CN107824134A - A kind of stirred tank of multilayer corrosion-resistance temperature controllable - Google Patents

A kind of stirred tank of multilayer corrosion-resistance temperature controllable Download PDF

Info

Publication number
CN107824134A
CN107824134A CN201711324067.0A CN201711324067A CN107824134A CN 107824134 A CN107824134 A CN 107824134A CN 201711324067 A CN201711324067 A CN 201711324067A CN 107824134 A CN107824134 A CN 107824134A
Authority
CN
China
Prior art keywords
kettle
stirred tank
chuck
agitating shaft
resistance temperature
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
Application number
CN201711324067.0A
Other languages
Chinese (zh)
Inventor
刘庭富
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sichuan SY Moly Technology Co Ltd
Original Assignee
Sichuan SY Moly Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sichuan SY Moly Technology Co Ltd filed Critical Sichuan SY Moly Technology Co Ltd
Priority to CN201711324067.0A priority Critical patent/CN107824134A/en
Publication of CN107824134A publication Critical patent/CN107824134A/en
Pending legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053—Details of the reactor
    • B01J19/0066—Stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/02—Apparatus characterised by being constructed of material selected for its chemically-resistant properties
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/1868—Stationary reactors having moving elements inside resulting in a loop-type movement
    • B01J19/1875—Stationary reactors having moving elements inside resulting in a loop-type movement internally, i.e. the mixture circulating inside the vessel such that the upwards stream is separated physically from the downwards stream(s)
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18—Stationary reactors having moving elements inside
    • B01J19/20—Stationary reactors having moving elements inside in the form of helices, e.g. screw reactors
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/001—Controlling catalytic processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/10—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by stirrers or by rotary drums or rotary receptacles or endless belts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10—Inorganic adsorbents
    • B01D2253/102—Carbon
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2258/00—Sources of waste gases
    • B01D2258/02—Other waste gases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00044—Temperature measurement
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
    • B01J2208/00212—Plates; Jackets; Cylinders
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00575—Controlling the viscosity
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00054—Controlling or regulating the heat exchange system
    • B01J2219/00056—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2219/00058—Temperature measurement
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00094—Jackets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00168—Controlling or regulating processes controlling the viscosity
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/02—Apparatus characterised by their chemically-resistant properties
    • B01J2219/0204—Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components
    • B01J2219/0213—Apparatus characterised by their chemically-resistant properties comprising coatings on the surfaces in direct contact with the reactive components of enamel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/18—Details relating to the spatial orientation of the reactor
    • B01J2219/185—Details relating to the spatial orientation of the reactor vertical

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Accessories For Mixers (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)

Abstract

The invention discloses a kind of stirred tank of multilayer corrosion-resistance temperature controllable, belong to stirred tank technical field, it is characterized in that, including kettle, the top surface of the kettle is provided with charge door and blast pipe, the outlet of the blast pipe is connected with filter, the filter is connected with clarifier, motor is provided with above the kettle, the output shaft of the motor is connected with decelerator, the agitating shaft stretched into the kettle is connected with below the decelerator, helical blade is connected with the agitating shaft, guide vane is provided with the agitating shaft bottom, agitating shaft is connected with a pair of scraper plates, one layer of chuck is cased with outside the kettle, inlet is provided with below the chuck, liquid outlet is provided with above chuck, thermometer and viscosimeter are additionally provided with the chuck, one layer of glass-lined coating is provided with the inwall of the kettle.Of the invention environmental protection, mixing effect are good, can corrosion-resistant high-low temperature resistant, and various temperature for the needs that can meet to chemically react.

Description

A kind of stirred tank of multilayer corrosion-resistance temperature controllable
Technical field
The invention belongs to stirred tank technical field, and in particular to a kind of stirred tank of multilayer corrosion-resistance temperature controllable.
Background technology
Stirred tank is reaction unit common in chemical industry, and the material in kettle is is well mixed by major function, industry The stirred-tank reactor of upper application has hundreds and thousands of kinds, is divided into homogeneous stirred tank by the phase of reaction mass and heterogeneous stirs Mix the major class of kettle two.Heterogeneous stirred tank includes solid-liquid stirred tank, liquid-liquid stirred tank, solution-air stirred tank and airwater mist cooling Stirred tank.
Usual stirred tank is all using increase chuck and is passed through biography wherein in the reaction for carrying out needing to be heated or cooled Thermal medium is heated and radiated to realize, but some required precisions of chemical reaction to temperature are higher, it is necessary to which temperature control is existed More accurately scope, existing stirred tank can not accurately temperature adjustment, constant temperature, it is impossible to meet the occasion high to temperature requirement, use When there is limitation.
For the high material of some viscosity, because stirring is easily accumulated and be adhered to its own property after stirred tank is added Kettle inwall and discharge outlet, cause stirring uneven and discharging opening blocks, and common reactor, which uses, improves speed of agitator and lifting The method of heating-up temperature is to reduce material viscosity, quickening disperses and the speed of mixing, but too high rotating speed may destroy The macro-radical structure of material, and too high temperature can also be easily destroyed the property of material in itself.
Often have reaction remaining in chemical reaction or reaction caused by tail gas discharge, and typically contained in tail gas poisonous Pernicious gas, directly drain into air not only can harmful to human, and pollute the environment.
Existing stirred tank is usually stainless steel manufacture, can high-low temperature resistant, but not corrosion-resistant, the material in chemical reaction Typically all there is acid, caustic corrosion, therefore single stainless steel stirred tank can not meet the production requirement of some techniques.
The content of the invention
It is an object of the invention to provide a kind of stirred tank of multilayer corrosion-resistance temperature controllable to solve the above problems.
The technical solution adopted by the present invention is as follows：
A kind of stirred tank of multilayer corrosion-resistance temperature controllable, it is characterised in that including kettle, the top surface of the kettle is set Charge door and blast pipe are equipped with, the outlet of the blast pipe is connected with filter, and the filter is connected with clarifier, the kettle Motor is provided with above body, the output shaft of the motor is connected with decelerator, is connected with below the decelerator described in stretching into Agitating shaft in kettle, helical blade is connected with the agitating shaft, guide vane is provided with the agitating shaft bottom, stir Axis connection has a pair of scraper plates, and the bottom of the kettle is provided with discharge gate, is cased with one layer of chuck outside the kettle, under the chuck Side is provided with inlet, is provided with liquid outlet above chuck, thermometer and viscosimeter, the temperature are additionally provided with the chuck Meter and viscosimeter are stretched into the kettle, and the bottom of the kettle is additionally provided with gas blow pipe, is provided with the inwall of the kettle One layer of glass-lined coating, the scraper plate are in contact with the glass-lined coating.
The helical blade is symmetrical, spiral surrounding is arranged on the agitating shaft.
The gas blow pipe of the bottom of the kettle bottom for being distributed in kettle annular in shape.
Multiple through holes are provided with the guide vane.
The kettle is stainless steel.
Preferably, it is provided with acticarbon in the filter.
The course of work of the present invention is as follows：
The present invention can support the various mixed types of gas-liquid-solid phase, and during work, solid material, gas are added at charge door Body is then passed through in kettle by the gas blow pipe of autoclave body bottom, the material of mixing is sufficiently stirred by helical blade so that kettle Internal material fully, uniformly mix and reaction, under the material scraper that scraper plate will can be accumulated on glass-lined coating inwall and adds In the stirring for entering helical blade, the guide vane agitation of agitating shaft bottom is blocked in the material of discharge gate, makes the smooth discharge of material, Gas caused by remaining and reaction is flowed up after reaction, and the blast pipe through top, which is discharged in filter, to be filtered, and finally It is passed through in clarifier and purifies, the chuck outside kettle is passed through cooling water or heating steam, and the temperature in kettle is carried out by thermometer Monitoring, the temperature that control reaction needs.
In summary, by adopting the above-described technical solution, the beneficial effects of the invention are as follows：
1. the present invention is using a pair of helical mixing blades being arranged symmetrically and the structure design of gas blow pipe, when progress material Stirring when, the outside for the spiral that material is formed in helical mixing blade and Matter Transfer is internally formed, outside spiral Material flowed up in the presence of helical mixing blade, the material at the top of kettle enter threaded interior after flow downward So as to form Matter Transfer, accelerate material mixing, make the material mixed effect of different parts in kettle homogeneous, thing can either be ensured The abundant reaction of material, while the demand of different process is disclosure satisfy that again so that the characteristics of present invention is well mixed with material, carry High product quality.
2. be provided with one layer of glass-lined coating on the inner wall of kettle of the present invention, can acid-alkali-corrosive-resisting, meet complicated production work Skill requirement, prevent that kettle is destroyed, corrodes, improve the applicability of equipment.
3. the present invention is provided with filter and clarifier in exhaust outlet, reacted tail gas is filtered, purified Processing, waste gas is removed in time, ensure the quality of product in kettle, and realize harmless, environmentally friendly.
4. the present invention is provided with scraper plate on glass-lined coating, the material accumulated on glass-lined coating can be scraped off addition and stirred In mixing so that material mixing is more uniform, further increases the quality of product, the material for avoiding the viscosity in material higher exists Accumulation is formed in kettle, existing stirred tank is solved the problems, such as there is material mixing dead angle, caking and blocks, it is ensured that product matter Amount.
5. the present invention is provided with multiple gas blow pipes in autoclave body bottom, gas can be disperseed to be passed through in reactor, make mixing more Uniformly, react more abundant.
6. the present invention is provided with corrugated guide vane in the top of the bottom of agitating shaft, discharging opening, material can be entered Row water conservancy diversion, increase the walking path of material, effectively prevent material, rapid accumulation causes in discharging opening under gravity Block, while multiple through holes are provided with guide vane, mitigate the pressure of guide vane, prevent by the pressure destruction of material.
7. the present invention is provided with chuck, inlet and liquid outlet are provided with chuck, cooling water or heating steam can be passed through, Kettle can be cooled down or heated, while there is provided thermometer that kettle body temperature is monitored, it is possible to achieve temperature adjustment, perseverance Temperature, meet the temperature requirement needed for various reactions.
Brief description of the drawings
Examples of the present invention will be described by way of reference to the accompanying drawings, wherein：
Fig. 1 is the structural representation of the present invention.
Description of reference numerals：
1- motors, 2- decelerators, 3- blast pipes, 4- journal stirrups, 5- scraper plates, 6- chucks, 7- helical blades, 8- kettlies, 9- temperature Degree meter, 10- guide vanes, 11- discharge gates, 12- gas blow pipes, 13- inlets, 14- viscosimeters, 15- agitating shafts, 16- liquid outlets, 17- glass-lined coatings, 18- charge doors, 19- filters, 20- clarifiers.
Embodiment
All features disclosed in this specification, or disclosed all methods or during the step of, except mutually exclusive Feature and/or step beyond, can combine in any way.
The present invention is elaborated with reference to Fig. 1.
A kind of stirred tank of multilayer corrosion-resistance temperature controllable, it is characterised in that including kettle 8, the top surface of the kettle 8 Charge door 18 and blast pipe 3 are provided with, the outlet of the blast pipe 3 is connected with filter 19, the filter 19 and clarifier 20 connections, the top of the kettle 8 are provided with motor 1, and the output shaft of the motor 1 is connected with decelerator 2, the decelerator 2 Lower section is connected with the agitating shaft 15 stretched into the kettle 8, and helical blade 7, the agitating shaft are connected with the agitating shaft 15 Guide vane 10 is provided with 15 bottoms, agitating shaft 15 is connected with a pair of scraper plates 5, and the bottom of the kettle 8 is provided with discharge gate 11, the kettle 8 is cased with one layer of chuck 6 outside, and the lower section of chuck 6 is provided with inlet 13, and the top of chuck 6 is provided with liquid outlet 16, thermometer 9 and viscosimeter 14 are additionally provided with the chuck 6, the thermometer 9 and viscosimeter 14 are stretched into the kettle 8, The bottom of the kettle 8 is additionally provided with gas blow pipe 12, and one layer of glass-lined coating 17 is provided with the inwall of the kettle 8, described to scrape Plate 5 is in contact with the glass-lined coating 17.
The helical blade 7 is symmetrical, spiral surrounding is arranged on the agitating shaft 15.
The gas blow pipe 12 of the bottom of the kettle 8 bottom for being distributed in kettle 8 annular in shape.
Multiple through holes are provided with the guide vane 10.
The kettle 8 is stainless steel.
Preferably, it is provided with acticarbon in the filter 19.
Embodiment 1
A kind of stirred tank of multilayer corrosion-resistance temperature controllable, it is characterised in that including kettle 8, the top surface of the kettle 8 Charge door 18 and blast pipe 3 are provided with, the outlet of the blast pipe 3 is connected with filter 19, the filter 19 and clarifier 20 connections, the top of the kettle 8 are provided with motor 1, and the output shaft of the motor 1 is connected with decelerator 2, the decelerator 2 Lower section is connected with the agitating shaft 15 stretched into the kettle 8, and helical blade 7, the agitating shaft are connected with the agitating shaft 15 Guide vane 10 is provided with 15 bottoms, agitating shaft 15 is connected with a pair of scraper plates 5, and the bottom of the kettle 8 is provided with discharge gate 11, the kettle 8 is cased with one layer of chuck 6 outside, and the lower section of chuck 6 is provided with inlet 13, and the top of chuck 6 is provided with liquid outlet 16, thermometer 9 and viscosimeter 14 are additionally provided with the chuck 6, the thermometer 9 and viscosimeter 14 are stretched into the kettle 8, The bottom of the kettle 8 is additionally provided with gas blow pipe 12, and one layer of glass-lined coating 17 is provided with the inwall of the kettle 8, described to scrape Plate 5 is in contact with the glass-lined coating 17.
The charge door 18 is opened into addition quick lime, heating steam is passed through in the chuck 6, when thermometer 9 shows temperature The gas blow pipe 12 that degree opens the bottom of kettle 8 at 650 degrees Celsius is passed through sulfurous gas, material is fully contacted carry out desulfurization Reaction, the crystal that the discharge of discharge gate 11 separates out, the gas after desulfurization is discharged by the blast pipe 3, and passes through filter 19 and clarifier 20 carry out filtration treatment.

Claims (5)

1. a kind of stirred tank of multilayer corrosion-resistance temperature controllable, including kettle (8), the top surface of the kettle (8), which is provided with, to be added Material mouth (18) and blast pipe (3), motor (1) are provided with above the kettle (8), the output shaft of the motor (1) is connected with Decelerator (2), decelerator (2) lower section are connected with the agitating shaft (15) stretched into the kettle (8), the kettle (8) Bottom is provided with discharge gate (11), it is characterised in that the outlet of the blast pipe (3) is connected with filter (19), the filtering Device (19) is connected with clarifier (20), is connected with helical blade (7) on the agitating shaft (15), on agitating shaft (15) bottom Guide vane (10) is provided with, agitating shaft (15) is also associated with a pair of scraper plates (5), one layer of chuck is cased with outside the kettle (8) (6) inlet (13), is provided with below the chuck (6), is provided with liquid outlet (16) above chuck (6), on the chuck (6) Thermometer (9) and viscosimeter (14) are additionally provided with, the thermometer (9) and viscosimeter (14) are stretched into the kettle (8), described The bottom of kettle (8) is additionally provided with gas blow pipe (12), and one layer of glass-lined coating (17), institute are provided with the inwall of the kettle (8) Scraper plate (5) is stated to be in contact with the glass-lined coating (17).
A kind of 2. stirred tank of multilayer corrosion-resistance temperature controllable according to claim 1, it is characterised in that the spiral Blade (7) is symmetrical, spiral surrounding is arranged on the agitating shaft (15).
A kind of 3. stirred tank of multilayer corrosion-resistance temperature controllable according to claim 1, it is characterised in that the kettle (8) gas blow pipe (12) of the bottom bottom for being distributed in kettle (8) annular in shape.
A kind of 4. stirred tank of multilayer corrosion-resistance temperature controllable according to claim 1, it is characterised in that the water conservancy diversion Blade is provided with multiple through holes on (10).
A kind of 5. stirred tank of multilayer corrosion-resistance temperature controllable according to claim 1, it is characterised in that the kettle (8) it is stainless steel.
CN201711324067.0A 2017-12-11 2017-12-11 A kind of stirred tank of multilayer corrosion-resistance temperature controllable Pending CN107824134A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711324067.0A CN107824134A (en) 2017-12-11 2017-12-11 A kind of stirred tank of multilayer corrosion-resistance temperature controllable

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711324067.0A CN107824134A (en) 2017-12-11 2017-12-11 A kind of stirred tank of multilayer corrosion-resistance temperature controllable

Publications (1)

Publication Number Publication Date
CN107824134A true CN107824134A (en) 2018-03-23

Family

ID=61642800

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711324067.0A Pending CN107824134A (en) 2017-12-11 2017-12-11 A kind of stirred tank of multilayer corrosion-resistance temperature controllable

Country Status (1)

Country Link
CN (1) CN107824134A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113274963A (en) * 2021-04-26 2021-08-20 中国科学院化学研究所 Reaction device for preparing polymer with high filling ratio and high viscosity and preparation method of polymer
CN114950313A (en) * 2022-05-12 2022-08-30 福建天翊有机硅新材料有限公司 Reation kettle is used in hydroxyl silicone oil production

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113274963A (en) * 2021-04-26 2021-08-20 中国科学院化学研究所 Reaction device for preparing polymer with high filling ratio and high viscosity and preparation method of polymer
CN114950313A (en) * 2022-05-12 2022-08-30 福建天翊有机硅新材料有限公司 Reation kettle is used in hydroxyl silicone oil production

Similar Documents

Publication Publication Date Title
CN207153705U (en) A kind of reactor with solid-liquid separation function
CN107824153A (en) A kind of stirred tank of environment-friendly high-efficiency
CN106390825A (en) Chemical stirring tank capable of achieving premixing and being conveniently cleaned
CN107824134A (en) A kind of stirred tank of multilayer corrosion-resistance temperature controllable
CN206008688U (en) A kind of circular response kettle
CN106378078A (en) Vibration attenuation temperature-adjustable efficient stirring reactor
CN106732230A (en) A kind of chemical mixing unit with knot screen
CN108101127A (en) A kind of sewage disposal efficiently mixes adding set with medicament
CN207401478U (en) A kind of new point of copper reaction kettle
JP2011194301A (en) Subcritical water treatment apparatus and method
CN205613417U (en) High -efficient reation kettle with sediment collection device
CN206500081U (en) A kind of Chemical Manufacture agitator
CN207913744U (en) A kind of stirred tank of multilayer corrosion-resistance temperature controllable
CN107812506A (en) A kind of Multifunctional agitating kettle of anti-clogging with temperature control
CN207970861U (en) A kind of stirred tank of environment-friendly high-efficiency
CN110743476B (en) Multifunctional calcium hydroxide preparation tank and preparation method
CN207913777U (en) A kind of Multifunctional agitating kettle of the anti-clogging with temperature control
KR20170131152A (en) Chemical reactor and preparation method of olefin using the same
CN206046019U (en) A kind of cement water reducing agent reactor
CN108311080A (en) A kind of efficient chemical industry feed liquid centrifugation reaction kettle
CN210993892U (en) A agitating unit for instant agar production
CN212982883U (en) Waste plastic treatment equipment
CN206253138U (en) It is a kind of to wash the chemical industry high-efficiency stirring retort that type is easy to temperature adjustment certainly
CN219308709U (en) Antiviral medicine preparation reaction unit
RU178404U1 (en) Mixer reactor for carrying out processes in heterogeneous environments

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20180323

WD01 Invention patent application deemed withdrawn after publication