CN109813148A - Cyclic annular sprinkle heat-exchanger rig and its application method - Google Patents

Cyclic annular sprinkle heat-exchanger rig and its application method Download PDF

Info

Publication number
CN109813148A
CN109813148A CN201910216750.5A CN201910216750A CN109813148A CN 109813148 A CN109813148 A CN 109813148A CN 201910216750 A CN201910216750 A CN 201910216750A CN 109813148 A CN109813148 A CN 109813148A
Authority
CN
China
Prior art keywords
sprinkle
heat
heat exchange
disk
coil
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.)
Pending
Application number
CN201910216750.5A
Other languages
Chinese (zh)
Inventor
苏宇贵
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201910216750.5A priority Critical patent/CN109813148A/en
Publication of CN109813148A publication Critical patent/CN109813148A/en
Pending legal-status Critical Current

Links

Landscapes

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

Abstract

The invention discloses a kind of cyclic annular sprinkle heat-exchanger rigs, including heat exchange coil, sprinkle disk, tray, circulation line and rack, the heat exchange coil, sprinkle disk and tray are installed in the rack, it is ring structure under the heat exchange coil overlook direction, the heat exchange coil has first port and second port, the first port is upward, the second port is downward, the sprinkle disk is mounted on above the first port, the tray is mounted below the second port, and the sprinkle disk and the tray pass through the circulation line connection.By the heat exchange of sprinkle disk and annular heat exchange coil, heat exchange efficiency is improved.

Description

Cyclic annular sprinkle heat-exchanger rig and its application method
Technical field
The present invention relates to field of heat exchange, especially a kind of cyclic annular sprinkle heat-exchanger rig and its application method.
Background technique
The heat exchanger tube of traditional heat exchanger is usually arranged as linear type, and then more heat exchanger tubes are arranged in serpentine configuration, but It is due to the faster outflow heat exchanger of heat-exchange working medium in shower process in heat exchanger tube, so heat exchange leads to heat exchange efficiency not It is high.
Summary of the invention
It is an object of the invention to improve the prior art, a kind of cyclic annular sprinkle heat-exchanger rig and its user are provided Method improves heat exchange efficiency.
Its technical solution is as follows:
Cyclic annular sprinkle heat-exchanger rig, including heat exchange coil, sprinkle disk, tray, circulation line and rack, the heat exchange plate Pipe, sprinkle disk and tray are installed in the rack, are ring structure, the heat exchange under the heat exchange coil overlook direction Coil pipe has first port and second port, and upward, downward, the sprinkle disk is mounted on the second port first port Above the first port, the tray is mounted below the second port, and the sprinkle disk and the tray pass through The circulation line connection.
The circulation line includes circulating line and the circulation pump housing, and the tray, the circulation pump housing, sprinkle disk pass through described Circulating line series connection.
It further include blower, the blower, for the assembling above the first port, the blower is located at institute It states on the straight line of central axis coincidence of heat exchange coil.
Offer circular through hole in the middle part of the sprinkle disk, the sprinkle dish type circlewise structure, the cricoid sprinkle disk Outer diameter is greater than or equal to the outer diameter of the heat exchange coil, and the cricoid sprinkle disk internal diameter is less than or equal to the heat exchange coil Internal diameter, the outer diameter of the tray are greater than or equal to the outer diameter of the sprinkle disk.
Inside diameter or top of the assembling in the cyclic annular sprinkle disk.
The heat exchange coil includes light pipe coil pipe, and the light pipe coil pipe is bent in the shape of a spiral by heat exchanger tube.
The heat exchange coil is provided with multiple groups heat exchanger tube, and heat exchanger tube described in every group is coiled into spiral helicine diameter and gradually increases Greatly, heat exchanger tube phase fitting described in multiple groups.
The input end of heat exchanger tube described in every group is connected to be connected with outlet end.
The heat exchange coil includes light pipe coil pipe and cooling fin coil pipe, and the light pipe coil pipe is bent in the shape of a spiral by heat exchanger tube At the heat exchange pipe external surface of the cooling fin coil pipe is provided with one layer of cooling fin, and cooling fin extends outwardly, and is arranged gelled The heat exchanger tube is bent in the shape of a spiral, forms the cooling fin coil pipe, and the light pipe coil pipe is connected with the cooling fin coil pipe.
The light pipe coil pipe light pipe coil pipe in parallel or described with the input end of the cooling fin coil pipe and the cooling fin disk The input end of pipe and outlet end series connection.
The light pipe coil pipe and the cooling fin coil pipe phase fitting, the light pipe coil pipe are located at outside, the cooling fin disk Pipe is located inside.
It further include ventilating duct, the ventilating duct is mounted on the sprinkle disk and top, and the assembling is in the wind-guiding At cylinder inside or port.
Cyclic annular sprinkle heat-exchanger rig application method, includes the following steps,
Heat-exchange working medium enters heat exchange coil, and the heat exchange coil around annular around flowing, start to work by circulation line, drives Liquid medium enters sprinkle disk in dynamic tray, and the liquid medium of sprinkle disk sprinkle downwardly gravitating, heat-exchange working medium is around ring The heat exchange coil of shape carries out heat with liquid medium around flowing and exchanges,
The liquid medium of sprinkle disk is entered tray by gravity, completes circulation.
Before heat-exchange working medium enters heat exchange coil step or simultaneously, cyclic annular sprinkle heat-exchanger rig receives working signal;
When receiving blower heat exchange working signal,
Heat-exchange working medium enters heat exchange coil, and the heat exchange coil around annular is around flowing, and blower starts, blower air blast, Make to form negative pressure inside heat exchange coil, air from heat exchange coil outside portion, inwardly flow by survey portion, and heat-exchange working medium and air carry out heat Amount exchange;
When receiving sprinkle heat exchange working signal,
Heat-exchange working medium enters heat exchange coil, and the heat exchange coil around annular around flowing, start to work by circulation line, drives Liquid medium enters sprinkle disk in dynamic tray, and the liquid medium of sprinkle disk sprinkle downwardly gravitating, heat-exchange working medium is around ring The heat exchange coil of shape carries out heat with liquid medium around flowing and exchanges,
The liquid medium of sprinkle disk is entered tray by gravity, completes circulation.
It should be understood that
Aforementioned " first, second, third ... " does not represent specific quantity and sequence, is only used for the area to title Point.
Fitting refer to solid that larger-size object shape is formed the lesser object parts of size are wrapped or It is fully wrapped around live.
Advantages of the present invention or principle are illustrated below:
1, cyclic annular sprinkle heat-exchanger rig is provided with heat exchange coil, sprinkle disk, tray, circulation line and rack, wherein changing Hot coil is ring structure under overlook direction, and the flow distance that heat-exchange working medium flows through heat exchange coil increases, additionally by sprinkle The setting of disk, tray and circulation line forms a set of sprinkle system,, can be with such as the sprinkle of water by the sprinkle of liquid medium The heat exchange efficiency of heat exchange coil is greatly speeded up, and liquid medium is recyclable use, therefore not will cause money when practical The waste in source, wherein sprinkle disk is mounted on the top of heat exchange coil, and tray is mounted on the lower part of heat exchange coil, the liquid of sprinkle disk Body medium is directly showered into heat exchange coil by gravity.
2, circulation line includes circulating line and the circulation pump housing, and structure is relatively easy, is either installing still cost On it is all advantageous.
3, heat exchange coil is ring structure under overlook direction, corresponding with the shape of blower, so blower is in air blast Can by the negative pressure of generation inside heat exchange coil when it is uniform, so air entered on the outside of heat exchange coil inside It is identical from all directions flow velocity, so heat exchange efficiency is also increased by.
4, circular through hole is opened up in the middle part of sprinkle disk, and the outer diameter of sprinkle disk is greater than or equal to the outer of the heat exchange coil Diameter, sprinkle disk internal diameter is less than or equal to the internal diameter of the heat exchange coil, so heat exchange plate is completely covered in the projection under overlook direction Pipe, liquid medium also cover heat exchange coil in sprinkle, it is possible to sufficiently heat exchange.The outer diameter of tray is greater than or equal to sprinkle The outer diameter of disk, it is possible to which the liquid medium that sprinkle gets off also can be directly within the scope of the recycling of tray.
5, assembling is not interfere with each other inside and above sprinkle disk internal diameter in two phases, while exchanging heat pipe progress Heat exchange.
6, heat exchange coil includes light pipe coil pipe, and bends to spiral helicine structure, and heat-exchange working medium can be contorted Track flowing then sufficiently heat exchange.
7, heat exchange coil is by multiple groups set of heat exchange tubes at the helical form diameter of every group of heat exchanger tube is gradually increased, and is then mutually covered Close, can compared in single group set of heat exchange tubes at heat exchange coil, multiple groups set of heat exchange tubes at heat exchange coil unit volume Heat exchange efficiency is higher.
8, the input end of every group of heat exchanger tube is mutually identical, outlet end also Xiang Xiangtong can pass through a root canal road and introduce heat exchange Working medium and a pipeline draw heat-exchange working medium, and it is excessive to avoid pipeline.
9, heat exchange coil includes light pipe coil pipe and cooling fin coil pipe, and two different heat exchange coils are adapted to different rings Border, when in summer in use, by sprinkle disk sprinkle liquid medium, light pipe coil pipe in conjunction with blower air blast, heat exchange efficiency and Higher, the heat exchange of cooling fin coil pipe does not need sprinkle liquid medium, is directly exchanged heat by blower air blast, is able to achieve preferable heat exchange Effect, in addition, working as in winter the winter in use, the especially north, since temperature is lower, so the case where liquid medium is water Under, sprinkle meeting frosting freezes, thus it is not applicable, so being unable to sprinkle, but pass through the heat exchange of cooling fin coil pipe, due to cooling fin The heat exchange area of coil pipe is larger, so good effect of heat exchange, therefore heat transfer effect is all guaranteed in refrigeration and heating.
10, there are two types of the connection types of light pipe coil pipe and cooling fin coil pipe, i.e., in parallel or series, when series connection, plays reinforcement and makees With, it can be implemented separately again when in parallel using function, by the difference of connection type, engagement blower and sprinkle system, realization Blower heat exchange, sprinkle heat exchange and the two engagement heat exchange, a variety of different use environments preferably.
11, during installation by light pipe coil pipe and cooling fin coil pipe phase fitting, and light pipe coil pipe is on the outside, and light pipe coil pipe is just In manufacture major diameter.
12, it is additionally provided with ventilating duct, is mounted on above sprinkle disk by ventilating duct, and assembling is in the inside of ventilating duct Or port, repetitive cycling is avoided convenient for the air just to have exchanged heat to be discharged to remotely by ventilating duct air draft.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the embodiment of the present invention;
Fig. 2 is the overlooking structure diagram of the embodiment of the present invention;
Fig. 3 be single group of embodiment of the present invention set of heat exchange tubes at heat exchange coil structural schematic diagram;
Fig. 4 be single group of embodiment of the present invention set of heat exchange tubes at heat exchange coil overlooking structure diagram;
Fig. 5 be multiple groups of embodiment of the present invention set of heat exchange tubes at heat exchange coil cutting structural schematic diagram;
Fig. 6 be multiple groups of embodiment of the present invention set of heat exchange tubes at heat exchange coil overlooking structure diagram;
Fig. 7 is the heat exchange coil cutting structural schematic diagram of multiple groups of embodiment of the present invention heat exchanger tube and cooling fin coil pipe composition;
Fig. 8 is the heat exchange coil overlooking structure diagram of multiple groups of embodiment of the present invention heat exchanger tube and cooling fin coil pipe composition;
Fig. 9 is the structural schematic diagram that heat exchanger tube of the embodiment of the present invention is connect with cooling fin.
Description of symbols:
10, heat exchange coil 10;11, light pipe coil pipe 11;12, cooling fin coil pipe 12;13, heat exchanger tube 13;14, cooling fin;15, First port 15;16, second port 16;20, sprinkle disk 20;21, through-hole 21;30, tray 30;40, the pump housing 40 is recycled;50, Circulating line 50;60, blower 60;70, ventilating duct 70.
Specific embodiment
The embodiment of the present invention is described in detail below.
As depicted in figs. 1 and 2, cyclic annular sprinkle heat-exchanger rig, including heat exchange coil 10, sprinkle disk 20, tray 30, circulation Pipeline and rack, the heat exchange coil 10, sprinkle disk 20 and tray 30 are installed in the rack, the heat exchange coil 10 It is ring structure under overlook direction, the heat exchange coil 10 has first port 15 and second port 16, the first port 15 Upward, downward, the sprinkle disk 20 is mounted on 15 top of first port to the second port 16, and the tray 30 is installed Below the second port 16, the sprinkle disk 20 and the tray 30 pass through the circulation line connection.The circulation Pipeline includes circulating line 50 and the circulation pump housing 40, and the tray 30, the circulation pump housing 40, sprinkle disk 20 pass through the circulation pipe Road 50 is connected, and further includes ventilating duct 70, the ventilating duct 70 is mounted on the sprinkle disk 20 and top, and the blower 60 is mounted on At 70 inside of ventilating duct or port.
Wherein, cyclic annular sprinkle heat-exchanger rig further includes blower 60, and the blower 60, the blower 60 is mounted on described 15 top of first port, the blower 60 are located on the straight line of central axis coincidence of the heat exchange coil 10, the sprinkle disk 20 middle parts offer circular through hole 21, and the sprinkle disk 20 forms cyclic structure, cricoid 20 outer diameter of sprinkle disk be greater than or Equal to the outer diameter of the heat exchange coil 10, cricoid 20 internal diameter of sprinkle disk is less than or equal to the interior of the heat exchange coil 10 Diameter, the outer diameter of the tray 30 are greater than or equal to the outer diameter of the sprinkle disk 20, and the blower 60 is mounted on the cyclic annular leaching Spill inside diameter or the top of disk 20.
As shown in Figures 3 to 6, the heat exchange coil 10 includes light pipe coil pipe 11, and the light pipe coil pipe 11 is by heat exchanger tube 13 It bends in the shape of a spiral, in the present embodiment, the heat exchange coil 10 is provided with multiple groups heat exchanger tube 13, heat exchanger tube 13 described in every group It is coiled into spiral helicine diameter to be gradually increased, 13 phase fitting of heat exchanger tube described in multiple groups, the input end phase of heat exchanger tube 13 described in every group Connection and outlet end are connected.
As shown in Figure 7 to 9, the heat exchange coil 10 includes light pipe coil pipe 11 and cooling fin coil pipe 12, the light pipe disk Pipe 11 is bent in the shape of a spiral by heat exchanger tube 13, and 13 outer surface of heat exchanger tube of the cooling fin coil pipe 12 is provided with one layer of cooling fin 14, cooling fin 14 extends outwardly, and the heat exchanger tube 13 for being provided with cooling fin 14 is bent in the shape of a spiral, forms the cooling fin disk Pipe 12, the light pipe coil pipe 11 are connected with the cooling fin coil pipe 12, the light pipe coil pipe 11 and the cooling fin coil pipe 12 Input end it is in parallel or the light pipe coil pipe 11 is connected with the input end of the cooling fin coil pipe 12 and outlet end.The light pipe Coil pipe 11 and the 12 phase fitting of cooling fin coil pipe, the light pipe coil pipe 11 are located at outside, and the cooling fin coil pipe 12 is located at interior Side.
Cyclic annular sprinkle heat-exchanger rig application method, includes the following steps,
Heat-exchange working medium enters heat exchange coil 10, and for the heat exchange coil 10 around annular around flowing, circulation line starts work Make, liquid medium in tray 30 is driven to enter sprinkle disk 20, the liquid medium of sprinkle disk 20 sprinkle downwardly gravitating, heat exchange Working medium carries out heat with liquid medium around flowing around the heat exchange coil 10 of annular and exchanges
The liquid medium of sprinkle disk 20 is entered tray 30 by gravity, completes circulation.
Cyclic annular sprinkle heat-exchanger rig application method, when work, there are three types of operating modes;
Before heat-exchange working medium enters heat exchange coil step or simultaneously, cyclic annular sprinkle heat-exchanger rig receives working signal;
Operating mode one,
When receive blower heat exchange working signal,
Heat-exchange working medium enters heat exchange coil 10, and the heat exchange coil 10 around annular is around flowing, and blower 60 starts, blower 60 air blast make to form negative pressure inside heat exchange coil 10, air from 10 outside portion of heat exchange coil inwardly survey portion flow, heat-exchange working medium with Air carries out heat exchange;
Operating mode two,
When receive sprinkle heat exchange working signal,
Heat-exchange working medium enters heat exchange coil 10, and for the heat exchange coil 10 around annular around flowing, circulation line starts work Make, liquid medium in tray 30 is driven to enter sprinkle disk 20, the liquid medium of sprinkle disk 20 sprinkle downwardly gravitating, heat exchange Working medium carries out heat with liquid medium around flowing around the heat exchange coil 10 of annular and exchanges, and the liquid medium of sprinkle disk 20 is by weight Power enters tray 30, completes circulation;
Operating mode three,
Heat exchange working signal is assisted when receiving,
Above-mentioned operating mode one and operating mode two work simultaneously.
Advantages of the present invention and principle:
1, cyclic annular sprinkle heat-exchanger rig is provided with heat exchange coil 10, sprinkle disk 20, tray 30, circulation line and rack, Wherein heat exchange coil 10 is ring structure under overlook direction, and the flow distance that heat-exchange working medium flows through heat exchange coil 10 increases, separately The outer setting for passing through sprinkle disk 20, tray 30 and circulation line, forms a set of sprinkle system, by the sprinkle of liquid medium, Such as the sprinkle of water, the heat exchange efficiency of heat exchange coil 10 can be greatly speeded up, and liquid medium is recyclable use, therefore The waste of resource is not will cause when practical, wherein sprinkle disk 20 is mounted on the top of heat exchange coil 10, and tray 30, which is mounted on, to be changed The liquid medium of the lower part of hot coil 10, sprinkle disk 20 is directly showered into heat exchange coil 10 by gravity.
2, circulation line includes circulating line 50 and the circulation pump housing 40, and structure is relatively easy, is either installing still It is all advantageous in cost.
3, heat exchange coil 10 is ring structure under overlook direction, corresponding with the shape of blower 60, so blower 60 exists Can be uniform at 10 inside of heat exchange coil by the negative pressure of generation when air blast, thus air from the outside of heat exchange coil 10 into The slave all directions flow velocity entered to inside is identical, so heat exchange efficiency is also increased by.
4, circular through hole 21 is opened up in the middle part of sprinkle disk 20, and the outer diameter of sprinkle disk 20 is greater than or equal to the heat exchange coil 10 outer diameter, 20 internal diameter of sprinkle disk is less than or equal to the internal diameter of the heat exchange coil 10, so the projection under overlook direction is complete Heat exchange coil 10 is covered, liquid medium also covers heat exchange coil 10 in sprinkle, it is possible to sufficiently heat exchange.Outside tray 30 Diameter is greater than or equal to the outer diameter of sprinkle disk 20, it is possible to which the liquid medium that sprinkle gets off also can be directly in tray 30 It recycles in range.
5, blower 60 is mounted on inside and above 20 internal diameter of sprinkle disk, is not interfere with each other in two phases, while exchanging heat pipe 13 exchange heat.
6, heat exchange coil 10 includes light pipe coil pipe 11, and bends to spiral helicine structure, and heat-exchange working medium can rotate The track flowing of shape then sufficiently heat exchange.
7, heat exchange coil 10 is made of multiple groups heat exchanger tube 13, and the helical form diameter of every group of heat exchanger tube 13 is gradually increased, then Mutual fitting, the heat exchange plate that can be formed compared with the heat exchange coil 10 formed in single group heat exchanger tube 13, multiple groups heat exchanger tube 13 The heat exchange efficiency of 10 unit volume of pipe is higher.
8, the input end of every group of heat exchanger tube 13 is mutually identical, outlet end also Xiang Xiangtong can be introduced by a root canal road and be changed Hot working fluid and a pipeline draw heat-exchange working medium, and it is excessive to avoid pipeline.
9, heat exchange coil 10 includes light pipe coil pipe 11 and cooling fin coil pipe 12, and two different heat exchange coils 10 are adapted to Different environment, when, in use, passing through 20 sprinkle liquid medium of sprinkle disk, light pipe coil pipe 11 is in conjunction with the drum of blower 60 in summer Wind, heat exchange efficiency and higher, the heat exchange of cooling fin coil pipe 12 does not need sprinkle liquid medium, is directly changed by 60 air blast of blower Heat is able to achieve preferable heat transfer effect, in addition, working as in winter the winter in use, the especially north, since temperature is lower, institute In the case where using liquid medium as water, sprinkle meeting frosting freezes, thus it is not applicable, so being unable to sprinkle, but pass through cooling fin The heat exchange of coil pipe 12, since the heat exchange area of cooling fin coil pipe 12 is larger, so good effect of heat exchange, therefore in refrigeration and heating Heat transfer effect is all guaranteed.
10, there are two types of the connection types of light pipe coil pipe 11 and cooling fin coil pipe 12, i.e., in parallel or series, when series connection play plus Use is pretended, can be implemented separately again when in parallel using function, by the difference of connection type, engage blower 60 and sprinkle system System realizes that blower 60 exchanges heat, sprinkle heat exchange and the two engagement heat exchange, a variety of different use environments preferably.
11, during installation by 12 phase fitting of light pipe coil pipe 11 and cooling fin coil pipe, and light pipe coil pipe 11 is on the outside, light pipe Coil pipe 11 is convenient for manufacture major diameter.
12, it is additionally provided with ventilating duct 70,20 top of sprinkle disk is mounted on by ventilating duct 70, and blower 60 is mounted on wind-guiding The inside or port of cylinder 70, avoid repetitive cycling by 70 air draft of ventilating duct convenient for the air just to have exchanged heat to be discharged to remotely.
The above is only specific embodiments of the present invention, are not limited the scope of protection of the present invention with this;Do not violating this hair Made any replacement and improvement, category protection scope of the present invention on the basis of bright design.

Claims (10)

1. cyclic annular sprinkle heat-exchanger rig, which is characterized in that including heat exchange coil, sprinkle disk, tray, circulation line and rack, The heat exchange coil, sprinkle disk and tray are installed in the rack, are ring junction under the heat exchange coil overlook direction Structure, the heat exchange coil have first port and second port, and upward, the second port is downward, described for the first port Sprinkle disk is mounted on above the first port, and the tray is mounted below the second port, the sprinkle disk and institute It states tray and passes through the circulation line connection.
2. ring-type sprinkle heat-exchanger rig as described in claim 1, which is characterized in that the circulation line includes circulating line and follows The ring pump housing, the tray, the circulation pump housing, sprinkle disk are connected by the circulating line.
3. ring-type sprinkle heat-exchanger rig as described in claim 1, which is characterized in that it further include blower, the blower, the blower It is mounted on above the first port, on the straight line that the central axis that the blower is located at the heat exchange coil is overlapped.
4. ring-type sprinkle heat-exchanger rig as claimed in claim 3, which is characterized in that offered in the middle part of the sprinkle disk round logical Hole, circlewise structure, the cricoid sprinkle dish external diameter are greater than or equal to the outer diameter of the heat exchange coil, ring to the sprinkle dish type The sprinkle disk internal diameter of shape is less than or equal to the internal diameter of the heat exchange coil, and the outer diameter of the tray is greater than or equal to described The outer diameter of sprinkle disk.
5. ring-type sprinkle heat-exchanger rig as claimed in claim 4, which is characterized in that the assembling is in the cyclic annular sprinkle disk Inside diameter or top.
6. the cyclic annular sprinkle heat-exchanger rig as described in any one of claim 1 to 5, which is characterized in that the heat exchange coil includes light Pipe dish pipe and cooling fin coil pipe, the light pipe coil pipe are bent in the shape of a spiral by heat exchanger tube, the heat exchanger tube of the cooling fin coil pipe Outer surface is provided with one layer of cooling fin, and cooling fin extends outwardly, and the gelled heat exchanger tube is arranged and is bent in the shape of a spiral, shape At the cooling fin coil pipe, the light pipe coil pipe is connected with the cooling fin coil pipe.
7. ring-type sprinkle heat-exchanger rig as claimed in claim 6, which is characterized in that the light pipe coil pipe and the cooling fin coil pipe Input end it is in parallel or the light pipe coil pipe is connected with the input end of the cooling fin coil pipe and outlet end.
8. ring-type sprinkle heat-exchanger rig as claimed in claim 6, which is characterized in that the light pipe coil pipe and the cooling fin coil pipe Phase fitting, the light pipe coil pipe are located at outside, and the cooling fin coil pipe is located inside.
9. cyclic annular sprinkle heat-exchanger rig application method, which is characterized in that include the following steps,
Heat-exchange working medium enters heat exchange coil, and the heat exchange coil around annular is around flowing, and circulation line is started to work, and driving is held It connects liquid medium in disk and enters sprinkle disk, the liquid medium of sprinkle disk sprinkle downwardly gravitating, heat-exchange working medium is around annular Heat exchange coil carries out heat with liquid medium around flowing and exchanges,
The liquid medium of sprinkle disk is entered tray by gravity, completes circulation.
10. ring-type sprinkle heat-exchanger rig application method as claimed in claim 9, which is characterized in that
Before heat-exchange working medium enters heat exchange coil step or simultaneously, cyclic annular sprinkle heat-exchanger rig receives working signal;
When receiving blower heat exchange working signal,
Heat-exchange working medium enters heat exchange coil, and the heat exchange coil around annular is around flowing, and blower starts, and blower air blast makes to change Negative pressure is formed inside hot coil, air from heat exchange coil outside portion inwardly flow by survey portion, and heat-exchange working medium and air carry out heat friendship It changes;
When receiving sprinkle heat exchange working signal,
Heat-exchange working medium enters heat exchange coil, and the heat exchange coil around annular is around flowing, and circulation line is started to work, and driving is held It connects liquid medium in disk and enters sprinkle disk, the liquid medium of sprinkle disk sprinkle downwardly gravitating, heat-exchange working medium is around annular Heat exchange coil carries out heat with liquid medium around flowing and exchanges,
The liquid medium of sprinkle disk is entered tray by gravity, completes circulation.
CN201910216750.5A 2019-03-20 2019-03-20 Cyclic annular sprinkle heat-exchanger rig and its application method Pending CN109813148A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910216750.5A CN109813148A (en) 2019-03-20 2019-03-20 Cyclic annular sprinkle heat-exchanger rig and its application method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910216750.5A CN109813148A (en) 2019-03-20 2019-03-20 Cyclic annular sprinkle heat-exchanger rig and its application method

Publications (1)

Publication Number Publication Date
CN109813148A true CN109813148A (en) 2019-05-28

Family

ID=66609810

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910216750.5A Pending CN109813148A (en) 2019-03-20 2019-03-20 Cyclic annular sprinkle heat-exchanger rig and its application method

Country Status (1)

Country Link
CN (1) CN109813148A (en)

Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6766655B1 (en) * 2003-10-16 2004-07-27 Ho Hsin Wu Evaporative condenser without cooling fins
CN2630754Y (en) * 2003-06-09 2004-08-04 广州市华德工业有限公司 Splash-proof evaporation condenser
CN201096431Y (en) * 2007-09-14 2008-08-06 周水良 Evaporation type condenser
CN202328151U (en) * 2011-11-30 2012-07-11 神华集团有限责任公司 Discharged steam recovery device
CN202329268U (en) * 2011-12-01 2012-07-11 上海宝丰机械制造有限公司 Countercurrent evaporation type condenser with fins
CN202734612U (en) * 2012-06-18 2013-02-13 扬州巨人机械有限公司 Evaporative condenser with high heat exchange efficiency
CN203964383U (en) * 2014-06-05 2014-11-26 广东纽恩泰新能源科技发展有限公司 A kind of coiled condensing heat exchanger
CN104197747A (en) * 2014-09-11 2014-12-10 诸文伟 Glass steel closed cooling tower
CN204494922U (en) * 2015-03-24 2015-07-22 浙江国祥空调股份有限公司 A kind of evaporative condenser flooded screw handpiece Water Chilling Units
CN205049011U (en) * 2015-10-21 2016-02-24 安徽理工大学 High efficiency spray -type heat exchanger
CN205262243U (en) * 2015-11-17 2016-05-25 武汉光谷节能技术有限公司 Overflow cooling tower
CN206724739U (en) * 2017-01-23 2017-12-08 赤峰和然节能设备有限责任公司 The high-efficiency heat exchange coil of absorption heat exchange device
CN206847129U (en) * 2017-04-24 2018-01-05 北京和海益制冷科技股份有限公司 A kind of integrated high-efficient inner cross pipe energy-saving evaporative condenser
CN207950758U (en) * 2018-01-10 2018-10-12 浙江山鹰纸业有限公司 A kind of inner-spiral type vacuum gun barrel
CN208049423U (en) * 2018-01-05 2018-11-06 新疆现代特油科技股份有限公司 Detachable reflux in tower spray thrower
CN208520229U (en) * 2018-06-30 2019-02-19 石家庄市普力制药有限公司 A kind of environment-friendly highly efficient cooling tower
CN109489282A (en) * 2018-11-09 2019-03-19 青岛海尔空调电子有限公司 Evaporative condenser water cooler
CN209763806U (en) * 2019-03-20 2019-12-10 苏宇贵 annular shower heat exchange device

Patent Citations (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN2630754Y (en) * 2003-06-09 2004-08-04 广州市华德工业有限公司 Splash-proof evaporation condenser
US6766655B1 (en) * 2003-10-16 2004-07-27 Ho Hsin Wu Evaporative condenser without cooling fins
CN201096431Y (en) * 2007-09-14 2008-08-06 周水良 Evaporation type condenser
CN202328151U (en) * 2011-11-30 2012-07-11 神华集团有限责任公司 Discharged steam recovery device
CN202329268U (en) * 2011-12-01 2012-07-11 上海宝丰机械制造有限公司 Countercurrent evaporation type condenser with fins
CN202734612U (en) * 2012-06-18 2013-02-13 扬州巨人机械有限公司 Evaporative condenser with high heat exchange efficiency
CN203964383U (en) * 2014-06-05 2014-11-26 广东纽恩泰新能源科技发展有限公司 A kind of coiled condensing heat exchanger
CN104197747A (en) * 2014-09-11 2014-12-10 诸文伟 Glass steel closed cooling tower
CN204494922U (en) * 2015-03-24 2015-07-22 浙江国祥空调股份有限公司 A kind of evaporative condenser flooded screw handpiece Water Chilling Units
CN205049011U (en) * 2015-10-21 2016-02-24 安徽理工大学 High efficiency spray -type heat exchanger
CN205262243U (en) * 2015-11-17 2016-05-25 武汉光谷节能技术有限公司 Overflow cooling tower
CN206724739U (en) * 2017-01-23 2017-12-08 赤峰和然节能设备有限责任公司 The high-efficiency heat exchange coil of absorption heat exchange device
CN206847129U (en) * 2017-04-24 2018-01-05 北京和海益制冷科技股份有限公司 A kind of integrated high-efficient inner cross pipe energy-saving evaporative condenser
CN208049423U (en) * 2018-01-05 2018-11-06 新疆现代特油科技股份有限公司 Detachable reflux in tower spray thrower
CN207950758U (en) * 2018-01-10 2018-10-12 浙江山鹰纸业有限公司 A kind of inner-spiral type vacuum gun barrel
CN208520229U (en) * 2018-06-30 2019-02-19 石家庄市普力制药有限公司 A kind of environment-friendly highly efficient cooling tower
CN109489282A (en) * 2018-11-09 2019-03-19 青岛海尔空调电子有限公司 Evaporative condenser water cooler
CN209763806U (en) * 2019-03-20 2019-12-10 苏宇贵 annular shower heat exchange device

Similar Documents

Publication Publication Date Title
CN205717928U (en) Heat exchanger and phase-change heat-storage water heater
CN102563872B (en) Water tank, heat pump water heater comprising water tank and control method of heat pump water heater
CN103925729A (en) Air-conditioning system and central air-conditioner with same
CN109813148A (en) Cyclic annular sprinkle heat-exchanger rig and its application method
CN205642097U (en) Dual -purpose jacket tubular heat exchanger
CN207990904U (en) A kind of reverse-flow fresh air heat exchanger Total heat exchange core
CN209926583U (en) Single-container double-circulation basic module
CN209763806U (en) annular shower heat exchange device
CN201246829Y (en) Heat pump air conditioner system using immersed type corrugated pipe sewage water heat exchanger
CN206362019U (en) A kind of double-source heat pump unit and the heating system with the source pump
CN205939579U (en) Outer quick -witted waste heat recovery unit of air conditioner
CN212030301U (en) Heat exchange system
CN203719239U (en) Condensation heat recovery system of refrigerating unit
CN202382339U (en) Heat exchange system for outdoor air and underground constant-temperature layer
CN207797796U (en) Heat exchanger tube and buried radiator
CN111006297A (en) Civil solar heating system
CN207456219U (en) Cooling column and its anti-freezing structure, cooling triangle
CN102226536B (en) Coal briquette air stove
CN202101288U (en) Moulded coal hot air furnace
CN206648350U (en) A kind of easily changeable geothermal heat pump
CN204438510U (en) A kind of Teat pump boiler of water circulation working medium
CN201387251Y (en) Evaporator
CN205940215U (en) Capillary vortex heat exchanger with guiding device
CN211575229U (en) Civil solar heating system
CN105841522A (en) Molten salt heat exchanger for intelligently controlling heat exchange flowing speed

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination