CN102059067A - Multi-shaft mortar and high-viscosity fluid stirrer for axial turbulent flow pattern multi-wire cutting machine - Google Patents
Multi-shaft mortar and high-viscosity fluid stirrer for axial turbulent flow pattern multi-wire cutting machine Download PDFInfo
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- CN102059067A CN102059067A CN201110009478.7A CN201110009478A CN102059067A CN 102059067 A CN102059067 A CN 102059067A CN 201110009478 A CN201110009478 A CN 201110009478A CN 102059067 A CN102059067 A CN 102059067A
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Abstract
The invention discloses a multi-shaft mortar and high-viscosity fluid stirrer for an axial turbulent flow pattern multi-wire cutting machine, comprising a plurality of single shaft stirring units which have the same structure and are uniformly arranged in a pot body of a stirring pot along the circumferential direction, each single shaft stirring unit comprises a stirring shaft arranged vertically, a stirring assembly and a driving mechanism, the stirring assemblies are coaxially installed at the bottom end of the stirring shaft and comprise impellers and short flow division tubes, the short flow division tubes are used for restricting a material flow direction to an axial movement along the stirring shaft, the impellers and the short flow division tubes are assembled into the stirring assembly which drives the material needed to be mixed and stirred to do an axial turbulent flow motion, the impellers are coaxially installed at the bottom end of the stirring shaft, and the short flow division tubes are coaxially sleeved at the outer sides of the impellers. The multi-shaft mortar and high-viscosity fluid stirrer has the advantages of simplicity in structure, high stirring ability, small shearing force, high dispersing power and high effect, and can be used for solving the problem that silicon carbide is broken due to the shearing force during the high-speed stirring of various traditional stirrers. Moreover, a stuck phenomenon is difficult to generate.
Description
Technical field
The present invention relates to a kind of multiaxis agitator, especially relate to a kind of axial turbulent flow pattern multi-line cutting machine with mortar and highly viscous fluid multiaxis agitator.
Background technology
Multi-line cutting machine is the high liquid-solid ratio that a kind of liquid-solid ratio was up to 1: 0.95 with the cutting mortar, be high viscosity suspension, and require the solid carborundum of its suspension that good dispersiveness must be arranged during actual the cutting, solid carborundum is suspended in the cutting liquid very equably to form the cutting mortar simultaneously.And in the slurries whipping process, must avoid violent stirring to make silicon-carbide particle be subjected to shear action and broken its cutting usefulness that influences.Traditional multi-line cutting machine mortar agitator tank, its agitator mostly is slurry formula or gate stirrer, the fluid flow pattern is generally radial motion in the whipping process, and many forms with laminar flow that flow of fluid occur, must increase power of agitator if improve mixing speed, the intensity of paddle or stirring frame just is subjected to certain influence simultaneously; If adopt high shear to disperse mixer, carborundum can be subjected to shear action and fragmentation, influences the cutting effect of multi-line cutting machine.In order to obtain the measured cutting mortar of matter suspension, many at present employing kneaders or slurry formula, gate stirrer, reach aim of even dispersion by prolonging mixing time, simultaneously for avoiding carborundum to be sheared broken effect, generally need continuous stirring more than 8 hours, mixing time is long.In the actual mechanical process and since the mixing time of mortar agitator tank that adopts long, a multi-line cutting machine company that has a certain scale need purchase a lot of mortar agitator tanks and could satisfy the production demand.In the actual production process, improve the production output of multi-line cutting machine, corresponding a plurality of mortar agitator tanks will be installed, propose new requirement again to mill construction etc., various expenses all can correspondingly increase.
In addition, in industrial circles such as chemical industry, commodity industry, mining industry, also be badly in need of a kind of fluid stirrer that can evenly stir at high solid-liquid ratio, high viscosity fluid of research and development, particularly the floatation process in the mining industry takes place owing to the solid granularity difference that once drops into very easily causes the stuck phenomenon of agitator, the solids that how to prevent bulk enters stuck agitator in the agitator, and people have to adopt various screen clothes to be realized.
Summary of the invention
Technical problem to be solved by this invention is at above-mentioned deficiency of the prior art, provide a kind of axial turbulent flow pattern multi-line cutting machine with mortar and highly viscous fluid multiaxis agitator, it is simple in structure, mixing power is strong, shearing force is little and dispersibility is strong, effect is high, can solve traditional various agitator and be subjected to the difficult problem that shearing force makes the carborundum fragmentation, and not be prone to stuck phenomenon owing to high-speed stirred makes carborundum.
For solving the problems of the technologies described above, the technical solution used in the present invention is: a kind of axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: comprise a plurality of a plurality of single shaft agitating units that along the circumferential direction evenly are laid in the agitator tank tank body, the structure of a plurality of described single shaft agitating units is all identical;
Described single shaft agitating unit comprises and is installed in the agitator tank tank body and is vertically the mixing component that rotates continuously and the agitator tank material in tank is evenly stirred to the shaft of laying, with shaft and is installed in the shaft top and drives the driving mechanism that shaft rotates continuously, is in transmission connection by transmission mechanism between described driving mechanism and the shaft; The coaxial bottom that is installed in shaft of described mixing component, and mixing component comprises that driving material upwards or by spin the gradually impeller that moves and material of material upper surface spins and the Flow of Goods and Materials direction is restricted to the water conservancy diversion short tube that axially moves along the axis of shaft when moving gradually at the bottom of by jar along the inwall of agitator tank tank body downwards, described impeller and water conservancy diversion short tube are assembled into and drive the mixing component that material is done axial turbulent motion in the whipping process, described impeller is coaxial to be installed in the shaft bottom, and the coaxial impeller outside that is fixedly set in of water conservancy diversion short tube; The mixing speed of described shaft is 600rmp～1500rmp.
Above-mentioned axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, and it is characterized in that: the quantity of described single shaft agitating unit is 2,3 or 4.
Above-mentioned axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, and it is characterized in that: the size of a plurality of described single shaft agitating units is all identical with setting height(from bottom).
Above-mentioned axial turbulent flow pattern multi-line cutting machine is characterized in that with mortar and highly viscous fluid multiaxis agitator: the size of relative two the described single shaft agitating units in position is all identical with setting height(from bottom) in 4 described single shaft agitating units.
Above-mentioned axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, and it is characterized in that: spacing between described shaft and the agitator tank tank body central axis and the ratio between the agitator tank tank body radius are 0.4～0.75.
Above-mentioned axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: described impeller comprises the coaxial connecting shaft cover and a plurality of blades that along the circumferential direction evenly are laid on the connecting shaft cover lateral wall that is fixedly mounted on the shaft bottom, a plurality of described blades be laid in the perpendicular same plane of the axis of shaft on, and the structure of a plurality of described blades is all identical with size.
Above-mentioned axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: described shaft extends the interior effective length of agitator tank tank body and the ratio between the agitator tank tank body height is 0.7～0.4, ratio between the diameter of shaft and the agitator tank tank diameter is 3～8: 100, ratio between the diameter of water conservancy diversion short tube and the agitator tank tank diameter is 15～25: 100, ratio between the wall thickness of water conservancy diversion short tube and the agitator tank tank diameter is 5～10: 1000, ratio between the thickness of blade and the agitator tank tank diameter is 3～15: 1000, angle between the center line of described blade and the axis of shaft is 20 °～60 °, and the ratio between the vertical height of described blade and the agitator tank tank diameter is for being 5～8: 100.
Above-mentioned axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: described blade is uniform straight plate blade of wall thickness or circular arc vane, described blade is installed between connecting shaft cover and the water conservancy diversion short tube, and the madial wall of described blade is fixed on the lateral wall that connecting shaft overlaps and its lateral wall is fixed on the madial wall of water conservancy diversion short tube; And the spacing between the lateral wall of the transverse width of blade and connecting shaft cover and the madial wall of water conservancy diversion short tube is identical; The height of the vertical height of described blade and water conservancy diversion short tube is identical and the two setting height(from bottom) is identical.
Above-mentioned axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, and it is characterized in that: the quantity of blade is 2～6 in the described mixing component.
Above-mentioned axial turbulent flow pattern multi-line cutting machine is characterized in that: carry out locking positioning by setscrew nut between described connecting shaft cover and the shaft, and described setscrew nut is installed in from the bottom to top on connecting shaft cover and the shaft with mortar and highly viscous fluid multiaxis agitator.
The present invention compared with prior art has the following advantages:
1, reasonable in design, it is convenient that processing and fabricating and installation are laid.
2, use easy and simple to handle and input cost is low.
3, be suitable for face width and use flexible operation, can effectively be suitable for extremely uniformly mixing in the process of multiple different viscosities medium, can satisfy the actual user demand of different volume size agitator tanks simultaneously.
4, result of use is good, the present invention can make multi-thread cutter use mortar in process for preparation, force carborundum and cutting liquid to enter agitator from container bottom, force material to axially move by the water conservancy diversion short tube, can guarantee that again liquid that can not is subjected to shear action, prevent the carborundum fragmentation in the whipping process again, and axially move that it has changed traditional multi-line cutting machine with the axial laminar flow flow pattern of mortar mixer with the flow pattern of turbulent flow.Design feature of the present invention is to rely on 2-6 blade with 30 °～60 ° of axial angles to rotate with the axial diversion short tube, force fluid along axially-movable, different mortar ratios can be realized by changing blade quantity and blade and axial angle, different tank volumes realizes that by changing the stirring wheel diameter fluid of different viscosities can be realized by the thickness that changes stirring wheel; Adjust with different liquid-solid ratioes according to different viscosity, because the higher relatively 600～1500rmp of rotary speed, fluid mobile flow pattern when doing radial motion is a turbulent condition, thereby the effectively dispersion of accelerated carbonation silicon, stir the user demand that can satisfy multi-line cutting machine usefulness cutting liquid in about 1 hour.Specifically, under the stirring action of blade, force carborundum and cutting liquid to move upward along agitator tank in the actual whipping process from container bottom; Simultaneously, force material to axially move, thereby the carborundum of avoiding that can minimum degree can not be subjected to shear action by the water conservancy diversion short tube, prevent carborundum first to shearing force effect and fragmentation and makes the carborundum and the suspension of cutting liquid composition do axial turbulent motion; And in the mortar process for preparation, under rotary speed 600～1500rmp state, carborundum is turbulent condition with the mobile flow pattern of suspension when doing radial motion that cutting liquid forms, and has quickened the dispersion of carborundum.
5, mixing time is short and prepare effectively, stirs and can satisfy multi-line cutting machine in about 1 hour with the user demand of cutting liquid, thereby prepare one jar of mortar and just can save 7 hours.
6, practical value height, the present invention is simple in structure, mixing power is strong, shearing force is little and dispersibility is strong, effect is high, can solve traditional various agitator and receive the difficult problem that makes the carborundum fragmentation of shearing force owing to high-speed stirred makes carborundum, and can be because of high solid-liquid ratio, solids major diameter, once drop into factors such as amount of solid is big and the phenomenon of stuck agitator occurs.
7, wide application, application mainly is that carborundum can make dispersed splendid multi-line cutting machine suspension with the cutting sufficient mixed preparing of liquid and its in the multi-thread cutter mortar process for preparation, the present invention simultaneously also can be used for places such as the high solid-liquid fluid in fields such as inorganic chemical industry, organic chemical industry, ore floatation, daily-use chemical industry and the solid dissolving in the highly viscous fluid, solid dispersed, highly viscous fluid stirring, and the viscosity size of the cutting mortar after the viscosity of highly viscous fluid and the multi-line cutting machine cutting use is close.
Below by drawings and Examples, technical scheme of the present invention is described in further detail.
Description of drawings
Fig. 1 is the user mode reference diagram of the present invention's first specific embodiment.
Fig. 2 is the structural representation of mixing component of the present invention.
Fig. 3 is the A-A profile of Fig. 2.
Fig. 4 is the perspective view of impeller of the present invention.
Fig. 5 is the user mode reference diagram of the present invention's second specific embodiment.
Fig. 6 is the user mode reference diagram of the present invention's the 3rd specific embodiment.
Fig. 7 is the vertical view of Fig. 6 of the present invention.
Description of reference numerals:
1-agitator tank tank body; The 2-shaft; The 3-mixing component;
The 3-1-impeller; 3-11-connecting shaft cover; The 3-12-blade;
3-2-water conservancy diversion short tube; The 4-drive motors; The 5-setscrew nut.
The specific embodiment
As Fig. 1, Fig. 2, Fig. 3 and shown in Figure 4, the present invention includes a plurality of a plurality of single shaft agitating units that along the circumferential direction are laid in the agitator tank tank body 1, the structure of a plurality of described single shaft agitating units is all identical.
Described single shaft agitating unit comprise be installed in the agitator tank tank body 1 and be vertically to the shaft of laying 2, rotate continuously with shaft 2 and to agitator tank tank body 1 in the mixing component 3 that evenly stirs of material and be installed in shaft 2 tops and driving mechanism that drive shaft 2 rotates continuously, be in transmission connection by transmission mechanism between described driving mechanism and the shaft 2.The described mixing component 3 coaxial bottoms that are installed in shaft 2, and mixing component 3 comprises that driving material upwards or by spin the gradually impeller 3-1 that moves and material of material upper surface spins and the Flow of Goods and Materials direction is restricted to the water conservancy diversion short tube 3-2 that axially moves along the axis of shaft 2 when moving gradually at the bottom of by jar along the inwall of agitator tank tank body 1 downwards, described impeller 3-1 and water conservancy diversion short tube 3-2 are assembled into and drive the mixing component that material is done axial turbulent motion in the whipping process, described impeller 3-1 is coaxial to be installed in shaft 2 bottoms, and the coaxial impeller 3-1 outside that is fixedly set in of water conservancy diversion short tube 3-2.The mixing speed of described shaft 2 is 600rmp～1500rmp.
In the present embodiment, the quantity of described single shaft agitating unit is 2, and the size of two described single shaft agitating units is all identical with setting height(from bottom).Spacing between described shaft 2 and agitator tank tank body 1 central axis and the ratio between agitator tank tank body 1 radius are 0.4～0.75.In the actual use, can adjust accordingly the spacing between shaft 2 and agitator tank tank body 1 central axis according to the concrete needs of reality, spacing between shaft 2 and agitator tank tank body 1 central axis is decided by the quantity of single shaft agitating unit and the volume of agitator tank tank body 1, wherein the quantity of single shaft agitating unit is many more, spacing between shaft 2 and agitator tank tank body 1 central axis is big more, and vice versa; The volume of agitator tank tank body 1 is big more, and the spacing between shaft 2 and agitator tank tank body 1 central axis is big more, and vice versa.Simultaneously, can adjust accordingly according to the quantity of concrete needs during actual the use the single shaft agitating unit, and the quantity of single shaft agitating unit is by different the deciding of viscosity of volume with the agitated medium (promptly stirring material) of agitator tank tank body 1, the volume of agitator tank tank body 1 is big more, the quantity of single shaft agitating unit is many more, and vice versa; The viscosity of agitated medium is big more, and the quantity of single shaft agitating unit is many more, and vice versa.
For each single shaft agitating unit, the quantity of blade 3-12 is 2～6 in the described mixing component 3.In the present embodiment, the quantity of blade 3-12 is 4, in the actual use, can adjust accordingly according to the quantity of the concrete needs of reality to blade 3-12.Specifically, the quantity of described blade 3-12 is decided according to the difference of agitated medium viscosity (being mortar ratio), and the viscosity of agitated medium is big more, and the quantity of blade 3-12 is few more, and vice versa.
In the present embodiment, during actual processing and fabricating, described impeller 3-1 comprises the coaxial connecting shaft cover 3-11 that is fixedly mounted on shaft 2 bottoms and along the circumferential direction evenly is laid in connecting shaft and overlaps a plurality of blade 3-12 on the 3-11 lateral wall, a plurality of described blade 3-12 be laid in the perpendicular same plane of the axis of shaft 2 on, and the structure of a plurality of described blade 3-12 is all identical with size.
Carry out locking positioning by setscrew nut 5 between described connecting shaft cover 3-11 and the shaft 2, and described setscrew nut 5 is installed in from the bottom to top on connecting shaft cover 3-11 and the shaft 2.In the actual whipping process, it is moving effectively to prevent at impeller 3-1 string to take place by setscrew nut 5 location.
Described shaft 2 extends effective length in the agitator tank tank body 1 and the ratio between agitator tank tank body 1 height is 0.7～0.4, ratio between the diameter of shaft 2 and agitator tank tank body 1 diameter is 3～8: 100, ratio between the diameter of water conservancy diversion short tube 3-2 and agitator tank tank body 1 diameter is 15～25: 100, ratio between the wall thickness of water conservancy diversion short tube 3-2 and agitator tank tank body 1 diameter is 5～10: 1000, ratio between the thickness of blade 3-12 and agitator tank tank body 1 diameter is 3～15: 1000, angle between the axis of the center line of described blade 3-12 and shaft 2 (being the blade angle degree) is 20 °～60 °, and the ratio between the vertical height of described blade 3-12 and agitator tank tank body 1 diameter is for being 5～8: 100.In the actual processing and making process, can the length of shaft 2, the diameter of shaft 2, the diameter of water conservancy diversion short tube 3-2, the wall thickness of water conservancy diversion short tube 3-2, wall thickness, blade angle degree, the mixing speed of shaft 2 and the vertical height of blade 3-12 and water conservancy diversion short tube 3-2 of blade 3-12 be adjusted accordingly according to the concrete needs of reality.
Wherein, according to different the adjusting accordingly of viscosity of agitated medium, the viscosity of agitated medium is big more for the height of agitator arm 3-1 (being the vertical height of blade 3-12 and water conservancy diversion short tube 3-2), and the vertical height of blade 3-12 and water conservancy diversion short tube 3-2 is high more, and vice versa.Thereby when the low viscosity medium was stirred, impeller height was low; When high viscosity medium is stirred, the impeller height height.
The size of described impeller 3-1 diameter not only by the volume size decision of agitator tank tank body 1, also will be decided according to the difference of agitated medium, and agitator tank tank body 1 diameter is big more, and the diameter of impeller 3-1 (being the transverse width of blade 3-12) is big more, and vice versa; The viscosity of agitated medium is big more, and the diameter of impeller 3-1 is more little, and vice versa.
It is fixed that the blade angle degree comes according to the difference of agitated medium viscosity, and the viscosity of agitated medium is big more, and the blade angle degree is big more, and vice versa.
The diameter of the length of described shaft 2 and shaft 2 is by the decision of the driving power size of the volume size of agitator tank tank body 1 and driving mechanism, and wherein the diameter of agitator tank tank body 1 is big more, and the diameter of the length of shaft 2 and shaft 2 is all big more, and vice versa; The driving power of driving mechanism is big more, and the diameter of the length of shaft 2 and shaft 2 is all big more.
The wall thickness of described water conservancy diversion short tube 3-2 is decided according to the different of agitated medium viscosity with the wall thickness of blade 3-12, and the viscosity of agitated medium is big more, and the wall thickness of water conservancy diversion short tube 3-2 and the wall thickness of blade 3-12 are all big more, and vice versa.
It is fixed that the mixing speed of described shaft 2 is come according to the difference of agitated medium viscosity, and the viscosity of agitated medium is big more, and the mixing speed of shaft 2 is more little, and vice versa.
In the present embodiment, described blade 3-12 is uniform straight plate blade of wall thickness or circular arc vane, described blade 3-12 is installed between connecting shaft cover 3-11 and the water conservancy diversion short tube 3-2, and the madial wall of described blade 3-12 is fixed on connecting shaft and overlaps on the lateral wall of 3-11 and its lateral wall is fixed on the madial wall of water conservancy diversion short tube 3-2; And the spacing between the lateral wall of the transverse width of blade 3-12 and connecting shaft cover 3-11 and the madial wall of water conservancy diversion short tube 3-2 is identical.Simultaneously, can select the stirring vane of other structure for use according to the concrete needs of reality.The height of the vertical height of described blade 3-12 and water conservancy diversion short tube 3-2 is identical and the two setting height(from bottom) is identical.Ratio between the radius of described circular arc vane and agitator tank tank body 1 diameter is 35～500: 1000.The wall thickness of described connecting shaft cover 3-11 and the ratio between agitator tank tank body 1 diameter are 5～10: 1000, and the external diameter of connecting shaft cover 3-11 is identical with the wall thickness sum that the diameter and the connecting shaft of shaft 2 overlap 3-11.
During actual installation, be connected with key between described connecting shaft cover 3-11 and the shaft 2 or thread connecting mode carries out fixedly connectedly, the while also can adopt other fixedly connected mode to fix.A plurality of described blade 3-12 all are fixedly mounted on the lateral wall middle part of connecting shaft cover 3-11, and the setting height(from bottom) unanimity of a plurality of described blade 3-12.
In the present embodiment, described driving mechanism is a drive motors 4.A plurality of described blade 3-12 and connecting shaft cover 3-11 processing and fabricating are one.A plurality of described blade 3-12, connecting shaft cover 3-11 and water conservancy diversion short tube 3-2 all adopt titanium steel material, acid resisting steel material or engineering plastics to make.During actual processing and fabricating, can select corresponding material according to the concrete needs of reality.In the present embodiment, a plurality of described blade 3-12, connecting shaft cover 3-11 and water conservancy diversion short tube 3-2 all adopt the titanium steel material to make, and blade 3-12 overlaps between 3-11 and the water conservancy diversion short tube 3-2 with connecting shaft and all adopts welding manner to fixedly connected.
During actual the preparation, mortar is in the mortar preparing tank in the process for preparation, under rotary speed 600rmp～1500rmp state, carborundum is turbulent condition with the mobile flow pattern of suspension when doing radial motion that cutting liquid forms, and has effectively quickened the dispersion of carborundum.
In the present embodiment, adopt diameter to be Φ 800mm and highly to be the ellipse head agitator tank of 1000mm, the power 2KW of drive motors and rotating speed are 1500rpm, the effective length 700mm of shaft 2 and its diameter are Φ 46mm, the external diameter Φ 159mm of water conservancy diversion short tube 3-2 and its wall thickness are 4mm, the external diameter of connecting shaft cover 3-11 is that Φ 50mm and its highly are 50mm, the wall thickness of connecting shaft cover 3-11 is 4mm, the blade angle degree is that 45 ° and blade 3-12 are straight plate blade, the vertical height of blade 3-12 is that 50mm and its thickness are 4mm, and connecting shaft cover 3-11 is connected with employing engage thread between the shaft 2.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 240mm.
As shown in Figure 5, in the present embodiment, with the different of embodiment 1 be: the quantity of described single shaft agitating unit is 3, and the size of three described single shaft agitating units is all identical with setting height(from bottom).In the present embodiment, the structure of remainder, mounting means and operation principle are all identical with embodiment 1.
As shown in Figure 6 and Figure 7, in the present embodiment, with the different of embodiment 1 be: the quantity of described single shaft agitating unit is 4, the size of relative two the described single shaft agitating units in position is all identical with setting height(from bottom) in 4 described single shaft agitating units, the effective length difference of shaft 2 in adjacent two single shaft agitating units, then the mixing component 3 of 4 described single shaft agitating units is not to be laid on the sustained height.During actual processing and fabricating, also can all adjust consistent with setting height(from bottom) the size of 4 described single shaft agitating units.In the present embodiment, the structure of remainder, mounting means and operation principle are all identical with embodiment 1.
In the present embodiment, as different from Example 1: adopt diameter to be Φ 1000mm and highly to be the ellipse head agitator tank of 1200mm, the power 4KW of drive motors and rotating speed are 1500rpm, the effective length of shaft 2 is that 840mm and its diameter are Φ 50mm, the external diameter Φ 180mm of water conservancy diversion short tube 3-2 and its wall thickness are 5mm, the external diameter of connecting shaft cover 3-11 is that 55mm and its highly are 50mm, the wall thickness of connecting shaft cover 3-11 is 5mm, the blade angle degree is 45 °, the vertical height of blade 3-12 is that 50mm and its thickness are 3mm, and connecting shaft cover 3-11 is connected with employing engage thread between the shaft 2.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 300mm.In the actual use, it is the circular arc vane of 500mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 1.
In the present embodiment, as different from Example 2: the effective length of shaft 2 is that 480mm and its diameter are Φ 30mm, the radius Φ 150mm of water conservancy diversion short tube 3-2 and its wall thickness are 5mm, the external diameter of connecting shaft cover 3-11 is that Φ 35mm and its highly are 50mm, the wall thickness of connecting shaft cover 3-11 is 5mm, the blade angle degree is 20 °, and the vertical height of blade 3-12 is that 50mm and its thickness are 5mm, and connecting shaft cover 3-11 is connected with employing key mode between the shaft 2.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 200mm.In the actual use, it is the circular arc vane of 35mm that blade 3-12 also can adopt radius of curvature.The mixing speed of described shaft 2 is 600rmp.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 6
In the present embodiment, as different from Example 2: the diameter of shaft 2 is Φ 80mm, the radius Φ 200mm of water conservancy diversion short tube 3-2 and its wall thickness are 10mm, the external diameter of connecting shaft cover 3-11 is that Φ 35mm and its highly are 80mm, the wall thickness of connecting shaft cover 3-11 is 10mm, the blade angle degree is 60 °, and the vertical height of blade 3-12 is that 80mm and its thickness are 15mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 375mm.In the actual use, it is the circular arc vane of 50mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 7
In the present embodiment, as different from Example 2: the diameter of shaft 2 is 40mm, the radius 160mm of water conservancy diversion short tube 3-2 and its wall thickness are 6mm, the external diameter of connecting shaft cover 3-11 is that 46mm and its highly are 60mm, the wall thickness of connecting shaft cover 3-11 is 6mm, the blade angle degree is 25 °, and the vertical height of blade 3-12 is that 60mm and its thickness are 6mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 225mm.In the actual use, it is the circular arc vane of 80mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 8
In the present embodiment, as different from Example 2: the diameter of shaft 2 is 45mm, the radius 170mm of water conservancy diversion short tube 3-2 and its wall thickness are 7mm, the external diameter of connecting shaft cover 3-11 is that 52mm and its highly are 70mm, the wall thickness of connecting shaft cover 3-11 is 7mm, the blade angle degree is 30 °, and the vertical height of blade 3-12 is that 60mm and its thickness are 8mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 250mm.In the actual use, it is the circular arc vane of 150mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 9
In the present embodiment, as different from Example 2: the diameter of shaft 2 is 55mm, the radius 180mm of water conservancy diversion short tube 3-2 and its wall thickness are 8mm, the external diameter of connecting shaft cover 3-11 is that 63mm and its highly are 75mm, the wall thickness of connecting shaft cover 3-11 is 8mm, the blade angle degree is 40 °, and the vertical height of blade 3-12 is that 75mm and its thickness are 10mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 275mm.In the actual use, it is the circular arc vane of 250mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 10
In the present embodiment, as different from Example 2: the diameter of shaft 2 is 65mm, the radius Φ 185mm of water conservancy diversion short tube 3-2 and its wall thickness are 9mm, the external diameter of connecting shaft cover 3-11 is that Φ 74mm and its highly are 70mm, the wall thickness of connecting shaft cover 3-11 is 9mm, the blade angle degree is 45 °, and the vertical height of blade 3-12 is that 75mm and its thickness are 12mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 300mm.In the actual use, it is the circular arc vane of 300mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 11
In the present embodiment, as different from Example 2: the diameter of shaft 2 is Φ 70mm, the radius Φ 190mm of water conservancy diversion short tube 3-2 and its wall thickness are 7mm, the external diameter of connecting shaft cover 3-11 is that Φ 77mm and its highly are 75mm, the wall thickness of connecting shaft cover 3-11 is 7mm, the blade angle degree is 50 °, and the vertical height of blade 3-12 is that 75mm and its thickness are 12mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 325mm.In the actual use, it is the circular arc vane of 350mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 12
In the present embodiment, as different from Example 2: the diameter of shaft 2 is Φ 75mm, the radius Φ 195mm of water conservancy diversion short tube 3-2 and its wall thickness are 6mm, the external diameter of connecting shaft cover 3-11 is that Φ 81mm and its highly are 78mm, the wall thickness of connecting shaft cover 3-11 is 6mm, the blade angle degree is 55 °, and the vertical height of blade 3-12 is that 78mm and its thickness are 14mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 350mm.In the actual use, it is the circular arc vane of 350mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 13
In the present embodiment, as different from Example 2: the diameter of shaft 2 is Φ 35mm, the radius Φ 175mm of water conservancy diversion short tube 3-2 and its wall thickness are 5mm, the external diameter of connecting shaft cover 3-11 is that Φ 40mm and its highly are 60mm, the wall thickness of connecting shaft cover 3-11 is 5mm, the blade angle degree is 35 °, and the vertical height of blade 3-12 is that 60mm and its thickness are 6mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 300mm.In the actual use, it is the circular arc vane of 400mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
Embodiment 14
In the present embodiment, as different from Example 2: the diameter of shaft 2 is 50mm, the radius 155mm of water conservancy diversion short tube 3-2 and its wall thickness are 5mm, the external diameter of connecting shaft cover 3-11 is that 55mm and its highly are 70mm, the wall thickness of connecting shaft cover 3-11 is 5mm, the blade angle degree is 35 °, and the vertical height of blade 3-12 is that 70mm and its thickness are 5mm.Spacing between described shaft 2 and agitator tank tank body 1 central axis is 375mm.In the actual use, it is the circular arc vane of 450mm that blade 3-12 also can adopt radius of curvature.In the present embodiment, the structure of remainder, annexation and operation principle are all identical with embodiment 4.
The above; it only is preferred embodiment of the present invention; be not that the present invention is imposed any restrictions, everyly any simple modification that above embodiment did, change and equivalent structure changed, all still belong in the protection domain of technical solution of the present invention according to the technology of the present invention essence.
Claims (10)
1. an axial turbulent flow pattern multi-line cutting machine is with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: comprise a plurality of a plurality of single shaft agitating units that along the circumferential direction are laid in the agitator tank tank body (1), the structure of a plurality of described single shaft agitating units is all identical;
Described single shaft agitating unit comprise be installed in the agitator tank tank body (1) and be vertically to the shaft of laying (2), rotate continuously with shaft (2) and to agitator tank tank body (1) in the mixing component (3) that evenly stirs of material and be installed in above the shaft (2) and driving mechanism that drive shaft (2) rotates continuously, described driving mechanism and shaft are in transmission connection by transmission mechanism between (2); The coaxial bottom that is installed in shaft (2) of described mixing component (3), and mixing component (3) comprises that driving material upwards or by spin the gradually impeller (3-1) of motion and material of material upper surface spins and the Flow of Goods and Materials direction is restricted to the water conservancy diversion short tube (3-2) that axially moves along the axis of shaft (2) when moving gradually at the bottom of by jar along the inwall of agitator tank tank body (1) downwards, described impeller (3-1) and water conservancy diversion short tube (3-2) are assembled into and drive the mixing component that material is done axial turbulent motion in the whipping process, described impeller (3-1) is coaxial to be installed in shaft (2) bottom, and coaxial impeller (3-1) outside that is fixedly set in of water conservancy diversion short tube (3-2); The mixing speed of described shaft (2) is 600rmp～1500rmp.
According to the described axial turbulent flow pattern multi-line cutting machine of claim 1 with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: the quantity of described single shaft agitating unit is 2,3 or 4.
According to claim 1 or 2 described axial turbulent flow pattern multi-line cutting machines with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: the size of a plurality of described single shaft agitating units is all identical with setting height(from bottom).
According to the described axial turbulent flow pattern multi-line cutting machine of claim 2 with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: the size of relative two the described single shaft agitating units in position is all identical with setting height(from bottom) in 4 described single shaft agitating units.
According to claim 1 or 2 described axial turbulent flow pattern multi-line cutting machines with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: spacing between described shaft (2) and agitator tank tank body (1) central axis and the ratio between agitator tank tank body (1) radius are 0.4～0.75.
According to claim 1 or 2 described axial turbulent flow pattern multi-line cutting machines with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: described impeller (3-1) comprises and coaxially is fixedly mounted on the connecting shaft cover (3-11) of shaft (2) bottom and along the circumferential direction evenly is laid in a plurality of blades (3-12) on connecting shaft cover (3-11) lateral wall, a plurality of described blades (3-12) are laid on the perpendicular same plane of axis with shaft (2), and the structure of a plurality of described blade (3-12) is all identical with size.
According to the described axial turbulent flow pattern multi-line cutting machine of claim 6 with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: described shaft (2) extends the interior effective length of agitator tank tank body (1) and the ratio between agitator tank tank body (1) height is 0.7～0.4, ratio between the diameter of shaft (2) and agitator tank tank body (1) diameter is 3～8: 100, ratio between the diameter of water conservancy diversion short tube (3-2) and agitator tank tank body (1) diameter is 15～25: 100, ratio between the wall thickness of water conservancy diversion short tube (3-2) and agitator tank tank body (1) diameter is 5～10: 1000, ratio between the thickness of blade (3-12) and agitator tank tank body (1) diameter is 3～15: 1000, angle between the axis of the center line of described blade (3-12) and shaft (2) is 20 °～60 °, and the ratio between the vertical height of described blade (3-12) and agitator tank tank body (1) diameter is for being 5～8: 100.
According to the described axial turbulent flow pattern multi-line cutting machine of claim 7 with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: described blade (3-12) is uniform straight plate blade of wall thickness or circular arc vane, described blade (3-12) is installed between connecting shaft cover (3-11) and the water conservancy diversion short tube (3-2), and the madial wall of described blade (3-12) is fixed on the lateral wall of connecting shaft cover (3-11) and its lateral wall is fixed on the madial wall of water conservancy diversion short tube (3-2); And the spacing between the lateral wall of the transverse width of blade (3-12) and connecting shaft cover (3-11) and the madial wall of water conservancy diversion short tube (3-2) is identical; The height of the vertical height of described blade (3-12) and water conservancy diversion short tube (3-2) is identical and the two setting height(from bottom) is identical.
According to the described axial turbulent flow pattern multi-line cutting machine of claim 6 with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: the quantity of blade (3-12) is 2～6 in the described mixing component (3).
According to the described axial turbulent flow pattern multi-line cutting machine of claim 6 with mortar and highly viscous fluid multiaxis agitator, it is characterized in that: carry out locking positioning by setscrew nut (5) between described connecting shaft cover (3-11) and the shaft (2), and described setscrew nut (5) is installed in from the bottom to top on connecting shaft cover (3-11) and the shaft (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100094787A CN102059067B (en) | 2011-01-17 | 2011-01-17 | Multi-shaft mortar and high-viscosity fluid stirrer for axial turbulent flow pattern multi-wire cutting machine |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100094787A CN102059067B (en) | 2011-01-17 | 2011-01-17 | Multi-shaft mortar and high-viscosity fluid stirrer for axial turbulent flow pattern multi-wire cutting machine |
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| Publication Number | Publication Date |
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| CN102059067A true CN102059067A (en) | 2011-05-18 |
| CN102059067B CN102059067B (en) | 2011-10-26 |
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| CN2011100094787A Expired - Fee Related CN102059067B (en) | 2011-01-17 | 2011-01-17 | Multi-shaft mortar and high-viscosity fluid stirrer for axial turbulent flow pattern multi-wire cutting machine |
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| CN103585918A (en) * | 2013-10-15 | 2014-02-19 | 安徽徽普生物科技有限责任公司 | Dual-stirring device |
| CN105983361A (en) * | 2015-01-27 | 2016-10-05 | 上海东冠纸业有限公司 | Glue mixing apparatus |
| CN106422897A (en) * | 2016-12-12 | 2017-02-22 | 衡阳市鑫晟新能源有限公司 | Mixing device for lithium battery cathode material |
| CN110184640A (en) * | 2018-12-27 | 2019-08-30 | 新阳硅密（上海）半导体技术有限公司 | Agitating device and electroplating device containing it |
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| CN110184640B (en) * | 2018-12-27 | 2024-06-28 | 新阳硅密（上海）半导体技术有限公司 | Stirring device and electroplating equipment comprising same |
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| Publication number | Publication date |
|---|---|
| CN102059067B (en) | 2011-10-26 |
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Inventor after: He Peng Inventor after: Yang Yi Inventor after: He Qing Inventor after: Chen Bo Inventor before: Yang Guonong Inventor before: He Peng Inventor before: Yang Yi Inventor before: He Qing Inventor before: Chen Bo |
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