CN107617400A - High-speed stirred reactor - Google Patents
High-speed stirred reactor Download PDFInfo
- Publication number
- CN107617400A CN107617400A CN201711085430.8A CN201711085430A CN107617400A CN 107617400 A CN107617400 A CN 107617400A CN 201711085430 A CN201711085430 A CN 201711085430A CN 107617400 A CN107617400 A CN 107617400A
- Authority
- CN
- China
- Prior art keywords
- tank body
- cylinder
- component
- speed stirred
- stirred reactor
- 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
- 239000007788 liquid Substances 0.000 claims abstract description 70
- 238000002156 mixing Methods 0.000 claims abstract description 13
- 238000000926 separation method Methods 0.000 claims abstract description 11
- 238000003825 pressing Methods 0.000 claims abstract description 9
- 230000008878 coupling Effects 0.000 claims description 11
- 238000010168 coupling process Methods 0.000 claims description 11
- 238000005859 coupling reaction Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000010025 steaming Methods 0.000 claims description 3
- 238000003756 stirring Methods 0.000 description 11
- 238000013461 design Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 230000004048 modification Effects 0.000 description 7
- 238000012986 modification Methods 0.000 description 7
- 238000012423 maintenance Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000013019 agitation Methods 0.000 description 3
- 230000001174 ascending effect Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000003905 agrochemical Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005984 hydrogenation reaction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The present invention relates to a kind of high-speed stirred reactor, the high-speed stirred reactor includes tank body component, Power Component, heat-exchanging component, mixing component and guiding subassembly；The Power Component is arranged on above tank body component；The mixing component is arranged on tank body component internal, and top is connected with Power Component；The guiding subassembly is arranged in tank body, and the guiding subassembly includes cylinder pressing plate, cylinder lattice gear, cylinder stent, guide shell cylinder, spiral guide groove, diffluence pass and liquid separation cross；The cylinder stent is fixed in inner tank wall；The cylinder lattice gear is arranged on guide shell cylinder top；The cylinder pressing plate is used to cylinder lattice gear being fixed on cylinder stent；The spiral guide groove is arranged on guide shell inwall, and the diffluence pass hole-opening is protruded from outside barrel on guide shell barrel；The liquid separation cross is arranged in diffluence pass.
Description
Technical field
The present invention relates to a kind of high-speed stirred reactor, belong to chemical technology field.
Background technology
Reactor is processing apparatus important in industrial production, is matched somebody with somebody by the structure design to reactor container with parameter
Put, realize the mixture function of the heating of technological requirement, evaporation, cooling and low high speed.Reactor be widely used in oil, chemical industry,
The fields such as rubber, agricultural chemicals, dyestuff, medicine, food, it is mainly used to complete the works such as vulcanization, nitrification, hydrogenation, hydrocarbonylation, polymerization, condensation
The pressure vessel of skill process.Reactor, if rotating speed is too fast and when liquid viscosity to be mixed is relatively low, easily exists in agitated liquid
Column raceway zone is produced in kettle.The generation of column raceway zone, liquid is followed agitator closely in kettle and quickly rotate.It is but to be mixed
Due to the influence of centrifugal force caused by high speed rotation between two or more liquid, it will not produce to each other and cross and melt
Close, therefore by the operating efficiency of strong influence agitator.
The content of the invention
The present invention is exactly for technical problem present in prior art, there is provided a kind of high-speed stirred reactor, whole technical side
Case is compact-sized, cost is relatively low, energy-conserving and environment-protective, the technical scheme by brand-new Machine Design, make product stirring viscosity compared with
During low liquid, due to the presence of guide shell, will great increase liquid flowing resistance, so as to avoid the production of column raceway zone
It is raw, improve the stirring capacity and mixing effect of product.
To achieve these goals, technical scheme is as follows, a kind of high-speed stirred reactor, the high-speed stirred
Reactor includes tank body component, Power Component, heat-exchanging component, mixing component and guiding subassembly；The Power Component is arranged on tank
Above body component；The mixing component is arranged on tank body component internal, and top is connected with Power Component；The guiding subassembly installation
In tank body.The design structure is simply clear, is closely connected and does not influence each other between each component, and required part replacement is convenient,
It is easy to the maintenance of product in use in the future.
As a modification of the present invention, the tank body component include tank body, manhole, liquid outlet, inlet, relief valve and
Blow-off pipe；The manhole is arranged on tank body top left side；The inlet is located at tank body left upper portion；The liquid outlet is located at tank
Body bottom centre position；The relief valve is arranged on tank body top right side；The blow-off pipe is located at tank body top right side.Relief valve
Setting can effectively avoid because in tank body gas pressure it is excessive and caused by explode so that reactor is in whole production process
In it is more safe and efficient.
As a modification of the present invention, the Power Component includes motor, decelerator, support, shaft coupling and axle envelope；
The motor is arranged on the top of reactor and stood on the axis of tank body；The decelerator is arranged on motor bottom；
Motor is fixed at the top of tank body by the support；The shaft coupling is arranged on decelerator bottom, other end connection agitating shaft；Axle
Envelope is positioned at tank body and the contact position of agitating shaft.Power Component uses vertical layout, and motor reduces to technological requirement through decelerator
Speed of agitator after, then by shaft coupling drive agitating shaft rotate, so as to drive anchor impeller to rotate.Each part of Power Component it
Between be connected with each other and compact-sized.Whole power transmitting procedure high efficiency smooth, energy loss are low.Therefore it is highly suitable as reacting
The power source of kettle.
As a modification of the present invention, the heat-exchanging component includes steam inlet, chuck and condensation-water drain；The steaming
Vapor inlet is located at chuck upper end；The chuck is arranged on the outer wall both sides of tank body；The condensation-water drain is located at the bottom of chuck.
Heat-exchanging component is simply efficient, rapidly can lift or reduce temperature in the kettle.Chuck is arranged on the outside of tank body, can effectively be made
One stable temperature of holding of tank interior, it is more beneficial for the raising of Product Precision and gathers the accuracy of experimental data.
As a modification of the present invention, the steam inlet end is provided with steam filter screen.The setting of steam filter screen, can
Effectively to avoid debris from entering chuck with steam, so as to cause to be blocked inside chuck.Maintenance of clean-up band to post facility
To facilitate.
As a modification of the present invention, the stirrer paddle can be adjusted according to the difference of stirring thing physical characteristic,
It should be noted that the width of propeller-blade is should be noted that during installation, to avoid colliding between blade and guide shell.Different
It has different agitation characteristics to blade, reasonably using the physical property difference between different blades, liquid is reached suitable in kettle
Flow regime.So as to further lift the adaptability of product, the different production requirements being more applicable between enterprise are allowed to, more preferably
For market service.
As a modification of the present invention, the guiding subassembly includes cylinder pressing plate, cylinder lattice gear, cylinder stent, water conservancy diversion
Cylinder cylinder, spiral guide groove, diffluence pass and liquid separation cross；The cylinder stent is fixed in inner tank wall；The cylinder lattice
Gear is arranged on guide shell cylinder top；The cylinder pressing plate is used to cylinder lattice gear being fixed on cylinder stent；The spiral draws
Guide groove is arranged on guide shell inwall, and the diffluence pass hole-opening is protruded from outside barrel on guide shell barrel；Described point
Liquid cross is arranged in diffluence pass.The setting of guide shell can increase the resistance run into when liquid flows in kettle, reduce
The flowing velocity of liquid, so as to reduce the generation of column raceway zone.The design of diffluence pass, then make the liquid of rotation from fixed hole
Hole sprays, and enhances the main body Convention diffusion ability of liquid, increases the probability that liquid mutually merges, improve stirring for reactor
Mix efficiency.Liquid separation cross is located in diffluence pass, and when running at a high speed by the liquid of diffluence pass, cross is cut to four
The small-sized liquid stream of stock, and change the original flow direction of liquid stream, strengthen its ability axially and radially flowed, make the stirring of liquid
Effect is further enhanced.
As a modification of the present invention, the spiral guide groove helically rises shape on the inside of barrel, and internally carves
There is screw-pushing type decorative pattern.Spiral guide groove and the spiral promotion formula decorative pattern being carved with inside it, can play liquid in kettle
The effect of water conservancy diversion.The circulating path of liquid is not only limit, reduces short-circuit chance between liquid.Can more liquid be set to draw along cylinder
Ascending motion is done in guide groove direction, the further ability for improving liquid and being seethed up and down in kettle.So as to improve whole reactor
Mixing efficiency.
Relative and prior art, the invention has the advantages that, 1）The technical scheme overall construction design is ingenious, it is compact,
Cost is relatively low；2）The setting of relief valve can effectively avoid because in tank body gas pressure it is excessive and caused by explode so that instead
Answer kettle more safe and efficient in whole production process；3）Power Component uses vertical layout, and motor reduces to work through decelerator
After the speed of agitator of skill requirement, then by shaft coupling drive agitating shaft rotation, so as to drive anchor impeller to rotate.Power Component is each
It is connected with each other between part and compact-sized, whole power transmitting procedure high efficiency smooth, energy loss is low, therefore is especially suitable for using
Make the power source of reactor；4）Heat-exchanging component is simply efficient, rapidly can lift or reduce temperature in the kettle.Chuck is arranged on tank
External side, it can effectively make one stable temperature of holding of tank interior, be more beneficial for the raising and collection of Product Precision
The accuracy of experimental data；5）The setting of steam filter screen, it is possible to prevente effectively from debris enters chuck and heat(ing) coil with steam, from
And cause to block inside both.Maintenance of clean-up to post facility offers convenience；6）Different blades its have it is different
Agitation characteristics, reasonably using the physical property difference between different blades, liquid is set to reach suitable flow regime in kettle, so as to enter
One step lifts the adaptability of product, is allowed to the different production requirements being more applicable between enterprise, is preferably market service；7）Lead
The setting of flow cartridge can increase the resistance run into when liquid flows in kettle, the flowing velocity of liquid be reduced, so as to reduce post
The generation of shape raceway zone.The design of diffluence pass, then the liquid of rotation is sprayed from fixed hole, enhance the main body pair of liquid
Diffusivity is flowed, the probability that liquid mutually merges is increased, improves the stirring efficiency of reactor.Liquid separation cross is positioned at shunting
Intraoral, when running at a high speed by the liquid of diffluence pass, cross is cut to four bursts of small-sized liquid streams, and changes liquid stream original
The flow direction come, strengthens its ability axially and radially flowed, the mixing effect of liquid is further enhanced；8）Spiral
Guiding groove and the spiral promotion formula decorative pattern being carved with inside it, can play a part of liquid guide flow in kettle.It not only limit
The circulating path of liquid, reduce short-circuit chance between liquid.It liquid guiding groove direction along cylinder is done ascending motion, enter
The ability that the raising liquid of one step seethes up and down in kettle.So as to improve the mixing efficiency of whole reactor；9）This product structure is clear
It is clear, convenient disassembly between each part, be advantageous to the plant maintenance and replacing in later stage, reduce the later stage productive expenditure of enterprise；10）
The technical scheme cost is relatively low, just with further popularization and application.
Brief description of the drawings
Fig. 1 is overall structure diagram of the present invention；
Fig. 2 is partial structural diagram；
Fig. 3 is overlooking the structure diagram；
In figure：1st, tank body, 2, manhole, 3, liquid outlet, 4, inlet, 5, relief valve, 6, blow-off pipe, 7, motor, 8, decelerator,
9th, support, 10, shaft coupling, 11, axle envelope, 12, steam inlet, 13, chuck, 14, condensation-water drain,
15th, steam filter screen, 16, agitating shaft, 17, cylinder pressing plate, 18, cylinder lattice gear, 19, cylinder stent, 20, guide shell cylinder,
21st, spiral guide groove, 22, diffluence pass, 23, liquid separation cross, 24, bolt push type decorative pattern, 25, propeller agitator.
Embodiment：
In order to deepen the understanding of the present invention, the present embodiment is described in detail below in conjunction with the accompanying drawings.
Embodiment 1：Referring to Fig. 1-Fig. 3, a kind of high-speed stirred reactor, the high-speed stirred reactor includes tank body group
Part, Power Component, heat-exchanging component, mixing component and guiding subassembly；The Power Component is arranged on above tank body component；It is described to stir
Mix component and be arranged on tank body component internal, top is connected with Power Component；The guiding subassembly is arranged in tank body.The design knot
Structure is simply clear, is closely connected and does not influence each other between each component, and required part replacement is convenient, is easy to product in the future and is using
During maintenance；The tank body component includes tank body 1, manhole 2, liquid outlet 3, inlet 4, relief valve 5 and extruded
Pipe 6；The manhole is arranged on tank body top left side；The inlet is located at tank body left upper portion；The liquid outlet is located at tank body
Bottom centre position；The relief valve is arranged on tank body top right side；The blow-off pipe is located at tank body top right side.Relief valve
Setting can effectively avoid because in tank body gas pressure it is excessive and caused by explode so that reactor is in whole production process
More safe and efficient, the Power Component includes motor 7, decelerator 8, support 9, shaft coupling 10 and axle envelope 11；It is described electronic
Machine is arranged on the top of reactor and stood on the axis of tank body；The decelerator is arranged on motor bottom；The support
Motor is fixed at the top of tank body；The shaft coupling is arranged on decelerator bottom, other end connection agitating shaft；Axle envelope is located at tank
The contact position of body and agitating shaft.Power Component uses vertical layout, and the stirring that motor reduces to technological requirement through decelerator turns
After speed, then by shaft coupling drive agitating shaft rotation, so as to drive anchor impeller to rotate.Phase each other between each part of Power Component
It is even and compact-sized.Whole power transmitting procedure high efficiency smooth, energy loss are low.Therefore it is highly suitable as the power of reactor
Source, the heat-exchanging component include steam inlet 12, chuck and condensation-water drain；The steam inlet is located at chuck upper end；It is described
Chuck is arranged on the outer wall both sides of tank body；The condensation-water drain is located at the bottom of chuck.Heat-exchanging component is simply efficient, can be with fast
The lifting of speed reduces temperature in the kettle.Chuck is arranged on the outside of tank body, can effectively make one stabilization of holding of tank interior
Temperature, be more beneficial for Product Precision raising and gather experimental data accuracy, the steam inlet end is provided with steaming
Vapour filter screen 15.The setting of steam filter screen, it is possible to prevente effectively from debris enters chuck with steam, it is stifled so as to cause to occur inside chuck
Plug.Maintenance of clean-up to post facility is offered convenience, and the stirrer paddle can be adjusted according to the difference of stirring thing physical characteristic
It is whole, it should be noted that the width of propeller-blade to be should be noted that during installation, to avoid colliding between blade and guide shell.It is different
Blade its there is different agitation characteristics, reasonably using the physical property difference between different blades, liquid is reached suitable in kettle
Suitable flow regime.So as to further lift the adaptability of product, the different production requirements being more applicable between enterprise are allowed to, more
It is good for market service, the guiding subassembly include cylinder pressing plate 17, cylinder lattice gear 18, cylinder stent 19, guide shell cylinder 20,
Spiral guide groove 21, diffluence pass 22 and liquid separation cross 23；The cylinder stent is fixed in inner tank wall；The cylinder lattice gear
Installed in guide shell cylinder top；The cylinder pressing plate is used to cylinder lattice gear being fixed on cylinder stent；The spiral guiding
Groove is arranged on guide shell inwall, and the diffluence pass hole-opening is protruded from outside barrel on guide shell barrel；The liquid separation
Cross is arranged in diffluence pass.The setting of guide shell can increase the resistance run into when liquid flows in kettle, reduce liquid
The flowing velocity of body, so as to reduce the generation of column raceway zone.The design of diffluence pass, then make the liquid of rotation from fixed hole
Spray, enhance the main body Convention diffusion ability of liquid, increase the probability that liquid mutually merges, improve the stirring of reactor
Efficiency.Liquid separation cross is located in diffluence pass, and when running at a high speed by the liquid of diffluence pass, cross is cut to four strands
Small-sized liquid stream, and change the original flow direction of liquid stream, strengthen its ability axially and radially flowed, imitate the stirring of liquid
Fruit is further enhanced.The spiral guide groove helically rises shape on the inside of barrel, and is internally carved with screw-pushing type
Decorative pattern 24.Spiral guide groove and the spiral promotion formula decorative pattern being carved with inside it, can play a part of liquid guide flow in kettle.
The circulating path of liquid is not only limit, reduces short-circuit chance between liquid.Liquid guiding groove direction along cylinder can more done
Ascending motion, the further ability for improving liquid and being seethed up and down in kettle.So as to improve the mixing efficiency of whole reactor.
It should be noted that above-described embodiment, is not used for limiting protection scope of the present invention, in above-mentioned technical proposal
On the basis of made equivalents or replacement each fall within the scope that the claims in the present invention are protected.
Claims (6)
- A kind of 1. high-speed stirred reactor, it is characterised in that the high-speed stirred reactor include tank body component, Power Component, Heat-exchanging component, mixing component and guiding subassembly；The Power Component is arranged on above tank body component；The mixing component is arranged on Tank body component internal, top are connected with Power Component；The guiding subassembly is arranged in tank body, and the tank body component includes tank Body, manhole, liquid outlet, inlet, relief valve and blow-off pipe；The manhole is arranged on tank body top left side；The inlet position In tank body left upper portion；The liquid outlet is located at tank base center；The relief valve is arranged on tank body top right side；Institute State blow-off pipe and be located at tank body top right side, the Power Component includes motor, decelerator, support, shaft coupling and axle envelope；It is described Motor is arranged on the top of reactor and stood on the axis of tank body；The decelerator is arranged on motor bottom；It is described Motor is fixed at the top of tank body by support；The shaft coupling is arranged on decelerator bottom, other end connection agitating shaft；Axle envelope position In tank body and the contact position of agitating shaft；The guiding subassembly includes cylinder pressing plate, cylinder lattice gear, cylinder stent, guide shell cylinder Body, spiral guide groove, diffluence pass and liquid separation cross；The cylinder stent is fixed in inner tank wall；The cylinder lattice gear peace Mounted in guide shell cylinder top；The cylinder pressing plate is used to cylinder lattice gear being fixed on cylinder stent；The spiral guide groove It is arranged on guide shell inwall, the diffluence pass hole-opening is protruded from outside barrel on guide shell barrel；The liquid separation ten Cabinet frame is arranged in diffluence pass.
- 2. according to the high-speed stirred reactor described in claim 1, it is characterised in that the axle envelope uses built-in type balanced type Single mechanical end face seal.
- 3. according to the high-speed stirred reactor described in claim 2, it is characterised in that the heat-exchanging component enters including steam Mouth, chuck and condensation-water drain；The steam inlet is located at chuck upper end；The chuck is arranged on the outer wall both sides of tank body；Institute State the bottom that condensation-water drain is located at chuck.
- 4. according to the high-speed stirred reactor described in claim 3, it is characterised in that the steam inlet end is provided with steaming Vapour filter screen.
- 5. according to the high-speed stirred reactor described in claim 4, it is characterised in that the mixing component include agitating shaft and Propeller agitator；The agitating shaft top is connected in shaft coupling, and bottom is used to install propeller agitator.
- 6. according to the high-speed stirred reactor described in claim 5, it is characterised in that the spiral guide groove is on the inside of barrel Helically rise shape, and be internally carved with screw-pushing type decorative pattern.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711085430.8A CN107617400A (en) | 2017-11-07 | 2017-11-07 | High-speed stirred reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711085430.8A CN107617400A (en) | 2017-11-07 | 2017-11-07 | High-speed stirred reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107617400A true CN107617400A (en) | 2018-01-23 |
Family
ID=61093522
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711085430.8A Pending CN107617400A (en) | 2017-11-07 | 2017-11-07 | High-speed stirred reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107617400A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108607467A (en) * | 2018-05-04 | 2018-10-02 | 濮阳市盛源能源科技股份有限公司 | Axial-flow type stirred tank and petrochemical material processing unit (plant) |
| CN108654533A (en) * | 2018-05-18 | 2018-10-16 | 苏州市金翔钛设备有限公司 | The reaction kettle of water base titanium alloy cutting liquid |
| CN109173817A (en) * | 2018-10-16 | 2019-01-11 | 杭州电子科技大学 | The anti-precipitating liquid container of multiple activation |
| CN112742326A (en) * | 2020-12-21 | 2021-05-04 | 安徽国星生物化学有限公司 | Intelligent monitoring refining kettle for 2, 3-dichloropyridine synthesis |
| CN117619238A (en) * | 2023-12-01 | 2024-03-01 | 深圳市尚水智能股份有限公司 | Dispersion system |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201002005Y (en) * | 2007-01-25 | 2008-01-09 | 杨爱民 | Multi-stage stirring spraying type esterification reaction still |
| CN105126276A (en) * | 2015-09-11 | 2015-12-09 | 中国石油化工股份有限公司 | Foam generator with combined turbulence parts |
| CN206064243U (en) * | 2016-08-19 | 2017-04-05 | 湖北雪飞化工有限公司 | Water conservancy diversion confuses groove |
| CN207605719U (en) * | 2017-11-07 | 2018-07-13 | 盐城市大丰匀力机械制造厂 | High-speed stirred reaction kettle |
-
2017
- 2017-11-07 CN CN201711085430.8A patent/CN107617400A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201002005Y (en) * | 2007-01-25 | 2008-01-09 | 杨爱民 | Multi-stage stirring spraying type esterification reaction still |
| CN105126276A (en) * | 2015-09-11 | 2015-12-09 | 中国石油化工股份有限公司 | Foam generator with combined turbulence parts |
| CN206064243U (en) * | 2016-08-19 | 2017-04-05 | 湖北雪飞化工有限公司 | Water conservancy diversion confuses groove |
| CN207605719U (en) * | 2017-11-07 | 2018-07-13 | 盐城市大丰匀力机械制造厂 | High-speed stirred reaction kettle |
Non-Patent Citations (1)
| Title |
|---|
| 张朝升主编，高等教育出版社, 高等教育出版社 * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108607467A (en) * | 2018-05-04 | 2018-10-02 | 濮阳市盛源能源科技股份有限公司 | Axial-flow type stirred tank and petrochemical material processing unit (plant) |
| CN108654533A (en) * | 2018-05-18 | 2018-10-16 | 苏州市金翔钛设备有限公司 | The reaction kettle of water base titanium alloy cutting liquid |
| CN108654533B (en) * | 2018-05-18 | 2021-04-06 | 苏州市金翔钛设备有限公司 | Reaction kettle for water-based titanium alloy cutting fluid |
| CN109173817A (en) * | 2018-10-16 | 2019-01-11 | 杭州电子科技大学 | The anti-precipitating liquid container of multiple activation |
| CN112742326A (en) * | 2020-12-21 | 2021-05-04 | 安徽国星生物化学有限公司 | Intelligent monitoring refining kettle for 2, 3-dichloropyridine synthesis |
| CN117619238A (en) * | 2023-12-01 | 2024-03-01 | 深圳市尚水智能股份有限公司 | Dispersion system |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107617400A (en) | High-speed stirred reactor | |
| CN109200984B (en) | Reation kettle with dual heat dissipation function | |
| CN111330523A (en) | Synthetic reation kettle of resin | |
| CN109200983B (en) | Efficient reaction kettle capable of accelerating heat dissipation speed | |
| CN201832626U (en) | Self-priming gas-liquid reactor | |
| CN112240713A (en) | Cooling device for producing antirust water-based paint | |
| CN205386443U (en) | But reation kettle stirring rake of independent assortment | |
| CN205235960U (en) | Epoxy production is with two -way stirring reation kettle | |
| CN107617411A (en) | Low energy consumption reaction unit | |
| CN207605719U (en) | High-speed stirred reaction kettle | |
| CN109603720A (en) | Hypergravity oxidation reactor device and application | |
| CN114950312A (en) | Preparation device and method of industrial salicylic acid | |
| CN107638859A (en) | High-efficiency helical coil pipe reaction unit | |
| CN207605728U (en) | Multithread state reaction unit | |
| CN107626276A (en) | More fluidised form reaction units | |
| CN107617410A (en) | Highly effective reaction device | |
| CN111804257A (en) | Synthetic reation kettle of resin | |
| CN115282914B (en) | Epoxy resin production process | |
| CN112221459B (en) | Polyether neutralization reactor | |
| CN115155500A (en) | Preparation facilities of viscous crude viscosity reducer | |
| CN208449162U (en) | A kind of chemicals blender | |
| CN207605727U (en) | It is provided with the highly effective reaction kettle of steam filter screen | |
| CN213699844U (en) | Phenolic resin reation kettle | |
| CN207786576U (en) | Low energy consumption reaction unit | |
| CN207838964U (en) | Highly effective reaction device |
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: 20180123 |
|
| RJ01 | Rejection of invention patent application after publication |