CN207472125U - High-performance heat exchanger system - Google Patents

High-performance heat exchanger system Download PDF

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Publication number
CN207472125U
CN207472125U CN201721492229.7U CN201721492229U CN207472125U CN 207472125 U CN207472125 U CN 207472125U CN 201721492229 U CN201721492229 U CN 201721492229U CN 207472125 U CN207472125 U CN 207472125U
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CN
China
Prior art keywords
heat exchanger
hydrocyclone
performance heat
exchanger system
recirculated water
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Expired - Fee Related
Application number
CN201721492229.7U
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Chinese (zh)
Inventor
徐建民
吴礼彬
林纬
喻九阳
郑小涛
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.)
Wuhan Institute of Technology
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Wuhan Institute of Technology
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Priority to CN201721492229.7U priority Critical patent/CN207472125U/en
Application granted granted Critical
Publication of CN207472125U publication Critical patent/CN207472125U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model is related to high-performance heat exchanger systems,It is pumped including sequentially connected into water management,Electrolytic cell,Go precipitation unit,Bubble removing unit,Heat exchanger and water tank,Precipitation unit is gone to include the first kinetic pump and the first hydrocyclone,Bubble removing unit includes the second kinetic pump and the second hydrocyclone,The high efficient heat exchanging system further includes a control system,It is pumped into water management,Electrolytic cell,First kinetic pump and the second kinetic pump are connect with control system,Recirculated water removes calcium ions and magnesium ions therein by electrolytic cell,Again by the way that precipitation unit is gone to separate precipitation,Bubble in recirculated water is removed by bubble removing unit,This high-performance heat exchanger system avoids the scale problems that heat exchanger frequently encounters,It also avoids corrosion being caused to happen equipment using antisludging agent,It is hardly damaged equipment,It is achieved thereby that the purpose of heat exchanger efficient operation and long-lived operation.

Description

High-performance heat exchanger system
Technical field
The utility model is related to chemical equipment technical field, more particularly, to high-performance heat exchanger system.
Background technology
Existing heat exchanger is exchanged heat using recirculated cooling water, water quality hardness itself and due to being concentrated by evaporation, Calcium ions and magnesium ions concentration can gradually rise in cyclic process, and the easily fouling in heat exchanger not only influences efficiency of heat exchanger in this way, The service life of heat exchanger can also be reduced.Heat exchanging device scale removal currently on the market mainly reduces scale inhibition, but hinder by antisludging agent Dirty agent meeting heat exchanging device causes to corrode in itself, damages heat exchanger, this results in heat exchanger reduced lifetime, is taken as production consumptive material Situation causes cost serious waste.
Utility model content
Scale inhibition can be reduced the technical problem to be solved by the utility model is to provide one kind, be hardly damaged, and improve The high-performance heat exchanger system in service life.
The utility model the technical scheme adopted is that high-performance heat exchanger system, including it is sequentially connected into water management pump, Electrolytic cell removes precipitation unit, bubble removing unit, heat exchanger and water tank, and precipitation unit is gone to include the first kinetic pump and first Hydrocyclone, bubble removing unit include the second kinetic pump and the second hydrocyclone, which further includes one Control system is connect into water management pump, electrolytic cell, the first kinetic pump and the second kinetic pump with control system.
The beneficial effects of the utility model are:Recirculated water removes calcium ions and magnesium ions therein by electrolytic cell, then by going to sink Shallow lake unit separates precipitation, removes the bubble in recirculated water by bubble removing unit, this high-performance heat exchanger system, which avoids, changes The scale problems that hot device frequently encounters also avoid corrosion being caused to happen equipment using antisludging agent, are hardly damaged and set It is standby, it is achieved thereby that the purpose of heat exchanger efficient operation and long-lived operation.
As priority, electrolytic cell is U-shaped structure, cathode and anode has been symmetrically arranged on electrolytic cell wall surface, using this Structure, recirculated water can continue that cell reaction occurs during flowing through electrolytic cell.
As priority, the first hydrocyclone includes the first cyclone body and is followed with what the first cyclone body was connect Ring water overflow channel, the first cyclone body include a first outlet for precipitation discharge, and recirculated water overflow channel includes one A second outlet for recirculated water outflow, using the structure, sediment is gradually downward on the internal face of the first cyclone body Deposition is discharged from first outlet, and the recirculated water for removing particulate matter is flowed out from the second outlet of recirculated water overflow channel.
As priority, recirculated water overflow channel further includes several through-holes being opened on conduit wall, can be with using the structure Increase the speed that recirculated water enters recirculated water overflow channel, improve water circulation efficiency.
As priority, the second hydrocyclone includes the second cyclone body, and the second cyclone body includes being opened in the The gas discharge pipe and be opened on the second cyclone body for recirculated water outflow that supplied gas is discharged on two cyclone bodies Third exports, can be by the gas in recirculated water from gas discharge pipe, so as to remove the bubble in recirculated water using the structure.
As priority, the first hydrocyclone and the second hydrocyclone include a butterfly valve, and butterfly valve is equal Including dish plate and the opening controller being connect with dish plate, using the structure, in the first hydrocyclone, recirculated water passes through dish Plate is entered in the first cyclone body, and staff can adjust opening controller to match flow, obtains best separation Effect;It, can be with arbitrarily to adjust the opening controller of the butterfly valve on the second hydrocyclone in the second hydrocyclone Suitable flow is adjusted according to the situation of underwater bubble to obtain best separating effect.
As priority, there are one separation cones for setting in the gas discharge pipe on the second cyclone body, detach the bottom of cone Setting offers several penetrating gaps there are one disk-shaped structure on the disk-shaped structure, using the structure, can by detach cone come Gas is formed and is disturbed, improves separating effect.
Description of the drawings
Fig. 1 is the structure diagram of the utility model high-performance heat exchanger system;
Fig. 2 is the structure diagram of the first hydrocyclone of the utility model high-performance heat exchanger system;
Fig. 3 is the structure diagram of the second hydrocyclone of the utility model high-performance heat exchanger system;
Fig. 4 is the structure diagram of the separation cone of the utility model high-performance heat exchanger system;
Fig. 5 is the structure diagram of the electrolytic cell of the utility model high-performance heat exchanger system;
As shown in the figure:1st, control system;2nd, it is pumped into water management;3rd, electrolytic cell;4th, precipitation unit is gone;5th, bubble removing unit; 6th, heat exchanger;7th, water tank;8th, the first kinetic pump;9th, the first hydrocyclone;10th, the second kinetic pump;11st, the second hydraulic cyclone Device;12nd, the first cyclone body;13rd, recirculated water overflow channel;14th, first outlet;15th, second outlet;16th, the second cyclone Ontology;17th, gas discharge pipe;18th, third exports;19th, dish plate;20th, opening controller;21st, separation cone;22nd, disk-shaped structure; 23rd, cathode;24th, anode;25th, through-hole.
Specific embodiment
Utility model is further described referring to the drawings and with reference to specific embodiment, to enable those skilled in the art It can implement according to this with reference to specification word, scope of protection of the utility model is not limited to the specific embodiment.
The utility model is related to high-performance heat exchanger system, as shown in Figure 1, including sequentially connected into water management pump 2, electrolysis Slot 3 removes precipitation unit 4, bubble removing unit 5, heat exchanger 6 and water tank 7, and precipitation unit 4 is gone to include the first kinetic pump 8 and the One hydrocyclone 9, bubble removing unit 5 include the second kinetic pump 10 and the second hydrocyclone 11, and the high efficient heat exchanging system is also Including a control system 1, into water management pump 2, electrolytic cell 3, the first kinetic pump 8 and the second kinetic pump 10 and control system 1 connection.
As priority, as shown in figure 5, electrolytic cell 3 is U-shaped structure, cathode 23 has been symmetrically arranged on 3 wall surface of electrolytic cell With anode 24, recirculated water, which flows through, can continue during electrolytic cell that cell reaction occurs, even if recirculated water flow velocity comparatively fast can Obtain preferable electrolysis effectiveness.
As priority, as shown in Fig. 2, the first hydrocyclone 9 include the first cyclone body 12 and with the first eddy flow The recirculated water overflow channel 13 that device ontology 12 connects, the first cyclone body 12 include a first outlet for precipitation discharge 14, recirculated water overflow channel 13 includes a second outlet 15 for recirculated water outflow.
As priority, recirculated water overflow channel 13 further includes several through-holes 25 being opened on conduit wall.
As priority, as shown in figure 3, the second hydrocyclone 11 includes the second cyclone body 16, the second cyclone sheet Body 16 includes being opened in the gas discharge pipe 17 and be opened in the second cyclone that supplied gas is discharged on the second cyclone body 16 For the third outlet 18 of recirculated water outflow on ontology 16.
As priority, as shown in Figure 2 and Figure 3, the first hydrocyclone 9 includes a butterfly valve, the second hydrocyclone 11 also include a butterfly valve, and butterfly valve includes dish plate 19 and the opening controller 20 being connect with dish plate 19, using this Structure, in the first hydrocyclone 9, recirculated water is entered by dish plate 19 in the first cyclone body 12.
As priority, the as shown in figure 3, there are one separation cones for setting in gas discharge pipe 17 on two cyclone bodies 16 21, as shown in figure 4, the bottom setting of separation cone 21 offers several perforations there are one disk-shaped structure 22 on the disk-shaped structure 22 Gap.
The heat exchange principle of high-performance heat exchanger system is:Recirculated water is stored in water tank 7, the control water inlet of control system 1 2 work of control pump, makes recirculated water flow into electrolytic cell 3 from water tank 7, control system 1 powers to electrolytic cell 3, passes through appropriate electricity The voltage-controlled system of galvanic electricity, occurs cell reaction between electrode, and the calcium ions and magnesium ions in recirculated water is made to form Precipitation, following comprising precipitation Ring water enters precipitation unit 4, recirculated water is made to enter in the first hydrocyclone 9 by the first kinetic pump 8, in centrifugal force Under the action of, sediment is discharged from the first outlet 14 on the first cyclone body 12, removes the recirculated water of sediment from cycle The second outlet 15 of water overflow channel flows out, and the recirculated water after removal precipitation enters bubble removing unit 5, passes through the second kinetic pump 10 make recirculated water enter in the second hydrocyclone 11, and under the influence of centrifugal force, gas in recirculated water is from the second eddy flow It is overflowed in the gas discharge pipe 17 of device ontology 16, the recirculated water for removing gas exports 18 from the third of the second cyclone body 16 Outflow, treated after recirculated water exchanged heat by heat exchanger 6, then flows into water tank 7, recycles and carries out according to above-mentioned steps, The hardness of recirculated water can be maintained to relatively low level, sustainable protection heat exchanger is needed periodically in use to electrolytic cell 3 Cathode 23 and 24 surface of anode are cleared up, and have prevented sediment absorption from influencing electrolysis on the electrode, the high-performance heat exchanger System can remove calcium ions and magnesium ions, and can divide rapidly by electrolysis during circulating water flow is through electrolytic cell From precipitation and bubble, avoid, using antisludging agent, while heat exchanger efficient operation is ensured, extending the service life of heat exchanger.

Claims (9)

1. high-performance heat exchanger system, it is characterised in that:Including it is sequentially connected into water management pump (2), electrolytic cell (3), go to precipitate Unit (4), bubble removing unit (5), heat exchanger (6) and water tank (7), go precipitation unit (4) including the first kinetic pump (8) and First hydrocyclone (9), bubble removing unit (5) include the second kinetic pump (10) and the second hydrocyclone (11), the height Effect heat-exchange system further includes a control system (1), into water management pump (2), electrolytic cell (3), the first kinetic pump (8) and second Kinetic pump (10) is connect with control system (1).
2. high-performance heat exchanger system according to claim 1, it is characterised in that:Electrolytic cell (3) be U-shaped structure, electrolytic cell (3) cathode (23) and anode (24) have been symmetrically arranged on wall surface.
3. high-performance heat exchanger system according to claim 1, it is characterised in that:First hydrocyclone (9) is including first Cyclone body (12) and the recirculated water overflow channel (13) being connect with the first cyclone body (12), the first cyclone body (12) including the first outlet (14) one for precipitation discharge, recirculated water overflow channel (13) is including one for recirculated water outflow Second outlet (15).
4. high-performance heat exchanger system according to claim 2, it is characterised in that:Recirculated water overflow channel (13) further includes out Several through-holes (25) being located on conduit wall.
5. high-performance heat exchanger system according to claim 1, it is characterised in that:Second hydrocyclone (11) is including second Cyclone body (16), the second cyclone body (16) is including being opened in the gas that supplied gas is discharged on the second cyclone body (16) Body delivery pipe (17) and be opened on the second cyclone body (16) for recirculated water outflow third outlet (18).
6. high-performance heat exchanger system according to claim 4, it is characterised in that:First hydrocyclone (9) includes one Butterfly valve, butterfly valve include dish plate (19) and the opening controller (20) being connect with dish plate (19).
7. high-performance heat exchanger system according to claim 5, it is characterised in that:Second hydrocyclone (11) includes one Butterfly valve, butterfly valve include dish plate (19) and the opening controller (20) being connect with dish plate (19).
8. high-performance heat exchanger system according to claim 5, it is characterised in that:Gas on second cyclone body (16) There are one separation cones (21) for setting in delivery pipe (17).
9. high-performance heat exchanger system according to claim 8, it is characterised in that:There are one the bottom settings of separation cone (21) Disk-shaped structure (22) offers several penetrating gaps on the disk-shaped structure.
CN201721492229.7U 2017-11-10 2017-11-10 High-performance heat exchanger system Expired - Fee Related CN207472125U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721492229.7U CN207472125U (en) 2017-11-10 2017-11-10 High-performance heat exchanger system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721492229.7U CN207472125U (en) 2017-11-10 2017-11-10 High-performance heat exchanger system

Publications (1)

Publication Number Publication Date
CN207472125U true CN207472125U (en) 2018-06-08

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CN201721492229.7U Expired - Fee Related CN207472125U (en) 2017-11-10 2017-11-10 High-performance heat exchanger system

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108151577A (en) * 2017-11-10 2018-06-12 武汉工程大学 High-performance heat exchanger system and its heat-exchange method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108151577A (en) * 2017-11-10 2018-06-12 武汉工程大学 High-performance heat exchanger system and its heat-exchange method

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

Granted publication date: 20180608

Termination date: 20201110

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