BRJ
Chemical
- Feb 24, 2003
- 1
Currently I'm working on a dehydrator debottlenecking assessment for Onshore Gas Plant.
I was keen to find out more information concerning the relationship of glycol losses (due to glycol vaporising into the gas phase rather than being entrained as a liquid mist) at higher contactor pressures and the significance that gas density can have with glycol losses, does anyone have any advice, experience or recommendations on the max gas density for reasonable operations or a good reference?
- GPSA and Shell DEP's state that the gas density should be limited to less than 100 kg/m3. I'm hoping for more information.
Thanks
Brendon
I was keen to find out more information concerning the relationship of glycol losses (due to glycol vaporising into the gas phase rather than being entrained as a liquid mist) at higher contactor pressures and the significance that gas density can have with glycol losses, does anyone have any advice, experience or recommendations on the max gas density for reasonable operations or a good reference?
- GPSA and Shell DEP's state that the gas density should be limited to less than 100 kg/m3. I'm hoping for more information.
Thanks
Brendon