2018
DOI: 10.1039/c8nj03007c
|View full text |Cite
|
Sign up to set email alerts
|

Relationship of cellulose and lignin contents in biomass to the structure and RB-19 adsorption behavior of activated carbon

Abstract: Activated carbon microspheres prepared from biomass resources serve as green, highly efficient, and reusable adsorbents for reactive blue 19.

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
2
1
1
1

Citation Types

1
12
0

Year Published

2018
2018
2024
2024

Publication Types

Select...
8
1

Relationship

2
7

Authors

Journals

citations
Cited by 40 publications
(13 citation statements)
references
References 31 publications
1
12
0
Order By: Relevance
“…The adsorption behaviors of atrazine with/without BPA onto WAC, WSAC, and ASAC were similar. The adsorption rates of atrazine with/without BPA onto WAC, WSAC, and ASAC were the fastest at first 1 h, after that the rates slowed down, which was because the concentration of atrazine and the active sites of the adsorbent sample reduced as the reaction going on [22]. The adsorption progress reached the equilibrium during 5 h (Figure 2).…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…The adsorption behaviors of atrazine with/without BPA onto WAC, WSAC, and ASAC were similar. The adsorption rates of atrazine with/without BPA onto WAC, WSAC, and ASAC were the fastest at first 1 h, after that the rates slowed down, which was because the concentration of atrazine and the active sites of the adsorbent sample reduced as the reaction going on [22]. The adsorption progress reached the equilibrium during 5 h (Figure 2).…”
Section: Resultsmentioning
confidence: 99%
“…The experimental data were fitted with Langmuir (Equation (6)), Freundlich (Equation (7)), Temkin (Equation (8)), and Dubinin–Radushkevich (D–R) (Equation (9)) isotherm models [22]. The residual root-mean squared error (RMSE) [19] function values can be analyzed using the Equation (10): q e = q m K L C e /(1 + K L C e ), q e = K F C e 1/ n , q e = B ln ( ACe ), Lnq e = lnq m − K d ln ( 1 + 1 / Ce ), RMSE = [∑( q e exp n − q e cal n ) 2 /(n − 1)] 1/2 , R L = 1/(1 + C m K L ) , where q m (mg/g) is the maximum adsorption capacity; q e (mg/g) is the adsorption amount of the adsorbate onto the adsorbents at the equilibrium time; K L (L/mg) and K F (L/mg) are the Langmuir and Freundlich constants, respectively; n is the empirical parameter; b (J/mol), A (L/mg), R (8.314 J/(mol∙K)), and T (K) are the Temkin constants related to the thermal constant of adsorption, equilibrium binding constant, gas constant, and absolute temperature, respectively; K d = R 2 T 2 / E 2 ; E (J/mol) is the constant related to free energy; and R L is the dimensionless separation factor.…”
Section: Methodsmentioning
confidence: 99%
“…Adsorption and activated carbon based technologies have also been widely used for several environmental applications [19][20][21][22][23][24]. To that end, the conversion of agricultural wastes into granular activated carbon (GAC) and its use for pollution control applications, has also attracted much attention, considering its multi-faceted and inherent economical, and environmental advantages.…”
Section: Introductionmentioning
confidence: 99%
“…However, after carbonisation, this content may increase above 80% or even 95% for ACs, which is interesting since it can lead to an elevated and developed porosity [ 37 ]. The high cellulose content also plays a crucial role in developing mesopore structure in ACs while lignin, for example, can promote the formation of layered structure and maximisation of micropores during the preparation of AC [ 38 ].…”
Section: Biomass Carbon Sources and Composition As Raw Materials Fomentioning
confidence: 99%