The effect of gas double-dynamic on mass distribution in solid-state fermentation

The mass distribution regularity in substrate of solid-state fermentation (SSF) has rarely been reported due to the heterogeneity of solid medium and the lack of suitable instrument and method, which limited the comprehensive analysis and enhancement of the SSF performance. In this work, the distributions of water, biomass, and fermentation product in different medium depths of SSF were determined using near-infrared spectroscopy (NIRS) and the developed models. Based on the mass distribution regularity, the effects of gas double-dynamic on heat transfer, microbial growth and metabolism, and product distribution gradient were systematically investigated. Results indicated that the maximum temperature of substrate and the maximum carbon dioxide evolution rate (CER) were 39.5 °C and 2.48 mg/(h g) under static aeration solid-state fermentation (SASSF) and 33.9 °C and 5.38 mg/(h g) under gas double-dynamic solid-state fermentation (GDSSF), respectively, with the environmental temperature for fermentation of 30 ± 1 °C. The fermentation production (cellulase activity) ratios of the upper, middle, and lower levels were 1:0.90:0.78 at seventh day under SASSF and 1:0.95:0.89 at fifth day under GDSSF. Therefore, combined with NIRS analysis, gas double-dynamic could effectively strengthen the solid-state fermentation performance due to the enhancement of heat transfer, the stimulation of microbial metabolism and the increase of the homogeneity of fermentation products.     

Nutrient control for stationary phase cellulase production in Trichoderma reesei Rut C-30

This work describes the use of nutrient limitations with Trichoderma reesei Rut C-30 to obtain a prolonged stationary phase cellulase production. This period of non-growth may allow for dependable cellulase production, extended fermentation periods, and the possibility to use pellet morphology for easy product separation. Phosphorus limitation was successful in halting growth and had a corresponding specific cellulase production of 5 ± 2 FPU/g-h. Combined with the addition of Triton X-100 for fungal pellet formation and low shear conditions, a stationary phase cellulase production period in excess of 300 h was achieved, with a constant enzyme production rate of 7 ± 1 FPU/g-h. While nitrogen limitation was also effective as a growth limiter, it, however, also prevented cellulase production.     

Effects of intermittent mechanical mixing on solid-state fermentation of wet corn distillers grain with Trichoderma reesei

The influence of mixing on microorganism integrity and product formation is a critical design parameter for solid-state fermentation bioreactors. The effects of intermittent mechanical mixing on the solid-state fermentation of wet corn distillers grain with Trichoderma reesei NRRL 11460 for the production of cellulase were investigated. Experiments were conducted using the unbuffered media at mixing frequencies of 0, 1, 2, 3, and 6 d⁻¹ at 27.5 °C with an initial moisture content of 50%. The results indicate that mixing caused about a tenfold increase in spore production compared to fermentations at static conditions. The cellulase enzyme activity produced was minimally affected by mixing with only a 5–10% decrease in filter paper activity for mechanically mixed fermentations compared to static fermentations. Mixing at lower frequencies of 1, 2, and 3 d⁻¹ caused an increase in CO₂ evolution compared to static conditions and higher mixing frequencies of 6 d⁻¹. A correlation between substrate weight loss and cumulative CO₂ evolution was established. The ability to intermittently mix a solid-state fermentation bioreactor with minimal detrimental effects increases the feasibility of onsite production of enzymes at biofuel facilities to lower the overall production costs of cellulosic biofuels.     

Production of endoxylanase with enhanced thermostability by a novel polyextremophilic Bacillus halodurans TSEV1 and its applicability in waste paper deinking

The screening and selection of the culture variables followed by optimization using statistical approaches led to a 23-fold enhancement in thermo-alkali-stable xylanase production by the polyextremophilic Bacillus halodurans TSEV1. The optimization of crucial parameters involved in the extraction of xylanase from the bacterial bran led to a high enzyme recovery. The purified xylanase produced in submerged fermentation (SmF) and solid state fermentation (SSF) was visualized as a single band on SDS-PAGE with a molecular mass of 40 kDa. The SSF-xylanase is optimally active at 78 °C and pH 9.0 and stable in the pH range between 7.0 and 12.0 with a T_1/2 of 65 min at 90 °C, which is higher than that of SmF-xylanase. The higher activation energy, enthalpy of deactivation (ΔH*), free energy change of deactivation (ΔG*) and T_1/2 of SSF-xylanase than these of SmF xylanase further confirmed higher thermostability of the former than the latter. The combination of commercial cellulase and TSEV1 xylanase was highly effective in deinking of waste paper at alkaline pH and elevated temperatures.     

Purification and characterization of cellulase from a marine Bacillus sp. H1666: A potential agent for single step saccharification of seaweed biomass

In this study, 115 marine bacterial isolates were screened for cellulase enzymatic activity and enzyme with a molecular mass of 40 kDa was purified from culture supernatant of the marine bacterium Bacillus sp. H1666 using ion exchange and size exclusion chromatography method. Growth of bacterial strain H1666 with efficient cellulase enzyme production was observed on untreated wheat straw and rice bran. The biochemical properties of the extracted cellulase were studied and enzyme was found active over a range of pH 3–9. The optimum cellulase activity was observed at pH 7 and temperature 50 °C. The enzyme was also shown to be slightly thermo-stable with 40% residual activity at 60 °C for 4 h. The potential applicability of enzyme was tested on dried green seaweed (Ulva lactuca) and 450 mg/g increase in glucose yield was obtained after saccharification. MALDI TOF–TOF analysis of cellulase peptide fingerprint showed similarity to the sequence of the glycoside hydrolase family protein.     

A novel membrane-surface liquid co-culture to improve the production of laccase from Ganoderma lucidum

In this work, a laccase producer, Ganoderma lucidum, was separated and identified according to its morphological characteristics and phylogenetic data. A 4000 U/l and 8500 U/l of laccase activity was obtained in 500 ml flask by submerged culture and biomembrane-surface liquid culture (BSLC), respectively. Furthermore, the novel biomembrane-surface liquid co-culture (BSLCc) was developed by adding Saccharomyces cerevisiae to reactor in order to shorten the fermentation period and improve laccase production. Laccase activity obtained by BSLCc, 23 000 U/l, is 5.8 and 2.7 times of that obtained by submerged culture and BSLC, respectively. In addition, laccase production by BSLCc was successfully scaled-up to 100 l reactor, and 38 000 U/l of laccase activity was obtained on day 8. The mechanism of overproducing laccase by BSLCc was investigated by metabolism pathway analysis of glucose. The results show glucose limitation in fermentation broth induces the secretion of laccase. The addition of S. cerevisiae, on one hand, leads to an earlier occurrence of glucose limitation state, and thus shortens the fermentation time; on the other hand, it also results in the appearance of a series of metabolites of the yeast including organic acids, ethanol, glycerol and so forth in fermentation broth, and both polyacrylamide gel electrophoresis analysis and enzyme activity detection of laccase show that these metabolites contribute to the improvement of laccase activity.     

An industrial level system with nonisothermal simultaneous solid state saccharification,fermentation and separation for ethanol production

To alleviate the problems of low substrate loading, nonisothermal, end-product inhibition of ethanol during the simultaneous saccharification and fermentation, a nonisothermal simultaneous solid state saccharification, fermentation, and separation (NSSSFS) process was investigated; one novel pilot scale nonisothermal simultaneous solid state enzymatic saccharification and fermentation coupled with CO₂ gas stripping loop system was invented and tested. The optimal pretreatment condition of steam-explosion was 1.5 MPa for 5 min in industrial level. In the NSSSFS, enzymatic saccharification and fermentation proceeded at around 50 °C and 37 °C, respectively, and were coupled together by the hydrolyzate loop; glucose from enzymatic saccharification was timely consumed by yeast, and the formed ethanol was separated online by CO₂ gas stripping coupled with adsorption of activated carbon; the solids substrate loading reached 25%; ethanol yields from 18.96% to 30.29% were obtained in fermentation depending on the materials tested. Based on the pilot level of 300 L fermenter, a novel industrial-level of 110 m³ solid state enzymatic saccharification, fermentation and ethanol separation plant had been successfully established and operated. The NSSSFS was a novel and feasible engineering solution to the inherent problems of simultaneous saccharification and fermentation, which would be used in large scale and in industrial production of ethanol.     

Cyanobacterial biomass as N-supplement to agro-waste for hyper-production of laccase from Pleurotus ostreatus in solid state fermentation

The potential application of dry biomass of a cyanobacterium Anacystis nidulans as a supplement in SSF for the production of laccase from Pleurotus ostreatus was evaluated. Experiments were carried out in solid culture using groundnut shell as a basic substrate supplemented with four independent nitrogen sources (ammonium sulphate, urea, yeast extract and dry powder of cyanobacteria). All the four supplements enhanced the enzyme yield, and yeast extract showed precedence over inorganic nitrogenous sources. However, when dry biomass of A. nidulans was used as an additive to groundnut shell (agricultural residues), it supported maximum cell growth (56.83 ± 5.56 mg/g dry substrate) and laccase production (49.21 ± 4.89 U/g dry substrate). Addition of 1 mM copper salt in the medium containing groundnut shell supplemented with yeast extract gave laccase activity of 32.64 ± 3.4 U/g dry substrate. When dry powder of cyanobacterial biomass was used as N-supplement, laccase production enhanced to 65.42 ± 6.48 U/g dry substrate. In addition to the enhancement to enzyme production inhibitory effects of high concentrations of copper was also diminished in the medium having dry cyanobacterial biomass. This study, forms the first report on the potential application of cyanobacterial biomass as an additive for production of laccase by Pleurotus ostraetus MTCC 1804 in solid state fermentation and has relevance in scale-up production of this fungal enzyme of commercial significance.     

Enhanced antioxidant and antitumor activities of Antrodia cinnamomea cultured with cereal substrates in solid state fermentation

Growing exclusively on stout camphor trees in Taiwan, Antrodia cinnamomea is known for its extraordinary antioxidant and antitumor activities. As an alternative to the limited supply of natural source, cultured A. cinnamomea from solid state or submerged liquid fermentation still offers many of its medicinal effects. To further enhance the production of functional compounds and corresponding activities, oat, wheat, buckwheat and pearl barley were used as substrates for solid state fermentation of A. cinnamomea in this study. Among these cereal-based culturing, the methanol extract of A. cinnamomea mycelia grown on oats showed stronger overall antioxidant properties. EC₅₀ for the antioxidant activity (conjugated diene method), the DPPH radicals scavenging ability and reducing power were estimated to be around 0.57 mg/mL, 1.07 mg/mL and 0.31 mg/mL, respectively. Incubating cultured cells with 150 ppm of the oat-cultured mycelial extract for 24 h greatly reduced the viability of MCF-7 breast cancer cells and HepG2 hepatocellular carcinoma cells to 29% and 76%, while 3T3 normal fibroblasts were virtually unaffected. In general, cereal-based solid state fermentation of A. cinnamomea produced more of the secondary metabolites and their methanolic extracts showed stronger antioxidant and anti-tumor activities than extracts obtained from liquid fermentation at the same concentration.     

Enhanced cellulase production of the Trichoderma viride mutated by microwave and ultraviolet

Cellulase-producing fungi Trichoderma viride were cultured and fermented on the solid-state wheat bran fermentation medium. The characteristics of its carboxymethyl cellulase (CMCase) in the condition of this solid-state fermentation were evaluated, and the optimum culture time, optimum pH and optimum temperature for CMCase activity of T. viride fermented in this solid state were 60 h, 5.0 and 50 °C, respectively. Carboxymethyl cellulose sodium (CMC-Na) and Congo red were used to screen the strains that had stronger ability to produce enzymes. After the compound mutagenesis by microwave and ultraviolet, seven mutant strains (M-B1–M-B7) were selected and their CMCase activities were assayed. Five of them (M-B1, M-B2, M-B3, M-B5 and M-B7) had significantly stronger ability to produce enzymes than the normal wild type, and they were also very stable for a long period up to 9 generations to produce cellulase. Molecular studies showed that there were some base mutations in endoglucanase I (EG I) genes of mutants M-B1, M-B2, M-B3 and M-B5, but no change in M-B7, suggesting that some amino mutations in EG I proteins caused by base mutations could lead to enhanced cellulase production.     

Enzymatic hydrolysis of corncob and ethanol production from cellulosic hydrolysate

 Enzymatic hydrolysis of corncob and ethanol fermentation from cellulosic hydrolysate were investigated. After corncob was pretreated by 1% H₂SO₄ at 108 °C for 3 h, the cellulosic residue was hydrolyzed by cellulase from Trichoderma reesei ZU-02 and the hydrolysis yield was 67.5%. Poor cellobiase activity in T. reesei cellulase restricted the conversion of cellobiose to glucose, and the accumulation of cellobiose caused severe feedback inhibition to the activities of β-1,4-endoglucanase and β-1,4-exoglucanase in cellulase system. Supplementing cellobiase from Aspergillus niger ZU-07 greatly reduced the inhibitory effect caused by cellobiose, and the hydrolysis yield was improved to 83.9% with enhanced cellobiase activity of 6.5 CBU g⁻¹ substrate. Fed-batch hydrolysis process was started with a batch hydrolysis containing 100 g l⁻¹ substrate, with cellulosic residue added at 6 and 12 h twice to get a final substrate concentration of 200 g l⁻¹. After 60 h of reaction, the reducing sugar concentration reached 116.3 g l⁻¹ with a hydrolysis yield of 79.5%. Further fermentation of cellulosic hydrolysate containing 95.3 g l⁻¹ glucose was performed using Saccharomyces cerevisiae 316, and 45.7 g l⁻¹ ethanol was obtained within 18 h. The research results are meaningful in fuel ethanol production from agricultural residue instead of grain starch.     

Characterization of a recombinant thermostable β-glucosidase from Putranjiva roxburghii expressed in Saccharomyces cerevisiae and its use for efficient biomass conversion

A β-glucosidase gene from Putranjiva roxburghii (PRGH1) was heterologously expressed in Saccharomyces cerevisiae to enable growth on cellobiose. The recombinant enzyme was secreted to the culture medium, purified and biochemically characterized. The enzyme is a glycoprotein with a molecular weight of ∼68 kDa and exhibited enzymatic activity with β‐linked aryl substrates like pNP-Fuc, pNP-Glc, pNP-Gal and pNP-Cel with catalytic efficiency in that order. Significant enzyme activity was observed for cellobiose, however the enzyme activity was decreased with increase in chain length of glycan substrates. Using cellobiose as substrate, the enzyme showed optimal activity at pH 5.0 and 65 °C. The enzyme was thermostable up to 75 °C for 60 min. The enzyme showed significant resistance towards both glucose and ethanol induced inhibition. The recombinant S. cerevisiae strain showed advantages in cell growth, glucose and bio-ethanol production over the native strain with cellobiose as sole carbon source. In simultaneous saccharification and fermentation (SSF) experiments, the recombinant strain was used for bio-ethanol production from two different cellulosic biomass sources. At the end of the SSF, we obtained 9.47 g L⁻¹ and 14.32 g L⁻¹ of bio-ethanol by using carboxymethyl cellulose and pre-treated rice straw respectively. This is first report where a β-glucosidase gene from plant origin has been expressed in S. cerevisiae and used in SSF.     

Liquid state fermentation of apple pomace sludge for the production of ligninolytic enzymes and liberation of polyphenolic compounds

Ligninolytic enzyme production and polyphenolic compound extraction by liquid-state culture of Phanerochaete chrysosporium ATCC 24275 was investigated by employing apple pomace sludge and synthetic medium. Different physico-chemical and biological parameters namely viscosity, zeta potential and particle size, viability and enzyme production were investigated. The ligninolytic enzyme production was higher in apple pomace sludge (45 U/l of laccase, 220 U/l of MnP and 6.5 U/l of LiP) than in synthetic medium (17 U/l of laccase, 37 U/l of MnP and 6 U/l). These maximal activities were found during the stationary and decline phase. It was also found that enzyme production was strongly correlated with P. chrysoporium viability in both synthetic medium and apple pomace sludge. Moreover, physico-chemical parameters, such as particle size, zeta potential and viscosity were strongly correlated to the viability of P. chrysosporium and to the ligninolytic enzyme production. An increase in polyphenol content extracted by acetone (383–720 mg GAE/l) was observed during fermentation of apple pomace and it was found that the polyphenol content extracted by ethanol increased ～1.5 fold until 67 h of fermentation and later it decreased. It was found that antioxidant activity increased to 35% and eventually decreased based on the change in the polyphenol content.     

Purification and characterisation of a xylanase from Thermomyces lanuginosus and its functional expression by Pichia pastoris

A xylanase produced by Thermomyces lanuginosus 195 by solid state fermentation (SSF) was purified 9.3-fold from a crude koji extract, with a 7.6% final yield. The purified xylanase (with an estimated mass of 22 kDa by SDS-PAGE) retained 18% relative activity when treated for 10 min at 100 °C and approximately 90% relative activity when incubated at pH values ranging from 6 to 10. Xylanase activity in the purified preparation was significantly enhanced following treatment with manganese and potassium chlorides (p < 0.05) but significantly reduced by calcium, cobalt and iron (p < 0.05). The purified enzyme was also shown to be exclusively xylanolytic. The gene encoding xylanase activity from T. lanuginosus 195 was functionally expressed by Pichia pastoris. MALDI-ToF mass spectrometry and zymography were employed to confirm functional recombinant expression. Maximum xylanase titres were achieved following 120 h induction of the recombinant culture, yielding 26.8 U/mL. Achieving functional protein expression facilitates future efforts to optimise the cultivation conditions for heterologous xylanase production.     

Simultaneous saccharification and fermentation of kraft pulp by recombinant Escherichia coli for phenyllactic acid production

Simultaneous saccharification and fermentation (SSF) of renewable cellulose for the production of 3-phenyllactic acid (PhLA) by recombinant Escherichia coli was investigated. Kraft pulp recovered from biomass fractionation processes was used as a model cellulosic feedstock and was hydrolyzed using 10–50 filter paper unit (FPU) g⁻¹ kraft pulp of a commercial cellulase mixture, which increased the glucose yield from 21% to 72% in an enzyme dose-dependent manner. PhLA fermentation of the hydrolyzed kraft pulp by a recombinant E. coli strain expressing phenylpyruvate reductase from Wickerhamia fluorescens TK1 produced 1.9 mM PhLA. The PhLA yield obtained using separate hydrolysis and fermentation was enhanced from 5.8% to 42% by process integration into SSF of kraft pulp (20 g L⁻¹) in a complex medium (pH 7.0) at 37 °C. The PhLA yield was negatively correlated with the initial glucose concentration, with a five-fold higher PhLA yield observed in culture medium containing 10 g L⁻¹ glucose compared to 100 g L⁻¹. Taken together, these results suggest that the PhLA yield from cellulose in kraft pulp can be improved by SSF under glucose-limited conditions.     

Potential use of nylon scouring pad cubes attachment method for pectinase production by Aspergillus niger HFD5A-1

This study investigated the novel use of scouring pad cubes as a support matrix for immobilization of fungal cell to enhance the pectinase production. Nylon scouring pad cubes were used for immobilized Aspergillus niger HFD5A-1 cells for pectinase production in flask submerge fermentation system. The enzyme activity of immobilized cell in scouring pad cubes gave higher activity compared to free cells. Various physical parameters for culture condition were studied to evaluate its effects on pectinase production. The maximum enzyme activity obtained was 11.05 U/mL on the 6th day of cultivation after using the optimized parameters of 6 scouring pad cubes, 1 × 10⁷ spores/mL of inoculum size, agitation speed of 150 rpm and incubated at 30 °C. The use of nylon scouring pad cubes gave an increment of about 335.0% of pectinase production (11.05 U/mL) compared to free cells (2.54 U/mL). The results therefore show scouring pad cubes could be a favorable carrier to immobilize the fungal cells for higher enzyme production in submerged fermentation.     

Utilization of agro-industrial waste for xylanase production by Aspergillus foetidus MTCC 4898 under solid state fermentation and its application in saccharification

Xylanase production by Aspergillus foetidus MTCC 4898 was carried out under solid state fermentation using wheat bran and anaerobically treated distillery spent wash. Response surface methodology involving Box–Behnken design was employed for optimizing xylanase production. The interactions among various fermentation parameters viz. moisture to substrate ratio, inoculum size, initial pH, effluent concentration and incubation time were investigated and modeled. The predicted xylanase activity under optimized parameters was 8200–8400 U/g and validated xylanase activity was 8450 U/g with very poor cellulase activity. Crude xylanase was used for enzymatic saccharification of agroresidues like wheat straw, rice straw and corncobs. Dilute NaOH and ammonia pretreatments were found to be beneficial for the efficient enzymatic hydrolysis of all the three substrates. Dilute NaOH pretreated wheat straw, rice straw and corncobs yielded 4, 4.2, 4.6 g/l reducing sugars, respectively whereas ammonia treated wheat straw, rice straw and corncobs yielded 4.9, 4.7, 4.6 g/l reducing sugars, respectively. The hydrolyzates were analysed by HPTLC. Xylose was found to be the major end product with traces of glucose in the enzymatic hydrolyzates of all the substrates.     

Conversion of cassava flour to fuel ethanol by sequential solid state and submerged cultures

A process for conversion of cassava flour to ethanol was developed. This involved direct inoculation of Aspergillus awamori spores into a cassava flour paste and incubation for some period during which hydrolytic enzymes are produced (solid state culture or koji production) and subsequent addition of water and yeast cells, during which there is simultaneous hydrolysis and ethanol production (submerged culture). When cassava flour alone was used for the solid state phase, the paste was very sticky, making mixing and aeration difficult. However, addition of rice bran improved the texture and enzyme production. The optima rice bran concentration, spore inoculum concentration, and duration of solid state culture before submerged culture were 20%, 6.16 × 10⁶ spores/100 g, and 2 days, respectively. Under these optimum conditions, a high ethanol concentration of 120 g/L and ethanol yield of 0.309 g-ethanol/g-cassava flour were obtained. This ethanol yield corresponds to 0.44 g-ethanol/g-cassava starch.     

Effects of exogenous enzymes on in vitro gas production kinetics and ruminal fermentation of four fibrous feeds

This study was conducted to investigate effects of increasing doses: 0 (control), 6 (low), 12 (medium) and 24 (high) mg/g DM of ZADO^® enzyme preparation mixture (ENZ) on in vitro gas production (GP) and some ruminal fermentation parameters of the fibrous feeds Saccharum officinarum (leaves), Andropogon gayanus (leaves), Pennisetum purpureum (leaves) and Sorghum vulgare (straw). Rumen liquor was obtained from two Brown Swiss cows fitted with permanent rumen cannulae fed a total mixed ration of a 500:500 commercial concentrate and alfalfa hay ad libitum. The GP was recorded at 2, 4, 6, 8, 10, 12, 24, 48, 72 and 96 h of incubation. After 96 h, the incubation was stopped and the pH of the mixture was determined and filtrate used to determine dry matter degradability (DMD), partitioning factor (PF₉₆), gas yield (GY₂₄), in vitro organic matter digestibility (OMD), metabolizable energy (ME), short chain fatty acids (SCFA), and microbial crude protien production (MCP). In general, the crude protein (CP) content of the fibrous feeds was low and ranged from 23 g/kg DM (S. officinarum) to 44 (A. gayanus). The fibre contents (i.e., NDFom and ADFom) were highest (P<0.05) in S. officinarum. Increasing ENZ dose linearly increased (P<0.05) GP of all fibrous feeds and had a quadratically increased (P<0.05) asymptotic gas production in P. purpureum and S. vulgare and rate of gas production in S. officinarum and S. vulgare. Addition of ENZ also quadratically increased (P<0.05) GP at all incubation times in S. officinarum and S. vulgare, and A. gayanus, but only at 72 h in A. gayanus. The parameters of ruminal fermentation of OMD, ME, GY₂₄ and SCFA linearly increased (P<0.05) and MCP linearly decreased (P<0.05) with the ENZ addition. Addition of enzyme affected ruminal fermentation of our feeds differently, mainly dependent on their fibre content, although dosage of enzyme was also important as impacts generally increased at higher dosages of ENZ.     

Lipolytic enzyme production by Thermus thermophilus HB27 in a stirred tank bioreactor

In this study, lipolytic enzyme production by Thermus thermophilus HB27 at bioreactor scale has been investigated. Cultivation was performed in a 5-L stirred tank bioreactor in discontinuous mode, at an agitation speed of 200 rpm. Different variables affecting intra- and extra-cellular lipolytic enzyme production such as culture temperature and aeration rate have been analysed. The bacterium was able to grow within the temperature range tested (from 60 to 70 °C) with an optimum value of 70 °C for intra- and extra-cellular lipolytic enzyme production.On the other hand, various aeration levels (from 0 to 2.5 L/min) were employed. A continuous supply of air was necessary, but no significant improvement in biomass or enzyme production was detected when air flow rates were increased above 1 L/min. Total lipolytic enzyme production reached a maximum of 167 U/L after 3 days, and a relatively high concentration of extra-cellular activity was detected (40% of the total amount). Enzyme yield was around 158 U/g cells. Moreover, it is noteworthy that the lipolytic activity obtained operating at optimal conditions (70 °C and air flow of 1 L/min) was about five-fold higher than that attained in shake flask cultures