Thermodynamic Study of Jojoba (Simmondsia Chinensis) Oil as a Function of Temperature

DOI : 10.17577/IJERTV6IS020168

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Thermodynamic Study of Jojoba (Simmondsia Chinensis) Oil as a Function of Temperature

Rebecca S. Andrade Departamento de Engenharia Química Universidade Salvador UNIFACS

41770-235 Salvador, Brasil Departamento de Engenharia Química Universidade Federal da Bahia

41210-630 Salvador, Brasil

André L. A. Simões

Ariana D. Andrade

Departamento de Engenharia Química Universidade Federal da Bahia

41210-630 Salvador, Brasil Miguel Iglesias

Departamento de Engenharia Química Universidade Federal da Bahia

41210-630 Salvador, Brasil

Departamento de Engenharia Ambiental Universidade Federal da Bahia

41210-630 Salvador, Brasil

Abstract This paper gathers a new experimental study of the temperature effect on different thermodynamic properties (density, refractive index, dynamic viscosity and ultrasonic velocity) of jojoba (Simmondsia Chinensis) oil. Halvorsens model, Gharagheizi´s group contribution method, Power Law and Collision Factor Theory were selected for prediction of these magnitudes, attending to ease of use and range of application of these thermodynamic magnitudes. Despite different molecular structural simplifications and application of molecular group contribution procedure for theoretical critical point estimation of the studied oil, the experimental thermodynamic data were accurately predicted at different temperatures.

KeywordsJojoba oil, Thermodynamic properties, Temperature, Theoretical model

  1. INTRODUCTION

    Jojoba, with the botanical name Simmondsia chinensis (it is the sole specie of the family Simmondsiaceae), and also known as wild hazel, goat nut, quinine nut, deer nut, pignut, and gray box bush, is native and endemic to Southwestern North America (California, Arizona, Utah (U.S. states) and Baja California (Mexico)). Jojoba is now cultivated in United States, Israel, Mexico, Peru, Australia, India, Egypt, Thailand, South West Africa, Costa Rica, Argentina, Chile and other countries. It has started to gain a lot of importance because of this unusual liquid wax, an ester of long unbranched chain fatty acids and alcohols, in fact, the only liquid wax known to be obtained from the vegetable world. The seeds obtained from the jojoba bush are the source for this liquid, commonly known as Jojoba Oil. The oil is obtained by pressing the seeds or by extraction with solvents. In the raw state it has a light yellow color. This oil is amazing rare in that it is an extremely long (C36C46) straight-chain wax ester and not a triglyceride, as it is common. The ester molecule has two double bonds, one at each side of the ester bond. Jojoba oil and its derivative esters are more similar to human sebum and whale oil than to traditional vegetable oils. With virtually no traces of

    glycerine during industrial processing (hydrogenation, sulfurization, halogenation, sulfurhalogenation, phosphosulfurization, ozonization, hydrolysis, amidation and many other techniques), the importance of jojoba oil in the global market is very high for industries like cosmetic, body-care, pharmaceutical, lubricant and petrochemicals. Jojoba oil is interesting for the industry because it is odorless oil, showing a curious almost temperature-independent viscosity and potential applications varying from lubrication uses to biofuel production [1]. Before developing any industrial application, it is imperative to have accurate and complete information about physico-chemistry and thermodynamic profile of the substances involved. Theoretical models and new procedures for estimation and simulation use experimental collections of thermodynamic data, and in what is referred to fats and oils, an important gap of accurate information is observed into technical and scientific open literature. As a continuation of previous papers related to oils characterization [2-5], we present a study of volumetric, optical, reologic and acoustic properties of jojoba oil. Halvorsens model [6-7], Gharagheizi´s group contribution method [8], Power Law [9-10] and Collision Factor Theory [11-12] were tested and the obtained results analyzed. These magnitudes were accurately estimated in the studied temperature range, despite molecular structural simplifications into the calculations and the application of molecular group contribution procedures for theoretical critical point estimation of the studied oil.

  2. EXPERIMENTAL

    1. Materials and measurement devices

      The oil was supplied by regional providers (Provital SA, Spain-S.G.S. International Eco Oil Argentina S.A, Argentina, Natural Jojoba Oil FP-35 Golden), and stored in sun light protected form and constant humidity and temperature. It was analyzed to determine their fatty acids compositions [4]. The average molar mass was computed as follows:

      M N

      x .M

      • P y .M

      (1)

      whole range of temperature. In Figure 2, 3 and 4, the

      oil

      i

      i1

      i

      Fatty _ Acids

      i

      i1

      i

      Alcohols

      temperature trend of refractive index, dynamic viscosity and ultrasonic velocity are enclosed. As previously commented

      being xi the molar fraction of fatty acids, yi the molar fraction of alcohols and Mi the molar mass of each fatty acid without a proton and each alcohol without a OH group. N is the number of fatty acids and P the number of alcohols found by analysis. The variation in the composition between different samples affects mainly the mono and polyunsaturated fatty acids, the change in molar mass being lower than ±1 g mol-1. The molar mass, alcohols/fatty acids composition, thermodynamic profile and open literature data are gathered in Table 1 [13- 20]. Densities and ultrasonic velocities were measured with an Anton Paar DSA-48 vibrational tube densimeter and sound analyser, (resolution of 10-5 gcm-3 and 1 ms-1), with accuracy in temperature better than 10-2 K by means of a Peltier control device. Refractive indices were measured with a Mettler RE50 refractometer with an uncertainty of 0.00005, and temperature was controlled as described above. The dynamic viscosities were measured with an Anton Paar AMV

      200 rolling ball viscometer with an accuracy of 0.5%, controlling temperature by a Polyscience 9001 thermal bath. Earlier works describe the experimental procedure usually applied in our laboratory [2-4].

    2. Data treatment

      The measured magnitudes were correlated as a function of temperature using Eq. 2:

      upon, disposable open literature of refractive index offers divergent values at the same experimental condition. While the experimental collections of Bagby, 1988, Spencer and List, 1988, El Bassam, 2010, and Arya and Khan, 2016, are coincident with our new measurements, previous values of Hussein et al., 2014 are really out of trend for this range of temperature (Figure 2).

      TABLE I: Thermodynamic profile of jojoba oil, open literature values, properties correlation parameters and models deviations

      N

      P

      i0

      A Ti

      Molar mass (gmol-1)

      653.905

      Fatty Acids Composition (mass%)

      Vaccenic (18:1): 1.1

      Stearic (18:0): 0.1

      Palmitoleic (16:1): 0.2

      Behenic (22:0): 0.2

      Palmitic (16:0): 1.2

      Oleic (18:1): 10.1

      Gadoleic (14:0): 71.3

      Erucic (22:1): 13.6

      Nervonic (24:1): 1.3

      Linoleic (18:2): 0.1

      Heptadecenoic (17:1): 0.1

      Arachidic (10:0): 0.1

      Alcohols Composition (mass %)

      Hexadecanol: 0.1

      Octadecanol: 0.2/p>

      Octadec-11-enol :0.4

      Octadec-9-enol: 0.7

      Docosanol: 1.0

      Tetracos-15-enol: 8.9

      Eicos-ll-enol: 43.8

      Docos-13-enol: 44.9

      Density (298.15 K)

      (gcm-3)

      0.861447

      0.84 (Wisniak, 1987) 0.8657 (Baldwin, 1988) 0.863 (El Bassam, 2010)

      0.863 (Abdelfatah et al., 2012)

      0.860 (Hussein et al., 2014)

      0.865705 (Arya et al., 2016)

      Refractive index (298.15 K)

      1.46434

      1.4650 (Bagby, 1988)

      1.4650 (El Bassam, 2010)

      1.460 (Hussein et al., 2014) 1.46491 (Arya et al., 2016)

      Dynamic viscosity (298.15 K)

      (cp)

      34.99

      58 (Bagby, 1988)

      35.97 (Spencer and List, 1988) 50 (Abdelfatah et al., 2014)

      35.71 (Arya et al., 2016)

      Ultras. veloc. (298.15 K)

      (ms-1)

      1395.11

      Density correlation parameters (Eq. 2)

      A0= -1.778355

      A1= 0.027251

      A2= -9.182365e-5

      A3= 1.010240e-7

      = 4.81188E-07

      Refractive index correlation parameters (Eq. 2)

      A0= 1.480721

      A1= 5.994956e-4

      A2= -3.298073e-6

      A3= 3.699800e-9

      = 3.67700e-6

      Dynamic viscosity correlation parameters (Eq. 2)

      A0= 12334.550748

      A1= -111.902568

      A2= 0.340018

      A3= -3.45656e-4

      = 5.10000e-3

      Ultrasonic velocity correlation parameters (Eq. 2)

      A0= 7195.865767

      A1= -47.105522

      A2= 0.133443

      A3= -1.34422e-4

      = 4.85635e-4

      Deviations of Halvorsen´s

      model at 288.15-323.15 K

      = 0.055158

      (2)

      i

      where P is density (gcm-3), refractive index, dynamic viscosity (cP) or ultrasonic velocity (ms-1), T is absolute temperature in Kelvin and Ai are fitting parameters. N stands for the extension of the mathematical serie, optimized by means of the Bevington test. The fitting parameters were obtained by the unweighted least squared method applying a fitting Marquardt algorithm. The root mean square deviations were computed using Eq. 3, where z is the value of the property, and nDAT is the number of experimental data.

      nDAT

      z

      exp

      • zpred

      1/ 2

      2

      i1

      (3)

      nDAT

      Fitting parameters (Eq. 2) and the root mean square deviations (Eq. 3) are gathered in Table 1. In Figure 1, the temperature trend of the experimental density is gathered with the disposable literature data [13-20]. This figure shows a diminution of density when temperature rises, due to a strong diminution of the packing efficiency by molecules kinetics, as well as, a growing difficult of packing molecules by steric hindrance into bulk liquid phase. Only the values at 298.15 K of Bagby, 1988, El Bassam, 2010, Hussein et al., 2014 and Abdelfatah et al., 2014 are coincident with our measurements. The other collections of Spencer and List, 1988 and Arya and Khan, 2016, overestimate the jojoba oil density until 333.15 K, offering an almost linear trend at the

      0,87

      Density / (g cm -3)

      0,86

      0,85

      Bagby, 1988

      El Bassam, 2010

      Hussein et al., 2014

      Abdelfatah et al., 2014 Baldwin, 1988

      Spencer and List, 1988

      Analogously, in Figure 3 for dynamic viscosity, the values of Bagby, 1988 or El Bassam, 2010, are completely amazing if compared with the collections of Spencer and List, 1988, Arya and Khan, 2016 or our experimental data, which show clearly the low temperature dependence of jojoba oil dynamic viscosities, as commented in previously published works. In what is referred to ultrasonic velocity for jojoba oil, no available open literature values were found, then our experimental data are the first measurements published, as far as we know. As observed in Figure 4, a decreasing linear tendency was observed for rising temperatures, which is coincident with other previously studied oils [3-4].

      Deviations of Gharagheizi´s

      model at 298.15 K

      = 0.00638

      Deviations of Power Law´s model at 288.15-323.15 K

      = 0.1208

      Deviations of Collision Factor

      Theory at 298.15 K

      = 151.0302

      1500

      0,84

      0,83

      Experimental data of this paper

      Wisniak, 1987

      Arya and Khan, 2016

      280 290 300 310 320 330 340 350

      Temperature / (K)

      1480

      Ultrasonic velocity / (ms-1)

      1460

      1440

      1420

      1400

      Figure 1: Experimental density and open literature data for jojoba oil

      1,470

      Bagby, 1988

      El Bassam, 2010

      1380

      1360

      1340

      Experimental data of this paper

      1,465

      Refractive index

      1,460

      Hussein et al., 2014

      Arya and Khan, 2016

      1320

      280 290 300 310 320 330 340 350

      Temperature / (K)

      1,455

      1,450

      1,445

      Experimental data of this paper

      Spencer and List, 1988

      280 290 300 310 320 330 340 350

      Temperature / (K)

      Figure 4: Experimental ultrasonic velocity and open literature data for jojoba oil

    3. Isobaric expansibility

    A frequently applied derived quantity for industrial mixtures is the temperature dependence of volumetric properties, expressed as isobaric expansibility or thermal expansion

    coefcient (). The data reported in the literature normally

    Figure 2: Experimental refractive index and open literature data for jojoba oil

    140

    120 El Bassam, 2010

    100

    show only values of the thermal expansion coefcients both of pure compounds and its mixtures, showing the relative changes in density, calculated by means of (-/) as a function of temperature, and assuming that remains constant over the temperature range. The variable can be computed by the following equation:

    Refractive index

    80 Bagby, 1988

    ln

    60

    40

    20 Arya and Khan, 2016

    Spencer and List, 1988

    T

    P, x

    (4)

    0 Experimental data of this paper

    280 300 320 340 360 380 400

    Temperature / (K)

    Figure 3: Experimental dynamic viscosity and open literature data for jojoba oil

    0,5

    0,4

    requiring critical magnitudes for the enclosed fatty acids. If these magnitudes are not known, they must be estimated as indicated. The method of Halvorsen is described as follows for jojoba oil:

    103 Isobaric expansibility / (K-1)

    0,3

    N x .M P

    y .M

    i i i i

    0,2

    i1 Fatty _ Acids i1 Alcohols

    2

    (5)

    R Tc,oil Z

    [1(1Tr ) 7 ]

    0,1

    P

    Ra,oil

    0,0

    -0,1

    Experimental data of this paper

    where

    N

    c,oil

    P

    xi .Tci yi .Tci

    -0,2

    Tc,oil i1 Fatty _ Acids i1 Alcohols

    (6)

    280 290 300 310 320 330 340 350

    P N

    P

    Temperature / (K)

    c,oil

    x .P

    y .P

    Figure 5 Isobaric expansibility of jojoba oil at different temperatures

    i1

    i ci

    Fatty _ Acids

    i1

    i ci

    Alcohols

    Figure 5 shows the isobaric expansibility of the jojoba oil as a

    Z

    1 N

    x .Z

    • P y .

    (7)

    function of temperature. As observed, the isobaric

    expansibility diminishes for rising temperatures from 288.15

    Ra,oil

    2 i

    i1

    Rai

    Fatty _ Acids

    i

    i1

    Rai

    Alcohols

    K until 297.65 K. From this temperature, the isobaric expansibility rises progressively for increasing temperatures. It is important to highlight as this magnitude reaches negative values around standard condition (from 292.65 to 306.90 K).

    TABLE II: Estimated critical properties for the enclosed fatty acids and alcohols into the jojoba oil by Constantinou and Gani method [21]

    where is the oil density, xi is the mole fraction of fatty acids and yi is the mole fraction of alcohols into that oil, Mi is the molar mass of each fatty acid or alcohol, R is the universal constant of gases, Pci is the critical pressure of each fatty acid or alcohol and Tr is the reduced temperature. ZRa is the Rackett factor of each fatty acid or alcohol [22] (Table II). The mixing rule to compute the pseudocritical temperature, and then the reduced temperature of the oil is described as follows:

    T

    N

    Fatty acids and alcohols

    Pc(MPa)

    Tc(K)

    Zra

    Heptadecenoic

    13.484

    789.59

    0.2267

    Palmitic

    14.307

    780.38

    0.2076

    Palmitoleic

    14.617

    781.32

    0.2083

    Oleic

    12.802

    797.50

    0.1999

    Linoleic

    13.059

    798.36

    0.2006

    Nervonic

    9.0218

    838.86

    0.1939

    Stearic

    12.553

    796.65

    0.1993

    Arachidic

    11.133

    811.57

    0.1917

    Erucic

    10.005

    826.09

    0.2005

    Behenic

    0.997

    825.36

    0.1848

    Gadoleic

    11.190

    812.36

    0.2172

    Vacenic

    12.6373

    797.50

    0.2142

    Hexadecanol

    12.876

    762.34

    0.2093

    Octadecanol

    12.091

    771.51

    0.2059

    Octadec-11-enol

    12.326

    772.49

    0.2068

    Octadec-9-enol

    12.326

    772.49

    0.2068

    Docosanol

    9.636

    804.13

    0.1925

    Tetracos-15-enol

    8.847

    819.25

    0.1870

    Eicos-ll-enol

    10.569

    819.36

    0.2039

    Docos-13-enol

    9.796

    804.95

    0.1934

    Tr

    i ci

    i ci

    (8)

    i 1

    x .T

    P

    Fatty _ acids

    i 1

    y .T

    Alcohols

    C. Prediction of refractive indices

    Gharagheizi´s group contribution model was applied for refractive index estimation [8]. This model is, until now, that using the larger database to compute the interaction contributions of the chemical substructures, showing a more robust trend than any other previously tested. Based in 80 chemical structure contributions, the model computes the refractive index using the following equation:

    80

  3. MODELING

    nD ni nDi nD0 i1

    (9)

    1. Critical point prediction

      The Constantinou and Gani method (CG method) [21] is an advanced group contribution method for critical point estimation, based on the UNIFAC molecular groups. It was applied to obtain the critical point of the fatty acids, and then used into the prediction methods (Table II).

    2. Prediction of densities

    Despite the success developing different procedures of density estimation, only a few of them may be of real application for

    where nD0 and nDi are the intercept of the equation, the contribution of the ith chemical substructure to the refractive index of the compound, and ni is the number of occurrences of the ith chemical substructure in every chemical structure of the pure compound, respectively.

    1. Prediction of dynamic viscosities

      The temperature dependence of viscosity of oils should be reasonably described by the Power Law equation [9-10]. The Power Law equation is expressed as:

      fats and oils into food technology. One proposed correlation

      T T

      that holds promise for application to oils is the Rackett equation of state. The modification of this equation by Halvorsen et al. [6-7] has demonstrated to be accurate, only

      0 x

      Tx

      (10)

      where is the dynamic viscosity of the oil and T is the

      ACKNOWLEDGMENT

      absolute temperature.

      , T , and are parameters that

      André Simões would like to acknowledge PROPCI (Pró-

      0 x Reitoria de Pesquisa, Criação e Inovação) for its support in

      depend on the reology of the fluid.

    2. Prediction of ultrasonic velocities

    In terms of fats and oils, ultrasonic measurements are extremely rare. As above indicated, the experimental measurements for ultrasonic velocity enclosed into this paper are the first into open literature. The experimental data were compared with the values obtained by the Collision Factor Theory (CFT) [11-12], which is dependent on the collision factors among molecules as a function of temperature:

    u u .Soil.Boil (11)

    V

    where

    developing this research.

    Ariana D. Andrade and Rebecca Andrade would like to acknowledge PIBIC-UFBA (Programa de Bolsas de Iniciação Científica – UFBA) and CAPES (Coordenação de Aperfeiçoamento de Pessoal de Nível Superior) for grants support.

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      The collision factors (S) were estimated by Eq. 11, using Wada method for estimation of ultrasonic velocity of each fatty acid and alcohol [24]. The deviations for jojoba oil by CFT method are gathered in Table I.

  4. CONCLUSIONS

This paper contains the results of a new experimental study of the effect of temperature on density, refractive index, dynamic viscosity and ultrasonic velocity for jojoba (Simmondsia Chinensis) oil. Halvorsens model for density, Gharagheizi´s group contribution model for refractive index, Power Law for dynamic viscosities and Collision Factor Theory for ultrasonic velocity were selected for prediction of these thermodynamic properties, attending to ease of use and range of application. As a whole, the studied models are, at least, of qualitative accuracy in terms of prediction. Deviations yielded for these thermodynamic magnitudes at the studied range should be considered as a satisfactory result, supporting their validity as predictive tools despite molecular structural simplifications into the calculations and the application of procedures for theoretical critical point estimation of the studied oil.

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