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Article
A Robust Model for Determination of Wax Deposition in Oil SystemsArash Kamari, Abbas Khaksar-Manshad, Farhad Gharagheizi, Amir H. Mohammadi, and Siavash Ashoori
Ind. Eng. Chem. Res., Just Accepted Manuscript • Publication Date (Web): 27 Sep 2013
Downloaded from http://pubs.acs.org on September 28, 2013
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1
A Robust Model for Determination of Wax Deposition in Oil
Systems
Arash Kamari,a Abbas Khaksar-Manshad,
b Farhad Gharagheizi,
a,c Amir H.
Mohammadi,,a,d
Siavash Ashoori, e
a Thermodynamics Research Unit, School of Engineering, University of KwaZulu-Natal, Howard College Campus,
King George V Avenue, Durban 4041, South Africa
b
Department of Petroleum Engineering, Abadan Faculty of Petroleum Engineering, Petroleum University of
Technology, Abadan, Iran
c Department of Chemical Engineering, Buinzahra Branch, Islamic Azad University, Buinzahra, Iran
d Institut de Recherche en Génie Chimique et Pétrolier (IRGCP), Paris Cedex, France
e Department of Petroleum Engineering, Petroleum University of Technology, Ahwaz, Iran
Abstract –Wax deposition is a serious problem during oil production in the petroleum
industry. Therefore, accurate predicting this solid deposition problem can result in increasing the
efficiency of oil/gas production. In this communication, a novel approach is proposed to develop
a predictive model for estimation of wax deposition. An intelligent reliable model is proposed
using a robust soft computing approach namely least square support vector machine
(LSSVM) modeling optimized with coupled simulated annealing (CSA) optimization
approach. The results of prediction operation demonstrate that there is good agreement between
the estimation of CSA-LSSVM and the experimental data of wax deposition. Furthermore, the
performance of the newly developed model is compared with the performance of the neural
network and multi-solid models for wax deposition prediction. Results of this comparison
indicate that the proposed method is superior, both in accuracy and generality, over the multi-
solid and neural network models. Finally, to check whether the newly developed CSA-LSSVM
model is statistically correct and valid, Leverage approach, in which the statistical Hat matrix,
Williams plot, and the residuals of the model results lead to identification of the probable
outliers, is applied. It is found that all of the wax deposition experimental data used in the present
study seem to be reliable and only one point of them is out of applicability domain of the
developed models for wax deposition.
Keywords: Wax deposition; Multi-solid Modeling; LSSVM; Coupled Simulated Annealing.
Corresponding authors Email: [email protected]
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1. Introduction
Wax deposition is a serious problem in the petroleum industry because it may result in
decreasing the efficiency of oil production, the plugging of well bores, production facilities and
transportation pipelines during production and even reservoir rock 1-3
. Without an appropriate,
accurate and detailed wax management program which it can be achieved by correctly predicting
this solid deposition problem, the production of oil with high wax content can result in reduced
amounts of productions, shutdown, and severe economic losses due to production loss and costly
remediation. This justifies the necessity for a reliable model that accurately estimates the amount
of precipitated wax deposition.
To design production processes efficiently, it is of great importance to predict the amount
of precipitated wax and wax appearance/disappearance temperatures (WAT/WDT) using a wax
model 2. Therefore, a reliable model is required to estimate the wax deposition, as already
mentioned. Burger et al. 4 presented one of the commonly used thermodynamic models in which
the crude oil is dissolved in a solvent mixture (ether/acetone), cooled at 253 K and filtered
afterwards at this temperature. This method is widely accepted to represent the total amount of
wax able to precipitate in a crude oil. Among thermodynamics methods, the multi-solid phase
one is frequently used in the literature 3. In multi-solid (MS) wax model developed by Lira-
Galeana et al. 5, each solid phase is considered as a pure component which does not mix with
other solid phases. Valinejad and Solaimany Nazar 6 conducted an experimental work to
determine the wax deposition potential of three waxy crude oils during laminar flow in a pipeline
system. The Taguchi experimental design approach is applied to evaluate the impact of important
operating factors such as inlet crude oil temperature, temperature difference between the oil and
the pipe wall, the flow rate of crude oil, wax content and time on wax precipitation phenomena.
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The obtained results indicated that a waxy crude oil with higher wax content could lead the more
precipitated solid wax in transportation lines. Akbarzadeh and Zougari 7 developed a novel
strategy for modeling wax deposition in fluid flows. They considered several mechanisms as
possible mechanisms in the wax deposition process. Among these mechanisms, particle
diffusion/deposition played the most significant role in formation of the deposit at the realistic
transport conditions. Bai and Zhang 8 applied the vane method to determine the yield stress of
waxy oil gels formed under quiescent or shear conditions, in which an implemented shear stress
maintained during the process of cooling and isothermal holding. The obtained results
demonstrated that the yield stresses dramatically decrease with increase of average carbon
number of wax regardless of the quiescent or shear conditions. Kelechukwu et al. 9 proposed an
empirical model for estimating wax precipitation of hydrocarbon production systems. The model
exhibited good estimation ability in comparison with the laboratory measurements.
However, thermodynamic models estimate wax formation conditions which are not in
excellent agreement with experimental data, and they normally over or under-estimate the
amount of precipitated wax and WAT/WDT 1. Three types of experiments were undertaken
10:
(1) wax crystallization experiments on live oil to define the conditions under which wax would
deposit, (2) diffusion precipitation experiments on dead oil to determine the contribution of wax
diffusion to precipitation rates under various conditions, and (3) shear precipitation experiments,
also on dead oil, to identify the rate of transport of deposited wax particles to the wall.
Consequently, experimental measurements require special equipment along with expensive,
difficult and time-consuming procedures. Therefore, introducing a rapid and accurate method
than the experimental measurements and the thermodynamic models which can solve the
aforementioned problems is necessary.
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Intelligent methods such as the Artificial Neural Network (ANN), Support Vector
Machine (SVM), Genetic Algorithms (GA), Fuzzy Logic (FL) and etc for data analysis and
interpretation are increasingly powerful and reliable tools that can be used in order to estimate
regression and classification problems 11-16
. Least Square Support Vector Machine (LSSVM) 17
is a modification of the original SVM mathematical approach. This method uses a set of linear
equations using support vectors (SVs) instead of quadratic programming problems in order to
facilitate the solution of the original SVM. So far, LSSVM methodology has been used for
several estimation targets in petroleum engineering18-22
. However, this intelligent mathematical
approach has not yet been applied for performance prediction of wax deposition in crude oil
systems.
This study presents a new model for the estimation of wax deposition in oil systems
based on LSSVM modeling approach using available data set collected from previously
published literature23-25
. Moreover, a novel feature selection mechanism base on Coupled
Simulated Annealing (CSA) optimization for tuning the optimal parameters is proposed. The
CSA-LSSVM model is an adequate nominee for characterizing the nonlinear behavior and
prediction of physical properties such as wax deposition. To evaluate the performance and
accuracy of the newly proposed model as well as previously published ones, both statistical and
graphical error analyses are applied simultaneously. Next, wax deposition predicted and in order
to observe the superiority or failure of our model than traditional methods, the results are
compared with the performance of multi-solid model for wax deposition and the experimental
data as well as ANN model. Finally, Leverage approach, in which the statistical Hat matrix,
Williams Plot, and the residuals of the model results lead to identification of the probable
outliers, is implemented.
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2. Experimental Data Acquisition
In general, the applicability, reliability and accuracy of the models for estimation of
physical properties and phase behaviors of fluids depends on the comprehensiveness of the
employed data set for their development 12, 26-29
. Therefore, the most important parameters which
affect deposition of wax must be selected. The change of oil composition, pressure and
temperature may cause deposition of wax 2.
As previously mentioned, wax deposition is one of the most important flow assurance
problems30
. The data used in this study 23-25
include nine parameters that also indicate
thermodynamic properties of the oil systems. These input parameters include compositions of
C1-C3, C4-C7, C8-C15, C16-C22, C23-C29, C30+, specific gravity, system pressure, and system
temperature and output parameter is wax deposition. The parameter ranges are shown in Table 1.
The weight percent of precipitated wax is defined as a function of temperature (T), pressure (P),
composition, and specific gravity of oil.
3. Model Development
3.1 Support Vector Machine Strategy
Although the neural network models have been generally examined to provide high
accuracy 31, 32
, they may have the disadvantages of non-reproducibility of results, partly as a
result of random initialization of the networks and variation of the stopping criteria during
optimization 20
. The SVM mathematical strategy has been recognized as a consistent and
effective method proposed from the machine-learning community 17, 33
. There are several criteria
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which may demonstrate the superiority of SVM-based models than the ANN-based methods
including more probability for convergence to the global optimum, no need to identify the
network topology in advance, which can be automatically determined as the training process
ends, over-fitting complications are less probable in SVM strategies, no need to choosing the
number of hidden neurons, acceptable generalization performance, and fewer adjustable
parameters (the developed model in this study has only two adjustable parameters 17, 34, 35
).
Summary of ANN-based models performance is explained in Appendix A.
A SVM is a tool for a set of related supervised learning techniques which analyze data and
recognize patterns and are also utilized for regression analysis. In other words, the SVM strategy
has been preliminary proposed for classification problems using the hyper-planes to define
decision boundaries between the experimental data points of different classes 17
. On the basis of
SVM primary formulations any function f(x) can be regressed as follow36
:
bwxf T (x))( (1)
where Tw is transposed output layer vector, )(x represents the Kernel function, and b stands
for the bias. The input of the model, x, is of a dimension N×n in which N and n express the
number of data points and number of input parameters, respectively (In case of training set, N
may be regarded as the number of training set data points). Vapnik proposed minimization of the
following cost function in order to calculate w and b 36
:
N
k
kk
T cw function Cost1
* )(2
1
(2)
To satisfy constraints:
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N1,2,....,k
N1,2,....,k ybxw
N1,2,....,k bxwy
kk
kkk
T
kk
T
k
,0,
,)(
,)(
*
*
(3)
where kk y and x stand for k
th data point input, and k
th data point output, respectively. The ε
denotes the fixed precision of the function approximation. The k and *
k are slack variables. It
should be considered that if we choose a small ε to propose a very accurate model, some data
points may be outside of the ε precision. Consequently, this issue may result in infeasible
solution. Accordingly, one should utilize slack parameters to determine the allowed margin of
error. The 0c in Eq. (2) is considered as the tuning parameter of the SVM which determines
the amount of the deviation from the desired ε. In other words, one of the tuning parameters of
the SVM is c. To minimize the cost function illustrated in Eq. (2) along with its constraints
defined in Eq. (3), one should use the Lagrangian for this problem as follows 36
:
N
k
kkk
N
k
kklkll
N
lk
kk aayaaxxKaaaaaaL1
*
1
**
1,
** ,2
1,
caa ,aa kk
N
k kk ,0,0 *
1
*
N1,2,...,k xxxxK l
T
klk ,,
(4)
(4a)
(4b)
where ak and ak* denote Lagrangin multipliers. Eventually, the final form of the SVM is obtained
as follows:
bxxKaaxf k
N
lk
kk
),()()(1,
*
(5)
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To solve the problem and find b and a a kk ,, * , one should solve a quadratic programming
problem which is immensely difficult. Later, Suykens and Vandewalle 17, 37
developed the least
square modification of the SVM (LSSVM) to facilitate the original SVM method. In the
developed LSSVM approach, Suykens and Vandewalle 17, 37
reformulated the SVM as follows 36
:
N
k
k
T eww function Cost1
2
2
1
2
1 (6)
Subjected to the following constraint:
kk
T
k ebxwy
(7)
where γ is tuning parameter in LSSVM method and ek represents the error variable. The
Lagrangian for this problem is as follows:
N
k
kkk
T
k
N
k
k
T yebxwaewwaebwL11
2
2
1
2
1,,,
(8)
where ka are Lagrangian multipliers. The derivatives of Eq. (8) should be equated to zero in
order to solve the problem. Thus, the following equations are obtained:
N1,2,...,k yebxw a
L
N1,2,...,k ea e
L
a b
L
xa w w
L
kkk
T
k
kk
k
N
1k
k
N
1k
kk
00
,0
00
)(0
(9)
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Eq. (9) indicates that there are 2N+2 equations and 2N+2 unknown parameters
b) and wea kk ,,,( . Thus, the parameters of LSSVM can be obtained by solving the system of
equations defined in Eq. (9) 36
.
As stated earlier, the LSSVM has a tuning parameter . Since, either of the LSSVM and
SVM are kernel-based technique, we should consider the parameters of the Kernel functions as
other tuning parameters. In case of RBF kernel function:
)/||||exp(),( 22 xxxxK kk (10)
The other tuning parameter is 2 . Therefore, in LSSVM algorithm with RBF Kernel
function, there are two tuning parameters which should be achieved by minimization of the
deviation of the LSSVM model from experimental values 36
. The mean square error (MSE) of
the results of the LSSVM algorithm has been measured using the following equation:
n
XX
MSEii
n
i
predrep
2
exp
1
/. )(
(11)
where X is the percent of precipitated wax, subscripts rep./pred. and exp. stand for the
represented/predicted, and experimental wax deposition, respectively, and n stands for the
number of samples from the initial population. In this study, the LSSVM algorithm developed
by Suykens and Vandewalle 17
has been used.
It is worthwhile to note that the main benefit of the LSSVM over the original SVM is the
idea of modifying the inequality constraints of Eq. (3) to the equality constraints of Eq. (7). The
parameters of the LSSVM are easily obtained by solving the system of equations presented in
Eq. (9) instead of solving a nonlinear quadratic programming 36
.
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3.2 Data Normalization
During training phase of the LSSVM, higher valued input variables may be likely to
suppress the impact of the smaller ones. To subdue such an obstacle and in order to make
LSSVM perform sufficiently, data must be well processed and sufficiently scaled prior to input
to the LSSVM. All of the inputs and their corresponding outputs are normalized as follows.
1.08.05.1 max
x
xxn (12)
where, x denotes actual data, xmax expresses the maximum value of the data and xn stands for the
normalized data 38
. Normalization procedure which is generally applied in optimization process
has been applied to obtain the parameters of LSSVM mathematical strategy, and it has no effect
on the model results 39, 40
. At the end, these values were returned to their original values.
3.3 Coupled Simulated Annealing
Simulated annealing (SA) 41-43
as the earliest mathematical strategy (algorithm) extending
local search techniques has an explicit algorithm in order to escape from local optima. The
primary idea is to allow moves which lead in solutions of worse quality than the present solution
to facilitate escaping from local optima. The possibility of doing such a move is decreasing
during the search process. Coupled Simulated Annealing (CSA), as a modification of SA, is
designed to be able to straightforwardly escape from local optima, and accordingly, improves the
accuracy of solutions without slowing down too much the speed of convergence. Suykens et al.
44 presented original principles of this method and demonstrated that coupling among local
optimization processes can be employed to improve gradient optimization approach to escape
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from local optima in non-convex problems. Moreover, in order to increase the quality of the final
solution, Wavier et al. 45
indicated the utilize of coupling in a global optimization technique.
Besides, by reducing a coupling strategy with minimal communication, these coupled strategies
can be applied very efficiently in parallel computer architectures, to make them very interesting
to the multi-core trend in the new generation of computer architectures 46
.
3.4 Computational Procedure
To develop our intelligent model nine input parameters have been selected including
compositions of C1-C3, C4-C7, C8-C15, C16-C22, C23-C29, C30+, specific gravity, system pressure,
and system temperature, as already mentioned. In this work, first, the database is randomly
divided into three sub-data sets involving the “Training” set, “Validating” set and the “Test” set.
Normally, the “Training” set is applied to generate the model structure and “Validating” set as
well as the “Test (prediction)” set are employed to investigate its prediction validity and
capability. To develop CSA-LSSVM model about 80% of the main data set randomly selected
for the “Training” set and the 10% and 10% have been applied for validating and testing phases,
respectively. In distribution of the existing data into these sub-data sets, several distributions
have been implemented to avoid the local minima and accumulations of the data in the feasible
region of the problem. As a result, the sufficient distribution is the one with homogeneous
accumulations of the data on the domain of the three sub-data sets 33
.
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4. Leverage Approach
In developing a model, outlier detection plays a key role to determine individual datum
(or groups of data) which may differ from the bulk of the data present in a dataset 47
. For this
end, the proposed methods, in general, consist of both numerical and graphical algorithms 47-52
.
The Leverage approach 47-49
is a well-known method for outlier detection. This method relates
with the values of the residuals (i.e., the deviations of a model results from the experimental
data) and a matrix known as Hat matrix consist of the experimental data and the
represented/predicted values obtained from a model. The main application criterion of this
method is to use a model, which is capable of adequate calculation/ estimation of the data of
interest. The Leverage or Hat indices are calculated based on Hat matrix (H) with the following
equation 47-52
:
tt XXXXH 1)( (13)
where X is a (nk) matrix, in which n stands for the number of data (rows) and k denotes
parameters of the model (columns), and t expresses the transpose matrix. The Hat values of the
data in the feasible region of the problem are the diagonal arrays of the H value. Afterward, the
Williams plot is sketched for graphical identification of the suspended data or outliers based on
calculated H value through Eq. (13). This plot demonstrates the correlation of Hat indices and
standardized cross-validated residuals (R), which are defined as the difference between the
represented/predicted values and the applied data. Normally, a warning Leverage (H*) is fixed at
the value equal to 3p/n, in which n stands for the number of training points and p is the number
of model parameters plus one. The Leverage equal to three is a ‘‘cut-off’’ value to accept the
points within 3 range standard deviations from the mean (to cover 99% normally distributed
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data). If majority of data points locate in the ranges of 0 HH*and -3R 3, it displays that
both model development and its predictions are done in applicability domain and this
consequently leads to a statistically valid model. It is worthwhile to note that ‘‘Good High
Leverage’’ points are located in the domain of HH *and -3R 3. The Good High Leverage
can be recognized as the points which are outside of applicability domain of the implemented
model. The points which are situated in the range of R -3 or 3R (whether they are greater or
smaller than the H* value) are identified as outliers of the model or ‘‘Bad High Leverage’’
points. These erroneous representations/predictions may be identified to the doubtful data 52
.
5. Results and Discussion
The LSSVM parameters consist of γ and σ2 must be evaluated and optimized in order to
achieve an accurate and reliable value for prediction of wax deposition. Therefore, these
parameters have been optimized using CSA mathematical optimization tool. It should be
mentioned that the numbers of reported digits of the two aforementioned parameters (σ2 and γ ),
in general, are obtained through sensitivity analysis of the overall error of the optimization
procedure 34
. Finally, the optimized values of σ2 and γ for the newly developed model have been
obtained 0.72381 and 615.8804, respectively
To evaluate the accuracy of the developed CSA-LSSVM model, statistical error analysis,
in which squared correlation coefficients (R2), average absolute relative deviations (AARDs),
standard deviation errors STD, and root mean square errors (RMSEs), and graphical error
analysis, in which crossplot and error distribution is sketched, have been utilized. Definitions and
equations of the aforementioned parameters are presented in Appendix B. Table 2 lists the
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statistical parameters of the developed model for prediction of wax deposition. The R2 and
average absolute relative deviation of CSA-LSSVM model in testing phase are reported 0.989
and 36.3, respectively. A comparison between the represented/predicted wax deposition values
and the experimental values are illustrated in Figs. 1 and 2. Fig. 1 displays the scatter diagram
that compares experimental wax deposition versus CSA-LSSVM model outputs. A tight cloud of
points about 45˚ line for training phase, validation and testing data sets illustrate the robustness
of the proposed CSA-LSSVM model. The obtained results demonstrate that excellent agreement
exists between the prediction of CSA-LSSVM and the experimental data of wax deposition.
Moreover, Fig. 2 represents the error distribution of the developed CSA-LSSVM model for
prediction of wax deposition. This figure confirms that the developed CSA-LSSVM model has
the low scatter around the zero error and the small error range to estimate the wax deposition.
These results display that the major advantage of CSA-LSSVM method is appropriate capability
for predict and modeling the physical properties.
Lira‐Galeana et al. 5 obtained the wax deposition values by using a multi-solid
thermodynamic model just for oils 12 and 15 among the all. Consequently, to represent the trend
plot of wax deposition versus temperature and also a comparison between experimental data, the
obtained values by CSA-LSSVM model, the ANN model 3, and the multi-solid wax
thermodynamic model 5, selection of oil 12 and oil 15 from the aforementioned experimental
database 23-25
seems adequate. The step-by-step solution of this thermodynamic model is
presented in Appendix C.
The solution of set of Eqs. (A8-13) in Appendix C, it is possible to estimate the amount
of wax deposition. However, the estimated amounts of deposited wax from the previous
equations are not in good agreement with experimental data. Figs. 3 and 4 indicate the trend plot
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of wax deposition versus temperature for oil 12 and 15, respectively. As can be seen in Figs. 3
and 4, by increasing in temperature the wax deposition decreases at both oil systems (oil 12 and
15). Moreover, these Figures indicate that there is more agreement between the experimental
data and the predicted values by CSA-LSSVM than the predicted values by ANN model 3 and
multi-solid wax thermodynamic model 5. Here, it should be noted that the CSA-LSSVM has
been developed by using “two adjustable parameters” while ANN and multi-solid wax
thermodynamic models require more adjustable parameters.
As previously mentioned, in developing a model, outlier detection plays a key role to
determine individual datum (or groups of data) which may differ from the bulk of the data
present in a dataset 47, 51, 53
. Therefore, to check whether the CSA-LSSVM model is statistically
correct and valid; the Williams plot has been sketched for the obtained results for wax deposition
using the CSA-LSSVM model (Fig. 5). Existence of majority of data points in the ranges 0 H
0.3103 and -3R demonstrate that the applied model for prediction of wax deposition is
statistically acceptable and valid. Good high leverage points are located in the domain of 0.3103<
H for developed CSA-LSSVM model. These points may be known to be outlier of the
applicability domain of the implemented model. The results of the wax deposition predictive
model show that only one data point is located in the aforementioned domain (Fig. 5). It may be
possible to eliminate these probable outliers from the developed model results and propose more
accurate ones; however, our aim, herein, has been to study the ability of all of the investigated
models to estimate the whole wax deposition values from a data set in the literature.
In final, it should be mentioned that although the CSA-LSSVM model was developed for
the dead oil systems, it can be applied for determination of wax deposition in live oil systems.
Therefore, at first, it is assumed that wax deposition does not affect the vapor-liquid equilibrium
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and using an appropriate model, a vapor-liquid equilibrium calculation is first performed on live
oil system, and then, the LSSVM model is applied on remaining liquid phase.
6. Conclusion
The implement of a LSSVM approach optimized by co-implementation of a CSA
algorithm was used to estimation of wax deposition as a serious problem in oil production. Field
and experimental data from the literature were utilized to build the new predictive model for wax
deposition at various compositions and temperature. The model was successfully applied to
prediction of wax deposition against experimental data. Moreover, to evaluate the capability of
the newly developed model the predicted values were compared with a multi-solid wax
thermodynamic model 5. The results indicate that the predicted values outperform than the
multi-solid wax thermodynamic model 5. Finally, the Leverage approach was applied to evaluate
the performance of wax deposition data. The results show that only one of the data points for
data points was found to be outliers (doubtful measured data) while all of the investigated data
were interpreted to be within the applicability of the developed model. Therefore, the developed
model is reliable for prediction of wax deposition in their domain. The results of this study reveal
that SVM-based technique with the CSA based parameters tuning approach, described in this
research, can result very good generalization and can advantageously be employed for estimation
of wax deposition.
Supporting information
The predicted values as well as the status of each data point (training, validation, test set).
This material is available free of charge via the Internet at http://pubs.acs.org.
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Appendix A. Artificial Neural Network Strategy
ANNs have large numbers of computational units called neurons, connected in a
massively parallel structure and do not need an explicit formulation of the physical or
mathematical relationships of the handled problem 54
. Several types of neural network strategies
have been developed in the literature. One of the most-widely used is called ‘‘Three-Layer Feed-
forward ANNs. This type is applied to generate a non-linear correlation between output and
input parameters. In Feed-forward ANNs, the design is based on one input layer, one output
layer and hidden layers 55
. The number of neurons in the input and output layers equals to the
number of inputs and outputs physical quantities, respectively 55
. But the number of the neurons
in the hidden layer may vary from one to the optimum one. The data from the input neurons are
propagated through the network via weighted interconnections 55
.Every i neuron in a k layer is
connected to every neuron in adjacent layers. The activation function of exponential sigmoid
function which has generally and traditionally been utilized to develop ANNs 56
as following:
xexf
1
1)( (A.1)
where x stands for parameter of activation function. A bias term, b, is associated with every
interconnection in order to introduce a supplementary degree of freedom. The expression of the
weighted sum, S, to the ith neuron in the kth layer (k ≥ 2) is 55
1
1
,,1,,1, )(kN
j
ikjkijkik bIwS (A.2)
where w is the weight parameter between each neuron-neuron interconnection. Using this feed-
forward network with activation function, the output, O, of the i neuron within the hidden k layer
is 55
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ikkN
jikjkijk
SbIw
ike
e
O,1
1,,1,,1 1
1
1
1
)((,
(A.3)
Appendix B. Statistical Error Parameters
In this study, to identify the accuracy of the newly CSA-LSSVM model a number of
statistical parameters have been applied including squared correlation coefficients (R2), average
absolute relative deviations (AARDs), standard deviation errors STD, and root mean square
errors (RMSEs). Definitions and equations of aforementioned parameters are as follows:
1. Squared correlation coefficients: (A.4)
N
i
N
i
i
XX
XX
R2
rep./pred (i)
1
2
rep./pred (i)exp)(2 1
2. Average absolute relative deviations: (A.5)
N
i i
ipredrepi
X
XXN
AARD
exp)(
exp)(/)(100%
3. Standard deviation errors: (A.6)
N
i
XaverageX predrepipredrepiNSTD ))()(( /)(/)(
1 2
4. Root mean square errors: (A.7)
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N
i
ii XXN
RMSE2
rep./pred)(exp)(
1
Appendix C. Multi-Solid Thermodynamic Model5
In this method, the criterion of vapor-liquid-solid equilibrium is that the fugacities of
component i in vapor, liquid, and solid phases are identical and the stability criteria exist:
N vapor-liquid isofugacity equations:
NixxxTPfyyyTPf NiN
v
i ,1,0),...,,,,(,...,,,,( 121
1
121 (A.8)
Ns liquid-solid isofugacity equations:
NNNiTPfxxxTPf s
s
ipureN
l
i ,1)(,0),(),...,,,,( ,121 (A.9)
N-1 material-balance equations:
(a) for the non-precipitating components:
)(,1,01 s
l
i
l
i
vl
i
N
j
jl
ii NNifF
VxK
F
V
F
Sxz
s
(A.10)
(b) for precipitating components, where all solid phases are pure:
)1(1,1)(,01
ss
l
i
l
i
vl
i
N
j
jl
ii NNNNifF
VxK
F
V
F
Sxz
s
(A.11)
where
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),,(
),,(
yPT
xPTK
v
i
ll
ivl
i
(A.12)
NiTPfzPTf s
ipurej
l
i ,1,0),(),,( , (A.13)
where fli is the liquid fugacity of component i, f
vi denotes the vapor fugacity of component
i, T and P are temperature and pressure, respectively. X, y, z and s express mole percent of liquid,
vapor, feed and solid phases, respectively.
Nomenclature
ANN artificial neural network
GA genetic algorithm
FL fuzzy logic
SVM support vector machine
LSSVM least square support vector machine
SA simulated annealing
CSA coupled simulated annealing
RBF radial basis function
WAT wax appearance temperatures
MSE mean square error
R2 correlation coefficient
AARD average absolute relative deviations, %
RMSE root mean square errors
SDE standard deviation errors
γ relative weight of the summation of the regression errors
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σ2 squared bandwidth
k slack variable
*
k slack variable
ak Lagrangin multiplier
ak* Lagrangin multiplier
ek error variable
H Hat matrix
Ski expression of the weighted sum
Oik output of a neural network
fli liquid fugacity of component i
fvi vapor fugacity of component i
T temperature
P pressure
x mole percent of liquid
y mole percent of vapor
z mole percent of feed
s mole percent of solid
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Table Captions
Table 1. Descriptive statistics of data set for prediction wax deposition; data from 23-25
.
Table 2. Statistical Parameters of the developed CSA-LSSVM model to determine the wax
deposition.
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Figures Captions
Fig. 1. Comparison between the results of the developed model and the experimental values 23-25
of wax deposition.
Fig. 2. Relative deviations of the wax deposition values obtained by the proposed model from
the database values 23-25
.
Fig. 3. Trend plot of wax deposition versus temperature and a comparison between the results of
the developed model and the experimental values of oil 12 from the database 23-25
and multi-solid
model 5.
Fig. 4. Trend plot of wax deposition versus temperature and a comparison between the results of
the developed model and the experimental values of oil 15 from the database 23-25
and multisolid
model 5.
Fig. 5. Detection of the probable doubtful data of wax deposition and the applicability domain of
the developed CSA-LSSVM model
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Table 1
Parameter Unit Type Min. Avg. Max.
Weight percent of wax deposition % Output 0 3.1419 13
System temperature K Input 230 272.657 314.150
System pressure bar Input 1 1 1
Specific gravity Input 0.872 0.918 0.963
Composition of C1-C3 % Input 0.218 1.315 2.127
Composition of C4-C7 % Input 3.057 18.476 30.952
Composition of C8-C15 % Input 33.468 44.495 49.791
Composition of C16-C22 % Input 16.029 29.005 57.335
Composition of C23-C29 % Input 0 2.811 10
Composition of C30+ % Input 0 3.538 13.230
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Table 2
Statistical Parameter Value
Training Set
R2 0.993
Average absolute relative deviation 16.0
Standard deviation error 0.24
Root mean square error 0.24
Number of used data points 71
Validation Set
R2 0.990
Average absolute relative deviation 43.7
Standard deviation error 0.68
Root mean square error 0.63
Number of used data points 8
Test Set
R2 0.989
Average absolute relative deviation 36.3
Standard deviation error 0.47
Root mean square error 0.44
Number of used data points 8
Total
R2 0.989
Average absolute relative deviation 20.4
Standard deviation error 0.32
Root mean square error 0.32
Number of used data points 87
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Fig. 1
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Fig. 2
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Fig. 3
Fig. 4
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Fig. 5
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