CN101118136A - Hot plate heat exchanger - Google Patents
Hot plate heat exchanger Download PDFInfo
- Publication number
- CN101118136A CN101118136A CNA2007101314773A CN200710131477A CN101118136A CN 101118136 A CN101118136 A CN 101118136A CN A2007101314773 A CNA2007101314773 A CN A2007101314773A CN 200710131477 A CN200710131477 A CN 200710131477A CN 101118136 A CN101118136 A CN 101118136A
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- heat
- plate
- hot plate
- exchanger according
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 238000005192 partition Methods 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical group [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000010949 copper Substances 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 4
- 239000003546 flue gas Substances 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000002918 waste heat Substances 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 238000005219 brazing Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
技术领域technical field
本发明热板换热器涉及一种热交换器,特别涉及一种用于高温烟气余热回收的热板换热器。The hot plate heat exchanger of the invention relates to a heat exchanger, in particular to a hot plate heat exchanger for recovering waste heat from high-temperature flue gas.
背景技术Background technique
现有高温烟气余热回收装置中,如果烟气温度很高(>800℃),大多采用高温热管换热器。高温热管作为换热器的主要传热单元,与普通热管相比,具有温差应力小、结构形式简单、不易受高温破坏等优点。但是,其制造成本高、加工工艺复杂,浪费能源等缺点成为制约高温热管换热器发展推广的主要因素。In existing high-temperature flue gas waste heat recovery devices, if the flue gas temperature is very high (>800°C), most high-temperature heat pipe heat exchangers are used. As the main heat transfer unit of the heat exchanger, the high-temperature heat pipe has the advantages of small temperature difference stress, simple structure, and less susceptible to high temperature damage compared with ordinary heat pipes. However, its high manufacturing cost, complicated processing technology, and waste of energy have become the main factors restricting the development and promotion of high-temperature heat pipe heat exchangers.
发明内容Contents of the invention
本发明旨在克服上述存在的问题,提供一种热板换热器,这种热板换热器传热面积大,均温性佳、结构强度高、制造成本低,存在体积小,重量轻,比高温热管换热器性能、成本都有很大的改进与提高。The purpose of the present invention is to overcome the above-mentioned problems and provide a heat plate heat exchanger, which has a large heat transfer area, good temperature uniformity, high structural strength, low manufacturing cost, small volume, light weight, and The performance and cost of high-temperature heat pipe heat exchangers have been greatly improved and improved.
本发明的目的是通过以下技术方案实现的:一种热板换热器,由芯体和隔板组成,所述芯体由若干热板组成,所述若干热板表面中间由所述隔板隔开,分成上下两个介质通道;所述热板由真空充液通道和接管组成。The purpose of the present invention is achieved through the following technical solutions: a heat exchanger consisting of a core and a partition, the core is composed of several heat plates, the surfaces of the several heat plates are in the middle of the partition Separated and divided into upper and lower medium channels; the hot plate is composed of a vacuum liquid-filled channel and a connecting pipe.
所述芯体的材质可为铝、铜、不锈钢或其它导热性能佳的材质。The material of the core body can be aluminum, copper, stainless steel or other materials with good thermal conductivity.
所述真空充液通道的断面可为圆形、椭圆形、三角形、多边形等的形状,例如,真空充液通道为由上、下盖板、侧封条和底封条密封连接围成的矩形通道。The cross-section of the vacuum liquid-filled channel can be circular, oval, triangular, polygonal, etc., for example, the vacuum liquid-filled channel is a rectangular channel enclosed by upper and lower cover plates, side seals and bottom seals.
作为本发明的进一步改进,在所述真空充液通道内设有翅片,所述翅片形式可为锯齿、多孔、波纹形,翅片排布形式可横排、纵排或倾斜一定角度排布。As a further improvement of the present invention, fins are provided in the vacuum liquid-filled channel, and the fins can be in the form of sawtooth, porous, or corrugated, and the arrangement of the fins can be arranged horizontally, vertically, or at a certain angle. cloth.
所述接管用以将真空充液通道抽真空并充装工作液体。The connecting pipe is used to evacuate the vacuum liquid-filled channel and fill it with working liquid.
作为本发明的进一步改进,在所述热板的表面上设有若干肋片或鳍片,从而强化蒸发段以及冷凝段的传热。此时,所述芯体由若干个带有肋片或鳍片的真空充液通道构成,其中肋片通道由一隔板分隔成冷介质和热介质通道,实现冷热流体逆流型流动。使用时,换热器整体呈垂直或倾斜一定的角度布置,以保证真空充液通道内的工作液体能够从冷介质段自然回流到热介质段。As a further improvement of the present invention, several ribs or fins are provided on the surface of the heat plate, so as to enhance the heat transfer in the evaporating section and the condensing section. At this time, the core body is composed of several vacuum liquid-filled passages with fins or fins, wherein the fin passages are divided into cold medium and hot medium passages by a partition to realize countercurrent flow of cold and hot fluids. When in use, the heat exchanger is arranged vertically or inclined at a certain angle to ensure that the working liquid in the vacuum liquid-filled channel can naturally flow back from the cold medium section to the hot medium section.
本发明将带有肋片的真空充液通道叠置,热介质通道和冷介质通道并列布置,真空充液通道内工作液体通过内部相变进行热量转移,使热流体和冷流体之间形成逆流型流动,具有均温性佳、传热面积大、结构强度高、换热效率高、成本低等优点。与高温热管换热器相比,成本下降40%,且易于制造。In the present invention, the vacuum liquid-filled channels with fins are stacked, the hot medium channel and the cold medium channel are arranged side by side, and the working liquid in the vacuum liquid-filled channel undergoes heat transfer through internal phase change, so that a counterflow is formed between the hot fluid and the cold fluid Type flow, has the advantages of good temperature uniformity, large heat transfer area, high structural strength, high heat transfer efficiency, and low cost. Compared with the high-temperature heat pipe heat exchanger, the cost is reduced by 40%, and it is easy to manufacture.
附图说明Description of drawings
图1是本发明实施例1总体结构示意图Fig. 1 is a schematic diagram of the overall structure of Embodiment 1 of the present invention
图2是本发明实施例1带肋片热板的空间剖视图Fig. 2 is a space sectional view of a ribbed hot plate in Embodiment 1 of the present invention
图3是本发明实施例2热板换热器外型结构示意图Fig. 3 is a schematic diagram of the external structure of the heat plate heat exchanger in Embodiment 2 of the present invention
具体实施方式Detailed ways
以下结合附图对本发明进一步说明:The present invention is further described below in conjunction with accompanying drawing:
实施例1Example 1
参照附图1,热板换热器由芯体100和隔板104组成。芯体100由若干热板103组成。热板103由若干个带有肋片或鳍片211、212的真空充液通道102和接管101构成。每个热板103的表面由一隔板104将肋片分隔成上、下两介质通道,即热介质通道105和冷介质通道106,实现热流体和冷流体的逆流流动。同时,隔板104将若干热板103连为一体。接管101设置在真空充液通道102的上部,用以将真空充液通道102抽成真空并充装工作液体,接管101封口的方式可为焊接或封口钳等可使其达到完全密合的封装方法。Referring to FIG. 1 , the heat plate heat exchanger is composed of a
参照附图2,真空充液通道102前后设有盖板221和盖板222,上部设有接管201,盖板211和盖板212上带有肋片211和212。内部设有纵排的锯齿型翅片231。盖板221和盖板222、以及锯齿型翅片231之间采用真空钎焊方式连接;接管201和真空充液通道102之间采用普通焊接的连接方式。Referring to accompanying drawing 2, the vacuum
工作时,热板103整体呈水平倾斜布置或垂直布置,真空充液通道102内的工作液体在热介质通道105段吸收热量,蒸发成为蒸汽,运动到冷介质通道106段冷凝放热成为液体,将热量传给冷介质后自然回流到热介质段。肋片结构211和212增大热板换热器的换热面积,强化了热板换热器的传热。When working, the
实施例2Example 2
参照附图3,热板换热器的另一种外形结构示意图。本实施例中与上例的不同之处在于,冷介质侧在各热板103的外部封闭环绕了中空的水夹套301,每个水夹套301上设有进口和出口,进出口焊有接管311和312,图3中箭头指向表示介质的流动方向,一般为低进高出。工作时,冷介质从进口接管312进入水夹套301,真空充液通道102内的工作液体在热介质段105吸收热量,蒸发成为蒸汽,运动到冷介质段106对水夹套301内的冷却介质释放热量,同时凝结成为液体,如此往复循环,使热量源源不断传给水夹套301内的冷介质,水夹套301内的冷介质吸热后变为热介质从出口接管311排出。热板以相变传热的方式进行工作,同时还加加有肋片结构211和212和水夹套301,因此,传热效率高。Referring to accompanying drawing 3, it is a schematic diagram of another shape and structure of the heat plate heat exchanger. The difference between this embodiment and the previous example is that the cold medium side is closed and surrounded by a
Claims (10)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2007101314773A CN101118136A (en) | 2007-08-31 | 2007-08-31 | Hot plate heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2007101314773A CN101118136A (en) | 2007-08-31 | 2007-08-31 | Hot plate heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101118136A true CN101118136A (en) | 2008-02-06 |
Family
ID=39054346
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNA2007101314773A Pending CN101118136A (en) | 2007-08-31 | 2007-08-31 | Hot plate heat exchanger |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101118136A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101922878A (en) * | 2010-08-11 | 2010-12-22 | 上海贝电实业股份有限公司 | Modularized heat pipe air heat exchanger |
CN101566331B (en) * | 2009-06-05 | 2011-04-20 | 南京工业大学 | pulse heat fin type radiator |
CN103471165A (en) * | 2013-09-23 | 2013-12-25 | 哈尔滨工业大学 | Packaging system provided with phase-change materials and used inside hot wall |
CN104089503A (en) * | 2014-07-31 | 2014-10-08 | 哈尔滨工程大学 | Plate-shell heat exchanger with oval corrugated plates |
CN112696940A (en) * | 2020-12-29 | 2021-04-23 | 河海大学 | Multichannel heat exchanger of large-scale air water making unit |
-
2007
- 2007-08-31 CN CNA2007101314773A patent/CN101118136A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101566331B (en) * | 2009-06-05 | 2011-04-20 | 南京工业大学 | pulse heat fin type radiator |
CN101922878A (en) * | 2010-08-11 | 2010-12-22 | 上海贝电实业股份有限公司 | Modularized heat pipe air heat exchanger |
CN103471165A (en) * | 2013-09-23 | 2013-12-25 | 哈尔滨工业大学 | Packaging system provided with phase-change materials and used inside hot wall |
CN103471165B (en) * | 2013-09-23 | 2016-01-20 | 哈尔滨工业大学 | A kind of for the packaging system that phase-change material is housed in wall with flues |
CN104089503A (en) * | 2014-07-31 | 2014-10-08 | 哈尔滨工程大学 | Plate-shell heat exchanger with oval corrugated plates |
CN112696940A (en) * | 2020-12-29 | 2021-04-23 | 河海大学 | Multichannel heat exchanger of large-scale air water making unit |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202229633U (en) | Pipe-foam type heat exchanger | |
CN101819000B (en) | Disconnect-type phase transition heat exchanger | |
CN101929813B (en) | Flat-plate heat pipe | |
CN105823360B (en) | Plate type heat exchanger containing wrong heat exhausting pipe array | |
CN106643244A (en) | Air-cooled plate-fin type composite capillary groove phase transition radiator | |
CN201772793U (en) | A flat heat pipe | |
CN101118136A (en) | Hot plate heat exchanger | |
CN108981438A (en) | A kind of heat exchanger and heat-exchange method | |
CN110360864A (en) | A kind of board-like regenerative heat exchange integrated apparatus of step phase transformation | |
CN111336841A (en) | A wrap-around microchannel heat exchanger | |
ITTO20001183A1 (en) | HEAT EXCHANGER APPARATUS. | |
CN206222991U (en) | A kind of heat pipe fin heat-exchanger | |
CN106382836B (en) | Separate heat pipe shower waste water residual heat recovery system and method | |
CN202254521U (en) | A Microchannel Condenser for Heat Pump Water Heater | |
CN101122448A (en) | a hot plate | |
CN103925818B (en) | Staggered plate pulsating heat pipe heat exchanger | |
WO2021012936A1 (en) | Plate heat exchanger having flow-dividing plate path | |
CN103712495B (en) | Heat exchange device for recycling flue gas waste heat | |
CN205537257U (en) | Plate heat exchanger who contains misalignment heat pipe array | |
CN104613798A (en) | Micro array heat pipe gas-liquid countercurrent flow heat exchange device | |
CN205690946U (en) | A kind of gas-liquid pulsating heat pipe heat exchanger | |
CN204226019U (en) | Compact type regenerator | |
CN210512784U (en) | Micro-channel heat exchanger | |
CN203928848U (en) | The condensing heat exchanger of a kind of condensing heat exchange plate and application thereof | |
CN103791741B (en) | A kind of phase transformation plate type heat exchanger |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |
Open date: 20080206 |