Problem:
We have Hydrogen Sulfide(H2S) generation plant. Generated H2S (@ 200 Kg/Hr.) is compressed from 1.2 atm g to 19-20 atm g to feed it into the Purge Tower of Main Unit. (Purge Tower is at pressure of 16-17 atm g). For this pupose we use 3 stage reciprocating compressor. I thought of a method to charge this gas from H2S generation plant to Main Unit without this compressor, thereby saving the energy cost of compressor.
In Main Unit, we have feed stream at a pressure of 28-30 atm g, This feed stream goes to purge tower, which is operated at 16-17 atm g. There is an LCV on this feed stream, which controls the level of purge tower. Hence there is 12-13 atm pressure drop across this control valve. I want to take advantage of this pressure drop and an eductor to charge H2S gas to Purge Tower. I want to provide the eductor across the LCV using the feed stream as power fluid. H2S gas dissolves immediately in the feed stream.
I want some help in the design of eductor for the above system. The following are the conditions:
Power fluid inlet pressure is 28-30 atm g, temp=30degC, density~1gr/cc
Power fluid outlet pressure is 16.5-17.5atm g
H2S gas pressure at the inlet to eductor is 0.6-0.7 atm g, temp is 30 degC
Throat pressure can be 0.3-0.4 atm g
I searched internet, books for the design but I did not find any. Can any body suggest me how to design or the web address where I can found some information, for which I will be very much thankful.
Regards
sskumar
