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US3997490A Expired / Lapsed US ⏱️ 0.0 years remaining

Aqueous dispersions of amphoteric polyurethane-urea and method of making

Assignee: Kao Corp
•
Filing: 1975-02-03
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Granted: 1976-12-14
•
Expires: 1995-02-03
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Abstract

Abstract A process for the preparation of thermosetting resin emulsions, which comprises (1) reacting an isocyanate-terminated urethane prepolymer with an excess of a polyalkylene-polyamine to form a polyurethane-urea-polyamine, (2) reacting the thus-formed polyurethane-urea-polyamine with an epihalohydrin, (3) rendering the resulting reaction product amphoteric by reacting said reaction product with (a) a compound selected from the group consisting of 1,3-propane sultone, 1,4-butane sultone, β-propiolactone, ε-caprolactone, δ-valerolactone and sodium monohalogenocarboxylates having the formula X(CH 2 ) n COONa, in which X is halogen and n is an integer of 1 to 2, in an amount sufficient to emulsify the final polymer, or by reacting said reaction product (b) with a compound selected from the group consisting of methyl acrylate, ethyl acrylate, methyl methacrylate, ethyl methylacrylate and acrylonitrile, in an amount sufficient to emulsify the final polymer and hydrolyzing the resulting product, and (4) mixing the thus-formed polymer with water.

Inventors

  • 👤 Kazuo Matsuda
  • 👤 Hidemasa Ohmura
  • 👤 Hirakazu Aritaki

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 01:42
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/08; C08G18/0804; C08G18/0833; C08G18/10

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 408 words
A process for preparing an amphoteric thermosetting polyurethane emulsion, which consists essentially of: 1. reacting, in the liquid phase and in a ketone solvent, at a temperature of from -20° to +70° C., (A) isocyanate-terminated urethane prepolymer prepared by reacting organic polyol having a molecular weight in the range of from 200 to 10,000 with an excess of organic polyisocyanate, with (B) an excess of polyalkylene polyamine having at least two primary or secondary amino groups, the total mole number of primary and secondary amino groups in the polyalkylene polyamine being greater than the total mole number of isocyanate groups in the isocyanate-terminated urethane prepolymer, the reaction being carried out until the presence of --NCO groups cannot be detected, whereby to form polyurethane-urea-polyamine, 2. reacting, in the liquid phase, the reaction product of step 1 with an epihalohydrin, at a temperature of +20° to +70° C., for 0.5 to 5 hours, the amount of said epihalohydrin being in the range of from 0.2 to 1.0 moles per mole of the primary and secondary amino groups of said polyurethane-urea-polyamine, 3. reacting, in the liquid phase, the reacting product of step 2 with either a. a substance selected from the group consisting of 1,3-propane sultone, 1,4-butane sultone, β-propiolactone, ε-caprolactone, δ-valerolactone and sodium monohalogenated carboxylate, at a temperature of +40° to +70° C., for 3 to 7 hours, the amount of said substance being in the range of 0.5 to 2.0 moles per mole of amino groups of the polyurethane-urea-polyamine and sufficient to render amphoteric the amino groups of the reaction product of step 2 so that a stable emulsion is formed when water is added and blended in the product of step 3(a), or b. a substance selected from the group consisting of methyl acrylate, ethyl acrylate, methyl methacrylate, ethyl methacrylate, and acrylonitrile, at a temperature of 40° to 70° C., for 3 to 7 hours and then hydrolyzing the reaction product, the amount of said substance (b) being in the range of 0.5 to 2.0 moles per mole of amino groups of the polyurethane-urea-polyamine and being sufficient to render amphoteric the amino group of the reaction product of step 2 so that a stable emulsion can be formed when water is added and blended in the product of step 3(b), 4. treating the product of step 3 to remove the organic solvent therefrom and adding water thereto and thereby obtaining an aqueous thermosetting polyurethane emulsion as a final product.
Claim 2
Dependent Claim 408 words
A process for preparing an amphoteric thermosetting polyurethane emulsion, which consists essentially of: 1. reacting, in the liquid phase and in a ketone solvent, at a temperature of from -20° to +70° C., (A) isocyanate-terminated urethane prepolymer prepared by reacting organic polyol having a molecular weight in the range of from 200 to 10,000 with an excess of organic polyisocyanate, with (B) an excess of polyalkylene polyamine having at least two primary or secondary amino groups, the total mole number of primary and secondary amino groups in the polyalkylene polyamine being greater than the total mole number of isocyanate groups in the isocyanate-terminated urethane prepolymer, the reaction being carried out until the presence of --NCO groups cannot be detected, whereby to form polyurethane-urea-polyamine, 2. reacting, in the liquid phase, the reaction product of step 1 with an epihalohydrin, at a temperature of +20° to +70° C., for 0.5 to 5 hours, the amount of said epihalohydrin being in the range of from 0.2 to 1.0 moles per mole of the primary and secondary amino groups of said polyurethane-urea-polyamine, 3. reacting, in the liquid phase, the reacting product of step 2 with either a. a substance selected from the group consisting of 1,3-propane sultone, 1,4-butane sultone, β-propiolactone, ε-caprolactone, δ-valerolactone and sodium monohalogenated carboxylate, at a temperature of +40° to +70° C., for 3 to 7 hours, the amount of said substance being in the range of 0.5 to 2.0 moles per mole of amino groups of the polyurethane-urea-polyamine and sufficient to render amphoteric the amino groups of the reaction product of step 2 so that a stable emulsion is formed when water is added and blended in the product of step 3(a), or b. a substance selected from the group consisting of methyl acrylate, ethyl acrylate, methyl methacrylate, ethyl methacrylate, and acrylonitrile, at a temperature of 40° to 70° C., for 3 to 7 hours and then hydrolyzing the reaction product, the amount of said substance (b) being in the range of 0.5 to 2.0 moles per mole of amino groups of the polyurethane-urea-polyamine and being sufficient to render amphoteric the amino group of the reaction product of step 2 so that a stable emulsion can be formed when water is added and blended in the product of step 3(b), 4. treating the product of step 3 to remove the organic solvent therefrom and adding water thereto and thereby obtaining an aqueous thermosetting polyurethane emulsion as a final product.
Claim 3
Dependent Claim 46 words
A process according to claim 1, in which the ratio of (b) the total mole number of amino groups containing active hydrogen atoms in the polyalkylene polyamine, to (a) the total mole number of isocyanate groups in said urethane prepolymer is in the range of 1<b/a≅5.
Claim 4
Dependent Claim 50 words
A process according to claim 1, in which said polyalkylene polyamine has the formula ##STR2## wherein n is an integer larger than one, z is an integer from 2 to 4 and R' is hydrogen, alkyl having one to 4 carbon atoms or hydroxyalkyl having one to 4 carbon atoms.
Claim 5
Dependent Claim 12 words
An aqueous amphoteric polyurethane emulsion prepared by the process of claim 1.
Claim 6
Dependent Claim 24 words
A polyurethane molded product prepared by forming the emulsion of claim 4 into a molded product and then heat-treating the product to effect cross-linking.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-12-14 1980-06-14 1980-12-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-12-14 1984-06-14 1984-12-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-12-14 1988-06-14 1988-12-14 $7700.00 Window Closed / Lapsed

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