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    • 3. 发明专利
    • FLUID BED TYPE COOLER
    • JPS6441014A
    • 1989-02-13
    • JP19636887
    • 1987-08-07
    • UBE INDUSTRIES
    • NISHIDA MASAHIRO
    • G05D23/00B65G53/18B65G53/40B65G65/40
    • PURPOSE:To reduce the cost of equipment of a fluid bed type cooling device by forming a circular opening at the circumference part of a table for accumulation of dropping powder granules and blowing the cool air to the accumulated powder granules via said circular opening. CONSTITUTION:A table 43 for accumulation of dropping powder granules 35A is formed concentrically with a down-opening 28 of a supply pipe 26 and supported horizontally under the opening 28 formed opposite to the center part of a cylindrical main body. A circular opening is formed at the outer circumference part of the table 43 and a cooling air device for dropping granules 35A blows out the cooling air to the granules 35A via said circular opening. Thus it is possible to perform the flow rate control to set the cooling temperature at a prescribed level to the high temperature granules 35A by controlling the volume of the cooling air blown out to the granules 35A accumulated on the table 43. Furthermore the flow rate of the granules 35A is always kept at a fixed level since the air is blown out to the granules 35A evenly over the entire circumference of the table 43. Thus the flow rate control of the granules 35A is carried out accurately and the structure of a cooling device is simplified for reduction of the cost of equipment. In addition, the cooling effect is improves since the granules 35A are cooled when those granules 35A are blown out by the cooling air.
    • 5. 发明专利
    • FLUDIZED BED BOILER
    • JPS63294412A
    • 1988-12-01
    • JP12921387
    • 1987-05-26
    • UBE INDUSTRIES
    • MAEDA SADAHIKONISHIDA MASAHIRO
    • F23C10/00F22B1/02F23C10/18
    • PURPOSE:To ehable a sharp decrease of the cost of dust collector equipment and operation cost thereof by providing a conduit type member in the lower edge of a baffle plate suspending from the upper lid part and connecting the end of the conduit type member with a feed pipe for dropping particles which is extendingly provided downward along the inner surface of the wall within the dust collector. CONSTITUTION:The baffle plate 32 of dust collector 32 is suspended slantly toward downstream from upper lid part 28D between feed inlet 28B and flowing outlet 28C, and take out port 28E for particles is provided downward. This baffle plate 32 is a recessed pentagonal type in the front view and its bottom part 32a penetrates thereinto in a chevron form. Moreover, a conduit type member 28F is established along the bottom part 32a. Both ends of the conduit type member 28F are extended to left and right sides of baffle plate 32, and are joined with the feed pipe 28G for dropping particles in its left and right sides. The feed pipe 28G is extended downward along the side wall of a casing 28A causing its lower end to reach the vicinity of the take out port 28E.
    • 6. 发明专利
    • FLOW RATE CONTROLLER FOR POWDER GRANULE
    • JPS6441013A
    • 1989-02-13
    • JP19636987
    • 1987-08-07
    • UBE INDUSTRIES
    • NISHIDA MASAHIRO
    • G05D7/00B65G53/66
    • PURPOSE:To reduce the cost of equipment of a flow rate controller for powder granule by adding an accumulating table for dropping powder granules having a circular opening at its outer circumference at a position under a power granule supply member and forming an air blow-out port at a place under the center part of said table. CONSTITUTION:An accumulating table 43 for dropping powder granules having a circular opening at its outer circumference is set concentrically with a down- opening 28 of a powder granule supply member like a supply pipe 26, etc. The table 43 is supported under the pipe 26. A ventilating device for dropping powder granules has an air blow-out port set opposite to a point under the center part of the table 43. Thus it is possible to control the flow rate of the powder granules 35A by controlling the volume of the air blown out to the powder granules accumulated on the table 43. At the same time, the flow rate of the granules 35A is always kept at a fixed level since the granules 35A are blown out evenly over the entire circumference of the table 43. As a result, the accurate flow rate control is possible for the powder granules with simple constitution. Thus the cost of equipment is reduced for a flow rate controller for powder granules.