Patent classifications
C25B3/00
ELECTROCHEMICALLY ENGINEERED SURFACE OF HYDROGELS, PARTICULARLY PEG HYDROGELS, FOR ENHANCED CELLULAR PENETRATION
The invention relates to a polymer structure (1) formed by at least a polymer, wherein said structure (1) comprises a volume (2) and a surface (3), wherein said polymer comprises a plurality of polymer chains connected by linkings, characterized by a linking density, wherein said linking density increases, particularly monotonously, from the surface (3) into the volume (2) of the polymer structure (1).
ELECTROCHEMICALLY ENGINEERED SURFACE OF HYDROGELS, PARTICULARLY PEG HYDROGELS, FOR ENHANCED CELLULAR PENETRATION
The invention relates to a polymer structure (1) formed by at least a polymer, wherein said structure (1) comprises a volume (2) and a surface (3), wherein said polymer comprises a plurality of polymer chains connected by linkings, characterized by a linking density, wherein said linking density increases, particularly monotonously, from the surface (3) into the volume (2) of the polymer structure (1).
METHOD FOR PREPARING IMIDE SALTS CONTAINING A FLUOROSULFONYL GROUP
The present invention concerns a method for preparing a compound of the following formula (III): R.sub.2(SO.sub.2)NM(SO.sub.2)F (III) in which R.sub.2 represents one of the following radicals: F, CF.sub.3, CHF.sub.2, CH.sub.2F, C.sub.2HF.sub.4, C.sub.2H.sub.2F.sub.3, C.sub.2H.sub.3F.sub.2, C.sub.2F, C.sub.3F.sub.7, C.sub.3H.sub.4F.sub.3, C.sub.3HF.sub.6, C.sub.4F.sub.9, C.sub.4H.sub.2F.sub.7, C.sub.4H.sub.4F, CF.sub.11, C.sub.6F.sub.13, C.sub.7F.sub.1, C.sub.8F.sub.17 or C.sub.9F.sub.19. M represents a monovalent or divalent cation; the method comprising: a step b) of fluorinating a compound of the following formula (I): R.sub.1(SO.sub.2)NH(SO.sub.2)Cl (I) in which R represents one of the following radicals: Cl, F, CF.sub.3, CHF.sub.2, CH.sub.2F, C.sub.2HF.sub.4, C.sub.2H.sub.2F.sub.3, C.sub.2H.sub.3F.sub.2, C.sub.2F, C.sub.3F.sub.7, C.sub.3H.sub.4F.sub.3, C.sub.3HF.sub.6, C.sub.4F.sub.9, C.sub.4H.sub.2F.sub.7, C.sub.4H.sub.4F, CF.sub.11, C.sub.6F.sub.13, C.sub.7F.sub.15, C.sub.8F.sub.17 or C.sub.9F.sub.19, R preferably representing Cl; with at least one fluorinating agent; 2a step c) of distilling the composition obtained in step b).
Process for starting mode or stand-by mode operation of a power-to-gas unit comprising a plurality of high-temperature electrolysis (SOEC) or co-electrolysis reactors
The application relates to a process for operating in starting mode or in stand-by mode a unit, termed power-to-gas unit, comprising a number N of reactors (1) with a stack of elemental electrolysis cells of solid oxide type (SOEC), the cathodes of which are made of methanation reaction catalyst material(s).
Process for starting mode or stand-by mode operation of a power-to-gas unit comprising a plurality of high-temperature electrolysis (SOEC) or co-electrolysis reactors
The application relates to a process for operating in starting mode or in stand-by mode a unit, termed power-to-gas unit, comprising a number N of reactors (1) with a stack of elemental electrolysis cells of solid oxide type (SOEC), the cathodes of which are made of methanation reaction catalyst material(s).
Electrochemical conversion of hydrocarbons
An electrochemical conversion method for converting at least a portion of a first mixture comprising hydrocarbon to C.sub.2+ unsaturates by repeatedly applying an electric potential difference, V(.sub.1), to a first electrode of an electrochemical cell during a first time interval .sub.1; and reducing the electric potential difference, V(.sub.1), to a second electric potential difference, V(.sub.2), for a second time interval .sub.2, wherein .sub.2.sub.1. The method is beneficial, among other things, for reducing coke formation in the electrochemical production of C.sub.2+ unsaturates in an electrochemical cell. Accordingly, a method of reducing coke formation in the electrochemical conversion of such mixtures and a method for electrochemically converting carbon to C.sub.2+ unsaturates as well as an apparatus for such methods are also provided.
Electrochemical conversion of hydrocarbons
An electrochemical conversion method for converting at least a portion of a first mixture comprising hydrocarbon to C.sub.2+ unsaturates by repeatedly applying an electric potential difference, V(.sub.1), to a first electrode of an electrochemical cell during a first time interval .sub.1; and reducing the electric potential difference, V(.sub.1), to a second electric potential difference, V(.sub.2), for a second time interval .sub.2, wherein .sub.2.sub.1. The method is beneficial, among other things, for reducing coke formation in the electrochemical production of C.sub.2+ unsaturates in an electrochemical cell. Accordingly, a method of reducing coke formation in the electrochemical conversion of such mixtures and a method for electrochemically converting carbon to C.sub.2+ unsaturates as well as an apparatus for such methods are also provided.
Impregnation of a non-conductive material with an intrinsically conductive polymer
Composite materials are made by impregnating a non-conductive material with a conducting monomer to form a monomer-impregnated non-conductive material, and polymerizing the monomer-impregnated non-conductive material to form the composite material. The composite materials are used in medical devices and implants.
Impregnation of a non-conductive material with an intrinsically conductive polymer
Composite materials are made by impregnating a non-conductive material with a conducting monomer to form a monomer-impregnated non-conductive material, and polymerizing the monomer-impregnated non-conductive material to form the composite material. The composite materials are used in medical devices and implants.
POROUS ELECTRODE FOR THE ELECTROCHEMICAL REACTION OF ORGANIC COMPOUNDS IN TWO IMMISCIBLE PHASES IN AN ELECTROCHEMICAL FLOW REACTOR
A method for the electrochemical reaction of an organic material, and a device in which a corresponding method is carried out including a porous electrode for the electrochemical reaction of organic compounds in two immiscible phases in an electrochemical flow reactor. A first nonpolar solvent and a first polar electrolyte or a first organic material in the form of a liquid or gas and the first polar electrolyte form a first phase boundary with one another in such a form that the first phase boundary in the electrochemical conversion is at least partly within a first electrode, preferably at an interface between a first lipophilic layer and a second hydrophilic layer.