CN103292618A - Heat exchanger - Google Patents
Heat exchanger Download PDFInfo
- Publication number
- CN103292618A CN103292618A CN2013101642699A CN201310164269A CN103292618A CN 103292618 A CN103292618 A CN 103292618A CN 2013101642699 A CN2013101642699 A CN 2013101642699A CN 201310164269 A CN201310164269 A CN 201310164269A CN 103292618 A CN103292618 A CN 103292618A
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- heat
- tube
- spiral
- group
- 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.)
- Granted
Links
Images
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention belongs to the technical field of cooling devices, and relates to a heat exchanger, in particular to a heat exchanger in a modified structure adopting spiral heat exchange tubes to realize cooling. The heat exchanger comprises a shell and a bottom cover, and heat exchange tubes are arranged in a sealed cavity formed by the shell and the bottom cover. The heat exchanger is characterized in that the heat exchange tubes include at least one group of spiral tubes, each group of spiral tubes includes more than two parallel spiral sub-tubes in same length, the bottom end of each spiral sub-tube is connected to a main feed pipe, and the top end thereof is connected to a main discharge pipe. An overturning structure capable of changing positions of the internal spiral sub-tube and the external spiral sub-tube side by side by 180 degrees is arranged in the middle of each group of the spiral tubes, so that heat radiation area is enlarged, positions of the parallel spiral sub-tubes can be changed after 180-degree overturning, integral heat radiation is uniform, heat exchange efficiency is high, and size is small. Since a coolant inlet and a coolant outlet of the sealing cavity and cooled medium inlets and outlets of the heat exchange tubes are led from the bottom cover, the heat exchanger is convenient to clean and maintain.
Description
Technical field
The present invention relates to the cooling device technical field, be specifically related to the heat converter structure improvement aspect that adopts the spiral heat-exchange tube to cool off.
Background technology
At present, for liquid or gas are cooled off, generally be to adopt high-temperature fluid or gas are imported in the spiral helicine heat-exchange tube, heat-exchange tube places cooling fluid, absorb heat-exchange tube by cooling fluid and conduct the heat that, reach cooling, the purpose of heat exchange.And present heat-exchange tube is higher owing to the less segment temperature in interval in the heat-exchange tube, and bigger at interval segment temperature is lower, and the heat that cooling fluid absorbs fails in time to be spread apart, and it is inhomogeneous to dispel the heat, and heat exchanger effectiveness is low.
Summary of the invention
In sum, the objective of the invention is to solve present heat exchanger and exist heat radiation inhomogeneous, the technical deficiency of heat exchanger effectiveness, and a kind of heat exchanger is proposed.
For solving technical problem proposed by the invention, the technical scheme of employing is: a kind of heat exchanger, include shell and bottom, and in the annular seal space of shell and bottom formation, be provided with heat-exchange tube; It is characterized in that: described heat-exchange tube includes one group of helix tube at least, and every group of helix tube constitutes by two identical spiral pipes side by side of above total length, and each spiral pipe bottom all is connected on the charging house steward, and the top all is connected on the discharge header pipe; Every group of helix tube is formed with a torsion structure that will and come internal helicoid pipe and external helicoid pipe location swap 180 degree at medium position.
When described helix tube is more than two groups the time, each spiral ring layer of organizing helix tube is stacked setting at interval.
The center of described bottom is provided with three-way connection, and straight-through section center line of three-way connection and the central lines of bottom are socketed with a cooling fluid water conservancy diversion sleeve pipe that places each helix tube inner ring on the top of three-way connection; Described charging house steward draws through described bottom non-central location, and described discharge header pipe is connected with one through straight-through section discharging straight tube of drawing of described cooling fluid water conservancy diversion sleeve pipe and three-way connection; Be positioned at cooling fluid water conservancy diversion sleeve pipe periphery at bottom and be provided with cooling liquid inlet, remain with the gap between straight-through section inwall of described discharging straight tube outer wall and three-way connection, the side of three-way connection is cooling liquid outlet.
Be filled with the cooling fluid membrane layer between the inwall of described heat-exchange tube and shell.
Top or the bottom of described heat-exchange tube are provided with sealing ring.
Be provided with elasticity between each helical layer ring layer of described each helix tube and separate fastener.
The bottom of described shell is tightly connected by ring flange and bottom.
The cooling fluid import and export of described annular seal space, and the import and export of the medium that is cooled of heat-exchange tube is drawn by described bottom.
The spiral pipe that constitutes described heat-exchange tube adopts the following conduit of diameter 10mm.
Beneficial effect of the present invention is: the spiral pipe that heat-exchange tube of the present invention includes more than two side by side constitutes many group helix tubes; Each spiral ring layer of organizing helix tube is stacked setting at interval; Every group of helix tube is formed with a torsion structure that will and come internal helicoid pipe and external helicoid pipe location swap 180 degree at medium position, not only enlarged radiating surface, after 180 degree reverse, each spiral pipe position side by side will be changed, and makes integral heat sink even, the heat exchanger effectiveness height, and volume is little, because the cooling fluid import and export of annular seal space, and the import and export of the medium that is cooled of heat-exchange tube draws by described bottom, then makes things convenient for clean and maintenance.The present invention can also oppositely use except can cooling off usefulness to the meson in the heat-exchange tube, that is to say the meson in the heat-exchange tube is oppositely heated usefulness.
Description of drawings
Fig. 1 is perspective view of the present invention;
Fig. 2 is decomposition texture schematic diagram of the present invention;
Fig. 3 is heat-exchange tube structure for amplifying schematic diagram of the present invention;
Fig. 4 is that two groups of helix tubes of the present invention constitute the structural principle schematic diagram that heat-exchange tube is simplified;
Structural principle schematic diagram when Fig. 5 is three the single group of spiral pipe formation helix tubes for the present invention.
The specific embodiment
Below in conjunction with the preferred specific embodiment of accompanying drawing the present invention structure of the present invention is further described.
Shown in Fig. 5, the present invention includes shell 1 and bottom 2, shell 1 integral body is cylindrical, the bottom of described shell 1 is tightly connected by ring flange 11 and bottom 2; According to the material hardness of shell 1, ring flange 11 can be and shell 1 integrative-structure, can be absolute construction also, during absolute construction, shell 1 bottom outer wall establish one with shell 1 with the integrative-structure ring flange 10 of material.Shell 1 and bottom 2 constitute an annular seal space, are provided with heat-exchange tube 3 in annular seal space, and are filled with cooling fluid, and cooling fluid absorbs the heat that heat-exchange tube 3 distributes.For convenience of clean and maintenance, the cooling fluid import and export of annular seal space, and the import and export of the medium that is cooled of heat-exchange tube is drawn by described bottom.
Mainly being made of many groups helix tube referring to figs. 1 through the heat-exchange tube 3 described in Fig. 4, is to be that example describes structure of the present invention with two groups among Fig. 1 to Fig. 4.Heat-exchange tube 3 is made of first group of helix tube 31, second group of helix tube 32, charging house steward 33, discharge header pipe 34 and discharging straight tube 35; First group of helix tube 31 and second group of helix tube 32 constitute by side by side spiral pipe more than two, first group of helix tube 31 and second group of helix tube 32 adopt 8 spiral pipes respectively among Fig. 1 to Fig. 4, each spiral pipe bottom all connects charging house steward 33, the top all connects discharge header pipe 34, each spiral pipe all adopts the following conduit of diameter 10mm, many the sub-pipe of spiral can limited increase radiating surface side by side, it is flat helix tube that many spiral pipes constitute a spiral section, first group of helix tube 31 and second group of flat helix tube that 32 of helix tubes are two same length; Spiral section and cooling fluid energy even contact for first group of helix tube 31 and second group of helix tube 32, the spiral section of the spiral section of first group of helix tube 31 and second group of helix tube 32 is stacked setting at interval, that is to say in manufacturing process coiling well wherein after one group of helix tube 31, another group helix tube carries out coiling in the gap of last helix tube 31.Reach identical radiating effect between the sub-pipe of each spiral for first group of helix tube 31 and second group of helix tube 32, first group of helix tube 31 and second group of helix tube 32 are formed with a torsion structure that will and come internal helicoid pipe and external helicoid pipe location swap 180 degree at medium position, then in first group of helix tube 31 top side by side near the spiral pipe 311 at the center, after the Rotate 180 degree, these spiral pipe 311 bottoms will and come outermost; Equally, constitute each spiral pipe of second group of helix tube 32, after the degree of Rotate 180 degree, each spiral pipe position, the interior outside exchanges, and it is identical to reach the sub-tube heat exchange effect of each spiral, has avoided local temperature difference bigger, has improved heat exchanger effectiveness.Constitute the spiral pipe coiling of first group of helix tube 31 and second group of helix tube 32 for convenience, and be convenient to cooling fluid circulation, the intersegmental elasticity that is provided with of each helical layer of described first group of helix tube 31 and second group of helix tube 32 is separated fastener (not drawing among the figure), each helical layer section can be established 2 ~ 4 elasticity and separated fasteners and isolate separately, reaches the purpose that spiral section is positioned.
Shown in Fig. 5, see heat-exchange tube 3 winding structures of the present invention for convenience clearly, adopt three spiral pipes 311 to constitute single group helix tube 31 among the figure, article three, spiral pipe 311 bottoms all connect charging house steward 33, the top all connects discharge header pipe 34, discharge header pipe 34 connects discharging straight tube 341, article three, the list of spiral pipe 311 formations is organized helix tube 31 medium position Rotate 180 degree, form the torsion structures 30 of 180 degree, that is to say when side by side three spirals pipes 311 are coiling to middle section position and carry out continuing coiling again after the 180 degree rotations.
Referring to figs. 1 through shown in Figure 5, the liquid that is cooled for the ease of need or the gas medium that is cooled imports in the heat-exchange tube 3, and be convenient to the cooling fluid injection and discharge shell 1 and annular seal space of bottom 2 formations, be provided with three-way connection 21 at the center of described bottom 2, straight-through section center line of three-way connection 21 and the central lines of bottom are socketed with a cooling fluid water conservancy diversion sleeve pipe 22 that places first group of helix tube 31 and second group of helix tube 32 inner ring on the top of three-way connection 21; Described charging house steward 33 draws through described bottom 2 non-central locations, also namely is provided with the charging hole 23 of drawing for charging house steward 33 at bottom 2 non-central locations, and 23 of charging holes are the medium import that is cooled; If need consider that be cooled medium discharging and charging are in same direction, described discharge header pipe 34 is connected with one through straight-through section discharging straight tube 341 of drawing of described cooling fluid water conservancy diversion sleeve pipe 22 and three-way connection 21, the bottom mouth of pipe of discharging straight tube 341 is the media outlet that is cooled, for better sealed discharging straight tube 341, the bottom end opening of three-way connection 21 is provided with the sealing-plug of a band discharge opening; Be positioned at cooling fluid water conservancy diversion sleeve pipe 22 peripheries at bottom 2 and be provided with cooling liquid inlet 24, remain with the gap between straight-through section inwall of described discharging straight tube 341 outer walls and three-way connection 21, the side of three-way connection 21 is cooling liquid outlet 25.In the use, need liquid or the gas of cooling to enter from charging house steward 33, flow to the top from the bottom of first group of helix tube 31 and second group of helix tube 32 simultaneously, after discharge header pipe 34 gathers, draw through discharging straight tube 341; Cooling fluid then enters the annular seal space bottom from cooling liquid inlet 24, overflow into from cooling fluid water conservancy diversion sleeve pipe 22 tops then, the gap that keeps between straight-through section inwall finally by discharging straight tube 341 outer walls and three-way connection 21 is that cooling liquid outlet 25 is discharged from the side of three-way connection 21.
Between the inwall of described heat-exchange tube 3 and shell 1, be filled with cooling fluid membrane layer 4, thermal insulation layer 4 stops that cooling fluid directly flows through from the gap of heat-exchange tube 3 and the inwall of shell 1, thereby cause the cooling fluid in heat-exchange tube 3 internal clearances not circulate, or circulation is slower, causes heat-exchange tube 3 heat radiations slow.
In order to guarantee that better heat eliminating medium requires to flow in accordance with regulations, the top of described heat-exchange tube 3 or bottom are provided with sealing ring 5.
Claims (9)
1. a heat exchanger includes shell and bottom, is provided with heat-exchange tube in the annular seal space of shell and bottom formation; It is characterized in that: described heat-exchange tube includes one group of helix tube at least, and every group of helix tube constitutes by two identical spiral pipes side by side of above total length, and each spiral pipe bottom all is connected on the charging house steward, and the top all is connected on the discharge header pipe; Every group of helix tube is formed with a torsion structure that will and come internal helicoid pipe and external helicoid pipe location swap 180 degree at medium position.
2. a kind of heat exchanger according to claim 1 is characterized in that: when described helix tube is more than two groups the time, each spiral ring layer of organizing helix tube is stacked setting at interval.
3. a kind of heat exchanger according to claim 1, it is characterized in that: the center of described bottom is provided with three-way connection, straight-through section center line of three-way connection and the central lines of bottom are socketed with a cooling fluid water conservancy diversion sleeve pipe that places each helix tube inner ring on the top of three-way connection; Described charging house steward draws through described bottom non-central location, and described discharge header pipe is connected with one through straight-through section discharging straight tube of drawing of described cooling fluid water conservancy diversion sleeve pipe and three-way connection; Be positioned at cooling fluid water conservancy diversion sleeve pipe periphery at bottom and be provided with cooling liquid inlet, remain with the gap between straight-through section inwall of described discharging straight tube outer wall and three-way connection, the side of three-way connection is cooling liquid outlet.
4. a kind of heat exchanger according to claim 1 is characterized in that: be filled with the cooling fluid membrane layer between the inwall of described heat-exchange tube and shell.
5. a kind of heat exchanger according to claim 1, it is characterized in that: top or the bottom of described heat-exchange tube are provided with sealing ring.
6. a kind of heat exchanger according to claim 1 is characterized in that: be provided with the separation keeper between each helical layer ring layer of described each helix tube.
7. a kind of heat exchanger according to claim 1, it is characterized in that: the bottom of described shell is tightly connected by ring flange and bottom.
8. a kind of heat exchanger according to claim 1 is characterized in that: the cooling fluid import and export of described annular seal space, and the import and export of the medium that is cooled of heat-exchange tube is drawn by described bottom.
9. a kind of heat exchanger according to claim 1 is characterized in that: the following conduit of spiral pipe employing diameter 10mm that constitutes described heat-exchange tube.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310164269.9A CN103292618B (en) | 2013-05-07 | 2013-05-07 | A kind of heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310164269.9A CN103292618B (en) | 2013-05-07 | 2013-05-07 | A kind of heat exchanger |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103292618A true CN103292618A (en) | 2013-09-11 |
CN103292618B CN103292618B (en) | 2016-02-03 |
Family
ID=49093892
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310164269.9A Active CN103292618B (en) | 2013-05-07 | 2013-05-07 | A kind of heat exchanger |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103292618B (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104489208A (en) * | 2014-12-25 | 2015-04-08 | 重庆勤发食品有限公司 | Device for cooling peach slice pulp |
CN107941413A (en) * | 2017-12-27 | 2018-04-20 | 苏州康姆普机械有限公司 | A kind of thermal insulation protection pressure sensor |
CN108590836A (en) * | 2018-07-03 | 2018-09-28 | 安吉前程竹木机械有限公司 | A kind of auto parts machinery |
CN112432520A (en) * | 2020-10-12 | 2021-03-02 | 浦江春生夏长环保科技有限公司 | Geothermal circulation heat exchange assembly |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201218635Y (en) * | 2008-05-27 | 2009-04-08 | 英特换热设备(浙江)有限公司 | High-efficiency condenser for sea water desalting |
CN101726109A (en) * | 2009-11-27 | 2010-06-09 | 广东诺科冷暖设备有限公司 | High-efficiency condensing type heat exchanger |
US20110174470A1 (en) * | 2010-01-20 | 2011-07-21 | Asia Vital Components Co., Ltd. | Spiral heat exchanger |
CN202613741U (en) * | 2011-08-04 | 2012-12-19 | 周卫红 | Hollow cylindrical-shaped heat exchanger |
CN203375861U (en) * | 2013-05-07 | 2014-01-01 | 周良海 | Heat exchanger |
-
2013
- 2013-05-07 CN CN201310164269.9A patent/CN103292618B/en active Active
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN201218635Y (en) * | 2008-05-27 | 2009-04-08 | 英特换热设备(浙江)有限公司 | High-efficiency condenser for sea water desalting |
CN101726109A (en) * | 2009-11-27 | 2010-06-09 | 广东诺科冷暖设备有限公司 | High-efficiency condensing type heat exchanger |
US20110174470A1 (en) * | 2010-01-20 | 2011-07-21 | Asia Vital Components Co., Ltd. | Spiral heat exchanger |
CN202613741U (en) * | 2011-08-04 | 2012-12-19 | 周卫红 | Hollow cylindrical-shaped heat exchanger |
CN203375861U (en) * | 2013-05-07 | 2014-01-01 | 周良海 | Heat exchanger |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104489208A (en) * | 2014-12-25 | 2015-04-08 | 重庆勤发食品有限公司 | Device for cooling peach slice pulp |
CN107941413A (en) * | 2017-12-27 | 2018-04-20 | 苏州康姆普机械有限公司 | A kind of thermal insulation protection pressure sensor |
CN107941413B (en) * | 2017-12-27 | 2024-06-04 | 苏州康姆普机械有限公司 | Heat-insulating protection pressure sensor |
CN108590836A (en) * | 2018-07-03 | 2018-09-28 | 安吉前程竹木机械有限公司 | A kind of auto parts machinery |
CN112432520A (en) * | 2020-10-12 | 2021-03-02 | 浦江春生夏长环保科技有限公司 | Geothermal circulation heat exchange assembly |
Also Published As
Publication number | Publication date |
---|---|
CN103292618B (en) | 2016-02-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN203375861U (en) | Heat exchanger | |
CN103292618A (en) | Heat exchanger | |
CN209655859U (en) | A kind of heat-exchanging component and high-performance heat exchanger | |
CN205011733U (en) | Novel making wine equipment | |
CN204574866U (en) | Waste water heat reclaim unit | |
CN104374098A (en) | Vacuum tube solar heat collector | |
CN104567481B (en) | A kind of wound tube heat exchanger | |
CN210400083U (en) | Heat exchanger with sufficient cooling | |
CN105387744B (en) | A kind of process energy conservation storage heater of cold and hot shunting | |
CN203518710U (en) | Spiral countercurrent flow heat exchange device provided with heat exchange tubes with inward-protruded ribs | |
CN206094990U (en) | Multilayer bushing type pre -heater | |
CN210128640U (en) | Double-tube plate heat exchanger | |
CN201593930U (en) | Tower-type efficient liquid condensing collector | |
CN205373482U (en) | Energy -conserving heat accumulator of process of cold and hot reposition of redundant personnel | |
CN102072678B (en) | Water bath type gasifying device | |
CN201974067U (en) | Water-bath type gasifier | |
CN202740795U (en) | Tangential feeding efficient falling film evaporator | |
CN212721020U (en) | Cold and hot energy storage conversion equipment system | |
CN206094994U (en) | Bushing type pre -heater | |
CN213811898U (en) | Spiral gradually-changed fin phase-change heat accumulator | |
CN201772812U (en) | Corrosion-resistant plastic heat exchanger | |
CN204285850U (en) | A kind of vacuum tube solar heating element | |
CN203893706U (en) | Heat exchanger with spiral tube banks | |
CN208432139U (en) | Superconduction heat exchange unit and its device, system | |
CN209230360U (en) | A kind of corrosion resistant sealed single-pipe silicon carbide tubular 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 | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |