DE102008016862A1 - Extruder i.e. two-shaft extruder, has conveyor elements with conveyor sections rotated at angle, where sections comprises axial angle corresponding to maximum of outer dimension of conveyor elements - Google Patents
Extruder i.e. two-shaft extruder, has conveyor elements with conveyor sections rotated at angle, where sections comprises axial angle corresponding to maximum of outer dimension of conveyor elements Download PDFInfo
- Publication number
- DE102008016862A1 DE102008016862A1 DE102008016862A DE102008016862A DE102008016862A1 DE 102008016862 A1 DE102008016862 A1 DE 102008016862A1 DE 102008016862 A DE102008016862 A DE 102008016862A DE 102008016862 A DE102008016862 A DE 102008016862A DE 102008016862 A1 DE102008016862 A1 DE 102008016862A1
- Authority
- DE
- Germany
- Prior art keywords
- conveyor
- extruder
- extruder according
- conveying
- elements
- 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
Links
- 230000004323 axial length Effects 0.000 claims abstract description 9
- 238000002844 melting Methods 0.000 claims description 2
- 230000008018 melting Effects 0.000 claims description 2
- 239000007787 solid Substances 0.000 description 5
- 210000001520 comb Anatomy 0.000 description 3
- 238000000265 homogenisation Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000011295 pitch Substances 0.000 description 2
- BUHVIAUBTBOHAG-FOYDDCNASA-N (2r,3r,4s,5r)-2-[6-[[2-(3,5-dimethoxyphenyl)-2-(2-methylphenyl)ethyl]amino]purin-9-yl]-5-(hydroxymethyl)oxolane-3,4-diol Chemical compound COC1=CC(OC)=CC(C(CNC=2C=3N=CN(C=3N=CN=2)[C@H]2[C@@H]([C@H](O)[C@@H](CO)O2)O)C=2C(=CC=CC=2)C)=C1 BUHVIAUBTBOHAG-FOYDDCNASA-N 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000005021 gait Effects 0.000 description 1
- 239000011346 highly viscous material Substances 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 238000010327 methods by industry Methods 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000011345 viscous material Substances 0.000 description 1
Classifications
-
- 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
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/48—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
- B29B7/485—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws with three or more shafts provided with screws
-
- 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
- B29B7/46—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft
- B29B7/48—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with more than one shaft with intermeshing devices, e.g. screws
- B29B7/488—Parts, e.g. casings, sealings; Accessories, e.g. flow controlling or throttling devices
- B29B7/489—Screws
-
- 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
- B29C48/251—Design of extruder parts, e.g. by modelling based on mathematical theories or experiments
- B29C48/2517—Design of extruder parts, e.g. by modelling based on mathematical theories or experiments of intermeshing screws
-
- 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
- B29C48/27—Cleaning; Purging; Avoiding contamination
- B29C48/2715—Cleaning; Purging; Avoiding contamination of plasticising units
-
- 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
- B29C48/40—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/402—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders the screws having intermeshing parts
-
- 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
- B29C48/40—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/405—Intermeshing co-rotating screws
-
- 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
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/507—Screws characterised by the material or their manufacturing process
-
- 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
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/67—Screws having incorporated mixing devices not provided for in groups B29C48/52 - B29C48/66
-
- 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
- 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
- B29C48/40—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/425—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders using three or more screws
-
- 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
- B29C48/40—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/425—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders using three or more screws
- B29C48/43—Ring extruders
-
- 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
- B29C48/40—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 using two or more parallel screws or at least two parallel non-intermeshing screws, e.g. twin screw extruders
- B29C48/435—Sub-screws
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Physics & Mathematics (AREA)
- Algebra (AREA)
- General Physics & Mathematics (AREA)
- Mathematical Analysis (AREA)
- Mathematical Optimization (AREA)
- Mathematical Physics (AREA)
- Pure & Applied Mathematics (AREA)
- Manufacturing & Machinery (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Abstract
Description
Die Erfindung bezieht sich auf einen Zwei- oder Mehrwellen-Extruder nach dem Oberbegriff des Anspruchs 1.The This invention relates to a two or more shaft extruder according to the preamble of claim 1.
Zwei- oder Mehrwellen-Extruder mit gleichsinnig antreibbaren Wellen weisen im Wesentlichen dichtkämmende Förderschnecken sowie Misch-, Knet- und Förderabschnitte auf. Geeignete Bauelemente in der benötigten Vielfalt werden zwecks einfacher Anpassung von Geometrie und Werkstoff an die verschiedenen Verfahrensaufgaben meist auf die Tragwellen drehfest aufsteckbar ausgeführt.Two- or multi-shaft extruder with corrugated drivable waves point essentially close-meshed screw conveyors as well as mixing, kneading and conveying sections. suitable Components in the required variety are made easier in order to Adaptation of geometry and material to the various process tasks usually designed rotatably attachable to the support shafts.
Um die nötige Flexibilität mit den hohen Ansprüchen an Wirtschaftlichkeit und Sicherheit in Einklang zu bringen, sind geometrische Einschränkungen, wie z. B. nur eine oder wenige Elementlängen und/oder gleiche Montageposition an den Enden, notwendig. Dies beschränkt die nötigen Schneckensteigungen, Elementtypen und/oder Baulängen wesentlich. Um die erforderliche Anpassungsfähigkeit bei den Elementen zu erreichen, müssen nur die Endpositionen und/oder Längen eingehalten werden, sodass die geometrischen Verhältnisse dazwischen, wie Steigung und Versatzwinkel, stufenlos oder in Stufen frei nach verfahrenstechnischen Gesichtspunkten wählbar werden. Effektivität und die Art des Energieübergangs von den Förderstrukturen in das Produkt beeinflussen beim Produktdurchlauf sowohl die Produkttemperatur als auch dessen Qualität. Um pulverförmige Feststoffe mit viskosen Stoffen zu benetzen und darin zu verteilen und/oder zu zerteilen, sind Scherströmungen und noch besser Dehnströmungen im hochviskosen Stoff zu generieren.Around the necessary flexibility with the high demands to reconcile efficiency with safety geometric constraints, such as B. only one or a few Element lengths and / or same mounting position at the ends, necessary. This limits the necessary screw pitches, Element types and / or lengths essential. To the required Adaptability to reach the elements need only the end positions and / or lengths are respected, so the geometric relationships between them, like slope and offset angle, stepless or in stages free according to process engineering Aspects are selectable. Effectiveness and the type of energy transfer from the conveyor structures in the product both product temperature affect during product flow as well as its quality. To powdered solids with viscous substances to moisten and distribute and / or to divide, are shear flows and even better Dehnströmungen in the highly viscous substance to generate.
Aus
Die Homogenisierung und Dispergierung der Feststoffe in einer viskosen Matrix, die mit den bekannten Extrudern erzielbar ist, lässt jedoch noch zu wünschen übrig. Dies gilt insbesondere für Feststoffe mit einer Teilchengröße im μm-Bereich.The Homogenization and dispersion of the solids in a viscous Matrix, which is achievable with the known extruders leaves but still to be desired. This is especially true for solids with a particle size in the μm range.
Aufgabe der Erfindung ist es, einen uneingeschränkt selbstreinigenden Mehrwellen-Extruder zur Verfügung zu stellen, mit dem die Produktqualität wesentlich und effektiv verbessert wird.task The invention is an unrestricted self-cleaning Multi-shaft extruder to provide, with the Product quality is significantly and effectively improved.
Dies wird erfindungsgemäß mit dem Extruder nach dem Anspruch 1 erreicht. In den Unteransprüchen sind vorteilhafte Ausgestaltungen der Erfindung wiedergegeben.This is inventively with the extruder after the Claim 1 reached. In the subclaims are advantageous Embodiments of the invention reproduced.
Erfindungsgemäß werden wenigstens zweigängige Förderelemente verwendet, die im Profilquerschnitt, also im senkrechten Querschnitt zur Welle aus Kreisbögen bestehen, wobei miteinander kämmende Förderelemente sich im Wesentlichen am ganzen Umfang gegenseitig dicht abstreifen. Neben zweigängigen werden insbesondere auch dreigängige Förderelemente verwendet.According to the invention used at least two-speed conveying elements, in the profile cross section, ie in the vertical cross section to the shaft consist of circular arcs, with intermeshing Conveying elements are mutually substantially around the entire circumference strip tightly. In addition to zweigängigen in particular also used three-speed conveying elements.
Dabei streift der Kamm des ersten Gangs die Innenwand des Gehäuses mit geringem Spiel ab, während zwischen dem Kamm des wenigstens einen anderen weiteren Ganges und der Innenwand des Gehäuses ein größerer Abstand besteht. Jedes Förderelement weist wenigstens zwei stufenlos oder in Stufen zueinander versetzte Förderabschnitte auf, wobei vorzugsweise jeder Förderabschnitt eine axiale Länge besitzt, die höchstens dem ganzen, vorzugsweise höchstens dem halben Außendurchmesser des Förderelements, also dem ganzen bzw. halben Innendurchmesser der Gehäuseinnenwand entspricht.there The first gear comb brushes the inside wall of the case with little play off, while between the crest of at least another another aisle and the inner wall of the housing a greater distance exists. Each conveyor element has at least two stepless or staggered steps Conveying sections, wherein preferably each conveyor section has an axial length which is at most the whole, preferably at most half the outer diameter of the conveying element, ie the whole or half inner diameter the housing inner wall corresponds.
Damit weist jeder Förderabschnitt im Winkel von 90° bei zweigängigen und 60° bei dreigängigen eine dazu entsprechend große sowie entsprechend kleine Gangtiefe auf. D. h. bei dem erfindungsgemäßen Förderelement folgt einem ersten Kamm mit geringem Spiel zur Gehäuseinnenwand ein zweiter Kamm mit größerem Abstand zur Gehäuseinnenwand und im Winkel dazu je eine entsprechend große Gangtiefe sowie eine kleine Gangtiefe nach einem maximalen Abstand von 1 Da oder ½ Da (Da = Außendurchmesser des Förderelements bzw. Innendurchmesser der Gehäuseinnenwand).In order to Each conveyor section has an angle of 90 ° double-flighted and 60 ° at three-speed one correspondingly large and correspondingly small gangway on. Ie. in the conveying element according to the invention follows a first comb with little clearance to the inside wall of the housing a second comb with a greater distance to the housing inner wall and at an angle to each a correspondingly large passage depth as well as a small gangway after a maximum distance of 1 Da or ½ Da (Da = outer diameter of the conveyor element or inner diameter of the housing inner wall).
Das bedeutet, dass über alle Förderkanäle hinweg in Umfangsrichtung von Kanal zu Kanal mit einer Vervielfachung der Stromteilungen ein großer Stoffaustausch möglich ist, der mit unterschiedlichen und wechselnden Gangtiefen und entsprechenden Kamm/Gehäuse-Spielen sowohl radial als auch axial in gleicher Weise erfolgt und somit der Füllgrad in allen Kanälen gleich groß ist. Durch die ständigen geometrischen Schikanen im Wechsel von Kamm und Gang in kurzer Folge in Umfangs- und axialer Richtung wird eine besonders hohe Dichte an Dehnströmungen erzeugt. Da dies ohne Spitzenbelastungen und damit ohne unerwünschtem Viskositätsabfall in allen Fördergängen im gesamten Querschnitt und über die gesamte Länge des Förderelements erfolgt, erreicht man eine effektivere, schnellere Mischung und bei gleichmäßigerer Homogenisierung eine wesentlich höhere Produktqualität. Dazu tragen wesentlich im Übergang des Produkts von einer Tragwelle auf die nächste zwei scharfe Umlenkungen beim Zwei-Wellen-Extruder und insbesondere 12 Umlenkungen bei einem 6-Wellen-Extruder sowie 24 Umlenkungen bei einem 12-Wellen-Extruder bei, die eine weitere Intensivierung der wirksamen Kräfte im Produkt bewirken.This means that across all conveyor channels in the circumferential direction from channel to channel with a multiplication of the flow divisions a large mass transfer is possible, which takes place with different and changing flight depths and corresponding comb / housing games both radially and axially in the same way and thus the Filling level is the same in all channels. Due to the constant geometric baffles in the change of comb and gait in short order in the circumferential and axial direction, a particularly high density of extensional flows is generated. Since this takes place without peak loads and thus without undesirable viscosity drop in all conveying paths in the entire cross section and over the entire length of the conveying element, to achieve a more effective, faster mixing and more uniform homogenization a much higher product quality. This contribute significantly in the transition of the product from one support shaft to the next two sharp deflections in the two-shaft extruder and in particular 12 deflections in a 6-shaft extruder and 24 deflections in a 12-shaft extruder, which further intensifies the effect effective forces in the product.
Damit werden über die Viskosität der kontinuierlichen Phase wiederholt Zug- und Biegekräfte auf die Dauerfestigkeit der Feststoffagglomerate ausgeübt, was deren Dauerbruch zur Folge hat. Erfindungsgemäß wird daher eine effektive Homogenisierung und Dispergierung des Feststoffs erzielt, und zwar selbst bei Feststoffteilchen mit einer Teilchengröße im μm-Bereich, also weniger als 100 μm, insbesondere weniger als 10 μm.In order to be about the viscosity of the continuous Phase repeats tensile and bending forces on fatigue strength the solid agglomerates exercised what their endurance break entails. According to the invention therefore a achieved effective homogenization and dispersion of the solid, even with particulate matter having a particle size in the micron range, that is less than 100 microns, in particular less than 10 μm.
Mit dem erfindungsgemäßen Förderelement ist das Produkt also auf ganz kurzer Länge ständig anderen Gangtiefen und Stoffgeschwindigkeiten und damit Dehnungsvorgängen ausgesetzt.With the conveying element according to the invention So the product is constantly changing for a very short time Gutsiefen and fabric speeds and thus stretching processes exposed.
Das erfindungsgemäße Förderelement ist vorzugsweise einstückig ausgebildet. Während erfindungsgemäß der Kamm des ersten Ganges die Innenwand des Gehäuses im Wesentlichen dicht abstreift, also nur ein geringes Spiel von beispielsweise weniger als 1, vorzugsweise weniger als 0,5 mm aufweist, entspricht der Abstand des Kamms des wenigstens einen weiteren Ganges des Schneckenelements von der Gehäuseinnenwand vorzugsweise höchstens der halben Gangtiefe des ersten Gangs, vorzugsweise jedoch mehr als 1 mm.The conveying element according to the invention is preferably integrally formed. While according to the invention of Comb first gear the inner wall of the housing substantially strikes tight, so only a small game of, for example, less as 1, preferably less than 0.5 mm, corresponds to Distance of the comb of the at least one further passage of the screw element from the housing inner wall preferably at most half the first-course corridor, but preferably more than 1 mm.
Die Steigung der Kämme des Förderelements beträgt vorzugsweise zwischen 1/3 Da und unendlich. D. h. das erfindungsgemäße Förderelement kann beispielsweise auch als Knetblock ausgebildet sein.The Slope of the combs of the conveyor element amounts preferably between 1/3 Da and infinity. Ie. the inventive Conveying element may for example be designed as a kneading block.
Die Gangsteigung des Förderelements kann von Förderabschnitt zu Förderabschnitt unterschiedlich sein. Auch kann sich das Verhältnis des Außendurchmessers Da zum Innen- oder Kerndurchmesser Di von Förderabschnitt zu Förderabschnitt ändern.The Gang pitch of the conveyor element can of conveyor section be different to conveyor section. Also can be the ratio of the outer diameter Da to the inner or change core diameter Di from conveyor section to conveyor section.
Die axiale Länge des Förderelements beträgt vorzugsweise mindestens 1 Da und sollte 4 Da nicht übersteigen, da es bei einer Länge über 4 Da schwierig zu handhaben, beispielsweise schwer von der Welle zu lösen ist.The axial length of the conveying element is preferably at least 1 Da and should not exceed 4 Da, since it is difficult to handle at a length greater than 4 Da, For example, it is difficult to release from the shaft.
Der
erfindungsgemäße Extruder weist vorzugsweise mindestens
drei achsparallele Wellen auf. Die Wellen können dabei
in einer geraden, ebenen Fläche angeordnet sein. Statt
dessen können auch längs eines Kreises oder Kreisbogens
angeordnete Wellen in dem Hohlraum des Extrudergehäuses
vorgesehen sein, wobei das Extrudergehäuse an der radial
innen- und außenliegenden Seite des Hohlraumes jeweils
mit zur Extruderachse parallelen konkaven Kreissegmenten versehen
ist, in denen die Schneckenelemente im Wesentlichen dicht geführt sind,
wie beispielsweise in
Mit den erfindungsgemäßen Förderelementen kann damit ein Stoffdurchtritt durch den Wellenkranz von einer Seite des Hohlraums zur anderen erfolgen. Bei beispielsweise sechs im Kreis mit gleichem Zentriwinkelabstand angeordneten Wellen wird mit zwölf Umlenkungen des Produkts die Homogenisierung damit wesentlich gesteigert.With the conveying elements according to the invention can thus a material passage through the ring gear from one side of the cavity to the other. For example, six in Circle with the same Zentriwinkelabstand arranged waves is with twelve deflections of the product homogenizing with it significantly increased.
Die Gangtiefe des ersten Kammes des erfindungsgemäßen Förderelements kann kleiner sein als die Gangtiefe der übrigen Standard-Förderelemente des Extruders, also der Förderelemente, die mit ihren Kämmen die Innenwand des Gehäuses im Wesentlichen dicht berühren. So kann beispielsweise das Förderelement in der Materialeinfüllzone des Extruders eine besonders große Gangtiefe besitzen. Beispielsweise kann das Verhältnis des Außendurchmessers Da der Förderelemente zum Innendurchmesser Di zwischen 1,25 und 2,3 betragen. Das Verhältnis des Außendurchmessers des Förderelements zum Innendurchmesser ist vorzugsweise in der Einfüllzone des Extruders am größten.The Gangtiefe of the first comb of the invention Conveying element may be smaller than the corridor depth of the rest Standard conveying elements of the extruder, ie the conveying elements, with their combs the inner wall of the housing essentially touch tightly. So, for example the conveying element in the material filling zone of Extruders have a particularly large flight depth. For example can the ratio of the outer diameter of the Conveying elements to the inner diameter Di between 1.25 and 2.3. The ratio of the outside diameter the conveying element to the inner diameter is preferably largest in the filling zone of the extruder.
Vorzugsweise bildet die Welle und das wenigstens eine erfindungsgemäße Förderelement, das sie trägt, ein einziges Bauteil. Durch die einstückige Ausbildung von Welle und Förderelement kann ein wesentlich höheres Drehmoment übertragen werden. Beispielsweise kann die Welle, einschließlich der Antriebswelle, sowie das Förderelement im Bereich der Einfüllzone, einschließlich der Aufschmelzzone aus einem einzigen Bauteil bestehen.Preferably forms the shaft and the at least one invention Conveyor, which carries them, a single component. Due to the one-piece design of shaft and conveyor element can transmit a much higher torque become. For example, the wave, including the Drive shaft, as well as the conveying element in the region of the filling zone, including the melting zone of a single component consist.
Der Einfüllzone kann dabei eine Zone mit einem Förderelement mit einem kleineren Verhältnis von Außendurchmesser zum Innendurchmesser folgen, der wiederum ein Förderelement mit einem größeren Verhältnis von Außen- zu Innendurchmesser folgen kann usw.Of the Filling zone can be a zone with a conveying element with a smaller ratio of outer diameter follow the inner diameter, which in turn is a conveying element with a larger ratio of foreign can follow to inner diameter, etc.
Nachstehend ist die Erfindung anhand der beigefügten Zeichnung beispielhaft näher erläutert. Darin zeigen:below the invention with reference to the accompanying drawings by way of example explained in more detail. Show:
Gemäß
Der
Profilquerschnitt, also der senkrechte Querschnitt zur Welle der
Förderabschnitte
Der
zweite Förderabschnitt
Die
Achse
Der
Außendurchmesser Da des Förderelements
D.
h. der zweite Kamm
Die
miteinander kämmenden Förderelemente weisen einen
Achsabstand Ax im Kreis auf, wie anhand der Förderlemente
Wie
insbesondere aus
Gemäß
Jedes
Förderelement
Wie
anhand der Förderabschnitte
Bei
der Doppelschnecke nach
Nach
Die
axiale Länge La der Ringe
Bei
dem Extruder nach
ZITATE ENTHALTEN IN DER BESCHREIBUNGQUOTES INCLUDE IN THE DESCRIPTION
Diese Liste der vom Anmelder aufgeführten Dokumente wurde automatisiert erzeugt und ist ausschließlich zur besseren Information des Lesers aufgenommen. Die Liste ist nicht Bestandteil der deutschen Patent- bzw. Gebrauchsmusteranmeldung. Das DPMA übernimmt keinerlei Haftung für etwaige Fehler oder Auslassungen.This list The documents listed by the applicant have been automated generated and is solely for better information recorded by the reader. The list is not part of the German Patent or utility model application. The DPMA takes over no liability for any errors or omissions.
Zitierte PatentliteraturCited patent literature
- - EP 0002131 B1 [0004] - EP 0002131 B1 [0004]
- - US 6738270 [0004] - US 6738270 [0004]
- - EP 0788867 B [0018] EP 0788867 B [0018]
Claims (15)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102008016862.9A DE102008016862C5 (en) | 2008-04-02 | 2008-04-02 | extruder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102008016862.9A DE102008016862C5 (en) | 2008-04-02 | 2008-04-02 | extruder |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| DE102008016862A1 true DE102008016862A1 (en) | 2009-10-08 |
| DE102008016862B4 DE102008016862B4 (en) | 2014-11-20 |
| DE102008016862C5 DE102008016862C5 (en) | 2019-12-19 |
Family
ID=41051353
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DE102008016862.9A Active DE102008016862C5 (en) | 2008-04-02 | 2008-04-02 | extruder |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE102008016862C5 (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008022421B3 (en) * | 2008-05-07 | 2009-11-19 | Blach Verwaltungs Gmbh & Co. Kg | Extruder drives |
| WO2011116965A1 (en) * | 2010-03-24 | 2011-09-29 | Blach Josef A | Extruder |
| EP2610045A1 (en) * | 2009-12-18 | 2013-07-03 | Bayer Intellectual Property GmbH | Screw feed elements for extruding viscoelastic masses |
| WO2013128463A1 (en) * | 2012-02-28 | 2013-09-06 | Steer Engineering Private Limited | An extruder mixing element |
| WO2013174878A1 (en) * | 2012-05-23 | 2013-11-28 | Blach Josef A | Multi-screw extruder with self-cleaning conveyor screws |
| US8783939B2 (en) | 2009-07-16 | 2014-07-22 | Blach Verwaltungs Gmbh & Co. Kg | Extruder |
| DE202015106285U1 (en) | 2015-11-18 | 2016-01-11 | Blach Verwaltungs Gmbh & Co. Kg | Ring extruder for the continuous preparation of rubber compounds with co-extruder and cooling system |
| DE202015104764U1 (en) | 2015-09-08 | 2016-01-12 | Blach Verwaltungs GmbH + Co. KG | Ring extruder for continuous preparation of rubber compounds with co-extruder |
| DE202015104765U1 (en) | 2015-09-08 | 2016-01-12 | Blach Verwaltungs GmbH + Co. KG | Plant for the continuous preparation of rubber compounds with barrel press |
| DE102015120586A1 (en) | 2015-09-08 | 2017-03-09 | Blach Verwaltungs Gmbh & Co. Kg | Ring extruder for the continuous preparation of rubber compounds with co-extruder and cooling system |
| DE102017123940A1 (en) | 2016-10-14 | 2018-05-09 | Blach Verwaltungs GmbH + Co. KG | Augmented reality at extruder plant |
| RU2673517C2 (en) * | 2013-06-24 | 2018-11-27 | Ковестро Дойчланд Аг | Screw elements for multi-shaft screw-type machines |
| CN112223720A (en) * | 2020-09-28 | 2021-01-15 | 南京卓越挤出装备有限公司 | High groove depth screw element |
| WO2023198550A1 (en) | 2022-04-11 | 2023-10-19 | Covestro Deutschland Ag | Multi-shaft screw machine comprising a pair of screw elements having an improved mixing and degassing effect with reduced energy input |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0002131A1 (en) * | 1977-11-19 | 1979-05-30 | Sekisui Kagaku Kogyo Kabushiki Kaisha | Improved self-cleaning type extruder |
| DE3123699A1 (en) * | 1980-06-16 | 1982-04-15 | Minnesota Mining and Manufacturing Co., 55133 Saint Paul, Minn. | "EXTRUDER SCREW" |
| EP0788867B1 (en) | 1996-02-06 | 1999-07-07 | Josef A. Blach | Apparatus for continuous processing of flowable materials |
| US20020074862A1 (en) * | 2000-12-15 | 2002-06-20 | Ryohei Saga | Parallel power source system |
| DE10207145A1 (en) * | 2002-02-20 | 2003-09-04 | Josef A Blach | Device for dispersing and melting flowable materials |
| DE10233213A1 (en) * | 2002-07-22 | 2004-02-19 | 3+Extruder Gmbh | extruder |
| US6783270B1 (en) * | 2000-07-31 | 2004-08-31 | Steer Engineering (P) Limited | Fractional and higher lobed co-rotating twin-screw elements |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19718292A1 (en) * | 1997-04-30 | 1998-11-05 | Krupp Werner & Pfleiderer Gmbh | Multi-shaft screw machine, in particular two-shaft extruder |
| US6116771A (en) * | 1999-02-05 | 2000-09-12 | Krupp Werner & Pfleiderer Corporation | Multi-shaft extruder screw bushing and extruder |
| JP3798595B2 (en) * | 2000-01-25 | 2006-07-19 | 株式会社神戸製鋼所 | Kneading rotor, screw set and twin screw extruder |
-
2008
- 2008-04-02 DE DE102008016862.9A patent/DE102008016862C5/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0002131A1 (en) * | 1977-11-19 | 1979-05-30 | Sekisui Kagaku Kogyo Kabushiki Kaisha | Improved self-cleaning type extruder |
| EP0002131B1 (en) | 1977-11-19 | 1982-06-23 | Sekisui Kagaku Kogyo Kabushiki Kaisha | Improved self-cleaning type extruder |
| DE3123699A1 (en) * | 1980-06-16 | 1982-04-15 | Minnesota Mining and Manufacturing Co., 55133 Saint Paul, Minn. | "EXTRUDER SCREW" |
| EP0788867B1 (en) | 1996-02-06 | 1999-07-07 | Josef A. Blach | Apparatus for continuous processing of flowable materials |
| US6783270B1 (en) * | 2000-07-31 | 2004-08-31 | Steer Engineering (P) Limited | Fractional and higher lobed co-rotating twin-screw elements |
| US20020074862A1 (en) * | 2000-12-15 | 2002-06-20 | Ryohei Saga | Parallel power source system |
| US6738270B2 (en) | 2000-12-15 | 2004-05-18 | Renesas Technology Corporation | Parallel power source system |
| DE10207145A1 (en) * | 2002-02-20 | 2003-09-04 | Josef A Blach | Device for dispersing and melting flowable materials |
| DE10233213A1 (en) * | 2002-07-22 | 2004-02-19 | 3+Extruder Gmbh | extruder |
Cited By (34)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102008022421B3 (en) * | 2008-05-07 | 2009-11-19 | Blach Verwaltungs Gmbh & Co. Kg | Extruder drives |
| EP2454078B1 (en) * | 2009-07-16 | 2016-04-27 | Blach Verwaltungs GmbH & Co. KG | Extruder |
| US8783939B2 (en) | 2009-07-16 | 2014-07-22 | Blach Verwaltungs Gmbh & Co. Kg | Extruder |
| EP2610045A1 (en) * | 2009-12-18 | 2013-07-03 | Bayer Intellectual Property GmbH | Screw feed elements for extruding viscoelastic masses |
| US8753003B2 (en) | 2009-12-18 | 2014-06-17 | Bayer Intellectual Property Gmbh | Screw feed elements for extrusion of viscoelastic masses |
| US9061452B2 (en) | 2010-03-24 | 2015-06-23 | Josef Blach | Extruder |
| WO2011116965A1 (en) * | 2010-03-24 | 2011-09-29 | Blach Josef A | Extruder |
| CN102834232A (en) * | 2010-03-24 | 2012-12-19 | 约瑟夫·布拉赫 | extruder |
| JP2013522088A (en) * | 2010-03-24 | 2013-06-13 | ブラハ、ヨーゼフ | Extruder |
| KR101832005B1 (en) * | 2010-03-24 | 2018-02-23 | 요제프 아. 블라흐 | Extruder |
| CN102834232B (en) * | 2010-03-24 | 2014-12-03 | 约瑟夫·布拉赫 | extruder |
| RU2568726C2 (en) * | 2010-03-24 | 2015-11-20 | БЛАХ Йозеф | Extruder |
| WO2013128463A1 (en) * | 2012-02-28 | 2013-09-06 | Steer Engineering Private Limited | An extruder mixing element |
| US11312041B2 (en) | 2012-02-28 | 2022-04-26 | Steer Engineering Private Limited | Extruder mixing element |
| US10207423B2 (en) | 2012-02-28 | 2019-02-19 | Steer Engineering Private Limited | Extruder mixing element for a co-rotating twin screw extruder |
| US20150138909A1 (en) * | 2012-05-23 | 2015-05-21 | Josef A. Blach | Multi-shaft extruder |
| AT512974B1 (en) * | 2012-05-23 | 2015-02-15 | Josef A Ing Blach | Multi-screw extruder |
| AT512974A1 (en) * | 2012-05-23 | 2013-12-15 | Blach | Multi-screw extruder |
| US10414081B2 (en) * | 2012-05-23 | 2019-09-17 | Blach Verwaltungs Gmbh & Co. Kg | Multi-shaft extruder |
| WO2013174878A1 (en) * | 2012-05-23 | 2013-11-28 | Blach Josef A | Multi-screw extruder with self-cleaning conveyor screws |
| RU2618565C2 (en) * | 2012-05-23 | 2017-05-04 | Йозеф А. Блах | Multi-roll extruder with self-cleaning furnish rolls |
| RU2673517C2 (en) * | 2013-06-24 | 2018-11-27 | Ковестро Дойчланд Аг | Screw elements for multi-shaft screw-type machines |
| DE202015104764U1 (en) | 2015-09-08 | 2016-01-12 | Blach Verwaltungs GmbH + Co. KG | Ring extruder for continuous preparation of rubber compounds with co-extruder |
| DE102015120583A1 (en) | 2015-09-08 | 2017-03-09 | Blach Verwaltungs GmbH + Co. KG | Ring extruder for continuous preparation of rubber compounds with co-extruder |
| DE102015120585B4 (en) * | 2015-09-08 | 2018-04-12 | Blach Verwaltungs GmbH + Co. KG | Plant for the continuous preparation of rubber compounds with barrel press |
| DE102015120586B4 (en) | 2015-09-08 | 2018-10-18 | Blach Verwaltungs Gmbh & Co. Kg | Ring extruder for the continuous preparation of rubber material with co-extruder, system and process for preprocessing a continuously processed rubber material |
| DE102015120585A1 (en) | 2015-09-08 | 2017-03-09 | Blach Verwaltungs GmbH + Co. KG | Plant for the continuous preparation of rubber compounds with barrel press |
| DE102015120586A1 (en) | 2015-09-08 | 2017-03-09 | Blach Verwaltungs Gmbh & Co. Kg | Ring extruder for the continuous preparation of rubber compounds with co-extruder and cooling system |
| DE202015104765U1 (en) | 2015-09-08 | 2016-01-12 | Blach Verwaltungs GmbH + Co. KG | Plant for the continuous preparation of rubber compounds with barrel press |
| DE102015120583B4 (en) | 2015-09-08 | 2020-07-23 | Blach Verwaltungs GmbH + Co. KG | Multi-shaft extruder and system for the continuous preparation of rubber compounds with a co-extruder |
| DE202015106285U1 (en) | 2015-11-18 | 2016-01-11 | Blach Verwaltungs Gmbh & Co. Kg | Ring extruder for the continuous preparation of rubber compounds with co-extruder and cooling system |
| DE102017123940A1 (en) | 2016-10-14 | 2018-05-09 | Blach Verwaltungs GmbH + Co. KG | Augmented reality at extruder plant |
| CN112223720A (en) * | 2020-09-28 | 2021-01-15 | 南京卓越挤出装备有限公司 | High groove depth screw element |
| WO2023198550A1 (en) | 2022-04-11 | 2023-10-19 | Covestro Deutschland Ag | Multi-shaft screw machine comprising a pair of screw elements having an improved mixing and degassing effect with reduced energy input |
Also Published As
| Publication number | Publication date |
|---|---|
| DE102008016862C5 (en) | 2019-12-19 |
| DE102008016862B4 (en) | 2014-11-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE102008016862B4 (en) | extruder | |
| EP2454078B1 (en) | Extruder | |
| DE4134026C2 (en) | Co-rotating screw kneader | |
| EP1390189B1 (en) | Homogenizing and/or dispersing device comprising endless screws | |
| EP0788867B1 (en) | Apparatus for continuous processing of flowable materials | |
| EP1526959B1 (en) | Extruder for the continuous handling and/or processing of free-flowing materials | |
| EP1829660B1 (en) | Mixer and kneader for plastics | |
| EP2550141B1 (en) | Extruder | |
| DE10233213B4 (en) | extruder | |
| EP2852485B1 (en) | Multi-screw extruder with self-cleaning conveyor screws | |
| DE102004052055B4 (en) | extruder | |
| DE10207145B4 (en) | Device for dispersing and melting flowable materials | |
| DE19622582C2 (en) | Device for the continuous processing of flowable materials | |
| DE102018128884A1 (en) | Multi-screw system and process for processing polymer melt with it | |
| DE4308098A1 (en) | Planetary-gear extruder | |
| DE2802125A1 (en) | Multi-screw homogenising extruder - with intermeshing disc section to restrict axial flow | |
| DE102005048847A1 (en) | conveyor | |
| EP3253554B1 (en) | Stuffing screw | |
| DE102015014865A1 (en) | Multi-shaft continuous mixing and kneading machine for plasticizable masses | |
| DE202005005212U1 (en) | Extruder advancing worm comprises at least two worm sections with a hub and a screw shaped spiral | |
| DE4025960C2 (en) | Mixed part structure for extruder screws | |
| DE20015290U1 (en) | Double screw extruder |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| OP8 | Request for examination as to paragraph 44 patent law | ||
| R016 | Response to examination communication | ||
| R016 | Response to examination communication | ||
| R018 | Grant decision by examination section/examining division | ||
| R026 | Opposition filed against patent | ||
| R079 | Amendment of ipc main class |
Free format text: PREVIOUS MAIN CLASS: B29C0047400000 Ipc: B29C0048400000 |
|
| R034 | Decision of examining division/federal patent court maintaining patent in limited form now final | ||
| R206 | Amended patent specification |