Systems and methods for removal of carbon dioxide from seawater

Abstract

The present invention generally relates to systems and methods for the separation and removal of carbon dioxide from a liquid, for example, seawater. The systems include an extraction system that collects carbon dioxide from the seawater through a medium, and removes carbon dioxide from the medium; the extraction systems comprising a reactor and a membrane. Alternatively, the extraction system includes a reactor, a membrane and a catalyst.

Claims

1. An extraction system for separating and removing carbon dioxide from a liquid, the system comprising: a reactor; and, a membrane capable of allowing the liquid to flow back and forth across the membrane until equilibrium is established with an air gap from which the carbon dioxide is removable, separated and sequestered; wherein the membrane comprises a membrane material permeable to carbon dioxide and water; whereby the system converts bicarbonate ion into dissolved carbon dioxide to replace the carbon dioxide which is removed from the liquid.

2. The system according to claim 1, wherein the liquid is seawater.

3. The system according to claim 1, wherein the membrane material comprises pores with sizes from about 4 angstroms to about 40 angstroms.

4. The system according to claim 1, wherein the membrane material comprises silicone.

5. The system according to claim 4, wherein the membrane material is polydimethylsiloxane.

6. The system according to claim 1, wherein the membrane material is hydrophilic.

7. The system according to claim 2, wherein the reactor further comprises a desalination reactor.

8. The system according to claim 1, wherein the system further comprises a catalyst, wherein the catalyst comprises a catalytic enzyme which converts bicarbonate ion into dissolved carbon dioxide.

9. The system according to claim 8, wherein the catalytic enzyme is carbonic anhydrase.

10. The system according to claim 8, wherein the membrane further comprises a first inner membrane layer comprising a membrane material which is hydrophilic; and, a second outer membrane layer comprising a membrane material which is hydrophobic; the first inner membrane layer capable of containing the catalyst such that the catalyst is not flushed out of the reactor with the liquid from which the carbon dioxide was removed; the second outer membrane layer capable of surrounding the first inner membrane containing the catalyst.

11. The system according to claim 10, wherein the first inner membrane layer is a cylindrical hydrophilic membrane, capped at both distal and proximal ends, capable of containing the catalyst in the reactor.

12. The system according to claim 10, wherein the first inner membrane layer and second outer membrane layer comprise membrane material having pores with sizes from about 4 angstroms to about 40 angstroms.

13. The system according to claim 10, wherein the liquid is seawater.

14. The system according to claim 1, wherein the system is mounted aboard a ship, whereby carbon dioxide is removed from the liquid.

15. The system according to claim 10, wherein the system is mounted aboard a ship, whereby carbon dioxide is removed from the liquid.

16. An extraction system for separating and removing carbon dioxide from a liquid, the system comprising: a reactor; a membrane capable of allowing the liquid to flow back and forth across the membrane until equilibrium is established with an air gap from which the carbon dioxide can be removed, separated and sequestered; and, a catalyst; wherein the catalyst comprises a catalytic enzyme which converts bicarbonate ion into dissolved carbon dioxide; wherein the membrane comprises a membrane material permeable to carbon dioxide and water and comprising pores with sizes from about 5 angstroms to about 40 angstroms; whereby the system converts bicarbonate ion into dissolved carbon dioxide to replace the carbon dioxide which is removed from the liquid.

17. A method of separating and removing carbon dioxide from a liquid in an extraction system according to claim 1, wherein the membrane comprises an inner membrane layer and an outer membrane layer, the method comprising the steps of: a) exposing the liquid to the inner membrane layer and the outer membrane layer, whereby the liquid is subjected to contact with a catalyst contained within the inner membrane layer; b) allowing the liquid to flow back and forth across both the inner membrane layer and the outer membrane layer until equilibrium is established, whereby carbon dioxide and water vapor form in the air gap; c) evacuating the air gap above the liquid to remove carbon dioxide and water vapor; d) separating the carbon dioxide and water vapor; and e) sequestering the carbon dioxide.

18. The method according to claim 17, wherein the inner membrane layer containing the catalyst such that the catalyst is not flushed out of the reactor with the liquid from which the carbon dioxide was removed; and the outer membrane layer surrounding the inner membrane containing the catalyst.

19. The method according to claim 17, wherein the inner membrane layer comprises a hydrophilic membrane material, the outer membrane layer comprises a hydrophobic membrane material, and the catalyst comprises a catalytic enzyme which converts bicarbonate ion into dissolved carbon dioxide.

20. The method according to claim 19, wherein the catalytic enzyme is carbonic anhydrase.

21. The method according to claim 17, wherein the inner membrane layer and the outer membrane layer comprise membrane material having pores with sizes from about 4 angstroms to about 40 angstroms.

22. The method according to claim 17, wherein the outer membrane layer comprises a membrane material comprising silicone.

23. The method according to claim 22, wherein the membrane material is polydimethylsiloxane.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) In order to describe embodiments of the present invention more fully, reference is made to the accompanying drawings. These drawings are not to be considered limitations in the scope of the invention, but are merely illustrative.

(2) FIG. 1A illustrates a schematic system of separating and removing carbon dioxide from seawater; according to an embodiment of the present invention.

(3) FIG. 1B illustrates a schematic system of separating and removing carbon dioxide from seawater combined with a desalination reactor; according to an embodiment of the present invention.

(4) FIG. 2 illustrates a method of separating and removing carbon dioxide from seawater, according to an embodiment of the present invention.

(5) FIG. 3 illustrates an alternate reactor of the system of separating and removing carbon dioxide from seawater; according to an embodiment of the present invention.

(6) FIG. 4 illustrates an alternate method of separating and removing carbon dioxide from seawater; according to an embodiment of the present invention.

(7) These and other features, aspects, and advantages of the present invention will become better understood with reference to the following description.

DETAILED DESCRIPTION OF EMBODIMENTS

(8) The description and the drawings of the present disclosure focus on one or more preferred embodiments of the present invention, and describe exemplary optional features and/or alternative embodiments of the present invention. The description and drawings are for the purpose of illustration and not limitation. Those of ordinary skill in the art would recognize variations, modifications and alternatives which are also within the scope of the invention.

(9) The present invention generally relates to systems and methods for separating, reduction and removal of carbon dioxide from a liquid, for example, seawater. The liquid can be any liquid known to those skilled in the art from which carbon dioxide can be removed. In a preferred embodiment of the present invention, the system includes an extraction system that sequesters and collects carbon dioxide from the liquid (e.g. seawater) through a medium, and removes carbon dioxide from the medium; the extraction system comprises a reactor, a membrane and a catalyst.

(10) The present invention addresses the aforementioned need for the reduction of carbon dioxide in the atmosphere by conversion of bicarbonate ion in seawater into carbon dioxide (CO.sub.2).

(11) Preferably a catalytic enzyme is used. More preferably, the enzyme is catalyzed by enzyme carbonic anhydrase. According to an embodiment of the present invention, carbon dioxide is removed by partial evacuation.

(12) In an embodiment of the present invention, systems and methods are provided to remove carbon dioxide from the ocean. According to a preferred embodiment, the systems and methods rely on a natural equilibrium between dissolved and atmospheric carbon dioxide, which constantly strive to be reestablished, pulling carbon dioxide out of the air and dissolving it in the ocean.

(13) Given the density of air, (1.2 g/L), and the molecular weight of CO.sub.2, (44.01 g/mol), the 415 ppm concentration of CO.sub.2 in the atmosphere corresponds to 1.13×10.sup.−5 mol/L (M). Typically, approximately half of the CO.sub.2 generated by combustion during for example, incineration, dissolves into oceans, where some of it can react to form carbonic acid. Most of the acid typically dissociates to bicarbonate ions, and some of that further dissociates to carbonate ion:
CO.sub.2+H.sub.2O←.fwdarw.H.sub.2CO.sub.3←.fwdarw.H.sup.++HCO.sub.3.sup.−←.fwdarw.2H.sup.++CO.sub.3.sup.−2  Equation 1

(14) It is known to those skilled in the art that most of the carbon in the ocean (approximately 89%) is in the form of bicarbonate, HCO.sub.3.sup.−. Typically, the bicarbonate concentration is 2.38×10.sup.−3 M, which is approximately 211 times the concentration of CO.sub.2 in air. It is well known to those skilled in the art that it can be easier to remove a species from a mixture selectively if that species' concentration is higher.

(15) Typically, the H.sup.+ ions given off by carbonic acid are responsible for the acidification of the ocean, with its concomitant destruction of the bottom of the food chain as well as coral reefs. Selective removal of bicarbonate will therefore also mitigate the destruction being caused by ocean acidification.

(16) As can be appreciated, the double arrows in Equation 1 indicates that all the reactions are reversible, (forward and backward reactions happening continuously in equilibrium). Typically, if one of the species in the mixture is selectively removed from the system, the reactions adjust according to Le Chatelier's Principle to reform and reestablish equilibrium. Therefore, selective removal of bicarbonate will result in more CO.sub.2 moving from the atmosphere into the ocean to compensate, thus lowering atmospheric CO.sub.2. The same effect will occur by partially evacuating a sample of seawater so that dissolved CO.sub.2 bubbles out; the chemistry will adjust to restore dissolved CO.sub.2 when the sample is pumped back into the sea.

(17) According to a preferred embodiment of the present invention, the systems and methods of restoring equilibrium can be speeded up by a catalyst. Typically the catalyst is an enzyme. More preferably, the catalytic enzyme is carbonic anhydrase (an enzyme used in many living things to maintain pH balance, by speeding up forward and reverse reactions). Typical applications for carbonic anhydrase have been used for the reverse of the present invention: to speed up conversion of CO.sub.2 and water to bicarbonate and H.sup.+ so that CO.sub.2 may be captured from flue gas in for example, fossil fuel power plants before being emitted into the air.

(18) Referring now to FIG. 1A a schematic diagram illustrating a system 100 to separate and remove carbon dioxide from a liquid, preferably seawater is provided according to an embodiment of the present invention. The liquid can be any liquid known to those skilled in the art from which carbon dioxide can be removed, such as fresh water (including lakes, ponds, reservoirs, rivers etc., for example), salt water, seawater or combinations thereof. First, seawater 112 is pumped from the ocean into an extraction system, and solids are filtered out using standard method filters 114 employed in desalination plants, with slow enough flow rate known to those skilled in the art (for example, 0.1 m/s) that fish can swim back out, resulting in filtered seawater 116. Preferably, the system 100 is an extraction system and comprises a reactor, and a membrane.

(19) In alternative embodiment of the present invention, the system can further include a catalyst. Preferably, the catalyst is a catalytic enzyme capable of boosting carbon-capture kinetics of bicarbonate. More preferably, the catalytic enzyme is carbonic anhydrase. Carbonic anhydrase is known to those skilled in the art to speed up the formation of bicarbonate by a factor of 10.sup.7.

(20) Next, the filtered seawater 116 flows into the reactor chamber 118. Typically, the reactor chamber 118 can be any reactor chamber which is a tank known to those skilled in the art and FIG. 1A illustrates the simplest possible reactor chamber, although those in the art can appreciate that other embodiments of the present invention can use reactor chambers with multiple channels with higher surface area. Preferably, the higher the surface area, the greater the amount of CO.sub.2 can be removed.

(21) According to an embodiment of the present invention, typically, the reactor 118 can be a batch or continuous flow reactor. Preferably, the reactor 118 is a reactor chamber capable of holding liquid and capable of removing gases (for example, air) above the seawater by evacuation.

(22) In yet a most preferred embodiment of the present invention, part of the reactor 118 contains a membrane 120. Typically, the membrane 120 can be made of any membrane material known to those skilled in the art. Preferably, the membrane material allows some of the gases to be pumped out more easily than others. For example, silicone (polydimethylsiloxane) has a permeability coefficient that is much higher for CO.sub.2 than it is for nitrogen, oxygen or argon; only water moves through silicone more efficiently. Preferably, the membrane material can be selected from the group consisting of polyvinylidene difluoride, polyether sulfone, cellulose acetate, cellulose nitrate nylon, and glass microfiber.

(23) In an embodiment of the present invention, the membrane 120 comprises a membrane material which comprises silicone. More preferably, the membrane material is polydimethylsiloxane.

(24) In yet an alternative embodiment of the present invention, the membrane 120 comprises a membrane material which is hydrophilic.

(25) Preferably, the membrane 120 is a membrane through which liquids such as water and gases can flow, but are impermeable to larger molecules like enzymes. Such membranes have pore sizes between about 4 and about 40 angstroms. According to an embodiment of the present invention, the pore size does not necessarily have to uniform and can be random.

(26) According to an embodiment of the present invention, the reactor chamber 118 contains a solution 122 between a wall of the reactor chamber 118 and the membrane 120. In a most preferred embodiment of the present invention, the solution 122 contains the catalyst of the system 100 for more efficient and quicker re-establishment of equilibrium. According to an embodiment of the present invention the catalyst is a catalytic enzyme. More preferably, the catalytic enzyme can be any one of the various carbonic anhydrases found in animals and plants.

(27) According to a yet preferred embodiment of the present invention, the filtered seawater 116 permeates freely back and forth across membrane 120 during its residence time in the reactor 118, rapidly establishing equilibrium between all species in Equation 1. Next, an air gap 124 above the filtered seawater 116 is partially evacuated by a vacuum pump through a port 126.

(28) Typically, the gases pumped out of the seawater in the air gap 124 of the reactor 118 will be a mixture of the major atmospheric gases: water vapor, CO2, nitrogen, oxygen and argon.

(29) According to a most preferred embodiment of the present invention, when silicone is used as the membrane material, the gases pumped out of the seawater will most likely be completely water vapor and CO.sub.2. These two gases can be easily separated, either by temperature or by adsorbents, so that once the water is stripped out, there should be no need for further gas separation before sequestration, although that always remains an option if desired.

(30) According to yet another preferred embodiment of the present invention, carbon dioxide and water are pulled out through the port 126 and are separated at a cooler 128, where the water condenses and is then directed to an output of the reactor 130 which typically leads out to sea. Next, the remaining CO.sub.2, preferably is pumped off to be compressed into cylinders ready for sequestration 132. In yet another preferred embodiment of the present invention a sequestration system that isolates the removed carbon dioxide to a location for at least one of storage and which can increase availability of renewable energy or non-fuel products (fertilizers and construction materials) and one or more energy sources that supply methods (heat) to the air extraction system to remove the carbon dioxide from the medium and which can regenerate it for continued used.

(31) In yet another embodiment of the present invention, additionally, pumps can be utilized.

(32) Referring now to FIG. 2, in yet another preferred embodiment of the present invention, a method 200 for separating and removing carbon dioxide from seawater is provided. Preferably the method uses the extraction system described in FIGS. 1A and 1B. First, seawater from the ocean is pumped into a system 210 comprising a reactor; and a membrane. In an alternative preferred embodiment of the present invention, the system can further comprise a catalyst. Next, the seawater is filtered to remove solids 212 resulting in filtered seawater followed by pumping the filtered seawater into a reactor 214. Next, the filtered seawater is exposed to a membrane 216. In a most preferred alternative embodiment of the present invention, when the catalyst is present; subjecting the filtered seawater to the catalyst 218. The next step, allowing the filtered seawater to flow back and forth across the membrane to establish equilibrium 220 forming an air gap above the filtered seawater, the air gap comprising gases including carbon dioxide and water vapor. Next, evacuating the air gap above the filtered seawater to remove the carbon dioxide and water vapor 222. Next, separating the carbon dioxide and water vapor at a cooler 224. Finally, sequestering the carbon dioxide and condensing the water vapor 226. In an alternative embodiment of the present invention, the method further includes a step of desalinating the filtered seawater.

(33) In a still further alternative embodiment of the present invention as shown in FIG. 1B, there is a system that includes a desalination reactor 140 that includes the preferred previously described system to remove carbon dioxide from seawater, such that the desalination reactor 140 removes carbon dioxide and is capable of producing fresh water. The desalination reactor can be built in by combining to the preferred described system.

(34) In order to facilitate system and reactor designs that do not rely solely on gravity to contain water, an alternate preferred embodiment of the present invention is disclosed. Referring now to FIG. 3 a schematic diagram illustrating an alternate system 300 to separate and remove carbon dioxide from a liquid, preferably seawater, is provided. According to an embodiment of the present invention, the system 300 comprises a reactor 302 which can be a shell; a membrane unit comprising a first inner membrane 304 layer and a second outer membrane 306 layer; and a catalyst 308. The first membrane 304 allows water and CO.sub.2 to flow back and forth between the region containing catalyst 308 and the region containing flowing water 316. The second membrane 306 allows CO.sub.2 to flow back and forth between the region containing flowing water 316 and the air gap 314 from which the carbon dioxide can be removed, separated and sequestered. Preferably, the first inner membrane 304 layer is comprised of a material permeable to both carbon dioxide and water. Preferably, the outer membrane 306 is comprised of a material permeable to carbon dioxide but not to water. Preferably, the inner membrane material comprises pores with sizes from about 4 angstroms to about 40 angstroms, while the outer membrane pore size is less than 4 angstroms. In a most preferred embodiment of the present invention, the system 300 converts bicarbonate ion into dissolved carbon dioxide to replace the carbon dioxide which is removed from the liquid.

(35) Typically, according to an embodiment of the present invention, the second outer membrane 306 layer completely encases and surrounds the first inner membrane 304 layer within the reactor 302. Preferably, the membrane 304, 306 layers are similar to those used in membrane degassers, through which liquids such as water and gases can flow.

(36) In a most preferred embodiment of the present invention, the first inner membrane 304 layer comprises a membrane material which is hydrophilic. Typically, the first inner membrane 304 layer can be made of any hydrophilic membrane material known to those skilled in the art, such as cellulose derivatives, polyamides, polyacrylonitrile, and polysulfones, among others. Preferably, the membrane material allows some of the gases to be pumped out more easily than others. More preferably, the first inner membrane 304 is capable of containing the catalyst 308, such that the catalyst 308 is not flushed out of the reactor 302 with the liquid 316 from which the carbon dioxide was removed.

(37) In yet another most preferred embodiment of the present invention, the first inner membrane 304 layer preferably is a cylindrical hydrophilic membrane, capped at both proximal end 310 and distal end 312 of the first inner membrane 304 cylinder; and contains a solution containing the catalyst 308 for more efficient and quicker re-establishment of equilibrium. Typically, the cap at the proximal end 310 is at the entrance 318a of reactor 302 where the liquid 316 enters, and the cap at the distal end 312 is at the exit of the reactor 302 where the liquid 316 without carbon dioxide exits 318b and flows out.

(38) Preferably, the first inner membrane 304 is impermeable to larger molecules such as enzymes and have pore sizes between about 4 and about 40 angstroms. According to an embodiment of the present invention, the pore size does not necessarily have to be uniform and can be random.

(39) In a most preferred embodiment of the present invention, the catalyst 308 is preferably contained within the first inner membrane 304 cylinder and retained within by both the cap at the proximal end 310 and the cap at the distal end 312 of the cylinder.

(40) Preferably, the catalyst 308 is a catalytic enzyme capable of boosting carbon-capture kinetics of bicarbonate. More preferably, the catalytic enzyme is carbonic anhydrase. In a most preferred embodiment of the present invention, any carbonic anhydrase known to those skilled in the art to speed up the formation of bicarbonate by a factor of 10.sup.7 can be used.

(41) In a most preferred embodiment of the present invention, the second outer membrane 306 layer comprises a membrane material which is hydrophobic. Typically, the second outer membrane 306 can be made of any hydrophobic membrane material known to those skilled in the art. Preferably, the membrane material allows some of the gases to be pumped out more easily than others. For example, silicone (polydimethylsiloxane) has a permeability coefficient that is much higher for CO.sub.2 than it is for nitrogen, oxygen or argon; only water moves through silicone more efficiently. More preferably, the second outer membrane 306 comprises a membrane material comprising silicone. In a most preferred embodiment of the present invention, the second outer membrane 306 is polydimethylsiloxane. Typically, when the first inner membrane 304 is cylindrical, the second outer membrane 306 layer can be cylindrical to completely surround first inner membrane 304.

(42) In a most preferred embodiment of the present invention, the liquid 316 is seawater. More preferably, the seawater is filtered.

(43) In a typical embodiment of the present invention, the reactor 302 further comprises an air gap 314 between second outer membrane layer 306 and reactor 302 shell. Preferably, the air gap 314 comprises dissolved gases from the seawater 316. Typically, the dissolved gases comprise carbon dioxide which can be collected 320 and removed via evacuation while under partial vacuum.

(44) According to an embodiment of the present invention, the liquid, (filtered seawater) 316 flows into the reactor chamber 302 into a space between first inner membrane 304 containing the catalyst 308, and second outer membrane 306. Typically, the reactor chamber 302 can be any reactor chamber which is a shell or tank known to those skilled in the art and FIG. 3 illustrates the simplest possible reactor chamber, although those in the art can appreciate that other embodiments of the present invention can use reactor 302 chambers with multiple channels with higher surface area. Preferably, the reactor 302 is a rigid and durable outer shell. Preferably, the higher the surface area, the greater the amount of CO.sub.2 can be removed. According to an embodiment of the present invention, the second outer membrane 306 layer holds the seawater in any desired orientation, allowing gases to pass out of the seawater 316 to vacuum 320. The structure of this portion of the reactor 302 can be duplicated many times in the system to maximize surface area.

(45) According to an embodiment of the present invention, typically, the system 300 can be a batch or continuous flow reactor. Preferably, the reactor 302 is a reactor chamber capable of holding liquid and capable of removing gases (for example, air) above the liquid (for example, seawater) by evacuation.

(46) According to a yet preferred embodiment of the present invention, the filtered seawater 316 is pumped from the ocean into the extraction system 300, and enters 318a the reactor 302 through a space between first inner membrane 304 and second outer membrane 306. The flowing filtered seawater 316 permeates freely back and forth across hydrophilic first inner membrane 304 so that the filtered seawater 316 is exposed to the catalyst 308 retained in the first inner membrane 304. During its residence time in the reactor 302, the filtered seawater 316 rapidly establishes equilibrium between all species in Equation 1. Next, the air gap 314 between an inner wall of the reactor 302 chamber and hydrophobic second outer membrane 306 exists to collect the gas mixtures from the filtered seawater 316 and is partially evacuated by a vacuum pump through a port 320. Typically, the gases pumped out of the seawater in the air gap 314 of the reactor 302 will be a mixture of the major atmospheric gases: water vapor, CO2, nitrogen, oxygen and argon.

(47) According to a most preferred embodiment of the present invention, when silicone is used as the second outer membrane 306 material, the gases pumped out of the filtered seawater into the air gap 314 will most likely be completely water vapor and carbon dioxide. These two gases can be easily separated by any separation known to those skilled in the art, for example, either by temperature (cooler) or by adsorbents; such that once the water is stripped out, there should be no need for further gas separation before sequestration, although that always remains an option if desired.

(48) According to a most preferred embodiment of the present invention, system 300 comprises reactor 302 comprising a rigid and durable outer shell surrounding and encasing a second outer hydrophobic membrane 306; surrounding and encasing a first inner hydrophilic membrane 304 capped at both ends 310, 312. The inner region contained by first inner hydrophilic membrane 304 and caps 310, 312 contains a catalyst 308. Seawater 316 flows into a middle region between first inner hydrophilic membrane 304 and second outer hydrophobic membrane 306. The flowing seawater 316 flows back and forth through hydrophilic membrane 304 so that seawater 316 is exposed to the catalyst 308, but the catalyst 308 cannot escape and is retained within the first inner hydrophilic membrane 304. Gases, carbon dioxide and water vapor are evacuated through port 320 and the remaining filtered seawater now depleted of carbon, exits through an output port 318b of the reactor which typically leads out to and can return to the sea.

(49) Thus, system 300, the inner region of reactor 302 contains both seawater 316 and catalyst 308. The middle region between second outer hydrophobic membrane 306 and first inner hydrophilic membrane 304 contains flowing seawater 316. The outer region air gap 314 between reactor 302 shell and second outer hydrophobic membrane 306 contains gases under partial vacuum. Seawater 316 enters at entrance 318a, experiences vacuum, and dissolved gasses depart through second outer hydrophobic membrane 306 to air gap 314. As the seawater 316 flows through the middle and inner region, catalyst 308 quickly reestablishes equilibrium (Equation 1) to generate more carbon dioxide gas, which permeates out through both membranes 304, 306 and evacuated at port 320. By the time seawater exits 318b, it has been depleted of carbon dioxide.

(50) Typically, the remaining CO.sub.2, can preferably be pumped off to be compressed into cylinders ready for sequestration. In yet another preferred embodiment of the present invention a sequestration system that isolates the removed carbon dioxide to a location for at least one of storage and which can increase availability of renewable energy or non-fuel products (fertilizers and construction materials) and one or more energy sources that supply methods (heat) to the air extraction system to remove the carbon dioxide from the medium and which can regenerate it for continued used.

(51) In yet another embodiment of the present invention, additionally, pumps can be utilized.

(52) Referring now to FIG. 4, in yet another preferred embodiment of the present invention, a method 400 for separating and removing carbon dioxide from a liquid is provided. Preferably the method uses the extraction system described in FIG. 3. In a preferred embodiment of the present invention, the liquid is seawater. More preferably, filtered seawater. First, the seawater from the ocean is pumped into a system 410 comprising a reactor; a first inner membrane containing a catalyst; and a second outer membrane. The seawater can be filtered to remove solids resulting in filtered seawater 412 prior to pumping the filtered seawater into a reactor 414. Next, the filtered seawater is exposed to a the first inner membrane containing the catalyst, and the second outer membrane 416 followed by subjecting the filtered seawater to the catalyst contained in the first inner membrane 418. The next step, allowing the filtered seawater to flow back and forth across the first inner membrane and the second outer membrane to establish equilibrium 420 forming an air gap above the filtered seawater, the air gap comprising gases including carbon dioxide and water vapor. Next, evacuating the air gap above the filtered seawater to remove the carbon dioxide and water vapor 422. Then, separating the carbon dioxide and water vapor at a cooler 424. Finally, sequestering the carbon dioxide and condensing the water vapor 426. In an alternative embodiment of the present invention, the method further includes a step of desalinating the filtered seawater.

(53) In still yet another embodiment of the present invention, the aforementioned system and methods can be scaled up and much more elaborate. For example, during membrane degassing, the surface area of the membrane interface can be greatly increased by use of multiple columns of the membrane polymer.

(54) In yet another embodiment of the present invention, the utilization of temperature control can be used to maximize the rate of degassing. As water is heated, the solubility of carbon dioxide decreases, so that more gas bubbles out.

(55) In still yet another embodiment of the present invention, methods for separation of the extracted carbon dioxide from the water vapor could be applied that would also be pumped out of the reactor.

(56) Referring to the system and methods in FIGS. 1A, 1B & 2, 3 and 4 according to embodiments of the present invention, the filtered seawater is subjected to a catalyst in the solution and the catalyst preferably is retained in the reactor by the membrane. Typically, according to an embodiment of the present invention, the low partial pressure causes dissolved CO.sub.2 to bubble out of the water, where it can be captured for sequestration. According to an embodiment of the present invention, addition of carbonic anhydrase forces the equilibrium to shift, decreasing bicarbonate concentrate to generate more dissolved CO.sub.2, which in turn is pumped out.

(57) According to an embodiment of the present invention, the cycle continues while the seawater is in the reactor. When the water is returned into the ocean, the water preferably has been depleted of both CO.sub.2 and bicarbonate, which causes it to absorb CO.sub.2 from the atmosphere to restore the equilibrium.

(58) According to yet another embodiment of the present invention, this method preferably requires an energy source. Preferably, the energy source is electrical. In order for the methods to create a net removal of CO.sub.2 from the ocean, preferably the reactor's electric power comes from carbon-free sources to ensure that the CO.sub.2 emitted during electrical power generation from the energy source is less than the amount of CO.sub.2 removed according to the methods of the present invention. Preferable carbon-free energy sources can be nuclear, solar, wind or hydroelectric. According to an embodiment of the present invention, reactors employing the methods of removing CO.sub.2 can be deployed to coastal areas that contract for clean energy or have their own dedicated solar panels.

(59) According to yet an alternative embodiment of the present invention, the aforementioned systems can be mounted aboard a ship. It is known to those skilled in the art that ocean vessels typically cool their engines with filtered seawater. The aforementioned systems can be installed in the filtered seawater streams of a ship such that carbon dioxide is removed from the seawater either before or after the water flows over the hot engines to cool them. Thus, any ocean vessel or ship that utilizes fossil fuels to operate its engines can therefore reduce its carbon footprint by installing the various embodiments of the systems and reactors for removing carbon dioxide described in the present invention.

(60) In summary, the present invention provides systems and methods to remove carbon dioxide from a liquid, preferably seawater, that is quick, efficient, not time consuming and inexpensive. Advantages of the system and methods according to preferred embodiments of the present invention over direct air capture methods since the preferred systems and methods disclosed utilizes the natural equilibrium already present in the environment. Typically, the concentration of carbon in seawater is much higher than in the air, and thus can be pulled out more efficiently. Natural equilibrium typically causes the ocean to absorb CO.sub.2 from the atmosphere if it is removed from seawater. The advantages of these preferred embodiments of the systems and methods of the present invention takes advantage of the already natural equilibrium occurring, over for example, electrochemical methods, since the methods and systems disclosed do not require energy to drive the chemical reaction. The methods and systems disclosed simply utilizes the natural equilibrium, accelerated by a natural catalyst, to separate the desired component, in this case carbon dioxide.

(61) Throughout the description and drawings, example embodiments are given with reference to specific configurations. It can be appreciated by those of ordinary skill in the art that the present invention can be embodied in other specific forms. Those of ordinary skill in the art would be able to practice such other embodiments without undue experimentation. The scope of the present invention, for the purpose of the present patent document, is not limited merely to the specific example embodiments or alternatives of the foregoing description.