CN116440833A - High-efficient stirring reactor system - Google Patents

High-efficient stirring reactor system Download PDF

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Publication number
CN116440833A
CN116440833A CN202211410270.0A CN202211410270A CN116440833A CN 116440833 A CN116440833 A CN 116440833A CN 202211410270 A CN202211410270 A CN 202211410270A CN 116440833 A CN116440833 A CN 116440833A
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CN
China
Prior art keywords
nozzle
reaction kettle
pipeline
communicated
pipe
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
CN202211410270.0A
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Chinese (zh)
Inventor
许显新
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.)
Shanghai Dynaflutec Pump Co ltd
Original Assignee
Shanghai Dynaflutec Pump 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 Shanghai Dynaflutec Pump Co ltd filed Critical Shanghai Dynaflutec Pump Co ltd
Priority to CN202211410270.0A priority Critical patent/CN116440833A/en
Publication of CN116440833A publication Critical patent/CN116440833A/en
Pending legal-status Critical Current

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Classifications

    • 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
    • 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
    • B01J19/0006—Controlling or regulating 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
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006—Controlling or regulating processes
    • B01J19/0013—Controlling the temperature of the process
    • 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
    • B01J4/007—Feed or outlet devices as such, e.g. feeding tubes provided with moving parts
    • 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
    • B01J4/00—Feed or outlet devices; Feed or outlet control devices
    • B01J4/008—Feed or outlet control devices
    • 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
    • B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
    • B01J2204/002—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the feeding side being of particular interest
    • 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
    • B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
    • B01J2204/005—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices the outlet side being of particular interest
    • 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
    • B01J2204/00—Aspects relating to feed or outlet devices; Regulating devices for feed or outlet devices
    • B01J2204/007—Aspects relating to the heat-exchange of the feed or outlet devices
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency

Landscapes

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

Abstract

The invention relates to a high-efficiency stirring reactor system which comprises a reaction kettle, a heat exchanger and a stirring pump, wherein a rotary joint is fixed at the top end of the reaction kettle and is communicated with the heat exchanger through a pipeline, the heat exchanger is communicated with the stirring pump through a pipeline, and the stirring pump is communicated with the bottom of the reaction kettle through a pipeline; the rotary joint is characterized in that a nozzle water pipe is fixed at the bottom end of the rotary joint, at least one nozzle is arranged on the nozzle water pipe, the center line of the nozzle coincides with the tangent line of the nozzle water pipe, and because the center line of the nozzle coincides with the tangent line of the nozzle water pipe, when the nozzle works, force along the tangent direction of the nozzle water pipe exists, the nozzle water pipe can start to rotate, so that materials in the reaction kettle are fully mixed.

Description

High-efficient stirring reactor system
Technical Field
The invention relates to the technical field of stirring equipment, in particular to a high-efficiency stirring reactor system.
Background
In chemical production, the reaction process of materials is usually carried out in a reaction kettle. The reaction kettle comprises a tank body and a stirring paddle arranged in the tank body, and the stirring paddle is connected with a gear motor at the upper end of the tank body through a transmission shaft. During operation, different reaction materials are added into the tank body, and the reducing motor drives the stirring paddle to rotate through the transmission shaft, so that stirring, mixing and reaction processes of the materials are completed. The existing reaction kettle has the following defects: 1. during charging, harmful gas in the reaction kettle overflows, so that the atmosphere is polluted, and the physical and mental health of people is influenced; 2. when the reducing motor drives the stirring paddle to stir the materials in the reaction kettle, the stirring is generally uneven and the blocks cannot be broken due to a large number of particles and blocks in the reaction kettle. 3. The existing reaction kettle has high energy consumption and low energy consumption utilization rate when in use.
Disclosure of Invention
The present invention is directed to a highly efficient stirred reactor system to solve the above-mentioned problems set forth in the background art.
In order to achieve the above purpose, the present invention provides the following technical solutions: the high-efficiency stirring reactor system comprises a reaction kettle, a heat exchanger and a stirring pump, wherein a rotary joint is fixed at the top end of the reaction kettle and is communicated with the heat exchanger through a pipeline, the heat exchanger is communicated with the stirring pump through a pipeline, and the stirring pump is communicated with the bottom of the reaction kettle through a pipeline; the bottom end of the rotary joint is fixedly provided with a nozzle water pipe, at least one nozzle is arranged on the nozzle water pipe, and the center line of the nozzle coincides with the tangent line of the nozzle water pipe.
As an optional embodiment of the present invention, optionally, the stirring pump includes a motor, a shaft, and a dispersion disc connected to the shaft, where the dispersion disc is disposed at a stirring pump feed inlet of the stirring pump.
As an optional embodiment of the invention, optionally, a feeding hole is arranged on a pipeline between the stirring pump and the reaction kettle, a discharging hole is arranged at the bottom of the reaction kettle, and a feeding hole is arranged at the top of the reaction kettle.
As an optional embodiment of the present invention, optionally, the dispersing disc is provided with a mounting through hole, a left flange and a right flange, and the left flange and the right flange are uniformly and mutually staggered on the outer circumference of the dispersing disc.
As an optional embodiment of the present invention, optionally, the rotary joint includes a fixing portion, a rotating portion, and a connecting portion, one end of the connecting portion is connected to the fixing portion, the other end is connected to the rotating portion, and the fixing portion, the rotating portion, and the connecting portion are internally communicated; the fixed part is fixedly connected with the reaction kettle, and the rotating part is communicated with the nozzle water pipe.
As an optional embodiment of the invention, optionally, the fixing part is a fixing tube, the connecting part is a ball bearing, the rotating part is a rotating tube, the rotating tube is fixedly connected with a bearing inner ring of the ball bearing, the fixing tube is fixedly connected with a bearing outer ring of the ball bearing, and the fixing tube is fixedly connected with the reaction kettle.
As an optional embodiment of the present invention, optionally, the nozzle includes a first nozzle pipe and a second nozzle pipe, and the first nozzle pipe and the second nozzle pipe are communicated through a connecting rod; the water outlet of the first nozzle pipeline is communicated with the water inlet of the second nozzle pipeline, the diameter of the water inlet of the first nozzle pipeline is larger than that of the water outlet of the first nozzle pipeline, and the diameter of the water inlet of the second nozzle pipeline is smaller than that of the water outlet of the second nozzle pipeline.
Compared with the prior art, the invention has the beneficial effects that:
1. according to the invention, the charging port is arranged on the pipeline between the reaction kettle and the stirring pump, so that no harmful gas overflows during charging;
2. according to the invention, the dispersing disc is arranged in the stirring pump, when solid or particulate matters pass through the dispersing disc, the left folded edge and the right folded edge on the dispersing disc can break the solid or particulate matters, meanwhile, the stirring pump is driven by the motor to rotate the dispersing disc, and the materials are broken by the stirring pump and have upward lift, so that the material flow speed is high, the pressure is high, and the materials can reenter the tank body, thereby being convenient for the materials to be circularly dissolved and mixed;
3. according to the invention, the nozzle water pipe is arranged in the reaction kettle, and the nozzle is arranged on the nozzle water pipe, so that the materials are smashed by the stirring pump and have upward lift, and the flow rate of the materials is high at the moment and the pressure is high, so that when the materials are sent into the nozzle water pipe by the stirring pump, the materials in the reaction kettle are more fully mixed under the action of the nozzle due to the higher flow rate of the materials at the moment.
4. The nozzle water pipe is connected with the rotary joint, and because the central line of the nozzle is coincident with the tangent line of the nozzle water pipe, when the nozzle works, the force along the tangent line direction of the nozzle water pipe is generated, the nozzle water pipe starts to rotate, and further, the materials in the reaction kettle are fully mixed.
Drawings
FIG. 1 is a schematic diagram of the structure of the present invention;
FIG. 2 is a schematic view of a portion of the structure of the present invention;
FIG. 3 is a schematic view of a structure of a dispersion disk according to the present invention;
FIG. 4 is a schematic diagram of a stirring pump according to the present invention;
FIG. 5 is a schematic view of a commercially available rotary joint for water according to the present invention;
FIG. 6 is a schematic view of the structure of the nozzle of the present invention;
FIG. 7 is a schematic view of a rotary joint according to the present invention;
fig. 8 is a schematic structural diagram of embodiment 2 of the present invention.
In the figure: 1. a reaction kettle; 2. a nozzle water pipe; 3. a nozzle; 31. a first nozzle pipe; 32. a second nozzle pipe; 33. a connecting rod; 4. a discharge port; 5. a rotary joint; 51. a fixing part; 52. a rotating part; 53. a connection part; 6. a heat exchanger; 7. a feed inlet; 8. a stirring pump; 81. a motor; 82. a shaft; 83. a dispersion plate; 831. mounting through holes; 832. a left edge folding; 833. right flanging; 84. a feed inlet of the stirring pump; 9. a feed inlet; 511. a fixed tube; 521. a ball bearing; 531. and (3) rotating the tube.
Detailed Description
In order to further describe the technical means and effects adopted by the present invention for achieving the intended purpose, the following detailed description will refer to the specific implementation, structure, characteristics and effects according to the present invention with reference to the accompanying drawings and preferred embodiments.
Example 1
As shown in fig. 1 to 6, a high-efficiency stirring reactor system comprises a reaction kettle 1, a heat exchanger 6 and a stirring pump 8, wherein a rotary joint 5 is fixed at the top end of the reaction kettle 1, the rotary joint 5 is communicated with the heat exchanger 6 through a pipeline, the heat exchanger 6 is communicated with the stirring pump 8 through a pipeline, and the stirring pump 8 is communicated with the bottom of the reaction kettle 1 through a pipeline; the bottom end of the rotary joint 5 is fixedly provided with a nozzle water pipe 2, at least one nozzle 3 is arranged on the nozzle water pipe 2, and the central line of the nozzle 3 coincides with the tangent line of the nozzle water pipe 2.
The rotating pipe 531 of the rotary joint 5 is communicated with the nozzle water pipe 2, the bottom of the nozzle water pipe 2 is sealed, a plurality of nozzles 3 are arranged around, all the nozzles 3 are arranged anticlockwise or clockwise along the tangential direction of the nozzle water pipe 2, when the rotary joint is used, materials enter the stirring pump 8 from the stirring pump feed inlet 84, particles and blocks in the materials are smashed through the dispersing disc 83, then the materials enter the heat exchanger 6 under the action of the stirring pump 8, reaction heat is taken away through the heat exchanger 6 and then enters the nozzle water pipe 2, at the moment, the materials are sprayed out of the nozzles 3, and because the number of the nozzles 3 is large, the direction is fixed, and under the continuous output of the stirring pump 8, all the nozzles 3 can give a thrust to the nozzle water pipe 2, so that the nozzle water pipe 2 can rotate to fully mix the materials in the reaction kettle 1; the process converts the energy of the stirring pump 8 into the kinetic energy of the nozzle water pipe 2, fully utilizes the energy output by the stirring pump 8 and improves the energy utilization rate.
The stirring pump 8 comprises a motor 81, a shaft 82 and a dispersion plate 83 connected with the shaft 82, wherein the dispersion plate 83 is arranged at a stirring pump feed inlet 84 of the stirring pump 8.
As shown in fig. 5, the dispersing plate 83 is fixed on the shaft 82, the motor 81 drives the dispersing plate 83 to rotate through the shaft 82, and in use, materials enter the dispersing plate 83 through the feeding hole 84 of the stirring pump to mix and break up the blocks and particles, and then are discharged through the discharging hole of the stirring pump 8 to enter the heat exchanger 6.
Be equipped with charge door 7 on the pipeline between stirring pump 8 and the reation kettle 1, reation kettle 1 bottom is equipped with discharge gate 4, reation kettle 1 top is equipped with feed inlet 9.
When in use, as shown in fig. 1, materials to be added can be added through the feed inlet 7, and the materials enter the nozzle water pipe 2 to enter the reaction kettle 1 for mixing after passing through the stirring pump 8.
The dispersing disc 83 is provided with a mounting through hole 831, a left folding edge 832 and a right folding edge 833, and the left folding edge 832 and the right folding edge 833 are uniformly and mutually staggered and arranged on the outer circumference of the dispersing disc 83.
As shown in fig. 3, four mounting through holes 831 are formed in the dispersion plate 83, the dispersion plate 83 is mounted on the shaft 82 of the motor 81 through the mounting through holes 831, and the left flange 832 and the right flange 833 are used for breaking up the blocks and particles in the material passing through the motor 81.
The rotary joint 5 comprises a fixed part 51, a rotating part 52 and a connecting part 53, wherein one end of the connecting part 53 is connected with the fixed part 51, the other end is connected with the rotating part 52, and the fixed part 51, the rotating part 52 and the connecting part 53 are communicated; the fixed part 51 is fixedly connected with the reaction kettle 1, and the rotating part 52 is communicated with the nozzle water pipe 2.
As shown in fig. 7, the fixing portion 51 is a fixing tube 511, the connecting portion 53 is a ball bearing 521, the rotating portion 52 is a rotating tube 531, the rotating tube 531 is fixedly connected to the inner ring of the ball bearing 521, the fixing tube 511 is fixedly connected to the outer ring of the ball bearing 521, and the fixing tube 511 is fixedly connected to the reaction kettle 1. When in use, the fixed pipe 511 is fixed on the top of the reaction kettle 1, the nozzle water pipe 2 in the reaction kettle 1 is communicated and fixed with the rotating pipe 531, the heat exchanger 6 is communicated and fixed with the fixed pipe 511, and the ball bearing 521 is sealed and protected to prevent materials from entering the ball bearing 521 and affecting the operation of the ball bearing 521; when the material enters the nozzle water pipe 2 through the ball bearing 521, the nozzle water pipe 2 rotates on the ball bearing 521 under the action of the stirring pump 8 and the nozzle 3.
The components that can realize the functions of the rotary joint 5 are all within the scope of the present embodiment, and as shown in fig. 5, the product is a commercially available rotary joint for water, and can also realize the functions. The rotary joint for water comprises a connecting part 53, a fixing part 51 and a rotating part 52, wherein a sealing element is arranged in the rotary joint, and the rotating part 52 can rotate relative to the fixing part 51.
The nozzle 3 comprises a first nozzle pipe 31 and a second nozzle pipe 32, and the first nozzle pipe 31 and the second nozzle pipe 32 are communicated through a connecting rod 33; the water outlet of the first nozzle pipe 31 is communicated with the water inlet of the second nozzle pipe 32, the diameter of the water inlet of the first nozzle pipe 31 is larger than that of the water outlet of the first nozzle pipe 31, and the diameter of the water inlet of the second nozzle pipe 32 is smaller than that of the water outlet of the second nozzle pipe 32.
As shown in fig. 6, the nozzle 3 is based on the principle of jet attraction, since the diameter of the water inlet of the first nozzle pipe 31 is larger than the diameter of the water outlet of the first nozzle pipe 31, the material is ejected from the conical nozzle of the first nozzle pipe 31 at a high speed, and meanwhile, since the connection part of the first nozzle pipe 31 and the second nozzle pipe 32 forms a guiding port, a low pressure area is formed around the guiding port, and the suction liquid is acted by the pressure difference and the hydraulic quantity of the area, so that the high-speed working jet and the sucked liquid are ejected together in the form of fluid delivery into the second nozzle pipe 32, thereby achieving the fluid mixing and stirring. In use, the first nozzle pipe 31 is communicated with the nozzle water pipe 2, the material in the nozzle water pipe 2 is sprayed into the second nozzle pipe 32 through the first nozzle pipe 31, and the connecting rod 33 is used for fixing the first nozzle pipe 31 on the second nozzle pipe 32.
Example 2
As shown in fig. 8, the other structures in this embodiment 2 are the same as those in embodiment 1, except that in this embodiment 2, the nozzle 3 is disposed obliquely in the Z-axis direction of the nozzle water pipe 2, specifically, the nozzle 3 is disposed with an included angle in the Z-axis direction of the nozzle water pipe 2, so that during mixing, the range of the spraying direction of the nozzle 3 is wider, and the materials in the reaction kettle 1 are mixed more fully.
The present invention is not limited to the above embodiments, but is capable of modification and variation in detail, and other modifications and variations can be made by those skilled in the art without departing from the scope of the present invention.

Claims (7)

1. The high-efficiency stirring reactor system comprises a reaction kettle (1), a heat exchanger (6) and a stirring pump (8), and is characterized in that a rotary joint (5) is fixed at the top end of the reaction kettle (1), the rotary joint (5) is communicated with the heat exchanger (6) through a pipeline, the heat exchanger (6) is communicated with the stirring pump (8) through a pipeline, and the stirring pump (8) is communicated with the bottom of the reaction kettle (1) through a pipeline;
the rotary joint is characterized in that a nozzle water pipe (2) is fixed at the bottom end of the rotary joint (5), at least one nozzle (3) is arranged on the nozzle water pipe (2), and the central line of the nozzle (3) coincides with the tangent line of the nozzle water pipe (2).
2. A high efficiency stirred reactor system according to claim 1, characterised in that the stirring pump (8) comprises a motor (81), a shaft (82) and a dispersion disc (83) connected to the shaft (82), the dispersion disc (83) being arranged at a stirring pump feed inlet (84) of the stirring pump (8).
3. The efficient stirring reactor system according to claim 1, wherein a feed inlet (7) is arranged on a pipeline between the stirring pump (8) and the reaction kettle (1), a discharge outlet (4) is arranged at the bottom of the reaction kettle (1), and a feed inlet (9) is arranged at the top of the reaction kettle (1).
4. An efficient agitation reactor system as recited in claim 2, wherein said dispersion disk (83) is provided with mounting through holes (831), left folded edges (832) and right folded edges (833), said left folded edges (832) and said right folded edges (833) being uniformly and alternately disposed on an outer circumference of said dispersion disk (83).
5. The efficient stirring reactor system according to claim 1, wherein the rotary joint (5) comprises a fixed part (51), a rotating part (52) and a connecting part (53), one end of the connecting part (53) is connected with the fixed part (51), the other end is connected with the rotating part (52), and the fixed part (51), the rotating part (52) and the connecting part (53) are communicated with each other;
the fixed part (51) is fixedly connected with the reaction kettle (1), and the rotating part (52) is communicated with the nozzle water pipe (2).
6. The efficient stirring reactor system as set forth in claim 5, wherein the fixing portion (51) is a fixing tube (511), the connecting portion (53) is a ball bearing (521), the rotating portion (52) is a rotating tube (531), the rotating tube (531) is fixedly connected with a bearing inner ring of the ball bearing (521), the fixing tube (511) is fixedly connected with a bearing outer ring of the ball bearing (521), and the fixing tube (511) is fixedly connected with the reaction kettle (1).
7. A high efficiency stirred reactor system according to claim 3, characterized in that the nozzle (3) comprises a first nozzle pipe (31) and a second nozzle pipe (32), the first nozzle pipe (31) and the second nozzle pipe (32) being in communication by means of a connecting rod (33);
the water outlet of the first nozzle pipeline (31) is communicated with the water inlet of the second nozzle pipeline (32), the diameter of the water inlet of the first nozzle pipeline (31) is larger than that of the water outlet of the first nozzle pipeline (31), and the diameter of the water inlet of the second nozzle pipeline (32) is smaller than that of the water outlet of the second nozzle pipeline (32).
CN202211410270.0A 2022-11-11 2022-11-11 High-efficient stirring reactor system Pending CN116440833A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202211410270.0A CN116440833A (en) 2022-11-11 2022-11-11 High-efficient stirring reactor system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202211410270.0A CN116440833A (en) 2022-11-11 2022-11-11 High-efficient stirring reactor system

Publications (1)

Publication Number Publication Date
CN116440833A true CN116440833A (en) 2023-07-18

Family

ID=87130832

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202211410270.0A Pending CN116440833A (en) 2022-11-11 2022-11-11 High-efficient stirring reactor system

Country Status (1)

Country Link
CN (1) CN116440833A (en)

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