Reduction of Quartz to Silicon Monoxide by Methane-Hydrogen Mixtures

被引:12
作者
Li, Xiang [1 ,2 ]
Zhang, Guangqing [1 ]
Tronstad, Ragnar [3 ]
Ostrovski, Oleg [4 ]
机构
[1] Univ Wollongong, Sch Mech Mat & Mechatron Engn, Wollongong, NSW 2522, Australia
[2] Univ Sci & Technol NTNU, Trondheim, Norway
[3] Elkem AS, R&D, Drammensveien 169,POB 334, N-0213 Oslo, Norway
[4] Univ New South Wales, Sch Mat Sci & Engn, Sydney, NSW 2052, Australia
来源
METALLURGICAL AND MATERIALS TRANSACTIONS B-PROCESS METALLURGY AND MATERIALS PROCESSING SCIENCE | 2016年 / 47卷 / 04期
基金
澳大利亚研究理事会;
关键词
ARGON GAS-MIXTURE; CARBIDE WHISKERS; SIC WHISKERS; VLS PROCESS; KINETICS; GROWTH;
D O I
10.1007/s11663-016-0670-5
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
The reduction of quartz was studied isothermally in a fluidized bed reactor using continuously flowing methane-hydrogen gas mixture in the temperature range from 1623 K to 1773 K (1350 A degrees C to 1500 A degrees C). The CO content in the off-gas was measured online using an infrared gas analyzer. The main phases of the reduced samples identified by XRD analysis were quartz and cristobalite. Significant weight loss in the reduction process indicated that the reduction products were SiO and CO. Reduction of SiO2 to SiO by methane starts with adsorption and dissociation of CH4 on the silica surface. The high carbon activity in the CH4-H-2 gas mixture provided a strongly reducing condition. At 1623 K (1350 A degrees C), the reduction was very slow. The rate and extent of reduction increased with the increasing temperature to 1723 K (1450 A degrees C). A further increase in temperature to 1773 K (1500 A degrees C) resulted in a decrease in the rate and extent of reduction. An increase in the gas flow rate from 0.4 to 0.8 NL/min and an increase in the methane content in the CH4-H-2 gas mixture from 0 to 5 vol pct facilitated the reduction. Methane content in the gas mixture should be maintained at less than 5 vol pct in order to suppress methane cracking.
引用
收藏
页码:2197 / 2204
页数:8
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