Method for synthesizing 2-methyl triethylene diamine by catalyzing ethylenimine
A technology of methyltriethylenediamine and methylpiperazine, which is applied in the field of catalyzing ethyleneimine and 2-methylpiperazine to synthesize 2-methyltriethylenediamine, and can solve the problems of multiple synthesis steps and product selectivity. Low-level problems to achieve obvious advantages
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Embodiment 1
[0017] A fixed bed reactor is adopted, and the size of the reactor is 700mm×Φ40mm×6mm. The reaction is carried out under normal pressure, with HZSM-5 (n(Si / Al)=200) as the catalyst, the loading volume is 30mL, and the ethyleneimine aqueous solution of 2-methylpiperazine is used as the raw material, wherein the ethyleneimine: The mass ratio of 2-methylpiperazine: water is 5:20:80, firstly through the advection pump, then preheated by the preheater and then enter the fixed bed reactor, the reaction temperature is 370°C, and the liquid space velocity is 1h -1 . After the reaction was stable for 6 hours, sampling and analysis showed that the conversion rate of 2-methylpiperazine was 51.1%, and the selectivity of 2-methyltriethylenediamine was 75.8%.
Embodiment 2
[0019] Adopt fixed bed reactor, reactor size is the same as embodiment 1. The reaction is carried out under normal pressure, using HZSM-11 (n(Si / Al)=120) as the catalyst, the loading capacity is 30mL, and the ethyleneimine aqueous solution of 2-methylpiperazine is used as the raw material, wherein the ethyleneimine: The mass ratio of 2-methylpiperazine: water is 10:18:70, firstly through the advection pump, then preheated by the preheater and then enter the fixed bed reactor, the reaction temperature is 360°C, and the liquid space velocity is 1h -1 . After the reaction was stable for 6 hours, sampling and analysis showed that the conversion rate of 2-methylpiperazine was 63.7%, and the selectivity of 2-methyltriethylenediamine was 68.6%.
Embodiment 3
[0021] Adopt fixed bed reactor, reactor size is the same as embodiment 1. The reaction is carried out under normal pressure, with Mn-ZSM-5 (n(Si / Mn)=210) as the catalyst, the loading capacity is 30mL, and the ethyleneimine aqueous solution of 2-methylpiperazine is used as the raw material, wherein the ethyleneimine The mass ratio of amine:2-methylpiperazine:ammonia water is 8:20:80. It first passes through the advection pump, then preheats through the preheater and then enters the fixed bed reactor. The reaction temperature is 350°C and the liquid space velocity is 0.8h -1 . After the reaction was stable for 6 hours, sampling and analysis showed that the conversion rate of 2-methylpiperazine was 47.3%, and the selectivity of 2-methyltriethylenediamine was 58.7%.
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