- Open Access
- Total Downloads : 1911
- Authors : Miss Diwan Tapoja, S. A. Desai
- Paper ID : IJERTV3IS110378
- Volume & Issue : Volume 03, Issue 11 (November 2014)
- Published (First Online): 13-11-2014
- ISSN (Online) : 2278-0181
- Publisher Name : IJERT
- License: This work is licensed under a Creative Commons Attribution 4.0 International License
Studies on Extraction of Ingredient Oil from Lemon Grass
Miss Diwan Tapoja Desai S. A.
PG Student, Associate Professor
Chemical Engineering Department Chemical Engineering Department TKIET, Warananagar, India TKIET, Warananagar, India
Abstract- The work done will focus on the study and optimization of extraction of ingredient oil from lemongrass. This study investigates the influence of operating parameters like time, size, type of grass on the extraction of oil. Lemon grass is an important herbal and aromatic plant and its oil is one of the major essential oils used in the perfumery and cosmetic industry. It is widely used in the scented soaps, sprays, deodorants, polishes and medicines. The extracted oil is rich in Citral A & P. Citral is the starting material for the manufacture of vitamin A. In the present experiment citral is isolated by Hydro-distillation of lemon grass, which is used to make lemongrass tea. The distillate contains 90 % citral and
10 % neral, the isomer about the 2,3-bond. Various experiments are carried out on a lab scale to optimize the parameters and get the maximum yield. The extracted oil is analyzed by using gas chromatography. The result indicates that the wet grass gives the maximum extract. The Yield can be raised from 8% to 12% by using Hydro-distillation and pre heated water as solvent.
Keywords- lemongrass, ingredient oil, optimization, extraction, time, size, gas chromatography.
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INTRODUCTION
Lemon grass (Cymbogen citratus) is found in many parts of world. It is mainly grown as an ornamental plant however lemongrass has many other uses such as a food crop eg. It is used in herbal tea because of its sharp lemon flavor. It is used as the perfume in soaps and a medicine to treat various health ailments, decreasing acne, athletes foot, flatulence, muscles aches and scabies[1]. Further, bioactivity studies have shown that the various components of this ingredient oil contains antimicrobial, antifungal, antibacterial and mosquito repellent properties make it a valuable product to be extracted [2]. The citral isolated from oil is used in the manufacturing of vitamin A, Because of those attributes lemon grass is of great use and value in the agriculture sector, especially for the protection of stored agricultural product. Crude essential oils are obtained by steam distillation of variety of natural products like plants, grasses, wood stumps saw dust, flowers, kernel and social hygiene of mankind in terms of their use in cosmetics, toiletries, medicinal formulations, aroma therapy, surface coatings etc.[3].
Most of the essential or ingredient oil occurring in nature consists of mixture of hydrocarbons like terpens [4] sequiterpenes, oxygenated compounds like alcohol esters,
ether, aldehydes, ketones, lactones, phenols and waxes. Out of these oxygenated compounds like alcohols are the principal odour carriers [2]. They are more stable against oxidation agents. The unsaturated hydrocarbon like terpenes are less stable and are responsible for degrading oils. To make essential or ingredient oils more stable, so that they retain most of their odor and flavor, these terpenes are removed so that only oxygenated compounds are retained.
The lemon grass oil is obtained by steam distillation or hydrodistilation of lemon grass. It is the most common and cheapest oil available in market [5]. The steam distillation or hydrodistilation process to obtain ingredient oil from leaves and the aromatic industry use this method because it is cheap when compared with technologically advanced methods as supercritical fluid extraction. [6].
The main objective of this work is to optimize the lemongrass oil extraction process variables (parameters) to define the best operational conditional with regard of yield and composition of lemon grass oil considering as function of time and raw state material.
-
MATERIALS AND METHODS
-
Materials:
Wet and dry lemon grass, water, distillation column, condenser, heating element, measuring cylinder, conical flasks, burette, glass bottles with stopper, gas chromatography.
-
Experimental methods:
Lemon grass (chopped r un-chopped) and water is filled in the distillation still and the lid is fitted tightly, so that oil and vapor do not leak. As steam forms it carries the oil from the plant material i.e. lemon grass and both oil and steam pass to condenser through vapor line. Where the vapors get condensed and oil and water are separated in separators. Oil being lighter is separated from the top and water being heavier is separated from the bottom of the separator.
Essential oils are highly sensitive as such that distillation is carried out at low temperatures. Further direct heat contact provided by steam, initially gives wet ability to grass at high temperatures, enhancing diffusion and osmosis of the oil. Rate of oil vaporization of the plant material in
Sr.N
o.
Weigh t of
plant taken (gram s)
Condition of grass
Packin g
temper ature
Oil
produced in ml
Dry (Chopp ed in cm approx.
)
Wet (Chopp ed in cm approx.
)
dry
W
et
1
300
2
2
loose
100ºC
25
31
2
250
1.5
1.5
loose
100ºC
23
42
3
300
1
1
loose
100ºC
35
38
4
290
0.6
0.6
loose
120ºC
30
33
5
250
0.3-0.4
0.3-0.4.
loose
120ºC
54
57
6
300
Below
0.1
Below
0.1
loose
130ºC
49
52
7
300
Below
0.1
Below
0.1
loose
130ºC
50
53
distillation is not influenced by relative volatility of oil components but by their solubility in water. Extraction of oil from lemon grass is a rate process. Also oil removed per unit is directly proportional to oil remained in grass. The balance equation for batch distillation can be given by first order kinetics;
-dx/dt=kx (1)
dx/x=kdt (2)
lnX/x=kt (3)
ln(1/1-y(t))=kt (4)
Where x is average concentration of oil in grass at time t
X is initial concentration of oil in grass before distillation starts;
t is time of distillation, y(t) is the fraction of oil extracted. If above model holds good then the plot of 1/ 1- y versus t shall produce a straight line passing through origin. The analysis of oil can be done qualitatively and quantitatively with the help of gas chromatography mass spectroscope apparatus.
-
-
EXPERIMENTAL WORK
The grass and water are mixed in desired quantities and are filled in the distillation apparatus. The temperature is set and after the boiling oint of water the vapors start generating with oil extract. The oil distillate is collected in measuring flask and extract of oil is measured.
The kinetic data i.e oil yield at half hour interval of time in all the experiments carried out in the lab will be presented in table. Using this data we will plot he graph as oil yields verses time for these experiments. Fractional yield of oil y is calculated as the ratio of oil extracted till time t to the cumulative amount of oil extracted. To verify the model we again plot the graph of 1/1-u versus t to show the straight line behavior. This will also show that oil extracted is directly proportional to the oil remaining in grass.
IV RESULT AND DISCUSSION
The following are the results obtained from the experiments conducted to extract the ingredient oil from lemon grass.
According to the above table it is clearly seen that the oil extracted from wet grass is more than that of dry grass. So the analysis of extraction process for oil from wet grass is given as follows;
Here y and ln(1/1-y) is calculate using the formula which is mentioned in experimental work. The graphs are plotted as time vs yield of oil and time vs ln(1/1-y).
For experiment no 1.
Time in minutes |
Yield in ml |
y |
ln(1/1-y) |
30 |
7 |
0.22 |
0.25 |
60 |
15 |
0.48 |
0.65 |
90 |
19 |
0.61 |
0.94 |
120 |
22.5 |
0.72 |
1.27 |
150 |
25.5 |
0.82 |
1.71 |
180 |
28.5 |
0.91 |
2.40 |
300 |
31.0 |
_ |
_ |
For experiment no 2.
Time in minutes |
Yield in ml |
y |
Ln (1/1-y) |
30 |
7 |
0.17 |
0.186 |
60 |
15 |
0.30 |
0.356 |
90 |
24 |
0.57 |
0.640 |
120 |
29 |
0.69 |
0.970 |
150 |
33 |
0.78 |
1.50 |
180 |
37.5 |
0.09 |
2.70 |
300 |
42 |
_ |
_ |
For experiment no 3
Time in minutes |
Yield in ml |
y |
Ln (1/1-y) |
30 |
7 |
0.18 |
0.19 |
60 |
18 |
0.46 |
0.615 |
90 |
27 |
0.70 |
0.203 |
120 |
31.5 |
0.82 |
1.713 |
150 |
35.0 |
0.91 |
1.40 |
180 |
– |
– |
– |
300 |
38.5 |
_ |
_ |
For experiment no 4
Time in minutes |
Yield in ml |
y |
Ln (1/1-y) |
30 |
10 |
0.3 |
0.356 |
60 |
20 |
0.6 |
0.91 |
90 |
23.5 |
0.71 |
0.23 |
120 |
27 |
0.82 |
1.70 |
150 |
30 |
0.91 |
– |
180 |
– |
– |
– |
300 |
330 |
_ |
_ |
For experiment no 5
Time in minutes |
Yield in ml |
y |
Ln (1/1-y) |
30 |
16.4 |
0.25 |
0.33 |
60 |
29.9 |
0.52 |
0.73 |
90 |
47.3 |
0.82 |
1.70 |
120 |
51.5 |
0.90 |
2.30 |
150 |
54 |
0.94 |
2.80 |
180 |
55.4 |
0.96 |
3.20 |
300 |
57.2 |
_ |
_ |
For experiment no 6
Time in minutes |
Yield in ml |
y |
ln (1/1-y) |
30 |
17 |
0.32 |
0.1385 |
60 |
30 |
0.57 |
0.844 |
90 |
39 |
0.74 |
1.347 |
120 |
45 |
0.86 |
1.96 |
150 |
49 |
0.94 |
2..813 |
180 |
51 |
0.97 |
3.5 |
300 |
52.25 |
_ |
_ |
Time in minutes |
Yield in ml |
y |
Ln (1/1-y) |
30 |
17 |
0.32 |
0.385 |
60 |
30 |
0.50 |
0.820 |
90 |
40 |
0.75 |
1.31 |
120 |
46 |
0.86 |
1.96 |
150 |
50 |
0.94 |
2.80 |
180 |
52 |
0.47 |
3.54 |
300 |
53 |
_ |
_ |
For experiment no 7
time vs yield
50
40
30
20
yield
10
0
0
200
400
time vs ln(1/1-y)
The graphs obtained are as follows;
For experiment no 1
time vs yield
40
1
0.8
0.6
0.4
0.2
0
ln(1/1-
y)
0 200 400
30
20
10
0
0 200 400
time vs ln(1/1-y)
2
1.5
1
0.5
0
0 200 400
For experiment no 2.
yield
ln(1/1-y)
Similar type of graphs are obtained for other experiments too. The graph of time vs ln(1/1-y) is a straight line which will not pass through the origin but will have an intercept. It shows that the extraction of oil does not start at the starting of the distillation but it takes time. The straight line in second graph indicates that the extraction process follows first order equation.
These samples are analyzed with the help of gas chromatography the results are as follows;
The peak that is generated at the around 15 minutes is lemongrass oil according to the reference retention time.
V. CONCLUSIONS
According to the data obtained from the experiments carried out following are the conclusions drawn;
-
The loose packing and the wet material in raw material in distillation still enhances the oil yield from plant material.
-
The kinetic studies of distillation process showed that oil is not instantly extracted and if it is the dry grass the yield is less.
-
The plot of time vs ln(1/1-y) is a straight line i.e. it follows first order kinetics.
-
Oil removed per unit time is directly proportional to the oil remaining in the grass.
-
The yield percent is raised from 8% to 12% by using water as solvent. As no chemicals are used ther is no need of purification for final product.
REFERENCES
-
W.R.L Masaba, J.F.M Kamanula, Elizabeth M.S, Henry G.K, Extraction and analysis of lemon grass (Cymbopgan Citratus) oil: An essential oil with potential to control the large grain borer in stored products in Malavi Malavi journal of agriculture science pp56-64, January 2003.
-
V K Koul, B M Candora, Suman Koul Steam distillation of lemon grass (Cymbopogan spp.),Indian journal of Chemical Technology, Vol-11, pp 135-139, January 2004
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Guenther E, The essential oils, Vol- 1 ( D. Van Nostrand Company Inc. New York), 1965.
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Scweltzer Philip A. Handbook of Separation techniques for Chemical Engineers 3rd Edn (Mc Graw Hill, New York) 1997, 1.
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Perry R H and Green Don, Perrys Chemical Engineers Handbook, 6th Edn ( MacGraw Hill, New York), 1984.
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R. Treybal, Mass Transfer operations, 3rd Edn, (MacGraw Hill, New York),1981, pp 426- 428.
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Svetomir . Milojevi,1 Dragana B. Radosavljevi,1 Vladimir P. Pavievi,2 Sran Pejanovi,2 Vlada B. Veljkovi3, Modeling the kinetics of essential oil hydrodistillation from plant materials, pp 1- 49, 2013.
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Adams, R.P., 1989. Identification of Essential Oil Componentsby Ion Trap Mass Spectroscopy. Academic Press, NewYork.
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Clevenger, J.F., 1928. Apparatus for the determination of volatile oil. J. Am. Pharm. Assoc.
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