Electrode assembly, dielectric barrier discharge system and use thereof

Information

  • Patent Grant
  • 10925144
  • Patent Number
    10,925,144
  • Date Filed
    Friday, June 14, 2019
    5 years ago
  • Date Issued
    Tuesday, February 16, 2021
    3 years ago
  • Inventors
  • Original Assignees
    • Nanoguard Technologies, LLC (St. Louis, MO, US)
  • Examiners
    • Tai; Xiuyu
    Agents
    • Evan Law Group LLC
Abstract
An electrode assembly, comprising (a) a conductive electrode, having (i) a first electrode surface, (ii) a second electrode surface, opposite the first electrode surface, (iii) an electrode edge, connecting the first and second electrode surfaces, and (iv) an electrode tab, for making an electrical connection to the electrode. The electrode assembly further comprises (b) a dielectric, enclosing the first and second electrode surfaces and the electrode edge, and (c) a first working surface, on the first electrode surface, wherein the dielectric is present between the first working surface and the first electrode surface. The dielectric is conformal with the first electrode surface, the second electrode surface and the electrode edge.
Description
BACKGROUND

Plasmas have been used for decontamination and sterilization. Plasma, a fourth state of matter distinguished from gas, liquid and solid, may be produced through electrical discharge, for example electrical discharge through a gas. Although all plasmas contain electrons, ions and neutral species, they will have different properties depending on the composition of the gas used to prepare the plasma, as well as the electrical and structural configuration of the device used to produce the plasma.


One type of plasma is high-voltage cold plasma (HVCP), which may be prepared using dielectric barrier discharge (DBD) systems. HVCP may be prepared using non-equilibrium breakdown of a gas, using voltages preferably of 30 kV to 500 kV, typically at a frequency of 50 or 60 Hz with a DBD system. HVCP has not been studied as well as other types of plasmas, such as thermal plasma or RF plasmas. Consequently, there is presently no theory which explains the properties of these plasmas, nor the various excited and reactive species produced in such plasma. Over the last decade experimental examination of HVCP has been carried out to study this plasma.


Direct exposure of materials to HVCP has been studied. Of particular relevance are the studies exposing biological products and contaminants to HVCP, where the biological products are sealed inside packages and the HVCP is produced inside the package. In such studies, packaged foods such as produce and other materials were sterilized in a short period of time. The product inside the packages comes into direct contact with the plasma. Since the packages are sealed, reactive gas produced in the plasma remains in contact with the product indefinitely, is not diluted or dispersed, and the packaged product is protected from recontamination, dramatically extending the shelf life of the products, such as fruits and vegetables. See, for example, U.S. Pat. Pub., Pub. Nos. 2013/0189156 and 2014/0044595, both to Keener et al.


U.S. Pat. No. 10,194,672 to Keener et al. describes the use of reactive gas produced by HVCP. The reactive gas is able to sterilize or pasteurize surfaces even when transported a significant distance from the DBD system where the plasma is produced. Furthermore, the reactive gas is able to break down some organic and biological materials, such as mycotoxins. Unlike HVCP produced within a package, there is no direct exposure of the product to the HVCP, the contact time of the reactive gas with the product is limited. Furthermore, because the reactive gas is transported away from the DBD system where the HVCP is produced, it is diluted by both diffusion into the surrounding gas, and mixed with the surrounding gas and/or the working gas. Since the reactive gas is transported away from the DBD system, much larger volumes of product may be exposed to the reactive gas, in batch processes or continuous processes. In addition, large scale disinfection, such as disinfection of a surgical suite, may also be carried out.


SUMMARY

In a first aspect, the present invention is an electrode assembly, comprising (a) a conductive electrode, having (i) a first electrode surface, (ii) a second electrode surface, opposite the first electrode surface, (iii) an electrode edge, connecting the first and second electrode surfaces, and (iv) an electrode tab, for making an electrical connection to the electrode. The electrode assembly further comprises (b) a dielectric, enclosing the first and second electrode surfaces and the electrode edge, and (c) a first working surface, on the first electrode surface, wherein the dielectric is present between the first working surface and the first electrode surface. The dielectric is conformal with the first electrode surface, the second electrode surface and the electrode edge.


Definitions

All current described herein is alternating current, specified as volts (V) and kilovolts (kV) root mean squared (RMS).


A cold plasma refers to plasma which has a temperature of at most 40° C. above the temperature of the gas used to prepare the plasma (that is, the working gas), more preferably a temperature of at most 20° C. above the temperature of the gas used to prepare the plasma.


High-voltage cold plasma (HVCP) means a cold plasma prepared using a dielectric barrier discharge (DBD) system, using voltages of at most 500 kV, with a frequency at most to 1000 Hz, prepared from a gas having a pressure of 10 to 50000 Torr, such as 760 Torr (atmospheric pressure). HVCP is not a thermal plasma, is not a microwave plasma and is not a radio frequency (RF) plasma. HVCP plasmas are prepared under non-equilibrium breakdown conditions.


Reactive gas means the gas produced by an HVCP, including excited and chemically reactive species, but not those species which dissipate in 0.2 seconds or less. The composition of a reactive gas will change over time as excited species dissipate and chemical reactions within the reactive gas take place. Reactive gas is the gas that may be moved away from the DBD system that is producing an HVCP. A reactive species or excited species is considered to be present in a reactive gas if it can be detected using spectroscopy.


Dielectric barrier discharge (DBD), or a DBD system, means a system having at least two electrodes separated by a dielectric barrier, and may have more electrodes, where a dielectric barrier is present between each electrode, to prevent charge generated in the gas by a discharge from reaching an electrode.


An “electrode” is a conductive material connected to a power source or ground.


“Conformal” means that the conformal material is entirely in contact with the surface of the material or object on which it is present, following its surface including curves, depressions and bumps.


The term “hot” is used to identify an electrode connected to high voltage, while “ground” is used to identify an electrode connected to ground. These terms are also used to identify electrodes which will be connected to high voltage and ground, respectively, when in use to produce an HVCP.


“Radius of curvature parallel to the electrode surface” mean that all the radii of the curvature are parallel to the electrode surface. This is the curvature that is observer at the corners of an electrode surface when looking down onto the surface (such as in FIG. 1).


“Radius of curvature perpendicular to the electrode surface” means that not all the radii of the curvature are parallel to an electrode surface. This is the curvature that is observer when viewing the electrode edge (such as in FIG. 2).





BRIEF DESCRIPTION OF THE DRAWINGS

The following figures are provided to help illustrate the products, devices and methods of the application, but other variations and configurations are possible. The figures are not drawn to scale, with the size of some parts increased or decreased for clarity.



FIG. 1 is an illustration of an electrode viewed from above.



FIG. 2 is an illustration of a cross section of an electrode, viewed through cross section E-E.



FIG. 3 is an illustration of an electrode assembly viewed from above.



FIG. 4 is an illustration of a cross section of an electrode assembly, viewed through cross section A-A.



FIG. 5 is an illustration of an electrode holder assembly.



FIG. 6 is an illustration of a cut-away view of an electrode holder assembly.



FIG. 7 is an illustration of a reactive gas generator assembly, with a cut-away view of the reactive gas generator to show internal structures.



FIG. 8 is an illustration of a side view of a reactive gas generator assembly.



FIG. 9 is an illustration of a partial view of a reactive gas generator assembly showing an optional blower and blower exhaust.



FIG. 10 is a schematic of a reactive gas generator assembly and a regulator.



FIG. 11 is a schematic of a product treatment assembly.



FIG. 12 is an illustration of two configurations for treating a room or other enclosed space with reactive gas.





DETAILED DESCRIPTION

Cost effective commercial treatment of products, surfaces or spaces with reactive gas requires a DBD system with a reasonable service life and efficient generation of reactive gas. Experimental testing of DBD systems identified the electrode assembly as the shortest service life component of the DBD system. Extensive testing of alternative designs, materials and construction of the electrode assembly, through more than 11 iterations, has identified important elements not only for extending the service life of the electrode assembly, but also for the efficient generation of reactive gas from DBD systems which incorporate the electrode assembly. Furthermore, extensive testing of alternative designs, materials and construction of the reactive gas generator and regulator has identified important elements for efficient reactive gas generation. The present invention makes use of these testing results to provide an innovative electrode and electrode assembly. Furthermore, the present invention also includes an innovative electrode holder assembly, reactive gas generator, reactive gas generator assembly, as well as a regulator. In addition, the present invention also includes an innovative product treatment assembly.



FIG. 1 is an illustration of an electrode, 100, viewed from above. The electrode has an electrode edge, 102, connecting a first electrode surface, 104, and a second electrode surface, 114 (not shown; shown in FIG. 2). The electrode also has an electrode tab, 106, which includes an electrode tab hole, 108. The curvature of the electrode edge includes the curvature of the parallel edge, 110, and the perpendicular edge, 112. In the figure ET represents the electrode thickness, EL represents the electrode length, and EW represents the electrode width. Furthermore, TL represents the tab length and TW represents the tab width.



FIG. 2 is an illustration of a cross section of an electrode, 100, viewed through cross section E-E. Shown are both the first electrode surface, 104, and a second electrode surface, 114, and the perpendicular edge, 112. In the figure ET represents the electrode thickness.


The electrode is formed of a metal plate with edges rounded into a semi-circle (that is, a bull-nose shape) and rounded corners. The rounding of the edges and corners is important for the longevity of the electrode assembly as it reduces the electrical field stresses to which the dielectric material is exposed. Early electrode assembly designs that had the electrode edge parallel to the electrode surfaces (that is, corners) having a curvature of only ⅜-inch radius of curvature, and made from thin 0.04-inch-thick copper had a high incidence of dielectric failure at the corners and edges, when the applied voltage exceeded 10 kV. Preferably, the radius of curvature of the electrode edge parallel to the first and second electrode surfaces is at least 2.5 cm (or at least 1 inch), including 2.5 cm to 1000 cm (or 1 inch to 400 inches), including 3, 4, 5, 10, 15, 20, 50, 100 and 500 cm (or 1.5, 2, 2.5.3, 10, 20, 50, 100, 200 and 300 inches). Preferably, the radius of curvature of the electrode edge perpendicular to the first and second electrode surfaces is at least 0.6 cm (or at least 0.25 inches), including 0.6 cm to 15 cm (or 0.25 inches to 6 inches), including 0.7, 0.8, 0.9, 1, 2, 3, 5 and 10 cm (or 0.3, 0.4, 0.5, 0.6, 0.8, 1, 2, 3 and 4 inches), although for applied voltages up to 60 kV, a radius of curvature of the electrode edge perpendicular to the first and second electrode surfaces as small as 0.1 cm (0.04 inches) may be suitable.


The electrode is made of a conductive material, such as copper or aluminum. For larger electrodes, aluminum is preferred to avoid excessive weight. Also possible would be a non-conductive core with the desired size and shape of the electrode entirely coated or plated with a conductor, such as silver or gold, to form the electrode. Furthermore, it may be desirable to avoid a perfectly flat smooth electrode surface to improve adhesion to the dielectric enclosing the first and second electrode surfaces and the electrode edge. The surface area of the electrode surfaces is chosen depending on the amount of reactive gas to be produced and the power of the reactive gas generator. Preferably, the electrode may have an electrode length EL of 30 cm to 300 cm (12 inches to 120 inches), including 35, 40, 45, 50, 65, 80, 100 and 200 cm (15, 20, 25, 30, 35, 50, 80 and 100 inches). Preferably, the electrode may have an electrode width EW of 15 cm to 150 cm (6 inches to 60 inches), including 20, 25, 30, 35, 50, 75, 100 and 125 cm (7, 8, 9, 10, 15, 20, 25, 30, 40 and 50 inches). Preferably, the electrode has an electrode thickness ET the same or similar to the radius of curvature of the electrode edge perpendicular to the first and second electrode surfaces.



FIG. 3 is an illustration of an electrode assembly, 120, viewed from above. The electrode assembly includes a conformal dielectric, 122, which encloses the first and second electrode surfaces and the electrode edge. On the first electrode surface is a first working surface, 124, with the conformal dielectric therebetween. Similarly, on the second electrode surface is a second working surface, 125 (not shown; shown in FIG. 4), with the conformal dielectric therebetween. Also illustrated is the lead assembly, 126, which includes a lead, 128 (not shown; shown in FIG. 4), in electrical contact with the electrode. In the figure AL represent the electrode assembly length and AW represents the electrode assembly width.



FIG. 4 is an illustration of a cross section of an electrode assembly, 120, viewed through cross section A-A. Shown are the electrode, 100, the conformal dielectric, 122, the first working surface, 124, and the second working surface, 125. Also shown are the lead assembly, 126, including the lead, 128. In the figure AT represents the electrode assembly thickness.


It is important that the dielectric is conformal to the electrode, as defects such a gas bubbles at the dielectric-electrode interface will significantly reduce the service life of the electrode assembly. This was determined by testing designs that contained incidental defects or bubbles, which were the location of failure of the dielectric material. One way to accomplish this is by sealing the electrode into a polymerizable liquid dielectric material, such as an epoxy, by vacuum casting of the liquid into a mold, with the electrode suspending in the center of the mold. Similarly, a polymer could be injection molded around the electrode to form the electrode assembly. Alternatively, a thin dielectric (such as 8690 STATICIDE® acrylic conformal coating) may be coated onto the electrode surface to form a conformal coating, and then the remaining thickness of dielectric, such as an epoxy glass composite (for example, an EPOXYGLAS G10 or FR4, such as that available from ACCULAM) is formed as a frame, with the conformally coated electrode sealed into the frame, using for example an epoxy resin (such as RESINLABO EP750 CLEAR food grade two part unfilled epoxy structural adhesive). Dimensional stability and heat resistance of the dielectric is important, as well as the strength of adhesion between dielectric materials including any adhesive or glue, which was determined when earlier versions were prepared from polypropylene and silicone calk. Resistance to oxidation from the reactive gas and resistance to ultraviolet (UV) radiation produced by the HVCP is also important, especially on the working surfaces of the electrode assembly. The thickness of the dielectric should be the same on both sides of the electrode, and extend beyond the electrode forming a perimeter around the metal conductor; in FIG. 3 the perimeter has a length X along the assembly width AW, and a width Y along the assembly length AL. The thickness of the dielectric depends on the voltage used for the electrodes, and the variability of the voltage over the desired services life: Preferably, the dielectric has a thickness which provide a breakdown voltage corresponding to at least 110% of the voltage used for the electrode, more preferably a breakdown voltage corresponding to at least 130% of the voltage used for the electrode, and most a breakdown voltage corresponding to at least 150% of the voltage used for the electrode. When the voltage of the electrode is at least 60 kV, preferably X is at least 1.5 cm (or at least 0.625 inches), and Y is at least 2.8 cm (or at least 1.125 inches). When the voltage of the electrode is at least 60 kV, preferably the dielectric has a thickness of at least 0.9 cm (at least ⅜ of an inch), both above and below the electrode. The upper limit of X, Y and the thickness of the dielectric above and below the electrode, is limited by the difficulty of handling the electrode assembly due to its weight and physical dimensions. The electrode assemblies are identical regardless of whether they are used as hot electrode assemblies or ground electrode assemblies.


Preferably, the first and second working surfaces of the electrode assembly comprise glass. By studying several different electrode assembly designs, it was determined that epoxy material could not withstand the long-term effects of UV radiation and oxidation from the reactive gasses. It was also determined that the amount of reactive gas produced was affected by the selection of materials for the working surfaces. As compared to mica, glass produced about twice as much reactive gas. Particularly preferred is an alkali-aluminosilicate thin sheet glass that has been subject to ion exchange to increase toughness and resistance to damage, such as GORILLA® glass 3 with NATIVE DAMAGE RESISTANCE™ (Corning). Preferably the glass has a thickness of about 2 mm and has a beveled edge. Because the glass has a coefficient of expansion different from epoxy, it should be attached to the surface with an elastomeric adhesive, such as a platinum cured two-part silicone resin (for example, DOW CORNING® 3-4207 dielectric tough gel). Each electrode assembly is handed (that is, they have a non-superimposable mirror image), and may be identified with a relative designation of “right hand” or “left hand”.


The lead assembly and attachment of the lead to the electrode tab can have a significant effect on electrode assembly lifetime. Preferably, the lead is soldered to a metal screw (such as brass), which is screwed into the electrode tab hole. The metal parts should be cemented in place with epoxy adhesive and further protected by, for example an epoxy glass composite tube filled with epoxy adhesive, and finally covered with a polyvinylidene fluoride (PVFD) tube, all of which is further sealed with epoxy adhesive. Alternatively, the wire may be attached to the electrode using a multilam style plug and socket. The socket has a threaded end that attaches to the metal electrode. The socket is protected by a molded epoxy tube which is vacuum cast with the dielectric. The plug is soldered to the end of the wire connector that has a molded silicon shroud that is attached to the wire insulation above the plug. The shroud and plug are coated with a dielectric silicone grease and are inserted into the tube protecting the socket, and the plug is engaged in the socket. The grease provides an air tight high voltage connection that eliminated air and prevent coronal discharges to the socket and plug. This removable plug assembly allows any right or left handed electrode to be used in any slot in the electrode holder assembly.


It is desirable for an electrode assembly to have a service life of at least 20 hours, or at least 30 hours, at a voltage of 10 kV, more preferably a voltage of 30 kV, and most preferably a voltage of 60 kV. In the most desirable forms, the electrode assembly will have a service life of at least 300 hours at a voltage of 60 kV, alternatively, the electrode assembly will have a service life of at least 20 hours, or at least 30 hours, at a voltage of 76 kV.



FIG. 5 is an illustration of an electrode holder assembly, 130. The electrode holder assembly includes an electrode holder frame, 132, and an electrode holder base, 134. Electrode assemblies, 120, each fit into slots present in the electrode holder frame, with the electrode tab of each electrode and the lead assembly of each electrode assembly protruding outside of the electrode holder frame, to allow for electrical connection to a high voltage power source. The figure also illustrates a convenient way to orient and organize the electrode assemblies within the electrode holder assembly to simplify connecting a split pole high voltage power source. One side of the electrode holder assembly may be identified with the relative designation of the “positive side of fixture” and the opposite side identified with a relative designation of the “negative side of fixture”, with the designation of “P” and “N” shown in the figure for polarity of each hot electrode (the electrode are also numbered in the figure). By alternating the lead assemblies of adjacent electrodes on each side of the electrode holder assembly, both working surfaces of each electrode assembly will participate in forming a HVCP and produce reactive gas. Furthermore, all leads present on the same side of the electrode holder assembly are connected to the same polarity of high voltage power. Lastly, the electrodes at the top and bottom of the electrode holder assembly are connected to ground. The presence of the ground electrodes protects against electrical discharge outside of the electrode holder assembly from charge buildup on the non-active side of the electrode assemblies at each end. In the figure, two electrodes are not visible—“RIGHT HAND P2” and “RIGHT HAND P4”. As illustrated, the gap between an end hot electrode and the adjacent ground electrode is blocked to further inhibit electrical discharge outside of the electrode holder assembly and prevent air or the working gas from flowing between the ground electrode assemblies and the adjacent hot electrode assemblies.



FIG. 6 is an illustration of a cut-away view of an electrode holder assembly, 130. This figure is used to show the active electrode gap, 140, between adjacent pairs of electrode assemblies, 120. In the figure EG means electrode gap size. Each active electrode gap will produce an HVCP and reactive gas. The electrode gap size is the same between each pair of hot electrode assemblies. Preferably, the gap between the ground electrode assemblies and the adjacent hot electrode assembly is smaller than the electrode gap size. The specific electrode gap is selected based on the voltage at which the reactive gas generator will be operated, with an electrode gap EG of 1.25 cm to 6.25 (0.5 to 2.5 inches). including 1.5, 2, 2.5, 3, 3.5, 4, 4.5, 5 and 6 (0.75, 1, 1.25, 1.5, 1.75, 2, and 2.25 inches) being preferred. The number of electrode assemblies is selected based on the power at which the reactive gas generator will be operated, and is preferably an odd number of hot electrode assemblies, such as 3, 5, 7, 9, 11, 13, 15, 17, 19, 21 and 23. Even numbers of hot electrode assemblies are also possible. Typically, only 2 ground electrode assemblies are used, one on each end of the electrode holder assembly.


Preferably, the electrode holder includes an insulating inorganic material, such as mica, a mica composite, glass, a glass composite, or ceramic or a ceramic composite. Several experiments using epoxy glass composite as the holder material demonstrated that it was unable to provide a long service life due to the effects of UV radiation and oxidation by reactive gas.



FIG. 7 is an illustration of a reactive gas generator assembly, with a cut-away view of the reactive gas generator, 150, to show internal details. The reactive gas generator assembly includes two main parts, a reactive gas generator, 150, and a filter assembly, 160, connected by a connector duct, 158. Also present are an intake duct, 180, where the working gas enters the reactive gas generator assembly, and an exhaust duct, 170, where reactive gas exits the reactive gas generator assembly.


The reactive gas generator, 150, includes an electrode holder assembly, 130, with two internal ducts, 154 and 154, fluidly connecting the electrode holder assembly to the intake duct and the exhaust duct. The reactive gas generator also includes a first power splitter, 157, a second power splitter, 159, and a return ground assembly, 156, for providing power and grounding to the electrodes (the electrical connections to the electrode assemblies in the electrode holder assembly are not shown). A generator cabinet, 152, holds the different parts of the reactive gas generator together. Also shown in the figure are a status light, 151, for notifying users when power is being applied to the electrode assemblies or it is safe to open the generator cabinet. Lastly, a dew point sensor, 162, for measure the dew point of the working gas, and a mass airflow sensor, 164, for measuring the amount of working gas entering the reactive gas generator are also shown in the figure.



FIG. 8 is an illustration of a side view of a reactive gas generator assembly. Illustrated are a first power input, 190, for providing power to the first power splitter, a second power input, 194, for providing power to the second power splitter, and a ground return, 192, for electrically connecting the return ground assembly to ground.



FIG. 9 is an illustration of a partial view of a reactive gas generator assembly showing an optional blower, 184, and blower exhaust, 182. The optional blower may be part of the reactive gas generator assembly when it is used in a room, for sterilizing the surfaces within the room (such as an operating theater, a room contaminated with microorganisms such viruses or bacteria including a cruise ship cabin, or space contaminated with a toxin including chemical warfare agents; and including killing viruses or rendering them uninfective, for example norovirus, measles, rotovirus, ebola, influenza, African swine fever virus, avian viruses, Middle East respiratory syndrome coronavirus, SARS; and rendering prions un-infective), or to provide a mobile station for producing and transporting reactive gas.



FIG. 10 is a schematic of a reactive gas generator assembly, and regulator, 200. The regulator, 200, controls the reactive gas generator, 150. Air (or another working gas) enters the reactive gas generator assembly through an intake duct, 180, allowing sensing by the dew point sensor, 162, and mass airflow sensor, 164. The dew point sensor and the mass airflow sensor may be position either before or after the working gas passes through the filter assembly, 160 and the filter, 166 (such as a HEPA filter). Furthermore, the mass airflow sensor may also measure the temperature of the working gas, or a separate temperature sensor may be used. From the filter assembly the working gas passes through the connector duct, 158, and into the reactive gas generator, 150, where reactive gas is produced from the working gas and an HVCP. The reactive gas then passes into the exhaust duct, 170, pulled along by a blower, 184, which is controlled by the blower controller, 186. The reactive gas is then delivered to the desired location for treating a product, surface or room.


As illustrated in FIG. 10, the regulator, 200, includes a power input, 202, and input/output interface, 204, a (CPU), 208, such as a programmable logic controller (PLC), controls, 214, for allowing control of the regulator by a human user, a computer readable memory, 210, and a human user interface, 212, such as a HMI display screen, all of which are in electrical communication. Also in electrical communication is a variable transformer, 216, which allows a human user (with the assistance of the CPU and any software and/or data present on the computer readable memory) to control the voltage going to a high voltage transformer, 218, which in turn provides power to the reactive gas generator. As illustrated, the high voltage transformer is a step-up transformer which is powered by household power derived from a split phase transformer (also known as a single phase three wire transformer), but other types of high voltage transformers may be used. The voltage supplied to the reactive gas generator may vary depending on the high voltage transformer, but preferably the voltage difference between the two poles ranges from 30 kV to 120 kV (that is, each pole supplying 15 kV to 60 kV, as alternating current (AC) with a 180° phase difference). An air conditioning unit, 206, is included to remove waste heat generating within the regulator. Data collected through the input/output interface from various sensors (such as a blower status indictor, 222, an inlet valve indicator, 224, an outlet valve indicator, 226, and a gas furnace indicator, 228) may be displayed to the user and used to prevent operation of the reactive gas generator when operation would be unsafe. Such information may also be used to control the operation of the status light, 151 (shown in FIG. 7, but not in FIG. 10), which may also be in electrical communication with the regulator or the reactive gas generator. Also through a connection in the input/output interface, the optional blower may be controlled through the blower controller. Lastly, a network connection, 220, may be used to send or receive information to/form the regulator, or for remote control or programming of the regulator.


In a split phase transformer, the (input) primary winding on the transformer is single phase, the (output) secondary winding is center-tapped, and the center tap is connected to a grounded neutral. Either end to the center of the transformer has half the voltage of end-to-end. The advantage of using this type of transformer is that it reduces the wire conductor size as well as reduces the thickness of the wire insulation going to the electrode, as the wire only has to carry half the voltage. This is necessary as the electrodes are stacked in the electrode holder assembly in such a way as to require a tight bend radius on the wire connectors. For example, one electrode assembly may be supplied with +40 kV (AC), with the adjacent electrode assembly supplied with −40 kV (AC), giving a voltage difference between the electrode assemblies of 80 kV (AC).


In order to most efficiently produce reactive gas for a given power consumption, the voltage is selected based on the electrode gap size. More specifically, the larger the electrode gap size, the greater the voltage necessary to produce the HVCP (referred to as the light off voltage). Efficient reactive gas production occurs when the reactive gas generator is operated at between 25% to 30% above the light off voltage. Higher voltages do not produce more reactive gas efficiently. For example, a 2.5 cm (1 inch) electrode gap will have a light off voltage of 48 kV, and will most efficiently produce reactive gas when operated at 60 to 65 kV. In another example, a 3.75 cm (1.5 inch) electrode gap will have a light off voltage of 72 kV, and will most efficiently produce reactive gas when operated at 90 to 95 kV. Also, for otherwise identical devices, a 1.25 cm (0.5 inch) increase in the electrode gap size will result in about a doubling of the power of the reactive gas generator, when operated at between 25% to 30% of the light off voltage. Regulators providing high voltage with a power output of 1 kW, 8 kW and 30 kW are preferred.



FIG. 11 is a schematic of a product treatment assembly, 300. This product treatment assembly may be a grain dryer modified to also allow for treatment of a product with reactive gas. This figure includes process stream identifiers to aid in understanding the flow of product (such as grain, fruit, seeds, nuts, ground forms thereof, as well as any product that could be moved through a fluidized bed). A working gas, such as air, enters through a filter assembly, 160, and into a reactive gas generator, 150, electrically connected to a regulator, 200. The reactive gas generator then produces reactive gas which flows through a blower, 184, and into process stream 4, prior to entering a fluid bed, 306. Air (or another gas) enters through a fluid bed blower, 302. Since the product treatment assembly may also be used to dry product (such as grain), a fluid bed heater, 304, may also be present, but typically it is not turned on during treatment of product with reactive gas. The air then enters a fluid bed filter, 316, to remove dust or other particulates, and then enters process stream 4. In an alternative embodiment, the reactive gas may be mixed with the air in process stream 3 before the air enters the fluid bed blower.


The reactive gas enters the fluid bed, 306. Product also enters the fluid bed at the product inlet, 312, passes through the fluid bed, 306, and then exits at the product outlet, 314, where it is collected as process stream 2. The product is exposed to, and treated by, the reactive gas in the fluid bed. Reactive gas then travels to optional entrained product separator, 308, for removal of any entrained product, and then exits the assembly through the exhaust blower, 310. Although illustrated with a fluid bed type grain dryer, other types of continuous flow dryers could be used in place of the fluid bed, such as those described in “Improving Energy Efficiency in Grain Drying” ENCON2.3 Fact Sheet (December 2012) (available at blogs.extension.org/encon1/files/2012/12/FS_FlowDryers.pd). Also possible is to use a perforated belt conveyor where articles are placed on the conveyor and passed through a tunnel where spaced nozzles pass the reactive gas across the article. Optionally, the reactive gas may be fed back into the assembly as the working gas.



FIG. 12 is an illustration of two configurations for treating a room, 400, or other enclosed space with reactive gas, 410. In a first configuration, the reactive gas generator assembly including the reactive gas generator, 150, is placed within a room. The regulator, 200, electrically connected to the reactive gas generator is placed outside the room so as to avoid exposing it to the reactive gas. In the figure the regulator is place in a hallway, 404, separated from the room by a door, 406. The reactive gas is blown through a blower, 184, and into the room so that it may treat or sterilize room surfaces, 408. In an alternative configuration for treating a room, the reactive gas generator assembly including the reactive gas generator, is present in the air handling duct system, 402, which is used to provide heat and/or air conditioning to the room. In this way, no blower is needed as part of the reactive gas generator assembly as the blower used in the air handling duct system may be used to blow the reactive gas into the room. When used in this way, all the components of the reactive gas generator assembly should be selected for resistance to damage from the reactive gas.


Examples

Several different electrode assemblies were tested. Each subsequent electrode assembly was designed to prevent the failure mechanism which had ended the use of the prior electrode assembly design. As the failure mechanisms which appeared most quickly were eliminated, and electrode assembly service life increased, higher voltages and longer service times revealed new failure mechanisms, which were each addressed in turn. Several different electrode assemblies are described in Tables 1-3, below. Not all electrode assemblies tested are included in the tables. Version 11 has been constructed, but testing has not been completed.









TABLE 1







Electrode Development (versions 1-4)









Electrode Assembly Version












1
2
3
4





Voltage Range kV
15 to 50
15 to 50
15 to 50
15 to 50


Electrode Gap
¼″ to 1″
¼″ to 1″
¼″ to 1″
¼″


Size






Radius on
⅜″
⅜″
⅜″
⅜″


Electrode






Corners






Dielectric Material
⅛″
⅛″
3/32″
⅛″


Thickness

Edge Chamfered
1.1 mm display





at 45°.
glass placed on






both top and






bottom surface.



Dielectric Material
⅜″
⅜″
⅜″
⅜″


Edge distance to






Electrode






Electrode
0.04″
0.04
0.04
0.04


Thickness






Radius on
No
Yes
Yes
Yes


Electrode edge






Construction
Metal electrode
Metal electrode
Metal electrode
Metal Electrode


Method
sandwiched
sandwiched
sandwiched
sandwiched



between dielectric
between dielectric
between the
between dielectric



material and
material and
dielectric material
material. Hot weld



sealed with silicone
sealed with silicone
and sealed
bead of



caulk along the
calk along the
together with
polypropylene



perimeter of
perimeter. New
silicone caulk.
around the



electrode.
plug wire soldered
Glass applied on
perimeter.




and sealed to
dielectric and glued





electrode.
together with






silicone caulk.



Failure Mode
Failure along the
Failure on the
Failure on the
Dielectric not



bond line between
corner along the
electrode assembly
dimensionally



the caulk and the
bond line. Noticed
corner along the
stable, causing a



polypropylene on
Polypropylene
bond line. Glass
weak weld.



electrode assembly
surface of the
subject to fracture




corners. Failure at
electrode assembly
with mechanical




the wire connection
becoming dull.
handling.




to the electrode.





Mean Run Time to
3 to 5 hours at less
1 to 2 hours at less
1 to 2 hours at less
0 hours.


Failure
than 60 kV.
than 60 kV.
than 60 kV.
















TABLE 2







Electrode Development (versions 5-8)









Electrode Assembly Version












5
6
7
8





Voltage Range kV
25 to 80
25 to 80
 40 to 100
 40 to 100


Electrode Gap
½″ to 1.5″
½″ to 1.5″
1″ to 2″
1″ to 2″


Size






Radius on
⅜″
1″
1″
1″


Electrode






Corners






Dielectric Material
¼″
11/32″
⅜″
⅜″


Thickness






Dielectric Material
1 1/16″ in flow path
1⅛″ in flow path
1⅛″
1⅛″


Edge distance to
½″ on sides
⅞″ on sides




Electrode
against electrode
against electrode





holder assembly.
holder assembly.




Electrode
0.04
0.04
0.04
0.04


Thickness






Radius on
Yes
Yes
Yes
Yes


Electrode edge






Construction
Bond line above
Bond line above
Bond line above
Two bond lines,


Method
electrode, sealed
the electrode,
electrode, sealed
both above the



with epoxy.
sealed with epoxy.
with epoxy.
electrode on each



Electrode
Moved tab to side
Increase length of
side, mica



assembly working
of electrode holder
tab. Used
composite sealed



surface covered
assembly.
conformal coating
with epoxy.



with 1.1 mm glass.
Electrode
on the electrode.
Conformal coating




assembly working
Electrode
on the electrode.




surface covered
assembly working





with 2 mm
surface covered





GORILLA ® glass.
with 2 mm






GORILLA ® glass.



Failure Mode
Failure midline to
Failure midline to
Failure midline to
Weakness at the



the electrode on
the electrode on
the electrode on
bond line. No



the corner. Failure
the side against
the side against
defined failure, but



at plug connection
the electrode
the electrode
arcing from the



to electrode.
holder assembly.
holder assembly.
edge of the



Failure through the

Infrequent failure of
electrode



glass.

wire connection to
assembly.





electrode.



Mean Run Time to
10-15 hours at less
20-30 hours up to
At 60 kV no
Operated for 3


Failure
than 60 kV.
60 kV.
failures (300+
hours at 60 kV.





hours). 20 to 30
Testing ended due





hours at 76 kV.
to arcing.
















TABLE 3







Electrode Development (versions 9-11)









Electrode Assembly Version











9
10
11





Voltage
 40 to 100
 40 to 100
 40 to 100


Range kV





Electrode
1″ to 2″
1″ to 2″
1″ to 2″


Gap Size





Radius on
1″
1″
1″


Electrode





Corners





Dielectric
⅜″
⅜″
⅜″


Material





Thickness





Dielectric
1⅛″
1⅛″
1⅛″


Material





Edge distance





to Electrode





Electrode
0.04
0.04
¼″


Thickness





Radius on
Yes
Yes
Yes


Electrode





edge





Construction
Version 7
Version 9
Version 9


Method
construction with
construction with
construction with



new design for
conformal coating
electrode coated



sealing wire to
on the electrode
with conformal



electrode featuring
and then the edge
coating on the



potting the wire
of the electrode
electrode. Edge of



with epoxy inside
assembly covered
electrode with full



dielectric tube
with mica tape that
bull-nose ¼″



sealed to the
was attached with
radius.



electrode
epoxy onto the




assembly,
electrode




Conformal coating
assembly.




on the electrode.




Failure Mode
Failure midline to
Failure midline to




the electrode
the electrode




assembly on the
assembly on the




side against the
side against the




electrode holder
electrode holder




assembly.
assembly.



Mean Run
20-30 hours at 76
20-30 hours at 76



Time to
kV.
kV.



Failure








Claims
  • 1. An electrode assembly, comprising: (a) a conductive electrode, having (i) a first electrode surface,(ii) a second electrode surface, opposite the first electrode surface,(iii) an electrode edge, connecting the first and second electrode surfaces, and(iv) an electrode tab, for making an electrical connection to the electrode,(b) a dielectric, enclosing the first and second electrode surfaces and the electrode edge,(c) a first working surface, on the first electrode surface, wherein the dielectric is present between the first working surface and the first electrode surface, AD(d) a second working surface, on the second electrode surface, wherein the dielectric is present between the second working surface and the second electrode surfacewherein the dielectric is conformal with the first electrode surface, the second electrode surface and the electrode edge, with no gas bubble defects at dielectric-electrode interfaces,the first working surface comprises glass, and the second working surface comprises glass, andthe glass has a thickness of at least 1 mm.
  • 2. The electrode assembly of claim 1, wherein the first and second electrode surfaces are planar.
  • 3. The electrode assembly of claim 2, wherein a radius of curvature of the electrode edge parallel to the first and second electrode surfaces is at least 1 inch.
  • 4. The electrode assembly of claim 3, wherein a radius of curvature of the electrode edge perpendicular to the first and second electrode surfaces is at least 0.25 inches.
  • 5. An electrode holder assembly, comprising: (1) an electrode holder base,(2) an electrode holder frame, on the electrode holder base, and(3) a plurality of electrode assemblies, in the electrode holder frame, wherein the electrode holder base and the electrode holder frame comprise an insulating inorganic material,an electrode gap size between each of the plurality of electrode assemblies is at least 0.5 inches, andeach of the plurality of electrode assemblies comprises the electrode assembly of claim 1.
  • 6. The electrode holder assembly of claim 5, wherein the electrode gap size is 0.5 inches to 2.5 Inches.
  • 7. A reactive gas generator, comprising: (I) a generator cabinet,(II) the electrode holder assembly of claim 5, in the generator cabinet,(III) an intake duct, on a first side of the cabinet, and(IV) an exhaust duct, on a second side of the cabinet, opposite the first side of the cabinet.
  • 8. The reactive gas generator of claim 7, further comprising (VI) a first power splitter, in the generator cabinet, electrically connected to a first portion of the plurality of electrode assemblies, and(VII) a second power splitter, in the generator cabinet, electrically connected to a second portion of the plurality of electrode assemblies.
  • 9. The reactive gas generator of claim 7, further comprising (IX) a blower, attached to the exhausted duct, and(X) a blower exhaust, attached to the blower.
  • 10. An electrode holder assembly, comprising: (1) an electrode holder base,(2) an electrode holder frame, on the electrode holder base, and(3) a plurality of the electrodes assemblies, in the electrode holder frame, each of the plurality of electrode assemblies comprising the electrode assembly of claim 4,wherein the electrode holder base and the electrode holder frame comprise an insulating inorganic material, andan electrode gap size between each of the plurality of electrode assemblies is at least 0.5 inches.
  • 11. A reactive gas generator, comprising: (I) a generator cabinet,(II) the electrode holder assembly of claim 10, in the generator cabinet,(III) an intake duct, on a first side of the cabinet, and(IV) an exhaust duct, on a second side of the cabinet, opposite the first side of the cabinet.
  • 12. A reactive gas generator assembly, comprising: (A) the reactive gas generator of claim 7, and(B) a regulator, electrically connected to the reactive gas generator,wherein the regulator comprises a high voltage transformer, for providing high voltage to the reactive gas generator.
  • 13. A product treatment assembly, comprising: a fluid bed, andthe reactive gas generator assembly of claim 7, connected to supply reactive gas generated by the reactive gas generator to air entering the fluid bed.
  • 14. A method of removing mycotoxins from a product or sterilizing a product, comprising generating reactive gas with the product treatment assembly of claim 3; andcontacting the product with the reactive gas.
  • 15. A method of killing viruses on surfaces in a room, comprising: generating reactive gas with the reactive gas generator of claim 9, andcontacting surfaces in the room with the reactive gas.
  • 16. The method of claim 15, wherein the room is a cruise ship cabin.
  • 17. The method of claim 16, wherein the viruses comprise norovirus.
  • 18. An electrode assembly, comprising: (a) a conductive electrode, having (i) a first electrode surface,(ii) a second electrode surface, opposite the first electrode surface,(iii) an electrode edge, connecting the first and second electrode surfaces, and(iv) an electrode tab, for making an electrical connection to the electrode,(b) a dielectric, enclosing the first and second electrode surfaces and the electrode edge,(c) a first working surface, on the first electrode surface, wherein the dielectric is present between the first working surface and the first electrode surface, and(d) a second working surface, on the second electrode surface, wherein the dielectric is present between the second working surface and the second electrode surface,wherein the electrode assembly has a service life of at least 300 hours at 60 kV,the dielectric is conformal with the first electrode surface, the second electrode surface and the electrode edge, with no gas bubble defects at dielectric-electrode interfaces,a radius of curvature of the electrode edge parallel to the first and second electrode surfaces is at least 1 inch,a radius of curvature of the electrode edge perpendicular to the first and second electrode surfaces is at least 0.25 inches,the first working surface comprises glass, and the second working surface comprises glass, andthe glass has a thickness of at least 1 mm.
US Referenced Citations (128)
Number Name Date Kind
3891561 Lowther Jun 1975 A
4524080 Sugisawa et al. Jun 1985 A
4643876 Jacobs et al. Feb 1987 A
5184046 Campbell Feb 1993 A
5482684 Martens et al. Jan 1996 A
5656238 Spencer et al. Aug 1997 A
5895587 Sorensen Apr 1999 A
6007770 Peiper et al. Dec 1999 A
6093432 Mittal et al. Jul 2000 A
6096564 Denes et al. Aug 2000 A
6171450 Behnisch et al. Jan 2001 B1
6403029 Schmidt Jun 2002 B1
6406759 Roth Jun 2002 B1
6543460 Denes et al. Apr 2003 B1
6638475 Lagunas-Solar et al. Oct 2003 B1
6667007 Schmidt Dec 2003 B1
6991768 Keras et al. Jan 2006 B2
7101518 Ko Sep 2006 B1
8097217 Song Jan 2012 B2
8343422 Sato et al. Jan 2013 B2
8372460 Meyers et al. Feb 2013 B2
8475712 Henriksson Jul 2013 B2
8475723 Keras Jul 2013 B2
8545764 Gesche Oct 2013 B2
8551546 Rasanayagam et al. Oct 2013 B2
8557187 Ehlbeck et al. Oct 2013 B2
8641977 Snowball Feb 2014 B2
8771595 Paskalov Jul 2014 B2
8834803 Sunderland Sep 2014 B2
8865085 Nam et al. Oct 2014 B2
8871145 Paskalov Oct 2014 B2
8920740 Yang et al. Dec 2014 B2
8961894 Keener et al. Feb 2015 B2
8980190 Diver et al. Mar 2015 B2
9067788 Spielman et al. Jun 2015 B1
9114373 Misawa et al. Aug 2015 B2
9220162 Takenoshita et al. Dec 2015 B2
9295280 Jacofsky et al. Mar 2016 B2
9363880 Keener et al. Jun 2016 B2
9408930 Keener et al. Aug 2016 B2
9539352 Keener et al. Jan 2017 B2
9597422 Snowball Mar 2017 B2
10194672 Keener et al. Feb 2019 B2
20020129902 Babayan et al. Sep 2002 A1
20020153241 Niv et al. Oct 2002 A1
20020175068 Hammerstrom et al. Nov 2002 A1
20020182101 Koulik et al. Dec 2002 A1
20030026877 Ruan et al. Feb 2003 A1
20030030374 Pai Feb 2003 A1
20030039726 Yuan Feb 2003 A1
20030164285 Korenev Sep 2003 A1
20030168009 Denes Sep 2003 A1
20040001773 Schmidt Jan 2004 A1
20040037736 Perruchot et al. Feb 2004 A1
20040047762 Masaoka et al. Mar 2004 A1
20040050682 Paskalov et al. Mar 2004 A1
20040076543 Sokolowski et al. Apr 2004 A1
20040131496 Goetzelmann et al. Jul 2004 A1
20040141278 Grosse et al. Jul 2004 A1
20040208804 Hall et al. Oct 2004 A1
20040216845 Golkowski Nov 2004 A1
20040250688 Farkas et al. Dec 2004 A1
20050019209 Burger et al. Jan 2005 A1
20050056596 Paskalov et al. Mar 2005 A1
20050109739 Destrez et al. May 2005 A1
20050127843 Koulik et al. Jun 2005 A1
20050196315 Babko-Malyi et al. Sep 2005 A1
20050274122 Chang et al. Dec 2005 A1
20060027539 Golkowski Feb 2006 A1
20060060464 Chang Mar 2006 A1
20060137212 Nomine Jun 2006 A1
20060251550 Keras Nov 2006 A1
20070020159 Tsui Jan 2007 A1
20070104610 Houston et al. May 2007 A1
20070261555 Aubert Nov 2007 A1
20070270833 Bonutti et al. Nov 2007 A1
20080006536 Cuomo et al. Jan 2008 A1
20080063559 Alexander et al. Mar 2008 A1
20080099406 Ruan et al. May 2008 A1
20080173621 Kuo Jul 2008 A1
20080193330 Hotta et al. Aug 2008 A1
20080258648 Bleukx et al. Oct 2008 A1
20080260578 Engemann et al. Oct 2008 A1
20080292497 Vangeneugden et al. Nov 2008 A1
20080314243 Chan et al. Dec 2008 A1
20090121637 Laroussi May 2009 A1
20090159461 McCutchen et al. Jun 2009 A1
20090274592 Bergeron Nov 2009 A1
20090288559 Kuo Nov 2009 A1
20090297409 Buchanan et al. Dec 2009 A1
20090304562 Hayashi et al. Dec 2009 A1
20100006121 Baxter et al. Jan 2010 A1
20100032285 Thomas et al. Feb 2010 A1
20100119670 Mazzariello May 2010 A1
20100206232 Duclos et al. Aug 2010 A1
20100209293 Ikawa et al. Aug 2010 A1
20100304146 Krebs et al. Dec 2010 A1
20110014330 Meyers et al. Jan 2011 A1
20110115415 Hong May 2011 A1
20110116967 Roy et al. May 2011 A1
20110251604 Staack et al. Oct 2011 A1
20110268850 Rasanayagam et al. Nov 2011 A1
20120000782 Hong Jan 2012 A1
20120093687 Snowball Apr 2012 A1
20120156093 Kitano Jun 2012 A1
20120156340 Rasanayagam et al. Jun 2012 A1
20120156341 Rasanayagam et al. Jun 2012 A1
20120183437 Keener et al. Jul 2012 A1
20120213664 Diver et al. Aug 2012 A1
20130053761 Morfill et al. Feb 2013 A1
20130104742 Deo et al. May 2013 A1
20130105025 Fehr et al. May 2013 A1
20130164173 Norris Jun 2013 A1
20130189156 Keener et al. Jul 2013 A1
20130196099 Sakamoto et al. Aug 2013 A1
20130319460 Schneider et al. Dec 2013 A1
20130345620 Zemel Dec 2013 A1
20140044595 Keener et al. Feb 2014 A1
20150150297 Kim et al. Jun 2015 A1
20150273094 Keener et al. Oct 2015 A1
20150327430 Dong et al. Nov 2015 A1
20150327562 Zwijack Nov 2015 A1
20150342397 Deo et al. Dec 2015 A1
20150373923 Ferrell et al. Dec 2015 A1
20160262410 Hoefnagels Sep 2016 A1
20170000167 Corrigan Jan 2017 A1
20170112157 Keener et al. Apr 2017 A1
20170133205 Ehlbeck et al. May 2017 A1
Foreign Referenced Citations (46)
Number Date Country
2 685 738 May 2010 CA
10 2014 107805 Jan 2015 DE
1 884 248 Feb 2008 EP
2 374 753 Oct 2011 EP
3 383 144 Mar 2018 EP
2102084 Jan 1998 RU
2199349 Feb 2003 RU
2254143 Jun 2005 RU
199718343 May 1997 WO
1997022369 Jun 1997 WO
199851608 Nov 1998 WO
199851609 Nov 1998 WO
2002022447 Apr 2000 WO
2000054819 Sep 2000 WO
2002078749 Oct 2002 WO
2006004399 Jan 2006 WO
2007067924 Jun 2007 WO
2007124910 Nov 2007 WO
2007124945 Nov 2007 WO
2008072170 Jun 2008 WO
2008096292 Aug 2008 WO
2008126068 Oct 2008 WO
2008127135 Oct 2008 WO
2008144499 Nov 2008 WO
2009040130 Apr 2009 WO
2009041861 Apr 2009 WO
2009098662 Aug 2009 WO
2011116984 Sep 2011 WO
2011123512 Oct 2011 WO
2012038669 Mar 2012 WO
2012079858 Jun 2012 WO
2012097987 Jul 2012 WO
2012112042 Aug 2012 WO
2012113568 Aug 2012 WO
2012125435 Sep 2012 WO
2012130197 Oct 2012 WO
2013076102 May 2013 WO
2013076458 May 2013 WO
2014135254 Sep 2014 WO
2014152169 Sep 2014 WO
2015091221 Jun 2015 WO
2016007000 Jan 2016 WO
2016140447 Sep 2016 WO
2017019621 Feb 2017 WO
2017070240 Apr 2017 WO
2018045378 Mar 2018 WO
Non-Patent Literature Citations (112)
Entry
R1, 11, Jul. 11, 2017, U.S. Appl. No. 14/921,910, US.
R2, 3, Aug. 30, 2017, U.S. Appl. No. 14/921,910, US.
R3, 22, Oct. 18, 2017, U.S. Appl. No. 14/921,920, US.
R4, 4, Jan. 4, 2018, 16788620.9, EP.
R5, 40, Sep. 25, 2018, 16788620.9, EP.
R6, 15, Sep. 28, 2018, U.S. Appl. No. 14/921,910, US.
R7, 23, Feb. 1, 2019, 201610939647.X, CN.
R8, 2, Feb. 21, 2019, 16788620.9, EP.
R9, 5, Apr. 12, 2019, MX/a/2018/004893, MX.
R10, 1, Jun. 17, 2019, 3,039,902, CA.
R11, 8, Jul. 5, 2019, 201827013136, IN.
R12, 13, Jul. 25, 2019, 2018-520174, JP.
R13, 9, Aug. 26, 2019, 201610939647.X, CN.
R14, 21, Sep. 17, 2019, U.S. Appl. No. 16/215,187, US.
R15, 4, Sep. 19, 2019, 10-2018-7012556, KR.
R16, 3, Sep. 19, 2019, 19155626.5, EP.
R17, 40, Apr. 9, 2018, 16788620.9, EP.
R18, 40, Sep. 25, 2018, 16788620.9, EP.
R19, 4, Dec. 10, 2019, 10-2018-7012556, KR.
R20, 12, Dec. 6, 2019, 2018118775, RU.
R21, 4, Jan. 7, 2020, 2018-520174, JP.
R22, 11, Jan. 22, 2020, U.S. Appl. No. 16/215,187, US.
R23, 5, Jan. 21, 2020, 201610939647.X, CN.
R24, 10, Feb. 13, 2020, 19189770.1, EP.
R25, 8, Feb. 25, 2020, 19155626.5, EP.
R27, 16, Apr. 1, 2020, 2018118775, RU.
R28, 1, May 17, 2019, 2018/03358, ZA.
R29, 1, Sep. 11, 2019 MX/a/2018/004893, MX.
R30, 2, Feb. 17, 2020, 10-2018-7012556, KR.
International Search Report dated Jan. 25, 2017 for PCT application No. PCT/US2016/057753, 12 pages.
Connolly, J. et al., “Characterization and antimicrobial efficacy against E. coli of a helium/air plasma at atmospheric pressure created in a plastic package”, Journal of Physics D: Applied Physics, vol. 46, No. 3, pp. 1-12, (2013).
Misra, N.N. et al., “In-package atmospheric pressure cold plasma treatment of cherry tomatoes”, Journal of Bioscience and Bioengineering, vol. 118, No. 2, pp. 177-182, (2014).
Chiper, A.S. et al., “Atmospheric pressure plasma produced inside a closed package by a dielectric barrier discharge in Ar/CO2 for bacterial inactivation of biological samples”, Plasma Sources Science and Technology, vol. 20, No. 2, pp. 1-10, (2011).
Kolb, J.F. et al., “Cold atmospheric pressure air plasma jet for medical applications”, Applied Physics Letters, vol. 92, pp. 241501-1-241501-3, (2008).
Winter, J. et al., “Aspects of UV-absorption spectroscopy on ozone in effluents of plasma jets operated in air”, Journal of Physics D: Applied Physics, vol. 45, pp. 1-7, (2012).
Katsonis, K. et al., “Global modeling of N2O discharges: Rate coefficients and comparison with ICP and glow discharges results”, International Journal of Aerospace Engineering, vol. 2013, pp. 1-25, (2013).
“Aflatoxin”, Wikipedia, pp. 1-5, found at https://en.wikipedia.org/wiki/Aflatoxin, printed on Jul. 10, 2015.
Lunov, O. et al., “Cell death induced by ozone and various non-thermal plasmas: therapeutic perspectives and limitations”, Scientific Reports, vol. 4, pp. 1-11, (2014).
“Volt”, Wikipedia, pp. 1-4, found at https://en.wikipedia.org/wiki/Volt, Printed on Jul. 10, 2015.
Moiseev, T. et al., “Post-discharge gas composition of a large-gap DBD in humid air by UV-Vis absorption spectroscopy”, Plasma Sources Science and Technology, vol. 23, pp. 1-13, (2014).
“Endospore”, Wikipedia, pp. 1-6, found at https://en.wikipedia.org/wiki/Endospore, Printed on Sep. 10, 2017.
Trombete, Fm. et al., “Efficacy of ozone treatment on mycotoxins and fungal reduction in artificially contaminated soft wheat grains”, Journal of Food Processing and Preservation, vol. 41, No. 3, (2017). Abstract Only.
McKenzie, K.S. et al., “Oxidative degradation and detoxification of mycotoxins using a novel source of ozone”, Food and Chemical Toxicology, vol. 35, No. 8, pp. 807-820, (1997). Abstract Only.
Wang L. et al., “Effect of ozone treatment on deoxynivalenol and wheat quality”, PLoS One, vol. 11, No. 1, pp. 1-13, (2016).
McDonougha, M.X. et al., “Ozone application in a modified screw conveyor to treat grain for insect pests, fungal contaminants, and mycotoxins”, Journal of Stored Products Research, vol. 47, No. 3, pp. 249-254, (2011).
Tiwari, B.K. et al., “Application of ozone in grain processing”, Journal of Cereal Science, vol. 51, issue 3, pp. 248-255, (2010). Abstract Only.
Guzel-Seydima, Z.B. et al., “Use of ozone in the food industry”, LWT-Food Science and Technology, vol. 37, No. 4, pp. 453-460, (2004).
“Listeria monocytogenes”, Wikipedia, pp. 1-7, found at https://en.wikipedia.org/wiki/Listeria_monocytogenes, printed on Jul. 10, 2015.
“Bacillus atrophaeus”, Wikipedia, pp. 1-2, found at https://en.wikipedia.org/wiki/Bacillus_atrophaeus, printed on Jul. 10, 2015.
“Salmonella enterica”, Wikipedia, pp. 1-3, found at https://en.wikipedia.org/wiki/Salmonella_enterica, printed on Jul. 10, 2015.
“Clostridium botulinum”, Wikipedia, pp. 1-6, found at https://en.wikipedia.org/wiki/Clostridium_botulinum, printed on Jul. 10, 2015.
“Sterilization (microbiology)”, Wikipedia, pp. 1-10, found at https://en.wikipedia.org/wiki/Sterilization_(microbiology), printed on Jul. 10, 2015.
Food and Drug Administration, “Guidance for industry for the submission documentation for sterilization process validation in applications for human and veterinary drug products”, Office of Training and Communication Division of Drug Information, CDER, FDA, pp. 1-18, (1994).
Chaven, S. et al., “Food safety systems for low-acid aseptic beverages”, Food Safety Magazine, pp. 1-6, found at www.foodsafetymagazine.com/magazine-archive1/junejuly-2012/food-safety-systems-for-low-acid-aseptic-beverages/, (2012).
US Food and Drug Administration, “Guidance for Industry: Juice HACCP hazards and controls guidance first edition: Final guidance”, pp. 1-67, (2004).
Lopez, J.L., “Dielectric barrier discharge, ozone generation, and their applications”, Complex Plasmas Summer Institute, pp. 1-93, (2008).
Pankaj, S.K. et al., “Degradation kinetics of organic dyes in water by high voltage atmospheric air and modified air cold plasma”, Water Science & Technology, pp. 1-8, (2017).
Pankaj, S.K. et al., “Effect of high voltage atmospheric cold plasma on white grape juice quality”, Journal of the Science of Food and Agriculture, vol. 97, pp. 4016-4021, (2017).
Yepez, X.V. et al., “High-voltage atmospheric cold plasma (HVACP) hydrogenation of soybean oil without trans-fatty acids”, Innovative Food Science and Emerging Technologies, vol. 38, pp. 169-174, (2016).
Wan, Z. et al., “High voltage atmospheric cold plasma treatment of refrigerated chicken eggs for control of Salmonella enteritidis contamination on egg shell”, LWT—Food Science and Technology, vol. 76, pp. 124-130, (2017).
Xu, L. et al., “Microbial inactivation and quality changes in orange juice treated by high voltage atmospheric cold plasma”, Food Bioprocess Technology, vol. 10, pp. 1778-1791, (2017).
McClurkin-Moore, J.D. et al., “The effect of high-voltage atmospheric cold plasma treatment on the shelf-life of distillers wet grains”, Food Bioprocess Technology, vol. 10, pp. 1431-1440, (2017).
Pankaj, S.K. et al., “Cold plasma: background, applications and current trends”, Current Opinion in Food Science, vol. 16, pp. 49-52, (2017).
Shi, H. et al., “Reduction of aflatoxin in corn by high viltage atmospheric cold plasma”, Food Bioprocess Technology, vol. 10, pp. 1042-1052, (2017).
Misra, N.N. et al., “The effects of nonthermal plasma on chemical quality of strawberries”, Postharvest Biology and Technology, vol. 110, pp. 197-202, (2015).
Hojnik, N. et al., “Mycotoxin decontamination of food: Cold atmospheric pressure plasma versus “classic”decontamination”, Toxins, vol. 9, No. 151, pp. 1-19, (2017).
Siciliano, I. et al., “Use of cold atmospheric plasma to detoxify hazelnuts from aflatoxins”, Toxins, vol. 8, No. 125, pp. 1-10, (2016).
Ma, H. et al., “Non-thermal pasteurization of liquid foods using non-thermal plasma”, Transactions of the CSAE, vol. 18, No. 5, pp. 155-159, (2002).
Li, Y. et al., “Degradation of aflatoxin B1 in agricultural products by low temperature radio frequency plasma”, Science and Technology of Cereals, Oils and Foods, vol. 22.5, pp. 1-11, (2014).
Chen, Y., “High voltage atmospheric cold plasma treatment of refrigerated chicken eggs for control of Salmonella enteritidis on external surfaces”, Purdue University, Theses and Dissertations, pp. 1-209, (2014).
Morfill, G.E. et al., “Nosocomial infections—a new approach towards preventive medicine using plasmas”, New Journal of Physics, vol. 11, 115019, pp. 1-10, (2009).
Lu, H. et al., “Bacterial inactivation by high-voltage atmospheric cold plasma: influence of process parameters and effects on cell leakage and DNA”, Journal of Applied Microbiology, vol. 116, pp. 784-794, (2013).
Lopez, M. et al., “A review on non-thermal atmospheric plasma for food preservation: Mode of action, determinants of effectiveness, and applications”, Frontiers in Microbiology, vol. 10, pp. 1-21, (2019).
Extended European Search Report dated Feb. 25, 2020 for European application No. 19155626.5, 8 pages.
“Ozone effects on pathogens”, Ozone Solutions, 5 pages, downloaded on Mar. 13, 2020, found at www.ozonesolutions.com/blog/ozone-effects-on-pathogens-bc5a25/.
“Ozone as a disinfectant to destroy pathogens, like the coronavirus”, Ozone Solutions, 2 pages, downloaded on Mar. 13, 2020, found at www.ozonesolutions.com/blog/ozone-as-a-disinfectant-to-destroy-pathogens-like-the-coronavirus/.
Foarde, K. et al., “Ozone antimicrobial efficacy”, U.S. Environmental Protection Agency, National Risk Management Research Laboratory, pp. 1-13, (2007).
Pradeep, P. et al., “Non-thermal plasmas (NTPs) for inactivation of viruses in abiotic environment”, Research Journal of Biotechnology, vol. 11, No. 6, pp. 91-96, (2016).
Wu, Y. et al., “MS2 virus inactivation by atmospheric-pressure cold plasma using different gas carriers and power levels”, Applied and Environmental Microbiology, vol. 81, No. 3, pp. 996-1002, (2015).
Yasuda, H. et al., “Biological evaluation of DNA damage in bacteriophages inactivated by atmospheric pressure cold plasma”, Plasma Processes and Polymers, vol. 7, pp. 301-308, (2010).
Alshraiedeh, N.H. et al., “Atmospheric pressure, nonthermal plasma inactivation of MS2 bacteriophage: effect of oxygen concentration on virucidal activity”, Journal of Applied Microbiology, vol. 115, pp. 1420-1426, (2013).
Bae, S.C. et al., “Inactivation of murine norovirus-1 and hepatitis A virus on fresh meats by atmospheric pressure jets”, Food Research International, vol. 76, pp. 342-347, (2015).
Cowling, B.J. et al., “Aerosol transmission is an important mode of influenza A virus spread”, Nature Communications, vol. 4, 1935, pp. 1-6, (2013).
Kuzmanovic, D.A. et al., “Bacteriophage MS2: Molecular weight and spatial distribution of the protein and RNA components by small-angle neutron scattering and virus counting”, Structure, vol. 11, pp. 1339-1348, (2003).
Wolf, C. et al., “Proxies to monitor the inactivation of viruses by ozone in surface water and wastewater effluent”, Water Research, vol. 166, (2019).
Brie, A. et al., “Inactivation of murine norovirus and hepatitis A virus on fresh raspberries by gaseous ozone treatment”, Food Microbiology, vol. 70, pp. 1-6, (2018).
Hudson, J.B. et al., “Development of a practical method for using ozone gas as a virus decontaminating agent”, Ozone: Science & Engineering, vol. 31, No. 3, pp. 216-223, (2009).
Muller, J.A. et al., “Development of a high-throughput colorimetric Zika virus Infection Assay”, Medical Microbiology and Immunology, vol. 206, issue 2, pp. 175-185, (2017).
World Health Organization, “Zika virus Situation Report—Feb. 5, 2016”, 6 pages, (2016).
Rasmussen, S.A. et al., “Zika virus and birth defects—reviewing the evidence for causality”, The New England Journal of Medicine, pp. 1-7, (2016).
Muller, J.A. et al., “Inactivation and environmental stability of Zika virus”, Emerging Infectious Diseases, vol. 22, No. 9, pp. 1685-1687, (2016).
Aubry, M. et al., “Inactivation of Zika virus in plasma with amotosalen and ultraviolet A illumination”, Transfusion, vol. 56, pp. 33-40, (2016).
Butot, S. et al., “Procedure for rapid concentration and detection of enteric viruses from berries and vegetables”, Applied and Environmental Microbiology, vol. 73, No. 1, pp. 186-192, (2007).
Woolston, J. et al., “Bacteriophage lytic for salmonella rapidly reduce salmonella contamination on glass and stainless-steel surfaces”, Bacteriophage, vol. 3, issue 3, pp. e25697-1-.e25697-6, (2013).
Carey-Smith, G.V. et al., “Isolation and characterization of bacteriophages infecting salmonella spp.”, FEMS Microbiology Letters, vol. 258, pp. 182-186, (2006).
Soffer, N. et al., “Bacteriophages safely reduce salmonella contamination in pet food and raw pet food ingredients”, Bacteriophage, vol. 6, No. 3, pp. e1220347-1-e1220347-8, (2016).
Shin, H. et al., “Receptor diversity and host interaction of bacteriophages infecting Salmonella enterica serovar typhimurium”, Plos One, vol. 7, issue 8, pp. e43392-1-e43392-11, (2012).
“Influenza type A viruses—Avian influenza (Flu)”, Centers for Disease Control and Prevention, 2 pages, found at www.cdc.gov/flu/avianflu/influenza-a-virus-subtypes.htm, (2020).
Dow Corning, Product Information, “Dow Corning® 3-4207 Dielectric Tough Gel”, 3 pages, (2017).
Cock, I. et al., “A modified MS2 bacteriophage plaque reduction assay for the rapid screening of antiviral plant extracts”, Pharmacognosy Research, vol. 2, issue 4, pp. 221-228, (2010).
Acl Inc., Product Information, “8690 Staticide Acrylic Conformal Coating”, 1 page, (2016).
Corning Gorilla Glass, Product Information, “Corning Gorilla Glass 3”, 2 pages, (2016).
ResinLab, an Ellsworth Adhesives Company, Product Information, “Technical Data Sheet EP750 Clear”, 3 pages, (2016).
ResinLab, an Ellsworth Adhesives Company, “Safety Data Sheet for EP750 Clear A”, pp. 1-13, (2015).
ResinLab, an Ellsworth Adhesives Company, “Safety Data Sheet for EP750 Clear B”, pp. 1-9, (2015).
Acculam Laminated Thermoset Plastic, Product Data Sheet, “Acculam® Epoxyglas G10, FR4”, 1 page, (2017).
Encon2.3 Fact Sheet, “Improving energy efficiency in grain drying”, 5 pages, (2012).
Biomin, “World Mycotoxin Survey, The global threat”, 5 pages, (2019).
SciFinder Search Report on “Inactivation of Viruses using Ozone”, pp. 1-14, generated on Feb. 10, 2020.
U.S. Appl. No. 16/215,187, mailed Nov. 16, 2020, 13 pages.
U.S. Appl. No. 17/017,517, filed Sep. 10, 2020.
International Search Report dated Oct. 27, 2020 for PCT application No. PCT/US2020/036833, 12 pages.
Related Publications (1)
Number Date Country
20200396819 A1 Dec 2020 US