CN206944799U - Polygon fin bielliptic(al) extended surface tube heat exchange element - Google Patents

Polygon fin bielliptic(al) extended surface tube heat exchange element Download PDF

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Publication number
CN206944799U
CN206944799U CN201720634054.2U CN201720634054U CN206944799U CN 206944799 U CN206944799 U CN 206944799U CN 201720634054 U CN201720634054 U CN 201720634054U CN 206944799 U CN206944799 U CN 206944799U
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China
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fin
base tube
heat exchange
tube
ellipse
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CN201720634054.2U
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陈金龙
刘晓燕
范云磊
崔亮
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Jianyin Dynamo Power Equipment Co Ltd
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Jianyin Dynamo Power Equipment Co Ltd
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Abstract

It the utility model is related to a kind of polygon fin bielliptic(al) extended surface tube heat exchange element, it includes the base tube of two parallel arrangements, and it is located at some groups of symmetrical fins of every foundation pipe both sides and is located at the band steel that is arranged symmetrically of the base tube along airflow direction both sides, the section of two described foundation pipes is ellipse, the fin is made up of two identical polygons, and the summit of monosymmetric two polygons of each base tube is on same ellipse, the ellipse is outwards to offset certain distance by the outward flange of each base tube to be formed, gap is left between every group of symmetrical fin, the fin is connected with the outside wall surface of oval base tube by the way of welding.Not only inned coefficient is high for the utility model, and uniform distribution of temperature field, and dust stratification is few, and the heat exchange efficiency of whole gilled tube is high, and opposing metallic consumption is low.

Description

Polygon fin bielliptic(al) extended surface tube heat exchange element
Technical field
It the utility model is related to a kind of heat exchange element, more particularly to a kind of polygon fin bielliptic(al) extended surface tube heat exchange member Part.It is related to electric power, environmental protection, the energy, chemical industry, building materials, metallurgy and other industry and people's livelihood technical field of heat exchange equipment.
Background technology
With the high speed development of Chinese national economy, environmental pollution is inevitably caused(Atmosphere pollution, water pollution and Land pollution), in recent years, environmental pollution becomes increasingly conspicuous, particularly atmosphere pollution, and haze weather is more and more, scope is more next It is wider, degree is increasingly severe, people are most deep to the susceptibility of atmosphere pollution, because related to people's " inhale inhale ".Atmosphere pollution Crack cause it is a lot, such as airborne dust, vehicle exhaust, industrial discharge, wherein industrial discharge increasingly attract attention, particularly fired The exhaust emissions of coal equipment, in power industry, National Development and Reform Committee, State Ministry of Environmental Protection and National Energy Board 2014 are according to State Council 《Energy development strategy action plan(2014-2020)》Combine and issue《The energy-saving and emission-reduction of coal electricity upgrade and transformation action plan (2014-2020)》, this action plan specify that target and the timing node requirement of energy-saving and emission-reduction.For this action plan, respectively Utilities Electric Co. and coal-burning power plant have accordingly formulated specific energy-saving and emission-reduction modification scheme and implemented, the measures of energy-saving and emission-reduction it One is exactly by the reduction of the exhaust gas temperature of boiler of power plant unit, so in modification scheme, will generally increase changing for flue gas and water newly Thermal, some power plant also transform original heat-exchanger rig simultaneously, by heat-exchanger rig by the heat transfer of flue gas to WATER AS FLOW MEDIUM, Reaching reduces the purpose of exhaust gas temperature.This heat-exchanger rig is commonly referred to as economizer or flue gas in power plant(Water)Heat exchanger or flue gas Cooler just claims heat exchanger.Most important element is exactly heat exchanger tube in heat-exchanger rig, the heat exchanger tube with extended surface Because comprehensive economic performance is high and saves space, it is widely used, the ellipse heat exchange especially with extended surface Pipe, because dust stratification and abrasion are relatively light, also progressively it is applied in some projects.
Extended surface currently used for the elliptical heat exchange tube of above-mentioned heat-exchanger rig is H type fins, is by H types circular section Heat exchanger tube is transplanted, as shown in figure 1, wherein base tube 1 is elliptical tube, fin 2 is H types, because its shape is like English alphabet H, And base tube is referred to as H type ellipse gilled tubes for elliptical tube, the H type gilled tubes that base tube is circular section are different from, as shown in Figure 2.Rib The heat-transfer mechanism of piece is by flue gas(Gas)Heat WATER AS FLOW MEDIUM in base tube 1 is delivered to by heat transfer(Or steam-water mixing Thing), or by the heat transfer of medium in base tube 1 to the gas outside base tube 1, in other influence factors all identical situations Under, fin transmits the size of heat ability, that is, heat conduction efficiency and the height of fin(The outermost edge of fin is apart from base tube 1 nearest outward flange size)There is close relationship, highly smaller heat-transfer capability is bigger, otherwise smaller.Can from Fig. 1 and Fig. 2 Go out, apart from base tube 1, outer peripheral size is all recently for H type fin outward flanges, and wherein summit A is outer recently apart from base tube 1 The size at edge is maximum, and the effect of A places transmission heat is worst, that is, at A heating surface utilization rate it is minimum, improve heating surface Utilization rate is the purpose of this utility patent, if the heating surface at A is used for into other places, such as the outside C of B points in Fig. 1 and Fig. 2 Place, as long as outer peripheral size L1 less than at A imitate recently apart from base tube 1 by outer peripheral size L, heat exchange recently apart from base tube 1 at C Fruit then increases.
Further to reduce dust stratification, the heat exchange efficiency of heat exchanger tube is improved, in both sides Welding flat steel of the base tube along airflow direction, Such as Fig. 3 and Fig. 4.From hydrodynamics, fluid transversal flow pipe(Pipe or elliptical tube)When, pipe is in flow of fluid side To front and rear sides vortex be present, containing ash air-flow will in vortex dust stratification, once heating surface pipe dust stratification will drop significantly Low heat transfer effect, band steel will destroy vortex, reduce dust stratification, especially lee face, so as to have the function that to improve heat transfer effect.
Utility model content
Technical problem to be solved in the utility model is double ellipse for a kind of polygon fin of above-mentioned prior art offer Circle extended surface tube heat exchange element, not only inned coefficient is high for it, and uniform distribution of temperature field, dust stratification are further reduced, whole fin The heat exchange efficiency of pipe is high, and metal consumption is low in the case of identical heat output.
The technical scheme in the invention for solving the above technical problem is:A kind of polygon fin bielliptic(al) pipe heat exchange member Part, it includes the base tube of two parallel arrangements, both sides Welding flat steel of the base tube along airflow direction, and is located at every foundation pipe both sides Some groups of symmetrical fins, the sections of two described foundation pipes is ellipse, and the fin is polygon by two identicals Shape is formed, and the summit of monosymmetric two polygons of each base tube, on same ellipse, the ellipse is by each base tube Outward flange outwards offset certain distance and formed, leave gap c between every group of symmetrical fin and band steel, the fin with it is oval The outside wall surface of base tube is connected by the way of welding.
Preferably, every group of fin is arranged symmetrically with the long axis direction of oval base tube.
The fin spacing for the adjacent sets being preferably located on oval base tube is arranged as required to, usually 5-50mm.
Preferably, the process gap c between every group of symmetrical fin and band steel is adjusted according to base tube size, usually 2- 20mm。
Preferably, the width a and thickness b of band steel determine that usual a is 6- according to the size of pipe and the characteristic of air-flow 50mm, b 3-12mm.
Preferably, the band steel and oval base tube are welded to connect or custom-made ellipse extended surface tube.
Compared with prior art, the utility model has the advantage of:
The utility model is made compared to reducing air-flow as a result of oval base tube, with circular base tube by base tube surface Into drag losses, so as to reduce energy consumption, and base tube has welded band steel along the both sides of airflow direction, destroys the vortex of air-flow Area, reduce containing grey air-flow at the back side of the dust stratification, especially airflow scouring of tube surface, so as to further increase heat exchange effect Fruit, simultaneously as fin outward flange is closely sized to equal apart from base tube is outer peripheral recently, the uniform distribution of temperature field of fin, change Thermal effect is best, the utilization rate highest of fin, and metal consumption is low in the case of identical heat output.
Brief description of the drawings
Fig. 1 is the structural representation of existing H types bielliptic(al) shape heat exchanger tube.
Fig. 2 is the structural representation of existing H types Double Circle heat exchanger tube.
Fig. 3 is front view of the present utility model.
Fig. 4 is Fig. 3 top view.
Fig. 5 is Fig. 3 side view.
Wherein:
Base tube 1, fin 2, band steel 3.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing embodiment.
As shown in Fig. 3-5, a kind of polygon fin bielliptic(al) extended surface tube heat exchange element, including two are the utility model is related to The base tube 1 of root parallel arrangement, and be located at some groups of symmetrical fins 2 of every both sides of foundation pipe 1 and be located at base tube 1 along gas The band steel 3 being arranged symmetrically of direction both sides is flowed, the plane of every group of symmetrical fin 2 composition is each perpendicular to the axial line of base tube Direction, the section of two described foundation pipes 1 is ellipse, and the fin 2 is made up of two identical polygons, and each base tube On same ellipse, the ellipse is outwards offset by the outward flange of each base tube 1 on the summit of monosymmetric two polygons Certain distance is formed so that each point on polygon to 1 outer peripheral minimum distance of base tube close to equal, reach temperature field It is evenly distributed, heat transfer effect is optimal, and process gap, the fin 2 and oval base tube 1 are left between every group of symmetrical fin 2 Outside wall surface is connected by the way of welding, and band steel 3 can connect with welding with oval base tube 1, can also custom-made ellipse fin Pipe.
In the present embodiment, every group of fin is arranged symmetrically with the long axis direction of oval base tube, on oval base tube The fin spacing of adjacent sets is 5-50mm, and the process gap between every group of fin 2 and band steel 3 being arranged symmetrically is 2-20mm, by In employing oval base tube, air-flow is reduced by the drag losses caused by base tube surface, so as to reduce energy consumption, and base tube Band steel has been welded along the both sides of airflow direction, has destroyed the vortex of air-flow, has reduced the dust stratification in tube surface containing grey air-flow, The especially back side of airflow scouring, so as to further increase heat transfer effect, while the outward flange of fin 2 is outer recently apart from base tube 1 Being closely sized to for edge is equal, reaches uniform distribution of temperature field, and heat transfer effect is optimal, therefore is to save material compared with H type fins Material so that the weight reduction of whole heat exchange element and heat-exchanger rig.
A kind of preferably implementation of the present utility model is the foregoing is only, not to limit the utility model, All non-essential modifications made in the utility model spirit, replacement, improvement etc., should be included in of the present utility model Within protection domain.

Claims (6)

1. a kind of polygon fin bielliptic(al) extended surface tube heat exchange element, it includes the base tube of two parallel arrangements(1), and be located at Per foundation pipe(1)Some groups of symmetrical fins of both sides(2)Be located at base tube(1)Along being arranged symmetrically for airflow direction both sides Band steel(3), it is characterised in that:Two described foundation pipes(1)Section for ellipse, the fin(2)By two identicals Polygon is formed, and the summit of monosymmetric two polygons of each base tube, on same ellipse, the ellipse is by each Base tube(1)Outward flange outwards offset certain distance and formed, every group of symmetrical fin(2)Between leave process gap, the rib Piece(2)With oval base tube(1)Outside wall surface using welding by the way of connect.
A kind of 2. polygon fin bielliptic(al) extended surface tube heat exchange element according to claim 1, it is characterised in that:Every group of rib Piece(2)It is with oval base tube(1)Long axis direction be arranged symmetrically.
A kind of 3. polygon fin bielliptic(al) extended surface tube heat exchange element according to claim 1, it is characterised in that:Positioned at ellipse Physa pipe(1)On adjacent sets fin(2)Spacing is arranged as required to, usually 5-50mm.
A kind of 4. polygon fin bielliptic(al) extended surface tube heat exchange element according to claim 1, it is characterised in that:Every group pair The fin of title(2)With band steel(3)Between process gap according to base tube(1)Size is adjusted, usually 2-20mm.
A kind of 5. polygon fin bielliptic(al) extended surface tube heat exchange element according to claim 1, it is characterised in that:Symmetrically Band steel(3)Width a and thickness b determine that usual a is 6-50mm, b 3- according to the size of pipe and the characteristic of air-flow 12mm。
A kind of 6. polygon fin bielliptic(al) extended surface tube heat exchange element according to claim 1, it is characterised in that:It is described Band steel(3)With oval base tube(1)It is welded to connect or custom-made ellipse extended surface tube.
CN201720634054.2U 2017-06-02 2017-06-02 Polygon fin bielliptic(al) extended surface tube heat exchange element Active CN206944799U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720634054.2U CN206944799U (en) 2017-06-02 2017-06-02 Polygon fin bielliptic(al) extended surface tube heat exchange element

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720634054.2U CN206944799U (en) 2017-06-02 2017-06-02 Polygon fin bielliptic(al) extended surface tube heat exchange element

Publications (1)

Publication Number Publication Date
CN206944799U true CN206944799U (en) 2018-01-30

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720634054.2U Active CN206944799U (en) 2017-06-02 2017-06-02 Polygon fin bielliptic(al) extended surface tube heat exchange element

Country Status (1)

Country Link
CN (1) CN206944799U (en)

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