期刊文献+

三维流化床内生物质及石英砂混合颗粒的流动特性 被引量:2

Flow characteristics of biomass particles and quartz sands in 3D fluidized bed
下载PDF
导出
摘要 选择锯花、花生壳、稻壳、蔗渣为实验对象,将不同质量的生物质与石英砂混合作为床料,加入三维流化床试验台内混合流动,测量床内的压差脉动信号,床高1000mm,截面尺寸为120mm×32mm。实验结果表明当生物质质量分数小于等于2%时,生物质的种类及质量分数对最小流化速度的影响可以忽略不计。利用快速傅里叶变换变换分析压差脉动信号,研究双组分流动特征。结果表明,添加稻壳时压力脉动在低气速下主频位于10~15Hz区间内,并随着气速的增加向20~25Hz的高频区移动;蔗渣、花生壳及锯花等片状生物质在较低气速下主频消失,较高气速下主频存在于10~15Hz区间内。 Waste wood,peanut shells,rice husk,and pomace of sugarcane were chosen as experiment raw materials and mixed with quartz sands at different mass ratio to investigate the influence of biomass species and mass ratio in a 3D laboratory fluidized bed. The bed size is 1000 mm in height and 120mm×32mm of cross section horizontally. The pressure fluctuation inside the bed was recorded and analyzed. The results show that biomass species and mass ratio had negligible effect on minimum fluidization velocity when mass ratio was less than 0.02. Fast Fourier transform was employed to obtain the power spectral density of pressure fluctuation signals. It's shown that the PSD of pressure fluctuation at lower velocity ranged from 10 Hz to 15 Hz when rice husk was added,and increased to about 20 Hz to 25 Hz when the velocity increased. Pomace of sugarcane,peanut shells,and waste wood had no main frequency at lower velocity,but when the velocity increased the main frequency was found to be ranged from 10 Hz to 15Hz.
出处 《化工进展》 EI CAS CSCD 北大核心 2017年第2期473-480,共8页 Chemical Industry and Engineering Progress
基金 国家自然科学基金项目(51276040,U1361115)
关键词 生物质 压力脉动 流化床 功率谱密度 biomass pressure fluctuation fluidized bed power spectral density
  • 相关文献

参考文献4

二级参考文献35

  • 1漆小波,曾涛,黄卫星,祝京旭,石炎福.循环流化床提升管中团聚物颗粒浓度的实验研究[J].四川大学学报(工程科学版),2005,37(5):46-50. 被引量:12
  • 2冯连芳,张文峰,王嘉骏,顾雪萍,王凯.气固搅拌流化床内的压力脉动特性[J].浙江大学学报(工学版),2007,41(3):524-528. 被引量:6
  • 3蔡平 汪展文 等.气-固流化床压力信号的细化功率谱分析系统[J].化工冶金,1988,9(1):15-21.
  • 4Lu Huilin, Gidaspow D, Bouillard J X. Dimension measurements of hydrodynamic attractors in circulating fluidized beds. Powder Technology, 1997, 90: 179-185.
  • 5Lu Huilin, Gidaspow D, Bouillard J X. Chaotic behavior of local temperature fluctuations in a laboratory scale circulating fluidized. Powder Technology, 2002, 123:59 -68.
  • 6Malcus S, Chaplin G, Pugsley T. The hydrodynamics of the high density bottom zone in a CFB riser analyzed by means of electrical capacitance tomography ( ECT ). Chemical Engineering Science, 2000, 55:4129 -4138.
  • 7Srivastava A, Agrawal K, Sundaresan S, et al. Dynamics of gas particle flow in circulating fluidized beds. Powder Technology, 1998, 100:173-182.
  • 8Hsiaotao T Bai. A critical review of the complex pressure fluctuation phenomenon in gas-solids fluidized beds. Chemical Engineering Science, 2007, 62:3473 -3493.
  • 9van der Schaaf J, Schouten J C, van den Bleek C M. Origin, propagation and attenuation of pressure waves in gas-solid fluidized beds. Powder Technology, 1998, 95: 220- 233.
  • 10Zijerveld R C, Characterization of fluidization Schouten J regimes by C, et al. time series analysis of pressure fluctuations. International Journal of Multiphase Flow, 2000, 26:663- 715.

共引文献115

同被引文献15

引证文献2

二级引证文献5

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部