Hi,
I am to design a contact condenser with the feed gas stream at the top of the column. The feed stream contains HTF (therminol VP-1) and low boilers. The purpose is to condense HTF only to be send to a expansion tank. The low boilers are to be sent to another vessel to be separated farther and removed from the system. For the spray condenser design, do the same vessel design parameters used for flash vessels (Souders-Brown) apply? Are there separate methods for the design of the vessel alone, and the design of the spray nozzles?
I have the inlet conditions of the vapor stream only (flow rate, T and P).
Thank you so much in advanced for your help!
|

Design Of Direct Contact Condenser ( With Spray Header Nozzles)
Started by anj3, Oct 27 2011 09:30 AM
condenser spray nozzles direct contact condenser
No replies to this topic
Share this topic:
#1
Posted 27 October 2011 - 09:30 AM
Similar Topics
Design Capacity Of Hydrogen Pullet During Hydroprocessing Units UpsetStarted by Guest_Divid Kelin_* , 18 Jun 2025 |
|
![]() |
||
Hot Oil Loop / Heating Medium DesignStarted by Guest_Lyne_* , 30 Mar 2024 |
|
![]() |
||
![]() Hello, Design Of Natural Gas Liquefaction Processes.Started by Guest_guoyinyanliner_* , 18 Jun 2025 |
|
![]() |
||
![]() Scrubber DesignStarted by Guest_nasss_* , 07 Aug 2024 |
|
![]() |
||
Refinery Lpg Deethanizer Column DesignStarted by Guest_Ilyes_* , 15 Feb 2025 |
|
![]() |