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公开(公告)号:US07393512B2
公开(公告)日:2008-07-01
申请号:US10510490
申请日:2003-03-21
申请人: Meinhard Schwefer , Michael Groves
发明人: Meinhard Schwefer , Michael Groves
IPC分类号: B01D53/56
CPC分类号: B01D53/8625 , B01D2251/202 , B01D2251/204 , B01D2251/208 , B01D2255/20738 , B01D2255/50 , B01D2257/402 , B01D2257/404 , Y02C20/10
摘要: A process for reducing the content of NOx and N2O in gases, in particular in process gases and offgases, which comprises the measures: a) addition of at least one nitrogen-containing reducing agent to the NOx- and N2O-containing gas in at least the amount required for complete reduction of the NOx; b) addition of a hydrocarbon, of carbon monoxide, of hydrogen, or of a mixture of one or more of these gases to the NOx- and N2O-containing gas for the reduction of the N2O; and c) introduction of the gas mixture into at least one reaction zone at temperatures of up to 450° C., which contains one or more iron-laden zeolites. The process can be used, in particular, in nitric acid production, for offgases from power stations or for gas turbines.
摘要翻译: 一种降低气体,特别是工艺气体和废气中的NO x和N 2 O的含量的方法,其包括以下措施:a)添加至少一种 含氮还原剂至少达到完全还原NO x所需的量的含NO x和N 2 O的含有气体 >; b)将一种一氧化碳的氢气或这些气体中的一种或多种的混合物的碳氢化合物加入到含N 2 O 2的N 2 O 3和N 2 O 气体用于还原N 2 O; 和c)在至多450℃的温度下,将气体混合物引入到至少一个反应区,其含有一个或多个含铁沸石。 该方法特别可用于硝酸生产,用于发电站或燃气轮机的废气。
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公开(公告)号:US20050244320A1
公开(公告)日:2005-11-03
申请号:US10510490
申请日:2003-03-21
申请人: Meinhard Schwefer , Michael Groves
发明人: Meinhard Schwefer , Michael Groves
CPC分类号: B01D53/8625 , B01D2251/202 , B01D2251/204 , B01D2251/208 , B01D2255/20738 , B01D2255/50 , B01D2257/402 , B01D2257/404 , Y02C20/10
摘要: A process for reducing the content of NOx and N2O in gases, in particular in process gases and offgases, which comprises the measures: a) addition of at least one nitrogen-containing reducing agent to the NOx- and N2O-containing gas in at least the amount required for complete reduction of the NOx, b) addition of a hydrocarbon, of carbon monoxide, of hydrogen or of a mixture of one or more of these gases to the NOx- and N2O-containing gas for the reduction of the N2O and c) introduction of the gas mixture into at least one reaction zone at temperatures of up to 450° C. which contains one or more iron-laden zeolites, is described. The process can be used, in particular, in nitric acid production, for offgases from power stations or for gas turbines.
摘要翻译: 一种降低气体,特别是工艺气体和废气中的NO x和N 2 O的含量的方法,其包括以下措施:a)添加至少一种 含氮还原剂至少达到完全还原NO x所需的量的含NO x和N 2 O的含有气体 ,b)将一种一氧化碳的氢气或这些气体中的一种或多种的混合物加入到NO 2 - 和N 2 O- 以及c)将气体混合物引入到至多一个反应区域中,所述反应区域在高达450℃的温度下,其含有一种或多种含铁载体的沸石, 被描述。 该方法特别可用于硝酸生产,用于发电站或燃气轮机的废气。
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3.
公开(公告)号:US09108175B2
公开(公告)日:2015-08-18
申请号:US12451874
申请日:2008-05-28
申请人: Meinhard Schwefer , Michael Groves , Jürgen Fuchs , Rainer Maurer , Rolf Siefert , Bernhard Hündgen
发明人: Meinhard Schwefer , Michael Groves , Jürgen Fuchs , Rainer Maurer , Rolf Siefert , Bernhard Hündgen
CPC分类号: B01J8/008 , B01J8/02 , B01J8/025 , B01J8/0278 , B01J8/0285 , B01J15/005 , B01J19/002 , B01J2208/00176 , B01J2208/00203 , B01J2208/00212 , B01J2208/00495 , B01J2208/0053 , B01J2208/00716 , B01J2219/00006 , B01J2219/00263 , B01J2219/025 , C01B21/265 , C01B21/28
摘要: Improved reactors for catalytic, exothermic gas-phase reactions having, viewed in the flow direction of a feed gas, an inlet zone (1), a reaction zone (2) containing at least one catalyst (4), and an outlet zone (3) for the product gas, are described. The reactors are provided in the inlet zone (1) or in the inlet zone (1) and the reaction zone (2) with an insulating liner (6) and/or apparatuses for the transport of cooling media and/or the interior walls of the reactor in the inlet zone (1) or in the inlet zone (1) and the reaction zone (2) consist of inert material. The insulating liner and/or cooling media reduce heat transport from the reaction zone (2) into the inlet zone (1) and thus reduce the risk of preignition of the feed gas mixture used or occurrence of undesirable secondary reactions in the inlet zone (1).
摘要翻译: 在进料气体的流动方向上观察催化,放热气相反应的改进的反应器,入口区(1),含有至少一种催化剂(4)的反应区(2)和出口区(3) )用于产品气体。 反应器在入口区域(1)或入口区域(1)和反应区域(2)中设置有绝缘衬垫(6)和/或用于输送冷却介质和/或内壁的内壁的装置 入口区(1)或入口区(1)和反应区(2)中的反应器由惰性材料组成。 绝缘衬垫和/或冷却介质减少了从反应区域(2)进入入口区域(1)的热传递,从而降低了进料区域(1)中所使用的进料气体混合物的预先燃烧或不期望的二次反应的出现的风险 )。
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公开(公告)号:US20130149225A1
公开(公告)日:2013-06-13
申请号:US13700853
申请日:2011-05-09
IPC分类号: B01D53/86
CPC分类号: B01D53/869 , B01D53/8628 , B01D53/8631 , B01D2255/20738 , B01D2255/50 , B01D2255/504 , B01D2257/402 , B01J29/072 , B01J29/46 , B01J37/0009 , Y02C20/10
摘要: A process for removing N2O and NOx from offgases by catalytic decomposition of N2O by means of iron-containing zeolite catalysts and catalytic reduction of the NOx by means of reducing agents, the deNOx stage connected downstream of the deN2O stage being operated at inlet temperatures of T
摘要翻译: 一种通过使用含铁沸石催化剂催化分解N2O并通过还原剂催化还原NOx的方法从废气中除去N2O和NOx,脱硝阶段连接在脱硝阶段的下游,在入口温度为T 并且具有选择的N 2 O / NO x比例的deN2O阶段的入口气体,并且选择脱硝阶段的温度,压力和空间速度的操作参数,以得到N 2 O 降解80〜98%。 在这些条件下,在脱硝阶段的出口处建立了30-70%的NOx氧化程度,其定义为NO 2的摩尔量与NOx的总摩尔量的比率。 其结果是下游脱硝阶段可以在最佳条件下运行。 还提供了一种用于执行该过程的装置。
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5.
公开(公告)号:US20100166631A1
公开(公告)日:2010-07-01
申请号:US12451874
申请日:2008-05-28
申请人: Meinhard Schwefer , Michael Groves , Jürgen Fuchs , Rainer Maurer , Rolf Siefert , Bernhard Hündgen
发明人: Meinhard Schwefer , Michael Groves , Jürgen Fuchs , Rainer Maurer , Rolf Siefert , Bernhard Hündgen
CPC分类号: B01J8/008 , B01J8/02 , B01J8/025 , B01J8/0278 , B01J8/0285 , B01J15/005 , B01J19/002 , B01J2208/00176 , B01J2208/00203 , B01J2208/00212 , B01J2208/00495 , B01J2208/0053 , B01J2208/00716 , B01J2219/00006 , B01J2219/00263 , B01J2219/025 , C01B21/265 , C01B21/28
摘要: Improved reactors for catalytic, exothermic gas-phase reactions, which comprise, viewed in the flow direction of a feed gas, an inlet zone (1), a reaction zone (2) containing at least one catalyst (4) an outlet zone (3) for the product gas, are described. The reactors are provided in the region of the inlet zone (1) or in the region of the inlet zone (1) and the reaction zone (2) with means, for example an insulating liner (6) and/or apparatuses for the transport of cooling media, which reduce heat transport from the reaction zone (2) into the inlet zone (1) and thus reduce the risk of preignition of the feed gas mixture used or occurrence of undesirable secondary reactions in the inlet zone (1) and/or the interior walls of the reactor in the region of the inlet zone (1) or in the region of the inlet zone (1) and the reaction zone (2) consist of inert material.The reactors can be used, in particular, for the oxidation of ammonia, for example in nitric acid plants in which transition metal catalysts configured as honeycombs and having smaller cross sections than the platinum gauzes customarily used are preferably used.
摘要翻译: 改进的用于催化,放热气相反应的反应器,其包括在进料气体的流动方向上观察入口区域(1),含有至少一种催化剂的反应区域(2),出口区域(3) )用于产品气体。 反应器在入口区域(1)的区域中或在入口区域(1)和反应区域(2)的区域中设置有例如绝缘衬垫(6)和/或用于运输的装置 的冷却介质,其减少从反应区域(2)进入入口区域(1)的热传递,并且因此降低了所使用的进料气体混合物的预先燃烧或在入口区域(1)中产生不期望的次级反应的风险和/ 或在入口区域(1)的区域中或在入口区域(1)和反应区域(2)的区域内的反应器的内壁由惰性材料构成。 反应器特别可用于氨的氧化,例如在硝酸设备中,其中优选使用配置为蜂窝状的过渡金属催化剂并且具有比通常使用的铂网布更小的横截面。
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公开(公告)号:US20060051277A1
公开(公告)日:2006-03-09
申请号:US10516918
申请日:2003-06-10
申请人: Meinhard Schwefer , Michael Groves , Rolf Siefert , Rainer Maurer
发明人: Meinhard Schwefer , Michael Groves , Rolf Siefert , Rainer Maurer
IPC分类号: B01D53/56
CPC分类号: B01J29/7007 , B01D53/8628 , B01D2255/20738 , B01D2255/50 , B01D2257/402 , B01D2257/404 , B01J8/008 , B01J8/0411 , B01J8/0415 , B01J8/0453 , B01J29/08 , B01J29/14 , B01J29/18 , B01J29/24 , B01J29/46 , B01J29/65 , B01J29/68 , B01J29/7615 , B01J2208/00539 , B01J2208/00849 , B01J2208/025 , Y02C20/10
摘要: The method comprises the following steps: conduction of the gas containing N2O and NOx over a series of two catalyst beds consisting of one or more zeolites° charged with iron: addition of a reduction agent for NOx between the catalyst beds; setting of a temperature of less than 500° C. in the first and second catalyst bed; setting of a gas pressure of at least 2 bar in the two catalyst beds; and the selection of a space velocity in the first and second catalyst bed that achieves a degradation of the N2O content of the gas in the first catalyst bed by a maximum of up to 90%, in relation to the N2O content at the entrance to the catalyst bed and an additional degradation of the N2O content of the gas in the second catalyst bed by at least 30% in relation to the N2O content at the entrance to the second catalyst bed. The first reaction zone is used to degrade the N2O and the second reaction zone reduces the NOx and breaks down at least part of the remaining N2O. The inventive device comprises at least one radially traversed catalyst bed.
摘要翻译: 该方法包括以下步骤:在由一种或多种带铁的沸石组成的一系列两个催化剂床上传导含有N 2 O和NO x的气体: 在催化剂床之间加入NO x还原剂; 在第一和第二催化剂床中设定小于500℃的温度; 在两个催化剂床中设定至少2巴的气体压力; 以及第一和第二催化剂床中的空速的选择,其使第一催化剂床中的气体的N 2 O 2含量降低最多达90%,相对于 在催化剂床入口处的N 2 O 2含量和第二催化剂床中气体的N 2 O 2含量的另外降解至少30% 相对于第二催化剂床入口处的N 2 O O含量。 第一反应区用于降解N 2 O 2,并且第二反应区减少NO x X并破坏剩余的N 2 O 2的至少一部分, / SUB> O。 本发明的装置包括至少一个径向穿过的催化剂床。
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公开(公告)号:US10022669B2
公开(公告)日:2018-07-17
申请号:US13700853
申请日:2011-05-09
IPC分类号: B01D53/56 , B01D53/86 , B01J29/072 , B01J29/46 , B01J37/00
摘要: A process for removing N2O and NOx from offgases by catalytic decomposition of N2O by means of iron-containing zeolite catalysts and catalytic reduction of the NOx by means of reducing agents, the deNOx stage connected downstream of the deN2O stage being operated at inlet temperatures of T
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8.
公开(公告)号:US20120034148A1
公开(公告)日:2012-02-09
申请号:US12998775
申请日:2009-12-01
申请人: Meinhard Schwefer , Michael Groves , Jürgen Fuchs , Rainer Maurer , Rolf Siefert , Bernhard Hündgen
发明人: Meinhard Schwefer , Michael Groves , Jürgen Fuchs , Rainer Maurer , Rolf Siefert , Bernhard Hündgen
CPC分类号: B01J8/0285 , B01J8/008 , B01J8/025 , B01J8/0278 , B01J12/007 , B01J15/005 , B01J19/0013 , B01J19/002 , B01J19/2485 , B01J19/26 , B01J2208/00203 , B01J2208/00212 , B01J2208/00495 , B01J2208/00548 , B01J2208/00716 , B01J2219/00083 , B01J2219/00094 , B01J2219/00119 , B01J2219/00155 , B01J2219/00164 , B01J2219/00245 , B01J2219/32296 , B01J2219/324 , C01B21/26 , C01B21/267 , C01B21/28 , C01C3/022
摘要: Improved reactors for catalytic, exothermic gas phase reactions with, as seen in the flow direction of a feed gas, which contains at least one oxidant and at least one component to be oxidized, an entry zone (1), a reaction zone (2) comprising at least one catalyst (4) and an exit zone (3) for the product gas are described. The reactors, at least in the area of the entry zone (1), have means, for example insulating jackets (6) and/or devices for the transport of cooling agents, which decrease the transport of heat produced in the reaction zone (2) into the entry zone (1) and thus decrease the risks of pre-ignition of the feed gas mixture employed or of the course of undesired side reactions in the entry zone (1) and/or wherein the inner walls of the reactor, at least in the area of the entry zone (1), are elaborated from inert material.The feed gas enters into the entry zone (1) as a homogeneous gas mixture with respect to its substance composition via one or more feed lines (30).The reactors can especially be employed for ammonia oxidation, for example in nitric acid plants, in which transition metal catalysts preferably elaborated in honeycomb form with smaller cross sections than the customarily employed platinum gauzes are used.
摘要翻译: 如在进料气体的流动方向上看到的含有至少一种氧化剂和至少一种待氧化的组分的入口区域(1),反应区域(2)的改进的催化,放热气相反应器, 描述了至少一种用于产品气体的催化剂(4)和出口区(3)。 至少在进入区域(1)的区域中的反应器具有诸如用于输送冷却剂的绝缘套(6)和/或装置的装置,这减少了在反应区(2)中产生的热的传输 )进入进入区(1),从而降低进料区(1)中所采用的进料气体混合物的预点火风险或不期望的副反应过程的风险,和/或其中反应器的内壁在 至少在进入区域(1)的区域,由惰性材料制成。 进料气体通过一个或多个进料管线(30)相对于其物质组合物作为均匀气体混合物进入入口区域(1)。 反应器可以特别用于氨氧化,例如在硝酸设备中,其中优选使用具有小于通常使用的铂网的横截面的蜂窝形式的过渡金属催化剂。
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公开(公告)号:US07462340B2
公开(公告)日:2008-12-09
申请号:US10516918
申请日:2003-06-10
申请人: Meinhard Schwefer , Michael Groves , Rolf Siefert , Rainer Maurer
发明人: Meinhard Schwefer , Michael Groves , Rolf Siefert , Rainer Maurer
CPC分类号: B01J29/7007 , B01D53/8628 , B01D2255/20738 , B01D2255/50 , B01D2257/402 , B01D2257/404 , B01J8/008 , B01J8/0411 , B01J8/0415 , B01J8/0453 , B01J29/08 , B01J29/14 , B01J29/18 , B01J29/24 , B01J29/46 , B01J29/65 , B01J29/68 , B01J29/7615 , B01J2208/00539 , B01J2208/00849 , B01J2208/025 , Y02C20/10
摘要: The disclosure involves a method for reducing the content of NOx and N2O in gases. The method includes the conduction of a gas containing N2O and NOX over a series of two catalyst beds containing of one or more zeolites charged with iron followed by the: addition of a reduction agent for NOX between the catalyst beds. The first catalyst bed reaction zone is used to degrade the N2O and the catalyst bed second reaction zone reduces the NOX and breaks down at least part of the remaining N2O. The inventive device comprises at least one radially traversed catalyst bed.
摘要翻译: 本公开涉及一种降低气体中NOx和N2O含量的方法。 该方法包括在含有一个或多个带有铁的沸石的一系列两个催化剂床上传导含有N 2 O和NO x的气体,然后在催化剂床之间加入NO x还原剂。 第一催化剂床反应区用于降解N2O,催化剂床第二反应区减少NO x并分解剩余的N2O的至少一部分。 本发明的装置包括至少一个径向穿过的催化剂床。
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公开(公告)号:US20080241034A1
公开(公告)日:2008-10-02
申请号:US11913450
申请日:2006-04-27
申请人: Meinhard Schwefer , Rolf Siefert , Michael Groves
发明人: Meinhard Schwefer , Rolf Siefert , Michael Groves
IPC分类号: B01D53/56
CPC分类号: B01D53/8628 , B01D2251/202 , B01D2251/204 , B01D2251/2062 , B01D2251/208 , B01D2255/20738 , B01D2255/50 , B01D2257/402 , B01D2257/404 , Y02C20/10
摘要: The method comprises passing an N2O- and NOx-containing gas over a sequence of two catalyst beds, adding reducing agents for NOx and for N2O between the catalyst beds in such an amount that not only NOx but also a predetermined proportion of N2O is reduced. The reaction conditions are set so that the N2O content of the gas is reduced by not more than 95%, based on the N2O content at the entrance of the first catalyst bed, by decomposition to nitrogen and oxygen in the first catalyst bed and that not only chemical reduction of NOx but also chemical reduction of N2O occurs in the second catalyst bed so that the N2O content of the gas is reduced by at least 50%, based on the N2O content at the entrance of the second catalyst bed.
摘要翻译: 该方法包括在两个催化剂床的序列上通过含N 2 O和NO x-x N的气体,向其中加入还原剂, 并且催化剂床之间的N 2 O 2的量不仅仅是NO 2 x N 2,而且N 2 O 2的预定比例减少 。 设定反应条件使得气体的N 2 O 2 O含量基于在入口处的N 2 O 2含量降低不超过95% 第一催化剂床,通过在第一催化剂床中分解成氮气和氧气,并且不仅在第二催化剂床中发生NO 2 X的化学还原,而且还发生N 2 O 2的化学还原 催化剂床,使得气体的N 2 O 2 O含量基于第二催化剂床入口处的N 2 O 2含量降低至少50%。
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