I. Martin-Arjol et al. / Process Biochemistry 48 (2013) 224–230
225
commercial lipases were classified according to a ratio competitive
factor (RCF), are very helpful in determining substrate selectivity
toward isomeric 9-octadecenoic acids in n-hexane [27].
Quantitative analysis of OA, (10S)-HPOME, (10S)-HOME and (7S,10S)-DiHOME
was carried out by liquid chromatography in a Shimadzu LC-9A Chromatograph
(Kyoto, Japan). Samples were injected into the HPLC with a Sedex 55 light-scattering
detector (Sedere, Alfortville Cedex, France) equipped with a Tracer Excel 120 C8 col-
umn (5 m, 150 mm × 4.6 mm) (Teknokroma, Sant Cugat del Vallès, Spain). Optimal
separation was achieved with an elution gradient using A, acetonitrile (Fischer Sci-
entific, Madrid, Spain) (0.1%, v/v acetic acid), and B, water (0.1%, v/v acetic acid),
at a flow rate of 1 ml min−1. The gradient (time (min), %B) used was as follows: (0,
70), (10, 0), (15, 0), (20, 70), and (25, 70). The injection volume was 20 l. A known
homemade standard of each hydroxy-fatty acid and substrate was used to identify
the retention times and to quantify the samples. Cell growth was calculated as dry
cell weight. The biomass of the samples was placed in an oven at 100 ◦C for 24 h. The
nitrate concentration was determined using QUANTOFIX® nitrate/nitrite test strips
It is a difficult to both detect and characterize estolides. Gas
chromatography coupled with mass spectrometry has proven use-
less due to the high boiling point of estolides [28–30]. In recent
years, matrix-assisted laser desorption/ionization time-of-flight
mass spectrometry (MALDI-TOF-MS) has emerged as a powerful
technique to analyze synthetic polymers. Cvacka and co-workers
analyzed WE using the MALDI-TOF-MS technique with a matrix
of lithium salt of 2,5-dihydroxybenzoic acid (DBH) to increase the
intensity of the signal for obtaining a good reproducibility [31].
They were able to characterize natural samples of WE with great
accuracy.
(Macherey-Nagel, Düren, Germany). All concentrations are expressed in g l−1
.
2.3. Purification of trans-hydroxy-fatty acids
At the end of cultivation, the culture was centrifuged (14,700 × g for 30 min
at 4 ◦C), the supernatant was acidified to pH 2.0 with 37% HCl (Panreac, Castellar
del Vallès, Spain), and two extractions were performed with a half volume of ethyl
acetate (Carlo-Erba Reagents-SdS, Sabadell, Spain). The organic phase was dried over
an anhydrous sodium sulfate filter (Panreac, Castellar del Vallès, Spain), and the
solvent of the combined extracts was evaporated with a rotary evaporator (Bücchi,
Postfach, Switzerland), resulting in a yellow oil. Organic extracts were kept in vials
at 4 ◦C under nitrogen to prevent further oxidation. The (10S)-HOME and (7S,10S)-
DiHOME were purified by flash-chromatography in a glass column (50 cm long and
with 3 cm inner diameter) filled with silica gel 60 (0.040–0.063 mm, Merck, Madrid,
Spain). The mobile phase used was formed by n-hexane:diethyl ether:methanol
The primary goal of this research is to develop new bio-based
materials from agroindustrial wastes. To this end, oleic acid, which
is present to a high degree in residual oily wastes, was used as
a substrate for the production of 10(S)-hydroxy-8(E)-octadecenoic
and 7,10(S,S)-dihydroxy-8(E)-octadecenoic acids ((10S)-HOME and
(7S,10S)-DiHOME, respectively) by P. aeruginosa 42A2. Next, the
monomer (10S)-HOME was used to synthesize estolides in vitro
with Novozym 435. MALDI-TOF-MS and LC–MS techniques were
used to determine the estolides’ structure. Finally, lipases were
screened in an organic medium to improve the reaction yield of
the catalytic synthesis of estolides.
under nitrogen, as stated above.
C
2. Materials and methods
2.4. Product yields and productivity of monomers
2.1. Materials
The whole specific product yield (YP/X (Eq. (1))) and specific (10S)-HOME and
(7S,10S)-DiHOME yields (Y(10S)-HOME/X and Y(7S,10S)-HOME/X (Eq. (2))), were calculated
P. aeruginosa 42A2 NCIMB 40045 was maintained on TSA (Trypticase soy agar;
Difco, Franklin lakes, IL, USA) slants at 30 ◦C and after an incubation period of 24 h
was kept at 4 ◦C and subcultured every two weeks. The strain was preserved frozen
(−80 ◦C) in cryobilles (AES CHEMUNEX S.A., Terrassa, Spain). A lipase from C. rugosa
(1104 units/mg solid) was purchased from Sigma–Aldrich (Madrid, Spain). Novozym
435, immobilized lipase B from C. antarctica (10,000 propyl laureate units/g solid),
Lipozyme RM IM (an immobilized lipase from R. miehei, 275 interestification units/g
solid) and Lipozyme TL IM (a lipase from Thermomyces lanuginosus, 250 interestifi-
cation units/g solid) were generous gifts from Novozym A/S (Bagsvaerd, Denmark).
Lipase A from Rhizopus oryzae was donated by Prof. Francisco Valero (Chem Eng
Dept UAB, Cerdanyola del Vallès, Spain). Analytical grade n-hexane, methanol and
diethyl ether were purchased from Carlo-Erba Reagents-SdS (Sabadell, Spain). Ana-
lytical grade iso-octane for spectroscopy UV–IR and potassium hydroxide (KOH) 85%
were purchased from Panreac (Castellar del Vallès, Spain). Ricinoleic acid (RA) 80%
was supplied by Fluka (Madrid, Spain) and oleic acid (OA) technical grade 90% was
purchased from Sigma–Aldrich (Madrid, Spain).
over the entire process as the productivity of each hydroxy-fatty acid, q(10S)-HOME
q(7S,10S)-DiHOME, instead of the OA consumption rate, qOA, which was calculated over
the first 15 h of cultivation (Eq. (3)).
,
ꢀC((10S)-HOME) + ꢀC(7S, 10S)-DiHOME)
YP/X (g
=
(1)
(2)
−1
g
)
ꢀC(X)
ꢀC(10S)-HOME
ꢀC(X)
Y(10S)-HOME/X (g
=
;
−1
g
)
ꢀC(7S, 10S)-DiHOME
=
ꢀC(X)
Y(7S,10S)-DiHOME/X (g
−1
g
)
ꢀC((7S, 10S)-DiHOME)
ꢀC(OA)
ꢀt
q(7S,10S)-DiHOME (g l−1 h−1) =
;
qOA (g l−1 h−1) =
ꢀt
(3)
2.2. Production and quantification of monomers
2.5. Measurement of the reaction yield of estolides synthesis
P. aeruginosa 42A2 NCIMB 40045 was cultured in the following saline medium
(in g l−1): CaCl2 (0.01), NaNO3 (3.5), K2HPO4 (2.0), KH2PO4 (1.0), KCl (0.1),
MgSO4·7H2O (0.5), FeSO4·7H2O (0.012) and 0.05 ml l−1 trace elements solution. The
trace elements solution was as follows (in mg 100 ml−1): H3BO3 (148), CuSO4·5H2O
(196), MnSO4·H2O (154), Na2MoO4·2H2O (15) and ZnSO4·7H2O (307). This medium
was supplemented with OA at 2% (v/v).
The reactions were monitored by titration to determine the acid value (AV)
[23] of the samples. After evaporating the organic solvent, a 30 mg aliquot of the
reaction mixture was titrated with 0.05 M KOH using phenolphthalein as indicator.
All samples were analyzed in triplicate. The AV and the yield of the reaction were
calculated as follows (Eq. (4)):
The bioreactor was inoculated with 200 ml of a 24 h culture in a saline medium
containing 20 g l−1 OA as a carbon source. The inoculum-culture was carried out
on an orbital shaker for 18 h at 150 rpm rotational speed and 30 ◦C. Cells were har-
vested by centrifugation (14,700 × g for 30 min at 4 ◦C) and resuspended with NaCl
0.9% (w/v) at 2% (v/v) to an optical density of 2.0 at 540 nm prior to inoculation
into the bioreactor. The cultures were cultivated at a working volume of 2 l in a 3-
L bench top bioreactor (Biostat B. Braun Biotech International GmbH, Melsungen,
Germany) using the mineral salts medium described above. During the culture, dis-
solved oxygen was monitored continuously with an O2 electrode (Ingold 12/200 B.
Braun Biotech. International GmbH, Melsungen, Germany) and maintained at 30%
oxygen saturation by automatic cascade control of the stirrer speed, 500–700 rpm,
with an air flow between 2.5 and 7.5 l min−1. The air flow was enriched with oxy-
gen (Carburos Metálicos, Spain) when needed. The temperature was measured at
30 ◦C by a Pt-100/200-4 temperature sensor (B. Braun Biotech. International GmbH,
Melsungen, Germany). The pH was automatically kept at 7.0 using 2 M HCl and 2 M
NaOH solutions. The data were recorded using an external computer connected to
the control unit of the bioreactor. The software used was MFCS/win 2.0 (B. Braun
Biotech International, Sartorius, Mesulgen, Germany). The culture was maintained
until all 10(S)-hydroperoxy-8(E)-octadecenoic acid ((10S)-HPOME) was converted
to (10S)-HOME and (7S,10S)-DiHOME.
AVsubstrate − AVproduct
ꢁ (%) =
· 100
(4)
AVsubstrate
2.6. Effect of enzyme concentration
Different quantities of Novozym 435 (0.3–1.5 g) were assayed to obtain the opti-
mal amount of enzyme for a reaction with 0.6 g of (10S)-HOME in 20 ml of n-hexane
in a 100 ml Erlenmeyer flask for 48 h at 50 ◦C. A rotary evaporator system was used to
achieve an efficient degree of contact between the enzyme and the substrate and to
maintain the required temperature. All reactions were carried out at atmospheric
pressure. The reaction extension was calculated using Eq. (4), as shown above. A
control was assayed to confirm that this reaction does not occur spontaneously.
An aliquot of 0.5 g of Novozym 435 was used to study polymerization with dif-
ferent amounts of (10S)-HOME (0.25–1.0 g). The enzymatic reaction was performed
under the same conditions described above and included a control. The yield of the
reaction was calculated with Eq. (4).