REACTOR AND METHOD FOR REDUCING THE NITROGEN OXIDE CONTENT OF A GAS
    12.
    发明公开
    REACTOR AND METHOD FOR REDUCING THE NITROGEN OXIDE CONTENT OF A GAS 审中-公开
    反应器的还原气体的氮氧化物

    公开(公告)号:EP1414551A1

    公开(公告)日:2004-05-06

    申请号:EP02773985.3

    申请日:2002-02-25

    Abstract: A parallel flow reactor (20) for the selective catalytic reduction of nitrogen oxide in a gas stream includes a shell (21) enclosing an interior space in which is located a plurality of substantially parallel planar catalyst beds (23a-f), each containing a catalyst for the selective conversion of NOx. Deflectors (24a-e) in the spaces between the catalyst beds direct the flow of gas through the beds. An injector (22) upstream of the catalyst beds introduces a reducing agent such as ammonia into the inlet gas stream. The catalyst bed can include monolith or microengineered catalyst.

    PYROLYSIS HEATER WITH PAIRED BURNER ZONED FIRING SYSTEM
    14.
    发明公开
    PYROLYSIS HEATER WITH PAIRED BURNER ZONED FIRING SYSTEM 有权
    与PAIRED刻录机和多个区域的FEUERUNGSSYTEM PYROLYSEERHITZER

    公开(公告)号:EP1397466A1

    公开(公告)日:2004-03-17

    申请号:EP02744331.6

    申请日:2002-06-12

    CPC classification number: C10G9/20

    Abstract: A pyrolysis heater has the inlet sections of the process coils grouped together and the outlet sections of these same process coils also grouped together. High heat liberation hearth burners are located adjacent to the inlet sections of the coils and lower heat liberation burners are located adjacent to the outlet sections. The secondary fuel tips of the burners are inclined toward the adjacent, heater wall. The high heat liberation hearth burners adjacent to the inlet coils are arranged in spaced apart pairs with the secondary burner tips of each of the pair being inclined toward the other burner of the pair.

    INTEGRATED RESIDUE THERMAL CRACKING AND PARTIAL OXIDATION PROCESS
    18.
    发明公开
    INTEGRATED RESIDUE THERMAL CRACKING AND PARTIAL OXIDATION PROCESS 有权
    综合热RÜCKSTANDKRACK-及部分氧化法处理

    公开(公告)号:EP1204719A1

    公开(公告)日:2002-05-15

    申请号:EP00918451.6

    申请日:2000-03-27

    CPC classification number: C10G9/38 C10G47/22 C10G49/007 C10G69/06 Y10S208/95

    Abstract: A residue from petroleum refining is thermally cracked to convert the residue to useful cracked products and to generate fuel gas. The residue is cracked by contact with hot synthesis gas produced by the gasification on the tar/pitch residue remaining after the cracking of the residue feed. Waste heat can be recovered from remaining portions of the synthesis gas from the gasifier in the form of steam which can be used in the gasification process and in the cracking process as needed for coke suppression. The combustible synthesis gas and the combustible gasses from the thermal cracking are separated from the cracked product liquid and used for power generation in a combined cycle plant.

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