The disclosure relates to systems, devices, and methods for purifying fluids. More specifically, this disclosure relates to systems, devices, and methods for removing or degrading contaminants from fluid streams such as flue gas streams and industrial exhaust streams.
Air purification is important in industrial facilities where the emission of airborne pollutants may have a significant impact on the environment, health, and safety of employees and neighboring communities. Traditional air purification methods, such as mechanical filtration and chemical scrubbers, have been utilized to control the release of particulate matter, volatile organic compounds, and other harmful substances from industrial processes. However, these methods often suffer from limitations in efficiency, maintenance requirements, and environmental footprint.
Industrial businesses require air purification systems that may operate efficiently and reliably in harsh conditions in order to neutralize a broad spectrum of contaminants. Furthermore, air purification systems must adhere to rigorous safety standards.
Described herein are various systems, devices, and methods for purifying and deodorizing various fluids, such as contaminated air. Although various the implementations described herein are described with air being the fluid to be used with the system, this is in no way intended to be restrictive and other fluids may be used with the system, as would be understood by those of skill in the art. Many other fluids, such as flue gas, petrochemical gases, steam, and similar fluids could be purified without departing from the scope of this disclosure.
Disclosed herein are systems, devices, and methods for purifying and deodorizing while also providing for increased ease of maintenance, increased containment of potentially harmful intermediates, and increased scalability to treat larger volumes of contaminated fluids.
Example 1 relates to a fluid purification system comprising a housing open at each end through which a fluid is able to pass, and a cassette within the housing comprising a plurality of lamps capable of emitting light, wherein the cassette is removable from the housing.
Example 2 relates to Examples 1 and 3-7, further comprising a plurality of ballasts capable of supplying electricity to the plurality of lamps.
Example 3 relates to Examples 1-2 and 4-7, wherein the lamps emit light in the ultraviolet wavelength band.
Example 4 relates to Examples 1-3 and 5-7, wherein the light in the ultraviolet wavelength band breaks down contaminants in the fluid.
Example 5 relates to Examples 1-4 and 6-7, wherein the light in the ultraviolet wavelength band generates ozone in the fluid.
Example 6 relates to Examples 1-5 and 7, further comprising an ozone monitor capable of detecting an ozone amount in the fluid, wherein the plurality of ballasts and plurality of lamps are configured to vary the amount of ultraviolet light emitted based on the ozone amount detected.
Example 7 relates to Examples 1-6, wherein a detected ozone amount in the fluid below a lower threshold causes the plurality of ballasts and plurality of lamps to increase the amount of ultraviolet light emitted and a detected ozone amount in the fluid above an upper threshold causes the plurality of ballasts and plurality of lamps to decrease the amount of ultraviolet light emitted.
Example 8 relates to a fluid purification system comprising a housing with a first end and a second end through which a fluid is able to pass from the first end to the second end, a cassette within the housing comprising a plurality of lamps capable of spurring the generation of ozone, a backflow damper disposed within the housing at the first end of the housing capable of allowing, restricting, and stopping the passage of fluid through the housing, and a makeup air damper disposed proximal to the first end of the housing capable of allowing, restricting, and stopping the passage of fluid through the housing, wherein the cassette is removable from the housing.
Example 9 relates to Examples 8 and 10-14, further comprising a plurality of ballasts capable of supplying electricity to the plurality of lamps.
Example 10 relates to Examples 8-9 and 11-14, further comprising an ozone monitor capable of detecting an ozone amount in the fluid.
Example 11 relates to Examples 8-10 and 12-14, further comprising an airflow sensor capable of measuring the flow of the fluid though the housing.
Example 12 relates to Examples 8-11 and 13-14, wherein the backflow damper is configured to close based upon the measured fluid flow by the airflow sensor.
Example 13 relates to Examples 8-12 and 14, further comprising a temperature probe positioned in the housing to measure the temperature of the fluid
Example 14 relates to Examples 8-13, wherein the makeup air damper is configured to adjust its position based on the temperature of the fluid.
Example 15 relates to a fluid purification system comprising a housing with a first end and a second end wherein a fluid is able to pass from the first end to the second end, a cassette within the housing comprising a plurality of lamps capable of spurring the generation of ozone, and a flow restrictor within the housing positioned between the cassette and the second end of the housing, wherein the cassette is removable from the housing, and wherein the flow restrictor increases the time needed for fluid to pass through the housing.
Example 16 relates to Examples 15 and 17-20, wherein the flow restrictor is one or more adjustable flow promoters.
Example 17 relates to Examples 15-16 and 18-20, wherein the flow restrictor is a plurality of baffles.
Example 18 relates to Examples 15-17 and 19-20, wherein the lamps emit light in the ultraviolet wavelength band.
Example 19 relates to Examples 15-18 and 20, further comprising an ozone monitor capable of detecting ozone in the fluid.
Example 20 relates to Examples 15-19, wherein the lamps are configured to emit more or less ultraviolet wavelength light based on the ozone detected in the fluid.
While multiple embodiments are disclosed, still other embodiments of the disclosure will become apparent to those skilled in the art from the following detailed description, which shows and describes illustrative embodiments of the disclosed system, devices, and methods. As will be realized, the disclosed system, devices, and methods are capable of modifications in various obvious aspects, all without departing from the spirit and scope of the disclosure. Accordingly, the drawings and detailed description are to be regarded as illustrative in nature and not restrictive.
The various implementations disclosed and contemplated herein relate to various devices, systems, and methods for purifying and deodorizing air. Various implementations use light with wavelengths in or around the ultraviolet spectrum (UV), optionally UV-C, to directly and indirectly break down air impurities by forming ozone, which breaks down the air impurities by oxidizing the molecules, as would be generally understood. Various implementations may contain a variety of process control and safety features to ensure efficient and safe operation of the system, such as temperature monitoring, ozone containment systems, airflow monitoring, and active interlocks.
The system described herein may be used for air purification applications and the like as would be appreciated by those of skill in the art in light of this disclosure. Various implementations include the use of the system in purifying and deodorizing the air of industrial cooking operations, restaurant kitchens, rendering plants, waste incineration facilities, fermentation facilities, and various other facilities that produce unpleasant volatile compounds. Various additional applications are possible and contemplated herein.
Various industries emit or produce fluids with contaminants that may be harmful to people, animals, and the environment and/or may carry undesirable smells. Examples of harmful chemicals emitted or produced in these fluid streams include nitrogen oxides, carbon monoxide, carbon dioxide, sulfur oxides, methane, and ammonia, among others, which are common in flue gas streams from burn facilities and petrochemical facilities. Examples of contaminants with undesirable smells include polycyclic aromatic hydrocarbons, nitrated polycyclic aromatic hydrocarbons, aldehydes, and aromatic amines, among others, which are often found as gaseous or vaporous emissions of industrial frying operations.
In various implementations, the system 100 has an inlet duct 12 and an outlet duct 14, on opposite ends of the housing 10. The inlet duct 12 and outlet duct 14 are open such that air or other fluids may flow through the inlet duct 12 into the lumen of the housing 10 and out of the outlet duct 14. Fluid flows from the inlet duct 12 to the outlet duct 14 via a channel 16 through the housing 10. In certain implementations, the inlet duct 12 and outlet duct 14 have tapered sections that adjust diameter of the channel 16, when the diameter of the inlet duct 12, outlet duct 14, and the housing 10 are different.
In certain implementations, near the inlet duct 12, the system 100 includes a temperature probe 18. In various implementations, the temperature probe 18 may be a thermocouple, resistance temperature detector (RTD), thermistor, semiconductor based integrated circuit (IC), or any other device for measuring temperature known in the art. Optionally, the temperature probe 18 is mounted with the sensing end inserted through the inlet duct 12 or housing 10 such that it may measure the temperature of the fluid in the channel 16, but with other components, such as electronic components, mounted outside of the housing 10 or inlet duct 12. In some implementations, a thermowell may be mounted in the inlet duct 12, which allows the temperature probe 18 to measure the temperature of the fluid in the channel 16 without being in direct contact with the fluid. As shown in
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In various implementations, the opening or closing of the backflow damper 22 is done by an output signal sent from the PLC 20; the control may be manual, automatic, or semiautomatic. In some implementations, the backflow damper 22 has a position feedback sensor 23, shown in
As would be understood, dust buildup, corrosion, loss of utilities, and other outside factors may compromise the ability for the backflow damper 22 to actuate despite an output signal being sent from the PLC 20 to adjust the position of the backflow damper 22, and as such a position feedback sensor 23 signal may indicate the actual position of the backflow damper 22 in real-time or near real-time. In various implementations, the backflow damper 22 is in electronic communication with the PLC 20 for one or more of the purposes of actuation and position feedback.
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As dust buildup, corrosion, loss of utilities, and other outside factors compromise the ability for the makeup air damper 24 to actuate despite an output signal being sent from the PLC 20 to adjust the position of the makeup air damper 24, the position feedback sensor 25 may provide an actual position of the makeup air damper 24 in real-time or near real-time. In various implementations, the makeup air damper 24 is in electronic communication with the PLC 20 for one or more of the purposes of actuation and position feedback.
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In various implementations, the PLC 20 will monitor the temperature of the tempering chamber 26 through the signal received from the temperature probe 28 and send output signals to actuate the makeup air damper 24 and/or the backflow damper 22 based on the temperature of the tempering chamber 26. In some implementations, the PLC 20 will be programmed to keep the tempering chamber 26 at a set temperature, optionally about 120° F. In certain implementations, the temperature in the tempering chamber 26 is modulated by the PLC 20 sending an output signal to the makeup air damper 24 and/or backflow damper 22 to open or close to adjust air flow as necessary. In a more specific example, when the temperature of the tempering chamber 26 is above the set temperature (optionally about 120° F.) the PLC 20 signal the makeup air damper 24 to become more open to draw in more cool air to decrease the temperature. Additionally or alternatively, the PLC 20 may signal the backflow damper 22 to become more closed to decrease the amount of warm air entering the tempering chamber 26 thereby reducing the temperature.
Continuing with this specific example, when the temperature of the tempering chamber 26 is below the set temperature (optionally about 120° F.) the PLC 20 may send a signal to the makeup air damper 24 to become more closed/restrict air flow and/or to the backflow air damper to become more open/allow increased air flow to increase temperature in the tempering chamber 26.
In another example, if the position feedback of the makeup air damper 24 indicates it is completely open or otherwise allowing the maximum amount of air into the tempering chamber 26, but the temperature of the tempering chamber 26 continues to remain above the set temperature (optionally about 120° F.), the PLC 20 may send an output signal to the backflow damper 22 instructing it to close, either completely or partially.
It would be understood in the art that the set temperature (optionally 120° F.) may be selected to reduce thermal degradation of components of the system 100, and that various target temperatures could be selected, depending on component temperature ratings.
In various implementations, a primary reaction chamber 30 is within the housing 10 and optionally proximal to the tempering chamber 26. The primary reaction chamber 30 may have a plurality of ballasts 32 (shown best in
In some implementations, such as are shown in
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In some implementations, the cabinet 36 has doors 38 that allow for access, such as for maintenance. Shown in
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In one specific example, the target cabinet 36 operating temperature is about 105° F. or below. It would be understood in the art that the temperature 105° F. would be selected to reduce thermal degradation of components of the system 100 in the cabinet 36, and that various other target temperatures could be selected, depending on component temperature ratings or other variables as would be understood.
In alternative implementations, such as shown in
In some implementations, shown in
A cassette 44, according to one implementation, may be seen in
In various implementations, the vertical plates 46 have a plurality of mounts 50 that are configured to hold one or more ends of the lamps 34, such that the lamps 34 are supported by the mounts 50 and the vertical plates 46. In some implementations, the mounts 50 are configured to allow electrical connectivity between the lamps 34 and the ballasts 32 when the lamps are mounted in the mounts 50. In such implementations, the mounts 50 are electrically connected to the ballasts 32 and possess a conductive element that allows electrical current from the ballasts 32 to pass through the mounts 50 into the lamps 34. In some implementations, the mounts 50 are formed from or possess a flexible polymer material that creates an air-tight seal with the cassette 44. According to some implementations, the flexible polymer material may be EPDM, PTFE, Buna-N, SBR, polyethylene, polypropylene, FKM, or any other polymer, material, or combination of materials that would be considered viable as an alternative in the art.
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In various implementations, the fluid passing through the channel 16, especially when passing through the portion of the channel 16 within the primary reaction chamber 30, is permeated by the light emitted by the lamps 34. In such implementations, the light emitted may be UV light, and the light may directly contact contaminants in the fluid.
In various implementations, the contaminants may be, but are not limited to, volatile organic compounds (VOCs) which may break down when the light directly contacts them.
In some implementations, the fluid may contain molecular oxygen (O2). In such implementations, when the light contacts the molecular oxygen in the fluid, the light may break the O2 molecule into two independent oxygen atoms. These oxygen atoms may then react with other nearby O2 molecules to produce ozone. The produced ozone molecules may then react with contaminants in the fluid, causing breakdown through oxidation. In some implementations, the light emitted from the lamps 34 breaks down contaminants in the fluid through both direct UV contact and ozone oxidation.
In various implementations, ozone formed in the primary reaction chamber 30 flows with the fluid passing through the channel 16 before reacting with other compounds, such as contaminants in the fluid.
As would be understood, ozone, in excessive concentrations, may be harmful to humans, animals, the environment, and objects prone to oxidation. Returning to
In some implementations, there is a temperature probe 58 positioned to measure the temperature of the fluid in the channel 16 as it leaves the primary reaction chamber 30 and enters the secondary reaction chamber 52. In various implementations, the temperature probe 58 is configured in relation to the PLC 20 and other devices in the same manner as the temperature probe 18 in the inlet duct 12 and temperature probe 28 in the tempering chamber 26 described above.
In various implementations, the PLC 20 will monitor the temperature of the fluid as detected by the temperature probe 58. In some implementations, if the temperature as measured by the temperature probe 58 has increased above a threshold value, determined by the temperature ratings of the lamps 34 or other equipment, the PLC 20 will send an output signal to the ballasts 32 to cease sending electrical current to the lamps 34. Various alternative devices and systems may be implemented to cool the fluid if the temperature exceeds the threshold temperature for operation.
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In some implementations, the system 100 may include an airflow sensor 62. The airflow sensor 62 may be configured to measure fluid flow through the channel 16. The airflow sensor 62 is optionally mounted within the cabinet 36, but may be mounted in a variety of locations as would be understood in the art. The airflow sensor 62 may be a differential pressure sensor, a turbine flow sensor, a vortex flow meter, a cup anemometer, a vane anemometer, a hot-wire anemometer, or any other sensor or meter that would be understood in the art.
In various implementations, the airflow sensor 62 is in electronic communication with the PLC. In some implementations, if the airflow sensor 62 measures fluid flow through the channel 16 that is sufficiently low, the PLC will send an output signal to the ballasts 32 to shut off electrical power to the lamps 34, such that ozone generation will cease if airflow is stopped or sufficiently slowed.
In various implementations, one or more gas detection probes 64 may be mounted in the housing 10. These gas detection probes 64 may be configured to detect a variety of products, byproducts, pollutants, or contaminants, as may be required by the application. These gases could include, but are not limited to, polycyclic aromatic hydrocarbons, nitrated polycyclic aromatic hydrocarbons, aldehydes, aromatic amines, nitrogen oxides, carbon monoxide, carbon dioxide, sulfur oxides, methane, ammonia, and various other gaseous compounds. In certain implementations, the gas detection probes 64 are in electronic communication with the PLC 20 to allow for reporting and data recording, as would be appreciated.
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In some implementations, the PLC 20 and other control equipment is housed in a control cabinet 68, optionally physically separate from the housing 10 and optionally mounted on the trailer 66. The control cabinet 68 may optionally have a human-machine-interface (HMI) located on its exterior or interior for human interaction with the system 100 such as inputting various temperatures, controls, or other values. The HMI may also allow for system overrides, manual control, and other features as would be understood.
In various implementations, the PLC 20, ballasts 32, and other electronic devices are rated at about 15% above their voltage and current requirements. The system 100 may also possess fan 70 to move the fluid through the channel 16.
In various implementations, the control cabinet 68, as well as other locations of the system 100, may have a main power disconnect that allows for disconnecting all power to the system 100 from external power sources, as well as the optional application of a safety lock to ensure power stays disconnected. The control cabinet 68, as well as other locations of the system 100, may have various emergency stops. These emergency stops may function to disconnect power to certain equipment, disconnect power to all equipment, or begin a particular shutdown sequence that is programmed into the PLC 20.
In some implementations, the system 100 may implement a fire alarm management system. The fire alarm management system may use various fire detection methods known in the art, such as ionization smoke detectors, photoelectric smoke detectors, thermistor heat detectors, electromagnetic flame detectors, or other equivalent fire detection methods. The fire alarm management system may use various devices and methods for fire suppression, such as the use of dry chemical fire suppressants, sprinklers, carbon dioxide, foam fire suppressants, and other fire suppression methods known in the art. Various implementations include the deployment of the fire suppression methods inside the housing 10 or outside of the housing 10, depending on the application and local requirements.
In some implementations, such as those shown in
As best seen in
In some implementations, the secondary reaction chamber 54 does not include baffles. Optionally, the secondary reaction chamber 54 has one or more adjustable flow promoters 80. As best seen in
In various implementations, the adjustable flow promoters 80, baffles 56, or other equivalent technology may be called a flow restrictor.
In various implementations, each actuated plate 84 may be actuated vertically or horizontally relative to the corresponding stationary plate 82 by a plate actuator 86, shown in
In some implementations, the system 100 may have one or more housings 10 functioning in tandem.
Although the disclosure has been described with reference to preferred implementations, persons skilled in the art will recognize that changes may be made in form and detail without departing from the spirit and scope of the disclosed apparatus, systems, and methods.
This application claims the benefit under 35 U.S.C. § 119 (e) to U.S. Provisional Application 63/604,522, filed Nov. 30, 2023, and entitled “SYSTEM TO PURIFY AND DEODORIZE FLUIDS AND ASSOCIATED DEVICES AND METHODS”, which is hereby incorporated herein by reference in its entirety for all purposes.
| Number | Date | Country | |
|---|---|---|---|
| 63604522 | Nov 2023 | US |