The present invention relates to a method for the separation and purification of glycoforms with an ion exchange separation material with amino-acid based endgroups.

This present invention is directed to variable affinity chromatography apparatus and methods for using the same. In particular, the polarity of the stationary phase or the mobile phase is modulated using an external stimulus. Exemplary external stimulus that can be used in the invention include, but are not limited to, electric field, electromagnetic radiation including UV, Vis, and infrared wavelengths, as well other stimuli that are known to one skilled in the art. Generally, any external stimulation that changes the polarity of a stimulus responsive material can be used. One particular embodiment of the invention provides a chromatography apparatus comprising: (i) a chromatography column having a stationary-phase separation medium contained therein; (ii) an external stimulus generator operatively connected to said chromatography column; and (iii) a chromatography mobile-phase, wherein at least one of said stationary-phase separation medium and said chromatography mobile-phase comprises a stimulus responsive material that adopts a different configuration based on the absence or the presence of said external stimulus, wherein different configurations of said stimulus responsive material results in a different stationary or mobile phase affinity, and wherein said external stimulus is selected from the group consisting of electric field, electromagnetic radiation, and a combination thereof.

A SO.sub.2 adsorption material, a preparation method therefor and an application thereof, and a method for removing SO.sub.2 from flue gas containing SO.sub.2 are provided. The SO.sub.2 adsorption material contains a carbonized metal organic framework material and a sulfite loaded on the carbonized metal organic framework material, and the carbonized metal organic framework material is a carbonized material obtained by carbonizing a metal organic framework material. On the basis of the total weight of the SO.sub.2 adsorption material, the loading amount of sulfite is not higher than 10 wt %. The SO.sub.2 adsorption material has a relatively high SO.sub.2 adsorption capacity, and may be desorbed and regenerated by heating, and the adsorption capacity still remains at a relatively high level after multiple cycles of adsorption-desorption.

The present invention relates yolk-shell nanoparticles having both a high stability towards sintering and high H.sub.25 adsorption capacities, the use of the yolk-shell nanoparticles in a method for H.sub.2S removal from gas streams, and a corresponding method for H.sub.2S removal from gas streams also comprising the regeneration of the yolk-shell nanoparticles, wherein the yolk-shell nanoparticles provide for high H.sub.2 adsorption capacities and/or high reusability.

Disclosed are systems and methods for processing liquefied natural gas (LNG). A LNG production system may include a contaminant removal process with one or more sets of sorbent beds co-loaded with a metal sulfide sorbent and/or metal oxide sorbent. In some examples, the contaminant removal process may include one or more molecular sieve dehydrators co-loaded with a 3A or 4A sieve and a 3A or 4A sieve impregnated with silver. The one or more sets of sorbent beds may be arranged at various locations throughout the LNG production system including upstream of or downstream of heavy component removal beds having activated carbon. In some instances, the LNG production system may include a regeneration process for moving heated fluid, typically feed gas, through a first heavy component removal bed while maintaining other heavy component removal beds online to reduce downtime for the LNG production system, increase production efficiency, and decrease an amount of greenhouse gases released from defrost and flare-offs.

Sorbent compositions, comprising a solid sorbent, a dispersive agent, and optionally a capture agent for enhanced wet-Flue Gas Desulfurization (wFGD) or wet scrubber unit function in a flue gas pollutant control stream is disclosed. The sorbent composition may include a sorbent with a dispersive agent, designed to enhance the dispersion of the sorbent in an aqueous sorption liquid of a wet scrubber unit, and therefore may be especially useful in EGU or industrial boiler flue gas streams that include one or more wet scrubber units. The sorbent composition may also include a capture agent useful in sequestering mercury and bromine, as well as other contaminants that may include arsenic, selenium and nitrates.

The present invention relates to an adsorbent comprising an alumina support and at least one alkali element, said adsorbent being obtained by introducing at least one alkali element, identical to or different from sodium, onto an alumina support the sodium content of which, expressed as Na.sub.2O equivalent, before the introduction of the alkali element or elements, is comprised between 1000 and 5000 ppm by weight with respect to the total weight of the support. The invention also relates to processes for the preparation of said adsorbent and use thereof in a process for the elimination of acidic molecules such as COS and/or CO.sub.2.

A separation matrix comprising porous particles to which antibody-binding protein ligands have been covalently immobilized, wherein the density of said ligands is above 5 mg/ml, the volume-weighted median diameter of said porous particles is at least 10 and below 30 μm and the said porous particles have a gel phase distribution coefficient, expressed as K.sub.D for dextran of molecular weight 110 kDa, of 0.5-0.9.

The invention relates to membranes for separation, removal, and/or concentration purposes. The object of the invention is the simple and reliable adsorption of the molecules and to simplify the desorption of target molecules that are adsorbed and chromatographically bonded on membranes, preferably without the addition of substances with a high ion content, such as acids, alkalis or salts. The object of the invention is also to develop a value that can be easily measured, which allows for an indication of the current and/or remaining binding capacity of the membrane during the adsorption process and/or the control thereof. The adsorption takes place on a charged membrane and desorption is achieved using physical, electromagnetic and/or the generation of electrical fields. This is carried out with a thin metal layer being applied to one or both sides of a positively or negatively charged membrane and a voltage is applied for desorption.

A blood treatment material adsorbs and removes blood components such as activated leukocytes and inflammatory cytokines with a high efficiency. The blood treatment material includes a water-insoluble material in the form of fibers or particles, wherein the difference between the maximum value (RaA) and the minimum value (RaB) of the arithmetic average roughness (Ra) of the surface of the water-insoluble material, as calculated using a laser microscope, is from 0.30 to 1.50 μm.