B01J39/19

METHOD FOR PRODUCING A COMPOSITE LAYER, ELECTROCHEMICAL UNIT AND USE OF THE COMPOSITE LAYER
20210384521 · 2021-12-09 ·

A method is proposed by means of which a composite layer is producible in as simple and controlled a manner as possible, and by means of which composite layers with different predetermined properties can be produced with as little expenditure as possible, and thus economically. The method includes: providing a nanofiber material, comminuting the nanofiber material while forming nanorods, providing a liquid medium, which comprises an ionomer component and a dispersant, dispersing the nanorods in the liquid medium while forming a nanorod ionomer dispersion, and applying the nanorod ionomer dispersion to a surface region of a substrate while forming a composite layer. An electrochemical unit including the composite layer is provided. The composite layer is useful in a fuel cell (hydrogen fuel cell or direct alcohol fuel cell), in a redox flow cell, in an electrolytic cell, or in an ion exchanger, and useful for anion or proton conduction.

Matrices containing lithium aluminates

Provided is a particulate composition comprising a collection of resin beads and LiX.2Al(OH).sub.3.nH.sub.2O, wherein n is 0 to 10, wherein X is a halogen, wherein the resin beads contain polymer having 0.5 to 3 equivalents of amine pendant groups per liter of the particulate composition, wherein the resin beads have average pore diameter of 5 to 100 nm, wherein the collection of resin beads has harmonic mean particle diameter of 200-1000 micrometers; wherein the collection of resin beads has surface area of 20 to 150 m.sup.2/g; and wherein aluminum is present in an amount of 14.5% percent or higher, by weight of aluminum atoms based on the total weight of the particulate composition. Also provided is a method of removing lithium from brine using such a composition.

Matrices containing lithium aluminates

Provided is a particulate composition comprising a collection of resin beads and LiX.2Al(OH).sub.3.nH.sub.2O, wherein n is 0 to 10, wherein X is a halogen, wherein the resin beads contain polymer having 0.5 to 3 equivalents of amine pendant groups per liter of the particulate composition, wherein the resin beads have average pore diameter of 5 to 100 nm, wherein the collection of resin beads has harmonic mean particle diameter of 200-1000 micrometers; wherein the collection of resin beads has surface area of 20 to 150 m.sup.2/g; and wherein aluminum is present in an amount of 14.5% percent or higher, by weight of aluminum atoms based on the total weight of the particulate composition. Also provided is a method of removing lithium from brine using such a composition.

Process for removal of sulfur and other impurities from olefinic liquefied petroleum gas

Organic sulfur compounds which are generally present in the crude oil undergoes various transformations while processing the crude oil in the secondary processing units such as fluid catalytic cracker, hydrocracker, delayed coker, visbreaker, etc. The sulfur present in the feed which enters into these secondary processing units are distributed into various products coming out of the units. Sulfur compounds which are present in the various product fractions are removed to meet the desired specifications before routing to the final product pool. Conventionally, sulfur present in the LPG has been removed by amine treatment followed by caustic and water wash. The present invention relates to a process for removal of sulfur and other impurities from Liquefied Petroleum Gas (LPG) comprising olefins through reactive desulfurization route. The present invention is an eco-friendly process as it minimizes or eliminates the use of caustic which is conventionally used to remove the sulfur from LPG.

Process for removal of sulfur and other impurities from olefinic liquefied petroleum gas

Organic sulfur compounds which are generally present in the crude oil undergoes various transformations while processing the crude oil in the secondary processing units such as fluid catalytic cracker, hydrocracker, delayed coker, visbreaker, etc. The sulfur present in the feed which enters into these secondary processing units are distributed into various products coming out of the units. Sulfur compounds which are present in the various product fractions are removed to meet the desired specifications before routing to the final product pool. Conventionally, sulfur present in the LPG has been removed by amine treatment followed by caustic and water wash. The present invention relates to a process for removal of sulfur and other impurities from Liquefied Petroleum Gas (LPG) comprising olefins through reactive desulfurization route. The present invention is an eco-friendly process as it minimizes or eliminates the use of caustic which is conventionally used to remove the sulfur from LPG.

Melamine-based crosslinked polymer Mannich product

Crosslinked polymers made up of polymerized units of cyclic diaminoalkane, aldehyde and bisphenol-S or melamine. A method for removing heavy metals, such as Pb(II) from an aqueous solution or an industrial wastewater sample with these crosslinked polymers is introduced. A process of synthesizing the crosslinked polymers is also described.

Melamine-based crosslinked polymer Mannich product

Crosslinked polymers made up of polymerized units of cyclic diaminoalkane, aldehyde and bisphenol-S or melamine. A method for removing heavy metals, such as Pb(II) from an aqueous solution or an industrial wastewater sample with these crosslinked polymers is introduced. A process of synthesizing the crosslinked polymers is also described.

PROTON-CONDUCTIVE MEMBRANE

A proton-conductive membrane includes a hydrophobic organic polymer and a hydrophilic proton-conductive component. The hydrophilic proton-conductive component includes one of an urea-containing material and a complex formed from an acidic substance and a basic substance, and a combination thereof. The hydrophilic proton-conductive component is present in an amount ranging from 23 parts by weight to 70 parts by weight based on 100 parts by weight of the proton-conductive membrane.

PROTON-CONDUCTIVE MEMBRANE

A proton-conductive membrane includes a hydrophobic organic polymer and a hydrophilic proton-conductive component. The hydrophilic proton-conductive component includes one of an urea-containing material and a complex formed from an acidic substance and a basic substance, and a combination thereof. The hydrophilic proton-conductive component is present in an amount ranging from 23 parts by weight to 70 parts by weight based on 100 parts by weight of the proton-conductive membrane.

METHODS FOR CHROMATOGRAPHIC PROTEIN EXTRACTION AND PURIFICATION

Disclosed herein are methods and compositions for isolating a protein fraction from a potato sample. The methods include adjusting the potato sample containing the protein fraction to a pH of about 4.0 to 5.2; and loading the potato sample onto a sulfonated epoxy resin, wherein the sulfonated epoxy resin comprising Formula (I) is adjusted to a pH of about 4.0 to 4.5. The methods also include washing the sulfonated epoxy resin and eluting the protein fraction.