C01B2203/1041

PHOTO-THERMAL REACTIONS OF ALCOHOLS TO HYDROGEN AND ORGANIC PRODUCTS OVER METAL OXIDE PHOTO-THERMAL CATALYSTS
20190047856 · 2019-02-14 ·

Photo-thermal catalysts and methods of use are described. The photo-thermal catalyst can include a photo-active metal oxide and, optionally, a plasmon resonance material. The photo-thermal catalyst has a temperature of 150 C. to 400 C. and is in contact with electromagnetic radiation. The photo-thermal catalyst can be used in a photo-thermal method to generate hydrogen from alcohols.

Highly robust efficient catalyst for selective dehydrogenation of neat glycerol to lactic acid

A catalyst system includes a complex having formula I which advantageously has a sterically protecting N-heterocyclic carbene (NHC) carbene-pyridine ligand to handle harsh reactions conditions than many prior art catalysts: ##STR00001##
wherein M is a transition metal; o is 0, 1, 2, 3, or 4; R.sub.1 is a C.sub.1-6 alkyl, a C.sub.6-18 aryl, or an optionally substituted C.sub.5-18 heteroaryl. In a refinement, R.sub.1 is methyl, ethyl, butyl, n-propyl, isopropyl, n-butyl, sec-butyl, or t-butyl; R.sub.2, R.sub.3, R.sub.3 are independently an optionally substituted C.sub.1-6 alkyl, halo (e.g., Cl, F, Br, etc), NO.sub.2, an optionally substituted C.sub.6-18 aryl, or an optionally substituted C.sub.5-18 heteroaryl; R.sub.4, R.sub.4 are independently an optionally substituted C.sub.1-6 alkyl, halo, NO.sub.2, an optionally substituted C.sub.6-18 aryl, or an optionally substituted C.sub.5-18 heteroaryl; and X.sup. is a negatively charge counter ion and L.sub.1, L.sub.2 are each independently a neutral ligand.

HIGH PURITY HYDROGEN PRODUCTION DEVICE AND HIGH PURITY HYDROGEN PRODUCTION METHOD

A hydrogen production device is provided. The device comprises: a dry reforming reaction unit for directly reacting methane and carbon dioxide in biogas to produce a synthesis gas containing hydrogen; and a gas shift unit for reacting carbon monoxide in the synthesis gas produced in the dry reforming reaction unit with water vapor to produce carbon dioxide and hydrogen, and for capturing the produced carbon dioxide.

Production of hydrogen gas and calcium carbonate from formaldehyde

Disclosed is a method of producing hydrogen (H.sub.2) gas and calcium carbonate from formaldehyde. The method includes combining an aqueous base, formaldehyde, and a transition metal complex having a coordination bond between a transition metal and a leaving group to form a homogeneous aqueous solution having a basic pH, wherein the leaving group dissociates from the transition metal complex in response to light and/or the basic pH of the solution, producing hydrogen (H.sub.2) gas and formate or a salt thereof from the formaldehyde present in the homogeneous aqueous solution, and producing calcium carbonate using the formate or salt thereof as a carbon source.

Process for purifying synthesis gas by washing with aqueous solutions of amines

The invention relates to a process for purifying synthesis gas, comprising at least one stage for separating the crude synthesis gas to be treated into at least two effluents, namely a first part and a complementary part, in which the said first part is subjected to a carbon monoxide conversion stage with steam and the said complementary part is subjected to a COS and HCN catalytic hydrolysis stage, the two gas flows, namely the first part and complementary part, are then each treated separately in two stages intended to remove acid gases such as CO.sub.2 and H.sub.2S, by washing with aqueous solutions of specific amines, before a recombination stage of the two treated effluents.

Shaped catalyst for sour gas shift reactions and methods for using them

The disclosure provides catalyst materials in the form of annular solids with high mechanical integrity useful for water gas shift reactions and methods for using such catalyst materials, for example, for converting carbon monoxide and steam to carbon dioxide and hydrogen.

PHOTOCATALYSIS-INDUCED PARTIAL OXIDATION OF METHANOL REFORMING PROCESS FOR PRODUCING HYDROGEN
20180305206 · 2018-10-25 · ·

A photocatalyst partial oxidation of methanol reforming process can be rapidly started via the use of a photocatalytic reaction at a reaction temperature below 150 C., and hydrogen having a low carbon monoxide content is produced at a high methanol conversion rate.

Phosphor monomolecular compound, organic transistor using same, and water decomposition and hydrogen production photocatalytic system using same

The present invention relates to a phosphor monomolecular compound, an organic transistor using same, and a water splitting and hydrogen production photocatalytic system using same. More specifically, the present invention comprises a water-soluble monomolecular compound including 1,5-naphtyridine-2,6-dione structure as a phosphor monomolecular compound.

ROBUST CATALYST FOR HYDROGEN PRODUCTION FROM P-FORMALDEHYDE

Disclosed is a method of producing hydrogen from formaldehyde. The method includes mixing an aqueous base, formaldehyde, and a transition metal complex having a transition metal-halide bond to form a homogenous aqueous solution having a basic pH. The halide dissociates from the transition metal complex in response to the basic pH of the solution to produce hydrogen from the formaldehyde present in the homogeneous aqueous solution.

Microwave Reforming Apparatus for Gas Reforming

The present disclosure relates to a microwave reforming apparatus for gas reforming, and provides a new technology of converting carbon dioxide which is a main greenhouse gas generated during combustion, pyrolysis/gasification, and operation of fossil fuels, methane, and dispersions thereof into high-quality fuels. A microwave reforming apparatus according to the present disclosure uses a carbon receptor and thus can solve the conventional problem of price of catalyst and also enables compactification of a device, rapid startup and response time in several seconds, and application of various kinds of product gases including polymer hydrocarbon. Also, the microwave reforming apparatus according to the present disclosure uses its own internal reaction heat at the time of reforming and thus can maintain the optimum operating conditions for a wide range of flow rate and gas properties. Therefore, it is possible to solve the conventional problem with the time required for normal operation and the efficiency of a reforming apparatus.