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Removal of sulfide from a micro-aerobic bio-reactor was studied at 10 000 mg L −1  chemical oxygen demand (COD) of inlet water, with the sulfate volumetric loading 0.75, 1.0, 1.5 and 2.0 kg (m −3  d −1 ), respectively.

rsc advances

Effect of sulfate removal in a high sulfate volumetric loading micro-aerobic bio-reactor and study of subsequent bio-sulfur adsorption by iron-modified activated carbon