Numerical Simulation on Superheated Steam Fluidized Bed Drying: I. Model Construction

2011 ◽  
Vol 29 (11) ◽  
pp. 1325-1331 ◽  
Author(s):  
Deyong Yang ◽  
Zhenhua Wang ◽  
Xiaoli Huang ◽  
Zhifeng Xiao ◽  
Xiangdong Liu
2011 ◽  
Vol 29 (11) ◽  
pp. 1332-1342 ◽  
Author(s):  
Yongchun Shi ◽  
Zhifeng Xiao ◽  
Zhenhua Wang ◽  
Xiangdong Liu ◽  
Deyong Yang

2017 ◽  
Vol 13 (10) ◽  
Author(s):  
Xiao Zhifeng ◽  
Zhang Fan ◽  
Xu Lei ◽  
Wang Jianhong ◽  
Wu Nanxing

AbstractDuring superheated steam fluidized bed drying process, the operating pressure has an important influence on heat and mass transfer characteristics and the vapor-solid two-phase flow characteristics. Based on the two-dimensional unsteady model of rapeseeds drying process, the influence of operating pressure on the superheated steam fluidized bed drying kinetics was revealed by computer numerical simulation. The quantitative analysis of relationship between operating pressure and maximum drying rate was conducted under negative pressure, near atmospheric pressure and high pressure environment, respectively. The optimum operating pressure values for superheated steam fluidized bed drying were obtained with the imported superheated steam temperature and superficial velocity. The simulation results provide a theoretical reference for superheated steam fluidized bed drying technology applying to agro-processing projects.


2013 ◽  
Vol 27 (11) ◽  
pp. 6598-6606 ◽  
Author(s):  
David Stokie ◽  
Meng Wai Woo ◽  
Sankar Bhattacharya

2013 ◽  
Vol 295-298 ◽  
pp. 467-470
Author(s):  
Zhi Feng Xiao ◽  
Xing Bao ◽  
Nan Xing Wu

In the paper, we theoretical analysis the gas-particle flow behaviors in the drying chamber. Then establish a small experimental device and conduct a comparative fluidization experiment with superheated steam and hot air, which the dried rapeseed particles are the experimental material. The critical fluidizing velocity of the rapeseed particles in superheated steam is 1.26 m/s in the experimental condition. The experimental results show that the inlet operating flow velocity of superheated steam fluidized bed drying is greater than which of the traditional hot air fluidized bed dying under the same conditions.


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