Application of Response Surface Methodology (RSM) to
optimize culture media for the production of rhamnolipids
by Pseudomonas aeruginosa
Athira
Gopakumar1, Jacyntha Thomas1,
G.Narendrakumar1, Preethi. T.V2
1Department of
Biotechnology, Sathyabama University, Chennai – 600
119.
2Research
Scholar, Department of Microbiology, School of Life Sciences, Vels University, Pallavaram,
Chennai – 600 117.
*Corresponding Author E-mail:
ABSTRACT:
Rhamnolipids,
naturally existent biosurfactantsassembledbyrhamnose
sugar molecules and β-hydroxyalkanoicacids that
has wide range of promising profitable applications. In the study Pseudomonas aeruginosabacterial isolates was identified
and screened for rhamnolipid production. P. aeruginosa achieved
the production of rhamnolipid at room temperature in
static cultures of a mineral salts medium containing olive oil. The pure
culture was enhanced and optimized at pH- 7, temperature-37oC and
olive oil as effective carbon source. The cultural media was optimized using
response surface methodology - Box-Behnken with 30 ml
of olive oil, 5 g/l NaNO3, 4 g/l KH2PO4 and
7.5 g/l FeSO4 mixture contributes maximum production of rhamnolipid. The R2 value was 99.8 that
correlated with adjusted R2 value of 99.7 and predicted R2
value of 99.5 shows the model is significant.
KEYWORDS: Rhamnolipids, RSM-BB, olive oil, optimization
INTRODUCTION:
A
surfactant is a molecule that has both a
hydrophilic end, which attracts water and
a hydrophobic end, which repels water and attracts non-polar chemicals. A
bio-surfactant are produced naturally including rhamnolipid
that are produced by Pseudomonas aeruginosa
and a number of other bacteria. Surfactants are chemicals that reduce the
surface tension of water(1-6).
Bio-surfactants
have been applied in many fields, such as microbial enhanced oil recovery,
bioremediation, cosmetics, rhamnolipidrmaceuticals,
detergents, food and other industries.The rhamnose-containing glycolipid biosurfactants produced by Pseudomonas aeruginosa were first
described in 1949. Rhamnolipids are class of compound that contain one or more
3-hydroxy fatty acids of various chain length (C7 – C21)
esters lined to a mono or di rhamnose
and produced as a complex molecule(7-11).
The regular method of media optimization changing one
factor at one time consume a lot of chemicals and time hence optimization can
be performed using response surface methodology (RSM) that involves factorial
design and regression analysis with multifactorial experiments(12,13).
The
aim of this work is to optimize the media components for higher production of rhamnolipid.
MATERIALS AND
METHODS:
P.
aeruginosa was isolated from oil contaminated soil using serial
dilution technique. Isolated organisms were confirmed by biochemical methods.
Preparation of
minimal salt medium:14
Minimal
Salt Medium (MSM) for 1000 ml for Rhamnolipid
production. MgSO4.7H2O -0.5g, FeSO4.7H2O
-0.01g, KH2PO4- 1.0g, K2HPO4-
0.5g, NaNO3- 2.0 g, CaCl2- 0.01 g, KCl - 0.01
g. maintained at pH 7.
Seed Culture:15
Pseudomonas aeruginosa was grown on plate count agar was
transferred to the seed culture medium. Seed culture grown in 250 ml flask
contain Mini mum Salt Medium at 30oC
at rotary shaker at 180 rpm for 14 hrs.
Preparation of
Inoculation medium (g/L) :16
Carbon
source (glucose, glycerol, liquid paraffin, Dextrose, lactose) were sterilized
separately.NaNO3 -2.125, (NH4)2SO2-1.65,
NH4NO3-1.0, MgSO4-7H2O-0.5, K2HPO4
-2.0, KH2PO4 -2.0, Yeast extract - 1.0, NaCl-1.0, CaCl 2-2H2O -0.01, MnSO4-5H2O
-0.01, FeSO4-2H2O - 0.01. From the seed culture, the inoculum was transferred to Inoculation medium.
Optimization of Rhamnolipid at different temperature:17
The
production of rhamnolipid was optimized by using
different temperature 27 °C, 37°C, 42°C.
Optimization of Rhamnolipid at different pH:18
Seed
culture grown in 250ml flask contain Minimal salt medium (MSM). The sample pH
is adjusted to 4 to 10 respectively by adding 1N HCl.
Optimization of Rhamnolipid (by different carbon source) :19
To
optimize the production of rhamnolipid different
carbon source like fish oil, sugarcane syrup, glycerol, olive oil, liquid
paraffin
Response Surface
Methodology:
Statistical
analysis Response Surface Methodology (RSM) was used to investigate the main
effects of dependable variables on the production of Rhamnolipid
by the organism. Olive oil (A), NaNO3 (B), KH2PO4(C),
FeSO4 (D), were selected as independent variables. Box-Behnken was used for the experimental data and data were
fitted to a second order polynomial model and regression coefficients obtained.
The software used for this analysis was Design expert – version - 7.0(20-22).
Regression
analysis for different models indicated that the fitted quadratic models
accounted for more than 95% of the variations in the experimental data, which
were significant. The ANOVA and F ratio test have been performed to justify the
goodness of fit of the developed mathematical models. The calculated values of
F ratios for lack-of-fit have been compared to standard values of F ratios
corresponding to their degrees of freedom to find the adequacy of the developed
mathematical models(23-25).
Extraction of Rhamnolipids
Each
flask received 100 ml of distilled water. The flasks were agitated for 1 h at 200
rpm at 30°C on an orbital shaker. The suspension was filtered through cheese
cloth; the excess liquid being squeezed out manually. This procedure was done
three times. The extract was centrifuged for 10 min at 12,500×g, and the
supernatant was extracted at least three times with chloroform–methanol (3:1,
v/v), with 15 ml of this solvent mixture being used for each extraction. The
organic rhamnolipidse was concentrated at reduced
pressure at 40°C, giving rise to a crude extract containing the rhamnolipids26.
Analytical
method:
Rhamnolipid concentration
was quantified by spectrophotometer method as rhamnose
content using a standard. Rhamnolipid27.
RESULT AND DISCUSSION:
Figure -1 (a) Effect of
carbon source
Figure -1(b) Effect of pH
Table
-1 The design summary used in RSM
|
Study Type |
Response Surface |
Runs |
29 |
Initial Design |
Box-Behnken |
Design Model |
Quadratic |
||
|
Factor |
Name |
Units |
Type |
Low Actual |
High Actual |
Low Coded |
High Coded |
Mean |
Std. Dev. |
|
A |
Olive oil |
v/v |
Numeric |
10 |
50 |
-1 |
1 |
30 |
12.86535 |
|
B |
NaNO3 |
g/l |
Numeric |
1 |
9 |
-1 |
1 |
5 |
2.57307 |
|
C |
KH2PO4 |
g/l |
Numeric |
2.5 |
5.5 |
-1 |
1 |
4 |
0.964901 |
|
D |
FeSO4 |
g/l |
Numeric |
5 |
10 |
-1 |
1 |
7.5 |
1.608169 |
Figure -1(c) Effect of
Temperature on the production of Rhamnolipid
Optimization of rhamnolipid
Production
The organism was found to
accumulate highest concentration of rhamnolipid at 35oC
in olive oil containing medium (Figure – 1a). To determine the ideal growth
condition for highest rhamnolipid yield, the most
important parameters such as carbon sources, temperature and pH were varied.
From the estimated rhamnolipid yield under these
varying conditions, it was determined that the highest yield by Pseudomonas aeruginosa
was at pH 7, temperature at 35°C and olive oil containing medium. A similar study on
optimization of rhamnolipid was done by Maier and
Chavez21 in which the Pseudomonas sp showed the maximum rhamnolipid accumulation at pH- 7, temperature 35°C
Response surface methodology:
The quadratic equation
Response = ɛo+
ɛ1 X1 + ɛ2 X2 + ɛ3 X3 + ɛ4 X4 +ɛ5 X12 + ɛ6 X22 + ɛ7 X32 + ɛ8 X42 +ɛ9 X1 X2+ ɛ10 X2 X3 + ɛ11 X1 X3+ ɛ12 X1 X4+ ɛ13 X2 X4+ ɛ1 X3 X4
Where Response is the
measured response, X1, X2, X3 and X4 are the coded independent input variables,
ɛo is the intercept term, ɛ1, ɛ2, ɛ3 and ɛ4 are the coefficients showing the linear
effects, ɛ5, ɛ6, ɛ7 and ɛ8, are the quadratic coefficients showing
the squared effects and ɛ9, ɛ10, ɛ11, ɛ12, ɛ13 and ɛ14 are the cross product coefficients
showing the interaction effects24.
Table -2 Design of Experiment
and its response
|
Std |
Factor
1 A:Olive
oil |
Factor 2 B:NaNO3 |
Factor 3 C:KH2PO4 |
Factor 4 D:FeSO4 |
Response
1 |
|
|
Actual |
Predicted |
|||||
|
v/v |
g/l |
g/dm3 |
||||
|
1 |
10 |
1 |
4 |
7.5 |
4.1 |
4.1 |
|
2 |
50 |
1 |
4 |
7.5 |
4 |
3.9 |
|
3 |
10 |
9 |
4 |
7.5 |
5.5 |
5.4 |
|
4 |
50 |
9 |
4 |
7.5 |
5.4 |
5.3 |
|
5 |
30 |
5 |
2.5 |
5 |
5.4 |
5.3 |
|
6 |
30 |
5 |
5.5 |
5 |
4.2 |
4.2 |
|
7 |
30 |
5 |
2.5 |
10 |
2.7 |
2.6 |
|
8 |
30 |
5 |
5.5 |
10 |
7.2 |
7.2 |
|
9 |
10 |
5 |
4 |
5 |
5.6 |
5.6 |
|
10 |
50 |
5 |
4 |
5 |
4.9 |
5.0 |
|
11 |
10 |
5 |
4 |
10 |
5.1 |
5.2 |
|
12 |
50 |
5 |
4 |
10 |
5.4 |
5.6 |
|
13 |
30 |
1 |
2.5 |
7.5 |
1.5 |
1.7 |
|
14 |
30 |
9 |
2.5 |
7.5 |
4.9 |
4.9 |
|
15 |
30 |
1 |
5.5 |
7.5 |
5.1 |
5.3 |
|
16 |
30 |
9 |
5.5 |
7.5 |
4.8 |
4.8 |
|
17 |
10 |
5 |
2.5 |
7.5 |
2.5 |
2.5 |
|
18 |
50 |
5 |
2.5 |
7.5 |
5.1 |
5.1 |
|
19 |
10 |
5 |
5.5 |
7.5 |
7.1 |
7.0 |
|
20 |
50 |
5 |
5.5 |
7.5 |
4.2 |
4.1 |
|
21 |
30 |
1 |
4 |
5 |
3.8 |
3.7 |
|
22 |
30 |
9 |
4 |
5 |
5.6 |
5.8 |
|
23 |
30 |
1 |
4 |
10 |
4.7 |
4.5 |
|
24 |
30 |
9 |
4 |
10 |
5.1 |
5.2 |
|
25 |
30 |
5 |
4 |
7.5 |
14.2 |
14.5 |
|
26 |
30 |
5 |
4 |
7.5 |
14.5 |
14.5 |
|
27 |
30 |
5 |
4 |
7.5 |
14.7 |
14.5 |
|
28 |
30 |
5 |
4 |
7.5 |
14.7 |
14.5 |
|
29 |
30 |
5 |
4 |
7.5 |
14.2 |
14.5 |
Table -3 ANOVA Table
|
Source |
Sum
of Squares |
df |
Mean Square |
F Value |
p-value Prob > F |
|
|
Model |
427.8906 |
14 |
30.56361 |
860.9469 |
< 0.0001 |
Significant |
|
A-Olive oil |
0.0675 |
1 |
0.0675 |
1.901408 |
0.1896 |
|
|
B-NaNO3 |
5.4675 |
1 |
5.4675 |
154.0141 |
< 0.0001 |
|
|
C-KH2PO4 |
9.1875 |
1 |
9.1875 |
258.8028 |
< 0.0001 |
|
|
D-FeSO4 |
0.040833 |
1 |
0.040833 |
1.150235 |
0.3016 |
|
|
AB |
0 |
1 |
0 |
0 |
1.0000 |
|
|
AC |
7.5625 |
1 |
7.5625 |
213.0282 |
< 0.0001 |
|
|
AD |
0.25 |
1 |
0.25 |
7.042254 |
0.0189 |
|
|
BC |
3.4225 |
1 |
3.4225 |
96.40845 |
< 0.0001 |
|
|
BD |
0.49 |
1 |
0.49 |
13.80282 |
0.0023 |
|
|
CD |
8.1225 |
1 |
8.1225 |
228.8028 |
< 0.0001 |
|
|
A^2 |
138.0509 |
1 |
138.0509 |
3888.757 |
< 0.0001 |
|
|
B^2 |
172.9298 |
1 |
172.9298 |
4871.262 |
< 0.0001 |
|
|
C^2 |
171.2593 |
1 |
171.2593 |
4824.205 |
< 0.0001 |
|
|
D^2 |
132.1309 |
1 |
132.1309 |
3721.997 |
< 0.0001 |
|
|
Residual |
0.497 |
14 |
0.0355 |
|||
|
Lack of Fit |
0.245 |
10 |
0.0245 |
0.388889 |
0.8971 |
not significant |
|
Pure Error |
0.252 |
4 |
0.063 |
|||
|
Cor Total |
428.3876 |
28 |
||||
|
Std. Dev. |
0.188414 |
R-Squared |
0.99884 |
|||
|
Mean |
6.42069 |
Adj R-Squared |
0.99768 |
|||
|
C.V. % |
2.934489 |
Pred R-Squared |
0.995787 |
|||
|
PRESS |
1.80495 |
Adeq Precision |
94.28807 |
|||
Figure -2 – Contour Plot and Surface
graph showing the interaction between the components
(a) A and B (b) A and C (c) A and D (d) B and C (e) B and D (f) C and D
CONCLUSION:
The application
of RSM was used to optimize culture media for the production of rhamnolipids by Pseudomonas
aeruginosa isolated from oil contaminated soil.
The pure culture was enhanced and optimized at pH- 7, temperature-37oC
and olive oil as effective carbon source. Further the cultural media was
optimized using RSM -BB perceiving with 30 olive oil, 5 NaNO3, 4 KH2PO4
and 7.5 FeSO4 mixture contributes maximum production of rhamnolipid. The R2 value was 99.8 that
correlated with Adjusted R2 value of 99.7 and Predicted R2
value of 99.5 shows the model is significant.
REFERENCE:
1.
Fiechter A. Biosurfactants: moving towards industrial application. Trends Biotechnol.
10; 1992:208–217
2.
Inakollu S, Hung HC,
Shreve GS. Biosurfactant enhancement of microbial
degradation of various structural classes of hydrocarbon in mixed waste
systems. Environ Eng Sci. 21;2004:
463–469
3.
Guerra-Santos L, Käpeli O,
Fiechter A. Pseudomonas
aeruginosabiosurfactant
production in continuous culture with glucose as carbon source. Appl Environ Microbiol.
48; 1984:302–305
4.
Abalos A, Vinas M, Sabate J, Manresa MA, Solanas AM. Enhanced biodegradation of Casablanca crude oil
by a microbial consortium in presence of a rhamnolipid
produced by Pseudomonas aeruginosa AT10. Biodegradation.
15;2004:249–260
5.
Lee Y, Lee SY, Yang JW.Production
of rhamnolipid biosurfactant
by fed-batch culture of Pseudomonas aeruginosa using glucose as a sole carbon source. BiosciBiotechnolBiochem.63;1999:946–947
6.
Manreas MA, Bastida J, Mercadé ME, Robert M,
de Andrés C, Espuny MJ, Guinea J. Kinetic studies on
surfactant production by Pseudomonas aeruginosa 44T1. J
IndMicrobiol 8;1991:133–136
7.
Prabhu Y, Rhamnolipidle PS. Biodegradation of phenanthrene
by Pseudomonas sp. strain PP2: novel
metabolic pathway, role of biosurfactant and cell
surface hydrophobicity in hydrocarbon assimilation. ApplMicrobiolBiotechnol.61;2003:342–351
8.
Rashedi H, Jamshidi E, MazaheriAssadi M, Bonakdarpour B. Biosurfactant
production with glucose as a carbon source. ChemBiochemEng
Q 20;2006: 99–106.
9.
Reiling HE, Thanei-Wyss U, Guerra-Santos LH, HirtR,
Käppeli O, Fiechter A.
Pilot plant production of rhamnolipid biosurfactant by Pseudomonas
aeruginosa. Appl Environ Microbiol51;1986:985–989
10.
VenkataRamana K, Karanth N (1989) Factors affecting biosurfactant
production using Pseudomonas aeruginosa CFTR-6 under
submerged conditions. J ChemTechnolBiotechnol. 45;1989:249–257
11.
Arino S, Marchal R, Vandecasteele JP.
Identification and production of rhamnolipidicbiosurfactants
by a Pseudomonas species. ApplMicrobiolBiotechnol
45;1996: 162–168
12.
Benincasa M, ContieroJ, Manresa MA, Moraes IO.
Rhamnolipid production by Pseudomonas aeruginosa LBI growing on soapstock as the sole carbon source. J Food Eng. 54; 2002:283–288
13.
Abdel-Fattah YR, Saeed HM,
Gohar YM, El-Baz MA. Improved production of Pseudomonas aeruginosauricase
by optimization of process parameters through statistical experimental designs.
Process Biochem.
40;2005:1707–1714
14.
Dubois M, Gilles KA, Hamilton JK, Rebers PA, Smith T. Colorimetric method
for determination of sugars and related substances. Anal Chem. 28;1956:350–356
15.
Soberón-Chávez G, Lépine F, Déziel E. Production of
rhamnolipids by Pseudomonas
aeruginosa.ApplMicrobiolBiotechnol.68;2005:718–725
16.
Goswami P, Singh HD.
Different modes of hydrocarbon uptake by two Pseudomonas species. BiotechnolBioeng.
37;1991:1–11
17.
Hauser G, Karnovsky ML.Rhamnose and rhamnolipid
biosynthesis by Pseudomonas aeruginosa. J BiolChem 224;1957:91–105
18.
Hori K, Matsuzaki Y, Tanji Y, Unno H. Effect of
dispersing oil rhamnolipidse on the biodegradability
of a solid alkane dissolved in non-biodegradable oil.
ApplMicrobiolBiotechnol. 59;2002:574–579
19.
Jarvis FG, Johnson MJ. A glycolipipd
produced by Pseudomonas aeruginosa. J Am
ChemSoc 71; 1949:4124–4126
20.
Lang S, Wullbrandt D. Rhamnose lipids—biosynthesis, microbial production and
application potential. ApplMicrobiolBiotechnol
51;1999:22–32
21.
Maier RM, Chavez GS. Pseudomonas aerugionsarhamnolipids:
biosynthesis and potential applications. ApplMicrobiolBiotechnol. 54; 2000:625–633
22.
Pruthi V, Cameotra SS. Rapid identification of biosurfactants
producing strains using a cell surface hydrophobicity
technique. Biotechnol Tech 11; 1997:671–674
23.
Mata-Sandoval J, Karns J
and Torrents A. High-performance liquid chromatography method for the
characterization of rhamnolipid mixture produced by
Pseudomonas aeruginosa UG2 on corn oil. J Chromatogr
864; 1999:211–220
24.
Matsufuji M, Nakata K,
Yoshimoto A. High production of rhamnolipid by
Pseudomonas aeruginosa growing on ethanol. Biotechnol Lett. 19;
1997:1213–1215
25.
Mukherjee S, Das P, Sen R. Towards commercial production of microbial
surfactants. Trends Biotechnology.
24; 2006:509–515
26.
Mulligan CN. Environmental applications for
bio-surfactants. Environ pollution
133;2005:183–198
27.
Neu TR andPoralla K. Emulsifying agents from bacteria isolating
during screening for cells with hydrophobic surfaces. ApplMicrobiolBiotechnol. 32; 1990:521–525
28.
Noordman WH and Janssen
DB. Rhamnolipid stimulates uptake of hydrophobic
compounds by Pseudomonas aeruginosa. Appl Environ Microbiol 68;
2002:4502–4508
29.
Perfumo A, Banat IM, Canganella F, Marchant R. Rhamnolipid production by a novel thermophilic
hydrocarbon-degrading Pseudomonas aeruginosa AP02-1. ApplMicrobiolBiotechnol 72;
2006:132–138
30. Reddy PG, Singh
HD, Pathak MG, Bhagat SD
and Baruah JN. Isolation and functional
characterization of hydrocarbon emulsifying and solubilizing
factors produced by a Pseudomonas
species. BiotechnolBioeng
25; 1983:387–401
Received on 16.03.2016 Modified on 04.04.2016
Accepted on 25.04.2016 © RJPT All right reserved
Research J.
Pharm. and Tech. 9(4): April, 2016; Page 335-339
DOI: 10.5958/0974-360X.2016.00059.7