A kind of method that reclaims nitrobenzene from nitrobenzene tar
A technology for nitrobenzene tar and nitrobenzene, which is applied in the field of nitrobenzene recovery, can solve the problems of high cumulative content, does not involve a method for recycling nitrobenzene tar, etc., and achieves the effects of simple recovery process and strong operability
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Embodiment 1
[0020] Nitrobenzene tar and 0.05% NaOH solution are mixed with a static mixer at a volume ratio of 1:1 for alkali washing. The temperature of the alkali wash is 20°C. After the alkali wash, the oil and water are separated, and the water phase and the oil phase are separated. The oil phase and the water are separated by The volume ratio is 1:1, and the static mixer is used to mix and wash with water. The washing temperature is 20°C. After washing, the oil and water are separated to separate the water phase and the oil phase. The specific surface area of the oil phase is 600m 2 / g of spherical silica gel adsorbent to adsorb and remove trace moisture, and the oil phase after adsorption and separation is subjected to intermittent rectification to recover nitrobenzene.
[0021] The content of nitrophenol and its sodium salt in the oil phase after adsorption separation was 9.3 mg / kg, and the recovery rate of nitrobenzene was 95.5%.
Embodiment 2
[0023] Nitrobenzene tar and 1% NaOH solution are mixed with a static mixer at a volume ratio of 1:1 for alkali washing. The temperature of the alkali wash is 80°C. After the alkali wash, the oil and water are separated to separate the water phase and the oil phase. The volume ratio is 1:1, and the static mixer is mixed and washed with water. The washing temperature is 80°C. After washing, the oil and water are separated to separate the water phase and the oil phase. The oil phase is subjected to batch distillation to recover nitrobenzene.
[0024] The content of nitrophenol and its sodium salt in the oil phase after adsorption separation was 5.1 mg / kg, and the recovery rate of nitrobenzene was 97.2%.
Embodiment 3
[0026] Nitrobenzene tar and 10% NaOH solution are stirred and mixed in a kettle for alkali washing at a volume ratio of 10:1. The temperature of the alkali washing is 65°C. After the alkali washing, the oil and water are separated to separate the water phase and the oil phase. The oil phase and the water are separated according to the The volume ratio is 1:1, and the washing temperature is 65 ℃ by mixing and washing in a kettle. After washing, the oil and water are separated to separate the water phase and the oil phase. The specific surface area of the oil phase is 600m 2 / g of spherical silica gel adsorbent to adsorb and remove trace moisture, and the oil phase after adsorption and separation is subjected to continuous rectification to recover nitrobenzene.
[0027] The content of nitrophenol and its sodium salt in the oil phase after adsorption separation was 7.7mg / kg, and the recovery rate of nitrobenzene was 96.3%.
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