DE19823563A1 - Mill drying of cellulose derivatives, especially methyl cellulose - Google Patents

Mill drying of cellulose derivatives, especially methyl cellulose

Info

Publication number
DE19823563A1
DE19823563A1 DE19823563A DE19823563A DE19823563A1 DE 19823563 A1 DE19823563 A1 DE 19823563A1 DE 19823563 A DE19823563 A DE 19823563A DE 19823563 A DE19823563 A DE 19823563A DE 19823563 A1 DE19823563 A1 DE 19823563A1
Authority
DE
Germany
Prior art keywords
cellulose
drying
product
stages
grinding
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.)
Withdrawn
Application number
DE19823563A
Other languages
German (de)
Inventor
Michael Andreae-Jaeckering
Guenter Werry
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.)
Altenburger Maschinen GmbH
Original Assignee
Altenburger Maschinen GmbH
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 Altenburger Maschinen GmbH filed Critical Altenburger Maschinen GmbH
Priority to DE19823563A priority Critical patent/DE19823563A1/en
Priority to EP99924882A priority patent/EP1082174B1/en
Priority to DE59900869T priority patent/DE59900869D1/en
Priority to PCT/EP1999/003077 priority patent/WO1999061157A1/en
Publication of DE19823563A1 publication Critical patent/DE19823563A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C13/00Disintegrating by mills having rotary beater elements ; Hammer mills
    • B02C13/14Disintegrating by mills having rotary beater elements ; Hammer mills with vertical rotor shaft, e.g. combined with sifting devices
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C23/00Auxiliary 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
    • B02C23/18Adding fluid, other than for crushing or disintegrating by fluid energy
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C23/00Auxiliary 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
    • B02C23/18Adding fluid, other than for crushing or disintegrating by fluid energy
    • B02C23/24Passing gas through crushing or disintegrating zone
    • B02C23/26Passing gas through crushing or disintegrating zone characterised by point of gas entry or exit or by gas flow path

Landscapes

  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Crushing And Grinding (AREA)

Abstract

Method for milling and drying cellulose derivatives in an air blast mill (1), wherein the product is fed to the air blast mill (1) in a wet state, the wet product is fine milled cold in the first or lower milling areas (8) of the air blast mill (1) and then fed to the other milling areas (steps) attached to the first milling areas (steps) for exposure to the warm/hot air for drying.

Description

1) Ausgangssituation1) Initial situation

Für die Vermahlung bzw. gleichzeitige Mahlung und Trocknung von Zellulose-Derivaten werden Luftwirbelmühlen vom Typ ULTRA- ROTOR seit vielen Jahren erfolgreich eingesetzt.For grinding or simultaneous grinding and drying of Cellulose derivatives are ULTRA- ROTOR has been used successfully for many years.

Zellulose wird üblicherweise in Reaktoren hergestellt und modifiziert und kommt dann als nasse Zellulose-Pulpe in den nächsten Verfahrens­ schritt.Cellulose is usually produced and modified in reactors and then comes as wet cellulose pulp in the next process step.

Hier wurde früher die Zellulose mit konventionellen Methoden getrock­ net und anschließend oder vorher auf Kugelmühlen mit hohem Aufwand zerkleinert.In the past, cellulose was dried using conventional methods net and then or beforehand on ball mills with great effort crushed.

Auch andere Verfahrenstechniken wurden eingesetzt.Other process technologies have also been used.

In den letzten Jahren wurden mehr und mehr Mahltrocknungsanlagen vom Typ ULTRA-ROTOR für die gleichzeitige Mahlung und Trocknung von Zellulose, insbesondere Methyl-Zellulose (MC) eingesetzt.In recent years there have been more and more grinding drying plants ULTRA-ROTOR type for simultaneous grinding and drying of cellulose, especially methyl cellulose (MC) used.

Hierbei erreichte man in einem Arbeitsschritt ein rieselfähiges Pulver von Methyl-Zellulose.A free-flowing powder was obtained in one step of methyl cellulose.

Neben anderen wichtigen Eigenschaften (z. B. Korngröße, Restfeuchte, Rieselfähigkeit) war immer wieder das Schüttgewicht der Zellulose von großer Bedeutung.In addition to other important properties (e.g. grain size, residual moisture, Free flowing) was the bulk density of the cellulose from  great importance.

Üblicherweise erreichte man Schüttgewichte zwischen 200 und 300 g pro Liter.Bulk weights between 200 and 300 g were usually achieved per liter.

Bestimmte Anwender suchten jedoch immer nach Wegen, ein höheres Schüttgewicht für die Zellulose zu erreichen.However, certain users always looked for ways, a higher one To achieve bulk density for the cellulose.

2) Problemlösung2) problem solving

Bisher wurde Heißluft in den ULTRA-ROTOR gefördert und das Pro­ dukt wurde in den Heißluftstrom dosiert und gleichzeitig gemahlen und getrocknet, wie viele andere Produkte.So far, hot air has been fed into the ULTRA-ROTOR and the Pro product was dosed into the hot air flow and simultaneously ground and dried like many other products.

Überraschenderweise haben wir jetzt folgendes andere Verfahren ent­ wickelt:
Die Zellulose wird im nassen Zustand, Feuchtigkeitsgehalt typischer­ weise 60-70%, jedoch auch 80% sind möglich und mehr, als nasses Produkt in einen Kaltluftstrom in den ULTRA-ROTOR gefördert.
Surprisingly, we have now developed the following other procedure:
The cellulose is conveyed in the wet state, moisture content typically 60-70%, but also 80% is possible and more as a wet product in a cold air stream in the ULTRA-ROTOR.

In den unteren Mahlzonen wird das Produkt dann als nasses Produkt kalt (kalt = Umgebungsluft oder gekühlte Luft, z. B. mit Stickstoff oder CO2 gekühlt) feingemahlen, die Heißluft wird erst in den oberen Mahlzonen zugeführt und das Produkt dort dann getrocknet (siehe Skizze).The product then becomes cold as a wet product in the lower grinding zones (cold = ambient air or cooled air, e.g. with nitrogen or CO2 cooled) finely ground, the hot air is only in the upper grinding zones fed and then dried the product there (see sketch).

Durch diese Anordnung erreicht man Schüttgewichte, die deutlich über den bisher erreichten Schüttgewichten liegen und zwischen 300, 400 oder sogar mehr Gramm pro Liter liegen. With this arrangement, bulk densities are achieved that are significantly higher the bulk densities achieved so far are between 300 and 400 or even more grams per liter.  

Zusätzlich kann im unteren Bereich des Rotors Wasser eingedüst wer­ den. Hiermit wird das Schüttgewicht weiter gesteigert.In addition, water can be injected in the lower area of the rotor the. This further increases the bulk weight.

Dieses höhere Schüttgewicht ist von enormer kommerzieller und techni­ scher Bedeutung.This higher bulk density is of enormous commercial and technical importance.

Sowohl feine Zellulosen, Korngröße 63 bis 150 my, als auch gröbere, eher für den Konsumbereich bestimmte Zellulosen, Korngröße 200 bis 800 my, können so gemahlen und getrocknet werden bei hohem Schütt­ gewicht.Both fine cellulose, grain size 63 to 150 my, and coarser, celluloses, grain size 200 to 800 my, can be ground and dried with a high bulk Weight.

Sollte die gewünschte Restfeuchte nicht erreicht werden, kann in einem nachgeschalteten Trockner jedweder Art die Restfeuchte auf den ge­ wünschten Grad eingestellt werden.If the desired residual moisture is not reached, it can be done in one downstream dryer of any kind the residual moisture on the ge desired degree can be set.

Claims (2)

1. Verfahren zum Mahlen und Trocknen von Zellulose-Derivaten in einer Luftwirbelmühle vom Typ ULTRA-ROTOR, dadurch gekennzeichnet, daß das Produkt in nassem Zustand in die Luftwirbelmühle gefördert wird, daß es in den ersten Mahlzonen (-stufen) der Luftwirbelmühle als nasses Produkt kalt feingemahlen wird und daß der Trocknung dienende Warm-/Heißluft erst weiteren, sich an die ersten Mahlzonen (-stufen) anschließenden Mahlzonen (-stufen) zugeführt wird.1. A method for grinding and drying cellulose derivatives in an air vortex mill of the ULTRA-ROTOR type, characterized in that the product is conveyed into the air vortex mill in the wet state, that it is in the first grinding zones (stages) of the air vortex mill as a wet product is finely ground cold and that the hot / hot air used for drying is supplied only to further grinding zones (stages) which adjoin the first grinding zones (stages). 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß im Bereich der ersten Mahlzonen (-stufen) Wasser eingedüst wird.2. The method according to claim 1, characterized in that in the area of water is injected in the first grinding zones (stages).
DE19823563A 1998-05-27 1998-05-27 Mill drying of cellulose derivatives, especially methyl cellulose Withdrawn DE19823563A1 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
DE19823563A DE19823563A1 (en) 1998-05-27 1998-05-27 Mill drying of cellulose derivatives, especially methyl cellulose
EP99924882A EP1082174B1 (en) 1998-05-27 1999-05-05 Mill drying of cellulose derivatives, especially methylcellulose
DE59900869T DE59900869D1 (en) 1998-05-27 1999-05-05 GRIND DRYING OF CELLULOSE DERIVATIVES, IN PARTICULAR METHYL CELLULOSE
PCT/EP1999/003077 WO1999061157A1 (en) 1998-05-27 1999-05-05 Mill drying of cellulose derivatives, especially methylcellulose

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE19823563A DE19823563A1 (en) 1998-05-27 1998-05-27 Mill drying of cellulose derivatives, especially methyl cellulose

Publications (1)

Publication Number Publication Date
DE19823563A1 true DE19823563A1 (en) 1999-12-02

Family

ID=7869001

Family Applications (2)

Application Number Title Priority Date Filing Date
DE19823563A Withdrawn DE19823563A1 (en) 1998-05-27 1998-05-27 Mill drying of cellulose derivatives, especially methyl cellulose
DE59900869T Expired - Lifetime DE59900869D1 (en) 1998-05-27 1999-05-05 GRIND DRYING OF CELLULOSE DERIVATIVES, IN PARTICULAR METHYL CELLULOSE

Family Applications After (1)

Application Number Title Priority Date Filing Date
DE59900869T Expired - Lifetime DE59900869D1 (en) 1998-05-27 1999-05-05 GRIND DRYING OF CELLULOSE DERIVATIVES, IN PARTICULAR METHYL CELLULOSE

Country Status (3)

Country Link
EP (1) EP1082174B1 (en)
DE (2) DE19823563A1 (en)
WO (1) WO1999061157A1 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007006456A2 (en) * 2005-07-09 2007-01-18 Tronox Pigments Gmbh Production of titanium dioxide pigments using an air vortex mill
DE10161275B4 (en) * 2000-12-22 2013-01-03 Michael Sniehotta Rotor impact mill for the treatment of regrind
EP3015171A2 (en) 2014-10-31 2016-05-04 Pallmann Maschinenfabrik GmbH & Co. KG Method and device for processing feedstock

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102006006096A1 (en) * 2006-02-10 2007-08-16 Altenburger Maschinen Jäckering GmbH Apparatus and method for feeding moist and / or sticky products, in particular cellulose, in an air vortex mill
DE102006033791A1 (en) * 2006-07-19 2008-01-24 Prokon Nord Energiesysteme Gmbh Improved processes for the production of ethanol, gluten and bran from cereals
DE102010009894A1 (en) 2010-03-02 2011-09-08 Rolf Schatz Rotor grinding tool for use in rotor impact mills for fine grinding, drying or grind drying, coating or deagglomeration of wet or dry material, has integrated turbo wheel-air classifier
DE102022132971A1 (en) 2022-12-12 2024-06-13 PWA recycling concept GmbH Device for crushing and/or processing material, arrangement and method

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3543370A1 (en) * 1985-12-07 1987-06-11 Jackering Altenburger Masch MILL WITH SEVERAL GRINDINGS
DE3811910C2 (en) * 1988-04-09 1997-04-10 Mahltechnik Goergens Gmbh Mill and method for grinding and drying a moist product simultaneously
DE3839831A1 (en) * 1988-11-25 1990-05-31 Hoechst Ag METHOD AND DEVICE FOR PRODUCT-FRIENDLY GRINDING AND SIMULTANEOUS DRYING OF DAMP CELLULOSE ETHERS
DE19641781A1 (en) * 1996-10-10 1998-04-16 Clariant Gmbh Method and device for the simultaneous grinding and drying of a ground material containing moist cellulose ether

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10161275B4 (en) * 2000-12-22 2013-01-03 Michael Sniehotta Rotor impact mill for the treatment of regrind
WO2007006456A2 (en) * 2005-07-09 2007-01-18 Tronox Pigments Gmbh Production of titanium dioxide pigments using an air vortex mill
WO2007006456A3 (en) * 2005-07-09 2007-05-24 Tronox Pigments Gmbh Production of titanium dioxide pigments using an air vortex mill
EP3015171A2 (en) 2014-10-31 2016-05-04 Pallmann Maschinenfabrik GmbH & Co. KG Method and device for processing feedstock
DE102014015964A1 (en) 2014-10-31 2016-06-16 Pallmann Maschinenfabrik Gmbh & Co. Kg Apparatus and method for processing feedstock
US11090658B2 (en) 2014-10-31 2021-08-17 Pallmann Maschinenfabrik Gmbh & Co. Kg Device and method for processing of feed material

Also Published As

Publication number Publication date
EP1082174B1 (en) 2002-02-13
EP1082174A1 (en) 2001-03-14
WO1999061157A1 (en) 1999-12-02
DE59900869D1 (en) 2002-03-21

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