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    • 3. 发明专利
    • Production of gaseous carbon dioxide using waste gas containing gaseous carbon dioxide
    • 使用含气体二氧化碳的废气生产气体二氧化碳
    • JPS59164612A
    • 1984-09-17
    • JP4025783
    • 1983-03-11
    • Tokyo Gas Co LtdTokyo Reinetsu Sangyo Kk
    • SUZUKI KAZUNARIHIRANO TADASHI
    • B01D53/62B01D53/34C01B32/50F25J1/02F25J3/02
    • F25J3/0266F25J2205/40F25J2205/50F25J2210/62F25J2210/70F25J2270/904Y02C10/04Y02C10/12
    • PURPOSE: To separate and recover high purity CO
      2 from waste gas contg. CO
      2 by absorbing and capturing the CO
      2 in an absorbing liq. cooled to an extremely low temp. with liquefied natural gas.
      CONSTITUTION: Waste gas 19 contg. CO
      2 such as combustion gas is cooled with sea water 21 in a precooler 20, passed through a dehydration tower 22 and a deodorization tower 6, introduced into a heat exchanger 1, and cooled to about -80°C. The cooled gas is fed to an absorption tower 2 provided with a cooler 3 contg. "Freon" cooled to -120°C with LNG13, and the gas is brought into contact with a spray of ethanol cooled to -80°C. Most of the CO
      2 in the waste gas is captured by absorption and separated from the waste gas. The ethanol contg. absorbed CO
      2 is fed to a stripper 5, and the CO
      2 is released by heating the ethanol with the heat of waste gas passing through the stripper 5. The released CO
      2 is liquefied with a liquefier 7 and stored in a tank 8 as liquefied CO
      2 .
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:从废气中分离和回收高纯度二氧化碳。 通过吸收和捕获二氧化碳在吸收液体中的二氧化碳。 冷却至极低温 与液化天然气。 构成:废气19 CO 2如燃烧气体用预冷器20中的海水21冷却,通过引入热交换器1的脱水塔22和除臭塔6,并冷却至约-80℃。 冷却的气体被供给到设置有冷却器3的吸收塔2。 “氟利昂”用LNG13冷却至-120℃,气体与冷却至-80℃的乙醇喷雾接触。 废气中的大部分二氧化碳被吸收并与废气分离。 乙醇 吸收的CO 2被供给到汽提器5中,并且通过用通过汽提器5的废气的热量加热乙醇来释放CO 2。释放的CO 2用液化器7液化并以液化CO 2的形式储存在罐8中。
    • 5. 发明专利
    • Leakage inspection gas mixer of buried pipeline, and leakage inspection method of buried pipeline
    • 管道泄漏检测气体混合器和管道泄漏检测方法
    • JP2013075277A
    • 2013-04-25
    • JP2011217925
    • 2011-09-30
    • Tokyo Gas Co Ltd東京瓦斯株式会社Tokyo Gas Chemical Hanbai Kk東京ガスケミカル販売株式会社
    • ISHIKAWA MOTOMICHISATAKE YUKINOBUHIGASHI MASAAKIHIRANO TADASHI
    • B01F15/04B01F3/02B01F5/00G01M3/22G01M3/28
    • PROBLEM TO BE SOLVED: To be able to immediately mix inspection gas that has a desired component proportion in situ doing a leakage inspection of buried pipeline.SOLUTION: An apparatus that mixes inspection gas injected to a buried pipeline to perform leakage inspection of the buried pipeline includes: a first channel 10 having an inlet end 10A connected to the source of a first constituent gas; a second channel 20 having an inlet end 20A connected to the source of a second constituent gas; and a mixing channel 30 that communicates with the first channel 10 and the second channel 20, in which mixed gas of the first constituent gas and the second constituent gas circulates, and that has an exit end 30A connected to the inlet of the buried pipeline, wherein the first channel 10 is provided with a first pressure reducing valve 11 that sets the component proportion of the first constituent gas, the second channel is provided with a second pressure reducing valve 21 that sets the component proportion of the second constituent gas, and in the first pressure reducing valve 11 and the second pressure reducing valve 21, the first pressure control chambers 11a, 21a thereof communicate each other.
    • 要解决的问题:为了能够立即将具有所需组分比例的检查气体与原位进行埋地管道的泄漏检查混合。 解决方案:一种将注入埋地管道的检查气体进行混合以对埋管进行泄漏检查的装置,包括:第一通道10,其具有连接到第一构成气体源的入口端10A; 第二通道20具有连接到第二构成气体的源的入口端20A; 以及与第一构成气体和第二构成气体的混合气体循环的第一流路10和第二流路20连通的混合流路30,具有与埋入管路的入口连接的出口端30A, 其中,第一通道10设置有设定第一构成气体的成分比例的第一减压阀11,第二通道设置有设定第二构成气体的成分比例的第二减压阀21, 第一减压阀11和第二减压阀21,第一压力控制室11a,21a彼此连通。 版权所有(C)2013,JPO&INPIT