THE NUMERICAL SIMULATION AND THE STRUCTURE OPTIMIZATION OF THE TINY-OIL IGNITION BURNER

被引:0
作者
Fu, Zhongguang [1 ]
Wang, Mingchen [1 ]
Zhou, Chenn Qian
Peng, Guosheng
Yang, Guoqiang
机构
[1] N China Elect Power Univ, Sch Energy & Power Engn, Beijing 102206, Peoples R China
来源
IMECE2009: PROCEEDINGS OF THE ASME INTERNATIONAL MECHANICAL ENGINEERING CONGRESS AND EXPOSITION, VOL 3 | 2010年
关键词
CFD; tiny-oil ignition burner; pulverized coal burner; structure optimization; pulverized coal boiler; power plant; COAL; COMBUSTION; HEAT;
D O I
暂无
中图分类号
O414.1 [热力学];
学科分类号
摘要
The pulverized coal burner is widely used in industry, especially in electricity industry. Stable combustion of the burner is very important to conserve energy and minimize environmental impact. Generally, most of gas or oil will be consumed when the burner is ignited. Meanwhile, the operation of the dust catcher will be affected when oil is burned in the furnace which leads to more emission of solid particle into the air. Tiny-oil ignition burner can be a solution to the above problems. The structure of burner should be different for fuel and each different application. It is a challenge to optimize the structure of burner. Three-dimensional CFD simulations were performed to optimize the design of a tiny-oil ignition burner. The temperature distributions along the central line of the tiny-oil ignition burner show that the structure of the oil combustion chamber and the first combustion chamber are worthy of optimization based on the type of Chinese coal.
引用
收藏
页码:167 / 172
页数:6
相关论文
共 6 条
[1]   PREDICTING COMBUSTION BEHAVIOUR OF COAL PARTICLES [J].
BAUM, MM ;
STREET, PJ .
COMBUSTION SCIENCE AND TECHNOLOGY, 1971, 3 (05) :231-&
[2]   RADIATIVE HEAT-TRANSFER MODEL INT HE INTERIOR OF A PULVERIZED COAL FURNACE [J].
CANADAS, L ;
SALVADOR, L ;
OLLERO, P .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (04) :669-675
[3]  
DEMICHELE G, 1989, ASME 26 NAT HEAT TRA, P275
[4]   RATE OF COMBUSTION OF SIZE-GRADED FRACTIONS OF CHAR FROM A LOW-RANK COAL BETWEEN 1200 DEGREES K AND 2000 DEGREES K [J].
FIELD, MA .
COMBUSTION AND FLAME, 1969, 13 (03) :237-&
[5]   CALCULATION PROCEDURE FOR HEAT, MASS AND MOMENTUM-TRANSFER IN 3-DIMENSIONAL PARABOLIC FLOWS [J].
PATANKAR, SV ;
SPALDING, DB .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1972, 15 (10) :1787-&
[6]  
Wang Zibing, 2008, THESIS N CHINA ELECT