CN104607087B - Paint stirring blend tank - Google Patents
Paint stirring blend tank Download PDFInfo
- Publication number
- CN104607087B CN104607087B CN201510092867.9A CN201510092867A CN104607087B CN 104607087 B CN104607087 B CN 104607087B CN 201510092867 A CN201510092867 A CN 201510092867A CN 104607087 B CN104607087 B CN 104607087B
- Authority
- CN
- China
- Prior art keywords
- agitator
- stir shaft
- valve
- urceolus
- jet flow
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Mixers Of The Rotary Stirring Type (AREA)
- Accessories For Mixers (AREA)
Abstract
The present invention discloses a kind of paint stirring blend tank, comprise tank body, motor and step-down gear and stir shaft, in stir shaft insertion tank body, motor and step-down gear drive stir shaft to rotate, stir shaft is followed successively by from lower to upper sweeps jet flow agitator under end agitator, plural serial stage, two-way jet flow agitator and the lower jet agitator that suspends, the lower jet agitator that wherein suspends limits by upper and lower positioning step, can fluctuate; Tank is external is provided with chuck, and chuck connects steam valve, drain valve and inline valve, and chuck is also connected with water intaking valve and return water pipe control valve; Tank base is connected Middle pressure draught fan and is provided with paint delivery valve. The present invention has less energy-consumption, can complete the heating needed for paint deployment, stirring, output Deng Ge road technique, material circulates very well, not easily sinks to the bottom, have a power failure even if long-time cause material sedimentation also can light-load starting, have a extensive future.
Description
Technical field
The present invention relates to a kind of blend tank, specifically refer to paint stirring blend tank.
Background technology
The allotment of paint needs to stir in heat-processed, otherwise easily coking and dead angle occurs, when the viscosity painted is very big, stir and not easily carry out, thus present paint deployment tank be all to Large Copacity, high solid-liquid ratio, strong mixing be developing direction, but also exist stir that electricity consumption is big, material sedimentation easily stuck, be difficult to eliminate the defect stirring dead angle.
Present paint deployment tank generally all adopts major axis multilayer sweep stirring at low speed, motor configuration power is big, agitator shaft speed about 1 turn/second, stirring rake radius are slightly less than tank body internal diameter, exist paint easily sink to the bottom, have a power failure material sedimentation can stuck stirring even cannot start defect, electricity consume very high, thus existing whipping appts can not meet the technical requirements of high viscosity, large size paint deployment tank.
Summary of the invention
The technical problem to be solved in the present invention overcomes the deficiencies in the prior art exactly, the each road technique that provide a kind of less energy-consumption, paint deployment can be completed, material circulates very well, not easily sink to the bottom, and having a power failure even if long-time causes the material sedimentation also can the paint stirring blend tank of light-load starting.
For overcoming the deficiencies in the prior art, the present invention takes following technical scheme:
A kind of paint stirring blend tank, comprise tank body, motor and step-down gear and stir shaft, in stir shaft insertion tank body, motor and step-down gear drive stir shaft to rotate, it is characterized in that: stir shaft is followed successively by from lower to upper sweeps jet flow agitator under end agitator, plural serial stage, two-way jet flow agitator and the lower jet agitator that suspends, the lower jet agitator that wherein suspends limits by upper and lower positioning step, can fluctuate; Tank is external is provided with chuck, and chuck connects steam valve, drain valve and inline valve, and chuck is also connected with water intaking valve and return water pipe control valve; Tank base is connected Middle pressure draught fan and is provided with paint delivery valve.
Described end agitator of sweeping comprises stir shaft, interior cylinder and urceolus, and stir shaft and interior cylinder are welded as a whole through axial blade, and interior cylinder extends to cone cylinder downwards, and cone cylinder is welded by fagging with urceolus; Interior cylinder inwall is welded with circulation blade, cone cylinder inwall is welded with centrifuge scraper.
Under described plural serial stage, jet flow agitator is in series by 2-10 lower jet flow agitator, and lower jet flow agitator comprises stir shaft and urceolus, and stir shaft and urceolus flow down spray blade through liquid and be welded as a whole.
Described two-way jet flow agitator comprises stir shaft, interior cylinder and urceolus, and stir shaft and interior cylinder flow down spray blade through liquid and be welded as a whole, and interior cylinder and urceolus spray blade on liquid stream and be welded as a whole.
Under described suspension, jet agitator comprises stir shaft, axle sleeve and urceolus, and stir shaft is splined shaft, and axle sleeve is also spline axle sleeve, and spline axle sleeve can move on splined shaft; Spline axle sleeve and urceolus connect as one through blade.
Described tank body is provided with manhole, is convenient to maintenance, observation and throws material.
When needs carry out process for processing, open motor and step-down gear, rotating speed in actual applications 3-15 p.s. turn can adapt to great majority use needs, progressively add material again, the lower jet agitator that suspends can fluctuate on the splined shaft between upper and lower positioning step flexibly, suspend lower jet agitator by the reverse towing force of gravity, downwards jet flow liquid and splined shaft and spline inner room frictional force acting in conjunction, can suspend stirring by relative liquid surface certain position, downward jet flow; Two-way jet flow agitator rotates, wherein liquid flows down the spray downward jet flow of blade, and liquid stream sprays blade upwards jet flow, and under suspending, jet agitator and two-way jet flow agitator produce the core flow decline of upper liquid jointly, liquid stream sprays blade to upper annular jet flow, make top convection current situation good.
Multiple downward tandem injection liquid of lower jet flow agitator, enter and sweep end agitator and accelerated downward conveying once again by axial blade, liquid is rotated speed-raising and is had remarkable circulation when flowing through circulation blade, becoming the integrated fluid of axial flow, circulation, the direct punching of core flow high speed carries out center to bottom and sweeps the end, and a part of centrifugal stream is centrifuged blade and rotates speed-raising once again, form tubaeform injection stream high speed diffusion, impact base plane, play big area without dead angle sweep the end stir, prevent material sedimentation.
The different process segments, need to carry out different parameters regulation and control, commitment material viscosity can be opened greatly valve and carry out the steam heating that indirectly heats up work efficiency is improved, if desired can start Middle pressure draught fan when heating up applicable and carry out rare gas element internal recycle, rare gas element from blower fan adds by the bottom of tank, mix and scatter in cone is bucket-shaped from stirring downward streams, rare gas element carries material and forms rising mixed solution stream in tank wall, so tank is formed centrally katabatic drainage, stirring region outside forms upwelling, form perfectly paint underflow convection circulation, after completing processing, product deployed in tank is cooled by Open valve cold water fast, opening paint delivery valve, can to implement lower step filling.
Compared with prior art, the useful effect of the present invention is also:
Center liquid axial flow from top to bottom series connection speed-raising always impact bottom downwards, make bottom well material suspended, can not sedimentation; The electric power consumed preferentially carries out liquid stream and sweeps end elimination sedimentation, then lets nature take its course to be converted to stirring again, makes liquid phase solid phase in whole bucket substantially even, and this kind of principle of work had both met service requirements, key significantly energy-conservation again.
The lower jet agitator that suspends suspends to stir and automatically adapts to different liquid level, completes to stir.
Axial force fully considers that gravity balances simultaneously mutually, reduces the detrimentally affect to transmission.
The bottom bucket-shaped jet flow of cone coordinates central jet, perfect realization sweeps the end, prevent sedimentation, little owing to stirring radius, even if material viscosity is very big, drag torque is also very little, therefore can stir by light start, entering normal whipped state, noble gas mixtures stream forms the perfect convection circulation of paint underflow further.
The scull leaf middling speed rotation that axial flow uses, electricity consumption is very low, and mixing effect is fine, particularly sweeps the urceolus of end agitator and bores cylinder when higher rotation speed, and internal and external walls liquid can play liquid-bearing supporting role, makes stirring reliable and stable.
Accompanying drawing explanation
Fig. 1 is the two dimensional structure schematic diagram of the present invention.
Fig. 2 is the three-dimensional structure schematic diagram of jet agitator under suspending.
Fig. 3 is the three-dimensional structure schematic diagram of two-way jet flow agitator.
Fig. 4 is the three-dimensional structure schematic diagram of lower jet flow agitator.
Fig. 5 is the two dimensional structure schematic diagram sweeping end agitator.
Fig. 6 is the plan structure schematic diagram sweeping end agitator.
Fig. 7 be sweep end agitator look up structural representation.
In figure, each label represents:
1, motor and step-down gear; 2, upper positioning step; 3, lower positioning step; 4, tank body; 5, indirect steam valve; 6, water intaking valve; 7, inline valve; 8, drain valve; 9, delivery valve is painted; 10, manhole; 11, backwater control valve; 12, Middle pressure draught fan; A, the lower injector of suspension; A1, splined shaft; A2, spline axle sleeve; A3, blade; A4, urceolus; B, two-way jet flow agitator; B1, urceolus; B2, liquid stream spray blade; B3, interior cylinder; B4, stir shaft; B5, liquid flow down spray blade; Jet flow agitator under C, plural serial stage; C1, urceolus; C2, liquid flow down spray blade; C3, stir shaft; D, sweep end agitator; D1, urceolus; D2, cone cylinder; D3, centrifuge scraper; D4, circulation blade; D5, interior cylinder; D6, axial blade; D7, stir shaft; D8, fagging.
Embodiment
Now by reference to the accompanying drawings, the present invention is specifically illustrated further.
As shown in Figure 1, Figure 2, paint stirring blend tank shown in Fig. 3, Fig. 4, Fig. 5, Fig. 6 and Fig. 7, comprise tank body 4, motor and step-down gear 1 and stir shaft, in stir shaft insertion tank body 4, motor and step-down gear 1 drive stir shaft to rotate, stir shaft is followed successively by from lower to upper sweeps jet flow agitator C, two-way jet flow agitator B and the lower jet agitator A that suspends under end agitator D, plural serial stage, the lower jet agitator A that wherein suspends limits by upper 2, lower positioning step 3, can fluctuate; Being provided with chuck outside tank body 4, chuck connects steam valve 5, drain valve 8 and inline valve 7, and chuck is also connected with water intaking valve 6 and return water pipe control valve 11; It is connected Middle pressure draught fan 12 bottom tank body 4 and it is provided with paint delivery valve 9.
The described end agitator D that sweeps comprises stir shaft D7, interior cylinder D5 and urceolus D1, stir shaft D7 and interior cylinder D5 and is welded as a whole through axial blade D6, and interior cylinder D5 extends to cone cylinder D2 downwards, and cone cylinder D2 is welded by fagging D8 with urceolus D1; Interior cylinder D5 inwall is welded with circulation blade D4, cone cylinder D2 inwall is welded with centrifuge scraper D3.
Under described plural serial stage, jet flow agitator C is in series by 2-10 lower jet flow agitator C, and lower jet flow agitator C comprises stir shaft C3 and urceolus C1, and stir shaft C3 and urceolus C1 flows down spray blade C2 through liquid and is welded as a whole.
Described two-way jet flow agitator B comprise stir shaft B4, interior cylinder B3 and urceolus B1, stir shaft B4 and interior cylinder B3 through liquid flow down spray blade B5 be welded as a whole, interior cylinder B3 and urceolus B1 sprays blade B2 on liquid stream and is welded as a whole.
Under described suspension, jet agitator A comprises stir shaft, axle sleeve and urceolus A4, and stir shaft is splined shaft A1, and axle sleeve is also spline axle sleeve A2, and spline axle sleeve A2 can move on splined shaft A1; Spline axle sleeve A2 and urceolus A4 connects as one through blade A3.
Described tank body is provided with manhole 10, is convenient to maintenance, observation and throws material.
When needs carry out process for processing, open motor and step-down gear 1, stir shaft rotates as illustrated by the arrows in fig. 1, rotating speed in actual applications 3-15 p.s. turn can adapt to great majority use needs, progressively add material again, the lower jet agitator A that suspends can fluctuate on the splined shaft A1 between upper and lower positioning step 2,3 flexibly, suspend lower jet agitator A by the reverse towing force of gravity, downwards jet flow liquid and frictional force acting in conjunction between splined shaft A and spline cover A2, can the suspension of relative liquid surface certain position stir, downward jet flow; Two-way jet flow agitator B rotates, wherein liquid flows down the spray downward jet flow of blade B5, liquid stream sprays blade B2 upwards jet flow, the lower jet agitator A and two-way jet flow agitator B that suspends produces the core flow decline of upper liquid jointly, liquid stream sprays blade B2 to upper annular jet flow, make top convection current situation good.
Multiple lower downward tandem injection liquid of jet flow agitator C, enter and sweep end agitator D and accelerated downward conveying once again by axial blade D6, liquid is rotated speed-raising when flowing through circulation blade D4 and is had remarkable circulation, becoming the integrated fluid of axial flow, circulation, the direct punching of core flow high speed carries out center to bottom and sweeps the end, and a part of centrifugal stream is centrifuged blade D3 and rotates speed-raising once again, form tubaeform injection stream high speed diffusion, impact base plane, play big area without dead angle sweep the end stir, prevent material sedimentation.
The different process segments, need to carry out different parameters regulation and control, commitment material viscosity can be opened greatly valve 5 and carry out the steam heating that indirectly heats up work efficiency is improved, if desired can start Middle pressure draught fan 12 when heating up applicable and carry out rare gas element internal recycle, rare gas element from blower fan 12 adds by the bottom of tank, mix and scatter in cone is bucket-shaped from stirring downward streams, rare gas element carries material and forms rising mixed solution stream in tank wall, so tank is formed centrally katabatic drainage, stirring region outside forms upwelling, form perfectly paint underflow convection circulation, after completing processing, Open valve 6, product deployed in tank is cooled fast by 11 with cold water, opening paint delivery valve 9, can to implement lower step filling.
The better embodiment of above-mentioned just the present invention, not does any restriction in form to the present invention. Any those of ordinary skill in the art, when not departing from technical solution of the present invention scope, can utilize the technology contents of above-mentioned announcement that technical solution of the present invention is made many possible variations and modification, or be revised as the equivalent embodiment of equivalent variations. Therefore, every content not departing from technical solution of the present invention, according to the technology of the present invention essence to any simple modification made for any of the above embodiments, equivalent variations and modification, all should drop in the scope of technical solution of the present invention protection.
Claims (2)
1. a paint stirring blend tank, comprise tank body, motor and step-down gear and stir shaft, in stir shaft insertion tank body, motor and step-down gear drive stir shaft to rotate, it is characterized in that: stir shaft is followed successively by from lower to upper sweeps jet flow agitator under end agitator, plural serial stage, two-way jet flow agitator and the lower jet agitator that suspends, the lower jet agitator that wherein suspends limits by upper and lower positioning step, can fluctuate; Tank is external is provided with chuck, and chuck connects steam valve, drain valve and inline valve, and chuck is also connected with water intaking valve and return water pipe control valve; Tank base is connected Middle pressure draught fan and is provided with paint delivery valve; Described end agitator of sweeping comprises stir shaft, interior cylinder and urceolus, and stir shaft and interior cylinder are welded as a whole through axial blade, and interior cylinder extends to cone cylinder downwards, and cone cylinder is welded by fagging with urceolus; Interior cylinder inwall is welded with circulation blade, cone cylinder inwall is welded with centrifuge scraper; Under described plural serial stage, jet flow agitator is in series by 2-10 lower jet flow agitator, and lower jet flow agitator comprises stir shaft and urceolus, and stir shaft and urceolus flow down spray blade through liquid and be welded as a whole; Described two-way jet flow agitator comprises stir shaft, interior cylinder and urceolus, and stir shaft and interior cylinder flow down spray blade through liquid and be welded as a whole, and interior cylinder and urceolus spray blade on liquid stream and be welded as a whole; Under described suspension, jet agitator comprises stir shaft, axle sleeve and urceolus, and stir shaft is splined shaft, and axle sleeve is also spline axle sleeve, and spline axle sleeve can move on splined shaft; Spline axle sleeve and urceolus connect as one through blade.
2. paint stirring blend tank according to claim 1, it is characterised in that: described tank body is provided with manhole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510092867.9A CN104607087B (en) | 2015-03-03 | 2015-03-03 | Paint stirring blend tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510092867.9A CN104607087B (en) | 2015-03-03 | 2015-03-03 | Paint stirring blend tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104607087A CN104607087A (en) | 2015-05-13 |
| CN104607087B true CN104607087B (en) | 2016-06-01 |
Family
ID=53141891
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510092867.9A Active CN104607087B (en) | 2015-03-03 | 2015-03-03 | Paint stirring blend tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104607087B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112452241A (en) * | 2020-10-27 | 2021-03-09 | 昆山协盛电子有限公司 | Paint mixing process for spraying water pump |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102188922B (en) * | 2010-03-10 | 2014-05-14 | 董保成 | Paddle floating-type stirring machine |
| CN102358760B (en) * | 2011-07-22 | 2012-12-19 | 浙江大学 | Stirred tank reactor |
| CN204097476U (en) * | 2014-11-05 | 2015-01-14 | 吉首大学 | Air-pump type fermentor tank |
-
2015
- 2015-03-03 CN CN201510092867.9A patent/CN104607087B/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN104607087A (en) | 2015-05-13 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104607076B (en) | Underflow stirs chemical combination bucket | |
| CN104028146B (en) | A kind of emulsion mixture multiaxial type Bidirectional agitator | |
| CN104043374B (en) | Multi-stage axial flow self-balancing type agitator | |
| CN204320459U (en) | A kind of ore pulp pretreatment system of intensified Daqu medicament dispersion | |
| CN109401524A (en) | A kind of preparation process of water paint, equipment and formula | |
| CN104624097B (en) | Low energy consumption lifting agitator | |
| CN104607087B (en) | Paint stirring blend tank | |
| CN201613119U (en) | Mortar stirring barrel with mortar spoiler | |
| CN104611194B (en) | Underflow stirred fermentor | |
| CN101721939A (en) | Mortar stirring bucket with mortar flow blocking device | |
| CN204455082U (en) | Underflow stirred fermentor | |
| CN204816354U (en) | Novel homogeneous emulsifying machine | |
| CN206045957U (en) | A kind of high efficiency dispersion system | |
| CN203346339U (en) | Production equipment for high-viscosity epoxy emulsified asphalt | |
| CN204447833U (en) | Underflow stirs chemical combination bucket | |
| CN104621422A (en) | Concentrated eight-treasure porridge slurry stirring and cooking pot | |
| CN212663895U (en) | Centrifugal machine for producing flotation agent | |
| CN104353377B (en) | A kind of agitating device with agitating plate | |
| CN101417217A (en) | Stirring device special for all-purpose adhesive | |
| CN203635090U (en) | Slurry unpowered mixing tank used for copper flotation technology | |
| CN208757341U (en) | For the mixing arrangement in waterborne polyurethane synthetic leather inorganic agent production system | |
| CN105268340A (en) | Spiral stirring device | |
| CN204933281U (en) | Spiral agitator | |
| CN206965196U (en) | Machinery emulsification continuous extraction equipment | |
| CN206996877U (en) | Crystallization backwash centrifuge |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20181212 Address after: 225300 Beizhuang Village, Suchen Town, Hailing District, Taizhou City, Jiangsu Province (Suchen) Patentee after: Taizhou Sihai CNC Machine Tool Factory Address before: 416000 No. 120 Renmin South Road, Jishou City, Xiangxi Tujia and Miao Autonomous Prefecture, Hunan Patentee before: Jishou University |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20211129 Address after: 225300 Haitong company, 2f, administrative service center, No. 3, Fuqian Road, Hailing District, Taizhou City, Jiangsu Province Patentee after: Taizhou Haitong Asset Management Co., Ltd Address before: 225300 Beizhuang Village, Suchen Town, Hailing District, Taizhou City, Jiangsu Province (Suchen) Patentee before: Taizhou Sihai CNC Machine Tool Factory |
|
| TR01 | Transfer of patent right |