A kind of structure-improved H-type finned tube
Technical field
The invention belongs to the technical field of heat exchangers that fume afterheat utilizes, and are suitable for the energy, power, refrigeration, chemical industry, smelting
The heat exchange equipment and heating equipment of the industries such as refining, petroleum, and in particular to a kind of structure-improved H-type finned tube.
Background technique
With the sustained and rapid development of China's economy, energy supply anxiety problem becomes increasingly conspicuous, and energy conservation, emission reduction, consumption reduction are
Inevitable requirement as the development of China's economy and society.Heat exchanger as power, petroleum, chemical industry, refrigeration, metallurgy or even aviation,
The important component of the industrial process such as rocket, its safe and highly efficient operation are significant.In various heat exchange equipments, pass through wing
It is common augmentation of heat transfer mode that piece, which increases heat exchange area,.
Increase heat exchange area in the big side reasonable Arrangement fin of heat exchanger thermal resistance, reduce thermal resistance, is that heat exchanger reinforcing is changed
One of the mode of heat, H-type finned tube is exactly typical example.By the optimization enhanced heat exchange of H-type finned tube, reduction flow resistance, subtract
The safe and highly efficient operation of no accretion of ash abrasion heat exchanging device is of great significance.
H-type finned tube, also known as H-type fin.It symmetrically welds together the steel disc for having circular arc among two panels with light pipe
It is formed, front shape is gained the name due to as alphabetical " H ".Research and practice have shown that H-type finned tube can dramatically increase heat exchange area,
Increase flue gas flow area, reduces cigarette speed, reduce dust stratification and abrasion.
Flue gas often carries a certain amount of flying dust, and when flue gas flows outside H-type finned-tube bundle can generate in leeward side
Air-flow separation and reflux, the region are known as being vortexed stagnation region.And the local space being vortexed the every two betweens of fins of stagnation region does not almost have
There is gas disturbance, the gas flowing of the local space is similar to plane flowing, and ash particle is difficult to flow between different fins, therefore
Easily form dust stratification.
Although H-type finned tube has good anti-dust stratification ability and abrasionproof performance, under containing grey air-flow, due to fluid itself
Viscous effect and adverse pressure gradient presence, flowing necessarily separate, and finned tube leeward side formed be vortexed stagnation region, from
And make constantly to accumulate containing the ash particle in grey air-flow in leeward side, a large amount of dust stratifications in part are caused, finned tube heat transfer effect is seriously affected
The safe and highly efficient operation of rate and heat exchanger.Traditional H-type fin has its intrinsic drawback, as quadrangle is right angle outside fins set
It will increase flow resistance;Fin windward side is consistent with leeward side gap-ratio, width is high unanimously makes windward side equal with heat exchange area
It will cause heat transfer deterioration, reduce heat exchange efficiency;Backflow phenomenon makes leeward side be easy to produce dust stratification, and dust stratification thermal coefficient is low to be caused
Heat exchange further deteriorates.
By the structural analysis to H-type finned tube, discovery when by H-type finned tube, is further exacerbated by containing grey air-flow
The formation of dust stratification.Therefore, by taking necessary structure optimization, reduce vortex stagnation region area to reduce dust stratification, be a kind of
Effective method.
Summary of the invention
To solve the problems, such as that above-mentioned industrial practical application, the present invention propose a kind of structure-improved H-type finned tube,
To improve the heat exchange property of H-type finned tube, its flow resistance is reduced, reduces flowing crushing, and mitigate the dust stratification and mill of finned tube
Damage.
In order to achieve the above objectives, the invention adopts the following technical scheme:
A kind of structure-improved H-type finned tube, including base tube and fins set;Fins set includes one group of two complete phase of size
There are the arc groove coincideing with base tube outer wall in same fin, fin inside;It is connected to outside base tube with what is axially arranged along base tube
Multiple parallel fins groups of wall;Base tube has certain length, and several parallel fins groups are connected to base along what base tube was axially arranged
Pipe outer wall;It is characterized by: taking comprising base tube axis and being divided into fin for interface perpendicular to the plane in flow of flue gas direction
Two parts, upstream are windward side, and downstream is leeward side;Fin surface windward side has a ball male structure, fin surface leeward side
With a winglet eddy generator.
Compared with prior art, present invention has the advantage that
A kind of structure-improved H-type finned tube proposed by the present invention, fin windward side or so respectively have a ball convex, and leeward side is each
There is a rectangular winglet eddy generator.The convex presence of ball can be effectively reduced crushing and prevent from forming big whirlpool turbulent flow in flow process.
When fluid flow through ball it is convex nearby when, the vortex in flow field can be siphoned away by the pit at the convex back side of ball, prevent bigger vortex from being formed, can
To reduce resistance.And when flue gas flows through rectangular winglet eddy generator, fluid, which is formed, to be vortexed, and generates disturbance, and boundary layer can not be held
Supervention exhibition, to achieve the purpose that enhanced heat exchange.This also means that the heat exchange equipment certain for heat exchange amount, takes the present invention
The structure of proposition can save steel consumption, reduce cost.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of a pair of of fins set and its institute's linker tube portion in the present invention;
Fig. 2 is the front view of a pair of of fins set and its institute's linker tube portion in the present invention;
Fig. 3 is the rearview of a pair of of fins set and its institute's linker tube portion in the present invention;
Fig. 4 is the side view of a pair of of fins set and its institute's linker tube portion in the present invention;
Wherein: 1 windward side;2 leeward sides.
Specific embodiment
The present invention will be described in more detail with reference to the accompanying drawings and detailed description.Following instance is conducive to corresponding skill
Art personnel are best understood from the present invention, but the invention is not limited in any way.And it will be noted that the skill of this research field
For art personnel, improvement can be made on the basis of present inventive concept, this belongs to protection scope of the present invention.
Fig. 1-4 is structural schematic diagram of the invention, includes a round base tube and a pair of of fin.
As shown, a kind of structure-improved H-type finned tube includes base tube and fins set.Substrate tube has fluid interchange work
Matter, generally liquid, and capacity of heat transmission is greater than finned outer fluid.Fins set includes one group of two identical wing of size
Piece, it is regularly arranged by certain pitch, there is the arc groove coincideing with base tube outer wall on the inside of fin, arc groove is located in fin
Between at axis, fin is symmetrical about arc groove.With the multiple parallel wings for being connected to base tube outer wall axially arranged along base tube
Piece group.Base tube has certain length, and several parallel fins groups are connected to base tube outer wall along what base tube was axially arranged.
Symmetrical H-type fin tube structure centered on the finned tube, or be non-centrosymmetrical H-type fin tube structure;When
When for non-centrosymmetrical H-type fin tube structure, arc groove inclined side setting, fin on fin is non-right about arc groove
Claim.If taking the face constituted using base tube axis and gas direction of flow as the plane of reference, which is divided into windward side for finned tube
It should meet lateral area windward at asymmetric arrangement fin with leeward side two parts and be greater than leeward lateral area, and two-part face
Product ratio should be between 1~2.
Fin uses rectangular plate structure.Relative to heat exchange flue gas stream direction, fin both ends are respectively that fin surface is met
Wind side and fin surface leeward side.
The surface shape of fin can be rectangle, parallelogram, trapezoidal or irregular quadrilateral.
It takes comprising base tube axis and fin is divided into two parts, upstream for interface perpendicular to the plane in flow of flue gas direction
For windward side, downstream is leeward side.
Fin surface windward side setting ball is convex, and ball projection is at fin width direction outside 1/3.Its height and diameter ratio
For (0.2~0.6): 1, recommend 0.4:1.Fin surface be equipped with ball it is convex can with rough air, prevent Development of Boundary Layer reduce pressure
Decreasing loss loses the particle reduced in flue gas and deposits in heat exchange surface, is conducive to heat exchanger long-time efficient operation.
Ball is convex to be improved to cylindrical structure.The shape of the base tube straight tube is cylindrical, oval tubulose, flat tube
In any one.
Rectangular winglet eddy generator is located at fin surface leeward side, is located at fin width direction 1/2.Winglet long side length
It is (0.2~0.4) with the ratio between base tube outer diameter: 1, recommend 0.3:1;The ratio between short side and long side are (0.3~0.6): 1, recommend 0.5:
1.The spacing ratio of winglet height and the parallel fins of setting is 0.5~1.0.
The angle of attack of rectangular winglet direction and gas direction of flow is 10 °~80 °.
Rectangular winglet and ball projection are placed in the same surface of fin.
Rectangular winglet can be improved to triangle winglet.
Rectangle through slot is machined on the fin of rectangular winglet root, rectangle penetrates through slot length and is equal to the long side length of rectangular winglet
Degree, perforation groove area approximately double winglet area of section, and rectangle through slot direction is consistent with rectangular winglet direction.The shape of through slot
Shape can be rectangle, arc or circle;For rectangular channel, using the long side of slot as fluting reference direction, slot direction and gas
The angle of attack of direction of flow is 10 °~80 °;Arc groove is come using secant where slot circular arc as fluting reference direction with gas
Direction is flowed into 10 °~80 °.
Through slot is capable of forming flowing and boundary layer is interrupted, and restarts boundary layer flow, so that boundary layer is thinned, part
The coefficient of heat transfer increases, and achievees the purpose that augmentation of heat transfer.When flue gas flows through fin, ball is convex, through slot and winglet generate fluid
Disturbance, to achieve the purpose that enhanced heat exchange.Especially fluid flows through rectangular winglet eddy generator, flow field heat-transfer pipe tail portion stagnation
Area significantly reduces, and flow disturbance enhancing, boundary layer is destroyed when stagnation region fluid enters main flow area, therefore the heat-exchange performance of finned tube
It can be strengthened.And the disturbance of tail portion stagnation region, purging effect is also increased, so that flying dust deposition is obviously reduced.
Above-mentioned H-type finned tube may be directly applied to flue gas waste heat recovery technique, can also be made as modular construction, answer
For occasions such as power plant's superheater, economizers.
Finally, it should be noted that being not intended to restrict the invention the foregoing is merely explanation of the invention, although to this hair
It is bright to be described in detail, it for those skilled in the art, still can be to aforementioned documented technical solution
It modifies or equivalent replacement of some of the technical features.All within the spirits and principles of the present invention, made
Any modification, equivalent substitution, improvement and etc. should all be included in the protection scope of the present invention.