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WO2000056457A1 - Method for milling of material with large range of grindability - Google Patents

Method for milling of material with large range of grindability Download PDF

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Publication number
WO2000056457A1
WO2000056457A1 PCT/CZ2000/000014 CZ0000014W WO0056457A1 WO 2000056457 A1 WO2000056457 A1 WO 2000056457A1 CZ 0000014 W CZ0000014 W CZ 0000014W WO 0056457 A1 WO0056457 A1 WO 0056457A1
Authority
WO
WIPO (PCT)
Prior art keywords
milling
grindability
grain size
milled
materials
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.)
Ceased
Application number
PCT/CZ2000/000014
Other languages
French (fr)
Inventor
Jiří ZEGZULKA
Karel Voit
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
PSP Engineering AS
Original Assignee
PSP Engineering AS
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by PSP Engineering AS filed Critical PSP Engineering AS
Priority to BR0010773-5A priority Critical patent/BR0010773A/en
Priority to SK1417-2001A priority patent/SK284706B6/en
Publication of WO2000056457A1 publication Critical patent/WO2000056457A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C21/00Disintegrating plant with or without drying of the material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C4/00Crushing or disintegrating by roller mills
    • B02C4/02Crushing or disintegrating by roller mills with two or more rollers

Definitions

  • the invention deals with a method for milling of material with different grain size and/or with different range of grindability from 30 up to 90 according to Hargrowe (Hg) in more, mutual consequential milling steps, with using of middle-pressure roll presses.
  • a disadvantage of the present procedures is, that during concurrent milling of several components with different value of grindability, for example in vertical roller mills, the components with higher grindability are over-milled and the components with lower grindability are under-milled. Than, it is necessary to repeat the milling of significant part of under-milled components. Such milling processes necessarily cause higher consumption of energies, what results in lower specific output of the milling system.
  • the aim of the invention is, that during concurrent milling of several components with different value of grindability, for example in vertical roller mills, the components with higher grindability are over-milled and the components with lower grindability are under-milled.
  • Such milling processes necessarily cause higher consumption of energies, what results in lower specific output of the milling system.
  • Further essence of the invention is, that at least between the first and the second milling step, further material is added to the milled material and that type and/or grindability of added material is different from grindability of admission milled material, advantageously material with lower grindability, than is that of material in previous step.
  • the procedure is according to the invention divided into three separate, mutually functionally defined steps, it is possible to adjust the operating conditions in the first one, so that the material with bad grindability, possibly mixture of such materials, is processed preferentially, efficiently from the functional and economical point of view.
  • it is possible advantageously to dose additionally materials with better grindability to further milling step, possibly materials with lower grain size.
  • Example 1 Method of milling according to the invention is in this example used for milling of material with practically the same grindability, for example cement clinker, after its exit from rotary kiln followed by inserted cooler. It is dealing with a material with middle grindability (Hg 80), but with significant different grain size, usually in the range from 0,1 to 45 mm.
  • the cement clinker is according to Fig. 1 collected in the reservoir 4, from there it is through the piping 40 lead to the milling bodies of the first used milling stage 1, for example in form of a roll middle-pressure press of standard construction, with the rest slot adjusted to 27 mm. There, supplied cement clinker is pre-formed, especially larger admission grains are being broken.
  • the pre-formed cement clinker is transferred by the means of the first transport element 10 to the second milling stage 2, for example again to a middle-pressure press, its not illustrated operating slot is adjusted on value of 15 mm, e.g. lower than that in the previous step and on the contrary, thrust of the milling roll is higher.
  • the pre-formed cement clinker which already doesn't contain grains of significantly different size, is pre-milled and simultaneously calibrated as to height, so that a layer of practically homogenous material, as to grain size and compactness, is produced.
  • the material is than transferred by the means of the second transport element 20 to the third milling stage 3.
  • the operating slot of this stage is adjusted on the value of 10 mm, thrust of the milling roll is on the contrary even higher than the thrust in the previous milling stage.
  • the material is after-milled to the final requested size and the result product is through the outlet 30 lead towards the further technological step.
  • a sorting system 6 is inserted according to Fig. 4 after the outlet 30 from the third milling stage 3, the system contains a separator 60, consisting for example of suitable chosen vibrating screen, air separator and so on. Sufficiently finely milled cement clinker passes through the separator 60 and is lead through the outlet 61 towards further technological step. Separated undesirable coarser fraction is through the discharge 62 and connected return transport element 620, for example a transporter, lead to the additional reservoir 51 and from there through the piping 510 and the first transport element 10 back to the second milling stage 2.
  • a separator 60 consisting for example of suitable chosen vibrating screen, air separator and so on.
  • Sufficiently finely milled cement clinker passes through the separator 60 and is lead through the outlet 61 towards further technological step.
  • Separated undesirable coarser fraction is through the discharge 62 and connected return transport element 620, for example a transporter, lead to the additional reservoir 51 and from there through the piping 510 and the first transport element 10 back to
  • Procedure according to the invention is used for preparation of mixed cement, which consists of 70% till 94% of mixture of cement clinker with average grindability of 75 Hg and with predominantly higher share of grains with larger dimensions, of 6% till 35% of slag with average grindability of 35 Hg, which has larger share of grains with small dimensions and of 5% of soft gypsum with average grindability of 95 Hg.
  • Example of procedure of milling of above mentioned components is illustrated in variants on Fig.2 and is as follows.
  • the first milled component is the cement clinker, dosed from the reservoir 4 through the piping 40 to the first milling stage 1.
  • the slag is dosed into the second milling stage 2 from the additional reservoir 51, e.g. the mixture of slag and cement clinker is entering it.
  • the gypsum with the best grindability is dosed from the additional reservoir 52 ' through the piping 520 to the third milling stage 3 together with pre-milled mixture of slag and cement clinker.
  • Procedure according to this example is a variant of preparation of mixed cement in composition according to previous example.
  • the first two materials e.g. cement clinker and slag
  • the first two materials are stored in the first reservoir 41 and the second reservoir 42, as is illustrated on Fig.3, from there, they are through the pipings 410 and 420 dosed into the common reservoir 4 and consequently through the piping 40 lead to the first milling stage 1 with relatively large operating slot and with low thrust of not illustrated milling roll.
  • the remaining component of prepared mixed cement e.g. soft gypsum
  • the additional sorting system 21 is advantageously inserted into the milling line yet before the final phase of after-milling.
  • Its separator 210 separates undesirable, so far insufficiently milled material, which exits the second milling stage 2 and it also transfers sufficiently fine fractions through the transport element 211 to the third milling stage 3.
  • Possible coarser under-milled fraction is, on the contrary, by the return transport element 220 returned to the second milling stage 2, namely through the additional reservoir 51 or directly by the means of the first transport element 10, as is illustrated on Fig.3 in broken line.
  • blast furnace cement which consists of mixture of 65% to 80% of blast furnace slag, 20% to 35% of cement clinker and 5% of gypsum, namely according to the procedure illustrated on Fig.4.
  • the first milled component is a slag dosed from the reservoir 4 through the piping 40 into the first milling stage.
  • Cement clinker and gypsum with lower grindability is dosed from the additional reservoir 51 to the second milling stage 2 together with slag, exiting the first milling stage 1.
  • Mixture of all three components, necessary for preparation of the blast furnace cement, is than dosed by the means of the second transport element 20 to the third milling stage 3 for after-milling and it exits it through the outlet 30 towards further technological step.
  • Possible application of the sorting system 6 was described in connection with example 1.
  • Method for milling of materials with different grain size and large range of grindability can be advantageously used especially for milling of recycled matters, cement clinker with admixture of slag, puzzolan, ash and so on, possibly for milling of two or more types of minerals with recycling of fractions and during fining of mixtures.

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  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

The subject of the invention is a method for milling of material with different grain size and/or with different range of grindability from 30 up to 90 according to Hargrowe (Hg) in more, mutual consequential milling steps and with using of middle-pressure roll presses. According to the invention, the milled material is gradually pre-formed, pre-milled and calibrated as to height and finally after-milled, whilst thrust of milling rolls in separate steps is increasing and dimension of rest slots are, on the contrary, gradually decreasing. Further subject of the invention is a definition of advantageous choice of material properties, entering different phases of milling, expressed either in stage of their grindability and either in range of their grain size.

Description

Method for milling of material with large range of grindability
Technical field of the invention
The invention deals with a method for milling of material with different grain size and/or with different range of grindability from 30 up to 90 according to Hargrowe (Hg) in more, mutual consequential milling steps, with using of middle-pressure roll presses.
The prior art
In present practice, one of necessary steps, which must be carried out to produce the fine crushed material, possibly fine powder, from originally differently grained materials or their mixtures, is the procedure of milling. During this process, the procedures are used, where the milling process is carried out in well-known facilities, advantageously in roller mills in connection with technologically related sorting mechanisms, as are fixed screens, air separators and so on and with mechanisms for transfer of milled material among separate milling, possible sorting stages.
A disadvantage of the present procedures is, that during concurrent milling of several components with different value of grindability, for example in vertical roller mills, the components with higher grindability are over-milled and the components with lower grindability are under-milled. Than, it is necessary to repeat the milling of significant part of under-milled components. Such milling processes necessarily cause higher consumption of energies, what results in lower specific output of the milling system. The aim of the invention
Above mentioned disadvantages of recent procedures are eliminated to a large extent by a subject of the invention - method for milling of material with different grain size and/or with different range of grindability from 30 up to 90 according to Hargrowe
(Hg) in more, mutual consequential milling steps, with using of middle-pressure roll presses.
Essence of the invention is, that milled material is gradually in the first milling step formed, in the second milling step it is pre-milled and calibrated as to height and in the third milling step it is after-milled, while the thrust of milling rolls is in separate milling steps gradually increasing and dimensions of rest slots are in separate milling steps gradually decreasing. According to this invention, the value of thrust of milling rolls is variable at least during one milling step.
Further essence of the invention is, that into the first step, at least two materials with the worst grindability are lead, while advantageously the grain size of at least of 50 % of volume of milled material is lower than its maximal grain size.
Further essence of the invention is, that at least between the first and the second milling step, further material is added to the milled material and that type and/or grindability of added material is different from grindability of admission milled material, advantageously material with lower grindability, than is that of material in previous step.
Finally, the essence of the invention is, that between the two milling steps the material is added, which was taken from the following step of milling.
Since the procedure is according to the invention divided into three separate, mutually functionally defined steps, it is possible to adjust the operating conditions in the first one, so that the material with bad grindability, possibly mixture of such materials, is processed preferentially, efficiently from the functional and economical point of view. According to the invention, it is possible advantageously to dose additionally materials with better grindability to further milling step, possibly materials with lower grain size. According to the invention, it is also possible advantageously to return a part of material, pre-milled in some milling step, for further processing into some of the previous steps and so to reach economically efficient and required re- milling or after-milling of desirable part of the milled material.
Summary of Figs on the drawings
Possible variants of methods for milling according to the invention are illustrated in block diagram on enclosed drawing, where on Fig.l the algorithm for milling of one type of material is given, on Fig.2 the algorithm for milling of materials with different grain size and grindability, which are gradually added and Fig.3 and 4 variant algorithms with return cycle.
Examples of embodiment of the invention
Examples of realisation of method for milling according to the invention are described in following examples and are also documented in block diagram on related Figtures.
Example 1 Method of milling according to the invention is in this example used for milling of material with practically the same grindability, for example cement clinker, after its exit from rotary kiln followed by inserted cooler. It is dealing with a material with middle grindability (Hg 80), but with significant different grain size, usually in the range from 0,1 to 45 mm. The cement clinker is according to Fig. 1 collected in the reservoir 4, from there it is through the piping 40 lead to the milling bodies of the first used milling stage 1, for example in form of a roll middle-pressure press of standard construction, with the rest slot adjusted to 27 mm. There, supplied cement clinker is pre-formed, especially larger admission grains are being broken.
In the first milling stage 1, the pre-formed cement clinker is transferred by the means of the first transport element 10 to the second milling stage 2, for example again to a middle-pressure press, its not illustrated operating slot is adjusted on value of 15 mm, e.g. lower than that in the previous step and on the contrary, thrust of the milling roll is higher. In this phase of milling, the pre-formed cement clinker, which already doesn't contain grains of significantly different size, is pre-milled and simultaneously calibrated as to height, so that a layer of practically homogenous material, as to grain size and compactness, is produced. The material is than transferred by the means of the second transport element 20 to the third milling stage 3. The operating slot of this stage is adjusted on the value of 10 mm, thrust of the milling roll is on the contrary even higher than the thrust in the previous milling stage. Here, the material is after-milled to the final requested size and the result product is through the outlet 30 lead towards the further technological step.
In case, that in final phase, e.g. on outlet of the third milling stage 3, the milled cement clinker is not sufficiently fine in all its volume and if its contains also certain fraction of undesirable higher grain size, a sorting system 6 is inserted according to Fig. 4 after the outlet 30 from the third milling stage 3, the system contains a separator 60, consisting for example of suitable chosen vibrating screen, air separator and so on. Sufficiently finely milled cement clinker passes through the separator 60 and is lead through the outlet 61 towards further technological step. Separated undesirable coarser fraction is through the discharge 62 and connected return transport element 620, for example a transporter, lead to the additional reservoir 51 and from there through the piping 510 and the first transport element 10 back to the second milling stage 2.
Example 2
Procedure according to the invention is used for preparation of mixed cement, which consists of 70% till 94% of mixture of cement clinker with average grindability of 75 Hg and with predominantly higher share of grains with larger dimensions, of 6% till 35% of slag with average grindability of 35 Hg, which has larger share of grains with small dimensions and of 5% of soft gypsum with average grindability of 95 Hg.
Example of procedure of milling of above mentioned components is illustrated in variants on Fig.2 and is as follows. The first milled component is the cement clinker, dosed from the reservoir 4 through the piping 40 to the first milling stage 1. The slag is dosed into the second milling stage 2 from the additional reservoir 51, e.g. the mixture of slag and cement clinker is entering it. The gypsum with the best grindability is dosed from the additional reservoir 52' through the piping 520 to the third milling stage 3 together with pre-milled mixture of slag and cement clinker.
Example 3
Procedure according to this example is a variant of preparation of mixed cement in composition according to previous example.
The first two materials, e.g. cement clinker and slag, are stored in the first reservoir 41 and the second reservoir 42, as is illustrated on Fig.3, from there, they are through the pipings 410 and 420 dosed into the common reservoir 4 and consequently through the piping 40 lead to the first milling stage 1 with relatively large operating slot and with low thrust of not illustrated milling roll. The remaining component of prepared mixed cement, e.g. soft gypsum, is through the additional reservoir 51 and to it connected piping 510 dosed into both first admission materials, which were pre-formed before in the previous - the first - milling stage 1, namely after their transport by the means of the first transport element 10 to the second milling stage 2.
In the second milling stage 2, all three components of prepared mixed cement are already together pre-milled, calibrated as to height and consequently by the second transport element 20 they are lead to the final third milling stage 3 and from there, after after-milling, they are through the outlet 30 lead towards further technological step.
As is illustrated on Fig.3, considering the fact that it is dealing with milling of three components with significantly different mechanical properties, the additional sorting system 21 is advantageously inserted into the milling line yet before the final phase of after-milling. Its separator 210 separates undesirable, so far insufficiently milled material, which exits the second milling stage 2 and it also transfers sufficiently fine fractions through the transport element 211 to the third milling stage 3. Possible coarser under-milled fraction is, on the contrary, by the return transport element 220 returned to the second milling stage 2, namely through the additional reservoir 51 or directly by the means of the first transport element 10, as is illustrated on Fig.3 in broken line.
Example 4
This example describes other variant of method for preparation, in this case of blast furnace cement, which consists of mixture of 65% to 80% of blast furnace slag, 20% to 35% of cement clinker and 5% of gypsum, namely according to the procedure illustrated on Fig.4.
The first milled component is a slag dosed from the reservoir 4 through the piping 40 into the first milling stage. Cement clinker and gypsum with lower grindability is dosed from the additional reservoir 51 to the second milling stage 2 together with slag, exiting the first milling stage 1. Mixture of all three components, necessary for preparation of the blast furnace cement, is than dosed by the means of the second transport element 20 to the third milling stage 3 for after-milling and it exits it through the outlet 30 towards further technological step. Possible application of the sorting system 6 was described in connection with example 1.
Practical applicability in industry
Method for milling of materials with different grain size and large range of grindability according to the invention can be advantageously used especially for milling of recycled matters, cement clinker with admixture of slag, puzzolan, ash and so on, possibly for milling of two or more types of minerals with recycling of fractions and during fining of mixtures.

Claims

Claims
1. The method for milling of material with different grain size and/or with different range of grindability from 30 up to 90 according to Hargrowe (Hg) in more, mutual consequential milling steps, with using of middle-pressure roll presses, charactezized by that the milled material is gradually pre-formed in the first milling step, in the second milling step it is pre-milled and calibrated as to height and in the third milling step it is after-milled, whilst thrust of the milling rolls is in separate milling steps gradually increasing and dimensions of the rest slots is in separate steps gradually decreasing.
2. The method for milling of materials with different grain size according to the claim 1, charactezized by that the value of thrust of the milling roll is at least in one milling step periodically variable.
3. The method for milling of materials with different grain size according to the claim 1 or 2, charactezized by that at least two materials with the worst grindability are supplied to the first step.
4. The method for milling of materials with different grain size according to some of the claims 1 to 3, charactezized by that the grain size of at least of 50% of volume of milled material is lower that its maximal grain size.
5. The method for milling of materials with different grain size according to some of the claims 1 to 4, charactezized by that at least between the first and the second milling step, further material is added to the milled material.
6. The method for milling of materials with different grain size according to the claim 5, charactezized by that the type and/or grindability of added material is different from the grindability of admission milled materials.
7. The method for milling of materials with different grain size according to the claim 6, charactezized by that grindability of added material is lower than the grindability of material in the previous step.
8. The method for milling of materials with large range of grindability according to some of the claims 5 to 7, charactezized by that between the two milling steps, material is added, which was taken from following step of milling.
PCT/CZ2000/000014 1999-03-18 2000-03-14 Method for milling of material with large range of grindability Ceased WO2000056457A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
BR0010773-5A BR0010773A (en) 1999-03-18 2000-03-14 Method for grinding materials with a wide range of crushing capacity
SK1417-2001A SK284706B6 (en) 1999-03-18 2000-03-14 Method for milling of material with large range of grindability

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CZ1999949A CZ292488B6 (en) 1999-03-18 1999-03-18 Process for grinding materials of different grain size
CZPV949-99 1999-03-18

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WO2000056457A1 true WO2000056457A1 (en) 2000-09-28

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CZ (1) CZ292488B6 (en)
SK (1) SK284706B6 (en)
WO (1) WO2000056457A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009043510A3 (en) * 2007-09-29 2009-06-18 Holcim Technology Ltd Method for the production of portland slag cement and blast furnace cement
CN117181412A (en) * 2023-08-31 2023-12-08 华南理工大学 A method for preparing composite mineral admixtures using multi-stage tandem mills

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2733866A (en) * 1956-02-07 bernard
DE1796963U (en) * 1958-05-24 1959-10-01 Esch Werke Kg ROLLER CRUSHER FOR THE PRODUCTION OF CRASHED MATERIAL WITH A LOW FINE GRAIN CONTENT.
US4592512A (en) * 1983-04-19 1986-06-03 Klockner-Humboldt-Deutz Ag Method and apparatus for the common grinding of two or more brittle materials having different grinding properties
DE3823929A1 (en) * 1987-08-11 1989-02-23 Smidth & Co As F L Method and apparatus for roll-crushing and -grinding or for mineral substances
US4840315A (en) * 1987-06-10 1989-06-20 Klockner-Humboldt-Deutz Aktiengesellschaft Method and installation for a continuous pressure communution of brittle grinding stock
WO1994022781A1 (en) * 1993-03-27 1994-10-13 Rüdersdorfer Zement Gmbh Method and device for producing a binder
US5375779A (en) * 1993-12-20 1994-12-27 Modern Process Equipment, Inc. Process for grinding limestone to predetermined particle size distribution
EP0715892A1 (en) * 1994-12-07 1996-06-12 Krupp Polysius Ag Method and plant for the grinding together of two or more substances of different grindability
JPH10265782A (en) * 1997-03-26 1998-10-06 Nisshin Steel Co Ltd Production of coke for producing sintered ore and device therefor

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2733866A (en) * 1956-02-07 bernard
DE1796963U (en) * 1958-05-24 1959-10-01 Esch Werke Kg ROLLER CRUSHER FOR THE PRODUCTION OF CRASHED MATERIAL WITH A LOW FINE GRAIN CONTENT.
US4592512A (en) * 1983-04-19 1986-06-03 Klockner-Humboldt-Deutz Ag Method and apparatus for the common grinding of two or more brittle materials having different grinding properties
US4840315A (en) * 1987-06-10 1989-06-20 Klockner-Humboldt-Deutz Aktiengesellschaft Method and installation for a continuous pressure communution of brittle grinding stock
DE3823929A1 (en) * 1987-08-11 1989-02-23 Smidth & Co As F L Method and apparatus for roll-crushing and -grinding or for mineral substances
WO1994022781A1 (en) * 1993-03-27 1994-10-13 Rüdersdorfer Zement Gmbh Method and device for producing a binder
US5375779A (en) * 1993-12-20 1994-12-27 Modern Process Equipment, Inc. Process for grinding limestone to predetermined particle size distribution
EP0715892A1 (en) * 1994-12-07 1996-06-12 Krupp Polysius Ag Method and plant for the grinding together of two or more substances of different grindability
JPH10265782A (en) * 1997-03-26 1998-10-06 Nisshin Steel Co Ltd Production of coke for producing sintered ore and device therefor

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN vol. 1999, no. 01 29 January 1999 (1999-01-29) *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009043510A3 (en) * 2007-09-29 2009-06-18 Holcim Technology Ltd Method for the production of portland slag cement and blast furnace cement
CN117181412A (en) * 2023-08-31 2023-12-08 华南理工大学 A method for preparing composite mineral admixtures using multi-stage tandem mills

Also Published As

Publication number Publication date
SK284706B6 (en) 2005-09-08
SK14172001A3 (en) 2002-01-07
CZ9900949A3 (en) 2000-11-15
CZ292488B6 (en) 2003-10-15
BR0010773A (en) 2002-04-09

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