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The Global ETD Search service is a free service for researchers
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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.
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Showing 11 to 20 of 91 (0.036 seconds)Spelling suggestions: "subject:"vaporliquid equilibrium"" "subject:"vapourliquid equilibrium""
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Vapor-liquid equilibrium relations in non-ideal systems. The binary systems: hexamethyldisiloxane-toluene hexamethyldisiloxane-ethyl alcohol and ethyl alcohol-toluene at 40,50,60, and 70̊C /Guzman, Jorge A. January 1973 (has links)
No description available.
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Solute-solvent interactions in dilute binary solutions of some polar nonelectrolytesMilanova, Etela. January 1975 (has links)
No description available.
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| 13 |
Vapor-liquid equilibrium of monoethanolamine/piperazine/water at 35-70°CMcLees, John Arthur 16 September 2015 (has links)
The equilibrium partial pressures of monoethanolamine (MEA), piperazine (PZ), and water were measured in a stirred reactor with a recirculating vapor phase by FTIR analysis at 35 - 70 Celsius degrees. MEA and PZ volatility were measured in two separate pilot plant campaigns to capture CO₂ from flue gas under a range of absorber conditions. The laboratory data were regressed to determine NRTL binary interaction parameters that predicted the experimental points within 10 - 20%. It was proven that MEA volatility (0.45<MEA<0.55) is a viable concern in CO₂ capture processes from an economic, environmental, and overall health perspective. PZ, on the other hand, was not observed to be as volatile (0.06<PZ<0.08) as predicted by previous models and therefore volatility loss would not be a significant drawback for using it as a CO₂ capture solvent. Pilot plant results show an average MEA gas phase concentration at the absorber outlet to be approximately 45 ppm while the PZ concentrations averaged 6 ppm and 8 ppm at the absorber inlet and outlet, respectively.
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| 14 |
Vapor-liquid equilibria of coal-derived chemicalsWillman, Bertram Thomas 05 1900 (has links)
No description available.
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| 15 |
The determination of the activity coefficient of a volatile component in a binary system by gas-liquid chromatographyChueh, Chun Fei 08 1900 (has links)
No description available.
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| 16 |
Vapor-liquid phase equilibria of the binary system argon-heliumMcCain, William David 05 1900 (has links)
No description available.
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| 17 |
Vapor-liquid equilibria in nitroparaffin-hydrocarbon systems which exhibit partial miscibilityEdwards, James Byrd 08 1900 (has links)
No description available.
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| 18 |
The effect of radiation and fluid properties on transient film boiling on a horizontal cylindrical surfaceWehmeyer, David Paul 08 1900 (has links)
No description available.
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| 19 |
Solute-solvent interactions in dilute binary solutions of some polar nonelectrolytesMilanova, Etela. January 1975 (has links)
No description available.
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| 20 |
Design of an apparatus for studying the vaporization of droplets in the region of their critical pointRicart-Lowe, Jaime Alberto, January 1966 (has links)
Thesis (M.S.)--University of Wisconsin--Madison, 1966. / eContent provider-neutral record in process. Description based on print version record. Includes bibliographical references.
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