公开(公告)号：US20100227241A1

公开(公告)日：2010-09-09

申请号：US12224282

申请日：2007-02-15

Applicant: Takafumi Sarata ,  Norimasa Yanase ,  Toru Ozaki ,  Tsuneaki Tamachi ,  Kazutaka Yuzurihara ,  Fumiharu Iwasaki ,  Noboru Ishisone

Inventor： Takafumi Sarata ,  Norimasa Yanase ,  Toru Ozaki ,  Tsuneaki Tamachi ,  Kazutaka Yuzurihara ,  Fumiharu Iwasaki ,  Noboru Ishisone

IPC: H01M8/04 ,  F16K15/00 ,  B01J3/00

CPC classification number: G05D16/0652 ,  F16K31/1266 ,  F16K31/365 ,  H01M8/04089 ,  H01M8/04216 ,  Y02E60/36 ,  Y10T137/1624 ,  Y10T137/7904

Abstract: A pressure regulating valve comprises a first pressure deformation part (120) receiving the pressure on the fuel demand side and deformable and a second pressure deformation part (130) so installed as to face the first pressure deformation part (120), receiving a predetermined pressure, and deformable. A first flow passage (140), a second flow passage (150), and a communication passage (160) allowing the first and second flow passages (140, 150) to communicate with each other are formed in the space between the first and second pressure deformation parts (120, 130). The pressure regulating valve further comprises a valve member (170) having a valve element (172) which has a connection part (171) extending through the communication passage (160) and connecting the first pressure deformation part (120) to the second pressure deformation part (130), installed in the connection part (171), and closing the communication passage (160) when moved to the second pressure deformation part (130) side. When the pressure on the fuel demand side is lower than a predetermined value, the valve element (172) does not close the communication passage (160). However, when the pressure on the fuel demand side is equal to or more than the predetermined value, the valve element (172) closes the communication passage (160).

Abstract translation: 压力调节阀包括接收燃料需求侧和可变形的压力的第一压力变形部分（120）和安装成面对第一压力变形部分（120）的第二压力变形部分（130），接收预定压力 ，并可变形。 第一和第二流动通道（140），第二流动通道（150）和允许第一和第二流动通道（140,150）彼此连通的连通通道（160）形成在第一和第二流动通道 压力变形部件（120,130）。 压力调节阀还包括具有阀元件（172）的阀构件（170），阀元件（172）具有延伸穿过连通通道（160）的连接部分（171），并将第一压力变形部件（120）连接到第二压力变形 部件（130），安装在连接部分（171）中，并且当移动到第二压力变形部分（130）侧时关闭连通通道（160）。 当燃料需求侧的压力低于预定值时，阀元件（172）不关闭连通通道（160）。 然而，当燃料需求侧的压力等于或大于预定值时，阀元件（172）关闭连通通道（160）。

公开(公告)号：US07556785B2

公开(公告)日：2009-07-07

申请号：US10435680

申请日：2003-05-12

Applicant: Shroff Rajnikant Devidas ,  Pushpaksen P. Asher

Inventor： Shroff Rajnikant Devidas ,  Pushpaksen P. Asher

IPC: B01J19/00 ,  A62B7/08 ,  B01J35/02 ,  B01J3/00 ,  A61L2/00 ,  A61L9/00 ,  C01B25/00 ,  B01F13/02 ,  B01D21/26 ,  F15C1/16 ,  B01D45/12 ,  B01D19/00

CPC classification number: A23B9/18 ,  A01M13/00 ,  A61L2/20 ,  C01B25/06 ,  Y10T137/2109 ,  Y10T137/4538

Abstract: Phosphine gas is generated by agitating a reaction mixture of a metal phosphide and water with agitation air in a reaction pot of a phosphine gas generator. The resulting phosphine gas is then diluted with dilution air to produce a fumigant phosphine gas which is directly delivered to a commodity for fumigation. The reaction pot does not have any rotating means such as agitators, rotors, or stirrers. The generator provides on-site generation of phosphine gas in a rapid manner improving the fumigation efficiency for a commodity, such as grain, preferably contained within a storage structures, such as a grain silo. The generator has a built in deactivation system for the unused metal phosphide and phosphine gas.

Abstract translation: 通过在磷化氢气体发生器的反应罐中用搅拌空气搅拌金属磷化物和水的反应混合物来产生磷化氢气体。 然后将所得的磷化氢气体用稀释空气稀释以产生熏蒸剂膦气体，其直接输送到商品进行熏蒸。 反应釜不具有任何旋转装置，例如搅拌器，转子或搅拌器。 发电机以快速的方式提供现场生成磷化氢气体，从而提高了诸如颗粒的商品的熏蒸效率，优选地包含在诸如谷仓的存储结构内。 该发生器具有用于未使用的金属磷化物和磷化氢气体的内置去激活系统。

公开(公告)号：US07431901B2

公开(公告)日：2008-10-07

申请号：US09775999

申请日：2001-02-02

Applicant: Paul Stiros ,  Jeffrey Donald Painter ,  Frank Andrej Kvietok ,  Charles Michael Hardy

Inventor： Paul Stiros ,  Jeffrey Donald Painter ,  Frank Andrej Kvietok ,  Charles Michael Hardy

IPC: A61L9/00 ,  A62B7/08 ,  B01J3/00 ,  B01D47/00 ,  B01D24/00

CPC classification number: A61L9/014 ,  A61L9/04 ,  A61L9/048 ,  A61L9/122 ,  A61L9/16 ,  A63F3/0478 ,  A63F3/06 ,  A63F2003/0489

Abstract: Apparatus and methods for removing malodor from the air, particularly from confined spaces are disclosed. Such devices and methods are useful for example for storing and preserving food in closed compartments such as refrigerators. The apparatus and methods utilize baking soda as the odor removing substance, either alone, or in combination with another odor removing substance, which may include activated carbon. In one embodiment, the apparatus has a detachable cartridge member which contains baking soda. In one version of this embodiment, the detachable cartridge member is used with an air moving member that draws air through the detachable cartridge member. In one embodiment, the method involves using a detachable cartridge member with an air moving member in one confined space, and using another cartridge member without the air moving member in another compartment of the confined space. In another embodiment, may also be used for emitting a scent, or other substance (including, but not limited to insecticides, air fresheners, deodorants, aromacology, aromatherapy, or any other odor that acts to condition, modify, or otherwise charge the atmosphere or to modify the environment) into the air.

Abstract translation: 公开了用于从空气中除去恶臭的装置和方法，特别是从密闭空间中去除恶臭。 这种装置和方法可用于例如用于在诸如冰箱的封闭隔室中储存和保存食物。 该装置和方法单独使用小苏打作为除臭物质，或者与可以包括活性炭的另一除臭物质组合使用。 在一个实施例中，该装置具有包含小苏打的可拆卸的盒构件。 在该实施例的一个版本中，可拆卸的盒构件与空气移动构件一起使用，空气移动构件通过可拆卸的盒构件吸入空气。 在一个实施例中，该方法包括在一个密闭的空间中使用具有空气移动构件的可拆卸的盒构件，并且在密闭空间的另一隔室中使用没有空气移动构件的另一个盒构件。 在另一个实施方案中，还可以用于发出香味或其它物质（包括但不限于杀虫剂，空气清新剂，除臭剂，芳香剂，芳香疗法或用于调节，改变或以其他方式对气氛充电的任何其它气味 或修改环境）进入空气。

公开(公告)号：US20080178490A1

公开(公告)日：2008-07-31

申请号：US12000741

申请日：2007-12-17

Applicant: Masahiro Matsunaga ,  Koichi Setoyama ,  Yutaka Kataoka ,  Hiroaki Matsui ,  Hiroshi Matsunaga ,  Takeshi Fujiwara

Inventor： Masahiro Matsunaga ,  Koichi Setoyama ,  Yutaka Kataoka ,  Hiroaki Matsui ,  Hiroshi Matsunaga ,  Takeshi Fujiwara

IPC: B01J3/00

CPC classification number: F26B7/00 ,  F26B21/14 ,  F26B2210/16

Abstract: A method for drying lumber in a short time with less use of energy. The method of drying lumber includes: enclosing lumber in a batch container having a pressure release valve; filling fluid into the batch container under pressure; maintaining a temperature and a pressure at or above a critical point of the fluid for a certain period of time; and then opening the pressure release valve of the batch container to reduce the internal pressure to atmospheric pressure.

Abstract translation: 一种在短时间内干燥木材的方法，较少使用能量。 干燥木材的方法包括：将木材包封在具有压力释放阀的批量容器中; 在压力下将液体填充到批量容器中; 保持温度和压力等于或高于流体的临界点一段时间; 然后打开批量容器的压力释放阀，以将内部压力降低至大气压力。

公开(公告)号：US20080006518A1

公开(公告)日：2008-01-10

申请号：US11572509

申请日：2005-07-20

Applicant: Mikio Shimojo ,  Kazunobu Inoue ,  Masao Tsurui ,  Yoshinori Suto ,  Tsutomu Katagiri ,  Koji Tamura ,  Fujio Tsuchiya ,  Katsuaki Osato

Inventor： Mikio Shimojo ,  Kazunobu Inoue ,  Masao Tsurui ,  Yoshinori Suto ,  Tsutomu Katagiri ,  Koji Tamura ,  Fujio Tsuchiya ,  Katsuaki Osato

IPC: C10B53/02 ,  B01J3/00 ,  C10B57/02 ,  B09B3/00

CPC classification number: C10B57/02 ,  C10B53/02 ,  C10L5/44 ,  C10L9/00 ,  C10L9/086 ,  Y02E50/10 ,  Y02E50/14 ,  Y02E50/30

Abstract: In the process for reforming a biomass in accordance with the present invention, a mixture of a biomass and water as a raw material is compressed by a compressing pump 2 to be deposited into the inlet side of a circulating pump 43 in a primary reactor 41. The mixture is discharged from the circulating pump 43, conveyed to a heater 45, and then heated at a temperature ranging from 200 to 260° C., and sent to a reacting bath 47. In the reacting bath 47, hemicellulose contained in the biomass dissolves in hot water and subjected to a carbonizing reaction. The mixture derived from the primary reactor 41 is deposited in the inlet side of a circulating pump 44 of a secondary reactor 42, and sent to a heater 46, heated here at a temperature ranging from 270 to 330° C., and sent to the reacting bath 47. In the reacting bath 47, cellulose contained in the biomass dissolves in hot water, and is subjected to a carbonizing reaction.

Abstract translation: 在根据本发明的重整生物质的方法中，作为原料的生物质和水的混合物通过压缩泵2压缩以沉积到初级反应器41中的循环泵43的入口侧。 混合物从循环泵43排出，输送到加热器45，然后在200-260℃的温度下加热，并送到反应槽47。 在反应槽47中，生物质中所含的半纤维素溶解在热水中并进行碳化反应。 来自初级反应器41的混合物沉积在二级反应器42的循环泵44的入口侧，并送到加热器46，加热器46在这里在270-330℃的温度范围内加热并送到 反应浴47。 在反应槽47中，生物质中所含的纤维素溶解在热水中，进行碳化反应。

公开(公告)号：US20070289214A1

公开(公告)日：2007-12-20

申请号：US11455524

申请日：2006-06-19

Applicant: Michael S. Briesch ,  Juan P. Gutierrez

Inventor： Michael S. Briesch ,  Juan P. Gutierrez

IPC: B01J3/00 ,  B01J8/06 ,  B01J8/00

CPC classification number: B01J8/067 ,  B01J2208/00212 ,  B01J2208/00309 ,  B01J2219/00006 ,  C01B3/323 ,  C01B3/384 ,  C01B2203/06 ,  C01B2203/0838 ,  C01B2203/0894 ,  C01B2203/1058 ,  C01B2203/1223 ,  C01B2203/1229 ,  C01B2203/1241 ,  C10J3/463 ,  C10J3/466 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10K3/00 ,  F01K23/067 ,  Y02E20/16 ,  Y02E20/18

Abstract: A system and method for producing multiple syngas products. In one embodiment (FIG. 5) a syngas producing system (200) includes a gasifier (210) and a hydrocarbon steam reformer (226). The gasifier (210) is configured to react a solid or liquid carbonaceous material (212) and provide a first syngas product (222). The reformer (226) is coupled to receive sensible heat from the first syngas product (222) and drive an endothermic reaction in which a second syngas product (238) is produced from a liquid or gaseous hydrocarbon supply (150). In a method of processing fuel, a solid or liquid carbonaceous material (212) is provided to a gasifier (210) in the form of a slurry, which is converted into a first syngas product (222) in an exothermic reaction. A liquid or gaseous hydrocarbon supply (150) receives sufficient sensible heat generated during the exothermic reaction to convert the liquid or gaseous hydrocarbon supply (150) into a second syngas product (238).

Abstract translation: 一种生产多种合成气产品的系统和方法。 在一个实施方案（图5）中，合成气生产系统（200）包括气化器（210）和烃蒸汽重整器（226）。 气化器（210）构造成使固体或液体碳质材料（212）反应并提供第一合成气产物（222）。 重整器（226）联接以接收来自第一合成气产物（222）的显热，并驱动其中由液态或气态碳氢化合物供应源（150）产生第二合成气产物（238）的吸热反应。 在处理燃料的方法中，将固体或液体碳质材料（212）以浆料形式提供给气化器（210），其在放热反应中转化为第一合成气产物（222）。 液体或气态烃供应源（150）在放热反应期间产生足够的显热，以将液态或气态碳氢化合物供应（150）转化成第二合成气产物（238）。

公开(公告)号：US07192460B2

公开(公告)日：2007-03-20

申请号：US10376367

申请日：2003-02-28

Applicant: Jeroen Valensa

Inventor： Jeroen Valensa

IPC: B01J3/00

CPC classification number: F28D7/1615 ,  B01J19/249 ,  B01J2219/2453 ,  B01J2219/2459 ,  B01J2219/2462 ,  B01J2219/2495 ,  C01B3/583 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/146 ,  F28D2021/0043 ,  H01M8/0612 ,  H01M8/0662 ,  H01M8/0668 ,  H01M8/1007

Abstract: A cooling system (10) is provided for use with a fuel processing subsystem (12) for reducing a level of carbon monoxide in a reformate flow (14) for a proton exchange membrane fuel cell system (16). The fuel processing subsystem (12) includes first and second preferential oxidizers (18, 20) to oxidize the carbon monoxide carried in the reformate flow. The reformate cooling system (10) includes a coolant flow path (30), a reformate flow path (32), and first, second, third, and fourth heat exchanger core portions (34, 36, 38, 40). The core portions (36–40) are arranged in numbered sequence along the reformate flow path (32) with the first and second core portions (34, 36) located upstream of the first preferential oxidizer (18), and the third and fourth core portions (38, 40) located downstream of the first preferential oxidizer (18) and upstream of the second preferential oxidizer (20). The first and second core portions (34, 36) are arranged in numbered sequence along the coolant flow path (30), one of the third and fourth core portions (38, 40) is arranged upstream of the first core portion (34) along the coolant flow path (30), and the other of the third and fourth core portions (38, 40) is arranged downstream of the second core portion along the coolant flow path (30).

Abstract translation: 提供了一种用于燃料处理子系统（12）的冷却系统（10），用于降低用于质子交换膜燃料电池系统（16）的重整产品流（14）中的一氧化碳含量。 燃料处理子系统（12）包括第一和第二优先氧化剂（18,20），以氧化重整产品流中携带的一氧化碳。 重整油冷却系统（10）包括冷却剂流路（30），重整油流路（32）以及第一，第二，第三和第四热交换器芯部（34,36,38,40）。 核心部分（36-40）沿着重整物流动路径（32）以编号的顺序排列，第一和第二核心部分（34,36）位于第一优先氧化剂（18）的上游，第三和第四核心 位于第一优先氧化器（18）下游和第二优先氧化器（20）上游的部分（38,40）。 第一和第二芯部分（34,36）沿着冷却剂流动路径（30）以数量的顺序排列，第三和第四芯部分（38,40）之一沿着第一芯部分（34）的上游布置 冷却剂流动路径30以及第三和第四芯部38,40中的另一个沿着冷却剂流动通道30设置在第二芯部的下游。

公开(公告)号：US07175817B2

公开(公告)日：2007-02-13

申请号：US10634380

申请日：2003-08-04

Applicant: Yoshihiro Kawamura ,  Naotsugu Ogura

Inventor： Yoshihiro Kawamura ,  Naotsugu Ogura

IPC: B01J8/04 ,  B01J3/00 ,  C10L3/00

CPC classification number: H01M8/0267 ,  B01J19/0093 ,  B01J2219/00783 ,  B01J2219/00835 ,  B01J2219/00873 ,  C01B3/323 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/1076 ,  C01B2203/1223 ,  C01B2203/1288 ,  H01M8/0263 ,  H01M8/0271 ,  H01M8/04074 ,  Y02P20/128 ,  Y02P20/52 ,  Y10T117/10

Abstract: The compact chemical reactor includes a first substrate, a second substrate attached to the first substrate. A micro flow path is defined between the first substrate and the second substrate. A thin film heater provided in the flow path.

Abstract translation: 紧凑型化学反应器包括第一基板，附接到第一基板的第二基板。 在第一衬底和第二衬底之间限定微流动路径。 设置在流路中的薄膜加热器。

公开(公告)号：US07172736B2

公开(公告)日：2007-02-06

申请号：US10628924

申请日：2003-07-28

Applicant: Yoshihiro Kawamura ,  Naotsugu Ogura

Inventor： Yoshihiro Kawamura ,  Naotsugu Ogura

IPC: B01J8/04 ,  B01J3/00 ,  C10L3/00

CPC classification number: C01B3/48 ,  B01J19/0093 ,  B01J2219/00783 ,  B01J2219/00822 ,  B01J2219/00828 ,  B01J2219/00835 ,  B01J2219/0086 ,  C01B3/323 ,  C01B2203/00 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/085 ,  C01B2203/0866 ,  C01B2203/1035 ,  C01B2203/1041 ,  C01B2203/1076 ,  C01B2203/1205 ,  C01B2203/1223 ,  C01B2203/1288 ,  C01B2203/82 ,  C01B2203/84 ,  H01M8/0618 ,  Y02P70/56

Abstract: A compact chemical reactor has a first substrate. A catalyst layer is provided on an inner surface of a groove formed in a first surface of the first substrate. A second substrate, in which a concave portion to receive a portion of the catalyst layer is formed on a surface opposite to the first surface of the substrate, contacts the first substrate on the opposite surface.

Abstract translation: 紧凑的化学反应器具有第一衬底。 催化剂层设置在形成在第一基板的第一表面中的槽的内表面上。 第二基板，其中，在与基板的第一表面相对的表面上形成有用于接收催化剂层的一部分的凹部与相对表面上的第一基板接触。

公开(公告)号：US07037473B1

公开(公告)日：2006-05-02

申请号：US09486784

申请日：1998-07-16

Applicant: Ralf Donner ,  Dietmar Degenkolb ,  Manfred Schingnitz

Inventor： Ralf Donner ,  Dietmar Degenkolb ,  Manfred Schingnitz

IPC: B01J3/00

CPC classification number: F28F9/00 ,  C10J3/485 ,  C10J3/74 ,  C10J3/78 ,  C10J2300/1223 ,  C10K1/08 ,  F28F2270/00

Abstract: An appliance for the gasification of carbon- and ash-containing fuel, residual and waste materials using an oxygen-containing oxidizing agent at temperatures above the melting point of the inorganic fractions, in a reaction chamber which is designed as an entrained-bed reactor, at pressures between atmospheric pressure and 80 bar, preferably between atmospheric pressure and 30 bar, the contour of the reaction chamber being delimited by a cooled reactor wall. The cooled reactor wall having the following structure, from the outside inward: a pressure shell, a cooling wall, a water-cooled gap between the pressure shell and the cooling wall, a ceramic protection for the cooling wall, and a layer of slag. The pressure and temperature of the cooling gap between the pressure shell and the cooling wall is controlled in such a way that it can be operated above and below the boiling point of the cooling water. The pressure in the cooling gap is higher than the pressure in the gasification chamber.

Abstract translation: 在设计为夹带床反应器的反应室中，用于在高于无机部分的熔点的温度下使用含氧氧化剂气化含碳和灰分燃料，残余物和废物的装置， 在大气压和80巴之间的压力下，优选在大气压和30巴之间，反应室的轮廓由冷却的反应器壁界定。 冷却的反应器壁具有以下结构：从外部向内：压力壳，冷却壁，压力壳和冷却壁之间的水冷间隙，用于冷却壁的陶瓷保护层和一层熔渣。 控制压力壳和冷却壁之间的冷却间隙的压力和温度，使其能够在冷却水的沸点之上和之下操作。 冷却间隙中的压力高于气化室内的压力。