UNIVERSAL ROTOR FOR ALL SYSTEMS EXPOSED TO FLUID IMPACT AND CENTRIFUGAL ACCELERATION

Description

Technical field

[0001] The present invention relates to a universal rotor for all systems requiring fluids to be subjected to centrifugal accelerations, this rotor being intended to carry out all operations requiring the circulation of single-phase or multi-phase fluids, for the purpose of chemical and biochemical reactions, extractions, purifications, separations. Previous techniques

[0002] Apparatuses consisting of reactors for chemical and biochemical reactions, apparatuses for carrying out extraction operations, apparatuses for carrying out purification operations, and apparatuses for carrying out separation operations such as those carried out by centrifugal partition chromatography (CPC) have been well known for a long time. Documents WO 2016 / 055821 A1 and FR 2868165 A1 describe such prior art devices.

[0003] A first drawback of the prior art relating to operations carried out by centrifugal partition chromatography (CPC), extraction operations, purification operations, separation operations is due to the very design of the cells and the connecting channels connecting them in series, dug into the thickness of the discs which requires the installation of sealing gaskets, generally flexible, for example made of Teflon, between each disc, thus closing each cell and each channel according to the plane of the disc, therefore perpendicular to the main axis of each cell. Even if the cell has rounded shapes to facilitate the homogeneity of the dispersion with a view to a better exchange of materials between the two phases, the joint planes create right angles, or even acute angles, with the cell, due to the elasticity of the gasket which is partially inserted into the cells, which is not conducive to a homogeneous dispersion of the liquids, and therefore constitutes a major drawback.Finally, these flexible joint planes have, on the one hand, a certain porosity which leads to adsorption of certain molecules and then to desorption, which can limit the purity of the molecules of interest. On the other hand, they are subject to continual pressure variations of the liquids, deform over time and modify the geometry of the cells, resulting in aging of the joints, even if by any means we try to limit this aging.

[0004] A second disadvantage of the prior art relating to centrifugal partition chromatography (CPC) and extraction operations, purification operations, separation operations is due to the fact that the cells are connected to each other by a ribbon-shaped channel. It is easily calculated and verified that this shape of conduit, for a given section, produces a pressure drop much higher than that caused by a conduit of the same cylindrical section or of very similar geometry. To limit excessive pressures and in certain cases for reasons of machining difficulty, it is necessary to increase the thickness of these rectangular channels, therefore to increase the excessive volumes of said channels. These do not enter into the separation process through which the products during separation pass but increase the passage times and consequently the separation time and the consumption of solvents.

[0005] A third disadvantage of the prior art relating to centrifugal partition chromatography (CPC) and relating to extraction operations, purification operations, separation operations, is due to the fact that the mass and therefore the heat capacity of the rotor discs is not favorable to precise thermal regulation and more particularly to a thermal time constant as short as possible, particularly during operation in a reactor. The temperature of the fluids passing through the cells during the reactions, which may be endothermic or exothermic, can become largely detrimental to performance or even compromise safety if it is not strictly controlled.

[0006] A fourth disadvantage of the prior art relating to centrifugal partition chromatography (CPC) and relating to extraction operations, purification operations, separation operations, is due to the fact that with the rotors of the prior art, if the injected volume is increased beyond a certain value relative to the volume of the cells, a hydraulic shock phenomenon appears, commonly called "water hammer" which partially or totally destroys the hydrodynamic balance of the first cells, an effect which propagates to the last cells of the rotor and puts an end to the manipulation.

[0007] According to the techniques used until now, the rotors used in centrifugal partition chromatography (CPC) devices for the separation of components, comprise in their thickness and over their entire periphery a succession of cells arranged in a radial or oblique direction placed in series by a set of fine sinuous pipes connected to the inlets and outlets of each cell, the circuits of all the discs communicating with each other. The rotation of the stack creates a significant centrifugal acceleration field which makes it possible, for example, to maintain a liquid phase, called stationary, fixed, while a mobile phase percolates said stationary phase in so-called ascending mode if it is lighter than the stationary phase, or in so-called descending mode if it is heavier.In this type of device consisting of the serial interconnection of one or more chains of cells, the separation of the constituents of a charge in liquid solution comprising at least two constituents with different partition coefficients is carried out, such that they are carried along at unequal speeds by the mobile phase, which may be one or other of the liquid phases.

[0008] In fact, the rotors used in these known centrifugal partition chromatography (CPC) devices can be used in all applications requiring a centrifugal acceleration field and very good thermal regulation, among others to carry out purifications, separations, extractions with conventional solvents but particularly with CO2 in liquid or supercritical phase in centrifugal partition chromatography (CPC), techniques in which the molecules are purified and / or separated between two liquid phases, taking place in each cell, the mass transfer being favored by a good dispersion of the mobile phase arriving through the inlet channel of each cell.

[0009] When one wishes to build an industrial production apparatus, the person skilled in the art knows how to make the change of scale from separations carried out on a laboratory apparatus, that is to say, the number of cells, the volume of said cells, the flow rates of the mobile phase, the hydrostatic pressure generated, etc.

[0010] However, these parameters being relatively numerous and the measurements tainted with errors, will mean that the constructed device will function, but will neither be exactly at its optimum nor simply modifiable with prior art technologies.

[0011] Prior art devices consist of rotors whose number and volume of cells are defined before their construction and cannot be modified afterward, which prevents optimization possibilities for the different applications that may arise. To simplify, we will remain in the field of CPC separation, namely: if a user has a prior art rotor consisting of 500 cells, and he wishes to perform a given separation, for which the optimum is 500 cells, everything works for the best. However, for another separation in which he would need 1000 cells, said separation will only be partially resolved.Conversely, for another separation to be carried out with the same 500-cell rotor, while a 200-cell rotor would be optimal, the separation time will be multiplied by approximately 2.5, which results in a loss of time, increased solvent consumption and a reduction in productivity in the same ratio.

[0012] The present invention provides in itself, with regard to the rotors used for separation, more particularly in centrifugal partition chromatography (CPC), significant advantages compared to known centrifugal partition chromatography (CPC) devices, if only through their possibility of duplication but also for their ease of use and their ease of adaptation to operating conditions.

[0013] Indeed, the present invention consists of a universal rotor allowing: on the one hand to separate from liquid mixtures one or more components having different partition coefficients, and on the other hand to carry out chemical reactions between several components.

[0014] The rotors according to the invention can also be applied to the two successive implementations mentioned above, namely a reaction between two or more compounds, followed by a separation of the desired product in the reaction mixture resulting from the chemical reaction or a separation of a component contained in a mixture followed by a chemical reaction of the component obtained with another product.

[0015] The present invention can therefore be considered for each of these two applications and for successive use of the two applications. Summary of the invention.

[0016] The present invention relates to a universal rotor for operations requiring subjecting fluids to centrifugal accelerations in the context of operations requiring the circulation of single-phase or multi-phase fluids, for the purpose of chemical and biochemical reactions operating in particular continuously, purifications, extractions, separations, centrifugal partition chromatography (CPC), liquid-liquid extractions among others.

[0017] The rotor according to the invention is capable of being implemented as chemical and / or biochemical reactors, liquid-liquid extractors, purification operations, centrifugal partition chromatographs (CPC), among others.

[0018] In fact, liquid or solvent phases can consist, among others, of organic, ionic, NADES (Natural deep eutectic solvent), CO2 in liquid or supercritical phase circulating in cells connected to each other by channels, and apply, in different fields, such as those of chemical and biochemical reaction, extraction, purification of separation.

[0019] The present invention relates to a universal rotor for operations requiring subjecting fluids to centrifugal accelerations involving the circulation of single-phase or multi-phase fluids, for the purpose of treatments consisting of purifications, extractions, separations, centrifugal partition chromatography (CPC), liquid-liquid extractions, chemical and biochemical reactions, in which: the rotor is formed of one or more disks stacked on top of each other, each of said disks consists of a support in which is inserted a crown (A1) consisting of the assembly of one or more circular sectors, in the case of a single circular sector, a space is arranged between the two ends of the single circular sector. in the case of several circular sectors the space is arranged between the ends of two contiguous circular sectors. a connecting connector is inserted in said space, the connecting connector has the bypass means consisting of channels necessary for the liquid phase entering through the inlets in said connecting connector to be guided to travel through said network of cells to the outlets of said connecting connector, which outlets are in direct contact with the inlets of the connecting connector of the following disk and so on.

[0020] According to one embodiment of the invention, the rotor is formed from a single circular sector comprising a network of successive cells interconnected with each other by channels and arranged in a more or less median plane of its thickness, characterized in that there is at least one gap between its two ends to place there in a sealed manner a connecting connector, said connecting connector comprising at least one inlet and at least one outlet intended to allow respectively the entry of a liquid mixture into networks of cells and the exit of said mixture from the channels of the cells.

[0021] According to another embodiment of the invention, the circular sectors are made from two circular half-sectors, each of which is the mirror image of the other, both comprising on their mirror plane, the half-cells and half-channels, the two half-sectors being assembled in a sealed manner, preferably by diffusion welding, face to face, to become a circular sector.

[0022] According to another embodiment of the invention, the circular sectors are preferably produced in a single piece, for example directly by additive construction.

[0023] According to yet another embodiment of the invention, the single circular sector comprises in its thickness one or more circular conduits of more or less rectangular section, in this case three, delimited by concentric walls and arranged in such a way that the average radii of each of said circular conduits are substantially arranged respectively on the same average radii of those of the circular networks of said corresponding cells, in order to circulate therein a temperature control fluid or thermostatting fluid in the most identical way possible for each of said networks of cells.

[0024] According to one embodiment of the invention, the connecting connector comprises the necessary branches so that the incoming temperature control fluid or thermostatting fluid passes through all the conduits connected in series of each of the circular sectors constituting the crown in question and then, guided by said connecting connector, passes to the connecting connector of the next disc to pass through the conduits connected in series in the same way, and so on until the rotor outlet.

[0025] According to yet another embodiment of the invention, said connecting connector also comprises an inlet and an outlet allowing the inlet and outlet of a temperature control fluid or thermostating fluid so that it flows through the temperature control conduit(s) or thermostating fluid.

[0026] According to one embodiment of the invention, the cells and channels have walls that are as thin as possible, and are provided with fins, said fins themselves being integral with the internal walls of the circular sector.

[0027] According to another embodiment of the invention, the connecting connector comprises at least one inlet and at least one outlet intended to allow respectively the entry of a liquid mixture into the cell networks and the exit of said mixture from the cell networks, such that between the outlet and the inlet, the liquid phase passes through all the cells and channels of the disc in question.

[0028] According to another embodiment of the invention, the connecting connector (B6) can be installed in place of the connecting connector (A6), in which case a one-way or multi-way valve with a two-position ball valve, "ON" and "BYPASS", is added, making it possible to choose the position such that in the "ON" position of said valve a liquid phase entering for example at (31) is directed from said valve to the inlet of the contiguous circular sector at (13) to travel through the entire network of cells of the disc and arrive at (14) of the last circular sector then at (35) then at (36) of said connecting connector, to enter the connecting connector of the next contiguous disc but, if the ball valve of this valve is in the "BYPASS" position, the liquid phase entering at (31) is directed directly to (36) without traveling through the cells of the disc concerned, the latter being short-circuited,which allows the user to adjust the number of cells for each of their various applications in steps of the number of cells contained in a disk.

[0029] According to yet another embodiment of the invention, each circular sector of a crown is formed from two superimposed circular half-sectors, face to face, or from a stack of such superpositions, each of these half-sectors comprising half-cells whose angles (20) are replaced by fillets forming rounded edges.

[0030] According to another embodiment of the invention, to increase the productivity of said rotor, in CPC mode, in ascending mode, the first "n" cells of said rotor have decreasing volumes according to a function to be determined ranging from (V7) to (V) with (V7>V), V being the constant volume of the majority of the cells of said rotor.

[0031] The present invention also relates to the use of the universal rotor in operations requiring subjecting fluids to centrifugal accelerations in the context of operations requiring the circulation of single-phase or multi-phase fluids, for the purpose of purification, extraction, separation, centrifugal partition chromatography (CPC) and liquid-liquid extraction treatments;

[0032] The present invention also relates to the use of the universal rotor in operations requiring fluids to be subjected to centrifugal accelerations in the context of operations requiring the circulation of single-phase or multi-phase fluids, for the purpose of chemical and / or biochemical reactions. Brief description of the figures.

[0033] The invention will be better understood by reading the following description of the preferred embodiments, given as a simple figurative and non-limiting example, and accompanied by the following figures: [ FIG. 1 ] schematic representation, in exploded view, of a crown (A1) consisting of four circular sectors (2 to 5) and a connecting connector (6) according to the invention. [ FIG. 2 ] schematic representation in exploded view of a crown (A1) inserted in its centering cup whose axis is (8) to form a disc (A2); [ FIG. 3 ] schematic representation in exploded view of an example of a circular sector (A3) by the assembly of two half-circular sectors (10 and 11) to form a circular sector according to the invention; [ FIG. 4] schematic representation of an example of a static connection connector (A6) between two circular sectors contiguous to two networks of cells of different volumes, as well as a path (37-38) for the circulation of a temperature control fluid in the rotor according to the invention; [ FIG. 5 ] schematic representation of another example of a connecting connector (B6) with a two-position valve between two circular sectors adjacent to two networks of cells of different volumes, as well as a path for the circulation of a fluid for thermal regulation of the temperature of the rotor according to the invention; [ FIG. 6A ] schematic representation in three sections of an example of a rotor according to an embodiment of the invention, limited to 6 discs so as not to overload the figure showing in detail the different fluid paths of the mobile and thermal phases; [ FIG. 6B] schematic sectional representation of two two-position valves installed in the connecting connector along a plane perpendicular to their axis and passing through one of the distribution channels; [ FIG. 7 ] schematic representation of an example of construction of a rotor mounted on a vertical axis according to an embodiment of the invention; [ FIG. 8 ] schematic representation of an example showing the possibility of simply adding or removing discs from the rotor according to the invention in order to adapt its geometry to various applications, to carry out after-sales service or for any other reasons. [FIG. 9] schematic representation of an example of cell arrangements in a CPC rotor allowing the injectable volume to be increased. Description of embodiments

[0034] There figure 1shows an example of a crown (A1) consisting of four circular sectors (2, 3, 4, 5) and a connecting connector (6) of a rotor according to the invention.

[0035] THE figures 2 , 3 , 4, 5 And 6 described in more detail below, show one or more concentric networks of cells formed on the surface of half-circular sectors, their face-to-face assembly forming a circular sector (A3). These cells are interconnected in series by channels figure (3 ).

[0036] The crown (A1) represented figure 1 , comprises a set of open circular sectors (2 to 5) each having two ends and comprising at least one network of cells concentric to the axis of said circular sector, formed on a plane more or less median of its thickness. In the example shown in figure 1, the crown (A1) - (2 to 6) is formed of several distinct circular sectors, in this case four distinct circular sectors (2 to 5), each comprising a part of the network(s) of cells which are assembled two by two in a sealed manner so as to ensure the continuity of this network of cells connected to the connecting connector (6), which will be described in more detail below. The number of circular sectors can of course vary. In particular, the device can very well comprise a single circular sector which then comprises the entire network(s) of cells of the crown (A1).

[0037] In the case of several circular sectors (2 to 5), the two ends of the circular sectors (2 and 5) correspond to one end of the first circular sector (2) not connected to another circular sector, and one end of the last circular sector (5) also not connected to another circular sector.

[0038] In the case of a single circular sector, its two ends correspond to those of an assembly of several circular sectors.

[0039] The connecting connector (6) is interposed in a sealed manner between the two ends of the assembly of circular sectors (2 to 5). This connecting connector allows, in one embodiment of the invention, to bring the mobile phase and the sample to be injected into the crown (A1), then after they have passed through all the cells, to direct them into the connecting connector of the adjacent crown which in turn performs the same operation, and so on up to the last crown of the rotor formed by their stack. The various components of the sample entrained by the mobile phase, in the case of a CPC separation application for example, are separated during the journey in the cells and channels and then are detected and / or collected by one of the means well known in liquid / liquid centrifugal partition chromatography (CPC) or for applications carried out in other fields.The connecting connector may include other functions according to the invention which will be presented in the detailed description of the . Figures 4 and 5 .

[0040] There figure 2shows in exploded view a non-limiting embodiment of the assembly of the crown (A1) in its centering cup to form a rotor disc (A2). The mechanical tolerances between the inner diameter of the centering cup and the outer diameter of the crown (A1) must be such that the crown (A1) is firmly clamped by the centering cup (7) in order to ensure good mechanical strength and good sealing between the different parts making up the crown (A1). The insertion operation can for example be carried out by a thermal expansion process by temperature difference between the two parts to be assembled. Openings (9) are provided on the plane of the centering cup to allow the possible extraction of the crown (A1) by press.The central bore (8) of the centering cup has a sliding fit having minimal play on the shaft (85) of the rotor in order to center it as best as possible and to allow it to slide on said shaft of said rotor. figures (7 and 8 ). Each rotor disc (A2), previously filled with liquid, is statically and dynamically balanced up to accelerations slightly higher than the maximum acceleration planned during the design of the device.

[0041] There figure 3shows in exploded view a circular sector (A3) according to an embodiment of the invention, consisting of a half-circular sector (10) and a half-circular sector (11), each being the mirror image of the other with respect to the plane (28) of said half-circular sector (10); after their face-to-face assembly in a sealed manner, this constitutes a circular sector (A3). In the present exemplary embodiment of the invention, the circular sector comprises two networks of twenty cells each, one of which is made up of cells (26) of volume (V) and the other of cells (27) of volume (8V). For a better understanding of the figures, it will be noted for example that a cell (27) is made up of the assembly of a half-cell (27A) made on the half-circular sector (10) and a half-cell (27B) made on the half-circular sector (11), the same is true for the channels.The said half-cells are not necessarily the image of one another because they can be asymmetrical, provided that at the contact plane (28) between the two half-sectors, they have rigorously the same profile.

[0042] Their respective connecting channels (18 and 19) (section along BB) have sections adapted to the expected flow rates necessary for the operation of the cells. These two circular half-sectors are positioned face to face as precisely as possible, for example by two pins (22) inserted in a slightly tight fit in two cylindrical holes of the circular half-sector (10). In the mirrored circular half-sector (11) two sliding fit holes are made, one of which is cylindrical and the other oblong corresponding to the positions of the pins inserted in the circular half-sector (10) in order to carry out an unstressed assembly of the two circular half-sectors, for example by diffusion welding.Pins made from the same grade of material as that used for the manufacture of the circular half-sectors, or a material with a coefficient of thermal expansion as close as possible, will preferably be used, in order to avoid possible mechanical stresses causing deformations due to thermal expansion during the welding operation. The entry of the mobile phase and the sample, when operating in descending mode in the circular sector (A3) is carried out through the inlets (13) or (15) and through the inter-sector seals (17) corresponding to the chosen cell network. The corresponding outlets are respectively at (14) and (16).The flat seal (23) ensures the seal between the circular sectors and the connecting connector (6) for the possible circulation of a thermal fluid inside (12) the two circular half-sectors which are in this case made up of three separate conduits (12A, 12B and 12C), separated by walls (12F, 12AB, 12BC and 12D), each being centered respectively on the same circles as each of the three cell networks. These cells have thin walls and are equipped with fins, which makes it possible to reduce the thermal resistance between the temperature control fluid or thermostatting fluid and the liquid phases passing through the cells and channels while increasing the mechanical resistance of said cells, by their mutually perpendicular arrangements.

[0043] According to the invention, rounded or "fillets" (20) are produced, shown in detail in the enlarged view of the half-cell (27A), in place of the sharp angles of said cells, the latter considerably degrading the hydrodynamic operation and consequently the performance of the device. This method can be advantageously applied to all conceivable cell geometries, whether symmetrical or asymmetrical and whatever their various applications. The connecting channels (18) and (19) between the cells are advantageously of circular section, also for good hydrodynamic operation. However, in the case of conventional mechanical machining of said channels, for reasons of ease of machining and / or surface condition, it will be possible to give them a polygonal section, for example square, taking care to round all the angles in order to obtain a section as close as possible to a circular section.

[0044] There figure 4presents an embodiment of the fixed configuration connection connector, in this case (A6), comprising one or more inlets for the liquid phases (29 & 31) and corresponding outlets (30 & 32), respectively connected in descending mode to (15 & 13) of the contiguous circular sector (A3) of said connection connector. The mobile phase passing through the network of selected cells (26 or 27) and channels (18 or 19) of said circular sector, exits at (16) or (14), are connected to the inputs (15 & 13) of the second circular sector, and so on up to the last circular sector of the contiguous crown of the second face of said connecting connector, the mobile phase entering at (33) or (35) to exit at (34) or (36) of said connecting connector and enters at (29) or (31) of the adjacent connecting connector of the following disc and so on from disc to disc up to the last disc of the rotor, the outputs (34) or (36) being connected to the outputs (54) or (56) of said rotor.

[0045] When the inlet / outlet of a cell network is chosen, it is recommended to tightly close the other network with two plugs at the rotor flanges, in order to avoid any loss of liquid phase during operation, which could lead to a dynamic imbalance of the rotating rotor.

[0046] For better understanding, the link connectors (A6 & B6) have been shown, Figures 4 and 5 between two circular sectors, the one placed on the left in semi-transparent form to better explain the example of realization, in this case comprising fins and concentric walls (12AB & 12BC), the circular sector placed on the right, non-transparent to show the connections between said connecting connectors and the networks of channels and cells of the circular sectors (A3), (2 & 5).

[0047] Said link connector (A6 or B6) ( Fig. 3 , 4 and 5and section according to (C - C) has an inlet (37) for injecting the temperature control fluid or thermostatting fluid which is guided by the channel (37B) into the conduit (12A) of the first circular sector, which is delimited by the concentric walls (12F & 12AB), it travels through said channel of the successive circular sectors to the connecting connector, passes into the channel (37C) of said connecting connector, then enters the conduit (12B), delimited by the walls (12AB and 12BC) which it travels through to the connecting connector which leads it by its channel (37D) to the inlet of the conduit (12C) delimited by the concentric walls (12BC and 12E),runs through said conduit to the connecting connector and exits through the connection (38) arranged in the same axis as (37) and on the opposite face which is adjacent to the inlet (38) of the connecting connector of the disc following the stack and this up to the outlet of the last disc of the rotor which conducts said temperature control liquid or thermostatting fluid to the outlets (58 or 59).,

[0048] There Figure 5 presents a second major embodiment according to the invention of the connecting connector (6), in this case (B6). It has all the same functions as those of the connecting connector (A6) of the figure 4 and the same reference numbers, to which a valve (42) has been added, for example of the ball type (41) with two positions, Run and Bypass.

[0049] In the Run position, the mobile phase enters the connecting connector at (29 or 31) to be conducted by the valve at (30 or 32) to enter at (15 or 13) of the first contiguous circular sector, then travels through the entire chosen network of the disc considered up to the inlets (33 or 35) and outlets (34 or 36) of said circular sector and enters the adjacent connecting connector of the next disc.

[0050] In the Bypass position, the mobile phase that had previously filled the relevant cell network is trapped there. The mobile phase entering (29 or 31) of said connecting connector is directed directly by the valve towards the outlet (34 or 36) of said adjacent connecting connector of the next connecting connector in the stack. This mode allows the user, by turning the valve (41) a quarter turn in one direction or the other using a screwdriver inserted in the slot (43), to adjust the number of active cells of the rotor in steps of the number of cells contained in a disc. The operation of this major mode of the invention is shown in more detail with the presentation of the Figures 6A and 6B following.

[0051] There Figures 6Apresents a top view of the rotor according to the invention showing the disc selection valves then in three sections (E1, E2 and E3) as a non-limiting example of a rotor according to the invention, formed of only 6 discs (D1, D2, D3, D4, D5 and D6), so as not to overload the figure.

[0052] As a non-limiting example, the present disc comprises two independent concentric networks of 80 cells, each of the two networks being made up of cells of different volumes and connecting channels whose respective sections are adapted to the flow rates required by said cells. As an indication and non-limiting example, the small cells have, in the present example, a volume V and the other cells have a volume 8V.

[0053] The link connectors (6), whether they are of fixed configuration (A6 Fig. 4 ), or associated with a switching valve (B6 Fig. 5 ), are directly interchangeable.

[0054] The cut (E1) is made according to a plane defined by a generator of the rotor cutting the axes of the valves (41) and the axis of the rotor.

[0055] The section (E2) is made along a plane perpendicular to the section (E1), passing through the axis of the channels crossing the switching valves hydraulically connected to the inlets and outlets (56 & 57) and / or (54 & 57) depending on the network used.

[0056] The section (E3) is made along a plane perpendicular to the section (E1) and passing through the axis of the inlets and outlets (58 and 59) of the temperature control fluid or thermostatting fluid.

[0057] The E1 cupshows an overview including the double-channel ball valves adapted to the two cell networks of different volumes (V and 8V) of the present embodiment. For its use, the network corresponding to the volume of the chosen cells is selected, for example by connecting the arrival of the mobile phase in descending mode to the inlets (56) the outlet (57) then being that of the rotor which will be connected to a detector and a fraction collector, for example. It is recommended to connect a plug at (54) and (55), to prevent the phase located in the corresponding cell network from escaping, in order not to risk a dynamic imbalance of the rotating rotor. This section (E1) also shows the inlet and outlet (58 and 59) intended for the circulation of a temperature control liquid or rotor thermostatting fluid.

[0058] The E2 cupshows more precisely the hydraulic operation of the "RUN"-"BYPASS" valves which are shown, on a larger scale in figure (6B ) those installed on the discs (D4 and D5). It is observed that the valves (41) of the rotor discs are arbitrarily positioned in "RUN" for the discs (D1, D2, D3, and D4) and in "BYPASS" for the discs (D5 and D6), as an example illustrating the operation according to the invention in which it is desired to use only 4 discs of active cells, i.e. 320 active cells out of the 480 of the present rotor.

[0059] The E3 Cupshows the plane parallel to section E2 and passing through the axis of the connections (58-59). The temperature control liquid or thermostating fluid enters for example through the connection (58), then arrives at the inlet (37) of the first connecting connector (A6 or B6). The diverter (60) directs it in the direction of the arrows towards the temperature control channel or thermostating fluid (12A) of the contiguous circular sector. After the temperature control liquid or thermostating fluid has passed through all the conduits (12A, 12B & 12C) of the circular sectors of the disc, arrives from (12C) to be directed at (38) of the diverter (60) of the connecting connector and passes directly from the outlet (38) to the inlet (37) of the adjacent connecting connector of the next disc and this until it arrives at the outlet (59) of the rotor.

[0060] There Figure 6Bshows in detail the path of the mobile phase coming from the outlet (34 or 36) of the disc (D3). It enters at (46) of the valve of the disc (D4) positioned in "RUN", then is directed by (45) to (47), inlet of the cell network of said disc (D4), then leaves at (43). It travels through the channel (45), arrives at (49), crosses the connection (49 / 50), then the channel of the valve (44) of the valve (D5) in the "BYPASS" position, to leave directly at (53) said outlet being connected to the inlet (29 or 31) of the connection connector of the adjacent disc (D6), which being also in the "BYPASS" position leads it directly to the outlet (55 or 57) of the rotor.

[0061] In this example, the mobile phase therefore travels through 320 cells of the rotor which has 480. Rotors can be made with many more cells to broaden the field of applications. It is understood from this example that the number of cells used in such a rotor can be modified in steps of a number of cells corresponding to the number of cells contained in each disc, by turning the valves (41) of the valves (42) a quarter turn and therefore making it possible to operate with 80, 160, 240, 320 or 400 cells of such a rotor, depending on the needs of the separations to be carried out. If the light mobile phase is connected to the inlet (57), the path of the cell networks remains the same but in ascending mode.

[0062] There figure 7presents an embodiment of the invention in which the rotor is formed from a stack (95) of discs (A2), and in which the rotation shaft (85) is at one end held in a vertical position by a suitable assembly and arranged in the cylinder (89). A motor (90) provided with a toothed pulley, rotates said rotor whose axis is also provided with a toothed pulley, the two toothed pulleys being mechanically coupled by a toothed belt (94) held in tension by an eccentric tensioner (97). Each end of the shaft (85) is equipped with a hydraulic rotating joint (88) which allows the mobile phase and the temperature control liquid or thermostatting fluid to enter and exit the rotor without retention volume.

[0063] These rotating joints must be adapted to the pressures and rotation speeds involved and must be easily accessible in order to simplify maintenance operations, cleaning, joint changes, after-sales service, etc.

[0064] A nut (86) provided with a bore to receive a spring (87), is screwed onto the shaft (85) of the rotor so that said spring (87) ensures sufficient permanent pressure to guarantee the sealing of all the joints of the discs of the stack constituting the rotor and so that the assembly is mechanically homogeneous and stable. The frame carrying this mechanical assembly is fixed to the device by shock absorbers (92) provided for this purpose, to which are added safety fixings and a mechanical lock for transport, meeting the standards in force.

[0065] There figure 8presents in detail an example of a non-limiting embodiment according to the invention of a rotor, for example a production rotor, consisting of a stack or superposition of (12) discs (A2), illustrating the ease with which it is possible to modify the number of discs of said rotor, and which proves to be particularly applicable on production devices. The latter frequently working long term on the same application do not necessarily need to be optimized frequently. However, the embodiment according to the invention comprising a "RUN-BYPASS" valve installed on each disc of the rotor can prove to be very effective if the objective of the device in question is to carry out various operations on demand, in synthesis, purification, extraction, etc., the user being able to quickly optimize the device as close as possible to the optimum, using said valves (42) for each of its various applications.

[0066] For the calculation and construction of a production device intended to carry out a given application in the long term, the calculations and experiments of change of scale, resulting from results of measurements carried out on laboratory devices, preferably equipped with said "RUN-BYPASS" valves on each disc according to the invention, should save time and improve accuracy.However, since the measurements may be somewhat tainted by errors, the industrial rotor constructed on these bases may not be exactly at its optimum, a defect which can be easily corrected thanks to the technological flexibility of the invention, due to the fact that it is possible to add or remove (one) or more disc(s) allowing the performance to be optimized in real conditions and by adjusting the number of cells required, an operation simplified thanks to the construction of said disc by the assembly of circular sectors, said circular sectors being able to comprise more or fewer cells on demand.

[0067] View A of the figure (8) has said rotor (A5) consisting of twelve discs according to the invention and which have all been previously and independently balanced. For some reason, it is desired to remove one or more discs, in this case (6). To do this, the upper rotating joint (88) is dismantled, then the nut (86) and the connection tubes (91) are unscrewed and the spring (87) is removed. We see in figures (8A and 8B) that we can remove the flange (93) then the 6 discs one by one in (8B), to arrive at (8C) in which we see the rotor consisting of the flange (93) placed on the stack then consisting of six discs, then the spacers (98) sliding on the shaft, the lengths of which will preferably be in binary progression so as to limit their number, the smallest spacer having a height equal to the thickness of a disc, then the nut (86) and the rotating joint (88).

[0068] This embodiment presented with a vertical axis does not exclude an assembly carried out with a horizontal or articulated rotation axis allowing the part supporting the rotor to be moved angularly. Those skilled in the art will know how to use various means known in traditional mechanics to carry out such an assembly.

[0069] Figure 9 shows a non-limiting example of another embodiment of the invention making it possible to increase the injectable quantity of sample to be treated with a rotor in CPC operation, consisting of a set of identical cells of the same volumes (V).

[0070] Before the entry of said rotor, when one wishes to operate in ascending mode (ASC), a network of cells is added whose volumes have progressive values and, to simplify the description, the first (V7) has a volume (n) times greater than the volume (V) of the cells of said rotor. Between (V7) and the first cell (V) of the network of identical cells, a certain number of cells (V6, V5, ....V1) are interposed, according to a law of variation of the volumes to be determined. In said figure, to simplify it, this variation is presented in a non-limiting manner according to a linear function. It is the same when one operates in descending mode (DSC) in which the same values of the volumes of the cells are represented as an example.

[0071] It is relevant to use discs equipped with valves (42) according to the invention making it possible to connect or not connect all or part of the discs of the rotor comprising the networks of cells of different volumes to adjust the number according to the needs of each application.

[0072] The rotor according to the invention is used in centrifugal partition chromatography (CPC) operations allowing the separation of a compound contained in a solution formed of several components. The separation of the sample is based on the partition coefficients specific to each of the sample components between the mobile and stationary phases. The partition coefficient determines the affinity of each molecule in the mobile and stationary phases and therefore the speed at which each molecule moves in the system. At the end of the purification process, the automated fraction collectors retain all the fractions selected according to the program parameters.

[0073] The rotor according to the invention can be used not only in separation operations, but also for reaction operations between components, thus acting as an intensified chemical and / or biochemical reactor due to the excellent mixing occurring in each of the cells. The advantage of the system is to obtain a piston reactor behavior, which is recognized to give the best performances, considering said universal rotor as a succession of perfectly stirred reactors, constituted by the cells. The reactions can be carried out in single-phase or two-phase, which is all the more relevant when the reactants and the product are in different phases.

[0074] This invention is a departure from traditional batch processes, the jacketed stirred tank, which is the most widely used tool with more than 50% of chemical production units worldwide. Reactor engineering has two key elements: reaction kinetics and reactor design. Reactor design must be designed so that the reaction proceeds at its intrinsic rate, that is, if there is perfect mixing and mass transfer in the reactor. It often happens that in large stirred tank reactors, the reaction does not proceed at its intrinsic rate, because it is limited by the mixing in the tank, that is, the reactants are not perfectly mixed. In this case, it is said to be "mixing limited." The role of process intensification is to reduce or remove these limitations so that the reaction can reach its intrinsic rate.Thus, the goal is to ensure that the mixing and heat / mass transfer rates will be relatively fast compared to the fundamental kinetics of the process. High acceleration can be achieved for as long as necessary by operating in such a rotating system. Transposing chemical syntheses into reactors in which the phases have a plug-type flow then makes it possible to minimize the reaction volumes involved (safety of the installations and operators), to intensify the exchanges of matter (mixing, reaction, separation), to servo-control and control the temperature with good precision and to add warning systems in case of overshoot. Examples include the reduction of benzal-aldehyde to benzyl alcohol by homogeneous ruthenium catalysis, or the two-phase esterification reaction of oleic acid to ethyl oleate by a lipase (. Candida Antartica ).

[0075] Liquid-liquid extraction is a basic operation in process engineering. It involves transferring a solute (the molecule of interest) from a so-called "feed" phase to a so-called "extract" phase. The two phases are immiscible or partially miscible. Many examples exist in industry, for example, the production of antibiotics with an acid-base extraction cycle.

Claims

1. Universal rotor for operations requiring the submission of fluids to centrifugal accelerations involving the circulation of single-phase or multi-phase fluids, for treatments consisting of purifications, extractions, separations, centrifugal partition chromatography (CPC), liquid-liquid extractions, chemical and / or biochemical reactions, characterized in that: - the rotor is formed of a disc or several discs stacked on top of each other, - each of the said discs consists of a support (7) in which a crown (A1) is inserted, consisting of the assembly of one or more circular sectors (A3), - in the case of a single circular sector (A3), a space is arranged between the two ends of the single circular sector in the case of several circular sectors, the space is arranged between the ends of two contiguous circular sectors. - a connecting connector (A6 or B6) is inserted in the said space or spaces, - the connecting connector has the means of derivation consisting of channels necessary for the liquid phase entering through the inlets (31 or 29) in the said connecting connector (A6 or B6) to be guided to travel through the said network of cells (26 or 27) to outlets (36 or 34) of the said connecting connector, which outlets are in direct contact with the inlets (A6 or B6) of the connecting connector of the next disc and so on, until the outlet of the last disc connected to the outlet (55 or 57) of the said rotor.

2. Rotor according to claim 1, formed of a single circular sector comprising a network of successive cells interconnected by channels (18) and (19) arranged in a plane more or less median of its thickness, characterized in that there is at least one interval between its two ends to arrange a connecting connector (A6 or B6) in a sealed manner, said connecting connector comprising at least one inlet (31) and at least one outlet (32) intended to allow respectively the entry of a liquid mixture into the networks (13) of cells and the exit of said mixture of the channels (14) of the cells (27).

3. Rotor according to claim 1 or 2, characterized in that the circular sectors are made from circular half-sectors (10) and circular half-sectors (11), each of which is the mirror part of the other, all comprising on their mirror plane, the half-cells (26A, 26B) & (27A & 27B) and half-channels (18A & 18B) & (19A & 19B), the two half-sectors being assembled in a sealed manner, face to face, to become a circular sector (A3).

4. Rotor according to claims 1 or 3, in which each circular sector (A3) of a crown (A1), is formed of a stack of superimpositions each comprising half-cells (27A, 27B) whose angles (20) are replaced by fillets forming rounded edges.

5. Rotor according to one of claims 1 to 4, characterized in that the circular sectors are made in one piece, by additive construction.

6. Rotor according to one of claims 1 to 5, characterized in that the single circular sector (A3) comprises in its thickness one or more circular conduits of more or less rectangular section, in this case three, (12A, 12B and 12C), delimited by concentric walls (12F, 12AB, 12BC and 12E) and arranged in such a way that the average radii of each of the said circular conduits are substantially arranged respectively on the same average radii as those of the circular networks of the said corresponding cells, in order to circulate a temperature control fluid or thermostatization fluid in the most identical way possible for each of the said cell networks.

7. Rotor according to any one of claims 1 to 6, in which the said connecting connector (6) also comprises an inlet (37) and an outlet (38) allowing the entry and exit of a temperature control fluid or thermostatization fluid so that it travels through the temperature control conduit(s) or the thermostatization fluid.

8. Rotor according to claim 7, characterized in that the connecting connector (A6 or B6) comprises the necessary derivations so that the temperature control fluid or thermostatization fluid entering (37) passes through all the ducts (12A) to (12C) connected in series of each of the circular sectors constituting the ring in question, then, guided by the said connecting connector, passes to the connecting connector of the next contiguous disc of the stack and so on until the rotor outlet (58 or 59).

9. Rotor according to any one of claims 1 to 8, characterized in that the cells (26 & 27) have walls provided with fins (12A, 12B and 12C).

10. Rotor according to any one of claims 1 to 9, in which the connecting connector (A6) comprises at least one inlet (31) and at least one outlet (36) intended to allow respectively the entry of a liquid mixture in the cell networks and the exit of the said mixture of the cell networks, so that between the exit and the entry, the liquid phase travels through all the cells and channels of the disc in question.

11. Rotor according to any one of claims 1 to 10, characterized in that when the connecting connector is the connector (B6) in this case a valve with one or more channels (42) comprising the positions, "ON" and "BYPASS", allowing to choose the position such that in the "ON" position of the said valve (42) a liquid phase entering through the inlet (31), is directed towards the outlet (32) of the said valve then towards the inlet (13) of the contiguous circular sector to traverse the entire network of cells of the disc and arrive at the outlet (14) of the last circular sector then at the inlet (35) then at the outlet (36) of the said connecting connector, to enter through the inlet (31) of the connecting the next contiguous disc but, if the plug of this valve (42) is in the "BYPASS" position, the liquid phase entering through the inlet (31) is directed directly towards the outlet (36) without passing through the cells of the disc concerned, the latter being short-circuited, which allows the user to adjust the number of cells to each of its various applications by steps of the number of cells contained in a disc.

12. Rotor according to any one of claims 1 to 11, characterized in that, the "n" first cells of the said rotor have decreasing volumes according to a function to be determined ranging from (V7) to (V) with (V7>V), V being the constant volume of the major part of the cells of the said rotor, which makes it possible to increase the productivity of the said rotor, in CPC mode, in ascending mode.

13. Use of the universal rotor according to any one of claims 1 to 12, on devices allowing to circulate one or more liquids needing to be subjected to stable and / or variable centrifugal accelerations, at pressures which can be high and at precise and / or variable temperatures with short time constants, devices which can be used as a chemical and / or biochemical reactor and / or for extractions, separations and purifications in centrifugal partition chromatography (CPC), from the laboratory to the industrial scale and to any other device and application requiring to circulate one or more fluids, such as organic or non-organic solvents, ionic liquids, CO2 in liquid or supercritical phase and corresponding devices.

14. Use of the universal rotor according to any one of claims 1 to 12, in operations requiring the subjecting of fluids to centrifugal accelerations in the context of operations requiring the circulation of single-phase or multi-phase fluids, for purification, extraction, separation, centrifugal partition chromatography (CPC), liquid-liquid extractions15. Use of the universal rotor according to any one of claims 1 to 12, in operations requiring the subjecting of fluids to centrifugal accelerations in the context of operations requiring the circulation of single-phase or polyphase fluids, for chemical and biochemical reactions.