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    • 2. 发明专利
    • Ceramic membrane type synthetic gas reaction apparatus and its operation method
    • 陶瓷膜型合成气反应装置及其操作方法
    • JP2005255476A
    • 2005-09-22
    • JP2004070721
    • 2004-03-12
    • Toshiba Corp株式会社東芝
    • KAWASHIMA MASATOSHIHOASHI EIJIARAI KENJI
    • B01D53/22B01D71/02C01B3/38
    • PROBLEM TO BE SOLVED: To easily perform replacement or repair by confining deficient parts when deterioration or breakage occurs at an oxygen-permeable ceramic membrane tube in a synthetic gas production apparatus. SOLUTION: This ceramic membrane type synthetic gas reaction apparatus producing a synthetic gas comprises a plurality of oxygen-permeable ceramic membrane tubes 4, a plurality of reforming catalyst tubes 3 into which a produced gas produced by a partial oxidation reaction flows in, and a reaction vessel 1 housing the plurality of the ceramic membrane tubes and the reforming catalyst tubes. The reaction vessel is composed so that the upper lid can be opened; and the ceramic membrane tubes 4 and the reforming catalyst tubes 3 are arranged so that they are divided into a plurality of blocks 10 each of which includes at least a ceramic membrane tube 4 and a reforming catalyst tube 3. Each block 10 can be independently carried in or out without being interfered by other blocks 10 into or from the reaction vessel the lid of which is opened. COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:通过在合成气体制备装置中的透氧陶瓷膜管上发生劣化或破裂时限制缺陷部分来容易地进行更换或修理。 < P>解决方案:制造合成气体的陶瓷膜式合成气体反应装置包括多个透氧陶瓷膜管4,多个通过部分氧化反应产生的生成气体流入的重整催化剂管3, 以及容纳多个陶瓷膜管和重整催化剂管的反应容器1。 反应容器构成为可以打开上盖; 并且陶瓷膜管4和重整催化剂管3被布置成它们被分成多个块10,每个块至少包括陶瓷膜管4和重整催化剂管3.每个块10可以独立地承载 进入或离开而不受其他块10干扰其打开的反应容器的反应容器中。 版权所有(C)2005,JPO&NCIPI
    • 3. 发明专利
    • Synthetic gas producing apparatus and method for operating the same
    • 合成气生产装置及其操作方法
    • JP2005255475A
    • 2005-09-22
    • JP2004070720
    • 2004-03-12
    • Toshiba Corp株式会社東芝
    • HOASHI EIJIKAWASHIMA MASATOSHIARAI KENJISHIMUTA KOJI
    • C01B3/38
    • PROBLEM TO BE SOLVED: To provide a synthetic gas producing apparatus in which an oxygen permeation ceramic film tube is easily replaced or repaired by limiting a deficiency part even when the tube is deteriorated or damaged.
      SOLUTION: The synthetic gas producing apparatus has a plurality of module reaction furnaces 1. Each of the module reaction furnaces 1 has the oxygen permeation type ceramic film tube 21, a reforming catalyst part 20, one vessel 15 housing the oxygen permeation type ceramic film tubes 21 and the reforming catalyst parts 20 in common, a raw material air supply port 3 for supplying raw material air to the vessel 15, a raw material gas supply port 2 for supplying a raw material gas to the vessel 15, a synthetic gas discharge port 4 for discharging a synthetic gas produced in the vessel 15 and an oxygen deficient air outlet 5 for discharging oxygen deficient air produced in the vessel 15. The raw material gas supply ports 2, the raw material air supply ports 3, the synthetic gas discharge ports 4 and the oxygen deficient air outlets 5 in the plurality of module reaction furnaces 1 are respectively connected to each other in common parts.
      COPYRIGHT: (C)2005,JPO&NCIPI
    • 解决的问题:提供一种合成气体制造装置,其中即使当管劣化或损坏时,通过限制缺陷部分也容易地更换或修理氧透过陶瓷膜管。 合成气体制造装置具有多个模块反应炉1.模块反应炉1中的每一个都具有透氧型陶瓷膜管21,重整催化剂部分20,容纳氧气渗透型的容器15 陶瓷膜管21和重整催化剂部件20,用于向容器15供给原料空气的原料空气供给口3,向容器15供给原料气体的原料气体供给口2, 用于排出在容器15中产生的合成气体的排气口4和用于排出在容器15中产生的缺氧空气的缺氧空气出口5.原料气体供给口2,原料空气供给口3,合成气 多个模块反应炉1中的气体排出口4和缺氧空气出口5分别以相同的部分彼此连接。 版权所有(C)2005,JPO&NCIPI
    • 10. 发明专利
    • REACTOR CORE STRUCTURE
    • JPH05323079A
    • 1993-12-07
    • JP12874692
    • 1992-05-21
    • TOSHIBA CORP
    • KAWASHIMA MASATOSHI
    • G21C5/00G21C5/22
    • PURPOSE:To practically increase heat generated fuel length, reduce reactivity coefficient for loss-of-coolant, and increase reactor trip margin in any neutron spectrum changing between during operation and tripping of reactor by arranging the core separately in the direction along the coolant flow. CONSTITUTION:A core is constituted of an upper core 1 in high temperature steam side and a lower core 2 in low temperature steam side and these are separated in the steam flow direction putting a medium part in between. Around the upper core 1 and the lower core 2, axial blanket 4, diametral blanket 5 and diametral blanket medium part 6 are provided. Though the upper core 1 and the lower core 2 are connected for the neutron flow, the state of separation into small cores like the upper core 1 and the lower core 2 appears during the tripping as the steam density is low in this method, and therefore reactor trip margin during flooding can be increased.