CN207446008U - A kind of venturi mixer nozzle and venturi mixer - Google Patents
A kind of venturi mixer nozzle and venturi mixer Download PDFInfo
- Publication number
- CN207446008U CN207446008U CN201721368407.5U CN201721368407U CN207446008U CN 207446008 U CN207446008 U CN 207446008U CN 201721368407 U CN201721368407 U CN 201721368407U CN 207446008 U CN207446008 U CN 207446008U
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- China
- Prior art keywords
- nozzle
- venturi mixer
- inner convex
- lug boss
- outer lug
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Abstract
The utility model discloses a kind of venturi mixer nozzle, the outer wall of nozzle is equipped with several outer lug boss, and each outer lug boss extends to nozzle by the input end of nozzle in the shape of a spiral(7)The port of export, form outer diversion trench, the spiral windings of several outer lug boss is to identical;The inner wall of nozzle is equipped with several inner convex platforms, and each inner convex platform extends to nozzle by the input end of nozzle in the shape of a spiral(7)The port of export, diversion trench in formation, the spiral windings of several inner convex platforms is to identical;The spiral winding of inner convex platform and outer lug boss is to opposite.Solve the problems, such as that venturi mixer mixing efficiency is low in the prior art, the uniformity is poor.The utility model can realize efficient mixing.
Description
Technical field
The utility model is related to mix special equipment technical field more particularly to a kind of venturi mixer nozzle and Wen Qiu
In mixer.
Background technology
Venturi mixer is a kind of device for mixing two kinds of different liquid phase mediums, is often installed on industrial pipeline
In, it is driven by the quick jet stream of main fluid and introduces fluid flowing, energy, momentum are transferred simultaneously using the viscous shear power between fluid
Make the device that quality mutually blends.It does not have mechanical moving element, simple in structure, reliable operation, realizes closed system mixing.Text
Mixer is widely used in technique mixing of two kinds of different mediums in pipeline in chemical production technology in mound.
But in actual production, since concentration of medium, density, viscosity are different, make mixing efficiency low, the uniformity is poor, can not
Meet actual process production needs, be forced to realize efficiently mixing purpose using the follow-up process equipment that increases, virtually increase investment
Expense.
Utility model content
The purpose of this utility model is to provide a kind of venturi mixer nozzle and venturi mixers, solve existing
The problem of venturi mixer mixing efficiency is low in technology, the uniformity is poor.The utility model can realize efficient mixing.
In order to achieve the above objectives, the utility model adopts the following technical solution:
The utility model provides a kind of venturi mixer nozzle, and the outer wall of nozzle is equipped with several outer lug boss, each
Outer lug boss is extended to the port of export of nozzle by the input end of nozzle in the shape of a spiral, forms outer diversion trench, several outer lug boss
Spiral winding is to identical;The inner wall of nozzle is equipped with several inner convex platforms, and each inner convex platform is prolonged in the shape of a spiral by the input end of nozzle
Extend the port of export of nozzle, diversion trench in formation, the spiral windings of several inner convex platforms is to identical;The spiral of inner convex platform and outer lug boss
Around to opposite.
Further, the utility model is also characterized by:
Outer lug boss height determines that inner convex platform height is determined according to main fluid viscosity according to fluid viscosity is introduced.
The quantity of outer lug boss is two, and two outer lug boss are symmetrical arranged along the circumferential direction of nozzle.
Outer lug boss vertical view is approximately semicircle shape.
The quantity of inner convex platform is four, and four inner convex platforms are uniformly distributed along the circumferential direction of nozzle.
Inner convex platform vertical view is approximately quadrant arcuation.
The port of export of nozzle and the intersection of inner convex platform are equipped with alveolus.
The port of export of nozzle is equipped with alveolus with the intersection of each inner convex platform.
The straight pipe outer wall at nozzle inlet end is equipped with screw thread.
The utility model additionally provides a kind of venturi mixer using said nozzle, the input end and venturi of nozzle
The sucking room of mixer is connected through a screw thread.
Further, the utility model is also characterized by:
The external screw thread of nozzle inlet end outer wall is connected with sucking the internal thread of chamber interior walls.
Compared with prior art, the utility model has technique effect beneficial below:
A kind of venturi mixer nozzle provided by the utility model, it is interior by the inner wall of nozzle inner convex platform being set to be formed
Diversion trench, main fluid enter nozzle by nozzle inlet end straight pipe, and cross-section area of nozzle reduction increases main fluid flow velocity, at a high speed from
Nozzle exit end flows out through sucking room and enters trunnion, occurs when part edge side liquid tangent line is sprayed at a high speed by spray nozzle front end inclined
Turn.By the outer wall in nozzle outer lug boss is set to form outer diversion trench, enter sucking room and in main fluid drive introducing fluid
It is lower to trunnion section flow while, part introduces outer return guide trough that fluid and outer lug boss are formed into reverse deflection, finally makes to draw
Enter fluid to collide with main fluid, and layering is generated in mixed flow moment, reach rapid, uniform by crossing over many times mixing
Ground is spread in the purpose in entire fluid, realizes the raising of mixing efficiency.
A kind of venturi mixer provided by the utility model, by being sprayed to former mixer in having venturi mixer
Mouth replace and can be achieved with efficiently mixing purpose.Meanwhile by sucking the internal thread of chamber interior walls and the external screw thread of outer nozzle wall
The front and rear adjusting of relative position, you can achieve the purpose that different mixing liquid measures than adjustment.With simple in structure, it is easy to operate easily
Understand, can be used under without mechanical dynamic environment and non-environmental-pollution.Mixing apparatus investment cost can be reduced after implementation and is improved mixed
Close efficiency.
Description of the drawings
Fig. 1 is the structure diagram of venturi mixer provided by the utility model;
Fig. 2 is the structure diagram of nozzle provided by the utility model.
Fig. 3 is the inside expanded view of nozzle provided by the utility model;
Fig. 4 is the external expansion figure of nozzle provided by the utility model;
In figure, 1:Main fluid connects nozzle;2:Introducing fluidly connects nozzle;3:Suck room;4:Converging transition;5:Trunnion section;
6:Diffuser;7:Nozzle;8:Outer lug boss;9:Inner convex platform;10:Alveolus;11:External screw thread;12:Internal thread.
Specific embodiment
The utility model is described in further detail below in conjunction with the accompanying drawings:
Referring to Fig. 1, the utility model provides a kind of venturi mixer, connects nozzle 1 including main fluid, introduces fluid
Nozzle 2 is connected, sucks room 3, converging transition 4, trunnion section 5, diffuser 6 and nozzle 7.The input end of nozzle 7 is mixed with venturi
The sucking room 3 of device is connected through a screw thread.Specifically, the external screw thread 11 of 7 input end straight pipe outer wall of nozzle and sucking 3 inner wall of room
Internal thread 12 connects.
Herein, venturi mixer is by sucking the internal thread 12 of 3 inner wall of room and 7 input end input end straight pipe of nozzle
The front and rear adjusting of 11 relative position of external screw thread of outer wall achievees the purpose that different mixing liquid measures than adjustment.
Referring to Fig. 2-4, the utility model additionally provides a kind of venturi mixer nozzle, and the outer wall of nozzle 7 is equipped with several
Outer lug boss 8, each outer lug boss 8 are extended to the port of export of nozzle 7 by the input end of nozzle 7 in the shape of a spiral, form outer water conservancy diversion
Slot, the spiral windings of several outer lug boss 8 is to identical;The inner wall of nozzle 7 is equipped with several inner convex platforms 9, and each inner convex platform 9 is in spiral shell
Rotation shape is extended to the port of export of nozzle 7 by the input end of nozzle 7, diversion trench in formation, and the spiral windings of several inner convex platforms 9 is to phase
Together;The spiral winding of inner convex platform 9 and outer lug boss 8 is to opposite.
Wherein, 8 height of outer lug boss determines that 9 height of inner convex platform is determined according to main fluid viscosity according to fluid viscosity is introduced.
Preferably, the quantity of outer lug boss 8 is two, and two outer lug boss are symmetrical arranged along the circumferential direction of nozzle 7.Inner convex platform 9
Quantity is four, and four inner convex platforms are uniformly distributed along the circumferential direction of nozzle 7.
Preferably, the vertical view of outer lug boss 8 is approximately semicircle shape, and the vertical view of inner convex platform 9 is approximately quadrant arcuation.
In the utility model, the port of export of nozzle 7 is equipped with alveolus 9 with the intersection of inner convex platform 9.Preferably, nozzle 7
The intersection of the port of export and each inner convex platform 9 is equipped with alveolus 9.
The principle of the utility model is:Main fluid connects nozzle 1 by main fluid and enters in nozzle 7, due to 7 section of nozzle
It constantly reduces, until flow velocity fast whole rise during front end, high-velocity fluid causes sucking 3 pressure of room to reduce, and drives liquid in sucking room 3
Trunnion section 5 is quickly entered by converging transition 4 to be mixed and flow into diffuser 6, since 6 section of diffuser starts to increase rapidly, is made
Liquid volume expands pulverization, is sufficiently mixed, so as to reach mixing purpose.Herein, master is passed through during two kinds of fluid mixing
The quick jet stream of fluid, which drives, introduces fluid flowing mixing, generates shunting in mixed flow moment, crosses over many times mixing and reversely rotation
Stream reaches rapid, is equably spread in entire fluid, achievees the purpose that moment rapidly and efficiently mixes.
Venturi mixer is while above-mentioned mixing is completed, when main fluid connects nozzle 1 into nozzle 7 by main fluid
While flow velocity increases, interior diversion trench is formed by nozzle 7 inner wall, 4 inner convex platforms 9, makes part edge side liquid tangent line by nozzle 7
Front end deflects when spraying at a high speed.It introduces fluid and fluidly connects nozzle 2 into sucking room 3 by introducing, under main fluid drive
While flowing to trunnion section 5, the outer lug boss 8 of segment fluid flow and 7 outer wall of nozzle forms outer return guide trough into reverse deflection, finally
Fluid is made to collide with main fluid, and generates and divides in mixed flow moment, layering, mixing is crossed over many times and reaches rapid, uniform
Ground is spread in entire fluid, realizes that mixing efficiency improves.Main fluid in the nozzle 7 to trunnion 5 flow at high speed of section when, due to interior
The stickiness that boss 9 makes the flow direction of segment fluid flow deflect between fluid causes shearing force that energy, momentum is brought to transfer, and makes
Part edge side main fluid generates pulsation, and the automatic fine tuning stream under hydraulic action when being sprayed by alveolus 9 within the specific limits
To mixed effect is strengthened, increase flow-disturbing effect, achieved the purpose that efficient mixing.Composite rate is up to more than 90%-95%.
The utility model by main fluid and introduce fluid boundary a fluid stream change realize shunting, layering, cross-mixing,
It is finally reached the purpose rapidly and efficiently mixed.Former mixer nozzle need to be only replaced in having venturi mixer with regard to energy
Realize efficiently mixing purpose.It is easy to operate understandable with simple in structure, it can be used under without mechanical dynamic environment and dirty without environment
Dye.Mixing apparatus investment cost can be reduced after implementation and improves mixing efficiency.
Claims (8)
1. a kind of venturi mixer nozzle, which is characterized in that the outer wall of nozzle (7) is equipped with several outer lug boss (8), each
Outer lug boss (8) in the shape of a spiral, the port of export of nozzle (7), the spiral shell of several outer lug boss (8) is extended to by the input end of nozzle (7)
It curls up to identical;The inner wall of nozzle (7) be equipped with several inner convex platforms (9), each inner convex platform (9) in the shape of a spiral, by nozzle (7)
Input end extend to the ports of export of nozzle (7), the spiral windings of several inner convex platforms (9) is to identical;Inner convex platform (9) and outer lug boss
(8) spiral winding is to opposite.
2. venturi mixer nozzle according to claim 1, which is characterized in that the quantity of outer lug boss (8) be two, two
Outer lug boss (8) is symmetrical arranged along the circumferential direction of nozzle (7).
3. venturi mixer nozzle according to claim 1, which is characterized in that the quantity of inner convex platform (9) be four, four
Inner convex platform (9) is uniformly distributed along the circumferential direction of nozzle (7).
4. venturi mixer nozzle according to claim 1, which is characterized in that the port of export and inner convex platform of nozzle (7)
(9) intersection is equipped with alveolus (10).
5. venturi mixer nozzle according to claim 4, which is characterized in that the port of export and each of nozzle (7)
The intersection of inner convex platform (9) is equipped with alveolus (10).
6. venturi mixer nozzle according to claim 1, which is characterized in that outside the straight pipe of nozzle (7) input end
Wall is equipped with screw thread.
7. one kind has the venturi mixer of the nozzle (7) described in claim 1-6 any one, which is characterized in that nozzle
(7) input end and the sucking room (3) of venturi mixer is connected through a screw thread.
8. venturi mixer according to claim 7, which is characterized in that the external screw thread of nozzle (7) input end outer wall
(11) it is connected with sucking the internal thread (12) of room (3) inner wall.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201721368407.5U CN207446008U (en) | 2017-10-23 | 2017-10-23 | A kind of venturi mixer nozzle and venturi mixer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201721368407.5U CN207446008U (en) | 2017-10-23 | 2017-10-23 | A kind of venturi mixer nozzle and venturi mixer |
Publications (1)
Publication Number | Publication Date |
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CN207446008U true CN207446008U (en) | 2018-06-05 |
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ID=62281125
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CN201721368407.5U Active CN207446008U (en) | 2017-10-23 | 2017-10-23 | A kind of venturi mixer nozzle and venturi mixer |
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CN (1) | CN207446008U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111714676A (en) * | 2020-04-30 | 2020-09-29 | 武汉大学 | Movable air sterilizing device |
-
2017
- 2017-10-23 CN CN201721368407.5U patent/CN207446008U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111714676A (en) * | 2020-04-30 | 2020-09-29 | 武汉大学 | Movable air sterilizing device |
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