EP1249219B1 - Method and apparatus for manufacturing shaped bodies made of a biopolymer material - Google Patents
Method and apparatus for manufacturing shaped bodies made of a biopolymer material Download PDFInfo
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- EP1249219B1 EP1249219B1 EP00128701A EP00128701A EP1249219B1 EP 1249219 B1 EP1249219 B1 EP 1249219B1 EP 00128701 A EP00128701 A EP 00128701A EP 00128701 A EP00128701 A EP 00128701A EP 1249219 B1 EP1249219 B1 EP 1249219B1
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- strip
- heat treatment
- material strip
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- shaped bodies
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61J—CONTAINERS SPECIALLY ADAPTED FOR MEDICAL OR PHARMACEUTICAL PURPOSES; DEVICES OR METHODS SPECIALLY ADAPTED FOR BRINGING PHARMACEUTICAL PRODUCTS INTO PARTICULAR PHYSICAL OR ADMINISTERING FORMS; DEVICES FOR ADMINISTERING FOOD OR MEDICINES ORALLY; BABY COMFORTERS; DEVICES FOR RECEIVING SPITTLE
- A61J3/00—Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms
- A61J3/07—Devices or methods specially adapted for bringing pharmaceutical products into particular physical or administering forms into the form of capsules or similar small containers for oral use
Definitions
- the invention relates to a method and an apparatus for producing shaped articles, in particular capsules, from a biopolymer material, in particular based on starch, according to the preamble of the independent claims 1 and 8.
- Shaped bodies, in particular capsules, are today produced in continuous, automatable processes from endless material strips.
- the production of the shaped body shell and the filling of the same happens, in particular in one-piece capsules, in a single step.
- moldings are made, from which the capsule shells are assembled during and after filling by welding the outer edges of the moldings.
- the molding is done either by means of diverging and merging forms, e.g. in the Norton, Banner and Schering processes or by means of rotating forming rolls, as e.g. in the rotary-die process and in the accordogel process ("The Capsule” Fahrig / Hofer, Stuttgart, 1983, Lachmann / Liebermann / Kanig, "The Theory and Practice of Industrial Pharmacy", Third Edition, Philadelphia 1986).
- the filling takes place with the aid of metering pumps, which deliver a defined amount of active substance during the punching and welding of the molded parts to form a one-piece capsule shell.
- Welding i.
- the seams
- the production process for moldings made of endless material straps makes a number of demands.
- One of the main requirements is the ability to use endless material belts To form a sufficient strength, which have a sufficient elongation at break and elasticity.
- Gelatin bands in particular for soft gelatine capsules, can be prepared from a homogeneous mass of gelatin and water which is readily flowable at 40 ° C. to 80 ° C., which usually also contains additives such as glycerol and sorbitol. This is done at atmospheric pressure, where the mass of so-called spreaders is gravity poured or extruded through a slot on a cooled drum. The mass should solidify at about 15 ° C to 25 ° C (gel state). At lower extrusion temperatures, the water content must be increased to lower the melting point and viscosity, or extrusion under pressure must be performed. At extrusion temperatures above 100 ° C there is a risk that the mixture foams on exiting from the so-called spreader.
- EP 0 397 819 a process for producing thermoplastically processable starch, wherein the crystalline fraction in the starch is less than 5%.
- the process consists of mixing native starch with at least 10% by weight of an aggregate having a solubility parameter of at least 30.7 (MPa) 1/2 .
- the mixture is transferred under heat in a temperature range between 120 ° C and 220 ° C in a melt, wherein an internal pressure of about 30 to 300 bar can be assumed.
- the water content of the starch is already reduced to less than 5% in the melt.
- the starch film which after the in EP 397 819
- the disclosed method does not show the weldability or seam strength, which would meet the quality requirements of one-piece molded body shells, in particular capsule shells.
- a method and an apparatus for producing Formed bodies are made of endless belts based on biopolymers, which allow the production of reproducible moldings, especially when the base mass of the belts is extruded under pressure and / or at high temperatures.
- the material band between the extrusion die and the die is subjected to at least one heat treatment to reduce stresses at a treatment station.
- the temperature for the heat treatment must be selected so that the desired relaxation of the material bands results and the belt can be controlled without further stress build-up. This temperature depends on the process and the material.
- the desired relaxation in the context of the invention is achieved when the strip after the heat treatment no longer anisotropic but has isotropic mechanical properties, so that the mechanical properties of the strip in the longitudinal direction and in the transverse direction to a good approximation are identical.
- a definition for the term pair "anisotropic / isotropic" can be found in Römpp Chemie Lexikon, ed.: J. Falbe, M. Regitz, 9th edition, 1992, Georg Thieme Verlag, Stuttgart.
- the tapes treated according to the invention thus also have a uniform elongation at break and a uniform elastic modulus E over the entire material strip.
- an elongation at break of at least 100% and a modulus of elasticity of less than or equal to 2 MPa in the temperature range from 40 ° C. to 80 ° C. are particularly advantageous.
- the measurement of the elongation at break and the modulus of elasticity E can be carried out according to DIN standard 53455 or DIN EN ISO 527-1 to ISO 527-3.
- the elongation at break is measured according to this DIN standard at the corresponding encapsulation temperature.
- At least one material strip is extruded and then subjected to heat at a treatment arrangement.
- a treatment arrangement it is also possible to extrude a plurality of material strips and then to subject them to a heat treatment.
- molded body is to be understood as meaning any type of molded article which is suitable for receiving a filling material and sealingly enclosing it in the interior.
- This includes not only capsules but also other forms such. B. balls, pillows and figures.
- B. balls, pillows and figures To date, there are numerous developments and deviations from the basic principle of the capsule.
- Biopolymers materials in the context of the invention are all materials that can be extruded by suitable methods to endless material bands. According to the invention, this also includes physically and / or chemically modified biopolymers. Examples of biopolymers according to the invention are cellulose, in particular partially hydroxypropylated cellulose, alginates, carrageenan, galactomannans, glucomannans, casein and starch. Likewise, mixtures of different biopolymer materials within the meaning of the invention are conceivable.
- starch should be understood to mean native starches as well as physically and / or chemically modified starches.
- all starches irrespective of the plant from which they are obtained, are suitable.
- it is starch whose amylopectin content is more than 50% based on the total weight of the anhydrous starch.
- Potato starch is particularly suitable.
- the process according to the invention can be an integral part of a known process for the production of moldings from endless bands of material, such as e.g. the Norton, Banner and Schering process or the methods by means of rotating forming rolls, e.g. realized in the Rotary-Die process and in the Accogel process ("The capsule” Fahrig / Hofer, editors, Stuttgart, 1983, Lachmann / Liebermann / Kanig, "The Theory and Practice of Industrial Pharmacy", Third Edition, Philadelphia 1986).
- At least two material strips are processed according to the Rotary-Die principle into moldings, wherein each of the material strips is subjected to at least one heat treatment between extrusion and processing into moldings at a treatment station.
- the Rotary Die process with rotating forming rolls has been known and used for many years and today represents one of the most widespread encapsulation processes for the production of pharmaceutical, dietetic and technical shaped bodies.
- the endless material bands are applied to both sides with heat.
- the heat treatment can be effected by radiation, in particular by IR radiation.
- IR radiation in particular by IR radiation.
- the use of ultrasound, microwave and other suitable radiation sources for heating is conceivable.
- the material bands are passed to a radiator or through a preheated cavity of a treatment arrangement, in particular passed through a heating tunnel.
- the material strips are passed through a heatable bath, in particular an oil bath.
- a heatable bath in particular an oil bath.
- the bath temperature is preferably maintained in a range between 40 ° C and 80 ° C.
- the tension of the material strips is kept constant with a compensating means, in particular with the aid of at least one dancer roller.
- Overlengths can z. B. by unequal or fluctuating rotational speeds of responsible for the movement of the endless material belts means of transportation, especially roles, arise.
- Another object of the present invention is an apparatus for producing moldings, in particular capsules, from a biopolymer material, in particular based on starch, with at least one extrusion tool for extruding an endless material strip and at least one molding tool for processing the material strip under the influence of a filling material to moldings wherein between the extrusion die and the mold at least one treatment station for applying the material strip is arranged with heat.
- the treatment arrangement has at least one radiation source, in particular an infrared radiation source. Also conceivable are combinations of different radiation sources.
- the treatment station has at least one heating element, wherein the material strips are acted upon by convection heat.
- the device according to the invention comprises a heatable bath, in particular an oil bath.
- a heatable bath in particular an oil bath.
- an oil is used, which is harmless from a pharmaceutical and toxicological point of view in the subsequent application of the moldings.
- oils are known and listed in the relevant legislation.
- the oil bath can be mixed with other additives that the properties of the material bands, such. B. affect elasticity or elongation at break positive.
- a heatable oil bath is particularly suitable for relaxing material strips, in particular based on starch.
- the device has at least one stripping device for stripping off liquid from the surface of the material strips between the oil bath and the molding tool.
- the stripping device can be designed such that the film thickness of the film remaining on the surface of the material strips can be predetermined.
- the device has at least one compensating means, in particular a dancer roller, for maintaining a uniform longitudinal tension of the material bands.
- a compensating means in particular a dancer roller, for maintaining a uniform longitudinal tension of the material bands.
- Unlength of the bands z. B. arise by non-synchronous means of transport, can be compensated. In particular, so can the tension so be kept as low as possible, particularly advantageous below 0.5 Mpa.
- the mold of the apparatus is a rotary die apparatus having two forming rolls and a filling wedge.
- the device has at least one adjustable positioning arrangement on which the extrusion tool and the molding tool can be adjusted relative to one another.
- a rigid but adjustable arrangement of extrusion and molding tool is achieved relative to each other.
- the positioning could z. B. have a displaceable on a rail machine frame for the extrusion tool.
- FIG. 1 shows a schematic representation of an inventive device for producing moldings from endless material bands in the rotary die process.
- the rotary die machine shown is used in a known manner for the processing of two endless material bands 15, 15 '.
- the material strips are extruded on each of an extrusion die 1, 1 'on the extruder 13 of slot dies 10 and withdrawn, each with a pair of rollers 7a, 7b and rolled to a constant thickness.
- the extruders 13 are continuously supplied with biopolymeric material 12, in particular with starch-based material.
- the extruded material strips 15 are fed to a mold 2 in a known manner. Shown is a substantially horizontal supply of material strips to the mold. Of course it is also conceivable the material bands in any to supply another angle to the mold. A vertical feed is particularly advantageous because it allows the load on the strip to be minimized by gravity.
- the molding tool consists of two molding rolls 4a, 4b, wherein in the surfaces of the molding rolls 4a, 4b, the recesses required for the deformation of the molded body 11, in particular to capsules, are arranged.
- a filling wedge 5 is arranged, through which by means of a feed pump 6 from a Golfguttank 8 filling material 9 between the material belts 15, 15 'is introduced, wherein the material bands are deformed on the forming rollers 4a, 4b to capsules 11.
- a feed pump 6 from a Greintank 8 filling material 9 between the material belts 15, 15 'is introduced, wherein the material bands are deformed on the forming rollers 4a, 4b to capsules 11.
- liquid, pasty or, in certain cases, also powdery filling material 9 is also conceivable is the encapsulation of pellets, tablets and much more.
- the material strips 15 between the extrusion die 1 and the die 2 are subjected to heat at a treatment arrangement 3a, 3b.
- the heat treatment in the embodiment shown by radiation z.
- different guide and / or drive rollers 20 can be attached at corresponding locations.
- FIG. 2 shows a schematic representation of an inventive device for producing moldings from endless material bands 15, 15 'in the Norton process.
- a material strip 15, 15 ' are extruded from an extrusion die 1 and stripped with a pair of rollers 7 and rolled to the correct thickness.
- the material strip 15 ' is guided in the region between the extrusion die 1 and the die 2 by a treatment station 3 for applying heat.
- the heat is generated by the radiator 24 in a heating tunnel 26.
- the material strip 15 ' can be guided via corresponding guide and / or drive rollers 20 to the mold 2.
- the dancer roller 21 is accordingly movable on an axis perpendicular to the direction of movement of the material strip 15 by a distance D required for maintaining the longitudinal tension of the material strip 15.
- the dancer roller could also be used to measure the actual tension on a sensor 29.
- the sensor could therefore also be used for feed control or for emergency shutdown with inadmissible tension. It is particularly favorable if the tensile stress is kept below 0.5 MPa.
- the material band 15 in the Norton process in a known manner into shaped bodies 11, in particular capsules shaped.
- the capsules are formed between a preforming unit 17 and a capsule forming unit 16.
- the capsules are preformed in a hose-like manner and filled via filling channels 18, which are supplied via a filling material feed 14.
- the final encapsulation takes place.
- the capsule is preformed lengthwise in the upper mold part, the preforming unit 17. It remains open at the top to allow the addition of the filling material 9.
- FIG. 3 shows a schematic representation of an alternative embodiment of an inventive device.
- the material strip 15 extruded from an extrusion die 1 is supplied to an oil bath 27 via drive rollers 19, which are driven by a motor M.
- the oil bath 27 can be heated via a heating unit 28.
- the desired relaxation of the material strip 15 is achieved by the release of conserved stresses.
- the material band 15 is lubricated by the oil bath 27.
- a dancer roller 21 is mounted in the region of the oil bath 27.
- the dancer roller 21 is otherwise the same design as in the embodiment according to FIG. 2 ,
- the material strip 15 is supplied on leaving the oil bath 27 of a stripping device 22. Excess oil can be removed from the surface of the material strip 15 on this stripping device 22.
- the stripping device 22 can be designed so that the film thickness of the oil film remaining on the surface of the material strips 15 can be set to a predeterminable value.
- the relaxed material band as already shown via guide rollers 20 is fed to a mold 2.
- this is the molding tool 2 of a device operated in the rotary-die method. This method has a particularly favorable effect from that additional heat was introduced in the embodiment shown by the oil bath on the starch ribbon 15. As a result, the segment temperature in the region of the filling wedge 5 can be kept low.
- FIG. 4 shows a diagram of the elongation at break of starch bands 15 before and after treatment with the inventive method.
- the elongation at break can be measured according to DIN standard 53455. Shown is in FIG. 4 the elongation at break in percent as a function of the temperature. Both the values for the elongation at break in the longitudinal direction and in the transverse direction of the starch strips 15 were determined.
- the elongations at break of at least 100% required for the forming process of the material strip 15 to form a shaped body 11 are achieved over the entire temperature range, both in the longitudinal direction and in the transverse direction. This is particularly important because a minimum elongation at break of 100% is necessary to encapsulate with existing Rotary-Die processes.
- FIG. 4 Clear that the elongation at break in the longitudinal and transverse directions before treatment with the inventive method are different.
- the starch band has anisotropic mechanical properties, which are due in particular to the resulting during the extrusion of the tapes conserved voltages.
- the processing of anisotropic ribbons can lead to bulky shaped bodies, in particular capsules, which increasingly also get caught in the forming rollers and hinder the production process.
- the starch ribbon 15 is relaxed after heat treatment and has isotropic properties.
- the measured breaking elongation of the material strips 15 is identical in the longitudinal direction and in the transverse direction to a good approximation. In the further processing of such material strips uniform moldings 11 are formed, which do not get caught in the forming rollers.
- FIG. 5 shows a diagram of the elastic modulus of thickness bands 15 before and after treatment with the inventive method.
- the measurement of the modulus of elasticity E can be carried out according to DIN EN ISO 527-1 to ISO 527-3.
- the modulus of elasticity in particular in the range of 40 ° C. to 80 ° C., which is important for the processing of the material bands 15 into shaped bodies 11, is significantly reduced to 2 MPa and less. This is particularly important because a modulus of elasticity of at most 2 MPa is necessary to perform encapsulation with existing Rotary-Die methods.
- the maximum pressure resp. the residence time of the material bands in Medkeil Symposium be chosen so that the material band can be "inflated" to a capsule.
- the filling wedge floats freely on the forming rollers and ensures the seal. The pressure can therefore not be increased arbitrarily, otherwise the filling material runs out between the material band and filling wedge.
- a deep modulus of elasticity of the material bands 15 plays a crucial role.
- the method according to the invention thus proves to be particularly advantageous with regard to the reduction of the modulus of elasticity achieved thereby.
- the material properties of the material strips are optimized for subsequent processing into shaped bodies.
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Abstract
Description
Die Erfindung betrifft ein Verfahren und eine Vorrichtung zum Herstellen von Formkörpern, insbesondere Kapseln, aus einem biopolymeren Material, insbesondere auf der Basis von Stärke gemäss dem Oberbegriff der unabhängigen Ansprüche 1 und 8.The invention relates to a method and an apparatus for producing shaped articles, in particular capsules, from a biopolymer material, in particular based on starch, according to the preamble of the
Formkörper, insbesondere Kapseln, werden heute in kontinuierlichen, automatisierbaren Verfahren aus endlosen Materialbändern hergestellt. Die Herstellung der Formkörperhülle und das Füllen derselben geschieht dabei, insbesondere bei einteiligen Kapseln, in einem einzigen Arbeitsschritt. In diesen kontinuierlichen Verfahren werden Formteile gefertigt, aus denen die Kapselhüllen während und nach dem Füllen durch Verschweissen der Aussenkanten der Formteile zusammengefügt werden. Die Formteilfertigung geschieht entweder mittels auseinander- und zusammengehender Formen, wie z.B. im Norton-, Banner- und Schering-Prozess oder mittels rotierender Formwalzen, wie es z.B. im Rotary-Die-Prozess und im Accogel-Verfahren verwirklicht ist ("Die Kapsel" Fahrig/Hofer Herausgeber, Stuttgart, 1983; Lachmann/Liebermann/Kanig, "The Theory and Practice of Industrial Pharmacy"; Third Edition, Philadelphia 1986). Das Füllen erfolgt mit Hilfe von Dosierpumpen, die eine definierte Menge Wirksubstanz während des Ausstanzens und Verschweissens der Formteile zur Bildung einer einteiligen Kapselhülle abgeben. Das Verschweissen, d.h. die Ausbildung der Nähte erfolgt generell durch Druck und Wärme.Shaped bodies, in particular capsules, are today produced in continuous, automatable processes from endless material strips. The production of the shaped body shell and the filling of the same happens, in particular in one-piece capsules, in a single step. In this continuous process moldings are made, from which the capsule shells are assembled during and after filling by welding the outer edges of the moldings. The molding is done either by means of diverging and merging forms, e.g. in the Norton, Banner and Schering processes or by means of rotating forming rolls, as e.g. in the rotary-die process and in the accordogel process ("The Capsule" Fahrig / Hofer, Stuttgart, 1983, Lachmann / Liebermann / Kanig, "The Theory and Practice of Industrial Pharmacy", Third Edition, Philadelphia 1986). The filling takes place with the aid of metering pumps, which deliver a defined amount of active substance during the punching and welding of the molded parts to form a one-piece capsule shell. Welding, i. The seams are generally formed by pressure and heat.
Der Herstellungsprozess für Formkörper aus endlosen Materialbändern stellt dabei eine Reihe von Anforderungen. Eine der Hauptvoraussetzungen ist die Fähigkeit, endlose Materialbänder mit einer ausreichenden Festigkeit auszubilden, welche über eine ausreichende Bruchdehnung und Elastizität verfügen.The production process for moldings made of endless material straps makes a number of demands. One of the main requirements is the ability to use endless material belts To form a sufficient strength, which have a sufficient elongation at break and elasticity.
Wenn Gelatine als Basismaterial verwendet wird, lassen sich Materialbänder herstellen, die all diese Bedingungen in nahezu idealer Weise erfüllen.When gelatine is used as the base material, it is possible to produce material ribbons which fulfill all these conditions in an almost ideal manner.
Gelatinebänder insbesondere für Weichgelatinekapseln, können aus einer bei 40°C bis 80°C gut fliessfähigen homogenen Masse aus Gelatine und Wasser, welche meist noch Zusätze wie Glycerol und Sorbitol enthält, hergestellt werden. Dies geschieht bei Atmosphärendruck, wobei die Masse aus sogenannten Spreadern unter Schwerkraft durch einen Schlitz auf eine gekühlte Trommel gegossen oder extrudiert wird. Dabei soll die Masse bei ca. 15°C bis 25°C erstarren (Gel-Zustand). Bei tieferen Extrusionstemperaturen muss der Wasseranteil erhöht werden, um Schmelzpunkt und Viskosität zu erniedrigen oder es muss eine Extrusion unter Druck durchgeführt werden. Bei Extrusionstemperaturen über 100°C besteht die Gefahr, dass die Mischung beim Austreten aus dem sogenannten Spreader schäumt.Gelatin bands, in particular for soft gelatine capsules, can be prepared from a homogeneous mass of gelatin and water which is readily flowable at 40 ° C. to 80 ° C., which usually also contains additives such as glycerol and sorbitol. This is done at atmospheric pressure, where the mass of so-called spreaders is gravity poured or extruded through a slot on a cooled drum. The mass should solidify at about 15 ° C to 25 ° C (gel state). At lower extrusion temperatures, the water content must be increased to lower the melting point and viscosity, or extrusion under pressure must be performed. At extrusion temperatures above 100 ° C there is a risk that the mixture foams on exiting from the so-called spreader.
Aus
Es hat sich gezeigt, dass die normalerweise angewandte drucklose Extrusionstechnik bei Gelatinebändern sich nicht auf andere Biopolymere, insbesondere mit Basismassen aus Stärke, welche Stärke und Wasser sowie gegebenenfalls Zusätze wie Glycerol oder Sorbitol enthalten, übertragen lässt, da sich die wasserhaltigen Filme auch bei Temperaturen weit unter der Extrusionstemperatur wegen ungenügender mechanischer Eigenschaften schlecht handhaben lassen. Es bildet sich kein Gelzustand bzw. der Erweichungsresp. Schmelzbereich ist sehr gross, so dass bei tiefen Temperaturen keine Festigkeit erreicht wird, während bei Temperaturen um die 100° noch keine ausreichenden Fliesseigenschaften vorhanden sind. Die Herstellung entsprechender endloser Materialbänder aus anderen Biopolymeren, insbesondere aus Stärke, gestaltet sich deshalb schwierig. Die Bänder weisen oft nicht die zur Weiterverarbeitung geforderten Eigenschaften, insbesondere bezüglich Bruchdehnung und Elastizität auf.It has been found that the normally used unpressurized extrusion technique in gelatin tapes can not be transferred to other biopolymers, in particular base starch bases which contain starch and water and, if appropriate, additives such as glycerol or sorbitol, since the water-containing films also extend far at temperatures can be handled poorly under the extrusion temperature due to insufficient mechanical properties. It forms no gel state or the softening resp. Melting range is very large, so that at low temperatures, no strength is achieved, while at temperatures around 100 ° are still no sufficient flow properties. The production of corresponding endless belts of material from other biopolymers, especially from starch, is therefore difficult. The bands often do not have the properties required for further processing, in particular with regard to elongation at break and elasticity.
So zeigt
Der Stärkefilm, welcher nach dem in
In der
Besonders nachteilig wirkt sich dies aus, wenn beim Füllen der Formkörper und anschliessendem Verschweissen die Materialbänder bei einer kurzen Verweildauer unvollständig erwärmt werden. Spannungen werden dabei unkontrolliert freigesetzt. Dies kann zu asymmetrischen und/oder deformierten Formkörpern führen. Dies ist für eine Routineproduktion bei der die Formkörper eine Masshaltigkeit von +/- 0.5 mm aufweisen müssen, nicht tolerierbar. Bei Normalgebrauch und bei Verarbeitung, insbesondere Verpakkung, der Formkörper ist aber die Masshaltigkeit und Ästhetik der Formkörper ein ausserordentlich wichtiger und unverzichtbarer Anteil.This is particularly disadvantageous when the material strips are incompletely heated during a short residence time during filling of the molded body and subsequent welding. Voltages are released uncontrollably. This can lead to asymmetric and / or deformed moldings. This is not tolerable for a routine production in which the moldings must have a dimensional accuracy of +/- 0.5 mm. In normal use and processing, in particular packaging, the molded body but the dimensional accuracy and aesthetics of the moldings is an extremely important and indispensable share.
Es ist deshalb Aufgabe der vorliegenden Erfindung die erwähnten Nachteile aus dem Stand der Technik zu vermeiden. Insbesondere sollen ein Verfahren und eine Vorrichtung zum Herstellen von Formkörpern aus endlosen Bändern auf der Basis von Biopolymeren geschaffen werden, welche die Herstellung von reproduzierbaren Formkörpern ermöglichen, insbesondere auch dann, wenn die Basismasse der Bänder unter Überdruck und/oder bei hohen Temperaturen extrudiert wird.It is therefore an object of the present invention to avoid the mentioned disadvantages of the prior art. In particular, a method and an apparatus for producing Formed bodies are made of endless belts based on biopolymers, which allow the production of reproducible moldings, especially when the base mass of the belts is extruded under pressure and / or at high temperatures.
Erfindungsgemäss wird diese Aufgabe durch eine Vorrichtung nach Patentanspruch 8 und durch ein Verfahren mit den Merkmalen in den unabhängigen Patentansprüchen 1 und 16 gelöst.According to the invention this object is achieved by a device according to claim 8 and by a method having the features in the
Es wurde gefunden, dass sich aus der Extrusion der Materialbänder bei hohem Druck und/oder hoher Temperatur resultierende Spannungen der Materialbänder durch ein Beaufschlagen der Materialbänder mit Wärme, insbesondere unmittelbar vor deren Verarbeitung zu Formkörpern, abbauen lässt. Das Materialband wird durch die Beaufschlagung mit Wärme entspannt. Konservierte Spannungen werden freigesetzt vor der Verarbeitung der Materialbänder zu Formkörpern und können damit den fertigen Formkörper nicht mehr beeinflussen.It has been found that stresses resulting from the extrusion of the material strips at high pressure and / or high temperature can be reduced by subjecting the material strips to heat, in particular immediately before they are processed into shaped articles. The material band is relaxed by the application of heat. Preserved stresses are released before the processing of the material strips to moldings and thus can no longer influence the finished molded body.
Gemäss dem erfindungsgemässen Verfahren, wird dabei das Materialband zwischen dem Extrusionswerkzeug und dem Formwerkzeug zum Abbauen von Spannungen an einer Behandlungsstation wenigstens einer Wärmebehandlung unterworfen.According to the method according to the invention, the material band between the extrusion die and the die is subjected to at least one heat treatment to reduce stresses at a treatment station.
Die Temperatur für die Wärmebehandlung muss so gewählt sein, dass die gewünschte Entspannung der Materialbänder resultiert und das Band kontrolliert- ohne weiteren Spannungsaufbau geführt werden kann. Diese Temperatur ist prozess- und materialabhängig. Die gewünschte Entspannung im Sinne der Erfindung ist dann erreicht, wenn das Band nach der Wärmebehandlung nicht mehr anisotrope sondern isotrope mechanische Eigenschaften aufweist, so dass die mechanischen Eigenschaften des Bandes in Längsrichtung und in Querrichtung in guter Näherung identisch sind. Eine Definition für das Begriffspaar "anisotrop / isotrop" findet sich in Römpp Chemie Lexikon, Hrsg: J. Falbe, M. Regitz, 9. Auflage, 1992, Georg Thieme Verlag, Stuttgart.The temperature for the heat treatment must be selected so that the desired relaxation of the material bands results and the belt can be controlled without further stress build-up. This temperature depends on the process and the material. The desired relaxation in the context of the invention is achieved when the strip after the heat treatment no longer anisotropic but has isotropic mechanical properties, so that the mechanical properties of the strip in the longitudinal direction and in the transverse direction to a good approximation are identical. A definition for the term pair "anisotropic / isotropic" can be found in Römpp Chemie Lexikon, ed.: J. Falbe, M. Regitz, 9th edition, 1992, Georg Thieme Verlag, Stuttgart.
Die erfindungsgemäss behandelten Bänder weisen damit auch über das ganze Materialband eine gleichmässige Bruchdehnung und ein gleichmässiges Elastizitätsmodul E auf. Für die Verarbeitung von Materialbändern zu Formkörpern, insbesondere zur Herstellung von Weichkapseln im Rotary-Die Prozess sind eine Bruchdehnung von wenigstens 100% und ein Elastizitätsmodul von kleiner oder gleich 2 MPa im Temperaturbereich von 40°C bis 80°C besonders vorteilhaft.The tapes treated according to the invention thus also have a uniform elongation at break and a uniform elastic modulus E over the entire material strip. For the processing of material strips into moldings, in particular for the production of soft capsules in the rotary process, an elongation at break of at least 100% and a modulus of elasticity of less than or equal to 2 MPa in the temperature range from 40 ° C. to 80 ° C. are particularly advantageous.
Die Messung der Bruchdehnung und des Elastizitätsmoduls E kann nach DIN-Norm 53455 bzw. DIN EN ISO 527-1 bis ISO 527-3 erfolgen. Die Bruchdehnungsmessung erfolgt nach dieser DIN Norm bei der entsprechenden Verkapselungstemperatur.The measurement of the elongation at break and the modulus of elasticity E can be carried out according to DIN standard 53455 or DIN EN ISO 527-1 to ISO 527-3. The elongation at break is measured according to this DIN standard at the corresponding encapsulation temperature.
Erfindungsgemäss wird wenigstens ein Materialband extrudiert und anschliessend an einer Behandlungsanordnung mit Wärme beaufschlagt. Selbstverständlich können entsprechend dem jeweils gewählten Verfahren zur Herstellung der Formkörper auch mehrere Materialbänder extrudiert und anschliessend einer Wärmebehandlung unterzogen werden.According to the invention, at least one material strip is extruded and then subjected to heat at a treatment arrangement. Of course, according to the particular method chosen for producing the shaped bodies, it is also possible to extrude a plurality of material strips and then to subject them to a heat treatment.
Im Sinne der Erfindung sollen unter dem Begriff Formkörper jegliche Art von Formkörpern verstanden werden, die geeignet sind ein Füllmaterial aufzunehmen und dichtend im Innern einzuschliessen. Dazu gehören nicht nur Kapseln sondern auch andere Formen wie z. B. Kugeln, Kissen und Figuren. Bis heute existieren zahlreiche Weiterentwicklungen und Abweichungen vom grundlegenden Prinzip der Kapsel.For the purposes of the invention, the term molded body is to be understood as meaning any type of molded article which is suitable for receiving a filling material and sealingly enclosing it in the interior. This includes not only capsules but also other forms such. B. balls, pillows and figures. To date, there are numerous developments and deviations from the basic principle of the capsule.
Biopolymere Materialien im Sinne der Erfindung sind alle Materialien, die durch geeignete Verfahren zu endlosen Materialbändern extrudiert werden können. Dazu gehören erfindungsgemäss auch physikalisch und/oder chemisch modifizierte Biopolymere. Beispiele für erfindungsgemässe Biopolymere sind Cellulose, insbesondere teilhydroxypropylierte Cellulose, Alginate, Carrageenan, Galactomannane, Glucomannane, Casein und Stärke. Ebenso sind Mischungen verschiedener Biopolymerer Materialien im Sinne der Erfindung denkbar.Biopolymers materials in the context of the invention are all materials that can be extruded by suitable methods to endless material bands. According to the invention, this also includes physically and / or chemically modified biopolymers. Examples of biopolymers according to the invention are cellulose, in particular partially hydroxypropylated cellulose, alginates, carrageenan, galactomannans, glucomannans, casein and starch. Likewise, mixtures of different biopolymer materials within the meaning of the invention are conceivable.
Besonders bevorzugt wird Stärke. Unter dem Begriff Stärke sollen native Stärken, sowie physikalisch und/oder chemisch modifizierte Stärken verstanden werden. Für die im erfindungsgemässen Verfahren eingesetzten Basismaterialien sind alle Stärken, unabhängig von der Pflanze aus der sie gewonnen werden, geeignet. In einer bevorzugten Ausführungsform handelt es sich um Stärke, deren Amylopektingehalt über 50% bezogen auf das Gesamtgewicht der wasserfreien Stärke liegt. Besonders geeignet ist dabei Kartoffelstärke.Strength is particularly preferred. The term starch should be understood to mean native starches as well as physically and / or chemically modified starches. For the base materials used in the process according to the invention, all starches, irrespective of the plant from which they are obtained, are suitable. In a preferred embodiment, it is starch whose amylopectin content is more than 50% based on the total weight of the anhydrous starch. Potato starch is particularly suitable.
Im erfindungsgemässen Verfahren sind jedoch im weitesten Sinne alle Polyglucane, d.h. 1.4 und/oder 1.6 Poly-α-D-glucase und/oder Abmischungen zwischen diesen geeignet.However, in the process of the invention, in the broadest sense, all polyglucans, i. 1.4 and / or 1.6 poly-α-D-glucase and / or mixtures between them are suitable.
Die Herstellung von endlosen Materialbändern auf der Basis von Stärke sowie Verfahrensparameter und Materialeigenschaften sind in der Spät Veröffentlichen (30.5.2001)
Das erfindungsgemässe Verfahren kann integraler Bestandteil in einem bekannten Verfahren zur Herstellung von Formkörpern aus endlosen Materialbändern sein wie z.B. dem Norton-, Banner- und Schering-Prozess oder den Verfahren mittels rotierender Formwalzen, wie z.B. im Rotary-Die-Prozess und im Accogel-Verfahren verwirklicht ("Die Kapsel" Fahrig/Hofer, Herausgeber, Stuttgart, 1983; Lachmann/Liebermann/Kanig, "The Theory and Practice of Industrial Pharmacy"; Third Edition, Philadelphia 1986).The process according to the invention can be an integral part of a known process for the production of moldings from endless bands of material, such as e.g. the Norton, Banner and Schering process or the methods by means of rotating forming rolls, e.g. realized in the Rotary-Die process and in the Accogel process ("The capsule" Fahrig / Hofer, editors, Stuttgart, 1983, Lachmann / Liebermann / Kanig, "The Theory and Practice of Industrial Pharmacy", Third Edition, Philadelphia 1986).
Besonders bevorzugt werden wenigstens zwei Materialbänder nach dem Rotary-Die-Prinzip zu Formkörpern verarbeitet, wobei jedes der Materialbänder zwischen Extrusion und Verarbeitung zu Formkörpern an einer Behandlungsstation wenigstens einer Wärmebehandlung unterworfen wird. Das Rotary-Die-Verfahren mit rotierenden Formwalzen ist seit vielen Jahren bekannt und gebräuchlich und stellt heute eines der am meisten verbreiteten Verkapselungsverfahren für die Herstellung pharmazeutischer, diätetischer und technischer Formkörper dar.Particularly preferably, at least two material strips are processed according to the Rotary-Die principle into moldings, wherein each of the material strips is subjected to at least one heat treatment between extrusion and processing into moldings at a treatment station. The Rotary Die process with rotating forming rolls has been known and used for many years and today represents one of the most widespread encapsulation processes for the production of pharmaceutical, dietetic and technical shaped bodies.
In einem besonders bevorzugten Ausführungsbeispiel werden die endlosen Materialbänder beidseitig mit Wärme beaufschlagt. Die Wärmebehandlung kann dabei durch Strahlung, insbesondere durch IR-Strahlung erfolgen. Ebenso ist der Einsatz von Ultraschall, Mikrowelle und anderen geeigneten Strahlungsquellen zur Erwärmung denkbar.In a particularly preferred embodiment, the endless material bands are applied to both sides with heat. The heat treatment can be effected by radiation, in particular by IR radiation. Likewise, the use of ultrasound, microwave and other suitable radiation sources for heating is conceivable.
Denkbar ist es auch die Wärmebehandlung durch Konvektionswärme durchzuführen. Dabei werden die Materialbänder an einem Heizkörper vorbei oder durch einen vorgeheizten Hohlraum einer Behandlungsanordnung, insbesondere durch einen Heiztunnel hindurchgeführt.It is also conceivable to carry out the heat treatment by convection heat. The material bands are passed to a radiator or through a preheated cavity of a treatment arrangement, in particular passed through a heating tunnel.
Bei einer weiteren Variante des erfindungsgemässen Verfahrens werden die Materialbänder durch ein beheizbares Bad, insbesondere ein Ölbad hindurchgeführt. Damit kann neben der gewünschten Entspannung auch eine Schmierung der Materialbänder erreicht werden, welche für weitere Prozessschritte besonders vorteilhaft sein kann. Die Badtemperatur wird vorzugsweise in einem Bereich zwischen 40°C und 80°C gehalten.In a further variant of the method according to the invention, the material strips are passed through a heatable bath, in particular an oil bath. Thus, in addition to the desired relaxation, a lubrication of the material strips can be achieved, which can be particularly advantageous for further process steps. The bath temperature is preferably maintained in a range between 40 ° C and 80 ° C.
Besonders vorteilhaft ist es, wenn die Zugspannung der Materialbänder mit einem Ausgleichsmittel, insbesondere mit Hilfe wenigstens einer Tänzerwalze konstant gehalten wird. Überlängen können z. B. durch ungleiche oder schwankende Rotationsgeschwindigkeiten der für die Fortbewegung der endlosen Materialbänder verantwortlichen Fortbewegungsmittel, insbesondere Rollen, entstehen. Durch die Aufrechterhaltung einer gleichbleibenden Längsspannung wird insbesondere erreicht, dass negative Einflüsse auf die nach dem erfindungsgemässen Verfahren durch Beaufschlagung mit Wärme entspannten Materialbänder minimiert werden.It is particularly advantageous if the tension of the material strips is kept constant with a compensating means, in particular with the aid of at least one dancer roller. Overlengths can z. B. by unequal or fluctuating rotational speeds of responsible for the movement of the endless material belts means of transportation, especially roles, arise. By maintaining a constant longitudinal tension is achieved in particular that negative influences on the relaxed by the inventive method by applying heat relaxed material bands.
Ein weiterer Gegenstand der vorliegenden Erfindung ist eine Vorrichtung zum Herstellen von Formkörpern, insbesondere Kapseln, aus einem biopolymeren Material, insbesondere auf der Basis von Stärke, mit wenigstens einem Extrusionswerkzeug zum Extrudieren eines endlosen Materialbandes und wenigstens einem Formwerkzeug zum Verarbeiten des Materialbandes unter Einfluss einer Füllmasse zu Formkörpern wobei zwischen dem Extrusionswerkzeug und dem Formwerkzeug wenigstens eine Behandlungsstation zum Beaufschlagen des Materialbands mit Wärme angeordnet ist.Another object of the present invention is an apparatus for producing moldings, in particular capsules, from a biopolymer material, in particular based on starch, with at least one extrusion tool for extruding an endless material strip and at least one molding tool for processing the material strip under the influence of a filling material to moldings wherein between the extrusion die and the mold at least one treatment station for applying the material strip is arranged with heat.
In einem Ausführungsbeispiel weist die Behandlungsanordnung wenigstens eine Strahlungsquelle, insbesondere eine Infrarot-Strahlungsquelle auf. Denkbar sind auch Kombinationen verschiedener Strahlungsquellen.In one embodiment, the treatment arrangement has at least one radiation source, in particular an infrared radiation source. Also conceivable are combinations of different radiation sources.
Denkbar ist es auch, dass die Behandlungsstation wenigstens einen Heizkörper aufweist, wobei die Materialbänder durch Konvektionswärme beaufschlagt werden.It is also conceivable that the treatment station has at least one heating element, wherein the material strips are acted upon by convection heat.
Bei einer weiteren Variante (Patentanspruch 16) weist die erfindungsgemässe Vorrichtung ein beheizbares Bad, insbesondere ein Ölbad auf. Damit kann neben der gewünschten Entspannung auch eine Schmierung der Materialbänder erreicht werden. Im Ölbad wird ein Öl verwendet, welches aus pharmazeutischer und toxikologischer Sicht bei der späteren Applikation der Formkörper unbedenklich ist. Solche Öle sind bekannt und in der einschlägigen Gesetzgebung aufgelistet. Gegebenenfalls können dem Ölbad weitere Zusatzstoffe beigemischt werden, die die Eigenschaften der Materialbänder, wie z. B. Elastizität oder Bruchdehnung positiv beeinflussen.In a further variant (claim 16), the device according to the invention comprises a heatable bath, in particular an oil bath. Thus, in addition to the desired relaxation and lubrication of the material bands can be achieved. In the oil bath, an oil is used, which is harmless from a pharmaceutical and toxicological point of view in the subsequent application of the moldings. Such oils are known and listed in the relevant legislation. Optionally, the oil bath can be mixed with other additives that the properties of the material bands, such. B. affect elasticity or elongation at break positive.
Die Verwendung eines beheizbaren Ölbads eignet sich besonders gut zum Entspannen von Materialbändern, insbesondere auf der Basis von Stärke.The use of a heatable oil bath is particularly suitable for relaxing material strips, in particular based on starch.
Besonders vorteilhaft ist es, wenn die Vorrichtung zwischen Ölbad und Formwerkzeug wenigstens eine Abstreifvorrichtung zum Abstreifen von Flüssigkeit von der Oberfläche der Materialbänder aufweist. Die Abstreifvorrichtung kann dabei so ausgestaltet sein, dass die Filmdicke des auf der Oberfläche der Materialbänder zurückbleibenden Films vorbestimmbar ist.It is particularly advantageous if the device has at least one stripping device for stripping off liquid from the surface of the material strips between the oil bath and the molding tool. The stripping device can be designed such that the film thickness of the film remaining on the surface of the material strips can be predetermined.
In einem weiteren bevorzugten Ausführungsbeispiel weist die Vorrichtung wenigstens ein Ausgleichsmittel, insbesondere eine Tänzerwalze zur Aufrechterhaltung einer gleichmässigen Längsspannung der Materialbänder auf. Unlängen der Bänder die z. B. durch nicht synchrone Fortbewegungsmittel entstehen, können so ausgeglichen werden. Insbesondere kann so auch die Zugspannung so tief wie möglich, besonders vorteilhaft unter 0.5 Mpa gehalten werden.In a further preferred embodiment, the device has at least one compensating means, in particular a dancer roller, for maintaining a uniform longitudinal tension of the material bands. Unlength of the bands z. B. arise by non-synchronous means of transport, can be compensated. In particular, so can the tension so be kept as low as possible, particularly advantageous below 0.5 Mpa.
In einem besonders bevorzugten Ausführungsbeispiel ist das Formwerkzeug der Vorrichtung eine Rotary-Die-Vorrichtung mit zwei Formwalzen und einem Füllkeil.In a particularly preferred embodiment, the mold of the apparatus is a rotary die apparatus having two forming rolls and a filling wedge.
Vorteilhaft für die Prozessführung ist es, wenn auf beiden Seiten des Formwerkzeugs wenigstens je ein Extrusionswerkzeug derart angeordnet ist, dass das Materialband auf einer Förderebene ohne seitliche Auslenkung in das Formwerkzeug eingeführt wird. Durch das Weglassen von seitlichen Auslenkungen, wie sie insbesondere bei der Verarbeitung von Gelatinebändern teilweise stattfinden, wird verhindert, dass zusätzliche Spannungen auf die Bänder gelangen, welche zu anisotropen Materialeigenschaften führen können.It is advantageous for the process control if at least one respective extrusion tool is arranged on both sides of the molding tool in such a way that the material strip is introduced into the molding tool on a conveying plane without lateral deflection. By omitting lateral deflections, as they occur in particular in the processing of gelatin ribbons partially, it is prevented that additional strains reach the ribbons, which can lead to anisotropic material properties.
Besonders vorteilhaft ist es aus den genannten Gründen, wenn die Vorrichtung wenigstens eine verstellbare Positionieranordnung aufweist, an der das Extrusionswerkzeug und das Formwerkzeug relativ zueinander justierbar sind. Dadurch wird eine starre aber einstellbare Anordnung von Extrusions- und Formwerkzeug relativ zueinander erreicht. Damit lässt sich insbesondere das Übertragen von Spannungen auf die Materialbänder durch ungleich ausgerichtete Extrusions- und Formwerkzeuge verhindern. Die Positionieranordnung könnte z. B. ein auf einer Schiene verschiebbares Maschinengestell für das Extrusionswerkzeug aufweisen.For the reasons mentioned, it is particularly advantageous if the device has at least one adjustable positioning arrangement on which the extrusion tool and the molding tool can be adjusted relative to one another. As a result, a rigid but adjustable arrangement of extrusion and molding tool is achieved relative to each other. In particular, this makes it possible to prevent the transfer of stresses to the material strips by unevenly aligned extrusion and molding tools. The positioning could z. B. have a displaceable on a rail machine frame for the extrusion tool.
Ausführungsbeispiele der Erfindung sind in den Zeichnungen dargestellt und werden nachstehend genauer beschrieben. Es zeigen:
Figur 1- eine schematische Darstellung einer erfindungsgemässen Vorrichtung zum Herstellen von Formkörpern aus endlosen Materialbändern im Rotary-Die-Verfahren,
Figur 2- eine schematische Darstellung einer erfindungsgemässen Vorrichtung zum Herstellen von Formkörpern aus endlosen Materialbändern im Norton-Prozess,
Figur 3- eine schematische Darstellung eines alternativen Ausführungsbeispiels mit Flüssigkeitsbad,
- Figur 4
- ein Diagramm zur Bruchdehnung von Stärkebändern vor und nach Behandlung mit dem erfindungsgemässen Verfahren, und
Figur 5- ein Diagramm zum Young'schen Elastizitätsmodul von Stärkebändern vor und nach Behandlung mit dem erfindungsgemässen Verfahren.
- FIG. 1
- a schematic representation of an inventive device for producing moldings from endless material bands in the rotary die process,
- FIG. 2
- a schematic representation of an inventive device for producing moldings from endless material bands in the Norton process,
- FIG. 3
- a schematic representation of an alternative embodiment with liquid bath,
- FIG. 4
- a diagram of the elongation at break of starch bands before and after treatment with the inventive method, and
- FIG. 5
- a diagram for Young's modulus of strength bands before and after treatment with the inventive method.
Das Formwerkzeug besteht aus zwei Formwalzen 4a, 4b, wobei in den Oberflächen der Formwalzen 4a, 4b die zur Verformung der Formkörper 11, insbesondere zu Kapseln, erforderlichen Ausnehmungen angeordnet sind. Im Einzugszwickel des Formwalzenpaares 4a, 4b ist ein Füllkeil 5 angeordnet, durch den mittels einer Förderpumpe 6 aus einem Füllguttank 8 Füllgut 9 zwischen die Materialbänder 15, 15' eingeführt wird, wobei die Materialbänder an den Formwalzen 4a, 4b zu Kapseln 11 verformt werden. Als Füllgut 9 kann dabei flüssiges, pastöses oder in bestimmten Fällen auch pulverförmiges Füllgut 9 eingesetzt werden. Denkbar ist auch die Verkapselung von Pellets, Tabletten und vieles mehr.The molding tool consists of two
Erfindungsgemäss werden die Materialbänder 15 zwischen Extrusionswerkzeug 1 und Formwerkzeug 2 an einer Behandlungsanordnung 3a, 3b mit Wärme beaufschlagt. An der Behandlungsanordnung 3a erfolgt die Wärmebehandlung im gezeigten Ausführungsbeispiel durch Strahlung z. B. aus einer Infrarot-Strahlenquelle 23. Es ist aber auch denkbar wie in der Behandlungsanordnung 3b gezeigt, die Materialbänder 15, durch Konvektionswärme, welche durch Heizkörper 24, insbesondere Heizschlangen, erzeugt und in einen Hohlraum 25 abgegeben wird, zu erwärmen. Zur Fortbewegung und Führung der Materialbänder 15, 15' können an entsprechenden Stellen verschiedene Führungs- und/oder Antriebsrollen 20 angebracht sein.According to the invention, the material strips 15 between the extrusion die 1 and the
Besonders vorteilhaft ist es, wenn zum Ausgleichen von Überlängen der Materialbänder 15 welche durch asynchrone Bewegungen der Rollen 20 entstehen können, mit Hilfe einer Tänzerwalze 21 ausgeglichen werden. Damit die Längsspannung des Materialbandes 15 konstant gehalten werden. Die Tänzerwalze 21 ist entsprechend auf einer Achse senkrecht zur Laufrichtung des Materialbandes 15 um einen zur Aufrechterhaltung der Längsspannung des Materialbandes 15 benötigten Abstand D bewegbar. Über die Tänzerwalze könnte an einem Sensor 29 auch die tatsächliche Zugspannung gemessen werden. Der Sensor könnte daher auch zur Vorschubregelung oder zur Notabschaltung bei unzulässiger Zugspannung eingesetzt werden. Besonders günstig ist es, wenn die Zugspannung unter 0.5 MPa gehalten wird.It is particularly advantageous if, to compensate for excess lengths of the
Im Formwerkzeug 2 wird das Materialband 15 beim Norton-Prozess in bekannter Weise zu Formkörpern 11, insbesondere Kapseln, geformt. Die Formung der Kapseln erfolgt zwischen einer Einheit zu einer Vorformung 17 und einer Einheit zur Kapselformung 16. In den oberen Teilen der Einheiten 16, 17 werden die Kapseln schlauchartig vorgeformt und über Einfüllkanäle 18, welche über eine Füllmaterialzuführung 14 versorgt werden, gefüllt. Im unteren Teil der Einheit zur Kapselformung findet die endgültige Verkapselung statt. Mit jedem Schritt oder mit jedem Auseinanderdrücken und vor dem Zusammendrücken der Einheiten 16, 17 bewegt sich das Materialband 15 gerade um eine Kapsellänge vorwärts. Dabei wird im oberen Formteil, der Einheit zur Vorformung 17 die Kapsel der Länge nach vorgeformt. Sie bleibt oben offen, um die Zudosierung des Füllgutes 9 zu erlauben.In the
Im gezeigten Ausführungsbeispiel wird das Materialband 15 beim Verlassen des Ölbades 27 einer Abstreifvorrichtung 22 zugeführt. An dieser Abstreifvorrichtung 22 kann überschüssiges Öl von der Oberfläche des Materialbandes 15 entfernt werden. Die Abstreifvorrichtung 22 kann dabei so ausgestaltet sein, dass die Filmdicke des auf der Oberfläche der Materialbänder 15 zurückbleibenden Ölfilms auf einen vorbestimmbaren Wert eingestellt werden kann. Anschliessend wird das entspannte Materialband wie bereits gezeigt über Führungsrollen 20 einem Formwerkzeug 2 zugeführt. Im gezeigten Ausführungsbeispiel handelt es sich dabei um das Formwerkzeug 2 einer im Rotary-Die-Verfahren betriebenen Vorrichtung. Bei diesem Verfahren wirkt es sich besonders günstig aus, dass zusätzliche Wärme, im gezeigten Ausführungsbeispiel durch das Ölbad auf das Stärkeband 15 eingebracht wurde. Dadurch kann die Segmenttemperatur im Bereich des Füllkeils 5 niedrig gehalten werden. Es können folglich auch Temperatur empfindlichere Füllgüter 9, insbesondere pharmazeutische Wirkstoffe, verkapselt werden. Durch die Bandbeölung im Ölbad 27 kann auf zusätzliche Beölungen, welche üblicherweise prozessbedingt notwendig sind verzichtet werden. Ein Ölbad 27 als Behandlungsstation 3 zum beaufschlagen des Materialbandes 15 mit Wärme weist überdies den Vorteil auf, dass weitere Zusatzstoffe, welche die Bandeigenschaften wie Viskosität, Elastizität, Bruchdehnung etc. positiv beeinflussen dem Bad beigemengt werden können. Andere Flüssigkeiten an Stelle von Oel wie z. B. Wasser, wässrige Dispersionen usw. sind denkbar.In the exemplary embodiment shown, the
Andererseits zeigt
Im Gegensatz dazu ist das Stärkeband 15 nach der Behandlung mit Wärme relaxiert und weist isotrope Eigenschaften auf. Die gemessene Bruchdehnung der Materialbänder 15 ist in Längsrichtung und in Querrichtung in guter Näherung identisch. Bei der Weiterverarbeitung derartiger Materialbänder entstehen gleichmässige Formkörper 11, die nicht in den Formwalzen hängen bleiben.In contrast, the
Deshalb kommt einem tiefen Elastizitätsmodul der Materialbänder 15 eine entscheidende Rolle zu. Das erfindungsgemässe Verfahren erweist sich damit auch im Hinblick auf die damit erreichte Senkung des Elastizitätsmoduls als besonders vorteilhaft. Insgesamt werden damit die Materialeigenschaften der Materialbänder für die nachfolgende Verarbeitung zu Formkörpern optimiert.Therefore, a deep modulus of elasticity of the
Claims (16)
- A method of producing shaped bodies, in particular capsules, from a biopolymeric material, in particular based on starch, in which at least one endless material strip (15) is extruded from an extrusion tool (13) and processed in a shaping tool (2) with the inclusion of a filling material at a plasticising temperature to form shaped bodies (11), characterised in that the material strip is subjected to at least one heat treatment at a treatment station (3) between the extrusion tool and the shaping tool to reduce stresses, wherein after the heat treatment the strip (15) no longer has anisotropic but isotropic mechanical properties so that the mechanical properties of the strip in the longitudinal direction and in the transverse direction are identical to a good approximation.
- A method according to claim 1 characterised in that at least two material strips are processed to give shaped bodies using the rotary die principle, wherein both material strips are subjected to at least one heat treatment at a treatment station between extrusion and processing to give shaped bodies.
- A method according to one of claims 1 and 2 characterised in that the heat treatment is effected by radiation from a radiation source, in particular by IR radiation.
- A method according to one of claims 1 and 2 characterised in that the heat treatment is effected by convection heat.
- A method according to one of claims 1 and 2 characterised in that the heat treatment is effected by immersing the material strip or strips in at least one heated bath, in particular an oil bath.
- A method according to claim 5 characterised in that the bath temperature is maintained in a range of 40°C to 130°C.
- A method according to one of claims 1 to 6 characterised in that the tensile stress in the material strip or strips is kept constant with a compensating means, in particular by means of a dancer roller (21).
- Apparatus for producing shaped bodies, in particular capsules, from a biopolymeric material, in particular based on starch, comprising at least one extrusion tool (13) for extruding an endless material strip (15) and at least one shaping tool (12) for processing the material strip with the inclusion of a filling material to provide shaped bodies (11), wherein at least one treatment station (3) for applying heat to the material strip is arranged between the extrusion tool and the shaping tool, characterised in that the temperature for the heat treatment is so selected that the result is the desired stress relief of the material strips, which is reached when the strip after the heat treatment no longer has anisotropic but isotropic mechanical properties so that the mechanical properties of the strip in the longitudinal direction and in the transverse direction are identical to a good approximation, and the strip can be controlledly guided without further stress reduction.
- Apparatus according to claim 8 characterised in that the treatment station for applying heat to the material strip includes a radiation source, in particular a radiation source emitting IR radiation.
- Apparatus according to one of claims 8 and 9 characterised in that the treatment station for applying heat to the material strip has at least one heating body.
- Apparatus according to one of claims 8 to 10 characterised in that the treatment station for applying heat to the material strip has a heatable bath, in particular an oil bath.
- Apparatus according to claim 11 characterised in that disposed between the bath and the shaping tool is at least one stripping device for stripping off liquid, in particular for metering the coating with liquid.
- Apparatus according to one of claims 8 to 12 characterised in that it has at least one compensating means, in particular a dancer roller, for maintaining a constant tensile stress on the material strip.
- Apparatus in particular according to one of claims 8 to 13 characterised in that it has at least one adjustable positioning arrangement at which the extrusion tool and the shaping tool are adjustable relative to each other in respect of their relative position.
- Apparatus according to one of claims 8 to 14 characterised in that the shaping tool (2) is a rotary die device having two shaping rollers and a filling wedge and at least one respective extrusion tool is arranged on each of the two sides of the shaping tool in such a way that the material strip is introduced into the shaping tool on a conveyor plane without lateral deflection.
- Use of a heatable oil bath for stress relief of material strips of a biopolymeric material, in particular on the basis of starch, by heat treatment, wherein the strip (15) after the heat treatment no longer has anisotropic but isotropic mechanical properties so that the mechanical properties of the strip in the longitudinal direction and in the transverse direction are identical to a good approximation, in particular the strip (15) has a uniform elongation to fracture and a uniform modulus of elasticity.
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE50015770T DE50015770D1 (en) | 2000-12-29 | 2000-12-29 | Method and device for producing moldings from a biopolymer material |
EP00128701A EP1249219B1 (en) | 2000-12-29 | 2000-12-29 | Method and apparatus for manufacturing shaped bodies made of a biopolymer material |
ES00128701T ES2334973T3 (en) | 2000-12-29 | 2000-12-29 | PROCEDURE AND DEVICE FOR OBTAINING MOLDED BODIES FROM A BIOPOLIMERO MATERIAL. |
AT00128701T ATE446075T1 (en) | 2000-12-29 | 2000-12-29 | METHOD AND DEVICE FOR PRODUCING MOLDED BODIES FROM A BIOPOLYMERIC MATERIAL |
US10/451,936 US20040071808A1 (en) | 2000-12-29 | 2001-12-15 | Method and device for producing shaped bodies, especially capsules, from a biopolymer material containing starch |
PCT/EP2001/014837 WO2002053088A1 (en) | 2000-12-29 | 2001-12-15 | Method and device for producing shaped bodies, especially capsules, from a biopolymer material containing starch |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP00128701A EP1249219B1 (en) | 2000-12-29 | 2000-12-29 | Method and apparatus for manufacturing shaped bodies made of a biopolymer material |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1249219A1 EP1249219A1 (en) | 2002-10-16 |
EP1249219B1 true EP1249219B1 (en) | 2009-10-21 |
Family
ID=8170865
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP00128701A Expired - Lifetime EP1249219B1 (en) | 2000-12-29 | 2000-12-29 | Method and apparatus for manufacturing shaped bodies made of a biopolymer material |
Country Status (6)
Country | Link |
---|---|
US (1) | US20040071808A1 (en) |
EP (1) | EP1249219B1 (en) |
AT (1) | ATE446075T1 (en) |
DE (1) | DE50015770D1 (en) |
ES (1) | ES2334973T3 (en) |
WO (1) | WO2002053088A1 (en) |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6949256B2 (en) * | 2002-01-18 | 2005-09-27 | Banner Pharmacaps, Inc. | Non-gelatin capsule shell formulation |
US7887838B2 (en) * | 2002-01-18 | 2011-02-15 | Banner Pharmacaps, Inc. | Non-gelatin film and method and apparatus for producing same |
DE50308456D1 (en) * | 2003-01-08 | 2007-12-06 | Swiss Caps Rechte & Lizenzen | Shaped body consisting of gelatin-free material and filled with a liquid filling material |
US7494667B2 (en) | 2004-03-02 | 2009-02-24 | Brunob Ii B.V. | Blends of different acyl gellan gums and starch |
US20050196437A1 (en) * | 2004-03-02 | 2005-09-08 | Bednarz Christina A. | Hard capsules |
PT103380B (en) * | 2005-11-09 | 2007-09-13 | Univ Do Minho | LINE OF EXTRUSION LABORATORIAL FOR THE PRODUCTION OF TUBULAR FILM CONVENTIONAL AND BIORIENTED, WITH SIMPLE SWITCHING BETWEEN THE TWO TECHNIQUES |
EP2108677A1 (en) | 2008-04-10 | 2009-10-14 | Swiss Caps Rechte und Lizenzen AG | Thermoplastic starch-containing materials |
US20120049410A1 (en) * | 2010-07-19 | 2012-03-01 | Carlos Salazar Altamar | Apparatus and process for making soft gel capsules |
CN105456037B (en) * | 2015-08-14 | 2022-05-17 | 新昌县恒泰隆机械设备有限公司 | Even oily mechanism and capsule production line |
AU2017371180B2 (en) * | 2016-12-08 | 2023-05-11 | R.P. Scherer Technologies, Llc | A method to relieve stress in capsule shells to reduce propensity to break |
Family Cites Families (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2390337A (en) * | 1941-05-13 | 1945-12-04 | Chester A Spotz | Method and machine for making capsules, particularly gelatin capsules |
US2513581A (en) * | 1947-06-23 | 1950-07-04 | Norton Co | Capsulator |
US2549327A (en) * | 1948-09-11 | 1951-04-17 | Norton Co | Capsule making machine and method |
US2643416A (en) * | 1949-03-05 | 1953-06-30 | Norton Co | Apparatus for casting ribbons of gelatin and the like |
DE1009357B (en) * | 1955-04-12 | 1957-05-29 | Sueka Ges M B H | Device for feeding the elastic bands, preferably gelatine bands, used to form capsules filled with medicinal or nutrients or the like, to the mold |
FR1204696A (en) * | 1958-06-10 | 1960-01-27 | Process for manufacturing packaging in heat-sealable material and device for its implementation | |
US3092942A (en) * | 1960-04-15 | 1963-06-11 | Sydney A Chasman | Apparatus for encapsulating |
US4154636A (en) * | 1975-08-27 | 1979-05-15 | Freund Industrial Co., Ltd. | Method of film-coating medicines |
US4165998A (en) * | 1975-12-15 | 1979-08-28 | Hoffmann-La Roche Inc. | Manufacture of pharmaceutical dosage forms |
US4349531A (en) * | 1975-12-15 | 1982-09-14 | Hoffmann-La Roche Inc. | Novel dosage form |
ZA767136B (en) * | 1975-12-15 | 1977-10-26 | Hoffmann La Roche | Novel dosage form |
US4139959A (en) * | 1977-05-13 | 1979-02-20 | Howard William J | Cartridge magazine |
NL8002835A (en) * | 1980-05-16 | 1981-12-16 | Stamicarbon | METHOD AND APPARATUS FOR THE MANUFACTURE OF FILLED PLASTIC GRANULES |
US4609403A (en) * | 1984-03-12 | 1986-09-02 | Warner-Lambert Company | Foam soft gelatin capsules and their method of manufacture |
US4614220A (en) * | 1984-11-16 | 1986-09-30 | The United States Of America As Represented By The Secretary Of The Air Force | Method for continuously casting thin sheet |
IE66735B1 (en) | 1988-11-03 | 1996-02-07 | Biotec Biolog Naturverpack | Thermoplastically workable starch and a method for the manufacture thereof |
US5146730A (en) * | 1989-09-20 | 1992-09-15 | Banner Gelatin Products Corp. | Film-enrobed unitary-core medicament and the like |
DE4134190A1 (en) * | 1991-10-16 | 1993-04-22 | Tomka Ivan | METHOD FOR IMPROVING THE MECHANICAL PROPERTIES OF ONE-OR MULTILAYER FOILS |
GB9606371D0 (en) * | 1996-03-26 | 1996-06-05 | Brown Malcolm D | An encapsulation process |
US5682733A (en) * | 1996-05-09 | 1997-11-04 | Perrone; Aldo | Apparatus for enrobing tablets |
US6238616B1 (en) * | 1998-12-14 | 2001-05-29 | Timecaps Inc. | Method of manufacturing gelatin capsule containing powder or time release pellets |
EP1103254B1 (en) * | 1999-11-19 | 2005-03-23 | Swiss Caps Rechte und Lizenzen AG | Process to manufacture starch-containing shaped bodies,mass containing homogenized starch and device to manufacture soft capsules |
EP1112740A1 (en) * | 1999-12-30 | 2001-07-04 | Greither, Peter | Use of a water-soluble composition comprising polyglycerine |
EP1151844B1 (en) * | 2000-05-03 | 2003-11-26 | Swiss Caps Rechte und Lizenzen AG | Method and apparatus for manufacturing a flexible band from at least two different materials flowable under the action of heat |
US6884060B2 (en) * | 2001-11-02 | 2005-04-26 | R.P. Scherer Technologies, Inc. | Apparatus for manufacturing encapsulated products |
US6949256B2 (en) * | 2002-01-18 | 2005-09-27 | Banner Pharmacaps, Inc. | Non-gelatin capsule shell formulation |
-
2000
- 2000-12-29 AT AT00128701T patent/ATE446075T1/en not_active IP Right Cessation
- 2000-12-29 DE DE50015770T patent/DE50015770D1/en not_active Expired - Lifetime
- 2000-12-29 ES ES00128701T patent/ES2334973T3/en not_active Expired - Lifetime
- 2000-12-29 EP EP00128701A patent/EP1249219B1/en not_active Expired - Lifetime
-
2001
- 2001-12-15 US US10/451,936 patent/US20040071808A1/en not_active Abandoned
- 2001-12-15 WO PCT/EP2001/014837 patent/WO2002053088A1/en not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
ATE446075T1 (en) | 2009-11-15 |
ES2334973T3 (en) | 2010-03-18 |
EP1249219A1 (en) | 2002-10-16 |
US20040071808A1 (en) | 2004-04-15 |
WO2002053088A1 (en) | 2002-07-11 |
DE50015770D1 (en) | 2009-12-03 |
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