US20120073483A1 - Method for supplying combustion air to a flue gas air preheater, a preheating apparatus, and an air guide sleeve - Google Patents
Method for supplying combustion air to a flue gas air preheater, a preheating apparatus, and an air guide sleeve Download PDFInfo
- Publication number
- US20120073483A1 US20120073483A1 US13/376,349 US201013376349A US2012073483A1 US 20120073483 A1 US20120073483 A1 US 20120073483A1 US 201013376349 A US201013376349 A US 201013376349A US 2012073483 A1 US2012073483 A1 US 2012073483A1
- Authority
- US
- United States
- Prior art keywords
- air
- guide sleeve
- flue gas
- air guide
- air pipe
- 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.)
- Abandoned
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 13
- 239000003546 flue gas Substances 0.000 claims 13
- 238000002485 combustion reaction Methods 0.000 claims 4
- 238000007493 shaping process Methods 0.000 claims 4
- 238000009413 insulation Methods 0.000 claims 3
- 239000004020 conductor Substances 0.000 claims 2
- 230000007423 decrease Effects 0.000 claims 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 229920006389 polyphenyl polymer Polymers 0.000 claims 1
- 230000001681 protective effect Effects 0.000 claims 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
- F28D7/1615—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium
- F28D7/1623—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation the conduits being inside a casing and extending at an angle to the longitudinal axis of the casing; the conduits crossing the conduit for the other heat exchange medium with particular pattern of flow of the heat exchange media, e.g. change of flow direction
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
- F23L15/04—Arrangements of recuperators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/002—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using inserts or attachments
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0001—Recuperative heat exchangers
- F28D21/0003—Recuperative heat exchangers the heat being recuperated from exhaust gases
-
- 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
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Definitions
- the invention relates to a method for supplying combustion air to a flue gas air preheater for combustion air in a boiler of a power plant. Furthermore, the invention relates to a flue gas air preheating apparatus for combustion air in a boiler of a power plant, as well as an air guide sleeve in an air pipe of a flue gas air preheater.
- flue gas air preheaters For preheating combustion air for a solid fuel boiler, flue gas air preheaters (LUVOs) are typically used, in which the heating medium, i.e. flue gas, flows outside heat exchanger pipes, and the medium to be heated, i.e. air, flows inside the heat exchanger pipes.
- the heat exchanger pipes (below: air pipes) are placed horizontally in the flue gas duct, and the heat exchanger units on different levels are connected to each other by air channels outside the flue gas duct.
- the flue gas flows inside the pipes and the pipes are vertical.
- the temperature of the air pipe is significantly low on the air inlet side.
- the considerable cooling effect of air at the inlet end of the pipe is due to the fact that at the point of inflow, the heat transfer coefficient of the flow is multiple compared to the developed flow deeper in the pipe.
- the air to be supplied has not been substantially warmed yet. Strong cooling induces a relatively low material temperature at the air inlet end of the heat exchanger structure of the preheater, in spite of the relatively high average temperature.
- the acid dew point of the flue gases may be reached at the surface of the heat exchanger structure.
- the acid dew point will cause strong corrosion in the cold heat exchanger structure and erosion in a short time, particularly with difficult fuels.
- the joint between the air pipe of the coldest LUVO bundle and the end plate (or the wall of the flue gas duct) may be corroded, if the temperature of the material is too low.
- the method according to the invention is primarily characterized in what will be presented in the independent claim 1 .
- the preheating apparatus for combustion air according to the invention is primarily characterized in what will be presented in the independent claim 4 .
- the air guide sleeve according to the invention is primarily characterized in what will be presented in the independent claim 13 .
- the other, dependent claims will present some preferred embodiments of the invention.
- the basic idea of the invention is to form a preheating apparatus for combustion air in a boiler by providing an air guide sleeve at the initial end of the air pipe, at least partly inside the air pipe, the air guide sleeve being made of a poorly heat conductive (i.e. thermally insulating) material and designed to diminish turbulence in the air flow.
- the air flow to be supplied into the air pipe is kept off the inner surface of the air pipe until the air flow has developed sufficiently, that is, the turbulence in the air flow has been sufficiently leveled out.
- the heat transfer coefficient of the developed air flow is significantly lower than that of a turbulent air flow, so that the air flow to be supplied from the air guide sleeve does not cause excessive cooling of the air pipe.
- turbulence in the combustion air flow to be supplied to the flue gas air preheater is leveled out by means of a structure keeping the airflow off the inner surface of the air pipe, after which the substantially turbulence-free combustion air flow is brought in contact with the inner surface of the air pipe, to heat the air.
- the corrosion shield or air guide sleeve according to the basic idea is made of a poorly heat conductive material, and it can be fitted inside the air pipe to diminish turbulence in the air flow and to guide the combustion air to be heated into the air pipe at a distance from the wall of the flue gas duct.
- the air guide sleeve is fitted to guide the combustion air to be heated into contact with the inner surface of the air pipe at a distance from the initial end of the air pipe, the distance being at least three times the diameter of the air pipe. In this way, the cooling of the outer surface of the initial end of the air pipe and the warming of air at the inlet point are minimized.
- the air guide sleeve is made at least partly of a polymer material, preferably heat-resistant plastic.
- the air guide sleeve is made of polyphenyl sulphide (PPS).
- the apparatus comprises a protective sleeve surrounding the air pipe at the initial end of the air pipe.
- the apparatus comprises a thermal insulation layer surrounding the flue gas duct, and the air guide sleeve extends through the insulation layer and the air pipe does not extend through the insulation layer.
- a single embodiment may comprise one or more of the following advantages depending on its implementation:
- FIG. 1 shows a power plant in a principle view
- FIG. 2 shows an embodiment of the flue gas air preheater in a principle view
- FIG. 3 shows one inlet of the flue gas air preheater in a cross-sectional view
- FIG. 4 shows another inlet of the flue gas air preheater
- FIG. 5 shows an embodiment of the air guide sleeve.
- FIG. 1 shows a power plant in a principle view.
- the power plant comprises a furnace 1 , a flue gas duct 2 , a flue gas air preheater 3 , and a stack 4 .
- the flue gas air preheater 3 is placed in the flue gas duct 2 .
- the flue gas air preheater 3 is placed at the terminal end of the flue gas duct 2 in the flow direction F of the flue gases.
- FIG. 2 shows an embodiment of the flue gas air preheater 3 in more detail.
- the air flows S, P to be heated are guided into the preheater 3 from air supply areas 5 , 6 in the lower part.
- the heated air is discharged from the upper part of the preheater.
- the preheater 3 comprises two air circulations, i.e. a primary air circulation P and a secondary air circulation S.
- Both air circulations P, S comprise air pipes 7 which are placed horizontally in the flue gas duct 2 , and the heat exchanger units on different levels are connected to each other by channels outside the flue gas duct.
- FIG. 3 shows one inlet of the flue gas air preheater 3 in a cross-sectional view.
- a unit in a typical vertical flue gas duct 2 comprises 20 to 30 pipes 7 on top of each other and about a hundred pipes adjacent to each other.
- the figure shows an air pipe 7 and an air guide sleeve 8 installed in the same.
- the air pipe 7 extends a short distance (about 1 ⁇ 3 of the length) into an insulation layer 9 that surrounds the flue gas duct 2 .
- the air pipe 7 is preferably welded in a gas-tight manner to the end plate (or inner wall) 10 of the flue gas duct 2 .
- the air guide sleeve 8 extends through the insulation layer 9 , and the outer surface of the air guide sleeve is connected tightly to the end of the air pipe 7 .
- silicone can be used for sealing.
- the inflow end 8 a of the air guide sleeve 8 i.e. the inlet of the air flow, is preferably shaped as a funnel.
- the length of the air guide sleeve 8 is advantageously more than three times the diameter of the air pipe 7 , preferably about 4 to 8 times the diameter of the air pipe or the air guide sleeve.
- the length of the air guide sleeve 8 is preferably about 20 to 40 cm.
- the end 8 b of the air guide sleeve 8 that is placed inside the air pipe 7 is shaped so as to induce no significant turbulence in the air flow discharging from the air guide sleeve.
- the end of the air guide sleeve 8 b is shaped so that the portion of the wall of the surface area limited by the outer circumference of the pipe decreases towards the end. In the configuration shown in the figure, this has been achieved by means of notches 8 c and thinning.
- the air guide sleeve 8 is provided with notches 8 c that become broader towards the end 8 b .
- the thickness of the wall of the air guide sleeve 8 has been reduced towards the end 8 b .
- the shaping that diminishes turbulence in the air flow is provided particularly at the end 8 b of the air guide sleeve within a length that constitutes about 1 ⁇ 6 to 1 ⁇ 3 of the length of the air guide sleeve.
- a clearance 11 is provided between the air guide sleeve 8 and the air pipe 7 .
- FIG. 4 shows one inlet of a flue gas air preheater according to another embodiment, in a cross-sectional view.
- a protective sleeve 12 is provided outside the air pipe 7 .
- the configuration according to FIG. 4 is particularly advantageous in structures to be retrofitted, already comprising the air pipe 7 and the protective sleeve 12 .
- the air guide sleeve 8 is fitted in the air inlet pipe 7 .
- the air pipe 7 and the protective sleeve 12 are cut out in such a way that they end inside the insulation material layer 9 . In this way, no heat will be conducted along the air pipe 7 and the protective sleeve 12 to the outside of the flue gas duct 2 .
- the air guide pipe 8 is connected to the end of the air pipe 7 in a gas-tight manner, for example with silicone or by another solution.
- FIG. 5 shows an advantageous embodiment of the air guide sleeve 8 , that is, the corrosion shield.
- the air guide sleeve 8 and particularly its outflow end 8 b are designed to diminish turbulence in the air flow.
- the end 8 b of the air guide sleeve is formed so that the portion of the wall of the surface area limited by the outer circumference of the pipe reduces towards the outflow end 8 b of the air guide sleeve 8 .
- the cross-sectional area available for the air flow increases towards the outflow end 8 b . This can be achieved, for example, by means of various notches 8 c and/or by thinning of the wall.
- the air guide sleeve 8 is provided with splits 8 c that become wider towards the end 8 b , and the thickness of the wall is reduced towards the end.
- the shaping that reduces turbulence in the air flow is provided particularly at the outflow end 8 b of the air guide sleeve 8 within a length that is about 1 to 3 three times the diameter of the air guide sleeve.
- elements 8 d are provided for controlling the clearance 11 between the outer surface of the air guide sleeve and the inner surface of the air pipe 7 .
- the elements 8 d are protrusions on the outer surface of the air guide sleeve 8 .
- protrusions 8 d are provided in two locations in the longitudinal direction of the air guide sleeve 8 and in four locations on the circumference.
- the shape and the number of the elements 8 d may vary according to the embodiment so that the desired clearance 11 between the outer surface of the air guide sleeve 8 and the inner surface of the air pipe 7 can be formed and maintained in use.
- the thickness and the material properties of the wall of the air guide sleeve 8 as well as the size of the clearance 11 are factors affecting the conduction of heat between the outer surface of the air pipe 7 and the inner surface of the air guide sleeve 8 .
- the air guide sleeve 8 can be made of a material having sufficient heat resistance and heat insulation properties.
- the heat resistance should be advantageously higher than 200° C., preferably higher than 250° C.
- the thermal conductivity should be advantageously lower than 0.3 W/(K*m) (23° C.).
- the materials used may be, for example, suitable polymers reinforced with glass fibre, such as PPS (polyphenyl sulphide, one commercial trademark being Fortron 1140 L6) or PPA (polyphtalamide).
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Air Supply (AREA)
Abstract
Description
- The invention relates to a method for supplying combustion air to a flue gas air preheater for combustion air in a boiler of a power plant. Furthermore, the invention relates to a flue gas air preheating apparatus for combustion air in a boiler of a power plant, as well as an air guide sleeve in an air pipe of a flue gas air preheater.
- For preheating combustion air for a solid fuel boiler, flue gas air preheaters (LUVOs) are typically used, in which the heating medium, i.e. flue gas, flows outside heat exchanger pipes, and the medium to be heated, i.e. air, flows inside the heat exchanger pipes. The heat exchanger pipes (below: air pipes) are placed horizontally in the flue gas duct, and the heat exchanger units on different levels are connected to each other by air channels outside the flue gas duct. There are also configurations, in which the flue gas flows inside the pipes and the pipes are vertical.
- In known configurations, the temperature of the air pipe is significantly low on the air inlet side. The considerable cooling effect of air at the inlet end of the pipe is due to the fact that at the point of inflow, the heat transfer coefficient of the flow is multiple compared to the developed flow deeper in the pipe. Furthermore, the air to be supplied has not been substantially warmed yet. Strong cooling induces a relatively low material temperature at the air inlet end of the heat exchanger structure of the preheater, in spite of the relatively high average temperature. Thus, the acid dew point of the flue gases may be reached at the surface of the heat exchanger structure. The acid dew point, in turn, will cause strong corrosion in the cold heat exchanger structure and erosion in a short time, particularly with difficult fuels. In particular, the joint between the air pipe of the coldest LUVO bundle and the end plate (or the wall of the flue gas duct) may be corroded, if the temperature of the material is too low.
- At the cold end (air inlet) of the LUVO pipe of the coldest LUVO bundles, various insulation sleeves fitted around the outer surface of the air pipe have been used to prevent corrosion of the air pipe.
- Now, a solution has been found that makes it possible to diminish the problem of corrosion at the joint between the air pipe of the preheating apparatus and the end plate.
- To achieve this aim, the method according to the invention is primarily characterized in what will be presented in the
independent claim 1. The preheating apparatus for combustion air according to the invention, in turn, is primarily characterized in what will be presented in theindependent claim 4. The air guide sleeve according to the invention, in turn, is primarily characterized in what will be presented in the independent claim 13. The other, dependent claims will present some preferred embodiments of the invention. - The basic idea of the invention is to form a preheating apparatus for combustion air in a boiler by providing an air guide sleeve at the initial end of the air pipe, at least partly inside the air pipe, the air guide sleeve being made of a poorly heat conductive (i.e. thermally insulating) material and designed to diminish turbulence in the air flow.
- By means of the air guide sleeve, the air flow to be supplied into the air pipe is kept off the inner surface of the air pipe until the air flow has developed sufficiently, that is, the turbulence in the air flow has been sufficiently leveled out. The heat transfer coefficient of the developed air flow is significantly lower than that of a turbulent air flow, so that the air flow to be supplied from the air guide sleeve does not cause excessive cooling of the air pipe.
- In the method according to the basic idea, turbulence in the combustion air flow to be supplied to the flue gas air preheater is leveled out by means of a structure keeping the airflow off the inner surface of the air pipe, after which the substantially turbulence-free combustion air flow is brought in contact with the inner surface of the air pipe, to heat the air.
- The corrosion shield or air guide sleeve according to the basic idea is made of a poorly heat conductive material, and it can be fitted inside the air pipe to diminish turbulence in the air flow and to guide the combustion air to be heated into the air pipe at a distance from the wall of the flue gas duct.
- In one embodiment, the air guide sleeve is fitted to guide the combustion air to be heated into contact with the inner surface of the air pipe at a distance from the initial end of the air pipe, the distance being at least three times the diameter of the air pipe. In this way, the cooling of the outer surface of the initial end of the air pipe and the warming of air at the inlet point are minimized.
- In one embodiment, the air guide sleeve is made at least partly of a polymer material, preferably heat-resistant plastic. In an advantageous embodiment, the air guide sleeve is made of polyphenyl sulphide (PPS).
- In an embodiment, the apparatus comprises a protective sleeve surrounding the air pipe at the initial end of the air pipe.
- In an embodiment, the apparatus comprises a thermal insulation layer surrounding the flue gas duct, and the air guide sleeve extends through the insulation layer and the air pipe does not extend through the insulation layer.
- The different embodiments of the above-described configuration, taken separately and in various combinations, provide various advantages. A single embodiment may comprise one or more of the following advantages depending on its implementation:
-
- the material temperature of the air pipe of the preheating apparatus can be raised at the air inflow point;
- the temperature at the joint between the air pipe of the preheating apparatus and the end plate becomes higher and the problem of corrosion is eliminated;
- the distortion of the temperature of the flue gases can be leveled out;
- the structure becomes simpler and the manufacture is faster.
- In the following, the invention will be described in more detail with reference to the appended principle drawings, in which
-
FIG. 1 shows a power plant in a principle view; -
FIG. 2 shows an embodiment of the flue gas air preheater in a principle view; -
FIG. 3 shows one inlet of the flue gas air preheater in a cross-sectional view; -
FIG. 4 shows another inlet of the flue gas air preheater; -
FIG. 5 shows an embodiment of the air guide sleeve. - For the sake of clarity, the drawings only show the details necessary for understanding the invention. The structures and details that are not necessary for understanding the invention but are obvious for anyone skilled in the art have been omitted from the figures in order to emphasize the characteristics of the invention.
-
FIG. 1 shows a power plant in a principle view. The power plant comprises afurnace 1, aflue gas duct 2, a fluegas air preheater 3, and astack 4. The fluegas air preheater 3 is placed in theflue gas duct 2. As can be seen from the figure, the fluegas air preheater 3 is placed at the terminal end of theflue gas duct 2 in the flow direction F of the flue gases. -
FIG. 2 shows an embodiment of the fluegas air preheater 3 in more detail. In this example, the air flows S, P to be heated are guided into thepreheater 3 fromair supply areas preheater 3 comprises two air circulations, i.e. a primary air circulation P and a secondary air circulation S. Both air circulations P, S compriseair pipes 7 which are placed horizontally in theflue gas duct 2, and the heat exchanger units on different levels are connected to each other by channels outside the flue gas duct. -
FIG. 3 shows one inlet of the fluegas air preheater 3 in a cross-sectional view. A unit in a typical verticalflue gas duct 2 comprises 20 to 30pipes 7 on top of each other and about a hundred pipes adjacent to each other. The figure shows anair pipe 7 and anair guide sleeve 8 installed in the same. In the example, theair pipe 7 extends a short distance (about ⅓ of the length) into aninsulation layer 9 that surrounds theflue gas duct 2. Theair pipe 7 is preferably welded in a gas-tight manner to the end plate (or inner wall) 10 of theflue gas duct 2. In the example, theair guide sleeve 8 extends through theinsulation layer 9, and the outer surface of the air guide sleeve is connected tightly to the end of theair pipe 7. For example, silicone can be used for sealing. The inflow end 8 a of theair guide sleeve 8, i.e. the inlet of the air flow, is preferably shaped as a funnel. - The length of the
air guide sleeve 8 is advantageously more than three times the diameter of theair pipe 7, preferably about 4 to 8 times the diameter of the air pipe or the air guide sleeve. For example, if the diameter of theair pipe 7 is about 50 mm, the length of theair guide sleeve 8 is preferably about 20 to 40 cm. - The
end 8 b of theair guide sleeve 8 that is placed inside theair pipe 7 is shaped so as to induce no significant turbulence in the air flow discharging from the air guide sleeve. In the example, the end of theair guide sleeve 8 b is shaped so that the portion of the wall of the surface area limited by the outer circumference of the pipe decreases towards the end. In the configuration shown in the figure, this has been achieved by means ofnotches 8 c and thinning. Theair guide sleeve 8 is provided withnotches 8 c that become broader towards theend 8 b. The thickness of the wall of theair guide sleeve 8, in turn, has been reduced towards theend 8 b. In the example, the shaping that diminishes turbulence in the air flow is provided particularly at theend 8 b of the air guide sleeve within a length that constitutes about ⅙ to ⅓ of the length of the air guide sleeve. - In the embodiment shown in
FIG. 3 , aclearance 11 is provided between theair guide sleeve 8 and theair pipe 7. By means of theclearance 11 and theair guide sleeve 8, the conduction of heat from the outer surface of theair pipe 7 to the inside of the air guide sleeve is efficiently prevented, thereby preventing the cooling of the initial end of the air pipe. -
FIG. 4 , in turn, shows one inlet of a flue gas air preheater according to another embodiment, in a cross-sectional view. In this embodiment, aprotective sleeve 12 is provided outside theair pipe 7. The configuration according toFIG. 4 is particularly advantageous in structures to be retrofitted, already comprising theair pipe 7 and theprotective sleeve 12. In such a case, theair guide sleeve 8 is fitted in theair inlet pipe 7. Theair pipe 7 and theprotective sleeve 12 are cut out in such a way that they end inside theinsulation material layer 9. In this way, no heat will be conducted along theair pipe 7 and theprotective sleeve 12 to the outside of theflue gas duct 2. It is also advantageous to connect the ends of theprotective sleeve 12 to theair pipe 7, for example by welding. Theair guide pipe 8, in turn, is connected to the end of theair pipe 7 in a gas-tight manner, for example with silicone or by another solution. -
FIG. 5 shows an advantageous embodiment of theair guide sleeve 8, that is, the corrosion shield. Theair guide sleeve 8 and particularly itsoutflow end 8 b are designed to diminish turbulence in the air flow. Advantageously, theend 8 b of the air guide sleeve is formed so that the portion of the wall of the surface area limited by the outer circumference of the pipe reduces towards theoutflow end 8 b of theair guide sleeve 8. In other words, the cross-sectional area available for the air flow increases towards theoutflow end 8 b. This can be achieved, for example, by means ofvarious notches 8 c and/or by thinning of the wall. In the example, theair guide sleeve 8 is provided withsplits 8 c that become wider towards theend 8 b, and the thickness of the wall is reduced towards the end. In the example, the shaping that reduces turbulence in the air flow is provided particularly at theoutflow end 8 b of theair guide sleeve 8 within a length that is about 1 to 3 three times the diameter of the air guide sleeve. - On the outer surface of the
air guide sleeve 8,elements 8 d are provided for controlling theclearance 11 between the outer surface of the air guide sleeve and the inner surface of theair pipe 7. In the example, theelements 8 d are protrusions on the outer surface of theair guide sleeve 8. In the example,protrusions 8 d are provided in two locations in the longitudinal direction of theair guide sleeve 8 and in four locations on the circumference. The shape and the number of theelements 8 d may vary according to the embodiment so that the desiredclearance 11 between the outer surface of theair guide sleeve 8 and the inner surface of theair pipe 7 can be formed and maintained in use. The thickness and the material properties of the wall of theair guide sleeve 8 as well as the size of theclearance 11 are factors affecting the conduction of heat between the outer surface of theair pipe 7 and the inner surface of theair guide sleeve 8. - The
air guide sleeve 8 can be made of a material having sufficient heat resistance and heat insulation properties. The heat resistance should be advantageously higher than 200° C., preferably higher than 250° C. The thermal conductivity should be advantageously lower than 0.3 W/(K*m) (23° C.). The materials used may be, for example, suitable polymers reinforced with glass fibre, such as PPS (polyphenyl sulphide, one commercial trademark being Fortron 1140 L6) or PPA (polyphtalamide). - By combining, in various ways, the modes and structures disclosed in connection with the different embodiments of the invention presented above, it is possible to produce various embodiments of the invention in accordance with the spirit of the invention. Therefore, the above-presented examples must not be interpreted as restrictive to the invention, but the embodiments of the invention may be freely varied within the scope of the inventive features presented in the claims hereinbelow.
Claims (12)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
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FI20095621 | 2009-06-04 | ||
FI20095621A FI123881B (en) | 2009-06-04 | 2009-06-04 | Flue gas preheating device for combustion air of the power plant boiler and its air control sleeve |
PCT/FI2010/050414 WO2010139852A1 (en) | 2009-06-04 | 2010-05-21 | A method for supplying combustion air to a flue gas air preheater, a preheating apparatus, and an air guide sleeve |
Publications (1)
Publication Number | Publication Date |
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US20120073483A1 true US20120073483A1 (en) | 2012-03-29 |
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ID=40825325
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US13/376,349 Abandoned US20120073483A1 (en) | 2009-06-04 | 2010-05-21 | Method for supplying combustion air to a flue gas air preheater, a preheating apparatus, and an air guide sleeve |
Country Status (13)
Country | Link |
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US (1) | US20120073483A1 (en) |
EP (1) | EP2438356B1 (en) |
CN (1) | CN102460021B (en) |
BR (1) | BRPI1012977B1 (en) |
CA (1) | CA2763578C (en) |
CL (1) | CL2011003062A1 (en) |
DK (1) | DK2438356T3 (en) |
ES (1) | ES2636744T3 (en) |
FI (1) | FI123881B (en) |
PL (1) | PL2438356T3 (en) |
PT (1) | PT2438356T (en) |
RU (1) | RU2524982C2 (en) |
WO (1) | WO2010139852A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140352931A1 (en) * | 2013-05-31 | 2014-12-04 | Steve Turner | Corrosion Resistant Air Preheater with Lined Tubes |
US20220333880A1 (en) * | 2019-09-02 | 2022-10-20 | Orion Engineered Carbons Ip Gmbh & Co. Kg | Anti-Fouling Device for Heat Exchangers and Its Use |
US11585613B2 (en) * | 2016-04-18 | 2023-02-21 | Corrosion Monitoring Service, Inc. | System and method for installing external corrosion guards |
US12264885B2 (en) * | 2019-09-02 | 2025-04-01 | Orion Engineered Carbons Ip Gmbh & Co. Kg | Anti-fouling device for heat exchangers and its use |
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CN103693627A (en) * | 2013-12-19 | 2014-04-02 | 中江能源回收(上海)有限公司 | High-temperature air preheater structure for sulfur acid preparation |
CN103968689A (en) * | 2014-05-26 | 2014-08-06 | 英尼奥斯欧洲股份公司 | Waste water cooler used in acrylonitrile manufacture |
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US20140352931A1 (en) * | 2013-05-31 | 2014-12-04 | Steve Turner | Corrosion Resistant Air Preheater with Lined Tubes |
US11149945B2 (en) * | 2013-05-31 | 2021-10-19 | Corrosion Monitoring Service, Inc. | Corrosion resistant air preheater with lined tubes |
US11585613B2 (en) * | 2016-04-18 | 2023-02-21 | Corrosion Monitoring Service, Inc. | System and method for installing external corrosion guards |
US20220333880A1 (en) * | 2019-09-02 | 2022-10-20 | Orion Engineered Carbons Ip Gmbh & Co. Kg | Anti-Fouling Device for Heat Exchangers and Its Use |
US12264885B2 (en) * | 2019-09-02 | 2025-04-01 | Orion Engineered Carbons Ip Gmbh & Co. Kg | Anti-fouling device for heat exchangers and its use |
Also Published As
Publication number | Publication date |
---|---|
EP2438356A1 (en) | 2012-04-11 |
CA2763578A1 (en) | 2010-12-09 |
CN102460021A (en) | 2012-05-16 |
CN102460021B (en) | 2014-11-26 |
PL2438356T3 (en) | 2017-10-31 |
EP2438356A4 (en) | 2015-01-07 |
CL2011003062A1 (en) | 2012-08-31 |
FI123881B (en) | 2013-11-29 |
ES2636744T3 (en) | 2017-10-09 |
WO2010139852A1 (en) | 2010-12-09 |
CA2763578C (en) | 2017-07-11 |
FI20095621L (en) | 2010-12-05 |
RU2524982C2 (en) | 2014-08-10 |
BRPI1012977B1 (en) | 2020-08-11 |
EP2438356B1 (en) | 2017-05-10 |
RU2011153616A (en) | 2013-07-20 |
BRPI1012977A2 (en) | 2018-01-16 |
DK2438356T3 (en) | 2017-07-24 |
FI20095621A0 (en) | 2009-06-04 |
PT2438356T (en) | 2017-08-08 |
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