张振兴;刘永启;高振强;刘瑞祥;
1:山东理工大学交通与车辆工程学院
摘要:为了选用合适的蓄热陶瓷体填充乏风氧化装置氧化床,首先对方形、圆管形和六边形蓄热陶瓷体的几何结构进行理论分析,得出特征长度对蓄热陶瓷体孔隙率和比表面积的影响规律。然后利用FLUENT软件对方形、圆管形和六边形蓄热陶瓷体进行模拟,得出在相同孔密度和开孔率条件下,选用方形孔可以获得较好的蓄热能力,选用圆管形、六边形孔可以降低其压强损失。在同孔隙率、比表面积和当量直径条件下,方形陶瓷体的阻力损失较低,六边形陶瓷体的传热效率较高。
关键词: 乏风;;蜂窝陶瓷;;传热;;氧化床;;压强损失
Abstract: In order to choose an appropriate
ceramic regenerator filled in regenerative oxidation bed of the thermal reverse
flow reactor,firstly the geometric structures of square,tube-shaped,and
hexagonal ceramic regenerators were analyzed and investigated theoretically and
effects of ceramic regenerator′s porosity and ratio surface area were obtained under the
characteristic length of the ceramic regenerator.And then these types of
ceramic regenerators were simulated by using Fluent software,the results were
that the square ceramic regenerator have a better regenerative ability while
the types of tube-shaped,hexagonal honeycomb ceramic regenerator can reduce the
pressure loss,concerning the same hole density and porosity.The resistance in a
square ceramic regenerator is lower and heat transfer efficiency in a hexagonal
ceramic regenerator is better under the conditions of the same
porosity,specific surface area and equivalent diameter.
Keywords: Ventilation Air Methane;Ceramic
Regenerator;Heat Transfer;Regenerative Oxidation Bed;Pressure Drop
基金项目: 国家(863)高技术研究发展计划重点项目(2009AA063202);
山东省自然科学基金(ZR2009FQ023)
参考文献:
[1]周娴.煤矿乏风低浓度甲烷氧化处理实验研究[D].北京:中国科学院,2009.
[2]K.Gosiewski,Y.S.Matros,K.Warmuzinski,et
al.Homogeneous vs.catalytic combustion of lean methane-airmixtures in
reverse-flow reactors[J].Chemical Engineer-ing Science,2008,63(10):5010-5019.
[3]王亚京,王璋保.节约能源是我国新型工业化的可观需求[J].工业炉.2003,25(4).9-13
[4]刘永启,刘瑞祥,高振强.矿井乏风瓦斯热氧化装置:中国,200810249860.3[P].2009-06-24.
[5]须藤淳,多田健.蜂窝型蓄热式燃烧系统的开发和应用[J].工业炉,1999(2):50-53.
[6]李茂德,程惠尔.高温空气燃烧系统中陶瓷蓄热体传热特性分析研究[J].热科学技术,2004,(33):255-260.
[7]靳世平,严亮,张喜来.陶瓷蓄热体换热性能和阻力性能的实验研究[J].湖北电力,2007,31(2):22-24.
[8]韩占忠,王敬,兰小平.FLUENT流体工程仿真计算实例与应用[M].北京:北京理工大学出版社,2004.
[9]陶文铨.数值传热学[M].西安:西安交通大学出版社,2001.
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