The invention discloses a method for producing KA oil through oxidizing
cyclohexane by using air on the basis of a gas-liquid-
solid heterogeneous reaction separation synchronization reactor, wherein the water-containing
cyclohexane is added into the reactor, the reactor comprises a reaction
tower and at least two constant temperature settlement towers communicated with the bottom of the reaction
tower, and the reaction
tower is internally provided with a
gas phase area, an oxidization area and a gas outlet; the oxidization area and the constant temperature settlement towers are filled with the
cyclohexane in the reaction, the air is introduced continuously from the bottom of the oxidization area and is in contact with the cyclohexane to carry out the oxidization reaction, meanwhile, the produced KA oil is blended with water to form a KA
oil phase, the KA
oil phase is settled into the constant temperature settlement tower, the cyclohexane in the constant temperature settlement tower at the moment enters the oxidization area through an external circulation
system, so that the reaction is conducted continuously, the KA
oil phase continues to settle in the constant temperature settlement tower until the constant temperature settlement tower is fully filled the KA oil phase, then the reaction tower is switched to be communicated with the other constant temperature settlement tower filled with the cyclohexane, the operation is conducted on the constant temperature settlement towers alternatively to continuously produce the KA oil. The method is used to continuously produce the KA oil with high percent of conversion and
high selectivity, the production efficiency is improved, and the production cost is lowered.