Jet Mill
20230415165 ยท 2023-12-28
Inventors
Cpc classification
B02C19/0043
PERFORMING OPERATIONS; TRANSPORTING
B02C2210/01
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
The invention relates to a jet mill comprising a milling chamber with a longitudinal axis, an inlet at one end of the axis and an outlet at the opposite end of the axis, the milling chamber comprising a multitude of pins arranged in the free flow cross-section of the milling chamber, wherein the pins are arranged in at least two planes perpendicular to the longitudinal axis, the planes being distant to each other in the longitudinal direction, and the pins of one plane being laterally offset to the pins of the subsequent plane, wherein the milling chamber is divided into alternate pin segments and acceleration segments, the pin segments each having at least two planes of pins, and the acceleration segments having no pins.
Claims
1. A jet mill comprising a milling chamber with a longitudinal axis, an inlet at one end of the axis and an outlet at the opposite end of the axis, the milling chamber comprising a multitude of pins arranged in the free flow cross-section of the milling chamber, wherein the pins are arranged in at least two planes perpendicular to the longitudinal axis, the planes being distant to each other in the longitudinal direction, and the pins of one plane being laterally offset to the pins of the subsequent plane, wherein the milling chamber is divided into alternate pin segments and acceleration segments, the pin segments each having at least two planes of pins, and the acceleration segments having no pins.
2. The jet mill according to claim 1, wherein the surface of the pins facing the inlet is convex.
3. The jet mill according to claim 1, wherein the pins are removably attached inside the milling chamber.
4. The jet mill according to claim 1, wherein at least some of the pins comprise a sensor capable of detecting a measure for abrasion of the respective pin.
5. The jet mill according to claim 1, wherein the pin segments each have two to five planes of pins.
6. The jet mill according to claim 1, wherein the length of the acceleration segments is larger than the longitudinal distance between planes in the pin segments.
7. The jet mill according to claim 1, wherein an acceleration chamber with an inlet and an outlet is connected to the milling chamber, the outlet of the acceleration chamber being the inlet of the milling chamber.
8. The jet mill according to claim 7, wherein the inlet of the acceleration chamber has a smaller cross-sectional area than its outlet.
9. The jet mill according to claim 1, wherein the height of the milling chamber is from 3 mm to 10 mm.
10. The jet mill according to claim 1, wherein the pins are made from a material selected from the group of wear resistant steel or wear resistant ceramics.
11. The jet mill according to claim 1, wherein the outlet of the milling chamber is coupled to the inlet of a classifier capable of separating fine particles from coarse particles.
12. The jet mill according to claim 11, wherein the outlet for the coarse fraction is recycled to the inlet of the milling chamber or to the inlet of the acceleration chamber.
13. A process for milling solid particles comprising the steps of (a) injecting the particles in a jet, and (b) feeding the jet including the injected particles into a jet mill according to claim 1.
14. The process according to claim 13, wherein the outlet of the milling chamber is coupled to the inlet of a classifier capable of separating fine particles from coarse particles, and separating at least one fine particle fraction from the classifier feed material.
Description
[0066] The invention is explained in more detail below with reference to the drawings. The drawings are to be interpreted as in-principle presentation. They do not constitute any restriction of the invention, for example with regards to specific dimensions or design variants. In the figures:
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LIST OF REFERENCE NUMERALS USED
[0076] 1 . . . milling chamber [0077] 2 . . . longitudinal axis [0078] 3 . . . inlet of the milling chamber [0079] 4 . . . outlet of the milling chamber [0080] 5 . . . pin [0081] 6 . . . acceleration chamber [0082] 7 . . . inlet of the acceleration chamber [0083] 11 . . . gas supply [0084] 12 . . . additional gas [0085] 13 . . . additional gas [0086] 14 . . . fine particles outlet [0087] 15 . . . medium particles outlet [0088] 16 . . . coarse particles outlet [0089] 17 . . . particle feed [0090] 18 . . . separation unit [0091] 19 . . . off gas [0092] A1, A2 . . . axial distance [0093] L1, L2 . . . lateral distance [0094] P1, P2, P3, P4 . . . planes of pins
[0095]
[0096] An acceleration chamber 6 with an inlet 7 and an outlet is connected to the milling chamber 1, the outlet of the acceleration chamber being the inlet 3 of the milling chamber. The cross-sectional areas of the milling chamber 1 and the acceleration chamber 6 are rectangular with the cross-sectional area of the inlet 7 of the acceleration chamber being smaller than its outlet.
[0097] All pins 5 of this example have the same cylindrical form. Their cross-section is circular, thus the surface of the pins facing the inlet 3 is convex.
[0098]
[0099] The pins of the second pin segment are larger in diameter than the pins of the first pin segment. Counting from the inlet 3 to the outlet 4, the first plane of the second pin segment comprises three pins. One pin is attached to the left wall of the milling chamber whereas the other two pins are arranged with an equal lateral distance between the pins. The cross-section of the left-most pin is half-circular whereas the cross-section of the other two pins is circular. The lateral distance of the right-most pin to the right wall is identical to the lateral extension of the left-most pin attached to the wall. The pins in the second plane of the second pin segment are arranged in a similar manner as the pins in the first plane but are laterally offset to the pins of the first plane. The right-most pin is attached to the right wall of the milling chamber whereas the other two pins are arranged with an equal lateral distance between the pins. The cross-section of the right-most pin is half-circular whereas the cross-section of the other two pins is circular. The lateral distance of the left-most pin to the left wall is identical to the lateral extension of the right-most pin attached to the wall. The pins of the third plane are arranged like the pins in the first plane, and the pins of the fourth plane are arranged like the pins of the second plane. The cross-section of all pins in the second pin segment is circular or half-circular, thus the surface of the pins facing the inlet 3 is convex.
[0100] All planes are distant to each other in the longitudinal direction. The pins of one plane are laterally offset to the pins of the adjacent planes.
[0101] An acceleration chamber 6 with an inlet 7 and an outlet is connected to the milling chamber 1, the outlet of the acceleration chamber being the inlet 3 of the milling chamber. The cross-sectional areas of the milling chamber 1 and the acceleration chamber 6 are rectangular with the cross-sectional area of the inlet 7 of the acceleration chamber being smaller than its outlet.
[0102]
[0103] In the lateral direction, i.e. perpendicularly to the longitudinal axis, the pins of a subsequent plane are arranged in the middle of the free passageway between two pins of the preceding plane. The ratio of the lateral distance L1 between two neighboring pins in a plane and the diameter of the respective pins is preferably from 0.8 to 1.5. In the example shown in
[0104] The axial distance A1 between two neighboring planes is defined via the envelope of the pins in the respective planes. In the example shown in
[0105]
[0106] The pins of the third plane P3 are laterally offset to the pins of the second plane P2 and to the pins of the first plane P1. In the lateral direction, the pin of plane P2 is arranged in the middle of the free passageway between the two pins of plane P1.
[0107] The ratio of the lateral distance L1 between the two pins in plane P1 and the diameter of the respective pins is preferably from 0.8 to 1.5. In the example shown in
[0108] The pins in the third plane P3 are arranged such that the shortest distance between a pin in the second plane P2 and a neighboring pin in the third plane P3 has an axial component A2 and a lateral component L2. It is preferred that the ratio of the lateral component L2 of the pin-to-pin distance and the lateral diameter of the respective pin in the third plane P3 is from 0.8 to 1.5.In the example shown in
[0109]
[0110] In the example shown the Coanda classifier is able to separate the milled particles into three fractions, a fine particle fraction, a medium particle fraction and a coarse particle fraction. Additional gas streams 12 and 13 without particle load are available to influence the separation into the three fractions. The fine particle fraction is removed from the classifier via a fine particle outlet 14. The medium particle fraction is removed from the classifier via a medium particle outlet 15. The coarse particle fraction is removed from the classifier via a coarse particle outlet 16 and is recycled to the gas supply 11 and thus the inlet of the milling chamber of the jet mill. Fresh particles to be milled can be fed into the gas supply 11 directly and/or into the recycle stream from the coarse particle outlet 16 back to the gas supply 11. This option is shown in
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EXAMPLES
[0112] A jet mill according to the invention was compared with an opposed jet mill and a spiral jet mill according to the prior art. A limestone powder (Juraperle 150-300 by company Omya Gmbh, Kln, Germany) was milled in each of the three mills. The grain size parameters of the powder were as follows:
TABLE-US-00001 D10 [m] 4.6 D50 [m] 119.0 D90 [m] 225.0
[0113] In each case the milling pressure for the respective mill was set as high as possible as this leads to the highest product fineness. All mills were then loaded until the particle size distribution of the milled product became significantly coarser or the mill reached a critical operating state.
Comparative Example 1
[0114] As comparative example 1 an opposed jet mill (type AFG 100 by company Hosokawa Alpine AG, Augsburg, Germany) was used. The mill was operated with three nozzles with a diameter 10 of 1.9 mm each to supply the milling gas with a pressure of 7 bar. The material was fed into the milling chamber with a screw feeder at a feed rate of 4 kg/h. The diameter of the deflecting wheel classifier in the mill was 50 mm. The air classifier was operated at 12,500 rpm resulting in a circumferential speed of 33 m/s.
Comparative Example 2
[0115] As comparative example 2 a spiral jet mill with a diameter of the milling chamber of 170 mm and a milling chamber height of 15 mm was used. The spiral jet mill was equipped with ten cylindrical milling gas nozzles with a diameter of 1.5 mm each, equally distributed over the circumference of the milling chamber. The milling gas pressure was 3.6 bar. The diameter of the injector nozzle was 2.5 mm and the diameter of the booster nozzle was 8 mm. The injector nozzle pressure was 3.8 bar. The vortex finder of the mill had a circular shape with a diameter of 40 mm.
Example 1 According to the Invention
[0116] A jet mill similar to the embodiment shown in
[0117] An acceleration chamber with an inlet and an outlet was connected to the milling chamber, the outlet of the acceleration chamber being the inlet of the milling chamber. The length of the acceleration chamber was 50 mm. The length of the milling chamber was 165 mm. The cross-sectional areas of the milling chamber and the acceleration chamber were rectangular. The width of the milling chamber was 20 mm and its height 5 mm. The width of the inlet of the acceleration chamber was 9 mm.
[0118] The outlet of the milling chamber was coupled to the inlet of a classifier based on the Coanda effect. The overall setup is schematically shown in
[0119] A screw conveyor was used to feed the feed material into the suction pipe of the injector. In the injector the solid feed material was dispersed in the milling gas jet. The dispersed material was accelerated in the acceleration chamber in a way that the particles reached a velocity similar to the milling gas velocity. Subsequently the particles hit the pins of the first pin segment and were crushed by the mechanical impact. Additionally, particle-particle contacts between particles reflected by the pin and particles dispersed in the milling gas led to high energy impacts and thus particle breakages. After the first pin segment the particles were re-accelerated until they hit the first pins of the second pin segment. After the third pin segment the particles were re-accelerated by the remaining milling gas pressure so that they could enter into the Coanda classifier at a speed similar to the milling gas. The main part of the milling gas entering into the Coanda classifier was forced into a bend motion along the bend shape of the Coanda inlet. Fine particles of a high specific surface followed the bend motion of the gas stream. Particles of a lower specific surface, e.g. medium sized or coarse particles, could only partially follow the motion of the bend gas and were less deviated from their initial straight motion. Thus, a parabolic distribution of fine to coarse particles could be realized inside the housing of the Coanda classifier. By adjusting the splitters in the paths of the particles of different size a split into a fine particle fraction and a coarse particle fraction was possible. To optimize the flight path of the particles in the Coanda classifier and thus to optimize the separation performance additional gas was sucked into the Coanda classifier. The split off fine particles were sucked into a filter to remove the solid phase from the gas phase. The coarse particles were sucked into a cyclone to remove the solid phase from the gas phase. The coarse particle fraction collected at the bottom of the cyclone was carried out of the cyclone by a screw conveyor and subsequently fed back into the suction pipe of the injector. Thus, the coarse particles were mixed with the fresh material and were re-fed to the mill.
[0120] Parameters and results of the milling experiments are shown in the following table:
TABLE-US-00002 Comp. Ex. 1 Comp. Ex. 2 Inv. Ex. Feed rate [kg/h] 4 2 10 Milling pressure [bar] 7 3.6 7.8 Volume flow [Nm.sup.3/h] 62 86.6 36 Specific load [g/m.sup.3] 65 23 278 Specific energy [kWh/kg] 1.12 1.86 0.28 D10 [m] 0.4 0.6 0.3 D50 [m] 3.0 3.7 3.0 D90 [m] 5.7 9.7 6.5
[0121] As can be seen from the above table the product fineness as a result of milling the powder in the jet mill according to the invention is very similar to the product fineness achieved with the opposed jet mill. The product of the milling process in the spiral jet mill is coarser.
[0122] Due to its design, the jet mill according to the invention can be operated at a significantly higher specific load of particles in the milling gas (jet). Due to the high solids loading of the milling gas and the comparatively low volumetric flow, the specific energy consumption of the milling process according to the invention is much lower than those of the processes according to the prior art. In the examples above the specific energy consumption is lower by a factor of 4 compared to the opposed jet mill and by a factor of 6.6 compared to the spiral jet mill.
Comparative Example 3
[0123] In a further set of experiments the influence of the intermediate acceleration segments was investigated. The material to be milled was the same limestone powder (Juraperle 150-300 by company Omya Gmbh, Kln, Germany) as in the previous examples. In each case the milling pressure for the respective mill was set to 8 bars (abs) and the feed rate of the limestone particles was set to 18 kg/h.
[0124] As comparative example 3 a jet mill according to the embodiment shown in
[0125] All planes were distant to each other. The distance in the longitudinal direction between the planes was 10 mm. The pins of one plane were laterally offset to the pins of the adjacent planes in that the center of the axis of a pin in one plane and the center of the axis of a pin in a subsequent plane lay on different lines parallel to the longitudinal axis of the mixing chamber. The pins were made of silicon carbide. All pins had the same cylindrical form. Their cross-section was circular with a diameter of 4 mm.
[0126] An acceleration chamber 6 with an inlet 7 and an outlet was connected to the milling chamber 1, the outlet of the acceleration chamber 6 being the inlet 3 of the milling chamber 1. The length of the acceleration chamber was 50 mm. The length of the milling chamber was 165 mm. The cross-sectional areas of the milling chamber and the acceleration chamber were rectangular. The width of the milling chamber was 20 mm and its height 5 mm. The width of the inlet of the acceleration chamber was 9 mm.
[0127] A screw conveyor was used to feed the feed material into the suction pipe of the injector. In the injector the solid feed material was dispersed in the milling gas jet. The dispersed material was accelerated in the acceleration chamber 6 in a way that the particles reached a velocity similar to the milling gas velocity. Subsequently the particles hit the pins 5 of the first pin segment and were crushed by the mechanical impact. Additionally, particle-particle contacts between particles reflected by the pin and particles dispersed in the milling gas led to high energy impacts and thus particle breakages. The limestone particles were collected at the outlet 4 of the jet mill and their particle size was determined.
Example 2 According to the Invention
[0128] A jet mill according to the embodiment shown in
[0129] The jet mill comprised a milling chamber 1 with a longitudinal axis 2, an inlet 3 at one end of the axis 2 and an outlet 4 at the opposite end of the axis 2. In the free flow cross-section inside the milling chamber 1 there were twenty pins 5 arranged in four pin segments with five pins each. Each pin segment comprised two planes of pins, the planes being perpendicular to the longitudinal axis 2. Counting from the inlet 3 to the outlet 4, in the first plane two pins 5 were symmetrically arranged with respect to the longitudinal axis. The second plane comprised three pins 5. One pin was arranged in the center of the milling chamber on the longitudinal axis. The two other pins were attached to the left wall and the right wall of the milling chamber respectively. The arrangement of pins in the second, third and fourth pin segment was identical to the arrangement of pins in the first pin segment.
[0130] All planes were distant to each other. The distance in the longitudinal direction between the first planes and the respective second planes in each pin segment was 10 mm. The pins of one plane were laterally offset to the pins of the adjacent planes in that the center of the axis of a pin in one plane and the center of the axis of a pin in a subsequent plane lay on different lines parallel to the longitudinal axis of the mixing chamber. The pins were made of silicon carbide. All pins had the same cylindrical form. Their cross-section was circular with a diameter of 4 mm, thus the surface of the pins facing the inlet was convex. The distance in the longitudinal direction between the first planes and the respective second planes in each pin segment in terms of their envelopes was thus 6 mm. Between the pin segments there was one acceleration segment each with no pins. The length of the three acceleration segments was 36 mm each.
[0131] An acceleration chamber 6 with an inlet 7 and an outlet was connected to the milling chamber 1, the outlet of the acceleration chamber 6 being the inlet 3 of the milling chamber 1. The length of the acceleration chamber was 50 mm. The length of the milling chamber was 165 mm. The cross-sectional areas of the milling chamber and the acceleration chamber were rectangular. The width of the milling chamber was 20 mm and its height 5 mm. The width of the inlet of the acceleration chamber was 9 mm.
[0132] A screw conveyor was used to feed the feed material into the suction pipe of the injector. In the injector the solid feed material was dispersed in the milling gas jet. The dispersed material was accelerated in the acceleration chamber 6 in a way that the particles reached a velocity similar to the milling gas velocity. Subsequently the particles hit the pins 5 of the first pin segment and were crushed by the mechanical impact. Additionally, particle-particle contacts between particles reflected by the pin and particles dispersed in the milling gas led to high energy impacts and thus particle breakages. After the first pin segment the particles were re-accelerated until they hit the first pins 5 of the second pin segment. After the second pin segment the particles were re-accelerated until they hit the first pins 5 of the third pin segment. After the third pin segment the particles were re-accelerated until they hit the first pins 5 of the fourth pin segment. The limestone particles were collected at the outlet 4 of the jet mill and their particle size was determined.
[0133]
[0134] The dash-dotted line shows the particle size distribution of the sample of particles obtained at the outlet of the jet mill of comparative example 3. About 54% of the particles of this sample were smaller than 50 m and about 30% of the particles were still larger than 100 m.
[0135] The solid line shows the particle size distribution of the sample of particles obtained at the outlet of the jet mill of example 2 according to the invention. About 62% of the particles of this sample were smaller than 50 m and about 14% of the particles were larger than 100 m.
[0136] The milling process in a jet mill with intermediate acceleration segments according to the invention yields smaller particles with a more homogeneous particle size distribution, which can also be deducted from the graph in
[0137] Further experiments with a triboluminescent material showed that the breakage of particles in a mill according to