Patent Application
20250129984
The present invention relates to a system suitable for controlling the freeze-drying process in a freeze dryer with a plate stack system, and it also relates to a method suitable for generating a design space and a method for monitoring and controlling the freeze-drying process comprising the use of said system, such that they can be used in the commercial manufacture of a pharmaceutical, cosmetic or food product.
An important step towards manufacturing many pharmaceutical products for injectable or parenteral use is freeze-drying. Freeze-drying is also a key technology for the GMP regulated sector.
Freeze-drying is a physical-chemical process in which water is removed from a product to promote its stability. This technique is used especially for injectable products or drugs which can be highly unstable in aqueous solutions and must be stored in freezers at low temperatures. In the freeze-drying process, for example, a vial or ampoule prefilled with the pharmaceutical product is placed inside a special freeze-drying chamber. First, the product is frozen by lowering the temperature inside the chamber. Subsequently, sublimation of the solvent (usually water) in the previously frozen product is carried out in an atmosphere with a very low solvent vapour pressure. By removing moisture and much of the solvent from the product in this manner, the product is more stable and its useful life can be extended.
Freeze-drying makes it possible to keep these products cold and at room temperature, significantly favouring the logistics of the storage, transport and distribution thereof.
Various methods and systems have been developed to control and monitor freeze-drying cycles, conditions of the process, and the quality of products obtained through freeze-drying.
For example, early designs such as those described in U.S. Pat. No. 3,176,408 describe a freeze-drying apparatus and method for items of the same size and type wherein said items were located in a sealed chamber, a shelf, and a tray prepared to support frozen items to be freeze-dried, means for freeze-drying the items deposited on the tray and means for responding directly to the loss of weight of the items due to sublimation, wherein the apparatus comprises at least two load cells, located under the shelves (see
Later, patent document CN206670234 disclosed a freeze dryer for carrying out a freeze-drying process, which comprised a chamber with three fixed shelves where vials to be freeze-dried were deposited. Said shelves included a resistance strain gauge weighing sensor and a sensor mounting bracket fixedly connected to the centre of each shelf. The bottom of one end of the strain gauge weighing sensor is fixedly connected to the sensor mounting bracket by a mounting bolt. The bottom of the other end of the resistance strain gauge weighing sensor is provided with an adjusting bolt to adjust the height position of the resistance strain gauge load cell; the side of the strain gauge load cell is provided with a sensor output terminal, the sensor. The gauge system was used to determine the amount of material resulting from the process by measuring the variation in weight over time. Said apparatus comprised one strain gauge for each shelf.
Said strain gauges were connected to a control device (which could be a PLC) that collected the weight measurements of the gauges and displayed them on a screen. Subsequently, an operator could determine the optimal freeze-drying time based on the weight variations displayed on the screen.
The operator can determine the end of the experiment when directly observing that the value shown on the display screen no longer changes, in addition to observing whether the indicator light 11 lights up. Moreover, the apparatus comprises a timer 12 configured to record the measured weight value of the strain gauge load cell once every 30 minutes until the measured values, for two consecutive times, are stable and the ice in the material is completely sublimated. The light 11 receives the signal from the electronic control unit 13 to light up, which leads the operator to finish the process. This system has the drawback that it limits the control and completion of the process to a manual process carried out by an operator.
The latest publications, such as US2020340743 A, described a non-invasive system and method to monitor and control a freeze-drying process using a network of wireless gas temperature and ambient pressure sensors; in particular, the method makes it possible to determine the sublimation rate of solvent from the vials deposited inside of using an arbitrary mathematical model during the freeze-drying process in real time.
More specifically, US2020340743 A described a system comprising:
A control unit adapted to collect pressure and gas temperature data from one or more wireless pressure sensors and calculate the sublimation rate in a product to be freeze-dried using the pressure temperature and gas data collected.
The control unit of the system calculates the sublimation rate in the follow manner: by applying a predetermined initial limit condition on a channel representing the space adjacent to the tray of the freeze-drying vial inside the freeze-drying chamber, it iteratively minimises a penalty function associated with the difference between the calculated spatial pressure information and that which is collected, which includes: calculating information on the spatial temperature and gas feed at distributed locations of one or more wireless pressures and as temperature sensors, calculating the difference between the calculated spatial pressure information and that which is collected; moreover, it calculates the penalty function for the associated intermediate reference between the collected and calculated spatial pressure information and the associated limit condition, determines a new limit condition that causes the calculated penalty function to be reduced, and calculates the sublimation rate by applying in g the associated limit condition with the penalty function.
Therefore, there is a need to design systems and methods for monitoring the different freeze-drying processes for different industries, which can be applied to different freeze-drying containers and which can also create a design space adjusted to the real conditions of the freeze-drying processes, in addition to being used as a reference or model for predicting future values of the conditions in a container suitable for freeze-drying, for example a vial, during the freeze-drying process.
Likewise, it is also necessary to develop systems and methods that facilitate the identification of the optimal conditions for a routine freeze-drying process, both on a large scale and in small manufactures, or the limits based on which the process can fail in said manufacturing process.
The system of the first aspect of the present invention is applicable, for example, to the freeze-drying process of injectable products that makes it possible to monitor the parameters that directly compromise the quality of the freeze-dried product, thus being integrated into the quality control of the product by controlling the process according to the “Quality by Design” concept. Likewise, it is also applicable to freeze-dried products for use in food, since they enable the flavour of said products to be preserved over time.
The system of the first aspect of the present invention has the advantages that makes it possible to directly obtain the weight of the plate stack (2) and of the heatable plates, to subsequently calculate the flow of water vapour that is sublimated in the freeze dryer through the use of load cells. Moreover, it makes it possible to obtain critical process parameters to help manufacturers obtain “Design Space” based on “Quality by Design” in a simple and robust way.
Additionally, the system makes it easier to monitor the different freeze-drying processes for different industries, which can be applied to different freeze-drying containers and which can also create a design space adjusted to the real conditions of the freeze-drying processes, in addition to being used as a reference or model for predicting future values of the conditions in a container suitable for freeze-drying, for example a vial, during the freeze-drying process, as well as identifying the optimal conditions for a routine freeze-drying process, both on a large scale and in small manufactures, the limits based on which the process can fail and the limits or ranges to perform validations of said manufacturing process.
Therefore, the system of the first aspect is a system suitable for controlling the freeze-drying process in a freeze dryer (1) with a hanging plate stack system (2) comprising at least one heatable plate (3), wherein the plate stack (2) hangs either from another heatable plate (3) or from an upper pressing plate (4), wherein each heatable plate (3) of the plate stack (2) is coupled to each other or to the upper pressing plate (4) by mechanical connection means (5); wherein said system comprises:
The second aspect of the invention relates to a freeze dryer (1) comprising:
The third aspect of the invention relates to a method suitable for generating a design space for
The fourth aspect of the invention relates to a method for monitoring and controlling a sample comprising receptacles suitable for freeze-drying which contain a product, routinely during a freeze-drying process inside a freeze-drying chamber (2) of a freeze dryer (1) which comprises the system according to claims 1-22, preferably the freeze dryer (1) according to any of claims 23 and 24, wherein said method comprises at least the following steps:
The foregoing and other advantages and features will be more fully understood from the following detailed description of exemplary embodiments referring to the attached drawings, which should be considered by way of illustration and not limitation, wherein:
The system of the first aspect is a system suitable for controlling the freeze-drying process in a freeze dryer (1) with a hanging plate stack system (2) comprising at least one heatable plate (3), wherein the plate stack (2) hangs either from another heatable plate (3) or from an upper pressing plate (4), wherein each heatable plate (3) of the plate stack (2) is coupled to each other or to the upper pressing plate (4) by mechanical connection means (5); wherein said system comprises:
The system of the first aspect has the advantage that it can be installed and used in large commercial freeze dryers as well as in small laboratory freeze dryers. This has the advantage that it can be installed without affecting the proper functioning of the freeze dryer.
Therefore, in all aspects of the present invention the load cells of the present invention are adapted to be able to work under vacuum conditions, and the most important challenge to overcome is doing so in a very low temperature environment.
In a more preferred embodiment, the system of the first aspect is suitable for freeze dryers comprising movable heatable plates (3).
In another preferred embodiment of the system of the first aspect, the freeze dryer is a freeze dryer with a top piston system.
In another more preferred embodiment, the system of the first aspect is suitable for freeze dryers comprising at least one freeze-drying chamber (14), an upper pressing plate (4), hanging heatable plates (3) suitable for depositing receptacles suitable for freeze-drying, a hydraulic piston, heating means (15), and means for modifying and controlling chamber pressure.
In the context of the present invention, the term sample comprises a receptacle suitable for freeze-drying which contains a product suitable for undergoing a freeze-drying process. Preferably, said product comprises a solvent, a cosmetically or pharmaceutically acceptable active ingredient, or a product suitable for food use. In another preferred embodiment, the receptacle suitable for freeze-drying the sample of any of the aspects of the invention is selected from the list consisting of vials, ampoules, syringes, cartridges, bulk trays, microtubes and flasks.
In the context of the present invention, the term standard sample refers to a sample that can be used as a reference or for calibrating samples for subsequent industrial manufacturing.
Normally, the hydraulic piston offers the possibility of raising and lowering all the heatable plates (3) making up the plate stack (2). When the freeze-dried samples are products deposited in vials, said vials are closed inside the chamber. This is carried out by the hydraulic piston which, when the plates are lowered, presses the upper plate on the caps of each of the vials until they close.
Freeze dryers with a hydraulic piston are frequently used in the pharmaceutical, cosmetic and food industries, for which reason the system of the first aspect is a highly versatile system that can be used in most commercial freeze dryers. Preferably with top piston freeze dryers.
In general, the freeze-drying chamber is the space where the sample that undergoes the freeze-drying process is placed. The sample is located on the heatable plates (3). The set of heatable plates together with the upper pressing plate is called plate stack (2). The plate stack (2) comprises at least one heatable plate (3) hanging from another heatable plate (3) or from an upper pressing plate (4) by mechanical connection means (5). The plate stack (2) can have other hanging heatable plates (3) that in turn hang from the hanging plate (3) immediately above it by mechanical connection means (5).
In general, a freeze dryer (1) further comprises a condenser which can be, for example, a coil that collects all the water vapour that sublimates from the sample deposited in the freeze-drying chamber (14).
In a preferred embodiment, the system of the first aspect comprises at least two strain gauges (9), more preferably, at least four strain gauges (9).
In the context of the present invention, each strain gauge (9) is configured to be coupled to a mechanical connection means (5); said mechanical connection means (5) have the feature that it adapts to the shape of the heatable plates (3) of the freeze dryer. In a preferred embodiment of the system of the first aspect, the at least one strain gauge (9) is configured to be coupled to the upper portion of the mechanical connection means (5) and on the upper portion of the heatable plates (3) or the pressing plate (2), thereby obtaining more precise and reproducible measurements. In another more preferred embodiment of the system of the first aspect, the at least strain gauge (3) is configured to be coupled to the upper portion of the mechanical connection means (5) directly or indirectly through a tool (20).
In the context of the present invention, the tool (20) or compression force transmission structure is located at the junction point between the load cells and the point where this force is produced.
In general, the mechanical connection means (5) are metal elements adapted to connect and support at least the weight of the lower or immediately lower heatable plates (3). The mechanical connection means (5) are configured to support the weight of the immediately lower heatable plates (3), forming a plate stack (2). The mechanical connection means (5) are configured to pass through the heatable plates (3) or the upper pressing plate (4) in such a way that the ends of said means are located above the heatable plate (3) or the upper pressing plate (4), as applicable.
In a particular embodiment, the mechanical connection means (5) are selected from the list consisting of cylindrical rods, preferably selected from hollow or solid cylindrical rods, metal shafts and metal guides. More preferably, the mechanical connection means (5) comprise metals selected from the list consisting of steel and stainless steel.
In a preferred embodiment of the system of the invention, the control unit (10) is external to the freeze dryer and the processor (11) is selected from a CPU or a PLC unit. Preferably, the control unit (10) comprises a processor (11), a network interface, a display device (12) selected from a monitor or screen, a user input device, and a memory unit.
The control unit (10) can be a server, a desktop computer, a laptop computer, a tablet, or any other suitable type of computing device(s).
In another preferred embodiment of the system of the invention, the system can have two control units (10), a control unit external to the freeze dryer (10EA) and another control unit connected to the freeze dryer (10EB), both in data connection with the pressure sensor (6), with the plate temperature sensor(s) (7), with the product temperature sensor(s) (8) and with the at least strain gauge (9), and wherein the external control unit (10EA) is in data connection with the control unit of the freeze dryer (10EB) through the processor (11).
In a preferred embodiment of the system of the invention, the at least strain gauge (9) is configured to measure the weight of the heatable plates (3) and the control unit (10) is configured to calculate the variation in weight of the heatable plates (3) of the freeze dryer. In the system of the invention, each strain gauge (9) is configured to measure the weight of the heatable plates (3) of the freeze dryer. The variation in weight of the heatable plates (3) of the freeze dryer is obtained by the control unit (10) and is used to calculate the mass flux that occurs in the receptacles suitable for freeze-drying during the freeze-drying process, in other words, the mass flux of vapour of the solvent that sublimates from the frozen product.
In a preferred embodiment of the system of the invention, the system further comprises at least one junction box (16) configured to unify the input signal of each strain gauge (9) into a single output signal towards the control unit (10). Preferably, the junction box (16) is an analogue junction box or a digital junction box and/or is located external to the freeze dryer (1). In this way, the signal from each strain gauge load cell is unified and helps to obtain more reliable and reproducible measurement values of the weight of the heatable plates (3) and the weight of the plate stack (2). It also makes system installation easier and helps reduce the risk of equipment damage.
In a more preferred embodiment of the system of the first aspect, the junction box (13) is an analogue junction box or a digital junction box.
In the context of the present invention, the term analogue junction box is understood as a junction box configured to convert the analogue signal of load cells to a digital signal and unify the resulting digital signals into a single output signal.
In the context of the present invention, the term digital junction box is understood as a junction box which is configured to unify the digital input signals of load cells into a single output signal.
In the context of the present invention, the term mass flux or mass flux rate is the mass of substance (solvent or any volatile substance) which sublimates from the frozen product in the freeze-drying container per unit of time which passes through a given surface per unit of time. The unit thereof is mass divided by time; therefore, kilogram/second in SI units.
In the context of the present invention, pressure sensors (6), suitable for detecting an absolute pressure in the freeze-drying chamber. Preferably, the pressure sensors are adapted to withstand temperatures of up to 121° C., to thereby withstand the conditions of periodic sterilization processes.
In a preferred embodiment of the system of the first aspect, the pressure sensor (6) is a capacitive sensor or a Pirani-type sensor. Preferably, the pressure sensor (6) is configured to be located inside the freeze-drying chamber (14) and connected to the control unit (10) by the electronic means (13A).
In a preferred embodiment of the system of the first aspect, the temperature sensors (7) and (8) are selected from the list consisting of thermocouples, Tempris®-type sensors and PT100-type sensors and thermocouples.
Preferably, the pressure and temperature sensors (7) and (8) are adapted to withstand temperatures in a range between-60 to 130° C. and/or be configured to measure pressures between 0.001 and 1 mbar, to thereby withstand the conditions of periodic sterilization processes.
In a preferred embodiment of the system of the invention, said system comprises at least one temperature sensor (8) in a receptacle suitable for freeze-drying. Preferably, the system comprises at least one product temperature sensor (8) located in at least one receptacle suitable for freeze-drying, preferably located inside the receptacle and/or in contact with the product.
In another preferred embodiment of the system of the invention, said system comprises at least one product temperature sensor (8) in at least one receptacle suitable for freeze-drying for each heatable plate (3); in this way, the product temperature measurements are more precise, making it possible to generate a design space better adjusted to the real conditions of the freeze-drying process. More preferably, the product temperature sensors (8) are wireless.
In a preferred embodiment of the system of the invention, the heating means (15) are thermal fluid heating means and the temperature sensor (7) is configured to be located on said heating means (15), for example, coupled with a flange.
In a more preferred embodiment of the system of the first aspect, the system comprises at least one temperature sensor (7) per system, located on the heating means (15) before the entry of said heating means into the heatable plates (3). The temperature of the heating means corresponds to the temperature of the heatable plates (3).
The plate temperature sensor (7) can be located on the thermal fluid heating means (15) or located inside a groove comprised on the thermal fluid heating means (15).
The thermal fluid heating means (15) can be, for example, a collector; therefore, the plate temperature sensor (7) is preferably located at the fluid inlet of said collector. The temperature at the collector inlet corresponds to the temperature of the heatable plates (3).
In another preferred embodiment of the system of the invention, the temperature sensor (7) is configured to be located on the heatable plates (3), more preferably inside the heatable plates (3), thereby obtaining more reliable and precise temperature measurements.
In a more preferred embodiment, the system of the first aspect comprises at least one temperature sensor (7) located on the heating means (15) before the entry of said heating means into the heatable plates (3) and one temperature sensor (7) located on at least one heatable plate (3), preferably inside the heatable plate (3), more preferably on the heating means that run inside the heatable plates (3).
Preferably, the system of the first aspect comprises at least one temperature sensor (7) located in a receptacle suitable for freeze-drying located on one heatable plate (3) for each heatable plate (3) comprising the freeze dryer.
In a more preferred embodiment of the system of the first aspect, the temperature sensors (7) and (8) are wireless and the electronic means (13B and 13C) are wireless. In this way installation is made easier, said installation also being faster and safer since the risk of the electronic means (13B and 13C) being damaged when they are in the form of wires, due to the movement of the plates, is reduced. In another more preferred embodiment of the system of the first aspect, temperature sensors (8) have an externa! memory for storing data (17), an external battery (18) and an external antenna (19) configured to communicate the data to the control unit (10); the antenna (19) is preferably configured to emit a radio signal. The external memory (17) and external antenna (19) can be located on
In a preferred embodiment of the system of the first aspect, the electronic means (13A, 13B,13C, 13D) are wireless or digital and are configured to be sterilizable, for example protected with coatings resistant to high temperatures of up to 121° C. and water vapour, to thus withstand the conditions of the periodic sterilization processes.
The second aspect of the invention relates to a freeze dryer (1) comprising:
In a preferred embodiment, the freeze dryer (1) of the second aspect is a freeze dryer with a top piston system.
The third aspect of the invention relates to a method suitable for generating a design space for a sample, comprising receptacles suitable for freeze-drying which contain a product, during a freeze-drying process inside a freeze-drying chamber of a freeze dryer (1) which comprises the system according to claims 1-22, preferably the freeze dryer (1) according to any of claims 23 and 24, wherein said method comprises:
In a preferred embodiment of the method of the third aspect, the graphs of the work map represent at least two and/or three of the measurements collected by a control unit (10) and the parameters obtained through said measurements by the control unit (10).
The term work map comprises, for example, the representation of the measurements collected or of the parameters obtained by the control unit (10) in graphs wherein at least one of said measurements or said parameters, or at least two of said measurements and/or said parameters, or at least three of said measurements and/or said parameters obtained by the control unit (10) are represented.
In the context of the present invention, the term design space is understood as the delimitation of the range for each parameter of a freeze-drying process within which it is ensured that the product obtained has the required quality attributes. An example of a productor sample design space can be seen in
The temperature of the heatable plates (3), the chamber pressure and the weight of said heatable plates (3) are measured at a number of time intervals (for example, at regular time intervals such as every minute, etc.). The values measured at each time interval are applied to a mechanistic combined heat and mass transfer balance model to infer/calculate the conditions in the receptacle suitable for freeze-drying at those time intervals, in addition to calculating the heat transfer coefficient received by the product to be freeze-dried and the resistance constant of the dry product to the passage of vapours, applying these calculated constants to a heat and mass transfer balance model, to represent a 2D or 3D map or graph. This representation is also called design space.
The process conditions or parameters of the sample or of the product in the receptacle suitable for freeze-drying are calculated based on the temperature of the heatable plates (3) and of the product, the pressure, and the weight of the heatable plates (3), measured by sensors/probes inside or outside the freeze-drying chamber.
In another more preferred embodiment of the method of the third aspect and fourth aspect (if necessary) of the invention, the measurement of the variation in weight of the sample in step ii) is carried out by the control unit (10) and gives the value of the vapour mass flux, and wherein the measurement of the variation in weight of the sample in step ii) is determined in response to the variation in weight measured by the strain gauge(s) (9) of the heatable plates (3) comprising the samples and based on the number of samples located on each heatable plate (3).
In another more preferred embodiment of the method of the third and fourth aspects of the invention, the number of samples located on each heatable plate (3) has been previously defined and entered in the control unit (10) or has been obtained by the control unit (10) externally through a server or is manually entered in the control unit (10) by a user.
In another more preferred embodiment of the method of the third and fourth aspects of the invention, the work map of the design space is carried out by the control unit (10) establishing a relationship between the chamber pressure and/or the product temperature and/or the mass flux in the form of a 2D or 3D graph.
Therefore, the creation of the design space of the method of the third aspect has the advantage that it can be used as a reference or model for predicting future values of the conditions in a container suitable for freeze-drying, for example in a vial, during a suitable period of time (e.g., the next hour, the next two hours, etc.), for example to be able to be used in the method of the fourth aspect of the invention.
The construction of said design space in 3D or 2D according to the method of the third aspect also has advantages that make it easier to identify the optimal conditions for a routine freeze-drying process, both on a large scale and in small manufactures, the limits based on which the process can fail and the limits or ranges to perform validations of said manufacturing process.
Moreover, it makes it possible to calculate or estimate the limits of the process control for a configuration of a specific freeze-drying receptacle, equipment, and manufacturing environment. Likewise, the method of the third aspect can be used to predict the effect of variations on process conditions, on the process yield, the time to complete it, and product quality, or to understand the deviations that might occur during manufacturing.
In a preferred embodiment of the method of the third aspect and fourth aspect of the invention, the freeze-drying process of step ii) comprises at least the steps of:
In a preferred embodiment of the method of the third aspect and fourth aspect of the invention, the freeze-drying process of step ii) comprises at least the steps of:
In freeze-drying processes, primary drying removes water by sublimation of ice from the product under vacuum conditions (the product having previously been frozen). By supplying heat, the ice sublimates and passage through the liquid phase is avoided. During primary drying, the water vapour generated in the sublimation interface is eliminated through the pores of the product structure.
Primary drying takes place from the freezing temperature to a temperature range typically between 2° and 40° C.
After the sublimation process is complete, secondary drying is performed to remove any or most of the remaining liquid or moisture. This drying is performed by desorption, evaporating, for example, the non-freezable water found in the previously dried material. In this way, final product moisture results close to and even below 2% can be obtained.
Secondary drying takes place from the temperature at which primary drying is completed to a temperature range between 20 and 70° C. Therefore, when the ice disappears, the free water begins to be eliminated by evaporation, leading to secondary drying.
In another preferred embodiment of the method of the third aspect of the invention, the control unit (10) is configured to establish the relationship between the chamber pressure, the mass flux and the product temperature, and wherein said relationship is represented by the control unit (10) in a 3D or 2D work map. This relationship can be established by applying a mass balance and energy balance during the sublimation process of primary drying. This relationship can be carried out for each different product temperature.
Therefore, in another preferred embodiment, the control unit (10) is configured to establish the relationship between the chamber pressure, the mass flux and the product temperature in a 2D work map at different product temperatures (different product isotherms) during the freeze-drying process.
In another preferred embodiment, the control unit (1O) is configured to establish the relationship between the chamber pressure, the mass flux and the plate temperature in a 2D work map at different plate temperatures during the freeze-drying process.
In another preferred embodiment, the control unit (10) is configured to establish the relationship between the chamber pressure, the mass flux, the different product temperatures (product isotherms) and the different plate temperatures (plate temperature isotherms) in a 2D work map at different plate temperatures during the freeze-drying process.
The heat transfer coefficient between the plate and the product and the resistance coefficient of the dry product to be freeze-dried to the vapour flow are used to establish the relationship between the chamber pressure and the mass flux, for each temperature of each of the heatable plates (3). Said parameters are obtained experimentally and fed to the control unit (10).
To calculate the heat transfer coefficient between the freeze dryer and the product to be freeze-dried (Kv), the following steps are carried out:
In this way, a 2D work map can be obtained wherein the different values of Kv are represented compared to the different pressures.
To calculate the resistance coefficient of the dry product to be freeze-dried to the vapour flux (Rp) the following steps are carried out:
In this way, a 2D work map (graph) can be obtained wherein the different values of Rp can be represented compared to different chamber pressures.
Once the values of Kv and Rp are characterised, the different points that will configure the plate temperature and product temperature isotherms can be calculated for the different values of the plate temperature, Ts. For example, using each value of Tb and dm/dt to represent the different plate temperature isotherms.
In a preferred embodiment, to establish the relationship between the chamber pressure, the mass flux and the product temperature, (product temperature isotherms), as seen in
In a preferred embodiment of the method of the third aspect of the invention, the method comprises an additional step once the design space has been established; this additional step comprises establishing the limits of the design space.
In another preferred embodiment of the method of the third aspect, it comprises an additional step vii) where the limits of the design space are established, which comprises establishing the maximum limits of the evaporation mass flux rate (Choke Flow or Choke Point) allowed by the freeze-drying equipment based on the pressure measured by the pressure sensors (6) and the critical product temperature. In another more preferred embodiment, the control unit (1O) is configured to establish the Choke Flow
In the context of the present invention, the process for establishing the maximum limits of the evaporation mass flux rate allowed by the freeze-drying equipment based on the pressure of
the freeze-drying chamber is called the Choke Point or Choke Flow. An example of a design space representing the established Choke Flow is shown in
In a preferred embodiment of the method of the invention, the Choke Point or Choke Flow) the following steps are carried out:
The critical temperature of the product is a parameter used to establish said limits. Preferably, the critical temperature is determined at least by a method selected from the list consisting of DSC, TGA and FDM. Specifically, the critical temperature is a relevant parameter for designing the primary drying phase of a freeze-drying cycle.
To determine the critical temperature of the product, the maximum product temperature allowed during primary drying is determined; this temperature can be the collapse temperature in the case of an amorphous product or the melting temperature in the case of a crystalline product. The critical temperature is necessary to establish the maximum temperature allowed for the product in primary drying. The critical temperature of primary drying is a parameter that is fed to the control unit (1O) to carry out step vi). In a preferred embodiment of the method of the third aspect of the invention, the control unit (1O) is configured to establish the relationship between the chamber pressure and the mass flux, for the temperature of the heatable plates (3), for example by using the average values obtained by the control unit (10) in the event that more than one temperature sensor of plates (3) present in the freeze dryer is used and wherein said relationship is represented by the control unit (1O) in a 20 work map at the different temperatures of the heatable plates (3) during the freeze-drying process.
The fourth aspect of the invention relates to a suitable freeze-drying method that contains a product, routinely during a freeze-drying process inside a freeze-drying chamber (2) of a freeze-dryer (1), which comprises the system according to the first aspect, preferably the freeze dryer (1) according to any of claims 23 and 24, wherein said method comprises at least the following steps:
In a preferred embodiment of the method of the fourth aspect of the invention, the control unit (10) is configured to apply the pressure values obtained and the heat transfer coefficient between the freeze dryer and the product to be freeze-dried measured at different chamber pressures, and/or the resistance coefficient of the dry product to be freeze-dried to the vapour flow measured at different chamber pressures, as inputs to a heat and mass transfer model in order to calculate the mass flux inside the freeze-drying chamber at different times and at different product temperatures in a 2D or 3D work map.
In a preferred embodiment of the method of the fourth aspect of the invention, the control unit (1O) is configured to subsequently establish the relationship between the chamber pressure, the mass flux and the product temperature in a 2D or 3D work map at different product temperatures.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/ES2022/070407 | 6/28/2022 | WO |
