The gas phase hydrodechlorination of methanolic and mixed methanol/water so
lutions of 2-chlorophenol, 2,6-dichlorophenol, 2,4,5-trichlorophenol and pe
ntachlorophenol has been studied at 573 K over nickel/silica catalysts of v
arying (1.5-20.3 wt.% Ni) nickel loading. Each catalyst was 100% selective
in promoting hydrodechlorination; the variation of catalytic activity and s
electivity with time-on-stream is illustrated and catalyst deactivation is
addressed. Dechlorination is quantified in terms of specific rate constants
, phenol selectivity/yield and chlorine removal efficiencies. Increasing th
e nickel loading resulted in a marked increase in dechlorination efficiency
while the introduction of water into the fed lowered the activity.