Regeneration method for gravity-flowing catalyst particles

Claim 1

A method for continuously regenerating deactivated hydrocarbon conversion catalyst particles comprising a Group VIII noble metal component and a halogen component in combination with a refractory inorganic oxide, and which particles have been deactivated by deposition of carbonaceous matter thereon and loss of halogen therefrom, said method comprising the steps of: a. passing said catalyst particles downwardly by gravity flow through a vertically positioned confined regeneration zone maintained at a temperature of from about 750°F. to about 1050°F. and having an interconnecting upper carbon-burning section, with an intermediate halogenation section in interconnection with a lower drying section in descending sectional order; b. introducing said deactivated hydrogen conversion catalyst particles to said carbon-burning section and a first air stream from an external source through a carbon-burning inlet port to said carbon-burning section; c. burning substantially all of the carbonaceous matter from the catalyst particles in said carbon-burning section; d. withdrawing the excess air and combustion products from said carbon-burning section through a carbon-burning withdrawal port and cooling at least a portion thereof; e. recycling at least a portion of said cooled excess air and combustion products to said carbon-burning section through said carbon-burning inlet port; f. introducing the catalyst particles in the carbon-burning section to said interconnecting intermediate halogenation section; g. introducing steam and halogen or a halogen-containing compound to said intermediate halogenation section through a halogen-steam inlet port and therein increasing the halogen content of the catalyst particles; h. introducing the catalyst particles of increased halogen content to said interconnecting lower drying section; i. introducing a second air steam from an external source to said lower drying section through a lower drying section inlet port, wherein substantially all the water from said catalyst particles of increased halogen content in said lower drying section is removed, and wherein the mole ratio of air in said first air stream of (b) and said second air stream is at least 1.0:1.0; j. withdrawing the substantially water-free regenerated catalyst particles from the lower end of the regeneration zone through a catalyst particle withdrawal conduit; and, k. wherein in said method of regenerating said first air stream, second air stream and steam and halogen or halogen-containing compound are introduced transversely and flow countercurrently to said gravitational flow of said catalyst particles, and wherein air from the lower drying section passes upwardly therefrom into the halogenation section and therethrough into the carbon burning section.

Claim 2

A method for continuously regenerating deactivated hydrocarbon conversion catalyst particles comprising a Group VIII noble metal component and a halogen component in combination with a refractory inorganic oxide, and which particles have been deactivated by deposition of carbonaceous matter thereon and loss of halogen therefrom, said method comprising the steps of: a. passing said catalyst particles downwardly by gravity flow through a vertically positioned confined regeneration zone maintained at a temperature of from about 750°F. to about 1050°F. and having an interconnecting upper carbon-burning section, with an intermediate halogenation section in interconnection with a lower drying section in descending sectional order; b. introducing said deactivated hydrogen conversion catalyst particles to said carbon-burning section and a first air stream from an external source through a carbon-burning inlet port to said carbon-burning section; c. burning substantially all of the carbonaceous matter from the catalyst particles in said carbon-burning section; d. withdrawing the excess air and combustion products from said carbon-burning section through a carbon-burning withdrawal port and cooling at least a portion thereof; e. recycling at least a portion of said cooled excess air and combustion products to said carbon-burning section through said carbon-burning inlet port; f. introducing the catalyst particles in the carbon-burning section to said interconnecting intermediate halogenation section; g. introducing steam and halogen or a halogen-containing compound to said intermediate halogenation section through a halogen-steam inlet port and therein increasing the halogen content of the catalyst particles; h. introducing the catalyst particles of increased halogen content to said interconnecting lower drying section; i. introducing a second air steam from an external source to said lower drying section through a lower drying section inlet port, wherein substantially all the water from said catalyst particles of increased halogen content in said lower drying section is removed, and wherein the mole ratio of air in said first air stream of (b) and said second air stream is at least 1.0:1.0; j. withdrawing the substantially water-free regenerated catalyst particles from the lower end of the regeneration zone through a catalyst particle withdrawal conduit; and, k. wherein in said method of regenerating said first air stream, second air stream and steam and halogen or halogen-containing compound are introduced transversely and flow countercurrently to said gravitational flow of said catalyst particles, and wherein air from the lower drying section passes upwardly therefrom into the halogenation section and therethrough into the carbon burning section.