华北电力大学能源与动力工程学院,河北,保定,071003
网络首发:2013-03-10,
纸质出版:2013
移动端阅览
阎维平, 马凯, 高正阳, 等. 增压富氧燃煤锅炉省煤器管束磨损研究[J]. 西安交通大学学报, 2013,47(3):53-59.
Erosion of Economizer Tube Bundles in Pressurized Oxy-Fuel Coal-Fired Boiler[J]. 2013, 47(3): 53-59.
阎维平, 马凯, 高正阳, 等. 增压富氧燃煤锅炉省煤器管束磨损研究[J]. 西安交通大学学报, 2013,47(3):53-59. DOI: 10.7652/xjtuxb201303010.
Erosion of Economizer Tube Bundles in Pressurized Oxy-Fuel Coal-Fired Boiler[J]. 2013, 47(3): 53-59. DOI: 10.7652/xjtuxb201303010.
针对常压空气燃烧和增压富氧燃烧两种工况
利用CFD软件、应用k-ε双方程模型模拟锅炉省煤器管束间烟气的流动
用拉格朗日方法研究管束间颗粒的运动
并利用颗粒与管壁的碰撞和反弹模型考虑颗粒与壁面碰撞后的运动。通过对比3种磨损模型
得出Oka模型考虑的因素相对更全面
与实验数据也比较吻合。利用该模型可得壁面磨损量随流速呈指数规律变化
随着入射角度的增大磨损量先增加后减小
壁面材料硬度越大
磨损量越小
并且随着颗粒粒径增大磨损量略有增加。增压富氧燃烧下
最大磨损速率比常压下小很多
且最大磨损位置也发生了变化
各管排的颗粒撞击和平均磨损速率分布较均匀
除了第1排管外
单管最大磨损区域位于管壁迎风阶两侧60°附近。这对省煤器实际运行及增压富氧燃烧下省煤器的设计有重要意义。
A simulation on the flue gas flow between the economizer tube bundles was performed using the k-ε two-equation model in the CFD software. The particle motion between the bundles was examined by the Lagrangian method and the particle motion after collision with the wall was investigated using the collision and bounce model for the situations of atmospheric air combustion and pressurized oxy-fuel combustion. By comparing three wear models
it is found that model Oka is relatively more comprehensive and more consistent with the experimental data. According to the model
the amount of wall erosion changes exponentially with an increase in the flow rate
and it increases first and then decreases with the increase in the incidence angle. The erosion decreases with an increase in the hardness of the wall
and it increases slightly with the particle size. Under pressurized oxy-fuel combustion
the maximum erosion rate is much lower than that under atmospheric condition
the position of the maximum erosion changes and the particle impact and erosion rate distributes more uniform on each tube row. The single-tube maximum erosion area is located near 60 degrees of the wall on both sides of the windward-order except the first row. These results are of significance for the economizer design and operation under pressurized oxy-fuel combustion.
阎维平. 洁净煤发电技术 [M]. 2版. 北京: 中国电力出版社, 2008: 183-190.
米翠丽. 富氧燃煤锅炉设计研究及其技术经济性分析 [D]. 北京: 华北电力大学, 2010.
岑可法, 樊建人, 池作和, 等. 锅炉和热交换器的积灰、结渣、磨损和腐蚀的防止原理和计算 [M]. 北京: 科学出版社, 1994.
陈丽华, 金军, 樊建人, 等. 电站锅炉受热面管束防磨技术的研究 [J]. 中国电机工程学报, 1999, 19(7): 67-71.
CHEN Lihua, JIN Jun, FAN Jianren, et al. Study on the erosion protection technique for the boiler tube bundles of power plant [J]. Proceedings of the CSEE, 1999, 19(7): 67-71.
GANDHI M B, VUTHALURU R, VUTHALURU H, et al. CFD based prediction of erosion rate in large scale wall-fired boiler [J]. Applied Thermal Engineering, 2012, 42(1): 90-100.
HONG J, CHAUDHRY G, BRISSON J G, et al. Analysis of oxy-fuel combustion power cycle utilizing a pressurized coal combustion [J]. Energy, 2009, 34(9): 1332-1340.
马凯, 阎维平, 高正阳. 增压富氧燃烧烟气物性及对流传热系数的研究 [J]. 动力工程学报, 2011, 31(11): 55-62.
MA Kai, YAN Weiping, GAO Zhengyang. Flue gas properties and convective heat transfer coefficient under pressurized oxy-fuel combustion [J]. Journal of Power Engineering, 2011, 31(11): 55-62.
MORSI Y S, TU J Y, YEOH G H, et al. Principal characteristics of turbulent gas-particulate flow in the vicinity of single tube and tube bundle structure [J]. Chemical Engineering Science, 2004, 59(15): 3141-3157.
刘洪涛. 气固两相流中微细颗粒沉积与扩散特性的数值研究 [D]. 重庆: 重庆大学, 2010.
WANG Jianrong, SHIRAZI S A. A CFD based correlation for erosion factor for long-radius elbows and bends [J]. ASME Journal of Energy Resources Technology, 2003, 125(1): 26-34.
吕萍, 王鹏. 不同粒径飞灰对顺列管束磨损的非线性特性研究 [J]. 太原理工大学学报, 2011, 42(4): 420-423.
LU Ping, WANG Peng. Non-linear characteristics study on wear of in-line bundle by fly-ash with different diameters [J]. Journal of Taiyuan University of Technology, 2011, 42(4): 420-423.
ROBERT W L, JACQUES X B. State-of-the-art review of erosion modeling in fluid/solids systems [J]. Progress in Energy and Combustion Science, 2002, 28(6): 543-602.
MBABAZI J G, SHEER T J, SHANDU R. A model to predict erosion on mild steel surfaces impacted by boiler fly ash particles [J]. Wear, 2004, 257(5/6): 612-624.
CHEN X H, MCLAURY B S, SHIRAZI S A. Application and experimental validation of a computational fluid dynamics(CFD)-based erosion prediction model in elbows and plugged tees [J]. Computers Fluids, 2004, 33(10): 1251-1272.
ZHANG Yongli. Application and improvement of computational fluid dynamics(CFD)in solid particle erosion modeling [D]. Tulsa, OK, USA: The University of Tulsa, 2006.
OKA Y I, OKAMURA K, YOSHIDA T. Practical estimation of erosion damage caused by solid particle impact: Part 1 Effects of impact parameters on a predictive equation [J]. Wear, 2005, 259(1/6): 95-101.
OKA Y I, YOSHIDA T. Practical estimation of erosion damage caused by solid particle impact: Part 2 Mechanical properties of materials directly associated with erosion damage [J]. Wear, 2005, 259(1/6): 102-109.
BENEDETTO B, MARCO E R, MARCO B, et al. Evaluation of erosion-corrosion in multiphase flow via CFD and experimental analysis [J]. Wear, 2003, 255(1/6): 237-245.
BOURGOYNE A. Experimental study of erosion in diverter systems due to sand production [C]∥Proceedings of SPE/IADC Drilling Conference. New Orleans, LA, USA: Society of Petroleum Engineers, 1989: 807-816.
0
浏览量
4
下载量
5
CSCD
关联资源
相关文章
相关作者
相关机构
京公网安备11010802024621