southtexashack
Chemical
- Apr 18, 2003
- 5
We recently installed a nickel oxide catalyst bed to remove trace amounts of sulfur from a gas stream that is 65%Ethane/35%Ethylene at the following temp. & pressure:
P=360 psig (about 25 atmospheres)
T=60 F
We ran into numerous problems, (high exotherm, byproducts of hydrogen, CO, CO2, etc) and eventually had to change out the catalyst after one day and replace it with something else. When we dumped the catalyst, it appeared that there were alot of coke fines. The temperature probably got to at least 550 F, but we had no thermocouples in the vessel, so I'm not exactly sure how hot it got.
A few questions
1. What reaction may have caused the exotherm? OR Would there have been a strong reduction of the catalyst at 60F?
2. Does it make sense that ethane/ethylene could coke over this catalyst at these temperatures and pressures? If so, is there any publications that document this?
Any help would be appreciated
P=360 psig (about 25 atmospheres)
T=60 F
We ran into numerous problems, (high exotherm, byproducts of hydrogen, CO, CO2, etc) and eventually had to change out the catalyst after one day and replace it with something else. When we dumped the catalyst, it appeared that there were alot of coke fines. The temperature probably got to at least 550 F, but we had no thermocouples in the vessel, so I'm not exactly sure how hot it got.
A few questions
1. What reaction may have caused the exotherm? OR Would there have been a strong reduction of the catalyst at 60F?
2. Does it make sense that ethane/ethylene could coke over this catalyst at these temperatures and pressures? If so, is there any publications that document this?
Any help would be appreciated