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Gokul Srinivasan Phones & Addresses

  • Akron, OH

Resumes

Resumes

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Gokul Srinivasan

Publications

Us Patents

Microcellular Foams

US Patent:
52526208, Oct 12, 1993
Filed:
Apr 2, 1992
Appl. No.:
7/862521
Inventors:
Jarrell R. Elliott - Northfield Center OH
Gokul Srinivasan - Akron OH
Manish Dhanuka - Akron OH
Ranjan Akhaury - Akron OH
Assignee:
University of Akron - Akron OH
International Classification:
C08J 928
US Classification:
521149
Abstract:
Supercritical drying has distinct advantages in generating microcellular materials. The dimensional stability of the polymer is not affected on drying because the supercritical process does not go through the two phase path and therefore the effect of capillary forces is absent. This helps in maintaining the morphology of the final polymer structure and better control over cell size. Organic microcellular foams were prepared by polymerizing directly in a near-critical fluid and pursuing the supercritical drying in the same reactor. The critical variables are the choice of a diluent with a strong enough solvent power to stabilize the polymer matrix, but with a low enough critical temperature to permit critical point drying without damage to the polymer matrix.

Microcellular Foams

US Patent:
51283824, Jul 7, 1992
Filed:
Nov 15, 1991
Appl. No.:
7/794124
Inventors:
Jarrell R. Elliott - Northfield Center OH
Gokul Srinivasan - Akron OH
Manish Dhanuka - Akron OH
Ranjan Akhaury - Akron OH
Assignee:
The University of Akron - Akron OH
International Classification:
C08J 920
US Classification:
521178
Abstract:
Supercritical drying has distinct advantages in generating microcellular materials. The dimensional stability of the polymer is not affected on drying because the supercritical process does not go through the two phase path and therefore the effect of capillary forces is absent. This helps in maintaining the morphology of the final polymer structure and better control over cell size. Organic microcellular foams were prepared by polymerizing directly in a near-critical fluid and pursuing the supercritical drying in the same reactor. The critical variables are the choice of a diluent with a strong enough solvent power to stabilize the polymer matrix, but with a low enough critical temperature to permit critical point drying without damage to the polymer matrix.
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