mahmmoud30
Chemical
- Aug 6, 2009
- 21
Hi all
regarding the title, it is a naphtha stabilizer column which separate LPG from hydrotreated naphtha with a bottom temp. of 176 deg C at the reboiler draw-out and 190 deg C at the reboiler return.
the feed flow into this column is ranging from 24~35 ton/h
* my question is why the reboiler return is designed below the reboiler draw-out?
thanks in advance
regarding the title, it is a naphtha stabilizer column which separate LPG from hydrotreated naphtha with a bottom temp. of 176 deg C at the reboiler draw-out and 190 deg C at the reboiler return.
the feed flow into this column is ranging from 24~35 ton/h
* my question is why the reboiler return is designed below the reboiler draw-out?
thanks in advance