Thesis (MTech (Chemical Engineering))--Peninsula Technikon, 2000. / Word processed copy. Summary in English. Includes bibliographical references. Also available online.

No description available.

No description available.

Thesis (Ph. D.)--University of Texas at Austin, 2000. Thesis (Ph. D.)--University of Missouri-Columbia, 2002. / Vita. Typescript. Includes bibliographical references (leaves 176-179). Includes bibliographical references (leaves -). Available also in a digital version from Dissertation Abstracts.

Thesis (Ph. D.)--University of Texas at Austin, 1998. / Vita. Includes bibliographical references (leaves 287-300). Available also in a digital version from Dissertation Abstracts.

Thesis (Ph.D)--Chemical Engineering, Georgia Institute of Technology, 2010. / Committee Chair: Sholl, David S.; Committee Member: Chance, Ronald R.; Committee Member: Jang, Seung Soon; Committee Member: Koros, William J.; Committee Member: Nair, Sankar. Part of the SMARTech Electronic Thesis and Dissertation Collection.

Thesis (Ph. D.)--University of Texas at Austin, 2004. / Supervisor: Benny D. Freeman. Vita. Includes bibliographical references.

Thesis (Ph.D.) in Materials Science--University of Maine, 2004. / Includes vita. Includes bibliographical references (leaves 112-122).

No description available.

Thesis (MTech (Chemical Engineering))--Peninsula Technikon, 2000. / Oxygen transport across biofilms and membranes may be a limiting factor in the operation of a membrane bio-reactor. A Gradostat fungal membrane bio-reactor is one in which fungi are immobilized within the wall of a porous polysulphone capillary membrane. In this study the mass transfer rates of gases (oxygen and carbon dioxide) were investigated in a bare membrane (without a biofilm being present). The work provides a basis for further transport study in membranes where biomass is present. The diaphragm-cell method can be employed to study mass transfer of gases in flat-sheet membranes. The diaphragm-cell method employs two well-stirred compartments separated by the desired membrane to be tested. The membrane is maintained horizontally. -The gas (solute) concentration in the lower compartment is measured versus time, while the concentration in the upper liquid-containing compartment is maintained at a value near zero by a chemical reaction. The resistances-in-series model can be used to explain the transfer rate in the system. The two compartments are well stirred; this agitation reduces the resistances in the liquid boundary layers. Therefore it can be assumed that in this work the resistance in the membrane will be dominating. The method was evaluated using oxygen as a test. The following factors were found to influence mass transfer coefficient: i) the agitation in the two compartments; ii) the concentration of the reactive solution and iii) the thickness of the membrane.