Solid Sorbents Used in Extractive Bioconversion Processes

2021 ◽  
pp. 189-205
Author(s):  
Olle Holst ◽  
Bo Mattiasson
2018 ◽  
Author(s):  
S. Pevida ◽  
Gudiyor Veerabhadrappa Manohara ◽  
M. Mercedes Maroto-Valer ◽  
Susana Garcia

2019 ◽  
Author(s):  
Hidetaka Yamada ◽  
Shin Yamamoto ◽  
Junpei Fujiki ◽  
Firoz Chowdhury ◽  
Nobuyuki Takayama ◽  
...  
Keyword(s):  

2020 ◽  
Vol 103 ◽  
pp. 103192
Author(s):  
Young Cheol Park ◽  
Sung-Ho Jo ◽  
Jae-Young Kim ◽  
Yooseob Won ◽  
Hyungseok Nam ◽  
...  

Author(s):  
W. Hartmeier ◽  
C. Bücker ◽  
J. Wallrath ◽  
T. Hembach ◽  
T. Döppner

2014 ◽  
Vol 12 (1) ◽  
pp. 441-449 ◽  
Author(s):  
Zhonglin Zhang ◽  
Daoyin Liu ◽  
Yaming Zhuang ◽  
Qingmin Meng ◽  
Xiaoping Chen

Abstract This paper describes a CFD-DEM modeling of CO2 capture using K2CO3 solid sorbents in a bubbling fluidized bed, which takes into heat transfer, hydrodynamics, and chemical reactions. Shrinking core model is applied in reaction kinetics. Simulation and experiment results of bed pressure drop and CO2 concentration in the reactor exit agree well. Instantaneous dynamics as well as time-averaged profiles indicate detailed characteristics of gas flow, particle motion, and chemical reaction processes. The simulation results show an obvious core-annular flow and strong back-mixing flow pattern. CO2 concentration decreases gradually along the bed height, while regards on the lateral distribution CO2 concentration near the wall is lower than that in the middle zone where gas passes through faster. The effect of bubbles on CO2 reaction is two-sided: it can promote mixing which strengthens reaction, while it can be a short pass of gas which is not beneficial to reaction. The simulation is helpful for further understanding and optimal design of fluidized bed reactors of CO2 capture.


2013 ◽  
Vol 37 ◽  
pp. 73-88 ◽  
Author(s):  
Holly Krutka ◽  
Sharon Sjostrom ◽  
Travis Starns ◽  
Martin Dillon ◽  
Roy Silverman
Keyword(s):  

2015 ◽  
Vol 13 (2) ◽  
pp. 143-152 ◽  
Author(s):  
K. Gallucci ◽  
F. Micheli ◽  
D. Barisano ◽  
A. Villone ◽  
P.U. Foscolo ◽  
...  

Abstract The aim of this work is to identify solid sorbents for CO2 capture for coal and biomass syngas conditioning and cleaning by means of a sorption-enhanced reaction process. Hydrotalcite-like compounds (HTlcs) were synthesized with and without K2CO3 impregnation. Samples were characterized by scanning electron microscopy with energy dispersive X-ray spectroscopy (SEM-EDX), X-ray diffraction (XRD), Brunauer–Emmett–Teller (BET) and Barrett–Joyner–Halenda (BJH) porosimetry after synthesis and after capture tests, respectively. Sorption and desorption tests were performed in a fluidized bed reactor, under cyclic conditions, at two different temperature levels: 350/450°C and 600/700°C. At low temperature only the Mg–Al HTlcs K promoted samples showed stability and sorption capacity comparable with literature values. On the other hand, results at high temperature indicate that the mixed Mg-Ca-Al HTlcs samples exhibit the best behavior with the highest sorption capacity (1.7 mmolCO2/g) almost stable over 5 sorption/regeneration cycles; furthermore, addition of steam allowed increasing their reactivity by 70% compared to the dry value. This type of sorbent could be a promising candidate to prepare a bifunctional sorbent–catalyst for sorption-enhanced processes, taking place directly in the fluidized bed gasifier, or downstream the reactor for adjustment of gas composition before further conversion in gaseous energy carriers.


Langmuir ◽  
2014 ◽  
Vol 30 (25) ◽  
pp. 7405-7413 ◽  
Author(s):  
Uma Tumuluri ◽  
Mathew Isenberg ◽  
Chung-Sung Tan ◽  
Steven S. C. Chuang

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