CN1986583B - Water PVDC latex specially for painting special cloth and its preparing method - Google Patents
Water PVDC latex specially for painting special cloth and its preparing method Download PDFInfo
- Publication number
- CN1986583B CN1986583B CN2006101550856A CN200610155085A CN1986583B CN 1986583 B CN1986583 B CN 1986583B CN 2006101550856 A CN2006101550856 A CN 2006101550856A CN 200610155085 A CN200610155085 A CN 200610155085A CN 1986583 B CN1986583 B CN 1986583B
- Authority
- CN
- China
- Prior art keywords
- water
- mix monomer
- consumption
- pvdc latex
- total amount
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
Abstract
The present invention relates to water-thinned PVDC latex, and is especially a kind of water-thinned PVDC latex for painting special cloth and its preparation process. The water-thinned PVDC latex is prepared with mixed monomer through emulsion polymerization in the presence of emulsifier and initiator. The mixed monomer includes vinylidene chloride 75-90 %, acrylate monomer 8-20 % and unsaturated fatty acid 1-5 %. The water-thinned PVDC latex is used in treating non-woven fabric, and the treated non-woven fabric is hard, elastic, waterproof, heat resistant and crease resistant and may be used widely. In addition, the water-thinned PVDC latex has excellent compatibility with acrylic acid emulsion.
Description
Technical field
The present invention relates to a kind of water-based PVDC latex, relate in particular to a kind of water PVDC latex specially for painting special cloth and preparation method thereof.
Background technology
Aspect the treatment agent of non-woven fabrics, mainly be the treatment agent that adopts single ACRYLIC EMULSION type at present, such treatment agent has good cementability, weather resistance and softness.But along with the variation in market, user's requirement also has nothing in common with each other, and the non-woven fabrics after the past require to handle is soft, and turns to harderly now gradually, and rich elasticity preferably also has water tolerance, thermotolerance and wrinkle resistance preferably simultaneously.As processing and the coating at the carpet back side and the processing of other non-woven fabrics that is mainly used in tent cloth now.
Chinese invention patent (publication number is CN1715559A) discloses a kind of latex for coating drinking filter bag cotton paper and preparation method thereof, it forms by emulsion polymerization way copolymerization in the presence of emulsifying agent, initiator, the mix monomer component of latex is: (1) vinylidene chloride, consumption are the 60-85% of mix monomer total amount; (2) acrylic ester monomer, consumption are the 5-30% of mix monomer total amount; (3) unsaturated fatty acids, consumption are the 5-10% of mix monomer total amount.This invention has: the tissue paper of coating is had than high wet strength, and the infiltration water ability is strong, characteristics such as few and cost performance height of nonpoisonous and tasteless, leachable thing, and the utmost point is applicable to bag for extracting beverage tissue paper surface coated such as coffee, tealeaves.But it can't satisfy the requirement that non-woven fabrics is handled owing to have higher water absorbability after the emulsion drying.
Summary of the invention
In order to address the deficiencies of the prior art, an object of the present invention is to provide and a kind ofly make the non-woven fabrics after the processing harder, rich elasticity preferably also has the water-based PVDC latex of water tolerance, thermotolerance and wrinkle resistance preferably simultaneously.
Another object of the present invention provides the preparation method of above-mentioned water-based PVDC latex.
In order to realize first above-mentioned purpose, the present invention mainly is achieved through the following technical solutions:
Water PVDC latex specially for painting special cloth is formed by emulsion polymerization way copolymerization in the presence of emulsifying agent, initiator by mix monomer, and the mix monomer component of described latex comprises:
(1) vinylidene chloride, its consumption are the 75-90% of mix monomer total amount;
(2) contain a kind of acrylic ester monomer of acrylate soft monomer at least, its consumption is the 8-20% of mix monomer total amount;
(3) unsaturated fatty acids, its consumption are the 1-5% of mix monomer total amount.
As preferably, the mix monomer component of described latex is:
(1) vinylidene chloride, its consumption are the 80-85% of mix monomer total amount;
(2) acrylic ester monomer, its consumption are the 15-20% of mix monomer total amount;
(3) unsaturated fatty acids, its consumption are the 1-5% of mix monomer total amount.
As preferably, the mix monomer component of described latex is:
(1) vinylidene chloride, its consumption are the 80-85% of mix monomer total amount;
(2) acrylic ester monomer, its consumption are the 15-20% of mix monomer total amount;
(3) unsaturated fatty acids, its consumption are the 1-4.5% of mix monomer total amount.
Preferred as in each above-mentioned scheme, acrylic ester monomer comprise one or more of ethyl propenoate, n-butyl acrylate, ethyl acrylate, glycidyl methacrylate.
Preferred as in each above-mentioned scheme, unsaturated fatty acids is a kind of of vinylformic acid, methacrylic acid or their mixture.
Preferred as in each above-mentioned scheme, emulsifying agent is a kind of of OP-10, OP-35, NP-35, NP-40, its consumption is for accounting for mix monomer gross weight 4-6%.Adopted to add above-mentioned nonionic emulsifier, often needed when in use to add many ionic comonomers, and made latex become unstable mainly due to above-mentioned latex.Therefore, the PVDC emulsion major part that the present invention does adopts nonionic emulsifier, has improved the ion stability of emulsion.
The present invention is by the content of rising vinylidene, reduces the monomeric content of unsaturated fatty acids, make the latex drying after, have water tolerance preferably; Be added to the lower acrylic ester monomer of acrylate soft monomer, particularly second-order transition temperature, make processing back cloth have certain flexibility.Non-woven fabrics after the present invention handles is harder, and rich elasticity preferably also has water tolerance, thermotolerance and wrinkle resistance preferably simultaneously.Therefore, be specially adapted to processing and the coating at the carpet back side and the processing of other non-woven fabrics of tent cloth.
In addition, water-based PVDC latex of the present invention is a kind of water-base resin, has extraordinary intermiscibility with ACRYLIC EMULSION, with ACRYLIC EMULSION type treatment agent and usefulness, has extraordinary modified effect.
In order to realize second above-mentioned purpose, the present invention mainly is achieved through the following technical solutions:
The preparation method of water PVDC latex specially for painting special cloth, described water PVDC latex specially for painting special cloth is formed by the copolymerization of seed semi-continuous emulsion polymerizing mode in the presence of nonionic emulsifier by vinylidene chloride, acrylic ester monomer and unsaturated fatty acids.
As preferably, the preparation method of above-mentioned water-based PVDC latex comprises following processing step:
(1) the still material is joined in the reactor, stir;
(2) with air in the abundant replacement reaction kettle of nitrogen; Vacuumize the mix monomer that sucks 5-20%;
(3) heat up, when temperature rises to 35～45 ℃; Begin to add initiator; Continue to heat up, when temperature rises to 50-55 ℃, react when pressure obviously descends, add remaining mix monomer and emulsifying agent by the volume pump average rate, the reinforced time is 8～12 hours, and the reinforced time of initiator is 12～18 hours;
(4) add material after, be warming up to 60～70 ℃, adopt vacuum to take off the method for analysing and remove residual monomer, the time is 2～4 hours;
(5) cool to then below 35 ℃, the stainless steel filtering net above with 100 orders filters discharging.
As preferably, the still material package in the above-mentioned step 1 is drawn together 80 parts of deionized waters, 0.2 part of ionic emulsifying agent, 0.004 part of organo-peroxide and is helped reductive agent on a small quantity.
As preferably, above-mentioned initiator is the redox system of t-butyl hydrogen peroxide and rongalite.
The present invention adopts the preparation of seeded emulsion polymerization method, earlier what is called " seed " polymerization will be carried out in the disposable adding reactor of 5～20% mix monomer, on this seed, carry out the polymerization of " on the seed " then, help controlling the quantity and the size of present latex particulate, all even enough big to guarantee the present latex particulate diameter.Adopt the semi-continuous emulsion polymerizing method to carry out polymerization in the polymerization of " on the seed ", add mix monomer, emulsifying agent, initiator to control the growth of present latex particulate, improved the stability of latex with the constant speed of successive.
Embodiment
Below by embodiment, technical scheme of the present invention is described in further detail.
Embodiment 1:
Specific operation process: earlier with 80 kilograms of deionized waters, help reductive agent on a small quantity, 500 gram alkyl sodium sulfonates are added to and lead to the air that nitrogen is fully replaced the inside in the reactor, the mix monomer of suction 10% heats up then, adds initiator A, B solution when temperature rises to 40 ℃.When temperature rises to 52 ℃, react when pressure obviously descends, continuously the mix monomer of remainder is joined in the reactor by volume pump, maintain the temperature at simultaneously 50-55 ℃ constant.The control mix monomer time of squeezing into is 10 hours, and the time of squeezing into of initiator is 15 hours.After finishing, the mix monomer adding continues to add initiator 1 hour, pressure will remain unchanged after will reducing to necessarily this moment, after pressure remained unchanged 30 minutes, stop to add initiator, reactor temperature is risen to 65 ℃, take off the suction method with vacuum and deviate from residual monomer 3 hours, cool to then below 35 ℃, the stainless steel filtering net above with 100 orders filters discharging.
Embodiment 2:
Repeat embodiment 1, the difference of present embodiment and embodiment 1 is that the component of mix monomer is:
(1) vinylidene chloride (VDC), consumption is 80kg;
(2) methacrylic acid (MAA), consumption is 2kg;
(3) Isooctyl acrylate monomer 18kg.
Embodiment 3:
Repeat embodiment 1, the difference of present embodiment and embodiment 1 is that the component of mix monomer is:
(1) vinylidene chloride (VDC), consumption is 80kg;
(2) methacrylic acid (MAA), consumption is 4.5kg;
(3) Isooctyl acrylate monomer 15.5kg.
Embodiment 4:
Repeat embodiment 1, the difference of present embodiment and embodiment 1 is, emulsifying agent is OP-35, and consumption is 4%, and other is constant.
The latex that embodiment obtains can and be used with ACRYLIC EMULSION, make ACRYLIC EMULSION the non-woven fabrics treatment agent performance be improved significantly, obtained a kind ofly making the cloth after the processing have certain rigidity, rich elasticity preferably also has the water-based latex of water tolerance, thermotolerance and wrinkle resistance preferably simultaneously.
Claims (10)
1. water PVDC latex specially for painting special cloth is formed by emulsion polymerization way copolymerization in the presence of emulsifying agent, initiator by mix monomer, it is characterized in that the mix monomer component of latex comprises:
(1) vinylidene chloride, its consumption are the 80-90% of mix monomer total amount;
(2) contain a kind of acrylic ester monomer of acrylate soft monomer at least, its consumption is the 8-20% of mix monomer total amount;
(3) unsaturated fatty acids, its consumption are the 1-4.5% of mix monomer total amount.
2. water PVDC latex specially for painting special cloth according to claim 1 is characterized in that the mix monomer component of described latex is:
(1) vinylidene chloride, its consumption are the 80-85% of mix monomer total amount;
(2) acrylic ester monomer, its consumption are the 15-20% of mix monomer total amount;
(3) unsaturated fatty acids, its consumption are the 1-4.5% of mix monomer total amount.
3. water PVDC latex specially for painting special cloth according to claim 1 is characterized in that the mix monomer component of described latex is:
(1) vinylidene chloride, its consumption are the 80-85% of mix monomer total amount;
(2) acrylic ester monomer, its consumption are the 15-20% of mix monomer total amount;
(3) unsaturated fatty acids, its consumption are the 1-4.5% of mix monomer total amount.
4. according to claim 1 or 2 or 3 described water PVDC latex specially for painting special cloth, it is characterized in that described acrylic ester monomer comprises one or more of ethyl propenoate, n-butyl acrylate, ethyl acrylate, glycidyl methacrylate.
5. according to claim 1 or 2 or 3 described water PVDC latex specially for painting special cloth, it is characterized in that described unsaturated fatty acids is a kind of of vinylformic acid, methacrylic acid or their mixture.
6. according to claim 1 or 2 or 3 described water PVDC latex specially for painting special cloth, it is characterized in that described emulsifying agent is a kind of of OP-10, OP-35, NP-35, NP-40, its consumption is for accounting for mix monomer gross weight 4-6%.
7. according to the preparation method of claim 1 or 2 or 3 described water PVDC latex specially for painting special cloth, it is characterized in that described water PVDC latex specially for painting special cloth is formed by the copolymerization of seed semi-continuous emulsion polymerizing mode in the presence of nonionic emulsifier by vinylidene chloride, acrylic ester monomer and unsaturated fatty acids.
8. the preparation method of water PVDC latex specially for painting special cloth according to claim 6 is characterized in that comprising following processing step:
(1) the still material is joined in the reactor, stir;
(2) with air in the abundant replacement reaction kettle of nitrogen; Vacuumize the mix monomer that sucks 5-20%;
(3) heat up, when temperature rises to 35～45 ℃; Begin to add initiator; Continue to heat up, when temperature rises to 50-55 ℃, react when pressure obviously descends, add remaining mix monomer and emulsifying agent by the volume pump average rate, the reinforced time is 8～12 hours, and the reinforced time of initiator is 12～18 hours;
(4) add material after, be warming up to 60～70 ℃, adopt vacuum to take off the method for analysing and remove residual monomer, the time is 2～4 hours;
(5) cool to then below 35 ℃, the stainless steel filtering net above with 100 orders filters discharging.
9. the preparation method of water PVDC latex specially for painting special cloth according to claim 7 is characterized in that the still material package in the step 1 is drawn together 80 parts of deionized waters, 0.2 part of ionic emulsifying agent, 0.004 part of organo-peroxide and helped reductive agent on a small quantity.
10. the preparation method of water PVDC latex specially for painting special cloth according to claim 7 is characterized in that described initiator is the redox system of t-butyl hydrogen peroxide and rongalite.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2006101550856A CN1986583B (en) | 2006-12-07 | 2006-12-07 | Water PVDC latex specially for painting special cloth and its preparing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2006101550856A CN1986583B (en) | 2006-12-07 | 2006-12-07 | Water PVDC latex specially for painting special cloth and its preparing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1986583A CN1986583A (en) | 2007-06-27 |
| CN1986583B true CN1986583B (en) | 2010-08-11 |
Family
ID=38183538
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2006101550856A Expired - Fee Related CN1986583B (en) | 2006-12-07 | 2006-12-07 | Water PVDC latex specially for painting special cloth and its preparing method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1986583B (en) |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103059201B (en) * | 2012-12-26 | 2015-04-22 | 海南必凯水性涂料有限公司 | Polyvinylidene chloride copolymer emulsion for pharmaceutical packing coating and preparation method and application thereof |
| CN103059202A (en) * | 2012-12-26 | 2013-04-24 | 海南必凯水性涂料有限公司 | Polyvinylidene chloride copolymer emulsion for pharmaceutical packing coating and preparation method and application thereof |
| CN103044603B (en) * | 2012-12-26 | 2016-03-16 | 海南必凯水性涂料有限公司 | Food packaging latex and its preparation method and application |
| CN103405335A (en) * | 2013-08-02 | 2013-11-27 | 山东威高集团医用高分子制品股份有限公司 | Surface-modified rubber plug and preparation method thereof |
| CN105153345A (en) * | 2015-09-25 | 2015-12-16 | 南通瑞普埃尔生物工程有限公司 | Preparation method of PVDC emulsion for water-based environment-friendly tableware |
| CN105153346A (en) * | 2015-09-29 | 2015-12-16 | 南通瑞普埃尔生物工程有限公司 | Special waterborne anti-corrosion emulsion for multi-component copolymerization rust converting primer and preparation method of emulsion |
| CN105294913B (en) * | 2015-11-25 | 2017-04-19 | 海南赛诺实业有限公司 | PVDC copolymerization emulsion for flame-retardant carpets, preparation method and applications thereof |
| CN107602753B (en) * | 2017-10-10 | 2019-07-26 | 上海路丰助剂有限公司 | A kind of rare earth/metallic compound function monomer and its preparation method and application |
| EP3677601B1 (en) | 2017-10-10 | 2023-06-21 | Shanghai Lufeng Auxiliary Co., Ltd | Rare earth/metal compound functional monomer and preparation method therefor and application thereof |
| CN109134736A (en) * | 2018-06-21 | 2019-01-04 | 安徽大学 | A kind of anticorrosive paint aqueous polyvinylidene dichloroethylene-acrylic ester copolymer latex and preparation method thereof |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1715559A (en) * | 2005-01-11 | 2006-01-04 | 东阳市野风塑胶有限公司 | Latex for coating drinking filter bag cotton paper and its preparing method |
-
2006
- 2006-12-07 CN CN2006101550856A patent/CN1986583B/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1715559A (en) * | 2005-01-11 | 2006-01-04 | 东阳市野风塑胶有限公司 | Latex for coating drinking filter bag cotton paper and its preparing method |
Non-Patent Citations (1)
| Title |
|---|
| CN 1715559 A,权利要求1－10以及实施例. |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1986583A (en) | 2007-06-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1986583B (en) | Water PVDC latex specially for painting special cloth and its preparing method | |
| CN104725550B (en) | Water resistant whiting emulsion pressure sensitive adhesive synthesis method | |
| AU759685B2 (en) | A process for the preparation of aqueous dispersions of latex particles having a heterogeneous morphology, the latex particles obtainable with the process, the dispersions and redispersible powders, as well as the use thereof | |
| CN103864976B (en) | The pre-emulsification semi-continuous seed emulsion polymerization technique of self-crosslinking styrene-acrylic emulsion for a kind of nonwoven | |
| CN103788298A (en) | Preparation method of carboxylated nitrile latex and article prepared from carboxylated nitrile latex | |
| CN107619449A (en) | A kind of environment-friendly type high solid content and low viscosity acrylic resin and preparation method thereof | |
| JP2002201242A5 (en) | ||
| JP4488401B2 (en) | Use of copolymers based on acrylamide alkyl sulfonic acids as thickeners in preparations containing organic solvents | |
| CN102408505A (en) | Method for preparing super absorbent resin by inverse suspension polymerization | |
| CN101775105B (en) | Preparation method of high-impact polyacrylate grafting vinyl chloride emulsion copolymer resin | |
| CN101056931A (en) | Process for preparing silicone-modified polymers | |
| CN102382235B (en) | Acrylic emulsion, preparation method and application thereof | |
| CN102070741B (en) | Novel hot-seal adhesive emulsion and preparation method thereof | |
| CN106189950B (en) | A kind of aqueous, environmental protective high intensity sticker adhesive and preparation method thereof | |
| CN1294326C (en) | Latex for coating drinking filter bag cotton paper and its preparing method | |
| CN103275260A (en) | Preparation method of acrylic plastic-plastic composite latex | |
| KR20000071052A (en) | Emulsifier For Aqueous Emulsion Polymerization | |
| CN102559103B (en) | Fine pasting glue and preparing process thereof | |
| CN109837046A (en) | A kind of compound aqueous adhesive and preparation method thereof of plastic film dry type | |
| JP6961478B2 (en) | Soil modifier, soil modifier | |
| CN107383119A (en) | A kind of method using alkyl-glucoside Lipase absobed modified acrylate emulsion | |
| CN102070738B (en) | Preparation method of hydroxyl group-containing functional monomer modified acrylate copolymer emulsion | |
| CN107459609A (en) | A kind of self-cross linking type epoxy/compound soap-free emulsion of polyacrylate and its preparation technology | |
| JP4661448B2 (en) | Low odor copolymer aqueous liquid and process for producing the same | |
| CN108468216A (en) | A kind of spinning sizing agent and preparation method thereof having rapid osmotic performance |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: ZHEJIANG SUNLAND PACKAGE SCIENCE AND TECHNOLOGY CO Free format text: FORMER NAME: ZHEJIANG WILDWIND PLASTIC CO., LTD. |
|
| CP03 | Change of name, title or address |
Address after: 322105, Jinhua City, Zhejiang province Dongyang Song Town Beijiang Industrial Zone Zhejiang Sen Rand Packaging Technology Co., Ltd. Patentee after: ZHEJIANG SENLANDE PACKAGING TECHNOLOGY CO., LTD. Address before: 322105 Beijiang Industrial Zone, Song Town, Zhejiang, Dongyang Patentee before: Zhejiang Wildwind Plastic Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100811 Termination date: 20161207 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |