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  • About
  • The Global ETD Search service is a free service for researchers to find electronic theses and dissertations. This service is provided by the Networked Digital Library of Theses and Dissertations.
    Our metadata is collected from universities around the world. If you manage a university/consortium/country archive and want to be added, details can be found on the NDLTD website.
11

Nanocrystal stabilization, synthesis and assembly using supercritical fluids

Shah, Parag Suresh 28 August 2008 (has links)
Not available / text
12

CO₂ -expanded liquids as environmentally benign process solvents

West, Kevin Neal 05 1900 (has links)
No description available.
13

A new apparatus for the determination of phase equilibrium properties of heavy hydrocarbon systems

Suleiman, David 08 1900 (has links)
No description available.
14

Processing of polymers using supercritical CO₂

Vincent, Michael Francis 05 1900 (has links)
No description available.
15

Wax particle formation from the rapid expansion of supercritical solutions

Griscik, Gregory J. 12 1900 (has links)
No description available.
16

Thermodynamic and spectroscopic investigations of solid-supercritical fluid equilibrium

Pouillot, Frederic 12 1900 (has links)
No description available.
17

Spectroscopic and kinetic investigations in supercritical fluid solutions

Knutson, Barbara Lynn 05 1900 (has links)
No description available.
18

Extensions of the theory of dilute solutions

Mendez-Santiago, Janette 12 1900 (has links)
No description available.
19

Environmentally benign chemical reactions in near-critical water and supercritical carbon dioxide

Chandler, Karen 12 1900 (has links)
No description available.
20

Safety and Techno-Economic Analysis of Solvent Selection for Supercritical Fischer-Tropsch Synthesis Reactors

Hamad, Natalie 2011 December 1900 (has links)
Fisher-Tropsch Synthesis is a primary pathway for gas-to-liquid technology. In order to overcome commercial problems associated with reaction and transport phenomena, the use of supercritical solvents has been proposed to increase chemical conversion and improve temperature control. One of the major challenges in designing the supercritical FTS systems is the solvent selection. Numerous alternatives exist and should be screened based on relevant criteria. The main aim of the thesis was to develop a safety metric that can be incorporated in the selection of an optimal supercritical solvent or a mixture of solvents. The objective was to minimize the cost while satisfying safety constraints or to establish tradeoffs between cost and safety. Hydrocarbons from C3 to C9 were identified as feasible solvents for FTS purposes. The choice of these solvents is dependent on their mixture critical temperature and pressure requirements that need to be satisfied upon entry into the FTS reactor. A safety metric system was developed in order to compare the risk issues associated with using the aforementioned solvents. In addition, an economic analysis of using the different solvents was performed. Finally, a case study was solved to illustrate the use of the proposed metrics and the selection of solvents based on safety and techno-economic criteria.

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