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    • 2. 发明授权
    • Gas-liquid mass transfer process
    • 气体液相转移过程
    • US3754377A
    • 1973-08-28
    • US3754377D
    • 1972-11-17
    • MERICHEM CO
    • CLONTS K
    • B01D47/02B01D53/16
    • B01D47/025
    • A component of at least one of two fluids is transferred into the other by introducing a liquid onto the surface of fibers extending generally linearly along a conduit with the fibers filling the cross-sectional area of at least a portion of the length of the conduit and being wetted by the liquid, flowing a gas through the conduit past the fibers thereby dragging a film of the liquid along the fibers, collecting the liquid in a gravity separator approximate the downstream end of the fibers and then separately removing the two fluids from the separator.
    • 将两种流体中的至少一种的组分转移到另一种流体中,通过将纤维引入到沿导管大致线性延伸的纤维的表面上,纤维填充导管长度的至少一部分的横截面积, 被液体润湿,使气体通过管道流过纤维,从而沿着纤维拖动液体膜,在重力分离器中收集液体近似于纤维的下游端,然后分离地从分离器中除去两种流体 。
    • 7. 发明授权
    • Gas-absorption process
    • 吸气过程
    • US4129425A
    • 1978-12-12
    • US816575
    • 1977-07-18
    • Michael J. StephensonRobert S. Eby
    • Michael J. StephensonRobert S. Eby
    • B01D3/32B01D53/14B01D53/16
    • B01D53/1418B01D3/322B01D53/14B01D53/1406
    • This invention is an improved gas-absorption process for the recovery of a desired component from a feed-gas mixture containing the same. In the preferred form of the invention, the process operations are conducted in a closed-loop system including a gas-liquid contacting column having upper, intermediate, and lower contacting zones. A liquid absorbent for the desired component is circulated through the loop, being passed downwardly through the column, regenerated, withdrawn from a reboiler, and then recycled to the column.A novel technique is employed to concentrate the desired component in a narrow section of the intermediate zone. This technique comprises maintaining the temperature of the liquid-phase input to the intermediate zone at a sufficiently lower value than that of the gas-phase input to the zone to effect condensation of a major part of the absorbent-vapor upflow to the section. This establishes a steep temperature gradient in the section. The stripping factors below this section are selected to ensure that virtually all of the gases in the downflowing absorbent from the section are desorbed. The stripping factors above the section are selected to ensure re-dissolution of the desired component but not the less-soluble diluent gases. As a result, a peak concentration of the desired component is established in the section, and gas rich in that component can be withdrawn therefrom.The new process provides important advantages. The chief advantage is that the process operations can be conducted in a single column in which the contacting zones operate at essentially the same pressure.
    • 本发明是一种改进的气体吸收方法,用于从含有该组分的原料 - 气体混合物回收所需组分。 在本发明的优选形式中,工艺操作在包括具有上,中,下接触区的气 - 液接触塔的闭环系统中进行。 用于所需组分的液体吸收剂循环通过循环,向下通过柱,再生,从再沸器中取出,然后再循环至塔中。