Comparative profiles of α-amylase production in conventional tray reactor and GROWTEK bioreactor

GROWTEK bioreactor was used as modified solid-state fermentor to circumvent many of the problems associated with the conventional tray reactors for solid-state fermentation (SSF). Aspergillus oryzae IFO-30103 produced very high levels of α-amylase by modified solid-state fermentation (mSSF) compared to SSF carried out in enamel coated metallic trays utilizing wheat bran as substrate. High α-amylase yield of 15,833 U g⁻¹ dry solid in mSSF were obtained when the fungus were cultivated at an initial pH of 6.0 at 32°C for 54 h whereas α-amylase production in SSF reached its maxima (12,899 U g⁻¹ dry solid ) at 30°C after 66 h of incubation. With the supplementation of 1% NaNO₃, the maximum activity obtained was 19,665 U g⁻¹ dry solid (24% higher than control) in mSSF, whereas, in SSF maximum activity was 15,480 U g⁻¹ dry solid in presence of 0.1% Triton X-100 (20% higher than the control).     

Thermophilic protease production by Streptomyces sp. 594 in submerged and solid-state fermentations using feather meal

AIMS: Protease production by Streptomyces sp. 594 in submerged (SF) and solid-state fermentation (SSF) using feather meal, an industrial poultry residue, and partial characterization of the crude enzyme. METHODS AND RESULTS: Streptomyces sp. 594 produced proteases in SF (7.2 +/- 0.2 U ml(-1)) and SSF (15.5 +/- 0.41 U g(-1)), with pH increase in both media. Considering protease activity, values obtained in the liquid extract after SSF (6.3 +/- 0.17 U ml(-1)) were lower than those from SF. The proteases, which belong to serine and metalloproteinase classes, were active over a wide range of pH (5.0-10.0) and high temperatures (55-80 degrees C). Strain 594 was also able to degrade feather in agar and liquid media. Keratinase activity (80 U l(-1)) also confirmed the keratin degrading capacity of this streptomycete. CONCLUSIONS: Proteases produced using residues from poultry industry have shown interesting properties for industrial purposes. SIGNIFICANCE AND IMPACT OF THE STUDY: As far as we are concerned, this is the first contribution towards the production of thermophilic protease by a streptomycete in SSF using a keratinous waste.     

Production and optimization of thermophilic alkaline protease in solid-state fermentation by <Emphasis Type="Italic">Streptomyces</Emphasis> sp. CN902

The purpose of the present research is to study the production of thermophilic alkaline protease by a local isolate, Streptomyces sp. CN902, under solid state fermentation (SSF). Optimum SSF parameters for enzyme production have been determined. Various locally available agro-industrial residues have been screened individually or as mixtures for alkaline protease production in SSF. The combination of wheat bran (WB) with chopped date stones (CDS) (5:5) proved to be an efficient mixture for protease production as it gave the highest enzyme activity (90.50 U g⁻¹) when compared to individual WB (74.50 U g⁻¹) or CDS (69.50 U g⁻¹) substrates. This mixed solid substrate was used for the production of protease from Streptomyces sp. CN902 under SSF. Maximal protease production (220.50 U g⁻¹) was obtained with an initial moisture content of 60%, an inoculum level of 1 × 10⁸ (spore g⁻¹ substrate) when incubated at 45°C for 5 days. Supplementation of WB and CDS mixtures with yeast extract as a nitrogen source further increased protease production to 245.50 U g⁻¹ under SSF. Our data demonstrated the usefulness of solid-state fermentation in the production of alkaline protease using WB and CDS mixtures as substrate. Moreover, this approach offered significant benefits due to abundant agro-industrial substrate availability and cheaper cost.     

Production of a novel raw-starch-digesting glucoamylase by <Emphasis Type="Italic">Penicillium</Emphasis> sp. X-1 under solid state fermentation and its use in direct hydrolysis of raw starch

Penicillium sp. X−1, isolated from decayed raw corn, produced high level of raw-starch-digesting glucoamylase (RSDG) under solid state fermentation (SSF). Maximum enzyme yield of 306.2 U g⁻¹ dry mouldy bran (DMB) was obtained after 36 h of culture upon optimized production. The enzyme could hydrolyse both small and large granule starches but did not adsorb on raw starch. The enzyme exhibited maximum activity at 65°C and pH 6.5, which provided an opportunity of synergism with α-amylase. It significantly hydrolysed 15% (w/v) raw corn starch slurry in synergism with the commercial α-amylase and a degree of hydrolysis of 92.4% was obtained after 2 h of incubation.     

Enzymatic resolution of racemic phenyloxirane by a novel epoxide hydrolase from Aspergillus niger SQ-6 and its fed-batch fermentation

A microorganism with the ability to catalyze the resolution of racemic phenyloxirane was isolated and identified as Aspergillus niger SQ-6. Chiral capillary electrophoresis was successfully applied to separate both phenyloxirane and phenylethanediol. The epoxide hydrolase (EH) involved in this resolution process was (R)-stereospecific and constitutively expressed. When whole cells were used during the biotransformation process, the optimum temperature and pH for stereospecific vicinal diol production were 35°C and 7.0, respectively. After a 24-h conversion, the enantiomer excess of (R)-phenylethanediol produced was found to be >99%, with a conversion rate of 56%. In fed-batch fermentations at 30°C for 44 h, glycerol (20 g L⁻¹) and corn steep liquor (CSL) (30 g L⁻¹) were chosen as the best initial carbon and nitrogen sources, and EH production was markedly improved by pulsed feeding of sucrose (2 g L⁻¹ h⁻¹) and continuous feeding of CSL (1 g L⁻¹ h⁻¹) at a fermentation time of 28 h. After optimization, the maximum dry cell weight achieved was 24.5±0.8 g L⁻¹; maximum EH production was 351.2±13.1 U L⁻¹ with a specific activity of 14.3±0.5 U g⁻¹. Partially purified EH exhibited a temperature optimum at 37°C and pH optimum at 7.5 in 0.1 M phosphate buffer. This study presents the first evidence for the existence of a predicted epoxide racemase, which might be important in the synthesis of epoxide intermediates.     

Production of inulinase by solid-state fermentation: effect of process parameters on production and preliminary characterization of enzyme preparations

This work was aimed at producing inulinase by solid-state fermentation of sugarcane bagasse, using factorial design to identify the effect of corn steep liquor (CSL) and soybean bran concentration, particle size of bagasse and size of inoculum. Maximum inulinase activity achieved was 250 U per g of dry substrate (gds) at 20% (w/w) of CSL, 5% (w/w) of soybean bran, 1 × 10¹⁰ cells mL⁻¹ and particle size of bagasse in the range 9/32 mesh. The use of soybean bran decreased the time to reach maximum activity from 96 to 24 h and the maximum productivity achieved was 8.87 U gds⁻¹ h⁻¹. The maximum activity was obtained at pH 5.0 and 55.0°C. Within the investigated range, the enzyme extract was more thermostable at 50.0°C, showing a D-value of 123.1 h and deactivation energy of 343.9 kJ gmol⁻¹. The extract showed highest stability from pH 4.5 to 4.8. Apparent K _m and V _max are 7.1 mM and 17.79 M min⁻¹, respectively.     

Comparison of SHF and SSF processes for the bioconversion of steam-exploded wheat straw

Two processes for ethanol production from wheat straw have been evaluated — separate hydrolysis and fermentation (SHF) and simultaneous saccharification and fermentation (SSF). The study compares the ethanol yield for biomass subjected to varying steam explosion pretreatment conditions: temperature and time of pretreatment was 200°C or 217°C and at 3 or 10 min. A rinsing procedure with water and NaOH solutions was employed for removing lignin residues and the products of hemicellulose degradation from the biomass, resulting in a final structure that facilitated enzymatic hydrolysis. Biomass loading in the bioreactor ranged from 25 to 100 g l⁻¹ (dry weight). The enzyme-to-biomass mass ratio was 0.06. Ethanol yields close to 81% of theoretical were achieved in the two-step process (SHF) at hydrolysis and fermentation temperatures of 45°C and 37°C, respectively. The broth required addition of nutrients. Sterilisation of the biomass hydrolysate in SHF and of reaction medium in SSF can be avoided as can the use of different buffers in the two stages. The optimum temperature for the single-step process (SSF) was found to be 37°C and ethanol yields close to 68% of theoretical were achieved. The SSF process required a much shorter overall process time (≈30 h) than the SHF process (96 h) and resulted in a large increase in ethanol productivity (0.837 g l⁻¹ h⁻¹ for SSF compared to 0.313 g l⁻¹ h⁻¹ for SHF). Journal of Industrial Microbiology & Biotechnology (2000) 25, 184–192. Received 02 December 1999/ Accepted in revised form 20 July 2000     

Effects of pH and corn steep liquor variability on mannitol production by Lactobacillus intermedius NRRL B-3693

Lactobacillus intermedius NRRL B-3693 produced mannitol, lactic acid, and acetic acid when grown on fructose at 37°C. The optimal pH for mannitol production from fructose by the heterofermentative lactic acid bacterium (LAB) in pH-controlled fermentation was at pH 5.0. It produced 160.7 ± 1.1 g mannitol in 40 h with a volumetric productivity of 4.0 g l⁻¹ h⁻¹ in a simplified medium containing 250 g fructose, 50 g corn steep liquor (CSL), and 33 mg MnSO₄ per liter. However, the mannitol production by the LAB was severely affected by the variability of CSL. The supplementation of CSL with soy peptone (5 g/l), tryptophan (50 mg/l), tryptophan (50 mg/l) plus tyrosine (50 mg/l), or commercial protease preparation (2 ml/100 g of CSL) enhanced the performance of the inferior CSL and thus helped to overcome the nutrient limitations.     

Comparing submerged and solid-state fermentation of agro-industrial residues for the production and characterization of lipase by Trichoderma harzianum

Lipase production by Trichoderma harzianum was evaluated in submerged fermentation (SF) and solid-state fermentation (SSF) using a variety of agro-industrial residues. Cultures in SF showed the highest activity (1.4 U/mL) in medium containing 0.5 % (w/v) yeast extract, 1 % (v/v) olive oil and 2.5 C:N ratio. This paper is the first to report lipase production by T. harzianum in SSF. A 1:2 mixture of castor oil cake and sugarcane bagasse supplemented with 1 % (v/w) olive oil showed the best results among the cultures in SSF (4 U/g ds). Lipolytic activity was stable in a slightly acidic to neutral pH, maintaining 50 % activity after 30 min at 50 °C. Eighty percent of the activity remained after 1 h in 25 % (v/v) methanol, ethanol, isopropanol or acetone. Activity was observed with vegetable oils (olive, soybean, corn and sunflower) and long-chain triacylglycerols (triolein), confirming the presence of a true lipase. The results of this study are promising because they demonstrate an enzyme with interesting properties for application in catalysis produced by fermentation at low cost.     

Production of β-galactosidase from thermophilic fungus Rhizomucor sp

A thermostable β-galactosidase was produced extracellularly by a thermophilic Rhizomucor sp, with maximum enzyme activity (0.21 U mg⁻¹) after 4 days under submerged fermentation condition (SmF). Solid state fermentation (SSF) resulted in a nine-fold increase in enzyme activity (2.04 U mg⁻¹). The temperature range for production of the enzyme was 38–55°C with maximum activity at 45°C. The optimum pH and temperature for the partially purified enzyme was 4.5 and 60°C, respectively. The enzyme retained its original activity on incubation at 60°C up to 1 h. Divalent cations like Co²⁺, Mn²⁺, Fe²⁺ and Zn²⁺ had strong inhibitory effects on the enzyme activity. The K _m and V _max for p-nitrophenyl-β- _D-galactopyranoside and o-nitrophenyl-β - _D-galactopyranoside were 0.39 mM, 0.785 mM and 232.1 mmol min⁻¹ mg⁻¹ respectively. The K _m and V _max for the natural substrate lactose were 66.66 μM and 0.20 μ mol min⁻¹ mg⁻¹. Received 10 March 1997/ Accepted in revised form 17 July 1997     

Optimization of polyhydroxybutyrate production by <Emphasis Type="Italic">Bacillus</Emphasis> sp. CFR 256 with corn steep liquor as a nitrogen source

Polyhydroxyalkanotes (PHAs), the eco-friendly biopolymers produced by many bacteria, are gaining importance in curtailing the environmental pollution by replacing the non-biodegradable plastics derived from petroleum. The present study was carried out to economize the polyhydroxybutyrate (PHB) production by optimizing the fermentation medium using corn steep liquor (CSL), a by-product of starch processing industry, as a cheap nitrogen source, by Bacillus sp. CFR 256. Response surface methodology (RSM) was used to optimize the fermentation medium using the variables such as corn steep liquor (5–25 g l⁻¹), Na₂HPO₄ 2H₂O (2.2–6.2 g l⁻¹), KH₂PO₄ (0.5–2.5 g l⁻¹), sucrose (5–55 g l⁻¹) and inoculum concentration (1–25 ml l⁻¹). Central composite rotatable design (CCRD) experiments were carried out to study the complex interactions of the variables. The optimum conditions for maximum PHB production were (g l⁻¹): CSL-25, Na₂HPO₄ 2H₂O-2.2, KH₂PO₄ − 0.5, sucrose − 55 and inoculum − 10 (ml l⁻¹). After 72 h of fermentation, the amount of PHA produced was 8.20 g l⁻¹ (51.20% of dry cell biomass). It is the first report on optimization of fermentation medium using CSL as a nitrogen source, for PHB production by Bacillus sp.     

Pectinase production by a Brazilian thermophilic fungus <Emphasis Type="Italic">Thermomucor indicae-seudaticae</Emphasis> N31 in solid-state and submerged fermentation

Thermophilic organisms produce thermostable enzymes, which have a number of applications, justifying the interest in the isolation of new thermophilic strains and study of their enzymes. Thirty-four thermophilic and thermotolerant fungal strains were isolated from soil, organic compost, and an industrial waste pile based on their ability to grow at 45°C and in a liquid medium containing pectin as the only carbon source. Among these fungi, 50% were identified at the genus level as Thermomyces, Aspergillus, Monascus, Chaetomium, Neosartoria, Scopulariopsis, and Thermomucor. All isolated strains produced pectinase during solid-state fermentation (SSF). The highest polygalacturonase (PG) activity was obtained in the culture medium of thermophilic strain N31 identified as Thermomucor indicae-seudaticae. Under SSF conditions on media containing a mixture of wheat bran and orange bagasse (1 : 1) at 70% of initial moisture, this fungus produced the maximum of 120 U/ml of exo-PG, while in submerged fermentation (SmF) it produced 13.6 U/ml. The crude PG from SmF was more thermostable than that from SSF and exhibited higher stability in acidic pH.     

Effect of growth substrate,method of fermentation,and nitrogen source on lignocellulose-degrading enzymes production by white-rot basidiomycetes

The exploration of seven physiologically different white rot fungi potential to produce cellulase, xylanase, laccase, and manganese peroxidase (MnP) showed that the enzyme yield and their ratio in enzyme preparations significantly depends on the fungus species, lignocellulosic growth substrate, and cultivation method. The fruit residues were appropriate growth substrates for the production of hydrolytic enzymes and laccase. The highest endoglucanase (111 U ml⁻¹) and xylanase (135 U ml⁻¹) activities were revealed in submerged fermentation (SF) of banana peels by Pycnoporus coccineus. In the same cultivation conditions Cerrena maxima accumulated the highest level of laccase activity (7,620 U l⁻¹). The lignified materials (wheat straw and tree leaves) appeared to be appropriate for the MnP secretion by majority basidiomycetes. With few exceptions, SF favored to hydrolases and laccase production by fungi tested whereas SSF was appropriate for the MnP accumulation. Thus, the Coriolopsis polyzona hydrolases activity increased more than threefold, while laccase yield increased 15-fold when tree leaves were undergone to SF instead SSF. The supplementation of nitrogen to the control medium seemed to have a negative effect on all enzyme production in SSF of wheat straw and tree leaves by Pleurotus ostreatus. In SF peptone and ammonium containing salts significantly increased C. polyzona and Trametes versicolor hydrolases and laccase yields. However, in most cases the supplementation of media with additional nitrogen lowered the fungi specific enzyme activities. Especially strong repression of T. versicolor MnP production was revealed.     

Production,purification, and characterization of acetyl esterase from <Emphasis Type="Italic">Streptomyces</Emphasis> sp. PC22 and its action in cooperation with xylanolytic enzymes on xylan degradation

Acetyl esterase was produced by Streptomyces sp. PC22 at comparable levels of about 0.3 U ml⁻¹ using either 1.0% (w/v) birchwood xylan or 1.5% (w/v) corn husks as a carbon source and cultivating at 45 °C, at pH 9 for 3 or 2 days, respectively. The enzyme was purified from culture filtrate to about 54-fold purity by ammonium sulfate precipitation, followed by consecutive chromatography using a Macro-Prep DEAE, t-butyl hydrophobic interaction and hydroxyapatite, respectively. The approximate molecular weight of the purified enzyme was 155 kDa as analyzed by gel filtration, and it contained four identical 34 kDa subunits, as assessed by SDS-PAGE. It had K _m and V _max values for p-nitrophenyl acetate of 0.43 mM and 70.78 U mg⁻¹ and 7.8 mM and 1,027 U mg⁻¹ for α-naphthyl acetate, respectively. Its optimal pH and temperature were 6.5–7.0 and 50 °C, respectively. It was stable for 30 min at a broad range of pH values, from 5.0 to 9.0, and at temperatures up to 60 °C. The purified enzyme had no other xylanolytic activities. It showed cooperative action on birchwood xylan degradation, when used in combination with xylanase from the same strain and β-xylosidase from Streptomyces sp. CH7. Enhancement was 1.4-fold, compared to the expected amount of individual enzymes alone. This indicates that the enzyme has potential industrial applications, especially for utilizing renewable hemicelluloses containing acetyl xylan for the production of biofuels or other fermentation products.     

Lignocellulose-degrading enzyme production by white-rot <Emphasis Type="Italic">Basidiomycetes</Emphasis> isolated from the forests of Georgia

The production of lignocellulolytic enzymes by eleven basidiomycetes species isolated from two ecosystems of Georgia was investigated for the first time under submerged (SF) and solid-state fermentation (SSF) of lignocellulosic by-products. Notable intergeneric and intrageneric differences were revealed with regard to the extent of hydrolase and oxidase activity. Several fungi produced laccase along with hydrolases in parallel with growth during the trophophase, showing that the synthesis of this enzyme is not connected with secondary metabolism. The lignocellulosic substrate type had the greatest impact on enzyme secretion. Some of the substrates significantly stimulated lignocellulolytic enzyme synthesis without supplementation of the culture medium with specific inducers. Exceptionally high carboxymethyl cellulase (CMCase, 122 U ml⁻¹) and xylanase (195 U ml⁻¹) activities were revealed in SF of mandarin peelings by Pseudotremella gibbosa IBB 22 and of residue after ethanol production (REP) by Fomes fomentarius IBB 38, respectively. The SSF of REP by T. pubescens IBB 11 ensured the highest level of laccase activity (24,690 U l⁻¹), whereas the SSF of wheat bran and SF of mandarin peels provided the highest manganese peroxidase activity (570–620 U l⁻¹) of Trichaptum biforme IBB 117. Moreover, the variation of lignocellulosic growth substrate provides an opportunity to obtain enzyme preparations containing different ratios of individual enzymes.     

Use of response surface methodology for optimizing process parameters for high inulinase production by the marine yeast <Emphasis Type="Italic">Cryptococcus aureus</Emphasis> G7a in solid-state fermentation and hydrolysis of inulin

The optimization of process parameters for high inulinase production by the marine yeast strain Cryptococcus aureus G7a in solid-state fermentation (SSF) was carried out using central composite design (CCD), one of the response surface methodologies (RSMs). We found that moisture, inoculation size, the amount ratio of wheat bran to rice husk, temperature and pH had great influence on inulinase production by strain G7a. Therefore, the CCD was used to evaluate the influence of the five factors on the inulinase production by strain G7a. Then, five levels of the five factors above were further optimized using the CCD. Finally, the optimal parameters obtained with the RSM were the initial moisture 61.5%, inoculum 2.75%, the amount ratio of wheat bran to rice husk 0.42, temperature 29 °C, pH 5.5. Under the optimized conditions, 420.9 U g⁻¹ of dry substrate of inulinase activity was reached in the solid-state fermentation culture of strain G7a within 120 h whereas the predicted maximum inulinase activity of 436.2 U g⁻¹ of inulinase activity of 436.2 U g⁻¹ of dry weight was derived from the RSM regression. This is the highest inulinase activity produced by the yeast strain reported so far. A large amount of monosaccharides and oligosaccharides were detected after inulin hydrolysis by the crude inulinase.     

Dynamics of bacterial communities during solid-state fermentation using agro-industrial wastes to produce poly-γ-glutamic acid,revealed by real-time PCR and denaturing gradient gel electrophoresis (DGGE)

The dynamics of bacterial communities play an important role in solid-state fermentation (SSF). Poly-γ-glutamic acid (γ-PGA) was produced by Bacillus amyloliquefaciens C1 in SSF using dairy manure compost and monosodium glutamate production residuals as basic substrates. The production of γ-PGA reached a maximum of 0.6% after 20 days fermentation. Real-time polymerase chain reaction showed the amount of total bacteria reached 3.95 × 10⁹ 16S rDNA copies/g sample after 30 days, which was in good accordance with the 4.80 × 10⁹ CFU/g obtained by plate counting. Denaturing gradient gel electrophoresis profile showed a reduction of microbial diversity during fermentation, while the inoculum, B. amyloliquefaciens C1, was detected as the dominant organism through the whole process. In the mesophilic phase of SSF, Proteobacteria was the dominant microbial, which was replaced by Firmicutes and Actinobacteria in the thermophilic phase. The molecular analysis of the bacterial diversity has significant potential for instructing the maturing process of SSF to produce γ-PGA at a large-scale level, which could be a benefit in the production of high quality and stable SSF products.     

Cellulase production from agricultural residues by recombinant fusant strain of a fungal endophyte of the marine sponge Latrunculia corticata for production of ethanol

Several fungal endophytes of the Egyptian marine sponge Latrunculia corticata were isolated, including strains Trichoderma sp. Merv6, Penicillium sp. Merv2 and Aspergillus sp. Merv70. These fungi exhibited high cellulase activity using different lignocellulosic substrates in solid state fermentations (SSF). By applying mutagenesis and intergeneric protoplast fusion, we have obtained a recombinant strain (Tahrir-25) that overproduced cellulases (exo-β-1,4-glucanase, endo-β-1,4-glucanase and β-1,4-glucosidase) that facilitated complete cellulolysis of agricultural residues. The process parameters for cellulase production by strain Tahrir-25 were optimized in SSF. The highest cellulase recovery from fermentation slurries was achieved with 0.2% Tween 80 as leaching agent. Enzyme production was optimized under the following conditions: initial moisture content of 60% (v/w), inoculum size of 10⁶ spores ml⁻¹, average substrate particle size of 1.0 mm, mixture of sugarcane bagasse and corncob (2:1) as the carbon source supplemented with carboxymethyl cellulose (CMC) and corn steep solids, fermentation time of 7 days, medium pH of 5.5 at 30°C. These optimized conditions yielded 450, 191, and 225 units/gram dry substrate (U gds⁻¹) of carboxylmethyl cellulase, filter-paperase (FPase), and β-glucosidase, respectively. Subsequent fermentation by the yeast, Saccharomyces cerevisiae NRC2, using lignocellulose hydrolysates obtained from the optimized cellulase process produced the highest amount of ethanol (58 g l⁻¹). This study has revealed the potential of exploiting marine fungi for cost-effective production of cellulases for second generation bioethanol processes.     

Solid state fermentation of a Mycelia Sterilia laccase using steam-exploded wheat straw

Mycelia Sterilia YY-5, an endophytic fungus isolated from Rhus Chinensis Mill, was used in SSF for laccase production using steam-exploded wheat straw (SEWS). The fermentation period of YY-5 in solid state fermentation (SSF) shortened to 4 days compared with 5 days of submerged liquid fermentation (SmF) and the maximum laccase activity was 678.1 IU g⁻¹ substrate. The steam-explosion intensity (Log₁₀ R ₀) of SEWS had a significant effect on the growth of YY-5 and laccase activity, since SEWS could provide enough carbon source for YY-5 and inducers for laccase. The optimum SSF conditions using SEWS with Log₁₀ R ₀ = 3.597 as substrate were: inoculating with liquid inocula, keeping the solid-to-liquid ratio (S/L) for 1:4 and cultivating at 26°C. Under the optimum fermentation condition the laccase activity of YY-5 reached 849.5 ± 42.5 IU g⁻¹ substrate. The enzyme composition analysis indicated that laccase was the dominant enzyme of YY-5. Assayed with SDS-PAGE and active PAGE electrophoresis, the molecular weight of YY-5 laccase was approximately 45 kDa.     

Technical viability of the production,partial purification and characterisation of inulinase using pretreated agroindustrial residues

The present work aimed to study the viability of the use of sugarcane molasses and corn steep liquor (CSL) in a sequential inulinase production performing an up-stream pretreatment of these agroindustrial residues. A sequential strategy was used applying three central composite rotatable designs (CCRDs) to optimise medium composition, followed by a down-stream step. The medium containing 150 g L⁻¹ molasses, 50 g L⁻¹ CSL and 6 g L⁻¹ yeast extract, yielded a maximum inulinase production of 1,294 ± 7 U mL⁻¹, after 72 h of fermentation. A down-stream evaluation was carried out using an expanded bed of Streamline DAE resin (Pharmacia), with and without the up-stream treatment. The results showed that the enzyme could not be recovered from the non-pretreated medium, whereas a yield of 91% was obtained in the adsorption stage from the medium prepared with the up-stream treatment, showing the viability of producing the enzyme inulinase from agroindustrial residues using the integrated process.