Carrier for synthesis gas production catalyst, method of manufacturing the same, synthesis gas production catalyst, method of manufacturing the same and method of producing synthesis gas

Patent metadata

Field	Value
Publication number	US-10376864-B2
Application number	US-201715755901-A
Country	US
Kind code	B2
Filing date	Jun 5, 2017
Priority date	Jun 10, 2016
Publication date	Aug 13, 2019
Grant date	Aug 13, 2019

Abstract

This invention provides a carrier for a synthesis gas production catalyst that can suppress carbon depositions and allows to efficiently produce synthesis gas on a stable basis for a long duration of time when producing synthesis gas by carbon dioxide reforming. It is a carrier to be used for producing synthesis gas containing carbon monoxide and hydrogen from source gas containing methane-containing light hydrocarbons and carbon dioxide. The carrier contains magnesium oxide grains and calcium oxide existing on the surfaces of magnesium oxide grains. The calcium oxide content thereof is between 0.005 mass % and 1.5 mass % in terms of Ca.

First claim

The invention claimed is:

1. A synthesis gas production catalyst to be used for producing synthesis gas containing carbon monoxide and hydrogen from source gas containing methane-containing light hydrocarbons and carbon dioxide, wherein the catalyst comprises at least either one of the metals of ruthenium and rhodium carried on a carrier which contains magnesium oxide grains and calcium oxide existing on the surfaces of the magnesium oxide grains and shows a calcium oxide content between 0.005 mass % and 1.5 mass % in terms of Ca, and
wherein the calcium oxide exists on the surfaces of the magnesium oxide grains by 0.05 mg-Ca/m 2 -MgO to 150 mg-Ca/m 2 -MgO in terms of Ca.

2. The synthesis gas production catalyst according to claim 1 , wherein the calcium oxide exists within 10% of the depth from the surface of the carrier.

3. The synthesis gas production catalyst according to claim 1 , wherein the magnesium oxide grains have a calcium oxide-containing layer formed on the surfaces thereof.

4. The synthesis gas production catalyst according to claim 1 , wherein the metal is carried by the carrier within a range between 200 mass ppm and 2,000 mass ppm relative to the carrier in terms of metal.

5. The synthesis gas production catalyst according to claim 1 , wherein the metal exists in the vicinity of the calcium oxide on the surfaces of the magnesium oxide grains.

6. The synthesis gas production catalyst according to claim 1 , wherein the metal exists within 10% of the depth from the surface of the synthesis gas production catalyst.

7. The synthesis gas production catalyst according to claim 1 , wherein the specific surface area of the synthesis gas production catalyst is between 0.1 m 2 /g and 1.0 m 2 /g.

8. The synthesis gas production catalyst according to claim 1 , wherein the magnesium oxide grains have a calcium oxide-containing layer containing calcium oxide and a metal-containing layer containing the metal on the surfaces thereof.

9. The synthesis gas production catalyst according to claim 1 , wherein metal particles containing the metal exist on the surfaces of the magnesium oxide grains.

Assignees

• Chiyoda Corp

Inventors

• Yagi Fuyuki
• Nagumo Atsuro
• Kanai Ryuichi

Classifications

• Y02P20/52

  using catalysts, e.g. selective catalysts · CPC title

• C01B32/40

  Carbon monoxide · CPC title

• B01J23/58

  with alkali- or alkaline earth metals · CPC title

• C01B2203/0233

  the reforming step being a steam reforming step · CPC title

• C01B2203/1241

  Natural gas or methane · CPC title