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Filter material and process for producing same

Assignee: Chemie-Anlagenbau Bischofsheim GmbH
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Filing: 1977-08-15
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Granted: 1979-04-10
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Expires: 1997-08-15
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Abstract

Abstract This invention relates to filter material consisting substantially of a microporous and/or macroporous sheet structure obtained by coagulation of a polymer solution in which at least one surface area of the sheet structure is abraded more or less, depending on the desired pore size and a process for producing said filter materials.

Inventors

  • 👤 Karl H. Hilterhaus
  • 👤 Franz G. Reuter

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 15:32
CPC Classifications
B; B01; B01D; B01D67/00; B01D67/0081; B01D67/0086; B01D39/00; B01D39/14; B01D39/16; B01D39/1607; B01D39/1623; B01D39/1692; B01D71/00; B01D71/06; B01D71/54; C; C08; C08J; C08J9/00; C08J9/28; C08J2375/00; C08J2375/04

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 280 words
A process of producing a porous polyurethane resin filter material comprising: a. providing a first solution containing 60 tp 80% by weight of an NCO-pre-adduct having 1.5 to 5% free isocyanate groups dissolved in a highly polar organic solvent; b. providing a second solution containing a highly polar organic solvent and at least one member selected from the group consisting of hydrazine hydrate, carbodihydrazide, piperazine and 1,4-diaminopiperazine and in which solution said member is present in an amount of from 0.02 to 0.05 mole percent; c. admixing said first solution into said second solution over an extended period of time during which the NCO pre-adduct and said member of said second solution react to form a highly viscous reaction product and continuing the admixing of said first solution into said second solution and monitoring the viscosity measured under reaction conditions until the viscosity of the admixture is such that the addition of even the minutest amount of said first solution would have resulted in instantaneous gelling of the admixture, and at which point the addition of said first solution is stopped immediately, the final admixture thus produced having a solids content of between 15 and 35% by weight; d. shaping the resulting high viscosity final solution into a sheet, e. introducing the sheet into a coagulating bath to provide a microporous sheet structure having two external non-porous skin stratum and a central stratum having pore channels aligned perpendicularly to the surfaces of the sheet structure, f. drying the resulting microporous sheet structure and g. abrading one or both sides of the resulting microporous sheet structure to provide a filter having pore channels perpendicular to the surfaces of the sheet structure.
Claim 2
Dependent Claim 280 words
A process of producing a porous polyurethane resin filter material comprising: a. providing a first solution containing 60 tp 80% by weight of an NCO-pre-adduct having 1.5 to 5% free isocyanate groups dissolved in a highly polar organic solvent; b. providing a second solution containing a highly polar organic solvent and at least one member selected from the group consisting of hydrazine hydrate, carbodihydrazide, piperazine and 1,4-diaminopiperazine and in which solution said member is present in an amount of from 0.02 to 0.05 mole percent; c. admixing said first solution into said second solution over an extended period of time during which the NCO pre-adduct and said member of said second solution react to form a highly viscous reaction product and continuing the admixing of said first solution into said second solution and monitoring the viscosity measured under reaction conditions until the viscosity of the admixture is such that the addition of even the minutest amount of said first solution would have resulted in instantaneous gelling of the admixture, and at which point the addition of said first solution is stopped immediately, the final admixture thus produced having a solids content of between 15 and 35% by weight; d. shaping the resulting high viscosity final solution into a sheet, e. introducing the sheet into a coagulating bath to provide a microporous sheet structure having two external non-porous skin stratum and a central stratum having pore channels aligned perpendicularly to the surfaces of the sheet structure, f. drying the resulting microporous sheet structure and g. abrading one or both sides of the resulting microporous sheet structure to provide a filter having pore channels perpendicular to the surfaces of the sheet structure.
Claim 3
Dependent Claim 14 words
A process according to claim 1 wherein the solvent employed is a polar solvent.
Claim 4
Dependent Claim 19 words
A process according to claim 2 wherein the second solution is a solution prepared from hydrazine hydrate and dimethylformamide.
Claim 5
Dependent Claim 31 words
A process according to claim 1 wherein the second solution is hydrazine solution and the first and second solutions are allowed to react at a temperature between 20° and 40° C.
Claim 6
Dependent Claim 49 words
A process according to claim 1 wherein there is added to the second solution one or more of other additives selected from the group consisting of crosslinking substances, chain propagating agents, chain terminating agents, gelling agents, solution fillers, organic or inorganic pigments, dyestuffs, optical brighteners, ultraviolet absorbers, and antioxidants.
Claim 7
Dependent Claim 13 words
A process according to claim 1 wherein the coagulating bath consists of water.
Claim 8
Dependent Claim 22 words
A process according to claim 1 wherein during shaping of the final solution a reinforcing insert is incorporated into the sheet structure.
Claim 9
Dependent Claim 17 words
A process according to claim 7 wherein the reinforcing insert is a fabric of woven glass filaments.
Claim 10
Dependent Claim 12 words
A process according to claim 1 wherein the process is operated continuously.

References Cited (Backward Citations)

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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) 1982-04-09 1982-10-09 1983-04-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1986-04-09 1986-10-09 1987-04-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1990-04-09 1990-10-09 1991-04-10 $7700.00 Window Closed / Lapsed

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