Absorber for selectively removing H2S from CO2-containing mixing gas
An absorbent and selective technology, applied to the separation of dispersed particles, chemical instruments and methods, separation methods, etc., to achieve high removal selectivity
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Embodiment 1
[0024] Such as figure 1 As shown, the prepared raw material gas (containing 1%H 2 S, 15% CO 2 , 84%N 2 ) into the bottom of the absorption tower and countercurrent contact with the absorbent entering the top of the tower, the H in the gas 2 S is absorbed, and the purified gas comes out from the top of the tower and enters the gas-liquid separator to recover the entrained liquid droplets and then vents.
[0025] The rich liquid that has absorbed the acid gas is drawn from the bottom of the absorption tower to the top of the regeneration tower, where it is regenerated by countercurrent contact with rising steam. The regenerated lean liquid is sent to the top of the absorption tower for absorption after being cooled. The gas from the top of the regeneration tower enters the regeneration gas cooler to recover the water vapor in the gas, and the regeneration gas is separated and then emptied.
[0026] When the gas flow rate is constant and the solution circulation volume is co...
Embodiment 2
[0030] Implementation example 2: Contains 1%H 2 S, 35% CO 2 , 64%N 2 The feed gas passes through such as figure 1 The absorption device, adopts the absorbent of the present invention to selectively remove H 2 S.
[0031] When the gas flow rate is constant and the solution circulation volume is constant, the operability of different absorbents is shown in Table 2.
[0032] Table 2: Operating performance of different absorbents
[0033]
[0034] The results show that the absorbent with added acid component has higher H 2 S selective.
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