Enrichment of residual carbon from coal gasification fine slag by spiral separator

被引:51
|
作者
Yu, Wei [1 ,2 ]
Zhang, Hanlin [1 ]
Wang, Xuebin [1 ]
Rahman, Zia Ur [1 ]
Shi, Zhaochen [1 ]
Bai, Yonghui [3 ]
Wang, Guishan [4 ]
Chen, Yongqiang [4 ]
Wang, Jianjun [4 ]
Liu, Lijun [2 ]
机构
[1] Xi An Jiao Tong Univ, MOE Key Lab Thermo Fluid Sci & Engn, Xian, Peoples R China
[2] Xian Univ Sci & Technol, Sch Chem & Chem Engn, Xian, Peoples R China
[3] Ningxia Univ, State Key Lab High Efficiency Utilizat Coal & Gree, Yinchuan, Peoples R China
[4] Beijing Huichao Yunji Technol Co Ltd, Beijing, Peoples R China
关键词
Coal gasification fine slag; Spiral separator; Specific surface area; Porosity; PARTICLES;
D O I
10.1016/j.jenvman.2022.115149
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Coal gasification is one of the most promising clean coal technologies. However, gasification process also produces a huge amount of solid waste of high carbon content, named coal gasification fine slag. The coal gasification fine slag is mainly handled by landfilling, which is not only a hazardous pollution, but also wasting the energy from residual carbon. Developing a technology to utilize coal gasification fine slag and recover the residual carbon is becoming essential for an eco-friendly coal chemical industry. In this paper, the enrichment behavior of residual carbon in coal gasification fine slag by a spiral separator is studied. The raw coal gasification fine slag sample and separator products are characterized on particle size distribution, size-depending ash content, reactivity, micromorphology and porous structure. The experimental results show that the spiral separator is efficient to remove ash and enriched carbonaceous components in coal gasification fine slag by separating feed (100%) into concentrate (81.2%), middlings (8.8%), and tailings (10.08%), where the ash content in tailings is up to 90%, accounting for 18.5% of total ash in feeding. The beneficial product "concentrate" has a good distribution of size-depending ash content, that most combustibles are enriched in these particles of diameter >100 mu m. After spiral separator, the concentrate products have a more pure and developed porous structure with the surface area increasing from 199.8 m2/g (feeding) to 231.8 m2/g, as well as a better combustion reactivity of lower ignition temperature compared with feedings. Accordingly, an economic and feasible combination process of spiral separator connecting sieve can produce an enriched-carbon product of similar to 45% yield and similar to 80% carbonaceous content. The Iodine adsorption ability of sieved products increases by 47.6% compared with feed, and reaches up to about half of industry activated carbon. The finally sieved concentrate products have a good market prospect as fuel and adsorbent.
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页数:7
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