Continuous extraction and destruction of chloro-organics in wastewater using ozone-loaded Volasil™245 solvent

• Published in: Journal of hazardous materials 2005-10, Vol.125 (1), p.65-79
• Main Authors: Ward, D.B., Tizaoui, C., Slater, M.J.
• Format: Article
• Language: English
• Subjects: Chloro-organics; Indirect ozonation; Liquid–liquid extraction; Ozone; Wastewater treatment
• ISSN: 0304-3894; 1873-3336
• DOI: 10.1016/j.jhazmat.2005.01.002

Extracting waterborne contaminants to ozone-loaded Volasil™245 (a siloxane solvent in which ozone is ten times more soluble than water) has been studied as a means of enhancing reaction kinetics and thus, providing more rapid wastewater decontamination. Investigation was carried out with respect to 2-chlorophenol and dichloromethane. Using a pilot scale continuous flow liquid–liquid/ozone water treatment system, 2-chlorophenol was extracted to the ozone-loaded solvent phase and considerable extents of destruction were achieved. However, the approach was demonstrated to yield slightly less destruction than direct gas contact for the same utilization of ozone and enhanced reaction kinetics were not shown to occur. This was suggested to be due to increased interfacial mass transfer resistance and/or the promotion of less destructive reaction pathways. Modification of the existing pilot system, by conversion from co- to counter-current solvent-loading, enabled greater dissolved ozone concentrations to be achieved within the solvent. Increasing the counter-current exchange column height to ∼2.5 m was suggested for achieving a near optimum level of performance. The liquid–liquid/ozone approach was demonstrated to be an effective means of indirectly exposing wastewater contaminants to concentrated ozone. As such the technology may be applicable as an alternative to direct gas contact in instances where the avoidance of contaminant sparging is desired (i.e. where contaminants are highly volatile, pungent and/or toxic) or foaming occurs.