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Kinetics of Reduction Reaction in Micro-Fluidized Bed

LIN Yin-he , GUO Zhan-cheng , TANG Hui-qing , REN Shan , LI Jing-wei

钢铁研究学报(英文版)

Micro-fluidized bed reactor is a new research method for the reduction of iron ore fines. The reactor is operated as a differential reactor to ensure a constant gas concentration and temperature within the reactor volume. In order to understand the dynamic process of the reduction reaction in micro-fluidized bed, a series of kinetic experiments were designed. In the micro-fluidized bed, the use of shrinking core model describes the dynamic behavior of reduction of iron ore. And the apparent activation energy is calculated in the range of 700-850 ℃ while the initial atmosphere is 100% content of CO.

关键词: iron ore reduction , micro-fluidized bed , dynamics

Combustion Ratio of Waste Tire Particle, PC and Mixture at Blast Temperature of BF

ZHANG Jian-liang , REN Shan , SU Bu-xin , LIN Yin-he , LONG Shi-gang

钢铁研究学报(英文版)

In order to study the combustion characteristics of waste tire particle (WTP), pulverized coal (PC) and their mixture, the contents of CO, CO2 and O2 of off-gas during the combustion of WTP, PC and mixture under the condition of rich oxygen by 0-4% in blast and at 1250 ℃ were measured simultaneously using synthetically infrared analyzer, and then the corresponding combustion ratio was calculated and compared. The results showed that the burning rate of WTP reached approximately 57%, which is much higher than that of PC (only about 18%) in the initial 650 s in fresh air, and then the increase of combustion rate of PC is faster than that of WTP; the combustion rate of PC improved remarkably with the addition of WTP. Meanwhile, the combustion rates of all these materials improved with the increase of oxygen content.

关键词: blast furnace , waste tire particle , pulverized coal , combustion ratio

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