CN219301352U - Coiled pipe type heat exchanger - Google Patents

Coiled pipe type heat exchanger Download PDF

Info

Publication number
CN219301352U
CN219301352U CN202223074803.0U CN202223074803U CN219301352U CN 219301352 U CN219301352 U CN 219301352U CN 202223074803 U CN202223074803 U CN 202223074803U CN 219301352 U CN219301352 U CN 219301352U
Authority
CN
China
Prior art keywords
heat exchange
heat
cover
tube
coil
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.)
Active
Application number
CN202223074803.0U
Other languages
Chinese (zh)
Inventor
文昌龙
吕建波
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.)
Sichuan Zhuoyi Environmental Protection And Energy Saving Equipment Co ltd
Original Assignee
Sichuan Zhuoyi Environmental Protection And Energy Saving Equipment Co ltd
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 Sichuan Zhuoyi Environmental Protection And Energy Saving Equipment Co ltd filed Critical Sichuan Zhuoyi Environmental Protection And Energy Saving Equipment Co ltd
Priority to CN202223074803.0U priority Critical patent/CN219301352U/en
Application granted granted Critical
Publication of CN219301352U publication Critical patent/CN219301352U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model discloses a coil pipe type heat exchanger, which relates to the field of heat exchangers and solves the problem of low heat exchange efficiency of the existing heat exchanger, and the technical scheme is as follows: comprises a heat exchange disc; the heat exchange disc comprises a first heat exchange tube and a second heat exchange tube; the first heat exchange tube and the second heat exchange tube are spiral in mosquito-repellent incense shape; the first heat exchange tube and the second heat exchange tube are combined into a mosquito-repellent incense disk shape; the center is communicated by an S-shaped pipe; the heat exchange disc is provided with a cold medium inlet and a cold medium outlet; the heat exchange cover is also included; the heat exchange disc is arranged in the heat exchange cover; the cold medium inlet and the cold medium outlet are arranged outside the heat exchange cover. The purposes of heat exchangers with the same height and higher heat exchange efficiency are achieved.

Description

一种盘管式换热器A coil heat exchanger

技术领域technical field

本实用新型涉及一种盘式换热器,更具体地说,它涉及一种用于锅炉尾气使用的换热器。The utility model relates to a plate heat exchanger, more specifically, it relates to a heat exchanger used for boiler tail gas.

背景技术Background technique

换热器是将热流体的部分热量传递给冷流体的设备,又称热交换器。常见的换热器为螺旋管式换热器,以类似与弹簧形状的方式布置,每层中心距相等,层与层之间的距离相等。为了保证管外的介质有足够的流速,需要在中间加入芯筒,从而保证管外的介质有足够的流速,导致中心部分体积的浪费,单管螺旋缠绕也增加的盘管高度,加大了外筒体的高度或长度,造成材料增加。A heat exchanger is a device that transfers part of the heat of a hot fluid to a cold fluid, also known as a heat exchanger. Common heat exchangers are spiral tube heat exchangers, which are arranged in a spring-like manner, with the center-to-center distance of each layer being equal, and the distance between layers being equal. In order to ensure that the medium outside the tube has a sufficient flow rate, it is necessary to add a core tube in the middle, so as to ensure that the medium outside the tube has a sufficient flow rate, resulting in a waste of the volume of the central part, and the spiral winding of the single tube also increases the coil height and increases the The height or length of the outer cylinder, resulting in increased material.

实用新型内容Utility model content

本实用新型的目的是提供一种盘管式换热器,在同等高度条件下,增加换热器的换热效率;使达到相同的换热效率,所需要的换热器高度更低。The purpose of the utility model is to provide a coil heat exchanger, which can increase the heat exchange efficiency of the heat exchanger under the condition of the same height; to achieve the same heat exchange efficiency, the height of the heat exchanger required is lower.

本实用新型的上述技术目的是通过以下技术方案得以实现的:一种盘管式换热器,包括换热盘;换热盘包括第一换热管和第二换热管;第一换热管和第二换热管呈蚊香状螺旋;第一换热管和第二管热管组合为蚊香盘状;中心采用S形管连通;换热盘上具有冷介质入口和冷介质出口;还包括换热罩;所述换热盘设置于换热罩内;冷介质入口和冷介质出口设置于换热罩外。The above technical purpose of the utility model is achieved through the following technical solutions: a coil heat exchanger, including a heat exchange plate; the heat exchange plate includes a first heat exchange tube and a second heat exchange tube; the first heat exchange tube The tube and the second heat exchange tube are in the shape of a mosquito-repellent coil; the combination of the first heat-exchange tube and the second heat pipe is a mosquito-repellent coil; the center is connected by an S-shaped tube; the heat-exchange plate has a cold medium inlet and a cold medium outlet; it also includes The heat exchange cover; the heat exchange plate is arranged inside the heat exchange cover; the cold medium inlet and the cold medium outlet are arranged outside the heat exchange cover.

根据热传递的基本公式可知:在同样工况冷热传递的过程中,总传热系数越低,需要的换热面积越大;反之总传热系数越高,需要的换热面积越小。目前,热交换器多采用弹簧状的螺旋管布置换热管,总传热相对较低,导致需要换热管,材料较多,从而设计出来的产品体积大,重量高,占地面积大,操作不方便。与现有弹簧状的螺旋管式换热器相比,本实用新型提供的换热器,中间无空间,介质从蚊香换热管之间的间隙流过,无须使用芯筒,也能达到良好的换热效果。可以降低换热器的高度,减少换热器所需要的材料。According to the basic formula of heat transfer, it can be known that in the process of cold and heat transfer under the same working conditions, the lower the total heat transfer coefficient, the larger the required heat transfer area; conversely, the higher the total heat transfer coefficient, the smaller the required heat transfer area. At present, heat exchangers mostly use spring-shaped spiral tubes to arrange heat exchange tubes. The total heat transfer is relatively low, resulting in the need for heat exchange tubes and more materials, so the designed products are large in size, high in weight, and occupy a large area. Inconvenient to operate. Compared with the existing spring-shaped spiral tube heat exchanger, the heat exchanger provided by the utility model has no space in the middle, and the medium flows through the gap between the mosquito coil heat exchange tubes, without using a core tube, and can also achieve good performance. heat transfer effect. The height of the heat exchanger can be reduced, and the materials required for the heat exchanger can be reduced.

进一步的,具有至少两个换热盘;所述换热盘堆叠设置;换热盘之间设置间距保持板;相邻两层换热盘之间相对旋转45度~90度;相邻两层换热盘相连通。Further, there are at least two heat exchange disks; the heat exchange disks are stacked; the distance maintaining plates are arranged between the heat exchange disks; the heat exchange disks of two adjacent layers are relatively rotated by 45 degrees to 90 degrees; The heat exchange plates are connected.

进一步的,所述上层换热盘相对下层换热盘,顺时针旋转90度。Further, the upper heat exchange disk rotates 90 degrees clockwise relative to the lower heat exchange disk.

进一步的,所述上层换热盘相对下层换热盘,逆时针旋转90度。Further, the upper heat exchange disk rotates 90 degrees counterclockwise relative to the lower heat exchange disk.

进一步的,所述换热罩包括筒体、发散罩和集气罩;换热盘设置于筒体内;发散罩设置于筒体下端;发散罩直径,由下至上逐渐变大;集气罩设置于筒体上端;集气罩直径,由下至上逐渐变小;冷介质入口设置于冷介质出口上方。Further, the heat exchange cover includes a cylinder, a divergence cover and a gas collection cover; the heat exchange plate is arranged in the cylinder; the divergence cover is arranged at the lower end of the cylinder; the diameter of the divergence cover gradually increases from bottom to top; the gas collection cover is set At the upper end of the cylinder; the diameter of the gas collecting hood gradually decreases from bottom to top; the inlet of the cold medium is set above the outlet of the cold medium.

进一步的,所述烟气入口和烟气出口上设置有法兰盘。Further, the flue gas inlet and the flue gas outlet are provided with flanges.

附图说明Description of drawings

图1是实施例示意图Fig. 1 is a schematic diagram of an embodiment

图2是实施例剖视图Figure 2 is a cross-sectional view of the embodiment

图3是多个换热盘示意图Figure 3 is a schematic diagram of multiple heat exchange plates

图4是单个换热盘示意图Figure 4 is a schematic diagram of a single heat exchange plate

图5是间距保持板示意图Figure 5 is a schematic diagram of the spacing maintaining plate

图中:11、筒体;12、集气罩;13、发散罩;21、冷介质入口;22、冷介质出口;23、换热盘;231、第一换热管;232、第二换热管;24、180度弯头;25、弯管;26、S形管;27、间距保持板;271、支撑槽。In the figure: 11, cylinder body; 12, gas collection hood; 13, divergence hood; 21, cold medium inlet; 22, cold medium outlet; 23, heat exchange plate; 231, first heat exchange tube; 232, second exchange Heat pipe; 24, 180-degree elbow; 25, elbow; 26, S-shaped pipe; 27, distance maintaining plate; 271, support groove.

具体实施方式Detailed ways

为了使本实用新型所要解决的技术问题、技术方案及有益效果更加清楚明白,以下结合附图及实施例,对本实用新型进行进一步详细说明。In order to make the technical problems, technical solutions and beneficial effects to be solved by the utility model clearer, the utility model will be further described in detail below in conjunction with the accompanying drawings and embodiments.

需说明的是,当部件被称为“固定于”或“设置于”另一个部件,它可以直接在另一个部件上或者间接在该另一个部件上。当一个部件被称为是“连接”另一个部件,它可以是直接或者间接连接至该另一个部件上,该“连接”不限定固定连接或活动连接,具体连接方式应根据所要解决的具体技术问题来判断。It should be noted that when a component is referred to as being “fixed on” or “disposed on” another component, it may be directly on the other component or indirectly on the other component. When a component is said to be "connected" to another component, it may be directly or indirectly connected to the other component. The "connection" does not limit to a fixed connection or a movable connection. The specific connection method should be based on the specific technology to be solved. question to judge.

需要理解的是,术语“长度”、“宽度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”“内”、“外”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本实用新型和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本实用新型的限制。It is to be understood that the terms "length", "width", "top", "bottom", "front", "rear", "left", "right", "vertical", "horizontal", "top" , "bottom", "inner", "outer" and other indicated orientations or positional relationships are based on the orientations or positional relationships shown in the drawings, which are only for the convenience of describing the utility model and simplifying the description, rather than indicating or implying No device or element must have a specific orientation, be constructed and operate in a specific orientation, and thus should not be construed as limiting the invention.

此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括一个或者更多个该特征。在本实用新型的描述中,“多个”的含义是两个或两个以上,除非另有明确具体的限定。In addition, the terms "first" and "second" are used for descriptive purposes only, and cannot be interpreted as indicating or implying relative importance or implicitly specifying the quantity of indicated technical features. Thus, a feature defined as "first" and "second" may explicitly or implicitly include one or more of these features. In the description of the present utility model, "plurality" means two or more, unless otherwise specifically defined.

实施例:Example:

一种盘式换热器,所述盘式换热器包括换热罩;换热罩内设置有换热盘23;换热盘23包括第一换热管231和第二换热管232;第一换热管231和第二换热管232呈蚊香状螺旋;第一换热管231和第二管换热管组合为蚊香盘状;中心采用S形管26连通;如此设置冷介质入口21和冷介质出口22均处于换热盘23外圈,便于伸出换热罩外。具有至少两个换热盘23,所述换热盘23堆叠设置;第一换热管231和第二换热管232之间间隙的宽为2~8毫米。两层换热盘23之间可以错开一定角度;可选的,设置方式可以为30度、45度、60度、90度。A disc heat exchanger, the disc heat exchanger includes a heat exchange cover; a heat exchange disc 23 is arranged inside the heat exchange cover; the heat exchange disc 23 includes a first heat exchange tube 231 and a second heat exchange tube 232; The first heat exchange tube 231 and the second heat exchange tube 232 are in the shape of a mosquito-repellent coil; the combination of the first heat-exchange tube 231 and the second tube heat-exchange tube is a mosquito-repellent coil; the center is connected by an S-shaped tube 26; the cold medium inlet is set in this way 21 and the cold medium outlet 22 are all located on the outer ring of the heat exchange plate 23, so as to be convenient to extend out of the heat exchange cover. There are at least two heat exchange plates 23, and the heat exchange plates 23 are stacked; the width of the gap between the first heat exchange tube 231 and the second heat exchange tube 232 is 2-8 mm. The two layers of heat exchange discs 23 can be staggered by a certain angle; optionally, the setting method can be 30 degrees, 45 degrees, 60 degrees, or 90 degrees.

本实施例中,所述换热盘23上层换热盘23相对下层换热盘23,逆时针旋转90度。相邻两层之间用层间连接管连接;所述层间连接管包括弯管25、180度弯头24,弯管25与180度弯头24连接;层间连接管分别与相邻换热盘23连接。通过上述设置,层间连接管,挡住上一层外圈较大缝隙部分,避免管外介质偏流。在一种可能的是实施例中,所述换热盘23上层换热盘23相对下层换热盘23,顺时针旋转90度。通过上述设置,上层换热盘23第一换热管231和第二管热管之间的缝隙,刚好被下层换热盘23第一换热管231或第二管热管所遮蔽;可以增加热气的流通距离,使其能够更加充分的与换热盘23换热。通过上述设置,多层换热盘23连接后,液体在管道内可以单向流经所有换热盘23,使其充分换热。In this embodiment, the upper heat exchange disk 23 of the heat exchange disk 23 rotates 90 degrees counterclockwise relative to the lower heat exchange disk 23 . The adjacent two layers are connected with interlayer connecting pipes; the interlayer connecting pipes include elbows 25 and 180 degree elbows 24, and the elbows 25 are connected with 180 degree elbows 24; Hot plate 23 is connected. Through the above arrangement, the connecting pipe between the layers blocks the large gap part of the outer ring of the upper layer to avoid the bias flow of the medium outside the pipe. In a possible embodiment, the upper heat exchange disk 23 of the heat exchange disk 23 rotates 90 degrees clockwise relative to the lower heat exchange disk 23 . Through the above arrangement, the gap between the first heat exchange tube 231 and the second heat pipe of the upper heat exchange plate 23 is just covered by the first heat exchange tube 231 or the second heat pipe of the lower heat exchange plate 23; The circulation distance enables it to exchange heat with the heat exchange disk 23 more fully. Through the above arrangement, after the multi-layer heat exchange disks 23 are connected, the liquid can flow through all the heat exchange disks 23 in one direction in the pipeline, so that the heat can be fully exchanged.

还包括间距保持板27,间距保持板27上有换热管支撑槽271;间距保持板27上的支撑槽271的槽间距与第一换热管231和第二换热管232的间隙距离相等;间距保持板27上下两侧均有换热管支撑槽271;间距保持板27的高度与相邻换热盘23之间的间隙距离相适应,使其满足,通过间距保持板27可以保持换热盘23之间的间隙距离。间距保持板27由耐热材料制成,通过间距保持板27避免在高温下,换热管之间以及换热盘23之间间距的变化,导致传热系数的变化。It also includes a distance maintaining plate 27, on which there are heat exchange tube support grooves 271; the distance between the support grooves 271 on the distance maintaining plate 27 is equal to the gap distance between the first heat exchange tube 231 and the second heat exchange tube 232 There are heat exchange tube support grooves 271 on the upper and lower sides of the space keeping plate 27; Gap distance between hot plates 23. The spacing maintaining plate 27 is made of heat-resistant material, and the spacing maintaining plate 27 prevents the variation of the spacing between the heat exchange tubes and the heat exchange discs 23 at high temperature, resulting in a change of the heat transfer coefficient.

所述换热罩包括筒体11、发散罩13和集气罩12;换热盘23设置于筒体11内;发散罩13设置于筒体11下端;发散罩13直径,由下至上逐渐变大;集气罩12设置于筒体11上端;集气罩12直径,由下至上逐渐变小。所述烟气入口和烟气出口上设置有法兰盘。冷介质入口21设置于冷介质出口22上方。烟气通过发散罩13进入换热器,由下至上,由集气罩12排出换热器。由于冷介质入口21在上方,由上至下依次经过个换热盘23,冷介质可以与烟气进行充分换热。The heat exchange cover includes a cylinder 11, a divergence cover 13 and a gas collection cover 12; a heat exchange plate 23 is arranged in the cylinder 11; a divergence cover 13 is arranged at the lower end of the cylinder 11; the diameter of the divergence cover 13 gradually changes from bottom to top Large; the gas collecting hood 12 is arranged on the upper end of the cylinder 11; the diameter of the gas collecting hood 12 gradually becomes smaller from bottom to top. The flue gas inlet and the flue gas outlet are provided with flanges. The cooling medium inlet 21 is disposed above the cooling medium outlet 22 . The flue gas enters the heat exchanger through the diffuser hood 13, and is exhausted from the heat exchanger by the gas collection hood 12 from bottom to top. Since the cold medium inlet 21 is at the top and passes through the heat exchange plates 23 sequentially from top to bottom, the cold medium can fully exchange heat with the flue gas.

该换热器用于与锅炉燃烧室的烟气出口通道连接。可以将烟气中的热量用于对介质的加热。能够避免能源的浪费。The heat exchanger is used to connect with the flue gas outlet channel of the boiler combustion chamber. The heat in the flue gas can be used to heat the medium. Energy waste can be avoided.

工作原理:working principle:

烟气从烟气入口法兰进入该热交换器后,经发散罩13将热流体分散布满整个圆筒,然后依次冲刷成错列的布置的蚊香盘管层,通过最顶部一层后,再由集气罩12进行汇集,最后由顶部热流体出口法兰进入下游;与此同时,冷介质由顶部冷介质入口21管进入换热管,从顶部依次流向底部,在此过程,与外部的热流体发生热量交换,最后由冷介质出口22法兰进入下游。在此热交换过程中,热流体从底部进入顶部流出,温度逐渐从高到低;冷流体从顶部进入底部流出,温度逐渐从低到高,形成了完全理想的全逆流传热模型,很大程度上提高热传递效率和传热系数。After the flue gas enters the heat exchanger from the flue gas inlet flange, the hot fluid is dispersed over the entire cylinder through the divergence cover 13, and then washed in turn into staggered mosquito coil layers, and after passing through the top layer, Then it is collected by the gas collecting hood 12, and finally enters the downstream from the top hot fluid outlet flange; at the same time, the cold medium enters the heat exchange tube from the top cold medium inlet 21, and flows from the top to the bottom in sequence. The heat exchange occurs in the hot fluid, and finally enters the downstream through the cold medium outlet 22 flange. In this heat exchange process, the hot fluid flows from the bottom to the top, and the temperature gradually changes from high to low; the cold fluid flows from the top to the bottom, and the temperature gradually changes from low to high, forming a completely ideal full counter heat transfer model, which is very large. Improve heat transfer efficiency and heat transfer coefficient to a certain extent.

本具体实施例仅仅是对本实用新型的解释,其并不是对本实用新型的限制,本领域技术人员在阅读完本说明书后可以根据需要对本实施例作出没有创造性贡献的修改,但只要在本实用新型的权利要求范围内都受到专利法的保护。This specific embodiment is only an explanation of the utility model, and it is not a limitation of the utility model. Those skilled in the art can make modifications without creative contribution to this embodiment as needed after reading this description, but as long as the utility model All claims are protected by patent law.

Claims (6)

1.一种盘管式换热器,其特征是:包括换热盘(23);换热盘(23)包括第一换热管(231)和第二换热管(232);第一换热管(231)和第二换热管(232)呈蚊香状螺旋;第一换热管(231)和第二管热管组合为蚊香盘状;换热盘中部中心采用S形管(26)将第一换热管和第二换热管连通;换热盘(23)上具有冷介质入口(21)和冷介质出口(22);1. A coil heat exchanger is characterized in that: it comprises a heat exchange plate (23); the heat exchange plate (23) comprises a first heat exchange tube (231) and a second heat exchange tube (232); the first The heat exchange tube (231) and the second heat exchange tube (232) are in the shape of a mosquito-repellent coil; the first heat exchange tube (231) and the second tube heat pipe are combined into a mosquito-repellent coil; the center of the heat exchange plate adopts an S-shaped tube (26 ) communicate the first heat exchange tube with the second heat exchange tube; the heat exchange plate (23) has a cold medium inlet (21) and a cold medium outlet (22); 还包括换热罩;所述换热盘(23)设置于换热罩内;冷介质入口(21)和冷介质出口(22)设置于换热罩外。It also includes a heat exchange cover; the heat exchange plate (23) is arranged inside the heat exchange cover; the cold medium inlet (21) and the cold medium outlet (22) are arranged outside the heat exchange cover. 2.根据权利要求1所述的一种盘管式换热器,其特征是:具有至少两个换热盘(23);所述换热盘(23)堆叠设置;换热盘(23)之间设置间距保持板(27);相邻两层换热盘(23)之间相对旋转45度~90度;相邻两层换热盘(23)相连通。2. A coil heat exchanger according to claim 1, characterized in that: it has at least two heat exchange disks (23); the heat exchange disks (23) are stacked; the heat exchange disks (23) A distance maintaining plate (27) is arranged between them; two adjacent layers of heat exchange disks (23) are relatively rotated by 45 degrees to 90 degrees; the two adjacent layers of heat exchange disks (23) are connected. 3.根据权利要求2所述的一种盘管式换热器,其特征是:所述上层换热盘(23)相对下层换热盘(23),顺时针旋转90度。3. The coil heat exchanger according to claim 2, characterized in that: the upper heat exchange plate (23) rotates 90 degrees clockwise relative to the lower heat exchange plate (23). 4.根据权利要求2所述的一种盘管式换热器,其特征是:所述上层换热盘(23)相对下层换热盘(23),逆时针旋转90度。4. The coil heat exchanger according to claim 2, characterized in that: the upper heat exchange plate (23) rotates 90 degrees counterclockwise relative to the lower heat exchange plate (23). 5.根据权利要求2所述的一种盘管式换热器,其特征是:所述换热罩包括筒体(11)、发散罩(13)和集气罩(12);换热盘(23)设置于筒体(11)内;发散罩(13)设置于筒体(11)下端;发散罩(13)直径,由下至上逐渐变大;烟气入口设置于发散罩上;集气罩(12)设置于筒体(11)上端;集气罩(12)直径,由下至上逐渐变小;烟气出口设置于集气罩(12)上。5. A coil heat exchanger according to claim 2, characterized in that: the heat exchange cover includes a cylinder (11), a diverging cover (13) and a gas collection cover (12); (23) is arranged in the cylinder body (11); the divergence cover (13) is arranged at the lower end of the cylinder body (11); the diameter of the divergence cover (13) gradually increases from bottom to top; the smoke inlet is arranged on the divergence cover; The gas hood (12) is arranged on the upper end of the barrel (11); the diameter of the gas collecting hood (12) gradually decreases from bottom to top; the flue gas outlet is arranged on the gas collecting hood (12). 6.根据权利要求5所述的一种盘管式换热器,其特征是:所述烟气入口和烟气出口上设置有法兰盘。6. A coil heat exchanger according to claim 5, characterized in that: flanges are provided on the flue gas inlet and flue gas outlet.
CN202223074803.0U 2022-11-18 2022-11-18 Coiled pipe type heat exchanger Active CN219301352U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202223074803.0U CN219301352U (en) 2022-11-18 2022-11-18 Coiled pipe type heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202223074803.0U CN219301352U (en) 2022-11-18 2022-11-18 Coiled pipe type heat exchanger

Publications (1)

Publication Number Publication Date
CN219301352U true CN219301352U (en) 2023-07-04

Family

ID=86983350

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202223074803.0U Active CN219301352U (en) 2022-11-18 2022-11-18 Coiled pipe type heat exchanger

Country Status (1)

Country Link
CN (1) CN219301352U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118089439A (en) * 2024-04-09 2024-05-28 北京航空航天大学 An Archimedean spiral air-fuel heat exchanger for an aviation gas turbine engine
CN119420283A (en) * 2024-11-01 2025-02-11 东莞市正康电子有限公司 Liquid cooling plate, liquid cooling system and liquid cooling plate manufacturing method for photovoltaic heat dissipation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN118089439A (en) * 2024-04-09 2024-05-28 北京航空航天大学 An Archimedean spiral air-fuel heat exchanger for an aviation gas turbine engine
CN119420283A (en) * 2024-11-01 2025-02-11 东莞市正康电子有限公司 Liquid cooling plate, liquid cooling system and liquid cooling plate manufacturing method for photovoltaic heat dissipation

Similar Documents

Publication Publication Date Title
CN219301352U (en) Coiled pipe type heat exchanger
CN104251629B (en) Heat exchanger and there is its gas heater
CN219200108U (en) A coiled tube condensing heat exchanger
CN104296546B (en) A kind of cement rotary kiln bootstrap system that smoke separator is set
CN103411454A (en) A tubular heat exchanger with staggered arrangement of convex corrugated tubes
CN110057214A (en) A kind of heat-exchanger rig
CN207866055U (en) A kind of cartridge type fin tube type hot-blast heat exchange device
CN114087597B (en) Gap type coil pipe heat conducting oil boiler
CN205090407U (en) Coiled heat exchange device
CN202813773U (en) Heat transfer structure provided with flow guide plate
CN222718736U (en) Heat exchange device, evaporator and condenser
CN106643215B (en) Choked flow type liquid heat-exchanger
CN212361977U (en) Three-coil gas flue gas turbulent flow heat exchange device
CN204100858U (en) Heat exchanger and there is its gas heater
CN103712495A (en) Heat exchange device for recycling flue gas waste heat
CN204227701U (en) A high-efficiency condensing heat exchanger
CN118746204A (en) Spiral multi-channel cooler
CN102278902B (en) Heat exchanger and manufacturing method thereof
CN115127370B (en) A multi-stage shell and tube heat exchanger
CN216770239U (en) Finned tube type condensation heat exchanger for wall-mounted furnace
CN215499606U (en) Composite electric heating device
CN103940276B (en) Exhaust gas inlet device and regenerative heat exchanger containing same
CN207990588U (en) Boiler energy-saving device
CN110567157A (en) Fire tube type condensation heat exchanger
CN206330448U (en) A kind of ring pipe collection bundle heat exchanger

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CP03 Change of name, title or address
CP03 Change of name, title or address

Address after: 611600 Sichuan Province, Chengdu City, Puyang County, Shou'an Street, Xin Yuan Road No. 58, Building 33, Unit 1Building 33, Unit 2

Patentee after: Sichuan Zhuoyi environmental protection and energy saving equipment Co.,Ltd.

Country or region after: China

Address before: 610400 Sichuan Province, Chengdu City, Jintang County, Huakou Town, Energy-saving Avenue No. 99 (within Sichuan Jintang Industrial Park)

Patentee before: Sichuan Zhuoyi environmental protection and energy saving equipment Co.,Ltd.

Country or region before: China