2-cyanophenol preparing method
A technology of o-hydroxybenzonitrile and o-hydroxybenzamide, which is applied in the field of preparation of o-hydroxybenzonitrile, can solve problems such as punching and clogging, and achieve the effects of promoting continued reaction, increasing contact area, and shortening reaction time
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Embodiment 1
[0029] In a 2000L glass-lined batching kettle, put 180kg of o-hydroxybenzamide, 0.5kg of catalyst dioxane and 1150L of solvent toluene for batching (1330L in total), turn on the jacket steam and heat to 105°C, stir for 15min, and o-hydroxybenzene After the formamide is completely dissolved in the solvent, the ingredients are put into a 5000L glass-lined storage kettle. Repeat the above process to keep the batching amount in the storage kettle to support extraction. The batching is pumped out with a raw material pump, and the flow rate is 665L / h, and it is input into a raw material mixer, where it is mixed with phosgene with a flow rate of 14700L / h. Control the temperature of the tube pass in the tubular reactor at 100-105°C, and the heat transfer area of the reactant flow is 20m 2 The tube side of the tubular reactor, the gas generated by the reaction passes through the gas-liquid separator and condenser, and then goes to the tail gas treatment system. The liquid material e...
Embodiment 2
[0031]In a 2000L glass-lined batching kettle, put 180kg of o-hydroxybenzamide, 0.5kg of catalyst dioxane and 1150L of solvent toluene for batching (1330L in total), turn on the jacket steam and heat to 105°C, stir for 15min, and o-hydroxybenzene After the formamide is completely dissolved in the solvent, the ingredients are put into a 5000L glass-lined storage kettle. Repeat the above process to keep the batching amount in the storage kettle to support extraction. The batching is pumped out with a raw material pump, and the flow rate is 443L / h, and it is input into a raw material mixer, where it is mixed with phosgene with a flow rate of 9800L / h. Control the temperature of the tube pass in the tubular reactor at 100-105°C, and the heat transfer area of the reactant flow is 20m 2 The tube side of the tubular reactor, the gas generated by the reaction passes through the gas-liquid separator and condenser, and then goes to the tail gas treatment system. The liquid material ent...
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