intangible1984
Chemical
Hi All!
We are currently installing new gas treatment unit from H2S on our gas plant.
the unit flow scheme is as follows:
untreated gas enters lower part of the scrubber (absorber), while treating reagent solution (liquid) is sprayed upon it from above through the nozzle.
after gas liquid contact gas leaves scrubber trhough pipe at the top, while reagent solution falls down and using gravity is drained through another pipe to the reagent regeneration tank.
after fast regeneration solution is again circulated into the scrubber, nozzle, etc by liquid pump.
QUESTION:
given the gas rate m3/hour, solution liquid rate m3/hour, scrubber operating pressure (2-3 barg) how can we calculate dimensions of the scrubber, solution tank, pipe diameters etc?
If you could propose some books to read on this subject.
Thanx a lot!
We are currently installing new gas treatment unit from H2S on our gas plant.
the unit flow scheme is as follows:
untreated gas enters lower part of the scrubber (absorber), while treating reagent solution (liquid) is sprayed upon it from above through the nozzle.
after gas liquid contact gas leaves scrubber trhough pipe at the top, while reagent solution falls down and using gravity is drained through another pipe to the reagent regeneration tank.
after fast regeneration solution is again circulated into the scrubber, nozzle, etc by liquid pump.
QUESTION:
given the gas rate m3/hour, solution liquid rate m3/hour, scrubber operating pressure (2-3 barg) how can we calculate dimensions of the scrubber, solution tank, pipe diameters etc?
If you could propose some books to read on this subject.
Thanx a lot!