JRLAKE
Mechanical
- Aug 2, 2006
- 145
Hey guys, I was hoping to get some direction on a unique gas compression application. I need a compressor (small at first for research pilot plant) to compress a mixture of gases about 50 PSI with an inlet pressure of either 100 PSIG or 250 PSIG. The final design will be a constant inlet pressure. We are exploring economic factors between 100 PSIG inlet and 250 PSIG inlet pressures.
Here are the rest of the details:
-Pulling from a sulfuric acid reactor / vessel (either 100 or 250 PSIG)
- Composition: primarily CO2 (90%) with the remaining 10% being a mixture of other acid gases: hydrogen sulfide, methyl mercaptan, ethyl mercaptan, dimethyl sulfide, diethyl sulfide.
- Estimated flow rate is 11 gms / min
-Temperatures at inlet estimated at 200 Degrees Celcius
I was leaning towards a liquid ring vacuum pump like a SiHi. However I am thinking the high inlet pressures will not work well with this design.
Suggestions?
Here are the rest of the details:
-Pulling from a sulfuric acid reactor / vessel (either 100 or 250 PSIG)
- Composition: primarily CO2 (90%) with the remaining 10% being a mixture of other acid gases: hydrogen sulfide, methyl mercaptan, ethyl mercaptan, dimethyl sulfide, diethyl sulfide.
- Estimated flow rate is 11 gms / min
-Temperatures at inlet estimated at 200 Degrees Celcius
I was leaning towards a liquid ring vacuum pump like a SiHi. However I am thinking the high inlet pressures will not work well with this design.
Suggestions?