Method for synthesizing N,N,N',N'-methylethylenediamine using transfer line reactor
A pipeline reactor, methylethylenediamine technology, applied in the chemical method for liquid-liquid reaction, chemical equipment and method, preparation of functional groups replaced by amino groups, etc., can solve the problem of harsh reaction conditions, catalyst recovery, and high price and other issues to achieve a good effect of safety
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Embodiment 1
[0027] Embodiment 1: a kind of N, N, N', the synthetic method of N'-methylethylenediamine, reaction process is as follows:
[0028] Take 989.7g (1mol) of 1,2-dichloroethane, 410g of sodium hydroxide, 4508g (10mol) of dimethylamine, and 1950g of benzene. The reactor adopts a pipeline reactor, and the feed adopts a metering pump. Keep the temperature of the reactor jacket at 180°C, adjust the flow rate, divide the above raw materials into two groups and inject them into the pipeline reactor at the same time, the system pressure is 0.82Mpa, and the reaction residence time is 10 minutes. The synthetic solution was rectified, and the fraction at 119-121°C was extracted to obtain 1005 g of the product, with a yield of 86.50%.
Embodiment 2
[0029] Embodiment 2: a kind of N, N, N', the synthetic method of N'-methylethylenediamine, reaction process is as follows:
[0030] Take 989.7g (1mol) of 1,2-dichloroethane, 410g of sodium hydroxide, 3606g (8mol) of dimethylamine, and 1800g of toluene. The reactor adopts a pipeline reactor, and the feed adopts a metering pump. Keep the reactor jacket temperature at 150°C, adjust the flow rate, divide the above raw materials into two groups and inject them into the pipeline reactor at the same time, the system pressure is 0.68Mpa, and the reaction residence time is 8 minutes. The synthetic solution was rectified, and the fraction at 119-121°C was extracted to obtain 1018g of the product, with a yield of 87.60%.
Embodiment 3
[0031] Embodiment 3: a kind of N, N, N', the synthetic method of N'-methylethylenediamine, reaction process is as follows:
[0032]Take 989.7g (1mol) of 1,2-dichloroethane, 410g of sodium hydroxide, 2704g (6mol) of dimethylamine, and 1500g of methanol. The reactor adopts a pipeline reactor, and the feed adopts a metering pump. Keep the reactor jacket temperature at 120°C, adjust the flow rate, divide the above raw materials into two groups and pour them into the pipeline reactor at the same time, the system pressure is 0.46Mpa, and the reaction residence time is 12 minutes. The synthetic solution was rectified, and the fraction at 119-121°C was extracted to obtain 1048g of the product, with a yield of 90.10%.
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