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.