Study on a separation technology for more efficient utilization of pulverized coals in cement plants

被引:5
作者
Ha, Si [1 ]
Li, Ying [1 ]
Zhang, Hong [1 ]
Shi, Hai-Yan [1 ]
Zhu, Chao [1 ]
机构
[1] China Univ Min & Technol, Sch Chem Engn, Jiangsu 221008, Peoples R China
关键词
Cement plant; Pulverized coals; Combustion; Simulation; MINERAL MATTER; PARTICLE-SIZE; COMBUSTION; CFD;
D O I
10.1016/j.fuproc.2010.04.007
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A new separation technology for pulverized coals in cement plants was proposed. Two pulverized coals, NJ and ZZ, were sampled in two cement plants in China. Not only the ash and volatile matter content but also the size of the ash-containing particles and of those from which volatiles have to evolve have been determined with a float-sink method and a laser particle size analyzer. As the coal needed in a kiln and in a calciner is usually at a ratio of 4:6 in calorific value, the pulverized coals can be separated at 60 pm and 50 pm for NJ and ZZ samples, respectively. It was found that the ash content (air dry base) of the coarser part of NJ sample was 23.51%, in contrast to 34.72% before separation. Similarly, the ash content (air dry base) of the coarser part of ZZ sample was 13.86%. in contrast to 19.50% before separation. The coarser part of the coals is proposed to burn in a kiln while the finer part in a calciner. It was found from combustion simulation that the flames in a kiln are improved while the temperature profiles in a calciner change little. It is expected that the energy efficiency and cement quality will both be improved with this separation technique. Expected economical benefit and possible problems were discussed. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:1261 / 1266
页数:6
相关论文
共 20 条
[1]   Prediction of ignition behavior in a tangentially fired pulverized coal boiler using CFD [J].
Asotani, T. ;
Yamashita, T. ;
Tominaga, H. ;
Uesugi, Y. ;
Itaya, Y. ;
Mori, S. .
FUEL, 2008, 87 (4-5) :482-490
[2]  
Chen W. M., 1993, CALORIFIC VALUE CALC
[3]   Development of advanced technology for biomass combustion - CFD as an essential tool [J].
Dixon, TF ;
Mann, AP ;
Plaza, F ;
Gilfillan, WN .
FUEL, 2005, 84 (10) :1303-1311
[4]   A theoretical analysis on combustion intensification for blended coal in rotary cement kiln [J].
Hou, LY ;
Fu, WB ;
Zhang, YJ .
FUEL, 2001, 80 (11) :1645-1650
[5]  
HUNDEBOL S, 1993, 3 BEIJ INT S CEM CON, V3, P245
[6]  
LOCKWOOD FC, 1994, 25 S INT COMB COMB I, P503
[7]   Investigation on catalyzed combustion of high ash coal by thermogravimetric analysis [J].
Ma, Bao-Guo ;
Li, Xiang-Guo ;
Xu, Li ;
Wang, Kai ;
Wang, Xin-Gang .
THERMOCHIMICA ACTA, 2006, 445 (01) :19-22
[8]   Influence of petrographic and mineral matter composition of coal particles on their combustion reactivity [J].
Méndez, LB ;
Borrego, AG ;
Martinez-Tarazona, MR ;
Menéndez, R .
FUEL, 2003, 82 (15-17) :1875-1882
[9]   Temperature-programmed combustion studies of coal and maceral group concentrates [J].
Milligan, JB ;
Thomas, KM ;
Crelling, JC .
FUEL, 1997, 76 (13) :1249-1255
[10]   Influence of coal particle size on particulate matter emission and its chemical species produced during coal combustion [J].
Ninomiya, Y ;
Zhang, LA ;
Sato, A ;
Dong, ZB .
FUEL PROCESSING TECHNOLOGY, 2004, 85 (8-10) :1065-1088