System and method for carbon dioxide capture and sequestration from relatively high concentration CO;mixtures

• US 9,028,592 B2
• Filed: 05/02/2013
• Issued: 05/12/2015
• Est. Priority Date: 04/30/2010
• Status: Active Grant

• Current Assignee: Global Thermostat Operations LLC
• Original Assignee: Peter Eisenberger
• Inventors: Eisenberger, Peter
• Primary Examiner(s): Jones, Christopher P
• Application Number:
  US13/886,207
• Publication Number:
  US 20130312606A1
• Time in Patent Office: 740 Days
• Field of Search: 951/07, 951/39, 961/28, 961/46
• US Class Current: 95/139
• CPC Class Codes: B01D 2252/204 Amines
• CPC Class Codes: B01D 2252/20421 Primary amines
• CPC Class Codes: B01D 2253/106 Silica or silicates
• CPC Class Codes: B01D 2253/108 Zeolites
• CPC Class Codes: B01D 2257/504 Carbon dioxide
• CPC Class Codes: B01D 2258/0283 Flue gases
• CPC Class Codes: B01D 2258/06 Polluted air
• CPC Class Codes: B01D 2259/4005 Nature of purge gas
• CPC Class Codes: B01D 2259/402 using two beds
• CPC Class Codes: B01D 53/0407 Constructional details of adsorbing systems
• CPC Class Codes: B01D 53/047 Pressure swing adsorption
• CPC Class Codes: B01D 53/06 with moving adsorbents, e.g. rotating beds B01D53/025 takes precedence
• CPC Class Codes: B01D 53/1406 Multiple stage absorption
• CPC Class Codes: B01D 53/1412 Controlling the absorption process
• CPC Class Codes: B01D 53/1418 Recovery of products
• CPC Class Codes: B01D 53/1425 Regeneration of liquid absorbents
• CPC Class Codes: B01D 53/1475 Removing carbon dioxide
• CPC Class Codes: B01D 53/1493 Selection of liquid materials for use as absorbents
• CPC Class Codes: B01D 53/18 Absorbing units; Liquid distributors therefor B01D3/16, B01D3/26, B01D3/30 take precedence; packing elements B01J19/30, B01J19/32
• CPC Class Codes: B01D 53/346 Controlling the process
• CPC Class Codes: B01D 53/62 : Carbon oxides
• CPC Class Codes: B01J 20/08 : comprising aluminium oxide or hydroxide; comprising bauxite
• CPC Class Codes: B01J 20/103 : comprising silica
• CPC Class Codes: B01J 20/22 : comprising organic material
• CPC Class Codes: B01J 20/28042 : Shaped bodies; Monolithic structures
• CPC Class Codes: B01J 20/3425 : of sorbents or filter aids comprising organic materials
• CPC Class Codes: B01J 20/3466 : with steam
• CPC Class Codes: Y02A 50/20 : Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
• CPC Class Codes: Y02C 20/40 : of CO2

Abstract

A system and method of reducing the net carbon dioxide footprint of an industrial process that generates power from the combustion of hydrocarbon fuels in which ambient air is admixed with up to 50% by volume of an effluent gas from the power generator of the industrial process, in order to substantially increase the CO₂ concentration in the air prior to treatment. The treatment comprises adsorbing CO₂ from the admixed ambient air utilizing a cooled, porous substrate-supported amine adsorbent, wherein the porous substrate initially contacts the mixed ambient air containing condensed water in its pores, which act as an intrinsic coolant with respect to the exothermic heat generated by the adsorption process. In addition, prior to regenerating the supported adsorbent, air pressure is substantially reduced in the sealed regeneration chamber and the low pressure chamber is placed in fluid connection with a higher pressure regeneration chamber containing steam and carbon dioxide, to preheat the sorbent to be regenerated and to quickly cool the regenerated sorbent prior to use for further CO₂ adsorption.

Claims

1. A method of removing and capturing concentrated carbon dioxide from carbon dioxide laden air, the method comprising

admixing a first flow of carbon dioxide-laden ambient air with not more than 50% by volume of an effluent gas, where the effluent gas is derived from a flue gas from the combustion of hydrocarbons, and directing the first flow of admixed ambient air to a first carbon dioxide removal structure;

the carbon dioxide removal structure comprising a sorbent supported upon a porous substrate and capable of exothermically and releasably binding carbon dioxide to remove a predetermined portion of the carbon dioxide from the first admixed ambient air mixture;

passing the first carbon dioxide removal structure into a first sealed carbon dioxide capture chamber, exhausting air from the first sealed capture chamber to reduce the air pressure therein, and passing steam, at a temperature of not greater than 120°

C. into and through the first carbon dioxide removal structure to strip carbon dioxide from the sorbent and regenerate the sorbent, and removing the stripped carbon dioxide from the first sealed capture chamber, so as to capture concentrated carbon dioxide;

admixing a second flow of carbon dioxide-laden ambient air with not more than 50% by volume of an effluent gas, where the effluent gas is derived from a flue gas from the combustion of hydrocarbons, and directing the flow of admixed ambient air to a second carbon dioxide removal structure;

the second carbon dioxide removal structure comprising a sorbent supported upon a porous substrate and capable of releasably binding carbon dioxide to remove a predetermined portion of the carbon dioxide from the second admixed ambient air mixture;

passing the second carbon dioxide removal structure into a second sealed carbon dioxide capture chamber, exhausting air from the second sealed capture chamber to reduce the air pressure therein, and passing steam, at a temperature of not greater than 120°

C. into and through the second carbon dioxide removal structure to strip carbon dioxide from the sorbent and regenerate the sorbent, while the steam condenses, and removing the stripped carbon dioxide from the second sealed capture chamber, so as to capture concentrated carbon dioxide;

the first and second carbon dioxide removal structures being operated in tandem, such that when the first carbon dioxide removal structure has completed a regeneration cycle, and the second carbon dioxide removal structure is prepared to carry out its regeneration, the remaining steam in the first carbon dioxide capture chamber is flashed into the reduced pressure second carbon dioxide capture chamber in order to cool the first carbon dioxide removal structure and prewarm the second carbon dioxide removal structure prior to regeneration with saturated steam; and

the first carbon dioxide removal structure is removed from the first capture chamber and moved into a flow of admixed ambient air;

passing saturated steam into the second carbon dioxide capture chamber to regenerate the second carbon dioxide removal structure and removal of the carbon dioxide and condensed steam from the second carbon dioxide removal structure; and

repeating the tandem operation so that the first carbon dioxide removal structure is returned to the first carbon dioxide capture chamber after adsorbing carbon dioxide from the flow of admixed air and the pressure in the first carbon dioxide capture chamber is reduced, and opened to the higher pressure in the second carbon dioxide capture chamber.

2. The method of claim 1, wherein the carbon dioxide and condensed steam removed from each of the capture structures is passed to a separation vessel to remove condensed steam as liquid and to pass the concentrated carbon dioxide for further processing.

3. The method of claim 2, wherein the carbon dioxide is further processed by being compressed sufficiently to remove remaining water vapor to obtain highly concentrated CO2 of at least 95% purity.

4. The method of claim 1, wherein the pressure in each of the carbon dioxide capture chambers is reduced to not greater than 0.2 BarA.

5. The method of claim 1, wherein the pressure in each of the carbon dioxide capture chambers is reduced to not greater than 0.15 BarA.

6. The method of claim 1, wherein the admixed ambient air contains a concentration of CO₂ at least two orders of magnitude greater than the concentration of CO₂ in ambient air.

7. The method of claim 1, wherein the carbon dioxide removal structure comprises an array of porous substrate monoliths formed of a material selected from the group consisting of silica, alumina, and alumina coated silica, and wherein the substrate is supporting an amine sorbent.

8. The method of claim 7, wherein the sorbent is a primary amine.

9. The method of claim 1, wherein the steam is saturated steam.

10. The method of claim 9, wherein the saturated steam is process heat steam.

11. The method of claim 5, wherein the pressure in each of the carbon dioxide capture chambers is reduced to 0.1 BarA.

12. The method of claim 1, wherein condensed steam remains in the pores of the substrate when the regenerated carbon dioxide removal structure is removed from the capture chamber and moved back into a flow of admixed ambient air, so as to serve to moderate the temperature of the sorbent and substrate when adsorbing CO₂ from the admixed air.

13. The method of claim 12, wherein the ambient air is admixed with less than 50% by volume of the effluent gas.