This utility model discloses a
triclocarban production apparatus, relating to the field of
triclocarban production technology. The inlet of the reactor is connected via pipelines to a p-chloroaniline tank, a 3,4,4'-
trichloroisocyanuric acid tank, a first
solvent tank, and a catalyst tank. The outlet of the reactor is connected via pipelines to a filter. The
liquid phase outlet of the filter is connected via pipelines to a
precipitation tank. The inlet of the
precipitation tank is connected via pipelines to a saturated
sodium carbonate solution tank. The outlet of the
precipitation tank is connected via pipelines to a first
centrifuge. The
solid phase outlet of the first
centrifuge is connected via pipelines to a crude product tank. After the p-chloroaniline reacts with 3,4,4'-
trichloroisocyanuric acid, the catalyst is removed. Then, under the action of the saturated
sodium carbonate solution,
triclocarban precipitates out. The first
centrifuge separates the
solid and liquid phases after precipitation, obtaining crude triclocarban, which is then transported to the crude product tank. The obtained product has high purity and is
environmentally friendly.