CN200998649Y - Agitating mechanism - Google Patents
Agitating mechanism Download PDFInfo
- Publication number
- CN200998649Y CN200998649Y CNU2006201549750U CN200620154975U CN200998649Y CN 200998649 Y CN200998649 Y CN 200998649Y CN U2006201549750 U CNU2006201549750 U CN U2006201549750U CN 200620154975 U CN200620154975 U CN 200620154975U CN 200998649 Y CN200998649 Y CN 200998649Y
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- CN
- China
- Prior art keywords
- agitator tank
- baffle plate
- liquid
- stirred
- inwall
- 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.)
- Expired - Fee Related
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Abstract
The utility model discloses a stirring mechanism. A rotary device is arranged in a stirring tank, and a baffle plate is arranged at the middle upper part of the inner wall of the stirring tank. The collision possibility of stirred liquid can be improved through the baffle plate in the stirring mechanism of the model utility, simultaneously to ensure the up and down convection to occurr on a liquid sample, and the stirring effect is enhanced.
Description
Technical field
The utility model relates to a kind of plant equipment, relates in particular to a kind of rabbling mechanism.
Background technology
What rabbling mechanism was a large amount of applies in the industries such as paint, printing and dyeing, building materials, pharmacy, its course of work is: object to be stirred is placed in the agitator tank, in agitator tank, be provided with whirligig, be stirred liquid at high speed rotation as drives such as high speed rotational blade, impeller, screws, make by the whirligig in the agitator tank to be stirred the effect that liquid reaches dispersions, even, stirring.But rabbling mechanism of the prior art still has following shortcoming: existing rabbling mechanism is to be stirred liquid by the whirligig drive to carry out the purpose that high speed rotary reaches stirring, so agitator tank is generally cylindrical, this not only is beneficial to the processing of agitator tank, also be in order in whipping process, to reduce energy consumption, so cause being stirred liquid in agitator tank in the high speed rotary, though it is fast to be stirred the liquid rotary speed, but owing to lack sufficient collision, that is to say, be stirred liquid and in agitator tank, dally, so mixing effect is unsatisfactory.
Summary of the invention
The rabbling mechanism that provides a kind of mixing effect better is provided the purpose of this utility model.
The utility model is achieved through the following technical solutions:
A kind of rabbling mechanism is provided with whirligig in agitator tank, be provided with baffle plate at the inwall of described agitator tank.
In the utility model, be stirred liquid in agitator tank in the high speed rotary, the baffle plate of agitator tank inwall be stirred liquid and bump, make and be stirred liquid in the agitator tank and become irregular motion by the gyration of rule, be stirred between liquid and the baffle plate in the increase agitator tank, be stirred the chance that bumps between the liquid, make the effect of stirring even more ideal.
Further improvement of the utility model is:
Described baffle plate is located at the position, middle and upper part of described agitator tank inwall.When stirring, liquid level highly is the middle and upper part of agitator tank generally, and described baffle plate is located at this height, and the liquid level of the liquid of high speed rotary is blocked by baffle plate, upwards gushes out from baffle plate, and is back to the center of agitator tank; Again because the vortex that flows downward that the liquid of high speed rotary forms at centre of gyration position, so upwards gush out from baffle plate through the liquid that baffle plate blocks, and flow to the vortex place and flow downward again, liquid is formed to circle round, its mode of circling round is: be stirred liquid in the rotating shaft high speed rotary of whirligig, form the backflow of above-below direction simultaneously.So baffle plate is located at the position, middle and upper part of agitator tank, strengthened mixing effect greatly, in the production of reality, the optimum position of described baffle plate setting is:
The center line of described baffle plate is positioned at 2/3rds positions of described agitator tank height.
Described baffle plate is perpendicular to the inwall of described agitator tank.This structure is provided with conveniently baffle plate, has also avoided stirring the formation at dead angle.
Described baffle plate becomes the angle of inclination with the axis of described agitator tank.Become with the axis of agitator tank after the liquid collision of the baffle plate at angle of inclination and high speed rotary, liquid flows up or down along this baffle plate, can make liquid form convection current up and down equally.
Be provided with heat exchange coil in described agitator tank, the two ends of this heat exchange coil pass to outside the described agitator tank.The steam or the liquid that feed high temperature in heat exchange coil can heat being stirred liquid.In the prior art, realize heating to being stirred liquid, generally be in agitator tank, to feed steam, but having moisture in the steam can make the ratio of the moisture that is stirred liquid change, so this structure is with respect to prior art, can avoid keeping constant to being stirred in the process that liquid heats, making the moisture that is stirred in the liquid.
To sum up, the utility model has the advantages that:
1, baffle plate strengthens being stirred the collision opportunity of liquid, improves the effect that stirs;
2, baffle plate is located at position, agitator tank middle and upper part, can be made to be stirred liquid formation convection current up and down;
3, baffle plate becomes the angle of inclination with the axis of agitator tank, also can make to be stirred liquid formation convection current up and down;
4, heat exchange coil is to being stirred in the liquid warming process, can avoid being stirred that the moisture ratio changes in the liquid.
Description of drawings
Fig. 1 is in the utility model, the structure chart of embodiment one;
Fig. 2 is in the utility model, the structure chart of embodiment two;
Fig. 3 is in the utility model, the structure chart of embodiment three;
Description of reference numerals:
1, whirligig, 2, agitator tank, 3, inwall, 4, baffle plate, 5, heat exchange coil, 6, rotating shaft.
The specific embodiment
Embodiment one:
See also Fig. 1, a kind of rabbling mechanism, (whirligig 1 is dispersion impeller to be provided with whirligig 1 in agitator tank 2, dispersion impeller is installed in the rotating shaft 6 and by drive motors and drives), inwall 3 middle parts at agitator tank 2 are provided with baffle plate 4, and this baffle plate 4 is positioned at the middle part of agitator tank 2 and baffle plate 4 inwall 3 perpendicular to agitator tank 2.
In the present embodiment, because the setting of baffle plate 4, being stirred the chance that liquid bumps in agitator tank increases greatly, and the effect of stirring is improved.
Embodiment two:
This embodiment is with the difference of embodiment one: baffle plate 4 becomes the angle of inclination with the axis of agitator tank 2.
In the present embodiment, baffle plate 4 becomes the angle of inclination with the axis of agitator tank 2, is stirred after liquid and baffle plate 4 bump, and the baffle plate 4 of inclination can make and be stirred liquid convection current up and down takes place, and further improves mixing effect.
Embodiment three:
The difference of this embodiment and embodiment one is: baffle plate 4 is located at the position, middle and upper part of agitator tank 2 inwalls 3, say more accurately, the center line of baffle plate 4 is positioned at 2/3rds positions of agitator tank 2 height, is provided with heat exchange coil 5 in agitator tank 2, and the two ends of this heat exchange coil 5 pass to outside the agitator tank 2.
In the present embodiment, baffle plate 4 is located at the position, middle and upper part of agitator tank 2, the liquid of high speed rotary can flow to the vortex place of liquid center after being blocked by baffle plate 4, makes liquid produce eddy current up and down, also can realize being stirred the convection current up and down of liquid, and mixing effect is good; Simultaneously, 5 pairs of heat exchange coils are stirred liquid when heating, and can make the moisture ratio that is stirred liquid keep constant.
Claims (7)
1, a kind of rabbling mechanism is provided with whirligig (1) in agitator tank (2), it is characterized in that: the inwall (3) in described agitator tank (2) is provided with baffle plate (4).
2, rabbling mechanism as claimed in claim 1 is characterized in that: described baffle plate (4) is located at the position, middle and upper part of described agitator tank (3) inwall (3).
3, rabbling mechanism as claimed in claim 2 is characterized in that: the center line of described baffle plate (4) is positioned at 2/3rds positions of described agitator tank (2) height.
4, as claim 1,2 or 3 described rabbling mechanisms, it is characterized in that: described baffle plate (4) is perpendicular to the inwall (3) of described agitator tank (2).
5, as claim 1,2 or 3 described rabbling mechanisms, it is characterized in that: described baffle plate (4) becomes the angle of inclination with the axis of described agitator tank (2).
6, rabbling mechanism as claimed in claim 5 is characterized in that: described baffle plate (4) is perpendicular to the inwall (3) of described agitator tank (2).
7, as claim 1,2 or 3 described rabbling mechanisms, it is characterized in that: be provided with heat exchange coil (5) in described agitator tank (2), the two ends of this heat exchange coil (5) pass to outside the described agitator tank (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2006201549750U CN200998649Y (en) | 2006-12-19 | 2006-12-19 | Agitating mechanism |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNU2006201549750U CN200998649Y (en) | 2006-12-19 | 2006-12-19 | Agitating mechanism |
Publications (1)
Publication Number | Publication Date |
---|---|
CN200998649Y true CN200998649Y (en) | 2008-01-02 |
Family
ID=39013057
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNU2006201549750U Expired - Fee Related CN200998649Y (en) | 2006-12-19 | 2006-12-19 | Agitating mechanism |
Country Status (1)
Country | Link |
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CN (1) | CN200998649Y (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI414490B (en) * | 2009-09-30 | 2013-11-11 | Kurita Water Ind Ltd | Fluid bed type biologically treating apparatus |
CN108592676A (en) * | 2018-05-10 | 2018-09-28 | 柳州市融腾商贸有限公司 | A kind of production of construction materials heat transmission equipment |
-
2006
- 2006-12-19 CN CNU2006201549750U patent/CN200998649Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TWI414490B (en) * | 2009-09-30 | 2013-11-11 | Kurita Water Ind Ltd | Fluid bed type biologically treating apparatus |
CN108592676A (en) * | 2018-05-10 | 2018-09-28 | 柳州市融腾商贸有限公司 | A kind of production of construction materials heat transmission equipment |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080102 Termination date: 20101219 |