Effect of waste incineration and gasification processes on heavy metal distribution

被引:42
作者
Wu, Min-Hao [1 ]
Lin, Chiou-Liang [1 ]
Zeng, Wun-Yue [1 ]
机构
[1] Natl Univ Kaohsiung, Dept Civil & Environm Engn, Kaohsiung 811, Taiwan
关键词
Incineration; Gasification; Heavy metal; Fluidized bed; Waste; MSWI FLY-ASH; FLUIDIZATION VELOCITY; PARTICLE-SIZE; CHLORINE; MOISTURE; BOTTOM; SULFUR; CD;
D O I
10.1016/j.fuproc.2014.03.027
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
This study investigates the distribution of heavy metals during incineration and gasification. Because heavy metals (Cr, Pb, Cd) become volatile at high temperatures, their concentrations in fly ash increase as the operating temperature of incineration/gasification increases. By contrast, the efficiency of the bed-material mixing and the contact between the bed material and the heavy metals inside the fluidized bed increase when the operating-gas velocity increases; hence, the heavy-metal content in the bed material also increases. Our results show that the heavy-metal content in the fly ash increases with the bed-material particle size. The probability of contact between the heavy metals and the bed material is reduced at higher bed-material particle sizes; hence, the emission concentration of heavy metals increases. The heavy-metal concentration in the fly ash after gasification is approximately 1/10-1/30 of that after incineration. However, the proportion of the heavy metals trapped in the bottom ash after gasification is higher than that after incineration under any of the operating conditions, regardless of the volatility of the heavy metals. Overall, gasification lowers the emissions of heavy metals, but traps more heavy metals in the bottom ash than incineration. Crown Copyright (C) 2014 Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:67 / 72
页数:6
相关论文
共 25 条
[1]   FATE OF METALS IN WASTE COMBUSTION SYSTEMS [J].
BARTON, RG ;
CLARK, WD ;
SEEKER, WR .
COMBUSTION SCIENCE AND TECHNOLOGY, 1990, 74 (1-6) :327-342
[2]   Theoretical and experimental study of metal capture during incineration process [J].
Chen, JC ;
Wey, MY ;
Yan, MH .
JOURNAL OF ENVIRONMENTAL ENGINEERING-ASCE, 1997, 123 (11) :1100-1106
[3]   BUBBLE-SIZE AND FREQUENCY IN GAS-FLUIDIZED BEDS [J].
CHOI, JH ;
SON, JE ;
KIM, SD .
JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1988, 21 (02) :171-178
[4]   Utilization of washed MSWI fly ash as partial cement substitute with the addition of dithiocarbamic chelate [J].
Gao, Xingbao ;
Wang, Wei ;
Ye, Tunmin ;
Wang, Feng ;
Lan, Yuxin .
JOURNAL OF ENVIRONMENTAL MANAGEMENT, 2008, 88 (02) :293-299
[5]   ATMOSPHERIC EMISSIONS OF METALS FROM SEWAGE-SLUDGE INCINERATION [J].
GERSTLE, RW ;
ALBRINCK, DN .
JOURNAL OF THE AIR POLLUTION CONTROL ASSOCIATION, 1982, 32 (11) :1119-1123
[6]  
Hiraoka M., 1980, TOXIC HAZARDOUS WAST, V3, P107
[7]   Use of a transient model to simulate fluidized bed incineration of sewage sludge [J].
Khiari, B. ;
Marias, F. ;
Zagrouba, F. ;
Vaxelaire, J. .
JOURNAL OF HAZARDOUS MATERIALS, 2006, 135 (1-3) :200-209
[8]   Mechanisms of particle agglomeration and inhibition approach in the existence of heavy metals during fluidized bed incineration [J].
Kuo, Jia-Hong ;
Lin, Chiou-Liang ;
Wey, Ming-Yen .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (17) :4955-4966
[9]   Investigation of heavy metal partitioning influenced by flue gas moisture and chlorine content during waste incineration [J].
Li, Qinghai ;
Meng, Aihong ;
Jia, Jinyan ;
Zhang, Yanguo .
JOURNAL OF ENVIRONMENTAL SCIENCES, 2010, 22 (05) :760-768
[10]   The effect of particle size distribution on minimum fluidization velocity at high temperature [J].
Lin, CL ;
Wey, MY ;
You, SD .
POWDER TECHNOLOGY, 2002, 126 (03) :297-301