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Adsorptive removal of lead (Pb2+) ion from water using cellulose
acetate/polycaprolactone reinforced nanostructured membrane
To cite this article: R R Aquino et al 2018 IOP Conf. Ser.: Earth Environ. Sci. 191 012139
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The 4th International Conference on Water Resource and Environment (WRE 2018)
IOP Conf. Series: Earth and Environmental Science 191 (2018) 012139 IOP Publishing
doi:10.1088/1755-1315/191/1/012139
1
Adsorptive removal of lead (Pb2+) ion from water using
cellulose acetate/polycaprolactone reinforced nanostructured
membrane
R R Aquino1,3, M S Tolentino1,3, R M P D Elacion1, R Ladrillono1, T R C
Laurenciana1 and B A Basilia1,2
1School of Chemical, Biological, and Materials Engineering and Sciences, Mapúa
University, 658 Muralla St., Intramuros, Manila 1002, Philippines
2Industrial Technology Development Institute, Department of Science and Technology,
Bicutan, Taguig City, Metro Manila 1631, Philippines
E-mail: rraquino@mapua.edu.ph/marvstolentino@yahoo.com
Abstract. Nanostructured membranes of cellulose acetate (CA) with various polycaprolactone
(PCL) loadings (0%, 10%, 20% and 30%) were produced via electrospinning process for the
removal of Pb2+ ion from wastewater. Optimized electrospinning parameters were utilized:
voltage supply (30 kV), temperature (25 °C), tip to collector distance (18 cm) and needle size
(25 G). Certain characterization techniques were used to investigate the effect of PCL addition
on CA nanostructured membranes. The surface morphology was examined through Scanning
Electron Microscopy (SEM), and chemical composition and molecular structure were
determined using Scanning Electron Microscope – Energy Dispersive X-ray Spectroscopy
(SEM-EDX) and Fourier Transform Infrared Spectroscopy (FTIR), respectively. Results
showed that the incorporation of PCL in CA produced finer fiber diameter which gave the
membrane a larger surface area; thus, increasing the adsorption sites. Based on the results,
adsorption capacity was improved from 43.96 mg Pb2+/g of pure CA membrane to 70.50 mg
Pb2+/g of CA/PCL doped membrane. Moreover, the results of this experiment best fitted the
pseudo second-order kinetics, and the Freundlich isotherm which appropriately describe the
adsorption process. CA membranes are widely used in several separation processes, and the
results showed, its capability can be further enhanced by the incorporation of PCL to produce
nanostructured membranes.
1. Introduction
The presence of heavy metals in different water sources can pose a great threat to various living
organisms, specifically to humans. With this as a problem, many researches in the past years focused
on the removal of certain heavy metals in water [1]. Several processes are being conducted to treat
wastewater to remove heavy metals, and protect further water resources [2]. Emerging treatment
techniques such as adsorption using different adsorbent media, namely, modified natural materials [3],
industrial by-products [4], agricultural wastes [5], biological wastes (bio-sorption) [6], and modified
biopolymers and hydrogels [7], are commonly used in the removal of heavy metals from water.
Furthermore, other techniques include membrane filtration using different membrane blends [8],
electrodialysis [9] and photocatalysis [10].
The 4th International Conference on Water Resource and Environment (WRE 2018)
IOP Conf. Series: Earth and Environmental Science 191 (2018) 012139 IOP Publishing
doi:10.1088/1755-1315/191/1/012139
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Among the known water treatment techniques, adsorption process is widely used because of its
versatile applications other than heavy metal adsorption. Its applications also include adsorptive
removal of nitrogen contamination [11] and organic pollutants [12]. In addition to adsorption is
membrane technology, which is also known for its significant contribution in the field of water
treatment processes [13]. Furthermore, distinct advantages in applying membrane processes compared
to other water treatment processes include low energy consumption, membrane separations with mild
operating conditions, possible optimization of different membrane properties to satisfy various
requirements, minimal footprint, and most importantly, the feasibility to combine membrane processes
with other processes [14]. Several ways can be utilized in producing membranes, but a prominent
method is the electrospinning process, wherein nanofibers can be produced exhibiting special
properties such as large surface area to mass ratio, low density, high pore volume and tight pore size
make them suitable for a wide range of applications [15]. With the flexible uses of adsorption together
with the unique properties of electrospun membranes, an innovative technique for water treatment
applications [16], specifically the removal of heavy metals from wastewater [17], can be achieved.
Cellulose acetate (CA) is mostly used as membrane in several separation and water treatment
processes because of its desirable properties, mainly low cost/benefit ratio [18]. Its competence in
sequestering heavy metals in water had been proven because of the presence of different functional
groups such as –COOH, –SO3H and –NH2 groups, which are naturally grafted on CA. Hence, heavy
metals ions can attach and form bonds on the surface of CA through complexation mechanisms [19].
Studies had been made wherein reinforcement of synthetic polymers with CA were done to improve
its adsorption capability. In the study conducted by Tian and co-workers [20], electrospun CA was
surface-modified using poly (methacrylic acid) (PMAA). The results of their study showed an
increased adsorption capacity for Cd2+, Cu2+ and Hg2+ upon modification of CA. For instance, it was
found that there is the shifting of adsorption peak for –COO– from 1734 cm-1 to 1730 cm-1. This
signifies the decrease in the electronegativity of –COO– which is the main reason in the attraction of
electropositive heavy metal ions.
Other than water treatment, electrospun membranes are also significant in the biomedical field,
usually used as wound dressing [21]. One of the promising materials being used to fabricate
biocompatible membranes is the polycaprolactone (PCL), mainly because of its outstanding structure,
and excellent mechanical and physical properties [22].
In this study, it was aimed to fabricate a novel electrospun CA nanostructured membrane
impregnated with PCL to remove toxic Pb2+ from wastewater by means of membrane adsorption. The
material that produced underwent a series of characterizations using Scanning Electron Microscopy
(SEM) and Fourier Transform Infrared Spectroscopy (FTIR) to investigate its acquired properties. The
ability of the nanostructured membrane in removing Pb2+ metal ions from wastewater was investigated.
The adsorption kinetics, equilibrium, and adsorption isotherm were also studied.
2. Experimental
CA (65,000 g/mol) and commercial grade PCL (60,000 g/mol) utilized in this study were
provided by Chemline Enterprises. Acetone and dichloromethane (DCM) were used as solvents
for CA and PCL, respectively. Pure CA and CA/PCL blends of different PCL loading (0%, 10%,
20%, and 30%) were electrospun and the following parameters were applied: room temperature
(25 °C), 30 kV applied voltage and the distance from the tip to the collector was fixed at 18 cm.
The nanostructured membranes produced were characterized using the following techniques:
Fourier Transform Infrared Spectroscopy (FTIR) to confirm the presence of organic molecules
and provides a direct evidence of PCL and CA attachment, Scanning Electron Microscope (SEM)
for the morphological investigation of the material, SEM–Energy Dispersive X-ray Spectroscopy
(SEM-EDX) – with SEM in combination to determine the elemental composition of the sample.
Afterwards, the adsorption analysis was performed making use of the best CA/PCL blend
membrane and pure CA membrane as adsorbent at various amounts (0.05 g to 0.15 g at 0.025 g
interval) in a 250 mL flask having 200 mL Pb2+ solution with 100 ppm concentration. From these
The 4th International Conference on Water Resource and Environment (WRE 2018)
IOP Conf. Series: Earth and Environmental Science 191 (2018) 012139 IOP Publishing
doi:10.1088/1755-1315/191/1/012139
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fiber dosages and volume, the liquor to sorbent ratio ranges from 500:1 to 2000:1. The set up was
then placed in a water bath shaker for24 hours. Then every 8 hours, a 50 mL aliquot was collected
and digested. Analysis of each solution was conducted using Absorption Spectrophotometer
analyzer (AAS) to determine the following:the effect of contact time and Pb2+ initial concentration
on the adsorption capacity, adsorption kinetics (the best fit between pseudo first-order and pseudo
second-order kinetic model), and adsorption isotherm (Langmuir and Freundlich isotherm model).
3. Results and discussion
3.1. Effect of PCL on fiber structure
Figure 1 shows the SEM micrograph of pure CA membrane having uniform and straight fiber
morphology. The incorporation of PCL to CA reduced the fiber diameter of the membrane produced
which can be observed from the morphologies of the CA/PCL blends and their corresponding average
fiber diameters. Since PCL has a better conductivity compared to CA, and has good adhesion to a
broad spectrum of substrates [23], it provides better stretching of the solution which produced finer
fiber diameter [24]. Based from the obtained micrographs, CA with 10% PCL produced the
nanostructured fiber with the minimum average fiber diameter (570 ± 188 nm).
Figure 1. SEM micrographs of electrospun pure CA and CA/PCL blends at low (first row) and high
(second row) magnifications, with their corresponding average fiber diameters.
3.2. Molecular structure of the fibers
The FTIR results of the electrospun membranes were presented in figure 2.a. For pure PCL, at around
2900 cm-1 and 1700 cm-1, the spectrum indicates the presence of carbon-hydrogen (C-H) stretching
and carbonyl (C=O) stretching of carboxylic acid, respectively. For pure CA, the carbonyl (C=O)
group stretching is found at 1748.26 cm-1. The three changes or shifting of peaks for pure CA as
shown in figure 2.a shows the effect of adding PCL in the solution. The continuous increase in peaks
upon PCL additionimplies the successful bonding of the CA with the PCL in the membrane.
3.3. Adsorption analysis
As observed from the SEM micrographs (figure 1), the CA/PCL (10%) blend produced, has the finest
fiber diameter among the different blends. Finer fiber diameter would mean larger surface area which
would, in turn, mean larger adsorption area. Hence, the said blend and pure CA were used in the
adsorption experiment to compare the adsorption capacity as well as the kinetics of both fibers.
The 4th International Conference on Water Resource and Environment (WRE 2018)
IOP Conf. Series: Earth and Environmental Science 191 (2018) 012139 IOP Publishing
doi:10.1088/1755-1315/191/1/012139
4
Furthermore, based on the results of the SEM-EDX as seen on figure 2.b and 2.c, traces of Pb2+ were
detected after the adsorption process which proved the effectivity of the membrane produced.
Figure 2. a.) FTIR spectra of the different membrane blends, and SEM-EDX results for
CA/PCL (10%) blend b.) before and c.) after Pb2+ adsorption.
3.3.1. Effect of adsorbent dosage. For pure CA, based on the graph on figure 3.a, there is a noticeable
increase in the Pb2+ uptake when the CA fiber dosage was increased from 0.05 g to 0.075 g. As for the
CA/PCL (figure 3.b), similar characteristics and behavior could be observed. In this case, the optimum
adsorption dosage was determined to be 0.075 g. For both membranes, decrease in the adsorption
capacity can be observed when the fiber dosage exceeds 0.075 g. The decrease in adsorption capacity
could mean two things. First, adsorption equilibrium may not have been attained as the fiber dosage
was increased. Second, it is also possible that all Pb2+ ions from the solution adhered to the adsorbent
while there were still available sites for adsorption [23]. Thus, the results show that 100 ppm of Pb2+
was enough to saturate 0.075 g of pure CA, and CA/PCL blend.
Figure 3. Adsorption capacity of a.) pure CA and b.) CA/PCL (10%) fibers for Pb2+
as a function of adsorbent dosage at different time intervals.
3.4. Kinetics study
3.4.1. Effect of contact time. As can be seen on figure 4.a, equilibrium state was reached after 6 hours
for pure CA. Increasing trend for the adsorption capacity with time was observed up to 6 hours but at
time values greater than 6 hours, the adsorption capacity remained constant. This is most possibly due
to the large amount of active sites in the adsorbent [25] initially available, before the fiber started to
become saturated. In addition, initially there exist a high concentration gradient which aids the fast
The 4th International Conference on Water Resource and Environment (WRE 2018)
IOP Conf. Series: Earth and Environmental Science 191 (2018) 012139 IOP Publishing
doi:10.1088/1755-1315/191/1/012139
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diffusion of Pb2+ onto the surface of the adsorbent. Conversely,for CA/PCL blend, equilibrium was not
attained. Based figure 4.a, even at 10 hours, the adsorption capacity sill tends to increase. In this case,
due to the interaction of CA and PCL, and also because of finer fiber diameters produced, higher
amount of active sites became available for the adsorption of Pb2+ on the membrane.
3.4.2. Adsorption kinetics. Based on the results of the experimental data fitting (figure 4.b and 4.c),
pseudo second-order was found to be the model that best fitted the adsorption of Pb2+ onto fibers with
R2 value of 0.9174 for pure CA and 0.9934 for CA/PCL (10%) blend, compared to that of the pseudo
first-order model with R2 value of 0.2502 and 0.1598 for pure CA and CA/PCL (10%), respectively.
This means that the Pb2+ ion first dissociate from its parent molecule and form a chemical bond, likely
dipolar covalent, with the potential functional group of the fibers thereafter. These potential binding
sites are the amines, hydroxyls and carbonyls from CA and PCL. Also, the pseudo second-order
kinetics reveals that for both pure CA and CA/PCL (10%) membranes, the chemisorption is the
rate-limiting step for the adsorption of Pb2+, wherein the Pb2+ ions affix to the membrane with a
covalent bond among the sorbent and sorbates. Here, sites may be searched to which maximizes
the coordination number with the surface [26].
Figure 4. a.) Effect of contact time on the adsorption capacity of the fibers for Pb2+,
b.) pseudo first-order and c.) pseudo second-order model plots for the adsorbents.
3.5. Equilibrium study
Based from the gathered results (figure 5), the adsorption capacity is linearly increasing with initial
concentration of Pb2+ for both fibers at a fixed adsorbent dosage. This is due to the increase in the
driving force of the concentration gradient which accelerates the diffusion of Pb2+from the solution to
the adsorbent surface. For pure CA adsorbent, an increase in the adsorption capacity was observed
from 3-6 hours of immersion and decreases at 9 hours of immersion due to reversibility in the
adsorption process. On the other hand, it was observed that the adsorption capacity of PCL is steady
and decreases slightly which suggests that PCL dope fibers were more stable adsorbent for metal
specie at longer times. In addition, it can be seen that PCL doped fibers have higher adsorption
capacities compared to pure CA for all varied initial concentration of Pb2+ solution.
Figure 5. Effect of initial Pb2+ concentration on the adsorption capacity of a.) pure CA and
b.) CA/PCL (10%) fibers at different time intervals.
The 4th International Conference on Water Resource and Environment (WRE 2018)
IOP Conf. Series: Earth and Environmental Science 191 (2018) 012139 IOP Publishing
doi:10.1088/1755-1315/191/1/012139
6
3.6. Adsorption isotherm
Based on the results in figure 6, the regression coefficient R2 of linear Freundlich isotherm for pure
CA and CA/PCL were found to be 0.9957 and 0.994, respectively. The experimental data best-fitted
the Freundlich isotherm model because it has the best R2 compared to Langmuir isotherm model. This
explains that the adsorption process occurred on a heterogenous (multiple layer) surface with uniform
energy [25]. Also, physisorption and chemisorption occur at low coverages.
Figure 6. Adsorption isotherm fitting; a.) Langmuir isotherm and b.) Freundlich isotherm.
4. Conclusion
Electrospun CA/PCL nanostructured membranes for the adsorption of Pb2+ were successfully
produced. The SEM results showed that CA/PCL (10%) exhibited the smallest average fiber
diameter, which means larger adsorption surface area. Interaction between CA and PCL was
supported by the results of FTIR analysis. For the adsorption experiment, based from the gathered
results, it was observed that the incorporation of 10% PCL improved the adsorption capacity of
pure CA from 43.96 mg Pb2+/g membrane of pure CA to 70.50 mg Pb2+/g of PCL doped fibrous
membrane, after 6 hours in which the saturation of pure CA had occurred. The adsorption data of
the study were best fitted in the pseudo-second order model and Freundlich isotherm model.In
general, it had been observed that the incorporation of PCL can improve the adsorption capacity
of pure CA, which shows that the CA/PCL (10%) blend is a more suitable adsorbent for heavy
metals at longer time intervals and can be a promising material for wastewater treatment.
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