See discussions, stats, and author profiles for this publication at: https://www.researchgate.net/publication/313367774

Methods for oil obtaining from oleaginous materials
Conference Paper · November 2016

CITATIONS

READS

0

8,040

5 authors, including:
M. Ionescu

Valentin Vladut

Australian Nuclear Science and Technology Organisation

National Institute of Research - Development for Machines and Installations Desig…

253 PUBLICATIONS 3,958 CITATIONS

357 PUBLICATIONS 1,050 CITATIONSSEE PROFILESEE PROFILE

Nicoleta Ungureanu

Mirela Dincă

Polytechnic University of Bucharest

Polytechnic University of Bucharest

209 PUBLICATIONS 733 CITATIONS

76 PUBLICATIONS 263 CITATIONSSEE PROFILE

All content following this page was uploaded by Nicoleta Ungureanu on 06 February 2017.
The user has requested enhancement of the downloaded file.

SEE PROFILEAnalele Universităţii din Craiova, seria Agricultură – Montanologie – Cadastru (Annals of the University of Craiova - Agriculture,
Montanology, Cadastre Series) Vol. XLVI 2016

METHODS FOR OIL OBTAINING FROM OLEAGINOUS MATERIALSIONESCU M.1), VLĂDUȚ V.2), UNGUREANU N.1), DINCĂ M.1),
ZĂBAVĂ B.ST.1), ȘTEFAN M 1)
1)

U.P. Bucharest / Romania; 2)INMA Bucharest;
E-mail: maneamaryana@yahoo.com

Keywords: oil, oleaginous materials, oil extraction, extraction methods, extraction efficiency

ABSTRACT
Lipids are an important component in human food since ancient times, having a
positive influence on the health of the human body. Thus, cultivation of oleaginous
materials is an important component of the global economy. To obtain vegetable oils fromoleaginous materials can be used different methods existent on the global scale. The
method used is chosen depending on the type of oleaginous material subjected toprocessing, on the oil quality that we want to achieve and on the amount of oil that wewant to extract. This paper presents an analysis of the literature, describing the various
existing methods for obtaining vegetable oil.

INTRODUCTION
The oleaginous materials production on global scale presents a continuous
increasing demand in the next years, due to the higher edible oil consumption, thedevelopment of the biofuels industry and the needs for green chemistry, [7].
In plants, fatty matter is concentrated only in some parts such as seeds, fruits andtubers, stone fruits, sprouts, representing a reserve substance that the plant uses during
its development as a source of energy. Although the oilseeds field is very wide, plants thatcan be used as raw material in vegetable oils industry are slightly because many of them
have low oil content - being unprofitable, others with higher oil content present difficulties
in oil extraction because of the special structure of the plant, [4].
Of more than 110 species of oleaginous plants, on the world market there arepresently about 50, grouped in 15 important botanical families, namely: compositae(sunflower), cruciferae (rape), leguminous plants (soya), malvaceae (cotton),
papaveraceae (poppy), rozaceae (almond tree, hazel tree), peduliaceae (sesame),
vitaceae (grape seed), jugladaceae (nut tree), palmae (oil palm, coconut palm, palm
kernel), foleaceae (olive tree), linaceae (flax), cucurbitaceae (pumpkin seeds),
leufobiaceae (castor oil plant) and solanaceae (tomato seeds, tobacco seeds), [6].
In our country, the main raw material is represented by the oleaginous plants which
produce seed. The oil can be obtained from different categories of plants: plants with oilconcentrated in seeds (sunflower, soybean, rapeseed etc.), plants producing oleaginous
fruits (olive, coconut and palm), plants producing oleaginous tubers (peanuts) and plants
producing oleaginous germ (corn). The main oleaginous crops, used for oil obtaining in
Romania, are: soybean, sunflower, line, rapeseed, mustard and castor, [2].
Oleaginous products industry manufactures edible oils and oils non edible. Edibleoils (which is about 2/3 of the total volume of the oil products) are used directly in food orused in the industry of margarine, mayonnaise, cooking fats, bakery products,
confectionery, canned food, confectionery and others, and the non edible oils
(representing one third of the total volume of oil produced) are used in production ofdetergents, paint, varnish, fatty acids, pharmaceuticals and cosmetics, [5].
Now, the main interest is the developing of energy industry by using biofuelsobtained from different oleaginous materials. Even if the oilseeds industry is high411

Analele Universităţii din Craiova, seria Agricultură – Montanologie – Cadastru (Annals of the University of Craiova - Agriculture,
Montanology, Cadastre Series) Vol. XLVI 2016

developed, there is still a major concern to improve the existing methods for the extraction,using new processing conditions and new equipments, even developing new methods withhigh extraction efficiency, [12]. In Romania, to extract vegetable oils from oleiferous seeds,
in most cases the combined process is used: pressing the seed material, ensuring oil
separation of up 80…85% , is followed by the solvent based extraction, a method by which
the oil is separated from the remainder (up to 99…99.5%), [1].
The oil extraction methods from oleaginous materials are designed to obtain highquality oil with minimal undesirable components, achieve high extraction yields andproduce high value meal, [10]. In this paper are presented the methods available for the
extraction of vegetable oil from oleaginous materials, such as those are presented in theliterature.
MATERIAL AND METHOD
Numerous references and clues are found that indicate the use of these oils during
stone age and bronze age. Documented oil extraction dates back to 1650 B.C. when
ripened olives were pressed by hand in Egypt using wooden pestles and stone mortars.
The extracted olive oil was filtered through goat hair filters and used as a lubricant.
Sesame, linseed, and castor oils were recovered in Egypt by hand pressing as far back as
259 B.C. By 184 B.C., the Romans developed more sophisticated technology such asedgerunner mills and screw and wedge presses. These technologies combined leverageand the use of animal power to aid in the milling and extraction of the oil. From Romantimes until the eighteenth century, similar technology was used for oil extraction, [8].
From the eighteenth century, various mechanized and innovative methods wereadopted for oil extraction from oilseeds. The purpose of those methods was to optimize theprocess by collecting the maximum quantity of the existing oil in oilseeds with the minimum
costs. The wind and water power was used to replace the animal power in the constructionof equipments used for the oil extraction. Currently, there are four basic methods for
obtaining vegetable oil from oleaginous material: chemical extraction, supercritical fluid
extraction, steam distillation and mechanical extraction (Fig.1).
In recent years, claim for natural and organic products has been growing, and newclean technologies for producing natural ingredients have been developed. In fact, present
attention is paid to the real quality of products and their potency, reliability andnaturalness. Owing to the increasing demand in bioactive compounds from plant origin,
new extraction methods was used to obtain products with high quality and safety features.
The conventional extraction methods are time consuming, laborious, have low selectivity
and/or low extraction yields, and possible solvent contamination of final products, [18].
OIL
EXTRACTIONMETHODSHIGHPRESSURE
CO2

CHEMICALSOLVENTDISTILLATIONMECHANICALHYDRAULICPRESSENZYMES

Fig. 1. Basic methods for oil extraction, [15]412

SCREW PRESSAnalele Universităţii din Craiova, seria Agricultură – Montanologie – Cadastru (Annals of the University of Craiova - Agriculture,
Montanology, Cadastre Series) Vol. XLVI 2016

RESULTS AND DISCUSSIONSOne of the most used and most ancient methods for oil extraction is represented by
the mechanical pressing. Mechanical oil extraction (also known as pressing) is based onmechanical compression of oleaginous materials. Through pressing, oil is separated fromthe oleaginous material (solid-liquid mixture) under the action of compressive external
forces that arise in special machines called presses, [3].
In practice, this operation can take two shapes: a hydraulic, uni-axial press or ascrew press (also called extruder or expeller). The advantages of a screw press (Fig. 2)
compared to a hydraulic press (Fig. 3) are its slightly higher yield and its continuous modeof operation.

Fig. 2. Schematic representation of a screw press, [16]Hydraulic oil press, so named because it works on the principle of the hydraulicram, are originary from England and was first patented in 1795 by Joseph Bramah,[5].
Hydraulic expression of oil involves application of pressure through a ram to digested
oleaginous material mash in a cylindrical cage. The cylindrical cage is usually perforated
laterally. This results in axial compaction and radial oil flow. In a typical hydraulic pressingof vegetable oil seeds three distinct stages can be identified (Fig. 3), [11]. The first
cottonseed oil mill constructed in the United States (1920) utilized a hydraulic press.

a.

b.

c.

Fig. 3. Stages of hydraulic expressions, [11]a – initial stage; b – dynamic stage; c – consolidation stage (final stage).

413

Analele Universităţii din Craiova, seria Agricultură – Montanologie – Cadastru (Annals of the University of Craiova - Agriculture,
Montanology, Cadastre Series) Vol. XLVI 2016

The first screw oil press was developed in 1900 by V.D. Anderson in the UnitedStates. This press permitted continuous operation of hydraulic presses which resulted ingreater capacities with smaller equipments and less labor, [5]. The mechanical screwpress (Fig. 2) consists of a vertical feeder and a horizontal screw with increasing body
diameter to exert pressure on the oilseeds as it advances along the length of the press.
The barrel surrounding the screw has slots along its length, allowing the increasing internalpressure to first expel air and then drain the oil through the barrel. Oil is collected in atrough under the screw and the de-oiled cake is discharged at the end of the screw. The
main advantage of the screw press is that large quantities of oilseeds can be processedwith minimal labor, and it allows continuous oil extraction, [10].
This method ensures extraction of a non-contaminated, protein-rich low fat cake at
relatively low-cost. The disadvantage of this method is that the mechanical presses do nothave high extraction efficiencies, about 8-14% of the available oil remain in the press cake.
Generally it is only used for smaller capacity plants, speciality products or as a prepress
operation in a large scale solvent extraction plant, [19].
Distillation is the extracting oil process, converts volatile liquid (essential oils) into
vapor state and then condenses the vapor into a liquid state. The extracting method is cost
to produce essential oils. In steam distillation method, the botanical material is placed ina still and steam is forced over the material. The hot steam is used to release the aromatic
molecules from the plant material. The steam forces to open the pockets and then themolecules of these volatile oils, escape from the plant material and evaporate into thesteam. The steam contains the essential oil, is passed through a cooling system tocondense the steam, which forms a liquid form of essential oil and then water is thenseparated. The steam is produced at greater pressure than the atmospheric pressure andtherefore boils at above 100°C which is used to the remove the essential oil from the plantmaterial.
The major advantage of steam distillation is that the temperature never goes above
100°C so temperature sensitive compounds can be distilled. The disadvantage is that not
many compounds can be steam distilled - usually aromatic ones, [14].

Fig. 4. Steam distillation process, [14]414Analele Universităţii din Craiova, seria Agricultură – Montanologie – Cadastru (Annals of the University of Craiova - Agriculture,
Montanology, Cadastre Series) Vol. XLVI 2016

The chemical methods are another technology used for oil extraction fromoilseeds. In the case of chemical methods, enzymes or solvents are used for the oil
extraction, [15]. The overwhelming majority of all vegetable oil is extracted using solvent
extraction. The advantage of solvent extraction is the high yield that can be obtained
economically with this method (>99 wt.%), but this is at the expense of a reduced oil
quality and a high initial capital cost to construct a facility. This quality reduction is causedby the extensive solvent recovery processes that are necessary and the fact that thesolvent co-extracts undesired components from the seeds. Especially for high value addedoils this quality reduction is unacceptable, limiting the production process to mechanicalexpression, [13].
In 1855, Deiss of Marseilles, France, was first to employ solvent extraction. He usedcarbon disulfide to dissolve olive oil retained in spent olive cakes. This technology usedbatch solvent extraction, where the material was held in a common kettle for both theextraction process as well as the subsequent meal desolventizing process. Deiss obtained
a patent for batch solvent extraction of olive oil in 1856, [8].
In solvent extraction, the seeds are first flaked (this operation is necessary in order toincrease the contact area of the seed with the solvent, resulting in a increasing of the oilyield) and cooked (cooking denatures cell tissues so that solvent can penetrate the flakes
more readily). After theses operations, the cooked seed flakes are mixed with the solvent
in order to extract the oil. It results a mixture of oil and solvent, called miscella, which isheated in evaporators at 80°C. Steam is injected on the shell side to vaporize and reducehexane to about 5% of the oil, then the oil is directly steam-stripped in a vacuum tower attemperatures rising to a final 110°C. For oil extraction using solvents, the following lightparaffinic petroleum fractions are used: pentane, hexane, heptanes and octanes.

Fig. 5. Flow diagram of solvent extraction method

Another chemical method used for oil extraction from oilseeds is represented byextraction using enzymes. This method is implemented by big vegetable oil companies
because the process produces many high value products. The first step necessary is the415Analele Universităţii din Craiova, seria Agricultură – Montanologie – Cadastru (Annals of the University of Craiova - Agriculture,
Montanology, Cadastre Series) Vol. XLVI 2016

cooking of the seeds and after that, the cooked sedds are put into water. The following
step is the enzymes adding which digest the solid material. At the end, the separation of
the residual enzymes and oil are made using a liquid-liquid centrifuge, [15].
Supercritical fluid extraction using carbon dioxide (SC-CO2) is a particularly
suitable isolation method for isolation of the valuable components from plant materials. A
natural plant extract, free from chemical alterations brought about by heat and water, andwithout solvent residues and other artifacts can be obtained by this method. Carbon
dioxide is non-toxic, non-explosive, readily available and easily removed from theextracted products, [17]. Supercritical fluids have gas-like diffusivities but liquid-likedensities. These properties vary as a function of pressure and temperature. Supercriticalcarbon dioxide (SC-CO2) has been the most frequently used supercritical fluid for oil
extraction, since it is nontoxic, nonflammable, inexpensive, and easily separated from theextract, [9]. In the supercritical carbon dioxide technique, the seeds are mixed with highpressure carbon dioxide in liquid form (at 31°C temperature and 7,3 MPa pressure). Then,oil dissolves in the carbon dioxide. When pressure is released from the system, the carbon
dioxide returns to the gas phase and oil precipitates out from CO 2-oil mixture.
The use of supercritical carbon dioxide is an green method to obtain cosmetic
product, functional and nutraceutical food, pure and free solvents for natural products andenvironmentally friendly.

Fig. 6. Supercritical CO2 pilot scale equipment

CONCLUSIONSThe present paper is a review of the most important methods used for obtaining
vegetable oil from oleaginous materials. Studying the paper available in the specialty
literature, it was established that currently, worldwide there are four basic methods for
obtaining vegetable oil: chemical extraction, supercritical fluid extraction, steam distillationand mechanical extraction. Taking into consideration the advantages and disadvantages
presented by each method, it can be noticed that the most used method for small scale
production is mechanical pressing using continuous screw presses, due to the simplicity ofthe process and equipments, the low investment cost and the high quality of the products.
But it is very important to take into account the main disadvantage presented bymechanical pressing which is represented by the fact that the cake have a higher residual
oil content, comparing with the solvent extraction method.

416

Analele Universităţii din Craiova, seria Agricultură – Montanologie – Cadastru (Annals of the University of Craiova - Agriculture,
Montanology, Cadastre Series) Vol. XLVI 2016

BIBLIOGRAPHY
1. Arișanu A.O., Hodîrnău E., 2011 - Particularities of oil extraction by pressing hulled
and hydrothermally processed sunflower seeds, Journal of EcoAgriTourism, vol. 7, no. 2,
p. 32-37;
2. Avram M., Stoica A., Dobre T., Stroescu M., 2014 - Extraction of vegetable oils fromground seeds by percolation techniques, U.P.B. Sci. Bull., Series B, Vol. 76, Iss. 2, ISSN
1454 – 2331;
3. Bamgboye A., Adejumo A., 2007 - Development of a sunflower oil expeller,
Agricultural Engineering International: the CIGR Ejournal. Manuscript EE 06 015, vol IX;
4. Banu C., 1999 - Manualul inginerului din industria alimentară, vol. I și II, Editura
Tehnică, București;5. Bargale P.C., 1997 - Mechanical oil expression from selected oilseeds under uniaxial
compression, Ph.D. Thesis, University of Saskatchewan, Canada;
6. Ghimbășan R., 2000 - Tehnologii în industria alimentară, Vol. 1, Brașov, Editura
Universității Transilvania din Brașov;7. Jolivet P., Deruyffelaere C., Boulard C., Quinsac A., Savoire R., Nesi N., Chardot
T., 2013 - Deciphering the structural organization of the oil bodies in the Brassica napus
seed as a mean to improve the oil extraction yield, Industrial Crops and Products, vol. 44,
pp. 549-557;
8. Kirschenbauer H. G.,1944 - Fats and Oils, Reinhold Publishing, New York, pp. 122–
123;
9. Naik, S.N., Lentz, H., Maheshwari, R.C., 1989 - Extraction of perfume and flavours
from plant materials with liquid carbon dioxide under liquid vapour equilibrium condition.
Fluid Phase Equilibria 49, pp. 115–126;
10. Nurhan D., - Oil and Oilseed Processing II, Robert M. Kerr Food & Agricultural
Products Center, FAPC-159;
11.
Owolarafe
O.K.,
Osunlekehttp://www.sciencedirect.com/science/article/pii/S1537511008002468 - aff2 A.S.,
Odejobi O.A., Ajadi S.O., Faborode M.O., 2008 - Mathematical modeling and simulationof the hydraulic expression of oil from oil palm fruit, Biosystems Engineering 101, pp. 331340;
12. Perez E. E., Carelli A. A., Crapiste G. H., 2011 - Temperature-dependent diffusion
coefficient of oil from different sunflower seeds during extraction with hexane, Journal of
Food Engineering, vol. 105, no. 1, pp. 180-185;
13. Pradhan R.C., Meda V., Rout P.K., Naik S., Dalai A.K., 2010 - Supercritical CO2
extraction of fatty oil from flaxseed and comparison with screw press expression andsolvent extraction processes, Journal of Food Engineering vol. 98, pp. 393–397;
14. Ranjitha J., Vijiyalakshmi S., 2014 - Facile methods for the extraction of essential oilfrom the plant species - a review, IJPSR, Vol. 5(4), pp. 1107-1115, E-ISSN: 0975-8232;
P-ISSN: 2320-5148;
15. Sari P., 2006 - Preliminary design and construction of a prototype canola seed oil
extraction machine, Ph.D. Thesis, Middle East Technical University, Ankara, Turkey;
16. Savoire R., Lanoiselle J.L., Vorobiev E., 2013 - Mechanical continuous oil
expression from oilseeds: A review, Food Bioprocess Technology, vol. 6, pp. 1-16;
17. Sovilj M.N., 2010 - Critical review of supercritical carbon dioxide extraction of selectedoil seeds, APTEFF, 41, 1-203, pg. 105-120;
18. Straccia M.C., Siano F., Coppola R., La Cara F., Volpe M.G., 2012 - Extraction andCharacterization of Vegetable Oils from Cherry Seed by Different Extraction Processes,
CHEMICAL ENGINEERING TRANSACTIONS, VOL. 27, pp. 391-396, ISBN 978-8895608-18-1; ISSN 1974-9791;
19. Willems P., 2007 - Gas assisted mechanical expression of oilseeds, PhD Thesis,
Twente, University of Twente, Netherlands.
417

View publication stats