CN108745021A - A kind of mixing and stirring system - Google Patents
A kind of mixing and stirring system Download PDFInfo
- Publication number
- CN108745021A CN108745021A CN201811039032.7A CN201811039032A CN108745021A CN 108745021 A CN108745021 A CN 108745021A CN 201811039032 A CN201811039032 A CN 201811039032A CN 108745021 A CN108745021 A CN 108745021A
- Authority
- CN
- China
- Prior art keywords
- mixing
- stirring system
- agitator tank
- stirring
- mixing chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000003756 stirring Methods 0.000 title claims abstract description 38
- 238000005213 imbibition Methods 0.000 claims abstract description 26
- 238000005183 dynamical system Methods 0.000 claims abstract description 16
- 239000012530 fluid Substances 0.000 claims description 18
- 239000007921 spray Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 description 16
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- 238000013019 agitation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000000149 chemical water pollutant Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Classifications
-
- 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
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
- B01F25/21—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
-
- 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
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/51—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
-
- 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
- B01F2025/91—Direction of flow or arrangement of feed and discharge openings
- B01F2025/919—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
Abstract
The invention discloses a kind of mixing and stirring system, including agitator tank, dynamical system, imbibition disk, pipette and jet mixer, the jet mixer includes the mixing chamber being connected with each other and jet stream arm；The dynamical system is connected to the inner cavity lower part of the agitator tank, while connecting the mixing chamber；The imbibition disk is located at the inner cavity top of the agitator tank, and the top of the mixing chamber is connected to by the pipette, and the side wall of the imbibition disk is arranged several imbibing holes, block-resistant lid is arranged above the imbibition disk.The mixing and stirring system is easy to operate, using flexible, work efficiency is high, in operation process without dead angle, stirring service radius is big, long lifespan, applied widely.
Description
Technical field
The present invention relates to materials, and equipment technical field is mixed, and in particular to a kind of mixing and stirring system.
Background technology
Currently, either in petroleum chemical industry, dyeing textile industry, deep processing industry, Fermentation Engineering industry, pharmacy industry
Or during in municipal wastewater processing procedure, landfill leachate, the mixing that can be all related to different material is used.However,
Each component density is different in mixed solution and molecule extension is weaker, is stirred even with allotment, after standing a period of time,
Mixed solution will appear lamination, the needs being unable to meet production.It then becomes necessary to it is sufficiently stirred, is mixed, it is real
It now homogenizes, to meet needed for production.
Moreover sometimes according to the needs of production, two kinds of (a variety of) liquid must reach in a short period of time homogenizes,
When the liquid that storage tank is multiplied it is sufficiently bulky when, this requires mixing and stirring systems extremely strong processing capacity.
There are many conventional stirring mixing method, such as the stirring of mechanical agitation, laser, neat liquid jet mixing etc..Wherein,
Laser stirring, neat liquid jet mixing require solute, smaller scope of application；Mechanical agitation is by blender in stirred tank
Middle rotation is stirred liquid, but this mode by mixing plant because its structure design is unreasonable, dead angle is more, often
Phenomena such as will appear stirring uneven, wall built-up, this has been resulted in, and working efficiency is low and the wasting of resources, while having an effect on the matter of product
Amount.
There are more drawbacks for the current mode that is stirred, and can not fully meet industrial requirement.Therefore, it is necessary to a variety of
The mixing equipment of material carries out further technological innovation.
Invention content
The embodiment of the present invention is designed to provide a kind of mixing and stirring system, to solve existing mixing equipment work
Make that efficiency is low, easily causes the wasting of resources, is difficult to realize the problem of suspension homogenizes.
To achieve the above object, the embodiment of the present invention provides a kind of mixing and stirring system, and the mixing and stirring system includes
Agitator tank, dynamical system, imbibition disk, pipette and jet mixer, the jet mixer include the mixing chamber being connected with each other
And jet stream arm；The dynamical system is connected to the inner cavity lower part of the agitator tank, while connecting the mixing chamber；The imbibition disk
Positioned at the inner cavity top of the agitator tank, the top of the mixing chamber, the side of the imbibition disk are connected to by the pipette
Several imbibing holes are arranged in wall, and block-resistant lid is arranged above the imbibition disk.
Preferably, the dynamical system includes circulating pump, inlet tube and outlet tube, is provided in the lower part of the agitator tank
The fluid hole is connect by fluid apertures and inlet opening, the inlet tube with the entrance of the circulating pump, and the outlet tube passes through described
The outlet of the circulating pump is connect by inlet opening with the mixing chamber.
Preferably, in the agitator tank tank base, the inlet opening is arranged in the agitator tank for the fluid hole setting
The lower sidewall of tank body.
Preferably, the mixing and stirring system further includes feed inlet and discharge port, and the inlet port and outlet port are respectively provided with
In the agitator tank tank wall.
Preferably, the outer diameter of the imbibition disk becomes larger from the bottom to top, is in Open architecture.
Preferably, the jet stream arm includes pipe arm and nozzle, and the nozzle is arranged in the end of the pipe arm.
Preferably, the pipe arm uses Venturi throat structure.
Preferably, the mixing and stirring system includes several jet stream arms, during several jet stream arms are with the mixing chamber
The heart extends downwardly setting outward.
The embodiment of the present invention has the following advantages that：Mixing and stirring system provided in an embodiment of the present invention, including it is agitator tank, dynamic
Force system, imbibition disk, pipette and jet mixer, jet mixer include the mixing chamber being connected with each other and jet stream arm.Power
System provides power for lower liquid in agitator tank, feeds them into mixing chamber, and supernatant liquid is sucked mixing chamber by imbibition disk, in turn
Realize being sufficiently mixed between upper layer, lower liquid.Meanwhile the mixed liquor in mixing chamber is constantly injected into from jet stream arm high speed
Enter agitator tank inner cavity, forms turbulent flow in tank, therefore accelerate homogenizing for pot liquid, work efficiency is high.
In addition, block-resistant lid is arranged above imbibition disk, to prevent whipping process imbibition blockage, job schedule is influenced, and
And reducing unnecessary system maintenance process, service life is long.
Mixing and stirring system provided in an embodiment of the present invention by mutually impacting between each layer fluid, move in circles and realize
Pot liquid homogenizes, and is stirred fully, big without dead angle, stirring service radius in operation process, economizes on resources.
The embodiment of the present invention also has many advantages, such as easy to operate, safe to use, applied widely.
Description of the drawings
Fig. 1 is the structural schematic diagram for the mixing and stirring system that the embodiment of the present invention 1 provides.
Fig. 2 is the enlarged diagram of the positions I in Fig. 1.
Fig. 3 is the vertical view of the positions I in Fig. 1.
Wherein, 1- agitator tanks, 11- fluid holes, 12- inlet openings, 2- dynamical systems, 21- circulating pumps, 22- inlet tubes, 23-
Outlet tube, 3- imbibitions disk, 4- pipette, 5- jet mixers, 51- mixing chambers, 52- jet streams arm, 6- block-resistant lids.
Specific implementation mode
The following examples are used to illustrate the present invention, but are not intended to limit the scope of the present invention..
Embodiment 1
As shown in Figure 1, 2, 3, mixing and stirring system provided in this embodiment includes agitator tank 1, dynamical system 2, imbibition disk
3, pipette 4 and jet mixer 5, jet mixer 5 include the mixing chamber 51 being connected with each other and jet stream arm 52.
Dynamical system 2 is connected to the inner cavity lower part of agitator tank 1, while connecting mixing chamber 51.Imbibition disk 3 is located at agitator tank 1
Inner cavity top, the top of mixing chamber 51 is connected to by pipette 4, the outer diameter of imbibition disk 3 becomes larger from the bottom to top, in opening
Put formula structure, several imbibing holes are arranged in side wall, and block-resistant lid 6 is arranged above it, and imbibing hole is avoided to be blocked, influence mixed flow into
Degree.
Jet stream arm 5 includes pipe arm and nozzle, and nozzle is arranged in the end of pipe arm.Pipe arm uses Venturi throat structure.It penetrates
Several are arranged in stream arm, and several jet stream arms extend downwardly setting outward centered on mixing chamber, and to reach, mixed flow is uniform, nothing is dead
Angle.
The operation principle of mixing and stirring system provided in this embodiment is：Lower liquid in agitator tank 1 is by dynamical system 2
It is entered in mixing chamber 51 as high speed motive force fluid after suction pressurization.High speed motive force fluid is via the pipe arm of jet stream arm 5 and spray
Mouth is ejected with very high speed, forms one jet beam, according to venturi principle, the rapid shape around high-speed jet beam
At negative static pressure area, to generate suction-operated.At this point, supernatant liquid is drawn into mixing chamber 51 by imbibition disk 3.Due to upper layer
Fluid density is smaller, and supernatant liquid is broken into small micel by the high speed motive force fluid for coming from dynamical system 2, and then is made small
Micel is sufficiently mixed with high speed motive force fluid.The jet beam sprayed from nozzle is once again stirred the liquid in agitator tank 1,
Turbulent flow in tank is formed, the fast homogeneous of each layer fluid in tank is realized.In general, being using mixing provided in this embodiment
System can complete homogenizing for entire pot liquid in 15 minutes.
Embodiment 2
As shown in Figure 1, mixing and stirring system provided in this embodiment includes agitator tank 1, dynamical system 2, imbibition disk 3, inhales
Liquid pipe 4 and jet mixer 5, jet mixer 5 include the mixing chamber 51 being connected with each other and jet stream arm 52.
Dynamical system 2 is connected to the inner cavity lower part of agitator tank 1, while connecting mixing chamber 51.Dynamical system 2 includes circulating pump
21, fluid hole 11 and inlet opening 12 is arranged in the lower part of agitator tank 1 in inlet tube 22 and outlet tube 23, and the setting of fluid hole 11 is being stirred
The tank base of tank 1 is mixed, the lower sidewall in the tank body of agitator tank 1 is arranged in inlet opening 12.Inlet tube 22 by fluid hole 12 with follow
The entrance connection of ring pump 21, outlet tube 23 pass through inlet opening 12, the outlet of circulating pump 21 are connect with mixing chamber 51.
Imbibition disk 3 is located at the inner cavity top of agitator tank 1, and the top of mixing chamber 51, imbibition disk 3 are connected to by pipette 4
Outer diameter become larger from the bottom to top, be in Open architecture, several imbibing holes are arranged in side wall, and block-resistant lid 6 is arranged above it,
It avoids imbibing hole from being blocked, influences mixed flow progress.
Jet stream arm 52 includes pipe arm and nozzle, and nozzle is arranged in the end of pipe arm.Pipe arm uses Venturi throat structure.It penetrates
Several are arranged in stream arm, and several jet stream arms extend downwardly setting outward centered on mixing chamber, and to reach, mixed flow is uniform, nothing is dead
Angle.
Embodiment 3
Mixing and stirring system provided in this embodiment and the structure of embodiment 2 are essentially identical, and difference is only fluid hole
The tank base of agitator tank is arranged at inlet opening.
Embodiment 4
The present embodiment adds feed inlet and discharge port on the basis of the mixing and stirring system that embodiment 3 provides, feed inlet and
Discharge port is arranged at the tank wall of agitator tank.
Although above having used general explanation and specific embodiment, the present invention is described in detail, at this
On the basis of invention, it can be made some modifications or improvements, this will be apparent to those skilled in the art.Therefore,
These modifications or improvements without departing from theon the basis of the spirit of the present invention belong to the scope of protection of present invention.
Claims (8)
1. a kind of mixing and stirring system, which is characterized in that the mixing and stirring system include agitator tank (1), dynamical system (2),
Imbibition disk (3), pipette (4) and jet mixer (5), the jet mixer (5) include the mixing chamber (51) being connected with each other
And jet stream arm (52)；The dynamical system (2) is connected to the inner cavity lower part of the agitator tank (1), while connecting the mixing chamber
(51)；The imbibition disk (3) is located at the inner cavity top of the agitator tank (1), and the mixing is connected to by the pipette (4)
Several imbibing holes are arranged in the side wall of the top of chamber (51), the imbibition disk (3), and block-resistant lid is arranged above the imbibition disk (3)
(6)。
2. mixing and stirring system according to claim 1, which is characterized in that the dynamical system (2) includes circulating pump
(21), fluid hole and inlet opening, the feed liquor is arranged in the lower part of the agitator tank (1) in inlet tube (22) and outlet tube (23)
The fluid hole is connect by pipe (22) with the entrance of the circulating pump (21), the outlet tube (23), passes through the inlet opening, will
The outlet of the circulating pump (21) is connect with the mixing chamber (51).
3. mixing and stirring system according to claim 2, which is characterized in that the fluid hole (11) is arranged in the stirring
The lower sidewall in the stirring tank is arranged in tank bottom, the inlet opening (12).
4. mixing and stirring system according to claim 1, which is characterized in that the mixing and stirring system further includes feed inlet
With discharge port, the inlet port and outlet port are arranged at the agitator tank tank wall.
5. mixing and stirring system according to claim 1, which is characterized in that the outer diameter of the imbibition disk (3) is from the bottom to top
It becomes larger, is in Open architecture.
6. mixing and stirring system according to claim 1, which is characterized in that the jet stream arm (52) includes pipe arm and spray
Mouth, the nozzle are arranged in the end of the pipe arm.
7. mixing and stirring system according to claim 6, the pipe arm uses Venturi throat structure.
8. mixing and stirring system according to claim 1, which is characterized in that the mixing and stirring system includes several jet streams
Arm (52), several jet stream arms (52) extend downwardly setting outward centered on the mixing chamber (51).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811039032.7A CN108745021A (en) | 2018-09-06 | 2018-09-06 | A kind of mixing and stirring system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811039032.7A CN108745021A (en) | 2018-09-06 | 2018-09-06 | A kind of mixing and stirring system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108745021A true CN108745021A (en) | 2018-11-06 |
Family
ID=63968005
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811039032.7A Pending CN108745021A (en) | 2018-09-06 | 2018-09-06 | A kind of mixing and stirring system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108745021A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111668518A (en) * | 2020-06-09 | 2020-09-15 | 上海电气集团股份有限公司 | Homogeneous phase distributor, electrolyte storage tank and all-vanadium redox flow battery energy storage system |
| CN114452851A (en) * | 2021-12-13 | 2022-05-10 | 湖南成成油化科技股份有限公司 | Method for improving homogenization of rice bran oil soapstock |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203530035U (en) * | 2013-10-09 | 2014-04-09 | 南京德邦金属装备工程股份有限公司 | Jet aerator |
| CN103706319A (en) * | 2012-10-08 | 2014-04-09 | 中国石油化工集团公司 | Self-suction pipeline mixing reactor |
| CN205760704U (en) * | 2016-05-26 | 2016-12-07 | 江苏国松环境科技开发有限公司 | A kind of hydraulic agitation device |
| CN208771232U (en) * | 2018-09-06 | 2019-04-23 | 辽阳博仕流体设备有限公司 | A kind of mixing and stirring system |
-
2018
- 2018-09-06 CN CN201811039032.7A patent/CN108745021A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103706319A (en) * | 2012-10-08 | 2014-04-09 | 中国石油化工集团公司 | Self-suction pipeline mixing reactor |
| CN203530035U (en) * | 2013-10-09 | 2014-04-09 | 南京德邦金属装备工程股份有限公司 | Jet aerator |
| CN205760704U (en) * | 2016-05-26 | 2016-12-07 | 江苏国松环境科技开发有限公司 | A kind of hydraulic agitation device |
| CN208771232U (en) * | 2018-09-06 | 2019-04-23 | 辽阳博仕流体设备有限公司 | A kind of mixing and stirring system |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111668518A (en) * | 2020-06-09 | 2020-09-15 | 上海电气集团股份有限公司 | Homogeneous phase distributor, electrolyte storage tank and all-vanadium redox flow battery energy storage system |
| CN114452851A (en) * | 2021-12-13 | 2022-05-10 | 湖南成成油化科技股份有限公司 | Method for improving homogenization of rice bran oil soapstock |
| CN114452851B (en) * | 2021-12-13 | 2022-12-27 | 湖南成成油化科技股份有限公司 | Method for improving homogenization of rice bran oil soapstock |
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| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20181106 |