ORIGINAL PAPER
Potential application of termite mound for adsorptionand removal of Pb(II) from aqueous solutions
N. Abdus-Salam • A. D. Itiola
Received: 18 February 2011 / Accepted: 26 May 2011 / Published online: 10 January 2012
� Iranian Chemical Society 2012
Abstract The morphological and mineralogical composi-
tion of a termite mound from Ilorin, Nigeria was investigated
with a view to understand its sorption properties. The termite
hill soil was subjected to some spectroscopic analyses such as
X-ray fluorescence (XRF) and Scanning Electron Micros-
copy. The XRF results revealed that the adsorbent contains a
large fraction of Silicon, Iron and Aluminium minerals. The
organic matter (OM) content expressed as percentage carbon
was 3.45% while the high value of cation exchange capacity
of 14.0 meq/100 g is in agreement with high percentage OM,
which signifies high availability of exchangeable ions. The
maximum Pb(II) adsorption capacity of the mound was found
to be 15.5 mg/g. Batch adsorption experiments were carried
out as a function of contact time, ionic strength and pH.
Maximum and constant adsorption was observed in the pH
range of 2–5.5. The experimental results of Pb(II) adsorption
were analyzed using Langmuir, Freundlich, and Temkin
isotherms. The Langmuir and Temkin isotherms were found
to fit the measured sorption data better than Freundlich. The
constants obtained from the Langmuir model are maximum
sorption value, Qm = 18.18 and Langmuir energy of
adsorption constant, b = 0.085, while the constants of the
Freundlich model are the intensity of adsorption constant,
n = 0.134, and maximum diffusion constant, Kf = 1.36. The
adsorption data for Pb(II) was found to fit well into the
pseudo-second order model. Desorption experiment was
conducted using different concentrations of leachant and this
was repeated three times to determine the life span of the
adsorbent. It was observed that 0.2 M HCl had the highest
desorption efficiency for reuse.
Keywords Termite mound � Cation exchange capacity
(CEC) � Adsorption isotherms � Pseudo-first and second
order models � Desorption
Introduction
Termites are social ants that exert significant influence on the
physical and chemical properties of tropical and sub-tropical
soils [1–3]. The feeding habit, the food processing and
mound construction operations introduce significant modi-
fications to the soil on which the mound is built [4, 5]. Studies
have shown that termite mounds in tropical soil like Nigeria
may have lower or higher values for exchangeable Ca, Mg
and K, effective cation exchange capacity (ECEC), water
holding capacity, and water infiltration rates [6]. African
farmers are familiar with the practice of applying termite
mounds on their farms as it contains required nutrients for
plants growth [7]. In a related research, termite-mound soil
was reported to contain as much as 20% of the total nitrogen
as inorganic nitrogen, an average organic carbon content of
9.3% and 2.25 times more total P than the adjacent soils [8].
Lead is one of the major industrial pollutants of human
concern as air-particulate or in dilute aqueous medium. The
metal is associated with industries such as paints, pigments,
batteries, ceramic glazes, metal products, petroleum and
cosmetic products, cable sheathing and ammunition pro-
duction [9]. The divalent form [Pb(II)] is the stable ionic
species of lead. The metal has the tendency to form insol-
uble compounds with OH-, CO32-, and S2-. The ratio of
suspended form to the soluble form of lead may vary from
4:1 in rural streams to 27:1 in urban streams [10].
Different methods for the removal of heavy metals from
aqueous solutions have been proposed [11–14]. These
include solvent extraction, ion exchange filtration and
N. Abdus-Salam (&) � A. D. Itiola
Department of Chemistry, University of Ilorin,
P.M.B.1515, Ilorin, Nigeria
e-mail: [email protected]
123
J IRAN CHEM SOC (2012) 9:373–382
DOI 10.1007/s13738-011-0047-2
membrane separation, reverse osmosis, chemical precipi-
tation and coagulation. These methods are known for one
shortcoming or the other, ranging from incomplete
removal, high energy consumption, reagents cost, disposal
of large volume of organic solvents and inefficiency when
the metal concentrations are \10 mg/l [9]. Adsorption
process is a promising alternative technique that is free
from the shortcomings of the earlier techniques. Adsor-
bents from natural or modified materials and synthetic
origin are subject of recent research efforts. These adsor-
bents include activated carbon from agricultural products
[15–17], clay and clay materials [11, 18, 19], and oxides of
iron [20].
Modifications of soil physical and chemical properties
by termite’s mounds and mechanical properties have been
reported, however, only limited studies have involved
application of the mounds in the decontamination of metal
polluted effluents. The objective of this study was to
characterize termite mound soils and determine the sorp-
tion characteristics. Langmuir isotherm equation was
employed to quantify the adsorption equilibrium. The
effects of solution pH, ionic strength and variation of time
on Pb(II) adsorption were examined.
Materials and methods
Collection of samples and pretreatment
The termite mound soil was collected within the compound
of Ilorin Grammar School, Ilorin, Kwara State. A sample of
about 2 kg was collected and air-dried in the laboratory at
room temperature for 5 days. The sample was then placed
in an oven set at 60 �C for 10 h before crushed in a mortar,
grounded and thoroughly mixed by repeated (more than 10
times) conning and quartering. The grounded mound was
then sieved into different fractions: U B 0.09 B 0.25 B
0.4 B 0.5 mm and the fraction with diameter U B 0.25 mm
was used for subsequent experiment. This fraction was pre-
treated to remove non-clay material such as carbonate and
quartz minerals in order to concentrate the active minerals
and improve the sorption property of the adsorbent. The pre-
treatment involved washing a pre-heated slurry of termite
mound at 90 �C with 0.1 M HNO3 to leach the non-clay
materials. The mixture was stirred for 2 h and then thor-
oughly washed with distilled water until the pH of the
washings remains constant and finally air-dried [21].
Soil pH was determined potentiometrically in 0.01 M
CaCl2 at a soil-solution ratio of 1:2.5 [22, 23]. The organic
carbon content of the mound sample was determined by
the dichromate oxidation, a Walkley–Black method [24].
The ammonium acetate method was used to determine the
cation exchange capacity (CEC). The CEC was obtained by
summation of the exchangeable acidity and exchangeable
cations, which are mostly Ca, Mg, Na, K (collectively
termed as bases). The K and Na were determined by flame
photometry method while Ca and Mg were determined by
titrimetric method [24]. The point of zero charge (pzc) was
determined by both mass titration and potentiometric
methods [25]. This involve measurement of pH of the
mound (0.5–2.0 g) suspension in 25 ml of different ionic
strength (10-3 to 10-1 M). The pH values at the start of
experiment and after 24 h were recorded. The pH of the
mixture was then adjusted to pH 5–6 with 0.01 M HNO3,
equilibrated for 24 h and pH measured. The pH of these
mixtures was then re-adjusted to pH 10–11 with 0.01 M
KOH, equilibrated for 24 h and the pH measured. The acid
and base adjustments were made in order to determine the
influence of pH on the pzc [25]. The termite mounds
sample was analyzed to determine its constituents and
qualities using X-ray flourescence (XRF) model Axios of
Analytical type with a 2.4kWatt Rh X-ray tube. The
scanning analysis was accomplished on a Leo 1430 VP
Scanning Electron Microscope.
Contact experiment
A 0.5 g portion of the various soil samples collected was
weighed in a 100 mL conical flask and 25 cm3 of working
standard solutions (500, 350, 250, 150, 100 and 50 ppm) of
Pb(II) prepared by serial dilution of the standard solution,
was added to the soil sample in the beaker. Each solution
was agitated on a flat orbital mechanical shaker for 7 h and
then filtered. The filtrate was analyzed using Atomic
Absorption Spectroscopy (AAS) to determine the quantity
of Pb(II) remaining in the solution. The quantity sorbed
was then evaluated using the following equation [26].
qe ¼Ci � Cf
M� V ð1Þ
where qe is the amount sorbed at equilibrium (mg/g), Ci is
the initial concentration of lead solution (mg/L), Cf is the
final concentration of lead solution (mg/L), V is the volume
of lead nitrate solution used (mL), M is the mass of soil
used (g).
The quantity sorbed was plotted against the initial
concentration to determine the equilibrium concentration
which is the concentration with the highest sorption
capacity [the adsorption capacity of the mound soil for
Pb(II)]. This equilibrium concentration was used subse-
quently for the sorption kinetics.
Effect of reaction time
The effect of reaction time was investigated using 25 mL
of 350 mg/L of Pb(II) solution and 0.5 g of the mound
374 J IRAN CHEM SOC (2012) 9:373–382
123
sample each in an 100 mL reactor flask. A total of ten
reactors were set up for time duration ranging between 5
and 420 min. The mixtures in reactors was then agitated on
a flat orbital shaker and allowed to equilibrate at different
time intervals. The flaks were removed at designed inter-
vals and content filtered. The Pb(II) in the filtrates were
analyzed using AAS and the amount sorbed were calcu-
lated from Eq. 1.
Effect of ionic strength
The influence of ionic strength on the adsorption of Pb(II)
was investigated using three different concentrations (0.1,
0.01, 0.001 M) of potassium nitrate (KNO3) solution. The
different concentration was added to the solution of
350 mg/L of Pb(II) solution and the mound sample in dif-
ferent flasks. The mixtures were equilibrated for 7 h and
then filtered; this filtrate was analyzed for Pb(II) using AAS
and the quantity adsorbed was calculated from Eq. 1 above.
Effect of pH
25 mL of 350 mg/L of Pb(II) solution was added to 0.5 g
of soil sample in a 100 mL conical flask and the initial pH
was noted. The pH of the resulting solution was then varied
between pH 2 and 7.5 using 0.1 M HNO3 and/or KOH
solution. The mixture was equilibrated for 7 h and then
filtered. The filtrate was analyzed for Pb(II) using AAS and
the quantity adsorbed calculated.
Fitness of Pb(II) adsorption data into Langmuir,
Freundlich, and Temkin equations
The equilibrium concentrations data obtained in the contact
experiment were subjected to the Langmuir, Freundlich,
and Temkin adsorption isotherms to find the equation that
best fits the data. Data were fed into Eqs. 2–4 separately
and constants were calculated.
Langmuir :Ce
Qe
¼ 1
bQm
þ Ce
Qm
ð2Þ
Freundlich : LogQe � LogKf þ1
nLogCe ð3Þ
Temkin : Qe ¼ BlnAþ BlnCe ð4Þ
where Qe is the quantity sorbed at equilibrium (mg/g), Ce is
the equilibrium concentration of adsorbate (mg/L), A and
B are Temkin isotherm constants related to adsorption
efficiency (dm3/mmol) and energy of adsorption, respec-
tively. The Langmuir adsorption isotherm constants were
determined by plotting Ce/Qe against Ce [27–29]. The
Freundlich adsorption isotherm was determined by plotting
log Qe against log Ce. The slopes and intercepts obtained
from the graphs were used to calculate the Langmuir and
Freundlich constants. In the case of Temkin, the quantity
sorbed Qe was plotted against lnCe and the constants were
determined from the slope and intercept.
Adsorption kinetics
The adsorption kinetic models are important in the process
of removal of toxic heavy metals from the environment
because it provides information on pollution flux. Both
pseudo- first and second order models were tested with the
data obtained to establish the model that best fits the data.
Pseudo-first order model [30, 31]
The equation for this reaction is
dqt
dt¼ kðqe � qtÞ ð5Þ
where qe is the quantity of solute adsorbed at equilibrium
per unit mass of adsorbent (mg/g), qt is the amount of
solute adsorbed at any given time t, (mg/g) and k is the rate
constant of first order sorption (1/min). By using the
boundary conditions t = 0 to t = t and qt = 0 to qt = qt
and simplifying, Eq. 5 becomes
log(qe � qtÞ ¼ logqe �k
2:303t ð6Þ
The plot of log (qe - qt) versus t gives the slope and
intercept from which k and qe were evaluated.
Pseudo-second order model
The pseudo-second order model [30, 31] was used for the
sorption data and the equation for this is
dqs
dt� kzðqe � qlÞ2 ð7Þ
On integration for boundary conditions when t = 0 to
t = t and qt = 0 to qt = qt then Eq. (7) can further
simplification results in the following equation
t
qt
¼ 1
k2q2e
þ 1
qe
t ð8Þ
where k2 is the rate constant of second order of sorption
(g/mg min). The plot of t/q versus t was made to evaluate
k2 and qe.
Sorption–desorption experiment
The normal sorption procedure was carried out using 1.0 g
of mound sample in 25 cm-3 of 500 ppm Pb(II) solution.
The mixture was equilibrated for 7 h and then filtered and
J IRAN CHEM SOC (2012) 9:373–382 375
123
the filtrate was analyzed for Pb(II) while the residue was
used for desorption experiment. A 25 cm-3 of different
concentrations of HCl (0.1, 0.2, 0.5 and 1.0 M) were added
to the residues in different conical flasks and each mixture
was equilibrated for 7 h and then filtered. The filtrate was
analyzed for the amount of Pb(II) released back into the
solution. This sorption and desorption processes were
repeated on the same sample for three times. The quantity
sorbed or desorbed was calculated using Eq. 1 above. A
graph of the quantity desorbed was plotted against the steps
of the desorption process for the different ionic strengths.
Results and discussion
The physical properties of the termite hill soil are summa-
rised in the Table 1. The termite hill soil obtained from
Ilorin Grammar School in Ilorin was brown with fine tex-
ture. The colour is within the variable colours of mound
hills (brownish to blackish) depending on the soil mor-
phology of the environment. The pH of the supernatant fluid
of a mixture of the termite hill soil and water was slightly
lower than neutral (pH 6.7).The termite hill soil is relatively
rich in organic matter as expressed by percentage organic
carbon (3.45%). Lower percentage organic matters were
reported for soil fractions such as utisol (1.86%) [18],
montmorillonite (2.1%) [32], and soil mound 0.8–1.32 [33].
The CEC depends greatly on the soil organic matter.
The more the soil’s organic matter content, the higher will
be its CEC. The high CEC value of 14.0 meq/100 g is in
agreement with high percentage of OM, signifying high
availability of exchangeable ions. This translates to
enhance adsorptive capability of the soil.
Spectroscopic studies
The XRF elemental analyses of virgin (A) and after sorption
of Pb(II) onto the mound are reported in Table 2. The result
showed that SiO2, Al2O3 and Fe2O3 were present as major
components as indicated from their high intensities. TiO2,
CaO, K2O, H2O and MgO were present as minor compo-
nents while P2O5, Cr2O3 and MnO were present as trace
components. This implies that the adsorbent contains a
large fraction of silicon, iron and aluminium minerals.
Sample B data also indicate an increase in the %weight of
aluminium oxides after sorption of Pb(II) and a decrease in
%weight of silicate after sorption of Pb(II) and conse-
quently a decrease in the total weight which may be due to
the presence of some minerals which were not present in the
list of the major elements used in the analysis. This trend is
attributable to the loss on ignition (LOI) which was found to
increase from 6.38 to 13.25 after sorption of Pb(II).
The result of SEM elemental and weight per cent of their
oxides for virgin and after sorption of Pb(II) onto the mound
are reported in Table 3. Although, there were variations in
the percent weights of elements obtained from the two
analyses (XRF and SEM), Si, Al and Fe remained major
elements while K, and Ti are minor elements. Figures 1 and
2 are the results of scanning electron micrographs of virgin
samples. Round crystals arranged well next to each other
and forming large round aggregates of crystals were
observed. A similar image was observed in an SEM pho-
tograph of lead hydroxide [34]. The presence of many open
pores is visible from Figs. 1 and 2. Figures 3 and 4 show the
filled pores and signify adsorption of Pb(II).
The point of zero charge (pzc) of the termite hill soil by
potentiometric method was found to be 7.8 for the different
ionic strengths which is similar to what was obtained for
natural goethite (pzc = 7.8) [35]. Comparative values
obtained for the same sample by mass titration were
between 6.1 and 6.5 range for the different ionic strengths
(0.1, 0.01, 0.001 M), but after acid adjustment, the pzc
increased proportionately to the range 6.4–6.9. After
alkaline adjustment, the pzc was observed at pH 8.2. The
variable pzc obtained from mass titration is often affected
by the nature of contaminants such as basic and acidic
elements in the sample [34]. The potentiometric method
may therefore be preferred because it is free from the
interference of acidic/basic contaminants. Therefore, the
pzc of this termite hill is 7.8. At pH below this pzc value,
the acidic water donates more protons than hydroxide
groups and so the termite hill soil will have a positive
surface charge characteristic and will therefore electro-
statically repel cations and attract anions to its surface.
Conversely, above pzc, the surface charge characteristic
will be negative [35]. The presence of ionic species or
complexing agents in the reaction medium may change this
adsorption pattern by conferring a net negative surface
charge at pH below pzc value. This explains the adsorption
of metal or hydrated metal ions onto surfaces at pH lower
than its pzc value.
Sorption capacity of termite mound
Figure 5 represents a two steps process. An initial linear
rise in the uptake of Pb(II) which is followed by a less steep
Table 1 Physico-chemical properties of termite hill soils
Properties Quantity/value
Colour Brown
Texture Fine
pH 6.7
Weight organic carbon (%) 3.45
CEC (meq/100 g) 14.0
376 J IRAN CHEM SOC (2012) 9:373–382
123
curve. As the initial concentration increases the amount
adsorbed increases proportionally until a plateau was
reached, where there was no corresponding rise in the
amount adsorbed. The favourable sites with lower
adsorption energies have been filled making the unfa-
vourable sites more difficult to fill. This is an indication of
surface saturation or a monolayer adsorption. The second
rise is a continuation of monolayer adsorption given a two-
step Langmuir curve
Influence of contact time on the adsorption of Pb(II)
Figure 6 which shows the effect of time on the adsorption
of Pb(II), can be classified into three portions according to
the behaviour of the curve. An initial decrease in the
quantity of Pb(II) (5–20 min) adsorbed due to inability of
the system to establish equilibrium. This is followed by
sharp rise in adsorption where majority of the metal ion
was adsorbed. This is a fast uptake (between 30 and
90 min) in which about 65% of Pb(II) was sorbed. The last
portion (90–600 min) represents a slow kinetics. It is
characterized by an increase in the quantity of Pb(II)
adsorbed but at a relatively slow rate compared to the
second portion of the curve. This occurs when the available
(favourable) binding sites on the adsorbent is low. The
energy of adsorption becomes relatively higher than before.
Similar trends were reported for adsorption of Pb(II) on a
natural goethite [35].
Effect of ionic strength on adsorption of Pb(II)
A steady decrease in the amount of Pb(II) adsorbed was
observed as the ionic strength increases (0–0.5 M) until it
gets to a point where a further increase in ionic strength has
no effect on the quantity of Pb(II) adsorbed. Higher ionic
strength of the reacting medium has no influence on the
adsorption of Pb(II) (Fig. 7). The decrease in the quantity of
Pb(II) sorbed between 0 and 0.2 M ionic strength is due to
modification of surface charge characteristics. As the ionic
strength increases, the net negative charge on the termite
hill surface decreases, thereby decreasing the attraction
between the metal and the surface.
Table 2 XRF analysis of Ilorin virgin termite hill soil (A) and after sorption of Pb (B)
Wt% Al2O3 CaO Cr2O3 Fe2O3 K2O MgO Na2O MnO P2O5 SiO2 TiO2 LOI H2O Total
A 11.36 0.10 0.01 6.38 0.72 0.10 bd 0.08 0.06 73.46 0.97 6.38 0.89 100.52
B 17.86 0.62 0.01 8.35 0.97 0.14 0.01 0.04 0.16 43.41 1.08 13.25 1.64 87.52
A: element analysis before sorption of Lead
B: element analysis after sorption of Lead
Bd below detection
Table 3 Scanning electron microscopy elemental and % compound results
Analysis Al (Al2O3) Si (SiO2) K (K2O) Ti (TiO2) Fe (FeO) O Total
Sample A (wt%) 18.02 (34.048) 20.38 (43.59) 0.39 (0.468) 0.75 (1.254) 16.04 (20.64) 44.42 100.00
Sample B (wt%) 16.93 (31.988) 25.04 (53.576) 0.56 (0.678) 1.29 (2.155) 9.02 (11.603) 47.15 100.00
Fig. 1 SEM photograph of termite hill soil using K91.50
magnification
Fig. 2 SEM photograph of termite hill soil after sorption using
K91.50 magnification
J IRAN CHEM SOC (2012) 9:373–382 377
123
Effect of pH on the adsorption of Pb(II)
The graphical illustration of the pH on the adsorption
characteristics of mound is shown in Fig. 8. The sorption
experiment was carried out at pH ranging from 2.0 to 7.5.
A steady increase was observed in the quantity of Pb(II)
adsorbed as the pH decreased from 7.5 until after a pH of
5.5. The quantity of Pb(II) adsorbed was highest and
practically constant between the pH of 2.0–5.5 but
decreases from 6.0 to 7.5. Although, the natural surface
charge characteristics of soil materials is positive at pHs
below the pzc but practically, adsorption of metal ions is
found to be favourable at pH less than the pzc values
because at this value, the adsorbent is in a monomeric
anion form and consequently has affinity for cations [36].
Fig. 3 SEM photograph of termite hill soil using K91.00
magnification
Fig. 4 SEM photograph of termite hill soil after sorption using
K91.00 magnification
Fig. 5 Determination of equilibrium concentration
Fig. 6 Effect of contact time on the adsorption of Pb(II)
Fig. 7 Quantity of Pb(II) sorbed versus ionic strength
Fig. 8 Quantity of Pb(II) sorbed versus pH
378 J IRAN CHEM SOC (2012) 9:373–382
123
The presence of anionic species such as nitrate ions from the
Pb(II) salt solution used confers a net negative charge on the
mound in a monomeric anionic form. This is attributed to a
higher adsorption of Pb(II) between pH 2 and 5. Above the
pzc value, the surface is positively charged and will repel
adsorption of cations. The only process that can increase
the quantity of metal adsorbed after pzc is by precipitation
of metals. Many metals precipitate out in an alkaline
medium.
Adsorption isotherms
The adsorption data obtained from the adsorption of Pb(II)
experiment were tested for fitness of data against three
common adsorption equations, Langmuir, Freundlich and
Temkin adsorption isotherms, respectively. Figure 9 is a
Langmuir adsorption isotherm for the sorption of Pb(II) by
termite hill soil. The adsorption isotherm data as analyzed
from Fig. 9 are 18.8, 0.085 and 0.993 for Qm, b and the
regression coefficient R2, respectively. The observed b
value (b � 1) shows that the mound sample prefers to bind
acidic ions and that speciation predominates on sorbent
characteristic when ion exchange is the predominant
mechanism that takes place in the adsorption of Pb(II) [28].
The observed R2 = 0.993 shows that the Langmuir iso-
therm fitted fairly well the adsorption data for Pb(II). The
favourability of this adsorption process was subjected to
the equation of separation factor RL [37] given as:
RL ¼1
1þ bCi
ð9Þ
where b is the Langmuir equilibrium constant (K), Ci is the
initial concentration.
For a favourable adsorption, 0 \ RL \ 1, while for an
unfavourable adsorption, RL [ 1 and when RL = 0,
adsorption is linear and irreversible. The RL value obtained
from this adsorption process is 0.033 which indicates that
the adsorption process is favourable.
The Freundlich adsorption constants obtained from
Fig. 10 are n = 0.134, Kf = 1.36 and the regression
coefficient R2 = 0.972. The relatively small slope, n � 1,
indicates that sorption intensity is favourable over the
entire range of concentrations studied [36, 38]. Likewise,
the high value of the intercept Kf, is indicative of a high
sorption capacity of termite hill soil. The regression coef-
ficient R2 = 0.972 shows that the Freundlich adsorption
isotherm equation fits the experimental data too. When the
R2 values are compared, the data fits into Eqs. 2 and 3,
while Langmuir predicts a physical and mono-layer
adsorption process, the possibility of two-step (Fig. 5) and
chemo-sorption may not be ruled out because of the fitness
into Eq. 3.
The adsorption data was subjected to Temkin equation
and Fig. 11 is a representation of the isotherm obtained.
The Temkin adsorption constant A, obtained from Fig. 11
is -0.122 and the regression coefficient R2 is 0.985. In
comparison, the regression coefficients, R2, for the iso-
therms are: Langmuir (0.993), Freundlich (0.972) and
Temkin (0.985). It shows that the Langmuir and Temkin
isotherms fitted the adsorption data for lead ions better than
the Freundlich isotherm.
Table 4 is a summary of isothermal constants and
regression coefficients. Comparing these data with similar
data for goethite, where the Langmuir constants (b and Qm)
obtained for Pb(II) on goethite are 4.99 and 2.40, respec-
tively [39], it can be concluded that Pb(II) is better sorbed
on to termite hill soil than natural goethite.
Adsorption kinetics
The data obtained from the influence of time on the
adsorption of Pb(II) onto the mound sample were subjected
to the pseudo-first order and pseudo-second order kinetics
(Lagergren) equations for a test of fitness of data and
the plots of which gave Figs. 12 and 13, respectively. A
negative and zero slopes were observed for pseudo-first
order model; therefore, pseudo-first order model was not
sufficient to explain the adsorption kinetics of Pb(II) on
termite hill soil. Figure 13 is the plot of t/qt versus t, theFig. 9 Langmuir isotherm curve
Fig. 10 Freundlich adsorption isotherm for the sorption Pb(II)
J IRAN CHEM SOC (2012) 9:373–382 379
123
pseudo-second order model, yields a very good plot with a
regression coefficient R2 = 0.998, pseudo-second order
rate constant k2 = 107.8 g/mg and qe = 13.6 mg/g.
Therefore, the kinetics is best described by the pseudo-
second order kinetics.
Desorption experiment
Desorption data obtained is graphically represented in
Fig. 14. From the graph, it was revealed that the quantity
desorbed for the first process was practically the same for
the various acid concentrations. There is significant differ-
ence in the quantity desorbed in the second process among
the different acid concentrations. The quantity of Pb(II)
desorbed from the second step was highest for 0.2 M HCl
concentration and has the greatest efficiency for reuse. The
adsorption efficiency of termite hill soil dropped by 52.8%
after the first desorption and by 86% after the second
desorption, the quantity desorbed between the processes is
consistent. The adsorption process is therefore reversible.
Desorption data for 1.0 M is the most irreversible, the
adsorption efficiency dropped by 88% after the first
desorption process and by 12% after the second. The
quantity desorbed between each process is inconsistent.
The desorption process using distilled water followed a
different pattern. The quantity desorbed during the first
process was very low but the efficiency increased after
each desorption process. With similar solutions for the
desorption process, it can be seen that the quantity des-
orbed decreased after subsequent desorption for all the
acidic strengths except for distilled water which increased
after subsequent desorption. The 0.5 M HCl solution has
the highest desorption efficiency. The quantity desorbed
dropped from 62 to 13% after subsequent desorption, fol-
lowed by 0.1 M HCl which dropped from 61 to 34% and
then 0.2 M HCl with 60% which also dropped to 28%. We
can deduce from this that the desorption efficiency of both
0.1 and 0.2 M are the most consistent and reversible which
can also be observed on the graph (33).
Conclusion
The mineralogical details of a Nigerian termite hill soil
were reported with the aid XRF and SEM. We have also
determined the surface charge characteristics and CEC of
this termite hill soil in order to understand its sorptive
characteristics. Both the mineralogical compositions and
Fig. 11 Temkin adsorption isotherm for the sorption of Pb(II)
Table 4 Isothermal constants and correlation coefficients
b Qm Kf n B A R2
Langmuir 0.085 18.18 – – – 0.993
Freundlich – – 1.36 0.134 – – 0.972
Temkin – – – – 1.567 -0.22 0.985
Fig. 12 Pseudo-first order plot for the sorption of lead on termite hill
soil
Fig. 13 Pseudo-second order plot for the sorption of lead on termite
hill soil. t Time (min), qt quantity adsorbed at time t (mg/g)
380 J IRAN CHEM SOC (2012) 9:373–382
123
surface characteristics suggest that the termite hill soil
material is a good adsorbent in the class of oxides of metals
or manganate–silicate.
From the adsorption kinetics, the sorptive property of
the mound was found to be dependent on contact time, pH,
and ionic strength. The equilibrium adsorption data showed
satisfactory correlation with the Langmuir adsorption data
and was also found to fit the pseudo-second order kinetics.
Termite mound (soil) has also been found to have a high
efficiency for desorption and also for reuse even at low
concentrations of leachant.
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