US3537658A - Autogenous airswept mill - Google Patents
Autogenous airswept mill Download PDFInfo
- Publication number
- US3537658A US3537658A US782698A US3537658DA US3537658A US 3537658 A US3537658 A US 3537658A US 782698 A US782698 A US 782698A US 3537658D A US3537658D A US 3537658DA US 3537658 A US3537658 A US 3537658A
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- United States
- Prior art keywords
- mill
- grinding
- autogenous
- chamber
- airswept
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- Expired - Lifetime
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- 238000000227 grinding Methods 0.000 description 36
- 238000000605 extraction Methods 0.000 description 19
- 239000000463 material Substances 0.000 description 18
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000006722 reduction reaction Methods 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 208000028659 discharge Diseases 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000007873 sieving Methods 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000004323 axial length Effects 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000011362 coarse particle Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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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
- 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
Definitions
- Each of the remote end walls of the grinding chambers is provided with a central inlet aperture for the introduction of gas and material to be ground, and the walls which separate the grinding chambers from the extraction chamber are provided with apertures which extend no farther from the common axis than the inlet apertures and which discharge gas laden with ground material into the extraction chamber.
- This invention relates to an autogenous airswept mill, wherein the grinding chamber diameter is at least twice the chamber length and the autogenously ground material is extracted from the grinding chamber by an air stream.
- the object of the invention is therefore to provide improved autogenous airswept mills of the kind described, which eliminate disadvantages of the known constructions, so that while the specific advantages in regard to reduction, sieving and drying are maintained, the manufacturing costs are lowered for the same output.
- the mill comprises two similarly shaped grinding chambers disposed in mirror-image fashion about a central plane, between which is a common central extraction chamber connected to the two grinding chambers by apertures whose distance from the mill axis does not exceed the radius of the two inlet apertures provided in the two end walls of the mill for the introduction of air and material to be ground.
- Mills with two grinding chambers and an intermediate central extraction chamber are already known in another connection.
- the grinding chambers which are filled with grinding bodies, have in general a diameter which is substantially less than twice the length of each grinding chamber. Therefore it is necessary to use one grinding chamber as a coarse grinding chamber and the other as a line grinding chamber.
- the apertures provided between the two grinding chambers and the central extraction chamber are mainly disposed in the outer area of the extraction wall, so that the ground maice terial is moved into the central extraction chamber by the rotary movement of the mill.
- the chamber diameter is at least twice as great as the grinding chamber length; that they are constructed completely alike; and that because of the form of the apertures provided between the two grinding chambers and the central extraction chamber, the autogenously ground material is exclusively extracted by the owing air.
- the constructional combination, as provided by the invention, of two similarly operating grinding chambers fed' in parallel produces an appreciable reduction in manufacturing costs for the same output.
- this construction there is achieved a smaller mill diameter and a larger mill length, for the same output, while maintaining the required large ratio of diameter to length in the grinding chambers. Since the price per kilogram for the end walls, made of steel castings, is higher than for the mill casing, this alone gives a reduction in manufacturing costs.
- the diameter of the bearings may also be reduced, since the quantity of raw material and air to be fed into the mill is distributed between the two journals of the mill. Cost studies thus show that in spite of the constructional expense involved in central extraction, the total manufacturing costs can be appreciably reduced.
- the mill contains two substantially cylindrical coaxial grinding chambers 2, 2 disposed in mirror-image fashion on both sides of a central plane 1, between which is disposed a common central extraction chamber 3.
- the mill is supported in two journals 4, 4', and adjacent each bearing is provided with an inlet 5, 5' for raw material and air (or hot gas). Mill drive is effected by a toothed wheel 6.
- the fixed extractor housing 12 is provided with a lower outlet pipe 12a into which coarse material falls, and an upper outlet pipe 12b for air charged with ground material.
- the central extraction chamber 3 communicates with the extractor housing 12 via apertures 13 provided in the periphery of the extraction chamber 3.
- the chamber diameter is more than twice the chamber length.
- Neither grinding chamber contains any filling of grinding elements; instead 3 autogenous grinding takes place therein through the material shattering and comminuting itself.
- Both grinding chambers 2, 2 are supplied in identical manner with fresh raw material and air (or hot gas) via the inlets 5, 5.
- the air streams passing axially through both grinding chambers 2, 2' towards the centre have a drying and sieving effect in each chamber and entrain material which has been suciently reduced into the central extraction chamber 3.
- any coarse particles which may have been taken up by the air stream fall out, and are removed through the lower pipe 12a via the extractor housing, to be subjected to ne grinding in another mill, possibly after initial air sifting.
- the air current, charged with the rest of the ground material is discharged through the upper pipe 12b of the extractor housing 12, preferably to an air classifier.
- An autogenous rotary mill from which the autogenously ground material is extracted by a gas stream wherein the improvement comprises two substantially cylindrical coaxial grinding chambers which are mounted to rotate as a unit about their common axis and are separated by a common extraction chamber, the remote end walls of the grinding chambers each being provided with a central inlet aperture for the introduction of gas and of material to be ground, and the walls which separate the grinding chambers from the extraction chamber being provided with apertures which extend no farther from the common axis than the inlet apertures and which discharges gas laden with ground material into the extraction chamber, the diameter of each grinding chamber being at least twice its axial length.
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- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
Description
Nov.-3, 1970 H. JURGENJANICH 3,537,658
AUTOGENOUS AIRSWEPT MILL Filed im. 1o, 196s United States Patent O 3,537,658 AUTOGENOUS AIRSWEPT MILL Hans Jurgenjanich, Neubeckum, Germany, assigner to Polysius G.m.b.H., Neubeckum, Germany Filed Dec. 10, 1968, Ser. No. 782,698 Int. Cl. B07b 3/00 U.S. Cl. 241-44 2 Claims ABSTRACT OF THE DISCLOSURE In this mill, from which the autogenously ground material is extracted by a gas stream, two substantially cylindrical coaxial grinding chambers are mounted to rotate as a unit about their common axis, and are separated by a common extraction chamber. Each of the remote end walls of the grinding chambers is provided with a central inlet aperture for the introduction of gas and material to be ground, and the walls which separate the grinding chambers from the extraction chamber are provided with apertures which extend no farther from the common axis than the inlet apertures and which discharge gas laden with ground material into the extraction chamber.
BACKGROUND OF THE INVENTION This invention relates to an autogenous airswept mill, wherein the grinding chamber diameter is at least twice the chamber length and the autogenously ground material is extracted from the grinding chamber by an air stream.
Previously known autogenous airswept mills only have one grinding chamber. The length of the mill thus corresponds to one grinding chamber length. Since a relatively large ratio of diameter to length is needed in such autogenous airswept mills to provide good reduction, sieving and drying properties, these known mills have a relatively large diameter and a small length. Since with known constructions the entire amounts of fresh material and air have to be introduced through one bearing journal, and all the air laden with line material has to be extracted through the other bearing journal, the bearings are also undesirably large.
SUMMARY OF THE INVENTION The object of the invention is therefore to provide improved autogenous airswept mills of the kind described, which eliminate disadvantages of the known constructions, so that while the specific advantages in regard to reduction, sieving and drying are maintained, the manufacturing costs are lowered for the same output.
According to the invention this object is achieved in that the mill comprises two similarly shaped grinding chambers disposed in mirror-image fashion about a central plane, between which is a common central extraction chamber connected to the two grinding chambers by apertures whose distance from the mill axis does not exceed the radius of the two inlet apertures provided in the two end walls of the mill for the introduction of air and material to be ground.
Mills with two grinding chambers and an intermediate central extraction chamber are already known in another connection. With these mills, however, the grinding chambers, which are filled with grinding bodies, have in general a diameter which is substantially less than twice the length of each grinding chamber. Therefore it is necessary to use one grinding chamber as a coarse grinding chamber and the other as a line grinding chamber. Also the apertures provided between the two grinding chambers and the central extraction chamber are mainly disposed in the outer area of the extraction wall, so that the ground maice terial is moved into the central extraction chamber by the rotary movement of the mill.
With the autogenous airswept mills of the invention, in contrast, it is a characteristic feature that in both grinding chambers the chamber diameter is at least twice as great as the grinding chamber length; that they are constructed completely alike; and that because of the form of the apertures provided between the two grinding chambers and the central extraction chamber, the autogenously ground material is exclusively extracted by the owing air.
As compared with previously known autogenous airswept mills, the constructional combination, as provided by the invention, of two similarly operating grinding chambers fed' in parallel produces an appreciable reduction in manufacturing costs for the same output. By this construction there is achieved a smaller mill diameter and a larger mill length, for the same output, while maintaining the required large ratio of diameter to length in the grinding chambers. Since the price per kilogram for the end walls, made of steel castings, is higher than for the mill casing, this alone gives a reduction in manufacturing costs. With the device provided by the invention, the diameter of the bearings may also be reduced, since the quantity of raw material and air to be fed into the mill is distributed between the two journals of the mill. Cost studies thus show that in spite of the constructional expense involved in central extraction, the total manufacturing costs can be appreciably reduced.
While the replacement of even a single autogenous airswept mill of known design in a grinding plant by a mill in accordance with the invention represents a considerable technical advance, there is even more advantage if two autogenous airswept mills are needed in a plant, which is frequently the case. While separate mills have hitherto been provided for this purpose, the invention provides constructional union of two similar autogenous airswept mills, which reduces by half the number of mill end' faces and mill bearings required.
BRIEF DESCRIPTION OF THE DRAWING The drawing shows in longitudinal section one form of mill embodying the invention.
DESCRIPTION OF THE PREFERRED EMBODIMENT The mill contains two substantially cylindrical coaxial grinding chambers 2, 2 disposed in mirror-image fashion on both sides of a central plane 1, between which is disposed a common central extraction chamber 3.
The mill is supported in two journals 4, 4', and adjacent each bearing is provided with an inlet 5, 5' for raw material and air (or hot gas). Mill drive is effected by a toothed wheel 6.
Between the grinding chambers 2, 2 and the central extraction chamber 3 are provided two walls 7, 7 which have apertures 8, 8' in their central areas only. 'Ille distance of these apertures 8, 8 from the mill axis 9 does not exceed the radius of the inlet apertures 11, 11' which are provided in the two end faces 10, 10 of the mill and are used for introducing air and material to be ground.
The fixed extractor housing 12 is provided with a lower outlet pipe 12a into which coarse material falls, and an upper outlet pipe 12b for air charged with ground material. The central extraction chamber 3 communicates with the extractor housing 12 via apertures 13 provided in the periphery of the extraction chamber 3.
For both grinding chambers 2, 2' the chamber diameter is more than twice the chamber length. Neither grinding chamber contains any filling of grinding elements; instead 3 autogenous grinding takes place therein through the material shattering and comminuting itself.
Both grinding chambers 2, 2 are supplied in identical manner with fresh raw material and air (or hot gas) via the inlets 5, 5. The air streams passing axially through both grinding chambers 2, 2' towards the centre have a drying and sieving effect in each chamber and entrain material which has been suciently reduced into the central extraction chamber 3. Here any coarse particles which may have been taken up by the air stream fall out, and are removed through the lower pipe 12a via the extractor housing, to be subjected to ne grinding in another mill, possibly after initial air sifting. The air current, charged with the rest of the ground material, is discharged through the upper pipe 12b of the extractor housing 12, preferably to an air classifier.
I claim:
1. An autogenous rotary mill from which the autogenously ground material is extracted by a gas stream, wherein the improvement comprises two substantially cylindrical coaxial grinding chambers which are mounted to rotate as a unit about their common axis and are separated by a common extraction chamber, the remote end walls of the grinding chambers each being provided with a central inlet aperture for the introduction of gas and of material to be ground, and the walls which separate the grinding chambers from the extraction chamber being provided with apertures which extend no farther from the common axis than the inlet apertures and which discharges gas laden with ground material into the extraction chamber, the diameter of each grinding chamber being at least twice its axial length.
2. An autogenous rotary mill according to claim 1 wherein the extraction chamber is provided with peripheral discharge apertures and is surrounded by a fixed extractor housing for collecting the discharged gas and ground material.
References Cited UNITED STATES PATENTS 5/1927 Crowe 241-44 6/ 1944 Newhouse 241-49 X TRAVIS S. MCGEHEE, Primary Examiner
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US78269868A | 1968-12-10 | 1968-12-10 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US3537658A true US3537658A (en) | 1970-11-03 |
Family
ID=25126901
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US782698A Expired - Lifetime US3537658A (en) | 1968-12-10 | 1968-12-10 | Autogenous airswept mill |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US3537658A (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3670973A (en) * | 1969-07-23 | 1972-06-20 | Fives Lille Cail | Crusher |
| US4078730A (en) * | 1975-11-20 | 1978-03-14 | F. L. Smidth & Co. | Tube mill |
| US4083500A (en) * | 1975-11-21 | 1978-04-11 | F. L. Smidth & Co. | Tube mill |
| US5649667A (en) * | 1993-06-23 | 1997-07-22 | F.L. Smidth & Co. A/S | Ring roller mill |
| US5716015A (en) * | 1993-08-02 | 1998-02-10 | F.L. Smidth & Co. A/S | Ring roller mill |
| US6299081B1 (en) * | 1999-03-30 | 2001-10-09 | Khd Humboldt Wedag Ag | Tube mill |
| WO2011035451A3 (en) * | 2009-09-23 | 2011-07-14 | Hamza Delic Mesic | Assembly of interconnected mineral pulverising mills |
| CN111804389A (en) * | 2020-07-22 | 2020-10-23 | 张纪彬 | Organic flour production and processing method |
| AT523622A1 (en) * | 2020-02-25 | 2021-09-15 | Ess Holding Gmbh | Wet mill |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1627488A (en) * | 1925-09-30 | 1927-05-03 | Paul L Crowe | Ball mill |
| US2351870A (en) * | 1940-12-26 | 1944-06-20 | Allis Chalmers Mfg Co | Combined ball mill and drier |
-
1968
- 1968-12-10 US US782698A patent/US3537658A/en not_active Expired - Lifetime
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1627488A (en) * | 1925-09-30 | 1927-05-03 | Paul L Crowe | Ball mill |
| US2351870A (en) * | 1940-12-26 | 1944-06-20 | Allis Chalmers Mfg Co | Combined ball mill and drier |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3670973A (en) * | 1969-07-23 | 1972-06-20 | Fives Lille Cail | Crusher |
| US4078730A (en) * | 1975-11-20 | 1978-03-14 | F. L. Smidth & Co. | Tube mill |
| US4083500A (en) * | 1975-11-21 | 1978-04-11 | F. L. Smidth & Co. | Tube mill |
| US5649667A (en) * | 1993-06-23 | 1997-07-22 | F.L. Smidth & Co. A/S | Ring roller mill |
| US5716015A (en) * | 1993-08-02 | 1998-02-10 | F.L. Smidth & Co. A/S | Ring roller mill |
| US5823450A (en) * | 1993-08-02 | 1998-10-20 | F.L. Smidth & Co. A/S | Ring roller mill |
| US6299081B1 (en) * | 1999-03-30 | 2001-10-09 | Khd Humboldt Wedag Ag | Tube mill |
| WO2011035451A3 (en) * | 2009-09-23 | 2011-07-14 | Hamza Delic Mesic | Assembly of interconnected mineral pulverising mills |
| AT523622A1 (en) * | 2020-02-25 | 2021-09-15 | Ess Holding Gmbh | Wet mill |
| AT523622B1 (en) * | 2020-02-25 | 2022-09-15 | Ess Holding Gmbh | wet mill |
| CN111804389A (en) * | 2020-07-22 | 2020-10-23 | 张纪彬 | Organic flour production and processing method |
| CN111804389B (en) * | 2020-07-22 | 2021-04-20 | 濉溪县鲁王制粉有限责任公司 | Organic flour production and processing method |
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