The preparation method of recyclable n-butyldiethanolamine
A technology of butyldiethanolamine and butylethanolamine, which is applied in the preparation of organic compounds, the preparation of aminohydroxyl compounds, chemical instruments and methods, etc., can solve the problems of high reaction temperature, increase of three wastes, large salty wastewater, etc., and achieve reaction Moderate conditions, low cost, environmental protection, and good safety
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Embodiment 1
[0024] The preparation of embodiment 1 N-butyldiethanolamine
[0025] Batch 01: After the reactor was evacuated twice for nitrogen replacement, 73.1kg of n-butylamine was pumped into the reactor under normal pressure, and then vacuumed again for nitrogen replacement. Then slowly raise the temperature in the reactor to 130°C, press 88.1kg of ethylene oxide into the reactor, control the flow rate at 6kg / min, keep the pressure of the reactor at 0-0.6MPa, and keep the reaction temperature at 130-135°C; After the feeding of ethylene oxide was completed, the heat was kept for 1 hour to obtain the crude product of N-butyldiethanolamine. The crude product of N-butyldiethanolamine is degassed and then transferred to the rectification tank. The temperature of the rectification tank is controlled at 120-140°C, the vacuum degree is 3-6mmHg, and the temperature at the top of the tank is 75-80°C. Ethanolamine 7.0kg. Control the rectification kettle temperature at 140-170°C, vacuum degree ...
Embodiment 2
[0032] Embodiment 2: the preparation of N-butyldiethanolamine
[0033]Batch 01: After the reactor was evacuated twice for nitrogen replacement, 73.1kg of n-butylamine was pumped into the reactor under normal pressure, and then vacuumed again for nitrogen replacement. Then slowly raise the temperature in the reactor to 130°C, press 79.2kg of ethylene oxide into the reactor, control the flow rate at 6kg / min, keep the pressure of the reactor at 0-0.6MPa, and keep the reaction temperature at 130-135°C; After the feeding of ethylene oxide was completed, the heat was kept for 1 hour to obtain the crude product of N-butyldiethanolamine. The crude product of N-butyldiethanolamine is degassed and then transferred to the rectification tank. The temperature of the rectification tank is controlled at 120-140°C, the vacuum degree is 3-6mmHg, and the temperature at the top of the tank is 75-80°C. Ethanolamine 15.2kg. Control the rectification kettle temperature to 140-170°C, vacuum degree...
Embodiment 3
[0040] Embodiment 3: the preparation of N-butyldiethanolamine
[0041] Batch 01: After the reactor was evacuated twice for nitrogen replacement, 65.8kg of n-butylamine was pumped into the reactor under normal pressure, and then evacuated for nitrogen replacement again after pumping. Then slowly raise the temperature in the reactor to 130°C, press 79.2kg of ethylene oxide into the reactor, control the flow rate at 6kg / min, keep the pressure of the reactor at 0-0.6MPa, and keep the reaction temperature at 165-170°C; After the feeding of ethylene oxide was completed, the heat was kept for 1 hour to obtain the crude product of N-butyldiethanolamine. The crude product of N-butyldiethanolamine is degassed and then transferred to the rectification tank. The temperature of the rectification tank is controlled at 120-140°C, the vacuum degree is 3-6mmHg, and the temperature at the top of the tank is 75-80°C. Ethanolamine 8.1kg. Control the rectification kettle temperature at 140-170°C...
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