Device and method for continuously synthesizing o-aminobenzeneethanol by microreactor method
A technology of microreactor and o-aminobenzene, which is applied in chemical instruments and methods, preparation of organic compounds, preparation of amino hydroxyl compounds, etc., can solve unfavorable process scale, continuous production, expensive catalysts, increased production costs, etc. problems, to achieve the effect of good product quality, low production cost and high production efficiency
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Embodiment 1
[0037] refer to figure 1 , a device for continuously synthesizing o-aminophenethyl alcohol with a microreactor method, comprising a jet mixer 1, a first microreactor 2, a second microreactor 3 and a product collection tank 4 connected in sequence, the jet The inlet end of mixer 1 communicates with the first component tank 5 and the second component tank 6 respectively, and the outlet port of jet mixer 1 communicates with the inlet end of the first microreactor 2, and the first microreactor 2 The outlet port of the second microreactor 3 is communicated with the inlet port of the second microreactor 3, and the outlet port of the second microreactor 3 is communicated with the product collection tank 4, and the inlet port of the second microreactor 3 is also connected with the gas distributor 7 connected.
[0038] The first component tank 5 communicates with the jet mixer 1 through the first metering pump 8, and the second component tank 6 communicates with the jet mixer 1 throug...
Embodiment 2
[0041] refer to figure 1 , a kind of micro-reactor method continuously synthesizes the method for anthranilol, comprises the steps:
[0042](1) Thoroughly mix 57.2g of 2-chloro-6-nitrotoluene and 13ml of dimethyl sulfoxide as the first component, and place it in the first component tank 5; mix 10g of paraformaldehyde, 0.457g of hydrogen Sodium oxide was dissolved in 37ml of methanol as the second component, placed in the second component tank 6. The first component in the first component tank 5 and the second component in the second component tank 6 are simultaneously input into the T-type jet mixer 1 by corresponding first metering pump 8 and second metering pump 9 Mixed, then enter the first microreactor 2 for hydroxymethylation reaction, the first microreactor diameter is 5mm, the length of the tube is 1m, the reaction temperature is controlled at 62°C, and the residence time is 22s to obtain 2-chloro-6-nitro A mixture of phenylethyl alcohol, sodium hydroxide and polar so...
Embodiment 3
[0046] Thoroughly mix 28.6g of 2-chloro-6-nitrotoluene and 6mL of dimethylsulfoxide as the first component; dissolve 5.5g of paraformaldehyde and 0.22g of sodium hydroxide in 19ml of methanol as the second component . The first component and the second component are simultaneously input into the T-shaped jet mixer for rapid mixing, and then enter the first microreactor for methylolation reaction, with a pipe diameter of 5mm and a pipe length of 1.5m, and the reaction temperature is controlled at 65 ℃, residence time 25s, obtain the mixture of 2-chloro-6-nitrophenylethanol, sodium hydroxide and polar solvent; The second microreaction that this mixture is loaded with 40 order Raney nickel catalysts by booster pump At the same time, hydrogen is continuously fed into the reactor through the gas distributor for catalytic hydrogenation. The second microreactor has a pipe diameter of 6mm, a pipe length of 10m, a reaction temperature of 62°C, a reaction pressure of 1.2MPa, and a resid...
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