The method comprises the following steps: filling a high-pressure
fixed bed reactor with a certain amount of a catalyst, reducing the catalyst by
hydrogen in advance, enabling raw materials 1, 6-hexanediol, a
solvent,
liquid ammonia and
hydrogen to pass through a
bed layer filled with the catalyst, controlling the temperature of the catalyst
bed layer, the reaction pressure and the weight hourly
space velocity of the materials, and carrying out direct hydrogenation ammoniation on the raw materials to synthesize cycloheximine. Carrying out selective
hydrogen ammonification on 1, 6-hexanediol to continuously prepare cycloheximine; the cheap
transition metal supported catalyst comprises a main catalytic
active component and a carrier. The method has the advantages of production process simplification, wide
raw material source, production and separation cost reduction,
resource utilization rate improvement, and solving of the problems of catalyst deactivation, reactant intermolecular condensation, and the like. And the technical problems that the yield of hexamethyleneimine is low, the process flow is complicated, the product quality is not high, the catalyst is easy to inactivate, and environmental
pollution is easy to generate after-treatment of the product in China at present can be solved.