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    • 81. 发明专利
    • WASTE PLASTIC TREATMENT SYSTEM
    • JPH06220458A
    • 1994-08-09
    • JP1324993
    • 1993-01-29
    • HITACHI LTD
    • SUGANO SHUICHIHONCHI AKIOYAMADA RYOKICHIKATO AKIRAYAMASHITA HISAOMIYADERA HIROSHI
    • C10G1/10
    • PURPOSE:To provide a waste plastic treatment system which is constituted of specific units for pyrolysis of waste plastic into an oil component and a gas component and enables a low-boiling hydrocarbon oil to be recovered with a high efficiency, by providing therefor a specific constitution. CONSTITUTION:The title system comprisies a pyrolysis oven 2 for pyrolysis of waste plastic, a catalytic reaction column 6 for increasing the low-boiling fraction content of a pyrolysis product formed in the oven 2 in the presence of a catalyst, and an oil separation unit for separating gas flowing from the column 6 into a gas component and an oil component. The first oil separation unit 3 is provided between the oven 2 and the column 6. The pyrolysis product is separated into a gas component and an oil component in the first unit 3 to introduce the gas component directly into the second oil separation unit 4 while evaporating the oil component again in a heating oven 5 and then introducing the evaporated oil component into the column 6 to increase the low-boiling fraction content. The gas flowing from the column 6 is introduced into the third oil separation unit 7.
    • 82. 发明专利
    • GAS TURBINE COMBUSTION DEVICE
    • JPH0694239A
    • 1994-04-05
    • JP24300492
    • 1992-09-11
    • HITACHI LTD
    • TANIGUCHI MASAYUKIITO KAZUYUKIMIYADERA HIROSHI
    • F23R3/40
    • PURPOSE:To provide a gas turbine combustion device having no extinguishing of blown flame, having a low discharged concentration of NOx and showing a poor deterioration in catalyst by a method wherein mixture gas of fuel and air passed through a combustion catalyst layer flows into a dispersion combustion burner. CONSTITUTION:Catalyst combustion fuel 4 is supplied into air 1 heated by a preheating burner 11 and mixed with it. Heating air mixed with the catalyst combustion fuel 4 flows into a combustion catalyst layer 10 so as to perform a catalyst combustion. Dispersion combustion fuel 3 is supplied into gas passed through the combustion catalyst layer 10 and then dispersion combustion is carried out by an after-burner (a dispersion combustion burner) 19. A premixing combustion burner 14 ignite with combustion gas of high temperature ignited by the dispersion combustion burner 19. With such an arrangement, NOx generated from a dispersion flame is lowered and a part of the fuel is catalyst ignited, so that the flame is not completely blown extinguished.