Black powder catalyst for hydrogen production via steam reforming

Patent metadata

Field	Value
Publication number	US-11814289-B2
Application number	US-202117140236-A
Country	US
Kind code	B2
Filing date	Jan 4, 2021
Priority date	Jan 4, 2021
Publication date	Nov 14, 2023
Grant date	Nov 14, 2023

Abstract

A steam reforming catalyst that includes treated black powder (primarily hematite), and a method of treating black powder (e.g., from a natural gas pipeline) to give the treated black powder. A steam reformer having the treated black powder as reforming catalyst, and a method of producing syngas with the steam reformer.

First claim

What is claimed is:

1. A method of steam reforming hydrocarbon, comprising:
receiving a black powder collected from a natural-gas pipeline system and that formed on an inside surface of a natural gas pipeline that is a steel pipeline of the natural-gas pipeline system, the black powder comprising magnetite and hematite; and
reacting hydrocarbon comprising methane with steam via reforming catalyst at a temperature in a range of 500° C. to 1100° C. and at a pressure in a range of 1 bar to 28 bar to generate synthesis gas comprising hydrogen and carbon monoxide, wherein the reforming catalyst comprises the black powder treated by:
heating the black powder at a temperature of at least 500° C. to remove carbon from the black powder; and
subjecting the black powder to air calcination at a temperature of at least 775° C., wherein the black powder as treated comprises at least 50 weight percent of hematite.

2. The method of claim 1 , comprising disposing the black powder as treated in a steam reformer vessel as the reforming catalyst, wherein reacting the hydrocarbon with the steam via the reforming catalyst is performed in the steam reformer vessel.

3. The method of claim 1 , wherein the natural gas pipeline is between a wellhead and a natural gas processing plant, and wherein reacting the hydrocarbon with steam comprises steam reforming of the methane.

4. The method of claim 1 , comprising collecting the black powder from the natural-gas pipeline system.

5. The method of claim 1 , wherein the black powder collected from the natural-gas pipeline system comprises black powder collected via a filter disposed along the natural gas pipeline between a wellhead and a gas processing plant or in an upstream portion of the gas processing plant.

6. The method of claim 1 , comprising collecting the black powder from the natural-gas pipeline system via a filter, a filter bag, a separator, or a cyclone, or any combinations thereof.

7. A method of steam reforming hydrocarbon, comprising:
receiving a black powder collected from a natural-gas pipeline system and that formed on an inside surface of a natural gas pipeline that is a steel pipeline of the natural-gas pipeline system, the black powder comprising magnetite and hematite;
providing hydrocarbon and steam to a steam reformer vessel, wherein the hydrocarbon comprises methane, wherein a reforming catalyst comprising a treated black powder is disposed in the steam reformer vessel, wherein the treated black powder comprises the black powder heated at a temperature of at least 500° C. to remove carbon from the black powder and subjected to air calcination at a temperature of at least 775° C., wherein the treated black powder comprises at least 50 weight percent of hematite;
steam reforming the hydrocarbon in the steam reformer vessel via the reforming catalyst at a temperature in a range of 500° C. to 1100° C. and at a pressure in a range of 1 bar to 28 bar to generate hydrogen and carbon monoxide; and
discharging the hydrogen and carbon monoxide from the steam reformer vessel.

8. The method of claim 7 , comprising collecting the black powder from the natural-gas pipeline system via a filter, a filter bag, a separator, or a cyclone, or any combinations thereof, and wherein the steam reforming comprises reacting the hydrocarbon with the steam.

9. The method of claim 7 , comprising:
collecting the black powder from the natural-gas pipeline system via a filter disposed along the natural gas pipeline between a wellhead and a gas processing plant or in an upstream portion of the gas processing plant; and
providing heat to the steam reformer vessel for the steam reforming comprising reacting of the hydrocarbon with the steam, wherein the reacting of the hydrocarbon with the steam is endothermic.

Assignees

• Saudi Arabian Oil Co

Inventors

• Wedhaya Ahmad A
• Fadhel Bandar A
• Albuali Mohammed A
• Bamagain Rami

Classifications

• B01J2235/15

  X-ray diffraction · 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

• C01B3/40 Primary

  characterised by the catalyst · CPC title

• B01J8/065

  Feeding reactive fluids · CPC title

• B01J23/745 Primary

  Iron · CPC title