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Title: Fixed-film, fluidized-bed bioreactors for biooxidation of coal conversion wastewaters. Progress report, October 1, 1984-September 30, 1985

Technical Report ·
DOI:https://doi.org/10.2172/5953994· OSTI ID:5953994

The technical feasibility of biooxidation treatment of 50% strength actual wastewater was successfully demonstrated using a fluidized-bed bioreactor. The wastewater was stripped to remove ammonia and sulfides prior to biotreatment. Additional experimental and modeling work confirmed the need to supply substantial oxygen to maintain high reaction rates. The reaction kinetics were shown to depend on the physical characteristics of the biofilms. Dynamic modeling and experimental studies have shown that classical reaction and diffusion concepts used in catalysis are adequate to describe the dynamic behavior of bench-scale bioreactors when the pH is constant. Oscillations in the reaction rate and phenol concentration were seen when the pH was not controlled. A status summary of the fluidized-bed bioreactor process for biooxidation of organics in coal gasification wastewaters is presented.

Research Organization:
Oak Ridge National Lab. (ORNL), Oak Ridge, TN (United States)
DOE Contract Number:
AC05-84OR21400
OSTI ID:
5953994
Report Number(s):
ORNL/TM-9806; ON: DE86010000
Resource Relation:
Other Information: Portions of this document are illegible in microfiche products. Original copy available until stock is exhausted
Country of Publication:
United States
Language:
English