in ozone production compared to what the ozone generator could produce at ambient pressure conditions under this arrangement ozone can be supplied at a flow rate of for example 0 5 u2013 50 cubic feet per hour cfh of ozone and 2 to 20 cubic feet per minute of air an exemplary set of rates is for 2 inch wells 3 u2013 5 cfm total gas air and ozone with ozone being 1 20 th to 1 100 th of the total volume the fine bubbles promote rapid gas gas water reactions with volatile organic compounds in which a substrate catalyst or enhancer participates in instead of solely enhancing dissolved aqueous disassociation and reactions the production of microbubbles and selection of appropriate size distribution is provided by using microporous material and a bubble chamber for optimizing gaseous exchange through high surface area to volume ratio and long residence time within the liquid to be treated the equipment promotes the continuous production of microbubbles while minimizing coalescing or adhesion the injected air ozone combination moves as a fluid into the material to be treated the use of microencapsulated ozone enhances and promotes in situ stripping of volatile organics and simultaneously terminates the normal reversible henry s reaction the process involves promoting simultaneous volatile organic compounds voc in situ stripping and gaseous decomposition with moisture water and substrate catalyst or enhancer the basic chemical reaction mechanism of air ozone encapsulated in microfine bubbles is further described in several of my issued patents such as u s pat no 5 855 775 us patent all of which are incorporated herein by reference the compounds commonly treated are hvocs halogenated volatile organic compounds pce tce dce vinyl chloride vc edb petroleum compounds aromatic ring compounds like benzene derivatives benzene toluene.