Systematic analysis of mixing and segregation patterns of binary mixtures in fluidised beds for multi-functional processes

被引:2
作者
Zhu, Hualun [1 ]
Lettieri, Paola [1 ]
Materazzi, Massimiliano [1 ]
机构
[1] UCL, Dept Chem Engn, London WC1E 7JE, England
基金
英国工程与自然科学研究理事会;
关键词
Binary particles; X-ray imaging; Fluidized bed; Mixing and segregation; Sorption-enhanced; ENHANCED METHANOL SYNTHESIS; MUNICIPAL SOLID-WASTE; PARTICLE-SIZE; HYDRODYNAMICS; MODEL; PERFORMANCE; COMBUSTION; VELOCITY; REACTOR;
D O I
10.1016/j.powtec.2024.120419
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Fluidized beds are increasingly used in renewable energy and chemical production due to their versatility in handling different solids for multi-functional industrial applications. The diversity in size and density of solid particles impacts fluidization, influencing mixing and segregation behaviours critical for optimizing chemical processes and reactor design. This study investigates the expansion and segregation behaviours of mixed Geldart group powders in binary systems, simulating polydispersed beds with different materials and catalysts. By applying a modified Cheung equation and an adapted Gibilaro-Rowe model, the study analyzes segregation behaviours of Geldart Group A and B materials at varying mixing rates and gas flow velocities. Results show a good match between experimental data and model predictions. Using novel non-invasive X-ray imaging, the study provides real-time analysis of mixing and segregation at different fluidization regimes and temperatures. These findings aid in designing and optimizing advanced thermochemical conversion technologies, enhancing process efficiency and resilience.
引用
收藏
页数:10
相关论文
共 47 条
[1]   Investigation of the efficiency of sorption-enhanced methanol synthesis process in circulating fast fluidized bed reactors [J].
Abashar, M. E. E. ;
Al-Rabiah, A. A. .
FUEL PROCESSING TECHNOLOGY, 2018, 179 :387-398
[2]   Effect of changes in particle size on the hydrodynamics of gas-solid fluidized beds through wall vibration [J].
Alamolhoda, Fatemeh ;
Zarghami, Reza ;
Sotudeh-Gharebagh, Rahmat ;
Mostoufi, Navid .
POWDER TECHNOLOGY, 2017, 307 :129-136
[3]  
Bhaskaran S, 2018, ENERGY ENV SUSTAIN, P425, DOI 10.1007/978-981-10-7335-9_17
[4]   Experimental analysis of bubble size distributions in 2D gas fluidized beds [J].
Busciglio, A. ;
Vella, G. ;
Micale, G. ;
Rizzuti, L. .
CHEMICAL ENGINEERING SCIENCE, 2010, 65 (16) :4782-4791
[5]  
CHEUNG L, 1974, CHEM ENG SCI, V29, P1301
[6]  
Cocco R.A., 2024, Fluidized Bed Scale-up for Sustainability Challenges. 1. Tomorrows Tools
[7]   Evaluation of two sorbents for the sorption-enhanced methanation in a dual fluidized bed system [J].
Coppola, Antonio ;
Massa, Fiorella ;
Salatino, Piero ;
Scala, Fabrizio .
BIOMASS CONVERSION AND BIOREFINERY, 2021, 11 (01) :111-119
[8]   Application of imaging techniques for the characterization of lumps behaviour in gas-solid fluidized-bed reactors [J].
Errigo, Matteo ;
Sebastiani, Alex ;
Iannello, Stefano ;
Materazzi, Massimiliano ;
Lettieri, Paola .
FUEL, 2023, 349
[9]   Minimum fluidization velocity of binary mixtures of medium particles in the Air Dense medium fluidized bed [J].
Fu, Zhijie ;
Zhu, Jesse ;
Barghi, Shahzad ;
Zhao, Yuemin ;
Luo, Zhenfu ;
Duan, Chenlong .
CHEMICAL ENGINEERING SCIENCE, 2019, 207 :194-201
[10]   CFD modeling the hydrodynamics of binary particle mixture in pseudo-2D bubbling fluidized bed: Effect of model parameters [J].
Geng, Shujun ;
Jia, Zhengrui ;
Zhan, Jinhui ;
Liu, Xiaoxing ;
Xu, Guangwen .
POWDER TECHNOLOGY, 2016, 302 :384-395