chemcad helps to clean bio gas without chemicals · pdf filefocused on process simulation page...
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�focused on process simulation
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CHEMCAD helps to clean bio gas without chemicals
The Pressurized Water Process is used to remove carbon dioxide and hydrogen sulfide from bio
gas in order to upgrade it to natural gas quality.
The good thing: No chemicals besides water are required for this gas treatment processes.
Besides CO2 and H2S, the methane is also absorbed in the pressurized water. In order to reduce
the loss of methane the rich water coming from the absorber is flashed at an intermediate
pressure. The pressure is chosen to be the pressure in between the two compressors used for
the feed compression. This helps to reduce the power consumption of the first compressor.
Have a look at the CHEMCAD flowsheet of the gas treatment process and the specified design
variables on the next page! Our solution has an exergetic efficiency of 50.09%.
However, there are still many degrees of freedom left!
• Which pressure levels (absorber pressure and intermediate pressures), which
temperatures (gas and liquid feed temperatures), and which flowrates (water cycle and
stripping air) lead to the optimal process by means of exergy conversion?
• Is it good to produce more methane at the costs of higher electricity consumption?
• Can the stripping air flowrate be reduced when more cycle water is circulated or
different pressures are used?
• How does the purge effect process performance?
Optimize the exergetic efficiency and send us your solution in the Process Simulation Cup 2016!
© Berthold Werkmann
�focused on process simulation
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Participants of the Process Simulation Cup 2016 can download CHEMCAD and the flowsheet
from this website and be a monthly or the overall winner.
Design
Variable Name
Unit Op /
Stream Value Unit
Lower
Bound
Upper
Bound
1 Intermediate Pressure U 1 2.6
bar abs. 1.1 20
2 Absorber Pressure U 4 17.5 bar abs. 1.1 25
3 Gas Feed Temperature U 5 50 °C 20 80
4 Liquid Feed Temperature U18 32 °C 20 80
5 Stripping Air Flowrate S 13 850 stdVm³/h 10 1000
6 Cycle Water Flowrate U 14 236 stdLm³/h 5 500
7 Purge Ratio U 11 3.00% - 1% 10%
8 Intermediate Pressure 2 U 20 7.5 bar abs. 1.1 20