EP1286777B1 - Rollenpresse - Google Patents
Rollenpresse Download PDFInfo
- Publication number
- EP1286777B1 EP1286777B1 EP01900220A EP01900220A EP1286777B1 EP 1286777 B1 EP1286777 B1 EP 1286777B1 EP 01900220 A EP01900220 A EP 01900220A EP 01900220 A EP01900220 A EP 01900220A EP 1286777 B1 EP1286777 B1 EP 1286777B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- roller
- press
- roller press
- rollers
- bed thickness
- 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.)
- Revoked
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C4/00—Crushing or disintegrating by roller mills
- B02C4/28—Details
- B02C4/42—Driving mechanisms; Roller speed control
Definitions
- the present invention relates to a roller press comprising two oppositely rotating rollers which are driven by means of a drive system.
- Roller presses are known i.a. from international patent application No. WO 92/00141 on from the European patent application EP 0 084 383 A2 .
- roller presses may entail operational problems manifested by torsional vibrations of the rollers. This may result in substantial torque variations in the drive system and, as a consequence hereof, overloading of the gear unit or cut-out of the safety coupling or main motor.
- this tendency seems to increase with an increase in the roller peripheral velocity, and, therefore, it is often a limiting factor for the roller peripheral velocity with which a roller press can be operated.
- a frequently attempted method for enhancing the capacity of a roller press installation relates to enhancements of the roller pheripheral velocity. For previously known roller presses this seems achievable only up to a roller peripheral speed of about 1.5 m/s.
- roller press it will thus be possible to design the roller press so that it can be driven at roller peripheral velocities in excess of 1.5 m/s. This is due to the fact that the roller press is designed with the lowest natural frequency, which for a given roller diameter and a given roller velocity exceeds the excitation frequency calculated on the basis of the above formula.
- the roller press according to the invention can thus be utilized in connection with methods for grinding of particulate material, such as cement raw materials, cement clinker and similar materials, where the roller peripheral velocity is greater than 1.5 m/s. According to the invention it is preferred that the roller peripheral velocity is greater than 5 m/s, preferably greater than 8 m/s. It is also preferred that the particulate material be subjected to a pressure of more than 50 MPa by subjecting the material once to pressing action between the rollers of the roller press.
- roller press comprising two rollers 1 and 2.
- Particulate material which is to be ground in the roller press is directed from the top via a not shown shaft into the gap between the rollers.
- the material being fed to the roller press behaves more or less like a liquid as it is drawn into the gap between the rollers by the roller surfaces. At a nip point the material is subjected to compaction until it behaves as a solid.
- the angle ⁇ between the roller surfaces at the nip point on each roller is termed the nip angle, and the angle ⁇ measured between the horizontal plane through the roller axis and the nip point is termed the nip angle.
- the quantity of material which passes through the rollers is the product of the grinding bed thickness H , roller width W , the roller peripheral velocity V and the density of the pressed material ⁇ out .
- the density increases as the material is subjected to pressing action and compaction between the two rollers.
- the ratio F between the density of the pressed material ⁇ out and the bulk density of the feed ⁇ in constitutes the compaction ratio.
- F ⁇ out ⁇ in
- the tendency towards torsional vibrations in the roller shafts occurs in case of uneven feeding to the press, choke feeding of the roller press or feeding of overly fine material to the roller.
- the grinding bed thickness is determined primarily by the feed characteristics, the feed rate and, in part, by the roller surfaces. If the particle distribution and the composition of material being fed to the press is constant and if the feed rate is constant, the grinding bed thickness will be constant. In connection with roller press grinding it will be possible to measure the maximum grinding bed thickness for a given type of feed. This constant maximum grinding bed thickness is achievable only in case of extremely low roller velocity ( ⁇ 0.05 m/s) and optimization of shaft feeding.
- Excitation of the roller occurs in connection with deviations from steady-state operation.
- the grinding bed thickness is less than the maximum grinding bed thickness.
- the greater the sudden deviation from the maximum grinding bed thickness the greater the excitation intensity of the system.
- the system can be made to oscillate at its natural torsional frequency.
- the excitation mechanism relates to the time it takes the material to pass through the compaction zone between the rollers, i.e. the angle of engagement ⁇ , the length L of the nip zone and the roller peripheral velocity.
- the frequency F is 1/T.
- the excitation frequency is the frequency achieved when the grinding bed thickness H is increased to a maximum
- the above-mentioned equation can be used to estimate the excitation frequency for a given roller diameter at a given roller velocity.
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Crushing And Grinding (AREA)
Claims (4)
- Walzenpresse, die zwei gegenläufig rotierende Walzen (1, 2) umfasst, die mittels eines Antriebssystems angetrieben werden, dadurch gekennzeichnet, dass das Antriebssystem entworfen ist, so dass eine niedrigste normale Drehfrequenz νsystem größer ist als eine berechnete Frequenz, die durch die Formel ausgedrückt wird:
wobeiν WalzengeschwindigkeitD WalzendurchmesserH Mahlbettdickeρ out Dichte des gepressten Kuchens / Blocksρ in Bulk-Gewicht der Einspeisung in die Walzenpresse - Verfahren zum Mahlen von partikulärem Material wie zum Beispiel Zementrohmaterialien, Zementklinker und ähnlichen Materialien in einer Walzenpresse gemäß Anspruch 1 dadurch gekennzeichnet, dass die Walzenumfangsgeschwindigkeit größer als 1,5 m/s ist.
- Verfahren gemäß Anspruch 2, dadurch gekennzeichnet, dass die Walzenumfangsgeschwindigkeit größer als 5 m/s, bevorzugt größer als 8 m/s, ist.
- Verfahren gemäß Anspruch 2 oder 3, dadurch gekennzeichnet, dass das partikuläre Material einem Druck von mehr als 50 MPa ausgesetzt wird, indem es einmalig einem Pressvorgang zwischen den Walzen der Walzenpresse ausgesetzt wird.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DK200000646A DK173915B1 (da) | 2000-04-17 | 2000-04-17 | Valsepresse og fremgangsmåde til formaling af partikelformet materiale |
DK200000646 | 2000-04-17 | ||
PCT/IB2001/000058 WO2001078898A1 (en) | 2000-04-17 | 2001-01-19 | Roller press |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1286777A1 EP1286777A1 (de) | 2003-03-05 |
EP1286777B1 true EP1286777B1 (de) | 2008-06-25 |
Family
ID=8159438
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP01900220A Revoked EP1286777B1 (de) | 2000-04-17 | 2001-01-19 | Rollenpresse |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP1286777B1 (de) |
AU (1) | AU2001223916A1 (de) |
DE (1) | DE60134548D1 (de) |
DK (1) | DK173915B1 (de) |
ES (1) | ES2309046T3 (de) |
WO (1) | WO2001078898A1 (de) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7122155B2 (en) | 2002-07-16 | 2006-10-17 | Mcgill University | Electron microscopy cell fraction sample preparation robot |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3302176A1 (de) * | 1983-01-24 | 1984-07-26 | Klöckner-Humboldt-Deutz AG, 5000 Köln | Verfahren und anlage zur kontinuierlichen druckzerkleinerung sproeden mahlgutes |
-
2000
- 2000-04-17 DK DK200000646A patent/DK173915B1/da not_active IP Right Cessation
-
2001
- 2001-01-19 WO PCT/IB2001/000058 patent/WO2001078898A1/en active IP Right Grant
- 2001-01-19 DE DE60134548T patent/DE60134548D1/de not_active Revoked
- 2001-01-19 ES ES01900220T patent/ES2309046T3/es not_active Expired - Lifetime
- 2001-01-19 EP EP01900220A patent/EP1286777B1/de not_active Revoked
- 2001-01-19 AU AU2001223916A patent/AU2001223916A1/en not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
DK200000646A (da) | 2001-10-18 |
EP1286777A1 (de) | 2003-03-05 |
DK173915B1 (da) | 2002-02-18 |
WO2001078898A1 (en) | 2001-10-25 |
DE60134548D1 (de) | 2008-08-07 |
ES2309046T3 (es) | 2008-12-16 |
AU2001223916A1 (en) | 2001-10-30 |
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