A kind of solid phase continuous reaction prepares the method for 1-amino-4 naphthalene sulfonate sodium
A technology of sodium naphthalenesulfonate and amino, which is applied in the field of solid-phase continuous reaction to prepare sodium 1-amino-4naphthalenesulfonate, can solve the problems of low batch reaction production capacity, low local overheating yield, production site pollution, etc., and achieve Realize the effect of DCS automatic control, easy enlargement of production scale and improvement of production environment
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Embodiment 1
[0035] A method for preparing 1-amino-4 naphthalenesulfonate sodium by solid phase continuous reaction, the steps are:
[0036] (A) Salt sulfonation: Add the reaction raw materials menaphthylamine, sulfuric acid and water to the salt forming kettle respectively, the quality of menaphthylamine, sulfuric acid and water is 2000KG\:1600KG\:600KG\, stir evenly, and react to get carbinol Amine sulfate;
[0037] (B) sulfonation: the menaphthylamine sulfate obtained in the step (A) is continuously introduced into the vertical sulfonation reactor of 10M3 at a speed of 1050KG / hr, and the reactor outside has a jacket, and heat transfer oil is used as heat The sulfonation reaction kettle was heated by medium indirect circulation heating method for sulfonation reaction, the stirring speed was 20 rpm, the stirring method was frame stirring, the sulfonation reaction temperature was 220°C, and the residence time was 4 hours. Water is removed, and the remaining reaction product is a solid mix...
Embodiment 2
[0042] With embodiment 1, difference is: the mass ratio of the menaphthylamine in the step (A), sulfuric acid and water is 2000KG\1300KG\:0.0KG; The sulfonation reactor of step (B) is a horizontal reactor, There is a heating coil outside the reaction kettle, the stirring method is rake stirring, the stirring speed is 40 rpm, the sulfonation reaction temperature is 180°C, the reaction time is 12 hours, and the reaction product is containing 1,4 acid (>94% ) and unreacted raw material (2.5%) solid mixture; the alkali that adds in the step (C) is potassium hydroxide, according to solid mixture: 30% sodium hydroxide: the mass ratio of water is 1:0.6:10 ratio to add , the extraction solvent is benzene; the sodium 1,4-acid content in the product obtained after concentration and crystallization is 99.2%, and the product yield after the crystallization mother liquor is 91.5%.
Embodiment 3
[0044] With embodiment 1, difference is: the mass ratio of menaphthylamine, sulfuric acid and water in step (A) is 2000KG\: 1800KG\: 3000KG; The sulfonation reaction temperature in step (B) is 230 ℃, reaction There is a heating coil inside the kettle, the stirring method is paddle stirring, the stirring speed is 60 rpm, the reaction time is 2 hours, and the reaction product is containing 1,4 acid (>93%) and unreacted raw materials (6.5%) ) solid mixture; the alkali added in the step (C) is sodium carbonate, according to the solid mixture: 30% sodium carbonate: the mass ratio of water is added in the ratio of 1:1.3:4, and the extraction solvent is toluene; after concentrated crystallization, obtain The sodium 1,4-acid content in the product is 99.3%, and the product yield is 89% after the crystallization mother liquor is applied mechanically.
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