CARBON DIOXIDE CONVERSION DEVICE

Abstract

A CO.sub.2 conversion device of the embodiment includes: a CO.sub.2 supply unit supplying CO.sub.2; a CO.sub.2 electrolysis unit including a cathode chamber supplied with CO.sub.2 from the CO.sub.2 supply unit and reducing and converting CO.sub.2 into CO and an anode chamber oxidizing substances to be oxidized to produce oxides; a fuel supply unit supplying fuel; an oxygen combustion power generation unit to which O.sub.2CO.sub.2-containing gas discharged from the anode chamber of the carbon dioxide electrolysis unit is supplied, the fuel is supplied from the fuel supply unit, and that combusts the O.sub.2CO.sub.2-containing gas; a condenser cooling and condensing water vapor-CO.sub.2-containing gas discharged from the oxygen combustion power generation unit; and a gas-liquid separator separating a water-CO.sub.2 two-phase fluid discharged from the condenser into water and CO.sub.2.

Claims

1. A carbon dioxide conversion device, comprising: a carbon dioxide supply unit that supplies carbon dioxide; a carbon dioxide electrolysis unit that includes a cathode chamber where carbon dioxide is supplied from the carbon dioxide supply unit and reduces and converts the carbon dioxide into carbon monoxide and an anode chamber that oxidizes substances to be oxidized to produce oxides; a fuel supply unit that supplies fuel; an oxygen combustion power generation unit to which oxygen-carbon dioxide-containing gas discharged from the anode chamber of the carbon dioxide electrolysis unit is supplied, the fuel is supplied from the fuel supply unit, and that combusts the oxygen-carbon dioxide-containing gas; a condenser that cools and condenses water vapor-carbon dioxide-containing gas discharged from the oxygen combustion power generation unit; and a gas-liquid separator that separates a water-carbon dioxide two-phase fluid discharged from the condenser into water and carbon dioxide.

2. The device according to claim 1, wherein the gas-liquid separator is configured to supply carbon dioxide separated from the water-carbon dioxide two-phase fluid to the cathode chamber of the carbon dioxide electrolysis unit.

3. The device according to claim 1, wherein the gas-liquid separator is configured to supply at least some of the separated water to the anode chamber of the carbon dioxide electrolysis unit as part of an electrolytic solution.

4. The device according to claim 1, wherein the oxygen combustion power generation unit includes a closed-cycle gas turbine, turbine combined cycle power generation, Graz cycle gas turbine, supercritical CO.sub.2 turbine, or oxy-fuel combustion device.

5. The device according to claim 4, wherein at least one of water and carbon dioxide produced by combustion and carbon dioxide in the oxygen-carbon dioxide-containing gas is supplied as a circulating medium for the oxygen combustion power generation unit.

6. The device according to claim 4, wherein at least one of water and carbon dioxide discharged from the gas-liquid separator is supplied as a circulating medium for the oxygen combustion power generation unit.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0004] FIG. 1 is a diagram illustrating a carbon dioxide conversion device of an embodiment.

[0005] FIG. 2 is a diagram illustrating gases produced by each unit and amounts of gases produced when hydrogen (H.sub.2) is used as fuel in the carbon dioxide conversion device of the embodiment.

[0006] FIG. 3 is a diagram illustrating gases produced by each unit and amounts of gases produced when methane (CH.sub.4) is used as fuel in the carbon dioxide conversion device of the embodiment.

[0007] FIG. 4 is a diagram illustrating gases produced by each unit and amounts of gases produced when carbon (C) is used as fuel in the carbon dioxide conversion device of the embodiment.

[0008] FIG. 5 is a diagram illustrating gases produced by each unit and amounts of gases produced when hydrogen (H.sub.2) and carbon monoxide (CO) are used as fuel in the carbon dioxide conversion device of the embodiment.

DETAILED DESCRIPTION

[0009] The carbon dioxide conversion device of the embodiment includes: a carbon dioxide supply unit that supplies carbon dioxide; a carbon dioxide electrolysis unit that includes a cathode chamber where carbon dioxide is supplied from the carbon dioxide supply unit and reduces and converts the carbon dioxide into carbon monoxide and an anode chamber that oxidizes substances to be oxidized to produce oxides; a fuel supply unit that supplies fuel; an oxygen combustion power generation unit to which oxygen-carbon dioxide-containing gas discharged from the anode chamber of the carbon dioxide electrolysis unit is supplied, the fuel is supplied from the fuel supply unit, and that combusts the oxygen-carbon dioxide-containing gas; a condenser that cools and condenses water vapor-carbon dioxide-containing gas discharged from the oxygen combustion power generation unit; and a gas-liquid separator that separates a water-carbon dioxide two-phase fluid discharged from the condenser into water and carbon dioxide.

[0010] Carbon dioxide conversion devices in embodiments will be described hereinafter with reference to the drawings. Substantially the same components are denoted by the same reference signs and explanation thereof may be omitted in some cases in the embodiments described below. The drawings are schematic, and a relationship between a thickness and a planar size, thickness proportions of the respective portions, and the like are sometimes different from actual ones. The ? symbol in the following explanation indicates a range between upper and lower limit values of the respective numerical values. In such cases, each numerical value range includes the upper and lower limit values.

[0011] FIG. 1 is a diagram illustrating a carbon dioxide conversion device of an embodiment. The carbon dioxide (CO.sub.2) conversion device 1 illustrated in FIG. 1 includes a CO.sub.2 supply unit 2 that supplies CO.sub.2; a CO.sub.2 electrolysis unit 5 that includes a cathode chamber 3 reducing and converting CO.sub.2 into carbon monoxide (CO) and an anode chamber 4 that oxidizes substances to be oxidized to produce oxides; a fuel supply unit 6 that supplies fuel; an oxygen combustion power generation unit 7 to which oxygen (O.sub.2)-carbon dioxide (CO.sub.2)-containing gas discharged from the anode chamber 4 of the CO.sub.2 electrolysis unit 2 is supplied, the fuel is supplied from the fuel supply unit 6, and that combusts the O.sub.2CO.sub.2-containing gas; a condenser 8 that cools and condenses water vapor (H.sub.2O)-carbon dioxide (CO.sub.2)-containing gas discharged from the oxygen combustion power generation unit 7; and a gas-liquid separator 9 that separates a water (H.sub.2O)-carbon dioxide (CO.sub.2) two-phase fluid discharged from the condenser 8 into water (H.sub.2O) and carbon dioxide (CO.sub.2).

[0012] As the CO.sub.2 supply unit 2, a device that recovers and supplies CO.sub.2 from carbon dioxide (CO.sub.2)-containing gas or a CO.sub.2 storage unit is used. For example, the CO.sub.2 supply unit 2 is configured to separate and recover CO.sub.2 from CO.sub.2-containing emission gas (CO.sub.2-containing gas) G1 emitted from thermal power plants, waste incineration plants, steel plants, and other plants, and supply CO.sub.2 gas G2 with increased CO.sub.2 concentration to the CO.sub.2 electrolysis unit 5. In such CO.sub.2 supply unit 2, for example, the following methods can be used: a chemical absorption method using a chemical absorbing liquid such as an amine aqueous solution, a physical absorption method using a physical absorbing liquid such as methanol or a polyethylene glycol solution, a solid absorption method using a solid absorbent such as an amine compound, a membrane separation method using a CO.sub.2 separation membrane, a physical adsorption method using zeolite or other inorganic substances as an absorber, a PSA (pressure swing adsorption) method, a TSA (thermal swing adsorption) method, and other methods. For example, in the chemical absorption method and a device using the amine aqueous solution, the emission gas G1 is supplied to an absorption tower where the amine aqueous solution is sprayed, and the amine aqueous solution that has absorbed CO.sub.2 is heated in a regeneration tower to recover CO.sub.2 emitted from the amine aqueous solution. The CO.sub.2 recovery methods and devices applied to the CO.sub.2 supply unit 2 are not limited, and various methods and devices that can recover CO.sub.2 from the emission gas G1 can be used.

[0013] The CO.sub.2 electrolysis unit 5 is a CO.sub.2 electrolytic device with an electrolysis cell and includes a cathode chamber (reduction portion) 3 and an anode chamber (oxidation portion) 4. The cathode chamber 3 includes a reduction electrode (cathode) and the anode chamber 4 includes an oxidation electrode (anode), and an electrolytic solution is circulated or filled in at least the anode chamber 4. In the cathode chamber 3, CO.sub.2 gas may be circulated or a CO.sub.2 containing electrolytic solution may be circulated or filled. In the cathode chamber 3 or anode chamber 4, the electrolytic solution is a solution using water (H.sub.2O), for example, an aqueous solution containing any electrolyte. Examples of the aqueous solutions containing electrolytes include aqueous solutions containing phosphate ions (PO.sub.4.sup.2-), borate ions (BO.sub.3.sup.3-), sodium ions (Na.sup.+), potassium ions (K.sup.+), calcium ions (Ca.sup.2+), lithium ions (Li.sup.+), cesium ions (Cs.sup.+), magnesium ions (Mg.sup.2+), chloride ions (Cl.sup.?), hydrogen carbonate ions (HCO.sub.3.sup.?), carbonate ions (CO.sub.3.sup.2-), hydroxide ions (OH.sup.?), and other ions. Concrete examples of the electrolytic solutions include alkaline aqueous solutions in which KOH, KHCO.sub.3, K.sub.2CO.sub.3, and the like are dissolved.

[0014] The cathode chamber 3 is supplied with the CO.sub.2 gas G2 from the CO.sub.2 supply unit 2. The cathode chamber 3 has a gas flow path facing the non-illustrated reduction electrode, and the CO.sub.2 gas is supplied to the gas flow path. The anode chamber 4 has a liquid flow path facing the non-illustrated oxidation electrode, and the electrolytic solution is supplied to the liquid flow path. A non-illustrated power supply is connected to the reduction and oxidation electrodes. The cathode chamber 3 and anode chamber 4 are separated from each other by a diaphragm 10 capable of moving ions such as hydrogen ions (H.sup.+), hydroxide ions (OH.sup.?), carbonate ions (CO.sub.3.sup.2-), hydrogen carbonate ions (HCO.sub.3.sup.?), and other ions, for example, an ion exchange membrane. The CO.sub.2 electrolysis unit 5 may be a single electrolysis cell, have a structure in which the single electrolysis cells are connected in a plane direction, or a stack structure in which a plurality of electrolysis cells are stacked and integrated.

[0015] In the cathode chamber 3 and anode chamber 4 of the CO.sub.2 electrolysis unit 5, the following reactions occur. In the cathode chamber 3, an electrolytic reaction and reduction reaction of CO.sub.2 occur as shown in formula (1) below. In the cathode chamber 3, the reduction reaction of CO.sub.2 produces CO and carbonate ions (CO.sub.3.sup.2-).

2CO.sub.2+2e.sup.?.fwdarw.CO+CO.sub.3.sup.2-(1)

[0016] The carbonate ions (CO.sub.3.sup.2-) produced in the cathode chamber 3 move to the anode chamber 4 through the diaphragm 10. In the anode chamber 4, as shown in formula (2) below, an oxidation reaction of the carbonate ions (CO.sub.3.sup.2-) produced in the cathode chamber 3 and moved through the diaphragm 10 occurs, resulting in production of CO.sub.2 and O.sub.2.

CO.sub.3.sup.2-.fwdarw.CO.sub.2+0.5O.sub.2+2e.sup.?(2)

[0017] Furthermore, in the cathode chamber 3, the electrolytic reaction (reduction reaction) of H.sub.2O in the electrolytic solution occurs simultaneously with the electrolytic reaction (reduction reaction) of CO.sub.2, producing hydrogen (H.sub.2) and hydroxide ions (OH.sup.?), as shown in formula (3) below.

2H.sub.2O+2e.sup.?.fwdarw.H.sub.2+2OH.sup.?(3)

[0018] The hydroxide ions (OH) produced in the cathode chamber 3 move to the anode chamber 4 through the diaphragm 10. Water (H.sub.2O) and oxygen (O.sub.2) are then produced in the anode chamber 4, as shown in formula (4) below.

2OH.sup.?.fwdarw.0.5O.sub.2+H.sub.2O+2e.sup.?(4)

[0019] In the anode chamber 4, water (H.sub.2O) in the electrolytic solution is electrolyzed to produce oxygen (O.sub.2) and hydrogen ions (H.sup.+), as shown in formula (5) below.

2H.sub.2O.fwdarw.4H.sup.++O.sub.2+4e.sup.?(5)

[0020] The produced hydrogen ions (H.sup.+) move to the cathode chamber 3 through the diaphragm 10. In the cathode chamber 3 where hydrogen ions (H.sup.+) reach and electrons (e.sup.?) reach through external circuits, hydrogen is generated by the reaction shown in formula (6) below.

4H.sup.++4e.sup.?.fwdarw.2H.sub.2(6)

[0021] In the cathode chamber 3, CO is produced by the reduction reaction of CO.sub.2 as shown in formula (1), and H.sub.2 is produced by the electrolytic reaction of H.sub.2O as shown in formula (3) and the reaction shown in formula (6). CO and H.sub.2 produced in the cathode chamber 3 are discharged from the cathode chamber 3 together with unreacted CO.sub.2. Mixed gas G3 containing CO and H.sub.2, and CO.sub.2 discharged from the cathode chamber 3 is supplied to an organic synthesis unit 11, for example, as part of source gas for an organic synthesis reaction. Hydrogen (H.sub.2) is supplied to the organic synthesis unit 11 as needed, in addition to the mixed gas G3 containing CO and H.sub.2, as part of the source gas for the organic synthesis reaction.

[0022] In the organic synthesis unit 11, the organic synthesis reactions are performed, for example, using the Fischer-Tropsch synthesis reaction to synthesize hydrocarbons, alcohols, and other organic substances, for example. Concrete examples of the organic substances synthesized in the organic synthesis unit 11 include carbon-containing liquid fuels, or the like. The products (organic substances) of the organic synthesis unit 11 are discharged from the organic synthesis unit 11 and sent, for example, to a separately installed tank or other storage facility (not illustrated).

[0023] Meanwhile, in the anode chamber 4 of the CO.sub.2 electrolysis unit 5, oxygen (O.sub.2) and carbon dioxide (CO.sub.2) are produced by oxidation of carbonate ions (CO.sub.3.sup.2-) and hydroxide ions (OH.sup.?), as shown in formulas (2) and (4) above. The gas containing O.sub.2 and CO.sub.2 (O.sub.2CO.sub.2-containing gas) produced in the anode chamber 4 is discharged from the anode chamber 4 together with the electrolytic solution. An electrolytic solution VL1 containing the O.sub.2CO.sub.2-containing gas is sent to a first gas-liquid separation unit 12, which is connected to a discharge pipe of the anode chamber 4, and O.sub.2CO.sub.2-containing gas G4 is separated from the electrolytic solution. The separated electrolytic solution is returned to the anode chamber 4, though not illustrated. Since a CO.sub.2 concentration of the separated O.sub.2CO.sub.2-containing gas G4 is as high as 60 volume % or more, effective utilization of CO.sub.2 would be hindered when the gas G4 is directly released into the atmosphere. Furthermore, since the O.sub.2CO.sub.2-containing gas G4 contains a relatively large amount of O.sub.2, operation and function of the CO.sub.2 electrolysis unit 5 will be degraded when it is sent directly to the cathode chamber 3. The O.sub.2CO.sub.2-containing gas G4 discharged from the anode chamber 4 of the CO.sub.2 electrolysis unit 5 and separated and recovered in the first gas-liquid separation unit 12 is sent to the oxygen combustion power generation unit 7.

[0024] Closed-cycle gas turbines, turbine combined cycle power generation, Graz cycle gas turbines, supercritical CO.sub.2 turbines, oxy-fuel combustion devices, and the like can be used as the oxygen combustion power generation unit 7. These can efficiently combust and consume O.sub.2 in the O.sub.2CO.sub.2-containing gas using hydrogen or the like as fuel, and can also efficiently operate gas turbines or the like based on combustion, so that electric power can be generated using O.sub.2 in the O.sub.2CO.sub.2-containing gas as an oxidant. The electric power generated by the oxygen combustion power generation unit 7 can be used as part of operating power of the CO.sub.2 electrolysis unit 5.

[0025] To combust and consume the O.sub.2CO.sub.2-containing gas in a combustion reaction in the oxygen combustion power generation unit 7, fuel is supplied to the oxygen combustion power generation unit 7 from the fuel supply unit 6 in addition to the O.sub.2CO.sub.2-containing gas G4. The fuel supplied from the fuel supply unit 6 is not limited, and may be any of hydrogen (H.sub.2), carbon (C), carbon monoxide (CO), and lower hydrocarbons such as methane (CH.sub.4). The fuel supply unit 6 may be an oxygen-blown gasification furnace or the like. The fuel supplied from the fuel supply unit 6 is preferably supplied in an equivalent ratio to O.sub.2 in the O.sub.2CO.sub.2 containing gas. In the oxygen combustion power generation unit 7, O.sub.2 is converted into H.sub.2O or CO.sub.2. For example, when hydrogen (H.sub.2) is supplied as the fuel, H.sub.2O is produced. When carbon (C) or carbon monoxide (CO) is supplied as the fuel, CO.sub.2 is produced. The same is true when methane (CH.sub.4) or other fuels are supplied, and H.sub.2O and CO.sub.2 are produced. The produced CO.sub.2 is recovered simultaneously with CO.sub.2 in the O.sub.2CO.sub.2-containing gas.

[0026] When the closed-cycle gas turbines, turbine combined cycle power generation, Graz cycle gas turbines, supercritical CO.sub.2 turbines, oxy-fuel combustion devices, and the like are used as the oxygen combustion power generation unit 7, simply supplying fuel for combustion will result in higher temperatures in the oxygen combustion power generation unit 7. In contrast, using the produced H.sub.2O (for example, water vapor) or CO.sub.2 as a circulating medium can suppress the temperature rise of the oxygen combustion power generation unit 7. For example, H.sub.2O and CO.sub.2 are used as the circulating media in the closed-cycle gas turbines, turbine combined cycle power generation, and Graz cycle gas turbines. In the supercritical CO.sub.2 turbines and oxy-fuel combustion devices, CO.sub.2 is used as the circulating medium. These allow the oxygen combustion power generation unit 7 to operate safely and efficiently.

[0027] H.sub.2O (water vapor)-CO.sub.2-containing gas G5 is discharged from the oxygen combustion power generation unit 7. The H.sub.2O (water vapor)-CO.sub.2-containing gas G5 is sent to the condenser 8 to be cooled and water vapor (H.sub.2O) is condensed to be converted into water. A water (H.sub.2O)-carbon dioxide (CO.sub.2) two-phase fluid VL2 containing water from the condensation of water vapor (H.sub.2O) is discharged from the condenser 8. The H.sub.2OCO.sub.2 two-phase fluid VL2 is sent to a second gas-liquid separator 9. In the second gas-liquid separator 9, water in the H.sub.2OCO.sub.2 two-phase fluid VL2 is separated. At least some of the separated water (H.sub.2O) may be used as part of the electrolytic solution supplied to the anode chamber 4 of the CO.sub.2 electrolysis unit, or may be returned to the oxygen combustion power generation unit 7 as the circulating medium. CO.sub.2 gas G6 separated in the second gas-liquid separator 9 is sent to a gas mixer 13. The gas mixer 13 is connected to the cathode chamber 3 of the CO.sub.2 electrolysis unit 5. In the gas mixer 13, the CO.sub.2 gas G6 separated in the second gas-liquid separator 9 is mixed with the CO.sub.2 gas G2 and supplied to the cathode chamber 3. At least one of the water and CO.sub.2 discharged from the second gas-liquid separator 9 may be used as the circulating medium in the oxygen combustion power generation unit 7.

[0028] As described above, the CO.sub.2 gas that is produced as a by-product in the anode chamber 4 and separated in the second gas-liquid separator 9 can be returned to the cathode chamber 3 of the CO.sub.2 electrolysis unit 5, with operation failure and functional degradation and the like in the cathode chamber 3 under control, by combusting the O.sub.2CO.sub.2-containing gas G4 discharged from the anode chamber 4 of the CO.sub.2 electrolysis unit 5 in the oxygen combustion power generation unit 7 to convert O.sub.2 in the O.sub.2CO.sub.2-containing gas G4 into H.sub.2O and CO.sub.2. Furthermore, O.sub.2 in the O.sub.2CO.sub.2-containing gas G4 can be regenerated as CO.sub.2. These features make it possible to reduce release of CO.sub.2 into the atmosphere in the carbon dioxide conversion device 1, increase an effective utilization rate of CO.sub.2, and improve device utilization efficiency.

[0029] FIG. 2 to FIG. 5 each illustrate a relationship between a type of fuel used in the carbon dioxide conversion device 1 of the embodiment and an amount of gas produced in each unit. FIG. 2 a diagram illustrating the amount of gas produced in each unit when hydrogen (H.sub.2) is used as fuel in the carbon dioxide conversion device 1 of the embodiment. FIG. 3 is a diagram illustrating the amount of gas produced in each unit when methane (CH.sub.4) is used as fuel in the carbon dioxide conversion device 1 of the embodiment. FIG. 4 is a diagram illustrating the amount of gas produced in each unit when carbon (C) is used as fuel in the carbon dioxide conversion device 1 of the embodiment. FIG. 5 is a diagram illustrating the amount of gas produced in each unit when hydrogen (H.sub.2) and carbon monoxide (CO) are used as fuel in the carbon dioxide conversion device 1 of the embodiment. In these figures, the numeric values in each unit indicate the volume of the target gas. In cases of using either fuel, CO.sub.2 can be effectively utilized.

[0030] Some of the water discharged from the second gas-liquid separator 9 may be supplied to the CO.sub.2 electrolysis unit 5. Although not illustrated, some of the water and CO.sub.2 recovered in the second gas-liquid separator 9 can be used as the circulating medium in the oxygen combustion power generation unit 7. Although not illustrated, there are pumps, compressors, blowers, control devices, and other devices to supply fluid between each piece of equipment. To avoid residual oxygen in CO.sub.2 released from the second gas-liquid separator 9, a fuel/oxygen ratio in the oxygen combustion power generation unit 7 is preferably set slightly larger than the equivalent ratio to prevent residual oxygen. Alternatively, a catalytic combustor may be installed upstream or downstream of the second gas-liquid separator 9 to react the residual oxygen with hydrogen or the like. Pt and Pd are used as combustion catalysts.

[0031] The configurations in the embodiments can be applied in combination and partially replaced. While certain embodiments of the present invention have been described herein, these embodiments have been presented by way of example only, and are not intended to limit the scope of the inventions. The embodiments described herein may be embodied in a variety of other forms; furthermore, various omissions, substitutions, and changes may be made without departing from the spirit of the inventions. The embodiments and modifications fall within the scope and spirit of the inventions and fall within the scope of the inventions as set forth in claims and their equivalents.