Optimal design of cryogenic distillation columns with side heat pumps for the propylene/propane separation

Author(s):  
J. Rafael Alcántara-Avila ◽  
Fernando I. Gómez-Castro ◽  
J. Gabriel Segovia-Hernández ◽  
Ken-Ichiro Sotowa ◽  
Toshihide Horikawa
2010 ◽  
Vol 431 (2) ◽  
pp. 116-119 ◽  
Author(s):  
G. M. Ostrovskii ◽  
N. N. Ziyatdinov ◽  
T. V. Lapteva ◽  
N. Yu. Bogula

1991 ◽  
Vol 20 (4P1) ◽  
pp. 419-424 ◽  
Author(s):  
Toshihiko Yamanishi ◽  
Mikio Enoeda ◽  
Kenji Okuno ◽  
Takumi Hayashi ◽  
Junzo Amano ◽  
...  

1992 ◽  
Vol 21 (2P2) ◽  
pp. 948-953 ◽  
Author(s):  
T. Yamanishi ◽  
K. Okuno ◽  
M. Enoeda ◽  
J. Amano ◽  
T. Hayashi ◽  
...  

Author(s):  
J. Rafael Alcántara-Avila ◽  
Fernando I. Gómez-Castro ◽  
J. Gabriel Segovia-Hernández ◽  
Ken-Ichiro Sotowa ◽  
Toshihide Horikawa

2016 ◽  
Vol 37 (1) ◽  
pp. 73-85
Author(s):  
Janusz Kotowicz ◽  
Sylwia Berdowska

AbstractIn this paper a 600 MW oxy-type coal unit with a pulverized bed boiler and a membrane-cryogenic oxygen separator and carbon capture installation was analyzed. A membrane-cryogenic oxygen separation installation consists of a membrane module and two cryogenic distillation columns. In this system oxygen is produced with the purity equal to 95%. Installation of carbon capture was based on the physical separation method and allows to reduce the CO2emission by 90%. In this work the influence of the main parameter of the membrane process – the selectivity coefficient, on the efficiency of the coal unit was presented. The economic analysis with the use of the break-even point method was carried out. The economic calculations were realized in view of the break-even price of electricity depending on a coal unit availability.


2015 ◽  
Vol 82 ◽  
pp. 48-56 ◽  
Author(s):  
Julien Ramousse ◽  
Damien Sgorlon ◽  
Gilles Fraisse ◽  
Maxime Perier-Muzet

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