FREEZE DRYER AND METHOD FOR FREEZE DRYING
20230417486 ยท 2023-12-28
Inventors
Cpc classification
F26B5/06
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
Abstract
A freeze dryer is provided, which comprises a freeze-drying chamber having an inlet for allowing material to be dried to be introduced into the freeze-drying chamber and configured for being evacuated at least partially, and a vacuum source in fluid communication with the drying chamber and configured for evacuating the freeze-drying chamber at least partially. A vacuum fluid path is defined between the freeze-drying chamber and the vacuum source. The freeze dryer further comprises a collecting filter configured for collecting dried material from the freeze-drying chamber, which collecting filter is arranged outside the freeze-drying chamber and within the vacuum fluid path between the freeze-drying chamber and the vacuum source.
Claims
1-27. (canceled)
28. A freeze dryer, comprising: a freeze-drying chamber having an inlet for allowing material to be dried to be introduced into the freeze-drying chamber and configured for being evacuated at least partially; and a vacuum source in fluid communication with the drying chamber and configured for evacuating the freeze-drying chamber at least partially, wherein a vacuum fluid path is defined between the freeze-drying chamber and the vacuum source, wherein the freeze dryer further comprises a material collector configured for collecting dried material from the freeze-drying chamber, which material collector is arranged outside the freeze-drying chamber and within the vacuum fluid path between the freeze-drying chamber and the vacuum source.
29. The freeze dryer according to claim 28, wherein the material collector is arranged next to and/or beside the freeze-drying chamber.
30. The freeze dryer according to claim 28, wherein the material collector comprises a collector housing having an inlet in fluid communication with the freeze-drying chamber, a vacuum outlet in fluid communication with the vacuum source and a collector fluid path between the inlet and the outlet, and a collecting device provided between the inlet and the outlet and dividing the collector fluid path in a first path portion downstream of the collecting device and a second path portion upstream of the collecting device.
31. The freeze dryer according to claim 30, wherein the collecting device comprises a collecting filter screen provided between the inlet and outlet and dividing the collector fluid path in a first path portion downstream of the collecting filter screen and a second path portion upstream of the collecting filter screen.
32. The freeze dryer according to claim 30, wherein the collector housing is provided with a material outlet in fluid communication with the first or second path portion of the collector fluid path and configured for allowing material collected by the collecting device to exit the collecting device.
33. The freeze dryer according to claim 30, wherein the collector housing has a bottom, wherein the material outlet is arranged at or near the bottom of the collector housing.
34. The freeze dryer according to claim 30, wherein the collector housing has a double-jacketed wall configured for receiving a heating fluid in order to heat fluid flowing through the collector fluid path and/or dried material collected within the material collector.
35. The freeze dryer according to claim 28, comprising a collected material recipient configured for receiving material collected by the material collector and provided at or near the material collector.
36. The freeze dryer according to claim 35, wherein the collected material recipient has a recipient body with a recipient chamber defined therein for receiving the collected material.
37. The freeze dryer according to claim 32, wherein the collected material recipient is arranged at the material outlet in order to receive collected material from the material collector.
38. The freeze dryer according to claim 35, wherein the collected material recipient is configured for heating the collected material received therein, preferably wherein the recipient body of the collected material recipient has a double-jacketed wall configured for allowing a heating fluid to circulate there through.
39. The freeze dryer according to claim 28, wherein the material collector is arranged at a first height, and the freeze-drying chamber is arranged at a second height, and/or wherein the material collector is provided on top of and/or above the freeze-drying chamber.
40. The freeze dryer according to claim 39, comprising a valve arranged within the vacuum fluid path and between the freeze-drying chamber and the material collector, wherein the valve is configured to be moved between an open position for allowing fluid flow from the freeze-drying chamber to the material collector, a closed position for preventing fluid flow from the freeze-drying chamber to the material collector, and/or an intermediate position for restricting fluid flow from the freeze-drying chamber to the material collector.
41. The freeze dryer according to claim 40, wherein the valve is further configured for temporarily holding material collected by the material collector, when in the closed position.
42. The freeze dryer according to claim 40, comprising a fluid bypass conduit provided between the freeze-drying chamber and the material collector, and providing a bypassing fluid path between the freeze-drying chamber and the material collector which bypasses the valve.
43. The freeze dryer according to claim 28, further comprising a purge inlet provided in fluid communication with the vacuum fluid path, preferably downstream of the material collector, wherein the purge inlet is configured to be connected to a purge source in order to allow a blow pulse to be provided to the material collector; and/or wherein all components of the freeze dryer are arranged for being contained and/or for being coupled to each other in a contained manner.
44. The freeze dryer according to claim 28, comprising a substantially conical vessel, preferably having a downwardly conical shape, in which the freeze-drying chamber is defined, and an agitating member arranged within the freeze-drying chamber and configured for agitating material introduced into the freeze-drying chamber.
45. The freeze dryer according to claim 44, wherein the substantially conical vessel comprises a lid for closing off a top of the freeze-drying chamber, wherein the lid and/or the substantially conical vessel is provided with one or more blow nozzles having an outlet orientated into the freeze-drying chamber and configured for being connected to a gas source.
46. The freeze dryer according to claim 44, wherein the substantially conical vessel comprises a releasable outlet at the bottom thereof, which releasable outlet is usually closed and can be opened.
47. A method for freeze-drying or sublimation of a material to be dried by means of a freeze dryer according to claim 28, wherein the method comprises the steps of: introducing a material to be dried into the freeze-drying chamber of the freeze dryer; and evacuating the freeze-drying chamber at least partially by means of the vacuum source, in order to reduce the pressure within the freeze-drying chamber to or below a predetermined pressure level, wherein the method further comprises the step of collecting dried material from the freeze-drying chamber by means of a material collector arranged outside the freeze-drying chamber and within the fluid path between the freeze-drying chamber and the vacuum source.
48. The method according to claim 47, comprising one or more of the following steps: reducing the temperature within the freeze-drying chamber to a temperature close to the freezing temperature of the material to be dried, preferably before the step of evacuating the freeze-drying chamber; introducing a gas bleed, such as an intermittent gas bleed, into the freeze-drying chamber, preferably at or near the end of the freeze-drying process; providing a blow-back pulse across the material collector, preferably periodically; at the end of the freeze-drying process, re-introducing material collected by the material collector into the freeze-drying chamber, and post-blending the re-introduced material and remaining material within the freeze-drying chamber; wherein the material collector is arranged at a first height, and the freeze-drying chamber is arranged at a second height, and/or wherein the material collector is provided on top of and/or above the freeze-drying chamber, wherein the freeze dryer comprises a valve arranged within the vacuum fluid path and between the freeze-drying chamber and the material collector, wherein the valve is configured to be moved between an open position for allowing fluid flow from the freeze-drying chamber to the material collector, a closed position for preventing fluid flow from the freeze-drying chamber to the material collector, and/or an intermediate position for restricting fluid flow from the freeze-drying chamber to the material collector, and wherein the freeze dryer comprises a fluid bypass conduit provided between the freeze-drying chamber and the material collector, and providing a bypassing fluid path between the freeze-drying chamber and the material collector which bypasses the valve, wherein the method comprises the steps of: maintaining the valve in its open position during freezing and early stages of the sublimation phase, therewith enabling the tiny ice particles to be recirculated back into the freeze-drying chamber; as drying progresses and more dust is released from freeze-drying chamber, moving the valve to its closed position, therewith forcing the released dust to move via the bypass conduit to the material collector; and optionally, at or near the end of the drying process, moving the valve into its open position in order to enable the collected dust on the valve to be returned into the freeze-drying chamber.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0040] The invention will be elucidated on the basis of an exemplary embodiment shown in the attached drawings, in which:
[0041]
[0042]
[0043]
DETAILED DESCRIPTION OF THE INVENTION
[0044] A freeze dryer 1 according to a first embodiment of the invention is shown in
[0045] As shown in
[0046] As further shown in
[0047] As shown in
[0048] The freeze dryer 1 further comprises a non-shown vacuum source, such as a vacuum pump, which is operatively connected to the freeze-drying chamber 3, i.e. is in fluid communication with the freeze-drying chamber 3. The vacuum source is configured for, during use, reducing the pressure within the freeze-drying chamber to a predetermined pressure value, such as within the range of 5 mbar-0.01 mbar, depending on material/process conditions.
[0049] As shown in
[0050] The material collector 40 further comprises a filter holder 55 arranged at the circular cylindrical tube 41 at the upper end 43 thereof. The filter holder 55 has a circular cylindrical holder body 56 having substantially the same diameter as the circular cylindrical tube 41. A holding ledge 57 is provided at the inner circumference of the circular cylindrical holder body 56, which holding ledge 57 extends inwardly in a direction substantially transversal to the longitudinal direction of the circular cylindrical tube 41, while defining a filter through hole 58 at the center thereof. A clamping ring 59 is placed on top of the holding ledge 57, thereby covering the filter through hole 58.
[0051] The filter holder 55 further has a filter holder lid 60 arranged at the filter holder 55 at the side facing away from the circular cylindrical tube 41. The filter holder lid 60 includes a holder lid body 61 having a first side, facing upwardly in
[0052] As shown in
[0053] As shown in
[0054] The freeze dryer 1 has a collected material recipient 83 configured for receiving material collected by the material collector 40. The collected material recipient 83 has a recipient body 84 with a recipient chamber 85 defined therein for receiving material from the material collector 40. The recipient body 85 has a coupling portion 86 for being coupled to the material outlet opening flange 82 by means of an intermediate coupling piece 87. Around a part of the recipient body 84 is provided a heating device 88 for heating the contents of the recipient chamber 85.
[0055] As show in
[0056] The freeze dryer 1 further comprises, as shown in
[0057] During use, a material to be dried or a mixture of materials to be dried is introduced into the freeze-drying chamber 3. After introducing the material or mixture, the top lid 13 is closed and subsequently the temperature within the freeze-drying chamber 3 is lowered to a temperature close to and above the freezing temperature of the material or the mixture, by introducing a heat-exchanging medium into the double-jacketed vessel wall 10. Optionally, the material or mixture is precooled, or pre-frozen into granular ice particles before being introduced into the freeze-drying chamber 3, or is pre-frozen or precooled by means of cooling the material or mixture by means of the double-jacketed vessel wall 10.
[0058] The cooling step is followed by a controlled lowering of the pressure within the freeze-drying chamber 3 by means of the non-shown vacuum pump, until it approaches a pressure suitable for sublimation/freeze drying. The suitable pressure depends on the product and process characteristics, but might be in a range between 0.1 and 3 mbar. The reduction in the pressure within the freeze-drying chamber 3 causes a corresponding reduction in temperature within the freeze-drying chamber 3 and of the material or mixture, until freezing begins. During the freezing step, the motion of the agitating screw 16 ensures that the material or mixture does not freeze into a solid mass of ice, since it is desired to obtain fine, loose ice granules at the end of the freezing step. Optionally, in order to support sublimation, the temperature of the double-jacketed vessel wall 10 is slowly increased until the required maximum double-jacketed vessel wall 10 and/or product temperature is reached, which subsequently is maintained until drying is completed.
[0059] During the freezing step, fine ice particles are formed from the initial material or mixture. As sublimation progresses and the temperature of the double-jacketed vessel wall 10 is increased, vapor flows through from the freeze-drying chamber 3 towards the non-shown vacuum pump via the material collector. As this happens, the individual ice particles shrink in size leading to the release of fine (powdery) dust which remains as drying progresses. The powder is carried along with the vapor flow towards the material collector 40, where the dust is deposited on the filter screen 76 of the filter 70. Upon application of a filter blowback pulse via the purge inlet 90, the deposited dust is removed from the filter screen 76 and falls towards and into the collected material recipient 83. The collected material may be further dried within the collected material recipient 83 by the heating device 88 for heating the contents of the recipient chamber 85 before discharge.
[0060] It is possible that a fraction of the dried material or mixture is not transported towards the material collector 40 and remains freeze-drying chamber 3, or is deposited on the inner circumference of the freeze-drying chamber 3. It is possible to force the remaining material out of the freeze-drying chamber 3 towards the material collector 40. This can be done by a short, intermittent introduction of a gas bleed, e.g. air or nitrogen, into the freeze-drying chamber 3 via blow nozzles 99. Since the vacuum conditions are still present within the freeze-drying chamber, the expansion of the gas introduced into the freeze-drying chamber 3 causes the remaining dust to be blown off, thereby increasing the likelihood of transport to the filter. Gas bleed into the freeze-drying chamber 3 could also be used to optimize the process yield.
[0061] If required, a post-blending step may be carried out at the end of drying by collecting the material from the collected material recipient 83, and re-introducing it into the freeze-drying chamber 3. Blending is achieved by means of the agitating screw 16 so that a single batch is recovered at the end.
[0062]
[0063] The freeze dryer 101 as shown in
[0064] Furthermore, the freeze dryer 101 is provided with a bypass conduit 210 having a first conduit end 211 and a second conduit end 212, opposite to the first end 211. As shown in
[0065] The valve 200 and the bypass conduit 210 are configured for enabling recirculation of tiny ice particles during the sublimation phase. It is noted in the context of the present patent application that during the freezing and early sublimation stages, the vapor flow through the material collector 140 and towards the non-shown vacuum pump is at its highest. At this stage, some of the fine, loose ice granules could be being transported along with the vapor flow in the direction of the filter 170 of the material collector 140. The valve 200 between the freeze-drying chamber 103 and the material collector 140 is in the open position thereof during freezing and early stages of the sublimation phase, therewith enabling the tiny ice particles to be recirculated back into the freeze-drying chamber 103 instead of being retained in the filter 70. As drying progresses and more (powdery) dust is released from the ice matrix, the valve 200 is brought into its closed state. Following on closing the valve 200, the released dust is forced to move via the bypass conduit 210 along with the vapor flow to the filter 170 of the material collector 140. When the dust has been filtered from the vapor flow by the filter screen 176, the dust falls off the filter screen 176 onto the closed valve 200. At this stage of drying, the valve 200 serves as a dust recipient for temporarily holding the collected dust. The valve 200 is opened towards the end the drying process to enable the collected dust on the valve 200 to be returned into the freeze-drying chamber 103.
[0066] The determination of when to close the valve 200, for example, can be largely based on the onset of dust release which can be assessed either by monitoring pressure drop increase across the material collector 140, or tailored to coincide with the initiation of a filter blowback pulse, by visual inspection of the process, or any other process analytical tool. On the other hand, the determination of when to re-open the valve 200 towards the end of freeze-drying process depends on the decrease in vapor flow, or when the maximum double-jacketed vessel wall 110 and/or material or mixture temperature is reached, or when the pressure within the freeze-drying chamber 103 has decreased sufficiently. At the end of the drying process, a single product batch is discharged from the freeze dryer 101. Alternatively, the dust within the material collector 140 can also be collected separately from the material or mixture remaining in the freeze-drying chamber 103.
[0067] It is to be understood that the above description is included to illustrate the operation of the preferred embodiments and is not meant to limit the scope of the invention. From the above discussion, many variations will be apparent to one skilled in the art that would yet be encompassed by the scope of the present invention.