Patent Application
20120228149
1. Field of the Invention (Technical Field)
The present invention is related to electrochemical conversion of quaternary ammonium halide salts to quaternary ammonium hypohalite salts preferably through the anodic oxidation of the halide anions of the quaternary ammonium halide salts.
2. Background Art
Note that the following discussion may refer to a number of publications and references. Discussion of such publications herein is given for more complete background of the scientific principles and is not to be construed as an admission that such publications are prior art for patentability determination purposes.
Disinfectants and biocides are used to control microorganisms which may be present either in air, on a surface, or in a bulk liquid. Common chemicals that are used as disinfectants include alcohols, aldehydes, oxidizing chemicals (including halogens, hypohalous acids, hypohalite anions, chloramines, hydrogen peroxide, and ozone), phenols, and quaternary ammonium compounds. Some disinfectants, including quaternary ammonium compounds, can also serve as surfactant cleaners or corrosion inhibitors. Each of these chemicals have unique and specific properties which make them suitable for many applications, but preferential for certain applications. Aqueous chlorine is perhaps the most prominent and universally applied biocide. While aqueous chlorine is typically produced either through bubbling chlorine gas into water (as in disinfection of potable water) or delivered to a point-of-use in the form of concentrated aqueous solutions, it can also be generated electrochemically from sodium chloride (salt). Electrolysis of aqueous sodium chloride solutions, and brines containing other alkali metal halide salts, has long been used in the production of halogen, hypohalous acid, and hypochlorite solutions. Typically, dimensionally stable anodes are used in the electrolytic production of halogen solution that can be used for disinfection, sanitization, cleaning and other applications.
Quaternary ammonium halide salts are a commonly used alternative biocide to aqueous halogen solutions in non-drinking water applications. The general chemical structure of a quaternary ammonium halide salt is NR4X, where N is a central nitrogen atom, R denotes an organic hydrocarbon functional group, and X represents a halide (Cl−, Br, or I−). Examples of quaternary ammonium halides commonly used for disinfection and sanitization include: benzalkonium chloride (N-alkyl-N-benzyl-N-dimethylammonium chloride where the alkyl chain contains between 8 and 18 carbon atoms), benzethonium chloride, centrimonium chloride or bromide (cetyltrimethylammonium chloride or bromide), cetylpyridium chloride, dequalinium, and didecyldimethylammonium chloride. The quaternary ammonium cation is the main active component, capable of killing microorganisms by perforating the cell membrane. Quaternary ammonium cations are environmentally stable, providing a long-lived residual disinfection capability in a given application. Quaternary ammonium halide compounds are often used to disinfect surfaces, especially in the medical, food, and beverage industries. Quaternary ammonium compounds are also used for disinfection and sanitization in other applications, including but not limited to treatment of oil/gas drilling hydraulic fracturing or process waters, as components of antibacterial consumer products, and treatment of cooling tower water. They are also used as corrosion inhibitors of iron and steel in acidic solutions or as part of an important part of a corrosion inhibition formulation.
Combinations of aqueous chlorine and/or mixed oxidant solution and quaternary ammonium salts, effectively producing quaternary ammonium hypohalite salts, may be used to enhance the germicidal properties of a disinfecting or sanitizing solution. However, the combined solution typically degrades quickly. It is believed the organic portion of the compound will react with the hypohalite portion, decreasing the efficacy of the overall combination for disinfection and sanitization, thereby adversely affecting stability of the compounds and solutions. Thus, a method by which quaternary ammonium hypohalite compounds can be generated on-site and on-demand is desirable, so the biocides may be produced just before use, particularly since the precursors (for example a halogen salt or brine and quaternary ammonium salts) are highly stable and can be stored for long periods of time. There are no known processes by which quaternary ammonium cations and either hypohalite anions or halogens with enhanced antimicrobial activity combinations can be made from quaternary ammonium halide salts at the point of use.
Electrochemical oxidation of halide ions is one such method by which quaternary ammonium hypohalite compounds can be produced on-site and on-demand. Electrochemical production of aqueous solutions of halogens (chlorine, bromine, or iodine) from the respective halide ions through electrochemical oxidation of the halide is a well known technology. However, electrochemistry may also destroy (through oxidation or reduction processes at electrode surfaces) organic compounds dissolved in water, such as aqueous solutions of quaternary ammonium compounds. Thus it is advantageous to develop a process for electrochemical oxidizing such compounds, either alone or in combination with additional alkali halide components, without destroying them, in order to produce quaternary ammonium hypohalite compounds that can act as an effective disinfectant, sanitizer, cleaner, surfactant, and/or corrosion inhibitor.
An embodiment of the present invention is a method for producing a solution, the method comprising electrolyzing a first solution comprising a quaternary ammonium compound in solution and producing a second solution comprising a quaternary ammonium hypohalite in solution. The quaternary ammonium compound preferably comprises a quaternary ammonium halide. The first solution optionally further comprises a halide salt, preferably an alkali metal halide salt, in solution. The first solution optionally comprises a compound selected from the group consisting of surfactant, organic surfactant, colorant, perfume, disinfectant, germicide, and biocide. The second solution preferably further comprises an additional oxidant species, optionally selected from the group consisting of halide based oxidant, halogen, hydrogen peroxide, ozone, chlorine dioxide, and combinations thereof. The combination of the quaternary ammonium hypohalite and the additional oxidant species in the second solution preferably substantially increases the disinfection efficacy of the second solution over an unelectrolyzed solution comprising the quaternary ammonium hypohalite and the additional oxidant species mixed together in solution. The second solution preferably does not substantially comprise a halide salt.
Another embodiment of the present invention is a method of producing a solution, the method comprising electrolyzing a first solution comprising a first quaternary ammonium compound in solution and a second component and producing a second solution comprising a second quaternary ammonium compound in solution and a second compound. The second component optionally comprises ammonia or an ammonium salt and the second compound comprises a haloamine. Alternatively, the second component comprises a chlorite salt and the second compound comprises chlorine dioxide. Alternatively, the second component comprises dissolved oxygen at a greater concentration than a naturally occurring dissolved oxygen concentration of the first solution and the second compound comprises hydrogen peroxide. In this case the electrolyzing step is preferably performed in a divided electrolytic cell and the second quaternary ammonium compound and hydrogen peroxide is produced in the cathodic compartment of the divided electrolytic cell. If the first solution comprises a quaternary ammonium halide or a halide salt, the second solution preferably further comprises a quaternary ammonium hypohalite produced in the anodic compartment of the divided electrolytic cell.
Another embodiment of the present invention is a device for dispensing the solution produced in any of claims 1-16, the device comprising a flow through electrolytic cell comprising an anode and a cathode and a spray nozzle for dispensing the solution. The device may optionally comprise a spray bottle configuration, wherein electrolysis of the solution is activated by a user squeezing a trigger. The device may alternatively comprise a hand washing station, wherein electrolysis of the solution is activated by a user moving a lever or a user placing at least one hand under the device.
Another embodiment of the present invention is a device for dispensing wipes comprising a solution, the device comprising a supply of wipes comprising a quaternary ammonium compound, an anode, and a cathode, wherein the wipes are disposable between the anode the said cathode, at which time the quaternary ammonium compound is electrolyzed. The anode may optionally comprise a drum anode and the cathode may optionally comprise a drum cathode. Alternatively, the anode and cathode comprise flat plates, and the device further comprises a mechanism for pressing a wipe between the anode and the cathode. The wipes preferably comprise a compound selected from the group consisting of quaternary ammonium halide, halide salt, surfactant, organic surfactant, colorant, perfume, disinfectant, germicide, and biocide.
Another embodiment of the present invention is a method for on demand generation of a quaternary ammonium hypohalite solution, the method comprising signaling a desired amount of a first solution comprising a quaternary ammonium hypohalite in solution to be produced; mixing a second solution comprising a quaternary ammonium compound in solution with a third solution comprising a halogen solution, the amounts of the second solution and third solution corresponding to the desired amount of the third solution; producing the desired amount of the third solution; and dispensing the desired solution immediately or prior to significant degradation of the third solution. The halogen solution preferably comprises a compound selected from the group consisting of bleach, hypochlorous acid, hypobromous acid, hypoiodous acid, hypochlorite, hypobromite, hypoiodite, and hypohalite.
Objects, advantages, novel features, and further scope of applicability of the present invention will be set forth in part in the detailed description to follow, taken in conjunction with the accompanying drawings, and in part will become apparent to those skilled in the art upon examination of the following, or may be learned by practice of the invention. The objects and advantages of the invention may be realized and attained by means of the instrumentalities and combinations particularly pointed out in the appended claims.
The accompanying drawings, which are incorporated into and form a part of the specification, illustrate an embodiment of the present invention and, together with the description, serve to explain the principles of the invention. The drawings are only for the purpose of illustrating various embodiments of the invention and are not to be construed as limiting the invention. In the drawings:
a and 10b show the foaming that sometimes occurs during the electrolysis of a quaternary ammonium halide solution or a quaternary ammonium halide/alkali metal halide solution.
Embodiments of the present invention are unique electrochemical cells and processes by which quaternary ammonium halide salts are preferably dissolved into solution and converted, preferably electrochemically, into quaternary ammonium hypohalite salts in solution, preferably in bulk, such as part of a delivery system (for example, a spray bottle) or as part of a dispensing system whereby quaternary ammonium halide salts absorbed onto wipes can be dispensed as quaternary ammonium hypohalite salts. Other blends between quaternary ammonium cations and halogen based disinfectants (such as diatomic halogens, hypohalous acids, or hypohalite anions) may be produced. By choosing an appropriate quaternary ammonium halide salt, a corresponding quaternary ammonium hypohalite salt solution can be formed that has one or more desired properties, such as corrosion inhibition, scale formation inhibition, surfactant, or cleaning properties.
In an embodiment of the present invention, an aqueous solution comprising dissolved quaternary ammonium salts is electrolyzed, which converts the halide component of the quaternary ammonium salt to the corresponding halogen. The halogen dissolves in the aqueous solution producing hypohalous acid and hypohalite anion. The general electrochemical reaction can be described by the simplified equation:
NR4+X−+H2O→NR4+XO−+H2
where NR4+ is the quaternary ammonium ion containing a central nitrogen atom connected to four hydrocarbon functional groups (denoted R), X− is a halide ion (e.g. Cl−, Br−, or I−), and XO− is a hypohalite ion (e.g. ClO−, BrO−, or IO−). Examples of quaternary ammonium compounds that could be utilized in this process include, but are not limited to, benzalkonium chloride, didecyldimethylammonium chloride, cetyltrimethylammonium chloride, octyltrimethylammonium chloride, tetramethylammonium chloride, tetraethylammonium chloride, tetrapropylammonium chloride, tetrabutylammonium chloride, cetylpyridinium chloride, benzalkonium bromide, didecyldimethylammonium bromide, cetyltrimethylammonium bromide, octyltrimethylammonium bromide, tetramethylammonium bromide, tetraethylammonium bromide, tetrapropylammonium bromide, tetrabutylammonium bromide, cetylpyridinium bromide, benzalkonium iodide, didecyldimethylammonium iodide, cetyltrimethylammonium iodide, octyltrimethylammonium iodide, tetramethylammonium iodide, tetraethylammonium iodide, tetrapropylammonium iodide, tetrabutylammonium iodide, and cetylpyridinium iodide. Polymeric quaternary ammonium compounds, for example, but not limited to, the polyquaternium polymers, can also be used as the quaternaryammonium halide source in these reactions.
Embodiments of the present invention utilize an electrochemical process by which a quaternary ammonium halide salt is converted to a quaternary ammonium hypohalite salt; one such process is shown in
There are a variety of solution compositions and operational conditions which can be employed for this invention. The quaternary ammonium halide salt used can be a singular salt or a mixture containing one or more quaternary ammonium moieties combined with one or more halide anions. Similarly, the counterions for the quaternary ammonium cations could be chloride, bromide, or iodide. In addition to the quaternary ammonium compound, the solution used in this electrolysis process may comprise additional halides such as alkali metal halide salts, which increase halogen, hypohalous acid, and hypohalite ion production capacity. In this case, the feed salts include, but are not limited to, sodium chloride, sodium bromide, sodium iodide, potassium chloride, potassium bromide, and potassium iodide. For example, NaCl and a quaternary ammonium halide salt can be electrolyzed simultaneously, producing a combined biocidal solution comprising quaternary ammonium hypohalite salt and one or more chlorine based oxidants. Moreover, the solution used during the electrolytic process described herein may comprise other germicidal components in addition to the quaternary ammonium cations, such as additional germicidal agents, colorants, and perfume components.
Halides, surfactants (e.g. linear alkyl benzene sulfonates), and/or other germicidal compounds such as biocides may optionally be dissolved with the quaternary ammonium halide into solution (such as a brine) prior to electrolysis. If a halide such as an alkali metal halide salt (e.g. NaCl) is added, then any quaternary ammonium compound, not just a quaternary ammonium halide, may be used, since the halide salt can contribute the halide to the solution. Embodiments of the present invention also encompass methods to control or tune the concentrations of different disinfectants or surfactants, thereby controlling synergy for a specific disinfection or cleaning application.
Other compounds may be added to the solution or brine used to feed the electrochemical cell. If ammonia or an ammonium salt (such as ammonium chloride, ammonium sulfate, ammonium bromide, ammonium iodide, etc) is added, solutions are produced that comprise both quaternary ammonium compound(s) and haloamine(s) such as monochloramine, dichloramine, trichloramine, monobromamine, dibromamine, tribromamine, monoiodamine, diiodamine, or triiodamine. If a chlorite (ClO2−) salt (such as sodium chlorite) is added, solutions are produced that comprise both quaternary ammonium compound(s) and chlorine dioxide. If the solution being fed into the electrochemical cell contains increased dissolved oxygen, solutions are produced that comprise both quaternary ammonium compound(s) and hydrogen peroxide. In this case it is preferable that the electrolytic cell is divided (i.e. the cathodic and anodic compartments are separate). The quaternary ammonium compound and hydrogen peroxide will be produced in the cathodic compartment. Additionally, quaternary ammonium hypohalites may simultaneously be produced on the anodic compartment of such a cell (if the feed stream comprises a quaternary ammonium halide and/or a halide salt).
One embodiment of the present invention is a batch electrochemical cell as depicted in
Another embodiment of the present invention is a flow through electrochemical cell as depicted in
Details of an embodiment of electrochemical cell 70 are given in
Practical operation of all types of cells will vary depending on a number of factors, such as the chemical nature of the quaternary ammonium halide salt, the concentration of all halide salts in solution, the desired level of halogen, hypohalous acid, and hypohalite ion in the product, the type of halide ion to be oxidized, and the presence of additional germicidal agents. Cell operational parameters that may be varied include, but are not limited to, cell voltage, electrode spacing, cell current, solution flow rate, and/or cell operating temperature. Additionally, other factors involved in cell construction may vary depending on the operating conditions, including but not limited to the spacing of the electrodes, the nature of the coating on the anode surfaces, and/or the nature of the coating on the cathode surfaces.
An embodiment of the present invention is a cell combined in a solution delivery system such as the spray bottle shown in
An embodiment of the present invention is a hand wash station as shown in
An alternative embodiment of the invention is a cell capable of oxidizing the halide component of quaternary ammonium halide salts impregnated onto wipes used for sanitizing various surfaces, as shown in
Another embodiment of the present invention is a device that can combine separate aqueous solutions of quaternary ammonium halide salts and halogen(s) to provide the quaternary ammonium hypohalite solution without the use of electrolysis. One example of such a device is illustrated in
Electrochemical processes such as the ones described herein may produce products that are substantively different than a process whereby two components are simply mixed together. In the case of quaternary ammonium hypohalite salts, the comparative processes are the physical combination of an aqueous solution of an alkali metal hypohalite with an aqueous solution of a quaternary ammonium halide without electrolysis, and the electrochemical oxidation of the halide portion of a quaternary ammonium halide salt. One major distinction between these processes is that the physical combination of the two individual components also produces a quantity of undesirable alkali metal halide salt, as is illustrated with the following chemical equation:
NR4X+MOCl→NR4OCl+MX
Here, NR4X is the quaternary ammonium halide salt, MOCl is the metal hypohalide, NR4OCl is the quaternary ammonium hypohalite compound that is the intended product of the chemical reaction, and MX is the alkali metal halide byproduct, such as NaCl. Comparatively, the electrochemical process involves only the oxidation of the halide component of the quaternary ammonium halide salt, and therefore, essentially no excess alkali metal halide is present in the resulting disinfection solution. This distinction is critical in a number of applications, and expressly so in the case of surface disinfection. The extra salts produced through physical combinations of a quaternary ammonium halide salt and an alkali metal hypohalite can lead to the excessive formation of residual solids on the surface to be cleared, thus necessitating a secondary cleaning step or agent to be used to remove the excess salts. Moreover, alkali metal halide salts are well known to be corrosive agents against stainless steels as well as other materials, and therefore limiting the exposure of corrosion-susceptible materials is a critical factor in the selection of surface disinfectants.
Another difference between simple combination of quaternary ammonium halide salts with alkali (or alkaline) metal hypochlorite and the electrochemical production of quaternary ammonium hypochlorite compounds is that the electrolysis process may produce other oxidative species beyond just the aqueous halogen, which species can demonstrate synergistic inactivation properties. Electrochemical cells exist, for example, that can produce a mixed oxidant solution, comprised primarily of aqueous chlorine but also having other oxidative species, that has been shown to be more effective at inactivating a wide range of microorganisms. Similarly, an electrochemical cell designed to produce quaternary ammonium hypochlorite compounds may also produce other oxidant species, resulting in a disinfecting solution that is more effective for microbial inactivation than simply physically mixing the two corresponding components together.
An aqueous solution of benzalkonium chloride was prepared by dissolving 10 grams of benzalkonium chloride in 1000 mL of deionized water to give a 1% (10,000 mg/L) solution. 200 mL of this solution was transferred to a 250 mL beaker, and a three electrode cell was immersed in the solution. The cell was then energized to 12 volts for 20 minutes. During this time, extensive bubbling was observed on the cathodic electrodes, producing a foam above the surface of the solution (similar to that shown in
An aqueous solution of cetyltrimethylammonium chloride was prepared by adding 20 mL of a 25% by weight cetyltrimethylammonium solution to 1000 mL of deionized water to give a 0.5% (5,000 mg/L) solution. 200 mL of this solution was transferred to a 250 mL beaker, and a three electrode cell was immersed in the solution. The cell was then energized to 12 volts for 60 minutes. During this time, extensive bubbling was observed on the cathodic electrodes, producing a foam above the surface of the solution (similar to that shown in
A solution containing 100 mg/L benzalkonium chloride and 5,000 mg/L sodium chloride was prepared by dissolving 0.1 g benzalkonium chloride and 5 g sodium chloride in 1000 mL deionized water. 200 mL of this solution was transferred to a 250 mL beaker, and a three electrode cell was immersed in the solution. The cell was then energized to 12 volts for 20 minutes. During this time, extensive bubbling was observed on the cathodic electrodes, producing a foam above the surface of the solution (similar to that shown
A solution containing 100 mg/L cetyltrimethylammonium chloride and 1,000 mg/L sodium chloride was prepared by dissolving 0.4 mL of a 25% cetyltrimethylammonium chloride solution and 1 g sodium chloride in 1000 mL deionized water. 200 mL of this solution was transferred to a 250 mL beaker, and a three electrode cell was immersed in the solution. The cell was then energized to 12 volts for 20 minutes. During this time, extensive bubbling was observed on the cathodic electrodes, producing a foam above the surface of the solution (similar to that shown in
a and 10b are photographs showing the foaming that sometimes occurs during the electrolysis of a quaternary ammonium halide solution or a quaternary ammonium halide/alkali metal halide solution. In these photographs, the solution being electrolyzed is a 100 mg/L benzalkonium chloride and 20 g/L sodium chloride solution, and the electrolysis is at 12 volts applied to the cell. Similar results were observed during electrolysis of brines comprised of cetyltrimethylammonium chloride, octyltrimethylammonium chloride, or didecyldimethylammonium chloride, either alone combined with sodium chloride. Solutions of tetraalkylammonium chlorides (such as tetramethylammonium chloride, tetraethylammonium chloride, tetrapropylammonium chloride, and tetrabutylammonium chloride), either alone or in sodium chloride based brines, produced chlorine when electrolyzed but the production of foam during electrolysis was minimized.
The differences between quaternary ammonium hypohalite compounds prepared by electrolysis of a quaternary ammonium halide compound and the mixing solutions of a quaternary ammonium halide compound with an alkali (or alkaline) metal hypochlorite compound were examined. Here, a 500 mg/L CTAC solution was electrolyzed as described above, producing a solution with a measured FAC of 32 mg/L. Similarly, a solution containing 500 mg/L CTAC and 31.2 mg/L FAC was prepared by combining CTAC and commercial bleach solutions. As a control, a 500 mg/L CTAC solution was prepared without either electrolysis or added bleach. All three solutions were then used to inactivation B. Globigii spores with a contact time of 2, 5, and 10 minutes, and the results from this test are shown in
As an example of the differences between quaternary ammonium hypochlorite solutions that are produced through the combination of a solution containing quaternary ammonium halide compounds with a solution containing an alkali (or alkaline) metal hypochlorite as compared to the direct electrolysis of a quaternary ammonium halide compound, solutions based on CTAC were prepared by combining CTAC (150 mg/L) and sodium hypochlorite (variable FAC concentration between 1 and 50 mg/L FAC). Similarly, CTAC (167 mg/L) was electrolyzed in an electrochemical cell, producing a solution that had a FAC concentration of 4.2 mg/L. Alone, CTAC at 167 mg/L was able to achieve a 0.90±0.14 log inactivation of B. globigii spores while that same solution, after electrolysis, achieved a 2.93±0.19 log inactivation of B. globigii spores. In comparison, the mixed CTAC and bleach solutions had lower log inactivation of B. globigii spores until the FAC concentration was at least 20 mg/L, and at that concentration, the solution was only able to achieve a log inactivation of 1.23±0.17. Similar results were observed when comparing other concentrations of mixed and electrolyzed solutions using other CTAC concentrations as well as other quaternary ammonium compounds. Enhanced spore inactivation associated with quaternary ammonium hypochlorite produced through electrolysis as opposed to quaternary ammonium produced through blending the individual components is consistent with the presence of other oxidizing biocides, possibly including hydrogen peroxide.
In some applications of the present disclosure, it may be necessary to vary the relative amounts of FAC and quaternary ammonium components in a produced quaternary ammonium hypochlorite solution. This can be readily achievable using the present invention by blending an alkali metal halide salt with a quaternary ammonium halide compound to produce a mixed brine that is then electrolyzed. In one specific example, CTAC was blended with sodium chloride to produce a series of brines with varying concentration of CTAC, with the concentration of sodium chloride being constant at 20 g/L. Here the concentration of CTAC in the brines was set to be 50, 100, 500, 1000, and 5000 mg/L. These solutions were then electrolyzed, and FAC concentrations of the electrolyzed solutions was found to be 4550, 4000, 3000, 2650, and 1600 mg/L respectively. These solutions were then diluted so that the FAC concentration was either 5 or 10 mg/L, resulting in an equivalent cetyltrimethylammonioum concentration of 0.06, 0.13, 0.83, 1.9, and 16 mg/L for the 5 mg/L FAC solutions and 0.11, 0.25, 1.67, 3.78, and 31 mg/L for the 10 mg/L FAC solutions respectively. These solutions were then used to inactivate B. globigii spores and the results of this test are shown in
As can be seen, the log inactivation of solutions based on a 5 mg/L FAC concentration were typically around 1.1 with the highest log inactivation of 1.51 seen with an equivalent cetyltrimethylammonioum concentration of 16 mg/L. However, when the FAC concentration was 10 mg/L, all solutions independent of cetyltrimethylammonioum concentration demonstrated a log inactivation of 3.5 (the maximum observable under this test design). Unelectrolyzed CTAC solutions under similar concentrations and exposure times typically resulted in log inactivation of around 0.27-0.30 while FAC alone solutions under these conditions typically result in a log inactivation of less than 1. This data indicates that it is possible to achieve a biocide of the desired strength by choosing the appropriate blend ratio of a quaternary ammonium halide compound with an alkali metal halide salt into the brine used for electrolysis. Moreover, these results are surprising in that only small amounts of CTAC were necessary to achieve the synergistic disinfection in the electrolyzed quaternary ammonium hypochlorite compound solution. Other concentrations of CTAC, as well as other concentrations of sodium chloride and other quaternary ammonium compounds, produced similar results with the main difference being actual ratios of quaternary ammonium compound to FAC in the produced solutions, which showed differing inactivation efficacy depending on the chemical nature of the quaternary ammonium compound.
For some quaternary ammonium halide compounds, electroxidation of the halide component of the compounds can install an unexpected biocidal capability. One example is the case of tetramethylammonium chloride (TMAC), a quaternary ammonium compound that is not traditionally effective as a microbiocide. When a 500 mg/L TMAC solution was electrolyzed, thereby producing tetramethylammonium hypochlorite, and the unelectrolyzed, electrolyzed, and electrolyzed/quenched TMAC solutions were then used to inactivate B. globigii spores.
Although the invention has been described in detail with particular reference to these preferred embodiments, other embodiments can achieve the same results. Variations and modifications of the present invention will be obvious to those skilled in the art and it is intended to cover all such modifications and equivalents. The entire disclosures of all patents and publications cited above are hereby incorporated by reference.
This application claims priority to and the benefit of filing of U.S. Provisional Patent Application Ser. No. 61/450,735, entitled “Electrochemical Generators for the Production of Quaternaryammonium Hypohalites from Quaternaryammonium Halide Salts”, filed on Mar. 9, 2011, the specification of which incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| 61450735 | Mar 2011 | US |
