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    • 2. 发明专利
    • Self-driving type pump for liquefied gas
    • 用于液化气的自驱动型泵
    • JP2006283736A
    • 2006-10-19
    • JP2005108576
    • 2005-04-05
    • Tokyo Gas Co Ltd東京瓦斯株式会社
    • MIYATA YOSHIAKIITO SHINICHI
    • F04B9/125F02M21/02F02M37/06F02M59/02F04B9/133F04B15/08F04B39/10
    • Y02T10/32
    • PROBLEM TO BE SOLVED: To provide a self-driving type reciprocating pump for liquefied gas requiring only small driving electric power. SOLUTION: A pump cylinder 130 for sucking the liquefied natural gas (LNG) and a drive cylinder 150 for driving a pump piston 13 of the pump cylinder 130 assume an integral construction in which they adjoin each other via a common piston rod 17. High pressure gas compressed and evaporated in the pump cylinder 130 is made alternatively flow into a left chamber 158 and a right chamber 156 of the drive cylinder so that the drive piston 15 of the drive cylinder 150 and the pump piston 13 of the pump cylinder 130 are driven to repeat suction and compression of the LNG. Changeover of the high pressure gas supplied to the two chambers of the drive cylinder 150 is performed by a selector valve which can be driven with small electric power. COPYRIGHT: (C)2007,JPO&INPIT
    • 要解决的问题:为了提供仅需要小的驱动电力的液化气的自驱动式往复泵。 解决方案:用于吸入液化天然气(LNG)的泵缸130和用于驱动泵缸130的泵活塞13的驱动缸150呈一体式结构,在该结构中,它们通过公共活塞杆17彼此相邻 在泵缸130中被压缩和蒸发的高压气体交替地流入驱动缸的左室158和右室156,使得驱动缸150的驱动活塞15和泵缸的泵活塞13 130被驱动以重复抽吸和压缩LNG。 供给到驱动气缸150的两个室的高压气体的切换由能够以小电力驱动的切换阀进行。 版权所有(C)2007,JPO&INPIT
    • 3. 发明专利
    • Fuel supply system
    • 燃油供应系统
    • JP2005351133A
    • 2005-12-22
    • JP2004171339
    • 2004-06-09
    • Osaka Gas Co LtdTokyo Gas Co Ltd大阪瓦斯株式会社東京瓦斯株式会社
    • MIYATA YOSHIAKIYAMADA TAMAKISATO TOSHIHARUITO SHINICHIOHASHI TAKAHIKO
    • F17C9/02F02M21/02F17C13/00
    • Y02T10/32
    • PROBLEM TO BE SOLVED: To provide a fuel supply system capable of keeping the pressure in a system within a fixed range over the whole stages from the driving to the stopping of the engine of an LNG automobile, capable of restraining the discharge of BOG to the outside, and capable of preventing the concentration of LNG.
      SOLUTION: This fuel supply system 1 is composed of a first pipe system 100 composed of an LNG storage vessel 2 and a first pipe 31 for sending vaporized LNG L2 to the engine E by vaporizing LNG L1 discharged from the LNG storage vessel 2, a second pipe system 200 composed of a gas storage vessel 5 for storing the BOG B and a second pipe 61 for connecting the gas storage vessel 5 to the LNG storage vessel 2, and a third pipe 7 for connecting the gas storage vessel 5 to the first pipe 31. The second pipe 61 is composed of a BOG sending pipe 63 for sending the BOG B to the gas storage vessel 5 from the LNG storage vessel 2, and a gas sending pipe 62 for sending the BOG B and the vaporized LNG L2 to the LNG storage vessel 2 from the gas storage vessel 5.
      COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供一种燃料供应系统,其能够将系统中的压力保持在从汽车的发动机的行驶到停止的整个阶段的固定范围内,能够限制排放 BOG到外面,能够防止LNG的集中。 解决方案:该燃料供给系统1包括由LNG储存容器2构成的第一管道系统100和通过蒸发从LNG储存容器2排出的LNG L1将蒸发的LNG L2发送到发动机E的第一管道31 ,由用于存储BOG B的气体存储容器5和用于将气体存储容器5连接到LNG储存容器2的第二管61构成的第二管道系统200和用于将气体存储容器5连接到 第一管道31.第二管道61由用于从LNG储存容器2将BOG B送入气体存储容器5的BOG送出管63和用于将BOG B和蒸发的LNG L2从气体存储容器5到LNG储存容器2。版权所有(C)2006,JPO&NCIPI
    • 5. 发明专利
    • LIQUID.LIQUID CONTACT TYPE LNG VAPORIZATION APPARATUS
    • JP2002309276A
    • 2002-10-23
    • JP2001113400
    • 2001-04-12
    • TOKYO GAS CO LTD
    • TSUI NOBUHIKOSEKIGUCHI MASARUITO SHINICHI
    • F28C3/04C10L3/06C10L3/12
    • PROBLEM TO BE SOLVED: To provide an apparatus for producing city gas 13A by conducting one-step operation of vaporization and controlling of a heat of combustion with the use of a liquid.liquid contact type vaporization system which solves the problem relating to the natural circulation of a high temperature liquid in setting up a vaporization process by bringing a low-boiling point liquid such as liquefied natural gas(LNG) into contact with a high-temperature liquid such as liquefied petroleum gas(LPG) in a liquid.liquid contact manner to effect heat exchange. SOLUTION: In a vaporization zone 1, LNG is continuously brought into contact with LPG in the liquid.liquid contacting manner to obtain natural gas (NG), and simultaneously the LPG rising with NG bubbles in the vaporization zone is flew out of the top of the vaporization zone, and the effluent LPG is deaerated in a deaeration zone 17 and heated with water of a normal temperature or hot water in a heating zone 3, and subsequently subjected to natural circulation to the bottom of the vaporization zone, and simultaneously fresh LPG is replenished to the vaporization zone in an amount corresponding to the amount of the LPG which leaves in the state included in liquefied gas (CG) by vaporization from the vaporization zone.