Dear All,
Can Anybody explain the concept of designing the Seperator Vessel for supercritical boiler. Whether the same Souders-Brown equation to determine the maximum allowable vapor velocity:
V = (k) [ (dL - dV) / dV ]^0.5
can be used?
If this is not right please explain?.
Regards
Siva
|

Supercritical Boiler Seperator Vessel
Started by siva_hps, Jun 30 2011 04:50 AM
2 replies to this topic
Share this topic:
#1
Posted 30 June 2011 - 04:50 AM
#2
Posted 21 July 2011 - 12:46 PM
What do you want to separate? Under supercritical conditions there are no seperate liquid and vapor phases.
#3
Posted 14 August 2011 - 04:23 AM
Googling "supercritical boiler" can reveal a lot of info, like the one in http://plainsjustice...ogy Matures.pdf. This web reference indicates no steam and mud drum in such boilers, djack77494 post also indicates that.
Edited by kkala, 14 August 2011 - 04:24 AM.
Similar Topics
Three Phase Seperator ModificationStarted by Guest_halkeshhulk_* , 10 Jun 2025 |
|
![]() |
||
![]() Supercritical Fluid Flowrate - He Tube RuptureStarted by Guest_flarewolf_* , 07 Apr 2025 |
|
![]() |
||
Batch Adsorption: H/d Ratio For Vessel SizingStarted by Guest_Victor_process_Engineer_* , 28 Feb 2025 |
|
![]() |
||
Effect Of Continuous Blow Down To Boiler Feed WaterStarted by Guest_Dyames027_* , 21 Nov 2024 |
|
![]() |
||
Minimum Vapor Disengagement Area For A Kettle BoilerStarted by Guest_Engib33r_* , 17 Oct 2024 |
|
![]() |