 (part), Sodium dodecylbenzene sulfonate 0.75 (part), di-isopropyl peroxydicarbonate 0.085 (part).
Dispersed feeding time 50min;
45 ℃ of polymerization temperatures;
With Sodium dodecylbenzene sulfonate, C
12～26Fatty Alcohol(C12-C14 and C12-C18), 10 parts of pure water dissolve in the emulsifiers dissolve jar, 2,2'-Azobis(2,4-dimethylvaleronitrile) are added stirring and dissolving in the initiator dissolving vessel that has 5 parts of pure water.With di-isopropyl peroxydicarbonate in dissolving vessel and add the dissolving of 5 parts of pure water.
The above-mentioned emulsifying agent of dissolved, initiator and vinyl chloride monomer, pure water measured in accordance with regulations send into dispersion tank, reinforced through dispersion machine while disperseing, reinforced jitter time 50 minutes, nitrogen is filled to polymeric kettle in the reinforced back of finishing, make the still internal pressure on the basis that former still is pressed, increase 0.1MPa, be warming up to 45 ℃ of beginning polyreactions then.Descend when peak value appears in temperature in the kettle again, judge when pressure decline 0.2MPa is above that polymerization finishes, carry out then from pushing back receipts, still begins when pressing 0.1MPa to force to reclaim, and adds viscosity modifier simultaneously, when the still internal pressure reduce to-finish to reclaim during 0.05Mpa.Latex is squeezed into the blowing jar, and spray-dried device drying, pulverizer pulverizing and cloth envelop collector enter the feed bin packing and be finished product.
Finished product median size 1.62 μ m, mean polymerisation degree 1700
Embodiment 2
Vinylchlorid 100 (part), pure water 100 (part), Diisopropyl azodicarboxylate 0.010 (part), the positive caproyl superoxide 0.0062 of 3.3.5-trimethylammonium (part), C
12～26Fatty Alcohol(C12-C14 and C12-C18) 0.85 (part), Sodium dodecylbenzene sulfonate 0.8 (part),
Dispersed feeding time 60min;
43 ℃ of polymerization temperatures;
Step by embodiment 1 is carried out, finished product median size 1.45 μ m, mean polymerisation degree 1750.
Embodiment 3
Vinylchlorid 100 (part), pure water 100 (part), 2,2'-Azobis(2,4-dimethylvaleronitrile) 0.008 (part) higher alcohols 0.95 (part), sodium lauryl sulphate 0.67 (part), ethoxyethyl peroxy dicarbonate fat 0.0095 (part)
Jitter time 60min, chuck heating temperature rise to 40 ℃ beginning polymerization, all the other each steps are carried out its finished product grain size 1.40 μ m, mean polymerisation degree 1780 by the step of embodiment 1.
Embodiment 4
In further each time experiment, be under embodiment 3 same steps as that temperature of reaction will become wayward with the minimizing of pure water amount after reducing pure water and adding umber.
Following table is that embodiment product and import gloves are the comparison of reference examples with the paste resin
| Resin | Plastisol viscosity mpa.s | The polymerization degree | ||
| ?1Hr | ?3Hr | ?24Hr | ||
| Embodiment 1 | ?2000 | ?2400 | ?2500 | ?1700 |
| Embodiment 2 | ?1780 | ?2300 | ?2450 | ?1750 |
| Reference examples | ?4200 | ?3600 | ?5220 | ?1280 |
| Embodiment 3 | Embodiment 1 | Reference examples | ||
| The gloves finished product | Elongation % | 468 | ?424 | ?380 |
| Tension intensity MPa | 14.2 | ?13.1 | ?10.9 | |
| Plastisol | Initial stage viscosity | 2100 | ?2500 | ?2000 |
| Later stage viscosity | 2700 | ?3300 | ?3200 |
Dissolved adhesiveness condition determination: 30 ℃ of Type B rotational viscosimeters, 3
#6 rev/mins of rotors.
Claims (8)
1, a kind of paste resin that is used to produce the PVC gloves that adopts the preparation of microsuspension method and process by pickling process, it comprises following monomeric chemical ingredients composition and prescription thereof:
Vinyl chloride monomer 100% (wt), account for monomer weight 0.5%～0.8% emulsifying agent, account for the Fatty Alcohol(C12-C14 and C12-C18) of monomer weight 0.9%～1.1%, account for the oil soluble composite initiator of monomer weight 0.007%～0.010%;
Emulsifying agent is one or more arbitrary proportion blended aniorfic surfactant, and this anion surfactant is hard soap, long chain alkyl sulfates, aromatic sulfonate, sodium laurylsulfate, hexadecanol sodium sulfate, sodium lauryl sulfate, Sodium dodecylbenzene sulfonate, tetradecyl benzene sulfonic acid sodium salt;
The oil soluble composite initiator is one or both azo classes and the combining of one or more peroxide initiators, and wherein the azo class is Diisopropyl azodicarboxylate, 2,2'-Azobis(2,4-dimethylvaleronitrile); Superoxide is di-cyclohexylperoxy dicarbonate, di-isopropyl peroxydicarbonate, peroxy dicarbonate hexichol oxygen ethyl ester and ethoxyethyl peroxy dicarbonate.
2, according to the paste resin that is used to produce the PVC gloves of claim 1, it is characterized in that: the Fatty Alcohol(C12-C14 and C12-C18) that the present invention added makes the more stable high fatty alcohol or the higher fatty acid of dispersion liquid of microsuspension for one or more.
3, according to the paste resin that is used to produce the PVC gloves of claim 1, it is characterized in that: add an amount of oxidative ethane or epoxypropane polymer as the viscosity modifier ring.
4, a kind of paste process for preparing resins that is used to produce the PVC gloves that adopts the preparation of microsuspension method and process by pickling process, get vinyl chloride monomer, pure water, emulsifying agent and initiator after dispersion machine disperses by following proportional range, make it to form fine droplets, under the effect of oil-soluble initiator, in 40～60 ℃ of reactions 10～30 hours, generate polyvinyl chloride homopolymer-latex.Operations such as latex is spray-dried, cloth bag filtration, pulverizing, packing make pvc resin paste grade;
Vinyl chloride monomer 100% (wt), account for monomer weight 0.5%～0.8% emulsifying agent, account for the Fatty Alcohol(C12-C14 and C12-C18) of monomer weight 0.9%～1.1%, account for the oil soluble composite initiator of monomer weight 0.007%～0.010%;
Emulsifying agent is one or more arbitrary proportion blended aniorfic surfactant, and this anion surfactant is hard soap, long chain alkyl sulfates, aromatic sulfonate, sodium laurylsulfate, hexadecanol sodium sulfate, sodium lauryl sulfate, Sodium dodecylbenzene sulfonate, tetradecyl benzene sulfonic acid sodium salt;
The oil soluble composite initiator is one or both azo classes and the combining of one or more peroxide initiators, and wherein the azo class is Diisopropyl azodicarboxylate, 2,2'-Azobis(2,4-dimethylvaleronitrile); Superoxide is di-cyclohexylperoxy dicarbonate, di-isopropyl peroxydicarbonate, peroxy dicarbonate hexichol oxygen ethyl ester and ethoxyethyl peroxy dicarbonate.
5, paste process for preparing resins according to claim 4 is characterized in that the selective polymerization temperature is 40～50 ℃.
6, paste process for preparing resins according to claim 4 is characterized in that composite initiator is composited by a kind of azo class and a kind of peroxide.
7,, it is characterized in that form by promoting agent and a kind of Fatty Alcohol(C12-C14 and C12-C18) by a kind of anionic table for emulsifier system according to the paste process for preparing resins of claim 1.
8,, it is characterized in that the reaction system material dispersed time is 40～60min according to the paste process for preparing resins of claim 1.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100479820A CN100509882C (en) | 2005-12-13 | 2005-12-13 | Dextrin for producing PVC gloves and production thereof |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100479820A CN100509882C (en) | 2005-12-13 | 2005-12-13 | Dextrin for producing PVC gloves and production thereof |
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| CN1982345A true CN1982345A (en) | 2007-06-20 |
| CN100509882C CN100509882C (en) | 2009-07-08 |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101955559A (en) * | 2010-09-21 | 2011-01-26 | 沈阳化工股份有限公司 | Paste resin with high thermostability and preparation method thereof |
| CN102775537A (en) * | 2012-08-29 | 2012-11-14 | 沈阳化工股份有限公司 | High-strength PVC (polyvinyl chloride) paste resin and production method thereof |
| CN102952224A (en) * | 2011-08-26 | 2013-03-06 | 沈阳化工股份有限公司 | Low-polymerization-degree polyvinyl chloride pasty resin preparation method |
| CN102952228A (en) * | 2011-08-26 | 2013-03-06 | 沈阳化工股份有限公司 | Production method for improving productivity of paste resin |
| CN104072649A (en) * | 2014-06-27 | 2014-10-01 | 唐山三友氯碱有限责任公司 | Method for producing polyvinyl chloride paste resin |
| CN104768982A (en) * | 2012-11-02 | 2015-07-08 | 韩化石油化学株式会社 | Polyvinyl chloride resin and method of preparing the same |
| CN107698700A (en) * | 2017-08-23 | 2018-02-16 | 天津渤天化工有限责任公司 | A kind of PVC paste resin and its production method for preparing medical gloves |
Family Cites Families (5)
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| CN1007406B (en) * | 1985-04-02 | 1990-04-04 | 山东工业大学 | A kind of needling force-measuring device device |
| DE69933437D1 (en) * | 1998-01-27 | 2006-11-16 | Shin Dai Ichi Vinyl Corp | METHOD TO MANUFACTURING FROM polyvinyl chloride resin FOR PASTE PRODUCTION |
| JP4257932B2 (en) * | 2002-07-19 | 2009-04-30 | 東ソー株式会社 | Manufacturing method of PVC resin for paste |
| CN100455610C (en) * | 2002-09-03 | 2009-01-28 | 沈阳化工股份有限公司 | Interpolymer paste resin and its preparing method |
| CN100513441C (en) * | 2005-01-07 | 2009-07-15 | 潜江市仙桥化学制品有限公司 | Formulating method of high quality PVC resin for A-21 type brei |
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| CN101955559A (en) * | 2010-09-21 | 2011-01-26 | 沈阳化工股份有限公司 | Paste resin with high thermostability and preparation method thereof |
| CN101955559B (en) * | 2010-09-21 | 2012-04-25 | 沈阳化工股份有限公司 | Paste resin with high thermostability and preparation method thereof |
| CN102952224A (en) * | 2011-08-26 | 2013-03-06 | 沈阳化工股份有限公司 | Low-polymerization-degree polyvinyl chloride pasty resin preparation method |
| CN102952228A (en) * | 2011-08-26 | 2013-03-06 | 沈阳化工股份有限公司 | Production method for improving productivity of paste resin |
| CN102775537A (en) * | 2012-08-29 | 2012-11-14 | 沈阳化工股份有限公司 | High-strength PVC (polyvinyl chloride) paste resin and production method thereof |
| CN102775537B (en) * | 2012-08-29 | 2015-04-08 | 沈阳化工股份有限公司 | High-strength PVC (polyvinyl chloride) paste resin and production method thereof |
| CN104768982A (en) * | 2012-11-02 | 2015-07-08 | 韩化石油化学株式会社 | Polyvinyl chloride resin and method of preparing the same |
| US9902817B2 (en) | 2012-11-02 | 2018-02-27 | Hanwha Chemical Corporation | Polyvinyl chloride resin and method of preparing the same |
| CN104072649A (en) * | 2014-06-27 | 2014-10-01 | 唐山三友氯碱有限责任公司 | Method for producing polyvinyl chloride paste resin |
| CN107698700A (en) * | 2017-08-23 | 2018-02-16 | 天津渤天化工有限责任公司 | A kind of PVC paste resin and its production method for preparing medical gloves |
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