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Magnesia synthesis

The catalysts used in the process are essentially nickel metal dispersed on a support material consisting of various oxide mixtures such as alumina, silica, lime, magnesia, and compounds such as calcium aluminate cements. When the catalyst is made, the nickel is present as nickel oxide which is reduced in the plant converter with hydrogen, usually the 3 1 H2 N2 synthesis gas ... [Pg.81]

The first, made by Ichikawa et al. [29], was the evidence that rhodium or iridium cluster carbonyls, when adsorbed on zinc oxide, titania, lanthanum oxides, zirconia or magnesia, could produce quite selectively ethanol by the Fischer-Tropsch synthesis. This was a timely discovery (metallic catalytic particles produced by traditional methods could not reproduce such selectivity) since it came at a period of geopolitical tension after the Kippur war in 1973, which caused the price of crude oil to increase enormously. Therefore, that period was characterized by intense research into selective Fischer-Tropsch catalysis. [Pg.7]

Menon, M., Warren, J. L. and Bullard, J. W. Synthesis of magnesia powders from an alkoxide precursor, Ceram. Trans., 1998, 95, 217-223. [Pg.197]

Table VIII presents analytical data for other nitrided catalysts (two fused and one precipitated) after use in the synthesis with 1H2 + ICO gas. The fused catalysts containing alumina (D3008) and zirconia (L3028) as structural promoters were more resistant to oxidation during synthesis at 21.4 atm. than was the catalyst promoted with magnesia (D3001). Nitrogen was removed more rapidly from the catalyst containing alumina (D3008) during synthesis at 21.4 atm. than at 7.8 atm. The analyses of catalyst P3003.24 indicate that nitrided, precipitated catalysts are also resistant to oxidation. Table VIII presents analytical data for other nitrided catalysts (two fused and one precipitated) after use in the synthesis with 1H2 + ICO gas. The fused catalysts containing alumina (D3008) and zirconia (L3028) as structural promoters were more resistant to oxidation during synthesis at 21.4 atm. than was the catalyst promoted with magnesia (D3001). Nitrogen was removed more rapidly from the catalyst containing alumina (D3008) during synthesis at 21.4 atm. than at 7.8 atm. The analyses of catalyst P3003.24 indicate that nitrided, precipitated catalysts are also resistant to oxidation.
Historical Development and Future Perspectives The Fischer-Tropsch process dates back to the early 1920s when Franz Fischer and Hans Tropsch demonstrated the conversion of synthesis gas into a mixture of higher hydrocarbons, with cobalt and iron as a catalyst [35, 36], Some 20 years earlier, Sabatier had already discovered the reaction from synthesis gas to methane catalyzed by nickel [37]. The FTS played an important role in the Second World War, as it supplied Germany and Japan with synthetic fuel. The plants used mainly cobalt catalysts supported on a silica support called kieselguhr and promoted by magnesia and thoria. [Pg.455]

Figsch V., Bunanova E. Synthesis of spinel-magnesia ceramics from finely milled mixtures of magnesite MgCOs and gibbsite Al(OH)j. In Book of Abstract I Int. Conf. INCOME, Kosice, 23-26 March,1993... [Pg.138]

Another test of validity is to check the performance of the model against experimental rate data obtained far from equilibrium. The microkinetic model presented in Table 7.3.1 predicts within a factor of 5 the turnover frequency of ammonia synthesis on magnesia-supported iron particles at 678 K and an ammonia concentration equal to 20 percent of the equilibrium value. This level of agreement is reasonable considering that the catalyst did not contain promoters and that the site density may have been overestimated. The model in Table 7.3.1 also predicts within a factor of 5 the rate of ammonia synthesis over an Fe(lll) single crystal at 20 bar and 748 K at ammonia concentrations less than 1.5 percent of the equilibrium value. [Pg.249]

Comparison of calculated and measured ammonia concentrations at the effluent of a steady-steady ammonia synthesis reactor containing ruthenium particles supported on magnesia and promoted by cesium. [Adapted from O. Hinrichsen. F Rosowski, M. Muhler, and G. Ertl, The Microkinetics of Ammonia Synthesis Catalyzed by Cesium-Promoted Supported Ruthenium, Chem. Eng. Sci., 51 (1996) 1683, copyright 1996, with permission from Elsevier Science.]... [Pg.251]

H. Reveron, et al., Chemical synthesis and thermal evolution of MgA1204 spinel precursor prepared from industrial gibbsite and magnesia powder. Mater. Lett. 56(1-2), 97-101 (2002). [Pg.69]

Catalysts composed of the following oxides have been found to be inert to the synthesis alumina, silica, molybdenum oxide (Mo2Ob), vanadium oxide (V2O3), blue tungsten oxide (W2O0), thoria, titania (TiOa), magnesia, lime, barium oxide, and strontium oxide.180 At a pressure of 150 atmospheres and a space velocity of 5000 conversions of... [Pg.132]

Surface-mediated solid phase reactions are of growing interest [195] because of their ease of set-up and work, mild reaction conditions, rate of the reaction, selectivity, high yields, lack of solvent, and the low cost of the reactions compared to their homogeneous counterparts. Kaboudin et al. have described a method for synthesis of diethyl 1-hydroxyarylmethylphosphonates from aldehydes and diethyl H-phosphonate on a magnesia surface without a solvent [196] (see Appendix). The important features of this... [Pg.62]


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