Mixing tank structure
By designing the mixing tank structure and using staggered stirring blades and reducer drive, the problem of low mixing efficiency of high-viscosity materials is solved, and efficient mixing and low power requirements are achieved.
Patent Information
- Application Number
- CN202422324531.8
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-09-23
- Publication Date
- 2025-10-03
- Estimated Expiration
- 2034-09-23
AI Technical Summary
The existing technology has low mixing efficiency and poor mixing effect when mixing high-viscosity materials. In addition, the multi-axis agitator has a complex structure and high driving power, resulting in high maintenance costs.
A mixing trough structure is designed, including a trough body, a first stirring shaft, a second stirring shaft and a third stirring shaft. The trough bottom is an arc surface with a discharge port. The stirring shaft is equipped with stirring blades, which are driven by bevel gears and a reducer to achieve axial and circumferential mixing. The stirring blades are staggered to improve the mixing effect.
It achieves efficient mixing of high-viscosity materials, reduces driving power requirements, reduces material residue, and improves material utilization.
Smart Images

Figure CN223404844U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the field of stirring equipment, in particular to a mixing tank structure. Background Art
[0002] When mixing high-viscosity materials, paint manufacturers often use single-shaft agitators at low speeds. This type of agitator has low mixing efficiency and poor mixing results. Multi-shaft agitators are also used for mixing. Currently, multi-shaft agitators have multiple shafts arranged in parallel and spaced apart. When mixing materials vertically, this is usually achieved using complexly designed stirring blades. These complex structures are prone to material residue and the overall stirring resistance is high, requiring the agitator to drive a large amount of power.
[0003] Therefore, designing a mixing tank structure with simple structure and low driving power for high viscosity materials is a technical problem that needs to be solved urgently by those skilled in the art. Summary of the Invention
[0004] The purpose of the utility model is to provide a mixing tank structure for addressing the deficiencies of the existing technology, which has a simple structure and low maintenance cost and can effectively ensure the mixing effect of high-viscosity materials.
[0005] The technical solution of the present utility model is: a mixing trough structure, comprising a trough body, and a first stirring shaft, a second stirring shaft, and a third stirring shaft rotatably arranged in the trough body, the bottom of the trough body is an arc surface, a discharge port is arranged at the low point of the arc surface bottom, and the opening and closing is controlled by a valve, the straight line where the second stirring shaft is located is located on the central axis of the trough body, a plurality of second stirring blades are arranged at intervals along the length direction on the second stirring shaft, and each second stirring blade is vertically distributed to the second stirring shaft, the first stirring shaft and the third stirring shaft are axially symmetrically distributed along the second stirring shaft, and the straight lines where they are located are respectively located on the radius extension lines corresponding to the arc surface where the trough bottom is located, a plurality of first stirring blades and third stirring blades are respectively arranged at intervals along the length direction on the first stirring shaft and the third stirring shaft, and each first stirring blade is vertically distributed to the first stirring shaft, each third stirring blade is vertically distributed to the third stirring shaft, and each second stirring blade is staggered with each first stirring blade and each third stirring blade.
[0006] The upper ends of the first, second and third stirring shafts extend out of the trough body, and the first, second and third bevel gears are fixedly arranged circumferentially respectively. The first and third bevel gears are both engaged with the second bevel gear, and the outwardly extending end of the second stirring shaft is connected to the output shaft of the reducer.
[0007] The number of the second stirring blades is three pairs, and each pair of second stirring blades is evenly spaced along the length direction of the second stirring shaft, and each pair of second stirring blades is axially symmetrically distributed along the second stirring shaft.
[0008] The number of the first stirring blades and the third stirring blades is two pairs, and the stirring blades of each pair are axially symmetrically distributed along the corresponding stirring axis.
[0009] The above technical solution has the following beneficial effects:
[0010] 1. The mixing tank structure includes a tank body, and a first stirring shaft, a second stirring shaft, and a third stirring shaft rotatably arranged in the tank body. The tank body is used to provide a space for mixing. Each stirring shaft drives the stirring blades to stir the high-viscosity material by rotating to achieve the purpose of mixing. The bottom of the tank body is an arc surface, and a discharge port is set at the low point of the arc surface bottom, and the opening and closing is controlled by a valve. The tank body with this structure is conducive to the discharge of the mixed material from the tank body through the discharge port after mixing, and can also reduce the residual amount of the mixed material in the tank body, thereby improving the utilization rate of the material. The straight line where the second stirring shaft is located is located on the central axis of the tank body, that is, the second stirring shaft is located at the center of the tank body. A plurality of second stirring blades are arranged at intervals along the length direction on the second stirring shaft, and each second stirring blade is vertically distributed to the second stirring shaft. These second stirring blades are driven by the second stirring shaft to rotate circumferentially to stir and mix the high-viscosity material around the second stirring shaft. The first stirring shaft and the third stirring shaft are axially symmetrically distributed along the second stirring shaft, and the straight lines where they are located are respectively located on the radius extension lines corresponding to the arc surface where the bottom of the groove is located, that is, the first stirring shaft and the third stirring shaft are inclined to extend toward the second stirring shaft, and the first stirring shaft and the second stirring shaft are perpendicular to the tangent line of the projection point. A plurality of first stirring blades and third stirring blades are respectively arranged on the first stirring shaft and the third stirring shaft along the length direction, and each first stirring blade is perpendicular to the first stirring shaft, and each third stirring blade is perpendicular to the third stirring shaft. Each first stirring blade and the third stirring blade are driven by the first stirring shaft and the third stirring shaft to rotate circumferentially, respectively, to stir and mix the high-viscosity materials around the first stirring shaft and the third stirring shaft, and also to form stirring and mixing along the height direction, so as to achieve the purpose of axial and circumferential mixing with a simple structure. Each of the second stirring blades and each of the first stirring blades and each of the third stirring blades are staggered, so that the stirring areas overlap, thereby improving the mixing effect on high-viscosity materials.
[0011] 2. The upper ends of the first, second and third stirring shafts extend out of the trough body, and the first, second and third bevel gears are fixedly arranged circumferentially respectively. The first and third bevel gears are engaged with the second bevel gear. The outward end of the second stirring shaft is connected to the output shaft of the reducer. This driving structure can use a set of reducers to provide power, reducing power requirements, and also making the adjacent stirring shafts rotate in opposite directions, thereby improving the mixing effect of high-viscosity materials.
[0012] The following is a further description with reference to the accompanying drawings and specific implementations. BRIEF DESCRIPTION OF THE DRAWINGS
[0013] Figure 1 It is a structural diagram of the utility model;
[0014] Figure 2 for Figure 1 A-direction view;
[0015] Figure 3 for Figure 2 bb cross-sectional view.
[0016] In the accompanying drawings, 1 is the first stirring shaft, 1a is the first stirring blade, 1b is the first bevel gear, 2 is the second stirring shaft, 2a is the second stirring blade, 2b is the second bevel gear, 3 is the third stirring shaft, 3a is the third stirring blade, 3b is the third bevel gear, 4 is the trough body, and 5 is the discharge port. DETAILED DESCRIPTION
[0017] See also Figures 1 to 3, is a specific embodiment of a mixing tank structure. The mixing tank structure includes a tank body 4, and a first stirring shaft 1, a second stirring shaft 2, and a third stirring shaft 3 rotatably arranged in the tank body. The installation structure of each stirring shaft in the tank body is a conventional structure. The bottom of the tank body 4 is an arc surface, and a discharge port 5 is set at the low point of the arc surface bottom, and the opening and closing is controlled by a valve. Obviously, a feeding port is also set at the top of the tank body. The straight line where the second stirring shaft 2 is located is located on the central axis of the tank body 4. A plurality of second stirring blades 2a are arranged at intervals along the length direction on the second stirring shaft 2, and each second stirring blade 2a is vertically distributed with the second stirring shaft 2. In this embodiment, the number of second stirring blades 2a is three pairs, and each pair of second stirring blades is evenly spaced along the length direction of the second stirring shaft 2, and each pair of second stirring blades is axially symmetrically distributed along the second stirring shaft. Usually, in order to meet the stirring needs of larger capacity materials, the length of each pair of second stirring blades gradually shortens from top to bottom. The first stirring shaft 1 and the third stirring shaft 3 are axially symmetrically distributed along the second stirring shaft 2, and the straight lines on which they are located are respectively located on the radius extension lines corresponding to the arc surface where the bottom of the groove is located. The first stirring shaft 1 and the third stirring shaft 3 are respectively provided with a plurality of first stirring blades 1a and third stirring blades 3a at intervals along the length direction, and each first stirring blade 1a is perpendicular to the first stirring shaft 1, and each third stirring blade 3a is perpendicular to the third stirring shaft 3. In this embodiment, the number of the first stirring blades 1a and the third stirring blades 3a is two pairs, and the stirring blades of each pair are axially symmetrically distributed along the corresponding stirring shaft. Each second stirring blade 2a is staggered with each first stirring blade 1a and each third stirring blade 3a. The upper ends of the first stirring shaft 1, the second stirring shaft 2, and the third stirring shaft 3 extend out of the trough body 4, and the first bevel gear 1b, the second bevel gear 2b, and the third bevel gear 3b are fixedly arranged circumferentially, respectively. The first bevel gear 1b and the third bevel gear 3b are both engaged with the second bevel gear 2b, and the outwardly extending end of the second stirring shaft 2 is connected to the output shaft of the reducer.
[0018] The working principle of this utility model is as follows: the second stirring shaft is driven forward or reversely by a speed reducer, and the first and third stirring shafts are driven reversely or forwardly by gears. The first, third, and second stirring blades are used to mix and stir the high-viscosity material in the circumferential direction, and the first and third stirring blades are used to mix and stir the high-viscosity material in the height direction, thereby achieving the purpose of efficient mixing. The stirred material is discharged through the discharge port, and almost no material residue is left.
Claims
1. A mixing tank structure, characterized in that: It comprises a tank body (4), and a first stirring shaft (1), a second stirring shaft (2), and a third stirring shaft (3) rotatably arranged in the tank body. The bottom of the trough body (4) is an arc surface, and a discharge port (5) is set at the lowest point of the arc surface bottom, and the opening and closing is controlled by a valve. The straight line on which the second stirring shaft (2) is located is located on the central axis of the tank body (4); a plurality of second stirring blades (2a) are arranged at intervals along the length direction on the second stirring shaft (2); and each second stirring blade (2a) is vertically distributed to the second stirring shaft (2). The first stirring shaft (1) and the third stirring shaft (3) are axially symmetrically distributed along the second stirring shaft (2), and the straight lines on which they are located are respectively located on the radius extension lines corresponding to the arc surface where the bottom of the tank is located. The first stirring shaft (1) and the third stirring shaft (3) are respectively provided with a plurality of first stirring blades (1a) and third stirring blades (3a) at intervals along the length direction, and each first stirring blade (1a) is vertically distributed with respect to the first stirring shaft (1), and each third stirring blade (3a) is vertically distributed with respect to the third stirring shaft (3). Each of the second stirring blades (2a) and each of the first stirring blades (1a) and each of the third stirring blades (3a) are arranged in a staggered manner.
2. The mixing tank structure according to claim 1, characterized in that: The upper ends of the first stirring shaft (1), the second stirring shaft (2), and the third stirring shaft (3) extend outward from the trough body (4), and a first bevel gear (1b), a second bevel gear (2b), and a third bevel gear (3b) are fixedly arranged circumferentially, respectively; the first bevel gear (1b) and the third bevel gear (3b) are both meshed with the second bevel gear (2b); and the extended end of the second stirring shaft (2) is connected to the output shaft of the reducer.
3. The mixing tank structure according to claim 1, characterized in that: The number of the second stirring blades (2a) is three pairs, and each pair of second stirring blades is evenly spaced along the length direction of the second stirring shaft (2), and each pair of second stirring blades is axially symmetrically distributed along the second stirring shaft.
4. The mixing tank structure according to claim 1, characterized in that: The number of the first stirring blades (1a) and the third stirring blades (3a) is two pairs, and the stirring blades of each pair are axially symmetrically distributed along the corresponding stirring axis.