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    • 1. 发明专利
    • HYDROGEN GENERATING DEVICE
    • JPH10212102A
    • 1998-08-11
    • JP1240297
    • 1997-01-27
    • OSAKA GAS ENG KK
    • FUNAMOTO KUNIHIROTAKEMOTO TETSUYA
    • C01B3/38
    • PROBLEM TO BE SOLVED: To suppress the deposition of carbon on the upstream side of a catalyst layer in a reformer, to consist essentially of butane gas in a hydrocarbon gas and to prevent the reliquefaction of butane gas even when outside temp. is low by providing a hydrogen adding means for adding gaseous hydrogen to hydrocarbon gas at the pre-stage from compression. SOLUTION: In an adjusting process of a gaseous starting material, gaseous hydrogen (H2 ) and butane gas (C4 H10 ) desulfurized in a time as short as possible are mixed in a volume ratio (gaseous hydrogen)/(butane gas) of a little over 4/5 and are supplied to a compressor 4. Gaseous hydrogen for producing the mixture is obtained by taking out a part of a gaseous hydrogen product from a gaseous hydrogen product taking out port 50 provided in the final process of a hydrogen generation device through a branched pipe 52 and a flow control valve 54, which are the gaseous hydrogen adding means. The branched pipe 52 is connected at the mid-way of a butane gas feed pipe 2 for supplying butane gas to the compressor 4.
    • 2. 发明专利
    • HEAT EXCHANGER
    • JPH10206042A
    • 1998-08-07
    • JP1100597
    • 1997-01-24
    • OSAKA GAS ENG KK
    • ONISHI OSAMUTAKEMOTO TETSUYA
    • F28D7/10C01B3/38
    • PROBLEM TO BE SOLVED: To enable keeping of the temperature of an object fluid discharged from a heat exchanger constant regardless of the flow rate of the object fluid by providing a heat transfer area altering means to allow altering of a contact area between a heat exchanger tube and a heat medium. SOLUTION: An object fluid passing through a heat exchanger tube 80b undergoes a heat exchange with water in a heat medium container 80a. Drain ports 80d, 80d' and 80d" and the heat exchanger tube 80b makes up a heat transfer area altering means in cooperation to allow altering of a contact area of the heat exchanger tube 80b with water. In other words, when the target production quantity of hydrogen is the maximum thereof and the flow rate of a mixture of H, and Co leaving a reformer 100 is high, it is necessary to set the heat exchange capacity of a heat exchanger 80 to the maximum. Hence, the drain port 80d of the maximum level alone is opened while the drain ports 80d' and 80d" of the medium and minimum levels respectively are closed. Thus, an overflow occurs only at the drain port 80d to maximize the amount of water within the heat medium container 80a thereby allowing the setting of the heat transfer area of the heat transfer tube 80b with the water to the maximum value.
    • 3. 发明专利
    • DEODORIZATION APPARATUS
    • JPH10118453A
    • 1998-05-12
    • JP27946796
    • 1996-10-22
    • OSAKA GAS ENG KKSUNRAY REINETSU CO
    • FUNAMOTO KUNIHIROTAKEMOTO TETSUYAKAWASE YOSHIAKI
    • B01D53/86
    • PROBLEM TO BE SOLVED: To provide deodorization apparatus with less unburned components in flue gas and without the need to increase the size of the apparatus by conducing perfect combustion in deodorization apparatus provided with a catalysis part for conducting deodorization treatment by contacting the catalysis part with target gas, an introduction passage for introducing the target gas into the catalysis part, and a burner for heating the target gas before the treatment. SOLUTION: A large diameter portion 11 expanding its cross sectional area toward the downstream side is provided at an introducing passage 10 and a combustion tube part 14 disposed at vicinity of the expanding diameter portion 11 in such a way as to cross the introducing passage 10 is connected to a burner 12. A U-shape is formed in composition of the combustion tube part 14, wherein the U-shape comprises an inlet of fuel gas 15, a first straight tube part 16 provided with a combustion pr 18, a second straight tube art 22 provided with ejection ports 24 in parallel for discharging the flue gas, and a curved tube part 20 connecting both straight parts so that the direction of combustion gas is changed from the one toward the first straight tube part 16 to the one toward the second straight tube part 22. The second straight tube part 22 is provided and disposed on the upper steam side of the first straight tube part 16.
    • 4. 发明专利
    • RADIANT TUBE
    • JPH102513A
    • 1998-01-06
    • JP15359696
    • 1996-06-14
    • OSAKA GAS ENG KK
    • WATANABE EIJI
    • F23D14/12F23C3/00
    • PROBLEM TO BE SOLVED: To allow heater of an electric furnace to be replaced by reduction in a separate distance between a combustion side tube and an exhaust side tube and a mounting opening while preventing a local heating by providing a gas retention part at an end side from a connector for connecting the exhaust side tube having a heat exchanger of the combustion side tube internally mounting a combustion burner with combustion air to a communicating part. SOLUTION: The radiant tube connects in communication a cylindrical combustion side tube 4a internally mounting a combustion burner 1 to an exhaust side tube 4c for allowing combustion exhaust gas from the burner 1 to flow and having a heat exchanger 2 with combustion air supplied to the burner 1 via a communicating part 4b of a rectangular section at one end sides of the tubes 4a and 4c in a parallel state. The other end side of the tubes 4a and 4c has a fixing part 3 fixed to a furnace wall. A columnar gas retention part 4d is provided at an end side from a connector of the tube 4a to the part 4b. Further, a second gas retention part 4e is provided near the connector of the tube 4c to the part 4b.
    • 7. 发明专利
    • GAS FLUIDIZED BED ROASTER
    • JPH08336377A
    • 1996-12-24
    • JP14725495
    • 1995-06-14
    • OSAKA GAS ENG KK
    • YAMAMOTO TATSUO
    • A47J27/04A23N12/08
    • PURPOSE: To provide a gas fluidized bed roaster capable of adopting a simple structure as the sealing structure of a roasting chamber and excellently carrying out a relatively high-temperature roasting, for example, roasting by using wheat as a target. CONSTITUTION: This gas fluidized bed roaster of a gas circulation type is equipped with a roasting chamber 2 capable of roasting a material 3 to be roasted in a fluidized state with roasting hot air and by a hot air supplying mechanism 4 for sending the roasting hot air to the roasting chamber 2 and returns a part of an exhaust gas discharged from the roasting chamber 2 through a return route 5 to the hot air supplying mechanism 4 and uses it as a part of the roasting hot air. The gas fluidized roaster is furnished with a position changing mechanism 30 capable of changing the roasting chamber 2 from a roasting position in which an exhaust gas outlet 8 of the roasting chamber 2 is connected to the return route 5 to an opening position in which the exhaust gas outlet 8 of the roasting chamber 2 is opened to a space of the outside and the material 3 to be roasted can be taken in and out from the exhaust gas outlet 8.
    • 9. 发明专利
    • METHOD FOR ROASTING GRANULAR MATERIAL TO BE TREATED AND APPARATUS THEREFOR
    • JPH067132A
    • 1994-01-18
    • JP16325292
    • 1992-06-23
    • OSAKA GAS ENG KK
    • ISAKA TAKAYUKI
    • A23L11/00A23N12/08A23L1/20
    • PURPOSE:To provide a method for roasting a granular material to be treated in which the amount of evaporated moisture per unit time can be increased, the efficiency of a roasting step is improved and the contribution can be made to improvement in quality of the product. CONSTITUTION:The objective method for roasting a granular material to be treated is to carry out a hot-air fluidized bed roasting step for housing the granular material 2 which is an object of roasting to be treated in a roasting chamber 3 equipped with a flow rectifying plate 15 in the bottom thereof, feeding hot air from the lower part of the flow rectifying plate 15 into the roasting chamber 3 and heat-treating the granular material 2 to be treated in a fluid state and a microwave roasting step for irradiating the granular material 2 to be treated in the fluid state with microwaves and heating the granular material 2 to be treated with the microwaves. In this case, the objective apparatus for roasting is equipped with the roasting chamber 3 provided with the flow rectifying plate 15 in the bottom thereof, a hot air feeder 13 for feeding the hot air from the lower part of the flow rectifying plate 15 into the roasting chamber 3 and heating the granular material 2 to be treated in the fluid state and a microwave heater 12 for irradiating the granular material 2 to be treated with microwaves and heating the granular material to be treated therewith.