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    • 4. 发明专利
    • SUBCOOLING DEVICE OF HIGH-PRESSURE LOW-TEMPERATURE FLUID PUMP
    • JPH02283999A
    • 1990-11-21
    • JP10005389
    • 1989-04-21
    • HITACHI LTD
    • HOSOKAWA JUNICHIOKABE MICHIMASAISHIZU HISAZUMI
    • F17C5/02F17C7/00
    • PURPOSE:To reduce filling loss, prevent gasification in a pump, and continue the stable operation of the pump by forming pump suction piping in a double pipe connecting blow piping from a pump to one end of outer piping, opening the other end of it to the atmosphere, and carrying out the supercooling work of pump suction fluid with pump blowing fluid. CONSTITUTION:After low temperature fluid stored in a low temperature fluid tank 1 is pressurized by a low temperature fluid pimp 2, it is heated to a normal temperature by an evaporator 4 to fill a bomb at a filling stand 5. Since the fluid is gasified in the cylinder of the low temperature fluid pump 2, a part of it is blown under a gas/liquid mixing condition to prevent any defective gas accumulation. The blowing fluid is fed to the outer piping of a double pipe 3 provided at a pump suction part, and by thermally expanding it under the atmosphere, it is kept in a subcooled condition of 5 to 10 deg.C and is heat- exchanged with pump suction fluid to cool the outer piping. It is thus possible to reduce the loss at the time of filling and continue the stable operation of a pump, because the pump suction fluid is supercooled by the pump blowing fluid.
    • 5. 发明专利
    • REMOVAL OF CARBON MONOXIDE IN NITROGEN PRODUCING DEVICE
    • JPH01247980A
    • 1989-10-03
    • JP7434888
    • 1988-03-30
    • HITACHI LTD
    • ISHIZU HISAZUMIOKABE MICHIMASA
    • F25J3/04F25J3/08
    • PURPOSE:To produce high-purity nitrogen, by a method wherein a sub- fractionating tower, accommodating a reboiler, is installed to effect heat exchange between circulating liquid of liquid nitrogen in the intermediate part of a fractionating tower and material air in the reboiler and effect the fractionating separation of nitrogen from carbon monoxide. CONSTITUTION:The pressure of material air is risen by a material air compressor 1 and the material air is guided to an adsorption tower 2 where moisture and carbon dioxide are removed by adsorption. The material air, discharged out of the adsorption tower 2, is cooled by a heat exchanger 3 and enters into a fractionating tower 4 in a condition that one part of it is liquefied. Liquid nitrogen is sent into the top of a sub-fractionating tower 7 to make it the circulating liquid of the sub-fractionating tower 7. The liquid nitrogen is supplied to a reboiler 8, installed at the bottom of the sub-fractionating tower 7 to effect heat exchange in the reboiler 8 and evaporate the liquid nitrogen in the bottom of the tower 7 whereby ascending gas is generated. Nitrogen gas, not containing carbon monoxide in the top of the sub-fractionating tower 7, is sent into the fractionating tower 4 through a conduit 12, then, product nitrogen gas, not containing carbon monoxide, is collected through the conduit 9.