process line and process for producing freeze-dried particles under closed conditions, process for p

专利摘要:
PROCESS LINE FOR THE PRODUCTION OF FREEZE DRY PARTICLES. The present invention relates to a process line (300) for the production of freeze-dried particles under closed conditions comprising at least one spray chamber (302) for droplet generation and freezing of liquid droplets to form particles and a bulk freeze dryer (304) to freeze dry the particles, the freeze dryer (304) comprising a rotating drum for receiving the particles. In addition, a transfer section (308) is provided for transferring product from the spray chamber (302) to the freeze dryer (304). For the production of particles under closed conditions end to end of each of the devices (302, 304) and the transfer section (308) it is separately adapted for the sterility preservation operation of the product to be dried by freezing and / or containment.
公开号:BR112014007862B1
申请号:R112014007862-9
申请日:2012-10-04
公开日:2021-01-19
发明作者:Bernhard Luy；Matthias Plitzko；Manfred Struschka
申请人:Sanofi Pasteur Sa；
IPC主号:

专利说明:

TECHNICAL FIELD
[001] The invention relates to freeze drying and in particular to the production of freeze-dried pellets as in bulk, wherein a process line for the production of freeze-dried pellets comprises at least one spray chamber for generating droplets and freezing solidification of liquid droplets to form pellets, and a freeze dryer to freeze pellets to freeze. BACKGROUND OF THE INVENTION
[002] Freeze drying, also known as freeze drying, is a process for drying high quality products such as, for example, pharmaceuticals, biological materials such as proteins, enzymes, microorganisms and, in general, any thermosensitive material and / or sensitive to hydrolysis. Freeze drying provides the drying of the target product through the sublimation of ice crystals in water vapor, that is, through the direct transition of water content from the solid phase to the gas phase. Freeze drying is often carried out under vacuum conditions, but it usually works under atmospheric pressure as well.
[003] In the fields of pharmaceuticals and biopharmaceuticals, freeze drying processes can be used, for example, for the drying of drug formulations, Active Pharmaceutical Ingredients ("APIs"), hormones, peptide-based hormones, monoclonal antibodies, products blood plasma or blood derivatives, immunological compositions including vaccines, therapeutics, other injectables, and in general substances that otherwise cannot be stable for a desired useful time. In products, water freeze driers and / or other volatile substances are removed before sealing the product in bottles or other containers. In the pharmaceutical and biopharmaceutical fields, target products are typically packaged in a way to preserve sterility and / or containment. The dried product can then be reconstituted by dissolving it in an appropriate reconstitution medium (for example, sterile water or other pharmaceutical grade diluents) before use and administration.
[004] The design principles for freeze dryer devices are known. For example, tray-based freeze dryers comprise one or more trays or shelves within a spray chamber (vacuum). The bottles can be filled with the product and arranged in a tray. The tray with the filled bottles is introduced into the dryer by freezing and the drying process begins.
[005] Process systems combining spray freezing and freeze drying are also known. For example, US 3,601,901 describes a highly integrated device comprising a vacuum chamber with a freezing compartment and a drying compartment. The freezing compartment comprises a spray nozzle at the top of a portion projecting over the vacuum chamber. The sprayed liquid is atomized and quickly frozen into a number of small frozen particles that fall into the freezer compartment to reach a conveyor assembly. The conveyor advances the particles progressively to freeze drying in the drying compartment. When the particles reach the discharge end of the conveyor, they are in freeze-dried form and fall into a discharge hopper.
[006] In another example, WO 2005/105253 describes a freeze drying apparatus for fruit juices, pharmaceuticals, nutraceuticals, teas and coffees. A liquid substance is atomized through a high pressure nozzle in a freezing chamber in which the substance is cooled to below its eutectic temperature, thereby inducing a phase change of liquids in the substance. A countercurrent flow of cold air freezes the droplets. The frozen droplets are then transported pneumatically by the cold air stream through a vacuum lock in a vacuum drying chamber and are further subjected to an energy source in the chamber to assist the sublimation of liquids as the substance is transported through the camera.
[007] Many products are compositions comprising two or more different agents or components that are mixed together before freeze drying. The composition is mixed with a predefined ratio and is then freeze-dried and filled into transport jars. A change in the mixing ratio of the composition after filling the bottles is practically impossible. In freeze drying procedures the mixing, filling and drying processes, therefore, cannot be separated normally.
[008] WO 2009/109550 A1 discloses a process for stabilizing a vaccine composition containing an adjuvant. It is proposed to separate, if desired, the drying of the antigen from the drying of the adjuvant, followed by mixing the two components before the combined filling or employing sequential filling of the respective components. Specifically, separate micropellets comprising both antigens and the adjuvant are generated. The antigen micropellets and the adjuvant micropellets are then mixed before filling the bottles, or are directly filled to obtain the desired mixing ratio specifically at the time of mixing or filling. The methods are referred to provide a further improvement in the total stability of the composition, as the formulations can be optimized independently for each component. Separate solid states are referred to to avoid interactions between different components throughout storage, even at the highest temperature.
[009] Products in the pharmaceutical and biopharmaceutical fields often have to be manufactured under closed conditions, that is, they have to be manufactured under sterile conditions and / or under containment. A process line adapted for production under sterile conditions must be designed so that no contaminants can enter the product. Similarly, a process line adapted for production under containment conditions has to be adapted so that neither the product, its elements, nor auxiliary materials can leave the process line and enter the environment.
[0010] Two approaches are known for engineering process lines adapted for production under closed conditions. The first approach comprises placing the entire process line or parts / devices of the same in at least one insulator, the last being a device isolating its interior and the environment from each other and maintaining defined conditions inside. The second approach involves developing an integrated process system providing sterility and / or containment, which is usually obtained by integrating a device housing that is specifically adapted and highly integrated to perform all the desired process functions.
[0011] As an example for the first approach, WO 2006/008006 A1 describes a process for sterile freezing, freeze drying, storage and testing of a pelleted product. The process comprises freezing droplets of the product to form pellets, freeze drying the pellets and then testing and loading the product in containers; More particularly, the frozen pellets are created in a freezing tunnel and are then directed into a drying chamber, in which the pellets are freeze-dried on a plurality of pellet transport surfaces. After freeze drying, the pellets are discharged into storage containers. The pelletizing and freeze-drying process is carried out in a sterile area implemented inside an insulator. The filled storage containers are transferred to a storage test. For final filling, the storage containers are transferred to another area of sterile insulator containing a filling line, where the contents of the container are transferred to bottles, which are sealed after filling and finally discharged from the isolated filling line.
[0012] Placing the process line inside a box, that is, in one or more insulators, seems to be a simple approach to ensure sterile production. However, such systems and their operation become increasingly complex and expensive with the increase in the size of the processes and the corresponding size of the required insulator (s). Cleaning and sterilizing these systems requires not only that the process line be cleaned and sterilized after each production cycle, but also the insulator. In cases where two or more insulators are required, interfaces between the isolated areas occur that require additional efforts to protect the sterility of the product. At some point, process devices and / or isolators may no longer be made using standard devices and have to be specifically developed to further increase complexity and costs.
[0013] An example of the second approach to providing process lines for production under closed conditions, namely, to provide a specifically adapted and highly integrated system, is given by US 3,601,901 mentioned above. According to the '901 patent, a freezing compartment and a drying compartment are formed within a single vacuum chamber. Such an approach generally excludes the use of standard devices, that is, process equipment is expensive in itself. In addition, due to the highly integrated implementation of the various process functions, the entire system is normally in a particular mode, for example, in a production cycle, or in a maintenance mode such as cleaning or sterilization which limits the flexibility of the line. process. SUMMARY OF THE INVENTION
[0014] In view of the above, an objective underlying the invention is to provide a process line and corresponding processes for the production of freeze-dried particles including particles produced under closed conditions. Another objective of the invention is to provide more cost-effective process lines that are currently available. Another objective of the present invention is to provide a process line that is flexibly adaptable so that, for example, production times are shorter, the overall operation of the process line is more effective, and / or the system can be configured more flexibly for sequential and / or simultaneous production, maintenance, cleaning and sterilization operations, etc.
[0015] According to an embodiment of the invention, one or more of the above objectives is achieved by a process line for the production of freeze-dried particles under closed conditions, wherein the process line comprises at least the following separate devices: 1) a spray chamber for droplet generation and freezing solidification of liquid droplets to form particles; and 2) a bulk freeze dryer to freeze dry the particles. A transfer section is provided for transferring product from the spray chamber to the freeze dryer. For the production of particles under closed end-to-end conditions, each of the transfer devices and sections is separately adapted for the sterility preservation operation of the product to be dried by freezing and / or containment.
The particles may comprise, for example, pellets and / or granules. The term "pellet (s)" as used herein can be understood to refer preferably to particles with a tendency to be generally spherical / round. However, the invention is likewise applicable to other particles or microparticles (i.e. particles in the micrometer range), such as, for example, irregularly formed granules or microgranules (where the latter have at least their average dimensions in the range micrometer). Pellets with sizes in the micrometer range are called micropellets. According to another example, the process line can be arranged for the production of essentially or predominantly freeze-dried round micropellets with an average value for their diameters chosen from a range of about 200 to about 800 micrometers (μm) , with a preferably narrow particle size distribution of about ± 50 μm around the chosen value.
[0017] The term "in bulk" can be widely understood to refer to a system or plurality of particles contacting one another, that is, the system comprises multiple particles, microparticles, pellets and / or micropellets. For example, the term "in bulk" can refer to a loose amount of pellets constituting at least part of a product stream, such as a batch of a product to be processed in a process device or a process line, wherein the bulk article is released in the sense that it is not loaded in bottles, containers or other containers to transport or transmit the particles / pellets within the process device or process line. It remains similar for the use of the noun or adjective "in bulk".
[0018] The bulk article as referred to in this document will normally refer to an amount of particles (pellets, etc.) exceeding one (secondary or final) package or intended dose for a single patient. Instead, the amount of bulk article refers to a primary package; for example, a production cycle may comprise the production of bulk articles sufficient to fill one or more containers of intermediate bulk articles (IBCs).
[0019] Flowable materials suitable for spraying and / or pelletizing using the devices and methods of the present invention include liquids and / or pastes which, for example, have a viscosity of less than about 300 mP * s (millipascals * s) . As used herein, the term "flowable materials" is interchangeable with the term "liquids" for the purpose of describing materials that enter the various process lines contemplated for spraying and / or pelletizing and / or freeze drying.
[0020] Any material can be suitable for use with the techniques according to the invention if the material is flowable, and can be atomized and / or pelletized. In addition, the material must be solidifiable and / or freezable.
[0021] The terms "sterility" ("sterile conditions) and" containment "(" contained conditions ") are understood to be required by the regulatory requirement applicable to a specific case. For example," sterility "and / or" containment "may be understood as defined according to GMP requirements ("Good Manufacturing Practice").
[0022] A "device" in this document is understood to mean an equipment unit or component that performs a particular process step, for example, a spray chamber or freeze dryer performs the droplet generation process step and freezing solidification of liquid droplets to form particles, a freeze dryer performs the process step of freezing the frozen particles, etc.
[0023] It is further understood in this document that a process line for the production of particles under closed end-to-end conditions must necessarily include means for feeding liquid under sterile conditions and / or containment conditions to the process line, and still has that include one or more means for discharging freeze-dried particles under sterile conditions and / or containment conditions.
[0024] In one embodiment, one or more transfer sections permanently interconnected two, or more, devices to form an integrated process line for the production of particles under closed point-to-point conditions. Generally, the various devices of a process line for producing freeze-dried particles under closed conditions can be provided as separate devices that are (for example, permanently connected) connected to one another by one or more transfer sections. Individual transfer sections can provide permanent connections between two or more devices, for example, mechanically, rigidly and / or securely connecting or joining the respective devices to each other. A transfer section can be single or double wall, where in the latter case an external wall can provide permanent interconnection of process devices and can, for example, delineate the process conditions defined in a process volume confined by the external wall, while an inner wall may or may not permanently interconnect process devices. For example, the inner wall can form a tube within the process volume that is connected between the devices only in the case of a product transfer.
[0025] In the preferred embodiments, each of the process devices such as the spray chamber and the freeze dryer are separately adapted for closed operation. For example, the spray chamber can be individually adapted for sterile operation and, independently of it, the freeze dryer can be individually adapted for sterile operation. Similarly, any (any) other device (s) included in the process line can also be individually adapted or optimized for operation under closed conditions. As for the devices, each of one or more transfer sections can also be individually adapted for operation under closed conditions, which implies that each transfer section can be adapted to maintain or protect sterility, and / or containment to the transfer of product through the transfer section, and transmission from one device into the transfer section and from the transfer section to another device.
[0026] The transfer sections may comprise means to operatively separate the two connected devices from one another so that at least one of the two devices is operable under closed conditions separately from another device without affecting the integrity of the process line.
[0027] The means for operationally separating the two connected devices may comprise a valve, for example, a vacuum-tight valve, a vacuum lock, and / or a component that makes it possible to seal the components from each other in a sealable manner. For example, operational separation may imply that closed conditions, that is, sterility and / or containment, are established between the separate devices. The integrity of the process line must be maintained regardless of operational separation, that is, the permanent connection between the devices via the transfer section is not affected.
[0028] According to various embodiments of the invention, at least one of the process devices and one of the transfer sections may comprise a containment wall that is adapted to provide predetermined process conditions (i.e., physical or thermodynamic conditions such as temperature , pressure, humidity, etc.) within a confined process volume, in which the confinement wall is adapted to isolate the process volume and a process device environment from each other. Regardless of whether the confinement wall comprises more structures such as tubes or similar "inner walls" confined to the process volume, the confinement wall must satisfy both functions simultaneously, this in addition to maintaining the desired process conditions in the volume of process. process, the wall must simultaneously adopt the functionality of a conventional insulator. No other insulator / insulators are, therefore, required for a process according to these embodiments of the invention. Conventional insulators are typically not suitable for use in the process devices according to the invention. In certain embodiments, at least one wall of an insulator is adapted so that it can simultaneously ensure the desired process conditions inside, thereby defining the interior of the insulator as the "process volume". Similarly, a conventional standard device cannot be suitable for use as a process device according to the invention: a wall thereof defining the interior of a process volume may at least have to be adapted so that it can simultaneously ensure insulation of the process volume and the environmental separation of the process devices with each other.
[0029] In one example, a transfer section according to the invention may comprise a containment wall that permanently or not permanently interconnects the process devices to enable closed operation (that is, the connection can be in place at least during a process phase comprising a product transfer between the connected devices). The confinement wall can isolate an internal volume such as a process volume (which can, for example, be sterile), from an external volume such as a process line environment that the transfer section is a part of ( which cannot be, and does not need to be sterile). In this regard, the containment wall simultaneously allows the maintenance of desired process conditions within the process volume. The term "process conditions" is intended to refer to temperature, pressure, humidity, etc., in the process volume, where a process control can comprise controlling or triggering such process conditions within the process volume according to a regime of desired process, for example, according to a time sequence of a desired temperature profile and / or pressure profile). Although "closed conditions" (sterile conditions and / or containment conditions) are also subject to process control, these conditions are discussed in this document in many cases explicitly and separately from the other process conditions indicated above.
[0030] In other embodiments, the transfer section may comprise, extending within the process volume, a transport mechanism such as a tube for obtaining the process transfer. In such a modality. the transfer section has a "double wall" configuration, in which the outer wall implements a confinement wall and the inner wall implements a tube. This double-walled transfer section differs from a tube included in a conventional insulator in that the confinement wall is adapted to enable the desired process conditions in the process volume. In the case of a permanent connection, the containment wall can permanently interconnect the process devices, while the inner wall (pipe, etc.) may or may not be in place permanently. For example, the tube can extend in a freeze dryer connected, for example, a drum of the same; the tube can be removed from the freeze dryer / tube as soon as a freeze dryer / tube load is completed. Regardless of such configurations, the closed operating conditions can be maintained by the outer (confinement) wall.
[0031] A confining wall of a process device or transfer section, which is adapted to function as a conventional insulator and in order to simultaneously provide a process volume according to the invention, has to conform to a plurality process conditions including, but not limited to, providing and maintaining a desired temperature regime, and / or a pressure regime, ECT. For example, according to prescriptions such as GPM requirements, a sensor system can be used to determine that sterile conditions and / or containment conditions are in place / being maintained. As another example, for effective cleaning and / or sterilization (for example, Cleaning at Site "CiP" and / or Sterilization at Site "SiP"), there may be a requirement that a confinement wall of a process device / section transfer is designed in order to avoid, as far as possible, critical areas that may tend to contamination / pollution and make cleaning / sterilization difficult. In yet another example, there may be a requirement that a transfer process / section device is specifically adapted for effective cleaning and / or sterilization of internal elements, such as the "inner wall" or the tube mentioned in the specific exemplary transfer section discussed above. All of these aspects are not addressed by conventional insulators.
[0032] Process devices, including a spray chamber, freeze dryer and, optionally, other devices, and one or more transfer sections connecting the devices can form an integrated process line providing end-to-end protection of the sterility of the product. In addition, or, alternatively, the process devices and the transfer section (s) can form an integrated process line providing end-to-end containment of the product.
[0033] The spray chamber modalities can comprise any device adapted for generating droplets from a liquid and for freezing solidification of the liquid droplets to form particles, where the particles preferably have a narrow size distribution. Exemplary droplet generators include, but are not limited to, ultrasonic nozzles, high frequency nozzles, rotating nozzles, two-component nozzles (binaries), hydraulic nozzles, multiple nozzle systems, etc. Freezing can be achieved by dropping the gravity of the droplets into a chamber, tower or tunnel. Exemplary spray chambers include, but are not limited to, pelletizing devices such as pelletizing chambers or towers, atomizing devices such as atomizing chambers, nebulization / freezing and freezing equipment, etc.
[0034] According to an embodiment of the invention, the spray chamber is adapted to separate the product from any cooling circuit. The product can be kept separate from any primary freezing / cooling medium or fluid, including gaseous or liquid media. According to a variant of this modality, an internal volume of the spray chamber comprises an optionally non-circulating sterile medium such as nitrogen or a mixture of nitrogen / air and a temperature-controlled one, that is, a cooled internal wall as the only cooling component. to freeze the droplets, so that a counterflow of cooling or simultaneous cooling can be avoided.
[0035] According to an embodiment of the invention, the freeze dryer can be adapted for separate operation (that is, an operation that is separate or distinct from the operation or non-operation of other process devices) under closed conditions, where the separate operation includes at least one particle freeze drying, freeze dryer cleaning, and freeze dryer sterilization.
[0036] In a process line mode, the freeze dryer can be adapted for direct product discharge into a final container under closed conditions. The container can comprise, for example, a container such as an Intermediate Volume Container ("IBC") for storage or temporary storage of the product for subsequent mixing in a final formulation, filling into final containers, further processing, or the container can comprise a final container such as a final fill bottle, and / or the container may comprise a sample vessel for sampling; Further subsequent product arrangements are also possible and / or the container may also comprise yet another storage component. According to a variant of this modality, the freeze dryer can be adapted for a direct discharge of the product into the final container under protection of the product's sterility. The freeze dryer may comprise an anchoring mechanism allowing anchoring and undocking of containers under protection from sterile and / or containment conditions for the product.
[0037] The integrated process line may comprise as another device, in addition to the spray chamber and the freeze dryer, such as a product handling device, which is adapted for at least one function of unloading the product from the line process, sample the product and / or handle the product under closed conditions. In addition to the transfer section (usually one or more transfer sections) permanently connecting the spray chamber and the freeze dryer, another transfer section (usually one or more transfer sections) can be provided to transfer the product from the dryer by freezing for the product handling device, where for the production of the particles under closed point-to-point conditions each of the transfer sections and the product handling device is separately adapted for closed operation. The other transfer section can permanently connect the freeze dryer to the product handling device so that the product handling device can form part of the integrated process line for producing the particles under closed point-to-point conditions.
[0038] In some embodiments, the spray chamber is adapted to separate the product flow from any (any) cooling circuit (s) for solidification by freezing the product. In addition, or alternatively, the spray chamber may comprise at least one temperature-controlled wall to freeze liquid droplets. The spray chamber can optionally be a double-walled spray chamber.
[0039] The freeze dryer can be a vacuum freeze dryer, that is, it can be adapted for operation under a vacuum. In addition, or alternatively, the freeze dryer may comprise a rotating drum for receiving the particles.
[0040] At least one of one or more transfer sections of the integrated process line can be permanently mechanically mounted to the devices connected to it. At least one of one or more transfer sections of the process line can be adapted for a product flow comprising a gravity transfer of the product. The present invention, however, is not limited to transferring the product through the process line only by gravity. Naturally, in certain embodiments, the process devices, and the transfer section (s) in particular, are configured to provide mechanical transfer of the product across the process line using one or more conveyor components, drill components and similar.
[0041] One or more of the transfer sections of the process line may comprise at least one temperature controlled wall. At least one of one or more transfer sections of the integrated process line may comprise a double wall. In addition, or, alternatively, at least one of one or more transfer sections of the process line may comprise at least one cooled tube. In the case where the freeze dryer comprises a rotating drum, the transfer section connecting the spray chamber and the freeze dryer can protrude into the rotating drum. For example, a transfer tube from the transfer section may protrude into the drum, where a tube (transfer) included in a transfer section should generally be understood as an element adapted for transporting the product or obtaining a flow of product, that is, a product transfer between process devices, for example, from one process device to another process device.
[0042] The process line may comprise a process control component adapted to control the operational separation and subsequently separate operation of one of at least two process devices on the process line. In certain of these embodiments, the process control component comprises one or more of the following: a module for controlling a separate element such as a valve or similar sealing element arranged in a transfer section to separate the devices, a module for determining whether closed conditions (for example, sterility or containment conditions) are established in at least one process volume provided by at least one of the devices, and a module for selectively controlling process control equipment related to the separate process device .
[0043] In particular modalities, the entire integrated process line (or portions thereof) can be adapted for CiP and / or SiP. Access points for introducing cleaning means and / or sterilization means including, but not limited to, use of nozzles, steam access points, etc., may be provided by all devices and / or a or more transfer sections of the process line. For example, steam access points can be provided for steam-based SiP. In some of these modalities, all or some of the access points are connected to a repository / generator of cleaning and / or sterilization medium. For example, in one variant, all steam access points are connected to one or more steam generators in any combination; for example, exactly one steam generator can be provided for the process line. In cases where, for example, a mechanical scrubbing is required, this can be included in a CiP concept, for example, by providing a correspondingly adapted robot, such as a robotic arm.
[0044] According to another aspect of the invention, a process line for the production of freeze-dried particles under closed conditions is proposed, which is carried out by a process line as described above. The process comprises at least the steps of generating liquid droplets and freezing the liquid droplets to form particles in a spray chamber, transferring the particles under closed conditions from the spray chamber to a freeze dryer through a section transfer, and freeze drying the particles as bulk articles in the freeze dryer. For the production of particles under closed point-to-point conditions, each of the devices and the transfer section (s) is separately adapted to preserve the sterility of the product to be dried by freezing and / or by containment. The transfer of product to the freeze dryer can optionally be carried out in parallel with the generation of droplets and freezing solidification in the spray chamber.
[0045] The process may comprise the other step of operationally separating the spray chamber and the freeze dryer after the completion of a batch product in the spray chamber and transfer of the product to the freeze dryer. In addition, or alternatively, the process may comprise a step of operatively separating the spray chamber and the freeze dryer to perform CiP and / or SiP in one of the separate devices. The step of operationally separating the spray chamber and the freeze dryer may comprise controlling a vacuum-tight valve in the transfer section (usually one or more transfer sections) connecting the two devices. ADVANTAGES OF THE INVENTION
[0046] Various embodiments of the present invention provide one or more of the advantages discussed in this document. For example, the present invention provides process lines for the production of freeze-dried particles under closed conditions. The handling of sterile and / or contained product is made possible while avoiding the need to place the entire process line in a separator or insulator. In other words, a process line according to the invention adapted, for example, for operation under closed conditions, can be operated in a non-sterile environment. The costs and complexity related to the use of an insulator can therefore be avoided while still complying with sterility and / or containment requirements, for example, GMP requirements. For example, there may be an analytical requirement to test at regular time intervals (for example, hourly or every few hours) whether sterile conditions are still maintained within the isolator. By avoiding such cost requirements, production costs can be reduced considerably.
[0047] In accordance with an embodiment of the invention, each of the process devices of a process line such as a spray chamber and a freeze dryer as well as any (any) transfer section (s) connecting the devices to obtain a flow and product between devices under closed conditions, are separately adapted for closed operation. Each transfer device / section can be individually adapted and optimized to obtain, protect and / or maintain closed operating conditions.
[0048] According to various modalities of the invention. In an integrated process line, the product flow works with a free end-to-end interface, for example, from the entry of a liquid to be pelletized into the process line to discharge particles outside the line. "Free interface" in this regard is to be understood as describing an uninterrupted flow of product without disruption such as, for example, product discharge into one or more intermediate receptacles, transfers thereof, and product refilling from the receptacles, as may be required for a process line contained within two or more insulators.
[0049] The modalities of the invention avoid several of the disadvantages of highly integrated concepts in which all process functions are implemented within a device. The invention allows the operation of the flexible process line. The transfer sections are adapted to operationally separate one or more connected devices, thus allowing independent control of the operating mode of each respective device. For example, while one device operates for particle production, the other device is operated for maintenance, for example, washing, cleaning or sterilizing. The possibility of operational separation provides the process control of relevant process parameters and / or product.
[0050] In addition, or, alternatively, a one-line process according to the invention can be operated entirely or in segments (below the level of the device) in continuous, semi-continuous or batch mode. For example, a continuous (quasi-) pelletizing process can result in the continuous flow of product into the freeze dryer which, in turn, is fixed to dry the product received in operation in batch mode. As the operations of different devices are separable, the control of the process line is preferably correspondingly flexible as well. Remaining with the example above, the freeze dryer can operate in parallel with the operation of the pelletizing process, or start operating only after the pelletizing process has ended. Generally, "closed end-to-end conditions" are provided according to the invention regardless of the respective mode configured for the process line or parts thereof. In other words, "point-to-point" protection from sterility and / or process containment is provided regardless of whether the product is processed in any combination of operations in continuous, semi-continuous or batch mode across the entire process line.
[0051] Certain preferred embodiments of a process line according to the invention also allow the decoupling of the different process devices. For example, a transfer section connecting a spray chamber and a freeze dryer can comprise at least one temporary storage component. A continuous flow of product from the spray chamber can then be completed in temporary storage. Temporary storage is opened towards the freeze dryer to allow the transfer of the product temporarily collected and stored in the warehouse to the freeze dryer only once a previous batch has been unloaded from the freeze dryer or the freeze dryer is out. another way ready to process the batch collected and stored in the temporary storage. Such temporary storage thus also allows you to control (define, limit, etc.) a batch size.
[0052] Separate process devices although being operable under closed conditions (optionally, point to point) can be optimized separately, for example, for effectiveness, robustness, reliability, physical process or product parameters, etc. The individual process steps can be optimized separately. For example, the freeze drying process can be optimized by employing a rotary drum freeze dryer to achieve a very fast drying process compared to conventional freeze drying in highly integrated single device process lines including variants tray-based freeze drying. The use of a freeze dryer for bulk articles avoids the need to use specific bottles, vases or other type of containers. In many conventional freeze dryers, specifically adapted containers (flasks, etc.) are required for the particular freeze dryer, for example, specific plugs for the passage of water vapor may be required. None of these specific adaptations are required for the modalities of the invention.
[0053] The invention allows the process lines to be easily adapted to different applications. Separate process devices (can be adapted for production under closed conditions) and can then be used according to the invention. In certain embodiments, the devices can be permanently interconnected with transfer sections. This allows for a cost effective design of process lines for the production of sterile and / or contained bulk articles (eg micropellet). It is possible to provide a "construction kit" of process devices including, for example, spray chamber and freeze dryer devices, which are generally previously adapted for operation under closed conditions, and to combine the desired devices for any specific application.
[0054] Compared to WO 2006/008006 A1, for example, which teaches that the doors through which the product must be transported in compartments or containers from one insulator to the next, the present invention preferably provides specific process lines having hermetically sealed conditions point to point for product flow, so that the interfaces between the devices do not require intermediate product transportation in compartments or containers, but the transfer sections are operable so as not to disturb the flow of product point to point, or separate devices without affecting the integrity of the process line.
[0055] In the particular modalities, once the desired devices are assembled, and permanently interconnected with one or transfer sections, there is no need to violate the mechanical and / or construction integrity of the process line. For example, the devices and transfer sections of the closed process line can be easily adapted for automatic washing, cleaning and / or sterilization on site (WiP, CiP and / or SiP), thus avoiding the need for manual cleaning that can include disassembling two or more parts of the process line.
[0056] A process line according to the invention enables the effective production of freeze-dried particles as bulk articles. In one embodiment, the liquid is introduced at the beginning of the process line and the sterile dried particles are collected at the end of the process line. This makes it possible to produce uniformly calibrated sterile lyophilized micro (particles) as a bulk article, in which the resulting product can be flowing free, free of dust and homogeneous. The resulting product, therefore, comes with good handling properties and can be combined with other components that may be incompatible in liquid form or only stable for a short period of time and thus not suitable for conventional freeze-drying techniques.
[0057] The invention, therefore, allows a separation of the final filling of the dosage form from the previous drying process, thus allowing performance of filling on demand and / or dosing on demand because the lengthy manufacture of article in bulk can be performed before filling and / or dosing a particular API. Costs can be reduced and specific requirements can be more easily met. For example, in particular embodiments, different fill levels are readily obtained since different final specifications do not require additional liquid filling and subsequent drying steps.
[0058] According to various modalities, process lines adapted for sterile processing do not require direct contact of the product with a cooling medium (for example, liquid nitrogen or gaseous nitrogen). For example, the spray chamber can be adapted to separate the product luxury from a primary cooling circuit. Consequently, a sterile cooling medium is not required. It is possible to operate certain process lines without using silicone oil.
[0059] The invention is applicable to process lines for the production of many formulations / compositions suitable for freeze drying. This can include, for example, generally any material sensitive to hydrolysis. Suitable liquid formulations include, but are not limited to, immunological compositions including vaccines, therapeutics, antibodies (e.g., monoclonal), antibody portions and fragments, other protein-based APIs (for example, DNA-based APIs, and substances of cell / tissue). APIs for oral dosage forms (for example, APIs with low solubility / bioavailability), fast dispersible or fast dissolving oral dosage forms (for example, ODTs, orally dispersible tablets) and stick-filled presentations, etc. DESCRIPTION OF THE FIGURES
[0060] Other aspects and advantages of the invention will become evident from the following description of the particular modalities illustrated in the figures, in which:
[0061] figure 1 is a schematic illustration of an embodiment of a product flow in a process line according to the invention;
[0062] figure 2a is a schematic illustration of a first embodiment of a method for configuring a process line according to the invention;
[0063] figure 2b is a schematic illustration of a second embodiment of a method of configuring a process line according to the invention;
[0064] figure 2c is a schematic illustration of a third embodiment of a method of configuring a process line according to the invention;
[0065] figure 3 schematically illustrates an embodiment of a process line according to the invention;
[0066] figure 4 is an enlarged section of the pelletizing tower of figure 3;
[0067] figure 5 is an embodiment of a transfer section according to the invention;
[0068] figure 6 is an embodiment of a discharge station according to the invention;
[0069] figure 7a is a flow chart illustrating a first embodiment of a process line operation according to the invention; and
[0070] figure 7b is a flow chart illustrating a second embodiment of a process line operation according to the invention. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0071] Figure 1 schematically illustrates a product flow 100 that is presumed to pass through a process line 102 for the production of freeze-dried pellets under closed conditions 104. A liquid feed section (LF) feeds liquid to a pelletizing chamber / tower (PT) where it is subjected to the generation of droplets and solidification by freezing. The resulting frozen pellets are then transferred through a first transfer section (1TS) to a freeze dryer (FD) in which the frozen droplets are lyophilized. After lyophilization, the pellets produced are transferred via a second transfer section (2TS) to a discharge station (DS) which provides filling under closed conditions within final containers 106 which are then removed from the process line.
[0072] Closure 104 is intended to indicate that the flow of product 100 from the inlet to the outlet of process line 102 is carried out under closed conditions, that is, the product is maintained under sterility and / or containment. In preferred embodiments, the process line provides closed conditions without the use of an insulator (the paper of which is as indicated by dashed line 108 that separates line 100 from environment 110). Instead, closure 104 separates product flow 100 from environment 110, where closure 104 (closed conditions) is / are implemented individually for each of the process line transfer devices and sections 102. In addition, the objective of end-to-end protection of sterility and / or containment is achieved without placing the entire process in a single device. Instead, the process line 100 according to the invention comprises separate process devices (for example, one or more PTs, FDs, DSs, etc.) that are connected as shown in figure 1 by one or more transfer sections (for example, 1TS, 2TS, etc.) to form the integrated process line 102 enabling the product flow 100 point-to-point of free interface (or start to end).
[0073] Figure 2a schematically illustrates a configuration of a process line 200 for the production of freeze-dried pellets (micropellets) under closed conditions. Briefly, the product flows as indicated by arrow 202 and is preferably kept sterile and / or contained by operation accordingly, each of the separate devices including LF, PT, FD and 1TS transfer section under sterile / containment conditions, which is intended to be indicated by enclosures 204, 206, 208 and 210. The DS discharge station, although not simultaneously in operation, is also adapted to protect the sterility / supply containing 214. In the exemplary configuration of process line 200, as illustrated in the figure 2a, the first transfer section (1TS) is configured in an open position not to limit or interfere with product flow 202, while the second transfer section (2TS) is configured to seal the freeze dryer (FD) sealingly and the discharge station (DS), that is, 2TS operates to seal the FD and provides closed conditions 212 in this regard. Each of the devices, for example, PT, FD, etc., and the transfer sections, for example, 1TS and 2TS, are separately adapted and optimized for operation under closed conditions, where "operation" refers to at least a mode of operation including, but not limited to the production of freeze-dried pellets, or maintenance modes (for example, sterilizing a process device or transfer section naturally also requires that the device / section be adapted to maintain sterility / containment.
[0074] The details of how the process devices such as PTs or FDs can produce sterility / provide obtaining for the products processed in them depend on the specific application. For example, in one embodiment, the sterility of a product is protected / maintained by sterilizing the process devices and transfer sections involved. It should be noted that the process volume confined within a hermetically sealed wall after a sterilization process will be considered sterile for a certain time under particular processing conditions, such as, but not limited to processing the product under excess light pressure ( positive) compared to a 215 environment. Containment can be considered to be achieved by processing the product under slightly decreased pressure compared to environment 215. These and other appropriate processing conditions are known to those skilled in the art.
[0075] As a general observation, the transfer sections such as 1TS and 2TS described in figure 2a are designed to ensure that the product flow through them is carried out under closed conditions; this includes the aspect that closed conditions have to be ensured / maintained also during a product transition in and out of the transfer section; in other words, an attachment or assembly of a transfer section to a device to obtain a product transfer has to preserve the desired closed conditions.
[0076] Figure 2b illustrates process line 200 of figure 2a in a different operational configuration 240, which can arrive controllably in a time sequence after the configuration described in figure 2a. Both transfer sections 1TS and 2TS are switched to operatively separate the corresponding interconnected process devices from each other. The liquid feed section (LF) 204 and the pelletizing tower (PT) 205, therefore, form a closed subsystem that is separated under conditions of sterility and / or containment: (1) from environment 215; and (2) from the parts of the process line 200 separated by 1TS 208.
[0077] Similarly, FD 210 forms a more closed subsystem that is separated: (1) from environment 215, and (2) from other adjacent process devices separated by 1TS 208 and 2TS 212. It is assumed that the Process devices of process line 200 are optimized to comply with CiP / SiP cleaning and / or sterilization procedures. Correspondingly, a CiP / SiP 216 system is provided that includes a tube system to provide a cleaning / sterilizing means for each of the process devices. The piping system is indicated with dashed lines in figure 2a. The solid system lines 216 in figure 2b are intended to indicate that in the operational configuration of process line 200 in figure 2b PT 206 it is subjected to a CiP / SiP process. At the same time, the FD freeze dryer processes a batch of material (product in volume) as indicated by the closed arrow 218. The discharge of the freeze-dried pellets from FD to DS can occur discontinuously, which is because the 2TS transfer section also is closed during the FD freeze dryer drying operation in figure 2a.
[0078] As shown schematically in the figures, enclosures 204-214 provide a completely closed "outer envelope" 222 encompassing process line 200. Transfer sections 208 and 212 interconnect process devices, while maintaining closed conditions for transfer of product throughout process line 200. Envelope 222 is unchanged from figure 2a to figure 2b, that is, envelope 222 is maintained independent of any specific process line configurations such as configurations 220 or 240 and in this way it implements the objective symbolized by enclosure 104 in figure 1. Process line 200 is designed so that the interconnections implemented by transfer sections 208 and 212 are permanent in the sense that disconnecting (for example, dismantling or removing) one or more of the transfer sections from one or more of the adjacent process devices connected to it is not required for any co n process and operation line configuration. Thus, in some embodiments, one or more of the connections to the process devices of one or more of the transfer sections may be intended to be permanent for the intended service life of the process line. For example, a permanent connection may include permanent mechanical fixings / assemblies, for example, by welded connections, riveted connections, industrial adhesives, etc. For example, as symbolized by the CiP / SiP system 216 in figures 2a, 2b, cleaning and / or sterilizing a process device or transfer section may not require any mechanical or manual intervention in which it is performed automatically in place throughout process line or in parts (for example, devices) of it. The automatic control of the valves (or similar separation means) provided in association with the transfer sections (preferably by remote access to them) also contributes to the ability to configure process line 200 for different operational configurations without mechanical intervention and / or manual.
[0079] It should also be noted that the enclosure 222 of the process line 200 described in figures 2a, 2b and 2c results from each of the process devices (for example, LF 204, PT 206, FD 210, and DS 214 ) and the transfer sections (eg 1TS 208 and 2TS 212) of process line 200 can be individually adapted for closed operation where one or more of the devices / sections can be individually optimized for sterility and / or containment conditions / operations . As a result, there is no requirement to use one or more insulators, as is typically required in conventional approaches to provide sterility and / or containment in conjunction with process devices such as PT 206, FD 210 and DS 214. Individual optimizations described in this document provide more cost effective solutions to protect sterility and / or provide containment as compared to systems based on conventional insulators. At the same time, according to the process devices of the invention such as PT, FD and DS they are provided as mechanically separated process devices and can therefore operate separately from one another. These and other embodiments of the invention allow for greater cost effectiveness compared to conventional approaches such as specifically designed and highly integrated unique devices that have to be redesigned for new process requirements.
[0080] Figure 2c illustrates another operational configuration 260 of process line 200. The liquid feed section (LF) 204 and the pelletizing tower (PT) 206 operate to produce the frozen product, for example, micropellets, which is transferred by gravity to transfer section (1TS) 208. However, opposite to configuration 220 in figure 2a, transfer section 1TS receives the product, but does not route the product to the FD freeze dryer. Instead, 1TS 208 is switched to operatively separate PT 206 and FD 210 from each other. The transfer section (1TS) 208 can be equipped with an intermediate storage component to receive the frozen pellets from the PT 206 (a detailed example of an intermediate storage component is illustrated in figure 5). In this way, the production of the pelletizing tower (PT) 206 can be stored intermittently in the transfer section 1TS 208.
[0081] The configuration illustrated in figure 2c illustrates that the freeze dryer (FD) 210 has just lyophilized a batch of product (for example, micropellets). The second transfer section (2TS) 212 is open and thus makes it possible to transfer 204 the freeze-dried product from the freeze dryer (FD) 210 to the discharge station (DS) 214 for discharge. It should be understood that in the preferred embodiments the separate production cycles in the pelletizing tower (PT) 206 (illustrated as product flow 262) and in the freeze dryer (FD) 210, respectively, each is carried out under closed conditions, respectively, for each of the different products handled in them. As the transfer section 1TS is adapted to operatively separate the pelletizing tower (PT) 206 and the freeze dryer (FD) 210 from each other, different products can be processed in both process devices. Prior to a transfer of the frozen pellets from intermediate storage of the transfer section (1TS) 208, the freeze dryer (FD) 210 can preferably be cleaned and / or sterilized (for example, through CiP / SiP).
[0082] Generally, process line 200 as described several times in figures 2a-2c illustrates an embodiment of an integrated process line for the production of freeze-dried product (eg micropellets) under closed point-to-point conditions where the various process devices are permanently connected to each other, and in which liquid can be fed into the system at one end of the process line, and the lyophilized product can be collected at the other end of the process line. If the flowable material (e.g., liquids and / or pastes) is sterile and process line 200 is operated under sterile conditions, the dried product will also be sterile.
[0083] In several preferred embodiments, the process line 200 is permanently mechanically integrated, thus negating the requirements to dismantle the various process devices, which is conventionally required, for example, after a production cycle to perform a cleaning / sterilization of the process line.
[0084] The design principles of process line 200 also allow process control of relevant process / product parameters since the devices can be operationally separated from each other (for example, through the operation of one or more transfer sections) and can be performed in different operating modes and / or process / product control modes can be performed individually optimized for the separate process devices. The process line control facilities 200 are preferably adapted to separately activate the operating modes for each of the process devices and transfer sections of the line.
[0085] Figure 3 illustrates a specific modality of a process line 300 designed according to the principles of the invention for the production of freeze-dried micropellets under closed conditions. Process line 300 generally comprises a liquid feed section 301, pelletizing tower 302, as a specific embodiment of a spray chamber or spray freezing equipment, a freeze dryer 304, and a discharge station 306. In a preferred embodiment, the pelletizing tower 302 and the freeze dryer 304 are permanently connected to each other via a first transfer section 308, while the freeze dryer 304 and the discharge station 306 are permanently connected to each other via a second transfer section 310. Each transfer section 308 and 310 provides product transfers between the connected process devices. The liquid feed section 301 shown only schematically in figure 3 is to supply the liquid product to the pelletizing tower 302. The generation of droplets in the pelletizing tower 302 is affected by the flow rate, viscosity at a given temperature, and more properties physical properties of the liquid as well as the processing conditions of the atomization process, such as the physical conditions of the spray equipment including frequency, pressure, etc. Therefore, the liquid feed section 301 is adapted to release the liquid controllably and to generally release the liquid in a regular and stable flow. For this purpose, the liquid supply section may include one or more pumps. Any pump can be used that allows precise dosing or measurement. Examples of suitable pumps include, but are not limited to, peristaltic pumps, diaphragm pumps, piston pumps, eccentric pumps, cavity pumps, progressive cavity pumps, Mohno pumps, etc. Such pumps can be provided separately and / or as part of control devices such as pressure damping devices, which can be provided for uniform flow and pressure at the point of entry into the droplet generating component of the pelletizing tower 302 (or more generally the spray device). Alternatively, or in addition, the liquid feed section may comprise a temperature control device, for example, a heat exchanger, to cool the liquid in order to reduce the required freezing capacities within the pelletizing tower. The temperature control device can be used to control the viscosity of the liquid and, in turn, in combination with the feed rate, the droplet size / formation rate. The liquid feed section may include one or more flow meters, for example, a flow meter for each nozzle of a multi-nozzle droplet generation system, for sensing the feed rate. One or more filtration components can be provided. Examples for such a filtration component include, but are not limited to, mesh filters, fabric filters, membrane filters and adsorption filters. The liquid feed section can also be configured to provide sterility of the liquid, in addition, or, alternatively, the liquid can be provided to the pre-sterilized liquid feed section.
[0086] Freezing of droplets in a spraying device such as pelletizing tower 302 can be obtained, for example, so that the diluted composition, i.e., the formulated liquid product, is sprayed and / or pelleted. "Pelletization" can be defined as a (for example, frequency-induced) disruption of a constant liquid flow in discrete droplets. Pelletizing does not exclude the use of other droplet generation techniques such as the use of hydraulic nozzles, two-component nozzles, etc. Generally, the purpose of spraying and / or pelletizing is to generate calibrated droplets with diameter ranges, for example, from 200 μm to 1,500 μm, with a narrow size distribution of ± 25%, more preferably ± 10%. The droplets fall into the pellet tower where a spatial temperature profile is maintained, for example, between -40oC to -60oC, preferably between -50oC and -60oC, in a top area and between -150oC to - 192oC, for example, between - 150oC and -160oC, in a bottom area of the tower. The lower temperature ranges can be obtained in the tower by alternative cooling systems, for example, a cooling system using helium. The droplets freeze during their fall to form calibrated frozen particles, preferably round ones (ie, micropellets).
[0087] Specifically, the pelletizing tower 302 preferably comprises side walls 320, a dome 322 and a bottom 324. The dome 322 is equipped with a droplet generation system 326 according to one or more of the aspects discussed above and can, for example, understanding one or more nozzles for generating droplets from a liquid (for example, by "atomization") provided to the 326 system from the liquid feed section 301. The droplets are frozen on their way down to bottom 324.
[0088] A sectional illustration of a particular embodiment and pelletizing tower wall 320 is described in figure 4. Preferably, wall 320 comprises a double wall comprising outer wall 402 and inner wall 404 with inner volume 403 defined therein. . The inner wall 404 has an inner surface 406 encompassing the inner volume 328 of the pelletizing tower 302 (as shown in figure 3). To cool the volume 328, the inner wall 404 (more precisely, the inner wall surface 406) is cooled by a cooling circuit 408 which, as shown in figure 4, preferably comprises a tube system 410 extending at least throughout a portion of internal volume 403 and being connected between an inflow of cooling medium 412 and a flow of cooling medium 414. The inflow 412 and flow 414 can be connected to an external cooling medium reservoir which in turn comprises another equipment such as pumps, valves and 415 control circuit and / or instrumentation (which can, for example, be controlled by computer) as required for a specific process. The control circuit 415 comprises sensor equipment 416 arranged on the internal wall 404 for sensing conditions within the internal volume 328, the equipment 416 connected via sensor liners (lines) 418 (for example, one or more electrically conductive wires, cables fiber optics, etc.) for remote control components of the control circuit.
[0089] As shown generally in figure 4, the internal volume 403 inside the double wall 320 houses the cooling circuit 408, sensor (linings) 418, and optionally sterilization pipe 420 providing the supply of sterilization medium for access points to the sterilization medium 422. Steam can be used as a sterilization medium that is supplied through the plumbing tubes 420 and enters the inner volume 328 of the pelletizing tower for sterilization, for example, from the inner wall surface 406 through one or more appropriately provided heads 424 (sterilization) at access points 422. Sterilization heads 424 may, for example, comprise a plurality of nozzles (or jets) 426 enabling the introduction of one or more appropriate sterilization means and potentially other fluids or gases in the pelletizing tower 302. The liners 418, piping 408, and / or plumbing 420 inside the double operating wall 320 are designed to minimize izing the number of openings 426 within the outer wall 402 and, therefore, contribute to effectively maintaining closed conditions, i.e., sterility and / or containment within the pelletizing tower 302 and thus the internal volume 328.
[0090] Cooling of the internal volume 328 of the pelletizing tower 302 sufficient to freeze the falling droplets 323 (as shown in figure 3) can be obtained by cooling the internal wall surface 406 through the pipeline leading to the cooling medium 408 and providing the pelletizing tower 302 with an appropriate height. Therefore, a simultaneous counterflow or flow of cooled gas in the internal volume 328 or another measure to direct the cooling of the falling droplets 323 is avoided. By avoiding the contact of a circulating primary cooling medium such as a simultaneous counterflow or gas flow with the product falling 323 in the internal volume 328 of the pelletizing tower 302, the need to provide an expensive sterile cooling medium is avoided when sterile production cycles are desired. The cooling medium circulating outside the internal volume 328, for example, in the 408 pipeline, does not need to be sterile. The present invention contemplates that the double-walled pelletizing tower and cooling apparatus described in some of the preferred embodiments in this document will allow operators to achieve considerable cost savings over existing pelletizing tower designs. In this way, the pelletizing tower 302 can be adapted to separate the product flow, that is, the droplets 323 passing through the internal volume 328, from the cooling circuit (primary) incorporated as pipe 408 and the circulating cooling medium. of the same to freeze liquid droplets 323. However, in still other embodiments, direct cooling and freezing solidification of droplets 323 through and a (sterile) cooling medium using typical pelletizing schemes is also contemplated. For example, a direct cooling medium can be recirculated in a closed loop to limit the need to provide a large amount of sterile cooling medium.
[0091] The cooling medium circulating inside spirals 408 can generally be liquid and / or gaseous. The cooling medium circulating within the 408 pipeline may comprise nitrogen, for example, it may comprise a mixture of nitrogen / air, and / or brine / silicon oil, which is introduced into the spiral system 408 via inflow 410. The present The invention is not, however, limited to the exemplary cooling media mentioned above.
[0092] The droplet generation system 326 disposed with the dome 322 can, for example, comprise one or more high frequency nozzles for transforming the flowable material (for example, liquids and / or pastes) to be pelletized in droplets. With respect to exemplary numerical values, high frequency nozzles can have an operating range of between 1-4 kHz at a productivity of 530 g / min per nozzle with a liquid with a solids content in the range of 550% (w / w ).
[0093] The droplets 323 are frozen in their gravity-induced drop inside the pelletizing tower 302 due to cooling mediated by the temperature-controlled wall 320 of the pelletizing tower 302 and an appropriate non-circulating atmosphere provided with internal volume 328, for example, an atmosphere of nitrogen and / or air (optionally sterile). In an exemplary modality, in the absence of other cooling mechanisms, forming droplets by freezing in round micropellets with sizes / diameters in the range of 100-800 μm, an appropriate height of the pelletizing tower is between 1-2 m (meters) while forming droplets by freezing in pellets with a size range of up to 1,500 μm (micrometers) the pelletizing tower is between about 2-3 m in which the diameter of the pelletizing tower can be between about 50-150 cm for a height of 200 -300 cm. The temperatures in the pelletizing tower can optionally be maintained or varied / cycled entirely between about -50oC to -190oC.
[0094] The frozen droplets / micropellets 323 reach a bottom 324 of the pelletizing tower 302. In the embodiment discussed at present, the product is then automatically transferred by gravity towards and into the transfer section 308.
[0095] The transfer section 308 as illustrated in figure 3 comprises an inflow 332, a flow 334, and an intermediate separation component 336. Each inflow 332 and flow 334, respectively, can comprise at least one double-walled tube , wherein the double wall can similarly be configured as described for the double walls 320 of the pelletizing tower 302 in figure 4. Specifically, the double inflow walls 332 and / or flow 334 can optionally comprise cooling circuit to cool an internal wall , sensor circuit, and / or access points for cleaning / sterilization. For example, in preferred embodiments, a constant / increasing / decreasing temperature in relation to the inner volume of the transfer section and the frozen / solidified product therein can be maintained throughout the transfer section 308.
[0096] As illustrated in figure 3, the inflow components 332 and flow 334 are arranged to carry out a transfer of the product from the pelletizing tower 302 to the freeze dryer 304 by gravity (in other embodiments, in addition, or alternatively, an active mechanical conveyor is provided comprising, for example, a conveyor component, a vibration component, etc.). In order to maintain closed conditions such as sterility and / or containment for the transfer of the product between the process devices, the transfer section 308 is optionally permanently connected to the pelletizing tower 302 and the freeze dryer 304, respectively, through clamping portions shown schematically 338. The mechanical clamping portions 338 allow protection from sterility and / or containment in the transition from the respective process device to a transfer section and in the transition from a transfer section to the next process device . The expert is aware of the design options available in this regard.
[0097] Permanent connections can be obtained with welding. In other modalities, the permanent connections, which are intended to be permanent during the production, cleaning, sterilization cycles, etc., but which can be disassembled for the purposes of inspection, review, validation, etc., can be obtained by screwing and / or screwing with nut. Sealing technologies that can be applied in conjunction with the techniques mentioned above in order to provide the prerequisite for "closed conditions" (sterile and / or containment conditions) include, but are not limited to, flat seals or gaskets, or flange connections, and the like. Any sealing material must be resistant to absorption and must withstand low temperatures in order to avoid embrittlement and / or friction with a risk of pollution of the product resulting from it. Also, adhesive bonding can be employed as long as any adhesive is emission free.
[0098] Note that a "sealing" property is understood as "leak-free" for gas, liquids and solids, to be maintained for pressure differences of, for example, atmospheric conditions on the one hand and vacuum conditions by on the other hand, where a vacuum can mean a pressure as low as 10 millibar, or 1 millibar, or 500 microbar, or 1 microbar.
[0099] The separation component 336 is adapted to provide a controllable operational separation between the pelletizing tower 302 and the freeze dryer 304. For example, the separation component 336 may comprise a closing device for closing a transfer device such as like a tube. The modalities of closing devices include, but are not limited to, sealable separating means, such as a flat door, cover or valve. Non-limiting examples for various suitable types include butterfly valves, compression valves, and guillotine valves and the like.
[00100] Closed conditions can be preserved not only with respect to a process line environment 300, the requirement for "operative separation" can also include the requirement for a sterile / contained enclosure between devices 302 and 304. For example, a vacuum tight seal or lock can be provided in the separation component 336 in this regard. This can enable, for example, a production cycle in batch mode of freeze drying in the freeze dryer 304 under vacuum, while a higher pressure, for example, atmospheric pressure or hyperbaric pressure, is maintained in a separate component (for example, example, the pelletizing tower 302) of the process line while it is engaged with another operational mode such as pelletizing, cleaning or sterilization. Generally, the separation means 336 can be adapted to separate several operating modes from one another, so that the operational separation includes the sealable separation of operating conditions such as pressure (with vacuum or overpressure conditions on the one hand), temperature, humidity, etc.
[00101] Figure 5 illustrates another exemplary transfer section modality 500 that can be used in place of transfer section 308 (and / or transfer section 310) in process line 300 illustrated in figure 3. Similar to transfer sections 308 and 310, the transfer section 500 comprises an inflow 502 and a flow 504. However, instead of just a separating means such as a valve, the transfer section 500 provides two of such separating means 506 and 508. In addition, the transfer section 500 comprises a temporary storage component 510 interconnected between the separation means 506 and 508. The modalities are contemplated, in which the transfer section 500 of figure 5 replaces the transfer section 308 in figure 3. Consequently, storage component 510 can optionally be adapted to store frozen pellets received from pelletizing tower 302, where storage component 510 can receive and collect the product of a continuous (semi-continuous) production cycle from the pelletizing tower 302, or a fraction of a cycle from it, as controlled and / or measured by the opening and closing of the 506 separation medium. Similarly, the medium opening and closing separator 508 controls the other flow of the product stored in the storage component 510 to the freeze dryer 304.
[00102] The provision of the two separation means, 506 and 508, with the intermediate storage component 510, therefore, provides more configuration options over that of the mandatory direct transfer of the product from the pelletizing tower 302 into the dryer by freezing 304 as with transfer section 308 in figure 3. In addition, the flexibility of this approach and the corresponding modalities provides another decoupling of the pelletizing tower 302 operation and freeze dryer 304, respectively, and consequently provides opportunities for advantageous independent operations respective process devices.
[00103] Transfer section 500 is generally designed to preserve closed conditions (i.e., sterile and / or containment conditions) during product transfer (and storage) between process devices connected to inflow 302 and flow 304, respectively. In this way, section 500 contributes to preserving the closed point-to-point conditions of the process line. This particular feature of the transfer section 500 is illustrated in Figure 5 by the mechanical fixings 522 providing a means for permanently mechanically attaching the transfer section 500 to the respective process device.
[00104] The transfer section 500, as illustrated in figure 5, comprises an inflow 502 of double wall, flow 504 and storage 510. Although the double walls 512 of inflow 502 or flow 504 can be passively cooled, for example, by insulation , the temporary storage double wall 514 510 can be adapted to provide a temperature-controlled inner wall, i.e., active cooling of the inner wall. In this regard, reference number 516 indicates the cooling circuit provided within the double walls 514 of storage component 510. Specifically, the double walls 514 of storage component 510 can be configured similarly as discussed above for double walls 320 of the tower pelletizing machine 302 (as shown in figure 4). In particular, in addition to the cooling circuit 516 for circulating a cooling medium, the double wall 514 (and / or the double walls 512) can also enclose in it one or more additional piping systems for transporting fluids and / or gases, such as cleaning means, and / or sterilization means. In some preferred embodiments, these additional piping systems are connected to access points 518 in transfer section 500. In still other embodiments, the sensor circuit for sensor elements 520 can also reside within / across the double walls 512 and / or 514. Sensor elements 520 may comprise one or more temperature sensors, pressure sensors and / or humidity sensors, etc.
[00105] Although the exemplary transfer sections illustrated in figures 3 and 5 contemplate the gravity-assisted product flow, other transfer mechanisms can optionally be employed, such as the combination of gravity and one or more other transfer mechanisms. For example, other mechanisms for transporting product include, but are not limited to, drill based mechanisms, conveyor belts, pressure drive mechanisms, gas supported mechanisms, pneumatic drive mechanisms, piston based mechanisms, electrostatic mechanisms, and the like .
[00106] With reference again to figure 3, the product drying step can be carried out by lyophilization, that is, the sublimation of ice and removal of the resulting water vapor. The lyophilization process can be carried out in a vacuum rotary drum processing device. In this regard, once the freeze dryer is loaded with product, a vacuum is created in the freeze drying chamber to initiate the freeze drying of the pellets. The low pressure conditions referred to as "vacuum" herein may comprise pressures at or below 10 millibar, preferably at or below 1 millibar, particularly preferably at or below 500 microbar. In one example, the temperature range in the drying unit is maintained between about - 20oC to -55oC, or generally at or within a temperature range as required for proper drying according to predefined specifications.
[00107] Consequently, the freeze dryer 304 is equipped with rotary drum 366 which, due to its rotation, provides a large effective drying surface of the product and therefore quick drying compared to bottle-based and / or tray-based drying. . The modalities of rotary drum drying devices, which may be appropriate depending on the individual case, include, but are not limited to, vacuum drum dryers, contact vacuum drum dryers, convective drum dryers, and the like. A specific rotary drum dryer is described, for example, in DE 196 54 134 C2.
[00108] The term "effective product surface" is understood in this document to refer to the product surface that is actually exposed and therefore available for heat and mass transfer during the drying process, where the transfer of mass may in particular include evaporation of sublimation vapor. Although the present invention is not limited to any particular mechanism of action or methodology, it is contemplated that the rotation of the product during the drying process exposes the surface area of the product (i.e., increases the surface of the effective product) more than the conventional bottle-based and / or tray-based drying methodologies (including, for example, vibrating tray drying). Thus, the use of one or more drying devices based on rotating drum can lead to shorter drying cycle times than conventional bottle-based and / or tray-based drying methodologies.
[00109] In the preferred embodiments, in addition to the process devices such as the pelletizing tower 302 and the transfer sections such as the transfer section 308, the freeze dryer 304 is also configured separately for operation under closed conditions. The 304 freeze dryer is adapted to carry out at least the operations and freeze drying of pellets, optionally automatic cleaning of the freeze dryer in place, and automatic sterilization of the freeze dryer in place.
[00110] Specifically, in certain embodiments, the freeze dryer 304 comprises a first chamber 362 and a second chamber 364, wherein the first chamber 362 comprises a rotating drum 366 for receiving the product from the pelletizing tower 302, and the second chamber 364 comprises a condenser 368 and a vacuum pump to provide a vacuum in the inner volume 370 of the chamber 362 and inner volume 372 of the barrel 366. The valve 371 is provided for separating the chambers 362 and 364 according to the operating modes of the freeze dryer 304. Chamber 362 and / or 364 may be referred to as "vacuum chambers" as used herein by virtue of their operation.
[00111] In preferred embodiments, the vacuum chamber 362 comprises a double wall structure having an outer wall 374 and an inner wall 376 being constructed similarly as shown in figure 4 for the double wall structure 320 of the pelletizing tower 302. Specifically , the double walls 374 and 376 optionally comprise a cooling circuit to cool the interior 370 of the vacuum chamber 362 and in particular the internal volume 372 of the rotating drum 366 and, in addition, it may further comprise one or more heating means such as heating tubes to be operable during the lyophilization process, cleaning process and / or sterilization process. In addition, or alternatively, the equipment for transferring heat to the particles during lyophilization such as, for example, heat conduction medium, for example, tubes for transporting a heating medium therefrom, medium for ohmic heating, for example , heating coils, and / or microwave heating means, for example, one or more magnetrons, can be provided anywhere in association with drum 366 and / or chamber 362. Vacuum chamber 362 and outer wall 374 and the inner wall 376 thereof may further comprise one or more lines of sensors and / or tubes for conducting the cleaning and / or sterilizing means. Sensor elements related to sensing temperature, pressure, and the like, and facilities 378 for automatic cleaning and / or sterilization in place can be arranged on the inner wall 376.
[00112] Drum 366 is supported in its rotational movement by support elements 380. Drum 366 has a free opening 382 so that pressure conditions (such as vacuum conditions), temperature conditions, etc., are promoted between internal volumes 370 and 372. In the freeze drying operation, for example, the steam resulting from sublimation is extracted from volume 370 of drum 366 containing the pellets to be freeze-dried in volume 370 of vacuum chamber 362 and still in camera 364.
The flow 334 of the transfer section 308 comprises a projection 384 protruding into the drum 366 of the freeze dryer 304 to guide the product into the drum 366. Since the drum 366 is completely contained within the chamber vacuum 362, it is not necessary to isolate or separate the drum 366 further; in other words, the function of providing closed conditions for processing inside the device 304 is with the vacuum chamber 362. Therefore, in certain embodiments, the flow 334 of the transfer section 308 can be permanently connected to the vacuum chamber 362 in this way . A complex assembly or anchoring / undocking arrangement of the stationary transfer section and the rotating drum 366 is not required. According to the various embodiments of the present invention, the sterile and / or contained transfer of product from the pelletizing tower 302 into the rotating drum 366 of the freeze dryer 304 is implemented safely and cost effectively.
[00114] Other proportional modalities the freeze dryer 304 being specifically adapted for closed operation (that is, for operation to preserve sterility of the product to be dried by freezing and / or containment) in which chambers 362 and 364 are designed to implement a housing properly closed. The fixing means 386 can be provided in the freeze dryer 304 to permanently connect with the transfer section 308, in particular the fixing means 338 of the transfer section 308, in which the fixing means 338 and 386 are adapted to ensure, when attached to each other, sterility and / or containment for the transition of the product from transfer section 308 in the freeze dryer 304. Fixing means 338 and means 38 together may comprise welding, riveting, screwing, etc.
[00115] The transfer section 310 connects the freeze dryer 304 and the discharge station 306. The discharge of the drum 366 can be obtained, for example, by providing one or more of the following: 1) a discharge opening (both the opening 382 and / or an opening in a barrel cylindrical section 366); 2) providing a means of discharge guidance; and 3) tilting drum 366. Unloaded pellets can then flow with gravity assistance and / or one or more mechanical conveyors from chamber 362 through transfer section 310 into discharge section 306.
The discharge station 306 comprises one or more filling means 390 provided for dispensing the product received from the freeze dryer 304 into containers 392. Containers 392 may comprise final containers such as bottles or intermediate containers such as Containers of Intermediate Bulk Items ("IBCs"). Similar to other process devices (for example, devices 302 and 304), the discharge station 306 is adapted for operation under closed conditions, so that, for example, a sterile product can be filled into a container 392 under sterile conditions. The discharge station 306 in the embodiment shown in figure 3 has double walls 394. Depending on the products intended to be processed using line 300, the double wall 394 can internally house installations such as those described in figure 4 with reference to the double wall 320 of the tower pelletizing unit 302. For example, the double wall 394 cannot be equipped with a cooling and / or heating circuit, but it can be equipped with a sensor lining that connects to the sensors arranged on the internal wall of the discharge station 306 to sense the temperature, humidity, etc. The double wall 394 can also be equipped with piping to provide access points 396 with cleaning / sterilization means. In addition to the loading containers 392, the unloading station 306 can, in addition, be adapted to take product samples and / or manipulate the product under closed conditions.
[00117] The freeze dryer 304 and the discharge station 306 are permanently connected via transfer section 310. Transfer section 310 comprises inflow 3102, flow 3104 and separation medium 3106. Transfer section 310 can be similar in design to transfer section 308. However, although transfer section 310 can be provided with double walls, the cooling circuit can be omitted either in flow 304 or in both inflow 3102 and flow 3104, since in many chaos the dried product ready for unloading no longer requires cooling. Even then the double walls can be used to install / close the sensor liners and pipes for cleaning and / or sterilization (for example, conducting the cleaning and / or sterilization means), and / or can be used to safely implement the conditions closed to protect the sterility from and / or provide containment for the product flow from the freeze dryer 304 to the discharge station 306.
[00118] Figure 6 illustrates in the pertinent part an alternative embodiment of a freeze dryer 600 according to the invention. The freeze dryer 600 comprises a vacuum chamber 602 housing an internal rotating drum 604, the construction of which can be similar to that described for a freeze dryer 304 in figure 3. The freeze dryer 600 is adapted for direct discharge of the product, inside the vacuum chamber 602, inside containers 606 under closed conditions, that is, for example, under protection of the sterility of the product.
[00119] A sterilization chamber 608 can be loaded with one or more IBCs 606 through sealable door 610. Chamber 608 has another sealable door 612 which when open allows the transfer of IBCs between vacuum chamber 602 and the sterilization chamber 608. After loading IBCs 606 from the environment through port 610 into chamber 608, IBCs 606 can be sterilized using sterilization equipment 616, which can, for example, be connected to a sterilization medium also supplying sterilization means for SiP equipment of the freeze dryer 600. After sterilization of the IBCs 606, the door 612 is opened and the IBCs 606 are moved into the vacuum chamber 602 of the freeze dryer 600 by a mechanical conveyor (for example, a system traction) 618.
[00120] The rotating drum 604 can optionally be equipped with a peripheral opening 620, as shown schematically in figure 6, which can be automatically controlled to open after freeze drying a batch of product is completed to discharge the product from the drum 604 in one or more of the 606 IBCs. The 618 drive system can move the filled 606 IBCs back into the 608 chamber for proper sterile sealing of the 606 IBCs, before unloading them from the 608 chamber. The appropriate 606 IBCs sealing filled can alternatively also be carried out in the vacuum chamber 602.
[00121] The transfer sections 308 and 310 described in the process line 300 (figure 3) are provided for a flow of bulk product between the process devices under preservation of closed conditions. As there is no bulk item between the vacuum chamber 602 and the sterilization chamber 608, no further transfer section is required in this embodiment. However, the sterilization chamber 608 is integrated with the vacuum chamber 602 so that closed point-to-point conditions can be preserved in case empty containers must be introduced into the vacuum chamber 602. Preferably, door 612 when closed preserves the sterility and / or containment of the processed product in the 600 freeze dryer.
[00122] It should be noted that the freeze dryers illustrated in figures 3 and 6 are not limited to vacuum freeze drying techniques. Generally, freeze drying including sublimation can be carried out with various pressure regimes and can be carried out, for example, under atmospheric pressure. Therefore, a freeze dryer used in a process line according to the invention can be a vacuum freeze dryer, a freeze dryer adapted for freeze drying under another pressure regime (which can still be adapted for closed operation, (ie, protect sterility and / or preserve containment), or a freeze dryer can be operated under various pressure regimes, for example, vacuum or atmospheric pressure.
[00123] Referring again to figure 3, as an aspect of providing a safe and cost effective permanently integrated process line that preserves closed end-to-end processing conditions, the entire process line 300 is adapted for CiP and / or SiP, as indicated by exemplary cleaning / sterilization medium access points 330 in the pelletizing tower 302, access points 340 in transfer section 308, access points 378 in the freeze dryer 304 and access points 396 at the station discharge 306. Each of these access points may be provided with a sterilization medium such as steam through the 3302 pipeline in flow communication with preferably a single 3304 sterilization medium repository (and in several other embodiments), optionally comprising, for example, a steam generator. The repository system 3304 and piping 3302 can be controlled accordingly so that cleaning / sterilization is performed for the entire line 300, or for one or more individual parts or subsections of the process line. This situation is illustrated exemplarily in figure 2b, in which only the PT pelletizing tower is cleaned and sterilized, while other devices such as FD and FS are in different operating modes (that is, not engaged in the maintenance of CiP and / or SiP or in another way). With respect to a transfer section adapted to operationally separate a first process device from a second process device, it is noted that optionally only part of this transfer section can be subjected to cleaning / sterilization, namely, in the case of first process device (or second) to be cleaned / sterilized: then (only) the inflow or flow of the transfer section connected to the first (or second) process device can also be cleaned / sterilized.
[00124] Figure 7a illustrates an exemplary operative processing modality 700 of process line 300 of figure 3, as such reference will be taken for the process line and the processing devices thereof as needed. Generally, the process is related to the production of freeze-dried pellets under closed conditions 702. In step 704, the pelletizing tower 302 is fed with flowable material (for example, liquids and / or pastes) to be pelletized and operates to generate droplets from the material and to freeze / solidify the liquid / liquefied droplets to form frozen bodies (eg product, particles, microparticles, pellets, micropellets). In step 706, which can be carried out subsequent to step 704 as shown in figure 7a, but can also be carried out at least parallel to step 704, the product is transferred from the pelletizing tower 302 through the transfer section 308 inward of the freeze dryer 304 (possibly inside the rotating drum 366 of the same) under closed conditions. For example, in case the production cycle 700 comprises the production of sterile micropellets, the transfer in step 706 occurs under protection of the sterility of the product.
[00125] When the pelletizing process in the pelletizing tower 302 is completed and the frozen pellets generated therein have been fully transferred into the freeze dryer 304, as illustrated operatively in step 708 of figure 7a, the pelletizing tower 302 and the Freeze dryer 304 are preferably operatively operated and independently controlled by valve 336 of transfer section 308 in order to seal sealably (for example, under vacuum tight conditions) devices 302 and 304 from each other. In certain embodiments, subsequent steps 710 and 712 can be carried out at least partially in parallel. In step 712, the freeze dryer 304 is operatively controlled to freeze dry the pellets previously transferred in step 706 as a bulk item. In step 710, CiP and / or SiP are carried out in the pelletizing tower 302, for example, to prepare the pelletizing tower for a subsequent production cycle.
[00126] In step 714 the freeze-dried product is discharged from the freeze dryer 304 into the discharge station 306. Step 714 can be performed after step 712 is completed, but it can also be performed in parallel to step 710 The discharge step 714 may comprise opening the transfer section 310. For the preservation of closed conditions, for example, sterility, the discharge station 306 can be cleaned and / or sterilized before opening the transfer section 310.
[00127] After the discharge is completed in step 714 and the entire batch production (or a portion thereof) is filled in one or more 392 containers, the transfer section 310 can be configured to operationally separate the freeze dryer 304 a from the unloading station 306. In step 716, CiP and / or SiP can then be carried out in the 304 freeze dryer. After the filled containers 392 unload from the unloading station 306, CiP and / or SiP can also be carried out at the discharge station 306 either in parallel to steps 716 and / or 710 in the freeze dryer 304 or subsequently. As soon as steps 710 and 716 are completed, operation 700 of process line 300 has been completed and process line 300 may be available for the next production cycle. Steps 710 and 716 of cleaning and / or sterilization can be carried out at any time, but are preferably carried out before the start of a production cycle.
[00128] However, in other modalities, the subsequent production cycles can start without cleaning and / or sterilizing the freeze dryer 304 being finalized (as in step 716 in figure 7), once in a process line that is separable operatively, subsequent production cycles can begin as soon as cleaning and / or sterilizing the pelletizing tower is completed.
[00129] An exemplary operational scheme 730 is similarly illustrated in figure 7b. Step 732 comprises feeding liquid, generating droplets from it, and solidifying - freezing the liquid droplets to form frozen pellets in the pelletizing tower 304. Step 734 comprises cleaning and / or sterilizing the freeze dryer 304 that is, it is identical to step 716. In certain embodiments, steps 732 and 734 can be performed in parallel. Thus, step 732 can also be inserted in the scheme 700 of figure 7a to be carried out after step 710 and in parallel to step 716.
[00130] After step 734 is completed, transfer section 308 can be opened at step 736 by giving a program flow of the frozen pellets produced in step 732 and loading them onto rotating drum 366. Although step 736 has to follow step 734 to protect the sterility of the product, step 732 can be performed with any time relation to step 736, for example, pelletizing can start before or after opening the transfer section in step 736. Depending on the settings and parameters of the process line, it can be advantageous to fill the frozen pellets in a slowly rotating drum, as this is envisaged to help prevent particle agglomerations (eg pellets or micropellets). Therefore, in certain embodiments, in step 706 and / or step 736 the rotating drum 366 is kept rotating. In addition, product transfer in step 706 and / or step 736 can be carried out continuously during (i.e., in parallel with) spray solidification in step 704 and / or step 732.
[00131] In a preferred embodiment of process line 300, the transfer section 500 of figure 5 is employed between the pelletizing tower 302 and the freeze dryer 304 so that the frozen pellets produced in the pelletizing tower 302 can be stored temporarily in the warehouse 512 of the transfer section 500 until the transfer valve 508 is opened in step 736 to load the frozen pellets into the rotating drum 366. This sequence is contemplated to further decouple the operation of the devices 302 and 304 from each other while maintaining closed conditions, that is, sterility and / or containment. After loading the pellets into the 304 freeze dryer, the pellets are freeze-dried in step 738. Process 730 in figure 7b can, for example, continue with steps (710 e) 714 and 716.
[00132] In another modified modality, the pelletizing tower continues to pellet and feed the temporary storage 512 of the transfer section 500 with freezing pellets, while the frozen pellets are unloaded in batch mode from the storage 512 inside the dryer by freezing 304 according to the capacity of the freeze dryer 304. Thus, the production rates of the pelletizing tower 302 and the freeze dryer 304, respectively, can be decoupled to some degree including (almost) continuous or batch operating modes. Process devices can be decoupled within the process line in the case of adapted and / or controllable transfer sections. The transfer sections cannot or may not be equipped with temporary storage illustrated in figure 5. A transfer section such as section 308 in figure 3 can simply be controlled to "buffer" the frozen pellets in the bottom area 324 of the tower. pelletizing 302 keeping the separation means 336 closed.
[00133] The exemplary modalities described in this document are intended to illustrate the flexibility of the process line concepts according to the invention. For example, the provision of closed conditions point by point by the process devices, each specifically adapted for operation under closed conditions and permanently interconnecting these devices with the transfer sections also adapted for sterility protection and / or containment preservation, prevents the need to employ one or more insulators to obtain closed conditions. A process line according to the invention can be operated in a non-sterile environment to manufacture a sterile product. This leads to corresponding advantages in the analytical requirements and associated costs. In addition, the preferred embodiments avoid the difficulties experienced in typical process lines that employ multiple insulators that arise during product handling while connecting the interfaces between the various insulators. The process lines according to the invention are thus not limited by the size of the insulator available, and, in principle, there is no size limit on the process lines adapted for operation under closed conditions. The invention contemplates that considerable cost reductions are possible in GMP, GLP (Good Laboratory Practice), and / or GCP (Good Clinical Practice) of totally typical conformation, and international equivalents, manufacturing processes and operations, avoiding the need to use a plurality of expensive insulators.
[00134] In these and other embodiments, although the process line concepts of the invention provide an integrated system, for example, in the sense of end-to-end closed conditions, process devices such as the pelletizing tower (or other pelletizing device) spray chamber) and freeze dryer are clearly kept separate from each other and are also operably separable by the function of the interconnected transfer sections. In this way, the disadvantages of highly integrated systems in which the entire process is carried out within a single device specifically adapted are avoided. Keeping multiple process devices as separate units allows you to separately optimize each process device with respect to its specific functionality. For example, according to an embodiment of the invention, it is contemplated that a process line comprising a freeze dryer comprising a rotating drum provides comparatively faster drying times than conventional methodologies. In other embodiments, the separate optimization of process devices such as the pelletizing tower and / or a freeze dryer allows separate optimization of the applied cooling mechanisms. As illustrated in the examples, it is possible to provide process lines that do not need a sterile cooling medium such as liquid / nitrogen gas (mixtures), which correspondingly reduces production costs. As the concepts of the invention are applicable for the production of bulk articles, the process lines do not need to be adapted to any specific containers such as IBCs or bottles and, in another example, specific buffers for drying in bottles are not required. If desired, a process line can be adapted to specific containers, but this can only refer to a device that relates to unloading, for example, a line loading station.
[00135] Products resulting from process lines adapted according to the invention can comprise virtually any formulation in liquid or flowable paste form which is also suitable for conventional freeze drying processes (for example, service life type), for example , monoclonal antibodies, protein-based APIs, DNA-based APIs, cell / tissue substances, vaccines, APIs for oral dosage forms such as APIs with low solubility / bioavailability, fast dispersible oral solid dosage forms such as ODTs, orally dispersible tablets , stick-filled adaptations, etc., as well as various products in the fine chemicals and food products industries. In general, flowable materials suitable for pelletizing include compositions that are receptive to the benefits of the freeze-drying process (e.g., increased stability once freeze-dried).
[00136] The invention allows the generation of, for example, sterile lyophilized particles and uniformly calibrated, for example, micropellets, as a bulk article. The resulting product can be flowing freely, free of dust and homogeneous. Such products have good handling properties and can be easily combined with other components, where the components may be incompatible in the liquid state or only stable for a short period of time and, therefore, otherwise not suitable for conventional freeze drying. . Certain process lines can thus provide a basis for separating filling processes and prior to drying processes, that is, filling on demand becomes practically feasible. The relatively time-consuming manufacture of bulk articles can readily be carried out even if the API dosage is yet to be defined. The filling of different compositions / levels can be easily accomplished without the requirement of another liquid composition, spraying, drying and subsequent filling. Time to market can be correspondingly reduced.
[00137] Specifically, the stability of a variety of products can be optimized (for example, including, but not limited to, single or multivariate vaccines with or without adjuvants). Conventionally, it is known that freeze drying is performed as a final step in the pharmaceutical industry, which conventionally follows filling in vials, syringes, or large containers. The dried product must be rehydrated before use. Freeze-drying in the form of particles, particularly in the form of micropellets, allows similar stabilization of, for example, a dry vaccine product as known for simple freeze-drying alone, or can improve stability for storage. Freeze drying of bulk articles (eg vaccine or fine chemical micropellets) offers several advantages compared to conventional freeze drying: for example, but not limited to the following: it allows mixing of dried products before filling , allows titles to be adjusted before filling, allows to minimize the interaction (s) between any products, so that the only product interaction occurs after rehydration, and allows in many cases an improvement in stability.
[00138] In fact, the product to be dried by freezing in bulk can result from a liquid containing, for example, antigens together with an adjuvant, the separate drying of the antigens and the adjuvant (in separate production cycles, which can, in the however, be carried out in the same process line according to the invention), followed by mixing two ingredients before filling or by sequential filling. In other words, stability can be improved by generating separate antigen and adjuvant micropellets, for example. The stabilization formulation can be optimized independently for each antigen and the adjuvant. The antigen and adjuvant micropellets can be subsequently filled into the final containers or mixed before filling into the containers. The separate solid state allows to avoid complete storage interactions (even at the highest temperature) between antigens and adjuvant. Thus, configurations can be achieved, in which the contents of the bottle can be more stable than any other configurations. The interactions between the components can be standardized since they occur only after rehydration of the dry combination with one or more rehydration agents such as an appropriate diluent (for example, water or buffered saline).
[00139] In order to support a permanently mechanically integrated system that provides point-to-point sterility and / or containment, in addition, a specific cleaning concept for the entire process line is contemplated. In one embodiment, a single steam generator, or similar generator / repository for a cleaning / sterilization medium is provided which, through appropriate conduits, serves various process devices including line transfer sections. The cleaning / sterilization system can be cg to perform automatic CiP / SiP for parts of the line or the entire line, which avoids the need for complex and expensive cleaning / sterilization processes that require disassembly of the process line and / or that have to be carried out at least in part manually. In certain embodiments, cleaning / sterilizing insulators is not required or avoided altogether. Cleaning / sterilization of only part of the process line can be performed, while other parts of the line are in different operating modes, including running at full processing capacity. Conventional, highly integrated systems typically only offer the possibility to clean and / or sterilize the entire system at once.
[00140] Consequently, the subject of the invention relates to a process for preparing a vaccine composition comprising one or more antigens in the form of freeze-dried particles comprising:
[00141] freeze-drying a liquid bulk solution comprising one or more antigens according to the process of the invention; and
[00142] fill the freeze-dried particles obtained in a container.
[00143] In another aspect the invention relates to a process for preparing an adjuvant containing vaccine composition comprising one or more antigens in the form of freeze-dried particles comprising:
[00144] freeze-drying a liquid bulk solution comprising an adjuvant and one or more antigens according to the process according to the invention, and
[00145] fill the freeze-dried particles obtained in a container.
[00146] Alternatively, when the one or more antigens and the adjuvant are not in the same solution, the process for preparing an adjuvant containing the vaccine composition comprises:
[00147] freeze drying, separately, a liquid bulk solution of adjuvant and a liquid bulk solution comprising one or more antigens according to the process of the invention,
[00148] mixing the freeze-dried particles of said one or more antigens with the freeze-dried particles of said adjuvant, and
[00149] fill the mixture of freeze-dried particles in a container.
[00150] The bulk liquid antigen (s) solution may contain, for example, dead, live attenuated viruses or antigenic component of viruses such as Influenza, Rotavirus, Flavivirus (including, for example, dengue virus serotypes (DEN) 1, 2, 3 and 4, Japanese encephalitis virus (JE), yellow fever virus (YF) and West Nile virus (WN) as well as chimeric flavivirus). Hepatitis A and B viruses, rabies virus. Bulk liquid solutions of antigen (s) may also contain dead, live attenuated bacteria, or an antigenic component of bacteria such as bacterial protein or polysaccharide antigens (conjugated or unconjugated), for example, of Hemophilus influenzae, Neisseria serotype b meningitidis, Clostridium tetani, Corynebacterium diphthriae, Bordetella pertussi, Clostridium botulinum, Clostridium difficile.
[00151] A liquid bulk solution comprising one or more antigens means a composition obtained at the end of the antigen production process. The bulk liquid antigen (s) solution can be a purified or unpurified antigen solution depending on whether the antigen production process comprises a purification step or not. When the liquid bulk solution comprises several antigens, it can originate from the same or different species of microorganisms. Generally, the bulk liquid antigen (s) solution comprises a buffer and / or stabilizer which can be, for example, a monosaccharide such as mannose, an oligosaccharide such as sucrose, lactose, trehalose, maltose, a sugar alcohol such as sorbitol, mannitol or inositol, or a mixture of two or more of these different stabilizers mentioned above such as a mixture of trehalose and sucrose. Advantageously, the concentration of oligosaccharide monosaccharide, sugar alcohol or mixture of them in the liquid bulk solution of antigen (s) is in the range of 2% (w / v) for the solubility limit in the formulated liquid product, more particularly in the range from 5% (w / v) to 40% (w / v), 5% (w / v) to 20% (w / v) or 20% (w / v) to 40% (w / v). Compositions of liquid bulk antigen (s) solutions containing such stabilizers are described in particular in WO 2009/109550, the subject of which is incorporated by reference.
[00152] When the vaccine composition contains an adjuvant it can be, for example:
[00153] A particulate adjuvant such as: liposomes and in particular cationic liposomes (for example, DC-Chol liposomes, see, for example, US 2006/0165717, DOTAP, 1,2-dialcanoyl-sn-glycero-3- DDAB ethylphosphocholine (EthylPC), (see US 7,344,720), lipid or detergent micelles or other lipid particles (eg CSL or Isconova iscomatrix, virosomes and proteococleat), polymeric nanoparticles or microparticles (eg nanoparticles or PLGA and PLA microparticles, PCPP particles, alginate / chitosan particles) or soluble polymers (eg PCPP, chitosan), protein particles such as Neisseria meningitidis proteasomes, mineral gels (standard aluminum adjuvants: AlOOH, AlPO4) , microparticles or nanoparticles (for example, Ca3 (PO4) 2), polymer / aluminum nanohybrids (for example, PMAA-PEG / AlOOH and PMAA-PEG / AlPO4 nanoparticles), O / W emulsions (for example, MF59 of Novartis, AS-03 from GlaxoSmithKline Biologicals) and W / O mixture (for example, Seppic's ISA51 and ISA720, or as disclosed in WO 2008/009309). For example, an adjuvant emulsion suitable for the process according to the present invention is that disclosed in WO 2007/006939.
[00154] Natural extracts such as: the saponin extract QS21 and its semi-synthetic derivatives such as those developed by Avantogen, bacterial cell wall extracts (eg mycobacterial cell wall skeleton developed by Corixa / GSK and factor mycobacterium cord and its synthetic derivative, trehalose dimethicolate).
[00155] A Toll Like Receptors (TLR) stimulator. In particular, they are natural or synthetic TLT agonists (for example, synthetic lipopeptides that stimulate the heterodimers of TLR2 / 1 or TLR2 / 6, double-stranded RNA that stimulates TLR3, LPS and its MPL derivative that stimulate TLR4, E6020 and RC-529 that stimulate TLR4, flagenin that stimulates TLR5, single-stranded RNA and 3M synthetic imidazoquinolines that stimulate TLR7 and / or TLR8, CpG DNA that stimulates TLR9, natural or synthetic NOD agonists (eg muramyl dipeptides), natural RIG agonists or synthetic (for example, viral nucleic acids and in particular 3'-phosphate RNA).
[00156] When there is no incompatibility between the adjuvant and the bulk liquid solution of antigen (s) it can be added directly to the solution. The liquid bulk solution of antigen (s) and adjuvant can be, for example, a liquid bulk solution of an anatoxin adsorbed on aluminum salt (alum, aluminum phosphate, aluminum hydroxide) containing a stabilizer such as mannose, a oligosaccharides such as sucrose, lactose, trehalose, maltose, a sugar alcohol such as sorbitol. Mannitol or inositol, or a mixture thereof. Examples of such compositions are described in particular in WO 2009/109550, the subject of which is incorporated by reference.
[00157] Freeze-dried particles of the vaccine composition without adjuvant or with adjuvant are generally in the form of spherical particles having an average diameter between 200 μm and 1500 microns. Furthermore, since the process line according to the invention is designed for the production of particles under "closed conditions" and can be advantageously sterilized, the freeze-dried particles of the vaccine compositions obtained are sterile.
[00158] Although the present invention has been described in relation to its preferred embodiments, it should be understood that this description is for illustrative purposes only.
[00159] This application requires priority from patent application EP 11 008 057.9-1266, the subjects of the embodiments of which are listed below for reasons of integrity: 1. A process line for the production of freeze-dried particles under closed conditions, the process line comprising at least the following separate devices: - a spray chamber for droplet generation and freezing solidification of liquid droplets to form particles; and - a bulk freeze dryer 304 for freeze drying the particles; where a transfer section is provided for a transfer of product from the spray chamber to the freeze dryer, and for the production of the particles under closed point-to-point conditions each of the devices and the transfer section is adapted separately for closed operation. 2. The process line, according to item 1, in which the transfer section permanently interconnects the two devices to form an integrated process line for the production of particles under closed point-to-point conditions. 3. The process line, according to item 2, in which the transfer section comprises means to operatively separate the two connected devices from each other so that at least one of the two devices is operable under closed conditions separately from the another device without affecting the integrity of the process line. 4. The process line, according to any of the preceding items, at least one of the process devices and the transfer section comprises a containment wall which is adapted to provide predetermined process conditions within a confined process volume, wherein the containment wall is adapted to isolate the process volume and one environment from the process device from each other. 5. The process line, according to any of the preceding items, in which the process devices and / or the transfer section form an integrated process line to provide point-to-point protection of product sterility and / or point containment to the point of the product. 6. The process line, according to any of the preceding items, in which the freeze dryer is adapted for separate operation under closed conditions, the separate operation including at least one freeze drying of particles, cleaning of the freeze dryer and sterilization of the freeze dryer. 7. The process line, according to any of the preceding items, in which the integrated process line comprises, as another device, a handling device and product adapted for at least one of unloading the product from the process line, taking product samples, and handle the product under closed conditions. 8. The process line, according to any of the preceding items, in which the spray chamber (comprises at least one temperature-controlled wall to freeze liquid droplets. 9. The process line, according to any of the preceding items, in which the freeze dryer is a vacuum freeze dryer 10. The process line, according to any of the preceding items, in which the freeze dryer comprises a rotating drum for receiving the particles 11. A process line, according to any of the preceding items, in which at least one of one or more transfer sections of the process line comprises at least one temperature-controlled wall. according to any of the preceding items, in which the entire process line is adapted for Cleaning at the "CiP" Site and / or Sterilization at the "SiP" Site. 13. A process for the production of freeze-dried particles then under closed conditions carried out by a process line according to any of the preceding items, the process comprising at least the following process steps; - generate liquid droplets and freeze the liquid droplets to form particles in a spray chamber; - transfer the product under closed conditions from the spray chamber to a freeze dryer through a transfer section; and - freeze drying the particles as bulk articles in the freeze dryer; wherein for the production of the particles under closed conditions point to point each of the devices and the transfer section is operated separately under closed conditions. 14. The process, according to item 13, in which the product transfer to the freeze dryer is carried out in parallel to generate droplets and freeze solidification in the spray chamber. 15. The process, according to any one of the items 13 and 14, comprising a step of operationally separating the spray chamber and the freeze dryer to perform CiP and / or SiP in one of the separate devices.

权利要求:
Claims (17)
[0001]
1. Process line (300) for the production of freeze-dried particles under closed conditions, the process line (300) comprising at least the following separate devices: a spray chamber (302) for droplet generation and freezing of droplets liquid (323) to form particles; and a bulk freeze dryer (304) for freeze drying the particles, the freeze dryer (304) comprising a rotating drum (366) for receiving the particles; characterized by the fact that a transfer section (308; 500) is provided for transferring product from the spray chamber (302) to the freeze dryer (304), with the transfer section (308; 500 ) permanently interconnects the two devices (302; 304) to form an integrated process line (300) for the production of particles under closed conditions from end to end; and for the production of the particles under closed conditions from end to end each of the devices (302; 304) and the transfer section (308; 500) is separately adapted for the operation of preserving the sterility of the product to be freeze-dried and / or containment in order to provide a process line (300) flexibly adaptable to allow independent control of the operating mode of each respective device (302; 304).
[0002]
2. Process line (300) according to claim 1, characterized by the fact that the transfer section (308; 500) comprises means (336; 506; 508) for operationally separating the two connected devices (302; 304 ) from each other so that at least one of the two devices (302; 304) is operable under closed conditions separately from the other device without affecting the integrity of the process line (300).
[0003]
Process line (300) according to any one of the preceding claims, characterized by the fact that at least one of the process devices (302; 304) and the transfer section (308; 500) comprises a containment wall (320; 374; 376, 394) which is adapted to provide predetermined process conditions within a confined process volume, the confining wall (320; 374; 376; 394) being adapted to isolate the process volume ( 328; 370; 372) and a process device environment (302, 304) from each other.
[0004]
4. Process line (300) according to any one of the preceding claims, characterized by the fact that the process devices (302; 304) and the transfer section (308; 500) form a process line (300) integrated providing end-to-end sterility protection of the product and / or end-to-end containment of the product.
[0005]
Process line (300) according to any one of the preceding claims, characterized in that the freeze dryer (304) is adapted for separate operation under closed conditions, the separate operation including at least one particle drying by freezing, freeze dryer cleaning (304) and freeze dryer sterilization (304).
[0006]
Process line (300) according to any one of the preceding claims, characterized in that the integrated process line (300) comprises another device, a product handling device (306) adapted to at least one of , unload the product from the process line (300), take product samples and handle the product under closed conditions.
[0007]
Process line (300) according to any one of the preceding claims, characterized in that the spray chamber (302) comprises at least one temperature-controlled wall (404) to freeze liquid droplets ( 323).
[0008]
Process line (300) according to any one of the preceding claims, characterized by the fact that the freeze dryer (304) is a vacuum freeze dryer.
[0009]
Process line (300) according to any one of the preceding claims, characterized in that at least one of one or more transfer sections (308; 310; 500) of the process line (300) comprises at least a temperature-controlled wall.
[0010]
10. Process line (300), according to any of the preceding claims, characterized by the fact that the entire process line (300) is adapted for Cleaning at the "CiP" Site and / or Sterilization at the "SiP" Site.
[0011]
11. Process (700) for the production of freeze-dried particles under closed conditions carried out by a process line (300), as defined in any of the preceding claims, the process (700) characterized by the fact that it comprises at least the following process steps (704; 706; 712): generating (704) liquid droplets (323) and solidifying by freezing the liquid droplets (323) to form particles in a spray chamber (302); transferring (706) the product under closed conditions from the spray chamber (302) to a freeze dryer (304) through a transfer section (308; 500); and freeze drying (712) the particles as in bulk in the freeze dryer (304), the freeze dryer (304) comprising a rotating drum (366) for receiving the particles; and for the production of the particles under closed conditions from end to end, each of the devices (302; 304) and the transfer section (308; 500) is separately adapted for the sterility preservation operation of the product to be freeze-dried and / or containment in order to provide a process line (300) flexibly adaptable to allow independent control of the operating mode of each respective device (302; 304).
[0012]
12. Process (700), according to claim 11, characterized by the fact that the transfer of product (706, 736) to the freeze dryer (304) is carried out in parallel to generate droplets and freeze by freezing (704 ; 732) in the spray chamber (302).
[0013]
Process (700) according to either of claims 11 or 12, characterized in that it comprises a step of operatively separating (708) the spray chamber (302) and the freeze dryer (304) to carry out CiP and / or SiP (710; 734) in one of the separate devices (302; 304).
[0014]
14. Process for preparing a vaccine composition comprising one or more antigens in the form of freeze-dried particles, characterized by the fact that it comprises, freeze-drying a liquid bulk solution comprising said one or more antigens according to the process (700 ), as defined in any one of claims 11 to 13, and filling the freeze-dried particles obtained in a container.
[0015]
15. Process for preparing an adjuvant containing vaccine composition comprising one or more antigens in the form of freeze-dried particles characterized by the fact that it comprises: a. freeze drying a liquid bulk solution comprising said adjuvant and said one or more antigens according to process (700), as defined in any one of claims 11 to 13, and b. fill the freeze-dried particles obtained in a container; or, alternatively, when the liquid bulk solution of a) does not comprise said adjuvant, c. freeze drying a liquid volume of said adjuvant and a liquid bulk solution comprising said one or more antigens according to process (700), as defined in any one of claims 11 to 13, d. mixing the freeze-dried particles of said one or more antigens with the freeze-dried particles of adjuvant, e.g. fill the mixture of freeze-dried particles in a container.
[0016]
16. Process according to either of claims 14 or 15, characterized by the fact that all stages of the process are carried out under sterile conditions.
[0017]
17. Process according to any one of claims 14 to 16, characterized in that the freeze-dried particles are sterile.

类似技术:

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BR112014007862B1|2021-01-19|process line and process for producing freeze-dried particles under closed conditions, process for preparing a vaccine composition and process for preparing an adjuvant containing vaccine composition

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US10527350B2|2020-01-07|Process line for the production of freeze-dried particles

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法律状态:
2018-01-16| B07D| Technical examination (opinion) related to article 229 of industrial property law|

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2018-07-31| B07E| Notice of approval relating to section 229 industrial property law|

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2018-12-11| B06F| Objections, documents and/or translations needed after an examination request according art. 34 industrial property law|

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2020-06-16| B06U| Preliminary requirement: requests with searches performed by other patent offices: suspension of the patent application procedure|

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2020-12-08| B09A| Decision: intention to grant|

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2021-01-19| B16A| Patent or certificate of addition of invention granted|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 04/10/2012, OBSERVADAS AS CONDICOES LEGAIS. |

优先权:

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申请号 | 申请日 | 专利标题

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EP11008057.9A|EP2578974A1|2011-10-05|2011-10-05|Process line for the production of freeze-dried particles|

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EP11008057.9|2011-10-05|

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PCT/EP2012/004162|WO2013050156A1|2011-10-05|2012-10-04|Process line for the production of freeze-dried particles|

---