CN206944804U

CN206944804U - Polygon fin bielliptic(al) pipe heat exchange element

Info

Publication number: CN206944804U
Application number: CN201720633002.3U
Authority: CN
Inventors: 陈金龙; 刘晓燕; 范云磊; 崔亮
Original assignee: Jianyin Dynamo Power Equipment Co Ltd
Current assignee: Jianyin Dynamo Power Equipment Co Ltd
Priority date: 2017-05-09
Filing date: 2017-06-02
Publication date: 2018-01-30
Anticipated expiration: 2027-06-02
Also published as: CN107167018A

Abstract

It the utility model is related to a kind of polygon fin bielliptic(al) pipe 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, 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 the heat exchange efficiency of whole gilled tube is high, and opposing metallic consumption is low.

Description

Polygon fin bielliptic(al) pipe 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) pipe heat exchange element.Relate to And 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.

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 Pipe heat exchange element, not only inned coefficient is high for it, and uniform distribution of temperature field, and the heat exchange efficiency of whole gilled tube is high, identical Metal consumption is low in the case of 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, and is located at some groups of symmetrical fins of every foundation pipe both sides, described The section of two foundation pipes is ellipse, and the fin is made up of two identical polygons, and each base tube monosymmetric two On same ellipse, the ellipse is outwards to offset certain distance by the outward flange of each base tube to be formed on the summit of individual polygon, 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.

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 between every group of symmetrical fin is adjusted according to base tube size, usually 3-50mm.

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, simultaneously as fin outward flange outer peripheral is closely sized to phase recently apart from base tube Deng, the uniform distribution of temperature field of fin, heat transfer effect is best, the utilization rate highest of fin, in the case of identical heat output metal consume Measure low.

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.

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) pipe heat exchange element is the utility model is related to, including two are put down The base tube 1 of row arrangement, and some groups of symmetrical fins 2 of every both sides of foundation pipe 1 are located at, every group of symmetrical fin The planes of 2 compositions are each perpendicular to the direction of axis line of base tube, and the sections of two described foundation pipes 1 is ellipse, the fin 2 by Two identical polygons are formed, and the summit of monosymmetric two polygons of each base tube, on same ellipse, this is ellipse Circle is outwards to offset certain distance by the outward flange of each base tube 1 to be formed so that each point on polygon to outside base tube 1 The minimum distance of edge reaches uniform distribution of temperature field, heat transfer effect is optimal, is left between every group of symmetrical fin 2 close to equal Process gap, the fin 2 are connected with the outside wall surface of oval base tube 1 by the way of welding.

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 being arranged symmetrically is 3-50mm, as a result of Oval base tube, air-flow is reduced by the drag losses caused by base tube surface, so as to reduce energy consumption, while the outside of fin 2 Edge is closely sized to equal apart from base tube 1 is outer peripheral recently, reaches uniform distribution of temperature field, and heat transfer effect is optimal, thus with H types It is to save material that fin, which is compared, 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

1. a kind of polygon fin bielliptic(al) pipe heat exchange element, it includes the base tube of two parallel arrangements（1）, and it is located at every Base tube（1）Some groups of symmetrical fins of both sides（2）, it is characterised in that：Two described foundation pipes（1）Section for ellipse Shape, the fin（2）It is made up of two identical polygons, and the summit of monosymmetric two polygons of each base tube is located at 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 fin（2）With oval base tube（1）Outside wall surface using welding by the way of connect.

A kind of 2. polygon fin bielliptic(al) pipe heat exchange element according to claim 1, it is characterised in that：Every group of fin （2）It is with oval base tube（1）Long axis direction be arranged symmetrically.

A kind of 3. polygon fin bielliptic(al) pipe heat exchange element according to claim 1, it is characterised in that：Positioned at oval base Pipe（1）On adjacent sets fin（2）Spacing is arranged as required to, usually 5-50mm.

A kind of 4. polygon fin bielliptic(al) pipe heat exchange element according to claim 1, it is characterised in that：Every group symmetrical Fin（2）Between process gap according to base tube（1）Size is adjusted, usually 3-50mm.