公开(公告)号：EP2094627B1

公开(公告)日：2011-02-09

申请号：EP07822801.2

申请日：2007-11-22

Applicant: BASF SE

Inventor： MÜLLER, Ulrich ,  FREIBERGER, Harald

IPC: C07C2/76 ,  C01C1/04 ,  C07C15/04

CPC classification number: C01C1/0488 ,  B01J29/44 ,  B01J37/0201 ,  B01J37/0238 ,  B01J2229/18 ,  B01J2229/34 ,  C07C2/76 ,  Y02P20/125 ,  Y02P20/52 ,  C07C15/04

Abstract: The invention relates to a method for the integrated production of aromatics and ammonia by reacting a gaseous stream A containing at least one C1 to C6 aliphatic compound and nitrogen in the presence of at least one catalyst. In one reaction, the C1 to C6 aliphatic compound is non-oxidatively converted into aromatics and the hydrogen released in said process is converted in a further reaction into ammonia.

公开(公告)号：EP2274093A1

公开(公告)日：2011-01-19

申请号：EP09739645.1

申请日：2009-04-29

Applicant: Dow Technology Investments LLC

Inventor： BRYDEN, Todd, R. ,  HOWARD, Kevin, E. ,  LEBARON, Peter, C. ,  WALLIN, Sten, A.

IPC: B01J23/46 ,  C07D301/10

CPC classification number: B01J27/055 ,  B01J21/04 ,  B01J23/50 ,  B01J23/66 ,  B01J23/688 ,  B01J35/002 ,  B01J35/1009 ,  B01J35/1038 ,  B01J35/1042 ,  B01J37/0009 ,  B01J37/0018 ,  B01J37/0201 ,  B01J37/0203 ,  B01J37/0205 ,  B01J37/0213 ,  C07D301/10

Abstract: The present invention provides porous body precursors and shaped porous bodies. Also included are catalysts and other end-use products based upon the shaped porous bodies and thus the porous body precursors. Finally, processes for making these are provided. The porous body precursors comprise a precursor alumina blend capable of enhancing one or more properties of a shaped porous body based thereupon. The need to employ modifiers to achieve a similar result may thus be substantially reduced, or even avoided, and cost savings are thus provided, as well as savings in time and equipment costs.

公开(公告)号：EP2261172A1

公开(公告)日：2010-12-15

申请号：EP09728372.5

申请日：2009-03-25

Applicant: Japan Oil, Gas and Metals National Corporation ,  INPEX Corporation ,  JX Nippon Oil & Energy Corporation ,  Japan Petroleum Exploration Co., Ltd. ,  Cosmo Oil Co., Ltd. ,  Nippon Steel Engineering Co., Ltd. ,  CHIYODA CORPORATION

Inventor： YAGI, Fuyuki ,  KAWAZUISHI, Kenichi

IPC: C01B3/38 ,  B01J23/46 ,  C01B3/48 ,  C01B3/56 ,  C10G2/00 ,  C10G49/00 ,  C10L3/10

CPC classification number: C01B3/48 ,  B01J21/10 ,  B01J23/462 ,  B01J23/58 ,  B01J37/0201 ,  C01B3/38 ,  C01B2203/0233 ,  C01B2203/0238 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/062 ,  C01B2203/1047 ,  C01B2203/1052 ,  C01B2203/1058 ,  C01B2203/1082 ,  C01B2203/1241 ,  C01B2203/127 ,  C01B2203/146 ,  C01B2203/148 ,  C10G2/32 ,  C10G49/00 ,  C10G2300/1025 ,  C10G2300/202 ,  C10G2300/42 ,  C10G2300/807 ,  Y02P20/52

Abstract: In a so-called GTL process for producing liquid hydrocarbons containing fuel oil by producing synthesis gas from natural gas, subsequently producing Fischer-Tropsch oil from the obtained synthesis gas by way of Fischer-Tropsch synthesis and upgrading the produced Fischer-Tropsch oil, the synthesis gas produced from a synthesis gas production step is partly branched at a stage prior to getting to a Fischer-Tropsch oil production step and high-purity hydrogen is separated and produced from the synthesis gas entering the branch line. All the separated high-purity hydrogen is supplied to an upgrading reaction step and consumed as hydrogen for an upgrading reaction. Additionally, the synthesis gas entering the branch line is subjected to a water gas shift reaction to raise the hydrogen concentration before the step of separating and producing high-purity hydrogen and the residual gas left after the separation may be circulated to the synthesis gas production step as raw material for producing synthesis gas.

Abstract translation: 在由天然气生产合成气生产含燃料油的液态烃的所谓GTL方法中，随后通过费 - 托合成法生产费 - 托合成法，并对生产的费 - 托油进行升级，生产费 - 托油 从合成气生产步骤产生的合成气在进入费 - 托油生产步骤之前的阶段部分支化，并且从进入分支管线的合成气分离和产生高纯度氢。 将所有分离的高纯度氢气供应至升级反应步骤，并作为氢气用于升级反应。 此外，进入分支管线的合成气进行水煤气变换反应，以在分离和生产高纯度氢气的步骤之前提高氢气浓度，并且分离后留下的残留气体可循环到合成气生产步骤 作为生产合成气的原料。

公开(公告)号：EP2260940A1

公开(公告)日：2010-12-15

申请号：EP08765411.7

申请日：2008-06-04

Applicant: CHIYODA CORPORATION

Inventor： KAWAMURA, Kazushige ,  TAKEDA, Dai ,  AWAI, Eiji

IPC: B01J27/08 ,  B01D53/86 ,  B01J21/18 ,  B01J33/00 ,  B01J37/22

CPC classification number: B01D53/8609 ,  B01D2255/702 ,  B01D2257/302 ,  B01D2257/602 ,  B01J21/18 ,  B01J23/04 ,  B01J27/08 ,  B01J37/0201 ,  C01B17/78 ,  F23J2215/20 ,  F23J2215/60 ,  F23J2219/10 ,  F23J2219/30 ,  F23J2219/60

Abstract: A carbon-based catalyst for flue gas desulfurization is brought into contact with a flue gas containing at least SO 2 gas, oxygen and water vapor so that the SO 2 gas can react with the oxygen and the water vapor to form sulfuric acid which is to be recovered. On a surface of the carbon-based catalyst, iodine, bromine or a compound thereof is added, ion exchanged or supported and a water-repellent treatment is applied. The carbon-based catalyst can also be used as a mercury adsorbent for flue gas treatment for adsorbing and removing metallic mercury from a flue gas containing metallic mercury, SO 2 gas, oxygen and water vapor.

Abstract translation: 排烟脱硫甲碳系催化剂所接触与烟道气含有至少SO 2个气体，氧气和水蒸汽，以便做的SO 2种气体可与氧和水蒸汽反应，以形成硫酸所有这是为了 恢复。 在碳系催化剂，碘，溴或它们被添加的化合物的表面，离子交换或负载和一个防水处理被应用。 因此，该碳系催化剂，可以使用作为汞吸附剂烟气处理用于吸附和从含有金属汞，二氧化硫气体，氧气和水蒸汽的烟道气中除去金属汞。

公开(公告)号：EP2248792A1

公开(公告)日：2010-11-10

申请号：EP09717329.8

申请日：2009-02-27

Applicant: Daicel Chemical Industries, Ltd.

Inventor： TAKANO, Minoru ,  HIRAI, Naruhisa ,  ISHII, Yasutaka

IPC: C07C27/12 ,  C07C29/50 ,  C07C35/37 ,  C07C45/33 ,  C07C45/36 ,  C07C47/542 ,  C07C49/39 ,  C07C49/78 ,  C07C51/235 ,  C07C51/265 ,  C07C53/126 ,  C07C63/06 ,  B01J27/02 ,  C07B61/00

CPC classification number: C07C45/33 ,  B01J27/053 ,  B01J37/0201 ,  C07C29/50 ,  C07C45/36 ,  C07C51/00 ,  C07C51/265 ,  C07C2603/74 ,  Y02P20/55 ,  C07C35/37 ,  C07C47/542 ,  C07C49/417 ,  C07C63/04

Abstract: Disclosed is a process for the production of an oxygen-containing organic compound by oxidizing an organic compound with molecular oxygen in a liquid phase in the presence both of a catalytic nitrogen-containing cyclic compound and a catalyst including a solid superacid and, supported thereon, a transition metal compound, in which the nitrogen-containing cyclic compound contains, as a ring constituent, a skeleton represented by following Formula (1), wherein X represents an -OR group, and wherein R represents hydrogen atom or a hydroxyl-protecting group. The process gives the oxygen-containing organic compound in a high yield and enables easy recovery and reuse of the catalyst.

公开(公告)号：EP1807199A4

公开(公告)日：2010-11-10

申请号：EP05800331

申请日：2005-09-22

Applicant: SIGNA CHEMISTRY LLC ,  UNIV MICHIGAN STATE

Inventor： LEFENFELD MICHAEL ,  DYE JAMES L

IPC: B01J23/04 ,  B01J37/02 ,  C07C17/25 ,  C07F1/02

CPC classification number: C01G23/00 ,  B01J21/04 ,  B01J21/063 ,  B01J23/04 ,  B01J35/1061 ,  B01J35/1066 ,  B01J37/0081 ,  B01J37/0201 ,  B01J37/023 ,  B01J37/08 ,  C01B3/042 ,  C01B3/065 ,  C01B3/08 ,  C01P2006/16 ,  C07C1/26 ,  C07C2/861 ,  C07C5/324 ,  C07C17/23 ,  C07C2521/04 ,  C07C2521/06 ,  C07C2523/04 ,  Y02E60/362 ,  Y02E60/364 ,  C07C15/18 ,  C07C15/20

公开(公告)号：EP2218493A3

公开(公告)日：2010-11-03

申请号：EP10151654.0

申请日：2010-01-26

Applicant: General Electric Company

Inventor： Lewis, Larry Neil ,  Hancu, Dan ,  Siclovan, Oltea Puica ,  Yin, Ming

IPC: B01D53/94 ,  B01J23/50 ,  B01J35/00 ,  B01J37/00 ,  B01J37/02 ,  B01J37/03

CPC classification number: B01J23/50 ,  B01D53/9418 ,  B01D2255/104 ,  B01J35/002 ,  B01J35/023 ,  B01J37/0018 ,  B01J37/0201 ,  B01J37/033 ,  B01J37/036

Abstract: A composition comprises a templated metal oxide substrate having a plurality of pores and a catalyst material comprising silver. The composition under H 2 at 30 degrees Celsius, at a wavelength in a range of from about 350 nm to about 500 nm has a VIS-UV absorbance intensity that is at least 20 percent less than a standard silver alumina catalyst (Ag STD). The standard alumina is Norton alumina, and which has the same amount of silver by weight.

公开(公告)号：EP2234718A2

公开(公告)日：2010-10-06

申请号：EP09703599.2

申请日：2009-01-23

Applicant: Total Petrochemicals Research Feluy

Inventor： NESTERENKO, Nikolai ,  VERMEIREN, Walter ,  VAN DONK, Sander ,  MINOUX, Delphine

IPC: B01J27/16 ,  B01J29/06 ,  B01J29/40 ,  C07C1/20 ,  C07C4/06

CPC classification number: C07C1/20 ,  B01J27/16 ,  B01J29/06 ,  B01J29/061 ,  B01J29/40 ,  B01J29/405 ,  B01J37/0201 ,  B01J37/0207 ,  B01J37/024 ,  B01J37/28 ,  B01J2229/16 ,  B01J2229/186 ,  B01J2229/36 ,  B01J2229/37 ,  C07C4/06 ,  C07C2523/02 ,  C07C2527/14 ,  C07C2529/06 ,  C07C2529/40 ,  C07C2529/82 ,  C07C2529/85 ,  C08F110/02 ,  C10G2400/20 ,  Y02P30/42 ,  C07C11/02

Abstract: The invention covers a process for obtaining an alkaline earth or rare earth metal-P-modified molecular sieve (M-P-modified molecular sieve) comprising the following steps: a). selecting a molecular sieve selected from one of: - a P-modified molecular sieve which contains at least 0.3 wt% of P - a molecular sieve which is modified with P prior to or during step b) thereby introducing at least 0.3 wt % of P b). contacting said molecular sieve with an alkaline earth or rare earth metal-containing compound (M-containing compound) to introduce at least 0.05 wt% of the alkaline earth or rare earth metal to the molecular sieve. The invention also covers a catalyst composite comprising: a). at least 10 wt % of a M-P-modified molecular sieve comprising at least 0.05 % by weight of an alkaline earth or rare earth metal (M) and at least 0.3 wt% of P, b). optionally metal phosphate, c). optionally matrix material, and d). optionally binder. The catalyst of the invention can also be used in a process for making an olefin product from an oxygen-containing, halogenide-containing or sulphur-containing organic feedstock wherein said oxygen-containing, halogenide-containing or sulphur-containing organic feedstock is contacted in the XTO reactor with the catalyst composite according to the invention under conditions effective to convert the oxygen-containing, halogenide-containing or sulphur-containing organic feedstock to olefin products (the XTO reactor effluent). The catalyst composite of the invention can also be used in addition or alternatively in an OCP process.

Abstract translation: 本发明涉及一种获得碱土金属或稀土金属-P改性分子筛（M-P-改性分子筛）的方法，包括以下步骤：a）。 选择选自以下之一的分子筛：P-改性分子筛，其含有至少0.3重量％的P - 在步骤b）之前或期间用P改性的分子筛，由此引入至少0.3重量％的P b）。 使所述分子筛与含碱土或含稀土金属的化合物（含M化合物）接触，以将至少0.05重量％的碱土金属或稀土金属引入到分子筛中。 本发明还涵盖了一种催化剂复合材料，其包括：a）。 至少10重量％的包含至少0.05重量％的碱土金属或稀土金属（M）和至少0.3重量％的P，b）的M-P改性分子筛。 任选的金属磷酸盐，c）。 任选的基质材料，和d）。 可选粘合剂。 本发明的催化剂也可用于从含氧，含卤素或含硫有机原料制备烯烃产物的方法，其中所述含氧卤化物或含硫有机原料接触 在具有将含氧，含卤素或含硫有机原料转化为烯烃产物（XTO反应器流出物）的条件下，具有根据本发明的催化剂复合材料的XTO反应器。 本发明的催化剂复合物也可以在OCP方法中加入或替代地使用。

公开(公告)号：EP2231310A1

公开(公告)日：2010-09-29

申请号：EP08860901.1

申请日：2008-12-17

Applicant: BASF Corporation

Inventor： LIU, Xinsheng ,  WEI, Xinyi ,  TRAN, Pascaline ,  LAPADULA, Gerard

IPC: B01D53/86 ,  B01D53/90

CPC classification number: B01D53/8656 ,  B01D53/90 ,  B01D53/9477 ,  B01D2251/2062 ,  B01D2255/1021 ,  B01D2255/1023 ,  B01D2255/20715 ,  B01D2255/9202 ,  B01J21/066 ,  B01J23/42 ,  B01J23/44 ,  B01J35/006 ,  B01J37/0201 ,  B01J37/0219 ,  B01J37/0248

Abstract: Catalysts, catalyst systems, and methods for removing oxides of nitrogen and/or carbon monoxide in flue gases are provided where ammonia is used with a selective catalytic reduction catalyst for reducing oxides of nitrogen. An oxidation catalyst is utilized, which comprises particulate platinum or platinum/palladium dispersed on zirconia particles, the particulate platinum or platinum/palladium having an average particle size less than about 10 nm. The catalyst is effective to convert less than 20% of NO to NO.

公开(公告)号：EP2212011A1

公开(公告)日：2010-08-04

申请号：EP08871723.6

申请日：2008-10-29

Applicant: IFP

Inventor： NEDEZ, Christophe ,  ROISIN, Eric

IPC: B01D53/86 ,  B01J23/882 ,  B01J21/06 ,  C01B17/16

CPC classification number: B01D53/8603 ,  B01D2255/20715 ,  B01D2255/20738 ,  B01D2255/20746 ,  B01D2255/20769 ,  B01D2257/30 ,  B01J21/063 ,  B01J21/066 ,  B01J21/12 ,  B01J23/02 ,  B01J23/78 ,  B01J23/882 ,  B01J23/883 ,  B01J23/8872 ,  B01J35/1014 ,  B01J35/1019 ,  B01J37/0009 ,  B01J37/0201 ,  C01B17/164 ,  C01B17/165 ,  C01B17/167

Abstract: The invention relates to a method for converting the sulphur compounds present in a gas, which contains H2S and sulphur compounds, into H2S. The method comprises the step A of contacting said gas with a reducing gas in the presence of a hydrogenation catalyst containing at least cobalt, molybdenum and an alumina substrate, the sum of the calculated contents of cobalt and molybdenum in their oxide form ranging from 3 to 25 wt %, the surface of said alumina being higher than 140 m2/g. The method further comprises the step B of contacting at least one fraction of the effluent gas from step A with a catalyst containing at least one alkaline-earth element, at least one dopant selected from the group containing iron, cobalt and molybdenum and at least one compound selected from the group including titanium oxide and zirconium oxide, wherein the catalyst of step B is either in a mass oxide form containing only said oxides, or in a supported oxide form.