Method for absorbing carbon dioxide in multistage microchannel reaction system
A technology of microchannel reaction and carbon dioxide, applied in the direction of absorption, chemical instruments and methods, separation methods, etc., can solve the problems of bulky absorption tower, limited mass transfer rate, high maintenance cost, etc., to shorten contact time and improve use efficiency , the effect of improving process efficiency
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Embodiment 1
[0034] A first-stage microchannel reaction system ( figure 1 ) to absorb carbon dioxide, the absorbent (LS1) used is an aqueous solution containing 30wt% monoethanolamine, the mixed gas (FG1) used is composed of carbon dioxide and nitrogen, and contains 100ppm oxygen at the same time, wherein the volume fraction of carbon dioxide is 30%, monoethanolamine The molar ratio to carbon dioxide is 2.3, the operating pressure of the microchannel absorber (R1) is 3MPa, the operating temperature is 45°C, and the equivalent diameter of the microchannel is 400 microns. The device absorbs carbon dioxide, such as Figure 6 As shown, the conversion rate of carbon dioxide is above 96%.
Embodiment 2
[0036] A first-stage microchannel reaction system ( figure 1 ) to absorb carbon dioxide, the absorbent (LS1) used is an aqueous solution containing 30wt% monoethanolamine, the mixed gas (FG1) used is composed of carbon dioxide and nitrogen, and contains 500ppm water vapor, wherein the volume fraction of carbon dioxide is 30%, slightly The operating pressure of the channel absorber (R1) is 5MPa, the operating temperature is 25°C, the equivalent diameter of the microchannel is 400 microns, the absorber containing 16 microchannels is adopted, the molar ratio of monoethanolamine to carbon dioxide is 6, and the residence time is 0.3 seconds, the concentration of carbon dioxide in the mixture (PG1) can be reduced to 50ppm.
Embodiment 3
[0038] A two-stage microchannel reaction system ( image 3 ) to absorb carbon dioxide, the absorbent used is an aqueous solution containing 30wt% diethanolamine, the mixed gas used comprises carbon dioxide, methane and a small amount of ethane and propane, and the volume fraction of carbon dioxide in the first stage mixed gas (FG1) is 70%, The operating pressure of the microchannel absorber (R1) is 3 MPa, and the operating temperature is 25°C. The microchannel absorber containing 16 microchannels is adopted. The equivalent diameter of the microchannel is 700 microns, and the molar ratio of diethanolamine to carbon dioxide is 2.2. The residence time is 0.06 seconds. After absorption, the volume fraction of carbon dioxide in the mixed gas (PG1) is reduced to 3.0%; the gas valve (GV1, 0) is fully closed, and the gas valve (GV1, 2) is fully opened to make the mixed gas ( PG1) all enter the second-stage microchannel system; the operating pressure of the second-stage microchannel ab...
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