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Prediction of hydrate formation temperature by both statistical
models and artificial neural network approaches
Gholamreza Zahedi *, Zohre Karami, Hamed Yaghoobi
Simulation and Artificial Intelligence Research Center, Department of Chemical Engineering, Razi University, Kermanshah, Iran
a r t i c l e i n f o
Article history:
Received 26 June 2008Received in revised form 18 March 2009
Accepted 6 April 2009
Available online 6 May 2009
Keywords:
Hydrate formation temperature
Natural gas hydrate
Artificial neural network
a b s t r a c t
In this study, various estimation methods have been reviewed for hydrate formation temperature (HFT)
and two procedures have been presented. In the first method, two general correlations have been pro-
posed for HFT. One of the correlations has 11 parameters, and the second one has 18 parameters. In order
to obtain constants in proposed equations, 203 experimental data points have been collected from liter-
atures. The Engineering Equation Solver (EES) and Statistical Package for the Social Sciences (SPSS) soft
wares have been employed for statistical analysis of the data. Accuracy of the obtained correlations also
has been declared by comparison with experimental data and some recent common used correlations.
In the second method, HFT is estimated by artificial neural network (ANN) approach. In this case, var-
ious architectures have been checked using 70% of experimental data for training of ANN. Among the var-
ious architectures multi layer perceptron (MLP) network with trainlm training algorithm was found as
the best architecture. Comparing the obtained ANN model results with 30% of unseen data confirms
ANN excellent estimation performance. It was found that ANN is more accurate than traditional methods
and even our two proposed correlations for HFT estimation.
2009 Published by Elsevier Ltd.
1. Introduction
Natural gas hydrates are a curious kind of chemical compound
called a ‘‘clathrate”. Clathrates consist of two dissimilar molecules
mechanically intermingled but not truly chemically bonded. In-
stead one molecule forms a framework that traps the other mole-
cules. Natural gas hydrates can be considered modified ice
structures enclosing methane and other hydrocarbons, but they
can melt at temperatures well above normal ice. This behavior
has two important practical implications. First, it is a big problem
to the gas companies. They have to dehydrate natural gas thor-
oughly to prevent methane hydrates from forming in high pres-
sure gas lines. Second, methane hydrates will be stable on the
sea floor at depths below a few hundred meters and will be solid
within sea floor sediments. Masses of methane hydrate have beenphotographed on the sea floor. Chunks occasionally break, loose
and float to the surface, where they are unstable as they decom-
pose [1,2]. The hydrate should nucleate and grow from dissolved
methane in fluids that migrate toward the sea floor from below.
The concentration of gas required to form the hydrate in the sea
floor is significantly lower than the concentration needed to form
gas bubbles. In fact, the gas concentration required for forming the
hydrate drops sharply as the temperature decreases toward the
sea floor [3]. Natural gas hydrates are considered as a new method
of storage and transmission of natural gas [4,5].
There are three types of methane hydrate structure. They all in-
clude pentagonal dodecahedra of water molecules enclosing meth-
ane. This geometry arises from the happy accident that the bond
angle in water is fairly close to the 108 angle of a pentagon. Gen-
erally, the dodecahedra are slightly distorted so that three dodeca-
hedra can share an edge. This requires a dihedral (interface) angle
of 120, whereas the dihedral angle of a true dodecahedron is
116.5. Inside the dodecahedra there are other cages of water mol-
ecules with different shapes. In practice, not all cages are occupied
by hydrocarbons, but occupancy rates are over 90% [1]. Hydrates
were discovered in 1810 by Sir Humphrey Davy, yet only in the last
half century their occurrence has been of interest to the natural gas
industry. In 1934, Hammerschmidt [6] determined that hydrateswere the cause of plugged natural gas pipelines, thereby leading
to the regulation of gas water content, and to the development of
improved methods of prevention of hydrate plugs, including the
injection of methanol and other inhibitors into the gas stream. Re-
cent processing practice, which emphasis on extreme conditions of
temperature, pressure, has caused a renewed interest in determin-
ing hydrate formation conditions. The gas gravity method is very
simple for predicting the gas hydrate conditions [7]. To avoid te-
dious calculations based on GPSA’s hydrate formation curve, a
regression analysis was used to fit the GPSA’s hydrate formation
curve to predict the hydrate developed for gases where specific
gravity was known. The available and currently used correlations
0196-8904/$ - see front matter 2009 Published by Elsevier Ltd.doi:10.1016/j.enconman.2009.04.005
* Corresponding author. Fax: +98 831 4274542.
E-mail address: [email protected] (G. Zahedi).
Energy Conversion and Management 50 (2009) 2052–2059
Contents lists available at ScienceDirect
Energy Conversion and Management
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for a specific gravity method to calculate the hydrate formation
conditions are Sloan [1], Berge [8], Motiee [9], and Hammersch-
midt [6] correlations.
Vu et al. [10], applied an electrolyte equation of state based on
Péneloux’s non-electrolyte PR-EOS to the prediction of the temper-
ature associated to the formation of gas hydrate from water–meth-
anol–salts solutions. Original assumptions have been developed to
allow the calculation of model ionic parameters from experimentalsolvation diameters. Their model when applied to systems with
CH4 and CO2 hydrates has less than 1 K over a wide range of
conditions.
Sun and Chen [11] proposed a thermodynamic model for hy-
drate formation condition of sour gases. The model studies dissolu-
tion of gas in water and assumes equilibrium for hydrolytic
reaction.
Taylor et al. study [12] describes laboratory experiments and
computational modeling to address several key areas in hydrate re-
search. The laboratory results are used in the computational mod-
els and the results from the computational modeling is used to
help direct future laboratory research. Laboratory research is
accomplished in one of the numerous high-pressure hydrate cells:
thermal conductivity of hydrates (synthetic and natural) at tem-
perature and pressure, computational modeling studies are inves-
tigating the kinetics of hydrate formation and dissociation,
modeling methane hydrate reservoirs, molecular dynamics simula-
tions of hydrate formation, dissociation, and thermal properties,
and Monte Carlo simulations of hydrate formation and
dissociation.
Ahmadi et al. [13] described one-dimensional and axisymmetric
models for natural gas production from the dissociation of meth-
ane hydrate in a confined reservoir by a depressurizing well. They
accounted for the heat sink from hydrate dissociation and solved
the convection–conduction heat transfer in the gas and hydrate
zones. Using a finite-difference scheme, they evaluated the gas
flow and hydrate dissociation process inside the reservoir. For dif-
ferent well pressures, and reservoir temperatures and pressures,
they simulated the pressure and temperature conditions in the res-ervoir. It was shown that the gas production rate was a sensitive
function of well pressure. In addition, both heat conduction and
convection in hydrate zone were important. The simulation results
were compared with the linearization approach and discussed.
Since 1945, the gas gravity method given by Katz has been an
indispensable and simple tool for predicting the gas hydrate stabil-
ity zone. Despite the development of more sophisticated predictive
tools, such as the vapor–solid equilibrium ratio (Ki value) method
or the solid solution theory of Van der Waals and Platteeuw (1959),
the gas gravity method has kept its popularity among engineers
in the petroleum industry. The main advantage of this technique
is the availability of input data (it only requires the specific gravity
of the mixture, i.e., the molecular mass of the gas mixture divided
by that of air) and the simplicity of the calculation, which can beperformed by using charts or hand-held calculators [14].
Noting all reviewed articles a simple, easy to use and simulta-
neously accurate model for estimation of HTF is necessary. In this
paper first, four correlations based on statistical analysis will be
presented for HFT. Next among various ANN methods and architec-
tures best network will be found. This approach is new based on
our literature survey and fulfils simplicity and accuracy aims. Fi-
nally estimation capability of statistical correlation, ANN and com-
mon used correlation will be compared.
2. Common correlations to estimate HFT
In this study different widely used relations to estimate HFTwere investigated. The relations are as below:
2.1. Berge-correlation [2,8]
This correlation is valid for 0.555 6 c g < 0.58:
T ¼ 96:03 þ 25:37 ln P 0:64 ðln P Þ2
þ ðc g 0:555Þ=0:025 ½80:61 P þ 1:16 104=ðP þ 596:16Þ
ð96:03 þ 25:37 ln P 0:64 ðln P Þ2Þ ð1Þ
and for 0.586 c g < 1.0 Eq. (2) provides estimation as:
T ¼ f80:61 P 2:1 104 1:22 10
3=ðc g 0:535Þ
½1:23 104 þ 1:71 10
3=ðc g 0:509Þg=½P ð260:42
15:18=ðc g 0:535ÞÞ ð2Þ
2.2. Motiee correlation [2,9,15]
The correlation describes logarithm of pressure as a function of
temperature and gas specific gravity as:
logðP Þ ¼ a1 þ a2T þ a3T 2 þ a4c g þ a5c
2 g þ a6T c g ð3Þ
Correlation (4) provides a relation to estimate HFT as a function of pressure and gas gravity:
T ¼ b1 þ b2 logðP Þ þ b3ðlogðP ÞÞ2 þ b4c g þ b5c2 g þ b6c g ðlogðP ÞÞ ð4Þ
2.3. Hammerschmidt correlation [2,3]
T ¼ 8:9 P 0:285 ð5Þ
This correlation describes HFT as a function of only pressure.
2.4. Kobayashi and Sloan correlation [2,15,16]
Kobayashi and Sloan in 1978 have presented correlation to pre-
dict HFT based on gas gravity curves [5,7] as:
T ¼ 1=½ A1 þ A2ðln P Þ þ A3ðln c g Þ þ A4ðln P Þ2 þ A5ðlnP Þðln c g Þ
þ A6ðln c g Þ2 þ A7ðlnP Þ3 þ A8ðlnP Þ2ðlnc g Þ þ A9ðln P Þðln c g Þ
2
þ A10ðlnc g Þ3 þ A11ðln P Þ4 þ A12ðln P Þ3ðln c g Þ þ A13ðlnP Þ2ðlnc g Þ
2
þ A14ðln P Þðlnc g Þ3 þ A15ðln c g Þ
4 ð6Þ
This correlation is one of the most accurate and reliable equa-
tions in gas industry which is widely used to estimate HFT.
3. Methods
3.1. Presented models
According to Kobayashi and Sloan correlation, pressure and spe-
cific gravity are independent variable and temperature has been
assumed as a depended variable. Correlations (7)–(10) are polyno-
mial form of depended and independent variables which include
cross terms. Variables of pressure and specific gravity have been
investigated in logarithm form in correlations (7) and (8). 203 data
point have been collected form gas–gravity curves [15]. At first
step, 136 data have been employed. One of the correlations (Eq.
(7)) has 11 unknown and the other correlation (Eq. (8)) has 18
parameters. Eq. (9) has 11 parameters and Eq. (10) again contains
18 unknowns. In order to find parameters of correlations (7)–(10),
ESS and SPSS software’s have been used [17,18]. EES allows the
user to enter any equation of the form Y = F ( X , Z ) with up to sevenunknown coefficients represented as a0, a1, a2, . . . , a6. EES em-
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ploys a nonlinear least squares curve-fitting method to determine
the unknown coefficients. EES calculates the standard error of
each fitted coefficient as well as other information such as the
root mean square error (RMSE) and bias errors. At second step,
68 unseen data were employed for validating equations. Corre-
sponding coefficient (R2) for each class of equations and parame-
ter values of correlations (7)–(10) have been obtained in Tables
1–4.T ¼ 1=½ A0 þ A1ðln P Þ þ A2ðln P Þ
2þ A3ðln P Þ
3þ A4ðln c g Þ
þ A5ðln c g Þ2 þ A6ðlnc g Þ
3 þ A7ðln P Þðlnc g Þ þ A8ðln P Þ
ðln c g Þ2 þ A9ðln P Þ2ðln c g Þ þ A10ðln P Þ2ðln c g Þ
2 ð7Þ
T ¼ 1=½ A0 þ A1ðln P Þ þ A2ðln P Þ2 þ A3ðln P Þ3 þ A4ðln P Þ4
þ A5ðln c g Þ þ A6ðln c g Þ2 þ A7ðln c g Þ
3 þ A8ðln c g Þ4
þ A9ðln P Þðln c g Þ þ A10ðln P Þðln c g Þ2 þ A11ðlnP Þðln c g Þ
3
þ A12ðln P Þ2
ðlnc g Þ þ A13ðln P Þ2
ðlnc g Þ2
þ A14ðln P Þ2
ðln c g Þ3
þ A15ðln P Þ3ðlnc g Þ þ A16ðln P Þ3ðlnc g Þ2 þ A17ðln P Þ3ðln c g Þ
3 ð8Þ
T ¼ ½ A0 þ A1ðP Þ þ A2ðP Þ2 þ A3ðP Þ3 þ A4ðc g Þ þ A5ðc g Þ2 þ A6ðc g Þ
3
þ A7ðP Þðc g Þ þ A8ðP Þðc g Þ2 þ A9ðP Þ2ðc g Þ þ A10ðP Þ2ðc g Þ
2 ð9Þ
T ¼ ½ A0 þ A1ðP Þ þ A2ðP Þ2
þ A3ðP Þ3
þ A4ðP Þ4
þ A5ðc g Þ
þ A6ðc g Þ2 þ A7ðc g Þ
3 þ A8ðc g Þ4 þ A9ðP Þðc g Þ þ A10ðP Þðc g Þ
2
þ A11ðP Þðc g Þ3
þ A12ðP Þ2
ðc g Þ þ A13ðP Þ2
ðc g Þ2
þ A14ðP Þ2
ðc g Þ3
þ A15ðP Þ3ðc g Þ þ A16ðP Þ3ðc g Þ2 þ A17ðP Þ3ðc g Þ
3 ð10Þ
3.1.2. Comparison between presented correlations and empirical
correlations
Correlations (7) and (8) have been illustrated in Figs. 1–6 and
have been compared with other methods, such as ‘‘Hammersch-midt” and ‘‘Katz” and Berge methods.
In low specific gravity, Katz’s diagram which has been plotted
based on pressure and temperature has a linear form.
All correlations and figures which have been presented based
on logarithm of pressure and specific gravity, have high accuracy
for prediction of HFT at low specific gravity.
Corresponding coefficient (R2) confirm high accuracy of correla-
tions (7)–(10). Correlations of Berge and Hammerschmidt, have
low accurate for prediction of HFT at higher pressures and specific
gravities (Figs. 4–6).
Finally, correlation (7) has 11 parameter ((4) parameter lessthan Sloan equation), and is recommended for practical use espe-
cially at high specific gravity. It is obvious that proposed correla-
tions have good overlap with experimental data at higher specific
gravities which currently used correlations don’t have such estima-
tion capability.
3.2. Artificial neural network
Neural network is an inductive model for the structure and
function of neuron. A neural network consists of complex units
which, in turn, are demonstrative of neurons of the body. The units
are in the shape of conjunct loop structure which, in fact, functions
like axons and dendrites.
Oneof thewell knowntypeneural network isthe multilayer per-ceptron which is utilized to classify and estimate neural problems.
Oneexampleof thelayerednetworks is provided in Fig. 7. Inthe fig-
ure, ANNinput, hidden and output layers areshown. In thisnetwork,
each pair of lines is interconnected via a weight. The two important
capabilities of neural network are swift response to problems and
the ability of generalization of these responses to the unobserved
samples. Thus, we must be familiar with the problems and ordinary
learning of the network which is called training.
In this figure L input layers, M hidden layers and N output lay-
ers, exist. The jth output of hidden layer can be found by the fol-
lowing linear combination of L times input layer:
Xv ija j ð11Þ
In this formula mij are weights; i is an index representing hidden
layer, and j is an index for input layer. One can estimate the output
neuron j by the following function for f :
Table 1
Statistical results and value of parameters for Eq. (7).
Coefficient Value Std. error Coefficient Value Std. error
A0 2.998674E3 1.491795E3 A6 2.169920E3 1.608001E4
A1 1.615272E3 3.034751E4 A7 7.114145E4 3.233519E4
A2 1.241929E4 2.061456E5 A8 2.062154E3 5.745757E4
A3 3.012534E6 4.677437E7 A9 2.288624E5 1.087459E5
A4 5.788643E3 2.394345E3 A10 7.044740E5 1.892436E5
A5 1.636478E2 4.324969E3
No. point = 136: RMS = 8.9978E6: bias = 1.7566E21: R2 = 98.95%.
Table 2
Statistical results and value of parameters for Eq. (8).
Coefficient Value Std. error Coefficient Value Std. error
A0 2.396490E2 1.397764E2 A9 1.956523E2 9.282471E3
A1 5.482741E3 3.829677E3 A10 9.083137E2 3.674821E2
A2 5.745664E4 3.934606E4 A11 9.845863E2 4.101932E2
A3 2.747777E5 1.796694E5 A12 1.352731E3 6.299044E4
A4 4.976688E7 3.076875E7 A13 6.356978E3 2.471904E3
A5 9.398840E2 4.547328E2 A14 6.993158E3 2.733194E3
A6 4.276777E1 1.816661E1 A15 3.110160E5 1.421058E5
A7 4.502661E1 2.047528E1 A16 1.475054E4 5.529886E5
A8 9.282732E3 6.397091E4 A17 1.644929E4 6.060549E5
No. point = 136: RMS = 4.8338E6: bias = 1.6476E20: R2 = 99.70%.
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b j ¼ f XLi¼0
v ija j
! ð12Þ
Training of the ANN is an improvement process in which error
of functions can be minimized by according them to the network
weights. When the pattern of teaching input data introduced in
the network, neural network computes output and compares it
with the real outputs. These differences can be used by improve-
ment technique to teach neural network. Function of errors, stud-
ied here, is Mean Square Error (MSE) which can be shown by E j inthe following formula:
E i ¼ 1
n
Xni¼1
ðC i C ir Þ2
ð13Þ
In this formula C ir is a real output and C i is a similar output for j
in the input. Training process is a way from input layer to output
layer in order to compute outputs and a backward route to correct
weights. This process continues until the E j is minimized. As soon
as errors of tested volumes were minimized, the teaching process
terminates.
Beside MLP, a group of ANN has recently been recognized which
is called Radial Basis Function (RBF) network. RBF also has three
layers including: input layers, hidden layer (with Gaussian func-
tion), and output layer. The weight of the loops between inputand hidden layer is a unit which remains constant. While being
taught, the hidden layer makes a non-linear change which, conse-
quently, draws a new space like MLP from the inner space. ANNs
have been used in recent years to avoid the problems associated
with deterministic approaches and have been shown to approxi-
mate non-linear functions up to any desired level of accuracy
[19–25].
Table 3
Statistical results and value of parameters for Eq. (9).
Coefficient Value Std. error Coefficient Value Std. error
A0 4.300068E2 5.878018E1 A6 7.987736E2 1.173947E2
A1 5.776973E2 3.044887E2 A7 2.229806E2 7.813343E2
A2 2.705239E5 9.703460E6 A8 2.208720E2 5.013645E2
A3 2.909084E9 3.236679E10 A9 2.067366E5 2.520617E5
A4 1.677816E3 2.235983E2 A10 1.939392E5 1.727848E5
A5
2.009781E3 2.816434E2
No. point = 136: RMS = 2.9803E0: bias = 1.591E15: R2 = 94.58%.
Table 4
Statistical results and value of parameters for Eq. (10).
Coefficient Value Std. error Coefficient Value Std. error
A0 2.116379E3 2.894034E2 A9 5.229394E1 1.028631E0
A1 6.674690E2 2.600775E1 A10 6.776850E1 1.339959E0
A2 2.004185E5 1.791694E4 A11 3.167324E1 5.735178E1
A3 3.394457E9 3.635251E8 A12 2.696084E4 7.311481E4
A4 1.500678E12 2.289350E13 A13 4.042360E4 9.827757E4
A5 1.077808E4 1.452659E3 A14 2.350797E4 4.333993E4
A6 2.018584E4 2.761310E3 A15 5.966861E8 1.549012E7
A7 1.669117E4 2.318908E3 A16
1.169590E
7 2.167171E
7 A8 5.135225E3 7.258498E2 A17 7.854232E8 9.930572E8
No. point = 136: RMS = 1.8117E00: bias = 6.8040E14: R2 = 98.00%.
Fig. 1. Comparison of Eqs. (7) and (8) with experimental data, Hammerschmidt andBerge methods. (Specific gravity is equal to 0.6.)
Fig. 2. Comparison of Eqs. (7) and (8) with experimental data, Hammerschmidt andBerge methods. (Specific gravity is equal to 0.65.)
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3.3. Applying ANN for HFT estimation
In this case among 203 data, the network is being taught by 136
data and the 67 remaining data is used to test generalization
capacity of the network [15]. Neural network variables and their
domains are illustrate in Table 5.
In order to estimate hydrate data, two networks, namely MLP
and RBF are utilized. In the first method, i.e., using MLP network
according to the Fig. 8, in which MSE is plotted in conformity with
the number of hidden layers, the optimal number for hidden layersis seven which has the least error. Fig. 9 depicts the error percent-
age for tested data in seven hidden layers. The second method uses
RBF neural network. In Fig. 10, MSE is plotted as a function of num-
ber of hidden layers. According to this figure in the three hidden
layer, MSE approaches its least amount. Error percentage for best
RBF network has been depicted in Fig. 11.
Fig. 3. Comparison of Eqs. (7) and (8) with experimental data, Hammerschmidt and
Berge methods. (Specific gravity is equal to 0.7.)
Fig. 4. Comparison of Eqs. (7) and (8) with experimental data, Hammerschmidt and
Berge methods. (Specific gravity is equal to 0.8.)
Fig. 5. Comparison of Eqs. (7) and (8) with experimental data, Hammerschmidt andBerge methods. (Specific gravity is equal to 0.9.)
Fig. 6. Comparison of Eqs. (7) and (8) with experimental data, Hammerschmidt and
Berge methods. (Specific gravity is equal to 1.0.)
InputLayer
HiddenLayer
OutputLayer
I1
I i
I L
V11
V1j
V1m
Vi1
Vij
Vim
VL1
VLj
VLm
aL
ai
ai W11
W1K
W1n
W j1
W jK
W jn
Wm1
WmK
Wmn
bm
b j
b1C1
CK
Cn
Fig. 7. Structure of a neural network.
Table 5
Neural network variables and domain.
Variables Domain
Specific gravity of gas 0.555–1
Pressure (psi) 200–2680.44
Temperature (F) 33.7–75.7
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3.4. Comparison between MLP and RBF
MLP and RBF are two advances models for estimation of the
HFT. Regarding Figs. 7 and 9, MLP networks have less MSE than
RBF networks. MSE is 0.2248 and 0.7053 for best MLP and RBF net- works, respectively. RBF, has more error for other data, but MLPnetwork represent an optimum error percentage for the most data.
0 10 20 30 40 50 0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
M
S E
number of hidden layers
Fig. 8. MSE versus number of hidden layer neurons for MLP.
0 10 20 30 40 50 60 70 0
0.5
1
1.5
2
2.5
number of tested data
e r r o r p e r c e n t a g e
Fig. 9. Percentage in generalization error for best obtained MLP network.
0 10 20 30 40 50 60 70 0
1
2
3
4
5
6
7
8
number of tested data
e r r o r p e r c e n t a g e
Fig. 11. Percentage of generalization error for best obtained RBF network.
30 35 40 45 50 55 60 65 70 10 2
10 3
10 4
temperature (F)
p r e s s u r e ( p s i )
SG=0.6
EXP
ANN
Eq.7
Eq.8
Eq.9
Eq.10
Fig. 12. Comparison of experimental data with ANN and present models. (Specific
gravity is equal to 0.6.)
35 40 45 50 55 60 65 70 75 10
2
10 3
10 4
temperature (F)
p r e s s u r e
( p s i )
SG=0.65
EXP
ANN
Eq.7
Eq.8
Eq.9
Eq.10
Fig. 13. Comparison of experimental data with ANN and present models. (Specific
gravity is equal to 0.65.)
0 10 20 30 40 50 0
0.25
0.5
0.75
1
1.25
1.5
1.75
2
2.25
2.5 2.5
number of hidden layers
M S E
Fig. 10. MSE in versus number of hidden layer neurons for RBF.
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MLP network has better prediction of the HFT rather than RBF
network. This model, approximately, can be generalized to all sorts
of data because the differences between predicted and real
amounts are diminutive, which proves the capability of artificial
neural network to predict unobserved data correctly.
4. Comparison between ANN and present models in HFT
estimation
The research has targeted investigation of HFT prediction by
presenting four models and ANN. This section deals with the HFT
in the different pressure and special gravities concerning predicted
temperature by MLP neural network and presented models. Re-
sults of the comparison are illustrated in Figs. 12–17.
Fig. 18 indicates comparison of generalization error of experi-
mental data with ANN and Eqs. (7) and (8). According to this figure
compared to predicted temperature by ANN and best present mod-
els (Eqs. (7) and (8)) shows that simulation with ANN has a better
result with a higher accuracy for HFT estimation.
5. Conclusion
Inthiswork,twocorrelationsbasedonKobayashiandSloanmod-el andtwo correlationsbased on Berge model,have been developed.
35 40 45 50 55 60 65 70 75 10
2
10 3
10 4
temperature (F)
p r e s s u r e
( p s i )
SG=0.7
EXP
ANN
Eq.7
Eq.8
Eq.9
Eq.10
Fig. 14. Comparison of experimental data with ANN and present models. (Specific
gravity is equal to 0.7.)
35 40 45 50 55 60 65 70 75 80 10
2
10 3
10 4
temperature (F)
p r e s s u r e ( p s i )
SG=0.8
EXP
ANN
Eq.7
Eq.8
Eq.9
Eq.10
Fig. 15. Comparison of experimental data with ANN and present models. (Specific
gravity is equal to 0.8.)
30 40 50 60 70 80 90 10
2
10 3
10 4
temperature (F)
p r e s s u r e ( p s i )
SG=0.9
EXP
ANN
Eq.7
Eq.8
Eq.9
Eq.10
Fig. 16. Comparison of experimental data with ANN and present models. (Specificgravity is equal to 0.9.)
40 45 50 55 60 65 70 75 80 10
2
10 3
10 4
temperature(F)
p r e s s u r e ( p s i )
SG=1.0
EXP
ANN
Eq.7
Eq.8
Eq.9
Eq.10
Fig. 17. Comparison of experimental data with ANN and present models. (Specific
gravity is equal to 1.0.)
0 10 20 30 40 50 60 70 0
5
10
15
20
25
30
35
40
number of tested data
e r r o r p e r c e n t a g e
ANN
Eq.7
Eq.8
Fig. 18. Comparison of percentage in generalization error of experimental data
with ANN and Eqs. (7) and (8).
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Themodelswhich estimateHFT as functionsof logarithm of pressure
and specific gravity have good accuracy compared to the common
used equations in industry.Obtained correlations are moreaccurate
than Kobayashi and Berge correlations and have good agreement
with experimental data and can be used for prediction of HFT and
amount of inhibitor that should be injected to gas stream line. In
the next step of work ANN model hasbeen build forHFT estimation.
Among the various MLP and RBF structures, MLP with seven neuronhas been found as the best predictor of HFT data. The obtained ANN
estimation capability was compared with our correlations. Results
show that ANN is more accurate than our obtained correlations. In
thiscase ANNis recommended for HFT rather thancommon correla-
tion and also our correlations.
Acknowledgement
This work was supported by Razi University research council.
References
[1] Sloan ED. Clathrates hydrates of natural gas. 2nd ed. New York: Marcel DekkerInc.; 1998. p. 757.
[2] Khaled Ahmed Abdel Fattah. Evaluation of empirical correlations for naturalgas hydrate predictions. Oil Gas Bus; 2004. <http://www.ogbus.ru/eng/>.[3] Buffett BA, Zatsepina OY. Formation of gas hydrate from dissolved gas in
natural porous media. Mar Geol 2000;164:69–77.[4] Hao Wenfeng, Wang Jinqu, Fan Shuanshi, Hao Wenbin. Evaluation and analysis
method for natural gas hydrate storage and transportation processes. EnergyConvers Manage 2008;49:2546–53.
[5] Sun Z, Wang R, Ma R, Guo K, Fan S. Natural gas storage in hydrates with thepresence of promoters. Energy Convers Manage 2003;44:2733–42.
[6] Hammerschmidt EG. Formation of gas hydrates in natural gas transmissionlines. Ind Eng Chem Res 1934;26:851.
[7] Katz DL, Lee RL. Natural gas engineering production and storage. NewYork: McGraw Hill; 1990.
[8] Berge BK. Hydrate prediction on a microcomputer, paper SPE 15306. Presentedat the 1986 symposium on petroleum industry applications of microcomputers.
[9] Motiee M. Estimate possibility of hydrates. In: Hydrological proceeding; July1991. p. 98.
[10] Vu Vinh Quang, Suchaux Pierre Duchet, Fürst Walter. Use of a predictiveelectrolyte equation of state for the calculation of the gas hydrate formationtemperature in the case of systems with methanol and salts. Fluid PhaseEquilibria 2002;194–197:361–70.
[11] Chang-Yu Sun, Guang-Jin Chen. Modelling the hydrate formation condition forsour gas and mixtures. Chem Eng Sci 2005;60:4879–85.
[12] Taylor CE, Link DD, English N. Methane hydrate research at NETL research tomake methane production from hydrates a reality. J Petrol Sci Eng
2007;56:186–91.[13] Ahmadi G, Ji C, Smith DH. Natural gas production from hydrate
disso ciation: an axisymmetric model. J Petrol Sci Eng2007;58:245–58.
[14] Østergaard Kasper K, Masoudi Rahim, Tohidi Bahman, Danesh Ali, Todd AdrianC. A general correlation for predicting the suppression of hydrate dissociationtemperature in the presence of thermodynamic inhibitors. J Petrol Sci Eng2005;48:70–80.
[15] Kobayashi R, Song KY, Sloan ED. Phase behavior of water/hydrocarbonsystems. Quoted in Bradley HB, ‘‘Petroleum engineers handbook”, andRichardson: ‘‘Society of petroleum engineers”; 1987.
[16] Elgibaly Ahmed A, Elkamel Ali M. A new correlation for predicting hydrateformation conditions for various gas mixtures and inhibitors. Fluid PhaseEquilibria 1998;152.
[17] http://www.mhhe.com/engcs/mech/ees/. 2003.[18] www.spss.com.[19] Blusari AB. Neural networks for chemical engineers. Amsterdam: Elsevier
Science Press; 1995.[20] Joseph B, Wang FH, Shieh PS. Exploratory data analysis a comparison of
statistical methods with artificial neural network. Comput Chem Eng1992;16:413.
[21] Matlab neural network toolbox; 2008. <www.mathwork.Com>.[22] Qi Xiaoni, Liu Zhenyan, Li Dandan. Numerical simulation of shower cooling
tower based on artificial neural network. Energy Convers Manage2008;49:724–32.
[23] Mohammad Zahedi G, Zadeh S, Moradi G. Enhancing gasoline production in anindustrial catalytic reforming unit using artificial neural networks. EnergyFuels 2008;22:2671–7.
[24] Zahedi G, Jahnmiri A, Rahimpor MR. A neural network approach for predictionof the CuO–ZnO–Al2O3 catalyst deactivation. Int J Chem Reactor Eng 2005;3[Article A8].
[25] Zahedi G, Fgaier H, Jahanmiri A, Al-Enezi G. Artificial neural networkidentification and evaluation of hydrotreater plant. Petrol Sci Technol2006;24:1447–56.
G. Zahedi et al. / Energy Conversion and Management 50 (2009) 2052–2059 2059