Method for synthesizing primary fatty acid amide and device of ammonia gas recovery and circulation
A technology of fatty acid amide and synthesis method, which is applied in the field of synthesis of oil fine chemicals, can solve the problems of high price, environmental pollution, low catalytic activity, etc., achieve strong adaptability, reduce processing difficulty and cost, and have good activity and stability Effect
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Embodiment 1
[0018] Embodiment 1: the synthesis of oleic acid amide
[0019] First add 1700kg of oleic acid (1818 type) to the ammoniation reactor (3m from the fatty acid feeding port of the ammoniation reactor) 3 ), then open the agitator and the dehydration vacuum pump of the ammoniation reactor, heat up to 100-110° C., dehydrate for 30 minutes, close the dehydration vacuum pump, and add a type A catalyst (60 mesh chromatography silica gel 87%, activated carbon 5% , amidation catalyst NC-3018%) 30kg, continue to heat up to about 165 ° C, open the ammonia valve to feed ammonia into the ammoniation reactor, adjust the ammonia return valve and the ammonia valve, and open the ammonia recovery and circulation device , control the reaction pressure at 0.35-0.4Mpa, control the ammonia flow at 0.75-1.5m 3 / h, and control the reaction temperature between 185-188°C. After reacting for 18-20h, take a sample to analyze the acid value of free fatty acid. If the acid value is qualified (AV≤1.0mgKOH / g...
Embodiment 2
[0020] Embodiment 2: the synthesis of erucamide
[0021] Add 1800kg of erucic acid (type 90) that has melted to the ammoniation reactor (3m 3 ), then open the agitator and dehydration vacuum pump of the ammoniation reactor, heat up to 100-110°C, dehydrate for 15min, close the dehydration vacuum pump, and add B-type catalyst (200 mesh chromatography silica gel 20% and amidation catalyst NC-301 80%) 30kg, continue to heat up to about 165°C, open the ammonia valve to feed ammonia into the ammoniation reactor, adjust the ammonia return valve and the ammonia valve, open the ammonia recovery and circulation device, reduce the reaction pressure Controlled at 0.32-0.4Mpa, ammonia flow controlled at 1.0-1.8m 3 / h, and control the reaction temperature between 186-190°C. After 15 hours of reaction, take a sample and analyze the free fatty acid (acid value). If the acid value is qualified (AV≤0.8mgKOH / g), stop the ammonia reaction, and then filter and separate the catalyst , to obtain e...
Embodiment 3
[0022] Embodiment 3: the synthesis of stearylamide
[0023] Add 1600kg of molten stearic acid (1801 type) to the ammoniation reactor (3m from the fatty acid feeding port of the ammoniation reactor) 3 ), then open the agitator and dehydration vacuum pump of the ammoniation reactor, heat up to 105-115°C, dehydrate for 20min, turn off the dehydration vacuum pump, and add C-type catalyst (100 mesh chromatography silica gel 85%; trisodium phosphate 5%; active aluminum oxide 10%) 28kg, continue to heat up to about 165°C, open the ammonia valve to feed ammonia into the ammoniation reactor, adjust the ammonia return valve and the ammonia valve, and start ammonia recovery and circulation device, the reaction pressure is controlled at 0.2-0.36Mpa, and the flow rate of ammonia gas is controlled at 0.8-1.5m 3 / h, and control the reaction temperature between 190-195°C. After 18 hours of reaction, take a sample to analyze the free fatty acid (acid value), if the acid value is qualified (AV≤...
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