Trapping device and process for production of 3,4-dichlorobenzonitrile
A dichlorobenzonitrile and process technology, which is applied in the field of trapping devices for the production of 3,4-dichlorobenzonitrile, can solve the problems of difficult cooling of circulating spray water, harsh working environment, and large amount of waste water, and achieve Reduce the workload of distillation and purification, the structure design is simple and reasonable, and realize the effect of recycling
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Embodiment 1
[0036] Such as figure 1 Shown, the present invention is a kind of trapping device that is used for 3,4-dichlorobenzonitrile production, comprises primary trap, secondary trap, tertiary trap, washing tower, rectifying tower , product tank, waste water treatment device and tail gas treatment device, the 3,4-dichlorobenzonitrile high-temperature mixed product from the reactor enters the primary trap through the feed inlet of the primary trap, and a The gas outlet at the top of the primary trap is connected to the feed port of the secondary trap, and the gas outlet at the top of the secondary trap is connected to the feed port of the tertiary trap. The gas outlet at the top of the stage trap is connected to the inlet of the water washing tower, and the gas outlet at the top of the water washing tower is connected to the tail gas treatment device;
[0037] The discharge port at the bottom of the primary trap is connected to the feed port of the first melting layered tank, the disc...
Embodiment 2
[0053] The difference between embodiment 2 and embodiment 1 is that (two) trapping section:
[0054] S1: The high-temperature mixed product of 3,4-dichlorobenzonitrile from the reactor enters the primary trap. At this time, the cold medium spray device sprays The cooling medium is evaporated and cooled, 54.69g of ammonium chloride solid and 34.2g of 3,4-dichlorobenzonitrile liquefaction condensation are precipitated in the primary trap, and the solid-liquid mixture produced in the primary trap is heated at 500g at 50°C Water dissolves, washes and stratifies, in which the upper aqueous phase is cooled and crystallized and centrifuged to separate the ammonium chloride solid product and centrifugate, the centrifugate is used as a solvent for the solid-liquid mixture generated in the primary trap, and the lower organic phase is sent to the separation Layer device, after washing with water for many times, the liquid product of 3,4-dichlorobenzonitrile with a purity ≥ 99.5% is obtai...
Embodiment 3
[0060] The difference between embodiment 3 and embodiment 1 is that (two) trapping section:
[0061] S1: The high-temperature mixed product of 3,4-dichlorobenzonitrile from the reactor enters the primary trap. At this time, the cold medium spray device sprays The cooling medium is evaporated and cooled, and 77.62g of ammonium chloride solid and 91.2g of 3,4-dichlorobenzonitrile liquefaction condensation are precipitated in the primary trap. Water dissolves, washes and stratifies, in which the upper aqueous phase is cooled and crystallized and centrifuged to separate the ammonium chloride solid product and centrifugate, the centrifugate is used as a solvent for the solid-liquid mixture generated in the primary trap, and the lower organic phase is sent to the separation Layer device, after washing with water for many times, the liquid product of 3,4-dichlorobenzonitrile with a purity ≥ 99.5% is obtained, and the mixed product atmosphere after the initial cooling of the primary t...
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