In order to solve the shortcomings of the existing technology that the reaction scale is small, industrialized continuous production cannot be produced, and the processing process is complicated, the present invention provides a method and device for continuous production of Para-Cymene, which have continuous production, simple operation, and no waste , no solvent and other reagents are needed, and the catalyst is simple and recyclable.
The invention provides the following technical scheme: a method for continuous production of Para-Cymene, in which 0.1kg to 50.0kg of Pd/C catalyst is loaded into the reactor, and the inert load is fed at a rate of 0.01L/min to 5.00L/min. Gas such as nitrogen, turn on the heating device, when the temperature of the reactor reaches 150 ℃ ~ 400 ℃, turn on the metering pump, and continuously feed the industrial dipentene raw material at a speed equivalent to the space velocity of 0.5h-1 ~ 5.0h-1, After preheating, gasification, and contact reaction with the catalyst, as the reaction progresses, the reaction product continuously enters the condenser connected to the bottom of the reactor, and after being condensed, it is directly collected by the condenser to the product storage tank. The product obtained is a Para-Cymene product. Wherein, the space velocity refers to a parameter that expresses the feed rate without being affected by the size of the reactor. The palladium content of the above Pd/C catalyst is between 0.1%wt and 10.0%wt.
The device for implementing the method described in the present invention, that is: a method device for implementing the continuous production of Para-Cymene from industrial dipentene, mainly consists of a raw material storage tank, a metering pump, a preheater, a gasification It is composed of a reactor, a reactor, a condenser, a product storage tank and a heating device. A metering pump capable of continuous constant flow feeding is provided between the preheater and the raw material storage tank, and the inlet of the metering pump is connected with the outlet of the raw material storage tank. The outlet of the metering pump is connected to the inlet of the preheater, then the outlet of the preheater is connected to the inlet of the vaporizer, the outlet of the vaporizer is connected to the inlet on the top of the reactor, the outlet at the bottom of the reactor is connected to the inlet of the condenser, and the outlet of the condenser is connected to the product The inlet of the storage tank is connected, and the preheater, gasifier, reactor and heating device are connected. A nozzle with an inner diameter of 0.05 mm to 1.00 mm is installed in the vaporizer. The reactor is a tube-and-tube reactor, the tubes are loaded with reaction catalysts, the reactor is provided with a temperature sensor, and the tube-and-tube reactor is provided with a jacket. The reactor is a tube-and-tube multi-tube reaction bed, and the reactor jacket can control the temperature. The feed port of the reactor is located at the top of the reactor. After the raw material is preheated and atomized and gasified by the nozzle, it enters the reaction bed from the top of the reactor. The feed port of the reactor is at the bottom of the reactor, and the reaction product directly enters the condensation After being condensed, it is directly collected into the product storage tank. The heating device includes an expander, a magnetic pump, a cold oil tank and a hot oil furnace. A magnetic pump is installed between the cold oil tank and the hot oil furnace. The magnetic pump is connected to the preheater, gasifier and reactor. One end of the hot oil furnace is connected to the expansion The other end is connected with the preheater, gasifier and reactor, and forms a closed heating circuit with the magnetic pump.
The raw material industrial dipentene used in the present invention is a type of monocyclic terpene with a six-membered ring structure, and this type of monocyclic terpene can be converted into Para-Cymene after catalytic dehydrogenation. The industrial dipentene referred to in the present invention is a mixture of a class of monocyclic monoterpenes with the same molecular weight and similar structure, and usually has many isomers, such as: limonene, α-terpinene, α-phellandrene , β-phellandrene, γ-terpinene, terpinene, etc.