EP1082174B1 - Mahltrocknung von zellulose-derivaten, insbesondere methyl-zellulose - Google Patents
Mahltrocknung von zellulose-derivaten, insbesondere methyl-zellulose Download PDFInfo
- Publication number
- EP1082174B1 EP1082174B1 EP99924882A EP99924882A EP1082174B1 EP 1082174 B1 EP1082174 B1 EP 1082174B1 EP 99924882 A EP99924882 A EP 99924882A EP 99924882 A EP99924882 A EP 99924882A EP 1082174 B1 EP1082174 B1 EP 1082174B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- air
- product
- milling
- turbulence mill
- mill
- 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.)
- Expired - Lifetime
Links
- 229920002678 cellulose Polymers 0.000 title claims description 15
- 239000001913 cellulose Substances 0.000 title claims description 14
- 238000001035 drying Methods 0.000 title claims description 11
- 229920000609 methyl cellulose Polymers 0.000 title description 4
- 239000001923 methylcellulose Substances 0.000 title description 4
- 239000003570 air Substances 0.000 claims description 26
- 238000000034 method Methods 0.000 claims description 18
- 238000003801 milling Methods 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 239000012080 ambient air Substances 0.000 claims description 4
- 238000000227 grinding Methods 0.000 description 18
- 235000010980 cellulose Nutrition 0.000 description 12
- 235000010981 methylcellulose Nutrition 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000013024 troubleshooting Methods 0.000 description 1
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
- B02C13/00—Disintegrating by mills having rotary beater elements ; Hammer mills
- B02C13/14—Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/18—Adding fluid, other than for crushing or disintegrating by fluid energy
- B02C23/24—Passing gas through crushing or disintegrating zone
- B02C23/26—Passing gas through crushing or disintegrating zone characterised by point of gas entry or exit or by gas flow path
Definitions
- Air vortex mills of this type are, for example from EP-A-226 900 and from the brochure "Grinding and Drying Plant “from Altenburger Maschinen KG Jiffering & Co.
- Cellulose is usually manufactured and modified in reactors and then comes as wet cellulose pulp in the next process step.
- a free-flowing powder of Methyl cellulose In one step, a free-flowing powder of Methyl cellulose.
- the cellulose is typically in the wet state, moisture content 60 - 70%, but also 80% are possible and more than wet product in a flow of cold air into the ULTRA-ROTOR.
- the hot air is first fed into the upper grinding zones and the product is then dried there.
- water can be injected in the lower area of the rotor. This further increases the bulk weight. Through the water injection it is achieved that the product is sufficient during the grinding phase stays moist and cool.
- Both fine cellulose, grain size 63 to 150 my, and coarser, rather celluloses intended for consumption, grain size 200 to 800 my, can be ground and dried with a high bulk density.
- each highly schematically an air vortex mill 1 show with their drive motor 2.
- the one to be ground and / or to be dried Product usually passes through such mills 1 from bottom to top. Because of the high flow velocities is the duration of the Product in the mill only a few seconds (e.g. 1 to 2 seconds).
- FIG 1 shows an air vortex mill according to the prior art. Below the lower grinding stage (grinding stages are only shown in Figure 3) their inlet 3. The product leaves the mill through the above the Outlet 4 located at this outlet 4 only close in Figure 3 shown devices, usually cyclones, the separation of the product from the air flow.
- FIG. 2 shows an air vortex mill 1 in which the grinding and drying of Cellulose derivatives carried out according to the inventive method becomes.
- the product is fed to inlet 3 together with ambient air. This takes place at the level of the lower and middle grinding stages or zones Shred the product when wet and at relatively low temperatures (around ambient temperature) instead.
- the air vortex mill 1 equipped with an inlet 5. It is located above the product inlet 3 and flows into the mill 1 at a height in which essentially the crushing process takes place. About the inlet 5 can be water be injected to get the product wet during the crushing process and keep it cool.
- FIG. 3 shows an air vortex mill 1 with seven grinding stages 8.
- the inlet 3 ambient air and product are supplied.
- product can also be added up to the level of the second grinding stage (inlet 7).
- the warm or hot air - e.g. with a temperature of 180 to 220 ° C - is only at the level of the upper stages (in the illustrated embodiment at the level of the sixth stage). This area essentially takes place the drying of the product takes place.
- a residual moisture of less than 5% H2O is aimed for. Should this be in the upper two levels are not reached, there is the possibility to increase the number of stages of the air vortex mill.
- a dryer of any kind downstream of the outlet 4 the residual moisture can be set to the desired degree.
- a dryer 9 connected to the outlet 4 schematically shown. This is followed by a cyclone system 10 known per se to separate product and air.
Landscapes
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Crushing And Grinding (AREA)
Description
Claims (11)
- Verfahren zum Mahlen und Trocknen von Zellulose-Derivaten in einer Luftwirbelmühle (1), dadurch gekennzeichnet, daß das Produkt in nassem Zustand in die Luftwirbelmühle (1) gefördert wird, daß es in den ersten bzw. unteren Mahlzonen (8) der Luftwirbelmühle (1) als nasses Produkt kalt feingemahlen wird und daß der Trocknung dienende Warm-/ Heißluft erst weiteren, sich an die ersten Mahlzonen anschließenden Mahlzonen zugeführt wird.
- Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß im Bereich der unteren bis mittleren Mahlzonen (8) Wasser eingedüst wird.
- Verfahren nach Anspruch 2, dadurch gekennzeichnet, daß an mehreren Stellen (5, 5') Wasser eingedüst wird.
- Verfahren nach Anspruch 1, 2 oder 3, dadurch gekennzeichnet, daß Warm-/Heißluft in Höhe der oberen Mahlzonen (8) zugeführt wird.
- Verfahren nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, daß das Produkt und Umgebungsluft über einen unterhalb der untersten Mahlzone (8) gelegenen Einlaß (3) zugeführt werden.
- Verfahren nach Anspruch 5, dadurch gekennzeichnet, daß Produkt auch noch bis zur Höhe der zweiten Mahlzone (8) zugeführt wird.
- Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß die Zellulose mit einem Feuchtigkeitsgehalt von 60 bis 80%, vorzugsweise 60 bis 70%, als nasses Produkt in einem Luftstrom in den unteren Bereich einer von unten nach oben durchströmten Luftwirbelmühle (1) eingeführt wird, daß in die unteren bis mittleren Mahlzonen (8), in denen im wesentlichen der Zerkleinerungsprozeß stattfindet, Wasser zugeführt wird und daß in die oberen Mahlzonen (8), in denen im wesentlichen der Trocknungsprozeß stattfindet, Warm-/Heißluft zugeführt wird.
- Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß das Produkt in einem der Luftwirbelmühle nachgeordneten Trockner (9) nachgetrocknet wird.
- Luftwirbelmühle (1) zur Durchführung des Verfahrens nach einem der vorhergehenden Verfahrensansprüche, dadurch gekennzeichnet, daß sie im unteren Bereich mit einem Produkt-/Luft-Einlaß (3), im unteren bis mittleren Bereich mit einem Wassereinlaß (5, 5') und im oberen Bereich mit einem Warm-/Heiß-Luft-Einlaß (6) ausgerüstet ist.
- Luftwirbelmühle (1) nach Anspruch 9, dadurch gekennzeichnet, daß an ihren Auslaß (4) ein Trockner (9) angeschlossen ist, dem ein Zyklon-System (10) nachgeordnet ist.
- Luftwirbelmühle (1) nach Anspruch 9 oder 10, dadurch gekennzeichnet, daß sie vom Typ ULTRA-ROTOR ist.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19823563A DE19823563A1 (de) | 1998-05-27 | 1998-05-27 | Mahltrocknung von Zellulose-Derivaten, insbesondere Methl-Zellulose |
DE19823563 | 1998-05-27 | ||
PCT/EP1999/003077 WO1999061157A1 (de) | 1998-05-27 | 1999-05-05 | Mahltrocknung von zellulose-derivaten, insbesondere methyl-zellulose |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1082174A1 EP1082174A1 (de) | 2001-03-14 |
EP1082174B1 true EP1082174B1 (de) | 2002-02-13 |
Family
ID=7869001
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP99924882A Expired - Lifetime EP1082174B1 (de) | 1998-05-27 | 1999-05-05 | Mahltrocknung von zellulose-derivaten, insbesondere methyl-zellulose |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP1082174B1 (de) |
DE (2) | DE19823563A1 (de) |
WO (1) | WO1999061157A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007090599A1 (de) * | 2006-02-10 | 2007-08-16 | Altenburger Maschinen Jäckering GmbH | Vorrichtung und verfahren zur einspeisung von feuchten und/oder klebrigen produkten, insbesondere zellulose, in eine luftwirbelmühle |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE20021758U1 (de) * | 2000-12-22 | 2002-05-08 | Sniehotta, Michael, Dipl.-Ing., Dipl.-Geol., 45699 Herten | Prallmühle mit Schlagwerkzeugen an einem motorgetriebenen Rotor |
DE102005032248B4 (de) * | 2005-07-09 | 2009-04-23 | Tronox Pigments Gmbh | Titandioxidpigmentherstellung unter Verwendung einer Luftwirbelmühle |
DE102006033791A1 (de) * | 2006-07-19 | 2008-01-24 | Prokon Nord Energiesysteme Gmbh | Verbesserte Verfahren zur Herstellung von Ethanol, Gluten und und Kleie aus Getreide |
DE102010009894A1 (de) | 2010-03-02 | 2011-09-08 | Rolf Schatz | Rotor-Mahlwerkzeug für Rotorprallmühlen |
DE102014015964A1 (de) | 2014-10-31 | 2016-06-16 | Pallmann Maschinenfabrik Gmbh & Co. Kg | Vorrichtung und Verfahren zum Bearbeiten von Aufgabegut |
DE102022132971A1 (de) | 2022-12-12 | 2024-06-13 | PWA recycling concept GmbH | Vorrichtung zum Zerkleinern und/oder Aufbereiten von Material, Anordnung und Verfahren |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3543370A1 (de) * | 1985-12-07 | 1987-06-11 | Jackering Altenburger Masch | Muehle mit mehreren mahlstufen |
DE3811910C2 (de) * | 1988-04-09 | 1997-04-10 | Mahltechnik Goergens Gmbh | Mühle und Verfahren zum gleichzeitigen Mahlen und Trocknen eines feuchten Produkts |
DE3839831A1 (de) * | 1988-11-25 | 1990-05-31 | Hoechst Ag | Verfahren und vorrichtung zur produktschonenden mahlung und gleichzeitigen trocknung von feuchten celluloseethern |
DE19641781A1 (de) * | 1996-10-10 | 1998-04-16 | Clariant Gmbh | Verfahren und Vorrichtung zum gleichzeitigen Mahlen und Trocknen eines feuchten Celluloseether enthaltenden Mahlgutes |
-
1998
- 1998-05-27 DE DE19823563A patent/DE19823563A1/de not_active Withdrawn
-
1999
- 1999-05-05 DE DE59900869T patent/DE59900869D1/de not_active Expired - Lifetime
- 1999-05-05 EP EP99924882A patent/EP1082174B1/de not_active Expired - Lifetime
- 1999-05-05 WO PCT/EP1999/003077 patent/WO1999061157A1/de active IP Right Grant
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007090599A1 (de) * | 2006-02-10 | 2007-08-16 | Altenburger Maschinen Jäckering GmbH | Vorrichtung und verfahren zur einspeisung von feuchten und/oder klebrigen produkten, insbesondere zellulose, in eine luftwirbelmühle |
Also Published As
Publication number | Publication date |
---|---|
DE59900869D1 (de) | 2002-03-21 |
DE19823563A1 (de) | 1999-12-02 |
EP1082174A1 (de) | 2001-03-14 |
WO1999061157A1 (de) | 1999-12-02 |
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