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    • 3. 发明专利
    • Gasifying method of gas hydrate and gasifying system thereof
    • 气体和气体系统的气化方法
    • JP2010018752A
    • 2010-01-28
    • JP2008182191
    • 2008-07-14
    • Japan Oil Gas & Metals National CorpMitsui Zosen Akishima Kenkyusho:Kk株式会社三井造船昭島研究所独立行政法人石油天然ガス・金属鉱物資源機構
    • KAWASAKI TATSUJISHIMADA KIYOSHITAKANO TSUKASAHISAMOTO TAKAYUKIOISHI TAKEO
    • C10L3/06B01J7/02
    • PROBLEM TO BE SOLVED: To provide a gasifying method of gas hydrate and a gasifying system thereof by which the quantity of return gas to a storage tank side, where a gas is stored under normal pressure, is reduced to eliminate needs of a compressor or the like for the return gas, a power stirring device of a liquid layer and a pulverizing apparatus for pellets of the gas hydrate, and reduce the incidental equipment and the power consumption, and also the gas is stably supplied to efficiently perform gasification. SOLUTION: The gas hydrate A is supplied to a housing chamber 21 of a rotary valve 20 from a normal pressure line gas hydrate supply pipe 10, the rotary valve is rotated to communicate the housing chamber 21 with a high pressure line gas hydrate supply pipe 31 and a high pressure line water circulation pipe 38, and the gas hydrate A in the housing chamber 21 is injected to the high pressure line gas hydrate supply pipe 31 with circulating water B and is supplied to a gasifying tank 32 with the circulating water Ba heated in a heat exchanger to be gasified and the produced gas C is discharged from the gas supply pipe 33 and the circulating water B is separated and discharged. COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供一种气体水合物的气化方法及其气化系统,通过该气化水合物的气化方式,在常压下储存气体的储罐侧的返回气体量减少,以消除 用于返回气体的压缩机等,液体层的动力搅拌装置和气体水合物的颗粒的粉碎装置,并且减少附带的设备和功率消耗,并且稳定地供给气体以有效地进行气化。 解决方案:气体水合物A从常压管线气体水合物供给管10供给到旋转阀20的容纳室21,使旋转阀旋转,将容纳室21与高压管线气体水合物 供给管31和高压管路水循环管38,并且容纳室21中的气体水合物A被循环水B注入到高压管线气体水合物供给管31中,并被供给到具有循环水的气化罐32 在热交换器中加热的水Ba被气化,产生的气体C从气体供给管33排出,循环水B分离排出。 版权所有(C)2010,JPO&INPIT
    • 4. 发明专利
    • Gas hydrate wash-column
    • 气体水化物清洗柱
    • JP2008274129A
    • 2008-11-13
    • JP2007119859
    • 2007-04-27
    • Mitsui Zosen Akishima Kenkyusho:Kk株式会社三井造船昭島研究所
    • TANAKA SUSUMUOMORI HIDEYUKITAKANO TSUKASAYAMAGUCHI HIROSHI
    • C10L3/00C07C7/152C07C9/02C10L3/06
    • PROBLEM TO BE SOLVED: To provide a gas hydrate wash-column that washes unreacted seawater accompanying hydrate with a required minimum of washing water and smoothly draining the seawater without obstructing washing. SOLUTION: The gas hydrate wash-column 4 comprises a hydrate slurry introduction part 22, a draining part 23 for dehydrating unreacted seawater in a hydrate slurry and a washing and scraping part 24 for diluting unreacted seawater attached to hydrate and scraping the hydrate after washing to the outside of the system. The washing and scraping part 24 is equipped with a rotary or wiper type gas hydrate scraping apparatus and a washing water spray nozzle. When the void percentage of a hydrate in a saturation area E is ε, the cross-sectional area of the wash-column is A, the rise rate of a hydrate sedimentary layer is U and the saturation degree of a hydrate in an unsaturation area F is S, the water amount Q of washing water sprayed from a washing water spray nozzle satisfies formula (1): Q=1.1ε×A×U×S. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种气体水合物洗涤塔,其以所需的最小洗涤水洗涤伴随水合物的未反应的海水​​,并平稳地排出海水而不阻碍洗涤。 气体水合物洗涤塔4包括水合物浆料引入部分22,用于使水合物浆料中的未反应的海水​​脱水的排出部分23和用于稀释附着到水合物上的未反应的海水​​并刮擦水合物的洗涤和刮除部分24 洗完后就到系统的外面。 洗涤和刮除部分24配备有旋转或刮水器式气体水合物刮擦装置和洗涤水喷雾喷嘴。 当饱和区域E中的水合物的空隙率为ε时,洗涤柱的横截面积为A,水合物沉积层的上升率为U,不饱和区域F中的水合物的饱和度为 是S,从洗涤水喷嘴喷射的洗涤水的水量Q满足式(1):Q =1.1ε×A×U×S。 版权所有(C)2009,JPO&INPIT
    • 5. 发明专利
    • Gas hydrate production system
    • 气体水合物生产系统
    • JP2008274130A
    • 2008-11-13
    • JP2007119873
    • 2007-04-27
    • Mitsui Zosen Akishima Kenkyusho:Kk株式会社三井造船昭島研究所
    • TANAKA SUSUMUOMORI HIDEYUKITAKANO TSUKASAYAMAGUCHI HIROSHI
    • C10L3/06
    • PROBLEM TO BE SOLVED: To provide a gas hydrate production system that is installed on an FPSO (Floating Production, Storage and Offloading System) moored on the ocean. SOLUTION: The gas hydrate production system comprises a first formation device 3 for introducing seawater b and a raw material gas (a) and forming a gas hydrate slurry d of mixture of gas hydrate e and the unreacted seawater b, a wash-column 4 for draining off the unreacted seawater b from the gas hydrate slurry d, diluting the seawater b attached to the drained gas hydrate slurry e and producing gas hydrate e' having a low water content and a low salt concentration and a melting tank 2 for regasifying the gas hydrate e' having the low water content and the low salt concentration introduced from the wash-column 4, decomposing the gas hydrate into the raw material gas (a) and water c, returning the raw material gas (a) produced by the decomposition to the first formation device 3 and supplying the water c produced by the decomposition as washing water to the wash-column 4. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供安装在海洋停泊的FPSO(浮式生产,储存和卸载系统)上的天然气水合物生产系统。 解决方案:气体水合物生产系统包括用于引入海水b的第一形成装置3和原料气体(a),并形成气体水合物e和未反应海水b的混合气体水合物浆料d, 柱4,用于从气体水合物浆料d中排出未反应的海水​​b,稀释附着在排出的气体水合物浆料e上的海水b并产生具有低含水率和低盐浓度的气体水合物e'和用于 使从洗涤塔4引入的低含水量和低盐浓度的天然气水合物e'再分解,将天然气水合物分解成原料气体(a)和水c,使原料气体(a) 分解成第一形成装置3并将由分解产生的水c作为洗涤水供给到洗涤塔4.版权所有(C)2009,JPO&INPIT