CN113000000A - Temperature-controlled reaction kettle capable of efficiently stirring - Google Patents

Temperature-controlled reaction kettle capable of efficiently stirring Download PDF

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Publication number
CN113000000A
CN113000000A CN202110306881.XA CN202110306881A CN113000000A CN 113000000 A CN113000000 A CN 113000000A CN 202110306881 A CN202110306881 A CN 202110306881A CN 113000000 A CN113000000 A CN 113000000A
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CN
China
Prior art keywords
stirring
temperature
paddle
rake
water conservancy
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Pending
Application number
CN202110306881.XA
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Chinese (zh)
Inventor
袁天刚
刘友琴
许红伍
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Shanghai Sijun Machinery Equipment Co ltd
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Shanghai Sijun Machinery Equipment Co ltd
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Priority to CN202110306881.XA priority Critical patent/CN113000000A/en
Publication of CN113000000A publication Critical patent/CN113000000A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • B01J19/0066Stirrers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00074Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00094Jackets

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The invention relates to the technical field of chemical equipment kettles, in particular to a high-efficiency stirring temperature control reaction kettle, which comprises a kettle body and a temperature control kettle sleeve wrapping the kettle body, wherein a stirring paddle which is close to the inner wall of the kettle body for stirring is arranged in the kettle body, and a flow guide scraping blade is arranged on the surface of the stirring paddle, facing the inner wall of the kettle body; the crossing position of stirring rake and its axis of rotation is provided with the water conservancy diversion paddle leaf, the flow direction that the water conservancy diversion paddle leaf promoted the material with the flow direction that the water conservancy diversion doctor-bar promoted the material is opposite, and the material exchange of cauldron body middle part and cauldron internal wall department is abundant, has the stirring effect good, the even advantage of cauldron internal material temperature.

Description

Temperature-controlled reaction kettle capable of efficiently stirring
Technical Field
The invention belongs to the technical field of chemical equipment, and particularly relates to a temperature-controlled reaction kettle capable of efficiently stirring.
Background
The high-speed grinding disperser adopts a high-speed stirrer (such as a circular saw-tooth stirrer) to form strong turbulence locally, and generally has strong dispersing and emulsifying effects on materials. The powerful centrifugal force of high-speed grinding dispersion machine throws the material radially into between the stator, the narrow accurate clearance of rotor, receives comprehensive effort such as centrifugal extrusion, liquid layer friction, hydraulic impact simultaneously, and the material is by preliminary dispersion. The high-speed rotating rotor of the dispersion machine generates a linear velocity of at least 15m/s, and the materials are dispersed and crushed under the action of strong hydraulic shearing, liquid layer friction, tearing collision and the like and are simultaneously ejected through the stator slot at a high speed. The material of the dispersion machine is continuously ejected from the radial direction at high speed, the flow direction is changed under the resistance of the material and the wall of the container, and meanwhile, an upper and a lower strong turning turbulence flows are formed under the action of an upper and a lower axial suction forces generated in a rotor area. The material is circulated for several times to finally complete the dispersion process.
Because the rotor of high-speed grinding dispenser has high rotational speed to and the narrow precision in clearance between the rotor, consequently the material need carry out abundant stirring and rough machining before getting into the high-speed grinding dispenser, in order to guarantee that the material that gets into the high-speed grinding dispenser is abundant even, and does not have the impurity or the granule of major diameter.
To above-mentioned demand, current technique often sets up reation kettle at the material entrance of high-speed grinding dispenser, put into reation kettle with the material ratio as required earlier and carry out intensive mixing and reaction in, and in order to improve industrial production's efficiency, reation kettle's volume is often great, make the stirring efficiency of material in the reation kettle lower, and stir or take place the reaction to material in the reation kettle, can produce endothermic reaction or exothermic reaction, consequently, the reation kettle outer wall often is provided with heat preservation device, and under the too big condition of reation kettle volume, heat preservation device is difficult to guarantee the even of temperature in the reation kettle equally, thereby influence the efficiency of material stirring or reaction, lead to the material to become nature under high temperature even.
Disclosure of Invention
1. Technical problem to be solved by the invention
The invention aims to solve the problems of low stirring efficiency and non-uniform temperature in the existing large-scale reaction kettle.
2. Technical scheme
In order to achieve the purpose, the technical scheme provided by the invention is as follows: a temperature control reaction kettle with efficient stirring comprises a kettle body and a temperature control kettle sleeve wrapping the kettle body, wherein a stirring paddle which is close to the inner wall of the kettle body for stirring is arranged in the kettle body, and a flow guide scraping blade is arranged on the surface of the stirring paddle, facing the inner wall of the kettle body; the stirring paddle is provided with a diversion paddle blade at the crossed position of the rotating shaft of the stirring paddle, and the flow direction of the materials pushed by the diversion paddle blade is opposite to the flow direction of the materials pushed by the diversion scraper blade.
Preferably, cauldron body bottom is the back taper setting, the stirring rake includes outer stirring rake and interior stirring rake, outer stirring rake and interior stirring rake are connected with different drive arrangement, just outer stirring rake is pressed close to the inner wall of the cauldron body stirs.
Preferably, outer stirring rake orientation one side of interior stirring rake is provided with a plurality of stirring leaf one, interior stirring rake orientation one side of outer stirring rake is provided with a plurality of stirring leaf two, just stirring leaf one with the setting of stirring leaf two is the alternate arrangement.
Preferably, the rotation directions of the outer stirring paddle and the inner stirring paddle are opposite.
Preferably, a plurality of stirring holes are uniformly distributed on the first stirring blade and the second stirring blade.
Preferably, the inner wall of the stirring hole is provided with a plurality of stirring bulges.
Preferably, cauldron body bottom is the back taper setting, the pointed end of cauldron body bottom is provided with the discharge gate, the discharge gate is provided with the ooff valve, just the discharge gate with the axis of rotation of stirring rake is in on the same straight line, the discharge gate is connected with high-speed dispersion machine.
3. Advantageous effects
Compared with the prior art, the technical scheme provided by the invention has the following beneficial effects:
the temperature control reaction kettle for efficient stirring comprises a kettle body and a temperature control kettle sleeve wrapping the kettle body, wherein a stirring paddle for stirring close to the inner wall of the kettle body is arranged in the kettle body, and a flow guide scraping blade is arranged on the surface of the stirring paddle facing the inner wall of the kettle body; the crossing position of stirring rake and its axis of rotation is provided with the water conservancy diversion paddle leaf, the flow direction that the water conservancy diversion paddle leaf promoted the material with the flow direction that the water conservancy diversion doctor-bar promoted the material is opposite, and the material exchange of cauldron body middle part and cauldron internal wall department is abundant, has the stirring effect good, the even advantage of cauldron internal material temperature.
Drawings
FIG. 1 is a schematic structural view of a kettle body according to the present invention;
FIG. 2 is a schematic structural view of the present invention as a whole;
FIG. 3 is a schematic structural view of the stirring blade of the present invention.
The reference numerals in the schematic drawings illustrate:
100. a kettle body; 110. a temperature control kettle sleeve; 111. a liquid inlet; 112. a liquid outlet; 120. a discharge port; 130. a feeding port; 200. a stirring paddle; 210. a flow guiding scraper; 220. a guide vane; 230. an outer stirring paddle; 231. stirring the first blade; 240. an inner stirring paddle; 241. stirring the second leaf; 250. a stirring hole; 251. stirring the bulges; 300. a high-speed disperser; 400. a motor platform; 410. a drive shaft; 411. an inner drive shaft; 412. an outer drive shaft; 420. a limiting device.
Detailed Description
In order to facilitate an understanding of the invention, the invention will now be described more fully hereinafter with reference to the accompanying drawings, in which several embodiments of the invention are shown, but which may be embodied in many different forms and are not limited to the embodiments described herein, but rather are provided for the purpose of providing a more thorough disclosure of the invention.
It will be understood that when an element is referred to as being "secured to" another element, it can be directly on the other element or intervening elements may also be present; when an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present; the terms "vertical," "horizontal," "left," "right," and the like as used herein are for illustrative purposes only.
Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs; the terminology used herein in the description of the invention is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention; as used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
Example 1
Referring to fig. 1 to fig. 3, the present embodiment provides a technical solution: a high-efficiency stirring temperature control reaction kettle comprises a kettle body 100 and a temperature control kettle sleeve 110 wrapping the kettle body 100, wherein the kettle body 100 comprises a top cover and a feeding port 130 arranged on the top cover, the temperature control kettle sleeve 110 is arranged in a hollow manner, a liquid inlet 111 is arranged at the lower end of the temperature control kettle sleeve 110, a liquid outlet 112 is arranged at the upper end of the temperature control kettle sleeve 110, when the temperature of materials in the kettle body 100 is too high, liquid with lower temperature can be filled into the liquid inlet 111, heat energy in the kettle body 100 is absorbed, and the liquid with raised temperature is discharged from the liquid outlet 112, so that the temperature in the kettle body 100 is rapidly reduced, and the materials in the kettle body 100 are placed to be subjected to biological change at high temperature; in the same way, when the temperature in the kettle body 100 is lower, the liquid with higher temperature is poured into the liquid inlet 111, so that the temperature of the kettle body 100 is increased, and the materials in the kettle body 100 are ensured to be in a proper temperature range.
The internal stirring rake 200 that is provided with the stirring of pressing close to the internal wall of cauldron 100 of cauldron, the stirring rake 200 passes through transmission shaft 410 and is connected with the outside motor platform 400 of the cauldron body 100, the vertical through set up of transmission shaft 410 in the central point of the 100 top covers of the cauldron body puts, the stirring rake 200 adopts frame stirring rake to set up, the stirring rake 200 outward flange arrives the distance department of the internal wall of cauldron body 100 equals everywhere, makes the stirring rake 200 can be right each department of the internal wall of cauldron body 100 carries out the even stirring at no dead angle, and is convenient for the stirring rake 200 with set up water conservancy diversion doctor-bar 210 between the internal wall of the cauldron body 100.
Stirring rake 200 is provided with water conservancy diversion doctor-bar 210 towards the surface of the internal wall of cauldron 100, water conservancy diversion doctor-bar 210 keeps away from the edge laminating of stirring rake 200 sets up in the internal wall of cauldron 100, just water conservancy diversion doctor-bar 210 is the acute angle setting with the direction of rotation, makes water conservancy diversion doctor-bar 210 can be right the internal wall of cauldron 100 scrapes the wall stirring, can again under the water conservancy diversion effect of water conservancy diversion doctor-bar 210, water conservancy diversion doctor-bar 210 can be with the material along the internal wall of cauldron 100 promotes towards the bottom of the cauldron body 100, makes and is close to the material of the internal wall of cauldron 100 flows to cauldron body 100 bottom.
Stirring rake 200 is provided with water conservancy diversion paddle 220 rather than the crossing position of axis of rotation A, makes stirring rake 200 is when rotating around its axis of rotation A, water conservancy diversion paddle 220 can rotate in step, water conservancy diversion paddle 220 be provided with two and central symmetry set up in stirring rake 200 both sides, water conservancy diversion paddle 220 is the acute angle setting with the level, makes water conservancy diversion paddle 220 can promote the material when rotating and remove, water conservancy diversion paddle 220 promote the flow direction of material with water conservancy diversion scraper 210 promotes the flow opposite direction of material.
In the using process, firstly, according to the mixture ratio of materials, sufficient materials are added into the kettle body 100 from the material inlet 130, wherein the materials comprise a liquid mixture, a solid-liquid mixture, a liquid-gas mixture or a solid-liquid-gas mixture, then the motor platform 400 is started, so that the motor platform 400 drives the stirring paddle 200 to rotate through the transmission shaft 410, the materials are subjected to mixing reaction through the stirring action of the stirring paddle 200, and in the stirring process, when the temperature in the kettle body 100 is too high, liquid with lower temperature needs to be filled into the temperature control kettle sleeve 110 to cool the materials in the kettle body 100; in the process of cooling, because the internal volume of the kettle body 100 is large, the heat conduction efficiency is low, the temperature of the material close to the inner wall of the kettle body 100 is low, and the temperature of the material in the central area of the kettle body 100 is high. At this time, the diversion scraper 210 diverts the material close to the inner wall of the kettle 100 to the bottom of the kettle 100, and the diversion scraper 210 diverts the material diverted to the bottom of the kettle 100 with a lower temperature to the central area of the kettle 100, so that the material on the inner wall of the kettle 100 is fully exchanged with the material in the central area of the kettle 100, the heat conduction efficiency is greatly improved, and the material temperature in the kettle 100 is in a more uniform state; meanwhile, the guide blades 220 and the guide blades 210 also play a role in improving the stirring efficiency.
In the preferred scheme, cauldron body 100 bottom is the back taper setting, makes water conservancy diversion scraper 210 can concentrate the water conservancy diversion extremely with the material that is close to cauldron body 100 inner wall the conical top region in cauldron body 100 bottom, simultaneously water conservancy diversion paddle 220 can carry out high-efficient water conservancy diversion to this regional material, is favorable to improving water conservancy diversion paddle 220 and water conservancy diversion scraper 210's convection action.
Stirring rake 200 includes outer stirring rake 230 and interior stirring rake 240, outer stirring rake 230 and interior stirring rake 240 are connected with different drive arrangement, interior stirring rake 240 through interior transmission shaft 411 with motor platform 400 is connected, outer stirring rake 230 through outer transmission shaft 412 with motor platform 400 is connected, outer transmission shaft 412 cover is located interior transmission shaft 411 outer wall, just interior transmission shaft 411 is by the driving motor direct drive in the motor platform 400, outer transmission shaft 412 is driven by the two-way gear engagement of driving motor in the motor platform 400, outer stirring rake 230 is pressed close to the inner wall of the cauldron body 100 stirs.
A limiting device 420 is arranged between the top cover of the kettle body 100 and the motor platform 400, and the outer transmission shaft 412 penetrates through the limiting device 420 and is connected with the motor platform 400; the limiting device 420 is used for stabilizing the rotation of the outer transmission shaft 412.
In a preferred embodiment, a plurality of first stirring blades 231 are disposed on one side of the outer stirring blade 230 facing the inner stirring blade 240, a plurality of second stirring blades 241 are disposed on one side of the inner stirring blade 240 facing the outer stirring blade 230, and the first stirring blades 231 and the second stirring blades 241 are arranged in an alternating manner. So that the first stirring blade 231 and the second stirring blade 241 do not collide with each other during the independent stirring process of the outer stirring blade 230 and the inner stirring blade 240.
In a preferred embodiment, the outer paddles 230 and the inner paddles 240 rotate in opposite directions. The outer stirring paddle 230 and the inner stirring paddle 240 form mixed flow in the stirring process, the mixed flow is adjacent to the first stirring blade 231 and the edge of the second stirring blade 241 can form certain shearing force on materials in the rotating process, the stirring effect of the outer stirring paddle 230 and the inner stirring paddle 240 is better, meanwhile, the first stirring blade 231 and the second stirring blade 241 can shear particles with larger diameters in the materials, the materials are mixed or react more fully, and the materials entering the high-speed dispersion machine 300 are finer and finer.
In a preferable scheme, a plurality of stirring holes 250 are uniformly distributed on the first stirring blade 231 and the second stirring blade 241. The stirring holes 250 are used for improving the stirring effect and reducing the resistance of the material to the first stirring blade 231 and the second stirring blade 241, so that the stirring speed of the outer stirring paddle 230 and the inner stirring paddle 240 can be improved; the diameter of the stirring hole 250 is 2-5 times of the diameter of the target particle, on one hand, the material can be deposited in the stirring hole 250, so that the blockage of the stirring hole 250 is inconvenient to clean, and on the other hand, the stirring hole 250 plays a role in filtering large particles and hard impurities in the material, and the large particles and hard impurities in the material are easily caught by the stirring hole 250 and are blocked in the stirring hole 250, so that the impurities are prevented from entering the high-speed dispersion machine 300, and the service life of the high-speed dispersion machine 300 is influenced.
In a preferable scheme, a plurality of stirring protrusions 251 are arranged on the inner wall of the stirring hole 250. The agitating protrusion 251 can enhance the agitating function of the agitating hole 250 and enhance the capturing function of the agitating hole 250 for large-particle impurities.
In preferred scheme, cauldron body 100 bottom is the back taper setting, the pointed end of cauldron body 100 bottom is provided with discharge gate 120, cauldron body 100 bottom adopts to be the back taper setting for the in-process material of the ejection of compact is changeed under the effect of gravity and is collected at discharge gate 120, the material ejection of compact of being convenient for, discharge gate 120 is provided with the ooff valve, just discharge gate 120 with the axis of rotation A of stirring rake 200 is located same straight line, discharge gate 120 is connected with high-speed dispersion machine 300. In the using process, the valve of the discharge port 120 is closed first, and after the materials in the kettle body 100 are fully stirred or reacted, the discharge port 120 is opened to enable the materials to enter the high-speed dispersion machine 300 for grinding and dispersion, and meanwhile, the stirring paddle 200 in the kettle body 100 is kept in a rotating state, so that the materials are prevented from silting or blocking in the discharging process.
The above-mentioned embodiments only express a certain implementation mode of the present invention, and the description thereof is specific and detailed, but not construed as limiting the scope of the present invention; it should be noted that, for those skilled in the art, without departing from the concept of the present invention, several variations and modifications can be made, which are within the protection scope of the present invention; therefore, the protection scope of the present patent shall be subject to the appended claims.

Claims (7)

1. The utility model provides a accuse temperature reation kettle of high-efficient stirring, includes accuse temperature cauldron cover (110) that the cauldron body (100) and parcel cauldron body (100) set up, its characterized in that: a stirring paddle (200) which is close to the inner wall of the kettle body (100) for stirring is arranged in the kettle body (100), and a flow guide scraping blade (210) is arranged on the surface of the stirring paddle (200) facing the inner wall of the kettle body; the stirring rake (200) is provided with water conservancy diversion paddle leaf (220) rather than the crossing position of axis of rotation (A), the flow direction that water conservancy diversion paddle leaf (220) promoted the material with the flow direction that water conservancy diversion doctor-bar (210) promoted the material is opposite.
2. The high-efficiency stirring temperature-controlled reaction kettle according to claim 1, characterized in that: the cauldron body (100) bottom is the back taper setting, stirring rake (200) are including outer stirring rake (230) and interior stirring rake (240), outer stirring rake (230) and interior stirring rake (240) are connected with different drive arrangement, just outer stirring rake (230) are pressed close to the inner wall of the cauldron body (100) stirs.
3. The high-efficiency stirring temperature-controlled reaction kettle according to claim 2, wherein: outer stirring rake (230) orientation one side of interior stirring rake (240) is provided with a plurality of stirring leaf (231), interior stirring rake (240) orientation one side of outer stirring rake (230) is provided with a plurality of stirring leaf two (241), just stirring leaf one (231) with stirring leaf two (241) are the alternate arrangement setting.
4. The high-efficiency stirring temperature-controlled reaction kettle according to claim 2, wherein: the rotating directions of the outer stirring paddle (230) and the inner stirring paddle (240) are opposite.
5. The high-efficiency stirring temperature-controlled reaction kettle according to claim 3, wherein: the first stirring blade (230) and the second stirring blade (240) are uniformly provided with a plurality of stirring holes (250).
6. The high-efficiency stirring temperature-controlled reaction kettle according to claim 5, wherein: the inner wall of the stirring hole (250) is provided with a plurality of stirring bulges (251).
7. The high-efficiency stirring temperature-controlled reaction kettle according to claim 1, characterized in that: the cauldron body (100) bottom is the back taper setting, the pointed end of the cauldron body (100) bottom is provided with discharge gate (120), discharge gate (120) are provided with the ooff valve, just discharge gate (120) with axis of rotation (A) of stirring rake (200) are in on the same straight line, discharge gate (120) are connected with high-speed dispersion machine (300).
CN202110306881.XA 2021-03-23 2021-03-23 Temperature-controlled reaction kettle capable of efficiently stirring Pending CN113000000A (en)

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CN202110306881.XA CN113000000A (en) 2021-03-23 2021-03-23 Temperature-controlled reaction kettle capable of efficiently stirring

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Application Number Priority Date Filing Date Title
CN202110306881.XA CN113000000A (en) 2021-03-23 2021-03-23 Temperature-controlled reaction kettle capable of efficiently stirring

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CN113000000A true CN113000000A (en) 2021-06-22

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114700021A (en) * 2022-04-27 2022-07-05 上海欧河机械设备有限公司 Reation kettle with guide plate
CN114748985A (en) * 2022-04-21 2022-07-15 浙江浙能镇海发电有限责任公司 Absorption tower that PH meter measuring accuracy is high

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN205761146U (en) * 2016-05-26 2016-12-07 宁波大学 A kind of rotation frame chemical reaction still
CN206529307U (en) * 2017-03-10 2017-09-29 天津沣博瑞环保科技有限公司 A kind of sewage disposal aeration agitation oar
WO2017219841A1 (en) * 2016-06-21 2017-12-28 山东日科化学股份有限公司 Corrosion-resistant metal chlorination reaction vessel
CN206881607U (en) * 2017-07-02 2018-01-16 厦门中凯新材石墨烯科技有限公司 A kind of graphene coating mixed stirring device
CN211303046U (en) * 2019-11-25 2020-08-21 河北省环保产品质量监督检验研究院 Reaction kettle stirrer suitable for reaction of viscous substances
CN211837477U (en) * 2020-03-09 2020-11-03 上海良晟科技有限公司 Two-way stirring and bottom dispersing emulsification reaction kettle

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN205761146U (en) * 2016-05-26 2016-12-07 宁波大学 A kind of rotation frame chemical reaction still
WO2017219841A1 (en) * 2016-06-21 2017-12-28 山东日科化学股份有限公司 Corrosion-resistant metal chlorination reaction vessel
CN206529307U (en) * 2017-03-10 2017-09-29 天津沣博瑞环保科技有限公司 A kind of sewage disposal aeration agitation oar
CN206881607U (en) * 2017-07-02 2018-01-16 厦门中凯新材石墨烯科技有限公司 A kind of graphene coating mixed stirring device
CN211303046U (en) * 2019-11-25 2020-08-21 河北省环保产品质量监督检验研究院 Reaction kettle stirrer suitable for reaction of viscous substances
CN211837477U (en) * 2020-03-09 2020-11-03 上海良晟科技有限公司 Two-way stirring and bottom dispersing emulsification reaction kettle

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114748985A (en) * 2022-04-21 2022-07-15 浙江浙能镇海发电有限责任公司 Absorption tower that PH meter measuring accuracy is high
CN114700021A (en) * 2022-04-27 2022-07-05 上海欧河机械设备有限公司 Reation kettle with guide plate

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Application publication date: 20210622

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