Vanesssa
Chemical
- Jul 16, 2007
- 1
Hi to everyone,
I have been asked to do a check and I have some doubts.
I have a kerosene stripper which is fed from a fractionation column.
Currently There is no baffle at the base of the stripper and the heat is supplied by means of a furnace (part of the bottom stream passes through the furnace before being sent back to the stripper).
I was wondering which are the benefits of installing a baffle at the base? Additional equilibrium stage?
Another point, if the furnace was to be replaced by a reboiler (to recover heat of a residual stream) there could be 2 options: thermosiphon or forced circulation using a pump.
Obviously there would a difference in the heat tranfer coeeficient, but would there be any other considerations to choose the best option?
Any suggestions on correlations to be used for this system?
Thanks.
I have been asked to do a check and I have some doubts.
I have a kerosene stripper which is fed from a fractionation column.
Currently There is no baffle at the base of the stripper and the heat is supplied by means of a furnace (part of the bottom stream passes through the furnace before being sent back to the stripper).
I was wondering which are the benefits of installing a baffle at the base? Additional equilibrium stage?
Another point, if the furnace was to be replaced by a reboiler (to recover heat of a residual stream) there could be 2 options: thermosiphon or forced circulation using a pump.
Obviously there would a difference in the heat tranfer coeeficient, but would there be any other considerations to choose the best option?
Any suggestions on correlations to be used for this system?
Thanks.