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Waterborne polyurethane-acrylate interpenetrating polymer network copolymer emulsion continuous production method and device

A technology of urethane acrylate and interpenetrating polymer, which is applied in the field of continuous production method and equipment of water-based urethane acrylate interpenetrating polymer network copolymer emulsion, can solve the mismatch between temperature and flow, deviation of product and formula design, labor intensity It can reduce the number of operators and equipment such as pumps, reduce the frequency of equipment failures, and reduce the labor intensity of personnel.

Active Publication Date: 2016-08-31
广东多正树脂科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] (1) The production process adopts "better soldiers and simpler administration" --- there are only one or two reactors in total, and there are more or less residues, cross-infection, and by-products in the reactor between the upper and lower processes or between production batches The ratio is increased, and the deviation from the formula design is large
(2), and because the reaction temperature sections required by each process flow are not exactly the same, the reaction is carried out in the same kettle, the temperature control is not timely, the side reactions increase, the molecular weight distribution is wide, the product purity is low, and the performance declines
(3), or add a few more sets of equipment, lack of system, increase pumps and pipelines and transport materials over many bends or long distances, temperature and flow do not match, materials are easy to block or leak in pumps or pipelines and other equipment, labor High strength, more equipment failures, material adhesion, large loss, low production yield and reduced production efficiency, the product deviates from the original design of the formula
(4) In the process of removing the solvent from the dispersion, the traditional process has no cyclone separator, the recovered solvent has a high water content, the recovered solvent has a narrow use area, low-cost treatment, and is allocated to the production cost of the emulsion, and the production cost of the emulsion increases.

Method used

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  • Waterborne polyurethane-acrylate interpenetrating polymer network copolymer emulsion continuous production method and device

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] The continuous production method of aqueous polyurethane acrylate interpenetrating polymer copolymer emulsion, it comprises the steps:

[0025] a. The addition of the following ingredients is calculated by weight. First, put 12 parts of PCL and 86 parts of PBA into the high-temperature kettle, raise the temperature to 120°C, start the vacuum pump, and dehydrate under reduced pressure for 1 hour for later use. Then add 7 parts of HDI and 6 parts of IPDI Add 2 drops of DBTDL to the prepolymerization reactor, open the bottom valve of the high temperature kettle, let the polyol in the high temperature kettle be naturally put into the prepolymerization reactor, draw a vacuum in the prepolymerization reactor, and completely suck the materials in the high temperature kettle into the prepolymerization reactor; again keep the inner temperature of the prepolymerization reactor at 80°C-90°C for prepolymerization for 2 hours, slightly lower the temperature to 70°C-80°C, add 0.2 part...

Embodiment 2

[0029] In this embodiment, it includes the following steps:

[0030] a. The addition of the following ingredients is calculated by weight. First, put 13 parts of PCL and 87 parts of PBA into the high-temperature kettle, raise the temperature to 120°C, start the vacuum pump, and dehydrate under reduced pressure for 1.1 hours for later use. Then add 6 parts of HDI, 5 parts of IPDI Add 2 drops of DBTDL and DBTDL into the prepolymerization reactor, open the bottom valve of the high temperature kettle, let the polyol in the high temperature kettle be naturally put into the prepolymerization reactor, and draw a vacuum in the prepolymerization reactor to completely discharge the materials in the high temperature kettle Inhale into the pre-polymerization reactor; keep the inner temperature of the pre-polymerization reactor at 80°C-90°C for 2.2 hours of pre-polymerization, slightly lower the temperature to 70°C-80°C, add 0.1 parts of TMP, 0.4 parts of BDO, and react for 1.1 hours After...

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Abstract

The invention discloses a waterborne polyurethane-acrylate interpenetrating polymer network copolymer emulsion continuous production method and device. The method comprises carrying out polyol manufacture or polyol dehydration through a high temperature reactor, putting the product into a prepolymerization reactor, carrying out performed polymer synthesis, hydrophilic chain extension and primary acrylate grafting insertion into the polyurethane performed polymer, transferring the performed polymer into a high-speed dispersion kettle, carrying out neutralization, adding water into the high-speed dispersion kettle, carrying out high-speed dispersion to obtain a uniform dispersion liquid, transferring the dispersion liquid into a solvent removal or polymerization kettle, carrying out secondary chain extension, carrying out reduced pressure removal on the solvent in the dispersion liquid, reducing water in the gaseous solvent through a cyclone separator and carrying out acrylate pre-emulsion-polyurethane copolymerization in an emulsification kettle to obtain a high-quality waterborne polyurethane-acrylate interpenetrating polymer network copolymer emulsion. The method and device greatly reduce labor intensity, reduce material adhesion caused by fault of a pipe device such as a pump, greatly improve production efficiency, reduce a formula material loss and reduce a production cost.

Description

technical field [0001] The invention relates to the technical field of chemical adhesive production, in particular to a continuous production method and equipment for water-based polyurethane acrylate interpenetrating polymer network copolymerization emulsion. Background technique [0002] In recent years, with the increasingly stringent environmental protection regulations in various countries, water-based adhesives have developed rapidly. Water-based polyurethane has good wear resistance, flexibility, low temperature resistance and fatigue resistance, etc., but has poor water resistance, solvent resistance, low solid content, and poor self-thickening property. [0003] Water-based acrylate emulsion: excellent adhesion, low price, excellent color retention, weather resistance, oil resistance. However, it tends to become brittle at low temperature and sticky at high temperature. [0004] Therefore, scientific researchers at home and abroad have modified them with complemen...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F290/06C08F283/00C08F220/14C08F220/18C08F220/32C08F220/02C08F2/01C08G18/75C08G18/73C08G18/67C08G18/66C08G18/42C08G18/34C08G18/12
CPCC08F2/01C08F283/00C08F290/06C08G18/12C08G18/4202C08G18/4238C08G18/4277C08G18/672C08G18/73C08G18/755C08F220/14C08G18/348C08G18/6659C08G18/6633C08G18/0823
Inventor 郑李华曾国良梁建锋
Owner 广东多正树脂科技有限公司
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