The cyclodehydration of 1,4-butanediol over cobalt catalysts in the liquid
phase is used for the production of 2,3-dihydrofuran. The catalyst preparat
ion parameters considered were the metal loading, precipitation pH and redu
ction temperature of cobalt salt. It was found that the use of Co(NO3)(2) t
ogether with Na2CO3 in a 1:1 ratio yielded better catalysts. Under the cond
itions used in this study the optimum cobalt loading for the selective prod
uction of 2,3-dihydrofuran is in the range 15-50 wt%. The optimum reduction
temperature of Co/porcelain catalyst depends on cobalt loading. The optimu
m reduction temperatures for 15 and 50 wt% cobalt loading are 773 and 723 K
(reduction time 20 min), respectively. (C) 2001 Society of Chemical Indust
ry.