US20030015413A1 - Photo-remediation of no2 plume - Google Patents

Photo-remediation of no2 plume Download PDF

Info

Publication number
US20030015413A1
US20030015413A1 US09/898,737 US89873701A US2003015413A1 US 20030015413 A1 US20030015413 A1 US 20030015413A1 US 89873701 A US89873701 A US 89873701A US 2003015413 A1 US2003015413 A1 US 2003015413A1
Authority
US
United States
Prior art keywords
exhaust gas
photo
illumination source
exhaust
wavelength
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
US09/898,737
Other versions
US6495108B1 (en
Inventor
Bruce Rising
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Siemens Energy Inc
Original Assignee
Siemens Westinghouse Power Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Siemens Westinghouse Power Corp filed Critical Siemens Westinghouse Power Corp
Priority to US09/898,737 priority Critical patent/US6495108B1/en
Assigned to SIEMENS WESTINGHOUSE POWER CORPORATION reassignment SIEMENS WESTINGHOUSE POWER CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: RISING, BRUCE
Application granted granted Critical
Publication of US6495108B1 publication Critical patent/US6495108B1/en
Publication of US20030015413A1 publication Critical patent/US20030015413A1/en
Assigned to SIEMENS POWER GENERATION, INC. reassignment SIEMENS POWER GENERATION, INC. CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: SIEMENS WESTINGHOUSE POWER CORPORATION
Assigned to SIEMENS ENERGY, INC. reassignment SIEMENS ENERGY, INC. CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: SIEMENS POWER GENERATION, INC.
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/54Nitrogen compounds
    • B01D53/56Nitrogen oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/80Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
    • B01D2259/804UV light

Definitions

  • This invention relates to a method for reducing a visible NO 2 plume in an exhaust stack of a combustion or “gas” turbine power plant, other power plants or other combustion systems, including those in stationary or mobile applications.
  • Combustion turbines used in power plants comprise a compressor section, a combustion section, and a turbine section.
  • a supply of air is compressed in the compressor section and directed into the combustion section.
  • Fuel enters the combustion section by means of a nozzle.
  • the compressed air enters the combustion inlet and is mixed with the fuel, which is then combusted to produce a high-temperature, high-pressure gas. This gas then exits past the combustor section via a transition section and is injected into the turbine section to run the turbine.
  • the hot gases produced by the combustion section exit the power turbine and pass into a duct designed to convey these gases either to a heat exchanger (where additional energy is extracted) or directly to the exhaust stack.
  • These exhaust gases will range in temperature from 600° F. to 1200° F. depending upon the type of fuel, the load on the engine, and the ambient temperature.
  • NO x (a mixture of NO and NO 2 ) is formed.
  • the NO x produced by the gas turbine, or any subsequent post-combustion firing, is released into the atmosphere unless some control mechanism is used.
  • the NO 2 component is a strong colorant in exhaust gases, and absorbs light in the blue region, including light in the wavelength between about 350-400 nm, resulting in a plume that appears from yellowish to orange-red.
  • NO 2 plume is evident in many DLN (dry low NO x ) combustion systems, and determination of the actual source and mechanism of formation of NO 2 in DLN systems has proven to be an intractable problem, limiting options for controlling it. NO 2 may even be produced in conventional combustion turbine systems and also from some chemical processing facilities, such as nitric acid production plants. Control of NO 2 is important because, among other reasons, concentrations of only 20-30 ppm can produce a very objectionable plume.
  • NO 2 plumes may also be present in other combustion systems different from the gas turbine. These include pulverized coal (pc) fired boilers (operating according to the Rankine cycle), diesel engines, and gasoline engines (operating according to the Otto cycle). In particular, coal/oil energy systems and diesel cycle energy conversion systems produce significant NO x levels and may have a noticeable plume.
  • pulverized coal (pc) fired boilers operating according to the Rankine cycle
  • diesel engines and gasoline engines (operating according to the Otto cycle).
  • pc pulverized coal
  • gasoline engines operating according to the Otto cycle
  • NO x emissions are most often reduced using emission control systems which employ chemical means, such as ammonia injection in an SCR (selective catalytic reduction) system.
  • Photometric methods have been studied in coal combustion where NO x is found in combination with other pollutants such as sulfur dioxide (SO 2 ). SO 2 and NO x are combustion products related to fuel burning associated with heat or power production.
  • Photometric remediation methods include illumination or irradiation of the exhaust gases prior to subsequent processing steps, but all require additional steps or processing parameters during the reduction process in order for NO 2 to be reduced. Many of the photometric methods reviewed result in formation of undesirable byproducts such as sulfuric acid mist, ozone, and particulates.
  • U.S. Pat. No. 4,995,955 discloses a process for reducing NO x contamination within an effluent stream using an ultraviolet light source having a wavelength of less than 220 nm.
  • This method requires particle filtration or electrostatic precipitators to remove particles formed from the chemical processes used to clean the exhaust gases. Using a wavelength in this region causes the formation of ozone, a well-known component of urban smog.
  • U.S. Pat. No. 3,869,362 discloses a process for reducing NO x /SO 2 emissions by controlling the ratio of NO x to SO 2 before introducing the gas mixture into an irradiation chamber. This method requires the presence of SO 2 and also additionally requires collecting chambers to cleanse the exhaust stream of mist and solid particles.
  • U.S. Pat. No. 3,984,296 discloses a photochemical process for removing gaseous pollutant compounds (including NO x ) from a contaminant gas stream, by introducing positive and/or negative ions into the flue gas prior to irradiation The ions form complexes with the pollutants which must be removed by precipitation or other methods.
  • U.S. Pat. No. 4,146,450 discloses a method for reducing or removing NO 2 from exhaust gases containing NO x using a catalytic reduction method with ammonia which has been previously excited by ultraviolet radiation.
  • the present invention provides a method of reducing a visible NO 2 plume in an exhaust stack by irradiating the exhaust gases within the duct or stack with at least one illumination source.
  • the visible plume is substantially reduced while minimizing the formation of additional pollutants.
  • This reduction may result in NO 2 concentrations of below 20-30 ppm, and may represent an NO 2 reduction of 90% or more in some cases.
  • the reduction process is effective irrespective of the source of the NO 2 (including the combustion of fuel gas, oil, or solid fuel).
  • the degree of reduction will be a function of, among other things, the initial NO 2 concentration, lamp intensity, and path length.
  • the illumination source can be placed directly within the exhaust duct/stack or optically coupled to these, and has a wavelength of light of at least 350 nm and preferably between 350 and 400 nm.
  • the method does not require the presence of other chemicals or additional processing steps to achieve its desired reduction.
  • FIG. 1 is a schematic representation of an exhaust path in a turbine engine having at least one illumination source to reduce the visible plume.
  • the present invention uses photo-remediation methods for reduction or elimination of a visible NO 2 plume in exhaust gases emitted from turbine engines, power plants, or any chemical process which releases NO x into the environment. More specifically (and referring now to FIG. 1), visible NO 2 emissions in an exhaust duct 1 of a combustion turbine engine, having a compressor section 2 , a combustion section 3 and a turbine section 4 .
  • the turbine engine can optionally be equipped with a duct burner or auxiliary burner 6 which is another source of NO x .
  • the NO 2 is substantially reduced by photo-irradiating the exhaust gases 5 with at least one illumination source 7 located within the exhaust duct and/or stack or optically coupled thereto.
  • the formation of secondary pollutants or byproducts is minimized, and additional processing steps are not required for removal.
  • the method takes advantage of low bonding energy that exists between the NO molecule and the additional oxygen (O) atom. This bonding energy is low in comparison to other species present in the exhaust (CO 2 , N 2 etc.). A moderately short wavelength light source is sufficient to decompose the NO 2 compound and reduce the plume's visual appearance.
  • the source of illumination 7 is one or more lamps which can be located within the exhaust duct and/or stack 1 or optically coupled to either of these.
  • Mercury vapor lamps are one class of source that produces the necessary wavelength of light, although other irradiation sources such as lasers or other high-energy sources may fulfill this requirement. Cooling and maintenance of the lamps located within the stack or duct may be required depending upon the exhaust gas conditions and the location of the illumination source.
  • Optical coupling of the illumination source to the stack is an approach that allows placement of the illumination source in a location outside the duct where it can be easily maintained, cleaned and replaced as necessary.
  • An optical fiber network can be used to connect the illumination source with the duct, with one end of the fiber lead placed at the illumination source and the other end of the fiber lead placed in the duct or stack.
  • the optical fiber network is fabricated from a material (such as silica-based fibers) exhibiting minimal losses in the UV region (about 300-400 nm), and with a high thermal stability.
  • Optical coupling may also be accomplished through use of a focusing lens, reflective materials, or similar techniques known to produce, transmit, and direct visible light. Any method of optical coupling known to those skilled in the art may be used to link the illumination source to the duct or stack.
  • the bond dissociation energy of the NO—O bond is 305 KJ/kg ⁇ mole.
  • E 1.2 ⁇ E ⁇ 4 kJ/mole/lambda, where lambda is in meters, 305 kJ/Mole corresponds to 393 nm radiation.
  • a UV source with strong emission between 350 and 400 nm would be an appropriate method of irradiation.
  • Use of wavelengths between 350-400 nm also decreases undesirable secondary reactions such as the formation of ozone.
  • the method of the present invention can be accomplished at any temperature, from ambient temperature up to temperatures of about 1,500° F. As the temperature increases, the wavelength of the light necessary to initiate the reaction to disassociate NO 2 into NO and O may be increased (the energy requirement of the light source is decreased).
  • At least one illumination source 7 is installed in the exhaust path 1 prior to the gases exiting to the atmosphere 8 .
  • the illumination source 7 may be located outside the exhaust path and optically coupled to locations in the exhaust path.
  • a fiber optic cable, not shown, may be used to provide such an optical coupling.
  • the exhaust gases should be in optical communication with the source of illumination 7 .
  • a light source having 46 watts of radiative power near 393 nm is required for illumination of an exhaust stack having a flow rate of 25 kg/hour.
  • the power required to accomplish the desired objectives is not significant.
  • test results show that the rate of photo-dissociation of NO 2 to NO is temperature sensitive. At 150° C., the rate of dissociation using photometric techniques is approximately an order of magnitude greater that at 25° C.
  • Temperature may also play a role in the suitable wavelength.
  • the light source appropriate for gases having temperatures over 25° C. may have a wavelength longer than 400 nm.
  • This method is effective to reduce the presence of NO 2 by about 50%-90%, depending upon operational considerations. As a result, the concentration of NO 2 in exhaust gases may reduced to below 20 ppm and below 10 ppm, or even less.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treating Waste Gases (AREA)

Abstract

An photo-remediation method for reducing a visible NO2 plume is provided. The method uses an illumination source having a wavelength of at least 350 nm, and preferably between 350-400 nm to irradiate gases within an exhaust path, and requires no additional steps or processing requirements for reduction of the visible plume.

Description

    BACKGROUND OF THE INVENTION
  • 1. Field of the Invention [0001]
  • This invention relates to a method for reducing a visible NO[0002] 2 plume in an exhaust stack of a combustion or “gas” turbine power plant, other power plants or other combustion systems, including those in stationary or mobile applications.
  • 2. Background Information [0003]
  • Combustion turbines used in power plants comprise a compressor section, a combustion section, and a turbine section. A supply of air is compressed in the compressor section and directed into the combustion section. Fuel enters the combustion section by means of a nozzle. The compressed air enters the combustion inlet and is mixed with the fuel, which is then combusted to produce a high-temperature, high-pressure gas. This gas then exits past the combustor section via a transition section and is injected into the turbine section to run the turbine. [0004]
  • The hot gases produced by the combustion section exit the power turbine and pass into a duct designed to convey these gases either to a heat exchanger (where additional energy is extracted) or directly to the exhaust stack. These exhaust gases will range in temperature from 600° F. to 1200° F. depending upon the type of fuel, the load on the engine, and the ambient temperature. [0005]
  • As a result of combustion, NO[0006] x (a mixture of NO and NO2) is formed. The NOx produced by the gas turbine, or any subsequent post-combustion firing, is released into the atmosphere unless some control mechanism is used. The NO2 component is a strong colorant in exhaust gases, and absorbs light in the blue region, including light in the wavelength between about 350-400 nm, resulting in a plume that appears from yellowish to orange-red.
  • The NO[0007] 2 plume is evident in many DLN (dry low NOx) combustion systems, and determination of the actual source and mechanism of formation of NO2 in DLN systems has proven to be an intractable problem, limiting options for controlling it. NO2 may even be produced in conventional combustion turbine systems and also from some chemical processing facilities, such as nitric acid production plants. Control of NO2 is important because, among other reasons, concentrations of only 20-30 ppm can produce a very objectionable plume.
  • NO[0008] 2 plumes may also be present in other combustion systems different from the gas turbine. These include pulverized coal (pc) fired boilers (operating according to the Rankine cycle), diesel engines, and gasoline engines (operating according to the Otto cycle). In particular, coal/oil energy systems and diesel cycle energy conversion systems produce significant NOx levels and may have a noticeable plume.
  • In gas turbine applications, NO[0009] x emissions are most often reduced using emission control systems which employ chemical means, such as ammonia injection in an SCR (selective catalytic reduction) system. Photometric methods have been studied in coal combustion where NOx is found in combination with other pollutants such as sulfur dioxide (SO2). SO2 and NOx are combustion products related to fuel burning associated with heat or power production. Photometric remediation methods include illumination or irradiation of the exhaust gases prior to subsequent processing steps, but all require additional steps or processing parameters during the reduction process in order for NO2 to be reduced. Many of the photometric methods reviewed result in formation of undesirable byproducts such as sulfuric acid mist, ozone, and particulates.
  • For example, U.S. Pat. No. 4,995,955 (Kim et al.) discloses a process for reducing NO[0010] x contamination within an effluent stream using an ultraviolet light source having a wavelength of less than 220 nm. This method requires particle filtration or electrostatic precipitators to remove particles formed from the chemical processes used to clean the exhaust gases. Using a wavelength in this region causes the formation of ozone, a well-known component of urban smog.
  • U.S. Pat. No. 3,869,362 (Machi et al.) discloses a process for reducing NO[0011] x/SO2 emissions by controlling the ratio of NOx to SO2 before introducing the gas mixture into an irradiation chamber. This method requires the presence of SO2 and also additionally requires collecting chambers to cleanse the exhaust stream of mist and solid particles.
  • U.S. Pat. No. 3,984,296 (Richards) discloses a photochemical process for removing gaseous pollutant compounds (including NO[0012] x) from a contaminant gas stream, by introducing positive and/or negative ions into the flue gas prior to irradiation The ions form complexes with the pollutants which must be removed by precipitation or other methods.
  • U.S. Pat. No. 4,146,450 (Araki et al.) discloses a method for reducing or removing NO[0013] 2 from exhaust gases containing NOx using a catalytic reduction method with ammonia which has been previously excited by ultraviolet radiation.
  • It is desirable, therefore, to provide a method of exhaust gas NO[0014] 2 decomposition without the need for additional processing requirements such as additional chemicals, temperature control, particle collection of precipitates, or other processing steps.
  • SUMMARY OF THE INVENTION
  • Accordingly, the present invention provides a method of reducing a visible NO[0015] 2 plume in an exhaust stack by irradiating the exhaust gases within the duct or stack with at least one illumination source. The visible plume is substantially reduced while minimizing the formation of additional pollutants. This reduction may result in NO2 concentrations of below 20-30 ppm, and may represent an NO2 reduction of 90% or more in some cases. The reduction process is effective irrespective of the source of the NO2 (including the combustion of fuel gas, oil, or solid fuel). The degree of reduction will be a function of, among other things, the initial NO2 concentration, lamp intensity, and path length.
  • The illumination source can be placed directly within the exhaust duct/stack or optically coupled to these, and has a wavelength of light of at least 350 nm and preferably between 350 and 400 nm. The method does not require the presence of other chemicals or additional processing steps to achieve its desired reduction. [0016]
  • It is an object of the invention therefore to provide a method of reducing a visible NO[0017] 2 plume within the exhaust.
  • It is a further object of the invention to provide a method of reducing a visible NO[0018] 2 plume in exhaust gasses by irradiating the exhaust stack gasses with a source of illumination within the stack or optically coupled thereto.
  • It is an additional object of the invention to provide such a method of reducing a visible NO[0019] 2 plume without requiring the presence of other chemicals or other processing steps to achieve the desired reduction.
  • It is a further object of the invention to reduce a visible NO[0020] 2 plume in exhaust without producing undesirable by-products.
  • These and other objects of the invention will be apparent from the following description and appended claims.[0021]
  • BRIEF DESCRIPTION OF THE DRAWINGS
  • The invention is further illustrated by the following non-limiting drawing, in which: [0022]
  • FIG. 1 is a schematic representation of an exhaust path in a turbine engine having at least one illumination source to reduce the visible plume.[0023]
  • DESCRIPTION OF PREFERRED EMBODIMENTS
  • The present invention uses photo-remediation methods for reduction or elimination of a visible NO[0024] 2 plume in exhaust gases emitted from turbine engines, power plants, or any chemical process which releases NOx into the environment. More specifically (and referring now to FIG. 1), visible NO2 emissions in an exhaust duct 1 of a combustion turbine engine, having a compressor section 2, a combustion section 3 and a turbine section 4. The turbine engine can optionally be equipped with a duct burner or auxiliary burner 6 which is another source of NOx. The NO2 is substantially reduced by photo-irradiating the exhaust gases 5 with at least one illumination source 7 located within the exhaust duct and/or stack or optically coupled thereto. The formation of secondary pollutants or byproducts (including sulfates and nitrates) is minimized, and additional processing steps are not required for removal.
  • The method takes advantage of low bonding energy that exists between the NO molecule and the additional oxygen (O) atom. This bonding energy is low in comparison to other species present in the exhaust (CO[0025] 2, N2 etc.). A moderately short wavelength light source is sufficient to decompose the NO2 compound and reduce the plume's visual appearance.
  • The source of [0026] illumination 7 is one or more lamps which can be located within the exhaust duct and/or stack 1 or optically coupled to either of these. Mercury vapor lamps are one class of source that produces the necessary wavelength of light, although other irradiation sources such as lasers or other high-energy sources may fulfill this requirement. Cooling and maintenance of the lamps located within the stack or duct may be required depending upon the exhaust gas conditions and the location of the illumination source. Optical coupling of the illumination source to the stack is an approach that allows placement of the illumination source in a location outside the duct where it can be easily maintained, cleaned and replaced as necessary. An optical fiber network can be used to connect the illumination source with the duct, with one end of the fiber lead placed at the illumination source and the other end of the fiber lead placed in the duct or stack. Preferably, the optical fiber network is fabricated from a material (such as silica-based fibers) exhibiting minimal losses in the UV region (about 300-400 nm), and with a high thermal stability. Optical coupling may also be accomplished through use of a focusing lens, reflective materials, or similar techniques known to produce, transmit, and direct visible light. Any method of optical coupling known to those skilled in the art may be used to link the illumination source to the duct or stack.
  • It may be desirable to use a purged-air system to maintain the lamps or the optical fiber interface, either on a continuous or periodic basis. [0027]
  • The bond dissociation energy of the NO—O bond is 305 KJ/kg−mole. Using the conversion E=1.2×E[0028] −4 kJ/mole/lambda, where lambda is in meters, 305 kJ/Mole corresponds to 393 nm radiation. Thus, a UV source with strong emission between 350 and 400 nm would be an appropriate method of irradiation. Use of wavelengths between 350-400 nm also decreases undesirable secondary reactions such as the formation of ozone.
  • The method of the present invention can be accomplished at any temperature, from ambient temperature up to temperatures of about 1,500° F. As the temperature increases, the wavelength of the light necessary to initiate the reaction to disassociate NO[0029] 2 into NO and O may be increased (the energy requirement of the light source is decreased).
  • In one embodiment, at least one [0030] illumination source 7 is installed in the exhaust path 1 prior to the gases exiting to the atmosphere 8. Alternatively, the illumination source 7 may be located outside the exhaust path and optically coupled to locations in the exhaust path. A fiber optic cable, not shown, may be used to provide such an optical coupling. In either arrangement, the exhaust gases should be in optical communication with the source of illumination 7.
  • Due to the prevention of undesirable secondary reactions and particulate matter, the need for other processing steps is advantageously eliminated. Physical methods such as scrubbers, temperature control, electrostatic precipitators and the like are unnecessary. It is also unnecessary to add other chemicals which facilitate precipitation or reduction of the pollutants by other mechanisms. While there can be some formation of ozone, ozone is unstable at the temperatures contemplated and is expected to break down; thus production of ozone is not expected to be a significant problem. Similarly, recombination of NO and O to form NO[0031] 2 is not expected to be a problem because the concentrations of NO and O will be very low; thus the likelihood of recombination is also very low.
  • Test results have shown that there is a strong relationship between the intensity of the illumination source (as measured in watts) and the decomposition rate of NO[0032] 2. Higher intensities revealed more rapid decomposition of the NO2: when plotted, the results show a log-linear relationship between NO2 concentration and time. Quantum efficiency (the number of photons required per molecule of NO2 dissociated) peaks at 390 nm; wavelengths much longer than this will not have sufficient energy to cause dissociation, while shorter wavelengths will not be as efficient in causing the dissociation of NO and O. The following example provides an estimate of lamp size requirements for a common exhaust, say from a combustion turbine power plant. Using a gas flow of 25 kg/hour of NO2 and the above bond dissociation energy of 305 kJ/kg−mole, 25 kg hour × kg - mole 46 kg × 305 , 000 Joules kg - mole × hr 3 , 600 sec = 46 watts
    Figure US20030015413A1-20030123-M00001
  • A light source having 46 watts of radiative power near 393 nm is required for illumination of an exhaust stack having a flow rate of 25 kg/hour. Thus, it can be seen that the power required to accomplish the desired objectives is not significant. [0033]
  • Additionally, test results show that the rate of photo-dissociation of NO[0034] 2 to NO is temperature sensitive. At 150° C., the rate of dissociation using photometric techniques is approximately an order of magnitude greater that at 25° C.
  • Temperature may also play a role in the suitable wavelength. For example, the light source appropriate for gases having temperatures over 25° C. may have a wavelength longer than 400 nm. [0035]
  • This method is effective to reduce the presence of NO[0036] 2 by about 50%-90%, depending upon operational considerations. As a result, the concentration of NO2 in exhaust gases may reduced to below 20 ppm and below 10 ppm, or even less.
  • While particular embodiments of this invention have been described above for purposes of illustration, it will be evident to those skilled in the art that numerous variations of the details of the present invention may be made without departing from the invention as defined in the appended claims. [0037]

Claims (17)

In the claims:
1. A method of reducing NO2 emissions in an exhaust gas comprising:
exposing the exhaust gas to a visibility-affecting amount of illumination from an illumination source, wherein the visibility of the exhaust gas is substantially reduced.
2. The method of claim 1, wherein the illumination source is located within the exhaust path.
3. The method of claim 1, wherein the illumination source is optically coupled to the exhaust path.
4. The method of claim 1, wherein the wavelength of said illumination is at least 350 nm.
5. The method of claim 1, wherein the wavelength of said illumination is between about 350 nm and 400 nm.
6. The method of claim 1 adapted to treat exhaust gasses produced by a power generation facility.
7. The method of claim 1, wherein the exhaust gas includes an amount of NO2 sufficient to visibly absorb light having a wavelength between about 350 nm and 400 nm, before said exposure occurs.
8. The method of claim 1, wherein said method reduces an amount of NO2 in said exhaust gas to below about 20 parts per million.
9. The method of claim 1, wherein said method reduces an amount of NO2 in said exhaust gas to below about 10 parts per million.
10. The method of claim 1, wherein said method minimizes the formation of pollutants.
11. A photo-remediation method using optical sources and coupling devices as an emission control technology.
12. A photo-remediation system suitable for reducing NO2 within an exhaust gas, said system comprising:
a source of exhaust gas containing an amount of NO2 sufficient to act as a visible colorant within said gas;
at least one illumination source in optical communication with said exhaust gas, said at least one illumination source adapted to produce light having a wavelength of at least about 350 nm;
whereby NO2 within said exhaust gas is decomposed, thereby reducing the visibility of said colorant.
13. The photo-remediation system of claim 12 wherein:
said at least one illumination source produces light having a wavelength between about 350 nm to 400 nm.
14. The photo-remediation system of claim 13 further including:
at least one optical fiber connection between said at least one illumination source and said exhaust gas.
15. The photo-remediation system of claim 14 further including:
a cleaning system to maintain said optical communication between said at least one illumination source and said gas.
16. The photo-remediation system of claim 15 wherein said cleaning system includes a purged-air system.
17. The photo-remediation system of claim 12 constructed and arranged to treat exhaust gasses produced by a power generation facility.
US09/898,737 2001-07-03 2001-07-03 Photo-remediation of NO2 plume Expired - Lifetime US6495108B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US09/898,737 US6495108B1 (en) 2001-07-03 2001-07-03 Photo-remediation of NO2 plume

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US09/898,737 US6495108B1 (en) 2001-07-03 2001-07-03 Photo-remediation of NO2 plume

Publications (2)

Publication Number Publication Date
US6495108B1 US6495108B1 (en) 2002-12-17
US20030015413A1 true US20030015413A1 (en) 2003-01-23

Family

ID=25409973

Family Applications (1)

Application Number Title Priority Date Filing Date
US09/898,737 Expired - Lifetime US6495108B1 (en) 2001-07-03 2001-07-03 Photo-remediation of NO2 plume

Country Status (1)

Country Link
US (1) US6495108B1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070089425A1 (en) * 2005-10-24 2007-04-26 General Electric Company Methods and systems for low emission gas turbine energy generation
NO20110960A1 (en) * 2010-02-19 2011-08-31 Commonwealth Scient And Industrial Research Organisati Process for solvent treatment
US10166505B2 (en) * 2016-05-13 2019-01-01 Ching-Jing Photonergy Co., Ltd Method of treating gas and gas treatment device
US11085344B2 (en) * 2019-10-21 2021-08-10 Saudi Arabian Oil Company Thermal- and photo-assisted aftertreatment of nitrogen oxides
US11097222B2 (en) * 2019-10-21 2021-08-24 Saudi Arabian Oil Company Thermal- and photo-assisted aftertreatment of nitrogen oxides
US11300031B2 (en) 2019-10-21 2022-04-12 Saudi Arabian Oil Company Thermal- and photo-assisted aftertreatment of nitrogen oxides

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6907831B1 (en) * 2003-12-11 2005-06-21 Siemens Westinghouse Power Corporation Photolytic method of improving mercury capture in fossil (coal) fired systems
US8865097B2 (en) * 2010-06-23 2014-10-21 Baoquan Zhang Flur-gas purification and reclamation system and method thereof
KR102079768B1 (en) * 2018-05-08 2020-02-20 에스케이가스 주식회사 A method for reducing nitrogen dioxide in the exhaust gas generated during an olefin production process

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3869362A (en) * 1973-01-11 1975-03-04 Ebara Mfg Process for removing noxious gas pollutants from effluent gases by irradiation
US3984296A (en) 1974-09-13 1976-10-05 Richards John R System and process for controlling air pollution
US4097349A (en) 1976-03-31 1978-06-27 Stephen Zenty Photochemical process for fossil fuel combustion products recovery and utilization
JPS5390159A (en) 1977-01-21 1978-08-08 Kureha Chem Ind Co Ltd Denitrating method
US4416748A (en) 1981-09-08 1983-11-22 Concord Scientific Corporation Process for reduction of the content of SO2 and/or NOx in flue gas
US4995955A (en) 1989-09-14 1991-02-26 Lehigh University Optically-assisted gas decontamination process
US5144146A (en) * 1990-07-06 1992-09-01 Ultraviolet Energy Generators, Inc. Method for destruction of toxic substances with ultraviolet radiation
US5489777A (en) * 1990-12-26 1996-02-06 Denver Seminary Apparatus for remote analysis of vehicle emissions using reflective thermography

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070089425A1 (en) * 2005-10-24 2007-04-26 General Electric Company Methods and systems for low emission gas turbine energy generation
US7513100B2 (en) 2005-10-24 2009-04-07 General Electric Company Systems for low emission gas turbine energy generation
NO20110960A1 (en) * 2010-02-19 2011-08-31 Commonwealth Scient And Industrial Research Organisati Process for solvent treatment
US10166505B2 (en) * 2016-05-13 2019-01-01 Ching-Jing Photonergy Co., Ltd Method of treating gas and gas treatment device
US11085344B2 (en) * 2019-10-21 2021-08-10 Saudi Arabian Oil Company Thermal- and photo-assisted aftertreatment of nitrogen oxides
US11097222B2 (en) * 2019-10-21 2021-08-24 Saudi Arabian Oil Company Thermal- and photo-assisted aftertreatment of nitrogen oxides
US11300031B2 (en) 2019-10-21 2022-04-12 Saudi Arabian Oil Company Thermal- and photo-assisted aftertreatment of nitrogen oxides

Also Published As

Publication number Publication date
US6495108B1 (en) 2002-12-17

Similar Documents

Publication Publication Date Title
US7498009B2 (en) Controlled spectrum ultraviolet radiation pollution control process
US4397823A (en) Process and apparatus for removing a pollutant from a gas stream
US8991149B2 (en) Dry 3-way catalytic reduction of gas turbine NOX
EP0877649B1 (en) IMPROVED ADVANCED REBURNING METHODS FOR HIGH EFFICIENCY NOx-CONTROL
US5547650A (en) Process for removal of oxides of nitrogen
US5120516A (en) Process for removing nox emissions from combustion effluents
US6495108B1 (en) Photo-remediation of NO2 plume
CN101947409B (en) Flue gas mercury removal system based on photochemical advanced oxidation
US4849192A (en) Methods for preventing formation of sulfuric acid and related products in combustion effluents
US4743436A (en) Methods for preventing ammonium bisulfate formation during the noncatalytic reduction of nitric oxide
JP2004532967A (en) Incineration process using high concentration of oxygen
US7473095B2 (en) NOx emissions reduction process and apparatus
WO2007061401A2 (en) Controlled spectrum ultraviolet radiation pollution control process
US5980610A (en) Apparatus and method for improving electrostatic precipitator performance by plasma reactor conversion of SO2 to SO3
US6969486B1 (en) Apparatus and method for treating pollutants in a gas using hydrogen peroxide and UV light
US4995955A (en) Optically-assisted gas decontamination process
CN201807287U (en) Flue gas demercuration system based on photochemistry advanced oxidation
EP3875167A1 (en) Improved nox removal method
Shemwell et al. Economics of an integrated approach to control SO2, NOx, HCl, and particulate emissions from power plants
US6907831B1 (en) Photolytic method of improving mercury capture in fossil (coal) fired systems
CN101055075A (en) Method for reducing coal-firing boiler NOx discharge and its implementing device
US4954323A (en) AOG incinerator NOx emission control via NH3 injection
KR100260743B1 (en) Exhaust gas purifier of an incinerator
US8636968B2 (en) Method for UV photolytic separation of pollutant gases from an emission stream
US12036508B2 (en) Nitrogen oxide reduction type regenerative thermal oxidation system and nitrogen oxide reduction method thereof

Legal Events

Date Code Title Description
AS Assignment

Owner name: SIEMENS WESTINGHOUSE POWER CORPORATION, FLORIDA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:RISING, BRUCE;REEL/FRAME:011974/0548

Effective date: 20010627

STCF Information on status: patent grant

Free format text: PATENTED CASE

AS Assignment

Owner name: SIEMENS POWER GENERATION, INC., FLORIDA

Free format text: CHANGE OF NAME;ASSIGNOR:SIEMENS WESTINGHOUSE POWER CORPORATION;REEL/FRAME:016996/0491

Effective date: 20050801

FPAY Fee payment

Year of fee payment: 4

AS Assignment

Owner name: SIEMENS ENERGY, INC., FLORIDA

Free format text: CHANGE OF NAME;ASSIGNOR:SIEMENS POWER GENERATION, INC.;REEL/FRAME:022482/0740

Effective date: 20081001

Owner name: SIEMENS ENERGY, INC.,FLORIDA

Free format text: CHANGE OF NAME;ASSIGNOR:SIEMENS POWER GENERATION, INC.;REEL/FRAME:022482/0740

Effective date: 20081001

FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

FPAY Fee payment

Year of fee payment: 8

FPAY Fee payment

Year of fee payment: 12