Systems And Methods For Treating Carbon Dioxide

Abstract

A heat exchange assembly for treating carbon dioxide (CO.sub.2) is described. The heat exchange assembly includes a housing that includes an inlet, an outlet, and an inner surface that defines a cavity extending between the inlet and the outlet. The housing is configured to receive solid CO.sub.2 through the inlet. At least one heat exchange tube extends through the housing. The heat exchange tube is oriented to contact solid CO.sub.2 to facilitate transferring heat from solid CO.sub.2 to a heat exchanger fluid being channeled through the heat exchange tube to facilitate converting at least a portion of solid CO.sub.2 into liquid CO.sub.2. The heat exchange assembly is configured to recover a refrigeration value from the solid CO.sub.2 and transfer at least a portion of the recovered refrigeration value to a flue gas.

Description

[0001] This Application is a Division of patent application Ser. No. 13/285,375, filed on Oct. 31, 2011, the contents of which are incorporated herein by reference.

BACKGROUND OF THE INVENTION

[0003] The subject matter described herein relates generally to gas treatment systems and, more particularly, to gas treatment system for use in treating carbon dioxide (CO.sub.2).

[0004] At least some known power generation systems include a combustor and/or boiler to generate steam that is used in a steam turbine generator. During a typical combustion process within a combustor or boiler, for example, a flow of combustion gases, or flue gases, is produced. Known combustion gases contain combustion products including, but not limited to, carbon, fly ash, carbon dioxide, carbon monoxide, water, hydrogen, nitrogen, sulfur, chlorine, arsenic, selenium, and/or mercury.

[0005] At least some known power generation systems include a gas treatment system for use in reducing an amount of combustion products within the flue gases. Known gas treatment systems include a low-temperature cooling system for separating CO.sub.2 from the flue gases. During operation, the low-temperature cooling system cools a flue gas stream to form solid CO.sub.2 from gaseous CO.sub.2 suspended within the flue gas stream. In addition, at least some known gas treatment systems include a low-temperature solids pump for use in transporting the solid CO.sub.2 from the low-temperature cooling system to a CO.sub.2 sequestration system for sequestration and deposition of the CO.sub.2. During operation, the low-temperature cooling system transfers a refrigeration value to the flue gas stream to form solid CO.sub.2. As the low-temperature solids pump conveys the solid CO.sub.2 from the cooling system, at least some of the refrigeration value may be lost to heat generated from operation of the solids pump. The loss of refrigeration value through the solids pump increases the cost of operating the gas treatment system by increasing an amount of energy required to cool the flue gas stream.

BRIEF DESCRIPTION OF THE INVENTION

[0006] In one aspect, a heat exchange assembly for treating carbon dioxide (CO.sub.2) is provided. The heat exchange assembly includes a housing that includes an inlet, an outlet, and an inner surface that defines a cavity extending between the inlet and the outlet. The housing is configured to receive solid CO.sub.2 through the inlet. At least one heat exchange tube extends through the housing. The heat exchange tube is oriented to contact solid CO.sub.2 to facilitate transferring heat from solid CO.sub.2 to a heat exchanger fluid being channeled through the heat exchange tube to facilitate converting at least a portion of solid CO.sub.2 into liquid CO.sub.2. The heat exchange assembly is configured to recover a refrigeration value from the solid CO.sub.2 and transfer at least a portion of the recovered refrigeration value to a flue gas.

[0007] In another aspect, a gas treatment system for use in treating carbon dioxide (CO.sub.2) in a flue gas is provided. The gas treatment system includes a cooling system coupled to a source of flue gas and configured to receive a flow of flue gas from the source. The cooling system is configured to cool gaseous CO.sub.2 suspended within the flue gas to form solid CO.sub.2. A heat exchange assembly is coupled to the cooling system for receiving a flow of solid CO.sub.2 from the cooling system. The heat exchange assembly is configured to recover a refrigeration value from the solid CO.sub.2 and transfer at least a portion of the recovered refrigeration value to the flue gas. The heat exchange assembly includes a housing that includes an inlet, an outlet, and an inner surface that defines a cavity extending between the inlet and the outlet. The housing is configured to receive solid CO.sub.2 through the inlet. At least one heat exchange tube extends through the housing. The heat exchange tube is oriented to contact solid CO.sub.2 to facilitate transferring heat from solid CO.sub.2 to a heat exchanger fluid being channeled through the heat exchange tube to facilitate converting at least a portion of solid CO.sub.2 into liquid CO.sub.2.

[0008] In yet another aspect, a method of treating carbon dioxide (CO.sub.2) is provided. The method includes channeling a flue gas containing CO.sub.2 to a cooling system to cool the flue gas to form solid CO.sub.2, and channeling solid CO.sub.2 to a heat exchanger assembly. The heat exchanger assembly includes a housing that is configured to receive solid CO.sub.2 therein, and at least one heat exchange tube extending through the housing. A pressure within the housing is adjusted to maintain the housing pressure within a predefined range of pressures to prevent re-sublimation of solid CO.sub.2. A flow of heat exchange fluid is channeled through the at least one heat exchange tube to facilitate a transfer of heat from solid CO.sub.2 to the heat exchange fluid to convert at least a portion of solid CO.sub.2 into liquid CO.sub.2, and to recover a refrigeration value from the CO.sub.2. At least a portion of the recovered refrigeration value is transferred to the flue gas to facilitate cooling the flue gas.

BRIEF DESCRIPTION OF THE DRAWINGS

[0009] FIG. 1 is a schematic view of an exemplary power generation system.

[0010] FIG. 2 is a schematic view of an exemplary heat exchanger assembly that may be used with the power generation system shown in FIG. 1.

[0011] FIGS. 3-4 are schematic views of alternative embodiments of the heat exchanger assembly shown in FIG. 2.

[0012] FIG. 5 is an alternative embodiment of the power generation system shown in FIG. 1.

[0013] FIG. 6 is another embodiment of the power generation system shown in FIG. 1.

[0014] FIG. 7 is a flow chart of an exemplary method that may be used to treat carbon dioxide generated during operation of the power generation system shown in FIG. 1.

DETAILED DESCRIPTION OF THE INVENTION

[0015] The exemplary systems and methods described herein overcome at least some disadvantages of known gas treatment systems by providing a gas treatment system that includes a heat exchange assembly that is configured to transfer heat from a heat exchange fluid to solid CO.sub.2 to facilitate recovering a refrigeration value from solid CO.sub.2. Moreover, the heat exchange assembly is configured to maintain CO.sub.2 in solid-liquid phase equilibrium to enable the heat exchange assembly to transfer heat to solid CO.sub.2 to facilitate forming liquid CO.sub.2 for use in pre-cooling a flue gas. By providing a gas treatment system that includes a heat exchange assembly configured to recover a refrigeration value from solid CO.sub.2, the cost of treating CO.sub.2 suspended within a flue gas is reduced as compared to known gas treatment systems.

[0016] FIG. 1 is a schematic view of an exemplary power generation system 10. FIG. 2 is a schematic view of an exemplary heat exchange assembly 12 that may be used with power generation system 10. In the exemplary embodiment, power generation system 10 includes a combustor assembly 14, a steam generation assembly 16 downstream of combustor assembly 14, and a steam turbine engine 20 coupled to steam generation assembly 16. Combustor assembly 14 includes at least one combustor 22, a fuel supply system 24, and an air supply system 26. Fuel supply system 24 is coupled to combustor 22 for channeling a flow of fuel such as, for example, coal to combustor 22. Alternatively, fuel supply system 24 may channel any other suitable fuel, including but not limited to, oil, natural gas, biomass, waste, and/or any other fossil and/or renewable fuel that enables power generation system 10 to function as described herein. In addition, air supply system 26 is coupled to combustor 22 for channeling a flow of air to combustor 22. Combustor 22 is configured to receive a predetermined quantity of fuel and air from fuel supply system 24 and air supply system 26, respectively, and ignite the fuel/air mixture to generate combustion or flue gases. Moreover, combustor 22 channels a flow of flue gases 28 to steam generation assembly 16 to generate steam that is channeled to steam turbine engine 20 for use in generating a power load.

[0017] In the exemplary embodiment, steam generation assembly 16 includes at least one heat recovery steam generator (HRSG) 30 that is coupled in flow communication with a boiler feedwater assembly 32. HRSG 30 receives a flow of boiler feedwater 33 from boiler feedwater assembly 32 to facilitate heating boiler feedwater 33 to generate steam. HRSG 30 also receives flue gases 28 from combustor assembly 14 to further heat boiler feedwater 33 to generate steam. HRSG 30 is configured to facilitate transferring heat from flue gases 28 to boiler feedwater 33 to generate steam, and channel steam 34 to steam turbine engine 20. Steam turbine engine 20 includes one or more steam turbines 36 that are rotatably coupled to a power generator 38 with a drive shaft 40. HRSG 30 discharges steam 34 towards steam turbine 36 wherein thermal energy in the steam is converted to mechanical rotational energy. Steam 34 imparts rotational energy to steam turbine 36 and to drive shaft 40, which subsequently drives power generator 38 to facilitate generating a power load.

[0018] In the exemplary embodiment, power generation system 10 includes a gas treatment system 42 that is downstream from combustor assembly 14 and steam generation assembly 16. Gas treatment system 42 is configured to receive flue gases 28 exhausted from combustor assembly 14 and/or steam generation assembly 16 to facilitate removing combustion products including, but not limited to, carbon, fly ash, carbon dioxide, carbon monoxide, water, hydrogen, nitrogen, sulfur, chlorine, arsenic, selenium, and/or mercury from the flue gases.

[0019] In the exemplary embodiment, gas treatment system 42 includes a flue gas pre-cooling system 44, a low-temperature cooling system 46 downstream of flue gas pre-cooling system 44, a CO.sub.2 separator 48 downstream of cooling system 46, heat exchange assembly 12 downstream of cooling system 46, and a CO.sub.2 utilization system 52 downstream of heat exchange assembly 12. Flue gases 28 including gaseous CO.sub.2 and nitrogen (N.sub.2) are channeled to flue gas pre-cooling system 44 from combustor assembly 14 and/or steam generation assembly 16. Flue gas pre-cooling system 44 facilitates a heat transfer from flue gases 28 to a heat exchange fluid 54 being channeled through flue gas pre-cooling system 44 to facilitate reducing a temperature of flue gases 28. Pre-cooling system 44 channels the cooled flue gases 28 to cooling system 46.

[0020] Cooling system 46 is configured to treat flue gases 28 to cool gaseous CO.sub.2 within flue gases 28 to form solid CO.sub.2. Cooling system 46 channels cooled flue gases 28 and solid CO.sub.2 to CO.sub.2 separator 48 to facilitate separating solid CO.sub.2 and N.sub.2 from flue gases 28. CO.sub.2 separator 48 channels solid CO.sub.2 56 to heat exchange assembly 12 to facilitate transferring heat from heat exchange fluid 54 to solid CO.sub.2 56. Moreover, heat exchange assembly 12 is configured to facilitate transferring of heat from solid CO.sub.2 56 to heat exchange fluid 54 being channeled through heat exchange assembly 12 to facilitate converting solid CO.sub.2 56 to liquid CO.sub.2 58. Moreover, heat exchange assembly 12 is configured to recover a refrigeration value from solid CO.sub.2 56 and transfer at least a portion of the recovered refrigeration value to the flue gases 28 to facilitate cooling flue gases 28. In addition, heat exchange assembly 12 is configured to channel liquid CO.sub.2 58 to CO.sub.2 utilization system 52 for utilization of rich CO.sub.2. In one embodiment, CO.sub.2 utilization system 52 includes a sequestration system for sequestration of rich CO.sub.2. Alternatively, utilization system 52 may include any system configured to use CO.sub.2 for any purpose. In the exemplary embodiment, heat exchange assembly 12 is also configured to adjust a temperature and a pressure within heat exchange assembly 12 such that CO.sub.2 within heat exchange assembly 12 is in solid-liquid phase equilibrium.

[0021] Heat exchange assembly 12 includes a heat exchanger 60 and a lockhopper assembly 62. Lockhopper assembly 62 is coupled between heat exchanger 60 and CO.sub.2 separator 48 for channeling solid CO.sub.2 56 from CO.sub.2 separator 48 to heat exchanger 60. Lockhopper assembly 62 includes a tank 64 that is configured to receive solid CO.sub.2 56 from CO.sub.2 separator 48, and a valve assembly 66 coupled between tank 64 and heat exchanger 60 to enable solid CO.sub.2 56 to be selectively channeled to heat exchanger 60 from tank 64. Lockhopper assembly 62 is configured to adjust a pressure within tank 64 such that a pressure within tank 64 is within a range of pressures such that solid CO.sub.2 56 remains in the solid phase. In addition, lockhopper assembly 62 is configured to enable solid CO.sub.2 56 to be gravity fed from tank 64 into heat exchanger 60. In the exemplary embodiment, lockhopper assembly 62 is configured to maintain an interior pressure equal to about 7 atm.

[0022] Heat exchanger 60 includes a housing 68 and at least one heat exchange tube 70 that extends through housing 68. Housing 68 includes an inlet 72, an outlet 74, and an inner surface 76 that defines a cavity 78 extending between inlet 72 and outlet 74. Housing 68 is configured to maintain a pressure within cavity 78 within a predefined range of pressures to facilitate preventing re-sublimation of solid CO.sub.2 56 to gaseous CO.sub.2 within cavity 78. In the exemplary embodiment, housing 68 is configured to maintain an internal pressure of about 7 atm. In one embodiment, housing 68 is configured to maintain an internal pressure between about 1 atm to about 10 atm. Moreover, lockhopper assembly 62 channels a flow of pressurized fluid to housing cavity 78 through valve assembly 66 to pressurize housing 68 to a predefined pressure. In the exemplary embodiment, inner surface 76 includes an upper portion 80, and a lower portion 82 that extends below upper portion 80. Inlet 72 extends through upper portion 80 and is coupled to lockhopper assembly 62 for receiving solid CO.sub.2 56 from lockhopper assembly 62. In addition, housing lower portion 82 is sized and shaped to contain liquid CO.sub.2 58 therein. Outlet 74 extends through lower portion 82, and is coupled to CO.sub.2 utilization system 52. More specifically, heat exchange assembly 12 includes a liquid CO.sub.2 pump 84 that is coupled between heat exchanger 60 and CO.sub.2 utilization system 52 for channeling liquid CO.sub.2 58 from lower portion 82 to CO.sub.2 utilization system 52.

[0023] In the exemplary embodiment, heat exchange tube 70 extends though housing cavity 78, and is configured to channel a flow of heat exchange fluid 54 through housing cavity 78. Heat exchange tube 70 extends along a centerline axis 85 between a first end 86, and a second end 88. Heat exchange tube 70 is oriented within cavity 78 such that an outer surface 90 of heat exchange tube 70 contacts solid CO.sub.2 56 to facilitate transferring heat from heat exchange fluid 54 to solid CO.sub.2 56 to increase a temperature of solid CO.sub.2 56 and facilitate converting at least a portion of solid CO.sub.2 56 to liquid CO.sub.2 58.

[0024] Heat exchange assembly 12 also includes a plurality of fins 92 that extend outwardly from tube outer surface 90. Each fin 92 includes an outer surface 94 that is configured to contact solid CO.sub.2 56 to facilitate transferring heat from heat exchange fluid 54 to solid CO.sub.2 56 to facilitate forming liquid CO.sub.2 58 from solid CO.sub.2 56, and to cool heat exchange fluid 54 to recover a refrigeration value from solid CO.sub.2 56. Each fin 92 is oriented within cavity 78 such that solid CO.sub.2 56 is at least partially supported by heat exchange tube 70 within housing upper portion 80. Moreover, each fin 92 is oriented to channel liquid CO.sub.2 58 formed within cavity 78 from upper portion 80 to lower portion 82 such that liquid CO.sub.2 58 is collected within a pool 96 formed within lower portion 82. In the exemplary embodiment, each fin 92 is oriented substantially perpendicular to centerline axis 85. In addition, each fin 92 is at least partially submerged within liquid CO.sub.2 58 to facilitate transferring heat from liquid CO.sub.2 58 to heat exchange fluid 54. In one embodiment, heat exchange tube 70 includes a plurality of pipes 98 that are each coupled to one or more fins 92. Each pipe 98 is oriented within cavity 78, and extends between first end 86 and second end 88. One or more pipes 98 are at least partially submerged within liquid CO.sub.2 58 to facilitate transferring heat from liquid CO.sub.2 58 to heat exchange fluid 54.

[0025] During operation of system 10, combustor 22 receives a predefined quantity of fuel from fuel supply system 24, and receives a predefined quantity of air from air supply system 26. Combustor 22 injects the fuel into the air flow, ignites the fuel-air mixture to expand the fuel-air mixture through combustion, and generates high temperature flue gases. Combustor 22 channels flue gases 28 to HRSG 30 to facilitate generating steam from flue gases 28. In addition, boiler feedwater assembly 32 channels a flow of boiler feedwater 33 to HRSG 30. HRSG 30 transfers heat from flue gases 28 to boiler feedwater 33 to facilitate heating boiler feedwater 33 to generate steam 34. HRSG 30 discharges steam 34 towards steam turbine 36 wherein thermal energy in the steam is converted to mechanical rotational energy. HRSG 30 and/or combustor 22 discharge flue gases 28 toward gas treatment system 42 to facilitate treating carbon dioxide CO.sub.2 suspended within flue gases 28.

[0026] In the exemplary embodiment, HRSG 30 and/or combustor 22 channel flue gases to pre-cooling system 44. Pre-cooling system 44 transfers heat from flue gases 28 to heat exchange fluid 54 to reduce a temperature of flue gases 28. Pre-cooling system 44 discharges flue gases 28 towards cooling system 46 to facilitate generating solid CO.sub.2 from gaseous CO.sub.2 suspended within flue gases 28. In addition, pre-cooling system 44 channels heat exchange fluid 54 towards heat exchange assembly 12. Cooling system 46 cools flue gases 28 to generate solid CO.sub.2 and channels cooled flue gases 28 and solid CO.sub.2 56 to CO.sub.2 separator 48 to facilitate separating solid CO.sub.2 and N.sub.2 from flue gases 28. CO.sub.2 separator 48 discharges solid CO.sub.2 towards lockhopper assembly 62. In addition, CO.sub.2 separator 48 channels a flow of CO.sub.2 lean gas 100 that includes a mixture of CO.sub.2 and N.sub.2 to cooling system 46 and/or lockhopper assembly 62. In one embodiment, CO.sub.2 lean gas 100 discharged from CO.sub.2 separator 48 is divided into a first sub-stream 102 and a second sub-stream 104. First sub-stream 102 is discharged to atmosphere. Second sub-stream 104 is compressed in a compressor 106 and channeled to lockhopper assembly 62 at a predefined pressure to facilitate adjusting a pressure within lockhopper assembly 62.

[0027] Lockhopper assembly 62 channels solid CO.sub.2 56 towards heat exchanger 60 to transfer heat from solid CO.sub.2 56 to heat exchange fluid 54 being channeled through heat exchanger 60. Solid CO.sub.2 56 is gravity fed to heat exchanger 60 to transfer heat from heat exchange fluid 54 to solid CO.sub.2 56 to convert at least of portion of solid CO.sub.2 58 to liquid CO.sub.2 58, and to cool heat exchange fluid 54 to recover a refrigeration value from solid CO.sub.2 56. Heat exchanger 60 discharges liquid CO.sub.2 58 to CO.sub.2 utilization system 52. In addition, heat exchanger 60 channels heat exchange fluid 54 towards pre-cooling system 44 for use in cooling flue gases 28.

[0028] In the exemplary embodiment lockhopper assembly 62 and heat exchanger 60 each include an internal pressure equal to about 7 atm to facilitate preventing re-sublimation of solid CO.sub.2 56 to gaseous CO.sub.2 within cavity 78, and to maintain CO.sub.2 in solid-liquid phase equilibrium. Lockhopper assembly 62 channels solid CO.sub.2 56 having a temperature equal to about -102.degree. C. towards heat exchanger 60. Heat exchange fluid 54 is channeled into heat exchanger 60 includes a temperature equal to about -51.degree. C. As solid CO.sub.2 56 contacts of heat exchange tube 70, at least a portion of solid CO.sub.2 56 is converted to liquid CO.sub.2 58. Liquid CO.sub.2 58 discharged from heat exchanger 60 includes a fluid temperature equal to about -51.degree. C. Heat exchange fluid 54 discharged from heat exchanger 60 includes a fluid temperature equal to about -80.degree. C.

[0029] FIGS. 3-4 are schematic views of alternative embodiments of heat exchange assembly 12. Identical components shown in FIGS. 3-4 are labeled with the same reference numbers used in FIG. 2. In an alternative embodiment, heat exchange tube 70 extends between a first section 108 and a second section 110. First section 108 is oriented within lower portion 82 such that first section 108 is at least partially submerged within liquid CO.sub.2 58. Second section 110 is oriented within upper portion 80, and is configured to support solid CO.sub.2 56 such that solid CO.sub.2 56 is oriented above liquid CO.sub.2 pool 96. Fins 92 are coupled to heat exchange tube 70 and are oriented obliquely with respect to centerline axis 85 to facilitate channeling liquid CO.sub.2 58 from upper portion 80 to lower portion 82. One or more fins 92 are coupled to tube first section 108, and are at least partially submerged within liquid CO.sub.2 58.

[0030] Referring to FIG. 4, in another embodiment, each fin 92 is coupled to second section 110 of heat exchange tube 70 such that each fin 92 is oriented within upper portion 80. Each fin 92 is oriented with respect to an adjacent fin 92 such that a plurality of openings 112 are defined between adjacent fins 92. Each opening 112 is sized and shaped to channel liquid CO.sub.2 58 from upper portion 80 to lower portion 82.

[0031] FIG. 5 is another embodiment of power generation system 10. Identical components shown in FIG. 5 are labeled with the same reference numbers used in FIG. 1. In an alternative embodiment, heat exchanger 60 channels cold liquid CO.sub.2 58 to flue gas pre-cooling system 44 for use in pre-cooling flue gases 28. More specifically, liquid CO.sub.2 pump 84 channels liquid CO.sub.2 58 from heat exchanger 60 to flue gas pre-cooling system 44. In addition, flue gas pre-cooling system 44 channels liquid CO.sub.2 58 to CO.sub.2 utilization system 52. In one embodiment, liquid CO.sub.2 pump 84 is configured to channel liquid CO.sub.2 58 through flue gas pre-cooling system 44, and to CO.sub.2 utilization system 52.

[0032] FIG. 6 is an alternative embodiment of power generation system 10. Identical components shown in FIG. 6 are labeled with the same reference numbers used in FIG. 1. In an alternative embodiment, power generation system 10 includes a top cycle or gas turbine engine assembly 114 and a bottom cycle or steam turbine engine 20. Gas turbine engine assembly 114 includes a compressor 116, a combustor 118 downstream of compressor 116, and a turbine 120 downstream of combustor 118 and powered by gases discharged from combustor 118. Turbine 120 drives an electrical generator 122. In addition, turbine 120 discharges flue gases 28 to HRSG 30 for generating steam from flue gases 28.

[0033] In the exemplary embodiment, heat exchanger 60 is coupled downstream of pre-cooling system 44 for receiving a flow of flue gases 28 from pre-cooling system 44. During operation HRSG 30 and/or turbine 120 discharge flue gases 28 to pre-cooling system 44 to transfer heat from flue gases 28 to liquid CO.sub.2 58. Pre-cooling system 44 channels flue gases 28 to heat exchanger 60 to transfer heat from flue gases 28 to solid CO.sub.2 56 to form liquid CO.sub.2 58 from solid CO.sub.2 56 to facilitate cooling flue gases 28, and to recover a refrigeration value from solid CO.sub.2 56. Heat exchanger 60 channels cooled flue gases 28 to cooling system 46 to cool flue gases 28 to form solid CO.sub.2 from gaseous CO.sub.2 suspended within flue gases 28. Cooling system 46 channels solid CO.sub.2 and flue gases 28 to CO.sub.2 separator 48 to separate solid CO.sub.2 from flue gases 28, and discharge solid CO.sub.2 to lockhopper assembly 62. Lockhopper assembly 62 discharges solid CO.sub.2 56 to heat exchanger 60 to transfer heat from solid CO.sub.2 56 to flue gases 28 being channeled through heat exchanger 60, and to form liquid CO.sub.2 58 from solid CO.sub.2 56. Heat exchanger 60 channels liquid CO.sub.2 58 to pre-cooling system 44 to facilitate transferring heat from flue gases 28 to liquid CO.sub.2 58. In addition, pre-cooling system 44 channels liquid CO.sub.2 58 to CO.sub.2 utilization system 52.

[0034] FIG. 7 is a flow chart of an exemplary method 200 that may be used to treat CO.sub.2 that is generated during an operation of power generation system 10. In the exemplary embodiment, method 200 includes channeling 202 solid CO.sub.2 from lockhopper assembly 62 to heat exchange assembly 12, and channeling 204 a flow of heat exchange fluid 54 through heat exchange tube 70 to facilitate a transfer of heat from solid CO.sub.2 to heat exchange fluid 54 to form liquid CO.sub.2 from solid CO.sub.2, and to recover a refrigeration value from solid CO.sub.2 and liquid CO.sub.2. Method 200 also includes adjusting 206 a pressure within housing 68 to maintain a housing pressure within a predefined range of pressures to prevent re-sublimation of solid CO.sub.2 to gaseous CO.sub.2. Heat exchange fluid 54 is channeled 208 from heat exchange assembly 12 to pre-cooling system 44 to pre-cool flue gases 28. Liquid CO.sub.2 is channeled 210 from heat exchange assembly 12 to a CO.sub.2 utilization system 52 to facilitate utilization of rich CO.sub.2.

[0035] The above-described systems and methods overcome at least some disadvantages of known gas treatment systems by providing a gas treatment system that includes a heat exchange assembly configured to transfer heat from a heat exchange fluid to solid CO.sub.2 to facilitate recovering a refrigeration value from solid CO.sub.2. In addition, the gas treatment system includes a heat exchange assembly that is configured to maintain CO.sub.2 in solid-liquid phase equilibrium to enable the heat exchange assembly to transfer heat from solid CO.sub.2 to a heat exchange fluid to facilitate forming liquid CO.sub.2 for use in pre-cooling a flue gas. By providing a gas treatment system that includes a heat exchange assembly that recovers a refrigeration value from solid CO.sub.2, the cost of treating CO.sub.2 suspended within a flue gas is reduced as compared to known gas treatment systems.

[0036] Exemplary embodiments of systems and methods for treating carbon dioxide are described above in detail. The systems and methods are not limited to the specific embodiments described herein, but rather, components of systems and/or steps of the method may be utilized independently and separately from other components and/or steps described herein. For example, the systems and method may also be used in combination with other gas treatment systems and methods, and are not limited to practice with only the gas treatment system as described herein. Rather, the exemplary embodiment can be implemented and utilized in connection with many other gas treatment system applications.

[0037] Although specific features of various embodiments of the invention may be shown in some drawings and not in others, this is for convenience only. In accordance with the principles of the invention, any feature of a drawing may be referenced and/or claimed in combination with any feature of any other drawing.

[0038] This written description uses examples to disclose the invention, including the best mode, and also to enable any person skilled in the art to practice the invention, including making and using any devices or systems and performing any incorporated methods. The patentable scope of the invention is defined by the claims, and may include other examples that occur to those skilled in the art. Such other examples are intended to be within the scope of the claims if they have structural elements that do not differ from the literal language of the claims, or if they include equivalent structural elements with insubstantial differences from the literal language of the claims.

Claims

1. A gas treatment system for use in treating carbon dioxide (CO.sub.2) in a flue gas, said gas treatment system comprising: a cooling system coupled to a source of flue gas and configured to receive a flow of flue gas from the source, said cooling system configured to cool CO.sub.2 within the flue gas to form solid CO.sub.2; and a heat exchange assembly coupled to said cooling system for receiving a flow of solid CO.sub.2 from said cooling system, wherein said heat exchange assembly is configured to recover a refrigeration value from the solid CO.sub.2 and transfer at least a portion of the recovered refrigeration value to the flue gas, said heat exchange assembly comprising: a housing comprising an inlet, an outlet, and an inner surface that defines a cavity extending between said inlet and said outlet, said housing configured to receive solid CO.sub.2 through said inlet; and at least one heat exchange tube extending through said housing, said heat exchange tube oriented to contact solid CO.sub.2 to facilitate transferring of heat from solid CO.sub.2 to a heat exchange fluid being channeled through said heat exchange tube to facilitate converting at least a portion of solid CO.sub.2 into liquid CO.sub.2.

2. A gas treatment system in accordance with claim 1, wherein said housing is configured to maintain said cavity within a predefined range of pressures to prevent re-sublimation of solid CO.sub.2 to gaseous CO.sub.2.

3. A gas treatment system in accordance with claim 1, wherein said housing inner surface extends between an upper portion and a lower portion extending below said upper portion, said lower portion configured to contain liquid CO.sub.2 therein.

4. A gas treatment system in accordance with claim 3, wherein said at least one tube includes an outer surface and a plurality of fins extending outwardly from said tube outer surface, each fin of said plurality of fins is configured to support solid CO.sub.2 within said upper portion.stf

5. A gas treatment system in accordance with claim 4, wherein each fin of said plurality of fins is at least partially submerged within liquid CO.sub.2.

6. A gas treatment system in accordance with claim 4, wherein adjacent fins are oriented such that a plurality of openings are defined between adjacent fins, each opening is sized to channel liquid CO.sub.2 from said upper portion to said lower portion.

7. A gas treatment system in accordance with claim 1, further comprising a lockhopper assembly coupled between said cooling system and said heat exchange assembly for receiving solid CO.sub.2 from said cooling system, said lockhopper assembly configured to enable solid CO.sub.2 to be gravity fed into said housing cavity.

8. A gas treatment system in accordance with claim 1, further comprising a CO.sub.2 sequestration system coupled to said heat exchange assembly for receiving a flow of liquid CO.sub.2 from said heat exchange assembly.

9. A method of treating carbon dioxide (CO.sub.2), said method comprising: channeling a flue gas containing CO.sub.2 to a cooling system to cool the flue gas to form solid CO.sub.2; channeling the solid CO.sub.2 to a heat exchange assembly, wherein the heat exchange assembly includes a housing configured to receive solid CO.sub.2 therein, and at least one heat exchange tube extending through the housing; adjusting a pressure within the housing to maintain the housing pressure within a predefined range of pressures to prevent re-sublimation of solid CO.sub.2; channeling a flow of heat exchange fluid through the at least one heat exchange tube to facilitate a transfer of heat from solid CO.sub.2 to the heat exchange fluid to convert at least a portion of solid CO.sub.2 into liquid CO.sub.2 and to recover a refrigeration value from the CO.sub.2; and transferring at least a portion of the recovered refrigeration value to the flue gas to facilitate cooling the flue gas.

10. A method in accordance with claim 9, further comprising channeling the heat exchange fluid to a pre-cooling system to facilitate transferring the recovered refrigeration value to the flue gas to facilitate cooling the flue gas.

11. A method in accordance with claim 9, further comprising channeling solid CO.sub.2 from a lockhopper assembly to the heat exchange assembly, wherein the lockhopper assembly is configured to enable solid CO.sub.2 to be gravity fed into the housing cavity.

12. A method in accordance with claim 9, further comprising channeling liquid CO.sub.2 from the heat exchange assembly to a CO.sub.2 sequestration system.