CN203489749U - Vertical separation technology based heat exchanger - Google Patents

Vertical separation technology based heat exchanger Download PDF

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Publication number
CN203489749U
CN203489749U CN201320559666.1U CN201320559666U CN203489749U CN 203489749 U CN203489749 U CN 203489749U CN 201320559666 U CN201320559666 U CN 201320559666U CN 203489749 U CN203489749 U CN 203489749U
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CN
China
Prior art keywords
heat exchange
heat exchanger
exchange core
end socket
isolation technique
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Expired - Lifetime
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CN201320559666.1U
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Chinese (zh)
Inventor
殷敏伟
蒋彩琴
雷春花
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WUXI YUDA HEAT EXCHANGER CO Ltd
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WUXI YUDA HEAT EXCHANGER CO Ltd
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Abstract

The utility model relates to the field of heat exchangers, and particularly to a vertical separation technology based heat exchanger. Inner fins in each layer are separated through sealing strips, so that a heat exchange core is divided into a first heat exchange core and a second heat exchange core respectively arranged in the front and at the back; meanwhile an inlet pipe and an outlet pipe are respectively arranged at the left upper side of the right end face of a first right seal head and the right upper side of the right end face of a second right seal head, so that the vertical separation technology based heat exchanger solves the problems of leakage hazard and reduction of heat exchange efficiency due to the fact that the heat exchanger in the prior art needs to adopt a pipeline extension way to adapt to a device with an inlet and an outlet in the same plane. Therefore, demands on installation positions under some conditions not only can be satisfied, but the heat exchange efficiency also can be increased; the production cost is further lowered as adoption of extra pipelines is unnecessary.

Description

Heat exchanger based on vertical isolation technique
Technical field
The utility model relates to a kind of heat exchanger, relates in particular to a kind of heat exchanger based on vertical isolation technique.
Background technology
Heat exchanger is very extensive in each field application of work, agricultural, and in people's lives, heat-transfer equipment is also seen everywhere, and is one of indispensable process equipment.Therefore the extremely great attention of countries in the world government and research institution of the research of heat exchanger; since time energy crisis outburst that beats the world; each state is all making great efforts to find the new energy and On A New on the saving energy; in research, have high input, human resources arrangement foot in the situation that, a collection of representative high-performance heat exchanger is born.Along with going deep into of research, commercial Application has obtained the achievement attracting people's attention, obtained a large amount of return, as the screwed pipe of plate-fin heat exchanger, large-scale lamella heat exchanger and the porous surface tube of strengthening boiling, T-shaped finned tube, strengthening condensation, sawtooth pipe etc. have all obtained international heat transfer circle expert's approval, social benefit highly significant, has alleviated the pressure of the energy greatly.
Heat exchanger is a kind of energy-saving equipment that between material, heat transmits of realizing, a kind of process equipment of generally applying in industries such as oil, chemical industry, petrochemical industry, metallurgy, electric power, light industry, food, in oil refining, chemical plant installations, heat exchanger accounts for 40% left and right of total number of devices, accounts for 30 ~ 45% of gross investment.Along with the development of power-saving technology, application constantly expands in recent years, and the recovery of high temperature and low temperature heat energy has brought significant economic benefit.At present, in heat transmission equipment, use amount is larger plate-fin heat exchanger, and the development of plate-fin heat exchanger, makes efficiency of heat exchanger bring up to new level, and structure is compacter.The employing of this heat exchanger, cooling in the middle of aircraft engine and diesel locomotive engine, the cooling needs of automobile engine have been met, because volume is little, lightweight, efficiency is high, can process two kinds of advantages of media above, in petrochemical industry, ethylene unit, be widely applied rapidly.
Yet what plate-fin heat exchanger of the prior art adopted conventionally is the heat exchanger of horizontal cellular-type, Fig. 1 is the right view of heat exchanger of the prior art; As shown in the figure, its import 01 of heat exchanger of the prior art is distributed on the centre position of the first end socket 03, its outlet 02 is distributed on the centre position of the second end socket 04, this structure is when needing equipment in one plane for import with outlet, just be difficult to adapt to, the common way of industry is to extend import and outlet by pipeline, causes so very easily occurring in the junction of pipeline and import and outlet damaging, and have the hidden danger of leaking, heat exchange efficiency is because exterior line is installed also reduction greatly.
Utility model content
Problem for above-mentioned existence, the utility model provides a kind of heat exchanger based on vertical isolation technique, to overcome heat exchanger of the prior art owing to need to adapting to import and outlet equipment in one plane, and the way that adopts pipeline to extend causes existing and leaks hidden danger, reduce the problem of heat exchange efficiency, thereby can either meet the demand of the installation site in some situation, can improve heat exchange efficiency again, and without adopting extra ducts, and then reduce production costs.
To achieve these goals, the technical scheme that the utility model is taked is:
A kind of heat exchanger based on vertical isolation technique, comprise heat exchange core, described heat exchange core comprises the outer fin of multilayer and multilayer inner fin, between every layer of described outer fin and every layer of described inner fin, be provided with dividing plate, wherein, in the middle of every layer of described inner fin, be equipped with a strip of paper used for sealing, with the first heat exchange core and the second heat exchange core of placing before and after described heat exchange core is divided into;
The left side of described the first heat exchange core and described the second heat exchange core is provided with a left end socket, the right side of described the first heat exchange core and described the second heat exchange core is respectively equipped with right side the first end socket and right side the second end socket, described right side the first end socket is provided with an inlet tube, and described right side the second end socket is provided with an outlet.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, described the first heat exchange core and described the second heat exchange core are aluminum plate-fin type heat exchange core.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, described inlet tube is arranged at the left side, top, right side of described right side the first end socket.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, described outlet is arranged at the right side, top, right side of described right side the second end socket.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, described right side the first end socket is provided with an outlet, and described right side the second end socket is provided with an inlet tube.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, described outlet is arranged at the left side, top, right side of described right side the first end socket.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, described inlet tube is arranged at the right side, top, right side of described right side the second end socket.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, described inlet tube and described outlet are the pipeline of L-type structure.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, the material of described inlet tube and described outlet is aluminium.
The above-mentioned heat exchanger based on vertical isolation technique, wherein, the material of described left end socket, described right side the first end socket and described right side the second end socket is aluminium.
Technique scheme tool has the following advantages or beneficial effect:
The utility model is separated every layer of inner fin by strip of paper used for sealing, thereby before and after heat exchange core is divided into, the first heat exchange core and the second heat exchange core are set, inlet tube and outlet right side above the right side of left side and right side the second end socket above the right side of right side the first end socket is respectively set simultaneously, thereby overcome the heat exchanger of prior art owing to need to adapting to import and outlet equipment in one plane, and the way that adopts pipeline to extend, cause existing leakage hidden danger, reduce the problem of heat exchange efficiency, thereby can either meet the demand of the installation site in some situation, can improve heat exchange efficiency again, and without adopting extra ducts, and then reduce production costs.
Accompanying drawing explanation
Fig. 1 is the right view of heat exchanger of the prior art;
Fig. 2 is the front view of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1;
Fig. 3 is the right view of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1;
Fig. 4 is the top view of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1;
Fig. 5 is the front view of the heat exchange core of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1;
Fig. 6 is the right view of the heat exchange core of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1;
Fig. 7 is that model configuration schematic diagram is looked on the right side of the heat exchange core of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment, the utility model is further described, but not as restriction of the present utility model.
Embodiment 1:
Fig. 2 is the front view of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1, Fig. 3 is the right view of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1, Fig. 4 is the top view of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1, Fig. 5 is the front view of the heat exchange core of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1, Fig. 6 is the right view of the heat exchange core of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1, Fig. 7 is that model configuration schematic diagram is looked on the right side of the heat exchange core of the heat exchanger based on vertical isolation technique that provides of the utility model embodiment 1, as shown in Fig. 2 ~ 7, the heat exchanger based on vertical isolation technique that the utility model provides comprises heat exchange core, this heat exchange core consists of the outer fin 20 of multilayer and multilayer inner fin 24, between every layer of outer fin 20 and every layer of inner fin 24, be all provided with dividing plate 21, and every layer of outer fin 20 is all (just can intuitively obtain referring to Fig. 5 and Fig. 6) that vertical direction arranges with every layer of inner fin 24, every layer of outer fin 20 two ends are provided with outer fixedly strip of paper used for sealing 22, every layer of inner fin 24 two ends are provided with interior fixedly strip of paper used for sealing 23, simultaneously, the place, centre position of every layer of inner fin 24 is equipped with a strip of paper used for sealing 25, by the strip of paper used for sealing of every layer 25, referring to Fig. 7, strip of paper used for sealing 25 simulations of every layer form a vertical strip of paper used for sealing 25 ', the first heat exchange core 11 and the second heat exchange core 12 before and after thereby heat exchange core can being divided into, placed.
In the left side of the first heat exchange core 11 and the second heat exchange core 12, be provided with a left end socket 14, simultaneously, on the right side of the first heat exchange core 11 and the second heat exchange core 12, be respectively equipped with right side the first end socket 15 and right side the second end socket 16, and right side the first end socket 15 is provided with an inlet tube 17, right side the second end socket 16 is provided with an outlet 18.
Wherein, the first heat exchange core 11 and the second heat exchange core 12 are aluminum plate-fin type heat exchange core, inlet tube 17 and outlet 18 are the pipeline of L-type structure, and the material of inlet tube 17 and outlet 18 is aluminium, the material of left end socket 14, right side the first end socket 15 and right side the first end socket 16 is also aluminium, simultaneously, in the utility model embodiment 1, inlet tube 17 is arranged at the left side, top, right side of right side the first end socket 15, and outlet 18 is arranged at the right side (2 ~ accompanying drawing 4 just can intuitively obtain by reference to the accompanying drawings), top, right side of right side the second end socket 16.
In addition, in the utility model embodiment 1, inlet tube 17 is arranged to the left side, top, right side of right side the first end socket 15, and outlet 18 is arranged to the right side, right side top of right side the second end socket 16, the in the situation that of customer demand, also inlet tube can be arranged to the right side, top, right side of right side the second end socket, and outlet be arranged to the left side, top, right side of right side the first end socket simultaneously.
During equipment operation, liquid or gas enter right side the first end socket 15 being connected with this inlet tube 17 from inlet tube 17, flow to again in the first heat exchange core 11 and dispel the heat, via left end socket 14, entering into the second heat exchange core 12 again dispels the heat again, flow into right side the second end socket 16, finally by being flowed out by outlet 18, via the heat exchange core effect of twice, thereby obtain larger heat exchange efficiency.
So, the heat exchanger based on vertical isolation technique that the utility model embodiment 1 provides is separated every layer of inner fin by strip of paper used for sealing, thereby before and after heat exchange core is divided into, the first heat exchange core and the second heat exchange core are set, inlet tube and outlet right side above the right side of left side and right side the second end socket above the right side of right side the first end socket is respectively set simultaneously, thereby overcome the heat exchanger of prior art owing to need to adapting to import and outlet equipment in one plane, and the way that adopts pipeline to extend, cause existing leakage hidden danger, reduce the problem of heat exchange efficiency, thereby can either meet the demand of the installation site in some situation, can improve heat exchange efficiency again, and without adopting extra ducts, and then reduce production costs.
It should be appreciated by those skilled in the art that those skilled in the art can realize described variation example in conjunction with prior art and above-described embodiment, do not repeat them here.Such variation example does not affect flesh and blood of the present utility model, does not repeat them here.
Above preferred embodiment of the present utility model is described.It will be appreciated that, the utility model is not limited to above-mentioned specific implementations, and the equipment of wherein not describing in detail to the greatest extent and structure are construed as with the common mode in this area to be implemented; Any those of ordinary skill in the art, make many possible changes and modification not departing from technical solutions of the utility model, or are revised as the equivalent embodiment of equivalent variations, and this does not affect flesh and blood of the present utility model.Therefore, every content that does not depart from technical solutions of the utility model,, all still belongs in the scope of technical solutions of the utility model protection any simple modification made for any of the above embodiments, equivalent variations and modification according to technical spirit of the present utility model.

Claims (10)

1. the heat exchanger based on vertical isolation technique, comprise heat exchange core, described heat exchange core comprises the outer fin of multilayer and multilayer inner fin, between every layer of described outer fin and every layer of described inner fin, be provided with dividing plate, it is characterized in that, in the middle of every layer of described inner fin, be equipped with a strip of paper used for sealing, with the first heat exchange core and the second heat exchange core of placing before and after described heat exchange core is divided into;
The left side of described the first heat exchange core and described the second heat exchange core is provided with a left end socket, the right side of described the first heat exchange core and described the second heat exchange core is respectively equipped with right side the first end socket and right side the second end socket, described right side the first end socket is provided with an inlet tube, and described right side the second end socket is provided with an outlet.
2. the heat exchanger based on vertical isolation technique as claimed in claim 1, is characterized in that, described the first heat exchange core and described the second heat exchange core are aluminum plate-fin type heat exchange core.
3. the heat exchanger based on vertical isolation technique as claimed in claim 1, is characterized in that, described inlet tube is arranged at the left side, top, right side of described right side the first end socket.
4. the heat exchanger based on vertical isolation technique as claimed in claim 1, is characterized in that, described outlet is arranged at the right side, top, right side of described right side the second end socket.
5. the heat exchanger based on vertical isolation technique as claimed in claim 1, is characterized in that, described right side the first end socket is provided with an outlet, and described right side the second end socket is provided with an inlet tube.
6. the heat exchanger based on vertical isolation technique as claimed in claim 5, is characterized in that, described outlet is arranged at the left side, top, right side of described right side the first end socket.
7. the heat exchanger based on vertical isolation technique as claimed in claim 5, is characterized in that, described inlet tube is arranged at the right side, top, right side of described right side the second end socket.
8. the heat exchanger based on vertical isolation technique as described in claim 1 or 5, is characterized in that, described inlet tube and described outlet are the pipeline of L-type structure.
9. the heat exchanger based on vertical isolation technique as described in claim 1 or 5, is characterized in that, the material of described inlet tube and described outlet is aluminium.
10. the heat exchanger based on vertical isolation technique as described in claim 1 or 5, is characterized in that, the material of described left end socket, described right side the first end socket and described right side the second end socket is aluminium.
CN201320559666.1U 2013-09-10 2013-09-10 Vertical separation technology based heat exchanger Expired - Lifetime CN203489749U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320559666.1U CN203489749U (en) 2013-09-10 2013-09-10 Vertical separation technology based heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320559666.1U CN203489749U (en) 2013-09-10 2013-09-10 Vertical separation technology based heat exchanger

Publications (1)

Publication Number Publication Date
CN203489749U true CN203489749U (en) 2014-03-19

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Application Number Title Priority Date Filing Date
CN201320559666.1U Expired - Lifetime CN203489749U (en) 2013-09-10 2013-09-10 Vertical separation technology based heat exchanger

Country Status (1)

Country Link
CN (1) CN203489749U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10782074B2 (en) 2017-10-20 2020-09-22 Api Heat Transfer, Inc. Heat exchanger with a cooling medium bar

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10782074B2 (en) 2017-10-20 2020-09-22 Api Heat Transfer, Inc. Heat exchanger with a cooling medium bar

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Granted publication date: 20140319

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