Ge Healthcare Bioprocess R&d Ab

Ge Healthcare Bio-Sciences Ab

Jamil Shanagar

James Van Alstine

Rolf Hjorth

Klaus Gebauer

Bo-Lennart Johansson

Martin Hall

Karol Lacki

Ola Lind

Kajsa Stridsberg-Friden

Mikael Berg

Gunnar Malmquist

Eggert Brekkan

Camilla Estmer Nilsson

Raf Lemmens

Elisabeth Hallgren

Kjell Eriksson

Emmanuel Macedo

Bjorn Johan Lundgren

Helena Widegren

Johanna Kjorning

Hans O Johansson

Björn Lundgren

Bjoern Lundgren

Kajsa Stridsberg-FRIDÉN

Johanna KJÖRNING

The invention provides a packing method for high efficiency chromatography columns starting from dry swellable particles, as well as columns packed by the method and the use of the columns in separation of biomolecules. In the packing method, an amount of dry swellable particles sufficient to give a swollen volume in a liquid of about 105-120% of the column chamber volume is transferred to the column, the column is closed and the liquid is provided to the column.

Method for dry packing chromatography columns

There is a recognized need for novel, more simplified, approaches to isolation of plasma from whole blood, as well as a need to isolate cell-free plasma fractions containing different plasma proteins. Methods are divulged for use of aqueous phase systems, formed in blood or blood containing solutions via addition of a single polymer at relatively low concentration, to effect isolation (clarification) of plasma proteins from blood cells. Methods are also divulged to replace widely used Cohn-type plasma protein fractionation which is based on sequential addition of up to 40% (v/v) ethanol and other precipitants, with simple sequential addition of a polyacid. The latter results in isolation of plasma protein fractions (i.e. fibrinogen, immunoglobulin, albumin) in sequence similar to that obtained with Cohn Fractionation and therefore may be suitable for use to reduce solvent use and solvent-related process complications in existing plasma protein purification processes. It may also support use of polymeric film based containers in novel solvent free plasma fractionation processes. The methods disclosed may also be suitable for use in smaller scale plasma protein isolation, in research and diagnostic applications. The general methodologies are robust and can function over a broad range of process variables such as temperature and pH.

Plasma protein fractionation by sequential polyacid precipitation

The present invention is within the field of biomolecule purification. More closely the invention relates to chromatographic purification of insulin using a specific kind of shell beads having an inner core and an outer functionalized layer. The method enables purification at high flow rates and high purity, over 90%.

Method for purification of cleaved pro-insulin

The present invention relates to a process of enriching one target compound from a liquid, which process comprises at least one step of isolation performed by differentially partitioning between two aqueous phases. In the present invention the phases are formed by adding a thermally responsive, self-associating (i.e. clouding) hydrophilic polymer, and if needed some additional salts, to an aqueous biotechnical solution (such as a fermentation sample or bioseparation process stream) under thermal and other conditions where the solution separates into a one polymer, two-phase system with one phase enriched in the polymer. The target compound is to be found in the phase not enriched in the polymer, while a significant though varying percentage of contaminants may differentially partition to the phase interface or the polymer enriched phase. With minor or no modification the target containing phase solution can be further processed via standard unit operations such as precipitation, chromatography, and filtration to further purify target and remove any residual polymer.

Separation method using single polymer phase systems

The present invention relates to a liquid mixture comprising a first polymer, which is a poly(acid), a second polymer, which is a poly(ether), and at least one salt, wherein the molecular weight of the poly(acid) is in the range of 1000-100,000 Da. The second polymer is selected to be capable of forming immiscible aqueous phases in the presence of the poly(acid) and salt. The poly(acid) may be selected from the group consisting of poly(acrylic acid) and poly(methacrylic acid), and the second synthetic polymer may comprise ethylene oxide. The invention may be used for separation of biomolecules, cells or particles.

Polymer two phase system and use thereof

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Uppsala, Sweden

Jamil Shanagar