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Preparation of PU binder resin for synthetic leather

A technology of adhesive resin and manufacturing method, applied in the direction of adhesive, adhesive type, polyurea/polyurethane adhesive, etc., can solve the problems of larger heating area requirements, poor elasticity, caking, etc.

Active Publication Date: 2009-07-08
JIAXING HEXIN CHEM IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the solid content of this type of adhesive is generally only up to 50%. In the winter environment, the resin tends to become turbid or agglomerated, and the produced synthetic leather has low bonding strength and poor elasticity, so it is not suitable for superfiber synthesis. Lamination of leather; and because of its high softening point, usually above 160°C, it is not suitable for the dry lamination process of mirror-like synthetic leather
Japan, South Korea and a small number of domestic large-scale synthetic leather companies usually use two-component PU adhesives. This type of adhesive overcomes the shortcomings of one-component adhesives, and has excellent performance in bonding strength, elasticity, etc., and the resin is transparent. Good performance, can achieve a high solid content of more than 50%, but the two-component PU binder resin has more soft segments, the viscosity stability is poor at the end of the reaction, and the viscosity is easy to drop during storage; use two-component PU for bonding Synthetic leather produced by synthetic resin needs to be placed in a warm room at 60°C to 80°C for 24 to 48 hours before the release paper and synthetic leather can be separated. This usually brings about several problems, one of which is high energy consumption. , it is necessary to build a constant temperature greenhouse, and the larger the output per unit time, the larger the greenhouse area requirement; the second problem is that the turnover of release paper is slow, and more release paper needs to be reserved; the third problem is release paper The use of paper is limited, some release papers that are not resistant to high temperature cannot be used, it is difficult to peel off the release paper and synthetic leather, and the number of times the release paper is used is significantly reduced; the fourth problem is that the product has poor embossing effect

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] (i) the preparation molecular weight is the MPD type polyol of 1000 ± 50:

[0021] Take 500 grams of AA, 432.4 grams of MPD (1.15 times the theoretical value), react at 210 ° C for 5 hours, the acid value reaches 18KOH / g, start vacuuming, after 1.5 hours, the acid value reaches 1.35KOH / g, increase the vacuum The reaction was continued for 30 minutes, and the acid value reached 0.25KOH / g to obtain 639.8 grams of MPD type polyols (theoretical value was 752.7 grams). The measured hydroxyl value was 110.84, and the final molecular weight was 1010.

[0022] (ii) Polymerization:

[0023] 360 grams of polyols obtained by (i) step pre-chain extender MPD 18 grams (1 / 20), MDI 143 grams, solvent DMF 201 grams, MEK 22.3 grams, (solid content is controlled at 70 ± 1%, DMF in the solvent The mass ratio to MEK is 9:1).

[0024] First mix 150 grams of DMF with polyols and MPD evenly, then add 140 grams of MDI in three times, react at 75-85°C to make it viscous, react for 3 hours, th...

Embodiment 2

[0026] (i) the MPD type polyol that preparation molecular weight is 1500 ± 50:

[0027] Take 500 grams of AA, 404.7 grams of MPD (1.15 times the theoretical value), react at 210 ° C for 5 hours, the acid value reaches 19KOH / g, start vacuuming, after 1.5 hours, the acid value reaches 1.42KOH / g, increase the vacuum The reaction was continued for 1 hour, and the acid value reached 0.28KOH / g to obtain 612.1 grams of MPD type polyols (theoretical value was 728.7 grams). The measured hydroxyl value was 73.83 and the final molecular weight was 1517.

[0028] (ii) Polymerization:

[0029] 390 grams of polyols obtained by (i) step pre-chain extender MPD 15.6 grams (1 / 25), MDI111.3 grams, solvent DMF 222.6 grams, MEK 55.7 grams, (solid content is controlled at 65 ± 1%, in solvent The mass ratio of DMF to MEK is 4:1).

[0030]First mix 150 grams of DMF with polyols and MPD evenly, then add 108.3 grams of MDI in three times, react at 75-85 ° C to viscous, react for 3 hours, the viscosi...

Embodiment 3

[0032] (i) the preparation molecular weight is the MPD type polyol of 2000:

[0033] Take 500 grams of AA, 374.5 grams of MPD (1.1 times the theoretical value), react at 215 ° C for 6 hours, the acid value reaches 21.5KOH / g, start vacuuming, after 4 hours, the acid value reaches 1.9KOH / g, increase The reaction was continued under vacuum for 2 hours, and the acid value reached 0.42KOH / g to obtain 595.3 grams of MPD polyols (theoretical value was 717.2 grams). The measured hydroxyl value was 56.43 and the final molecular weight was 1985.

[0034] (ii) Polymerization:

[0035] Press (i) step gained 360 grams of MPD type polyol preparatory chain extender MPD 20 grams (1 / 18), MDI 100.6 grams, solvent DMF 267 grams, MEK 53.4 grams, (solid content is controlled at 60 ± 1%, solvent The mass ratio of DMF to MEK is 5:1).

[0036] First mix 180 grams of DMF with polyols and MPD evenly, then add 97.6 grams of MDI in three times, react at 75-85°C and become viscous, react for 3 hours, t...

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Abstract

The invention relates to a method for manufacturing PU adhesive resin for synthetic leather. The method comprises the following steps that: (i) AA and MPD are heated to undergo esterification and polycondensation reaction, when reaction is carried out till acid value is less than or equal to 25 mgKOH / g, reactant is vacuumized, residual water is removed, the acid value is reduced, when the reaction is carried out till the acid value is less than or equal to 2.5mgKOH / g, the vacuum degree is enlarged, and the reaction is continuously carried out to prepare hydroxyl-end capped MPD type polylol; and (ii) the MPD type polylol prepared in step (i) and a chain extender MPD are mixed, added with DMF, evenly stirred, added with MDI, heated and reacted, and polymerized to generate polyurethane; the polyurethane is added with the DMF and MEK; and the viscosity is adjusted between 12*10 MPa.s / 25 DEG C. The adhesive resin prepared by the method is a semiliquid type PU adhesive, has the advantages of high connecting strength, peeling performance, hot dry pasting, good resin permeability, and the like, can be used for common synthetic leather, and is in particular suitable for ultrafine fiber leather and mirror face rear pasting leather.

Description

technical field [0001] The present invention relates to a kind of manufacture method of PU binder resin for synthetic leather, Background technique [0002] Polyols used in PU binder resins are usually polyester polyols such as ethylene glycol, 1,4-butanediol, diethylene glycol, octapentyl glycol, and 1,6-hexanediol. , Only ethylene glycol and 1,4-butanediol are used as chain extenders. The bonding strength of general PU leather can be produced by using PU binder resin of linear polyols, but there are always various kinds of binders for high-grade synthetic leather such as special microfiber leather and mirror-coated leather. Such limitations. [0003] In the production of synthetic leather, a layer of solvent-diluted PU resin is usually applied on the release paper to a viscosity of 3000-6000cps / 25°C, and the dry-process surface layer PU resin is added with coloring material, and dried; and then coated with a layer Solvent dilutes the viscosity to 6000-20000cps / 25℃, and ...

Claims

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Application Information

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IPC IPC(8): C09J175/06C08G18/42C08G18/76
Inventor 石磊徐欣欣沈连根纪尚超朱崇恩武锦锋
Owner JIAXING HEXIN CHEM IND