shvet
Petroleum
- Aug 14, 2015
- 692
Hello everyone
We are dealing with process design of caustic treatment of LPG from mercaptans. Our issue concerns spent air of caustic regeneration. We have no fired heater nearby to route this in firebox and would not like to use fired incinerator. Please advice links to options:
- an incinerator with electric "burner" instead of fired one
- treatment on a small separate open elevated flare
Please note that spent air flowrate is 50-200 kg/h and it contains only traces of VOC and we do not need high degree of destruction as low odor threshold of disulfides is the only issue we faced. We are currently modelling a emissions dispersion to find out limits. But currently I would suggest 98% destruction is enough. It is unlikely will be more 99%.
P.S. Activated carbon and chemical adsorbent options were already rejected.
We are dealing with process design of caustic treatment of LPG from mercaptans. Our issue concerns spent air of caustic regeneration. We have no fired heater nearby to route this in firebox and would not like to use fired incinerator. Please advice links to options:
- an incinerator with electric "burner" instead of fired one
- treatment on a small separate open elevated flare
Please note that spent air flowrate is 50-200 kg/h and it contains only traces of VOC and we do not need high degree of destruction as low odor threshold of disulfides is the only issue we faced. We are currently modelling a emissions dispersion to find out limits. But currently I would suggest 98% destruction is enough. It is unlikely will be more 99%.
P.S. Activated carbon and chemical adsorbent options were already rejected.