CN112604777A - Superfine powder grinding preparation device and method - Google Patents
Superfine powder grinding preparation device and method Download PDFInfo
- Publication number
- CN112604777A CN112604777A CN202011474642.7A CN202011474642A CN112604777A CN 112604777 A CN112604777 A CN 112604777A CN 202011474642 A CN202011474642 A CN 202011474642A CN 112604777 A CN112604777 A CN 112604777A
- Authority
- CN
- China
- Prior art keywords
- grinding
- main shaft
- driving device
- grinding disc
- speed reducer
- 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.)
- Pending
Links
- 238000000227 grinding Methods 0.000 title claims abstract description 233
- 239000000843 powder Substances 0.000 title claims abstract description 91
- 238000000034 method Methods 0.000 title claims abstract description 18
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 40
- 239000000463 material Substances 0.000 claims abstract description 29
- 230000007246 mechanism Effects 0.000 claims abstract description 26
- 238000012216 screening Methods 0.000 claims abstract description 20
- 239000002245 particle Substances 0.000 claims description 32
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 238000007664 blowing Methods 0.000 claims description 2
- 229910010293 ceramic material Inorganic materials 0.000 claims description 2
- 230000000694 effects Effects 0.000 abstract description 11
- 239000002994 raw material Substances 0.000 abstract description 6
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 12
- 239000000395 magnesium oxide Substances 0.000 description 9
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 7
- 239000000347 magnesium hydroxide Substances 0.000 description 7
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 7
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 7
- 230000009471 action Effects 0.000 description 5
- 230000008878 coupling Effects 0.000 description 5
- 238000010168 coupling process Methods 0.000 description 5
- 238000005859 coupling reaction Methods 0.000 description 5
- 238000005096 rolling process Methods 0.000 description 4
- 239000011362 coarse particle Substances 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 239000003381 stabilizer Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000003801 milling Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 229910021532 Calcite Inorganic materials 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 1
- 239000010428 baryte Substances 0.000 description 1
- 229910052601 baryte Inorganic materials 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002367 phosphate rock Substances 0.000 description 1
- 238000005498 polishing Methods 0.000 description 1
- 238000009700 powder processing Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C15/08—Mills with balls or rollers centrifugally forced against the inner surface of a ring, the balls or rollers of which are driven by a centrally arranged member
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
- B02C23/24—Passing gas through crushing or disintegrating zone
- B02C23/32—Passing gas through crushing or disintegrating zone with return of oversize material to crushing or disintegrating zone
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C2015/002—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs combined with a classifier
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
Abstract
The invention discloses a superfine powder grinding preparation device and a method, the device comprises a shell, a first grinding mechanism, a second grinding mechanism, a screening device and a first fan, a feed inlet and a discharge outlet are arranged on the shell, the first grinding mechanism comprises a first driving device, a first speed reducer, a first main shaft and a grinding disc which are sequentially connected, the grinding disc can rotate by taking the first main shaft as a rotating shaft, the second grinding mechanism comprises a second driving device, a second speed reducer, a second main shaft, a rotary table supporting frame and a grinding roller which are sequentially connected, the rotary table supporting frame and the grinding roller can rotate by taking the second main shaft as the rotating shaft, the grinding roller and the grinding disc are matched for grinding, and a first air inlet and the screening device are arranged on the shell; also included are methods of using the above-described apparatus. The grinding roller and the grinding disc rotate reversely at high speed, and the grinding roller and the grinding disc are matched with wind power movement in the direction opposite to the rotation direction of the grinding roller, so that the grinding roller has high-efficiency grinding and grinding effects on raw materials, and can grind the materials into superfine powder in a short time.
Description
Technical Field
The invention relates to the technical field of powder preparation, in particular to a device and a method for grinding and preparing ultrafine powder.
Background
The Raymond mill has excellent milling performance, can efficiently grind multiple raw materials such as barite, calcite, dolomite, limestone, activated carbon, cement, phosphate rock, gypsum and the like to prepare fine powder, and is widely applied to multiple fields such as industrial production, daily life and the like. Traditional raymond machine includes parts such as grinding roller, grinding ring, spiller, selection powder machine, air-blower, and its basic operating principle is: the material enters a grinding chamber of the Raymond mill, the grinding roller revolves around a vertical axis under the drive of an electrode and simultaneously rotates, the grinding roller swings outwards under the action of centrifugal force to press a grinding ring, a scraper knife shovels the material and sends the material to a position between the grinding roller and the grinding ring, and the material is crushed into fine powder under the rolling and rolling of the grinding roller.
Although the traditional Raymond mill can realize material grinding, the problems of low grinding efficiency, long grinding time, high energy consumption, difficulty in preparing superfine powder and the like still exist, so that the working efficiency of the equipment is limited, and the milling cost is increased. Therefore, a new grinding device is urgently needed to be developed so as to improve the grinding efficiency and the productivity and meet the actual production needs.
Disclosure of Invention
Aiming at the problems, the invention researches and designs a superfine powder grinding and preparing device and a superfine powder grinding and preparing method to solve the problems of low grinding efficiency, long grinding time, high energy consumption, difficulty in preparing superfine powder and the like of the traditional Raymond mill. The technical means adopted by the invention are as follows:
a superfine powder grinding and preparing device comprises a shell, a first grinding mechanism, a second grinding mechanism, a screening device and a first fan, wherein a feed inlet and a discharge outlet are formed in the shell, the first grinding mechanism is arranged at the bottom of the shell and comprises a first driving device, a first speed reducer, a first main shaft and a grinding disc, the first driving device is connected with the first speed reducer, the first speed reducer is connected with the first main shaft, the first main shaft is connected with the grinding disc, the grinding disc is arranged in the shell and can rotate by taking the first main shaft as a rotating shaft, the second grinding mechanism is arranged at the top of the first grinding mechanism and comprises a second driving device, a second speed reducer, a second main shaft, a rotary table supporting frame and a grinding roller, and the second driving device is connected with the second speed reducer, the second speed reducer with the second main shaft links to each other, the second main shaft with the revolving stage support frame is connected, the revolving stage support frame with grinding roller fixed connection, revolving stage support frame and grinding roller can with the second main shaft is rotatory as the rotation axis, the grinding roller stretches into in the mill, and with the mill cooperation is ground, be equipped with first air intake on the casing, the height of first air intake is less than the bottom height of mill, first air intake with first fan links to each other, discharge gate department is equipped with the sieving mechanism that can filter the powder particle diameter.
Preferably, the grinding disc comprises a grinding ring, a base and air holes, the air holes penetrate through the base, the inner wall of the grinding ring is abutted against the side face of the grinding roller, and the rotation directions of the grinding roller and the grinding disc are opposite.
Preferably, a second air inlet is formed in the shell, the height of the second air inlet is higher than that of the top of the grinding disc, the second air inlet is connected with a second fan, and the airflow direction of the second air inlet is tangential to the periphery of the grinding disc.
Preferably, the screening device comprises a third driving device, a third main shaft and a powder concentrator, the third driving device is connected with the powder concentrator through the third main shaft, and the powder concentrator is arranged between the grinding disc and the discharge hole.
Preferably, the grinding device further comprises a bearing frame, the first driving device and the first speed reducer are fixed on the bearing frame, the first main shaft extends into the shell and is connected with the centers of the grinding rollers, the axes of the first main shaft and the second main shaft are overlapped, the second main shaft is connected with the center of the turntable support frame, at least two grinding rollers are uniformly distributed on the periphery of the turntable support frame, and the diameter of the grinding disc is 2/3-5/6 of the diameter of the shell.
Preferably, the first driving device and the second driving device are motors, and the grinding disc and the grinding roller are made of steel or ceramic materials.
A method for applying the superfine powder grinding preparation device comprises the following steps:
s1, feeding the materials into the grinding disc through the feeding hole, starting a first driving device and a second driving device, wherein the first driving device drives a first speed reducer to work, and the first speed reducer drives a first main shaft and the grinding disc to rotate;
s2, starting the first fan and the second fan, blowing air into the shell from the first air inlet and the second air inlet simultaneously, and forming spiral upward swirling air in the shell to assist material grinding;
and S3, starting a third driving device, and driving the powder concentrator to work through a third main shaft.
Preferably, in step S1, the first spindle and the second spindle rotate in opposite directions, and the grinding disc and the grinding roller rotate at 50-800 rpm.
Preferably, the first fan and the second fan are connected to an exhaust duct of the cyclone.
Preferably, the particle size range of the powder screened by the powder concentrator is 80-12000 meshes.
Compared with the prior art, the superfine powder grinding preparation device and the superfine powder grinding preparation method have the beneficial effects that:
1. the grinding roller and the grinding disc are connected by a large-torque and high-power motor, the grinding roller and the grinding disc rotate reversely at a high speed, and the grinding roller and the grinding disc are matched with wind power movement in a direction opposite to the rotating direction of the grinding roller or the grinding disc, so that the grinding roller has a powerful crushing effect, a high-speed friction effect, even an accelerating rolling and grinding effect on raw materials, and can grind the materials into ultrafine powder in a short time.
2. The material screening efficiency is high, and the controllability of the discharged particle size is strong. The discharged particle size screening not only depends on the powder concentrator, but also can be carried out by controlling the wind power rising in the machine body. The fine powder with smaller particle size can reach the powder concentrator under the wind power, while the coarse powder with larger particle size can not fall to the millstone along with the wind rise, and the particle size of the powder reaching the powder concentrator can be regulated and controlled by controlling the wind power.
3. The universality is good. The device and the method can be widely used for grinding and processing various powder, including magnesium oxide, magnesium hydroxide, various powder medicines and the like, and can also be used for material mixing, chemical reaction and other purposes.
4. Simple structure, flexible and convenient operation, low operation energy consumption and capability of realizing macro and continuous preparation of the ultrafine powder.
Drawings
FIG. 1 is a schematic view of the overall structure of the apparatus for producing a polishing pad according to the present invention.
Fig. 2 is a schematic view of the structure of the grinding disc of the present invention.
FIG. 3 is a particle size distribution diagram of the powder prepared in example 2 of the present invention.
In the figure, 1, a housing; 2. a first grinding mechanism; 3. a second grinding mechanism; 4. a screening device; 5. a first fan; 6. a second fan; 11. a feed inlet; 12. a discharge port; 13. a carrier; 14. a first air inlet; 15. a second air inlet; 21. a first driving device; 22. a first coupling; 23. a first speed reducer; 24. a first main shaft; 25. a grinding disc; 31. a second driving device; 32. a second coupling; 33. a second speed reducer; 34. a second main shaft; 35. a turntable support frame; 36. a minor axis; 37. a grinding roll shaft; 38. a stabilizer bar; 39. grinding the roller; 41. a third driving device; 42. a third main shaft; 43. selecting a powder machine; 251. grinding a ring; 252. a base; 253. and (4) air holes.
Detailed Description
Example 1:
as shown in fig. 1-2, an apparatus for grinding and preparing ultrafine powder comprises a housing 1, a first grinding mechanism 2, a second grinding mechanism 3, a screening device 4, and a first fan 5. Casing 1 is hollow structure, is equipped with feed inlet 11 and discharge gate 12 on casing 1, and feed inlet 11 sets up in the side of casing 1, and discharge gate 12 sets up in the top of casing 1. The first grinding mechanism 2 is arranged at the bottom of the shell 1, the first grinding mechanism 2 comprises a first driving device 21, a first speed reducer 23, a first main shaft 24 and a grinding disc 25, the first driving device 21 is connected with the first speed reducer 23 through a first coupler 22, the output end of the first speed reducer 23 is connected with one end of the first main shaft 24, and the other end of the first main shaft 24 is connected with the grinding disc 25. The grinding disc 25 is arranged in the shell 1, the grinding disc 25 can rotate by taking the first main shaft 24 as a rotating shaft, and materials to be ground are sent into the grinding disc 25 through the feeding hole 11 to be ground. The second grinding mechanism 3 is arranged at the top of the first grinding mechanism 2, the second grinding mechanism 3 comprises a second driving device 31, a second speed reducer 33, a second main shaft 34, a rotary table supporting frame 35 and a grinding roller 39, the second driving device 31 is connected with the second speed reducer 33 through a second coupler 32, the output end of the second speed reducer 33 is connected with one end of the second main shaft 34, and the other end of the second main shaft 34 is connected with the rotary table supporting frame 35. The turntable support frame 35 is fixedly connected with the grinding roller 39, the turntable support frame 35 and the grinding roller 39 can rotate by taking the second main shaft 34 as a rotating shaft, and the grinding roller 39 extends into the grinding disc 25 and is matched with the grinding disc 25 for grinding.
The shell 1 is provided with a first air inlet 14, the first air inlet 14 is connected with a first fan 5, the height of the first air inlet 14 is lower than that of the bottom of the grinding disc 25, and the discharge hole 12 is provided with a screening device 4 capable of screening the particle size of powder. The first fan 5 provides wind power to enable the ground materials in the grinding disc 25 to be discharged from the discharge hole 12 along with the airflow, powder particles with qualified particle sizes can smoothly pass through the screening device 4, and materials with larger particle sizes can be prevented from being fed back into the grinding disc 25 to be continuously ground until the particle sizes meet the requirements. Meanwhile, the particle size screening can be carried out by controlling the air volume of the first fan 5, fine particle powder (lighter material) with smaller particle size can reach the powder concentrator 43 under the carrying of wind power, and coarse particle (heavier material) with larger particle size can not fall to the grinding disc 25 along with the rising of the wind, and is ground again. The two particle size regulation and control modes are combined for use, so that the material screening efficiency is higher, and the controllability of the discharged particle size is stronger.
The casing 1 is provided with a second air inlet 15, the height of the second air inlet 15 is higher than that of the top of the grinding disc 25, the second air inlet 15 is connected with the second fan 6, air flow entering from the second air inlet 15 is mixed with air flow entering from the first air inlet 14, spiral upward swirling air is formed in the casing 1, on one hand, material grinding can be assisted, and on the other hand, material screening can be performed. The air inlet direction of the second air inlet 15 is the same as the tangential direction of the shell 1, the air outlet direction of the second air inlet 15 is opposite to the rotation direction of the grinding disc 25 or the grinding roller 39, and air flow entering from the second air inlet 15 can drive materials to enter between the grinding roller 39 and the grinding disc 25, so that the grinding effect is enhanced.
The material with qualified particle size enters a subsequent cyclone separator from a discharge port 12 for powder collection. The first fan 5 and the second fan 6 are connected with an exhaust gas pipe of the cyclone separator, and hot air is continuously blown into the shell 1 by utilizing the exhaust gas of the cyclone separator, so that the cost is saved by recycling. And the hot air can promote the evaporation of water in the processing process and reduce the water content of the grinding powder.
The grinding disc 25 comprises a grinding ring 251, a base 252 and an air hole 253, wherein the base 252 is provided with a central concave form, which is beneficial to the accumulation of large particle powder in the middle of the grinding disc 25. The air hole 253 penetrates through the base 252, the ground materials are gathered in the middle of the base 252 under the driving of the spiral air flow in the shell 1, and the air force provided by the first fan 5 can pass through the air hole 253 to directly bring the materials on the base 252 to the discharge hole 12. The inner wall of the grinding ring 251 is pressed against the side surface of the grinding roller 39, the rotating directions of the grinding roller 39 and the grinding disc 25 are opposite, and the rotating speeds of the grinding disc 25 and the grinding roller 39 are 50-800 r/min. A large-torque and high-power motor is adopted to connect the grinding roller 39 and the grinding disc 25, the grinding roller 39 and the grinding disc 25 rotate reversely at a high speed, and the wind power movement opposite to the rotation direction of the grinding roller 39 is matched, so that the grinding roller has a powerful crushing effect, a high-speed friction effect, even an accelerating rolling and grinding effect on raw materials, and can grind the materials into superfine powder in a short time.
The screening device 4 comprises a third driving device 41, a third main shaft 42 and a powder concentrator 43, wherein the third driving device 41 is connected with the powder concentrator 43 through the third main shaft 42, the powder concentrator 43 is arranged in the shell 1, and the particle size range of powder screened by the powder concentrator 43 is 80-12000 meshes. Specifically, the powder concentrator 43 is disposed below the discharge port 12 and above the second speed reducer 33, and the air flow in the housing 1 is filtered by the powder concentrator 43 and then discharged from the discharge port 12.
The grinding device further comprises a bearing frame 13, wherein the first driving device 21 and the first speed reducer 23 are vertically fixed on the bearing frame 13, and the first main shaft 24 extends into the shell 1 and is connected with the center of the grinding roller 39. The axes of the first main shaft 24 and the grinding roller 39 coincide with the axis of the second main shaft 34, the second main shaft 34 is connected with the center of the turntable support frame 35, the turntable support frame 35 is horizontally arranged at the bottom of the second main shaft 34, at least two short shafts 36 are uniformly distributed on the periphery of the turntable support frame 35, the turntable support frame 35 is fixedly connected with the grinding roller shaft 37 through the short shafts 36, the grinding roller shaft 37 is distributed perpendicular to the turntable support frame 35 and can rotate around the central axis of the turntable support frame 35 by an angle of 0-360 degrees, the grinding roller shaft 37 is fixedly connected with the grinding roller 39 through a stabilizer bar 38 arranged at the lower part, and the side surface of the grinding roller 39 is abutted against the.
The diameter of grinding disc 25 is 2/3-5/6 of the diameter of housing 1, and is optionally 3/4. If the diameter of the grinding disc 25 is too small, the powder treatment capacity is small; if the diameter of the grinding disc 25 is too large, the grinding disc is easy to contact and rub with the shell 1, and the fault occurs. Therefore, by selecting the value, the sufficient powder processing amount can be ensured on the premise of ensuring the operation safety.
The first driving device 21 and the second driving device 31 are motors, which have simple structure, convenient control and large power range and can meet various operation requirements. The grinding disc 25 and the grinding roller 39 are made of high hardness materials, and one or more than two of steel and ceramics can be selected according to different processing raw materials, and ceramics is selected in the embodiment.
A superfine magnesia powder grinding preparation method applying the grinding preparation device comprises the following steps:
s1, placing the pre-ground magnesia powder into a base 252 of a grinding disc 25 through a feed inlet 11, simultaneously starting a first driving device 21 and a second driving device 31, driving a first coupling 22 and a first speed reducer 23 to operate by the first driving device 21, driving a first main shaft 24 and the grinding disc 25 to rotate clockwise by the first speed reducer 23, wherein the rotating speed is 120 revolutions per minute, and the material flows to a grinding ring 251 on the inner periphery under the action of centrifugal force; the second driving device 31 drives the second coupler 32 and the second speed reducer 33 to operate, the second speed reducer 33 drives the second main shaft 34 and the turntable support 35 to rotate anticlockwise, the turntable support 35 drives the grinding roller 39 to rotate anticlockwise through the short shaft 36, the grinding roller shaft 37 and the stabilizer bar 38, the rotating speed is 120 revolutions per minute, at this time, the side surface of the grinding roller 39 is in close contact with the grinding ring 251 on the grinding disc 25, and magnesium oxide clamped in the middle is ground.
S2, starting the first fan 5 and the second fan 6, enabling hot air to enter the device body from the first air inlet 14 and the second air inlet 15 simultaneously, enabling the air outlet direction of the second air inlet 15 to be clockwise, and forming spiral upward swirling air in the device body to assist grinding of magnesium oxide.
And S3, starting the third driving device 41, and driving the powder concentrator 43 to work through the third main shaft 42. The ground light magnesium oxide powder moves upwards under the drive of wind power, the magnesium oxide fine powder meeting the requirement of the particle size passes through the powder concentrator 43 and reaches the discharge port 12, and then enters a subsequent cyclone separator from the discharge port 12 for powder collection; coarse particles which do not reach the particle size requirement cannot reach the powder concentrator 43, descend into the grinding disc 25 under the action of gravity, and are ground again until the particle size requirement is met.
The particle size of the magnesium oxide powder screened by the powder concentrator 43 is 100-1250 meshes, and the yield is 2-4 tons/h.
Example 2:
the difference from the embodiment 1 is that a method for preparing magnesium hydroxide powder comprises the following steps:
and S1, mixing the light-burned magnesia powder with water to form slurry with the solid mass fraction of 30-70%. Adding slurry into a base 252 of a grinding disc 25 through a feed port 11, simultaneously starting a first driving device 21 and a second driving device 31, driving a first coupling 22 and a first speed reducer 23 to operate by the first driving device 21, and driving a first main shaft 24 and the grinding disc 25 to rotate clockwise by the first speed reducer 23, wherein the rotating speed is 200 revolutions per minute, and the material flows through a grinding ring 251 on the inner periphery under the action of centrifugal force; the second driving device 31 drives the second coupling 32 and the second speed reducer 33 to operate, the second speed reducer 33 drives the grinding roller 39 to rotate counterclockwise, the rotation speed is 200 r/min, at the moment, the side surface of the grinding roller 39 is in close contact with the grinding ring 251 on the grinding disc 25, the slurry clamped in the middle is ground, and meanwhile, the magnesium oxide is promoted to hydrate to form magnesium hydroxide.
S2, starting the first fan 5 and the second fan 6, enabling hot air to enter the device body from the first air inlet 14 and the second air inlet 15 simultaneously, enabling the air outlet direction of the second air inlet 15 to be clockwise, drying the ground magnesium hydroxide, forming spiral upward swirling air in the device body, and carrying the formed magnesium hydroxide powder to move upward.
And S3, starting the third driving device 41, and driving the powder concentrator 43 to work through the third main shaft 42. The magnesium hydroxide fine powder meeting the particle size requirement passes through the powder concentrator 43, reaches the discharge port 12, and then enters a subsequent cyclone separator through the discharge port 12 to be collected; coarse particles which do not reach the particle size requirement cannot reach the powder concentrator 43, descend into the grinding disc 25 under the action of gravity, and are ground again until the particle size requirement is met.
The particle size of the magnesium hydroxide powder screened by the powder concentrator 43 is 1000-12000 meshes, and the yield is 1-3 tons/h. The specific particle size distribution is shown in FIG. 3.
Based on the above, the device has the advantages of simple structure and convenient operation, adopts a large-torque and high-power motor to connect the grinding roller 39 and the grinding disc 25, enables the grinding roller 39 and the grinding disc 25 to rotate reversely at a high speed, is matched with wind power grinding in the direction opposite to the rotation direction of the grinding roller 39, has a strong crushing effect, a high-speed friction effect and even an accelerating grinding and grinding effect on raw materials, can grind the materials into ultrafine powder in a short time, and realizes efficient powder screening.
The above-mentioned embodiments are merely illustrative of the preferred embodiments of the present invention, and do not limit the scope of the present invention, and various modifications and improvements of the technical solution of the present invention by those skilled in the art should fall within the protection scope defined by the claims of the present invention without departing from the spirit of the present invention.
Claims (10)
1. The utility model provides an ultra-fine powder grinds preparation facilities which characterized in that: comprises a shell (1), a first grinding mechanism (2), a second grinding mechanism (3), a screening device (4) and a first fan (5), wherein a feed inlet (11) and a discharge outlet (12) are arranged on the shell (1), the first grinding mechanism (2) is arranged at the bottom of the shell (1), the first grinding mechanism (2) comprises a first driving device (21), a first speed reducer (23), a first main shaft (24) and a grinding disc (25), the first driving device (21) is connected with the first speed reducer (23), the first speed reducer (23) is connected with the first main shaft (24), the first main shaft (24) is connected with the grinding disc (25), the grinding disc (25) is arranged in the shell (1), the grinding disc (25) can rotate by taking the first main shaft (24) as a rotating shaft, the second grinding mechanism (3) is arranged at the top of the first grinding mechanism (2), the second grinding mechanism (3) comprises a second driving device (31), a second speed reducer (33), a second main shaft (34), a rotary table supporting frame (35) and a grinding roller (39), the second driving device (31) is connected with the second speed reducer (33), the second speed reducer (33) is connected with the second main shaft (34), the second main shaft (34) is connected with the rotary table supporting frame (35), the rotary table supporting frame (35) is fixedly connected with the grinding roller (39), the rotary table supporting frame (35) and the grinding roller (39) can rotate by taking the second main shaft (34) as a rotating shaft, the grinding roller (39) extends into the grinding disc (25) and is matched and ground with the grinding disc (25), a first air inlet (14) is formed in the shell (1), and the height of the first air inlet (14) is lower than the bottom height of the grinding disc (25), the first air inlet (14) is connected with the first fan (5), and the discharge hole (12) is provided with a screening device (4) capable of screening the particle size of the powder.
2. The grinding and preparing device of the ultrafine powder according to claim 1, characterized in that: the grinding disc (25) comprises a grinding ring (251), a base (252) and air holes (253), the air holes (253) penetrate through the base (252), the inner wall of the grinding ring (251) is abutted against the side surface of the grinding roller (39), and the rotation directions of the grinding roller (39) and the grinding disc (25) are opposite.
3. The grinding and preparing device of the ultrafine powder according to claim 2, characterized in that: the grinding disc is characterized in that a second air inlet (15) is formed in the shell (1), the height of the second air inlet (15) is higher than the top height of the grinding disc (25), the second air inlet (15) is connected with a second fan (6), and the airflow direction of the second air inlet (15) is tangent to the periphery of the grinding disc (25).
4. The grinding and preparing device of the ultrafine powder according to claim 1, characterized in that: the screening device (4) comprises a third driving device (41), a third main shaft (42) and a powder concentrator (43), the third driving device (41) is connected with the powder concentrator (43) through the third main shaft (42), and the powder concentrator (43) is arranged between the grinding disc (25) and the discharge hole (12).
5. The grinding and preparing device of the ultrafine powder according to claim 1, characterized in that: the grinding table further comprises a bearing frame (13), the first driving device (21) and the first speed reducer (23) are fixed on the bearing frame (13), the first main shaft (24) extends into the shell (1) and is connected with the center of the grinding roller (39), the axis of the first main shaft (24) is overlapped with the axis of the second main shaft (34), the second main shaft (34) is connected with the center of the rotary table supporting frame (35), at least two grinding rollers (39) are uniformly distributed on the periphery of the rotary table supporting frame (35), and the diameter of the grinding disc (25) is 2/3-5/6 of the diameter of the shell (1).
6. The grinding and preparing device of the ultrafine powder according to claim 1, characterized in that: the first driving device (21) and the second driving device (31) are motors, and the grinding disc (25) and the grinding roller (39) are made of steel or ceramic materials.
7. A method for using the apparatus for grinding and preparing ultrafine powder according to any one of claims 1 to 6, comprising: the method comprises the following steps:
s1, feeding the materials into a grinding disc (25) through a feeding hole (11), starting a first driving device (21) and a second driving device (31), wherein the first driving device (21) drives a first speed reducer (23) to work, the first speed reducer (23) drives a first main shaft (24) and the grinding disc (25) to rotate, the second driving device (31) drives a second speed reducer (33) to work, and the second speed reducer (33) drives a second main shaft (34), a rotary table supporting frame (35) and a grinding roller (39) to rotate;
s2, starting the first fan (5) and the second fan (6), and blowing air into the shell (1) from the first air inlet (14) and the second air inlet (15) simultaneously;
and S3, starting the third driving device (41), and driving the powder concentrator (43) to work through the third main shaft (42).
8. The method for grinding and preparing ultrafine powder according to claim 7, wherein the method comprises the following steps: in step S1, the rotating directions of the first main shaft (24) and the second main shaft (34) are opposite, and the rotating speeds of the grinding disc (25) and the grinding roller (39) are both 50-800 r/min.
9. The method for grinding and preparing ultrafine powder according to claim 7, wherein the method comprises the following steps: the discharge port (12) is connected with the cyclone separator, and the first fan (5) and the second fan (6) are connected with an exhaust gas pipe of the cyclone separator.
10. The method for grinding and preparing ultrafine powder according to claim 7, wherein the method comprises the following steps: the particle size range of the powder screened by the powder selector (43) is 80-12000 meshes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011474642.7A CN112604777A (en) | 2020-12-14 | 2020-12-14 | Superfine powder grinding preparation device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011474642.7A CN112604777A (en) | 2020-12-14 | 2020-12-14 | Superfine powder grinding preparation device and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112604777A true CN112604777A (en) | 2021-04-06 |
Family
ID=75234072
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011474642.7A Pending CN112604777A (en) | 2020-12-14 | 2020-12-14 | Superfine powder grinding preparation device and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112604777A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113510244A (en) * | 2021-04-28 | 2021-10-19 | 湖南新威凌金属新材料科技股份有限公司 | Method and device for producing flaky metal pigment |
| CN114260063A (en) * | 2021-11-26 | 2022-04-01 | 安徽一作农业发展有限公司 | Stepless fine grinding device for deep processing of Chinese wolfberry powder and use method thereof |
| CN114749243A (en) * | 2022-04-19 | 2022-07-15 | 湖州南浔兴云建材有限公司 | Blast furnace slag vertical mill grinding device and process thereof |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202387518U (en) * | 2011-12-19 | 2012-08-22 | 陕西斯达实业有限公司 | Large vertical roller mill for ultrafine milling |
| CN202962567U (en) * | 2012-12-04 | 2013-06-05 | 王今奇 | Multilayer vertical miller |
| CN204892002U (en) * | 2015-07-28 | 2015-12-23 | 河南金宜福机械设备有限公司 | Flour mill |
| WO2017143543A1 (en) * | 2016-02-24 | 2017-08-31 | 马骏 | Novel coal grinding device for thermal power system of power plant |
| CN208771541U (en) * | 2018-05-22 | 2019-04-23 | 南京威普粉体工程有限公司 | A kind of grinding roller bull ring dual AC power grinding superfine powder flour mill |
| CN209109277U (en) * | 2018-10-26 | 2019-07-16 | 南京中材粉体工程科技有限公司 | A kind of pre-separation bypass wind roller type vertical mill |
| CN110860342A (en) * | 2019-11-15 | 2020-03-06 | 南京钜力智能制造技术研究院有限公司 | External circulation roller type vertical mill |
| CN210358068U (en) * | 2019-05-10 | 2020-04-21 | 江苏吉达机械制造有限公司 | Powder concentrator |
| CN211051620U (en) * | 2019-10-11 | 2020-07-21 | 常熟市宏宇钙化物有限公司 | Multi-effect grinding Raymond mill |
| CN211385344U (en) * | 2019-12-18 | 2020-09-01 | 广州市立德环保科技有限公司 | Powder grinding device of vertical paint pulverizer |
| CN214320361U (en) * | 2020-12-14 | 2021-10-01 | 辽宁荣邦科技有限公司 | Superfine powder grinding preparation device |
-
2020
- 2020-12-14 CN CN202011474642.7A patent/CN112604777A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202387518U (en) * | 2011-12-19 | 2012-08-22 | 陕西斯达实业有限公司 | Large vertical roller mill for ultrafine milling |
| CN202962567U (en) * | 2012-12-04 | 2013-06-05 | 王今奇 | Multilayer vertical miller |
| CN204892002U (en) * | 2015-07-28 | 2015-12-23 | 河南金宜福机械设备有限公司 | Flour mill |
| WO2017143543A1 (en) * | 2016-02-24 | 2017-08-31 | 马骏 | Novel coal grinding device for thermal power system of power plant |
| CN208771541U (en) * | 2018-05-22 | 2019-04-23 | 南京威普粉体工程有限公司 | A kind of grinding roller bull ring dual AC power grinding superfine powder flour mill |
| CN209109277U (en) * | 2018-10-26 | 2019-07-16 | 南京中材粉体工程科技有限公司 | A kind of pre-separation bypass wind roller type vertical mill |
| CN210358068U (en) * | 2019-05-10 | 2020-04-21 | 江苏吉达机械制造有限公司 | Powder concentrator |
| CN211051620U (en) * | 2019-10-11 | 2020-07-21 | 常熟市宏宇钙化物有限公司 | Multi-effect grinding Raymond mill |
| CN110860342A (en) * | 2019-11-15 | 2020-03-06 | 南京钜力智能制造技术研究院有限公司 | External circulation roller type vertical mill |
| CN211385344U (en) * | 2019-12-18 | 2020-09-01 | 广州市立德环保科技有限公司 | Powder grinding device of vertical paint pulverizer |
| CN214320361U (en) * | 2020-12-14 | 2021-10-01 | 辽宁荣邦科技有限公司 | Superfine powder grinding preparation device |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113510244A (en) * | 2021-04-28 | 2021-10-19 | 湖南新威凌金属新材料科技股份有限公司 | Method and device for producing flaky metal pigment |
| CN113510244B (en) * | 2021-04-28 | 2022-06-28 | 湖南新威凌金属新材料科技股份有限公司 | Method and device for producing flaky metal pigment |
| CN114260063A (en) * | 2021-11-26 | 2022-04-01 | 安徽一作农业发展有限公司 | Stepless fine grinding device for deep processing of Chinese wolfberry powder and use method thereof |
| CN114749243A (en) * | 2022-04-19 | 2022-07-15 | 湖州南浔兴云建材有限公司 | Blast furnace slag vertical mill grinding device and process thereof |
| CN114749243B (en) * | 2022-04-19 | 2023-12-22 | 湖州南浔兴云建材有限公司 | Blast furnace slag vertical mill grinding device and process thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN214320361U (en) | Superfine powder grinding preparation device | |
| CN112604777A (en) | Superfine powder grinding preparation device and method | |
| CN206356113U (en) | A kind of Chemical Manufacture material high-efficiency circular grinding equipment | |
| CN203291915U (en) | Ultrafine powder differential swing arm roller grinding machine | |
| CN206082697U (en) | Horizontal stirring mill suitable for mining production | |
| CN207951609U (en) | Vertical roll grinder | |
| CN202137015U (en) | Open-circuit finish grinding equipment | |
| CN112958256A (en) | Cement clinker grinding equipment and process | |
| JPS6224134B2 (en) | ||
| CN2673505Y (en) | High speed rotating grinding drying machine | |
| CN202336373U (en) | Micro powder preparing system | |
| CN215963896U (en) | Raymond mill feeding adjusting device | |
| CN202336368U (en) | Superfine grinder with slag remover | |
| CN202336374U (en) | Ultrafine smashing machine | |
| CN202336372U (en) | Uniform-granularity micro-powder preparation system | |
| CN102380447A (en) | Superfine crushing machine | |
| CN208975938U (en) | A kind of ball-milling device | |
| CN100414233C (en) | Rotary grinding flash drier | |
| CN209093565U (en) | A kind of fine grinding processing unit for diamond particles grinding | |
| CN103182339A (en) | Special drying type cone-cavity mill for producing powder from construction wastes | |
| CN202377037U (en) | Classification grinder | |
| CN205462666U (en) | Pulverizing mill pay -off and unloading subassembly are cut to roller | |
| CN205462667U (en) | Pulverizing mill pay -off and unloading subassembly are cut to roller | |
| CN205462438U (en) | Pulverizing mill feeding system that can automatic unloading | |
| CN205462437U (en) | Pulverizing mill feeding system that can automatic unloading |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |