CN2809568Y - Cooperative enhanced heat exchange surface - Google Patents
Cooperative enhanced heat exchange surface Download PDFInfo
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- CN2809568Y CN2809568Y CN 200520017142 CN200520017142U CN2809568Y CN 2809568 Y CN2809568 Y CN 2809568Y CN 200520017142 CN200520017142 CN 200520017142 CN 200520017142 U CN200520017142 U CN 200520017142U CN 2809568 Y CN2809568 Y CN 2809568Y
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- heat exchange
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Abstract
The utility model relates to a cooperative type enhanced heat-exchange surface, which comprises a basal plate (1) and many fins (2) arranged on the basal plate. The utility model is characterized in that the fins adopt three-dimensional forms, and are formed from two side faces (3) with the same structures and the upper end face (4) of a rectangle; the side faces (3) form right-angle trapezoidal structures; the edge connected with the basal plate is a right-angle edge; along a main flow direction, an inclination angle beta which is not more than 90DEG is arranged between the upper end face and the basal plate; the inclination angle beta is 15 to 17 DEG when used for the heat exchange of layer flow on the heat exchange surface; the inclination angle beta is 23 to 24 DEG when used for the heat exchange of turbulent flow; a partial gradual reducing channel is formed between the fins and the basal plate. The utility model is an enhanced heat-exchange surface having low pump work consumption and high heat exchange coefficient, and has relatively higher input-output ratio. By using the surface to manufacture a heat exchanger, under the conditions of the same fluid mass and flow rate, heat-transfer quantity is increased. When the heat-transfer quantity has a certain requirement, the required fluid flow can be reduced, thereby, pumping power consumption can be reduced.
Description
Technical field
The utility model relates to a kind of synergic type reinforced heat exchange surface, and its technology contents belongs to heat energy utilization and power engineering technology field.This heat exchange surface can specifically be applied to Refrigeration and Cryogenic Engineering, Chemical Engineering, nuclear reactor thermal technology, fields such as electronic system cooling and Aerospace Engineering.
Background technology
Fluid interchange is a heat transfer form common in the engineering in the passage.In order to improve the utilization rate of heat energy, or in order to improve the operating efficiency of thermal machine, diabatic process often needs to strengthen.The outstanding problem of stream strengthened heat exchange method is in the tradition, the relative contradictory problems of hanging down between the output of the high investment of the pumping power that flows and enhanced heat exchange effect.Weigh the quality of certain intensified heat transfer method, not only will see the amplitude that its coefficient of overall heat transmission improves, also will see it is to obtain this raising with great cost.The structure of " low input, high production " is desirable, and the structure of " high investment, low output " is worthless.The thermal technology adopts in the field " strengthening effect under the same pump merit condition " to estimate the quality of intensified heat transfer method usually.Its keynote idea is, under the precondition of identical pumping power, determines heat transfer rate that reinforced structure can reach and do not have the multiple that the corresponding smooth passage heat transfer rate strengthened is compared.This multiple is greater than one, and intensifying method is desirable; Less than one is worthless.Multiple is bigger, and strengthening effect better, and is more with practical value.
The reinforcement of interior stream heat-exchange system is adopted the way that flow-disturbing unit is set, as shown in Figure 1 mostly on channel inner surface.
This class flow-disturbing is first or square or circular, generally all along perpendicular to being provided with on the main flow direction.The thinking of its enhanced heat exchange is, utilizes flow-disturbing unit periodically to destroy the boundary layer, reduces nearly wall place thermal resistance, thereby reaches the purpose of augmentation of heat transfer.This structure can cause flow resistance to increase considerably when heat exchange is strengthened, and this is disadvantageous from energy-conservation angle.Cause the basic reason of this phenomenon, be that flow-disturbing unit downstream can produce a recirculating zone naturally, it consumes flow work both meaninglessly, increase drag losses, hindered the heat exchange between main flow fluid and the solid wall surface again, therefore from the angle of capacity usage ratio, this structure is not optimum.
The utility model content
The purpose of this utility model is to solve the interior outstanding problem that flows strengthened heat exchange method of tradition, the high investment of the pumping power that promptly flows and the relative contradictory problems of hanging down between the output of enhanced heat exchange effect.
Based on this purpose, the utility model proposes a kind of synergic type reinforced heat exchange surface, structural representation has adopted inclining fin referring to accompanying drawing 2 in the new structure, forcing fluid, thereby avoided forming the recirculating zone in flow-disturbing unit downstream at the periodic oblique impact channel inner surface of near wall region.Fin is the extension heat exchange surface of conduit wall, is again the baffling unit that fluid is folded to wall.Form the local contraction passage between fin and the wall, make flow velocity increase, help heat exchange.For the ease of laying, fin adopts three dimensional form in the reality.
The concrete structure of the synergic type reinforced heat exchange surface in the utility model is referring to accompanying drawing 3,4,5, comprise substrate 1 and many fins 2 that is arranged on the substrate 1, it is characterized in that: described fin 2 adopts three dimensional form, form by two identical side 3 and upper surfaces 4 of structure, side 3 is a ladder structure of right angle, and the limit that links to each other with substrate is a right-angle side; Along main flow direction, have one between upper surface 4 and the substrate less than 90 ° angle of inclination beta, form local tapered channels between fin 2 and the substrate 1.
Described a kind of synergic type reinforced heat exchange surface is characterized in that: two sides 3 of fin 2 are parallel to each other, and upper surface 4 is a rectangle.
Described a kind of synergic type reinforced heat exchange surface is characterized in that: the angle of inclination beta between upper surface 4 and the substrate 1 is 15～17 ° when heat exchange surface is used for laminar heat transfer, is 23～24 ° when heat exchange surface is used for turbulent-flow heat-exchanging.
Described a kind of synergic type reinforced heat exchange surface is characterized in that: the connected mode between fin 2 and the substrate 1 is soldering.
Fin 2 in the utility model adopts copper or aluminium or the good material of other thermal conductivity.
The utility model is based on following theoretical propose: heat exchange is meant that fluid is in flow process and the exchange heat process that is taken place between the surface of solids.The power and the fluid flow of heat exchange have much relations.Generally speaking, flow for single-phase, the heat exchange in smooth, the straight passage is the most weak, and near the heat exchange the jet impulse stationary point is the strongest.The enhanced heat exchange theory is thought, the dot product between the velocity of fluid and the thermograde vector in the flow field is the key factor of restriction heat convection power.This dot product is bigger, and heat exchange is just stronger.The aforementioned method that horizontal flow-disturbing unit is set has objectively also improved the dot product of field vector, has caused the eddy current at flow-disturbing unit adherent place, downstream to produce only simultaneously, and this is not desirable, because this can make resistance increase.
The utility model is the enhanced heat exchange surface of a kind of low pump work consumption, the high coefficient of heat transfer, and it has higher relatively input-output ratio.Make heat exchanger if use this kind surface design, under identical fluid mass flow rate condition, heat output can increase.In other words, heat output requires one regularly, and required fluid flow can reduce, thereby reduces the consumption of pumping power.In a word, this kind heat exchange surface helps improving the heat energy utilization rate, can be widely used in existing the occasion of fluid interchange.
Description of drawings
Fig. 1 is provided with traditional enhanced heat exchange structure of flow-disturbing unit;
Fig. 2 is provided with the cooperating type enhanced heat exchange structure schematic diagram of baffling fin;
Fig. 3 fin arrangement;
Fig. 4 synergic type reinforced heat exchange surface front view;
Fig. 5 three-dimension fin structural representation;
The ratio of smooth passage heat exchange Nu number (channel height H is 24mm) under Fig. 6 cooperating type enhanced heat exchange structure heat exchange Nu number and the same pump merit;
(a) laminar flow operating mode, (b) turbulent operating mode;
Fig. 7 is used for a channel period (zoning get wherein half) of computer simulation;
Wherein among Fig. 1-5,
1, substrate, 2, fin, 3, the fin side, 4, the fin upper surface, 5, main flow direction, 6, flow-disturbing unit.
The specific embodiment
Embodiment of the present utility model is referring to accompanying drawing 3,4,5, comprise substrate 1 and many fins 2 that is arranged on the substrate 1, fin 2 adopts three dimensional form, is made up of two identical side 3 and upper surfaces 4 of structure, side 3 is a ladder structure of right angle, and the limit that links to each other with substrate is a right-angle side; Along main flow direction, have one between upper surface 4 and the substrate less than 90 ° angle of inclination beta, form local tapered channels between fin 2 and the substrate 1.
Two sides 3 of fin 2 are parallel to each other, and upper surface 4 is a rectangle.
Angle of inclination beta between upper surface 4 and the substrate 1 is 15～17 ° when heat exchange surface is used for laminar heat transfer, is 23～24 ° when heat exchange surface is used for turbulent-flow heat-exchanging.
Connected mode between fin 2 and the substrate 1 is soldering.
Fin 2 in the utility model can adopt copper or aluminium or the good material of other thermal conductivity.
At aforementioned enhanced heat exchange thinking, the situation of channel height H=24mm has been carried out computer simulation.Simulated object is the heat convection of periodically fully development section, and accompanying drawing 7 is seen in the zone of analog computation.This operating mode has been represented the least favorable part of interior stream heat exchange.Result of calculation is carried out the strengthening effect evaluation according to aforementioned same pump merit condition, is organized into the change curve of the ratio of reinforcement channel for heat exchange Nu number and smooth passage Nu number with flow Reynolds number.The centreline spacing of fin setting is: the horizontal and vertical 30mm of being.Fin width is that the distance between the two sides 3 is 20mm, and longshore current is 7mm to length.The windward side height keeps 6mm constant, changes the fin angle of inclination beta by changing lee face height h.The h=3 that gets, 4,5, the β angle of 6mm correspondence is respectively 23.2 °, 16.0 °, 8.1 ° and 0 °.The strengthening effect that is respectively laminar flow operating mode and turbulent operating mode shown in Figure 6, pairing thermal boundary condition is different, and the laminar flow operating mode is permanent wall temperature boundary condition, and turbulent operating mode is permanent hot-fluid boundary condition.
Result of study shown in Figure 6 shows that the strengthening effect of new structure is clearly, especially to the laminar flow operating mode, strengthens than 1.7～5.7, increases with the increase of Re number.The Changing Pattern of turbulent flow operating mode is different with laminar flow, strengthens than the increase with the Re number to reduce, and maximum is about 1.9.The Re number surpasses after 60000, and the fin structure of Low Angle Of Attack can occur strengthening than less than one situation, illustrates that this structure not too is applicable to the turbulent operating mode that the Re number is too high.
Claims (4)
1, a kind of synergic type reinforced heat exchange surface, comprise substrate (1) and many fins (2) that is arranged on the substrate (1), it is characterized in that: described fin (2) adopts three dimensional form, form by two identical side (3) and upper surface (4) of structure, side (3) is a ladder structure of right angle, and the limit that links to each other with substrate is a right-angle side; Along main flow direction, have one between upper surface (4) and the substrate (1) less than 90 ° angle of inclination beta, form local tapered channels between fin (2) and the substrate (1).
2, a kind of synergic type reinforced heat exchange surface according to claim 1 is characterized in that: two sides (3) of fin (2) are parallel to each other, and upper surface (4) are rectangle.
3, a kind of synergic type reinforced heat exchange surface according to claim 1 and 2, it is characterized in that: the angle of inclination beta between upper surface (4) and the substrate (1), being 15～17 ° when heat exchange surface is used for laminar heat transfer, is 23～24 ° when heat exchange surface is used for turbulent-flow heat-exchanging.
4, a kind of synergic type reinforced heat exchange surface according to claim 1 and 2 is characterized in that: the connected mode between fin (2) and the substrate (1) is soldering.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520017142 CN2809568Y (en) | 2005-04-22 | 2005-04-22 | Cooperative enhanced heat exchange surface |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520017142 CN2809568Y (en) | 2005-04-22 | 2005-04-22 | Cooperative enhanced heat exchange surface |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2809568Y true CN2809568Y (en) | 2006-08-23 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520017142 Expired - Lifetime CN2809568Y (en) | 2005-04-22 | 2005-04-22 | Cooperative enhanced heat exchange surface |
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| Country | Link |
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| CN (1) | CN2809568Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1329708C (en) * | 2005-04-22 | 2007-08-01 | 北京工业大学 | Synergic type reinforced heat exchange surface |
| CN102155851A (en) * | 2011-04-01 | 2011-08-17 | 株洲时代金属制造有限公司 | Water-cooling heat dissipater |
-
2005
- 2005-04-22 CN CN 200520017142 patent/CN2809568Y/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1329708C (en) * | 2005-04-22 | 2007-08-01 | 北京工业大学 | Synergic type reinforced heat exchange surface |
| CN102155851A (en) * | 2011-04-01 | 2011-08-17 | 株洲时代金属制造有限公司 | Water-cooling heat dissipater |
| CN102155851B (en) * | 2011-04-01 | 2013-10-16 | 株洲时代金属制造有限公司 | Water-cooling heat dissipater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Effective date of abandoning: 20050422 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |