CN1044419A - The continuous micron mill of a kind of high yield of micropowder grinding technology and this technology of enforcement - Google Patents
The continuous micron mill of a kind of high yield of micropowder grinding technology and this technology of enforcement Download PDFInfo
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- CN1044419A CN1044419A CN89109354A CN89109354A CN1044419A CN 1044419 A CN1044419 A CN 1044419A CN 89109354 A CN89109354 A CN 89109354A CN 89109354 A CN89109354 A CN 89109354A CN 1044419 A CN1044419 A CN 1044419A
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- mill
- storehouse
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C17/00—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls
- B02C17/04—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls with unperforated container
- B02C17/06—Disintegrating by tumbling mills, i.e. mills having a container charged with the material to be disintegrated with or without special disintegrating members such as pebbles or balls with unperforated container with several compartments
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Abstract
A kind of continuous micron mill that is used for granular material is made up of the rotating cylinder of a big L/D ratio, and this rotating cylinder is divided into several mill storehouses, and wherein the size of the mill amboceptor of Fang Zhiing reduces gradually, and shot-like particle and mill Jie's ratio is also inequality.
Description
The present invention relates to a kind of high yield tubular type micron mill of continuous periodic duty.
The dry type or the wet type grinding that reduce solid granulates shape product size are in production low-cost, high yield, particularly in mining industry and the building industry and the production of expensive, low-yield, in particularly fine chemistry industry, pharmaceuticals industry and the cosmetics industry, one of the most universal production operation.
Above-mentioned back one class industry can be born to obtaining granularity less than 10 microns superfine product required high-energy and high processing cost, yet, under the low situation of workinprocess cost, just can not bear.
On commercial scale, per hour being equal to or greater than, 10 tonnes high yield grinding is to carry out in the tube mill that partial stowage's mill is situated between.This mill is situated between and is made up of impact-resistant, regular solid, and this solid generally is a Metal Ball, but also can be other shapes and kind, as metal cylinder or metal bar, or the stone of rule.
As everyone knows, when the tube mill rotating speed reached certain value, mill was situated between and begins to be subjected to action of centrifugal force.This certain rotating speed is called critical speed, is formulated as:
In the formula, W is the revolutions per minute (r.p.m) of tube mill, and D is the internal diameter (unit: rice) of tube mill.When the rotating speed of tube mill is the about 85% time of its critical speed, the effectiveness maximum that mill is situated between.
The comminution ratio of such grinding machine can surpass 100, but when pulverizer (being reducing of particle size) when being about 25-30, grinding machine most effective.
In general, the high-yield tube grinder of circulation can be produced the abrasive product of particle size distribution between the 0-64 micron continuously, but thinner finished product can not be provided.Thinner if desired product then must use different flour mills, as microballoon grinding machine, compressed air micron mill.Such flour mill output extremely low (being not more than 1000 kilograms/hour) and energy consumption is high, need generally to be used to Size Distribution at the 0-20 micron is sometimes in the production of the ultra micro granularity material of 0-10 micron, in the production as dyestuff, agricultural chemicals and ink.
The present invention adopts a kind of dry type or wet type continuous powder milling technology, and the above-mentioned limitation of known equipment is overcome.This dry type or wet lapping technology can be at the specific yield height, produce particle size under the low situation of energy consumption less than 20 microns abrasive product.
Micron mill of the present invention is made up of a multi-compartment tube grinding machine, 1 is illustrated with reference to the accompanying drawings.Fig. 1 has shown a typical example of the present invention, as a non-limiting example.
This embodiment relates to the grinding of coal, its purpose be to obtain granularity be suitable for being used in can be directly as the coal dust in stable, the high-concentration suspension liquid of industrial burner fuel.
Be the rotational circle tubular according to micron mill of the present invention, this rotating cylinder 1 has big L/D ratio, and ratio is 5 at least, and preferably 6 or bigger.The internal capacity of rotating cylinder is divided into several cylindric mill storehouses 3 by partition panel 2, places mill and be situated between in the mill storehouse.Grind the storehouse from the feed mill storehouse to discharge, the size that mill is situated between reduces gradually.The detail shape of partition panel 2 is seen accompanying drawing 2.By the magazine charging of known band feeding screw 5, the rotating speed of this feeding screw decision thruput.
The metal mill of packing in the inside in garden tubular mill storehouse 3 is situated between, as the steel ball rod iron.
To the tail storehouse of discharging micro mist shape product, the size that mill wherein is situated between reduces gradually from the first storehouse of charging.According to the present invention, it is found that when in each mill storehouse, the size of the mill amboceptor of particularly placing is incomplete same but when having certain size to distribute, can obtain best mill efficiency in first storehouse.Because can make the possible collision frequency between abrasive product and the mill Jie reach maximum like this, and the unit kinetic energy that has at least part mill to be situated between is enough to the particle of size maximum is clayed into power.
The Size Distribution that mill is situated between must be relevant with the particle size of charging.The liner plate 6 of trough of belt is housed on the barrel in mill storehouse 3; it not only provides necessary protection to barrel; but also mixed, the reach of grind materials are treated in decision; the mill amboceptor is rotated and rise to the certain height directly related with rotating speed along the wall of trough of belt; fall on the stratum granulosum along a parabolic path then; circulation just makes material obtain grinding so repeatedly.
According to the embodiment of a recommendation of the present invention, rotating cylinder 1 is divided into three cylindric mill storehouses 3, and wherein, middle mill storehouse is longer than two other greatly.
The effect in the first mill storehouse is the size that reduces that part of particle the thickest in the charging, and the major part of grinding operation is carried out in spacious middle mill storehouse, and grinding is then finished in the tail storehouse.
The micro mist product is discharged tubular tail storehouse by the blade of partition panel, is carried in known manner by magazine 7 and goes to store.One of essential part of micron mill of the present invention is a partition panel, and this partition panel both played bulkhead between different mill storehouses, plays product charge level controller again, sees Fig. 2 A and B.
Partition panel is made up of an outer ring 11 and two flat circular sector wallboards 12 and 13 in front.Wherein, outer ring 11 is used for partition panel is fixed to the tubulose barrel, and wallboard 12 and 13 is in the face of adjacent mill storehouse 3, and material is sent between these two wallboards from left to right.
In the wallboard 12 in mill storehouse, upper reaches, there is being annular to comb in close central circular zone and stitching 14, at the seam of then combing near peripheral border circular areas.At the center of partition panel, be provided with a tubaeform member 15, the shape such as the truncated cone, its handle face is towards dirty mill storehouse.In the wallboard 13 in dirty mill storehouse, a center hole is arranged, this hole and the truncated cone 15 coaxial lines are discharged for material.
In the disc space that limits by wallboard 12 and 13, except that the truncated cone 15, also be provided with a series of blades 16.These blades are used for transmitting material between each mill storehouse.According to grinding machine of the present invention, its course of work is basic identical for dry mill process and wet-grinding technology and relative device, and in wet-grinding technology and relative device, solid material is present among the liquid phase with the high-concentration suspension state.
When grinding machine rotates, having forwarded annular in the circular sector part of the low level seam 14 of combing to allows muddy liquid (under the wet-milling situation) or powder (under the dry grinding situation) to pass through, enter by wallboard 12 and 13 and annular element is 11 that surround, the partition panel female parts of blade 16 is wherein arranged from upper reaches Mo Cang, and be accumulated by the direction shown in the arrow at this.The fan-shaped part that contains the turbid liquid that accumulates in this female parts or solid-state powder continues when low level turns to a high position, the turbid liquid or the solid-state powder that are blocked by blade 16 just drop on the truncated cone 15 in the effect of gravity, and the center hole by wallboard 13 enters the dirty mill storehouse that is arranged in Fig. 2 B right side.The truncated cone 15 also can be the butt positive tetrahedron that the regular polygon bottom surface is arranged.
In this respect, should be noted in the discussion above that the needed thruput of grinding machine is usually much smaller than the conveying capacity of blade 16 if the circular sector zone separates each other fully.
By changing the thruput that series of parameters can change grinding machine.These parameters mainly are: number, size and the position of the seam 14 of combing, and particularly wallboard 12 periphery places do not have the width of the seam part of combing; The number of blade 16, shape, size and they are with respect to the conveying capacity of the radial position in bypass slit and the blade that obtains thus.
In an embodiment who selects the superior of the present invention, the tail storehouse of micron mill is to separate by partition panel and the discharge gate that wallboard 12 is housed.Wherein, the nothing of wallboard 12 peripheries is combed the width in seam zone significantly less than the comb width in seam district of the nothing of the wallboard 12 of other partition panel, like this, the charge level of abrasive product is just low, and all surrounded, make the effect of grinding the sieve that has been situated between, prevent the discharge of the particle beyond size range by mill Jie.
For advantage of the present invention is described, some carry out the wet-milling test of coal on the exemplary micron mill of making according to the present invention situation is described below.
Example 1
Treat that grind materials is a coal, during grinding, dry coal and water are with the separately feeding of about 1: 1 weight ratio.
Effective internal diameter in the mill storehouse 3 of exemplary grinding machine (promptly add liner plate after clean internal diameter) is 550 millimeters, effectively total length (i.e. length except that partition panel) is 3300 millimeters, first storehouse that is divided into 760 millimeters long, second storehouse of 1780 millimeters long and the 3rd storehouse of 760 millimeters long.
The shape of partition panel has following feature shown in Fig. 2 A and B:
First partition panel:
By the ratio 3% of area with the gross area
Comb and stitch 8 millimeters of width
There are not 86 millimeters of the seam of comb circle width
Lobe numbers 4, C shape
Second partition panel:
By the ratio 2% of area with the gross area
Comb and stitch 5 millimeters of width
There are not 86 millimeters of the seam of comb circle width
Lobe numbers 4, C shape
The 3rd partition panel (discharge partition panel):
By the ratio 2.9% of area with the gross area
Comb and stitch 5 millimeters of width
There are not 69 millimeters of the seam of comb circle width
Lobe numbers 4, C shape
Rotating speed: 37 rev/mins, equal 65% of critical speed.
Mill Jie specification is as follows:
The first mill storehouse: steel ball, distribution of weight is as follows:
Diameter is 30 millimeters persons 13%
Diameter is 25 millimeters persons 25%
Diameter is 20 millimeters persons 25%
Diameter is 15 millimeters persons 37%
The second mill storehouse: steel ball, distribution of weight is as follows:
Diameter is 15 millimeters persons 24%
Diameter is 10 millimeters persons 76%
The 3rd mill storehouse: the rod iron of the steel ball that diameter is 8 millimeters or 8 * 8 millimeters.
Pack completeness in the mill storehouse remains on following level:
Mill Jie product material
The first mill storehouse: 36% 29%
The second mill storehouse: 36% 35%
The 3rd mill storehouse: 34% 28%
The performance that is obtained is as follows:
Feed coal granularity 0-6 millimeter
Association index (Bond Index) 0-6 millimeter
53 kilograms/hour of dry basic throughputs
Finished product maximum particle size＜20 micron
100 kilowatt-hours of/ton dry bases of power consumption
Example 2
Make the thinner coal micronizing of granularity that feeds with the suspension form with same grinding machine.
Remove first partition panel, mill be situated between with pack completeness with second the same with the 3rd storehouse in the precedent.
The performance that is obtained is as follows:
Feed coal granularity 0-350 micron
21 kilowatt-hours/ton of association indexs
Feeding capacity contains for 110 kilograms/hour
49%(weight) drying
The muddy liquid of base
Wear into product maximum particle size＜20 micron
65 kilowatt-hours of/ton dry bases of power consumption
37 rev/mins of rotating speeds equal
65% of critical speed
In addition, on another demonstration grinding machine, carried out of the test of definite L/D ratio to the influence that grinds product by the effective length that reduces grinding machine.In test, dry material and moisture separately feed.
Example 3
L
Total length/ D=4 L
Total length/ D=6
600 millimeters 600 millimeters of internal diameters
2400 millimeters 3600 millimeters of effective lengths
Mill storehouse several 22
560 millimeters 830 millimeters of the first mill storehouse effective lengths
First grinds the storehouse mill is situated between identical with first mill storehouse mill Jie in the example 1
840 millimeters 2770 millimeters of the second mill storehouse effective lengths
Second grinds the storehouse mill is situated between identical with second mill storehouse mill Jie in the example 1
Feed coal
Granularity 0-6 millimeter 0-6 millimeter
Association index (kilowatt-hour/ton) 21 21
Throughput, dry base (kilogram/hour) 20.8 39
Finished product full-size＜20 micron＜20 microns
Energy consumption (kilowatt-hour/ton) 225 180
Specific yield (kilogram/rice
3Hour) 30.8 38.3
Rotating speed (rev/min) 35.5 35.5
Example 4
L
Total length/ D=4 L
Total length/ D=6
600 millimeters 600 millimeters of internal diameters
2400 millimeters 3600 millimeters of effective lengths
Mill storehouse several 33
560 millimeters 830 millimeters of the first mill storehouse effective lengths
1280 millimeters 1940 millimeters of the second mill storehouse effective lengths
560 millimeters 830 millimeters of the 3rd mill storehouse effective lengths
Mill is situated between with example 1 with example 1
Pack completeness with example 1 with example 1
Feed coal
Granularity 0-6 millimeter 0-6 millimeter
Association index (kilowatt
Hour/ton) 21 21
Throughput, dry base (public affairs
Jin/hour) 27 65
Finished product maximum particle size＜20 micron＜20 microns
Energy consumption (kilowatt-hour/ton)
Dry base 160 100
Specific yield (kilogram/rice
3
Hour) 39.8 64
Rotating speed (rev/min) 35.5 35.5
From example 3 and example 4 as can be seen, increase length and can make the output of fine granularity (＜20 microns) finished product that surprising increase is arranged, this increase is considerably beyond the increase of corresponding dischargeable capacity.
Along with the mill that grinds the storehouse number adds, specific energy consumption also significantly reduces.
When carrying out these tests, find that also in the process of production maximum particle size less than 20 microns micro mist material, when rotating speed was in the 60-67% of critical speed scope, energy efficiency was the highest.Velocity interval during test is the 40-80% of critical speed.
In actual production, both can be used for wet-milling according to micron mill of the present invention, also can be used for dry grinding.Fig. 3 represents a wet-milling process figure.Particulate coal is sent into mixing arrangement 21 by conveyer belt 20, and pump 22 and pipeline 23 are sent water in suspension into this mixing arrangement 21.Then, resulting suspension is fed micron mill 1 of the present invention.Suspension is discharged by discharge device 24.This discharge device has the rotational structure of tape punching wall 25.Perforated wall 25 can pass through the micro powder article pulp suspension, and discharges through pipeline 26, and other any Jie by the mill under partition panel 2 sieves all discharges from the perforated wall end, is collected and is transported by the cycle by magazine 27.
The energy that is consumed in the grinding process rises the temperature of aqueous suspension, and produces certain steam.The delivery flow of steam and the temperature of material suspended liquid are by control valve 28 controls.Control valve 28 is connected between steam discharge fan 29 and the discharge device 24.
Fig. 4 represents a dry type micropowder grinding process chart that combines with cyclone classifier.The coarse-grained material of granular charging and recirculation feeds charging magazine 31 together, and is inhaled into micron mill 1 of the present invention under swabbing action.Keep vacuum state in the grinding machine 1, if desired, then remain under a certain controlled atmosphere.This controlled atmosphere generally is used for such occasion, treat that promptly grind materials (as coal) can produce dust or volatile substances, and these dust or volatile substances is dangerous under the situation that has air to exist.This atmosphere can be made of air and the noble gas mixtures that the one-tenth that is in outside the explosive boundary is grouped into.
Because swabbing action, the micro mist product by fluidisation, enters first cyclone classifier 33 by pipeline 32 at the discharge place.This clasfficiator is isolated coarse component, and this part material returns magazine 31 by pipeline 34 recirculation.Fine fraction still keeps the fluidisation state, and enters the higher second level cyclone classifier of efficient by pipeline 35, and this clasfficiator is isolated fine.Carry fluid to leave the top of cyclone classifier, magazine 31 is returned in 37 recirculation by sucktion fan.Blower fan 37 has compensated the pressure drop that produces in whole loops and the pipeline 38.
Make the part of the fluidised gas of material, after in the end Sheng Xia dust is removed by filter 40, enter atmosphere by pipeline 39.The grinding finished product is discharged by pipeline 41.Make the fluidised conveying gas of material must discharge a part, so that its component is remained in the safe limit, because a certain amount of extraneous air is inevitable from drawing-in device and the infiltration of rotation joint portion.Air and inert gas are respectively by pipeline 41 and 42 inputs.
Under vacuum state, carry out grinding processing.Can prevent that dust from escaping into atmosphere.In order further to emphasize the advantage of the present invention in actual production, provide structure and the technological parameter of wet type coal micron mill when processing spheroidizing bone coal and petroleum coke below by the flow process of Fig. 3 by the present invention's design.
Charging
Coal fossil coal stone oil coke
Feed rate
(ton/hour dry) 20 20
Water content (percentage by weight %) 5-10 6-11
Density (kilogram/decimetre
3) 1.35 1.4
Grindability
The H.G.I(stiffness) 52 55
Association index (kilowatt-hour/ton) 21 n.d
The two equates size distribution
Residue accounts for whole materials on screen size (millimeter) sieve
Percentage by weight
2 average 1 maximums 5
1.5 average 5 maximums 14
1 average 15 maximums 34
0.7 average 30 maximums 45
0.5 average 45 maximums 56
0.35 average 60 maximums 65
0.25 average 73 maximums 75
Average 0.6 maximum 0.65 of average diameter (millimeter)
The fluid (added water) that injects
Flow (ton/hour) 22.7
Temperature (℃) 20-24
PH value 9-10
The fluid of discharging
The suspension flow (ton/hour) 42.1
The gas flow (ton/hour) 1.7
Temperature (℃) 69
Weight percent concentration 49-50
Viscosity (CP) 80-180
PH value 7
The solid 99.5% that suspends is complete by 20 microns
Portion is by 32 microns
The grinding machine feature
Add 3.1 meters of clean internal diameters behind the liner plate
19.0 meters of cylindrical shell total lengths
4.0 meters of the first mill storehouse effective lengths
9.5 meters of the second mill storehouse effective lengths
4.3 meters of the 3rd mill storehouse effective lengths
Mill is situated between
51 tons in the first mill storehouse
119 tons in the second mill storehouse
50 tons in the 3rd mill storehouse
Type, distribution and pack completeness are with example 1
Be equipped with 2700 kilowatts of power
Partition panel
500 millimeters of the first and second partition panel gross thickness
250 millimeters of the 3rd partition panel gross thickness
The number 14 of blade and sector region
Comb the seam width with example 1
Comb and stitch the gross area
0.252 meter in the first mill storehouse
2
0.154 meter in the second mill storehouse
2
0.232 meter in the 3rd mill storehouse
2
Running parameter:
Holdup time (branch) 36
Rotating speed (rev/min) 15.5
Percentage (%) 65 to critical speed
Absorbed power (kilowatt) 2200
Energy consumption (kilowatt-hour/ton dry base) 110
Claims (9)
1, a kind of continuous micron mill of high yield that is used for granular material dry type or wet type micropowder grinding, has a rotating cylinder, this rotating cylinder is divided into several mill storehouses, placing the mill of being made up of the hard objects of regular shape in the mill storehouse is situated between, it is characterized in that, the draw ratio of rotating cylinder is 5 at least, preferably 6 or bigger, in described mill storehouse, the average-size that the mill of being placed is situated between is ground the storehouse and is reduced gradually from the feed mill storehouse to discharging, described mill storehouse is separated from each other by partition panel, partition panel is made up of two horizontal wallboards with holes and transmission blade, and this blade moves material within partition panel, and one of the upper reaches wallboard is arranged in middle border circular areas the seam of comb is arranged, dirty wallboard has a centre bore, this Kong Yuyi tubaeform component coaxial line that links to each other with two wallboards.
According to a kind of continuous micron mill of high yield that is used for granular material dry type or wet type micropowder grinding of claim 1, it is characterized in that 2, mill storehouse number is 3, the volume maximum in wherein middle mill storehouse.
According to a kind of continuous micron mill of high yield that is used for granular material dry type or wet type micropowder grinding of claim 1, it is characterized in that 3, mill Jie who is placed in one or more mill storehouses is to be mixed by the different abrasive body of size.
4, according to a kind of continuous micron mill of high yield that is used for granular material dry type or wet type micropowder grinding of claim 1, it is characterized in that, the comb width in seam zone of the nothing along circumferential distribution of the partition panel that tail storehouse and exhaust end are separated is less, like this, ground low in storehouse by the charge level of mill solid material than other upper reaches in this storehouse.
5, a kind ofly use above-mentioned one or described micron mill of above claim that granular material is carried out the method for continuous micropowder grinding, it is characterized in that, the rotating speed of micron mill this machine critical speed 60% to 67% between.
6, a place uses in the claim 1 to 4 one or described micron mill of above claim granular material to be carried out the method for continuous micropowder grinding, it is characterized in that, micropowder grinding carries out under vacuum state, and material is liquid phase and classification in a series of cyclone separators behind the mill of discharge.
7, a kind of method as claimed in claim 6 is characterized in that raw granulate fraction recycles back micron mill.
8, a kind of method of using in the claim 1 to 4 one or described micron mill of above claim granular material to be carried out continuous micropowder grinding, it is characterized in that, by shape that changes blade in the partition panel and/or the thruput that the position changes micron mill.
9, a kind ofly use in the claim 1 to 4 one or described micron mill of above claim that shot-like particle is carried out the method for continuous micropowder grinding, it is characterized in that, in the tail rolls storehouse, mill is situated between and the ratio of the grinding charge material mill storehouse less than the front.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT8822989A IT1228049B (en) | 1988-12-16 | 1988-12-16 | GRINDING PROCEDURE AND CONTINUOUS HIGH CAPACITY MICRONIZER MILL FOR ITS REALIZATION |
| IT22989A/88 | 1988-12-16 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1044419A true CN1044419A (en) | 1990-08-08 |
| CN1025292C CN1025292C (en) | 1994-07-06 |
Family
ID=11202613
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN89109354A Expired - Fee Related CN1025292C (en) | 1988-12-16 | 1989-12-16 | Grinding process and continuous high-capacity micronizing mill for its implementation |
Country Status (6)
| Country | Link |
|---|---|
| CN (1) | CN1025292C (en) |
| AU (1) | AU619369B2 (en) |
| DE (2) | DE3940906A1 (en) |
| GB (1) | GB2229940B (en) |
| IT (1) | IT1228049B (en) |
| SU (1) | SU1776199A3 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102002266A (en) * | 2010-10-28 | 2011-04-06 | 长沙族兴金属颜料有限公司 | Preparation method of silver dollar-shaped aluminum pigment |
| CN102002267A (en) * | 2010-08-25 | 2011-04-06 | 长沙奥特金属颜料有限公司 | Method for preparing high-whiteness highly-metallic fine and white aluminum paste |
| CN106238155A (en) * | 2016-08-21 | 2016-12-21 | 横店集团东磁股份有限公司 | A kind of material breaking mixing apparatus |
| CN107032131A (en) * | 2017-05-19 | 2017-08-11 | 中国恩菲工程技术有限公司 | Monazite processing/transfer system |
| CN107952528A (en) * | 2017-12-18 | 2018-04-24 | 洛阳中伟环保科技有限公司 | Intelligent two phase flow tube mill |
| CN113102044A (en) * | 2021-05-10 | 2021-07-13 | 江苏金木土科技有限公司 | High-performance concrete admixture grinding device and grinding method |
| CN113814039A (en) * | 2021-09-30 | 2021-12-21 | 广西蒙娜丽莎新材料有限公司 | Continuous ball milling system for standardized processing of building ceramic raw materials |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1992006725A1 (en) * | 1990-10-12 | 1992-04-30 | Habley Medical Technology Corporation | Disposal module with sleeve for prefilled cartridges |
| CN105381841A (en) * | 2015-11-25 | 2016-03-09 | 重庆帅昌机械制造有限公司 | Stagewise type ball mill |
| RU193347U1 (en) * | 2019-07-03 | 2019-10-24 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Ивановский государственный химико-технологический университет" | Ball mill |
| IT202200026127A1 (en) * | 2022-12-20 | 2024-06-20 | Certech S P A Con Socio Unico | air injection in continuous mill |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB278214A (en) * | 1926-12-06 | 1927-10-06 | Traylor Engineering And Mfg Co | Improvements in and relating to ball mills |
| DE1285277B (en) * | 1965-04-15 | 1968-12-12 | Basf Ag | Process and device for the continuous wet grinding of solids in tubular mills |
| DE2207484C3 (en) * | 1971-02-18 | 1988-07-07 | Slegten, Pierre, Brüssel/Bruxelles | Partition in a ball tube mill |
| US4498634A (en) * | 1983-09-01 | 1985-02-12 | Fuller Company | Division head for grinding mill |
-
1988
- 1988-12-16 IT IT8822989A patent/IT1228049B/en active
-
1989
- 1989-12-11 GB GB8927959A patent/GB2229940B/en not_active Expired - Fee Related
- 1989-12-11 DE DE3940906A patent/DE3940906A1/en not_active Ceased
- 1989-12-13 DE DE8914652U patent/DE8914652U1/en not_active Expired - Lifetime
- 1989-12-15 AU AU46840/89A patent/AU619369B2/en not_active Ceased
- 1989-12-15 SU SU4742694A patent/SU1776199A3/en active
- 1989-12-16 CN CN89109354A patent/CN1025292C/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102002267A (en) * | 2010-08-25 | 2011-04-06 | 长沙奥特金属颜料有限公司 | Method for preparing high-whiteness highly-metallic fine and white aluminum paste |
| CN102002267B (en) * | 2010-08-25 | 2013-02-06 | 长沙奥特金属颜料有限公司 | Method for preparing high-whiteness highly-metallic fine and white aluminum paste |
| CN102002266A (en) * | 2010-10-28 | 2011-04-06 | 长沙族兴金属颜料有限公司 | Preparation method of silver dollar-shaped aluminum pigment |
| CN102002266B (en) * | 2010-10-28 | 2013-03-13 | 长沙族兴新材料股份有限公司 | Preparation method of silver dollar-shaped aluminum pigment |
| CN106238155A (en) * | 2016-08-21 | 2016-12-21 | 横店集团东磁股份有限公司 | A kind of material breaking mixing apparatus |
| CN106238155B (en) * | 2016-08-21 | 2018-06-08 | 横店集团东磁股份有限公司 | A kind of material breaking mixing apparatus |
| CN107032131A (en) * | 2017-05-19 | 2017-08-11 | 中国恩菲工程技术有限公司 | Monazite processing/transfer system |
| CN107952528A (en) * | 2017-12-18 | 2018-04-24 | 洛阳中伟环保科技有限公司 | Intelligent two phase flow tube mill |
| CN113102044A (en) * | 2021-05-10 | 2021-07-13 | 江苏金木土科技有限公司 | High-performance concrete admixture grinding device and grinding method |
| CN113814039A (en) * | 2021-09-30 | 2021-12-21 | 广西蒙娜丽莎新材料有限公司 | Continuous ball milling system for standardized processing of building ceramic raw materials |
Also Published As
| Publication number | Publication date |
|---|---|
| SU1776199A3 (en) | 1992-11-15 |
| GB8927959D0 (en) | 1990-02-14 |
| GB2229940B (en) | 1992-10-21 |
| DE3940906A1 (en) | 1990-06-21 |
| IT1228049B (en) | 1991-05-27 |
| DE8914652U1 (en) | 1990-03-22 |
| AU619369B2 (en) | 1992-01-23 |
| GB2229940A (en) | 1990-10-10 |
| IT8822989A0 (en) | 1988-12-16 |
| AU4684089A (en) | 1990-06-21 |
| CN1025292C (en) | 1994-07-06 |
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