会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明专利
    • Switching type chemical loop combustor
    • 切换式化学循环机
    • JP2013053803A
    • 2013-03-21
    • JP2011191921
    • 2011-09-02
    • Tokyo Gas Co Ltd東京瓦斯株式会社Ikutoku Gakuen学校法人幾徳学園
    • FUJIMINE TOMOYANAKAJIMA YOSHIFUMITAKEMURA KAZUYAHAYAKAWA ATSUHIKOOBA TAKEYASUISHIDA MASARU
    • F24V30/00
    • PROBLEM TO BE SOLVED: To provide a switching type chemical loop combustor A of a new configuration in which only one reaction tower 1 is used, the reaction tower is allowed to have both of a function as an oxidation tower and a function as a reduction tower, and thus the entire configuration is simplified and durability is also improved.SOLUTION: The switching chemical loop combustor A includes one reaction tower 1, gas supply means (air supply system 50, a fuel supply system 60) for supplying an oxidant or a reductant into the reaction tower 1 by alternately switching them, a purge gas supply system 70, and exhaust gas exhausting means (Nexhaust system 80, a COexhaust system 90) for exhausting exhaust gas in the reaction tower 1. The Nexhaust system 80 and the COexhaust system 90 are each provided with a purge gas exhaust pipe 100. The reaction tower 1 has an inner tube 5. A control means switches a shut-off valve provided respectively, so that air and fuel gas are alternately supplied to the inner tube 5 and the purge gas is supplied into the reaction tower 1. According to this, a shut-off valve 101 is also switched which is included in the purge gas exhaust pipe 100.
    • 要解决的问题:为了提供一种仅使用一个反应塔1的新结构的开关型化学循环燃烧器A,使反应塔具有氧化塔的功能和作为氧化塔的功能, 还原塔,因此整体结构简化,耐久性也得到改善。 解决方案:开关化学回路燃烧器A包括一个反应塔1,用于通过交替切换它们将氧化剂或还原剂供应到反应塔1中的气体供应装置(空气供应系统50,燃料供应系统60) 净化气体供给系统70和废气排出装置(N 2 排气系统80,CO 2 排气系统90) 排气系统80和CO 2 排气系统90分别配备有排气系统 吹扫气体排出管100.反应塔1具有内管5.控制装置切换分别设置的截止阀,使得空气和燃料气体交替地供给到内管5,并且将净化气体供应到 反应塔1.据此,切换阀101也被包括在吹扫气体排出管100中。切换:(C)2013,JPO和INPIT
    • 2. 发明专利
    • Chemical loop combustion equipment equipped with means for supplying inert gas as separate gas
    • 化学循环燃烧设备配备独立气体供应气体
    • JP2012172893A
    • 2012-09-10
    • JP2011034898
    • 2011-02-21
    • Tokyo Gas Co LtdIkutoku Gakuen学校法人幾徳学園東京瓦斯株式会社
    • FUJIMINE TOMOYANAKAJIMA YOSHIFUMITAKEMURA KAZUYAHAYAKAWA ATSUHIKOOBA TAKEYASUISHIDA MASARU
    • F24V30/00
    • PROBLEM TO BE SOLVED: To provide chemical loop combustion equipment which can evade decrease in solid-gas segregation efficiency and a direct contact between an oxidizing agent and a reducing agent without increasing an operation cost even if an amount of circulation of metal particles (oxygen carriers) increases by using effectively separate gas self-supplied inside the equipment preferably.SOLUTION: The chemical loop combustion equipment A1 includes a means for supplying inert gas as separate gas in order to prevent gas with the oxidizing agent and gas with the reducing agent, which are supplied into the equipment, from be mixed inside the equipment. Preferably, Ngas included in exhaust gas from an oxidation tower 1 and COgas included in exhaust gas from a reduction tower 3 are used as the separate gas. Further, the equipment also includes a means for adding vapor generated inside the equipment to the gas with the reducing agent which is supplied to the reduction tower 3.
    • 要解决的问题:提供化学循环燃烧设备,其可以避免固体气体分离效率的降低和氧化剂与还原剂之间的直接接触,而不增加操作成本,即使金属颗粒的循环量 (氧载体)通过在设备内部自供给的有效分离的气体优选地增加。 解决方案:化学循环燃烧设备A1包括用于将惰性气体作为单独气体供应的装置,以便防止与供给到设备中的氧化剂的气体和与还原剂的气体混合在设备内 。 优选地,来自氧化塔1的废气中包含的N 2 3用作单独的气体。 此外,该设备还包括一种将在设备内产生的蒸汽与还原塔3供应的还原剂一起加入到气体中的装置。(C)2012年,JPO和INPIT
    • 5. 发明专利
    • Apparatus and method for separating and recovering voc using pressurized carbon dioxide
    • 使用加压二氧化碳分离和回收VOC的装置和方法
    • JP2008296179A
    • 2008-12-11
    • JP2007147360
    • 2007-06-01
    • Ikutoku Gakuen Kanagawa Koka DaigakuTama Tlo Kkタマティーエルオー株式会社学校法人幾徳学園神奈川工科大学
    • KOJIMA HIROMITSUOBA TAKEYASUISHIDA MASARU
    • C02F1/26B01D11/00
    • PROBLEM TO BE SOLVED: To provide an apparatus for separating and recovering VOC, which can realize complete treatment not involving the occurrence of secondary waste after the separation and recovery of VOC, and a method for separating and recovering the VOC.
      SOLUTION: VOC contained in contaminated underground water is extracted with supercritical carbon dioxide. Thereafter, the step of extracting VOC using carbon dioxide and water alternately as an extraction medium is repeated under two conditions which have rendered the equilibrium constant of an aqueous VOC solution-pressurized carbon dioxide system significantly different. The repetition of this step can realize the concentration of VOC corresponding to the equilibrium constant difference, and, finally, a substantially 100% VOC phase can be separated. Accordingly, VOC can be recovered at low cost without use of any additional constitution such as an adsorbent.
      COPYRIGHT: (C)2009,JPO&INPIT
    • 待解决的问题:提供一种用于分离和回收挥发性有机化合物的装置,其可以实现在分离和回收挥发性有机化合物之后不涉及二次废物的完全处理,以及分离和回收挥发性有机化合物的方法。

      解决方案:用超临界二氧化碳提取含污染地下水中的VOC。 此后,在使VOC水溶液 - 加压二氧化碳体系的平衡常数显着不同的两个条件下重复使用二氧化碳和水交替提取VOC作为萃取介质的步骤。 该步骤的重复可以实现对应于平衡恒定差的VOC浓度,最后可以分离基本上100%的VOC相。 因此,可以以低成本回收VOC,而不使用任何附加结构如吸附剂。 版权所有(C)2009,JPO&INPIT