公开(公告)号：US09364812B2

公开(公告)日：2016-06-14

申请号：US13885468

申请日：2011-11-17

Applicant: Alan Paul Watkinson ,  Yong Hua Li ,  Cef Haligva

Inventor： Alan Paul Watkinson ,  Yong Hua Li ,  Cef Haligva

IPC: B01J19/24 ,  C10J3/84 ,  C10J3/48 ,  C10K3/00 ,  B01J6/00 ,  B01J8/02 ,  B01J8/04

CPC classification number: B01J19/24 ,  B01J6/008 ,  B01J8/0207 ,  B01J8/0242 ,  B01J8/0403 ,  B01J8/0446 ,  B01J2219/00006 ,  B01J2219/0004 ,  C10J3/482 ,  C10J3/84 ,  C10J2200/06 ,  C10J2300/0916 ,  C10J2300/0976 ,  C10J2300/12 ,  C10J2300/1606 ,  C10J2300/1637 ,  C10J2300/1807 ,  C10K3/008 ,  Y02P20/145

Abstract: A tar destruction unit for a biomass gasifier is described, comprising a catalyst and/or heating means situated within the free-board section of the gasifier. Also described is a biomass gasifier having such a tar destruction unit.

Abstract translation: 描述了用于生物质气化器的焦油消除单元，其包括位于气化器的空隙部分内的催化剂和/或加热装置。 还描述了具有这种焦油破坏单元的生物质气化器。

公开(公告)号：US09258851B2

公开(公告)日：2016-02-09

申请号：US14409616

申请日：2013-11-13

Applicant: Microwave Chemical Co., Ltd.

Inventor： Yasunori Tsukahara ,  Akinori Ishizuka ,  Yukari Deguchi

IPC: G06F19/00 ,  H05B6/66 ,  G01R21/00 ,  H05B6/64

CPC classification number: H05B6/666 ,  B01J8/001 ,  B01J8/0403 ,  B01J8/0496 ,  B01J19/0013 ,  B01J19/126 ,  B01J19/1862 ,  B01J2208/00442 ,  B01J2219/00063 ,  B01J2219/002 ,  B01J2219/00202 ,  B01J2219/00209 ,  B01J2219/00213 ,  B01J2219/00238 ,  B01J2219/0871 ,  B01J2219/0892 ,  B01J2219/1218 ,  B01J2219/1272 ,  B01J2219/1275 ,  B01J2219/1296 ,  G01R21/00 ,  H05B6/6447 ,  H05B6/705 ,  H05B6/80

Abstract: An information processing apparatus includes: a supplied electric power value accepting unit accepting a supplied electric power value, which is a difference between an electric power value of microwaves incident on a microwave irradiation apparatus and an electric power value of microwaves reflected by the microwave irradiation apparatus; a temperature accepting unit; an electric energy calculating unit calculating an electric energy corresponding to a microwave irradiation time, using the supplied electric power value; a temperature change calculating unit calculating a temperature change corresponding to the microwave irradiation time, using the accepted temperature; a judging unit, using the electric energy, the temperature change, and a relational expression for associating the electric energy and the temperature change, judging whether the relational expression is satisfied within a tolerable range; and an output unit outputting occurrence of an abnormality, when it is judged that the relational expression is not satisfied within the tolerable range.

Abstract translation: 一种信息处理装置，包括：接受作为微波照射装置的微波的电功率值与由微波照射装置反射的微波的电功率值之差的供给电力值的供给电力值接受部 ; 温度接收单元; 电能计算单元，使用所提供的电功率值来计算与微波照射时间相对应的电能; 温度变化计算单元，使用接受的温度来计算与微波照射时间对应的温度变化; 判断单元，使用电能，温度变化和关联表达式来关联电能和温度变化，判断关系表达式是否在容许范围内得到满足; 以及在可容许范围内判断为不满足关系式的情况下，输出发生异常的输出部。

公开(公告)号：US20130044559A1

公开(公告)日：2013-02-21

申请号：US13639342

申请日：2011-04-06

Applicant: Robert Ashe ,  David Morris

Inventor： Robert Ashe ,  David Morris

IPC: B01F11/00 ,  B01F15/06

CPC classification number: B01F11/0077 ,  B01F13/005 ,  B01F13/0057 ,  B01F13/1013 ,  B01F13/1027 ,  B01J8/0403 ,  B01J19/006 ,  B01J19/0066 ,  B01J19/0093 ,  B01J19/1818 ,  B01J19/285 ,  B01J2208/00814 ,  B01J2208/028 ,  B01J2219/00063 ,  B01J2219/00094 ,  B01J2219/00135 ,  B01J2219/00189 ,  B01J2219/002 ,  B01J2219/00238

Abstract: A continuous mixer/reactor and a mixing process are provided in which materials flow in an orderly fashion along the length of a channel (9) and the materials are mixed in a direction transverse to the axis of the channel (9) by the provision of agitator elements (5, 7) within the channel (9) and shaking the channel (9) so that the agitator elements (5, 7) move within the channel (9) in the radial direction of the channel (9).

Abstract translation: 提供连续的混合器/反应器和混合过程，其中材料沿着通道（9）的长度以有序的方式流动，并且材料通过提供通道（9）的横向于通道（9）的轴线的方向混合 在通道（9）内的搅拌器元件（5,7）和振动通道（9），使得搅拌器元件（5,7）在通道（9）的径向方向上在通道（9）内移动。

公开(公告)号：US07416570B2

公开(公告)日：2008-08-26

申请号：US10545092

申请日：2004-02-12

Applicant: Motohiro Suzuki ,  Tomonori Asou ,  Yuji Mukai ,  Kunihiro Ukai ,  Akira Maenishi

Inventor： Motohiro Suzuki ,  Tomonori Asou ,  Yuji Mukai ,  Kunihiro Ukai ,  Akira Maenishi

IPC: B01J8/00 ,  B01J7/00 ,  B01J19/00 ,  C01B3/36 ,  H01M8/18 ,  H01M8/00 ,  F28F3/00

CPC classification number: H01M8/0631 ,  B01J8/0257 ,  B01J8/0285 ,  B01J8/0403 ,  B01J8/0465 ,  B01J8/0496 ,  B01J23/63 ,  B01J2208/00309 ,  B01J2208/0053 ,  C01B3/384 ,  C01B3/48 ,  C01B2203/00 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/066 ,  C01B2203/0844 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/82 ,  H01M8/0668 ,  Y02P20/52

Abstract: A body of a hydrogen generator includes a reformer configured to generate a reformed gas mainly containing hydrogen, a material passage configured to supply a reforming material, which is a material for a reforming reaction, to the reformer, a shifter configured to convert CO contained in a reformed gas obtained from the reformer into CO2, a reformed gas passage configured to supply the reformed gas obtained from the reformer to the shifter, and a passage for the shifted gas obtained from the shifter. The shifted gas passage and the material passage are adjacent to each other with a shared horizontal wall interposed therebetween, and thereby, heat from the shifted gas and radiant heat from the downstream end face of the shifter are transferred to the reforming material that travels in the material passage.

Abstract translation: 一种氢发生器，其特征在于，包括：重整器，其配置成生成主要含有氢的重整气体，构成为向所述重整器供给作为重整反应的材料的重整材料的材料通路， 从重整器获得的重整气体转化为CO 2，将从重整器获得的重整气体供给到换档器的重整气体通道，以及从换档器得到的换流气体的通路。 移位的气体通道和材料通道彼此相邻，并且其间具有共用的水平壁，从而来自移动的气体的热量和来自换挡器的下游端面的辐射热被传递到在 物质通道

公开(公告)号：US20040254402A1

公开(公告)日：2004-12-16

申请号：US10312520

申请日：2003-07-03

Inventor： Giancarlo Sioli

IPC: C07C045/29

CPC classification number: B01J8/067 ,  B01J8/0403 ,  B01J8/0419 ,  B01J8/0446 ,  C07C45/38 ,  C07C47/04

Abstract: A method for formaldehyde production through catalytic oxidation of methanol, comprising the steps of feeding to a first oxidation catalytic bed (2) a gas flow comprising methanol and oxygen at a predetermined crossing linear flow rate, obtaining at the outlet of said first catalytic bed (2) a flow of gaseous reaction products comprising unreacted methanol, and feeding the flow of gaseous products to a second oxidation catalytic bed (6) is distinguished by the fact that the flow of gaseous reaction products comprising unreacted methanol is fed to the second catalytic bed (6) with a crossing linear flow rate substantially equal to said predetermined first catalytic bed (2) feeding flow rate.

Abstract translation: 一种通过甲醇的催化氧化生产甲醛的方法，包括以下步骤：以预定的交联线性流速向第一氧化催化床（2）供给包含甲醇和氧气的气流，在所述第一催化床的出口 2）包含未反应的甲醇的气态反应产物流并将气态产物流送入第二氧化催化剂床（6）的特征在于将包含未反应的甲醇的气态反应产物的流量送入第二催化床 （6），其交叉线性流速基本上等于所述预定的第一催化床（2）进料流量。

公开(公告)号：US06814944B1

公开(公告)日：2004-11-09

申请号：US09914378

申请日：2001-08-28

Applicant: Nobuki Matsui ,  Shuji Ikegami ,  Yasunori Okamoto ,  Kazuo Yonemoto

Inventor： Nobuki Matsui ,  Shuji Ikegami ,  Yasunori Okamoto ,  Kazuo Yonemoto

IPC: B01J1000

CPC classification number: H01M8/0631 ,  B01J8/0214 ,  B01J8/0228 ,  B01J8/025 ,  B01J8/0403 ,  B01J8/0446 ,  B01J8/0453 ,  B01J8/0496 ,  B01J19/2485 ,  B01J19/249 ,  B01J23/40 ,  B01J35/04 ,  B01J2208/00185 ,  B01J2208/00221 ,  B01J2208/00309 ,  B01J2208/00495 ,  B01J2208/0053 ,  B01J2208/00716 ,  B01J2219/00006 ,  B01J2219/2453 ,  B01J2219/2455 ,  B01J2219/2465 ,  B01J2219/2479 ,  B01J2219/2485 ,  C01B3/16 ,  C01B3/386 ,  C01B3/48 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/0805 ,  C01B2203/0844 ,  C01B2203/0883 ,  C01B2203/1023 ,  C01B2203/1035 ,  C01B2203/1064 ,  C01B2203/1082 ,  C01B2203/1241 ,  C01B2203/146 ,  C01B2203/1604 ,  C01B2203/82 ,  H01M8/0662 ,  Y02P20/52

Abstract: Shift conversion of hydrogen-rich reformed gas produced by reaction including partial oxidation of feed gas in a reforming reaction section (6) is made by its water gas shift reaction with shift conversion catalyst in a shift reaction section (10) in order to reduce CO contained in the reformed gas and enhance the yield of hydrogen. In this case, for the purpose of enabling high-temperature reformed gas from the reforming reaction section (6) to undergo the shift conversion as it is and thereby simplifying the construction of a shift conversion unit, the reformed gas from the reforming reaction section (6) is introduced directly into a reformed gas passage (11) of the shift reaction section (10) and thereby undergoes the shift reaction while heat-exchanging with the feed gas.

Abstract translation: 通过在转化反应部（10）中通过与换档转化催化剂的水煤气变换反应来进行在重整反应部（6）中的进料气体的部分氧化的反应而产生的富氢重整气的转换，以减少CO 包含在重整气中并提高氢的产率。 在这种情况下，为了使来自重整反应部（6）的高温重整气体原样进行变换转换，从而简化变换转换部的结构，来自重整反应部（ 6）直接引入变换反应部（10）的重整气体通道（11）中，由此在与进料气体进行热交换的同时进行变换反应。

公开(公告)号：US06764660B1

公开(公告)日：2004-07-20

申请号：US09593789

申请日：2000-06-14

Applicant: William Wiede, Jr. ,  Kevin J. Brandner ,  Bruce A. Briggs ,  Donald E. Felch ,  Constante P. Tagamolila

Inventor： William Wiede, Jr. ,  Kevin J. Brandner ,  Bruce A. Briggs ,  Donald E. Felch ,  Constante P. Tagamolila

IPC: F28D700

CPC classification number: C10G35/04 ,  B01J8/0207 ,  B01J8/0285 ,  B01J8/0403 ,  B01J8/0496 ,  B01J8/087 ,  B01J8/125 ,  B01J19/32 ,  B01J2208/022 ,  B01J2219/32466 ,  B01J2219/32475 ,  C07C5/333 ,  Y02P20/582 ,  Y10S585/911 ,  Y10S585/912 ,  C07C15/46

Abstract: A process and apparatus for contacting reactants with a particulate catalyst while indirectly heating the reactants with a heat exchange medium improves temperature control by using an intermediate heat exchange fluid and system to prevent overheating of reactants and maintain parallel heating characteristics through multiple reaction-heat exchange zones. The internal flow path minimizes the circulation of the reaction zone heat exchange fluid by incorporating interstage reheating of the reaction zone heat exchange fluid as it passes in series flow. A particularly useful application of the process and apparatus is in the dehydrogenation of ethylbenzene to produce styrene. The process and apparatus can also be used with simultaneous exchange of catalyst particles by an operation that restricts reactant flow while moving catalyst through reaction stacks in which the reactant flow has been restricted.

Abstract translation: 用于使反应物与颗粒催化剂接触的方法和装置，同时用热交换介质间接加热反应物通过使用中间热交换流体和系统来改善温度控制，以防止反应物过热并通过多个反应 - 热交换区保持平行加热特性 。 内部流路通过在反应区热交换流体串联流动的同时加入反应区热交换流体的级间再加热来使反应区热交换流体的循环最小化。 该方法和装置的特别有用的应用是乙苯的脱氢生产苯乙烯。 该方法和装置还可以通过在催化剂通过其中反应物流被限制的反应堆中移动的同时限制反应物流动的操作同时交换催化剂颗粒。

公开(公告)号：US20020085966A1

公开(公告)日：2002-07-04

申请号：US09988388

申请日：2001-11-19

Inventor： Bruno Motzet ,  Alois Tischler

IPC: F28D001/00 ,  F28F007/00 ,  B01J007/00

CPC classification number: B01J8/0496 ,  B01B1/005 ,  B01J8/0207 ,  B01J8/0285 ,  B01J8/0403 ,  B01J2208/0053 ,  B01J2219/00063 ,  B01J2219/00117 ,  B01J2219/00157 ,  B01J2219/00164 ,  B01J2219/00186 ,  B01J2219/00202 ,  B01J2219/00213 ,  B01J2219/00231 ,  C01B3/323 ,  C01B3/38 ,  C01B2203/02 ,  C01B2203/0233 ,  C01B2203/066 ,  C01B2203/0811 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/0833 ,  C01B2203/0844 ,  C01B2203/0866 ,  C01B2203/0883 ,  C01B2203/1217 ,  C01B2203/1235 ,  C01B2203/1288 ,  C01B2203/142 ,  C01B2203/1619 ,  C01B2203/169 ,  C01B2203/1695 ,  H01M8/0612 ,  Y02P20/128

Abstract: A gas generation system for providing a gas flow to be supplied to a reformer includes an evaporator for evaporating the components contained in a gas flow, wherein the gas flow includes at least one carbon compound, such as hydrocarbon or alcohol, and water vapor. A normalizing stage is connected between the evaporator and the reformer for equalizing the temperature distribution in the gas flow to be supplied to the reformer. The temperature of the gas flow should be equalized to a temperature range below the maximum allowable reformer inlet temperature. In this way, temperature maxima caused by a load change are equalized, thereby significantly increasing the service life of the reformer catalyst.

Abstract translation: 用于提供要供应到重整器的气流的气体发生系统包括用于蒸发气流中所含的组分的蒸发器，其中气流包括至少一种碳化合物，例如烃或醇，以及水蒸气。 在蒸发器和重整器之间连接有归一化阶段，用于均衡供应给重整器的气流中的温度分布。 气流的温度应等于低于最大允许重整器入口温度的温度范围。 以这种方式，由负载变化引起的温度最大值相等，从而显着提高重整器催化剂的使用寿命。

公开(公告)号：US20020018738A1

公开(公告)日：2002-02-14

申请号：US09827258

申请日：2001-04-05

Inventor： Richard Woods ,  Shawn Barge

IPC: B01J008/00

CPC classification number: C01B3/583 ,  B01J8/0207 ,  B01J8/0278 ,  B01J8/0403 ,  B01J8/0492 ,  B01J19/245 ,  B01J19/2485 ,  B01J23/56 ,  B01J2208/00168 ,  B01J2208/00176 ,  B01J2208/00548 ,  B01J2208/00628 ,  B01J2219/0002 ,  B01J2219/00087 ,  B01J2219/00164 ,  B01J2219/00186 ,  B01J2219/00231 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/12 ,  C01B2203/1276 ,  C01B2203/145 ,  C01B2203/169 ,  H01M8/0631

Abstract: A multi-stage preferential oxidation reactor for removing carbon-monoxide from a product-gas comprises at least one preferential oxidation reactor stage having a product-gas stream inlet end and a product-gas stream outlet end. A first inlet is provided to introduce the product-gas stream into the preferential oxidation reactor stage, and is located at the product-gas stream inlet end of the preferential oxidation reactor stage. The first inlet is configured with a pulsator for pulsing the flow of the product-gas stream into the preferential oxidation reactor stage. A second inlet is also provided to introduce an oxidant into the preferential oxidation reactor stage. The second inlet is located at the product-gas stream inlet end of the oxidizer preferential oxidation reactor stage. An outlet is provided for removal of the treated product-gas stream from the preferential oxidation reactor stage.

Abstract translation: 用于从产物气体中除去一氧化碳的多级优先氧化反应器包括至少一个具有产物 - 气流入口端和产物气流出口端的优先氧化反应器级。 提供第一入口以将产物气流引入优先氧化反应器阶段，并且位于优先氧化反应器阶段的产物 - 气流入口端。 第一入口配置有用于使产物气流的流动脉动到优先氧化反应器阶段的脉动器。 还提供第二入口以将氧化剂引入优先氧化反应器阶段。 第二个入口位于氧化剂优先氧化反应器阶段的产物 - 气流入口端。 提供出口用于从优先氧化反应器阶段除去经处理的产物 - 气流。

公开(公告)号：US06221320B1

公开(公告)日：2001-04-24

申请号：US08147086

申请日：1993-11-03

Applicant: Tadayoshi Nagaoka

Inventor： Tadayoshi Nagaoka

IPC: B01J802

CPC classification number: B01J8/0207 ,  B01J8/0214 ,  B01J8/0403 ,  B01J2208/00814 ,  B01J2208/00884 ,  C01C1/0417 ,  Y02P20/52

Abstract: A device for holding catalyst in a radial flow reactor includes a plurality of catalyst containers each of which is a segment of a cylinder divided in the axial plane thereof. Each catalyst container has a cross section of a size which enables the container to be carried in and out of the radial fow reactor through an opening formed in an upper or lower portion of the radial flow reactor, and includes a screen provided on a liquid inlet side and a screen provided on a liquid outlet side. The catalyst containers are assembled together to form a cylindrical catalyst bed in the radial flow reactor. The catalyst containers attains a uniform thickness of a catalyst bed in a radial direction between its inlet side and outlet side over the entire height of the cylindrical catalyst bed. One or more catalyst containers requiring checking or repair only can be taken out of the reactor.

Abstract translation: 用于在径向流动反应器中保持催化剂的装置包括多个催化剂容器，每个催化剂容器是在其轴向平面上划分的气缸的段。 每个催化剂容器具有的尺寸的横截面使得容器能够通过形成在径向流动反应器的上部或下部的开口进入和离开径向母体反应器，并且包括设置在液体入口上的筛网 侧面和设置在液体出口侧的筛子。 将催化剂容器组装在一起以在径向流动反应器中形成圆柱形催化剂床。 催化剂容器在圆柱形催化剂床的整个高度上在其入口侧和出口侧之间沿径向方向获得均匀的催化剂床厚度。 可以将仅需要检查或修理的一个或多个催化剂容器从反应器中取出。