Method and device for recycling hydrazine hydrate in preparation process of 3-chloro-2-hydrazinopyridine intermediate
A technology of hydrazine pyridine and hydrazine hydrate, which is applied in the field of recovery and reuse of hydrazine hydrate, can solve the problems of waste of hydrazine hydrate and less effective recovery of hydrazine hydrate, and achieves the effects of saving production cost, improving heat exchange efficiency and promoting effective precipitation
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Embodiment 1
[0033] A method for recovering and reusing hydrazine hydrate in a 3-chloro-2-hydrazinopyridine intermediate preparation process, comprising the following steps: adding 1mol / L sodium hydroxide solution to a hydrazine-containing solution to adjust the solution to neutrality, and then adding The cooling coil in the crystallization tank is fed with liquid ammonia to quickly cool down to -3°C, and the precipitate is filtered out. The filtered filtrate is evaporated in the circulating evaporator at 110°C for 1 hour, and the evaporated gas is condensed by the condenser and then re-enters the reused in the reactor.
Embodiment 2
[0035] A method for recovering and reusing hydrazine hydrate in a 3-chloro-2-hydrazinopyridine intermediate preparation process, comprising the following steps: adding 1mol / L sodium hydroxide solution to a hydrazine-containing solution to adjust the solution to neutrality, and then adding Liquid ammonia is passed into the cooling coil in the crystallization kettle to quickly cool down to ~0°C, and the precipitate is removed by filtration. The filtered filtrate is evaporated in the circulating evaporator at 120°C for 2 hours, and the evaporated gas is condensed by the condenser and then re-enters the reused in the reactor.
Embodiment 3
[0037] A method for recovering and reusing hydrazine hydrate in a 3-chloro-2-hydrazinopyridine intermediate preparation process, comprising the following steps: adding 1mol / L sodium hydroxide solution to a hydrazine-containing solution to adjust the solution to neutrality, and then adding The cooling coil in the crystallization kettle is fed with liquid ammonia to quickly cool down to -3°C, and the precipitate is filtered out. The filtered filtrate is evaporated in the circulating evaporator at 120°C for 1 hour, and the evaporated gas is condensed by the condenser and then re-enters the reused in the reactor.
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