Abstract: Processes for increasing an affinity of a filter media to airborne viral particles. A fiber substrate comprising borosilicate is provided. The fiber substrate may comprise acidic functional groups. A metal salt solution is introduced to the fiber substrate to form a treated substrate. The metal salt solution includes divalent and/or trivalent metal cations. The pH of the metal salt solution is adjusted, and a divalent and/or trivalent metal cation is exchanged with a proton from the acidic functional groups. The metal may be present in an amount ranging from about 0.001 to about 3.0 wt. % of the treated fiber substrate. The treated fiber substrate is incorporated into a filter media before or after the deposition of the metal onto the fiber substrate.

Abstract: A composite virucidal filter media is described. The filter media comprises a fibrous substrate comprising a plurality of intermingled fibers, a low cost, nontoxic, hydrophilic polymer without acidic functional groups deposited on a surface of the fibers without the formation of a continuous coating layer on the substrate, and a virucidal metal, a virucidal metal-containing compound, or combinations thereof deposited on the surface of the fibers comprising the hydrophilic polymer without acidic functional groups. The hydrophilic polymer without acidic functional groups can be charged or non-charged. Methods of making virucidal fibrous filter media are also described.

Abstract: Processes for treating a fiber substrate are disclosed. A fiber substrate comprising borosilicate with acidic functional groups. A metal salt solution is introduced to the fiber substrate. The metal salt solution includes cations having an ionic charge of +2 or greater. The pH of the metal salt solution may be adjusted, and the cations are deposited on the glass fibers. The treated fiber substrate may be utilized to form a filter media.

Abstract: Processes for increasing the viricidal activity of a fiber substrate. The fiber substrate is provided. An antiviral treatment containing a quaternary ammonium or phosphonium compound is introduced to the fiber substrate to form an antiviral substrate. The treated fiber substrate is washed and dried. The antiviral treatment may occur before or after the fiber substrate is incorporated into the HEPA filter media in a papermaking process. Also a filter made from treated fiber substrates.

Abstract: Processes for increasing a viricidal activity of a fiber substrate. The fiber substrate is provided. The fiber substrate may comprise acidic functional groups and may be acid leached to provide additional acidic groups. Metal ions may thereafter be exchanged with a proton from the acidic functional groups. A divalent metal is introduced to the fiber substrate. An antiviral metal is introduced and deposited onto the fiber substrate by galvanic displacement. Subsequently, a further antiviral metal is introduced and deposited on the fiber substrate by an electroless process. The treated fiber substrate is washed and dried. The deposition of antiviral metals onto the fiber substrate to form a treated fiber substrate may occur before or after the fiber substrate is incorporated into a filter media in a wet-laid paper making process.

Abstract: Processes for increasing a virucidal activity of a fiber substrate are disclosed. A fiber substrate comprising borosilicate is provided. The fiber substrate may comprise acidic functional groups. An antiviral metal salt solution is introduced to the fiber substrate to form an antiviral substrate. The pH of the antiviral metal salt solution is adjusted, and an antiviral metal ion is exchanged with a proton from the acidic functional groups. The antiviral metal is present in an amount ranging from about 0.001 to about 3.0 wt. % of the antiviral fiber substrate. The antiviral fiber substrate is incorporated into a filter media before or after the deposition of the antiviral metal onto the fiber substrate.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.

Abstract: A process for removing at least one product from coal tar is described. The process involves extraction with an extraction agent or adsorption with an adsorbent. The extraction agent includes at least one of amphiphilic block copolymers, cyclodextrins, functionalized cyclodextrins, and cyclodextrin-functionalized polymers, and the adsorbent includes exfoliated graphite oxide, thermally exfoliated graphite oxide or intercalated graphite compounds.

Abstract: A process for purifying at least one product from coal tar is described. The process involves separating a coal tar fraction having a boiling point in the range of about 180° C. to about 230° C. into an acidic portion and a non-acidic portion by contacting the fraction with a caustic compound. The acidic portion is separated into a cresol portion and a xylenol portion, and the non-acidic portion is separated into a naphthalene portion and a naphthalene co-boiler portion. The acidic portion and the non-acidic portions are separated by contacting with an adsorbent comprising small, discrete crystallites, the adsorbent having less than 10 wt % amorphous binder component. The various portions can be separated in a similar manner.