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Molten carbonate fuel cells anodes

Yuh CY, Selman JR (1984) Polarization of the molten carbonate fuel cell anode and cathode. [Pg.246]

Molten Carbonate Fuel Cell. The electrolyte ia the MCFC is usually a combiaation of alkah (Li, Na, K) carbonates retaiaed ia a ceramic matrix of LiA102 particles. The fuel cell operates at 600 to 700°C where the alkah carbonates form a highly conductive molten salt and carbonate ions provide ionic conduction. At the operating temperatures ia MCFCs, Ni-based materials containing chromium (anode) and nickel oxide (cathode) can function as electrode materials, and noble metals are not required. [Pg.579]

The Surface Fractal Investigatioii of Anode Electrode of Molten Carbonate Fuel Cell... [Pg.621]

In order to describe the geometrical and structural properties of several anode electrodes of the molten carbonate fuel cell (MCFC), a fractal analysis has been applied. Four kinds of the anode electrodes, such as Ni, Ni-Cr (lOwt.%), Ni-NiaAl (7wt.%), Ni-Cr (5wt.%)-NijAl(5wt.%) were prepared [1,2] and their fractal dimensions were evaluated by nitrogen adsorption (fractal FHH equation) and mercury porosimetry. These methods of fractal analysis and the resulting values are discussed and compared with other characteristic methods and the performances as anode of MCFC. [Pg.621]

K. Hoshino, T. Kohno, Central Research Institute, Mitsubishi Material Co., "Development of Copper Base Anodes for Molten Carbonate Fuel Cells," in The International Fuel Cell Conference Proceedings, NEDO/MITI, Tokyo, Japan, Pgs. I69-I72, 1992. [Pg.166]

Molten Carbonate Fuel Cell The electrolyte in the MCFC is a mixture of lithium/potassium or lithium/sodium carbonates, retained in a ceramic matrix of lithium aluminate. The carbonate salts melt at about 773 K (932°F), allowing the cell to be operated in the 873 to 973 K (1112 to 1292°F) range. Platinum is no longer needed as an electrocatalyst because the reactions are fast at these temperatures. The anode in MCFCs is porous nickel metal with a few percent of chromium or aluminum to improve the mechanical properties. The cathode material is hthium-doped nickel oxide. [Pg.49]

Molten carbonate fuel cells (MCFCs) are currently being developed for natural gas and coal-based power plants for electrical utility, industrial, and military applications. MCFCs are high-temperature fuel cells that use an electrolyte composed of a molten carbonate salt mixture suspended in a porous, chemically inert ceramic lithium aluminium oxide (LiAI02) matrix. Since they operate at extremely high temperatures of 650°C and above, non-precious metals can be used as catalysts at the anode and cathode, reducing costs. [Pg.27]

The molten carbonate fuel cells employ LijCOj-f CC (62.38 mol.%) electrolytes, porous Ni alloy, and lithiated nickel oxide as anodes and cathodes at an operating temperature of 723 K. The half-cell reactions of each side are, respectively... [Pg.377]

The electrolyte in this fuel cell is generally a combination of alkali carbonates, which are retained in a ceramic matrix of LiA102 [8], This fuel cell type works at 600°C-700°C, where the alkali carbonates form a highly conductive molten salt with carbonate ions providing ionic conduction. At the high operating temperatures in the molten carbonate fuel cell, a metallic nickel anode and a nickel oxide cathode are adequate to promote the reaction [9], Noble metals are not required. [Pg.379]

Molten carbonate fuel cells (MCFC), with alkali carbonate (in LiA102 matrixes) electrolyte, conduct C032 -anions, generated at an 02/C02 exposed cathode to electro-oxidise H2 at the anode and at high temperatures. [Pg.52]

The internal reforming molten carbonate fuel cell has a particular construction. In the anode chamber there is a catalyst for the reforming reaction of natural... [Pg.549]

The principal product from the reforming reaction, which is H2, is consumed in the anode reaction. Figure 35 is a picture of a molten carbonate fuel Cell [316], It is composed of a stack of many superposed cells, each cell having a thickness of 5 mm and an area of 1 m2. [Pg.549]

Chapters I to III introduce the reader to the general problems of fuel cells. The nature and role of the electrode material which acts as a solid electrocatalyst for a specific reaction is considered in chapters IV to VI. Mechanisms of the anodic oxidation of different fuels and of the reduction of molecular oxygen are discussed in chapters VII to XII for the low-temperature fuel cells and the strong influence of chemisorhed species or oxide layers on the electrode reaction is outlined. Processes in molten carbonate fuel cells and solid electrolyte fuel cells are covered in chapters XIII and XIV. The important properties of porous electrodes and structures and models used in the mathematical analysis of the operation of these electrodes are discussed in chapters XV and XVI. [Pg.175]

Lim and Winnick [110] examined removal of H2S from a simulated hot coal-gas stream fed to the cathode while elemental sulfur gas was evolved at the anode. This process was performed in a cell that was similar in construction to a molten carbonate fuel cell (Fig. 23). The electrolyte was a mixture of Na2S and Li2S retained in a porous inert matrix material (MgO). The cathodic reaction involved the two-electron reduction of hydrogen sulfide to hydrogen (information on the equilibrium potential for H2S reduction can be obtained from [111] ... [Pg.402]

Similar efforts in solid-state electrochemistry for SOFC development focus on the exploration of new perovskites not only for the ORR but also for the anodic oxidation of hydrocarbons [182]. In this area, the discovery that Cu-based anodes present a viable alternative to the classical Ni-YSZ cermet anodes is particularly noteworthy [166, 183, 184], owing to the significant enhancement of performance by avoiding coke deposition. Similar important advances have occurred in the molten carbonate fuel cell (MCFC) area [9]. [Pg.69]

Fig. 12 Methane reforming reaction at the anode of a molten carbonate fuel cell. The reaction between fuel and water takes place in the outer part of the anode, the produced hydrogen reacts at the interface anode-electrolyte. Fig. 12 Methane reforming reaction at the anode of a molten carbonate fuel cell. The reaction between fuel and water takes place in the outer part of the anode, the produced hydrogen reacts at the interface anode-electrolyte.
Bychin, V.P. Zvezdkin, V.A. Samatov, O.M. Porous nickel anodes for molten-carbonate fuel cells. Russ. J. Electrochem. 1993, 29 (11), 1346-1349. [Pg.1761]

Kudo, T. Nishina, T. Uchida, I. Fabrication of porous gas-diffusion anode for molten-carbonate fuel cell by composite coating method. Denki Kagaku 1990, 58 (4), 354-359. [Pg.1761]

Niikura, J. Hatoh, K. Iwaki, T. In-cell sintering anodes for molten carbonate fuel cell. J. Chem. Soc. Jpn. 1989, 1, 20-25. [Pg.1761]

Lithium aluminates are also important in the development of molten carbonate fuel cells (MCFC) [82, 83], In these fuel cells, a molten carbonate salt mixture is used as an electrolyte. These fuel cells operate through an anode reaction, which is a reaction between carbonate ions and hydrogen. A cathode reaction combines oxygen, C02, and electrons from the cathode to produce carbonate ions, which enter the electrolyte. These cells operate at temperatures of 650°C and the electrolyte, which is usually lithium and potassium carbonate, is suspended in an inert matrix, which is usually a lithium aluminate. [Pg.59]

Molten Carbonate Fuel Cells—The anode fuel is hydrogen, with the following oxidation reaction ... [Pg.1822]

A molten carbonate fuel cell is an energy conversion device that converts chemical energy in fossil fuels into electricity. The operating temperature of an MCFC is 600 to 700°C.The principal anode reaction is the oxidation of hydrogen or carbon monoxide ... [Pg.161]


See other pages where Molten carbonate fuel cells anodes is mentioned: [Pg.1759]    [Pg.94]    [Pg.816]    [Pg.1759]    [Pg.94]    [Pg.816]    [Pg.583]    [Pg.601]    [Pg.621]    [Pg.160]    [Pg.120]    [Pg.623]    [Pg.320]    [Pg.286]    [Pg.432]    [Pg.21]    [Pg.3844]    [Pg.1748]    [Pg.1761]    [Pg.1761]    [Pg.291]    [Pg.69]    [Pg.178]    [Pg.158]    [Pg.285]    [Pg.167]   
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