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    • 1. 发明专利
    • Production of gaseous co
    • 生产气体有限公司
    • JPS59116114A
    • 1984-07-04
    • JP22214782
    • 1982-12-20
    • Ishii Tekkosho:KkOsaka Gas Co Ltd
    • HAYASHI AKIOOOOKA ISAMI
    • C01B3/34C01B31/02C01B31/18C01B31/20C10K3/04F25J3/02F25J3/08
    • F25J3/0261F25J3/0223F25J3/0252F25J2205/04Y02C10/12
    • PURPOSE:To obtain CO by easy operation at a low cost of equipment while saving energy by bringing hydrocarbon such as naphtha, steam and CO2 into catalytic reactions by a cyclic system, compressing the resulting reformed gas, removing CO2, and carrying out low temperature cooling and rectification. CONSTITUTION:Catalyst in a reforming furnace 1 is heated to a temp. required to produce a reformed gas (a heating stage). Hydrocarbon starting material such as LPG, steam and gaseous CO2 are fed into the furnace 1, and a reformed gas is produced by catalytic cracking reactions (a production stage). At this time, the temp. of the catalyst falls, so the production of the gas is stopped before the temp. falls below the required endothermic reaction temp., and the catalyst is heated again to the required temp. The heating and production stages are alternately repeated by cyclic system operation while interposing a purge stage. The resulting reformed gas is cooled through a water sealed scrubber 2, stored once in a holder 3, compressed with a compressor 4, and introduced into a washing tower 5 to remove CO2. The remaining gas is fed to a low temperature processing equipment 12, and it is passed through one of the adsorbers 9, one of the vapor-liq. separators 10 and the rectifying tower 11. Gaseous CO is obtd. as a product.
    • 目的:通过以低成本的设备轻松操作,通过将石脑油,蒸汽和二氧化碳等烃类循环系统引入催化反应,节省能源,从而以低成本的方式获得CO,压缩生成的改性气体,除去CO2,进行低温冷却 并整改。 构成:将重整炉1中的催化剂加热至温度 需要生产重整气体(加热阶段)。 将烃原料如LPG,蒸汽和气态CO 2进料到炉1中,通过催化裂化反应(生产阶段)产生重整气体。 这时候, 的催化剂下降,所以气体的产生在温度下停止。 低于所需的吸热反应温度,并将催化剂再次加热至所需温度。 通过循环系统操作交替重复加热和生产阶段,同时插入清洗阶段。 将所得重整气体通过水密封的洗涤器2冷却,一次储存在保持器3中,用压缩机4压缩,并引入洗涤塔5中以除去CO 2。 剩余的气体被供给到低温处理设备12,并且通过其中一个吸附器9, 分离器10和精馏塔11.气体CO是可以得到的。 作为产品。
    • 4. 发明专利
    • OPEN CYCLE GAS TURBINE POWER GENERATING SYSTEM
    • JPS55125324A
    • 1980-09-27
    • JP3388979
    • 1979-03-22
    • OSAKA GAS CO LTD
    • OOOKA ISAMI
    • F02C3/14F01K23/10F02C6/18F02C7/18
    • PURPOSE:To obtain high efficiency and high output by introducing combustion gas from a burner for a gas turbine, cooling either stationary blades or moving blades with this combustion gas and burning again in a gas line within the gas turbine. CONSTITUTION:Liquefied natural gas cools the air passed a filter 16 by means of a suction type cooler 20, and a part is extracted out of the system, while the remainder is heated by a heater 22, and is introduced to a natural gas turbine 24 provided with a generator 23. And the gas whose pressure is dropped is introduced to a burner 1 and is burnt along with air being passed through a compressor 26. The combustion gas is introduced to a three stage axial flow type gas turbine 3 provided with a generator 2, and after performing work it is discharged to a chimney 4. Within the chimney 4, a part of natural gas is introduced and burnt and steam is generated by a boiler 5. The steam is passed through a superheater 7, high pressure turbine 8, reheater 9, low pressure turbine 10 and etc. and drives a generator 14.
    • 5. 发明专利
    • LIQUEFIED NATURAL GAS GASIFIER
    • JPS54136414A
    • 1979-10-23
    • JP3640278
    • 1978-03-28
    • OSAKA GAS CO LTD
    • OOOKA ISAMI
    • F02C7/141F17C9/02F28D15/00
    • PURPOSE:To increase operational and econimic efficiency, by using sea water as heat source and coolant as heat medium, and by changing the course of sea water in accordance with its temperature. CONSTITUTION:Intermediate heat medium type heat exchangers 1, 2 use propane as coolant and sea water as heat source. Heat exchanger 1 exchanges heat between sea water and coolant, heat exchanger 2 between coolant and LNG. LNG enters heat exchanger 2 from line 18, is gasified as it passes the heat transfer pipe, and leaves heat exchanger 2 via line 19. In heat exchanger 1, 2, propane is used as low solidifying-point collant. The coolant is heated by sea water, and by using its evaporation and condensation, LNG is heated and gasified. When the sea water temperture is comparatively high, the water is discharged from lines 8, 9 via lines 6,7. When the sea water temperature is extremely low, the water is discharged from line 6 via line 10, 8 and line 7, 12.
    • 6. 发明专利
    • LIQUEFIED CARBON DIOXIDE PRODUCING EQUIPMENT
    • JPS54115691A
    • 1979-09-08
    • JP1332278
    • 1978-02-07
    • OSAKA GAS CO LTD
    • OOOKA ISAMIHISAKADO YOSHINORI
    • C01B32/50F25J1/00F25J3/02F25J3/08
    • PURPOSE:To econimically produce liquefied CO2 in simple facilities with high thermal efficiency by compressing CO2-based raw gas to above a specific press, followed by drying, purification and heat exchange for LNG of a specific press. CONSTITUTION:Raw CO2 gas 1 is water-cooled 2 and introduced into raw gas compressor 4 through drain separator 3. In compressor 4, the gas is pressurized to above 7 kg/cm G in two steps through intermediate cooler 5 and drain separator 6. The gas is then passed through precooler 7, drain separator 8, dryer 9 and deodorizer 10, and introduced into reboiler 20, where it is cooled by heat exchange for liquefied CO2. The cooled gas is introduced into low temp. part 22 through a rectifying part 21 of the distilling column and cooled to below the saturation temp. to be liquefied. On the other hand, ING 23 of 30-70 kg/cm acting as refrigerant is fed to vapor-liquid separator 25 and deprived of its cold source in part 22. The gasified NG is heated with water in heat exchanger 30 through separator 25 to be turned to NG of ordinary temp. The liquefied CO2 is stored in liquefied CO2 tank 38.
    • 10. 发明专利
    • LIQUEFIED NATURAL GAS CARBURETER
    • JPS5655797A
    • 1981-05-16
    • JP13137079
    • 1979-10-11
    • OSAKA GAS CO LTD
    • OOOKA ISAMIHISAKADO YOSHINORI
    • F17C9/02F17C7/04
    • PURPOSE:To prevent condensate liquid from overcooling to improve heating-vaporizing efficiency of intermediate thermal medium by heating and vaporizing liquefied natural gas with the intermediate thermal medium and providing filler at a contact portion between condensate liquid drops of the gas and a vaporizer. CONSTITUTION:Filler 5 is disposed in the center of a drum at the boundary between a carbureter 3 for LNG and a vaporizer 4 for liquefied propane gas outside pipe. Thus, LNG is introduced into the carbureter 3 to be heated and vaporized by PG outside pipe, introduced from a line 13 to the outside of the pipe of a heater 11, heated by seawater in the pipe and taken out of a line 14 to the outside of system. On the other hand, the seawater introduced from an end chamber 16 heats and vaporizes LPG in the pipe with the vaporizer 4, and is taken out of a line 17 to the outside of system. LPG condensated outside the pipe of the carbureter 3 is attached to the filler 5 as it drops and contacts PG ascending to have temperature for approximately saturating pressure in the drum. Thus the condensated LPG is prevented from overcooling to improve heating efficiency of a intermediate thermal medium.