The catalytic behavior of WOx/gamma-Al2O3 (having different tungsten loadin
g) during the 1-butene skeletal isomerization at 380 degrees C, atmospheric
pressure, and 0.15 atm 1-butene partial pressure was measured. Catalysts w
ere prepared by impregnation using an equilibrium-adsorption technique, bei
ng characterized by specific surface area and cumulative pore volume measur
ements, temperature-programmed reduction (TPR), ammonia temperature-program
med desorption (NH3-TPD), X-ray photoelectron spectroscopy (XPS), laser Ram
an spectroscopy (LRS), and microcalorimetric measurements. After a standard
calcination procedure the isobutene production (which was practically cons
tant with time-on-stream) reached a maximum when increasing the tungsten lo
ading. After 240 min of reaction the catalytic bed showed two layers: the u
pper part of the bed is completely black and the bottom is light brown. By
modifying the calcination conditions, the isobutene production is decreased
with time and the catalyst finished completely black all along the bed. Te
mperature-programmed oxidation (TPO) analysis indicated that the coke depos
ited during the reaction burns at high temperature independently of both tu
ngsten loading and calcination conditions, mainly differing in the total am
ount. Product distribution shows the absence of C-1 and C-2 and a C-3/C-5 r
atio of practically one; then it can be considered that Cg intermediate spe
cies are formed. According to these data, deactivation could take place fro
m a common intermediate, which can either desorb isobutene or produce coke,
in a parallel-type deactivation mechanism. (C) 1999 Elsevier Science B.V.
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