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    • 2. 发明专利
    • ENDOTHERMIC REACTION APPARATUS
    • JPS58124533A
    • 1983-07-25
    • JP747582
    • 1982-01-22
    • MITSUI TOATSU CHEMICALS
    • TAKARADA SHINZOUKIMURA TETSUOCHIMASA KIYOKATAARAI AKIRAHOSONUMA AKIRAOGUCHI GOROU
    • C01B3/38B01J8/02B01J8/06
    • PURPOSE:To enhance working efficiency, by a method wherein a reactor is divided into plural blocks and each block is formed from an integrated structure consisting a reaction tube, a stock gas introducing manifold, a reaction product gas discharge manifold, a stock gas inlet manifold and a product gas outlet manifold. CONSTITUTION:Plural reaction tubes 21 are parallelly arranged in a reaction vessel 2. Each reaction tube 21 has a multilayered ring like cross section and a first combustion gas passage 11 is formed to the innermost side thereof, the first partitioned chamber 20a of a reaction chamber 20 to the outside thereof, a regeneration chamber 40 to the outside of said partitioned chamber 20a and the second partitioned chamber 20b of the reaction chamber 20 to the outermost side thereof. To the outside of each reaction tube 21, a second combustion gas passage 12 is formed. Each reaction tubes 21 are arranged in five rows toward a traverse direction and the reaction tube 21a of the first row and the reaction tube of the second row form the first block 23 of the reaction tubes and, by the reaction tube 21d of the fourth row and the reaction tube 21e of the fifth row. the second block 24 of the reaction tubes is formed.
    • 3. 发明专利
    • METHOD FOR FINDING NEW LEAKAGE IN MINUTE LEAKAGE GAS ATMOSPHERE IN PLANT
    • JPH08304216A
    • 1996-11-22
    • JP11611695
    • 1995-05-15
    • MITSUI TOATSU CHEMICALS
    • HOSONUMA AKIRATAKAHASHI SABURO
    • G01M3/04
    • PURPOSE: To find newly arising gas leakage under a condition where minute gas leakage unavoidably is present at many points by always processing measurements of a plurality of gas sensors and a plurality of anemometers by means of an arithmetic unit. CONSTITUTION: By assuming a plurality of leaking points 1-10 (numerals in squares) in a plant, the leaking amounts at the assumed leaking points are calculated by applying the measurements of gas sensors and anemometers during a fixed period of time in the past and coordinate values of the assumed leaking points to a gaseous diffusion equation. Then, the present theoretical values of the gas sensors are calculated from the present measurements of the anemometers on the leaking amounts. The differences between the theoretical values and the present actual values of the gas sensors are calculated. Thereafter, the fluctuating ranges of the filtered numerical values from the gas sensors due to the conventionally existing minute leakage are estimated by statistically processing the filtered numerical values from the gas sensors during a fixed period of time (e.g. 12-24 hours) and, when a larger filtered numerical value than the fluctuating width is obtained from a gas sensor, the occurrence of new leakage is recognized.