Solvent-free waterborne polyurethane capable of being continuously produced and preparation method of solvent-free waterborne polyurethane

A water-based polyurethane and solvent-free technology, applied in the field of water-based polyurethane, can solve the problems of poor compatibility between resin and cationic materials, negative impact on consumers and the environment, and inability to realize continuous production, so as to achieve continuous automatic production, save equipment investment, The effect of saving organic solvent resources

Pending Publication Date: 2021-02-05
明新梅诺卡(江苏)新材料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Patent CN108530600A provides a preparation method of solvent-free water-based polyurethane resin, wherein the hydrophilic chain extender uses dimethylol butyric acid, and no organic solvent is used in the synthesis process, which shortens the reaction time to a certain extent, but increases the production cost. At the same time, the use of organic amine neutralizers increases the risk of production and use; in addition, the prepared resin has poor compatibility with cationic materials
[0007] Patent CN201711492249.4 provides a

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0044]Example 1

[0045]Step 1: accurate weighing

[0046]92 parts of isophorone diisocyanate;

[0047]300 parts of polytetrahydrofuran glycol (number average molecular weight is 2000);

[0048]1.5 parts neopentyl glycol;

[0049]38 parts of Ymer-N120 non-ionic hydrophilic glycol of Perstorp Group;

[0050]750 parts of deionized water;

[0051]Step 2: Add polytetrahydrofuran diol and Perstorp’s Ymer-N120 non-ionic hydrophilic diol into the reaction kettle and vacuum dehydration at 120°C for 1 hour;

[0052]Step 3: Cool the reactor to 70°C, add isophorone diisocyanate at a stirring speed of 300r / min, control the temperature to 80°C, and react for 2h;

[0053]Step 4: Add neopentyl glycol to the reaction kettle, control the temperature at 80°C, and react for 2 hours;

[0054]Step 5: Add 10 parts of emulsifier DNS-18 to the reaction kettle, control the temperature at 60°C, and react for 0.5h;

[0055]Step 6: Pass the prepolymer and deionized water through a static mixer, then through a high-gravity dispersion reactor, a

Example Embodiment

[0056]Example 2

[0057]Step 1: accurate weighing

[0058]215 parts of dicyclohexylmethane diisocyanate;

[0059]205 parts of polytetrahydrofuran diol (number average molecular weight is 1000);

[0060]100 parts polypropylene glycol (number average molecular weight is 2000);

[0061]2 parts of 1,4-butanediol;

[0062]46 parts of Ymer-N120 non-ionic hydrophilic glycol of Perstorp Group;

[0063]792 parts of deionized water;

[0064]Step 2: Add polytetrahydrofuran diol, polypropylene glycol and Perstorp’s Ymer-N120 non-ionic hydrophilic diol into the reaction kettle and vacuum dehydration at 120°C for 1.5 hours;

[0065]Step 3: Cool the reactor to 70°C, add dicyclohexylmethane diisocyanate at a stirring speed of 300r / min, control the temperature to 85°C, and react for 2h;

[0066]Step 4: Add 1,4-butanediol to the reaction kettle, control the temperature at 80°C, and react for 2 hours;

[0067]Step 5: Add 20 parts of emulsifier DNS-500 to the reaction kettle, control the temperature at 60°C, and react for 2 hours;

[0068

Example Embodiment

[0069]Example 3

[0070]Step 1: accurate weighing

[0071]115 parts of toluene diisocyanate;

[0072]210 parts of polytetrahydrofuran glycol (number average molecular weight is 2000);

[0073]100 parts of polybutylene adipate diol (number average molecular weight is 1000);

[0074]2 parts of 1,6-hexanediol;

[0075]42 parts of Ymer-N120 non-ionic hydrophilic glycol of Perstorp Group;

[0076]945 parts of deionized water;

[0077]Step 2: Add polytetrahydrofuran diol, polybutylene adipate diol and Perstorp’s Ymer-N120 non-ionic hydrophilic diol into the reaction kettle and vacuum dehydration at 120°C for 1 hour;

[0078]Step 3: Cool the reactor to 50°C, add toluene diisocyanate at a stirring speed of 300r / min, control the temperature to 70°C, and react for 2h;

[0079]Step 4: Add 1,4-butanediol to the reaction kettle, control the temperature at 85°C, and react for 2.5 hours;

[0080]Step 5: Add dimethylethanolamine to the reaction kettle, control the temperature at 40°C, and react for 0.5h;

[0081]Step 6: Pass the prepo

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PUM

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Abstract

The invention discloses solvent-free waterborne polyurethane capable of being continuously produced and a preparation method of the solvent-free waterborne polyurethane, and belongs to the field of preparation of waterborne polyurethane, the solvent-free waterborne polyurethane comprises the following components in parts by weight: 50-200 parts of diisocyanate, 150-50 parts of dihydric alcohol, 1-20 parts of a micromolecular chain extender, 10-45 parts of a nonionic hydrophilic chain extender, 2-50 parts of an emulsifier and 400-1200 parts of deionized water. The method has the beneficial effects that 1) organic pollution is thoroughly eliminated from the source, organic solvent resources are saved, potential safety hazards are eliminated, and the employment environment of workers is improved; 2) the production process is optimized, heavy metal pollution is avoided, and the production cost is reduced; 3) the nonionic hydrophilic chain extender and the emulsifier are introduced at the same time, so that the electrolyte resistance is higher, the compatibility with other materials is good, and the application field is wider; and 4) multiple sets of synthesis reaction kettles are connected in series to share one set of supergravity dispersion reaction equipment, so that the equipment investment is saved, continuous automatic production is realized, and the product stability is higher.

Description

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Claims

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Application Information

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Owner 明新梅诺卡(江苏)新材料有限公司
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