选矿
分离器(采油)
流化床
煤
洁净煤
粉煤灰
析因实验
粒径
废物管理
材料科学
环境科学
制浆造纸工业
冶金
工程类
数学
化学工程
物理
统计
热力学
作者
Ebrahim Azimi,Shayan Karimipour,Zhenghe Xu,Jozef Szymanski,Rajender Gupta
标识
DOI:10.1080/19392699.2015.1123155
摘要
ABSTRACTIn this study, the performance of a continuous air dense medium fluidized bed (ADMFB) separator is investigated for coal beneficiation. The full factorial experimental design method is used to study the effect of superficial air velocity (U), bed length (T), and bed height (H) on the clean-coal ash content, organic material recovery, and overall system separation efficiency. Optimum operating conditions are determined and followed by the effect of feed particle size on separation quality. Statistical analysis of the results revealed that H had no significant effect on product ash content while U and T had negative effects. A reduction in ash content from 19% to 10% was obtained once full bed length was utilized. The increase of all parameters had a negative effect on organic material recovery, while recovery was always above 88%. The only significant mutual interaction was found to be between T and H with even more effectiveness than U on the recovery. Separation efficiency increased by increasing the bed length and reached 20% once full bed length was utilized. The optimum operating condition was determined to be at U = 19.5 cm/s, T = full bed length, and H = 15 cm. It was observed that feeding finer particles deteriorated the beneficiation process.KEYWORDS: Dry coal beneficiationgravity separationcontinuous air dense medium fluidized beddesign of experimentsstatistical analysis AcknowledgmentThe valuable assistance of Dr. Moshfiqur Rahman from the University of Alberta is gratefully acknowledged for the experimental work of this article.FundingThe authors acknowledge the financial support from Carbon Management Canada (CMC) and Canadian Centre for Clean Coal/Carbon and Mineral Processing Technologies (C5MPT) that made this research possible.Additional informationFundingThe authors acknowledge the financial support from Carbon Management Canada (CMC) and Canadian Centre for Clean Coal/Carbon and Mineral Processing Technologies (C5MPT) that made this research possible.
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