公开(公告)号：US20080027255A1

公开(公告)日：2008-01-31

申请号：US11780693

申请日：2007-07-20

申请人： Christopher Blessing ,  Scott Brown ,  Tin-Tack Cheung ,  David Glova ,  Daniel Hasenberg ,  Dennis Holtermann ,  Gyanesh Khare ,  Daniel Knorr

发明人： Christopher Blessing ,  Scott Brown ,  Tin-Tack Cheung ,  David Glova ,  Daniel Hasenberg ,  Dennis Holtermann ,  Gyanesh Khare ,  Daniel Knorr

IPC分类号： C07C6/00

CPC分类号： C10G35/095 ,  C10G2300/4081 ,  C10G2400/30

摘要： A hydrocarbon aromatization process comprising adding a nitrogenate, an oxygenate, or both to a hydrocarbon stream to produce an enhanced hydrocarbon stream, and contacting the enhanced hydrocarbon stream with an aromatization catalyst, thereby producing an aromatization reactor effluent comprising aromatic hydrocarbons, wherein the catalyst comprises a non-acidic zeolite support, a group VIII metal, and one or more halides. Also disclosed is a hydrocarbon aromatization process comprising monitoring the presence of an oxygenate, a nitrogenate, or both in an aromatization reactor, monitoring at least one process parameter that indicates the activity of the aromatization catalyst, modifying the amount of the oxygenate, the nitrogenate, or both in the aromatization reactor, thereby affecting the parameter.

摘要翻译： 烃芳构化方法包括将氮化物，含氧化合物或二者加入到烃流中以产生增强的烃流，以及使增强的烃流与芳构化催化剂接触，从而产生包含芳族烃的芳构化反应器流出物，其中催化剂包含 非酸性沸石载体，VIII族金属和一种或多种卤化物。 还公开了一种烃芳构化方法，其包括在芳构化反应器中监测含氧物，氮酸盐或二者的存在，监测指示芳构化催化剂的活性的至少一个工艺参数，改变含氧化合物的量， 或二者在芳构化反应器中，从而影响参数。

公开(公告)号：US20050203328A1

公开(公告)日：2005-09-15

申请号：US10799987

申请日：2004-03-12

申请人： David Glova ,  Tin-Tack Cheung ,  Dan Knorr

发明人： David Glova ,  Tin-Tack Cheung ,  Dan Knorr

IPC分类号： B01J8/00 ,  B01J19/00 ,  B01J29/90 ,  B01J38/12 ,  B01J38/14 ,  C10G35/04 ,  B01J20/34

CPC分类号： C10G35/04 ,  B01J29/90 ,  B01J38/12 ,  B01J38/14 ,  B01J2208/02

摘要： A method of servicing a catalytic reactor system, comprising an abatement of at least one hazardous substance from the catalytic reactor system while preserving activity of a catalyst contained therein. A method of servicing a catalytic reactor system, comprising oxidizing the catalytic reactor system at a temperature of from about 350° F. to about 500° F. to abate at least one hazardous substance from the catalytic reactor system and reducing servicing time by about 50% of a time required for complete regenerative oxidation of the catalytic reactor system. A method of servicing a catalytic reactor system, comprising abating at least one hazardous substance from the catalytic reactor system such that a fouling rate of a catalyst contained therein is substantially the same before and after the servicing. A method of controlling an oxidation procedure in a catalytic reactor system, comprising: oxidizing the catalytic reactor system at a temperature of from about 350° F. to about 500° F.; monitoring abatement of at least one hazardous substance within the catalytic reactor system; and controlling the oxidation in response to the monitoring such that activity of a catalyst contained therein is preserved and the at least one hazardous substance is oxidized to a safe exposure level.

摘要翻译： 一种维修催化反应器系统的方法，包括从催化反应器系统中减少至少一种有害物质，同时保持其中所含催化剂的活性。 一种维修催化反应器系统的方法，包括在约350°F至约500°F的温度下氧化催化反应器系统以从催化反应器系统中减少至少一种有害物质，并将维修时间减少约50 催化反应器系统的完全再生氧化所需的时间的百分比。 一种维修催化反应器系统的方法，包括从催化反应器系统中减少至少一种有害物质，使得其中所含催化剂的结垢率在维修前后基本相同。 一种在催化反应器系统中控制氧化程序的方法，包括：在约350°F至约500°F的温度下氧化催化反应器系统; 监测在催化反应器系统内减少至少一种有害物质; 并且响应于监测来控制氧化，使得其中所含的催化剂的活性被保存并且所述至少一种有害物质被氧化到安全的暴露水平。