CN101226021A - Finned tube heat exchanger lined with metal foam - Google Patents

Finned tube heat exchanger lined with metal foam Download PDF

Info

Publication number
CN101226021A
CN101226021A CNA2008100332891A CN200810033289A CN101226021A CN 101226021 A CN101226021 A CN 101226021A CN A2008100332891 A CNA2008100332891 A CN A2008100332891A CN 200810033289 A CN200810033289 A CN 200810033289A CN 101226021 A CN101226021 A CN 101226021A
Authority
CN
China
Prior art keywords
metal
tube
heat exchanger
metal foam
foam
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.)
Pending
Application number
CNA2008100332891A
Other languages
Chinese (zh)
Inventor
丁国良
朱禹
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Jiao Tong University
Original Assignee
Shanghai Jiao Tong University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shanghai Jiao Tong University filed Critical Shanghai Jiao Tong University
Priority to CNA2008100332891A priority Critical patent/CN101226021A/en
Publication of CN101226021A publication Critical patent/CN101226021A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/40Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being only inside the tubular element
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F1/00Tubular elements; Assemblies of tubular elements
    • F28F1/10Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses
    • F28F1/42Tubular elements and assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with projections, with recesses the means being both outside and inside the tubular element
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/003Arrangements for modifying heat-transfer, e.g. increasing, decreasing by using permeable mass, perforated or porous materials

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Geometry (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

本发明涉及一种制冷技术领域的内衬泡沫金属的翅片管式换热器,包括管外金属翅片、金属管和泡沫金属,管内填充有泡沫金属,以提高换热器管内换热性能。所述的泡沫金属内部有供气体或液体介质流通的孔洞。所述的泡沫金属在金属管内有内衬形式为全截面式、内环式或上薄下厚式中的一种或两种或三种。本发明传热效果明显优于现有的翅片管式换热器,从而减小换热器体积,节约材料,经初步计算换热器体积和用料均可减少20%-40%;并且与目前普遍使用的翅片管换热器相比成本增加不多。

Figure 200810033289

The invention relates to a finned tube heat exchanger lined with metal foam in the field of refrigeration technology, which includes metal fins outside the tube, metal tubes and metal foam, and the tube is filled with metal foam to improve the heat transfer performance in the tube of the heat exchanger . There are holes inside the metal foam for the circulation of gas or liquid medium. The metal foam is lined in the metal pipe in the form of one or two or three of the full-section type, the inner ring type, or the top-thin bottom-thickness type. The heat transfer effect of the present invention is obviously better than that of the existing finned tube heat exchanger, thereby reducing the volume of the heat exchanger and saving materials. According to preliminary calculations, both the volume of the heat exchanger and the materials used can be reduced by 20%-40%; and Compared with the finned tube heat exchanger commonly used at present, the cost increase is not much.

Figure 200810033289

Description

内衬泡沫金属的翅片管式换热器 Finned tube heat exchanger lined with metal foam

技术领域technical field

本发明涉及一种制冷技术领域的换热器,具体涉及一种内衬泡沫金属的翅片管式换热器。The invention relates to a heat exchanger in the technical field of refrigeration, in particular to a finned tube heat exchanger lined with foam metal.

背景技术Background technique

翅片管式换热器是一种在制冷、空调、化工等工业领域广泛采用的换热器形式。翅片管式换热器由金属翅片和金属管组成,多片形状相同的金属翅片平行分布,多根金属管穿过所有金属片,管内流体在各自管内流动,管与管间不相互掺混,管外的流体(一般为气体)则在管与金属片所构成的空间中流动。以在房间空调器中的应用为例,翅片管式换热器已广泛用作蒸发器和冷凝器。当用作蒸发器时,制冷剂在管内蒸发变成气体,空气在管外翅片间流动的方式,将热量传递给制冷剂,从而降低空气温度。当用作冷凝器时,制冷剂在管内冷凝成液体,管外翅片间流过的空气将制冷剂冷凝时放出的热量带走。随着人们对节能降耗要求的不断提高,对换热器的高效节能和小型化的要求也越来越高,传统的翅片管式换热器结构存在效率偏低、功率密度偏小、结构不够紧凑的问题,越来越难满足市场的需求,因此急需寻找一种更有效的管内强化传热方式,以提高翅片管式换热器的整体效率。Finned tube heat exchanger is a form of heat exchanger widely used in refrigeration, air conditioning, chemical and other industrial fields. The finned tube heat exchanger is composed of metal fins and metal tubes. Multiple metal fins with the same shape are distributed in parallel. Multiple metal tubes pass through all the metal sheets. The fluid in the tubes flows in their respective tubes, and the tubes do not interact with each other. Blending, the fluid (usually gas) outside the tube flows in the space formed by the tube and the metal sheet. Taking the application in room air conditioners as an example, finned tube heat exchangers have been widely used as evaporators and condensers. When used as an evaporator, the refrigerant evaporates into gas in the tube, and the way the air flows between the fins outside the tube transfers heat to the refrigerant, thereby reducing the air temperature. When used as a condenser, the refrigerant condenses into a liquid in the tube, and the air flowing between the fins outside the tube takes away the heat released by the refrigerant when it condenses. With the continuous improvement of people's requirements for energy saving and consumption reduction, the requirements for high efficiency, energy saving and miniaturization of heat exchangers are also getting higher and higher. The traditional finned tube heat exchanger structure has low efficiency, small power density, The problem of insufficient compact structure is becoming more and more difficult to meet the needs of the market. Therefore, it is urgent to find a more effective way to enhance heat transfer in the tube to improve the overall efficiency of the finned tube heat exchanger.

针对翅片管式换热器管内换热面积无法大幅度增加的问题,泡沫金属作为一种比表面积(单位体积内的表面积)很大(可达2000-10000m2/m3)的多孔材料,它的应用可提供一种新的解决方案。泡沫金属是由刚性骨架和内部孔洞组成的,具有优异的物理特性和良好的机械性能的新型材料。泡沫金属的显著特征是其内部有大量的孔隙,根据各个孔隙之间联通还是封闭有开孔结构和闭孔结构之分。大量的内部孔隙使得泡沫金属材料具有诸多优异特性,如比重小、比表面积大、能量吸收性能好、换热散热能力高(开孔结构)、吸声性好(开孔结构)、渗透性优(开孔结构)、电磁波吸收性好(开孔结构)、阻热、耐热耐火、抗热震、能再生、加工性好等等。泡沫金属具有很大的比表面积,以PMF方法制作的开孔型泡沫金属为例,其比表面积最大可达45cm2/cm3。可见,翅片管式换热器中金属管内衬泡沫金属可以有效增大管内换热面积,强化管内传热。而且由于泡沫金属结构复杂,在强迫对流条件下使用有利于利用三维复杂流动,克服边界层的不利影响。此外,对于流体沸腾相变换热过程,管内填充泡沫金属还可增加发泡点,引起流体内部沸腾换热。In view of the problem that the heat exchange area in the tube of the finned tube heat exchanger cannot be greatly increased, metal foam is a porous material with a large specific surface area (surface area per unit volume) (up to 2000-10000m 2 /m 3 ), Its application can provide a new solution. Metal foam is composed of rigid skeleton and internal holes, and it is a new type of material with excellent physical properties and good mechanical properties. The salient feature of metal foam is that it has a large number of pores inside. According to whether the pores are connected or closed, there are open-pore structure and closed-pore structure. A large number of internal pores make the metal foam material have many excellent characteristics, such as small specific gravity, large specific surface area, good energy absorption performance, high heat exchange and heat dissipation capacity (open cell structure), good sound absorption (open cell structure), and excellent permeability. (open cell structure), good electromagnetic wave absorption (open cell structure), heat resistance, heat and fire resistance, thermal shock resistance, regeneration, good processability, etc. Metal foam has a large specific surface area. Taking the open-cell metal foam produced by the PMF method as an example, the specific surface area can reach up to 45cm 2 /cm 3 . It can be seen that the metal tube lined with metal foam in the finned tube heat exchanger can effectively increase the heat transfer area in the tube and enhance the heat transfer in the tube. Moreover, due to the complex structure of the metal foam, it is beneficial to use the three-dimensional complex flow under the condition of forced convection to overcome the adverse effects of the boundary layer. In addition, for the fluid boiling phase transfer heat process, filling the tube with metal foam can also increase the bubble point, causing the internal boiling heat exchange of the fluid.

经对现有技术的文献检索发现,目前用泡沫金属材料实现换热器强化换热已有相关专利,但皆与本专利申请的内容有区别。之前的专利利用泡沫金属强化管外传热,或者是在其他形式换热器内填充泡沫金属以达到强化换热的目的,如申请号为200610105100.6、名称为“一种管式换热器”的专利,便是利用泡沫金属代替传统铝箔来强换管外传热,而申请号为200610104597.X、名称为“一种套管式金属泡沫换热器”的专利,则是针对套管式换热器形式,通过外管内和内管内都填充泡沫金属来实现内管内流体与两管间流体强化换热的目的。但管内换热面积无法大幅度增加而使得管内强化换热遇到瓶颈。According to the literature search of the prior art, it is found that there are related patents on the use of foamed metal materials to realize the enhanced heat transfer of heat exchangers, but they are different from the content of this patent application. The previous patents used metal foam to enhance heat transfer outside the tube, or filled metal foam in other forms of heat exchangers to achieve the purpose of enhancing heat exchange, such as the application number 200610105100.6, named "a tube heat exchanger" The patent is to use foam metal instead of traditional aluminum foil to forcefully replace the heat transfer outside the tube, and the patent with the application number 200610104597. In the form of a heater, both the outer tube and the inner tube are filled with metal foam to achieve the purpose of enhancing heat exchange between the fluid in the inner tube and the fluid between the two tubes. However, the heat exchange area in the tube cannot be greatly increased, so that the enhanced heat exchange in the tube encounters a bottleneck.

发明内容Contents of the invention

本发明针对现有技术的上述不足,提供一种内衬泡沫金属的翅片管式换热器,使其通过管内布置泡沫金属的方式,以提高管内换热系数,从而提高翅片管换热器管内外流体的换热效率,达到缩小翅片管换热器体积,节约材料的目的。The present invention aims at the above-mentioned deficiencies in the prior art, and provides a finned tube heat exchanger lined with metal foam, which can improve the heat transfer coefficient in the tube by arranging metal foam in the tube, thereby improving the heat transfer rate of the finned tube. The heat exchange efficiency of the fluid inside and outside the tube can be improved to achieve the purpose of reducing the volume of the finned tube heat exchanger and saving materials.

本发明是通过以下技术方案来实现的,本发明包括:金属翅片、金属管、泡沫金属,金属翅片位于金属管外部,泡沫金属填充在金属管内,泡沫金属的内部有供气体或液体介质流通的孔洞。The present invention is achieved through the following technical solutions, the present invention includes: metal fins, metal tubes, metal foam, the metal fins are located outside the metal tube, the metal foam is filled in the metal tube, and the inside of the metal foam has gas or liquid medium holes for circulation.

所述金属翅片可以由铝、铜或其他金属制成,每片翅片形状相同,长10-200cm,宽2-20cm,可以为平翅片、波纹形翅片、条缝形翅片、百叶窗形翅片或其他翅片类型以强化翅片表面的换热。The metal fins can be made of aluminum, copper or other metals, each fin has the same shape, 10-200cm long and 2-20cm wide, and can be flat fins, corrugated fins, slotted fins, Louvered fins or other fin types to enhance heat transfer across the fin surface.

所述金属管可以是铝、铜或其他金属材料的光管,管的内径范围2.5-30mm,管壁厚0.2-5mm,多根规格相同的金属管等距平行分布,每根管一段由金属弯管和它相邻一根管联通,另一端由金属弯管和它相邻的另一根管联通,由此所有管联通成一条通路,需要换热的流体流过其中。The metal tube can be a bare tube of aluminum, copper or other metal materials, the inner diameter of the tube is 2.5-30mm, the wall thickness of the tube is 0.2-5mm, and a plurality of metal tubes of the same specification are equidistantly distributed in parallel, and each tube section is made of metal The elbow is in communication with its adjacent pipe, and the other end is connected with the other adjacent pipe by the metal elbow, so that all the pipes are connected into a passage through which the fluid to be exchanged for heat flows.

所述的泡沫金属通过液态金属注入气体发泡剂、电镀或熔模浇注、固体粉末烧结或注射成型方法制成,泡沫金属为铜、铝、不锈钢或其他金属,孔径为0.05mm-5mm。泡沫金属在管内有三种内衬形式:The foam metal is made by injecting gas foaming agent into liquid metal, electroplating or investment casting, solid powder sintering or injection molding. The foam metal is copper, aluminum, stainless steel or other metals, and the hole diameter is 0.05mm-5mm. Metal foam has three lining forms in the pipe:

(1)全截面式:泡沫金属充满整根金属管。此种形式可以得到最大的换热面积和最复杂的空间结构,预期可以得到最好的换热效果,但其压降可能最大。(1) Full-section type: metal foam fills the entire metal tube. This form can get the largest heat transfer area and the most complex space structure, and it is expected to get the best heat transfer effect, but its pressure drop may be the largest.

(2)内环式:金属管内壁与厚度均匀的泡沫金属相连,金属管中心为空,泡沫金属的厚度为金属管内直径的1%-45%。考虑到全截面式可能使得流体流动阻力系数偏大,设计此种形式兼顾强化换热的效果和流阻大小。(2) Inner ring type: the inner wall of the metal tube is connected with metal foam with uniform thickness, the center of the metal tube is empty, and the thickness of the metal foam is 1%-45% of the inner diameter of the metal tube. Considering that the full-section type may make the fluid flow resistance coefficient too large, this type of design takes into account the effect of enhancing heat transfer and the size of the flow resistance.

(3)上薄下厚式:金属管底部相比顶部分布更多的泡沫金属,金属管底部泡沫金属的厚度为金属管内直径的1%-45%,顶部泡沫金属的厚度为金属管内直径0%-45%。考虑管内相变换热的实际过程,以蒸发过程为例,制冷剂在进入蒸发器的初始阶段干度较低,制冷剂液体由于重力作用会分布在靠近金属管底部的位置,所以金属管底部更需要强化换热措施。(3) Thin top and thick bottom: more metal foam is distributed at the bottom of the metal tube than at the top, the thickness of the metal foam at the bottom of the metal tube is 1%-45% of the inner diameter of the metal tube, and the thickness of the metal foam at the top is 0% of the inner diameter of the metal tube %-45%. Considering the actual process of phase transformation heat in the tube, taking the evaporation process as an example, the refrigerant has a low dryness at the initial stage of entering the evaporator, and the refrigerant liquid will be distributed near the bottom of the metal tube due to gravity, so the bottom of the metal tube It is more necessary to strengthen the heat exchange measures.

在一个翅片管式换热器中,以上三种形式可以只应用一种,例如所有金属管内都内衬内环式泡沫金属,也可以应用其中的两种或三种,例如在换热器靠近换热流体入口的几根金属管内采用上薄下厚式内衬方式,更有利于低干度流体更快蒸发,而在其后的金属管内采用内环式内衬方式。In a finned tube heat exchanger, only one of the above three forms can be used, for example, all metal tubes are lined with inner ring metal foam, or two or three of them can be used, for example, in the heat exchanger Several metal tubes close to the heat exchange fluid inlet are lined with a thin top and a thick bottom, which is more conducive to faster evaporation of low-dryness fluids, and the inner ring lining is used in the subsequent metal tubes.

上述翅片管式换热器,金属翅片、金属管和泡沫金属的材料可以为相同的,也可以为两两相同或互不相同。In the above-mentioned fin-tube heat exchanger, the materials of the metal fins, metal tubes and metal foam can be the same, or can be the same or different from each other.

本发明具有显著的优点和积极的效果。传热效果可以明显优于现有的翅片管式换热器,从而减小换热器体积,节约材料,经初步计算换热器体积和用料均可减少20%-40%;并且与目前普遍使用的翅片管换热器相比成本增加不多。The present invention has significant advantages and positive effects. The heat transfer effect can be significantly better than the existing finned tube heat exchanger, thereby reducing the volume of the heat exchanger and saving materials. According to preliminary calculations, the volume and materials of the heat exchanger can be reduced by 20%-40%; and with Compared with the commonly used finned tube heat exchanger at present, the cost increase is not much.

附图说明Description of drawings

图1为泡沫金属在管内的三种分布方式,其中:图1a为全截面式,图1b为内环式,图1c为上薄下厚式。Figure 1 shows three distribution modes of metal foam in the pipe, among which: Figure 1a is the full-section type, Figure 1b is the inner ring type, and Figure 1c is the top-thin bottom-thick type.

图2为翅片管式换热器的结构示意图,其中:图2a为换热器正面视图,图2b为换热器侧面视图。Fig. 2 is a schematic structural view of a fin-tube heat exchanger, wherein: Fig. 2a is a front view of the heat exchanger, and Fig. 2b is a side view of the heat exchanger.

图中,1为金属管,2为金属管内泡沫金属,3为金属翅片,4为金属弯管。In the figure, 1 is a metal pipe, 2 is metal foam in the metal pipe, 3 is a metal fin, and 4 is a metal elbow.

具体实施方式Detailed ways

下面结合附图对本发明的实施例作详细说明:本实施例在以本发明技术方案为前提下进行实施,给出了详细的实施方式和具体的操作过程,但本发明的保护范围不限于下述的实施例。The embodiments of the present invention are described in detail below in conjunction with the accompanying drawings: this embodiment is implemented on the premise of the technical solution of the present invention, and detailed implementation methods and specific operating procedures are provided, but the protection scope of the present invention is not limited to the following the described embodiment.

传统的翅片管式换热器由金属翅片3和金属管1组成,其中金属管1可采用光管,亦可采用强化管,如螺纹槽管、横纹槽管、波纹管等,目的都是强化管内换热效果。The traditional finned tube heat exchanger consists of metal fins 3 and metal tubes 1, in which the metal tube 1 can be a plain tube or a strengthened tube, such as a threaded grooved tube, a horizontal grooved tube, a corrugated tube, etc. They all enhance the heat transfer effect in the tube.

如图1-2所示,本发明翅片管式换热器,包括管外金属翅片3、金属管1和金属管1内的泡沫金属2,管内泡沫金属2以增大管内换热面积,增强扰流,泡沫金属2内部有供气体或液体介质流通的通孔。As shown in Figure 1-2, the finned tube heat exchanger of the present invention includes metal fins 3 outside the tube, metal tube 1 and metal foam 2 inside the metal tube 1, and metal foam 2 inside the tube to increase the heat exchange area inside the tube , to enhance the turbulence, the metal foam 2 has a through hole for the gas or liquid medium to circulate.

由于泡沫金属2独特的结构和性能,使得换热器管内的换热效率大大提高,从而使换热器管内外流体间的换热效率大大提高。Due to the unique structure and performance of the metal foam 2, the heat exchange efficiency in the heat exchanger tube is greatly improved, so that the heat exchange efficiency between the fluid inside and outside the heat exchanger tube is greatly improved.

上述管内泡沫金属2,可以使三种内衬形式中的任意一种,以达到适应不同换热需求的目的。泡沫金属2的孔洞直径为0.05mm-5mm。泡沫金属2通过金属粉末烧结、电镀或熔模烧注(渗流)等方法覆盖在管内表面。The above-mentioned metal foam 2 in the tube can be any one of three lining forms, so as to meet different heat exchange requirements. The hole diameter of the metal foam 2 is 0.05mm-5mm. The metal foam 2 is covered on the inner surface of the tube by methods such as metal powder sintering, electroplating or investment casting (seepage).

以采用全截面的泡沫金属2内衬形式为例,介绍制作如图2所示翅片管式换热器的具体实施方式:Taking the full-section foam metal 2 lining form as an example, the specific implementation method of making the finned tube heat exchanger shown in Figure 2 is introduced:

切割好长度与金属管1长相同,直径比金属管1内径稍大的圆柱形泡沫金属2(轴向截面如图1a所示)。固定金属管1,将圆柱形泡沫金属2沿管的轴向方向推入金属管1,同时可以使用金属丝与柱状泡沫金属2的进入金属管1的一端连接,通过拉拽金属丝来帮助克服泡沫金属2与管壁之间的摩擦阻力,直至泡沫金属2完全内置于金属管1。由于柱状泡沫金属2的直径要稍大于金属管1内径,故泡沫金属2的边缘将受到挤压变形,从而更紧密的和金属管1内壁相结合,当然也可以采用其他方法将泡沫金属2填充于金属管1内,只要两者紧密结合,达到增加换热效果的目的即可。Cut the cylindrical metal foam 2 whose length is the same as that of the metal pipe 1 and whose diameter is slightly larger than the inner diameter of the metal pipe 1 (the axial section is shown in Figure 1a). Fix the metal tube 1, push the cylindrical metal foam 2 into the metal tube 1 along the axial direction of the tube, and at the same time use a wire to connect with the end of the columnar metal foam 2 entering the metal tube 1, and help overcome the problem by pulling the metal wire. The frictional resistance between the metal foam 2 and the pipe wall until the metal foam 2 is completely embedded in the metal pipe 1. Since the diameter of the columnar metal foam 2 is slightly larger than the inner diameter of the metal tube 1, the edge of the metal foam 2 will be squeezed and deformed, so as to be more tightly combined with the inner wall of the metal tube 1. Of course, other methods can also be used to fill the metal foam 2 In the metal tube 1, as long as the two are closely combined to achieve the purpose of increasing the heat exchange effect.

在每片金属翅片3上钻圆形孔,孔径比金属管1外径略小,孔数目与金属管1数目相同,每片金属翅片3上孔洞的位置相同(金属翅片3钻孔位置如图2b所示)。所有金属翅片3平行放置,每根内衬泡沫金属2的金属管1穿过每片翅片相同位置的孔。由于金属翅片3上的孔径比金属管1外径略小,当金属管1穿过金属翅片3时,金属翅片3的圆孔周围会产生挤压变形,从而和金属管1外壁紧密接触。Drill circular holes on each metal fin 3, the aperture is slightly smaller than the outer diameter of the metal tube 1, the number of holes is the same as the number of the metal tube 1, and the positions of the holes on each metal fin 3 are the same (the metal fins 3 are drilled The location is shown in Figure 2b). All the metal fins 3 are placed in parallel, and each metal tube 1 lined with metal foam 2 passes through the hole at the same position of each fin. Since the aperture on the metal fin 3 is slightly smaller than the outer diameter of the metal tube 1, when the metal tube 1 passes through the metal fin 3, extrusion deformation will occur around the round hole of the metal fin 3, so that it is tightly connected to the outer wall of the metal tube 1. touch.

金属管1之间通过金属弯管4连接,管与管之间的连接方式如图2所示,没有连接金属弯管4的最上方的两根金属管1作为换热器内需要换热流体的进口和出口(如图2a所示)。The metal pipes 1 are connected by metal elbows 4. The connection between the pipes is shown in Figure 2. The two uppermost metal pipes 1 that are not connected to the metal elbows 4 are used as the heat exchange fluid in the heat exchanger. The import and export of (as shown in Figure 2a).

泡沫金属2主要由液态金属注入气体或发泡剂法、熔模浇注法、固体粉末烧结法及注射成型等方法生成。泡沫金属2的内部有供气体或液体介质流通的孔洞,孔洞的直径为几十微米到几毫米不等,。Metal foam 2 is mainly produced by liquid metal injection gas or foaming agent method, investment casting method, solid powder sintering method and injection molding. There are holes in the metal foam 2 for the circulation of gas or liquid medium, and the diameter of the holes ranges from tens of microns to several millimeters.

泡沫金属2的材料可以采用与常用的换热管相同的材料,亦可采用与换热管不同种类的金属,如铝、铜或其他金属材料。采用泡沫金属2的显著优点是,其具有传热效率高,比表面积大及密度低、重量轻、结构紧凑、优良的降噪功能等特点,且任意金属材料均可加工制成,所以在设计高效紧凑的翅片管式换热器方面显示出极大的应用价值。The material of the foamed metal 2 can be the same material as the commonly used heat exchange tube, or a metal different from the heat exchange tube, such as aluminum, copper or other metal materials. The remarkable advantages of using metal foam 2 are that it has the characteristics of high heat transfer efficiency, large specific surface area, low density, light weight, compact structure, and excellent noise reduction function, and any metal material can be processed, so in the design High-efficiency and compact fin-tube heat exchangers have shown great application value.

对于泡沫金属2内环式内衬方式的金属管1的制备,下面给出一种具体实施方法:For the preparation of the metal pipe 1 of the metal foam 2 inner ring type lining mode, a kind of specific implementation method is provided below:

切割一片用于内衬在金属管1内的泡沫金属2,其长度等于金属管1长度,宽度等于金属管1内壁周长,厚度等于设计需要内衬泡沫金属2的厚度。将泡沫金属2片以长度方向为轴向卷曲成圆筒形状,将泡沫金属2内置于金属管1内,具体方法可参考全截面式的放置方法。当然,也可以采用其他方法制备泡沫金属2内环或者上薄下厚的内衬方式的金属管1,只要泡沫金属2在金属管1内能够形成设计所需的分布形式,并且泡沫金属2与金属管1内壁能够紧密衔接即可。Cut a piece of metal foam 2 for lining in the metal pipe 1, its length is equal to the length of the metal pipe 1, its width is equal to the circumference of the inner wall of the metal pipe 1, and its thickness is equal to the thickness of the metal foam 2 that needs to be lined in the design. The metal foam 2 pieces are curled into a cylindrical shape with the length direction as the axial direction, and the metal foam 2 is built into the metal tube 1. For the specific method, please refer to the full-section placement method. Of course, other methods can also be used to prepare the metal pipe 1 of the inner ring of the metal foam 2 or the inner lining mode with a thin top and a thick bottom, as long as the metal foam 2 can form the distribution form required by the design in the metal pipe 1, and the metal foam 2 and the It is sufficient that the inner walls of the metal pipe 1 can be closely connected.

Claims (10)

1.一种内衬泡沫金属的翅片管式换热器,包括金属翅片、金属管、泡沫金属,金属翅片位于金属管外部,其特征在于,所述的金属管内填充泡沫金属,泡沫金属内部有供气体或液体介质流通的孔洞。1. A finned tube heat exchanger lined with metal foam, comprising metal fins, metal tubes, metal foam, metal fins located outside the metal tube, characterized in that the metal tube is filled with metal foam, the foam metal There are holes in the metal for the flow of gas or liquid medium. 2.根据权利要求1所述的内衬泡沫金属的翅片管式换热器,其特征是,所述的泡沫金属在金属管内有内衬形式为全截面式、内环式或上薄下厚式中的一种或两种或三种。2. The finned tube heat exchanger lined with metal foam according to claim 1, characterized in that, the metal foam is lined in the metal tube in the form of a full-section type, an inner ring type or an upper thinner lower One or two or three in thick style. 3.根据权利要求2所述的内衬泡沫金属的翅片管式换热器,其特征是,所述的全截面式内衬形式,是指泡沫金属充满整根金属管。3. The finned tube heat exchanger lined with metal foam according to claim 2, wherein the full-section lining means that the metal foam fills the entire metal tube. 4.根据权利要求2所述的内衬泡沫金属的翅片管式换热器,其特征是,所述的内环式内衬形式,是指金属管内壁与厚度均匀的泡沫金属相连,金属管中心为空。4. The finned tube heat exchanger lined with metal foam according to claim 2, characterized in that, the inner ring type lining means that the inner wall of the metal tube is connected with the metal foam with uniform thickness, and the metal The center of the tube is empty. 5.根据权利要求2或4所述的内衬泡沫金属的翅片管式换热器,其特征是,所述的内环式内衬形式中,泡沫金属的厚度为金属管内直径的1%-45%。5. The finned tube heat exchanger lined with metal foam according to claim 2 or 4, characterized in that, in the form of the inner ring lining, the thickness of the metal foam is 1% of the inner diameter of the metal tube -45%. 6.根据权利要求2所述的内衬泡沫金属的翅片管式换热器,其特征是,所述的上薄下厚式内衬形式,是指金属管底部相比顶部分布更多的泡沫金属。6. The finned tube heat exchanger lined with metal foam according to claim 2, characterized in that, the upper thinner and lower thick lining means that the bottom of the metal tube is more distributed than the top metal foam. 7.根据权利要求2或6所述的内衬泡沫金属的翅片管式换热器,其特征是,所述的上薄下厚式内衬形式中,金属管底部泡沫金属的厚度为金属管内直径的1%-45%,顶部泡沫金属的厚度为金属管内直径0%-45%。7. The finned tube heat exchanger lined with metal foam according to claim 2 or 6, characterized in that, in the form of the upper thinner and lower thick inner lining, the thickness of the metal foam at the bottom of the metal tube is 1%-45% of the inner diameter of the tube, and the thickness of the metal foam at the top is 0%-45% of the inner diameter of the metal tube. 8.根据权利要求1或2或3或4或6所述的内衬泡沫金属的翅片管式换热器,其特征是,所述的泡沫金属,其孔径为0.05mm-5mm。8. The finned tube heat exchanger lined with metal foam according to claim 1 or 2 or 3 or 4 or 6, characterized in that the metal foam has a pore diameter of 0.05mm-5mm. 9.根据权利要求1所述的内衬泡沫金属的翅片管式换热器,其特征是,所述金属翅片,其每片翅片形状相同,长为10cm-200cm,宽为2cm-20cm。9. The finned tube heat exchanger lined with metal foam according to claim 1, characterized in that, the metal fins have the same shape of each fin, with a length of 10cm-200cm and a width of 2cm-200cm. 20cm. 10.根据权利要求1或2或3或4或6所述的内衬泡沫金属的翅片管式换热器,其特征是,所述金属管,其管的内径范围为2.5mm-30mm,管壁厚为0.2mm-5mm,多根规格相同的金属管等距平行分布,每根管一段由金属弯管和它相邻一根管联通,另一端由金属弯管和它相邻的另一根管联通,由此所有管联通成一条通路,需要换热的流体流过其中。10. The metal foam-lined finned tube heat exchanger according to claim 1 or 2 or 3 or 4 or 6, characterized in that the metal tube has an inner diameter ranging from 2.5 mm to 30 mm, The wall thickness of the tube is 0.2mm-5mm, and a plurality of metal tubes of the same specification are equidistantly distributed in parallel. One section of each tube is connected by a metal elbow and its adjacent tube, and the other end is connected by a metal elbow and its adjacent one. One tube is connected, so all the tubes are connected to form a passage through which the fluid requiring heat exchange flows.
CNA2008100332891A 2008-01-31 2008-01-31 Finned tube heat exchanger lined with metal foam Pending CN101226021A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNA2008100332891A CN101226021A (en) 2008-01-31 2008-01-31 Finned tube heat exchanger lined with metal foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNA2008100332891A CN101226021A (en) 2008-01-31 2008-01-31 Finned tube heat exchanger lined with metal foam

Publications (1)

Publication Number Publication Date
CN101226021A true CN101226021A (en) 2008-07-23

Family

ID=39858145

Family Applications (1)

Application Number Title Priority Date Filing Date
CNA2008100332891A Pending CN101226021A (en) 2008-01-31 2008-01-31 Finned tube heat exchanger lined with metal foam

Country Status (1)

Country Link
CN (1) CN101226021A (en)

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101408389B (en) * 2008-11-26 2010-12-22 北京航空航天大学 Combined type foamed metal core material and phase-change thermal storage apparatus using the same
CN102425964A (en) * 2011-11-07 2012-04-25 太原理工大学 Plate-type heat exchanger
CN102661524A (en) * 2012-05-02 2012-09-12 浙江全加好科技有限公司 High-power LED (light-emitting diode) line lamp provided with metal heat abstractor
CN103191940A (en) * 2013-04-02 2013-07-10 中南大学 Preparation method of heat exchanging metal composite pipe
WO2014055045A1 (en) 2012-10-03 2014-04-10 Technická Univerzita V Košiciach Flow profile with debossed boundaries
CN103727825A (en) * 2013-09-11 2014-04-16 太仓派欧技术咨询服务有限公司 Refractory metal heat-exchange tube
CN103722790A (en) * 2013-09-11 2014-04-16 太仓派欧技术咨询服务有限公司 Preparation method of Re (rhenium) foam
CN103727833A (en) * 2013-09-11 2014-04-16 太仓派欧技术咨询服务有限公司 Ceramic-based composite material heat exchange tube
US8708034B2 (en) 2008-11-10 2014-04-29 Mitsubishi Electric Corporation Air conditioner
CN104236366A (en) * 2013-06-19 2014-12-24 三星电子株式会社 Heat exchanger and manufacturing method thereof
CN104949563A (en) * 2015-06-19 2015-09-30 中国石油大学(华东) Density-gradient metal foam heat exchange tube
CN106090866A (en) * 2016-06-13 2016-11-09 东南大学 A kind of being applicable to becomes the steam generator under gravity environment
CN109029035A (en) * 2018-05-17 2018-12-18 上海电力学院 Using the shell-and-tube exchanger of foam copper product
CN109780893A (en) * 2017-11-10 2019-05-21 王晋声 A metal fin heat exchange unit and a heat exchanger using the same
CN110500830A (en) * 2019-04-29 2019-11-26 何家密 Method of Reducing Power Consumption for Refrigerant Evaporation and Condensation Cooling and Heating
CN110705043A (en) * 2019-09-12 2020-01-17 广东志高暖通设备股份有限公司 Optimization design method of noise reduction type heat exchanger
WO2021047463A1 (en) * 2019-09-12 2021-03-18 青岛海尔电冰箱有限公司 Evaporator assembly for ice-making apparatus
CN113473762A (en) * 2020-03-30 2021-10-01 华为技术有限公司 Equipment shell, equipment and laser radar

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8708034B2 (en) 2008-11-10 2014-04-29 Mitsubishi Electric Corporation Air conditioner
CN101408389B (en) * 2008-11-26 2010-12-22 北京航空航天大学 Combined type foamed metal core material and phase-change thermal storage apparatus using the same
CN102425964A (en) * 2011-11-07 2012-04-25 太原理工大学 Plate-type heat exchanger
CN102661524A (en) * 2012-05-02 2012-09-12 浙江全加好科技有限公司 High-power LED (light-emitting diode) line lamp provided with metal heat abstractor
WO2014055045A1 (en) 2012-10-03 2014-04-10 Technická Univerzita V Košiciach Flow profile with debossed boundaries
CN103191940A (en) * 2013-04-02 2013-07-10 中南大学 Preparation method of heat exchanging metal composite pipe
CN104236366B (en) * 2013-06-19 2018-03-30 三星电子株式会社 The manufacture method of heat exchanger
CN104236366A (en) * 2013-06-19 2014-12-24 三星电子株式会社 Heat exchanger and manufacturing method thereof
CN103722790B (en) * 2013-09-11 2016-05-04 太仓派欧技术咨询服务有限公司 A kind of preparation method of rhenium foam
CN103727833A (en) * 2013-09-11 2014-04-16 太仓派欧技术咨询服务有限公司 Ceramic-based composite material heat exchange tube
CN103727833B (en) * 2013-09-11 2016-05-04 太仓派欧技术咨询服务有限公司 A kind of ceramic matric composite heat-exchange tube
CN103722790A (en) * 2013-09-11 2014-04-16 太仓派欧技术咨询服务有限公司 Preparation method of Re (rhenium) foam
CN103727825B (en) * 2013-09-11 2017-01-11 太仓派欧技术咨询服务有限公司 Refractory metal heat-exchange tube
CN103727825A (en) * 2013-09-11 2014-04-16 太仓派欧技术咨询服务有限公司 Refractory metal heat-exchange tube
CN104949563A (en) * 2015-06-19 2015-09-30 中国石油大学(华东) Density-gradient metal foam heat exchange tube
CN106090866A (en) * 2016-06-13 2016-11-09 东南大学 A kind of being applicable to becomes the steam generator under gravity environment
CN109780893A (en) * 2017-11-10 2019-05-21 王晋声 A metal fin heat exchange unit and a heat exchanger using the same
CN109029035A (en) * 2018-05-17 2018-12-18 上海电力学院 Using the shell-and-tube exchanger of foam copper product
CN110500830A (en) * 2019-04-29 2019-11-26 何家密 Method of Reducing Power Consumption for Refrigerant Evaporation and Condensation Cooling and Heating
CN110705043A (en) * 2019-09-12 2020-01-17 广东志高暖通设备股份有限公司 Optimization design method of noise reduction type heat exchanger
WO2021047463A1 (en) * 2019-09-12 2021-03-18 青岛海尔电冰箱有限公司 Evaporator assembly for ice-making apparatus
CN114364935A (en) * 2019-09-12 2022-04-15 青岛海尔电冰箱有限公司 Evaporator assembly for ice making apparatus
EP4030126A4 (en) * 2019-09-12 2022-10-19 Qingdao Haier Refrigerator Co., Ltd EVAPORATOR ASSEMBLY FOR ICE MAKER
CN110705043B (en) * 2019-09-12 2024-04-02 广东开利暖通空调股份有限公司 Optimal design method of noise reduction type heat exchanger
CN113473762A (en) * 2020-03-30 2021-10-01 华为技术有限公司 Equipment shell, equipment and laser radar
CN113473762B (en) * 2020-03-30 2022-12-13 华为技术有限公司 Equipment shell, equipment and laser radar

Similar Documents

Publication Publication Date Title
CN101226021A (en) Finned tube heat exchanger lined with metal foam
CN100516756C (en) A casing metal foam heat exchanger
CN201392115Y (en) A sleeve-type high-efficiency foam metal heat exchanger
CN201034436Y (en) Double enhanced heat transfer tube for evaporation
CN101818999B (en) Pulsating heat pipe heat-transfer device for low grade heat energy utilization
CN104266519B (en) There is the open-pore metal foam heat pipe of hole density gradual change
CN103994682A (en) Heat pipe and manufacturing method thereof
CN103060592A (en) Through-hole metal foam with gradually varied morphologic characteristics, preparation method of through-hole metal foam, and heat exchange device
CN104903673A (en) Evaporation heat transfer tube
CN104870926B (en) Evaporation heat transfer pipe with hollow cavity
CN105276865A (en) Coaxial threaded tube inner-inserted-core heat exchanger
CN203908113U (en) Microchannel heat exchanger and heat exchanging device
CN104296584A (en) Spiral band passive enhancement heat exchanging pipe
CN106839795A (en) A kind of efficient foam metal steam condenser processed through hydrophobicity
CN101118130A (en) A casing heat exchanger
CN202254521U (en) A Microchannel Condenser for Heat Pump Water Heater
CN206410585U (en) A kind of novel heat exchange pipe
CN101929821A (en) A through-hole metal foam porous threaded pipe
CN204665982U (en) A kind of water-cooled shell oil cooler
CN103994674A (en) Unequal-interval pipe and fin type heat exchanger
CN102878850A (en) Foam metal fins and porous flat tube micro-channel heat exchanger with foam metal fins
CN203349682U (en) High-performance composite-structure superconducting flat heat pipe
CN204705254U (en) A kind of heat exchanger tube of external metal foam
CN202734639U (en) Foamed metal fin and porous flat tube micro-channel heat exchanger provided with same
CN104964486A (en) Heat exchanger suitable for fluid phase change on outer side

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C12 Rejection of a patent application after its publication
RJ01 Rejection of invention patent application after publication

Open date: 20080723