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    • 6. 发明申请
    • Method for NOx reduction
    • 降低NOx的方法
    • US20040042947A1
    • 2004-03-04
    • US10648885
    • 2003-08-26
    • John HoardChristopher L. AardahlPaul W. Park
    • B01J008/00C01B021/00
    • F01N3/2066B01D53/32B01D53/9418B01D53/9431B01D2251/208B01D2251/21B01D2255/104B01D2255/2027B01D2255/2042B01D2255/2092B01D2255/2094B01D2255/50F01N3/0814F01N3/0842F01N3/0892F01N3/2006F01N3/206F01N13/009F01N2240/28F01N2250/12F01N2330/06F01N2370/24F01N2610/03Y02C20/30Y02T10/24Y02T10/26
    • A method for reducing NOx in a gas stream by sequentially exposing the gas stream to a first and a second catalyst. The first catalyst converts at least a portion of the gas stream to a reducing gas, it reduces at least a portion of the NOx in a first temperature range, and it absorbs at least a portion of the NOx in the first temperature range. The second catalyst reduces at least a portion of the NOx in a second temperature range utilizing the reducing gas produced by the second catalyst. The reducing gas produced by the first catalyst is typically a partially oxidized hydrocarbon, preferably an aldehyde, and more preferably acetaldehyde or formaldehyde. In addition to the first and second catalysts, the gas stream may be exposed to a plasma. Preferably, the first catalyst is selected as a zeolite, and more preferably a zeolite impregnated with a cation. The cation is preferably selected from the group consisting of an alkaline cation, an alkaline earth cation, and combinations thereof and preferably exhibits pores sizes of greater than 4 angstroms, and more preferably exhibits pores sizes of greater than 7 angstroms. The second catalyst is preferably a null-alumina catalyst, and more preferably a null-alumina catalyst impregnated with transition metals, including, but not limited to, Ag, In and Sn.
    • 一种通过将气流顺序地暴露于第一和第二催化剂来还原气流中的NOx的方法。 第一催化剂将至少一部分气流转化为还原气体,其在第一温度范围内减少NOx的至少一部分,并且其在第一温度范围内吸收至少一部分NOx。 第二催化剂利用由第二催化剂产生的还原气体在第二温度范围内还原NOx的至少一部分。 由第一催化剂产生的还原气体通常是部分氧化的烃,优选醛,更优选乙醛或甲醛。 除了第一和第二催化剂之外,气流可以暴露于等离子体。 优选地,选择第一催化剂作为沸石,更优选选择用阳离子浸渍的沸石。 阳离子优选选自碱性阳离子,碱土金属阳离子及其组合,并且优选显示大于4埃的孔径,更优选地具有大于7埃的孔径。 第二催化剂优选是γ-氧化铝催化剂,更优选浸渍有过渡金属的γ-氧化铝催化剂,包括但不限于Ag,In和Sn。
    • 7. 发明申请
    • Process for removing nitrogen oxides from gases
    • 从气体中除去氮氧化物的方法
    • US20030124041A1
    • 2003-07-03
    • US10326970
    • 2002-12-24
    • Linde Aktiengesellschaft
    • Hartmut NeumannUlrike Wenning
    • C01B021/00
    • B01D53/565
    • The invention relates to a process for removing nitrogen oxides from a fluid, the fluid being the feed air or a product or product mixture or a process fluid of an air separation plant. According to the invention, the nitrogen oxides are removed by chemisorption on metal oxides. The metal oxides are preferably formed from metals of the 6th to 8th subgroup, manganese dioxide (MnO2) being particularly preferred as the metal oxide. The process can comprise one or more reactor beds, which are preferably operated at 10 to 40null C. and are regenerated with nitrogen at a temperature from 130 to 170null C. The process can be used for the recovery of gases of extreme purity, for example for the manufacture of semiconductors.
    • 本发明涉及从流体中除去氮氧化物的方法,流体是进料空气或空气分离设备的产物或产物混合物或工艺流体。 根据本发明,通过金属氧化物上的化学吸附除去氮氧化物。 金属氧化物优选由第6〜8族的金属形成,特别优选作为金属氧化物的二氧化锰(MnO 2)。 该方法可以包括一个或多个反应器床,其优选在10至40℃下操作,并在130-170℃的温度下用氮气再生。该方法可用于回收极端纯度的气体, 例如用于制造半导体。