System for capturing CO2 from a fuel cell

Abstract

A carbon dioxide capture system for capturing carbon dioxide from an exhaust stream. The system may include a fuel cell configured to output a first exhaust stream comprising carbon dioxide and water. The system may further include an electrolyzer cell configured to receive a first portion of the first exhaust stream and output a second exhaust stream comprising oxygen and carbon dioxide. The fuel cell may be a solid oxide fuel cell. The electrolyzer cell may be a molten carbonate electrolysis cell.

Claims

1. A carbon dioxide capture system for capturing carbon dioxide from an exhaust stream comprising: a fuel cell configured to output a first exhaust stream comprising carbon dioxide and water; an electrolyzer cell comprising an anode and a cathode, wherein the anode of the electrolyzer cell is configured to receive a first portion of the first exhaust stream, and the cathode of the electrolyzer cell is configured to output a second exhaust stream comprising oxygen and carbon dioxide; and a gas oxidizer configured to receive a second portion of the first exhaust stream and the second exhaust stream from the cathode of the electrolyzer cell, and output a third exhaust stream comprising water and carbon dioxide.

2. The system according to claim 1, wherein the fuel cell is a solid oxide fuel cell.

3. The system according to claim 1, wherein the electrolyzer cell is a molten carbonate electrolysis cell.

4. The system according to claim 1, wherein the first exhaust stream further comprises hydrogen and carbon monoxide.

5. The system according to claim 1, wherein the fuel cell is configured to internally reform a fuel supplied to the fuel cell to produce hydrogen.

6. The system according to claim 1, wherein the electrolyzer cell is further configured to output a fourth exhaust stream comprising a high purity hydrogen gas.

7. The system according to claim 6, wherein the fourth exhaust stream comprises at least 90% hydrogen gas.

8. The system according to claim 1, wherein the fuel cell comprises an anode and a cathode, and wherein the anode of the fuel cell is configured to receive a fuel and output the first exhaust stream.

9. The system according to claim 8, wherein the anode of the fuel cell is further configured to receive a third portion of the first exhaust stream.

10. The system according to claim 8, wherein the fuel is natural gas.

11. The system according to claim 8, wherein the cathode of the fuel cell is configured to receive an air stream.

12. The system according to claim 6, wherein the anode of the electrolyzer cell is further configured to output the fourth exhaust stream.

13. The system according to claim 1, wherein the first portion of the first exhaust stream supplied to the electrolyzer cell is in an amount such that the oxygen present in the second exhaust stream is approximately equal to the stoichiometric amount needed to convert hydrogen, carbon monoxide, and methane present in the second portion of the first exhaust stream to carbon dioxide and water present in the third exhaust stream.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) FIG. 1 shows a schematic view of a CO.sub.2 capture system for a solid oxide fuel cell, according to one embodiment of the present invention.

(2) FIG. 2 shows a detailed, schematic view of a reformer-electrolyzer-purifier used in the CO.sub.2 capture system of FIG. 1.

(3) FIG. 3 is a table showing components of gas streams within the CO.sub.2 capture system of FIG. 1.

DETAILED DESCRIPTION

(4) Referring generally to the figures, disclosed herein is a CO.sub.2 capture system for capturing highly purified CO.sub.2 from an anode exhaust stream produced by a fuel cell that is both less costly and highly efficient in terms of energy production.

(5) FIG. 1 shows a CO.sub.2 capture system 100 for removing carbon dioxide from an anode exhaust stream produced by a fuel cell. As shown in FIG. 1, a hydrocarbon fuel, such as natural gas, is supplied to the system 100 through a fuel supply line 110. The fuel stream is first directed through a gas cleanup station 10, which removes impurities contained in the fuel stream that may be harmful to the fuel cell. The cleaned fuel stream is then mixed with an anode exhaust recycle stream (third portion of a first exhaust stream) from an anode 174 of a fuel cell 170, which is supplied by a return line 132 and will be described in more detail below. This recycle stream provides water to the fuel to prevent carbon formation and also increases the fuel-cell efficiency. In the embodiment shown in FIG. 1, the fuel cell 170 is configured as a solid oxide fuel cell (SOFC). The fuel cell 170 may be capable of internally reforming the mixed fuel stream by converting methane and water to hydrogen and carbon dioxide. Alternatively, the system 100 may incorporate an external reformer to reform the mixed fuel stream before being introduced into the fuel cell 170. In addition, the fuel cell 170 may comprise a plurality of unit cells connected to form a fuel cell stack.

(6) The mixed fuel stream, containing the hydrocarbon fuel and anode exhaust, is directed through the fuel supply line 110 by a first blower 50, where, after being heated by a first heat exchanger 20, the mixed fuel stream is supplied to the anode 174 of the SOFC 170 to facilitate the electrochemical reactions needed for the production of electricity.

(7) As further shown in FIG. 1, an air stream is supplied to the system 100 through an air supply line 120, where it is directed by a second blower 30 through a second heat exchanger 40. The air stream is heated by the second heat exchanger 40 and continues through the air supply line 120 to a third heat exchanger 60 to be heated further. After passing through the third heat exchanger 60, the air supply line 120 supplies the hot air stream to a cathode 172 of the SOFC 170. As described above, the mixed fuel stream supplied to the anode 174 and the air stream supplied to the cathode 172 facilitate internal reactions that result in the transfer of negatively charged oxygen ions across the solid oxide electrolyte layer of the SOFC 170 such that electricity may be produced. After completion of the reactions, the cathode 172 outputs a cathode exhaust stream containing oxygen-depleted air, which is vented out of the system 100 via a cathode exhaust line 140. Waste heat from the cathode exhaust stream is used by the second heat exchanger 40 to warm the air stream 120 that will be supplied to the cathode 172.

(8) At the anode 174, an anode exhaust stream (first exhaust stream) is produced. The anode exhaust stream largely contains carbon dioxide, water, and unreacted hydrogen gas, which is carried from the solid oxide fuel cell 174 and split into two streams that flow through a reformer-electrolyzer-purifier (REP) supply line 130 (first portion of the first exhaust stream) and an anode gas oxidizer (AGO) supply line 131 (second portion of the first exhaust stream). As further shown in FIG. 1, at least a portion of the anode exhaust stream (third portion of the first exhaust stream) flows through the return line 132 to be mixed with the fuel stream supplied by the fuel supply line 110. The flow ratio of the anode exhaust stream to the REP supply line 130 and the anode exhaust stream to the AGO supply line 131 is controlled so that the amount of H2 and O2 in the exhaust gas from the AGO 190 (described below) is minimized. For example, in certain embodiments, the portion of the anode exhaust stream supplied to the REP supply line 130 is controlled such that the amount of oxygen produced in the exhaust stream (second exhaust stream) outputted by the REP 180 is approximately equal, or equal to, the stoichiometric amount needed to convert the hydrogen, carbon monoxide, and methane present in the portion of the anode exhaust stream supplied to the AGO supply line 131 to carbon dioxide and water, minimizing the impurities present in the carbon dioxide captured in the exhaust gas from the AGO 190 (third exhaust stream). In addition, although not shown in FIG. 1, in some embodiments, additional methane is burned in a separate oxidizer with air in order to achieve improved heat balance in the overall system.

(9) FIG. 2 shows a detailed, schematic view of the REP 180. The REP 180 is capable of internally reforming and purifying hydrogen from fuel, which can later be used for the production of electricity. An example of an REP system is described in greater detail in International Patent Application No. PCT/US2015/013837, which is incorporated by reference herein in its entirety. In the embodiment shown in FIG. 2, the REP 180 is configured as an electrolyzer cell, such as a molten carbonate electrolysis cell (MCEC). The REP 180 may comprise a plurality of individual cells to form an REP stack. As shown in FIG. 2, the REP 180 generally comprises the anode 184, which includes a catalyst layer 181a, an electrolyte layer 183, the cathode 182, which includes a catalyst layer 181b, and a power supply 186 configured to apply a voltage to the anode 184 and cathode 182.

(10) The anode exhaust stream from the SOFC 170 is supplied to the anode 184 through the anode exhaust line 130. The anode exhaust stream largely contains water, hydrogen gas, carbon dioxide, and small amounts of carbon monoxide and methane. In some embodiments, a small amount of additional methane (not shown) is added to the exhaust stream supplied to the REP 180 to obtain the desired heat balance in the system. During an internal reforming reaction driven by the catalyst layer 181a, water reacts with methane to produce hydrogen and carbon dioxide. Because the methane contained in the anode exhaust stream is present in residual amounts due to the reforming reaction that occurred in the SOFC 170, minimal reforming of the anode exhaust stream is required. In addition, during an internal gas-shift reaction, water reacts with carbon monoxide to produce additional hydrogen and carbon dioxide.

(11) As further shown in FIG. 2, during an electrolysis/CO.sub.2 pump reaction, water, carbon dioxide, and electrons supplied by the power supply 186 react to produce hydrogen, carbonate ions CO.sub.3.sup.=, and residual heat. The residual heat facilitates the internal reforming and gas-shift reactions described above. The hydrogen produced by the reactions in the anode 184 is purified by the transfer of almost all of the carbon from the gas as carbonate ions flowing to the cathode 182 across the electrolyte layer 183. The high purity hydrogen gas is removed as a hydrogen supply stream (fourth exhaust stream) from the REP 180 through a hydrogen supply line 150, which may then be recycled back to the SOFC 170 to reduce fuel needs for energy production or exported and stored as a separate product stream. In some embodiments, the anode exhaust stream comprises at least 90% hydrogen. In certain embodiments, the anode exhaust stream comprises at least 98% hydrogen.

(12) As noted above, the carbonate ions produced by the electrolysis/CO.sub.2 pump reaction are transferred from the anode 184 to the cathode 182 via the electrolyte layer 183. At the cathode 182, the carbonate ions separate to produce oxygen, carbon dioxide, and electrons. These electrons complete the circuit with the power supply 186 and return to the anode 184. The oxygen and carbon dioxide produced from the carbonate ions are removed from the REP 180 through an REP cathode exhaust line 135. Thus, the transfer of the carbonate ions together with the subsequent reaction at the cathode 182 has the effect of pumping carbon dioxide together with pure oxygen gas out of the anode exhaust stream.

(13) As shown in FIG. 1, the REP cathode exhaust line 135 carries the REP exhaust stream containing oxygen and carbon dioxide to an AGO 190. In addition, as described above, a portion of the anode exhaust stream from the SOFC 170, containing carbon dioxide, hydrogen, and water, is also supplied to the AGO 190 via the AGO supply line 131. Here, the oxygen contained within the REP cathode exhaust stream facilitates the oxidation of the anode exhaust stream such that carbon dioxide, along with water, may be removed from the system 100 via a removal line 160 in the form of an AGO exhaust stream. As the AGO exhaust stream is removed, it is first cooled by the third exchanger 60 and subjected to additional cooling (not shown) so that water may be condensed out of the AGO exhaust stream and carbon dioxide in a highly purified concentration can be obtained for storage purposes. In some embodiments, carbon dioxide may be removed in concentrations of at least 95%.

(14) FIG. 3 is a table showing the compositions of the various gas streams present in the carbon dioxide capture system 100, according to one embodiment of the present invention. Each column 1-6 corresponds to the composition of the gas stream present at points 1-6 shown in FIG. 1. As shown in column 1, the hydrocarbon fuel supplied to the SOFC 170 contains mainly methane, with residual amounts of carbon dioxide and water. After producing electrical energy in the SOFC 170, the anode exhaust stream to the REP 180 now contains a much larger amount of carbon dioxide, along with water and hydrogen, as shown in column 3. As shown in column 4 of the table, hydrogen is capable of being extracted at over 90 mole percent purity due to the reactions within the REP 180, providing highly useful feed supplies for the SOFC 170 or additional external energy systems. As shown in column 5, the exhaust from the AGO 190 contains a higher concentration of carbon dioxide (e.g., at least 44 mole percent), compared to the anode exhaust stream fed to the REP 180, together with water and trace amounts of nitrogen. At this point, water may be easily condensed out of the AGO exhaust stream to produce dry carbon dioxide in a highly purified form of about 99 mole percent, as shown in column 5a. In addition, as shown in column 6, the exhaust vented out of the system 100 from the cathode 172 of the SOFC 170 contains mostly nitrogen gas and a minimal amount of carbon dioxide (e.g., less than 1 mole percent).

(15) The CO.sub.2 capture system described herein provides a highly efficient and cost-effective method for removing carbon dioxide from an anode exhaust stream produced by a fuel cell, in particular a solid oxide fuel cell. By incorporating an electrolyzer cell in the form of an REP, a stream containing carbon dioxide and oxygen gas necessary to facilitate the removal of pure carbon dioxide from the anode exhaust stream can be produced. In addition, as a byproduct of this process, a valuable, exportable high purity hydrogen stream is produced, increasing the energy output of the system as a whole, thereby offsetting most of the energy needed to drive the removal system. Thus, a fuel cell system may be provided where clean, reliable energy is supplied and harmful CO.sub.2 emissions are minimized.

(16) As utilized herein, the terms approximately, about, substantially, and similar terms are intended to have a broad meaning in harmony with the common and accepted usage by those of ordinary skill in the art to which the subject matter of this disclosure pertains. It should be understood by those of skill in the art who review this disclosure that these terms are intended to allow a description of certain features described and claimed without restricting the scope of these features to the precise numerical ranges provided. Accordingly, these terms should be interpreted as indicating that insubstantial or inconsequential modifications or alterations of the subject matter described and claimed are considered to be within the scope of the invention as recited in the appended claims.

(17) The terms coupled, connected, and the like as used herein mean the joining of two members directly or indirectly to one another. Such joining may be stationary (e.g., permanent) or moveable (e.g., removable or releasable). Such joining may be achieved with the two members or the two members and any additional intermediate members being integrally formed as a single unitary body with one another or with the two members or the two members and any additional intermediate members being attached to one another.

(18) References herein to the positions of elements (e.g., top, bottom, above, below, etc.) are merely used to describe the orientation of various elements in the Figures. It should be noted that the orientation of various elements may differ according to other exemplary embodiments, and that such variations are intended to be encompassed by the present disclosure.

(19) It is important to note that the construction and arrangement of the various exemplary embodiments are illustrative only. Although only a few embodiments have been described in detail in this disclosure, those skilled in the art who review this disclosure will readily appreciate that many modifications are possible (e.g., variations in sizes, dimensions, structures, shapes and proportions of the various elements, values of parameters, mounting arrangements, use of materials, colors, orientations, etc.) without materially departing from the novel teachings and advantages of the subject matter described herein. For example, elements shown as integrally formed may be constructed of multiple parts or elements, the position of elements may be reversed or otherwise varied, and the nature or number of discrete elements or positions may be altered or varied. The order or sequence of any process or method steps may be varied or re-sequenced according to alternative embodiments. Other substitutions, modifications, changes and omissions may also be made in the design, operating conditions and arrangement of the various exemplary embodiments without departing from the scope of the present invention. For example, the heat recovery heat exchangers may be further optimized.