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US 8,721,898B2 34 tank to accelerate mass transfer as well as electrodes to break down contaminants atafasterrate. Thus anobjectiveoftheinventionistoprovidean improved cavitation reactor cone to treat ?uids, the ?uids subjected to ozone saturation and ?ash mixed with hydro dynamiccavitationanddualfrequencyultrasonictransducers to initiate dissolved as ?otation of oils and suspended solids and the conversion of ozone to hydroxyl radicals. Yetstilanotherobjectiveoftheinventionistodisclosethe use of a cavitation reactor cone that can be used in treatment of most any type of ?uid by providing an effective means to destroyaerobicandanaerobicbacteria,andprovideareduc tionincontaminants. Still another objective of the invention is to provide an improved cavitation reactor cone that eliminates the need for biocideandanti-scalantchemicaltypicallyemployedinfrac waters. Still another objective of the invention is to provide a processtoreducescalingtendencieswithouttheaidofacid, 20 ionexchangeprocesses,orantiscalingchemicals. Yetstilanotherobjectiveoftheinventionistoaprocessfor loweringscalingtendenciesinfrac,?owbackwater,byreduc ing the Langelier Saturation Index to below zero. Anotherobjectiveoftheinventionisemploynano-cavita 25 tionimplodingbubblestoprovidetheliquidgasinterfacethat isinstantaneouslyheatedtoapproximately900degreesFahr enheitwhich oxides alorganic compounds through sonolu minescence. Stillanotherobjectiveoftheinventionistoprovidean 30 improved cavitation reactor cone for an on-site process that willlowerthecostofoilproductsbyreducingthecurrentand expensive processes used for off-site treatment of waste ?u ids. Another objective of the invention is to provide an 35 improved cavitation reactor cone for on-site process that will extend the life of ?elds and increase the extraction rate per well. FIG. 2 is a sectional perspective view of the cavitation reactorcone shown inFIG. 1. FIGS.3Aand3Baredifferentsideviewsofthecavitation reactor cone of FIG. 1. FIG. 4 is a cross sectional view of a transducer assembly andmounting?angearrangement. FIG.5isacrosssectionalviewofFIG.3B takenalonglines BB ofFIG.3B. FIG. 6 is a cross sectional top view of the cavitation reactor conetakenalonglinesAA ofFIG.3A. FIG. 7 is top view of the treatment tank of FIG. 1 without a cover plate. FIG. 8 is a top view of the cover for the treatment tank of FIG. 1. FIG. 9 is a perspective view of a truck trailer designed to disinfect water on the ?y prior to the hydro fracing process. FIG. 10 is a perspective view of a truck trailer designed to process frac ?ow back and produces water and clean brine that is free from bacteria. FIGS. 11A, 11B and 11C illustrate an alternative ?ow diagramforprocessing?ow backwateratthewellsite. FIG. 12 illustrates the cavitation reactor cone used in the ?ow processing shown inFIGS. 1111through 11C. FIG. 13 is a cutaway perspective view of a truck trailer containingtheequipmentnecessaryforprocessingthe?ow back water at the well site. FIGS. 14A and 14B are data tables representing two samples of ?ow back water. Each data table sets forth the contaminantswithinthe?ow backwaterpriortotreatmentin themainreactiontankascomparedtothesamecontaminants subsequent to treatment in the main reaction tank. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT Now referringtotheFiguresingeneral,FIG.1illustrates the improved cavitation reactor cone 700 of the instant inven tion having a generally cone shaped con?guration. The cavi tation reactor cone includes four ultrasonic transducers assemblies702,704,706and708.Eachtransducerisratedat Still another objective of the instant invention is to teach thecombinationofultrasonicandhydrodynamicagitationin40 conjunctionwithozoneintroductionintoaclosedpressurized approximately500watts.Threeofthetransducerassemblies; generally cone shaped container whereby the cavitations cause disruption of the materials allowing the ozone to fully interactwiththecontaminated?ow backwaterforenhance mentofseparationpurposes.Inaddition,anodesinthecon 45 tainerprovideDC currenttothe?owbackwatertodrivethe electro precipitation reaction for the hardness ions present withthe?ow backwater. Still another objective is to teach a process of enhanced ozoneinjectionwhereinozonelevelscanbereducedbemade 50 more effective. Another objective of the invention is to provide a cost effectiveandenvironmentallyfriendlyprocessandapparatus for cleaning and recycling frac water at the well site using transportableequipment. 55 Other objectives and advantages of this invention will become apparent from the following description taken in conjunctionwiththeaccompanyingdrawingswhereinareset forth, by way of illustration and example, certain embodi mentsofthisinvention.Thedrawingsconstituteapartofthis60 speci?cation and include exemplary embodiments of the present invention and illustrate various objects and features thereof. BRIEFDESCRIPTIONOFTHEDRAWINGS 65 FIG.1isperspectiveviewofacavitationreactorcone. 702, 704 and 706 are located at the upper portion of the cavitation reactor cone 700 and are spaced approximately 120 degrees apart from one another around the upper portion of thetank.Eachofthesetransducersisdirectedtowardsa longitudinalcenterlineofthetank700.Thefourthtransducer, 708,islocatedatthebottomofthegenerallyconeshapedtank and is directed in a direction that is upwards into and gener ally along the longitudinal centerline of the tank. The tank includesaninlet710communicatingwith?owconduit712 thatexitsintoatangentiallyorientedtankinlet714 (asshown in FIG. 15) located adjacent the upper end of tank 700. Flow conduit 712 is curved to conform to the shape at the outer periphery of tank 700. The tank 700 also includes an outlet 716 located at the bottom of the tank near what would be identi?ed as the tip of the generally cone shaped tank. Locatedattheverytopofthecone shapedtankisaremovable circular cover plate 718. A plurality of holes are formed around the periphery of plate 718 and are sized and con?g uredtoreceivefastenersthatarethreadedintotheupper peripheral wall of cone shaped tank 700 thereby sealing the upper end of the tank. As canbestbe seeninthesectionalview oftank700 inFIG. 2 the cover 718 supports a plurality of electrodes 720 that extendintothetank700.Electrodes720areplatinumcoated and electrically charged to precipitate hardness salt on the surface ofthe cone shaped tank. The electrodes 720 arePDF Image | REACTOR TANK
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