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1 This work is licensed under Creative Commons Attribution 4.0 International License.
ISSN: 2349-8889
Volume-7, Issue-1 (January 2020)
https://doi.org/10.31033/ijrasb.7.1.1
International Journal for Research in
Applied Sciences and Biotechnology
www.ijrasb.com
Examination of Adsorption Abilities of Natural and Acid Activated
Bentonite for Heavy Metals Removal from Aqueous Solutions
Nedim Hodžić1
, Abdel Đozić2
, Indira Šestan3
and Hana Alihodžić4
1
PhD. Candidate, Department of Environmental Engineering, Faculty of Technology, University of Tuzla, BOSNIA AND
HERZEGOVINA
2
Assoc. Prof. Dr., Department of Environmental Engineering, Faculty of Technology, University of Tuzla, BOSNIA AND
HERZEGOVINA
3
Asst. Prof. Dr., Department of Physical chemistry and Electrochemistry, Faculty of Technology, University of Tuzla,
BOSNIA AND HERZEGOVINA
4
Sen. Asst., Department of Environmental research laboratory, Institute for quality, standardization and ecology, BOSNIA
AND HERZEGOVINA
2
Corresponding Author: abdel.dozic@untz.ba
ABSTRACT
The effect of the initial concentration of Cr, Co,
Cu, Ni, and Pb metal ions from multicomponent solutions on
the sorption capacity of natural and acid activated bentonite
was examined in this paper. The acid activation was
performed by using hydrochloric and sulfuric acid at
different concentrations. The results of adsorption research
have shown that bentonite can be effectively used as an
adsorbent for the removal of metal ions from
multicomponent solutions. Acid activation of bentonite
changes the structure and content of individual oxides,
increases the porosity and the number of available spots for
the adsorption process. For this reason, the bentonite
removal efficiency increased after acid activation for all
heavy metals tested. With increased acid concentration, the
degree of bentonite adsorption increased, and sulfuric acid
rather than chloric acid showed better results in removal
efficiency.
Keywords-- Adsorption, Bentonite, Heavy Metals, Acid
Activation
I. INTRODUCTION
Pollution of natural and wastewater is most often
the result of the heavy metals discharge into the
watercourses [1]. Heavy metals can be removed from
aqueous solutions by various methods such as chemical
precipitation, solvent extraction, membrane filtration, ion
exchange, electrochemical removal, coagulation, etc. [2].
However, these techniques have disadvantages such as
incomplete removal, high energy consumption, toxic
sludge generation, low efficiency, sensitive operating
conditions and high waste disposal costs [3,4]. To
overcome such disadvantages, different approaches have
been proposed, aimed at developing more inexpensive
and more efficient methods for improving the quality of
effluents [2]. Most are based on the application of the
adsorption process, because adsorption has the greatest
impact on the transport, toxicity and bioavailability of
heavy metals (especially at low concentrations, in trace
amounts) in aqueous solution, in addition the process is
inexpensive and easy to perform. [5,6].
Considering the fact that bentonite is a natural
material, the mechanical milling method can produce
inexpensive adsorbents, and the activating adsorbents
method is also environmentally friendly.
Aluminum oxides and clay minerals such as
bentonite, kaolin and pyrophyllite are relatively
widespread minerals in the earth’s crust, which are
known to be good adsorbents of various metal ions.
Bentonite belongs to the smectite family and is classified
as a natural clay of layered phyllosilicates composed of
alternating octahedrons and tetrahedrons in a 2:1 ratio.
The structure, chemical composition, exchangeable ionic
type and small size of the crystals contribute to the unique
properties of these clays, including a large chemically
active surface, high cation exchange ability and high
porosity. The degree of adsorption efficiency of heavy
metals depends on a number of factors such as: pH value
influence, temperature influence, adsorbent dose
influence, initial concentration influence, contact time
influence, etc. Bentonite has been shown to be effective
adsorbent for heavy metals removal from waste water.
However, despite the very good adsorption properties
they possess naturally, there is increasing emphasis on the
modification of natural clays in order to improve the
general physicochemical properties. Activation methods
with chemical agents or temperature are most commonly
used to improve these properties. Acidic activation of
clay achieves an increase in specific surface area and
porosity [7]. The alteration degree of the active surface
and the clay structure porosity caused by the action of
acids depends on the type of clay minerals, i.e. chemical
composition of clays, the type of interlayer cations, the
acid applied and its concentration, temperature and time
of action [8]. Acid-activated clays in industry are most
commonly used as adsorbents, bleaches and catalysts [9].
The aims of the paper are as follows:
- To examine the possibility of using natural and
modified bentonite as an inexpensive adsorption material
2 This work is licensed under Creative Commons Attribution 4.0 International License.
ISSN: 2349-8889
Volume-7, Issue-1 (January 2020)
https://doi.org/10.31033/ijrasb.7.1.1
International Journal for Research in
Applied Sciences and Biotechnology
www.ijrasb.com
for the removal of heavy metal ions.
- To examine the adsorption capacity of heavy metals
(Pb, Cr, Cu, Co and Ni) from multi component solutions
using natural and modified bentonite.
- To determine the effect of acid activation (with
hydrochloric and sulfuric acid) on the sorption removal
properties of heavy metals.
II. EXPERIMENTAL PART
The bentonite sorption property for Pb, Cr, Cu,
Co, and Ni ions was examined for its natural and
modified form. The modified form of bentonite was
obtained by acid activation with hydrochloric (HCl, 36%)
and sulfuric acid (H2SO4 96%). Based on the previous
calculation, 0,4; 0,5; 0,6 M HCl and 0,4: 0,5; 0,6 M
H2SO4 were prepared by adding known concentrations of
pure acid into a 500 ml volumetric flask. After the
required acids were prepared, 400 ml of 0.4 M HCl were
weighed using a measuring cylinder and carefully
transferred into a 500 ml laboratory beaker.
The resulting mixture was stirred on a magnetic
stirrer for eight hours at 200 rpm. Upon completion of the
mixing process, the suspension was filtered through fine
filter paper on a pre-set apparatus. During the filtration,
the bentonite on the filter paper was washed with distilled
water until a negative reaction to Cl-ions, which was
checked with silver nitrate (AgNO3 5%).
The bentonite filter paper was dried in a drying
oven at 105 ° C for four hours. The dried bentonite was
then ground in a porcelain mill and sieved through a 75
micrometer sieve. In this way, bentonite was acid
activated with 0.4; 0.5; 0.6 M HCl. The same procedure
was repeated for 0.4; 0.5; 0.6 M H2SO4, except that the
bentonite on the filter paper was washed by distilled
water until negative reaction to SO4
2-
ions, which was
checked by BaSO4 solution.
2.1. Materials
Bentonite from a deposit in Šipovo, Bosnia and
Herzegovina, was used for experimental research.
Experimental research was performed in the accredited
laboratory of the Institute for Quality, Standardization
and Ecology. The laboratory is licensed for wastewater
testing and is accredited to BAS ISO 17025: 2006, which
implies that certified reference materials and chemicals of
proven traceability and purity are used.
Standard solutions of Cr, Co, Cu, Ni and Pb
prepared from certified reference materials in different
concentration ranges were used.
After preparation of all materials, a batch
adsorption process of the tested heavy metals ions from
aqueous solutions was carried out using the following:
1. Natural (crude) bentonite
2. Acid-activated bentonite with 0.4; 0.5; 0.6 M HCl
3. Acid-activated bentonite with 0.4; 0.5; 0.6 M H2SO4
The following standard method was used to
determine the content of Cr, Co, Cu, Ni, Pb heavy metals:
BAS ISO 8288: 2002 Method A Water quality (Flame
atomic absorption spectrometry method). A 240 Series
Agilent Technology atomic absorption spectrophotometer
was used to determine the content of heavy metals. All
experiments were performed at room temperature.
The contact time between the adsorbent and the
multipart solution was 2 hours and did not change during
the analyses.
The X-Ray method was used to determine the
chemical composition of bentonite, and the pH value of
the biosorbent was determined by the zero-charge
method.
III. RESULTS AND DISCUSSION
The obtained chemical analysis values for SiO2,
Al2O3, Fe2O3 (48.28%, 23.04%, 4.52%) show a similar
trend in the results obtained by researchers Abdullahi and
Audu, 2017: who tested two bentonite samples in parallel,
and those were: (48.16% and 49.87% for SiO2, 14.86 and
14.98% for Al2O3 and Fe2O3, respectively: 4.80% and
5.12%).
The results also obtained for SiO2 are similar to
the values reported by other autors (45 wt. %); and (48.35
wt. %) [11,12]. However, when it comes to Fe2O3
content, the results obtained are lower than those (11.10
wt. %) (8.26 wt. %) but higher than (3.82 wt. %)
[11,12,13].
Since these are clays of smectite origin, the
presence of Ca, Mg, Na and K is expected. Considering
that the adsorption of heavy metal ions on clays depends
on a large number of parameters, and that the pH value is
one of the most significant, the optimal pH value at which
the process is guided was determined before following
the sorption processes of heavy metal removal.
The figure 1 presents a review of the change in
pH values, concluding that the zero charge point for
bentonite is 8.27. Above these values the removal of
positively charged ions will be more efficient. Comparing
the results for natural clay 7.8 can be concluded that a
slightly lower value than our [14].
Figure 1: Zero charge point for bentonite
3 This work is licensed under Creative Commons Attribution 4.0 International License.
ISSN: 2349-8889
Volume-7, Issue-1 (January 2020)
https://doi.org/10.31033/ijrasb.7.1.1
International Journal for Research in
Applied Sciences and Biotechnology
www.ijrasb.com
The effect of different metal concentrations in
solution on the removal efficiency was examined, as well
as the different types of acid activation carried out using
HCl and H2SO4 in different concentration ranges.
By varying the concentration of individual ions
from 5 to 30 mg/dm3 in multicomponent solution, the
effect of this parameter on the adsorption of Cr, Co, Cu,
Ni, and Pb ions on natural bentonite and bentonite
activated with HCl and H2SO4 in a different concentration
range was investigated. The individual results of removal
efficiency, E (%) and adsorption capacity qi (mg/L) for
the indicated ions are shown in the figures 2. - 8.
a)
b)
Figure 2: Effect of initial concentration of
multicomponent heavy metal solution Ci (mg/dm3
) on
removal efficiency a) E (%), and b) equilibrium
adsorption capacity qe (mg/L) of crude bentonite
a)
b)
Figure 3: Effect of initial concentration of
multicomponent heavy metal solution Ci (mg/dm3
) on a)
removal efficiency E (%), and b) equilibrium adsorption
capacity qe (mg/L) for bentonite activated with 0,4 M
H2SO4
a)
0
10
20
30
40
50
60
70
80
90
100
Cr Co Cu Ni Pb
E(%)
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
4 This work is licensed under Creative Commons Attribution 4.0 International License.
ISSN: 2349-8889
Volume-7, Issue-1 (January 2020)
https://doi.org/10.31033/ijrasb.7.1.1
International Journal for Research in
Applied Sciences and Biotechnology
www.ijrasb.com
b)
Figure 4: Effect of initial concentration of
multicomponent heavy metal solution Ci (mg/dm3
) on a)
removal efficiency E (%), and b) equilibrium adsorption
capacity qe (mg/L) for bentonite activated with 0,4 M
HCl
a)
b)
Figure 5: Effect of initial concentration of
multicomponent heavy metal solution Ci (mg/dm3
) on a)
removal efficiency E (%), and b) equilibrium adsorption
capacity qe (mg/L) for bentonite activated with 0,5 M
H2SO4
a)
b)
Figure 6: Effect of initial concentration of
multicomponent heavy metal solution Ci (mg/dm3
) on a)
removal efficiency E (%), and b) equilibrium adsorption
capacity qe (mg/L) for bentonite activated with 0,5 M
HCl
a)
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
8.0
Cr Co Cu Ni Pb
qemg/L
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
0
20
40
60
80
100
Cr Co Cu Ni Pb
E(%)
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
Cr Co Cu Ni Pb
qemg/L
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
0
20
40
60
80
100
Cr Co Cu Ni Pb
E(%)
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
8.0
Cr Co Cu Ni Pb
qemg/L
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
0
20
40
60
80
100
Cr Co Cu Ni Pb
E(%)
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
5 This work is licensed under Creative Commons Attribution 4.0 International License.
ISSN: 2349-8889
Volume-7, Issue-1 (January 2020)
https://doi.org/10.31033/ijrasb.7.1.1
International Journal for Research in
Applied Sciences and Biotechnology
www.ijrasb.com
b)
Figure 7. Effect of initial concentration of
multicomponent heavy metal solution Ci (mg/dm3
) on a)
removal efficiency E (%), and b) equilibrium adsorption
capacity qe (mg/L) for bentonite activated with 0,6 M
H2SO4
a)
b)
Figure 8. Effect of initial concentration of
multicomponent heavy metal solution Ci (mg/dm3
) on a)
removal efficiency E (%), and b) equilibrium adsorption
capacity qe (mg/L) for bentonite activated with 0,6 M
HCl
The initial concentration of the metal has a
significant effect on the adsorption process. The removal
efficiency of Cr, Co, Cu, Ni, and Pb using natural and
treated bentonite is decreased when increasing the initial
concentration of heavy metal ions in aqueous solutions.
The reason for the decrease lies in the fact that as the
concentration increases, the contact surface of the
adsorbent decreases in such a way that the number of
adsorption spots is reduced. In contrast, the change in the
equilibrium adsorption capacities, qi, shows the opposite
process, that is, the increasing trend of changes relative to
the change in the removal efficiency of heavy metal ions;
the increase in qi with increasing initial concentration of
solution of heavy metal ions is a result of stronger
attractive forces between the active spots of bentonite and
metal ions.
Using natural bentonite, it was concluded that
heavy metals were removed from aqueous solutions in the
following sequence: Pb (63.5-91.9%) ˃ Cu (55.4 - 91.5%)
˃ Ni (49.5-73.2 %) ˃ Co (25.4–65.5%) ˃ Cr (38.5–
90.2%). The use of acid-treated bentonite showed an
increase in ion removal efficiency, and the series of
adsorbed heavy metals remained the same as in natural
bentonite.
Many authors have tried to explain in their
works the influence of certain physicochemical properties
of metal ions on different removal adsorption.
The affinity of the adsorbent for a given metal
ion is correlated with the physicochemical properties
(ionic radius, electronegativity, electronic configuration,
molar mass, oxidation state, etc.).
In order to determine the efficiency of the
process of bentonite acid activation, the influence of
different starting concentrations of HCl and H2SO4 on the
adsorption removal capacity was observed. The results
obtained show that with increasing acid concentration, the
removal efficiency of all tested heavy metals increases, as
expected, the surface areas increased after acid treatment,
which is a likely consequence of the cations removal
from the clay structure, thereby promoting porosity.
Following acid activation of bentonite, it was noticed that
higher removal efficiency of heavy metals was given by
H2SO4 compared to HCl acid. From the obtained values it
can be concluded that 0.6M H2SO4 gives the best results.
Similar results were obtained by many other authors for
different metal ions.
IV. CONCLUSION
Adsorption results have shown that bentonite
can be used as an effective adsorbent for the simultaneous
removal of Cr, Co, Cu, Ni and Pb ions from aqueous
solutions when the pH value is adjusted to about 8.2.The
improvement in the adsorption properties of acid-treated
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
Cr Co Cu Ni Pb
qemg/L
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
0
20
40
60
80
100
Cr Co Cu Ni Pb
E(%)
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
8.0
Cr Co Cu Ni Pb
qemg/L
Metal ions
5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
6 This work is licensed under Creative Commons Attribution 4.0 International License.
ISSN: 2349-8889
Volume-7, Issue-1 (January 2020)
https://doi.org/10.31033/ijrasb.7.1.1
International Journal for Research in
Applied Sciences and Biotechnology
www.ijrasb.com
bentonite is the result of structural alterations, which have
led to an increase in the number of spots available for
adsorption. Sulfuric and hydrochloric acid can be used to
increase the sorption properties of bentonite, since
sulfuric acid obtains better results.
REFERENCES
[1] Ahmetović M., Šestan I., Begić S., Tučić E.,
Hasanbašić A. (2019). Biosorption of heavy metals from
the multi-component systems of the galvannic industry
using brewe's grain as adsorbents. International Journal
of Applied Science, 5(5), 26-32.
[2] Alexander E. B., Evgeny V.G., Irina V. B., Anastassia
E. K., Shilpi A., Alexey G. ., Vinod K. G. (2018).
Adsorption of heavy metals on conventional and
nanostructured materials for wastewater treatment
purposes. Ecotoxicology and Environmental Safety,
(148), 702-712.
[3] Eccles H. (1999). Treatment of metal-contaminated
wastes: why select a biological process?. Trends
Biotechnol, 17(12), 462-465.
[4] Barakat M.A. (2011). New trends in removing heavy
metals from industrial wastewater. Arabian Journal of
Chemistry, 4(4), 361-377.
[5] Leung W.C., Wong M.F., Chua H., Lo W., Leung
C.K., (2000). Removal and recovery of heavy metals by
bacteria isolated from activated sludge treating industrial
effluents and municipal wastewater. Water Science &
Technology, 41(12), 233-240.
[6] Santhosh C., Velmurugan V., Jacob G., Jeong S.K.,
Grace A.N., Bhatnagar A. (2016). Role of nanomaterials
in water treatment applications: a review, Chemical
Engineering Journal, (306), 1116-1137.
[7] Đukić A. (2015). Adsorpcija jona teških metala iz
vodenih rastvora na kompozitu montmorionit/kaolinit
glina - titan(IV)oksid, PhD dissertation.
[8] Bhattacharyya K. G. & S. Sen Gupta, (2008).
Adsorption of a few heavy metals on natural and
modified kaolinite and montmorillonite: a review. Adv
Colloid Interface Sci., 140(2):114-31.
[9] Önal M., & Sarikaya Y. (2007). Preparation and
characterization of acid-activated bentonite powders,
Powder Technology, 172(1), 14-18.
[10] Abdullahi S., Audu A. (2017). Comparative analysis
on chemical composition of bentonite clays obtained
from ashaka and tango deposits in gombe state, nigeria.
African Journals Online (AJOL), 8(2), 35-40.
[11] Newke O. M., Igwe E. O., Nnabo, P. N. (2015)
Comparative Evaluation of clays from abakaliki
formation with commercial bentonite clays for use as
drilling mud. African Journal of Environmental Science
and Technology, 9(6), 508-518.
[12] Tabak, A. Afsin, B. Caglar B. and Koksal (2008).
Characterization and pillaring of a Turkish bentonite
(Resadiye), Journal of Colloid and Interface Science,
313(1), 5-11.
[13] Kiviranta, L. and Kumpulainen, S. (2011). Quality
Control and Characterization of Bentonite Materials,
Working Report. Posiva, pp. 84.
Available at: http://www.posiva.fi/files/1994/WR_2011-
84_web.pdf
[14] Ajemba R. O. (2014). Kinetics and equilibrium
modeling of lead(II) and chromium(III) ions’ adsorption
onto clay from Kono-bowe, Turkish Journal of
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479.

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Examination of Adsorption Abilities of Natural and Acid Activated Bentonite for Heavy Metals Removal from Aqueous Solutions

  • 1. 1 This work is licensed under Creative Commons Attribution 4.0 International License. ISSN: 2349-8889 Volume-7, Issue-1 (January 2020) https://doi.org/10.31033/ijrasb.7.1.1 International Journal for Research in Applied Sciences and Biotechnology www.ijrasb.com Examination of Adsorption Abilities of Natural and Acid Activated Bentonite for Heavy Metals Removal from Aqueous Solutions Nedim Hodžić1 , Abdel Đozić2 , Indira Šestan3 and Hana Alihodžić4 1 PhD. Candidate, Department of Environmental Engineering, Faculty of Technology, University of Tuzla, BOSNIA AND HERZEGOVINA 2 Assoc. Prof. Dr., Department of Environmental Engineering, Faculty of Technology, University of Tuzla, BOSNIA AND HERZEGOVINA 3 Asst. Prof. Dr., Department of Physical chemistry and Electrochemistry, Faculty of Technology, University of Tuzla, BOSNIA AND HERZEGOVINA 4 Sen. Asst., Department of Environmental research laboratory, Institute for quality, standardization and ecology, BOSNIA AND HERZEGOVINA 2 Corresponding Author: abdel.dozic@untz.ba ABSTRACT The effect of the initial concentration of Cr, Co, Cu, Ni, and Pb metal ions from multicomponent solutions on the sorption capacity of natural and acid activated bentonite was examined in this paper. The acid activation was performed by using hydrochloric and sulfuric acid at different concentrations. The results of adsorption research have shown that bentonite can be effectively used as an adsorbent for the removal of metal ions from multicomponent solutions. Acid activation of bentonite changes the structure and content of individual oxides, increases the porosity and the number of available spots for the adsorption process. For this reason, the bentonite removal efficiency increased after acid activation for all heavy metals tested. With increased acid concentration, the degree of bentonite adsorption increased, and sulfuric acid rather than chloric acid showed better results in removal efficiency. Keywords-- Adsorption, Bentonite, Heavy Metals, Acid Activation I. INTRODUCTION Pollution of natural and wastewater is most often the result of the heavy metals discharge into the watercourses [1]. Heavy metals can be removed from aqueous solutions by various methods such as chemical precipitation, solvent extraction, membrane filtration, ion exchange, electrochemical removal, coagulation, etc. [2]. However, these techniques have disadvantages such as incomplete removal, high energy consumption, toxic sludge generation, low efficiency, sensitive operating conditions and high waste disposal costs [3,4]. To overcome such disadvantages, different approaches have been proposed, aimed at developing more inexpensive and more efficient methods for improving the quality of effluents [2]. Most are based on the application of the adsorption process, because adsorption has the greatest impact on the transport, toxicity and bioavailability of heavy metals (especially at low concentrations, in trace amounts) in aqueous solution, in addition the process is inexpensive and easy to perform. [5,6]. Considering the fact that bentonite is a natural material, the mechanical milling method can produce inexpensive adsorbents, and the activating adsorbents method is also environmentally friendly. Aluminum oxides and clay minerals such as bentonite, kaolin and pyrophyllite are relatively widespread minerals in the earth’s crust, which are known to be good adsorbents of various metal ions. Bentonite belongs to the smectite family and is classified as a natural clay of layered phyllosilicates composed of alternating octahedrons and tetrahedrons in a 2:1 ratio. The structure, chemical composition, exchangeable ionic type and small size of the crystals contribute to the unique properties of these clays, including a large chemically active surface, high cation exchange ability and high porosity. The degree of adsorption efficiency of heavy metals depends on a number of factors such as: pH value influence, temperature influence, adsorbent dose influence, initial concentration influence, contact time influence, etc. Bentonite has been shown to be effective adsorbent for heavy metals removal from waste water. However, despite the very good adsorption properties they possess naturally, there is increasing emphasis on the modification of natural clays in order to improve the general physicochemical properties. Activation methods with chemical agents or temperature are most commonly used to improve these properties. Acidic activation of clay achieves an increase in specific surface area and porosity [7]. The alteration degree of the active surface and the clay structure porosity caused by the action of acids depends on the type of clay minerals, i.e. chemical composition of clays, the type of interlayer cations, the acid applied and its concentration, temperature and time of action [8]. Acid-activated clays in industry are most commonly used as adsorbents, bleaches and catalysts [9]. The aims of the paper are as follows: - To examine the possibility of using natural and modified bentonite as an inexpensive adsorption material
  • 2. 2 This work is licensed under Creative Commons Attribution 4.0 International License. ISSN: 2349-8889 Volume-7, Issue-1 (January 2020) https://doi.org/10.31033/ijrasb.7.1.1 International Journal for Research in Applied Sciences and Biotechnology www.ijrasb.com for the removal of heavy metal ions. - To examine the adsorption capacity of heavy metals (Pb, Cr, Cu, Co and Ni) from multi component solutions using natural and modified bentonite. - To determine the effect of acid activation (with hydrochloric and sulfuric acid) on the sorption removal properties of heavy metals. II. EXPERIMENTAL PART The bentonite sorption property for Pb, Cr, Cu, Co, and Ni ions was examined for its natural and modified form. The modified form of bentonite was obtained by acid activation with hydrochloric (HCl, 36%) and sulfuric acid (H2SO4 96%). Based on the previous calculation, 0,4; 0,5; 0,6 M HCl and 0,4: 0,5; 0,6 M H2SO4 were prepared by adding known concentrations of pure acid into a 500 ml volumetric flask. After the required acids were prepared, 400 ml of 0.4 M HCl were weighed using a measuring cylinder and carefully transferred into a 500 ml laboratory beaker. The resulting mixture was stirred on a magnetic stirrer for eight hours at 200 rpm. Upon completion of the mixing process, the suspension was filtered through fine filter paper on a pre-set apparatus. During the filtration, the bentonite on the filter paper was washed with distilled water until a negative reaction to Cl-ions, which was checked with silver nitrate (AgNO3 5%). The bentonite filter paper was dried in a drying oven at 105 ° C for four hours. The dried bentonite was then ground in a porcelain mill and sieved through a 75 micrometer sieve. In this way, bentonite was acid activated with 0.4; 0.5; 0.6 M HCl. The same procedure was repeated for 0.4; 0.5; 0.6 M H2SO4, except that the bentonite on the filter paper was washed by distilled water until negative reaction to SO4 2- ions, which was checked by BaSO4 solution. 2.1. Materials Bentonite from a deposit in Šipovo, Bosnia and Herzegovina, was used for experimental research. Experimental research was performed in the accredited laboratory of the Institute for Quality, Standardization and Ecology. The laboratory is licensed for wastewater testing and is accredited to BAS ISO 17025: 2006, which implies that certified reference materials and chemicals of proven traceability and purity are used. Standard solutions of Cr, Co, Cu, Ni and Pb prepared from certified reference materials in different concentration ranges were used. After preparation of all materials, a batch adsorption process of the tested heavy metals ions from aqueous solutions was carried out using the following: 1. Natural (crude) bentonite 2. Acid-activated bentonite with 0.4; 0.5; 0.6 M HCl 3. Acid-activated bentonite with 0.4; 0.5; 0.6 M H2SO4 The following standard method was used to determine the content of Cr, Co, Cu, Ni, Pb heavy metals: BAS ISO 8288: 2002 Method A Water quality (Flame atomic absorption spectrometry method). A 240 Series Agilent Technology atomic absorption spectrophotometer was used to determine the content of heavy metals. All experiments were performed at room temperature. The contact time between the adsorbent and the multipart solution was 2 hours and did not change during the analyses. The X-Ray method was used to determine the chemical composition of bentonite, and the pH value of the biosorbent was determined by the zero-charge method. III. RESULTS AND DISCUSSION The obtained chemical analysis values for SiO2, Al2O3, Fe2O3 (48.28%, 23.04%, 4.52%) show a similar trend in the results obtained by researchers Abdullahi and Audu, 2017: who tested two bentonite samples in parallel, and those were: (48.16% and 49.87% for SiO2, 14.86 and 14.98% for Al2O3 and Fe2O3, respectively: 4.80% and 5.12%). The results also obtained for SiO2 are similar to the values reported by other autors (45 wt. %); and (48.35 wt. %) [11,12]. However, when it comes to Fe2O3 content, the results obtained are lower than those (11.10 wt. %) (8.26 wt. %) but higher than (3.82 wt. %) [11,12,13]. Since these are clays of smectite origin, the presence of Ca, Mg, Na and K is expected. Considering that the adsorption of heavy metal ions on clays depends on a large number of parameters, and that the pH value is one of the most significant, the optimal pH value at which the process is guided was determined before following the sorption processes of heavy metal removal. The figure 1 presents a review of the change in pH values, concluding that the zero charge point for bentonite is 8.27. Above these values the removal of positively charged ions will be more efficient. Comparing the results for natural clay 7.8 can be concluded that a slightly lower value than our [14]. Figure 1: Zero charge point for bentonite
  • 3. 3 This work is licensed under Creative Commons Attribution 4.0 International License. ISSN: 2349-8889 Volume-7, Issue-1 (January 2020) https://doi.org/10.31033/ijrasb.7.1.1 International Journal for Research in Applied Sciences and Biotechnology www.ijrasb.com The effect of different metal concentrations in solution on the removal efficiency was examined, as well as the different types of acid activation carried out using HCl and H2SO4 in different concentration ranges. By varying the concentration of individual ions from 5 to 30 mg/dm3 in multicomponent solution, the effect of this parameter on the adsorption of Cr, Co, Cu, Ni, and Pb ions on natural bentonite and bentonite activated with HCl and H2SO4 in a different concentration range was investigated. The individual results of removal efficiency, E (%) and adsorption capacity qi (mg/L) for the indicated ions are shown in the figures 2. - 8. a) b) Figure 2: Effect of initial concentration of multicomponent heavy metal solution Ci (mg/dm3 ) on removal efficiency a) E (%), and b) equilibrium adsorption capacity qe (mg/L) of crude bentonite a) b) Figure 3: Effect of initial concentration of multicomponent heavy metal solution Ci (mg/dm3 ) on a) removal efficiency E (%), and b) equilibrium adsorption capacity qe (mg/L) for bentonite activated with 0,4 M H2SO4 a) 0 10 20 30 40 50 60 70 80 90 100 Cr Co Cu Ni Pb E(%) Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
  • 4. 4 This work is licensed under Creative Commons Attribution 4.0 International License. ISSN: 2349-8889 Volume-7, Issue-1 (January 2020) https://doi.org/10.31033/ijrasb.7.1.1 International Journal for Research in Applied Sciences and Biotechnology www.ijrasb.com b) Figure 4: Effect of initial concentration of multicomponent heavy metal solution Ci (mg/dm3 ) on a) removal efficiency E (%), and b) equilibrium adsorption capacity qe (mg/L) for bentonite activated with 0,4 M HCl a) b) Figure 5: Effect of initial concentration of multicomponent heavy metal solution Ci (mg/dm3 ) on a) removal efficiency E (%), and b) equilibrium adsorption capacity qe (mg/L) for bentonite activated with 0,5 M H2SO4 a) b) Figure 6: Effect of initial concentration of multicomponent heavy metal solution Ci (mg/dm3 ) on a) removal efficiency E (%), and b) equilibrium adsorption capacity qe (mg/L) for bentonite activated with 0,5 M HCl a) 0.0 1.0 2.0 3.0 4.0 5.0 6.0 7.0 8.0 Cr Co Cu Ni Pb qemg/L Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L 0 20 40 60 80 100 Cr Co Cu Ni Pb E(%) Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L 0.0 1.0 2.0 3.0 4.0 5.0 6.0 7.0 Cr Co Cu Ni Pb qemg/L Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L 0 20 40 60 80 100 Cr Co Cu Ni Pb E(%) Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L 0.0 1.0 2.0 3.0 4.0 5.0 6.0 7.0 8.0 Cr Co Cu Ni Pb qemg/L Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L 0 20 40 60 80 100 Cr Co Cu Ni Pb E(%) Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
  • 5. 5 This work is licensed under Creative Commons Attribution 4.0 International License. ISSN: 2349-8889 Volume-7, Issue-1 (January 2020) https://doi.org/10.31033/ijrasb.7.1.1 International Journal for Research in Applied Sciences and Biotechnology www.ijrasb.com b) Figure 7. Effect of initial concentration of multicomponent heavy metal solution Ci (mg/dm3 ) on a) removal efficiency E (%), and b) equilibrium adsorption capacity qe (mg/L) for bentonite activated with 0,6 M H2SO4 a) b) Figure 8. Effect of initial concentration of multicomponent heavy metal solution Ci (mg/dm3 ) on a) removal efficiency E (%), and b) equilibrium adsorption capacity qe (mg/L) for bentonite activated with 0,6 M HCl The initial concentration of the metal has a significant effect on the adsorption process. The removal efficiency of Cr, Co, Cu, Ni, and Pb using natural and treated bentonite is decreased when increasing the initial concentration of heavy metal ions in aqueous solutions. The reason for the decrease lies in the fact that as the concentration increases, the contact surface of the adsorbent decreases in such a way that the number of adsorption spots is reduced. In contrast, the change in the equilibrium adsorption capacities, qi, shows the opposite process, that is, the increasing trend of changes relative to the change in the removal efficiency of heavy metal ions; the increase in qi with increasing initial concentration of solution of heavy metal ions is a result of stronger attractive forces between the active spots of bentonite and metal ions. Using natural bentonite, it was concluded that heavy metals were removed from aqueous solutions in the following sequence: Pb (63.5-91.9%) ˃ Cu (55.4 - 91.5%) ˃ Ni (49.5-73.2 %) ˃ Co (25.4–65.5%) ˃ Cr (38.5– 90.2%). The use of acid-treated bentonite showed an increase in ion removal efficiency, and the series of adsorbed heavy metals remained the same as in natural bentonite. Many authors have tried to explain in their works the influence of certain physicochemical properties of metal ions on different removal adsorption. The affinity of the adsorbent for a given metal ion is correlated with the physicochemical properties (ionic radius, electronegativity, electronic configuration, molar mass, oxidation state, etc.). In order to determine the efficiency of the process of bentonite acid activation, the influence of different starting concentrations of HCl and H2SO4 on the adsorption removal capacity was observed. The results obtained show that with increasing acid concentration, the removal efficiency of all tested heavy metals increases, as expected, the surface areas increased after acid treatment, which is a likely consequence of the cations removal from the clay structure, thereby promoting porosity. Following acid activation of bentonite, it was noticed that higher removal efficiency of heavy metals was given by H2SO4 compared to HCl acid. From the obtained values it can be concluded that 0.6M H2SO4 gives the best results. Similar results were obtained by many other authors for different metal ions. IV. CONCLUSION Adsorption results have shown that bentonite can be used as an effective adsorbent for the simultaneous removal of Cr, Co, Cu, Ni and Pb ions from aqueous solutions when the pH value is adjusted to about 8.2.The improvement in the adsorption properties of acid-treated 0.0 1.0 2.0 3.0 4.0 5.0 6.0 7.0 Cr Co Cu Ni Pb qemg/L Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L 0 20 40 60 80 100 Cr Co Cu Ni Pb E(%) Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L 0.0 1.0 2.0 3.0 4.0 5.0 6.0 7.0 8.0 Cr Co Cu Ni Pb qemg/L Metal ions 5 mg/L 10 mg/L 15 mg/L 20 mg/L 25 mg/L 30 mg/L
  • 6. 6 This work is licensed under Creative Commons Attribution 4.0 International License. ISSN: 2349-8889 Volume-7, Issue-1 (January 2020) https://doi.org/10.31033/ijrasb.7.1.1 International Journal for Research in Applied Sciences and Biotechnology www.ijrasb.com bentonite is the result of structural alterations, which have led to an increase in the number of spots available for adsorption. Sulfuric and hydrochloric acid can be used to increase the sorption properties of bentonite, since sulfuric acid obtains better results. REFERENCES [1] Ahmetović M., Šestan I., Begić S., Tučić E., Hasanbašić A. (2019). Biosorption of heavy metals from the multi-component systems of the galvannic industry using brewe's grain as adsorbents. International Journal of Applied Science, 5(5), 26-32. [2] Alexander E. B., Evgeny V.G., Irina V. B., Anastassia E. K., Shilpi A., Alexey G. ., Vinod K. G. (2018). Adsorption of heavy metals on conventional and nanostructured materials for wastewater treatment purposes. Ecotoxicology and Environmental Safety, (148), 702-712. [3] Eccles H. (1999). Treatment of metal-contaminated wastes: why select a biological process?. Trends Biotechnol, 17(12), 462-465. [4] Barakat M.A. (2011). New trends in removing heavy metals from industrial wastewater. Arabian Journal of Chemistry, 4(4), 361-377. [5] Leung W.C., Wong M.F., Chua H., Lo W., Leung C.K., (2000). Removal and recovery of heavy metals by bacteria isolated from activated sludge treating industrial effluents and municipal wastewater. Water Science & Technology, 41(12), 233-240. [6] Santhosh C., Velmurugan V., Jacob G., Jeong S.K., Grace A.N., Bhatnagar A. (2016). Role of nanomaterials in water treatment applications: a review, Chemical Engineering Journal, (306), 1116-1137. [7] Đukić A. (2015). Adsorpcija jona teških metala iz vodenih rastvora na kompozitu montmorionit/kaolinit glina - titan(IV)oksid, PhD dissertation. [8] Bhattacharyya K. G. & S. Sen Gupta, (2008). Adsorption of a few heavy metals on natural and modified kaolinite and montmorillonite: a review. Adv Colloid Interface Sci., 140(2):114-31. [9] Önal M., & Sarikaya Y. (2007). Preparation and characterization of acid-activated bentonite powders, Powder Technology, 172(1), 14-18. [10] Abdullahi S., Audu A. (2017). Comparative analysis on chemical composition of bentonite clays obtained from ashaka and tango deposits in gombe state, nigeria. African Journals Online (AJOL), 8(2), 35-40. [11] Newke O. M., Igwe E. O., Nnabo, P. N. (2015) Comparative Evaluation of clays from abakaliki formation with commercial bentonite clays for use as drilling mud. African Journal of Environmental Science and Technology, 9(6), 508-518. [12] Tabak, A. Afsin, B. Caglar B. and Koksal (2008). Characterization and pillaring of a Turkish bentonite (Resadiye), Journal of Colloid and Interface Science, 313(1), 5-11. [13] Kiviranta, L. and Kumpulainen, S. (2011). Quality Control and Characterization of Bentonite Materials, Working Report. Posiva, pp. 84. Available at: http://www.posiva.fi/files/1994/WR_2011- 84_web.pdf [14] Ajemba R. O. (2014). Kinetics and equilibrium modeling of lead(II) and chromium(III) ions’ adsorption onto clay from Kono-bowe, Turkish Journal of Engineering and Environmental Sciences, 38(3), 455- 479.