The present invention relates to a fuel cell system, and more particularly to a fuel cell system enabling waste-heat recovery.
A fuel cell is a power-generating unit that generates electrical energy through electrochemical reaction of hydrogen-containing fuel with air. Since the fuel cell has the advantages of low pollution, high efficiency, and high energy density, it has been actively researched, developed, and promoted in many countries. Among others, the proton exchange membrane fuel cell (PEMFC) is the most industrially valuable product due to its low operating temperature, quick activation, and high energy density.
In a fuel cell system using methanol as an anodic fuel, the fuel cell stack thereof includes an air inlet, a reaction-produced waste gas outlet, an anodic fuel inlet, and an anodic fuel outlet. In the reaction in the fuel cell system, air required at the cathode is supplied into the fuel cell stack via the air inlet. And, air having been used in the reaction is expelled as waste gas via the reaction-produced waste gas outlet.
On the other hand, anodic fuel required at the anode in the reaction in the fuel cell stack is supplied from a fuel supply unit, which supplies a mixture of pure methanol and water to the anodic fuel inlet of the fuel cell stack. And, excessive methanol that does not react with the air in the reaction is expelled via the anodic fuel outlet of the fuel cell stack.
In a general big-scaled fuel cell system, the fuel supply unit includes a pure methanol tank for storing pure methanol, a methanol pump, a circulation pump, and a water tank for storing water.
In the conventional fuel cell system using methanol as the anodic fuel for the fuel cell, pure methanol in the pure methanol tank and water in the water tank are separately supplied into a mixing tank and evenly mixed. The methanol/water mixture is then pumped by a circulation pump for supplying to the anodic fuel inlet of the fuel cell stack. However, it is frequently unable to thoroughly stir and evenly mix the pure methanol and the water using conventional mixing techniques.
Further, in the fuel cell system, the air having been used in the reaction in the fuel cell stack is expelled via the reaction-produced waste gas outlet. The expelled waste gas usually has a pretty high temperature. If the waste gas is simply exhausted without being recovered, the heat of the waste gas is wasted. On the other hand, the fuel cell must operate under proper temperature and humidity conditions to achieve the best possible performance. However, it is a pity the heat energy of the exhausted waste gas in the conventional fuel cell system has not been recovered and utilized in regulation of the temperature of the system.
A primary object of the present invention is to provide a fuel cell system enabling waste-heat recovery, in which air source for supplying to a fuel cell stack for reaction is properly preheated by recovered waste gas produced in the reaction in the fuel cell stack.
Another object of the present invention is to provide a structurally simple air supply unit for a fuel cell system. In the air supply unit, there is provided waste gas conveying lines for recovering waste gas produced in the reaction in the fuel cell system and guiding the recovered waste gas to an air source to preheat air for supplying to a fuel cell stack of the fuel cell system for reaction.
A further object of the present invention is to provide a fuel cell system in which waste gas expelled from a fuel cell stack is guided into a mixing tank to enable thorough stirring and even mixing of methanol with water in the mixing tank.
A still further object of the present invention is to provide a fuel cell system enabling full use of reaction heat produced in the reaction in a fuel cell stack as a heat source to preheat air for supplying to the fuel cell stack for reaction, so as to upgrade the performance of the fuel cell system.
A still further object of the present invention is to provide a fuel cell system in which a cover is provided to enclose a fuel cell stack therein, so that air in the cover is supplied to the fuel cell stack for reaction, and reaction heat produced in the reaction in the fuel cell stack is partially recovered for use.
The structure and the technical means adopted by the present invention to achieve the above and other objects can be best understood by referring to the following detailed description of the preferred embodiments and the accompanying drawings, wherein
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The fuel cell stack 1 has an air inlet 11, a reaction-produced waste gas outlet 12, an anodic fuel inlet 13, and an anodic fuel outlet 14.
Air required in the reaction in the fuel cell stack 1 is supplied from an air source A via the air supply unit 2 to the air inlet 11 of the fuel cell stack 1. The air supply unit 2 includes an air filter 21, an air pump 22, and an air conveying line 23 led to the air inlet 11. Air having been used in the reaction in the fuel cell stack 1 is then expelled as waste gas from the reaction-produced waste gas outlet 12.
The mixing tank 3 includes a water inlet 31, a water outlet 32, a methanol inlet 33, a methanol-water mixture outlet 34, a waste gas/water inlet 35, and an expelled anodic fuel inlet 36. The waste gas/water inlet 35 is communicable with the reaction-produced waster gas outlet 12 of the fuel cell stack 1 via a waste gas conveying line 121, and the expelled anodic fuel inlet 36 is communicable with the anodic fuel outlet 14 of the fuel cell stack 1 via an expelled anodic fuel conveying line 141.
The fuel required in the reaction in the fuel cell stack 1 is supplied from the fuel supply unit 4 to the fuel cell stack 1. The fuel supply unit 4 includes a water tank 41, a pure methanol tank 42, a methanol pump 5, and a circulation pump 6. The water tank 41 and the pure methanol tank 42 store water and pure methanol, respectively. The water stored in the water tank 41 is supplied to the mixing tank 3 via a water-conveying line and the water inlet 31 on the mixing tank 3. The pure methanol stored in the pure methanol tank 42 is supplied to the mixing tank 3 via the methanol pump 5 and the methanol inlet 33 on the mixing tank 3.
The pure methanol and the water separately supplied to the mixing tank 3 are mixed in the mixing tank 3, and the mixture of pure methanol and water is then pumped by the circulation pump 6 from the methanol/water mixture outlet 34 and supplied to the fuel cell stack 1 via the anodic fuel inlet 13 for use as the anodic fuel needed in the reaction in the fuel cell stack 1. A methanol concentration sensor 61 may be mounted on a communicating line between the circulation pump 6 and the anodic fuel inlet 13 of the fuel cell stack 1 for detecting the concentration of the methanol/water mixture.
Before the waste gas expelled from the reaction-produced waste gas outlet 12 of the fuel cell stack 1 is guided to the waste gas/water inlet 35 of the mixing tank 3 via the waste gas conveying line 121, it first passes the gas/water separator 7, so that water contained in the expelled waste gas is separated from the waste gas. Thereafter, water separated from the expelled waste gas by the gas/water separator 7 is guided into the mixing tank 3 via the waste gas/water inlet 35, and then evenly mixed with the methanol in the mixing tank 3 through thorough stirring.
An excessive part of the pure methanol that is supplied to the fuel cell stack 1 for use as the anodic fuel but is not reacted with the air, which is used as the cathodic fuel, is expelled via the anodic fuel outlet 14 of the fuel cell stack 1 and guided to the expelled anodic fuel inlet 36 of the mixing tank 3 via the expelled anodic fuel conveying line 141, and be recovered.
In a circuit system of the fuel cell system enabling waste heat recovery, there is a DC-DC converter 8. Power generated during the reaction in the fuel cell stack 1 is converted by the DC-DC converter 8 to supply a predetermined output voltage. The circuit system also includes a sensing and control unit 81, which is adapted to detect an output power P produced by the DC-DC converter 8, and use the methanol/water mixture concentration detected by the methanol concentration sensor 61 to control the methanol pump 5 to supply a proper amount of methanol.
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In the third embodiment shown in