Provided are sorption materials and devices using the sorption materials, and methods of using the sorption materials and devices containing the sorption materials. In various examples, the sorption materials bind to various inflammation stimulating and/or mediating molecules, which are often associated with systemic infections and systemic inflammation associated with conditions such as, for example, sepsis.

Provided are sorption materials and devices using the sorption materials, and methods of using the sorption materials and devices containing the sorption materials. In various examples, the sorption materials bind to various inflammation stimulating and/or mediating molecules, which are often associated with systemic infections and systemic inflammation associated with conditions such as, for example, sepsis.

A method of recovering substantially rare earth elements (REEs) from magnets, including first dissolving a magnet to yield a solution containing Nd, Pr, and Dy, and then equilibrating a first column with Cu2+ solution to yield a first equilibrated column, introducing the solution to the first equilibrated column, and introducing a ligand solution to the first equilibrated column to establish three bands of different liquid compositions in the column, wherein the three bands comprise a Dy/Nd mixed band, a first pure Nd band, and a Nd/Pr mixed band. Next, sending the Dy/Nd mixed band to a second column containing a Cu2+ solution and introducing a ligand solution to the second column to establish a pure Dy band and a second pure Nd band in the second column, and sending the Nd/Pr mixed band to a third column containing a Cu2+ solution and introducing a ligand solution to the third column to establish a third pure Nd band and a pure Pr band in the third column. Finally, eluting the respective pure Nd bands to recover Nd, eluting the pure Dy band to recover Dy, and eluting the pure Pr band to recover Pr.

A method for purifying a nonaqueous liquid substance includes: filling a cartridge container with a macroporous or porous type ion exchange resin in a water-wet state to obtain an ion exchange resin-filled cartridge filled with the macroporous or porous type ion exchange resin before water content reduction; reducing a water content of the macroporous or porous type ion exchange resin in the cartridge container until a water content (A) of the macroporous or porous type ion exchange resin after water content reduction becomes 90 to 97% of a water content (B) of the macroporous or porous type ion exchange resin in a saturated equilibrium state; an initial blowing step of allowing the nonaqueous liquid substance before being purified to pass inside the cartridge container filled with the macroporous or porous type ion exchange resin after water content reduction and discharging an initial blow effluent from inside the cartridge container; and purification.

The invention relates to a system and method of use for concentrating a solution that is eluted from an ion exchange process (elution solution) during an ion exchange regeneration using the osmotic pressure of the salt saturator. This method recovers solvent from the elution solution that could be used in a future ion exchange regeneration process. The concentration of the elution solution may include the precipitation and removal of solids from the elution solution.

The present invention relates to a needle (1), wherein the needle (1) comprises a channel (12) extending through the needle (1), wherein the needle (1) comprises a needle tip (11), wherein the channel (12) comprises an opening at the needle tip (11), wherein the needle (1) defines an axial direction (x), wherein the axial direction (x) defines a distal direction and a proximal direction, wherein the needle tip (11) is a distal portion of the needle (1), and wherein the needle tip (11) comprises a first surface section (112) and a second surface section (111), wherein the first surface section (112) is arranged at a first angle (α) with respect to the axial direction (x) and the second surface section (111) is arranged at a second angle (β) with respect to the axial direction (x), wherein the first angle is different from the second angle. The present invention also relates to a corresponding apparatus, system and use.

A solid fiber is described, where the solid fiber is characterized by (a) a modification degree Do/Di, in a cross section of the solid fiber of 1.20 to 8.50 where the inscribed circle diameter is denoted by Di and the circumscribed circle diameter is denoted by Do; and (b) a porous specific surface area of not less than 30 m.sup.2/g.

A chromatography device (201; 201′) comprising: – at least one chromatography material unit (203), wherein said chromatography material unit comprises a convection-based chromatography material and is of a substantially rectangular shape having a length (L) and a width (W); - at least one fluid distribution system (207) which is configured to distribute fluid into and out from the at least one chromatography material unit (203), wherein said fluid distribution system (207) comprises a distribution device (209a) and a collection device (209b) between which said chromatography material unit (203) is sandwiched, wherein said distribution device (209a) and said collection device (209b) each comprises a number of parallel grooves (255) for distribution and collection respectively of a fluid to be passed through the chromatography material unit (203), wherein said parallel grooves are reaching over substantially the whole length (L) of the chromatography material unit (203) and are distributed over substantially the whole width (W) of the chromatography material unit (203).

A protein purification process with virus inactivation or removal uses caprylic acid (octanoic acid) at acidic pH. The method comprises caprylic acid treatment as part of the chromatographic step so as to perform viral inactivation without a discontinuous process and without the requirement of attention by personnel, particularly when the pH adjustment of the eluate is performed automatically by eluting into buffer. The method of the invention further results in mycoplasmas being inactivated, and reduced impurities like Host Cell Protein (HCP).

A protein purification process with virus inactivation or removal uses caprylic acid (octanoic acid) at acidic pH. The method comprises caprylic acid treatment as part of the chromatographic step so as to perform viral inactivation without a discontinuous process and without the requirement of attention by personnel, particularly when the pH adjustment of the eluate is performed automatically by eluting into buffer. The method of the invention further results in mycoplasmas being inactivated, and reduced impurities like Host Cell Protein (HCP).