CN208687990U - A kind of interior anti-corrosion type volumetric heat exchanger - Google Patents

A kind of interior anti-corrosion type volumetric heat exchanger Download PDF

Info

Publication number
CN208687990U
CN208687990U CN201821078438.1U CN201821078438U CN208687990U CN 208687990 U CN208687990 U CN 208687990U CN 201821078438 U CN201821078438 U CN 201821078438U CN 208687990 U CN208687990 U CN 208687990U
Authority
CN
China
Prior art keywords
fluid reservoir
heat exchanging
exchanging chamber
chamber
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.)
Expired - Fee Related
Application number
CN201821078438.1U
Other languages
Chinese (zh)
Inventor
黄云刚
江广华
黄杨新
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.)
Guangzhou Laun Heat Exchange Machinery Co Ltd
Original Assignee
Guangzhou Laun Heat Exchange Machinery 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 Guangzhou Laun Heat Exchange Machinery Co Ltd filed Critical Guangzhou Laun Heat Exchange Machinery Co Ltd
Priority to CN201821078438.1U priority Critical patent/CN208687990U/en
Application granted granted Critical
Publication of CN208687990U publication Critical patent/CN208687990U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model provides a kind of interior anti-corrosion type volumetric heat exchanger, including fluid reservoir, heat exchanging chamber, inlet tube, outlet tube, adaptor cover and heating tube bundle, the inlet tube is connected to the top of the fluid reservoir, the outlet tube is connected to the bottom of the fluid reservoir, the heat exchanging chamber is set to the inner wall of the fluid reservoir, phase change medium is perfused in the heat exchanging chamber, to be formed with liquid phase region and gas phase zone in the heat exchanging chamber, the gas phase zone is located at the top of the liquid phase region, multiple heat exchange fins are provided at the top of the heat exchanging chamber, corrosion-inhibiting coating is coated on the outer wall of the heat exchanging chamber, admission chamber and out sap cavity are formed in the adaptor cover, the admission chamber is connected to the sap cavity out by the heating tube bundle, the heating tube bundle is immersed in the liquid phase region.The utility model, which aims to solve the problem that, has that corrosion-inhibiting coating influences heat exchange efficiency when existing volumetric heat exchanger carries out corrosive liquid heat exchange.

Description

A kind of interior anti-corrosion type volumetric heat exchanger
Technical field
A kind of the utility model category technical field of heat exchange devices, and in particular to interior anti-corrosion type volumetric heat exchanger.
Background technique
Volumetric heat exchanger is the heat-exchanging tube bundle flowed through in tank body using hot coal, to carry out to the refrigerant in tank body The cold and hot fluid of the heat exchanger heated, partition volumetric heat exchanger is separated by solid partition, and carries out heat by partition The heat exchanger of exchange, therefore also known as surface-type heat exchanger.
Existing volumetric heat exchanger is chiefly used in the heat exchange of the lower liquid of corrosivity, when volumetric heat exchanger is for corroding When the higher liquid heat exchange of property, then need to coat corrosion-inhibiting coating on the outer wall of heat-exchanging tube bundle, to avoid corrosive liquids to gold The corrosion for belonging to heat-exchanging tube bundle causes conduction oil to be revealed, however coats the heat exchange efficiency of corrosion-inhibiting coating exchange heat pipe bundle with biggish It influences, causes the heat exchange efficiency of volumetric heat exchanger to decline serious.
Utility model content
For the above technical problems, the utility model provides a kind of interior anti-corrosion type volumetric heat exchanger, with solution Certainly existing volumetric heat exchanger carries out there are problems that corrosion-inhibiting coating influences heat exchange efficiency when corrosive liquid heat exchange, devises one Anti-corrosion type volumetric heat exchanger, can effectively improve heat exchange efficiency while guaranteeing requirement for anticorrosion in kind.
The utility model provides a kind of interior anti-corrosion type volumetric heat exchanger, including fluid reservoir, heat exchanging chamber, inlet tube, goes out Liquid pipe, adaptor cover and heating tube bundle, the inlet tube are connected to the top of the fluid reservoir, and the outlet tube is connected to the storage The bottom of flow container, the heat exchanging chamber is set to the inner wall of the fluid reservoir, and the heat exchanging chamber is not connected to mutually with the fluid reservoir, It is perfused with phase change medium in the heat exchanging chamber, to be formed with liquid phase region and gas phase zone, the gas phase position in the heat exchanging chamber It is provided with multiple heat exchange fins at the top of the top of the liquid phase region, the heat exchanging chamber, is coated on the outer wall of the heat exchanging chamber There is corrosion-inhibiting coating, the heat exchange fin part is located in the gas phase zone, and the heat exchange fin part is located in the fluid reservoir, The adaptor cover is set on the outer wall of the fluid reservoir, and admission chamber and out sap cavity, the switching are formed in the adaptor cover It covers and is provided with the oil inlet for being connected to the admission chamber and the oil outlet for being connected to the sap cavity out, the admission chamber It is connected to the sap cavity out by the heating tube bundle, the heating tube bundle is immersed in the liquid phase region.
Further, liquid valve is provided on the outlet tube.
Further, the fluid reservoir includes tank body and lid, and the lid is removably attachable to the top of the tank body Portion, the inlet tube are located at the top of the lid, and the outlet tube is located at the bottom of the tank body.
Anti-corrosion type volumetric heat exchanger is applied to the heat exchange of corrosive liquids in this, and heat exchanging chamber is provided in fluid reservoir, Heating and gasifying is carried out by the phase change medium in heating tube bundle heat exchanging chamber, the phase change medium of gasification is by the heat exchange fin and institute The corrosive liquids stated in fluid reservoir exchanges heat, so that heat conduction is carried out, since the heating tube bundle is not direct and corrosion Property liquid contact, can not the outer surface of heating tube bundle coat corrosion-inhibiting coating, only need to coat on the outer wall of the heat exchanging chamber prevent Rotten coating, and the heat exchanging chamber is exchanged heat with corrosive liquids by the heat exchange fin, and corrosion-inhibiting coating heat exchanging is reduced The influence of efficiency, corrosion resistant stainless steel plate may be selected in the heat exchange fin, and even if corrosive liquids heat exchanging fin has Certain corrosivity will not lead to the leakage of phase change medium.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor Under, it is also possible to obtain other drawings based on these drawings.
Fig. 1 is a kind of structural schematic diagram of interior anti-corrosion type volumetric heat exchanger.
Specific embodiment
The utility model discloses a kind of interior anti-corrosion type volumetric heat exchangers, can be effective while guaranteeing requirement for anticorrosion Improve heat exchange efficiency.
Below in conjunction with the attached drawing in the utility model, the technical solution in the utility model is carried out clearly and completely Description, it is clear that described is only the utility model a part of the embodiment, instead of all the embodiments.It is practical based on this Embodiment in novel, those of ordinary skill in the art are obtained every other without creative labor Embodiment is fallen within the protection scope of the utility model.
Shown in Figure 1, the utility model provides a kind of interior anti-corrosion type volumetric heat exchanger, including fluid reservoir 15, changes Hot chamber 3, inlet tube 1, outlet tube 10, adaptor cover 16 and heating tube bundle 8, the inlet tube 1 are connected to the top of the fluid reservoir 15 Portion, the outlet tube 10 are connected to the bottom of the fluid reservoir 15, and the heat exchanging chamber 3 is set to the inner wall of the fluid reservoir 15, And the heat exchanging chamber 3 is not connected to mutually with the fluid reservoir 15, phase change medium is perfused in the heat exchanging chamber 3, in the heat exchange Liquid phase region 12 and gas phase zone 13 are formed in chamber 3, the gas phase zone 13 is located at the top of the liquid phase region 12, the heat exchanging chamber 3 Top be provided with multiple heat exchange fins 14, corrosion-inhibiting coating, the heat exchange fin 14 are coated on the outer wall of the heat exchanging chamber 3 Quartile is in the gas phase zone 3, and 14 part of heat exchange fin is located in the fluid reservoir 15, and the adaptor cover 16 is set to institute On the outer wall for stating fluid reservoir 15, it is formed with admission chamber 6 and out sap cavity 4 in the adaptor cover 16, is provided in the adaptor cover 16 Oil outlet 5 for being connected to the oil inlet 7 of the admission chamber 6 and for being connected to the sap cavity 4 out, the admission chamber 6 and institute It states out sap cavity 4 to be connected to by the heating tube bundle 8, the heating tube bundle 8 is immersed in the liquid phase region 12.
Liquid valve 9 is provided on the outlet tube 10.
The fluid reservoir 15 includes tank body 11 and lid 2, and the lid 2 is removably attachable to the top of the tank body 11 Portion, the inlet tube 1 are located at the top of the lid 2, and the outlet tube 10 is located at the bottom of the tank body 11.
Anti-corrosion type volumetric heat exchanger is applied to the heat exchange of corrosive liquids in this, and heat exchanging chamber is provided in fluid reservoir, Heating and gasifying is carried out by the phase change medium in heating tube bundle heat exchanging chamber, the phase change medium of gasification is by the heat exchange fin and institute The corrosive liquids stated in fluid reservoir exchanges heat, so that heat conduction is carried out, since the heating tube bundle is not direct and corrosion Property liquid contact, can not the outer surface of heating tube bundle coat corrosion-inhibiting coating, only need to coat on the outer wall of the heat exchanging chamber prevent Rotten coating, and the heat exchanging chamber is exchanged heat with corrosive liquids by the heat exchange fin, and corrosion-inhibiting coating heat exchanging is reduced The influence of efficiency, corrosion resistant stainless steel plate may be selected in the heat exchange fin, and even if corrosive liquids heat exchanging fin has Certain corrosivity will not lead to the leakage of phase change medium.
It, cannot the above content is specific preferred embodiment further detailed description of the utility model is combined Assert that the specific implementation of the utility model is only limited to these instructions.For the ordinary skill of the utility model technical field For personnel, without departing from the concept of the premise utility, a number of simple deductions or replacements can also be made, should all regard To belong to the protection scope of the utility model.

Claims (3)

1. a kind of interior anti-corrosion type volumetric heat exchanger, which is characterized in that including fluid reservoir, heat exchanging chamber, inlet tube, outlet tube, turn Lid and heating tube bundle are connect, the inlet tube is connected to the top of the fluid reservoir, and the outlet tube is connected to the fluid reservoir Bottom, the heat exchanging chamber is set to the inner wall of the fluid reservoir, and the heat exchanging chamber is not connected to mutually with the fluid reservoir, described to change It is perfused with phase change medium in hot chamber, to be formed with liquid phase region and gas phase zone in the heat exchanging chamber, the gas phase zone is located at described The top of liquid phase region is provided with multiple heat exchange fins at the top of the heat exchanging chamber, is coated with anti-corrosion on the outer wall of the heat exchanging chamber Coating, the heat exchange fin part are located in the gas phase zone, and the heat exchange fin part is located in the fluid reservoir, and described turn It connects lid to be set on the outer wall of the fluid reservoir, admission chamber and out sap cavity is formed in the adaptor cover, is set in the adaptor cover Be equipped with the oil inlet for being connected to the admission chamber and for be connected to it is described go out sap cavity oil outlet, the admission chamber and described Sap cavity is connected to by the heating tube bundle out, and the heating tube bundle is immersed in the liquid phase region.
2. a kind of interior anti-corrosion type volumetric heat exchanger according to claim 1, which is characterized in that be arranged on the outlet tube There is liquid valve.
3. a kind of interior anti-corrosion type volumetric heat exchanger according to claim 1, which is characterized in that the fluid reservoir includes tank Body and lid, the lid are removably attachable to the top of the tank body, and the inlet tube is located at the top of the lid, institute State the bottom that outlet tube is located at the tank body.
CN201821078438.1U 2018-07-09 2018-07-09 A kind of interior anti-corrosion type volumetric heat exchanger Expired - Fee Related CN208687990U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821078438.1U CN208687990U (en) 2018-07-09 2018-07-09 A kind of interior anti-corrosion type volumetric heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821078438.1U CN208687990U (en) 2018-07-09 2018-07-09 A kind of interior anti-corrosion type volumetric heat exchanger

Publications (1)

Publication Number Publication Date
CN208687990U true CN208687990U (en) 2019-04-02

Family

ID=65880174

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821078438.1U Expired - Fee Related CN208687990U (en) 2018-07-09 2018-07-09 A kind of interior anti-corrosion type volumetric heat exchanger

Country Status (1)

Country Link
CN (1) CN208687990U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111748269A (en) * 2019-03-29 2020-10-09 青岛海尔智能技术研发有限公司 Preservative for aluminum alloy micro-channel heat exchanger, protection method of preservative and heat exchanger

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111748269A (en) * 2019-03-29 2020-10-09 青岛海尔智能技术研发有限公司 Preservative for aluminum alloy micro-channel heat exchanger, protection method of preservative and heat exchanger

Similar Documents

Publication Publication Date Title
CN202018219U (en) Multistage combined heat exchange device
CN208687990U (en) A kind of interior anti-corrosion type volumetric heat exchanger
CN103424012A (en) Immersion type ring tube heat exchanger
CN209783349U (en) Sleeve type self-cleaning heat exchanger
CN204705216U (en) Leakage resistance vapour type shell-and-tube experiment condenser
CN205332517U (en) Can increase water quality and possess displacement heat exchanger of anticorrosive function
CN109668451A (en) A kind of high-efficiency falling film type evaporation equipment and liquid distribution method
CN103438753A (en) Novel baffle plate
CN203586882U (en) Immersed annular tube heat exchanger
CN109253633A (en) Pipe arranges unitized exchanger
CN102478366A (en) Multistage combined heat exchanging device
CN203785520U (en) Novel baffle plate
CN204932895U (en) A kind of silicon carbide ceramics tubular type falling film evaporator
CN204043474U (en) Shell-and-tube phase change heat exchanger and liquid spray thrower thereof
CN209386612U (en) A kind of dry type shell and tube evaporator condenser combined system
CN207422941U (en) Corrosion-resistant heat exchanger
CN207231003U (en) A kind of low-temperature air source heat pump heating machine water-side heat
CN215337930U (en) Partition plate type heat exchange tube
CN215003073U (en) Corrosion-resistant ultrathin metal heat exchanger
CN208651094U (en) A kind of compressor heat exchanger
CN207487467U (en) A kind of tubular heat exchanger
CN209386857U (en) Anti- seawater corrosion shell-and-tube heat exchanger
CN213300927U (en) Corrosion-resistant heat exchanger
CN109703927A (en) A kind of outer coil pipe basin of enamel
CN107741167A (en) Corrosion-resistant heat exchanger

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190402

Termination date: 20210709