A two-step one-pot process for reacting glycolaldehyde with an aminating agent in the presence of a reactive organic fluid for instance a reactive solvent is provided. The first step comprises of contacting glycolaldehyde with an aminating agent in the presence of a reactive fluid for instance a reactive solvent under inert atmosphere to produce unsaturated intermediates, and reacting the reaction mixture obtained in step 1 with hydrogen in the presence of a supported hydrogenation catalyst in a second step.

A two-step one-pot process for reacting glycolaldehyde with an aminating agent in the presence of a reactive organic fluid for instance a reactive solvent is provided. The first step comprises of contacting glycolaldehyde with an aminating agent in the presence of a reactive fluid for instance a reactive solvent under inert atmosphere to produce unsaturated intermediates, and reacting the reaction mixture obtained in step 1 with hydrogen in the presence of a supported hydrogenation catalyst in a second step.

A two-step one-pot process for reacting glycolaldehyde with an aminating agent in the presence of a reactive organic fluid for instance a reactive solvent is provided. The first step comprises of contacting glycolaldehyde with an aminating agent in the presence of a reactive fluid for instance a reactive solvent under inert atmosphere to produce unsaturated intermediates, and reacting the reaction mixture obtained in step 1 with hydrogen in the presence of a supported hydrogenation catalyst in a second step.

A two-step one-pot process for reacting glycolaldehyde with an aminating agent in the presence of a reactive organic fluid for instance a reactive solvent is provided. The first step comprises of contacting glycolaldehyde with an aminating agent in the presence of a reactive fluid for instance a reactive solvent under inert atmosphere to produce unsaturated intermediates, and reacting the reaction mixture obtained in step 1 with hydrogen in the presence of a supported hydrogenation catalyst in a second step.

A two-step one-pot process for reacting glycolaldehyde with an aminating agent in the presence of a reactive organic fluid for instance a reactive solvent is provided. The first step comprises of contacting glycolaldehyde with an aminating agent in the presence of a reactive fluid for instance a reactive solvent under inert atmosphere to produce unsaturated intermediates, and reacting the reaction mixture obtained in step 1 with hydrogen in the presence of a supported hydrogenation catalyst in a second step.

A process for the production of aromatic primary amines, by reacting an aromatic dialdehyde with hydrogen and ammonia or an ammonia-liberating compound, in the presence of a hydrogenation catalyst and an amine, wherein the molar ratio of the amine to the aromatic dialdehyde is no less than 1:4 at the start of the reaction.

A process for the production of aromatic primary amines, by reacting an aromatic dialdehyde with hydrogen and ammonia or an ammonia-liberating compound, in the presence of a hydrogenation catalyst and an amine, wherein the molar ratio of the amine to the aromatic dialdehyde is no less than 1:4 at the start of the reaction.

A process for the production of aromatic primary amines, by reacting an aromatic dialdehyde with hydrogen and ammonia or an ammonia-liberating compound, in the presence of a hydrogenation catalyst and an amine, wherein the molar ratio of the amine to the aromatic dialdehyde is no less than 1:4 at the start of the reaction.

A preparation method of substituted primary amine is disclosed. The preparation method uses cyanophenyl and a derivative thereof as raw materials, nanoporous palladium as a catalyst, and H.sub.2 as a hydrogen source, and conducts selective hydrogenation to prepare the substituted primary amine. The molar concentration of the cyanophenyl and the derivative thereof in the solvent is 0.01-2 mmol/mL, and the molar ratio of the cyanophenyl to the derivative thereof to the catalyst is 1: 0.01-1: 0.5. The size of a pore framework of the nanoporous palladium is 1 nm-50 nm. The pressure of the H.sub.2 is 0.1-20.0 MPa. The obtained product has high selectivity; the present invention has mild reaction conditions, does not need any additive, and has simple operation and post-processing and good catalyst reproducibility. After repeatedly used, the catalytic activity of the present invention is not significantly reduced, thereby providing the possibility of realizing industrialization.

A preparation method of substituted primary amine is disclosed. The preparation method uses cyanophenyl and a derivative thereof as raw materials, nanoporous palladium as a catalyst, and H.sub.2 as a hydrogen source, and conducts selective hydrogenation to prepare the substituted primary amine. The molar concentration of the cyanophenyl and the derivative thereof in the solvent is 0.01-2 mmol/mL, and the molar ratio of the cyanophenyl to the derivative thereof to the catalyst is 1: 0.01-1: 0.5. The size of a pore framework of the nanoporous palladium is 1 nm-50 nm. The pressure of the H.sub.2 is 0.1-20.0 MPa. The obtained product has high selectivity; the present invention has mild reaction conditions, does not need any additive, and has simple operation and post-processing and good catalyst reproducibility. After repeatedly used, the catalytic activity of the present invention is not significantly reduced, thereby providing the possibility of realizing industrialization.