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

Ethylene Oxide Flash Calculation With Aspen Plus


This topic has been archived.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

#1 deltaChe

deltaChe

    Gold Member

  • ChE Plus Subscriber
  • 153 posts

Posted 14 July 2010 - 09:55 AM



I would like to ask a very simple and mundane question for professional process engineer about simulating flash scenario through Aspen plus.

Please bear with me.

EO stream : OT=-5C, OP=6barg, a PSV set pressure=24 barg, and will relief to scrubber (O.P.=1 atm)

I tried use Aspen plus to see if any flash will happen when PSV relief, but I encounter some questions in the following.



N1. What is the inlet pressure for flash drum inlet stream in Aspen?

I used 24 barg for flash drum inlet pressure because PSV set pressure is 24 barg, but I wonder if possible I can used the EO stream O.P.=6barg for flash drum inlet.

N2. What is the pressure in the flash drum? I used the Scrubber O.P.=0 barg as flash drum O.P. and heat duty=0(adiabatic condition) in Aspen.

I got the a little EO will flash after running the Aspen (please see the attached file) , and it seems contradict with the No EO will flash result that I found the EO properties in the MSDS.(EO boiling point = 17 C at 1 atm. EO at OT=-5 C will never get flash)



Thank you very much for your kindly help.



My Aspen input variable:

  • Thermodynamics properties:SRK,
  • Inlet stream : EO flow rate : 500lb/hr. OP=24 barg, OT=-5 C
  • flash block : flash specifications : temp : -5 C, heat duty = 0 btu/hr, valid phase: vapor-liquid-free water.


Attached Files



#2 MrShorty

MrShorty

    Gold Member

  • ChE Plus Subscriber
  • 517 posts

Posted 15 July 2010 - 09:58 AM

and it seems contradict with the No EO will flash result that I found the EO properties in the MSDS.(EO boiling point = 17 C at 1 atm. EO at OT=-5 C will never get flash)

I'm not sure where this statement comes from, but it seems wrong to me. We have to remember that everything at any temperature has a vapor pressure. "Coincidentally," the vapor pressure of ethylene oxide at -5 C is about 0.5 atm as reported in your flash calculation.

#3 deltaChe

deltaChe

    Gold Member

  • ChE Plus Subscriber
  • 153 posts

Posted 16 July 2010 - 08:34 AM

and it seems contradict with the No EO will flash result that I found the EO properties in the MSDS.(EO boiling point = 17 C at 1 atm. EO at OT=-5 C will never get flash)

I'm not sure where this statement comes from, but it seems wrong to me. We have to remember that everything at any temperature has a vapor pressure. "Coincidentally," the vapor pressure of ethylene oxide at -5 C is about 0.5 atm as reported in your flash calculation.



I should use 1 atm in flash drum as input insteand -5 C because this is vent to atm.
Thank you.




Similar Topics