US 4,647,549 AGranted

Regeneration of hydrocarbon conversion catalyst

AssigneeUpo LLC

InventorArthur R. Greenwood

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Abstract

A vessel for effecting multiple treatment steps needed to regenerate spent hydrocarbon conversion catalyst. Regeneration is accomplished by means of a moving bed of catalyst, where catalyst is passed through several treatment zones in the regeneration vessel. Catalyst is contacted with a hot oxygen-containing gas stream in order to remove coke which accumulates on the catalyst while it is in a hydrocarbon conversion zone. After the coke is burned off in a combustion zone, catalyst is passed into a drying zone for removal of water formed in the combustion zone which has remained on the catalyst instead of being carried off with combustion gases. Water removal is accomplished by passing a hot dry air stream through the catalyst. This air stream is introduced into the bottom of the regeneration vessel and is heated by exchange of heat with catalyst, thereby effecting the required cooling of the catalyst. Before passing into the drying zone, the air is heated further by heating means located in the vessel. After passing through the drying zone, the air stream provides oxygen for combustion in the combustion zone.

Claims2

Dependent claims

A method for effecting regeneration of spent catalyst particles used in hydrocarbon conversion reactions comprising:

(a) passing spent catalyst particles through a burn zone, by means of gravity, which is maintained at a coke-oxidizing temperature, wherein said catalyst is contacted with a recycle gas comprising oxygen;
(b) passing catalyst leaving said burn zone through a catalyst drying zone, by means of gravity, wherein water is removed from said catalyst;
(c) passing catalyst particles leaving said catalyst drying zone through a catalyst cooling zone, by means of gravity, wherein the temperature of the catalyst is reduced, where the cooling zone is located in the same vessel as the drying zone;
(d) compressing air drawn from the atmosphere to an elevated pressure;
(e) cooling said compressed air stream and passing said air stream through an air drying zone wherein water is removed from said air;
(f) passing said cooled and dried air stream upward through said catalyst cooling zone in countercurrent contact with said catalyst, thereby cooling the catalyst and heating said air stream;
(g) heating said air stream to a coke oxidizing temperature, after it leaves said catalyst cooling zone, in an air heating zone which is provided with heating tubes or elements and is located in the same vessel as said catalyst cooling zone;
(h) passing said air stream leaving said air heating zone upward through said catalyst drying zone in countercurrent contact with said catalyst, thereby removing water from the catalyst, the catalyst drying zone being located in the same vessel as said catalyst cooling zone;
(i) passing said air stream leaving said drying zone into said burn zone and mixing said air stream with gas emanating from said catalyst in the burn zone to form a flue gas stream;
and,
(j) withdrawing said flue gas stream from the burn zone, discharging a first portion of flue gas from the regeneration system, and passing a second portion into contact with spent catalyst in the burn zone as recycle gas.

8 more elements

A method for effecting regeneration of spent catalyst particles used in hydrocarbon conversion reactions comprising:

(a) passing spent catalyst particles through a burn zone, by means of gravity, which is maintained at a coke-oxidizing temperature, wherein said catalyst is contacted with a recycle gas comprising oxygen;
(b) passing catalyst leaving said burn zone through a halogenation zone, by means of gravity, wherein said catalyst is contacted with a halogenation gas comprising a halogen compound;
(c) passing catalyst leaving said halogenation zone through a catalyst drying zone, by means of gravity, wherein water is removed from said catalyst;
(d) passing catalyst particles leaving said catalyst drying zone through a catalyst cooling zone, by means of gravity, wherein the temperature of the catalyst is reduced, where the cooling zone is located in the same vessel as the drying zone;
(e) compressing air drawn from the atmosphere to an elevated pressure;
(f) cooling said compressed air stream and passing said air stream through an air drying zone wherein water is removed from said air;
(g) passing said cooled and dried air stream upward through said catalyst cooling zone in countercurrent contact with said catalyst, thereby cooling the catalyst and heating said air stream;
(h) heating said air stream to a coke oxidizing temperature, after it leaves said catalyst cooling zone, in an air heating zone which is provided with heating tubes or elements and is located in the same vessel as said catalyst cooling zone;
(i) passing said air stream leaving said air heating zone upward through said catalyst drying zone in countercurrent contact with said catalyst, thereby removing water from the catalyst, the catalyst drying zone being located in the same vessel as said catalyst cooling zone;
(j) passing said air stream leaving said catalyst drying zone into said halogenation zone and mixing said air stream with a first portion of gas emanating from said catalyst in the halogenation zone to form spent halogenation gas;
(k) withdrawing said spent halogenation gas from said halogenation zone and adding steam and a halogen compound to said spent halogenation gas to form fresh halogenation gas;
(l) passing said fresh halogenation gas into contact with said catalyst in said halogenation zone;
(m) withdrawing a first portion of gas from contact with said halogenation zone catalyst to comprise said spent halogenation gas;
(n) withdrawing a second portion of gas from contact with said halogenation zone catalyst and passing said second portion into the burn zone into admixture with gas emanating from said burn zone catalyst to form flue gas;
and,
(o) withdrawing said flue gas from said burn zone, discharging a first portion of said flue gas from the regeneration system, and passing a second portion of flue gas into contact with burn zone catalyst as recycle gas.

13 more elements

Dependencies are inferred from the claim text.