A separation medium for removing small molecules from biomacromolecule in aqueous mixtures comprises gel filtration chromatography beads having a nominal protein fractional range of about 1000 Da to about 5000 Da and having an internal adsorbent matrix derived from a hydrophobicized scaffold. The gel filtration chromatography beads remove small molecules that are less than 1500 Da and have log Pow values greater than about −0.5 from biomacromolecules in aqueous mixtures. Devices containing the separation medium are also provided.

A chromatographic medium having a separating agent layer, which is used to separate target substances, and a permeation layer, which is laminated so as to face the separating agent layer and which is used to enable permeation of the target substances separated by the separating agent layer, wherein a region in which the permeation layer is not laminated is present on a part of the separating agent layer, the separating agent layer exhibits a separating property for the target substances and exhibits an optical responsiveness to ultraviolet rays, and the permeation layer exhibits an optical responsiveness that is different from those of the target substances and the separating agent layer.

A chromatographic medium having a separating agent layer, which is used to separate target substances, and a permeation layer, which is laminated so as to face the separating agent layer and which is used to enable permeation of the target substances separated by the separating agent layer, wherein a region in which the permeation layer is not laminated is present on a part of the separating agent layer, the separating agent layer exhibits a separating property for the target substances and exhibits an optical responsiveness to ultraviolet rays, and the permeation layer exhibits an optical responsiveness that is different from those of the target substances and the separating agent layer.

A chromatographic medium having a separating agent layer, which is used to separate target substances, a filling agent layer, which is used to fix the target substances before the target substances are separated, and a permeation layer, which is used to enable permeation of the target substances separated by the separating agent layer, wherein the filling agent layer comes into contact with the separating agent layer via a plane that intersects the direction of development of the target substances in the chromatographic medium and is positioned on the upstream side in the direction of development, the separating agent layer exhibits separability of the target substances and optical responsiveness to ultraviolet rays, and the permeation layer exhibits an optical responsiveness that is different from those of the target substances and the separating agent layer.

A chromatographic medium having a separating agent layer, which is used to separate target substances, a filling agent layer, which is used to fix the target substances before the target substances are separated, and a permeation layer, which is used to enable permeation of the target substances separated by the separating agent layer, wherein the filling agent layer comes into contact with the separating agent layer via a plane that intersects the direction of development of the target substances in the chromatographic medium and is positioned on the upstream side in the direction of development, the separating agent layer exhibits separability of the target substances and optical responsiveness to ultraviolet rays, and the permeation layer exhibits an optical responsiveness that is different from those of the target substances and the separating agent layer.

A filtration material including a silica base material having a group represented by the following general formula (a0-1) [in formula (a0-1), Ya.sup.01 represents a divalent linking group; Ra.sup.01 represents a hydrocarbon group which may have a substituent; Ra.sup.02 represents a hydroxyl group or a hydrocarbon group having 1 to 6 carbon atoms which may have a substituent; n.sup.01 represents an integer of 0 to 5; and the symbol “*” represents a valence bond with respect to the silica base material].

##STR00001##

A filtration material including a silica base material having a group represented by the following general formula (a0-1) [in formula (a0-1), Ya.sup.01 represents a divalent linking group; Ra.sup.01 represents a hydrocarbon group which may have a substituent; Ra.sup.02 represents a hydroxyl group or a hydrocarbon group having 1 to 6 carbon atoms which may have a substituent; n.sup.01 represents an integer of 0 to 5; and the symbol “*” represents a valence bond with respect to the silica base material].

##STR00001##

Provided are: an Fc-binding protein having improved stability, particularly to heat and acid; a method for producing the protein; an antibody adsorbent using the protein; and a method for separating the antibodies using the adsorbent. Specifically provided are: an Fc-binding protein having improved stability to heat and acid, achieved by substituting an amino-acid residue in a specific position in the extracellular region of human FcyRIIIa with another specific amino acid; a method for producing the protein; an antibody adsorbent using the protein; and a method for separating the antibodies using the adsorbent.

The invention relates to a process for the preparation of polypropylene having: a molecular weight of 450,000-950,000, a molecular weight distribution of 3-6, and xylene soluble content of 2-6 wt %, by converting propylene into the polypropylene without pre-polymerization in the presence of a polymerization catalyst under a condition where the volume ratio of H.sub.2 to propylene is at most 0.0020, wherein the catalyst comprises a catalyst component and a co-catalyst, wherein the catalyst component is obtained by a process wherein a compound with formula Mg(OAlk).sub.xCl.sub.y wherein x is larger than 0 and smaller than 2, y equals 2−x and each Alk, independently, represents an alkyl group, is contacted with a titanium tetraalkoxide and/or an alcohol in the presence of an inert dispersant to give an intermediate reaction product and wherein the intermediate reaction product is contacted with titanium tetrachloride in the presence of an internal donor.

Chromatography method in which a gaseous, liquid or supercritical mobile phase containing species to be separated is circulated through a packing, said packing being characterized in that: it comprises a plurality of capillary ducts extending in the packing between an upstream face through which the mobile phase enters the packing and a downstream face through which the mobile phase leaves the packing—the material of the walls comprises a first population of connected pores, providing passages from one duct to the next enabling molecular diffusion to take place between adjacent ducts, pores having a mean diameter (d.sub.pore) of greater than 2 times the molecular diameter of at least one species to be separated—the diameter of the ducts is less than 50 μm.