CN102500256A - Rotary jet mixer - Google Patents
Rotary jet mixer Download PDFInfo
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- CN102500256A CN102500256A CN2011103570450A CN201110357045A CN102500256A CN 102500256 A CN102500256 A CN 102500256A CN 2011103570450 A CN2011103570450 A CN 2011103570450A CN 201110357045 A CN201110357045 A CN 201110357045A CN 102500256 A CN102500256 A CN 102500256A
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Abstract
The invention discloses a rotary jet mixer, which comprises a high-pressure fluid inlet, a low-pressure fluid inlet and a mixed fluid outlet, wherein the high-pressure fluid inlet is communicated with a nozzle; an inlet of the nozzle is provided with a cyclone; the nozzle is arranged in a jet chamber; the jet chamber is communicated with an inlet of the low-pressure fluid inlet; the bottom of the jet chamber is provided with a drain outlet; an outlet of the nozzle is communicated with one end of a mixing chamber; the other end of the mixing chamber is communicated with one end of a diffusing chamber; and the other end of the diffusing chamber is communicated with a mixed fluid outlet. The rotary jet mixer has the advantages that: the cyclone which can freely rotate is additionally arranged at the inlet of the nozzle; when the high-pressure fluid flows by the cyclone, the cyclone is driven to rotate; the fluid is dispersed into a plurality of flows of fluids in different rotation directions and then is mixed with the ejected low-pressure fluid to achieve a full mixing effect; the dispersion degree is high, and the non-uniformity coefficient is less than 0.5 percent; and due to high-speed rotation of the cyclone, the port of the nozzle is not easily blocked, and the jet mixer can be used for high-viscosity gas-gas, gas-liquid and liquid-liquid mixing.
Description
Technical field
The present invention relates to blender, relate in particular to the rotary spray blender.
Background technology
Jet mixer is that the working fluid through high pressure quickens to expand through jet pipe, forms one low-pressure fluid in outside nozzle, and driven fluid is introduced mixing chamber, reaches the purpose of mixing.But jet mixer commonly used exists and mixes inequality, jet hole is prone to blocked shortcoming.Therefore, need provide a kind of new technical scheme to solve the problems referred to above.
Summary of the invention
The purpose of this invention is to provide the rotary spray blender that a kind of jet hole is difficult for obstruction, good mixing effect.
The technical scheme that the present invention adopts:
The rotary spray blender comprises high-pressure fluid inlet, low-pressure fluid inlet and fluid-mixing outlet, and said high-pressure fluid inlet is communicated with nozzle; The porch of said nozzle is provided with eddy flow, and said nozzle places in the injecting chamber, and said injecting chamber is communicated with the low-pressure fluid inlet; Said injecting chamber bottom has sewage draining exit; The exit of said nozzle is communicated with mixing chamber one end, and the said mixing chamber other end is communicated with diffuser casing one end, and the said diffuser casing other end is communicated with the fluid-mixing outlet.
Beneficial effect of the present invention:
1, adds eddy flow that can rotate freely in the porch of nozzle; When the high-pressure fluid eddy flow period of the day from 11 p.m. to 1 a.m of flowing through, drive the rotation of eddy flow, fluid is dispersed into the fluid of countless bursts of different rotation directions; Mix again with by the low-pressure fluid of injection, reach well-mixed effect;
2, decentralization is high, and the unevenness coefficient is less than 0.5%;
3, because the high speed of eddy flow is rotated, jet hole is difficult for stopping up, and can be used for the mixing of full-bodied gas-gas, solution-air, liquid-liquid.
Description of drawings
Below in conjunction with the accompanying drawing and the specific embodiment the present invention is done further explain.
Fig. 1 is a structural representation of the present invention.
Wherein, 1, high-pressure fluid inlet, 2, the low-pressure fluid inlet, 3, the fluid-mixing outlet, 4, sewage draining exit, 5, nozzle, 6, eddy flow, 7, injecting chamber, 8, mixing chamber, 9, diffuser casing, 10, jet pipe.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment the present invention is described further.
As shown in Figure 1, rotary spray blender of the present invention comprises high-pressure fluid inlet 1, low-pressure fluid inlet 2 and fluid-mixing outlet 3; High-pressure fluid inlet 1 is communicated with nozzle 5, and it is sub 6 that the porch of nozzle 5 is provided with eddy flow, and nozzle 5 places in the injecting chamber 7; Injecting chamber 7 is communicated with low-pressure fluid inlet 2, and injecting chamber 7 bottoms have sewage draining exit 4, and the exit of nozzle 5 is communicated with mixing chamber 8 one ends; Mixing chamber 8 other ends are communicated with diffuser casing 9 one ends, and diffuser casing 9 other ends are communicated with fluid-mixing outlet 3.
The working fluid of high pressure quickens to expand through jet pipe 10, forms one low-pressure fluid in jet pipe 10 exits, and driven fluid is introduced mixing chamber 8, reaches the purpose of mixing, utilizes high-pressure fluid, drives 6 rotations of eddy flow, thereby reaches the purpose that mixes.
Add eddy flow 6 that can rotate freely in the porch of nozzle 5; When high-pressure fluid is flowed through eddy flow 6, drive 6 rotations of eddy flow, fluid is dispersed into the fluid of countless bursts of different rotation directions; Mix again with by the low-pressure fluid of injection, reach well-mixed effect; Decentralization is high, and the unevenness coefficient is less than 0.5%; Because the high speed rotation of eddy flow 6, jet hole is difficult for stopping up, and can be used for the mixing of full-bodied gas-gas, solution-air, liquid-liquid.
Claims (1)
1. rotary spray blender; Comprise high-pressure fluid inlet, low-pressure fluid inlet and fluid-mixing outlet, said high-pressure fluid inlet is communicated with nozzle, and it is characterized in that: the porch of said nozzle is provided with eddy flow; Said nozzle places in the injecting chamber; Said injecting chamber is communicated with the low-pressure fluid inlet, and said injecting chamber bottom has sewage draining exit, and the exit of said nozzle is communicated with mixing chamber one end; The said mixing chamber other end is communicated with diffuser casing one end, and the said diffuser casing other end is communicated with the fluid-mixing outlet.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2011103570450A CN102500256A (en) | 2011-11-11 | 2011-11-11 | Rotary jet mixer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2011103570450A CN102500256A (en) | 2011-11-11 | 2011-11-11 | Rotary jet mixer |
Publications (1)
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CN102500256A true CN102500256A (en) | 2012-06-20 |
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Family Applications (1)
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CN2011103570450A Pending CN102500256A (en) | 2011-11-11 | 2011-11-11 | Rotary jet mixer |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103510073A (en) * | 2013-09-28 | 2014-01-15 | 无锡荣能半导体材料有限公司 | Gas mixer |
CN108443239A (en) * | 2018-04-11 | 2018-08-24 | 大连理工大学 | A kind of multifunctional static induction apparatus |
CN108889150A (en) * | 2017-09-14 | 2018-11-27 | 华北电力大学 | A kind of emulsifier unit |
CN109931043A (en) * | 2019-04-22 | 2019-06-25 | 荆州市现代菲氏化工科技有限公司 | A kind of online filling apparatus and method of slippery water powder drag reducer |
CN111514702A (en) * | 2020-04-30 | 2020-08-11 | 武汉大学 | Mixer and separation type air purification device comprising same |
CN111677659A (en) * | 2020-06-12 | 2020-09-18 | 山东金燕自动化科技有限公司 | Automatic control system of unattended emulsion pump |
CN112221459A (en) * | 2020-10-14 | 2021-01-15 | 华东理工大学 | Polyether neutralization reactor |
CN113058759A (en) * | 2020-01-02 | 2021-07-02 | 杭州三花研究院有限公司 | Injection device |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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CN2316022Y (en) * | 1997-12-30 | 1999-04-28 | 曲文安 | Spray type flue gas desulfurization equipment |
US7029165B2 (en) * | 2001-10-26 | 2006-04-18 | Allen Thomas E | Automatically adjusting annular jet mixer |
CN201664585U (en) * | 2010-03-12 | 2010-12-08 | 重庆欣欣向荣精细化工有限公司 | Gas-liquid mixing ejector for ethyl vanillin oxidation tower |
CN202315728U (en) * | 2011-11-11 | 2012-07-11 | 南通申东冶金机械有限公司 | Rotary jet mixer |
-
2011
- 2011-11-11 CN CN2011103570450A patent/CN102500256A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN2316022Y (en) * | 1997-12-30 | 1999-04-28 | 曲文安 | Spray type flue gas desulfurization equipment |
US7029165B2 (en) * | 2001-10-26 | 2006-04-18 | Allen Thomas E | Automatically adjusting annular jet mixer |
CN201664585U (en) * | 2010-03-12 | 2010-12-08 | 重庆欣欣向荣精细化工有限公司 | Gas-liquid mixing ejector for ethyl vanillin oxidation tower |
CN202315728U (en) * | 2011-11-11 | 2012-07-11 | 南通申东冶金机械有限公司 | Rotary jet mixer |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103510073A (en) * | 2013-09-28 | 2014-01-15 | 无锡荣能半导体材料有限公司 | Gas mixer |
CN108889150A (en) * | 2017-09-14 | 2018-11-27 | 华北电力大学 | A kind of emulsifier unit |
CN108889150B (en) * | 2017-09-14 | 2023-04-18 | 华北电力大学 | Emulsifying device |
CN108443239B (en) * | 2018-04-11 | 2023-10-31 | 大连理工大学 | Multifunctional static injection device |
CN108443239A (en) * | 2018-04-11 | 2018-08-24 | 大连理工大学 | A kind of multifunctional static induction apparatus |
CN109931043A (en) * | 2019-04-22 | 2019-06-25 | 荆州市现代菲氏化工科技有限公司 | A kind of online filling apparatus and method of slippery water powder drag reducer |
CN109931043B (en) * | 2019-04-22 | 2024-01-30 | 荆州市现代菲氏化工科技有限公司 | Online filling device and method for powder drag reducer for slickwater |
CN113058759A (en) * | 2020-01-02 | 2021-07-02 | 杭州三花研究院有限公司 | Injection device |
CN111514702A (en) * | 2020-04-30 | 2020-08-11 | 武汉大学 | Mixer and separation type air purification device comprising same |
CN111677659A (en) * | 2020-06-12 | 2020-09-18 | 山东金燕自动化科技有限公司 | Automatic control system of unattended emulsion pump |
CN111677659B (en) * | 2020-06-12 | 2022-03-11 | 山东金燕自动化科技有限公司 | Automatic control system of unattended emulsion pump |
CN112221459A (en) * | 2020-10-14 | 2021-01-15 | 华东理工大学 | Polyether neutralization reactor |
CN112221459B (en) * | 2020-10-14 | 2022-07-22 | 华东理工大学 | Polyether neutralization reactor |
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Application publication date: 20120620 |