sshep
Chemical
- Feb 3, 2003
- 761
Does anyone in this forum have knowledge of improved distributor design for conventional hydrotreating reactors(mixed phase, downflow, 9ftDia x 45ftT-T)? Our application is to treat kerosene streams for a downstream chemical process for which S and N are poisons.
We are considering a change-out of our conventional trays to get some additional reactor volume and any better performance which is possible from such a change. Currently I am inquiring into Shell's High Dispersion (HD) trays. I have a concern that the cost to benifit ratio of a change-out could be overstated.
If anyone has either installed or considered installing this type hardware, I would be most interested in your comments and experience. Thanks, sshep
We are considering a change-out of our conventional trays to get some additional reactor volume and any better performance which is possible from such a change. Currently I am inquiring into Shell's High Dispersion (HD) trays. I have a concern that the cost to benifit ratio of a change-out could be overstated.
If anyone has either installed or considered installing this type hardware, I would be most interested in your comments and experience. Thanks, sshep