EP3641916A1 - Scr-system for removing ash from a flue gas stream generated in a combustion system - Google Patents

Scr-system for removing ash from a flue gas stream generated in a combustion system

Info

Publication number
EP3641916A1
EP3641916A1 EP18737171.1A EP18737171A EP3641916A1 EP 3641916 A1 EP3641916 A1 EP 3641916A1 EP 18737171 A EP18737171 A EP 18737171A EP 3641916 A1 EP3641916 A1 EP 3641916A1
Authority
EP
European Patent Office
Prior art keywords
scr
filtering screen
flue gas
gas stream
vertical duct
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.)
Withdrawn
Application number
EP18737171.1A
Other languages
German (de)
French (fr)
Inventor
Manfred Ryba
Adi Johann Leopold ZOBL
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.)
Yara International ASA
Original Assignee
Yara International ASA
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 Yara International ASA filed Critical Yara International ASA
Publication of EP3641916A1 publication Critical patent/EP3641916A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8621—Removing nitrogen compounds
    • B01D53/8625—Nitrogen oxides
    • B01D53/8631—Processes characterised by a specific device
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
    • F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
    • F23J15/025—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using filters
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00—Arrangements of devices for treating smoke or fumes
    • F23J15/06—Arrangements of devices for treating smoke or fumes of coolers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2251/00—Reactants
    • B01D2251/20—Reductants
    • B01D2251/206—Ammonium compounds
    • B01D2251/2062—Ammonia
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2257/00—Components to be removed
    • B01D2257/40—Nitrogen compounds
    • B01D2257/404—Nitrogen oxides other than dinitrogen oxide
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B01D2258/0283—Flue gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J2219/00—Treatment devices
    • F23J2219/10—Catalytic reduction devices
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/30—Technologies for a more efficient combustion or heat usage

Definitions

  • the application relates to prolonging the active life time of an selective catalytic reduction (SCR)-reactor of an SCR-system that is provided to remove NOx from the flue gas stream that is produced in a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of the flue gas stream to an outlet, of which at least one duct is essentially vertically disposed, this by removing at least part of the ash from the flue gas stream before it reaches the SCR- reactor.
  • SCR selective catalytic reduction
  • flue gas streams are produced containing polluting components to the atmosphere such as nitrous oxides (NOx) and sulfur oxides (SOx) which must be removed from the produced flue gases before these are discharged into the environment.
  • NOx nitrous oxides
  • SOx sulfur oxides
  • the standard for removing nitrous oxides from flue gases is the SCR-process using an SCR-catalyst (also called a DeNOx catalyst), where a reducing agent, typically ammonia, is injected and mixed into the flue gases, and sent through a catalytic reactor where the catalyst facilitates the reduction of NOx using the reducing agent to form elemental nitrogen (N2) and water.
  • SCR-catalyst also called a DeNOx catalyst
  • the flue gases from the combustion processes furthermore typically contain fly ash particulates (also known as pulverised fuel ash) formed during the combustion process.
  • fly ash particulates also known as pulverised fuel ash
  • This ash may stick together or in power boilers may stick to the heating surfaces of the different heat exchangers, or can even sinter together. If the combustion system is not running in full load, there can be accumulation of the ash due to lower velocity. If the load of the combustion system is then increased again, the ash may accumulate in the SCR catalyst or in or on various components of an SCR system. Ash that has been sticking together on a surface may crack and bigger particles can drop down.
  • the ash can range from a fine powder to Large Particle Ash (LPA also known as "popcorn ash", from about 0.1 cm to about 2.5 cm), that can even further develop into large chunky pieces (from about 2.5 cm to about 13 cm or even larger), for instance when it accumulates in or on the SCR catalyst surface and passageways or on components of an SCR system.
  • LPA Large Particle Ash
  • the various types of ash are formed in the combustion system and can easily be carried over into the SCR system causing accumulation and plugging of the various components of the SCR system.
  • SCR systems typically are equipped with a plate or honeycomb-type catalyst and may have a pitch or opening ranging up to 8 millimetres. A part of the ash particles, and especially the LPA particles, are larger than the openings of the SCR catalyst.
  • the SCR catalysts becomes plugged on the inlet grid and after longer operation times also between the plates in case of a plate type catalyst and in the channels in case of a honeycomb type catalyst. This may result in misdistribution of the flue gas, loss of catalytic performance through loss of available DeNOx, potential, unacceptable NEb slip, excessive pressure drop and catalyst erosion damage.
  • the SCR system must frequently be cleaned using for instance soot blowers or ultrasound.
  • soot blowers or ultrasound the tendency for the channels of the SCR catalysts of the SCR system to become obstructed or clogged stays, and in particular in such a way that after a certain time period, the obstructions can no longer be removed with conventional cleaning methods.
  • Removal of ash from the flue gas may involve various technologies depending on the physical properties of the ash.
  • the physical properties of the fly ash varies depending on the fuel type and the operating conditions in the thermal processes.
  • Fine powder ash may be removed using Electro Static Precipitators (ESP), which are typically installed upstream and/or downstream of the SCR system depending on the SCR arrangement, (i.e. high dust, low dust or tail end arrangement).
  • ESP Electro Static Precipitators
  • LPA can be collected prior to the SCR-reactor by means of LPA screens, which are typically located in the flue gas stream between the economizer outlet and the SCR inlet.
  • LPA screens typically located in the flue gas stream between the economizer outlet and the SCR inlet.
  • These techniques may not be sufficiently efficient to remove the ash in order to protect the SCR-catalyst(s) or the various components of the SCR system from plugging by or accumulation of fly ash particulates, which can lead to premature loss of SCR performance.
  • loose powder can plug channels of honeycomb-type and corrugated-type catalysts with individual channels becoming partially or fully inaccessible to flue gas.
  • chunky fly ash particulates and LPA can deposit on top of the catalysts or on other components of the SCR-system, blocking the flue gas passage through honeycomb-, plate-, or corrugated-type SCR catalysts and access to the catalytic surfaces.
  • Popcorn ash can travel into the channels of honeycomb, corrugated, or plate SCR-catalysts and deposit in the channel where it can become wedged between the channel walls, blocking flue gas flow and providing an environment for further fly ash particulates to accumulate and plug the channel.
  • the ash removal may not be sufficient to protect the SCR-catalyst(s) or the various components of the SCR-system from plugging by or accumulation of fly ash particulates, which can lead to premature loss of SCR- performance.
  • loose powder can plug channels of honeycomb-type and corrugated-type catalysts with individual channels becoming partially or fully inaccessible to flue gas.
  • chunky fly ash particulates and LPA can deposit on top of the catalyst(s) or on other components of the system, blocking the flue gas passage through honeycomb-, plate-, or corrugated-type SCR-catalysts and access to the catalytic surfaces.
  • Popcorn ash can travel into the channels of honeycomb, corrugated, or plate SCR-catalysts and deposit in the channel where it can become wedged between the channel walls, blocking flue gas flow and providing an environment for further fly ash particulates to accumulate and plug the channel.
  • the result can be a catalyst with pluggage ranging from 5% to 100% and reduced NOx removal efficiency.
  • EP 1 146 2866 a combustion system containing multiple ceramic filters is disclosed.
  • One ceramic filter is placed inside the combustion chamber that acts as a barrier wall for the passage of LPA.
  • a principle disadvantage is that LPA rebounding from the ceramic filter falls back into the combustion chamber, and onto the flame. This ash on top of the flame hinders the combustion process. Further, it must pass through the combustible material before it can be removed from the combustion chamber, which passage is clearly obstructed by the combustible material itself.
  • a ceramic filter located directly over the flame is exposed to extreme temperatures, limiting the choice of materials therefor.
  • the combustion chamber is typically disposed with sensors and nozzles for the control of gases, rendering the chamber wall cutting and installation more technically challenging and expensive to avoid damage of ancillary parts.
  • US 2005/0061261 discloses a coal fired boiler that comprises a filtering screen that protects the SCR-catalysts from LPA.
  • the filtering screen is pivotally attached to the connection between a horizontal duct and a vertical duct.
  • a primary disadvantage is that it acts as a one-way flap-valve, and the force of the flue gas stream places the screen into an open configuration, thereby allowing the downstream passage of LPA.
  • the system is installed in a dedicated loop that is attached to the combustion system. This makes retrofitting the SCR-system in an existing combustion system complex and will not always be possible due to space restrictions.
  • an SCR-reactor comprising one or more SCR-catalyst layers each comprising one or more SCR-catalyst modules each comprising one or more SCR-catalysts arranged for reducing an amount of NO x in the flue gas stream, the SCR-reactor being configured for operative and fitting placement within the vertical duct, and
  • a filtering screen-unit comprising a filtering screen for filtering-out ash particles from the flue gas stream prior to entry into the one or more SCR-reactor wherein the filtering screen is arranged to protectively cover the SCR-reactor, and wherein the flue gas stream passes from an upper to a lower surface of the filtering screen, wherein the filtering screen-unit further comprises a vibration device in operative connection with the filtering screen, configured to actively vibrate the filtering screen.
  • the filtering screen is placed in an essentially vertical duct, more in particular the same vertical duct as wherein the SCR-reactor is fitted.
  • the vibration device that is in operative connection with the filtering screen is configured to continuously vibrate the filtering screen.
  • Vibrating refers to a regular displacement motion between two different positions, where a direction of motion (along the same path) changes during a cycle.
  • Protectively cover means that the filtering screen unit is placed above the SCR-catalyst reactor. More specifically, a footprint of the filtering-screen unit is superimposed over a foot print of the SCR-reactor.
  • Such an SCR-system can be retrofitted in an existing combustion system and this with very limited space available in the existing duct system.
  • the SCR-system according to the application will not cause heavy vibrations in the combustion system because only the filtering screen vibrates.
  • Such an SCR-system furthermore does not cause the ash particles to fall back into the combustion chamber or to fall back into the flame, through which the SCR-system according to this application does not interfere with the combustion process.
  • the active vibration of the filtering screen provides a constant clearance preventing build-up of ash on the filtering screen, and continually protects the SCR- catalyst(s). This is contrary to rapping systems, where hammers hit the screen or parts of the duct at regular intervals.
  • Rapping systems are considered less effective because they still allow the build-up of ash between the hits of the hammer, they do not remove all ash and require additional structural reinforcements that render the system bulkier. Furthermore, rapping systems do not cause a fast removal of the ash particles when the screen is mounted under an angle, especially when working at a shallow angle and since the vibration is not continuous, the ash particles move only a short distance every time the hammer hits. Between different hits, the ash particles remain on the screen. This less efficient removal system causes pressure to build up, as the ash particles at least partially block the screen for a longer time than when an active vibration is used. Also, rapping systems cause noise pollution, heavy Shockwaves through the whole duct system and render the system more liable to wear.
  • the vibration device is not a discontinuous vibrating system, preferably not a rapping system.
  • the vibration device causes a continuous vibration, more in particular a vibration being a wave or a sum of different waves.
  • the wave is a sinusoidal wave or the sum of sinusoidal waves.
  • Continuous vibration may refer to a vibration such that the filtering screen keeps vibrating at any point in time. It is therewith remarked that the amplitude of the vibration may decrease and increase over time, but never becomes zero. Continuous vibration may comprise different vibrations but these vibrations are forming an unbroken whole. Continuous vibration may be understood as vibration without interruption, uninterrupted vibration, constant vibration or permanent vibration.
  • the vibration device causes the filtering screen to resonate.
  • the frequency of the vibration emitted by the vibration device is equal to one of the resonant frequencies of the filtering screen.
  • the vibration frequency of the filtering screen may be between 5.00 Hz and 6.25 Hz, possibly around 5.40 Hz.
  • the advantage of having an SCR-system that is not placed in the same duct as wherein the heat source is or the combustion chamber, is that the SCR-system is protected from the radiant heat coming from the heat source.
  • heat exchangers are present in the first duct, allowing the SCR-system that is placed in another duct to operate at a more moderate temperature. The more moderate temperatures allow a larger choice of materials suitable to build the SCR-system and are more suitable for the catalytic reaction to take place.
  • the filtering screen is positioned at an angle of 5.0 to 75.0°, possibly 5.5 to 60.0°, possibly 6.0 to 45°, possibly 7.0 to 35.0°, possibly 7.5 to 25.0°, possibly 7.5 to 20.0, possibly 10.0° or 15.0°, relative to a horizontal plane.
  • the advantage of the vibrating screen being installed under an angle as indicated above is that the SCR-system can be installed in a duct where limited space is available. Once the SCR-system is installed in a duct, the space required for the vibration of the filtering screen depends on the angle under which the screen needs to be installed. Due to the active vibration that is applied to the filtering screen, the angle can be kept as low as indicated above and therefore limited headspace is necessary above the SCR-system, much less than a passive system, wherein the angle needs to be large enough to cause the ash particles to be removed from the filtering screen by force of gravity only.
  • the filtering screen comprises a barrier having a plurality of apertures therein, the apertures having a diameter from 2 mm to 10 mm. More in particular, the apertures have a diameter of around 4 mm.
  • the filtering screen is formed from a mesh screen.
  • the mesh screen more in particular can have a mesh size of between 2 mm and 10 mm. More in particular, the mesh size of the mesh screen is around 4 mm.
  • the at least one SCR-catalyst module comprises catalytic particles in a fixed bed. More in particular, all catalytic particles can be contained in a fixed bed.
  • the SCR- system further comprises an ash collector configured to receive the ash particles from the filtering screen.
  • the ash collector may more in particular be positioned at the lowest point of the filtering screen so that the ash particles can roll of the upper surface of the filtering screen into the ash collector.
  • the ash collector comprises a conveyor, more in particular a chain conveyor or a conveyor belt.
  • the ash collector may be sealed from the atmosphere.
  • the vibration device comprises a motor or a sound transducer.
  • the combustion system is a power boiler or a waste incinerator.
  • a combustion system comprising a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of a flue gas stream to an outlet, at least one duct being essentially vertically disposed, provided in the vertical duct that is arranged with an SCR-system according to the application as described above.
  • the invention further provides a combustion system that comprises a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of a flue gas stream to an outlet, at least one duct being essentially vertically disposed, provided that a SCR-system according to the application as described above is arranged in the vertical duct.
  • the combustion system is a power boiler or a waste incinerator.
  • the combustion chamber is provided in a first vertical duct and the SCR-system is provided in a second vertical duct downstream the first vertical duct.
  • the combustion chamber is provided in a first vertical duct and the SCR-system is provided in a third vertical duct downstream of the first vertical duct.
  • the combustion system is further provided with a heat exchanger for extracting heat from the flue gas stream, wherein the SCR-system is disposed downstream of the heat exchanger.
  • a method for retroactively fitting a system for reducing an amount of NOx in a flue gas stream to a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of the flue gas stream to an outlet, at least one duct being essentially vertically disposed, comprising the step of installing an SCR-system according to the present application as described above in the vertical duct.
  • FIG. 1 shows a schematic view of a power boiler which is provided with an SCR system provided in the second boiler draft and arranged with a filtering screen-unit to remove ash from the flue gas conducted through the flue gas ductwork of the power boiler according to the present application;
  • FIG. 2 shows a cross-section of an embodiment of a filtering screen-unit according to the application. Detailed description of the invention
  • the application relates to an SCR (Selective Catalytic Reduction)-system for a combustion system and a combustion system.
  • a combustion system in general is provided with a combustion chamber and an arrangement of ducts that are in connection with the combustion chamber for conduction of a flue gas stream to an outlet. At least one of the ducts is essentially vertically disposed. This vertical duct is different from a duct containing the combustion chamber.
  • FIG. 1 a combustion system in the form of a power boiler (1) is shown as an exemplary embodiment. It must be noted that this exemplary embodiment is not limitative to the scope of the application. The application is also applicable to a waste incinerator.
  • the combustion chamber for burning fossil fuel is arranged in a first vertical duct (la). Downstream the first vertical duct (la), a second vertical duct (lc) is provided including one or more heat exchangers (2). This second vertical duct (lc) is connected to the first vertical duct (la) via a third horizontal duct (lb).
  • the heat exchangers (2) that are provided in the second vertical duct (lc) contain more specifically economizers which are heat exchange devices that heat fluids, usually water, up to, but normally not beyond the boiling point of that fluid.
  • Economizers are so named because they can make use of the enthalpy in fluid streams that are hot, but not hot enough to be used in a boiler, thereby recovering more useful enthalpy and improving the boiler's efficiency. It are devices fitted to the power boiler (1) which save energy by using the exhaust gases from the power boiler (1) to preheat the cold water circulating therein.
  • the economizer(s) (2) are supported by a supporting beam (20).
  • the second duct (lc) is connected with a vertical exit duct (le) of the power boiler (1) through a fourth horizontal duct (Id).
  • a flue gas stream (A) is produced that travels through the different ducts (la - le) of the power boiler (1) and finally exits the power boiler (1) through an outlet (If) arranged in the exit duct (le).
  • An SCR-reactor (7) is positioned downstream of the combustion chamber in the second vertical duct (lc).
  • the SCR-reactor (7) forms part of an SCR-system further comprising amongst others means for ammonia injection, a heat exchanger if necessary, a mixer, dilution air.
  • An SCR-reactor (7) comprises one or more SCR-catalyst layers (8, 8') that are located in a housing, for instance a steel housing.
  • Each of the SCR-catalyst layers (8, 8') comprises one or more SCR-catalyst modules (3). In case of a plurality of SCR- catalyst modules (3), these are arranged side-by-side on the same elevation.
  • An SCR- catalyst module (3) comprises a plurality of single SCR-catalysts assembled in a frame, for instance a steel frame.
  • the SCR-reactor (7) is more in particular positioned downstream these heat exchangers (2).
  • Heat exchangers (2) are used in case the temperature of the flue gas is not sufficiently high to convert the oxides of nitrogen (NOx) catalytically. The heat exchangers (2) then heat the flue gas to a temperature of 220°C - 320°C.
  • the SCR-reactor (7) is configured for operative and fitting placement within the second vertical duct (lc), more specifically, it is configured for fitting exclusively (only) within a void space of the second vertical duct (lc).
  • the SCR-reactor (7) is dimensioned essentially for occlusion of the second vertical duct (lc). It is remarked that for instance in a waste incinerator, the SCR-system can be positioned in a third vertical duct that is downstream the first vertical duct.
  • Each of the SCR-catalyst modules comprises catalytic particles in a fixed bed.
  • ash refers to solid- phase combustion by-products including from a fine powder to Large Particle Ash (LPA also known as "popcorn ash", having a particle size from 0.1 cm to about 2.5 cm), which can even develop further into large chunk pieces (having a particle size from about 2.5 cm to about 13 cm or even larger).
  • LPA fine powder to Large Particle Ash
  • a filtering screen unit (4) is arranged upstream the SCR-reactor (7).
  • the filtering screen unit (4) comprises a filtering screen (41) for filtering-out ash particles from the flue gas stream prior to entry into the SCR-reactor (7).
  • the filtering screen (41) is thus configured to protectively cover the SCR-reactor (7). More in particular, the filtering screen (41) is extending above the upper SCR-catalyst layer (8) from the SCR- catalyst layers (8, 8') of the SCR-reactor (7).
  • a filtering screen (41) is provided with an upper and a lower surface (41a, 41b). The flue gas stream passes through a filtering screen (41) from the upper surface (41a) to the lower surface (41b) thereof.
  • the filtering screen (41) is disposed at an incline to a horizontal plane.
  • the filtering screen (41) can be positioned at an angle of 5.0 to 75.0° relative to a horizontal plane, in particular 5.5 to 60.0°, more in particular 6.0 to 45°, even more in particular 7.0 to 35.0°, still more in particular 7.5 to 25.0°, most in particular 7.5 to 20.0, like 10.0° or 15.0°, relative to a horizontal plane.
  • the filtering screen (41) comprises a barrier having a plurality of apertures therein to prevent the ash from passing through the filtering screen (41).
  • the apertures more in particular have a diameter from 2 to 10mm, more in particular having a diameter of around 4 mm.
  • the filtering screen (41) can be formed from one or more mesh screens. In that case, the mesh size is more in particular between 2 and 10 mm and more in particular around 4 mm.
  • the filtering screen (41) may have a cross-section of 50% which allows for undisturbed flow of fly ash and retaining the bigger ash particles which cannot get through the SCR-catalysts.
  • the filtering screen (41) can be made out of stainless steel.
  • the filtering screen unit (4) furthermore comprises a vibration device (42) that is in operative connection with the filtering screen (41) and that is configured to actively vibrate this filtering screen (41).
  • the vibrating device (42) applies vibration, optionally continuous vibration, to the filtering screen (41) such that the filtered ash is agitated downwards across the upper surface (41a) of the inclined filtering screen (42) for collection.
  • the vibration frequency of the filtering screen (41) may be between 5 Hz and 6,25 Hz. More in particular, the frequency of the filtering screen (41) may be around 5,4 Hz.
  • the vibration device (42) may comprise a motor or a sound transducer.
  • the vibration device (42) may produce a sinusoidal vibration.
  • the resonance frequency of the filtering screen (41) may be determined, the vibration device (42) may produce a vibration with the same frequency of the resonance frequency of the filtering screen (41).
  • the vibration of the filtering screen (41) may result in constant movement of the ash particles on the filtering screen (41) in the down slope direction or the ash collector (43), resulting in a fast and efficient removal of the ash particles of the filtering screen (41), even when the filtering screen (41) is mounted in the duct under a shallow angle.
  • the fast and efficient removal process of ash particles from the filtering screen result in a lower pressure drop SCR-system, compared to SCR-systems with a lesser efficient ash collecting systems.
  • an ash collector (43) is arranged.
  • the ash collector (43) can be sealed from the atmosphere.
  • the ash collector (43) can comprise a conveyor, more in particular a chain or screw conveyor or a conveyor belt.
  • the ash collector (43) can be in connection with any kind of ash collecting system (not shown in the figures). It is for instance possible to connect the ash collector (43) with a vertically positioned duct or pipe system (not shown on the figures) at the end of the ash collector (43) and into which the collected ash falls down by gravity and also because the pressure is higher there.
  • the lower end of the duct / pipe system can be connected with the lower SCR-catalyst layer (8').
  • the duct / pipe thus serves as a kind of bypass over the SCR-catalyst layers (8, 8'). It is remarked that it is also possible to place the ash collector (43) and the pipe / duct inside the SCR-reactor (7).
  • an expansion joint (44) can be provided between the vibration device (42) and the filtering screen (41).
  • the application also relates to a method for retroactively fitting a system for reducing an amount of NOx in a flue gas stream to a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of the flue gas stream to an outlet.
  • At least one duct is essentially vertically disposed.
  • the method comprises the step of installing an SCR-system (7) as disclosed above in the vertical duct.
  • the combustion chamber is more in particular disposed in a first vertical duct (la), and the SCR-system can be installed in the second (lc) or third vertical duct downstream the first vertical duct.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Chimneys And Flues (AREA)

Abstract

The application relates to an SCR (Selective Catalytic Reduction)-system for a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of a flue gas stream to an outlet, at least one duct being essentially vertically disposed, which SCR-system comprises an SCR-reactor comprising one or more SCR-catalyst layers each comprising one or more SCR-catalyst modules each comprising one or more SCR-catalysts arranged for reducing an amount of NOx in the flue gas stream, wherein the SCR-reactor is configured for operative and fitting placement within the vertical duct, and a filtering screen-unit comprising a filtering screen for filtering-out ash particles from the flue gas stream prior to entry into the one or more SCR-catalyst layers, wherein the filtering screen is arranged to protectively cover the SCR-reactor, and wherein the flue gas stream passes from an upper to a lower surface of the filtering screen, wherein the filtering screen-unit further comprises a vibration device in operative connection with the filtering screen, configured to actively vibrate the filtering screen. The application furthermore relates to such a combustion system and a method for retroactively fitting a system for reducing an amount of NOx in a flue gas stream to such a combustion system.

Description

SCR-SYSTEM FOR REMOVING ASH FROM A FLUE GAS STREAM
GENERATED IN A COMBUSTION SYSTEM
Field of the application
[0001] The application relates to prolonging the active life time of an selective catalytic reduction (SCR)-reactor of an SCR-system that is provided to remove NOx from the flue gas stream that is produced in a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of the flue gas stream to an outlet, of which at least one duct is essentially vertically disposed, this by removing at least part of the ash from the flue gas stream before it reaches the SCR- reactor.
Background of the application
[0002] In high temperature thermal processes performed in combustion systems, such as for instance power boilers, where steam is generated for the production in power plants or waste incinerators, flue gas streams are produced containing polluting components to the atmosphere such as nitrous oxides (NOx) and sulfur oxides (SOx) which must be removed from the produced flue gases before these are discharged into the environment.
[0003] The standard for removing nitrous oxides from flue gases is the SCR-process using an SCR-catalyst (also called a DeNOx catalyst), where a reducing agent, typically ammonia, is injected and mixed into the flue gases, and sent through a catalytic reactor where the catalyst facilitates the reduction of NOx using the reducing agent to form elemental nitrogen (N2) and water.
[0004] The flue gases from the combustion processes furthermore typically contain fly ash particulates (also known as pulverised fuel ash) formed during the combustion process. This ash may stick together or in power boilers may stick to the heating surfaces of the different heat exchangers, or can even sinter together. If the combustion system is not running in full load, there can be accumulation of the ash due to lower velocity. If the load of the combustion system is then increased again, the ash may accumulate in the SCR catalyst or in or on various components of an SCR system. Ash that has been sticking together on a surface may crack and bigger particles can drop down. The ash can range from a fine powder to Large Particle Ash (LPA also known as "popcorn ash", from about 0.1 cm to about 2.5 cm), that can even further develop into large chunky pieces (from about 2.5 cm to about 13 cm or even larger), for instance when it accumulates in or on the SCR catalyst surface and passageways or on components of an SCR system. The various types of ash are formed in the combustion system and can easily be carried over into the SCR system causing accumulation and plugging of the various components of the SCR system. SCR systems typically are equipped with a plate or honeycomb-type catalyst and may have a pitch or opening ranging up to 8 millimetres. A part of the ash particles, and especially the LPA particles, are larger than the openings of the SCR catalyst. As a consequence, the SCR catalysts becomes plugged on the inlet grid and after longer operation times also between the plates in case of a plate type catalyst and in the channels in case of a honeycomb type catalyst. This may result in misdistribution of the flue gas, loss of catalytic performance through loss of available DeNOx, potential, unacceptable NEb slip, excessive pressure drop and catalyst erosion damage.
[0005] Therefore, the SCR system must frequently be cleaned using for instance soot blowers or ultrasound. Despite of the cleaning, the tendency for the channels of the SCR catalysts of the SCR system to become obstructed or clogged stays, and in particular in such a way that after a certain time period, the obstructions can no longer be removed with conventional cleaning methods.
[0006] Removal of ash from the flue gas may involve various technologies depending on the physical properties of the ash. The physical properties of the fly ash varies depending on the fuel type and the operating conditions in the thermal processes.
[0007] Fine powder ash may be removed using Electro Static Precipitators (ESP), which are typically installed upstream and/or downstream of the SCR system depending on the SCR arrangement, (i.e. high dust, low dust or tail end arrangement).
[0008] LPA can be collected prior to the SCR-reactor by means of LPA screens, which are typically located in the flue gas stream between the economizer outlet and the SCR inlet. These techniques however may not be sufficiently efficient to remove the ash in order to protect the SCR-catalyst(s) or the various components of the SCR system from plugging by or accumulation of fly ash particulates, which can lead to premature loss of SCR performance. For example, loose powder can plug channels of honeycomb-type and corrugated-type catalysts with individual channels becoming partially or fully inaccessible to flue gas. Furthermore, chunky fly ash particulates and LPA can deposit on top of the catalysts or on other components of the SCR-system, blocking the flue gas passage through honeycomb-, plate-, or corrugated-type SCR catalysts and access to the catalytic surfaces. Popcorn ash can travel into the channels of honeycomb, corrugated, or plate SCR-catalysts and deposit in the channel where it can become wedged between the channel walls, blocking flue gas flow and providing an environment for further fly ash particulates to accumulate and plug the channel.
[0009] Despite the above mentioned technologies, the ash removal may not be sufficient to protect the SCR-catalyst(s) or the various components of the SCR-system from plugging by or accumulation of fly ash particulates, which can lead to premature loss of SCR- performance. For example, loose powder can plug channels of honeycomb-type and corrugated-type catalysts with individual channels becoming partially or fully inaccessible to flue gas. Furthermore, chunky fly ash particulates and LPA can deposit on top of the catalyst(s) or on other components of the system, blocking the flue gas passage through honeycomb-, plate-, or corrugated-type SCR-catalysts and access to the catalytic surfaces. Popcorn ash can travel into the channels of honeycomb, corrugated, or plate SCR-catalysts and deposit in the channel where it can become wedged between the channel walls, blocking flue gas flow and providing an environment for further fly ash particulates to accumulate and plug the channel. The result can be a catalyst with pluggage ranging from 5% to 100% and reduced NOx removal efficiency. In addition, it is generally known in the regeneration of SCR-catalysts that the physical cleaning of the catalyst to remove any loose fly ash accumulated on the module frame, box frame, on top of the catalyst and within the various passageways of the catalyst, for example plugs within the catalyst channels, is an important step prior to a subsequent wet chemical based regeneration process.
[0010] Removal of fly ash plugs prior to wet-chemical regeneration ensures that loose, fly ash particulates are not carried into the treatment tanks or accumulate in the chemical solutions used during the regeneration processes where the fly ash particulates could potentially cause problems, such as plugged equipment, damaged equipment due to the abrasive effects of the fly ash and a reduced effectiveness of the chemicals in the process. Therefore, reducing the amount of loose fly ash particulates results in decreased discharge rates of chemical solutions, savings in chemical solutions, and preventing mechanical failures due to abrasive corrosion. Further, removal of the fly ash prior to wet-chemical treatment may also decrease the accumulation of catalyst poisons, such as iron, in the treatment tanks.
[0011] To address the problem, equipment manufacturers and utilities have experimented with various solutions with LPA screens, but, none appeared capable of performing satisfactorily in the long term.
[0012] In EP 1 146 286, a combustion system containing multiple ceramic filters is disclosed. One ceramic filter is placed inside the combustion chamber that acts as a barrier wall for the passage of LPA. A principle disadvantage is that LPA rebounding from the ceramic filter falls back into the combustion chamber, and onto the flame. This ash on top of the flame hinders the combustion process. Further, it must pass through the combustible material before it can be removed from the combustion chamber, which passage is clearly obstructed by the combustible material itself. Moreover, a ceramic filter located directly over the flame is exposed to extreme temperatures, limiting the choice of materials therefor. In the case of retrofitting, the combustion chamber is typically disposed with sensors and nozzles for the control of gases, rendering the chamber wall cutting and installation more technically challenging and expensive to avoid damage of ancillary parts.
[0013] US 2005/0061261 discloses a coal fired boiler that comprises a filtering screen that protects the SCR-catalysts from LPA. The filtering screen is pivotally attached to the connection between a horizontal duct and a vertical duct. A primary disadvantage is that it acts as a one-way flap-valve, and the force of the flue gas stream places the screen into an open configuration, thereby allowing the downstream passage of LPA. In the case of retrofitting, the system is installed in a dedicated loop that is attached to the combustion system. This makes retrofitting the SCR-system in an existing combustion system complex and will not always be possible due to space restrictions. [0014] It is an aim of the invention to provide in a SCR- system that can be retrofitted in an existing combustion system and that with using a small amount of space so that the SCR- device can be retrofitted in combustion system with only limited space available. Another aim of the invention is to provide an SCR-system that influences the combustion process as little as possible. Still another aim of the invention is an SCR-system that does not cause any major differences in flow rate and pressure build-up of the flue gasses.
Summary of the invention
[0015] According to a first aspect of the present application, an SCR (Selective Catalytic Reduction)-system for a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of a flue gas stream to an outlet, at least one duct being essentially vertically disposed, which SCR- system comprises:
an SCR-reactor comprising one or more SCR-catalyst layers each comprising one or more SCR-catalyst modules each comprising one or more SCR-catalysts arranged for reducing an amount of NOx in the flue gas stream, the SCR-reactor being configured for operative and fitting placement within the vertical duct, and
a filtering screen-unit comprising a filtering screen for filtering-out ash particles from the flue gas stream prior to entry into the one or more SCR-reactor wherein the filtering screen is arranged to protectively cover the SCR-reactor, and wherein the flue gas stream passes from an upper to a lower surface of the filtering screen, wherein the filtering screen-unit further comprises a vibration device in operative connection with the filtering screen, configured to actively vibrate the filtering screen.
[0016] In some embodiments, the filtering screen is placed in an essentially vertical duct, more in particular the same vertical duct as wherein the SCR-reactor is fitted.
[0017] In some embodiments, the vibration device that is in operative connection with the filtering screen is configured to continuously vibrate the filtering screen.
[0018] Vibrating refers to a regular displacement motion between two different positions, where a direction of motion (along the same path) changes during a cycle. Protectively cover means that the filtering screen unit is placed above the SCR-catalyst reactor. More specifically, a footprint of the filtering-screen unit is superimposed over a foot print of the SCR-reactor.
[0019] Such an SCR-system can be retrofitted in an existing combustion system and this with very limited space available in the existing duct system. The SCR-system according to the application will not cause heavy vibrations in the combustion system because only the filtering screen vibrates. Such an SCR-system furthermore does not cause the ash particles to fall back into the combustion chamber or to fall back into the flame, through which the SCR-system according to this application does not interfere with the combustion process. The active vibration of the filtering screen provides a constant clearance preventing build-up of ash on the filtering screen, and continually protects the SCR- catalyst(s). This is contrary to rapping systems, where hammers hit the screen or parts of the duct at regular intervals. Rapping systems are considered less effective because they still allow the build-up of ash between the hits of the hammer, they do not remove all ash and require additional structural reinforcements that render the system bulkier. Furthermore, rapping systems do not cause a fast removal of the ash particles when the screen is mounted under an angle, especially when working at a shallow angle and since the vibration is not continuous, the ash particles move only a short distance every time the hammer hits. Between different hits, the ash particles remain on the screen. This less efficient removal system causes pressure to build up, as the ash particles at least partially block the screen for a longer time than when an active vibration is used. Also, rapping systems cause noise pollution, heavy Shockwaves through the whole duct system and render the system more liable to wear.
[0020] In some embodiments, the vibration device is not a discontinuous vibrating system, preferably not a rapping system.
[0021] In some embodiments, the vibration device causes a continuous vibration, more in particular a vibration being a wave or a sum of different waves. In some embodiments, the wave is a sinusoidal wave or the sum of sinusoidal waves.
[0022] The term "continuous vibration" may refer to a vibration such that the filtering screen keeps vibrating at any point in time. It is therewith remarked that the amplitude of the vibration may decrease and increase over time, but never becomes zero. Continuous vibration may comprise different vibrations but these vibrations are forming an unbroken whole. Continuous vibration may be understood as vibration without interruption, uninterrupted vibration, constant vibration or permanent vibration.
[0023] In some embodiments, the vibration device causes the filtering screen to resonate.
[0024] In some embodiments, the frequency of the vibration emitted by the vibration device is equal to one of the resonant frequencies of the filtering screen.
[0025] In some embodiments, the vibration frequency of the filtering screen may be between 5.00 Hz and 6.25 Hz, possibly around 5.40 Hz.
[0026] The advantage of having an SCR-system that is not placed in the same duct as wherein the heat source is or the combustion chamber, is that the SCR-system is protected from the radiant heat coming from the heat source. Moreover, in most combustion systems, heat exchangers are present in the first duct, allowing the SCR-system that is placed in another duct to operate at a more moderate temperature. The more moderate temperatures allow a larger choice of materials suitable to build the SCR-system and are more suitable for the catalytic reaction to take place.
[0027] In a possible embodiment of an SCR-system according to the application, the filtering screen is positioned at an angle of 5.0 to 75.0°, possibly 5.5 to 60.0°, possibly 6.0 to 45°, possibly 7.0 to 35.0°, possibly 7.5 to 25.0°, possibly 7.5 to 20.0, possibly 10.0° or 15.0°, relative to a horizontal plane.
[0028] The advantage of the vibrating screen being installed under an angle as indicated above is that the SCR-system can be installed in a duct where limited space is available. Once the SCR-system is installed in a duct, the space required for the vibration of the filtering screen depends on the angle under which the screen needs to be installed. Due to the active vibration that is applied to the filtering screen, the angle can be kept as low as indicated above and therefore limited headspace is necessary above the SCR-system, much less than a passive system, wherein the angle needs to be large enough to cause the ash particles to be removed from the filtering screen by force of gravity only.
[0029] In an embodiment of an SCR-system according to the application, the filtering screen comprises a barrier having a plurality of apertures therein, the apertures having a diameter from 2 mm to 10 mm. More in particular, the apertures have a diameter of around 4 mm.
[0030] In a possible embodiment of an SCR-system according to the application, the filtering screen is formed from a mesh screen. The mesh screen more in particular can have a mesh size of between 2 mm and 10 mm. More in particular, the mesh size of the mesh screen is around 4 mm.
[0031] In an embodiment of an SCR-system according to the application, the at least one SCR-catalyst module comprises catalytic particles in a fixed bed. More in particular, all catalytic particles can be contained in a fixed bed.
[0032] In a possible embodiment of an SCR-system according to the application, the SCR- system further comprises an ash collector configured to receive the ash particles from the filtering screen. The ash collector may more in particular be positioned at the lowest point of the filtering screen so that the ash particles can roll of the upper surface of the filtering screen into the ash collector.
[0033] In an embodiment of an SCR-system according to the application, the ash collector comprises a conveyor, more in particular a chain conveyor or a conveyor belt.
[0034] In a particular embodiment of an SCR-system according to the application, the ash collector may be sealed from the atmosphere.
[0035] In a possible embodiment of an SCR-system according to the application, the vibration device comprises a motor or a sound transducer.
[0036] In an embodiment of an SCR-system according to the application, the combustion system is a power boiler or a waste incinerator.
[0037] According to a further aspect of the present application, a combustion system is disclosed that comprises a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of a flue gas stream to an outlet, at least one duct being essentially vertically disposed, provided in the vertical duct that is arranged with an SCR-system according to the application as described above.
[0038] More in particular, the invention further provides a combustion system that comprises a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of a flue gas stream to an outlet, at least one duct being essentially vertically disposed, provided that a SCR-system according to the application as described above is arranged in the vertical duct.
[0039] In an embodiment of a combustion system according to the application, the combustion system is a power boiler or a waste incinerator.
[0040] In an embodiment where the combustion system is a power boiler, the combustion chamber is provided in a first vertical duct and the SCR-system is provided in a second vertical duct downstream the first vertical duct.
[0041] In an embodiment where the combustion system is a waste incinerator, the combustion chamber is provided in a first vertical duct and the SCR-system is provided in a third vertical duct downstream of the first vertical duct.
[0042] In a possible embodiment of a combustion system according to the application, the combustion system is further provided with a heat exchanger for extracting heat from the flue gas stream, wherein the SCR-system is disposed downstream of the heat exchanger.
[0043] According to another aspect of the present application, a method is described for retroactively fitting a system for reducing an amount of NOx in a flue gas stream to a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of the flue gas stream to an outlet, at least one duct being essentially vertically disposed, comprising the step of installing an SCR-system according to the present application as described above in the vertical duct.
[0044]
Brief description of the figures
[0001] FIG. 1 shows a schematic view of a power boiler which is provided with an SCR system provided in the second boiler draft and arranged with a filtering screen-unit to remove ash from the flue gas conducted through the flue gas ductwork of the power boiler according to the present application;
[0045] FIG. 2 shows a cross-section of an embodiment of a filtering screen-unit according to the application. Detailed description of the invention
[0046] The application relates to an SCR (Selective Catalytic Reduction)-system for a combustion system and a combustion system. A combustion system in general is provided with a combustion chamber and an arrangement of ducts that are in connection with the combustion chamber for conduction of a flue gas stream to an outlet. At least one of the ducts is essentially vertically disposed. This vertical duct is different from a duct containing the combustion chamber.
[0047] In FIG. 1, a combustion system in the form of a power boiler (1) is shown as an exemplary embodiment. It must be noted that this exemplary embodiment is not limitative to the scope of the application. The application is also applicable to a waste incinerator.
[0048] In the power boiler (1) as shown in FIG. 1, the combustion chamber for burning fossil fuel is arranged in a first vertical duct (la). Downstream the first vertical duct (la), a second vertical duct (lc) is provided including one or more heat exchangers (2). This second vertical duct (lc) is connected to the first vertical duct (la) via a third horizontal duct (lb). The heat exchangers (2) that are provided in the second vertical duct (lc) contain more specifically economizers which are heat exchange devices that heat fluids, usually water, up to, but normally not beyond the boiling point of that fluid. Economizers are so named because they can make use of the enthalpy in fluid streams that are hot, but not hot enough to be used in a boiler, thereby recovering more useful enthalpy and improving the boiler's efficiency. It are devices fitted to the power boiler (1) which save energy by using the exhaust gases from the power boiler (1) to preheat the cold water circulating therein. The economizer(s) (2) are supported by a supporting beam (20). The second duct (lc) is connected with a vertical exit duct (le) of the power boiler (1) through a fourth horizontal duct (Id). Through the combustion of the fossil fuel, a flue gas stream (A) is produced that travels through the different ducts (la - le) of the power boiler (1) and finally exits the power boiler (1) through an outlet (If) arranged in the exit duct (le).
[0049] An SCR-reactor (7) is positioned downstream of the combustion chamber in the second vertical duct (lc). The SCR-reactor (7) forms part of an SCR-system further comprising amongst others means for ammonia injection, a heat exchanger if necessary, a mixer, dilution air. An SCR-reactor (7) comprises one or more SCR-catalyst layers (8, 8') that are located in a housing, for instance a steel housing. Each of the SCR-catalyst layers (8, 8') comprises one or more SCR-catalyst modules (3). In case of a plurality of SCR- catalyst modules (3), these are arranged side-by-side on the same elevation. An SCR- catalyst module (3) comprises a plurality of single SCR-catalysts assembled in a frame, for instance a steel frame. In the presence of heat exchangers (2), the SCR-reactor (7) is more in particular positioned downstream these heat exchangers (2). Heat exchangers (2) are used in case the temperature of the flue gas is not sufficiently high to convert the oxides of nitrogen (NOx) catalytically. The heat exchangers (2) then heat the flue gas to a temperature of 220°C - 320°C.
[0050] The SCR-reactor (7) is configured for operative and fitting placement within the second vertical duct (lc), more specifically, it is configured for fitting exclusively (only) within a void space of the second vertical duct (lc). The SCR-reactor (7) is dimensioned essentially for occlusion of the second vertical duct (lc). It is remarked that for instance in a waste incinerator, the SCR-system can be positioned in a third vertical duct that is downstream the first vertical duct. Each of the SCR-catalyst modules comprises catalytic particles in a fixed bed.
[0051] During the combustion of the fossil fuel, amongst others (fly) ash is produced that is carried along with the flue gas stream. As used herein, the term "ash" refers to solid- phase combustion by-products including from a fine powder to Large Particle Ash (LPA also known as "popcorn ash", having a particle size from 0.1 cm to about 2.5 cm), which can even develop further into large chunk pieces (having a particle size from about 2.5 cm to about 13 cm or even larger). In order to remove the ash from the flue gas that is conducted throughout the second vertical duct (lc) to protect the SCR system against fouling and clogging, a filtering screen unit (4) is arranged upstream the SCR-reactor (7).
[0052] The filtering screen unit (4) comprises a filtering screen (41) for filtering-out ash particles from the flue gas stream prior to entry into the SCR-reactor (7). The filtering screen (41) is thus configured to protectively cover the SCR-reactor (7). More in particular, the filtering screen (41) is extending above the upper SCR-catalyst layer (8) from the SCR- catalyst layers (8, 8') of the SCR-reactor (7). [0053] A filtering screen (41) is provided with an upper and a lower surface (41a, 41b). The flue gas stream passes through a filtering screen (41) from the upper surface (41a) to the lower surface (41b) thereof. The filtering screen (41) is disposed at an incline to a horizontal plane. The filtering screen (41) can be positioned at an angle of 5.0 to 75.0° relative to a horizontal plane, in particular 5.5 to 60.0°, more in particular 6.0 to 45°, even more in particular 7.0 to 35.0°, still more in particular 7.5 to 25.0°, most in particular 7.5 to 20.0, like 10.0° or 15.0°, relative to a horizontal plane.
[0054] The filtering screen (41) comprises a barrier having a plurality of apertures therein to prevent the ash from passing through the filtering screen (41). The apertures more in particular have a diameter from 2 to 10mm, more in particular having a diameter of around 4 mm. The filtering screen (41) can be formed from one or more mesh screens. In that case, the mesh size is more in particular between 2 and 10 mm and more in particular around 4 mm. The filtering screen (41) may have a cross-section of 50% which allows for undisturbed flow of fly ash and retaining the bigger ash particles which cannot get through the SCR-catalysts. The filtering screen (41) can be made out of stainless steel.
[0055] The filtering screen unit (4) furthermore comprises a vibration device (42) that is in operative connection with the filtering screen (41) and that is configured to actively vibrate this filtering screen (41). The vibrating device (42) applies vibration, optionally continuous vibration, to the filtering screen (41) such that the filtered ash is agitated downwards across the upper surface (41a) of the inclined filtering screen (42) for collection. The vibration frequency of the filtering screen (41) may be between 5 Hz and 6,25 Hz. More in particular, the frequency of the filtering screen (41) may be around 5,4 Hz. The vibration device (42) may comprise a motor or a sound transducer. The vibration device (42) may produce a sinusoidal vibration. The resonance frequency of the filtering screen (41) may be determined, the vibration device (42) may produce a vibration with the same frequency of the resonance frequency of the filtering screen (41).
[0056] The vibration of the filtering screen (41) may result in constant movement of the ash particles on the filtering screen (41) in the down slope direction or the ash collector (43), resulting in a fast and efficient removal of the ash particles of the filtering screen (41), even when the filtering screen (41) is mounted in the duct under a shallow angle. The fast and efficient removal process of ash particles from the filtering screen result in a lower pressure drop SCR-system, compared to SCR-systems with a lesser efficient ash collecting systems.
[0057] To collect the ash particles that are vibrated downwards from the filtering screen (42), an ash collector (43) is arranged. The ash collector (43) can be sealed from the atmosphere. The ash collector (43) can comprise a conveyor, more in particular a chain or screw conveyor or a conveyor belt. The ash collector (43) can be in connection with any kind of ash collecting system (not shown in the figures). It is for instance possible to connect the ash collector (43) with a vertically positioned duct or pipe system (not shown on the figures) at the end of the ash collector (43) and into which the collected ash falls down by gravity and also because the pressure is higher there. The lower end of the duct / pipe system can be connected with the lower SCR-catalyst layer (8'). The duct / pipe thus serves as a kind of bypass over the SCR-catalyst layers (8, 8'). It is remarked that it is also possible to place the ash collector (43) and the pipe / duct inside the SCR-reactor (7).
[0058] In order to safely absorb the heat-induced expansion and contraction of the different parts of the system, to absorb the vibration of the vibration device (42) and to hold the parts of the system together, an expansion joint (44) can be provided between the vibration device (42) and the filtering screen (41).
[0059] The application also relates to a method for retroactively fitting a system for reducing an amount of NOx in a flue gas stream to a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of the flue gas stream to an outlet. At least one duct is essentially vertically disposed. The method comprises the step of installing an SCR-system (7) as disclosed above in the vertical duct. The combustion chamber is more in particular disposed in a first vertical duct (la), and the SCR-system can be installed in the second (lc) or third vertical duct downstream the first vertical duct.

Claims

C L A I M S
1 SCR (Selective Catalytic Reduction)-system for a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of a flue gas stream to an outlet, at least one duct being essentially vertically disposed, which SCR-system comprises:
an SCR-reactor comprising one or more SCR-catalyst layers each comprising one or more SCR-catalyst modules each comprising one or more SCR-catalysts arranged for reducing an amount of NOx in the flue gas stream, the SCR- reactor being configured for operative and fitting placement within the vertical duct, and
a filtering screen-unit comprising a filtering screen for filtering-out ash particles from the flue gas stream prior to entry into the one or more SCR- reactor wherein the filtering screen is arranged to protectively cover the SCR- reactor, and wherein the flue gas stream passes from an upper to a lower surface of the filtering screen,
wherein the filtering screen-unit further comprises a vibration device in operative connection with the filtering screen, configured to actively vibrate the filtering screen; and,
wherein the filtering screen is placed in an essentially vertical duct
2. SCR-system according to claim 1, wherein the filtering screen is placed in the same vertical duct wherein the SCR-reactor is fitted.
3. SCR-system according to claim 1 or 2, wherein the vibration device in operative connection with the filtering screen is configured to continuously vibrate the filtering screen.
4. SCR-system according to any one of claims 1 to 3, wherein the vibration frequency of the filtering screen is between 5.00 Hz and 6.25 Hz.
5. SCR-system according to any one of claims 1 to 4, wherein the filtering screen is positioned at an angle of 5.0 to 75.0° relative to a horizontal plane.
6. SCR-system according to any one of claims 1 to 5, wherein the filtering screen comprises a barrier having a plurality of apertures therein, the apertures having a diameter from 2 mm to 10 mm.
7. SCR-system according to any one of claims 1 to 6, wherein the filtering screen is formed from one or more mesh screens, more in particular having a mesh size of between 2 and 10 mm.
8. SCR-system according to any one of claims 1 to 7, wherein the at least one SCR- catalysts comprise catalytic particles in a fixed bed.
9. SCR-system according to any one of claims 1 to 8, wherein the SCR-system comprises an ash collector configured to receive the ash particles from the filtering screen.
10. SCR-system according to claim 9, wherein the ash collector comprises a conveyor.
11. SCR-system according to claim 9 or 10, wherein the ash collector is sealed from the atmosphere.
12. SCR-system according to any of previous claims, wherein the vibration device comprises a motor or a sound transducer.
13. SCR-system according to any of the previous claims, wherein the combustion system is a power boiler or a waste incinerator.
14. Combustion system comprising a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of a flue gas stream to an outlet, at least one duct being essentially vertically disposed, provided that a SCR-system according to any one of claims 1 to 13 is arranged in the vertical duct.
15. Combustion system according to claim 14, that is a power boiler, preferably a power boiler wherein the combustion chamber is provided in a first vertical duct and the
SCR-system is provided in a second vertical duct downstream of the first vertical duct, or a waste incinerator, preferably a waste incinerator wherein the combustion chamber is provided in a first vertical duct and the SCR-system is provided in a third vertical duct downstream of the first vertical duct.
16. Combustion system according to any of claims 14 to 15, further provided with a heat exchanger for extracting heat from the flue gas stream, wherein the SCR-system is disposed downstream of the heat exchanger.
17. Method for retroactively fitting a system for reducing an amount of NOx in a flue gas stream to a combustion system having a combustion chamber and an arrangement of ducts in connection with the combustion chamber for conduction of the flue gas stream, to an outlet at least one duct being essentially vertically disposed, comprising the step of installing an SCR-system according to any of claims 1 to 12 in the vertical duct.
18. Method according to claim 17, wherein the combustion chamber is disposed in a first vertical duct and the SCR-system is installed in a second or third vertical duct downstream of the first vertical duct.
EP18737171.1A 2017-06-23 2018-06-22 Scr-system for removing ash from a flue gas stream generated in a combustion system Withdrawn EP3641916A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP17177558.8A EP3417927A1 (en) 2017-06-23 2017-06-23 Scr-system for removing ash from a flue gas stream generated in a combustion system
PCT/EP2018/066738 WO2018234536A1 (en) 2017-06-23 2018-06-22 SCR SYSTEM FOR REMOVING ASHES FROM A COMBUSTION GAS STREAM GENERATED IN A COMBUSTION SYSTEM

Publications (1)

Publication Number Publication Date
EP3641916A1 true EP3641916A1 (en) 2020-04-29

Family

ID=59337418

Family Applications (2)

Application Number Title Priority Date Filing Date
EP17177558.8A Withdrawn EP3417927A1 (en) 2017-06-23 2017-06-23 Scr-system for removing ash from a flue gas stream generated in a combustion system
EP18737171.1A Withdrawn EP3641916A1 (en) 2017-06-23 2018-06-22 Scr-system for removing ash from a flue gas stream generated in a combustion system

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP17177558.8A Withdrawn EP3417927A1 (en) 2017-06-23 2017-06-23 Scr-system for removing ash from a flue gas stream generated in a combustion system

Country Status (2)

Country Link
EP (2) EP3417927A1 (en)
WO (1) WO2018234536A1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111013379B (en) * 2019-11-29 2024-06-04 华电电力科学研究院有限公司 Reciprocating vibration device for reducing dust accumulation and blockage of SCR denitration catalyst and working method of reciprocating vibration device
CN117180974B (en) * 2023-10-11 2025-10-17 润电能源科学技术有限公司 SCR denitration system

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19536444C2 (en) * 1995-09-29 1998-11-26 Siemens Ag Process for operating a catalytic converter arrangement in one or more parts, in particular for use in flue gas cleaning processes, and catalytic converter arrangement for carrying out the process
JP2001153327A (en) 1999-11-22 2001-06-08 Maejima Fumio Incinerator provided with ceramic filter
DE10227639B4 (en) 2002-06-20 2006-06-22 Steag Encotec Gmbh coal-fired power station
DE502005009308D1 (en) * 2005-02-14 2010-05-12 Evonik Energy Services Gmbh Arrangement for separating coarse ash from a flue gas stream
DE102006021670A1 (en) * 2006-05-10 2007-11-15 Lentjes Gmbh coarse ash separator
US8052766B2 (en) * 2006-08-16 2011-11-08 Alstom Technology Ltd Device and method for cleaning selective catalytic reduction protective devices
US8475573B2 (en) * 2009-08-25 2013-07-02 Babcock & Wilcox Power Generation Group, Inc. System and method for protection of SCR catalyst
US20110056417A1 (en) * 2009-09-10 2011-03-10 Electric Power Research Institute, Inc. Catalyst ash protector
KR101180699B1 (en) * 2010-05-20 2012-09-07 두산중공업 주식회사 Screen apparatus of a combustion system for preventing particle ashes from being accumulated
US8425850B1 (en) * 2010-12-08 2013-04-23 American Electric Power Company, Inc. Large particle ash mitigation system
CN102698597B (en) * 2012-06-18 2014-09-17 中国华电工程(集团)有限公司 Method and system for preventing catalyst blockage
KR101263829B1 (en) * 2012-10-04 2013-05-13 주식회사 지스코 Exhaust gas ventilation apparatus having dust removing fucntion
CN203469703U (en) * 2013-09-11 2014-03-12 湖南麓南脱硫脱硝科技有限公司 Ash removing and dust pre-removing device applicable to SCR (Selective Catalytic Reduction) denitrification system

Also Published As

Publication number Publication date
WO2018234536A1 (en) 2018-12-27
EP3417927A1 (en) 2018-12-26

Similar Documents

Publication Publication Date Title
JP4702761B2 (en) Sonic soot blower and its operation method
JP5743054B2 (en) Exhaust gas treatment equipment
TWI529353B (en) System and method for protection of scr catalyst
CN212283555U (en) SCR denitrification facility of cement kiln flue gas
CN117180974B (en) SCR denitration system
CN107970772A (en) A kind of SCR equipment for denitrifying flue gas
US6571420B1 (en) Device and process to remove fly ash accumulations from catalytic beds of selective catalytic reduction reactors
EP3641916A1 (en) Scr-system for removing ash from a flue gas stream generated in a combustion system
JP4858727B2 (en) Flue gas denitration equipment
KR101263829B1 (en) Exhaust gas ventilation apparatus having dust removing fucntion
WO2015098411A1 (en) Exhaust duct and boiler
JP5848032B2 (en) Smoke removal equipment
KR101623083B1 (en) Catalyst Pre Filter
EP3507544B1 (en) Scr-system for removing ash from a flue gas stream generated in a combustion system
CN220834953U (en) SCR denitration system
EP1965133B1 (en) Assembly for ash removal from a particle separator
JP7603385B2 (en) Denitrification equipment and cement kiln exhaust gas treatment equipment
JP4795801B2 (en) Gas purification device and exhaust gas treatment method
JP6785046B2 (en) How to remove exhaust ducts, boilers and solid particles
KR101294240B1 (en) The Large particle ash capture system for coal-fired power plant boiler
JP3489938B2 (en) Flue gas treatment equipment
WO2023053218A1 (en) Denitration device
KR101180699B1 (en) Screen apparatus of a combustion system for preventing particle ashes from being accumulated
CN223909561U (en) Biomass grate furnaces and biomass power generation units that meet nitrogen oxide emission standards
CN207287143U (en) A kind of online device for keeping denitrating catalyst activity

Legal Events

Date Code Title Description
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: UNKNOWN

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE

PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE

17P Request for examination filed

Effective date: 20200109

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

DAV Request for validation of the european patent (deleted)
DAX Request for extension of the european patent (deleted)
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN

18W Application withdrawn

Effective date: 20230605