C07C51/295

FORMIC ACID PRODUCTION METHOD AND FORMIC ACID PRODUCTION SYSTEM

The purpose of the present invention is to provide a formic acid production method and a formic acid production system with high production efficiency and in low cost. It is a formic acid production method comprising: preparing a mixed solution by mixing a solution containing an organic substance with a metal oxide powder having a photocatalyst function; and producing a formic acid by irradiating a light to the mixed solution. Also, it is a formic acid production system comprising: a raw material charging unit into which a solution containing an organic substance and a metal oxide powder having a photocatalyst function are charged; an artificial photosynthesis reaction unit for reacting a mixed solution of the organic substance and the metal oxide powder by irradiating a sunlight or a light to the mixed solution; and a formic acid recovery unit for recovering a formic acid from the mixed solution after an artificial photosynthesis reaction.

FORMIC ACID PRODUCTION METHOD AND FORMIC ACID PRODUCTION SYSTEM

The purpose of the present invention is to provide a formic acid production method and a formic acid production system with high production efficiency and in low cost. It is a formic acid production method comprising: preparing a mixed solution by mixing a solution containing an organic substance with a metal oxide powder having a photocatalyst function; and producing a formic acid by irradiating a light to the mixed solution. Also, it is a formic acid production system comprising: a raw material charging unit into which a solution containing an organic substance and a metal oxide powder having a photocatalyst function are charged; an artificial photosynthesis reaction unit for reacting a mixed solution of the organic substance and the metal oxide powder by irradiating a sunlight or a light to the mixed solution; and a formic acid recovery unit for recovering a formic acid from the mixed solution after an artificial photosynthesis reaction.

Method for the production of 2,4-dihydroxybutyric acid
11578029 · 2023-02-14 · ·

Methods for the production of 2,4-dihydroxybutyrate (2,4-DHB) from erythrose and other four-carbon sugars are disclosed. The improved methods facilitate the production of 2,4-DHB that is a precursor for biorenewable and animal nutrition chemicals among others.

Method for the production of 2,4-dihydroxybutyric acid
11578029 · 2023-02-14 · ·

Methods for the production of 2,4-dihydroxybutyrate (2,4-DHB) from erythrose and other four-carbon sugars are disclosed. The improved methods facilitate the production of 2,4-DHB that is a precursor for biorenewable and animal nutrition chemicals among others.

Method for the production of 2,4-dihydroxybutyric acid
11578029 · 2023-02-14 · ·

Methods for the production of 2,4-dihydroxybutyrate (2,4-DHB) from erythrose and other four-carbon sugars are disclosed. The improved methods facilitate the production of 2,4-DHB that is a precursor for biorenewable and animal nutrition chemicals among others.

Heterogeneous catalyst complex for carbon dioxide conversion

Proposed is a catalyst complex having high activity for carbon dioxide conversion reaction that converts carbon dioxide to useful compounds through reaction of carbon dioxide and hydrocarbon containing at least one hydroxyl group, and a carbon dioxide conversion process using the same, wherein the catalyst complex includes, as an active metal in the catalyst complex, at least one of noble metals and at least one of transition metals other than noble metals, thereby having high activity for the carbon dioxide conversion reaction.

Heterogeneous catalyst complex for carbon dioxide conversion

Proposed is a catalyst complex having high activity for carbon dioxide conversion reaction that converts carbon dioxide to useful compounds through reaction of carbon dioxide and hydrocarbon containing at least one hydroxyl group, and a carbon dioxide conversion process using the same, wherein the catalyst complex includes, as an active metal in the catalyst complex, at least one of noble metals and at least one of transition metals other than noble metals, thereby having high activity for the carbon dioxide conversion reaction.

Highly Robust Efficient Catalyst For Selective Dehydrogenation Of Neat Glycerol To Lactic Acid
20170217870 · 2017-08-03 ·

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.

Highly Robust Efficient Catalyst For Selective Dehydrogenation Of Neat Glycerol To Lactic Acid
20170217870 · 2017-08-03 ·

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.

Highly Robust Efficient Catalyst For Selective Dehydrogenation Of Neat Glycerol To Lactic Acid
20170217870 · 2017-08-03 ·

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.