CN208635614U - A kind of shell side formula condenser of high efficient heat exchanging - Google Patents
A kind of shell side formula condenser of high efficient heat exchanging Download PDFInfo
- Publication number
- CN208635614U CN208635614U CN201820820295.0U CN201820820295U CN208635614U CN 208635614 U CN208635614 U CN 208635614U CN 201820820295 U CN201820820295 U CN 201820820295U CN 208635614 U CN208635614 U CN 208635614U
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- China
- Prior art keywords
- partition
- cylinder
- high efficient
- right end
- heat exchanging
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- Expired - Fee Related
Links
- 238000005192 partition Methods 0.000 claims abstract description 41
- 239000000463 material Substances 0.000 claims abstract description 20
- 230000003139 buffering effect Effects 0.000 claims abstract description 8
- 239000000498 cooling water Substances 0.000 claims abstract description 7
- 238000009413 insulation Methods 0.000 claims description 11
- 239000005030 aluminium foil Substances 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 6
- 239000011248 coating agent Substances 0.000 claims description 5
- 238000000576 coating method Methods 0.000 claims description 5
- 201000005581 enamel erosion Diseases 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 8
- 238000001816 cooling Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 239000002826 coolant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000005439 thermosphere Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000012809 cooling fluid Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses a kind of shell side formula condensers of high efficient heat exchanging, it is related to cooler technical field, the utility model includes the cylinder of centre and the left head for being located at cylinder both ends and right end socket, cooling water inlet and cooling water outlet are respectively arranged on left head and right end socket, the inner barrel both ends are respectively arranged with first partition and second partition, first partition and left head constitute first material buffer area, main convective region is constituted between first partition and second partition, the second partition and right end socket constitute second buffering area, muti-piece flow-disturbing transverse slat is staggeredly provided in the intracorporal first partition of the cylinder and second partition at equal intervals, main convection current is distinguished into several convective regions by multiple flow-disturbing transverse slats, several heat exchange straight pipelines being connected to first material buffer area and second buffering area are evenly equipped in each convective region, this is practical new Type have structure it is simple, while increase contact cold water and material to be cooled time of contact the advantages of.
Description
Technical field
The utility model relates to novel combination type cooler technical fields, more particularly to a kind of shell of high efficient heat exchanging
Formula condenser.
Background technique
Cooler is one kind of heat exchange equipment, to cooling fluid.It is usually coolant to remove heat with water or air.
There are dividing wall type novel combination type cooler, fountain novel combination type cooler, jacket type novel combination type cooler and coiled pipe
Formula novel combination type cooler etc. is usually coolant to remove heat with water or air.There is dividing wall type novel combination type cooling
Device, fountain novel combination type cooler, jacket type novel combination type cooler and coil pipe type novel combination type cooler etc..
Fluid convection in existing shell-and-tube cooler is apart from small, and the time of contact of cold water and heat exchanger tube is short, cooling effect
Fruit is bad.
How above-mentioned technical problem is solved into the striving direction of those skilled in the art.
Utility model content
The purpose of this utility model is that: it is cold in order to solve the fluid convection in existing shell-and-tube cooler apart from small
The time of contact of water and heat exchanger tube is short, and cooling effect is bad, and the utility model provides a kind of shell side formula condenser of high efficient heat exchanging.
The utility model specifically uses following technical scheme to achieve the goals above:
A kind of shell side formula condenser of high efficient heat exchanging, including intermediate cylinder and the left head and right envelope that are located at cylinder both ends
Cooling water inlet and cooling water outlet are respectively arranged on head, left head and right end socket, the inner barrel both ends are respectively arranged with
First partition and second partition, first partition and left head constitute first material buffer area, between first partition and second partition
Constitute main convective region, the second partition and right end socket constitute second buffering area, the intracorporal first partition of the cylinder and the
Staggeredly be provided with muti-piece flow-disturbing transverse slat at equal intervals on two partitions, the length of flow-disturbing transverse slat be less than first partition and second partition it
Between distance, main convection current is distinguished into several convective regions, is evenly equipped in each convective region several by multiple flow-disturbing transverse slats
The heat exchange straight pipeline being connected to first material buffer area and second buffering area.
Further, cylinder one end of the main convective region is provided with material inlet, and the other end is provided with material outlet.
Further, hang plate that is being staggeredly equipped with several equal lengths up and down in the convective region and being parallel to each other,
The sum of length of two blocks of hang plates be less than adjacent two pieces of flow-disturbing transverse slats 2 times of distances, greater than adjacent two pieces of flow-disturbing transverse slats times away from
From.
Further, the angular range of the hang plate and horizontal plane is 45 ° ~ 60 °.
Further, it is arranged with insulation shell outside the cylinder, left head and right end socket, is provided in insulation shell absolutely
Thermosphere.
Further, the heat insulation layer includes several glass layers and aluminium foil layer of intersecting, the thickness of aluminium foil layer
Degree be 0.18 ~ 0.65mm, glass layer with a thickness of 0.32 ~ 0.78mm.
Further, enamel erosion resistant coating is coated on the inner wall of the cylinder, left head and right end socket.
The beneficial effects of the utility model are as follows:
1, the utility model structure is simple, staggeredly sets at equal intervals in the intracorporal first partition of the cylinder and second partition
It is equipped with muti-piece flow-disturbing transverse slat, the length of flow-disturbing transverse slat is less than the distance between first partition and second partition, described multiple to disturb
It flows transverse slat and main convection current is distinguished into several convective regions, several and first material buffer area and second are evenly equipped in each convective region
The heat exchange straight pipeline of buffer area connection, the setting of this structure increase the time of contact of cold water Yu material delivery branch pipe road, fill
Divide cooling material to be cooled, good cooling results.
2, hang plate that is being staggeredly equipped with several equal lengths up and down in convective region and being parallel to each other, the length of two blocks of hang plates
The sum of degree is less than 2 times of distances of adjacent two pieces of flow-disturbing transverse slats, and greater than times distance of adjacent two pieces of flow-disturbing transverse slats, this structure is set
It sets and further extends cold water and material time of contact, enhance condensation effect.
3, enamel erosion resistant coating is coated on the inner wall of cylinder, left and right end socket, the setting of this erosion resistant coating can cool down
With corrosive material, while avoiding the first novel combination type cooler and the second novel combination type cooler is corroded, tool
There is very strong practicability.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the structural schematic diagram of heat insulation layer.
Specific embodiment
In order to which those skilled in the art better understand the utility model, with reference to the accompanying drawing with following embodiment to this
Utility model is described in further detail.
Embodiment 1
As illustrated in fig. 1 and 2, the present embodiment provides a kind of shell side formula condensers of high efficient heat exchanging, including intermediate 5 He of cylinder
It is located at the left head 2 and right end socket 12 at 5 both ends of cylinder, is respectively arranged with cooling water inlet 1 and cold water on left head 2 and right end socket 12
Outlet 7, which is characterized in that the 5 inside both ends of cylinder are respectively arranged with first partition 3 and second partition 13, first partition 3
First material buffer area 11 is constituted with left head 2, main convective region 10 is constituted between first partition 3 and second partition 13, it is described
Second partition 13 and right end socket 12 constitute second buffering area 8, and the first partition 3 and second partition 13 in the cylinder 5 are submitted
Wrong to be provided with muti-piece flow-disturbing transverse slat 6 at equal intervals, the length of flow-disturbing transverse slat 6 is less than between first partition 3 and second partition 13
Distance, main convective region 10 is divided into several convective region 10-1 by multiple flow-disturbing transverse slats 6, if being evenly equipped in each convective region
The dry heat exchange straight pipeline 6-1 being connected to first material buffer area 11 and second buffering area 8.
5 one end of cylinder of the main convective region 10 is provided with material inlet 4, and the other end is provided with material outlet 9.
Embodiment 2
The present embodiment is to be further optimized on the basis of embodiment 1, specifically:
Hang plate 15 that is being staggeredly equipped with several equal lengths up and down in the convective region 10-1 and being parallel to each other, two pieces
The sum of length of hang plate 15 be less than adjacent two pieces of flow-disturbing transverse slats 62 times of distances, greater than adjacent two pieces of flow-disturbing transverse slats 6 times away from
From.
The angular range of the hang plate 15 and horizontal plane is 45 ° ~ 60 °.
It is arranged with insulation shell 14 outside cylinder 5, left head 2 and the right end socket 12, is provided in insulation shell 14 absolutely
Thermosphere 16.
The heat insulation layer 16 includes several glass layer 16-1 and aluminium foil layer 16-2, aluminium foil layer 16-2 of intersecting
With a thickness of 0.18 ~ 0.65mm, glass layer 16-1 with a thickness of 0.32 ~ 0.78mm.
Enamel erosion resistant coating is coated on the inner wall of the cylinder 5, left head 2 and right end socket 12.
The above, the only preferred embodiment of the utility model, are not intended to limit the utility model, the utility model
Scope of patent protection be subject to claims, it is equivalent made by all specifications and accompanying drawing content with the utility model
Structure change similarly should be included in the protection scope of the utility model.
Claims (7)
1. a kind of shell side formula condenser of high efficient heat exchanging, including intermediate cylinder (5) and it is located at the left head at cylinder (5) both ends
(2) and right end socket (12) it, is respectively arranged with cooling water inlet (1) and cooling water outlet (7) on left head (2) and right end socket (12),
It is characterized in that, the internal both ends of the cylinder (5) are respectively arranged with first partition (3) and second partition (13), first partition (3)
First material buffer area (11) are constituted with left head (2), constitute main convective region between first partition (3) and second partition (13)
(10), the second partition (13) and right end socket (12) constitute second buffering area (8), first in the cylinder (5) every
It is staggeredly provided at equal intervals muti-piece flow-disturbing transverse slat (6) on plate (3) and second partition (13), the length of flow-disturbing transverse slat (6) is less than
The distance between first partition (3) and second partition (13), multiple flow-disturbing transverse slats (6) are main convective region (10) if being divided into
Dry convective region (10-1) is evenly equipped in each convective region several with first material buffer area (11) and second buffering area (8) company
Logical heat exchange straight pipeline (6-1).
2. the shell side formula condenser of high efficient heat exchanging according to claim 1, which is characterized in that the main convective region (10)
Cylinder (5) one end be provided with material inlet (4), the other end is provided with material outlet (9).
3. the shell side formula condenser of high efficient heat exchanging according to claim 1, which is characterized in that the convective region (10-1)
Hang plate (15) that is interior being staggeredly equipped with several equal lengths up and down and being parallel to each other, the sum of length of two pieces of hang plates (15) are small
In 2 times of distances of adjacent two pieces of flow-disturbing transverse slats (6), it is greater than times distance of adjacent two pieces of flow-disturbing transverse slats (6).
4. the shell side formula condenser of high efficient heat exchanging according to claim 3, which is characterized in that the hang plate (15) with
The angular range of horizontal plane is 45 ° ~ 60 °.
5. the shell side formula condenser of high efficient heat exchanging according to claim 1, which is characterized in that the cylinder (5), left envelope
It is arranged with insulation shell (14) outside head (2) and right end socket (12), is provided with heat insulation layer (16) in insulation shell (14).
6. the shell side formula condenser of high efficient heat exchanging according to claim 5, which is characterized in that heat insulation layer (16) packet
Include several glass layers (16-1) and aluminium foil layer (16-2) of intersecting, aluminium foil layer (16-2) with a thickness of 0.18 ~
0.65mm, glass layer (16-1) with a thickness of 0.32 ~ 0.78mm.
7. the shell side formula condenser of high efficient heat exchanging according to claim 1, which is characterized in that the cylinder (5), left head
(2) and on the inner wall of right end socket (12) it is coated with enamel erosion resistant coating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820820295.0U CN208635614U (en) | 2018-05-30 | 2018-05-30 | A kind of shell side formula condenser of high efficient heat exchanging |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820820295.0U CN208635614U (en) | 2018-05-30 | 2018-05-30 | A kind of shell side formula condenser of high efficient heat exchanging |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208635614U true CN208635614U (en) | 2019-03-22 |
Family
ID=65733121
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820820295.0U Expired - Fee Related CN208635614U (en) | 2018-05-30 | 2018-05-30 | A kind of shell side formula condenser of high efficient heat exchanging |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208635614U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111271990A (en) * | 2020-02-25 | 2020-06-12 | 纳盛洁净技术（苏州）有限公司 | Shear type spiral diversion sanitary heat exchanger |
-
2018
- 2018-05-30 CN CN201820820295.0U patent/CN208635614U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111271990A (en) * | 2020-02-25 | 2020-06-12 | 纳盛洁净技术（苏州）有限公司 | Shear type spiral diversion sanitary heat exchanger |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190322 |