KNOCK OUT VESSEL
Posted: 30 Dec 2010, 18:50
Dear All,
I have following questions about the knock out vessel, the fluid is natural gas, the vessel is vertical
1- What is the acceptable range of the vapor velocity exiting the vessel?
2- What is the acceptable range of the liquid velocity exiting the vessel?
3- Why LCV is used at the outlet line of the liquid exiting the vessel?
4- How the different levels are set i-e LLL, HLL, HHLL, HHLA etc? is there any good engineering practice about this or any thumb rules?
5- Is it required to use mist eliminator made of UNS 08825 for natural gas? I have seen only SS304 eliminators.
6- Please share some renowned vendors for these mist eliminators.
7- What odering information is required for the vendors of mist eliminators?
I have following questions about the knock out vessel, the fluid is natural gas, the vessel is vertical
1- What is the acceptable range of the vapor velocity exiting the vessel?
2- What is the acceptable range of the liquid velocity exiting the vessel?
3- Why LCV is used at the outlet line of the liquid exiting the vessel?
4- How the different levels are set i-e LLL, HLL, HHLL, HHLA etc? is there any good engineering practice about this or any thumb rules?
5- Is it required to use mist eliminator made of UNS 08825 for natural gas? I have seen only SS304 eliminators.
6- Please share some renowned vendors for these mist eliminators.
7- What odering information is required for the vendors of mist eliminators?