WO2010077862A2 - Apparatus and methods for controlling chlorine dioxide concentration - Google Patents
Apparatus and methods for controlling chlorine dioxide concentration Download PDFInfo
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- WO2010077862A2 WO2010077862A2 PCT/US2009/068050 US2009068050W WO2010077862A2 WO 2010077862 A2 WO2010077862 A2 WO 2010077862A2 US 2009068050 W US2009068050 W US 2009068050W WO 2010077862 A2 WO2010077862 A2 WO 2010077862A2
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- Prior art keywords
- chlorine dioxide
- concentration
- gas
- target chamber
- valve
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B11/00—Oxides or oxyacids of halogens; Salts thereof
- C01B11/02—Oxides of chlorine
- C01B11/021—Chlorine hemioxide (Cl2O)
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N59/00—Biocides, pest repellants or attractants, or plant growth regulators containing elements or inorganic compounds
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
- A61L2/16—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using chemical substances
- A61L2/20—Gaseous substances, e.g. vapours
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
- A61L2202/10—Apparatus features
- A61L2202/14—Means for controlling sterilisation processes, data processing, presentation and storage means, e.g. sensors, controllers, programs
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2202/00—Aspects relating to methods or apparatus for disinfecting or sterilising materials or objects
- A61L2202/20—Targets to be treated
- A61L2202/25—Rooms in buildings, passenger compartments
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L2209/00—Aspects relating to disinfection, sterilisation or deodorisation of air
- A61L2209/10—Apparatus features
- A61L2209/11—Apparatus for controlling air treatment
- A61L2209/111—Sensor means, e.g. motion, brightness, scent, contaminant sensors
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L9/00—Disinfection, sterilisation or deodorisation of air
- A61L9/015—Disinfection, sterilisation or deodorisation of air using gaseous or vaporous substances, e.g. ozone
Definitions
- the present invention relates to methods and apparatuses for controlling chlorine dioxide concentration in an enclosed or partially enclosed space.
- Chlorine dioxide was discovered in the early 1800's, and was adopted by commerce in the
- Chlorine dioxide has been called the ideal biocide and the ability of chlorine dioxide to reduce or eliminate viable microbes, e.g., bacteria, viruses, fungi, mold spores, algae and protozoa, is well-documented and well known. See, for example, Franklin, CL. et al.
- chlorine dioxide inactivates microorganisms by oxidizing key components of a micro-organism's membrane proteins that are vital to the membrane's structure and function. Also, the oxidizing reaction that causes microorganism inactivation does not form trihalomethanes
- THMs haloacetic acids
- HAAs haloacetic acids
- chlorine dioxide A major limitation to the use of chlorine dioxide is that chlorine dioxide can not be manufactured in bulk at an industrial gas plant and shipped to final use destinations. Accordingly, chlorine dioxide must be generated on-site.
- Apparatus and methods for controlling the concentration of chlorine dioxide would be beneficial for disinfection in a variety of applications including biosafety cabinets, isolators, filters, air handling equipment, food and drug processing equipment, etc.
- the instant invention provides apparatus and methods for controlling the concentration of chlorine dioxide in a space, e.g., biosafety cabinets, isolators, filters, air handling equipment, food and or drug processing equipment.
- the instant invention comprises an apparatus comprising a source of chlorine dioxide, a target chamber to be treated, one or more pumps, and at least two paths connecting elements of this system.
- the system may also comprise one or more valves.
- the system may also comprise a chlorine dioxide concentration sensor.
- the source of chlorine dioxide may be, for example, an aqueous solution as made by a variety of chlorine dioxide generating processes. For example, mixing citric acid with sodium chlorite in water will spontaneously produce a solution of chlorine dioxide.
- valve(s) and/or pump(s) are arranged in the system in such a way that adjusting them controls the amount of gas circulated in the two loops and the concentration of chlorine dioxide in a target chamber.
- Figures 1-7 show a variety of useful arrangements of pumps, valves and sensor locations.
- the flow loop that contains the target chamber, but not the chlorine dioxide source is typically run at a higher gas flow rate than the flow loop that flows through the chlorine dioxide source. This higher flow rate maintains a more dioxide concentration in the target chamber by increased mixing in the target chamber and therefore minimizing gradient effects due to chlorine dioxide losses in the target chamber or system.
- Chlorine dioxide losses may be due to, for example, leaks in the system, reaction with the chlorine dioxide by elements in the target chamber or system, or by absorption of the chlorine dioxide by elements in the target chamber or system.
- the flow of gas that goes through the chlorine dioxide source is set to control the amount of chlorine dioxide that enters the target chamber so the desired concentration profile can be generated in the target chamber.
- the flow of gas through the chlorine dioxide chamber may be fixed, controlled manually by an operator or controlled automatically.
- the flow of gas through the chlorine dioxide chamber may be controlled in response to the reading on the chlorine dioxide concentration sensor either manually or automatically. If the flow is controlled automatically, feedback control well known in the art, such as PID control, may be used.
- the sensor may be located in a slip stream with a different flow rate than the main circulation loop.
- the light In optical chlorine dioxide concentration sensors the light, typically in the ultraviolet range, may breakdown the chlorine dioxide into undesirable byproducts. These byproducts may include the hypochlorite ion. These byproducts may cause corrosion or other deleterious effects to elements of the system.
- a lower flow through the sensor may be used to reduce the amount of byproducts.
- the sensor outflow may be vented to prevent byproducts from returning to the system. In this case the sensor flow may be lower to reduce the amount of chlorine dioxide gas lost from the system. If the outflow is vented there must also be an inlet to avoid developing too much negative pressure in the apparatus and target chamber.
- the sensor outflow may be sent through a gas scrubbing device to remove the undesirable byproducts. If the scrubber also reduces the amount of chlorine dioxide in the sensor flow stream the sensor flow rate may be kept low to reduce the amount of chlorine dioxide lost in the scrubber.
- Figure 1 depicts an apparatus of the invention comprising a chlorine dioxide source, a target chamber, an air circulating device, and a valve.
- Figure 2 depicts the apparatus of Figure 1 further comprising a concentration sensor.
- Figure 3 depicts the apparatus of Figure 1 further comprising a concentration sensor in the target chamber.
- Figure 4 depicts the apparatus of Figure 2 further comprising a controller.
- Figure 5 depicts an apparatus of the invention comprising a chlorine dioxide source, a target chamber, two air circulating device, and a concentration sensor.
- Figure 6 depicts an apparatus of the invention comprising a chlorine dioxide source, a target chamber, an air circulating device, a concentration sensor, a gas scrubbing device and a valve.
- Figure 7 depicts an apparatus of the invention comprising a chlorine dioxide source, a target chamber, an air circulating device, a concentration sensor, an inlet, an outlet and a valve.
- Figure 8 is exemplary data of chlorine dioxide concentration vs. time from a testing using the invention.
- the instant invention provides methods and apparatus for controlling the concentration of chlorine dioxide in a target chamber.
- the invention utilizes chlorine dioxide generators described in, for example, US patent 7,534,398, US patent publication 2008/029507A1, or International patent application PCT/US2009/49924, all of which are incorporated herein by reference.
- These previously described chlorine dioxide generators can be used to create an aqueous solution of chlorine dioxide which can be the source of chlorine dioxide in the instant invention.
- an aqueous solution of chlorine dioxide may be made by other methods that are well known in the art. For example, chlorite and an acid may be combined with water to spontaneously generate an aqueous solution of chlorine dioxide.
- the target space or chamber to be treated is an enclosed, or partially enclosed, space that is to be disinfected, deodorized or otherwise treated with chlorine dioxide, by a targeted concentration profile over time of chlorine dioxide.
- the target chamber may be part of the apparatus or the target chamber may be connected to the apparatus. Examples of typical target spaces or chambers include filters, biological safety cabinets (BSCs), isolators, air handling equipment, and food and drug processing equipment.
- BSCs biological safety cabinets
- the target chamber may also be a series of elements in a system and/or connecting elements of a system such as a variety of chambers and the piping that connects the chambers.
- An exemplary concentration profile is 900 ppm for 60 min to reduce the bacterial population by 6 logs. A variety of other concentration profiles may be desired. Factors influencing concentration profiles are: target organisms, kill rates, time available for disinfection, and humidity level. Exemplary organisms include bacteria, bacterial spores, viruses and fungi.
- the chlorine dioxide sensor may be any of a variety of sensors.
- the sensing technology may be optical or ion-sensitive field effect transistor.
- the pump may be any kind of gas moving device.
- a diaphragm pump, a fan and a blower are examples of useful gas moving devices.
- the valve may be an on/off type or proportional type.
- the valve may be a needle valve. If the valve is an on/off type it may be pulse width modulated to control the flow.
- the controller may be any kind of devices capable of taking in a measurement signal and outputting a control signal.
- the controller could be a microcontroller or a programmable logic controller (PLC).
- the gas scrubber may, for example, be activated carbon matrices or work by bubbling gas through an aqueous solution that reacts with the undesirable byproducts.
- Figure 1 depicts exemplary apparatus 50 of the invention.
- the apparatus 50 comprises a chlorine dioxide source 1, a target chamber 4, an air circulating device 5, and a valve 7.
- the components are arranged so there are two gas flow loops.
- the first loop 12, includes the chlorine dioxide source 1, target chamber 4, and air circulating device 5.
- the second loop 13 includes the target chamber 4, the air circulating device 5 and the valve 7.
- the valve 5 may be set or adjusted to control the relative flow between the first loop 12 and the second loop 13 to control the concentration of chlorine dioxide in the target chamber 4.
- the valve 7 is adjusted to control the relative flow through the chlorine dioxide source 1 and through the target chamber 4.
- the flow in the target chamber 4 is high to maintain good mixing and distribution of the chlorine dioxide while the flow through the chlorine dioxide source 1 is relatively lower.
- the valve 5 is manually controlled to adjust the flow rate.
- Figure 2 depicts an exemplary apparatus 50 of the invention.
- the apparatus 50 further comprises a concentration sensor 2.
- the reading on the concentration sensor 2 may be used when setting or adjusting the valve to maintain a desired concentration of chlorine dioxide in the target chamber.
- the concentration sensor 2 may be located in a variety of places in the apparatus 50. For example, as in Figure 2, the concentration sensor 2 may be located next to the pump, or, for example, as in Figure 3, concentration sensor 2 may be located in the target chamber 4.
- Figure 3 depicts an exemplary apparatus 50 of the invention with an alternate arrangement of elements for the apparatus 50 shown in Figure 2.
- the concentration sensor 2 is shown in the target chamber 4.
- the valve 7 is shown in first loop 12.
- Figure 4 depicts an exemplary apparatus 50 of the invention.
- the apparatus 50 further comprise a controller 3.
- the controller 3 is electrically connected to the concentration sensor 2 and the three-way valve 6.
- the controller 3 will input the signal from the concentration sensor 2 and output a control signal to the three-way valve 6 to adjust the flow between the first loop 12 and the second Ioopl3.
- the controller is connected to the valve in alternate locations as shown in Figure 2 and Figure 3.
- FIG. 5 depicts an exemplary apparatus 50 of the invention.
- the apparatus 50 comprises a chlorine dioxide source 1, a target chamber 4, and two air circulating devices 5.
- the components are arranged so there are two gas flow loops.
- the first loop 12, includes the chlorine dioxide source 1, target chamber 4, and an air circulating device 5.
- the second loop 13 includes the target chamber 4, and the second air circulating device 5.
- the air circulating devices 5 may be set or adjusted to control the relative flow between the first loop 12 and the second loop 13 to control the concentration and mixing of chlorine dioxide in the target chamber 4.
- Figure 6 depicts an exemplary apparatus 50 of the invention.
- the apparatus 50 further comprise a slip stream loop 14.
- the concentration sensor 2 is located on the slip stream loop 14.
- a gas scrubber 10 is located on the slip stream loop 14.
- Figure 7 depicts an exemplary apparatus 50 of the invention.
- the apparatus 50 further comprises an inlet 8 and an outlet 11.
- the concentration sensor 2 is located on the outlet 11.
Abstract
The instant invention provides apparatus and methods for controlling the concentration of chlorine dioxide in a chamber.
Description
APPARATUS AND METHODS FOR CONTROLLING CHOLORINE DIOXIDE
CONCENTRATION
RELATED APPLICATIONS
This application claims the benefit of US Provisional Application No.: 61/201,858, filed December 15, 2008, the contents of which are hereby incorporated herein by reference.
FIELD OF THE INVENTION
The present invention relates to methods and apparatuses for controlling chlorine dioxide concentration in an enclosed or partially enclosed space.
BACKGROUND OF THE INVENTION Chlorine dioxide was discovered in the early 1800's, and was adopted by commerce in the
United States in the 1940's. Chlorine dioxide has been called the ideal biocide and the ability of chlorine dioxide to reduce or eliminate viable microbes, e.g., bacteria, viruses, fungi, mold spores, algae and protozoa, is well-documented and well known. See, for example, Franklin, CL. et al.
(1991) Am Vet Med Assoc 198:1625-30; Korich K. G., et al. (1990) Appl Environ Microbiol. 56:1423-8; Boddie et al. (2000) J Dairy Sci. 83:2975-9; Lee et al. (2004) J Food Prot. 67:1371-
6; Han et al. (2003) J Environ Health 66: 16-21; Sy et al. (2005) J Food Prot. 68:1 176-87; and
LeChevallier M.W. et al. (1988) Appl Environ Microbiol. 54:2492-9.
It is believed that chlorine dioxide inactivates microorganisms by oxidizing key components of a micro-organism's membrane proteins that are vital to the membrane's structure and function. Also, the oxidizing reaction that causes microorganism inactivation does not form trihalomethanes
(THMs) orhaloacetic acids (HAAs).
Approvals and registrations for use of chlorine dioxide in a wide variety of applications have been granted by the EPA, FDA and USDA, and such approvals and registrations have led to an increasing adoption of the use of chlorine dioxide.
There are many reasons for the ongoing expansion of chlorine dioxide use including its effectiveness against microorganisms at very low concentrations.
A major limitation to the use of chlorine dioxide is that chlorine dioxide can not be manufactured in bulk at an industrial gas plant and shipped to final use destinations. Accordingly, chlorine dioxide must be generated on-site.
The use of chlorine dioxide in large scale applications is well known, however, the use of chlorine dioxide in small scale applications has not been widely adopted. The lack of adoption in small scale applications is a result of the limitations in the prior art with respect to the cost, speed, size and user friendly generation of chlorine dioxide in sufficient concentration and purity to be useful. However, there are many small scale applications that would benefit from the use of chlorine dioxide as a disinfectant or sanitizing agent.
Apparatus and methods for controlling the concentration of chlorine dioxide would be beneficial for disinfection in a variety of applications including biosafety cabinets, isolators, filters, air handling equipment, food and drug processing equipment, etc.
Description of the invention
The instant invention provides apparatus and methods for controlling the concentration of chlorine dioxide in a space, e.g., biosafety cabinets, isolators, filters, air handling equipment, food and or drug processing equipment. In one embodiment, the instant invention comprises an apparatus comprising a source of chlorine dioxide, a target chamber to be treated, one or more pumps, and at least two paths connecting elements of this system. The system may also comprise one or more valves. The system may also comprise a chlorine dioxide concentration sensor.
The source of chlorine dioxide may be, for example, an aqueous solution as made by a variety of chlorine dioxide generating processes. For example, mixing citric acid with sodium chlorite in water will spontaneously produce a solution of chlorine dioxide.
- ? -
In various embodiments of the invention, the valve(s) and/or pump(s) are arranged in the system in such a way that adjusting them controls the amount of gas circulated in the two loops and the concentration of chlorine dioxide in a target chamber. Figures 1-7 show a variety of useful arrangements of pumps, valves and sensor locations. The flow loop that contains the target chamber, but not the chlorine dioxide source is typically run at a higher gas flow rate than the flow loop that flows through the chlorine dioxide source. This higher flow rate maintains a more
dioxide concentration in the target chamber by increased mixing in the target chamber and therefore minimizing gradient effects due to chlorine dioxide losses in the target chamber or system. Chlorine dioxide losses may be due to, for example, leaks in the system, reaction with the chlorine dioxide by elements in the target chamber or system, or by absorption of the chlorine dioxide by elements in the target chamber or system. The flow of gas that goes through the chlorine dioxide source is set to control the amount of chlorine dioxide that enters the target chamber so the desired concentration profile can be generated in the target chamber. The flow of gas through the chlorine dioxide chamber may be fixed, controlled manually by an operator or controlled automatically. The flow of gas through the chlorine dioxide chamber may be controlled in response to the reading on the chlorine dioxide concentration sensor either manually or automatically. If the flow is controlled automatically, feedback control well known in the art, such as PID control, may be used. The sensor may be located in a slip stream with a different flow rate than the main circulation loop. In optical chlorine dioxide concentration sensors the light, typically in the ultraviolet range, may breakdown the chlorine dioxide into undesirable byproducts. These byproducts may include the hypochlorite ion. These byproducts may cause corrosion or other
deleterious effects to elements of the system. A lower flow through the sensor may be used to reduce the amount of byproducts. Furthermore, the sensor outflow may be vented to prevent byproducts from returning to the system. In this case the sensor flow may be lower to reduce the amount of chlorine dioxide gas lost from the system. If the outflow is vented there must also be an inlet to avoid developing too much negative pressure in the apparatus and target chamber.
The sensor outflow may be sent through a gas scrubbing device to remove the undesirable byproducts. If the scrubber also reduces the amount of chlorine dioxide in the sensor flow stream the sensor flow rate may be kept low to reduce the amount of chlorine dioxide lost in the scrubber. Brief Description of the Drawings
Figure 1 depicts an apparatus of the invention comprising a chlorine dioxide source, a target chamber, an air circulating device, and a valve.
Figure 2 depicts the apparatus of Figure 1 further comprising a concentration sensor.
Figure 3 depicts the apparatus of Figure 1 further comprising a concentration sensor in the target chamber.
Figure 4 depicts the apparatus of Figure 2 further comprising a controller.
Figure 5 depicts an apparatus of the invention comprising a chlorine dioxide source, a target chamber, two air circulating device, and a concentration sensor.
Figure 6 depicts an apparatus of the invention comprising a chlorine dioxide source, a target chamber, an air circulating device, a concentration sensor, a gas scrubbing device and a valve.
Figure 7 depicts an apparatus of the invention comprising a chlorine dioxide source, a target chamber, an air circulating device, a concentration sensor, an inlet, an outlet and a valve.
Figure 8 is exemplary data of chlorine dioxide concentration vs. time from a testing using the invention.
Detailed Description The instant invention provides methods and apparatus for controlling the concentration of chlorine dioxide in a target chamber.
In exemplary embodiments the invention utilizes chlorine dioxide generators described in, for example, US patent 7,534,398, US patent publication 2008/029507A1, or International patent application PCT/US2009/49924, all of which are incorporated herein by reference. These previously described chlorine dioxide generators can be used to create an aqueous solution of chlorine dioxide which can be the source of chlorine dioxide in the instant invention. Alternatively, an aqueous solution of chlorine dioxide may be made by other methods that are well known in the art. For example, chlorite and an acid may be combined with water to spontaneously generate an aqueous solution of chlorine dioxide. The target space or chamber to be treated is an enclosed, or partially enclosed, space that is to be disinfected, deodorized or otherwise treated with chlorine dioxide, by a targeted concentration profile over time of chlorine dioxide. The target chamber may be part of the apparatus or the target chamber may be connected to the apparatus. Examples of typical target spaces or chambers include filters, biological safety cabinets (BSCs), isolators, air handling equipment, and food and drug processing equipment. The target chamber may also be a series of elements in a system and/or connecting elements of a system such as a variety of chambers and the piping that connects the chambers. An exemplary concentration profile is 900 ppm for 60 min to reduce the bacterial population by 6 logs. A variety of other concentration profiles may
be desired. Factors influencing concentration profiles are: target organisms, kill rates, time available for disinfection, and humidity level. Exemplary organisms include bacteria, bacterial spores, viruses and fungi.
The chlorine dioxide sensor may be any of a variety of sensors. For example, the sensing technology may be optical or ion-sensitive field effect transistor.
The pump may be any kind of gas moving device. A diaphragm pump, a fan and a blower are examples of useful gas moving devices.
The valve may be an on/off type or proportional type. For example, the valve may be a needle valve. If the valve is an on/off type it may be pulse width modulated to control the flow. The controller may be any kind of devices capable of taking in a measurement signal and outputting a control signal. For example, the controller could be a microcontroller or a programmable logic controller (PLC).
The gas scrubber may, for example, be activated carbon matrices or work by bubbling gas through an aqueous solution that reacts with the undesirable byproducts. Figure 1 depicts exemplary apparatus 50 of the invention. The apparatus 50 comprises a chlorine dioxide source 1, a target chamber 4, an air circulating device 5, and a valve 7. The components are arranged so there are two gas flow loops. The first loop 12, includes the chlorine dioxide source 1, target chamber 4, and air circulating device 5. The second loop 13 includes the target chamber 4, the air circulating device 5 and the valve 7. The valve 5 may be set or adjusted to control the relative flow between the first loop 12 and the second loop 13 to control the concentration of chlorine dioxide in the target chamber 4.
The valve 7 is adjusted to control the relative flow through the chlorine dioxide source 1 and through the target chamber 4. In one aspect of the invention the flow in the target chamber 4
is high to maintain good mixing and distribution of the chlorine dioxide while the flow through the chlorine dioxide source 1 is relatively lower. In one aspect of the invention the valve 5 is manually controlled to adjust the flow rate.
Figure 2 depicts an exemplary apparatus 50 of the invention. As depicted in Figure 2 the apparatus 50 further comprises a concentration sensor 2. The reading on the concentration sensor 2 may be used when setting or adjusting the valve to maintain a desired concentration of chlorine dioxide in the target chamber. The concentration sensor 2 may be located in a variety of places in the apparatus 50. For example, as in Figure 2, the concentration sensor 2 may be located next to the pump, or, for example, as in Figure 3, concentration sensor 2 may be located in the target chamber 4.
Figure 3 depicts an exemplary apparatus 50 of the invention with an alternate arrangement of elements for the apparatus 50 shown in Figure 2. The concentration sensor 2 is shown in the target chamber 4. The valve 7 is shown in first loop 12.
Figure 4 depicts an exemplary apparatus 50 of the invention. As depicted in Figure 4 the apparatus 50 further comprise a controller 3. In one aspect of the invention the controller 3 is electrically connected to the concentration sensor 2 and the three-way valve 6. The controller 3 will input the signal from the concentration sensor 2 and output a control signal to the three-way valve 6 to adjust the flow between the first loop 12 and the second Ioopl3. In a related embodiment, not shown, the controller is connected to the valve in alternate locations as shown in Figure 2 and Figure 3.
Figure 5 depicts an exemplary apparatus 50 of the invention. The apparatus 50 comprises a chlorine dioxide source 1, a target chamber 4, and two air circulating devices 5. The components are arranged so there are two gas flow loops. The first loop 12, includes the
chlorine dioxide source 1, target chamber 4, and an air circulating device 5. The second loop 13 includes the target chamber 4, and the second air circulating device 5. The air circulating devices 5 may be set or adjusted to control the relative flow between the first loop 12 and the second loop 13 to control the concentration and mixing of chlorine dioxide in the target chamber 4.
Figure 6 depicts an exemplary apparatus 50 of the invention. As depicted in Figure 6 the apparatus 50 further comprise a slip stream loop 14. In one embodiment of the invention the concentration sensor 2 is located on the slip stream loop 14. In a related embodiment of the invention a gas scrubber 10 is located on the slip stream loop 14. Figure 7 depicts an exemplary apparatus 50 of the invention. As depicted in Figure 7 the apparatus 50 further comprises an inlet 8 and an outlet 11. In one embodiment of the invention the concentration sensor 2 is located on the outlet 11.
Claims
1. An apparatus for controlling the concentration of chlorine dioxide gas in a target chamber comprising,
a chlorine dioxide source,
a gas moving device,
a valve,
a first flow path that includes the chlorine dioxide source, and
a second flow path that does not include the chlorine dioxide source.
2. The apparatus of claim 1, further comprising a sensor.
3. The apparatus of claim 2, further comprising a controller.
4. The apparatus of claim 3, where the controller maintains a concentration of chlorine dioxide to deliver controlled dosage.
5. The apparatus of claim 4, wherein the controlled dosage is 50 ppm-min to 60,000 ppm- min to the target chamber.
6. The apparatus of claim 4, where the controller maintains a controlled concentration of chlorine dioxide for a controlled period of time.
7. The apparatus of claim 1, wherein the chlorine dioxide source is an aqueous solution of chlorine dioxide.
8. The apparatus of claim 1 , wherein the air moving device is a diaphragm pump, a fan or a blower.
9. The apparatus of claim 1 , wherein the sensor is an optical sensor.
10. The apparatus of claim 1 , wherein the valve is a proportional valve.
11. The apparatus of claim 1 , wherein the valve is a 3-way valve.
12. The apparatus of claim 2, further comprising a third flow path.
13. The apparatus of claim 12, wherein the concentration sensor is located in the third path.
14. The apparatus of claim 13, further comprising a gas scrubber.
15. The apparatus of claim 1, further comprising a gas inlet and a gas outlet.
16. The apparatus of claim 15, further comprising a gas scrubber.
17. An apparatus for controlling the concentration of chlorine dioxide gas in a target chamber comprising,
a chlorine dioxide source,
a gas moving device, a second gas moving device,
a flow path that does not include the chlorine dioxide source, and
a second flow path that does include the chlorine dioxide source.
18. The apparatus of claim 17, further comprising a sensor.
19. The apparatus of claim 18, further comprising a controller.
20. The apparatus of claim 19, where the controller maintains a concentration as a function of time of chlorine dioxide to deliver a controlled dosage to the target chamber.
21. The apparatus of claim 20, where the controller maintains a controlled concentration of chlorine dioxide.
22. The apparatus of claim 21, wherein the chlorine dioxide source is an aqueous solution of chlorine dioxide.
23. The apparatus of claim 51 , wherein at least one of the air moving devices is a diaphragm pump.
24. The apparatus of claim 17, wherein the sensor is an optical sensor.
25. The apparatus of claim 17, wherein the valve is a proportional valve
26. The apparatus of claim 17, wherein the valve is a 3-way valve.
27. The apparatus of claim 18, further comprising a third flow path.
28. The apparatus of claim 27, wherein the concentration sensor is located in the third path.
29. The apparatus of claim 28, further comprising a gas scrubber.
30. The apparatus of claim 17, further comprising a gas inlet and a gas outlet.
31. The apparatus of claim 30, further comprising a gas scrubber.
32. A method for controlling the concentration of chlorine dioxide gas in a target chamber comprising, providing the apparatus of any one of claims 1-31, and
starting the apparatus;
thereby controlling the concentration of chlorine dioxide in a chamber.
33. The method of claim 32, wherein the valve is adjusted to control the concentration of chlorine dioxide.
34. The method of claim 32, wherein the controller is set to control the concentration of chlorine dioxide
35. The method of claim 32, wherein the target chamber is a filter.
36. The method of claim 32, wherein the target chamber further comprises an element to be disinfected.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US20185808P | 2008-12-15 | 2008-12-15 | |
US61/201,858 | 2008-12-15 |
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WO2010077862A3 WO2010077862A3 (en) | 2010-10-14 |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5409978B1 (en) * | 2013-06-18 | 2014-02-05 | 株式会社Fmi | Chlorine dioxide gas treatment structure, chlorine dioxide gas treatment device, sterilization device and environmental purification device |
EP2468806B1 (en) * | 2010-12-21 | 2017-09-13 | L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Method for functionalizing a container and device for carrying out this method and corresponding container |
WO2021224673A1 (en) * | 2020-05-05 | 2021-11-11 | CO2Apps S.R.L. | Substance and method for preventing the transmission of viruses in the respiratory system |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4128454A (en) * | 1977-12-07 | 1978-12-05 | Ingersoll-Rand Co. | System and method for gas phase pulp bleaching |
US4311485A (en) * | 1980-12-23 | 1982-01-19 | E. I. Du Pont De Nemours And Company | Method and apparatus for photometrically monitoring the concentrations of both chlorine and chlorine dioxide |
EP0847759A2 (en) * | 1996-12-12 | 1998-06-17 | Johnson & Johnson | Optical measurement system for sterilising gas |
US6042802A (en) * | 1997-10-15 | 2000-03-28 | Medivators Inc. | Method and apparatus for generating and using chlorine dioxide |
US20030229422A1 (en) * | 2002-06-11 | 2003-12-11 | Vulcan Chemicals | Chlorine dioxide generation systems |
-
2009
- 2009-12-15 WO PCT/US2009/068050 patent/WO2010077862A2/en active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4128454A (en) * | 1977-12-07 | 1978-12-05 | Ingersoll-Rand Co. | System and method for gas phase pulp bleaching |
US4311485A (en) * | 1980-12-23 | 1982-01-19 | E. I. Du Pont De Nemours And Company | Method and apparatus for photometrically monitoring the concentrations of both chlorine and chlorine dioxide |
EP0847759A2 (en) * | 1996-12-12 | 1998-06-17 | Johnson & Johnson | Optical measurement system for sterilising gas |
US6042802A (en) * | 1997-10-15 | 2000-03-28 | Medivators Inc. | Method and apparatus for generating and using chlorine dioxide |
US20030229422A1 (en) * | 2002-06-11 | 2003-12-11 | Vulcan Chemicals | Chlorine dioxide generation systems |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2468806B1 (en) * | 2010-12-21 | 2017-09-13 | L'Air Liquide Société Anonyme pour l'Etude et l'Exploitation des Procédés Georges Claude | Method for functionalizing a container and device for carrying out this method and corresponding container |
JP5409978B1 (en) * | 2013-06-18 | 2014-02-05 | 株式会社Fmi | Chlorine dioxide gas treatment structure, chlorine dioxide gas treatment device, sterilization device and environmental purification device |
WO2014203319A1 (en) * | 2013-06-18 | 2014-12-24 | 株式会社Fmi | Chlorine dioxide gas treatment structure, chlorine dioxide gas treatment device, sterilization device, and environment cleaning device |
WO2021224673A1 (en) * | 2020-05-05 | 2021-11-11 | CO2Apps S.R.L. | Substance and method for preventing the transmission of viruses in the respiratory system |
Also Published As
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