CN218884327U - Evaporative type condensation coil and evaporative type condenser - Google Patents

Evaporative type condensation coil and evaporative type condenser Download PDF

Info

Publication number
CN218884327U
CN218884327U CN202222865606.4U CN202222865606U CN218884327U CN 218884327 U CN218884327 U CN 218884327U CN 202222865606 U CN202222865606 U CN 202222865606U CN 218884327 U CN218884327 U CN 218884327U
Authority
CN
China
Prior art keywords
stay tube
tube
supporting pipe
support tube
pipe
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
CN202222865606.4U
Other languages
Chinese (zh)
Inventor
杨洋
郑兴庆
孙清华
桂林松
顾海华
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.)
Schlee Nanjing Refrigeration Machinery Manufacturing Co ltd
Original Assignee
Schlee Nanjing Refrigeration Machinery Manufacturing 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 Schlee Nanjing Refrigeration Machinery Manufacturing Co ltd filed Critical Schlee Nanjing Refrigeration Machinery Manufacturing Co ltd
Priority to CN202222865606.4U priority Critical patent/CN218884327U/en
Application granted granted Critical
Publication of CN218884327U publication Critical patent/CN218884327U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

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

Abstract

The utility model discloses an evaporative condenser coil and evaporative condenser, evaporative condenser coil is including the first stay tube of connecting the refrigerant entry, third stay tube, second stay tube and a plurality of stroke pipeline of connecting the refrigerant export, the third stay tube coaxial arrangement in the below of first stay tube, the second stay tube with first stay tube and third stay tube are parallelly arranged, a plurality of stroke pipeline parallel connection are between first stay tube and second stay tube and between third stay tube and the second stay tube. The utility model discloses a three spinal branch stay tubes for the refrigerant that has liquefied can be earlier from the export outflow, and gas-liquid mixture's refrigerant is by spray cooling once more, improves the heat transfer effect.

Description

Evaporative type condensation coil and evaporative type condenser
Technical Field
The utility model relates to a condenser, concretely relates to evaporation formula condenser coil and evaporation formula condenser.
Background
The condenser is one of main heat exchange devices in various industries such as food, chemical industry, pharmacy and the like, and has wide application. The evaporation type air conditioning technology is energy-saving, environment-friendly and sustainable in development, and effectively solves the problems of high initial investment, high running energy consumption and the like of the traditional mechanical refrigeration. The evaporative condenser is one of condensers, and is a high-power condensing device which takes away heat of a refrigerant by using forced air convection circulation and moisture evaporation. There is now an increasing number of people working on the use of evaporative condensers. The principle of the evaporative condenser is that circulating cooling water with small flow rate is evaporated on the outer surface of a condensing coil, and refrigerant gas is condensed into liquid in the condensing coil. At present, a commonly used condensing coil is formed by bending an internal tooth copper pipe, as shown in fig. 1 and fig. 2, a longer copper pipe is bent back and forth to form a snake-shaped loop, the number of middle welding spots is small, but the copper pipe still has the defects that the wall thickness of the copper pipe is not smaller than 1.2mm due to strength and erosion abrasion, so that the manufactured coil is large in size and needs a larger space. In addition, the refrigerant is not necessarily completely liquefied after being sprayed by the spraying device, and a gas-liquid mixed state exists, so that the heat exchange effect is poor. In most cases, the evaporation system needs to be equipped with a gas-liquid separator, which increases the equipment cost.
SUMMERY OF THE UTILITY MODEL
Utility model purpose: the utility model relates to an overcome not enough among the prior art, provide a novel evaporation formula condensation coil and evaporative condenser, improve refrigerant performance, make the heat transfer more even, improve the heat transfer effect, and the processing degree of difficulty is low.
The technical scheme is as follows: an evaporative condenser coil, include: the first supporting pipe, the third supporting pipe, the second supporting pipe and a plurality of stroke pipelines of connecting the refrigerant export of connection refrigerant entry, the third supporting pipe coaxial arrange in the below of first supporting pipe, the second supporting pipe with first supporting pipe and third supporting pipe parallel arrangement, a plurality of stroke pipeline parallel connection are between first supporting pipe and second supporting pipe and between third supporting pipe and second supporting pipe.
As a preferred structure of the utility model, the second stay tube includes first pipeline and second pipeline, the stroke pipeline includes first stroke pipeline and second stroke pipeline, communicate through a plurality of first stroke pipelines between first pipeline and the first stay tube, communicate through a plurality of second stroke pipelines between second pipeline and the third stay tube.
As an optimized structure of the utility model, the cross section of the first supporting tube, the second supporting tube and the third supporting tube is square.
As an optimized structure of the utility model, the cross section of the stroke pipeline is circular.
As an optimized structure of the utility model, the first supporting tube, the second supporting tube, the third supporting tube and the stroke pipeline are stainless steel tubes.
As an optimized structure of the present invention, the length of the first supporting tube is greater than the length of the third supporting tube.
The evaporative condenser comprises the evaporative condensing coil pipe of any one of the above items.
Has the advantages that: (1) The utility model discloses a three stay tubes for the refrigerant that has liquefied can follow the export earlier and flow, and the refrigerant of gas-liquid mixture is spray cooling once more, improves the heat transfer effect. (2) Adopt nonrust steel pipe structure pipeline, compare in copper pipe corrosion resistance stronger, intensity is also bigger, can reduce the pipeline and change the number of times to reduce the maintenance cost.
Drawings
FIG. 1 is an elevation view of a typical condenser coil tube;
FIG. 2 is a side view of a typical condenser coil tube;
FIG. 3 is a front view of the condenser coil pipe of the present invention;
fig. 4 is a side view of one side of the second support tube of the condenser coil of the present invention;
fig. 5 is a side view of one side of the first support tube and the third support tube of the condenser coil according to the present invention.
Detailed Description
The technical solution of the present invention is further explained with reference to the accompanying drawings.
The embodiment is as follows: as shown in fig. 3, the evaporative condenser coil according to the present invention comprises a first support tube 10 connected to a refrigerant inlet, a third support tube 30 connected to a refrigerant outlet, a second support tube 20 and a plurality of stroke pipelines 40, wherein the third support tube 30 is coaxially disposed below the first support tube 10, the second support tube 20 is disposed in parallel with the first support tube 10 and the third support tube 30, and the plurality of stroke pipelines 40 are connected in parallel between the first support tube 10 and the second support tube 20 and between the third support tube 30 and the second support tube 20.
The second support pipe 20 includes a first pipe 21 and a second pipe 22, the stroke pipe 40 includes a first stroke pipe 41 and a second stroke pipe 42, the first pipe 21 is communicated with the first support pipe 10 through a plurality of first stroke pipes 41, and the second pipe 22 is communicated with the third support pipe 30 through a plurality of second stroke pipes 42. Illustratively, one port of each first stroke conduit 41 is welded to the first conduit 21, and the other port is welded to the first support tube 10, forming a communicating passage; similarly, one port of each second travel tube 42 is welded to the second tube 22 and the other port is welded to the third support tube 30 to provide a passageway for communication.
Referring to fig. 4 and 5, the first support tube 10, the second support tube 20, and the third support tube 30 have a square cross section, and thus have a strong supporting function. The cross section of the stroke pipeline 40 (including the first stroke pipeline 41 and the second stroke pipeline 42) is circular, so that the manufacturing is convenient, meanwhile, the large contact area with the spray cooling water can be ensured, and the cooling effect is improved. The length of the first support tube 10 is greater than that of the third support tube 30, and the refrigerant gas can be sufficiently heat-exchanged in the plurality of first stroke lines 41.
Gaseous refrigerant enters the first supporting pipe 10 through the inlet, then flows into the stainless steel pipe communicated with the first supporting pipe 10, is liquid through the evaporation cooling of the spraying system, flows into the second supporting pipe 20 welded at the other side, but in the process, the completely liquefied state can not be achieved, a gas-liquid mixed state exists, under the action of gravity, the completely liquefied refrigerant in the second supporting pipe 20 flows into the bottommost end of the pipeline firstly, then flows into the third supporting pipe 30 through the lower second stroke pipeline 42, flows out through the outlet, and the original gas-liquid mixed liquid flows into the first supporting pipe 10 through the plurality of first stroke pipelines 41 in the second supporting pipe 20, and is sprayed and cooled again in the advancing process. Thus, the heat exchange is more uniform, the utilization rate of the refrigerant is greatly improved, and the heat exchange effect can be improved.
The first support tube 10, the second support tube 20, the third support tube 30 and the stroke pipeline 40 are stainless steel tubes. The stainless steel pipe has stronger corrosion resistance and higher strength compared with a copper pipe, and can reduce the replacement times of pipelines, thereby reducing the maintenance cost.
In a further embodiment, the evaporative condenser coil of the present invention is used in an evaporative condenser. Evaporative condenser includes evaporative condensing coil, is equipped with cooling water spray set and fan in evaporative condensing coil's top, the refrigerant gets into condensing coil from the intake pipe, along pipeline flow direction liquid outlet, cooling water sprays on condensing coil surface, the fan makes the air convection, realizes the refrigeration through the evaporation.

Claims (7)

1. An evaporative condensing coil, comprising: the refrigerant inlet connecting structure comprises a first supporting pipe (10), a third supporting pipe (30), a second supporting pipe (20) and a plurality of stroke pipelines (40), wherein the first supporting pipe (10) is connected with a refrigerant inlet, the third supporting pipe (30) is coaxially arranged below the first supporting pipe (10), the second supporting pipe (20) is arranged in parallel with the first supporting pipe (10) and the third supporting pipe (30), and the stroke pipelines (40) are connected in parallel between the first supporting pipe (10) and the second supporting pipe (20) and between the third supporting pipe (30) and the second supporting pipe (20).
2. Evaporative condensing coil according to claim 1, characterized in that the second support tube (20) comprises a first (21) and a second (22) tube, the travel tube (40) comprising a first (41) and a second (42) tube, the first tube (21) communicating with the first support tube (10) through a number of first travel tubes (41) and the second tube (22) communicating with the third support tube (30) through a number of second travel tubes (42).
3. Evaporative condensing coil according to claim 1, characterised by the fact that the first (10), second (20) and third (30) support tubes are square in section.
4. Evaporative condensing coil according to claim 3, characterised by the fact that the travel tubes (40) are circular in section.
5. The evaporative condensing coil according to claim 1, wherein the first support tube (10), the second support tube (20), the third support tube (30) and the travel line (40) are stainless steel tubes.
6. Evaporative condensing coil according to claim 1, characterised in that the length of the first support tube (10) is greater than the length of the third support tube (30).
7. An evaporative condenser comprising an evaporative condenser coil as claimed in any one of claims 1 to 6.
CN202222865606.4U 2022-10-28 2022-10-28 Evaporative type condensation coil and evaporative type condenser Active CN218884327U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202222865606.4U CN218884327U (en) 2022-10-28 2022-10-28 Evaporative type condensation coil and evaporative type condenser

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202222865606.4U CN218884327U (en) 2022-10-28 2022-10-28 Evaporative type condensation coil and evaporative type condenser

Publications (1)

Publication Number Publication Date
CN218884327U true CN218884327U (en) 2023-04-18

Family

ID=85954411

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202222865606.4U Active CN218884327U (en) 2022-10-28 2022-10-28 Evaporative type condensation coil and evaporative type condenser

Country Status (1)

Country Link
CN (1) CN218884327U (en)

Similar Documents

Publication Publication Date Title
CN101886836B (en) Machine room heat removal device for evaporation cooling type heat-pipe heat exchange
CN102445100A (en) Heat exchange tube unit, finned tube air-cooled condenser and cooling air evaporator
CN108709341A (en) A kind of pre- cold mould spray evaporation type condenser
CN214581930U (en) Copper pipeline structure for micro-fine tube heat exchanger and heat exchanger using same
CN218884327U (en) Evaporative type condensation coil and evaporative type condenser
CN211953332U (en) Energy-saving and water-saving efficient evaporative condenser
CN1648589A (en) Spring tube evaporation type cold exchange device
CN2869739Y (en) Mixed-tube-bundle vaporating type cold exchanging apparatus
CN204717949U (en) The straight swollen air-conditioner set of a kind of tape channel evaporative condenser
CN203249442U (en) Novel sleeve evaporative condenser
CN214581941U (en) Intelligent energy-saving air conditioner double-condenser device
CN210832621U (en) Dual-control air conditioning system comprising V-shaped vertical pipe evaporative cooling tower
CN104596005A (en) Water-saving pipe-wrapped-by-filler type evaporative cooling air-conditioning system
CN2084186U (en) Vapouring type condensing cooler
CN204923933U (en) Evaporative condenser
CN201867086U (en) Gas-liquid separation type air cooled condenser
CN202304124U (en) Novel efficient flooded evaporator
CN218915472U (en) Pipeline evaporation type condensing coil and evaporation type condenser
CN219841673U (en) Coil pipe for evaporative condenser
CN110986433A (en) Open type spiral winding type efficient cooling system
CN220648484U (en) Effectual air conditioner of cooling
CN215113342U (en) Evaporator for making water from air
CN218764726U (en) Evaporative condensing coil and sleeve type condensing heat exchanger
CN221197586U (en) Evaporation type high-ambient-temperature ultra-efficient energy-saving refrigerator
CN221036237U (en) Refrigerating system for guaranteeing saturated gas of return air header based on liquid supply pipeline

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant