A device for removing high-concentration iron and manganese in mine water by an oxidation catalytic column and its treatment method
A technology for oxidizing catalytic columns and mine water, which is applied in the direction of oxidized water/sewage treatment, mining wastewater treatment, water/sewage treatment, etc. It can solve the problems of high treatment cost, long process flow, and complicated control, and achieve compact equipment structure, Good processing effect and high efficiency
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Embodiment 1
[0071] Make the catalytic medium 3-4 of the present invention according to the following steps:
[0072] Step 1: 340 to 940 parts of ultra-clean water with a conductivity of 0.0111 to 0.0511Mv was treated by a particle accelerator for 4 to 15 minutes, injected into an anion exchange column for 15 to 29 minutes, eluted with a strong base and a weak acid salt, and added Into the reaction kettle, start the stirring motor of the reaction kettle, stir at a speed of 80-160 rpm, add 1-7 parts of m-trifluorotoluidine, 2-8 parts of sodium acid pyrophosphate, hydrogenated terpene resin 2 to 8 parts, turn on the high-pressure steam switch, pass high-temperature and high-pressure steam into the heat exchanger, so that the temperature of the reactor rises to 61-82 degrees, and heat preservation treatment for 1-2.5 hours;
[0073] Step 2: Take another 8-27 parts of vanadium mica, 10-21 parts of composite iron-titanium powder, and 1-24 parts of titanium silicon carbide, ultrafinely pulverize...
Embodiment 2
[0080] Make the catalytic medium 3-4 of the present invention according to the following steps:
[0081] Step 1: 340 parts of ultra-clean water with a conductivity of 0.0111Mv was treated by a particle accelerator for 4 minutes, injected into an anion exchange column for 15 minutes, eluted with strong base and weak acid salt and added to the reactor, and the reactor was started Stirring motor, stirring at a speed of 80 rpm, add 1 part of m-trifluorotoluidine, 2 parts of sodium acid pyrophosphate, and 2 parts of hydrogenated terpene resin in sequence, turn on the high-pressure steam switch, and pass to the heat exchanger Enter high-temperature and high-pressure steam to make the temperature of the reactor rise to 61 degrees, and heat preservation treatment for 1 hour;
[0082] Step 2: Take another 8 parts of vanadium mica, 10 parts of composite iron-titanium powder, and 1 part of titanium silicon carbide, and ultrafinely pulverize the three to 480 mesh, and make a mixed solutio...
Embodiment 3
[0089] Make the catalytic medium 3-4 of the present invention according to the following steps:
[0090] Step 1: 940 parts of ultra-clean water with a conductivity of 0.0511Mv was treated by a particle accelerator for 15 minutes, injected into an anion exchange column for 29 minutes, eluted with strong base and weak acid salt and added to the reactor, and the reactor was started The stirring motor is stirred at a speed of 160 rpm, and 7 parts of m-trifluorotoluidine, 8 parts of sodium acid pyrophosphate, and 8 parts of hydrogenated terpene resin are sequentially added, and the high-pressure steam switch is turned on to pass through the heat exchanger. Enter the high-temperature and high-pressure steam, so that the temperature of the reactor rises to 82 degrees, and the heat preservation treatment is 2.5 hours;
[0091] Step 2: Take another 27 parts of vanadium mica, 21 parts of composite iron-titanium powder, and 24 parts of titanium silicon carbide, and ultrafinely pulverize ...
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