Phosphoric acid fuel cell

Abstract: A series of modified phosphoric acid electrolytes containing fluorinated carbon compounds and silicone fluids as additives are disclosed. The modified electrolytes can improve the fuel cell performance due to the enhanced oxygen reduction kinetics. These additives are, preferably, potassium perfluorohexanesulphonate (C₆F₁₃KO₃S), potassium nonafluorobutanesulphonate (C₄F₉KO₃S), perfluorotributylamine [(C₄F₉)₃N] and polymethylsiloxanes [(-Si(CH₃)₂O-) n ]. The additives are added in an amount of 0.1-5 wt% with respect to the phosphoric acid electrolyte.

Description: The present invention is directed to phosphoric acid fuel cells with improved electrolytes. In a fuel cell, chemical energy of gaseous fuel is converted into electrical power. A conventional fuel cell comprises an anode, a cathode, and an electrolyte impregnated matrix disposed between the electrodes. In the operation of a phosphoric acid fuel cell, a hydrogen containing gas is fed to the anode and an oxygen containing gas to the cathode. The gases diffuse through the electrodes and react with the electrolyte in the presence of a catalyst on the electrodes to yield water, heat and electrical energy. At the anode, hydrogen in the feed gas gives up electrons by electrochemical oxidation reaction. The electrical current so generated is conducted from the anode through an external circuit to the cathode. At the cathode, the electrons are then electrochemically combined with oxygen. A flow of ions through the electrolyte completes the circuit. The electrochemical reactions proceeding in a phosphoric acid fuel cell are thus: H 2 → 2H + + 2e - at the anode, and ½O 2 + 2H + + 2e - → H 2 O at the cathode. Phosphoric acid is the conventional electrolyte for acidic hydrogen-oxygen fuel cells because of its high stability at elevated temperatures, the ease of removal of CO 2 and water, and its high ionic conductivity. However, phosphoric acid has several undesirable properties. Its low oxygen solubility at high acid concentrations and relatively slow oxygen reduction rate lead to a very high polarization of the cathode. To enhance the oxygen reduction rate and thereby improve the efficiency of phosphoric acid fuel cells, it has been suggested to substitute trifluoromethanesulphonic acid for the phosphoric acid electrolyte in the cells. The oxygen reduction rate in trifluoromethanesulphonic acid is substantially higher than in phosphoric acid because of the higher oxygen solubility resulting in improved limiting current of the cell (R.C. Bhardway, N.G. Smart and J.O Bockris; Proc. Intersoc. Energy Convers. Eng. Conf., 1991, Vol. 26, No. 3; pages 546-569; P. Zellenay, B.R. Scharifker and J.O. Bockris; J. Electrochem. Soc., 1986, Vol. 133, No. 11; pages 2262-2267). Despite of its better performance, the use of trifluromethanesulphonic acid is limited to temperatures below the operation temperature of practical phosphoric acid fuel cells, because of its high vapour pressure. As a further disadvantage of trifluromethanesulphonic acid, it absorbs very easily in the porous electrodes resulting in low gas diffusion and thereby a higher electrode polarization. Final Report, April 1985 - March 1989, Clemson University, discloses the addition of fluorinated acids to phosphoric acid electrolytes in fuel cells for the purpose of promoting oxygen depolarisation. Final Report, May 1991, International Fuel Cells Corporation, relates to natural gas fuel cells. Subscale cell test results with sulfonyl carbon electrolytes indicate that oxygen reduction activity was enhanced above that of phosphoric acid. JP-A-3034266 describes electrolytes for fuel cells containing phosphoric acid and fluorinated surfactants. US-A-3379573 discloses a porous polytetrafluoroethylene or polytrifluoromonochloroethylene matrix material saturated with an aqueous inorganic electrolyte containing a small amount of a water-soluble salt of a highly fluorinated aliphatic surfactant which may be between water-proofed electrodes in a fuel cell. We have now found that addition of small amounts of specific fluorinated organic compounds or silicone compounds, having a vapour pressure not higher than that of phosphoric acid, to the phosphoric acid electrolyte of a phosphoric acid fuel cell enhances oxygen solubility and diffusitivity of the electrolyte without detrimental absorption of the electrolyte in the electrodes of the cell and thus improves the performance of conventional operated phosphoric acid fuel cells. The present invention provides a phosphoric acid fuel cell comprising within a housing a gas diffusion cathode utilizing an oxygen-containing oxidant gas, a gas diffusion anode using a hydrogencontaining fuel gas, and an electrolyte comprising phosphoric acid and at least 0.1 percent by weight of an additive selected from a perfluorinated trialkylamine having the general formula R 1 R 2 R 3 N, or salts thereof, where R 1 , R 2 and R 3 are independent fluorocarbon groups, and silicone compounds with a vapour pressure not higher than that of phosphoric acid, thereby decreasing polarization of the cathode and increasing efficiency of the cell. As a theoretical explanation, the above electrolyte additives form a physically adsorbed layer on the electrode/electrolyte interface, in which layer the concentration of oxygen is higher than in the bulk phosphoric acid and, thereby, increases the rate of oxygen reduction on the cathode and thus the thermal efficiency of the cell. In the following examples, the invention will be illustrated in detail by reference to preferred embodiments thereof and to the drawings in which Fig. 1 and Fig. 2 show cell polarization curves obtained with different electrolyte additives in comparison with 100% phosphoric acid electrolyte. In the Examples, the electrodes used were Pt-catalyzed carbon gas diffusion electrodes (0.5 mg/cm 2 Pt loading on both anode and cathode). All the experiments were carried out with 100% H 3 PO 4 as electrolyte, at a temperature of 190°C, by using pure hydrogen as fuel and pure oxygen as oxidant. The fuel cell housing used to test the electrolyte additives was a product from Giner, Inc. (General License GLV). The temperature was controlled by a controller (Dowty TC-48, Dowty Electronics Company) and heat was provided to the cell by two flexible electrical heaters glued one to each steel end plate of the housing. The temperature in the cell was maintained within ±1°C. To maintain the water balance in the cell, the fuel gas was passed through a saturator containing distilled water at 72°C. 100% phosphoric acid for the Examples was prepared as follows: Phosphoric acid (85%, Riedel-de Haën) was purified by treatment with hydrogen peroxide and concentrated to 100% by heating. Example 1 Perfluorotributylamine; [(C 4 F 9 ) 3 N; amine] was used as electrolyte additive. (C 4 F 9 ) 3 N is a transparent liquid (technical grade) purchased from PCR Incorporated. Modified electrolytes were prepared by adding perfluorotributylamine to 100% phosphoric acid giving weight ratios of 0.5 : 99.5, 1.0 : 99.0 and 1.5 : 98.5, respectively. When agitated with a magnetic stirrer at about 100°C, emulsions were achieved which were used immediately as electrolytes in the tests. The cell test results are shown in Figure 1. Example 2 Silicone DC-550® (Si-550), [-Si(CH 3 ) 2 O-] n was used as electrolyte additive. Silicone DC-550® is a transparent liquid purchased from Dow Co.. A modified electrolyte was prepared by adding silicone DC-550® to 100% phosphoric acid in a weight ratio of 1.0 : 99.0. When agitated with a magnetic stirrer at about 100°C, an emulsion was achieved, which was used immediately as electrolyte in the tests. The cell test results are shown in Figure 2. For a hydrogen-oxygen fuel cell operating at 190°C, AH is about ÷280 kJ/mole H 2 O. It can be converted to a thermal voltage equivalent: (280 kJ/mole)/2 x 96.5 kA · s) = 1.45 V. Therefore, the thermal efficiency of a fuel cell is V TERM /1.45, where V TERM is the cell terminal voltage. According to Figures 1 and 2, at the same current density of 400 mA/cm 2 , the cell thermal efficiencies can be calculated as follows: When 100% H 3 PO 4 was the electrolyte (as the reference), Eff T = 0.54/1.45 = 37.2%. When 1.5% (C 4 F 9 ) 3 N was used as the additive (Example 1), Eff T = 0.65/1.45 = 44.8%, (7.6% increase in efficiency compared to 100% H 3 PO 4 ). When 1.0% silicone DC-550 was used as the additive (Example 2), Eff T = 0.66/1.45 = 45.5%, (8.3% increase in efficiency compared to 100% H 3 PO 4 ).

Claims: A phosphoric acid fuel cell comprising within a housing a gas diffusion cathode utilizing an oxygen-containing oxidant gas, a gas diffusion anode using a hydrogencontaining fuel gas, and an electrolyte comprising phosphoric acid and at least 0.1 percent by weight of an additive selected from a perfluorinated trialkylamine having the general formula R 1 R 2 R 3 N, or salts thereof, where R 1 , R 2 and R 3 are independent fluorocarbon groups, and silicone compounds with a vapour pressure not higher than that of phosphoric acid, thereby decreasing polarization of the cathode and increasing efficiency of the cell. The phosphoric acid fuel cell of claim 1, wherein the perfluorinated trialkylamine is perfluorotributylamine. The phosphoric acid fuel cell of claim 1, wherein the additive consists of a polyalkylsiloxane. The phosphoric acid fuel cell of claim 3, wherein the polyalkylsiloxane is polymethylsiloxane.

Inventors: BERG ROLF W, BJERRUM NIELS J, GANG XIAO, HJULER HANS AAGE, OLSEN CHRISTIAN, BERG,ROLF W., BJERRUM,NIELS J., GANG,XIAO, HJULER,HANS AAGE, OLSEN,CHRISTIAN
Applicants: TOPSOE HALDOR AS, HALDOR TOPSOE A/S
Application year: 1992
Main classification: H01M8
IPC codes: H01M8