公开(公告)号：US10011482B2

公开(公告)日：2018-07-03

申请号：US15430592

申请日：2017-02-13

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Hamilton Sean Michael Whitney ,  Daniel A. Burciaga

IPC: C01B3/38 ,  C01B3/58 ,  C01B3/52 ,  C01B3/56 ,  B01D5/00 ,  B01D17/02 ,  B01D29/27 ,  B01D29/66 ,  B01D46/00 ,  B01D47/10 ,  B01D50/00 ,  B01D53/14 ,  B01D53/18 ,  B01D53/04 ,  B01D53/047 ,  B01D53/48 ,  B01D53/76 ,  B01D61/36

CPC classification number: C01B3/52 ,  B01D5/0027 ,  B01D5/006 ,  B01D5/0072 ,  B01D5/0075 ,  B01D5/009 ,  B01D17/0208 ,  B01D29/27 ,  B01D29/66 ,  B01D46/0036 ,  B01D47/10 ,  B01D50/006 ,  B01D53/0423 ,  B01D53/0462 ,  B01D53/047 ,  B01D53/0476 ,  B01D53/12 ,  B01D53/1406 ,  B01D53/1412 ,  B01D53/1431 ,  B01D53/1462 ,  B01D53/1468 ,  B01D53/1487 ,  B01D53/18 ,  B01D53/265 ,  B01D53/326 ,  B01D53/48 ,  B01D53/76 ,  B01D61/362 ,  B01D2252/102 ,  B01D2252/103 ,  B01D2252/20436 ,  B01D2252/504 ,  B01D2252/602 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2257/304 ,  B01D2257/306 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2257/60 ,  B01D2257/708 ,  B01D2259/402 ,  C01B3/24 ,  C01B3/38 ,  C01B3/382 ,  C01B3/386 ,  C01B3/56 ,  C01B3/58 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0261 ,  C01B2203/04 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/0435 ,  C01B2203/045 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/068 ,  C01B2203/0877 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/142 ,  C01B2203/147 ,  C01B2203/84 ,  H05K999/99 ,  Y02P20/13 ,  Y02P30/30

Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.

公开(公告)号：US20180155193A1

公开(公告)日：2018-06-07

申请号：US15726445

申请日：2017-10-06

Applicant: Panasonic Intellectual Property Management Co., Ltd.

Inventor： OSAMU SAKAI ,  KUNIHIRO UKAI ,  HIDENOBU WAKITA ,  YUKIMUNE KANI ,  YUUICHI YAKUMARU ,  TAKASHI SOTOKU

IPC: C01B3/58 ,  C25B1/12 ,  H01M8/14 ,  C01B3/50 ,  H01M8/04082 ,  H01M8/0662 ,  B01D53/32

CPC classification number: C01B3/58 ,  B01D53/326 ,  B01D2256/16 ,  C01B3/503 ,  C25B1/12 ,  H01M8/0232 ,  H01M8/0271 ,  H01M8/04201 ,  H01M8/0681 ,  H01M8/141 ,  H01M8/248 ,  H01M2008/1095 ,  Y02E60/366

Abstract: An apparatus includes: an electrolyte membrane; a cathode catalyst layer provided to one main surface of the electrolyte membrane; an anode catalyst layer provided to the other main surface of the electrolyte membrane; a cathode gas diffusion layer provided on a main surface of the cathode catalyst layer not facing the electrolyte membrane; a separator including a recess through which cathode gas flows; an anode gas diffusion layer provided on a main surface of the anode catalyst layer not facing the electrolyte membrane; a voltage applicator applying a voltage between the cathode catalyst layer and the anode catalyst layer; and a fastener fastening a laminated body. The cathode gas diffusion layer is accommodated in the recess, projects from the recess in a thickness direction before fastening of the laminated body, and includes an elastic member between side surfaces of the cathode gas diffusion layer and of the recess.

公开(公告)号：US09975105B2

公开(公告)日：2018-05-22

申请号：US14416374

申请日：2013-07-23

Applicant: SEKISUI CHEMICAL CO., LTD. ,  RENAISSANCE ENERGY RESEARCH CORPORATION

Inventor： Toshihito Miyama ,  Tomoaki Nishino ,  Osamu Okada ,  Tamotsu Nonouchi

IPC: C07C29/158 ,  B01J19/24 ,  C07C45/49 ,  C01B3/58 ,  B01J37/03 ,  B01J21/06 ,  B01J23/60 ,  B01J23/80 ,  B01J35/10 ,  B01J37/02 ,  C07C29/141 ,  B01J21/08 ,  B01J23/656

CPC classification number: B01J19/245 ,  B01J21/063 ,  B01J21/08 ,  B01J23/6562 ,  B01J23/80 ,  B01J35/1019 ,  B01J35/1038 ,  B01J35/1042 ,  B01J35/1061 ,  B01J37/0201 ,  B01J37/031 ,  B01J37/033 ,  B01J2219/24 ,  C01B3/58 ,  C01B2203/045 ,  C01B2203/0485 ,  C07C29/141 ,  C07C29/158 ,  C07C45/49 ,  C07C31/08 ,  C07C47/06

Abstract: A system for producing an oxygenate, comprising: a desulfurization apparatus for contacting a raw material gas comprising hydrogen and carbon monoxide with a desulfurizing agent comprising copper; and a synthesis apparatus for contacting the raw material gas treated by the desulfurizing apparatus with an oxygenate-synthesis catalyst comprising rhodium.

公开(公告)号：US09790092B2

公开(公告)日：2017-10-17

申请号：US14372853

申请日：2012-12-19

Applicant: H-TEC SYSTEMS GmbH

Inventor： Nils Mantai ,  Claus Würfel ,  Dennis Wilken ,  Uwe Küter ,  Stefan Höller

IPC: C25B15/08 ,  C25B1/12 ,  C01B3/58 ,  C25B15/00 ,  C25B1/04 ,  B01J19/08 ,  C25B9/06

CPC classification number: C01B3/58 ,  B01J19/087 ,  C25B1/04 ,  C25B1/12 ,  C25B9/06 ,  C25B15/00 ,  C25B15/08 ,  Y02E60/366

Abstract: A method is provided for running up/starting up an electrolysis device (10), which device includes a reactor container (3) which is arranged downstream of an electrolyzer (1) and in which oxygen reacts with hydrogen into water, in order to reduce an oxygen share in a hydrogen gas flow coming from the electrolyzer (1). The electrolysis device (10) is operated with a predefined operating pressure. Upon running up/starting up the electrolyzer (1), the hydrogen gas flow coming from the electrolyzer (1) is led past the reactor container (3) via a bypass conduit (11).

公开(公告)号：US20170166446A1

公开(公告)日：2017-06-15

申请号：US15430592

申请日：2017-02-13

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Hamilton Sean Michael Whitney ,  Daniel A. Burciaga

IPC: C01B3/58 ,  C01B3/56 ,  C01B3/38 ,  B01D5/00 ,  B01D17/02 ,  B01D29/27 ,  B01D29/66 ,  B01D46/00 ,  B01D47/10 ,  B01D50/00 ,  B01D53/14 ,  B01D53/18 ,  B01D53/04 ,  B01D53/047 ,  B01D53/48 ,  B01D53/76 ,  B01D61/36 ,  C01B3/52

CPC classification number: C01B3/52 ,  B01D5/0027 ,  B01D5/006 ,  B01D5/0072 ,  B01D5/0075 ,  B01D5/009 ,  B01D17/0208 ,  B01D29/27 ,  B01D29/66 ,  B01D46/0036 ,  B01D47/10 ,  B01D50/006 ,  B01D53/0423 ,  B01D53/0462 ,  B01D53/047 ,  B01D53/0476 ,  B01D53/12 ,  B01D53/1406 ,  B01D53/1412 ,  B01D53/1431 ,  B01D53/1462 ,  B01D53/1468 ,  B01D53/1487 ,  B01D53/18 ,  B01D53/265 ,  B01D53/326 ,  B01D53/48 ,  B01D53/76 ,  B01D61/362 ,  B01D2252/102 ,  B01D2252/103 ,  B01D2252/20436 ,  B01D2252/504 ,  B01D2252/602 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2257/304 ,  B01D2257/306 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2257/60 ,  B01D2257/708 ,  B01D2259/402 ,  C01B3/24 ,  C01B3/38 ,  C01B3/382 ,  C01B3/386 ,  C01B3/56 ,  C01B3/58 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0261 ,  C01B2203/04 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/0435 ,  C01B2203/045 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/068 ,  C01B2203/0877 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/142 ,  C01B2203/147 ,  C01B2203/84 ,  H05K999/99 ,  Y02P20/13 ,  Y02P30/30

Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.

公开(公告)号：US09634344B2

公开(公告)日：2017-04-25

申请号：US14384376

申请日：2013-03-07

Applicant: PANASONIC CORPORATION

Inventor： Takahiro Kusuyama ,  Hidenobu Wakita ,  Chie Harada ,  Seiji Fujihara ,  Tomoyuki Nakajima

IPC: H01M8/06 ,  H01M8/0668 ,  C01B3/58 ,  H01M8/0662 ,  H01M8/0612 ,  H01M8/1018

CPC classification number: H01M8/0668 ,  C01B3/58 ,  C01B3/583 ,  C01B2203/0233 ,  C01B2203/0244 ,  C01B2203/0283 ,  C01B2203/0435 ,  C01B2203/044 ,  C01B2203/0465 ,  C01B2203/047 ,  C01B2203/066 ,  H01M8/0618 ,  H01M8/0662 ,  H01M2008/1095 ,  H01M2250/20 ,  H01M2250/30 ,  Y02B90/18 ,  Y02T90/32

Abstract: A hydrogen purifier includes: a CO remover configured to reduce carbon monoxide in a hydrogen-containing gas through an oxidation reaction, the hydrogen-containing gas containing ammonia and carbon monoxide; and an ammonia remover provided upstream from the CO remover, the ammonia remover being configured to cause a reaction between ammonia in the hydrogen-containing gas and oxygen by using a catalyst to decompose the ammonia.

公开(公告)号：US09580315B2

公开(公告)日：2017-02-28

申请号：US14939025

申请日：2015-11-12

Applicant: ThermoChem Recovery International, Inc.

Inventor： Ravi Chandran ,  Daniel Michael Leo ,  Shawn Robert Freitas ,  Dave G. Newport ,  Hamilton Sean Michael Whitney ,  Daniel A. Burciaga

IPC: C01B3/52 ,  C01B3/56 ,  B01D53/047 ,  B01D53/12 ,  B01D53/14 ,  B01D53/18 ,  B01D53/32 ,  C01B3/24 ,  B01D5/00 ,  B01D47/10 ,  B01D17/02 ,  B01D29/27 ,  B01D29/66

CPC classification number: C01B3/52 ,  B01D5/0027 ,  B01D5/006 ,  B01D5/0072 ,  B01D5/0075 ,  B01D5/009 ,  B01D17/0208 ,  B01D29/27 ,  B01D29/66 ,  B01D46/0036 ,  B01D47/10 ,  B01D50/006 ,  B01D53/0423 ,  B01D53/0462 ,  B01D53/047 ,  B01D53/0476 ,  B01D53/12 ,  B01D53/1406 ,  B01D53/1412 ,  B01D53/1431 ,  B01D53/1462 ,  B01D53/1468 ,  B01D53/1487 ,  B01D53/18 ,  B01D53/265 ,  B01D53/326 ,  B01D53/48 ,  B01D53/76 ,  B01D61/362 ,  B01D2252/102 ,  B01D2252/103 ,  B01D2252/20436 ,  B01D2252/504 ,  B01D2252/602 ,  B01D2256/16 ,  B01D2256/20 ,  B01D2257/304 ,  B01D2257/306 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2257/60 ,  B01D2257/708 ,  B01D2259/402 ,  C01B3/24 ,  C01B3/38 ,  C01B3/382 ,  C01B3/386 ,  C01B3/56 ,  C01B3/58 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/025 ,  C01B2203/0261 ,  C01B2203/04 ,  C01B2203/0415 ,  C01B2203/042 ,  C01B2203/043 ,  C01B2203/0435 ,  C01B2203/045 ,  C01B2203/0465 ,  C01B2203/0475 ,  C01B2203/048 ,  C01B2203/0485 ,  C01B2203/061 ,  C01B2203/062 ,  C01B2203/068 ,  C01B2203/0877 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/142 ,  C01B2203/147 ,  C01B2203/84 ,  H05K999/99 ,  Y02P20/13 ,  Y02P30/30

Abstract: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.

Abstract translation: 用于处理未条件合成气的系统和方法首先除去固体和半挥发性有机化合物（SVOC），然后除去挥发性有机化合物（VOC），然后从合成气中除去至少一种含硫化合物。 可以根据诸如待处理的合成气的来源，期望形成，捕获或再循环的产物，副产物和中间产物等因素进行附加处理和环境考虑。

公开(公告)号：US09540293B2

公开(公告)日：2017-01-10

申请号：US14261114

申请日：2014-04-24

Applicant: Minish Mahendra Shah ,  Raymond Francis Drnevich ,  Vasilis Papavassiliou

Inventor： Minish Mahendra Shah ,  Raymond Francis Drnevich ,  Vasilis Papavassiliou

IPC: C07C7/00 ,  B01D53/48 ,  B01D53/86 ,  C10G70/00 ,  C10G70/02 ,  C10G70/06

CPC classification number: C07C7/005 ,  B01D53/1406 ,  B01D53/1468 ,  B01D53/1493 ,  B01D53/48 ,  B01D53/52 ,  B01D53/8603 ,  B01D53/8612 ,  B01D53/869 ,  B01D53/8696 ,  B01D2251/206 ,  B01D2252/204 ,  B01D2255/207 ,  B01D2256/24 ,  B01D2257/306 ,  C01B3/52 ,  C01B3/58 ,  C01B2203/0415 ,  C01B2203/045 ,  C01B2203/0485 ,  C01B2203/0872 ,  C01B2203/147 ,  C10G70/00 ,  C10G70/02 ,  C10G70/06 ,  C10G2300/202 ,  C10G2300/207

Abstract: Organic sulfur compounds contained in refinery off gas streams having either high ort low concentrations of olefins are converted to hydrogen sulfides which can be then be removed using conventional amine treating systems. The process uses a catalytic reactor with or without a hydrotreater depending on the olefin concentration of the off gas stream. The catalytic reactor operates in a hydrogenation mode or an oxidation mode to convert a majority of organic sulfur compounds into hydrogen sulfides.

Abstract translation: 包含在具有高或低浓度烯烃的炼油厂废气流中的有机硫化合物转化为硫化氢，然后可以使用常规的胺处理系统除去。 该方法使用具有或不具有加氢处理器的催化反应器，取决于废气流的烯烃浓度。 催化反应器以氢化模式或氧化模式操作，以将大部分有机硫化合物转化为硫化氢。

公开(公告)号：US20160368767A1

公开(公告)日：2016-12-22

申请号：US15105075

申请日：2014-12-16

Applicant: AVRIL ,  AXENS ,  IFP ENERGIES NOUVELLES ,  BIONEXT ,  THYSSENKRUPP INDUSTRIAL SOLUTIONS AG ,  TOTAL RAFFINAGE CHIMIE ,  COMMISSARIAT A L'ENERGIE ATOMIQUE ET AUX ENERGIES ALTERNATIVES

Inventor： David CHICHE ,  Anne Claire PIERRON ,  Norbert ULLRICH

IPC: C01B3/52 ,  C01B3/58 ,  C10G2/00 ,  C01B3/16

CPC classification number: C01B3/52 ,  C01B3/16 ,  C01B3/56 ,  C01B3/58 ,  C01B2203/0283 ,  C01B2203/0415 ,  C01B2203/0435 ,  C01B2203/045 ,  C01B2203/0465 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/0485 ,  C01B2203/06 ,  C01B2203/062 ,  C01B2203/1041 ,  C01B2203/1047 ,  C01B2203/1052 ,  C01B2203/1082 ,  C01B2203/145 ,  C01B2203/146 ,  C01B2203/147 ,  C10G2/331

Abstract: The invention relates to a process for purifying synthesis gas, comprising at least one stage for separating the crude synthesis gas to be treated into at least two effluents, namely a first part and a complementary part, in which the said first part is subjected to a carbon monoxide conversion stage with steam and the said complementary part is subjected to a COS and HCN catalytic hydrolysis stage, the two gas flows, namely the first part and complementary part, are then each treated separately in two stages intended to remove acid gases such as CO2 and H2S, by washing with aqueous solutions of specific amines, before a recombination stage of the two treated effluents.

Abstract translation: 本发明涉及一种纯化合成气的方法，包括至少一个阶段，用于将待处理的粗合成气分离成至少两个流出物，即第一部分和互补部分，其中所述第一部分经受 一氧化碳转化阶段用蒸汽和所述互补部分进行COS和HCN催化水解阶段，然后将两个气体流，即第一部分和互补部分分开处理两个阶段，分两个阶段，用于除去酸性气体，例如 通过在两种处理过的流出物的重组阶段之前用特定胺的水溶液洗涤，将CO 2和H 2 S.

公开(公告)号：US20160251229A1

公开(公告)日：2016-09-01

申请号：US15093998

申请日：2016-04-08

Applicant: Khalid T. Alkusayer

Inventor： Khalid T. Alkusayer

IPC: C01C1/04 ,  C07C273/10 ,  C01B3/58 ,  B01J19/24 ,  C01B3/06

CPC classification number: C01C1/0488 ,  B01J19/0006 ,  B01J19/24 ,  B01J19/2475 ,  B01J2219/00058 ,  B01J2219/24 ,  C01B3/025 ,  C01B3/06 ,  C01B3/16 ,  C01B3/505 ,  C01B3/58 ,  C01B2203/0283 ,  C01B2203/041 ,  C01B2203/0435 ,  C01B2203/066 ,  C01B2203/068 ,  C01B2203/1205 ,  C01C1/0405 ,  C01C1/0411 ,  C01C1/0417 ,  C01C1/0452 ,  C01C1/0458 ,  C07C273/10 ,  C25B5/00 ,  Y02E60/36 ,  Y02P20/52

Abstract: A method for synthesizing ammonia for agricultural fertilizers employs water (H2O) as the source of hydrogen (H2) in ammonia (NH3) synthesis, and gathers carbon monoxide (CO) as a limiting reagent for combining in a WGS (Water-Gas-Shift) reaction for producing hydrogen. The WGS reaction employs CO with the water to produce Carbon Dioxide (CO2) and H2, consuming undesirable CO from other industrial applications. A by-product of the process includes generating 1.5 mole of CO2 for each mole of ammonia synthesized. An intermediate step consumes 3 moles of hydrogen for each mole of Nitrogen (N2). The use of methane gas is avoided as the process employs CO and the WGS reaction as an exclusive source of H2 without introducing methane (CH4). A downstream synthesis of ammonia can be done through a fuel cell to produce electricity for the ammonia synthesis for further sustainability.

Abstract translation: 用于农业肥料合成氨的方法使用水（H 2 O）作为氨（NH 3）合成中的氢（H 2）源，并且收集一氧化碳（CO）作为在WGS（水煤气转换） ）反应生成氢。 WGS反应使用CO与水一起生产二氧化碳（CO2）和H2，从其他工业应用中消耗不需要的CO。 该方法的副产物包括为合成的每摩尔氨产生1.5摩尔的CO 2。 中间步骤每摩尔氮（N 2）消耗3摩尔氢。 避免使用甲烷气体，因为该方法使用CO和WGS反应作为H2的独家来源，而不引入甲烷（CH4）。 氨的下游合成可以通过燃料电池进行，以产生氨合成用于进一步可持续性的电。