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    • 3. 发明专利
    • TURBINE EXPANDER
    • JPH05149635A
    • 1993-06-15
    • JP31666691
    • 1991-11-29
    • JAPAN ATOMIC ENERGY RES INSTKOBE STEEL LTD
    • KAMIYANAI YOUICHIKATO TAKASHIKAWASHIMA IWAO
    • F25B9/06
    • PURPOSE:To perform the safe and stable start or stop during operation of a freezer by a method wherein a fluid feed line through which a fluid inlet and a fluid outlet are intercommunicated, a bypass line, and a flow passage switching mechanism to switch inflow of fluid to each line are provided in a casing. CONSTITUTION:In a turbine expansion machine useful to a helium freezer to cool a superconduction magnet, a fluid feed line 13 through which a fluid inlet 11 and a fluid outlet 12 for a refrigerant, such as very low temperature helium, are intercommunicated and a bypass line 14 are provided in a casing 15. A valve body drive disc 19 to the upper and lower parts of which a valve body 17 for opening and closing the fluid feed line 13 and a valve body 18 for opening and closing the bypass line 14 are arranged is vertically movably disposed to a branch part 16 where the fluid inlet 11 is branched to the fluid feed line 13 and the bypass line 14. In the case of a turbine being operated, the valve body drive disc 19 is lowered through a drive shaft 20 to open the fluid feed line 13, the line 13 is communicated to the fluid inlet 11, and the bypass line 14 is closed with the valve body 18.
    • 6. 发明专利
    • JPH05296589A
    • 1993-11-09
    • JP9674592
    • 1992-04-16
    • KOBE STEEL LTD
    • KAMIYANAI YOUICHI
    • F25B9/06
    • PURPOSE:To perform a precooling operation based on a turbine expansion mechanism in a short time as much as possible, while preventing overload operation of a turbine type expansion mechanism on both high temperature side and a low temperature side. CONSTITUTION:Based on an inlet pressure P2 of a low temperature turbine and inlet temperatures T1 and T2 of each turbine, opening control of a turbine inlet valve 15 on a high temperature turbine inlet side is carried out. A low temperature turbine inlet temperature setting means 31 sets a limit value P2 set for the low temperature turbine inlet pressure P2 based on the high temperature turbine inlet temperature T1. A first valve opening arithmetic operation means 32a computes a first valve opening Va based on the pressure limit valve P2 set while a second valve opening arithmetic operation means 32b computes a second valve opening Vb based on a temperature ratio T1/T2. A turbine inlet valve opening control means 33 controls the opening of the turbine inlet valve 15 based on a lower side valve opening Va (or Vb).
    • 9. 发明专利
    • PRESSURE SWING ADSORPTION PROCESS
    • JPH01203018A
    • 1989-08-15
    • JP2996788
    • 1988-02-09
    • KOBE STEEL LTDKANSAI COKE & CHEMICALS
    • YAMAGATA MASAHIROAOKATA TAKUKASUYA FUMIHIKOKAMIYANAI YOUICHIYOKOE JINTAROTSUJI TOSHIAKI
    • B01D53/04C01B32/40
    • PURPOSE:To enhance CO purity by treating gas containing CO in the processes of temperature rise, adsorption, pressure reduction, washing and desorption respectively, dividing the desorption process into a preliminary desorption process and a longer main desorption process to recover CO and overlapping the main desorption process in two adsorption columns. CONSTITUTION:Raw material gas containing CO is pressurized by a compressor 10 and fed to an adsorption column A for carrying out the temperature rise process, and then CO is adsorbed by an adsorbent to which a Cu component is annexed and non-adsorbent components such as N2 and the like are discharged from a tube 2 into the outer air. The adsorption column A is connected with an adsorption column B, reduced in pressure and washed with CO gas from a product gas storage tank 6. After that, the pressure of the same is reduced by a small vacuum pump 70 down to atmospheric pressure or lower, followed by preliminary desorption, and its pressure is further reduced by a vacuum pump 50 for a time longer than the preliminary desorption. Then, water desorption process is carried out and the desorption gas is recovered as product gas. The main desorption process is partially overlapped in the beginning process in a adsorption column D and in the final stage in an adsorption column C.