Process and device for separation with variable-length

• US 6,136,198 A
• Filed: 12/10/1998
• Issued: 10/24/2000
• Est. Priority Date: 10/29/1998
• Status: Expired due to Term

• Current Assignee: Novasep Process SAS (Gilde Buy-Out Management Holding BV), Institut Francais Du Petrole (IFP Energies Nouvelles)
• Original Assignee: Institut Francais Du Petrole (IFP Energies Nouvelles)
• Inventors: Nicoud, Roger Narc, Bailly, Michel, Adam, Philippe, Ludemann-Hombourger, Olivier
• Primary Examiner(s): Therkorn, Ernest G.
• Application Number:
  US09/208,765
• Time in Patent Office: 684 Days
• Field of Search: 210/635, 210/656, 210/659, 210/662, 210/672, 210/198.2
• US Class Current: 210/659
• CPC Class Codes: B01D 15/1828 characterized by process features
• CPC Class Codes: B01D 2215/023 Simulated moving beds

Abstract

A process for separating at least one component of a mixture in a set of closed-loop chromatographic columns is described, whereby the loop comprises at least one feedstock injection point, a raffinate draw-off point, an eluant injection point, and an extract draw-off point, in which a determination is made between an injection point and a draw-off point or vice-versa a chromatographic zone, and at the end of a given period of time, all of the injection and draw-off points are shifted by one column or column section in a given direction that is defined relative to that of the flow of a main fluid that circulates through the loop. During the period, the shifting of different injection and draw-off points of a column or column section is done at different times in such a way that the lengths of the zones that are defined by said different points are variable. The process is useful for the seperation particularly of stereoisumers for pharmaceuticals.

Claims

1. A process for separating at least one component of a mixture that contains it, comprising introducing said mixture into a device that has a set of chromatographic columns or chromatographic column sections that contain an adsorbent and are arranged in series and in a closed loop, whereby the loop comprises at least one feedstock injection point, a raffinate draw-off point, an eluant injection point, and an extract draw-off point, in which a chromatographic zone is determined between an injection point and a draw-off point or vice-versa, and at the end of a given period of time, shifting all of the injection and draw-off points by one column or column section in a given direction that is defined relative to that of the flow of a main fluid that circulates through the loop, and during said period, shifting different injection and draw-off points of a column or column section at different times such that the lengths of the zones that are defined by said different points are variable.

2. A process according to claim 1, comprising at least once:

At time t1 during said period shifting the position of the injection point or draw-off point in a given direction relative to at least one zone by a column or column section in such a way as to increase the length of said zone and to reduce the length of the zone that is adjacent to said zone, and then at time t2 during said period, shifting the position of an injection or draw-off point that is relative to at least one other zone in the same direction by a column or column section in such a way as to increase the length of said other zone and to reduce the length of the zone that is adjacent to said other zone, and optionally repeating the operation such that after said time period, the same column or column section configuration as the initial configuration is regained with a shifting of all of the positions of the injection points and draw-off points of a column or a column section.

3. A process according to claim 1, wherein during the period, all of the shiftings of injection or draw-off positions are carried out with a time phase shift that is approximately constant.

4. A process according to claim 1, wherein during the period, shiftings of the positions of the injection or draw-off points are carried out with a non-constant time phase shift.

5. A process according to claim 1, wherein the flow rate of fluid that circulates in a given zone is kept approximately constant.

6. A process according to claim 1, wherein said shiftings are carried out in the same direction as that of flow in the loop.

7. A process according to claim 1, wherein at least one flow rate of fluid that circulates in an injection or draw-off line is controlled by pressure in the device.

8. A process according to claim 7, wherein the flow rate of fluid drawn off as raffinate, extract or both is controlled by pressure.

9. A process according to claim 1, wherein the eluant is a liquid or a supercritical or subcritical fluid.

10. A process according to claim 1, wherein the number of columns is less than 8.

11. A process according to claim 1, wherein the loop comprises four chromatographic zones.

12. A process for the separation of stereoisomers, comprising subjecting a mixture of stereoisomers to a process according to claim 1.

13. A process according to claim 1, wherein during the period, all of the shiftings of injection or draw-off positions are carried out with a time phase shift that is at least equal to one quarter-period.