CN206670438U - One kind mixing sphere ripple heat exchanger plates - Google Patents
One kind mixing sphere ripple heat exchanger plates Download PDFInfo
- Publication number
- CN206670438U CN206670438U CN201720010845.8U CN201720010845U CN206670438U CN 206670438 U CN206670438 U CN 206670438U CN 201720010845 U CN201720010845 U CN 201720010845U CN 206670438 U CN206670438 U CN 206670438U
- Authority
- CN
- China
- Prior art keywords
- heat exchange
- spherical
- sphere
- plate
- heat exchanger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000013461 design Methods 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 238000007789 sealing Methods 0.000 abstract description 2
- 239000012530 fluid Substances 0.000 description 9
- 238000012546 transfer Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000012827 research and development Methods 0.000 description 2
- 238000004378 air conditioning Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
本实用新型公开了一种混合球面波纹换热板,它是在单板尺寸长*宽*高为829.18mm*370.82mm*0.5mm的长方形板材上做出两种混合球面波纹设计,其中一种为满足方程x2/16+y2/16+z2/64=1的椭球面,另一种为半径r=4的球面,二者单位均为毫米。同一行的椭球面或球面的凹凸性相同,且左右间隔均为1.2705mm,整行个数均为40个;相邻上下椭球面与球面的凹凸性相反,且首尾恰好处于同一水平面上。经设计计算,单个换热板每面均有椭球面和球面25行。在进出水方面,采用在四角设置直径为60mm的圆形孔,板两面的边缘均加有厚为4mm的密封橡胶带。本新型混合球面换热板具有较低的流动阻力和更为复杂的紊流状态。另外,对单纯的用于换热使用的混合球面采用宽与长之比近似黄金比例的设计理念。
The utility model discloses a mixed spherical corrugated heat exchange plate, which is made of two kinds of mixed spherical corrugated designs on a rectangular plate with a length*width*height of 829.18mm*370.82mm*0.5mm, one of which is An ellipsoid satisfying the equation x 2 /16+y 2 /16+z 2 /64=1, and a sphere with a radius r=4, and the units of both are millimeters. The ellipsoidal or spherical surfaces in the same row have the same concavity and convexity, and the left and right intervals are 1.2705 mm, and the number of the entire row is 40; the concavity and convexity of the adjacent upper and lower ellipsoidal surfaces are opposite to the spherical surface, and the head and tail are exactly on the same horizontal plane. According to the design calculation, each surface of a single heat exchange plate has 25 rows of ellipsoidal and spherical surfaces. In terms of water inlet and outlet, circular holes with a diameter of 60mm are set at the four corners, and sealing rubber belts with a thickness of 4mm are added to the edges of both sides of the plate. The novel hybrid spherical heat exchange plate has lower flow resistance and more complicated turbulent flow state. In addition, the design concept that the ratio of width to length approximates the golden ratio is adopted for the purely mixed spherical surface used for heat exchange.
Description
技术领域technical field
本实用新型涉及换热器领域的一种混合球面波纹换热板。The utility model relates to a hybrid spherical corrugated heat exchange plate in the field of heat exchangers.
背景技术Background technique
换热器是一种使不同温度下的两种或两种以上流体实现物料之间热量传递的节能设备,它使热量由温度较高的流体传递给温度较低的流体,使流体温度达到流程规定的指标,以满足工艺条件的需要。换热器的发展已经深入到人们生活的方方面面,如:空调暖通、压力容器、水处理设备等等。可以说,换热器行业研究发展水平的高低,直接体现出一个国家在能源综合利用率方面的科研发展水平。在种类繁多的换热器当中,板式换热器以其传热系数高、结构紧凑、初期投资成本少、末端温差小、适用于多种流体介质传热等优点,在形式众多的换热器中独占一席之地。而换热板作为板式换热器最为重要的组成部分之一,其研究水平的高低直接影响着板式换热器换热能力的大小。目前应用较为广泛的换热板为人字形波纹换热板和水平平直波纹换热板,近来也出现了诸如球面不连续波纹换热板等一系列新型的波纹换热板。A heat exchanger is an energy-saving device that enables two or more fluids at different temperatures to transfer heat between materials. It transfers heat from a fluid with a higher temperature to a fluid with a lower temperature, making the fluid temperature reach the process Specified indicators to meet the needs of process conditions. The development of heat exchangers has penetrated into all aspects of people's lives, such as: air conditioning, HVAC, pressure vessels, water treatment equipment and so on. It can be said that the level of research and development of the heat exchanger industry directly reflects the level of scientific research and development of a country in terms of comprehensive energy utilization. Among the various types of heat exchangers, the plate heat exchanger has the advantages of high heat transfer coefficient, compact structure, low initial investment cost, small temperature difference at the end, and is suitable for heat transfer in various fluid media. occupy a place in the As the heat exchange plate is one of the most important components of the plate heat exchanger, its research level directly affects the heat transfer capacity of the plate heat exchanger. At present, the widely used heat exchange plates are herringbone corrugated heat exchange plates and horizontal flat corrugated heat exchange plates. Recently, a series of new corrugated heat exchange plates such as spherical discontinuous corrugated heat exchange plates have also appeared.
发明内容Contents of the invention
为了提高现存换热板的换热系数,减小换热流体的流动阻力,以及进一步改善其美学欣赏价值等,本实用新型提供了一种混合球面波纹换热板,板面凹凸不平的设计极大地增加了换热板整体换热面积,提高了换热能力。In order to improve the heat transfer coefficient of the existing heat exchange plate, reduce the flow resistance of the heat exchange fluid, and further improve its aesthetic appreciation value, the utility model provides a hybrid spherical corrugated heat exchange plate with an extremely uneven surface design. The overall heat exchange area of the heat exchange plate is greatly increased, and the heat exchange capacity is improved.
本实用新型解决其技术问题所采用的技术方案是:在长方形板材(单板尺寸长*宽*高为829.18mm*370.82mm*0.5mm)上做出两种混合球面波纹设计,其中一种为满足方程x2/16+y2/16+z2/64=1(单位mm)的椭球面,另一种为半径r=4 (单位mm)的球面。同一行的椭球面或球面的凹凸性相同,且左右间隔均为 1.2705mm,整行个数均为40个;相邻上下椭球面与球面的凹凸性相反,且首尾恰好处于同一水平面上。经设计计算,单个换热板每面均有椭球面和球面25行。在进出水方面,采用现有的技术在换热板四个角开有直径为60mm的圆形孔,板两面的边缘均加有厚为4mm的密封橡胶带,整体采用冷热双流道逆流换热模式。这种混合球面波纹换热板,较以往的水平平直波纹板、竖直波纹板、人字形波纹板等,一定程度上增加了换热的面积,同时比较近期才出现的球面不连续波纹换热板,该新型混合球面换热板具有较低的流动阻力和更为复杂的紊流状态,从而具备更为高效的换热性能。另外,在板材美学应用方面,也做出了进一步的改善,对单纯用于换热使用的混合球面的设计尺寸符合黄金比例 设计理念。The technical solution adopted by the utility model to solve the technical problem is: make two kinds of mixed spherical corrugated designs on the rectangular plate (the length*width*height of the single plate is 829.18mm*370.82mm*0.5mm), one of which is An ellipsoid that satisfies the equation x 2 /16+y 2 /16+z 2 /64=1 (unit mm), and the other is a spherical surface with a radius r=4 (unit mm). The ellipsoidal or spherical surfaces in the same row have the same concavity and convexity, and the left and right intervals are 1.2705 mm, and the number of the entire row is 40; the concavity and convexity of the adjacent upper and lower ellipsoidal surfaces are opposite to the spherical surface, and the head and tail are exactly on the same horizontal plane. According to the design calculation, each surface of a single heat exchange plate has 25 rows of ellipsoidal and spherical surfaces. In terms of water inlet and outlet, using the existing technology, circular holes with a diameter of 60mm are opened at the four corners of the heat exchange plate, and sealing rubber belts with a thickness of 4mm are added to the edges of both sides of the plate. heat mode. This kind of hybrid spherical corrugated heat exchange plate increases the heat exchange area to a certain extent compared with the previous horizontal flat corrugated plate, vertical corrugated plate, herringbone corrugated plate, etc. Heat plate, the new hybrid spherical heat exchange plate has lower flow resistance and more complex turbulence state, so it has more efficient heat exchange performance. In addition, further improvements have been made in the aesthetic application of the plate, and the design size of the mixed spherical surface purely used for heat exchange conforms to the golden ratio design concept.
本实用新型的有益效果是:在一定程度上增加了现有板式换热器的换热能力,提高了传统换热板片的美学价值。The beneficial effects of the utility model are: to a certain extent, the heat exchange capacity of the existing plate heat exchanger is increased, and the aesthetic value of the traditional heat exchange plates is improved.
附图说明Description of drawings
下面将结合附图对本实用新型作进一步说明(单位mm):The utility model will be further described below in conjunction with accompanying drawing (unit mm):
图1是本实用新型混合球面波纹换热板的整体示意图;Fig. 1 is the overall schematic diagram of the hybrid spherical corrugated heat exchange plate of the present invention;
图2是本实用新型换热板混合球面波纹的局部示意图;Fig. 2 is a partial schematic diagram of the hybrid spherical corrugation of the heat exchange plate of the present invention;
图中,A、B分别为某一种流体的进、出口,C、D分别为另一种流体的进、出口。In the figure, A and B are respectively the inlet and outlet of a certain fluid, and C and D are respectively the inlet and outlet of another fluid.
具体实施方式detailed description
图1中,较粗的黑色实线是用来密封换热介质的橡胶线圈,厚度为4mm。在实际应用时,一种换热介质从A孔口流入,经分流道,顺着该混合球面波纹换热板波纹的径向向下流动,最后经过分流道汇集,从B孔口流出;而与此同时,另一种换热介质从C孔口流入,经分流道,在另一面顺着该混合球面波纹换热板波纹的径向向上流动,最后经过分流道汇集,从D孔口流出。这种逆流换热模式使温度不同的两种换热介质在隔着换热板的情形下得以充分接触,实现热量的传递。同时,在板材尺寸方面,融入了中国传统的美学特性,对单纯用于换热使用的混合球面的设计尺寸符合黄金比例设计理念。In Figure 1, the thick black solid line is the rubber coil used to seal the heat exchange medium, with a thickness of 4mm. In practical application, a heat exchange medium flows in from the port A, passes through the flow channel, flows downward along the radial direction of the corrugation of the mixed spherical corrugated heat exchange plate, and finally collects through the flow channel and flows out from the port B; At the same time, another heat exchange medium flows in from C orifice, passes through the flow channel, flows upward along the radial direction of the hybrid spherical corrugated heat exchange plate on the other side, and finally gathers through the flow channel and flows out from D orifice . This counter-current heat exchange mode allows two heat exchange media with different temperatures to fully contact with each other through the heat exchange plate to realize heat transfer. At the same time, in terms of plate size, traditional Chinese aesthetic characteristics are incorporated, and the design size of the hybrid spherical surface purely used for heat exchange conforms to the golden ratio design concept.
图2是本新型换热板混合球面波纹的局部情形,换热介质从混合球面换热板表面流过,实现两种流体的热量传递效果。Fig. 2 is a local situation of the mixed spherical corrugation of the new heat exchange plate, the heat exchange medium flows through the surface of the mixed spherical heat exchange plate to realize the heat transfer effect of the two fluids.
Claims (4)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720010845.8U CN206670438U (en) | 2017-01-05 | 2017-01-05 | One kind mixing sphere ripple heat exchanger plates |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201720010845.8U CN206670438U (en) | 2017-01-05 | 2017-01-05 | One kind mixing sphere ripple heat exchanger plates |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206670438U true CN206670438U (en) | 2017-11-24 |
Family
ID=60356292
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201720010845.8U Expired - Fee Related CN206670438U (en) | 2017-01-05 | 2017-01-05 | One kind mixing sphere ripple heat exchanger plates |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN206670438U (en) |
-
2017
- 2017-01-05 CN CN201720010845.8U patent/CN206670438U/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102435086A (en) | A bionic honeycomb plate for plate heat exchanger | |
CN207922922U (en) | A kind of minim channel flat plate heat exchanger | |
CN102322757B (en) | Honeycomb type heat exchanger adopting multiple times of diffluence and confluence | |
CN107606977A (en) | Heat exchange monomer, heat exchange movement and total-heat exchanger | |
CN201844716U (en) | High-efficiency compact condensing heat exchanger | |
CN104236361B (en) | Honeycomb ribbed plate heat storage and exchange device | |
CN206670438U (en) | One kind mixing sphere ripple heat exchanger plates | |
CN203454859U (en) | Novel laminated sheet type longitudinal flow heat exchanger | |
CN206019420U (en) | Movable tube sheets heat exchanger | |
CN205482512U (en) | Sinusoidal ripple heat transfer board | |
CN201096433Y (en) | Condenser | |
CN110360858A (en) | A kind of heat exchanger plate beam for phase-change heat-exchange | |
CN201764873U (en) | Drain pipe flow diversion and heat exchange plate and heat exchanger using heat exchange plate | |
CN201269712Y (en) | Multi-channel heat exchanger pipe | |
CN208567605U (en) | A kind of plate heat exchanger for exchanging heat between gas-liquid | |
CN104501638B (en) | Heat exchange fin, heat exchanger and air conditioner | |
CN209263756U (en) | Special-shaped strip-fin oil cooler | |
CN203240948U (en) | Heat exchanging pipeline | |
CN203224046U (en) | Flat-plate solar collector | |
CN203824403U (en) | Fin of air heat exchanger | |
CN102305560A (en) | Design method of plate heat exchanger | |
CN209445851U (en) | A kind of novel combined graphite heat exchanger | |
CN202145108U (en) | Plate type heat exchanger with non-uniform section | |
CN209371833U (en) | A kind of water cooled condenser energy saver | |
CN201844719U (en) | Compact condensing heat exchanger |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171124 Termination date: 20190105 |
|
CF01 | Termination of patent right due to non-payment of annual fee |