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The results have been compared to similar tests with a model gas mixture and a series of test in a laboratory scale reactor for monolithic samples.
The successful application of a microchannel reactor to reduce the CO content by methanation in a model gas mixture containing CO, CO2, O2 and H2 can be shown.
Yet, the beneficial effect of ceria, dominant in the model gas mixture, is largely dumped in tail gases at low temperature.
We have demonstrated the application of a Pt/Al2O3/CeO2 catalyst into a microreactor to reduce the CO content by preferential oxidation in a H2 rich model gas mixture.
The catalysts were thoroughly characterized (XRD, RS, SEM/TEM/EDX, XRF), and their catalytic deN2O activity was investigated using model gas mixture (2000 ppm N2O/N2), and tail gases (1400 ± 50 ppm N2O, 900 ± 100 ppm NOx, 0.8 ± 0.2 vol.% H2O, 2.0 ± 0.2 vol.% O2) of the nitric acid pilot plant.
For adsorption, a model gas mixture containing (99.4 % of CH4, 0.41 % of CO2, and 0.15 % of H2S) was passed through the adsorption cell with a flow rate of 40 mL min−1.
Similar(54)
A theoretical model simulating gas mixture separation using a composite inorganic membrane for high temperatures (T>400 °C) is proposed.
This model needs the gas mixture compositions.
Development and verification of 3-d transient mathematical model of chemically reacting gas mixture flows incorporating hydrogen was performed.
The tissue explants were incubated for 4 h at 37°C in 4 mL medium (DMEM-F12 with 10% FCS) in a sterile CO2 incubator (Shel Lab Model IR2424) with a gas mixture that composed of 8percentt O2, +87percentN2+5percentent CO2 (normoxia), with constant gas pressure.
This model could simulate a multicomponent gas mixture separation by solving the governing differential mass balance equations with numerical methods.
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model gas reactor
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model gas network
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model gas holdup
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model gas survival
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