A waste acid recycling process based on nanocomposite carrier retardation method
A nano-composite, treatment process technology, applied in the direction of metallurgical wastewater treatment, filtration treatment, special treatment goals, etc., can solve the problems of low acid recovery rate, high operating cost, unstable operation of waste acid concentration device, etc., and achieve high separation rate , the effect of low operating costs
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Embodiment 1
[0042] (1) Suspension copolymerization
[0043] In a 3000L polymerization reaction kettle, add 1275kg of NaCl solution with a mass percentage of 4%, add 2.5kg of polyvinyl alcohol with a degree of polymerization of 1000 and a degree of alcoholysis of preferably 80%, and heat to 55 ° C to make the polyvinyl alcohol fully Disperse in the solution; add 235kg of divinylbenzene, 265kg of styrene, 125kg of liquid wax, 125kg of toluene, 100kg of xylene, and 2.5kg of benzoyl peroxide with a mass percentage of 50%, mix well, and keep the temperature at 45~55℃ , At the same time, the mixer was stirred at a constant speed of 800r / min for 1h.
[0044] After 1 h, the temperature was raised to 77 °C and kept for 4 h; then, the temperature was raised to 87 °C and kept for 3 h; the temperature was raised to 97 °C, and the temperature was kept for 5 h, and then the NaCl solution in the reaction kettle was released to prepare Copolymer I.
[0045] (2) Washing and drying
[0046] The copolyme...
Embodiment 2
[0055] (1) Suspension copolymerization
[0056] In a 7000L polymerization reactor, add 5250kg of NaCl solution with a mass concentration of 6%, add 14kg of polyvinyl alcohol with a degree of polymerization of 2000 and a degree of alcoholysis of preferably 85%, and heat to 55°C to fully disperse the polyvinyl alcohol in the In the solution; add 60% divinylbenzene 335kg, styrene 365kg, liquid wax 445kg, toluene 345kg, xylene 260kg, benzoyl peroxide 7.7kg, mix well, keep the temperature at 45~55 ℃, simultaneously , and the mixer was stirred at a constant speed of 1000r / min for 1h.
[0057] After 1h, the temperature was raised to 77°C and kept for 4.5h; then, the temperature was raised to 87°C and kept for 3.5h; the temperature was raised to 97°C, and the temperature was kept for 6.5h, and then the NaCl solution in the reaction kettle was released , the copolymer sphere I was prepared.
[0058] (2) Washing and drying
[0059] The copolymerized sphere I obtained in step 1 was tr...
Embodiment 3
[0068] (1) Suspension copolymerization
[0069] In a 5000L polymerization reactor, add 4400kg of NaCl solution with a mass concentration of 5%, add 10kg of polyvinyl alcohol with a degree of polymerization of 1500 and an alcoholysis degree of preferably 83%, and heat to 55°C to fully disperse the polyvinyl alcohol in the In the solution; add 70% divinylbenzene 400kg, styrene 600kg, liquid wax 450kg, toluene 400kg, xylene 350kg, benzoyl peroxide 10kg, mix well, keep the temperature at 45~55 ℃, meanwhile, The mixer was stirred at a constant speed of 900r / min for 1.5h.
[0070] After 1.5h, the temperature was raised to 77°C and kept for 5h; then, the temperature was raised to 88°C and kept for 4h; the temperature was raised to 97°C and the temperature was kept for 7h, and then the NaCl solution in the reaction kettle was released to prepare The copolymer sphere I was obtained.
[0071] (2) Washing and drying
[0072] The copolymerized sphere I obtained in step 1 was transferre...
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