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US4025593A Expired / Lapsed US ⏱️ 0.0 years remaining

Fabrication of discontinuous fibrils

Assignee: Hercules LLC
•
Filing: 1975-06-09
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Granted: 1977-05-24
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Expires: 1995-06-09
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Abstract

Abstract A continuous fibrillated structure, formed by the abrupt pressure release of a two-phase liquid mixture of polymer and solvent at elevated temperature and pressure so as to cause the instantaneous vaporization of the solvent, is shredded by introducing a make-up fluid into the two-phase liquid mixture before the pressure release is complete.

Inventors

  • 👤 Carlo Raganato
  • 👤 Georges Voituron

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 20:09
CPC Classifications
D; D01; D01D; D01D5/00; D01D5/11

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 146 words
In a process for the manufacture of a fibrillated structure by the abrupt pressure release of a liquid mixture of molten polymer and solvent which is at a temperature and pressure such as to be in the form of a system of two phases consisting of a continuous liquid phase, which is poor in polymer and a second liquid phase dispersed therein which is rich in polymer, the abrupt pressure release taking place in a device which creates high losses and bringing about the instantaneous vaporization of the solvent and the solidification of the said polymer normally in the form of a continuous fibrillated structure, the improvement which comprises introducing a diluent fluid into the two-phase liquid mixture in the device before the pressure release is completed so that the abrupt pressure release results in the production of discontinuous fibrils instead of a continuous fibrillated structure.
Claim 2
Dependent Claim 146 words
In a process for the manufacture of a fibrillated structure by the abrupt pressure release of a liquid mixture of molten polymer and solvent which is at a temperature and pressure such as to be in the form of a system of two phases consisting of a continuous liquid phase, which is poor in polymer and a second liquid phase dispersed therein which is rich in polymer, the abrupt pressure release taking place in a device which creates high losses and bringing about the instantaneous vaporization of the solvent and the solidification of the said polymer normally in the form of a continuous fibrillated structure, the improvement which comprises introducing a diluent fluid into the two-phase liquid mixture in the device before the pressure release is completed so that the abrupt pressure release results in the production of discontinuous fibrils instead of a continuous fibrillated structure.
Claim 3
Dependent Claim 26 words
A process as defined in claim 1, wherein the diluent fluid is introduced into the two-phase liquid mixture before the abrupt pressure release of the latter.
Claim 4
Dependent Claim 14 words
A process as defined in claim 1, wherein the diluent fluid is a gas.
Claim 5
Dependent Claim 13 words
A process as defined in claim 3, wherein the diluent fluid is nitrogen.
Claim 6
Dependent Claim 14 words
A process as defined in claim 1, wherein the diluent fluid is a vapor.
Claim 7
Dependent Claim 14 words
A process as defined in claim 5, wherein the diluent fluid is water vapor.
Claim 8
Dependent Claim 14 words
A process as defined in claim 1, wherein the diluent fluid is a liquid.
Claim 9
Dependent Claim 15 words
A process as defined in claim 7, wherein the diluent fluid is water under pressure.
Claim 10
Dependent Claim 15 words
A process as defined in claim 8, wherein the diluent fluid contains a wetting agent.
Claim 11
Dependent Claim 27 words
A process as defined in claim 1, wherein the diluent fluid is identical with the solvent used for making the two-phase liquid mixture to be released abruptly.
Claim 12
Dependent Claim 35 words
A process as defined in claim 1, wherein the diluent fluid is at a temperature between 20° C. and its boiling point at the pressure at which it is injected into the two-phase liquid mixture.
Claim 13
Dependent Claim 29 words
A process as defined in claim 1, wherein the ratio between the volume of diluent fluid introduced and the volume of two-phase liquid mixture is from 0.3 to 10.
Claim 14
Dependent Claim 26 words
A process as defined in claim 1, wherein the polymer is selected from the group consisting of polyolefins, polyamides, polyesters, polyurethanes, polycarbonates, vinyl and acrylic polymers.

References Cited (Backward Citations)

US2297726A Cited
US2728753A Cited
US2831845A Cited
US2967327A Cited
US3227794A Cited
GB1124578A Cited
US3549732A Cited
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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) 1980-05-23 1980-11-22 1981-05-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-05-23 1984-11-22 1985-05-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-05-23 1988-11-22 1989-05-24 $7700.00 Window Closed / Lapsed

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