CN207823174U - A kind of system of grinding superfine powder production technology - Google Patents
A kind of system of grinding superfine powder production technology Download PDFInfo
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- CN207823174U CN207823174U CN201721446929.2U CN201721446929U CN207823174U CN 207823174 U CN207823174 U CN 207823174U CN 201721446929 U CN201721446929 U CN 201721446929U CN 207823174 U CN207823174 U CN 207823174U
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Abstract
The utility model discloses a kind of systems of grinding superfine powder production technology, including elevator one, elevator two, elevator three, roll squeezer, weighing cabin, V-type powder concentrator, intelligence is double to drive powder fine grading machine, cyclone collector, wind turbine one, bag filter, integral type separate compiling ball mill, by using elevator one, elevator two, elevator three, roll squeezer, weighing cabin, V-type powder concentrator, intelligence is double to drive powder fine grading machine, cyclone collector, wind turbine one, combination connection between bag filter and integral type separate compiling ball mill, solves the irrealizable large-scale continuous production of the prior art, quality is low, the high problem of production cost.
Description
Technical field
The utility model is related to a kind of systems of grinding superfine powder production technology.
Background technology
Industrial waste is used widely in building materials industry as mixing material, such as gangue in the prior art, this
It is the effective way for digesting industrial waste without coagulating.Research and engineering practice show industrial waste as mixing material to cement and mix
The size of solidifying soil effect is closely related with fineness, and fineness is thinner, and function and effect are better.Especially mixing material Blain specific surface is big
In or equal to 700 ㎡/㎏, average grain diameter is less than 6 μm, and the chemically and physically effect of mixing material is not fully exerted, in this way
Not only quality is high but also at low cost for the cement produced.Existing superfine powder production technology is all first to carry out powder to industrial waste
Mill, then carry out selecting powder, finally mix.Not only technology is excessively single for above-mentioned production technology, production equipment used, cannot achieve big
Scale continuous production, and production cost is high.
Utility model content
Technical problem to be solved in the utility model provides a kind of system of grinding superfine powder production technology, and the grinding is super
The system of fine powder production technique can not only realize large-scale continuous production, and quality is high, production cost is low.
In order to solve the above technical problems, a kind of system of grinding superfine powder production technology of the utility model, including elevator
One, elevator two, elevator three, roll squeezer, weighing cabin, V-type powder concentrator, intelligence are double drives powder fine grading machine, cyclone collection
Device, wind turbine one, bag filter, integral type separate compiling ball mill, the discharge port of elevator one pass through pipeline and weighing cabin
Feed inlet is connected, and the discharge port of weighing cabin is connected with the feed inlet of roll squeezer, and the discharge port of roll squeezer passes through pipeline and elevator
Two feed inlet is connected, and the discharge port of elevator two is connected by pipeline with the feed inlet of V-type powder concentrator, the air outlet of wind turbine one
It is connected with the air inlet of V-type powder concentrator by pipeline, the air outlet of V-type powder concentrator is divided by pipeline and the double powder precisions of driving of intelligence
The air inlet of grade machine is connected, the air inlet phase that the double air outlets for driving powder fine grading machine of intelligence pass through pipeline and cyclone collector
Even, the air outlet of cyclone collector is connected by pipeline with the air inlet of wind turbine one, and intelligence is double to drive the thick of powder fine grading machine
Tube cell is connected by pipeline with the feed inlet of weighing cabin, and the double middle coarse powder pipes for driving powder fine grading machine of intelligence pass through pipeline and one
The spout of body formula separate compiling ball mill front is connected, and the discharge port of cyclone collector passes through air conveyer flume one and pipeline
It is connected with the feed inlet of the charging/discharging device at integral type separate compiling ball mill rear portion, integral type separate compiling ball mill rear portion
The discharge port of charging/discharging device is connected by air conveyer flume with the feed inlet of elevator three, integral type separate compiling ball mill
The air outlet of the charging/discharging device at rear portion is connected by pipeline with the air inlet of bag filter, and the air outlet of bag filter is logical
Air duct is crossed with the air inlet of wind turbine two to be connected, the discharge port of bag filter with pass through screw conveyor and pipeline and elevator three
Feed inlet be connected, the discharge port of elevator three is connected by air conveyer flume two and pipeline with warehouse for finished product.
The integral type separate compiling ball mill, including driving device, drawing-in device, cylinder, partition panel, input and output material dress
It sets, inner cylinder, conveying device, drawing-in device and charging/discharging device are separately positioned on the front-end and back-end of cylinder, drawing-in device packet
Spout is included, cylinder disposes on the drive means, and partition panel is arranged in cylinder, and inner cylinder is arranged by supporting rod in cylinder
Rear portion internal and positioned at cylinder, one end of conveying device is arranged on one end of inner cylinder；Charging/discharging device includes shell, sky
Mandrel, roto-siofter, material guiding hopper, guide channel, opening material storing box, shell upper end is equipped with feed inlet, the lower part of shell is equipped with discharging
Mouthful, the top of shell be equipped with air outlet, hollow shaft is located at turn around in sieve, and roto-siofter is located in shell, hollow shaft and roto-siofter
One end is arranged on the rear end of cylinder, and the axial line of hollow shaft and the axial line of roto-siofter overlap, and hollow shaft is circumferentially uniformly distributed
Equipped with through-hole, guide channel includes straight tube and inclined tube, and straight tube one end is arranged on the through-hole of hollow shaft circumferential direction, the other end of straight tube
It is connected with the lower end of material guiding hopper across roto-siofter, one end of inclined tube is connected with straight tube one end, and the other end and the conveying of inclined tube fill
The feed opening set is connected, and is equipped with striker plate between adjacent material guiding hopper, left plate of the opening material storing box by semi-circular shape, semi-circular shape
Right plate and semicircular arc plate constitute, the side point of the large semi-circular of the left plate of semi-circular shape and the right plate of semi-circular shape
One opening babinet of composition, the opening box body on the two sides of semicircular arc plate are not set and are located at the side of roto-siofter and setting
On shell, the material guiding hopper in hollow shaft side is located in the opening box body, the left side of the semi-circular shape of the opening babinet
The circular side of the smaller part of plate and the right plate of semi-circular shape and the periphery of roto-siofter match, and opening babinet is equipped with feed inlet,
The feed inlet is equipped with feed pipe, which passes through shell；Lightweight abrasive body is respectively arranged in the cylinder and inner cylinder.
Material guiding hopper includes left plate, right panel, front and rear panels, and left plate is parallel with right panel and keeps a spacing, front and rear panels
The front-end and back-end for being separately positioned on left plate and right panel constitute a hollow taper structure, under the material guiding hopper of hollow taper structure
Port is arranged on the through-hole of hollow shaft circumferential direction, and the left plate and right panel of the material guiding hopper of hollow taper structure are opened with described respectively
The left plate of the semi-circular shape of mouth material storing box and the right plate of semi-circular shape are corresponding, the back plate of the material guiding hopper of hollow taper structure
Upper end it is corresponding with the opening semicircular arc plate of material storing box.
The back plate of the material guiding hopper of the hollow taper structure is arc plate structure.
The conveying device is helix transporting device.
The axial line of the cylinder and inner cylinder overlaps.
The quantity of the material guiding hopper is three to ten.
In the system of above-mentioned grinding superfine powder production technology, by using elevator one, elevator two, elevator three,
Roll squeezer, weighing cabin, V-type powder concentrator, intelligence is double drive powder fine grading machines, cyclone collector, wind turbine one, bag filter and
Combination connection between integral type separate compiling ball mill, solves the irrealizable large-scale continuous production of the prior art, matter
Measure problem low, that production cost is high.
Description of the drawings
Fig. 1 is the structural schematic diagram of the system of the utility model grinding superfine powder production technology；
Fig. 2 is the structural schematic diagram of integral type separate compiling ball mill；
Fig. 3 is the structure enlargement diagram of charging/discharging device in Fig. 2.
Specific implementation mode
In Fig. 1, the utility model discloses a kind of system of grinding superfine powder production technology, including elevator 1, carry
Rise the double drive powder fine grading machines 6 of machine 22, elevator 3 13, roll squeezer 3, weighing cabin 4, V-type powder concentrator 5, intelligence, whirlwind is received
Storage 7, wind turbine 1, bag filter 14, integral type separate compiling ball mill 10, the discharge port of elevator 1 by pipeline with
The feed inlet of weighing cabin 4 is connected.The discharge port of weighing cabin 4 is connected with the feed inlet of roll squeezer 3, and the discharge port of roll squeezer 3 passes through
Pipeline is connected with the feed inlet of elevator 22, the feed inlet phase that the discharge port of elevator 22 passes through pipeline and V-type powder concentrator 5
Even.The air outlet of wind turbine 1 is connected by pipeline with the air inlet of V-type powder concentrator 5.The air outlet of V-type powder concentrator 5 passes through pipeline
It is connected with the double air inlets for driving powder fine grading machine 6 of intelligence, the double air outlets for driving powder fine grading machine 6 of intelligence pass through pipeline
It is connected with the air inlet of cyclone collector 6, the air outlet of cyclone collector 7 is connected by pipeline with the air inlet of wind turbine 1.Intelligence
The double coarse powder pipes for driving powder fine grading machines 6 of energy are connected by pipeline with the feed inlet of weighing cabin 4, the double drive powder precisions point of intelligence
The middle coarse powder pipe of grade machine 6 is connected by pipeline with the spout 11 of 10 front of integral type separate compiling ball mill.Cyclone collector 7
Discharge port pass through air conveyer flume 1 and pipeline and the charging/discharging device 12 at 10 rear portion of integral type separate compiling ball mill
Feed inlet is connected.The discharge port of the charging/discharging device 12 at 10 rear portion of integral type separate compiling ball mill by air conveyer flume with
The feed inlet of elevator 3 13 is connected.The air outlet of the charging/discharging device 12 at 10 rear portion of integral type separate compiling ball mill passes through pipe
Road is connected with the air inlet of bag filter 14.The air inlet phase that the air outlet of bag filter 14 passes through air duct and wind turbine two
Even.The discharge port of bag filter 14 is connected with by screw conveyor 15 and pipeline with the feed inlet of elevator 3 13, is promoted
The discharge port of machine 3 13 is connected by air conveyer flume two and pipeline with warehouse for finished product.
As shown in Figures 2 and 3, in the present embodiment, the integral type separate compiling ball mill 10, including driving device, feed
Expect device 26, cylinder 25, partition panel, charging/discharging device 12, inner cylinder 16, conveying device 17, drawing-in device 26 and input and output material dress
Set 12 front-end and back-end for being separately positioned on cylinder 25.Drawing-in device 26 includes spout, and drawing-in device 26 is the prior art, therefore
It is not described in detail.Cylinder 25 disposes on the drive means, and driving device is the prior art, and it is also existing that cylinder 25, which is placed in driving device,
Technology, therefore be not described in detail.Partition panel is arranged in cylinder 25.Inner cylinder 16 is arranged in the inside of cylinder 25 and is located at by supporting rod
The rear portion of cylinder 25.One end of conveying device 17 is arranged on one end of inner cylinder 16.Charging/discharging device includes shell 27, hollow
Axis 19, roto-siofter 29, material guiding hopper 20, guide channel, opening material storing box 21, hollow shaft 19 are located in shell 27,27 upper end of shell
Top equipped with feed inlet 23, shell 27 is equipped with feed inlet, the lower part of shell 27 is equipped with discharge port 24, the top of shell 27 is equipped with
Air outlet.Hollow shaft 19 is located at turn around in sieve 29, and roto-siofter 29 is located in shell 27, and one end of hollow shaft 19 and roto-siofter 29 is equal
It is arranged on the rear end of cylinder 25, the axial line of hollow shaft 19 and the axial line of roto-siofter 29 overlap.Hollow shaft 19 is circumferential equal
It is laid with through-hole.Guide channel includes straight tube 28 and inclined tube 18, and 28 one end of straight tube is arranged on the circumferential through-hole of hollow shaft 19, directly
The other end of pipe 28 is connected across roto-siofter 29 with the lower end of material guiding hopper 20, and one end of inclined tube 18 is connected with 28 one end of straight tube,
The other end of inclined tube 18 is connected with the feed opening of conveying device 17, and striker plate 30 is equipped between adjacent material guiding hopper 20.Be open storing
Case 21 is made of the left plate of semi-circular shape, the right plate of semi-circular shape and semicircular arc plate, the left plate of semi-circular shape and half
The side of the large semi-circular of the right plate of circular ring shape is separately positioned on one opening babinet of composition on the two sides of semicircular arc plate,
The opening box body is located at the side of roto-siofter 29 and is arranged on shell 27, and the material guiding hopper 20 in 19 side of hollow shaft is located at institute
It states in opening babinet 21, the circular side of smaller part of the left plate of the semi-circular shape of the opening babinet 21 and the right plate of semi-circular shape
Side and the periphery of roto-siofter 29 match.The babinet 21 that is open is equipped with feed inlet, which is equipped with feed pipe 22, the feed pipe
22 pass through shell 27；It is respectively arranged with lightweight abrasive body in the cylinder 25 and inner cylinder 16.
Material guiding hopper 20 includes left plate 32, right panel, foreboard 33 and back plate 31, and left plate 32 is parallel with right panel and keeps a spacing,
Foreboard 33 and back plate 31 are separately positioned on left plate 32 and the front-end and back-end of right panel constitute a hollow taper structure.Hollow taper
The lower port of the material guiding hopper 20 of structure is arranged on the circumferential through-hole of the hollow shaft 19, the material guiding hopper 20 of hollow taper structure
Left plate 32 and right panel are corresponding with the left plate of the semi-circular shape of the opening material storing box 21 and the right plate of semi-circular shape respectively,
The semicircular arc plate 34 of the upper end of the back plate 31 of the material guiding hopper 20 of hollow taper structure and the opening material storing box 21
It is corresponding.
For the ease of guide, the back plate 31 of the material guiding hopper 20 of the hollow taper structure is arc plate structure, the arc panel
Upper end it is corresponding with the opening semicircular arc plate 34 of material storing box 21.
In order to simplify structure and reduce cost, the conveying device 17 is helix transporting device,
For smooth running, the axial line of the cylinder 25 and inner cylinder 16 overlaps.
In order to improve guide effect, the quantity of the material guiding hopper 20 is three to ten.
In above-mentioned multilevel grinding superfine powder production technology, material passes through the broken of roll squeezer 10, point of V-type powder concentrator 5
It selects, after intelligence pair drive powder fine grading machines 6 sort the collection with cyclone collector 7 again, respectively enters integral type difference powder
The front-end and back-end of abrading-ball grinding machine 10 become finished product entering cost library after being ground, and above-mentioned technique not only realizes to be connected on a large scale
Continuous production, and quality is high, production cost is low；In the system of above-mentioned grinding superfine powder production technology, by using elevator
One 1, elevator 22, elevator 3 13, roll squeezer 3, weighing cabin 4, V-type powder concentrator 5, intelligence it is double drive powder fine grading machines 6,
Combination connection between cyclone collector 7, wind turbine 1, bag filter 14 and integral type separate compiling ball mill 10, solves
The irrealizable large-scale continuous production of the prior art, the problem that quality is low, production cost is high.
Claims (1)
1. a kind of system of grinding superfine powder production technology, which is characterized in that including elevator one, elevator two, elevator three,
Roll squeezer, weighing cabin, V-type powder concentrator, intelligence is double drive powder fine grading machines, cyclone collector, wind turbine one, bag filter,
The discharge port of integral type separate compiling ball mill, elevator one is connected by pipeline with the feed inlet of weighing cabin, and weighing cabin goes out
Material mouth is connected with the feed inlet of roll squeezer, and the discharge port of roll squeezer is connected by pipeline with the feed inlet of elevator two, elevator
Two discharge port is connected by pipeline with the feed inlet of V-type powder concentrator, and the air outlet of wind turbine one passes through pipeline and V-type powder concentrator
Air inlet is connected, and the air outlet of V-type powder concentrator is connected by pipeline with the double air inlets for driving powder fine grading machine of intelligence, intelligence
Double air outlets for driving powder fine grading machine are connected by pipeline with the air inlet of cyclone collector, the air outlet of cyclone collector
It is connected with the air inlet of wind turbine one by pipeline, the double coarse powder pipes for driving powder fine grading machines of intelligence pass through pipeline and weighing cabin
Feed inlet is connected, and the double middle coarse powder pipes for driving powder fine grading machine of intelligence pass through pipeline and integral type separate compiling ball mill front
Spout be connected, the discharge port of cyclone collector passes through air conveyer flume one and pipeline and integral type separate compiling ball mill
The feed inlet of the charging/discharging device at rear portion is connected, and the discharge port of the charging/discharging device at integral type separate compiling ball mill rear portion passes through
Air conveyer flume is connected with the feed inlet of elevator three, the outlet air of the charging/discharging device at integral type separate compiling ball mill rear portion
Mouthful it is connected with the air inlet of bag filter by pipeline, the air inlet that the air outlet of bag filter passes through air duct and wind turbine two
It is connected, the discharge port of bag filter is connected with by screw conveyor and pipeline with the feed inlet of elevator three, elevator three
Discharge port be connected with warehouse for finished product by air conveyer flume two and pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721446929.2U CN207823174U (en) | 2017-11-02 | 2017-11-02 | A kind of system of grinding superfine powder production technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721446929.2U CN207823174U (en) | 2017-11-02 | 2017-11-02 | A kind of system of grinding superfine powder production technology |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207823174U true CN207823174U (en) | 2018-09-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721446929.2U Active CN207823174U (en) | 2017-11-02 | 2017-11-02 | A kind of system of grinding superfine powder production technology |
Country Status (1)
| Country | Link |
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| CN (1) | CN207823174U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107617501A (en) * | 2017-11-02 | 2018-01-23 | 江苏吉能达环境能源科技有限公司 | Multilevel grinding superfine powder production technology and its system |
| CN109759212A (en) * | 2019-01-23 | 2019-05-17 | 宁波北新建材有限公司 | A kind of preparation facilities preparing coagulant using waste gypsum plate |
-
2017
- 2017-11-02 CN CN201721446929.2U patent/CN207823174U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107617501A (en) * | 2017-11-02 | 2018-01-23 | 江苏吉能达环境能源科技有限公司 | Multilevel grinding superfine powder production technology and its system |
| CN107617501B (en) * | 2017-11-02 | 2023-10-31 | 江苏吉能达环境能源科技有限公司 | Multistage grinding superfine powder production process and system thereof |
| CN109759212A (en) * | 2019-01-23 | 2019-05-17 | 宁波北新建材有限公司 | A kind of preparation facilities preparing coagulant using waste gypsum plate |
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