Macro-porous adsorption resin regeneration method
A pore adsorption and resin technology, applied in the field of macroporous adsorption resin regeneration, can solve the problems of poor resin regeneration effect, inability to use it again, and high operational risk, and achieve good regeneration effect, low regeneration cost and high safety performance. Effect
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Embodiment 1
[0022] Filled with LSA-5 macroporous adsorption resin 5 m 3 , a resin bed used to adsorb organic impurities in industrial hydrogen peroxide produced by anthraquinone method.
[0023] After the hydrogen peroxide resin bed exits the system, the hydrogen peroxide in the resin bed is returned and cleaned up to the standard, and the process water in the resin bed is purged with nitrogen pressure, starting with 9 m 3 Alcohol compounds replace the residual process water in the resin bed, the flow rate is 5~8m 3 / h, soak for 24~32 hours, the effluent is recycled into the raffinate tank, and then 6 m 3 Alcohol compounds displace the regenerant in the resin bed, the flow rate is 5~8m 3 / h, then soak for 24 hours, continue to recover the effluent, replace and soak three times, and then establish a cycle: pure alcohol compound tank→resin bed→pure alcohol compound tank, cycle for 2~8 hours, soak for 8~16 hours, replace with process water Alcohol compounds are removed, after the cleaning...
Embodiment 2
[0025] Filled with LSA-5 macroporous adsorption resin 15 m 3 , a resin bed used to adsorb organic impurities in industrial hydrogen peroxide produced by anthraquinone method.
[0026] After the hydrogen peroxide resin bed exits the system, the hydrogen peroxide in the resin bed is returned and cleaned up to the standard, and the process water in the resin bed is purged with nitrogen pressure, starting with 27 m 3 Alcohol compounds replace the residual process water in the resin bed, the flow rate is 5~15m 3 / h, soak for 24~32 hours, the effluent is recycled into the raffinate tank, and then used for 18 m 3 Alcohol compounds displace the regenerant in the resin bed, the flow rate is 5~15m 3 / h, then soak for 24 hours, continue to recover the effluent, replace and soak three times, and then establish a cycle: pure alcohol compound tank→resin bed→pure alcohol compound tank, cycle for 2~8 hours, soak for 8~16 hours, replace with process water Alcohol compounds are removed, afte...
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