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M. Aminul Haque*
A Statistical Comparison of Mathematical Modelsfor Heavy Metal Leaching Phenomena from
Solidified Landfill Waste MortarDOI 10.1515/cppm-2015-0046
Received October 28, 2015; revised December 30, 2015;
accepted December 30, 2015
Abstract:In this research, landfill solid waste was solidified
as cement-waste matrix to protect the environment from
excessive intrusive contaminants like Fe, Cu and Ni and
minimize the waste load. Within this context, ingredients
of cement-waste mortar were characterized to determine
their physical properties. Long-term feasibility study was
conducted to examine the metal contents stabilization by
employing the standard mass transfer-leaching test. The
cumulative leaching concentration of Fe, Cu and Ni were
found to be 1.29 mg/l, 0.18 mg/l and 0.63 mg/l respectively
up to 180 days static leaching test period that satisfied the
surface water quality standard. Mechanical strength test
was also conducted to characterize the solidification
technique. Five well-established non-linear mathematical
Models were conducted to evaluate the mechanisms of Fe,
Cu and Ni migration. Goodness of fit statistical parameter
analysis and visual examination indicated that polynomial
equation Model is better for explaining the experimentallygenerated data. Moreover, parameter of polynomial equa-
tion was extended from five to nine for examining the best
calibration profile to the observations. In context of slope-
intercept and visual observation analysis resulted that poly-
nomial equation based Model bearing five parameters with
0.5 power interval of each parameter describes the leaching
phenomena quite similar with the experimental observa-
tions whereas goodness of fit parameters and information
criterion shows reverse. It was found that the studied immo-
bilized landfill waste mortar have acceptable mechanical
performance that confirms to be used as construction
material.
Keywords: landfill waste mortar, leaching phenomena,
fitted models, statistical analysis, visual examination
1 Introduction
Landfill leachate is a significant source of ground water
pollution [1] that formed by decomposition of municipal
solid waste [2, 3] and excess rainwater percolating through
the waste layers [1, 2]. Leachates are highly concentrated
complex effluents which contain dissolved organic matters;
inorganic compounds, such as ammonium, calcium, mag-
nesium, sodium, potassium, iron, sulphates, chlorides andheavy metals such as cadmium, chromium, copper, lead,
nickel, zinc etc.; and xenobiotic organic substances [1, 46].
Especially presence of heavy metals in leachate have poten-
tial impact on human health and the quality of environment
having the greater possibility of surface and ground water
pollution [7].
The long-term safe landing of the solidified hazardous
waste is an important request for keeping the surrounding
environment more secure for the coming generations [8].
Therefore, solidification/stabilization (S/S) techniques
are used to minimize the immense pressure of waste load
in landfill sites and leachate production by reducing themobility as well as solubility of contaminants in wastes
and converts them into chemically inert form [9]. In S/S
process, the immobilization of the contaminants is achieved
by formation of chemical bonds and/or by physical encap-
sulation. This ensures the reduction of the quantity and
release speed of contaminants to the environment to a
large extent [10] and avoids a back release of contaminants
from the matrix during aggressive conditions of storage and
disposal [11]. Macroencapsulationworks in S/S by physically
entrapping contaminants within a large structural matrix
whereas microencapsulation entraps contaminants withinthe crystalline structure of solidified matrix at a microscopic
level [12] and incapable of chemical interactions [9].
Cementitious materials are widely used in waste man-
agement systems with different aims and requirements for
long-term performance. Both conventional and novel
cementitious materials are used to create reliable immobi-
lizing elements for safe storage and disposal of wastes.
Conventional cementitious materials such as Portland
cement and composite cements with supplementary cemen-
titious materials in the form of fly ash, iron blast furnace
*Corresponding author: M. Aminul Haque, Department of Civil
Engineering, Leading University, 5th Floor, Rangmahal, Bandar
bazar, Sylhet-3100, Bangladesh, E-mail: [email protected]
Chem. Prod. Process Model. 2016; aop
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added an additional conception of leaching phenomena.
The last stage of contaminant leaching mechanism
from waste matrix is the slow portion of dissolution
control the leaching phenomena. Moreover, the dissolu-
tion of materials from the surface proceeds faster that
the diffusion through the pores. Both the rapid and
slow portion of dissolution will result in the release ofhighly soluble materials but it will not cause depletion
of material.
For interpreting the contaminants leaching mechan-
ism from waste matrix, some researchers have been used
different non-linear Models. To identify the long term
leaching phenomena, some researchers [1720] provided
a Fickian diffusion based equation that is,
f =
Pana0
=2S
ffiffiffiffiffiffiffiffiffiffiDetn
p
V
ffiffiffi
p (1)
Where f = Cumulative fraction leached of heavy metals. Decan be calculated from the slope of an/A0 versus tn
1/2,
according to the following relationship:
De=
4 m2 V
S
2(2)
Where, m=
Pana0ffiffiffitn
pFrom eqs (1) and (2),
f = m
ffiffiffiffiffitn
p (3)
To generalize the Model equation (3) can be expressed as,
f = A0 + A1t1=2 (4)
As the diffusion rate gradually slow down with the
leaching period elapsed. Therefore, if the diffusion
path becomes longer, diffusion rate is not a controlling
factor in any of the leaching intervals. Some researchers
[2123] adopted polynomial equation based a semi-
empirical method to overcome this problem because
polynomial equation describes the long-term leaching
characteristics of a waste component. In this Model,
the cumulative amount of contaminant leached isexpressed by:
f = A0+ A1t1=2 + A2t (5)
Plecas [24] applied polynomial equation based Model up
to its fourth terms of this Model to observe the leaching
behavior of 137Cs from radioactive waste formation,
f = A0+ A1t1=2 + A2t + A3t
3=2 (6)
Similarly, Plecas and Dimovic [25] and Plecas and
Dimovic [26] used same Model up to its fifth terms for
characterizing the immobilization of industrial waste within
cement-bentonite clay matrix and transport phenomena of60Co from radioactive material respectively,
f = A0+ A1t1=2
+ A2t + A3t3=2
+ A4t2
(7)
In the current study, concentration of five heavy
metals like Fe, Cu, Ni, Cr and Cd were examined in land-
fill decomposed solid waste and effluent leachate. It was
observed that concentration of Fe, Cu and Ni exceeded
the Bangladesh standard [27]. Therefore, the aims of
present work is oriented to characterize the leaching
phenomena of Fe, Cu and Ni from waste matrices with
controlling leaching mechanism and predict the long-
term leaching phenomena by applying various non-linear
mathematical Models such as diffusion, polynomial,
logarithmic, exponential and power based equations.The performance of the prediction Models were measured
based on some statistical goodness of fit indicators with
the accuracy of 95 % confidence interval of the estimated
Model parameters.
2 Materials and methods
2.1 Experimental approach
In the current study, solidified waste mortar (SWM) speci-
men was prepared using stabilizing binding materials
like Ordinary Portland cement (OPC) and fine aggregate
such as sand and landfill decomposed solid waste
(LDSW). OPC and sand were collected from locally avail-
able areas. LDSW was collected from Matuail Sanitary
Landfill Site (MSLS), Dhaka, Bangladesh and prepared
through air drying, blending and sieving at room
temperature (25 1 C). Concentration of selected heavy
metals in LDSW and effluent leachate samples were
determined using flame emission atomic absorption spec-
trophotometer (AAS) (Spectra AA Varian). Physical char-
acteristics of specimen ingredients were measured
following the ASTM standard methods that are men-
tioned in Figure 3. Cubical specimen having the mold
dimensions of 5cm5cm5cm was prepared whereas
in each specimen 30 % of the total volume of fine aggre-
gate was replaced by LDSW [28]. Standard leaching
test method ANS 16.1 was used to observe the Fe, Cu
and Ni leaching phenomena from solidified waste form.
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Leaching tests were performed for 17, 14, 21, 28, 56, 90
and 180 days immersion period and results were recordedin terms of cumulative release in the curing leachant
versus curing ages. The compressive strength test, given
as applied maximum load divided by the cross-sectional
area of a specimen, was performed to confirm the struc-
tural integrity of solidified waste matrix. All tests were
performed three times to ensure the statistical signifi-
cance of the experimental data. Average value of each
test was presented in this study along with the standard
deviation. The overall experimental and analytical work-
ing steps are briefly depicted in Figure 3.
2.2 Fitting of the leachate Models
Five different well-known non-linear mathematical equa-
tion based Models were fitted as leachate Model to cali-
brate for demonstrating the leaching mechanism and
justify against the experimental observations showing
Collection of SWMBs
ingredients.
Collection of
effluent leachate
from landfill
leachate pond.
Measurement of heavy
metal concentration in
effluent leachate using
AAS.
Comparison of results
with the inland surface
water quality standard
[27].
Collection of
DSW
Digestion by
Aqua-regia
Solution (1:3).
Measurement of heavy
metal concentration in
LDSW sample using AAS.
Collection
MSLS
Sand and LDSW:
1. pH (Hevi-sand-TP283)
2. Dry density (ASTM-D2937-00)
3. Bulk density (ASTM C29)
4. Specific gravity (ASTM 128-15)
5. Porosity (Bowels, 1997)
6. Water content (ASTM D2216-80)
7. WAC (ASTM C 128-88)
8. FM (ASTM C136 96a)
OPC:
1. Fineness (ASTM C184-94)
2. Consistancy limit (ASTM C187)
3. Initial settting time (ASTM C150)
4. Final setting time (ASTM C150)
5. Specific gravity (IS -2720)Physical
property
analysis
1. Analysis of
oxides
2. Compressive
strength test at 3
and 7-day.
Grinding
Sieve
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heavy metal migration phenomena from SLWM. Fitted
non-linear Models are presented below:
1. Diffusion equation based Model (Generalize form):
f = A0 + A1t1=2 (4)
2. Polynomial equation based Model:
f = A0+ A1t1=2 + A2t (5)
3. Logarithmic equation based Model:
f =a +b l n t (8)4. Exponential equation based Model:
f =aebt (9)
5. Power equation based Model:
f =atb (10)
2.3 Parameter extension of well-fittedleachate Model
In this study, parameter of polynomial equation based
Model was extended in different longer terms with 0.5
and 0.25 intervals as trial basis using the least squares
procedure for demonstrating the best fit Model of
metal leaching mechanism in a better way with high
accuracy. The study adopted the following fitted Model
options such as Polynomial extended model one (PEMO),Polynomial extended model two (PEMT), Polynomial
extended model three (PEMTh), Polynomial extended
model four (PEMF), Polynomial extended model five
(PEMFv) and Polynomial extended model six (PEMS) as
trial basis to well calibrate with the experimental obser-
vations of Fe, Cu and Ni releasing data from SWM with
curing ages:
f = A0+ A1t1=2 + A2t 5 PEMO
f = A0+ A1t1=2 + A2t + A3t
3=2 6 PEMT
f = A0+ A1t1=2 + A2t + A3t3=2 + A4t2 7 PEMThf = A0+ A1t
1=4 + A2t1=2 + A3t
3=4 + A4t1 11 PEMF
f = A0+ A1t1=4 + A2t
1=2 + A3t3=4 + A4t
1 + A5t5=4 + A6t
3=2
12 PEMFv
f = A0+ A1t1=4 + A2t
1=2 + A3t3=4 + A4t
1 + A5t5=4
+ A6t3=2 + A7t
7=4 + A8t2
13 PEMS
The estimation of Model parameters was done following
non-linear techniques using MATLAB (R2015a).
2.4 Evaluation of fitted leachate Modelscalibration
Well calibration between the simulated data from fitted
Models and experimentally generated data from leaching
(Fe, Cu and Ni) test were evaluated using the most commonly
used statistical parameters like goodness of fit indicators and
information criteria. These are presented in Table 2.
3 Results and discussions
3.1 Heavy metal concentration in DSWand leachate samples
In the current study, concentration of five heavy metals like
Fe, Cu, Cd, Ni and Cr in LDSW and effluent (Outflowing to
the surface water body) leachate samples collected from
MSLS were examined. The average concentration of tested
heavy metals are presented in Table 3. In DSW, the study
observed that Fe was the highest concentration about
11,233.35 mg/kg at MSLS. Similar results of Fe concentration
was observed in landfill waste by Oluyemi et al. [42],
Mamtaz and Chowdhury [43] and Esakku et al. [44] about
4,130.02 mg/kg, 9,600 mg/kg and 20,485 mg/kg respec-
tively. Cu content was found greater about 260.675 mg/kg
than the observation of Esakku et al. [44], almost 169.9 mg/
kg. Moreover, the study revealed the significant level of restof the three tested metals such as Ni, Cr and Cd contents in
DSW as compared to the observations of Adjia et al. [45],
Mamtaz and Chowdhury [43] and Esakku et al. [44].
Though the average concentration of Cd and Cr in
outflowing treated leachate samples were observed to be
safety limit (Table 3) according to the BECR [27], the
contents of Fe, Cu and Ni were found not safe for disposal
to the near surface water body at landfill site, since they
exceed the Bangladesh standards that may be pointed
out a potential risk of metals entrance into food chain
through overflow of landfill site due to heavy rainfall
and leachate disposal to the surrounding environment.
Therefore, solidification/stabilization of landfill waste
may be a promising solution to prevent the metal intru-
sion and contamination into the environmental cycle.
3.2 Characteristics of SWM ingredients
As the LDSW was used as the partial replacement of sand in
the mortar specimen, physical properties of sand and LDSW
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were analyzed in mix condition to measure the values withquality parameters and the level of effectiveness and effi-
ciency for using waste as fine aggregate in constructional
purposes. The study revealed that water absorption capa-
city and moisture content in mix condition of study sample
were slightly higher due to the presence of LDSW. Waste
sample was organic matter which generally absorbs higher
water amount than inert material like sand. Otherwise, rest
of the examined parameters showed quite similar results
with the reported studies. Experimental results of SWM
ingredients characteristics are represented in Table 4.
Table 3:Concentration of heavy metals in DSW and effluent leachateof MSLS.
Heavy
Metal
DSW (mg/kg) Effluent
leachate
(mg/l)
Inland surface water
quality standard
(mg/l) []
Fe ,. . . . .
Cu . . . . .
Ni ,. . . . .
Cr . . . . .
Cd . . . . .
Table 2: Goodness of fit indicators for the selection of fitted model.
Parameter Expression Reference
Correlation coefficient (r) r= n
Pxy
Px Py ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi
nP
x2 Px 2q ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffin Py2 Py 2q []
Coefficient of determination (R-squared) R2 =Pn
i=0 Oi
O pi p ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiPni=0
Oi O 2q ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiPn
i=0 pi p 2
p0@ 1A2
; oi = Observed data pi = Predicted data [,]
Adjusted R-squared R2 = n 1 SSEn k SST; Here, n = Nos. of observations, k = Nos. parameter in model,
SSE = Sum of squares error; SST= Total sum of squares.
[]
NashSutcliffe efficiency(NSE) NSE = 1
PNi= 1
oi pi 2PNi =1
Oi O 2; = Mean of observed data [,]
Coefficient of persistence (cp) cp = 1
PNi= 2
oi pi 2PN 1i= 1
Oi +1 O 2 []
Index of Agreement (d) d= 1
PNi=1
Oi pi 2
PN
i=1 pi Oj j + Oi Oj j 2 [,]
Kling-Gupta Efficiency (KGE) KGE = 1 ED []
ED =
ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffis 1 r 1 2 + s 2 vr 1 2 + s 3 1 2
qr = Person product moment correlation coefficient
= s=o
vr = , method= 2009, method=2012
= s=0
= CVsCV0
= s=s0=0
Root mean square error (RMSE) rmse =
ffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffiffi1N
PNi= 1
Oipi 2s
[]
Percent bias (PBIAS) PBIAS= 100*PN
i=1 oipi
PNi=1 Oi []Weighted coefficient of determination (wr) wr2 = |b|R2, |b| 1; br2 = R
2
bj j, b>1; b = Slope of the regressionline between observed and predicted data
[,]
Akaike Information Criteria (AICc) (Second
order). Generally used when n/k < .
AICC = 2 ln L + 2K+ 2K K+ 1 n K 1 ; ln(L) = Likelihood function for the model,n = Number of observations, K = Number of estimated parameters
of the model.
[,]
Schwarz Bayesian Information Criteria (SBIC) SBIC = 2 ln L + Kln n [,]HannanQuinn information criterion(HQC) HQC = 2 ln L + 2Kln ln n []Mallows Cp Cp = RSS
2 n 2k; RSS = Residual sum of squares,
2 = Residual mean square error.
[]
6 M. A. Haque: Statistical Comparison of Mathematical Models
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In the study OPC was used as stabilizing agent. The
chemical compositions and different properties of OPC
are given in Table 5, which were analyzed in the labora-
tory. The examined results showed the quite well as
compared with the standard and reported studies that
ensured as a binding material to be used for the solidified
waste mortar.
3.3 Leaching characteristics of Fe, Cuand Ni ions
Leaching is generally considered as the basic criterion to
evaluate the safety, acceptability and the chemical beha-
vior of the final waste forms in the disposal site [52]. The
cumulative migration characteristics of Fe, Cu and Ni
from Solidified waste mortar block (SWMB) to curing
leachant with the increases of curing ages are shown in
Figure 4. It could be noticed clearly from Figure 4 that the
rate of Fe, Cu and Ni release contents were high at early
ages of leaching and then decreased with the increases in
leaching duration. The cumulative releasing behavioral
curves of Fe, Cu and Ni can be characterized by three
distinct regions. 1st region from 1 to 7 days, observed
highest leaching trend ranges from 0.483 mg/l to 0.951
mg/l, 0.039 mg/l to 0.108 mg/l and 0.166 mg/l to 0.416
mg/l for Fe, Cu and Ni respectively. 2nd region from 7 to56 days, slightly lower releasing content was found than
1st region whereas drastic reduction of metal releasing
Table 4: Physical characteristics of mixed MLSW and sand as fine
aggregate.
Parameters Experimental
values
References
Dry density (gm/cm) . . .[]
Bulk density (gm/cm) . . .[]Specific gravity . . .[, ]
Water absorption capacity (%) . . .[, ]
Moisture content (%) . .[]
Porosity (%) . []
Fineness modulus . . ..[]
pH . .
Table 5: Properties and chemical analysis of OPC.
Parameters Experimental values References
Physical property
Fineness (%) . . not less than % (ASTM standard)
Consistency Limit (%) . . % % by weight (ASTM standard)
Initial setting time (min.) not less than minutes (ASTM standard)
Final setting time (min.) not more than minutes (ASTM standard)
Specific Gravity . . .[IS: (Part -)]
Mechanical property
Compressive strength (MPa)
days . . Minimum .(ASTM standard)
days . . Minimum .(ASTM standard)
days . . Minimum .(ASTM standard)
Chemical composition (%)
Oxides
CaO . []
SiO . []
AlO . .[]
FeO . .[]
SO . Maximum .(ASTM standard)
MgO . Maximum .(ASTM standard)
Loss on Ignition (LOI) . Maximum .(ASTM standard)
Insoluble Residue (IR) . Maximum .(ASTM standard)
NaO + .KO . Maximum .(ASTM standard)
Free Lime (FCaO) .
Mineral composition (%)
CS . (Test results by ASTM C )
CS . (Test results by ASTM C )
CA . (Test results by ASTM C )
CAF . (Test results by ASTM C )
LSF . % []
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tendency or quite steady state condition observed in 3rd
region from 56 to 180 days curing ages.
The study revealed the cumulative leaching concentra-
tion of Fe, Cu and Ni were about 1.29 mg/l, 0.18 mg/l and
0.63 mg/l respectively up to 180 days static leaching testperiod that satisfied the surface water quality standard [27]
by using the mixing proportion of 1:2. These leaching results
ensured the potentiality of waste product as reusable with
environmental safety. The leach incremental rate of Fe, Cu
and Ni with the development of waste mortars compressive
strength over the examined period are graphically depicted
in Figure 5. Before the immersion of waste mortar block in
curing leachant, ionic species contents are fully encapsu-
lated or entrapped within the waste matrix. At the initial
contact time of curing, incremental rate of each ion release
was high. This trend could be attributed to the washout
of the loosely bounded surficial compounds of the waste
block [52]. When each ion has been leached out from the
surface of the block [16] incremental rate dramatically
reduced in release from 1st region to 2nd region that is
maintained over a longer period of curing time (Up to 180
days) by longer pathways from the bulk through diffusion-
controlled stage, which determines the long term leaching
behavior of the block [15, 16]. Even the study observed
that the rate is reduced to about zero in the 3rd region
from 56 to 180 days curing ages. Similar results were
observed in some reported studies in the literature [15, 53].
Moreover, a major reason of metal ion release rate
reduction is that compressive strength of waste mortar
block increases over the curing age due to the hydrationof binding material like OPC (Figure 5). Compressive
strength and structural integrity bond develops for the
hydration of OPC with the presence of water. The metal
ion species are strongly captured and pore spaces in
waste forms decreased day by day. Therefore, migration
rate of metal ion contents are impeded from SWMB
through diffusion.
3.4 Controlling leaching phenomenaof Fe, Cu and Ni
In some reported studies [1517, 54] the contaminant
content releasing phenomena from waste forms are char-
acterized by three distinct parts such as surface-wash off,
diffusion and dissolution. But under the which region
contaminants leachates from the waste matrices in the
duration of leaching, to determine it, some researchers
[53, 55, 56] indicated that controlling leaching mechanism
could be conducted based on the slope of the linear
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 20 40 60 80 100 120 140 160 180 200
Leaching
ofHeavymetal(mg/l)
Curing age (Day)
Fe (mg/l)
Cu (mg/l)
Ni (mg/l)
Figure 4: Cumulative leaching characteristics of Fe, Cu and Ni from SWMB.
0
5
10
15
20
25
30
0
0.03
0.06
0.09
0.12
0.15
0.18
0.210.24
0.27
0 20 40 60 80 100 120 140 160 180 200
CSofSWMB(MPa)
Incrementalrate(mg/d)
Curing age (Day)
Fe
Cu
Ni
CS
Figure 5: Leaching incremental rate of Fe, Cu and Ni with CS development and curing age.
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regression of the logarithm of CLF versus the logarithm of
time. If the slope is less than 0.35 the controlling leaching
mechanism will be the surface wash-off, for the slope
values ranging from 0.35 to 0.65 the controlling mechan-
ism will be the diffusion, and higher slope values repre-
sent the dissolution mechanism [10, 53, 57]. The plots of
the log(Fe, Cu and Ni concentration) versus log(Curingduration) are shown in Figure 6. From the result of the
linear regression for Fe, Cu and Ni leaching content using
logarithm, it can be clearly concluded that the values of
the correlation factor (R2) have high values for three
tested metal ions leaching. The values of the slopes for
Fe, Cu and Ni are less than 0.35 (Figure 6) which indicate
that surface wash-off govern the leaching phenomena.
That means Fe, Cu and Ni contents only migrated from
the surface of studied waste mortar during the whole
curing period that confirms the studied waste mortar
can be catalogued as sustainable potential re-usable
material in the construction field.
3.5 Calibration of fitted leachate Model
and parameter estimation
The prediction of Fe, Cu and Ni transport phenomena trend
(Figure 4) from the studied SWMB, the experimental lea-
chate data of Fe, Cu and Cu were fitted to the five non-
linear equation based Models such as diffusion equation
(DE), polynomial equation (PE), logarithmic equation (LE),
exponential equation (EE) and power equation (Power E) as
illustrated in Figures 79. From the visual observation of
Figures 79, it could be concluded that for the studied
y = 0.1807x 0.2118
R2= 0.8504
y = 0.299x 1.305
R2= 0.8862
y = 0.2601x 0.6794
R2= 0.8742
1.5
1.3
1.1
0.9
0.7
0.5
0.3
0.1
0.10.3
0 0.25 0.5 0.75 1 1.25 1.5 1.75 2 2.25 2.5
Log(Heavymetalcontent)
Log (Curing age)
Fe
Cu
Ni
Figure 6: Controlling leaching phenomena identification of Fe, Cu and Ni.
0
0.5
1
1.5
2
0 20 40 60 80 100 120 140 160 180 200
LeachingofFe(mg/l)
Curing age (day)
Fe
DE
PE
LE
EE
Power E
Figure 7: Calibration of non-linear models with the Fe leaching concentration.
0
0.05
0.1
0.15
0.2
0.25
0.3
0 20 40 60 80 100 120 140 160 180 200
LeachingofCu(mg/l)
Curing age (day)
Cu
DE
PE
LE
EE
Power E
Figure 8: Calibration of non-linear models with the Cu leaching concentration.
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waste matrix, the DE, LE, EE and power E Model cannot
represent the experimental observations adequately during
the whole examined curing period. In every cases, the
polynomial equation based Model were found to be suc-
cessful and quite good for demonstrating the experimental
releasing behavior of metal ion contents from the wastematrix. Although metal ion species releasing phenomena
associated with the matter of diffusion based, diffusion rate
is not a controlling factor because the diffusion path was
longer. The reason is that diffusion rate rapidly occur at the
initial period but gradually slow down with the leaching
time elapsed. Moreover, LE, EE and power E Model under-
estimates the releasing profile of Fe, Cu and Ni that shows
unrealistic leaching pattern (Figures 79). In order to assess
the better calibration statistically of the leachate Models to
the experimental observations, goodness of fit indicators
like R2 and RMSE values were calculated which are shown
in Table 6. Statistical analysis shows that polynomial equa-tion Model have ability to explain each data point for that
matter R2 was found greater and RMSE also lower as com-
pared to the other fitted Models.
3.6 Statistical comparison of fitted PEModels for well calibration
Several techniques have been used by the previous
researchers to provide a comparison between the simulated
and measured data. In the study, quantitative and graphical
technique were used to evaluate the better demonstrating
leachate Model of Fe, Cu and Ni from the SWMB. Graphical
technique provide a visual comparison and a first overview
of Model performance [33, 58] and are essential to appro-
priate Model evaluation [29, 31].
3.6.1 Goodness of fit indicators
The number parameters of the fitted PE Model were
extended in different terms as trial basis for the well cali-
bration to the experimentally generated leaching data of Fe,
Cu and Ni (Figure 4). From the visual examination of
Figures 1012, it is clearly seen that PE Models shows
comparatively better calibration with the increases of para-
meter from 3 to 5 (From PEMO to PEMTh). But reverse result
is seen for further extension of parameters. PE Model with 7
and 9 parameters (PEMTFv and PEMS) are shown deviated
profile with the experimental metal release contents. The
visual analysis revealed that PEMTh and PEMF with 5 para-
meters shows well calibration by comparison whereas
PEMTS with 9 parameters cannot represent the experimen-
tal data adequately (Figures 1012) that describes the most
unrealistic predicted pattern. For the selection of PE based
well calibrate leachate Model among the six fitted, the
statistical analysis using goodness of fit parameters are
shown in Table 6 that measure the how well the experi-
mental data points fit the PE based regression Models. Inthe study, goodness of fit parameters are calculated using
the simulated data predicted from PEMO to PEMTS and
experimental observed data. The analysis shows a specific
trend that is, fitting the experimental leaching data of Fe, Cu
and Ni to the fitted PE Modelsresulting in a high accuracy of
each statistical parameter with the increases of parameters
from PEMO to PEMTS, which confirm that PEMTS is better
than other Models to represent the leaching data (Table 7).
However, it is quite reverse result than visual examination.
The reason behind that if the parameter of PE based Model
Table 6: Statistical evaluation of fitted leachate models for Fe, Cu
and Ni.
Heavy
metal
Parameter DE PE LE EE Power E
Fe R . . . . .
RMSE
.
.
.
.
.
Cu R . . . . .
RMSE . . . . .
Ni R . . . . .
RMSE . . . . .
0
0.2
0.4
0.6
0.8
1
0 20 40 60 80 100 120 140 160 180 200
LeachingofNi(mg/l)
Curing age (Day)
Ni
DE
PE
LE
EE
Power E
Figure 9: Calibration of non-linear models with the Ni leaching concentration.
10 M. A. Haque: Statistical Comparison of Mathematical Models
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increases, it explainsor touch the each data point in a better
way but deviates from the original smooth curve line of
experimental data. As the simulated data predicted by
PEMTS are almost near to experimental observations, there-fore goodness fit parameters of PEMTS shows better results
than other fitted Models.
3.6.2 Model selection based on information criteria
The Model selection problem can be tackled using a tradi-
tional approach in which parameter learning is repeated on
a set of candidate Model scales among which one is selected
by a Model selection criterion [39] like AIC, SBIC, HQC and
Mallows cp. AIC means the Akaike Information Criterion
that is useful in selecting the best Model in the set [36]. In
addition, AIC is designed to select the Model that will pre-
dict best and is less concerned with having a few too manyparameters. Schwarz Bayesian Information Criterion (SBIC)
is designed to select the true values of parameters exactly
like AIC. SBIC can be used to compare in sample or out
of sample predicting performance of a Model. The
Hannan-Quinn Criterion (HQC) for identifying an autore-
gressive Model denoted by HQ (p) was introduced by
Hannan and Quinn (1979). The best Model is the Model
that corresponds to minimum HQC [59]. These criteria
attempt to select a Model with small generalization error,
by trading off between the likelihood-based goodness of fit
0.5
0.7
0.9
1.1
1.3
1.5
0 20 40 60 80 100 120 140 160 180 200
Con
centrationofFe(mg/l)
Curing age (Day)
Fe
PEMO
PEMT
PEMTh
PEMF
PEMFv
PEMS
Figure 10: Calibration of PE Models for demonstrating the Fe migration phenomena.
0
0.05
0.1
0.15
0.2
0.25
0.3
0.35
0.4
0 20 40 60 80 100 120 140 160 180 200
ConcentrationofCu(mg/l)
Curing age (Day)
Cu
PEMO
PEMT
PEMTh
PEMF
PEMFv
PEMS
Figure 11: Calibration of PE Models for demonstrating the Cu migration phenomena.
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
0 20 40 60 80 100 120 140 160 180 200
Concentra
tionofNi(mg/l)
Curing age (Day)
Ni
PEMO
PEMT
PEMTh
PEMF
PEMFv
PEMS
Figure 12: Calibration of PE Models for demonstrating the Ni migration phenomena.
M. A. Haque: Statistical Comparison of Mathematical Models 11
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and Model complexity subject to noise and uncertainty in a
finite number of observations [39]. In the current study,
statistical analysis using information criterion including
AIC, SBIC, HQC and Mallows cp for Model selection
shows the similar results with the goodness of fit para-
meters and contrast with visual observation. In addition,
the study found a trend for PE Models that is, the lowernumber of parameters the lower value of AIC, SBIC, HQC
and Mallows cp. Generally, the Model bear the compara-
tively lower value of AIC, SBIC, HQC and Mallows cp is
selected as the better Model. The calculated values from the
analysis of AIC, SBIC, HQC and Mallows cp (Table 8), it is
clearly seen that PEMO shows the lowest values. Therefore,
according to the principle, PEMO is better Model to repre-
sent the Fe, Cu and Ni leaching data than other fitted
Models that is opposite result of visual examination.
3.6.3 Slope and y-intercept
The slope and y-intercept of the best-fit regression line can
indicate howwellsimulateddata match with measured data.
The slope indicates the relative relationship between the
simulated and measured data. The y-intercept indicates the
presence of a lag or lead between Model predictions andmeasured data, or that the data sets are not perfectly aligned
[29, 60]. The current study compared the well calibration
between the simulated PE Models curves to the experimen-
tally measured data of Fe, Cu and Ni ion leaching curves
(Figures 1012) using slope and y-intercept of the best-fit
regression line which are shown in Table 9. The slope and
y-intercept of the simulated curves were calculated by three
distinct parts based on the three regions which is already
mentioned in Section 3.3. The comparative analysis shows
Table 7: Model evaluation based on goodness of fit parameters.
Parameter Heavy metal PEMO PEMT PEMTh PEMF PEMFv PEMS Standard range
r Fe . . . . . . [, + ]
Cu . . . . . .
Ni . . . . . .
R-squared Fe . . . . . . to
Cu . . . . . .
Ni . . . . . .
Adjusted R-squared Fe . . . . . . to
Cu . . . . . .
Ni . . . . . .
NSE Fe . . . . . . and .
Cu . . . . . .
Ni . . . . . .
cp Fe . . . . . . to
Cu . . . . . .
Ni . . . . . .
d Fe . . . . . . to Cu . . . . . .
Ni . . . . . .
KGE Fe . . . . . . and .
Cu . . . . . .
Ni . . . . . .
rmse Fe . . . . . . Minimum value is taken.
Cu . . . . . .
Ni . . . . . .
pbias Fe . Optimal value is
Cu . . .
Ni
br Fe . . . . . . Maximum value is
Cu . . . . . .
Ni . . . . . .
12 M. A. Haque: Statistical Comparison of Mathematical Models
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that slope and y-intercept values of simulated curve by
PEMTh are quite similar with the Fe, Cu and Ni ion leaching
curves (Table 8). Moreover, it can be concluded that PEMTh
can demonstrate the experimental metal ion leaching con-tents profile with curing ages quite well than other five fitted
PE Models. Although PEMTF can explain approximately
the phenomena but PEMTh can better that result shows
similar with the visual examination of the figures whereas
the goodness of fit parameters and information criterion
measures opposite results. So, the study suggests based on
the visual examination and comparison results using slope
andy-intercept,PEMThcanbe used to represent the leaching
phenomena.
The accuracy of the PE Models calibration result was
justified through statistical comparison. Goodness of fit
parameters and information criterion were calculated
using the statistical software R.
3.7 Statistical significance test ofwell-calibrated PE Model parameters
The parameter estimation outcomes of well-calibrated
PEMTh for Fe, Cu and Ni are presented in the Table 10.
Parameters were calculated with their 95 % confidence
Table 8: Model selection based on statistical information criteria.
Parameter Heavy metal PEMO PEMT PEMTh PEMF PEMFv PEMS Standard value
AIC Fe . . . . . . Minimum value is taken
Cu . . . . . .
Ni . . . . . .
SBIC Fe . . . . . .Cu . . . . . .
Ni . . . . . .
HQC Fe . . . . . .
Cu . . . . . .
Ni . . . . . .
Mallows cp Fe . . . .
Cu . . . . . .
Ni . . . . . .
Table 9: Comparison of slope and intercept between the experimental observations and fitted PE models.
Parameter Heavy metal Curing days Experimental observation PEMO PEMT PEMTh PEMF PEMFv PEMS
Slope Fe to . . . . . . .
to . . . . . . .
to . . . . . .
Cu to . . . . . . .
to . . . . . . .
to .
Ni to . . . . . . .
to . . . . . . .
to . . . . .
Intercept Fe to . . . . . . .
to . . . . . . .
to
.
.
.
.
.
.
.
Cu to . . . . . . .
to . . . . . . .
to . . . . . . .
Ni to . . . . . . .
to . . . . . . .
to . . . . . . .
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interval. The study tested the statistical significance level
of each parameter using t and p-value statistics. The t-
value measures the ratio between the coefficient and its
standard error whereas p-value quantify the statistical
significance level of parameter. If the p-value of each
parameter is less than the significance level (e. g., p A3 >
A4 > A1 > A5.
3.8 Statistical prediction boundsof well-calibrated PE Model
Statistical prediction bounds of PEMTh with 95 % confi-
dence intervals for Fe, Cu and Ni are presented in the
Figures 1315 respectively. Each figure contains the three
curves such as the fit, the lower confidence bounds, and the
upper confidence bounds. The confidence interval consists
of the space between the two curves (dotted lines).The fit
means fitted of PEMTh to the experimentally generated data
and the bounds reflect a 95 % confidence level. Confidence
interval with 95% means there is a 95% probability that the
fitted line of PEMTh for the Fe, Cu and Ni leaching data will
lie within the confidence interval.
Table 10: Estimated parameters of model 03 with statistical significant test.
Heavy metal Parameter Estimate Std. Error t-stat p-value Range of p-value
Fe A . . . . Significance level ifp < .
A . . . and
A . . . . Insignificance level ifp > .
A . . . .A . . . .
Cu A . . . .
A . . . .
A . . . .
A . . . .
A . . . .
Ni A . . . .
A . . . .
A . . . .
A . . . .
A . . . .
Figure 13: Fitted prediction PEMTh for Fe leaching contents with 95 % prediction bounds.
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4 Conclusion
Fe, Cu and Ni leaching phenomena from solidified landfill
waste matrices were evaluated by performing static leach-
ing tests. The major conclusions pertaining to the findings
presented herein may be drawn from this research:
(1) The leaching contents of studied metal ions were
substantially reduced from waste matrices at
28 days curing age and similar result observed up
to 180 days that confirms the waste mortar block
to be used as an environmental friendly re-usable
product.
(2) Compressive strength test result was found quite satis-factory value 19.1 MPa at 28 days curing age that fulfill
the paving block standard (15 Mpa) in Bangladesh.
(3) The only surface wash off leaching phenomena was
found to control Fe, Cu and Ni leaching contents
that ensure the safe disposal of the product.
(4) By fitting the experimentally generated data to some
well-established non-linear models, it was revealed by
the visual examination and statistical analysis that the
migration phenomena of the studied metal ions from
landfill waste mortar block can be represented quite
well by semi-empirical Model PE for longer period.(5) From the statistical analysis, it was found that PE
Model bearing five parameters (PEMTh) with 0.5
power interval with each parameter can well explain
the leaching phenomena during the whole immersion
period in leachant that fails to prove using goodness of
fit indicators and information criteria like AIC, SBIC,
HQC and Mallows cp.
(6) Experimental leaching behavior of Fe, Cu and Ni
versus curing age can quite describe using slope
and intercept of the fitted PEMTh curves.
(7) It is recommended that the outcome of the study may
be a potential solution to recycle the landfill waste as
re-usable by product like paving blocks, road construc-
tion materials, etc. using S/S process.
Acknowledgements: The Author would like to acknowl-
edge the authority of Dhaka City Corporations for the
permission to collect the decomposed solid waste and
leachate samples from Matuail Sanitary Landfill Site.
Figure 14: Fitted prediction PEMTh for Cu leaching contents with 95 % prediction bounds.
Figure 15: Fitted prediction PEMTh for Ni leaching contents with 95 % prediction bounds.
M. A. Haque: Statistical Comparison of Mathematical Models 15
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