CN204987980U - High temperature liquid cooling's heat exchanger suitable for during chemical production - Google Patents

High temperature liquid cooling's heat exchanger suitable for during chemical production Download PDF

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Publication number
CN204987980U
CN204987980U CN201520658747.6U CN201520658747U CN204987980U CN 204987980 U CN204987980 U CN 204987980U CN 201520658747 U CN201520658747 U CN 201520658747U CN 204987980 U CN204987980 U CN 204987980U
Authority
CN
China
Prior art keywords
heat exchanger
cooling
chemical industry
temp liquid
industry high
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
Application number
CN201520658747.6U
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Chinese (zh)
Inventor
毛永钦
刘海洋
张晓强
张阳
宁万衡
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.)
Henan Lei Bairui new Mstar Technology Ltd
Original Assignee
Puyang Dingtai Chemical Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Puyang Dingtai Chemical Co Ltd filed Critical Puyang Dingtai Chemical Co Ltd
Priority to CN201520658747.6U priority Critical patent/CN204987980U/en
Application granted granted Critical
Publication of CN204987980U publication Critical patent/CN204987980U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a high temperature liquid cooling's heat exchanger suitable for during chemical production, base under heat exchanger body, heat exchanger upper end cover, heat exchanger, install heat exchanger body top the heat exchanger upper end cover, install heat exchanger body below base under the heat exchanger, the heat exchanger upper end cover with be provided with chemical industry high temperature liquid working chamber under the heat exchanger between the base, chemical industry high temperature liquid working chamber internally mounted has cooling liquid work cooling worm, heat exchanger upper end cover below is connected with the built -in agitator of working chamber and extends to cooling liquid work cooling worm central authorities, heat exchanger body top layer is provided with the heat exchanger vacuum and prevents the layer of frosting. The utility model has the advantages of simple structure and reasonable design, coil and agitated vessel makes cooling rate obviously accelerate through the worm, can prevent that the heat exchanger outside from frosting, and manufacturing cost is not high moreover, is fit for the application and promotes.

Description

A kind of heat exchanger of high-temp liquid cooling when being applicable to Chemical Manufacture
Technical field
The utility model belongs to chemical industry heat dissipation equipment field, is specifically related to a kind of heat exchanger of high-temp liquid cooling when being applicable to Chemical Manufacture.
Background technology
At present, rapidly, the liquid in a lot of Chemical Manufacture needs cooling rapidly to China's Chemical Manufacture development, also varied for the equipment of lowering the temperature, but is still faced with very many-sided challenge, and demand finds the solution meeting client.Application number: the Chinese patent literature of 201310260964.5 reports a kind of heat exchanger, particular content is: a kind of heat exchanger, it comprises inlet header, outlet collection pipe and some runner pipes, described inlet header be provided with the punching of inserting for described runner pipe and with the medial surface being positioned at described punching opposite side, described runner pipe comprises passage and inserts the first end in described inlet header from described punching, described first end is provided with first end face relative with described medial surface, the roof be positioned on described first end is provided with the breach running through described first end face, described channel part is exposed to this breach, on the axis direction of described inlet header, cold-producing medium main channel is formed between described first end face and described medial surface, described breach and described passage form cold-producing medium and distribute passage on the direction perpendicular to described axis direction.The invention has the beneficial effects as follows: by arranging breach, more large-area passage can be come out, thus make fluid distrbution evenly.This new structure contains the advantage that above-mentioned patent has, but above-mentioned patent cooling velocity is comparatively slow, and due to higher to the requirement of material, make cost higher, be not suitable for application.In sum, so I devises a kind of heat exchanger of high-temp liquid cooling when being applicable to Chemical Manufacture.
Summary of the invention
In order to solve above-mentioned Problems existing, the utility model provides a kind of heat exchanger of high-temp liquid cooling when being applicable to Chemical Manufacture.
The utility model is achieved through the following technical solutions:
The heat exchanger that high-temp liquid when being applicable to Chemical Manufacture cools, comprises heat exchanger body, heat exchanger upper end cover, heat exchanger lower bottom base, is provided with described heat exchanger upper end cover above described heat exchanger body; Described heat exchanger lower bottom base is installed below described heat exchanger body; Chemical industry high-temp liquid working chamber is provided with between described heat exchanger upper end cover and described heat exchanger lower bottom base; Described chemical industry high-temp liquid working chamber inside is provided with cooling liquid work cooling worm; Be connected with the built-in agitator of working chamber below described heat exchanger upper end cover and extend to described cooling liquid work cooling worm central authorities; Described heat exchanger body top layer is provided with heat exchanger vacuum anti-caking frost layer.
As further prioritization scheme of the present utility model, below the left side of described heat exchanger body, be connected with cooling liquid tube inlet; The outlet of cooling liquid row of conduits is connected with above the left side of described heat exchanger body; Cooling liquid pipeline intermediate thermal insulating layer is provided with between described cooling liquid tube inlet and described cooling liquid row of conduits export.
As further prioritization scheme of the present utility model, the lower right-hand side of described heat exchanger body is connected with chemical industry high-temp liquid tube inlet; The outlet of chemical industry high-temp liquid row of conduits is connected with above the right side of described heat exchanger body; Chemical industry high-temp liquid pipeline intermediate thermal insulating layer is provided with between described chemical industry high-temp liquid tube inlet and described chemical industry high-temp liquid row of conduits export.
As further prioritization scheme of the present utility model, described cooling liquid tube inlet and described cooling liquid row of conduits export right side and are provided with cooling liquid pipeline automatic pressure regulating switch; Described chemical industry high-temp liquid tube inlet and described chemical industry high-temp liquid row of conduits export left side and are provided with chemical industry high-temp liquid pipeline intermediate thermal insulating layer.
Compared with prior art, the beneficial effects of the utility model are: the utility model structure is simple, reasonable in design, are coiled and mixing plant makes cooling velocity obviously accelerate by coiled pipe, can prevent the outside frosting of heat exchanger, and manufacturing cost is not high, is applicable to using and promotes.
Accompanying drawing explanation
Fig. 1 is structural front view of the present utility model;
Fig. 2 is structure left view of the present utility model.
In figure: 1, heat exchanger body; 2, heat exchanger upper end cover; 3, heat exchanger lower bottom base; 4, cooling liquid row of conduits outlet; 5, cooling liquid tube inlet; 6, cooling liquid pipeline automatic pressure regulating switch; 7, cooling liquid work cooling worm; 8, chemical industry high-temp liquid tube inlet; 9, chemical industry high-temp liquid row of conduits outlet; 10, chemical industry high-temp liquid working chamber; 11, the built-in agitator of working chamber; 12, work high-temp liquid pipe switch; 13, heat exchanger vacuum anti-caking frost layer; 14, cooling liquid pipeline intermediate thermal insulating layer; 15, work high-temp liquid pipeline intermediate thermal insulating layer.
Detailed description of the invention
Below in conjunction with accompanying drawing and detailed description of the invention, the utility model is described in further detail:
As shown in Figure 1 and Figure 2, a kind of heat exchanger of high-temp liquid cooling when being applicable to Chemical Manufacture, comprises heat exchanger body 1, heat exchanger upper end cover 2, heat exchanger lower bottom base 3, is provided with described heat exchanger upper end cover 2 above described heat exchanger body 1; Below described heat exchanger body 1, described heat exchanger lower bottom base 3 is installed; Chemical industry high-temp liquid working chamber 10 is provided with between described heat exchanger upper end cover 2 and described heat exchanger lower bottom base 3; Described chemical industry high-temp liquid working chamber 10 inside is provided with cooling liquid work cooling worm 7; Be connected with the built-in agitator of working chamber 11 below described heat exchanger upper end cover 2 and extend to described cooling liquid work cooling worm 7 central authorities; Described heat exchanger body 1 top layer is provided with heat exchanger vacuum anti-caking frost layer 13.
Cooling liquid tube inlet 5 is connected with below the left side of described heat exchanger body 1; Cooling liquid row of conduits outlet 4 is connected with above the left side of described heat exchanger body 1; Described cooling liquid tube inlet 5 and described cooling liquid row of conduits are provided with cooling liquid pipeline intermediate thermal insulating layer 14 between exporting 4.
Described new structure is provided with cooling liquid work cooling worm 7, cooling liquid tube inlet 5, cooling liquid row of conduits outlet 4, cooling liquid is flowed into by cooling liquid tube inlet 5, then by cooling liquid work cooling worm 7, be rapidly the liquid cools cooling in chemical industry high-temp liquid working chamber 10, then flowed out by cooling liquid row of conduits outlet 4; The built-in agitator 11 of working chamber is to make high-temp liquid evenly and fully lowering the temperature.
More than show and describe general principle of the present utility model, principal character and advantage.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and description just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.

Claims (4)

1. the heat exchanger of high-temp liquid cooling when being applicable to Chemical Manufacture, it is characterized in that: comprise heat exchanger body (1), heat exchanger upper end cover (2), heat exchanger lower bottom base (3), described heat exchanger body (1) top is provided with described heat exchanger upper end cover (2); Described heat exchanger body (1) below is provided with described heat exchanger lower bottom base (3); Chemical industry high-temp liquid working chamber (10) is provided with between described heat exchanger upper end cover (2) and described heat exchanger lower bottom base (3); Described chemical industry high-temp liquid working chamber (10) inside is provided with cooling liquid work cooling worm (7); Described heat exchanger upper end cover (2) below is connected with the built-in agitator of working chamber (11) and extends to described cooling liquid work cooling worm (7) central authorities; Described heat exchanger body (1) top layer is provided with heat exchanger vacuum anti-caking frost layer (13).
2. the heat exchanger of a kind of high-temp liquid cooling when being applicable to Chemical Manufacture according to claim 1, is characterized in that: be connected with cooling liquid tube inlet (5) below the left side of described heat exchanger body (1); Cooling liquid row of conduits outlet (4) is connected with above the left side of described heat exchanger body (1); Described cooling liquid tube inlet (5) and described cooling liquid row of conduits export between (4) and are provided with cooling liquid pipeline intermediate thermal insulating layer (14).
3. the heat exchanger of a kind of high-temp liquid cooling when being applicable to Chemical Manufacture according to claim 1, is characterized in that: the lower right-hand side of described heat exchanger body (1) is connected with chemical industry high-temp liquid tube inlet (8); Chemical industry high-temp liquid row of conduits outlet (9) is connected with above the right side of described heat exchanger body (1); Described chemical industry high-temp liquid tube inlet (8) and described chemical industry high-temp liquid row of conduits export between (9) and are provided with chemical industry high-temp liquid pipeline intermediate thermal insulating layer (15).
4. the heat exchanger of a kind of high-temp liquid cooling when being applicable to Chemical Manufacture according to claim 2, is characterized in that: described cooling liquid tube inlet (5) and described cooling liquid row of conduits exports on the right side of (4) and be provided with cooling liquid pipeline automatic pressure regulating switch (6); Described chemical industry high-temp liquid tube inlet (8) and described chemical industry high-temp liquid row of conduits export (9) left side and are provided with chemical industry high-temp liquid pipeline intermediate thermal insulating layer (15).
CN201520658747.6U 2015-08-28 2015-08-28 High temperature liquid cooling's heat exchanger suitable for during chemical production Expired - Fee Related CN204987980U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520658747.6U CN204987980U (en) 2015-08-28 2015-08-28 High temperature liquid cooling's heat exchanger suitable for during chemical production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520658747.6U CN204987980U (en) 2015-08-28 2015-08-28 High temperature liquid cooling's heat exchanger suitable for during chemical production

Publications (1)

Publication Number Publication Date
CN204987980U true CN204987980U (en) 2016-01-20

Family

ID=55122341

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520658747.6U Expired - Fee Related CN204987980U (en) 2015-08-28 2015-08-28 High temperature liquid cooling's heat exchanger suitable for during chemical production

Country Status (1)

Country Link
CN (1) CN204987980U (en)

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20170808

Address after: 457000, 1 km west of Jianshe Road, Puyang and Pucheng waterway intersection, Henan, China

Patentee after: Henan Lei Bairui new Mstar Technology Ltd

Address before: 457000 Zhongyuan ethylene wastewater treatment plant, Shengli Road, Henan, Puyang

Patentee before: PUYANG DINGTAI CHEMICAL CO., LTD.

TR01 Transfer of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160120

Termination date: 20180828

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