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US3963558A Expired / Lapsed US ⏱️ 0.0 years remaining

Apparatus and method for producing solid polymeric material from a dilute polymer solution

Assignee: W Bar E Inc
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Filing: 1974-12-09
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Granted: 1976-06-15
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Expires: 1994-12-09
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Abstract

Abstract Dilute polymer solution (about 5 to 50% by weight of solid polymer) is heated and flashed in a concentrator, is delivered to an extruder at a concentration of about 30 - 80% by weight of solid polymer, further solvent is vaporized and vented off, and the solid polymer material is subjected to counter-current fluid flow in single or multiple stages, with back pressure control at the polymer exit.

Inventors

  • 👤 Richard H. Skidmore

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-24 08:13
CPC Classifications
B; B01; B01D; B01D1/00; B29; B29C; B29C48/00; B29C48/25; B29C48/36; B29C48/375; B29C48/38; B29C48/50; B29C48/76; B29C48/03

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 250 words
In an apparatus for producing solid polymer from a polymer solution which contains about 5 - 50% by weight of solid polymer in about 50 - 95% by weight of a solvent, the combination which comprises: a. means for heating said polymer solution, and means for feeding it under pressure. b. a concentrator connected to accept said heated and pressurized solution as a feed solution, including a low pressure chamber portion into which the feed polymer solution is introduced, and a vent means for release of solvent vapor vaporized in said chamber, c. an extruder connected to receive the concentrated polymer solution from said concentrator, said concentrated polymer solution having a polymer content of about 30 - 80% by weight and about 70 - 20% by weight of solvent, d. vent means on said extruder upstream of said solution receiving connection for venting further solvent vapor from the concentrated polymer feed, e. counter-current fluid introducing means positioned downstream of the feed to said extruder and having connecting means for the introduction and flow of fluid counter-current to the movement of said concentrated polymer in said extruder, f. means on said extruder for removal of said fluid and of materials stripped from said concentrated polymer by said fluid, at a location upstream of the point of introduction of said counter-current fluid but downstream of the point of introduction of said concentrated polymer, and g. means at the extruder exit for controlling the back pressure of the polymer extruded from said extruder.
Claim 2
Dependent Claim 250 words
In an apparatus for producing solid polymer from a polymer solution which contains about 5 - 50% by weight of solid polymer in about 50 - 95% by weight of a solvent, the combination which comprises: a. means for heating said polymer solution, and means for feeding it under pressure. b. a concentrator connected to accept said heated and pressurized solution as a feed solution, including a low pressure chamber portion into which the feed polymer solution is introduced, and a vent means for release of solvent vapor vaporized in said chamber, c. an extruder connected to receive the concentrated polymer solution from said concentrator, said concentrated polymer solution having a polymer content of about 30 - 80% by weight and about 70 - 20% by weight of solvent, d. vent means on said extruder upstream of said solution receiving connection for venting further solvent vapor from the concentrated polymer feed, e. counter-current fluid introducing means positioned downstream of the feed to said extruder and having connecting means for the introduction and flow of fluid counter-current to the movement of said concentrated polymer in said extruder, f. means on said extruder for removal of said fluid and of materials stripped from said concentrated polymer by said fluid, at a location upstream of the point of introduction of said counter-current fluid but downstream of the point of introduction of said concentrated polymer, and g. means at the extruder exit for controlling the back pressure of the polymer extruded from said extruder.
Claim 3
Dependent Claim 13 words
The apparatus defined in claim 1, wherein said means (g) is a valve.
Claim 4
Dependent Claim 13 words
The apparatus defined in claim 1, wherein said means (g) is a turbulator.
Claim 5
Dependent Claim 47 words
The apparatus defined in claim 1, wherein said means (f) comprises a mechanical filter including a vent outlet housing mounted on said extruder (c) and containing a pair of rotating screws, said screws being driven in rotation in a direction to prevent solids from leaving the system.
Claim 6
Dependent Claim 37 words
The apparatus defined in claim 4, wherein the axes of said rotating screws of said mechanical filter are spaced from one another such that the flights of neither screw penetrate into the inter-flight spaces of the other.
Claim 7
Dependent Claim 17 words
The apparatus defined in claim 5, wherein the peripheries of said screws are tangent to each other.
Claim 8
Dependent Claim 26 words
The apparatus defined in claim 1, wherein said means for introducing said stripping fluid is located immediately upstream of and adjacent to said controlling means (g).
Claim 9
Dependent Claim 46 words
The apparatus defined in claim 1, wherein at least two separate counter-current stripping stages are provided, both being downstream of the location of concentrated polymer feed and one being downstream of the other, and wherein means are provided for forming a polymer seal between said stages.
Claim 10
Dependent Claim 21 words
The apparatus defined in claim 1, wherein means are provided for forming a polymer seal upstream of said vent means (d).
Claim 11
Dependent Claim 41 words
The apparatus defined in claim 1, wherein a transporting means is provided which includes a separately driven screw conveyor arranged transversely of the axis of either or both of said concentrator (b) and extruder (c) and connecting them to each other.
Claim 12
Dependent Claim 25 words
The apparatus defined in claim 10, wherein means are provided for introducing energy into said concentrated polymer while it is moving in said transporting means.
Claim 13
Dependent Claim 57 words
The apparatus defined in claim 1, wherein said concentrator (b) is horizontally elongated and wherein a pair of polymer solution feed ports are provided in said concentrator, axially spaced apart from one another, wherein respective vents are provided upstream of each said feed port, and wherein a single solid polymer outlet is provided between said feed ports.
Claim 14
Dependent Claim 19 words
The apparatus defined in claim 12, wherein means are provided for condensing and collecting said vapor from said vents.

References Cited (Backward Citations)

US3082816A Cited
US2836851A Cited
US3046609A Cited
US3067462A Cited
US3376603A Cited
US3535737A Cited
US3738409A Cited
US3799234A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-06-15 1979-12-15 1980-06-15 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-06-15 1983-12-15 1984-06-15 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-06-15 1987-12-15 1988-06-15 $7700.00 Window Closed / Lapsed

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