Page 474 - Advanced Organic Chemistry Part A - Structure and Mechanisms, 5th ed (2007) - Carey _ Sundberg
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to reduce pollution from partial combustion. In the 1980s methyl t-butyl ether (MTBE)  455
          was introduced as a major antiknock component, but it was soon discovered that
          MTBE contaminated groundwater as a result of leakage and spillage. 157  It is being  TOPIC 4.1
          phased out as a gasoline performance enhancer. 158  As a result, new emphasis has been  The Role Carbocations
                                                                                    and Carbonium Ions in
          placed on catalytic reforming as a means of meeting engine performance requirements.  Petroleum Processing
              A possible replacement for MTBE is the mixture of branched C hydrocarbons
                                                                   8
          prepared by dimerization of C compounds. 159  This is economically attractive since
                                    4
          the C compounds are by-products of other stages of petroleum refining. Isobutane
               4
          and isobutene react with strong acid to give C products. 160  The reaction involves
                                                  8
          intermolecular hydride transfers.
            CH 3         H +
                C   CH 2     (CH ) C +
                                3 3
            CH 3
                               CH 3
                                                    +
            (CH ) C +   CH 2  C           (CH 3 ) 3 CCH 2 C (CH 3 ) 2
               3 3
                               CH 3
                       +
             (CH ) CCH C (CH )  +  H  C(CH3)3       (CH ) CCH CH(CH )  +  + C(CH )
                          3 2
               3 3
                     2
                                                      3 3
                                                            2
                                                                  3 2
                                                                            3 3
          The same kind of product can be obtained by acid-catalyzed dimerization of isobutene,
          followed by hydrogenation.
           CH 3        H +
               C  CH 2      (CH ) C +
                               3 3
           CH 3
                          CH 3
                                            +
           (CH ) C +  H C  C      (CH ) CCH C (CH )        (CH ) CCH  C(CH )  +
                                                3 2
                                     3 3
             3 3
                                          2
                   2
                                                                          3 2
                                                              3 3
                          CH 3
                                                          H 2    (CH ) CCH C  CH 2
                                                                         2
                                                                   3 2
                                       (CH ) CCH CH(CH )                 CH 3
                                               2
                                                     3 2
                                          3 3
          The hydrocarbon mixtures formed by these processes have octane numbers ranging
          from 90 to 95.

              Cracking, which is done at high temperatures  480–550 C  in flow reactors
          with short contact times (seconds), converts high-boiling components of petroleum
          to hydrocarbons in the gasoline-boiling range. The catalysts are rapidly degraded
          and are regenerated by high-temperature  700 C  exposure to air. 161  The product

          mixture is complex but is enriched in hydrocarbons in the gasoline range. Low-boiling
          hydrocarbons such as methane and ethane are produced as by-products. Reactivity
          toward cracking increases with molecular weight and branching. Carbocations are
          intermediates in the cracking process, which leads to isomerizations.
          157   S. Fiorenza, M. P. Suarez, and H. S. Rifai, J. Envir. Eng., 128, 773 (2002); S. Erdal and B. D. Goldstein,
             Ann. Rev. Energy Environ., 25, 765 (2000).
          158
             A. K. Kolah, Q. Zhiwen, and S. M. Mahajani, Chem. Innovation, 31, 15 (2001).
          159   J. M. Meister, S. M. B. Black, B. S. Muldoon, D. H. Wei, and C. M. Roesseler, Hydrocarbon Process.,
             79, 63 (2000).
          160   G. A. Olah, P. Batamack, D. Deffieux, B. Toeroek, Q. Wang, A. Molnar, and G. K. S. Prakash, Appl.
             Catal. A, 146, 107 (1996).
          161
             Y. V. Kissin, J. Catal., 126, 600 (1990); Y. V. Kissin, Catal. Rev., 43, 85 (2001).
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