EP0370181A1 - Mélangeur travaillant en continu - Google Patents

Mélangeur travaillant en continu Download PDF

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Publication number
EP0370181A1
EP0370181A1 EP89115813A EP89115813A EP0370181A1 EP 0370181 A1 EP0370181 A1 EP 0370181A1 EP 89115813 A EP89115813 A EP 89115813A EP 89115813 A EP89115813 A EP 89115813A EP 0370181 A1 EP0370181 A1 EP 0370181A1
Authority
EP
European Patent Office
Prior art keywords
housing
cutting devices
mixer
wall
knives
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.)
Granted
Application number
EP89115813A
Other languages
German (de)
English (en)
Other versions
EP0370181B1 (fr
Inventor
Paul Eirich
Werner Christen
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.)
Draiswerke GmbH
Original Assignee
Draiswerke 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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=6367805&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=EP0370181(A1) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Draiswerke GmbH filed Critical Draiswerke GmbH
Priority to AT89115813T priority Critical patent/ATE88661T1/de
Publication of EP0370181A1 publication Critical patent/EP0370181A1/fr
Application granted granted Critical
Publication of EP0370181B1 publication Critical patent/EP0370181B1/fr
Anticipated expiration legal-status Critical
Revoked legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
    • B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
    • B27N1/00—Pretreatment of moulding material
    • B27N1/02—Mixing the material with binding agent
    • B27N1/0227—Mixing the material with binding agent using rotating stirrers, e.g. the agent being fed through the shaft of the stirrer
    • B27N1/0236—Mixing the material with binding agent using rotating stirrers, e.g. the agent being fed through the shaft of the stirrer with the stirrers rotating about an horizontal axis, e.g. in consecutive casings
    • B27N1/0245—Mixing the material with binding agent using rotating stirrers, e.g. the agent being fed through the shaft of the stirrer with the stirrers rotating about an horizontal axis, e.g. in consecutive casings with a single stirrer shaft
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/62—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis comprising liquid feeding, e.g. spraying means
    • B01F27/621—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis comprising liquid feeding, e.g. spraying means the liquid being fed through the shaft of the stirrer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/21—Mixers with rotary stirring devices in fixed receptacles; Kneaders characterised by their rotating shafts
    • B01F27/2123—Shafts with both stirring means and feeding or discharging means
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
    • B01F27/70—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with paddles, blades or arms
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B01F33/83—Mixing plants specially adapted for mixing in combination with disintegrating operations
    • B01F33/833—Devices with several tools rotating about different axis in the same receptacle
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F33/00—Other mixers; Mixing plants; Combinations of mixers
    • B01F33/80—Mixing plants; Combinations of mixers
    • B01F33/836—Mixing plants; Combinations of mixers combining mixing with other treatments
    • B01F33/8361—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating
    • B01F33/83612—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating by crushing or breaking

Definitions

  • the invention relates to a mixer according to the preamble of claim 1.
  • Mixers of the generic type which are also referred to as ring-layer mixers, are known in large numbers, for example from DE-PS 20 57 594 (corresponding to US Pat. No. 3,734,471).
  • special measures have been taken in the form of mixing tools tapering towards the container wall in order to dissolve the fibers that tend to agglomerate after gluing, as described in DE-OS 24 38 818 (corresponding to US Pat. No. 4 006 887) is known.
  • these measures have not led to the desired success, that is to say a dissolution of the agglomerates.
  • the residence time of the wetted material in the mixer was increased by providing adjustable or regulated outlet flaps at the outlet, through which an adjustable or adjustable back pressure was exerted on the material in order to prolong the dissolving effect to expose the special tools. This led to considerable material caking in the outlet area, which was also not desirable.
  • the invention is based on the object of developing a mixer of the generic type in such a way that agglomerates are dissolved in a targeted and reliable manner, at the same time achieving a high throughput and a high uniformity of wetting.
  • the measures according to the invention ensure that the wetted material, which has largely formed agglomerates, is passed through the cutting devices immediately before reaching the outlet, it being ensured that each agglomerate comes into contact with a knife at least once, but preferably several times and is dissolved.
  • the wetted, non-agglomerated material particles leaving the area of the cutting devices are fed directly to the outlet and cannot agglomerate again.
  • the number of cutting devices depends on the size of the mixer and the ratio of the peripheral speed of the mixing tools the axial flow rate of the material. This ratio must be chosen so that all material particles are reliably grasped by them as they pass the cutting devices.
  • - fibrous material such as paper fibers or also wood fibers
  • powder such as lime
  • agglomerates ie agglomerations of several millimeters in diameter
  • the granules with a diameter of less than 1 mm, for example, which are specifically produced during the wetting can be retained.
  • the mixer shown in the drawing has a substantially cylindrical housing 1 which is divided in a horizontal plane which is laid through a horizontal central-longitudinal axis 2 of the housing. It consists of a semi-cylindrical housing lower part 3 and a likewise semi-cylindrical housing upper part 4, which are connected on one side by means of swivel joints 5 and which can be connected to one another on the opposite side by means of easily releasable toggle locks 6, so that after releasing these fasteners 6 which is balanced with a counterweight 7, the upper housing part 4 can easily be swung up and away from the lower part 3.
  • the housing 1 is closed at its end faces with end walls 8, 9, which also carry the lower part 3 and end in machine bearings 10, 11. These machine bearings 10, 11 are supported on a foundation 12.
  • a mixer 13 is arranged in the housing 1 concentrically to the central longitudinal axis 2, the shaft 14 of which is led out sealed through the end walls 8, 9 at both ends of the housing 1.
  • the shaft 14 is supported in shaft bearings 15, 16, which are also supported on the machine bearings 10, 11.
  • a pulley 17 is attached to it in a rotationally fixed manner, via which a drive belt 18 is guided, which in turn is guided via a belt drive pinion 19 of a drive motor 20, which is also supported and fastened on the foundation 12.
  • the housing 1 At one - in Fig. 1 right - end of the housing 1 opens into the interior 21 of a material supply nozzle 22 which is attached to the upper part 4 and - as can be seen in Fig. 2 - opens approximately tangentially into the interior 21.
  • a material outlet connection 23 opens from the interior 21 thereof, which is also arranged approximately tangentially to the interior, as can be seen in FIG. 3.
  • the housing 1 is double-walled, i.e. it has a temperature control jacket 24 through which a temperature control medium, in particular thus cooling water, but also a heating medium, can be passed.
  • a feed zone a is formed, in which feed or acceleration tools 25 are attached to the shaft 14 are.
  • feed or acceleration tools 25 consist essentially of relatively large blades 26, which are set in the axial conveying direction 27 and in the direction of rotation 28 of the mixer 13, so that they accelerate the pourable material 29 fed through the feed pipe 22 in the direction of rotation 28 and set in motion in the axial conveying direction 27.
  • the blades 26 are fastened to the shaft 14 by means of arms 30. As can be seen in FIG. 1, the blades 26 completely overlap in the axial direction; they also extend close to the inner wall 31 of the housing 1, so that there are no dead spaces in which material 29 could be deposited.
  • the mixer 13 is driven at 20- to 40-times the critical speed, so that the material 29 is already directly behind the feed pipe 22 in the form of a material ring 32 on the inner wall 31 of the housing 1, on which it is helical through the interior 21 of the Housing 1 is promoted.
  • the critical speed is understood to be the speed of the mixer 13 at which gravitational acceleration occurs at the radially outer ends of the tools.
  • a wetting zone b adjoins the feed zone a in the conveying direction 27.
  • liquid addition and mixing tools 33 are attached to the shaft 14.
  • These tools 33 can be designed as approximately cylindrical mixing arms which are brought close to the inner wall 31 and which - as can also be seen in FIG. 1 - overlap one another in the axial direction, so that also in the Wetting zone b no dead spaces can arise in which material 29 is not acted upon intensively.
  • the liquid addition and mixing tools 33 are connected to a liquid supply pipe 34 which is guided concentrically to the axis 2 through a shaft cavity 35 of the hollow shaft 14.
  • This liquid supply pipe 34 has liquid outlet openings 36 in the region of the wetting zone b. From these outlet openings 30, liquid supplied by a pump, not shown, enters the shaft cavity 35 through the supply pipe 34. Due to the high speed and the resulting centrifugal forces, this liquid becomes in flung the individual tools 33, flows through them and is discharged from them at their radially outer end in the form of finely divided liquid 37 into the material ring 32, which is also maintained in the wetting zone b by the tools 33.
  • the rotational speed of the material ring 32 in the direction of rotation 28 is approximately half the rotational speed of the tools 33 in the radially outer region.
  • the design of the liquid addition and mixing tools 33 can also be in terms of the liquid flow as described and described in DE-OS 24 38 818 (corresponding to US Pat. No. 4,006,887).
  • the wetting zone b is followed by a post-mixing zone c which extends as far as the outlet nozzle 23, that is to say approximately to the axial end of the interior 21.
  • mixing tools 38 are arranged which have the same outer structure as that of the tools 33 Chen can, but are no longer used for hydration.
  • approximately hook-shaped mixing tools 39 can also be attached, which have a cylindrical tubular, radially extending section 40 and a tapering hook section 41 which leads in the direction of rotation 28 and is bent relative to section 40 and extends close to the inner wall 31 .
  • These tools 39 can be designed in detail, for example, as shown and described in DE-OS 27 31 767 (corresponding to US Pat. No. 4,183,676).
  • the hook-shaped mixing tools 39 can also be replaced by other mixing tools, in particular those which exert an increased axial impulse or a deceleration on the material 29 by changing the angle of attack.
  • mixing tools are known for example from DE-PS 20 57 594 (corresponding to US Pat. No. 3,734,471).
  • a plurality of — in the present case four — cutting devices 44 are arranged in a common radial plane 43 to the central longitudinal axis 2. As can be seen in FIG. 4, they are each arranged at equal angular intervals, for example 90 °, and offset because of the separation of the housing 1 in a horizontal plane to this plane.
  • Each cutting device 44 has an electric motor 45 which is screwed to a holder 46 which is attached to the housing 1 and passes through it.
  • the holder 46 is penetrated by a knife shaft 47 driven by the electric motor 45, which is directed radially into the interior 21.
  • the axes 48 of the knife shafts 47 thus lie in the radial plane 43 and intersect the axis 2.
  • a plurality of knives 49, 50 are attached to each knife shaft 47 at an axial distance - based on the axes 48.
  • the knives 49 are identical to one another; only the knives 50 directly adjacent to the inner wall 31 have wipers 51 bent toward the inner wall 31, by means of which material 29 which may settle between this knife 50 and the inner wall 31 is thrown back into the material ring 32.
  • the axial extent e of knives 49, 50 corresponds approximately to the thickness f of the material ring 32.
  • the diameter g of the knives 49 and 50 is only slightly smaller than the distance h of the mixing tools 39 which are axially adjacent to one another in this area.
  • counter to the conveying direction device 27 can be brought about that the material 29 conveyed as a material ring 32 remains longer in the area of the cutting devices 44, that is to say by exerting an impulse counter to the conveying direction 27 on the material 29.
  • the measures described ensure that all not very small material particles inevitably pass through a knife 49 or 50 at least once.
  • the knife shafts are driven at a speed such that the peripheral speed on the outer diameter of the knives 49 and 50 is approximately 10 to 40 m / s.
  • the diameter g of the knives 49.50 is approximately 50 to 250 mm, depending on the size of the mixer, ie depending on the diameter d of the interior 21 of the housing 1.
  • the mixing tools 25 and 39 are designed and set in relation to the axial conveying direction 27 that, taking into account the speed of the mixer 13, an axial feed rate of the material in the mixer between 0.02 m / s and 0.2 m / s is achieved.
  • a thickness f of the material ring 32 of 30 to 120 mm is used.
  • the axial extent e of the knives 49, 50 in the direction of the axes 48 should be between 40 and 130 mm, so that there can be no material particles in the radially inner region of the material ring 32 that are not separated by at least one knife 49 or 50 can be detected.
  • the ratio of the thickness f of the material ring 32 to the diameter d of the housing 1 is 0.06 ⁇ f / d ⁇ 0.24.
  • FIG. 5 shows the shape of the knives, only the knife 50 adjacent to the inner wall 31 being shown. Starting from a hub 52, this has two cutting edges 54 leading in the direction of rotation 53 of the cutting devices 44. In the case of the knives 50, the stripper 51 is formed in each case in the region of the rear edge 55 lagging in the direction of rotation 53 by bending the flat knife 50.
  • the knives 49 look exactly the same in principle; they only have no wipers.
  • Materials 29 that tend to agglomerate are preferably wetted with liquid binder in the mixer. These agglomerates formed in the wetting zone b after the supply of the binder are completely dissolved by the cutting devices 44.
  • paper fibers can be wetted with glue, which are then used to manufacture plasterboard.
  • other materials that agglomerate after wetting can be wetted with a liquid as part of a so-called material ring mixture.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Forests & Forestry (AREA)
  • Wood Science & Technology (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Processing Of Solid Wastes (AREA)
  • Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
  • Confectionery (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
EP89115813A 1988-11-24 1989-08-28 Mélangeur travaillant en continu Revoked EP0370181B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT89115813T ATE88661T1 (de) 1988-11-24 1989-08-28 Kontinuierlich arbeitender mischer.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3839671A DE3839671A1 (de) 1988-11-24 1988-11-24 Kontinuierlich arbeitender mischer
DE3839671 1988-11-24

Publications (2)

Publication Number Publication Date
EP0370181A1 true EP0370181A1 (fr) 1990-05-30
EP0370181B1 EP0370181B1 (fr) 1993-04-28

Family

ID=6367805

Family Applications (1)

Application Number Title Priority Date Filing Date
EP89115813A Revoked EP0370181B1 (fr) 1988-11-24 1989-08-28 Mélangeur travaillant en continu

Country Status (8)

Country Link
US (1) US5018673A (fr)
EP (1) EP0370181B1 (fr)
JP (1) JPH02180628A (fr)
AT (1) ATE88661T1 (fr)
BR (1) BR8905664A (fr)
CA (1) CA2003118A1 (fr)
DE (2) DE3839671A1 (fr)
ZA (1) ZA898730B (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995011206A1 (fr) * 1993-10-20 1995-04-27 Universal Greening Pty Ltd Appareil de compostage
EP0812616A1 (fr) * 1996-06-11 1997-12-17 Gebrüder Lödige Maschinenbaugesellschaft mbH Dispositif pour la désagrégation des materiaux
WO2010081477A1 (fr) * 2009-01-13 2010-07-22 Biogasol Ipr Aps Appareil pour le mélange rapide de milieux et procédé correspondant
CZ306488B6 (cs) * 2015-12-18 2017-02-08 Rudolf Ryzner Zařízení pro máčení, míchání a obohacování organických substrátů

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JP2696435B2 (ja) * 1991-03-26 1998-01-14 顯治 前田 コンクリートの混練方法及びその装置
DE4124984C2 (de) * 1991-07-27 1995-04-27 Babcock Bsh Ag Verwendung einer Misch-, Granulier- und Trocknungsvorrichtung
DE4132906C2 (de) * 1991-10-04 1994-09-29 Loedige Maschbau Gmbh Geb Verwendung einer Maschine zur Gipskartonplattenwiederaufarbeitung
DE19503266C2 (de) * 1995-02-02 2003-06-18 Suma Sondermaschinen Gmbh Zerkleinerungsvorrichtung zum Einbau in Rohrleitungen
US5580170A (en) * 1995-10-06 1996-12-03 Ferro-Tech, Inc. Mixing and conditioning machine
DE19740676C2 (de) * 1997-09-16 2003-07-17 Fraunhofer Ges Forschung Verfahren zum Beleimen von Fasern
ES2189557B1 (es) * 1999-04-29 2004-10-16 Ekolur, S.L. Alimentador y mezclador de paletas para la proyeccion del hormigon o gunita y del compos.
US6414054B1 (en) * 1999-12-21 2002-07-02 General Electric Company Continuous preparation of heat-vulcanizable silicone compositions
US6548574B1 (en) 1999-12-21 2003-04-15 General Electric Company Heat-vulcanizable silicone compositions from premix
EP1157736A1 (fr) * 2000-05-20 2001-11-28 Glatt Maschinen- und Apparatebau AG Dispositif et procédé pour le traitement quasi-continu d'un produit granulaire
US6511217B1 (en) * 2000-11-03 2003-01-28 General Electric Company Method and system to compound silicone compositions
DE10059881B4 (de) 2000-12-01 2005-06-02 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Anlage zur Faseraufbereitung
DE10126783A1 (de) * 2001-06-01 2003-01-02 Glatt Systemtechnik Gmbh Einrichtung zur Zuführung eines Trocknungsgases in einen Mischgranulator
DE10215806A1 (de) * 2002-04-10 2003-10-23 Buehler Ag Mischer mit Durchsatzglättung
US7563017B1 (en) * 2002-09-06 2009-07-21 Bracegirdle Paul E Process for mixing congealable materials such as cement, asphalt, and glue with fibers from waste carpet
ES2264356B1 (es) * 2004-11-11 2008-01-01 Tecnicas De Mezclado, S.L. Aparato para la dispersion de colorantes y pigmentos en mezclas de productos pulverulentos.
DE102009057916B4 (de) * 2009-05-15 2015-04-02 Siempelkamp Maschinen- Und Anlagenbau Gmbh Verfahren und Vorrichtung zum kontinuierlichen Mischen von Fasern mit einem Bindemittel
US9194092B2 (en) * 2010-01-26 2015-11-24 Mark Kline Mechanism for automated mixing of liquid solutions and granular materials
JP2016087808A (ja) * 2014-10-30 2016-05-23 株式会社タイガーマシン製作所 給材箱装置
CN107921155A (zh) * 2015-08-26 2018-04-17 株式会社佐竹 过热蒸汽灭菌装置
US10981294B2 (en) 2016-08-05 2021-04-20 United States Gypsum Company Headbox and forming station for fiber-reinforced cementitious panel production
US11224990B2 (en) * 2016-08-05 2022-01-18 United States Gypsum Company Continuous methods of making fiber reinforced concrete panels
US10272399B2 (en) 2016-08-05 2019-04-30 United States Gypsum Company Method for producing fiber reinforced cementitious slurry using a multi-stage continuous mixer
US11173629B2 (en) * 2016-08-05 2021-11-16 United States Gypsum Company Continuous mixer and method of mixing reinforcing fibers with cementitious materials
CN109876720A (zh) * 2017-12-06 2019-06-14 天津发洋环保科技有限公司 一种光触媒乳液连续生产线
JP6889924B2 (ja) * 2018-01-17 2021-06-18 株式会社切川物産 撹拌混合装置
CN109926432A (zh) * 2019-03-15 2019-06-25 深圳市发现环保科技有限公司 固体有机物细碎机
CN110625814B (zh) * 2019-09-30 2021-02-02 广州胜帆新材料科技有限公司 一种弧形grg板材生产用快速成型装置及方法
RU2728441C1 (ru) * 2019-10-23 2020-07-29 Федеральное государственное бюджетное образовательное учреждение высшего образования "Поволжский государственный технологический университет" Устройство для получения арболита

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US3506201A (en) * 1965-12-17 1970-04-14 Draiswerke Gmbh Trough mixer having a dosing arrangement for mixing fibrous materials
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Publication number Priority date Publication date Assignee Title
CH367379A (de) * 1957-12-20 1963-02-15 Loedige Wilhelm Verfahren und Vorrichtung zum Mischen und Zerkleinern von pulverförmigen, feinkörnigen und faserigen Mischgütern
DE1432028A1 (de) * 1964-02-18 1968-10-31 Draiswerke Gmbh Verfahren zum Betrieb von Mischmaschinen sowie zugehoerige Mischmaschine
US3506201A (en) * 1965-12-17 1970-04-14 Draiswerke Gmbh Trough mixer having a dosing arrangement for mixing fibrous materials
FR1511391A (fr) * 1967-02-14 1968-01-26 Appareil pour mélanger et, le cas échéant, fragmenter et/ou humecter des substances pulvérulentes, à grains fins ou fibreuses
DE1782585A1 (de) * 1968-09-20 1971-10-14 Draiswerke Gmbh Mischmaschine
CH525702A (de) * 1970-11-24 1972-07-31 Draiswerke Gmbh Verfahren und Vorrichtung zum kontinuierlichen Mischen bzw. Benetzen von Feststoffen mit Flüssigkeiten
DE2924326A1 (de) * 1979-06-15 1981-01-08 Loedige Maschbau Gmbh Geb Verfahren zum trocknen von zum verkleben neigenden klebrigen pasten
DE3711987A1 (de) * 1987-04-09 1988-10-27 Durmersheim Baustoffwerke Misch- und verteilvorrichtung fuer mischungen aus pulverigen bis koernigen feststoffen

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995011206A1 (fr) * 1993-10-20 1995-04-27 Universal Greening Pty Ltd Appareil de compostage
EP0812616A1 (fr) * 1996-06-11 1997-12-17 Gebrüder Lödige Maschinenbaugesellschaft mbH Dispositif pour la désagrégation des materiaux
US5803374A (en) * 1996-06-11 1998-09-08 Gebrueder Loedige Maschinenbaugesellschaft Mbh Breakdown tool
WO2010081477A1 (fr) * 2009-01-13 2010-07-22 Biogasol Ipr Aps Appareil pour le mélange rapide de milieux et procédé correspondant
AU2010205966B2 (en) * 2009-01-13 2014-06-05 Biogasol Aps Apparatus for rapid mixing of media and method
CN102271792B (zh) * 2009-01-13 2014-09-17 拜格索有限公司 快速混合介质的装置及方法
US8845976B2 (en) 2009-01-13 2014-09-30 Biogasol Aps Apparatus for rapid mixing of media and method
US9605223B2 (en) 2009-01-13 2017-03-28 Biogasol Aps Apparatus for rapid mixing of media and method
CZ306488B6 (cs) * 2015-12-18 2017-02-08 Rudolf Ryzner Zařízení pro máčení, míchání a obohacování organických substrátů

Also Published As

Publication number Publication date
DE3839671A1 (de) 1990-05-31
US5018673A (en) 1991-05-28
CA2003118A1 (fr) 1990-05-24
ATE88661T1 (de) 1993-05-15
DE58904203D1 (de) 1993-06-03
ZA898730B (en) 1990-08-29
EP0370181B1 (fr) 1993-04-28
JPH02180628A (ja) 1990-07-13
BR8905664A (pt) 1990-06-05

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