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Virginia Tech

Melt Processing Thermally Unstable and High Molecular Weight Polymers with Supercritical Carbon Dioxide

Abstract

dc:description.abstract

This thesis is concerned with the development of a continuous melt extrusion process utilizing CO₂ for the production of materials that cannot be typically melt processed. The first goal of this study is to determine under what conditions it is possible to use CO₂ to plasticize and, thereby, reduce the viscosity of an acrylonitrile (AN) copolymer in an extrusion process and render it melt processable. In order to assess whether it was possible to absorb adequate amounts of CO₂ in short residence times by injection into a single screw extruder, a slit-die rheometer was attached to the end of the extrusion system for the purpose of directly assessing the viscosity reduction. A chemorheological analysis was performed on 65 and 85% AN copolymers to establish the temperature at which the 85% material would be stable for melt processing. This, coupled with studies correlating the degree of Tg and viscosity reduction with the amount of absorbed CO₂, allowed one to establish conditions for melt extrusion of the 85% AN. It was determined that the 85% AN material should absorb at least 5 weight percent CO₂ for a processing temperature reduction of 26°C in the extrusion process. The second goal of this study is to determine to what extent CO₂ can be used as a processing aid to melt process polyethylenes of higher molecular weight than can be typically melt processed. To assess the ability to melt process high molecular weight polyethylenes with CO₂, the viscosity of a 460,000 g/mol HDPE plasticized with various amounts of absorbed CO₂ as determined with the slit-die rheometer. A relationship was developed to determine the maximum molecular weight polyethylene that could be processed at a given viscosity reduction due to absorbed CO₂. The viscosity of a blend of 40 weight percent UHMWPE with the 460,000 g/mol HDPE with 12 weight percent CO₂ was reduced to that of the pure 460,000 g/mol HDPE as predicted by the relationship. Preliminary studies using a pressurized chamber attached to the exit of the die allowed one to assess the conditions under which suppression of foaming is possible.

Degree

thesis:*
Name thesis:degree_name
Ph. D.
Level thesis:degree_level
doctoral
Discipline thesis:degree_discipline
Chemical Engineering
Department dc:contributor.department
Chemical Engineering
Grantor dc:publisher
Virginia Tech
Year dc:date.issued
2007

Author and committee

dc:creator, dc:contributor.*
Author dc:creator
  • Wilding, Matthew David
Chair dc:contributor.committeechair
  • Baird, Donald G.
Committee members dc:contributor.committeemember
  • Davis, Richey M.
  • McGrath, James E.
  • Kiran, Erdogan R.

Subjects

dc:subject × 3

Rights

dc:rights
Statement dc:rights
  • In Copyright

Identifiers

dc:identifier.*
Dc Identifier Other
etd-05042007-184715
OAI identifier oai:identifier
oai:vtechworks.lib.vt.edu:10919/27537

Chain of custody

source
Harvested from
Virginia Tech
Base URL
vtechworks.lib.vt.edu/oai/request
Last updated
2026-07-22
Source record
OAI-PMH GetRecord
citation

Wilding, Matthew David. Melt Processing Thermally Unstable and High Molecular Weight Polymers with Supercritical Carbon Dioxide. doctoral thesis, Virginia Tech, 2007. http://hdl.handle.net/10919/27537