US3891785A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for forming a flexible polyurethane coating
Assignee: USM Corp
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Filing: 1973-03-20
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Granted: 1975-06-24
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Expires: 1993-03-20
Abstract
Abstract Process for forming polyurethane films and coatings particularly for fabrics in which the coating composition is a mixture including a polyisocyanate and one or more selected diols and diamines which are mixed in controlled proportions and blended, deposited and spread in a controlled sequence to give a film or coating which retains its uniformity against undue penetration as a coating on fabrics and against beading up as a layer on a release sheet when heated to effect cure.
Inventors
- 👤 John C Zemlin
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 13:33
CPC Classifications
D; D06; D06N; D06N3/00; D06N3/12; D06N3/14; C; C08; C08G; C08G18/00; C08G18/06; C08G18/08; C08G18/0895; D06M; D06M15/00; D06M15/19; D06M15/37; D06M15/564; D06N3/0086; D06N3/0088; D06N3/009
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
484 words
IN THE PROCESS FOR FORMING A FLEXIBLE POLYURETHANE COATING OR FILM INCLUDING THE STEPS OF CONTINUOUSLY INTRODUCING POLYURETHANE-FORMING REAGENTS FROM SUPPLY CONTAINERS TO A MIXING ZONE UNDER TEMPERATURE CONDITIONS MAINTAINING SAID REAGENTS IN LIQUID CONDITION, MIXING SAID REAGENTS IN SAID ZONE, CONTINUOUSLY DISCHARGING THE MIXED REAGENT FROM SAID ZONE AS A SUBSTANTIALLY SOLVENT FREE LIQUID CONTINUOUS STREAM OF A MIXTURE OF SAID REGENTS, SAID REGENTS COMPRISING A POLYISOCYANATE, A DIFUNCTIONAL AMINE IN AMOUNT EQUIVALENT TO FORM ABOUT 5 TO ABOUT 35 PERCENT OF THE REACTIVE :NCO OF SAID POLYISOCYANATE AND A DIOL HAVING A MOLECULAR WEIGHT OF FROM ABOUT 500 TO ABOUT 3,000, THE REACTIVE HYDROGEN OF SAID DIOL AND AMINE BEING SUBSTANTIALLY EQUIVALENT TO THE REACTIVE -NCO GROUPS OF SAID POLYISOCYANATE AND SAID MIXTURE BEING REACTIVE TO FORM A PSEUDOPLASTIC INTERMEDIATE STAGE MATERIAL HAVING AN EXTREMELY HIGH VISCOSITY AT WHICH IT WILL NOT DIVE INTO POROSITIES ON A CASTING SURFACE AT SHEAR RATES APPROCHING ZERO AND VERY MUCH LOWER VISCOSITY SUITABLE FOR BLENDING, SPREADING AND COATING UNDER SHEARING AGITATION, DEPOSITING SAID STREAM OF MIXED REACTANTS ON A CONTAINOUSLY MOVING SURFACE WHOSE PATH LEADS BENEATH A SPREADER ELEMENT AND THEN THROUGH A HEATED CURING ZONE, SAID SPREADER ELEMENT EXTENDING ACROSS SAID SURFACE AND BEING DISPOSED RELATIVE TO SAID SURFACE TO FORM A LAYER ON SAID SURFACE BY ALLOWING PASSAGE BETWEEN SAID ELE-MENT AND SAID SURFACE OF A THICKNESS OF SAID MIXTURE ON SAID SURFACE DETERMINED BY THE DESIRED THICKNESS OF SAID COATING OR FILM AND TO HOLD BACK PASSAGE OF MIXED REACTANTS ON SAID SURFACE GREATER THAN SAID DETERMINED THICKNESS ABOVE SAID SURFACE, REACTING SUCCESSIVE PORTIONS OF SAID MIXTURE OF REAGENTS TO SAID PSEUDOPLASTIC INTERMEDIATE STATE WHILE BEING MOVED TOWARD SAID SPREADER ELEMENT, COLLECTING ON SAID SURFACE MIXED MATERIAL HELD BACK BY SAID SPREADER ELEMENT AS A BANK, THE RELATIVE MOVEMENT BETWEEN SAID SURFACE AND SAID SPREADER ELEMENT CREATING SHEARING AGITATION IN AND A ROLLING MOVEMENT OF SAID BANK TO PROVIDE SAID LOWER VISOCSITY STATE IN THE MATERIAL IN SAID BANK, CONTINUOUSLY INCORPORATING AND BLENDING FURTHER MIXTURE FROM SAID SURFACE INTO THE MASS OF REACTIVE MIXTURE IN SAID BANK, SPREADER ELEMENT, WITHDRAWING BANK ON SAID SURFACE BY SAID SPREADER ELEMENT, WITHDRAWING PORTIONS OF THE BLENDED MATERIAL ON SAID SURFAE FROM THE AGITATED MASS IN SAID BANK AS A LAYER PASSING BENEATH SAID SPREADER ELEMENT WHILE THE MASS REMAINS SPREADABLE THROUGH BALANCE OF FRESHLY MIXED AGAINST PREVIOUSLY MIXED REAGENTS AND DOES NOT SET UP, CONTROLLING THE SIZE OF THE AGITATED MASS IN SAID BANK BY CORRELATION OF THE RATE OF SUPLY OF THE MIXTURE OF REGENTS TO SAID SURFACE AND THE RATE OF WITHDRAWAL TO PROVIDE DWELL TIME OF REACTIVE MIXTURE IN SAID BANK, THE VISCOSITY OF SAID MIXTURE IN SAID LAYER BECOMING EXTREMELY HIGH WHEN THE LAYER HAS LEFT THE SPERADER ELEMENT AND SHEARING AGITATION CEASES, AND THEN HEATING SAID LAYER TO CURING TEMPERATURE DURING PASSAGE ON SAID SURFACE THROUGH SAID HEATED CURING ZONE.
Claim 2
Dependent Claim
484 words
IN THE PROCESS FOR FORMING A FLEXIBLE POLYURETHANE COATING OR FILM INCLUDING THE STEPS OF CONTINUOUSLY INTRODUCING POLYURETHANE-FORMING REAGENTS FROM SUPPLY CONTAINERS TO A MIXING ZONE UNDER TEMPERATURE CONDITIONS MAINTAINING SAID REAGENTS IN LIQUID CONDITION, MIXING SAID REAGENTS IN SAID ZONE, CONTINUOUSLY DISCHARGING THE MIXED REAGENT FROM SAID ZONE AS A SUBSTANTIALLY SOLVENT FREE LIQUID CONTINUOUS STREAM OF A MIXTURE OF SAID REGENTS, SAID REGENTS COMPRISING A POLYISOCYANATE, A DIFUNCTIONAL AMINE IN AMOUNT EQUIVALENT TO FORM ABOUT 5 TO ABOUT 35 PERCENT OF THE REACTIVE :NCO OF SAID POLYISOCYANATE AND A DIOL HAVING A MOLECULAR WEIGHT OF FROM ABOUT 500 TO ABOUT 3,000, THE REACTIVE HYDROGEN OF SAID DIOL AND AMINE BEING SUBSTANTIALLY EQUIVALENT TO THE REACTIVE -NCO GROUPS OF SAID POLYISOCYANATE AND SAID MIXTURE BEING REACTIVE TO FORM A PSEUDOPLASTIC INTERMEDIATE STAGE MATERIAL HAVING AN EXTREMELY HIGH VISCOSITY AT WHICH IT WILL NOT DIVE INTO POROSITIES ON A CASTING SURFACE AT SHEAR RATES APPROCHING ZERO AND VERY MUCH LOWER VISCOSITY SUITABLE FOR BLENDING, SPREADING AND COATING UNDER SHEARING AGITATION, DEPOSITING SAID STREAM OF MIXED REACTANTS ON A CONTAINOUSLY MOVING SURFACE WHOSE PATH LEADS BENEATH A SPREADER ELEMENT AND THEN THROUGH A HEATED CURING ZONE, SAID SPREADER ELEMENT EXTENDING ACROSS SAID SURFACE AND BEING DISPOSED RELATIVE TO SAID SURFACE TO FORM A LAYER ON SAID SURFACE BY ALLOWING PASSAGE BETWEEN SAID ELE-MENT AND SAID SURFACE OF A THICKNESS OF SAID MIXTURE ON SAID SURFACE DETERMINED BY THE DESIRED THICKNESS OF SAID COATING OR FILM AND TO HOLD BACK PASSAGE OF MIXED REACTANTS ON SAID SURFACE GREATER THAN SAID DETERMINED THICKNESS ABOVE SAID SURFACE, REACTING SUCCESSIVE PORTIONS OF SAID MIXTURE OF REAGENTS TO SAID PSEUDOPLASTIC INTERMEDIATE STATE WHILE BEING MOVED TOWARD SAID SPREADER ELEMENT, COLLECTING ON SAID SURFACE MIXED MATERIAL HELD BACK BY SAID SPREADER ELEMENT AS A BANK, THE RELATIVE MOVEMENT BETWEEN SAID SURFACE AND SAID SPREADER ELEMENT CREATING SHEARING AGITATION IN AND A ROLLING MOVEMENT OF SAID BANK TO PROVIDE SAID LOWER VISOCSITY STATE IN THE MATERIAL IN SAID BANK, CONTINUOUSLY INCORPORATING AND BLENDING FURTHER MIXTURE FROM SAID SURFACE INTO THE MASS OF REACTIVE MIXTURE IN SAID BANK, SPREADER ELEMENT, WITHDRAWING BANK ON SAID SURFACE BY SAID SPREADER ELEMENT, WITHDRAWING PORTIONS OF THE BLENDED MATERIAL ON SAID SURFAE FROM THE AGITATED MASS IN SAID BANK AS A LAYER PASSING BENEATH SAID SPREADER ELEMENT WHILE THE MASS REMAINS SPREADABLE THROUGH BALANCE OF FRESHLY MIXED AGAINST PREVIOUSLY MIXED REAGENTS AND DOES NOT SET UP, CONTROLLING THE SIZE OF THE AGITATED MASS IN SAID BANK BY CORRELATION OF THE RATE OF SUPLY OF THE MIXTURE OF REGENTS TO SAID SURFACE AND THE RATE OF WITHDRAWAL TO PROVIDE DWELL TIME OF REACTIVE MIXTURE IN SAID BANK, THE VISCOSITY OF SAID MIXTURE IN SAID LAYER BECOMING EXTREMELY HIGH WHEN THE LAYER HAS LEFT THE SPERADER ELEMENT AND SHEARING AGITATION CEASES, AND THEN HEATING SAID LAYER TO CURING TEMPERATURE DURING PASSAGE ON SAID SURFACE THROUGH SAID HEATED CURING ZONE.
Claim 3
Dependent Claim
118 words
The process for forming a flexible polyurethane coating on a surface as defined in claim 1 in which said surface is a flexible fibrous backing, said polyisocyanate and diol are reacted in proportions forming a quasiprepolymer having a reactive -NCO content of from about 12 to about 25 percent by weight constituting a first reactive component, a mixture comprising diamine and further diol is a second reactive component, and said first and second reactive components are continuously mixed and deposited as a stream on said fibrous backing, the deposition on said fibrous backing being carried out when said mixture of reagents has developed a viscosity under substantially zero shear rate of at least about 1 X 106 centipoises.
Claim 4
Dependent Claim
84 words
The process for forming a flexible polyurethane coating on a surface as defined in claim 2 in which said bank is maintained at a diameter of from about 1/2 to about 2 inches coordinated with the rate of movement of said surface relative to said spreader element to provide shearing agitation at a shear rate of the order of 5 to 50 sec. 1 in said bank to reduce the viscosity of the material in the bank to under about 100,000 centipoises for spreading.
Claim 5
Dependent Claim
120 words
The process for forming a flexible polyurethane film as defined in claim 1 in which said surface is a smooth imperVious release sheet, said polyisocyanate and diol are reacted in proportions forming a quasiprepolymer having a reactive - NCO content of from about 12 to about 25 percent by weight constituting a first reactive component, said first and second reactive components are continuously mixed and deposited as a stream on said release sheet, the deposition on said release sheet being carried out when said mixture of reagents has developed a viscosity under substantially zero shear rate of at least about 1 X 106 centipoises and the cured layer being stripped from said release sheet after leaving said heated curing zone.
Claim 6
Dependent Claim
81 words
The process for forming a flexible polyurethane film as defined in claim 4 in which said bank is maintained at a diameter of from about 1/2 to about 2 inches coordinated with the rate of movement of said surface relative to said spreader element to provide shearing agitation at a shear rate of the order of 5 to 50 sec. 1 in said bank to reduce the viscosity of the material in the bank to under about 100,000 centipoises for spreading.
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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) | 1978-06-23 | 1978-12-23 | 1979-06-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1982-06-23 | 1982-12-23 | 1983-06-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1986-06-23 | 1986-12-23 | 1987-06-24 | $7700.00 | Window Closed / Lapsed |