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3. FOOD ChEMISTRy & bIOTEChNOLOGy 3.1. Lectures

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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

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