Introduction
Lately, due to environmental issues and more restrictive environmental laws, there has been a strong demand for “environmentally friendly" lubricants with as little negative impact as possible. In this context, lubricants obtained from plants are in the attention of tribologists, their main advantages being the relatively inexhaustible source, non-toxicity and biodegradability [1-6]. The problem is that, in addition to these advantages, the disadvantages are not to be neglected either: poor lubricating properties, instability to oxidation. Vegetable and animal oils are considered liquid lubricants and are chemically glycerin compounds with fatty acids. They consist of fatty acid fragments bound by an ester with glycerol (the result being triglycerides) [7-12]. May also contain in the raw state: phospholipids (8%), glycolipids (5%), sterile esters and sterols (5%), mono or diglycerides and free fatty acids (2%), waxes and other hydrocarbons (1%), but by various processes they can be totally or partially eliminated. Refined vegetable oils have a fairly uniform chemical composition compared to mineral ones and can be classified according to the fatty acids contained:
– saturated acids (without double bonds) myristic, palmitic, stearic acid, etc.,
– monounsaturated acids (double-linked only): oleic, erucic,
– polyunsaturated acids (with several double bonds): linoleic, linolenic,
– special acids (contain hydroxy, epoxy radicals, etc.).
Vegetable oils with high oleic acid content can be considered as highly monounsaturated, thus having better properties at low temperatures compared to other saturated vegetable oils.
Castor oil is obtained from the seeds of the castor plant, of which several varieties are known, the most cultivated being Ricinus communis and Ricinus sanguineus. The plant is native to India and has been acclimatized to South America, the USA, Italy, Turkey and France. In Romania it has been cultivated since 1930, with satisfactory results, but being a tropical plant requires a warmer, longer period of time for ripening. The regions where castor has been best cultivated are: Dobrogea, southern Muntenia and Oltenia, Bărăgan, and especially in calcareous soils. Castor oil is obtained by cold and hot pressing the grains, the yields generally differ from the theoretical ones, the qualitative assessment of the seeds being made after the manufacturing yields. Under correct technical conditions, an oil yield of 39… 40% is obtained from almost all assortments. Due to the high viscosity, high flammability and strong polar character, with high adhesion to the metal, castor oil has long been used simply or mixed with mineral oils to lubricate aircraft engines. Castor oil obtained by cold pressing is used in medicine, and that obtained by hot pressing for industrial uses. Castor oil is also obtained by extraction with gasoline without light fractions, but with some difficulties and can only be used for technical purposes. Castor oil contains 80-85% glycerides of hydroxyoleic oil, the rest being glycerides of palmitic and stearic acids. When castor oil comes from wet and partially degraded castor beans and is dark in color, it must be refined. The high viscosity causes some difficulties in the refining process.
The object of this paper is to determine the rheological behaviour for castor oil at shear rates ranging between 3 and 120 s-1 and temperatures ranging between 40 and 100oC.
Material and Methods
The castor oil used in this work is provided by a company in Bucharest, Romania. In this paper we studied only castor oil not additives.
Castor oil have been investigated using a Haake VT 550 Viscotester developing shear rates ranging between 3 and 120s-1 and measuring viscosities from 104 to 106 mPa.s when the HV1 viscosity sensor is used. The temperature ranged between 40 and 1000C and the measurements were made from 10 to 100C. The accuracy of the temperature was 0.10C [5-13].
Results and Discussion
Figure 1 shows the dependence of the dynamic viscosity of the shear speed at all the temperatures at which the castor oil has been was studied. The curves obtained exhibit an exponential decrease at low temperatures and at high temperatures the decrease becomes less significant.
Figure 1: Dependence dynamic viscosity versus shear rate at temperature for castor oil: B-400C, C-500C, D-600C, E-700C, F-800C, G-900C and H-1000C
Figure 2 shows the reograms of castor oil at all temperatures at which the oil was studied. From the graphical representation of the dependence of the shear rate and the shear voltage, straight lines are obtained which have different slopes depending on the temperature at which the oil was studied. The highest slope is at 400C and the smallest at 1000C.
Figure 2: Rheograms for oil castor at temperature: B-400C, C-500C, D-600C, E 700C, F-800C, G-900C and H-1000C
Figure 3 shows the log dependence of dynamic temperature viscosity at all shear rates. The straight with the highest slope is at the shear speed 3.3s-1, and the smallest slope is at 120s-1.
Figure 3: Dependence log dynamic viscosity versus temperature at shear rate: B-3.3s-1, C-6s-1, D-10.6s-1, E-17.87s-1, F-30s-1,G-52.95s-1, H-80s-1 and I-120s-1
Figure 4 shows the dependence of the dynamic viscosity as on the correlation coefficients at all the temperatures at which the castor oil was studied. All correlation coefficients have values close to the one value.
Figure 4: Dependence dynamic viscosity versus R2 at temperature: B-400C, C-500C, D-600C, E-700C, F-800C, G-900C and H-1000C
If the temperature is plotted as a function of correlation coefficients, a reduction of the values of the correlation coefficients to the values of 0.985-0.990 is being can ben observed.
Conclusions
In this article I have presented the rheological characteristics of castor oil used as a biodegradable lubricant. The rheograms of castor oil have quite different slopes. The highest slope is at shear speed 3.3s-1, and the smallest slope is at 120s-1.
From the representation of the dependence of the dynamic viscosity on the correlation coefficients at all the temperatures at which the castor oil has been was studied, the correlation coefficients have values close to the one value. The correlation coefficients have get values between 0.985-0.990.
1. Alonso M.L., Garzon E., Melcon B., Zapico J. 1990, Alimentaria, 27(213), 53-57.
2. Rao M.A 1977, Journal Texture Studies, 8, 135-168.
3. Rao M.A., Cooley J.H. 1992, Journal Texture Stu-dies, 23, 415-425.
4. Rosen R.M., Forster W.E. 1978, Journal Coating Technology, 50, 456-468.
5. Stanciu I., 2018, Journal of Science and Arts, 1(42), 197-202.
6. Moretto E., Fett R. 1998, Tecnologia de oleos e gorduras vegetais na industria de alimentos, Sao Paolo, Varela, 43–156.
7. Santos J.C.O., Santos I.M.G., Souza, A.G. 2005, Journal of Food Engineering, 67, 401.
8. Eiteman M.A., Goodrum J.W. 1993, Transactions ASAE, 36, 503-507.
9. Stanciu I. 2017, Journal of Science and Arts, 4(41), 771-778.
10. Stanciu I. 2018, Journal of Science and Arts, 2(43), 443-458.
11. Femlab, Chemical Engineering Module, Version 2.3.COMSOL AB.2002.
12. Goodrum J.W., Geller D.P., Lee S.A. 1998, Thermochimica Acta, 311, 71-.79.
13. Stanciu I., 2012, Analele Universitatii “Ovidius" Constanta – Seria Chimie, 23(1), 27-30.
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Abstract
In this article I have presented the rheological characteristics of castor oil used as a biodegradable lubricant. The rheograms of castor oil have quite different slopes. The highest slope is at shear speed 3.3s-1, and the smallest slope is at 120s-1. From the representation of the dependence of the dynamic viscosity on the correlation coefficients at all the temperatures at which the castor oil has been was studied, the correlation coefficients have values close to the one value. The correlation coefficients have values between 0.985-0.990.
You have requested "on-the-fly" machine translation of selected content from our databases. This functionality is provided solely for your convenience and is in no way intended to replace human translation. Show full disclaimer
Neither ProQuest nor its licensors make any representations or warranties with respect to the translations. The translations are automatically generated "AS IS" and "AS AVAILABLE" and are not retained in our systems. PROQUEST AND ITS LICENSORS SPECIFICALLY DISCLAIM ANY AND ALL EXPRESS OR IMPLIED WARRANTIES, INCLUDING WITHOUT LIMITATION, ANY WARRANTIES FOR AVAILABILITY, ACCURACY, TIMELINESS, COMPLETENESS, NON-INFRINGMENT, MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE. Your use of the translations is subject to all use restrictions contained in your Electronic Products License Agreement and by using the translation functionality you agree to forgo any and all claims against ProQuest or its licensors for your use of the translation functionality and any output derived there from. Hide full disclaimer