Bakeri, G., Delavar, M., Soleimani Lashkenari, M. (2015). Surface Tension Prediction of Hydrocarbon Mixtures Using Artificial Neural Network. Journal of Oil, Gas and Petrochemical Technology, 2(Number 1), 14-26. doi: 10.22034/jogpt.2015.9713

Gholamreza Bakeri; Maedeh Delavar; Mohammad Soleimani Lashkenari. "Surface Tension Prediction of Hydrocarbon Mixtures Using Artificial Neural Network". Journal of Oil, Gas and Petrochemical Technology, 2, Number 1, 2015, 14-26. doi: 10.22034/jogpt.2015.9713

Bakeri, G., Delavar, M., Soleimani Lashkenari, M. (2015). 'Surface Tension Prediction of Hydrocarbon Mixtures Using Artificial Neural Network', Journal of Oil, Gas and Petrochemical Technology, 2(Number 1), pp. 14-26. doi: 10.22034/jogpt.2015.9713

Bakeri, G., Delavar, M., Soleimani Lashkenari, M. Surface Tension Prediction of Hydrocarbon Mixtures Using Artificial Neural Network. Journal of Oil, Gas and Petrochemical Technology, 2015; 2(Number 1): 14-26. doi: 10.22034/jogpt.2015.9713

Surface Tension Prediction of Hydrocarbon Mixtures Using Artificial Neural Network

^{1}Advanced Membrane and Biotechnology Research Center, Babol Noshirvani University of Technology, Babol, Iran

^{2}Faculty of Chemical Engineering, Babol Noshirvani University of Technology, Babol, Iran

Abstract

In this study, artificial neural network was used to predict the surface tension of 20 hydrocarbon mixtures. Experimental data was divided into two parts (70% for training and 30% for testing). Optimal configuration of the network was obtained with minimization of prediction error on testing data. The accuracy of our proposed model was compared with four well-known empirical equations. The artificial neural network was more accurate as the result showed that while standard deviation of ARD for artificial neural network was 3.63001, the standard deviation of ARD for Brock and Bird, Pitzer, Zuo-Stenby and Sastri-Rao models were 23.77569, 18.44848, 13.00388 and 9.63137 respectively.

Surface tension is a characteristic property of fluids as scientific and technological researches on many areas need data on surface tension of the materials, such as chemical engineering, materials engineering, oil recovery, environmental protection, etc [1,2]. The surface tension of pure liquids and of liquid mixtures is often required in calculations such as those involving flow through porous media or boiling heat transfer.

In addition to experimental measurements, numerous theoretical researches have been carried out on the surface tension modeling [3-5]. Some of the presented models have a very strong theoretical basis such as those that are based on statistical mechanical theories of liquids and density functional theory [2,6]. Also corresponding state principles have been employed to predict the surface tension of pure materials [7-10]. The experimental data of surface tension for non-polar liquids have been correlated by utilizing the Riedel parameter at the critical point [7]. The critical temperature, pressure and acentric factor have been used as correlation parameters for determining the surface tension [9].

Two-reference corresponding states methods were initially proposed by Rice and Teja [11] in which critical temperature and volume were used to obtain a correlation. Later, Zuo and Stenby employed the same method for calculating surface tensions where critical pressure and temperature were considered as correlation parameters [12]. These equations have not presented satisfactory results for chemical compounds with strong hydrogen-bonding forces. To overcome these hurdles, Sastri and Rao introduced a correlation based on critical pressure and temperature, normal boiling point temperature, reduced temperature and reduced boiling temperature [13]. Although these equations are usually much simpler, their dependency on experimental data for each component limits their application to the cases for which some experimental data exist. These methods usually fail to give accurate predictions for other situations. The surface tension of a liquid mixture is not a simple function of the surface tensions of the pure components. In general, there are several approaches for estimating the surface tension of mixtures (i) based on empirical or semiempirical relations suggested first for pure fluids and (ii) based on statistical mechanical grounds. It is impractical to measure the surface tension for all liquids and liquid mixtures of interest and a method for the prediction of surface tension is therefore of practical importance [11,14,15].

Because of nonlinear nature of surface tension, artificial neural network method may be considered as an alternative tool for the prediction of surface tension. Gharagheizi, et al. applied an artificial neural network-group contribution method to predict the surface tension of pure chemical compounds [16]. Kumar, et al. effectively used parachor, density and refractive indices as input parameters required in the neural network for the prediction of surface tension of various polar and non-polar compounds [17]. Strechan, et al. used artificial neural network for correlations of the surface tension of molecular liquids [10]. Furthermore, artificial neural network has been applied for surface tension prediction of pure liquid metals [18]. To the authors' best knowledge, there has been no study on the application of artificial neural network for the surface tension prediction of hydrocarbon mixtures.

In this study, a feed-forward artificial neural network with Levenberg–Marquardt training algorithm was applied in order to investigate its capability in prediction of the surface tension of 20 hydrocarbon mixtures. The proposed ANN model results were compared with four well-known classical models.

2. Research Method

2.1. Classical models

Numbers of correlations based on the law of corresponding states have been developed for the prediction of surface tension (σ) which relate surface tension to the absolute temperature (T). Brock and Bird [7] proposed Eq. 1 for non-polar liquids.

(1)

where σ is the surface tension (dyn/cm) and is the Riedel parameter [19] at the critical point and is defined through Eq. 2.

(2)

where T is the absolute temperature (K), P is pressure (bar) and subscripts c, r and b denote the critical, reduced and boiling values respectively.

Pitzer [20] presented a corresponding state relation for surface tension in terms of critical pressure (P_{c}), critical temperature (T_{c}) and acentric factor (ω) as shown in Eq. 3.

(3)

Zuo and Stenby [12] used a two-reference fluid corresponding state to estimate the surface tensions as was shown in Eq. 4.

(4)

In this method, the surface tension for the fluid of interest is related to the surface tension of two reference fluids, methane (1) and n-Octane (2) by Eq. 5.

(5)

where the surface tension of methane is calculated by Eq. 6.

(6)

and the surface tension of n-octane is calculated by Eq. 7.

(7)

Even though the three above-mentioned corresponding-states methods are satisfactory for the non-polar liquids, they are not suitable for compounds that exhibit strong hydrogen-bonding (e.g. alcohols, acids). To deal with these types of compounds, Sastri and Rao [13] modified the equations as presented in Eq. 8.

(8)

where the values for the constants are presented in Table 1.

Table 1. Values for the constants of Eq. 8.

K

X

Y

Z

m

Alcohols

2.28

0.25

0.175

0

0.8

Acids

0.125

0.50

-1.5

1.85

1.22

All others

0.158

0.50

-1.5

1.85

1.22

2.2. Artificial neural network (ANN)

Neural networks are composed of simple elements operating in parallel. These elements are inspired by biological nervous systems. As in nature, the network function is determined largely by the connections between elements. One can train a neural network to perform a particular function by adjusting the values of the connections (weights) between elements. Commonly, neural networks are adjusted or trained, so that a particular input leads to a specific target output.

In an ANN, a neuron sums the weighted inputs from several connections and then outputs of neurons are produced by applying transfer function to the sum. There are many transfer functions but the most common one is sigmoid which is used in this study as presented in Eq. 9.

(9)

where is the sum of weighted inputs to each neuron and is the output of each neuron which is calculated through Eq. 10.

(10)

where denotes connection between node j of interlayer l to node i of interlayer l-1, b_{j} is a bias term and n is the number of neuron in each layer. In any interlayer l and neuron j input values integrate and generate.

In order to minimize the difference between experimental data and the data calculated by neural network, the afore-mentioned process repeats for the total number of training data. After training, validation of neural network can be done by testing the data.

Numerous types of the artificial neural networks exist such as multi-layer perceptron (MLP), radial basis function (RBF) networks and recurrent neural networks (RNN) where the former was used in this study. Multi-layer perceptron networks are one of the most popular and successful neural network architectures which are suited to a wide variety of applications such as the prediction and process modeling [21-23].

2.3. Preparation of dataset

578 datasets for surface tension of 20 hydrocarbon mixtures at different temperature and composition were collected [24] in addition to the critical temperature, critical pressure, critical volume, acentric factor, normal boiling point, molecular weight and ideal liquid density for pure components which were considered as the input for the ANN. Table 2 shows the list of hydrocarbon mixtures, the number of data point for each mixture and the temperature range. Furthermore, Table 3 shows the values of the physical properties of pure hydrocarbons. In this study, the data sets were divided into three parts: training subset (60% of all data), validation subset (10% of all data) and testing subset (30% of all data). To avoid larger number from overriding smaller number, all data is normalized between [0.1-0.9] using Eq. 11.

(11)

Table 2. The list of experimental data used in this study [24].

Mixtures

Number of data point

Temperature (K)

Tetrachloromethane - Iodomethane

47

288-308

Tetrachloromethane - Nitromethane

33

303-317

Tetrachloromethane - Methanol

12

308

Tetrachloromethane - Acetonitrile

44

298-317

Tetrachloromethane - Iodo-ethane

33

298-322

Tetrachloromethane - Nitroethane

33

303-317

Tetrachloromethane - Ethanol

18

293-345

Tetrachloromethane - Dimethylsulfoxide

24

303-322

Formic acid - Acetic acid

34

287-349

Formic acid - Pyridine

27

287-298

Formic acid - 2-methyl-aniline

8

298

Iodomethane - Acetic acid

33

293-313

Nitromethane - Acetic acid

11

293

Nitromethane - Benzene

26

293-303

Nitromethane - Cyclohexane

6

293

Methane - Propane

46

258-338

Methanol - Acetic acid

11

308

Methanol - Ethanol

50

293-333

Methanol - Dimethylsulfoxide

55

293-323

Methanol - Benzene

27

273-303

Table 3. Physical properties of pure hydrocarbons used in this study.

Hydrocarbons

Critical Temperature (˚C)

Critical pressure (bar)

Critical volume (m^{3}/kgmol)

Acentric Factor

Normal boiling point (˚C)

Molecular weight

Ideal liquid density (kg/m^{3})

Tetrachloromethane

283.3

45.6

0.2759

0.193

76.75

153.8

1601

Nitromethane

313.9

63.1

0.1732

0.31

101.1

61.04

1138

Methanol

239.4

73.76

0.1270

0.557

64.65

32.04

795.7

Acetonitrile

272.4

48.2

0.1729

0.327

81.65

41.05

782

Iodo-ethane

278.9

47

0.2705

0.1563

72.45

156

1961

Nitroethane

321.8

51.16

0.2295

0.3684

114.8

75.07

1052

Ethanol

240.8

61.47

0.1671

0.6444

78.25

46.07

796

Dimethylsulfoxide

455.9

56.5

0.227

0.2806

189.0

78.14

1105

Formic acid

296.9

55

0.112

0.3525

100.6

46.03

1225

Pyridine

346.9

56.2

0.254

0.243

115.2

79.10

988.8

2- methyl-aniline

420.9

37.5

0.35

0.438

200.4

107.2

1002

Iodomethane

251.9

65.9

0.1842

0.1446

42.55

141.9

2293

Acetic acid

319.6

57.7

0.1710

0.447

118.0

60.05

1052

Benzene

288.9

49.24

0.26

0.215

80.09

78.11

882.2

Cyclohexane

280.1

40.53

0.308

0.2133

80.73

84.16

781.8

Methane

-82.45

46.41

0.099

0.0115

-161.5

16.04

299.4

Propane

96.75

42.57

0.2

0.1524

-42.1

44.10

506.7

2.4. ANN modeling

Programming, validation, training and testing of the ANN model were carried out by MATLAB 7.7.0. To determine the optimized values of weights and biases, the following steps were done:

Data sets were divided into three parts, training subset (60% of all data), validation subset (10% of all data) and testing subset (30% of all data).

Data was normalized using Eq. 11.

The number of neurons in hidden layer was optimized.

3. Results and Analysis

Three layers feeding forward neural network were used for surface tension prediction of 20 hydrocarbon mixtures and all parameters of neural network were determined by trial and error procedure. According to the experimental data and for a fair comparison with the classical models, temperature (T), composition (x), critical temperature (T_{c}), critical pressure (P_{c}), critical volume (V_{c}), acentric factor (ω), normal boiling point (T_{b}), molecular weight (M) and ideal liquid density (ρ) of mixtures were used as inputs to our proposed neural network.

The physical properties of hydrocarbon mixture were related to the physical properties of pure components, using mixing rules as were shown in Eqs. 12-13 for mixture critical temperature (T_{cm}) and mixture critical pressure (P_{cm}) respectively.

(12)

(13)

where x_{i} and x_{j} are the composition of component i and j in the mixture. Binary critical temperature (T_{cij}) and binary critical pressure (P_{cij}) were obtained through Eqs. 14-15, respectively.

(14)

(15)

Furthermore, mixture normal boiling point (T_{bm}), mixture critical volume (V_{cm}), mixture acentric factor (), mixture molecular weight (M_{m}) and mixture ideal liquid density () were calculated using Eqs. 16-20, respectively.

(16)

(17)

(18)

(19)

(20)

where subscripts m and i denote the mixture and pure value of each physical property, respectively.

Sigmoid function was used as transfer function in hidden layers and purelin function was used as the transfer function of output layers. Also Levenberg-Marquardt back propagation learning algorithm was used for training. Usually one hidden layer is enough but the numbers of neurons in hidden layers need to be optimized for each problem. In order to optimize the number of neurons in hidden layers, average relative deviation (ARD), (calculated through Eq. 21) of testing data versus the neuron number in hidden layers is plotted, as was shown in Fig. 1. The Results showed that 9-5-1 is the best topology of the neural network (Fig. 2). The cross plot graph which shows the results of training and testing calculations are presented in Fig. 3.

(21)

Figure 1. ARD of testing data versus neuron number in hidden layer.

Figure 2. Topology of the proposed neural network.

Figure 3. Cross plot graph of the results of training and testing calculations.

Surface tension of each hydrocarbon mixtures was further calculated by four aforementioned classical models: Brock and Bird (Eq. 1), Pitzer (Eq. 3), Zuo-Stenby (Eq. 4) and Sastri-Rao (Eq. 8). The mixing rules used in these four models were the same as the mixing rules used in artificial neural network method.

The accuracy of artificial neural network and four well-known classical models were tabulated in Table 4. They indicate that ARD of artificial neural network is 3.72223% while the ARD of Brock and Bird, Pitzer, Zuo-Stenby and Sastri-Rao models are 28.56102, 25.23901, 25.49967 and 13.58419 respectively.

One of the best advantages of artificial neural network is low dependency of accuracy of this method to the type of compounds. Classical methods give quite accurate results for some compounds while their answers for some other compounds may be very inaccurate. To have a quantitative measure of this quality, standard deviation parameter was calculated for each method which is presented in Table 4. The standard deviation of ARD for Brock and Bird, Pitzer, Zuo-Stenby and Sastri-Rao models are 23.77569, 18.44848, 13.00388 and 9.63137 respectively while standard deviation of ARD for artificial neural network is 3.63001.

Table 4. Accuracy of artificial neural network and four well-known classical models.

Compound

Brock –Bird [7]

Pitzer [20]

Zuo –Stenby [12]

Sastri –Rao [13]

ANN

Tetrachloromethane - iodomethane

2.7273

2.0888

17.3285

3.538

2.1173

Tetrachloromethane - nitromethane

10.1782

11.6841

19.9798

3.4726

2.356

Tetrachloromethane - methanol

41.3494

50.4831

50.631

15.6244

2.387

Tetrachloromethane - acetonitrile

1.8799

4.2103

16.5798

4.1368

9.9893

Tetrachloromethane - iodo-ethane

13.3881

10.2459

13.0284

11.7174

1.9742

Tetrachloromethane - nitroethane

7.4096

10.5393

13.6943

1.5743

1.3618

Tetrachloromethane - ethanol

27.1397

34.5764

37.6013

7.6215

0.9921

Tetrachloromethane - dimethylsulfoxide

13.8216

17.434

15.0959

8.1284

8.077

formic acid - acetic acid

28.1053

30.3465

15.0238

12.9732

1.2466

formic acid - pyridine

12.8345

11.2285

19.3833

22.2164

8.8339

formic acid - 2-methyl-aniline

5.4993

3.8937

26.2993

16.7077

0.0213

Iodomethane - acetic acid

33.716

36.5589

36.8824

15.3109

4.549

Nitromethane - acetic acid

32.0827

34.4518

19.3669

9.3977

1.2423

Nitromethane - benzene

92.2474

12.6289

10.7804

20.7877

7.4623

Nitromethane - cyclohexane

6.1214

7.8804

6.8466

2.93

0.8193

Methane - propane

37.3632

41.1241

25.4103

44.6959

2.4441

Methanol - acetic acid

57.8839

65.3992

43.6485

19.1128

13.4216

Methanol - ethanol

71.7885

25.3453

48.2051

21.9246

1.791

Methanol - dimethylsulfoxide

47.1162

56.4907

33.2154

16.2331

1.6447

Methanol - benzene

28.5681

40.259

40.9924

13.5803

1.7139

Average

28.56102

25.23901

25.49967

13.58419

3.72223

Standard Deviation

23.77569

18.44848

13.00388

9.63137

3.63001

4. Conclusion

In this study, artificial neural network was used to predict the surface tension of hydrocarbon mixtures. The accuracy of our proposed model was compared to four well-known empirical equations. It showed higher accuracy for the artificial neural network method. Also, results of standard deviation indicated that these empirical relations are so dependent on the type of compounds and some special parameters, while ANN is more independent. The optimized neural network parameters such as inputs and the number of neurons in hidden layers were presented for the calculation of surface tensions for the before mentioned compounds and can be used by other researchers in solving the problems which deal with the surface tension calculations.

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