- 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.
Search results
Showing 11 to 20 of 91 (0.059 seconds)Spelling suggestions: "subject:"vaporliquid equilibrium."" "subject:"vapourliquid equilibrium.""
| 11 |
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.
|
| 12 |
Solute-solvent interactions in dilute binary solutions of some polar nonelectrolytesMilanova, Etela. January 1975 (has links)
No description available.
|
| 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.
|
| 14 |
Vapor-liquid equilibria of coal-derived chemicalsWillman, Bertram Thomas 05 1900 (has links)
No description available.
|
| 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.
|
| 16 |
Vapor-liquid phase equilibria of the binary system argon-heliumMcCain, William David 05 1900 (has links)
No description available.
|
| 17 |
Vapor-liquid equilibria in nitroparaffin-hydrocarbon systems which exhibit partial miscibilityEdwards, James Byrd 08 1900 (has links)
No description available.
|
| 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.
|
| 19 |
Solute-solvent interactions in dilute binary solutions of some polar nonelectrolytesMilanova, Etela. January 1975 (has links)
No description available.
|
| 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.
|
Page generated in 0.0656 seconds