CN109173765A - A kind of mixed method of different pressures fluid - Google Patents
A kind of mixed method of different pressures fluid Download PDFInfo
- Publication number
- CN109173765A CN109173765A CN201811257444.8A CN201811257444A CN109173765A CN 109173765 A CN109173765 A CN 109173765A CN 201811257444 A CN201811257444 A CN 201811257444A CN 109173765 A CN109173765 A CN 109173765A
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- fluid
- mixing
- pipeline
- pressure
- mixed
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
- B01F25/3123—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements
- B01F25/31233—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements used successively
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
Abstract
The invention discloses a kind of mixed methods of different pressures fluid, it is shunted by the fluid to high discharge pressure, shunting is allowed successively to be mixed with the fluid of low first class pressure, gradually reduce the pressure difference between high pressure fluid and low-pressure fluid, achieve the purpose that mix different pressures difference fluid gradually, its method is simply applicable in, is easily operated, the different fluid of high pressure differential and high flow capacity difference can be made, which to be sufficiently mixed, uniformly can be widely used in the various experimental studies or production for needing to carry out fluid mixing.
Description
Technical field
The present invention relates to fluid mixing techniques field, especially a kind of mixed method of different pressures fluid.
Background technique
It includes isolating state, non-isolated state and part isolation state completely that different fluid, which carries out mixed admixture, no matter
No matter which kind of admixture is conveyed all when the discharge pressure between mixed fluid has big difference using pump conveying or gravity
The mixing that will lead between fluid is extremely uneven, can cause adverse effect to the use of subsequent fluid-mixing.
Summary of the invention
The technical problems to be solved by the present invention are: providing a kind of mixed method of different pressures fluid, can make different defeated
It is uniformly mixed between the fluid of pressurization pressure.
To solve above-mentioned technical problem the technical scheme adopted by the invention is that: a kind of mixing side of different pressures fluid
Method, comprising the following steps:
A, multiple fluid pressing force height to be mixed is ranked up, first the progress highest first order fluid of pressure with
The mixing of the high second level fluid of pressure second;
B, first order fluid is shunted, the series of shunting is according to the pressure between first order fluid and second level fluid
Difference is allocated, and series is at least 2 grades;
C, the pipeline with multiple branch pipes is taken, the shunting of first order fluid is passed through pipeline from the entrance of pipeline, and according to
It is secondary that the remaining shunting of second level fluid and first order fluid is each led into pipeline from each branch pipe;
D, the fluid-mixing flowed out from pipe outlet is subjected to the mixing with third level fluid, subsequent progress by above-mentioned steps
With the mixing between remaining fluid.
Further, the inner cavity of the pipeline is the Venturi tube being connected.
Further, the shunting series in step b is 2~6 grades.
The beneficial effects of the present invention are: the present invention is shunted by the fluid to high discharge pressure, allow shunting successively with
The fluid of low first class pressure is mixed, and gradually reduces the pressure difference between high pressure fluid and low-pressure fluid, reaching makes not
With the purpose that pressure difference fluid gradually mixes, method is simply applicable in, is easily operated, can make high pressure differential and high flow capacity difference not
Being sufficiently mixed with fluid uniformly can be widely used in the various experimental studies or production for needing to carry out fluid mixing.
Detailed description of the invention
Fig. 1 is mixture length schematic diagram of the invention.
Specific embodiment
To facilitate the understanding of the present invention, the present invention is further detailed with reference to the accompanying drawings and embodiments.
Embodiment 1
As shown in Figure 1, being mixed to the fluid of fluid a, fluid b and tri- kinds of fluid c different discharge pressures, first by three
Kind fluid sorts by the height of discharge pressure, is followed successively by fluid a, fluid b, fluid c.Fluid a is shunted, split into a1,
A2, a3, a4 will shunt a1 and from the entrance of pipeline be passed through pipeline, fluid b is passed through pipeline from first branch pipe of pipeline, allow point
Stream a1 is mixed with fluid b progress first time, then will be shunted a2 from second branch pipe of pipeline and is passed through pipeline, and allow and shunt a1 and stream
The fluid-mixing of body b carries out second of mixing with a2 is shunted, and then successively carries out fluid-mixing and shunts a3, shunts mixing for a4
It closes, finally obtains the fluid-mixing i.e. fluid-mixing ab of fluid a Yu fluid b.Followed by the mixed of fluid-mixing ab and fluid c
It closes, fluid-mixing ab is shunted, ab1, ab2, ab3, ab4, ab5 are split into, mixing is shunted into ab1 and is led to from the entrance of pipeline
Enter pipeline, fluid c be passed through pipeline from first branch pipe of pipeline, allows mixing to shunt ab1 and mixed with fluid c progress first time,
Then mixing is shunted into ab2 and is passed through pipeline from second branch pipe of pipeline, the fluid-mixing for allowing mixing to shunt ab1 and fluid c is same
Mixing, which shunts ab2 and carries out second, to be mixed, and is then successively carried out fluid-mixing and is shunted ab3, mixing shunting ab4, mixes with mix
The mixing for shunting ab5, finally obtains the fluid-mixing after fluid a, fluid b and fluid c are sufficiently mixed.
It present invention can be suitably applied to the mixing between the fluid of a variety of different discharge pressures, be suitable for pressure difference 20~200
The mixing of fluid between times, the channel mixed using Venturi tube as fluid, the resistance generated to fluid is small, Venturi tube
Diffuser can make different fluid gradually slow down upon mixing, reduce the mixed pressure loss of fluid, guarantee different pressures difference stream
Body mixes uniform.
Claims (3)
1. a kind of mixed method of different pressures fluid, it is characterised in that: the following steps are included:
A, multiple fluid to be mixed is ranked up by discharge pressure height, first the progress highest first order stream of discharge pressure
The mixing of body and the high second level fluid of pressure second;
B, first order fluid is shunted, the series of shunting according to the pressure difference between first order fluid and second level fluid into
Row distribution, series are at least 2 grades;
C, the pipeline with multiple branch pipes is taken, the shunting of first order fluid is passed through pipeline from the entrance of pipeline, and successively will
Second level fluid and remaining shunt from each branch pipe of first order fluid each lead into pipeline;
D, the fluid-mixing flowed out from pipe outlet is subjected to the mixing with third level fluid by above-mentioned steps, it is subsequent to carry out and remain
Mixing between lower fluid.
2. a kind of mixed method of different pressures fluid as described in claim 1, it is characterised in that: the inner cavity of the pipeline is
The Venturi tube being connected.
3. a kind of mixed method of different pressures fluid as described in claim 1, it is characterised in that: the shunting grade in step b
Number is 2~6 grades.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201811257444.8A CN109173765A (en) | 2018-10-26 | 2018-10-26 | A kind of mixed method of different pressures fluid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201811257444.8A CN109173765A (en) | 2018-10-26 | 2018-10-26 | A kind of mixed method of different pressures fluid |
Publications (1)
Publication Number | Publication Date |
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CN109173765A true CN109173765A (en) | 2019-01-11 |
Family
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Family Applications (1)
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CN201811257444.8A Pending CN109173765A (en) | 2018-10-26 | 2018-10-26 | A kind of mixed method of different pressures fluid |
Country Status (1)
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CN (1) | CN109173765A (en) |
Citations (9)
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---|---|---|---|---|
CN101091954A (en) * | 2007-04-18 | 2007-12-26 | 清华大学 | Distributing injection device for mixing liquid in flowing course |
WO2012013879A1 (en) * | 2010-07-29 | 2012-02-02 | Exel Industries | Direct-injection spraying device for a vehicle, in particular an agricultural vehicle, and vehicle provided with such a device |
CN103111212A (en) * | 2013-02-04 | 2013-05-22 | 西安交通大学 | Multi-point introduction structure and flow control mode of venturi mixer |
CN103664424A (en) * | 2013-09-26 | 2014-03-26 | 石家庄成功机电有限公司 | Emulsion method and equipment for emulsion explosive |
CN203695000U (en) * | 2013-12-23 | 2014-07-09 | 攀钢集团西昌钢钒有限公司 | Water adding device for sintering cylinder mixer |
CN204134486U (en) * | 2014-08-04 | 2015-02-04 | 江阴市华能电热器材有限公司 | Jet rotary dispenser |
CN106621881A (en) * | 2010-03-10 | 2017-05-10 | 芬兰温德造纸湿部技术公司 | A method and apparatus for mixing various flows into a process liquid flow |
CN107388040A (en) * | 2017-09-04 | 2017-11-24 | 中煤(天津)洗选科技有限公司 | The pulp conveying device on preparation equipment |
CN108636154A (en) * | 2018-04-28 | 2018-10-12 | 佛山市高明区杨和金属材料专业镇技术创新中心 | A kind of venturi mixer |
-
2018
- 2018-10-26 CN CN201811257444.8A patent/CN109173765A/en active Pending
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101091954A (en) * | 2007-04-18 | 2007-12-26 | 清华大学 | Distributing injection device for mixing liquid in flowing course |
CN106621881A (en) * | 2010-03-10 | 2017-05-10 | 芬兰温德造纸湿部技术公司 | A method and apparatus for mixing various flows into a process liquid flow |
WO2012013879A1 (en) * | 2010-07-29 | 2012-02-02 | Exel Industries | Direct-injection spraying device for a vehicle, in particular an agricultural vehicle, and vehicle provided with such a device |
CN103111212A (en) * | 2013-02-04 | 2013-05-22 | 西安交通大学 | Multi-point introduction structure and flow control mode of venturi mixer |
CN103664424A (en) * | 2013-09-26 | 2014-03-26 | 石家庄成功机电有限公司 | Emulsion method and equipment for emulsion explosive |
CN203695000U (en) * | 2013-12-23 | 2014-07-09 | 攀钢集团西昌钢钒有限公司 | Water adding device for sintering cylinder mixer |
CN204134486U (en) * | 2014-08-04 | 2015-02-04 | 江阴市华能电热器材有限公司 | Jet rotary dispenser |
CN107388040A (en) * | 2017-09-04 | 2017-11-24 | 中煤(天津)洗选科技有限公司 | The pulp conveying device on preparation equipment |
CN108636154A (en) * | 2018-04-28 | 2018-10-12 | 佛山市高明区杨和金属材料专业镇技术创新中心 | A kind of venturi mixer |
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Title |
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P•埃里克•甘德森等: "《机敏问答 物理》", 31 January 2011, 上海:上海科学技术文献出版社 * |
李维礼主编: "《木材工业气力输送及场内运输机械 第2版》", 31 August 1993, 北京:中国林业出版社 * |
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Application publication date: 20190111 |