公开(公告)号：US20180111084A1

公开(公告)日：2018-04-26

申请号：US15568461

申请日：2016-03-04

申请人： BEIJING UNIVERSITY OF CHEMICAL TECHNOLOGY

发明人： Biaohua CHEN ,  Runduo ZHANG ,  Jie ZHANG ,  Dongjun SHI ,  Yingxia LI

IPC分类号： B01D53/72 ,  B01D53/78 ,  B01D53/86 ,  B01J29/46 ,  B01J35/04 ,  F23J15/02

CPC分类号： B01D53/72 ,  B01D53/30 ,  B01D53/56 ,  B01D53/78 ,  B01D53/86 ,  B01D53/8621 ,  B01D53/8625 ,  B01D53/8628 ,  B01D53/864 ,  B01D53/865 ,  B01D53/8668 ,  B01D53/8696 ,  B01D2255/1021 ,  B01D2255/1023 ,  B01D2255/20761 ,  B01D2255/504 ,  B01D2255/904 ,  B01D2257/408 ,  B01D2258/0283 ,  B01J23/44 ,  B01J29/46 ,  B01J35/0006 ,  B01J35/04 ,  B01J37/0246 ,  B01J2229/66 ,  C07C255/08 ,  F23J15/02 ,  F23J2219/10

摘要： An integrated purification method and an integrated purification system for an industrial exhaust gas containing cyanides, hydrocarbons and NOx. The method comprises the steps of: 1) subjecting the exhaust gas containing pollutants such as cyanides, hydrocarbons and nitrogen oxides (NOx) to a gas-liquid separation device (1) to separate the free fluid, then mixing with the air blown by the air blower (201, 202), and preheating by the heating unit; 2) the mixture entering into the selective catalytic combustion (SCC) reactor (5) for the selective catalytic combustion reaction to convert harmful substances into CO2, H2O and N2, the catalysis being performed in two stages: the earlier stage is catalyzed by supported molecular sieve catalyst, and the latter stage is catalyzed by supported precious metal catalyst; and 3) the gas came out from the SCC reactor (5) entering into the heating unit to recover the heat, and then the purified exhaust gas being discharged directly through the chimney (6). The system comprises a gas-liquid separation device (1), a heating unit and a selective catalytic combustion reactor (5), a gas outlet of the gas-liquid separation device (1) being connected to the selective catalytic combustion reactor (5) through the heating unit, and an exhaust gas outlet of the selective catalytic combustion reactor (5) being connected to a chimney (6) through the heating unit.

公开(公告)号：US09878310B2

公开(公告)日：2018-01-30

申请号：US14373597

申请日：2013-02-14

申请人： MITSUBISHI HEAVY INDUSTRIES, LTD.

发明人： Masanao Yonemura ,  Toshinobu Yasutake ,  Shuji Fujii ,  Koji Higashino ,  Makoto Susaki ,  Kaori Yoshida

IPC分类号： B01J27/25 ,  B01J27/232 ,  B01J27/24 ,  B01D53/86 ,  B01J21/06 ,  B01J23/02 ,  B01J37/00 ,  B01J21/08 ,  B01J23/755 ,  B01J23/28 ,  B01J23/46 ,  B01J23/75 ,  B01J35/04

CPC分类号： B01J27/25 ,  B01D53/8606 ,  B01D53/8621 ,  B01D2255/2042 ,  B01D2255/20746 ,  B01D2255/20753 ,  B01D2255/20769 ,  B01D2257/30 ,  B01D2257/408 ,  B01J21/063 ,  B01J21/066 ,  B01J21/08 ,  B01J23/02 ,  B01J23/28 ,  B01J23/462 ,  B01J23/75 ,  B01J23/755 ,  B01J27/232 ,  B01J27/24 ,  B01J35/04 ,  B01J37/0018

摘要： Provided are a catalyst for hydrolysis and use of a titanium dioxide-based composition which are capable of removing COS and HCN simultaneously at high degradation percentages. The catalyst for hydrolysis is a catalyst for hydrolysis of carbonyl sulfide and hydrogen cyanide, having at least: an active component containing, as a main component, at least one metal selected from the group consisting of barium, nickel, ruthenium, cobalt, and molybdenum; and a titanium dioxide-based support supporting the active component.

公开(公告)号：US08906329B2

公开(公告)日：2014-12-09

申请号：US13966382

申请日：2013-08-14

申请人： Johnson Matthey Public Limited Company

发明人： Todd Howard Ballinger ,  Philip Gerald Blakeman ,  Guy Richard Chandler ,  Hai-Ying Chen ,  Julian Peter Cox ,  Joseph M. Fedeyko ,  Alexander Nicholas Michael Green ,  Paul Richard Phillips ,  Stuart David Reid ,  Erich Conlan Weigert ,  James Alexander Wylie

IPC分类号： B01D53/56 ,  B01D53/94 ,  B01J29/00 ,  B01J29/06 ,  F01N3/28 ,  B01J37/00 ,  B01J35/02 ,  B01J37/02 ,  B01J29/76

CPC分类号： B01J29/763 ,  B01D53/565 ,  B01D53/8621 ,  B01D53/9413 ,  B01D53/9418 ,  B01D53/9422 ,  B01D2251/2062 ,  B01D2251/2067 ,  B01D2255/2065 ,  B01D2255/20738 ,  B01D2255/20761 ,  B01D2255/50 ,  B01D2255/9202 ,  B01D2258/012 ,  B01J29/7065 ,  B01J35/023 ,  B01J37/0009 ,  B01J37/0215 ,  B01J37/0246 ,  B01J2229/186 ,  B01J2229/42

摘要： A catalyst composition is provided having a zeolite material of a CHA crystal structure and a silica to alumina mole ratio (SAR) of about 10 to about 25 and preferably having a mean crystal size of at least 1.0 microns; and a non-aluminum base metal (M), wherein said zeolite material contains said base metal in a base metal to aluminum ratio (M:Al) of about 0.10 to about 0.24.

摘要翻译： 提供一种催化剂组合物，其具有CHA晶体结构的沸石材料和约10至约25的二氧化硅与氧化铝的摩尔比（SAR），优选具有至少1.0微米的平均晶体尺寸; 和非铝贱金属（M），其中所述沸石材料含有基本金属与铝的比例（M:Al）为约0.10至约0.24的所述贱金属。

公开(公告)号：US20140072508A1

公开(公告)日：2014-03-13

申请号：US13997109

申请日：2011-12-21

申请人： Silke Sauerbeck ,  Frank Klose ,  Arno Tissler ,  Grigory Reznikov

发明人： Silke Sauerbeck ,  Frank Klose ,  Arno Tissler ,  Grigory Reznikov

IPC分类号： B01D53/56 ,  B01J29/89

CPC分类号： B01D53/565 ,  B01D53/8621 ,  B01D53/8628 ,  B01D53/9413 ,  B01J21/063 ,  B01J23/38 ,  B01J23/56 ,  B01J23/70 ,  B01J23/72 ,  B01J29/85 ,  B01J29/89 ,  B01J35/1019 ,  B01J35/1023 ,  B01J35/1028 ,  B01J37/0246 ,  C01B39/54 ,  Y02C20/10

摘要： The invention relates to a method for the selective catalytic transformation of nitrogen-containing compounds. The transformation relates to the selective catalytic reduction (SCR) of nitrogen oxides, or the selective catalytic oxidation (SCO) of nitrogen hydrides and nitrogen-containing organic compounds, preferably in waste gas flows of combustion processes with motors and without motors and industrial applications. The catalytic converter comprises a titano-(silico)-alumo-phosphate.

摘要翻译： 本发明涉及含氮化合物的选择性催化转化的方法。 该转化涉及氮氧化物的选择性催化还原（SCR）或氮化氢和含氮有机化合物的选择性催化氧化（SCO），优选在具有电动机和没有电动机和工业应用的燃烧过程的废气流中。 催化转化器包括钛 - （硅） - 钼 - 磷酸盐。

公开(公告)号：US20140050643A1

公开(公告)日：2014-02-20

申请号：US13987555

申请日：2013-08-05

申请人： Baoquan Zhang ,  Xiaoqing Zhang

发明人： Baoquan Zhang ,  Xiaoqing Zhang

IPC分类号： B01D53/68 ,  B01D53/50 ,  B01D53/52 ,  B01D53/62 ,  B01D53/54 ,  B01D53/64 ,  B01D53/56

CPC分类号： B01D53/86 ,  B01D53/00 ,  B01D53/50 ,  B01D53/507 ,  B01D53/52 ,  B01D53/54 ,  B01D53/56 ,  B01D53/60 ,  B01D53/62 ,  B01D53/64 ,  B01D53/68 ,  B01D53/75 ,  B01D53/76 ,  B01D53/8606 ,  B01D53/8609 ,  B01D53/8612 ,  B01D53/8621 ,  B01D53/8631 ,  B01D53/8637 ,  B01D53/8646 ,  B01D53/8659 ,  B01D53/8665 ,  B01D53/8671 ,  B01D2251/10 ,  B01D2251/102 ,  B01D2251/104 ,  B01D2251/106 ,  B01D2251/11 ,  B01D2251/2062 ,  B01D2252/102 ,  B01D2257/204 ,  B01D2257/2045 ,  B01D2257/2047 ,  B01D2257/302 ,  B01D2257/304 ,  B01D2257/40 ,  B01D2257/404 ,  B01D2257/504 ,  B01D2257/602 ,  B01D2258/0283 ,  B01D2259/804

摘要： A flue-gas purification system includes a flue-gas cycling system, a reactor, and an absorbent adding system having at least a catalytic absorbent, wherein the catalytic absorbent is being gasified for reacting with the flue-gas in the reactor in a homogenous gas-gas phase reacting manner. Therefore, the purification system has fast reaction rate between the pollutants of the flue-gas and the catalytic absorbent, which is preferably ammonia, to efficiently remove pollutants, so as to effectively purify the flue-gas.

摘要翻译： 烟道气净化系统包括烟道气循环系统，反应器和至少具有催化吸收剂的吸收剂添加系统，其中催化吸收剂被气化以使反应器中的烟道气与均匀的气体 气相反应方式。 因此，净化系统在烟气污染物和催化吸收剂（优选氨）之间具有较快的反应速率，以有效地除去污染物，从而有效地净化烟道气。

公开(公告)号：US07655205B2

公开(公告)日：2010-02-02

申请号：US10558448

申请日：2004-05-28

申请人： Petrus Franciscus Antonius Van Grinsven ,  Wiebe Sjoerd Kijlstra ,  Inge Roos ,  Cornelis Jacobus Smit

发明人： Petrus Franciscus Antonius Van Grinsven ,  Wiebe Sjoerd Kijlstra ,  Inge Roos ,  Cornelis Jacobus Smit

IPC分类号： B01D53/48 ,  B01D53/58

CPC分类号： B01D53/8621 ,  B01D53/1425 ,  B01D53/1468 ,  B01D53/8603 ,  C10K1/12 ,  C10K1/34 ,  C10K3/00 ,  Y10S423/17

摘要： Disclosed is a process for the removal of sulfur from a gas stream containing sulfur dioxide, hydrogen cyanide and hydrogen sulfide. The process includes a hydrogenation step, a hydrolysis step, an ammonia removal step and a hydrogen sulfide removal step. An aqueous alkaline washing liquid is used in the hydrogen sulfide removal step and with the spent sulfide containing washing liquid being regenerated using an oxidation bioreactor that utilizes sulfide oxidizing bacteria such as autotropic aerobic cultures of Thiobacillus and Thiomicrospira.

摘要翻译： 公开了从含有二氧化硫，氰化氢和硫化氢的气流中除去硫的方法。 该方法包括氢化步骤，水解步骤，除氨步骤和硫化氢去除步骤。 在硫化氢去除步骤中使用水性碱性洗涤液，并且使用利用硫化物氧化细菌如硫杆菌和硫杆菌的自转需氧培养物的氧化生物反应器再生废硫化物洗涤液。

公开(公告)号：US07368094B2

公开(公告)日：2008-05-06

申请号：US10948403

申请日：2004-09-23

申请人： Byong K. Cho ,  Jong-Hwan Lee

发明人： Byong K. Cho ,  Jong-Hwan Lee

IPC分类号： B01D53/56 ,  B01D53/94

CPC分类号： B01D53/90 ,  B01D53/32 ,  B01D53/8621 ,  B01D2251/104

摘要： Ozone, preferably produced in an ambient air stream passed through a non-thermal hyperplasma reactor, is added to the hot exhaust gas stream from a lean-burn (oxygen-rich) combustion source. The ozone converts much of the NO in the NOx containing exhaust stream to NO2. The resulting NO2/NOx ratio can be controlled by the input energy density to the plasma reactor. Ammonia and/or urea is added to the ozone treated exhaust in proportion to the NOx content, and the stream passed into contact with a reduction catalyst, such as a base metal-exchanged zeolite, to convert the NOx to nitrogen.

摘要翻译： 优选在通过非热等离子体反应器的环境空气流中产生的臭氧被添加到来自稀燃（富氧）燃烧源的热废气流中。 臭氧将含有NO 的排气流中的大部分NO转化为NO 2。 可以通过等离子体反应器的输入能量密度来控制所得到的NO 2 2 / NO x比率。 将氨和/或尿素与NO x含量成比例地添加到经臭氧处理的废气中，并且流与还原催化剂如贱金属交换的沸石接触以将 NO x向氮。

公开(公告)号：US06484733B2

公开(公告)日：2002-11-26

申请号：US09792797

申请日：2001-02-23

申请人： Richard Budin ,  Krzysztof Krotla ,  Hermann Rabitsch

发明人： Richard Budin ,  Krzysztof Krotla ,  Hermann Rabitsch

IPC分类号： B08B704

CPC分类号： B01J38/64 ,  B01D53/8621 ,  B01D53/8662 ,  B01D53/96 ,  B01J23/92 ,  B01J38/48 ,  B01J38/60

摘要： Used deNOx or dedioxin catalytic converters are regenerated by washing the catalyst with a solution of surface-active substances in a liquid. At the same time, metal compounds are added for creating active centers.

摘要翻译： 通过用表面活性物质在液体中的溶液洗涤催化剂来再生二氧化氮或杜仲毒素催化转化器。 同时，添加金属化合物以形成活性中心。

公开(公告)号：US06482376B2

公开(公告)日：2002-11-19

申请号：US09799542

申请日：2001-03-05

申请人： Walter Fischer ,  Ronald Neufert

发明人： Walter Fischer ,  Ronald Neufert

IPC分类号： C01G3000

CPC分类号： F01N3/2066 ,  B01D53/8621 ,  B01D53/8628 ,  B01D53/9404 ,  B01D53/9418 ,  B01D2251/2067 ,  B01D2255/20707 ,  B01J23/28 ,  B01J23/30 ,  F01N2610/02 ,  Y02T10/24

摘要： A process is provided for the catalytic removal of polycyclic aromatic nitro, nitroso and/or amino compounds from the exhaust gas of a combustion system, in particular a diesel engine. The exhaust gas is brought into contact with a catalytic converter which includes a catalytically active material that contains titanium dioxide, at a temperature of from 150 to 600° C. The polycyclic aromatic compounds are oxidized at the catalytic converter through the use of oxygen to form nitrogen oxides, carbon dioxide and water.

摘要翻译： 提供了用于从燃烧系统，特别是柴油发动机的排气中催化除去多环芳基硝基，亚硝基和/或氨基化合物的方法。 废气与催化转化器接触，催化转化器包括在150-600℃的温度下含有二氧化钛的催化活性物质。多环芳族化合物在催化转化器中通过使用氧来形成 氮氧化物，二氧化碳和水。

公开(公告)号：US06284807B1

公开(公告)日：2001-09-04

申请号：US09134304

申请日：1998-08-14

申请人： Stephen C. Leviness ,  Charles J. Mart ,  William C. Behrmann ,  Stephen J. Hsia ,  Daniel R. Neskora

发明人： Stephen C. Leviness ,  Charles J. Mart ,  William C. Behrmann ,  Stephen J. Hsia ,  Daniel R. Neskora

IPC分类号： C07C104

CPC分类号： C10K1/34 ,  B01D53/14 ,  B01D53/8621 ,  B01D2255/20707 ,  B01D2257/406 ,  B01D2257/408 ,  C01B3/52 ,  C01B3/56 ,  C01B3/58 ,  C01B2203/0415 ,  C01B2203/0435 ,  C01B2203/0465 ,  C10G2/30

摘要： A slurry catalytic hydrocarbon synthesis process which employs a catalyst comprising a supported cobalt component achieves a short term catalyst half life of more than 10 days, by using a syngas feed which contains less than fifty parts per billion of a combined total amount of HCN and NH3.

摘要翻译： 使用包含负载的钴组分的催化剂的淤浆催化烃合成方法通过使用含有少于每十亿份HCN和NH 3的总量的合成气进料的短期催化剂半衰期超过10天 。