CN202630530U - Rotational flow coolant branching body - Google Patents
Rotational flow coolant branching body Download PDFInfo
- Publication number
- CN202630530U CN202630530U CN 201220122963 CN201220122963U CN202630530U CN 202630530 U CN202630530 U CN 202630530U CN 201220122963 CN201220122963 CN 201220122963 CN 201220122963 U CN201220122963 U CN 201220122963U CN 202630530 U CN202630530 U CN 202630530U
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- Prior art keywords
- refrigerant
- along separate
- separate routes
- branching
- shunt
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Abstract
The utility model belongs to the technical field of air conditioners, and particularly relates to a rotational flow coolant branching body used for an air conditioning heat exchanger. The rotational flow coolant branching body comprises a cylindrical body, one end face of the cylindrical body is sealed, the other end face of the cylindrical body is provided with a plurality of branching outlets, an inner cavity of the body is a distributary inner cavity, and the branching outlets are communicated with the distributary inner cavity. A body side wall situated at the sealed end of the body is provided with a tangential coolant inlet hole, the centre line of the coolant inlet hole is perpendicular to but does not intersect the centre line of the body, and is close to and parallel to a tangent line of the inner wall of the branching hollow cavity, and coolants in a liquid feed pipe inserted in the coolant inlet hole enter the branching hollow cavity in a tangential direction. The rotational flow coolant branching body is good in distributary effect, little in gravity effect, flexible to install, simple in structure, and low in manufacturing difficulty, and has economic and technical advantages.
Description
Technical field
The utility model belongs to air-conditioning technical field, is specifically related to the eddy flow refrigerant shunt body that a kind of air-condition heat exchanger is used.
Background technology
In the refrigeration system; Directly evaporate the compact aerial cooler of feed flow; For guaranteeing heat exchange effect and cold-producing medium flow velocity best in the refrigerant tubing, must adopt the form of multichannel coil pipe parallel connection, can reach best heat exchange effect so on the one hand; Can keep best cold-producing medium flow velocity on the other hand, and fall restriction to pressure within the specific limits.And the cold-producing medium that expansion valve or capillary come out normally the bubble stream of gas-liquid two-phase or the mixture of cork flow pattern, the purpose of body is fully mixed two phase refrigerant exactly along separate routes, and ana is assigned in each road coil pipe and goes again.
At present, especially domestic air conditioner adopts air-conditioner mainly is the shunt body of pressure drop type.Get into the gas-liquid two-phase cold-producing medium of body along separate routes through expansion valve or capillary outlet, at first through the interior restricting orifice of establishing, because the sudden contraction of restricting orifice cross section raises the dynamic pressure of cold-producing medium, flow velocity increases, and both sides form pressure reduction through restricting orifice the time.Rear side at restricting orifice is provided with a mixing chamber, and cold-producing medium at a high speed produces eddy current after getting into mixing chamber, thereby refrigerant air-liquid two is fully mixed mutually, evenly gets into each road evaporation coil along separating tube again.This shunt body is through the throttling to cold-producing medium, and turbulization is fully mixed two phase refrigerant, has bigger pressure to fall, and when refrigerant flow altered a great deal simultaneously, throttle diameter needed corresponding adjustment, gives the actual a series of problems of bringing of using.The shunt body of pressure drop type in addition must be noted that also that when mounted outlet need reduce the separatory uneven phenomenon of bringing owing to the difference of gas-liquid density, but in narrow and small conditioned space, often be difficult to be guaranteed as far as possible by the gravity direction layout.
Summary of the invention
The purpose of the utility model is the above-mentioned defective that exists to prior art, provides a kind of shunting effect good and receive gravity effect seldom, and is flexible for installation, simple in structure, the eddy flow refrigerant shunt body that difficulty of processing reduces.
The purpose of the utility model is to realize through following technical scheme: this eddy flow refrigerant is body along separate routes; Be mainly used in air-condition heat exchanger; It comprises a columnar main body, the one end-face sealing, and other end end face is provided with some shunt and portals; The main body inner chamber is the shunting cavity, and said shunt is portalled and shunting cavity UNICOM; Be positioned on the body wall of main body blind end and have refrigerant ingate, a tangential; The center line of refrigerant ingate is vertical but non-intersect with the center line of main body; Parallel with shunting cavity inner wall tangent line near also, the refrigerant tangential in the feed pipe that inserts in the refrigerant ingate is got in the shunting cavity.
Further, the cross-sectional area of said shunting cavity is promptly increasing on the direction of portalling along separate routes on the refrigerant flow direction gradually.
For the gas-liquid two-phase refrigerant mixes better, said shunting cavity inner wall is processed into screw thread form.
For the ease of the installation of shunt tubes, it is that said shunt is portalled and is distributed near its circumferential edge to the protruding inclined-plane of main center that said main body is provided with the end face that portals along separate routes, goes out centerline hole with respect to the outer tilt of main center's alignment along separate routes.
The utility model utilizes high pressure refrigerant tangential to get in the shunt body shunting cavity, forms helical flow, increases turbulence level, fully mixes the gas-liquid two-phase refrigerant thereby reach.Body structure is simple along separate routes for the utility model refrigerant; Each the shunting outlet of refrigerant inlet and refrigerant spatially roughly is 90 degree; Its cardinal principle is to utilize centrifugal force to carry out gas-liquid mixed; Be that with the main distinction of tradition shunt body the utility model refrigerant shunt body has utilized the mutual conversion of dynamic and static pressure.The shunting effect of the utility model receives gravity effect seldom, and is flexible for installation, simple in structure, and difficulty of processing reduces, and has more economy and technical advantage.
Description of drawings
Fig. 1 is the front view of the utility model embodiment.
Fig. 2 is the right view of Fig. 1.
Fig. 3 is the upward view of Fig. 1.
Fig. 4 is that the A-A of Fig. 3 is to cutaway view.
Fig. 5 is the perspective view of the utility model embodiment.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is described in further detail.
Referring to Fig. 1, Fig. 2, Fig. 3, Fig. 4 and Fig. 5, present embodiment comprises columnar main body 2.Visible from Fig. 4 and Fig. 5, the sealing of main body 2 right-hand member end faces, main body 2 left end end faces are provided with 3 shunt and portal 1; Also visible from figure; The left side of main body 2 is to the protruding inclined-plane of main center; 3 shunt are portalled and 1 are distributed near the circumferential edge of left side, and 1 the center line of portalling along separate routes is with respect to the center line outward inclining of main body 2, are convenient to each shunt tubes like this and are installed on each and portal along separate routes on 1.The inner chamber of main body 2 is shunting cavity 3, portal along separate routes 1 with shunting cavity 3 UNICOMs.From figure, can see; Be positioned on the body wall of main body 2 blind ends and have refrigerant ingate, a tangential 4; The center line of refrigerant ingate 4 is vertical but non-intersect with the center line of main body 2; Parallel with the inwall tangent line of shunting cavity 3 near also, the refrigerant tangential in the feed pipe that inserts in the refrigerant ingate is got in the shunting cavity 3.Main body 2 are one one end diameters greater than other end diameter be toy trumpet shape circle tube member, the cross-sectional area that is to say shunting cavity 3 is in i.e. increase gradually on 1 the direction of portalling along separate routes on the refrigerant flow direction.
For better mixing, the inwall of shunting cavity 3 also can be processed into screw thread form, with the uniformity coefficient of further reinforcement gas-liquid two-phase refrigerant mixing.
During operation of air conditioner, gas-liquid two-phase refrigerant at a high speed gets into from tangential, shunting cavity 3 right side shown in Figure 4, forms the helical flow that moves right along shunting cavity 3 inwalls; Gas-liquid is fully mixed under action of centrifugal force, because shunt body cavity 3 cross sections area on the refrigerant flow direction increases gradually, flow velocity reduces simultaneously; Static pressure raises; The part gas phase refrigerant becomes the liquid phase refrigerant mutually, in uniform pressure field of left bottom formation of shunting cavity 3, under same pressure effect; Refrigerant is evenly distributed in the middle of its corresponding stream from 1 outflow of portalling along separate routes.Also visible from Fig. 4, the left side in shunting cavity 3 is centered close to shunt portals near 1, and the processome of a vertebra shape is arranged, and this vertebra shape processome can be used for the water conservancy diversion of refrigerant.
Adopt the shunt body of the utility model, feed pipe is comparable traditional littler.Under same refrigerant mass flow, the speed that gets into shunt body cavity is bigger, and the intensity of its screw is also big more, and gas-liquid mixed gets more even, and shunting effect is better.The internal diameter of import feed pipe is bigger than orifice in tradition shunt body; The speed of cold-producing medium is lowered in the forward position, aperture; Biphase gas and liquid flow through the time lack of homogeneity (be prone to cause two be separated), and the utility model can be avoided being separated in the import feed pipe.
The utlity model has better separatory effect through experiment showed,, separatory is more even; Refrigerating capacity increases; Do not receive the influence of import mass velocity and steam mass dryness fraction, the power of its mixing is centrifugal force, thereby the inclination angle when installing also has only faint influence to its separatory effect.Install with the also fine small space that is applicable to of roughly 90 degree interlaced arrangement that portals along separate routes the refrigerant ingate.
The content of not doing in this specification to describe in detail belongs to this area professional and technical personnel's known prior art.
Claims (4)
1. an eddy flow refrigerant shunt body is mainly used in air-condition heat exchanger, and it is characterized in that: it comprises a columnar main body; The one end-face sealing; Other end end face is provided with some shunt and portals, and the main body inner chamber is the shunting cavity, and said shunt is portalled and shunting cavity UNICOM; Be positioned on the body wall of main body blind end and have refrigerant ingate, a tangential; The center line of refrigerant ingate is vertical but non-intersect with the center line of main body; Parallel with shunting cavity inner wall tangent line near also, the refrigerant tangential in the feed pipe that inserts in the refrigerant ingate is got in the shunting cavity.
2. eddy flow refrigerant according to claim 1 is body along separate routes, it is characterized in that: the cross-sectional area of said shunting cavity is promptly increasing on the direction of portalling along separate routes on the refrigerant flow direction gradually.
3. eddy flow refrigerant according to claim 1 and 2 is body along separate routes, and it is characterized in that: said shunting cavity inner wall is processed into screw thread form.
4. eddy flow refrigerant according to claim 3 is body along separate routes; It is characterized in that: said main body is provided with the end face that portals along separate routes and is the inclined-plane to main center's convexity; Said shunt is portalled and is distributed near its circumferential edge, goes out centerline hole with respect to the outer tilt of main center's alignment along separate routes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220122963 CN202630530U (en) | 2012-03-28 | 2012-03-28 | Rotational flow coolant branching body |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201220122963 CN202630530U (en) | 2012-03-28 | 2012-03-28 | Rotational flow coolant branching body |
Publications (1)
Publication Number | Publication Date |
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CN202630530U true CN202630530U (en) | 2012-12-26 |
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CN 201220122963 Expired - Fee Related CN202630530U (en) | 2012-03-28 | 2012-03-28 | Rotational flow coolant branching body |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102607216A (en) * | 2012-03-28 | 2012-07-25 | 湖南科技大学 | Cyclone refrigerant branching device |
-
2012
- 2012-03-28 CN CN 201220122963 patent/CN202630530U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102607216A (en) * | 2012-03-28 | 2012-07-25 | 湖南科技大学 | Cyclone refrigerant branching device |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121226 Termination date: 20160328 |