Method for preparing ethylene diamine from ethanolamine and ammonia serving as raw materials under hydrogen condition
A technology of ethanolamine and ethylenediamine, applied in the field of hydroxyethylpiperazine and hydroxyethylethylenediamine, aminoethylpiperazine, piperazine, and co-production of diethylenetriamine, can solve the problem of high energy consumption and equipment corrosion serious problems, to achieve the effect of improving selectivity, reducing reaction pressure and energy consumption
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Embodiment 1
[0018] The catalyst used is Ni-Re-B / Al 2 o 3 . The weight composition of the catalyst is: Ni=15%, Re=1.6%, B=1.2%, and the rest is carrier Al 2 o 3 . The carrier adopts commercial Al 2 o 3 , and the catalyst active component Ni and additives Re and B were loaded on the carrier Al by conventional impregnation method 2 o 3 (Al 2 o 3 The particle size is 20-40 mesh). 8.0 grams (about 10ml) of the catalyst was activated by hydrogen before the reaction, and the activation conditions were: GHSV=2400h -1 , Atmospheric pressure, 375°C, reduction time 5 hours. Choose a fixed bed reactor. The reaction temperature is 155°C, the hydrogen pressure is 8.0MPa, the ammonia / ethanolamine molar ratio is 10, and the H 2 / ethanolamine molar ratio is 0.015 ethanolamine liquid space velocity is 0.5h -1 , the reaction time is 50h, sampling analysis. Samples were analyzed by gas chromatography, HP-15 capillary column, and FID detector. Dimethylformamide (DMFA) was used as internal stan...
Embodiment 2
[0020] The liquid space velocity of ethanolamine is 0.3h -1 , other conditions are identical with embodiment 1.
Embodiment 3
[0022] The liquid space velocity of ethanolamine is 0.7h -1 , other conditions are identical with embodiment 1.
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