Method for reactivating used hydrogenation treatment titania catalyst, and regenerated hydrogenation treatment titania catalyst

Patent metadata

Field	Value
Publication number	US-10071370-B2
Application number	US-201314411083-A
Country	US
Kind code	B2
Filing date	May 16, 2013
Priority date	Jul 19, 2012
Publication date	Sep 11, 2018
Grant date	Sep 11, 2018

Abstract

Provided is a method of reactivating a used titania catalyst for hydrogenation treatment, capable of improving the catalytic activity of the used titania catalyst for hydrogenation treatment that is obtained by supporting a catalyst component on a titania support and exhibits reduced catalytic activity after having been used for hydrogenation treatment of a hydrocarbon oil, to a level comparable to that of a newly prepared fresh titania catalyst before use. The method of reactivating a used titania catalyst for hydrogenation treatment, the used titania catalyst for hydrogenation treatment being obtained by supporting a catalyst component on a titania support and exhibiting reduced catalytic activity after having been used for hydrogenation treatment of a hydrocarbon oil, includes: a coke removal step of removing a carbonaceous component on a surface of the used catalyst by heating the catalyst in an oxygen-containing gas atmosphere; an impregnation step of impregnating the carbonaceous component-removed catalyst obtained by the coke removal step with a saccharide-containing solution; and a drying step of drying the saccharide-impregnated catalyst obtained by the impregnation step, to obtain a catalyst in which a saccharide is supported.

First claim

The invention claimed is:

1. A method of reactivating a used titania catalyst for hydrogenation treatment, the method comprising:
obtaining a titania-coated alumina support comprising an alumina hydrate particle and a titania coating layer formed on a surface of the alumina hydrate particle between an isoelectric point of aluminum oxide and an isoelectric point of titanium oxide by coating the alumina hydrate particle with the titania coating layer in a condition of 5.0±0.1 of a pH,
wherein the titania-coated alumina support does not have an anatase crystal form of titania as detected by X-ray diffraction;
supporting a catalyst component and a saccharide on the titania-coated alumina support to obtain a fresh titania catalyst supported on the titania-coated alumina support;
conducting hydrogenation treatment of a hydrocarbon oil in the presence of the fresh titania catalyst supported on the titania-coated alumina support, thereby resulting in a used titania catalyst supported on the titania-coated alumina support, and a carbonaceous component deposited on a surface of the used titania catalyst; and then
subjecting the used titania catalyst supported on the titania-coated alumina support to a reactivation process, wherein the reactivation process comprises:
a coke removal step of removing the carbonaceous component on the surface of the used catalyst supported on the titania-coated alumina support by heating the catalyst in an oxygen-containing gas atmosphere;
an impregnation step of impregnating the carbonaceous component-removed catalyst obtained by the coke removal step with a saccharide-containing solution in a pH region that a zeta potential of titania is ±0 or less; and
a drying step of drying the saccharide-impregnated catalyst obtained by the impregnation step to obtain a catalyst in which a saccharide is supported.

2. The method of reactivating a used titania catalyst for hydrogenation treatment according to claim 1 , wherein the catalyst component comprises at least one kind of periodic table group VI metal compound, at least one kind of periodic table group VIII to X metal compound, and at least one kind of phosphorus compound.

3. The method of reactivating a used titania catalyst for hydrogenation treatment according to claim 1 , wherein the saccharide-containing solution to be used in the impregnation step comprises a solution containing one kind or two or more kinds of saccharides selected from the group consisting of glucose, fructose, erythritol, xylose, xylitol, sorbitol, mannitol, invert sugar, maltose, trehalose, maltitol, isomerized sugar, and raffinose.

4. The method of reactivating a used titania catalyst for hydrogenation treatment according to claim 1 , wherein the saccharide-containing solution to be used in the impregnation step comprises a solution containing, in addition to the saccharide, a catalyst component comprising at least one kind of periodic table group VI metal compound, at least one kind of periodic table group VIII to X metal compound, and at least one kind of phosphorus compound.

5. The method of reactivating a used titania catalyst for hydrogenation treatment according to claim 4 , wherein the catalyst component contained in the saccharide-containing solution comprises the same catalyst component as the catalyst component supported on the titania support of the titania catalyst for hydrogenation treatment.

6. The method of reactivating a used titania catalyst for hydrogenation treatment according to claim 4 or 5 , wherein a total amount of the periodic table group VI metal compound, the periodic table group VIII to X metal compound, and the phosphorus compound, in the catalyst component contained in the saccharide-containing solution, is 5 mass % or less with respect to a catalyst component of a regenerated titania catalyst for hydrogenation treatment after reactivation, in terms of an oxide.

7. The method of reactivating a used titania catalyst for hydrogenation treatment according to claim 1 , wherein the oxygen-containing gas to be used in the coke removal step comprises air.

8. The method of reactivating a used titania catalyst for hydrogenation treatment according to claim 1 , wherein the impregnation step of impregnating the carbonaceous component-removed catalyst obtained by the coke removal step with a saccharide-containing solution is in a weakly acidic region of from pH 3 to 7.

Assignees

• Chiyoda Corp

Inventors

• Inoue Shinichi
• Wada Yukitaka
• Muto Akihiro

Classifications

• B01J31/4053

  with recovery of phosphorous catalyst system constituents · CPC title

• B01J23/882

  and cobalt · CPC title

• C10G2300/708

  Coking aspect, coke content and composition of deposits · CPC title

• B01J38/02

  Heat treatment · CPC title

• B01J27/28

  Regeneration or reactivation · CPC title