Reversible solid adsorption method and system utilizing waste heat for on-board recovery and storage of CO2 from motor vehicle internal combustion engine exhaust gases

US9581062B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9581062-B2
Application numberUS-201213980508-A
CountryUS
Kind codeB2
Filing dateJan 20, 2012
Priority dateJan 20, 2011
Publication dateFeb 28, 2017
Grant dateFeb 28, 2017

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  1. Title

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  2. Abstract

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  5. First independent claim

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Abstract

Official abstract text for this publication.

A method and system for on-board treatment of an exhaust stream containing CO 2 emitted by an internal combustion engine in order to reduce the amount of CO 2 discharged into the atmosphere which include: a. a treatment zone, preferably operating in swing mode with at least two subsystems, on board the vehicle containing a capture agent having a predetermined capacity for extracting CO 2 from the exhaust stream, each subsystem having a heat exchanger with an inlet for admitting the hot exhaust gas stream for passage in heat relation with the capture agent to release CO 2 and regenerate the capture agent, an outlet for passage of a treated, cooled exhaust stream having a reduced CO 2 content, and an outlet for CO 2 released from the regenerated capture agent; b. a compression zone for reducing the volume of the CO 2 ; and c. a storage zone for the temporary storage of compressed CO 2 .

First claim

Opening claim text (preview).

The invention claimed is: 1. An integrated method for reducing the amount of CO 2 discharged into the atmosphere with an exhaust gas stream emitted by an internal combustion engine (ICE) used to power a vehicle, the method comprising: a. passing the exhaust gas stream into contact with a CO 2 capture agent on board the vehicle, the capture agent having a predetermined capacity to extract CO 2 from the exhaust stream; b. discharging a treated exhaust gas stream having a reduced CO 2 content into the atmosphere; c. discontinuing the passage of the exhaust gas stream in contact with the capture agent when the concentration of the CO 2 extracted by the capture agent has reached a predetermined level; d. heating the CO 2 capture to release the extracted CO 2 and regenerate the capture agent by heat exchange with a hot engine coolant stream at a temperature in the range of about 90° C. to 120° C. and the hot exhaust gas stream at a temperature in the range of about 300° C. to 650° C.; e. recovering an essentially pure CO 2 gas stream; f. recovering heat and energy from the hot exhaust gas stream emitted by the ICE by contact with an energy conversion medium; g. compressing the recovered CO 2 gas on board the vehicle to reduce its volume using the energy recovered in step (f); and h. temporarily storing the compressed CO 2 on board the vehicle. 2. The method of claim 1 which operates substantially continuously following start-up of the vehicle's ICE. 3. The method of claim 1 which further includes measuring the CO 2 level remaining in the treated exhaust gas stream and comparing the value of the measured level to a predetermined limiting value. 4. The method of claim 3 where the limiting value corresponds to the predetermined capacity of the CO 2 capture agent and the passage of the exhaust gas stream in contact with the CO 2 capture agent is discontinued when the limiting value is reached. 5. The method of claim 1 in which the heat exchange occurs in a tube and shell heat exchanger. 6. The method of claim 1 in which the CO 2 capture agent is a high temperature solid adsorbent selected from the group consisting of chemical adsorbents and physical adsorbents. 7. The method of claim 1 in which the CO 2 capture agent is selected from solid adsorbents and liquid adsorbents on a solid carrier. 8. The method of claim 1 in which the CO 2 capture agent is a solid adsorbent that is contacted with the exhaust gas stream in a fixed bed or a fluidized bed. 9. The method of claim 1 in which a portion of the heat energy of the exhaust stream is utilized in the regeneration step (d) and compression of step (g). 10. The method of claim 1 in which the CO 2 content of the exhaust gas stream is reduced by at least 10%. 11. The method of claim 1 in which the capture agent is maintained in two separate swing zones and the exhaust gas is passed through one of the zones while the other zone is heated to release CO 2 and regenerate the capture agent. 12. The method of claim 1 in which the hot exhaust from the vehicle's engine is passed in heat exchange relation in step (d) to regenerate the capture agent. 13. The method of claim 1 in which the passage of the exhaust gas stream in contact with the capture agent in step (c) is discontinued when the temperature or rate of increase of the temperature of the capture agent reaches a predetermined value. 14. The method of claim 13 in which the temperature is measured by a plurality of temperature sensors in contact with the capture agent. 15. The method of claim 1 in which the passage of the exhaust gas stream in contact with the capture agent in step (c) is discontinued when the pressure or the rate of increase of the pressure in a vessel containing the capture agent of step (c) during its heating in step (d) reaches a predetermined value. 16. An integrated system for on-board treatment of an exhaust gas stream containing CO 2 emitted by a hydrocarbon-fueled internal combustion engine (ICE) used to power a vehicle in order to reduce the amount of CO 2 discharged into the atmosphere, the ICE including a liquid coolant system, the system comprising: a. a treatment zone on board the vehicle containing a capture agent having a predetermined capacity for extracting CO 2 from the exhaust stream, the treatment zone having an inlet for admitting the exhaust gas stream and an outlet for passage of a treated exhaust stream having a reduced CO 2 content, the treatment zone further including a heat exchanger with an inlet for receiving the hot exhaust gas stream that has a temperature in the range from about 300° C. to 650° C. from the ICE tor passage in heat exchange relation with the capture agent to heat the capture agent to a temperature in the range from about 300° C. to 500° C. to release CO 2 and regenerate the capture agent, and an outlet for the cooled exhaust gas stream, an inlet for receiving a hot engine coolant stream that has a temperature in the range from about 90° C. to 120° C. for passage in heat exchange relation with the capture agent to release CO 2 and regenerate the capture agent, and an outlet for the cooled coolant stream, the treatment zone having a CO 2 discharge outlet for CO 2 released from the regenerated capture agent; b. a compression zone in fluid communication with the CO 2 discharge outlet from the treatment zone, the compression zone including one or more compressors for reducing the volume of the CO 2 ; c. a storage zone for receiving the compressed CO 2 for temporary storage on board the vehicle; and d. an exhaust gas conduit in fluid communication with the treated exhaust gas stream outlet from the treatment zone. 17. The system of claim 16 in which the treatment system is comprised of at least two parallel subsystems configured and constructed to operate in swing mode, with valves to direct the vehicle's exhaust to one and then another of the at least two subsystems for extraction of CO 2 and simultaneously regenerate the capture agent in another of the at least two subsystems, whereby the system is operable continuously to treat the engine exhaust stream. 18. The system of claim 16 which includes a diverter valve for regulating the volumetric amount of the exhaust gas stream which passes into the treatment zone before being discharged into the atmosphere. 19. The system of claim 18 in which the diverter valve is controlled based on the operating conditions of the ICE. 20. The system of claim 16 which includes control means for discharging all or a portion of the exhaust gas stream into the atmosphere without passing through the treatment zone.

Assignees

Inventors

Classifications

  • Cross-Sectional Technologies · mapped topic

  • of sodium · CPC title

  • of magnesium · CPC title

  • Employing advanced heat integration, e.g. Pinch technology · CPC title

  • F01N3/00Primary

    Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust (electric control F01N9/00; monitoring or diagnostic devices for exhaust-gas treatment apparatus F01N11/00) · CPC title

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What does patent US9581062B2 cover?
A method and system for on-board treatment of an exhaust stream containing CO 2 emitted by an internal combustion engine in order to reduce the amount of CO 2 discharged into the atmosphere which include: a. a treatment zone, preferably operating in swing mode with at least two subsystems, on board the vehicle containing a capture agent having a predetermined capacity for extracting …
Who is the assignee on this patent?
Hamad Esam Zaki, Al-Sadat Wajdi Issam, Saudi Arabian Oil Co
What technology area does this patent fall under?
Primary CPC classification F01N3/00. Mapped technology areas include Mechanical Engineering.
When was this patent published?
Publication date Tue Feb 28 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).