Method for obtaining sponge iron by treating high-iron low-tin ore by sulfurizing volatilization direct-reduction process
A technology of high iron and low tin ore and sponge iron, applied in the field of comprehensive utilization of resources, can solve the problem of high tin content, and achieve the effects of reducing tin content, realizing recovery and reducing tin content
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Embodiment 1
[0036] (1) Dry and grind high iron and low tin raw ore, vulcanizing agent and reducing agent to 200 mesh respectively, add to the raw ore according to the mass ratio of vulcanizing agent: raw ore is 1:50, reducing agent: raw ore is 1:10 FeS 2 , FeS and S, and pulverized coal, and mix them evenly;
[0037] (2) Place the obtained product in step (1) at 1150°C, and at the same time, pass in nitrogen gas with a flow rate of 0.4L / min, keep it warm for 40 minutes for vulcanization and volatilization treatment; then change it to oxygen with a flow rate of 0.4L / min, Heat preservation for 60 minutes to carry out coal-based direct reduction;
[0038] (3) The high-temperature flue gas formed during the reaction in step (2) is routinely cooled and dust-collected to recover the tin resources, and the flue gas is then routinely dust-removed and washed to remove harmful gases, and discharged into the atmosphere after meeting the emptying requirements. Sponge iron is obtained after the mate...
Embodiment 2
[0040] (1) Dry the high-iron and low-tin raw ore, vulcanizing agent and reducing agent separately, and grind them to 250 meshes, and add them to the raw ore according to the mass ratio of vulcanizing agent: raw ore is 1:30, reducing agent: raw ore is 1:5 Gypsum and reducing agent oil and coke powder, and mix well;
[0041] (2) Place the obtained product in step (1) at 1300°C, and at the same time pass in argon gas with a flow rate of 0.2L / min, keep it warm for 80min for vulcanization and volatilization treatment; Air, heat preservation for 80min for coal-based direct reduction;
[0042] (3) The high-temperature flue gas formed during the reaction in step (2) is routinely cooled and dust-collected to recover the tin resources, and the flue gas is then routinely dust-removed and washed to remove harmful gases, and discharged into the atmosphere after meeting the emptying requirements. Sponge iron is obtained after the material is cooled. Sampling and analysis showed that the t...
Embodiment 3
[0044](1) Dry the high-iron and low-tin raw ore, vulcanizing agent and reducing agent separately, and grind them to 150 mesh, and add them to the raw ore according to the mass ratio of vulcanizing agent: raw ore is 1:5, reducing agent: raw ore is 1:50 Vulcanizing agent FeS, gypsum and reducing agent coke powder, and mix evenly;
[0045] (2) Place the obtained product in step (1) at 1000°C, and at the same time, pass nitrogen gas with a flow rate of 1L / min, and keep it warm for 20 minutes for vulcanization and volatilization treatment; then change it to air with a flow rate of 0.2L / min, keep it warm 20min for coal-based direct reduction;
[0046] (3) The high-temperature flue gas formed during the reaction in step (2) is routinely cooled and dust-collected to recover the tin resources, and the flue gas is then routinely dust-removed and washed to remove harmful gases, and discharged into the atmosphere after meeting the emptying requirements. Sponge iron is obtained after the ...
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