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 PDF

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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
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water
mix monomer
consumption
pvdc latex
total amount
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CN1986583A (en
Inventor
应忠芳
何祥麟
阮国富
王婧
季国华
陈荣
黄建
柳继禹
邓焕青
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ZHEJIANG SENLANDE PACKAGING TECHNOLOGY CO., LTD.
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ZHEJIANG WILDWIND PLASTIC CO Ltd
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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

Water PVDC latex specially for painting special cloth and preparation method thereof
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:
Figure G061F5085620061227D000051
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.
CN2006101550856A 2006-12-07 2006-12-07 Water PVDC latex specially for painting special cloth and its preparing method Expired - Fee Related CN1986583B (en)

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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
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
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
JP2020536163A (en) 2017-10-10 2020-12-10 上海路豊助剤有限公司 Rare earth / metal compound functional monomer and its manufacturing method, application
CN109134736A (en) * 2018-06-21 2019-01-04 安徽大学 Aqueous polyvinylidene chloride-acrylate copolymer latex for heavy-duty anticorrosive paint and preparation method thereof

Citations (1)

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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

Patent Citations (1)

* Cited by examiner, † Cited by third party
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

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* Cited by examiner, † Cited by third party
Title
CN 1715559 A,权利要求1-10以及实施例.

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Owner name: ZHEJIANG SUNLAND PACKAGE SCIENCE AND TECHNOLOGY CO

Free format text: FORMER NAME: ZHEJIANG WILDWIND PLASTIC CO., LTD.

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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.

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