Jump to content



Featured Articles

Check out the latest featured articles.

File Library

Check out the latest downloads available in the File Library.

New Article

Product Viscosity vs. Shear

Featured File

Vertical Tank Selection

New Blog Entry

Low Flow in Pipes- posted in Ankur's blog

Adsorber Pressurisation Step


This topic has been archived. This means that you cannot reply to this topic.
1 reply to this topic
Share this topic:
| More

#1 Bodhisatya

Bodhisatya

    Gold Member

  • Members
  • 156 posts

Posted 01 April 2017 - 06:45 AM

As a part of Front end purification in Air Separation Unit, a pair of adsorber (one online, other in Regn mode) is used to eliminate impurities that might act as a hindrance in Cryo temperatures.

While studying a macro enabled excel, stumbled across following calculated values during pressurisation step.
(Re-generated bed is pressurised by ramp opening a globe valve, injecting pressurise from the online bed)

(a) Pressurisation valve Cv
(B) Largest Cv allowed in pressurisation line.

Esteemed members throw some light on how to proceed.

Bodhisatya Das



#2 sgkim

sgkim

    Gold Member

  • ChE Plus Subscriber
  • 289 posts

Posted 03 April 2017 - 11:12 PM

Hi, 

The pressurization valve opening shall not subject the other online bed to process upset by pressure fluctuation, then the size of the valve may be limited, while a suitable Cv value would be selected based on the differential pressures between the running and regenerating beds to minimize the time for pressurization.

 

The flow through the valve shall be determined by the typical method applied for orifice calculation.  As the velocity of air in the nozzle is limited by the sonic velocity, the pressurization process shall be divided by the critical (sonic) flow session and subsonic.  Total time required shall be summed for the two sessions.

 

~Stefano






Similar Topics