CN205717833U - Annular heat pipe array heat exchanger and comprise its heat-exchange system - Google Patents
Annular heat pipe array heat exchanger and comprise its heat-exchange system Download PDFInfo
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Abstract
Description
技术领域 technical field
本实用新型涉及热交换领域,进一步涉及一种环形热管阵列换热器,以及包含该换热器的换热系统。 The utility model relates to the field of heat exchange, and further relates to an annular heat pipe array heat exchanger and a heat exchange system including the heat exchanger.
背景技术 Background technique
数据中心或者通信机柜的用能量大而集中(单位面积的用能量远高于办公建筑的用量),24小时不间断运行,年运行小时数远高于其他商业建筑。随着全球变暖和能源的短缺,能源的高效利用问题日益凸显,如何降低功率利用效率(功率利用效率=设施总功率/IT设备功率),已成为数据中心运行管理人员追求的目标。 The energy consumption of data centers or communication cabinets is large and concentrated (the energy consumption per unit area is much higher than that of office buildings), 24 hours of uninterrupted operation, and the annual operating hours are much higher than other commercial buildings. With global warming and energy shortages, the problem of efficient energy utilization has become increasingly prominent. How to reduce power utilization efficiency (power utilization efficiency = total facility power/IT equipment power) has become the goal pursued by data center operation managers.
根据设备的运行要求,数据中心或者通信机柜需要在一个环境可控的空间内确保系统的可靠运行,其中,最主要的就是运行的温度环境在20-25℃范围内,并保持内部环境的清洁。目前最通用的做法就是采用空调或者热电致冷装置。 According to the operation requirements of the equipment, the data center or the communication cabinet needs to ensure the reliable operation of the system in an environment-controlled space, among which, the most important thing is to operate the temperature environment within the range of 20-25 ℃, and keep the internal environment clean . At present, the most common way is to use air conditioning or thermoelectric cooling device.
对于数据中心而言,一般采用大功率空调并安装温度自动控制装置来调节数据中心的温度,随着主机系统的散热量越来越高,空调的功率越来越大,同时为了避免主机超温故障,机房内一般采用下送风、上回风的送风方式。在每个机柜前部有开孔地板,用于送冷风。此外,机房的空调还必须保证机房内具有良好的空气流动,不存在局部热点和风短路现象,机房的不同地点温差较小。 For data centers, high-power air conditioners are generally used and automatic temperature control devices are installed to adjust the temperature of the data center. As the heat dissipation of the host system increases, the power of the air conditioner increases. If there is a fault, the air supply mode of downward air supply and upward return air is generally adopted in the computer room. There is a perforated floor at the front of each cabinet for cooling air. In addition, the air conditioner in the computer room must also ensure that the computer room has good air flow, there are no local hot spots and wind short circuits, and the temperature difference between different locations in the computer room is small.
对于通信机柜而言,除了采用空调进行冷却外,由于热电致冷(TEC)本身没有运动部件、无制冷剂污染、结构简单且集成度高,在通信机柜中也有广泛的应用。但是单个TEC的功率很小,在通信机柜的应用中,需要将TEC串并联后组合成堆进行使用。在使用过程中,TEC的冷端表面安装散热片和风扇放置于通信机柜内,在TEC的热端安装散热片和风扇放置于通信机柜的外侧,由此控制通信机柜内部的温度。 For communication cabinets, in addition to using air conditioners for cooling, thermoelectric cooling (TEC) itself has no moving parts, no refrigerant pollution, simple structure and high integration, so it is also widely used in communication cabinets. However, the power of a single TEC is very small. In the application of the communication cabinet, the TECs need to be connected in series and parallel and combined into a stack for use. During use, the cooling fins and fans installed on the cold side of the TEC are placed inside the communication cabinet, and the cooling fins and fans installed on the hot side of the TEC are placed outside the communication cabinet, thereby controlling the temperature inside the communication cabinet.
目前的高效传热器件中热管已经被广泛的应用,如图1所示,现有技术提供一种采用热管换热器进行机房的冷却,采用相互独立的蒸发端与冷凝端,蒸发端与冷凝端之间连接有构成循环通路的导管,导管内设有热管介质。由此能有效利用冬季与春秋季节较低的环境温度。 Heat pipes have been widely used in current high-efficiency heat transfer devices. As shown in Figure 1, the existing technology provides a heat pipe heat exchanger for cooling the machine room, using independent evaporation ends and condensation ends, and evaporation ends and condensation ends. A conduit forming a circulation path is connected between the ends, and a heat pipe medium is arranged in the conduit. Therefore, the lower ambient temperature in winter and spring and autumn can be effectively utilized.
从上述的技术方案可见,不管是采用大功率空调还是TEC来控制设备的温度,都需要消耗大量的电能。另外,由于TEC的热电转换效率较低,这种冷却方式的能源利用效率低下,为了达到要求的负荷,需要将很多TEC进行串并联使用,系统复杂,可靠性低。 It can be seen from the above technical solutions that no matter whether a high-power air conditioner or a TEC is used to control the temperature of the equipment, a large amount of electric energy is consumed. In addition, due to the low thermoelectric conversion efficiency of TEC, the energy utilization efficiency of this cooling method is low. In order to achieve the required load, many TECs need to be used in series and parallel, the system is complicated and the reliability is low.
在较冷的春秋冬季,由于室外温度低,可以利用室内外的温差,在不消耗动力的条件下,将室内的热量转移到室外,节省空调的电能消耗。但是由于洁净度的要求,不能直接将室内外空气进行交换,而需要使用热管等高效传热设备。 In the colder spring, autumn and winter, due to the low outdoor temperature, the indoor and outdoor temperature difference can be used to transfer the indoor heat to the outdoor without consuming power, saving the power consumption of the air conditioner. However, due to the requirements of cleanliness, it is not possible to directly exchange indoor and outdoor air, but it is necessary to use efficient heat transfer equipment such as heat pipes.
蒸发端和冷凝端分离的热管换热器采用的是连接导管的方式,所有的蒸发端产生的蒸汽均通过连接导管输运,造成了流动阻力增加;蒸汽在冷凝侧的入口处即开始冷凝,下方蒸汽较少,造成冷凝侧器的温度分布不均匀,不能很好的发挥冷凝侧的换热能力。另一方面如果机房面积较大,蒸发端和冷凝端的距离较远,造成了连接导管的长度增加,也会带来热阻增加的后果。如果热管换热器的热阻增加,则意味着蒸发端和冷凝端的温差增大,只有的更低的室外温度环境下,热管换热器才能启用,因此导致全年可用天数减少,节能效果降低。 The heat pipe heat exchanger that separates the evaporating end and the condensing end adopts the method of connecting pipes. All the steam generated at the evaporating end is transported through the connecting pipes, resulting in increased flow resistance; the steam starts to condense at the entrance of the condensing side. There is less steam at the bottom, resulting in uneven temperature distribution of the condenser side, which cannot make good use of the heat exchange capacity of the condenser side. On the other hand, if the area of the machine room is large, the distance between the evaporation end and the condensation end is relatively long, resulting in an increase in the length of the connecting pipe, which will also increase the thermal resistance. If the thermal resistance of the heat pipe heat exchanger increases, it means that the temperature difference between the evaporating end and the condensing end increases, and the heat pipe heat exchanger can only be used in a lower outdoor temperature environment, resulting in a reduction in the number of available days throughout the year and a reduction in energy saving effect .
实用新型内容 Utility model content
有鉴于此,本实用新型的目的在于提供一种环形热管阵列换热器以及包含其的换热系统。 In view of this, the purpose of the present utility model is to provide an annular heat pipe array heat exchanger and a heat exchange system comprising it.
为实现上述目的,根据本实用新型一方面,提供一种环形热管阵列换热器,包括冷凝端和蒸发端,其中: In order to achieve the above purpose, according to one aspect of the present invention, there is provided an annular heat pipe array heat exchanger, including a condensation end and an evaporation end, wherein:
所述冷凝端和蒸发端均包括多路水平管路; Both the condensation end and the evaporation end include multiple horizontal pipelines;
所述换热器还包括两个多通管路,所述两个多通管路相对设置,且每个多通管路均连接至冷凝端和蒸发端的水平管路,以使换热器形成多个闭合环路,两个多通管路分别为第一多通管路和第二多通管路。 The heat exchanger also includes two multi-pass pipelines, the two multi-pass pipelines are arranged oppositely, and each multi-pass pipeline is connected to the horizontal pipelines at the condensing end and the evaporating end, so that the heat exchanger forms Multiple closed loops, the two multi-way pipelines are respectively the first multi-way pipeline and the second multi-way pipeline.
根据本实用新型的一具体实施方案,所述蒸发端的多路水平管路包含蒸发端上部管路,所述蒸发端上部管路的至少部分管路被设置为一端连接第一多通管路,在蒸发端经一个或多个折返另一端再连接至第二多通管路。 According to a specific embodiment of the present invention, the multi-channel horizontal pipeline at the evaporation end includes an upper pipeline at the evaporation end, and at least part of the upper pipeline at the evaporation end is configured such that one end is connected to the first multi-way pipeline, At the evaporation end, the other end is connected to the second multi-way pipeline through one or more turns.
根据本实用新型的一具体实施方案,所述冷凝端的多路水平管路包含冷凝端下部管路,所述冷凝端下部管路的至少部分管路被设置为一端连接至第二多通管路,在冷凝端经一个或多个折返另一端连接至第一多通管路。 According to a specific embodiment of the present invention, the multi-channel horizontal pipeline at the condensing end includes a lower pipeline at the condensing end, and at least part of the lower pipeline at the condensing end is configured such that one end is connected to the second multi-way pipeline , the other end is connected to the first multi-pass pipeline through one or more turns at the condensing end.
根据本实用新型的一具体实施方案,还包括一竖直设置的母管,所述母管与所述多个闭合环路连通,使多个闭合环路实现介质交换。 According to a specific embodiment of the present invention, a vertically arranged main pipe is also included, and the main pipe communicates with the plurality of closed loops, so that the plurality of closed loops realize medium exchange.
根据本实用新型的一具体实施方案,所述母管设置于第一多通管路与冷凝端之间,或者设置于第二多通管路与冷凝端之间,所述母管设置有一换热介质充装口;优选的,所述多通管路的部分管路与水平方向呈1-30°的倾斜角度。 According to a specific embodiment of the present utility model, the main pipe is arranged between the first multi-way pipeline and the condensation end, or between the second multi-way pipeline and the condensation end, and the main pipe is provided with a replacement Heat medium filling port; preferably, part of the multi-way pipeline has an inclination angle of 1-30° with respect to the horizontal direction.
根据本实用新型的一具体实施方案,所述冷凝端的水平管路经过一段高度增加的连接管路连接至母管,以避免冷凝液进入母管。 According to a specific embodiment of the present invention, the horizontal pipeline at the condensing end is connected to the main pipe through a connection pipeline with increased height, so as to prevent the condensate from entering the main pipe.
根据本实用新型的一具体实施方案,还包括多个竖直的母管,分别连通部分所述多个闭合环路。 According to a specific embodiment of the present invention, it further includes a plurality of vertical main pipes, respectively communicating with part of the plurality of closed loops.
根据本实用新型的一方面,提供一种环形热管阵列换热器,包括冷凝端和蒸发端,其中: According to one aspect of the present invention, there is provided an annular heat pipe array heat exchanger, including a condensation end and an evaporation end, wherein:
所述冷凝端和蒸发端均包括多路水平管路; Both the condensation end and the evaporation end include multiple horizontal pipelines;
还包括N组两两相对设置的2N个多通管路,每个多通管路均连接至冷凝端和蒸发端的水平管路,形成N组闭合环路; It also includes N groups of 2N multi-pass pipelines arranged opposite to each other, and each multi-pass pipeline is connected to the horizontal pipelines at the condensation end and the evaporation end to form N groups of closed loops;
还包括N个竖直设置的母管,每个所述母管与每个所述闭合环路连通,其中N为2以上的自然数。 It also includes N vertically arranged main pipes, each of which is in communication with each of the closed loops, wherein N is a natural number greater than 2.
根据本实用新型的一具体实施方案,所述冷凝端和蒸发端的多路水平管路呈内外多层分布。 According to a specific embodiment of the present invention, the multi-channel horizontal pipelines at the condensing end and the evaporating end are distributed in inner and outer layers.
根据本实用新型的一方面,提供一种用于通信机柜或计算机中心的换热系统,包括以上任意一种环形热管阵列换热器,优选的还包括收集热量的风道,所述风道末端通至所述换热系统的环形热管阵列换热器的蒸发端。 According to one aspect of the present invention, there is provided a heat exchange system for a communication cabinet or a computer center, including any one of the above annular heat pipe array heat exchangers, and preferably also includes an air duct for collecting heat, and the end of the air duct Lead to the evaporation end of the annular heat pipe array heat exchanger of the heat exchange system.
通过上述技术方案,本实用新型的有益效果在于: Through the above technical scheme, the beneficial effects of the utility model are:
(1)通过在蒸发端和冷凝端之间设置相对的多通管路,蒸汽可沿两 个方向流向冷凝端,蒸汽的流动阻力大幅减小; (1) By setting relative multi-pass pipelines between the evaporating end and the condensing end, the steam can flow to the condensing end in two directions, and the flow resistance of the steam is greatly reduced;
(2)通过设置带有母管的环形热管阵列换热器,利用春秋冬季节室外温度较低的条件,在消耗动力较少的条件下,将空间内部的热量转移到室外,从而节省了大量的空调能耗,并且在热量转移的过程中不产生内外空气的交换,保证了数据中心或机柜内部的洁净度; (2) By setting up an annular heat pipe array heat exchanger with a main pipe, taking advantage of the low outdoor temperature in spring, autumn and winter, and under the condition of less power consumption, the heat inside the space is transferred to the outside, thus saving a lot of energy. The energy consumption of the air conditioner is low, and there is no exchange of internal and external air during the heat transfer process, which ensures the cleanliness of the data center or the inside of the cabinet;
(3)本系统相较于带有空调或TEC的系统相比,系统节省电能,结构简单,可靠性高。 (3) Compared with the system with air conditioner or TEC, the system saves electric energy, has simple structure and high reliability.
(4)与母管接触的部分有高度逐渐上升的管路(尤其为一乙字形结构),从而避免了冷凝液进入到母管,在重力的作用下跌落到母管的底端,全部积聚到蒸发端的底部,影响热管换热器,同时也部分避免了汽液的逆向流动造成流动阻力增加,上述设计均减小了系统的热阻; (4) The part in contact with the main pipe has a pipeline with a height gradually rising (especially a B-shaped structure), thereby preventing the condensate from entering the main pipe, falling to the bottom of the main pipe under the action of gravity, and all accumulating To the bottom of the evaporation end, it affects the heat pipe heat exchanger, and also partially avoids the increase of flow resistance caused by the reverse flow of vapor and liquid. The above designs all reduce the thermal resistance of the system;
(5)通过设置带母管环形热管换热器阵列,蒸汽可以在整个换热器内弥漫,在冷源温度低的地方,蒸发端与冷凝端的压差较大,冷凝量也多,温度均匀性好,适应局部热量变化,适应冷热源分布不均匀的能力强; (5) By setting up an array of annular heat pipe heat exchangers with parent pipes, the steam can diffuse in the entire heat exchanger. In places where the temperature of the cold source is low, the pressure difference between the evaporation end and the condensation end is large, the condensation is also large, and the temperature is uniform Good performance, adapt to local heat changes, and have a strong ability to adapt to uneven distribution of cold and heat sources;
(6)热管阵列共用一个充装口,只需充装一次,充装工艺简单,成本大幅降低。由于内部容积大,充装率精度易于保证,给工业设计和制造带来方便; (6) The heat pipe arrays share one filling port, only need to be filled once, the filling process is simple, and the cost is greatly reduced. Due to the large internal volume, the filling rate accuracy is easy to guarantee, which brings convenience to industrial design and manufacturing;
(7)对于面积较大的计算中心,通过安装风道收集每个机柜产生的热量,通过热管换热器集中处理的方案进行设计,克服了由于连接导管的长度增加,带来的热阻增加; (7) For a computing center with a large area, the heat generated by each cabinet is collected by installing an air duct, and the heat pipe heat exchanger is designed for centralized processing, which overcomes the increase in thermal resistance due to the increase in the length of the connecting duct ;
(8)除应用于通信机柜、通信基站、服务器机柜、服务器机房等设备的冷却,还可用于暖通空调、化工、能源等行业的余热回收。 (8) In addition to being used for cooling equipment such as communication cabinets, communication base stations, server cabinets, and server rooms, it can also be used for waste heat recovery in HVAC, chemical, energy and other industries.
附图说明 Description of drawings
图1是现有技术中的一种换热器。 Fig. 1 is a kind of heat exchanger in the prior art.
图2是本实用新型一实施例的环形热管阵列换热器的原理图。 Fig. 2 is a schematic diagram of an annular heat pipe array heat exchanger according to an embodiment of the present invention.
图3是本实用新型一实施例的环形热管阵列换热器的三维视图。 Fig. 3 is a three-dimensional view of an annular heat pipe array heat exchanger according to an embodiment of the present invention.
图4是本实用新型一实施例隐藏翅片的环形热管阵列结构示意图。 Fig. 4 is a structural schematic diagram of an annular heat pipe array with hidden fins according to an embodiment of the present invention.
图5是图4的冷凝端与母管的连接关系放大立体示意图。 Fig. 5 is an enlarged perspective view showing the connection relationship between the condensation end and the main pipe in Fig. 4 .
图6是图4的冷凝端与母管的连接关系放大截面示意图。 Fig. 6 is an enlarged schematic cross-sectional view of the connection relationship between the condensation end and the main pipe in Fig. 4 .
图7是本实用新型又一实施例的环形热管阵列换热器的三维视图。 Fig. 7 is a three-dimensional view of an annular heat pipe array heat exchanger according to another embodiment of the present invention.
图8是本实用新型又一实施例的环形热管阵列换热器的三维视图。 Fig. 8 is a three-dimensional view of an annular heat pipe array heat exchanger according to another embodiment of the present invention.
图9是本实用新型又一实施例的环形热管阵列换热器的三维视图。 Fig. 9 is a three-dimensional view of an annular heat pipe array heat exchanger according to another embodiment of the present invention.
图10是本实用新型一实施例的大型换热系统示意图。 Fig. 10 is a schematic diagram of a large-scale heat exchange system according to an embodiment of the present invention.
具体实施方式 detailed description
为使本实用新型的目的、技术方案和优点更加清楚明白,以下结合具体实施例,并参照附图,对本实用新型作进一步的详细说明。在说明书中,相同或相似的附图标号指示相同或相似的部件。下述参照附图对本实用新型实施方式的说明旨在对本实用新型的总体实用新型构思进行解释,而不应当理解为对本实用新型的一种限制。 In order to make the purpose, technical solutions and advantages of the utility model clearer, the utility model will be further described in detail below in combination with specific embodiments and with reference to the accompanying drawings. In the specification, the same or similar reference numerals designate the same or similar components. The following descriptions of the embodiments of the utility model with reference to the accompanying drawings are intended to explain the overall utility model concept of the utility model, and should not be construed as a limitation of the utility model.
根据本实用新型总体上的实用新型构思,提供一种环形热管阵列换热器,包括冷凝端和蒸发端,通过相对设置的两个多通管路,实现多环路换热。以下对各部件的设置结合附图进行具体说明。 According to the overall utility model idea of the utility model, an annular heat pipe array heat exchanger is provided, which includes a condensation end and an evaporation end, and realizes multi-loop heat exchange through two multi-pass pipelines arranged oppositely. The arrangement of each component will be described in detail below in conjunction with the accompanying drawings.
如图2所示,热源2(如通信机柜)内的高温空气首先经过环形热管阵列换热器1(以下简称:热管换热器)的蒸发端101,热管的蒸发端101吸收高温空气中携带的热量,热管中的工质吸收热量后蒸发,进入到冷凝端102,在冷凝端中,工质冷凝释放给柜外低温空气,由此实现了通信机柜内外热量的交换,并且不发生内外空气交换。热管的应用在保证柜内温度的情况下,节省了空调或TEC的用电。 As shown in Figure 2, the high-temperature air in the heat source 2 (such as a communication cabinet) first passes through the evaporation end 101 of the annular heat pipe array heat exchanger 1 (hereinafter referred to as: heat pipe heat exchanger), and the evaporation end 101 of the heat pipe absorbs the air carried by the high-temperature air. The working fluid in the heat pipe absorbs heat and then evaporates, entering the condensation end 102. In the condensation end, the working fluid is condensed and released to the low-temperature air outside the cabinet, thereby realizing the exchange of heat inside and outside the communication cabinet, and no internal and external air exchange. The application of the heat pipe saves the electricity consumption of the air conditioner or TEC while ensuring the temperature in the cabinet.
如图3是热管换热器的三维视图,图4是隐去换热翅片的环形回路。本热管换热器可由一带有母管的环形热管阵列组成。 Figure 3 is a three-dimensional view of the heat pipe heat exchanger, and Figure 4 is a ring circuit with heat exchange fins hidden. The heat pipe heat exchanger can be composed of an annular heat pipe array with a parent pipe.
如图4是热管阵列的结构示意图,由上部管路103-1、中部管路103-2、下部管路103-3、母管104组成阵列。在位于蒸发端101和冷凝端102中带有翅片的部分,内部的管路呈水平状态,而在连接蒸发端101和冷凝端102的管路103-a和103-b部分与水平方向呈1°-30°的倾斜角度,保证凝结液体的顺利回流。在热管换热器1最上层的管路103-1的蒸发端侧多走一个回程,在热管换热器1最下层的管路103-3的冷凝端侧多走一个回程,由此增加了热管换热器中蒸发端101和冷凝端102的换热面积。 FIG. 4 is a structural diagram of a heat pipe array, which consists of an upper pipeline 103 - 1 , a middle pipeline 103 - 2 , a lower pipeline 103 - 3 and a main pipe 104 . In the part with fins in the evaporating end 101 and the condensing end 102, the internal pipeline is in a horizontal state, while the parts of the pipelines 103-a and 103-b connecting the evaporating end 101 and the condensing end 102 are in a horizontal direction. The inclination angle of 1°-30° ensures the smooth return of condensed liquid. One more return journey is made on the evaporation end side of the uppermost pipeline 103-1 of the heat pipe heat exchanger 1, and one more return journey is taken on the condensation end side of the lowermost pipeline 103-3 of the heat pipe heat exchanger 1, thereby increasing the The heat exchange area of the evaporating end 101 and the condensing end 102 in the heat pipe heat exchanger.
在环路103上安装连接母管104,将管路103-1、103-2、103-3连接起来,形成一个联通的整体。在母管104上安装有用于抽真空和注液的封装口。管路103-1、103-2、103-3从冷凝端出来后经过一乙字形(图5,图6所示)结构,使两侧的高差h达到或超过管径,并与母管相连。如图5所示设计成两侧具有一定高差结构的主要目的是防止冷凝液回流的时候进入到母管,全部坠落到母管的底部,导致工质不能在蒸发端内部均匀的分布。 A connecting main pipe 104 is installed on the loop 103 to connect the pipelines 103-1, 103-2, and 103-3 to form a connected whole. A sealing port for vacuuming and liquid injection is installed on the main pipe 104 . Pipelines 103-1, 103-2, and 103-3 pass through a B-shaped structure (shown in Figure 5 and Figure 6) after coming out of the condensing end, so that the height difference h on both sides reaches or exceeds the pipe diameter, and is connected with the main pipe connected. As shown in Figure 5, the main purpose of designing a structure with a certain height difference on both sides is to prevent the condensate from entering the main pipe when it flows back, and all fall to the bottom of the main pipe, causing the working fluid to not be evenly distributed inside the evaporator.
该热管换热器的封装工艺和工作机理是: The packaging process and working mechanism of the heat pipe heat exchanger are:
(1)对热管换热器1进行超声波清洗,去除表面的油污。 (1) Ultrasonic cleaning is performed on the heat pipe heat exchanger 1 to remove oil stains on the surface.
(2)将热管换热器1放入高温干燥箱内,去除热管换热器内部的水分。 (2) Put the heat pipe heat exchanger 1 into a high-temperature drying oven to remove moisture inside the heat pipe heat exchanger.
(3)通过母管上的封装口抽真空,当系统内部的压力小于1Pa时,关闭真空泵,并保持热管换热器1处于真空状态。 (3) Vacuum through the sealing port on the main pipe. When the pressure inside the system is less than 1Pa, turn off the vacuum pump and keep the heat pipe heat exchanger 1 in a vacuum state.
(4)在热管换热器内封装一定量的液体工质,这些工质可以为:乙醇、R134a、R22、R410a、R113等多种有机工质或氟利昂类工质,根据工质热物性参数的不同,充液率在20%-80%之间。 (4) Encapsulate a certain amount of liquid working fluid in the heat pipe heat exchanger, these working fluids can be: ethanol, R134a, R22, R410a, R113 and other organic working fluids or Freon-like working fluids, according to the thermal physical properties of the working fluid The liquid filling rate is between 20% and 80%.
在热管换热器1中的工质相变过程如下: The phase change process of the working fluid in the heat pipe heat exchanger 1 is as follows:
工质在蒸发端101中吸收热量蒸发,通过蒸发端和冷凝端之间的连接管路103-a,103-b输运到冷凝端中,相较于冷凝端和蒸发端通过两根管路连接的方式,在采用103-a和103-b这种双侧连接管路中,每个环路均对应两根连接管路,蒸汽可沿两个方向流向冷凝端,蒸汽的流动阻力大幅减小。液体在冷凝端中冷凝后通过103-a流回到蒸发端中,而103-b中并没有冷凝液的回流,这是由于103-b与母管接触的部分有一乙字形结构,从而避免了冷凝液进入到母管,在重力的作用下跌落到母管的底端,全部积聚到蒸发端的底部,影响热管换热器1的性能,同时也部分避免了汽液的逆向流动造成流动阻力增加。 The working fluid absorbs heat and evaporates in the evaporating end 101, and is transported to the condensing end through the connecting pipelines 103-a and 103-b between the evaporating end and the condensing end. The way of connection, in the double-sided connecting pipelines of 103-a and 103-b, each loop corresponds to two connecting pipelines, steam can flow to the condensation end in two directions, and the flow resistance of steam is greatly reduced Small. After the liquid is condensed in the condensing end, it flows back to the evaporating end through 103-a, but there is no reflux of condensate in 103-b. This is because the part of 103-b in contact with the main pipe has a B-shaped structure, thus avoiding The condensate enters the main pipe, falls to the bottom of the main pipe under the action of gravity, and all accumulates at the bottom of the evaporating end, which affects the performance of the heat pipe heat exchanger 1, and also partly avoids the increase of flow resistance caused by the reverse flow of vapor and liquid .
1.根据散热负荷和不同要求,组成热管阵列的环路数量可进行调整。 1. According to the heat dissipation load and different requirements, the number of loops forming the heat pipe array can be adjusted.
2.根据散热负荷和不同要求,如图7所示,可将上述实施方案设计成内外双层环路或多层环路的结构。 2. According to the heat dissipation load and different requirements, as shown in Fig. 7, the above implementation scheme can be designed as a structure of inner and outer double-layer loops or multi-layer loops.
3.当设计成内外双层环路或多层环路时,如图8所示,可以共用一根粗母管或与之等效的方腔。 3. When it is designed as an inner and outer double-layer loop or a multi-layer loop, as shown in Figure 8, it is possible to share a thick mother pipe or an equivalent square cavity.
4.当设计成双环路或多环路的结构时,如图9所示,可以在上中下部各段分别共用母管或方腔。 4. When designing a double-loop or multi-loop structure, as shown in Figure 9, the upper, middle and lower sections can share the main pipe or square cavity respectively.
基于同一实用新型构思,本实用新型提供一种用于通信机柜或计算机中心的换热系统。 Based on the same concept of the utility model, the utility model provides a heat exchange system for a communication cabinet or a computer center.
在小型换热系统的实施方案里,例如面向的是机柜的散热,由于机柜的体积较小,依靠热管换热器中蒸发端上的风扇即可实现机柜内部的气流组织。而对于大型散热系统,如数据中心的换热,会存放很多组类似的机柜,如果每个接轨安装类似的热管换热器会导致系统复杂,安装困难。本实施例拟通过风道收集每个机柜产生的热量,通过热管换热器集中处理的方案进行设计。 In the implementation of the small heat exchange system, for example, it is oriented to the heat dissipation of the cabinet. Due to the small size of the cabinet, the air distribution inside the cabinet can be realized by relying on the fan on the evaporating end of the heat pipe heat exchanger. For large-scale heat dissipation systems, such as heat exchange in data centers, many groups of similar cabinets will be stored. If similar heat pipe heat exchangers are installed on each rail, the system will be complicated and installation will be difficult. In this embodiment, the heat generated by each cabinet is collected through the air duct, and the heat generated by the heat pipe heat exchanger is used for centralized processing.
如图10不同位置处的热源2(如机柜)所释放的热量通过风道3收集,通过热管换热器1与室外进行热量交换。图中箭头的方向为热空气流动的方向。 As shown in Figure 10, the heat released by the heat sources 2 (such as cabinets) at different positions is collected through the air duct 3, and the heat is exchanged with the outside through the heat pipe heat exchanger 1. The direction of the arrow in the figure is the direction of hot air flow.
以上所述的具体实施例,对本实用新型的目的、技术方案和有益效果进行了进一步详细说明,应理解的是,以上所述仅为本实用新型的具体实施例而已,并不用于限制本实用新型,凡在本实用新型的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。 The specific embodiments described above have further described the purpose, technical solutions and beneficial effects of the utility model in detail. It should be understood that the above descriptions are only specific embodiments of the utility model and are not intended to limit the utility model. For new models, any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present utility model shall be included within the protection scope of the present utility model.
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CN105737361A (en) * | 2016-04-21 | 2016-07-06 | 中国科学院工程热物理研究所 | Annular heat pipe array heat exchanger and heat exchange system comprising annular heat pipe array heat exchanger |
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