3. FOOD ChEMISTRy & bIOTEChNOLOGy 3.1. Lectures
3. FOOD ChEMISTRy & bIOTEChNOLOGy 3.1. Lectures
3. FOOD ChEMISTRy & bIOTEChNOLOGy 3.1. Lectures
Create successful ePaper yourself
Turn your PDF publications into a flip-book with our unique Google optimized e-Paper software.
Chem. Listy, 102, s265–s1311 (2008) Food Chemistry & Biotechnology<br />
L03 SOLID STATE FERMENTATION AS A TOOL<br />
FOR PREPARATION OF bIOPRODuCTS<br />
ENRIChED wITh POLyuNSATuRATED<br />
FATTy ACIDS<br />
MILAn ČERTíK, ZUZAnA ADAMECHOVá and LInDA<br />
néMETH<br />
Department of Biochemical Technology, Faculty of Chemical<br />
and Food Technology, Slovak University of Technology, Radlinského<br />
9, 812 37 Bratislava, Slovak Republic,<br />
milan.certik@stuba.sk<br />
Introduction<br />
Increasing demand for high-value lipids has focused<br />
commercial attention on the provision of suitable biosynthetic<br />
framework for their production. One of the main target for<br />
microbial oil transformation is construction of healthy and<br />
dietary important polyunsaturated fatty acids, such as γ-linolenic<br />
acid (18 : 3 ω-6; GLA), dihomo-γ-linolenic acid (20 : 3<br />
ω-6; DGLA), arachidonic acid (20 : 4 ω-6; AA), eicosapentaenoic<br />
acid (20 : 5 ω-3; EPA) and docosahexaenoic acid (22 : 6<br />
ω-3; DHA). Their applications in biomedical, nutritional and<br />
pharmaceutical fields coupled with their inadequacy from<br />
conventional agricultural and animal sources has looked for<br />
developing suitable biotechnologies to produce these compounds<br />
1 .<br />
Particularly active in the synthesis of PUFAs are species<br />
of fungi belonging to Zygomycetes 2 . Oleaginous fungi<br />
producing PUFA could be economically valuable because<br />
the most of their PUFAs occur in the triacylglycerol fraction<br />
of their lipids. Two basic processes have been developed for<br />
microbial production of PUFAs: submerged and solid state<br />
fermentations 3,4 . However, the principal difficulty that has<br />
been experienced with submerged PUFA-riched oil production<br />
has been in its marketing rather than in developing<br />
the large-scale fermentation and oil extraction process. Therefore,<br />
the association of oleaginous fungi with solid state<br />
fermentations (SSF) has been developed in order to improve<br />
commercial potential of microbial oils and thus to create new<br />
perspectives for the economic competitiveness and market of<br />
microbial polyunsaturated fatty acids (PUFAs). Solid state<br />
fermentation is a process in which microorganisms grow<br />
on a moist solid substrate in the absence of free water 5 . SSF<br />
simulates fermentation reactions occurring in the nature and<br />
allows microbial utilization of raw agro-materials or byproducts<br />
of the agro-food industries. Because some oleaginous<br />
fungi simultaneously decrease anti-nutrient compounds in<br />
the substrates (e.g. phytic acid) and partially hydrolyze substrate<br />
biopolymers, prefermented mass with a high content<br />
of PUFAs may be used as inexpensive food and feed supplement<br />
6 . Thus, SSF might provide the other opportunity to fill<br />
marketing claims in food, feed, pharmaceutical, veterinary<br />
and environmental fields.<br />
This paper deals with effectivity of several lower filamentous<br />
fungi to synthesize various PUFAs during their utilization<br />
of cereals by solid state fermentations.<br />
s544<br />
Experimental<br />
M i c r o o r g a n i s m s<br />
Thamnidium elegans CCF 1456, Cunninghamella echinulata<br />
CCF-103, Cunninghamella elegans CCF-1318, Mortierella<br />
isabelina CCF-14, Mortierella isabelina CCF-1098,<br />
Mortierella alpina CCF 185 were obtained from the Culture<br />
Collection of Fungi (Charles University, Prague, Czech<br />
Republic). The culture was maintained on modified Czapek-<br />
Dox agar slants with yeast extract (2.5 g dm –3 ) at 4 °C.<br />
S u b s t r a t e s a n d C u l t i v a t i o n<br />
C o n d i t i o n s<br />
Depending on the microorganism, various types of substrates<br />
were employed during SSF experiments. Spent malt<br />
grains (SMG) were added to some substrates. Autoclavable<br />
microporous polypropylene bags (160 × 270 mm 2 ) were filled<br />
with 10 g of dry substrate, moistened by the addition of 10 ml<br />
distilled water, soaked for 2 h at laboratory temperature and<br />
sterilized in autoclave (120 kPa, 120 °C, 20 min). In order<br />
to increased yield of PUFAs, sunflower or linseed oils were<br />
added to some substrates. In addition, various amounts of<br />
10% acetone or ethanol solutions of selected plant extracts<br />
were tested with the aim to activate enzymes involved into<br />
PUFA biosynthesis. The substrates were inoculated and<br />
mixed with 2 ml of spore suspension (1–2 × 10 6 spores per<br />
ml). Then each bag was closed with sterile cotton plugs,<br />
inoculated substrate was spread in the bags to obtain substrate<br />
layer of about 1 cm and incubated statically at 25 °C<br />
for 4–6 days (T. elegans, C. echinulata, C. elegans, M. isabellina)<br />
and 10–14 days (M. alpina). Triplicate SSF experiments<br />
for each substrate were prepared to assess reproducibility and<br />
average results are presented.<br />
L i p i d E x t r a c t i o n a n d F a t t y A c i d<br />
A n a l y s i s<br />
Prefermented cereal materials (bioproducts) were gently<br />
dried at 65 °C for 10 h and weighed. Lipids from homogenized<br />
bioproducts were isolated with chloroform/methanol<br />
(2 : 1, v/v) and purified according to Čertík et al. 7 and total<br />
lipids were determined gravimetrically. Fatty acids of total<br />
lipids were analyzed as their methyl esters 8 by gas chromatography<br />
according to Čertík et al 9 . Gas chromatograph (GC-<br />
6890 n, Agilent Technologies) was equipped with a capillary<br />
column DB-23 (60 m × 0.25 mm, film thickness 0.25 μm,<br />
Agilent Technologies) and a FID detector (constant flow,<br />
hydrogen 35 ml min –1 , air 350 ml min –1 , 250 °C). Analyses<br />
were carried out under a temperature gradient (130 °C for<br />
1 min; 130–170 °C at program rate 6.5 °C min –1 ; 170–215°C<br />
at program rate 2.7°C min –1 ; 215 °C for 7 min; 220–240 °C at<br />
program rate 2 °C min –1 ; 240 °C for 2 min) with hydrogen as<br />
a carrier gas (flow 2.1 ml min –1 , velocity 49 cm s –1 , pressure<br />
174 kPa) and a split ratio of 1/50 (inlets: heater 230 °C, total<br />
hydrogen flow 114 ml min –1 , pressure 174 kPa). The fatty<br />
acid methylester peaks were identified by authentic standards<br />
of C 4 –C 24 fatty acid methylesters mixture (Supelco, USA)<br />
and quantified by an internal standard of heptadecanoic acid