A system and method for producing sulfur and iron oxide from pyrite
A technology of iron oxide and pyrite, applied in the preparation/purification of iron oxide, iron oxide/iron hydroxide, sulfur, etc., can solve the problems of high cost and stop use of sulfur, achieve low production cost and eliminate pollution problems , the effect of strong implementability
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Embodiment 1
[0041] This embodiment provides a system for producing sulfur and iron oxide from pyrite, which includes: primary desulfurization equipment, oxidation equipment and secondary desulfurization equipment;
[0042] Among them, such as figure 1 As shown, the primary desulfurization equipment includes a closed desulfurization furnace 3, a waste heat utilization device 5, a waste heat power generation device 6, a dust removal device 7 and a sulfur recovery device 8; the lower part of the closed desulfurization furnace 3 is connected to the opposite side. The feed hopper 1 and the discharge hopper 4, the closed desulfurization furnace 3 is provided with a heat supply device 2, and the bottom of the furnace body of the closed desulfurization furnace 3 is provided with an air inlet pipe 9; One interface is connected to the upper part of the furnace body of the closed desulfurization furnace 3 through a pipeline, and the second interface of the waste heat utilization device 5 is connecte...
Embodiment 2
[0048] The present embodiment provides a kind of method that utilizes pyrite to manufacture sulfur and iron oxide, and it is the method that adopts the system of embodiment 1 to utilize pyrite to manufacture sulfur and iron oxide, and the method comprises the following steps:
[0049] Step (1): Pyrite is delivered to the feed hopper 1 of the closed desulfurization furnace 3 of the primary desulfurization equipment and carried out in the feed hopper 1 (conventional methods can be used, such as feeding nitrogen and / or nitrogen into the feed hopper 1 or water vapor, etc.), and then sent to the closed desulfurization furnace 3, and at the same time pass the non-oxidizing gas into the closed desulfurization furnace 3 through the air inlet pipe 9, and use the heat supply device 2 to make The temperature in the closed desulfurization furnace 3 reaches 445-1000°C (preferably 600-700°C), so that pyrite is desulfurized to be decomposed into ferrous sulfide and elemental sulfur; The reac...
Embodiment 3
[0055] In this embodiment, the system of Embodiment 1 and the method of Embodiment 2 are used to produce sulfur and iron oxide from granular pyrite. The particle size of the granular pyrite is about 3.0 mm.
[0056] In step (1), the closed desulfurization furnace in the primary desulfurization equipment used is a fluidized roaster, and the method for deoxidizing pyrite in the feed hopper is to feed nitrogen and / or water into the feed hopper steam, the non-oxidizing gas is nitrogen, and the consumption of the non-oxidizing gas is 5-50m 3 / second, the temperature in the closed desulfurization furnace during desulfurization treatment is 600-700°C, and the temperature of the non-oxidizing medium gas with elemental sulfur after being cooled by the waste heat utilization device and the waste heat power generation device is 450-480°C, The non-oxidizing gas discharged from the sulfur recovery unit enters the waste heat utilization unit and reaches 540-560°C after being heated. The ...
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Abstract
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