Patent classifications
C07C67/10
METHOD FOR PRODUCING CURING AGENT OF COATING AND ITS APPLICATION ON COATING
The curing agent for coatings includes at least 1,3,5-triglycidyl benzenetricarboxylate and 1,3,5-diglycidyl benzenetricarboxylate. To produce the curing agent, 1,3,5-benzenetricarboxylic acid reacts with a base and chloropropene to produce triallyl benzene-1,3,5-tricarboxylate. Then the triallyl benzene-1,3,5-tricarboxylate reacts with a surfactant, hydrogen peroxide and a catalyst to produce 1,3,5-triglycidyl benzenetricarboxylate and/or 1,3,5-diglycidyl benzenetricarboxylate. The 1,3,5-triglycidyl benzenetricarboxylate can be applied to coatings as a curing agent.
METHANOL AND SULFURIC ACID CO-PRODUCTION SYSTEM
Disclosed is a methanol and sulfuric acid co-production system capable of producing methanol and sulfuric acid in equal equivalents. Specifically, the system includes an oxidation reaction unit configured to produce methyl bisulfate (CH.sub.3OSO.sub.3H) by reacting methane gas with an acid solution in the presence of a catalyst, a reactive distillation unit disposed downstream of the oxidation reaction unit and configured to esterify methyl bisulfate (CH.sub.3OSO.sub.3H) supplied from the oxidation reaction unit with trifluoroacetic acid (CF.sub.3COOH) to obtain a product and to separate the product into methyl trifluoroacetate (CF.sub.3COOCH.sub.3) and sulfuric acid (H.sub.2SO.sub.4) through thermal distillation, and a hydrolysis reaction unit disposed downstream of the reactive distillation unit and configured to produce methanol by hydrolyzing methyl trifluoroacetate (CF.sub.3COOCH.sub.3) supplied from the reactive distillation unit, in which the reactive distillation unit recirculates the sulfuric acid resulting from separation to the oxidation reaction unit.
METHANOL AND SULFURIC ACID CO-PRODUCTION SYSTEM
Disclosed is a methanol and sulfuric acid co-production system capable of producing methanol and sulfuric acid in equal equivalents. Specifically, the system includes an oxidation reaction unit configured to produce methyl bisulfate (CH.sub.3OSO.sub.3H) by reacting methane gas with an acid solution in the presence of a catalyst, a reactive distillation unit disposed downstream of the oxidation reaction unit and configured to esterify methyl bisulfate (CH.sub.3OSO.sub.3H) supplied from the oxidation reaction unit with trifluoroacetic acid (CF.sub.3COOH) to obtain a product and to separate the product into methyl trifluoroacetate (CF.sub.3COOCH.sub.3) and sulfuric acid (H.sub.2SO.sub.4) through thermal distillation, and a hydrolysis reaction unit disposed downstream of the reactive distillation unit and configured to produce methanol by hydrolyzing methyl trifluoroacetate (CF.sub.3COOCH.sub.3) supplied from the reactive distillation unit, in which the reactive distillation unit recirculates the sulfuric acid resulting from separation to the oxidation reaction unit.
PEROVSKITES FOR PHOTOCATALYTIC ORGANIC SYNTHESIS
Nature is capable of storing solar energy in chemical bonds via photosynthesis through a series of C—C, C—O and C—N bond-forming reactions starting from CO.sub.2 and light. Direct capture of solar energy for organic synthesis is a promising approach. Lead (Pb)-halide perovskite solar cells reach 24.2% power conversion efficiency, rendering perovskite a unique type material for solar energy capture. We show that photophysical properties of perovskites is useful in photoredox organic synthesis. Because the key aspects of these two applications are both relying on charge separation and transfer. Here we demonstrated that perovskites nanocrystals are exceptional candidates as photocatalysts for fundamental organic reactions, i.e. C—C, C—N and C—O bond-formations. Stability of CsPbBr.sub.3 in organic solvents and ease-of-tuning their bandedges garner perovskite a wider scope of organic substrate activations.
PEROVSKITES FOR PHOTOCATALYTIC ORGANIC SYNTHESIS
Nature is capable of storing solar energy in chemical bonds via photosynthesis through a series of C—C, C—O and C—N bond-forming reactions starting from CO.sub.2 and light. Direct capture of solar energy for organic synthesis is a promising approach. Lead (Pb)-halide perovskite solar cells reach 24.2% power conversion efficiency, rendering perovskite a unique type material for solar energy capture. We show that photophysical properties of perovskites is useful in photoredox organic synthesis. Because the key aspects of these two applications are both relying on charge separation and transfer. Here we demonstrated that perovskites nanocrystals are exceptional candidates as photocatalysts for fundamental organic reactions, i.e. C—C, C—N and C—O bond-formations. Stability of CsPbBr.sub.3 in organic solvents and ease-of-tuning their bandedges garner perovskite a wider scope of organic substrate activations.
Diester compound having a dimethylcyclobutane ring, a process for preparing the same, and a process for preparing dimethylcyclobutane compound derived from the diester compound
The present invention provides a process for preparing a diester compound of the following general formula (1), having a dimethylcyclobutane ring, wherein R.sup.1 and R.sup.2 represent, independently of each other, a monovalent hydrocarbon group having 1 to 10 carbon atoms, the process comprising reacting a dimethylcyclobutanone compound of the following general formula (2), wherein R.sup.1 is as defined above, with a phosphonic ester compound of the following general formula (3), wherein R.sup.2 and R.sup.3 represent, independently of each other, a monovalent hydrocarbon group having 1 to 10 carbon atoms, to produce the diester compound (1), having a dimethylcyclobutane ring. ##STR00001##
Diester compound having a dimethylcyclobutane ring, a process for preparing the same, and a process for preparing dimethylcyclobutane compound derived from the diester compound
The present invention provides a process for preparing a diester compound of the following general formula (1), having a dimethylcyclobutane ring, wherein R.sup.1 and R.sup.2 represent, independently of each other, a monovalent hydrocarbon group having 1 to 10 carbon atoms, the process comprising reacting a dimethylcyclobutanone compound of the following general formula (2), wherein R.sup.1 is as defined above, with a phosphonic ester compound of the following general formula (3), wherein R.sup.2 and R.sup.3 represent, independently of each other, a monovalent hydrocarbon group having 1 to 10 carbon atoms, to produce the diester compound (1), having a dimethylcyclobutane ring. ##STR00001##
PROCESS FOR PREPARING A CYCLOALIPHATIC DIESTER
The present invention relates to a method for producing a cycloaliphatic diester, to a method for producing a polyestercarbonate using the one cycloaliphatic diester, to the use of a cycloaliphatic diester for producing polyestercarbonates and also to a polyestercarbonate. The method according to the invention is here in particular characterized in that the cycloaliphatic diester is separated by means of distillation from the reaction mixture.
PROCESS FOR PREPARING A CYCLOALIPHATIC DIESTER
The present invention relates to a method for producing a cycloaliphatic diester, to a method for producing a polyestercarbonate using the one cycloaliphatic diester, to the use of a cycloaliphatic diester for producing polyestercarbonates and also to a polyestercarbonate. The method according to the invention is here in particular characterized in that the cycloaliphatic diester is separated by means of distillation from the reaction mixture.
METHOD FOR PREPARING 3-CHLORO-4-OXOPENTYL ACETATE USING FULLY CONTINUOUS-FLOW MICRO-REACTION SYSTEM
This disclosure relates to organic synthesis, and more particularly to a method for preparing 3-chloro-4-oxopentyl acetate using a fully continuous-flow micro-reaction system. In this method, chlorine and an acetylbutyrolactone-containing liquid are simultaneously transported to a first micro-channel reactor for continuous chlorination to obtain α-acetyl-α-chloro-γ-butyrolactone. The reaction mixture is simultaneously transported to a micro-mixer and a second micro-channel reactor together with a mixed solution of glacial acetic acid, hydrochloric acid and water, and the continuous acylation is carried out to obtain 3-chloro-4-oxopentyl acetate. After quenched with a quenching agent, the reaction mixture was subjected to extraction and separation to obtain the 3-chloro-4-oxopentyl acetate.