CN207493637U - Compound batch mixing pulping device - Google Patents
Compound batch mixing pulping device Download PDFInfo
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- CN207493637U CN207493637U CN201721550008.0U CN201721550008U CN207493637U CN 207493637 U CN207493637 U CN 207493637U CN 201721550008 U CN201721550008 U CN 201721550008U CN 207493637 U CN207493637 U CN 207493637U
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- cylinder body
- mixing tank
- coating colors
- pulping device
- batch mixing
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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Abstract
This application involves mixed between a kind of compound fertilizer raw materials for production, melt slurry, pulping device more particularly to a kind of compound batch mixing pulping device；Its emulsification pulper, controller for including at least two connected mixing tank for coating colors, being connected with least significant end mixing tank for coating colors；Mixing tank for coating colors includes cylinder body, variable-frequency motor and agitating shaft；The variable-frequency motor being connected with controller outside cylinder body is installed, the agitating shaft being connected with variable-frequency motor is equipped in cylinder body.Due to implementing above-mentioned technical proposal, the application makes the good slurry of low concentration meltbility by least two connected mixing tank for coating colors, and consolute is abundant, viscosity increases；Ensure finished particle uniformity, improve granule strength, reduce finished product caking rate；Utilize the cooperation of press-down type blade group, upper-turn-type blade group, slurry is enabled to form inner ebullition movement, it is made to stir intensity and is greatly increased, has effectively ensured the uniform and stable property of slurry, viscous wall fouling and spraying state are all eliminated simultaneously, ensure that the safety and stability of production.
Description
Technical field
This application involves mixed between a kind of compound fertilizer raw materials for production, melt slurry, pulping device more particularly to a kind of compound batch mixing
Pulping device.
Background technology
At present during composite heat transfer, in addition between material to be considered mixing, other than the control of nutrient, more to ensure life
Output particle shape is good（Particle is uniform, intensity is high, crushes and does not lump less,）, nutrient content stablize, diversification of varieties is deep by vast fertilizer
Expect the composite fertilizer of user's favorable comment；Some, scientific and reasonable in the various raw material proportions for ensureing production composite fertilizer more than accomplishing
In the case of, material must stir evenly inside mixing tank for coating colors, congruent melting is sufficiently mixed between various raw materials, in corresponding temperature
Made within control range dissolubility is good, nutrient uniformly, the slurry of proper temperature, be this process key point.
Volume, heat exchange area, agitating mode, the control means of stirring, the product structure of current batch mixing pulping equipment are equal
Not as good as people's will：1）In terms of finished product, nutrient fluctuation is big, granule strength is relatively low, crushed particles are more, rounding property is poor, caking phenomenon compared with
It is serious；2）Control aspect is produced, production slurry, which is easily adhered, to be susceptible to plugging phenomenon in equipment inner wall, process pipelines, melts
Slurry liquid is uneven easily to cause nozzle to block interruption production and a large amount of substandard products is caused to generate；3）Secure context, due to stirring side
Formula influences high temperature feed liquid spillage equipment and easily personnel is caused to scald；4）Scene and equipment, consolute slurry splash out adhering device and cause
Corresponding field device cleaning, cleaning difficulty are big after burn into material cooling caking；5）Xinjiang four seasons difference variation is big, and common changes
Heat pipe is difficult to meet demand.
Invention content
The purpose of the application be to propose a kind of finished particle uniformly, caking rate reduce, increase stirring intensity ensures slurry
Stability, eliminate the compound batch mixing pulping device of viscous wall fouling and spraying state.
What the application was realized in：Compound batch mixing pulping device, including at least two connected mixing tank for coating colors and most end
Emulsification pulper, the controller that end mixing tank for coating colors is connected；Mixing tank for coating colors includes cylinder body, variable-frequency motor and agitating shaft；It is installed outside cylinder body
Have a variable-frequency motor being connected with controller, be equipped with the agitating shaft being connected with variable-frequency motor in cylinder body, on agitating shaft from top to bottom according to
It is secondary that press-down type blade group, upper-turn-type blade group are installed；The viscosity inductor being connected with controller is also equipped in cylinder body.
Further, feed inlet is equipped at the top of cylinder body, cylinder side wall is equipped with overflow port；The overflow port of upper level mixing tank for coating colors leads to
The feed inlet that pipeline is crossed with next stage mixing tank for coating colors is connected；The connected emulsification pulper of least significant end mixing tank for coating colors.
Further, overflow port is equipped with blow valve port.
Further, the height of overflow port is more than the height of press-down type blade group.
Further, the inside of cylinder body and outer wall are equipped with heating coil.
Further, the barrel for emulsifying pulper is externally provided with heat tracing coil pipe.
Due to implementing above-mentioned technical proposal, the application is by least two connected mixing tank for coating colors by solid material and nitrogenous height
The good slurry of low concentration meltbility is made in warm molten liquid mixing, and consolute is abundant, viscosity increases；Finally by emulsification pulper to big
Particulate material is sheared, is crushed, is mixed again；Ensure finished particle uniformity, improve granule strength, reduce finished product caking
Rate；Using the cooperation of press-down type blade group, upper-turn-type blade group, slurry is enabled to form inner ebullition movement, it is made to stir intensity significantly
Increase, effectively ensured the uniform and stable property of slurry, while viscous wall fouling and spraying state are all eliminated, ensure that production
Safety and stability.
Description of the drawings：The concrete structure of the application is provided by following drawings and examples：
Fig. 1 is the connection diagram of the application；
Fig. 2 is the structure diagram of mixing tank for coating colors；
Fig. 3 is the structure diagram for emulsifying pulper.
Legend：1. pulper is emulsified, 2. controllers, 3. cylinder bodies, 4. variable-frequency motors, 5. agitating shafts, 6. press-down type blade groups,
7. upper-turn-type blade group, 8. viscosity inductors, 9. feed inlets, 10. overflow ports, 11. blow valve ports, 12. heating coils, 13. heat tracings
Coil pipe.
Specific embodiment：
The application is not limited by following embodiments, can be determined specifically with actual conditions according to the technical solution of the application
Embodiment.
As shown in Figures 1 to 3, compound batch mixing pulping device includes at least two connected mixing tank for coating colors and least significant end mixing tank for coating colors
Connected emulsification pulper 1, controller 2；Mixing tank for coating colors includes cylinder body 3, variable-frequency motor 4 and agitating shaft 5；It is equipped with outside cylinder body 3
The variable-frequency motor 4 being connected with controller 2, is equipped with the agitating shaft 5 being connected with variable-frequency motor 4 in cylinder body 3, on agitating shaft 5 by up to
Under be sequentially installed with press-down type blade group 6, upper-turn-type blade group 7；The viscosity sense being connected with controller 2 is also equipped in cylinder body 3
Answer device 8.
By taking two mixing tank for coating colors as an example：50%（Phosphorous, potassium, filler material）Solid material is tentatively incorporated from the mixing tank for coating colors of head end, with
The good slurry of low concentration meltbility is made in nitrogenous high-temperature fusion liquid mixing, and the mixing tank for coating colors of second is then entered by overflow manner
With other 50%（Phosphorous, potassium, filler material）The secondary consolute of solid material, the phosphoric acid after consolute increases, again by overflow side
Formula enters emulsification pulper 1, and emulsification pulper 1 carries out the uniform bulky grain raw material of consolute non-inside prepared slurry again
Shearing crushes, mixing, and last slurry produces all kinds of complex fertilizer products by prilling spry；The product nutrient obtained in this way is more
Add stabilization, finished particle uniformity, granule strength are obtained for raising, reduce the caking rate of finished product.
Existing upper-turn-type agitating mode, consolute slurry all move upwards, and part adheres to chamber wall bonding into dirt, part
It splashes out container and causes insecurity, while the spilling slurry after consolute is it is difficult to ensure that uniformity；And on agitating shaft 5 from top to bottom
Press-down type blade group 6, upper-turn-type blade group 7 are sequentially installed with, motion mode of the consolute material in mixing tank for coating colors can be changed：Lower part
Upper-turn-type blade group 7 bottom slurry dug move upwards, it is pressed downward hitting again by the press-down type blade group 6 of top,
Inner ebullition movement is formed, it is made to stir intensity and is greatly increased, has effectively ensured the uniform and stable property of consolute slurry, while will be existing
There are the viscous wall fouling occurred in technology and spraying state to effectively eliminate, ensure that the safety and stability of production.
Viscosity inductor 8 in cylinder body 3 can detect slurry density, signal be passed to controller 2, controller 2 passes through
Variable-frequency motor 4 is controlled to realize the velocity of rotation for changing agitating shaft 5.It can be directed to the consolute slurry of different product, different viscositys in this way
Different stirring intensities is provided；When the low-phosphorous low potassium product of production（Or the mixing tank for coating colors supplying solid material of head end is less）When, it mixes
The viscosity of melt slurry is significant lower, and required stirring intensity is also just low；Produce the high potassium product of high phosphorus（Or the mixing tank for coating colors supplying of end
Solid material is more）When, required stirring intensity is just corresponding to be improved.Therefore by adjusting, low frequency control can be used, prevent consolute from starching
Liquid is glued wall and splash or is controlled using high frequency, ensures the uniform and stable property of its consolute slurry.
The application is supported in batch mixing uniformity, the control of the temperature of batch mixing, the stirring intensity of batch mixing, the safety of operation, finished product
Stability, all various aspects of rounding property of particle divided are obtained for abundant guarantee, consolidate so as to efficiently control and reduce phosphorus potassium
The cost consumption of body material, has widened market at the caking rate for reducing screening defect rate, reducing finished product.
As shown in Figure 1,3 top of cylinder body is equipped with feed inlet 9,3 side wall of cylinder body is equipped with overflow port 10；Upper level mixing tank for coating colors overflows
Head piece 10 is connected by pipeline with the feed inlet 9 of next stage mixing tank for coating colors；The connected emulsification pulper 1 of least significant end mixing tank for coating colors.It overflows
Head piece 10 is located at side wall, then can be achieved to enter the mixing tank for coating colors of next stage or emulsification pulper 1 by overflow manner, safer flat
Surely.
As shown in Fig. 2, overflow port 10 is equipped with blow valve port 11.It, can when some mixing tank for coating colors breaks down or blocks
Quickly corresponding mixing tank for coating colors is unloaded, individually carries out pipeline sweeping maintenance.
As shown in Fig. 2, the height of overflow port 10 is more than the height of press-down type blade group 6.
As shown in Fig. 2, the inside of cylinder body 3 and outer wall are equipped with heating coil 12.Nitrogenous high-temperature molten material and addition
The solid material of the phosphorous potassium of different proportion etc. to form consolute slurry, temperature must be controlled within the scope of certain, high
Much more required for the low-phosphorous potassium of heat ratio, production in summer finished product needed for phosphorus potassium, winter production product, this has been resulted in for not
The difference of same product, Various Seasonal the application required temperature, passes through the setting of heating coil 12 so that the application adapts to various productions
The slurrying work of product under circumstances.
As shown in figure 3, the barrel of emulsification pulper 1 is externally provided with heat tracing coil pipe 13.
More than technical characteristic constitutes the most preferred embodiment of the application, is imitated with stronger adaptability and best implementation
Fruit can increase and decrease inessential technical characteristic according to actual needs, to meet the needs of different situations.
Claims (8)
1. a kind of compound batch mixing pulping device, it is characterised in that：Including at least two connected mixing tank for coating colors and least significant end mixing tank for coating colors
Connected emulsification pulper, controller；Mixing tank for coating colors includes cylinder body, variable-frequency motor and agitating shaft；It is equipped with and controls outside cylinder body
The variable-frequency motor that device is connected, cylinder body is interior to be equipped with the agitating shaft being connected with variable-frequency motor, is from top to bottom sequentially installed on agitating shaft
Press-down type blade group, upper-turn-type blade group；The viscosity inductor being connected with controller is also equipped in cylinder body.
2. compound batch mixing pulping device according to claim 1, it is characterised in that：Feed inlet, cylinder body are equipped at the top of cylinder body
Side wall is equipped with overflow port；The overflow port of upper level mixing tank for coating colors is connected by pipeline with the feed inlet of next stage mixing tank for coating colors；Least significant end
The connected emulsification pulper of mixing tank for coating colors.
3. compound batch mixing pulping device according to claim 2, it is characterised in that：Overflow port is equipped with blow valve port.
4. the compound batch mixing pulping device according to Claims 2 or 3, it is characterised in that：The height of overflow port, which is more than, to be pushed
The height of formula blade group.
5. the compound batch mixing pulping device according to claims 1 or 2 or 3, it is characterised in that：The inside of cylinder body and outer wall are equal
Equipped with heating coil.
6. compound batch mixing pulping device according to claim 4, it is characterised in that：The inside of cylinder body and outer wall, which are equipped with, to be added
Hot coil.
7. the compound batch mixing pulping device according to claims 1 or 2 or 3, it is characterised in that：Outside the barrel for emulsifying pulper
Equipped with heat tracing coil pipe.
8. compound batch mixing pulping device according to claim 4, it is characterised in that：The barrel of emulsification pulper is externally provided with companion
Hot coil.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721550008.0U CN207493637U (en) | 2017-11-20 | 2017-11-20 | Compound batch mixing pulping device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721550008.0U CN207493637U (en) | 2017-11-20 | 2017-11-20 | Compound batch mixing pulping device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207493637U true CN207493637U (en) | 2018-06-15 |
Family
ID=62504783
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721550008.0U Active CN207493637U (en) | 2017-11-20 | 2017-11-20 | Compound batch mixing pulping device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207493637U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113209891A (en) * | 2021-05-08 | 2021-08-06 | 新疆慧尔智联技术有限公司 | Liquid fertilizer production process and production system |
| CN114307921A (en) * | 2021-12-15 | 2022-04-12 | 防城港盛农磷化有限公司 | Device and method for controlling slurry fluidity and curing efficiency |
-
2017
- 2017-11-20 CN CN201721550008.0U patent/CN207493637U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113209891A (en) * | 2021-05-08 | 2021-08-06 | 新疆慧尔智联技术有限公司 | Liquid fertilizer production process and production system |
| CN114307921A (en) * | 2021-12-15 | 2022-04-12 | 防城港盛农磷化有限公司 | Device and method for controlling slurry fluidity and curing efficiency |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180824 Address after: 842200 circular economy industrial park in Sha Ya county, Akesu, the Xinjiang Uygur Autonomous Region Patentee after: Xinjiang Jade Elephant Yang Chemical Co., Ltd. Address before: 842200 circular economy industrial park in Sha Ya county, Akesu, the Xinjiang Uygur Autonomous Region Patentee before: Xinjiang Jinsheng poplar Chemical Co., Ltd. |
|
| TR01 | Transfer of patent right |