Method for restraining generation of manganous dithionate in process of leaching sulfur dioxide gas out of pyrolusite
A technology of manganese dithionate and sulfur dioxide, applied in the fields of environmental protection and metallurgy, can solve the problems of increasing the difficulty of iron removal, failing to realize industrialization, and being difficult to meet industrialized continuous production, and achieve the effect of inhibiting the generation of manganese dithionate.
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Embodiment 1
[0025] Water, pyrolusite with a particle size of not less than 100 meshes and granular charcoal activated carbon with a particle size in the range of 0.1 to 10 mm are made into pyrolusite slurry according to the mass ratio of water: pyrolusite: granular charcoal activated carbon of 10: 1: 0.5. After the ore pulp is injected into the reactor, sulfur dioxide gas is introduced into the reactor, and air is blown into the reactor slurry at the same time, and the pH value of the slurry is monitored by a pH online monitor, so that the pH value of the slurry is lower than 3.5. The air blowing is automatically controlled, and when the pH value of the slurry is greater than 3.5, the blower is started to blow in air.
Embodiment 2
[0027] Water, pyrolusite with a particle size of not less than 100 mesh and granular coke activated carbon with a particle size in the range of 0.1 to 10 mm are formulated into a pulp according to the mass ratio of water: pyrolusite: granular coke activated carbon of 10:2:0.2, and the pulp is beaten After entering the reactor, feed sulfur dioxide gas into the reactor, and at the same time blow air into the reactor slurry, and monitor the pH value of the slurry through a pH online monitor, so that the pH value of the slurry is lower than 3.5. The air blowing is automatically controlled, and when the pH value of the slurry is greater than 3.5, the blower is started to blow in air.
Embodiment 3
[0029] Water, pyrolusite with a particle size of not less than 100 mesh and granular activated carbon with a particle size in the range of 0.1 to 10 mm are formulated into a pulp according to the mass ratio of water: pyrolusite: granular activated carbon at 10:5:1.0, and the pulp is poured into the reactor Finally, feed sulfur dioxide gas into the reactor, and at the same time blow air into the reactor slurry, and monitor the pH value of the slurry through a pH online monitor, so that the pH value of the slurry is lower than 3.5. The air blowing is automatically controlled, and when the pH value of the slurry is greater than 3.5, the blower is started to blow in air.
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