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
    • 11. 发明专利
    • Method and apparatus for synthesizing ethanol
    • 用于合成乙醇的方法和装置
    • JP2008239539A
    • 2008-10-09
    • JP2007081397
    • 2007-03-27
    • Ihi CorpToyama Univ国立大学法人富山大学株式会社Ihi
    • TSUBAKI NORITATSUCHO IKAMATA HIROYUKINISHINO JUNYA
    • C07C29/149C07B61/00C07C31/08C07C41/00C07C43/04C07C67/37C07C69/14
    • PROBLEM TO BE SOLVED: To provide a method for synthesizing ethanol by which the ethanol can be synthesized by using a hardly fermentable raw material such as wood pitch, coal, natural gas, petroleum residue, heavy oil, biomass or the like as a raw material to enlarge the range of the raw material for producing the ethanol, and to provide an apparatus therefor. SOLUTION: The method for synthesizing the ethanol includes a methyl acetate-synthesizing step of synthesizing a methyl acetate-containing gas containing the methyl acetate (CH 3 COOCH 3 ) by the carbonylation reaction of dimethyl ether (CH 3 OCH 3 ), an ethanol-containing gas-synthesizing step of synthesizing an ethanol-containing gas containing the ethanol (C 2 H 5 OH) by the hydrogenation reaction of the methyl acetate, and an ethanol-separating step of separating the ethanol from the ethanol-containing gas. COPYRIGHT: (C)2009,JPO&INPIT
    • 待解决的问题:提供一种合成乙醇的方法,通过使用难以发酵的原料如木沥青,煤,天然气,石油残渣,重油,生物质等可以合成乙醇,作为 用于扩大生产乙醇的原料的范围的原料,并提供其设备。 解决方案:合成乙醇的方法包括乙酸甲酯合成步骤,该步骤合成含有乙酸甲酯(CH 3 SBH 3 COOCH 3 SBB)的含乙酸甲酯的气体, 通过二甲醚(CH 3 SB 3 OCH 3 SBS)的羰基化反应,合成含有乙醇的含乙醇气体(C
    • 12. 发明专利
    • Method and apparatus for producing hydrogen from glycerol
    • 从甘油生产氢的方法和装置
    • JP2009298615A
    • 2009-12-24
    • JP2008152871
    • 2008-06-11
    • Ihi Corp株式会社Ihi
    • KAMATA HIROYUKI
    • C01B3/38C01B3/48C01B3/56
    • PROBLEM TO BE SOLVED: To provide a method and an apparatus for producing hydrogen from glycerol capable of efficiently supplying glycerol to a reformer without carbonizing glycerol and leaving as a non-evaporated residue in producing hydrogen from glycerol.
      SOLUTION: The apparatus is equipped with a mixing part 2 for mixing water in glycerol, a spraying nozzle 4 for spraying a glycerol mixture obtained by the mixing part 2 to an evaporator 3 heated to 290°C or more and a reformer 5 for steam-reforming a mist-like glycerol mixture produced by spraying from the spraying nozzle 4, wherein the glycerol mixture prepared by mixing water into glycerol is sprayed to the evaporator 3 heated to 290°C or more through the spraying nozzle 4 and the mist-like glycerol mixture thus produced is supplied to the reformer 5 to be steam-reformed.
      COPYRIGHT: (C)2010,JPO&INPIT
    • 要解决的问题:提供一种用于从甘油生产氢的方法和装置,其能够有效地向重整器供应甘油,而不使碳酸化甘油,并作为未蒸发的残余物从甘油产生氢气中留下。 解决方案:该装置装备有用于在甘油中混合水的混合部分2,用于将由混合部分2获得的甘油混合物喷射到加热至290℃或更高的蒸发器3的喷雾喷嘴4和重整器5 用于通过喷雾喷嘴4喷雾生成的雾状甘油混合物进行蒸汽重整,其中将通过将水混合到甘油中制备的甘油混合物通过喷雾喷嘴4喷雾至加热至290℃或更高的蒸发器3, 如此制备的甘油混合物供给重整器5进行蒸汽重整。 版权所有(C)2010,JPO&INPIT
    • 13. 发明专利
    • Method and apparatus for continuously regenerating fischer-tropsch synthesis catalyst
    • 连续再生FISCHER-TROPSCH合成催化剂的方法和装置
    • JP2009214013A
    • 2009-09-24
    • JP2008060396
    • 2008-03-11
    • Ihi Corp株式会社Ihi
    • NARAI KENTAROOHARA HIROAKIKAMATA HIROYUKI
    • B01J38/10B01J23/75B01J23/94C10G2/00
    • PROBLEM TO BE SOLVED: To regenerate a Fischer-Tropsch synthesis catalyst continuously so that the regenerated catalyst can be used circularly. SOLUTION: The method for continuously regenerating the Fischer-Tropsch synthesis catalyst comprises the steps of: supplying mixed slurry 2 of a liquid hydrocarbon with the catalyst to a reactor 1; supplying a gaseous raw material 4 to the mixed slurry-supplied reactor to perform a Fischer-Tropsch synthesis reaction by contacting the supplied gaseous raw material 4 with particles of the catalyst to produce a product based on a straight-chain hydrocarbon; withdrawing a mixed fluid 11 composed of the product produced in the reactor 1 and the catalyst; separating the withdrawn mixed fluid into the product 18 and the catalyst 19; treating the separated catalyst 19 with a reductive gas 28 at high temperature to obtain the regenerated catalyst 19a; mixing the regenerated catalyst 19a in a part of the liquid hydrocarbon 26 separated from the product 18 to prepare the mixed slurry 2; and supplying the prepared mixed slurry 2 to the reactor 1. COPYRIGHT: (C)2009,JPO&INPIT
    • 待解决的问题:连续地再生费 - 托合成催化剂,使循环使用再生催化剂。 解决方案:用于连续再生费 - 托合成催化剂的方法包括以下步骤:将液体烃与催化剂的混合浆料2供应到反应器1; 向混合浆料供应的反应器中供应气态原料4以通过使所提供的气态原料4与催化剂的颗粒接触以制备基于直链烃的产物进行费 - 托合成反应; 取出由反应器1中产生的产物和催化剂组成的混合流体11; 将抽出的混合流体分离成产物18和催化剂19; 在高温下用还原气体28处理分离的催化剂19,得到再生催化剂19a; 将再生催化剂19a混合在与产物18分离的液体烃26的一部分中以制备混合浆料2; 并将制备的混合浆料2供应到反应器1.版权所有(C)2009,JPO&INPIT
    • 14. 发明专利
    • Method and apparatus for recovering metal from petroleum-based unused resource
    • 从石油基的未利用资源中回收金属的方法和装置
    • JP2009046744A
    • 2009-03-05
    • JP2007216075
    • 2007-08-22
    • Ihi Corp株式会社Ihi
    • FUJIYOSHI HIRONOBUKAMATA HIROYUKIOHARA HIROAKINAKANO KUNIHIKOHIRATA TETSUYAAYABE TSUNEO
    • C25C7/02B09B3/00B09B5/00C25C1/00
    • Y02P10/234
    • PROBLEM TO BE SOLVED: To provide a method and apparatus for recovering metals from a petroleum-based unused resource by which conventionally effectively unused metals can be easily and quickly recovered in high purity from a petroleum-based unused resource containing a large amount of carbon and the remaining unused resource from which the metals have been recovered can be used as a heat source. SOLUTION: The apparatus 1 is used for recovering metals such as nickel from a petroleum-based unused resource containing a large amount of carbon, such as petrocoke or oil sand. The apparatus 1 is equipped with: a sheet-shaped cathode 2; a separator 4 having no conductivity, which is allowed to face the cathode 2 while setting a sheet-shaped petroleum-based unused resource, obtained by mixing a binder with the unused resource and forming the resulting mixture into a sheet, as an anode; a solution tank 5 accommodating an electrolyte solution L; and a voltage applying part 6 for applying a prescribed voltage between the both electrodes 2, 3 in such a state that the cathode 2 and the sheet-shaped anode 3 are immersed in the electrolyte solution L in the solution tank 5. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种从石油基未使用的资源中回收金属的方法和装置,通过该方法和装置可以从含有大量的石油基的未使用资源中容易且快速地以高纯度回收常规有效的金属 的碳和剩余的未回收的金属可以用作热源。 解决方案:装置1用于从含有大量碳的石油基未使用的资源(例如石油焦油或油砂)中回收诸如镍的金属。 装置1装备有:片状阴极2; 没有导电性的隔板4,同时设置通过将粘合剂与未使用的资源混合并将所得混合物形成为片材而获得的片状石油基未使用的资源,同时面向阴极2作为阳极; 容纳电解液L的溶液槽5; 以及在阴极2和片状阳极3浸渍在溶液罐5中的电解液L中的状态下,在两个电极2,3之间施加规定电压的电压施加部6。 (C)2009,JPO&INPIT
    • 15. 发明专利
    • Ozone water application equipment and its fungicidal treatment
    • 臭氧水应用设备及其杀真菌治疗
    • JP2009039614A
    • 2009-02-26
    • JP2007205243
    • 2007-08-07
    • Ihi Corp株式会社Ihi
    • OSAWA NORIYOSHIKAMATA HIROYUKINAKANO KUNIHIKONARAI KENTARO
    • B08B3/08A61B1/12A61L2/18C02F1/50
    • PROBLEM TO BE SOLVED: To provide ozone water application equipment which can perform a fungicidal treatment to fungicide inside the equipment, using an existing function to the maximum possible extent. SOLUTION: This ozone water application equipment 1 includes a cleaning tank 2 for cleaning an object to be cleaned "x", an oxygen enricher 3 of a pressure fluctuating adsorption type, an ozone generator 4 which generates ozone, using highly enriched oxygen from the oxygen enricher 3, a water supply line 17 for supplying water to the cleaning tank 2 and an ozone water manufacturing line 18 which manufactures ozone water by mixing water filtered through the cleaning tank 2 with the ozone from the ozone generator 4. Regarding the application of the ozone water, the ozone water is supplied to the cleaning tank 2 and the object to be cleaned "x" is ozone-cleaned, then the ozone water is drained and the object "x" is taken out of the cleaning tank 2, and the cleaning tank 2 is cleaned. This equipment 1 incorporates a cleaning means for removing the residue from the cleaning tank 2 by water rinsing, a sterilizing means for making the cleaning tank 2 sterilze with the ozone water and a drying means for drying the cleaning tank 2. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供可以对设备内的杀真菌剂进行杀真菌处理的臭氧水应用设备,尽可能地利用现有的功能。 解决方案:该臭氧水施加设备1包括用于清洁待清洁物体“x”的清洗槽2,压力波动吸附型氧气浓缩器3,使用高浓度氧气产生臭氧的臭氧发生器4 来自氧浓缩器3,用于向清洗槽2供水的供水管17和臭氧水生产线18,其通过将通过清洗槽2过滤的水与来自臭氧发生器4的臭氧混合而制造臭氧水。关于 应用臭氧水,将臭氧水供给至清洗槽2,将待清洁物体“x”进行臭氧清洗,然后排出臭氧水并将物体“x”从清洗槽2中取出 清洗清洗槽2。 该设备1包括用于通过水冲洗从清洁槽2中除去残留物的清洁装置,用于使清洗槽2与臭氧水灭菌的消毒装置和用于干燥清洗槽2的干燥装置。版权所有: (C)2009,JPO&INPIT
    • 16. 发明专利
    • Oxygen enricher
    • 氧气环保
    • JP2009006256A
    • 2009-01-15
    • JP2007169583
    • 2007-06-27
    • Ihi Corp株式会社Ihi
    • OSAWA NORIYOSHIKAMATA HIROYUKINAKANO KUNIHIKONARAI KENTARO
    • B01D53/04B01D53/26C01B13/02
    • PROBLEM TO BE SOLVED: To provide an oxygen enricher which can inhibit the diffusion of moisture to an adsorption cylinder during a shutdown. SOLUTION: This oxygen enricher 1 comprises a compressor 2 for compressing air, a plurality of adsorption cylinders 3a and 3b filled with an adsorbent a3 for adsorbing nitrogen selectively, and a switching means 4 for making the adsorption cylinders 3a and 3b adsorb nitrogen by alternately supplying the compressed air from the compressor 2 to each adsorption cylinder 3a and 3b, and on the other hand, making the adsorption cylinders 3a and 3b desorb/exhaust the nitrogen. In addition, moisture absorption cylinders 7a and 7b filled with a moisture absorbent "m" which absorbs moisture from the compressed air, are arranged independently between the switching means 4 and each adsorption cylinder 3a and 3b. Further, shut-off valves 8a and 8b which open during operation to enrich oxygen and close to shut off the penetration of moisture into the adsorption cylinders 3a and 3b during operation stoppage, are arranged between the moisture absorption cylinders 7a and 7b and each adsorption cylinder 3a and 3b. COPYRIGHT: (C)2009,JPO&INPIT
    • 要解决的问题:提供一种氧气浓缩器,其可以在关闭期间抑制湿气向吸附筒的扩散。 该氧浓缩器1包括用于压缩空气的压缩机2,填充有用于选择性地吸附氮的吸附剂a3的多个吸附缸3a和3b;以及用于使吸附缸3a和3b吸附氮的切换装置4 通过将压缩机2的压缩空气交替地供给到各吸附筒3a,3b,另一方面使吸附筒3a,3b解吸/排出氮。 此外,填充有从压缩空气吸收水分的吸湿剂“m”的吸湿筒7a和7b独立地设置在开关装置4和每个吸附缸3a和3b之间。 此外,在操作期间打开以在运行停止期间将氧气浓缩并接近以阻止水分渗透到吸附缸3a和3b中的截止阀8a和8b布置在吸湿筒7a和7b与每个吸附缸 3a和3b。 版权所有(C)2009,JPO&INPIT
    • 17. 发明专利
    • Co selective oxidation method and co selective oxidation reactor
    • CO选择性氧化方法和CO选择性氧化反应器
    • JP2008222501A
    • 2008-09-25
    • JP2007064164
    • 2007-03-13
    • Ihi Corp株式会社Ihi
    • OHARA HIROAKINARAI KENTAROMURAMOTO TOMOYAKAMATA HIROYUKIHAMADA YUKITAKA
    • C01B3/38B01J23/76C01B3/58H01M8/06
    • Y02P20/52
    • PROBLEM TO BE SOLVED: To provide a CO selective oxidation method and a CO selective oxidation reactor to be used for allowing carbon monoxide (CO) included in a reformed gas produced by reforming a hydrocarbon fuel such as city gas, LPG, kerosene and biogas to selectively react with oxygen to be removed, wherein a noble metal-based catalyst for CO selective oxidation is unnecessary. SOLUTION: A Cu-based CO selective oxidation catalyst 17 is formed by depositing CuO as an active metal on a CeO 2 carrier mixed with Al 2 O 3 . A cooling pipe 21 to which a cooling fin 24 is attached is disposed in a square cylindrical chamber 18 having a gas inlet 19 at the lower end and a gas outlet 20 at the upper end, and functioning as a gas passage 16 inside. The both ends of the cooling pipe 21 are made to penetrate through the side walls of the chamber to protrude outward, and are respectively connected to a supply line 22 and a discharge line 23 of cooling water 12. The square cylindrical chamber 18 is charged with the Cu-based CO selective oxidation catalyst 17, and the gas inlet 19 and the gas outlet 20 are sealed with a porous catalyst receiving plate 25 to form the CO selective oxidation reactor 15. By allowing a reformed gas 8 of hydrocarbon fuel with addition of oxygen or air to flow in the gas passage 16 and bringing into contact with the Cu-based CO selective oxidation catalyst 17, CO in the reformed gas 9 is selectively oxidized to reduce the CO concentration. COPYRIGHT: (C)2008,JPO&INPIT
    • 待解决的问题:提供CO选择性氧化法和CO选择氧化反应器,用于允许通过重整烃燃料如城市燃气,LPG,煤油所产生的重整气体中包含的一氧化碳(CO) 和沼气选择性地与待除去的氧反应,其中不需要用于CO选择性氧化的贵金属基催化剂。 解决方案:通过将CuO作为活性金属沉积在与Al 2 SBB混合的CeO 2 SBB载体上形成Cu基CO选择氧化催化剂17, 3 。 安装冷却翅片24的冷却管21设置在具有下端的气体入口19和上端的气体出口20的方形圆筒形室18中,并且作为内部的气体通道16。 使冷却管21的两端穿过室的侧壁向外突出,并且分别连接到冷却水12的供应管线22和排出管线23.方圆筒室18被带有 Cu基CO选择氧化催化剂17,气体入口19和气体出口20用多孔催化剂接收板25密封,形成CO选择氧化反应器15.通过添加碳氢燃料的重整气体8, 氧气或空气在气体通道16中流动并与Cu基CO选择氧化催化剂17接触,选择性地氧化重整气体中的CO以降低CO浓度。 版权所有(C)2008,JPO&INPIT
    • 18. 发明专利
    • Sodium separation apparatus
    • 钠分离装置
    • JP2013216960A
    • 2013-10-24
    • JP2012090357
    • 2012-04-11
    • Ihi Corp株式会社Ihi
    • MURAMOTO TOMOYAITO AKIRAKAMATA HIROYUKI
    • C22B26/10C22B9/02
    • Y02P10/234
    • PROBLEM TO BE SOLVED: To provide a sodium separation apparatus capable of effectively separating sodium from impurities even in a small amount.SOLUTION: A sodium separation apparatus 1 is for separating a sodium A from impurities contained in the sodium A, and includes a tank 2 having a containing space S for containing the sodium A, a temperature regulator 3 for adjusting temperature in the containing space S, and a net-like member 4 provided in the containing space S. The tank 2 includes an impurity discharging part 5 provided to a bottom part 2a1 and a sodium extraction part 6 provided above the impurity discharging part 5.
    • 要解决的问题:提供一种能够有效地将钠与杂质分离的钠分离装置即使少量。解决方案:钠分离装置1用于将钠A与钠A中所含的杂质分离,并且包括罐2 具有用于容纳钠A的容纳空间S,用于调节容纳空间S中的温度的温度调节器3和设置在容纳空间S中的网状构件4.储罐2包括设置在容纳空间S中的杂质排出部5 底部2a1和设置在杂质排出部5上方的钠提取部6。
    • 19. 发明专利
    • Exhaust gas treatment method and exhaust gas treatment equipment
    • 排气处理方法和排气处理设备
    • JP2011025123A
    • 2011-02-10
    • JP2009171834
    • 2009-07-23
    • Ihi Corp株式会社Ihi
    • SATO NAOKIUENO SHUNICHIROKAMATA HIROYUKI
    • B01D53/94B01D53/86
    • PROBLEM TO BE SOLVED: To provide an exhaust gas treatment method which can inhibit the adsorption of ammonia by a catalyst for mercury oxidation reaction and simplify treatment steps as a whole, as well as exhaust gas treatment equipment.
      SOLUTION: This exhaust gas treatment equipment 1 is for sending an exhaust gas to a denitrification device 5 from a fire furnace 2, and the denitrification device 5 includes a first catalyst 10 which brings about mercury oxidation reaction and a second catalyst 11 which generates a denitrification reaction downstream of the first catalyst 10. In addition, an ammonia adding line 12 which adds ammonia, is arranged between the first catalyst 10 and the second catalyst 11. When the exhaust gas is treated, a halogenated gas is kept in such a state that it coexists in the exhaust gas from the fire furnace 2, and a hardly soluble metallic mercury contained in the exhaust gas is transformed to a water-soluble divalent mercury with the help of the first catalyst 10. Next, the exhaust gas is denitrified by the second catalyst 11 with the addition of ammonia supplied from the ammonia adding line 12.
      COPYRIGHT: (C)2011,JPO&INPIT
    • 要解决的问题:提供一种能够抑制由用于汞氧化反应的催化剂吸附氨的废气处理方法,并且简化整个处理步骤以及废气处理设备。 解决方案:该废气处理设备1用于将废气从消防炉2送至脱氮装置5,脱氮装置5包括引起汞氧化反应的第一催化剂10和第二催化剂11, 在第一催化剂10的下游产生脱氮反应。此外,在第一催化剂10和第二催化剂11之间配置有添加氨的氨添加管线12.当处理废气时,将卤化气体保持在 在来自火炉2的废气中共存的状态,废气中含有的难溶金属汞在第一催化剂10的帮助下转变为水溶性二价汞。接下来,废气为 通过加入从氨添加管线12供应的氨,由第二催化剂11反硝化。版权所有(C)2011,JPO&INPIT