Continuous countercurrent spiral chromatography
Inventors
Shinkazh, Oleg • FEDORENKO, Dmitriy
Assignees
Interested in licensing this patent?
MTEC can help explore whether this patent might be available for licensing for your application.
Abstract
A system, module and method for continuous countercurrent spiral chromatography are disclosed. The module includes an input port for receiving an input solution, a first mixer for mixing the input solution with a recycled solution to produce a first mixed output, a stage I separator for concentrating the first mixed output to produce a stage I solid fraction, a second mixer for mixing the stage I solid fraction from the stage I separator and an optional buffer solution to produce a second mixed output, and a stage II separator for concentrating the second mixed output to produce a stage II solid fraction which exits the module. At least one separator is a spiral separator. The system includes a plurality of modules, and at least one of the plurality of modules includes a spiral separator. The method includes purifying an unpurified solution with the plurality of modules.
Core Innovation
The invention provides a continuous countercurrent spiral chromatography module in which an input solution is received at a first input port and mixed with a recycled solution to produce a first mixed output. The first mixed output is concentrated in a stage I separator to form a stage I solid fraction with a stage I liquid fraction exiting via a first output port. A second mixer mixes the stage I solid fraction with an optional buffer solution to produce a second mixed output.
The second mixed output is concentrated in a stage II separator to produce a stage II solid fraction that exits via a second output port, while a stage II liquid fraction exits via a third output port. A pump provides recycled solution that flows countercurrent to the input solution into the second input port. At least one of the stage I separator and the stage II separator is a spiral separator including a curvilinear channel arranged and disposed to generate at least one Dean vortex.
The spiral separator includes at least one inlet, at least one liquid fraction outlet, and at least one solid fraction outlet. In additional embodiments, a continuous countercurrent spiral chromatography system includes a binding step module for binding product from an unpurified product solution with a resin slurry, a washing step module for washing impurities from the resin slurry, and a regeneration step module for regenerating the resin slurry.
In further embodiments, a method purifies an unpurified solution using continuous countercurrent spiral chromatography with a plurality of modules that may include binding, washing, optionally elution, capturing purified product solution, regeneration of the resin slurry, and providing buffer solutions.
Claims Coverage
The partial content contains three independent claims: a continuous countercurrent spiral chromatography module, a continuous countercurrent spiral chromatography system with binding, washing, and regeneration, and a method for purifying an unpurified solution using continuous countercurrent spiral chromatography. Each independent claim centers on the same two-stage continuous module architecture with countercurrent recycling and spiral separation that generates Dean vortices, with system and method claims extending the architecture to process modules and purification steps.
Continuous countercurrent spiral chromatography module architecture with countercurrent recycling
A continuous countercurrent spiral chromatography module comprising a first input port for receiving an input solution; a first mixer for mixing the input solution with a recycled solution to produce a first mixed output; a stage I separator for concentrating the first mixed output to produce a stage I solid fraction and a stage I liquid fraction exiting via a first output port; a second mixer for mixing the stage I solid fraction with an optional buffer solution to produce a second mixed output; a stage II separator for concentrating the second mixed output to produce a stage II solid fraction and a stage II liquid fraction exiting via a third output port; at least one pump where the recycled solution flows countercurrent to the input solution; and wherein at least one of the stage I separator and the stage II separator is a spiral separator.
Spiral separator with Dean vortex generation for liquid and solid fraction outlets
In the module, at least one of the stage I separator and the stage II separator is a spiral separator including at least one inlet; a curvilinear channel arranged and disposed to generate at least one Dean vortex; at least one liquid fraction outlet; and at least one solid fraction outlet.
Continuous countercurrent spiral chromatography system with binding, washing, and regeneration modules
A continuous countercurrent spiral chromatography system having a plurality of modules comprising a binding step module for binding product from an unpurified product solution with a resin slurry; a washing step module for washing impurities from the resin slurry; and a regeneration step module for regenerating the resin slurry; wherein at least one of the plurality of modules is a continuous countercurrent spiral chromatography module with a first mixer mixing the input solution with a recycled solution, stage I and stage II separators concentrating first and second mixed outputs into stage I and stage II solid fractions, and countercurrent flow of the recycled solution to the input solution into the second input port; and wherein at least one of the stage I separator and the stage II separator is a spiral separator generating at least one Dean vortex.
Method of purifying an unpurified solution by continuous countercurrent spiral chromatography
A method for purifying an unpurified solution by continuous countercurrent spiral chromatography with a plurality of modules comprising receiving the unpurified solution; receiving resin slurry from a resin slurry tank for containing the resin slurry; a binding step for binding product in the unpurified product solution to the resin slurry; a washing step for washing impurities from the resin slurry; optionally an elution step for eluting product from the resin slurry after the washing step; capturing purified product solution; a regeneration step for cleaning the resin slurry; and providing buffer solutions for the steps; wherein at least one module is a continuous countercurrent spiral chromatography module including first and second mixers, stage I and stage II separators concentrating mixed outputs into stage I and stage II solid fractions and liquid fractions exiting via output ports, countercurrent flow of the recycled solution to the input solution into the second input port, and at least one spiral separator generating at least one Dean vortex.
Spiral separation generating Dean vortices within a continuous countercurrent purification module
In the method, wherein at least one of the stage I separator and the stage II separator is a spiral separator including at least one inlet; a curvilinear channel arranged and disposed to generate at least one Dean vortex; at least one liquid fraction outlet; and at least one solid fraction outlet.
Across the independent claims, the core claim coverage is for a continuous countercurrent spiral chromatography architecture using first and second mixers, stage I and stage II separators producing solid and liquid fractions, and a recycled solution that flows countercurrent to the input. At least one separator is a spiral separator with a curvilinear channel generating Dean vortices and providing liquid and solid outlets. The system and method independent claims further incorporate binding, washing, regeneration, and optionally elution and capture using resin slurry and buffers with the same continuous countercurrent spiral module.
Stated Advantages
Documented Applications
No documented applications found
Interested in licensing this patent?