专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US5830346A FCC regenerator in partial CO burn with downstream air addition 失效
标题翻译： FCC再生器部分CO燃烧与下游空气添加
公开(公告)号：US5830346A
公开(公告)日：1998-11-03
申请号：US521177
申请日：1995-08-30
申请人： Mohsen N. Harandi , Paul H. Schipper , David S. Shihabi , Scott A. Stevenson
发明人： Mohsen N. Harandi , Paul H. Schipper , David S. Shihabi , Scott A. Stevenson
IPC分类号： B01D53/86 , C10G11/18 , C10G11/00 , B01J21/20 , C01B21/02
CPC分类号： C10G11/182 , B01D53/8625
摘要： Oxides of nitrogen (NO.sub.x) emissions from an FCC regenerator are reduced by operating the regenerator in partial CO burn mode to produce flue gas with more CO than O.sub.2 and with NO.sub.x precursors. This flue gas is then enriched with controlled amounts of oxygen and charged over catalyst, preferably Group VIII noble metal on a support, to convert most NO.sub.x precursors to nitrogen. Flue gas may then be charged to a CO boiler. Eliminating more than 90% of NO.sub.x emissions is possible by operating the FCC regenerator in partial CO burn mode, then adding air and catalytically converting NO.sub.x precursors at substoichiometric conditions. Conversion of NO.sub.x, if formed in the regenerator, may be achieved as well.
摘要翻译：通过在部分CO燃烧模式下操作再生器来减少来自FCC再生器的氮（NOx）排放的氧化物，以产生具有比O 2和NO x前体更多的CO的烟道气。然后，该烟道气用受控量的氧气富集，并通过催化剂，优选载体上的VIII族贵金属加入，以将大部分NOx前体转化为氮气。然后将烟道气充入CO锅炉。通过在部分CO燃烧模式下操作FCC再生器，然后在亚化学计量条件下添加空气和催化转化NOx前体，可以消除超过90％的NOx排放。也可以在再生器中形成NOx的转化。

2. 发明授权

US5382352A Conversion of NO.sub.x in FCC bubbling bed regenerator 失效
标题翻译： FCC沸腾床再生器中NOx的转化
公开(公告)号：US5382352A
公开(公告)日：1995-01-17
申请号：US963357
申请日：1992-10-20
申请人： Allen R. Hansen , David L. Johnson , Scott A. Stevenson , Paul H. Schipper , Mohsen N. Harandi
发明人： Allen R. Hansen , David L. Johnson , Scott A. Stevenson , Paul H. Schipper , Mohsen N. Harandi
IPC分类号： C10G11/18 , C10G11/00 , C01B21/00
CPC分类号： C10G11/182
摘要： Oxides of nitrogen (NO.sub.x) emissions from FCC regenerators in complete CO combustion mode are reduced by degrading regenerator performance to increase the coke on regenerated catalyst. High zeolite content cracking catalyst, regenerated to contain more coke, gives efficient conversion of feed and reduces NO.sub.x emissions from the regenerator. Operating with less catalyst, e.g., 30-60% of the normal amount of catalyst in the bubbling dense bed, can eliminate most NO.sub.x emissions while increasing slightly plant capacity and reducing catalyst deactivation.
摘要翻译：通过降低再生器的性能，增加再生催化剂上的焦炭，可以降低FCC再生器在完全CO燃烧模式下的氮氧化物（NOx）排放。再生含有更多焦炭的高沸石含量裂化催化剂能够有效地转化进料并减少再生器的NOx排放。以较少的催化剂操作，例如起泡致密床中正常量的催化剂的30-60％可以消除大部分NOx排放物，同时增加轻微的装置容量并减少催化剂失活。

3. 发明授权

US5401478A Selective catalytic reduction of nitrogen oxides 失效
标题翻译：氮氧化物的选择性催化还原
公开(公告)号：US5401478A
公开(公告)日：1995-03-28
申请号：US100940
申请日：1993-08-03
申请人： Clarence D. Chang , Jose G. Santiesteban , David S. Shihabi , Scott A. Stevenson
发明人： Clarence D. Chang , Jose G. Santiesteban , David S. Shihabi , Scott A. Stevenson
IPC分类号： B01D53/86 , B01D53/94 , B01J23/68 , B01J23/888 , B01J23/889 , C01B21/02 , C01B21/20
CPC分类号： C01B21/02 , B01D53/8628 , B01D53/9418 , B01J23/683 , B01J23/687 , B01J23/888 , B01J23/8892 , B01D2251/2062 , B01D2255/20715 , B01D2255/20776
摘要： There is provided a catalytic method for converting nitrogen oxides to nitrogen (i.e., N.sub.2). The catalyst for this method comprises an acidic solid component comprising a Group IVB metal oxide modified with an oxyanion of a Group VIB metal. An example of this catalyst is zirconia, modified with tungstate. This method may be used for reducing emissions of nitrogen oxides from waste gases, including industrial exhaust gases and automobile exhaust gases. In a particular embodiment, nitrogen oxides in waste gases may be reacted with ammonia before the waste gases are discharged to the atmosphere.
摘要翻译：提供了将氮氧化物转化为氮气（即N 2）的催化方法。用于该方法的催化剂包括酸性固体组分，其包含用VIB族金属的氧阴离子改性的IVB族金属氧化物。该催化剂的实例是用钨酸盐改性的氧化锆。该方法可用于减少来自废气（包括工业废气和汽车废气）的氮氧化物的排放。在一个具体实施方案中，废气中的氮氧化物可以在废气排放到大气中之前与氨反应。

4. 发明授权

US5552128A Selective catalytic reduction of nitrogen oxides 失效
标题翻译：氮氧化物的选择性催化还原
公开(公告)号：US5552128A
公开(公告)日：1996-09-03
申请号：US410156
申请日：1995-03-24
申请人： Clarence D. Chang , Jose G. Santiesteban , David S. Shihabi , Scott A. Stevenson , James C. Vartuli
发明人： Clarence D. Chang , Jose G. Santiesteban , David S. Shihabi , Scott A. Stevenson , James C. Vartuli
IPC分类号： B01D53/86 , B01D53/94 , B01J23/68 , B01J23/888 , B01J23/889 , C01B21/02 , B01D53/56
CPC分类号： B01D53/8628 , B01D53/9413 , B01J23/683 , B01J23/687 , B01J23/888 , B01J23/8892 , C01B21/02
摘要： There is provided a catalytic method for converting nitrogen oxides to nitrogen (i.e., N.sub.2). The catalyst for this method comprises an acidic solid component comprising a Group IVB metal oxide modified with an oxyanion of a Group VIB metal and further comprising at least one metal selected from the group consisting of Group IB, Group IVA, Group VB, Group VIIB, Group VIII, and mixtures thereof. An example of this catalyst is zirconia, modified with tungstate, and iron. This method may be used for reducing emissions of nitrogen oxides from waste gases, including industrial exhaust gases and automobile exhaust gases. In a particular embodiment, nitrogen oxides in waste gases may be reacted with ammonia before the waste gases are discharged to the atmosphere.
摘要翻译：提供了将氮氧化物转化为氮气（即N 2）的催化方法。用于该方法的催化剂包括酸性固体组分，其包含用VIB族金属的氧阴离子改性的IVB族金属氧化物，并且还包含选自组IB，组IVA，组VB，组VIIB的至少一种金属， VIII族及其混合物。该催化剂的实例是用钨酸盐和铁改性的氧化锆。该方法可用于减少来自废气（包括工业废气和汽车废气）的氮氧化物的排放。在一个具体实施方案中，废气中的氮氧化物可以在废气排放到大气中之前与氨反应。

5. 发明授权

US5451387A Selective catalytic reduction of nitrogen oxides using an iron impregnated zeolite catalyst 失效
标题翻译：使用铁浸渍的沸石催化剂选择性还原氮氧化物
公开(公告)号：US5451387A
公开(公告)日：1995-09-19
申请号：US271692
申请日：1994-07-07
申请人： Maria D. Farnos , John P. McWilliams , Sanjay B. Sharma , David S. Shihabi , Scott A. Stevenson , James C. Vartuli
发明人： Maria D. Farnos , John P. McWilliams , Sanjay B. Sharma , David S. Shihabi , Scott A. Stevenson , James C. Vartuli
IPC分类号： B01D53/86 , B01D53/94 , B01J29/072 , B01J29/46 , B01J37/02 , C01B21/20
CPC分类号： B01J37/0203 , B01D53/8621 , B01D53/8628 , B01D53/865 , B01D53/9418 , B01J29/072 , B01J29/46 , B01D2251/2062 , B01D2255/20738 , B01D2255/50
摘要： An exhaust gas treatment process useful for the removal of nitrogen oxides using an iron containing zeolite as the catalyst and ammonia as a reducing agent. It is desired to extend the effective temperature range for the selective catalytic reduction (SCR) of nitrogen oxides below about 400.degree. C. This is accomplished in the instant invention through the use of an intermediate pore size zeolite, such as ZSM-5, based catalyst which has been treated to incorporate iron into its pores.
摘要翻译：用于使用含铁沸石作为催化剂除去氮氧化物的废气处理方法和氨作为还原剂。期望将氮氧化物的选择性催化还原（SCR）的有效温度范围延伸到低于约400℃。这在本发明中通过使用中等孔径的沸石，例如ZSM-5，基于已经处理以将铁掺入其孔中的催化剂。

6. 发明授权

US5173278A Denitrification of flue gas from catalytic cracking 失效
标题翻译：烟气从催化裂化中脱氮
公开(公告)号：US5173278A
公开(公告)日：1992-12-22
申请号：US669821
申请日：1991-03-15
申请人： David O. Marler , Ajit V. Sapre , David S. Shihabi , Richard F. Socha , Scott A. Stevenson
发明人： David O. Marler , Ajit V. Sapre , David S. Shihabi , Richard F. Socha , Scott A. Stevenson
IPC分类号： B01D53/86 , C10G11/18
CPC分类号： B01D53/8625 , B01D53/8621 , C10G11/182 , B01D2257/408 , Y02P30/446
摘要： A flue gas that contains small amounts of both HCN and NO.sub.x, produced, for example, by catalyst regeneration in the fluid catalytic cracking of a petroleum gas oil, is readily denitrified by the catalyzed reaction that proceeds approximately according to:HCN+NO.fwdarw.N.sub.2 (gas)+CO+CO.sub.2 +H.sub.2 OIf the molar ratio of HCN to NO in the flue gas is about 1.0, e.g. in the range of about 0.8 to 1.2, effective denitrification is achieved without first changing the composition of the flue gas by contacting it with catalyst under conversion conditions including elevated temperature. If the molar ratio of HCN to NO exceeds 1.2, the ratio may be adjusted to about 1.0 to 1.1 by thermal or catalytic oxidation in the presence of oxygen gas, followed by catalytic denitrification. If the molar ratio is less than about 0.8, the effective molar ratio is adjusted to about 1.0 to 1.1 by adding NH.sub.3 gas, followed by denitirification. In all three instances an excessive content of carbon monoxide in the flue gas may be corrected by passing the denitrified flue gas to a CO-boiler.Catalysts for the denitrification reaction are described and exemplified by crystalline zeolites of the ZSM-5 type, and by vanadium oxide supported on titania.
摘要翻译：含有少量HCN和NOx的烟道气，例如通过在石油瓦斯油的流化催化裂化中的催化剂再生产生的烟气，可以通过大致按以下方式进行的催化反应脱氮：HCN + NO-> N2（气体）+ CO + CO2 + H2O如果烟气中HCN与NO的摩尔比为约1.0，在约0.8至1.2的范围内，无需首先在包括升高的温度的转化条件下将催化剂与催化剂接触，而不改变烟道气的组成，实现有效的脱氮。如果HCN与NO的摩尔比超过1.2，则在氧气存在下通过热或催化氧化将该比例调节至约1.0至1.1，然后进行催化反硝化。如果摩尔比小于约0.8，则通过加入NH 3气体将有效摩尔比调节至约1.0-1.1，然后进行脱硝。在所有三种情况下，可以通过将反硝化烟道气通过CO锅炉来校正烟道气中过量的一氧化碳。用于脱氮反应的催化剂通过ZSM-5型的结晶沸石和负载在二氧化钛上的氧化钒来描述和例示。

7. 发明授权

US5463168A Process for the removal of hydrogen cyanide from FCC hydrocarbon product gas streams 失效
标题翻译：从FCC烃产品气流中除去氰化氢的方法
公开(公告)号：US5463168A
公开(公告)日：1995-10-31
申请号：US291802
申请日：1994-08-17
申请人： Costandi A. Audeh , David S. Shihabi , Richard F. Socha , Scott A. Stevenson
发明人： Costandi A. Audeh , David S. Shihabi , Richard F. Socha , Scott A. Stevenson
IPC分类号： B01D3/00 , B01D53/86 , B01J8/02 , C07C7/148 , C10G70/00 , C07C7/00 , B01J8/00 , C01C3/00
CPC分类号： B01D3/009 , B01D53/8621 , B01J8/02 , C07C7/148 , C10G70/00 , Y02P20/127
摘要： A process is described wherein the HCN in FCC hydrocarbon gas streams is converted to NH.sub.3 over a catalyst. This conversion has the desirable result of decreasing the amount of CN.sup.- in the water leaving the sour-water stripper, and ultimately in the refinery water effluent.
摘要翻译：描述了一种方法，其中FCC烃气流中的HCN在催化剂上转化为NH 3。这种转化具有减少离开酸水汽提塔的水中的CN-的量以及最终在炼厂水中流出物的期望结果。

8. 发明授权

US08969232B2 Catalyst for conversion of hydrocarbons, process of making and process of using thereof—incorporation 2 有权
标题翻译：碳氢化合物转化催化剂，制备方法及其使用方法
公开(公告)号：US08969232B2
公开(公告)日：2015-03-03
申请号：US12125753
申请日：2008-05-22
申请人： Scott F. Mitchell , Alla K. Khanmamedova , Scott A. Stevenson , Jim Vartuli
发明人： Scott F. Mitchell , Alla K. Khanmamedova , Scott A. Stevenson , Jim Vartuli
IPC分类号： B01J29/06 , B01J27/182 , B01J29/89 , B01J29/40 , B01J29/44 , B01J29/86 , C07C1/20 , C07C2/24 , C07C2/66 , C07C2/76 , C07C6/12 , C10G11/05 , C10G25/03 , C10G35/06 , C10G35/085 , C10G45/10 , C10G45/12 , C10G45/62 , C10G45/64 , C10G47/16 , C10G47/18 , C10G50/00 , C10G3/00 , B01J29/88
CPC分类号： B01J29/89 , B01J29/047 , B01J29/064 , B01J29/068 , B01J29/072 , B01J29/405 , B01J29/42 , B01J29/44 , B01J29/46 , B01J29/48 , B01J29/82 , B01J29/83 , B01J29/84 , B01J29/85 , B01J29/86 , B01J29/88 , B01J2229/18 , B01J2229/186 , C07C1/20 , C07C2/24 , C07C2/66 , C07C2/76 , C07C6/123 , C07C6/126 , C07C2529/44 , C10G3/47 , C10G3/49 , C10G11/05 , C10G25/03 , C10G35/065 , C10G35/085 , C10G45/10 , C10G45/12 , C10G45/62 , C10G45/64 , C10G47/16 , C10G47/18 , C10G50/00 , C10G2300/1081 , C10G2300/1088 , C10G2400/20 , C10G2400/30 , C07C15/02
摘要： This invention is for a catalyst for conversion of hydrocarbons. The catalyst contains a zeolite with one element from Group 13, Group 14, or the first series transition metals and, optionally, germanium and/or aluminum in the zeolite framework. At least one Group 10 metal, such as platinum, is deposited on the zeolite. Examples of the elements in the framework are tin, boron, iron or titanium. The catalyst is prepared by synthesizing a zeolite with one element from Group 13, Group 14, or the first series transition metals and, optionally, germanium and/or aluminum in the zeolite framework; depositing the metal; and calcining after preparation of the zeolite and before or after depositing the metal. The catalyst may be used in a process for the conversion of hydrocarbons, such as propane to aromatics, by contacting the catalyst with alkanes having 2 to 12 carbon atoms per molecule and recovering the product.
摘要翻译：本发明是用于烃转化的催化剂。催化剂含有沸石，沸石具有来自第13族，第14族或第一系列过渡金属的一种元素，和任选的在沸石骨架中的锗和/或铝。在沸石上沉积至少一种第10族金属，例如铂。框架中的元素的实例是锡，硼，铁或钛。通过在沸石骨架中合成具有来自第13族，第14族或第一系列过渡金属和任选的锗和/或铝的一种元素的沸石来制备催化剂; 沉积金属; 并在制备沸石之后和在沉积金属之前或之后煅烧。催化剂可用于通过使催化剂与每分子具有2至12个碳原子的烷烃接触并回收产物来将烃类如丙烷转化成芳族化合物的方法。

9. 发明授权

US08153852B2 Process of using germanium zeolite catalyst for alkane aromatization 有权
标题翻译：使用锗沸石催化剂进行烷烃芳构化的工艺
公开(公告)号：US08153852B2
公开(公告)日：2012-04-10
申请号：US12387179
申请日：2009-04-29
申请人： Paul E. Ellis , Gopalakrishnan G. Juttu , Alla K. Khanmamedova , Scott F. Mitchell , Scott A. Stevenson
发明人： Paul E. Ellis , Gopalakrishnan G. Juttu , Alla K. Khanmamedova , Scott F. Mitchell , Scott A. Stevenson
IPC分类号： C07C2/42
CPC分类号： C07C2/76 , C07C15/02
摘要： This invention is for a catalyst for conversion of alkanes having two to six carbon atoms per molecule to aromatics. The catalyst is a MFI zeolite with a crystallite size of less than 15 microns with, in addition to silicon and aluminum, germanium as a framework element. Platinum is deposited on the zeolite. The zeolite may contain other optional tetravalent and trivalent elements in the zeolite framework. The catalyst is synthesized by preparing a zeolite containing aluminum, silicon, germanium and, optionally, other elements in the framework, calcining the zeolite and depositing platinum on the zeolite. The catalyst may be used for aromatization of alkanes, such as propane, to aromatics, such as benzene, toluene and xylenes.
摘要翻译：本发明是用于将每分子具有2-6个碳原子的烷烃转化成芳族化合物的催化剂。催化剂是微晶尺寸小于15微米的MFI沸石，除了硅和铝之外，锗作为骨架元素。铂沉积在沸石上。沸石在沸石骨架中可以含有其它任选的四价和三价元素。该催化剂是通过在骨架中制备含有铝，硅，锗和任选的其它元素的沸石来合成的，煅烧沸石并在沸石上沉积铂。催化剂可用于烷烃如丙烷的芳构化成芳族化合物如苯，甲苯和二甲苯。

10. 发明申请

US20100323882A1 METHODS FOR PREPARING CATALYSTS FOR METHACROLEIN OXIDATION 有权
标题翻译：制备甲基纤维素氧化催化剂的方法
公开(公告)号：US20100323882A1
公开(公告)日：2010-12-23
申请号：US12790928
申请日：2010-05-31
申请人： Scott A. Stevenson , Wugeng Liang , James W. Kauffman , Lixia Cai , Angie McGuffey , Joseph R. Linzer
发明人： Scott A. Stevenson , Wugeng Liang , James W. Kauffman , Lixia Cai , Angie McGuffey , Joseph R. Linzer
IPC分类号： B01J27/199 , B01J27/19 , B01J27/192
CPC分类号： B01J27/188 , B01J23/002 , B01J27/199 , B01J35/10 , B01J35/1061 , B01J35/1066 , B01J2523/00 , C07C51/252 , C07C57/04 , B01J2523/15 , B01J2523/17 , B01J2523/305 , B01J2523/51 , B01J2523/53 , B01J2523/54 , B01J2523/55 , B01J2523/68
摘要： Methods of making catalysts for oxidation of unsaturated and/or saturated aldehyde to unsaturated acids is disclosed where the catalyst including at least molybdenum (Mo) and phosphorus (P), where the catalyst has a pore size distribution including at least 50% medium pores and if bismuth is present, a nitric acid to molybdenum mole ratio of at least 0.5:1 or at least 6.0:1 moles of HNO3 per mole of Mo12.
摘要翻译：公开了将不饱和和/或饱和醛氧化成不饱和酸的催化剂的方法，其中催化剂至少包括钼（Mo）和磷（P），其中催化剂的孔径分布包括至少50％的中等孔隙，如果存在铋，每摩尔Mo12，硝酸与钼的摩尔比为至少0.5:1或至少6.0:1摩尔HNO 3。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式