WO2020112411A3 - System for continuous purification of biochemical mixtures - Google Patents
System for continuous purification of biochemical mixtures Download PDFInfo
- Publication number
- WO2020112411A3 WO2020112411A3 PCT/US2019/062012 US2019062012W WO2020112411A3 WO 2020112411 A3 WO2020112411 A3 WO 2020112411A3 US 2019062012 W US2019062012 W US 2019062012W WO 2020112411 A3 WO2020112411 A3 WO 2020112411A3
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- module
- wash
- solution
- chromatography resin
- source
- Prior art date
Links
- 239000000203 mixture Substances 0.000 title abstract 2
- 238000000746 purification Methods 0.000 title abstract 2
- 239000012539 chromatography resin Substances 0.000 abstract 5
- 150000001875 compounds Chemical class 0.000 abstract 4
- 239000000243 solution Substances 0.000 abstract 4
- 239000003480 eluent Substances 0.000 abstract 2
- 238000010828 elution Methods 0.000 abstract 2
- 239000012527 feed solution Substances 0.000 abstract 2
- 239000011347 resin Substances 0.000 abstract 1
- 229920005989 resin Polymers 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/02—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor with moving adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
- B01D15/08—Selective adsorption, e.g. chromatography
- B01D15/26—Selective adsorption, e.g. chromatography characterised by the separation mechanism
- B01D15/38—Selective adsorption, e.g. chromatography characterised by the separation mechanism involving specific interaction not covered by one or more of groups B01D15/265 - B01D15/36
- B01D15/3804—Affinity chromatography
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/18—Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/08—Flat membrane modules
- B01D63/082—Flat membrane modules comprising a stack of flat membranes
- B01D63/084—Flat membrane modules comprising a stack of flat membranes at least one flow duct intersecting the membranes
- B01D63/085—Flat membrane modules comprising a stack of flat membranes at least one flow duct intersecting the membranes specially adapted for two fluids in mass exchange flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/08—Flat membrane modules
- B01D63/088—Microfluidic devices comprising semi-permeable flat membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
- C07K1/34—Extraction; Separation; Purification by filtration, ultrafiltration or reverse osmosis
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
- C07K1/36—Extraction; Separation; Purification by a combination of two or more processes of different types
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/25—Recirculation, recycling or bypass, e.g. recirculation of concentrate into the feed
- B01D2311/252—Recirculation of concentrate
- B01D2311/2523—Recirculation of concentrate to feed side
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/26—Further operations combined with membrane separation processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/26—Further operations combined with membrane separation processes
- B01D2311/2674—Condensation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/26—Further operations combined with membrane separation processes
- B01D2311/2697—Chromatography
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2315/00—Details relating to the membrane module operation
- B01D2315/04—Reciprocation, oscillation or vibration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2315/00—Details relating to the membrane module operation
- B01D2315/10—Cross-flow filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2317/00—Membrane module arrangements within a plant or an apparatus
- B01D2317/02—Elements in series
- B01D2317/022—Reject series
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2317/00—Membrane module arrangements within a plant or an apparatus
- B01D2317/06—Use of membrane modules of the same kind
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/04—Backflushing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/18—Use of gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/20—By influencing the flow
- B01D2321/2033—By influencing the flow dynamically
- B01D2321/2058—By influencing the flow dynamically by vibration of the membrane, e.g. with an actuator
Abstract
A multimodule system for continuous purification of biochemical mixtures is provided. The system includes at least one immobilization module in which chromatography resin from a resin source is contacted with a feed solution from a feed source to bind target compounds from the feed solution with the chromatography resin. The system also includes at least one wash module fluidly connected to the at least one immobilization module and to a wash solution source, wherein in the wash module, chromatography resin having target compounds bound thereto is contacted with a wash solution. The system further includes at least one elution module fluidly connected to the at least one wash module and to an eluent solution source, wherein in the elution module, chromatography resin having target compounds bound thereto is contacted with an eluent solution to release the target compounds from the chromatography resin.
Applications Claiming Priority (8)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201862773635P | 2018-11-30 | 2018-11-30 | |
US201862773625P | 2018-11-30 | 2018-11-30 | |
US201862773838P | 2018-11-30 | 2018-11-30 | |
US201862773618P | 2018-11-30 | 2018-11-30 | |
US62/773,838 | 2018-11-30 | ||
US62/773,618 | 2018-11-30 | ||
US62/773,625 | 2018-11-30 | ||
US62/773,635 | 2018-11-30 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2020112411A2 WO2020112411A2 (en) | 2020-06-04 |
WO2020112411A3 true WO2020112411A3 (en) | 2020-08-20 |
Family
ID=68916561
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2019/062012 WO2020112411A2 (en) | 2018-11-30 | 2019-11-18 | System for continuous purification of biochemical mixtures |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO2020112411A2 (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20170045483A1 (en) * | 2014-04-23 | 2017-02-16 | Oleg Shinkazh | High efficiency continuous countercurrent tangential chromatography |
-
2019
- 2019-11-18 WO PCT/US2019/062012 patent/WO2020112411A2/en active Application Filing
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20170045483A1 (en) * | 2014-04-23 | 2017-02-16 | Oleg Shinkazh | High efficiency continuous countercurrent tangential chromatography |
Non-Patent Citations (5)
Title |
---|
AMIT K. DUTTA ET AL: "Performance optimization of continuous countercurrent tangential chromatography for antibody capture", BIOTECHNOLOGY PROGRESS, vol. 32, no. 2, 1 March 2016 (2016-03-01), pages 430 - 439, XP055666229, ISSN: 8756-7938, DOI: 10.1002/btpr.2250 * |
ERNO PUNGOR ET AL: "1987 Nature Publishing Group http://www.nature.com/naturebiotechnology @BULLET CONTINUOUS AFFINITY-RECYCLE EXTRAfflON: A NOVEL PROTEIN SEPARATION TECHNIQUE", 30 June 1987 (1987-06-30), XP055666011, Retrieved from the Internet <URL:https://www.nature.com/articles/nbt0687-604.pdf?proof=true> [retrieved on 20200206] * |
GORDON N F ET AL: "AN OVERVIEW OF CONTINUOUS PROTEIN PURIFICATION PROCESSES", BIOTECHNOLOGY ADVANCES, ELSEVIER PUBLISHING, BARKING, GB, vol. 8, 1 January 1990 (1990-01-01), pages 741 - 762, XP000601595, ISSN: 0734-9750, DOI: 10.1016/0734-9750(90)91995-S * |
S LABORIE ET AL: "Flux Enhancement bv a Continuous Tangential Gas Flow in Ultrafiltra- tion Hollow Fibres for Drinking Water Production: Effects of Slug Flow on Cake Structure", 30 May 1996 (1996-05-30), XP055666234, Retrieved from the Internet <URL:https://www.sciencedirect.com/science/article/pii/S0015188297814139> [retrieved on 20200207] * |
Y. WIBISONO ET AL: "Two-phase flow in membrane processes: A technology with a future", JOURNAL OF MEMBRANE SCIENCE, vol. 453, 1 March 2014 (2014-03-01), NL, pages 566 - 602, XP055666211, ISSN: 0376-7388, DOI: 10.1016/j.memsci.2013.10.072 * |
Also Published As
Publication number | Publication date |
---|---|
WO2020112411A2 (en) | 2020-06-04 |
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