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Processing of Zirconia

Carbothermal reduction. Thermal demixing by carbothermal reduction at temperatures 1750 °C generated by an electric arc is governed by the chemical reaction  [Pg.197]

In a second processing step, the zirconia is purified by treating it with chlorine and hydrogen according to  [Pg.197]

The zirconium chloride is subsequently converted to zirconia (see below). [Pg.197]

Direct chlorination. A variant of this process is the direct chlorination, which is conducted at temperatures between 800 and 1200 °C according to  [Pg.197]

ZrSi04 + 4C + 4CI2 ZrCU T + SiCU T + 4COT ZrCU + H2O ZrOCl2 + 2HC1. [Pg.198]


Further Stages of Sol-Gel Processing of Zirconia-Related Materials... [Pg.702]

Bender, B., Shadwell, D., Bulik, C., Incorvat, L. and Lewis III, D. (1986). Effect of fiber coating and composite processing on properties of zirconia-based matrix SiC fiber composites. Am. Ceram. Soc. Bull. 65, 363-369. [Pg.229]

Randon et al. reported on an alternative approach for the preparation of zirconia monoliths [96]. The sol-gel process is initiated by hydrolysis of an ethanolic zirconium alkoxide solution, on addition... [Pg.15]

Tetragonal zirconia was partly transformed into the cubic phase during the sintering process of the UAP (uniaxially pressed) and CIP-prepared green compacts, and was accompanied by the formation of a-TPC. The transformation tends to accelerate as the PSZ quantity increases. [Pg.715]

Ceramic foils are produced continuously by tape-casting methods. These ceramic tapes consist of an organic binder and oxide powder material, for example, zirconia, titania or alumina. If it is possible to integrate the production process of a micro structured reactor into such a continuous process, production costs would decrease strongly. An early approach used unstructured ceramic foils to build up a micro reactor [159], The reactor consisted essentially of two functional layers, a reaction layer and a heating layer (Figure 4.102). [Pg.619]

What precautions could be taken to prevent the take up of impurities when reducing the particle size of zirconia from 10 pm to 1 pm Describe the beneficial effects that addition of a deflocculating agent might be expected to have on the ball-milling process. [Pg.132]

In the NGASE operation both the anode gas (methane-steam) and cathode gas (hydrogen-steam) are reducing (low ), and thus both electrode materials must be capable of low Po stability. A Ni-based cermet electrode for both anode and cathode will be appropriate for this mode of operation. The authors have observed erosion of zirconia electrolyte at temperatures above 700°C under these conditions. This phenomenon may limit the usefulness of the NGASE process. [Pg.73]

Eguchi, K., Akasaka, N., Mitsuyasu, H., and Nonaka, Y., Process of solid state reaction between doped ceria and zirconia, Solid State Ionics, 2000, 135, 589-594. [Pg.227]


See other pages where Processing of Zirconia is mentioned: [Pg.189]    [Pg.226]    [Pg.357]    [Pg.277]    [Pg.197]    [Pg.221]    [Pg.1863]    [Pg.324]    [Pg.189]    [Pg.226]    [Pg.357]    [Pg.277]    [Pg.197]    [Pg.221]    [Pg.1863]    [Pg.324]    [Pg.328]    [Pg.253]    [Pg.382]    [Pg.216]    [Pg.16]    [Pg.71]    [Pg.274]    [Pg.123]    [Pg.67]    [Pg.448]    [Pg.587]    [Pg.328]    [Pg.120]    [Pg.10]    [Pg.408]    [Pg.63]    [Pg.109]    [Pg.254]    [Pg.510]    [Pg.5]    [Pg.55]    [Pg.567]    [Pg.202]    [Pg.8]    [Pg.567]    [Pg.324]    [Pg.324]    [Pg.64]    [Pg.628]    [Pg.60]    [Pg.226]   


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