CN2723940Y - Heat exchanger in hot water supply system - Google Patents
Heat exchanger in hot water supply system Download PDFInfo
- Publication number
- CN2723940Y CN2723940Y CN 200420087891 CN200420087891U CN2723940Y CN 2723940 Y CN2723940 Y CN 2723940Y CN 200420087891 CN200420087891 CN 200420087891 CN 200420087891 U CN200420087891 U CN 200420087891U CN 2723940 Y CN2723940 Y CN 2723940Y
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- pipe
- heat exchanging
- layer
- exchanger tube
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model comprises a crust, a heating medium inlet, a heating medium outlet, a cool water inlet and a hot water outlet. The crust is provided with a core pipe. The inlet and the outlet of the heating medium are respectively sealed and welded with the inlet pipe plate and the outlet pipe plate of a heat exchanging pipe. The inlet pipe plate and the outlet pipe plate of the heat exchanging pipe are respectively provided with a plurality of pipe holes which are corresponding to each other. The numbers of the pipe holes are the same. The heat exchanging pipes are respectively provided between each corresponding pipe hole. The heat exchanging pipes are winded out of the core pipe in the multilayer spiral type. Each layer comprises a plurality of heat exchanging pipes. The heat exchanging pipes are glued to arrange in parallel. The spiral directions of the winding heat exchanging pipes of the adjacent layer are reverse. The heat exchanging pipes of the furthest inner layer are glued with the outer wall of the core pipe and a gap is between the heat exchanging pipe and the core pipe. The head exchanging pipes of the furthest outer layer are glued with the inner wall of the cylinder part of the crust and a gap is also provided between the heat exchanging pipe and the inner wall of the cylinder part of the crust. Each heat exchanging pipe layer is glued in sequence. Each heat exchanging pipe is a thin wall screw tube. The heat exchanging quotiety of the utility model can reach to 10000-14000w/m<2> DEG C . The utility model also has the advantages of small volume and light weight.
Description
Technical field
The utility model relates to heat-exchanger rig, specifically the heat exchanger in the hot water supply system.
Background technology
Heat exchanger in the hot water supply system generally is made up of the heat exchanger tube in shell, heating agent import, heating agent outlet, cooling water inlet, hot water outlet and the shell.The coefficient of heat transfer is generally at 2000W/m
2About ℃.
The utility model content
The purpose of this utility model is the higher heat exchanger of a kind of coefficient of heat transfer of design.
The utility model comprises the cylindrical housing of two ends band end socket, on the end socket of this shell the heating agent import is arranged, the heating agent outlet is arranged on another end socket, close on heating agent import department on the shell hot water outlet is arranged, close on the heating agent exit cooling water inlet is arranged, there are two ends that the core pipe of end cap is arranged in the shell, porose on the end cap, core pipe and shell have common center line, heating agent advances, exporting seal weld respectively is connected to a heat exchanger tube and advances, the outlet tube sheet, heat exchanger tube advances, on the outlet tube sheet the identical a plurality of heating agent pores in correspondence with each other of quantity are arranged respectively, between the heating agent pore of every pair of correspondence heat exchanger tube is arranged respectively, adopt Type of Welding to connect between heat exchanger tube and the tube sheet, these heat medium pipes divide the multi-layer helical formula to be wrapped in outside the core pipe, each layer all comprises a plurality of heat exchanger tubes, and these heat exchanger tubes are to paste mutually side by side to arrange, the hand of spiral that the heat exchanger tube of adjacent layer twines is opposite, the heat exchanger tube of innermost layer pastes mutually with core tube wall, and it is gapped between the two, outermost heat exchanger tube pastes mutually with the inwall of shell cylindrical portion, and it is gapped between the two, also paste mutually successively between the heat exchanger tube layer of each layer and the layer, every heat exchanger tube is all the thin-walled screwed pipe.
The coefficient of heat transfer of the present utility model can reach 10000-14000W/m
2℃.The reason that the utility model coefficient of heat transfer is so high is that the slit between heat exchanger tube is very little, and be the spirality trend, the slit of per pass spirality trend is connected again with remaining slit, will be divided into middle tortuous the flowing of the small gap of a lot of strands of weeps between heat exchanger tube after cold water is come in from import like this, form turbulent flow, mobile route is elongated, and the flow velocity of water is accelerated.Another reason is that heat exchanger tube is the thin-walled screwed pipe, and heat exchanger tube has a plurality ofly, and this attenuates each heat exchanger tube.These screw thread tubule layerings in outer cover of heat exchanger, intersection, spiral gathering cause the interior heat exchanger tube of shell to take up space and reach more than 80%, have increased heat exchange area.The technical program has not only increased the thermal efficiency, and heat exchanger volume is diminished, and weight saving is compared same output volume with general heat exchanger and can be tapered to 1/10.
Description of drawings
Fig. 1 is the cutaway view of an embodiment of the present utility model, and wherein the heat exchanger tube in the shell and the tube sheet of heat exchanger tube import and export are not analysed and observe.
The specific embodiment
As seen from Figure 1, present embodiment comprises shell, and this shell is by cylindrical portion (4), and left end socket (2) and right end socket (8) are welded.Be welded with heating agent import (1) on the end socket of a left side, be welded with heating agent outlet (9) on the right end socket, the left end of shell cylindrical portion is welded with hot water outlet (10), and the right-hand member of cylindrical portion is welded with cooling water inlet (6).The core pipe (5) that a two ends band edge lid is arranged in the shell, shell, heating agent import and outlet, core Guan Sizhe has common center line.The inner of heating agent import and outlet is welded with heat exchanger tube tube sheet (3) and (7) of the identical circular plate type of structure respectively, and 38 heat exchanger tube pores are all arranged on each heat exchanger tube tube sheet.All be welded with heat exchanger tube between the heat exchanger tube pore of the correspondence on two tube sheets, these heat exchanger tubes divide 5 helical layer formulas to be wrapped in outside the core pipe, from inside to outside the 1st layer has 4 heat exchanger tubes, the 2nd layer has 6, and the 3rd layer has 8, and the 4th layer has 10, the 5th layer has 10, the heat exchanger tube of each layer all is to paste mutually side by side to arrange, and wherein the 1st, the 3rd is identical with the hand of spiral of the 5 three layer of heat exchanger tube, and the 2nd is identical with the hand of spiral of the 4th two-layer heat exchanger tube but opposite with the 1st, the 3rd and the 5 three layer the hand of spiral.The 1st layer heat exchanger tube and core pipe paste mutually and are gapped, and the 5th layer heat exchanger tube pastes mutually with the inwall of shell cylindrical portion and be gapped, the 1st, the 2nd, the 3rd, the 4th with the 5th layer of heat exchanger tube subsides mutually successively, every heat exchanger tube all is the thin-walled screwed pipe.There is external screw thread the outer end of heating agent import and export of the present utility model, cooling water inlet, hot water outlet.All component materials of present embodiment all are stainless.
Claims (1)
1. the heat exchanger in the hot water supply system, the cylinder type shell that comprises two ends band end socket, on the end socket of shell the heating agent import is arranged, the heating agent outlet is arranged on another termination, close on heating agent import department on the shell hot water outlet is arranged, close on the heating agent exit cooling water inlet is arranged, the core pipe that a two ends band edge lid is arranged in the shell that is characterised in that of the present utility model, porose on the end cap, this core pipe and shell have common center line, heating agent advances, exporting seal weld respectively is connected to heat exchanger tube and advances, the outlet tube sheet, heat exchanger tube advances, on the outlet tube sheet the identical a plurality of heating agent pores in correspondence with each other of quantity are arranged respectively, be welded with heat exchanger tube respectively between the heating agent pore of every pair of correspondence, these heat exchanger tubes divide the multi-layer helical formula to be wrapped in outside the core pipe, the heat exchanger tube of each layer all comprises a plurality of heat exchanger tubes, and these heat exchanger tubes are to paste mutually side by side to arrange, the hand of spiral that the heat exchanger tube of adjacent layer twines is opposite, the heat exchanger tube of innermost layer pastes mutually with core tube wall, and it is gapped between the two, outermost heat exchanger tube pastes mutually with the inwall of shell cylindrical portion, and it is also gapped between the two, also paste mutually successively between the heat exchanger tube layer of each layer and the layer, every heat exchanger tube is all the thin-walled screwed pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420087891 CN2723940Y (en) | 2004-08-24 | 2004-08-24 | Heat exchanger in hot water supply system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200420087891 CN2723940Y (en) | 2004-08-24 | 2004-08-24 | Heat exchanger in hot water supply system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2723940Y true CN2723940Y (en) | 2005-09-07 |
Family
ID=35037564
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200420087891 Expired - Fee Related CN2723940Y (en) | 2004-08-24 | 2004-08-24 | Heat exchanger in hot water supply system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2723940Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100425933C (en) * | 2006-10-23 | 2008-10-15 | 杨文� | Conversion diverting type heat exchanger |
| CN102200398A (en) * | 2011-04-11 | 2011-09-28 | 山东北辰压力容器有限公司 | Double-shell heat exchanger |
| CN103267434A (en) * | 2013-05-23 | 2013-08-28 | 山东豪迈机械制造有限公司 | Detachable spiral winding heat exchanger |
| CN103363815A (en) * | 2013-08-07 | 2013-10-23 | 济南擎雷换热科技有限公司 | Detachable spiral wound tube type condenser |
-
2004
- 2004-08-24 CN CN 200420087891 patent/CN2723940Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100425933C (en) * | 2006-10-23 | 2008-10-15 | 杨文� | Conversion diverting type heat exchanger |
| CN102200398A (en) * | 2011-04-11 | 2011-09-28 | 山东北辰压力容器有限公司 | Double-shell heat exchanger |
| CN102200398B (en) * | 2011-04-11 | 2012-11-14 | 山东北辰机电设备股份有限公司 | Double-shell heat exchanger |
| CN103267434A (en) * | 2013-05-23 | 2013-08-28 | 山东豪迈机械制造有限公司 | Detachable spiral winding heat exchanger |
| CN103363815A (en) * | 2013-08-07 | 2013-10-23 | 济南擎雷换热科技有限公司 | Detachable spiral wound tube type condenser |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105937857B (en) | A kind of shell-and-tube heat exchanger being suitable for three fluid heat transfers | |
| CN202018225U (en) | Circular plate case type heat exchanger | |
| CN105823348B (en) | Bifilar stream mixed tube bundle shell-and-tube heat exchanger | |
| CN103954153B (en) | The pure reverse stream pipe shell heat exchanger of multipaths | |
| CN101363694A (en) | Shell-pipe head exchanger by double helix flowing of fluid medium in or out of heat exchange tube | |
| CN201281561Y (en) | Shell-pipe head exchanger by double helix flowing of fluid medium in or out of heat exchange tube | |
| CN107255422A (en) | Shell side multiple flow wound tube heat exchanger | |
| CN1140764C (en) | Axial flow-type heat exchanger with convergent-divergent tube, full counterflow and dual shell passes and its heat-exchange method | |
| CN2723940Y (en) | Heat exchanger in hot water supply system | |
| CN208139899U (en) | Heat exchanger and heat-exchange system | |
| CN2754038Y (en) | Twist flat-tube heat exchanger | |
| CN108253821A (en) | A kind of tube bank coiled heat exchanger | |
| CN201715899U (en) | Double-thread spiral pipe reverse flow heat exchanger | |
| CN201434621Y (en) | Multiple spiral flow shell and tube heat exchanger for fluid outside heat transfer tubes | |
| CN108519007A (en) | A kind of self-supporting double helix finned tube exchanger | |
| CN208398689U (en) | A kind of self-supporting double helix finned tube exchanger | |
| CN206724748U (en) | Spiral winding tube type heat exchanger | |
| CN2901224Y (en) | Non-continuous asymmetric corrugated tube heat exchanger | |
| CN216845784U (en) | Multi-flow structure wound tube type heat exchanger | |
| CN206974236U (en) | Shell side multiple flow wound tube heat exchanger | |
| CN110542334A (en) | Pure countercurrent shell and tube type fresh water cooler | |
| CN206724747U (en) | Spiral winding tube type heat exchanger | |
| CN216245714U (en) | Double-tube pass wound tube heat exchanger | |
| CN105823349B (en) | Two-tube-pass mixed tube bundle heat exchanger | |
| CN207976014U (en) | A kind of tube bank coiled heat exchanger |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |