scholarly journals Packed Bed Column Adsorption of Phenol Onto Corn Cob Activated Carbon: Linear and Nonlinear Kinetics Modeling

Abstract The authors have requested that this preprint be withdrawn due to author disagreement.

2021 ◽  
Vol 36 ◽  
pp. 80-93
Author(s):  
Ositadinma Chamberlain Iheanacho ◽  
Joseph Tagbo Nwabanne ◽  
Christopher Chiedozie Obi ◽  
Chijioke Elijah Onu

2020 ◽  
Author(s):  
Christopher Chiedozie Obi ◽  
Chamberlain Ositadinma Iheanacho ◽  
Joseph Tagbo Nwabanne ◽  
Chijioke Elijah Onu

Abstract In the present study, linear and nonlinear regression analysis for packed bed column adsorption of phenol onto corn cob activated carbon was investigated. The activation of the corn cob provided the activated carbon with enhanced surface area and micropore volume of 903.7m2/g and 0.389 cm3/g respectively. The analysis of the physical properties of the corn cob activated carbon (CCAC) revealed that it contained 33.47% of fixed carbon. SEM images indicated the presence of interspatial pores within the matrix of the adsorbent, while the FTIR analysis revealed that the major functional groups in CCAC were alkanol, alkanes, alkyls, carboxylic acids, ethers, esters, and nitro compounds. The effect of the process parameters influencing the dynamic adsorption process was investigated at flow rates (9 – 18mg/min), initial phenol concentration (100-300mg/l), bed height (5 – 10cm), and particle size (300-800µm). Breakthrough time and adsorption capacity increased with an increase in bed height but decreased with an increase in flow rate, initial phenol concentration, and particle size. At 9mg/min flow rate, 100mg/l initial phenol concentration, 10 cm bed height, and 300µm, the breakthrough and saturation points adsorption capacities were 2.143 and 8.570 mg/g respectively, the volume of effluent treated at saturation point was 12.96L, the length of mass transfer zone (MTZ) was 7.50cm, while 66.13% phenol removal efficiency was achieved. The linear and nonlinear regression analysis of the dynamic column adsorption models viz. Thomas, Adam Bohart, and Wolborska fitted better with the experimental data as compared to Yoon–Nelson. Generally, the nonlinear regression analysis proved to be a better tool for dynamic adsorption model analysis because the model parameters it predicted are in higher proximity to the experimental data when compared to those obtained via linear regression analysis. Conclusively, this study has shown that CCAC can successfully be used for the removal of phenol from aqueous solutions. It also provided experimental evidence that for a more accurate analysis of dynamic adsorption models nonlinear regression tool should be considered.


Adsorption ◽  
2006 ◽  
Vol 12 (3) ◽  
pp. 205-212 ◽  
Author(s):  
Fengsong Wang ◽  
Jun Li ◽  
Jiarong Wang ◽  
Haoqi Gao

2014 ◽  
Vol 14 (23) ◽  
pp. 3294-3299
Author(s):  
S.M. Anisuzzama ◽  
D. Krishnaiah ◽  
C.G. Joseph ◽  
S. Abang ◽  
W.K. Tai

2018 ◽  
Vol 117 ◽  
pp. 350-362 ◽  
Author(s):  
Radhika R. ◽  
Jayalatha T. ◽  
Rekha Krishnan G. ◽  
Salu Jacob ◽  
Rajeev R. ◽  
...  

2015 ◽  
Vol 2015 ◽  
pp. 1-9 ◽  
Author(s):  
Prapaporn Luekittisup ◽  
Visanu Tanboonchauy ◽  
Jitlada Chumee ◽  
Somrudee Predapitakkun ◽  
Rattanawan W. Kiatkomol ◽  
...  

Activated carbon (GAC) was impregnated by sodium and used as adsorbent to remove chlorinated hydrocarbon (CHC) gases contaminated in H2feedstock. The adsorption was carried out in a continuous packed-bed column under the weight hourly space velocity range of 0.8–1.0 hr−1. The adsorption capacity was evaluated via the breakthrough curves. This modified GAC potentially adsorbed HCl and VCM of 0.0681 gHCl/gadsorbentand 0.0026 gVCM/gadsorbent, respectively. It showed higher adsorption capacity than SiO2and Al2O3balls for both organic and inorganic CHCs removal. In addition, the kinetic adsorption of chlorinated hydrocarbons on modified GAC fit well with Yoon-Nelson model.


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