CN108955312A - A kind of heat exchanger - Google Patents
A kind of heat exchanger Download PDFInfo
- Publication number
- CN108955312A CN108955312A CN201710349901.5A CN201710349901A CN108955312A CN 108955312 A CN108955312 A CN 108955312A CN 201710349901 A CN201710349901 A CN 201710349901A CN 108955312 A CN108955312 A CN 108955312A
- Authority
- CN
- China
- Prior art keywords
- end socket
- cabinet
- heat exchanger
- fin
- heat
- 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
- 238000005192 partition Methods 0.000 claims description 5
- 230000003447 ipsilateral effect Effects 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 8
- 230000005494 condensation Effects 0.000 abstract description 7
- 238000009833 condensation Methods 0.000 abstract description 7
- 238000009434 installation Methods 0.000 abstract description 4
- 238000001816 cooling Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000011084 recovery Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 2
- 239000002250 absorbent Substances 0.000 description 2
- 239000002826 coolant Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 208000002925 dental caries Diseases 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0062—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0202—Header boxes having their inner space divided by partitions
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a kind of heat exchangers, including cabinet, the first end socket and the second end socket, first end socket and the second end socket are separately positioned on the both ends of the cabinet, and the cabinet is detachably connected with the first end socket and the second end socket, the first end socket intake pipe is provided with escape pipe on second end socket.This kind of heat exchanger structure is simply easy to use, when in use, VOC gas enter in cabinet from the air inlet pipe on the first end socket, utilize the intracorporal heat-exchanging component of case, carry out condensation cooling, then deicing is removed water, mainly cooled down using fin plate, organic gas is condensed liquefaction, " V " type fin structure is used using fin plate, it is stifled to be not easy to occur ice, the working efficiency of heat exchanger can effectively be improved, prolong the service life, in addition, first end socket and the second end socket are separately positioned on the both ends of cabinet, cabinet is detachably connected with the first end socket and the second end socket, it is easy for installation, it is time saving and energy saving.
Description
[technical field]
The present invention relates to a kind of heat exchangers.
[background technique]
The recovery technology of VOC mainly has condensation method, absorption method, absorption process and membrane separation process;Absorption method, absorption process and film point
It is to separate and recover the organic solvent in exhaust gas by using selective absorbent and absorbent, selective membrane infiltration from method.Place
Reason technology mainly has catalysis burning, directly burning etc., it is that the organic matter in gas is changed into CO by chemical reaction2With
Water.
Condensation method is simplest recovery method, it is the dew-point temperature that exhaust gas is cool below to organic matter, is made organic
Object is condensed into drop and separates from gas.Usually used cooling medium mainly has cold water, chilled brine and liquefied ammonia.It is logical
The normal technology is only used for the recovery processing of VOC content high (a few percent), the lesser organic exhaust gas of gas flow, need to be using compared with low temperature
The cooling medium of degree uses high-handed measures, and early stage heat pump is inserted into the form of open flume type fin with microchannel fin using flat tube,
Condensation water can be discharged from top to bottom along the fin that end connects, but technology difficulty is big when the fin and flat tube assembling, it is difficult to real
Existing production demand.A kind of currently used heat exchanger fin includes multiple spaced central fins, each centre
By connection fin connection between fin, wavy shaped configuration is formed.The heat exchanger fin of this kind of form be mounted on up and down two it is flat
When between pipe, sink is easily formed at the trough of heat exchanger fin, is not easy to drain.And it is located at heat exchanger fin and the position on upper layer
In lower layer heat exchanger fin there are certain gap, condensation water can rest on the seam of upper and lower two unconnected heat exchanger fins
At gap, water bridge is formed, is also unfavorable for draining.For this purpose, it is proposed that a kind of heat exchanger.
[summary of the invention]
The main purpose of the present invention is to provide a kind of heat exchangers, can effectively solve the problems in background technique.
To achieve the above object, the technical scheme adopted by the invention is as follows: a kind of heat exchanger, including cabinet, the first end socket and
Second end socket, first end socket and the second end socket are separately positioned on the both ends of the cabinet, and the cabinet and the first end socket
It is detachably connected with the second end socket, the first end socket intake pipe, is provided with escape pipe, the cabinet on second end socket
It is inside provided with heat-exchanging component, the heat-exchanging component includes fin plate and baffle plate, and the fin plate is mounted on the baffling
On plate, the fin sheet structure is " V " type fin structure.
Further, the upper end of the cabinet is provided with inlet tube, and lower end is provided with outlet, and the inlet tube and goes out
The not ipsilateral of the cabinet is arranged in mouth pipe.
Further, the two sides of the cabinet are provided with support.
Further, partition is provided in first end socket and second end socket.
Further, it is connected by flange between first end socket and cabinet, between second end socket and cabinet
It connects, and is provided with gasket on the flange of junction.
Compared with prior art, the invention has the following beneficial effects: this kind of heat exchanger structure is simply easy to use, make
Used time, VOC gas enter in cabinet from the air inlet pipe on the first end socket, using the intracorporal heat-exchanging component of case, carry out condensation drop
Then temperature removes water deicing, mainly cooled down using fin plate, and organic gas is condensed liquefaction, is used using fin plate
" V " type fin structure, it is not easy to ice occur and block up, can effectively improve the working efficiency of heat exchanger, prolong the service life, separately
Outside, the first end socket and the second end socket are separately positioned on the both ends of cabinet, and cabinet is detachably connected with the first end socket and the second end socket,
It is easy for installation, it is time saving and energy saving.
[Detailed description of the invention]
Fig. 1 is a kind of overall structure diagram of heat exchanger of the present invention.
In figure: 1, cabinet;2, the first end socket;3, the second end socket;4, air inlet pipe;5, escape pipe;6, heat-exchanging component;7, fin
Plate;8, baffle plate;9, inlet tube;10, outlet;11, support;12, partition;13, flange;14, gasket.
[specific embodiment]
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below with reference to
Specific embodiment, the present invention is further explained.
As shown in Figure 1, a kind of heat exchanger of the present invention, including cabinet 1, the first end socket 2 and the second end socket 3, first envelope
First 2 and second end socket 3 be separately positioned on the both ends of the cabinet 1, and the cabinet 1 and the first end socket 2 and the second end socket 3 are removable
Unload connection, 2 intake pipe 4 of the first end socket is provided with escape pipe 5 on second end socket 3, is provided in the cabinet 1
Heat-exchanging component 6, the heat-exchanging component 6 include fin plate 7 and baffle plate 8, and the fin plate 7 is mounted on the baffle plate 8
On, 7 structure of fin plate is " V " type fin structure.
Further, the upper end of the cabinet 1 is provided with inlet tube 9, and lower end is provided with outlet 10, and the inlet tube
9 and outlet 10 the not ipsilateral of the cabinet 1 be set, inlet tube 9 is used for air inlet, and outlet 10 can be used in draining.
Further, the two sides of the cabinet 1 are provided with support 11, convenient for the installation of heat exchanger.
Further, it is provided with partition 12 in first end socket 2 and second end socket 3, two partitions 12 can
First end socket 2, the second end socket 3 are divided into two cavitys, form counter-flow heat exchange structure.
Further, pass through flange between first end socket 2 and cabinet 1, between second end socket 3 and cabinet 1
13 are connected, and gasket 14 is provided on the flange 13 of junction, install the first end socket 2 and the second end socket 3 by flange 13
On cabinet 1, gasket 14 can play better sealing.
Working principle of the present invention is as follows: when in use, VOC gas enter cabinet from the air inlet pipe 4 on the first end socket 2
In 1, using the heat-exchanging component 6 in cabinet 1, condensation cooling is carried out, then removes water deicing, is mainly dropped using fin plate 7
Temperature, organic gas are condensed liquefaction, use " V " type fin structure using fin plate 7, it is not easy to which it is stifled ice occur, can be effective
Raising heat exchanger working efficiency, prolong the service life, in addition, the first end socket 2 and the second end socket 3 are separately positioned on cabinet 1
Both ends, cabinet 1 is detachably connected with the first end socket 2 and the second end socket 3, easy for installation, time saving and energy saving.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (5)
1. a kind of heat exchanger, including cabinet, the first end socket and the second end socket, it is characterised in that: first end socket and the second envelope
Head is separately positioned on the both ends of the cabinet, and the cabinet is detachably connected with the first end socket and the second end socket, and described first
End socket intake pipe is provided with escape pipe on second end socket, heat-exchanging component, the heat-exchanging component is provided in the cabinet
Including fin plate and baffle plate, the fin plate is mounted on the baffle plate, and the fin sheet structure is " V " type wing
Chip architecture.
2. a kind of heat exchanger according to claim 1, it is characterised in that: the upper end of the cabinet is provided with inlet tube, under
End is provided with outlet, and the not ipsilateral of the cabinet is arranged in the inlet tube and outlet.
3. a kind of heat exchanger according to claim 1, it is characterised in that: the two sides of the cabinet are provided with support.
4. a kind of heat exchanger according to claim 1, it is characterised in that: in first end socket and second end socket
It is provided with partition.
5. a kind of heat exchanger according to claim 2, it is characterised in that: between first end socket and cabinet, described
It is connected by flange between two end sockets and cabinet, and is provided with gasket on the flange of junction.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710349901.5A CN108955312A (en) | 2017-05-17 | 2017-05-17 | A kind of heat exchanger |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710349901.5A CN108955312A (en) | 2017-05-17 | 2017-05-17 | A kind of heat exchanger |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108955312A true CN108955312A (en) | 2018-12-07 |
Family
ID=64461893
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710349901.5A Pending CN108955312A (en) | 2017-05-17 | 2017-05-17 | A kind of heat exchanger |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108955312A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111054182A (en) * | 2019-12-24 | 2020-04-24 | 中投(天津)智能管道股份有限公司 | Tail gas dust removal purification device for insulating tube workshop |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030190513A1 (en) * | 2002-04-03 | 2003-10-09 | Meissner Alan P. | Contact heater/humidifier for fuel cell systems |
CN204188046U (en) * | 2014-07-21 | 2015-03-04 | 张丽 | Condensation method recycling organic gas (VOC s) preposition plate type heat exchanger |
CN104990433A (en) * | 2015-06-04 | 2015-10-21 | 中国科学院理化技术研究所 | Plate-fin heat exchanger |
CN106440522A (en) * | 2016-07-05 | 2017-02-22 | 天津商业大学 | Gas extracting type plate fin type heat exchanger |
CN206095005U (en) * | 2015-09-30 | 2017-04-12 | 张丽 | Fin plate formula heat exchanger |
CN206739945U (en) * | 2017-05-17 | 2017-12-12 | 江苏视野天地环保研究院有限公司 | A kind of heat exchanger |
-
2017
- 2017-05-17 CN CN201710349901.5A patent/CN108955312A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20030190513A1 (en) * | 2002-04-03 | 2003-10-09 | Meissner Alan P. | Contact heater/humidifier for fuel cell systems |
CN204188046U (en) * | 2014-07-21 | 2015-03-04 | 张丽 | Condensation method recycling organic gas (VOC s) preposition plate type heat exchanger |
CN104990433A (en) * | 2015-06-04 | 2015-10-21 | 中国科学院理化技术研究所 | Plate-fin heat exchanger |
CN206095005U (en) * | 2015-09-30 | 2017-04-12 | 张丽 | Fin plate formula heat exchanger |
CN106440522A (en) * | 2016-07-05 | 2017-02-22 | 天津商业大学 | Gas extracting type plate fin type heat exchanger |
CN206739945U (en) * | 2017-05-17 | 2017-12-12 | 江苏视野天地环保研究院有限公司 | A kind of heat exchanger |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111054182A (en) * | 2019-12-24 | 2020-04-24 | 中投(天津)智能管道股份有限公司 | Tail gas dust removal purification device for insulating tube workshop |
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PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20181207 |