CN206019419U - Heat exchanger - Google Patents
Heat exchanger Download PDFInfo
- Publication number
- CN206019419U CN206019419U CN201620647666.0U CN201620647666U CN206019419U CN 206019419 U CN206019419 U CN 206019419U CN 201620647666 U CN201620647666 U CN 201620647666U CN 206019419 U CN206019419 U CN 206019419U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- exchanger tube
- reducer pipe
- circulation
- port
- 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
- 239000000463 material Substances 0.000 claims abstract description 75
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 37
- 210000005239 tubule Anatomy 0.000 claims abstract description 17
- 238000004140 cleaning Methods 0.000 abstract description 12
- 235000013305 food Nutrition 0.000 abstract description 10
- 238000012545 processing Methods 0.000 abstract description 9
- 239000007788 liquid Substances 0.000 abstract description 6
- 235000013336 milk Nutrition 0.000 abstract description 4
- 239000008267 milk Substances 0.000 abstract description 4
- 210000004080 milk Anatomy 0.000 abstract description 4
- 230000001954 sterilising effect Effects 0.000 abstract description 4
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 4
- 238000005057 refrigeration Methods 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 239000012530 fluid Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 3
- 238000012546 transfer Methods 0.000 description 3
- 239000011538 cleaning material Substances 0.000 description 2
- 235000019628 coolness Nutrition 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 238000000429 assembly Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 235000005770 birds nest Nutrition 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 235000021056 liquid food Nutrition 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 235000005765 wild carrot Nutrition 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model heat exchanger is included in heat exchanger tube arranged in parallel under transversely, along heat exchanger tube internal pipeline parallel be provided with material circulation tubule, and the cavity for supplying flow of media is formed in heat exchanger tube internal pipeline, the adapter of medium S-type circulation is available for through setting between adjacent heat exchange tubes simultaneously, the port of every row's heat exchanger tube both sides bore is provided with end socket I, the U-shaped bend pipe of the reducer pipe I and connection both sides reducer pipe I for being available for the S-type circulation of material is fixedly connected between adjacent heat exchange tubes two-port, material inlet is set respectively in two ports of heat exchanger tube of S-type circulating form, material outlet.The utility model beneficial effect：Simple structure, with low cost, be easily assembled to, simple operation, cleaning thoroughly, the refrigeration of achievable milk, food liquid etc., high temperature sterilization, heat exchange efficiency height, simple structure, easy processing and low cost, without cleaning dead angle inside heat exchanger, can be with effectively solving because not washing clean clearly the generation of situations such as causing rotten.
Description
Technical field
The utility model is related to the heat displacement apparatus such as refrigeration, high temperature sterilization field, specially milk and other liquid food
The heat exchanger of the quickly coolings such as product.
Background technology
Heat exchanger is a kind of section for realizing heat transfer between material between two or more fluid of different temperatures
Energy equipment, is to make heat pass to the relatively low fluid of temperature by higher fluid, makes fluid temperature (F.T.) reach the index of flow specification,
One of to meet the needs of process condition, while also improve the capital equipment of energy utilization rate, also known as heat exchanger.Heat exchange
Device is the common apparatus of chemical industry, oil, power, food and other many Industry departments, occupies critical role aborning.
In recent years, with the improvement of people's living standards, vigorous to food demand, promote food industry to obtain fast development.For chasing after
Ask low cost, high benefit, numerous food product enterprise constantly to expand the scale of production so that food mechanical equipment to maximization, serialization,
Automation direction develops.On the other hand, demand is obtained according to market diversification, being particularly some agricultural byproducts processings has its season
Property feature, it is desirable to the more production of equipment application, with set up can multi items, production system that is a small amount of and being rich in economic benefit.Cause
This, the heat exchanger as most basic operation-heating in food processing, sterilization, cooling will also adapt to multi items, small lot
Production, should be heat-treated to the raw material of various physical property, can process season product again.Due to food processing increasingly complicated,
Must be designed according to industry itself productive prospecting, manufacture heat transmission equipment, and while production equipment service firing, it is also noted that
The attachment of bird nest is prevented, this is accomplished by effectively being cleaned, otherwise clean not thoroughly, make the residual that processes raw material for a long time, can lead
Microorganism amount reproduction is caused, the quality for processing raw material eventually is affected.
, mainly based on plate type heat exchanger, this kind of heat exchanger consumption is very big, accounts for total amount for currently known heat exchanger
More than 99%, plate type heat exchanger is by a series of a kind of heat exchanger of sheet metal closed assemblies with certain bellows-shaped.Respectively
Planting and thin rectangular shape passage is formed between plate, heat exchange is carried out by plate.Plate type heat exchanger is that liquid liquid, liquid vapour carry out heat
The equipment of exchange.Although plate type heat exchanger heat exchange area is big, heat exchange efficiency is high, there is cleaning dead angle inside plate type heat exchanger,
For the quickly coolings such as milk, food liquid, processing industry, thoroughly cleaning to be realized becomes abnormal difficult.
Utility model content
The purpose of this utility model is for the deficiencies in the prior art, propose a kind of simple structure, with low cost, be easy to
Assembling, simple operation, cleaning thoroughly heat exchanger.
The utility model heat exchanger includes：In heat exchanger tube arranged in parallel under transversely, parallel along heat exchanger tube internal pipeline
Be provided with material circulation tubule, and form the cavity for flow of media in the heat exchanger tube internal pipeline, at the same adjacent heat exchange tubes it
Between be available for the adapter of the S-type circulation of medium through arranging, the port of every row's heat exchanger tube both sides bore is provided with end socket I,
The U of the reducer pipe I and connection both sides reducer pipe I for being available for the S-type circulation of material is fixedly connected between adjacent heat exchange tubes two-port
Type bend pipe, sets material inlet, material outlet respectively in two ports of heat exchanger tube of S-type circulating form.
It is fixedly connected by end socket II between described reducer pipe I and U-shaped bend pipe.The installation of end socket II can cause reducer pipe
I is easy to disassemble with U-shaped bend pipe, more conducively cleans, time saving and energy saving.
At the heat exchanger tube two-port of described S-type circulating form, fixation connects between material inlet, material outlet respectively
Meet reducer pipe II.The setting of reducer pipe II is more convenient for cleaning material inlet, residual processes raw material at material outlet.
The heat exchanger tube of described S-type circulating form is respectively equipped with Jie near two ends and through heat exchanger tube upper wall, lower wall
Matter outlet, medium inlet.
The beneficial effects of the utility model：
1) along heat exchanger tube internal pipeline parallel be provided with material circulation tubule, be fixedly connected between adjacent heat exchange tubes two-port
There is the U-shaped bend pipe of the reducer pipe I and connection both sides reducer pipe I for being available for the S-type circulation of material, lead between reducer pipe I and U-shaped bend pipe
Cross end socket II to be fixedly connected, material inlet, material outlet is set respectively in two ports of heat exchanger tube of S-type circulating form,
The material being processed during use enters into material by material inlet and circulates in tubule, and then is circulated to reducer pipe I and U
Type bend pipe and then S-type circulation in the material circulation tubule, flow out finally by material outlet, therefore can be in reducer pipe I and U-shaped
There is residual in bend pipe, as reducer pipe I and U-shaped bend pipe interior surface adopt the design of radian, not only so that material circulation is more smooth
Logical, residual is reduced, and causes cleaning more thorough, convenient, the end socket II arranged between reducer pipe I and U-shaped bend pipe, further
Make cleaning become to be more prone to, convenient, thorough, time saving and energy saving, simultaneously facilitate dismounting and install, preferably used by people；
2) it is fixedly connected between material inlet, material outlet at the heat exchanger tube two-port of S-type circulating form respectively
Reducer pipe II, at thoroughly cleaning of being more convenient for material inlet, material outlet, residual processes raw material；
3) heat exchanger tube in S-type circulating form is respectively equipped with medium near two ends and through heat exchanger tube upper wall, lower wall
Outlet, medium inlet, and the port of every row's heat exchanger tube both sides bore is provided with end socket I, during use, can pass through
The medium inlet for being located at heat exchanger tube lower wall adds medium (frozen water, hot water, cold-producing medium, steam), and medium is inside heat exchanger tube and thing
By taking over S-type circulation in the cavity formed between the logical tubule of stream, the setting of end socket I can prevent medium from flowing into reducer pipe I
And mix with material in U-shaped bend pipe, fully ensure that processing materials and medium separates circulation；
4) simple structure, with low cost, be easily assembled to, simple operation, cleaning thoroughly, can achieve milk, food liquid etc.
Refrigeration, high temperature sterilization, heat exchange efficiency height, simple structure, easy processing and low cost, without cleaning dead angle inside heat exchanger, can be with
Effectively solving is not because washing clean clearly the generation of situations such as causing rotten.
Description of the drawings
Structural representations of the Fig. 1 for heat exchanger.
Profiles of the Fig. 2 for heat exchanger A-A.
In figure：Heat exchanger tube 1, material circulation tubule 2, cavity 3, end socket I 4, reducer pipe I 5, adapter 6, U-shaped bend pipe 7, Jie
Matter outlet 8, medium inlet 9, material inlet 10, material outlet 11, reducer pipe II 12, end socket II 13.
Specific embodiment
Embodiment 1.
Below with reference to accompanying drawing 1,2, the utility model is described in further detail.
The utility model is circulated tubule 2, cavity 3, end socket I 4, reducer pipe I 5, adapter 6, U-shaped curved by heat exchanger tube 1, material
Pipe 7, material inlet 10, material outlet 11, reducer pipe II 12 are constituted, and specific structure is：Change in arranged in parallel under transversely
Heat pipe 1, is provided with material circulation tubule 2 along 1 internal pipeline of heat exchanger tube is parallel, and is formed in 1 internal pipeline of heat exchanger tube and supply medium
The cavity 3 of circulation, while being available for the adapter 6 of the S-type circulation of medium between adjacent heat exchange tubes 1 through setting, exchanges heat in every row
The port of 1 both sides bore of pipe is provided with end socket I 4, and it is in S to be fixedly connected between 1 two-port of adjacent heat exchange tubes and be available for material
The reducer pipe I 5 of type circulation and the U-shaped bend pipe 7 of connection both sides reducer pipe I 5, at 1 two ends of heat exchanger tube of S-type circulating form
Material inlet 10, material outlet 11 are set respectively at mouthful.At 1 two-port of heat exchanger tube of described S-type circulating form respectively with thing
Reducer pipe II 12 is fixedly connected between material entrance 10, material outlet 11.The setting of reducer pipe II is more convenient for cleaning material inlet
10th, remained at material outlet 11 processes raw material.The quantity of described material material circulation tubule 2 is 12, and radius is 19,
The radius of described heat exchanger tube 1 is 108.
Using method：Material outlet 11 is blocked, into the heat exchanger tube 1 of bottom injected media (frozen water, hot water, cold-producing medium,
Steam), by 6 S-type circulation of adapter in the cavity 3 that medium is formed inside heat exchanger tube 1 and material circulation tubule 2 between, when
Medium full of after 1 pipeline of whole heat exchanger tube, closed by end socket I 4 by whole cavity 3, and now into material inlet 10, injection will add again
The material of work, material circulate along material circulation tubule 2, and then are circulated to reducer pipe I 5 and U-shaped bend pipe 7 and then circulate in material
S-type circulation in tubule 2, material are entered from material inlet 10 and are flowed in 1 internal pipeline of heat exchanger tube with the direction of relative medium, from
Material outlet 11 flows out, using heat transfer principle, so as to reach heat displacement.Using medium and material convection type, Hot swapping
Efficiency high.As reducer pipe I 5 and 7 interior surface of U-shaped bend pipe adopt the design of radian, not only so that material circulation is more unimpeded,
Residual is reduced, and causes cleaning more thorough, convenient.
Embodiment 2.
Below with reference to accompanying drawing 1,2, the utility model is described in further detail.
The utility model is circulated tubule 2, cavity 3, end socket I 4, reducer pipe I 5, adapter 6, U-shaped curved by heat exchanger tube 1, material
Pipe 7, material inlet 10, material outlet 11, reducer pipe II 12, end socket II 13 are constituted, specific structure with described in embodiment 1,
It is fixedly connected by end socket II 13 between described reducer pipe I 5 and U-shaped bend pipe 7.
With described in embodiment 1, described end socket II further makes cleaning become to be more prone to, convenient, thorough to using method
Bottom, time saving and energy saving, simultaneously facilitate dismounting and install, preferably used by people.
Embodiment 3.
Below with reference to accompanying drawing 1,2, the utility model is described in further detail.
The utility model is circulated tubule 2, cavity 3, end socket I 4, reducer pipe I 5, adapter 6, U-shaped curved by heat exchanger tube 1, material
Pipe 7, media outlet 8, medium inlet 9, material inlet 10, material outlet 11, reducer pipe II 12, end socket II 13 are constituted, specifically
Structure with described in embodiment 1, the heat exchanger tube of described S-type circulating form 1 near two ends and through 1 upper wall of heat exchanger tube,
Lower wall is respectively equipped with media outlet 8, medium inlet 9.
Using method：Medium (frozen water, hot water, cold-producing medium, steaming can be added by being located at the medium inlet 9 of 1 lower wall of heat exchanger tube
Vapour), by 6 S-type circulation of adapter, end socket I in the cavity 3 that medium is formed inside heat exchanger tube 1 and material circulation tubule 2 between
4 setting can prevent from mixing with material in medium inflow reducer pipe I5 and U-shaped bend pipe 7, fully ensure that processing materials with medium
Separately circulate, after medium is filled it up with, material can be added by material inlet 10, make material with the direction of relative medium in heat exchanger tube
1 internal pipeline flows, and flows out from material outlet 11, using heat transfer principle, so as to reach heat displacement.Using medium and material
Convection type, Hot swapping efficiency high.
Claims (4)
1. heat exchanger, it is characterised in that the heat exchanger includes：In heat exchanger tube (1) arranged in parallel under transversely, along heat exchanger tube
(1) internal pipeline is parallel is provided with material circulation tubule (2), and forms the sky for flow of media in heat exchanger tube (1) internal pipeline
Chamber (3), while the adapter (6) of the S-type circulation of medium is available between adjacent heat exchange tubes (1) through setting, in every row's heat exchanger tube
(1) port of both sides bore is provided with end socket I (4), is fixedly connected with and is available for material between adjacent heat exchange tubes (1) two-port
The reducer pipe I (5) of S-type circulation and the U-shaped bend pipe (7) of connection both sides reducer pipe I (5), in the heat exchanger tube of S-type circulating form
(1) two port sets material inlet (10), material outlet (11) respectively.
2. heat exchanger as claimed in claim 1, it is characterised in that：Pass through between described reducer pipe I (5) and U-shaped bend pipe (7)
End socket II (13) is fixedly connected.
3. heat exchanger as claimed in claim 1, it is characterised in that：Heat exchanger tube (1) two-port of described S-type circulating form
Place is fixedly connected reducer pipe II (12) respectively between material inlet (10), material outlet (11).
4. the heat exchanger as described in one of claim 1,2,3, it is characterised in that：The heat exchanger tube of described S-type circulating form
(1) near two ends and run through heat exchanger tube (1) upper wall, lower wall and be respectively equipped with media outlet (8), medium inlet (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620647666.0U CN206019419U (en) | 2016-06-27 | 2016-06-27 | Heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620647666.0U CN206019419U (en) | 2016-06-27 | 2016-06-27 | Heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206019419U true CN206019419U (en) | 2017-03-15 |
Family
ID=58243930
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620647666.0U Expired - Fee Related CN206019419U (en) | 2016-06-27 | 2016-06-27 | Heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206019419U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109405598A (en) * | 2018-11-08 | 2019-03-01 | 上海慧得节能科技有限公司 | Variable diameter tube side heat exchanger for hot-blast stove |
| CN110326734A (en) * | 2019-07-23 | 2019-10-15 | 浙江百珍堂食品有限公司 | A kind of soup ice slurry cooling technique |
-
2016
- 2016-06-27 CN CN201620647666.0U patent/CN206019419U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109405598A (en) * | 2018-11-08 | 2019-03-01 | 上海慧得节能科技有限公司 | Variable diameter tube side heat exchanger for hot-blast stove |
| CN109405598B (en) * | 2018-11-08 | 2024-05-14 | 上海慧得节能科技有限公司 | Reducing pipe-line hot-blast stove heat exchanger |
| CN110326734A (en) * | 2019-07-23 | 2019-10-15 | 浙江百珍堂食品有限公司 | A kind of soup ice slurry cooling technique |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205011733U (en) | Novel making wine equipment | |
| CN206019419U (en) | Heat exchanger | |
| CN201600062U (en) | Demountable complete contra-flow cooling medium to water heat exchanger for air source heat pump | |
| CN208901932U (en) | A kind of high efficient heat exchanging system | |
| CN207197316U (en) | A kind of big number double-tube heat exchanger of high energy efficiency | |
| CN203687378U (en) | Water tank used for heat pump water heater | |
| CN205991726U (en) | Storage tank formula heat-exchanger rig is used in a kind of Wet-smelting method | |
| CN201972002U (en) | Energy-saving dyeing machine | |
| CN203550696U (en) | Plate heat exchanger | |
| CN201764873U (en) | Drain pipe flow diversion and heat exchange plate and heat exchanger using heat exchange plate | |
| CN209166192U (en) | A kind of starch-based product production plate heat exchanger structure | |
| CN206404756U (en) | A kind of multi-function outer circulation kettle system | |
| CN215295907U (en) | Corrosion-resistant heat exchanger | |
| CN205014864U (en) | Heat exchanger fin and adopt dislocation formula heat exchanger of this heat exchanger fin | |
| CN212841794U (en) | Ready-package hot press heating equipment | |
| CN208296647U (en) | A kind of petroleum pipeline heat-exchanger rig | |
| CN205102620U (en) | Detachable condenser | |
| CN209558959U (en) | Heat exchanger containing solid slurry | |
| CN209263453U (en) | A kind of circulation | |
| CN221714269U (en) | Reation kettle control by temperature change mechanism for catalyst production | |
| CN222528399U (en) | Efficient heat exchanger | |
| CN211854990U (en) | Air cooler with good cooling effect | |
| CN205077149U (en) | Plate heat exchanger online cleaning equipment | |
| CN214346355U (en) | A reation kettle for chemical synthesis | |
| CN222012791U (en) | Petrochemical uses high-efficient heat exchanger |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170315 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |