Preparation method of piperazine and own derivatives
A derivative, piperazine technology, applied in the field of chemical drug synthesis, can solve the problems of difficulty in extraction, low piperazine content, few by-products, etc., and achieves the effects of cheap and easy-to-obtain raw materials, good product selectivity, and simple and safe operation.
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Embodiment 1
[0021] The reactor is a fixed-bed tubular reactor with an inner diameter of 25mm, a tube length of 1220mm, and a built-in catalyst of 100ml. The catalyst is Γ-Al with a mass percentage of copper of 15% and a mass percentage of nickel of 10%. 2 o 3 . The ethylene glycol aqueous solution with a mass percentage of 50% enters the catalyst bed layer at a reaction temperature of 230° C. at a flow rate of 30 g / h, the hydrogen pressure is 8 MPa, and the flow rate of the hydrogen gas is 8.2 L / h; the flow rate of liquid ammonia is 40 g / h. The reaction result is that the conversion rate of raw materials is 80%, and the effective selectivity of piperazine, N-methylpiperazine and N-ethylpiperazine is 81.5%.
Embodiment 2
[0023] Add 100ml catalyzer in above-mentioned reactor, and the composition of catalyzer is the Γ-Al that copper mass percent composition is 15%, cobalt mass percent composition is 15% 2 o 3 . The flow rate of 50% ethylene glycol aqueous solution is 30g / h into the catalyst bed with a reaction temperature of 250°C, the hydrogen pressure is 8MPa, and the flow rate of hydrogen is 9.0L / h; the flow rate of liquid ammonia is 42g / h. The result of the reaction is that the conversion rate of raw materials is 90%, and the effective selectivity of piperazine, N-methylpiperazine and N-ethylpiperazine is 85.5%. The HPLC spectrum of the product is shown in figure 1 , and the spectral data are shown in Table 1 below.
[0024] The HPLC spectrum data of table 1 product
[0025] peak time
Embodiment 3
[0027] Add 100ml catalyst in above-mentioned reactor, and the composition of catalyst is the Γ-Al that contains copper mass percent and is 5%, cobalt oxide mass percent and is 10% 2 o 3 , after the catalyst is activated, the flow rate of 30% ethylene glycol aqueous solution is 30g / h into the catalyst bed with a reaction temperature of 270°C, the hydrogen pressure is 8MPa, and the flow rate of hydrogen is 9.0L / h; the flow rate of liquid ammonia is 42g / h. The result of the reaction is that the conversion rate of raw materials is 82%, and the effective selectivity of piperazine, N-methylpiperazine and N-ethylpiperazine is 84.4%.
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