← Back to Patent Explorer
US4024307A Expired / Lapsed US ⏱️ 0.0 years remaining

Polyurethane solutions

Assignee: Akzo NV
•
Filing: 1975-02-24
•
Granted: 1977-05-17
•
Expires: 1995-02-24
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for the production of polyurethane solutions by reaction of a diisocyanate with a mixture of a glycol and a polymer bearing terminal hydroxy groups in a solvent medium under certain prescribed conditions. The resulting polyurethane solutions are especially valuable as impregnants or coating agents for textile substrates, for example in the preparation of a microporous synthetic leather.

Inventors

  • 👤 Helmut Brahm
  • 👤 Helmut Schulze

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 21:23
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/65; C08G18/66; C08G18/6603; C08G18/6607; C08G18/08; C08G18/10; C08G18/12; C08K; C08K3/00; C08K3/16; C08K3/32; C08K5/00; C08K5/04; C08K5/09; C08K5/16; C08K5/17; Y; Y10; Y10S; Y10S428/00; Y10S428/904; Y10T; Y10T428/00; Y10T428/31504; Y10T428/31551; Y10T428/31591; Y10T442/00; Y10T442/20; Y10T442/2139; Y10T442/2148

Claims Analysis

Total Claims: 31
Claim 1
Independent Claim 146 words
In a process for the production of polyurethane solutions by reaction of hydroxy compounds with diisocyanates in a solvent consisting essentially of dimethylformamide, the improvement which comprises: concurrently reacting (a) one mol of a polyester or polyether having hydroxy end groups and a molecular weight of about 800 to 4000 and (b) 1.2 to 9 mols of an aliphatic glycol of 2 to 9 carbon atoms in said dimethylformamide together with (c) a diisocyanate at a temperature of about 80° C. to 110° C., the reaction being carried out at a concentration in the solvent of about 25 to 45% by weight of the initial reactants; maintaining a molar ratio of NCO-groups to OH-groups of about 1 ± 0.08 during the reaction; and stopping the reaction after reaching a viscosity of about 200 to 3500 poise, measured at 20° C., by addition of a monovalent alcohol.
Claim 2
Dependent Claim 146 words
In a process for the production of polyurethane solutions by reaction of hydroxy compounds with diisocyanates in a solvent consisting essentially of dimethylformamide, the improvement which comprises: concurrently reacting (a) one mol of a polyester or polyether having hydroxy end groups and a molecular weight of about 800 to 4000 and (b) 1.2 to 9 mols of an aliphatic glycol of 2 to 9 carbon atoms in said dimethylformamide together with (c) a diisocyanate at a temperature of about 80° C. to 110° C., the reaction being carried out at a concentration in the solvent of about 25 to 45% by weight of the initial reactants; maintaining a molar ratio of NCO-groups to OH-groups of about 1 ± 0.08 during the reaction; and stopping the reaction after reaching a viscosity of about 200 to 3500 poise, measured at 20° C., by addition of a monovalent alcohol.
Claim 3
Dependent Claim 17 words
The process of claim 1 wherein a stabilizer is added to the solution after stopping the reaction.
Claim 4
Dependent Claim 13 words
The process of claim 1 wherein polyethylene adipate is used as the polyester.
Claim 5
Dependent Claim 13 words
The process of claim 1 wherein polytetramethylene glycol is used as the polyether.
Claim 6
Dependent Claim 24 words
The process of claim 1 wherein a mixed polyester of adipic acid esterified with ethylene glycol and butylene glycol is used as the polyester.
Claim 7
Dependent Claim 17 words
The process of claim 1 wherein component (a) is a mixture of a polyester and a polyether.
Claim 8
Dependent Claim 17 words
The process of claim 6 wherein component (a) is a mixture of polyethylene adipate and polytetramethylene glycol.
Claim 9
Dependent Claim 27 words
The process of claim 1 wherein the simultaneously used components (a) and (b) taken together as a mixture have a hydroxyl number of about 180 to 200.
Claim 10
Dependent Claim 27 words
The process of claim 1 wherein the simultaneously used components (a) and (b) taken together as a mixture have a hydroxyl number of about 200 to 250.
Claim 11
Dependent Claim 39 words
The process of claim 1 wherein the polyester or polyether of component (a) exhibits a reaction velocity constant K 2 =1.0 to 10 × 10 - 3 l./mol×sec. in a reaction with 4,4'-diphenylmethane-diisocyanate in dimethyl formamide at 25° C.
Claim 12
Dependent Claim 18 words
The process of claim 10 wherein said constant K 2 =2 to 4 × 10 - 3 l./mol×sec.
Claim 13
Dependent Claim 20 words
The process of claim 1 wherein the reaction is carried out at a temperature of about 90° to 95° C.
Claim 14
Dependent Claim 31 words
The process of claim 1 wherein the concentration of initial reactants or the corresponding reaction products in the solvent during the reaction is maintained between about 30 and 40% by weight.
Claim 15
Dependent Claim 36 words
The process of claim 1 wherein the molar ratio of NCO-groups to OH-groups during the reaction is maintained constant in the range of 0.93 to 0.98 with a variation of not more than about ± 0.02.
Claim 16
Dependent Claim 36 words
The process of claim 1 wherein the molar ratio of NCO-groups to OH-groups during the reaction is maintained constant in the range of 0.93 to 0.98 with a variation of not more than about ± 0.01.
Claim 17
Dependent Claim 58 words
The process of claim 14 wherein the reaction is first carried out up to about 90% conversion of the functional reactive groups at a molar ratio of NCO-groups to OH-groups of between about 0.93 and 0.96 and thereafter the reaction is completed with the addition of the diisocyanate to increase said molar ratio to about 0.98 ± 0.015.
Claim 18
Dependent Claim 39 words
The process of claim 10 wherein the initially selected polyester or polyether of component (a) is deactivated and is used in combination with an activator to provide said constant K 2 = 1.0 to 10 × 10 3 l./mol×sec.
Claim 19
Dependent Claim 41 words
The process of claim 11 wherein the initially selected polyester or polyether of component (a) is deactivated and is used in combination with an activator to provide said constant K 2 = 2 to 4 × 10 - 3 l./mol× sec.
Claim 20
Dependent Claim 19 words
The process of claim 1 wherein the polyester or polyether being used is essentially free of a heavy metal.
Claim 21
Dependent Claim 18 words
The process of claim 1 wherein ethanol is added as the monovalent alcohol used to stop the reaction.
Claim 22
Dependent Claim 15 words
The process of claim 20 wherein a solution of ethanol in dimethyl formamide is used.
Claim 23
Dependent Claim 11 words
The process of claim 2 wherein the stabilizer is salicylic acid.
Claim 24
Dependent Claim 16 words
The process of claim 22 wherein a solution of salicylic acid in dimethyl formamide is used.
Claim 25
Dependent Claim 10 words
The polyurethane solution obtained by the process of claim 1.
Claim 26
Dependent Claim 19 words
The process of claim 1 wherein the resulting polyurethane solution is used to impregnate or coat a textile substrate.
Claim 27
Dependent Claim 27 words
The process of claim 8 wherein the resulting polyurethane solution is used to impregnate or coat a textile substrate in the production of a microporous synthetic leather.
Claim 28
Dependent Claim 27 words
The process of claim 9 wherein the resulting polyurethane solution is used to impregnate or coat a textile substrate in the production of a microporous synthetic leather.
Claim 29
Dependent Claim 13 words
A coated textile substrate obtained by the process as claimed in claim 25.
Claim 30
Dependent Claim 13 words
A synthetic leather product obtained by the process as claimed in claim 26.
Claim 31
Dependent Claim 13 words
A synthetic leather product obtained by the process as claimed in claim 27.

References Cited (Backward Citations)

US3457326A Cited
US3236811A Cited
US3635907A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-05-16 1980-11-15 1981-05-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-05-16 1984-11-15 1985-05-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-05-16 1988-11-15 1989-05-17 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag