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US4211737A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing synthetic fibers for use in paper-making

Assignee: Montedison SpA
•
Filing: 1977-10-31
•
Granted: 1980-07-08
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Expires: 1997-10-31
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Abstract

Abstract There is disclosed an improvement in the production of microfibers or fibrils of synthetic thermoplastic polymeric materials by flash-spinning solutions, emulsions or suspensions of the synthetic polymers in solvents, under the action of a high-speed jet of gaseous or vaporous fluid having an angular direction with respect to the solution, emulsion or suspension being flash-spun. The improvement consists in causing the fluid jet to expand through a nozzle (or duct) of the convergent-divergent type and in extruding the polymer solution, emulsion or dispersion under flash conditions at an angle towards the fluid jet in expansion in the divergent portion of the nozzle.

Inventors

  • 👤 Giovanni Di Drusco
  • 👤 Deoscaride Zaffagnini

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 08:51
CPC Classifications
D; D01; D01D; D01D5/00; D01D5/11

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 122 words
Process for preparing fibrils or microfibers of synthetic polymers, suitable for use in the manufacture of paper, in which solutions, emulsions or dispersions of fiber-forming thermoplastic polymers in a liquid medium are extruded through a nozzle under conditions such that instantaneous vaporization of the liquid medium occurs in the ambient of extrusion, and are caused to be impacted, in said ambient of extrusion, by a highspeed gaseous fluid jet having an angular direction with respect to the extrusion direction of such solution, emulsion or dispersion, characterized in that said fluid is initially made to expand through a convergent-divergent nozzle of the DeLaval type, and in that the polymeric solution, emulsion or dispersion is extruded into the divergent portion of such convergent-divergent nozzle.
Claim 2
Dependent Claim 122 words
Process for preparing fibrils or microfibers of synthetic polymers, suitable for use in the manufacture of paper, in which solutions, emulsions or dispersions of fiber-forming thermoplastic polymers in a liquid medium are extruded through a nozzle under conditions such that instantaneous vaporization of the liquid medium occurs in the ambient of extrusion, and are caused to be impacted, in said ambient of extrusion, by a highspeed gaseous fluid jet having an angular direction with respect to the extrusion direction of such solution, emulsion or dispersion, characterized in that said fluid is initially made to expand through a convergent-divergent nozzle of the DeLaval type, and in that the polymeric solution, emulsion or dispersion is extruded into the divergent portion of such convergent-divergent nozzle.
Claim 3
Dependent Claim 56 words
The process according to claim 1, in which the polymeric solution, emulsion or dispersion is extruded at, or in proximity to, the terminal section of the divergent portion of the convergent-divergent nozzle of DeLaval type in which the fluid reaches the maximum speed compatible with its thermodynamic conditions upstream of the divergent portion of the nozzle.
Claim 4
Dependent Claim 34 words
The process according to claim 1, in which the polymeric solution, emulsion or dispersion is extruded through a number of nozzles arranged around the divergent portion of the nozzle through which the fluid runs.
Claim 5
Dependent Claim 14 words
The process according to claim 1, in which the gaseous fluid is dry steam.
Claim 6
Dependent Claim 19 words
The process according to claim 1, in which the gaseous fluid is n-hexane in the form of superheated steam.
Claim 7
Dependent Claim 28 words
The process according to claim 1, in which a solution, emulsion or dispersion of polyethylene is extruded into the divergent portion of the convergent-divergent nozzle of DeLaval type.
Claim 8
Dependent Claim 27 words
The process of claim 1, in which a solution, emulsion or dispersion of polypropylene is extruded into the divergent portion of the convergent-divergent nozzle of DeLaval type.

References Cited (Backward Citations)

US2297726A Cited
US2413420A Cited
US2317875A Cited
US2336745A Cited
US2929436A Cited
US3785918A Cited
US3885014A Cited
US3794731A Cited
US4001357A Cited
US3874886A Cited
US3885940A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-07-08 1984-01-07 1984-07-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-07-08 1988-01-07 1988-07-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-07-08 1992-01-07 1992-07-08 $7700.00 Window Closed / Lapsed

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