A liquid chromatographic system includes a column, a needle, a valve, a pump, and an analysis flow path. The valve sets the analysis flow path by switching between a first flow path through which an eluent flows from the valve to the column via the needle and a second flow path through which the eluent flows from the valve to the column not via the needle. The first flow path can be cleaned by drive of a first cleaning pump while the first flow path is set, and the second flow path can be cleaned by drive of the first cleaning pump while the second flow path is set.

A method for transferring a radioisotope which is fixed on a first stationary phase contained in a first chromatography column to a second stationary phase contained in a second chromatography column, to fix the radioisotope on the second stationary phase, wherein the radioisotope is selected from the radioactive isotopes of thorium, radium, lead, bismuth and uranium, the method comprising at least the following steps: a) eluting the radioisotope from the first stationary phase with an aqueous solution A1 comprising a citric acid salt as an agent complexing the radioisotope, whereby an aqueous solution A2 which comprises citrate complexes of the radioisotope is obtained; b) dissociating the citrate complexes of the radioisotope present in the aqueous solution A2 by modifying the pH of the aqueous solution A2, whereby an aqueous solution A3 comprising the decomplexed radioisotope is obtained; c) loading the second stationary phase with the aqueous solution A3; and d) washing at least one the second stationary phase with an aqueous solution A4.

A method for monitoring, evaluating and controlling a cyclic chromatographic purification process that involves at least two adsorbers. According to the method, one step is monitoring of the chromatogram, including the measurement of at least one current concentration-proportional signal in the liquid. Another step is conducting an evaluation of the chromatogram, including a comparison of at least one of the current concentration-proportional signals measured in the monitoring step with a threshold value thereof. A further step is controlling the chromatographic purification process by adapting the termination of the currently running phase as a function of the comparison of the evaluation step and initiating the next phase. Finally, according to the method, the sequence of steps is carried out in given order at least twice.

A chromatography device (1; 101) comprising: —at least one chromatography material unit (3), wherein said chromatography material unit comprises a convection-based chromatography material; —at least one fluid distribution system (7) which is configured to distribute fluid into and out from the at least one chromatography material unit (3); —an inlet (15); —at least one inlet fluid channel (17a, 17b) connecting the inlet (15) with each chromatography material unit (3) via the fluid distribution system (7); —an outlet (19); and —at least one outlet fluid channel (21) connecting the outlet (19) with each chromatography material unit (3) via the fluid distribution system (7), wherein at least some parts of said chromatography device (1; 101) are overmolded and sealed together by plastic or elastomer leaving at least the inlet (15) and the outlet (19) open.

Disclosed is a process for the purification of LNnT (lacto-N-neotetraose) from a fermentation broth, the process comprises subjecting a fermentation broth to a first step of membrane filtration, thereby providing a filtrated solution, such filtrated solution is subjecting to a second step of simulated moving bed chromatography, obtaining a purified solution thereof, then subjecting this purified solution to a third step of crystallization, obtaining crystals containing the LNnT of interest, and subjecting the crystals to a fourth and final step of drying, thereby providing a highly purified powder of LNnT.

Provided is a bioreactor arrangement for producing a biopolymer expressed by a cell and a continuous process for a capturing the biopolymer employing two chromatography units operated in series or independently.

The present invention relates to a bioreactor arrangement for producing a biopolymer expressed by a cell and a continuous process for a capturing the biopolymer employing two chromatography units operated in series or independently.

The present invention relates to a method for purifying a feed comprising at least one target product in a chromatography system having a plurality of purifying units, each having an inlet and an outlet, and a valve assembly having an outlet port and an inlet port. The inlet and the outlet of each purifying unit being connected to a respective port of the valve assembly. The method comprising loading (S10) the plurality of purifying units with feed provided through the inlet port of the valve assembly by sequentially connecting each purifying unit to the inlet port of the valve assembly: eluting (S12) the plurality of purifying units using an elution provided through the inlet port of the valve assembly by sequentially connecting each purifying unit to the inlet port of the valve assembly: and collecting (S14) the at least one target product from the outlet port of the valve.

A liquid chromatographic (LC) system is introduced which comprises at least one fluidic stream, the fluidic stream comprising a sample-injection valve, a trap-bypass-selection valve, a column-bypass valve, a load-elute valve and a trap-selection valve. Also, a liquid chromatographic (LC) system is introduced which comprises at least one fluidic stream. The fluidic stream comprises a first substream and a second substream. The first substream comprises a first sample-injection valve, a load-elute valve and a trap-selection valve. The second substream comprises a second sample-injection valve and a column-bypass valve. The fluidic stream further comprises a trap-LC substream transfer valve and a substream-selection valve. The LC systems provide a broad choice of chromatographic options and modes and enable to flexibly and rapidly switch between them.

Determining optimum operating binding capacity for a MCC process using one column, the process including N number of columns, comprises loading target product on a first column at a first residence time and/or flow rate; loading the product on the column at a second residence time and/or flow rate, the first residence time and/or flow rate being different than the second residence time and/or flow rate; generating a first breakthrough curve for the first residence time and/or flow rate and a second breakthrough curve for the second residence time and/or flow rate, wherein the first curve represents product breakthrough for the first column and the second curve represents product breakthrough for an Nth column; and using the curves to determine product loading capacity of the first column before product breakthrough at the Nth column; the product loading capacity of the first column equaling optimum operating binding capacity for the process.