CN205669954U - Shell-and-tube heat exchanger and liquid distributing device thereof - Google Patents

Shell-and-tube heat exchanger and liquid distributing device thereof Download PDF

Info

Publication number
CN205669954U
CN205669954U CN201620523831.1U CN201620523831U CN205669954U CN 205669954 U CN205669954 U CN 205669954U CN 201620523831 U CN201620523831 U CN 201620523831U CN 205669954 U CN205669954 U CN 205669954U
Authority
CN
China
Prior art keywords
tube
heat exchanger
liquid
distributing device
shell
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.)
Active
Application number
CN201620523831.1U
Other languages
Chinese (zh)
Inventor
吴宏择
龙忠铿
刘华
罗炽亮
李莹
张丙
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.)
Gree Electric Appliances Inc of Zhuhai
Original Assignee
Gree Electric Appliances Inc of Zhuhai
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 Gree Electric Appliances Inc of Zhuhai filed Critical Gree Electric Appliances Inc of Zhuhai
Priority to CN201620523831.1U priority Critical patent/CN205669954U/en
Application granted granted Critical
Publication of CN205669954U publication Critical patent/CN205669954U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a kind of shell-and-tube heat exchanger and liquid distributing device thereof, liquid distributing device is in the admission chamber (5) being arranged on shell-and-tube heat exchanger, and liquid distributing device includes: for covering the liquid separatnig plate (1) at described heat exchanger tube (7) mouth of pipe;It is arranged on described liquid separatnig plate (1), for the liquid separating port (2) arranged with heat exchanger tube (7) one_to_one corresponding of described admission chamber (5), the circulation area of described liquid separating port (2) is less than the circulation area of described heat exchanger tube (7).The liquid distributing device that this utility model provides, circulation area due to liquid separating port is less than the circulation area of heat exchanger tube, bigger through liquid separating port fluid resistance at fluid, fluid is uniformly distributed in admission chamber, fluid is pressure filling balance-dividing everywhere in the space of admission chamber so that fluid is uniformly distributed in every heat exchanger tube of shell-and-tube heat exchanger.By above-mentioned setting, take full advantage of the exchange capability of heat of heat exchanger tube, improve the heat exchange efficiency of shell-and-tube heat exchanger.

Description

Shell-and-tube heat exchanger and liquid distributing device thereof
Technical field
This utility model relates to technical field of heat exchange equipment, particularly to a kind of shell-and-tube heat exchanger and liquid distributing device thereof.
Background technology
Under advocating energy-conserving and environment-protective theory, there is the highest power conservation requirement in country to wasted work product, to air-conditioning products The standard-required of the coefficient of performance is more and more higher.
Shell-and-tube heat exchanger is widely used in air-conditioning equipment.As a example by dry evaporator in shell-and-tube heat exchanger, system The fluid that cryogen is formed enters in the admission chamber that shell-and-tube heat exchanger front tube box-shaped becomes, and enters back into the heat exchange arranged on tube sheet Pipe.Owing to fluid enters admission chamber through feed tube, therefore, near the heat exchange tube of feed tube in fluid preferentially enters admission chamber Mouthful, and the fluid away from the heat exchanger tube mouth of pipe of feed tube is less so that fluid cannot be uniformly distributed in shell-and-tube heat exchanger In every heat exchanger tube, have impact on heat exchange efficiency.
Therefore, how to make fluid be uniformly distributed, improve heat exchange efficiency, be those skilled in the art's problem demanding prompt solution.
Utility model content
In view of this, this utility model provides a kind of liquid distributing device, so that fluid is uniformly distributed, improves heat exchange efficiency. The invention also discloses a kind of shell-and-tube heat exchanger.
For achieving the above object, the following technical scheme of this utility model offer:
From above-mentioned technical scheme it can be seen that a kind of liquid distributing device of this utility model offer, it is used for being arranged on shell In the admission chamber of formula heat exchanger, including:
For covering the liquid separatnig plate of the heat exchanger tube mouth of pipe at described admission chamber;
It is arranged on described liquid separatnig plate, for the liquid separating port arranged with described heat exchanger tube one_to_one corresponding, described liquid separating port Circulation area is less than the circulation area of described heat exchanger tube.
Preferably, in above-mentioned liquid distributing device, also include being arranged in described liquid separating port, for stretching into dividing of described heat exchanger tube Liquid pipe.
Preferably, in above-mentioned liquid distributing device, described separating tube is copper pipe.
Preferably, in above-mentioned liquid distributing device, the outer surface of described liquid separatnig plate is stretched out in the end of described separating tube;Described separatory The outer surface of plate is the one side of its most described heat exchanger tube.
Preferably, in above-mentioned liquid distributing device, described separating tube seals and is arranged in described liquid separating port.
Preferably, in above-mentioned liquid distributing device, described separating tube is perpendicular to described liquid separatnig plate.
Preferably, in above-mentioned liquid distributing device, the outer wall of described separating tube is for contacting with the inwall of described heat exchanger tube Contact surface.
Preferably, in above-mentioned liquid distributing device, described liquid separatnig plate is provided with bolt fixing hole.
This utility model additionally provides a kind of shell-and-tube heat exchanger, including the liquid distributing device as described in above-mentioned any one.
Preferably, in above-mentioned shell-and-tube heat exchanger, the quantity of described liquid distributing device is one.
Preferably, in above-mentioned shell-and-tube heat exchanger, the liquid separatnig plate of described liquid distributing device is covered in described shell-and-tube heat exchanger Admission chamber whole heat exchanger tube mouths of pipe on.
Preferably, in above-mentioned shell-and-tube heat exchanger, the quantity of described liquid distributing device is multiple.
Preferably, in above-mentioned shell-and-tube heat exchanger, the liquid separatnig plate formation liquid separatnig plate group of multiple described liquid distributing devices, described point Liquid plate group covers whole heat exchanger tube mouths of pipe of the admission chamber of described shell-and-tube heat exchanger.
Preferably, in above-mentioned shell-and-tube heat exchanger, the liquid separating port of described liquid distributing device and described heat exchanger tube are circular hole.
Preferably, in above-mentioned shell-and-tube heat exchanger, described liquid separating port and the dead in line of corresponding described heat exchanger tube.
This utility model provide liquid distributing device, in the admission chamber being installed on shell-and-tube heat exchanger after, due to liquid separatnig plate Covering on the mouth of pipe of the heat exchanger tube of admission chamber, fluid is entered after admission chamber by the feed tube of shell-and-tube heat exchanger, need through Liquid separating port on liquid separatnig plate, enters back into heat exchanger tube.Circulation area due to liquid separating port is less than the circulation area of heat exchanger tube, at fluid Relatively big through liquid separating port fluid resistance, therefore so that fluid is uniformly distributed in admission chamber, fluid is each in the space of admission chamber The pressure filling balance-dividing at place so that fluid is uniformly distributed in every heat exchanger tube of shell-and-tube heat exchanger.By above-mentioned setting, fully Make use of the exchange capability of heat of heat exchanger tube, improve the heat exchange efficiency of shell-and-tube heat exchanger.
This utility model additionally provides a kind of shell-and-tube heat exchanger with above-mentioned liquid distributing device.Due to above-mentioned liquid distributing device Having above-mentioned technique effect, the shell-and-tube heat exchanger with above-mentioned liquid distributing device also should have same technique effect, at this not It is discussed in detail again.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, the accompanying drawing in describing below is only It is embodiments more of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work Under, it is also possible to other accompanying drawing is obtained according to these accompanying drawings.
First structural representation of the liquid distributing device that Fig. 1 provides for this utility model embodiment;
Second structural representation of the liquid distributing device that Fig. 2 provides for this utility model embodiment;
The structural representation of the shell-and-tube heat exchanger that Fig. 3 provides for this utility model embodiment.
Detailed description of the invention
The utility model discloses a kind of liquid distributing device, so that fluid is uniformly distributed, improve heat exchange efficiency.This utility model Also disclose a kind of shell-and-tube heat exchanger.
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not under making creative work premise The every other embodiment obtained, broadly falls into the scope of this utility model protection.
As shown in Figures 1 and 3, a kind of feed liquor for being arranged on shell-and-tube heat exchanger that this utility model embodiment provides Liquid distributing device in chamber 5, including liquid separatnig plate 1 and the liquid separating port 2 that is arranged on liquid separatnig plate 1.Liquid distributing device is being arranged on shell After in the admission chamber 5 of formula heat exchanger, liquid separatnig plate 1 covers on the mouth of pipe of the heat exchanger tube 7 of admission chamber 5;Liquid separating port 2 and heat exchanger tube 7 One_to_one corresponding is arranged, i.e. a liquid separating port 2 is only correspondingly arranged with a heat exchanger tube 7, and, a heat exchanger tube 7 is at most only with one Individual liquid separating port 2 is correspondingly arranged.Further, the circulation area of liquid separating port 2 is less than the circulation area of heat exchanger tube 7.
This utility model embodiment provide liquid distributing device, in the admission chamber 5 being installed on shell-and-tube heat exchanger after, due to Liquid separatnig plate 1 covers on the mouth of pipe of the heat exchanger tube 7 of admission chamber 5, and fluid is entered admission chamber 5 by the feed tube 8 of shell-and-tube heat exchanger After, need the liquid separating port 2 on liquid separatnig plate 1, enter back into heat exchanger tube 7.Owing to the circulation area of liquid separating port 2 is less than heat exchanger tube 7 Circulation area, when fluid is through liquid separating port 2, fluid resistance is relatively big, therefore so that fluid is uniformly distributed in admission chamber 5, Fluid is pressure filling balance-dividing everywhere in the space of admission chamber 5 so that be uniformly distributed in shell-and-tube heat exchanger every changes fluid Heat pipe 7.By above-mentioned setting, take full advantage of the exchange capability of heat of heat exchanger tube 7, improve the heat exchange efficiency of shell-and-tube heat exchanger.
It is understood that liquid separatnig plate 1 covers on the mouth of pipe of the heat exchanger tube 7 of admission chamber 5 so that liquid separatnig plate 1 hides and changes The mouth of pipe of heat pipe 7, all or part of of fluid cannot flow directly into heat exchanger tube 7, needs the liquid separating port 2 on liquid separatnig plate 1. The inlet that the mouth of pipe is heat exchanger tube 7 of above-mentioned heat exchanger tube 7.The circulation area of liquid separating port 2 is the cross-sectional area of its inner ring, heat exchanger tube The cross-sectional area of its endoporus of circulation area of 7.
Further, liquid distributing device also includes the separating tube 3 being arranged in liquid separating port 2.Liquid distributing device is installed on into After in sap cavity 5, it is internal that separating tube 3 stretches into heat exchanger tube 7.By arranging separating tube 3, further increase fluid through liquid distributing device Fluid resistance time (separating tube 3 in liquid separating port 2), further increases fluid distrbution in the uniformity of every heat exchanger tube 7.
Preferably, in order to reduce the impact that separating tube 3 stretches into the part heat exchanging ability of heat exchanger tube 7, preferably by separating tube 3 It is set to the copper pipe that heat exchange property is higher.
In order to reduce production cost, Q235A material can be used to make liquid separatnig plate 1.
In the present embodiment, the size of separating tube 3 is φ 4.5mm × φ 1.5mm × 40mm, i.e. the outer diameter of separating tube 3 For 4.5mm, inner diameter is 1.5mm, a length of 40mm.The thickness of liquid separatnig plate 1 is 6mm.It can also be provided that other sizes, tool Body size is depending on actual demand.
As in figure 2 it is shown, the outer surface of liquid separatnig plate 1 is stretched out in the end of separating tube 3;The outer surface of liquid separatnig plate 1 is that it changes dorsad The one side of heat pipe 7.By above-mentioned setting so that fluid cannot flow in separating tube 3 along the outer surface of liquid separatnig plate 1, needs to make stream Body just flows into separating tube 3 after being uniformly distributed in admission chamber 5.Improve fluid further and enter the uniformity coefficient of every heat exchanger tube 7.
Preferably, separating tube 3 seals and is arranged in liquid separating port 2.That is, fluid is only capable of flowing into heat exchanger tube 7 by separating tube 3 In, improve the effect of convection cell drain.Can also make to there is gap between the outer wall of separating tube 3 and the inwall of liquid separating port 2, stream Body is entered in heat exchanger tube 7 by gap and separating tube 3 homomergic flow.
In the present embodiment, separating tube 3 is connected with liquid separatnig plate 1 by welding, it is also possible to connected by interference fit or screw thread The mode such as connect is arranged in liquid separating port 2, reaches the connection effect of separating tube 3 and liquid separatnig plate 1.
In the liquid distributing device that this utility model embodiment provides, separating tube 3 is perpendicular to liquid separatnig plate 1.Due to pipe shell type heat exchange The tube sheet 6 of device is mutually perpendicular to heat exchanger tube 7, and the separating tube 3 of liquid distributing device is perpendicular to liquid separatnig plate 1, in installation process, in order to By parallel with tube sheet 6 for liquid separatnig plate 1 laminating, it is simple to connect.Separating tube 3 can also be distributed in certain acute angle with liquid separatnig plate 1, when So, separating tube 3 is parallel to each other, in installation process, and liquid separatnig plate 1 and tube sheet 6 setting in a certain angle.
The outer wall of separating tube 3 is the contact surface for contacting with the inwall of heat exchanger tube 7.That is, liquid distributing device is installed on pipe After in the admission chamber 5 of shell heat exchanger, separating tube 3 inserts in heat exchanger tube 7, and, the outer wall of separating tube 3 is interior with heat exchanger tube 7 Wall contacts, in order to support mutually between separating tube 3 and heat exchanger tube 7, and the structure further increasing shell-and-tube heat exchanger is steady Qualitative.
Bolt fixing hole 4 it is provided with on liquid separatnig plate 1.By arranging bolt so that it is with shell-and-tube after bolt fixing hole 4 The tube sheet 6 of heat exchanger connects, it is achieved that the installation of liquid distributing device is fixed.It is easy to maintenance and the maintenance of liquid distributing device.Can also lead to Cross and the mode such as weld or snap connection and complete the installation of liquid distributing device and fix, and all within protection domain.
This utility model embodiment additionally provides a kind of shell-and-tube heat exchanger, including the most above-mentioned any one liquid distributing device A.As Shown in Fig. 3, owing to above-mentioned liquid distributing device A has above-mentioned technique effect, the shell-and-tube heat exchanger with above-mentioned liquid distributing device A also should There is same technique effect, tire out the most one by one at this and state.
As it is shown on figure 3, the quantity of the liquid distributing device A in the present embodiment is one.
Preferably, the liquid separatnig plate 1 of liquid distributing device A is covered in whole heat exchanger tubes 7 mouth of pipe of admission chamber 5 of shell-and-tube heat exchanger On.That is, fluid is required to could be flowed in heat exchanger tube 7 by liquid distributing device A.Liquid separatnig plate 1 can also be covered near shell On part heat exchanger tube 7 mouth of pipe of the feed tube 8 of formula heat exchanger, and the pipe of heat exchanger tube 7 of the feed tube 8 away from shell-and-tube heat exchanger Mouth does not the most cover liquid separatnig plate 1, and the fluid at this can be directly entered heat exchanger tube 7.
In another kind of embodiment, the quantity of liquid distributing device A is multiple.
Preferably, the liquid separatnig plate 1 of multiple liquid distributing device A forms liquid separatnig plate group, and liquid separatnig plate group covers shell-and-tube heat exchanger The liquid separatnig plate group of whole heat exchanger tubes 7 mouth of pipe of admission chamber 5.By arranging multiple liquid distributing device A so that it is be installed on pipe shell type heat exchange After in the admission chamber 5 of device, cover whole heat exchanger tubes 7 mouth of pipe of the admission chamber 5 of shell-and-tube heat exchanger.
Wherein, multiple liquid separatnig plates 1 can be connected with each other, it is also possible to separate.
Similarly, liquid separatnig plate group can also be covered in part heat exchanger tube 7 mouth of pipe of the feed tube 8 near shell-and-tube heat exchanger On, the mouth of pipe away from the heat exchanger tube 7 of the feed tube 8 of shell-and-tube heat exchanger does not the most cover liquid separatnig plate 1, and the fluid at this can be straight Tap into into heat exchanger tube 7.
Preferably, the liquid separating port 2 of liquid distributing device A is circular hole with heat exchanger tube 7.Liquid separating port 2 can also be set to other The hole of structure, such as square hole or elliptical aperture etc..
Further, liquid separating port 2 and the dead in line of corresponding heat exchanger tube 7, i.e. liquid separating port 2 is with corresponding Heat exchanger tube 7 is correspondingly arranged in concentric circular.By above-mentioned setting so that the fluid flowing into heat exchanger tube 7 is flowed to serve by liquid separating port 2 Guiding function, decreases kinetic energy rejection.Be provided with in liquid separating port 2 in the embodiment of separating tube 3, also ensure that separating tube 3 with Heat exchanger tube 7 is arranged in concentric circular.
In this specification, each embodiment uses the mode gone forward one by one to describe, and what each embodiment stressed is and other The difference of embodiment, between each embodiment, identical similar portion sees mutually.
Described above to the disclosed embodiments, makes professional and technical personnel in the field be capable of or uses this practicality new Type.Multiple amendment to these embodiments will be apparent from for those skilled in the art, is determined herein The General Principle of justice can realize in the case of without departing from spirit or scope of the present utility model in other embodiments.Cause This, this utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein The widest scope consistent with features of novelty.

Claims (15)

1. a liquid distributing device, in the admission chamber (5) being arranged on shell-and-tube heat exchanger, it is characterised in that including:
For covering the liquid separatnig plate (1) of heat exchanger tube (7) mouth of pipe in described admission chamber (5);
It is arranged on described liquid separatnig plate (1), for the liquid separating port (2) arranged with described heat exchanger tube (7) one_to_one corresponding, described separatory The circulation area of mouth (2) is less than the circulation area of described heat exchanger tube (7).
2. liquid distributing device as claimed in claim 1, it is characterised in that also include being arranged in described liquid separating port (2), be used for stretching Enter the separating tube (3) of described heat exchanger tube (7).
3. liquid distributing device as claimed in claim 2, it is characterised in that described separating tube (3) is copper pipe.
4. liquid distributing device as claimed in claim 2, it is characterised in that described liquid separatnig plate is stretched out in the end of described separating tube (3) (1) outer surface;The outer surface of described liquid separatnig plate (1) is the one side of its most described heat exchanger tube (7).
5. liquid distributing device as claimed in claim 2, it is characterised in that described separating tube (3) seals and is arranged at described liquid separating port (2) in.
6. liquid distributing device as claimed in claim 2, it is characterised in that described separating tube (3) is perpendicular to described liquid separatnig plate (1).
7. liquid distributing device as claimed in claim 2, it is characterised in that the outer wall of described separating tube (3) is for for changing with described The contact surface that the inwall of heat pipe (7) contacts.
8. the liquid distributing device as described in any one of claim 1-7, it is characterised in that described liquid separatnig plate is provided with bolt on (1) Fixing hole (4).
9. a shell-and-tube heat exchanger, it is characterised in that include the liquid distributing device (A) as described in any one of claim 1-8.
10. shell-and-tube heat exchanger as claimed in claim 9, it is characterised in that the quantity of described liquid distributing device (A) is.
11. shell-and-tube heat exchangers as claimed in claim 10, it is characterised in that the liquid separatnig plate (1) of described liquid distributing device (A) covers On whole heat exchanger tubes (7) mouth of pipe of the admission chamber (5) being placed on described shell-and-tube heat exchanger.
12. shell-and-tube heat exchangers as claimed in claim 9, it is characterised in that the quantity of described liquid distributing device (A) is multiple.
13. shell-and-tube heat exchangers as claimed in claim 12, it is characterised in that the liquid separatnig plate of multiple described liquid distributing devices (A) (1) forming liquid separatnig plate group, described liquid separatnig plate group covers whole heat exchanger tubes (7) pipe of the admission chamber (5) of described shell-and-tube heat exchanger Mouthful.
14. shell-and-tube heat exchangers as described in any one of claim 9-13, it is characterised in that dividing of described liquid distributing device (A) Liquid mouth (2) and described heat exchanger tube (7) are circular hole.
15. shell-and-tube heat exchangers as claimed in claim 14, it is characterised in that described liquid separating port (2) and corresponding institute State the dead in line of heat exchanger tube (7).
CN201620523831.1U 2016-06-01 2016-06-01 Shell-and-tube heat exchanger and liquid distributing device thereof Active CN205669954U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620523831.1U CN205669954U (en) 2016-06-01 2016-06-01 Shell-and-tube heat exchanger and liquid distributing device thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620523831.1U CN205669954U (en) 2016-06-01 2016-06-01 Shell-and-tube heat exchanger and liquid distributing device thereof

Publications (1)

Publication Number Publication Date
CN205669954U true CN205669954U (en) 2016-11-02

Family

ID=57194516

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620523831.1U Active CN205669954U (en) 2016-06-01 2016-06-01 Shell-and-tube heat exchanger and liquid distributing device thereof

Country Status (1)

Country Link
CN (1) CN205669954U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105890409A (en) * 2016-06-01 2016-08-24 珠海格力电器股份有限公司 Shell and tube heat exchanger and liquid distribution device thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105890409A (en) * 2016-06-01 2016-08-24 珠海格力电器股份有限公司 Shell and tube heat exchanger and liquid distribution device thereof

Similar Documents

Publication Publication Date Title
CN104807351B (en) Pure counterflow shell-and-tube heat exchanger and manufacturing method thereof
CN105890409A (en) Shell and tube heat exchanger and liquid distribution device thereof
CN204007233U (en) The U-shaped pipe heat exchanger of a kind of continuous helical deflecting plate
CN201359464Y (en) Parallel-flow evaporator
CN202928410U (en) Double-tube pass graphite tube type seawater heat exchanger
CN205669954U (en) Shell-and-tube heat exchanger and liquid distributing device thereof
CN111043881A (en) Plate heat exchanger with secondary distribution function
CN201607149U (en) Horizontal finned shell-and-tube heat exchanger
CN205316751U (en) Efficient monosystem is U type pipe evaporimeter all
CN203385245U (en) Shell-and-tube condenser
CN204718448U (en) The energy-saving shell-and-tube oil cooler of circulation
CN110595114A (en) Micro-channel condenser for circulating air source heat pump water heater
CN204006813U (en) A kind of highly effective dry-type shell-and-tube evaporator
CN206192145U (en) Plastic heat exchanger
CN202478618U (en) Plate type falling film evaporator
CN105423649A (en) Micro-channel heat exchanger and air conditioner provided with same
CN202547447U (en) Shell and tube condenser
CN205878962U (en) Mould high -efficient novel shell tube heat exchanger of shell
CN205641695U (en) Condenser
CN110779196B (en) Heat exchange tube and heat exchanger
CN211451460U (en) Micro-channel condenser for circulating air source heat pump water heater
CN210533118U (en) Shell-and-tube heat exchanger with inner tube bundle convenient to disassemble
CN206252988U (en) A kind of glass steel shell is bonded tubulation graphite falling film absorber without clay
CN207172562U (en) A kind of powdery paints tabletting machine roller
PH12018500588A1 (en) Double plated heat exchange

Legal Events

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