Method for operating rotary heartn type reducing furnace and rotary hearth type reducing furnace facilities
A rotary furnace bottom and reduction furnace technology, applied to the operation of the rotary hearth reduction furnace and the field of rotary furnace bottom reduction furnace equipment, can solve the problem of heat exchanger blockage, insufficient prevention of adhesion, and inability to give sufficient powder components attention and other issues
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Embodiment 1~ Embodiment 3 and comparative example 1
[0084] exist figure 1 In the reduction furnace of the rotary furnace bottom processing method shown, powdered coke is mixed with powdered iron ore, electric furnace powder and finely powdered rolling scale to produce green pellets of 10-20mm, and the Restore it in the furnace. The hearth of the rotary furnace has a central diameter of 17 m and a hearth width of 4 m, and has a capacity of producing 15 tons of reduced iron per hour. The reduction zone 19 of the rotary kiln has a length of 35 m and the length of the heating zone 18 is 18 m. The results of the operation using this equipment are shown in Table 1. In addition, in Examples 1, 2 and Comparative Example, the amount of combustion gas generated is 27000 to 30000 Nm 3 / hour, while in Example 3, the amount of generation is 17000Nm 3 / Hour. In Example 1, the temperature of the reduction zone of the rotary kiln 1 was 1270° C., and the molar ratio of carbon monoxide to carbon dioxide was 0.55. The green pellets are redu...
Embodiment 4~ Embodiment 6 and comparative example 2
[0092] figure 1 It is an exhaust gas treatment facility of a reduction furnace performed by a rotary hearth used in Examples 4 to 6 and Comparative Example 2 of the working method of the present invention. The reduction furnace reduces 18 tons of green pellets as a raw material per hour, and the exhaust gas at 1100°C produces 45000Nm per hour 3 . Table 2 shows the operating conditions and results of Examples and Comparative Examples.
[0093] Example 1
Embodiment 6
[0094]In Example 6, the composition of the raw material or powder was within the scope of the present invention, but the temperature of the exhaust gas in the exhaust gas treatment system was not the result of operating under good conditions despite the method of the present invention. In addition, the same raw material as Example 5 was used as a raw material. Index 1 and Index 2 are the same as in Example 5. However, the temperature of the exhaust gas at the inlet of the exhaust gas outlet passage 2 is low at 760°C, and the temperature of the exhaust gas at the inlet of the heat exchanger 5 is high at 570°C. As a result, slight powder adhesion problems can occur in the exhaust gas treatment system. At the overhaul after 3 months of operation, it was confirmed that there was attachment at the entrance of exhaust gas outlet channel 2. Also, the inlet of the heat exchanger 5 is gradually clogged and must be cleaned after 2 months.
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