WO2011072470A1 - 一种盘管及具有该盘管的换热器 - Google Patents

一种盘管及具有该盘管的换热器 Download PDF

Info

Publication number
WO2011072470A1
WO2011072470A1 PCT/CN2010/000917 CN2010000917W WO2011072470A1 WO 2011072470 A1 WO2011072470 A1 WO 2011072470A1 CN 2010000917 W CN2010000917 W CN 2010000917W WO 2011072470 A1 WO2011072470 A1 WO 2011072470A1
Authority
WO
WIPO (PCT)
Prior art keywords
tube
coil
side plate
heat exchanger
arc
Prior art date
Application number
PCT/CN2010/000917
Other languages
English (en)
French (fr)
Inventor
沈卫立
Original Assignee
Shen Weili
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 Shen Weili filed Critical Shen Weili
Priority to KR1020127018381A priority Critical patent/KR101710088B1/ko
Priority to EP10836909.1A priority patent/EP2515062B1/en
Priority to JP2012543442A priority patent/JP5680669B2/ja
Priority to US13/515,616 priority patent/US9234711B2/en
Publication of WO2011072470A1 publication Critical patent/WO2011072470A1/zh

Links

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/007—Auxiliary supports for elements
    • F28F9/013—Auxiliary supports for elements for tubes or tube-assemblies
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/08—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag
    • F28D7/082—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being otherwise bent, e.g. in a serpentine or zig-zag with serpentine or zig-zag configuration
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates

Definitions

  • the utility model relates to a coil and a heat exchanger, in particular to a coil and a heat exchanger having the same.
  • Heat exchangers also known as heat exchangers, are devices that exchange heat between hot and cold fluids.
  • heat exchangers are widely used as heaters, coolers, and condensers. According to the heat exchange between the hot and cold fluids, the heat exchangers can be divided into three categories: 1 wall heat exchanger 2 contact heat exchanger 3 regenerative heat exchanger.
  • the wall-mounted heat exchanger is divided into a tube heat exchanger according to the structure of the heat transfer surface (such as a shell-and-tube heat exchanger, a coil heat exchanger, a casing heat exchanger, a spray heat exchanger, Air coolers, etc.) and plate heat exchangers (such as spiral plate heat exchangers, plate heat exchangers, plate-fin heat exchangers, etc.).
  • the above-mentioned shell-and-tube heat exchanger is also called a tube-and-tube heat exchanger, and is a partition-type heat exchanger that is closed on the wall surface of the tube bundle in the casing as a heat transfer surface, and performs two kinds of heat and cold fluids, one in The flow inside the tube is called the tube-flow fluid; the other is flowing outside the tube, called the shell-side fluid.
  • the heat exchanger has a simple structure and reliable operation, can be manufactured by various structural materials (mainly metal materials), can be used under high temperature and high pressure, and is the most widely used type at present.
  • Cid patent document CN2524163Y discloses a counterflow shell-and-tube heat exchanger comprising a rectangular casing, a coil and an electric heater placed in the casing, a liquid separator and a gas collecting box connected to the inlet and outlet of the coil, and a casing Upper water inlet, water outlet, descaling rinse port, drain port, temperature sensor mount, spoiler and fork plate bracket.
  • the inside of the rectangular casing is a serpentine water flow passage separated by a baffle.
  • the inner wall surface of the water flow passage is provided with a spoiler and a fork plate bracket, and the refrigerant side passage has a 180-degree serpentine coil.
  • the adjacent refrigerant side passages of the countercurrent shell-and-tube heat exchanger of the prior art are parallel to each other and have a certain length, and the semicircular connecting tubes are adjacent to the upper and lower sides at both ends of the refrigerant side passage.
  • the refrigerant side passages are connected to form a serpentine (U-shaped) coil.
  • an internal thread or a micro-rib structure is often provided in the coil, so that the coil has a minimum bending radius so that the internal thread or the micro-rib structure does not deform.
  • the technical problem to be solved by the present invention is that the coil in the prior art is seriously wasted due to the limitation of the bending radius, and the structure is not compact, and the heat exchanger having the above coil is in the unit.
  • the coil of the present invention is composed of a plurality of ortho-shaped tubes in which the head end and the tail end are successively connected to form a continuous bending line, and the head end and the tail end of the arc tube are formed.
  • the angle between the spanning is greater than 180 degrees, the leading end and the trailing end of the solitary tube are on the same plane, and the center line of the junction of the two adjacent arc tubes has a common tangent point or two adjacent The center line of the arc tube connection is connected to the center line of the straight tube.
  • the angle between the leading end and the trailing end of the arc tube is 186 to 286 degrees.
  • a heat exchanger comprising an outer casing, a frame surrounded by four sides, and a first side plate and a second side plate sealingly connecting the remaining two opposite faces of the frame body to form a sealed space in the outer casing; a liquid pipe and a gas collecting pipe, wherein the liquid dividing pipe and the gas collecting pipe are respectively formed with a liquid separating hole and a gas collecting hole, and the liquid dividing pipe and the gas collecting pipe are respectively sealed through a liquid dividing pipe on the outer casing a mounting hole and the gas collecting pipe mounting hole, penetrates into the inside of the outer casing; and - a coil placed in the outer casing, one end of the coil is connected to the liquid dividing hole, and the other end of the coil is a gas collecting hole connection;
  • the coil tube is composed of a plurality of arc-shaped tubes whose leading ends and tail ends are successively connected to form a continuous curved line, and the angle between the leading end and the trailing end of the arc-shaped tube spans more than 180 degrees, the arc
  • the bus bars of the flow guiding device are perpendicular to the first side plate and/or respectively The second side panel is described.
  • the flow guiding device cooperating with a plurality of the arc tubes on the same side of the line connecting the leading end and the trailing end of the arc tube is formed on the first side plate, and the remaining flow guiding device is formed in the Said second side panel.
  • the flow guiding device is composed of a plurality of guiding columns, the guiding column is composed of a guiding cylinder and a connecting wall, the guiding cylinder is matched with the braided tube, and the connecting wall is away from one end of the guiding cylinder A circular arc transition is provided which is matched with the adjacent arc tube.
  • the frame is detachable from the first side plate.
  • the second side panel and the frame are also detachable.
  • a bolted connection is formed between the first side panel and/or the second side panel and the frame body.
  • the sealing of the liquid separation tube and the liquid separation tube mounting hole is completed by injection molding integrally with the first side plate through a liquid separation tube connection plate that is sealingly connected with the liquid separation tube; the gas collection tube and the gas collection tube.
  • the sealing of the collecting pipe mounting hole is completed by injection molding integrally with the first side plate through a gas collecting pipe connecting plate which is sealedly connected to the collecting pipe.
  • a plurality of single-layer single-row coils are connected in series on the same plane by a straight pipe to form a single-layer multi-row coil, and the two ends are connected to the liquid-discharging hole and the gas-collecting hole.
  • the single-layer multi-row coil is formed by multi-layered multi-row coils in a direction perpendicular to the single-layer multi-row coil, and is respectively formed with a plurality of the liquid-distributing holes and a plurality of the gas-collecting holes. A corresponding connection.
  • the coil is adopted by The plurality of leading ends and the trailing ends are sequentially connected to form a continuous curved line of a solitary tube, and the angle between the leading end and the trailing end of the arcuate tube spans more than 180 degrees, preferably between the leading end and the trailing end of the curved tube
  • the angle of the span is 186 - 286 degrees
  • the center line of the adjacent two arc tube joints has a common tangent point or the center line of the adjacent two solitary tube joints is tangent to the center line of the straight tube
  • the coil length of the coil of the above structure is extended as long as possible within the minimum bending radius, thereby ensuring that the internal thread or the rib structure in the guilloche tube is not deformed, and at the same time saving space as much as possible, and having a compact structure, therefore,
  • the heat exchanger of the coil has a small volume, and the number of coils per unit volume is large, and the heat exchange
  • a flow guiding device that cooperates with the coil is formed on the first side plate and/or the second side plate, and a bus bar of the flow guiding device
  • the guides are respectively perpendicular to the first side panel and/or the second side panel, preferably a plurality of the orphan tubes on the same side of the line connecting the head end and the tail end of the arc tube a flow device formed on the first side plate, the remaining flow guiding device being formed on the second side plate, and the first flow guiding device is composed of a plurality of flow guiding columns, the guiding column is composed of a flow guiding cylinder and a connecting wall, wherein the guiding cylinder cooperates with the arc tube, and one end of the connecting wall away from the guiding cylinder is provided with a circular arc transition with the adjacent arc tube, the second guiding
  • the flow device has the same arrangement as the first flow guiding device; the shell fluid flows in the flow guiding device, increases the disturbance to the shell-side fluid, avoids
  • the casing is welded to the coil after being installed in the coil. Therefore, the coil cannot be removed from the casing, and the scale or other dirt may not be timely after being used for a period of time. Clearing, thereby affecting the heat exchange efficiency between the coil and the shell-side fluid, and the present invention places the first side panel and/or the second side panel with the frame in the heat exchanger Provided as a detachable structure, preferably, the frame body is bolted to the first side plate and/or the second side plate, and therefore, the coil in the heat exchanger of the present invention It can be easily removed from the housing to facilitate the removal of scale or other dirt on the coil, and then disassembled and then installed.
  • the sealing of the liquid separation tube and the liquid separation tube mounting hole is through a liquid separation tube connection plate and the first side which are sealed and connected with the liquid separation tube
  • the plate injection molding is completed integrally;
  • the sealing of the gas collecting pipe and the collecting pipe mounting hole is completed by injection molding integrally formed with the first side plate through a gas collecting pipe connecting plate which is sealed and connected with the gas collecting pipe, thereby ensuring liquid separation Tube
  • the sealing effect of the collecting pipe and the first side plate is good, and the sealing property is not affected by the disassembly of the coil and the casing.
  • a plurality of the coils are arranged in an array in a horizontal and/or vertical direction, and are respectively connected to the liquid separation holes and the gas collection holes one by one, the coils
  • the scalability is good, and the heat exchange area can be increased or decreased according to customer needs.
  • FIG. 1 is a schematic structural view of the coil of the present invention
  • FIG. 2 is a front view of the heat exchanger of the present invention.
  • FIG. 3 is a top view of the heat exchanger of the present invention.
  • Figure 4 is a cross-sectional view taken along line A-A of Figure 3;
  • Figure 5 is a schematic view of a flow guiding device of the heat exchanger of the present invention.
  • Figure 6 is a cross-sectional view of the heat exchanger of the present invention with the flow guiding device taken along line AA of Figure 3;
  • Figure 7 is the liquid dividing tube and the gas collecting tube of the heat exchanger of the present invention and the first A schematic view of the integration of the side plates;
  • Figure 8 is a schematic view showing a single-layer single-row coil having a common point of cut in the center line of the two arc-shaped pipe joints adjacent to the coil of the heat exchanger of the present invention
  • FIG. 9 is a schematic view of a single-layer multi-row coil of the heat exchanger of the present invention.
  • Figure 10 is a schematic view of a liquid separation tube or a gas collection tube of the heat exchanger of the present invention.
  • the reference numerals in the figures are: 1-coil, 11-single single-row coil, 12-single-layer multi-row coil, 2-noisy tube, 3-shell, 31-first side panel, 32- Two side plates, 33-frame, 34-separate pipe connection plate, 35-collector connection plate, 4-dispensing tube, 41-distribution hole, 5-collector, 51-gear, 6-inlet , 7-outlet, 8-flow guide, 80-flow guide, 801 - guide cylinder, 802-connecting wall, 81-guide busbar, 9-straight, 10-shell path, a- Head end, b-tail.
  • Embodiments Embodiment 1 Embodiments Embodiment 1
  • the arc tube 2 is connected to a continuous bending line, and the angle between the head end a and the tail end b of the arc tube 2 is greater than 180 degrees, and the head end a and the tail end b of the arc tube 2 are in the same
  • the angle between the leading end a and the trailing end b of the arc tube is 186 degrees
  • the center line of the junction of the two adjacent arc tubes 2 and the tube 9 The center line is tangentially connected, that is, the trailing end b and the adjacent head end a are connected by a straight tube tangentially.
  • the bending length of the coil 1 in the minimum bending radius is extended as much as possible, thereby ensuring that the internal thread or the microrib structure in the arc tube 2 is not deformed, and at the same time, space is saved as much as possible, and the structure is compact.
  • the angle spanned between the head and the tail of the solitary tube is the angle that the cross section perpendicular to the center line of the solitary tube spans from the head end a to the tail end b of the track through which it passes.
  • the heat exchanger using the coil 1 described above comprises a casing 3, a liquid separation pipe 4, a gas collecting pipe 5 and a coil pipe 1 (shown in Fig. 2); the casing 3 is surrounded by a frame 33 surrounded by four sides, and The first side plate 31 and the second side plate 32 of the remaining two opposite faces of the frame form a sealed space, and the coil 1 is placed in the outer casing 3.
  • the coil 1 is preferably The first side plate 31 and the second side plate 32 are parallel; in this embodiment, the coil 1 is a single-layer single-row coil, that is, the coil 1 is parallel to the first side plate 31 and There is only one row of coils on the plane of the two side plates 32, and only one layer of coils (shown in FIG.
  • the liquid separation hole 41 is connected to the body, and the other end of the coil 1 is connected to the gas collecting hole 51 provided on the tube body of the gas collecting pipe 5, and the liquid separation pipe 4 and the gas collecting pipe 5 are respectively sealed and passed through.
  • the liquid pipe mounting hole on the outer casing and the gas collecting pipe mounting hole are connected to the outside (see FIGS. 3 and 4).
  • the sealing of the liquid separation tube 4 and the liquid separation tube mounting hole is injection-molded with the first side plate 31 through a liquid separation tube connection plate 34 that is sealingly connected to the liquid separation tube 4
  • the molding is completed;
  • the sealing of the gas collecting pipe 5 and the gas collecting pipe mounting hole is completed by injection molding of the gas collecting pipe connecting plate 35 and the first side plate 31 which are sealed and connected with the gas collecting pipe 5 (see FIG. 7).
  • the single-layer single-row coil 1 in the heat exchanger of the present invention can also be replaced by a multi-layer single-row coil, that is, a plurality of the single-layer single-row coils are arranged in a vertical direction.
  • the rear ends of the multi-layer single-row coil are connected to the liquid-discharging hole 41 and the gas-collecting hole 51; that is, the coil has only one row of coils on the same plane, and is distributed in a direction perpendicular to the coil 1 Several layers of single layer Single row coil (see Figure 7).
  • the outer casing is also provided with a water inlet 6 and a water outlet 7, two kinds of cold and hot fluids for heat exchange, one flowing in the pipe, called a pipe-flow fluid, and the other flowing outside the pipe, called a shell-side fluid.
  • the shell-side fluid flows into the casing of the outer casing 3 through the water inlet 6, flows outside the coil 1, flows out through the water outlet 7, and the pipe-flow fluid flows in through the liquid-dividing pipe 4, and exchanges heat with the shell-side fluid through the coil 1 to realize heat exchange. After the purpose of cooling or heating, it flows out through the collecting pipe 5.
  • the utility model can also be in the above embodiment!
  • On the first side plate 31 and the second side plate 32, a flow guiding device 8 is formed on the first side plate 31 and the second side plate 32, and the flow guiding device 8 is composed of a plurality of guiding columns 80.
  • the flow guiding column 80 is composed of a guiding cylinder 801 and a connecting wall 802.
  • the guiding cylinder 801 is matched with the arc tube 2.
  • the end of the connecting wall 802 away from the guiding cylinder 801 is provided adjacent to the guiding column 802. a circular arc transition of the arc tube 2 (shown in FIG. 5), the arc tube 2 on the same side of the line connecting the leading end a and the trailing end b of the solitary tube (ie, the arc tube)
  • the flow guiding device 8 with the highest point on the same side is formed on the first side plate 31, and the remaining flow guiding device 8 is formed on the second side plate 32; at the first side plate 31 Cooperating with the coil 1 is a first flow guiding device, and the second side plate 32 is matched with the coil 1 to be a second flow guiding device, the first guiding flow
  • the bus bar 81 of the device and the bus bar 81 of the second flow guiding device are perpendicular to the first side plate 31 and the second side plate 32, respectively; that is, the first guide bar passes through the lone tube 2 of the coil 1 bend Forming a space and having a gap with the tube 2
  • the bus bar 81 is a pull-up trajectory in a direction perpendicular to the plane of the first side plate parallel to the plane of the flow guiding column parallel to the plane of the first side plate.
  • the present invention may further be detachable between the frame body 33 and the first side plate 31, and the second side plate 32 and the frame body 33 may be integrally formed on the basis of the above embodiments.
  • a bolt connection between the first side plate 31 and the coil 1 to facilitate the removal of the coil 1 from the housing of the outer casing 3.
  • the present invention can also provide the frame 33 and the above based on the above embodiments.
  • the first side plate 31 and the second side plate 32 are detachable.
  • the first side plate 31 and the coil 1 and the second side plate 32 are connected to the coil 1 by bolts.
  • Embodiment 2 the coil 1 is composed of a plurality of arc-shaped tubes 2 in which the head end a and the tail end b are successively connected to form a continuous curved line, and between the head end a and the tail end b of the arc tube 2 The angle of the span is greater than 180 degrees, and the leading end a and the trailing end b of the arc tube 2 are on the same plane.
  • the angle between the head end a and the trailing end b of the arc tube 2 is preferably 286.
  • the center line of the junction of two adjacent solitary tubes 2 has a common tangent point, that is, the head end a and the tail end b coincide (see FIG. 8).
  • the single-row multilayer coil described in Embodiment 1 is replaced by a multi-row multilayer coil, that is, a plurality of single-layer single-row coils 11 are connected in series on the same plane to form a single-layer multi-row disc.
  • a multi-layer multi-row coil is formed, and the multi-row multi-row coil respectively has the liquid-discharging hole 41 corresponding to each layer and the corresponding set
  • the air holes 51 - corresponding connections (shown in FIG. 10 ), in the present embodiment, it is preferable to connect the single-layer single-row coils 11 with a straight tube 9 , thereby connecting the single-layer single-row coils 11 in a single layer and multiple columns.
  • the coil 12 (shown in Figure 9) can further increase the heat exchange area of the heat exchanger.
  • a flow guiding device 8 that cooperates with the coil 1 is formed on the first side plate 31 or the second side plate 32, that is, all the flow guiding devices 8 are formed on the first side plate 31 or the first side plate
  • the purpose of the utility model can also be implemented on the two side panels 32, that is, the flow guiding device 8 and the coil 1 together form the shell path 10 .
  • the heat exchange area may be increased or decreased according to customer needs, and the arrangement of the coils may be changed.
  • Other variations or modifications of the various forms may be made by those skilled in the art. There is no need and no way to exhaust all of the implementations. The obvious changes or variations derived therefrom are still within the scope of protection created by the present invention.

Landscapes

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

Description

一种盘管及具有该盘管的换热器 技术领域
本实用新型涉及一种盘管及换热器，具体地说是一种盘管及具有该盘管 的换热器。 背景技术
换热器又称热交换器， 是冷热流体间进行换热的设备， 在化工、 石油、 动力、 食品等部门， 换热器广泛用作加热器、 冷却器和冷凝器。 才艮据冷热流 体间的换热方式，换热器可分为三类： ①间壁式换热器②接触式换热器③蓄 热式换热器。 其中， 间壁式换热器按传热面的结构形式， 又分为管式换热器 (如管壳式换热器、 蛇管换热器、 套管换热器、 喷淋式换热器、 空气冷却器 等）和板式换热器（如螺旋板式换热器、 平板式换热器、 板翅式换热器等）。 上述管壳式换热器又称列管式换热器，是以封闭在壳体中管束的壁面作 为传热面的间壁式换热器， 进行换热的冷热两种流体， 一种在管内流动， 称 为管程流体； 另一种在管外流动， 称为壳程流体。 这种换热器结构较简单， 操作可靠， 可用各种结构材料（主要是金属材料）制造， 能在高温、 高压下 使用， 是目前应用最广的一种类型。 中国专利文献 CN2524163Y公开了一种逆流管壳式换热器， 包括矩形壳 体，放置在壳体内的盘管和电加热器，与盘管进出口连接的分液器和集气盒， 壳体上的进水口、 出水口、 除垢冲洗液口、 排污口、 温度传感器安装座、 扰 流器和叉流板支架。矩形壳体内部由导流隔板分隔出的蛇形水流通道， 水流 通道的内壁面安装有扰流器和叉流板支架，制冷剂侧通道为具有 180度蛇形 盘管。即该现有技术中所述逆流管壳式换热器的相邻制冷剂侧通道之间相互 平行并具有一定的长度，在制冷剂侧通道的两端以半圓连接管与上下相邻的 制冷剂側通道连接， 形成蛇形 （U形）盘管。 但是， 因管程流体.在盘管申流 动， 为了提高换热效率， 常在盘管内设置内螺纹或微肋结构， 为使内螺紋或 微肋结构不变形， 因此该盘管存在最小弯曲半径， 并尽量避免多次弯曲， 由 此导致盘管空间浪费严重， 即在单位体积内所述盘管数量少， 单位体积内的 换热面积小， 不紧凑， 结果导致具有现有技术所述盘管的换热器体积变大， 热系数较小 , 进而导致现有技术所述换热器的换热效率不高。 实用新型内容 为此，本实用新型所要解决的技术问题在于现有技术中的盘管因弯曲半 径的限制导致所述盘管空间浪费严重， 结构不紧凑， 具有上述盘管的换热器 在单位体积内盘管数量少， 单位体积内的换热面积小， 体积大； 进而提供一 种尽可能减小空间浪费的具有结构紧凑、体积小， 换热效率高的盘管及具有 该盘管的换热器。 为解决上述技术问题， 本实用新型的一种盘管， 所述盘管由若干个首端 和尾端依次相接成连续弯曲线的孤状管组成 ,所述弧状管的首端和尾端之间 跨越的角度大于 180度， 所述孤状管的首端和尾端在同一平面上，相邻的两 个所述弧状管连接处的中心线有公共切点或相邻的两个所述弧状管连接处 的中心线与一直管中心线相切连接。 所述弧状管的首端和尾端之间跨越的角度为 186 ~ 286度。 一种换热器， 包括外壳， 由四面包围的框体、 及密封连接所述框体剩余 两个相对面的第一侧板和第二侧板組成， 使所述外壳内形成密封空间； 分液管和集气管，所述分液管和所述集气管上分别成形有分液孔和集气 孔，所述分液管和所述集气管分别密封的穿过所述外壳上的分液管安装孔和 所述集气管安装孔， 深入所述外壳内部； 及 - 放置于所述外壳内的盘管， 所述盘管一端与所述分液孔连接， 所述盘管 另一端与所述集气孔连接； 所述盘管由若干个首端和尾端依次相接成连续弯曲线的弧状管组成，所 述弧状管的首端和尾端之间跨越的角度大于 180度，所述弧状管的首端和尾 端在同一平面上， 相邻的两个所述弧状管 （2 )连接处的中心线有公共切点 或相邻的两个所述弧状管连接处的中心线与一直管中心线相切连接。 所述孤状管的首端和尾端之间跨越的角度为 186 ~ 286度。 所述盘管与所述第一侧板及所述第二侧板平行。
在所述第一侧板和 /或所述第二侧板上成形有与所述盘管配合的导流装 置， 所述导流装置的母线分别垂直于所述第一侧板和 /或所述第二侧板。
与在所述弧状管的首端和尾端连线的同一侧的若干个所述弧状管配合 的所述导流装置成形在所述第一侧板， 余的所述导流装置成形在所述第二 侧板上。
所述导流装置由若干个导流柱组成，所述导流柱由导流圆柱和连接壁组 成， 所述导流圆柱与所述瓠状管配合， 所述连接壁远离导流圆柱的一端设有 与相邻所述弧状管配合的圆弧过渡。 所述框体与所述第一侧板之间可拆卸。
所述第二侧板与所述框体之间也可拆卸。 所述第一侧板和 /或所述第二侧板与所述框体之间采用螺栓连接。 所述分液管与所述分液管安装孔的密封是通过与所述分液管密封连接 的分液管连接板与所述第一侧板注塑一体成型完成；所述集气管与所述集气 管安装孔的密封是通过与所述集气管密封连接的集气管连接板与所述第一 側板注塑一体成型完成。
若干单层单列盘管在同一平面上通过直管串联形成单层多列盘管后两 端与所述分液孔和所述集气孔连接。 所述单层多列盘管在垂直于所述单层多列盘管方向上多层排列后形成 多层多列盘管后分别与若干个所述分液孔和若干个所述集气孔一一对应连 接。 本实用新型的上述技术方案相比现有技术具有以下优点， 首先， 本实用新型所述盘管及具有该盘管的换热器中， 所述盘管采用由 若干个首端和尾端依次相接成连续弯曲线的孤状管组成，所述弧状管首端和 尾端之间跨越的角度大于 180度，优选所述弧状管首端和尾端之间跨越的角 度为 186 - 286度， 相邻的两个所述弧状管连接处的中心线有公共切点或相 邻的两个所述孤状管连接处的中心线与一直管中心线相切连接，由上述结构 的盘管在最小弯曲半径内弯曲弧长尽可能延长，既保证瓜状管内的内螺纹或 敖肋结构不变形， 同时又尽可能的节约空间， 结构紧凑， 因此， 具有该盘管 的换热器体积小， 在单位体积内盘管数量多， 换热效率高。
第二， 本实用新型所述换热器中， 在所述第一侧板和 /或所述第二侧板 上成形有与所述盘管配合的导流装置，所述导流装置的母线分别垂直于所述 第一侧板和 /或所述第二侧板， 优选与在所述弧状管的首端和尾端连线的同 一侧的若干个所述孤状管配合的所述导流装置成形在所述第一侧板，其余的 所述导流装置成形在所述第二侧板上，且所述第一导流装置由若干个导流柱 组成， 所述导流柱由导流圆柱和连接壁组成， 所述导流圆柱与所述弧状管配 合， 所述连接壁远离导流圆柱的一端设有与相邻所述弧状管配合的圆弧过 渡， 所述第二导流装置与所述第一导流装置具有相同设置； 壳程流体在导流 装置中流动， 增加对壳程流体的扰动， 避免壳程局部流体滞留现象， 增强换 热效杲。 第三， 现有技术中壳体在装入盘管后与盘管都焊接在一起， 因此， 盘管 不能从壳体中拆卸出来，在使用一段时间后会出现水垢或其他污垢后不能及 时对其进行清除， 因而影响盘管与壳程流体间的热交换效率， 而本实用新型 在所述换热器中将所述第一侧板和 /或所述第二侧板与所述框体之间设置为 可拆卸结构 , 优选所述框体与所述第一侧板和 /或所述第二侧板之间采用螺 栓连接， 因此， 本实用新型所述的换热器中的盘管能很方便的从壳体中拆卸 出来， 以利于对盘管上的水垢或其他污垢进行清除， 也便拆卸后再安装。
第四， 本实用新型所述换热器中， 所述分液管与所述分液管安装孔的密 封是通过与所述分液管密封连接的分液管连接板与所述第一侧板注塑一体 成型完成；所述集气管与所述集气管安装孔的密封是通过与所述集气管密封 连接的集气管连接板与所述第一侧板注塑一体成型完成， 因此， 保证分液管 和集气管与第一侧板的密封效果好， 其密封性不受盘管与壳体拆卸的影响。 第五， 本实用新型所述换热器中， 若干所述盘管在水平和 /或垂直方向 上阵列排布， 并分別与所述分液孔和所述集气孔一一对应连接， 盘管的可扩 展性好， 可根据客户需要增加或减少换热面积。 附图说明 为了使本实用新型的内容更容易被清楚的理解，下面根据本实用新型的 具体实施例并结合附图， 对本实用新型作进一步详细的说明， 其中
图 1 是本实用新型所述盘管的结构示意图；
图 2 是本实用新型所述换热器主视图；
图 3 是本实用新型所述换热器俯视图；
图 4 是图 3的 A-A剖视图；
图 5 是本实用新型所述换热器的导流装置示意图；
图 6 是本实用新型带导流装置的所述换热器的图 3的 A-A剖视图； 图 7 是本实用新型所述换热器中所述分液管和所述集气管与所述第一 側板融注一体成型的示意图；
图 8 是本实用新型所述换热器的盘管相邻的两个所述弧状管连接处的 中心线有公共切点的单层单列盘管示意图；
图 9 是本实用新型所述换热器的单层多列盘管示意图；
图 10是本实用新型所述换热器的分液管或集气管的示意图；
图中附图标记表示为： 1-盘管， 11-单层单列盘管， 12—单层多列盘管， 2 -孤状管， 3-外壳， 31-第一侧板， 32-第二侧板， 33-框体， 34-分液管连接 板， 35-集气管连接板， 4-分液管， 41-分液孔， 5-集气管， 51-集气孔， 6- 进水口， 7-出水口， 8-导流装置， 80-导流柱， 801 -导流圆柱， 802-连接壁， 81-导流装置的母线， 9-直管， 10-壳程通道， a-首端， b-尾端。 实施方式 实施例 1
本实施例中所述的一种盘管 1, 所述盘管 1由若干个首端 a和尾端 b依 次相接成连续弯曲线的弧状管 2组成，所述弧状管 2的首端 a和尾端 b之间 跨越的角度大于 180度， 所述弧状管 2的首端 a和尾端 b在同一平面上，在 本实施例中优选所述弧状管的首端 a和尾端 b之间跨越的角度为 186度，相 邻的两个所述弧状管 2连接处的中心线与一直管 9的中心线相切连接，即尾 端 b和相邻的首端 a通过一直管相切连接。 因此，盘管 1在最小弯曲半径内 弯曲弧长尽可能延长， 既保证弧状管 2内的内螺紋或微肋结构不变形， 同时 又尽可能的节约空间， 结构紧凑。 其中， 所述孤状管首尾之间跨越的角度即 为与所述孤状管中心线垂直的横截面从首端 a至其所经过的轨迹的尾端 b所 跨越的角度。
采用上述盘管 1的换热器， 包括外壳 3、 分液管 4、 集气管 5和盘管 1 (见图 2所示）； 所述外壳 3由四面包围的框体 33、 及与所述框体剩余两个 相对面密封连接的第一侧板 31和第二侧板 32组成一个密封空间，所述盘管 1放置于所述外壳 3内， 本实施例中优选所述盘管 1与所述第一侧板 31及 第二侧板 32平行； 本实施例中， 所述盘管 1为单层单列盘管， 即所述盘管 1在平行于所述第一侧板 31及第二侧板 32平面上只有一列盘管， 在垂直于 所述盘管的方向上只有一层盘管 （见图 1所示）， 所述盘管 1的一端与所述 分液管 4的管身上设置的分液孔 41连接， 所述盘管 1的另一端与所述集气 管 5的管身上设置的集气孔 51连接， 所述分液管 4和所述集气管 5分别密 封的穿过外壳上的分液管安装孔和所述集气管安装孔与外界连接（见图 3及 图 4所示）。 本实施例中优选， 所述分液管 4与所述分液管安装孔的密封是 通过与所述分液管 4密封连接的分液管连接板 34与所述第一侧板 31注塑一 体成型完成；所述集气管 5与所述集气管安装孔的密封是通过与所述集气管 5密封连接的集气管连接板 35与所述第一侧板 31注塑一体成型完成（见图 7所示）。 作为可变换的实施例，本实用新型所述换热器中的单层单列盘管 1也可 替换为多层单列盘管，即若干所述单层单列盘管在垂直方向上阵列排布形成 多层单列盘管后两端与所述分液孔 41和所述集气孔 51连接；也即所述盘管 在同一平面上只有一列盘管，在垂直于所述盘管 1的方向分布有若干层单层 单列盘管 （见图 7所示）。 外壳上还设置有进水口 6和出水口 7 , 进行换热的冷热两种流体， 一种 在管内流动， 称为管程流体； 另一种在管外流动， 称为壳程流体。 壳程流体 通过进水口 6流入外壳 3的壳体内， 在盘管 1外流动， 经出水口 7流出， 管 程流体经分液管 4流入， 经过盘管 1与壳程流体进行热交换， 实现制冷或制 热的目的后经集气管 5流出。 本实用新型还可在上述实施例的！¾¾上， 在所述第一側板 31和所述第 二侧板 32上成形有与所述盘管 1 g合的导流装置 8， 所述导流装置 8由若 干个导流柱 80组成， 所述导流柱 80由导流圆柱 801和连接壁 802组成， 所 述导流圆柱 801与所述弧状管 2配合， 所述连接壁 802的远离导流圆柱 801 的一端设有与相邻所述弧状管 2配合的圆弧过渡（见图 5所示）， 与在所述 孤状管的首端 a和尾端 b连线的同一侧的所述弧状管 2 (也即所述弧状管最 高点在同一侧）配合的所述导流装置 8成形在所述第一側板 31， 其余的所 述导流装置 8成形在所述第二侧板 32上；在所述第一侧板 31上成形的与所 述盘管 1配合的为第一导流装置， 在所述第二侧板 32上成形的与所述盘管 1配合的为第二导流装置， 所述第一导流装置的母线 81和所述第二导流装 置的母线 81分别垂直于所述第一侧板 31和所述第二侧板 32; 即第一导流 柱穿过盘管 1的孤状管 2弯曲形成的空间并与 状管 2存有间隙；第二导流 柱穿过与第一侧板 31穿过的孤状管 2相邻的孤状管 2弯曲形成的空间， 并 与该弧状管 2存有间隙， 第一导流装置、 第二导流装置和盘管 1一起形成壳 程通道 10 (见图 6所示）。 其中， 所述母线 81为平行于第一侧板平面的导 流柱截平面在垂直于第一侧板平面的方向上的拉升轨迹。 此外， 本实用新型还可在上述实施例的基础上， 设置所述框体 33与所 述第一侧板 31之间可拆卸， 所述第二侧板 32与所述框体 33—体成型， 为 了便于将盘管 1从外壳 3壳体中拆卸出来， 本实施例中优选第一侧板 31与 盘管 1之间采用螺栓连接， 便于盘管 1从外壳 3的壳体中拆卸出来， 以利于 对盘管 1上的水垢或其他污垢进行清除。
进一步， 本实用新型还可在上述实施例的基础上， 设置所述框体 33与 所述第一侧板 31和所述第二侧板 32之间可拆卸，本实施例中优选第一侧板 31与盘管 1及第二侧板 32与盘管 1之间采用螺栓连接。 实施例 2 本实施例中，所述盘管 1由若干个首端 a和尾端 b依次相接成连续弯曲 线的弧状管 2组成， 所述弧状管 2首端 a和尾端 b之间跨越的角度大于 180 度， 所述弧状管 2的首端 a和尾端 b在同一平面上， 在本实施例中优选所述 弧状管 2首端 a和尾端 b之间跨越的角度在 286度，相邻的两个所述孤状管 2连接处的中心线有公共切点， 即首端 a和尾端 b重合（见图 8所示）。 在上述实施例的^出上，将实施例 1中所述的单列多层盘管替换为多列 多层盘管， 即将若干单层单列盘管 11在同一平面上串联形成单层多列盘管 12 后在垂直于所述盘管的方向上多层分布形成多层多列盘管， 所述多层多 列盘管分别与每层对应的所述分液孔 41和对应的所述集气孔 51——对应连 接（见图 10所示）， 在本实施例中优选单层单列盘管 11之间采用直管 9连 接， 由此， 将单层单列盘管 11 串联成单层多列盘管 12 (见图 9所示）， 可 进一步增加换热器的换热面积。 进一步， 在所述第一侧板 31或所述第二侧板 32上成形有与所述盘管 1 配合的导流装置 8， 即所有导流装置 8都成形在第一侧板 31或第二侧板上 32 , 也可实施本实用新型的目的， 即导流装置 8和盘管 1一起形成壳程通道 10。 显然， 上述实施例仅仅是为清楚地说明所作的举例， 而并非对实施方式 的限定， 也可根据客户需要增加或减少换热面积， 变更盘管的排布形式。 对 于所属领域的普通技术人员来说，在上述说明的 出上还可以做出其它不同 形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。 而由此所 引伸出的显而易见的变化或变动仍处于本实用新型创造的保护范围之中。

Claims

权 利 要 求 书
1. 一种盘管， 所述盘管 （ 1 ) 由若干个首端 （ a )和尾端（ b)依次相接 成连续弯曲线的弧状管（ 2 )组成， 其特征在于， 所述弧状管（ 2 )的首端（ a ) 和尾端（b)之间跨越的角度大于 180度， 所述弧状管 （2) 的首端 （a)和尾 端 （b)在同一平面上， 相邻的两个所述弧状管 （2)连接处的中心线有公共 切点或相邻的两个所述孤状管 （2)连接处的中心线与一直管 （9) 中心线相 切连接。
2. 根据权利要求 1所述盘管，其特征在于，所述弧状管（ 2 )的首端（ a ) 和尾端 (b)之间跨越的角度为 186 - 286度。
3. —种换热器， 包括外壳（3)， 由四面包围的框体（33)、 及密封连接 所述框体（ 33 )剩余两个相对面的第一侧板（ 31 )和第二侧板（ 32 )组成， 使所述外壳（3) 内形成密封空间； 分液管 （4)和集气管 （5)， 所述分液管 （4)和所述集气管 （5)上分 別成形有分液孔（ 41 )和集气孔（ 51 )， 所述分液管（ 4 )和所述集气管（ 5 ) 分别密封的穿过所迷外壳 （3)上的分液管安装孔和所述集气管安装孔， 深 入所述外壳（3) 内部； 及 放置于所述外壳（ 3 ) 内的盘管（ 1 )， 所述盘管（ 1 )一端与所述分液孔 (41)连接， 所述盘管 （1) 另一端与所述集气孔（51)连接；
其特征在于， 所述盘管 （1) 由若干个首端 （a)和尾端 （b)依次相接 成连续弯曲线的弧状管（ 2 )组成， 所述弧状管（ 2 )的首端（ a )和尾端（ b ) 之间跨越的角度大于 180度， 所述瓜状管 （2) 的首端 （a)和尾端 （b)在 同一水平面上， 相邻的两个所述弧状管 （2)连接处的中心线有公共切点或 相邻的两个所述弧状管（ 2 )连接处的中心线与一直管（ 9 )中心线相切连接。
4. 根据权利要求 3所述换热器， 其特征在于， 所述弧状管 （2)的首端 (a)和尾端 （b)之间跨越的角度为 186 - 286度。
5. 根据权利要求 3或 4所述盘管， 其特征在于， 所述盘管与所述第一 侧板（ 31 )及所述第二侧板（ 32 )平行。
6. 根据权利要求 5所述换热器， 其特征在于， 在所述第一侧板 (31) 和 /或所述第二侧板（ 32 )上成形有与所述盘管 （ 1 )配合的导流装置 （ 8 )， 所述导流装置 （ 8 ) 的母线（ 81 )分别垂直于所述第一侧板（ 31 ) 和 /或所述 第二侧板（ 32 )。
7. 根据权利要求 6所述换热器， 其特征在于， 与在所述弧状管（ 2 )的 首端 )和尾端 （b)连线的同一侧的若干个所述孤状管（2)配合的所述导 流装置（ 8 )成形在所述第一侧板（ 31 )， 其余的所述导流装置（ 8 )成形在所 述第二侧板（ 32 )上。
8. 根据权利要求 7所述换热器， 其特征在于， 所述导流装置（8) 由若 干个导流柱 ( 80 )组成， 所述导流柱（ 80 )由导流圆柱（ 801 )和连接壁（ 802 ) 组成， 所述导流圆柱（801)与所述 I 状管 （2)配合， 所述连接壁（ 802 )远 离导流圓柱（801) 的一端设有与相邻所述孤状管 （2)配合的圆弧过渡。
9. 根据权利要求 8所述换热器， 其特征在于， 所述框体（33)与所述 第一侧板 ( 31 )之间可拆卸。
10. 根据权利要求 9所述换热器， 其特征在于， 所迷第二侧板（32) 与 所述框体（ 33 )之间也可拆卸。
11. 根据权利要求 10所述换热器， 其特征在于， 所述第一侧板（31)和 /或所述第二侧板 ( 32 )与所述框体（ 33 )之间采用螺栓连接。
12. 根据权利要求 11 所述换热器， 其特征在于， 所述分液管 （4)与所 述分液管安装孔的密封是通过与所述分液管 （4) 密封连接的分液管连接板
( 34 )与所述第一侧板（ 31 )注塑一体成型完成； 所述集气管 （ 5 ) 与所述集 气管安装孔的密封是通过与所述集气管 （5) 密封连接的集气管连接板（35) 与所述第一侧板（31)注塑一体成型完成。
13. 根据权利要求 12所述管壳式换热器， 其特征在于， 若干单层单列盘 管 （11)在同一平面上通过直管（9) 串联形成单层多列盘管 （12)后两端与 所述分液孔 ( 41 )和所述集气孔（ 51 )连接。
14. 才艮据权利要求 13所述管壳式换热器， 其特征在于， 所述单层多列盘 管 （12)在垂直于所述单层多列盘管 （12) 方向上多层排列后形成多层多列 盘管后分别与若干个所述分液孔（41)和若干个所述集气孔（51)—一对应 连接。
PCT/CN2010/000917 2009-12-14 2010-06-22 一种盘管及具有该盘管的换热器 WO2011072470A1 (zh)

Priority Applications (4)

Application Number Priority Date Filing Date Title
KR1020127018381A KR101710088B1 (ko) 2009-12-14 2010-06-22 코일 및 코일을 구비하는 열교환기
EP10836909.1A EP2515062B1 (en) 2009-12-14 2010-06-22 Heat exchanger with coil
JP2012543442A JP5680669B2 (ja) 2009-12-14 2010-06-22 折り曲げ管及びその折り曲げ管を有する熱交換器
US13/515,616 US9234711B2 (en) 2009-12-14 2010-06-22 Coil and heat exchanger with the same

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN200910250518.X 2009-12-14
CN200910250518XA CN101738122B (zh) 2009-12-14 2009-12-14 一种盘管及具有该盘管的换热器

Publications (1)

Publication Number Publication Date
WO2011072470A1 true WO2011072470A1 (zh) 2011-06-23

Family

ID=42461905

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2010/000917 WO2011072470A1 (zh) 2009-12-14 2010-06-22 一种盘管及具有该盘管的换热器

Country Status (6)

Country Link
US (1) US9234711B2 (zh)
EP (1) EP2515062B1 (zh)
JP (1) JP5680669B2 (zh)
KR (1) KR101710088B1 (zh)
CN (1) CN101738122B (zh)
WO (1) WO2011072470A1 (zh)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10508867B2 (en) 2015-05-28 2019-12-17 Dometic Sweden Ab Corrosion resistant coaxial heat exchanger assembly

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101738122B (zh) * 2009-12-14 2011-12-21 杭州沈氏换热器有限公司 一种盘管及具有该盘管的换热器
CN102322752B (zh) * 2011-08-01 2013-05-22 西安交通大学 一种换热器
CN103206874A (zh) * 2013-03-28 2013-07-17 尚小女 汽车废气热交换器
CN105485972B (zh) * 2014-09-18 2019-12-03 浙江盾安人工环境股份有限公司 一种微通道换热器及安装方法
CN110433682B (zh) * 2019-08-30 2024-04-12 欧志安 一种承压流体混合装置
DE102020200110A1 (de) * 2020-01-08 2021-07-08 Robert Bosch Gesellschaft mit beschränkter Haftung Kühlvorrichtung

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB122626A (en) * 1918-01-25 Shaw Edward Improvements in and relating to Changing and Transfering Fluid Temperatures.
JPS6484098A (en) * 1987-09-26 1989-03-29 Junkosha Co Ltd Plastic tube heat exchanger
CN2198589Y (zh) * 1994-01-24 1995-05-24 王闰 波浪管换热器
CN2524163Y (zh) 2002-02-01 2002-12-04 李进龙 逆流盘管式换热器
CN101738121A (zh) * 2009-12-14 2010-06-16 杭州沈氏换热器有限公司 盘管及具有该盘管的换热器
CN101738122A (zh) * 2009-12-14 2010-06-16 杭州沈氏换热器有限公司 一种盘管及具有该盘管的换热器

Family Cites Families (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1456255A (en) * 1923-05-22 Apparatus for hkat exchange
FR353403A (fr) * 1905-04-15 1905-09-11 Emile Giraud Radiateur pour moteurs à explosion
US1895720A (en) * 1930-11-26 1933-01-31 P H Ma Girl Foundry And Furnac Boiler
US2199216A (en) * 1937-12-22 1940-04-30 Conti Piero Ginori Vaporizer
US2171369A (en) * 1937-12-27 1939-08-29 Marcus Nathan Hot water heater
DE937884C (de) * 1952-09-07 1956-01-19 Max Aurich Waermeaustauscher von chemischen Reinigungsanlagen, insbesondere Kuehler
GB1263254A (en) * 1968-08-08 1972-02-09 Foster Wheeler Brown Boilers Improvements in tube and shell heat exchangers
JPS47138Y1 (zh) * 1969-06-30 1972-01-06
JPS5237339Y2 (zh) * 1973-02-03 1977-08-25
DE2913092A1 (de) * 1979-04-02 1980-10-16 Benteler Werke Ag Aus rohren gefertigtes, wassergekuehltes wandelement fuer lichtbogenschmelzofen
JPS5916697Y2 (ja) * 1979-12-28 1984-05-16 三井造船株式会社 熱交換器
DE3012961A1 (de) * 1980-04-02 1981-10-08 Friedrich 7900 Ulm Bilger Indirekter waermetauscher
SE456935B (sv) * 1984-05-24 1988-11-14 Armaturjonsson Ab Vaermevaexlare daer stroemningsplaatar med strilhaal aer placerade i varje slingaav ett serpentinformat roer samt saett foer framstaellning
FR2570173B1 (fr) * 1984-09-13 1989-03-31 Leblanc Sa E L M Echangeur thermique, notamment pour chaudiere a condensation
JPS6183890A (ja) * 1984-09-29 1986-04-28 Toshiba Corp 冷凍機械用熱交換器
DE3611696A1 (de) * 1985-08-02 1987-02-12 Bernd Henting Waermetauscher fuer den waermeaustausch zwischen einem gasfoermigen und einem fluessigen medium
FR2627266B1 (fr) * 1988-02-16 1990-06-01 Leblanc Sa E L M Installation de chauffage central avec circuit d'eau chaude a usage sanitaire
DE4037986A1 (de) * 1990-11-29 1992-06-04 Richard Vetter Roehrenwaermeaustauscher
DE9204952U1 (de) * 1991-06-04 1992-07-16 Autokühler GmbH & Co KG, 3520 Hofgeismar Wärmetauscher, insbesondere für Kondensations-Wäschetrockner
JPH0571671U (ja) * 1992-02-28 1993-09-28 大阪瓦斯株式会社 熱交換器
US5579650A (en) * 1994-12-05 1996-12-03 Cleland; Robert K. Heat exchanger
EP0822596A3 (en) 1996-08-02 2000-01-05 Texas Instruments Inc. Improvements in or relating to integrated circuits
CN2274333Y (zh) * 1997-03-28 1998-02-11 烟台市牟平区压力容器制造厂 热交换器弯曲形扁平盘管
CN2793647Y (zh) * 2005-04-06 2006-07-05 小天鹅（荆州）电器有限公司 一种改进的冰箱冷柜蒸发器
TWI461237B (zh) * 2006-08-08 2014-11-21 Sulzer Chemtech Ag 用於聯合實施使用液體的熱交換與靜態混合之設備
TWI404903B (zh) * 2007-03-09 2013-08-11 Sulzer Chemtech Ag 用於流體媒介物熱交換及混合處理之設備
CN201555485U (zh) * 2009-12-14 2010-08-18 杭州沈氏换热器有限公司 一种盘管及具有该盘管的换热器

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB122626A (en) * 1918-01-25 Shaw Edward Improvements in and relating to Changing and Transfering Fluid Temperatures.
JPS6484098A (en) * 1987-09-26 1989-03-29 Junkosha Co Ltd Plastic tube heat exchanger
CN2198589Y (zh) * 1994-01-24 1995-05-24 王闰 波浪管换热器
CN2524163Y (zh) 2002-02-01 2002-12-04 李进龙 逆流盘管式换热器
CN101738121A (zh) * 2009-12-14 2010-06-16 杭州沈氏换热器有限公司 盘管及具有该盘管的换热器
CN101738122A (zh) * 2009-12-14 2010-06-16 杭州沈氏换热器有限公司 一种盘管及具有该盘管的换热器

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10508867B2 (en) 2015-05-28 2019-12-17 Dometic Sweden Ab Corrosion resistant coaxial heat exchanger assembly

Also Published As

Publication number Publication date
KR20120112560A (ko) 2012-10-11
JP2013513780A (ja) 2013-04-22
KR101710088B1 (ko) 2017-02-27
EP2515062A1 (en) 2012-10-24
US9234711B2 (en) 2016-01-12
US20120298342A1 (en) 2012-11-29
CN101738122A (zh) 2010-06-16
EP2515062A4 (en) 2018-04-04
JP5680669B2 (ja) 2015-03-04
EP2515062B1 (en) 2020-06-17
CN101738122B (zh) 2011-12-21

Similar Documents

Publication Publication Date Title
WO2011072470A1 (zh) 一种盘管及具有该盘管的换热器
CN101551207B (zh) 管壳式螺旋扁管换热器
CN202267394U (zh) 用于烟气余热回收的一次表面换热器
CN202018225U (zh) 一种圆形板壳式换热器
CN105823360B (zh) 含错排热管阵列的板式换热器
CN200993548Y (zh) 一种u型管式换热器
CN101650140A (zh) 传热管外流体多股螺旋流壳管式换热器
CN102374799A (zh) 壳管式换热器
CN201032418Y (zh) 一种板式蒸发式冷凝器
CN1140764C (zh) 缩放管全逆流双壳程轴流式换热器及其换热方法
CN210689299U (zh) 一种高效节能的管式换热器
CN105841525A (zh) 一种宽通道板式换热器
CN2672595Y (zh) 一种倾斜折流板列管式换热器
CN101435669A (zh) 内翅片扁管壳管式换热器
CN201434621Y (zh) 传热管外流体多股螺旋流壳管式换热器
CN202582237U (zh) 一种板壳式冷凝器
CN2809453Y (zh) 渣水冷却器
CN104296383A (zh) 一种高效冷凝换热器
CN201413066Y (zh) 管壳式螺旋扁管换热器
CN113566611B (zh) 一种u形管三股流换热器
CN2872275Y (zh) 管壳式换热器
CN110542334A (zh) 一种纯逆流壳管式淡水冷却器
CN201555485U (zh) 一种盘管及具有该盘管的换热器
CN101738121B (zh) 盘管及具有该盘管的换热器
CN204227701U (zh) 一种高效冷凝换热器

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 10836909

Country of ref document: EP

Kind code of ref document: A1

DPE1 Request for preliminary examination filed after expiration of 19th month from priority date (pct application filed from 20040101)
WWE Wipo information: entry into national phase

Ref document number: 2012543442

Country of ref document: JP

NENP Non-entry into the national phase

Ref country code: DE

WWE Wipo information: entry into national phase

Ref document number: 2010836909

Country of ref document: EP

ENP Entry into the national phase

Ref document number: 20127018381

Country of ref document: KR

Kind code of ref document: A

WWE Wipo information: entry into national phase

Ref document number: 13515616

Country of ref document: US