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Title: Treatment of refinery wastewaters using various modified activated sludge processes

Thesis/Dissertation ·
OSTI ID:6711151

Biological processes for treating refinery industry wastewater for reuse were studied. A pilot-scale biological reactor was constructed to simulate the activated sludge treatment process. Actual refinery industry wastewater collected from a regional refinery and spiked with additions of selected priority organics was fed at a rate of 1.3 liters/hour into a 6-liter pilot plant having a hydraulic retention time of 4 hours. Activated sludge (AS) which was augmented by additions of powdered activated carbon (PAC) at dosages of 10, 50 and 120 mg/l was evaluated. The AS process removed 70-80% of the BOD, COD and TOC. With the addition of PAC, removal efficiencies of the indicator compounds rose to 80-95%. The sludge physical parameters and kinetic constants were determined with and without the addition of PAC to the AS. PAC additions to the AS increased the amount of biomass in the reactor. Volatile compounds (benzene, chloroform, ethylbenzene, toluene, m-xylene and o-xylene) were removed from the reactor by volatilization which occurred from air stripping. PAC alone (without AS) was primarily responsible for removing base and acid/neutral-extractable compounds (2,4-dimethylphenol, fluorene, naphthalene and pyrene).

Research Organization:
Rhode Island Univ., Kingston (USA)
OSTI ID:
6711151
Resource Relation:
Other Information: Thesis (Ph. D.)
Country of Publication:
United States
Language:
English