阅读说明：本技术 一种增强整体热性能的构形截断肋结构 (Structure of structural truncated rib for enhancing integral thermal performance ) 是由 谢公南 张国花 朱睿 于 2021-10-10 设计创作，主要内容包括：本发明一种增强整体热性能的构形截断肋结构,属于强化换热技术领域；在高温部件的冷却通道中设置有构形截断肋,所述构形截断肋按周期沿冷却通道底部壁面长度方向均布；每个周期包括8排截断肋片,沿着气流方向,奇数排的肋片被截断,形成被截断肋片和截断区域,且沿气流方向每排被截断肋片和截断区域的数量逐渐递增；被截断后各奇数排内位于截断区域的肋片均沿气流方向向下游平移,形成周期内的偶数排。相较于传统的连续直肋,本发明在截断区域产生的横向涡,使近壁面流动结构发生变化,加强了主流与边界层流体的掺混,提高了冷却通道的换热性能和整体热性能。本发明结构简单,设计合理,适用于高温部件的内部冷却系统和强化换热系统。(The invention relates to a structural truncated rib structure for enhancing the overall thermal performance, belonging to the technical field of heat exchange enhancement; configurational cut-off ribs are arranged in a cooling channel of the high-temperature component and are uniformly distributed along the length direction of the wall surface at the bottom of the cooling channel according to cycles; each period comprises 8 rows of truncated ribs, odd rows of ribs are truncated along the airflow direction to form truncated ribs and truncated areas, and the number of the truncated ribs and the truncated areas of each row is gradually increased along the airflow direction; and after being cut off, the fins in the cut-off area in each odd row translate downstream along the airflow direction to form an even row in the period. Compared with the traditional continuous straight rib, the transverse vortex generated in the truncation area changes the near-wall surface flow structure, strengthens the mixing of the main flow and the boundary layer fluid, and improves the heat exchange performance and the overall thermal performance of the cooling channel. The invention has simple structure and reasonable design, and is suitable for an internal cooling system and a heat-transfer enhancement system of high-temperature components.)

1. A structure of configurational cut ribs for enhancing the overall thermal performance is characterized in that configurational cut ribs are arranged in a cooling channel of a high-temperature component and are uniformly distributed along the length direction of the wall surface at the bottom of the cooling channel periodically; the method is characterized in that: each period comprises 8 rows of truncated ribs, odd rows of ribs are truncated along the airflow direction to form truncated ribs and truncated areas, and the number of the truncated ribs and the truncated areas of each row is gradually increased along the airflow direction; and after being cut off, the fins in the cut-off area in each odd row translate downstream along the airflow direction to form an even row in the period.

2. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the two ends of the truncated ribs in the odd rows are tightly attached to the side wall surface of the cooling channel, and the truncation areas are positioned in the internal cooling channel.

3. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the odd-numbered rows of the intercepting regions in the period form a configuration structure along the airflow direction, and the number of the intercepting regions is 1, 2, 4 and 8 in sequence.

4. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the distance between the rib positioned in the truncation area and the truncated rib at the upstream of the rib is D after translation, the distance between two adjacent rows of truncated ribs is P, and the ratio of D/P is greater than or equal to 1/5 and less than or equal to 4/5.

5. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the total length of the intercepting regions in each odd row within said period is equal, and thus the total length of the ribs of the intercepting regions in each even row is equal.

6. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the total length of the intercepting areas in each odd row in the period is L, the width of the cooling channel is W, and L/W is larger than or equal to 1/5 and smaller than or equal to 1/2.

7. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the height of the truncated ribs is e, and the proportional relation between the height of the truncated ribs and the distance P between two adjacent rows of truncated ribs is that P/e is more than or equal to 8 and less than or equal to 15.

8. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the proportional relation between the height e of the intercepting rib and the internal height H of the cooling channel is that e/H is more than or equal to 1/10 and less than or equal to 1/4.

9. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the cross-sectional shape of the truncated ribs is arbitrary.

10. The structural truncated rib structure for enhancing overall thermal performance of claim 1, wherein: the truncated ribs are straight ribs or inclined ribs, the truncated ribs serving as the straight ribs are perpendicular to the right side wall in the cooling channel, the truncated ribs serving as the inclined ribs and the right side wall in the cooling channel form an alpha included angle, and the included angle is larger than or equal to 30 degrees and smaller than or equal to 90 degrees.

Technical Field

The invention belongs to the technical field of heat exchange enhancement, and particularly relates to a structural truncated rib structure for enhancing the overall thermal performance.

Background

The fin structure is a main enhanced heat exchange technology in practical engineering application, and is widely applied to internal cooling of turbine blades of gas turbines, regenerative cooling of scramjet engines, solar air heaters, heat sinks of miniature electronic components and the like. The temperature of the turbine inlet of the gas turbine which is gradually increased far exceeds the tolerance temperature limit of the turbine blade material, and the development of efficient turbine blade cooling technology to reduce the temperature of the blade and prolong the service time of the blade is imperative. Due to the fact that the flight Mach number and the cruising time of the hypersonic aircraft are increased, the thermal environment borne by the scramjet is quite severe, regenerative cooling is considered to be the best cooling mode of the scramjet, and the key scientific and technical problem of the scramjet is solved by exploring an efficient regenerative cooling system. For the solar air heater, because the heat conductivity coefficient of air is small, the convective heat transfer coefficient is small, and the key for improving the performance of the air heater is to try to strengthen the heat transfer between the air and the solar heat absorbing plate. In addition, in modern high-power aerospace precision instruments, high-intensity lasers and other devices, microelectronic components are highly integrated and miniaturized, so that the heating power of the components continuously rises, and the heat dissipation performance of the electronic components becomes one of the bottlenecks restricting the development of the microelectronic industry.

The use of the fins can generate secondary flow in the internal channel, generate disturbance to fluid and increase the heat exchange area, thereby achieving the purpose of enhancing the heat exchange performance of the channel. However, the arrangement of the ribs increases the flow resistance of the passage, which increases the pressure loss of the fluid in the passage. Interrupted ribs have been extensively studied because of their ability to reduce the pressure loss of the continuous rib channels. Through the search of prior art documents, Chinese patent application No. 201910344045.3, patent publication date 2019, 7 and 23 days, patent name: the utility model provides an interrupted rib internal cooling structure for gas turbine blade, this patent sets up U type fork wall at blade major structure, all sets up between lateral wall and U type fork wall and is interrupted the rib to it sets up in pairs to be interrupted the rib. The disturbance generated by the cooling mode to the gas flow is enhanced, so that the separation degree generated by the gas flow is increased, the turbulence degree of the fluid is enhanced, the heat exchange is enhanced, and the pressure loss is reduced. However, because the discontinuous ribs are arranged in pairs in the structure, the fluid in the middle area of the inner channel is not disturbed, so that a low heat exchange area is formed in the middle of the channel, and the uniformity of heat exchange in the channel is reduced. To address this problem, chinese patent application No. 202010992833.6, patent publication date 2021, 1 month 5 day, patent name: a fractal intermittent rib structure suitable for internal cooling of a turbine blade is characterized in that fractal intermittent fins are arranged in an internal cooling channel, continuous disturbance is caused to incoming flow by the cooling mode, and the continuously increased intermittent areas are beneficial to improving the uniformity of channel heat exchange. However, the absence of fins in the discontinuous regions of the structure reduces the heat exchange area of the channels compared to continuous straight ribs.

In addition, the document "Street network term of organization in nature" (ASME Journal of Heat Transfer,2008, 40 th) firstly applies the configuration theory to improve the Heat exchange performance of the Heat exchange system, and at present, the configuration theory has been widely applied to a plurality of fields such as engineering and life, and is used for better organizing the flow and connection of personnel, goods and information. The document "Design with constraint the term the" (1)^stInternational works hop,2008) states that a topographical structure can provide better fluid permeability when the number of branches of the topographical structure is equal to or greater than 4, and that the topographical structure performs better when the length of the next stage topographical branch is 1/2 times the length of the previous stage topographical branch.

Disclosure of Invention

The technical problem to be solved is as follows:

in order to avoid the disadvantages of the prior art, the invention proposes a profiled truncated rib structure with enhanced overall thermal performance, which, thanks to the presence of the truncated ribs downstream of the truncated rib, causes a separation of the cooling fluid flow, forming transverse vortices at the two ends of the truncated rib. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved.

The technical scheme of the invention is as follows: a structure of configurational cut ribs for enhancing the overall thermal performance is characterized in that configurational cut ribs are arranged in a cooling channel of a high-temperature component and are uniformly distributed along the length direction of the wall surface at the bottom of the cooling channel periodically; the method is characterized in that: each period comprises 8 rows of truncated ribs, odd rows of ribs are truncated along the airflow direction to form truncated ribs and truncated areas, and the number of the truncated ribs and the truncated areas of each row is gradually increased along the airflow direction; and after being cut off, the fins in the cut-off area in each odd row translate downstream along the airflow direction to form an even row in the period.

The further technical scheme of the invention is as follows: the two ends of the truncated ribs in the odd rows are tightly attached to the side wall surface of the cooling channel, and the truncation areas are positioned in the internal cooling channel.

The further technical scheme of the invention is as follows: the odd-numbered rows of the intercepting regions in the period form a configuration structure along the airflow direction, and the number of the intercepting regions is 1, 2, 4 and 8 in sequence.

The further technical scheme of the invention is as follows: the distance between the rib positioned in the truncation area and the truncated rib at the upstream of the rib is D after translation, the distance between two adjacent rows of truncated ribs is P, and the ratio of D/P is greater than or equal to 1/5 and less than or equal to 4/5.

The further technical scheme of the invention is as follows: the total length of the intercepting regions in each odd row within said period is equal, and thus the total length of the ribs of the intercepting regions in each even row is equal.

The further technical scheme of the invention is as follows: the total length of the intercepting areas in each odd row in the period is L, the width of the cooling channel is W, and L/W is larger than or equal to 1/5 and smaller than or equal to 1/2.

The further technical scheme of the invention is as follows: the height of the truncated ribs is e, and the proportional relation between the height of the truncated ribs and the distance P between two adjacent rows of truncated ribs is that P/e is more than or equal to 8 and less than or equal to 15.

The further technical scheme of the invention is as follows: the proportional relation between the height e of the intercepting rib and the internal height H of the cooling channel is that e/H is more than or equal to 1/10 and less than or equal to 1/4.

The further technical scheme of the invention is as follows: the cross-sectional shape of the truncated ribs is arbitrary.

The further technical scheme of the invention is as follows: the truncated ribs are straight ribs or inclined ribs, the truncated ribs serving as the straight ribs are perpendicular to the right side wall in the cooling channel, the truncated ribs serving as the inclined ribs and the right side wall in the cooling channel form an alpha included angle, and the included angle is larger than or equal to 30 degrees and smaller than or equal to 90 degrees.

Advantageous effects

The invention has the beneficial effects that: firstly, compared with a smooth channel, the arrangement of the cutting ribs increases the heat exchange area in the channel, increases the disturbance effect on fluid, and greatly improves the convection heat exchange performance of the channel. And compared with a continuous straight fin channel, although the heat exchange area of the channel is not obviously increased by the truncated fins, the turbulence effect on airflow is enhanced by the transverse vortex pair induced by the truncated fin region, the mixing effect of the main flow and the boundary layer fluid is enhanced, the turbulence degree of the fluid is increased, and the heat exchange performance of the channel is improved. And finally, the fins are cut off by utilizing the configuration principle, and the continuous disturbance is generated on the fluid along the flow direction to strengthen the heat exchange of the channel. Therefore, the structural truncated rib structure suitable for enhancing the overall thermal performance has the advantages of high convection heat exchange performance, high overall thermal performance and the like, and the improvement of the heat exchange performance, the pressure loss and the overall thermal performance is shown in the attached figure 8 of the specification.

Compared with the prior art, the invention has the advantages that the heat exchange in the channel is greatly improved, and the overall thermal performance is greatly improved by comparing the specific test results, and the specific analysis is as follows:

in example 1, after the cold fluid enters the internal channel, a part of the fluid flows into the intercepting region, and a pair of transverse vortexes are respectively formed at two sides of the intercepting region, and are attached to the rear parts of the two intercepting fins, so that the backflow region behind the ribs is reduced, the heat exchange is enhanced, the other part of the fluid flows through the intercepting fins, the backflow region is generated at the upstream and the downstream of the intercepting fins, and the reattachment phenomenon occurs between two adjacent rows of fins. The presence of the fins of the intercepting region downstream of the intercepted fins separates the flow of the cooling fluid, forming transverse vortices at the two ends of the intercepting region fins. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation result shows that when the Reynolds number of the cold fluid is 80000, the heat exchange of the embodiment is increased by 69% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 60%.

In the embodiment 2, since the cross-sectional shape of the rib is triangular and the oblique side faces away from the incoming flow direction, compared with the embodiment 1, the back flow area of the rib is small in the embodiment, and the average heat exchange performance of the channel is enhanced. The presence of the fins of the intercepting region downstream of the intercepted fins separates the flow of the cooling fluid, forming transverse vortices at the two ends of the intercepting region fins. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation result shows that when the reynolds number of cold fluid is 80000, the heat exchange of the embodiment is increased by 80% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 62%.

In example 3, compared to example 1, the pair of transverse vortices formed on both sides downstream of the truncated zone rib has a larger vorticity and a stronger disturbance to the fluid. While the other part flows through the truncated ribs, creating recirculation zones both upstream and downstream of the truncated ribs and reattachment phenomena between two adjacent rows of ribs. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation result shows that when the Reynolds number of the cold fluid is 80000, the heat exchange of the embodiment is increased by 76% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 65%.

In example 4, the calculation results show that when the cold fluid Reynolds number is 80000, the heat exchange of the embodiment is increased by 69% relative to the heat exchange of the continuous straight rib channels, and the overall thermal performance is improved by 60%.

In example 5, the lateral vorticity on the right side in the flow direction was greater due to the inclination of the fins. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation results show that when the Reynolds number of the cold fluid is 80000, the heat exchange of the embodiment is increased by 75% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 64%.

Drawings

FIG. 1 is a schematic view of the structure of example 1 of the present invention with the top wall removed;

FIG. 2 is a top view of example 1 of the present invention with the top wall removed;

FIG. 3 is a front view of embodiment 1 of the present invention with the right side wall removed;

FIG. 4 is a front view of embodiment 2 of the present invention with the right side wall removed;

FIG. 5 is a top view of example 3 of the present invention with the top wall removed;

FIG. 6 is a top view of example 4 of the present invention with the top wall removed;

FIG. 7 is a top view of example 5 of the present invention with the top wall removed;

FIG. 8 is a graph showing heat exchange performance (Nu/Nu) of examples 1, 2, 3, 4 and 5 of the present invention₀) Pressure loss (f/f)₀) And bulk thermal performance (Nu/Nu)₀/(f/f₀)^1/3) Comparison of heat exchange performance, pressure loss and overall thermal performance with example 0 (continuous straight rib channel).

Description of reference numerals: 1. the left side wall surface, the right side wall surface, the bottom wall surface, the truncated ribs, the truncated areas, the ribs, the truncated areas, the configuration period, the width of the cooling channel, the total length of each row of discontinuous areas, the space between two adjacent rows of truncated ribs in the flow direction, the flow direction space between the truncated ribs and the truncated ribs, the height of the ribs, the internal height of the cooling channel, and the inclination angle of the truncated ribs.

Detailed Description

The embodiments described below with reference to the drawings are illustrative and intended to be illustrative of the invention and are not to be construed as limiting the invention.

In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "clockwise", "counterclockwise", and the like, indicate orientations and positional relationships based on those shown in the drawings, and are used only for convenience of description and simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be considered as limiting the present invention.

The invention provides a structural truncated rib structure for enhancing the overall thermal performance, which comprises a left side wall surface 1, a right side wall surface 2, a bottom wall surface 3, truncated ribs 4, a truncated area 5 and truncated area ribs 6, wherein the truncated ribs are placed in cooling channels of internal cooling components such as wide W and high H blades. The height of the truncation rib is e, the interval between every two adjacent rows of truncated ribs is P along the incoming flow direction of the airflow, the ribs in the truncation area move towards the downstream of the truncated ribs, and the moving distance D satisfies 1/5-4/5. The profiled chopping ribs are characterized in that all the chopping ribs are arranged in the cooling member channel in profiled cycles 7, each profiled cycle comprising four rows of chopped ribs and four rows of chopping area ribs moving downstream. Specifically, in the direction of fluid flow, the first row of truncated ribs has 1 truncated zone located in the center of the channel, the second row of truncated ribs has 2 truncated zones, the third row of truncated ribs has 4 truncated zones, and the fourth row of truncated ribs has 8 truncated zones. Correspondingly, the number of the truncated zone ribs moving downstream in the fluid flow direction is 1 in the first row, 2 in the second row, 4 in the third row and 8 in the fourth row. The total length of the truncated area of each row of truncated ribs is L, the total length of the truncated ribs of each row is also L, and the condition that L/W is more than or equal to 1/5 and less than or equal to 1/2 is met. In addition, the ratio of the rib spacing P of two adjacent rows of truncated ribs to the height e of the truncated ribs satisfies 8-15, and the ratio of the height e of the truncated ribs to the internal height H of the cooling channel satisfies 1/10-1/4.

Fig. 1 to 3 show embodiment 1 of the present invention. In the present embodiment, a two-period configuration truncated rib structure is arranged in the cooling channel, wherein the truncated rib is perpendicular to the right side wall of the channel, the cross-sectional shape of the truncated rib is square, and the rib width of the truncated rib is equal to the rib height e of the truncated rib. The rib of the truncation area is positioned in the middle of two adjacent rows of the truncated ribs, the distance between the rib of the truncation area and the corresponding truncated rib is P/2, the length L of the truncation area is 1/4 of the width W of the channel, the height e of the truncation rib is 1/10 of the distance P between the two adjacent rows of the truncated ribs, and the height e of the truncation rib is 1/8 of the internal height H of the channel. After cold fluid enters the internal channel, a part of the fluid flows into the intercepting area, a pair of transverse vortexes are respectively formed at two sides of the intercepting area and attached to the rear parts of the two intercepting fins, a backflow area behind the ribs is reduced, heat exchange is enhanced, the other part of the fluid flows through the intercepting fins, backflow areas are generated at the upstream and the downstream of the intercepting fins, and the reattachment phenomenon occurs between two adjacent rows of fins. The presence of the fins of the intercepting region downstream of the intercepted fins separates the flow of the cooling fluid, forming transverse vortices at the two ends of the intercepting region fins. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation result shows that when the Reynolds number of the cold fluid is 80000, the heat exchange of the embodiment is increased by 69% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 60%.

Fig. 4 shows example 2 of the present invention. In this embodiment, two periodic configuration truncated rib structures are arranged in the cooling channel, wherein the truncated ribs are perpendicular to the right side wall of the channel, the cross-sectional shape of the truncated ribs is an isosceles right triangle with a side length of e, and the right-angle sides of the ribs face the incoming flow direction. The rib of the truncation area is positioned in the middle of two adjacent rows of the truncated ribs, the distance between the rib of the truncation area and the corresponding truncated rib is P/2, the length L of the truncation area is 1/4 of the width W of the channel, the height e of the truncation rib is 1/10 of the distance P between the two adjacent rows of the truncated ribs, and the height e of the truncation rib is 1/8 of the internal height H of the channel. After the cold fluid enters the internal channel, a part of the fluid flows into the truncation area, a pair of transverse vortexes are respectively formed on two sides of the truncation area and attached to the rear parts of the two truncation fins, a backflow area behind the ribs is reduced, heat exchange is enhanced, the other part of the fluid flows through the truncation fins, the backflow area is formed on the upstream and the downstream of the truncation fins, but the cross section of each fin is triangular, and the inclined side faces back to the incoming flow direction, so that compared with embodiment 1, the backflow area behind the ribs is small, and the average heat exchange performance of the channel is enhanced. The presence of the fins of the intercepting region downstream of the intercepted fins separates the flow of the cooling fluid, forming transverse vortices at the two ends of the intercepting region fins. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation result shows that when the reynolds number of cold fluid is 80000, the heat exchange of the embodiment is increased by 80% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 62%.

Fig. 5 shows example 3 of the present invention. In the present embodiment, a two-period configuration truncated rib structure is arranged in the cooling channel, wherein the truncated rib is perpendicular to the right side wall of the channel, the cross-sectional shape of the truncated rib is square, and the rib width of the truncated rib is equal to the rib height e of the truncated rib. The rib of the truncation area is positioned in the middle of two adjacent rows of the truncated ribs, the distance between the rib of the truncation area and the corresponding truncated rib is P/3, the length L of the truncation area is 1/4 of the width W of the channel, the height e of the truncation rib is 1/10 of the distance P between the two adjacent rows of the truncated ribs, and the height e of the truncation rib is 1/8 of the internal height H of the channel. After cold fluid enters the internal channel, a part of fluid flows into the intercepting area, but because the intercepting area rib is close to the intercepted rib, the fluid flowing through the intercepting area cannot form transverse vortexes on two sides of the rib, the fluid is separated in a flowing mode under the action of the intercepting area rib, and a pair of transverse vortexes are formed on two sides of the downstream of the intercepting area rib. While the other part flows through the truncated ribs, creating recirculation zones both upstream and downstream of the truncated ribs and reattachment phenomena between two adjacent rows of ribs. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation result shows that when the Reynolds number of the cold fluid is 80000, the heat exchange of the embodiment is increased by 76% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 65%.

Fig. 6 shows example 4 of the present invention. In the present embodiment, a two-period configuration truncated rib structure is arranged in the cooling channel, wherein the truncated rib is perpendicular to the right side wall of the channel, the cross-sectional shape of the truncated rib is square, and the rib width of the truncated rib is equal to the rib height e of the truncated rib. The rib of the intercepting area is positioned between two adjacent rows of the intercepted ribs, the distance between the rib of the intercepting area and the corresponding intercepted rib is 2/3P, the length L of the intercepting area is 1/4 of the width W of the channel, the height e of the intercepting rib is 1/10 of the distance P between two adjacent rows of the intercepted ribs, and the height e of the intercepting rib is 1/8 of the internal height H of the channel. After cold fluid enters the internal channel, a part of the fluid flows into the truncation area, a pair of transverse vortexes are respectively formed at two sides of the truncation area and attached to the rear parts of the two truncation ribs, a backflow area behind the ribs is reduced, heat exchange is enhanced, the other part of the fluid flows through the truncation ribs, backflow areas are generated at the upstream and the downstream of the truncation ribs, and the reattachment phenomenon occurs between two adjacent rows of ribs. The presence of the fins of the intercepting region downstream of the intercepted fins separates the flow of the cooling fluid, forming transverse vortices at the two ends of the intercepting region fins. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation result shows that when the Reynolds number of the cold fluid is 80000, the heat exchange of the embodiment is increased by 69% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 60%.

Fig. 7 shows example 5 of the present invention. In the present embodiment, two periodic configurations of truncated rib structures are arranged in the cooling channel, wherein the included angle between the truncated rib and the right side wall of the channel is 75 °, the cross-sectional shape of the truncated rib is square, and the rib width of the truncated rib is equal to the rib height e. The rib of the truncation area is positioned in the middle of two adjacent rows of the truncated ribs, the distance between the rib of the truncation area and the corresponding truncated rib is P/2, the length L of the truncation area is 1/4 of the width W of the channel, the height e of the truncation rib is 1/10 of the distance P between the two adjacent rows of the truncated ribs, and the height e of the truncation rib is 1/8 of the internal height H of the channel. After cold fluid enters the internal channel, a part of the fluid flows into the intercepting region, a pair of transverse vortexes are respectively formed at two sides of the intercepting region, the other part of the fluid flows through the intercepting ribs, backflow regions are generated at the upstream and the downstream of the intercepting ribs, and the phenomenon of reattachment occurs between two adjacent rows of ribs, so that the heat exchange of the channel is enhanced. The presence of the fins in the cutoff zone downstream of the cutoff fins separates the cooling fluid flow, forming transverse vortices at the two ends of the cutoff zone fins, the transverse vortices on the right side in the flow direction being of greater strength due to the fins being inclined. The existence of the transverse vortex enables a near-wall surface flow structure to change, the mixing of a main flow and a boundary layer fluid is enhanced, and the heat exchange performance and the overall thermal performance of the channel are improved. The calculation results show that when the Reynolds number of the cold fluid is 80000, the heat exchange of the embodiment is increased by 75% relative to the heat exchange of the continuous straight rib channel, and the overall thermal performance is improved by 64%.

Although embodiments of the present invention have been shown and described above, it is understood that the above embodiments are exemplary and should not be construed as limiting the present invention, and that variations, modifications, substitutions and alterations can be made in the above embodiments by those of ordinary skill in the art without departing from the principle and spirit of the present invention.