Novel saturation adsorption process of pressure swing adsorption decarburization and device thereof
A pressure swing adsorption, a new type of technology, applied in the direction of chemical instruments and methods, dispersed particle separation, separation methods, etc., can solve the problems of large loss of effective components and low absorption rate of gas, so as to reduce the loss of effective components and reduce the loss of gas Loss, the effect of realizing the recovery rate
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Embodiment 1
[0051] refer to figure 1 with figure 2 As shown, a novel saturated adsorption process of pressure swing adsorption decarburization provided by the present invention utilizes the adsorption towers arranged side by side to remove the CO in the feed gas 2 The gas is adsorbed and removed by the adsorbent in the adsorption tower to obtain purified gas. Each cycle of the adsorption process includes adsorption, pressure equalization drop, recovery RG, vacuum V, equal pressure rise, isolation Q and final boost FR, the adsorption includes pre-adsorption A1, adsorption A and post-adsorption A2, wherein: the specific process of the pre-adsorption A1 is to input the output gas of other adsorption towers in the post-adsorption A2 stage, and output the purified gas; the specific process of the adsorption A is Input the raw material gas and output the purified gas; the specific process of the post-adsorption A2 is to output the gas exceeding the purification gas index, which is used as the...
Embodiment 2
[0074] refer to figure 1 As shown, the present invention also provides a device for realizing the novel saturated adsorption process of above-mentioned pressure swing adsorption decarburization, comprising multiple groups of adsorption towers (a, b, c...) arranged side by side, and adsorption towers (a, b , c...) is connected to the raw material inlet valve (1a, 1b, 1c...) for feeding the raw material gas, and connected to the top of the adsorption tower (a, b, c...) for the purification of the output purified gas Gas outlet valves (2a, 2b, 2c...), the first pressure equalizing valves (3a, 3b, 3c...) connected to the top of the adsorption tower (a, b, c...) for equalizing pressure drop and equalizing pressure rise ...), the second pressure equalizing valve (4a, 4b, 4c...) and the third pressure equalizing valve (5a, 5b, 5c...), through the first control valve K3 and the second control valve K4 and the second equalizing valve respectively Pressure valve (4a, 4b, 4c...) and the...
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