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    • 1. 发明专利
    • JPH05306884A
    • 1993-11-19
    • JP6186892
    • 1992-03-18
    • HITACHI LTDHITACHI TECHNO ENG
    • YAGIMURA NOBUYUKITSUSHIMA HIROSHISOMEYA KAZUO
    • F25J3/04
    • PURPOSE:To shorten the restarting time after a stop of a device by a method wherein a descending liquid discharging means is provided in the upper tower of a dual type fractionating tower while liquid reservoir is provided at the outside of a fractionating tower. CONSTITUTION:Upon stop of a device, a valve 8 is fully opened to reserve liquefied gas descending from the upper tower 1 of a fractionating tower into a liquid receiver 6, into a liquid reservoir 4 at the outside of the tower through a conduit 14. In this case, the liquid receiver 6 is provided with a chimney structure capable of separating liquid from gas and the descending liquid overflows the liquid receiver 6 under a condition that the valve 8 is fully opened whereby the liquid flows into a main condenser 3. Under this condition, liquefied oxygen is reserved in the main condenser 3 while the liquefied gas, descended through the upper tower 1 if the fractionating tower and containing impurities, is reserved in the liquid reservoir 4. Upon restarting the device, the liquid reservoir 4 is boosted by gas from a lower tower 2 or liquefied gas to return gas and/or liquefied gas in the liquid reservoir 4 into the upper tower 1. In this case, the supply under gaseous condition or liquidous condition is selected so that the distribution of concentration in the upper tower becomes optimum. Accordingly, the purity of the liquefied gas in the main condenser 3 can be maintained in a high purity at all times.
    • 3. 发明专利
    • PROCESS FOR REMOVING HYDROCARBON
    • JPS60209229A
    • 1985-10-21
    • JP6339184
    • 1984-04-02
    • HITACHI LTDHITACHI TECHNO ENG
    • WATANABE SHIGEOSOMEYA KAZUOYAMAZAKI MASAHIRO
    • B01D53/86C01B23/00
    • PURPOSE:To improve removing efficiency of hydrocarbons from feed gas by withdrawing a portion of the feed gas before a catalyst tank and determining the concn. of CO2 after burning the gas completely, determining also the concn. of CO2 at the downstream side of the catalyst tank, and controlling the flow rate of O2 to be added based on the difference between both CO2 concn. CONSTITUTION:A portion of feed gas supplied from a duct 11 is fed to a combustion device 3 together with sufficient amt. of O2 through a duct 15 where it is burnt completely and the concn. of generated CO2 is determined by a densitometer 7. Hydrocarbons in the feed gas fed to the catalyst tank 1 together with O2 is burnt in the catalyst tank 1 and the CO2 concn. of the gas is determined at the downstream side of the catalyst tank 1 with a densitometer 8. Both determined values A1 and A2 of the CO2 concn. and flow rate Q0 are inputted to an operating device 10 and a set value for optimum flow rate Qs for O2 is decided, which is outputted to a flow rate controller 6 to control a controlling valve 2 and the amt. of O2 to be added appropriately.