EP1379867A1 - Protective device for the chromatographic bed in dynamic axial compression chromatographic columns - Google Patents

Protective device for the chromatographic bed in dynamic axial compression chromatographic columns

Info

Publication number
EP1379867A1
EP1379867A1 EP02761925A EP02761925A EP1379867A1 EP 1379867 A1 EP1379867 A1 EP 1379867A1 EP 02761925 A EP02761925 A EP 02761925A EP 02761925 A EP02761925 A EP 02761925A EP 1379867 A1 EP1379867 A1 EP 1379867A1
Authority
EP
European Patent Office
Prior art keywords
bed
pressure
fluid
piston
column
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP02761925A
Other languages
German (de)
French (fr)
Inventor
Wilhelm Hauck
Harlene Marks
Jean Blehaut
Roger-Marc Nicoud
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Novasep Process SAS
Original Assignee
Novasep SAS
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Novasep SAS filed Critical Novasep SAS
Publication of EP1379867A1 publication Critical patent/EP1379867A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1809Controlling processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D15/00Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08Selective adsorption, e.g. chromatography
    • B01D15/10Selective adsorption, e.g. chromatography characterised by constructional or operational features
    • B01D15/20Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to the conditioning of the sorbent material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D15/00Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08Selective adsorption, e.g. chromatography
    • B01D15/10Selective adsorption, e.g. chromatography characterised by constructional or operational features
    • B01D15/22Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to the construction of the column
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N30/60Construction of the column
    • G01N30/6004Construction of the column end pieces
    • G01N30/6021Adjustable pistons
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N2030/022Column chromatography characterised by the kind of separation mechanism
    • G01N2030/027Liquid chromatography
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N30/50Conditioning of the sorbent material or stationary liquid
    • G01N30/52Physical parameters
    • G01N2030/522Physical parameters pressure
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N30/60Construction of the column
    • G01N30/6004Construction of the column end pieces

Definitions

  • the present invention relates to the protection of the chromatographic bed of chromatographic columns and in particular in columns with dynamic axial compression.
  • the column is generally filled with a solid product in the form of very fine grains, usually between 5 and 100 ⁇ m in size, forming the chromatographic bed.
  • the arrangement of the grains inside the column must be as homogeneous as possible and, moreover, empty volumes must be avoided between the chromatographic bed and the inputs-outputs of the column. It is known in the prior art to use columns with dynamic axial compression in order to ensure the existence of a compact bed, with no free space between the inlet-outlet distributors and the bed.
  • a chromatography device in the form of a column intended to contain a bed of adsorbent material.
  • the apparatus consists of a tube comprising a cover and a body sliding in the tube for exerting pressure in the tube.
  • the sliding body is a piston comprising at its head a porous plate permeable to fluids.
  • a suspension of particles of a material capable of constituting an adsorbent bed is introduced into the tube devoid of its cover, the piston being set back enough to allow the introduction of the suspension, without being necessarily in neutral.
  • the cover is adapted to the tube, then pressure is exerted on said suspension by means of the piston.
  • the liquid is discharged through the porous plates, and said particles are compressed between the piston and the cover.
  • This device makes it possible, in an exemplary embodiment, to reach the stage of compression of the bed chosen and the settlement of the particles desired when the sliding body has traveled 2/5 of the height of the column.
  • this device has the disadvantage of achieving imprecise settlement of the bed, since it is evaluated by the sole position of the piston along the tube.
  • a chromatography apparatus comprising a tube of which a part is intended for contain an adsorbent bed.
  • This tube has two end walls and a piston sliding longitudinally in the tube.
  • the piston marks between the two end walls a separation between a chamber chromatography containing the bed and an enclosure in which a pressure prevails so as to move the piston along the tube.
  • the particularity of this device is that the fluid contained in the enclosure is liquid to be chromatographed derived from the inlet pipe thereof.
  • a part of the liquid is diverted towards the enclosure by an enclosure conduit and the other part of the liquid is entrained towards the chromatographic chamber by a flow conduit passing through the enclosure and the piston.
  • the force exerted on the side of the enclosure on the piston is equal to the sum of the force on the piston caused by the flow of the liquid in the chamber to be chromatographed and the mechanical force of the bed on the piston.
  • This device allows, in addition to performing the elution step, to define the pressure exerted on the bed.
  • the piston has a constant cross-section but the pressure in the flow and enclosure conduits is regulated by pressure reducing valves.
  • the tabs can be tared so that the difference in pressures exerted by the flow of the liquid and by the liquid in the enclosure is adjusted to a set pressure on the bed.
  • the pressure in the flow and enclosure conduits is the same but the cross section of the piston varies.
  • the piston has two sections sliding in corresponding bores, the smallest section A being located on the side of the chromatographic chamber and the largest section B on the side of the enclosure. Due to the difference in surface area of the faces A and B of the piston, the force exerted at B is greater than the force exerted at A.
  • the sections of the piston can be chosen so that the difference in pressures exerted by the flow of the liquid and by the liquid in the enclosure is adjusted to a set pressure on the bed.
  • the apparatus described in the above document has various drawbacks. If a pressure drop occurs in the flow conduit, the pressure exerted on the piston by the liquid in the enclosure applies directly to the bed which can cause deterioration of the bed. In addition, the movements of the chromatographic bed not being monitored and the enclosure being unable to discharge liquid during the chromatography, this device cannot adapt the pressure exerted on the bed as a function of the movements of the latter. A deterioration of the bed can again follow. On the other hand, this system cannot be used in SMB (Simulated Moving Bed) or in NARICOL. In such configurations, the chromatography devices are mounted in a loop and the liquids injected into the beds alternate. In the apparatus described in EP-A-0 145 578, the same liquid is sent into the bed and into the enclosure, the alternation of injection of liquids generates a mixture of these.
  • SMB Simulated Moving Bed
  • the present invention relates to an improved chromatography device which overcomes the drawbacks of known devices. This device increases the efficiency of the chromatographic bed while protecting it.
  • the present invention relates to a chromatography device comprising:
  • the regulator is Integral Proportional Action (PI), Differential Proportional Action (PD) or Differential Integral Proportional Action (PID).
  • PI Integral Proportional Action
  • PD Differential Proportional Action
  • PID Differential Integral Proportional Action
  • the device further includes a first sensor which measures the flow pressure of the first fluid at the inlet of the column and a second sensor which measures the pressure in the chamber.
  • the first fluid flows through the bed from the piston towards the end of the column.
  • the first fluid flows through the bed from the end of the column towards the piston.
  • the piston sliding in the column is connected to another piston sliding in the chamber by a rod.
  • the second fluid is regulated by bypass by the regulator.
  • the invention also provides a set of devices as described above, associated in a loop.
  • the invention also relates to a method for separating at least two compounds from a first fluid, comprising the chromatography of said fluid in the device described above, the method comprises the steps:
  • the invention also relates to a method for adjusting the pressure on the chromatographic bed in the device described above, the method comprising the step:
  • FIG. 1 schematically represents a chromatography device 10 comprising a column 12 for performing the chromatography and a part of which is intended to contain a chromatographic bed 14 resting on an end wall 16.
  • the device 10 also comprises a jack 22.
  • the jack 22 comprises a movable piston 24 connected to one end of a rod 26.
  • the piston 24 delimits two chambers 28 and 30 in the jack 22.
  • the first chamber 28, or upper chamber is delimited between the piston 24 and the upper wall 32 of the cylinder 22.
  • the second chamber 30, or lower chamber is delimited between the piston 24 and the lower wall 34 of the cylinder 22.
  • the lower wall 34 marks the separation between the cylinder 22 and the column 12.
  • the rod 26 connected to the piston 24 is located in the lower chamber 30 and opens into the column 12 passing through the lower wall 34 of the jack 22. Appropriate seals will be used. ilises to seal between the chamber 30 and the column 12.
  • the other end of the rod 26 located in the column 12 is connected to a body 36.
  • the body 36 slides in the column 12.
  • the sliding body 36 is for example a piston. It comes to bear on the chromatographic bed 14.
  • the position of the actuator 22 relative to the column 12 is not limited to that described above. It is in fact possible to envisage placing the jack under the column so that the piston 36 is pressed upwards against the bed 14.
  • the liquid to be chromatographed is conveyed to the bed 14 and is discharged therefrom via flexible communication lines to the outside.
  • the piston 36 includes a conduit 20 provided with a first flow pressure sensor 45.
  • the wall 16 also has a conduit 18.
  • the liquid to be chromatographed reaches the bed 14 via the conduit 20 and then leaves via the of the conduit 18, after passing through the bed 14.
  • the sensor 45 makes it possible to measure the flow pressure of the fluid at the inlet of the column 12.
  • the liquid to be chromatographed can also circulate in the other direction. It then reaches the column 12 via the conduit 18, flows through the bed 14, then leaves the column 12 through the conduit 20.
  • the sensor 45 is placed on the inlet conduit 18.
  • the jack 22 is supplied by a propellant fluid circuit.
  • the cylinder 22 is a double-acting hydraulic cylinder.
  • the propellant fluid is then a hydraulic liquid.
  • a first conduit 38 connects the chamber 28 with a source of hydraulic fluid 44.
  • the conduit 38 includes a second pressure sensor 46.
  • a second conduit 40 connects the lower chamber 30 with the source of hydraulic fluid 44.
  • a conduit bypass 42 connects the conduits 38 and 40.
  • the bypass conduit 42 includes means for regulating the flow of propellant in the bypass. These means include an all or nothing valve (TOR) 48 and a regulation valve 50.
  • the regulation valve is controlled by a regulator 52 of the type with integral proportional action (PI), with differential proportional action (PD) or with proportional action. Differential Integral (PID).
  • PI integral proportional action
  • PD differential proportional action
  • PID Differential Integral
  • the liquids used in the device are separate fluids.
  • the first fluid that is to say the gas or the liquid to be chromatographed, is not the same as the propellant fluid, or second fluid, used in the jack 22. In other words, there has no bypass in the conduits of the first fluid to supply the jack 22.
  • the device is used in a mode of descent of the piston 36 to compact the chromatographic bed 14 in the column 12.
  • the column 12 is previously filled with the material forming the bed 14.
  • the hydraulic fluid is then sent to the chamber 28 of the jack 22 in order to lower the piston 36 into the column 12 until the piston 36 comes into contact with the bed 14 and ensures its compaction.
  • the digital valve 48 and the control valve 50 are closed.
  • the device allows the piston 36 to be raised to allow the bed 14 to be emptied from the column 12.
  • the hydraulic fluid is sent to the chamber 30 of the jack 22 in order to reassemble the piston 36.
  • the valve TOR 48 and the control valve 50 are also closed.
  • the device is used for the separation of at least two compounds from a liquid to be chromatographed. The process includes the steps:
  • the separation of the compounds is accompanied by the regulation of the pressure exerted on the bed 14.
  • Al is the surface of the piston 36 in the column 12 and A2 is the surface of the piston 24 in the chamber 28.
  • equation 3 shows that PI can be kept constant at the value of Pcl by varying Ph. To do this, it is necessary to measure the hydraulic pressure Ph and the flow pressure at entry of column 12.
  • the use of a regulator 52 of the PI, PD, PID type allows the pressure on the bed 14 to be adjusted according to the steps:
  • the separation process can then be completed by the step of introducing the hydraulic liquid into the chamber 28 and the step of regulating the pressure in the chamber 28.
  • the flow pressure drops to zero.
  • the regulator 52 derives the hydraulic fluid in the bypass duct 42 by opening the TOR valve 48 and by opening the control valve 50 at a percentage controlled by the regulator 52.
  • the hydraulic fluid sent by the hydraulic source 44 does not enter the chamber 28 but is diverted into the bypass duct 42. It is then evacuated towards the hydraulic source 44. In this way, the pressure in the chamber 28 is reduced, generating less pressure from the piston 36 on the bed 14.
  • the adjustment of the pressure exerted by the piston 36 on the bed 14 makes it possible to adapt to the movements of the bed 14 when the latter inflates, for example.
  • the increase in the volume of the bed 14 would result in an increase in the mechanical pressure of the bed PI which would become greater than the set pressure Pcl.
  • the hydraulic fluid cannot exit from the upper chamber 28 of the cylinder 22, and an increase in the pressure PI would result in an increase in the hydraulic pressure. It is therefore necessary in this case to evacuate the hydraulic fluid from the chamber 28 in order to keep PI constant.
  • the digital valve 48 is open and the control valve 50 is open at a percentage controlled by the regulator 52, allowing the pressure PI to be kept constant and equal to Pcl.
  • the regulation of the pressure of the piston 36 on the bed 14 makes it possible to adapt to the operating conditions of the device. It provides all the efficiency of the bed 14 while protecting it.
  • the device described above is not limited to a single piston compacting the bed 14 but it is possible to envisage the action of two pistons on the bed 14.
  • the skilled person will able to use other types of cylinders such as pneumatic cylinders.
  • the chromatography device according to the invention is advantageously used in a method of separation by SMB, Simulated Moving Bed (US 2,985,589, US 3,291,726, US 3,268,605 and US 3,268,604 belonging to UOP, US 5,578,215 and US 5,578,216 belonging to IFP and NONASEP, EP 471,082 and EP 563,388 belonging to DAICEL) or in a process by NARICOL (US 6,136,198).
  • SMB Simulated Moving Bed
  • Simulated Moving Bed US 2,985,589, US 3,291,726, US 3,268,605 and US 3,268,604 belonging to UOP
  • US 5,578,215 and US 5,578,216 belonging to IFP and NONASEP EP 471,082 and EP 563,388 belonging to DAICEL
  • NARICOL US 6,136,198

Abstract

The invention concerns a chromatographic device comprising: a column (12) for receiving a chromatographic bed (14) through which flows a first fluid; a piston (36) sliding inside the column (12) and exerting pressure on the bed (14), a chamber (28) containing a second fluid exerting pressure on the piston (36); a regulator (52) for the pressure exerted by the piston (36) on the bed based on the pressure inside the chamber (28), on the flow pressure of the first fluid at the intake of the column (12) and on a reference pressure on the bed (14). Said device enables to separate at least two compounds to be subjected to chromatographic analysis, while adjusting the pressure exerted on the chromatographic bed. The device efficiently uses the chromatographic bed while protecting it.

Description

DISPOSITIF DE PROTECTION DU LIT CHROMATOGRAPHIQUE CHROMATOGRAPHIC BED PROTECTION DEVICE
DANS LES COLONNES CHROMATOGRAPHIQUESIN THE CHROMATOGRAPHIC COLUMNS
A COMPRESSION AXIALE DYNAMIQUEDYNAMIC AXIAL COMPRESSION
Domaine de l'inventionField of the invention
La présente invention se rapporte à la protection du lit chromatographique de colonnes chromatographiques et en particulier dans les colonnes à compression axiale dynamique.The present invention relates to the protection of the chromatographic bed of chromatographic columns and in particular in columns with dynamic axial compression.
Arrière-plan technologique Dans un procédé de séparation par chromatographie, l'efficacité de la colonne utilisée est un paramètre clef. La colonne est généralement remplie avec un produit solide sous forme de grains très fins habituellement d'une taille comprise entre 5 et lOOμm, formant le lit chromatographique. Afin d'obtenir une efficacité élevée, l'arrangement des grains à l'intérieur de la colonne doit être le plus homogène possible et de plus, il faut éviter des volumes vides entre le lit chromatographique et les entrées-sorties de la colonne. Il est connu de l'art antérieur de recourir à des colonnes à compression axiale dynamique afin d'assurer l'existence d'un lit compact, sans espace libre entre les distributeurs d'entrée-sortie et le lit.Technological background In a separation process by chromatography, the efficiency of the column used is a key parameter. The column is generally filled with a solid product in the form of very fine grains, usually between 5 and 100 μm in size, forming the chromatographic bed. In order to obtain high efficiency, the arrangement of the grains inside the column must be as homogeneous as possible and, moreover, empty volumes must be avoided between the chromatographic bed and the inputs-outputs of the column. It is known in the prior art to use columns with dynamic axial compression in order to ensure the existence of a compact bed, with no free space between the inlet-outlet distributors and the bed.
Ainsi, on connaît de la demande de brevet français FR-A-2 219 797 un appareil de chromatographie se présentant sous forme d'une colonne destinée à contenir un lit en matière adsorbante. L'appareil est constitué d'un tube comprenant un couvercle et un corps coulissant dans le tube permettant d'exercer une pression dans le tube. Le corps coulissant est un piston comportant à sa tête une plaque poreuse perméable aux fluides. Pour obtenir le lit destiné à la chromatographie, on introduit dans le tube démuni de son couvercle, une suspension de particules d'une matière susceptible de constituer un lit adsorbant, le piston étant suffisamment reculé pour permettre l'introduction de la suspension, sans être forcément au point mort. On adapte le couvercle au tube, puis on exerce une pression sur ladite suspension au moyen du piston. Le liquide est refoulé à travers les plaques poreuses, et lesdites particules sont comprimées entre le piston et le couvercle. Cet appareil permet d'atteindre, dans un exemple d'exécution, le stade de compression du lit choisi et le tassement des particules désiré quand le corps coulissant a parcouru les 2/5 de la hauteur de la colonne.Thus, known from French patent application FR-A-2 219 797 is a chromatography device in the form of a column intended to contain a bed of adsorbent material. The apparatus consists of a tube comprising a cover and a body sliding in the tube for exerting pressure in the tube. The sliding body is a piston comprising at its head a porous plate permeable to fluids. To obtain the bed intended for chromatography, a suspension of particles of a material capable of constituting an adsorbent bed is introduced into the tube devoid of its cover, the piston being set back enough to allow the introduction of the suspension, without being necessarily in neutral. The cover is adapted to the tube, then pressure is exerted on said suspension by means of the piston. The liquid is discharged through the porous plates, and said particles are compressed between the piston and the cover. This device makes it possible, in an exemplary embodiment, to reach the stage of compression of the bed chosen and the settlement of the particles desired when the sliding body has traveled 2/5 of the height of the column.
Cet appareil comporte toutefois l'inconvénient de parvenir à un tassement imprécis du lit, puisqu'il est évalué par la seule position du piston le long du tube.However, this device has the disadvantage of achieving imprecise settlement of the bed, since it is evaluated by the sole position of the piston along the tube.
On connaît également de la demande de brevet européen EP-A-0 145 578, sous priorité des demandes FR-A-2 556 099 et FR-A-2 573 532, un appareil de chromatographie comprenant un tube dont une partie est destinée à contenir un lit adsorbant. Ce tube comporte deux parois d'extrémité et un piston coulissant longitudinalement dans le tube. Le piston marque entre les deux parois d'extrémité une séparation entre une chambre chromatographique contenant le lit et une enceinte dans laquelle règne une pression de sorte à déplacer le piston le long du tube. La particularité de ce dispositif est que le fluide contenu dans l'enceinte est du liquide à chromatographier dérivé depuis le conduit d'arrivée de celui- ci. Une partie du liquide est dérivée vers l'enceinte par un conduit d'enceinte et l'autre partie du liquide est entraîné vers la chambre chromatographique par un conduit d'écoulement traversant l'enceinte et le piston. A l'équilibre du piston, la force exercée du côté de l'enceinte sur le piston est égale à la somme de la force sur le piston provoquée par l'écoulement du liquide dans la chambre à chromatographier et de la force mécanique du lit sur le piston.Also known from European patent application EP-A-0 145 578, under priority of applications FR-A-2 556 099 and FR-A-2 573 532, a chromatography apparatus comprising a tube of which a part is intended for contain an adsorbent bed. This tube has two end walls and a piston sliding longitudinally in the tube. The piston marks between the two end walls a separation between a chamber chromatography containing the bed and an enclosure in which a pressure prevails so as to move the piston along the tube. The particularity of this device is that the fluid contained in the enclosure is liquid to be chromatographed derived from the inlet pipe thereof. A part of the liquid is diverted towards the enclosure by an enclosure conduit and the other part of the liquid is entrained towards the chromatographic chamber by a flow conduit passing through the enclosure and the piston. At equilibrium of the piston, the force exerted on the side of the enclosure on the piston is equal to the sum of the force on the piston caused by the flow of the liquid in the chamber to be chromatographed and the mechanical force of the bed on the piston.
Cet appareil permet, outre d'effectuer l'étape d'élution, de définir la pression exercée sur le lit.This device allows, in addition to performing the elution step, to define the pressure exerted on the bed.
Dans un premier mode de réalisation, le piston a une section constante mais la pression dans les conduits d'écoulement et d'enceinte est régulée par des taquets détendeurs. Ainsi on peut tarer les taquets de sorte que la différence des pressions exercées par l'écoulement du liquide et par le liquide dans l'enceinte soit ajustée à une pression de consigne sur le lit. Dans un autre mode de réalisation, la pression dans les conduits d'écoulement et d'enceinte est la même mais la section du piston varie. Le piston est à deux sections coulissant dans des alésages correspondants, la section la plus petite A étant située du côté de la chambre chromatographique et la section la plus grande B du côté de l'enceinte. Du fait de la différence de surface des faces A et B du piston, la force exercée en B est supérieure à la force exercée en A. Ainsi on peut choisir les sections du piston de sorte que la différence des pressions exercées par l'écoulement du liquide et par le liquide dans l'enceinte soit ajustée à une pression de consigne sur le lit.In a first embodiment, the piston has a constant cross-section but the pressure in the flow and enclosure conduits is regulated by pressure reducing valves. Thus, the tabs can be tared so that the difference in pressures exerted by the flow of the liquid and by the liquid in the enclosure is adjusted to a set pressure on the bed. In another embodiment, the pressure in the flow and enclosure conduits is the same but the cross section of the piston varies. The piston has two sections sliding in corresponding bores, the smallest section A being located on the side of the chromatographic chamber and the largest section B on the side of the enclosure. Due to the difference in surface area of the faces A and B of the piston, the force exerted at B is greater than the force exerted at A. Thus the sections of the piston can be chosen so that the difference in pressures exerted by the flow of the liquid and by the liquid in the enclosure is adjusted to a set pressure on the bed.
En fait, l'appareil décrit dans le document ci-dessus présente divers inconvénients. Si une chute de pression survient dans le conduit d'écoulement, la pression exercée sur le piston par le liquide dans l'enceinte s'applique directement sur le lit ce qui peut engendrer une détérioration du lit. De plus, les mouvements du lit chromatographique n'étant pas surveillés et l'enceinte ne pouvant pas refouler du liquide au cours de la chromatographie, cet appareil ne peut pas adapter la pression exercée sur le lit en fonction des mouvements de celui-ci. Une détérioration du lit peut de nouveau s'en suivre. D'autre part, ce système ne peut pas être utilisé en SMB (Simulated Moving Bed) ou en NARICOL. Dans de telles configurations, les appareils de chromatographie sont montés en boucle et les liquides injectés dans les lits alternent. Dans l'appareil décrit dans EP-A-0 145 578, le même liquide est envoyé dans le lit et dans l'enceinte, l'alternance d'injection de liquides engendre un mélange de ceux-ci.In fact, the apparatus described in the above document has various drawbacks. If a pressure drop occurs in the flow conduit, the pressure exerted on the piston by the liquid in the enclosure applies directly to the bed which can cause deterioration of the bed. In addition, the movements of the chromatographic bed not being monitored and the enclosure being unable to discharge liquid during the chromatography, this device cannot adapt the pressure exerted on the bed as a function of the movements of the latter. A deterioration of the bed can again follow. On the other hand, this system cannot be used in SMB (Simulated Moving Bed) or in NARICOL. In such configurations, the chromatography devices are mounted in a loop and the liquids injected into the beds alternate. In the apparatus described in EP-A-0 145 578, the same liquid is sent into the bed and into the enclosure, the alternation of injection of liquids generates a mixture of these.
Résumé de l'inventionSummary of the invention
La présente invention a pour objet un dispositif de chromatographie perfectionné permettant de remédier aux inconvénients des appareils connus. Ce dispositif permet d'augmenter l'efficacité du lit chromatographique tout en le protégeant. La présente invention se rapporte à un dispositif de chromatographie comprenant :The present invention relates to an improved chromatography device which overcomes the drawbacks of known devices. This device increases the efficiency of the chromatographic bed while protecting it. The present invention relates to a chromatography device comprising:
- une colonne destinée à recevoir un lit chromatographique à travers lequel s'écoule un premier fluide,- a column intended to receive a chromatographic bed through which a first fluid flows,
- un piston coulissant dans la colonne et exerçant une pression sur le lit, - une chambre contenant un deuxième fluide exerçant une pression sur le piston,- a piston sliding in the column and exerting pressure on the bed, - a chamber containing a second fluid exerting pressure on the piston,
- un régulateur de la pression exercée par le piston sur le lit en fonction de la pression dans la chambre, de la pression d'écoulement du premier fluide à l'entrée de la colonne et d'une pression de consigne sur le lit.a regulator of the pressure exerted by the piston on the bed as a function of the pressure in the chamber, the flow pressure of the first fluid at the inlet of the column and a set pressure on the bed.
Le régulateur est à action Proportionnelle Intégrale (PI), à action Proportionnelle Différentielle (PD) ou à action Proportionnelle Intégrale Différentielle (PID).The regulator is Integral Proportional Action (PI), Differential Proportional Action (PD) or Differential Integral Proportional Action (PID).
Le dispositif comprend en outre un premier capteur qui mesure la pression d'écoulement du premier fluide à l'entrée de la colonne et un second capteur qui mesure la pression dans la chambre.The device further includes a first sensor which measures the flow pressure of the first fluid at the inlet of the column and a second sensor which measures the pressure in the chamber.
Dans un mode de réalisation, le premier fluide s'écoule à travers le lit à partir du piston en direction de 1 ' extrémité de la colonne.In one embodiment, the first fluid flows through the bed from the piston towards the end of the column.
Dans un autre mode de réalisation le premier fluide s'écoule à travers le lit à partir de l'extrémité de la colonne en direction du piston.In another embodiment the first fluid flows through the bed from the end of the column towards the piston.
Le piston coulissant dans la colonne est relié à un autre piston coulissant dans la chambre par une tige. Dans un mode de réalisation, le deuxième fluide est régulé par dérivation par le régulateur.The piston sliding in the column is connected to another piston sliding in the chamber by a rod. In one embodiment, the second fluid is regulated by bypass by the regulator.
L'invention propose également un ensemble de dispositifs tels que décrits ci-dessus, associés en boucle.The invention also provides a set of devices as described above, associated in a loop.
L'invention concerne aussi un procédé de séparation d'au moins deux composés d'un premier fluide, comprenant la chromatographie dudit fluide dans le dispositif décrit ci-dessus, le procédé comprend les étapes :The invention also relates to a method for separating at least two compounds from a first fluid, comprising the chromatography of said fluid in the device described above, the method comprises the steps:
- introduction du premier fluide dans la colonne contenant le lit et mesure de la pression d'écoulement à l'entrée de celle-ci,- introduction of the first fluid into the column containing the bed and measurement of the flow pressure at the inlet thereof,
- écoulement du premier fluide à travers le lit chromatographique, - collecte du premier fluide chromatographie.- flow of the first fluid through the chromatographic bed, - collection of the first chromatography fluid.
Avec le dispositif selon l'invention, il est possible, au cours du procédé de séparation, d'effectuer les étapes :With the device according to the invention, it is possible, during the separation process, to carry out the steps:
- introduction d'un deuxième fluide dans la chambre et mesure de la pression,- introduction of a second fluid into the chamber and measurement of the pressure,
- régulation de la pression dans la chambre en fonction de la pression mesurée dans la chambre, de la pression d'écoulement du premier fluide à l'entrée de la colonne et d'une pression de consigne sur le lit. L'invention se rapporte également à un procédé de réglage de la pression sur le lit chromatographique dans le dispositif décrit ci-dessus, le procédé comprenant l'étape :- regulation of the pressure in the chamber as a function of the pressure measured in the chamber, the flow pressure of the first fluid at the inlet of the column and a set pressure on the bed. The invention also relates to a method for adjusting the pressure on the chromatographic bed in the device described above, the method comprising the step:
- régulation de la pression dans la chambre en fonction de la pression mesurée dans la chambre, de la pression d'écoulement du premier fluide à l'entrée de la colonne et d'une pression de consigne sur le lit.- regulation of the pressure in the chamber as a function of the pressure measured in the chamber, the flow pressure of the first fluid at the inlet of the column and a set pressure on the bed.
La régulation de la pression exercée sur le lit permet d'en tirer toute l'efficacité tout en le protégeant contre sa dégradation.The regulation of the pressure exerted on the bed makes it possible to draw all the efficiency while protecting it against its degradation.
Brève description des dessinsBrief description of the drawings
D'autres caractéristiques et avantages de l'invention apparaîtront à la lecture de la description détaillée qui suit des modes de réalisation de l'invention, donnés à titre d'exemple uniquement et en références au dessin qui représente schématiquement :Other characteristics and advantages of the invention will appear on reading the detailed description which follows of embodiments of the invention, given by way of example only and with reference to the drawing which represents schematically:
- la figure 1, une coupe axiale d'un dispositif de chromatographie conforme à l'invention.- Figure 1, an axial section of a chromatography device according to the invention.
Description de l'inventionDescription of the invention
On se référera à la chromatographie en phase liquide et ceci à titre illustratif, ce que l'homme du métier transposera aisément à la chromatographie gazeuse sans sortir de l'invention. De même ce dispositif est adapté pour la chromatographie de fluides supercritiques.Reference will be made to liquid phase chromatography and this by way of illustration, which a person skilled in the art will easily transpose to gas chromatography without departing from the invention. Likewise, this device is suitable for the chromatography of supercritical fluids.
La figure 1 représente schématiquement un dispositif de chromatographie 10 comprenant une colonne 12 pour réaliser la chromatographie et dont une partie est destinée à contenir un lit chromatographique 14 reposant sur une paroi d'extrémité 16. Au-dessus de la colonne 12, le dispositif 10 comprend également un vérin 22. Le vérin 22 comporte un piston mobile 24 relié à une extrémité d'une tige 26. Le piston 24 délimite deux chambres 28 et 30 dans le vérin 22. La première chambre 28, ou chambre supérieure, est délimitée entre le piston 24 et la paroi supérieure 32 du vérin 22. La deuxième chambre 30, ou chambre inférieure, est délimitée entre le piston 24 et la paroi inférieure 34 du vérin 22. La paroi inférieure 34 marque la séparation entre le vérin 22 et la colonne 12. La tige 26 reliée au piston 24 se trouve dans la chambre inférieure 30 et débouche dans la colonne 12 en traversant la paroi inférieure 34 du vérin 22. Des joints appropriés seront utilisés pour assurer l'étanchéité entre la chambre 30 et la colonne 12. L'autre extrémité de la tige 26 se trouvant dans la colonne 12 est reliée à un corps 36. Le corps 36 coulisse dans la colonne 12. Le corps coulissant 36 est par exemple un piston. Il vient en appui sur le lit chromatographique 14. La position du vérin 22 par rapport à la colonne 12 n'est pas limitée à celle décrite précédemment. On peut en effet envisager de disposer le vérin sous la colonne de sorte que le piston 36 soit pressé vers le haut contre le lit 14.FIG. 1 schematically represents a chromatography device 10 comprising a column 12 for performing the chromatography and a part of which is intended to contain a chromatographic bed 14 resting on an end wall 16. Above the column 12, the device 10 also comprises a jack 22. The jack 22 comprises a movable piston 24 connected to one end of a rod 26. The piston 24 delimits two chambers 28 and 30 in the jack 22. The first chamber 28, or upper chamber, is delimited between the piston 24 and the upper wall 32 of the cylinder 22. The second chamber 30, or lower chamber, is delimited between the piston 24 and the lower wall 34 of the cylinder 22. The lower wall 34 marks the separation between the cylinder 22 and the column 12. The rod 26 connected to the piston 24 is located in the lower chamber 30 and opens into the column 12 passing through the lower wall 34 of the jack 22. Appropriate seals will be used. ilises to seal between the chamber 30 and the column 12. The other end of the rod 26 located in the column 12 is connected to a body 36. The body 36 slides in the column 12. The sliding body 36 is for example a piston. It comes to bear on the chromatographic bed 14. The position of the actuator 22 relative to the column 12 is not limited to that described above. It is in fact possible to envisage placing the jack under the column so that the piston 36 is pressed upwards against the bed 14.
Le liquide à chromatographier est acheminé vers le lit 14 et en est refoulé par des conduits souples de communication vers l'extérieur. Le piston 36 comporte un conduit 20 muni d'un premier capteur de pression d'écoulement 45. La paroi 16 présente également un conduit 18. Le liquide à chromatographier parvient au lit 14 par l'intermédiaire du conduit 20 puis ressort par l'intermédiaire du conduit 18, après le passage dans le lit 14. Le capteur 45 permet de mesurer la pression d'écoulement du fluide à l'entrée de la colonne 12. Le liquide à chromatographier peut également circuler dans l'autre sens. Il parvient alors à la colonne 12 par l'intermédiaire du conduit 18, s'écoule à travers le lit 14, puis ressort de la colonne 12 par le conduit 20. Le capteur 45 est disposé sur le conduit d'entrée 18.The liquid to be chromatographed is conveyed to the bed 14 and is discharged therefrom via flexible communication lines to the outside. The piston 36 includes a conduit 20 provided with a first flow pressure sensor 45. The wall 16 also has a conduit 18. The liquid to be chromatographed reaches the bed 14 via the conduit 20 and then leaves via the of the conduit 18, after passing through the bed 14. The sensor 45 makes it possible to measure the flow pressure of the fluid at the inlet of the column 12. The liquid to be chromatographed can also circulate in the other direction. It then reaches the column 12 via the conduit 18, flows through the bed 14, then leaves the column 12 through the conduit 20. The sensor 45 is placed on the inlet conduit 18.
Le vérin 22 est alimenté par un circuit de fluide propulseur. Typiquement, le vérin 22 est un vérin hydraulique à double effet. Le fluide propulseur est alors un liquide hydraulique. Un premier conduit 38 met en relation la chambre 28 avec une source de liquide hydraulique 44. Le conduit 38 comporte un second capteur de pression 46. Un second conduit 40 met en relation la chambre inférieure 30 avec la source de liquide hydraulique 44. Un conduit de dérivation 42 relie les conduits 38 et 40. Le conduit de dérivation 42 comporte des moyens de régulation de l'écoulement du liquide propulseur dans la dérivation. Ces moyens comprennent une vanne tout ou rien (TOR) 48 et une vanne de régulation 50. La vanne de régulation est contrôlée par un régulateur 52 du type à action Proportionnelle Intégrale (PI), à action Proportionnelle Différentielle (PD) ou à action Proportionnelle Intégrale Différentielle (PID). Les liquides utilisés dans le dispositif sont des fluides distincts. Le premier fluide, c'est- à-dire le gaz ou le liquide à chromatographier, n'est pas le même que le fluide propulseur, ou deuxième fluide, utilisé dans le vérin 22. En d'autres termes, il n'y a pas de dérivation dans les conduits du premier fluide pour alimenter le vérin 22.The jack 22 is supplied by a propellant fluid circuit. Typically, the cylinder 22 is a double-acting hydraulic cylinder. The propellant fluid is then a hydraulic liquid. A first conduit 38 connects the chamber 28 with a source of hydraulic fluid 44. The conduit 38 includes a second pressure sensor 46. A second conduit 40 connects the lower chamber 30 with the source of hydraulic fluid 44. A conduit bypass 42 connects the conduits 38 and 40. The bypass conduit 42 includes means for regulating the flow of propellant in the bypass. These means include an all or nothing valve (TOR) 48 and a regulation valve 50. The regulation valve is controlled by a regulator 52 of the type with integral proportional action (PI), with differential proportional action (PD) or with proportional action. Differential Integral (PID). The liquids used in the device are separate fluids. The first fluid, that is to say the gas or the liquid to be chromatographed, is not the same as the propellant fluid, or second fluid, used in the jack 22. In other words, there has no bypass in the conduits of the first fluid to supply the jack 22.
Le fonctionnement du dispositif va maintenant être expliqué.The operation of the device will now be explained.
Le dispositif est utilisé dans un mode de descente du piston 36 pour tasser le lit chromatographique 14 dans la colonne 12. La colonne 12 est au préalable remplie par le matériau formant le lit 14. Le liquide hydraulique est ensuite envoyé dans la chambre 28 du vérin 22 afin de descendre le piston 36 dans la colonne 12 jusqu'à ce que le piston 36 vienne en contact avec le lit 14 et assure son tassement. Dans ce cas, la vanne TOR 48 et la vanne de régulation 50 sont fermées.The device is used in a mode of descent of the piston 36 to compact the chromatographic bed 14 in the column 12. The column 12 is previously filled with the material forming the bed 14. The hydraulic fluid is then sent to the chamber 28 of the jack 22 in order to lower the piston 36 into the column 12 until the piston 36 comes into contact with the bed 14 and ensures its compaction. In this case, the digital valve 48 and the control valve 50 are closed.
En fin de séparation, le dispositif permet de remonter le piston 36 pour permettre de vider le lit 14 de la colonne 12. Le liquide hydraulique est envoyé dans la chambre 30 du vérin 22 afin de remonter le piston 36. Dans ce cas, la vanne TOR 48 et la vanne de régulation 50 sont également fermées. Le dispositif est utilisé pour la séparation d'au moins deux composés d'un liquide à chromatographier. Le procédé comprend les étapes :At the end of separation, the device allows the piston 36 to be raised to allow the bed 14 to be emptied from the column 12. The hydraulic fluid is sent to the chamber 30 of the jack 22 in order to reassemble the piston 36. In this case, the valve TOR 48 and the control valve 50 are also closed. The device is used for the separation of at least two compounds from a liquid to be chromatographed. The process includes the steps:
- introduction du liquide à chromatographier dans la colonne 12 contenant le lit 14. Le liquide est par exemple introduit par le conduit souple 20. - écoulement du liquide à travers le lit 14. Suivant les affinités des composés avec le lit- introduction of the liquid to be chromatographed in column 12 containing the bed 14. The liquid is for example introduced through the flexible conduit 20. - flow of the liquid through the bed 14. Depending on the affinities of the compounds with the bed
14, les composés s'écoulent avec des vitesses différentes le long du lit 14.14, the compounds flow with different speeds along the bed 14.
- Collecte du liquide chromatographie. Les composés du liquide sont séparés et collectés dans le conduit souple 18.- Collection of liquid chromatography. The liquid compounds are separated and collected in the flexible conduit 18.
La séparation des composés s'accompagne de la régulation de la pression exercée sur le lit 14.The separation of the compounds is accompanied by the regulation of the pressure exerted on the bed 14.
Lorsque le piston 36 est statique, les différentes forces s 'exerçant sur le piston sont en équilibre. Les différentes forces sont la force hydraulique (Fh) fournie par la source hydraulique au piston 36 compensée par la force d'écoulement (Fe) du liquide à chromatographier à l'entrée de la colonne 12 et par la force mécanique du lit (FI). La force mécanique du lit est ainsi donnée par le bilan des forcesWhen the piston 36 is static, the different forces exerted on the piston are in equilibrium. The different forces are the hydraulic force (Fh) supplied by the hydraulic source to the piston 36 compensated by the flow force (Fe) of the liquid to be chromatographed at the inlet of the column 12 and by the mechanical force of the bed (FI) . The mechanical strength of the bed is thus given by the balance of forces
Fl ≈ Fh- Fe Eq. 1Fl ≈ Fh- Fe Eq. 1
La transformation du bilan des forces en un bilan des pressions conduit àThe transformation of the balance of forces into a balance of pressures leads to
Pl = Ph . AlJA2 -Pe Eq. 2Pl = Ph. AlJA2 -Pe Eq. 2
où Al est la surface du piston 36 dans la colonne 12 et A2 est la surface du piston 24 dans la chambre 28.where Al is the surface of the piston 36 in the column 12 and A2 is the surface of the piston 24 in the chamber 28.
Au cours de l'utilisation d'un appareil de chromatographie, un arrêt abrupt de l'écoulement du liquide à chromatographier peut survenir, par exemple lors d'un arrêt d'urgence. La force d'écoulement Fe devient alors nulle et toute la force hydraulique Fh s'exerce sur le lit. On a donc : FI = Fh. Si la résistance mécanique du lit est moyenne (par exemple si le lit est en silice avec des diamètres de pores importants), celui-ci risque de subir un tassement non souhaité voire d'être endommagé par le piston 36. De même, lors de l'utilisation, le lit peut gonfler au point d'être plus fortement pressé contre le piston. Il est alors nécessaire que le piston 36 suive le lit dans ses mouvements.During the use of a chromatography device, an abrupt stop of the flow of the liquid to be chromatographed can occur, for example during an emergency stop. The flow force Fe then becomes zero and all the hydraulic force Fh is exerted on the bed. We therefore have: FI = Fh. If the mechanical strength of the bed is medium (for example if the bed is made of silica with large pore diameters), it may suffer unwanted compaction or even be damaged by the piston 36. Similarly, when in use, the bed may swell to the point of being more strongly pressed against the piston. It is then necessary for the piston 36 to follow the bed in its movements.
Suivant les conditions de réalisation de la chromatographie (le liquide à chromatographier, vitesse d'écoulement dans le lit...) et des caractéristiques du lit utiliséDepending on the conditions for carrying out the chromatography (the liquid to be chromatographed, flow speed in the bed, etc.) and the characteristics of the bed used
(matériau utilisé, porosité, résistance mécanique...), il est possible de déterminer une pression de consigne (Pcl) exercée sur le lit. La pression hydraulique Ph doit être calculée en fonction de la pression d'écoulement de façon à vérifier :(material used, porosity, mechanical resistance ...), it is possible to determine a pressure deposit (Pcl) exerted on the bed. The hydraulic pressure Ph must be calculated as a function of the flow pressure so as to check:
Ph = (Pcl + Pe).Al/A2 Eq. 3Ph = (Pcl + Pe). Al / A2 Eq. 3
Lorsque la pression d'écoulement Pe varie, l'équation 3 montre que PI peut être maintenue constante à la valeur de Pcl en faisant varier Ph. Pour ce faire, il faut mesurer la pression hydraulique Ph et la pression d'écoulement à l'entrée de la colonne 12. L'utilisation d'un régulateur 52 du type PI, PD, PID permet le réglage de la pression sur le lit 14 selon les étapes :When the flow pressure Pe varies, equation 3 shows that PI can be kept constant at the value of Pcl by varying Ph. To do this, it is necessary to measure the hydraulic pressure Ph and the flow pressure at entry of column 12. The use of a regulator 52 of the PI, PD, PID type allows the pressure on the bed 14 to be adjusted according to the steps:
- programmation d'une pression de consigne sur le lit ;- programming of a set pressure on the bed;
- introduction du liquide à chromatographier dans la colonne 12 qui contient le lit 14 et mesure de la pression d'écoulement du liquide par le capteur 45 à l'entrée de la colonne 12 ; - Ecoulement du liquide à travers le lit 14 ;- introduction of the liquid to be chromatographed in the column 12 which contains the bed 14 and measurement of the liquid flow pressure by the sensor 45 at the inlet of the column 12; - Flow of the liquid through the bed 14;
- Introduction du liquide hydraulique dans la chambre 28 et mesure de la pression hydraulique fournie au vérin 22 par le capteur 46 ;- Introduction of the hydraulic fluid into the chamber 28 and measurement of the hydraulic pressure supplied to the jack 22 by the sensor 46;
- comparaison suivant un algorithme de régulation des trois pressions précitées ;- comparison according to an algorithm for regulating the three aforementioned pressures;
- régulation de la pression dans la chambre 28 en fonction de la pression mesurée dans la chambre 28, de la pression d'écoulement du liquide à chromatographier à l'entrée de la colonne 12 et de la pression consigne sur le lit.- Regulation of the pressure in the chamber 28 as a function of the pressure measured in the chamber 28, of the flow pressure of the liquid to be chromatographed at the inlet of the column 12 and of the pressure set on the bed.
Le procédé de séparation peut alors être complété par l'étape d'introduction du liquide hydraulique dans la chambre 28 et de l'étape de régulation de la pression dans la chambre 28. A titre d'illustration, lorsqu'il se produit un arrêt de l'écoulement du liquide à chromatographier, la pression d'écoulement descend vers zéro. Avec l'équation 3, on déduit que la pression hydraulique doit être diminuée pour atteindre Ph = Pcl. A2/A1. Pour réaliser ceci, le régulateur 52 dérive le liquide hydraulique dans le conduit de dérivation 42 par ouverture de la vanne TOR 48 et par ouverture de la vanne de régulation 50 à un pourcentage contrôlé par le régulateur 52. Le liquide hydraulique envoyé par la source hydraulique 44 ne pénètre pas dans la chambre 28 mais est détourné dans le conduit de dérivation 42. Il est ensuite évacué vers la source hydraulique 44. De cette manière, la pression dans la chambre 28 est diminuée engendrant une pression moins importante du piston 36 sur le lit 14.The separation process can then be completed by the step of introducing the hydraulic liquid into the chamber 28 and the step of regulating the pressure in the chamber 28. By way of illustration, when a stop occurs from the flow of the liquid to be chromatographed, the flow pressure drops to zero. With equation 3, we deduce that the hydraulic pressure must be reduced to reach Ph = Pcl. A2 / A1. To achieve this, the regulator 52 derives the hydraulic fluid in the bypass duct 42 by opening the TOR valve 48 and by opening the control valve 50 at a percentage controlled by the regulator 52. The hydraulic fluid sent by the hydraulic source 44 does not enter the chamber 28 but is diverted into the bypass duct 42. It is then evacuated towards the hydraulic source 44. In this way, the pressure in the chamber 28 is reduced, generating less pressure from the piston 36 on the bed 14.
Le réglage de la pression exercée par le piston 36 sur le lit 14 permet de s'adapter aux mouvements du lit 14 lorsque celui-ci gonfle, par exemple. L'augmentation du volume du lit 14 aurait pour conséquence une augmentation de la pression mécanique du lit PI qui deviendrait supérieure à la pression de consigne Pcl. Dans une mise en œuvre classique du vérin 22, le liquide hydraulique ne peut pas sortir de la chambre supérieure 28 du vérin 22, et une augmentation de la pression PI aurait pour conséquence une augmentation de la pression hydraulique. Il faut donc dans ce cas évacuer le liquide hydraulique de la chambre 28 afin de conserver PI constant. De nouveau, la vanne TOR 48 est ouverte et la vanne de régulation 50 est ouverte à un pourcentage contrôlé par le régulateur 52, permettant de garder la pression PI constante et égale à Pcl.The adjustment of the pressure exerted by the piston 36 on the bed 14 makes it possible to adapt to the movements of the bed 14 when the latter inflates, for example. The increase in the volume of the bed 14 would result in an increase in the mechanical pressure of the bed PI which would become greater than the set pressure Pcl. In a classic implementation of the cylinder 22, the hydraulic fluid cannot exit from the upper chamber 28 of the cylinder 22, and an increase in the pressure PI would result in an increase in the hydraulic pressure. It is therefore necessary in this case to evacuate the hydraulic fluid from the chamber 28 in order to keep PI constant. Again, the digital valve 48 is open and the control valve 50 is open at a percentage controlled by the regulator 52, allowing the pressure PI to be kept constant and equal to Pcl.
La régulation de la pression du piston 36 sur le lit 14 permet de s'adapter aux conditions de fonctionnement de l'appareil. Elle permet de disposer de toute l'efficacité du lit 14 tout en le protégeant.The regulation of the pressure of the piston 36 on the bed 14 makes it possible to adapt to the operating conditions of the device. It provides all the efficiency of the bed 14 while protecting it.
Le dispositif décrit ci-dessus n'est pas limitée à un seul piston effectuant le tassement du lit 14 mais il est possible d'envisager l'action de deux pistons sur le lit 14. D'autre part, l'homme du métier sera en mesure d'utiliser d'autres types de vérin tels qu'un vérin pneumatique.The device described above is not limited to a single piston compacting the bed 14 but it is possible to envisage the action of two pistons on the bed 14. On the other hand, the skilled person will able to use other types of cylinders such as pneumatic cylinders.
Le dispositif de chromatographie selon l'invention est avantageusement utilisée dans un procédé de séparation par SMB, Simulated Moving Bed (US 2,985,589, US 3,291,726, US 3,268,605 et US 3,266,604 appartenant à UOP, US 5,578,215 et US 5,578,216 appartenant à IFP et NONASEP, EP 471 082 et EP 563 388 appartenant à DAICEL) ou dans un procédé par NARICOL (US 6,136,198). Un tel procédé met en œuvre un ensemble de ces colonnes associées en boucle. The chromatography device according to the invention is advantageously used in a method of separation by SMB, Simulated Moving Bed (US 2,985,589, US 3,291,726, US 3,268,605 and US 3,268,604 belonging to UOP, US 5,578,215 and US 5,578,216 belonging to IFP and NONASEP, EP 471,082 and EP 563,388 belonging to DAICEL) or in a process by NARICOL (US 6,136,198). Such a method implements a set of these associated columns in a loop.

Claims

REVENDICATIONS
1. Dispositif de chromatographie comprenant :1. Chromatography device comprising:
- une colonne (12) destinée à recevoir un lit chromatographique (14) à travers lequel 5 s ' écoule un premier fluide,- a column (12) intended to receive a chromatographic bed (14) through which 5 flows a first fluid,
- un piston (36) coulissant dans la colonne (12) et exerçant une pression sur le lit (14),- a piston (36) sliding in the column (12) and exerting pressure on the bed (14),
- une chambre (28) contenant un deuxième fluide exerçant une pression sur le piston (36),- a chamber (28) containing a second fluid exerting pressure on the piston (36),
- un régulateur (52) de la pression exercée par le piston (36) sur le lit en fonction de la 10 pression dans la chambre (28), de la pression d'écoulement du premier fluide à l'entrée de la colonne (12) et d'une pression de consigne sur le lit (14)- a regulator (52) of the pressure exerted by the piston (36) on the bed as a function of the pressure in the chamber (28), of the flow pressure of the first fluid at the inlet of the column (12 ) and a set pressure on the bed (14)
2. Dispositif selon la revendication 1, caractérisé en ce que le régulateur (52) est à action Proportionnelle Intégrale (PI), à action Proportionnelle Différentielle (PD) ou à action Proportionnelle Intégrale Différentielle (PID).2. Device according to claim 1, characterized in that the regulator (52) is with integral proportional action (PI), with differential proportional action (PD) or with differential integral proportional action (PID).
15. 15.
3. Dispositif selon la revendication 1 ou 2, caractérisé en ce qu'un premier capteur (45) mesure la pression d'écoulement du premier fluide à l'entrée de la colonne (12) et un second capteur (46) mesure la pression dans la chambre (28).3. Device according to claim 1 or 2, characterized in that a first sensor (45) measures the flow pressure of the first fluid at the inlet of the column (12) and a second sensor (46) measures the pressure in the room (28).
4. Dispositif selon l'une des revendications 1 à 3, caractérisé en ce que le premier fluide s'écoule à travers le lit (14) à partir du piston (36) en direction de l'extrémité (16) de la4. Device according to one of claims 1 to 3, characterized in that the first fluid flows through the bed (14) from the piston (36) towards the end (16) of the
20 colonne (12).20 column (12).
5. Dispositif selon l'une des revendications 1 à 3, caractérisé en ce que le premier fluide s'écoule à travers le lit (14) à partir de l'extrémité (16) de la colonne (12) en direction du piston (36).5. Device according to one of claims 1 to 3, characterized in that the first fluid flows through the bed (14) from the end (16) of the column (12) towards the piston ( 36).
6. Dispositif selon l'une des revendications 1 à 5, caractérisé en ce qu'un piston (24) 25 coulissant dans la chambre (28) est relié à une tige (26) actionnant le piston (36).6. Device according to one of claims 1 to 5, characterized in that a piston (24) sliding in the chamber (28) is connected to a rod (26) actuating the piston (36).
7. Dispositif selon l'une des revendications 1 à 6, caractérisé en ce que le deuxième fluide est régulé par dérivation par le régulateur (52).7. Device according to one of claims 1 to 6, characterized in that the second fluid is regulated by bypass by the regulator (52).
8. Ensemble de dispositifs de chromatographie selon l'une des revendications 1 à 7 dans lequel les dispositifs sont associés en boucle. 8. Set of chromatography devices according to one of claims 1 to 7 wherein the devices are associated in a loop.
9. Procédé de séparation d'au moins deux composés d'un premier fluide, comprenant la chromatographie dudit fluide dans le dispositif selon l'une des revendications 1 à 8, le procédé comprenant les étapes :9. A method of separating at least two compounds from a first fluid, comprising the chromatography of said fluid in the device according to one of claims 1 to 8, the method comprising the steps:
- introduction du premier fluide dans la colonne (12) contenant le lit (14), - écoulement du premier fluide à travers le lit chromatographique,- introduction of the first fluid into the column (12) containing the bed (14), - flow of the first fluid through the chromatographic bed,
- collecte du premier fluide chromatographie.- collection of the first chromatography fluid.
10. Procédé selon la revendication 9, caractérisé en ce qu'entre les étapes d'écoulement et de collecte, le procédé comprend en outre les étapes de :10. Method according to claim 9, characterized in that between the flow and collection steps, the method further comprises the steps of:
- introduction d'un deuxième fluide dans la chambre (28) et mesure de la pression, - régulation de la pression dans la chambre (28) en fonction de la pression mesurée dans la chambre (28), de la pression d'écoulement du premier fluide à l'entrée de la colonne (12) et d'une pression de consigne sur le lit (14).- introduction of a second fluid into the chamber (28) and measurement of the pressure, - regulation of the pressure in the chamber (28) as a function of the pressure measured in the chamber (28), of the flow pressure of the first fluid at the inlet of the column (12) and a set pressure on the bed (14).
11. Procédé de réglage de la pression sur le lit chromatographique dans le dispositif selon l'une des revendications 1 à 8, le procédé comprenant l'étape : - régulation de la pression dans la chambre (28) en fonction de la pression mesurée dans la chambre (28), de la pression d'écoulement du premier fluide à l'entrée de la colonne (12) et d'une pression de consigne sur le lit (14). 11. Method for adjusting the pressure on the chromatographic bed in the device according to one of claims 1 to 8, the method comprising the step: - regulating the pressure in the chamber (28) as a function of the pressure measured in the chamber (28), the flow pressure of the first fluid at the inlet of the column (12) and a set pressure on the bed (14).
EP02761925A 2001-04-10 2002-04-09 Protective device for the chromatographic bed in dynamic axial compression chromatographic columns Withdrawn EP1379867A1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR0104866A FR2823134B1 (en) 2001-04-10 2001-04-10 CHROMATOGRAPHIC BED PROTECTION DEVICE IN CHROMATOGRAPHIC COLUMNS WITH DYNAMIC AXIAL COMPRESSION
FR0104866 2001-04-10
PCT/FR2002/001223 WO2002084275A1 (en) 2001-04-10 2002-04-09 Protective device for the chromatographic bed in dynamic axial compression chromatographic columns

Publications (1)

Publication Number Publication Date
EP1379867A1 true EP1379867A1 (en) 2004-01-14

Family

ID=8862156

Family Applications (1)

Application Number Title Priority Date Filing Date
EP02761925A Withdrawn EP1379867A1 (en) 2001-04-10 2002-04-09 Protective device for the chromatographic bed in dynamic axial compression chromatographic columns

Country Status (4)

Country Link
US (1) US7132053B2 (en)
EP (1) EP1379867A1 (en)
FR (1) FR2823134B1 (en)
WO (1) WO2002084275A1 (en)

Families Citing this family (43)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050227187A1 (en) * 2002-03-04 2005-10-13 Supercritical Systems Inc. Ionic fluid in supercritical fluid for semiconductor processing
GB0328674D0 (en) * 2003-12-10 2004-01-14 Euroflow Uk Ltd Chromatography columns and their operation
GB0415394D0 (en) * 2004-07-08 2004-08-11 Euroflow Uk Ltd Chromatography columns and their operation
ATE523783T1 (en) * 2004-09-07 2011-09-15 Asahi Kasei Bioprocess Inc COLUMN AND METHOD FOR LIFTING-FREE CHROMATOGRAPHY
US20060102282A1 (en) * 2004-11-15 2006-05-18 Supercritical Systems, Inc. Method and apparatus for selectively filtering residue from a processing chamber
US20060185694A1 (en) * 2005-02-23 2006-08-24 Richard Brown Rinsing step in supercritical processing
US7238282B2 (en) * 2005-03-04 2007-07-03 Millipore Corporation System for automated compression of chromatography columns
US7767145B2 (en) * 2005-03-28 2010-08-03 Toyko Electron Limited High pressure fourier transform infrared cell
US20060226117A1 (en) * 2005-03-29 2006-10-12 Bertram Ronald T Phase change based heating element system and method
US20060225772A1 (en) * 2005-03-29 2006-10-12 Jones William D Controlled pressure differential in a high-pressure processing chamber
US20060225769A1 (en) * 2005-03-30 2006-10-12 Gentaro Goshi Isothermal control of a process chamber
US7494107B2 (en) * 2005-03-30 2009-02-24 Supercritical Systems, Inc. Gate valve for plus-atmospheric pressure semiconductor process vessels
US20060223899A1 (en) * 2005-03-30 2006-10-05 Hillman Joseph T Removal of porogens and porogen residues using supercritical CO2
US20060219268A1 (en) * 2005-03-30 2006-10-05 Gunilla Jacobson Neutralization of systemic poisoning in wafer processing
US7435350B2 (en) * 2005-04-04 2008-10-14 Millipore Corporation Intelligent system and method for automated packing of chromatography columns
US7452471B2 (en) * 2005-10-21 2008-11-18 Ge Healthcare Bio-Sciences Ab Automated packing system and method for chromatography columns
US7419599B2 (en) * 2005-07-12 2008-09-02 Ge Healthcare Bio-Sciences Ab Automated packing system and method for chromatography columns
US20070000519A1 (en) * 2005-06-30 2007-01-04 Gunilla Jacobson Removal of residues for low-k dielectric materials in wafer processing
US7402251B2 (en) * 2005-12-28 2008-07-22 Mann Welding Company Chromatography column and method of operation
FR2898064A1 (en) * 2006-03-03 2007-09-07 Novasep Soc Par Actions Simpli MODULAR CHROMATOGRAPHY DEVICE
EP2132217A2 (en) * 2007-02-26 2009-12-16 Alltech Associates Inc. Ultra-fast chromatography
CN101946176B (en) 2008-02-21 2015-03-25 全技术联合公司 Column packing apparatus and method of making and using the same
US8845903B2 (en) * 2008-10-07 2014-09-30 William H. Mann Chromatography column method of variable speed operation
US20100312480A1 (en) * 2009-04-24 2010-12-09 Hansteen Fredrik Method for monitoring fluid flow in a multi-layered system
CA2764934A1 (en) * 2009-06-24 2010-12-29 F. Hoffmann-La Roche Ag Characterization of re-useable chromatography equipment
JP5872483B2 (en) 2009-12-30 2016-03-01 ビーエイエスエフ ファーマ(コーラニッシュ)リミテッド Simulated moving bed chromatograph separation method
US20110259831A1 (en) * 2010-04-22 2011-10-27 Michael Brandt Tracking regulator system and method for processing columns
CN102441295A (en) * 2010-09-30 2012-05-09 中国科学院昆明植物研究所 Separation and preparation chromatograph containing series dynamic axial compression (DAC) preparative chromatographic columns
CN102070568B (en) * 2011-02-28 2012-09-26 珠海联邦制药股份有限公司 Preparation method of orlistat
GB201111589D0 (en) 2011-07-06 2011-08-24 Equateq Ltd New modified process
GB201111591D0 (en) 2011-07-06 2011-08-24 Equateq Ltd Further new process
GB201111594D0 (en) 2011-07-06 2011-08-24 Equateq Ltd New improved process
GB201111595D0 (en) 2011-07-06 2011-08-24 Equateq Ltd Improved process
GB201111601D0 (en) 2011-07-06 2011-08-24 Equateq Ltd New process
US20130213486A1 (en) * 2012-02-09 2013-08-22 Michael Brandt Column pressure regulation system and method
GB201300354D0 (en) 2013-01-09 2013-02-20 Basf Pharma Callanish Ltd Multi-step separation process
US8802880B1 (en) 2013-05-07 2014-08-12 Group Novasep Chromatographic process for the production of highly purified polyunsaturated fatty acids
US9428711B2 (en) 2013-05-07 2016-08-30 Groupe Novasep Chromatographic process for the production of highly purified polyunsaturated fatty acids
CN103399109A (en) * 2013-08-15 2013-11-20 宋家玉 Special apparatus for coating gas-phase capillary column
EP3118186B1 (en) 2013-12-11 2022-02-09 Novasep Process Chromatographic facility for producing polyunsaturated fatty acids
EP3092218B1 (en) 2014-01-07 2022-03-09 Novasep Process Solutions Process for the purification of aromatic aminoacids
CN107519667A (en) * 2017-09-29 2017-12-29 江苏汉邦科技有限公司 A kind of new low clearance chromatography rod structure
US11179691B1 (en) 2020-08-12 2021-11-23 Asahi Kasei Bioprocess America, Inc. Dynamically adjustable chemical processing column

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3487938A (en) * 1968-08-08 1970-01-06 Sondell Research & Dev Co Chromatographic column head space reducer
FR2219797B1 (en) 1973-03-01 1978-03-03 Roussel Uclaf
US4043906A (en) * 1976-03-18 1977-08-23 Varian Associates, Inc. Method and apparatus for reducing the transient effects of liquid compressibility in a liquid chromatography system
FR2573532B2 (en) 1984-11-22 1987-01-23 Groupe Indl Realisa Applic IMPROVEMENTS ON CHROMATOGRAPHY DEVICES.
FR2556099B1 (en) 1983-12-02 1986-06-20 Groupe Indl Realisa Applic IMPROVEMENT IN CHROMATOGRAPHY DEVICES
DE3477967D1 (en) 1983-12-02 1989-06-01 Groupe Ind De Realisations Et Chromatographic apparatuses
FR2606882B1 (en) * 1986-11-13 1989-01-20 Couillard Francois LIQUID PHASE CHROMATOGRAPHY APPARATUS
JP2595015B2 (en) 1988-02-25 1997-03-26 東ソー株式会社 Method for forming a packed bed of liquid chromatography column, and movable stopper type column apparatus used in the method
DE3918142A1 (en) * 1989-05-31 1990-12-13 Wiest Peter P PRESSURE MEASURING DEVICE FOR FLUIDS FLOWING IN LINE
DE4016760A1 (en) * 1990-05-25 1991-11-28 Merck Patent Gmbh CHROMATOGRAPHY SYSTEMS
JPH06123123A (en) * 1992-05-22 1994-05-06 Hitachi Constr Mach Co Ltd Hydraulic driving device
JP3189143B2 (en) * 1994-09-19 2001-07-16 株式会社ユニシアジェックス Fuel supply device for internal combustion engine
US5667675A (en) * 1996-02-29 1997-09-16 Varian Associate, Inc. Collapsible apparatus for compressing packing material in liquid chromatography columns and methods of use
US5919361A (en) * 1997-12-17 1999-07-06 Uop Llc Spring-loaded hydraulically active liquid chromatography column
FR2836230B1 (en) * 2002-02-15 2004-04-23 Novasep PROTECTION OF THE CHROMATOGRAPHIC BED IN CHROMATOGRAPHY DEVICES WITH DYNAMIC AXIAL COMPRESSION

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO02084275A1 *

Also Published As

Publication number Publication date
FR2823134B1 (en) 2003-09-19
US20040099604A1 (en) 2004-05-27
WO2002084275A1 (en) 2002-10-24
US7132053B2 (en) 2006-11-07
FR2823134A1 (en) 2002-10-11

Similar Documents

Publication Publication Date Title
WO2002084275A1 (en) Protective device for the chromatographic bed in dynamic axial compression chromatographic columns
EP0145578B1 (en) Chromatographic apparatuses
FR2836230A1 (en) PROTECTION OF THE CHROMATOGRAPHIC BED IN CHROMATOGRAPHY DEVICES WITH DYNAMIC AXIAL COMPRESSION
EP0106746B1 (en) Apparatus for packing chromatography columns
EP0642839B1 (en) Process and device for storing and dispensing a fluid product held in a container pressurized with a propellant gas
EP0811900A1 (en) Gas control and dispensing assembly for gas cylinder
FR2510705A1 (en) Pilot-controlled safety valve - has pilot valve operating in two stages with flow adaptor
BE529033A (en) Device for regulating the flow pressure of a fluid in a conduit with pilot device
FR2898064A1 (en) MODULAR CHROMATOGRAPHY DEVICE
JPH0346783B2 (en)
EP0056913B1 (en) Protective device for differential-pressure detectors against surpassing a given maximum differential pressure
WO2006108931A1 (en) Valve adjusting device for fire extinguishing systems
EP0214023B1 (en) Flow limitation device for a tap of a bottle containing gas liquefied or compressed under pressure
CA2528342C (en) Expansion valve block with co-ordinated high- and low-pressure circuit control means
EP1634002B1 (en) Filler and drain valve and cleaning tools for a pressure-fluid cylinder
FR2556099A1 (en) Improvement to chromatography apparatuses
WO1998053299A1 (en) Apparatus for titration and circulation of gases and circulation of an absorbent or adsorbent substance
FR2517360A1 (en) COMBINED INSTALLATION OF AN ACTIVATION PUMP AND A SAFETY VALVE PROVIDED BELOW SUCH A PUMP IN A HYDROCARBON PRODUCTION WELL
FR2618727A1 (en) Ink jet printers comprising a suction manifold and a manifold connected to a reservoir for storing compressed gases and vapours
FR2921489A1 (en) Product e.g. petroleum, sampling and storing device for e.g. laboratory, has cylinder closed by cover, where upper and lower plates of cylinder have sealing units defining intermediate pressurized compartment
FR2668462A1 (en) HYDROCARBON DISPENSER WITH VAPOR RECOVERY SYSTEM.
FR2458708A1 (en)
FR2573532A2 (en) Improvements to chromatography apparatuses
FR2560340A1 (en) Gas pressure regulator and installation for maintaining a gas pressure in an enclosure
EP4078013A1 (en) Device and method for filling tanks

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20031110

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Extension state: AL LT LV MK RO SI

RIN1 Information on inventor provided before grant (corrected)

Inventor name: NICOUD, ROGER-MARC

Inventor name: BLEHAUT, JEAN

Inventor name: MARKS, HARLENE

Inventor name: HAUCK, WILHELM

17Q First examination report despatched

Effective date: 20070214

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

RIC1 Information provided on ipc code assigned before grant

Ipc: G01N 30/60 20060101ALI20101105BHEP

Ipc: B01D 15/22 20060101ALI20101105BHEP

Ipc: B01D 15/20 20060101AFI20101105BHEP

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20110412