The present disclosure relates to apparatuses and methods for microwave vacuum-drying of organic materials, including biologically-active materials such as vaccines, antibiotics, proteins, and microorganism cultures.
Microwave vacuum-drying is a drying method that can be employed to dehydrate pharmaceutical biologic materials such as vaccines and antibodies. Microwave vacuum-drying, also called microwave vacuum dehydration, is a rapid drying method that can yield products with improved quality compared to air-dried and freeze-dried products. Because the drying is done under reduced pressure, the boiling point of water and the oxygen content of the atmosphere are lowered, so that components sensitive to oxidation and thermal degradation can be retained to a higher degree than by air-drying. The drying process is also much faster than air-drying and freeze-drying.
However, microwave vacuum-drying of pharmaceutical biologic materials at a large scale, while also complying with current Good Manufacturing Practice (cGMP) regulations, is difficult. Microwave vacuum-drying machines are currently made to address food safety concerns and are not designed to be used in a more stringently controlled GMP environment for drying pharmaceutical products. Using a microwave vacuum drying in cGMP conditions must be able to minimize particle generation during the drying process, allow drying to occur in a controlled and reproducible manner, as well as allow cleaning and sterilization of the drying chamber according to cGMP regulations.
In one aspect of the disclosure, a microwave vacuum dryer includes a loading chamber and a first vacuum pump in communication with the loading chamber, a first door separating the loading chamber from an external environment, a drying chamber adjacent the loading chamber, a second vacuum pump in communication with the drying chamber, and a condenser in communication with the drying chamber, a second door separating the loading chamber and the drying chamber, an unloading chamber adjacent the drying chamber and a third vacuum pump in communication with the unloading chamber, a third door separating the drying chamber from the unloading chamber, a fourth door separating the unloading chamber from the external environment, and a microwave chamber having a plurality of magnetrons, the microwave chamber positioned on a different plane from the loading and unloading chambers and adjacent the drying chamber.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the microwave chamber is positioned underneath the drying chamber.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the drying chamber has at least two walls and a floor that define two inner parallel edges, the two edges comprising removable tray guidance rails.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the loading chamber, the drying chamber and the unloading chamber are each aligned along a central axis.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the first door and the fourth door are manually operable.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the second door and the third door are automatically operable and allow for simultaneous movement of the second and third doors.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the plurality of magnetrons is arranged in an array along a length of the drying chamber between the second and third doors.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the array of magnetrons is arranged in banks.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the banks comprise six banks of magnetrons.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein each of the six banks of magnetrons includes three individual magnetrons.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein each of the plurality of magnetrons has a predetermined power setting based on a location along the length of the drying chamber.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the drying chamber comprises a plurality of ports for monitoring the drying of containers of frozen solution. In some embodiments, the plurality of ports comprise a thermal imaging or fiber optic probe.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein at least one of the unloading, drying and loading chambers comprises an outer gasket to act as a microwave seal when one of the doors to the chamber is closed, and an inner gasket adjacent the outer gasket, the inner gasket to provide a sterile boundary when one of the doors to the chamber is closed.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein each of the unloading, drying and loading chambers comprises an outer gasket to act as a microwave seal when one of the doors to the chamber is closed, and an inner gasket adjacent the outer gasket, the inner gasket to provide a sterile boundary when one of the doors to the chamber is closed.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, further comprising a tray unloader housed within the unloading chamber, and a tray loader housed within the loading chamber.
In another embodiment of the disclosure is a microwave vacuum dryer in accordance with the foregoing, wherein the unloading chamber comprises a closeable valve for partially backfilling the unloading chamber with an inert gas, and a stoppering mechanism to close partially-stoppered containers.
In another aspect of the disclosure a method of drying a product, including but not limited to a pharmaceutical product that reflects GMP requirements, comprises providing a microwave vacuum dryer having a loading chamber and a first vacuum pump in communication with the loading chamber, a first door separating the loading chamber from an external environment, a drying chamber adj acent the loading chamber, a second vacuum pump in communication with the drying chamber, and a condenser in vapor communication with the drying chamber, a second door separating the loading chamber and the drying chamber, an unloading chamber adj acent the drying chamber and a third vacuum pump in communication with the unloading chamber, a third door separating the drying chamber from the unloading chamber, a fourth door separating the unloading chamber from the external environment, a microwave chamber having a plurality of magnetrons, the microwave chamber positioned on a different plane from the loading and unloading chambers and adj acent the drying chamber, evacuating air from the drying chamber using the second vacuum pump, and activating at least one of the plurality of magnetrons to generate a microwave field within the drying chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the step of recirculating water adjacent to the drying chamber to remove excess microwaves from the drying chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the steps of opening the first door, loading a first tray holding one or more containers having frozen solution into the loading chamber, closing the first door, and evacuating air from the loading chamber to equilibrate the environment of the loading chamber with the environment of the drying chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the steps of opening the second door, advancing the first tray of containers into the drying chamber using a tray loader housed within the loading chamber, and closing the second door.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the steps of loading an additional tray into the loading chamber, closing the first door, and evacuating air from the loading chamber to equilibrate the environment of the loading chamber with the environment of the drying chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, wherein the additional tray holds one or more containers having frozen solution, or wherein the additional tray is empty.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the steps of pushing the additional tray into the drying chamber using a tray loader housed within the loading chamber, thereby pushing the first tray further into the drying chamber with the additional tray.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising repeating the step of loading additional trays into the loading chamber and pushing the tray ahead of it through the drying chamber, until the drying chamber is filled with trays.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, wherein the plurality of magnetrons is arranged in an array along a length of the drying chamber between the second and third doors, and wherein the magnetrons in different parts of the array are activated at different power levels before the first tray of containers is pushed into the drying chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, wherein the plurality of magnetrons is arranged in an array along a length of the drying chamber between the second and third doors, and wherein the plurality of magnetrons are activated to one or more predetermined power levels, and wherein the plurality of magnetrons is activated after the drying chamber is filled with trays.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the step of opening the third door, and advancing the first tray into the unloading chamber using a tray unloader housed within the unloading chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the step of advancing all of the trays from the drying chamber to the unloading chamber in a sequential manner.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the step of removing the first tray from the unloading chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, wherein the drying chamber has at least two walls and a floor that define two inner parallel edges, the two edges comprising removable tray guidance rails.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the steps of operating the microwave vacuum dryer in a semi-continuous mode by performing the following steps sequentially: (i) evacuating air from the drying chamber with the second vacuum pump, (ii) recirculating water in a water chamber above the drying chamber, (iii) generating the microwave field within the drying chamber, (iv) loading a first tray of containers having frozen solution into the loading chamber and closing the first door, (v) evacuating air from the loading chamber to equilibrate the environment of the loading chamber with the environment of the drying chamber, and (vi) drying the frozen solution in the containers of the first tray within the drying chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, further comprising the steps of operating the microwave vacuum dryer in a batch mode by performing the following steps sequentially: (i) evacuating air from the drying chamber with the second vacuum pump, (ii) loading a plurality of trays of containers containing frozen solution into the drying chamber via the loading chamber, (iii) recirculating water in a water chamber above the drying chamber, (iv) generating the microwave field within the drying chamber, and (v) drying the frozen solution in the containers within the drying chamber.
In another embodiment of the disclosure is a method of drying a product in accordance with the foregoing, wherein the unloading chamber comprises a closeable valve for partially backfilling the unloading chamber with an inert gas, and a stoppering mechanism to close partially-stoppered containers.
Various embodiments of the presently disclosed devices and methods are disclosed herein with reference to the drawings, wherein:
Various embodiments will now be described with reference to the appended drawings. It is to be appreciated that these drawings depict only some embodiments of the disclosure and are therefore not to be considered limiting of its scope.
Despite the various improvements that have been made to microwave vacuum drying, conventional devices and methods suffer from some shortcomings.
Therefore, there is a need for further improvements to the devices and methods used for microwave vacuum drying, and especially for devices and methods that allow for more efficient manufacturing and permit, for example, continuous or semi-continuous manufacturing of live virus vaccines. Among other advantages, the present disclosure may address one or more of these needs.
A number of vacuum pumps 146, best seen in
As best shown in
Each of the chambers may generally include stainless steel, or other metals, or suitable materials that are capable of blocking the passage of microwaves.
Turning back to
As noted, in certain examples, microwave chamber 116 is disposed below drying chamber 112 and microwaves are generated from the microwave chamber 116 below the drying chamber. The microwave may pass a travelling waveguide to get to the drying chamber. In these examples, the microwaves then pass through drying chamber 112 to a water circulation system 117 located above the drying chamber. Water circulation system 117 may include a microwave transparent tubing (e.g., plastic tube or pipe) in which cold water is recirculated. The tubing may be routed in a serpentine path parallel to the drying surface. This may prevent reflection of waves and standing waves, and allow for a single pass microwave. The floor and ceilings of the drying chamber may be formed of plastic or other microwave-transparent material to allow the passing of microwaves. At least one of the sides (e.g., sidewall, floor or ceiling) of the drying chamber may include a port for process monitoring. In at least some examples, this port is used for thermal imaging or fiber optic probes, which are desirable as they allow monitoring without breaking a sterile boundary. For example, ports 118 are located on the ceiling of drying chamber 112 (see
Microwave vacuum dryer 100 may further include a condenser 132 in communication with drying chamber 112 via a duct or tubing 133, the condenser being configured to receive sublimated vapor from the dehydrating product, and capturing it as ice on cold coils. Optionally, a removable microwave barrier 134 may be placed between the condenser and the drying chamber to prevent microwaves from getting into the condenser 132 (
In
In addition to a belt system, a ratcheting system or a smooth channel, a tray transport assembly may be used as best seen in
Optionally, drying chamber 112 may include a lid 150 configured to be opened or closed (
Optionally, loading chamber 110, drying chamber 112, unloading chamber 114, and condenser 132 can be configured for sterilization by Vaporized Hydrogen Peroxide (VHP) using an external VHP generator system. Generally, VHP may use vaporized hydrogen peroxide as a broad spectrum anti-microbial and has efficacy against bacteria, yeast, viruses and bacterial spores thereby decontaminating the systems against the biological agent. The dryer may be configurable by the operator so that the optimal sterilization cycle can be achieved via circulation of VHP. VHP ports can be used either as inlets or outlets and may be located on the loading chamber 110, unloading chamber 114, and/or condenser 132. The system can be configured so that there is a single inlet and a single outlet, or multiple inlets and/or outlets (e.g., two inlets and one outlet, or two outlets and one inlet). The internal surfaces of the vacuum dryer 100 may be fabricated from materials that are not reactive with VHP, such as stainless steel, aluminum, acrylonitrile butadiene styrene (ABS), or polyvinyl chloride (PVC). In at least some examples, tray pusher 142, tray puller 144, second door 122, and/or third door 123 are cycled during VHP to ensure sterilization of their surfaces as well.
In use, vacuum dryer 100 may operate in one of two modes: a semi-continuous mode or a batch mode. Each of these modes will be now be described in greater detail. It will be understood that the same microwave vacuum dryer may be operated in either mode, and that the mode may be chosen by connecting the vacuum dryer to a computer, laptop, tablet or phone via either a wired or wireless connection, or through a built-in computer having a memory, a processor and an interface. In at least some examples, vacuum dryer 100 may have a controller “C” having a processor and a memory, the controller being capable of monitoring, adjusting or regulating the vacuum pumps 146, the magnetrons 130, the chiller 139, the condensers 132 and/or the water circulation system 117 (
In semi-continuous mode, a vacuum pump evacuates condenser 132 and drying chamber 112 while doors 122, 123 remain closed. Chiller 139 is enabled to cool the condenser 132 to a desired temperature. Optionally, chiller 139 is also used to cool a cooling table or plate disposed on the floor of loading chamber 110. The cooling plate may ensure that the frozen product does not exceed its glass transition temperature (Tg). The glass transition temperature is the temperature at which an amorphous material transitions from a rigid glass to a viscous solid. By keeping the product below its glass transition temperature during the loading process, the product is protected from damage and the bulk material is protected from collapsing. Vaccines and biologics formulations may have a glass transition temperature in a range of -28 to -41° C. and thus it is desirable to keep them frozen below their respective glass transition temperature prior to starting the drying process.
Once a target vacuum in drying chamber 112 and a target temperature in condenser 132 is reached, magnetrons 130 in microwave chamber 116 are turned on to generate a microwave field. Water is recirculated through water circulation system 117 to remove excess microwaves from the drying chamber. Frozen product disposed in containers (e.g., vials, beads, dual chamber cartridges, bulk cake in a bottle or tray, etc.) may be placed on a tray and loaded manually into loading chamber 110. The frozen product itself may include any one or more of a live virus vaccine, enveloped and non-enveloped virus, adjuvants, subunit vaccine, protein, peptide, antibody-drug conjugate (ADC), bispecific, fusion protein and/or small molecule drug. Door 121 is then closed and a second vacuum pump evacuates the loading chamber 110. If enabled, the cooling table in the loading chamber 110 is used to keep the product frozen during evacuation.
Once loading chamber 110 has equilibrated with drying chamber 112, second door 122 is automatically (or manually) opened and a tray pushing mechanism pushes the tray of products into drying chamber 112. Optionally, position sensors may be incorporated into the drying chamber or loading chamber to monitor the position of the tray. The tray pusher 142 may then retract and optionally provide subsequent pushes to completely load the tray into the drying chamber. After the final push, the tray pusher 142 may then retract and second door 122 may close. The drying process in drying chamber 112 may then begin for the first tray. At any point, the operator can load a second tray into loading chamber 110. Specifically, vacuum is released in loading chamber 110 and the first door 121 is opened. Next, the operator may load a tray having frozen product as described above. First door 121 may then be closed, and loading chamber 110 may be evacuated and held within the loading chamber 110 for a calculated amount of time. In some examples, the calculated time is determined by the desired overall drying time divided by the number of positions in drying chamber 112. Once the calculated time has elapsed, this second tray is pushed into drying chamber 112 as described above. When the second tray moves into drying chamber 112, the second tray will contact and push the abutting first tray further down the line within drying chamber 112. In this manner, each tray being pushed by tray pusher 142 is used to advance trays within the drying chamber 112 without generating particulates.
This process may repeat at timed intervals until all drying positions in drying chamber 112 are filled. Throughout this process, trays of product are dehydrated and their water vapor collected at condenser 132. At any point in time, each tray is at a different point in its dehydration profile. Therefore, magnetrons 130 may be programmed, configured and arranged to be activated at different power settings based on their locations within the drying chamber 112 and/or the heat required for that portion of the dehydration cycle.
At the second end 104 of vacuum dryer 100, trays are unloaded in the same sequence that they were loaded. Once the first tray has spent the appropriate amount of time in the final drying location in drying chamber 112, the unloading process starts. Vacuum is pulled in unloading chamber 114 by a third pump. When unloading chamber 114 is equilibrated to drying chamber 112, third door 123 is automatically opened. A tray puller 144 reaches into drying chamber 112 and retrieves the tray into unloading chamber 114. Optionally, the tray puller 144 may perform multiple reach/retraction steps to incrementally unload the tray. After full retraction, the third door 123 may then be closed. For partially stoppered vials, an optional gaseous backfill can be performed to provide partial vacuum in the vials. The gas may be selected from selected from nitrogen, argon or a suitable gas, and the backfilling may be conducted at a pressure of between 200 Torr-750 Torr, between 450-700 Torr, or at or about 540 Torr. A stoppering plate compresses the vials to seat the vials. The stoppering plate may be driven by a hydraulic, pneumatic, or electrical motor in the external environment that couples to the stoppering plate via a bellowed shaft to maintain sterility of the unloading chamber 114. The stoppering plate may be configured to perform multiple compressions at programmable forces and dwell times. After this, the vacuum is released and the operator manually unloads the tray from fourth door 124.
When trays are removed from unloading chamber 114, fourth door 124 is closed and vacuum is pulled in unloading chamber 114 again. The unloading process repeats as described above until the final tray is removed. Because tray movement through drying chamber 112 is dependent upon new trays being introduced through loading chamber 110, “dummy trays” that contain no product, but are of similar weight as the product tray, must be loaded until the final product tray is unloaded. Alternatively, weights equal to loaded vials may be added to the “dummy trays”.
A similar method may be used in batch mode, with certain differences. After drying chamber 112 is evacuated, but before the magnetrons 130 are turned on, the product trays may be loaded into loading chamber 110. Trays are loaded using the same loading process as above, but there is no hold time between tray loading events. Once drying chamber 112 is loaded using tray pusher 142, the magnetrons 130 are turned on. Instead of having different power settings by location within the drying chamber 112, magnetron 130 power is varied by time. After a sufficient drying time (e.g., between 3 and 24 hours, the magnetrons 130 are turned off. Trays are then unloaded as described previously, one tray immediately after the other from the unloading chamber 114.
It is to be understood that the embodiments described herein are merely illustrative of the principles and applications of the present disclosure. Moreover, certain components are optional, and the disclosure contemplates various configurations and combinations of the elements disclosed herein. It is therefore to be understood that numerous modifications may be made to the illustrative embodiments and that other arrangements may be devised without departing from the spirit and scope of the present disclosure as defined by the appended claims.
It will be appreciated that the various dependent claims and the features set forth therein can be combined in different ways than presented in the initial claims. It will also be appreciated that the features described in connection with individual embodiments may be shared with others of the described embodiments.
Filing Document | Filing Date | Country | Kind |
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PCT/US2021/035085 | 6/1/2021 | WO |
Number | Date | Country | |
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63035495 | Jun 2020 | US |