Title of Invention	OZONE CLEANING SYSTEM
Abstract	An industrial cleaning system 10 that produces and distributes an aqueous ozone solution is described. The system 10 includes an ozone generator 240 for generating ozone gas, which is injected by an injector 310 into a supply of water to form the aqueous ozone solution. A reaction vessel 350 receives the aqueous ozone solution from the injector 310 as the reaction vessel 350 reduces the bubbles of ozone gas in the aqueous ozone solution to increase the oxidation reduction potential of the aqueous ozone solution. The reaction vessel 350 includes a conical-shaped surface 385 having two or more edges 380 or ridges 382. The conical-shaped surface 385 defines a generally hollow interior 388. An inlet port 355 is in fluidic communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution to the conical-shaped surface 380. Nozzles 360 direct water under pressure at the conical-shaped surface 380, and the water mixes with the aqueous ozone solution from the inlet port 355. An outlet 390 is in fluidic communication with the industrial cleaning system 10. A method of making an aqueous ozone solution is described. The reaction vessel 350 is in fluidic communication with a supply of a first aqueous ozone solution. The first aqueous ozone solution is directed to the reaction vessel 350. Water is directed to the reaction vessel 350, and the water and the first aqueous ozone solution are mixed to form a second aqueous ozone solution. Compositions for aqueous ozone solutions are also described. The aqueous ozone solution contains approximately 1 part by volume water mixed with approximately 4 parts by volume to approximately 9 parts by volume of the first aqueous ozone solution to form the second aqueous ozone solution that has an oxidation reaction potential of up to approximately 2.6 and having an ozone concentration of up to approximately 20 ppm.

Title of Invention

OZONE CLEANING SYSTEM

Abstract

An industrial cleaning system 10 that produces and distributes an aqueous ozone solution is described. The system 10 includes an ozone generator 240 for generating ozone gas, which is injected by an injector 310 into a supply of water to form the aqueous ozone solution. A reaction vessel 350 receives the aqueous ozone solution from the injector 310 as the reaction vessel 350 reduces the bubbles of ozone gas in the aqueous ozone solution to increase the oxidation reduction potential of the aqueous ozone solution. The reaction vessel 350 includes a conical-shaped surface 385 having two or more edges 380 or ridges 382. The conical-shaped surface 385 defines a generally hollow interior 388. An inlet port 355 is in fluidic communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution to the conical-shaped surface 380. Nozzles 360 direct water under pressure at the conical-shaped surface 380, and the water mixes with the aqueous ozone solution from the inlet port 355. An outlet 390 is in fluidic communication with the industrial cleaning system 10. A method of making an aqueous ozone solution is described. The reaction vessel 350 is in fluidic communication with a supply of a first aqueous ozone solution. The first aqueous ozone solution is directed to the reaction vessel 350. Water is directed to the reaction vessel 350, and the water and the first aqueous ozone solution are mixed to form a second aqueous ozone solution. Compositions for aqueous ozone solutions are also described. The aqueous ozone solution contains approximately 1 part by volume water mixed with approximately 4 parts by volume to approximately 9 parts by volume of the first aqueous ozone solution to form the second aqueous ozone solution that has an oxidation reaction potential of up to approximately 2.6 and having an ozone concentration of up to approximately 20 ppm.

Full Text	OZONE CLEANING SYSTEM Field of Invention [0001] The present invention relates to a system of providing an aqueous solution of ozone for industrial cleaning applications. The present invention relates to a reaction vessel for entraining ozone gas in an aqueous solution of ozone for industrial cleaning applications. The present invention relates to a method of producing an ozone solution and a composition of an ozone solution. Background of Invention [0002] Ozone in a solution has been previously used for cleaning and sanitizing. Maintaining a solution with a consistent ozone concentration has proven difficult. Ozone is unstable, which provides for it cleaning and sanitizing capabilities, but also makes consistent ozone levels difficult to maintain in a solution. If the ozone solution has too much ozone or large bubbles of ozone, then off-gassing problems may occur, as the excess ozone is released into the work facility creating environmental problems and possible violating workplace safety regulations. If the solution has too little ozone, then the cleaning and sterilizing may not be as effective as desired. [0003] Other systems utilize a spraying device that simultaneously sprays two separate streams of water and an ozone solution. The stream of water is applied at high pressure for removing particles and the ozone solution is applied for sanitizing. [0004] Ozone solutions have proven difficult to consistently and uniformly prepare in sufficient quantities required for industrial cleaning applications. Summary of Invention [0005] The system produces an aqueous ozone solution to attack and destroy pathogens and to act as a no-rinse sanitizer for hard surfaces in a variety of applications, especially for industrial cleaning applications in facilities related to food processing. The system includes a reaction vessel that entrains ozone gas in an aqueous ozone solution. Methods of making aqueous ozone solutions for industrial cleaning systems are described. Compositions for aqueous ozone solutions for use with industrial cleaning systems are also described. [0006] The system, the reaction vessel, the aqueous ozone solution may be used for many different sanitation applications in many different industries and facilities. For example, the system, reaction vessel, and aqueous ozone solution may be used in cosmetic manufacturing facilities, hospitals, fast food outlets, individual homes, etc. The system, reaction vessel, and the aqueous ozone solution may be used with a variety of different "clean in place" systems, such as, for example, water-bottling facilities and equipment, breweries and brewing equipment, ethanol processing facilities, water-bottling facilities and equipment, snack food processing facilities, cooling towers etc. The use of the system, the reaction vessel, and the aqueous ozone solution is not limited to any particular type of industry or application type. [0007] The reaction vessel includes a conical-shaped surface having a plurality of edges or ridges. The conical-shaped surface defines a generally hollow interior, and the plurality of edges or ridges are in contact with the generally hollow interior. An inlet port is in fluidic communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution to the conical-shaped surface. Nozzles are in fluidic communication with a supply of water, and the nozzles direct the water under pressure at the conical-shaped surface, and the water mixes with the aqueous ozone solution from the inlet port. An outlet is in fluidic communication with the industrial cleaning system. The reaction vessel may receive the aqueous ozone solution from an injector. The reaction vessel reduces the number and size of bubbles of ozone gas in the aqueous ozone solution and entrains the bubbles of ozone gas in the aqueous ozone solution to increase the oxidation reduction potential of the aqueous ozone solution. [0008] The system comprises an ozone generator for producing ozone gas. The ozone generator directs the ozone gas to the injector, which is also in communication with the supply of water. The injector injects ozone gas from the ozone generator into the water from the supply of water to form the aqueous ozone solution. The reaction vessel receives the aqueous ozone solution from the injector and additional water from the water supply. A pump in communication with the reaction vessel distributes the aqueous ozone solution to the hard surfaces for cleaning the hard surfaces. [0009] The system and the reaction vessel reduces the amount of bubbles and the bubble size of the ozone gas in the aqueous ozone solution, which allows for the system and reaction vessel to produce an aqueous ozone solution with a greater concentration of ozone gas and a higher oxidation reduction potential. Since the bubbles of ozone are smaller and fewer than the bubbles of ozone in a typical ozone solution, the system and reaction vessel allows the aqueous ozone solution to contain a greater amount of ozone and have the higher oxidation reduction potential. This provides for a more effective cleaning and sanitizing system. [0010] The reaction vessel may be used with a variety of industrial cleaning systems. In the system described herein, the system entrains ozone gas into water, forming the aqueous ozone solution and delivers the aqueous ozone solution to the reaction vessel for further entraining and concentrating of the ozone gas into the aqueous ozone solution. The system provides an applied dosage of an aqueous ozone solution that is consistent over time in terms of concentration and flow rate. [0011] The aqueous ozone solutions serve as a cleaning and sterilizing agent. Systems for making and applying the aqueous ozone solutions are also described. In one embodiment, the method of making the aqueous ozone solution for the industrial cleaning system includes providing the reaction vessel for entraining the ozone gas in the aqueous solution. The reaction vessel includes the conical-shaped surface having the plurality of edges or ridges. The conical-shaped surface defines the generally hollow interior, and the plurality of edges or ridges are in contact with the interior. The reaction vessel is in fluidic communication with the supply of water. The reaction vessel is also in fluidic communication with a supply of a first aqueous ozone solution. The first aqueous ozone solution is directed to the conical-shaped surface. Water is directed to the conical-shaped surface, and the water and the first aqueous ozone solution are mixed to form a second aqueous ozone solution. [0012] In one embodiment of the composition, the aqueous ozone solution comprises approximately 1 part by volume water mixed with approximately 4 parts by volume to approximately 9 parts by volume of the first aqueous ozone solution to form the second aqueous ozone solution that has an oxidation reaction potential of up to approximately 2.6, wherein the second aqueous ozone solution has an ozone concentration of up to approximately 20 ppm, wherein the second ozone solution has less ozone gas bubbles than the first aqueous ozone solution. [0013] The first aqueous ozone solution is mixed with water in the reaction vessel to form the second aqueous ozone solution. The reaction vessel reduces the bubbles of ozone gas in the first aqueous ozone solution and entrains the remaining bubbles of ozone gas in the second aqueous ozone solution to increase the oxidation reduction potential of the second aqueous ozone solution. The reaction vessel reduces the amount of bubbles and the bubble size of the ozone gas in the first and second aqueous ozone solutions, which allows for the system to produce the second aqueous ozone solution with a greater concentration of ozone gas and a higher oxidation reduction potential. [0014] In the methods described herein for forming the aqueous ozone solution, ozone gas is entrained into water, forming the first aqueous ozone solution, which is delivered to the to the reaction vessel for further entraining and concentrating of the ozone gas into the aqueous ozone solution. The water is mixed with the first aqueous ozone solution to form the second aqueous ozone solution. [0015] In the methods described herein for forming the aqueous ozone solution, the ozone generator produces the ozone gas. The ozone generator directs the ozone gas to the injector, which is also in communication with the supply of water. The injector injects ozone gas from the ozone generator into the water from the supply of water to form the first aqueous ozone solution. The reaction vessel receives the first aqueous ozone solution from the injector and additional water from the water supply. The reaction vessel comprises the conical-shaped vessel having the plurality of edges or ridges for reducing a bubble size of the ozone gas in the first aqueous ozone solution and for mixing the water with the first aqueous ozone solution to form the second aqueous ozone solution. The pump in communication with the reaction vessel distributes the second aqueous ozone solution to the hard surfaces for cleaning the hard surfaces. [0016] The hard surfaces may include, for example, conveyor systems, processing equipment, floors, tables, etc. The solution of aqueous ozone may be applied at a high pressure to the hard surfaces, and is effective for sanitizing the hard surfaces and removing soils and bulk materials from the hard surfaces. When applied at high pressure, the solution penetrates and destroys the soils and oxides of a biofilm that acts as the bond or glue that allows the soils and oxides to attach themselves to the hard surfaces. [0017] The methods and solution may be used in the system described herein. The system is a chemical-free system that destroys the biofilm on hard surfaces during food processing production in food processing facilities. The system allows for continuous or extended production in the facility. When installed in processing facilities, the hard surfaces can be maintained 24 hours a day, 7 days a week accomplishing both a microbial reduction as well as improving aesthetics. The system allows the plant to do mid-shift sanitation or a cleaning application that the plant could not do with present conventional systems (because ozone is approved by the Food and Drug Administration for direct food contact and chemicals are not). [0018] The system provides a chemical-free, high pressure cleaning system that replaces present conventional cleaning systems. The system reduces the need for chemicals, hot water, and labor. As such, the processors operating costs may be reduced by 50%. Conventional cleaning systems often require the use of warm or hot water, which may form condensation on the hard surfaces. The condensation may provide for or encourage the growth of microbes. Because the system only uses cold water, condensation is not likely to form on the hard surfaces. The system also reduces the hydraulic load on the waste-water treatment system and eliminates the need to treat the chemicals that would be present in conventional wastewater discharge streams. [0019] Ozone gas is generally unstable (a property that gives ozone its extraordinary oxidizing capabilities). Ozone gas cannot be packaged or stored and must be generated on site. The system includes an on-site ozone generator combined with an air preparation unit and an injector to safely get the ozone into the water. As such, the system requires no drums to store ozone, records and reports relating to the drums, or disposal concerns relating to the drums. [0020] The use of ozone as cleaning and sterilizing agent is a chemical treatment like other oxidizers, including chlorine, potassium permanganate, hydrogen peroxide, etc. Ozone's extraordinary speed and power sets ozone apart from the other oxidizers, but there are rules to be followed in its application. Stoichiometric (chemical value) calculation charts and formulas are readily available for all common inorganic contaminants, including but not limited to, iron, manganese, sulfide compounds. Simple formulas for flow and contaminant loading make ozone generator sizing easy. With contact times in the 2-6 minute range for common contaminants, instead of the 20-30 minute times associated with chlorination, the system described herein is simpler, more compact and efficient than traditional cleaning treatments. Description of Figures [0021] Figure 1 shows a process flow diagram of the ozone cleaning system. [0022] Figure 2 shows a sectional view of the reaction vessel. [0023] Figure 3 shows a view of the compressed dry air supply skid. [0024] Figure 4 shows a view of the ozone generation skid. [0025] Figure 5 shows a view of the mixing skid. [0026] Figure 6 shows an alternative embodiment of the reaction vessel. Detailed Description of Preferred Embodiments [0027] An ozone system 10 for applying an aqueous solution of ozone will now be described with reference to the accompanying Figures. The system 10 provides many advantages over the prior art. The system 10 provides a centralized system for producing an aqueous ozone solution, i.e., the aqueous ozone solution is prepared and distributed from a central location in an industrial facility to different application points throughout the industrial facility. The system 10 provides for the distribution of the aqueous ozone solution at different flow rates and at different concentrations to the different application points. The system 10 monitors and maintains the ozone concentration and flow rate of the aqueous ozone solution at desired levels. The system 10 provides a uniform and consistent aqueous ozone solution without off-gassing problems. Fluctuations in the concentration of ozone in the aqueous ozone solution are kept to a minimum with the aid of monitoring systems that monitor the concentration of ozone in the aqueous ozone solution and modulate levels of ozone gas introduced into the aqueous ozone solution. The system 10 increases the oxidation reaction potential of a conventional aqueous ozone solution by reducing the bubble size of ozone gas and minimizing the amount of bubbles of ozone in the aqueous ozone solution. [0028] A process flow diagram for the system 10 is shown in Figure 1. A control panel/central server 50 comprising a programmable logic controller and user interface is in electrical communication with the components of the system 10 to operate, monitor, and direct the system 10. The control panel/central server 50 regulates the concentration of ozone in the ozonated water solution and the flow of ozonated water solution. The control panel/central server 50 is in electrical communication with the various components, systems and assemblies of the system 10 to ensure that the desired flow and concentration of the ozonated water solution are maintained. The control panel/central server 50 regulates the flow and amount of ozone gas that is entrained in the solution. The system 10 produces high pressure and high volumes of the ozonated water solution to clean and sanitize industrial facilities. The system 10 may be scaled depending upon its application, for example, the system 10 may provide lower volumes, e.g., 1 gallon per minute and higher volumes, e.g. 10,000 gallons per minute. [0029] A reaction vessel 350 is incorporated in the system 10. The reaction vessel 350 entrains ozone gas in an aqueous solution of ozone. Figure 2 shows a sectional view of the reaction vessel 350. The reaction vessel 350 reduces the bubble size of the ozone gas in the aqueous ozone solution and the number of bubbles in the aqueous ozone solution. The reaction vessel 350 increases the concentration of ozone in the aqueous ozone solution as well as its oxidation reduction potential to improve the cleaning and sanitizing capabilities of the aqueous ozone solution. Decreasing the bubble size of the ozone gas also assists in maintaining a uniform concentration of ozone gas in the aqueous ozone solution and reducing off-gassing. [0030] In the reaction vessel 350, fresh water and an aqueous ozone solution mix. The reaction vessel 350 circulates the fresh water and forms a vortex, which mixes with the aqueous ozone solution. The mixing in the reaction vessel 350 breaks the ozone gas in the aqueous ozone solution into smaller and smaller bubbles, which exit the reaction vessel 350 in the aqueous ozone solution. In reaction vessel 350, the aqueous ozone solution is forced into a saturated aqueous ozone solution having an ozone concentration of up to approximately 20 ppm and an oxidation reaction potential of up to approximately 2.6. Off-gassing of ozone gas is reduced by the reaction vessel 350. [0031] The reaction vessel 350 is in fluidic communication with a supply of the aqueous ozone solution, e.g., a venturi 310, in which an aqueous ozone solution is formed by injection of ozone gas into water in the venturi 310. The reaction vessel 350 is also in fluidic communication with a supply of water 330 for mixing with the aqueous ozone solution. After the mixing in the reaction vessel 350, the reaction vessel 350 outputs the aqueous ozone solution to a contact tank 405. [0032] The reaction vessel 350 comprises a conical-shaped surface 385 having a plurality of edges 380 or ridges 382 on the conical-shaped surface 385. The conical-shaped surface 385 imparts a rotating action or a vortex to the water entering the reaction vessel 350 from the supply of water 330, and the water rotates about the conical-shaped surface 385 toward the aqueous ozone solution entering the reaction vessel 350, which crushes ozone gas bubbles in the aqueous ozone water solution. [0033] The reaction vessel 350 is shown illustrated for use with an exemplary system 10 in Figures 1 and 3-5. One of ordinary skill in the art will recognize that the reaction vessel 350 may be used with other industrial cleaning systems that use an aqueous solution of ozone. [0034] The methods of forming the aqueous ozone solution will now be described. The methods described herein reduce the bubble size of ozone gas in the aqueous ozone solution and the number of bubbles in the aqueous ozone solution. The methods increases the concentration of ozone in the aqueous ozone solution as well as its oxidation reduction potential to improve the cleaning and sanitizing capabilities of the aqueous ozone solution. The compositions of aqueous ozone solution described herein have less bubbles and smaller bubbles of ozone gas than conventional solutions. Decreasing the bubble size of the ozone gas also assists in maintaining a uniform concentration of ozone gas in the aqueous ozone solution and reducing off-gassing. The compositions of aqueous ozone solution provide for cleaning and sanitizing of industrial facilities. [0035] Fresh water and a first aqueous ozone solution are mixed to form a second aqueous ozone solution. The reaction vessel 350 circulates the fresh water and forms a vortex, which mixes with the first aqueous ozone solution with the water. The mixing in the reaction vessel 350 of the water and the first aqueous ozone solution breaks the ozone gas bubbles in the first aqueous ozone solution into smaller and smaller bubbles and forms the second aqueous ozone solution that exits the reaction vessel 350. In reaction vessel 350, the first aqueous ozone solution is forced into a saturated aqueous ozone solution having an ozone concentration of up to approximately 20 ppm and an oxidation reaction potential of up to approximately 2.6. Off- gassing of ozone gas is reduced by the reaction vessel 350, as many of the gas bubbles in the first aqueous ozone solution are crushed. [0036] The reaction vessel 350 is in fluidic communication with a supply of the first aqueous ozone solution, e.g., the venturi 310. The reaction vessel 350 is also in fluidic communication with the supply of water 330 for mixing with the first aqueous ozone solution. After the mixing in the reaction vessel 350, the reaction vessel 350 outputs the second aqueous ozone solution to a contact tank 405. The reaction vessel and its conical-shaped surface 385 imparts a rotating action or a vortex to the water entering the reaction vessel 350 from the supply of water 330, and the water rotates about the conical-shaped surface 385 toward the first aqueous ozone solution entering the reaction vessel 350, which crushes ozone gas bubbles in the first aqueous ozone water solution. [0037] The preparation of the ozone gas will now be described. [0038] The ozone gas for use with the system 10 is produced from ambient air. An important feature of the system 10 is that it ensures that a consistent supply of dried air is delivered to oxygen concentrators 160, which produce essentially pure oxygen gas for ozone generation in ozone generators 240, such that the system 10 provides a sufficient quantity of ozone gas with consistent quality. The consistent supply of dried air ultimately assists in creating the consistent supply of the aqueous ozonated solution produced by the system 10. [0039] The system 10 draws in the ambient air to a compressed dry air supply skid 100 (shown in Figure 3) comprising an air compressor 120, a dryer 140, a dew point monitor 150, the oxygen concentrators 160, and an oxygen storage tank 180. The air compressor 120 is in communication with the dryer 140. The air compressor 120 compresses the ambient air and delivers the compressed air to the dryer 140. The compressed air is dried in the dryer 140. The dryer 140 is in communication with the dew point monitor 150, which measures the dew point of air exiting the dryer 140. A suitable dew point monitor 150 is commercially available from Vaisala Instruments. [0040] From the dew point monitor 150, the compressed and dried air passes to the oxygen concentrators 160, which produce essentially pure oxygen gas from the dried and compressed air that is stored in the oxygen storage tank 180. The oxygen storage tank 180 acts as a storage and supply reservoir of oxygen for ozone generation. Excess oxygen is stored in the oxygen storage tank. [0041] Maintaining a high concentration of oxygen in the oxygen gas assists in creating the consistent supply of the aqueous ozonated solution produced by the system 10. Generally, the essentially pure oxygen gas will contain over 90% pure oxygen, with a preferred range of approximately 95% to 98% pure oxygen. The oxygen concentrators 160 may use a pressure swing adsorption process using a molecular sieve. A suitable oxygen concentrator 160 is commercially available from the AirSep Corporation. The compressed dry air supply skid 100 may further include one or more filters 132 for oil and contaminant removal, one or more pressure indicators 134 for monitoring the pressures of the compressed air and the stored oxygen gas in the oxygen storage tank 180, and one or more pressure relief valves 136 for discharging pressurized gas. A flow controller 138 modulates the flow of oxygen gas from the oxygen concentrators 160 to the oxygen storage tank 180, while one of the pressure indicators 134 and one of the pressure relief valves 136 is also employed to monitor and provide pressure relief for the oxygen gas directed to the oxygen storage tank 180 from the oxygen concentrators 160. [0042] The essentially pure oxygen gas is delivered to an ozone generation skid 200 (shown in Figure 4) comprising the ozone generator 240, an ozone destruct unit 260, a distribution manifold 270, and one or more mass flow controllers 305. The ozone generation skid produces ozone and directs it via the distribution manifold 270 and the one or more mass flow controllers 305 to one or more mixing skids 300 (shown in Figure 5). [0043] The ozone generator 240 produces ozone gas from the essentially pure oxygen gas. The ozone generator 240 is in communication with the oxygen storage tank 180. The ozone generator 240 is configured with a cooling system, such as a cool-water recirculation jacket 243, to maintain the ozone generator 240 at under approximately 100° F. The ozone generator may utilize a corona discharge method of ozone generation. Maintaining a cool temperature is preferred to regulate ozone concentration, as higher concentrations of ozone gas are achieved from the ozone generator 240 when the temperature of the ozone generator 240 is maintained at these cool levels. The ozone destruct unit 260 receives excess ozone or ozone that has separated from the aqueous ozone solution in other parts of the system 10 for destruction. [0044] As shown in Figure 4, the ozone generation skid 200 comprises one or more ozone generators 240. Some of the one or more ozone generators may only be used in a backup capacity, i.e., when one of the previously operational ozone generators 240 require maintenance or breaks-down. As such, the industrial facility will not need to shut down for a conventional cleaning process when one of the ozone generators 240 is non-operational. Depending on the overall size of the system 10, up to 30 or more ozone generators 240 may be included in the ozone generation skid 200. The ozone generators 240 are in electrical communication with the control panel/central server 50 in order to monitor and control their operation. [0045] The ozone generation skid 200 includes the distribution manifold 270 and the mass flow controllers 305 for disseminating the ozone gas to the one or more mixing skids 300 for mixing with water to produce the aqueous ozone solution. The distribution manifold 270 is in communication with the ozone generators 240. An isolation valve 242, an air actuated ball valve 244, and a back flow preventer 246 are positioned between the ozone generator 240 and the distribution manifold 270 to direct the flow of ozone gas from the ozone generator 240 to the distribution manifold 270. [0046] The mass flow controllers 305 are in electrical communication with the control panel/central server 50 for modulating the flow of the ozone gas. A suitable mass flow controller 305 is commercially available from Eldrige, Products, Inc. [0047] Typically, the distribution manifold 270 will branch into separate lines each having a mass flow controller 305a-g in communication with each of the one or more mixing skids 300a-g. Additional isolation valves 242 are configured between the mass flow controllers 305a-g and the distribution manifold 270. The number of mixing skids 300a-g and mass flow controllers 305a-g will depend upon the application requirements of the system 10. For example, certain industrial facilities may only require two to four mixing skids 300a-g and mass flow controllers 305a-g, while other industrial facilities may require six to eight mixing skids 300a-g and mass flow controllers 305a-g. The distribution manifold 270 further directs ozone gas to an auxiliary use, such as a deodorizer, or to the ozone destruction unit 260. [0048] As shown in Figure 5, the one or more mixing skids 300 comprise the venturi 310, the reaction vessel 350, the contact tank 405, a degassing separator 420, a demister 440, a mixing ozone monitor 460, and a pump 480. At the mixing skids 300, water from the water supply 330 and ozone gas from the ozone generation skid 200 are directed via lines, hoses, and/or piping to the venturi 310 for forming an aqueous ozone solution. The venturi 310 acts as an injector, i.e., it injects the ozone gas into the water. A preferred injector is commercially available from the Mazzei Injector Corporation; however, any of a variety of injectors could be utilized in the one or more mixing skids 300. [0049] As previously noted, before reaching the venturi 310, the ozone gas passes through the one or more mass flow controllers 305a-g, which measures the flow of ozone to the venturi 310 and modulates the flow of ozone to the venturi 310. The mass flow controllers 305a- g are in electrical communication with the control panel/central server 50 in order regulate and control the flow of ozone gas through the mass flow controllers 305a-g. The operator of the system may adjust the flow of ozone to the venturi 310 to obtain the desired ozone concentrations level in the aqueous ozone solution. [0050] Although an aqueous ozone solution has now been formed by the venturi 310, the aqueous ozone solution is now directed to the reaction vessel 350 for further processing to reduce the bubble size of the ozone gas in the aqueous ozone solution and number of bubbles and to increase the concentration of ozone in the aqueous ozone solution as well as its oxidation reduction potential. Decreasing the bubble size of the ozone gas also assists in maintaining a uniform concentration of ozone gas in the aqueous ozone solution. A supply of water is in communication with the reaction vessel 350. The supply of water directs water to a conical- shaped surface of the reaction vessel 350, and the water mixes with the aqueous ozone solution to form the second aqueous ozone solution. [0051] The operation and structure of the reaction vessel 350 will now be described in detail with reference to Figure 2. The aqueous ozone solution from the venturi 310 is discharged into the bottom of reaction vessel 350 at an inlet port 355. The aqueous ozone solution travels up an inner vortex assembly sleeve 370 in the interior of the reaction vessel 350. [0052] Nozzles 360 discharge a stream of fresh water, at approximately 50 to 55 psi, at the top of the reaction vessel 350 into the inner vortex assembly sleeve 370. The water from the nozzles 360 dilutes the aqueous ozone solution from the venturi 310. The nozzles 360 receive the fresh water from the water supply 330 through a fresh water inlet 345 and a regulator 348. The regulator 348 is in electrical communication with the control panel/central server 50. The regulator 348 provides pressure readings to the control panel/central server 50, and the regulator 348 modulates the pressure and flow of fresh water into the inner vortex assembly sleeve 370 at the direction of the control panel/central server 50. The pressure in the inner vortex assembly sleeve 370 is varied to accommodate the desired flow rate of the aqueous ozonated water solution from the particular mixing skid 300 a-g. If the pressure in the inner vortex assembly sleeve 370 is too high, then off-gassing problems of ozone gas may occur. [0053] The inner vortex assembly sleeve 370 is shown in Figure 2. The inner vortex assembly sleeve 370 is under a pressure of approximately 50 psi to approximately 125 psi. The inner vortex assembly sleeve 370 comprises a conical-shaped surface 385. The aqueous ozone solution enters the bottom of the reaction vessel 350 at the inlet port 355, while fresh water is discharged from nozzles 360 toward the entering aqueous ozone solution. [0054] From the inlet port 355, the aqueous ozone solution enters a cavity 358, which acts as a reservoir to receive the aqueous ozone solution. An opening 365 separates the conical- shaped surface 385 from the cavity 358. The opening 365 is in fluidic communication with the cavity 358 and the inner vortex assembly sleeve 370. The inner vortex assembly sleeve 370 has a narrow diameter toward the inlet port 355 and the opening 365 and gradually increases in diameter toward an outlet 390, which creates the conical-shaped surface 385. The opening 365 is at the narrowest point of the conical-shaped surface 385. [0055] The nozzles 360 direct the fresh water at the conical-shaped surface 385. Specifically, the nozzles 360 direct the fresh water at the sloping surfaces of the conical-shaped surface 385. The conical-shaped surface has sloping surfaces or sides leading to the opening 365. The direction of the nozzles 360 and the conical-shaped surface 385 imparts a rotating action or a vortex to the fresh water, and the fresh water rotates about the conical-shaped surface 385 toward the opening 365. As such, fresh water from the nozzles 360 moves down the conical-shaped surface 385 in the rotating manner, under centrifugal force, which crushes ozone gas bubbles in the aqueous ozone water solution entering the inner vortex assembly sleeve 370 through the opening 365 from the cavity 358 and crushes ozone gas bubbles in the aqueous ozone water solution in the cavity 358. [0056] At the opening 365, some of the rotating fresh water from the nozzles 360 may enter the cavity 358. Ozone gas from the aqueous ozone solution may diffuse with the fresh water in the cavity 358 and at the opening 365. At the opening 365, the aqueous ozone solution from the cavity 358 passes into a cone void 388, which is the generally hollow central region of the inner vortex assembly sleeve 370, as defined by the conical-shaped surface 385. [0057] The inner vortex assembly sleeve 370 comprises approximately 10 to approximately 50 of the edges 380 on the conical-shaped surface 385. Each of the edges 380 may comprise a generally perpendicular angle above and below the adjacent edge 380. The edges 380 form a stair-step like surface for the conical-shaped surface 385. The edges 380 surround a perimeter of the cone void 388. The edges 380 are in contact with the hollow interior, i.e., the cone void 388. Other constructions, geometries, or surfaces on the conical-shaped surface 385 may be employed to reduce the bubble size of the ozone gas. For example, as shown in Figure 6, the conical-shaped surface 385 may include a plurality of the concentric ridges 382 about the conical-shaped surface 385. [0058] The inner vortex assembly sleeve 370 turns the aqueous ozone solution, under high pressure, around and against the series of edges 380 on the interior conical shaped surface 385 of the inner vortex assembly sleeve 370. The interaction of the fresh water, the aqueous ozone solution, and the edges 380 crush and break the ozone gas into smaller and smaller bubbles in the second aqueous ozone solution, which exits the reaction vessel 350 at the outlet 390. Off-gassing of ozone gas into the cone void 388 is re-mixed into the aqueous ozone solutions. The conical-shaped surface 385 and discharge of fresh water from the nozzles 360 causes the fresh water to circulate and form a vortex which mixes with the aqueous ozone solution passing through the inner vortex assembly sleeve 370 and eventually exiting at the outlet 390. The sleeve 370 is significant to cause the necessary break down of the microscopic bubbles of ozone gas and allows the maximum molar absorptivity of the ozone gas into the aqueous solution. The aqueous ozone solution is forced into a saturated aqueous ozone solution having an ozone concentration of up to approximately 20 ppm and an oxidation reaction potential of up to approximately 2.6. Breaking down the bubbles of ozone into smaller bubbles of ozone increases the oxidation reduction potential of the ozone in the aqueous ozone solution. The greater oxidation reduction potential of the aqueous ozone solution water allows the ozone to act not only as a sanitizer, but as a degreaser and therefore has more oxidizing power than conventionally mixed solutions. [0059] Typically, the aqueous ozone solution entering the reaction vessel 350 at the inlet port 355 and the fresh water entering the reaction vessel forms a solution that is approximately 10% to approximately 20% fresh water, i.e., approximately 1 part by volume fresh water from the water supply is mixed with approximately 4 parts to approximately 9 parts by volume aqueous ozone solution from the inlet port 355. However, due to the crushing of the ozone bubbles in the reaction vessel 350, the ORP value for the aqueous ozone solution exiting the outlet 390 is approximately the same as the ORP value for the aqueous ozone solution entering the inlet 355, despite the dilution of the aqueous ozone solution entering the inlet 355 by the fresh water from the nozzles 360. [0060] The reaction vessel 350 and the inner vortex assembly sleeve may be made from stainless steel, metal alloys, or hard plastic materials, such as chlorinated Polyvinyl Chloride (CPVC). [0061] From the outlet port 390 of the reaction vessel 350, the aqueous ozone solution is directed to the contact tank 405 and a degassing separator 420 in communication with the reaction vessel 350. The contact tank 405 should have a volume approximately twice the desired amount of volume of aqueous ozone solution. For example, if the mixing skid 300a is providing 100 gallons/per minute in flow, then the contact tank 405 should have a capacity of approximately 200 gallons. As such, in this particular example, the solution is spending approximately two minutes in the contact tank 405. [0062] Large gas bubbles are separated from the aqueous ozone solution in the degassing separator 420. The degassing separator is important to remove the excess ozone bubbles from the aqueous ozone solution to reduce the levels of free ozone gas released at an application point during the spraying of the aqueous ozone solution, which in high concentrations could breach OSHA regulations. The separated gas bubbles are directed to a demister 440, where a liquid component of the separated gas bubble is collected and drained, while an ozone gas component of the separated gas bubbles is directed from the demister 440 to the ozone destruction unit 260. [0063] The aqueous ozone solution exiting the degassing separator 420 passes through and the mixing ozone monitor 460 and on to one or more pumps 480 via piping, hosing and/or lines. Depending upon the cleaning and sanitizing application of the system 10, the aqueous ozone solution may be directed to one or more of the pumps 480 which may pump the aqueous ozone solution at different flow rates and pressures from the mixing skid 300. The aqueous ozone solution is pumped from the mixing skid 300 via distribution piping/hosing 510 in communication with the pumps 480 to one or more applicators 530 for applying the aqueous ozone solution to the hard surfaces and other items for sanitation. The applicators 530 include spray wands, nozzles, brushes, nebulizers, spray guns and the like, and various combinations thereof. Each applicator 530 includes an applicator ozone monitor 550. [0064] The concentration of the aqueous ozone solution is monitored by the applicator ozone monitor 550, which measures the exact concentration of ozone in the aqueous ozone solution exiting from the applicator 530. The plant operator may monitor and adjust the concentration of ozone in the aqueous ozone solution based on readings from the applicator ozone monitor 550. [0065] The applicator ozone monitor 550 is in electrical communication with the control panel/central server 50. If the applicator ozone monitor 550 indicates that the levels of ozone in the aqueous ozone solution are too low, then the operator or automated systems in the control panel/central server 50 may adjust the mass flow controller 305 to increase the amount of ozone gas directed to the venturi 310, such that concentration levels of ozone in the aqueous ozone solution at the applicator ozone monitor 550 are increased. [0066] The system 10 may comprise one or mixing skids 300 with one or more pumps 480 supplying one or more applicators 530. The one or more pumps 480 may pump the aqueous ozone solution at different rates and at different concentrations to the different applicators 530. The system 10 may be customized, depending upon a specific industrial facility and its specific cleaning needs. For example, the system 10 may comprise a variety of high pressure and low pressure applicators 530 and with certain applicators applying different concentrations of aqueous ozone solution. The system 10 provides an applied dosage of an aqueous ozone solution that is consistent over time in terms of the desired concentration and flow rate to the one or more applicators 530. The control panel/central server 50, in conjunction with the applicator ozone monitor 550 and mass flow controllers 305, monitor and regulate the concentration and flow of the aqueous ozone solution. [0067] The reaction vessel 350 is important to the mass transfer of ozone gas in the water, i.e., how the ozone gas is dissolved into the water to form the aqueous ozone solution. The system 10 produces a saturated aqueous ozone solution having an ozone concentration of up to approximately 20 ppm. [0068] The system 10, and specifically the reaction vessel 350, help reduce the number of bubbles and create the smallest possible bubbles of ozone in the aqueous ozone solution in order to produce the saturated aqueous ozone solution with an ozone concentration of up to approximately 20 ppm and an oxidation reduction potential of 2.6. The amount of ozone dissolved into the water depends, in part, on the surface area of the gas/water interaction. The smaller the bubble, the better the mass transfer because one cubic inch of tiny bubbles has much more surface area than a single, one cubic inch bubble. [0069] The edges 380 on the inner vortex assembly sleeve 370 assist in physically reducing the bubble size of the ozone gas. As the aqueous ozone solution is forced through the inner vortex assembly sleeve 370, the bubbles of ozone contact the edges 380 and break into smaller and smaller bubbles. The smaller bubbles dissolving in the water help to saturate the aqueous ozone solution with ozone. [0070] The pressure applied in the reaction vessel 350, of approximately 50 psi to approximately 125 psi, also improves the mass transfer between the bubbles of ozone gas and the water. The higher the pressure, the more a "squeeze" is put on the transfer of gas bubbles into the water enhancing the process of dissolving the gas bubbles into the aqueous ozone solution and creating the saturated aqueous ozone solution. The higher pressure also forces the gas bubbles against the edges 380 further breaking them down into smaller bubbles. [0071] The temperature of the water is also an important consideration in the mass transfer process. At cooler temperatures, the ozone diffuses better in the water. At cooler water temperatures, the contact time between the ozone gas bubbles and the water in forming the aqueous ozone solution is reduced. In general, it is difficult for water to absorb a gas when the water is trying to become a gas. The water from the water supply 330 should be at a temperature of approximately 33° F. to approximately 50° F. [0072] The concentration of the ozone gas in the carrier gas also affects the mass transfer of the ozone gas in to the water. Higher concentrations of ozone in the carrier gas will result in higher concentrations of ozone being absorbed into the aqueous ozone solution. Corona discharge ozone generation equipment generally creates higher concentrations of ozone gas in the carrier gas than ultraviolet types of ozone generation. [0073] The system 10 produces an aqueous ozone solution to attack and destroy pathogens and act as a no-rinse sanitizer for hard surfaces in a variety of applications, especially industrial processing facilities related to food processing. The solution of aqueous ozone is applied at high pressure to the hard surfaces, and is effective for the removal of soils and bulk materials from the hard surfaces. When applied at high pressure, the solution penetrates the soils and oxides of the biofilm that acts as the bond or glue that allows the soils and oxides to attach themselves to the hard surfaces. The system 10 is designed to be the first totally chemical free system to destroy the biofilm on conveyors systems and hard surfaces during food processing production allowing for continuous or extended production. [0074] There are many applications for both high and low pressure. When the solution discharges from the assembly, the solution could be channeled into both a high pressure stream as well as a low pressure stream. The high-pressure stream of aqueous ozone solution may be better suited for cleaning and sterilizing highly soiled hard surfaces due to the extra force supplied by the high pressure aqueous ozone solution which will help destroy the biofilm adhering the soils to the hard surfaces. The low pressure aqueous ozone solution may be suited for the continuous sanitization of hard surface or application to a food item. [0075] In the embodiment shown, the ozone produced by the ozone generator 240 uses a high electrical discharge called "corona discharge" or "CD". This method is most commonly used to generate usable amounts of ozone for most water treatment applications. Corona discharge creates a small, controlled lightning storm, which involves producing a constant, controlled spark (corona) across an air gap through which a prepared feed gas is passed. This feed gas may be air that has simply had most of its moisture removed or air with enhanced oxygen levels. An important aspect of using the corona discharge methods of ozone production is ensuring that feed gas is dried at the dryer 140 to a dew point of at least approximately -60F. This is important because as the electrical discharge splits the oxygen molecules, nitrogen molecules are also being split, forming several species of nitrogen oxides, which are normally benign. If feed gas is not sufficiently dried, then the nitrogen oxides combine with moisture from ordinary humidity and form nitric acid, which may be corrosive to the system 10, the hard surfaces, and the industrial facility. Consequently, proper air preparation is important for the operation of the system 10. The relative strength of corona discharge ozone expressed as a percentage of concentration by weight is commonly 0.5 — 1.7% for systems using dried air, and 1.0 — 6.0% when an oxygen enhanced feed gas is used. [0076] A properly installed and operated system 10 poses no health hazards. While ozone is a toxic gas and the established concentration limits must be adhered to, the odor threshold of 0.01 ppm is far below the safety limit of 0.1 ppm exposure over an eight hour period. The first symptoms of excessive ozone exposure are headaches, eye, nose or throat irritation or a shortness of breath. These symptoms can be relieved by the simple application of fresh air. While no deaths have been reported from ozone, sound safety practices deserve attention. Ozone off-gas containment and destruction equipment for most water treatment applications is readily available and is usually a simple device containing either activated carbon or manganese dioxide. [0077] Ozone is a much more powerful oxidizer than chlorine. Based on EPA charts of surface water CT values (disinfectant residual and time constant), chlorine CT values are nearly 100 times greater than ozone, meaning that ozone acts much more quickly than chlorine. Ozone creates none of the trihalomethanes commonly associated with chlorine compounds and properly matched to the application; ozone will reduce most organic compounds to carbon dioxide, water and a little heat. Finally, as ozone sheds the atom of the oxygen causing its molecular instability during the oxidation process, it becomes oxygen again. [0078] Facilities processing bottled water, perishable goods (meat, seafood, fruit, vegetables, etc.) are examples of ideal applications for the system 10. The fact that ozone efficiently oxidizes the organics that cause taste, odor, and color problems without leaving a high residual helps to simplify many water treatment. The lack of residual from ozone cleaning and santiation also makes ozone perfect for pre- and post-treatment processes in wash pad recycle systems, where the use of a chlorine compound would contribute to pH control or off gas problems. Additionally, ozone oxidizes and precipitates many metals and destroys some pesticides without leaving a trace. Finally, ozone functions as a preoxidizer of iron, manganese and sulfide compounds, allowing for their removal by simple direct filtration. Ozone acts quickly and easily, and the water quality resulting from its use is unmatched. [0079] It should be understood from the foregoing that, while particular embodiments of the invention have been illustrated and described, various modifications can be made thereto without departing from the spirit and scope of the present invention. Therefore, it is not intended that the invention be limited by the specification; instead, the scope of the present invention is intended to be limited only by the appended claims. We claim: 1. An industrial cleaning system that produces and distributes an aqueous ozone solution, comprising: an ozone generator for generating ozone gas; an injector in communication with the ozone generator and in communication with a supply of water, wherein the injector injects ozone gas from the ozone generator into the water from the supply of water to form an aqueous ozone solution; a reaction vessel in fluidic communication with the injector for receiving the aqueous ozone solution from the injector, wherein the reaction vessel comprises a conical- shaped surface having a plurality of edges or ridges; and a pump in communication with the reaction vessel for distributing the aqueous ozone solution. 2. The industrial cleaning system according to claim 1, wherein the aqueous ozone solution from the injector is discharged into the bottom of the reaction vessel at an inlet port, and the aqueous ozone solution travels up an inner vortex assembly sleeve in the interior of the reaction vessel, and nozzles discharge a stream of fresh water at the top of the reaction vessel into the inner vortex assembly sleeve. 3. The industrial cleaning system according to claim 2, wherein the inner vortex assembly sleeve has a narrow diameter near the inlet port and gradually increases in diameter toward an outlet which creates the conical-shaped surface on the inner vortex assembly sleeve. 4. The industrial cleaning system according to claim 1, further comprising a degassing separator in communication with the reaction vessel to remove Ozone bubbles from the aqueous ozone solution. 5. The industrial cleaning system according to claim 1, further comprising an air compressor in communication with a dryer to provide compressed air to the dryer; a dew point monitor that measures the dew point of the compressed and dried air from the dryer; an oxygen concentrator in communication with the dryer that receive the compressed and dried air from the dryer to produce oxygen gas; an oxygen storage tank in communication with the oxygen concentrator that receives the oxygen gas from the oxygen concentrator; the oxygen storage tank in supply communication with the ozone generators to supply the ozone generators with the oxygen gas. 6. The industrial cleaning system according to claim 1, wherein the oxygen gas is approximately 95% to approximately 98% oxygen. 7. The industrial cleaning system according to claim 1, wherein the ozone generator comprises a cooling system to maintain the ozone generator at under approximately 100° F. 8. The industrial cleaning system according to claim 7, wherein the cooling system is a water-cooled jacket in contact with the ozone generator. 9. The industrial cleaning system according to claim 1, wherein the reaction vessel is in fluidic communication with the injector for receiving the aqueous ozone solution from the injector and in fluid communication with the fresh water supply for supplying fresh water to the reaction vessel. 10. The industrial cleaning system according to claim 1, further comprising a distribution manifold in communication with the ozone generator to distribute the ozone gas, and one or more mass flow controllers to modulate the flow of ozone gas from the distribution manifold. 11. The industrial cleaning system according to claim 1, further comprising an applicator in fluidic communication with the pump, wherein the applicator dispenses the aqueous ozone solution, and the applicator comprises an ozone monitor to measure the concentration of ozone in the aqueous ozone solution dispensed from the applicator, wherein the ozone monitor is in electrical communication with a control panel that operates the system 12. The industrial cleaning system according to claim 11, wherein the control panel modulates the flow of ozone gas to the venturi based on the concentration of ozone in the aqueous ozone solution dispensed from the applicator as measured by the ozone monitor. 13. The industrial cleaning system according to claim 1, wherein the system produces and distributes aqueous ozone solution with an oxidation reaction potential of up to approximately 2.6. 14. The industrial cleaning system according to claim 1, wherein the system produces and distributes an aqueous ozone solution with an ozone concentration of up to approximately 20 ppm. 15. The industrial cleaning system according to claim 1, wherein the reaction vessel comprises approximately 10 to approximately 50 edges or ridges. 16. The industrial cleaning system according to claim 1, wherein the edges comprise a perpendicular angle. 17. The industrial cleaning system according to claim 1, wherein the reaction vessel is in fluidic communication with a supply of water, and water mixes with the aqueous ozone solution in the reaction vessel to form a solution that is approximately 10% to approximately 20% water. 18. The industrial cleaning system according to claim 1, wherein the reaction vessel is in fluidic communication with a contact tank. 19. The industrial cleaning system according to claim 1, wherein the system provides an applied dosage of an aqueous ozone solution that is consistent over time in terms of concentration and flow rate. 20. The industrial cleaning system according to claim 1, wherein the system is centrally located in an industrial facility, and the system comprises one or pumps that are in fluidic communication with one or more applicators for spraying the aqueous ozone solution in or about the industrial facility. 21. An industrial cleaning system that produces and distributes an aqueous ozone solution, comprising: an air supply skid comprising an air dryer in communication with an oxygen concentrator to produce oxygen gas; an ozone generation skid comprising an ozone generator in communication with the air supply skid to receive oxygen gas in order to generate ozone, the ozone generator in communication with a distribution manifold for distributing the ozone gas to one or more mixing skids; and one or more mixing skids each comprising an injector in communication with the ozone generation skid and a supply of water, wherein the injector injects ozone gas from the ozone generation skid into the water from the supply of water to form an aqueous ozone solution; a reaction vessel in fluidic communication with the injector for receiving the aqueous ozone solution from the injector, the reaction vessel in fluidic communication with the supply of water for mixing water with the aqueous ozone solution from the injector, and one or more pumps in communication with the reaction vessel for distributing the aqueous ozone solution to one or more applicators. 22. An industrial cleaning system that produces and distributes an aqueous ozone solution, comprising: an ozone generator for generating ozone gas; an injector in communication with the ozone generator and in connection with a supply of water, wherein the injector injects ozone gas from the ozone generator into the water from the supply of water to form an aqueous ozone solution; a reaction vessel in fluidic communication with the injector for receiving the aqueous ozone solution from the injector; the reaction vessel in fluidic communication with the supply of water for mixing the aqueous ozone solution with the water, a pump in communication with the reaction vessel for distributing the aqueous ozone solution; a control panel that operates the system; and an applicator in fluidic communication with the pump, wherein the applicator dispenses the aqueous ozone solution, and the applicator comprises an ozone monitor to measure the concentration of ozone in the aqueous ozone solution dispensed from the applicator, wherein the ozone monitor is in electrical communication with the control panel. 23. An industrial cleaning system that produces and distributes an aqueous ozone solution, comprising: an ozone generation system, comprising: an air compressor in communication with a dryer to provide compressed air to the dryer; an oxygen concentrator in communication with the dryer that receive the compressed and dried air from the dryer to produce oxygen gas; an oxygen storage tank in communication with the oxygen concentrator that receives the oxygen gas from the oxygen concentrator; the oxygen storage tank in supply communication with one or more ozone generators to supply the ozone generators with the oxygen gas to generate ozone; an injector in communication with the one or more ozone generators and in communication with a supply of water, wherein the injector injects ozone gas from the ozone generator into the water from the supply of water to form an aqueous ozone solution; a reaction vessel in fluidic communication with the injector for receiving the aqueous ozone solution from the injector and reducing a bubble size of ozone gas in the aqueous ozone solution; a pump in communication with the reaction vessel for distributing the aqueous ozone solution; and a control panel that operates the system. 24. A reaction vessel for entraining ozone gas in an aqueous solution in an industrial cleaning system, comprising: a conical-shaped surface having a plurality of edges, the conical-shaped surface defining a generally hollow interior, and the plurality of edges in contact with the generally hollow interior; an inlet port in fluidic communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution to the conical-shaped surface; nozzles in fluidic communication with a supply of water, wherein the nozzles direct the water under pressure at the conical-shaped surface, and the water mixes with the aqueous ozone solution from the inlet port; and an outlet in fluidic communication with the industrial cleaning system. 25. The reaction vessel for an industrial cleaning system according to claim 24, wherein the inlet port discharges the aqueous ozone solution in a bottom of the reaction vessel, and the aqueous ozone solution travels up an inner vortex assembly sleeve in the interior of the reaction vessel, and the nozzles discharge the fresh water at a top of the reaction vessel into the inner vortex assembly sleeve, and the inner vortex assembly sleeve comprises the conical-shaped surface. 26. The reaction vessel for an industrial cleaning system according to claim 25, wherein the inner vortex assembly sleeve has a narrower diameter near the inlet port and increases in diameter toward the outlet. 27. The reaction vessel for an industrial cleaning system according to claim 24, wherein the reaction vessel is in fluidic communication with an injector for receiving the aqueous ozone solution from the injector. 28. The reaction vessel for an industrial cleaning system according to claim 24, wherein the conical-shaped surface has sloping sides. 29. The reaction vessel for an industrial cleaning system according to claim 24, wherein the conical-shaped surface has sloping sides leading to an opening. 30. The reaction vessel for an industrial cleaning system according to claim 29, wherein the opening is in fluidic communication with a cavity, wherein the cavity is in fluidic communication with the inlet port supplying the aqueous ozone solution. 31. The reaction vessel for an industrial cleaning system according to claim 24, wherein an opening separates the conical-shaped surface from a cavity, and the opening is in fluidic communication with the cavity and an inner vortex assembly sleeve. 32. The reaction vessel for an industrial cleaning system according to claim 24, wherein the reaction vessel produces an aqueous ozone solution with an oxidation reaction potential of up to approximately 2.6. 33. The reaction vessel for an industrial cleaning system according to claim 24, wherein the reaction vessel produces an aqueous ozone solution with an ozone concentration of up to approximately 20 ppm. 34. The reaction vessel for an industrial cleaning system according to claim 24, wherein the reaction vessel comprises approximately 10 to approximately 50 edges. 35. The reaction vessel for an industrial cleaning system according to claim 24, wherein the edges comprise a perpendicular angle. 36. The reaction vessel for an industrial cleaning system according to claim 24, wherein the nozzles are in operational communication with a regulator, and the regulator provides a pressure of approximately 50 psi to approximately 125 psi in the reaction vessel. 37. The reaction vessel for an industrial cleaning system according to claim 24, wherein the water from the nozzles mixes with the aqueous ozone solution to form a solution that is approximately 10% to approximately 20% water, 38. The reaction vessel for an industrial cleaning system according to claim 24, wherein the reaction vessel is in fluidic communication with a contact tank. 39. The reaction vessel for an industrial cleaning system according to claim 24, comprising a plurality of ridges on the conical-shaped surface instead of the plurality of edges. 40. A reaction vessel for entraining ozone gas in an aqueous solution in an industrial cleaning system, comprising: a conical-shaped surface having a plurality of edges or ridges, the conical-shaped surface defining a generally hollow interior, and the plurality of edges or ridges are in contact with the generally hollow interior; an inlet port in a bottom of the reaction vessel in fluidic communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution to the conical- shaped surface; a supply of water in communication with the reaction vessel, wherein the supply of water directs water to the conical-shaped surface, and the water mixes with the aqueous ozone solution from the inlet port; and an outlet in fluidic communication with the industrial cleaning system. 41. A reaction vessel for entraining ozone gas in an aqueous solution in an industrial cleaning system, comprising: a conical-shaped surface having a plurality of edges or ridges; an opening at the narrowest portion of the conical-shaped surface; a supply of an aqueous ozone solution in communication with the reaction vessel to supply the aqueous ozone solution to the conical-shaped surface via the opening; and a supply of water in communication the reaction vessel, wherein the supply of water directs water to the conical-shaped surface, and the water mixes with the aqueous ozone solution. 42. A method of producing an aqueous ozone solution in an industrial cleaning system, comprising: providing a reaction vessel for entraining ozone gas in an aqueous solution in an industrial cleaning system, comprising: a conical-shaped surface having a plurality of edges, the conical-shaped surface defining a generally hollow interior, and the plurality of edges in contact with the generally hollow interior; an inlet port in fluidic communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution to the conical-shaped surface; a supply of water that directs the water, under pressure, at the conical-shaped surface; an outlet in fluidic communication with the industrial cleaning system; and directing the aqueous ozone solution through the inlet port to the conical-shaped surface; directing the water to the conical-shaped surface; and mixing the water and the aqueous ozone solution. 43. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 42, further comprising reducing a bubble size of ozone gas in the aqueous ozone solution in the reaction vessel. 44. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 42, further comprising directing the water at the conical-shaped surface and imparting a rotating action or vortex to the water as it mixes with the aqueous ozone solution. 45. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 42, further comprising directing the water at the conical-shaped surface and imparting a rotating action or vortex to the water and crushing ozone bubbles in the aqueous ozone solution. 46. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 42, further comprising diluting the aqueous ozone solution from the inlet port with the water from the supply of water. 47. A method of producing an aqueous ozone solution for an industrial cleaning system, comprising: providing a reaction vessel for entraining ozone gas in an aqueous solution in an industrial cleaning system, comprising: a conical-shaped surface having a plurality of edges or ridges, the conical-shaped surface defining an interior, and the plurality of edges or ridges in contact with the interior; the reaction vessel in fluidic communication with a supply of water; the reaction vessel in fluidic communication with a supply of a first aqueous ozone solution; directing the first aqueous ozone solution to the conical-shaped surface; directing the water to the conical-shaped surface; and mixing the water and the first aqueous ozone solution to form a second aqueous ozone solution. 48. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 47, further comprising reducing a bubble size of ozone gas in the first aqueous ozone solution in the reaction vessel. 49. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 47, wherein the concentration of ozone in the second aqueous ozone solution is consistent over time. 50. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 47, further comprising directing the water at the conical-shaped surface and imparting a rotating action or vortex to the water as it mixes with the first aqueous ozone solution. 51. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 47, further comprising directing the water at the conical-shaped surface and imparting a rotating action or vortex to the water and crushing ozone bubbles in the first aqueous ozone solution. 52. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 47, further comprising diluting the first aqueous ozone solution with the water from the supply of water. 53. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 47, wherein the second aqueous ozone solution has an oxidation reduction potential of up to approximately 2.6. 54. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 47, wherein the second aqueous ozone solution has an ozone concentration of up to approximately 20 ppm. 55. The method of producing an aqueous ozone solution in an industrial cleaning system according to claim 47, wherein the second aqueous ozone solution is formed in a ratio of approximately 1 part by volume water from the water supply with approximately 4 parts by volume to approximately 9 parts by volume of the first aqueous ozone solution. 56. The aqueous ozone solution according to claim 47, wherein the water mixes with the first aqueous ozone solution to form the second aqueous ozone solution that is approximately 10% to approximately 20% water. 57. A method of producing an aqueous ozone solution for an industrial cleaning system, comprising: compressing and drying ambient air; concentrating oxygen gas from the ambient air into a supply of oxygen gas that contains over 90% pure oxygen; directing the oxygen gas to an ozone generator; cooling the ozone generator; producing ozone gas in the ozone generator; directing the ozone gas and water from a water supply to an injector; injecting the ozone gas into the water with the injector to form a first aqueous ozone solution; mixing the first aqueous ozone solution with water; and forming a second aqueous ozone solution. 58. The method of producing an aqueous ozone solution according to claim 57, further comprising mixing the water with the first aqueous ozone solution in a reaction vessel. 59. The method of producing an aqueous ozone solution according to claim 57, further comprising reducing the number and size of ozone gas bubbles in the first aqueous ozone solution. 60. A method of producing an aqueous ozone solution for an industrial cleaning system, comprising: providing a reaction vessel for entraining ozone gas in an aqueous solution in an industrial cleaning system, wherein the reaction vessel is in fluidic communication with a supply of water; wherein the reaction vessel is in fluidic communication with a supply of a first aqueous ozone solution; directing the first aqueous ozone solution to the reaction vessel; directing water to the reaction vessel; crushing bubbles of ozone gas in the first aqueous ozone solution with the water in the reaction vessel; and mixing the water and the first aqueous ozone solution to form a second aqueous ozone solution, wherein an oxidation reduction potential value for the first aqueous ozone solution is approximately the same as an oxidation reduction potential value for the second aqueous ozone solution. 61 An aqueous ozone solution, prepared by the process comprising: providing a reaction vessel for entraining ozone gas in an aqueous solution in an industrial cleaning system, comprising: a conical-shaped surface having a plurality of edges or ridges, the conical-shaped surface defining an interior, and the plurality of edges or ridges in contact with the interior; the reaction vessel in fluidic communication with a supply of water; the reaction vessel in fluidic communication with a supply of a first aqueous ozone solution; directing the first aqueous ozone solution to the conical-shaped surface; directing water to the conical-shaped surface; and mixing the water and the first aqueous ozone solution to form a second aqueous ozone solution. 62. The aqueous ozone solution according to claim 61, further comprising reducing a bubble size of ozone gas in the first aqueous ozone solution as it mixes with the water. 63. The aqueous ozone solution according to claim 61, further comprising directing the water at the conical-shaped surface and imparting a rotating action or vortex to the water as it mixes with the first aqueous ozone solution. 64. The aqueous ozone solution according to claim 61, further comprising diluting the first aqueous ozone solution during the mixing with the water to form the second aqueous ozone solution. 65. The aqueous ozone solution according to claim 61, further comprising directing the water at the conical-shaped surface and imparting a rotating action or vortex to the water and crushing ozone bubbles in the first aqueous ozone solution. 66. The aqueous ozone solution according to claim 61, wherein the second aqueous ozone solution has an oxidation reduction potential of up to approximately 2.6 and an ozone concentration of up to approximately 20 ppm. 67. An aqueous ozone solution comprising approximately 1 part by volume water mixed with approximately 4 parts by volume to approximately 9 parts by volume of a first aqueous ozone solution to form a second aqueous ozone solution that has an oxidation reduction potential of up to approximately 2.6, wherein the second aqueous ozone solution has an ozone concentration of up to approximately 20 ppm, wherein the second ozone solution has less ozone gas bubbles than the first aqueous ozone solution. 68. The aqueous ozone solution ozone solution according to claim 67, wherein the second ozone solution has smaller ozone gas bubbles than the first aqueous ozone solution. 69. An aqueous ozone solution comprising approximately 1 part by volume water mixed with approximately 4 parts by volume to approximately 9 parts by volume of a first aqueous ozone solution to form a second aqueous ozone solution, wherein the second aqueous ozone solution has an ozone concentration of up to approximately 20 ppm, wherein an oxidation reduction potential value for the first aqueous ozone solution is approximately the same as an oxidation reduction potential value for the second aqueous ozone solution. An industrial cleaning system 10 that produces and distributes an aqueous ozone solution is described. The system 10 includes an ozone generator 240 for generating ozone gas, which is injected by an injector 310 into a supply of water to form the aqueous ozone solution. A reaction vessel 350 receives the aqueous ozone solution from the injector 310 as the reaction vessel 350 reduces the bubbles of ozone gas in the aqueous ozone solution to increase the oxidation reduction potential of the aqueous ozone solution. The reaction vessel 350 includes a conical-shaped surface 385 having two or more edges 380 or ridges 382. The conical-shaped surface 385 defines a generally hollow interior 388. An inlet port 355 is in fluidic communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution to the conical-shaped surface 380. Nozzles 360 direct water under pressure at the conical-shaped surface 380, and the water mixes with the aqueous ozone solution from the inlet port 355. An outlet 390 is in fluidic communication with the industrial cleaning system 10. A method of making an aqueous ozone solution is described. The reaction vessel 350 is in fluidic communication with a supply of a first aqueous ozone solution. The first aqueous ozone solution is directed to the reaction vessel 350. Water is directed to the reaction vessel 350, and the water and the first aqueous ozone solution are mixed to form a second aqueous ozone solution. Compositions for aqueous ozone solutions are also described. The aqueous ozone solution contains approximately 1 part by volume water mixed with approximately 4 parts by volume to approximately 9 parts by volume of the first aqueous ozone solution to form the second aqueous ozone solution that has an oxidation reaction potential of up to approximately 2.6 and having an ozone concentration of up to approximately 20 ppm.

Full Text

OZONE CLEANING SYSTEM
Field of Invention
[0001] The present invention relates to a system of providing an aqueous solution of
ozone for industrial cleaning applications. The present invention relates to a reaction vessel for
entraining ozone gas in an aqueous solution of ozone for industrial cleaning applications. The
present invention relates to a method of producing an ozone solution and a composition of an
ozone solution.
Background of Invention
[0002] Ozone in a solution has been previously used for cleaning and sanitizing.
Maintaining a solution with a consistent ozone concentration has proven difficult. Ozone is
unstable, which provides for it cleaning and sanitizing capabilities, but also makes consistent
ozone levels difficult to maintain in a solution. If the ozone solution has too much ozone or
large bubbles of ozone, then off-gassing problems may occur, as the excess ozone is released
into the work facility creating environmental problems and possible violating workplace safety
regulations. If the solution has too little ozone, then the cleaning and sterilizing may not be as
effective as desired.
[0003] Other systems utilize a spraying device that simultaneously sprays two
separate streams of water and an ozone solution. The stream of water is applied at high pressure
for removing particles and the ozone solution is applied for sanitizing.
[0004] Ozone solutions have proven difficult to consistently and uniformly prepare
in sufficient quantities required for industrial cleaning applications.
Summary of Invention
[0005] The system produces an aqueous ozone solution to attack and destroy
pathogens and to act as a no-rinse sanitizer for hard surfaces in a variety of applications,
especially for industrial cleaning applications in facilities related to food processing. The system
includes a reaction vessel that entrains ozone gas in an aqueous ozone solution. Methods of
making aqueous ozone solutions for industrial cleaning systems are described. Compositions for
aqueous ozone solutions for use with industrial cleaning systems are also described.
[0006] The system, the reaction vessel, the aqueous ozone solution may be used for
many different sanitation applications in many different industries and facilities. For example,
the system, reaction vessel, and aqueous ozone solution may be used in cosmetic manufacturing
facilities, hospitals, fast food outlets, individual homes, etc. The system, reaction vessel, and the
aqueous ozone solution may be used with a variety of different "clean in place" systems, such as,
for example, water-bottling facilities and equipment, breweries and brewing equipment, ethanol
processing facilities, water-bottling facilities and equipment, snack food processing facilities,
cooling towers etc. The use of the system, the reaction vessel, and the aqueous ozone solution is
not limited to any particular type of industry or application type.
[0007] The reaction vessel includes a conical-shaped surface having a plurality of
edges or ridges. The conical-shaped surface defines a generally hollow interior, and the plurality
of edges or ridges are in contact with the generally hollow interior. An inlet port is in fluidic
communication with a supply of an aqueous ozone solution to supply the aqueous ozone solution
to the conical-shaped surface. Nozzles are in fluidic communication with a supply of water, and
the nozzles direct the water under pressure at the conical-shaped surface, and the water mixes
with the aqueous ozone solution from the inlet port. An outlet is in fluidic communication with
the industrial cleaning system. The reaction vessel may receive the aqueous ozone solution from
an injector. The reaction vessel reduces the number and size of bubbles of ozone gas in the
aqueous ozone solution and entrains the bubbles of ozone gas in the aqueous ozone solution to
increase the oxidation reduction potential of the aqueous ozone solution.
[0008] The system comprises an ozone generator for producing ozone gas. The
ozone generator directs the ozone gas to the injector, which is also in communication with the
supply of water. The injector injects ozone gas from the ozone generator into the water from the
supply of water to form the aqueous ozone solution. The reaction vessel receives the aqueous
ozone solution from the injector and additional water from the water supply. A pump in
communication with the reaction vessel distributes the aqueous ozone solution to the hard
surfaces for cleaning the hard surfaces.
[0009] The system and the reaction vessel reduces the amount of bubbles and the
bubble size of the ozone gas in the aqueous ozone solution, which allows for the system and
reaction vessel to produce an aqueous ozone solution with a greater concentration of ozone gas
and a higher oxidation reduction potential. Since the bubbles of ozone are smaller and fewer
than the bubbles of ozone in a typical ozone solution, the system and reaction vessel allows the
aqueous ozone solution to contain a greater amount of ozone and have the higher oxidation
reduction potential. This provides for a more effective cleaning and sanitizing system.
[0010] The reaction vessel may be used with a variety of industrial cleaning systems.
In the system described herein, the system entrains ozone gas into water, forming the aqueous
ozone solution and delivers the aqueous ozone solution to the reaction vessel for further
entraining and concentrating of the ozone gas into the aqueous ozone solution. The system
provides an applied dosage of an aqueous ozone solution that is consistent over time in terms of
concentration and flow rate.
[0011] The aqueous ozone solutions serve as a cleaning and sterilizing agent.
Systems for making and applying the aqueous ozone solutions are also described. In one
embodiment, the method of making the aqueous ozone solution for the industrial cleaning system
includes providing the reaction vessel for entraining the ozone gas in the aqueous solution. The
reaction vessel includes the conical-shaped surface having the plurality of edges or ridges. The
conical-shaped surface defines the generally hollow interior, and the plurality of edges or ridges
are in contact with the interior. The reaction vessel is in fluidic communication with the supply
of water. The reaction vessel is also in fluidic communication with a supply of a first aqueous
ozone solution. The first aqueous ozone solution is directed to the conical-shaped surface.
Water is directed to the conical-shaped surface, and the water and the first aqueous ozone
solution are mixed to form a second aqueous ozone solution.
[0012] In one embodiment of the composition, the aqueous ozone solution comprises
approximately 1 part by volume water mixed with approximately 4 parts by volume to
approximately 9 parts by volume of the first aqueous ozone solution to form the second aqueous
ozone solution that has an oxidation reaction potential of up to approximately 2.6, wherein the
second aqueous ozone solution has an ozone concentration of up to approximately 20 ppm,
wherein the second ozone solution has less ozone gas bubbles than the first aqueous ozone
solution.
[0013] The first aqueous ozone solution is mixed with water in the reaction vessel to
form the second aqueous ozone solution. The reaction vessel reduces the bubbles of ozone gas
in the first aqueous ozone solution and entrains the remaining bubbles of ozone gas in the second
aqueous ozone solution to increase the oxidation reduction potential of the second aqueous ozone
solution. The reaction vessel reduces the amount of bubbles and the bubble size of the ozone gas
in the first and second aqueous ozone solutions, which allows for the system to produce the
second aqueous ozone solution with a greater concentration of ozone gas and a higher oxidation
reduction potential.
[0014] In the methods described herein for forming the aqueous ozone solution,
ozone gas is entrained into water, forming the first aqueous ozone solution, which is delivered to
the to the reaction vessel for further entraining and concentrating of the ozone gas into the
aqueous ozone solution. The water is mixed with the first aqueous ozone solution to form the
second aqueous ozone solution.
[0015] In the methods described herein for forming the aqueous ozone solution, the
ozone generator produces the ozone gas. The ozone generator directs the ozone gas to the
injector, which is also in communication with the supply of water. The injector injects ozone gas
from the ozone generator into the water from the supply of water to form the first aqueous ozone
solution. The reaction vessel receives the first aqueous ozone solution from the injector and
additional water from the water supply. The reaction vessel comprises the conical-shaped vessel
having the plurality of edges or ridges for reducing a bubble size of the ozone gas in the first
aqueous ozone solution and for mixing the water with the first aqueous ozone solution to form
the second aqueous ozone solution. The pump in communication with the reaction vessel
distributes the second aqueous ozone solution to the hard surfaces for cleaning the hard surfaces.
[0016] The hard surfaces may include, for example, conveyor systems, processing
equipment, floors, tables, etc. The solution of aqueous ozone may be applied at a high pressure
to the hard surfaces, and is effective for sanitizing the hard surfaces and removing soils and bulk
materials from the hard surfaces. When applied at high pressure, the solution penetrates and
destroys the soils and oxides of a biofilm that acts as the bond or glue that allows the soils and
oxides to attach themselves to the hard surfaces.
[0017] The methods and solution may be used in the system described herein. The
system is a chemical-free system that destroys the biofilm on hard surfaces during food
processing production in food processing facilities. The system allows for continuous or
extended production in the facility. When installed in processing facilities, the hard surfaces can
be maintained 24 hours a day, 7 days a week accomplishing both a microbial reduction as well as
improving aesthetics. The system allows the plant to do mid-shift sanitation or a cleaning
application that the plant could not do with present conventional systems (because ozone is
approved by the Food and Drug Administration for direct food contact and chemicals are not).
[0018] The system provides a chemical-free, high pressure cleaning system that
replaces present conventional cleaning systems. The system reduces the need for chemicals, hot
water, and labor. As such, the processors operating costs may be reduced by 50%. Conventional
cleaning systems often require the use of warm or hot water, which may form condensation on
the hard surfaces. The condensation may provide for or encourage the growth of microbes.
Because the system only uses cold water, condensation is not likely to form on the hard surfaces.
The system also reduces the hydraulic load on the waste-water treatment system and eliminates
the need to treat the chemicals that would be present in conventional wastewater discharge
streams.
[0019] Ozone gas is generally unstable (a property that gives ozone its extraordinary
oxidizing capabilities). Ozone gas cannot be packaged or stored and must be generated on site.
The system includes an on-site ozone generator combined with an air preparation unit and an
injector to safely get the ozone into the water. As such, the system requires no drums to store
ozone, records and reports relating to the drums, or disposal concerns relating to the drums.
[0020] The use of ozone as cleaning and sterilizing agent is a chemical treatment like
other oxidizers, including chlorine, potassium permanganate, hydrogen peroxide, etc. Ozone's
extraordinary speed and power sets ozone apart from the other oxidizers, but there are rules to be
followed in its application. Stoichiometric (chemical value) calculation charts and formulas are
readily available for all common inorganic contaminants, including but not limited to, iron,
manganese, sulfide compounds. Simple formulas for flow and contaminant loading make ozone
generator sizing easy. With contact times in the 2-6 minute range for common contaminants,
instead of the 20-30 minute times associated with chlorination, the system described herein is
simpler, more compact and efficient than traditional cleaning treatments.
Description of Figures
[0021] Figure 1 shows a process flow diagram of the ozone cleaning system.
[0022] Figure 2 shows a sectional view of the reaction vessel.
[0023] Figure 3 shows a view of the compressed dry air supply skid.
[0024] Figure 4 shows a view of the ozone generation skid.
[0025] Figure 5 shows a view of the mixing skid.
[0026] Figure 6 shows an alternative embodiment of the reaction vessel.
Detailed Description of Preferred Embodiments
[0027] An ozone system 10 for applying an aqueous solution of ozone will now be
described with reference to the accompanying Figures. The system 10 provides many
advantages over the prior art. The system 10 provides a centralized system for producing an
aqueous ozone solution, i.e., the aqueous ozone solution is prepared and distributed from a
central location in an industrial facility to different application points throughout the industrial
facility. The system 10 provides for the distribution of the aqueous ozone solution at different
flow rates and at different concentrations to the different application points. The system 10
monitors and maintains the ozone concentration and flow rate of the aqueous ozone solution at
desired levels. The system 10 provides a uniform and consistent aqueous ozone solution without
off-gassing problems. Fluctuations in the concentration of ozone in the aqueous ozone solution
are kept to a minimum with the aid of monitoring systems that monitor the concentration of
ozone in the aqueous ozone solution and modulate levels of ozone gas introduced into the
aqueous ozone solution. The system 10 increases the oxidation reaction potential of a
conventional aqueous ozone solution by reducing the bubble size of ozone gas and minimizing
the amount of bubbles of ozone in the aqueous ozone solution.
[0028] A process flow diagram for the system 10 is shown in Figure 1. A control
panel/central server 50 comprising a programmable logic controller and user interface is in
electrical communication with the components of the system 10 to operate, monitor, and direct
the system 10. The control panel/central server 50 regulates the concentration of ozone in the
ozonated water solution and the flow of ozonated water solution. The control panel/central
server 50 is in electrical communication with the various components, systems and assemblies of
the system 10 to ensure that the desired flow and concentration of the ozonated water solution
are maintained. The control panel/central server 50 regulates the flow and amount of ozone gas
that is entrained in the solution. The system 10 produces high pressure and high volumes of the
ozonated water solution to clean and sanitize industrial facilities. The system 10 may be scaled
depending upon its application, for example, the system 10 may provide lower volumes, e.g., 1
gallon per minute and higher volumes, e.g. 10,000 gallons per minute.
[0029] A reaction vessel 350 is incorporated in the system 10. The reaction vessel
350 entrains ozone gas in an aqueous solution of ozone. Figure 2 shows a sectional view of the
reaction vessel 350. The reaction vessel 350 reduces the bubble size of the ozone gas in the
aqueous ozone solution and the number of bubbles in the aqueous ozone solution. The reaction
vessel 350 increases the concentration of ozone in the aqueous ozone solution as well as its
oxidation reduction potential to improve the cleaning and sanitizing capabilities of the aqueous
ozone solution. Decreasing the bubble size of the ozone gas also assists in maintaining a
uniform concentration of ozone gas in the aqueous ozone solution and reducing off-gassing.
[0030] In the reaction vessel 350, fresh water and an aqueous ozone solution mix.
The reaction vessel 350 circulates the fresh water and forms a vortex, which mixes with the
aqueous ozone solution. The mixing in the reaction vessel 350 breaks the ozone gas in the
aqueous ozone solution into smaller and smaller bubbles, which exit the reaction vessel 350 in
the aqueous ozone solution. In reaction vessel 350, the aqueous ozone solution is forced into a
saturated aqueous ozone solution having an ozone concentration of up to approximately 20 ppm
and an oxidation reaction potential of up to approximately 2.6. Off-gassing of ozone gas is
reduced by the reaction vessel 350.
[0031] The reaction vessel 350 is in fluidic communication with a supply of the
aqueous ozone solution, e.g., a venturi 310, in which an aqueous ozone solution is formed by
injection of ozone gas into water in the venturi 310. The reaction vessel 350 is also in fluidic
communication with a supply of water 330 for mixing with the aqueous ozone solution. After
the mixing in the reaction vessel 350, the reaction vessel 350 outputs the aqueous ozone solution
to a contact tank 405.
[0032] The reaction vessel 350 comprises a conical-shaped surface 385 having a
plurality of edges 380 or ridges 382 on the conical-shaped surface 385. The conical-shaped
surface 385 imparts a rotating action or a vortex to the water entering the reaction vessel 350
from the supply of water 330, and the water rotates about the conical-shaped surface 385 toward
the aqueous ozone solution entering the reaction vessel 350, which crushes ozone gas bubbles in
the aqueous ozone water solution.
[0033] The reaction vessel 350 is shown illustrated for use with an exemplary
system 10 in Figures 1 and 3-5. One of ordinary skill in the art will recognize that the reaction
vessel 350 may be used with other industrial cleaning systems that use an aqueous solution of
ozone.
[0034] The methods of forming the aqueous ozone solution will now be described.
The methods described herein reduce the bubble size of ozone gas in the aqueous ozone solution
and the number of bubbles in the aqueous ozone solution. The methods increases the
concentration of ozone in the aqueous ozone solution as well as its oxidation reduction potential
to improve the cleaning and sanitizing capabilities of the aqueous ozone solution. The
compositions of aqueous ozone solution described herein have less bubbles and smaller bubbles
of ozone gas than conventional solutions. Decreasing the bubble size of the ozone gas also
assists in maintaining a uniform concentration of ozone gas in the aqueous ozone solution and
reducing off-gassing. The compositions of aqueous ozone solution provide for cleaning and
sanitizing of industrial facilities.
[0035] Fresh water and a first aqueous ozone solution are mixed to form a second
aqueous ozone solution. The reaction vessel 350 circulates the fresh water and forms a vortex,
which mixes with the first aqueous ozone solution with the water. The mixing in the reaction
vessel 350 of the water and the first aqueous ozone solution breaks the ozone gas bubbles in the
first aqueous ozone solution into smaller and smaller bubbles and forms the second aqueous
ozone solution that exits the reaction vessel 350. In reaction vessel 350, the first aqueous ozone
solution is forced into a saturated aqueous ozone solution having an ozone concentration of up to
approximately 20 ppm and an oxidation reaction potential of up to approximately 2.6. Off-
gassing of ozone gas is reduced by the reaction vessel 350, as many of the gas bubbles in the first
aqueous ozone solution are crushed.
[0036] The reaction vessel 350 is in fluidic communication with a supply of the first
aqueous ozone solution, e.g., the venturi 310. The reaction vessel 350 is also in fluidic
communication with the supply of water 330 for mixing with the first aqueous ozone solution.
After the mixing in the reaction vessel 350, the reaction vessel 350 outputs the second aqueous
ozone solution to a contact tank 405. The reaction vessel and its conical-shaped surface 385
imparts a rotating action or a vortex to the water entering the reaction vessel 350 from the supply
of water 330, and the water rotates about the conical-shaped surface 385 toward the first aqueous
ozone solution entering the reaction vessel 350, which crushes ozone gas bubbles in the first
aqueous ozone water solution.
[0037] The preparation of the ozone gas will now be described.
[0038] The ozone gas for use with the system 10 is produced from ambient air. An
important feature of the system 10 is that it ensures that a consistent supply of dried air is
delivered to oxygen concentrators 160, which produce essentially pure oxygen gas for ozone
generation in ozone generators 240, such that the system 10 provides a sufficient quantity of
ozone gas with consistent quality. The consistent supply of dried air ultimately assists in
creating the consistent supply of the aqueous ozonated solution produced by the system 10.
[0039] The system 10 draws in the ambient air to a compressed dry air supply skid
100 (shown in Figure 3) comprising an air compressor 120, a dryer 140, a dew point monitor
150, the oxygen concentrators 160, and an oxygen storage tank 180. The air compressor 120 is
in communication with the dryer 140. The air compressor 120 compresses the ambient air and
delivers the compressed air to the dryer 140. The compressed air is dried in the dryer 140. The
dryer 140 is in communication with the dew point monitor 150, which measures the dew point of
air exiting the dryer 140. A suitable dew point monitor 150 is commercially available from
Vaisala Instruments.
[0040] From the dew point monitor 150, the compressed and dried air passes to the
oxygen concentrators 160, which produce essentially pure oxygen gas from the dried and
compressed air that is stored in the oxygen storage tank 180. The oxygen storage tank 180 acts
as a storage and supply reservoir of oxygen for ozone generation. Excess oxygen is stored in the
oxygen storage tank.
[0041] Maintaining a high concentration of oxygen in the oxygen gas assists in
creating the consistent supply of the aqueous ozonated solution produced by the system 10.
Generally, the essentially pure oxygen gas will contain over 90% pure oxygen, with a preferred
range of approximately 95% to 98% pure oxygen. The oxygen concentrators 160 may use a
pressure swing adsorption process using a molecular sieve. A suitable oxygen concentrator 160
is commercially available from the AirSep Corporation. The compressed dry air supply skid 100
may further include one or more filters 132 for oil and contaminant removal, one or more
pressure indicators 134 for monitoring the pressures of the compressed air and the stored oxygen
gas in the oxygen storage tank 180, and one or more pressure relief valves 136 for discharging
pressurized gas. A flow controller 138 modulates the flow of oxygen gas from the oxygen
concentrators 160 to the oxygen storage tank 180, while one of the pressure indicators 134 and
one of the pressure relief valves 136 is also employed to monitor and provide pressure relief for
the oxygen gas directed to the oxygen storage tank 180 from the oxygen concentrators 160.
[0042] The essentially pure oxygen gas is delivered to an ozone generation skid 200
(shown in Figure 4) comprising the ozone generator 240, an ozone destruct unit 260, a
distribution manifold 270, and one or more mass flow controllers 305. The ozone generation
skid produces ozone and directs it via the distribution manifold 270 and the one or more mass
flow controllers 305 to one or more mixing skids 300 (shown in Figure 5).
[0043] The ozone generator 240 produces ozone gas from the essentially pure oxygen
gas. The ozone generator 240 is in communication with the oxygen storage tank 180. The ozone
generator 240 is configured with a cooling system, such as a cool-water recirculation jacket 243,
to maintain the ozone generator 240 at under approximately 100° F. The ozone generator may
utilize a corona discharge method of ozone generation. Maintaining a cool temperature is
preferred to regulate ozone concentration, as higher concentrations of ozone gas are achieved
from the ozone generator 240 when the temperature of the ozone generator 240 is maintained at
these cool levels. The ozone destruct unit 260 receives excess ozone or ozone that has separated
from the aqueous ozone solution in other parts of the system 10 for destruction.
[0044] As shown in Figure 4, the ozone generation skid 200 comprises one or more
ozone generators 240. Some of the one or more ozone generators may only be used in a backup
capacity, i.e., when one of the previously operational ozone generators 240 require maintenance
or breaks-down. As such, the industrial facility will not need to shut down for a conventional
cleaning process when one of the ozone generators 240 is non-operational. Depending on the
overall size of the system 10, up to 30 or more ozone generators 240 may be included in the
ozone generation skid 200. The ozone generators 240 are in electrical communication with the
control panel/central server 50 in order to monitor and control their operation.
[0045] The ozone generation skid 200 includes the distribution manifold 270 and the
mass flow controllers 305 for disseminating the ozone gas to the one or more mixing skids 300
for mixing with water to produce the aqueous ozone solution. The distribution manifold 270 is
in communication with the ozone generators 240. An isolation valve 242, an air actuated ball
valve 244, and a back flow preventer 246 are positioned between the ozone generator 240 and
the distribution manifold 270 to direct the flow of ozone gas from the ozone generator 240 to the
distribution manifold 270.
[0046] The mass flow controllers 305 are in electrical communication with the
control panel/central server 50 for modulating the flow of the ozone gas. A suitable mass flow
controller 305 is commercially available from Eldrige, Products, Inc.
[0047] Typically, the distribution manifold 270 will branch into separate lines each
having a mass flow controller 305a-g in communication with each of the one or more mixing
skids 300a-g. Additional isolation valves 242 are configured between the mass flow controllers
305a-g and the distribution manifold 270. The number of mixing skids 300a-g and mass flow
controllers 305a-g will depend upon the application requirements of the system 10. For
example, certain industrial facilities may only require two to four mixing skids 300a-g and mass
flow controllers 305a-g, while other industrial facilities may require six to eight mixing skids
300a-g and mass flow controllers 305a-g. The distribution manifold 270 further directs ozone gas
to an auxiliary use, such as a deodorizer, or to the ozone destruction unit 260.
[0048] As shown in Figure 5, the one or more mixing skids 300 comprise the venturi
310, the reaction vessel 350, the contact tank 405, a degassing separator 420, a demister 440, a
mixing ozone monitor 460, and a pump 480. At the mixing skids 300, water from the water
supply 330 and ozone gas from the ozone generation skid 200 are directed via lines, hoses,
and/or piping to the venturi 310 for forming an aqueous ozone solution. The venturi 310 acts as
an injector, i.e., it injects the ozone gas into the water. A preferred injector is commercially
available from the Mazzei Injector Corporation; however, any of a variety of injectors could be
utilized in the one or more mixing skids 300.
[0049] As previously noted, before reaching the venturi 310, the ozone gas passes
through the one or more mass flow controllers 305a-g, which measures the flow of ozone to the
venturi 310 and modulates the flow of ozone to the venturi 310. The mass flow controllers 305a-
g are in electrical communication with the control panel/central server 50 in order regulate and
control the flow of ozone gas through the mass flow controllers 305a-g. The operator of the
system may adjust the flow of ozone to the venturi 310 to obtain the desired ozone
concentrations level in the aqueous ozone solution.
[0050] Although an aqueous ozone solution has now been formed by the venturi 310,
the aqueous ozone solution is now directed to the reaction vessel 350 for further processing to
reduce the bubble size of the ozone gas in the aqueous ozone solution and number of bubbles and
to increase the concentration of ozone in the aqueous ozone solution as well as its oxidation
reduction potential. Decreasing the bubble size of the ozone gas also assists in maintaining a
uniform concentration of ozone gas in the aqueous ozone solution. A supply of water is in
communication with the reaction vessel 350. The supply of water directs water to a conical-
shaped surface of the reaction vessel 350, and the water mixes with the aqueous ozone solution
to form the second aqueous ozone solution.
[0051] The operation and structure of the reaction vessel 350 will now be described
in detail with reference to Figure 2. The aqueous ozone solution from the venturi 310 is
discharged into the bottom of reaction vessel 350 at an inlet port 355. The aqueous ozone
solution travels up an inner vortex assembly sleeve 370 in the interior of the reaction vessel 350.
[0052] Nozzles 360 discharge a stream of fresh water, at approximately 50 to 55 psi,
at the top of the reaction vessel 350 into the inner vortex assembly sleeve 370. The water from
the nozzles 360 dilutes the aqueous ozone solution from the venturi 310. The nozzles 360 receive
the fresh water from the water supply 330 through a fresh water inlet 345 and a regulator 348.
The regulator 348 is in electrical communication with the control panel/central server 50. The
regulator 348 provides pressure readings to the control panel/central server 50, and the regulator
348 modulates the pressure and flow of fresh water into the inner vortex assembly sleeve 370 at
the direction of the control panel/central server 50. The pressure in the inner vortex assembly
sleeve 370 is varied to accommodate the desired flow rate of the aqueous ozonated water
solution from the particular mixing skid 300 a-g. If the pressure in the inner vortex assembly
sleeve 370 is too high, then off-gassing problems of ozone gas may occur.
[0053] The inner vortex assembly sleeve 370 is shown in Figure 2. The inner vortex
assembly sleeve 370 is under a pressure of approximately 50 psi to approximately 125 psi. The
inner vortex assembly sleeve 370 comprises a conical-shaped surface 385. The aqueous ozone
solution enters the bottom of the reaction vessel 350 at the inlet port 355, while fresh water is
discharged from nozzles 360 toward the entering aqueous ozone solution.
[0054] From the inlet port 355, the aqueous ozone solution enters a cavity 358, which
acts as a reservoir to receive the aqueous ozone solution. An opening 365 separates the conical-
shaped surface 385 from the cavity 358. The opening 365 is in fluidic communication with the
cavity 358 and the inner vortex assembly sleeve 370. The inner vortex assembly sleeve 370 has
a narrow diameter toward the inlet port 355 and the opening 365 and gradually increases in
diameter toward an outlet 390, which creates the conical-shaped surface 385. The opening 365
is at the narrowest point of the conical-shaped surface 385.
[0055] The nozzles 360 direct the fresh water at the conical-shaped surface 385.
Specifically, the nozzles 360 direct the fresh water at the sloping surfaces of the conical-shaped
surface 385. The conical-shaped surface has sloping surfaces or sides leading to the opening
365. The direction of the nozzles 360 and the conical-shaped surface 385 imparts a rotating
action or a vortex to the fresh water, and the fresh water rotates about the conical-shaped surface
385 toward the opening 365. As such, fresh water from the nozzles 360 moves down the
conical-shaped surface 385 in the rotating manner, under centrifugal force, which crushes ozone
gas bubbles in the aqueous ozone water solution entering the inner vortex assembly sleeve 370
through the opening 365 from the cavity 358 and crushes ozone gas bubbles in the aqueous
ozone water solution in the cavity 358.
[0056] At the opening 365, some of the rotating fresh water from the nozzles 360
may enter the cavity 358. Ozone gas from the aqueous ozone solution may diffuse with the fresh
water in the cavity 358 and at the opening 365. At the opening 365, the aqueous ozone solution
from the cavity 358 passes into a cone void 388, which is the generally hollow central region of
the inner vortex assembly sleeve 370, as defined by the conical-shaped surface 385.
[0057] The inner vortex assembly sleeve 370 comprises approximately 10 to
approximately 50 of the edges 380 on the conical-shaped surface 385. Each of the edges 380
may comprise a generally perpendicular angle above and below the adjacent edge 380. The
edges 380 form a stair-step like surface for the conical-shaped surface 385. The edges 380
surround a perimeter of the cone void 388. The edges 380 are in contact with the hollow interior,
i.e., the cone void 388. Other constructions, geometries, or surfaces on the conical-shaped
surface 385 may be employed to reduce the bubble size of the ozone gas. For example, as shown
in Figure 6, the conical-shaped surface 385 may include a plurality of the concentric ridges 382
about the conical-shaped surface 385.
[0058] The inner vortex assembly sleeve 370 turns the aqueous ozone solution, under
high pressure, around and against the series of edges 380 on the interior conical shaped surface
385 of the inner vortex assembly sleeve 370. The interaction of the fresh water, the aqueous
ozone solution, and the edges 380 crush and break the ozone gas into smaller and smaller
bubbles in the second aqueous ozone solution, which exits the reaction vessel 350 at the outlet
390. Off-gassing of ozone gas into the cone void 388 is re-mixed into the aqueous ozone
solutions. The conical-shaped surface 385 and discharge of fresh water from the nozzles 360
causes the fresh water to circulate and form a vortex which mixes with the aqueous ozone
solution passing through the inner vortex assembly sleeve 370 and eventually exiting at the outlet
390. The sleeve 370 is significant to cause the necessary break down of the microscopic bubbles
of ozone gas and allows the maximum molar absorptivity of the ozone gas into the aqueous
solution. The aqueous ozone solution is forced into a saturated aqueous ozone solution having
an ozone concentration of up to approximately 20 ppm and an oxidation reaction potential of up
to approximately 2.6. Breaking down the bubbles of ozone into smaller bubbles of ozone
increases the oxidation reduction potential of the ozone in the aqueous ozone solution. The
greater oxidation reduction potential of the aqueous ozone solution water allows the ozone to act
not only as a sanitizer, but as a degreaser and therefore has more oxidizing power than
conventionally mixed solutions.
[0059] Typically, the aqueous ozone solution entering the reaction vessel 350 at the
inlet port 355 and the fresh water entering the reaction vessel forms a solution that is
approximately 10% to approximately 20% fresh water, i.e., approximately 1 part by volume
fresh water from the water supply is mixed with approximately 4 parts to approximately 9 parts
by volume aqueous ozone solution from the inlet port 355. However, due to the crushing of the
ozone bubbles in the reaction vessel 350, the ORP value for the aqueous ozone solution exiting
the outlet 390 is approximately the same as the ORP value for the aqueous ozone solution
entering the inlet 355, despite the dilution of the aqueous ozone solution entering the inlet 355 by
the fresh water from the nozzles 360.
[0060] The reaction vessel 350 and the inner vortex assembly sleeve may be made
from stainless steel, metal alloys, or hard plastic materials, such as chlorinated Polyvinyl
Chloride (CPVC).
[0061] From the outlet port 390 of the reaction vessel 350, the aqueous ozone
solution is directed to the contact tank 405 and a degassing separator 420 in communication with
the reaction vessel 350. The contact tank 405 should have a volume approximately twice the
desired amount of volume of aqueous ozone solution. For example, if the mixing skid 300a is
providing 100 gallons/per minute in flow, then the contact tank 405 should have a capacity of
approximately 200 gallons. As such, in this particular example, the solution is spending
approximately two minutes in the contact tank 405.
[0062] Large gas bubbles are separated from the aqueous ozone solution in the
degassing separator 420. The degassing separator is important to remove the excess ozone
bubbles from the aqueous ozone solution to reduce the levels of free ozone gas released at an
application point during the spraying of the aqueous ozone solution, which in high
concentrations could breach OSHA regulations. The separated gas bubbles are directed to a
demister 440, where a liquid component of the separated gas bubble is collected and drained,
while an ozone gas component of the separated gas bubbles is directed from the demister 440 to
the ozone destruction unit 260.
[0063] The aqueous ozone solution exiting the degassing separator 420 passes
through and the mixing ozone monitor 460 and on to one or more pumps 480 via piping, hosing
and/or lines. Depending upon the cleaning and sanitizing application of the system 10, the
aqueous ozone solution may be directed to one or more of the pumps 480 which may pump the
aqueous ozone solution at different flow rates and pressures from the mixing skid 300. The
aqueous ozone solution is pumped from the mixing skid 300 via distribution piping/hosing 510
in communication with the pumps 480 to one or more applicators 530 for applying the aqueous
ozone solution to the hard surfaces and other items for sanitation. The applicators 530 include
spray wands, nozzles, brushes, nebulizers, spray guns and the like, and various combinations
thereof. Each applicator 530 includes an applicator ozone monitor 550.
[0064] The concentration of the aqueous ozone solution is monitored by the
applicator ozone monitor 550, which measures the exact concentration of ozone in the aqueous
ozone solution exiting from the applicator 530. The plant operator may monitor and adjust the
concentration of ozone in the aqueous ozone solution based on readings from the applicator
ozone monitor 550.
[0065] The applicator ozone monitor 550 is in electrical communication with the
control panel/central server 50. If the applicator ozone monitor 550 indicates that the levels of
ozone in the aqueous ozone solution are too low, then the operator or automated systems in the
control panel/central server 50 may adjust the mass flow controller 305 to increase the amount of
ozone gas directed to the venturi 310, such that concentration levels of ozone in the aqueous
ozone solution at the applicator ozone monitor 550 are increased.
[0066] The system 10 may comprise one or mixing skids 300 with one or more
pumps 480 supplying one or more applicators 530. The one or more pumps 480 may pump the
aqueous ozone solution at different rates and at different concentrations to the different
applicators 530. The system 10 may be customized, depending upon a specific industrial facility
and its specific cleaning needs. For example, the system 10 may comprise a variety of high
pressure and low pressure applicators 530 and with certain applicators applying different
concentrations of aqueous ozone solution. The system 10 provides an applied dosage of an
aqueous ozone solution that is consistent over time in terms of the desired concentration and
flow rate to the one or more applicators 530. The control panel/central server 50, in conjunction
with the applicator ozone monitor 550 and mass flow controllers 305, monitor and regulate the
concentration and flow of the aqueous ozone solution.
[0067] The reaction vessel 350 is important to the mass transfer of ozone gas in the
water, i.e., how the ozone gas is dissolved into the water to form the aqueous ozone solution.
The system 10 produces a saturated aqueous ozone solution having an ozone concentration of up
to approximately 20 ppm.
[0068] The system 10, and specifically the reaction vessel 350, help reduce the
number of bubbles and create the smallest possible bubbles of ozone in the aqueous ozone
solution in order to produce the saturated aqueous ozone solution with an ozone concentration of
up to approximately 20 ppm and an oxidation reduction potential of 2.6. The amount of ozone
dissolved into the water depends, in part, on the surface area of the gas/water interaction. The
smaller the bubble, the better the mass transfer because one cubic inch of tiny bubbles has much
more surface area than a single, one cubic inch bubble.
[0069] The edges 380 on the inner vortex assembly sleeve 370 assist in physically
reducing the bubble size of the ozone gas. As the aqueous ozone solution is forced through the
inner vortex assembly sleeve 370, the bubbles of ozone contact the edges 380 and break into
smaller and smaller bubbles. The smaller bubbles dissolving in the water help to saturate the
aqueous ozone solution with ozone.
[0070] The pressure applied in the reaction vessel 350, of approximately 50 psi to
approximately 125 psi, also improves the mass transfer between the bubbles of ozone gas and the
water. The higher the pressure, the more a "squeeze" is put on the transfer of gas bubbles into
the water enhancing the process of dissolving the gas bubbles into the aqueous ozone solution
and creating the saturated aqueous ozone solution. The higher pressure also forces the gas
bubbles against the edges 380 further breaking them down into smaller bubbles.
[0071] The temperature of the water is also an important consideration in the mass
transfer process. At cooler temperatures, the ozone diffuses better in the water. At cooler water
temperatures, the contact time between the ozone gas bubbles and the water in forming the
aqueous ozone solution is reduced. In general, it is difficult for water to absorb a gas when the
water is trying to become a gas. The water from the water supply 330 should be at a temperature
of approximately 33° F. to approximately 50° F.
[0072] The concentration of the ozone gas in the carrier gas also affects the mass
transfer of the ozone gas in to the water. Higher concentrations of ozone in the carrier gas will
result in higher concentrations of ozone being absorbed into the aqueous ozone solution. Corona
discharge ozone generation equipment generally creates higher concentrations of ozone gas in
the carrier gas than ultraviolet types of ozone generation.
[0073] The system 10 produces an aqueous ozone solution to attack and destroy
pathogens and act as a no-rinse sanitizer for hard surfaces in a variety of applications, especially
industrial processing facilities related to food processing. The solution of aqueous ozone is
applied at high pressure to the hard surfaces, and is effective for the removal of soils and bulk
materials from the hard surfaces. When applied at high pressure, the solution penetrates the soils
and oxides of the biofilm that acts as the bond or glue that allows the soils and oxides to attach
themselves to the hard surfaces. The system 10 is designed to be the first totally chemical free
system to destroy the biofilm on conveyors systems and hard surfaces during food processing
production allowing for continuous or extended production.
[0074] There are many applications for both high and low pressure. When the
solution discharges from the assembly, the solution could be channeled into both a high pressure
stream as well as a low pressure stream. The high-pressure stream of aqueous ozone solution
may be better suited for cleaning and sterilizing highly soiled hard surfaces due to the extra force
supplied by the high pressure aqueous ozone solution which will help destroy the biofilm
adhering the soils to the hard surfaces. The low pressure aqueous ozone solution may be suited
for the continuous sanitization of hard surface or application to a food item.
[0075] In the embodiment shown, the ozone produced by the ozone generator 240
uses a high electrical discharge called "corona discharge" or "CD". This method is most
commonly used to generate usable amounts of ozone for most water treatment applications.
Corona discharge creates a small, controlled lightning storm, which involves producing a
constant, controlled spark (corona) across an air gap through which a prepared feed gas is
passed. This feed gas may be air that has simply had most of its moisture removed or air with
enhanced oxygen levels. An important aspect of using the corona discharge methods of ozone
production is ensuring that feed gas is dried at the dryer 140 to a dew point of at least
approximately -60F. This is important because as the electrical discharge splits the oxygen
molecules, nitrogen molecules are also being split, forming several species of nitrogen oxides,
which are normally benign. If feed gas is not sufficiently dried, then the nitrogen oxides
combine with moisture from ordinary humidity and form nitric acid, which may be corrosive to
the system 10, the hard surfaces, and the industrial facility. Consequently, proper air preparation
is important for the operation of the system 10. The relative strength of corona discharge ozone
expressed as a percentage of concentration by weight is commonly 0.5 — 1.7% for systems
using dried air, and 1.0 — 6.0% when an oxygen enhanced feed gas is used.
[0076] A properly installed and operated system 10 poses no health hazards. While
ozone is a toxic gas and the established concentration limits must be adhered to, the odor
threshold of 0.01 ppm is far below the safety limit of 0.1 ppm exposure over an eight hour
period. The first symptoms of excessive ozone exposure are headaches, eye, nose or throat
irritation or a shortness of breath. These symptoms can be relieved by the simple application of
fresh air. While no deaths have been reported from ozone, sound safety practices deserve
attention. Ozone off-gas containment and destruction equipment for most water treatment
applications is readily available and is usually a simple device containing either activated carbon
or manganese dioxide.
[0077] Ozone is a much more powerful oxidizer than chlorine. Based on EPA charts
of surface water CT values (disinfectant residual and time constant), chlorine CT values are
nearly 100 times greater than ozone, meaning that ozone acts much more quickly than chlorine.
Ozone creates none of the trihalomethanes commonly associated with chlorine compounds and
properly matched to the application; ozone will reduce most organic compounds to carbon
dioxide, water and a little heat. Finally, as ozone sheds the atom of the oxygen causing its
molecular instability during the oxidation process, it becomes oxygen again.
[0078] Facilities processing bottled water, perishable goods (meat, seafood, fruit,
vegetables, etc.) are examples of ideal applications for the system 10. The fact that ozone
efficiently oxidizes the organics that cause taste, odor, and color problems without leaving a high
residual helps to simplify many water treatment. The lack of residual from ozone cleaning and
santiation also makes ozone perfect for pre- and post-treatment processes in wash pad recycle
systems, where the use of a chlorine compound would contribute to pH control or off gas
problems. Additionally, ozone oxidizes and precipitates many metals and destroys some
pesticides without leaving a trace. Finally, ozone functions as a preoxidizer of iron, manganese
and sulfide compounds, allowing for their removal by simple direct filtration. Ozone acts
quickly and easily, and the water quality resulting from its use is unmatched.
[0079] It should be understood from the foregoing that, while particular embodiments
of the invention have been illustrated and described, various modifications can be made thereto
without departing from the spirit and scope of the present invention. Therefore, it is not intended
that the invention be limited by the specification; instead, the scope of the present invention is
intended to be limited only by the appended claims.
We claim:
1. An industrial cleaning system that produces and distributes an aqueous ozone
solution, comprising:
an ozone generator for generating ozone gas;
an injector in communication with the ozone generator and in communication with a
supply of water, wherein the injector injects ozone gas from the ozone generator
into the water from the supply of water to form an aqueous ozone solution;
a reaction vessel in fluidic communication with the injector for receiving the aqueous
ozone solution from the injector, wherein the reaction vessel comprises a conical-
shaped surface having a plurality of edges or ridges; and
a pump in communication with the reaction vessel for distributing the aqueous ozone
solution.
2. The industrial cleaning system according to claim 1, wherein the aqueous ozone
solution from the injector is discharged into the bottom of the reaction vessel at an inlet port, and
the aqueous ozone solution travels up an inner vortex assembly sleeve in the interior of the
reaction vessel, and nozzles discharge a stream of fresh water at the top of the reaction vessel
into the inner vortex assembly sleeve.
3. The industrial cleaning system according to claim 2, wherein the inner vortex
assembly sleeve has a narrow diameter near the inlet port and gradually increases in diameter
toward an outlet which creates the conical-shaped surface on the inner vortex assembly sleeve.
4. The industrial cleaning system according to claim 1, further comprising a
degassing separator in communication with the reaction vessel to remove Ozone bubbles from the
aqueous ozone solution.
5. The industrial cleaning system according to claim 1, further comprising an air
compressor in communication with a dryer to provide compressed air to the dryer; a dew point
monitor that measures the dew point of the compressed and dried air from the dryer; an oxygen
concentrator in communication with the dryer that receive the compressed and dried air from the
dryer to produce oxygen gas; an oxygen storage tank in communication with the oxygen
concentrator that receives the oxygen gas from the oxygen concentrator; the oxygen storage tank
in supply communication with the ozone generators to supply the ozone generators with the
oxygen gas.
6. The industrial cleaning system according to claim 1, wherein the oxygen gas is
approximately 95% to approximately 98% oxygen.
7. The industrial cleaning system according to claim 1, wherein the ozone generator
comprises a cooling system to maintain the ozone generator at under approximately 100° F.
8. The industrial cleaning system according to claim 7, wherein the cooling system
is a water-cooled jacket in contact with the ozone generator.
9. The industrial cleaning system according to claim 1, wherein the reaction vessel is
in fluidic communication with the injector for receiving the aqueous ozone solution from the
injector and in fluid communication with the fresh water supply for supplying fresh water to the
reaction vessel.
10. The industrial cleaning system according to claim 1, further comprising a
distribution manifold in communication with the ozone generator to distribute the ozone gas, and
one or more mass flow controllers to modulate the flow of ozone gas from the distribution
manifold.
11. The industrial cleaning system according to claim 1, further comprising an
applicator in fluidic communication with the pump, wherein the applicator dispenses the aqueous
ozone solution, and the applicator comprises an ozone monitor to measure the concentration of
ozone in the aqueous ozone solution dispensed from the applicator, wherein the ozone monitor is
in electrical communication with a control panel that operates the system
12. The industrial cleaning system according to claim 11, wherein the control panel
modulates the flow of ozone gas to the venturi based on the concentration of ozone in the
aqueous ozone solution dispensed from the applicator as measured by the ozone monitor.
13. The industrial cleaning system according to claim 1, wherein the system produces
and distributes aqueous ozone solution with an oxidation reaction potential of up to
approximately 2.6.
14. The industrial cleaning system according to claim 1, wherein the system produces
and distributes an aqueous ozone solution with an ozone concentration of up to approximately 20
ppm.
15. The industrial cleaning system according to claim 1, wherein the reaction vessel
comprises approximately 10 to approximately 50 edges or ridges.
16. The industrial cleaning system according to claim 1, wherein the edges comprise
a perpendicular angle.
17. The industrial cleaning system according to claim 1, wherein the reaction vessel is
in fluidic communication with a supply of water, and water mixes with the aqueous ozone
solution in the reaction vessel to form a solution that is approximately 10% to approximately
20% water.
18. The industrial cleaning system according to claim 1, wherein the reaction vessel is
in fluidic communication with a contact tank.
19. The industrial cleaning system according to claim 1, wherein the system provides
an applied dosage of an aqueous ozone solution that is consistent over time in terms of
concentration and flow rate.
20. The industrial cleaning system according to claim 1, wherein the system is
centrally located in an industrial facility, and the system comprises one or pumps that are in
fluidic communication with one or more applicators for spraying the aqueous ozone solution in
or about the industrial facility.
21. An industrial cleaning system that produces and distributes an aqueous ozone
solution, comprising:
an air supply skid comprising an air dryer in communication with an oxygen concentrator
to produce oxygen gas;
an ozone generation skid comprising an ozone generator in communication with the air
supply skid to receive oxygen gas in order to generate ozone, the ozone generator
in communication with a distribution manifold for distributing the ozone gas to
one or more mixing skids; and
one or more mixing skids each comprising an injector in communication with the ozone
generation skid and a supply of water, wherein the injector injects ozone gas from
the ozone generation skid into the water from the supply of water to form an
aqueous ozone solution; a reaction vessel in fluidic communication with the
injector for receiving the aqueous ozone solution from the injector, the reaction
vessel in fluidic communication with the supply of water for mixing water with
the aqueous ozone solution from the injector, and one or more pumps in
communication with the reaction vessel for distributing the aqueous ozone
solution to one or more applicators.
22. An industrial cleaning system that produces and distributes an aqueous ozone
solution, comprising:
an ozone generator for generating ozone gas;
an injector in communication with the ozone generator and in connection with a supply of
water, wherein the injector injects ozone gas from the ozone generator into the
water from the supply of water to form an aqueous ozone solution;
a reaction vessel in fluidic communication with the injector for receiving the aqueous
ozone solution from the injector;
the reaction vessel in fluidic communication with the supply of water for mixing the
aqueous ozone solution with the water,
a pump in communication with the reaction vessel for distributing the aqueous ozone
solution;
a control panel that operates the system; and
an applicator in fluidic communication with the pump, wherein the applicator dispenses
the aqueous ozone solution, and the applicator comprises an ozone monitor to
measure the concentration of ozone in the aqueous ozone solution dispensed from
the applicator, wherein the ozone monitor is in electrical communication with the
control panel.
23. An industrial cleaning system that produces and distributes an aqueous ozone
solution, comprising:
an ozone generation system, comprising:
an air compressor in communication with a dryer to provide compressed air to the
dryer;
an oxygen concentrator in communication with the dryer that receive the
compressed and dried air from the dryer to produce oxygen gas;
an oxygen storage tank in communication with the oxygen concentrator that
receives the oxygen gas from the oxygen concentrator;
the oxygen storage tank in supply communication with one or more ozone
generators to supply the ozone generators with the oxygen gas to generate
ozone;
an injector in communication with the one or more ozone generators and in
communication with a supply of water, wherein the injector injects ozone gas
from the ozone generator into the water from the supply of water to form an
aqueous ozone solution;
a reaction vessel in fluidic communication with the injector for receiving the aqueous
ozone solution from the injector and reducing a bubble size of ozone gas in the
aqueous ozone solution;
a pump in communication with the reaction vessel for distributing the aqueous ozone
solution; and
a control panel that operates the system.
24. A reaction vessel for entraining ozone gas in an aqueous solution in an
industrial cleaning system, comprising:
a conical-shaped surface having a plurality of edges, the conical-shaped surface defining
a generally hollow interior, and the plurality of edges in contact with the generally
hollow interior;
an inlet port in fluidic communication with a supply of an aqueous ozone solution to
supply the aqueous ozone solution to the conical-shaped surface;
nozzles in fluidic communication with a supply of water, wherein the nozzles direct the
water under pressure at the conical-shaped surface, and the water mixes with the
aqueous ozone solution from the inlet port; and
an outlet in fluidic communication with the industrial cleaning system.
25. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the inlet port discharges the aqueous ozone solution in a bottom of the reaction vessel,
and the aqueous ozone solution travels up an inner vortex assembly sleeve in the interior of the
reaction vessel, and the nozzles discharge the fresh water at a top of the reaction vessel into the
inner vortex assembly sleeve, and the inner vortex assembly sleeve comprises the conical-shaped
surface.
26. The reaction vessel for an industrial cleaning system according to claim 25,
wherein the inner vortex assembly sleeve has a narrower diameter near the inlet port and
increases in diameter toward the outlet.
27. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the reaction vessel is in fluidic communication with an injector for receiving the
aqueous ozone solution from the injector.
28. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the conical-shaped surface has sloping sides.
29. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the conical-shaped surface has sloping sides leading to an opening.
30. The reaction vessel for an industrial cleaning system according to claim 29,
wherein the opening is in fluidic communication with a cavity, wherein the cavity is in fluidic
communication with the inlet port supplying the aqueous ozone solution.
31. The reaction vessel for an industrial cleaning system according to claim 24,
wherein an opening separates the conical-shaped surface from a cavity, and the opening is in
fluidic communication with the cavity and an inner vortex assembly sleeve.
32. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the reaction vessel produces an aqueous ozone solution with an oxidation reaction
potential of up to approximately 2.6.
33. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the reaction vessel produces an aqueous ozone solution with an ozone concentration of
up to approximately 20 ppm.
34. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the reaction vessel comprises approximately 10 to approximately 50 edges.
35. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the edges comprise a perpendicular angle.
36. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the nozzles are in operational communication with a regulator, and the regulator
provides a pressure of approximately 50 psi to approximately 125 psi in the reaction vessel.
37. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the water from the nozzles mixes with the aqueous ozone solution to form a solution that
is approximately 10% to approximately 20% water,
38. The reaction vessel for an industrial cleaning system according to claim 24,
wherein the reaction vessel is in fluidic communication with a contact tank.
39. The reaction vessel for an industrial cleaning system according to claim 24,
comprising a plurality of ridges on the conical-shaped surface instead of the plurality of edges.
40. A reaction vessel for entraining ozone gas in an aqueous solution in an industrial
cleaning system, comprising:
a conical-shaped surface having a plurality of edges or ridges, the conical-shaped surface
defining a generally hollow interior, and the plurality of edges or ridges are in
contact with the generally hollow interior;
an inlet port in a bottom of the reaction vessel in fluidic communication with a supply of
an aqueous ozone solution to supply the aqueous ozone solution to the conical-
shaped surface;
a supply of water in communication with the reaction vessel, wherein the supply of water
directs water to the conical-shaped surface, and the water mixes with the aqueous
ozone solution from the inlet port; and
an outlet in fluidic communication with the industrial cleaning system.
41. A reaction vessel for entraining ozone gas in an aqueous solution in an industrial
cleaning system, comprising:
a conical-shaped surface having a plurality of edges or ridges;
an opening at the narrowest portion of the conical-shaped surface;
a supply of an aqueous ozone solution in communication with the reaction vessel to
supply the aqueous ozone solution to the conical-shaped surface via the opening;
and
a supply of water in communication the reaction vessel, wherein the supply of water
directs water to the conical-shaped surface, and the water mixes with the aqueous
ozone solution.
42. A method of producing an aqueous ozone solution in an industrial cleaning
system, comprising:
providing a reaction vessel for entraining ozone gas in an aqueous solution in an
industrial cleaning system, comprising:
a conical-shaped surface having a plurality of edges, the conical-shaped surface
defining a generally hollow interior, and the plurality of edges in contact
with the generally hollow interior;
an inlet port in fluidic communication with a supply of an aqueous ozone solution
to supply the aqueous ozone solution to the conical-shaped surface;
a supply of water that directs the water, under pressure, at the conical-shaped
surface;
an outlet in fluidic communication with the industrial cleaning system; and
directing the aqueous ozone solution through the inlet port to the conical-shaped surface;
directing the water to the conical-shaped surface; and
mixing the water and the aqueous ozone solution.
43. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 42, further comprising reducing a bubble size of ozone gas in the
aqueous ozone solution in the reaction vessel.
44. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 42, further comprising directing the water at the conical-shaped
surface and imparting a rotating action or vortex to the water as it mixes with the aqueous ozone
solution.
45. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 42, further comprising directing the water at the conical-shaped
surface and imparting a rotating action or vortex to the water and crushing ozone bubbles in the
aqueous ozone solution.
46. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 42, further comprising diluting the aqueous ozone solution from the
inlet port with the water from the supply of water.
47. A method of producing an aqueous ozone solution for an industrial cleaning
system, comprising:
providing a reaction vessel for entraining ozone gas in an aqueous solution in an
industrial cleaning system, comprising:
a conical-shaped surface having a plurality of edges or ridges, the conical-shaped
surface defining an interior, and the plurality of edges or ridges in contact
with the interior;
the reaction vessel in fluidic communication with a supply of water;
the reaction vessel in fluidic communication with a supply of a first aqueous
ozone solution;
directing the first aqueous ozone solution to the conical-shaped surface;
directing the water to the conical-shaped surface; and
mixing the water and the first aqueous ozone solution to form a second aqueous ozone
solution.
48. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 47, further comprising reducing a bubble size of ozone gas in the first
aqueous ozone solution in the reaction vessel.
49. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 47, wherein the concentration of ozone in the second aqueous ozone
solution is consistent over time.
50. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 47, further comprising directing the water at the conical-shaped
surface and imparting a rotating action or vortex to the water as it mixes with the first aqueous
ozone solution.
51. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 47, further comprising directing the water at the conical-shaped
surface and imparting a rotating action or vortex to the water and crushing ozone bubbles in the
first aqueous ozone solution.
52. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 47, further comprising diluting the first aqueous ozone solution with
the water from the supply of water.
53. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 47, wherein the second aqueous ozone solution has an oxidation
reduction potential of up to approximately 2.6.
54. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 47, wherein the second aqueous ozone solution has an ozone
concentration of up to approximately 20 ppm.
55. The method of producing an aqueous ozone solution in an industrial cleaning
system according to claim 47, wherein the second aqueous ozone solution is formed in a ratio of
approximately 1 part by volume water from the water supply with approximately 4 parts by
volume to approximately 9 parts by volume of the first aqueous ozone solution.
56. The aqueous ozone solution according to claim 47, wherein the water mixes with
the first aqueous ozone solution to form the second aqueous ozone solution that is approximately
10% to approximately 20% water.
57. A method of producing an aqueous ozone solution for an industrial cleaning
system, comprising:
compressing and drying ambient air;
concentrating oxygen gas from the ambient air into a supply of oxygen gas that contains
over 90% pure oxygen;
directing the oxygen gas to an ozone generator;
cooling the ozone generator;
producing ozone gas in the ozone generator;
directing the ozone gas and water from a water supply to an injector;
injecting the ozone gas into the water with the injector to form a first aqueous ozone
solution;
mixing the first aqueous ozone solution with water; and
forming a second aqueous ozone solution.
58. The method of producing an aqueous ozone solution according to claim 57,
further comprising mixing the water with the first aqueous ozone solution in a reaction vessel.
59. The method of producing an aqueous ozone solution according to claim 57,
further comprising reducing the number and size of ozone gas bubbles in the first aqueous ozone
solution.
60. A method of producing an aqueous ozone solution for an industrial cleaning
system, comprising:
providing a reaction vessel for entraining ozone gas in an aqueous solution in an
industrial cleaning system, wherein the reaction vessel is in fluidic
communication with a supply of water; wherein the reaction vessel is in fluidic
communication with a supply of a first aqueous ozone solution;
directing the first aqueous ozone solution to the reaction vessel;
directing water to the reaction vessel;
crushing bubbles of ozone gas in the first aqueous ozone solution with the water in the
reaction vessel; and
mixing the water and the first aqueous ozone solution to form a second aqueous ozone
solution, wherein an oxidation reduction potential value for the first aqueous
ozone solution is approximately the same as an oxidation reduction potential
value for the second aqueous ozone solution.
61 An aqueous ozone solution, prepared by the process comprising:
providing a reaction vessel for entraining ozone gas in an aqueous solution in an
industrial cleaning system, comprising:
a conical-shaped surface having a plurality of edges or ridges, the conical-shaped
surface defining an interior, and the plurality of edges or ridges in contact
with the interior;
the reaction vessel in fluidic communication with a supply of water;
the reaction vessel in fluidic communication with a supply of a first aqueous
ozone solution;
directing the first aqueous ozone solution to the conical-shaped surface;
directing water to the conical-shaped surface; and
mixing the water and the first aqueous ozone solution to form a second aqueous ozone
solution.
62. The aqueous ozone solution according to claim 61, further comprising reducing a
bubble size of ozone gas in the first aqueous ozone solution as it mixes with the water.
63. The aqueous ozone solution according to claim 61, further comprising directing
the water at the conical-shaped surface and imparting a rotating action or vortex to the water as it
mixes with the first aqueous ozone solution.
64. The aqueous ozone solution according to claim 61, further comprising diluting the
first aqueous ozone solution during the mixing with the water to form the second aqueous ozone
solution.
65. The aqueous ozone solution according to claim 61, further comprising directing
the water at the conical-shaped surface and imparting a rotating action or vortex to the water and
crushing ozone bubbles in the first aqueous ozone solution.
66. The aqueous ozone solution according to claim 61, wherein the second aqueous
ozone solution has an oxidation reduction potential of up to approximately 2.6 and an ozone
concentration of up to approximately 20 ppm.
67. An aqueous ozone solution comprising approximately 1 part by volume water
mixed with approximately 4 parts by volume to approximately 9 parts by volume of a first
aqueous ozone solution to form a second aqueous ozone solution that has an oxidation reduction
potential of up to approximately 2.6, wherein the second aqueous ozone solution has an ozone
concentration of up to approximately 20 ppm, wherein the second ozone solution has less ozone
gas bubbles than the first aqueous ozone solution.
68. The aqueous ozone solution ozone solution according to claim 67, wherein the
second ozone solution has smaller ozone gas bubbles than the first aqueous ozone solution.
69. An aqueous ozone solution comprising approximately 1 part by volume water
mixed with approximately 4 parts by volume to approximately 9 parts by volume of a first
aqueous ozone solution to form a second aqueous ozone solution, wherein the second aqueous
ozone solution has an ozone concentration of up to approximately 20 ppm, wherein an oxidation
reduction potential value for the first aqueous ozone solution is approximately the same as an
oxidation reduction potential value for the second aqueous ozone solution.

An industrial cleaning system 10 that produces and distributes an aqueous ozone
solution is described. The system 10 includes an ozone generator 240 for
generating ozone gas, which is injected by an injector 310 into a supply of water
to form the aqueous ozone solution. A reaction vessel 350 receives the aqueous
ozone solution from the injector 310 as the reaction vessel 350 reduces the
bubbles of ozone gas in the aqueous ozone solution to increase the oxidation
reduction potential of the aqueous ozone solution. The reaction vessel 350
includes a conical-shaped surface 385 having two or more edges 380 or ridges
382. The conical-shaped surface 385 defines a generally hollow interior 388.
An inlet port 355 is in fluidic communication with a supply of an aqueous ozone
solution to supply the aqueous ozone solution to the conical-shaped surface 380.
Nozzles 360 direct water under pressure at the conical-shaped surface 380, and
the water mixes with the aqueous ozone solution from the inlet port 355. An
outlet 390 is in fluidic communication with the industrial cleaning system 10. A
method of making an aqueous ozone solution is described. The reaction vessel
350 is in fluidic communication with a supply of a first aqueous ozone solution.
The first aqueous ozone solution is directed to the reaction vessel 350. Water
is directed to the reaction vessel 350, and the water and the first aqueous ozone
solution are mixed to form a second aqueous ozone solution. Compositions for
aqueous ozone solutions are also described. The aqueous ozone solution
contains approximately 1 part by volume water mixed with approximately 4 parts
by volume to approximately 9 parts by volume of the first aqueous ozone solution
to form the second aqueous ozone solution that has an oxidation reaction
potential of up to approximately 2.6 and having an ozone concentration of up to
approximately 20 ppm.

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Patent Number

270800

Indian Patent Application Number

3596/KOLNP/2009

PG Journal Number

04/2016

Publication Date

22-Jan-2016

Grant Date

21-Jan-2016

Date of Filing

14-Oct-2009

Name of Patentee

FOOD SAFETY TECHNOLOGY, LLC

Applicant Address

1004 FARNAM STREET, SUITE 103, OMAHA, NEBRASKA 68102, U.S.A.

Inventors:

#	Inventor's Name	Inventor's Address
1	LYNN, DANIEL W.	3418 SOUTH 165TH AVENUE, OMAHA,, NEBRASKA 68130, U.S.A.

PCT International Classification Number

C01B 13/10

PCT International Application Number

PCT/US2008/056936

PCT International Filing date

2008-03-14

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1	12/047,461	2008-03-13	U.S.A.
2	12/047,498	2008-03-13	U.S.A.
3	60/894,746	2007-03-14	U.S.A.
4	12/047,442	2008-03-13	U.S.A.