会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 1. 发明授权
    • Copper-silver zeolite catalysts
    • 铜 - 银沸石催化剂
    • US5908806A
    • 1999-06-01
    • US857640
    • 1997-05-16
    • Karl C. C. Kharas
    • Karl C. C. Kharas
    • B01D53/94B01J29/068B01J29/072B01J29/44B01J29/46B01J29/68B01J29/76B01J29/06
    • B01D53/945B01J29/068B01J29/072B01J29/44B01J29/46Y02T10/22
    • A catalyst for the removal of carbon monoxide, hydrocarbons and nitrogen oxides in an exhaust gas made by a process comprising:a) preparing a suspension comprising a liquid, a zeolite, a weak base, and salts of copper and silver,said zeolite being crystalline and having a Si/Al atomic ratio between about 5 and about 100, a pore size between about 0.5 nm and about 1.3 nm, essentially no octahedral aluminum detectable by .sup.27 Al NMR spectroscopy and a sodium ion exchange capacity, with regard to total aluminum content, greater than 75%, and wherein said suspension contains sufficient amounts of said copper and silver salts to result in a copper content in said catalyst, when finished, between about 0.5 wt. % and about 12 wt. % and a silver content between about 0.25 wt. % and about 20 wt. %;b) adding a sufficient amount of a strong base to raise the pH of the suspension to between about 7 and about 9, thereby creating a metal-containing zeolite support in said suspension;c) separating the support from said liquid;d) dispersing said support on a substrate; ande) drying and calcining the product of step (d).
    • 一种用于除去废气中的一氧化碳,烃和氮氧化物的催化剂,其通过包括以下步骤的方法制备:a)制备包含液体,沸石,弱碱和铜和银的盐的悬浮液,所述沸石是结晶 并且Si / Al原子比在约5至约100之间,孔径在约0.5nm至约1.3nm之间,基本上没有可通过27Al NMR光谱检测的八面体铝和钠离子交换容量,关于总铝含量, 大于75%,并且其中所述悬浮液含有足够量的所述铜和银盐,以使所述催化剂中的铜含量在完成时在约0.5wt。 %和约12wt。 %,银含量在约0.25wt。 %和约20wt。 %; b)加入足够量的强碱以将悬浮液的pH提高至约7至约9,从而在所述悬浮液中产生含金属的沸石载体; c)将载体与所述液体分离; d)将所述载体分散在基材上; 和e)干燥和煅烧步骤(d)的产物。
    • 5. 发明授权
    • Reduction of NOx in the exhaust from leanOx internal combustion engines
    • 减少来自稀燃内燃机的排气中的NOx
    • US06365118B1
    • 2002-04-02
    • US09387083
    • 1999-08-31
    • Karl C. C. KharasHeinz J. Robota
    • Karl C. C. KharasHeinz J. Robota
    • B01D5394
    • B01D53/945B01D53/9418B01D53/9454B01D2251/208B01D2255/1021B01D2255/1025B01D2255/104B01D2255/2042B01D2255/20746B01D2255/20761B01D2255/9207B01J35/0006B01J2219/007B01J2219/00745B01J2219/00747C40B30/08C40B40/18Y02T10/22Y02T10/24
    • A process for removal of carbon monoxide, hydrocarbons, and nitrogen oxides from the exhaust gas from lean-burn, diesel and other engines which produce exhaust gases containing excess oxygen is disclosed. An exhaust gas from an engine operating at an air-fuel ratio above about 18 is contacted with a multi-component catalyst having at least two catalytic components, each capable of reducing nitrogen oxides within a range of exhaust gas temperatures that is different from the range of exhaust gas temperatures within which each other component is capable of reducing nitrogen oxides. Oxidation of the remaining reducing gases is also accomplished. One example of a two catalytic component catalyst of this invention has a first component of Au supported on alumina, which reduces nitrogen oxides at exhaust gas temperatures between about 600° C. and 900° C., and a second component of Pt supported on Y-zeolite, which reduces nitrogen oxides at exhaust gas temperatures below 600° C.; an example of a three catalytic component catalyst of this invention has a first component of CoO supported on &ggr;-alumina, which reduces nitrogen oxides at exhaust gas temperatures above about 475° C., a second component of an alloy of Pt, Rh and Co supported on BaO2-stabilized &dgr;-alumina, which reduces nitrogen oxides at exhaust gas temperatures between about 315° C. and about 475° C. and a third component of an alloy of Pt and Rh supported on &ggr;-alumina, which reduces nitrogen oxides at exhaust gas temperatures between about 200° C. and about 425° C.
    • 公开了从产生含有过量氧气的废气的来自稀燃燃烧,柴油和其它发动机的废气中除去一氧化碳,碳氢化合物和氮氧化物的方法。 来自以大于约18的空燃比工作的发动机的废气与具有至少两个催化组分的多组分催化剂接触,每个催化组分能够在不同于范围的废气温度范围内还原氮氧化物 的排气温度,其中每个其它组分能够还原氮氧化物。 还实现了剩余还原气体的氧化。 本发明的两种催化组分催化剂的一个实例具有负载在氧化铝上的Au的第一组分,其在约600℃和900℃之间的废气温度下还原氮氧化物,并且在Y上负载的Pt的第二组分 沸石,其在低于600℃的废气温度下还原氮氧化物; 本发明的三种催化组分催化剂的实例具有负载在γ-氧化铝上的CoO的第一组分,其在高于约475℃的废气温度下还原氮氧化物,Pt,Rh和Co的合金的第二组分 负载在BaO 2稳定的δ-氧化铝上,其在约315℃至约475℃的废气温度下还原氮氧化物,并且负载在γ-氧化铝上的Pt和Rh的合金的第三组分,其还原氮氧化物 在约200℃至约425℃的废气温度下
    • 8. 发明授权
    • Barium-containing alumina
    • 含钡氧化铝
    • US5389589A
    • 1995-02-14
    • US994838
    • 1992-12-22
    • Karl C. C. Kharas
    • Karl C. C. Kharas
    • B01J23/02C01F7/02C04B35/111C04B35/624C04B35/10
    • C04B35/111C04B35/624
    • The present invention is a barium-containing alumina with the X-ray pattern of the FIGURE. The alumina may be synthesized by simultaneously adding a polyether or a polyalcohol and an aqueous solution of a water soluble barium carboxylate to an aqueous boehmite sol or suspension to form a gel, the gel having a polyether or polyalcohol content of about 2 wt. % to about 26 wt. %, preferably about 10 wt. % to about 20 wt. %. The gel is then dried and calcined to convert it to an essentially pure barium-containing delta alumina. The alumina may be optionally hydrothermally treated to induce further crystallization. The final product contains about 2 wt. % to about 18 wt. % Ba, preferably about 8 wt. % to about 12 wt. %.
    • 本发明是具有图的X射线图案的含钡氧化铝。 氧化铝可以通过将聚醚或多元醇和水溶性羧酸钡的水溶液同时加入到勃姆石溶液或悬浮液中以形成凝胶来合成,该凝胶具有约2重量%的聚醚或多元醇含量。 %至约26wt。 %,优选约10wt。 %至约20wt。 %。 然后将凝胶干燥并煅烧以将其转化为基本上纯的含钡的δ氧化铝。 氧化铝可以任选地进行水热处理以诱导进一步结晶。 最终产品含有约2重量% %至约18wt。 %Ba,优选约8wt。 %至约12wt。 %。
    • 10. 发明授权
    • Reduction of NO.sub.x in the exhaust gases from internal combustion
engines containing excess oxygen
    • 减少含有过量氧气的内燃机废气中的NOx
    • US6087295A
    • 2000-07-11
    • US107673
    • 1998-06-30
    • Karl C. C. KharasHeinz J. Robota
    • Karl C. C. KharasHeinz J. Robota
    • B01D53/94B01J35/00C40B30/08C40B40/18B01J21/04B01J29/04
    • B01D53/945B01D53/9418B01D53/9454B01J35/0006B01D2251/208B01D2255/1021B01D2255/1025B01D2255/104B01D2255/2042B01D2255/20746B01D2255/20761B01D2255/9207B01J2219/007B01J2219/00745B01J2219/00747C40B30/08C40B40/18Y02T10/22Y02T10/24
    • Removal of carbon monoxide, hydrocarbons, and nitrogen oxides from the exhaust gas from lean-burn, diesel and other engines which produce exhaust gases containing excess oxygen is provided by a multi-component catalyst having at least two catalytic components, each capable of reducing nitrogen oxides within a range of exhaust gas temperatures that is different from the range of exhaust gas temperatures within which each other component is capable of reducing nitrogen oxides. Oxidation of the remaining reducing gases is also accomplished. One example of a two catalytic component catalyst of this invention has a first component of Au supported on alumina, which reduces nitrogen oxides at exhaust gas temperatures between about 600.degree. C. and 900.degree. C., and a second component of Pt supported on Y-zeolite, which reduces nitrogen oxides at exhaust gas temperatures below 600.degree. C.; an example of a three catalytic component catalyst of this invention has a first component of CoO supported on .gamma.-alumina, which reduces nitrogen oxides at exhaust gas temperatures above about 475.degree. C., a second component of an alloy of Pt, Rh and Co supported on BaO.sub.2 -stabilized .delta.-alumina, which reduces nitrogen oxides at exhaust gas temperatures between about 315.degree. C. and about 475.degree. C. and a third component of an alloy of Pt and Rh supported on .alpha.-alumina, which reduces nitrogen oxides at exhaust gas temperatures between about 200.degree. C. and about 425.degree. C. A method of selecting such catalysts is also provided.
    • 通过具有至少两种能够还原氮的催化剂组分的多组分催化剂来提供从产生含有过量氧气的废气的来自稀燃燃烧的废气,柴油和其它发动机中除去一氧化碳,碳氢化合物和氮氧化物 废气温度范围内的氧化物不同于其中每个其它组分能够还原氮氧化物的废气温度的范围。 还实现了剩余还原气体的氧化。 本发明的两种催化组分催化剂的一个实例具有负载在氧化铝上的Au的第一组分,其在约600℃和900℃之间的废气温度下还原氮氧化物,并且在Y上负载的Pt的第二组分 沸石,其在低于600℃的废气温度下还原氮氧化物。 本发明的三催化组分催化剂的实例具有负载在γ-氧化铝上的CoO的第一组分,其在高于约475℃的废气温度下还原氮氧化物,Pt,Rh和Co的合金的第二组分 负载在BaO 2稳定的δ-氧化铝上,其在约315℃至约475℃的废气温度下还原氮氧化物,并且负载在α-氧化铝上的Pt和Rh的合金的第三组分,其还原氮氧化物 在约200℃至约425℃的废气温度下。还提供了选择这种催化剂的方法。