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US4417043A Expired / Lapsed US ⏱️ 0.0 years remaining

Anisotropic melt-forming polymer

Assignee: Imperial Chemical Industries Ltd
•
Filing: 1981-01-05
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Granted: 1983-11-22
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Expires: 2001-01-05
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Abstract

Abstract A polymer capable of forming an anisotropic melt characterized in that the polymer chain includes residues of cross-linking reactants at a concentration sufficient to give a polymer with a melt viscosity of not greater than 10 7 Nsec/m 2 measured by capillary rheometry at a shear rate of 10 4 N/m 2 . The polymers exhibit favorable shear dependent viscosity characteristics in that the viscosity is high under low shear conditions and is low under high shear conditions, as judged by the viscosity characteristics of polymers of the same composition but not containing the residues of cross-linking reactants.

Inventors

  • 👤 Frederic N. Cogswell
  • 👤 Brian P. Griffin
  • 👤 Clive P. Smith

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 19:34
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/68; C08G63/682; C08G63/02; C08G63/12; C08G63/16; C08G63/20

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 91 words
A polymer which is capable of forming an anisotropic melt characterised in that the polymer has been prepared in the presence of cross-linking reactants whereby the polymer chain includes residues derived from said cross-linking reactants, the residues being present at a concentration which is insufficient to give a fully cross-linked polymer as defined by having a melt viscosity of less than 10 7 Nsec/m 2 when measured using capillary rheometry at a temperature below the decomposition point of the polymer and at a shear stress of 10 4 N/m 2 .
Claim 2
Dependent Claim 91 words
A polymer which is capable of forming an anisotropic melt characterised in that the polymer has been prepared in the presence of cross-linking reactants whereby the polymer chain includes residues derived from said cross-linking reactants, the residues being present at a concentration which is insufficient to give a fully cross-linked polymer as defined by having a melt viscosity of less than 10 7 Nsec/m 2 when measured using capillary rheometry at a temperature below the decomposition point of the polymer and at a shear stress of 10 4 N/m 2 .
Claim 3
Dependent Claim 55 words
A polymer which is capable of forming an anisotropic melt according to claim 1 characterised in that the viscosity of the polymer melt is shear dependent and is low under conditions of high shear and is high under conditions of low shear, relative to a polymer of the same composition not containing the cross-linking residues.
Claim 4
Dependent Claim 36 words
A polymer according to either of claims 1 or 2 characterised in that the polymer is a condensation polymer and the residues of cross-linking reactants are derived from reactants containing at least three reactive functional groups.
Claim 5
Dependent Claim 22 words
A polymer according to claim 3 in which the reactive functional groups are selected from hydroxyl, carboxyl, amino, isocyanate and carbodiimide groups.
Claim 6
Dependent Claim 42 words
A polymer according to either of claims 1 or 2 characterised in that the polymer is an addition polymer of mono-ethylenically unsaturated materials and the residues of cross-linking reactants are derived from polyethylenically unsaturated compounds containing at least two ethylenically unsaturated groups.
Claim 7
Dependent Claim 27 words
A polymer according to claim 1 characterised in that the concentration of cross-linking residues in the polymer is between 0.01 and 5% by weight of the polymer.
Claim 8
Dependent Claim 27 words
A polymer according to claim 1 characterised in that the concentration of cross-linking residues in the polymer is between 0.01 and 1% by weight of the polymer.
Claim 9
Independent Claim 94 words
A method of producing an anisotropic melt-forming polymer which has a shear dependent viscosity in the melt characterised in that the anisotropic melt-forming polymer is polymerised in the presence of cross-linking reactants at a concentration sufficient to give a polymer with a melt viscosity in excess of that for the same polymer not containing cross-linking agent but insufficient to exceed a melt viscosity of 10 7 Nsec/m 2 when measured using capillary rheometry at a temperature below the decomposition point of the polymer and at a shear stress of 10 4 N/m 2 .
Claim 10
Independent Claim 94 words
A method of producing an anisotropic melt-forming polymer which has a shear dependent viscosity in the melt characterised in that the anisotropic melt-forming polymer is polymerised in the presence of cross-linking reactants at a concentration sufficient to give a polymer with a melt viscosity in excess of that for the same polymer not containing cross-linking agent but insufficient to exceed a melt viscosity of 10 7 Nsec/m 2 when measured using capillary rheometry at a temperature below the decomposition point of the polymer and at a shear stress of 10 4 N/m 2 .
Claim 11
Dependent Claim 10 words
An anisotropic melt of a polymer according to claim 1.
Claim 12
Dependent Claim 11 words
A shaped article formed from the anisotropic melt of claim 9.

References Cited (Backward Citations)

US3991014A Cited
US4118372A Cited
US4153779A Cited
US4294953A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-11-21 1987-05-23 1987-11-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-11-21 1991-05-23 1991-11-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-11-21 1995-05-23 1995-11-22 $7700.00 Window Closed / Lapsed

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