Solid oxide fuel cell catalytic converter
11101482 · 2021-08-24
Assignee
Inventors
Cpc classification
H01M8/1233
ELECTRICITY
Y02E60/50
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
Y02T90/40
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
H01M2250/20
ELECTRICITY
International classification
H01M8/06
ELECTRICITY
H01M8/1233
ELECTRICITY
Abstract
A dual chamber solid oxide fuel cell integrated into the exhaust stream of an internal combustion engine, in which engine exhaust gases are routed to the anode of a tubular solid oxide fuel cell (SOFC) and heated secondary air is supplied to the cathode of the SOFC. The secondary air supply is heated using the existing engine temperature and exhaust gas temperature through a heat exchanger formed by a modified cylinder head and exhaust manifold. The dual chamber solid oxide fuel provides the necessary hydrocarbon and carbon monoxide scrubbing to achieve mandatory catalytic conversion for vehicle operation. In addition, the dual chamber solid oxide fuel cell is capable of generating sufficient electrical power for the vehicle. Omission of conventional catalytic convertors and alternators allows for improved efficiency and fuel economy of the internal combustion engine.
Claims
1. An apparatus for reducing engine emissions, comprising: a stack of fuel cells defining a first chamber, wherein each fuel cell comprises a tube having an anode positioned on an inside the tube and a cathode positioned on an outside the tube; a first port coupled to the first chamber for delivering a quantity of engine exhaust to the inside of the tubes; a second chamber enclosing the outside of each of the tubes and coupled to the inside of the tubes such that all of the quantity of engine exhaust that has passed through the insides of the tubes will contact the cathodes of the tubes; a second port coupled to the second chamber for delivering a quantity of fresh air to the cathodes of the tubes; and an exhaust coupled to the second chamber for exhausting the engine exhaust after it has contacted the cathodes of the tubes.
2. The apparatus of claim 1, further comprising a manifold coupled to the first port and the second port.
3. The apparatus of claim 2, wherein the manifold comprises a first portion in communication with the first port and configured to collect engine exhaust from an engine and a second portion coupled to the second port and configured to receive fresh air.
4. The apparatus of claim 3, wherein the first portion and the second portion are positioned proximately to each other such that any fresh air passing through the second portion will be warmed by any exhaust gas in the first portion.
5. The apparatus of claim 4, wherein the manifold is configured to be coupled to an engine block.
6. The apparatus of claim 5, wherein the manifold is configured as a single block having passages formed therethrough to define the first portion and the second portion.
7. A method of reducing engine emissions, comprising the steps of: providing a first chamber defined by a stack of fuel cells, each of which comprises a tube having an anode positioned on an inside the tube and a cathode positioned on an outside the tube; passing a quantity of engine exhaust through the inside of the tubes so that the engine exhaust contacts the anodes of the tubes; collecting the engine exhaust from the inside of the tubes and passing all of the quantity of the engine exhaust over the outside of the tubes in a second chamber so that the engine exhaust contacts the cathodes of the tubes; delivering a quantity of fresh air to the second chamber; and exhausting the engine exhaust from the second chamber after the engine exhaust has contacted the cathodes.
8. The method of claim 7, further comprising a manifold coupled to the first port and the second port.
9. The method of claim 8, wherein the manifold comprises a first portion in communication with the first port and configured to collect engine exhaust from an engine and a second portion coupled to the second port and configured to receive fresh air.
10. The method of claim 9, wherein the first portion and the second portion are positioned proximately to each other such that any fresh air passing through the second portion will be warmed by any exhaust gas in the first portion.
11. The method of claim 10, wherein the manifold is configured to be coupled to an engine block.
12. The method of claim 11, wherein the manifold is configured as a single block having passages formed therethrough to define the first portion and the second portion.
Description
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWING(S)
(1) The present invention will be more fully understood and appreciated by reading the following Detailed Description in conjunction with the accompanying drawings, in which:
(2)
(3)
(4)
(5)
(6)
(7)
(8)
DETAILED DESCRIPTION OF THE INVENTION
(9) Referring to the figures, wherein like numeral refer to like parts throughout, there is seen in
(10) Referring to
(11) This arrangement provides a highly efficient, dual chambered design for fuel cell stack 16 that can deliver larger power outputs. Electrical power may be carried away from fuel cell stack 16 using conventional fuel cell circuitry to provide electrical energy to the vehicle and/or charge the battery of the vehicle. As described below, the use of the additional heat contained within the exhaust as it exits exhaust manifold 14 may provide the thermal energy needed for high SOFC performance.
(12) Referring to
(13) Referring to
(14) As an alternative, there is seen in
(15) As seen in
(16) The exhaust gas provided through the tubular anodes of the fuel cells thus acts as the primary fuel source for the SOFC. At the anodes of the fuel cells, any unburned hydrocarbons, H.sub.2, and CO are reacted into water and carbon dioxide, while generating electrical energy. The exhaust gas, upon exiting the tubular anode of the SOFC, is recycled to the cathode side of the SOFC. The SOFC cathode layer is able to react NOx in lean conditions and will decompose NOx into N.sub.2, allowing the oxygen ions to travel through the electrolyte layer to react with particulate carbon, CO, H.sub.2, or hydrocarbons present on the anode layer. The exhaust gas then leaves the cathode side of the fuel cell stack and travels out of the tailpipe to the atmosphere.
(17) The omission of the catalytic convertor will increase the thermal efficiency of the internal combustion engine, and thus increase fuel economy, as well as reducing engine emissions. In addition, the omission of an alternator as well as a catalytic convertor will reduce parasitic drag on the engine, eliminate the need for a conventional charging system, reduce the number of moving parts that can deteriorate and fail, and decrease the weight of the vehicle. These results are not achievable with a traditional catalytic system as a conventional catalytic converter cannot withstand the additional heat.
(18) The present invention provides a highly efficient, dual-chambered design for the fuel cell stack in order to deliver larger power outputs. Electrical power may be carried away from the fuel cell stack to provide electrical energy to the vehicle. The present invention could be used immediately in the automotive industry and can significantly benefit internal combustion engine driven vehicles, as seen in the comparison of the present invention to a conventional system of Table 1 below.
(19) TABLE-US-00001 TABLE 1 SOFC Comparison to Current Alternator System at Estimated Cruise of 65 mph Conventional Alternator System SOFC System Maximum Electrical Power 840 W 840 W Generated Engine Crank Power Consumed 1.964 kW 0 Fuel Required for Operation 0.186 g/s 0.048 g/s Fuel Required for Engine to Develop 1.227 g/s 1.227 g/s 13 kW (Cruise Condition) Total Fuel Required 1.413 g/s 1.275 g/s Fuel Savings — 9.7% *Estimations done at hypothetical cruise of 2018 Chevrolet Malibu with a 1.5 L, 160 hp engine. Cruise assumes a 20 hp load at 36 mpg. Assuming a 35% fuel to electrical conversion.
EXAMPLE
(20) A model exhaust flow was created in a lab and included: Air, CO.sub.2, CH.sub.4, CO, and NO to mimic extremely lean exhaust conditions, such as those seen when the fuel supply to the engine is stopped but is still being rotated via the wheels, thereby causing air to be pumped through the engine. The flow composition was measured before and after each test without any emission reduction device, and then averaged to give a baseline flow. A piece of catalytic converter was used from a 2005 Volkswagen with the same surface area as the SOFC. The catalytic converter section was then tested against the new SOFC design. The equivalence ratio shown is the equivalence ratio of the model exhaust and does not indicate engine conditions.
(21) TABLE-US-00002 TABLE 1 SOFC and Catalytic Converter Emission Reduction Comparison at 580° C. NO NO.sub.2 C.sub.xH.sub.y O.sub.2 % CO % CO.sub.2 % ppm ppm ppm Equivalence Ratio of 0.3 Baseline 8 2.2 22.9 46 0 6625 Catalytic Converter 7.57 1.36 23.6 39.17 1.83 6550 SOFC 7.11 0.59 24.6 34.5 0 6656 Percent Difference 5.62 35.2 4.73 10.1 NA −1.6 Equivalence Ratio of 0.2 Baseline 11.3 3 22.1 125 0 3100 Catalytic Converter 10.9 2.79 23 122.8 0 3141 SOFC 6.15 2.44 26.1 72.25 3 2615 Percent Difference 42.3 11.6 14.1 11.6 NA 16.9
(22) The final row for each equivalence ratio in Table 1, labeled “Percent Difference,” gives the percentage difference between the SOFC performance and the catalytic converter. A positive number indicates a higher performance from the SOFC, whereas a negative number indicates a higher performance from the catalytic converter.
(23) The new design for the SOFC system performs better than the catalytic converter. The SOFC significantly outperforms the catalytic converter in oxygen utilization, carbon dioxide production, as well as in the reduction of NO and CO reduction at an equivalence ratio of 0.3 and 0.2.
(24) The SOFC closely matched (within 2%) the catalytic converter for hydrocarbon reduction at an equivalence ratio of 0.2. However, as the exhaust became leaner the SOFC significantly outperformed the catalytic converter in hydrocarbon reduction. Neither the SOFC nor the catalytic converter displayed consistent performance for NO.sub.2.
(25) Utilization of a SOFC in place of a traditional catalytic converter also has the potential for power generation while the engine is consuming fuel at stoichiometric or rich conditions. Initial testing indicates that an engine operating at stoichiometric conditions results in an exhaust of ˜2-3% H.sub.2 and CO and ˜1% mixed hydrocarbons. These exhaust constituents may be used by the SOFC for electrical power generation. Direct utilization of the byproduct of the internal combustion engine for electrical power generation could result in higher overall efficiency for the automobile system by reducing the need for traditional charging systems.
(26) The SOFC stack may be built within a cylindrical canister for ease of integration into current automotive exhaust systems. The canister can be approximately 6 inches in diameter by approximately 9 inches long so that it is of comparable size to the catalytic converter being replaced by the SOFC system of the present invention. The present invention is estimated to generate up to a 9.7% increase in fuel economy, leading to a reduction of 12 billion gallons of gasoline a year if adopted by the industry. That amounts to 1.74 Quads of hydrocarbon fuel saved each year; while saving drivers 9.7% of their yearly gasoline bill.