Synthesis method of multi-element tertiary amine
A synthesis method and technology for polyvalent tertiary amines, which are applied in chemical instruments and methods, preparation of amino compounds, preparation of organic compounds, etc., can solve the problems affecting reaction yield and long reaction time, and achieve high yield and short reaction time. , the effect of less by-products
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Embodiment 1
[0025] Catalyst preparation: take nano-powders of aluminum silicate, tin oxide, and antimony oxide with a mass ratio of 2:1:1, and disperse nano-powders of calcium silicate, tin oxide, and antimony oxide in a solution with a mass concentration of 1% sodium benzoate. Dispersion liquid, the quality of the dispersion liquid is 5~100 times of the total mass of zinc silicate, tin oxide, and antimony oxide nanopowder; adding molecular sieve to the dispersion liquid, the particle size of the molecular sieve is 100±50 μm, and the dispersion liquid added with molecular sieve is Stir to make the molecular sieve microspheres evenly distributed in the dispersion liquid, and then use an ultrasonic instrument to ultrasonicate the dispersion liquid for 2 hours; filter the ultrasonic dispersion liquid, and place the filtered molecular sieve in a muffle furnace for roasting. The temperature was 750°C, and the calcination time was 2 hours; the loading amount of active components on the loaded ca...
Embodiment 2
[0030] Catalyst preparation: take calcium silicate, tin oxide, and antimony oxide nano-powders with a mass ratio of 3:1:1, and disperse aluminum silicate, tin oxide, and antimony oxide nano-powders in a mass concentration of 1% sodium benzoate solution. Dispersion liquid, the quality of the dispersion liquid is 5~100 times of the total mass of zinc silicate, tin oxide, and antimony oxide nanopowders; add activated alumina microspheres to the dispersion liquid, the particle size of the activated alumina microspheres is 100±50 μm, Stir the dispersion liquid with alumina microspheres, so that the microspheres are evenly distributed in the dispersion liquid, and then use an ultrasonic instrument to ultrasonicate the dispersion liquid for 2 hours, and filter the ultrasonic dispersion liquid, and obtain The microspheres were calcined in a muffle furnace at a temperature of 600°C and a calcining time of 4 hours. The loading rate of the active components of the catalyst after loading w...
Embodiment 3
[0035] The catalyzer that embodiment 2 obtains is filled in the stainless steel 316L microreactor, and wherein the single module liquid holding capacity of microreactor is 300ml, and flow channel cross-section is 8mm 2 .
[0036] The by-product raw materials N,N-dimethyl-1,3-propanediamine, N,N,N'-trimethyl-1,3-propanediamine, N,N,N',N'-tetra Methyl-1,3-propylenediamine and methanol are passed into the reactor, and methanol is added to N,N-dimethyl-1,3-propylenediamine, N,N,N'-trimethyl- The molar ratio of 1,3-propanediamine to methanol is [2n(N,N-dimethyl-1,3-propanediamine)+n(N,N,N'-trimethyl-1,3- Propylenediamine)]: n methanol = 1:1.2, the reaction temperature was controlled at 150°C, the reaction pressure was 3.0MPa, the residence time was 35min, and the reaction conversion rate was tested by gas chromatography to be 92.26%.
[0037] Pass the reacted reaction liquid into the azeotropic rectification system for rectification. The tail gas (dimethyl ether) in the distillat...
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