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    SUPPORT STRUCTURE FOR A CATALYST
    5.
    发明专利
    SUPPORT STRUCTURE FOR A CATALYST 未知

    公开(公告)号：CA2257874A1

    公开(公告)日：1997-12-18

    申请号：CA2257874

    申请日：1996-06-10

    Applicant: TANAKA PRECIOUS METAL IND ,  CATALYTICA INC

    Inventor： BEEBE KENNETH WINSTON ,  SCHLATTER JAMES C ,  DALLA BETTA RALPH A ,  CUTRONE MARTIN BERNARD

    IPC: F23R3/40 ,  B01J32/00 ,  B01J35/00

    Abstract: A support structure (53) for securing a catalyst structure (52) comprising a multiplicity of longitudinally disposed channels for passage of a flowing gas mixture within a reactor, said support structure being comprised of a monolithic open celled or honeycomb-like structure formed by thin strips or ribs of high temperature resistant metal or ceramic which abuts against one end of the catalyst structure, and extends in a direction perpendicular to the longitudinal axis of the catalyst structure to essentially cover an end face (at either the inlet end or outlet end or both) of the catalyst structure with the support structure being secured (54) on its periphery to the reactor wall. The strips or ribs making up the support structure are bounded together to form a unitary structure having cellular openings at least as large as the catalyst structure channel openings. The cellular openings in the support structure are also positioned to be in fluid communication with the channels of the catalyst structure thus affording essentially unaltered gas flow (50) from the catalyst structure through the support structure.

    MULTISTAGE PROCESS FOR COMBUSTING FUEL MIXTURES
    7.
    发明专利
    MULTISTAGE PROCESS FOR COMBUSTING FUEL MIXTURES 未知

    公开(公告)号：CA2096951A1

    公开(公告)日：1992-05-27

    申请号：CA2096951

    申请日：1991-11-26

    Applicant: CATALYTICA INC ,  TANAKA PRECIOUS METAL IND

    Inventor： DALLA BETTA RALPH A ,  SCHLATTER JAMES C ,  NICKOLAS SARENTO G ,  TSURUMI KAZUNORI ,  EZAWA NOBUYASU

    IPC: F23D14/18 ,  F23C6/04 ,  F23C13/00 ,  F23C99/00

    Abstract: 2096951 9209849 PCTABS00013 This invention is a combustion process having a series of stages in which a fuel/oxygen-gas-containing mixture (16, 18) is combusted stepwise using a series of specific catalysts and catalytic structures (figure 2) and, optionally, a final homogeneous combustion zone to produce a combusted gas at a selected temperature preferably between 1050· and 1700 ·C. Depending upon the pressure of operation, there may be two or three discrete catalytic stages (stages 1, 2 and 3). The choice of catalysts and the use of specific structures, including those employing integral heat exchange (44) results in a catalyst and its support which are stable due to their comparatively low temperature, do not deteriorate, and yet the product combustion gas is at a temperature suitable for use in a gas turbine, furnace, boiler, or the like, but has low NOx content. Neither fuel nor air is added to the combustion process except in the initial stage.

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