B01J20/3234

METHOD OF FORMING INTEGRATED COMPOSITE COMPRISING CONDUCTIVE CARBON NETWORK

A method for forming an integrated composite comprises providing a three-dimensional substrate having at least one channel; coating the substrate with a phenolic resin, wherein coating comprises dispersing the phenolic resin on the substrate, impregnating the phenolic resin in the substrate or a combination of both; curing the substrate and the phenolic resin; heating the cured substrate and cured phenolic resin to a temperature in a range of about 600 C. to about 1100 C. in an inert environment thereby pyrolyzing the phenolic resin, forming a conductive carbon network on, in, or both on and in the substrate; and coating a support material on, in, or both on and in the substrate to form an integrated composite.

Biochar products and method of manufacture thereof

A method for producing charcoal particles or pellets which use different additives as binders for the biochar pellets. The method includes producing a mixture with charcoal and additives selected from nanocrystalline cellulose, bentonite, and polyvinyl acetate. The mixture is created by mixing one or more of the additives with charcoal and water. The mixture is then processed in a pelletizer device. While processing, the surface of the mixture is sprayed with a liquid. Once turned into pellets by way of the pelletizer device, the resulting pellets are then dried by applying heat to the pellets. The liquid can be water or a solution of water and sodium borate.

SORBENT SYSTEMS AND METHODS

A sorbent bed may comprise a sorbent support comprising at least one of a carbon material, a polymeric material, or alumina, wherein the sorbent support comprises a plurality of pores; and an impregnant configured to absorb ammonia disposed within the plurality of pores in the sorbent support, wherein the sorbent bed comprises between 20% and 60% by weight impregnant.

CHILL-PROOFING COMPOSITE FILTER AIR AND RELATED METHODS
20180126356 · 2018-05-10 ·

A chill-proofing composite filter aid may include a filtration component and an adsorption component including precipitated silica at least partially coating the filtration component. The composite filter aid may have a pore volume of at least about 0.15 cm.sup.3/gram at an average pore size between 3 nanometers and 15 nanometers. A method for removing particles from a fluid may include providing a chill-proofing composite filter aid, pre-coating a filter element with the composite filter aid, and passing a fluid containing particles to be adsorbed through the coated filter element. A method of making a chill-proofing composite filter aid may include providing a filtration component, and at least partially coating the filtration component with an adsorption component including precipitated silica. The composite filter aid may have a pore volume of at least about 0.15 cm.sup.3/gram at an average pore size between 3 nanometers and 15 nanometers.

POROUS MATERIALS WITH CONTROLLED POROSITY; PROCESS FOR THE PREPARATION THEREOF; AND USE THEREOF FOR CHROMATOGRAPHIC SEPARATIONS

The present invention provides novel chromatographic materials, e.g., for chromatographic separations, processes for their preparation and separations devices containing the chromatographic materials. The chromatographic materials of the invention have controlled porosity and comprise a chromatographic core material and one or more layers of chromatographic surface materials which each independently provide an average pore diameter, an average pore volume, or a specific surface area such that the combined layers form a chromatographic material having a predetermined or desired pattern of porosity from the core material to the outermost surface. The materials are useful for HPLC separations, normal-phase separations, reversed-phase separations, chiral separations, HILIC separations, SFC separations, affinity separations, perfusive separations, partially perfusive separations, and SEC separations.

Adsorption device for compressed gas

An adsorption device for compressed gas or a non-compressed gas, is provided with a vessel with an inlet for the supply of a compressed gas or a non-compressed gas to be treated, and an outlet for treated gas and an adsorption element is affixed in the vessel. The adsorption element extends along the flow direction of the compressed gas or the non-compressed gas to be treated, between the inlet and the outlet. The adsorption element has a monolithic supporting structure that is at least partially provided with a coating that contains an adsorbent.

PARTICULATE HYDROXYAPATITE (HA) SUBSTRATES AND USES THEREOF

This disclosure relates to particulate hydroxyapatite (HA)-coated substrates, methods of making particulate HA-coated substrates, and methods of using particulate HA-coated substrates. Thus, the disclosure provides chromatography media composed of a particulate substrate (such as polymer beads or other particulate substrates) that is coated with HA. Also provided is a chromatography media (optionally contained within a column) comprising a HA-coated substrate (e.g., a plurality of beads or another particulate substrate that is coated with HA). The beads or particulate substrate can be a porous or non-porous substrate.

Processes For Suppressing Emission of Mercury Vapor

This invention provides processes for suppressing emission of mercury vapor from substances containing vaporizable mercury.

Chromatographic materials

In one aspect, the present invention provides a chromatographic stationary phase material for various different modes of chromatography represented by Formula 1: [X](W).sub.a(Q).sub.b(T).sub.c (Formula 1). X can be a high purity chromatographic core composition having a surface comprising a silica core material, metal oxide core material, an inorganic-organic hybrid material or a group of block copolymers thereof. W can be absent and/or can include hydrogen and/or can include a hydroxyl on the surface of X. Q can be a functional group that minimizes retention variation over time (drift) under chromatographic conditions utilizing low water concentrations. T can include one or more hydrophilic, polar, ionizable, and/or charged functional groups that chromatographically interact with the analyte. Additionally, b and c can be positive numbers, with the ratio 0.05?(b/c)?100, and a?0.

METHODS FOR THE TREATMENT OF FLUE GAS STREAMS USING SORBENT COMPOSITIONS WITH REDUCED AUTO-IGNITION PROPERTIES

An activated carbon sorbent composition comprising activated carbon and a passivation agent, wherein the activated carbon sorbent composition exhibits reduced self-heating or auto-ignition properties as compared to the activated carbon. The activated carbon sorbent composition may be utilized to sequester contaminants such as mercury from a flue gas stream. The passivation agent includes a sulfur species, and may be a sulfur oxide compound, a sulfide compound, or an organic sulfur compound. Methods for the manufacture of the activated carbon sorbent composition and for the sequestration of contaminants in a flue gas stream using the composition are also disclosed.