22.
    发明专利
    未知

    公开(公告)号:DE59603806D1

    公开(公告)日:2000-01-05

    申请号:DE59603806

    申请日:1996-09-10

    Applicant: BASF AG

    Abstract: PCT No. PCT/EP96/03971 Sec. 371 Date Mar. 10, 1998 Sec. 102(e) Date Mar. 10, 1998 PCT Filed Sep. 10, 1996 PCT Pub. No. WO97/10042 PCT Pub. Date Mar. 20, 1997The invention relates to a process for removing nitrogen oxides from a gas stream containing same, which comprises passing the gas stream (A) through a stage for absorbing the nitrogen oxides other than N2O in an absorbent or reacting the nitrogen oxides other than N2O with an absorbent at a pressure of from 1,5 to 20 bar, and (B) through a stage for reducing the amount of N2O, preferably employing the pressure level of step A, and to apparatus therefor and the use thereof.

    Reactor for catalytically oxidizing ammonia to nitrogen oxides

    公开(公告)号:DE19819882A1

    公开(公告)日:1999-10-28

    申请号:DE19819882

    申请日:1998-04-27

    Applicant: BASF AG

    Abstract: Reactor for catalytically oxidizing ammonia to nitrogen oxides contains a catalyst for decomposing N2O arranged between a precious metal lattice catalyst and a heat exchanger. Independent claims are also included for: (A) an apparatus for the production of nitric acid from ammonia comprising a reactor for catalytically oxidizing ammonia to nitrogen oxides containing a catalyst for decomposing N2O arranged between a precious metal lattice catalyst and a heat exchanger, and an absorber for nitrogen oxides, and a reducer for reducing nitrogen oxides; and (B) a process for catalytically decomposing N2O comprising contacting a hot gas mixture produced from the catalytically oxidation of ammonia with the catalyst for decomposing N2O before subsequent cooling.

    METHOD FOR THE CATALYTIC DECOMPOSITION OF N2O

    公开(公告)号:CA2329871C

    公开(公告)日:2008-10-07

    申请号:CA2329871

    申请日:1999-04-15

    Applicant: BASF AG

    Abstract: In the reactor for the catalytic oxidation of ammonia into nitrogen oxides, which in the direction of flow contains, in this order, a precious-metal gauze catalyst and a heat exchanger, a catalyst for the decomposition of N20 is positioned between the precious-metal gauze catalyst and the heat exchanger. According to said method for the catalytic decomposition of N20 in a gaseous mixture obtained during the production of nitric acid by catalytic oxidation of ammonia, on a catalyst intended for the decomposition of N20, the hot gas mixture obtained as a result of the catalytic oxidation of ammonia is brought into contact with the catalyst used for the decomposition of N20 before being cooled.

    30.
    发明专利
    未知

    公开(公告)号:NO20000666L

    公开(公告)日:2000-08-14

    申请号:NO20000666

    申请日:2000-02-10

    Applicant: BASF AG

    Abstract: Use of an apparatus for distributing an ammonia/air mixture arising from ammonia oxidation on the cross-section of a reactor whose diameter is a multiple of the pipe diameter, where the inlet pipe is provided with a concentric inner pipe, to prevent the formation of N2O during ammonia oxidation is new.

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