Communications in Science and T echnology 1 .
COMMUNICATIONS IN
SCIENCE AND TECHNOLOGY
Homepage: cst.
Kinetics study of oil extraction from Citrus auranticum L.
by solvent-free microwave extraction Heri Septya Kusuma*.
Prilia Dwi Amelia.
Cininta Admiralia.
Mahfud Mahfud* Department of Chemical Engineering.
Institut Teknologi Sepuluh Nopember.
Jalan Raya ITS.
Keputih.
Sukolilo.
Surabaya 60111.
Indonesia Article history:
Received: 21 April 2016 / Received in revised form: 6 M ay 2016 / Accepted: 19 M ay 2016 Abstract Citrus and its oil are of high economic and medicinal value because of their multiple uses, such as in the food industry, cosmetics and folk The aim of this study is to investigate the potential of solvent-free microwave extraction for the extraction of essential oils from Citrus auranticum L.
Specifically, this study verifies the kinetics based on second-order model and mechanism of solvent-free microwave extraction of Citrus auranticum L.
Solvent-free microwave extraction is used to extract essential oils from Citrus auranticum L.
The initial extraction rate, the extraction capacity and the second-order extraction rate constant were calculated using the model.
Using a three-step experimental design of the kinetics of oil extraction from Citrus auranticum L.
peels by solvent-free microwave extraction, this study showed that the extraction process was based on the second-order extraction model.
The initial extraction rate .
, the extraction capacity (CS), the second-order extraction rate constant .
, and coefficient of determination (R.
7483 g L-1 min-1, 0.
7291 g L-1, 1.
4075 L g-1 min-1 and 0.
9992, respectively.
Keywords: Citrus auranticum L.
citrus oil.
kinetic study.
solvent-free microwave extraction Introduction Citrus fruits and their by-products are of high economic and medicinal value because of their multiple uses, such as in the food industry, cosmetics and folk medicine .
In addition to large scale consumption as fresh fruits, the Citrus fruits are mainly processed to produce juice.
The waste of Citrus processing industry, left after juice extraction, such as peels, seeds and pulps, corresponding to about 50% of the raw processed fruit, can be used as a potential source of valuable by-products .
Specifically, the Citrus peels, commonly treated as agro-industrial waste, are a potential source of valuable secondary plant metabolites and essential oils .
Citrus peel essential oils are reported to be one of the rich sources of bioactive compounds namely coumarins, flavonoids, carotenes, terpenes and linalool etc.
Recently.
Citrus peel essential oils have also been searched for their natural antioxidant and antimicrobial properties .
It is widely accepted that biological activities of plant materials are strongly linked with their specific chemical composition, mainly the secondary metabolites such as plant phenolics and flavonoids .
These substances can be extracted by different methods:
hydrodistillation, extraction with organic solvent and supercritical fluid extraction (SFE) .
Among these methods, hydrodistillation has been the most common approach to extract the essential oils from the medicine herbs and plants * Corresponding author.
Tel.
: 6285730780240
Email: heriseptyakusuma@gmail.
mahfud@chem-eng.
Alternative methods, employing microwaves, have been developed in order to shorten extraction time, improve the extraction yield, and reduce the operational costs.
Microwaveassisted procedures for isolating essential oils have become attractive for use in laboratories and industry.
The advantages of using microwave energy for oil extraction are more effective heating, fast energy transfer, faster response to process heating control, faster start-up, increased production, and elimination of some process steps.
Novel microwaveassisted extraction (MAE) .
methods such as microwaveassisted hydrodistillation (MAHD) .
,11,12,.
and solventfree microwave extraction (SFME) .
have proven to be fast and efficient methods for extracting essential oils.
However, to the best of the authorsAo knowledge no work has been published on the extraction of essential oil from Citrus auranticum L.
peels using microwave ovens for Therefore, the objective of this study was to investigate the potential of SFME for the extraction of essential oils from Citrus auranticum L.
In this study, the authors also attempted to know and verify the kinetics based on second-order model and mechanism of SFME of Citrus auranticum L.
Materials and Methods Raw materials In this study.
Citrus auranticum L.
was collected from Keputran market.
Surabaya.
Indonesia.
Orange fruits were A 2016 KIPMI Kusuma et al / Communications in Science and Technology 1 .
15-18 peeled using a hand procedure which separates the external part of the orange, giving a yield of A20% w/w of orange peel with respect to the whole friut.
Fresh plant material was employed in solvent-free microwave extraction.
All other chemicals and solvents used were of analytical grade.
oil contained in the solid to solution can be described by Equation .
Solvent-free microwave extraction where k is the second-order extraction rate constant (L g -1 min -1 ).
CS the extraction capacity .
oncentration of essential oil at saturation in g L-1 ) and Ct is the concentration of citrus oil at any time t .
By considering the initial and boundary conditions, t = 0 to t and Ct = 0 to Ct , the integrated rate law for second-order extraction was obtained:
In employing SFME, we used a domestic microwave oven (EMM-2007X.
Electrolux, 20 l, maximum delivered power of 800 W) with wave frequency of 2450 MHz.
The dimensions of the PTFE-coated cavity of the microwave oven were 46.
cm x 28.
0 cm x 37.
3 cm.
The microwave oven was modified by drilling a hole at the top.
A round bottom flask with a capacity of 1000 ml was placed inside the oven and was connected to the three-way adapter and liebig condenser through the hole.
Then, the hole was closed with PTFE to prevent any loss of the heat inside.
In this method, fresh peels were placed in the microwave Fourty grams of Citrus auranticum L.
peels was placed inside the reaction flask and heated by microwave irradiation with 400 W .
% powe.
for 60 min.
During the process, the vapor passed through the condenser outside the microwave cavity where it was condensed (Fig.
The essential oils and water was simply separated by decantation.
Every 10 min, the collected essential oils was decanted from the condensate.
The essential oils were collected in amber vials, dried under anhydrous sodium sulfate and stored at 4o C.
The extraction yield of citrus oil was calculated according to the equation .
By transforming Eq.
, a linear form shown in Eq.
can be obtained and the extraction rate can be written as Eq.
The initial extraction rate, h, as Ct/t when t approaches 0, can be defined as:
and, the concentration of essential oil at any time can be expressed after rearrangement as:
where y is the citrus oil yield (%, w/.
V is the weight or mass of extracted citrus oil .
and W is the weight or mass of fresh Citrus auranticum L.
The initial extraction rate, h, the extraction capacity.
CS, and the second-order extraction rate constant, k, can be determined experimentally from the slope and intercept by plotting t/Ct versus t.
Results and Discussion Fig.
Schematic representation of the solvent-free microwave extraction apparatus used in this study Kinetic model Second-order mechanism model means that the extraction occurs in two simultaneous processes.
The amount of extracted oil increases rapidly with time at the beginning and then decreases slowly with the time until the end of extraction process .
,16,17,.
The rate of dissolution for the essential As shown in Fig.
2, the rate of extraction was increased as the time of extraction increased until it reached plateau or constant after 50 min of extraction.
65% extractable oil was obtained in the 10 min of extraction until it became plateau .
72%).
The experimental result was analyzed using secondorder model by plotting t/Ct versus time as shown in Fig.
According to Fig.
2, the rate of extraction was fast at the beginning and slow until the end of the extraction process.
The extraction process takes place in three different steps: an equilibrium phase where the phenomena of solubilization and partition intervene, in which the substrate is removed from the outer surface of the particle at an approximately constant Then, this stage is followed by an intermediary transition phase to diffusion.
The resistance to mass transfer begins to appear in the solidAeliquid interface.
in this period the mass transfer by convection and diffusion prevails.
In the last phase, the solute must overcome the interactions that bin d it to the matrix and diffuse into the extracting solvent.
The extraction rate in this period is low, characterized by the H.
Kusuma et al / Communications in Science and Technology 1 .
15-18 removal of the extract through the diffusion mechanism.
This point is an irreversible step of the extraction process.
it is often regarded as the limiting step of the process .
Diffusion rate decreased as the time of extraction increased due to the high solute concentration in liquid at the third stage.
Even though the extraction time increased after the maximum citrus oil was extracted, it did not show any changes or significant in amount of oil extracted.
The trend of citrus oil recovery under extraction time of 10 min, 50 min and 60 min, respectively was 89.
89%, 9.
06% and 1.
citrus oil yield extracted from fresh peels by HD for 3 hours is 24 A 0.
Fig.
4 shows the mechanism of SFME compared to HD In HD, the temperature increased often slowly, depended on the thermal conductivity and on convection currents, where the heat transfer was occurring from the outside to the inside while mass transfer was occurring from the inside to the outside of the Citrus auranticum L.
Whereas, in SFME the cell was subjected to severe thermal stress, the temperature increased much faster than the conventional heating, depending on the effects of microwave irradiations and the internal dielectric heating of the Citrus auranticum L.
peels with the action of the Auin situAy water, where both the heat and mass transfers were in the same direction from the inside to the outside of the gland.
As a result of internal superheating which leaded to the severe vaporization of the AoAoin situAy water and localized a high pressure gradient inside the gland, a dramatic expansion and a rapid rupture of the cell walls were occurring.
Finally, the essential oils were migrated quickly from the inside of the Citrus auranticum L.
peels to the surrounding.
Fig.
T he concentration of citrus oil in the solution at any time.
Ct .
L-.
versus time .
Fig.
Heat and mass transfer mechanisms in conventional hydrodistillation and solvent-free microwave extraction of citrus oil Conclusion Fig.
Second-order extraction kinetics of citrus oil The initial extraction rate, h, the extraction capacity.
CS, the second-order extraction rate constant, k, and coefficient of determination.
R2 , were calculated experimentally by referring to the linier curve in Fig.
From graph t/Ct versus time, slope is equal to 1/CS, and intercept is equal to 1/h.
The data showed in Table 1.
The extraction yield of citrus oil obtained by SFME method for 60 min is 0.
Kinetics of oil extraction from Citrus auranticum L.
peels by SFME method proved that the extraction process was based on the second-order extraction model as the experiment was conducted in three different The initial extraction rate .
, the extraction capacity (CS), the second-order extraction rate constant .
, and coefficient of determination (R2 ), respectively was 0.
7483 g L1 min -1 , 0.
7291 g L-1 , 1.
4075 L g -1 min -1 and 0.
T able 1.
Linierization of second-order kinetic model of solvent-free microwave extraction of Citrus auranticum L.
References