CN108854822A - A kind of combined type stirring system - Google Patents
A kind of combined type stirring system Download PDFInfo
- Publication number
- CN108854822A CN108854822A CN201811038214.2A CN201811038214A CN108854822A CN 108854822 A CN108854822 A CN 108854822A CN 201811038214 A CN201811038214 A CN 201811038214A CN 108854822 A CN108854822 A CN 108854822A
- Authority
- CN
- China
- Prior art keywords
- agitator tank
- circulation pump
- combined type
- type stirring
- stirring system
- 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 48
- 238000002156 mixing Methods 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims description 19
- 210000000867 larynx Anatomy 0.000 claims 1
- 239000012530 fluid Substances 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 4
- 238000010338 mechanical breakdown Methods 0.000 abstract description 3
- 230000008569 process Effects 0.000 abstract description 3
- 239000002131 composite material Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 239000007787 solid Substances 0.000 description 7
- 238000003860 storage Methods 0.000 description 5
- 239000000047 product Substances 0.000 description 4
- 239000006228 supernatant Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005669 field effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003758 nuclear fuel Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000007582 slurry-cast process Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000002604 ultrasonography Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
-
- 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
-
- 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
- B01F25/30—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
-
- 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
-
- 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
- B01F25/70—Spray-mixers, e.g. for mixing intersecting sheets of material
- B01F25/72—Spray-mixers, e.g. for mixing intersecting sheets of material with nozzles
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention discloses a kind of combined type stirring systems, including agitator tank, disc type fluidic system, central jet system, first circulation pump, second circulation pump.The stirring system provides power for the stirring of agitator tank, promotes the circulation hybrid motion in agitator tank between each fluid using first circulation pump and second circulation pump as power source, simultaneously, disc type fluidic system and central jet system are combined, easy to use, mixed effect is good.In addition, this composite structure realizes the rapid mixing between multi-fluid, work efficiency is high.Without dead angle, saving energy, the degree that homogenizes height in entire whipping process.And mechanical breakdown hidden danger existing for this system is few, and long service life, the later period is non-maintaining, save the cost, applied widely.
Description
Technical field
The present invention relates to suspensions to store mixing plant technical field, and in particular to a kind of combined type stirring system.
Background technique
Petrochemical industry production, nuclear fuel storage, high solid component coating storage, solid rocket propellant medicine slurry casting,
It detects a flaw in the industrial productions such as magnetic flaw detection ink allotment, aluminum oxide raw slurry allotment, often encounters what liquid was mixed with little particle
Products, this kind of product such as suspension, emulsion, petroleum crude oil, product oil high solid component coating largely belong to non newtonian liquid
Body.
Due to each component great disparity in mass of non-newtonian liquid, mixed with foreign liquid when density contrast great disparity, and liquid is viscous
Degree can be reduced with the raising of temperature, it is serious in storage layered phenomenon to be led to non-newtonian liquid, or even solid is caused to deposit, caused
Prevent it from accurately measuring or carrying out quality analysis, influences the measurement of product quality, quality dispute occurs.Moreover, solid deposits
The storage space of tank body can be reduced afterwards.
Therefore, the non-newtonian liquid raw material stored for a long time, which has to pass through, to homogenize again and can use, meanwhile, deposition
Solid is disturbed, and can effectively avoid the storage capacity decline of tank body.
Agitating mode common at present has following several：
Machinery rotation agitating mode, be suitable in, low-pressure vertical steel vessel, by stirring blade in mixed material fluid
Stirring is completed in middle rotation.The transmission parts that this mode needs to rely on are more, easily generation mechanical breakdown；Installation is complicated, service radius
Small, stirring dead angle area is big.
Air-flow homogeneous agitating mode is suitable for corrosive liquids and high temperature high pressure liquid, suitable for large scale equipment or constructs
Mechanical rotating stirring device is difficult to the occasion installed and used in object.By being generated to fluid by gas injection to fluid layer
Stirring action, or be distributed to gas behind fluid bottom and promotion liquid generation convection circulation is risen with high density state, to realize
Stirring.Which is unsuitable for high viscosity liquid, is unsuitable for easily producing the liquid of bubble, and require stirring air-flow that cannot send out with material
Biochemical reaction, applicable elements are limited.
Ultrasound field energy agitating mode, using the generating collision propagation characteristic of acoustic wavefield in a fluid come Accelerative mass transfer rate
(molecule is vibrated by audio frequency), primary efficacy are to accelerate chemical reaction rate, but application range is narrow；Regular dredging is needed,
Dredging and processing deposit are at high cost；In addition to main equipment, cost of labor, vulnerable part cost, operation expense, synthesis are also needed
Cost is high；And in replacement allotment medium as needed, there are medium pollutions.
Summary of the invention
The embodiment of the present invention is designed to provide a kind of combined type stirring system, to solve existing stirring system stirring
The low problem of low efficiency, the degree that homogenizes.
To achieve the above object, the embodiment of the present invention provides a kind of combined type stirring system, the combined type stirring system
Including：Agitator tank, disc type fluidic system, central jet system, first circulation pump, second circulation pump, the disc type fluidic system
The lower inside of the agitator tank is set, and the central jet system is located at the center of the agitator tank；The first circulation
The entrance of pump connects the inner cavity top of the agitator tank, and the outlet of the first circulation pump connects the first outlet tube and second simultaneously
Outlet tube, first outlet tube and the central jet system connectivity, second outlet tube and the disc type fluidic system
Connection；The entrance of the second circulation pump is connect with the inner cavity lower part of the agitator tank, the outlet of the second circulation pump and institute
State the connection of central jet system.
Preferably, the combined type stirring system further includes the first valve and the second valve, and the first valve setting exists
Between the outlet and first outlet tube of the first circulation pump, going out for the first circulation pump is arranged in second valve
Between mouth and second outlet tube.
Preferably, the disc type fluidic system includes disc type endless tube and nozzle, and the disc type endless tube is fixed on the stirring
The inner wall of tank is connect with second outlet tube, and the nozzle is connected to the disc type endless tube.
Preferably, the nozzle sum is 10~36.
Preferably, the longitudinal center line of the nozzle and level intersect 30 °~150 ° downwards.
Preferably, multiple, axis of multiple central jet systems along the agitator tank is arranged in the central jet system
The setting of line interval.
Preferably, the central jet system includes mixing chamber and jet stream arm, and the jet stream arm is connect with the mixing chamber,
The mixing chamber is connect with the outlet that first outlet tube and the second circulation pump.
Preferably, the jet stream arm uses Venturi throat structure.
Preferably, the combined type stirring system further includes barricade, and the barricade is fixed on the inner wall of the agitator tank
Portion forms feed liquor area, the entrance in the feed liquor area and first circulation pump between the barricade and the inner wall of the agitator tank
Connection.
The embodiment of the present invention has the following advantages that：
Combined type stirring system provided in an embodiment of the present invention includes：Agitator tank, disc type fluidic system, central jet system
System, first circulation pump, second circulation pump.Wherein, first circulation pump, second circulation pump are mentioned as the stirring that power source is agitator tank
For power, promote the circulation hybrid motion in agitator tank between each fluid.Disc type fluidic system or dish-style fluidic system, setting
In the lower inside of agitator tank, high-speed jet can produce, the solid at agitator tank bottom can be acted on biggish effluxvelocity
Deposit or compared with heavy suspension, emulsion, plays it clearly, is mixed after being switched to central jet stirring system.Center is penetrated
Stream stirring system is located at the center of agitator tank, can spray low speed, light fluid downwards, makes its heavy-fluid constantly with stirring pot bottom
Mixing is then stirred continuously by flow field effect and mixes more uniform so as to stir pot liquid.The embodiment of the present invention is by disk
Formula fluidic system is combined with central jet system, easy to install and use, good mixing effect；Composite structure realizes multithread
Rapid mixing between body, work efficiency is high；In entire whipping process without dead angle, energy saving, the degree that homogenizes height；And
Mechanical breakdown hidden danger is few, and long service life, the later period is non-maintaining, and save the cost is applied widely.
Detailed description of the invention
Fig. 1 is the structural schematic diagram for the combined type stirring system that the embodiment of the present invention 1 provides.
The structure top view of disc type fluidic system in the combined type stirring system that Fig. 2 provides for the embodiment of the present invention 1.
Disc type fluidic system and agitator tank part-structure in the combined type stirring system that Fig. 3 provides for the embodiment of the present invention 1
Longitudinal cross section schematic.
Wherein, 1- agitator tank, 2- disc type fluidic system, 21- disc type endless tube, 22- nozzle, 3- central jet system, 31- are mixed
Close chamber, 32- jet stream arm, 4- first circulation pump, 5- second circulation pump, the first outlet tube of 6-, the second outlet tube of 7-, the first valve of 8-
Door, 9 second valves, 10- barricade.
Specific embodiment
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, combined type stirring system provided in this embodiment includes：Agitator tank 1, disc type fluidic system 2,
Central jet system 3, first circulation pump 4, second circulation pump 5.The lower inside of agitator tank 1 is arranged in disc type fluidic system 2, in
Heart fluidic system 3 is located at the center of agitator tank 1.The inner cavity top of the entrance connection agitator tank 1 of first circulation pump 4, first circulation
The outlet of pump 4 connects the first outlet tube 6 simultaneously and the second outlet tube 7, the first outlet tube 6 are connected to central jet system 3, and second
Outlet tube 7 is connect with disc type fluidic system 2.The entrance of second circulation pump 5 is connect with the inner cavity lower part of agitator tank 1, second circulation
The outlet of pump 5 is connect with central jet system 3.
The first valve 8 is also set up between the outlet and the first outlet tube 6 of first circulation pump 4, in going out for first circulation pump 4
Second valve 9 is set between mouth and the second outlet tube 7.
Disc type fluidic system 2 includes disc type endless tube 21 and nozzle 22, and disc type endless tube 21 is fixed on the inner wall of agitator tank 1, water
Flat setting, connect with the second outlet tube 7, and nozzle 22 is connected to disc type endless tube 21, the longitudinal center line of nozzle 22 and level towards
Under intersect 30 °~150 °, in general, nozzle sum be 10~36.
Central jet system 3 includes mixing chamber 31 and jet stream arm 32, and jet stream arm 32 is connect with mixing chamber 31, mixing chamber 31 and
First outlet tube 6 is connected with the outlet of second circulation pump 5.Jet stream arm 32 uses Venturi throat structure.
Barricade 10 is fixedly installed in the upper inside wall of agitator tank 1, forms feed liquor between barricade 10 and the inner wall of agitator tank 1
Area, feed liquor area are connect with the entrance of first circulation pump 4.Barricade 10 is set and is effectively prevented from first circulation pump 4 in the process of suction
In influence the turbulent flow formed in agitator tank 1 so that it is more efficient to homogenize.
The course of work of combined type stirring system provided in this embodiment is：
The first valve 8 is opened, so that first circulation pump 4 is sent to the disc type of disc type fluidic system 2 after sucking supernatant
Endless tube 21 can cause high-speed jet via nozzle 22, and high-speed jet impact bottom settlings object simultaneously quickly makes liquid consolidate mixing, makes
Heavy liquid, which generates, in tank rises flowing.
The second valve 9 is opened, first circulation pump 4 is sent to the mixing chamber 31 of central jet system 3 after sucking supernatant,
It is sprayed with high-velocity fluid from jet stream arm 32, forms turbulent flow in agitator tank 1, meanwhile, negative pressuren zone is formed in mixing chamber 31, second follows
Tank bottom heavy-fluid is pumped to mixing chamber 31 and continues to mix by ring pump 5, is sprayed, is moved in circles by jet stream arm 32, realization homogenizes.
Combined type stirring system provided in this embodiment is stirred, disk at the initial stage of using mainly by disc type fluidic system 2
The structure of nozzle 22 on formula endless tube 21 is Venturi tube structure, can cause high-speed jet, the nozzle 22 on 1 disc type endless tube 21 can
It to stir the surrounding liquid of 4 times of volumes, while realizing impact bottom settlings object, accelerates liquid and mix admittedly, make the heavy in agitator tank 1
Liquid, which generates, rises flowing.Phase after use, start central jet stirring system 3, promotion supernatant is mixed with lower part heavy industry
It closes, guarantees the degree that homogenizes
Embodiment 2
The present embodiment and the combined type stir system design that embodiment 1 provides are essentially identical.In the present embodiment, center is penetrated
Streaming system setting is multiple, and multiple central jet systems are arranged along the axis interval 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 are fallen within the scope of the claimed invention.
Claims (9)
1. a kind of combined type stirring system, which is characterized in that the combined type stirring system includes：Agitator tank (1), disc type jet stream
System (2), central jet system (3), first circulation pump (4), second circulation pump (5), disc type fluidic system (2) setting exist
The lower inside of the agitator tank (1), the central jet system (3) are located at the center of the agitator tank (1)；Described first follows
The entrance that ring pumps (4) connects the inner cavity top of the agitator tank (1), and the outlet of the first circulation pump (4) connects first simultaneously
Outlet tube (6) and the second outlet tube (7), first outlet tube (6) are connected to the central jet system (3), and described second
Outlet tube (7) is connect with the disc type fluidic system (2)；The entrance of the second circulation pump (5) is interior with the agitator tank (1)
The outlet of the connection of chamber lower part, the second circulation pump (5) is connect with the central jet system (3).
2. combined type stirring system according to claim 1, which is characterized in that the combined type stirring system further includes
One valve (8) and the second valve (9), the first valve (8) setting is in the outlet and described first of first circulation pump (4)
Between outlet tube (6), outlet and second outlet tube (7) of the second valve (9) setting in first circulation pump (4)
Between.
3. combined type stirring system according to claim 1, which is characterized in that the disc type fluidic system (2) includes disk
Formula endless tube (21) and nozzle (22), the disc type endless tube (21) are fixed on the inner wall of the agitator tank (1) and described second and go out liquid
(7) connection is managed, the nozzle (22) is connected to the disc type endless tube (21).
4. combined type stirring system according to claim 3, which is characterized in that nozzle (22) sum is 10~36
It is a.
5. combined type stirring system according to claim 3, which is characterized in that the longitudinal center line of the nozzle (22) with
Level intersects 30 °~150 ° downwards.
6. combined type stirring system according to claim 1, which is characterized in that central jet system (3) setting is more
A, multiple central jet systems (3) are arranged along the axis interval of the agitator tank (1).
7. combined type stirring system according to claim 1, which is characterized in that the central jet system (3) includes mixed
Close chamber (31) and jet stream arm (32), the jet stream arm (32) connect with the mixing chamber (31), the mixing chamber (31) with it is described
First outlet tube (6) is connected with the outlet of second circulation pump (5).
8. combined type stirring system according to claim 7, which is characterized in that the jet stream arm (32) uses venturi larynx
Pipe structure.
9. combined type stirring system according to claim 1, which is characterized in that the combined type stirring system further includes gear
Wall (10), the barricade (10) are fixed on the upper inside wall of the agitator tank (1), the barricade (10) and the agitator tank (1)
Inner wall between form feed liquor area, the entrance that the feed liquor area pumps (4) with the first circulation connect.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811038214.2A CN108854822A (en) | 2018-09-06 | 2018-09-06 | A kind of combined type stirring system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811038214.2A CN108854822A (en) | 2018-09-06 | 2018-09-06 | A kind of combined type stirring system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108854822A true CN108854822A (en) | 2018-11-23 |
Family
ID=64323140
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811038214.2A Pending CN108854822A (en) | 2018-09-06 | 2018-09-06 | A kind of combined type stirring system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108854822A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109430217A (en) * | 2018-12-12 | 2019-03-08 | 济南大学 | A kind of spraying machine mixes medicine and medication delivery systems and method |
| CN109939575A (en) * | 2019-04-29 | 2019-06-28 | 河南卷烟工业烟草薄片有限公司 | A kind of powder polyacrylamide dissolver |
| CN113799253A (en) * | 2021-09-29 | 2021-12-17 | 青岛亿联建设集团股份有限公司 | Commercial concrete member forming device of prefabricated formula |
| CN115400642A (en) * | 2022-11-01 | 2022-11-29 | 联仕(昆山)化学材料有限公司 | Electronic grade negative photoresist developer solution configuration stirring equipment |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2253554A1 (en) * | 1996-05-03 | 1997-11-13 | Lindenport Sa | Method and device for liquefaction of sediments of thickened crude oil |
| CN101612535A (en) * | 2009-08-04 | 2009-12-30 | 上海巴斯夫聚氨酯有限公司 | Blending tank is provided with the dinitrotoluene (DNT) process units of ejector mixing |
| CN107158982A (en) * | 2017-06-15 | 2017-09-15 | 江苏金曼科技有限责任公司 | A kind of dissolver of indissoluble material |
| CN208771347U (en) * | 2018-09-06 | 2019-04-23 | 辽阳博仕流体设备有限公司 | A kind of combined type stirring system |
-
2018
- 2018-09-06 CN CN201811038214.2A patent/CN108854822A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CA2253554A1 (en) * | 1996-05-03 | 1997-11-13 | Lindenport Sa | Method and device for liquefaction of sediments of thickened crude oil |
| CN101612535A (en) * | 2009-08-04 | 2009-12-30 | 上海巴斯夫聚氨酯有限公司 | Blending tank is provided with the dinitrotoluene (DNT) process units of ejector mixing |
| CN107158982A (en) * | 2017-06-15 | 2017-09-15 | 江苏金曼科技有限责任公司 | A kind of dissolver of indissoluble material |
| CN208771347U (en) * | 2018-09-06 | 2019-04-23 | 辽阳博仕流体设备有限公司 | A kind of combined type stirring system |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109430217A (en) * | 2018-12-12 | 2019-03-08 | 济南大学 | A kind of spraying machine mixes medicine and medication delivery systems and method |
| CN109430217B (en) * | 2018-12-12 | 2024-05-14 | 山东博胜动力科技股份有限公司 | Spraying machine medicine mixing and supplying system and method |
| CN109939575A (en) * | 2019-04-29 | 2019-06-28 | 河南卷烟工业烟草薄片有限公司 | A kind of powder polyacrylamide dissolver |
| CN113799253A (en) * | 2021-09-29 | 2021-12-17 | 青岛亿联建设集团股份有限公司 | Commercial concrete member forming device of prefabricated formula |
| CN115400642A (en) * | 2022-11-01 | 2022-11-29 | 联仕(昆山)化学材料有限公司 | Electronic grade negative photoresist developer solution configuration stirring equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108854822A (en) | A kind of combined type stirring system | |
| CN208771347U (en) | A kind of combined type stirring system | |
| US9446358B2 (en) | Process and apparatus of mixing a fluid within a vessel | |
| CN109821435B (en) | Hydrodynamic cavitation device for preparing blending lubricating oil through oil-water mixing | |
| CN108325462A (en) | A kind of agitating device that efficient mechanical agitation is combined with air agitation | |
| CN209771868U (en) | Stirrer and stirring device | |
| CN105688729B (en) | The three-level mixing device of hydrodynamics automatic control | |
| RU171497U1 (en) | Jet mixing device | |
| CN214389658U (en) | Liquid jet mixer | |
| US8596857B2 (en) | Means and method for mixing a particulate material and a liquid | |
| CN208260682U (en) | A kind of agitating device of efficient mechanical stirring in conjunction with air agitation | |
| US20090316518A1 (en) | Vertical mixing tank | |
| CN208771231U (en) | A kind of thermally conductive stirring system | |
| CN210645920U (en) | Fluid stirring device | |
| CN204395875U (en) | A kind of ultrasonic vibration agitating device | |
| RU172010U1 (en) | Jet mixing device | |
| CN109142119B (en) | Device for testing abrasion resistance and cavitation erosion resistance of material | |
| CN107649063B (en) | Nanometer material ultrasonic resonance emulsification blending device | |
| CN108786511A (en) | A kind of heat conduction stirring system | |
| CN203043913U (en) | Air stirring device | |
| RU2782587C1 (en) | Mixing liquid device | |
| CN106754288B (en) | Anaerobic digester and its stir process method | |
| CN217473354U (en) | Nano solid particle oil displacement agent blending device | |
| CN218516487U (en) | Calcium silicate board powder raw material stirring device | |
| CN220697647U (en) | Small solid particle cleaning equipment adhered with soil |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 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: 20181123 |
|
| RJ01 | Rejection of invention patent application after publication |