Gas-based reduction shaft furnace for low-intensity pellets
A low-strength, shaft furnace technology, applied in the direction of shaft furnaces, furnaces, furnace types, etc., to achieve the effect of strong industrial practicability and lower compressive strength requirements
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Embodiment 1
[0046] This embodiment adopts figure 1 The gas-based reduction shaft furnace shown reduces lateritic nickel ore oxide pellets. The compressive strength of the laterite nickel ore oxidized pellets is 1400N.
[0047] In the gas-based reduction shaft furnace used in this embodiment, the shaft furnace body 1 has a height of 10 m, the feed chamber 11 has a height of 2 m, the reduction chamber 12 has a height of 5 m, and the cooling chamber 13 has a height of 3 m. Wherein, the first pressure-bearing flow-dividing component 31 is a triangular pyramid, the longitudinal section passing through the apex is triangular, and the angle of the apex of the triangle is 45°. The second pressure-bearing flow-dividing component 32 is a cone, and its longitudinal section passing through the apex is an isosceles triangle, and the angle of the apex of the isosceles triangle is 75°. The height of the first pressure-bearing flow-dividing component 31 is 1.25m, and the height of the second pressure-b...
Embodiment 2
[0050] This embodiment adopts image 3 The gas-based reduction shaft furnace shown reduces high phosphorus ore. The compressive strength of the high phosphate rock is 1600N.
[0051] In the gas-based reduction shaft furnace used in this embodiment, the shaft furnace body 1 has a height of 10 m, the feed chamber 11 has a height of 2 m, the reduction chamber 12 has a height of 5 m, and the cooling chamber 13 has a height of 3 m. Wherein, the first pressure-bearing flow-dividing assembly 31', the second pressure-bearing flow-dividing assembly 32' and the third pressure-bearing flow-dividing assembly 33' are all cones, and the longitudinal section passing through the apex is an isosceles triangle, and the apex angle of the isosceles triangle is The angle is 60°. The heights of the first pressure-bearing flow-dividing component 31', the second pressure-bearing flow-dividing component 32' and the third pressure-bearing flow-dividing component 33' are all 0.1 m.
[0052] The third...
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Abstract
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