The SCADA suggests the plant is licensed to Air Liquide and is built with the premises of a renowned Steel Plant in India. This ASU is the prime supplier of Oxygen used in blast furnaces.
Chowdhury to re confirm
Bodhisatya.
|
Posted 14 June 2014 - 12:00 PM
The SCADA suggests the plant is licensed to Air Liquide and is built with the premises of a renowned Steel Plant in India. This ASU is the prime supplier of Oxygen used in blast furnaces.
Chowdhury to re confirm
Bodhisatya.
Posted 15 June 2014 - 03:23 AM
Dear Bodhisatya,
I am very glad to well informed from you.
I do have more questions about the ASU process. This might be basic though.
When we are adapting Linde cycle or others for cryogenic system, why compressing up to 40 to 60 bar instead just maintaining it below 6 bar.
From my knowledge, in order to sustain cryogenic environment, isn't 6 bar is enough?
When I have a look present SCADA and other practical cases, many of'em aplying stages of compression.
Is this configuration just for the system start-up? or for the stable ASU operation?
And, why don't or can't use membrane separator? Membrane separator can feed enriched oxygen to the latter distilation process to raise the selectivity. However, many of practical cases are not using membrane separator. Why is that?
For your information, I am in PhD course studying on ASU for now and trying to leanr very hard.
Thank you
Best regards
Shin Yoo
Posted 14 September 2014 - 03:12 AM
Hi, i have a similar project, please send your PFD file to this address
mohammadheydari86@yahoo.com
Aspen Hysys - Creating A New Component And Defining PropertiesStarted by Guest_catiiiii_* , 22 Apr 2024 |
|
|
||
Separation Of Ethyl Acetate And IpaStarted by Guest_Jaiganesh_* , 14 Apr 2024 |
|
|
||
How To Find K-Values Of A Hydrocarbon Mixture On Aspen Hysys?Started by Guest_Alexis Azamar_* , 08 Apr 2024 |
|
|
||
Ammonium Sulfate Process SimulationStarted by Guest_amir55261_* , 06 Apr 2024 |
|
|
||
Extension Reaction Kinetic In HysysStarted by Guest_Ulbert Zsolt_* , 29 Mar 2024 |
|
|