ISSN : 0970 - 020X, ONLINE ISSN : 2231-5039
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Study of Rheological Behavior of Olive Oil Used as Biodegradable Lubricant

Ioana Stanciu

University of Bucharest, Faculty of Chemistry, Department of Physical Chemistry, 4-12 Elisabeta Blvd, 030018, Bucharest, Romania.

Corresponding Author E-mail: Istanciu75@yahoo.com

DOI : http://dx.doi.org/10.13005/ojc/370533

Article Publishing History
Article Received on : 16-Jul-2021
Article Accepted on : 15-Sep-2021
Article Published : 16 Sep 2021
Article Metrics
Article Review Details
Reviewed by: Dr. A. Leema Rose
Second Review by: Dr. Andrei Klyndyuk
Final Approval by: Dr. Attilio Naccarato
ABSTRACT:

In this article, based on experimental data, we obtained three dependence relations of dynamic viscosity versus temperature by polynomial and exponential fitting. The correlation coefficients have values close to unity which proves that the obtained relations accurately describe the non-Newtonian behavior of olive oil.

KEYWORDS:

Lubricant; Olive; Rheology

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Introduction

Olive oil can be obtained by one of the following methods: chemical extraction involves treating the olives with chemicals (various organic solvents) that help separate the oil from the other components of the olives.

Mechanical extraction by hot pressing in which the olives are pressed to squeeze the oil from them. It is called “hot pressing” because during this process the heat is released and the olive paste is heated.

Mechanical extraction by cold pressing, which unlike hot pressing, this process involves pressing the olives and squeezing the oil from them in a controlled environment, which ensures a low temperature. This method is also the one through which the oil keeps most of its nutrients.

Furthermore, the process of obtaining olive oil may involve refining. By refining, however, a significant amount of nutrients is lost from the oil. Refining involves treating the oil – with chemicals, exposure to very high temperatures – the purpose of this process being to remove impurities. Refining olive oil increases its shelf life, but also fades its flavors. However, you can also find raw, unrefined olive oil, with an intense olive aroma and a higher acidity.

Both virgin and extra virgin olive oil are obtained by cold mechanical methods, so without the use of chemical solvents. Both types have the same level of antioxidants and nutrients, but differ in oleic acid concentration. At a concentration of up to 0.8% oleic acid, the oil is considered extra virgin, and between 0.8 and 2% is considered virgin.

As you saw above, olive oil can be of several kinds and, depending on how it is produced, it can provide you with a different level of nutrients. No matter what type of olive oil you choose, it is certain that you will have most of the benefits of this product. It is ideal to have in the house both a refined olive oil, which you can use for cooking, and a virgin or extra virgin olive oil for salads, soups, cold sauces, etc.

Problems choosing olive oil arise when we talk about counterfeit products, which contain chemicals meant to mimic the color, taste and density of olive oil, but which have a much lower price. Here are some ways you can make sure the olive oil you plan to buy is truly quality 1-14.

Andrade equation showing the dependence of dynamic viscosity versus temperature 14, 15, 16, 17, 19:

By logarithm equation (1) we obtain

The last equation is used for making linear the equation (1).

Esteban et al. [16] recommend the Azian equation (3) [18,19], they introduced another equation with three constants:

where T is the absolute temperature and A, B and C are constant of the material.

In this article we found three relationships of viscosity dependence temperature by fitting experimental data. The polynomial and exponential relations found starting from the Andrade equation accurately describe the non-Newtonian behavior of olive oil.

Material and methods

Olive oil is a liquid fat obtained from olive produced by pressing whole olives and extracting the oil. Olive oil was obtained by hot pressing. At a concentration of up to 0.8% oleic acid, the oil is considered extra virgin. Extra virgin olive oil produced in Romania was studied with the Haake VT 550 viscometer equipped with a VH1 sensor for shear speeds between 3 and 120s-1 and viscosities dynamic between 104 and 106 mPa.s. The determinations were made at temperatures between 40 and 100 from 10 to 100C.

The physico-chemical characteristics of the olive oil are: refraction index 1.4677– 1.4705; the mass fraction of water and volatile substances 0.2%, the mass fraction of the impurities other than those from the fats (mass sediment) 0.1%, saponification index = 184- 196 mg KOH/g, iodine index = 75-94 g I2/100g, mass fraction of non-saponifiable substances max 15%, relative density at 20ºC = 0.910 – 0.916; 20 mmol oxigen activ/kg.

Result and discussion

Rheograms 1, 2 and 3 of olive oil at shear rates of 6 s-1, 17.87 s-1 and 52.95 s-1. There is a decrease in dynamic viscosity with temperature and shear rate at high temperatures due to the orientation of the oil molecules.

Figure 1: Rheogram of olive oil at shear rate of 6 s-1

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Figure 2: Rheolgram of olive oil at shear rate of 17.87 s-1

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Figure 3: Rheogram of olive oil at shear rate of 52.95 s-1

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The decrease in dynamic viscosity is more pronounced in the temperature range 40-600C degrees Celsius compared to the temperature range 60-1000C. At the shear rate of 52.95 s-1 the decrease is 63%, in the temperature range of 30ºC – 60ºC. For the temperature range of 60ºC – 100ºC, the decrease is 44.4%.

Equations (4) – (6) were obtained by polynomial and exponential fitting of the experimental data of olive oil. 20

The parameters of equations A, B, C and D as well as the correlation coefficients are included in tables 1,2, and 3.

The correlation coefficients have values between 0.8754 and 0.9999.

where T is the absolute temperature and A, B, C and D are constant of the material.

Table 1: Parameters equation (4) and correlation coefficient R2 [20]

Shear rate,

s-1

Correlation parameters (eq. 4)

Correlation coefficient, R2

A

B

C

3.30

1077.6917

-5.9273

0.0083

0.9475

6.00

941.3095

-5.2266

0.0074

0.8942

10.60

739.5499

-4.0639

0.0057

0.9177

17.87

628.4163

-3.4335

0.0048

0.9045

30.00

682.6112

-3.7636

0.0053

0.8772

52.95

705.4780

-3.8999

0.0055

0.9077

80.00

702.5944

-3.8844

0.0054

0.8754

120.0

208.7929

-1.0777

0.0014

0.9886

Table 2: Parameters equation (5) and correlation coefficient R2 [20]

Shear rate,

s-1

Correlation parameters (eq.5)

R2

A

B

C

D

3.30

9947.2339

-83.8129

0.2358

-2.21111E-4

0.9874

6.00

11337.3934

-96.517

0.2740

-2.59167E-4

0.9842

10.60

8427.9721

-71.5778

0.2029

-1.91667E-4

0.9793

17.87

8428.2649

-71.9260

0.2049

-1.94444E-4

0.9807

30.00

9429.5843

-80.5796

0.2296

   -2.18056E-4

0.9740

52.95

8705.8941

-74.1537

0.2107

-1.99444E-4

0.9886

80.00

9460.7101

-80.7917

0.2300

   -2.18333E-4

0.9685

120.0

1230.8024

-9.9127

0.0269

   -2.43519E-5

0.9925

Table 3: Parameters equation (6) and correlation coefficient R2 [20]

Shear rate,

s-1

Correlation parameters (eq.6)

R2

η0

A

B

3.30

15.4796

   7.42971E15 

9.3010

0.9868

6.00

12.2465

1.50282E13

11.3020

0.9842

10.60

10.6018

9.44701E11

12.5041

0.9859

17.87

9.4467

1.11163E10

15.1372

0.9696

30.00

9.0584

1.19194E11

13.5677

0.9617

52.95

8.3325

1.96634E11

13.2852

0.9809

80.00

8.1306

2.28666E12

12.0368

0.9703

120.0

7.9697

1.9415E13

12.0548

0.9658

 

Conclusion

The article proposes three relations obtained by exponential and polynomial fitting of the experimental data starting from the Andrade equation. The relationships found accurately describe the curves obtained so the correlation coefficients are close to unity.  The correlation coefficients are close to unity which shows that the three equations found accurately describe the behavior of olive oil.

Acknowledgement

None

Conflict of interest

None

References

  1. Crudu I., 2008, Tribosistem-Tribomodel în studiul sistemelor mecanice, Galaţi University Press, Galaţi.
  2. Hohn B.R., Michaelis K., Dobereiner R., 1999, Lubr. Eng., p. 15.
  3. Aguilera M.P., Beltran G., Ortega D., Fernandez A., Jimenez A., Uceda M., 2005, Food Chemistry, 89, 387-391.
    CrossRef
  4. Gouveia J.M.B., 1997, OLIVAE, 66, 34-45.
    CrossRef
  5. Dais P., Hatzakis E., 2013, Analytica Chimica Acta, 765, 1-27.
    CrossRef
  6. Lazzez A., Perri E., Caravita M.A., Khlif M., Cossentini M., 2008, Journal of Agricultural and Food Chemistry, 56, 982-988.
    CrossRef
  7. Kandylis P., Vekiari A.S., Kanellaki N., Kamoun Grati N., Msallem M., Kourkoutas Z., 2011, Food Science and Tehnology, 44, 1333-1341.
    CrossRef
  8. Vekiari S.A., Papadopoulou P., Kiritsakis A., 2007, Grasas Y Aceites, 58, 237-242.
    CrossRef
  9. Stanciu I.,  2011, Journal of Science and Arts, 1, 55-58.
  10. Goodrum J.W., Law S.E., 1982, Am. Soc. Agic. Eng, 897-900.
    CrossRef
  11. Mustafa E.T., Gerpen J.H.V., 1999,  J. Am. Oil Chem. Soc., 76, 1511-1513.
    CrossRef
  12. Kosmert T., Abramovic H., Klofutar C., 2000,  J. Food Eng., 46, 165-171.
    CrossRef
  13. Wan Nik W., Ani F.N., Masjuki H.H., Eng Giap S.G., 2005, Industrial Crops and Products, 22, 249-255.
    CrossRef
  14. Rodenbush C.M., Hsieh F.H., Viswanath D.S., 1999, J. Am. Oil Chem. Soc., 76-141.
    CrossRef
  15. Krisnangkura K., Yimsuwan T., Pairintra R., 2006, Fuel, 85-107.
    CrossRef
  16. Esteban B., Riba J.R., Baquero G., Rius A., Puig R., 2012, Biomass and Bioenergy, 42, 164-171.
  17. Stanciu I., 2013, Journal of Science and Arts, 4(25), 355-360.
    CrossRef
  18. Azian M.N., Kamal A.A.M., Panau F., Ten W.K., 2001, J. Am. Oil Chem. Soc., 78, 1001.
  19. Solea L.V., Deleanu L., Georgescu C., 2013, Mechanical Testing and Diagnosis, 3, 44-48
  20. Stanciu I., 2012,  Ovidius University Annals of Chemistry, 23(1), 27-30.
    CrossRef

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