CN203648423U - Mixing tank - Google Patents
Mixing tank Download PDFInfo
- Publication number
- CN203648423U CN203648423U CN201320807556.2U CN201320807556U CN203648423U CN 203648423 U CN203648423 U CN 203648423U CN 201320807556 U CN201320807556 U CN 201320807556U CN 203648423 U CN203648423 U CN 203648423U
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- shaft
- kettle
- stirred tank
- tank body
- cooling water
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- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The utility model discloses a mixing tank, which comprises a tank body and a stirring mechanism arranged in the tank body, wherein a liquid feed pipe, a powder feed inlet, a manhole and a pressure gauge are arranged at the top of the tank body respectively, a material outlet is formed in the bottom of the tank body, the tank body is externally sheathed with a jacket, and a cooling water inlet and a cooling water outlet are formed in the jacket; the material outlet is connected with a material circulating pipe which is positioned outside the tank body and communicated with the top of the tank body; the stirring mechanism comprises a first stirring shaft, a second stirring shaft and a third stirring shaft, the first stirring shaft is perpendicularly arranged in the middle of the tank body, and the second stirring shaft and the third stirring shaft are respectively arranged on two sides of the first stirring shaft, the first stirring shaft is connected with a scraper plate type stirring paddle, a scraper plate of the scraper plate type stirring paddle is clung to the inner wall of the tank body. The stirring tank is applicable for producing viscous liquid products with high solid content such as plastic sol and damping coatings, capable of promoting the quality of the product, and enabling the product to be exquisite and stable in performance.
Description
Technical field
The utility model relates to a kind of stirred tank, is applicable to produce plastisol and the high rheid product of damping paint class viscosity.
Background technology
The rheid product of the high solids content of plastisol and damping paint class, is mainly used in automobile main frame maker, plays the effect of sealing corrosion, dust-separation waterproof and damping noise-reducing.Conventionally require prepared material exquisiteness, there is certain viscosity, and stable performance.
The feature of plastisol and damping paint series products requires the production equipment stirred tank using that the wider range of speeds can be provided, and makes the different phase of production process can adopt applicable speed of agitator, reaches the object that material fully disperses and stirs.Need to there is cooling water system with timer, the material in production process is controlled to desirable temperature range all the time, guarantee the stable performance of finished product within the whole quality guarantee period.In addition, device also needs to be equipped with circulating pipe system, and this can make there is no dead angle in the material mixed process in stirred tank, and whole system is fully stirred.But also do not meet in the market the stirred tank of all requirements.
Summary of the invention
The purpose of this utility model is to overcome the defect of prior art and a kind of stirred tank is provided, be applicable to produce plastisol and the high rheid material of damping paint class viscosity, can more dispersed material, simultaneously at the cooling water layer of the outer design of still body, product can be kept in process of production compared with stationary temperature, make prepared product there is stable performance.
The technical scheme that realizes above-mentioned purpose is: a kind of stirred tank, comprise kettle and be arranged on the rabbling mechanism in kettle, the top of described kettle is respectively arranged with liquid material feed pipe, powder dog-house, manhole and Pressure gauge, and the bottom of described kettle is provided with material outlet;
There is chuck at described kettle overcoat, on described chuck, have cooling water inlet and coolant outlet;
On described material outlet, connect a Matter Transfer pipe, this Matter Transfer pipe is positioned at the outside of described kettle and is communicated with the top of described kettle;
Described rabbling mechanism comprises the first shaft of the centre that is vertically set on described kettle and divides the second shaft and the 3rd shaft that are located at the first shaft both sides, and described the second shaft and all vertical settings of the 3rd shaft, on described the first shaft, connect scraper-type stirring arm, the fit inwall of described kettle of the scraper plate of described scraper-type stirring arm, on described the second shaft, be socketed some Monolayer Dispersion dishes, on described the 3rd shaft, be socketed some double-deck dispersion impellers.
In above-mentioned a kind of stirred tank, the equal indentation in the edge of described Monolayer Dispersion dish and the edge of described double-deck dispersion impeller.
In above-mentioned a kind of stirred tank, described the first shaft is stirring at low speed axle, and described the second shaft and the 3rd shaft are high-speed stirred axle.
In above-mentioned a kind of stirred tank, on described cooling water inlet, cooling water valve is set, on described Matter Transfer pipe, circulation line valve is set.
In above-mentioned a kind of stirred tank, described stirred tank also comprises the controller being arranged on outside described kettle, and described controller is electrically connected with described the first shaft, the second shaft, the 3rd shaft, cooling water valve and circulation line valve respectively.
In above-mentioned a kind of stirred tank, at the top of described kettle, one temperature sensor is set, described temperature sensor is electrically connected with described controller.
In above-mentioned a kind of stirred tank, described kettle forms at the bottom of by columniform kettle body and conical still, is arranged on the bottom of described kettle body at the bottom of described still.
Stirred tank of the present utility model, be applicable to produce plastisol and the high rheid product of damping paint class viscosity, also be applicable to the production of the high viscosity product such as paint in building trade, can more dispersed material, simultaneously at the cooling water layer of the outer design of still body, product can be kept in process of production compared with stationary temperature, make prepared product there is stable performance.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model (vertical cross section).
Detailed description of the invention
In order to make those skilled in the art can understand better the technical solution of the utility model, below in conjunction with accompanying drawing, the utility model is described in further detail.
Refer to Fig. 1, embodiment of the present utility model, a kind of stirred tank, comprises kettle 1 and is arranged on the rabbling mechanism in kettle, the top of kettle 1 is respectively arranged with liquid material feed pipe 2, powder dog-house, manhole and Pressure gauge 3, and the bottom of kettle 1 is provided with material outlet 4; Kettle 1 overcoat has chuck 5, has cooling water inlet and coolant outlet on chuck 5, and cooling water valve is set on cooling water inlet; On material outlet 4, connect a Matter Transfer pipe 6, this Matter Transfer pipe 6 is positioned at the outside of kettle 1 and is communicated with the top of kettle 1, and circulation line valve 61 is set on Matter Transfer pipe 6; Rabbling mechanism comprises the first shaft 7 of the centre that is vertically set on kettle 1 and divides the second shaft 8 and the 3rd shaft 9 that are located at the first shaft 7 both sides, and the second shaft 8 and all vertical settings of the 3rd shaft 9, on the first shaft 7, connect scraper-type stirring arm, the fit inwall of kettle 1 of the scraper plate 71 of scraper-type stirring arm, on the second shaft 8, be socketed on some Monolayer Dispersion dish 81, the three shafts 9 and be socketed some double-deck dispersion impellers 91.The equal indentation in edge of the edge of Monolayer Dispersion dish 81 and double-deck dispersion impeller 91, by high speed shear, the powder in material is dispersed in liquid material when rotation.The first shaft 7 is stirring at low speed axle, the second shaft 8 and the 3rd shaft 9 are high-speed stirred axle, scraper-type paddle 71 stirring at low speed, Monolayer Dispersion dish 81 and double-deck dispersion impeller 91 high-speed stirred, pass through triple interaction, turbulence effect in increase system mixed process, reaches the object of rapid dispersion, is convenient to raise the efficiency.On material outlet 4, also connect a discharge nozzle, for the discharging of final products.
Preferably, stirred tank also comprises the controller being arranged on outside kettle 1, and controller is electrically connected with the first shaft 7, the second shaft 8, the 3rd shaft 9, cooling water valve and circulation line valve 61 respectively.The top of kettle arranges a temperature sensor, and temperature sensor is also electrically connected with controller.Controller is mainly used in:
1) control mixing speed, control the rotating speed of the first shaft 7, the second shaft 8, the 3rd shaft 9, thereby control the rotating speed of scraper-type paddle 71, Monolayer Dispersion dish 81, double-deck dispersion impeller 91;
2) the temperature upper and lower limit while setting cooling water valve open and close;
3) open and close of control cooling water valve, when material temperature in stirred tank is higher than temperature upper limit, controller is opened cooling water valve automatically, and when material temperature is lower than lowest temperature, controller cuts out cooling water valve automatically;
4) open and close of circulation line valve 61.
Controller can also be used for controlling the extraction amount of liquid material, the discharging control of final products etc.
Preferably, kettle 1 12 forms at the bottom of by columniform kettle body 11 and conical still, 12 bottoms that are arranged on kettle body 11 at the bottom of still.
Stirred tank of the present utility model, when use, arranges other required auxiliary devices outward at stirred tank, and the discharging pump of exporting as the mateiral pump for delivery of liquid material, for final products etc., use the production process of stirred tank of the present utility model as follows:
1) the temperature bound of produced product is set on controller, when material temperature in stirred tank is higher than the upper limit, controller is opened cooling water valve automatically, when material temperature is lower than lower limit, controller cuts out cooling water valve automatically, and product can be kept in process of production compared with stationary temperature;
2) by mateiral pump by the first liquid material by liquid material feed pipe 2 suction kettlies 1, open high speed dispersion, start the second shaft 8 and the 3rd shaft 9, make Monolayer Dispersion dish 81 and double-deck dispersion impeller 91 High Rotation Speeds, make liquid material dispersed, and add successively follow-up liquid material by mateiral pump;
3) open stirring at low speed, start the first shaft 7, make scraper-type paddle 71 low speed rotation, stir a period of time (as 2 minutes), add successively required auxiliary agent;
4) improve the stir speed (S.S.) of each shaft, add successively required powder from powder dog-house, after completing, constant speed stirs a period of time (as 10 minutes);
5) ON cycle pipe valve 61, at the bottom of still, 12 material is delivered to the top of kettle by Matter Transfer pipeline 6, and again falls in kettle 1, and stirred tank base material is stirred, this can make there is no dead angle in the material mixed process in stirred tank, and whole system is fully stirred;
6) close circulation line valve 62, closing high-speed stirs, and the second shaft 8 and the 3rd shaft 9 stop operating, and opens discharging pump;
7) discharging finishes, and closes discharging pump, closes stirring at low speed, and the first shaft 7 stops operating.
In sum, stirred tank of the present utility model, be applicable to produce plastisol and the high rheid product of damping paint class viscosity, also be applicable to the production of the high viscosity product such as paint in building trade, adopt controller control mixing speed, the wider range of speeds can be provided, make the different phase of production process can adopt applicable speed of agitator, reach the object that material fully disperses and stirs, can more dispersed material, there is chuck at kettle overcoat simultaneously, in chuck, be connected with cooling water, product can be kept in process of production compared with stationary temperature, make prepared product there is stable performance, in material mixed process in stirred tank, there is no dead angle simultaneously, whole system is fully stirred.
Above embodiment is only for illustration of the utility model, but not to restriction of the present utility model, person skilled in the relevant technique, in the situation that not departing from spirit and scope of the present utility model, can also make various conversion or modification, therefore all technical schemes that are equal to also should belong to category of the present utility model, should be limited by each claim.
Claims (7)
1. a stirred tank, comprises kettle and is arranged on the rabbling mechanism in described kettle, the top of described kettle is respectively arranged with liquid material feed pipe, powder dog-house, manhole and Pressure gauge, and the bottom of described kettle is provided with material outlet, it is characterized in that,
There is chuck at described kettle overcoat, on described chuck, have cooling water inlet and coolant outlet;
On described material outlet, connect a Matter Transfer pipe, this Matter Transfer pipe is positioned at the outside of described kettle and is communicated with the top of described kettle;
Described rabbling mechanism comprises the first shaft of the centre that is vertically set on described kettle and divides the second shaft and the 3rd shaft that are located at the first shaft both sides, and described the second shaft and all vertical settings of the 3rd shaft, on described the first shaft, connect scraper-type stirring arm, the fit inwall of described kettle of the scraper plate of described scraper-type stirring arm, on described the second shaft, be socketed some Monolayer Dispersion dishes, on described the 3rd shaft, be socketed some double-deck dispersion impellers.
2. a kind of stirred tank according to claim 1, is characterized in that, the equal indentation in the edge of described Monolayer Dispersion dish and the edge of described double-deck dispersion impeller.
3. a kind of stirred tank according to claim 1, is characterized in that, described the first shaft is stirring at low speed axle, and described the second shaft and the 3rd shaft are high-speed stirred axle.
4. a kind of stirred tank according to claim 1 and 2, is characterized in that, on described cooling water inlet, cooling water valve is set, and on described Matter Transfer pipe, circulation line valve is set.
5. a kind of stirred tank according to claim 4, it is characterized in that, described stirred tank also comprises the controller being arranged on outside described kettle, and described controller is electrically connected with described the first shaft, the second shaft, the 3rd shaft, cooling water valve and circulation line valve respectively.
6. a kind of stirred tank according to claim 5, is characterized in that, at the top of described kettle, one temperature sensor is set, and described temperature sensor is electrically connected with described controller.
7. a kind of stirred tank according to claim 6, is characterized in that, described kettle forms at the bottom of by columniform kettle body and conical still, is arranged on the bottom of described kettle body at the bottom of described still.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320807556.2U CN203648423U (en) | 2013-12-10 | 2013-12-10 | Mixing tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320807556.2U CN203648423U (en) | 2013-12-10 | 2013-12-10 | Mixing tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203648423U true CN203648423U (en) | 2014-06-18 |
Family
ID=50914866
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320807556.2U Expired - Fee Related CN203648423U (en) | 2013-12-10 | 2013-12-10 | Mixing tank |
Country Status (1)
| Country | Link |
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| CN (1) | CN203648423U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104399400A (en) * | 2014-12-15 | 2015-03-11 | 蔡澳明 | Integrated printing adhesive cement manufacturing equipment |
| CN104984708A (en) * | 2015-06-24 | 2015-10-21 | 张家港市顺佳隔热技术有限公司 | High-speed mixing reaction kettle |
| CN105478032A (en) * | 2015-09-10 | 2016-04-13 | 湖州格尔泰斯环保技术有限公司 | Polytetrafluoroethylene renewable powder material mixing machine |
| CN105664758A (en) * | 2016-02-16 | 2016-06-15 | 北京泛博清洁技术研究院有限公司 | High cut disperse emulsification tank and application method thereof |
| CN106732008A (en) * | 2017-02-22 | 2017-05-31 | 康福民 | A kind of high force dispersion machine |
| CN108079926A (en) * | 2017-12-27 | 2018-05-29 | 郑州仁宏医药科技有限公司 | A kind of environment-friendly type reaction kettle |
| CN109395652A (en) * | 2018-11-05 | 2019-03-01 | 浙江长城搅拌设备股份有限公司 | Breaking high-speed stirring apparatus |
-
2013
- 2013-12-10 CN CN201320807556.2U patent/CN203648423U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104399400A (en) * | 2014-12-15 | 2015-03-11 | 蔡澳明 | Integrated printing adhesive cement manufacturing equipment |
| CN104984708A (en) * | 2015-06-24 | 2015-10-21 | 张家港市顺佳隔热技术有限公司 | High-speed mixing reaction kettle |
| CN105478032A (en) * | 2015-09-10 | 2016-04-13 | 湖州格尔泰斯环保技术有限公司 | Polytetrafluoroethylene renewable powder material mixing machine |
| CN105664758A (en) * | 2016-02-16 | 2016-06-15 | 北京泛博清洁技术研究院有限公司 | High cut disperse emulsification tank and application method thereof |
| CN106732008A (en) * | 2017-02-22 | 2017-05-31 | 康福民 | A kind of high force dispersion machine |
| CN108079926A (en) * | 2017-12-27 | 2018-05-29 | 郑州仁宏医药科技有限公司 | A kind of environment-friendly type reaction kettle |
| CN109395652A (en) * | 2018-11-05 | 2019-03-01 | 浙江长城搅拌设备股份有限公司 | Breaking high-speed stirring apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140618 Termination date: 20181210 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |