Reconstituted dehydrogenation catalyst showing slowed activity loss when compared with fresh catalyst

Abstract

A process for dehydrogenating alkane or alkylaromatic compounds comprising contacting the given compound and a dehydrogenation catalyst in a fluidized bed. The dehydrogenation catalyst is prepared from an at least partially deactivated platinum/gallium catalyst on an alumina-based support that is reconstituted by impregnating it with a platinum salt solution, then calcining it at a temperature from 400° C. to 1000° C., under conditions such that it has a platinum content ranging from 1 to 500 ppm, based on weight of catalyst; a gallium content ranging from 0.2 to 2.0 wt %; and a platinum to gallium ratio ranging from 1:20,000 to 1:4. It also has a Pt retention that is equal to or greater than that of a fresh catalyst being used in a same or similar catalytic process.

1 . A process for dehydrogenating alkane or alkylaromatic compounds comprising
 contacting, in a fluidized bed, an alkane compound or an alkylaromatic compound and a reconstituted dehydrogenation catalyst,   such reconstituted dehydrogenation catalyst having been prepared by   (a) obtaining a dehydrogenation catalyst comprising platinum and gallium on an alumina-based support, the dehydrogenation catalyst having been previously fresh but having become at least partially deactivated;   (b) impregnating the at least partially deactivated dehydrogenation catalyst with a platinum salt solution to form an impregnated dehydrogenation catalyst; and   (c) calcining the impregnated dehydrogenation catalyst at a temperature ranging from 400° C. to 1000° C.;   (b) and (c) being carried out under conditions suitable to form a reconstituted dehydrogenation catalyst having (i) a platinum content ranging from 1 part per million, based on weight of catalyst, to 500 parts per million, based on weight of catalyst; (ii) a gallium content ranging from 0.2 wt % to 2.0 wt %; and (iii) a ratio of platinum to gallium ranging from 1:20,000 to 1:4;   wherein the reconstituted dehydrogenation catalyst further exhibits a platinum retention greater than or equal to the platinum retention of a fresh dehydrogenation catalyst when each is used in the same or another, otherwise identical dehydrogenation process.   
     
     
         2 . The process of  claim 1 , wherein the platinum content of the reconstituted dehydrogenation catalyst ranges from 40 parts per million, based on weight of catalyst, to 400 parts per million, based on weight of catalyst, and the ratio of platinum to gallium content ranges from 1:500 to 1:5. 
     
     
         3 . The process of  claim 2 , wherein the platinum content of the reconstituted dehydrogenation catalyst ranges from 150 parts per million, based on weight of catalyst, to 300 parts per million, based on weight of catalyst, and the ratio of platinum to gallium content ranges from 3:400 to 3:80. 
     
     
         4 . The process of  claim 1 , wherein the reconstituted dehydrogenation catalyst exhibits a propane dehydrogenation activity that is at least 2% absolute propane conversion greater than that exhibited by the at least partially deactivated catalyst. 
     
     
         5 . The process of  claim 1 , further comprising the step of drying the impregnated dehydrogenation catalyst at a temperature ranging from 50° C. to 150° C. prior to calcining it. 
     
     
         6 . A dehydrogenation catalyst composition comprising
 a reconstituted platinum/gallium catalyst on an alumina-based support,   the reconstituted platinum/gallium catalyst having been prepared by a process comprising   (a) obtaining a dehydrogenation catalyst comprising platinum and gallium on an alumina-based support, the dehydrogenation catalyst having been previously fresh but having become at least partially deactivated;   (b) impregnating the at least partially deactivated dehydrogenation catalyst with a platinum salt solution to form an impregnated dehydrogenation catalyst; and   (c) calcining the impregnated dehydrogenation catalyst at a temperature ranging from 400° C. to 1000° C.;   (b) and (c) being carried out under conditions suitable to form a reconstituted dehydrogenation catalyst having (i) a platinum content ranging from 1 part per million, based on weight of catalyst, to 500 parts per million, based on weight of catalyst; (ii) a gallium content ranging from 0.2 wt % to 2.0 wt %; and (iii) a ratio of platinum to gallium ranging from 1:20,000 to 1:4;   wherein the reconstituted dehydrogenation catalyst further exhibits having a platinum retention greater than or equal to the platinum retention of a fresh dehydrogenation catalyst when each is used in the same or another, otherwise identical dehydrogenation process.   
     
     
         7 . A process to prepare a catalyst comprising
 (a) obtaining a dehydrogenation catalyst comprising platinum and gallium on an alumina-based support, the dehydrogenation catalyst having been previously fresh but having become at least partially deactivated;   (b) impregnating the at least partially deactivated dehydrogenation catalyst with a platinum salt solution to form an impregnated dehydrogenation catalyst; and   (c) calcining the impregnated dehydrogenation catalyst at a temperature ranging from 400° C. to 1000° C.;   (b) and (c) being carried out under conditions suitable to form a reconstituted dehydrogenation catalyst having (i) a platinum content ranging from 1 part per million, based on weight of catalyst, to 500 parts per million, based on weight of catalyst; (ii) a gallium content ranging from 0.2 wt % to 2.0 wt %; and (iii) a ratio of platinum to gallium ranging from 1:20,000 to 1:4;   wherein the reconstituted dehydrogenation catalyst further exhibits a platinum retention greater than or equal to the platinum retention of a fresh dehydrogenation catalyst when each is used in the same or another, otherwise identical dehydrogenation process.   
     
     
         8 . The process of  claim 7 , further comprising a step, between (b) and (c), of drying the impregnated dehydrogenation catalyst at a temperature ranging from 50° C. to 150° C.