Process for recycling ammonium sulfate and synthesizing acidic dye by T-acid mother liquor wastewater
A technology for recycling acid dyes and wastewater, applied in disazo dyes, ammonium sulfate and other directions, can solve the problems of inhibiting the normal development of the H acid industry, and achieve good economic and social benefits, and good solubility.
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Embodiment 1
[0017] 1) In a reaction vessel with a stirring device, mix the T-acid mother liquor wastewater and tert-butyl quaternary ammonium salt at a ratio of 4:1, and start stirring at the same time at a stirring speed of 100 rpm. After stirring and mixing for 30 minutes, let it stand for 1 After hours of stratification, the obtained water phase is recovered by conventional concentration process ammonium sulfate; the obtained organic phase is added with liquid caustic soda to adjust the pH of the organic phase to 6.0 for back extraction, and the obtained back extraction liquid is concentrated under reduced pressure by conventional technology until the amino value reaches 110g / kg is qualified, obtains 3.5.7-naphthylamine trisulfonate and 4.6.8-naphthylamine trisulfonate as the T acid mother liquor treatment liquid of main component;
[0018] 2) Weigh 172.35Kg of 100% T-acid mother liquor treatment solution, put it into a diazo kettle with stirring, start stirring, stir at 45rpm for 8 mi...
Embodiment 2
[0026] 1) In a reaction vessel with a stirring device, mix the T-acid mother liquor wastewater and tert-butyl quaternary ammonium salt at a ratio of 5:1, and start stirring at the same time at a stirring speed of 110rpm. After stirring and mixing for 30 minutes, let it stand for 1 After hours of stratification, the obtained water phase is recovered by conventional concentration process ammonium sulfate; the obtained organic phase is added with liquid caustic soda to adjust the pH of the organic phase to 6.3 for back extraction, and the obtained back extraction liquid is concentrated under reduced pressure by conventional technology until the amino value reaches 130g / kg is qualified, obtains 3.5.7-naphthylamine trisulfonate and 4.6.8-naphthylamine trisulfonate as the T acid mother liquor treatment liquid of main component;
[0027] 2) Weigh 258.53Kg of 100% T-acid mother liquor treatment solution, put it into a diazo kettle with stirring, start stirring, stir at 45rpm for 9 min...
Embodiment 3
[0035] 1) In a reaction vessel with a stirring device, mix the T-acid mother liquor wastewater and tert-butyl quaternary ammonium salt at a ratio of 6:1, and start stirring at the same time at a stirring speed of 120rpm. After stirring and mixing for 30 minutes, let it stand for 1 After hours of stratification, the obtained aqueous phase is recovered by conventional concentration process ammonium sulfate; the obtained organic phase is added with liquid caustic soda to adjust the pH of the organic phase to 6.5 for back extraction, and the obtained back extraction liquid is concentrated under reduced pressure by conventional technology until the amino value reaches 140g / kg is qualified, obtains 3.5.7-naphthylamine trisulfonate and 4.6.8-naphthylamine trisulfonate as the T acid mother liquor treatment liquid of main component;
[0036] 2) Weigh 344.7Kg of 100% T acid mother liquor treatment solution, put it into a diazo kettle with stirring, start stirring, stir at 45rpm for 10 m...
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