CN101158561A - Plate heat exchanger composite corrugated plate bind - Google Patents
Plate heat exchanger composite corrugated plate bind Download PDFInfo
- Publication number
- CN101158561A CN101158561A CNA2007101780710A CN200710178071A CN101158561A CN 101158561 A CN101158561 A CN 101158561A CN A2007101780710 A CNA2007101780710 A CN A2007101780710A CN 200710178071 A CN200710178071 A CN 200710178071A CN 101158561 A CN101158561 A CN 101158561A
- Authority
- CN
- China
- Prior art keywords
- ripple
- plate
- ripples
- heat exchanger
- wave height
- 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
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a plate exchanger compound ripple lamella bundle. A plurality of ripple plates are folded to form a lamella bundle of the plate exchanger; the ripple plate is struck out of a plurality of rectangle compound ripples arranged by matrix on a flat plate, and each matrix unit comprises two layers of ripples of different height and different shapes. Ripples arranged in the outer circle have relatively high wave height and a relatively big pitch of waves with the top being a bearing part between plates, and the ripples of the outer circle are arranged in pairs and in parallel with the vertical axes of two pairs of ripples forming a rectangle. Ripples heave transversely arranged in the rectangle, vertical ripples subside, and one or a plurality of raised inner layer ripples of relatively small wave height is/are arranged between the ripples of the outer circle. The invention has the advantages that the invention has high efficiency and intensifies the heat transmitting; the invention has a relatively wide flow passage and can allow relatively ropy liquid to get through; the invention enlarges the circulating surface, reduces the flowage resistance, and is helpful for energy saving and expense reducing in the industry process; the invention is easy to be processed, decreases the production cost and is helpful for the product popularization and application.
Description
Technical field
The present invention relates to a kind of heat exchange element of plate type heat exchanger, be specially adapted to the composite corrugated plate of major path that two kinds of fluids conduct heat.
Background technology
Plate type heat exchanger is a kind of compact conformation, heat exchanger efficiently, is widely used in oil, chemical industry, the energy, HVAC, electric power and metallurgy industry.The research of plate form is the core of plate type heat exchanger research, exploitation efficient heat transfer, low flow resistance, and the template of wide adaptability is numerous designers' pursuit.Domestic and international existing template adopts simple corrugated cardboard sheet, and is all not ideal enough to heat transfer property and rigidity, and the passage of runner is narrower.
Summary of the invention
The purpose of this invention is to provide a kind of major path plate heat exchanger composite corrugated plate bind that is applicable to two kinds of fluid heat transferring processes, to solve problems such as poor, higher circulating resistance of heat transfer property that traditional plate type heat exchanger exists and rigidity is all not ideal enough.
Plate heat exchanger composite corrugated plate bind of the present invention is superimposed together by two corrugated cardboard sheets, it is corresponding to press ripple by two corrugated cardboard sheets, forward and reverse being superimposed together, both sides sealing is constituted the basic heat transfer element of plate pipe, a plurality of plate pipes are superimposed together and form the plate bundle of a plate type heat exchanger, at the two ends of plate bundle adjacent plate edge are sealed; Corrugated cardboard sheet is that to strike out many rectangles that matrix arranges on flat board composite corrugated, each matrix unit comprises two layer heights and difform ripple, be arranged in peripheral ripple and have the higher wave height and the bigger pitch of waves, its napex is the supporting position between plate, peripheral ripple is arranged in parallel in pairs, the longitudinal axis of two pairs of ripples constitutes a rectangle, transversely arranged ripple projection in the rectangle, vertical ripple is recessed, is the internal layer ripple of less flow-disturbing of one or several protruding wave height and the effect of raising conductivity of heat between the ripple of periphery.
Described plate heat exchanger composite corrugated plate bind, the peripheral ripple that is parallel to each other of each matrix unit, staggered mutually along parallel direction.
Described plate heat exchanger composite corrugated plate bind, the scope of the pitch of waves of peripheral ripple: 30mm-80mm, the scope of wave height is between 3mm-10mm, and the axial length of ripple is slightly smaller than the pitch of waves.
Described plate heat exchanger composite corrugated plate bind, the internal layer ripple that is provided with in peripheral ripple inboard, adopt a kind of in the following pattern: the one, the ripple of the similar peripheral ripple rectangular arranged of shape, the scope of the pitch of waves is at 10mm-50mm, and the scope of wave height is between 1mm-6mm; The 2nd, many parallel ripples are set; The 3rd, a hemispherical dimples is set.
The present invention be directed to the existing problem of present template and propose a kind of new heat transfer template, it has higher heat transfer performance and lower circulating resistance.Because the runner broad, the scope of application can further expand the heat transfer of the liquid of comparison thickness to, and this is that in the past plate type heat exchanger is beyond one's reach.Effect of the present invention has: 1, efficient, augmentation of heat transfer: the action and function difference of inside and outside two-layer different ripples, realize efficient heat transfer.2, the runner that has broad can allow to pass through than the fluid of thickness, has enlarged the range of application of plate type heat exchanger, can be widely used in the occasion of heat energy, petrochemical industry, electric power, metallurgical equal energy source utilization and recovery.3, enlarge flow area, reduced flow resistance, helped the energy-saving and cost-reducing of industrial process.4, be easy to processing, reduce production costs, help promoting the use of of product.5, be provided with the internal layer ripple of hemispherical dimples in peripheral ripple inboard, plate bundle inner chamber is had self-cleaning function.
Description of drawings
Fig. 1 is a plate plane of the present invention.
Fig. 2 is a plate ripple list ripple plane of the present invention.
Fig. 3 is one of composite corrugated embodiment of plate of the present invention.
Fig. 4 is two of the composite corrugated embodiment of plate of the present invention.
Fig. 5 is three of the composite corrugated embodiment of plate of the present invention.
Fig. 6 be Fig. 3 along A-A directional profile figure.
Fig. 7 be Fig. 4 along A-A directional profile figure.
Fig. 8 be Fig. 5 along A-A directional profile figure.
The specific embodiment
Concrete technical scheme of the present invention is: it strikes out inside and outside two layer heights and variform ripple on flat board, and peripheral ripple has the higher wave height and the bigger pitch of waves.The also double supporting role of doing between plate of fin of peripheral ripple.The wave height of internal layer ripple is less, mainly plays flow-disturbing and improves conductivity of heat.
On a flat board, strike out the composite corrugated plane of many rectangles that matrix arranges as shown in Figure 1; Described composite corrugatedly form by inside and outside two layers of ripple 2,3.The waveform of outer single ripple 2 as shown in Figure 2.Ripple 2 is arranged in pairs, and the longitudinal axis of two pairs of ripples 2 constitutes a rectangle.Transversely arranged ripple projection in the rectangle, vertical ripple is recessed, otherwise or.Outer ripple 2 has the bigger pitch of waves and higher wave height.Thereby can form big channel cross-section, the passing through of favourable liquid than thickness.The distance of rectangle opposite side is called the pitch of waves.The scope of the pitch of waves L1 of outer ripple: 30mm-80mm, the scope of wave height H is between 3mm-10mm, and the axial length of ripple is slightly smaller than the pitch of waves.
Be provided with ripplet 3 in outer ripple 2 inboards, its pattern has three kinds: the one, and the ripple of the similar outer ripple rectangular arranged of shape, shown in figure-3, the scope of pitch of waves L2 is at 10mm-50mm, and the scope of wave height h is between 1mm-6mm.The 2nd, many parallel ripples are set, as shown in Figure 4.The 3rd, a hemispherical dimples is set, shown in figure-5.The effect of internal layer ripple 3 has two: one, increases the rigidity of corrugated plating; The 2nd, increase the flow-disturbing of fluid at corrugated cardboard sheet, improve heat transfer coefficient.
Above-mentioned three kinds of composite corrugated cutaway views such as Fig. 6 are to shown in Figure 8.
2 one-tenth rectangular arranged of outside ripple on the plate of the present invention.Transversely arranged ripple projection in the rectangle, vertical ripple is recessed.Plate pipe of two plate 1 reverse superimposed compositions, a plurality of plate pipes constitute the plate bundle of a plate type heat exchanger.The ripple 2 of outer rectangular arranged is because the concavo-convex layout of ripple, thereby forms the passage of both direction in length and breadth.
The action and function of inside and outside two-layer different ripples 3,2 is different.The acting body of outer big ripple forms bigger runner now.Cross one another two wing passages of the fashionable formation of the plate groups that groove or fin are adjacent.The size decision fluid resistance of passage reduces, thereby can allow to pass through than the liquid of thickness.It is the reverse superimposed back formation supporting-point of two plates that the effect of fin has two: one; The 2nd, to the runner formation metering function of this side.Ripplet and hemispherical groove that ripple in the big ripple in the outside has rectangular arranged, bar shaped to arrange, its effect are to promote that fluid produces second-disturbing flow at corrugated plating, destroy fluid boundary layer, strengthen the coupling in velocity field and temperature field.Efficient hardening conducts heat, and realizes efficient heat transfer.Ripple also works to strengthen rigidity simultaneously.The size of the height of the tongue and groove of size, spacing and the ripple of outside ripple and the shape of interior ripple, wave groove all can be according to the physical parameter of heat transfer medium, and conditions such as allowable pressure drop are determined.Be combined to form the different runner of sectional area by corrugated plating.
During work, it is corresponding oppositely superimposed and form a plate pipe along the dual-side welding that two corrugated platings are pressed ripple.A plurality of plate pipes superpose and the vertical passage of formation plate pipe and the interconnection of plate pipe are welded in the port one side merging of adjacent two plate pipes.Two kinds of heat transferring mediums form two kinds of fluid cross flow one respectively by runner between plate pipe runner and plate, finish the diabatic process of two kinds of fluids.
Complex wave card bundle production example: the plate that profile is identical, it is corresponding to press ripple, forward and reverse basic heat transfer element that is superimposed together and continuous welding formation in both sides is called the plate pipe.A plurality of plate pipes are built up a plate bundle, at the two ends of plate bundle adjacent sheet film pack side weld are connect, thereby form plate pipe wing passage.Then the plate bundle is placed in the airtight housing.A kind of fluid is by plate pipe internal channel, and one other fluid is by the passage between the plate pipe.The fluid of different conditions passes through runner separately, and heat is passed to cryogen by high temperature fluid, and two kinds of fluids form cross-currents and finish the partition heat exchange.
Claims (4)
1. plate heat exchanger composite corrugated plate bind, it is corresponding to press ripple by two corrugated cardboard sheets, forward and reverse being superimposed together, both sides sealing is constituted the basic heat transfer element of plate pipe, a plurality of plate pipes are superimposed together and form the plate bundle of a plate type heat exchanger, at the two ends of plate bundle adjacent plate edge are sealed; It is characterized in that: corrugated cardboard sheet is that to strike out many rectangles that matrix arranges on flat board composite corrugated, each matrix unit comprises two layer heights and difform ripple, be arranged in peripheral ripple and have the higher wave height and the bigger pitch of waves, its top is the supporting position between plate, peripheral ripple is arranged in parallel in pairs, the longitudinal axis of two pairs of ripples constitutes a rectangle, transversely arranged ripple projection in the rectangle, vertical ripple is recessed, is the internal layer ripple of less flow-disturbing of one or several protruding wave height and the effect of raising conductivity of heat between the ripple of periphery.
2. a kind of plate heat exchanger composite corrugated plate bind as claimed in claim 1 is characterized in that: the peripheral ripple that is parallel to each other of each matrix unit, and staggered mutually along parallel direction.
3. a kind of plate heat exchanger composite corrugated plate bind as claimed in claim 1 or 2 is characterized in that: the scope of the pitch of waves of peripheral ripple: 30mm-80mm, and the scope of wave height is between 3mm-10mm, and the axial length of ripple is slightly smaller than the pitch of waves.
4. a kind of plate heat exchanger composite corrugated plate bind as claimed in claim 1 or 2, it is characterized in that: the internal layer ripple that is provided with in peripheral ripple inboard, adopt a kind of in the following pattern: the one, the ripple of the similar peripheral ripple rectangular arranged of shape, the scope of the pitch of waves is at 10mm-50mm, and the scope of wave height is between 1mm-6mm; The 2nd, many parallel ripples are set; The 3rd, a hemispherical dimples is set.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007101780710A CN101158561A (en) | 2007-11-26 | 2007-11-26 | Plate heat exchanger composite corrugated plate bind |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007101780710A CN101158561A (en) | 2007-11-26 | 2007-11-26 | Plate heat exchanger composite corrugated plate bind |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101158561A true CN101158561A (en) | 2008-04-09 |
Family
ID=39306728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2007101780710A Pending CN101158561A (en) | 2007-11-26 | 2007-11-26 | Plate heat exchanger composite corrugated plate bind |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101158561A (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101806552A (en) * | 2010-05-20 | 2010-08-18 | 甘肃蓝科石化高新装备股份有限公司 | Corrugated sheet structure for welded plate type heat exchanger |
| CN102168929A (en) * | 2010-02-26 | 2011-08-31 | 株式会社地球清洁东北 | Indirect evaporative cooling apparatus |
| CN102798307A (en) * | 2012-09-10 | 2012-11-28 | 张月明 | Shell-and-plate heat exchanger with asymmetric structure and manufacturing method thereof |
| CN102997742A (en) * | 2012-12-14 | 2013-03-27 | 新兴能源装备股份有限公司 | Sheet bar for full-welded plate type heat exchanger and heat exchanger using same |
| CN103822521A (en) * | 2014-03-04 | 2014-05-28 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchange plate and plate type heat exchanger |
| CN104132576A (en) * | 2014-08-12 | 2014-11-05 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchange plate and plate heat exchanger |
| WO2015131758A1 (en) * | 2014-03-07 | 2015-09-11 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchange plate used for plate-type heat exchanger and plate-type heat exchanger provided with the heat exchange plate |
| CN104132576B (en) * | 2014-08-12 | 2016-11-30 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchanger plates and plate type heat exchanger |
| CN108332586A (en) * | 2017-01-18 | 2018-07-27 | 维美德技术有限公司 | Heat exchanger plate and the method for manufacturing heat exchanger plate |
| US10323883B2 (en) | 2014-03-07 | 2019-06-18 | Danfoss Micro Channel Heat Exchanger (Jiaxing) Co., Ltd. | Heat exchange plate for plate-type heat exchanger and plate-type heat exchanger provided with said heat exchange plate |
| CN110514041A (en) * | 2019-08-23 | 2019-11-29 | 兰州兰石换热设备有限责任公司 | Nuclear power system plate heat exchanger core |
| CN111765787A (en) * | 2020-07-14 | 2020-10-13 | 北京市京海换热设备制造有限责任公司 | Heat transfer structure and heat exchanger |
| US11499786B2 (en) | 2018-11-26 | 2022-11-15 | Alfa Laval Corporate Ab | Heat transfer plate |
-
2007
- 2007-11-26 CN CNA2007101780710A patent/CN101158561A/en active Pending
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102168929A (en) * | 2010-02-26 | 2011-08-31 | 株式会社地球清洁东北 | Indirect evaporative cooling apparatus |
| CN101806552A (en) * | 2010-05-20 | 2010-08-18 | 甘肃蓝科石化高新装备股份有限公司 | Corrugated sheet structure for welded plate type heat exchanger |
| CN102798307A (en) * | 2012-09-10 | 2012-11-28 | 张月明 | Shell-and-plate heat exchanger with asymmetric structure and manufacturing method thereof |
| CN102798307B (en) * | 2012-09-10 | 2014-03-19 | 张月明 | Shell-and-plate heat exchanger with asymmetric structure and manufacturing method thereof |
| CN102997742A (en) * | 2012-12-14 | 2013-03-27 | 新兴能源装备股份有限公司 | Sheet bar for full-welded plate type heat exchanger and heat exchanger using same |
| CN103822521A (en) * | 2014-03-04 | 2014-05-28 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchange plate and plate type heat exchanger |
| EP3115731A4 (en) * | 2014-03-07 | 2017-11-15 | Danfoss Micro Channel Heat Exchanger (Jiaxing) Co. | Heat exchange plate used for plate-type heat exchanger and plate-type heat exchanger provided with the heat exchange plate |
| US10323883B2 (en) | 2014-03-07 | 2019-06-18 | Danfoss Micro Channel Heat Exchanger (Jiaxing) Co., Ltd. | Heat exchange plate for plate-type heat exchanger and plate-type heat exchanger provided with said heat exchange plate |
| WO2015131758A1 (en) * | 2014-03-07 | 2015-09-11 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchange plate used for plate-type heat exchanger and plate-type heat exchanger provided with the heat exchange plate |
| WO2016023393A1 (en) * | 2014-08-12 | 2016-02-18 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchange plate and plate-type heat exchanger |
| CN104132576B (en) * | 2014-08-12 | 2016-11-30 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchanger plates and plate type heat exchanger |
| US10066879B2 (en) | 2014-08-12 | 2018-09-04 | Danfoss Micro Channel Heat Exchanger (Jiaxing) Co., Ltd. | Heat exchange plate and plate-type heat exchanger |
| CN104132576A (en) * | 2014-08-12 | 2014-11-05 | 丹佛斯微通道换热器（嘉兴）有限公司 | Heat exchange plate and plate heat exchanger |
| CN108332586A (en) * | 2017-01-18 | 2018-07-27 | 维美德技术有限公司 | Heat exchanger plate and the method for manufacturing heat exchanger plate |
| US11499786B2 (en) | 2018-11-26 | 2022-11-15 | Alfa Laval Corporate Ab | Heat transfer plate |
| CN110514041A (en) * | 2019-08-23 | 2019-11-29 | 兰州兰石换热设备有限责任公司 | Nuclear power system plate heat exchanger core |
| CN110514041B (en) * | 2019-08-23 | 2024-10-11 | 兰州兰石换热设备有限责任公司 | Plate heat exchanger core for nuclear power system |
| CN111765787A (en) * | 2020-07-14 | 2020-10-13 | 北京市京海换热设备制造有限责任公司 | Heat transfer structure and heat exchanger |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101158561A (en) | Plate heat exchanger composite corrugated plate bind | |
| CN104896977A (en) | Integrated primary surface micro-channel compact heat exchanger | |
| CN101655321B (en) | High-pressure aluminum plate-fin heat exchanger | |
| US20120125583A1 (en) | Heat exchanger | |
| CN207180438U (en) | Plate type heat exchanger main heat exchange plate ripple plot structure | |
| CN103868380A (en) | Plate heat exchanger | |
| CN102706187A (en) | Integrated type micro-channel heat exchanger | |
| CN104880106A (en) | Microchannel plate heat exchanger with sine-shaped flow channels | |
| CN202188782U (en) | Honeycomb bunch tube type heat exchanger | |
| CN112944996A (en) | Compound heat transfer runner and contain its heat transfer board based on subregion is reinforceed | |
| CN108061471B (en) | A kind of multiple-unit composite screw plate heat exchanger | |
| CN102226655B (en) | Honeycomb-bundle tubular heat exchanger and manufacturing process thereof | |
| CN203687734U (en) | Plate heat exchanger plate sheet with unequal cross sectional areas of fluid flow passages and plate heat exchanger | |
| CN202885612U (en) | Welded plate heat exchanger | |
| CN202599166U (en) | Integrated micro-channel heat exchanger | |
| CN107966057A (en) | A kind of plate heat exchanger and its application method | |
| CN201225853Y (en) | Wide channel plate heat exchanger with detachable intensified element on one side | |
| CN104390507A (en) | Chevron corrugated plate | |
| CN205388435U (en) | Stagnant area disturbance slab | |
| CN102853693A (en) | Double-flow-channel heat exchanger | |
| CN110530179B (en) | Symmetrical bubbling type plate heat transfer element | |
| CN201255599Y (en) | Corrugated plate piece | |
| CN103791741B (en) | A kind of phase transformation plate type heat exchanger | |
| CN2809567Y (en) | Soft and hard corrugated board structure | |
| CN102853707A (en) | Heat exchanger plate sheet and double-channel 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 | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |