USRE46682E1 - System and method for separating high molecular weight gases from a combustion source - Google Patents

System and method for separating high molecular weight gases from a combustion source Download PDF

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USRE46682E1
USRE46682E1 US15/016,678 US201615016678A USRE46682E US RE46682 E1 USRE46682 E1 US RE46682E1 US 201615016678 A US201615016678 A US 201615016678A US RE46682 E USRE46682 E US RE46682E
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exhaust stack
exhaust
stack
molecular weight
high molecular
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US15/016,678
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Jerry Lang
David Scott
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Gas Separation Technologies Inc
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Gas Separation Technologies Inc
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    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
    • C01D7/00—Carbonates of sodium, potassium or alkali metals in general
    • C01D7/07—Preparation from the hydroxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/24—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by centrifugal force
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/62—Carbon oxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/30—Alkali metal compounds
    • B01D2251/304—Alkali metal compounds of sodium
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/50—Carbon oxides
    • B01D2257/504—Carbon dioxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • Y02C10/04—
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
    • Y02P20/152—

Definitions

  • the present invention relates generally to the field of separation and sequestration of combustion exhaust gases.
  • Combustion systems have come under increased scrutiny for toxic emissions which are a by-product of the combustion process. Depending upon the extent of the combustion, carbon monoxide and NO X may be emitted at unacceptable levels. Carbon monoxide levels are normally controlled through complete combustion resulting in carbon dioxide. In fact, in years past, carbon dioxide was measured to determine the efficiency of the process. Traditionally, NO X and other VOC emissions have been either controlled by cleaner fuels or techniques that reduce formation. Recently, because of the push for alternative and renewable fuels, carbon dioxide being the only component here-to-fore not regulated has come under increased scrutiny (green house gases, carbon footprints and global warming).
  • CO 2 comprises from 10 to 15% of the exhaust or flue gas by volume, it is impractical to treat it without separating it from the remaining gases.
  • Several systems have been developed to reduce the CO 2 , and in some cases to concentrate the gas. Increasing the amount of hydrogen in the fuel will reduce the fraction of CO 2 in the flue gas, since hydrogen combustion does not produce CO 2 . If the exhaust or flue gas is recirculated and the incoming fuel is mixed with pure O 2 the nitrogen in the air is eliminated. And, with enough recycling of the exhaust or flue gas, the CO 2 is concentrated to higher levels. After concentration, there are accepted methods of either using or treating the CO 2 . The burning of the hydrogen simply reduces the CO 2 . These known methods are quite inflexible and require reconfiguring the combustion equipment. In many cases, very flexible control algorithms will need to be employed to adjust the various fuel-air curves needed for the ever changing fuel compositions. The production or purchase of the hydrogen or oxygen needed in these processes also tend to make them impractical.
  • the present invention provides a system and method for separating high molecular weight gases, such as CO 2 , from any combustion source. More specifically, the present invention imparts centrifugal force on the exhaust or flue gas by spinning the exhaust or flue gas with enough velocity to remove the heavy components, such as CO 2 , to the outside diameter of the stack and removing it thru an annular space or gap formed by an interior vent.
  • the spin needed for the centrifugal action may be imparted by using a blower to remove the gas tangentially from one side of the stack and blowing it tangentially back into the stack on the other side.
  • the use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower.
  • the velocity of the system may be varied to accommodate various fuels and flue gas mixtures.
  • the system may be fitted to stacks of virtually any size or flow.
  • the present invention provides a simple process to take care of the hardest and most expensive step in controlling CO 2 . Many treatment options are available after separation.
  • One embodiment of the present invention provides a method for separating high molecular weight gases from an exhaust gas of a combustion source by providing (a) a blower attached to an intake of an exhaust stack to receive the exhaust gas from the combustion source, (b) an interior vent within the exhaust stack comprising (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall, and (c) a transfer pipe connected to the at least one opening in the interior surface of the exhaust stack.
  • a tangential flow of the exhaust gas is created within the exhaust stack using the blower, wherein the blower imparts sufficient centrifugal force on the exhaust gas to concentrate substantially all of the high molecular weight gases along the inner surface of the exhaust stack.
  • the high molecular weight gases concentrated along the inner surface of the exhaust stack are collected using the interior vent.
  • the high molecular weight gases are removed from the interior vent using the transfer pipe.
  • the present invention provides a system for separating high molecular weight gases in an exhaust stack from an exhaust gas of a combustion source using a blower, an interior vent and a transfer pipe.
  • the blower is attached to an intake of the exhaust stack to receive the exhaust gas from the combustion source and create a tangential flow of the exhaust gas within the exhaust stack.
  • the blower imparts sufficient centrifugal force on the exhaust gas to concentrate the high molecular weight gases along the inner surface of the exhaust stack.
  • the interior vent is disposed within the exhaust stack and collects the high molecular weight gases concentrated along the inner surface of the exhaust stack.
  • the interior vent includes (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall.
  • the transfer pipe is connected to the at least one opening in the interior surface of the exhaust stack to remove the high molecular weight gases from the interior vent.
  • the present invention provides a system for separating high molecular weight gases from an exhaust gas of a combustion source using an exhaust stack, a blower, an interior vent and a transfer pipe.
  • the blower is attached to an intake of the exhaust stack to receive the exhaust gas from the combustion source and create a tangential flow of the exhaust gas within the exhaust stack.
  • the blower imparts sufficient centrifugal force on the exhaust gas to concentrate the high molecular weight gases along the inner surface of the exhaust stack.
  • the interior vent is disposed within the exhaust stack and collects the high molecular weight gases concentrated along the inner surface of the exhaust stack.
  • the interior vent includes (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall.
  • the transfer pipe is connected to the at least one opening in the interior surface of the exhaust stack to remove the high molecular weight gases from the interior vent.
  • the high molecular weight gases have a molecular weight greater than 35 and at least 85% of the high molecular weight gases are concentrated along the inner surface of the exhaust stack.
  • the annular space or gap has an area of approximately 10% of a cross-sectional area of the exhaust stack.
  • the at least one opening is positioned at a height above the bottom of the exhaust stack approximately equal to three diameters of the exhaust stack.
  • the blower causes the exhaust gases to spin around the exhaust stack at least five times within a height approximately equal to one diameter of the exhaust stack.
  • FIGS. 1A, 1B and 1C are a cross sectional side view ( FIG. 1A ), a cross-sectional top view at cross section E-E ( FIG. 1B ), and a cross-sectional bottom view at cross section F-F ( FIG. 1C ) of a system for separating high molecular weight (HMW) gases in an exhaust stack in accordance with one embodiment of the present invention;
  • FIGS. 2A, 2B and 2C are a cross sectional side view ( FIG. 2A ), a cross-sectional top view at cross section E-E ( FIG. 2B ), and a cross-sectional bottom view at cross section F-F ( FIG. 2C ) of a system for separating high molecular weight (HMW) gases in an exhaust stack in accordance with another embodiment of the present invention;
  • HMW high molecular weight
  • FIGS. 3A, 3B and 3C are a cross sectional side view ( FIG. 3A ), a cross-sectional top view at cross section E-E ( FIG. 3B ), and a cross-sectional bottom view at cross section F-F ( FIG. 3C ) of a system for separating high molecular weight (HMW) gases in an exhaust stack in accordance with one embodiment of the present invention;
  • FIG. 4 is a flow chart of a method for separating high molecular weight (HMW) gases from an exhaust gas in accordance with one embodiment of the present invention.
  • FIG. 5 is a block diagram of a system incorporating the embodiments of the present invention.
  • the present invention provides a system and method for separating high molecular weight gases, such as CO 2 , from any combustion source. More specifically, the present invention imparts centrifugal force on the exhaust or flue gas by spinning the exhaust or flue gas with enough velocity to remove the heavy components, such as CO 2 , to the outside diameter of the stack and removing it thru an annular space or gap formed by an interior vent.
  • the spin needed for the centrifugal action may be imparted by using a blower to remove the gas tangentially from one side of the stack and blowing it tangentially back into the stack on the other side.
  • the use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower.
  • the velocity of the system may be varied to accommodate various fuels and flue gas mixtures.
  • the system may be fitted to stacks of virtually any size or flow.
  • the present invention provides a simple process to take care of the hardest and most expensive step in controlling CO 2 . Many treatment options are available after separation.
  • the typical constituent parts of exhaust or flue gas are as follows: the molecular weight of CO 2 is 44 and it comprises 10-15% of flue gases, the molecular weight of N 2 is 28 and it comprises approximately 78% of flue gases, the molecular weight of O 2 is 32 and it comprises approximately 3% of flue gases, the molecular weight of H 2 O is 18 and it comprises approximately 10-15% of flue gases, and the molecular weight of CO is 28 and it is normally a negligible percentage of the flue gas.
  • These numbers indicate the CO 2 will need to be basically separated from the N 2 with a differential molecular weight of 16. After the CO 2 is separated from the flue gases, it can be compressed, injected into the ground, or used for other processes.
  • the CO 2 is collected in a tank and then flowed up thru bubble trays containing sodium hydroxide which will cause the CO 2 to combine and produce sodium carbonate which can be collected for use otherwise.
  • This embodiment is particularly useful in refineries and chemical plants where sodium hydroxide is commonly used in their processes (sometimes called “caustic soda”). After the sodium hydroxide is used, the plants use acid to reduce the used sodium hydroxide to a neutral PH so it can be disposed of. Using this byproduct does not require the purchase of gases and eliminates a disposal problem.
  • FIGS. 1A, 1B and 1C a cross sectional side view ( FIG. 1A ), a cross-sectional top view at cross section E-E ( FIG. 1B ), and a cross-sectional bottom view at cross section F-F ( FIG. 1C ) of a system 100 for separating high molecular weight (HMW) gases 112 in an exhaust stack 102 from an exhaust gas 104 of a combustion source in accordance with one embodiment of the present invention are shown.
  • a blower 106 is attached to an intake 108 of the exhaust stack 102 to receive the exhaust gas 104 from the combustion source ( 502 , FIG. 5 ) and create a tangential flow 110 of the exhaust gas 104 within the exhaust stack 102 .
  • the blower 106 imparts sufficient centrifugal force on the exhaust gas 104 to concentrate the high molecular weight gases 112 , such as CO 2 or other gases having a higher molecular weight than N 2 or O 2 (e.g., greater than 35), along the inner perimeter or surface 114 of the exhaust stack 102 .
  • “along the inner perimeter or surface of the exhaust stack” means an area within the exhaust stack 102 that is much closer to the inner surface 114 of the exhaust stack 102 than to the center of the exhaust stack 102 .
  • the high molecular weight gases 112 are concentrated near, towards or proximate to the inner surface 114 of the exhaust stack 102 .
  • the low molecular weight gases 130 exit through the top of the exhaust stack 102 .
  • the blower 106 causes the exhaust gases 104 to spin around the interior of the exhaust stack 102 at least five times within a height approximately equal to one diameter (D) of the exhaust stack 102 .
  • the blower 106 is external to the exhaust stack 102 and is connected to the intake 108 of the exhaust stack 102 with a first pipe 116 .
  • a second pipe 118 connects the blower 106 to the bottom of the exhaust stack 102 at a point 120 approximately opposite to the intake 108 and in line with the tangential flow 110 in order to create the sufficient centrifugal force on the exhaust gas 104 .
  • the use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower 106 .
  • the interior vent 122 within the exhaust stack 102 collects the high molecular weight gases 112 concentrated along the inner surface 114 of the exhaust stack 102 .
  • the interior vent 122 includes: (i) a vent wall 122ab having a top portion 122 a attached to the interior surface 114 of the exhaust stack 102 along the entire inner perimeter of the exhaust stack 102 (e.g., the top portion 122 a is attached to the inner surface 114 along any side cross section of the exhaust stack 102 ) and a lower portion 122 b that extends downward into the exhaust stack 102 to form an annular space or gap 124 between the vent wall 122 lower portion 122b and the interior surface 114 of the exhaust stack 102 ; and (ii) at least one opening 122 c in the interior surface 114 of the exhaust stack 102 between the top 122 a and bottom lower 122 b portions of the vent wall 122 122ab.
  • a transfer pipe 128 is connected to the at least one opening 122 c in the interior surface 114 of the exhaust stack 102 to remove the high molecular weight gases 112 from the interior vent 122 .
  • the at least one or more openings 122 c can be holes, slots, or any other geometrically shaped passageway. Moreover, more than one transfer pipe 128 can be used.
  • the lower portion 122 b of the vent wall 122 122ab can be substantially parallel to the interior surface 114 of the exhaust stack 102 , curved or angled with respect to the interior surface 114 of the exhaust stack 102 . Note that the top portion 122 a of the interior vent 122 does not have to be aligned with a horizontal plane of the exhaust stack 102 .
  • the top portion 122 a can be angled from the horizontal plane in accordance with the tangential flow 110 (top portion 122 a on the opposite side of the exhaust stack 102 from the opening 122 c positioned lower than the top portion 122 a adjacent to the opening 122 c).
  • the top portion 122 a can form one or more spirals down from the one or more openings 122 c.
  • an optional baffle or guide 122 d proximate to the at least one opening 122 c can be used to direct the flow of the high molecular weight gases 112 from the interior vent 122 into the transfer pipe 128 .
  • the baffle or guide 122 d can be straight, angled, curved or any other shape and orientation to more efficiently guide the high molecular weight gasses gases 112 into the transfer pipe 128 .
  • the dimensions (A, B, C, D) of the vent wall 122 122ab will vary in accordance with the design specifications for the system 100 .
  • the design specification may take into account one or more parameters, such as temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture.
  • the system 100 dimensions should be configured to concentrate and capture at least 85% of the high molecular weight gases.
  • the at least one opening 122 c is positioned at a height (A) such that the high molecular weight gases 112 have spun around the exhaust stack 102 approximately fifteen to twenty times or more.
  • the at least one opening 122 c is positioned at a height (A) above the bottom of the exhaust stack 102 approximately equal to three diameters (3 ⁇ D) of the exhaust stack 102
  • the annular space or gap 124 has an area (B) of approximately 10% of a cross-sectional area of the exhaust stack 102
  • the bottom lower portion 122 a 122b of the vent wall 122 122ab extends down a distance (C) approximately equal to one half diameter (0.5 ⁇ D) of the exhaust stack 102 .
  • the system 100 may also include other components, such as a tank ( 504 , FIG. 5 ) connected to the transfer pipe 128 to store the removed high molecular weight gases 112 , a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 ( 506 , FIG. 5 ), a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the annular space or gap 124 based on one or more parameters (e.g., temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture, etc.), and/or one or more sensors (not shown) attached to the blower 106 , exhaust stack 102 , interior vent 122 or transfer pipe 128 .
  • a tank 504 , FIG. 5
  • a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 ( 506 , FIG. 5 )
  • a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the
  • a controller can be communicably coupled to the motor (not shown) and the one or more sensors to adjust the size (B) of the annular space or gap 124 using the motor based on one or more parameters detected by the one or more sensors.
  • one or more bubble trays ( 508 , FIG. 5 ) containing sodium hydroxide can be attached to the transfer pipe 128 or tank such that the removed CO 2 is combined with the sodium hydroxide to produce sodium carbonate.
  • FIGS. 2A, 2B and 2C a cross-sectional side view ( FIG. 2A ), a cross-sectional top view at cross section E-E ( FIG. 2B ) and a cross-sectional bottom view at cross section F-F ( FIG. 2C ) of the system 200 for separating high molecular weight (HMW) gases 112 in an exhaust stack 102 from an exhaust gas 104 of a combustion source in accordance with one embodiment of the present invention are shown.
  • a blower 106 is attached to an intake 108 of the exhaust stack 102 to receive the exhaust gas 104 from the combustion source ( 502 , FIG. 5 ) and create a tangential flow 110 of the exhaust gas 104 within the exhaust stack 102 .
  • the blower 106 imparts sufficient centrifugal force on the exhaust gas 104 to concentrate the high molecular weight gases 112 , such as CO 2 or other gases having a higher molecular weight greater than N 2 or O 2 (e.g., greater than 35), along the inner perimeter or surface 114 of the exhaust stack 102 .
  • the blower 106 causes the exhaust gases 104 to spin around the interior of the exhaust stack 102 at least five times within a height approximately equal to one diameter (D) of the exhaust stack 102 .
  • the blower 106 is external to the exhaust stack 102 and is connected to the intake 108 of the exhaust stack 102 with a first pipe 116 .
  • a second pipe 118 connects the blower 106 to the bottom of the exhaust stack 102 at a point 120 approximately opposite to the intake 108 and in line with the tangential flow 110 in order to create the sufficient centrifugal force on the exhaust gas 104 .
  • the use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower 106 .
  • the interior vent 122 within the exhaust stack 102 collects the high molecular weight gases 112 concentrated along the inner surface 114 of the exhaust stack 102 .
  • the interior vent 122 includes: (i) a vent wall 122ab having a top portion 122 a attached to the interior surface 114 of the exhaust stack 102 along the entire inner perimeter of the exhaust stack 102 (e.g., the top portion 122 a is attached to the inner surface 114 along any side cross section of the exhaust stack 102 ) and a lower portion 122 b that extends downward into the exhaust stack 102 to form an annular space or gap 124 between the vent wall 122 122ab and the interior surface 114 of the exhaust stack 102 ; (ii) at least one opening 122 c in the interior surface 114 of the exhaust stack 102 between the top 122 a and bottom lower 122 b portions of the vent wall 122 122ab; and (iii) a bustle 202 attached to or integrated into the exhaust stack 102 between the at least one
  • the transfer pipe 128 is connected to bustle 202 to remove the high molecular weight gases 112 from the interior vent 122 122ab.
  • the at least one or more openings 122 c can be holes, slots, or any other geometrically shaped passageway. Moreover, more than one transfer pipe 128 can be used.
  • the lower portion 122 b of the vent wall 122 122ab can be substantially parallel to the interior surface 114 of the exhaust stack 102 , curved or angled with respect to the interior surface 114 of the exhaust stack 102 . Note that the top portion 122 a of the interior vent 122 122ab does not have to be aligned with a horizontal plane of the exhaust stack 102 .
  • the top portion 122 a can be angled from the horizontal plane in accordance with the tangential flow 110 (top portion 122 a on the opposite side of the exhaust stack 102 from the opening 122 c positioned lower than the top portion 122 a adjacent to the opening 122 c).
  • the top portion 122 a can form one or more spirals down from the one or more openings 122 c.
  • an optional baffle or guide 122 d proximate to the at least one opening 122 c can be used to direct the flow of the high molecular weight gases 112 from the interior vent 122 into the transfer pipe 128 .
  • the baffle or guide 122 d can be straight, angled, curved or any other shape and orientation to more efficiently guide the high molecular weight gases 112 into the transfer pipe 128 .
  • the dimensions (A, B, C, D) of the vent wall 122 122ab will vary in accordance with the design specifications for the system 200 .
  • the design specification may take into account one or more parameters, such as temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture.
  • the system 200 dimensions should be configured to concentrate and capture at least 85% of the high molecular weight gases.
  • the at least one opening 122 c is positioned at a height (A) such that the high molecular weight gases 112 have spun around the exhaust stack 102 approximately fifteen to twenty times or more.
  • the at least one opening 122 c is positioned at a height (A) above the bottom of the exhaust stack 102 approximately equal to three diameters (3 ⁇ D) of the exhaust stack 102
  • the annular space or gap 124 has an area (B) of approximately 10% of a cross-sectional area of the exhaust stack 102
  • the bottom lower portion 122 a 122b of the vent wall 122 122ab extends down a distance (C) approximately equal to one half diameter (0.5 ⁇ D) of the exhaust stack 102 .
  • the system 100 may also include other components, such as a tank ( 504 , FIG. 5 ) connected to the transfer pipe 128 to store the removed high molecular weight gases 112 , a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 ( 506 , FIG. 5 ), a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the annular space or gap 124 based on one or more parameters (e.g., temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture, etc.), and/or one or more sensors (not shown) attached to the blower 106 , exhaust stack 102 , interior vent 122 or transfer pipe 128 .
  • a tank 504 , FIG. 5
  • a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 ( 506 , FIG. 5 )
  • a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the
  • a controller (not shown) can be communicably coupled to the motor and the one or more sensors to adjust the size (B) of the annular space or gap 124 using the motor based on one or more parameters detected by the one or more sensors.
  • one or more bubble trays ( 508 , FIG. 5 ) containing sodium hydroxide can be attached to the transfer pipe 128 or tank such that the removed CO 2 is combined with the sodium hydroxide to produce sodium carbonate.
  • FIGS. 3A, 3B and 3C a cross sectional side view ( FIG. 3A )), a cross-sectional top view at cross section E-E ( FIG. 3B ) and a cross-sectional bottom view at cross section F-F ( FIG. 3C ) of the system 300 for separating high molecular weight (HMW) gases in an exhaust stack 102 from an exhaust gas 104 of a combustion source in accordance with one embodiment of the present invention are shown.
  • a blower 106 is attached to an intake 108 of the exhaust stack 102 to receive the exhaust gas 104 from the combustion source ( 502 , FIG. 5 ) and create a tangential flow 110 of the exhaust gas 104 within the exhaust stack 102 .
  • the blower 106 imparts sufficient centrifugal force on the exhaust gas 104 to concentrate the high molecular weight gases 112 , such as CO 2 or other gases having a higher molecular weight greater than N 2 or O 2 (e.g., greater than 35), along the inner perimeter or surface 114 of the exhaust stack 102 .
  • the blower 106 causes the exhaust gases 104 to spin around the interior of the exhaust stack 102 at least five times within a height approximately equal to one diameter (D) of the exhaust stack 102 .
  • the blower 106 is internal to the exhaust stack 102 .
  • a second pipe 118 or channel connects the blower 106 to the bottom of the exhaust stack 102 at a point 120 approximately opposite to the intake 108 and in line with the tangential flow 110 in order to create the sufficient centrifugal force on the exhaust gas 104 .
  • the use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower 106 .
  • the interior vent 122 within the exhaust stack 102 collects the high molecular weight gases 112 concentrated along the inner surface 114 of the exhaust stack 102 .
  • the interior vent 122 includes: (i) a vent wall 122ab having a top portion 122 a attached to the interior surface 114 of the exhaust stack 102 along the entire inner perimeter of the exhaust stack 102 (e.g., the top portion 122 a is attached to the inner surface 114 along any side cross section of the exhaust stack 102 ) and a lower portion 122 b that extends downward into the exhaust stack 102 to form an annular space or gap 124 between the vent wall 122 122ab and the interior surface 114 of the exhaust stack 102 ; (ii) at least one opening 122 c in the interior surface 114 of the exhaust stack 102 between the top 122 a and bottom lower 122 b portions of the vent wall 122 122ab; and (iii) a bustle 202 attached to or integrated into the exhaust stack 102 between the at least one
  • the transfer pipe 128 is connected to bustle 202 to remove the high molecular weight gases 112 from the interior vent 122 .
  • the at least one or more openings 122 c can be holes, slots, or any other geometrically shaped passageway. Moreover, more than one transfer pipe 128 can be used.
  • the lower portion 122 b of the vent wall 122 122ab can be substantially parallel to the interior surface 114 of the exhaust stack 102 , curved or angled with respect to the interior surface 114 of the exhaust stack 102 . Note that the top portion 122 a of the interior vent 122 does not have to be aligned with a horizontal plane of the exhaust stack 102 .
  • the top portion 122 a can be angled from the horizontal plane in accordance with the tangential flow 110 (top portion 122 a on the opposite side of the exhaust stack 102 from the opening 122 c positioned lower than the top portion 122 a adjacent to the opening 122 c).
  • the top portion 122 a can form one or more spirals down from the one or more openings 122 c.
  • an optional baffle or guide 122 d proximate to the at least one opening 122 c can be used to direct the flow of the high molecular weight gases 112 from the interior vent 122 into the transfer pipe 128 .
  • the baffle or guide 122 d can be straight, angled, curved or any other shape and orientation to more efficiently guide the high molecular weight gases 112 into the transfer pipe 128 ).
  • the dimensions (A, B, C, D) of the vent wall 122 122ab will vary in accordance with the design specifications for the system 300 .
  • the design specification may take into account one or more parameters, such as temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture.
  • the system 300 dimensions should be configured to concentrate and capture at least 85% of the high molecular weight gases.
  • the at least one opening 122 c is positioned at a height (A) such that the high molecular weight gases 112 have spun around the exhaust stack 102 approximately fifteen to twenty times or more.
  • the at least one opening 122 c is positioned at a height (A) above the bottom of the exhaust stack 102 approximately equal to three diameters (3 ⁇ D) of the exhaust stack 102
  • the annular space or gap 124 has an area (B) of approximately 10% of a cross-sectional area of the exhaust stack 102
  • the bottom lower portion 122 a 122b of the vent wall 122 122ab extends down a distance (C) approximately equal to one half diameter (0.5 ⁇ D) of the exhaust stack 102 .
  • the system 100 may also include other components, such as a tank ( 504 , FIG. 5 ) connected to the transfer pipe 128 to store the removed high molecular weight gases 112 , a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 ( 506 , FIG. 5 ), a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the annular space or gap 124 based on one or more parameters (e.g., temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture, etc.), and/or one or more sensors (not shown) attached to the blower 106 , exhaust stack 102 , interior vent 122 or transfer pipe 128 .
  • a tank 504 , FIG. 5
  • a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 ( 506 , FIG. 5 )
  • a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the
  • a controller (not shown) can be communicably coupled to the motor and the one or more sensors to adjust the size (B) of the annular space or gap 124 using the motor based on one or more parameters detected by the one or more sensors.
  • one or more bubble trays ( 508 , FIG. 5 ) containing sodium hydroxide can be attached to the transfer pipe 128 or tank such that the removed CO 2 is combined with the sodium hydroxide to produce sodium carbonate.
  • FIG. 4 a flow chart of a method 400 for separating high molecular weight gases in an exhaust stack from an exhaust gas of a combustion source in accordance with one embodiment of the present invention is shown.
  • the following components are provided in block 402 to perform the method 400 : (a) a blower attached to an intake of an exhaust stack to receive the exhaust gas from the combustion source, (b) an interior vent within the exhaust stack comprising (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall, and (c) a transfer pipe connected to the at least one opening in the interior surface of the exhaust stack.
  • a tangential flow of the exhaust gas within the exhaust stack is created using the blower in block 404 .
  • the blower imparts sufficient centrifugal force on the exhaust gas to concentrate substantially all of the high molecular weight gases along the inner surface of the exhaust stack.
  • the high molecular weight gases concentrated along the inner surface of the exhaust stack are collected using the interior vent in block 406 .
  • the high molecular weight gases are removed from the interior vent using the transfer pipe in block 408 .
  • Additional steps may include storing the removed high molecular weight gases in a tank ( 504 , FIG. 5 ) connected to the transfer pipe, compressing the removed high molecular weight gases ( 506 , FIG. 5 ), injecting the removed high molecular weight gases into a below-ground storage, or flowing the removed CO 2 up through one or more bubble trays containing sodium hydroxide which causes the removed CO 2 to combine with the sodium hydroxide to produce sodium carbonate ( 508 , FIG. 5 ).
  • FIG. 5 a block diagram of a system 500 incorporating the embodiments of the present invention is shown.
  • the combustion source 502 creates exhaust 104 , which is transported to the exhaust stack 102 (not specifically illustrated in FIG. 5) of system 100 , 200 or 300 .
  • Low molecular gas 130 exits the exhaust stack 100 , 200 or 300 .
  • the high molecular weight gas 112 is collected and removed from the exhaust stack 100 , 200 or 300 for further processing (e.g., storage in a tank 504 , compression followed by storage 506 , bubble trays to produce sodium carbonate 508 , etc.).
  • the high molecular weight gas 112 can be used in other ways as will be appreciated and known by those skilled in the art.
  • the various illustrative logical blocks, modules, circuits, and algorithm steps described herein may be implemented as electronic hardware, computer software, or combinations of both, depending on the application and functionality.
  • the various logical blocks, modules, and circuits described herein may be implemented or performed with a general purpose processor (e.g., microprocessor, conventional processor, controller, microcontroller, state machine or combination of computing devices), a digital signal processor (“DSP”), an application specific integrated circuit (“ASIC”), a field programmable gate array (“FPGA”) or other programmable logic device, discrete gate or transistor logic, discrete hardware components, or any combination thereof designed to perform the functions described herein.
  • a general purpose processor e.g., microprocessor, conventional processor, controller, microcontroller, state machine or combination of computing devices
  • DSP digital signal processor
  • ASIC application specific integrated circuit
  • FPGA field programmable gate array
  • steps of a method or process described herein may be embodied directly in hardware, in a software module executed by a processor, or in a combination of the two.
  • a software module may reside in RAM memory, flash memory, ROM memory, EPROM memory, EEPROM memory, registers, hard disk, a removable disk, a CD-ROM, or any other form of storage medium known in the art.

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Abstract

High molecular weight (HMW) gases are separated from an exhaust gas of a combustion source using a blower and an interior vent within the exhaust stack. The interior vent includes a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall. The blower creates a tangential flow of the exhaust gas with sufficient centrifugal force to concentrate substantially all of the HMW gases along the inner surface of the exhaust stack. A transfer pipe removes the HMW gases from the interior vent.

Description

CROSS-REFERENCE TO RELATED APPLICATIONS
This application claims priority to U.S. Provisional Application Ser. No. 61/420,751, filed Dec. 7, 2010, the entire contents of which are incorporated herein by reference.
FIELD OF THE INVENTION
The present invention relates generally to the field of separation and sequestration of combustion exhaust gases.
BACKGROUND OF THE INVENTION
Combustion systems have come under increased scrutiny for toxic emissions which are a by-product of the combustion process. Depending upon the extent of the combustion, carbon monoxide and NOX may be emitted at unacceptable levels. Carbon monoxide levels are normally controlled through complete combustion resulting in carbon dioxide. In fact, in years past, carbon dioxide was measured to determine the efficiency of the process. Traditionally, NOX and other VOC emissions have been either controlled by cleaner fuels or techniques that reduce formation. Recently, because of the push for alternative and renewable fuels, carbon dioxide being the only component here-to-fore not regulated has come under increased scrutiny (green house gases, carbon footprints and global warming).
The problem is, burning fossil fuels makes carbon dioxide, and burning fossil fuels more efficiently makes even more carbon dioxide. NOX and SOX along with other pollutants, which comprise only parts per million in the resulting emissions, are controlled by many effective methods; but there few effective methods of controlling CO2 emissions.
Since CO2 comprises from 10 to 15% of the exhaust or flue gas by volume, it is impractical to treat it without separating it from the remaining gases. Several systems have been developed to reduce the CO2, and in some cases to concentrate the gas. Increasing the amount of hydrogen in the fuel will reduce the fraction of CO2 in the flue gas, since hydrogen combustion does not produce CO2. If the exhaust or flue gas is recirculated and the incoming fuel is mixed with pure O2 the nitrogen in the air is eliminated. And, with enough recycling of the exhaust or flue gas, the CO2 is concentrated to higher levels. After concentration, there are accepted methods of either using or treating the CO2. The burning of the hydrogen simply reduces the CO2. These known methods are quite inflexible and require reconfiguring the combustion equipment. In many cases, very flexible control algorithms will need to be employed to adjust the various fuel-air curves needed for the ever changing fuel compositions. The production or purchase of the hydrogen or oxygen needed in these processes also tend to make them impractical.
SUMMARY OF THE INVENTION
The present invention provides a system and method for separating high molecular weight gases, such as CO2, from any combustion source. More specifically, the present invention imparts centrifugal force on the exhaust or flue gas by spinning the exhaust or flue gas with enough velocity to remove the heavy components, such as CO2, to the outside diameter of the stack and removing it thru an annular space or gap formed by an interior vent. The spin needed for the centrifugal action may be imparted by using a blower to remove the gas tangentially from one side of the stack and blowing it tangentially back into the stack on the other side. The use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower. Note that the velocity of the system may be varied to accommodate various fuels and flue gas mixtures. Moreover, the system may be fitted to stacks of virtually any size or flow. As a result, the present invention provides a simple process to take care of the hardest and most expensive step in controlling CO2. Many treatment options are available after separation.
One embodiment of the present invention provides a method for separating high molecular weight gases from an exhaust gas of a combustion source by providing (a) a blower attached to an intake of an exhaust stack to receive the exhaust gas from the combustion source, (b) an interior vent within the exhaust stack comprising (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall, and (c) a transfer pipe connected to the at least one opening in the interior surface of the exhaust stack. A tangential flow of the exhaust gas is created within the exhaust stack using the blower, wherein the blower imparts sufficient centrifugal force on the exhaust gas to concentrate substantially all of the high molecular weight gases along the inner surface of the exhaust stack. The high molecular weight gases concentrated along the inner surface of the exhaust stack are collected using the interior vent. The high molecular weight gases are removed from the interior vent using the transfer pipe.
In addition, the present invention provides a system for separating high molecular weight gases in an exhaust stack from an exhaust gas of a combustion source using a blower, an interior vent and a transfer pipe. The blower is attached to an intake of the exhaust stack to receive the exhaust gas from the combustion source and create a tangential flow of the exhaust gas within the exhaust stack. The blower imparts sufficient centrifugal force on the exhaust gas to concentrate the high molecular weight gases along the inner surface of the exhaust stack. The interior vent is disposed within the exhaust stack and collects the high molecular weight gases concentrated along the inner surface of the exhaust stack. The interior vent includes (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall. The transfer pipe is connected to the at least one opening in the interior surface of the exhaust stack to remove the high molecular weight gases from the interior vent.
Moreover, the present invention provides a system for separating high molecular weight gases from an exhaust gas of a combustion source using an exhaust stack, a blower, an interior vent and a transfer pipe. The blower is attached to an intake of the exhaust stack to receive the exhaust gas from the combustion source and create a tangential flow of the exhaust gas within the exhaust stack. The blower imparts sufficient centrifugal force on the exhaust gas to concentrate the high molecular weight gases along the inner surface of the exhaust stack. The interior vent is disposed within the exhaust stack and collects the high molecular weight gases concentrated along the inner surface of the exhaust stack. The interior vent includes (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall. The transfer pipe is connected to the at least one opening in the interior surface of the exhaust stack to remove the high molecular weight gases from the interior vent. The high molecular weight gases have a molecular weight greater than 35 and at least 85% of the high molecular weight gases are concentrated along the inner surface of the exhaust stack. The annular space or gap has an area of approximately 10% of a cross-sectional area of the exhaust stack. The at least one opening is positioned at a height above the bottom of the exhaust stack approximately equal to three diameters of the exhaust stack. The blower causes the exhaust gases to spin around the exhaust stack at least five times within a height approximately equal to one diameter of the exhaust stack.
The present invention is described in detail below with reference to the accompanying drawings which are not to scale.
BRIEF DESCRIPTION OF THE DRAWINGS
The above and further advantages of the invention may be better understood by referring to the following description in conjunction with the accompanying drawings, in which:
FIGS. 1A, 1B and 1C are a cross sectional side view (FIG. 1A), a cross-sectional top view at cross section E-E (FIG. 1B), and a cross-sectional bottom view at cross section F-F (FIG. 1C) of a system for separating high molecular weight (HMW) gases in an exhaust stack in accordance with one embodiment of the present invention;
FIGS. 2A, 2B and 2C are a cross sectional side view (FIG. 2A), a cross-sectional top view at cross section E-E (FIG. 2B), and a cross-sectional bottom view at cross section F-F (FIG. 2C) of a system for separating high molecular weight (HMW) gases in an exhaust stack in accordance with another embodiment of the present invention;
FIGS. 3A, 3B and 3C are a cross sectional side view (FIG. 3A), a cross-sectional top view at cross section E-E (FIG. 3B), and a cross-sectional bottom view at cross section F-F (FIG. 3C) of a system for separating high molecular weight (HMW) gases in an exhaust stack in accordance with one embodiment of the present invention;
FIG. 4 is a flow chart of a method for separating high molecular weight (HMW) gases from an exhaust gas in accordance with one embodiment of the present invention; and
FIG. 5 is a block diagram of a system incorporating the embodiments of the present invention.
 DETAILED DESCRIPTION OF THE INVENTION
While the making and using of various embodiments of the present invention are discussed in detail below, it should be appreciated that the present invention provides many applicable inventive concepts that can be embodied in a wide variety of specific contexts. The specific embodiments discussed herein are merely illustrative of specific ways to make and use the invention and do not delimit the scope of the invention.
The present invention provides a system and method for separating high molecular weight gases, such as CO2, from any combustion source. More specifically, the present invention imparts centrifugal force on the exhaust or flue gas by spinning the exhaust or flue gas with enough velocity to remove the heavy components, such as CO2, to the outside diameter of the stack and removing it thru an annular space or gap formed by an interior vent. The spin needed for the centrifugal action may be imparted by using a blower to remove the gas tangentially from one side of the stack and blowing it tangentially back into the stack on the other side. The use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower. Note that the velocity of the system may be varied to accommodate various fuels and flue gas mixtures. Moreover, the system may be fitted to stacks of virtually any size or flow. As a result, the present invention provides a simple process to take care of the hardest and most expensive step in controlling CO2. Many treatment options are available after separation.
The typical constituent parts of exhaust or flue gas (used interchangeably) are as follows: the molecular weight of CO2 is 44 and it comprises 10-15% of flue gases, the molecular weight of N2 is 28 and it comprises approximately 78% of flue gases, the molecular weight of O2 is 32 and it comprises approximately 3% of flue gases, the molecular weight of H2O is 18 and it comprises approximately 10-15% of flue gases, and the molecular weight of CO is 28 and it is normally a negligible percentage of the flue gas. These numbers indicate the CO2 will need to be basically separated from the N2 with a differential molecular weight of 16. After the CO2 is separated from the flue gases, it can be compressed, injected into the ground, or used for other processes. In one embodiment of the present invention, the CO2 is collected in a tank and then flowed up thru bubble trays containing sodium hydroxide which will cause the CO2 to combine and produce sodium carbonate which can be collected for use otherwise. This embodiment is particularly useful in refineries and chemical plants where sodium hydroxide is commonly used in their processes (sometimes called “caustic soda”). After the sodium hydroxide is used, the plants use acid to reduce the used sodium hydroxide to a neutral PH so it can be disposed of. Using this byproduct does not require the purchase of gases and eliminates a disposal problem.
Now referring to FIGS. 1A, 1B and 1C, a cross sectional side view (FIG. 1A), a cross-sectional top view at cross section E-E (FIG. 1B), and a cross-sectional bottom view at cross section F-F (FIG. 1C) of a system 100 for separating high molecular weight (HMW) gases 112 in an exhaust stack 102 from an exhaust gas 104 of a combustion source in accordance with one embodiment of the present invention are shown. A blower 106 is attached to an intake 108 of the exhaust stack 102 to receive the exhaust gas 104 from the combustion source (502, FIG. 5) and create a tangential flow 110 of the exhaust gas 104 within the exhaust stack 102. The blower 106 imparts sufficient centrifugal force on the exhaust gas 104 to concentrate the high molecular weight gases 112, such as CO2 or other gases having a higher molecular weight than N2 or O2 (e.g., greater than 35), along the inner perimeter or surface 114 of the exhaust stack 102. As used herein, “along the inner perimeter or surface of the exhaust stack” means an area within the exhaust stack 102 that is much closer to the inner surface 114 of the exhaust stack 102 than to the center of the exhaust stack 102. In other words, the high molecular weight gases 112 are concentrated near, towards or proximate to the inner surface 114 of the exhaust stack 102. The low molecular weight gases 130 exit through the top of the exhaust stack 102.
Typically, the blower 106 causes the exhaust gases 104 to spin around the interior of the exhaust stack 102 at least five times within a height approximately equal to one diameter (D) of the exhaust stack 102. As shown, the blower 106 is external to the exhaust stack 102 and is connected to the intake 108 of the exhaust stack 102 with a first pipe 116. A second pipe 118 connects the blower 106 to the bottom of the exhaust stack 102 at a point 120 approximately opposite to the intake 108 and in line with the tangential flow 110 in order to create the sufficient centrifugal force on the exhaust gas 104. The use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower 106.
An interior vent 122 within the exhaust stack 102 collects the high molecular weight gases 112 concentrated along the inner surface 114 of the exhaust stack 102. The interior vent 122 includes: (i) a vent wall 122ab having a top portion 122a attached to the interior surface 114 of the exhaust stack 102 along the entire inner perimeter of the exhaust stack 102 (e.g., the top portion 122a is attached to the inner surface 114 along any side cross section of the exhaust stack 102) and a lower portion 122b that extends downward into the exhaust stack 102 to form an annular space or gap 124 between the vent wall 122 lower portion 122b and the interior surface 114 of the exhaust stack 102; and (ii) at least one opening 122c in the interior surface 114 of the exhaust stack 102 between the top 122a and bottom lower 122b portions of the vent wall 122 122ab. A transfer pipe 128 is connected to the at least one opening 122c in the interior surface 114 of the exhaust stack 102 to remove the high molecular weight gases 112 from the interior vent 122. The at least one or more openings 122c can be holes, slots, or any other geometrically shaped passageway. Moreover, more than one transfer pipe 128 can be used. The lower portion 122b of the vent wall 122 122ab can be substantially parallel to the interior surface 114 of the exhaust stack 102, curved or angled with respect to the interior surface 114 of the exhaust stack 102. Note that the top portion 122a of the interior vent 122 does not have to be aligned with a horizontal plane of the exhaust stack 102. For example, the top portion 122a can be angled from the horizontal plane in accordance with the tangential flow 110 (top portion 122a on the opposite side of the exhaust stack 102 from the opening 122c positioned lower than the top portion 122a adjacent to the opening 122c). For example, the top portion 122a can form one or more spirals down from the one or more openings 122c. In addition, an optional baffle or guide 122d proximate to the at least one opening 122c can be used to direct the flow of the high molecular weight gases 112 from the interior vent 122 into the transfer pipe 128. The baffle or guide 122d can be straight, angled, curved or any other shape and orientation to more efficiently guide the high molecular weight gasses gases 112 into the transfer pipe 128.
The dimensions (A, B, C, D) of the vent wall 122 122ab will vary in accordance with the design specifications for the system 100. The design specification may take into account one or more parameters, such as temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture. The system 100 dimensions should be configured to concentrate and capture at least 85% of the high molecular weight gases. The at least one opening 122c is positioned at a height (A) such that the high molecular weight gases 112 have spun around the exhaust stack 102 approximately fifteen to twenty times or more. In one example, the at least one opening 122c is positioned at a height (A) above the bottom of the exhaust stack 102 approximately equal to three diameters (3×D) of the exhaust stack 102, the annular space or gap 124 has an area (B) of approximately 10% of a cross-sectional area of the exhaust stack 102, and the bottom lower portion 122a 122b of the vent wall 122 122ab extends down a distance (C) approximately equal to one half diameter (0.5×D) of the exhaust stack 102.
The system 100 may also include other components, such as a tank (504, FIG. 5) connected to the transfer pipe 128 to store the removed high molecular weight gases 112, a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 (506, FIG. 5), a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the annular space or gap 124 based on one or more parameters (e.g., temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture, etc.), and/or one or more sensors (not shown) attached to the blower 106, exhaust stack 102, interior vent 122 or transfer pipe 128. A controller (not shown) can be communicably coupled to the motor (not shown) and the one or more sensors to adjust the size (B) of the annular space or gap 124 using the motor based on one or more parameters detected by the one or more sensors. As previously discussed, one or more bubble trays (508, FIG. 5) containing sodium hydroxide can be attached to the transfer pipe 128 or tank such that the removed CO2 is combined with the sodium hydroxide to produce sodium carbonate.
Referring now to FIGS. 2A, 2B and 2C, a cross-sectional side view (FIG. 2A), a cross-sectional top view at cross section E-E (FIG. 2B) and a cross-sectional bottom view at cross section F-F (FIG. 2C) of the system 200 for separating high molecular weight (HMW) gases 112 in an exhaust stack 102 from an exhaust gas 104 of a combustion source in accordance with one embodiment of the present invention are shown. A blower 106 is attached to an intake 108 of the exhaust stack 102 to receive the exhaust gas 104 from the combustion source (502, FIG. 5) and create a tangential flow 110 of the exhaust gas 104 within the exhaust stack 102. The blower 106 imparts sufficient centrifugal force on the exhaust gas 104 to concentrate the high molecular weight gases 112, such as CO2 or other gases having a higher molecular weight greater than N2 or O2 (e.g., greater than 35), along the inner perimeter or surface 114 of the exhaust stack 102. Typically, the blower 106 causes the exhaust gases 104 to spin around the interior of the exhaust stack 102 at least five times within a height approximately equal to one diameter (D) of the exhaust stack 102. As shown, the blower 106 is external to the exhaust stack 102 and is connected to the intake 108 of the exhaust stack 102 with a first pipe 116. A second pipe 118 connects the blower 106 to the bottom of the exhaust stack 102 at a point 120 approximately opposite to the intake 108 and in line with the tangential flow 110 in order to create the sufficient centrifugal force on the exhaust gas 104. The use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower 106.
An interior vent 122 within the exhaust stack 102 collects the high molecular weight gases 112 concentrated along the inner surface 114 of the exhaust stack 102. The interior vent 122 includes: (i) a vent wall 122ab having a top portion 122a attached to the interior surface 114 of the exhaust stack 102 along the entire inner perimeter of the exhaust stack 102 (e.g., the top portion 122a is attached to the inner surface 114 along any side cross section of the exhaust stack 102) and a lower portion 122b that extends downward into the exhaust stack 102 to form an annular space or gap 124 between the vent wall 122 122ab and the interior surface 114 of the exhaust stack 102; (ii) at least one opening 122c in the interior surface 114 of the exhaust stack 102 between the top 122a and bottom lower 122b portions of the vent wall 122 122ab; and (iii) a bustle 202 attached to or integrated into the exhaust stack 102 between the at least one opening 122c in the inner surface 114 of the exhaust stack 102 and a transfer pipe 128. The transfer pipe 128 is connected to bustle 202 to remove the high molecular weight gases 112 from the interior vent 122 122ab. The at least one or more openings 122c can be holes, slots, or any other geometrically shaped passageway. Moreover, more than one transfer pipe 128 can be used. The lower portion 122b of the vent wall 122 122ab can be substantially parallel to the interior surface 114 of the exhaust stack 102, curved or angled with respect to the interior surface 114 of the exhaust stack 102. Note that the top portion 122a of the interior vent 122 122ab does not have to be aligned with a horizontal plane of the exhaust stack 102. For example, the top portion 122a can be angled from the horizontal plane in accordance with the tangential flow 110 (top portion 122a on the opposite side of the exhaust stack 102 from the opening 122c positioned lower than the top portion 122a adjacent to the opening 122c). For example, the top portion 122a can form one or more spirals down from the one or more openings 122c. In addition, an optional baffle or guide 122d proximate to the at least one opening 122c can be used to direct the flow of the high molecular weight gases 112 from the interior vent 122 into the transfer pipe 128. The baffle or guide 122d can be straight, angled, curved or any other shape and orientation to more efficiently guide the high molecular weight gases 112 into the transfer pipe 128.
The dimensions (A, B, C, D) of the vent wall 122 122ab will vary in accordance with the design specifications for the system 200. The design specification may take into account one or more parameters, such as temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture. The system 200 dimensions should be configured to concentrate and capture at least 85% of the high molecular weight gases. The at least one opening 122c is positioned at a height (A) such that the high molecular weight gases 112 have spun around the exhaust stack 102 approximately fifteen to twenty times or more. In one example, the at least one opening 122c is positioned at a height (A) above the bottom of the exhaust stack 102 approximately equal to three diameters (3×D) of the exhaust stack 102, the annular space or gap 124 has an area (B) of approximately 10% of a cross-sectional area of the exhaust stack 102, and the bottom lower portion 122a 122b of the vent wall 122 122ab extends down a distance (C) approximately equal to one half diameter (0.5×D) of the exhaust stack 102.
The system 100 may also include other components, such as a tank (504, FIG. 5) connected to the transfer pipe 128 to store the removed high molecular weight gases 112, a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 (506, FIG. 5), a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the annular space or gap 124 based on one or more parameters (e.g., temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture, etc.), and/or one or more sensors (not shown) attached to the blower 106, exhaust stack 102, interior vent 122 or transfer pipe 128. A controller (not shown) can be communicably coupled to the motor and the one or more sensors to adjust the size (B) of the annular space or gap 124 using the motor based on one or more parameters detected by the one or more sensors. As previously discussed, one or more bubble trays (508, FIG. 5) containing sodium hydroxide can be attached to the transfer pipe 128 or tank such that the removed CO2 is combined with the sodium hydroxide to produce sodium carbonate.
Now referring to FIGS. 3A, 3B and 3C, a cross sectional side view (FIG. 3A)), a cross-sectional top view at cross section E-E (FIG. 3B) and a cross-sectional bottom view at cross section F-F (FIG. 3C) of the system 300 for separating high molecular weight (HMW) gases in an exhaust stack 102 from an exhaust gas 104 of a combustion source in accordance with one embodiment of the present invention are shown. A blower 106 is attached to an intake 108 of the exhaust stack 102 to receive the exhaust gas 104 from the combustion source (502, FIG. 5) and create a tangential flow 110 of the exhaust gas 104 within the exhaust stack 102. The blower 106 imparts sufficient centrifugal force on the exhaust gas 104 to concentrate the high molecular weight gases 112, such as CO2 or other gases having a higher molecular weight greater than N2 or O2 (e.g., greater than 35), along the inner perimeter or surface 114 of the exhaust stack 102. Typically, the blower 106 causes the exhaust gases 104 to spin around the interior of the exhaust stack 102 at least five times within a height approximately equal to one diameter (D) of the exhaust stack 102. As shown, the blower 106 is internal to the exhaust stack 102. A second pipe 118 or channel connects the blower 106 to the bottom of the exhaust stack 102 at a point 120 approximately opposite to the intake 108 and in line with the tangential flow 110 in order to create the sufficient centrifugal force on the exhaust gas 104. The use of a stationary tubulator, or spin vanes, or actual in-stack centrifuge may be necessary in addition to the blower 106.
An interior vent 122 within the exhaust stack 102 collects the high molecular weight gases 112 concentrated along the inner surface 114 of the exhaust stack 102. The interior vent 122 includes: (i) a vent wall 122ab having a top portion 122a attached to the interior surface 114 of the exhaust stack 102 along the entire inner perimeter of the exhaust stack 102 (e.g., the top portion 122a is attached to the inner surface 114 along any side cross section of the exhaust stack 102) and a lower portion 122b that extends downward into the exhaust stack 102 to form an annular space or gap 124 between the vent wall 122 122ab and the interior surface 114 of the exhaust stack 102; (ii) at least one opening 122c in the interior surface 114 of the exhaust stack 102 between the top 122a and bottom lower 122b portions of the vent wall 122 122ab; and (iii) a bustle 202 attached to or integrated into the exhaust stack 102 between the at least one opening 122c in the inner surface 114 of the exhaust stack 102 and a transfer pipe 128. The transfer pipe 128 is connected to bustle 202 to remove the high molecular weight gases 112 from the interior vent 122. The at least one or more openings 122c can be holes, slots, or any other geometrically shaped passageway. Moreover, more than one transfer pipe 128 can be used. The lower portion 122b of the vent wall 122 122ab can be substantially parallel to the interior surface 114 of the exhaust stack 102, curved or angled with respect to the interior surface 114 of the exhaust stack 102. Note that the top portion 122a of the interior vent 122 does not have to be aligned with a horizontal plane of the exhaust stack 102. For example, the top portion 122a can be angled from the horizontal plane in accordance with the tangential flow 110 (top portion 122a on the opposite side of the exhaust stack 102 from the opening 122c positioned lower than the top portion 122a adjacent to the opening 122c). For example, the top portion 122a can form one or more spirals down from the one or more openings 122c. In addition, an optional baffle or guide 122d proximate to the at least one opening 122c can be used to direct the flow of the high molecular weight gases 112 from the interior vent 122 into the transfer pipe 128. The baffle or guide 122d can be straight, angled, curved or any other shape and orientation to more efficiently guide the high molecular weight gases 112 into the transfer pipe 128).
The dimensions (A, B, C, D) of the vent wall 122 122ab will vary in accordance with the design specifications for the system 300. The design specification may take into account one or more parameters, such as temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture. The system 300 dimensions should be configured to concentrate and capture at least 85% of the high molecular weight gases. The at least one opening 122c is positioned at a height (A) such that the high molecular weight gases 112 have spun around the exhaust stack 102 approximately fifteen to twenty times or more. In one example, the at least one opening 122c is positioned at a height (A) above the bottom of the exhaust stack 102 approximately equal to three diameters (3×D) of the exhaust stack 102, the annular space or gap 124 has an area (B) of approximately 10% of a cross-sectional area of the exhaust stack 102, and the bottom lower portion 122a 122b of the vent wall 122 122ab extends down a distance (C) approximately equal to one half diameter (0.5×D) of the exhaust stack 102.
The system 100 may also include other components, such as a tank (504, FIG. 5) connected to the transfer pipe 128 to store the removed high molecular weight gases 112, a compressor attached to the transfer pipe 128 to compress the removed high molecular weight gases 112 (506, FIG. 5), a motor (not shown) attached to the vent wall 122 122ab that adjusts a size of the annular space or gap 124 based on one or more parameters (e.g., temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture, etc.), and/or one or more sensors (not shown) attached to the blower 106, exhaust stack 102, interior vent 122 or transfer pipe 128. A controller (not shown) can be communicably coupled to the motor and the one or more sensors to adjust the size (B) of the annular space or gap 124 using the motor based on one or more parameters detected by the one or more sensors. As previously discussed, one or more bubble trays (508, FIG. 5) containing sodium hydroxide can be attached to the transfer pipe 128 or tank such that the removed CO2 is combined with the sodium hydroxide to produce sodium carbonate.
Referring now to FIG. 4, a flow chart of a method 400 for separating high molecular weight gases in an exhaust stack from an exhaust gas of a combustion source in accordance with one embodiment of the present invention is shown. The following components are provided in block 402 to perform the method 400: (a) a blower attached to an intake of an exhaust stack to receive the exhaust gas from the combustion source, (b) an interior vent within the exhaust stack comprising (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the entire inner perimeter of the exhaust stack and a lower portion that extends downward into the exhaust stack to form an annular space or gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall, and (c) a transfer pipe connected to the at least one opening in the interior surface of the exhaust stack. A tangential flow of the exhaust gas within the exhaust stack is created using the blower in block 404. The blower imparts sufficient centrifugal force on the exhaust gas to concentrate substantially all of the high molecular weight gases along the inner surface of the exhaust stack. The high molecular weight gases concentrated along the inner surface of the exhaust stack are collected using the interior vent in block 406. The high molecular weight gases are removed from the interior vent using the transfer pipe in block 408.
Additional steps may include storing the removed high molecular weight gases in a tank (504, FIG. 5) connected to the transfer pipe, compressing the removed high molecular weight gases (506, FIG. 5), injecting the removed high molecular weight gases into a below-ground storage, or flowing the removed CO2 up through one or more bubble trays containing sodium hydroxide which causes the removed CO2 to combine with the sodium hydroxide to produce sodium carbonate (508, FIG. 5).
Now referring to FIG. 5, a block diagram of a system 500 incorporating the embodiments of the present invention is shown. As previously described, the combustion source 502 creates exhaust 104, which is transported to the exhaust stack 102 (not specifically illustrated in FIG. 5) of system 100, 200 or 300. Low molecular gas 130 exits the exhaust stack 100, 200 or 300. The high molecular weight gas 112 is collected and removed from the exhaust stack 100, 200 or 300 for further processing (e.g., storage in a tank 504, compression followed by storage 506, bubble trays to produce sodium carbonate 508, etc.). The high molecular weight gas 112 can be used in other ways as will be appreciated and known by those skilled in the art.
The various illustrative logical blocks, modules, circuits, and algorithm steps described herein may be implemented as electronic hardware, computer software, or combinations of both, depending on the application and functionality. Moreover, the various logical blocks, modules, and circuits described herein may be implemented or performed with a general purpose processor (e.g., microprocessor, conventional processor, controller, microcontroller, state machine or combination of computing devices), a digital signal processor (“DSP”), an application specific integrated circuit (“ASIC”), a field programmable gate array (“FPGA”) or other programmable logic device, discrete gate or transistor logic, discrete hardware components, or any combination thereof designed to perform the functions described herein. Similarly, steps of a method or process described herein may be embodied directly in hardware, in a software module executed by a processor, or in a combination of the two. A software module may reside in RAM memory, flash memory, ROM memory, EPROM memory, EEPROM memory, registers, hard disk, a removable disk, a CD-ROM, or any other form of storage medium known in the art. Although preferred embodiments of the present invention have been described in detail, it will be understood by those skilled in the art that various modifications can be made therein without departing from the spirit and scope of the invention as set forth in the appended claims.

Claims (45)

What is claimed is:
1. A system for separating high molecular weight gases in an exhaust stack from an exhaust gas of a combustion source comprising:
a blower attached coupled to an intake of the exhaust stack and configured to receive the exhaust gas from the combustion source and create a tangential flow of the exhaust gas within the exhaust stack, wherein the blower imparts sufficient centrifugal force on the exhaust gas to concentrate the high molecular weight gases along the inner surface of the exhaust stack;
an interior vent within the exhaust stack that collects the configured to collect high molecular weight gases concentrated along the inner an interior surface of the exhaust stack, the interior vent comprising (i) a vent wall having a top portion attached coupled to the interior surface of the exhaust stack along the an entire inner perimeter of the exhaust stack and a lower bottom portion that extends downward into the exhaust stack to form a gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall; and
a transfer pipe connected coupled to the at least one opening in the interior surface of the exhaust stack, configured to remove the high molecular weight gases from the interior vent.
2. The system as recited in claim 1, further comprising:
a tank connected to the transfer pipe; or
a compressor attached to the transfer pipe to compress the removed high molecular weight gases.
3. The system as recited in claim 1, wherein the high molecular weight gases have a molecular weight greater than 35.
4. The system as recited in claim 1, wherein the high molecular weight gases comprise CO2.
5. The system as recited in claim 4, further comprising one or more bubble trays containing sodium hydroxide attached to the transfer pipe such that the removed CO2 is combined with the sodium hydroxide to produce sodium carbonate.
6. The system as recited in claim 1, wherein:
the sufficient centrifugal force is provided by the blower in combination with a stationary tabulator, spin vanes, or in-stack centrifuge; and
the blower is located inside or outside of the exhaust stack.
7. The system as recited in claim 1, further comprising a bustle attached to or integrated into the exhaust stack between the at least one opening in the inner surface of the exhaust stack and the transfer pipe.
8. The system as recited in claim 1, wherein the vent wall is substantially parallel to the interior surface of the exhaust stack, curved, or is angled with respect to the interior surface of the exhaust stack.
9. The system as recited in claim 1, wherein at least 85% of the high molecular weight gases are concentrated along the inner interior surface of the exhaust stack.
10. The system as recited in claim 1, wherein the gap comprises an area of approximately 10% of a cross-sectional area of the exhaust stack.
11. The system as recited in claim 1, wherein the at least one opening is positioned such that the high molecular weight gases have spun around the exhaust stack approximately fifteen to twenty times.
12. The system as recited in claim 1, wherein the blower causes the exhaust gases to spin around the exhaust stack at least five times within a height approximately equal to one diameter of the exhaust stack.
13. The system as recited in claim 1, wherein the at least one opening is positioned at a height above the bottom of the exhaust stack approximately equal to three diameters of the exhaust stack.
14. The system as recited in claim 1, wherein the bottom portion of the vent wall extends down to a height above the bottom of the exhaust stack approximately equal to one half diameter of the exhaust stack.
15. The system as recited in claim 1, further comprising a motor attached to the vent wall that adjusts a size of the gap.
16. The system as recited in claim 15, wherein the motor is used to adjust the size of the gap based on one or more parameters comprising temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture.
17. The system as recited in claim 15, further comprising:
one or more sensors attached to the blower, exhaust stack, interior vent or transfer pipe; and
a controller communicably coupled to the motor and the one or more sensors, wherein the controller to adjusts the size of the gap using the motor based on one or more parameters detected by the one or more sensors.
18. A system for separating high molecular weight gases from an exhaust gas of a combustion source comprising:
an exhaust stack;
a blower attached to an intake of the exhaust stack to receive the exhaust gas from the combustion source and create a tangential flow of the exhaust gas within the exhaust stack, wherein the blower imparts sufficient centrifugal force on the exhaust gas to concentrate the high molecular weight gases along the inner an interior surface of the exhaust stack;
an interior vent within the exhaust stack that collects the high molecular weight gases concentrated along the inner interior surface of the exhaust stack, the interior vent comprising (i) a vent wall having a top portion attached to the interior surface of the exhaust stack along the an entire inner perimeter of the exhaust stack and a lower bottom portion that extends downward into the exhaust stack to form a gap between the vent wall and the interior surface of the exhaust stack, and (ii) at least one opening in the interior surface of the exhaust stack between the top and bottom portions of the vent wall; and
a transfer pipe connected to the at least one opening in the interior surface of the exhaust stack to remove the high molecular weight gases from the interior vent; and
wherein (a) the high molecular weight gases have a molecular weight greater than 35, (b) at least 85% of the high molecular weight gases are concentrated along the inner interior surface of the exhaust stack, (c) the gap comprises an area of approximately 10% of a cross-sectional area of the exhaust stack, (d) the at least one opening is positioned at a height above the a bottom of the exhaust stack approximately equal to three diameters of the exhaust stack, and (e) the blower causes the exhaust gases to spin around the exhaust stack at least five times within a height approximately equal to one diameter of the exhaust stack.
19. The system as recited in claim 18, further comprising:
a tank connected to the transfer pipe; or
a compressor attached to the transfer pipe to compress the removed high molecular weight gases.
20. The system as recited in claim 18, wherein the high molecular weight gases comprise CO2.
21. The system as recited in claim 20, further comprising one or more bubble trays containing sodium hydroxide attached to the transfer pipe such that the removed CO2 is combined with the sodium hydroxide to produce sodium carbonate.
22. The method as recited in claim 18, wherein:
the sufficient centrifugal force is provided by the blower in combination with a stationary tabulator, spin vanes, or in-stack centrifuge; and
the blower is located inside or outside of the exhaust stack.
23. The system as recited in claim 18, further comprising a bustle attached to or integrated into the exhaust stack between the at least one opening in the an inner surface of the exhaust stack and the transfer pipe.
24. The system as recited in claim 18, wherein the vent wall is substantially parallel to the interior surface of the exhaust stack, curved, or is angled with respect to the interior surface of the exhaust stack.
25. The system as recited in claim 18, wherein the bottom portion of the vent wall extends down to a height above the bottom of the exhaust stack approximately equal to one half diameter of the exhaust stack.
26. The system as recited in claim 18, further comprising a motor attached to the vent wall that adjusts a size of the gap.
27. The system as recited in claim 26, wherein the motor is used to adjust the size of the gap based on one or more parameters comprising temperature, humidity, velocity, gas composition, fuel type, or exhaust gas mixture.
28. The system as recited in claim 26, further comprising:
one or more sensors attached to the blower, exhaust stack, interior vent or transfer pipe; and
a controller communicably coupled to the motor and the one or more sensors, wherein the controller to adjusts the size of the gap using the motor based on one or more parameters detected by the one or more sensors.
29. A system for separating high molecular weight gases in an exhaust stack from an exhaust gas of a combustion source comprising:
a blower coupled to an intake of the exhaust stack and configured to receive exhaust gas from the combustion source and create a tangential flow of the exhaust gas within the exhaust stack;
an interior vent within the exhaust stack configured to collect high molecular weight gases concentrated, by the tangential flow of the exhaust gas, along an inner surface of the exhaust stack;
an opening in the inner surface of the exhaust stack; and
a transfer pipe coupled to the opening in the inner surface of the exhaust stack and configured to remove the high molecular weight gases from the interior vent,
wherein the interior vent includes a vent wall having a top portion coupled to the inner surface of the exhaust stack and a lower portion that extends downward into the exhaust stack to form a gap between the vent wall and the inner surface of the exhaust stack.
30. A system for removing high molecular weight gases from an exhaust stream, comprising:
an exhaust stack;
means for concentrating high molecular weight gases toward an inner surface of the exhaust stack, wherein the means for concentrating high molecular weight gases toward an inner surface of the exhaust stack comprises means for spinning the exhaust gas and imparting centrifugal force, and wherein the means for spinning the exhaust gas and imparting centrifugal force comprises a blower coupled to an exhaust stack inlet, the inlet being configured to introduce exhaust gas into the exhaust stack tangentially, with respect to movement of gases within the stack, and further wherein the means for spinning the exhaust gas and imparting centrifugal force comprises an exhaust stack outlet coupled to the blower and configured to withdraw gas from the stack, tangentially, with respect to movement of gases within the stack, the blower being configured to reintroduce the withdrawn gas into the stack at the exhaust stack inlet; and
means for removing high molecular weight gases concentrated along the inner surface of the exhaust stack.
31. An exhaust system, comprising:
an exhaust stack, including:
an exhaust inlet positioned and configured such that gases introduced into the exhaust stack via the exhaust inlet tend to spin within the exhaust stack,
an exhaust port positioned on a side of the exhaust stack opposite the exhaust inlet and configured to receive gases introduced via the exhaust inlet and spinning within the exhaust stack, and
an opening extending through an interior surface of the exhaust stack, positioned above the exhaust inlet and below a top of the exhaust stack;
a blower, including a blower inlet coupled to the exhaust port and a blower outlet coupled to the exhaust inlet, the blower being configured to draw gases from the exhaust stack via the exhaust port and to blow the drawn gases into the exhaust stack via the exhaust inlet; and
an interior vent coupled to the opening, positioned and configured to collect gases from along the interior surface of the exhaust stack, wherein the blower is positioned external to the exhaust stack.
32. The system of claim 31, wherein the blower outlet is coupled to the exhaust inlet via a first pipe, and the blower inlet is coupled to the exhaust port via a second pipe.
33. The system of claim 31, wherein the interior vent includes a gap configured to collect gases from along the interior surface of the exhaust stack.
34. The system of claim 33, wherein the gap has an annular shape, and extends around the interior surface of the exhaust stack.
35. The system of claim 33, wherein a size of the gap is adjustable.
36. The system of claim 31, wherein the interior vent includes a gap defined by a space between a vent wall and the interior surface of the exhaust stack.
37. The system of claim 36, wherein a top portion of the interior vent is closed, the vent wall extending downward from the top portion to the gap at a bottom portion of the interior vent.
38. The system of claim 37, wherein the opening is positioned between the top and bottom portions of the interior vent.
39. The system of claim 38, wherein the opening is coupled to a transfer pipe configured to remove the collected gases from the interior vent.
40. The system of claim 38, wherein the transfer pipe is coupled to a compressor.
41. The system of claim 38, wherein the transfer pipe is coupled to a storage tank.
42. The system of claim 38, wherein the transfer pipe is coupled to a bubble tray.
43. The system of claim 36, wherein the vent wall extends downward substantially parallel to the interior surface of the exhaust stack.
44. A system for removing high molecular weight gases from an exhaust stream, comprising:
an exhaust stack;
means for concentrating high molecular weight gases toward an inner surface of the exhaust stack, wherein the means for concentrating high molecular weight gases toward an inner surface of the exhaust stack comprises means for spinning the exhaust gas and imparting centrifugal force, and wherein the means for spinning the exhaust gas and imparting centrifugal force comprises a blower coupled to an exhaust stack inlet, the inlet being configured to introduce exhaust gas into the exhaust stack tangentially, with respect to movement of gases within the stack; and
means for removing high molecular weight gases concentrated along the inner surface of the exhaust stack, wherein the exhaust stack inlet and the exhaust stack outlet are positioned in a bottom portion of the exhaust stack, substantially opposite each other.
45. A system for separating high molecular weight gases in an exhaust stack from an exhaust gas of a combustion source comprising:
a blower coupled to an intake of the exhaust stack and configured to receive exhaust gas from the combustion source and create a tangential flow of the exhaust gas within the exhaust stack;
an interior vent within the exhaust stack configured to collect high molecular weight gases concentrated, by the tangential flow of the exhaust gas, along an inner surface of the exhaust stack;
an opening in the inner surface of the exhaust stack; and
a transfer pipe coupled to the opening in the inner surface of the exhaust stack and configured to remove the high molecular weight gases from the interior vent,
wherein the interior vent extends along an entire inner perimeter of the exhaust stack.
US15/016,678 2010-12-07 2016-02-05 System and method for separating high molecular weight gases from a combustion source Expired - Fee Related USRE46682E1 (en)

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US20120141352A1 (en) 2012-06-07
WO2012078821A3 (en) 2012-09-20
WO2012078821A2 (en) 2012-06-14
US8657919B2 (en) 2014-02-25
USRE46829E1 (en) 2018-05-08
US8652234B1 (en) 2014-02-18

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