Studies were performed on the separation of pyridine/water solutions u
sing pervaporation. Organic permeation experiments were performed usin
g a 'silicalite'-filled silicone composite membrane. Effects of feed c
oncentration, feed temperature, and permeate side pressure were examin
ed. Benchmark conditions of 5.0 wt% pyridine, 50 degrees C, and 2 torr
were chosen. At the benchmark conditions, an organic selectivity of 3
4 and a permeate flux of 0.428 kg/m(2) . h was achieved. An increase i
n feed concentration caused an increase in both the permeate concentra
tion and flux, but caused a decrease in the selectivity. Also, permeat
e compositions far exceeded standard vapor-liquid equilibrium. Tempera
ture had an Arrhenius-type relationship with regard to flux, but had n
o effect on the selectivity. Increasing the permeate pressure caused a
steady decrease in permeate flux and also decreased the permeate comp
osition and selectivity.