2011
DOI: 10.2478/v10176-011-0029-z
|View full text |Cite
|
Sign up to set email alerts
|

Modelling of NO adsorption in fixed bed on activated carbon

Abstract: Adsorption experiments of nitric oxide in nitrogen carrier gas were held on activated carbon in a fixed bed flow system. Breakthrough curves describing the dependence of exit concentrations of nitric oxide on time were matched with theoretical response curves calculated from the linear driving force model (LDF). The model assumes Langmuir adsorption isotherm for the description of non-linear equilibrium and overall mass transfer coefficient for mass transfer mechanism. Overall mass transfer coefficients were o… Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
5
0

Year Published

2015
2015
2022
2022

Publication Types

Select...
7
1

Relationship

0
8

Authors

Journals

citations
Cited by 10 publications
(6 citation statements)
references
References 15 publications
1
5
0
Order By: Relevance
“…It also notices that the adsorption process occurs in the beginning quickly and be a decline in the curves and clear because of the abundance of the active sites and the presence of small surface resistance on the surface of adsorbents, then more smoothness gradually less steep and alignment over time because of the fullness of all the active sites on the surface of adsorbents and that the process has become controlled by internal diffusion within the adsorbents in accordance with what has been presented previously [39]. Also the results of comparison for both that the amount of the CO 2 adsorbed onto AC increases due to increase of the concentration difference of CO 2 between bulk and surface of AC leading to an increase of mass transfer [9,40].…”
Section: Dynamic Studiessupporting
confidence: 86%
See 1 more Smart Citation
“…It also notices that the adsorption process occurs in the beginning quickly and be a decline in the curves and clear because of the abundance of the active sites and the presence of small surface resistance on the surface of adsorbents, then more smoothness gradually less steep and alignment over time because of the fullness of all the active sites on the surface of adsorbents and that the process has become controlled by internal diffusion within the adsorbents in accordance with what has been presented previously [39]. Also the results of comparison for both that the amount of the CO 2 adsorbed onto AC increases due to increase of the concentration difference of CO 2 between bulk and surface of AC leading to an increase of mass transfer [9,40].…”
Section: Dynamic Studiessupporting
confidence: 86%
“…The total pore volume and surface area of AC were determined using Gemini VII 2390a analyzer. The particle size is obtained by using standard mesh sieves (standard sieve AS 200), and average value of bed porosity is calculated in terms of the average diameter of particles [9].…”
Section: Preparation Of Activated Carbonmentioning
confidence: 99%
“…The adsorption capacity increased as the increased CO 2 concentration, which was attributed to the high driving force of the CO 2 concentration between the bulk phase and the surface of AC that can promote a high mass transfer rate 73 , 74 . For all the explored ACs, the Freundlich model provided a better fit with the experimental results over the entire range of CO 2 concentrations than the Langmuir model, considered in terms of the higher R 2 and S values.…”
Section: Resultsmentioning
confidence: 99%
“…This is probably because a high concentration of (Au 2 S 2 O 3 )(SO 3 ) 2 5− in the bulk liquid can initiate a high concentration gradient between the bulk phase and the surface of TiO 2 , resulting in an increased mass transfer as well as an increased adsorption capacity. 30,31 In the presence of light, increasing the concentration of mixed complexing agents slightly decreased the photocatalytic efficiency for Au recovery compared with that in the absence of complexing agents, probably attributed to the shielding behavior of densely surrounded species in the presence of a high concentration of complexing agents. Based on the obtained results, among all employed commercial semiconductors, TiO 2 exhibited the highest photocatalytic recovery of Au from the simulated spent non-cyanide plating bath both in the absence and presence of complexing agents at all explored concentrations.…”
Section: Resultsmentioning
confidence: 99%