MULTI-FUEL FUEL CELL SYSTEM AND OPERATION METHOD THEREOF

Abstract

A multi-fuel fuel cell system is based on the distributed hydrogen production and fuel cell technologies is presented. The system includes fuel supply unit, fuel processor, fuel cell, heat exchange and oxidizer supply units. The fuel processor is a plasma-catalytic reformer. The heat exchange unit is a multiflow heat exchanger which is of a cascading structure from bottom top or a concentric cylinder structure from inside to outside. The multiflow heat exchanger has the function of balancing the heat of fuel processor and fuel cell. The fuel storage is connected to the fuel processor by the pipeline and provides fuel for the fuel processor. The outlet of fuel processor is connected via the multiflow heat exchanger to the fuel cell anode, and provides reactant for the fuel cell.

Claims

1. A multi-fuel based fuel cell system which comprises fuel supply unit, fuel processor, fuel cell, heat exchange and oxidizer supply units; (a) The fuel supply unit has a fuel storage and pipelines; (b) The fuel processor is a plasma reactor which comprises high voltage and ground electrodes; the reactor involves fuel inlet, oxidizer inlet and product outlet, and is used to convert fuel to mixture of hydrogen and carbon monoxide; (c) The type of fuel cell unit used in the system is high temperature fuel cell stack which includes inlets and outlets of anode and cathode; (d) The heat exchange unit is a multiflow heat exchanger which is of a cascading structure from bottom to top or a concentric cylinder structure from inside to outside; the multiflow heat exchanger has the function of balancing the heat of fuel processor and fuel cell; (e) The oxidizer supply unit is connected to the fuel cell cathode and the inlet of fuel processor respectively, and provides oxidant for the fuel cell and fuel processor units; (f) The fuel storage is connected to the fuel processor by the pipeline and provides fuel for the fuel processor; the outlet of fuel processor is connected via the multiflow heat exchanger to the fuel cell anode, and provides reactant for the fuel cell.

2. The system of claim 1, wherein the multiflow heat exchanger includes a compartment for the water gas shift reaction; the compartment which improves the hydrogen concentration and reduces the carbon monoxide concentration is filled with catalyst for the shift reaction; the product of fuel processor is delivered via the shift compartment of the heat exchanger to the fuel cell anode.

3. The system of claim 2, wherein the compartment for shift reaction is filled with high and low temperature shift catalysts; the temperature tolerance of the catalyst decreases along the flow direction.

4. The system of claim 3, the shift compartment is filled with three types of water gas shift catalysts; the active components of catalyst is platinum/nickel, iron and copper along the flow direction.

5. The system of claim 2, two sides of the shift compartment is compartments for fuel preheating and steam/air preheating compartment.

6. The system according to claim 2, the multiflow heat exchanger includes a catalytic combustion compartment which is apart from the shift compartment; the catalytic combustion compartment is filled with combustion catalyst; mixture of tail gas of fuel cell anode (or combustible gas at the startup) and air is delivered to the catalytic combustion compartment, and is discharged after catalytic combustion.

7. The system according to claim 2, the multiflow heat exchanger includes a compartment for the heat transfer medium, and it is apart from the shift compartment; the fuel cell comprises channels for the heat transfer medium and is connected to the compartment of heat transfer medium; heat transfer medium is cycled between the two units.

8. The system of claim 7, wherein the multiflow heat exchanger, the heat transfer medium compartment is apart from the shift and catalytic combustion compartments; the fuel cell comprises channels for the heat transfer medium and is connected to the compartment of heat transfer medium; heat transfer medium is cycled between the two units.

9. The system of claim 6, the multiflow heat exchanger contains a heat transfer medium compartment and a compartment to preheat the mixture of air and steam; one side of the steam/air mixture preheating compartment is adjacent to the shift compartment or the catalytic combustion compartment, the other side is adjacent to the heat transfer medium compartment; the fuel cell comprises channels for the heat transfer medium and is connected to the compartment of heat transfer medium; heat transfer medium is cycled between the two units.

10. The system of claim 9, the multiflow heat exchanger contains a compartment for water preheating; the water preheating compartment is adjacent to the heat transfer medium compartment.

11. The system of claim 6, the multiflow heat exchanger contains a heat transfer medium compartment and a water preheating compartment; one side of the water preheating compartment is adjacent to the shift compartment or the catalytic combustion compartment, the other side is adjacent to the heat transfer medium compartment; the fuel cell comprises channels for the heat transfer medium and is connected to the compartment of heat transfer medium; heat transfer medium is cycled between the two units.

12. The system of claim 11, the multiflow heat exchanger contains a compartment for air preheating, which is adjacent to the heat transfer medium compartment.

13. The system according to claim 7, the heat transfer medium for the multiflow heat exchanger and fuel cell is heat transfer oil.

14. The system according to claim 2, the compartments for fuel preheating, steam/air mixture preheating, heat transfer medium, water preheating and air preheating involve fin structure.

15. The system according to claim 6, the active component of the combustion catalyst is platinum.

16. The system according to claim 1, the oxidizer supply unit is air pump or compressor, and the fuel cell cathode is connected to the air pump or compressor.

17. The system of claim 1, the multi-fuel can be methane, methanol, ethanol, gasoline, diesel, dimethyl ether, biodiesel or their mixture.

18. The system of claim 1, the type of fuel cell stack is high temperature proton exchange membrane fuel cell (HT-PEMFC), and the operating temperature is 120-200° C.

19. The system according to claim 1, a method of operating the system, comprising: The fuel storage provides fuel to the fuel processor, and the oxidizer supply unit provides oxidant to the fuel processor; start the fuel processor and make sure outlet of the fuel processor connected to shift compartment inlet of heat exchanger unit; in the shift compartment, the product of fuel processor is cooled down, and hydrogen concentration is increased and carbon monoxide concentration is decreased after the shift reaction; At the startup phase of the system, liquid fuel is delivered via the atomizing nozzle to the fuel processor, and it is completely or partly combusted by adjusting the ratio of oxidizer and fuel; the produced gas is delivered via shift compartment of the heat exchange unit to the fuel cell, and then to the catalytic combustion compartment of the heat exchange unit; or the produced gas is delivered via shift compartment to the combustion compartment of the heat exchange unit, without entering into the fuel cell; the combustible components in the produced gas is further removed, and the tail gas is discharged from the outlet of the catalytic combustion compartment; heat released from catalytic combustion is used to heat up the system; The heat transfer medium is cycled between the compartment of heat exchange unit and channels of fuel cell to heat up the fuel cell stack at startup phase; the outlet of shift compartment is connected to the fuel cell anode, and the oxidizer supply unit is connected to the fuel cell cathode for oxidant supply; at steady state, heat generated by the fuel cell is taken by the heat transfer medium to the compartment of heat exchange unit where the medium is cooled down; the cooled medium is cycled to the fuel cell stack to cool the fuel cell stack.

20. The method of claim 19, further comprising following: Mixture of air and steam is delivered via the steam/air mixture preheating compartment of heat exchanger to the fuel processor; Air is delivered via air preheating compartment of the heat exchanger to the fuel processor; Water is delivered via water preheating compartment of the heat exchanger to the fuel processor; Fuel storage is connected via heat exchange unit where the fuel is preheated to the fuel processor; Tail gas of fuel cell anode is delivered to the catalytic combustion compartment of heat exchanger, and then is discharged.

Description

DESCRIPTION OF FIGURES

[0039] FIG. 1 is a flow diagram of the multi-fuel based fuel cell system.

[0040] In FIG. 1, 1. fuel pump; 2. compressor; 3. air assisted atomizing nozzle; 4. water pump; 5. multi-channel heat exchanger; 6. plasma reactor (the bottom part is the catalytic reforming section); 7. high voltage power source; 8. air pump; 9. fuel cell stack; 10. air pump for cathode; 11. heat transfer oil pump

[0041] FIG. 2 is the schematic diagram showing flow pattern of the multiflow plate fin heat exchanger.

[0042] FIG. 3 is discharge curve of the fuel cell system.

EMBODIMENTS

[0043] A multi-fuel based fuel cell system, as shown in FIG. 1, comprises fuel supply unit, fuel processor, fuel cell, heat exchange and oxidizer supply units.

[0044] The fuel processor is a plasma reactor which comprises high voltage and ground electrodes. An air-assisted atomization nozzle is installed on the top of the reactor. The middle part of the reactor is plasma reforming section and the lower part is catalytic reforming section which is filled with reforming catalyst. The outlet is set at the bottom of the reactor. One inlet of the atomizing nozzle is connected to the fuel storage via the fuel pump and pipeline, the other inlet of the nozzle is connected to the outlet of the air compressor. The upper section of the reactor has an air inlet, from which the purging air is introduced to the inner wall of the reactor. The inlet is connected to the outlet of compressor via the multiflow heat exchanger. The side wall of the plasma reactor involves a feed inlet. Water is pressurized via pump to the exchanger, where it is preheated and vaporized, and is mixed with air from the compressor. The mixture is further preheated and mixed with the preheated/vaporized fuel which is delivered via fuel pump from the fuel storage. The final mixture is delivered via the feed inlet to the gap between high voltage and ground electrodes in the plasma reactor. The product from the outlet of plasma reactor is delivered via heat exchanger to the inlet of fuel cell anode.

[0045] The fuel cell unit includes fuel inlet and tail gas outlet of anode, and inlet and outlet of cathode. Tail gas from fuel cell anode mixes with air, and is delivered to the heat exchanger where the combustible gas is burned. Then the exhaust gas is discharged.

[0046] Heat transfer medium of fuel cell is delivered via pump to fuel cell, enters into the heat exchanger, and then returned to the fuel cell.

[0047] The heat exchanger is a multiflow heat exchanger which includes seven compartments arranged in a cascading structure from bottom to top or a concentric cylinder structure from inside to outside

From bottom to up or inside to outside:

[0048] fuel preheating compartment which includes the first inlet and outlet.

[0049] water gas shift compartment which is filled with three sections of catalysts. From the inlet to the outlet, the active component of catalysts is nickel, iron and copper. The shift compartment includes the second inlet and outlet.

[0050] mixture of air and steam preheating compartment which includes the third inlet and outlet.

[0051] catalytic combustion compartment for tail gas of fuel cell which is filled with combustion catalyst , and the active component of the catalyst is platinum. The catalytic combustion compartment includes the fourth inlet and outlet.

[0052] water preheating compartment which includes the fifth inlet and outlet.

[0053] heat transfer medium compartment which includes the sixth inlet and outlet.

[0054] air preheating compartment which includes the seventh inlet and outlet.

[0055] Fuel from fuel storage of fuel supply unit is delivered via the first inlet and outlet to the fuel processor. The oxidizer supply unit comprises three streams. The streams are delivered via the third, fifth and seventh inlets and outlets respectively to the inlet of fuel processor. After reaction between fuel and oxidant, the product is discharged from the outlet of the fuel processor.

[0056] The outlet of fuel processor is connected to the fuel cell anode via the second inlet and outlet of the heat exchange unit.

[0057] Tail gas of fuel cell anode is delivered to the fourth inlet of heat exchange unit. After catalytic combustion, the exhaust gas is discharged from the fourth outlet.

[0058] Heat transfer medium of fuel cell flows through fuel cell to the sixth inlet of heat exchange unit. After preheating or cooling, it is delivered via the sixth outlet of heat exchange unit to the fuel cell. The heat transfer medium is cycled in the system.

[0059] In the system operation, ethanol is taken as an example. Lower part of the plasma reactor is filled with the reforming catalyst whose active component is nickel. From inlet to outlet of the second compartment of heat exchanger, the active component of water gas shift catalyst is nickel, iron and copper. The fourth compartment of heat exchanger is filled with combustion catalyst. At startup, liquid ethanol is delivered via the atomizing nozzle to the fuel processor, and the flow rate is 5-15 ml/min. Adjusting the flow rate of air to make sure fuel is completely combusted, and the released heat is used to preheat the system. At steady state, ethanol is delivered to the first compartment of heat exchanger rather than to the atomizing nozzle. After preheating and evaporation, ethanol mixes with mixture of air and steam from the third compartment of heat exchanger, and enters into the plasma reactor from the middle inlet. The flow rate of ethanol is 35 ml/min, the steam to carbon ratio (H.sub.2O/C) is 1.85, the oxygen-to-carbon ratio (O/C) is 0.58. The outlet gas of plasma reactor is delivered to the second compartment of heat exchanger where it is cooled down and the water gas shift reaction occurs. The product gas has about 40% (molar composition) hydrogen and less than 3% (molar composition) carbon monoxide. The product gas is delivered to the fuel cell anode where the discharge is realized. The relationships of current, voltage and power are shown in FIG. 3.

[0060] For the shutdown of the system, firstly turn off the fuel and water pumps, then adjust the air to about 1 m.sup.3/h and stop power discharge of fuel cell. Keep the air feeding for about 1 min, then stop the air compressor, lastly turn off the heat transfer oil pump. The invention has the advantages of small size, quick start, high power density and compactness, and can convert ethanol to the hydrogen rich gas for fuel cell application, which is beneficial to the promotion and application of fuel cell technology.