Fired equipment exhaust recovery system

Patent metadata

Field	Value
Publication number	US-12533633-B2
Application number	US-202217932923-A
Country	US
Kind code	B2
Filing date	Sep 16, 2022
Priority date	Sep 16, 2022
Publication date	Jan 27, 2026
Grant date	Jan 27, 2026

Abstract

A system and a process for reducing greenhouse gas emissions are disclosed herein. The system may include a combustion zone, a catalytic converter, a methanation reactor, a compressor, a normal venting unit, a vacuum protection unit, and a control system. The process may include feeding a fuel, a methane-containing gas, and an oxygen-containing gas into a first reactor unit, and producing a combustion products stream comprising carbon monoxide, carbon dioxide, and water. The process may include cooling the combustion products stream via a cooling system, feeding the cooled exhaust stream and hydrogen to a second reactor unit. The second reactor unit may include a first catalyst for reacting oxygen with carbon monoxide to form carbon dioxide, and a second catalyst for reacting carbon dioxide with hydrogen to produce methane. The process may include recovering an effluent from the second reactor unit and feeding it to the first reactor unit.

First claim

What is claimed as new and desired to be protected by Letters Patent is:

1 . A process for reducing greenhouse gas emissions in fired equipment, the process comprising:
feeding a fuel, a methane-containing gas, and an oxygen-containing gas into a first reactor unit; producing a combustion products stream from the first reactor unit, the combustion products stream comprising carbon monoxide, carbon dioxide, and water; cooling the combustion products stream via a cooling system to produce a cooled exhaust stream; feeding the cooled exhaust stream and hydrogen to a second reactor unit, the second reactor unit comprising a first reaction zone containing a catalyst for catalytically reacting oxygen with carbon monoxide to form carbon dioxide and a second reaction zone containing a catalyst for reacting carbon dioxide with hydrogen to produce methane, and converting at least 80% of the carbon dioxide to methane; recovering an effluent from the second reactor unit comprising methane and carbon dioxide; and feeding the effluent to the first reactor unit as the methane-containing gas.

2 . The process of claim 1 , comprising converting at least 90% of the carbon dioxide to methane.

3 . The process of claim 1 , wherein the hydrogen is mixed with the cooled exhaust stream intermediate the first reaction zone and second reaction zone.

4 . The process of claim 1 , wherein the catalyst in the first reaction zone comprises one or more of platinum, palladium, and rhodium, and wherein the catalyst in the second reaction zone comprises one or more of ruthenium and cobalt.

5 . The process of claim 1 , wherein cooling comprising maintaining the first reaction zone and the second reaction zone at a temperature in a range from about 650° F. to about 720° F.

6 . The process of claim 1 , further comprising maintaining the first reaction zone and the second reaction zone at a pressure in a range from about 25 to about 45 psig.

7 . The process of claim 1 , wherein:
the fuel comprises one or more of coal, wood, or a hydrocarbon mixture; and the oxygen-containing gas is one or selected from the group consisting of air, oxygen-enriched air, and purified oxygen.

8 . The process of claim 1 , further comprising one or both of:
compressing the methane-containing gas; and condensing water out of the methane-containing gas.

9 . The process of claim 1 , further comprising one or both of:
feeding the oxygen-containing gas to the first reactor unit at a flow rate to provide greater than stoichiometric oxygen; and feeding hydrogen to the second reaction zone at a flow rate to provide less than stoichiometric hydrogen.

10 . The process of claim 1 , wherein the first reactor unit is a firebox comprising a radiant zone, a convective zone, and an exhaust zone, and wherein the second reactor unit is disposed in either the convective zone or the exhaust zone.

11 . The process of claim 10 , further comprising reducing a temperature of the combustion products stream, the cooled exhaust stream, or the effluent from the second reactor unit via indirect heat exchange with one or more of a water stream, a steam stream, a fuel stream, a hydrocarbon containing stream, or an oxygen-containing gas.

12 . The process of claim 1 , further comprising controlling a pressure of the cooled exhaust stream by opening or closing a valve of a vacuum protection unit.

Assignees

• Saudi Arabian Oil Co

Inventors

• Alhazmi Shadi M
• Alahdal Ahmad M
• Alsowayigh Hamed S
• Almulla Abdullraheem U

Classifications

• B01J2219/00245

  Avoiding undesirable reactions or side-effects · CPC title

• B01J2219/00225

  stopping the system or generating an alarm · CPC title

• B01J2219/00186

  controlling the composition of the reactive mixture · CPC title

• B01J2219/00164

  controlling the flow · CPC title

• B01J2219/00162

  controlling the pressure · CPC title