Investigation into the elutriation of fines from binary mixtures via CFD simulation with a multi-scale drag model

2018 ◽  
Vol 339 ◽  
pp. 633-640 ◽  
Author(s):  
Shuai Wang ◽  
Bang Hu ◽  
Siyu Liu ◽  
Weijie Yin ◽  
Kai Zhang
2007 ◽  
Vol 62 (18-20) ◽  
pp. 5487-5494 ◽  
Author(s):  
Bona Lu ◽  
Wei Wang ◽  
Jinghai Li ◽  
Xianghui Wang ◽  
Shiqiu Gao ◽  
...  

Energies ◽  
2019 ◽  
Vol 12 (15) ◽  
pp. 2965 ◽  
Author(s):  
Augusto Della Torre ◽  
Gianluca Montenegro ◽  
Angelo Onorati ◽  
Sumit Khadilkar ◽  
Roberto Icarelli

Plate heat exchangers including offset-strip fins or dimple-type turbulators have a wide application in the automotive field as oil coolers for internal combustion engines and transmissions. Their optimization is a complex task since it requires targeting different objectives: High compactness, low pressure drop and high heat-transfer efficiency. In this context, the availability of accurate Computational Fluid Dynamics (CFD) simulation models plays an important role during the design phase. In this work, the development of a computational framework for the CFD simulation of compact oil-to-liquid heat exchangers, including offset-strip fins and dimples, is presented. The paper addresses the modeling problem at different scales, ranging from the characteristic size of the turbulator geometry (typically µm–mm) to the full scale of the overall device (typically cm–dm). The simulation framework is based on multi-scale concept, which applies: (a) Detailed simulations for the characterization of the micro-scale properties of the turbulator, (b) an upscaling approach to derive suitable macro-scale models for the turbulators and (c) full-scale simulations of the entire cooler, including the porous models derived for the smaller scales. The model is validated comparing with experimental data under different operating conditions. Then, it is adopted to investigate the details of the fluid dynamics and heat-transfer process, providing guidelines for the optimization of the device.


2015 ◽  
Vol 138 (3) ◽  
Author(s):  
Bahareh Estejab ◽  
Francine Battaglia

In order to accurately predict the hydrodynamic behavior of gas and solid phases using an Eulerian–Eulerian approach, it is crucial to use appropriate drag models to capture the correct physics. In this study, the performance of seven drag models for fluidization of Geldart A particles of coal, poplar wood, and their mixtures was assessed. In spite of the previous findings that bode badly for using predominately Geldart B drag models for fine particles, the results of our study revealed that if static regions of mass in the fluidized beds are considered, these drag models work well with Geldart A particles. It was found that drag models derived from empirical relationships adopt better with Geldart A particles compared to drag models that were numerically developed. Overall, the Huilin–Gidaspow drag model showed the best performance for both single solid phases and binary mixtures, however, for binary mixtures, Wen–Yu model predictions were also accurate.


2014 ◽  
Vol 28 (10) ◽  
pp. 6351-6360 ◽  
Author(s):  
Juhui Chen ◽  
Guangbin Yu ◽  
Bing Dai ◽  
Di Liu ◽  
Lei Zhao

Author(s):  
Wei Wang ◽  
Wei Ge ◽  
Ning Yang ◽  
Jinghai Li

2015 ◽  
Vol 5 (4) ◽  
pp. 255-261 ◽  
Author(s):  
Jin H. Zhang ◽  
Zhen B. Wang ◽  
Hui Zhao ◽  
Yuan Y. Tian ◽  
Hong H. Shan ◽  
...  

2008 ◽  
Vol 86 (3) ◽  
pp. 448-457 ◽  
Author(s):  
Wei Wang ◽  
Bona Lu ◽  
Weigang Dong ◽  
Jinghai Li
Keyword(s):  

2011 ◽  
Vol 66 (14) ◽  
pp. 3212-3222 ◽  
Author(s):  
Ning Yang ◽  
Zongying Wu ◽  
Jianhua Chen ◽  
Yuhua Wang ◽  
Jinghai Li

Sign in / Sign up

Export Citation Format

Share Document