CN207395543U - A kind of total-heat exchanger - Google Patents

A kind of total-heat exchanger Download PDF

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Publication number
CN207395543U
CN207395543U CN201720696672.XU CN201720696672U CN207395543U CN 207395543 U CN207395543 U CN 207395543U CN 201720696672 U CN201720696672 U CN 201720696672U CN 207395543 U CN207395543 U CN 207395543U
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CN
China
Prior art keywords
sections
frame
total
heat exchanger
plate
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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
Application number
CN201720696672.XU
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Chinese (zh)
Inventor
刘文杰
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianjin Deep Breath Rui Rui Environmental Technology Co Ltd
Original Assignee
Tianjin Deep Breath Rui Rui Environmental Technology Co Ltd
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Priority to CN201720696672.XU priority Critical patent/CN207395543U/en
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Publication of CN207395543U publication Critical patent/CN207395543U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model provides a kind of total-heat exchanger, including exchange membrane, the first frame, the second frame, bottom plate, top plate and side plate, first frame and the second frame are set between the bottom plate and top plate, first frame and the alternately laminated setting of the second frame are multigroup, the exchange membrane is arranged between the first frame and the second frame, the side plate is arranged on the first frame and the second frame facet of stacking, and the side plate top is connected with top plate, and the side plate lower part is connected with bottom plate.A kind of total-heat exchanger described in the utility model is simple in structure, convenient for cleaning, ensure with fresh air, new gas channel arrangement can be obviously improved the efficiency of Total heat exchange, speed when passing the gas through exchanger faster, noise smaller, and the partition plate for forming gas channel is reinforced, it prevents malformation, influences durability and reliability.

Description

A kind of total-heat exchanger
Technical field
The utility model belongs to air exchange field, more particularly, to a kind of total-heat exchanger.
Background technology
In order to improve the ventilatory of air-conditioning equipment, room air pollution is solved the problems, such as, within air-conditioning systems on one side The exchange of temperature and humidity is carried out while the equipment taken a breath becomes total-heat exchanger.With the popularization of total-heat exchanger, it is The efficiency of Total heat exchange is improved, and exchanger volume is made not change, it is necessary to gas channel be reasonably set, reaches more Good heat exchange efficiency.
The content of the invention
In view of this, the utility model is directed to a kind of total-heat exchanger, to improve the heat exchange efficiency of total-heat exchanger, And make its convenient for cleaning, ensure with fresh air.
In order to achieve the above objectives, the technical solution of the utility model is realized in:
A kind of total-heat exchanger, including exchange membrane, the first frame, the second frame, bottom plate, top plate and side plate, the bottom plate First frame and the second frame are set between top plate, and first frame and the alternately laminated setting of the second frame are multigroup, described Exchange membrane is arranged between the first frame and the second frame, and the side plate is arranged on the first frame and the second frame side of stacking Face, the side plate top are connected with top plate, and the side plate lower part is connected with bottom plate;
First frame includes a plurality of gas channel being mutually parallel, and the gas channel includes tri- sections, A sections of A, B, C For arrival end, C sections are the port of export, wherein, A sections are parallel with C sections, and B sections are arranged between A sections and C sections, and A sections are more than with B sections of angles 100 degree, and less than 170 degree, B sections are more than 100 degree with C sections of angles, and less than 170 degree;
Second frame includes a plurality of gas channel being mutually parallel, and the gas channel includes tri- sections, D sections of D, E, F For the port of export, F sections are arrival end, wherein, D sections are vertical with A sections, and E sections are parallel with B sections, and F sections are vertical with C sections;
The gas channel is to surround the space formed, the direction flowed on the partition plate along gas by partition plate and exchange membrane Baffle equipped with protrusion, the baffle are alternatively arranged on partition plate, and adjacent two rows baffle is staggered.
Further, the baffle is arranged on the arrival end and the port of export of fluid passageway, i.e. A sections, C sections, D sections and F sections.
Further, the B sections of the gas channel on partition plate and the E sections of wings for being equipped with to slow down speed air flow Piece, the fin oblique cutting are arranged on partition plate, and the air in gas channel is made to generate rotation.
Further, the baffle is one kind in ellipse, round rectangle or spindle.
Further, the exchange membrane is the polyolefin film that permeable coating is covered on surface.
Further, between the A sections of first frame and B sections reinforcement, is equipped between B sections and C sections, prevents temperature Variation is deformed partition plate.
Further, the exchange film surface scribbles hygroscopic agent.
Compared with the prior art, a kind of total-heat exchanger described in the utility model has the advantage that:
A kind of total-heat exchanger described in the utility model is simple in structure, convenient for cleaning, ensures gas with fresh air, unique Circulation road arrangement can be obviously improved the efficiency of Total heat exchange, make gas pass in and out exchanger when speed faster, noise is more Small, the baffle in gas channel helps to make steady air current, reduces noise, air A sections in the channel, C sections, D sections, F Section, in B sections and the E sections of speed air flows slowed down due to fin, can make air by filling since baffle accelerates flowing velocity The abundant time exchanges heat, and the design of this passage not only facilitates space layout, but also can maximize exchange efficiency, and forms air-flow The partition plate of passage is reinforced, and prevents malformation, influences durability and reliability.
Description of the drawings
The attached drawing for forming the part of the utility model is used to provide a further understanding of the present invention, this practicality is new The schematic description and description of type does not form the improper restriction to the utility model for explaining the utility model. In attached drawing:
Fig. 1 is the overall structure diagram described in the utility model embodiment;
Fig. 2 is the internal structure schematic diagram described in the utility model embodiment;
Fig. 3 is the internal structure explosive view described in the utility model embodiment;
Fig. 4 is the top view of Fig. 2;
Fig. 5 is the projection view at P visual angles in Fig. 4;
Fig. 6 is along the cross section view of N-N in Fig. 5.
Reference sign:
1- top plates;2- side plates;3- bottom plates;The first frames of 4-;The second frames of 5-;6- reinforcements;7- baffles;8- partition plates.
Specific embodiment
It should be noted that in the case where there is no conflict, the feature in embodiment and embodiment in the utility model can To be mutually combined.
In the description of the utility model, it is to be understood that term " " center ", " longitudinal direction ", " transverse direction ", " on ", " under ", The orientation or position relationship of the instructions such as "front", "rear", "left", "right", " vertical ", " level ", " top ", " bottom ", " interior ", " outer " are Based on orientation shown in the drawings or position relationship, it is for only for ease of description the utility model and simplifies description rather than instruction Or imply that signified device or element must have specific orientation, with specific azimuth configuration and operation, therefore be not understood that For the limitation to the utility model.In addition, term " first ", " second " etc. are only used for description purpose, and it is not intended that instruction Or imply relative importance or the implicit quantity for indicating indicated technical characteristic." first ", " second " etc. are defined as a result, Feature can express or implicitly include one or more this feature.In the description of the utility model, unless separately It is described, " multiple " are meant that two or more.
, it is necessary to which explanation, unless otherwise clearly defined and limited, term " are pacified in the description of the utility model Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be being fixedly connected or being detachably connected or integrally Connection;Can be mechanical connection or electrical connection;It can be directly connected, can also be indirectly connected by intermediary, It can be the connection inside two elements.For the ordinary skill in the art, on being understood by concrete condition State concrete meaning of the term in the utility model.
The utility model will be described in detail below with reference to the accompanying drawings and embodiments.
A kind of total-heat exchanger, it is described including exchange membrane, the first frame 4, the second frame 5, bottom plate 3, top plate 1 and side plate 2 Exchange membrane, the first frame 4, the second frame 5, bottom plate 3, top plate 1 are octagon, and first is set between the bottom plate 3 and top plate 1 4 and second frame 5 of frame, first frame 4 and the second frame 5 is alternately laminated sets multigroup, the exchange membrane is arranged on the Between one frame 4 and the second frame 5, the side plate 2 be disposed on stacking the first frame 4 and the second frame 5 wherein four A side, 2 top of side plate is connected with top plate 1, and 2 lower part of the side plate is connected with bottom plate 3;First frame 4 wraps The a plurality of gas channel being mutually parallel is included, the gas channel includes tri- sections of A, B, C, and A sections are arrival end, and C sections are the port of export, In, A sections parallel with C sections, and B sections are arranged between A sections and C sections, and A sections are more than 100 degree with B section angles, and be less than 170 degree, B sections and C sections of angles are more than 100 degree, and less than 170 degree;Second frame 5 includes a plurality of gas channel being mutually parallel, the air-flow Passage includes tri- sections of D, E, F, and D sections are the port of export, and F sections are arrival end, wherein, D sections are vertical with A sections, and E sections are parallel with B sections, F sections It is vertical with C sections;The gas channel is to surround the space formed by partition plate 8 and exchange membrane, is flowed on the partition plate 8 along gas Direction is equipped with baffle 7, and the baffle 7 is alternatively arranged on partition plate, and adjacent two rows baffle 7 is staggered, the water conservancy diversion Body 7 is one kind in ellipse, round rectangle or spindle.The B sections of the gas channel on partition plate 8 are equipped with E sections and use In the fin for slowing down speed air flow, the fin oblique cutting is arranged on partition plate 8, and the air in gas channel is made to generate rotation Turn.The baffle 7 is arranged on the arrival end and the port of export of fluid passageway, i.e. A sections, C sections, D sections and F sections.The exchange membrane is The polyolefin film of permeable coating is covered on surface.The permeable coating be crosslinked non-ionic polyurethane-polyether polymer, institute It states exchange film surface and is also coated with hygroscopic agent.Between the A sections of first frame and B sections, reinforcement 6 is equipped between B sections and C sections.
As shown in figure 3, hot-air enters the first frame to a kind of total-heat exchanger described in the utility model from A sections when in use In the gas channel of frame 4, by B sections from C sections of outlet discharges, cold air enters from F sections in the gas channel of the second frame 5, warp E sections are crossed from D sections of outlet discharges, cold air and hot-air are being separated by exchange membrane in gas channel, carried out through exchange membrane It flowing to and intersects when the exchange of temperature and humidity, cold air and hot-air start, stage casing flow direction is intersected again on the contrary, finally flowing to, Baffle 7 in passage helps to make steady air current, reduces noise, air A sections in the channel, C sections, D sections, F sections due to leading Fluid 7 accelerates flowing velocity, in B sections and the E sections of speed air flows slowed down due to fin, can make air by plenty of time It exchanges heat, the design of this passage not only facilitates space layout, but also can maximize exchange efficiency.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this Within the spirit and principle of utility model, any modifications, equivalent replacements and improvements are made should be included in the utility model Protection domain within.

Claims (7)

1. a kind of total-heat exchanger, it is characterised in that:Including exchange membrane, the first frame (4), the second frame (5), bottom plate (3), top Plate (1) and side plate (2), set the first frame (4) and the second frame (5) between the bottom plate (3) and top plate (1), and described first Frame (4) and the alternately laminated setting of the second frame (5) are multigroup, and the exchange membrane is arranged on the first frame (4) and the second frame (5) Between, the side plate (2) is arranged on the first frame (4) of stacking and the second frame (5) side, side plate (2) top and top Plate (1) connects, and the side plate (2) lower part is connected with bottom plate (3);
First frame (4) includes a plurality of gas channel being mutually parallel, and the gas channel includes tri- sections of A, B, C, and A sections are Arrival end, C sections are the port of export, wherein, A sections are parallel with C sections, and B sections are arranged between A sections and C sections, and A sections are more than with B sections of angles 100 degree, and A sections are less than 170 degree with B sections of angles, B sections are more than 100 degree with C sections of angles, and B sections are less than 170 degree with C sections of angles;
Second frame (5) includes a plurality of gas channel being mutually parallel, and the gas channel includes tri- sections of D, E, F, and D sections are The port of export, F sections are arrival end, wherein, D sections are vertical with A sections, and E sections are parallel with B sections, and F sections are vertical with C sections;
The gas channel is to surround the space formed, the side flowed on the partition plate (8) along gas by partition plate (8) and exchange membrane To the baffle (7) equipped with protrusion, the baffle (7) is alternatively arranged on partition plate (8), and adjacent two rows baffle (7) is staggeredly It sets.
2. a kind of total-heat exchanger according to claim 1, it is characterised in that:The baffle (7) is arranged on fluid and leads to The arrival end and the port of export in road, i.e. A sections, C sections, D sections and F sections.
3. a kind of total-heat exchanger according to claim 2, it is characterised in that:The gas channel on partition plate (8) B sections and E section equipped with for slowing down the fins of speed air flow, the fin oblique cutting is arranged on partition plate (8), leads to air-flow Air in road generates rotation.
4. a kind of total-heat exchanger according to claim 1, it is characterised in that:The baffle (7) is ellipse, fillet One kind in rectangle or spindle.
5. a kind of total-heat exchanger according to claim 1, it is characterised in that:The exchange membrane is permeable to be covered on surface The polyolefin film of coating.
6. a kind of total-heat exchanger according to claim 1, it is characterised in that:The A sections of first frame (4) with B sections Between, reinforcement (6) is equipped between B sections and C sections, be equipped between the D sections of second frame (5) and E sections, between E sections and C sections Reinforcement (6).
7. a kind of total-heat exchanger according to claim 1, it is characterised in that:The exchange film surface scribbles hygroscopic agent.
CN201720696672.XU 2017-06-15 2017-06-15 A kind of total-heat exchanger Expired - Fee Related CN207395543U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720696672.XU CN207395543U (en) 2017-06-15 2017-06-15 A kind of total-heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720696672.XU CN207395543U (en) 2017-06-15 2017-06-15 A kind of total-heat exchanger

Publications (1)

Publication Number Publication Date
CN207395543U true CN207395543U (en) 2018-05-22

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ID=62402398

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720696672.XU Expired - Fee Related CN207395543U (en) 2017-06-15 2017-06-15 A kind of total-heat exchanger

Country Status (1)

Country Link
CN (1) CN207395543U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109780702A (en) * 2019-03-18 2019-05-21 浙江华龙机械股份有限公司 A kind of Total heat exchange core in fresh air system
CN111780609A (en) * 2020-07-15 2020-10-16 翟文静 Full heat exchanger for urban rail transit train
CN114303031A (en) * 2019-08-30 2022-04-08 荷兰空气处理创新公司 Airflow system
CN114485223A (en) * 2022-02-07 2022-05-13 朱德梅 Full heat exchanger with corrugated structure

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109780702A (en) * 2019-03-18 2019-05-21 浙江华龙机械股份有限公司 A kind of Total heat exchange core in fresh air system
CN109780702B (en) * 2019-03-18 2024-03-15 浙江华龙机械股份有限公司 Total heat exchange core in fresh air system
CN114303031A (en) * 2019-08-30 2022-04-08 荷兰空气处理创新公司 Airflow system
CN114303031B (en) * 2019-08-30 2024-01-26 荷兰空气处理创新公司 Air flow system
CN111780609A (en) * 2020-07-15 2020-10-16 翟文静 Full heat exchanger for urban rail transit train
CN114485223A (en) * 2022-02-07 2022-05-13 朱德梅 Full heat exchanger with corrugated structure

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GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20180522

Termination date: 20200615

CF01 Termination of patent right due to non-payment of annual fee