METHOD FOR THE DEACIDIFICATION OF A FLUID STREAM BY MEANS OF AN INERT SCRUBBING COLUMN AND CORRESPONDING DEVICE
    1.
    发明申请
    METHOD FOR THE DEACIDIFICATION OF A FLUID STREAM BY MEANS OF AN INERT SCRUBBING COLUMN AND CORRESPONDING DEVICE 审中-公开
    方法流体流过脱酸惰性洗涤塔及其装置

    公开(公告)号:WO2004108244A3

    公开(公告)日:2005-01-27

    申请号:PCT/EP2004005849

    申请日:2004-05-29

    Abstract: The invention relates to a method for the deacidification of a fluid stream, containing acidic gases as impurities, whereby the fluid stream is brought into intimate contact with an absorption agent at a pressure of 0.5 to 20 bar in at least one absorption step, with the proviso that the absorption step and, in the case of multiple absorption steps, at least one of the absorption steps is carried out in an inert scrubbing column, the internal surface of which is essentially made from plastic or rubber.

    Abstract translation: 一种用于在其条件紧密接触脱酸含有酸性气体作为杂质的流体流,该方法包括将至少一个吸收步骤,以0.5:1的压力至20巴的流体流与吸收过程的吸收步骤和在的情况下 几个吸收步骤在惰性洗涤塔的吸收步骤中的至少一个,所述内表面基本上由塑料或橡胶,被执行。

    3.
    发明专利
    未知

    公开(公告)号:DE10133788A1

    公开(公告)日:2003-02-06

    申请号:DE10133788

    申请日:2001-07-16

    Applicant: BASF AG

    Abstract: The invention relates to a method for the separation of ammonia from a mixture which contains ammonia and whose boiling point in an ammonia-free state is more than 50 DEG C higher than the boiling point of pure ammonia, characterized in that said method comprises n stages, n being a natural number of at least 2, wherein a) said mixture is fed to stage 1; b) at each stage m, m being a natural number of 1 to n-1, part of the ammonia is separated from the educt mixture fed from stage 1 at a pressure Pm by means of evaporation in order to obtain a product mixture which has an ammonia content corresponding to pressure Pm and temperature tm, and gaseous ammonia, c) the product mixture obtained in stage m is used in step m+1 as an educt mixture, with the exception of stage n, according to step b), d) in step n, the ammonia is separated at a pressure Pn and temperature tn either partially or fully from the educt mixture fed from stage n-1 by means of evaporation in order to obtain a product and gaseous ammonia, each pressure Pm being greater than Pm+1.

    Treating combustion gases containing sulfur- and carbon dioxides, e.g. from power stations, by two-stage scrubbing with aqueous calcium hydroxide or carbonate then e.g. amine or potassium hydroxide solution

    公开(公告)号:DE10340349A1

    公开(公告)日:2005-03-24

    申请号:DE10340349

    申请日:2003-09-02

    Applicant: BASF AG

    Abstract: Treatment of combustion gases (I) containing sulfur dioxide (SO2) and carbon dioxide (CO2) comprises a first absorption stage (a), in which SO2 is removed by scrubbing with aqueous suspension of calcium hydroxide or calcium carbonate, followed by a second absorption stage (b) in which CO2 is removed by scrubbing with amine(s) (II) (optionally in aqueous solution), aqueous potassium hydroxide solution (optionally containing (II)) or aqueous aliphatic aminoacid alkali metal salt solution, the CO2-charged scrubbing liquid from (b) being regenerated and recycled. Treatment of combustion gases (I) containing sulfur dioxide (SO2) and carbon dioxide (CO2) as impurities involves: (1) an absorption stage (a), in which the gas is intimately contacted with a scrubbing liquid (A) comprising an aqueous suspension of calcium hydroxide or calcium carbonate, followed by separating the SO2-charged scrubbing liquid (A) and the remaining, non-absorbed part of (I); (2) an absorption stage (b), in which the non-absorbed part of (I) is intimately contacted with a scrubbing liquid (B) comprising a solution (b1) consisting of at least one amine compound (II) (optionally in aqueous solution), a solution (b2) consisting of water, potassium hydroxide and optionally (II) or a solution (b3) consisting of water and the alkali metal salt of an aliphatic aminoacid, followed by separating the CO2-charged scrubbing liquid (B) and the remaining, non-absorbed part of (I); and (3) regenerating the CO2-charged solution (B) and recycling it to absorption stage (b). (II) are selected from 4-12C aliphatic or cycloaliphatic amines; 4-12C alkanolamines; and cyclic amines consisting of 5-7 membered heterocycles consisting of 1 or 2 N atoms and 1 or 2 alkanediyl groups.

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