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    • 6. 发明专利
    • Piping thickness measuring apparatus
    • 管道厚度测量装置
    • JP2008002873A
    • 2008-01-10
    • JP2006171002
    • 2006-06-21
    • Fuji Electric Systems Co LtdTohoku Electric Power Co Inc富士電機システムズ株式会社東北電力株式会社
    • FUJITA HIROYUKIKOBAYASHI HIRONOBUFURUYA HIROTAKETAKAGI AKIRAMAEZONO SHINYAAZUMA YASUHIKO
    • G01B15/02
    • PROBLEM TO BE SOLVED: To provide a piping thickness measuring apparatus for achieving an accurate mount for passing a line for connecting a radiation source and a detection section through the center of the piping in various types of piping having different pipe diameters, and improving the usability and the measurement accuracy.
      SOLUTION: A radiation source attaching section 100 and a sensor attaching section 300 abut on the piping 10 through two rollers, and are fixed by a fastening belt 200 for fastening an outer circumference of the piping 10. The fastening belt 200 is formed with a fittable concave and convex face. If both ends correspond to each other, a length of a contact position with the piping is the same, a radiation reaches the detection section in a sensor through the center of the piping 10, and the piping thickness measuring apparatus 1 can accurately measure a thickness of the piping 10.
      COPYRIGHT: (C)2008,JPO&INPIT
    • 要解决的问题:提供一种管道厚度测量装置,用于实现准确的安装,以使通过用于连接辐射源和检测部分的管线通过管道的中心在具有不同管径的各种类型的管道中,以及 提高可用性和测量精度。 解决方案:辐射源安装部分100和传感器安装部分300通过两个辊邻接在管道10上,并通过紧固带200固定,用于紧固管道10的外周。紧固带200形成 具有可弯曲的凹凸面。 如果两端对应,则与配管的接触位置的长度相同,通过配管10的中心到达传感器的检测部,通过配管厚度测定装置1能够精确地测定厚度 的管道10.版权所有(C)2008,JPO&INPIT
    • 7. 发明专利
    • TREATMENT OF WASTE WATER CONTAINING SULFURIC ACID
    • JPH10137770A
    • 1998-05-26
    • JP30473796
    • 1996-11-15
    • TOHOKU ELECTRIC POWER COKURITA WATER IND LTD
    • FUJITA HIROYUKINIHEI MIKIOCHIKASAWA KIYOHITOTAKADOI TADASHISATO TAKESHI
    • C02F1/44C02F1/58
    • PROBLEM TO BE SOLVED: To prevent reduction in membrane flux due to clogging, breakage, etc., of membranes, to stabilize the treatment and to improve efficiency of the treatment by adding a calcium compound to waste water contg. sulfuric acid in two stages, i.e., in a first stage and a second stage respectively to adjust pH of the waste water to specified values in the first and second stages respectively, subjecting insoluble matter thus formed in the resulting water to membrane separation to obtain permeant water and discharging the permeant water to the outside of the treatment system as treated water. SOLUTION: In the system of this treatment, waste water contg. sulfuric acid is introduced into a first reaction vessel 1 fitted with a pH meter IA and thereafter, a calcium compound such as Ca(OH)2 , or the like is added to the waste water to adjust the pH to 4 to 6, or preferably, about 4.5 to 5.5. Then, this waste water is further introduced into a second reaction vessel 2 fitted with a pH meter 2A and similarly, a calcium compound is added to the waste water to adjust the pH to 6.5 to 8. The resulting water is treated with a circulation vessel 3 and a membrane module 5, to obtain membrane permeant water. The permeant water is transferred to a permeant water tank 6 for backwashing to discharge the permeant water from the tank 6 to the outside of the system as treated water. By performing the addition of a calcium compound to waste water contg. sulfuric acid and the adjustment of pH of the waste water in two stages, the dissolution amounts of scale-forming components can sufficiently be reduced and also, deposition of coarse particles can be prevented from occurring. Thus, trouble due to scale formation, membrane breakage, etc., can be prevented from being caused.
    • 8. 发明专利
    • METHOD FOR CLEANING MEMBRANE MODULE WITH CLEANING AGENT
    • JPH11319515A
    • 1999-11-24
    • JP13531498
    • 1998-05-18
    • TOHOKU ELECTRIC POWER COKURITA WATER IND LTD
    • SASAKI YUNIHEI MIKIOFUJITA HIROYUKISATO TAKESHI
    • B01D65/02B01D65/06
    • PROBLEM TO BE SOLVED: To significantly reduce the consumption of a cleaning agent, and dispense with a specical chemical-resistant member as a material for a heating installation, piping or the like by supplying a cleaning agent to and filling an untreated water and concentrated water chamber with the cleaning agent and supplying a heated water to a permeating water chamber, when cleaning a membrane module with a cleaning agent. SOLUTION: When treating an untreated water by membrane separation, the untreated water is guided to the primary side 1A of a membrane module 1 through piping, and the permeating water which permeates to the secondary side 1B is delivered through a water collecting valve V-5. When cleaning the membrane module with a cleaning agent, the water collecting valve V-5, V-3, V-4 are closed and the valves V-1, V-2 are opened. Then a cleaning liquid is supplied to the primary side 1A of the membrane module 1 from a cleaning liquid tank 2 with the help of a cleaning pump 3 to replace the liquid on the primary side 1A with the cleaning liquid. After that, the valves V-1, V-2 are closed and the valves V-3, V-4 are opened. Further, a heated process water in a heated process water circulation tank 5 is circulated to the secondary side 1B of the membrane module 1 using a circulation pump 6 and thereby the cleaning liquid on the primary side 1A is heated to increase the effect to clean the membrane.