Method and apparatus for separating carbon dioxide from a residual gas in a fluidised bed catalytic cracking plant (FCC)

Patent metadata

Field	Value
Publication number	US-12551840-B2
Application number	US-202017786956-A
Country	US
Kind code	B2
Filing date	Dec 10, 2020
Priority date	Dec 19, 2019
Publication date	Feb 17, 2026
Grant date	Feb 17, 2026

Abstract

A process for separating carbon dioxide from a waste gas of a fluid catalytic cracking installation including converting at least a portion of the carbon monoxide of the waste gas into carbon dioxide to form a flow enriched in carbon dioxide, separating at least a portion of the flow enriched in carbon dioxide to form a gas enriched in carbon dioxide and depleted in nitrogen and a gas rich in nitrogen and depleted in carbon dioxide, and at least a portion of the gas enriched in carbon dioxide and depleted in nitrogen is separated by way of separation at a temperature of less than 0° C. to form a fluid rich in carbon dioxide and a fluid depleted in carbon dioxide and sending a gas containing at least 90% oxygen to combustion.

First claim

The invention claimed is:

1 . A process for separating carbon dioxide from a waste gas of a fluid catalytic cracking installation containing carbon dioxide, nitrogen and carbon monoxide, the process comprising:
i) converting at least a portion of the carbon monoxide of the waste gas into carbon dioxide to form a flow enriched in carbon dioxide by combustion, ii) separating at least a portion of the flow enriched in carbon dioxide from step i) by adsorption to form a gas enriched in carbon dioxide and depleted in nitrogen and a gas rich in nitrogen and depleted in carbon dioxide, and at least a portion of the gas enriched in carbon dioxide and depleted in nitrogen is separated in a separation apparatus at a temperature of less than 0° C. by partial condensation and/or by distillation to form a fluid rich in carbon dioxide and a fluid depleted in carbon dioxide and iii) sending a gas containing at least 90% oxygen and a gas containing at least 40% carbon dioxide, consisting either of a product of the separation of the flow enriched in carbon dioxide, or of a portion of the flow enriched in carbon dioxide, to the combustion of step i).

2 . The process as claimed in claim 1 , wherein the gas rich in nitrogen and depleted in carbon dioxide contains less than 5 mol % CO 2 .

3 . The process as claimed in claim 1 , wherein the fluid rich in carbon dioxide contains more than 45 mol % CO 2 .

4 . The process as claimed in claim 1 , wherein the fluid depleted in carbon dioxide is compressed and mixed with the flow enriched in carbon dioxide sent to step ii).

5 . The process as claimed in claim 1 , wherein the gas rich in nitrogen and depleted in carbon dioxide is expanded in a turbine and is sent to the atmosphere.

6 . The process as claimed in claim 5 , wherein the gas rich in nitrogen and depleted in carbon dioxide is heated by a fluid originating from the catalytic cracking installation or by at least a portion of the gas enriched in carbon dioxide and depleted in nitrogen or by at least a portion of the waste gas, or at least a portion of the flow enriched in carbon dioxide.

7 . The process as claimed in claim 1 , wherein the waste gas is expanded upstream of step i) in a turbine and the flow enriched in carbon dioxide is compressed in a compressor driven by the turbine upstream of step ii).

8 . The process as claimed in claim 7 , wherein the compressor for the flow enriched in carbon dioxide upstream of step ii) and the turbine for the waste gas are mounted on a shaft or a speed-increasing gearing, and wherein an electricity generator and/or a motor is mounted on the shaft or the speed-increasing gearing.

9 . The process as claimed in claim 1 , wherein the fluid depleted in carbon dioxide and/or the gas rich in nitrogen and depleted in carbon dioxide is expanded in a turbine to a temperature of less than 0° C. and greater than −100° C. in a chamber containing the separation apparatus.

10 . The process as claimed in claim 1 , wherein at least a portion of the gas rich in nitrogen and depleted in carbon dioxide and/or at least a portion of the fluid rich in carbon dioxide and/or at least a portion of the fluid depleted in carbon dioxide is/are sent to the combustion of the carbon monoxide.

11 . The process as claimed in claim 1 , wherein the waste gas leaving a regenerator of the fluid catalytic cracking installation contains more than 50% nitrogen.

Assignees

• Air Liquide
• Air Liquide

Inventors

• Rodrigues Guillaume
• Dubettier-Grenier Richard

Classifications

• F25J2260/80

  Integration in an installation using carbon dioxide, e.g. for EOR, sequestration, refrigeration etc. · CPC title

• F25J2240/90

  Hot gas waste turbine of an indirect heated gas for power generation · CPC title

• F25J2240/12

  the fluid being nitrogen · CPC title

• F25J2230/30

  Compression of the feed stream · CPC title

• F25J2230/20

  Integrated compressor and process expander; Gear box arrangement; Multiple compressors on a common shaft · CPC title