Method for preparing a steam reforming catalyst, catalyst and related use

Patent metadata

Field	Value
Publication number	US-12544746-B2
Application number	US-202117791643-A
Country	US
Kind code	B2
Filing date	Jan 5, 2021
Priority date	Jan 8, 2020
Publication date	Feb 10, 2026
Grant date	Feb 10, 2026

Abstract

The present invention addresses to a method of preparing steam reforming catalysts, of the eggshell type, using a solution of glycerin, in polar solvent, preferably water, to occupy the pores of a support. Next, the solvent is removed and the support is impregnated with a nickel salt solution, which may contain promoters such as rare earths. The steps can be repeated until the desired content of the active phase and promoters is reached.

First claim

The invention claimed is:

1 . A method of preparing a steam reforming catalyst, the method comprising:
a) impregnating an inorganic oxide support with a solution of glycerin and polar solvent, at temperatures lower than 90° C. and contact times of less than 1 hour; b) drying the inorganic oxide support of step (a) to remove the polar solvent, at a temperature between 50° C. and lower than 290° C. such that glycerin remains in the inorganic oxide support; c) impregnating the inorganic oxide support containing glycerin obtained in step (b) with a solution containing a nickel salt and optionally promoters, at a temperature between 25° C. and 90° C. and contact times between the nickel solution and the inorganic oxide support containing glycerin of less than 1 hour; d) drying the catalyst obtained in step (c) at a temperature of less than 150° C.; e) calcining the catalyst at temperatures between 300° C. and 600° C.; f) optionally, repeating steps c) to e) to obtain the desired content of nickel oxide in the catalyst.

2 . The method of preparing the steam reforming catalyst according to claim 1 , wherein the inorganic oxide support is selected from alpha- or theta-alumina, calcium aluminate, magnesium aluminate, hexa-aluminates, or a mixture thereof.

3 . The method of preparing the steam reforming catalyst according to claim 1 , the promoters are lanthanum, cerium, or a combination thereof.

4 . The method of preparing the steam reforming catalyst according to claim 2 , wherein a shape of particles of the inorganic oxide support is cylindrical or spherical, contains one or multiple holes, and/or has a smooth or wavy outer surface.

5 . The method of preparing the steam reforming catalyst according to claim 4 , wherein the particles have diameters and lengths between 10 mm and 25 mm and a surface area between 1 and 100 m 2 /g.

6 . The method of preparing the steam reforming catalyst according to claim 5 , wherein the surface area of the particles is between 10 m 2 /g and 80 m 2 /g.

7 . The method of preparing the steam reforming catalyst according to claim 1 , the wherein impregnation of the inorganic oxide support with glycerin is carried out by a pore volume method or by an excess solution method.

8 . The method of preparing the steam reforming catalyst according to claim 1 , wherein the polar solvent used to impregnate the inorganic oxide support with glycerin is water.

9 . The method of preparing the steam reforming catalyst according to claim 1 , wherein, in step (a), a polar solvent:glycerin ratio is adjusted in order to control a thickness of an active phase on the inorganic oxide support.

10 . The method of preparing the steam reforming catalyst according to claim 1 , wherein drying the inorganic oxide support (step (b)) is carried out at temperatures between 50° C. and 90° C.

11 . The method of preparing the steam reforming catalyst according to claim 1 , wherein the impregnation step c) with the nickel salt uses nickel nitrate.

12 . The method of preparing the steam reforming catalyst according to claim 1 , wherein the impregnation of step (c) occurs at temperatures of up to 90° C., with the contact time between the nickel solution and the inorganic oxide support containing glycerin of less than 30 minutes.

13 . The method of preparing the steam reforming catalyst according to claim 1 , wherein the calcination temperature of step e) is between 350° C. and 450° C.

14 . The method of preparing the steam reforming catalyst according to claim 1 , wherein the nickel oxide and optional promoters are deposited on an outer surface of the inorganic oxide support.

15 . The method of preparing the steam reforming catalyst according to claim 1 , wherein the catalyst comprises an active phase layer comprising nickel oxide that has a thickness of less than 0.2 mm.

16 . The method of preparing the steam reforming catalyst according to claim 1 , wherein the polar solvent comprises methanol, ethanol, or water.

17 . The method of preparing the steam reforming catalyst according to claim 9 , wherein, in step (a), the polar solvent:glycerin ratio is adjusted from 10:90 to 20:80 v/v.

18 . The method of preparing the steam reforming catalyst according to claim 15 , wherein the thickness of the active phase layer is less than 0.1 mm.

Assignees

• Petroleo Brasileiro S A —Petrobras

Inventors

• Pontes Bittencourt Roberto Carlos

Classifications

• B01J35/55

  Cylinders or rings · CPC title

• B01J2235/00

  Indexing scheme associated with group B01J35/00, related to the analysis techniques used to determine the catalysts form or properties · CPC title

• B01J35/40

  characterised by dimensions, e.g. grain size (in a colloidal state B01J35/23; crystallite size B01J35/77) · CPC title

• B01J35/613

  10-100 m2/g · CPC title

• B01J35/51

  Spheres · CPC title