Patent Application
20230364621
The invention relates to a set of exchangeable separation inserts for a modular centrifugal separator system, to a modular centrifugal separator system, and to a method for operating a modular centrifugal separator system.
In the field of pharmaceuticals, biopharmaceuticals, biotechnology and thereto related fields, separation of substances from a liquid mixture, such as separation of cells from a cell culture mixture, are performed in a sterile environment. Traditionally, equipment made e.g. from stainless steel has been used, which equipment is sterilised between batches.
Disposable separation equipment made for single use, i.e. for one batch or a limited number of batches, has been suggested. For instance, US2011/0319248 discloses a single use centrifuge and WO 2015/181177 discloses a separator comprising an exchangeable inner drum.
Such disposable separation equipment is supplied to the user in a sterile manner. Thus, a sterile environment for the product in the separator may be provided without sterilisation of the separation equipment at the production facility of the user.
EP 3666394 discloses a base unit and a modular centrifugal separator. The base unit comprises a stationary frame, a rotatable member, and a drive unit. The rotatable member delimits an inner space being configured for receiving at least one part of an exchangeable separation insert therein. The rotatable member is provided with a first opening at a first axial end configured for a first fluid connection of the exchangeable separation insert to extend through the first opening. The rotatable member comprises a second opening at a second axial end configured for a second fluid connection of the exchangeable separation insert to extend through the second opening.
U.S. Pat. No. 6,973,925 discloses a ventilation device for a crankcase of an internal combustion engine. Said device comprises a centrifugal oil separator comprising plates/disks, which has an inlet for an oil-air mixture, an air vent for the purified air and an oil outlet for the oil. In this context of a gas liquid separator, the use of different numbers of plates adapted to the volumetric flow of gas requiring oil removal is described.
Different separation processes may require different separation capacities.
It would be advantageous to achieve different separation capacities in the context of a modular centrifugal separator system with a base unit and exchangeable separation inserts. In particular, it would be desirable, within the limitations set by a particularly sized base unit of a modular centrifugal separator system, to provide different separation capacities. To better address one or more of these concerns, at least one of a set of exchangeable separation inserts for a modular centrifugal separator system, a modular centrifugal separator system, and a method for operating a modular centrifugal separator system, having the features defined in the independent claims is provided.
According to an aspect of the invention, there is provided a set of exchangeable separation inserts for a modular centrifugal separator system comprising a base unit. The set of exchangeable separation inserts comprises at least a first exchangeable separation insert and a second exchangeable separation insert. Each of the first and second exchangeable separation inserts comprises a rotor casing configured to rotate about an axis of rotation and forming a separation space, separation discs arranged in the separation space, and fluid connections for a liquid feed mixture, a separated heavy phase, and a separated light phase. The separation discs of the first exchangeable separation insert have a first area equivalent and the separation discs of the second exchangeable separation insert have a second area equivalent. Each of the rotor casings of the first and second separation inserts have a same external shape to an extent that they fit a rotatable member of a base unit of a modular centrifugal separator system. The first area equivalent differs from the second area equivalent with each of the first and second area equivalents calculated for the same rotational speed.
As an example, each of the rotor casings of the first and second separation inserts may have a same external shape to an extent that they fit inside an inner space of a rotatable member of a base unit of a modular centrifugal separator system and abut against at least part of an inner surface of the rotatable member, the inner surface delimiting at least part of the inner space.
According to a further aspect of the invention, there is provided a modular centrifugal separator system configured for separating a liquid feed mixture into a heavy phase and light phase. The modular centrifugal separator system comprises a base unit and a first exchangeable separation insert. The base unit comprises a stationary frame, a rotatable member and a drive unit for rotating the rotatable member about the axis of rotation. The rotatable member may be configured to rotate about an axis of rotation arranged in the stationary frame. The rotatable member may delimit an inner space at least in a radial direction, the inner space being configured for receiving at least one part of the first exchangeable separation insert therein. The modular separation system comprises a set of exchangeable separation inserts according to any one of aspects and/or embodiments discussed herein. The first exchangeable separation insert forms part of the set of exchangeable separation inserts.
The rotatable member may be a rotatable member into which a separation insert is inserted, thereby transmitting torque to the separation insert during operation by direct contact with the separation insert. However, the rotatable member may also be realised as at least one electromagnetic bearing, which does not necessarily have to rotate on its own, for transmitting torque to the separation insert without a direct contact. The drive unit may thus be a magnetic drive device.
According to a further aspect of the invention, there is provided a method for operating a modular centrifugal separator system configured for separating a liquid feed mixture into a heavy phase and light phase according to any one of aspects and/or embodiments discussed herein. The method comprises steps of:
Since the set of exchangeable separation inserts of the modular centrifugal separator system comprises first and second exchangeable separation inserts have different area equivalents at the same rotational speed, different separation capacities are provided by each of the set of exchangeable separation inserts, the modular centrifugal separator system, and the method. Thus, within the limitations of one and the same base unit of the modular centrifugal separator system, by using either the first or second exchangeable separation insert, an adequate separation capacity is selectable.
The inventor has contemplated the situation; that for certain separation operations, centrifugation of certain liquid feed mixtures, their contents may not be suited to be subjected to centrifugal forces above a certain level, such as e.g. a liquid feed mixture comprising a fermentation broth containing CHO cells. The inventor has realised that different separation capacities can be achieved in a modular centrifugal separator comprising an exchangeable separation insert at up to a maximum separation speed, i.e. at up to a maximum centrifugal force, defined by properties of a particular liquid feed mixture but with the use of different total surfaces areas provided in the exchangeable separation inserts. Thus, in the context of disposable separation equipment made for single use, i.e. for separating one batch only or a limited number of batches, the supplying of the first and second exchangeable separation inserts discussed herein provide adaptation to required or desired separation capacity in the modular centrifugal separator system.
In this manner also a cost reduction for a lower capacity separation may be provided by the use of a separation insert having fewer separation discs or smaller diameter separation discs.
In the context of traditional disc stack centrifugal separators configured for continuous or multiple use and which are devised for being disassembled only for service and/or cleaning purposes, differently sized separators having different separation capacities are well known. Also, the use of differently sized disc stacks utilising the same type and size of separation discs are known, such as e.g. discussed in the above cited U.S. Pat. No. 6,973,925.
However, the provision of differently sized disc stacks of separation discs of the same type and size has traditionally served the purpose of providing centrifugal separators in different versions. In the selection of a suitable centrifugal separator or version of centrifugal separator for a particular separation operation, inter alia the type of liquid feed mixture, its volumetric flow, viscosity, temperature, feed composition, and particle content determine the selection of one particular centrifugal separator. Once selected, the composition of different parts and in particular the number and size of separation disc is not altered.
According to the present invention the exchangeability of exchangeable separation inserts of a modular centrifugal separator is utilised for providing differing separation performance within one and the same base unit. Thus, a greater flexibility in the use of a modular centrifugal separator, now forming part of a modular centrifugal separator system including first and second exchangeable separation inserts, is utilised. This greater flexibility may be utilised e.g. in the context of separating different cell culture mixtures, particular biomolecules produced, or particular cells produced.
The term separation performance relates to flow of liquid feed mixture that can be separated to a certain concentration of heavy phase and/or a certain clarity of light phase.
A modular centrifugal separator may comprise two main parts, the base unit and an exchangeable separation insert. In such a modular centrifugal separator separation of a liquid feed mixture may be performed. The modular centrifugal separator system may comprise such a modular centrifugal separator and a further exchangeable separation insert, i.e. comprising a set of exchangeable separation inserts as defined above.
Herein, descriptions may refer to a modular centrifugal separator. Such descriptions also relate to a modular centrifugal separator system and its different components. In particular, general aspects of the exchangeable separation insert of the modular centrifugal separator relate to both the first and second exchangeable separation insert of the set of exchangeable separation inserts and of the modular centrifugal separator system.
The base unit may comprise basic components for supporting and rotating the exchangeable separation insert. The exchangeable separation insert may be configured for the actual separation of the liquid feed mixture to take place in the separation space thereof. The liquid feed mixture may flow through one fluid connection into the separation space and the separated heavy and light phases may leave the separation space via one fluid connection each.
The term area equivalent of the separation discs of the first and second exchangeable separation inserts is a measure of the separation capacity of the relevant exchangeable separation insert. That is, the higher the area equivalent, the higher the separation performance of an exchangeable separation insert.
According to embodiments, the separation discs are frustoconical separation discs, as known in the art. However, the separation discs may also have any other suitable shape, such as being axial separation sheets, i.e. axial sheets having an axially extending surfaces and having a straight or curved extension in a radial direction. Such extending surfaces of the separation sheets may extend in parallel with the rotational axis. However, the axially extending surfaces may also extend with a small angle relative the rotational axis, or e.g. be slightly curved in relation to the rotational axis. Each separation sheet has two axially extending surfaces, a first surface facing forwardly in a rotational direction of the rotor casing and a second surface facing rearwardly from the rotational direction of the rotor casing.
The area equivalent, Ae, is calculated according to the following formula for frustoconical separation discs:
Ae=(2π/3g)(Ncotαω2(ry3−ri3))
Wherein: g=gravity, N=the number of frustoconical separation discs of the separation insert, α=half the apex angle of the frustoconical separation discs, i.e. the angle between the axis of rotation and an inner surface of one of the frustoconical separation discs, ω=rotational speed of the separation insert, ry=outer radius of the frustoconical separation disc, ri=inner radius of the frustoconical separation disc.
In order to provide a comparative measure between the first and second exchangeable separation inserts when not in use, i.e. non-rotating, a rotational speed neutral figure is provided by the area equivalent of the respective first and second exchangeable separation insert calculated for the same rotational speed, e.g. ω=1 for both the first and second exchangeable separation insert.
The exchangeable separation insert may be configured for single use, i.e. for separation of one batch only or a limited number of batches of liquid feed mixture. The base unit on the other hand may be configured for repeated use with different exchangeable separation inserts such as the first and second exchangeable separation inserts, i.e. the base unit may be used for the separation of numerous batches of liquid feed mixture using different exchangeable separation inserts.
The first and second exchangeable separation inserts may be configured to form the only part of the modular centrifugal separator system, which is in contact with the liquid feed mixture, and the separated heavy and light phases. Thus, the first and second exchangeable separation inserts may be provided to a user as a sterile entity. The sterile entity may include parts configured for separating the liquid feed mixture as well as conduits for the liquid feed mixture and the separated heavy and light phases. The exchangeable separation inserts are mounted in the base unit by the user. Thus, the user will readily have available a centrifugal separator with a sterile environment for separation of the liquid feed mixture.
The rotatable member of the base unit may be rotatably supported in the stationary frame. The rotatable member may be supported in the stationary frame without the aid of a spindle or other kind of rotor shaft. The stationary frame is stationary in the sense that it is stationary during use of modular centrifugal separator.
According to embodiments, the first area equivalent differing from the second area equivalent may be provided by a difference in number of separation discs between the first and second exchangeable separation insert. In this manner, different separation performance may be provided by differing number of separation discs in the first and second exchangeable separation discs.
According to embodiments, the frustoconical separation discs of the first exchangeable separation insert and the frustoconical separation discs of the second exchangeable separation insert may have a same total height along the axis of rotation. A distance between at least two of the frustoconical separation discs of the first exchangeable separation insert may differ from a distance between at least two of the frustoconical separation discs of the second exchangeable separation insert. In this manner, the frustoconical separation discs may occupy the same amount of space in the separation space in the first and second exchangeable separation discs, while the distance between the separation discs in the respective first and second exchangeable separation insert differ to accommodate for the differing number of separation discs in the first and second exchangeable separation insert.
According to embodiments, the first area equivalent differing from the second area equivalent may be provided by at least one of:
According to embodiments, the rotor casing of each of the first and second exchangeable separation insert has a first axial end portion and a second axial end portion and each of the first and second exchangeable separation insert may comprise at least a first fluid connection arranged at the first axial end portion. In this manner, the liquid feed mixture may be led to the exchangeable separation inserts or one of the heavy phase or light phase may be led from the exchangeable separation inserts at the first axial end portion thereof. Optionally, a second and even a third fluid connection may be provided at the first axial end portion permitting one or more of the liquid feed mixture, the heavy phase, and/or light phase to also enter or exit the exchangeable separation insert at the first axial end portion thereof.
In connection with such embodiments of the set of exchangeable separation inserts, according to embodiments of the modular centrifugal separator system, the rotatable member has a first axial end and a second axial end. The rotatable member may be provided with a first opening at the first axial end configured for at least a first fluid connection of the first or second exchangeable separation insert to extend through the first opening. In this manner, the liquid feed mixture may be led to the exchangeable separation inserts or one of the heavy phase or light phase may be led from the exchangeable separation inserts via the first opening of the rotatable member. Optionally, a second and even a third fluid connection of the exchangeable separation inserts may extend to/from the exchangeable separation inserts via the first opening of the rotatable member.
According to embodiments, each of the first and second exchangeable separation insert may comprise at least a second fluid connection arranged at the second axial end portion. In this manner, the liquid feed mixture may be led to the exchangeable separation inserts or one of the heavy phase or light phase may be led from the exchangeable separation inserts at the second axial end portion thereof. A third fluid connection may be provided at the first or second axial end portion.
In connection with such embodiments of the set of exchangeable separation inserts, according to embodiments of the modular centrifugal separator system, the rotatable member may comprise a second opening at the second axial end configured for at least a second fluid connection of the first or second exchangeable separation insert to extend through the second opening. In this manner, the liquid feed mixture may be led to the exchangeable separation inserts or one of the heavy phase or light phase may be led from the exchangeable separation inserts via the second opening of the rotatable member. A third fluid connection of the exchangeable separation inserts may extend through the first or second opening of the rotatable member.
According to embodiments of the method, each of the first and second batch of liquid feed mixture may comprise solid matter. The first batch of liquid feed mixture may differ from the second batch of liquid feed mixture by at least one of: type of solid matter, concentration of solid matter, and/or content of the separated first light phase and content of the separated second light phase.
According to embodiments of the method, each of the first and second batch of liquid feed mixture may be a cell culture mixture. The cell culture mixture may be produced as a fermentation broth in a fermenter tank. The heavy phase separated in the centrifugal separator system may comprise a concentrate of cells in a small portion of fermentation broth. The light phase separated in the centrifugal separator system may contain substantially only fermentation broth.
Further features of, and advantages with, the invention will become apparent when studying the appended claims and the following detailed description.
Various aspects and/or embodiments of the invention, including its particular features and advantages, will be readily understood from the example embodiments discussed in the following detailed description and the accompanying drawings, in which:
Aspects and/or embodiments of the invention will now be described more fully. Like numbers refer to like elements throughout. Well-known functions or constructions will not necessarily be described in detail for brevity and/or clarity.
The disclosure of EP 3666394 is enclosed herein by reference. In particular, details of the modular separator, its base unit and exchangeable separation insert are applicable in the context of the present invention including the set of exchangeable separation inserts, the modular centrifugal separator system, and the method for operating a modular centrifugal separator system.
Herein the base unit 4 with one of the first or second exchangeable separation inserts 6, 6′ mounted there may be referred to as a modular centrifugal separator 2.
The modular centrifugal separator 2 is configured for separating a liquid feed mixture into a heavy phase and light phase. For instance, the liquid feed mixture may be formed by a fermentation broth including a cell culture, the heavy phase may comprise the cells separated from the main part of the fermentation broth. The light phase may be formed by main part the fermentation broth without the cells or with only a minimum rest amount of cells.
The modular centrifugal separator system 1 is modular in the sense that it comprises the base unit 4 and the first and second exchangeable separation inserts 6, 6′. The exchangeable separation inserts 6, 6′ are exchanged for each new batch of liquid feed mixture, which is to be separated. Alternatively, the exchangeable separation inserts 6, 6′ may be exchanged for each new type of liquid feed mixture, which is to be separated, i.e. subsequent batches containing same type of liquid feed mixtures may be separated with the same exchangeable separation insert 6, 6′.
During use of the modular centrifugal separator system 1 the liquid feed mixture, the heavy phase, and the light phase only come into contact with the relevant first or second exchangeable separation insert 6, 6′ of the modular centrifugal separator system 1. Naturally, conduits in the form of tubes 10 configured for conducting the liquid feed mixture to the exchangeable separation insert 6 and for conducting the heavy phase and the light phase from the exchangeable separation insert 6 also come into contact with the liquid feed mixture and the heavy and light phases. The tubes 10 may form part of the exchangeable separation insert 6. The base unit 4 does not come into contact with the liquid feed mixture or any of the heavy and light phases.
The first and second exchangeable separation inserts 6, 6′ form a set of exchangeable separation inserts of the modular centrifugal separator system 1.
The first and second exchangeable separation inserts 6, 6′ are further discussed below with reference to
The base unit 4 comprises components for supporting and rotating the exchangeable separation insert. Thus, the base unit 4 comprises inter alia a stationary frame 8, a rotatable member, and a drive unit for rotating the rotatable member. The stationary frame 8 comprises a vertical member 12. Part of the drive unit may be arranged in the vertical member 12.
The stationary frame 8 is stationary during use of the modular centrifugal separator. However, the base unit 4 as such may be movable, e.g. in order to be positioned at different locations at a production facility of the user. For this purpose, the stationary frame 8 may be provided with wheels 14.
The base unit 4 is further discussed below with reference to
As mentioned above, the base unit 4 comprises the stationary frame 8, the rotatable member 16, and the drive unit 18. The rotatable member 16 is arranged in the stationary frame 8 and is configured to rotate about an axis 20 of rotation. The drive unit 18 is configured for rotating the rotatable member 16 about the axis 20 of rotation.
Seen along the axis 20 of rotation, the rotatable member 16 has a first axial end 22 and a second axial end 24. The rotatable member 16 delimits an inner space 26 at least in a radial direction. The radial direction extends perpendicularly to the axis 20 of rotation. The inner space 26 is configured for receiving at least one part of the first or second exchangeable separation insert therein, see further below with reference to
The rotatable member 16 is provided with a first opening 28 at the first axial end 22. The rotatable member 16 further is provided with a second opening 30 at the second axial end 24. Each of the first and second openings 28, 30 forms a through hole in the rotatable member 16. Thus, the inner space 26 is accessible via each of the first and second openings 28, 30. Accordingly, the first and second openings 28, 30 are configured for fluid connections of the first or second exchangeable separation insert to extend therethrough. See further below with reference to
Access to the inner space 26 is provided via a cap 34. Thus, the first or second exchangeable separation insert may be mounted in and removed from the inner space 26. The rotatable member 16 is arranged inside a stationary housing 52. The housing 52 comprises a lid 54. In an open position of the lid 54, access is provided to the rotatable member 16 inside the housing 52, e.g. for exchange of the exchangeable separation insert.
The inner space 26 of the rotatable member 16 is delimited at least in part by an inner surface 67. The first and second separation inserts have a same external shape to an extent that they fit inside the inner space 26. Each of the first and second separation insert, when fitted in the inner space 26 abut against at least part of an inner surface 67. Thus, the first and second exchangeable separation inserts are supported in the inner space 26.
In the illustrated embodiments, the rotatable member 16 comprises a frustoconical wall member 68 having an imaginary apex in a region of the second axial end 24. The frustoconical wall member 68 delimits a portion of the inner space 26 and comprises the inner surface 67. When positioned in the inner space 26, an exchangeable separation insert having a conical or frustoconical shape may be supported by the frustoconical wall member 68.
The exchangeable separation insert 6, 6′ is configured for part of it to be arranged inside an inner space 26 of a rotatable member 16 of a base unit, e.g. a base unit 4 as discussed above in connection with
The exchangeable separation insert 6, 6′ comprises a rotor casing 82, a first stationary portion 84 arranged at a first end portion 85 of the rotor casing 82, and a second stationary portion 86 arranged at a second end portion 87 of the rotor casing 82. The exchangeable separation insert 6 is configured to rotate about an axis 20 of rotation. The rotor casing 82 is arranged between the first stationary portion 84 and the second stationary portion 86. During operation of the modular centrifugal separator, the first stationary portion 84 is arranged at an upper axial end of the exchangeable separation insert 6, whereas the second stationary portion 86 is arranged at a lower axial end of the exchangeable separation insert 6.
Each of the rotor casings 82 of the first and second separation inserts 6, 6′ have a same external shape to an extent that they fit inside an inner space 26 of a rotatable member 16 of a base unit 4 of a modular centrifugal separator system 1 and abut against at least part of an inner surface 67 of the rotatable member, e.g. as discussed above with reference to
The rotor casing 82 delimits a separation space 88 therein. The exchangeable separation insert 6 comprises a stack 90 of frustoconical separation discs 92 arranged in the separation space 88. The separation discs 92 in the stack 90 are arranged with an imaginary apex at the second stationary portion 86, and/or pointing towards the second stationary portion 86. The stack 90 may comprise at least 50 separation discs 92, such as at least 100 separation discs 92, such as at least 150 separation discs 92. Mentioned as an example, a separation disc 92 may have an outer radius, ry, within a range of −80-200 mm, an inner radius, ri, within a range of 30-50 mm, and an angle α between the axis 20 of rotation and an inner surface of the disc 92 (half the apex angle of the frustoconical separation discs 92) within a range of 35-45 degrees. For clarity reasons, only a few discs 92 are shown in
In the illustrated embodiments, each of the first and second exchangeable separation insert 6, 6′ comprises at least a first fluid connection 94 arranged at the first axial end portion 85. Each of the first and second exchangeable separation insert 6, 6′ comprises at least a second fluid connection 96 arranged at the second axial end portion 87.
More specifically, the exchangeable separation insert 6, 6′ comprises a first fluid connection 94 arranged at the first stationary portion 84. A first conduit portion 95 forms part of the first fluid connection 94. The first conduit portion 95 of the first fluid connection 94 extents through the first stationary portion 84. The exchangeable separation insert 6 comprises a second fluid connection 96 arranged at the second stationary portion 86. A second conduit portion 97 forms part of the second fluid connection 96. The second conduit portion 97 of the second fluid connection 96 extents through the second stationary portion 86. In these embodiments, the exchangeable separation insert 6 comprises a third fluid connection 98 arranged at the second stationary portion 86. A third conduit portion 99 forms part of the third fluid connection 98. The third conduit portion 99 of the third fluid connection 98 extents through the second stationary portion 86. Inside the rotor casing 82 there is arranged one or more outlet conduits 102 for the separated heavy phase from the separation space 88. The first, second, and third fluid connections 94, 96, 98 may comprise tubing, such as plastic tubing.
The first stationary portion 84 abuts against the rotor casing 82. The second stationary portion 86 abuts against the rotor casing 82. Seals 104 are provided between the respective first and second stationary portions 84, 86 and the rotor casing 82. The seals 104 form mechanical seals between the stationary portions 84, 86 and the rotor casing 82. Thus, the exchangeable separation insert 6 is provided with mechanically hermetically sealed inlet and outlets. A mechanical hermetical seal includes an abutment between part of the rotatable rotor casing and a stationary portion.
During operation, the exchangeable separation insert 6, 6′, arranged in a rotatable member 16, is brought into rotation around the axis 20 of rotation. Liquid feed mixture to be separated is supplied via the second fluid connection 96 arranged in the second stationary portion 86 and guiding channels 106 into the separation space 88. The liquid feed mixture to be separated is guided along an axially upwardly path into the separation space 88. Due to a density difference the liquid feed mixture is separated into a liquid light phase and a liquid heavy phase. This separation is facilitated by the interspaces between the separation discs 92 of the stack 90 fitted in the separation space 88. The heavy phase may comprise particles, such as e.g. cells. The heavy phase may comprise a concentrated mixture of light phase and particles.
The separated liquid heavy phase is collected from the periphery of the separation space 88 via outlet conduit 102 and is forced out of the rotor casing 82 to the first fluid connection 94 arranged in the first stationary portion 84. Separated liquid light phase is forced radially inwardly through the stack 90 of separation discs 92 and led out of the rotor casing 82 to the third fluid connection 98 arranged in the second stationary portion 86. Consequently, in this embodiment, the liquid feed mixture is supplied at a lower axial end of the exchangeable separation insert 6, the separated light phase is discharged at the lower axial end, and the separated heavy phase is discharged at the upper axial end of the exchangeable separation insert 6.
The first and second exchangeable separation inserts 6, 6′ differ from each other with respect to aspects of the frustoconical separation discs 92. More specifically, the frustoconical separation discs 92 of the first exchangeable separation insert 6 have a first area equivalent and the frustoconical separation discs 92 of the second exchangeable separation insert 6′ have a second area equivalent. The first area equivalent differs from the second area equivalent with each of the first and second area equivalents calculated for the same rotational speed. Thus, different separation performances are provided in the first and second exchangeable separation inserts 6, 6′.
According to embodiments, the first area equivalent differing from the second area equivalent is provided by a difference in number of frustoconical separation discs 92 between the first and second exchangeable separation insert 6, 6′. Thus, the stacks 90 of separation discs 92 of the first and second exchangeable separation inserts 6, 6′ may have different heights along the axis 20 of rotation.
According to alternative embodiments, the stacks 90 of separation discs 92 of the first and second exchangeable separation inserts 6, 6′ may have the same heights, but still with a difference in number of frustoconical separation discs 92. Accordingly, the frustoconical separation discs 92 of the first exchangeable separation insert 6 and the frustoconical separation discs 92 of the second exchangeable separation insert 6′ may have a same total height along the axis 20 of rotation. With a distance between at least two of the frustoconical separation discs 92 of the first exchangeable separation insert 6 differing from a distance between at least two of the frustoconical separation discs 92 of the second exchangeable separation insert 6′, the same height of both stacks 90 of separation discs may be achieved. The difference in distance between the separation discs 92 of the first and second exchangeable separation inserts 6, 6′ may be achieved by a difference in the height of caulks or other distance members, such as pointed projections, provided on the surfaces of the separation discs 92.
According to embodiments, the first area equivalent differing from the second area equivalent is alternatively or further provided by at least one of:
According to alternative embodiments, the stack 90 of frustoconical separation discs 92 may be arranged with an imaginary apex at the first stationary portion 84, and/or pointing towards the first stationary portion 84.
According to alternative embodiments, the first, second, and third fluid connections and corresponding fluid pathways inside the rotor casing 82 and the separation space 88 may be arranged differently than in the illustrate embodiments, e.g. two fluid connections may be provided at the first stationary portion 84 and one fluid connection at the second stationary portion 86.
According to alternative embodiments, the exchangeable separation insert 6, 6′ may comprise only the first or second stationary portion 84, 86. In such embodiments, the first, second, and third fluid connections are provided at the first or second stationary portion 84, 86, respectively.
In
The inner space 26 of the rotatable member 16 is delimited at least in part by an inner surface 67. The inner space 26 is configured for receiving at least one part of the first and second exchangeable separation inserts 6, 6′, respectively, therein.
The first and second separation inserts 6, 6′ have a same external shape to an extent that they fit inside the inner space 26. Each of the first and second separation insert, when fitted in the inner space 26 abut against at least part of an inner surface 67. Thus, the first and second exchangeable separation inserts 6, 6′ are supported in the inner space 26.
For instance, and as also mentioned above with reference to
It is to be noted that the first and second exchangeable separation inserts 6, 6′ need not be supported in exactly the same manner in the inner space 26. Each the first and second exchangeable separation inserts 6, 6′ may be supported in a different manner by the inner surface 67. For instance, one of the exchangeable separation inserts 6, 6′ may be supported at larger diameter portion of the frustoconical wall member 67 and the other of the exchangeable separation inserts 6, 6′ may be supported at smaller diameter portion of the frustoconical wall member 67.
During use of the modular centrifugal separator 2, the first stationary portion 84 is fixed in relation to the stationary frame 8 and the second stationary portion 86 is fixed in relation to the stationary frame 8.
In the illustrated embodiments, the rotatable member 16 has a first axial end 22 and a second axial end, and the rotatable member 16 is provided with a first opening 28 at the first axial end 22 configured for at least a first fluid connection 94 of the first or second exchangeable separation insert 6, 6′ to extend through the first opening 28. In this manner, the first fluid connection 94 may be arranged for extending into or out of the rotatable member 16.
In the illustrated embodiments, the rotatable member 16 comprises a second opening 30 at the second axial end 24 configured for at least a second fluid connection 96 of the first or second exchangeable separation insert 6, 6′ to extend through the second opening 30. In this manner, the second fluid connection 96 may be arranged for extending into or out of the rotatable member 16.
In the illustrated embodiments, a third fluid connection 98 of the first or second exchangeable separation insert 6, 6′ may extend through the second opening 30.
According to alternative embodiments, the third fluid connection 98 of the first or second exchangeable separation insert 6, 6′ may extend through the first opening 28.
According to further alternative embodiments, only the first or second opening 28, 30 is provided in the rotatable member and all fluid connections of the first or second exchangeable separation insert 6, 6′ extend through the first or second opening 28, 30 respectively.
The method 100 comprises steps of:
According to embodiments, the liquid feed mixture may be a cell culture mixture, i.e. each of the first and second batch of liquid feed mixture may be a cell culture mixture. The first batch of liquid feed mixture in the form of a cell culture mixture may be produced in a fermentation broth in a fermenter tank. Accordingly, a fermentation period in the fermenter tank may be followed by separation of the first batch of liquid feed mixture in the modular centrifugal separator system 1 utilising the first exchangeable separation insert 6. That is, the fermentation period may be followed by steps 102-108 of the method 100 being performed. The second batch of liquid feed mixture, after a subsequent or parallel fermentation period in a fermenter tank, may be follow in the modular centrifugal separator system 1 utilising the second exchangeable separation insert 6′. That this, the subsequent or parallel fermentation period may be followed by steps 110-114 of the method 100 being performed.
According to embodiments, each of the first and second batch of liquid feed mixture may comprise solid matter. The first batch of liquid feed mixture may differ from the second batch of liquid feed mixture by at least one of: type of solid matter, concentration of solid matter, and/or content of the separated first light phase and content of the separated second light phase.
In embodiments wherein the liquid feed mixture is a cell culture mixture, the solid matter corresponds to the cells of the cell culture mixture. The light phase is the liquid of the cell culture mixture with cells removed. The heavy phase contains the separated cells and a small amount of liquid.
The fermentation in the fermenter tank may for example be for expression of an extracellular biomolecule, such as an antibody, from a mammalian cell culture mixture. The extracellular biomolecule may be extracted from the separated light phase in subsequent process step/s. In other processes the cells of the cell culture mixture may be, or may contain, the sought-after substance from the fermentation in the fermenter tank. The cells or the substance may be extracted from the separated heavy phase in subsequent process step/s.
Thus, the first batch of liquid feed mixture differing from the second batch of liquid feed mixture by type of solid matter may be by different types of cells of the first and second cell culture mixtures. The first batch of liquid feed mixture differing from the second batch of liquid feed mixture by concentration of solid matter may be by different concentrations of cells, of the same or different kinds. The first batch of liquid feed mixture differing from the second batch of liquid feed mixture by content of the separated first light phase and content of the separated second light phase may be by a difference in extracellular biomolecule.
According to embodiments, following the separating step 114, the second exchangeable separation insert 6′ may be removed from the inner space 26 of the rotatable member 16, and a further first exchangeable separation insert 6 or a further second exchangeable separation insert 6′ may be provided and mounted in the inner space 26. Alternatively, further kinds of exchangeable separation inserts with further differing separation capacities may be provided and mounted in the inner space 26.
It is to be understood that the foregoing is illustrative of various example embodiments and that the invention is defined only by the appended claims. A person skilled in the art will realize that the example embodiments may be modified, and that different features of the example embodiments may be combined to create embodiments other than those described herein, without departing from the scope of the invention, as defined by the appended claims.
| Number | Date | Country | Kind |
|---|---|---|---|
| 20200087.3 | Oct 2020 | EP | regional |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2021/075919 | 9/21/2021 | WO |
