Isbn: 9783659649585 - simulation of extractive distillation of the co2- ethane azeotrope: process optimization, process intensification (5 resultados)

Taschenbuch. Condición: Neu. Simulation of extractive distillation of the CO2- ethane azeotrope | Process Optimization, Process Intensification | Yadollah Tavan | Taschenbuch | 148 S. | Englisch | 2015 | LAP LAMBERT Academic Publishing | EAN 9783659649585 | Verantwortliche Person für die EU: preigu GmbH & Co. KG, Lengericher Landstr. 19, 49078 Osnabrück, mail[at]preigu[dot]de | Anbieter: preigu.…

Taschenbuch. Condición: Neu. This item is printed on demand - it takes 3-4 days longer - Neuware -High concentrations of carbon dioxide in natural gas occur when carbon dioxide is used for enhanced oil recovery. The separation of CO2 from the hydrocarbons in the natural gas is complicated due to the existence of an azeotrope between ethane (C2) and CO2 at the cryogenic temperatures required for distillation. The main disadvantage of the conventional process lies in its high capital investment and external energy input required to fulfill the desired purification. In addition, current process is different from conventional extractive distillation columns. Because in conventional extractive columns a third component is added to the system and solvent losses in the product streams requires a make-up stream. However, in the present book, the solvent is a mixture of C3 and heavier components in which the solvent stream is quite similar to the light key (ethane) and these distinct features of the process leads to some convergence problems. In order to address these issues, applications of reactive absorption, dividing-wall column and feed-splitting techniques are investigated for this azeotropic mixture and a comparison is made for the new processes. 148 pp. Englisch.…

Taschenbuch. Condición: Neu. nach der Bestellung gedruckt Neuware - Printed after ordering - High concentrations of carbon dioxide in natural gas occur when carbon dioxide is used for enhanced oil recovery. The separation of CO2 from the hydrocarbons in the natural gas is complicated due to the existence of an azeotrope between ethane (C2) and CO2 at the cryogenic temperatures required for distillation. The main disadvantage of the conventional process lies in its high capital investment and external energy input required to fulfill the desired purification. In addition, current process is different from conventional extractive distillation columns. Because in conventional extractive columns a third component is added to the system and solvent losses in the product streams requires a make-up stream. However, in the present book, the solvent is a mixture of C3 and heavier components in which the solvent stream is quite similar to the light key (ethane) and these distinct features of the process leads to some convergence problems. In order to address these issues, applications of reactive absorption, dividing-wall column and feed-splitting techniques are investigated for this azeotropic mixture and a comparison is made for the new processes.…

Condición: New. Dieser Artikel ist ein Print on Demand Artikel und wird nach Ihrer Bestellung fuer Sie gedruckt. Autor/Autorin: Tavan YadollahHe received his M.Sc in Chemical Engineering from Petroleum University of Technology.He is now a member of National Iranian Gas Company, acted as senior operator in Ilam Gas Treating Plant for a year.He has published ov.…

Taschenbuch. Condición: Neu. This item is printed on demand - Print on Demand Titel. Neuware -High concentrations of carbon dioxide in natural gas occur when carbon dioxide is used for enhanced oil recovery. The separation of CO2 from the hydrocarbons in the natural gas is complicated due to the existence of an azeotrope between ethane (C2) and CO2 at the cryogenic temperatures required for distillation. The main disadvantage of the conventional process lies in its high capital investment and external energy input required to fulfill the desired purification. In addition, current process is different from conventional extractive distillation columns. Because in conventional extractive columns a third component is added to the system and solvent losses in the product streams requires a make-up stream. However, in the present book, the solvent is a mixture of C3 and heavier components in which the solvent stream is quite similar to the light key (ethane) and these distinct features of the process leads to some convergence problems. In order to address these issues, applications of reactive absorption, dividing-wall column and feed-splitting techniques are investigated for this azeotropic mixture and a comparison is made for the new processes.VDM Verlag, Dudweiler Landstraße 99, 66123 Saarbrücken 148 pp. Englisch.…