Numerical modeling and uncertainty quantification of a bubbling fluidized bed with immersed horizontal tubes

2014 ◽  
Vol 253 ◽  
pp. 733-743 ◽  
Author(s):  
William A. Lane ◽  
Curtis B. Storlie ◽  
Christopher J. Montgomery ◽  
Emily M. Ryan
Fuel ◽  
2014 ◽  
Vol 130 ◽  
pp. 197-202 ◽  
Author(s):  
Wang Shuai ◽  
Lu Huang ◽  
Hao Zhenhua ◽  
Lu Huilin ◽  
Liu Guodong ◽  
...  

Author(s):  
Salim A.R.K. Deshmukh ◽  
Sander Volkers ◽  
Martin van Sint Annaland ◽  
Hans Kuipers

The effect of gas permeation through horizontally immersed membrane tubes on the heat transfer characteristics in a membrane assisted fluidized bed operated in the bubbling fluidization regime was investigated experimentally. Local time-averaged heat transfer coefficients from copper tubes arranged in a staggered formation with the membrane tubes to the fluidized bed were measured in a square bed (0.15 m x 0.15 m x 0.95 m). Glass particles (75-110 micrometer) were fluidized with air distributed via a porous plate, where the ratio of gas fed or removed through the membrane bundles and the porous plate distributor was varied. The experimental results revealed that high gas permeation rates through the membranes strongly decreased the heat transfer coefficient at high superficial gas velocities for tubes at the top of the tube bundle, which was attributed to the reduced mobility and increased bubble hold up and/or dilution of the emulsion phase, reducing overall heat capacity.In the design of membrane assisted fluidized beds care must be taken to include the effect of gas addition or withdrawal through the membranes on the required heat transfer surface area.


2006 ◽  
Vol 45 (20) ◽  
pp. 6818-6827 ◽  
Author(s):  
Lu Huilin ◽  
Zhao Yunhua ◽  
Jianmin Ding ◽  
Zeng Linyan ◽  
Liu Yaning

Author(s):  
William A. Lane ◽  
Curtis Storlie ◽  
Christopher Montgomery ◽  
Emily M. Ryan

As the effects of climate change continue to rise with increasing carbon dioxide emission rates, it is imperative that we develop an efficient method for carbon capture. This paper outlines the framework used to break down a large, complex carbon capture system into smaller unit problems for model validation, and uncertainty quantification. We use this framework to investigate the uncertainty and sensitivity of the hydrodynamics of a bubbling fluidized bed. Using the open-source computational fluid dynamics code MFIX we simulate a bubbling fluidized bed with an immersed horizontal tube bank. Mesh resolution and statistical steady state studies are conducted to identify the optimal operating conditions. The preliminary results show good agreement with experimental data from literature. Employing statistical sampling and analysis techniques we designed a set of simulations to quantify the sensitivity of the model to model parameters that are difficult to measure, including: coefficients of restitution, friction angles, packed bed void fraction, and drag models. Initial sensitivity analysis results indicate that no parameters may be omitted. Further uncertainty quantification analysis is underway to investigate and quantify the effects of model parameters on the simulations results.


2021 ◽  
Vol 229 ◽  
pp. 113749
Author(s):  
D.T. Pio ◽  
L.C.M. Ruivo ◽  
L.A.C. Tarelho ◽  
J.R. Frade ◽  
E. Kantarelis ◽  
...  

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