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Presentation for Conference (Kochi, India)
1. Preeti Pal
Indian Institute of Technology,
Kharagpur, India, 721302.
SURFACTANT-MODIFIED CHITOSAN
BEADS FOR CADMIUM
ADSORPTION
1
IIT Kharagpur
11th Asia Pacific Chitin and Chitosan Symposium &
5th Indian Chitin and Chitosan Society Symposium
28-30th September, 2016
2. 2
Chitosan beads (CS beads) preparation
Preparation of surfactant modified beads
(SMCS beads)
Cadmium removal by the CS and SMCS beads
Kinetic study
Characterization of beads
Equilibrium study
pH study
Effect of dose
SEM (Scanning electron microscopy)
FTIR (Fourier transform infrared
spectroscopy)
XRD (X-ray powder diffraction)
3. 3
•Highly toxic and carcinogenic
•Non degradable
•Persistent metal
•Specific density> 5gm/cm3
•PVC products
•Color pigments
•Alloys
•Ni-Cd batteries
•Anticorrosion
agent
•Liver
•Kidney
•Respiratory
system
•Skeletal system
4000-13000
tons/year
agricultural field
and natural water
bodies
Cadmium
Health
effectsUses
Properties
•Half-life:38 years
•Limit :0.003 mg/L (WHO)
•LOD :0.01 mg/L by
ICP/MS;2 mg/L by AAS
(Ades and Kazantzis
1988; Elinder et al. 1985;
Pesch et al. 2000;
WHO, 2008; USEPA, 1999)
Guidelines
5. •Chitosan was discovered in 1859
by Prof C. Rouget.
• In 1930s and 1940s, 50 patents
filed on application of chitosan.
•Today there are more than 2000
applications.
Special characteristics
•Hydrophilicity
•Biocompatibility
•Biodegradability
•Nontoxicity
•Adsorption properties
•Poly-functionality
Structural properties
• A linear polysaccharide
composed of randomly
distributed β-linked D-
glucosamine and N-acetyl-
D-glucosamine
•Presence of –OH and
–NH2 groups make it
feasible modifications.
• Chitosan is second abundant
biopolymer after cellulose.
• Prepared from chitin
deacetylation
•Obtained by treating outer
skeleton of marine waste with
the sodium hydroxide.
Chitosan
5
11. 11
10 20 30 40 50 60 70
Iobs(Counts)
2 Theta (Degree)
CdL-SMCS beads
SMCS beads
SDS
CS
Fig. 4. XRD images of (a) CS powder,
(b) SDS powder, (c) SMCS beads, (d)
CdL-SMCS beads.
XRD
At 2Ɵ18.36o and 22o SDS
and at 20o chitosan showed
high intensity peak due to the
crystalline structure
The intensity of the MMCS
composite has been decreased
due to the disruption of
hydrogen bonds
Decrease in crystallinity
results in improvement of
metal adsorption capacity
(a)
(b)
(c)
(d)
(Wang et al., 2014)
13. 13
0
10
20
30
40
50
60
70
80
90
100
5 30 60 120 240 480 720 1440 2160 2880
%Removal
Time (min)
0
20
40
60
80
100
120
140
5 30 60 120 240 480 720 1440 2160 2880
Capacity(mg/g)
Time (min)
10 mg/L 20 mg/L 30 mg/L 40 mg/L 50 mg/L 100 mg/L
Fig. 6. Effect of contact
time on the % removal and
capacity of Cd by SMCS
beads. Dose (0.45 g/L).
Optimum time: 10 hrs.
[Cd] % R
10
>90
20
30
~80
40
50
>50
100
14. 14
Cd
Concentration
(mg/L)
Pseudo First Order Pseudo Second Order
qt (mg g−1) k1 (min−1) R2 qt(mg g−1) k2 (g mg−1
min−1)
R2
10 14.01 0.0023 0.948 22.73 4 x10-4 0.997
20 27.183 0.0019 0.966 45.45 2.12 x10-3 0.995
30 44.625 0.0017 0.982 66.66 1.2 x10-4 0.993
40 46.279 0.0021 0.928 83.33 1.34 x10-4 0.997
50 56.042 0.0016 0.982 100.00 8.07x10-5 0.991
100 52.56 0.0069 0.865 125.00 2.82 x10-4 0.997
Table 3. Parameters of the kinetics study of Cd adsorption onto the SMCS beads.
0
20
40
60
80
100
120
0 500 1000 1500 2000 2500
t/qt(ming/mg)
Time (min)
10 mg/L 20 mg/L 30 mg/L
40 mg/L 50 mg/L 100 mg/L
Fig. 9. Pseudo-second order
model for Cd adsorption
onto SMCS beads.
•Adsorption follows pseudo
second order model
•Physiosorption
15. 15
0
20
40
60
80
100
120
140
0 300 600 900 1200 1500 1800 2100 2400 2700
qt(mg/g)
Time (min.)
Cal (10 mg/L) Expl (10 mg/L) Cal (20 mg/L) Exp(20 mg/L) Cal (30 mg/L) Exp(30 mg/L)
Cal (40 mg/L) Exp (40 mg/L) Cal (50 mg/L) Exp (50 mg/L) Cal (100 mg/L) Exp (100 mg/L)
Fig. 10. Plot of qt vs. t for experimental data and theoretical data based on the pseudo-second order model.
Theoretical and experimental curve fitting
16. 16
0
20
40
60
80
100
120
0.09 0.225 0.36 0.45 0.675 0.9 1.125 1.35
%Removal
Dose (g/L)
10 mg/L
40 mg/L
100 mg/L
0
10
20
30
40
50
60
70
80
90
100
4 5 6 7 8
%Removal
pH
% R
Fig.7. Effect of dose on the %
removal of Cd by SMCS beads
(contact time: 10 hours).
Fig.8. Effect of pH on Cd removal
with 30 mg/L Cd conc., dose:0.45
g/L, time: 10 h.
Optimum dose- 0.45 g/L
Optimum pH- 7
(For standard deviation calculation ;n= 3)
100 mg/L>50 % removal
10-40 mg/L >80 % removal
30 mg/L ~90 % removal
ADSORBENT DOSE AND pH STUDY
17. 17
Isotherm Models R2 Linear Equation Equation
Langmuir qm (mg/g) 125 0.996 Ce/qe = 1/(qm.KL) + (1/qm).Ce y = 0.008x + 0.013
KL (L/mg) 0.615
Freundlich KF(mg/g)(L/mg)1/n 46.94 0.855 ln qe = ln KF + (1/n) ln Ce y = 0.2829x + 3.8496
1/n 0.282
0
1
2
3
4
5
6
-2 0 2 4 6
ln(qe)
ln (Ce)
(b)
Fig. 11. (a) Langmuir, (b) Freundlich adsorption isotherm on removal of Cd2+ using SMCS
beads.
Table 4. Values of isotherm constants for Langmuir and Freundlich isotherms and their corresponding R2
values.
0.00
0.05
0.10
0.15
0.20
0.25
0.30
0.35
0.40
0.45
0 20 40 60
Ce/qe
Ce
(a)
18. 18
Adsorbent Capacity
(mg/g)
Dose
(g/L)
Isotherm Reference
Cross-linked chitosan–zeolite
composite
102.15 1.0 L (Zhang et al., 2014)
Raw chitosan >100 4.0 F (Bamgbose et al., 2010)
Chitosan pyruvic acid derivative 98.04 2 L (Boamah et al., 2015)
Chitin 14 6 L (Benguella and Benaissa, 2002)
Banana peels 0.25 10 L (Mohd Said et al., 2015)
Agbani Clay 1.427 100 F (Dawodu et al., 2012)
TiO2 Nanoparticles 29.28 2.5 L (Sharaf El-Deen and Zhang, 2016)
Surface oxidized CNT 11.0 0.5 L (Li et al., 2003)
SMCS beads 125 0.45 L Present work
Table 5. Comparison of the maximum adsorption capacities (qmax) of SMCS beads with other reported
adsorbents for Cd2+ removal.
19. 19
Chitosan beads successfully modified with the anionic surfactant
SDS.
The kinetics of the Cd2+ removal on SMCS beads indicates that the
adsorption is physiosorption.
Equilibrium data fitted well with Langmuir isotherm.
Maximum adsorption capacity obtained was 125 mg/g .
Time taken to attain equilibrium was 10 h with optimum dose of
0.45 g/L.
SMCS beads are economically cheap and environmental friendly
adsorbent.
20. 20
The authors are thankful to IIT Kharagpur for providing the instrumental
facility and financial support.
21. 21
Ades A. E, Kazantzis G, 1988, “Lung cancer in a non-ferrous smelter: the role of cadmium.”British
Journal of Industrial Medicine, 45:435-42.
Boamah P. O., Huang Y., Hua M., Zhang Q., Liu Y., Onumah J., Wang W., Song Y. 2015. “Removal
of Cadmium from Aqueous Solution Using Low Molecular Weight Chitosan Derivative.”
Carbohydrate polymers 122:255–64.
Bamgbose J. T., Adewuyi S., Bamgbose O., and Adetoye A. A. 2010. “Adsorption Kinetics of
Cadmium and Lead by Chitosan.” Journal of Biotechnology 9:2560–65.
Benguella B., Benaissa H., 2002. “Cadmium removal from aqueous solutions by chitin: Kinetic and
equilibrium studies.” Water Research. 36:2463–74.
Das D., Pal A., 2016. “Adsolubilization phenomenon perceived in chitosan beads leading to a fast
and enhanced malachite green removal.” Chemical Engineering Journal 290: 371–380.
Dawodu F. A., Akpomie G. K., Ogbu I. C., 2012. “Isotherm Modeling on the Equilibrium Sorption
of Cadmium ( II ) from Solution by Agbani Clay.” International journal of multidisciplinary
Science and engineering 3:9–14.
Elinder C. G, Kjellström T, Hogstedt C, Andersson K, Spång G. 1985. “Cancer mortality of
cadmium workers.” British Journal of Industrial Medicine 42:651-65.
Mohd Said M. I., Sabri S., Azman S., 2015. “Effect of particle size on cadmium removal by banana
peels.” Journal Teknologi 72, 99–101.
Kumar Ravi M. N. V. 2000. “A Review of Chitin and Chitosan Applications.” Reactive and
Functional Polymers 46:1–27.
22. 22
Li Y. H., Wang S., Luan Z., Ding J., Xu C., Wu D., 2003. “Adsorption of cadmium (II) from
aqueous solution by surface oxidized carbon nanotubes.” Carbon 41:1057–1062.
Pesch B, Haerting J, Ranft U, Klimpel A, Oelschlägel B, Schill W. 2000. “Occupational risk
factors for renal cell carcinoma: agent-specific results from a case-control study in Germany.
MURC Study Group. Multicenter urothelial and renal cancer study.” International Journal of
Epidemiology 29:1014-24.
Rathi A. K. A. 2002. “Chemical Industry Wastewater Treatment Using Adsorption.” Industrial
Research 61:53–60.
Sharaf El-Deen S. E. A., Zhang F. S., 2016. “Immobilisation of TiO2 - nanoparticles on sewage
sludge and their adsorption for cadmium removal from aqueous solutions.” Journal of
Experimental Nanoscience 11:239–258.
Viana R. B., da Silva A. B. F., Pimentel A. S. 2012. "Adsorption of sodium dodecyl sulfate on Ge
substrate: The effect of a Low-Polarity solvent." International Journal of Molecular Sciences
13: 7980–7993.
World Health Organization. 2008. “Guidelines for drinking-water quality.” World Health
Organization, Geneva, Vol I, Third edition.
Wang W., Lu H., Liu Y., Leng J. 2014. "Sodium dodecyl sulfate/epoxy composite: water-induced
shape memory effect and its mechanism." Journal of Materials Chemistry A 2: 5441-49.