Numerical Investigation of liquefaction in earth dams: A Comparison of Darcy and Non-Darcy flow models

2019 ◽  
Vol 116 ◽  
pp. 103182 ◽  
Author(s):  
Farideh Hosseinejad ◽  
Farhoud Kalateh ◽  
Alireza Mojtahedi
2016 ◽  
Vol 34 ◽  
pp. 124-138 ◽  
Author(s):  
Gang Huang ◽  
Hongqing Song ◽  
Yang Cao ◽  
Jiaosheng Yang ◽  
Yuhe Wang ◽  
...  

2018 ◽  
Vol 22 (5) ◽  
pp. 1987-1998 ◽  
Author(s):  
Jingyu Wang ◽  
Jian Yang ◽  
Long Li ◽  
Pei Qian ◽  
Qiuwang Wang

Packing configuration is widely used in chemical industries such as chemical re-action and chromatograph where the flow distribution has a significant effect on the performance of heat and mass transfer. In the present paper, numerical simulation is carried out to investigate the fluid-flow in three 2-D array configurations including in-line array, staggered array and hexagonal array. Meanwhile, a simplified equivalent circuit network model based on the Voronoi tessellation is proposed to simulate the flow models. It is found that firstly, the local Reynolds number could be used as a criterion to determine the flow regime. Flow with maximum local Reynolds number less than 40 could be regarded as Darcy flow. Secondly, the flow pattern can be well represented by the network model in the range of Darcy flow with the determination method of hydraulic resistance pro-posed in the present paper.


2019 ◽  
Vol 5 (4) ◽  
pp. 1231-1238 ◽  
Author(s):  
Leila Shakarami ◽  
Hamed Javdanian ◽  
Hamed Reza Zarif Sanayei ◽  
Gholamreza Shams

REAKTOR ◽  
2017 ◽  
Vol 6 (2) ◽  
pp. 77
Author(s):  
N. Aryanti ◽  
Y. Bindar ◽  
I. G. Wenten

Membrane contactor is separation processing unit using membrane as a contacting device. The major advantage of membrane contactor relies on its high contact area compared to conventional scrubber. One of the important applications of membrane contactor is to reduce emission of acid gases. In this work, modeling of membrane contactor is conductedto describe concentration distribution along fiber length used to predict effective fiber length by solving mass conservation equation. Solving of mass conservation equation required information of fluid flow  distribution obtained by solving continuity and momentum equation simultaneously. The finite volume method is used to obtain the solution. Modeling of fluid flow was carried out by adding Darcy`s and Brinkman-Darcy flow models into Navier-Stokes equation. The momentum and continuity equation  are solved for two-dimentional cylindrical coordinate. The result of velocity profile at axial direction were validated with Pangrle et.al. (1992) experimental data. The comparison shows that consideration using Brinkman-Darcy flow model give agood agreement with experimental data in which maximal axial velocity achieved is 0,047 m/s for this model and 0,05 m/s for experimental data.the concentration profile at radial direction using Darcy and Brickman-Darcy flow models have also been investigated. Furthermore, concentration profile at axial direction using the both two flow models indicate a decrease of concentration along fiber length. The comparison between models and experimental data by Subhakti and Azmier (1997) agree very closely to the Brinkman- Darcy flow model. The prediction of effective  fiber length was conducted based on minimum economical flux oe\f membrane contactor. The calculation gives the effective fiber length obtained is 0.19 m at gas concentration, gas flow rate, and sorbent concentration of 0.02 mol/L, 0.8 m/s and 0.256 M respectively.Keywords : modeling, membrane contactor, Darcy, Brinkman-Darcy


2020 ◽  
Vol 141 ◽  
pp. 110335
Author(s):  
Qing Wei ◽  
Hongwei Zhou ◽  
Shuai Yang
Keyword(s):  

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