Attrition behavior of calcium-based waste during CO2 capture cycles using calcium looping in a fluidized bed reactor

被引:32
作者
Zhang, Wan [1 ]
Li, Yingjie [1 ]
Duan, Lunbo [2 ]
Ma, Xiaotong [1 ]
Wang, Zeyan [3 ]
Lu, Chunmei [1 ]
机构
[1] Shandong Univ, Sch Energy & Power Engn, Jinan 250061, Peoples R China
[2] Southeast Univ, Sch Energy & Environm, Key Lab Energy Thermal Convers & Control, Minist Educ, Nanjing 210096, Jiangsu, Peoples R China
[3] Shandong Univ, State Key Lab Crystal Mat, Jinan 250100, Peoples R China
基金
中国国家自然科学基金;
关键词
Carbide slag; Calcium looping; Attrition; CO2; capture; Fluidized bed; CAO-BASED SORBENT; CARBIDE SLAG; LIMESTONE CALCINATION; THERMAL-ANALYSIS; CARBON CAPTURE; PERFORMANCE; COMBUSTION; PELLETS; COAL; REACTIVATION;
D O I
10.1016/j.cherd.2016.04.003
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effects of reaction temperature, fluidization number, particle size and number of calcination/carbonation cycles on attrition and CO2 uptake characteristics of carbide slag during the calcium looping cycles were investigated in a fluidized bed reactor. The attrition behaviors of carbide slag and limestone were also compared. Higher calcination temperature in 850-950 degrees C improves the attrition rate of carbide slag particles. CO2 uptake capacity of carbide slag increases with fluidization number in carbonation. As fluidization number increases from 7 to 15, the mean diameter of carbide slag particles decreases by 4% and the attrition rate increases by 1.7 times after 10 cycles. Smaller particles show higher attrition resistance during the cycles. The breakage of larger particles of limestone is more severe than that of carbide slag during the cycles. CO2 uptake capacity of the carbide slag is practically identical to that of limestone in short carbonation duration (e.g. 5 min) during the cycles. The effects of the number of calcination/carbonation cycles on the mean diameter and the attrition rate of carbide slag are less than those of limestone. Carbide slag possesses higher attrition resistance than limestone during the multiple CO2 capture cycles. (C) 2016 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:806 / 815
页数:10
相关论文
共 47 条
[31]   Influence of calcination conditions on carrying capacity of CaO-based sorbent in CO2 looping cycles [J].
Manovic, Vasilije ;
Charland, Jean-Pierre ;
Blamey, John ;
Fennell, Paul S. ;
Lu, Dennis Y. ;
Anthony, Edward J. .
FUEL, 2009, 88 (10) :1893-1900
[32]   Crystallographic transformation of limestone during calcination under CO2 [J].
Manuel Valverde, Jose ;
Medina, Santiago .
PHYSICAL CHEMISTRY CHEMICAL PHYSICS, 2015, 17 (34) :21912-21926
[33]   On the negative activation energy for limestone calcination at high temperatures nearby equilibrium [J].
Manuel Valverde, Jose .
CHEMICAL ENGINEERING SCIENCE, 2015, 132 :185-193
[34]   Ca-based synthetic materials with enhanced CO2 capture efficiency [J].
Manuel Valverde, Jose .
JOURNAL OF MATERIALS CHEMISTRY A, 2013, 1 (03) :447-468
[35]   Attrition of sorbents during fluidized bed calcination and sulphation [J].
Scala, F ;
Salatino, P ;
Boerefijn, R ;
Ghadiri, M .
POWDER TECHNOLOGY, 2000, 107 (1-2) :153-167
[36]   Attrition of limestone by impact loading in fluidized beds [J].
Scala, Fabrizio ;
Montagnaro, Fabio ;
Salatino, Piero .
ENERGY & FUELS, 2007, 21 (05) :2566-2572
[37]   A twin fluid-bed reactor for removal of CO2 from combustion processes [J].
Shimizu, T ;
Hirama, T ;
Hosoda, H ;
Kitano, K ;
Inagaki, M ;
Tejima, K .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 1999, 77 (A1) :62-68
[38]   Feasibility Study on the Carbonate Looping Process for Post-Combustion CO2 Capture from Coal-Fired Power Plants [J].
Stroehle, Jochen ;
Galloy, Alexander ;
Epple, Bernd .
GREENHOUSE GAS CONTROL TECHNOLOGIES 9, 2009, 1 (01) :1313-1320
[39]   Enhanced performance of extruded-spheronized carbide slag pellets for high temperature CO2 capture [J].
Sun, Jian ;
Liu, Wenqiang ;
Hu, Yingchao ;
Wu, Jianqun ;
Li, Mingkui ;
Yang, Xinwei ;
Wang, Wenyu ;
Xu, Minghou .
CHEMICAL ENGINEERING JOURNAL, 2016, 285 :293-303
[40]   Limestone Calcination Nearby Equilibrium: Kinetics, CaO Crystal Structure, Sintering and Reactivity [J].
Valverde, J. M. ;
Sanchez-Jimenez, P. E. ;
Perez-Maqueda, L. A. .
JOURNAL OF PHYSICAL CHEMISTRY C, 2015, 119 (04) :1623-1641