CH437217A - Device for the continuous production of solutions and suspensions - Google Patents
Device for the continuous production of solutions and suspensionsInfo
- Publication number
- CH437217A CH437217A CH1769665A CH1769665A CH437217A CH 437217 A CH437217 A CH 437217A CH 1769665 A CH1769665 A CH 1769665A CH 1769665 A CH1769665 A CH 1769665A CH 437217 A CH437217 A CH 437217A
- Authority
- CH
- Switzerland
- Prior art keywords
- mixing
- suspensions
- solutions
- elements
- continuous production
- Prior art date
Links
- 239000000725 suspension Substances 0.000 title claims description 7
- 238000010924 continuous production Methods 0.000 title claims description 5
- 238000004898 kneading Methods 0.000 claims description 7
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 230000001419 dependent effect Effects 0.000 claims 2
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 2
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 2
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920002239 polyacrylonitrile Polymers 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- SMEGJBVQLJJKKX-HOTMZDKISA-N [(2R,3S,4S,5R,6R)-5-acetyloxy-3,4,6-trihydroxyoxan-2-yl]methyl acetate Chemical compound CC(=O)OC[C@@H]1[C@H]([C@@H]([C@H]([C@@H](O1)O)OC(=O)C)O)O SMEGJBVQLJJKKX-HOTMZDKISA-N 0.000 description 1
- 229940081735 acetylcellulose Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
- B29B7/426—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix with consecutive casings or screws, e.g. for charging, discharging, mixing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/71705—Feed mechanisms characterised by the means for feeding the components to the mixer using belts
-
- 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
- B01F27/72—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices
-
- 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
- B01F33/82—Combinations of dissimilar mixers
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
-
- 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
- B01F33/831—Devices with consecutive working receptacles, e.g. with two intermeshing tools in one of the receptacles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/711—Feed mechanisms for feeding a mixture of components, i.e. solids in liquid, solids in a gas stream
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/712—Feed mechanisms for feeding fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/714—Feed mechanisms for feeding predetermined amounts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/7173—Feed mechanisms characterised by the means for feeding the components to the mixer using gravity, e.g. from a hopper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/286—Raw material dosing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/285—Feeding the extrusion material to the extruder
- B29C48/29—Feeding the extrusion material to the extruder in liquid form
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/375—Plasticisers, homogenisers or feeders comprising two or more stages
- B29C48/38—Plasticisers, homogenisers or feeders comprising two or more stages using two or more serially arranged screws in the same barrel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/71—Feed mechanisms
- B01F35/717—Feed mechanisms characterised by the means for feeding the components to the mixer
- B01F35/7176—Feed mechanisms characterised by the means for feeding the components to the mixer using pumps
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
- B29K2105/0005—Condition, form or state of moulded material or of the material to be shaped containing compounding ingredients
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S516/00—Colloid systems and wetting agents; subcombinations thereof; processes of
- Y10S516/924—Significant dispersive or manipulative operation or step in making or stabilizing colloid system
- Y10S516/929—Specified combination of agitation steps, e.g. mixing to make subcombination composition followed by homogenization
- Y10S516/931—High shear followed by low shear
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
Einrichtung zum kontinuierlichen Herstellen von Lösungen und Suspensionen
Die vorliegende Erfindung bezieht sich auf leine liin- richtung zum kontinuierlichen Herstellen von Lösungen und Suspensionen.
Kontinuierliche Löseprozesse sind mittels Schnekkenmaschinen verschiedener Bauart durchführbar. Dabei wurde jedoch als nachteilig empfunden, dass beim Dosieren im Einfüllbereich oft grössere Agglomerate entstehen, die vom Lösemittel umhüllt werden und den weiteren Lösevorgang erschweren. Nur durch Aufbringen von relativ grossen Scherkräften sind die gallertartigen Häute abzureiben, um dadurch neue Oberflächen für die Lösemittelpenetration frei zu legen. Dazu ist jedoch grosser technischer Aufwand nötig und oft müssen spezielle Reibelemente Anwendung finden. Bei der Herstellung von Suspensionen stellen sich oft ähnliche Probleme.
Es wird angestrebt, eine Einrichtung vorzuschlagen, bei welcher bei separater Dosierung der Flüssigkeitskomponenten die Bildung von Agglomeraten verhindert wird, so dass diese mit bekannten Schneckenmaschinen verarbeitet werden können.
Die erfindungsgemässe Einrichtung zum kontinuierTi- chen Herstellen von Lösungen und Suspensionen weist eine Knetvorrichtung und eine der Knetvorrichtung vorgeschaltete rotierende Mischvorrichtung auf, welche mit einer höheren Drehzahl als die Knetvorrichtung arbeitet.
Zweckmässigerweise kann die Mischvorrichtung eine rotierende mit Misch- und Zerkleinerungsorganen versehene vertikale Welle aufweisen. Auf beiliegender Zeichnung ist ein Ausführungsbeispiel des Erfindungsgegenstandes schematisch dargestellt.
Die dargestellte Einrichtung zum kontinuierlichen Durchführen von Löseprozessen weist eine Knetvorrichtung 1 auf, welche eine in einem Gehäuse 2 rotierende Schnecke 3 besitzt, die mittels eines in einem Gehäuse 4 angeordneten nicht dargestellten Motors über ein Getriebe angetrieben wird. An die Einfüllöffnung des Gehäuses 2 ist eine Mischvorrichtung 5 mit ihrer Austrittsdüse 6 angeschlossen. Die Mischvorrichtung weist eine in einem vertikalen Gehäuse 7 langeordnete Welle 8 auf, die mit Mlisch-und Zerkleinerungsorganen 9 ausgerüstet ist. Die Misch- und Zerkleinerungsorgane 9 sind entlang der Welle radial verteilt. Zum Antrieb der Welle 8 dient ein Elektromotor 10, welcher am oberen aus dem Gehäuse 7 herausragenden Ende der Welle 8 befestigt ist.
Die Welle 8 rotiert mit mehrfach erhöhten Drehzahlen gegenüber der Schnecke 3.
Die Feststoffe, welche in einer Flüssigkeit gelöst werden sollen, befinden sich in einem Behälter 11 und gelangen mittels eines Förderbandes oder Dosierwaage 12 durch den Einfüllstutzen 13 in die Mischvorrichtung.
Der Einfüllstutzen 13 der Mischvorrichtung ist am oberen Teil des Gehäuses 7 angeordnet Die pulverförmigen Feststoffe werden im Gehäuse 7 von den rotierenden flügelartigen Misch- und Zerkleinerungsorganen erfasst und in wirbelnde Bewegung versetzt. Die Flüssigkeit wird aus einem Behälter 14 mittels einer Leitung 15 über eine Dosierpumpe 17 in das Gehäuse 7 eingeführt. An Stelle der einzigen Leitung 15, können weitere aus der Leitung 15 abzweigende Leitung vorhanden sein, die an verschiedenen Umfangsstellen in das Gehäuse 7 münden. Das benetzte oder angeteigte Material wird zwangläufig oder durch die Schwerkraft nach unten gefördert, wobei die relativ lockeren Agglomerate zerschlagen werden.
Zur Unterstützung dieser Wirkung können im Gehäuse 7 noch Statorelemente 16 vorhanden sein, welche mit den Misch- und Zerkleinerungsorganen 9 zusammenwirken. Durch die Düse 6 tritt ein Gemenge in die Knetvorrichtung 1 ein, welches in dieser ohne Schwierigkeiten weiter verarbeitet wird.
Die beschriebene Einrichtung ist z. B. besonders geeignet zur Lösung von Polyacrylnitril in Dimethylfornamid, von Acetyl-Cellulose in Aceton, PVC in Cyclohexanon usw. und Herstellung von Suspensionen z. B. aus Therephthalsäure und Glykol, wobei die Verweilzeit des Produktes in der kontinuierlichen gegenüber der chargenweise arbeitenden Einrichtung wesentlich herabgesetzt werden kann. Dadurch wird die Qualität des Produktes verbessert und beispielsweise ;bei der Lö sung von Polyacrylnitril in Dimethylfornamid d die sonst auftretende Gelbfärbung wesentlich herabgesetzt oder sogar ganz verhindert.
Device for the continuous production of solutions and suspensions
The present invention relates to a line for the continuous production of solutions and suspensions.
Continuous dissolving processes can be carried out using various types of screw machines. However, it was found to be disadvantageous that when metering in the filling area, larger agglomerates are often formed which are enveloped by the solvent and make the further dissolving process more difficult. The gelatinous skins can only be rubbed off by applying relatively high shear forces in order to expose new surfaces for solvent penetration. However, this requires a great deal of technical effort and often special friction elements have to be used. Similar problems often arise in the production of suspensions.
The aim is to propose a device in which, with separate dosing of the liquid components, the formation of agglomerates is prevented so that they can be processed with known screw machines.
The device according to the invention for the continuous production of solutions and suspensions has a kneading device and a rotating mixing device connected upstream of the kneading device, which works at a higher speed than the kneading device.
The mixing device can expediently have a rotating vertical shaft provided with mixing and crushing elements. An exemplary embodiment of the subject matter of the invention is shown schematically in the accompanying drawing.
The device shown for continuously performing loosening processes has a kneading device 1 which has a screw 3 rotating in a housing 2, which is driven by means of a motor, not shown, arranged in a housing 4 via a gear. A mixing device 5 with its outlet nozzle 6 is connected to the filling opening of the housing 2. The mixing device has a shaft 8 which is arranged in a vertical housing 7 and is equipped with mixing and comminuting elements 9. The mixing and crushing elements 9 are distributed radially along the shaft. An electric motor 10, which is fastened to the upper end of the shaft 8 protruding from the housing 7, is used to drive the shaft 8.
The shaft 8 rotates at several times higher speeds than the worm 3.
The solids which are to be dissolved in a liquid are located in a container 11 and reach the mixing device by means of a conveyor belt or metering scale 12 through the filler neck 13.
The filler neck 13 of the mixing device is arranged on the upper part of the housing 7. The pulverulent solids are captured in the housing 7 by the rotating, wing-like mixing and comminuting elements and set in a whirling motion. The liquid is introduced into the housing 7 from a container 14 by means of a line 15 via a metering pump 17. Instead of the single line 15, further lines branching off from the line 15 can be present, which open into the housing 7 at various points on the circumference. The wetted or pasted material is forced downwards or by gravity, whereby the relatively loose agglomerates are broken up.
To support this effect, stator elements 16 can also be present in the housing 7, which interact with the mixing and comminuting elements 9. A mixture enters the kneading device 1 through the nozzle 6 and is further processed in this without difficulty.
The device described is z. B. particularly suitable for the solution of polyacrylonitrile in dimethylformamide, acetyl cellulose in acetone, PVC in cyclohexanone, etc. and the production of suspensions z. B. from terephthalic acid and glycol, whereby the residence time of the product in the continuous compared to the batch-wise operating device can be significantly reduced. This improves the quality of the product and, for example, when polyacrylonitrile is dissolved in dimethylformide, the yellow coloration that otherwise occurs is significantly reduced or even completely prevented.
Claims (1)
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH1769665A CH437217A (en) | 1965-12-20 | 1965-12-20 | Device for the continuous production of solutions and suspensions |
| SE16966/66A SE334143B (en) | 1965-12-20 | 1966-12-12 | |
| AT1147566A AT274742B (en) | 1965-12-20 | 1966-12-13 | Process for the continuous production of solutions and suspensions and device for carrying out the process |
| FR87812A FR1506697A (en) | 1965-12-20 | 1966-12-16 | Device for the continuous production of solutions and suspensions |
| BR185479/66A BR6685479D0 (en) | 1965-12-20 | 1966-12-19 | INSTALLATION FOR THE CONTINUOUS PREPARATION OF SOLUTIONS AND SUSPENSIONS |
| NL6617778A NL6617778A (en) | 1965-12-20 | 1966-12-19 | |
| BE691483D BE691483A (en) | 1965-12-20 | 1966-12-20 | |
| US875962A US3647493A (en) | 1965-12-20 | 1969-11-12 | Method and apparatus for continuously producing solutions and suspensions |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH1769665A CH437217A (en) | 1965-12-20 | 1965-12-20 | Device for the continuous production of solutions and suspensions |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CH437217A true CH437217A (en) | 1967-06-15 |
Family
ID=4427386
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CH1769665A CH437217A (en) | 1965-12-20 | 1965-12-20 | Device for the continuous production of solutions and suspensions |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US3647493A (en) |
| AT (1) | AT274742B (en) |
| BE (1) | BE691483A (en) |
| BR (1) | BR6685479D0 (en) |
| CH (1) | CH437217A (en) |
| FR (1) | FR1506697A (en) |
| NL (1) | NL6617778A (en) |
| SE (1) | SE334143B (en) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2701542C2 (en) * | 1977-01-15 | 1985-09-12 | Dietrich Dipl.-Ing. 6240 Königstein Maurer | Device for the continuous production and delivery of a mixture of a granular or powdery, dry solid and a liquid |
| US4211574A (en) * | 1977-07-26 | 1980-07-08 | Akzona Incorporated | Process for making a solid impregnated precursor of a solution of cellulose |
| US4144080A (en) * | 1977-07-26 | 1979-03-13 | Akzona Incorporated | Process for making amine oxide solution of cellulose |
| US4428852A (en) * | 1982-01-18 | 1984-01-31 | E. I. Du Pont De Nemours And Company | Continuous synthesis of chromium dioxide |
| PL142347B1 (en) * | 1984-02-28 | 1987-10-31 | Biuro Studiow I Projektow Energetycznych "Energoprojekt" | Flow-through mixer |
| US4778835A (en) * | 1985-12-09 | 1988-10-18 | Eastman Kodak Company | Process and apparatus for preparing polyester dissipations |
| DE3601324A1 (en) * | 1986-01-17 | 1987-07-23 | Wacker Chemie Gmbh | METHOD FOR THE CONTINUOUS PRODUCTION OF SILICONE MATERIALS VULCANIZABLE AT ROOM TEMPERATURE |
| DE4027888A1 (en) * | 1990-09-03 | 1992-03-05 | Stoess & Co Gelatine | METHOD FOR CONTINUOUSLY RELEASING GELATINE |
| DE4227542A1 (en) * | 1992-08-20 | 1994-02-24 | Werner Kempter | Device for producing a cross-linked extruded product |
| US6414054B1 (en) * | 1999-12-21 | 2002-07-02 | General Electric Company | Continuous preparation of heat-vulcanizable silicone compositions |
| EP2446957B1 (en) * | 2005-09-28 | 2016-05-18 | China Tobacco Hunan Industrial Corporation | Device for adding tobacco dust in production process of papermaking tobacco sheet |
| WO2011146896A2 (en) * | 2010-05-21 | 2011-11-24 | Kinetikgruppen Sverige Ab | Comminution reactor |
| USD1057770S1 (en) | 2023-05-12 | 2025-01-14 | Bühler AG | Food and feed industry machine (extruder) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3160352A (en) * | 1959-06-15 | 1964-12-08 | Gilman B Mollring | Apparatus for pulverizing and dispersing solid material into liquid suspension |
-
1965
- 1965-12-20 CH CH1769665A patent/CH437217A/en unknown
-
1966
- 1966-12-12 SE SE16966/66A patent/SE334143B/xx unknown
- 1966-12-13 AT AT1147566A patent/AT274742B/en active
- 1966-12-16 FR FR87812A patent/FR1506697A/en not_active Expired
- 1966-12-19 BR BR185479/66A patent/BR6685479D0/en unknown
- 1966-12-19 NL NL6617778A patent/NL6617778A/xx unknown
- 1966-12-20 BE BE691483D patent/BE691483A/xx unknown
-
1969
- 1969-11-12 US US875962A patent/US3647493A/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| SE334143B (en) | 1971-04-19 |
| US3647493A (en) | 1972-03-07 |
| NL6617778A (en) | 1967-06-21 |
| AT274742B (en) | 1969-09-25 |
| BR6685479D0 (en) | 1973-12-27 |
| FR1506697A (en) | 1967-12-22 |
| BE691483A (en) | 1967-05-29 |
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