Dear friends,
I'm currently involved in geothermal project. Basically, we separate brine from its vapor in separator and then flow the vapor to scrubber to ensure no liquid carried along with the dry vapor. The question is, when I do the simulation in HYSYS, I get the size of separator, but I don't get the size of the scrubber. I think because the fluid entering it is dry (vapor fraction = 1). So, is there any approach or assumption to size the scrubber? Thank you very much for your attention.
Note: we use the vapor to move the turbine, so the vapor has to be completely dry.
Best regards,
Erwan
|

Scrubber Sizing
Started by Skyline, Oct 22 2009 08:35 PM
2 replies to this topic
Share this topic:
#1
Posted 22 October 2009 - 08:35 PM
#2
Posted 23 October 2009 - 11:29 AM
You will need to size both the separator and the scrubber yourself. Hysys will not really do it for you (even if it pretends to do so).
You need to calculate the required diameter using the Souders-Brown equation, and size the vessels yourself. In the scrubber, for the liquid density, assume it is the same as in the separator, so that you can calculate the maximum vapor velocity.
There is a good spreadsheet by Art Montemayor, and a lot of discussion, in these forums. Just search for "separator sizing" or "scrubber sizing" and you should be able to understand how to size these vessels.
Also, you could take a look at the article on Citizendium.
You need to calculate the required diameter using the Souders-Brown equation, and size the vessels yourself. In the scrubber, for the liquid density, assume it is the same as in the separator, so that you can calculate the maximum vapor velocity.
There is a good spreadsheet by Art Montemayor, and a lot of discussion, in these forums. Just search for "separator sizing" or "scrubber sizing" and you should be able to understand how to size these vessels.
Also, you could take a look at the article on Citizendium.
#3
Posted 26 October 2009 - 05:25 AM
Dear joerd,
I think you're right, HYSYS gave a considerably bigger size than it should be. The question is about the scrubber then. What assumption do I need to do the sizing? (Because the vapor leaving separator suppose to be dry, I have no idea about the load in scrubber). Thank you before.
Best regards,
Erwan
I think you're right, HYSYS gave a considerably bigger size than it should be. The question is about the scrubber then. What assumption do I need to do the sizing? (Because the vapor leaving separator suppose to be dry, I have no idea about the load in scrubber). Thank you before.
Best regards,
Erwan
Similar Topics
![]() Liquid Liquid Separator SizingStarted by Guest_Kentucky08_* , 03 Apr 2025 |
|
![]() |
||
Critical Pressure For Choke Valve SizingStarted by Guest_Sherif Morsi_* , 07 Nov 2017 |
|
![]() |
||
Scrubber(Absorber) In Apsen PlusStarted by Guest_Seonwoo_* , 20 Mar 2025 |
|
![]() |
||
Alkaline Electrolytic Cell/stack Sizing/design For H2 ProductionStarted by Guest_BRS09_* , 13 Mar 2025 |
|
![]() |
||
Batch Adsorption: H/d Ratio For Vessel SizingStarted by Guest_Victor_process_Engineer_* , 28 Feb 2025 |
|
![]() |