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    • 1. 发明专利
    • Hydrocarbon adsorption/combustion catalyst
    • 碳氢化合物吸附/燃烧催化剂
    • JP2006167540A
    • 2006-06-29
    • JP2004361345
    • 2004-12-14
    • Babcock Hitachi Kkバブコック日立株式会社
    • MURAKAMI KAZUMITOMINAGA SHIGERUHAMADA IKUHISASUGANO SHUICHI
    • B01J29/74B01D53/94F01N3/08F01N3/10F01N3/28
    • PROBLEM TO BE SOLVED: To provide a hydrocarbon adsorption/combustion catalyst capable of exhibiting a high cold hydrocarbon (HC) cleaning performance and improving the cleaning performance for three components of HC, CO and NO X upon the stationary operation. SOLUTION: The hydrocarbon adsorption/combustion catalyst, which is arranged on the downstream of a ternary catalyst installed on an exhaust system of an internal combustion engine and facilitates adsorption/combustion purification of hydrocarbon exhausted upon the engine starting, has a three layer structure formed by applying: a first layer of a hydrocarbon adsorption layer formed by depositing silver (Ag), palladium (Pd) and titanium (Ti) which are deposited on catalyst substrates on zeolite in a prescribed proportion; a second layer of a hydrocarbon purification layer formed on the first layer by depositing Pd and platinum (Pt) as a catalyst component on ceria-alumina multiple oxide single system or ceria-alumina multiple oxide and ceria-zirconia multiple oxide as a catalyst carrier; and a third layer of a ternary catalyst layer formed by depositing rhodium (Rh) and Pt as a catalyst component on the catalyst carrier. COPYRIGHT: (C)2006,JPO&NCIPI
    • 要解决的问题:提供能够表现出高的冷烃(HC)清洗性能并提高HC,CO和NO三种组分的清洁性能的烃吸附/燃烧催化剂。 静止操作。 解决方案:安装在内燃机排气系统上的三元催化剂下游的碳氢化合物吸附/燃烧催化剂有助于在发动机启动时排出的碳氢化合物的吸附/燃烧净化,具有三层 通过施加形成的结构:通过以规定比例沉积在沸石上的催化剂基底上沉积银(Ag),钯(Pd)和钛(Ti)而形成的第一层烃吸附层; 通过在二氧化铈 - 氧化铝多氧化物单系或二氧化铈 - 氧化铝复氧化物和二氧化铈 - 氧化锆复合氧化物上沉积Pd和铂(Pt)作为催化剂组分作为催化剂载体,形成在第一层上的第二层烃纯化层; 以及通过在催化剂载体上沉积铑(Rh)和Pt作为催化剂组分而形成的三元催化剂层的第三层。 版权所有(C)2006,JPO&NCIPI
    • 2. 发明专利
    • Hydrocarbon adsorption and combustion catalyst, and its production process
    • 碳氢化合物吸附和燃烧催化剂及其生产工艺
    • JP2005224704A
    • 2005-08-25
    • JP2004036059
    • 2004-02-13
    • Babcock Hitachi Kkバブコック日立株式会社
    • TOMINAGA SHIGERUMURAKAMI KAZUMIITO TAKESHIHAMADA IKUHISAHIGASHIYAMA KAZUHISA
    • F01N3/10B01D53/94B01J29/74B01J37/08F01N3/24F01N3/28
    • PROBLEM TO BE SOLVED: To provide a HC adsorption and combustion catalyst preventing Ag from transpirating and excellent in HC hold performance and oxidation activity, and its production process. SOLUTION: In the hydrocarbon adsorption and combustion catalyst having an adsorbent layer 5 placed in the downstream side of a three-way catalyst provided on an exhaust gas flow path of an internal combustion engine and adsorbing hydrocarbon in an exhaust gas, and a combustion catalyst layer 6 provided on the adsorbent layer 5, the adsorbent layer 5 comprises zeolite which carries an Ag-Pd alloy or a precursor thereof as a main component and the combustion catalyst layer 6 comprises a carrier of ceria and/or zirconia which carries at least one kind of oxidation catalyst component selected from the group consisting of palladium (Pd), platinum (Pt) and rhodium (Rh). COPYRIGHT: (C)2005,JPO&NCIPI
    • 要解决的问题:提供一种HC吸附和燃烧催化剂,其防止Ag蒸发并具有优异的HC保持性能和氧化活性及其制备方法。 解决方案:在具有吸附剂层5的烃吸附和燃烧催化剂中,该吸附剂层5放置在设置在内燃机的排气流路上并在废气中吸附碳氢化合物的三元催化剂的下游侧, 设置在吸附剂层5上的燃烧催化剂层6,吸附剂层5包含承载Ag-Pd合金或其前体作为主要成分的沸石,燃烧催化剂层6包含二氧化铈和/或氧化锆载体, 至少一种选自钯(Pd),铂(Pt)和铑(Rh)的氧化催化剂组分。 版权所有(C)2005,JPO&NCIPI
    • 3. 发明专利
    • HEAT STORAGE TYPE WASTE GAS TREATMENT DEVICE
    • JP2002195540A
    • 2002-07-10
    • JP2000396745
    • 2000-12-27
    • BABCOCK HITACHI KK
    • KOBAYASHI KAZUKITOMINAGA SHIGERUMUKAI TOSHIFUMIKAWAZOE HIROSHI
    • F23L15/02F23G5/50F23G7/06
    • PROBLEM TO BE SOLVED: To perform a stable operation for a long period by preventing the closure of an opening part of a heat storage material through which untreated waste gas flows in a heat storage type waste gas treatment device. SOLUTION: The heat storage type waste gas treatment device comprises a furnace 4 for treating the untreated waste gas including VOC at high temperature, a heat storage layer 3 of honeycomb shape in section for preheating the untreated waste gas and removing heat of treated waste gas and a distributing valve 2 for distributing the untreated waste gas to the high temperature heat storage layer. A pressure loss part of a waste gas passage is detected in accordance with the differential pressure of the heat storage layer, and the rotation of the distributing valve 2 is controlled to adjust the flowing time of the high temperature treated waste gas flowing through the heat storage layer 3, so that the pressure loss part is heated to 450 to 500 deg.C. Thus, adhering silicone oil is rapidly oxidized to become silica particles. The silica particles can be simply removed by a blower to suppress the closure of the waste gas passage with a stable operation.
    • 4. 发明专利
    • HEAT STORAGE TYPE WASTE GAS TREATMENT DEVICE
    • JP2002195538A
    • 2002-07-10
    • JP2000394232
    • 2000-12-26
    • BABCOCK HITACHI KK
    • KOBAYASHI KAZUKITOMINAGA SHIGERUMUKAI TOSHIFUMI
    • F23L15/02F23G7/06
    • PROBLEM TO BE SOLVED: To provide a heat storage type waste gas treatment device provided with means for treating waste gas such as silicone oil producing a solid inorganic compound upon combustion, preventing the closure of heat storage materials or the increase of pressure loss even when a sintering is generated at a high temperature part, suppressing the increase of power energy of a fan and performing a stable operation. SOLUTION: In the heat storage type waste gas treatment device, a plurality of heat storage chambers including a heat storage layer 3 in which when high temperature treated waste gas from a furnace (waste gas treating zone) 4 flows, heat is stored, and when low temperature untreated waste gas flows, the stored heat is discharged to preheat the untreated waste gas are made to communicate mutually through the waste gas treating zone. The supply and exhaust directions of the waste gas are sequentially switched to treat the untreated waste gas. The heat storage layer 3 is formed by laminating a plurality of steps of honeycomb type heat storage materials. The diameter of the cell of the honeycomb type heat storage material 7 at least in an outlet side is larger than the diameter of the cell of the honeycomb type heat storage material 8 on other step.
    • 5. 发明专利
    • CONTROL METHOD FOR VOLATILE ORGANIC COMPOUND PROCESSING APPARATUS
    • JP2002048325A
    • 2002-02-15
    • JP2000230634
    • 2000-07-31
    • BABCOCK HITACHI KK
    • MUKAI TOSHIFUMITOMINAGA SHIGERUSHIBATA KENJIITAMI TETSUOUENISHI MASATO
    • F23G5/50B01D53/86F23G7/06F23G7/07
    • PROBLEM TO BE SOLVED: To provide a control method for a volatile organic compound processing apparatus including a procedure of securely protecting a combustion catalyst even when a rapid increase of the amount of heat produced from VOC containing gas in a catalyst combustion/heat storage type volatile organic compound(VOC) processing apparatus. SOLUTION: There are provided a furnace 1 including therein a heat source 2, a heat storage layer 20 containing a heat storage structure 6 that form a plurality of flow passages by disposing a catalyst layer 3 on the side of the furnace 1 and the catalyst layer 3, and a distributor 18 for changing over in succession and supplying three kinds of gases of VOC containing as, purge gas, and processed gas to the heat storage layer 20, and exhausted waste gas passing through the heat storage layer 20, furnace 1, and heat storage layer 20. A processing apparatus for subjecting the VOC containing gas to catalytic combustion processing and leaning the same, and further regenerating heat of the waste gas interrupts a heat supply operation of the heat source 2 and increases the amount Qp of purge gas by SQp when temperature Tc of the catalyst layer 3 exceeds catalyst upper limit reference temperature Tcc lower than heat resistant temperature or when passage gas average temperature Td of the distributor 18 exceeds upper limit reference temperature Tdc of the distributor lower than the heat insulation temperature.
    • 7. 发明专利
    • HEAT ACCUMULATIVE TYPE HEAT EXCHANGER
    • JP2001183081A
    • 2001-07-06
    • JP37128199
    • 1999-12-27
    • BABCOCK HITACHI KK
    • MUKAI TOSHIFUMITOMINAGA SHIGERUISHIHARA ISAO
    • F28D17/02
    • PROBLEM TO BE SOLVED: To cause a heat accumulative type heat exchanger used in a VOC processor or the like of catalyst combustion/rotary heat accumulative system to become one in which a temperature efficiency is hardly decreased even if an amount of processing gas is varied. SOLUTION: In a heat accumulative type heat exchanger in which gases showing different temperatures are flowed alternatively in a flow passage filled with heat accumulating material and a heat exchanging operation is carried out between gases of different temperatures through the heat accumulating material, metallic lath plates 2 acting as heat accumulative material are applied, a shape having a ridge line 3 extending along a direction of long diameter of a rhombus grid is formed in advance at the same position as that of each of the metallic lath plates 2, this ridge line 3 is applied as a position setting line, a plurality of ridge lines are laminated and further filled in the heat exchanger in such a way that the ridge lines may become in parallel with the gas flow.
    • 9. 发明专利
    • HONEYCOMB CATALYST
    • JPH11290699A
    • 1999-10-26
    • JP10474998
    • 1998-04-15
    • BABCOCK HITACHI KK
    • TOMINAGA SHIGERUMUKAI TOSHIFUMIHIROTA TAKESHI
    • B01D53/94B01J23/30B01J35/04
    • PROBLEM TO BE SOLVED: To reduce a boundary film diffusion resistance in gas flow paths and enhance a catalytic performance without changing a catalyst manufacturing process by providing a cut part traversing plural parallel gas flow paths. SOLUTION: Cut parts 3 reaching the half of the depth of a honeycomb cross section perpendicularly with gas flow paths 2 are alternately provided from two oppositely positioned side faces. In addition, the cut parts 3 are alternately formed at a specified interval on the same side face to reduce a boundary film diffusion resistance and thereby enhance a catalytic performance. The flow paths 2 are cut off through the entire cell of the honeycomb 1, together with the cut parts 3 from the opposite direction. Therefore, it is expected that the activity of the entire cross section of the parallel gas flow paths 2 can be uniformly enhanced. Further, the cut parts 3 need not be provided perpendicularly with the gas flow paths 2 but can have a specified angle with the gas flow paths 2. Thus, it is possible to enhance the catalytic efficiency by preventing the boundary film diffusion resistance from increasing in the gas flow paths 2 almost without changing a manufacturing process.