A kind of method and equipment for producing adipic acid by oxidizing alcohol and ketone with nitric acid
A technology for oxidizing alcohols and ketones and oxidizing acids, which is applied in the field of nitric acid oxidation of alcohols and ketones to adipic acid, which can solve the problems of cumbersome equipment and low conversion rate, and achieve the effects of suppressing side reactions, stable reaction, and wide reaction temperature range
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Embodiment 1-4
[0022] The equipment used for the preparation of adipic acid by nitric acid oxidation of alcohol and ketone comprises alcohol and ketone storage tank 1, oxidation acid storage tank 2, buffer tank 3, absorption tank 4, reaction kettle 5, oxidation acid feed pump 6, alcohol and ketone feed pump 7. Vacuum pump 8, condenser 9;
[0023] The outlet of the oxidizing acid storage tank 2 is connected to the reaction kettle equipped with an agitator through a pipeline, or connected to the inlet of the oxidizing acid feed pump 6 through a pipeline, and the outlet of the alcohol and ketone storage tank 1 is connected through a pipeline Connect with the feed inlet of alcohol and ketone feed pump 7, the outlet of oxidation acid feed pump, the outlet of alcohol and ketone feed pump are connected with reactor 5 through pipeline; Reactor is connected with condenser 9 through pipeline, The condenser is connected with the buffer tank 3 through the pipeline, the buffer tank is connected with the ...
Embodiment 5-8
[0032]Under the condition of reaction temperature 65~105℃, stirring speed 300rpm, negative pressure -0.020~-0.005Mpa (gauge pressure), the oxidizing acid reacts with alcohol and ketone, the oxidizing acid is excessive, and the oxidizing acid in the oxidizing acid storage tank passes through The feed pump is continuously added to the reaction kettle at a certain speed, and the alcohol and ketone in the alcohol and ketone storage tank are continuously added to the reaction kettle at a certain speed through the alcohol and ketone feed pump under the conditions of heating, stirring and negative pressure, so that the oxidation acid and alcohol and ketone Reaction, oxidation acid excess, oxidation reaction continues. The gas generated by the reaction enters the buffer tank after being condensed by the condenser, and the non-condensable gas enters the absorption tank after passing through the buffer tank. After being absorbed by water, the non-water-soluble gas is discharged through t...
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