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    • 22. 发明专利
    • MOVING MECHANISM OF MACHINERIES IN LIQUIDIZED GAS TANK
    • JPS63145897A
    • 1988-06-17
    • JP29098186
    • 1986-12-06
    • TOKYO GAS CO LTD
    • SUGAWARA YUZOKANEDA YUKIHIRO
    • F17C13/02F17C13/00
    • PURPOSE:To enable lateral movement of machineries in a liquidized gas tank, by heating and vaporizing liquidized gas being fed from a storage chamber of body for supporting machineries into a vaporization chamber then ejecting said gas from the outer circumference at the side of the vaporization chamber. CONSTITUTION:A liquidized gas storage chamber 2 is provided to a body 1 and a vaporization chamber 4 associated with a heating means 3 is arranged below said storage chamber 2 while furthermore a communicating section 5 for supplying liquidized gas is arranged between the storage chamber 2 and the vaporization chamber 4. Furthermore, a communicating section 6 for leading liquidized gas is provided in the storage chamber 2 and a communicating section 7 for ejecting vaporized gas is provided on the outer circumference at the side of the vaporization chamber 4. Valves 8-10 are arranged in said communicating sections 5-7 and a cable 11 for controlling said valves 8-10 and the heating means 3 is laid between the upper section of a liquidized gas tank 12.
    • 28. 发明专利
    • METHOD FOR RUNNING SEAWATER PUMP IN LNG VAPORIZER
    • JPH09183987A
    • 1997-07-15
    • JP34362995
    • 1995-12-28
    • TOKYO GAS CO LTD
    • ARAKAWA MASAHIROKANEDA YUKIHIROKIZU YOSHIKAZUSEKIGUCHI MASARU
    • C10L3/06F17C9/02
    • PROBLEM TO BE SOLVED: To reduce the amt. of water sprayed in an LNG vaporizer to thereby reduce the power cost of a seawater pump. SOLUTION: In the method for running a seawater pump 8 by calculating the amt. of seawater supplied by the pump 8 by using the higher value of the two amts. of water: the necessary amt. of sprayed water obtd. by comparing the temp. of seawater at the entry side of an LNG evaporator 1 to be monitored with the designed conditions of the evaporator 1 and the amt. of sprayed water at the film-breaking limit, as the set amt. of sprayed water, the temps. of sprayed water at tubes 4 near the lower header part 3 of the panel 5 of the evaporator 1 are measured along the right-and-left direction to calculate the difference between each of the above-obtd. temps. and the temp. of seawater at the entry sides of each of the tubes 4; then the apparent amt. of sprayed water is calculated about each tube from the above-obtd. temp. difference, the flow rate of the LNG, the enthalpies of the entry-side LNG and the exit-side gas, and the specific heat of water sprayed; and the amt. of seawater supplied by the pump 8 is increased when the apparent amt. of sprayed water becomes lower than the above set amt.