Catalyst composition and reactivation process useful for alkane dehydrogenations

Patent metadata

Field	Value
Publication number	US-9884314-B2
Application number	US-201314420677-A
Country	US
Kind code	B2
Filing date	Jul 31, 2013
Priority date	Aug 28, 2012
Publication date	Feb 6, 2018
Grant date	Feb 6, 2018

Abstract

A catalyst comprising a Group IIIA metal, a Group VIII noble metal, and an optional promoter metal, on a support selected from silica, alumina, silica-alumina compositions, rare earth modified alumina, and combinations thereof, doped with iron, a Group VIB metal, a Group VB metal, or a combination thereof, offers decreased reactivation time under air soak in comparison with otherwise identical catalysts. Reducing reactivation time may, in turn, reduce costs, both in inventory and capital.

First claim

We claim:

1. An alkane dehydrogenation catalyst composition comprising
a Group IIIA metal selected from gallium, indium, thallium and combinations thereof, wherein the Group IIIA metal ranges from 0.25 percent by weight to 5 percent by weight;
a Group VIII noble metal selected from platinum, palladium, rhodium, iridium, ruthenium, osmium, and combinations thereof, wherein the Group VIII noble metal ranges from 5 parts by weight to 500 parts by weight;
at least one dopant selected from iron, chromium, vanadium, and combinations thereof, wherein:
when iron is present, iron ranges from 100 parts by weight to 2100 parts per weight;
when chromium is present, chromium ranges from 100 parts by weight to 800 parts by weight; and
when vanadium is present, vanadium ranges from 100 parts by weight to 800 parts by weight;

and
an optional promoter metal selected from sodium, potassium, rubidium, cesium, magnesium, calcium, strontium, barium and combinations thereof, wherein the optional promoter metal ranges from 0 percent by weight to 2.0 percent by weight;
wherein each percent by weight based upon weight of the total alkane dehydrogenation catalyst, and each part by weight based upon one million parts by weight of the total alkane dehydrogenation catalyst;

on a catalyst support selected from silica, alumina, silica-alumina composites, rare earth modified alumina, and combinations thereof.

2. The catalyst composition of claim 1 wherein at least one selection is made from: the alkane is propane, the Group VIII noble metal is platinum, the Group IIIA metal is gallium, the optional promoter metal is potassium, and combinations thereof.

3. A process to dehydrogenate an alkane comprising employing as an alkane dehydrogenation catalyst the catalyst composition of claim 1 .

4. A process to at least partially reactivate the alkane dehydrogenation catalyst of claim 1 , which has been at least partially deactivated comprising
treating the at least partially deactivated alkane dehydrogenation catalyst by exposing it to an oxygen-containing gas at a temperature of at least 660° C.,
such that the alkane dehydrogenation activity of the at least partially deactivated alkane dehydrogenation catalyst is increased to a level such that, upon contact with a selected alkane, it converts the selected alkane to a given percent in a time that is shortened by at least 10 percent in comparison with the time required to increase the alkane dehydrogenation activity, under otherwise identical conditions, of an otherwise identical alkane dehydrogenation catalyst to the same level, wherein the otherwise identical alkane dehydrogenation catalyst differs only in that it lacks the same amount of the same dopant.

5. The process of claim 4 wherein at least one selection is made from: the alkane is propane; the Group IIIA metal is gallium; the Group VIII noble metal is platinum; the optional promoter metal is potassium; and combinations thereof.

6. The process of claim 4 for regenerating an alkane dehydrogenation catalyst, the process including the steps of
(a) heating the at least partially deactivated, particulate alkane dehydrogenation catalyst containing coke thereon, to a temperature of at least 660° C. using heat generated by combusting the coke and from a fuel source other than the coke, this heating yielding a heated, further deactivated catalyst which has an alkane dehydrogenation activity that is less than that of the at least partially deactivated, particulate catalyst;
(b) maintaining the heated, further deactivated, particulate alkane dehydrogenation catalyst at a temperature of at least 660° C. while exposing it to a flow of an oxygen-containing gas for a period of time sufficient to increase the activity of the further deactivated, particulate alkane dehydrogenation catalyst and thereby form an at partially reactivated, particulate alkane dehydrogenation catalyst;
the at least partially reactivated, particulate alkane dehydrogenation catalyst comprising molecular oxygen trapped within or between the particles thereof and physisorbed oxygen;
(c) optionally, maintaining the at least partially reactivated, particulate alkane dehydrogenation catalyst at a temperature of at least 660° C. while exposing it to a flow of stripping gas that is substantially free of both molecular oxygen and combustible fuel for a period of time such that at least a portion of both the molecular oxygen trapped within or between catalyst particles, and of the physisorbed oxygen that is desorbable at that temperature during that period of time, are removed from the at least partially reactivated, particulate alkane dehydrogenation catalyst, thereby forming a rejuvenated, particulate alkane dehydrogenation catalyst; and
(d) transporting the rejuvenated, particulate alkane dehydrogenation catalyst to the reactor by means of at least a motive force;
provided that the time required in step (b) to increase the activity level of the further deactivated, particulate alkane dehydrogenation catalyst, such that, upon contact with a selected alkane, it converts the selected alkane to a given percent, in a time that is shortened by at least 10 percent in comparison with the time required to increase an otherwise identical further deactivated, particulate alkane dehydrogenation catalyst to the same activity level under identical conditions, wherein the otherwise identical further deactivated, particulate alkane dehydrogenation catalyst differs only in that it lacks the effective amount of the dopant.

7. The process of claim 6 wherein at least one selection is made from: the alkane is propane; the Group IIIA metal is gallium; the Group VIII noble metal is platinum; the optional promoter metal is potassium; the Group VIB metal is chromium; the Group VB metal is vanadium; and combinations thereof.

Assignees

• Dow Global Technologies Llc

Inventors

• Luo Lin
• Stears Brien A

Classifications

• B01J23/6522

  Chromium · CPC title

• C07C2523/22

  Vanadium · CPC title

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• B01J23/6482

  Vanadium · CPC title

• C07C11/04

  Ethene · CPC title