公开(公告)号：US09669374B2

公开(公告)日：2017-06-06

申请号：US14459309

申请日：2014-08-13

Applicant: McAlister Technologies, LLC

Inventor： Roy Edward McAlister

IPC: B01J10/00 ,  C07C31/04 ,  C07C2/00 ,  C10L3/00 ,  F17D3/01 ,  C10G2/00 ,  C10G3/00 ,  B01J7/00 ,  F03G7/04

CPC classification number: B01J10/00 ,  B01J7/00 ,  C07C2/00 ,  C07C31/04 ,  C10G2/00 ,  C10G3/00 ,  C10L3/00 ,  F03G7/04 ,  F17D3/01 ,  Y02P30/10 ,  Y02P30/20 ,  Y10T137/0318 ,  Y10T137/402

Abstract: Techniques, systems and material are disclosed for transport of energy and/or materials. In one aspect, a method includes generating gaseous fuel (e.g., from biomass dissociation) at a first location of a low elevation. The gaseous fuel can be self-transported in a pipeline to a second location at a higher elevation than the first location by traveling from the first location to the second location without adding energy of pressure. A liquid fuel can be generated at the second location of higher elevation by reacting the gaseous fuel with at least one of a carbon donor, a nitrogen donor, and an oxygen donor harvested from industrial waste. The liquid fuel can be delivered to a third location of a lower elevation than the second location while providing pressure or kinetic energy.

公开(公告)号：US20170043742A1

公开(公告)日：2017-02-16

申请号：US15306411

申请日：2015-04-20

Applicant: NIPPON KAYAKU KABUSHIKI KAISHA

Inventor： Shinya UEDA ,  Yoshitaka IWAI ,  Satoshi OHSUGI ,  Masahiro YAMAGUCHI

IPC: B60R21/264

CPC classification number: B60R21/2644 ,  B01J7/00 ,  B60R21/264

Abstract: A gas generator includes a cylindrical partition wall portion including a plurality of gas passage holes through which a gas generated as a result of burning of a gas generating agent passes. Two sealing tapes in a form of a band are contiguously bonded to the partition wall portion such that a direction of extension thereof matches with a circumferential direction of the partition wall portion and each one of a pair of end portions located in each direction of extension is layered on an adjacent sealing tape. The gas passage hole is closed by a layered bonding region which is a portion where adjacent sealing tapes are layered on each other, and the gas passage hole is closed by a non-layered bonding region which is a portion where adjacent sealing tapes are not layered on each other.

Abstract translation: 气体发生器包括：圆筒形分隔壁部分，包括多个气体通过孔，由气体发生剂燃烧产生的气体通过该气体通道孔。 带状形式的两个密封带被连续地结合到隔壁部分，使得其延伸方向与分隔壁部分的圆周方向一致，并且位于每个延伸方向上的一对端部中的每一个是 层叠在相邻的密封带上。 气体通过孔被相邻的密封带彼此层叠的部分的层叠接合区域封闭，并且气体通过孔被相邻的密封带不层叠的部分的非层状接合区域封闭 彼此之间

公开(公告)号：US09567226B2

公开(公告)日：2017-02-14

申请号：US14193323

申请日：2014-02-28

Applicant: Mallinckrodt Hospital Products IP Limited

Inventor： Tammer Mosa ,  Gerard T. Taylor

IPC: B01J19/00 ,  B01J19/24 ,  C01B31/00 ,  C01B31/18

CPC classification number: C01B31/18 ,  B01D53/1487 ,  B01D2252/10 ,  B01J7/00 ,  B01J19/00 ,  C01B32/40 ,  C01P2006/80

Abstract: Apparatus for making at least 99.99% pure gaseous carbon monoxide comprising a reactor vessel, a cooling vessel, a compressor and optionally a chiller, a dryer or a pressurized cylinder. The chiller can be adapted to chill the scrubbed carbon monoxide gas to a temperature in the range of −30° C. to −90° C. to remove impurities. The dryer can be adapted to dry the scrubbed gaseous carbon monoxide to remove impurities. The pressurized cylinder can be adapted to store the compressed gaseous carbon monoxide.

Abstract translation: 用于制造至少99.99％的纯气体一氧化碳的装置，包括反应器容器，冷却容器，压缩机和任选的冷却器，干燥器或加压缸。 冷却器可以适于将洗涤的一氧化碳气体冷却至-30℃至-90℃的温度以除去杂质。 干燥器可以适于干燥洗涤的气态一氧化碳以除去杂质。 加压缸可适于储存压缩的气态一氧化碳。

公开(公告)号：US20170001176A1

公开(公告)日：2017-01-05

申请号：US15191844

申请日：2016-06-24

Applicant: SABIC Global Technologies B.V.

Inventor： Lawrence D'Souza ,  Vinu Viswanath ,  Jessica Scaranto ,  Ugo Ravon

IPC: B01J23/89 ,  B01J23/20 ,  B01J23/18 ,  B01J23/10 ,  C01B3/40 ,  B01J35/00 ,  B01J35/02 ,  B01J37/02 ,  B01J37/08 ,  B01J7/00 ,  B01J23/755 ,  B01J21/04

CPC classification number: B01J23/892 ,  B01J7/00 ,  B01J21/04 ,  B01J23/10 ,  B01J23/18 ,  B01J23/20 ,  B01J23/755 ,  B01J23/8871 ,  B01J23/8874 ,  B01J23/8877 ,  B01J23/894 ,  B01J23/896 ,  B01J23/898 ,  B01J35/0006 ,  B01J35/008 ,  B01J35/023 ,  B01J35/026 ,  B01J37/0201 ,  B01J37/0205 ,  B01J37/0207 ,  B01J37/0236 ,  B01J37/088 ,  C01B3/40 ,  C01B2203/0227 ,  C01B2203/0238 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/107 ,  C01B2203/1082 ,  C01B2203/1247 ,  Y02P20/52

Abstract: Disclosed are catalysts capable of catalyzing the dry reforming of methane. The catalysts have a core-shell structure with the shell surrounding the core. The shell has a redox-metal oxide phase that includes a metal dopant incorporated into the lattice framework of the redox-metal oxide phase. An active metal(s) is deposited on the surface of the shell.

Abstract translation: 公开了能够催化甲烷干重整的催化剂。 催化剂具有核壳结构，壳体围绕核心。 壳具有氧化还原金属氧化物相，其包括掺入氧化还原金属氧化物相的晶格框架中的金属掺杂剂。 活性金属沉积在壳体的表面上。

公开(公告)号：US20160368775A1

公开(公告)日：2016-12-22

申请号：US15253193

申请日：2016-08-31

Applicant: SO SPARK LTD.

Inventor： Pinchas SHALEV

IPC: C01B31/20 ,  B01J19/12 ,  A23L2/54 ,  B01J7/00

CPC classification number: B67D1/0057 ,  A23L2/54 ,  A23V2002/00 ,  B01J7/00 ,  B01J19/126 ,  B65D81/3453 ,  B65D2581/3428 ,  B65D2581/3494 ,  C01B32/50

Abstract: Carbon dioxide, such as may be used for a carbonated beverage, is produced by microwave thermal decomposition of a starting material. An apparatus for the process includes a microwave generator, a microwave chamber, a capsule received in the chamber containing starting material(s) and one or more channel(s) for recovering CO2 generated in the process.

公开(公告)号：US09522371B2

公开(公告)日：2016-12-20

申请号：US13465798

申请日：2012-05-07

Applicant: Stephen A. Marsh ,  Donald M. Parker ,  Peter N. Pintauro

Inventor： Stephen A. Marsh ,  Donald M. Parker ,  Peter N. Pintauro

IPC: B01J7/00 ,  C01B3/36 ,  C01B3/06 ,  C01B13/02

CPC classification number: B01J7/00 ,  C01B3/065 ,  C01B13/02 ,  Y02E60/362

Abstract: A self-regulating gas generator that, in response to gas demand, supplies and automatically adjusts the amount of gas (e.g., hydrogen or oxygen) catalytically generated in a chemical supply chamber from an appropriate chemical supply, such as a chemical solution, gas dissolved in liquid, or mixture. In some embodiments, the gas generator may employ a piston, rotating rod, or other element(s) to expose the chemical supply to the catalyst in controlled amounts. In another embodiment, the self-regulating gas generator uses bang-bang control, with the element(s) exposing a catalyst, contained within the chemical supply chamber, to the chemical supply in ON and OFF states according to a self-adjusting duty cycle, thereby generating and outputting the gas in an orientation-independent manner. The gas generator may be used to provide gas for various gas consuming devices, such as a fuel cell, torch, or oxygen respiratory devices.

Abstract translation: 一种自我调节气体发生器，其响应于天然气需求，供应并自动调节化学品供应室中催化产生的气体（例如氢气或氧气）的数量，从适当的化学物质（如化学溶液），溶解的气体 在液体或混合物中。 在一些实施方案中，气体发生器可以使用活塞，旋转杆或其它元件以以受控的量暴露出催化剂的化学物质。 在另一个实施例中，自调节气体发生器使用爆炸控制，其中包含在化学物质供应室内的催化剂的元素根据自调节占空比在ON和OFF状态下进入化学物质供应 ，从而以取向不依赖的方式产生和输出气体。 气体发生器可用于为各种燃气消耗装置（例如燃料电池，割炬或氧气呼吸装置）提供气体。

公开(公告)号：US09486477B2

公开(公告)日：2016-11-08

申请号：US14803308

申请日：2015-07-20

Applicant: SYK TECHNOLOGIES, LLC

Inventor： J. W. Randolph Miller ,  Christie W. Jones

IPC: B01J7/00 ,  A61K33/00 ,  C01B21/24

CPC classification number: B01J7/00 ,  A61K33/00 ,  A61M16/12 ,  B01J2219/00121 ,  B01J2219/00135 ,  C01B21/24

Abstract: An apparatus to generate nitric oxide is disclosed in one embodiment in accordance with the invention as including a heat source and a vessel containing the heat source. A tablet may be placed within the vessel such that it is in thermal communication with the heat source to receive heat therefrom. The tablet may contain reactants that are substantially non-deliquescent and form nitric oxide in response to heat from the heat source.

公开(公告)号：US20160289141A1

公开(公告)日：2016-10-06

申请号：US15038205

申请日：2014-11-20

Applicant: BASF SE

Inventor： Kati BACHMANN ,  Friedrich GLENK ,  Grigorios KOLIOS

IPC: C07C2/76 ,  C01B3/38 ,  B01J7/00 ,  B01J19/00 ,  B01J29/48 ,  B01J23/62 ,  B01J21/04 ,  B01J21/06 ,  B01J23/26 ,  B01J23/08 ,  B01J29/18 ,  B01J29/70 ,  B01J29/85 ,  B01J27/232 ,  B01J23/745 ,  B01J23/755 ,  B01J23/02 ,  B01J23/00 ,  C07C5/333 ,  C07C5/03 ,  C07C5/10 ,  C01B3/40

CPC classification number: C07C2/76 ,  B01J7/00 ,  B01J8/062 ,  B01J8/065 ,  B01J8/1809 ,  B01J8/1827 ,  B01J8/1836 ,  B01J8/1872 ,  B01J8/26 ,  B01J19/0046 ,  B01J21/04 ,  B01J21/063 ,  B01J21/066 ,  B01J23/005 ,  B01J23/02 ,  B01J23/08 ,  B01J23/26 ,  B01J23/626 ,  B01J23/745 ,  B01J23/755 ,  B01J27/232 ,  B01J29/18 ,  B01J29/48 ,  B01J29/70 ,  B01J29/85 ,  B01J29/90 ,  B01J38/10 ,  B01J2208/00238 ,  B01J2208/00504 ,  B01J2208/00557 ,  B01J2208/06 ,  B01J2219/00495 ,  B01J2219/00585 ,  B01J2219/00594 ,  B01J2219/0072 ,  B01J2219/00756 ,  B01J2219/185 ,  C01B3/384 ,  C01B3/40 ,  C01B3/44 ,  C01B2203/0233 ,  C01B2203/0238 ,  C01B2203/0833 ,  C01B2203/1058 ,  C01B2203/1082 ,  C01B2203/1241 ,  C01B2203/141 ,  C07C5/03 ,  C07C5/10 ,  C07C5/3332 ,  C07C5/35 ,  C07C5/367 ,  C07C2521/04 ,  C07C2521/06 ,  C07C2523/04 ,  C07C2523/08 ,  C07C2523/14 ,  C07C2523/26 ,  C07C2523/42 ,  C07C2523/62 ,  C07C2523/86 ,  C07C2529/18 ,  C07C2529/46 ,  C07C2529/48 ,  C07C2529/85 ,  Y02P20/52 ,  Y02P20/584 ,  C07C15/04 ,  C07C15/46 ,  C07C11/06 ,  C07C11/08 ,  C07C11/09 ,  C07C11/22

Abstract: The present invention relates to a method for carrying out endothermic reactions comprising the method steps of:a) externally heating at least two reaction tubes (5), wherein the reaction tubes (5) have been arranged vertically in a heating chamber (3) and each of the reaction tubes (5) has been at least partially packed with a fluidizable material,b) introducing at least one gaseous reactant (R) into the reaction tubes (5),c) forming a fluidized bed (7) in the reaction tubes (5), d) carrying out the endothermic reaction in the reaction tubes (5) at a first temperature (T1) and a first pressure (P1), wherein the reaction volume has been distributed over at least two of the reaction tubes (5), and e) discharging the reaction product (P) from the reaction tubes (5).The present invention further relates to an apparatus (1) for carrying out endothermic reactions comprising at least one heating chamber (3), at least two reaction tubes (5), wherein the reaction tubes (5) have been arranged vertically in the heating chamber (3) and each of the reaction tubes (5) comprises an at least partial packing of a fluidizable material, at least one entry point (9) for gaseous reactants (R) for each reaction tube (5), at least one exit point (11) for reaction products (P) for each reaction tube (5) and at least one heating apparatus (13) for externally heating the reaction tubes (5).The present invention further provides for the use of the apparatus (1) according to the invention for the non-oxidative dehydroaromatization of C1 to C4 aliphatics.

Abstract translation: 本发明还提供了根据本发明的装置（1）用于C1至C4脂族体的非氧化脱氢芳化作用的用途。

公开(公告)号：US20160289067A1

公开(公告)日：2016-10-06

申请号：US15177821

申请日：2016-06-09

Applicant: IHI Corporation

Inventor： Yosuke TSUBOI ,  Shintaro ITO

IPC: C01B3/02 ,  C10K3/00 ,  C01B3/50 ,  B01J7/00 ,  B01J19/00

CPC classification number: C01B3/02 ,  B01J7/00 ,  B01J19/0046 ,  B01J2219/00495 ,  B01J2219/0059 ,  B01J2219/00756 ,  C01B3/36 ,  C01B3/50 ,  C01B2203/0255 ,  C01B2203/048 ,  C01B2203/061 ,  C01B2203/0833 ,  C01B2203/1252 ,  C01B2203/142 ,  C01B2203/146 ,  C10J3/00 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/0946 ,  C10J2300/1603 ,  C10K3/005

Abstract: Syngas is alternatingly introduced by a syngas alternating lead-in system through either of one- and the other-end-side heat storage bodies into flow passages in a primary reforming furnace, and oxidant is alternatingly supplied to the syngas by a primary-oxidant alternating supply system. The syngas derived from the primary reforming furnace by a syngas alternating lead-out system is introduced into a secondary reforming furnace to which connected is a secondary-oxidant supply system for supply of oxidant only at alternation in the syngas alternating lead-in and -out systems.

Abstract translation: 合成气通过合成气交替引入系统通过一端和另一端侧储热体交替地引入初级重整炉中的流动通道中，氧化剂通过一次氧化剂交替地交替地供给合成气 供应系统 通过合成气交替引出系统将来自初级重整炉的合成气引入二次转化炉，二次转化炉中连接有辅助氧化剂供应系统，仅在合成气交替引入和输出 系统。

公开(公告)号：US20160271597A1

公开(公告)日：2016-09-22

申请号：US14907598

申请日：2015-07-28

Applicant: Ashim Kumar GHOSH ,  Alla KHANMAMEDOVA ,  Mike MIER ,  Jonathan BANKE ,  SABIC Global Technologies B.V.

Inventor： Ashim Kumar Ghosh ,  Alla Khanmamedova ,  Mike Mier ,  Jonathan Banke

IPC: B01J29/85 ,  C07C1/26 ,  B01J7/00 ,  C01B39/54 ,  B01J35/10

CPC classification number: B01J29/85 ,  B01J7/00 ,  B01J35/002 ,  B01J35/023 ,  B01J35/1061 ,  B01J2229/37 ,  C01B39/54 ,  C07C1/26 ,  C07C2529/85 ,  Y02P20/52 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/06 ,  C07C11/08

Abstract: Disclosed is a method for converting an alkyl halide to an olefin. The method includes contacting a silicoaluminophosphate (SAPO) catalyst with a feed that includes an alkyl halide under reaction conditions sufficient to produce an olefin hydrocarbon product that includes C2 to C4 olefins. The SAPO catalyst has bimodal acidity designated as weak acid sites and strong acid sites. The weak acid concentration is less than 0.55 mmol/g-cat and the total acid concentration is less than 1.5 mmol/g-cat.

Abstract translation: 公开了将烷基卤转化为烯烃的方法。 该方法包括在足以产生包括C 2至C 4烯烃的烯烃产物的反应条件下使硅铝磷酸盐（SAPO）催化剂与包含烷基卤的进料接触。 SAPO催化剂具有指定为弱酸性位点和强酸性位点的双峰酸性。 弱酸浓度小于0.55 mmol / g-cat，总酸浓度小于1.5 mmol / g-cat。