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    • 2. 发明专利
    • MOVING LAYER REACTION TANK
    • JPS60118232A
    • 1985-06-25
    • JP22326083
    • 1983-11-29
    • MITSUI MIIKE KAKOKI KKMITSUI MINING CO LTD
    • FURUYAMA KUNINORIITOU YOSHIROU
    • B01D46/34B01D53/08B01D53/50B01D53/81B01J8/12
    • PURPOSE:To prevent the accumulation of dust to the louver part in a gas inlet side and the excessive rising in pressure loss, by eliminating the stay of the particulate substance on a louver to bring a good moving state. CONSTITUTION:In a moving layer reaction tank wherein a particulate substance 12 is held in a packed state by a louver structure and brought into contact with gas 25 passing louvers whole moved from above to below, sub-louvers 18, 19 each having an inverted V-shape cross-sectional area are provided to the insides of main louvers 17, which are arranged in one line in a vertical direction, in one line in parallel to the louvers 17 in order to hold the substance 12 in a packed state. The one side 18 of each sub-louver originates from the intermediate position in the height direction of each stage and forms a reverse gradient with respect to each louver 17 toward the inside of each louver 17 while the other side 19 is directed to a vertical downward direction from the apex of the V-shape and all stages are arranged so as to be present in the same vertical plane as well as the lower end of this vertically and downwardly directed side is prevented from contacting with the apex of the V-shape in the adjacent lower stage.
    • 9. 发明专利
    • WASTE GAS TREATING DEVICE
    • JPH11137945A
    • 1999-05-25
    • JP31073897
    • 1997-11-12
    • MITSUI MINING CO LTD
    • FURUYAMA KUNINORISHIMIZU SHIRO
    • B01D53/34B01D53/08B01D53/81
    • PROBLEM TO BE SOLVED: To prevent the leakage of a waste gas by renewing an adsorbent by the intermittent operation of a reaction tower and to keep the heights of the devices and entire equipment low. SOLUTION: A quantitative discharger 2, and automatic stop valve A, a closed chamber 3, a quantitative discharger 4 and an automatic stop valve B are provided between the outlet of a reaction tower 1 and a discharge conveyor 5 to form a first closed system. An automatic stop valve A, a closed chamber 10, an automatic stop valve B and a hopper 11 are furnished between a supply conveyor 9 and the supply port of the reaction tower 1 to form a second closed system. The supply port and discharge port of the gas for making the inside of each closed system a dry atmosphere are connected to each system. The reaction tower is intermittently operated to intermittently renew the adsorbent, the two automatic stop valves A and B of the first closed system or second closed system are alternately opened in synchronization with the renewal, and the adsorbent is discharged from or supplied to the reaction tower without discharging the waste gas.
    • 10. 发明专利
    • DRY TYPE EXHAUST GAS TREATMENT AND TREATING DEVICE
    • JP2000061253A
    • 2000-02-29
    • JP23724598
    • 1998-08-24
    • MITSUI MINING CO LTD
    • FURUYAMA KUNINORI
    • B01D53/34B01D53/08B01D53/81B01J20/20B01J20/34
    • PROBLEM TO BE SOLVED: To completely remove ammonia contained in desorbed gas. SOLUTION: An exhaust gas is caused to flow through an adsorber 1 packed with carbonaceous material to form a moving bed to perform solid-liquid contact of the carbonaceous material and the exhaust gas and to remove nitrogen oxides and other harmful materials contained in the exhaust gas. The carbonaceous material whose activity has been lowered is drawn out from the adsorber 1 and is fed to an ammonia removing column 2 and desorbed gas and oxygen containing gas generated in a regenerator 3 is fed to the ammonia removing column 2 to perform solid-gas contact with carbonaceous material and to remove ammonia contained in the desorbed gas. The carbonaceous material is drawn out from the ammonia removing column 2 and is fed to the regenerator 3 to perform heating/regenerating treatment of the carbonaceous material and to desorb and remove the harmful material. The carbonaceous material is drawn out from the regenerator 3 and is fed to a classifier 4 to remove dust and powdered carbonaceous material. In this way, the regenerating treatment of the carbonaceous material is performed, and also ammonia contained in the desorbed gas is removed.