Gas purification method
A technology of air flow and methanation, applied in the direction of carbon monoxide, through chemical separation, air quality improvement, etc., can solve expensive and other problems
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Embodiment 1
[0051] A 3 mm diameter, 10 feet long adsorbent bed was packed with commercially available 40 x 60 mesh activated carbon. The total weight of the adsorbent is about 5.4 grams. A feed stream containing 1% methane and 99% carbon monoxide was passed through the bed at -173°C and a pressure of 10 psig at a flow rate of 0.1 standard liters per minute. The methane concentration at the outlet of the bed was monitored using a total hydrocarbon analyzer. After the methane concentration started to rise rapidly, the methane concentration at the outlet of the bed remained below 1 ppm for about 343 minutes.
Embodiment 2
[0053] The experiment was performed using the column of Example 1 but at a feed pressure of 50 psig. The remaining conditions are the same as in Example 1. The methane concentration at the outlet of the bed remained below 1 ppm for 340 minutes.
Embodiment 3
[0055] About 250 grams of 6 * 8 purpose commercially available activated carbons are filled in a container with an inner diameter of about 1 inch. A feed containing 1% methane in carbon monoxide was fed to the above bed at a flow rate of 5 standard liters per minute at -173°C and a pressure of 50 psig. The methane concentration at the outlet of the bed is monitored. A methane concentration of less than 1 ppm was observed for about 217 minutes.
[0056] These examples show that relatively high hydrocarbon adsorption capacities can be obtained by adsorbing impurities from carbon monoxide at low adsorption temperatures.
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