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    • 23. 发明专利
    • AIR LIQUEFYING AND SEPARATING DEVICE
    • JPH06147750A
    • 1994-05-27
    • JP29517892
    • 1992-11-04
    • KOBE STEEL LTD
    • MIYAGAWA YUTAKATANAKA YASUO
    • F25J3/04
    • PURPOSE:To make the liquefying and separation of air efficient by separating the mixture of gas and liquid by a gas and liquid separator into vapor rich in nitrogen and condensed liquid rich in oxygen. CONSTITUTION:Vapor, fractionated in a lower pressure tower 1 and supplied to a lower evaporator 31a as a heat source for evaporation after being introduced out of the top of a lower pressure tower 1, becomes the mixture of gas and liquid after being condensed as the result of heat exchange, then, is supplied to a gas and liquid separator 4. The mixture of gas and liquid is separated in the gas and liquid separator 4 into vapor, rich in nitrogen, and condensed liquid, rich in oxygen. The vapor, rich in nitrogen, is supplied to an upper pressure tower 2 whereby the inside of the upper pressure tower 2 becomes a condition rich in nitrogen and nitrogen is taken out from the top of the upper pressure tower 2 as vapor while liquefied air, rich in nitrogen, is taken out of the bottom and is supplied to the upper tower 32 of a low pressure tower 3. According to this method, fractionating operation becomes favourable and efficient liquefying and separating treatment of air can be effected.
    • 24. 发明专利
    • DISTILLATION UNIT
    • JPS62273004A
    • 1987-11-27
    • JP11596986
    • 1986-05-20
    • KOBE STEEL LTD
    • TANAKA YASUO
    • B01D3/20
    • PURPOSE:To reduce connecting sections with outside units and simplify the construction by providing a heat exchanging section functioning as an intermediate condenser in a distillation column. CONSTITUTION:A plurality of column plates 1 are provided in up and down directions, with separating plates 8 disposed between the upper column plates 1 and the lower column plates 1, and heat transfer preventing components 7 are provided close to both faces of the upper column plates 1. A plurality of risers 9 are installed to connect the column plates 1 with separating plates 8, and spaces constructed by the heat transfer preventing components 7 in which said risers 9 are through an separating plates 8 form a process fluid passing chamber 11. When a main distillation column is in operation, process fluid is charged in from one side of the fluid passing chamber 11 and discharged out of the other side, and the steam rising from the lower column plates 1 to the upper column plates 1 through risers 9 exchanges heat with the fluid to be partly liquefied.