Effect of acyl donor chain length and sugar/acyl donor molar ratio on enzymatic synthesis of fatty acid fructose esters

Lipase-catalyzed synthesis of fatty acid sugar esters through direct esterification was performed in 2-methyl 2-butanol as solvent. Fructose and saturated fatty acids were used as substrates and the reaction was catalyzed by immobilized Candida antarctica lipase. The effect of the initial fructose/acyl donor molar ratio and the carbon-chain length of the acyl donor as well as their reciprocal interactions on the reaction performance were investigated. For this purpose, an experimental design taking into account variations of the molar ratio (from 1:1 to 1:5) and the carbon-chain length of the fatty acid (from C8 to C18) was employed. Statistical analysis of the data indicated that the two factors as well as their interactions had significant effects on the sugar esters synthesis. The obtained results showed that whatever the molar ratio used, the highest concentration (73 g l⁻¹), fructose and fatty acid conversion yields (100% and 80%, respectively) and initial reaction rate (40 g l⁻¹ h⁻¹) were reached when using the C18 fatty acid as acyl donor. Low molar ratios gave the best fatty acid conversion yields and initial reaction rates, whereas the best total sugar ester concentrations and fructose conversion yields were obtained for high molar ratios.     

Effects of medium glucose concentration and pH on docosahexaenoic acid content of heterotrophic Crypthecodinium cohnii

The effects of medium glucose concentration and pH on growth and docosahexaenoic acid (DHA, C22:6 ω-3) content of Crypthecodinium cohnii were investigated. Over a range of glucose concentrations (5–40 g l⁻¹) investigated, the highest specific growth rate (0.12 h⁻¹), highest cell dry weight concentration (3.13 g l⁻¹) and highest growth yield on glucose (0.6 g g⁻¹) were obtained at 20 g l⁻¹ glucose. However, the highest degree of fatty acid unsaturation (3.2) and highest DHA proportion (53.4% of total fatty acids) were achieved at 5 g l⁻¹ glucose. Low glucose concentrations enhanced the degree of fatty acid unsaturation and DHA formation. Medium pH also affected cell growth, fatty acid unsaturation and DHA proportion. When medium pH was 7.2, the highest specific growth rate (0.089 h⁻¹), highest cell dry weight concentration (2.73 g l⁻¹), highest growth yield on glucose (0.564 g g⁻¹), highest degree of fatty acid unsaturation (3.4) and highest DHA proportion (56.8% of total fatty acids) were obtained. Results suggest that glucose concentration and pH value could be effectively manipulated to achieve maximum DHA production by C. cohnii.     

High-density cultivation of Perilla frutescens cell suspensions for anthocyanin production: Effects of sucrose concentration and inoculum size

High-density cultivation of Perilla frutescens cells for anthocyanin production was carried out in both batch and fed-batch modes in a 500-ml shake flask. In fed-batch cultures, a high cell density of 27.7 g dry cells l⁻¹ and a total anthocyanin production of 3.87 g l⁻¹ by intermittent feeding of all medium components except hormones were obtained. In batch cultures, both initial sucrose concentration and inoculum size showed a conspicuous effect on the kinetics of cell growth, sugar consumption, and secondary metabolite (anthocyanins) production by suspended P. frutescens cells. At an inoculum size of 50 g wet cells l⁻¹, the maximum cell density of 38.3 g dry cells l⁻¹ was obtained after 11 days of cultivation at an initial sucrose concentration of 60 g l⁻¹, the highest pigment production of>5.8 g l⁻¹ was attained after 10 days of cultivation at an initial sucrose concentration of 45 g l⁻¹. These amounts of cell mass and anthocyanin pigments were 3.3 and 24 times higher than those at an initial sucrose concentration of 15 g l⁻¹ and inoculum size of 15 g wet cells l⁻¹, respectively.     

Effects of feed sugar concentration on continuous ethanol fermentation of cheese whey powder solution (CWP)

Cheese whey powder (CWP) solution with different CWP or sugar concentrations was fermented to ethanol in a continuous fermenter using pure culture of Kluyveromyces marxianus (DSMZ 7239). Sugar concentration of the feed CWP solution varied between 55 and 200 g l⁻¹ while the hydraulic residence time (HRT) was kept constant at 54 h. Ethanol formation, sugar utilization and biomass formation were investigated as functions of the feed sugar concentration. Percent sugar utilization and biomass concentrations decreased and the effluent sugar concentration increased with increasing feed sugar concentrations especially for the feed sugar contents above 100 g l⁻¹. Ethanol concentration and productivity (DP) increased with increasing feed sugar up to 100 g l⁻¹ and then decreased with further increases in the feed sugar content. The highest ethanol concentration (3.7%, v v⁻¹) and productivity (0.54 gE l⁻¹ h⁻¹) were obtained with the feed sugar content of 100 g l⁻¹ or 125 g l⁻¹. The ethanol yield coefficient (Y_P/S) was also maximum (0.49 gE gS⁻¹) when the feed sugar was between 100 and 125 g l⁻¹. The growth yield coefficient (Y_X/S) decreased steadily from 0.123 to 0.063 gX gS⁻¹ when the feed sugar increased from 55 to 200 g l⁻¹ due to adverse effects of high sugar contents on yeast growth. The optimal feed sugar concentration maximizing the ethanol productivity and sugar utilization was between 100 and 125 g l⁻¹ under the specified experimental conditions.     

Identification of by-products in hydrogen producing bacteria; Rhodobacter sphaeroides O.U. 001 grown in the waste water of a sugar refinery

Rhodobacter sphaeroides O.U. 001 is able to produce hydrogen anaerobically upon illumination. The cells were screened for the presence of valuable by-products such as poly-β-hydroxy (PHB) butyric acid aiming to improve the feasibility of the system. Also waste water from a sugar refinery was used for bacterial growth to further increase the feasibility. Under aerobic conditions the standard growth media containing -malic acid and sodium glutamate in 7.5/10 and 15/2 molar ratios and a medium containing 30% waste water from sugar refinery were used. In this case the maximum concentration of PHB produced were approximately 0.2 g l⁻¹ in both of the standard media whereas it was 0.3 g l⁻¹ in medium containing 30% waste water. By using the medium containing 30% waste water, PHB and hydrogen productions were determined under anaerobic conditions. The maximum concentration of PHB produced was around 0.5 g l⁻¹ and the amount of gas collected was 35 ml in 108 h. From these results it can be concluded that PHB can be collected during hydrogen production. The use of waste water from sugar refinery increased the yield.     

Characterization of two-substrate fermentation processes for xylitol production using recombinant Saccharomyces cerevisiae containing xylose reductase gene

Fermentation characteristics of recombinant Saccharomyces cerevisiae containing a xylose reductase gene from Pichia stipitis were investigated in an attempt to convert xylose to xylitol, a natural five-carbon sugar alcohol used as a sweetener. Xylitol was produced with a maximum yield of 0.95 g g⁻¹ xylitol xylose consumed in the presence of glucose used as a co-substrate for co-factor regeneration. Addition of glucose caused inhibition of xylose transport and accumulation of ethanol. Such problems were solved by adopting glucose-limited fed-batch fermentations where a high ratio of xylose to glucose was maintained during the bioconversion phase. The optimized two-substrate fed-batch fermentation carried out with S. cerevisiae EH13.15:pY2XR at 30°C resulted in 105.2 g l⁻¹ xylitol concentration with 1.69 g l⁻¹ h⁻¹ productivity.     

Arachidonic acid production by Mortierella alpina with growth-coupled lipid synthesis

The fungus Mortierella alpina LPM 301, a producer of arachidonic acid (ARA), was found to possess a unique property of a growth-coupled lipid synthesis. An increase in specific growth rate (μ) from 0.03 to 0.05 h⁻¹ resulted in a two-fold increase in the specific rate of lipid synthesis (milligram lipid (gram per lipid-free biomass) per hour). Under batch cultivation in glucose-containing media with urea or potassium nitrate as nitrogen sources, the ARA content was 46.0 and 60.4% of lipid; 16.4 and 18.8% of dry biomass; and 4.2 and 4.5 g l⁻¹, respectively. Under continuous cultivation of the strain, the productivity of ARA synthesis was 16.2 and 19.2 mg l⁻¹ h⁻¹ at μ=0.05 and 0.03 h⁻¹, respectively.     

Optimisation of docosahexaenoic acid production in batch cultivations by Crypthecodinium cohnii

The heterotrophic micro alga Crypthecodinium cohnii was cultivated in media containing glucose, yeast extract and sea salt. Increasing amounts of yeast extract stimulated growth but influenced lipid accumulation negatively. Sea salt concentrations above half the average seawater salinity were required for good growth and lipid accumulation. C. cohnii was able to grow on a glucose concentration as high as 84.3 g l⁻¹, although concentrations above 25 g l⁻¹ decreased the growth rate. Comparison of growth at 27 and 30°C showed that the higher incubation temperature was more favourable for growth. However, lipid accumulation was higher at the lower incubation temperature. In a bioreactor the biomass concentration increased from 1.5 to 27.7 g l⁻¹ in 74 h. In the final 41 h of the process the lipid content of the biomass increased from 7.5 to 13.5%. In this period the percentage of docosahexaenoic acid of the lipid increased from 36.5 to 43.6%. The total amounts of lipid and docosahexaenoic acid after 91 h were 3.7 and 1.6 g l⁻¹, respectively.     

Optimization of lipase-catalyzed glucose fatty acid ester synthesis in a two-phase system containing ionic liquids and t-BuOH

Selective lipase-catalyzed synthesis of glucose fatty acid esters in two-phase systems consisting of an ionic liquid (1-butyl-3-methyl imidazolium tetrafluoroborate [BMIM][BF₄] or 1-butyl-3-methyl imidazolium hexafluorophosphate [BMIM][PF₆]) and t-butanol as organic solvent was investigated. The best enzyme was commercially available lipase B from Candida antarctica (CAL-B), but also lipase from Thermomyces lanuginosa (TLL) gave good conversion. After thorough optimization of several reaction conditions (chain-length and type of acyl donor, temperature, reaction time, percentage of co-solvent) conversions up to 60% could be achieved using fatty acid vinyl ester as acyl donors in [BMIM][PF₆] in the presence of 40% t-BuOH with CAL-B at 60 °C.     

Continuous production of lactic acid from whey permeate by Lactobacillus helveticus in two chemostats in series

The effect of dilution rate on the production of lactic acid from whey permeate by Lactobacillus helveticus has been investigated. In the first chemostat of a two-stage system, total conversion (98.1%) and maximum lactic acid concentration (43.7 g l⁻¹) were obtained at a dilution rate (D_Itot) of 0.06 h⁻¹. Maximum volumetric productivities of lactic acid (8.27 g l⁻¹ h⁻¹) and biomass (1.90 g l⁻¹ h⁻¹) occurred at D_Itot of 0.40 h⁻¹. The fraction of -lactate in the product was found to increase with dilution rate and reached a maximum of 66% at the same dilution rate. The maximum specific growth rate (μ_max) on this medium was 0.7 h⁻¹. A Y_ATP (max) value of 22.4 g dry weight (mol ATP)⁻¹ and a maintenance coefficient of 8.0 mmol ATP (g dry weight h)⁻¹ were determined. The second stage, in series with the first, confirmed these results and further showed that the total residence time could be reduced by 50%, compared with a single chemostat for the same nearly complete level of substrate conversion.     

The growth and nutrient utilization of the insect cell line Spodoptera frugiperda Sf9 in batch and continuous culture

The growth of the Spodoptera frugiperda cell line Sf9 was studied in batch and continuous culture. The results of batch cultivations showed that glucose was the preferred energy and carbon source limiting the cell density in both TNM-FH and IPL-41 media. Continuous culture using IPL-41-based feeding medium with different glucose (2.5, 5 and 10 g l⁻¹) and yeast extract concentrations (4, 8 and 16 g l⁻¹) showed that in serum-supplemented medium the maximum cell density was limited by glucose and yeast extract concentration. The transition to glucose limitation caused a decrease in growth rate and viability. A high cell density culture (18 × 10⁶ ml⁻¹) was obtained using a glucose concentration of 10 g l⁻¹ and a yeast extract concentration of 8 g l⁻¹ in the feeding medium. A yeast extract concentration of 16 g l⁻¹ inhibited growth. Unlike mammalian cell cultures, lactate, alanine and ammonia were not involved in growth inhibition. Lactate did not accumulate under aerobic conditions. Ammonia accumulation, if observed, was insignificant. The level of alanine synthesized and excreted into the culture medium never reached an inhibitory level. During glucose limitation alanine did not accumulate and ammonia was released. However, even in the presence of glucose significant amounts of Asp, Glu, Gln, Asn, Ser, Arg and Met were utilized for energy production. The amino groups of these amino acids were transferred to pyruvate or used for nucleic acid synthesis and excreted in the form of alanine into the culture medium. The consumption of His, Lys, Thr, Gly, Val, Leu, Phe, Tyr, Trp and Ile by growing Sf-9 cells was almost equal to their concentration in the biomass.     

The effect of water concentration on the activity and stability of CLECs in supercritical CO2 in continuous operation

In this study the effect of the water concentration on a crystallized enzyme of Candida antarctica lipase B (ChiroCLEC™-CAB) in supercritical carbon dioxide (scCO₂) is studied. The model reaction used is the enantioselective esterification of racemic 1-phenyl ethanol with vinyl acetate; the reaction is performed in scCO₂ at 40 °C and 90 bar in batch and in continuous operation. Kinetic parameters have been derived from continuous experiments, leading to a catalytic turnover number of 0.95 s⁻¹. The optimum activity is reached at low water concentrations (0.05 g L⁻¹). At lower concentrations, CO₂ is stripping water from the enzyme leading to deactivation. However, adding a small amount of water to the substrates can reverse this deactivation and the enzyme activity is restored.     

Oxygen limitation improves glycerol production by Candida krusei in a bioreactor

An oxygen limitation strategy based on dynamic enzyme activity was applied to improve glycerol accumulation and decrease the residual sugar level in a fermentation of Candida krusei in a bioreactor. By applying oxygen limitation at 88 h when the activities of two glycerol synthetic enzymes cytosolic glycerol-3-phosphate dehydrogenase (ctGPD) and glycerol-3-phosphatase (GPP) were low and the activity of mitochondrial glycerol-3-phosphate dehydrogenase (mtGPD) which catalyzes the glycerol dissimilation was high, the glycerol dissimilation was efficiently reduced. The final glycerol concentration reached 51.8 g l⁻¹ at 96 h and 54.9 g l⁻¹ at 116 h, which was 18 and 60% higher than the control (without oxygen limitation), respectively. The residual sugar was consumed completely while it was 11.2 g l⁻¹ at the end of fermentation in the control. Under oxygen limitation, ethanol production was detected at a final concentration of 3.6 g l⁻¹. This work suggests a metabolic flux shift by oxygen limitation in the bioreactor.     

A perfusion air-lift bioreactor for high density plant cell cultivation and secreted protein production

A new bioreactor design that allows continuous perfusion cultivation of plant cell suspensions is described in this paper. This design incorporates an internal cell settling zone with an external-loop air-lift bioreactor. The settling zone is created by inserting a baffle plate into the upper portion of the downcomer. Using this bioreactor, Anchusa officinalis suspension culture was cultivated to a cell density of 27.2 g l⁻¹ DW in 14 days at a perfusion rate of 0.123 per day. The maximum total extracellular protein concentration attained 1.11 g l⁻¹. Complete cell retention was achieved throughout the culture during which the maximum packed cell volume (PCV) exceeded 80%. In comparison, the maximum cell density and extracellular protein concentration in the batch culture were 12.6 g l⁻¹ DW and 0.47 g l⁻¹, respectively. SDS-PAGE of the extracellular protein samples revealed two major bands at 58 and 47 kDa, each accounted for approximately 45% of the total secreted proteins.     

Enzymatic Synthesis of Ethyl-glucoside Monooleate with Lipase in Solvent-free Medium

Ethylglucoside monooleate was synthesized by esterification between ethylglucoside and oleic acid with immobilized lipase from Candida antarctica in a solvent-free system. It was shown that a stirred tank reactor was suitable for the enzymatic reaction process involving substrates with low miscibility, in which the biocatalyst was recycled five times without significant activity loss. Removal of the co-product, water, from the reaction medium by carrying out the reaction under reduced pressure benefited the esterification reaction and increased the monooleate yield up to 97% within 8 hours.     

Acylation of natural flavonoids using lipase of candida antarctica as biocatalyst

Several flavonoids (quercetin, hesperidin, rutin and esculin) were acylated with fatty acids using an immobilised lipase from Candida antarctica in 2-methyl-2-butanol at 60 °C. It appears that esculin with primary OH on the sugar part is the most reactive substrate. With palmitic acid as acyl donor, the conversion yields were of about 80, 71 and 38%, respectively, for esculin, rutin and hesperidin. No reaction was observed with aglycon flavonoid (quercetin). For a given flavonoid (rutin), the conversion yield increased from 42 to 76% when the carbon number of the fatty acids rose from C6 to C12. For fatty acids with higher carbon-chain length, both conversion yield and initial rate dropped slightly. Furthermore, compared to the saturated fatty acid (C18: 0), the unsaturated one (C18: 1) exhibited a lower reactivity. For all molecules studied ¹H nuclear magnetic resonance (NMR) and ¹³C NMR analyses indicated that only flavonoid monoester was produced.     

Batch and continuous fermentation of succinic acid from wood hydrolysate by Mannheimia succiniciproducens MBEL55E

Batch and continuous cultures of Mannheimia succiniciproducens MBEL55E were carried out in a complex medium containing a NaOH-treated wood hydrolysate for the production of succinic acid. The wood hydrolysate based medium was treated with NaOH before sterilization to reduce the formation of inhibitory compounds. M. succiniciproducens MBEL55E utilized xylose as well as glucose in the wood hydrolysate based medium as a carbon source for the succinic acid production. In batch cultures, the final succinic acid concentration of 11.73 g l⁻¹ was obtained from the pre-treated wood hydrolysate based medium, resulting in a succinic acid yield of 56% and a succinic acid productivity of 1.17 g l⁻¹ h⁻¹, while the corresponding continuous cultures gave the succinic acid yield and productivity of 55% and 3.19 g l⁻¹ h⁻¹, respectively. These results suggest that succinic acid can be produced economically and efficiently by the fermentation of M. succiniciproducens MBEL55E from an inexpensive biomass-based wood hydrolysate.     

Production of eicosapentaenoic acid by Nannochloropsis sp. cultures in outdoor tubular photobioreactors

Autotrophic microalgae cultures have been proposed as an alternative source of EPA, a nutritionally important polyunsaturated fatty acid that plays a key role in the prevention and treatment of several human diseases and disorders. The technology currently available is however, considered commercially not viable because of the low degree of control of algae cultures in outdoor open ponds. The use of closed reactors could overcome these limitations and bring EPA production by microalgae closer to becoming a reality. In this study, we have demonstrated the feasibility of outdoor cultivation of Nannochloropsis sp. in tubular reactors and the potential of this eustigmatophyte as an alternative source of EPA. Nannochloropsis sp. was cultivated in NHTRs of different sizes (from 10.2 to 610 l) from spring to autumn under the climatic conditions of central Italy. EPA productivity essentially reflected the productivity of the culture and reached its maximum in May–June (mean monthly value: 32 mg l⁻¹ day⁻¹). Although the fatty acid composition of the biomass varied significantly during the cultivation period, EPA content remained rather stable around the value of 4% of dry biomass. The transfer of the cultures from laboratory to outdoor conditions, the exposure to natural light–dark cycles, along with lowering the salt concentration from 33 g l⁻¹ (seawater salinity value) to 20 g l⁻¹, factors that caused lasting modifications in the fatty acid content and composition of Nannochloropsis sp., did not significantly affect the EPA content of the biomass.     

Simultaneous production of anthocyanin and triterpenoids in suspension cultures of Perilla frutescens

When cultivated in Murashige & Skoog medium supplemented with 0.2 mg l⁻¹ 2,4-dichlorophenoxy acetic acid and 0.5 mg l⁻¹ 6-benzyladenine, Perilla frutescens cells in suspension culture grew rapidly reaching about 13.6 g dry wt l⁻¹ after 12 days. The cell line produced both anthocyanin 0.9 g l⁻¹ and triterpenoids: 16 mg l⁻¹ oleanolic acid (OA), 25 mg l⁻¹ ursolic acid (UA) and 14 mg l⁻¹ tormentic acid (TA). When P. frutescens cells of 7-day-old cultures were exposed to a yeast elicitor at 0.5–5% (v/v) for 7 days, it was found that anthocyanin content peaked at 10.2% of dry weight with yeast elicitor at 1% (v/v) whereas the maximum production of oleanolic acid and ursolic acid in cultures treated with 2% (v/v) yeast elicitor was 19 and 27 mg l⁻¹, a 46 and 24% increase over the control, respectively. This is the first report of simultaneous production of both anthocyanin and triterpenoids in a single culture system.     

Effect of agitation speed on the synthesis of Mucor miehei acid protease

Different experiments using Mucor miehei CBS 370.65 were carried out to study the effect of agitation speed on the production of the mold acid protease. The experiments were conducted in shake flasks at a fixed substrate concentration of 58 g l⁻¹ of total carbohydrates and at shaker speeds from 80 to 380 rev min⁻¹. Enzyme production was found to be directly proportional to the shaker speeds, with the highest concentration of enzyme of 1,400 Soxhlet Rennet units (SU) ml⁻¹ obtained at 380 rev min⁻¹. The yield of product to substrate at 380 rev min⁻¹ was determined to be 27,081.0 SU g⁻¹ substrate and the productivity of the process was 221 SU g⁻¹ h⁻¹. Enzyme production was partially growth associated, and glucose supported both cell growth and enzyme production. Product formation and cell concentration were directly related to the rate of substrate consumption. The rate of product formation decreased when product started to accumulate, suggesting that the process was affected by feedback repression.