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    • 1. 发明专利
    • HIGH TEMPERATURE GAS PIPELINE
    • JPH1122901A
    • 1999-01-26
    • JP17802997
    • 1997-07-03
    • HITACHI LTD
    • INAGE SHINICHISASAO TOSHIBUMIMURAKAMI TADATAKAKOBAYASHI SHIGEYOSHI
    • F16L9/00F22B1/02F23J11/00
    • PROBLEM TO BE SOLVED: To permit the restraining of abrasion and the like of a pipe while lowering a pressure loss by a method wherein a plurality of projections are arranged on the inner wall of curved part of a high temperature gas pipeline, through which exhaust gas, discharged out of a boiler, flows, with a space circumferentially between them. SOLUTION: Pulverized coal is burnt in a fluidized bed boiler by air, supplied by an air compressor, while high temperature gas 5, generated by the combustion of the pulverized coal, is introduced into a heat transfer tube, installed in the boiler. The high temperature gas 5 is transported to a gas turbine by a high temperature pipeline 10 through a header after removing ash particles by a cyclone. In this case, numberless of ash particles 13 are collided against the wall surface of the high temperature pipeline 10 and serious abrasion is generated on the wall surface of the pipe sometimes. Especially, the abrasion is remarkable in the curved part of the high temperature pipeline 10. Therefore, the projections or eddy generating devices 14 are installed on the inner wall of outer wall side of the curved part of high temperature pipeline 10. The eddy generating device 14 is provided with a triangular pyramid shape and the plurality of eddy generating devices 14 are installed across an area from the upstream side to the downstream side of the flow direction of gas in the pipeline with a space between each other.
    • 7. 发明专利
    • BURNER
    • JPH05113207A
    • 1993-05-07
    • JP27416991
    • 1991-10-22
    • HITACHI LTD
    • MURAKAMI TADATAKATANIGUCHI MASAYUKINARATO KIYOSHIKOBAYASHI YOSHINOBUAZUHATA SHIGERUKURODA MICHIOSATO ISAOTSUKAHARA SATOSHI
    • F23D14/26F23D14/74F23D14/78
    • PURPOSE:To provide a burner in which there is no fear of damage by burning and flames can be stably formed, by a method wherein a cooling medium is allowed to flow in the hollow part of the inside of a flame holder and is discharged into a combustion chamber. CONSTITUTION:A primary flame holder 2 and a secondary flame holder 4 are formed in a hollow structure. At the outside of a combustion chamber, a cooling medium 16 composed of combustion air 26, cooling air 37 and a mixture of spray water and the cooling air 37 is individually introduced into the insides of the primary flame holder 2 and the secondary flame holder 4 through guide pipes 21, which are the inlets of the cooling medium, and at the inside thereof, a heat-receiving surface on each of these flame holders is individually cooled. After the cooling medium 16 cools these surface, the cooling medium 16 is discharged into a primary mixed gas stream 1 and a secondary gas stream 3 through cut surface-like openings 17 which are formed at right angles to the primary and secondary gas streams 1, 3 respectively colliding with the primary and secondary flame holders 2, 4. In this way, even if the cooling medium discharged into the combustion chamber is increased, flames held on the basical surface of each of these flame holders are not affected thereby. In such a manner, the flame holders 2, 4 are cooled on combustion and damage by burning is prevented.
    • 9. 发明专利
    • INTERNAL REFORMING CATALYZER FOR FUEL CELL
    • JPS62287575A
    • 1987-12-14
    • JP13014086
    • 1986-06-06
    • HITACHI LTD
    • HIGASHIYAMA KAZUHISAYOSHIOKA SUSUMUMURAKAMI TADATAKASHIMODA MAKOTO
    • H01M8/02H01M8/06
    • PURPOSE:To kept off any catalytic degradation due to upward seepage of an electrolyte as well as to aim at the promotion of long service life in an internal reforming catalizer, by forming each end of two-side frames being opposed to each other, among frames of four sides, into a knife edge form. CONSTITUTION:A catalytic compact 23 set up in a catalyzer supporter 24 comes into contact with a catalyzer supporting surface 19 by a knife edge 22, and this contact part 14 comes to a linear contact. Methane and water vapor out of a fuel gas inlet 8 comes into contact with a catalytic layer while they flow in a space 15 at a lower part of the catalytic compact 23, and converted into hydrogen gas, while a rib 3 stably holds an electrolytic plate 12. An electrolyte contained in this plate 12 tries to climb by way of an anode 11, a collector plate 10 and a porous corrosive layer on a surface of the rib 3 and reach to the catalytic layer 1, but a linear contact part 14 by the knife edge and the supporting surface exists in the point midway in the route so that it fails to reach the catalytic layer, thus a reforming catalyzer can keep its activity for a long period of time.
    • 10. 发明专利
    • FUEL CELL
    • JPS6269467A
    • 1987-03-30
    • JP20650485
    • 1985-09-20
    • HITACHI LTD
    • SHIMODA MAKOTOYOSHIOKA SUSUMUMURAKAMI TADATAKAHIGASHIYAMA KAZUHISA
    • H01M8/02H01M8/06H01M8/24
    • PURPOSE:To uniform the distributions of electrical current density and temperature in a fuel cell, by annularly disposing an electrolyte plate, a fuel electrode, an oxidizer electrode, current collection plates and separators. CONSTITUTION:An annular fuel electrode 2 and an annular oxidizer electrode 3 are stuck to both the sides of an annular electrolyte plate 1. Annular current collection plates 5 are stuck to the surfaces of the fuel electrode 2 and the oxidizer electrode 3, which are not in contact with the electrolyte plate 1. This assembly is interposed between separators 4 whose central and peripheral portions have inlet and outlet ports for a fuel and an oxidizer. A catalyst for internal reformation is stuck to the separator 4 hear the fuel electrode 2. As as result, the distribution of heat in endothermic reaction is uniformed so that the distribution of temperature in a fuel cell is evened. Since the concentration of the fuel on the feed side thereof is higher, the velocity of gas flow is heightened. The velocity of gas flow is lowered where the fuel is consumed and the concentration of hydrogen is decreased. As a result, a sufficient cell reaction progresses even with a low concentration of hydrogen.