Mixing and segregation of binary mixtures of biomass and silica sand in a fluidized bed

Particuology ◽  
2021 ◽  
Author(s):  
Tolu Emiola-Sadiq ◽  
Jiachen Wang ◽  
Lifeng Zhang ◽  
Ajay Dalai
Energies ◽  
2019 ◽  
Vol 12 (10) ◽  
pp. 2011
Author(s):  
Guiying Wu ◽  
Bangting Yu ◽  
Yanjun Guan ◽  
Xuehui Wu ◽  
Kai Zhang ◽  
...  

Aiming to better understand the biomass pyrolysis and gasification processes, a detailed experimental study of the mixing characteristics is conducted in a fluidized bed with binary mixtures. Rapeseed is used as biomass, and silica sand or resin as inert material. The effect of mixture composition, initial packing manner, and superficial gas velocity on the concentration distribution is investigated in a rectangular fluidized bed by means of photography and sampling methods. The results show that the mixture composition plays an important role in the axial solids profile of binary mixtures. The mixing behavior of binary mixture is dominated by the bubble movement. The axial distribution of binary mixtures becomes uniform with increasing superficial gas velocity, whilst no obvious effect of initial packing manner is observed in this study.


2005 ◽  
Vol 38 (12) ◽  
pp. 960-968 ◽  
Author(s):  
Zhanyong Li ◽  
Noriyuki Kobayashi ◽  
Masanobu Hasatani

2020 ◽  
Vol 371 ◽  
pp. 161-169 ◽  
Author(s):  
Zhijie Fu ◽  
Jesse Zhu ◽  
Shahzad Barghi ◽  
Yuemin Zhao ◽  
Zhenfu Luo ◽  
...  

Author(s):  
Anton Pylypenko ◽  
Yevgenii Rastigejev ◽  
Lijun Wang ◽  
Abolghasem Shahbazi

The objective of this work is to analyze the dynamics and regimes of cold gas-solid flow in a biomass gasifier that is built at North Carolina Agricultural and Technical State University and to identify its corresponding ranges of operating conditions. The value of the minimum fluidization velocity Umf ≈ 8 cm/s has been found experimentally in a series of measurements of a pressure drop in the fluidized bed filled with Gledart type-B silica sand for the range of superficial gas velocities between 0 and 40 cm/s. To complement the experimental results, a set of three-dimensional numerical simulations of the isothermal gas-solid flow based on Eulerian-Eulerian approach has been performed. The analysis of the fluidization characteristics such as axial void fraction distributions has allowed us to evaluate the dependence of the bed expansion ratios from the flow superficial velocity. Good agreement between experimental and numerical results for the considered operating conditions of the gasifier has been observed.


2020 ◽  
Vol 31 (2) ◽  
pp. 867-874
Author(s):  
Yosuke Tsuboi ◽  
Yasuzo Kumagai ◽  
Toshiyuki Suda ◽  
Jun-ichiro Hayashi

Fuel ◽  
2019 ◽  
Vol 243 ◽  
pp. 509-518 ◽  
Author(s):  
Zhijie Fu ◽  
Jesse Zhu ◽  
Shahzad Barghi ◽  
Yuemin Zhao ◽  
Zhenfu Luo ◽  
...  

2011 ◽  
Vol 66 (8) ◽  
pp. 1702-1714 ◽  
Author(s):  
Pei Pei ◽  
Kai Zhang ◽  
Bangting Yu ◽  
Jing Gao ◽  
Guiying Wu ◽  
...  

2013 ◽  
Vol 234 ◽  
pp. 67-75 ◽  
Author(s):  
Yingjuan Shao ◽  
Bing Ren ◽  
Baosheng Jin ◽  
Wenqi Zhong ◽  
Hao Hu ◽  
...  

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