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Title: Volatilization of organic compounds in an aerated stirred-tank reactor

Miscellaneous ·
OSTI ID:5119528

Volatilization must be considered as a removal mechanism when treating waste-waters containing volatile organic compounds (VOC's). This study investigated the simultaneous mass transfer of oxygen and three organic compounds in an aerated stirred tank reactor to determine if the ratio of the two mass transfer coefficients, K{sub L}a{sub VOC}/k{sub L}a{sub O2}, can be used to predict volatilization rates for semi-volatile compounds. This work expands the range of compound volatility and the types of waters investigated to semi-volatile organic compounds in water containing an anionic surfactant over a larger power range than previously studied. The mass transfer coefficients of oxygen and three VOC's: toluene, dichloromethane, and 1,2-dichlorobenzene, were determined in three water systems: tap water, tap water with an anionic surfactant, dodecyl sodium sulfate (DSS), and tap water with biomass (k{sub L}a{sub O2} only). A steady state method was used. Experiments were made to span the range of mass transfer coefficients found in both municipal and industrial wastewater treatment processes. The results were analyzed using dimensional analysis.

Research Organization:
California Univ., Los Angeles, CA (United States)
OSTI ID:
5119528
Resource Relation:
Other Information: Thesis (Ph.D.)
Country of Publication:
United States
Language:
English