Microwave Continuous Suspension Roasting Method for Enhancing Dissociation of Complex Refractory Iron Ore
A suspension roasting and iron ore technology, applied in the field of mineral processing, to achieve the effect of improving the level of device automation and intelligence, realizing development and utilization, and achieving significant sorting effects
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Embodiment 1
[0054] The structure of the microwave continuous suspension roasting system is as follows: figure 1 As shown, it includes feeding bin 1, pretreatment fluidizer 2, microwave cavity 8, microwave generating device 5, reduction fluidizer 17, cooler 18 and collection tank 19;
[0055] The discharge port at the bottom of the feeding bin 1 is connected with the feed port of the pretreatment fluidizer 2, and the pretreatment fluidizer 2 is provided with a microwave cavity 8 outside, and a pretreatment baffle is arranged inside the pretreatment fluidizer 2 The interior is divided into a pretreatment feed chamber and a pretreatment discharge chamber. The top edge of the pretreatment baffle is connected to the top plate of the pretreatment fluidizer 2, and the two sides of the pretreatment baffle are connected to the pretreatment fluidizer 2. The side wall is connected, and the gap between the bottom edge of the pretreatment baffle and the bottom plate of the pretreatment fluidizer 2 is ...
Embodiment 2
[0081] System structure is the same as embodiment 1, and the difference is:
[0082] (1) The gas in the first gas storage tank is CO 2 ; The gas in the second gas storage tank is CO 2 , the gas in the third gas storage tank is H 2 ;
[0083](2) The volume ratio of the pretreatment feed chamber to the pretreatment discharge chamber is 1:5, the height ratio of the pretreatment baffle to the pretreatment fluidizer is 1:1; the reduction feed chamber to the reduction discharge chamber The volume ratio is 1:5, and the height ratio of the reduction baffle to the reduction fluidizer is 1:1;
[0084] Method is with embodiment 1, and difference is:
[0085] (1) Particle size ≤ 0.074mm in the iron ore powder accounts for 70% of the total mass, and the iron grade of the iron ore is 15.1%;
[0086] (2) The ratio of the total volume of protective gas passing into the pretreatment feed chamber and the pretreatment discharge chamber per unit time to the mass of iron ore powder passing in...
Embodiment 3
[0091] System structure is the same as embodiment 1, and the difference is:
[0092] (1) The gas in the third gas storage tank is CH 4 ;
[0093] (2) The volume ratio of the pretreatment feed chamber to the pretreatment discharge chamber is 1:8, the height ratio of the pretreatment baffle to the pretreatment fluidizer is 1:1.5; the reduction feed chamber to the reduction discharge chamber The volume ratio is 1:8, and the height ratio of the reduction baffle to the reduction fluidizer is 1:1.5;
[0094] Method is with embodiment 1, and difference is:
[0095] (1) Particle size ≤ 0.074mm in the iron ore powder accounts for 90% of the total mass, and the iron grade of the iron ore is 29.6%;
[0096] (2) The ratio of the total volume of protective gas passing into the pretreatment feed chamber and the pretreatment discharge chamber per unit time to the mass of iron ore powder passing into the pretreatment feed chamber is 7.5m 3 / kg, wherein the volume ratio of the protective g...
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