Method to capture and utilize CO2 and an installation for capturing and utilizing CO2

Patent metadata

Field	Value
Publication number	US-12460143-B2
Application number	US-202017783012-A
Country	US
Kind code	B2
Filing date	Dec 8, 2020
Priority date	Dec 9, 2019
Publication date	Nov 4, 2025
Grant date	Nov 4, 2025

Abstract

The invention relates to a cyclic method for capturing and utilizing CO 2 contained in a gas stream. The method uses three different materials, a first solid material, a second solid material and a CO 2 sorbent material.
In a first step a first gas stream comprising CO 2 and at least one reductant is brought in contact with the three materials, resulting in an outlet stream comprising water. In a second step, the captured CO 2 from the first step is released and converted to CO to produce a CO rich outlet stream. The invention further relates to an installation for capturing and utilizing CO 2 .

First claim

The invention claimed is:

1 . Cyclic method of capturing and utilizing CO 2 contained in a gas stream, said method comprising a first and a second step wherein
said first step comprises introducing a first gas stream to contact a first solid material, a second solid material and a CO 2 sorbent material, said first gas stream comprising CO 2 and at least one reductant, with the process conditions of said first step comprising a temperature ranging between 573 K and 1473 K and a pressure ranging between 0.1 and 100 bar; said second step comprises introducing a second gas stream to contact said CO 2 sorbent material, said second solid material and said first solid material, said second gas stream comprising at least one oxidant, said oxidant comprising oxygen or nitrogen oxides with the process conditions of said second step comprising a temperature ranging between 573 K and 1473 K and a pressure ranging between 0.01 and 10 bar;
wherein said first solid material has a first thermodynamic equilibrium oxygen partial pressure and said second solid material having a second thermodynamic equilibrium oxygen partial pressure, with said second thermodynamic equilibrium oxygen partial pressure being larger than said first thermodynamic equilibrium oxygen partial pressure at the process conditions of said first step and at the process conditions of said second step,
wherein said first solid material oxidizes said at least one reductant at least partially in said first step and under the process conditions of said first step and said first solid material is oxidized by CO 2 in said second step and under the process conditions of said second step and wherein said second solid material oxidizes said at least one reductant in said first step and under the process conditions of said first step and said second solid material is not oxidized by CO 2 and not oxidized by H 2 O in said second step and under the process conditions of said second step and
wherein said CO 2 sorbent material is capturing CO 2 in said first step under the process conditions of said first step and said CO 2 sorbent material is releasing CO 2 , in said second step and under the process conditions of said second step.

2 . The method according to claim 1 , wherein said second thermodynamic equilibrium oxygen partial pressure is at least one order of magnitude larger than said first thermodynamic equilibrium oxygen partial pressure at the process conditions of said first step and at the process conditions of said second step.

3 . The method according to claim 1 , wherein said first step and said second step are repeated periodically and/or wherein said method comprises in said first and/or in said second step one or more intermediate steps before or after contacting said first solid material and/or before or after contacting said second solid material and/or before or after contacting said CO2 sorbent material.

4 . The method according to claim 1 , wherein said second solid material is oxidized in said second step and under the process conditions of said second step.

5 . The method according to claim 1 , wherein said first solid material is reversibly reduced in said first step and under the process conditions of said first step.

6 . The method according to claim 1 , wherein said first solid material comprises a material comprising iron, cerium, zirconium, iridium, tungsten, molybdenum, lanthanum, strontium, samarium, neodymium, manganese or combinations thereof.

7 . The method according to claim 1 , wherein said second solid material comprises a material comprising manganese, nickel, copper, cobalt, iron, strontium, magnesium, titanium, calcium, lanthanum or combinations thereof.

8 . The method according to claim 1 , wherein said CO 2 sorbent material comprises an alkali metal or alkaline earth metal and wherein said CO 2 sorbent material is optionally promoted with a doping element selected from the group selected from the group consisting of aluminium, cerium, zirconium, magnesium or combinations thereof.

9 . The method according to claim 1 , wherein said at least one reductant comprises an organic compound, an alcohol, CO, H 2 or a mixture thereof.

10 . The method according to claim 1 , wherein said first gas stream is subsequently contacting said first solid material, said second solid material and said CO 2 sorbent material in said first step and said second gas stream is subsequently contacting said CO 2 sorbent material, said second solid material and said first solid material in said second step.

Assignees

• Univ Gent

Inventors

• Singh Varun
• Galvita Vladimir
• Saeys Mark
• Marin Guy

Classifications

• B01J20/041

  Oxides or hydroxides · CPC title

• B01D2257/504

  Carbon dioxide · CPC title

• B01D2253/1122

  Metals · CPC title

• B01D2251/102

  Oxygen · CPC title

• B01D53/82

  with stationary reactants · CPC title