The efficiency of arsenic removal from source waters and artificial fr
eshwaters during coagulation with ferric chloride and alum was examine
d in bench-scale studies. Arsenic(V) removal by either ferric chloride
or alum was relatively insensitive to variations in source water comp
osition below pH 8. At pH 8 and 9, the efficiency of arsenic(V) remova
l by ferric chloride was decreased in the presence of natural organic
matter. The pH range for arsenic(V) removal with alum was more restric
ted than with ferric chloride. For source waters spiked with 20 mu g/L
arsenic(V), final dissolved arsenic(V) concentrations in the product
water of less than 2 mu g/L were achieved with both coagulants at neut
ral pH. Removal of arsenic(III) from source waters by ferric chloride
was both less efficient and more strongly influenced by source water c
omposition than removal of arsenic(V). The presence of sulfate (at pH
4 and 5) and natural organic matter (at pH 4 through 9) adversely affe
cted the efficiency of arsenic(III) removal by ferric chloride. Arseni
c(III) could not be removed from source waters by coagulation with alu
m.