The invention discloses a
continuous reaction system for producing 2-hydroxy-
benzonitrile, which comprises two groups of batching kettles, a
static mixer, a micro-channel reactor and a
heat exchanger, the two groups of batching kettles are respectively
salicylamide-o-
xylene solution preparation kettles and
thionyl chloride-catalyst
system preparation kettles; the batching kettle is communicated with the
static mixer through a pipeline, the
static mixer is communicated with the micro-channel reactor, reaction liquid enters the
heat exchanger from an outlet of the micro-channel reactor for cooling, an outlet of the
heat exchanger is communicated with an inlet of the degassing
tower, the bottom of the degassing
tower is communicated with an alkalization kettle, and the alkalization kettle is communicated with a multi-stage
crystallization kettle. And the multi-stage
crystallization kettle is communicated with a
vacuum drying box. According to the
system disclosed by the invention, the degassing
tower, the alkalization kettle and the multi-stage
crystallization are connected in series, so that the integration of reaction, separation and purification is realized. The degassing tower adopts
nitrogen stripping to recover unreacted SOCl2, and three-stage
tail gas absorption is matched, so that the
utilization rate of SOCl2 is increased to 95% or above, and the
environmental protection requirement is met.