CN202195630U - Gas-liquid separation structure of compressor - Google Patents

Gas-liquid separation structure of compressor Download PDF

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Publication number
CN202195630U
CN202195630U CN2011202646049U CN201120264604U CN202195630U CN 202195630 U CN202195630 U CN 202195630U CN 2011202646049 U CN2011202646049 U CN 2011202646049U CN 201120264604 U CN201120264604 U CN 201120264604U CN 202195630 U CN202195630 U CN 202195630U
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China
Prior art keywords
compressor
gas
liquid
cylindrical shell
separating structure
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Expired - Lifetime
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CN2011202646049U
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Chinese (zh)
Inventor
钟瑞兴
张治平
蒋楠
陈杰东
蒋彩云
谢蓉
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Gree Electric Appliances Inc of Zhuhai
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Gree Electric Appliances Inc of Zhuhai
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Abstract

The embodiment of the utility model discloses compressor gas-liquid separation structure for improve the separation effect of the gas-liquid mixture that refrigerant and lubricating oil formed in the compressor system. The utility model discloses compressor gas-liquid separation structure, including a baffle group, gas-liquid filter screen, further include secondary baffle subassembly, secondary baffle subassembly is including the fender stream board and the secondary baffle group of locating compressor suction opening department, and the gas-liquid mixture flows through a baffle group and gas-liquid filter screen earlier and carries out the initial gross separation, flows through secondary baffle subassembly again and carries out the secondary separation.

Description

A kind of compressor vapor-liquid separating structure
Technical field
The utility model relates to field of air conditioning, relates in particular to a kind of compressor vapor-liquid separating structure.
Background technology
For centrifugal unit, in evaporimeter, evaporate to guarantee the unit high-performance for making the normally lubricated and relative purer refrigerant of bearing, need refrigerant is fully separated with lubricating oil.Special in the pressure-equalizing pipe in the fuel tank, reduce for making tank pressure, balance pipe is caused the compressor inlet place, can make the mixture of refrigerant and oil get into compressor assembly like this, influence the normally lubricated and refrigerant purity of bearing.For this problem, conventional solution is at the fuel-tank outlet place gas-liquid filter net to be set, to reach the purpose of gas-liquid separation.Because the restriction of screen pack size and precision; For obtaining filter effect preferably; The order number of gas-liquid filter net is more and more closeer, simultaneously for guaranteeing certain pressure loss, needs the profile of gas-liquid filter net is further enlarged; Cause the increase of cost to increase appearance and size simultaneously, be unfavorable for optimization of inside structure.
The utility model content
The utility model embodiment provides a kind of compressor vapor-liquid separating structure; In order to overcome present gas-liquid filter net for obtaining filter effect preferably; What need the order number of gas-liquid filter net be provided with is more and more closeer; For guaranteeing certain pressure loss, the profile of gas-liquid filter net is further done greatly simultaneously, increased cost and structure space.
A kind of compressor vapor-liquid separating structure; Comprise baffle groups, gas-liquid filter net; Further comprise secondary baffling assembly; Secondary baffling assembly comprises flow-stopping plate and the secondary baffle groups of being located at compressor air suction mouth place, and flow through earlier baffle groups and gas-liquid filter net of gas-liquid mixture carries out initial gross separation, and the secondary baffling assembly of flowing through again carries out secondary separation.
Preferably, baffle groups and gas-liquid filter net are arranged in the same cylindrical shell of compressor oil box top, and cylindrical shell is apart from the oily nearer end opening setting of tank lubrication; Gas-liquid filter net is arranged at the baffle groups top one time; Secondary baffling assembly is arranged at the inside top of compressor housing, and cylindrical shell is communicated with through balance pipe with compressor housing, and balance pipe has an air inlet that is connected with cylindrical shell; A gas outlet that is connected with compressor housing, flow-stopping plate place the below, gas outlet.
Preferably, one time baffle groups comprises a deflection plate more than at least, and one time deflection plate is provided with at interval, and is fixed in the cylindrical shell so that downward-sloping mode is staggered, and deflection plate and between fixing end of cylindrical shell and the cylindrical shell does not leave air gap.
Preferably, the diameter of cylindrical shell is D, is spaced apart 0.15D-0.35D between deflection plate.
Preferably, downtilt angles is smaller or equal to 10 degree.
Preferably, flow-stopping plate surrounds secondary baffling square cavity with compressor housing above the compressor air suction mouth.
Preferably, secondary baffling square cavity flows out the end opening setting at air-flow.
Preferably, the secondary baffle groups comprises at least one secondary deflection plate, one side fixing of secondary deflection plate one end and flow-stopping plate leaves air gap between the other end and the secondary baffling square cavity.
Preferably, the bond length of secondary baffling square cavity is L, and the length of secondary deflection plate is 0.1L-0.4L.
Can find out that from above technical scheme the utility model embodiment has the following advantages:
(1) utilizes the gas-liquid mixture air-flow velocity to realize gas-liquid separation, do not need gas-liquid filter net is made particular design with flowing to change;
(2) through being set repeatedly, baffling can improve the gas-liquid separation precision;
(3) can in time adjust deflection plate number and baffling number of times according to the separation accuracy needs, applicability is strong.
Description of drawings
Shown in Figure 1 is the utility model example structure sketch map;
Shown in Figure 2 is the plan structure sketch map of secondary baffling square cavity among the utility model embodiment.
The specific embodiment
The utility model embodiment provides a kind of compressor vapor-liquid separating structure; Be used to utilize gas-liquid mixture when flow velocity reduction and flow direction change; Because the existence of viscosity; The characteristic that drop invests obstacle easily reaches the purpose of gas-liquid separation, can obtain higher separation accuracy through baffling repeatedly, improves the separating effect of the gas-liquid mixture that refrigerant and lubricating oil form in the compressor assembly.
With reference to figure 1, be depicted as a kind of compressor vapor-liquid separating structure of the utility model embodiment, it comprises baffle groups 3, gas-liquid filter net 4; And further be provided with flow-stopping plate 6 and secondary baffle groups 7; Wherein, a baffle groups 3 is arranged in the same cylindrical shell 2 at compressor sump 1 top the end opening setting that cylindrical shell 2 lubricating oil in fuel tank 1 is nearer with gas-liquid filter net 4; Gas-liquid filter net 4 is arranged at baffle groups 3 tops one time; Flow-stopping plate 6 and secondary baffle groups 7 are arranged at the inside top of compressor housing 5, and cylindrical shell 2 is communicated with through balance pipe 8 with compressor housing 5, and balance pipe has an air inlet that is connected with cylindrical shell 2; A gas outlet that is connected with compressor housing 5, flow-stopping plate 6 place below, balance pipe gas outlet.
In order to obtain better first gas-liquid separation effect; One time baffle groups 3 comprises a deflection plate more than at least, and one time deflection plate is provided with at interval, and is fixed in the cylindrical shell 2 with downward-sloping mode interleaved; And deflection plate and between fixing end of cylindrical shell 2 and the cylindrical shell 2 does not leave certain air gap; The diameter of supposing cylindrical shell 2 is D, and then the interval between deflection plate is set at 0.15D-0.35D, and downtilt angles is smaller or equal to 10 degree.
Secondary deflection plate assembly comprises the flow-stopping plate 6 and at least one secondary deflection plate of being located at compressor air suction mouth place, one side fixing of secondary deflection plate one end and said flow-stopping plate 6 leaves air gap between the other end and the secondary baffling square cavity.The cavity that the compressor inlet top is surrounded by flow-stopping plate is square; Form secondary baffling square cavity, and flow out the end opening setting, referring to Fig. 2 at air-flow; Be depicted as the plan structure sketch map of secondary baffling square cavity; If its minor face is L, in order to reach better secondary baffling effect, the length of secondary flow-stopping plate is made as 0.1L-0.4L.
Technical scheme through present embodiment; Machine is from the refrigerant of fuel tank and the gas-liquid mixture of the lubricating oil formation baffle groups of flowing through earlier successively a time in air conditioner compressed; Because the reduction of air velocity and the change of direction, lubricating oil can invest on deflection plate, and gas gets into next piece deflection plate again after the direction change; Through baffling repeatedly, most lubricating oil is separated and under the effect of gravity, flows back into fuel tank along a deflection plate; Getting into the gas-liquid filter net with certain order number through the gas-liquid mixture after the baffle groups separation separates; Gas after initial gross separation and part residual liquid enter to the compressor housing place along balance pipe; Owing to communicate with compressor inlet here, this part gas-liquid mixture is easy to be inhaled into the compressor inlet place, and the utility model embodiment avoids remaining lubricating oil gas to get into compressor assembly through flow-stopping plate and secondary baffle groups are set at the compressor housing place again; Flow-stopping plate and secondary baffle groups make the flow velocity of gas change with flowing to once more; Improve separating effect, the lubricating oil that here filters can draw and is back to fuel tank through pipeline is set, at last; Purer cold media gas is inhaled into compressor inlet, has improved systematic function.
More than a kind of compressor vapor-liquid separating structure that the utility model provided has been carried out detailed introduction; For one of ordinary skill in the art; Thought according to the utility model embodiment; The part that on the specific embodiment and range of application, all can change, in sum, this description should not be construed as the restriction to the utility model.

Claims (9)

1. compressor vapor-liquid separating structure; Comprise baffle groups, gas-liquid filter net; It is characterized in that, further comprise secondary baffling assembly, said secondary baffling assembly comprises flow-stopping plate and the secondary baffle groups of being located at compressor air suction mouth place; A flow through earlier said baffle groups and gas-liquid filter net of gas-liquid mixture carries out initial gross separation, and the said secondary baffling assembly of flowing through again carries out secondary separation.
2. compressor vapor-liquid separating structure according to claim 1; It is characterized in that: a said baffle groups and gas-liquid filter net are arranged in the same cylindrical shell of compressor oil box top; Said cylindrical shell is apart from the oily nearer end opening setting of tank lubrication, and said gas-liquid filter net is arranged at the baffle groups top one time, and said secondary baffling assembly is arranged at the inside top of compressor housing; Said cylindrical shell is communicated with through balance pipe with compressor housing; Said balance pipe has an air inlet that is connected with said cylindrical shell, a gas outlet that is connected with said compressor housing, and said flow-stopping plate places below, said gas outlet.
3. compressor vapor-liquid separating structure according to claim 2; It is characterized in that: a said baffle groups comprises a deflection plate more than at least; A said deflection plate is provided with at interval; And be fixed in the said cylindrical shell so that downward-sloping mode is staggered, and a said deflection plate and between fixing end of said cylindrical shell and the said cylindrical shell does not leave air gap.
4. compressor vapor-liquid separating structure according to claim 3 is characterized in that: the diameter of said cylindrical shell is D, is spaced apart 0.15D-0.35D between the said deflection plate.
5. compressor vapor-liquid separating structure according to claim 3 is characterized in that: said downtilt angles is smaller or equal to 10 degree.
6. compressor vapor-liquid separating structure according to claim 1 is characterized in that: said flow-stopping plate surrounds secondary baffling square cavity with said compressor housing above the compressor air suction mouth.
7. compressor vapor-liquid separating structure according to claim 6 is characterized in that: described secondary baffling square cavity flows out the end opening setting at air-flow.
8. compressor vapor-liquid separating structure according to claim 6; It is characterized in that: said secondary baffle groups comprises at least one secondary deflection plate; One side of said secondary deflection plate one end and said flow-stopping plate is fixed, and leaves air gap between the other end and the secondary baffling square cavity.
9. compressor vapor-liquid separating structure according to claim 8 is characterized in that: the bond length of said secondary baffling square cavity is L, and the length of said secondary deflection plate is 0.1L-0.4L.
CN2011202646049U 2011-07-25 2011-07-25 Gas-liquid separation structure of compressor Expired - Lifetime CN202195630U (en)

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Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
CN2011202646049U CN202195630U (en) 2011-07-25 2011-07-25 Gas-liquid separation structure of compressor

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102900709A (en) * 2011-07-25 2013-01-30 珠海格力电器股份有限公司 Gas-liquid separation structure of compressor
CN102997522A (en) * 2012-11-26 2013-03-27 浙江盾安人工环境股份有限公司 Centrifugal refrigerating compressor, and oil separation system and oil separation method for centrifugal refrigerating compressor
CN104019590A (en) * 2014-06-26 2014-09-03 吉首大学 Novel ammonia refrigeration gas-liquid separator
CN107388648A (en) * 2017-07-19 2017-11-24 珠海格力电器股份有限公司 Flash tank and air conditioner using same
CN108465300A (en) * 2018-04-02 2018-08-31 杨大鹏 A kind of chemical industry gas-liquid separation tower

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102900709A (en) * 2011-07-25 2013-01-30 珠海格力电器股份有限公司 Gas-liquid separation structure of compressor
CN102900709B (en) * 2011-07-25 2015-10-07 珠海格力电器股份有限公司 Gas-liquid separation structure of compressor
CN102997522A (en) * 2012-11-26 2013-03-27 浙江盾安人工环境股份有限公司 Centrifugal refrigerating compressor, and oil separation system and oil separation method for centrifugal refrigerating compressor
CN102997522B (en) * 2012-11-26 2015-05-27 浙江盾安人工环境股份有限公司 Centrifugal refrigerating compressor, and oil separation system and oil separation method for centrifugal refrigerating compressor
CN104019590A (en) * 2014-06-26 2014-09-03 吉首大学 Novel ammonia refrigeration gas-liquid separator
CN104019590B (en) * 2014-06-26 2016-06-01 吉首大学 Ammonia refrigeration gas-liquid separator
CN107388648A (en) * 2017-07-19 2017-11-24 珠海格力电器股份有限公司 Flash tank and air conditioner using same
CN107388648B (en) * 2017-07-19 2023-06-30 珠海格力电器股份有限公司 Flash device and air conditioner using same
CN108465300A (en) * 2018-04-02 2018-08-31 杨大鹏 A kind of chemical industry gas-liquid separation tower
CN108465300B (en) * 2018-04-02 2020-08-25 华融化学股份有限公司 Gas-liquid separation tower for chemical industry

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C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20120418

Effective date of abandoning: 20151007

AV01 Patent right actively abandoned

Granted publication date: 20120418

Effective date of abandoning: 20151007

C25 Abandonment of patent right or utility model to avoid double patenting