CN202057109U - Parallel-flow air conditioning - Google Patents

Parallel-flow air conditioning Download PDF

Info

Publication number
CN202057109U
CN202057109U CN2011201044634U CN201120104463U CN202057109U CN 202057109 U CN202057109 U CN 202057109U CN 2011201044634 U CN2011201044634 U CN 2011201044634U CN 201120104463 U CN201120104463 U CN 201120104463U CN 202057109 U CN202057109 U CN 202057109U
Authority
CN
China
Prior art keywords
collector tube
tube
heat exchanger
air conditioner
flat heat
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN2011201044634U
Other languages
Chinese (zh)
Inventor
冯利峰
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.)
Guangdong Mechanical and Electrical College
Original Assignee
Guangdong Mechanical and Electrical College
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 Guangdong Mechanical and Electrical College filed Critical Guangdong Mechanical and Electrical College
Priority to CN2011201044634U priority Critical patent/CN202057109U/en
Application granted granted Critical
Publication of CN202057109U publication Critical patent/CN202057109U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Abstract

The utility model discloses a parallel-flow air conditioning, which comprises a compressor, a compressor air return pipe, a four-way valve, an indoor unit, a capillary component, an upper liquid collection pipe, a flat heat exchange tube and a lower liquid collection pipe. An air-liquid separator is arranged at a first end of the lower liquid collection pipe and connected with a one-way valve, and the one-way valve and the first end of the upper liquid collection pipe are connected in parallel with a same connector of the four-way valve. The parallel-flow air conditioning enables the parallel flow technique to achieve refrigerating and heating, and the problems of uneven flow distribution, low heat exchange efficiency, large size, high cost and the like are solved.

Description

A kind of concurrent flow air conditioner
Technical field
The utility model belongs to the air-conditioner technical field, is specifically related to a kind of air conditioner that uses parallel-flow heat exchanger, is used for domestic air conditioner, commercial air conditioner or other refrigeration plants.
Background technology
Parallel-flow heat exchanger is also referred to as micro-channel heat exchanger, has heat transfer efficiency height, compact conformation, low, in light weight, the low cost and other advantages of noise.Be taken as condenser and be widely used in air conditioning for automobiles, in recent years, also be used as the condenser of family expenses, especially commercial use air conditioner.
Parallel-flow heat exchanger adopts flat tube augmentation of heat transfer technology, is a kind of porous aluminum flat pipe heat exchanger, and its structure is to adopt louvered fin in air side, and refrigerant side adopts the multi-channel flat pipe of minor diameter, thereby the heat exchange of air side and refrigerant side is strengthened.Use in family expenses air-conditioner field, help improving efficiency, reduce refrigerant charge and alleviate unit weight, reduce the air-conditioner cost, compare with common copper pipe heat exchanger, make domestic air conditioner obtain bigger improvement at aspects such as performance, volume, weight, costs.
Because in refrigerated air-conditioning system, the cold-producing medium that enters evaporimeter is a gas-fluid two-phase mixture, be divided into multichannel usually and enter and absorb heat in the evaporimeter, liquid phase is evaporated to gas to realize the purpose of refrigeration.Can cold-producing medium two-phase fluid, particularly liquid wherein be assigned to uniformly and carry out heat exchange in each paths, are the keys of evaporator designs.Under the service condition of actual complex, if each flat heat exchanger tube separatory is uneven in the evaporimeter, can cause different tube refrigerant mass flow discrepancies even, the less very fast evaporation of flow in the pipe, the degree of superheat of pipeline outlet is higher; The too much evaporation of flow does not finish in the pipe, and it is little to cause exporting the degree of superheat, even contains liquid; Make all under two kinds of situations that flat heat exchanger tube heat exchange area is not in full use.In addition, the volume that accounts for owing to the gaseous refrigerant that enters flat heat exchanger tube is bigger, has occupied most space and heat exchange area, has had a strong impact on heat exchange efficiency, makes evaporimeter have to volume is done greatly, and cost improves.
In view of the foregoing, at present in the family expenses commercial use air conditioner, parallel-flow heat exchanger is only made condenser and is used on single-cooling air-conditioner, has limited it at the application development of commercial, domestic air conditioner with popularize.
The utility model content
The utility model provides a kind of concurrent flow air conditioner in order to overcome the deficiency that above prior art exists, and makes the concurrent flow technology can realize freezing and heating, and solves shunting inequality, problems such as heat exchange efficiency is low, volume is big, cost height.
The purpose of this utility model realizes by following technical scheme: a kind of concurrent flow air conditioner, it is characterized in that: comprise compressor, the compressor return air pipe, cross valve, indoor set, capillary module, last collector tube upper pipes, last collector tube, flat heat exchanger tube and following collector tube, collector tube on described in the depression angle, following collector tube is " L " shape of circular arc bending, compressor, the compressor return air pipe connects two connectors of cross valve respectively, indoor set, last collector tube first end connects two other connector of cross valve respectively, indoor set connects by capillary module goes up the collector tube upper pipes, last collector tube upper pipes connects upward collector tube second end, last collector tube inside is provided with at least one dividing plate, the flat heat exchanger tube by a plurality of parallel arrangements is communicated with between the collector tube up and down, each flat heat exchanger tube has fin, following collector tube first end is provided with gas-liquid separator, gas-liquid separator connects check valve, the be connected in parallel same connector of cross valve of check valve and last collector tube first end.
According to different use occasions, the described collector tube inside of going up is provided with a dividing plate, and the concurrent flow air conditioner is 2 flow processs.
According to different use occasions, the described collector tube inside of going up is provided with two dividing plates, and following collector tube inside is provided with a dividing plate, and the concurrent flow air conditioner is 4 flow processs.
As a kind of preferred structure, described collector tube and the following collector tube horizontal positioned of going up, flat heat exchanger tube is vertically placed.
As a kind of preferred structure, the insertion depth of described flat heat exchanger tube in last collector tube is littler than the insertion depth of flat heat exchanger tube in following collector tube.
As a kind of preferred structure, described fin is corrugated V-arrangement fin.
The processing method of the concurrent flow air conditioner of 2 flow processs (principle of 4 flow processs is too) is as follows:
When refrigerating operaton: the gaseous refrigerant of HTHP is from compressor, enter collector tube first end through cross valve, flat heat exchanger tube through dividing plate the right arrives collector tube down again, gaseous refrigerant in the following collector tube, flat heat exchanger tube through the dividing plate left side arrives upward collector tube second end, bring out the cold-producing medium that comes from last collector tube second this moment and become the high-pressure gas-liquid two phase refrigerant, the collector tube upper pipes arrives capillary module on the process, capillary module becomes low-temp low-pressure gas-liquid two-phase cold-producing medium to the high-pressure gas-liquid two phase refrigerant, enter indoor set then, the heat exchange refrigeration, become low-pressure gaseous refrigerant, get back to the compressor return air pipe through cross valve, enter compressor at last, the continual circulation;
When heating operation: the cross valve commutation, the gaseous refrigerant of HTHP is from compressor, enter indoor set through cross valve, heat exchange heats, become the high-pressure gas-liquid two phase refrigerant, enter capillary module, capillary module becomes low-temp low-pressure gas-liquid two-phase cold-producing medium to the high-pressure gas-liquid two phase refrigerant, the collector tube upper pipes arrives and goes up collector tube second end on the process, flat heat exchanger tube through the dividing plate left side enters down collector tube, then shunt, gaseous refrigerant passes through gas-liquid separator, check valve, cross valve is got back to the compressor return air pipe, and liquid refrigerant carries out heat exchange through the flat heat exchanger tube on the right of the dividing plate and becomes gaseous refrigerant, gets back to the compressor return air pipe by cross valve then, enter compressor at last, the continual circulation.
When heating operation, described liquid refrigerant is through flat heat exchanger tube endothermic gasification, the outer fin of pipe produces condensation film, under the effect of gravity and air-conditioning fan wind-force, flow down to down the liquid collecting tube-surface along fin surface, by horizontal wind drive, all condensed waters are along collector tube nature water conservancy diversion eliminating down.
The utility model has following advantage with respect to prior art: this concurrent flow air conditioner makes the concurrent flow technology can realize refrigeration and heats, and solves shunting inequality, problems such as heat exchange efficiency is low, volume is big, cost height, and is specific as follows:
1, during the utility model heating operation, for the 2 flow processs parallel-flow evaporator of (principle of 4 flow processs too), parallel stream flat heat exchanger tube distribute according to a certain percentage (position of dividing plate is greatly about 1/3 length place of last collector tube), when first flow process finishes, adopt gas-liquid separator, gaseous refrigerant is directly turned back to compressor by check valve, liquid refrigerant is assigned to uniformly in the flat heat exchanger tube in each road of second flow process and carries out heat exchange, the equal flow problem when having solved parallel-flow heat exchanger and making evaporimeter and use.The gaseous refrigerant dividing technology has improved the flow velocity of liquid refrigerant in the flat heat exchanger tube, and then has improved heat exchange efficiency greatly, significantly improves heating performance.
This concurrent flow air conditioner can both cooling and heating, simple in structure, shunting evenly, realized that parallel-flow heat exchanger is applied to air conditioner, made that the heating efficiency of air conditioner improves more than 30%, cost reduces more than 35%, the off-premises station volume reduces more than 25%.
2, the flat heat exchanger tube in microchannel is vertically placed, and is furnished with corrugated V-arrangement fin between flat tube, and every layer of fin and flat tube are at angle.In the air conditioner heat-production running, condensation film on the louvered fin under the effect of gravity and air-conditioning fan wind-force, flows down to down the liquid collecting tube-surface along fin surface, by horizontal wind drive, all condensed waters are along collector tube nature water conservancy diversion eliminating down.Thereby thoroughly solved the drainage problem when off-premises station adopts parallel-flow heat exchanger to make evaporimeter.
3, collector tube be horizontally placed on flat heat exchanger tube about, the flat heat exchanger tube in microchannel is vertically placed, last collector tube upper pipes is at the top of last collector tube, it is simple that the off-premises station pipeline is arranged, and saves the space, and, collector tube is made crooked shape up and down, make its complete with present copper pipe heat exchanger shape identical, do not need to change the off-premises station structure and directly replacement, save alternative costs greatly.
4, the insertion depth of flat heat exchanger tube in last collector tube is more shallow, just insert and go up the collector tube bottom, to guarantee the not residual liquid refrigerant in collector tube bottom, the insertion depth of flat heat exchanger tube in following collector tube is darker, during with the assurance heating operation, the gaseous refrigerant in the following collector tube can directly arrive the compressor return air pipe by gas-liquid separator and check valve.
Description of drawings
Fig. 1 is the vertical face figure of concurrent flow air conditioner of the present utility model.
Fig. 2 is the vertical view of collector tube on 2 flow processs.
Fig. 3 is the 4 flow processs vertical face figure of collector tube up and down.
Label and title are as follows in Fig. 1~3:
1 Flat heat exchanger tube 2 Dividing plate
3 Last collector tube upper pipes 4 Capillary module
5 Indoor set 6 Last collector tube
7 Cross valve 8 Check valve
9 The compressor return air pipe 10 Compressor
11 Gas-liquid separator 12 Following collector tube
13 Fin
The specific embodiment
The utility model is described in further detail below in conjunction with drawings and Examples.
Embodiment 1:
2 flow process concurrent flow air conditioners as shown in Figure 1, comprise compressor, the compressor return air pipe, cross valve, indoor set, capillary module, last collector tube upper pipes, last collector tube, flat heat exchanger tube and following collector tube, as shown in Figure 2, collector tube on described in the depression angle, following collector tube is " L " shape of circular arc bending, compressor, the compressor return air pipe connects two connectors of cross valve respectively, indoor set, last collector tube first end connects two other connector of cross valve respectively, indoor set connects by capillary module goes up the collector tube upper pipes, last collector tube upper pipes connects upward collector tube second end, last collector tube inside is provided with a dividing plate, the position of dividing plate is greatly about 1/3 length place of last collector tube, the flat heat exchanger tube by a plurality of parallel arrangements is communicated with between the collector tube up and down, flat heat exchanger tube about dividing plate respectively is a flow process, each flat heat exchanger tube has fin, following collector tube first end is provided with gas-liquid separator, gas-liquid separator connects check valve, the be connected in parallel same connector of cross valve of check valve and last collector tube first end.
Last collector tube and following collector tube horizontal positioned, flat heat exchanger tube is vertically placed.
The insertion depth of flat heat exchanger tube in last collector tube is littler than the insertion depth of flat heat exchanger tube in following collector tube.
Fin is corrugated V-arrangement fin.
The processing method of the concurrent flow air conditioner of 2 flow processs is as follows:
When refrigerating operaton: the gaseous refrigerant of HTHP is from compressor, enter collector tube first end through cross valve, flat heat exchanger tube through dividing plate the right arrives collector tube down again, gaseous refrigerant in the following collector tube, flat heat exchanger tube through the dividing plate left side arrives upward collector tube second end, bring out the cold-producing medium that comes from last collector tube second this moment and become the high-pressure gas-liquid two phase refrigerant, the collector tube upper pipes arrives capillary module on the process, capillary module becomes low-temp low-pressure gas-liquid two-phase cold-producing medium to the high-pressure gas-liquid two phase refrigerant, enter indoor set then, the heat exchange refrigeration, become low-pressure gaseous refrigerant, get back to the compressor return air pipe through cross valve, enter compressor at last, the continual circulation;
When heating operation: the cross valve commutation, the gaseous refrigerant of HTHP is from compressor, enter indoor set through cross valve, heat exchange heats, become the high-pressure gas-liquid two phase refrigerant, enter capillary module, capillary module becomes low-temp low-pressure gas-liquid two-phase cold-producing medium to the high-pressure gas-liquid two phase refrigerant, the collector tube upper pipes arrives and goes up collector tube second end on the process, flat heat exchanger tube through the dividing plate left side enters down collector tube, then shunt, gaseous refrigerant passes through gas-liquid separator, check valve, cross valve is got back to the compressor return air pipe, and liquid refrigerant carries out heat exchange through the flat heat exchanger tube on the right of the dividing plate and becomes gaseous refrigerant, gets back to the compressor return air pipe by cross valve then, enter compressor at last, the continual circulation.
When heating operation, described liquid refrigerant is through flat heat exchanger tube endothermic gasification, the outer fin of pipe produces condensation film, under the effect of gravity and air-conditioning fan wind-force, flow down to down the liquid collecting tube-surface along fin surface, by horizontal wind drive, all condensed waters are along collector tube nature water conservancy diversion eliminating down.
Embodiment 2:
As shown in Figure 3, last collector tube inside is provided with two dividing plates, following collector tube inside is provided with a dividing plate, the concurrent flow air conditioner is 4 flow processs, partition position is seen diagram, above the flat heat exchanger tube on the dividing plate left side, the left side be a flow process, above flat heat exchanger tube between left side dividing plate and the following dividing plate be a flow process, flat heat exchanger tube between following dividing plate and the top the right dividing plate is a flow process, above the flat heat exchanger tube on dividing plate the right, the right be a flow process.
The operation principle of the concurrent flow air conditioner of 4 flow processs and 2 flow processs basic identical.
The above-mentioned specific embodiment is a preferred embodiment of the present utility model; can not limit the utility model; other any change that does not deviate from the technical solution of the utility model and made or other equivalent substitute mode are included within the protection domain of the present utility model.

Claims (6)

1. concurrent flow air conditioner, it is characterized in that: comprise compressor, the compressor return air pipe, cross valve, indoor set, capillary module, last collector tube upper pipes, last collector tube, flat heat exchanger tube and following collector tube, collector tube on described in the depression angle, following collector tube is " L " shape of circular arc bending, compressor, the compressor return air pipe connects two connectors of cross valve respectively, indoor set, last collector tube first end connects two other connector of cross valve respectively, indoor set connects by capillary module goes up the collector tube upper pipes, last collector tube upper pipes connects upward collector tube second end, last collector tube inside is provided with at least one dividing plate, the flat heat exchanger tube by a plurality of parallel arrangements is communicated with between the collector tube up and down, each flat heat exchanger tube has fin, following collector tube first end is provided with gas-liquid separator, gas-liquid separator connects check valve, the be connected in parallel same connector of cross valve of check valve and last collector tube first end.
2. concurrent flow air conditioner according to claim 1 is characterized in that: the described collector tube inside of going up is provided with a dividing plate, and the concurrent flow air conditioner is 2 flow processs.
3. concurrent flow air conditioner according to claim 1 is characterized in that: the described collector tube inside of going up is provided with two dividing plates, and following collector tube inside is provided with a dividing plate, and the concurrent flow air conditioner is 4 flow processs.
4. concurrent flow air conditioner according to claim 1 is characterized in that: described collector tube and the following collector tube horizontal positioned of going up, flat heat exchanger tube is vertically placed.
5. concurrent flow air conditioner according to claim 4 is characterized in that: the insertion depth of described flat heat exchanger tube in last collector tube is littler than the insertion depth of flat heat exchanger tube in following collector tube.
6. concurrent flow air conditioner according to claim 1 is characterized in that: described fin is corrugated V-arrangement fin.
CN2011201044634U 2011-04-12 2011-04-12 Parallel-flow air conditioning Expired - Lifetime CN202057109U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011201044634U CN202057109U (en) 2011-04-12 2011-04-12 Parallel-flow air conditioning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011201044634U CN202057109U (en) 2011-04-12 2011-04-12 Parallel-flow air conditioning

Publications (1)

Publication Number Publication Date
CN202057109U true CN202057109U (en) 2011-11-30

Family

ID=45017081

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011201044634U Expired - Lifetime CN202057109U (en) 2011-04-12 2011-04-12 Parallel-flow air conditioning

Country Status (1)

Country Link
CN (1) CN202057109U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102121760A (en) * 2011-04-12 2011-07-13 广东机电职业技术学院 Parallel flow air conditioner and processing method thereof
CN103759569A (en) * 2013-12-10 2014-04-30 柳州五菱宝马利汽车空调有限公司 Distributing cavity embedded collecting and distributing tube for automotive parallel flow evaporator
CN103759570A (en) * 2013-12-10 2014-04-30 柳州五菱宝马利汽车空调有限公司 Flow connection-division tube for automobile parallel-flow evaporator
CN104204690A (en) * 2012-04-09 2014-12-10 大金工业株式会社 Air-conditioning device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102121760A (en) * 2011-04-12 2011-07-13 广东机电职业技术学院 Parallel flow air conditioner and processing method thereof
CN104204690A (en) * 2012-04-09 2014-12-10 大金工业株式会社 Air-conditioning device
CN104204690B (en) * 2012-04-09 2017-05-10 大金工业株式会社 Air-conditioning device
CN103759569A (en) * 2013-12-10 2014-04-30 柳州五菱宝马利汽车空调有限公司 Distributing cavity embedded collecting and distributing tube for automotive parallel flow evaporator
CN103759570A (en) * 2013-12-10 2014-04-30 柳州五菱宝马利汽车空调有限公司 Flow connection-division tube for automobile parallel-flow evaporator

Similar Documents

Publication Publication Date Title
CN102121760B (en) Parallel flow air conditioner and processing method thereof
CN202927982U (en) Air conditioning system
CN202002233U (en) Dehumidifier
CN201779925U (en) Parallel flow evaporator and heat pump air conditioner
CN101900460A (en) Parallel flow evaporator and heat pump air conditioner
CN203053095U (en) Novel process parallel flow condenser of automobile air conditioner
CN201621986U (en) Microchannel heat exchanger
CN101298951A (en) Slice penetrating type mini channel heat exchanger with automatic solution dividing structure
CN202057109U (en) Parallel-flow air conditioning
CN101298950A (en) Wind cooling heat exchanger with solution division structure for air conditioner
CN202647990U (en) Double-pole and double-condensation air conditioner
CN201229093Y (en) Air-cooled heat exchanger for air conditioner with liquid division structure
CN203595244U (en) Integrated heat exchanger and air conditioner
CN202562136U (en) Concurrent flow heat exchanger applied in heat pump air conditioner
CN202057111U (en) Multifunctional air source hot water and air-conditioning heat pump unit
CN101639306B (en) Refrigeration circulation system of heat exchanger of air conditioner outdoor unit
CN201795645U (en) Novel evaporation type parallel flow heat exchanger and air conditioner employing same
CN201476415U (en) Heat exchanger of outdoor unit of air-cooled heat pump air conditioner
CN203605511U (en) Air cooling compression condensing unit for deep supercooling
CN201401872Y (en) Air conditioner
CN207379124U (en) A kind of multi-online air-conditioning system of quickly defrosting
CN2921723Y (en) Concurrent flow condenser and domestic air conditioner using the same condenser
CN2826304Y (en) Refrigerating system of heat pump type central and household central air conditioning
CN109900018A (en) Air source heat pump system
CN203163105U (en) Movable air-conditioner

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20111130

Effective date of abandoning: 20130227

RGAV Abandon patent right to avoid regrant