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    • 12. 发明专利
    • MAGNETIC SEPARATION APPARATUS
    • JPH09248485A
    • 1997-09-22
    • JP5481596
    • 1996-03-12
    • MITSUBISHI HEAVY IND LTD
    • NAKAYA JIYUNNOSUKEKATAYAMA HIROYUKIMATSUGAMI MANABUIMATAKE SHIGENORIKIMURA TAKUYA
    • B03C1/26
    • PROBLEM TO BE SOLVED: To provide a magnetic separation apparatus capable of enhancing separation efficiency py reducing the effect of an element other than magnetic force and increasing the stagnation time of particles within an internal duct. SOLUTION: In this magnetic separation apparatus passing fine particles consisting of a plurality of components through an internal duct 17 having a magnetic field gradient in its radius direction and separating a specific substance by the difference between the magnetic forces acting on particles of a substance to be separated, a container 1, a multipole magnet 4, a cooling medium container 6, the internal duct 17, multistage fins 18 and a multistage fin support means 19 are provided and the cooling medium container 6 is arranged in the container l so as to be positioned outside the internal duct 17 and the multipole magnet 4 is arranged between the inner and outer cylinders 2,3 of the cooling medium container 6 and the gap between the inner and outer cylinders 2, 3 is filled with a cooling medium Z and the internal duct 17 has the multistage fins 18 therein and each of the multistage fins 18 has a large opening end at the upper part thereof and a small opening and at the lower part thereof.
    • 13. 发明专利
    • CIRCULATED FLUIDIZED BED BOILER
    • JPH09133316A
    • 1997-05-20
    • JP28973795
    • 1995-11-08
    • MITSUBISHI HEAVY IND LTD
    • BANDAI SHIGEMIYAMAUCHI TAKAMASAKATAYAMA HIROYUKI
    • F23C10/00F22B1/02F23C11/02
    • PROBLEM TO BE SOLVED: To make it unnecessary to install a fluidized bed heat exchanger in a seal pot into which fluidized material separated from combustion gas is guided by providing a circulating pipe for part of the combustion gas which has been discharged from a furnace and passed through a group of heat transfer pipes to return to the furnace. SOLUTION: Fuel and air are supplied to a bottom portion of a furnace 1 and are mixed with fluidized material supplied from a seal pot 3 to effect combustion. The fluidized material discharged together with combustion gas from the furnace 1 is separated from the combustion gas in a cyclone 2 before being returned to the furnace 1 via the seal pot 3. The exhaust combustion gas is utilized to produce superheated vapor in a group of the heat transfer pipes 4 before being discharged. Part of the combustion gas temperature of which has been lowered by being allowed to pass through the group of the heat transfer pipes 4 is guided into the furnace 1 through a circulating pipe 5 to be injected into air. By introducing the part of exhaust gas passing through the group of the heat transfer pipes 4 and having a temperature of 100 to 200 deg.C into the furnace 1 through the circulating pipe 5, temperature within the furnace 1 can be controlled at around 800 deg.C without installing a fluidized bed heat exchanger in the seal pot 3.
    • 16. 发明专利
    • WET ELECTRIC PRECIPITATOR
    • JPH07232098A
    • 1995-09-05
    • JP2666194
    • 1994-02-24
    • MITSUBISHI HEAVY IND LTD
    • MAEKAWA SHIKIAKIMAEJIMA HIDEYUKIKATAYAMA HIROYUKIKOJIMA KATSUHISA
    • B03C3/16B03C3/41
    • PURPOSE:To increase a dust collection rate by providing flat plate-type dust collection electrodes arranged in parallel in a vertical direction, and bar-type discharge electrodes arranged in the center between the dust collection electrodes, with a specified clearance left to a face on which the top and bottom ends of the discharge electrode come in contact with those between the dust collection electrodes. CONSTITUTION:A wet electric precipitation consists of flat plate-type dust collection electrodes 2a arranged parallel to each other in a vertical direction, and bar-type discharge electrodes 3a arranged in the center between the dust collection electrodes 2a with a specified clearance left to a face P on which the top and bottom ends of the bar-type discharge electrode 3a come into contact with the top and bottom ends between the dust collection electrodes. That is, liquid droplets collected by the dust collection electrodes 2a run downward over the surface of the dust collection electrode and drip down from the edge of the dust collection electrode. In this case, from the face P which comes into contact with the top and bottom ends between the dust collection electrodes 2a, i.e., the top end surface and the bottom end surface, the top end and the bottom end of the discharge electrode are arranged, leaving a specified clearance L. Therefore, an attraction from the discharge electrode 3a lessens so that the liquid droplets do not become deformed significantly compared to a conventional dust collector. Thus it is possible to apply a higher collector voltage and consequently, the dust collection rate is enhanced.
    • 17. 发明专利
    • ELECTROSTATIC PRECIPITATOR
    • JPH06343896A
    • 1994-12-20
    • JP13849193
    • 1993-06-10
    • MITSUBISHI HEAVY IND LTD
    • KATAYAMA HIROYUKIKOJIMA KATSUHISANAGATA MASAYUKIKITA TOSHITOMO
    • B03C3/16B03C3/41B03C3/78
    • PURPOSE:To avoid a spark by notching the lower end part of a dust collecting electrode from the center toward the corners of the lower end in a downward inclination to enlarge the distance between the droplets of washing liquid falling on the dust collecting electrode and a wire type discharge electrode. CONSTITUTION:In an electrostatic precipitator having plural rectangular dust collecting electrode 1, wire type discharge electrodes 2 coaxially arranged to the rectangular dust collecting electrode 1, and spray nozzles 7 arranged downward above the rectangular dust collecting electrodes, the lower end part of each face (a) of the rectangular dust collecting electrodes 1 is notched from the center toward the corners (b) of the lower end in a downward inclination. Mist collected by the rectangular dust collecting electrodes 1 and washing liquid fall on the surface of the rectangular dust collecting electrodes 1. And after they fall toward the corners of the lower end along the notches at the lower end part, they fall from the corners, turned into droplets. Therefore, since the distance between the falling droplets and the discharge electrodes 2 is made longer, compared to the case the lower part is not notched, a spark is not easily generated, the lowering of charge voltage can be restrained. Thus, higher voltage of the discharge electrodes on washing is used to improve the dust collecting performance.
    • 18. 发明专利
    • HIGH-PERFORMANCE FLUE GAS DESULFURIZING METHOD
    • JPH06226041A
    • 1994-08-16
    • JP1637993
    • 1993-02-03
    • MITSUBISHI HEAVY IND LTD
    • HINO MASAOTATANI ATSUSHIUGAWA NAOHIKOKATAYAMA HIROYUKIIWASHITA KOICHIRO
    • B01D53/50B01D53/34B01D53/77B03C3/01B03C3/013B03C3/16
    • PURPOSE:To desulfurize the SOx in waste gases contg. the SOx down to a low-concn. level by installing a wet process electrostatic precipitator to the rear flow part in the outlet of the absorption column of a desulfurizer, spraying a slurry contg. solid calcium carbonate and executing two-stage desulfurization. CONSTITUTION:The waste gases 1 contg. the SOx is introduced to the SOx is introduced into the desulfurizer 2 and the slurry absorbing liquid 4 from a route 3 is sprayed from a route 8 into the desulfurizer 2. The absorbing liquid, then, comes into gas-liquid contact with the waste gases in an absorption section 9 packed with grid and desulfurizes the gases. The waste gases from which the greater part of the SOx is removed are thereafter introduced via a route 14 into the wet process electrostatic precipitator 15. The slurry absorbing liquid contg. solid CaCO3 is sprayed from a route 20 in this precipitator. The slurry absorbing liquid is then attracted to an electrostatic precipitation plate 16 and wet wall parts are formed, by which a precipitation effect and a desulfurization effect are generated. In addition, ion wind is generated on the precipitation plate 16 and the gaseous boundary film of SO2 is diminished. The desulfurization performance is thus improved by the synergistic effect. A part of the absorbing liquid withdrawn therefrom is returned to the desulfurizer 2.
    • 20. 发明专利
    • ELECTROSTATIC PRECIPITATOR
    • JPH03232554A
    • 1991-10-16
    • JP2794790
    • 1990-02-07
    • MITSUBISHI HEAVY IND LTD
    • NAGATA MASAYUKITOMIMATSU KAZUTAKAKATAYAMA HIROYUKIKOJIMA KATSUHISA
    • B03C3/08B03C3/41
    • PURPOSE:To make free from maintenance and improve performance by providing aperture part having projections within the plane of planar discharge electrodes provided to face dust collecting electrodes over the entire surface and generating local corona discharges from these projecting parts. CONSTITUTION:The discharge electrodes 3 provided to face the dust collecting electrodes 2 are formed as flat plates and the aperture part 8 having the projections 9 are provided within the plane of the discharge electrodes 3 over the entire surface. The local corona discharges are generated from the projecting parts 9. Namely, the local high current parts provided on the discharge electrodes eliminate the possibility of troubles, such as disconnections, and are maintenance-free. The local high-current parts are distributed uniformly in the electrostatic precipitator so that the improvement in the performance proportional to the capacity of the electrostatic precipitator is possible. Further, the operation of the electrostatic precipitator with at least one unit of a high- voltage power source per unit of the electrostatic precipitator is possible. The wider electrode spacing than with the high-current parts of the conventional two-stage type electrostatic precipitator can be taken and, therefore, the deterioration in the performance by electrode staining is lessened.