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Methyl t-Butyl Ether (MTBE) Production: A Comparison of Montmorillonite-Derived Catalysts with an Ion-Exchange Resin

Published online by Cambridge University Press:  02 April 2024

J. M. Adams
Affiliation:
Edward Davies Chemical Laboratories, University College of Wales, Aberystwyth SY23 1NE, United Kingdom
K. Martin
Affiliation:
Edward Davies Chemical Laboratories, University College of Wales, Aberystwyth SY23 1NE, United Kingdom
R. W. McCabe
Affiliation:
Edward Davies Chemical Laboratories, University College of Wales, Aberystwyth SY23 1NE, United Kingdom
S. Murray
Affiliation:
Edward Davies Chemical Laboratories, University College of Wales, Aberystwyth SY23 1NE, United Kingdom
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Abstract

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Montmorillonite-based catalysts were compared with an acidic ion-exchange resin of the type used industrially for the production of methyl t-butyl ether (MTBE) from methanol and isobutene or t-butanol. When 1,4-dioxan was used as solvent, Al3+-exchanged montmorillonites had about half the efficiency of the resin Amberlyst 15 at 60°C; they were, however, about twice as efficient at this temperature at Ti3+-montmorillonite or K10, a commercially available acid-treated bentonite. Montmorillonite exchanged with Chlorhydrol solutions to give interlayer [Al13O4(OH)2(H2O)12]7+ ions and pillared clays derived from such materials were poor catalysts, as was K306, a more drastically acid-treated bentonite- based commercial catalyst. Freeze-drying of the Al3+-clay before reaction to produce a more open, porous structure had no effect on its catalytic efficiency. The activation energy for the reaction of isobutene and methanol in dioxan was 44 kj/mole for an Al3+-clay catalyst compared with 25 kJ/mole for reactions catalyzed by Amberlyst 15. With no solvent (as in industrial processes), the rates of reaction were considerably slower for both the clay- and resin-catalyzed reactions. As has been found previously for resin-catalyzed reactions using stoichiometric amounts or an excess of methanol, the rate was proportional to the isobutene concentration, and the rate-determining step appeared to be protonation of the alkene. The performance of the Al3+-clay catalyst was increased by reducing the water content of the clay. In most reactions the clay catalysts were equilibrated at 12% relative humidity. Exposure of the clay to a low vacuum (10−1 torr) before use increased its catalytic activity from 50 to 60% of that of Amberlyst 15.

Type
Research Article
Copyright
Copyright © 1986, The Clay Minerals Society

References

Adams, J. M., Clapp, T. V. and Clement, D. E., 1983 Catalysis by montmorillonites Clay Miner. 18 411421.CrossRefGoogle Scholar
Adams, J. M., Clement, D. E. and Graham, S. H., 1981 Low temperature reaction of alcohols to form t-butyl ethers using clay catalysts J. Chem. Res. S254 255.Google Scholar
Adams, J. M., Clement, D. E. and Graham, S. H., 1982 Synthesis of methyl-t-butyl ether from methanol and isobutene using a clay catalyst Clays & Clay Minerals 30 129134.CrossRefGoogle Scholar
Adams, J. M., Clement, D. E. and Graham, S. H., 1983 Reactions of alcohols with alkenes over an aluminum-exchanged montmorillonite Clays & Clay Minerals 31 129136.CrossRefGoogle Scholar
Ancillotti, F., Masi Mauri, M. and Pescarollo, E., 1977 Ion exchange resin catalyzed addition of alcohols to olefins J. Catal. 46 4957.CrossRefGoogle Scholar
Ancillotti, F., Massi Mauri, M., Pescarollo, E. and Romagnoni, L., 1978 Mechanisms in the reaction between olefins and alcohols catalyzed by ion-exchange resins J. Mol. Catal. 4 3748.CrossRefGoogle Scholar
Anonymous, 1967 Amberlyst 15 Synthetic Resin Catalyst Pennsylvania Rhom and Haas Co., Philadelphia.Google Scholar
Bylina, A., Adams, J. M., Graham, S. H. and Thomas, J. M., 1980 Chemical conversions using sheet silicates: simple method for producing methyl t-butyl ether J. Chem. Soc. Chem. Comm. 10031004.CrossRefGoogle Scholar
Csikos, R., Laky, J., Pallay, I., and Vajta, L. (1975) Ether additives for gasoline: Ger. Offen. DE 2, 444, 528, 4 pp.Google Scholar
Diddams, P. A., Thomas, J. M., Jones, W., Ballantine, J. A. and Purnell, J. H., 1984 Synthesis, characterization, and catalytic activity of beidellite-montmorillonite layered silicates and their pillared analogues J. Chem. Soc. Chem. Comm. 13401342.CrossRefGoogle Scholar
Gates, B. C. and Rodriguez, W., 1973 General and specific acid catalysis in sulphonic acid resin J. Catal. 31 2731.CrossRefGoogle Scholar
Gicquel, A. and Torck, B., 1983 Synthesis of methyl tertiary butyl ether catalyzed by ion-exchange resin. Influence of methanol concentration and temperature J. Catal. 83 918.CrossRefGoogle Scholar
Gregory, R. and Westlake, D. J. (1982) Method of promoting the activity of cation-exchangeable layered clay and zeolite catalysts in proton-catalyzed reactions: European Patent Application 0045618A2, 17 pp.Google Scholar
Gregory, R. and Westlake, D. J. (1983) Use of stabilized pillared interlayered clays as catalysts in reactions capable of catalysis by protons: European Patent Application 0083970Al, 23 pp.Google Scholar
Gupta, J. C. and Prakash, J., 1980 MTBE technology Chem. Eng. World 15 2731.Google Scholar
Hojabri, F., 1971 Dimerization of propylene and its uses for isoprene manufacture J. Appl. Chem. Biotech. 21 8789.CrossRefGoogle Scholar
Morikawa, Y., Wang, F., Moro-oka, Y. and Ikawa, T., 1983 Conversion of methanol to low molecular weight hydrocarbons over Ti ion-exchanged form of layered silicate minerals Chem. Letters 965968.CrossRefGoogle Scholar
Mortland, M. M. and Raman, K. V., 1968 Surface acidity of smectites in relation to hydration, exchangeable cation, and structure Clays & Clay Minerals 16 393398.CrossRefGoogle Scholar
Muddaris, G. R. and Pettman, M. J., 1980 Now, MTBE from butane Hydrocarbon Processing Int. Ed. 59 9195.Google Scholar
Nishizawa, T., Tokumaru, T., Kamiyama, Y., and Watanabe, Y. (1974) Gasoline composition with high octane number: Japan Kokai 74, 26, 306, 44 pp.Google Scholar
Norrish, K. and Raussell-Colom, J. A., 1962 Effect of freezing on the swelling of clay minerals Clay Min. Bull. 5 916.CrossRefGoogle Scholar
Occelli, M. L. and Tindwa, R. M., 1983 Physiochemical properties of montmorillonite interlayered with cationic oxyaluminum pillars Clays & Clay Minerals 31 2228.CrossRefGoogle Scholar
Pecci, G. and Floris, T., 1977 Ether ups anti-knock of gasoline Hydrocarbon Processing Int. Ed. 56 98102.Google Scholar
Pinnavaia, T. J., Tzou, M. S., Landau, S. D. and Raythatha, R. H., 1984 On the pillaring and determination of smectite clay catalysts by polyoxocations of aluminium J. Mol. Catal. 27 195212.CrossRefGoogle Scholar
Purnell, J. H. and Ballantine, J. A., 1984 Competitive intercalation and intercalary kinetics J. Mol. Catal. 27 169178.CrossRefGoogle Scholar
Süd-Chemie, A.G., 1985 K-Catalysts Munich, Federal Republic of Germany Süd-Chemie AG 2.Google Scholar
Vaughan, D. E. W., Lussier, R. J. and Rees, V. C., 1980 Preparation of molecular sieves based on pillared interlayered clays (PILC) Proc. 5th Int. Conf. Zeolites, Naples, 1980, L. London Heyden 94101.Google Scholar
Vaughan, D. E. W., Lussier, R. J., and Maggee, J. S. (1979) Pillared interlayered clay materials useful as catalysts and sorbents: U.S. Patent 4,176,090, 9 pp.Google Scholar
Vaughan, D. E. W., Lussier, R. J., and Maggee, J. S. (1981) Pillared interlayered clay products: U.K. Patent Application GB 2,059,408A, 5 pp.Google Scholar
Watanabe, Y., Kobayashi, J., and Nishizawa, T. (1973) Modifying agents raising octane number of gasoline: Japan Kokai 73,23,803, 4 pp.Google Scholar
Weiss, A., Fahn, R. and Hofmann, U., 1952 Skeletal structure in thixotropic gels Naturwissenschaften 89 351352.CrossRefGoogle Scholar