ELECTROLYZED WATER COMPOSITION
20170267553 · 2017-09-21
Assignee
Inventors
Cpc classification
Y02E60/36
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C02F2201/4618
CHEMISTRY; METALLURGY
A23V2002/00
HUMAN NECESSITIES
C25B9/17
CHEMISTRY; METALLURGY
C02F1/46104
CHEMISTRY; METALLURGY
C02F2001/46185
CHEMISTRY; METALLURGY
International classification
C02F1/467
CHEMISTRY; METALLURGY
Abstract
The present invention provides a method for producing electrolyzed water composition for use in cleaning and disinfecting of an object. The method comprises preparing an electrolyte solution comprising water, at least one carbonate salt selected from: alkali metal carbonate salts, and at least one chloride salt selected from: alkali metal chloride salts and/or alkali earth metal chloride salts. The method further comprises introducing the aqueous electrolyte solution into an electrolytic cell comprising a plurality of boron-doped diamond electrodes. The method further comprises operating a power supply to apply a predetermined voltage to the electrolyte solution to produce an electrolyzed water composition comprising a plurality of active molecular and ionic species with antimicrobial activity.
Claims
1. A method for producing electrolyzed water composition for disinfecting an area, the method comprising: preparing an electrolyte solution comprising water, at least one carbonate salt selected from: anhydrous alkali metal carbonate salts, and at least one chloride salt selected from: alkali metal chloride salts and/or alkali earth metal chloride salts; introducing the aqueous electrolyte solution into an electrolytic cell comprising a plurality of boron-doped diamond electrodes; and operating a power supply to apply a predetermined voltage to the electrolyte solution within the electrolytic cell to produce an electrolyzed water composition comprising a plurality of active molecular and ionic species having antimicrobial properties.
2. A method as claimed in claim 1, in which the mixture of at least two salts of the electrolyte are selected such that the dissolved O.sub.3 concentration is in the range of from 0.1 to 1,000 ppm.
3-4. (canceled)
5. A method as claimed in claim 1, in which the electrolyte solution is introduced into the electrolytic cell in a continuous or batch process manner.
6. A method as claimed in claim 1, in which the predetermined voltage is in the range of between about 1 and 1000 volts DC.
7. A method as claimed in claim 1, in which the power supply has a current in the range of between about 1 and 1000 ampere.
8. An apparatus for producing electrolyzed water composition for use in disinfecting an area, the apparatus comprising: a reservoir comprising an electrolyte solution comprising water, at least one carbonate salt selected from anhydrous alkali metal carbonate salts and at least one chloride salt selected from: alkali metal chloride salts and/or alkali earth metal chloride salts; an electrolytic cell in fluid communication with the reservoir to receive a feed stream comprising the aqueous electrolyte solution; and a plurality of boron-doped diamond electrodes located within the electrolytic cell and arranged in use to be connected to a power supply.
9-10. (canceled)
11. (canceled)
12. An electrolyzed water composition as claimed in claim 11, in which the composition has antimicrobial properties and is substantially chlorine-free.
13. Use of an electrolyzed water as claimed in claim 11, as an antimicrobial agent, or an antibacterial agent, or as a cleaning agent, or as a pesticidal agent, or for reducing and/or eliminating food borne pathogens on or in a food substrate.
14. An applicator for disinfecting equipment or for treating crops, in which the applicator comprises a reservoir comprising an electrolyzed water composition as claimed in claim 11, and a nozzle or outlet in fluid communication with the reservoir.
15. An applicator as claimed in claim 14 in which the applicator is selected from one or more of: a nebuliser, a fogging mist applicator, a jet spray applicator, a spray applicator, an irrigation system or a wash system, or any combination thereof.
16. A method as claimed in claim 1, wherein the electrolyte solution comprises water, at least one anhydrous alkali metal carbonate salt and at least one chloride salt selected from alkali metal chloride salts and/or alkali earth metal chloride salts.
17. An apparatus as claimed in claim 8, wherein the electrolytic cell is an electrolytic flow cell.
18. An apparatus as claimed in claim 8, wherein the electrolyte solution comprises water, at least one anhydrous alkali metal carbonate salt and at least one chloride salt selected from alkali metal chloride salts and/or alkali earth metal chloride salts.
Description
BRIEF DESCRIPTION OF FIGURES
[0116] Embodiments of the invention will now be described, by way of example, with reference to the following figures:
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DETAILED DESCRIPTION
Example 1
Electrolyzed Water Composition
[0129] An electrolyte solution comprising 16 g anhydrous sodium carbonate (Na.sub.2CO.sub.3) and 14 g sodium chloride (NaCl) in 5 l of water was prepared. The electrolyte solution is stored within a reservoir chamber in fluid communication with an electrolytic cell.
[0130] A feed stream comprising the electrolyte solution was introduced into the electrolytic cell. The feed stream can optionally include one or more additional salts to enhance the disinfectant properties of the resultant electrolyzed water composition. The electrolytic cell is a non-membrane electrolytic cell. The electrolytic cell comprises a casing, a plurality of boron doped diamond electrodes (BDEs) located within the cell, and metal ‘contact plates’ used for transmitting charge across the electrolyte solution.
[0131] The BDEs are sheet-like components and are provided in a stack of between 3 and 10 sheets. Each sheet is located at a fixed distance away from an adjacent sheet. The distance between adjacent sheets of BDEs provides a cell gap, which is preferably less than 5 mm, for example between approximately 2 and 3 mm. The BDEs are provided in a plastic frame. The BDEs transmit charge across the electrolyte solution, inducing a strong dipole and creating positively and negatively charged radicals on alternate surfaces of the diamonds.
[0132] The electrolyte solution may be introduced into the electrolytic cell in any suitable manner so as to produce electrolyzed water composition in a continuous process or in a batch process. In the continuous process, the electrolyte solution may be introduced at a suitable flow rate, such as for example at a flow rate in the range of from 0.1 to 100 l/min, for example in the range of from 3 to 5 l/min. In the batch process, the electrolyte solution may have a flow rate of approximately 16 l/min.
[0133] A power supply was operated to apply a voltage in the range of between 1 and 1000 Volt D.C. and a current within the range of from 1-1000 ampere to the electrolyte solution. The over-potential provided between the electrodes shifts the equilibrium within the electrolyte solution such that a range of ‘active species’ ions and molecules are produced and remain within the electrolyzed water for a significant amount of time. For example, the half life of the active species within the electrolyzed water composition is preferably at least a number of minutes, more preferably at least ten minutes, especially preferably at least 30 minutes, for example about 45 minutes.
[0134] The electrolytic cell preferably comprises an outlet through which the electrolyzed water composition exits the cell. The resulting electrolyzed water composition comprises a range of active molecular and ionic species which have anti-microbial properties. The electrolyzed water composition preferably also has detergent properties. The electrolyzed water composition preferably comprises surfactant species.
[0135] The active molecular and ionic species include dissolved ozone O.sub.3 and one or more of: hydrogen peroxide H.sub.2O.sub.2, hydroxyl ions OH.sup.− and/or hydronium ions OH.sub.3.sup.+. The electrolyzed water composition according to this embodiment comprises dissolved ozone at a level of approximately 300 ppm. This level of dissolved ozone is approximately 100 times greater than the level which can be achieved by injecting gaseous ozone into water. As a result, the electrolyzed water composition of the present invention has an increased anti-microbial efficacy compared to water which has been injected with gaseous ozone. The electrolyzed water composition may be used as an antimicrobial agent, including as an antibacterial agent, antifungal agent, antiviral agent and/or antiparasitic agent, or any combination thereof.
[0136] Although the electrolyzed water composition of the present invention contains dissolved ozone at a level of approximately 300 ppm, it is to be understood that the electrolyzed water composition of the present invention may comprise any suitable level of dissolved ozone, preferably within the range of between 0.1 and 1000 ppm, for example within the range of 0.1 ppm and 750 ppm.
[0137] Conventional electrolyzed water compositions based on chloride electrolytes generate free accessible chlorine (FAC). Use of the conventional compositions therefore produces, either when prepared or when reacted, a smell which is associated with swimming pools. There is a risk that disinfected equipment within a food processing environment may produce food products which have become tainted with this chlorine associated smell. In contrast, the electrolyzed water composition of the present invention is substantially free of free accessible chlorine (FAC). In the embodiment used in the example, the composition of Example 1 comprises <0.1 ppm FAC both when produced, and when reacted. The compositions of the present invention may therefore be used to clean and disinfect processing lines and equipment without producing a smell associated with a swimming pool and with a significantly reduced risk of tainting the food product. The electrolyzed water compositions of the present invention retain potent anti-microbial properties even though the compositions have low FAC.
Example 2
[0138] With reference to Table 1, the electrolysed water composition of Example 1 was applied using an EN1276 test. EN1276 test is the European standard test method to formally evaluate the bactericidal activity of a disinfectant. To meet the requirements of EN 1276 at least a 5 Log.sub.10, reduction in test bacteria within 5 minutes is required.
[0139] The test method involved mixing 1ml of the test bacteria, in this instance E. coli, with 1 ml of interfering substance, in this case 0.3% w/v albumin (simulating dirty conditions), and then adding 8 ml of the electrolysed water composition. After the required contact time, 0.1 ml was removed and added to 8.9 ml of the neutralizer (sterile water) and 1 ml of sterile distilled water. Following a 5 minute neutralization period, 1 ml was plated onto LB Agar to detect surviving test bacteria.
[0140] As shown in Table 1, when tested in accordance with EN 1276, the electrolysed water composition achieved >8 log.sub.10 reduction at 1 and 5 minutes at room temperature under dirty conditions for E. coli. The result demonstrates that the electrolysed water composition has high bactericidal activity against E. coli and fulfils the requirement of EN1276.
[0141] The present invention provides an electrolyzed water composition providing improved anti-microbial activity, for example improved anti-bacterial activity. Although the present invention demonstrates the effectiveness of the electrolyzed water composition with respect to E. coli, it is to be understood that the compositions of the present invention are effective against other microbial strains and are not limited to E. coli. elimination.
[0142] The electrolyzed water composition of the present invention preferably achieves 100% microbial, for example bacterial, elimination within 1 minute of exposure to the composition. The electrolyzed water composition of the present invention preferably achieves 100% microbial, for example bacterial, elimination within 5 minutes, more preferably within 3 minutes, for example within 1 minute, of exposure to the composition. The electrolyzed water composition of the present invention preferably achieves at least 80%, more preferably at least 90%, especially preferably at least 95%, for example at least 99.999% (5 log order) microbial, for example bacterial, elimination within 5 minutes, more preferably within 1 minutes, of exposure to the composition by washing.
Example 3
E. coli Elimination Tests using Dry Fogging
[0143] With reference to
[0144] The electrolyzed water composition was applied using a pulsFOG Rapid Fogger, fitted with a W03 nozzle (herein referred to as a fogging mist applicator). The fogging mist applicator's output rate was approximately 4.5 L/hour, using 2 bar of pressure from a separate air compressor. The output droplet size of the electrolyzed water composition was around 10 to 15 microns.
[0145] The fogging mist applicator was located at one end of a shipping container and the four substrates were located adjacent the opposing surface of the shipping container out of direct line of the spray, giving a separation of approximately 6 m.
[0146] Although this embodiment illustrates the use of a specific fogging mist applicator it is to be understood that the electrolyzed composition may be applied by any suitable applicator or application method at any suitable output rate using any suitable pressure and producing any suitable output droplet size. The applicator or application method may be located at any suitable distance away from the substrate. For example, the electrolyzed water composition may be contained within a reservoir which is adapted to releasably engaged to equipment for disinfecting, such as for example food processing lines.
[0147]
[0148] The presence of E. coli is illustrated by white sections/markings on the substrate. The areas where the E. coli has been killed by the composition are clear and colourless (no white markings).
[0149] As shown in
[0150] A high kill rate is also achieved on the wood and glass substrates after 5 minutes of fog exposure to a low dosage of the electrolyzed water composition. It can be seen from
[0151] As shown in
[0152] The present invention provides an electrolyzed water composition having improved efficiency for santizing substrates, including but not limited to wood, steel, plastic and glass substrates.
[0153] The present invention provides an electrolyzed water composition providing improved anti-microbial activity, for example improved anti-bacterial activity. Although the present invention demonstrates the effectiveness of the electrolyzed water composition with respect to E. coli, it is to be understood that the compositions of the present invention are effective against other microbial strains and are not limited to E. coli. elimination. It is also to be understood that the electrolyzed water composition of the present invention may be applied at a higher dosage to the area/substrates and achieve 100% microbial, for example E. coli, elimination over a much shorter period of time than achieved for the low dosage application of the composition as shown in this Example. The time for achieving a high microbial kill, such as for example at least 5 log order kill, depends on the concentration of the composition during application. The electrolyzed water compositions of the present invention provide improved antimicrobial activity, for example antibacterial activity, within a significantly shorter time period after exposure to the composition than conventional food-safe disinfecting compositions.
[0154] The electrolyzed water composition of the present invention preferably achieves 100% microbial, for example bacterial, elimination within 20 minutes of exposure to the composition. The electrolyzed water composition of the present invention preferably achieves 100% microbial, for example bacterial, elimination within 15 minutes, more preferably within 10 minutes, for example within 5 minutes, of exposure to the composition. The electrolyzed water composition of the present invention preferably achieves at least 80%, more preferably at least 90%, especially preferably at least 95%, for example at least 99.999% (5 log order) microbial, for example bacterial, elimination within 10 minutes, more preferably within 5 minutes, of exposure to the composition by fogging.
Example 4
E. coli Elimination Tests using Flood Based Method
[0155] Disinfection may also be achieved by flooding the area to be disinfected with the electrolyzed water composition. With reference to
[0156] It can be seen by comparing the images of
[0157] The compositions of the present invention when applied at a concentration of 100% preferably achieve at least 5 log order kill, more preferably at least 6 log order kill, for example 7 to 8 log order microbial kill within 30 seconds of application of the composition by a flood based method. The compositions of the present invention when applied at a concentration of 100% preferably achieve at least 5 log order kill, preferably at least 6 log order kill, for example 7 to 8 log order microbial kill within 20 seconds of application of the composition by a flood based method. The compositions of the present invention when applied at a concentration of 100% preferably achieve at least 5 log order kill, preferably at least 6 log order kill, for example 7 to 8 log order microbial kill within 10 seconds of application of the composition by a flood based method.
[0158] Conventional electrolyzed water compositions based on chloride electrolytes generate free accessible chlorine (FAC). Use of the conventional compositions therefore produces, either when prepared or when reacted, a smell which is associated with swimming pools. There is a risk that disinfected equipment within a food processing environment may produce food products which have become tainted with this chlorine associated smell. In contrast, the electrolyzed water composition of the present invention is substantially free of free accessible chlorine (FAC). In the embodiment used in the example, the composition of Example 1 comprises <0.1 ppm FAC both when produced, and when reacted. The compositions of the present invention may therefore be used to clean and disinfect processing lines and equipment without producing a smell associated with a swimming pool and with a significantly reduced risk of tainting the food product.
[0159] The method of disinfecting an area using the compositions of the present invention has significantly reduced environmental issues compared to conventional methods. In contrast to a number of conventional methods, the present invention does not require a considerable water supply and does not produce a large volume of waste water. Furthermore, in accordance with one embodiment of the present invention the electrolyte composition comprises a mixture of sodium chloride, otherwise known as table salt and anhydrous sodium carbonate which is an approved food ingredient (E500) and can be found in, amongst other things, sherbet. In use, the electrolyzed water composition will revert to sodium chloride and sodium carbonate, and neither of these components provides any significant environmental concerns. The other alkali metal carbonate salts, alkali metal chloride salts and/or alkali earth metal chloride salts present within the electrolyte solutions of the present invention are also food safe.
[0160] The electrolyzed water composition of the present invention is a food-safe, non-tainting disinfecting composition which can be used to quickly clean and disinfect food processing lines and equipment, in situ, during and/or between shifts, with improved efficiency and with a significantly higher anti-microbial activity than conventional food-safe disinfecting solutions.
Example 5
Salad Washing
[0161] In conventional salad washing process, the salad is washed by exposing the salad to up to 60 m.sup.3 of chilled (6° C.) water per hour per washing line in order to remove gross debris and reduce the microbial load by 1 log order (90% kill). Approximately half of this water is then removed as waste water every hour.
[0162] This conventional process requires a large water supply, produces a significant waste water output and has high energy and cost implications associated with chilling the water supply prior to washing. There are also considerable time constraints associated with this method. It has been found that once the lengthy washing cycles have been completed that there is still a significant microbial presence on the washed salad.
[0163] The electrolyzed water composition of Example 1 is sprayed onto the leaves. As shown in
[0164] Furthermore, the methods of the present invention provide electrolyzed water compositions having improved antimicrobial activity which are effective within a significantly shorter time period than the conventional salad washing process. The electrolyzed water composition achieves this level of antimicrobial activity before the salad enters the water washing line.
[0165] The composition of the present invention therefore provides a quick and safe method for disinfecting salad which requires a reduced water supply, requires less washing, produces less waste water, has significantly less energy and cost implications and produces a cleaner food product than the conventional salad washing process.
Example 6
Meat Processing
[0166] In meat processing plants, a conventional lengthy five-step cutting line clean down procedure is required. This can take a significant amount of time, for example up to 8 hrs per night, in order to clean the equipment sufficiently. The process also involves the use of harsh chemicals and disinfectants and a significant volume of hot water (70° C.). Furthermore, it is difficult to achieve consistent disinfection using conventional methods and as a result potential sources of food cross-contamination may remain. There are therefore environmental and health issues, as well as significant time and cost implications associated with conventional meat processing plant cleaning procedures.
[0167] In contrast, the composition of Example 1 is used to disinfect the meat processing plant equipment in a much simplified, for example a 2 stage, process, with improved antimicrobial activity. Furthermore, the composition of Example 1 is used to disinfect the meat processing plant more quickly, for example within a 2 hour time period. The method of the present invention therefore provides quick, effective disinfection of the relevant environment and requires less shutdown time of the processing/preparation equipment. The composition of Example 1 can be used to disinfect the meat processing plant in an automated process using for example a spray bar. Furthermore, the method of the present invention only requires the use of ambient temperature water and therefore there is no need to heat or cool a water supply prior to disinfecting the equipment.
[0168] The present invention provides an electrolyzed water composition and a method for disinfecting equipment with improved antimicrobial activity, reduced cost and energy implications, reduced down time of the processing/preparation equipment, and/or reduced environmental implications.
[0169] Although Examples 2 to 6 illustrate the effectiveness of the electrolyzed water compositions of the present invention within food processing environments, it is to be understood that the compositions, method and apparatus of the present invention can be used to disinfect any suitable environment, and is not to be limited to food processing environments.
Example 7
Electrolyzed Water Composition
[0170] An aqueous electrolyte solution comprising 14 g sodium chloride and 16 g anhydrous sodium carbonate in 12 l of water was prepared. The electrolyte solution was stored within a reservoir chamber in fluid communication with an electrolytic cell.
[0171] A feed stream comprising the electrolyte solution was introduced into an electrolytic flow cell. The feed stream can optionally include one or more additional salts to enhance the biocidal properties of the resultant electrolyzed water composition.
[0172] The electrolytic cell is a non-membrane electrolytic cell. It is however to be understood that any suitable electrolytic cell may be used.
[0173] The electrolytic cell comprises a casing, a plurality of boron doped diamond electrodes (BDEs) located within the cell, and metal ‘contact plates’ used for transmitting charge across the electrolyte solution.
[0174] The BDEs are sheet-like components and are provided in a stack of between 3 and 10 sheets. Each sheet is located at a fixed distance away from an adjacent sheet. The distance between adjacent sheets of BDEs provides a cell gap, which is preferably less than 5 mm, for example between approximately 2 and 3 mm. The BDEs are provided in a plastic frame. The BDEs transmit charge across the electrolyte solution, inducing a strong dipole and creating positively and negatively charged radicals on alternate surfaces of the diamonds.
[0175] The electrolyte solution may be introduced into the electrolytic cell in any suitable manner so as to produce electrolyzed water composition in a continuous process or in a batch process. In the continuous process, the electrolyte solution may be introduced at a suitable flow rate, such as for example at a flow rate in the range of from 0.1 to 100 l/min, for example in the range of from 3 to 5 l/min. In the batch process, the electrolyte solution may have a flow rate of approximately 16 l/min.
[0176] A power supply was operated to apply a voltage in the range of between 1 and 1,000 Volt D.C. and a current within the range of from 1-1,000 ampere to the electrolyte solution.
[0177] The over-potential provided between the electrodes shifts the equilibrium within the electrolyte solution such that a range of ‘active species’ ions and molecules are produced and remain within the electrolyzed water for a significant amount of time. The term ‘significant amount of time’ is used herein to refer to at least 10 minutes, preferably at least 30 minutes, more preferably at least 45 minutes, for example at least 60 minutes. The combination of active molecular and ionic species together with the over-potential which supports the equilibrium confers a variable degree of pesticidal activity to the electrolyzed water composition.
[0178] The electrolytic cell preferably comprises an outlet through which the electrolyzed water composition exits the cell. The resulting electrolyzed water composition comprises a range of active molecular and ionic species which have biocidal properties.
[0179] The active molecular and ionic species include dissolved ozone. The electrolyzed water composition according to this embodiment comprises dissolved ozone at a level of approximately 50 ppm.
[0180] Although the electrolyzed water composition of the present invention contains dissolved ozone at a level of approximately 50 ppm, it is to be understood that the electrolyzed water composition of the present invention may comprise any suitable level of dissolved ozone within the range of between 0.1 and 1,000 ppm.
[0181] It is also to be understood that the electrolyzed water composition may be varied by varying one or more of: the components of the electrolyte composition, the concentration of the components within the electrolyte composition, the degree of over-potential, the current applied, or any combination thereof. In this way the biocidal properties of the electrolyzed water biocidal composition may be tailored to suit different agricultural targets, such as for example crops, pathogens, delivery mechanism, and time points, or any combination thereof. For example, the biocidal properties of the electrolyzed water biocidal composition may be tailored in relation to when the composition is to be applied, such as for example during preparation of growing beds, during sowing and/or during growing seasons.
[0182] The system may further comprise one or more flow regulators arranged in use to adjust the flow of the electrolyte feed stream between the reservoir and the cell.
[0183] The system may further comprise a heater arranged in use to adjust the temperature of the flow of the electrolyte feed stream and/or the electrolyte solution within the cell.
[0184] The system may further comprise a control system arranged in use to control the flow rate of the electrolyte feed stream as required, such as for example by controlling the flow regulator(s).
[0185] The system may comprise a control system arranged in use to control the power supply to the electrodes.
[0186] The system may comprise a control system arranged in use to control the temperature of the electrolyte solution.
[0187] Control of the temperature of the electrolyte solution, the flow rate of the electrolyte solution feed stream, and the power supply to the electrodes may be provided by a single control system. Alternatively, these factors may be controlled by separate control systems.
Example 8
Phytophthora infestans Control on Tomato Plants
[0188] Phytophthora infestans infected tomato plants were treated with five different treatments.
[0189] Treatment 1: untreated control (UT); Treatment 2: Revus (known pesticide);
[0190] Treatment 3: Mix 1 (Comparative Example of an alternate electrolysed water solution, with salts comprising NaCl at 0.30 g/l, Na.sub.2CO.sub.3 at 1.60 g/l, KH.sub.2PO.sub.4 at 0.90 g/l, KNO.sub.3 at 0.80 g/l, CaCl.sub.2•6H.sub.2O at 1.60 g/l, Mg(NO.sub.3).sub.2•6H.sub.2O at 0.80 g/l);
[0191] Treatment 4: Mix 60 (Comparative Example of an alternate electrolysed water solution, with salts comprising NaCl at 0.30 g/l, Na.sub.2CO.sub.3 at 1.20 g/l, KH.sub.2PO.sub.4 at 1.70 g/l, CaCl.sub.2•6H.sub.2O at 1.60 g/l, Mg(NO.sub.3).sub.2•6H.sub.2O at 1.20 g/l); and
[0192] Treatment 5: composition of Example 7 (Mix 38).
[0193] The treatments were applied using a foliar spray. Each treatment group consisted of four replicates of 8 plants. Each treatment was sprayed onto the diseased plants for 30 seconds. It is to be understood that the treatment is to be applied until the treatment begins to run off from the leaves.
[0194] The results of the treatment are illustrated in
[0195]
[0196]
[0197]
[0198] As shown in
[0199] As shown in
[0200] (
[0201] The electrolyzed water composition of Example 7 therefore has an improved pesticidal effect against late blight than the known pesticide Revus.
[0202]
Example 9
Treatment of Stem Bortrytis Infected tomato plants
[0203] The average lesion length of diseased plants was measured for five different samples of diseased tomato plants. Each sample was treated with a different treatment regime.
[0204] Treatment 1: untreated control (UT);
[0205] Treatment 2: known pesticidal agent Signum;
[0206] Treatment 3: Mix 1 (Comparative Example of an alternate electrolysed water solution, with salts comprising NaCl at 0.30 g/l, Na.sub.2CO.sub.3 at 1.60 g/l, KH.sub.2PO.sub.4 at 0.90 g/l, KNO.sub.3 at 0.80 g/l, CaCl.sub.2•6H.sub.2O at 1.60 g/l, Mg(NO.sub.3).sub.2•6H.sub.2O at 0.80 g/l);
[0207] Treatment 4: Mix 60 (Comparative Example of an alternate electrolysed water solution, with salts comprising NaCl at 0.30 g/l, Na.sub.2CO.sub.3 at 1.20 g/l, KH.sub.2PO.sub.4 at 1.70 g/l, CaCl.sub.2•6H.sub.2O at 1.60 g/l, Mg(NO.sub.3).sub.2•6H.sub.2O at 1.20 g/l); and
[0208] Treatment 5: composition of Example 7 (Mix 38).
[0209] The size of the lesions on each plant sample were measured after a period of 31 days and 44 days after treatment.
[0210] As shown in
Example 10
Treatment of Sclerotinia Infected Carrots
[0211] The average disease prevalence in carrot plants was measured for five different samples of plants which had been exposed to the Sclerotinia fungus through direct spore transfer. Each sample was identical in the number of carrot plants. The plants were sprayed with a single foliar spray until run off of the treatment solution from the leaves was observed.
[0212] Each sample was treated with a different treatment regime.
[0213] Treatment 1: untreated control (UT);
[0214] Treatment 2: known pesticidal agent Tebecur;
[0215] Treatment 3: Mix 1 (Comparative Example of an alternate electrolysed water solution, with salts comprising NaCl at 0.30 g/l, Na.sub.2CO.sub.3 at 1.60 g/l, KH.sub.2PO.sub.4 at 0.90 g/l, KNO.sub.3 at 0.80g/l, CaCl.sub.2•6H.sub.2O at 1.60 g/l, Mg(NO.sub.3).sub.2•6H.sub.2O at 0.80 g/l);
[0216] Treatment 4: Mix 60 (Comparative Example of an alternate electrolysed water solution, with salts comprising NaCl at 0.30 g/l, Na.sub.2CO.sub.3 at 1.20 g/l, KH.sub.2PO.sub.4 at 1.70 g/l, CaCl.sub.2•6H.sub.2O at 1.60 g/l, Mg(NO.sub.3).sub.2•6H.sub.2O at 1.20 g/l); and
[0217] Treatment 5: composition of Example 7 (Mix 38).
[0218] The prevalence of disease in each plant sample was measured after a period of 7 days, 14 days and 21 days after treatment.
[0219] As shown in
Example 11
Powdery Mildew (Oidium neolycopersici) in Tomatoes
[0220] Groups of tomato plants (of the variety ‘Juanita’) infected with an inoculum of powdery mildew (as shown in
[0221] Treatment 1: Untreated;
[0222] Treatment 2: Amistar (conventional fungicide);
[0223] Treatment 3: Mix 1 (Comparative Example of an alternate electrolysed water solution, with salts comprising NaCl at 0.30 g/l, Na.sub.2CO.sub.3 at 1.60 g/l, KH.sub.2PO.sub.4 at 0.90 g/l, KNO.sub.3 at 0.80g/l, CaCl.sub.2•6H.sub.2O at 1.60 g/l, Mg(NO.sub.3).sub.2•6H.sub.2O at 0.80 g/l);
[0224] Treatment 4: Mix 60 (Comparative Example of an alternate electrolysed water solution, with salts comprising NaCl at 0.30 g/l, Na.sub.2CO.sub.3 at 1.20 g/l, KH.sub.2PO.sub.4 at 1.70 g/l, CaCl.sub.2•6H.sub.2O at 1.60 g/l, Mg(NO.sub.3).sub.2•6H.sub.2O at 1.20 g/l);
[0225] Treatment 5: Composition of Example 7 comprising sodium salts; and
[0226] Treatment 6: Composition of the present invention (K38) comprising potassium carbonate and potassium chloride in the same carbonate: chloride ratio by weight as the composition of Example 7; and
[0227] The plants were stored in a NIAB growth room using daily conditions cycle of 20° C. for a 16 hour day, and then 16° C. for an 8 hour night.
[0228] The plants were then scored for the degree of infection 3 weeks after the single spray treatment. The results are illustrated in
[0229] Each of the comparative Examples (Treatments 3 and 4) provided a degree of fungicidal activity. However, none of the comparative Examples provided a fungicidal effect which was as effective as either the known fungicide, Amistar or the Composition of Example 7.
[0230] The plants were left for a further three weeks (a total of 6 weeks after single spray treatment) without any further treatment. The plants were then scored again for the degree of infection 6 weeks after the single spray treatment. The results are illustrated in
[0231] The method of pesticidal treatment of a substrate using the compositions of the present invention have significantly reduced environmental issues compared to conventional methods. In contrast to a number of conventional methods, the compositions of the present invention contain only simple, non-toxic and food-approved salts. The compositions of the present invention are therefore more environmentally friendly than known pesticidal compositions. Furthermore, the compositions of the present invention do not leave any harmful chemical residues on treated food. The compositions of the present invention are non-toxic and non-tainting. The compositions of the present invention have a significantly improved ozone concentration compared to the level which can be achieved by injection of gaseous ozone into water. For example, the compositions of the present invention may have approximately 100 times the level which can be achieved by injection of gaseous ozone into water. As such, the compositions of the present invention may be used more frequently, during extended periods of crop production, such as for example closer to crop harvest, and without requiring any additional health and safety protection or equipment. The compositions of the present invention provide a cost effective alternative to the use of known chemical pesticides. The compositions of the present invention provide medium term protective effect and an ongoing protective effect.
[0232] It is to be understood that Examples 7 to 11 are illustrative of the pesticidal properties of the compositions of the present invention. It is to be understood that the compositions of the present invention may be applied in any suitable manner to an agricultural area or crop(s).
[0233] Although the Examples of claims 7 to 11 illustrate the use of the compositions of the present invention for the treatment of crops, it is to be understood that the compositions of the present invention may be used for the treatment of soil, and/or in any suitable industry, in particular the agricultural industry, which requires the use of pesticidal compositions. For example, the compositions of the present invention may be used to treat any equipment, such as for example irrigation systems, tanks including water tanks, and/or crop treatment equipment as well as water such as for example surface, rain and/or ground water.
Example 12
Electrolyzed Water Composition
[0234] An electrolyte solution comprising a total salt concentration of 10.4 g/l in water (5.6 g/l anhydrous sodium carbonate (Na.sub.2CO.sub.3) and 4.8 g/l sodium chloride (NaCl)) was prepared. The electrolyte solution is stored within a reservoir chamber in fluid communication with an electrolytic cell.
[0235] A feed stream comprising the electrolyte solution was introduced into the electrolytic cell. The feed stream can optionally include one or more additional salts to enhance the antipathogenic properties of the resultant electrolyzed water composition. The electrolytic cell is a non-membrane electrolytic cell. The electrolytic cell comprises a casing, a plurality of boron doped diamond electrodes (BDEs) located within the cell, and metal ‘contact plates’ used for transmitting charge across the electrolyte solution.
[0236] The BDEs are sheet-like components and are provided in a stack of between 3 and 10 sheets. Each sheet is located at a fixed distance away from an adjacent sheet. The distance between adjacent sheets of BDEs provides a cell gap, which is preferably less than 5 mm, for example between approximately 2 and 3 mm. The BDEs are provided in a plastic frame. The BDEs transmit charge across the electrolyte solution, inducing a strong dipole and creating positively and negatively charged radicals on alternate surfaces of the diamonds.
[0237] The electrolyte solution may be introduced into the electrolytic cell in any suitable manner so as to produce electrolyzed water composition in a continuous process or in a batch process. In the continuous process, the electrolyte solution may be introduced at a suitable flow rate, such as for example at a flow rate in the range of from 0.1 to 100 l/min, for example in the range of from 3 to 5 l/min. In the batch process, the electrolyte solution may have a flow rate of approximately 16 l/min.
[0238] A power supply was operated to apply a voltage in the range of between 1 and 1000 Volt D.C. and a current within the range of from 1-1000 ampere to the electrolyte solution. The over-potential provided between the electrodes shifts the equilibrium within the electrolyte solution such that dissolved ozone is produced and remains within the electrolyzed water for a significant amount of time. For example, the half life of the dissolved ozone within the electrolyzed water composition is preferably at least a number of minutes, more preferably at least ten minutes, especially preferably at least 30 minutes, for example about 45 minutes.
[0239] The electrolytic cell preferably comprises an outlet through which the electrolyzed water composition exits the cell. The electrolyzed water composition preferably also has detergent properties. The electrolyzed water composition preferably comprises surfactant species.
[0240] The electrolyzed water composition according to this embodiment comprises dissolved ozone at a level of approximately 300 ppm. This level of dissolved ozone is approximately 100 times greater than the level which can be achieved by injecting gaseous ozone into water. As a result, the electrolyzed water composition of the present invention has an increased anti-microbial efficacy compared to water which has been injected with gaseous ozone. The electrolyzed water composition may be used as an antipathogenic agent against food borne pathogens.
[0241] Although the electrolyzed water composition of the present invention contains dissolved ozone at a level of approximately 300 ppm, it is to be understood that the electrolyzed water composition of the present invention may comprise any suitable level of dissolved ozone, preferably within the range of between 0.1 and 10000 ppm, preferably between 1 and 1000 ppm.
[0242] Conventional electrolyzed water compositions based on chloride electrolytes generate free accessible chlorine (FAC). Use of the conventional compositions therefore produces, either when prepared or when reacted, a smell which is associated with swimming pools. There is a risk that disinfected equipment within a food processing environment may produce food products which have become tainted with this chlorine associated smell. In contrast, the electrolyzed water composition of the present invention is substantially free of free accessible chlorine (FAC). In the embodiment used in the example, the composition of Example 1 comprises <0.1 ppm FAC both when produced, and when reacted. The compositions of the present invention may therefore be used to clean and disinfect processing lines and equipment without producing a smell associated with a swimming pool and with a significantly reduced risk of tainting the food product.
Example 13
[0243] With reference to Tables 2 and 3, three groups of 30 poultry carcasses were treated with three different treatment methods.
[0244] Treatment 1: Untreated as a control sample;
[0245] Treatment 2: the Sonosteam process involving exposure to steam and ultrasound.
[0246] Treatment 3: the Sonosteam process followed by exposure to the electrolyzed water composition of Example 12. The Sonosteam treated poultry carcasses were immersed for 20 seconds per bird in a reservoir comprising the electrolyzed water composition of Example 12 as shown in
[0247] The poultry carcasses of each group were then subjected to biopsy of the neck skin (a particularly difficult area to treat effectively) and breast skin (an easier part of the carcass to treat), with weighed skin samples being sent to a specialist testing lab to determine the level of Campylobacter present (as colony forming units/gram of skin) at the day of kill (herein referred to as DOK) plus 4 days (Table 2); and again at the day of kill plus 7 days (Table 3).
TABLE-US-00001 TABLE 2 Campylobacter level at DOK plus 4 days Campylobacter Level Treatment (log.sub.10) Birds > 1,000 cfu/g Treatment 1 (Control) 3.10 35% Treatment 2 (Sonosteam) 2.85 30% Treatment 3 (Sonosteam + 1.70 0% Composition of Example 12)
[0248] The average background contamination level of Campylobacter after 4 days (DOK plus 4 days) was found to be 3+ log (ie. 1000 cfu/g). 35% of the group of the untreated control poultry carcasses were found, after four days, to have a level of Campylobacter of greater than 1000 cfu/g. This level of Campylobacter contamination is considered to be indicative of a heavily contaminated group of poultry.
TABLE-US-00002 TABLE 3 Campylobacter level at DOK plus 7 days Campylobacter Level Treatment (log.sub.10) Birds > 1,000 cfu/g Treatment 1 (Control) 2.66 30% Treatment 2 (Sonosteam) 2.30 14% Treatment 3 (Sonosteam + 1.27 0% Composition of Example 12)
[0249] As shown in Tables 2 and 3, exposure of the carcass to the composition of Example 13 for a time period of 20 seconds per bird results in a reduction in the level of Campylobacter of at least 1 log (90%). The level of reduction may be further improved by prolonged exposure to the composition of Example 12. This significant reduction in the level of Campylobacter furthermore would result in a significant reduction in the number of human food poisonings as a result of eating contaminated poultry carcasses. This significant reduction in the level of Campylobacter would therefore have significant benefits and associated cost savings for food producers, such as for example poultry farmers, food processors, and retailers.
[0250] It can be seen from Tables 2 and 3 that the electrolyzed water compositions of the present invention achieves a significant reduction of at least 95% of Campylobacter pathogens on the poultry carcasses over a period of at least 7 days from the Day of Kill. Furthermore, the compositions of the present invention are effective in ensuring that no carcasses within the group have a Campylobacter level of over 1000 cfu/g. The compositions of the present invention are therefore effective in reducing pathogen levels on carcasses to be within safer limits and thereby significantly reducing the risk of food poisoning.
[0251] The compositions of the present invention have also been found to not provide any negative organoleptic results, such as for example poor taste or smell residues and/or visual or tactile degradation of carcass quality.
[0252] The present invention provides an electrolyzed water composition providing improved anti-pathogenic activity on or in food substrates. Although the present invention demonstrates the effectiveness of the electrolyzed water composition with respect to reducing and/or Campylobacter on poultry carcasses, it is to be understood that the compositions of the present invention are effective against other pathogens, and in particular food borne pathogens, and are not limited to Campylobacter reduction and/or elimination. The compositions of the present invention are effective against a number of different pathogens on any suitable food substrate and are therefore not limited to reduction and/or eliminated of pathogens on or in poultry carcasses. The compositions of the present invention may be applied to the food substrate by any suitable method and/or for any suitable application time.
[0253] It is also to be understood that the electrolyzed water compositions of the present invention may be applied at a higher dosage to the food substrate, and/or may reduce and/or eliminate food borne pathogens over a much shorter period of time than achieved for the low dosage application of the composition as shown in this Example.
Example 14
[0254] With reference to Table 4, three groups of 30 poultry carcasses were treated with three different treatment methods.
[0255] Treatment 1: Untreated as a control sample;
[0256] Treatment 2: the Sonosteam process involving exposure to steam and ultrasound.
[0257] Treatment 3: exposure to the electrolyzed water composition of Example 12. The poultry carcasses were immersed for 15 seconds per bird in a reservoir comprising the electrolyzed water composition of Example 12. The electrolyzed water composition of Example 12 was warmed to and maintained at a temperature between 43° C. and 50° C.
[0258] The poultry carcasses of each group were then subjected to biopsy of the neck skin and breast skin, with weighed skin samples being sent to a specialist testing lab to determine the level of Campylobacter present at day of kill plus 4 days (Table 4).
TABLE-US-00003 TABLE 4 Campylobacter level at DOK plus 4 days Campylobacter Level Treatment (log.sub.10) Birds > 1,000 cfu/g Treatment 1 (Control) 2.01 7% Treatment 2 (Sonosteam) 1.47 0% Treatment 3 (Composition of 1.17 0% Example 12)
[0259] The average background contamination level of Campylobacter after 4 days (DOK plus 4 days) was found to be 2+ log (ie. 100 cfu/g). 7% of the group of the untreated control poultry carcasses were found, after four days, to have a level of Campylobacter of greater than 1000 cfu/g. This level of Campylobacter contamination is considered to be indicative of an unusually lowly contaminated group of poultry, and smaller level of reductions following treatment are expected when the starting population of Campylobacter is lower.
[0260] Although Examples 12 to 14 illustrate the effectiveness of embodiments of the electrolyzed water compositions of the present invention within poultry processing environments, it is to be understood that the compositions, method and apparatus of the present invention can be used to reduce and/or eliminate food borne pathogens in any suitable environment, and is not to be limited to poultry processing environments.