A kind of method for extracting and recovering toburic acid from tunic acid waste water
A technology for recovering Tobacic acid and Tobacic acid, which is applied in chemical instruments and methods, alkali metal sulfites/sulfites, water pollutants, etc., can solve the problem of long energy consumption, increase of inorganic salts in Tobacic acid wastewater, and Ammonia nitrogen content, large consumption of ammonia water and hydrochloric acid, etc., to save time, reduce acidity and improve efficiency
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Embodiment 1
[0026] Step (1), fully mix 1000ml Tuburic acid waste water with the extraction agent at a ratio of 1:1 to oil and water under normal temperature and pressure, and obtain the first raffinate phase and the first extracted water after layering. The extraction agent is determined by mass Concentration is 10% triisooctylamine, 50% sulfonated kerosene and 40% tributyl phosphate;
[0027] Step (2), fully mix the first extracted water and the extractant according to the oil-water ratio of 1:1, and obtain the second raffinate phase and the second extracted water after layering. The extractant is the same as that of step (1). Extracting agent;
[0028] Step (3), combine the first raffinate phase and the second raffinate phase, then add liquid caustic soda until the pH value is 8, heat to 60°C for thorough mixing, and obtain stripping liquid and extractant after layering, extractant Recycled for primary and secondary extraction;
[0029] Step (4), centrifuge the back-extraction to obta...
Embodiment 2
[0031] Step (1), fully mix 1000ml Tuburic acid waste water with the extraction agent at a ratio of 1:1 to oil and water under normal temperature and pressure, and obtain the first raffinate phase and the first extracted water after layering. The extraction agent is determined by mass The concentration is 10% tri-n-butylamine, 50% sulfonated kerosene and 40% tributyl phosphate;
[0032] Step (2), fully mix the first extracted water and the second extractant according to the oil-water ratio of 1:1, and obtain the second raffinate phase and the second extracted water after layering, and the extractant is the same as in the step (1 ) extractant;
[0033] Step (3), combine the first raffinate phase and the second raffinate phase, then add liquid caustic soda until the pH value is 8, heat to 60°C for thorough mixing, and obtain stripping liquid and extractant after layering, extractant Recycled for primary and secondary extraction;
[0034] Step (4), centrifuge the back-extraction...
Embodiment 3
[0036] Basically the same as Example 1, the only difference is that the complexing agent is a mixture of tri-isooctylamine and tri-n-butylamine according to the mass ratio ratio of 1:1, 2.6g of Tuccinic acid obtained in this embodiment, and the content of Tuccinic acid is 92.2% .
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