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

Patent metadata

Field	Value
Publication number	US-11559790-B2
Application number	US-202017137978-A
Country	US
Kind code	B2
Filing date	Dec 30, 2020
Priority date	Feb 20, 2012
Publication date	Jan 24, 2023
Grant date	Jan 24, 2023

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.

First claim

What is claimed is:

1. 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 solution consisting of platinum salt in water 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.

2. 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 by the selective removal of platinum from the dehydrogenation catalyst, wherein the gallium content of the at least partially deactivated dehydrogenation catalyst is approximately equal to the gallium content of the previously fresh dehydrogenation catalyst;
(b) impregnating the at least partially deactivated dehydrogenation catalyst with a solution consisting of a platinum salt in water 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.

3. The process of claim 2 , further comprising a step, between (b) and (c), of drying the impregnated dehydrogenation catalyst at a temperature ranging from 50° C. to 150° C.

4. The process of claim 2 , 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.

5. 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.

6. The process of claim 2 , wherein the alumina-based support has a Davison Attrition index of less than 14.

7. The process of claim 2 , wherein the alumina-based support is modified with silica.

8. The process of claim 2 , wherein the gallium content ranges from 0.8 wt % to 2.0 wt %.

9. The process of claim 2 , wherein the calcining comprises calcining the impregnated dehydrogenation catalyst at a temperature ranging from 600° C. to 800° C.

10. The process of claim 9 , wherein the calcining is carried out for a time of from 20 to 720 minutes.

11. The process of claim 9 , wherein the calcining is carried out for a time of from 40 to 360 minutes.

12. The process of claim 2 , wherein the platinum salt is selected from the group consisting of tetraamine platinum (II) nitrate, platinum (II) nitrate, platinum (II) acetylacetonate, and combinations thereof.

13. The process of claim 2 , wherein the process excludes precursor steps that remove extraneous materials deposited on surfaces of the at least partially deactivated dehydrogenation catalyst.

14. The process of claim 2 , wherein the calcination is carried out under an atmosphere comprising oxygen.

15. The process of claim 14 , wherein the calcination is carried out in air.

16. The process of claim 2 , wherein the at least partially deactivated dehydrogenation catalyst has a ratio of platinum to gallium that is less than a ratio of platinum to gallium of the previously fresh dehydrogenation catalyst.

Assignees

• Dow Global Technologies Llc

Inventors

• Luo Lin
• Rosenfeld Devon C
• Malek Andrzej M

Classifications

• C07C11/06

  Propene · CPC title

• C07C2521/12

  Silica and alumina · CPC title

• C07C5/322

  with metal oxides or metal sulfides · CPC title

• C07C2527/224

  Silicon carbide · CPC title

• C07C2523/42

  Platinum · CPC title