Method for preparing 4-hydroxy-4-methyl-2-pentanone
A technology of methyl and pentanone, applied in the field of preparation of 4-hydroxy-4-methyl-2-pentanone, can solve the problems of easy dehydration, short service period of acid resin, long reaction time, etc., and achieve less side reactions. , The effect of good product quality and short reaction time
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Embodiment 1
[0015] Pump 4.5 tons of industrial acetone with a content of 99% into a 5500L still, and add 200kg of processed macroporous strong basic anion exchange resin D296 and 100Kg of hydrogen with a particle size of about 1mm to 40mm in the reactor at the same time Magnesium oxide particles are used as a catalyst (magnesium hydroxide particles are placed in a mesh bag and placed in a resin), and steam is used to heat the still, so that the evaporated acetone vapor is cooled to 0°C by refrigerated water and then enters the reactor, and the reaction liquid continuously flows back to the still. Control the flow rate, carry out continuous distillation reaction, stop the reaction when the temperature of the still pot rises to 120°C, and carry out rectification operation on the reaction liquid in the still pot to obtain 4-hydroxy-4-methyl-2 - 3.6 tons of pentanone, with a single yield of 79.6%. 0.85 tons of the front fraction (mainly composed of acetone) that is rectified can be returned t...
Embodiment 2
[0017] 4.5 tons of industrial acetone with a content of 99% is pumped into a 5500L still, and 100kg of treated macroporous strong basic anion exchange resin D296 and 200Kg of hydrogen with a particle size of about 1mm to 40mm are added to the reactor at the same time Magnesium oxide particles are used as a catalyst (magnesium hydroxide particles are placed in a mesh bag and placed in a resin), and steam is used to heat the still, so that the evaporated acetone vapor is cooled to 20°C by refrigerated water and then enters the reactor, and the reaction liquid continuously flows back to the still. Control the flow rate, carry out continuous distillation reaction, stop the reaction when the temperature of the still pot rises to 120°C, and carry out rectification operation on the reaction liquid in the still pot to obtain 4-hydroxy-4-methyl-2 - 3.58 tons of pentanone, with a single yield of 79.4%. The 0.86 ton fraction (mainly composed of acetone) of the rectified fraction can be r...
Embodiment 3
[0019] 4.5 tons of industrial acetone with a content of 99% is pumped into a 5500L still, and 150kg of treated macroporous strong basic anion exchange resin D261 and 150Kg of hydrogen with a particle size of about 1mm to 40mm are added to the reactor at the same time Magnesium oxide particles are used as a catalyst (magnesium hydroxide particles are placed in a mesh bag and placed in a resin), and steam is used to heat the still, so that the evaporated acetone vapor is cooled to 10°C by refrigerated water and then enters the reactor, and the reaction liquid continuously flows back to the still. Control the flow rate, carry out continuous distillation reaction, stop the reaction when the temperature of the still pot rises to 120°C, and carry out rectification operation on the reaction liquid in the still pot to obtain 4-hydroxy-4-methyl-2 - 3.64 tons of pentanone, with a single yield of 81%. 0.83 tons of the front cut (mainly composed of acetone) that is rectified can be return...
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