CN214076221U - High-performance fluid mixing and stirring reaction kettle - Google Patents
High-performance fluid mixing and stirring reaction kettle Download PDFInfo
- Publication number
- CN214076221U CN214076221U CN202023171720.4U CN202023171720U CN214076221U CN 214076221 U CN214076221 U CN 214076221U CN 202023171720 U CN202023171720 U CN 202023171720U CN 214076221 U CN214076221 U CN 214076221U
- Authority
- CN
- China
- Prior art keywords
- kettle body
- reaction kettle
- pipe
- reation kettle
- fluid mixing
- 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.)
- Active
Links
Images
Abstract
The utility model belongs to the field of mechanical manufacturing of high-performance fluid mixing separation, in particular to a high-performance fluid mixing and stirring reaction kettle, which comprises a reaction kettle body, wherein a fixed frame is fixedly arranged on the upper end surface of the reaction kettle body, a motor is fixedly arranged inside the fixed frame, a reducer is fixedly arranged at the output end of the motor, the bottom end surface of the reducer is fixedly connected with a connecting shaft, the bottom end of the connecting shaft penetrates through the upper end surface of the reaction kettle body and extends to the inside of the reaction kettle body, a baffle is arranged below the connecting shaft, so that gas is added into the reaction kettle body through an air inlet pipe, the baffle separates the solution in the reaction kettle body, the solution in the reaction kettle body is prevented from blocking a vent pipe, the gas is circulated, and the unmixed gas enters the interior of the vent pipe through a plurality of air holes, so that the gas is circularly added into the solution in the reaction kettle body to be mixed, thereby achieving high-efficiency mixing.
Description
Technical Field
The utility model relates to a machine-building field of high performance fluid mixing separation, concretely relates to high performance fluid mixing stirring reation kettle.
Background
The chemical process is various chemical changes, it is premised on taking part in the thorough mixing of the reaction mass, to heating, cooling and physical change processes such as liquid extraction and gas absorption, often need to adopt the stirring operation to get good results, the stirring apparatus is used as the reactor in many occasions, in trades such as dyestuffs, medicine, pesticide, paint, etc., the use of the stirring apparatus is very extensive, the nonferrous metallurgy department has investigated and tested the power to the stirring apparatus in the national nonferrous metallurgy trade, the result is that more than 50% of the power consumption of many wet-process plants is used in stirring operation, the best method to save the power consumption of the stirring apparatus is: the reaction time is shortened.
The utility model discloses a high performance fluid mixes stirring reation kettle, the air inlet that is located the shaft coupling both sides is when letting in the air current, because the solution of reation kettle body can appear rocking and splashing under the circumstances of stirring, and then can block up the air inlet to influence gaseous circulation with higher speed and mix.
Disclosure of Invention
For solving the problem that proposes in the above-mentioned background art, the utility model provides a high performance fluid mixing stirring reation kettle has and adds gas to this internal through the intake pipe to reation kettle, and the baffle carries out the separation with this internal solution of reation kettle, avoids this internal solution of reation kettle to block the breather pipe, makes gas circulate to and the inside that the gas that does not mix gets into the breather pipe again then through a plurality of bleeder vents, thereby mix in adding this internal solution of reation kettle with gas circulation, and then reach the characteristics that the efficient mixes.
In order to achieve the above object, the utility model provides a following technical scheme: a high-performance fluid mixing and stirring reaction kettle comprises a reaction kettle body, wherein a fixing frame is fixedly arranged on the upper end face of the reaction kettle body, a motor is fixedly arranged in the fixing frame, a speed reducer is fixedly arranged at the output end of the motor, a connecting shaft is fixedly connected to the bottom end face of the speed reducer, the bottom end of the connecting shaft penetrates through the upper end face of the reaction kettle body and extends into the reaction kettle body, a partition plate is arranged below the connecting shaft, a rotating shaft is arranged below the partition plate, a plurality of connecting rods which are symmetrically distributed left and right are fixedly connected to the outer side wall of the rotating shaft, a stirring rod is fixedly connected to one end, which is relatively far away from the left and right, of each connecting rod, a plurality of self-suction type stirrers are fixedly arranged on the outer side of the rotating shaft, a vent pipe is embedded in the rotating shaft, a plurality of connecting pipes which are distributed in a vertically staggered manner are communicated with the outer side wall of the vent pipe, and the plurality of connecting pipes are respectively communicated with the plurality of self-suction type stirrers, the inside bottom fixed mounting of reation kettle body has the closing plate, and the bottom of axis of rotation runs through the closing plate and extends to the below of closing plate and installs in the bottom face of reation kettle body, and the bottom face through connection of closing plate has the discharging pipe, and the discharging pipe runs through the bottom face of reation kettle body and extends to the outside of reation kettle body, and the zone of heating is installed to the lateral wall of reation kettle body.
In order to add gaseous this internal solution of reation kettle in the convenience, as the utility model relates to a high performance fluid mixing stirring reation kettle is preferred, the top of axis of rotation run through the baffle and extend to the up end of baffle and with the bottom fixed connection of connecting axle, the top of breather pipe runs through the lateral wall at both ends about the axis of rotation respectively.
In order to make the gas circulation circulate, as the utility model relates to a high performance fluid mixing stirring reation kettle is preferred, and the up end of baffle runs through the bleeder vent of having seted up a plurality of evenly distributed, and the top face intercommunication of reation kettle body has the intake pipe, and the intake pipe is located the top of baffle, and the seal valve is installed to the lateral wall of intake pipe.
In order to make gaseous even distribution in this internal solution of reation kettle, as the utility model relates to a high performance fluid mixing stirring reation kettle is preferred, and the turbine is all installed to a plurality of inside from inhaling the formula agitator.
In order to carry out the even heating with the reation kettle body, make the reaction more abundant, as the utility model relates to a high performance fluid mixing stirring reation kettle is preferred, and the left end intercommunication of zone of heating lateral wall has the inlet tube, and the right-hand member intercommunication of zone of heating lateral wall has the outlet pipe.
For the convenient inside chemical reactant that adds to the reation kettle body, as the utility model relates to a high performance fluid mixing stirring reation kettle is preferred, the top intercommunication of reation kettle body lateral wall has the inlet pipe, and the inlet pipe is located the below of baffle.
Compared with the prior art, the beneficial effects of the utility model are that:
1. this kind of high performance fluid mixes stirring reation kettle adds chemical reactant to the inside of reation kettle body through the inlet pipe, opens the seal valve after that, adds gas to this internal through the intake pipe to reation kettle, and the baffle carries out the separation with this internal solution of reation kettle, avoids this internal solution of reation kettle to block the breather pipe, drives the connecting axle through the motor and drives the axis of rotation and rotate, makes the puddler stir this internal solution of reation kettle.
2. This kind of high performance fluid mixes stirring reation kettle, because a plurality of turbines rotate, the negative pressure of production makes the air current of baffle top pass through the inside that the breather pipe got into a plurality of connecting pipes, and then mutually support with the axis of rotation through a plurality of self-priming stirrers, make self-priming stirrers carry out quick mixture with this internal solution of reation kettle with gaseous fast-speed the throwing away, and then reach the effect that the efficient mixes, the gas that does not mix gets into the inside of breather pipe again through a plurality of bleeder vents then, thereby mix in adding this internal solution of reation kettle with gas circulation, add hot water through the inlet tube in the inside of zone of heating, hot water carries out the even heating with the reation kettle body, make the reaction more abundant.
To sum up, this kind of high performance fluid mixes stirring reation kettle adds gas to this internal through the intake pipe to reation kettle, and the baffle carries out the separation with this internal solution of reation kettle, avoids this internal solution of reation kettle to block the breather pipe, makes gas circulate to and the inside that the gas of unmixing got into the breather pipe again then through a plurality of bleeder vents, thereby mixes in adding this internal solution of reation kettle with gas circulation, and then reaches the effect that the efficient mixes.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present application, the drawings needed to be used in the embodiments or the prior art descriptions will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present application, and it is obvious for those skilled in the art to obtain other drawings based on these drawings without inventive exercise.
FIG. 1 is a perspective view of a high performance fluid mixing and stirring reactor of the present invention;
FIG. 2 is a sectional view of a high performance fluid mixing and stirring reactor of the present invention;
fig. 3 is a plan view of the separator of the present invention.
The symbols in the figures indicate:
1. a reaction kettle body; 101. a feed pipe; 102. an air inlet pipe; 103. a sealing valve; 2. a fixing frame; 201. a motor; 202. a speed reducer; 3. a connecting shaft; 4. a rotating shaft; 401. a breather pipe; 5. a partition plate; 501. air holes are formed; 6. a connecting rod; 601. a stirring rod; 7. a connecting pipe; 701. a self-priming agitator; 702. a turbine; 8. a heating layer; 801. a water inlet pipe; 802. a water outlet pipe; 9. a sealing plate; 901. and (4) discharging the pipe.
Detailed Description
In order to make the technical problems, technical solutions and advantageous effects to be solved by the present application clearer, the present application is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the present application and are not intended to limit the present application.
Referring to fig. 1-3, the present invention provides the following technical solutions: a high-performance fluid mixing and stirring reaction kettle comprises a reaction kettle body 1, wherein a fixed frame 2 is fixedly installed on the upper end face of the reaction kettle body 1, a motor 201 is fixedly installed inside the fixed frame 2, a speed reducer 202 is fixedly installed at the output end of the motor 201, a connecting shaft 3 is fixedly connected to the bottom end face of the speed reducer 202, the bottom end of the connecting shaft 3 penetrates through the upper end face of the reaction kettle body 1 and extends into the reaction kettle body 1, a partition plate 5 is installed below the connecting shaft 3, a rotating shaft 4 is arranged below the partition plate 5, a plurality of connecting rods 6 which are symmetrically distributed left and right are fixedly connected to the outer side wall of the rotating shaft 4, a stirring rod 601 is fixedly connected to one end of each connecting rod 6 which is relatively far away from the left and right, a plurality of self-suction type stirrers 701 are fixedly installed on the outer side of the rotating shaft 4, a ventilating pipe 401 is embedded in the rotating shaft 4, a plurality of connecting pipes 7 which are staggered and distributed up and down are communicated to the outer side wall of the connecting pipe, a plurality of connecting pipes 7 communicate with a plurality of from inhaling formula agitator 701 respectively, the inside bottom fixed mounting of reation kettle body 1 has closing plate 9, the bottom of axis of rotation 4 runs through closing plate 9 and extends to the below of closing plate 9 and installs in the bottom face of reation kettle body 1, the bottom face through connection of closing plate 9 has discharging pipe 901, discharging pipe 901 runs through the bottom face of reation kettle body 1 and extends to the outside of reation kettle body 1, zone of heating 8 is installed to reation kettle body 1's lateral wall.
In this embodiment: the self-suction type stirrer 701 (model: MZX) adds gas into the reaction kettle body 1 through the air inlet pipe 102, the baffle plate 5 separates the solution in the reaction kettle body 1, the solution in the reaction kettle body 1 is prevented from blocking the vent pipe 401, the connecting shaft 3 is driven by the motor 201 to drive the rotating shaft 4 to rotate, the stirring rod 601 is promoted to stir the solution in the reaction kettle body 1, at the moment, as the turbines 702 rotate, the generated negative pressure enables the airflow above the baffle plate 5 to enter the inside of the connecting pipes 7 through the vent pipe 401, and then the self-suction type stirrers 701 and the rotating shaft 4 are mutually matched, so that the self-suction type stirrer 701 throws the gas out at high speed to be rapidly mixed with the solution in the reaction kettle body 1, the unmixed gas enters the interior of the vent pipe 401 through the vent holes 501, and the gas is circularly added into the solution in the reaction kettle body 1 to be mixed, through inlet tube 801 at the inside of zone of heating 8 add hot water, hot water carries out the even heating with reation kettle body 1, makes the reaction more abundant.
As a technical optimization scheme of the utility model, baffle 5 is run through on the top of axis of rotation 4 and extend to baffle 5 the up end and with the bottom fixed connection of connecting axle 3, the lateral wall at both ends about axis of rotation 4 is run through respectively on the top of breather pipe 401.
In this embodiment: carry out the separation through baffle 5 with the solution in the reation kettle body 1, the inside that the air current of baffle 5 top passes through breather pipe 401 and gets into a plurality of connecting pipes 7, and then lets in a plurality of inside from inhaling formula agitator 701, throws away the solution of evenly distributed in reation kettle body 1 that gaseous is fast-speed.
As a technical optimization scheme of the utility model, the up end of baffle 5 runs through the bleeder vent 501 who sets up a plurality of evenly distributed, and the top face intercommunication of reation kettle body 1 has intake pipe 102, and intake pipe 102 is located the top of baffle 5, and seal valve 103 is installed to the lateral wall of intake pipe 102.
In this embodiment: the sealing valve 103 is opened, gas is added into the reaction kettle body 1 through the gas inlet pipe 102, so that the gas enters the self-suction type stirrer 701 through the vent pipe 401, and after the gas is thrown out from the self-suction type stirrer 701, the gas enters the vent pipe 401 through the plurality of gas holes 501, so that the gas circulates.
As a technical optimization scheme of the present invention, a plurality of self-suction agitators 701 are all provided with a turbine 702 inside.
In this embodiment: the turbines 702 rotate, and the generated negative pressure enables gas to pass through the self-suction stirrer 701 at a high speed, so that the gas is thrown out at a high speed to be mixed with the solution in the reaction kettle body 1, and the efficient mixing effect is achieved.
As a technical optimization scheme of the utility model, the left end intercommunication of zone of heating 8 lateral wall has inlet tube 801, and the right-hand member intercommunication of zone of heating 8 lateral wall has outlet pipe 802.
In this embodiment: through inlet tube 801 at the inside of zone of heating 8 add hot water, hot water carries out the even heating with reation kettle body 1, makes the reaction more abundant.
As a technical optimization scheme of the utility model, the top intercommunication of 1 lateral wall of reation kettle body has inlet pipe 101, and inlet pipe 101 is located the below of baffle 5.
In this embodiment: by arranging the feed pipe 101 below the partition plate 5, chemical reactants are conveniently added into the reaction kettle body 1 through the feed pipe 101.
The utility model discloses a theory of operation and use flow: firstly, chemical reactants are added into a reaction kettle body 1 through a feeding pipe 101, then a sealing valve 103 is opened, gas is added into the reaction kettle body 1 through an air inlet pipe 102, a solution in the reaction kettle body 1 is blocked by a partition plate 5, the solution in the reaction kettle body 1 is prevented from blocking a vent pipe 401, a connecting shaft 3 is driven by a motor 201 to drive a rotating shaft 4 to rotate, the solution in the reaction kettle body 1 is stirred by a stirring rod 601, at the moment, the air flow above the partition plate 5 enters the inside of a plurality of connecting pipes 7 through the vent pipe 401 due to the rotation of a plurality of turbines 702, and then the air flow is matched with the rotating shaft 4 through a plurality of self-suction stirrers 701, so that the gas is thrown out at high speed and uniformly distributed in the solution in the reaction kettle body 1, and further, the efficient mixing effect is achieved, the unmixed gas enters the interior of the vent pipe 401 through a plurality of vent holes 501, thereby mix in adding the solution in reation kettle body 1 with gas circulation, add hot water through inlet tube 801 in the inside of zone of heating 8, hot water carries out the even heating with reation kettle body 1, makes the reaction more abundant.
In the description of the present invention, it is to be understood that the terms "length", "width", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like indicate orientations or positional relationships based on those shown in the drawings, and are merely for convenience of description and simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention. In addition, in the description of the present invention, "a plurality" means two or more unless specifically limited otherwise.
The above description is only exemplary of the present application and should not be taken as limiting the present application, as any modification, equivalent replacement, or improvement made within the spirit and principle of the present application should be included in the protection scope of the present application.
Claims (6)
1. The utility model provides a high performance fluid mixing stirring reation kettle, includes reation kettle body (1), its characterized in that: the automatic stirring device is characterized in that a fixed frame (2) is fixedly mounted on the upper end face of the reaction kettle body (1), a motor (201) is fixedly mounted inside the fixed frame (2), a speed reducer (202) is fixedly mounted on the output end of the motor (201), a connecting shaft (3) is fixedly connected to the bottom end face of the speed reducer (202), the bottom end of the connecting shaft (3) penetrates through the upper end face of the reaction kettle body (1) and extends into the reaction kettle body (1), a partition plate (5) is mounted below the connecting shaft (3), a rotating shaft (4) is arranged below the partition plate (5), a plurality of connecting rods (6) which are distributed in bilateral symmetry are fixedly connected to the outer side wall of the rotating shaft (4), a plurality of stirring rods (601) which are fixedly connected to the left and right of the connecting rods (6) and are relatively far away from the left and right, and a plurality of self-suction type stirrers (701) are fixedly mounted on the outer side of the rotating shaft (4), breather pipe (401) are installed in the inside embedding of axis of rotation (4), the lateral wall intercommunication of breather pipe (401) has a plurality of connecting pipe (7) of staggering distribution from top to bottom, and is a plurality of connecting pipe (7) communicate with a plurality of self-priming stirrers (701) respectively, the inside bottom fixed mounting of reation kettle body (1) has closing plate (9), the bottom of axis of rotation (4) runs through closing plate (9) and extends to the below of closing plate (9) and installs in the bottom face of reation kettle body (1), the bottom face through connection of closing plate (9) has discharging pipe (901), discharging pipe (901) run through the bottom face of reation kettle body (1) and extend to the outside of reation kettle body (1), zone of heating (8) are installed to the lateral wall of reation kettle body (1).
2. The high performance fluid mixing and stirring reactor as set forth in claim 1, wherein: the top end of the rotating shaft (4) penetrates through the partition plate (5) and extends to the upper end face of the partition plate (5) and is fixedly connected with the bottom end of the connecting shaft (3), and the top end of the vent pipe (401) penetrates through the outer side walls of the left end and the right end of the rotating shaft (4) respectively.
3. The high performance fluid mixing and stirring reactor as set forth in claim 1, wherein: the air inlet pipe is characterized in that a plurality of uniformly distributed air holes (501) are formed in the upper end face of the partition plate (5) in a penetrating mode, the top end face of the reaction kettle body (1) is communicated with an air inlet pipe (102), the air inlet pipe (102) is located above the partition plate (5), and a sealing valve (103) is installed on the outer side wall of the air inlet pipe (102).
4. The high performance fluid mixing and stirring reactor as set forth in claim 1, wherein: turbines (702) are installed inside the self-suction type stirrers (701).
5. The high performance fluid mixing and stirring reactor as set forth in claim 1, wherein: the left end intercommunication of zone of heating (8) lateral wall has inlet tube (801), the right-hand member intercommunication of zone of heating (8) lateral wall has outlet pipe (802).
6. The high performance fluid mixing and stirring reactor as set forth in claim 1, wherein: the top intercommunication of reation kettle body (1) lateral wall has inlet pipe (101), inlet pipe (101) are located the below of baffle (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023171720.4U CN214076221U (en) | 2020-12-24 | 2020-12-24 | High-performance fluid mixing and stirring reaction kettle |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202023171720.4U CN214076221U (en) | 2020-12-24 | 2020-12-24 | High-performance fluid mixing and stirring reaction kettle |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN214076221U true CN214076221U (en) | 2021-08-31 |
Family
ID=77432839
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202023171720.4U Active CN214076221U (en) | 2020-12-24 | 2020-12-24 | High-performance fluid mixing and stirring reaction kettle |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214076221U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023246125A1 (en) * | 2022-06-23 | 2023-12-28 | 海安南京大学高新技术研究院 | Reaction kettle, and coating preparation method using reaction kettle |
-
2020
- 2020-12-24 CN CN202023171720.4U patent/CN214076221U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2023246125A1 (en) * | 2022-06-23 | 2023-12-28 | 海安南京大学高新技术研究院 | Reaction kettle, and coating preparation method using reaction kettle |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN214076221U (en) | High-performance fluid mixing and stirring reaction kettle | |
| CN208711598U (en) | A kind of top center aeration mixing device | |
| CN207371511U (en) | A kind of double-deck paddle Self-suction Type Stirred Tank of Gas-Liquid Dispersion | |
| CN209155859U (en) | It is a kind of for producing the circulating consersion unit of chemical liquid | |
| CN207822903U (en) | A kind of self-suction mixing reactor | |
| KR100581748B1 (en) | Fluid Supply Equipments with the Function of Self-priming and Mixing and the Aerators with using the equipments | |
| CN215743021U (en) | High homogeneity emulsification tank of cosmetics production usefulness | |
| CN213556983U (en) | Waterborne PVB emulsion reation kettle agitated vessel | |
| CN212189059U (en) | Kettle type stirring reactor | |
| CN216419007U (en) | Slurry conditioning and mixing device | |
| CN209155622U (en) | A kind of constant temperature mixing plant applied to chemical liquid production | |
| CN209872533U (en) | Aeration tank | |
| CN207153551U (en) | A kind of agitator with cooling device | |
| CN214076434U (en) | Stirring reation kettle uses inside air guide device | |
| CN210058227U (en) | Energy-saving cleaning agent preparation system | |
| CN219252493U (en) | Automatic ammonia absorber for ammonia water preparation | |
| CN219849604U (en) | High-efficiency cyclone mixed liquid medicine reactor | |
| CN213376159U (en) | Cooling device for mixer | |
| CN213791434U (en) | Automobile-used urea preparation facilities with prevention crystallization | |
| CN210787348U (en) | A reation kettle for producing curing agent | |
| CN214319800U (en) | Raw material stirring device for urea aqueous solution production | |
| CN217940189U (en) | Hierarchical cooling system of reation kettle | |
| CN216321586U (en) | Full-automatic dosing device | |
| CN210448825U (en) | Device is used in dilute acid production | |
| CN213160790U (en) | Pipeline reactor for fine chemical production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |