CN208983320U - A kind of high-temperature acidic flue gas economizer prevents swollen support construction - Google Patents
A kind of high-temperature acidic flue gas economizer prevents swollen support construction Download PDFInfo
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- CN208983320U CN208983320U CN201821589840.6U CN201821589840U CN208983320U CN 208983320 U CN208983320 U CN 208983320U CN 201821589840 U CN201821589840 U CN 201821589840U CN 208983320 U CN208983320 U CN 208983320U
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Abstract
The utility model discloses a kind of high-temperature acidic flue gas economizers to prevent swollen support construction, including heat transfer flue and economizer, and the support plate with stream flue gas port is equipped in heat transfer flue, is provided with economizer in support plate；Economizer is connected to the heat exchange tube panel formed by several heat exchanger tubes in a row；It further include connector and several support rims, connector includes the fixed link being arranged in pairs, the cooperation support slipper that is connected to the fixed plate being arranged in pairs between fixed link, bottom of fixed is arranged in；Pairs of fixed link is a pair of of support component, and support component is equipped with multiple groups along heat exchange tube panel, and the through-hole with heat exchanger tube cooperation support is provided in the fixed plate of every group of support component, and the through-hole cooperation on heat exchanger tube and muti-piece fixed plate wears support；Cooperation support slipper is contacted with the cooperation of support rim contact surface；Support rim is set in support plate.Economizer is flexibly placed in support plate, simplifies the mounting structure of economizer, gives economizer sufficient expansion displacement space in use.
Description
Technical field
The utility model relates to flue residue heat recycling fields, and in particular to a kind of high-temperature acidic flue gas economizer prevents swollen support
Structure.
Background technique
The energy-saving and emission-reduction of Large-scale fire-electricity unit are the important state basic policies of current country, stringent with national energy conservation and emission reduction index
It is required that and coal price rise fluctuation, the cost of electricity-generating based on coal increasingly increases, and each power plant is faced with energy-efficient huge pressure
Power.In order to reduce exhaust gas temperature, flue gas loss is reduced, performance driving economy is improved, is industrially commonly used in boiler
Install economizer on back-end ductwork additional.
Technical solution disclosed in CN206094053U is circulating fluid-bed coal-burning boiler energy-saving economizer, including from top to bottom
Higher level's economizer, SCR catalyst structure and the junior's economizer being connected in boiler, higher level's economizer include from top to bottom successively
Higher level's economizer exit header of setting, upper the Tubes of Membrane Economizer and higher level's economizer import header, junior's economizer wrap respectively
Include the junior's economizer exit header set gradually under, lower the Tubes of Membrane Economizer and junior's economizer import header；Higher level
Economizer import header connects the water route of junior's economizer exit header by pipeline one and pipeline two.It is fixed in above structure to connect
Connecing is to connect and fix, although easy to disassemble, also have ignored the expanded by heating displacement of economizer in use process, easily influences it
Service life.
Economizer ontology both ends are respectively equipped with economizer exit flue and province in technical solution disclosed in CN206234809U
Coal device inlet flue duct, economizer ontology upper and lower ends are equipped with header, and header is connect with the base tube that economizer body interior is equipped with；It saves
Coal device ontology includes the enamel low-level (stack-gas) economizer module that several outsides are equipped with frame, if enamel low-level (stack-gas) economizer inside modules are equipped with
Dry fagging, several faggings are connect with frame, and enamel low-level (stack-gas) economizer module both ends are additionally provided with sealing plate, sealing plate and frame in frame
Frame connection.Above structure although solve low-level (stack-gas) economizer in operation dust stratification, blocking, corrosion the problems such as, but sealing plate and frame
The setting of frame greatly limits economizer displacement space needed for expanded by heating in use, will increase to sealing plate and frame
The support force of frame, to destroy the stability and leakproofness of structure.
Economizer mentioned by above scheme does not consider the expanded by heating displacement of economizer in use process.Therefore, have
Necessity carries out structure improvement to the installation of economizer in the prior art, and expansion displacement in use process can be met by making one kind
Economizer.
Utility model content
The purpose of the utility model is to overcome defects existing in the prior art, provide a kind of high-temperature acidic flue gas province coal
Device prevents swollen support construction, avoids economizer expansion displacement damage caused by overall structure in use process.
In order to realize the above technical effect, the technical solution of the utility model are as follows: a kind of high-temperature acidic flue gas economizer is prevented swollen
Support construction, including heat transfer flue and economizer, heat transfer flue is interior to be equipped with the support plate with stream flue gas port, is arranged in support plate
There is economizer；Economizer is connected to the heat exchange tube panel formed by several heat exchanger tubes in a row, and heat exchange tube panel is equipped with and enters supply mains
The water inlet and water outlet being cooperatively connected with outfall sewer；It further include connector and several support rims, connector includes pairs of
The fixed link of setting, the cooperation support slipper for being connected to the fixed plate being arranged in pairs between fixed link, bottom of fixed being set；
Pairs of fixed link is a pair of of support component, and support component is equipped with multiple groups along heat exchange tube panel, in the fixed plate of every group of support component
It is provided with the through-hole with heat exchanger tube cooperation support, the through-hole cooperation on heat exchanger tube and muti-piece fixed plate wears support；Cooperation support
Sliding block is contacted with the cooperation of support rim contact surface；Support rim is set in support plate.
Through the above technical solutions, simplifying the installation steps of economizer, economizer need to be only placed on support rim, and
Guarantee that support rim is corresponding with cooperation support slipper.Fixed knot is not set between support rim and cooperation support slipper
Structure ensure that the sufficient displacement space of economizer in use.
Specifically, the contact surface of support rim and/or cooperation support slipper is equipped with sliding layer.Sliding layer includes polytetrafluoro
Vinyl coating and stainless steel layer.Such structure increases support rim and cooperates the smoothness of contact surface between support slipper,
Keep economizer economizer expansion displacement more sensitive.
Preferred technical solution be further include position-limit mechanism, position-limit mechanism be retention bead and it is fixed on the supporting plate, limit
Position protrusion is set to the periphery of support rim, and retention bead is higher than support rim；Support rim among several support rims
For center support rim, left phase is equipped between retention bead and support rim from length and right phase from length, central supported boss
Left phase from length and right phase from equal length, be initial phase from length L/2；Support rim on the left of central supported boss
Left phase be successively incremented by L outward from length, right phase is constant from length；The right side of support rim on the right side of central supported boss
Mutually successively it is incremented by L outward from length, left phase is constant from length；The calculation formula of L specifically:
L=α × Δ T × L0；Wherein:
L is mutually from length；
α is the coefficient of expansion；
Δ T is temperature difference；
L0For metal length.
Such design, the i.e. displacement space of guarantee economizer in use, also the displacement of economizer sets up limit
System, improves the stability of economizer.Meanwhile the different settings by the left phase at center to two sides from length from right phase from length,
Make the more accurate displacement for controlling economizer of retention bead.
Preferred technical solution be further include position-limit mechanism, position-limit mechanism is limit baffle, and limit baffle is downwardly projecting simultaneously
It is located on cooperation support slipper periphery；It limits and is equipped with left phase between baffle and support rim from length and right phase from length, be located at
Support rim among several support rims is center support rim, and the left phase of central supported boss is from length with right phase from length
It is equal, it is initial phase from length L/2；The right phase of support rim on the left of central supported boss is successively passed outward from length
Increase L, left phase is constant from length；The left phase of support rim on the right side of central supported boss is successively incremented by L from length outward,
Right phase is constant from length；The calculation formula of L specifically:
L=α × Δ T × L0；Wherein:
L is mutually from length；
α is the coefficient of expansion；
Δ T is temperature difference；
L0For metal length.
Such design, the i.e. displacement space of guarantee economizer in use, also the displacement of economizer sets up limit
System, improves the stability of economizer.Meanwhile the different settings by the left phase at center to two sides from length from right phase from length,
Make to limit the more accurate displacement for controlling economizer of baffle.
Preferred technical solution be further include several dust-proof roll films, dust-proof roll film by sheet metal interior end edge side outward
Roll gained；Outer end edges are fixed on the lower part of cooperation support slipper, and adjacent two dust-proof roll film is fitted close or lap fit；It is dust-proof
The press of roll film elasticity is set in support rim side wall and support plate.Such structure, effectively prevents in use process, dust etc.
Fine impurities enter support rim and cooperate the contact surface between support slipper；Meanwhile the elasticity of dust-proof roll film makes it can be with
The displacement of economizer and move, expansion displacement will not be caused to limit.
Preferred technical solution be further include recessed baffle and the cooperation baffle matched with recessed baffle, recessed baffle
One end with limit baffle periphery be connected, and ring set with limit baffle periphery；Between the connecting pin and free end of recessed baffle
Equipped with recess under ring-type；Cooperation baffle is located at the lower section of recessed baffle, including the first cooperation baffle and several second cooperation baffles；
One end of first cooperation baffle is connected with support rim periphery, and is located on support rim periphery；Second cooperation baffle annular
Protrusion setting cooperates baffle upper surface first, and is equipped with recess under ring-type, and the second cooperation baffle is contained under ring-type
Recess, and the upper end of the second cooperation baffle and cyclic annular lower pocket top have gap；Recessed baffle combines to be formed with cooperation baffle
It is bent the dust-proof labyrinth circuit of detour.Horizontal distance and the second cooperation baffle institute between second cooperation baffle and cyclic annular lower recess
The left phase between baffle is limited where recess under support rim and ring-type to be adapted to from length and right phase from length.It is such to set
Meter is effectively prevented in use process, dust etc. is tiny miscellaneous using the interaction barrier effect of recessed baffle and cooperation baffle
Matter enters support rim and cooperates the contact surface between support slipper；Water between second cooperation baffle and cyclic annular lower recess simultaneously
The correspondence suitability of flat distance reduces second cooperation baffle interference caused by expansion displacement, optimizes the dustproof construction.
Preferred technical solution be further include connecting plate and connection sheet with through-hole, connecting plate is respectively arranged on heat exchanger tube
Shield two sides, heat exchanger tube is set in through-hole；One end of connection sheet is fixedly connected with heat transfer flue inner wall, the other end and connecting plate medial surface
Elastic Contact；Connection sheet is respectively arranged on the two sides up and down of connecting plate.Such structure, further reinforces economizer.
In normal condition, connection sheet produces certain pulling force to economizer by connecting plate；In use, the bullet of connection sheet
Property contact jaw can be moved as connecting plate moves outward, and can mobile generation one stable pulling force to connecting plate；To province
Coal device, which has carried out left and right limit, reduces double swerve caused by extraneous factor, meanwhile, fortune is displaced to the expanded by heating of economizer
It is dynamic to be stablized.
Specifically, being welded with metal spiral fin in heat exchange pipe outer wall.Such structure expands flue gas heat exchange contact
Area increases heat exchange efficiency.
Advantages and beneficial effects of the utility model lie in that economizer is flexibly placed in support plate, economizer is simplified
Mounting structure, give economizer sufficient expansion displacement space in use.
Detailed description of the invention
Fig. 1 is that a kind of high-temperature acidic flue gas economizer of the utility model prevents that the front view structure of swollen support construction embodiment 1 is shown
It is intended to；
Fig. 2 is the side structure schematic view of support plate and connector in embodiment 1；
Fig. 3 is the schematic view of the front view of embodiment 2；
Fig. 4 is the enlarged structure schematic diagram of part A in embodiment 2；
Fig. 5 is the schematic view of the front view of embodiment 3；
Fig. 6 is the enlarged structure schematic diagram of part B in embodiment 3；
Fig. 7 is the schematic view of the front view of embodiment 4；
Fig. 8 is the enlarged structure schematic diagram of C portion in embodiment 4.
In figure: 1, heat transfer flue；2, support plate；3, flue gas port；4, heat exchanger tube；5, water inlet；6, water outlet；7, it supports
Boss；7-1, central supported boss；8, fixed link；9, fixed plate；10, cooperate support slipper；11, through-hole；12, sliding layer；13,
Connecting plate；14, connection sheet；15, retention bead；16, dust-proof roll film；17, baffle is limited；18, recessed baffle；Under 18-1, ring-type
Recess；19, cooperate baffle；19-1, the first cooperation baffle；19-2, the second cooperation baffle；20, dust-proof baffle；21, metal spiral
Fin.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is further described.Implement below
Example is only used for clearly illustrating the technical solution of the utility model, and cannot be used as a limitation the protection model of limitation the utility model
It encloses.
Embodiment 1
As shown in Fig. 1 to 2, the high-temperature acidic flue gas economizer of embodiment 1 prevents swollen support construction, including heat transfer flue 1 with
Economizer, heat transfer flue 1 is interior to be equipped with the support plate 2 with flue gas port 3, is provided with economizer in support plate 2；If economizer be by
Do the heat exchange tube panel of heat exchanger tube 4 in a row connection composition, heat exchange tube panel is equipped with and enters supply mains and outfall sewer is cooperatively connected
Water inlet 5 and water outlet 6；It further include connector and several support rims 7, connector includes the fixed link 8 being arranged in pairs, connection
In the fixed plate 9 being arranged in pairs between fixed link 8, the cooperation support slipper 10 of 8 bottom of fixed link is set；Pairs of fixed link
8 be a pair of of support component, and support component is equipped with multiple groups along heat exchange tube panel, is provided with and changes in the fixed plate 9 of every group of support component
The through-hole 11 of the cooperation support of heat pipe 4, heat exchanger tube 4 wear support with the cooperation of through-hole 11 in muti-piece fixed plate 9；Cooperate support slipper
10 contact with the cooperation of 7 contact surface of support rim；Convex 7 are supported to be set in support plate 2；On the contact surface for cooperating support slipper 10
Equipped with sliding layer 12, sliding layer 12 is polytetrafluorethylecoatings coatings；Further include connecting plate 13 and connection sheet 14 with through-hole 11, connects
Fishplate bar 13 is respectively arranged on heat exchange tube panel two sides, and heat exchanger tube 4 is set in through-hole 11；One end of connection sheet 14 is fixedly connected with heat transfer flue
1 inner wall, the other end and 13 medial surface Elastic Contact of connecting plate；Connection sheet 14 is respectively arranged on the two sides up and down of connecting plate 13.
Before economizer installation, installation and the cooperation of cooperation 10 phase position of support slipper and one-to-one branch in support plate 2
Support boss 7.When installation, the economizer equipped with fixing piece is placed in 7 top of support rim, slides support rim 7 and cooperation support
Block 10 matches contact；Then, one end of connection sheet 14 is connected with 1 inner sidewall of heat transfer flue, the other end of connection sheet 14
With 13 medial surface Elastic Contact of connecting plate.It before work, opens into supply mains, if high-temperature flue gas will be from from top to bottom passing through heat exchange
Flue then enters supply mains and is connected with water inlet 5；It is connected conversely, then entering supply mains with water outlet 6.When work, a large amount of high temperature
Flue gas can make economizer expanded by heating by economizer.Due to non-sticking lining set on the projecting surface of cooperation support slipper 10
12, make that support slipper 10 and the coefficient of friction of the contact surface of support rim 7 is cooperated to greatly reduce, it will not be to the expanding position of economizer
Shift-in row limitation.Simultaneously as the connection sheet 14 of two sides has pulling force outward to connecting plate 13, economizer can be made expanded
Displacement in journey is relatively gentle, is not in whole the case where offseting to one side.
Embodiment 2
As shown in Figs. 3-4, embodiment 2 the difference from embodiment 1 is that, further include the limit convex being fixed in support plate 2
15 are played, retention bead 15 is set to the periphery of support rim 7, and retention bead 15 is higher than support rim 7；Positioned at several support rims 7
Intermediate support rim 7 is center support rim 7-1, and left phase is equipped between retention bead 15 and support rim 7 from length and the right side
Mutually from length, the left phase of central supported boss 7-1, from equal length, is initial phase from length L/2 from length and right phase；In being located at
The left phase of support rim on the left of heart support rim 7-1 is successively incremented by L from length outward, and right phase is constant from length；In being located at
The right phase of support rim on the right side of heart support rim 7-1 is successively incremented by L from length outward, and left phase is constant from length；The calculating of L
Formula specifically:
The calculation formula of L specifically:
L=α × Δ T × L0；Wherein:
L is mutually from length；
α is the coefficient of expansion；
Δ T is temperature difference；
L0For metal length.
It further include several dust-proof roll films 16, by the interior end edge of sheet metal, side rolls gained to dust-proof roll film 16 outward；Outer end
While being fixed on the lower part of cooperation support slipper 10, adjacent two dust-proof roll film 16 is fitted close or lap fit；Dust-proof 16 bullet of roll film
Property press be set in 7 side wall of support rim and support plate 2.
At work, economizer is heated is expanded outward by center, the setting of retention bead 15, i.e., without limitation on economizer
Lateral displacement, also play the role of limit to economizer.Meanwhile the setting of dust-proof roll film 16 can avoid economizer and be displaced
When, the impurity (solid particle) in flue gas enters the contact surface between cooperation support slipper 10 and support rim 7, increases displacement
Frictional force.
Embodiment 3
As shown in FIG. 5 and 6, embodiment 3 the difference from embodiment 1 is that, further include limit baffle 17, the limit baffle
17 is downwardly projecting and be located on cooperation support slipper 10 periphery；Between the limit baffle 17 and support rim 7 be equipped with left phase from
Length is with right phase from length, and the support rim 7 among several support rims 7 is center support rim 7-1, and central supported is convex
The left phase of platform 7-1, from equal length, is initial phase from length L/2 from length and right phase；On the left of central supported boss 7-1
The right phase of support rim 7 is successively incremented by L from length outward, and left phase is constant from length；On the right side of central supported boss 7-1
The left phase of support rim 7 is successively incremented by L from length outward, and right phase is constant from length；The calculation formula of L specifically:
L=α × Δ T × L0；Wherein:
L is mutually from length；
α is the coefficient of expansion；
Δ T is temperature difference；
L0For metal length.
The cooperation baffle 19 for further including recessed baffle 18 and being matched with recessed baffle 18, one end of recessed baffle 18 and limit
Position 17 periphery of baffle is connected, and ring is set and 17 periphery of limit baffle；It is equipped between the connecting pin and free end of recessed baffle 18
The lower recess 18-1 of ring-type；Cooperation baffle 19 is located at the lower section of recessed baffle 18, including the first cooperation baffle 19-1 and several second
Cooperate baffle 19-2；One end of first cooperation baffle 19-1 is connected with 7 periphery of support rim, and is located on outside support rim 7
It encloses；Second cooperation baffle 19-2 annular protrusion setting cooperates the upper surface baffle 19-2 first, and matches with recess 18-1 under ring-type
Setting is closed, the second cooperation baffle 19-2 is contained in recess under ring-type, and the upper end of the second cooperation baffle 19-2 and cyclic annular lower recess
There is gap at the top of 18-1；Recessed baffle 18 combines the dust-proof labyrinth circuit for forming bending detour with cooperation baffle 19.Second matches
Close the horizontal distance between 19-2 baffle and cyclic annular lower recess 18-1 and support rim 7 and ring-type where the second cooperation baffle 19-2
Left phase where lower recess 18-1 between limit baffle 17 is adapted to from length and right phase from length.
At work, economizer is heated is expanded outward by center, limits the setting of baffle 17, i.e., without limitation on economizer
Lateral displacement, also play the role of limit to economizer.Meanwhile the setting of recessed baffle 18 and cooperation baffle 19 can be significantly
Reduce the contact surface that the impurity (solid particle) in flue gas enters between cooperation support slipper 10 and support rim 7.
Embodiment 4
As shown in Fig. 7 to 8, embodiment 4 and the difference of embodiment 3 are, are welded with metal spiral in the pipe outer wall that exchanges heat
Fin 21；Recessed 18 top of baffle is equipped with dust-proof baffle 20, and recessed baffle 18 is located above cyclic annular lower recess 18-1.Such knot
Structure increases heat exchange contact area when work, meanwhile, dust stratification in recess 18-1 can be effectively prevent under ring-type.
The above is only the preferred embodiment of the utility model, it is noted that for the common skill of the art
For art personnel, without deviating from the technical principle of the utility model, several improvements and modifications can also be made, these change
It also should be regarded as the protection scope of the utility model into retouching.
Claims (10)
1. a kind of high-temperature acidic flue gas economizer prevents swollen support construction, including heat transfer flue and economizer, in the heat transfer flue
Equipped with the support plate with flue gas port, economizer is provided in support plate；The economizer is connected to by several heat exchanger tubes in a row
The heat exchange tube panel of composition, heat exchange tube panel be equipped with the water inlet and water outlet that enter supply mains and outfall sewer and be cooperatively connected,
It is characterized in that, further includes connector and several support rims, the connector includes the fixed link being arranged in pairs, is connected in pairs
The cooperation support slipper that fixed plate between fixed link is set, bottom of fixed is set；The pairs of fixed link is a pair
Support component, the support component are equipped with multiple groups along heat exchange tube panel, are provided in the fixed plate of every group of support component and heat exchanger tube
Cooperate the through-hole of support, the through-hole cooperation on the heat exchanger tube and muti-piece fixed plate wears support；The cooperation support slipper with
The cooperation contact of support rim contact surface；The support rim is set in support plate.
2. high-temperature acidic flue gas economizer according to claim 1 prevents swollen support construction, which is characterized in that the support is convex
The contact surface of platform and/or cooperation support slipper is equipped with sliding layer.
3. high-temperature acidic flue gas economizer according to claim 1 prevents swollen support construction, which is characterized in that further include limit
Mechanism, the position-limit mechanism are retention bead and fix on the supporting plate that the retention bead is set to the periphery of support rim, limit
Position protrusion is higher than support rim；Support rim among several support rims is center support rim, the retention bead
Left phase is equipped between support rim from length and right phase from length, the left phase of central supported boss is from length with right phase from length
It is equal, it is initial phase from length L/2；The left phase of support rim on the left of central supported boss is successively passed outward from length
Increase L, right phase is constant from length；The right phase of support rim on the right side of central supported boss is successively incremented by L from length outward,
Left phase is constant from length.
4. high-temperature acidic flue gas economizer according to claim 1 prevents swollen support construction, which is characterized in that further include limit
Mechanism, the position-limit mechanism are limit baffle, and the limit baffle is downwardly projecting and is located on cooperation support slipper periphery；It is described
It limits and is equipped with left phase between baffle and support rim from length and right phase from length, the support among several support rims is convex
Platform is center support rim, and the left phase of central supported boss, from equal length, is initial phase from length L/2 from length and right phase；
The right phase of support rim on the left of central supported boss is successively incremented by L from length outward, and left phase is constant from length；It is located at
The left phase of support rim on the right side of central supported boss is successively incremented by L from length outward, and right phase is constant from length.
5. high-temperature acidic flue gas economizer according to claim 3 prevents swollen support construction, which is characterized in that further include several
Dust-proof roll film, by the interior end edge of sheet metal, side rolls gained to the dust-proof roll film outward；The outer end edges are fixed on cooperation branch
The lower part of sliding block is supportted, adjacent two dust-proof roll film is fitted close or lap fit；It is convex that the dust-proof roll film elasticity press is set to support
On platform side wall and support plate.
6. high-temperature acidic flue gas economizer according to claim 4 prevents swollen support construction, which is characterized in that further include recessed
One end of baffle and the cooperation baffle matched with recessed baffle, the recessed baffle is connected with limit baffle periphery, and ring
If with limit baffle periphery；Cyclic annular lower recess is equipped between the connecting pin and free end of the recessed baffle；The cooperation baffle
Positioned at the lower section of recessed baffle, including the first cooperation baffle and several second cooperation baffles；One end of the first cooperation baffle
It is connected with support rim periphery, and is located on support rim periphery；The second cooperation baffle annular protrusion is arranged first
Cooperate baffle upper surface, and be equipped with recess under ring-type, the second cooperation baffle is contained in recess under ring-type, and second
The upper end and cyclic annular lower pocket top for cooperating baffle have gap；The recessed baffle combines to form bending detour with cooperation baffle
Dust-proof labyrinth circuit.
7. high-temperature acidic flue gas economizer according to claim 6 prevents swollen support construction, which is characterized in that described second matches
Limit where closing support rim where the horizontal distance between baffle and cyclic annular lower recess cooperates baffle with second and cyclic annular lower recess
Left phase between the baffle of position is adapted to from length and right phase from length.
8. high-temperature acidic flue gas economizer according to claim 1 prevents swollen support construction, which is characterized in that further include having
The connecting plate and connection sheet of through-hole, the connecting plate are respectively arranged on heat exchange tube panel two sides, and heat exchanger tube is set in through-hole；The connection
One end of piece is fixedly connected with heat transfer flue inner wall, the other end and connecting plate medial surface Elastic Contact.
9. high-temperature acidic flue gas economizer according to claim 8 prevents swollen support construction, which is characterized in that the connection sheet
It is respectively arranged on the two sides up and down of connecting plate.
10. high-temperature acidic flue gas economizer according to claim 1 prevents swollen support construction, which is characterized in that the heat exchange
Metal spiral fin is welded in pipe outer wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821589840.6U CN208983320U (en) | 2018-09-28 | 2018-09-28 | A kind of high-temperature acidic flue gas economizer prevents swollen support construction |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821589840.6U CN208983320U (en) | 2018-09-28 | 2018-09-28 | A kind of high-temperature acidic flue gas economizer prevents swollen support construction |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208983320U true CN208983320U (en) | 2019-06-14 |
Family
ID=66785874
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821589840.6U Active CN208983320U (en) | 2018-09-28 | 2018-09-28 | A kind of high-temperature acidic flue gas economizer prevents swollen support construction |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208983320U (en) |
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2018
- 2018-09-28 CN CN201821589840.6U patent/CN208983320U/en active Active
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