2019
DOI: 10.11648/j.ijec.20190301.15
|View full text |Cite
|
Sign up to set email alerts
|

Synergistic Study of Hydroxyiron (III) and Kaolinite Composite for the Adsorptive Removal of Phenol and Cadmium

Abstract: This research used raw kaolinite (RK), thermally activated Kaolinite (TAK), hydroxyiron (iii) kaolinitecomposite (HKC), as adsorbent for the adsorption of phenol and cadmium from aqueous solutions over a concentration range of 5-25 mg/l and 10-50 mg/l respectively. Effect of initial pH on the adsorbates was carried out at pH 2-11 at (298 K), and adsorbent dosage from 0.5-2.5 g with 50 ml adsorbate solution. Adsorption thermodynamics were developed for 25-55°C for 5-25 mg/L and 10-50 mg/L of phenol and cadmium … Show more

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

0
1
0

Year Published

2021
2021
2024
2024

Publication Types

Select...
6

Relationship

0
6

Authors

Journals

citations
Cited by 6 publications
(6 citation statements)
references
References 14 publications
(15 reference statements)
0
1
0
Order By: Relevance
“…Co = initial concentration of ammonium, Ce = equilibrium concentration of ammonium, M = mass of adsorbent (ball clay), V = solution volume, and Re = adsorptive removal efficiency (Seliem et al, 2023). To evaluate the adsorption kinetics of ammonium, the pseudo-first order kinetic model and pseudo-secondorder kinetic model were employed, as shown in equations 3 and 4 where K 1 and K 2 are constants of the equilibrium rate (Ngouateu et al, 2015;Egah et al, 2019).…”
Section: Data Analysesmentioning
confidence: 99%
See 1 more Smart Citation
“…Co = initial concentration of ammonium, Ce = equilibrium concentration of ammonium, M = mass of adsorbent (ball clay), V = solution volume, and Re = adsorptive removal efficiency (Seliem et al, 2023). To evaluate the adsorption kinetics of ammonium, the pseudo-first order kinetic model and pseudo-secondorder kinetic model were employed, as shown in equations 3 and 4 where K 1 and K 2 are constants of the equilibrium rate (Ngouateu et al, 2015;Egah et al, 2019).…”
Section: Data Analysesmentioning
confidence: 99%
“…To further analyze the adsorption mechanism, the Langmuir and Freundlich isotherm models were adopted (Egah et al, 2019).…”
Section: 𝑡 𝑞 𝑡mentioning
confidence: 99%
“…To evaluate the adsorption kinetics of ammonium, the pseudo-first order kinetic model and pseudo-second-order kinetic model were employed as shown in equations 8 and 9 where K 1 and K 2 are constants of the equilibrium rate [14].…”
Section: Data Analysesmentioning
confidence: 99%
“…To further analyze the adsorption mechanism, the Langmuir and Freundlich isotherm models were adopted [14].…”
Section: Data Analysesmentioning
confidence: 99%
“…The amount of tailings produced ranged from 90-98 % for copper ores and 20-50 % for other minerals [3]. Some of the heavy metals found in contaminated tailings are Pb, Cr, As, Zn, Cd, Cu, Ni and Hg [4,5,6]. Heavy metal contamination and their human health threats are some of the serious environmental problems limiting mining activities [7,8].…”
Section: Introductionmentioning
confidence: 99%