The increased demand for isobutene, used for the production of the oct
ane-enhancer methyl tert-butyl ether, has generated tremendous interes
t in the catalytic conversion of the linear butenes to isobutene. In t
his review we survey the progress made since the late 1970s in impleme
nting the catalytic skeletal isomerization reaction of these linear al
kenes. Halogenated catalysts, especially those based on alumina, and p
repared using a variety of compounds of fluorine, chlorine or bromine,
have been shown to exhibit both high conversions and selectivities fo
r the reaction, resulting in high yields of isobutene, when water is a
dded to the feed stream. Elution of the halogen from the catalyst lead
s to the loss of catalytic activity and necessitates the continuous or
discontinuous addition of the halogen compound. As a consequence, env
ironmental and other considerations are most likely to weigh against t
he industrial usage of these catalysts. Another class of catalysts exh
ibiting high activities and selectivities, again in the presence of wa
ter, are the silicated aluminas. No information is, however, available
on their long-term stability. Even alumina on its own displays high a
ctivity and selectivity, provided water is co-fed with the hydrocarbon
stream. More recent results obtained over other types of catalysts su
ch as zeolites and molecular sieves are also presented. Most promising
are the results obtained with the zeolite ferrierite which gives high
yields of the branched isomer in the absence of any other additive or
diluent. The catalyst also appears to be fairly stable showing no dec
rease in the yield of isobutene after 14 days on-stream. The high yiel
ds of isobutene can be ascribed to the small channel diameters which p
revent the extensive dimerization or oligomerization of the linear but
enes or of the product isobutene. Plans for the first large-scale demo
nstration plant to produce isobutene from n-butenes using ferrierite a
s catalyst have already been announced in the United States.