Impact of an acid fungal protease in high gravity fermentation for ethanol production using indian sorghum as a feedstock

This study evaluated the conventional jet cooking liquefaction process followed by simultaneous saccharification and fermentation (SSF) at 30% and 35% dry solids (DS) concentration of Indian sorghum feedstock for ethanol production, with addition of acid fungal protease or urea. To evaluate the efficacy of thermostable α‐amylase in liquefaction at 30% and 35% DS concentration of Indian sorghum, liquefact solubility, higher dextrins, and fermentable sugars were analyzed at the end of the process. The liquefact was further subjected to SSF using yeast. In comparison with urea, addition of an acid fungal protease during SSF process was observed to accelerate yeast growth (μ), substrate consumption (Q_s), ultimately ethanol yield based on substrate (Y_p/s) and ethanol productivity based on fermentation time (Q_p). The fermentation efficiency and ethanol recovery were determined for both concentrations of Indian sorghum and found to be increased with use of acid fungal protease in SSF process. © 2013 American Institute of Chemical Engineers Biotechnol. Prog., 29: 329–336, 2013     

Enhanced lignin peroxidase synthesis by Phanerochaete Chrysosporium in solid state bioprocessing of a lignocellulosic substrate

Summary A solid state fermentation (SSF) process for the production of lignin peroxidase was optimized to enhance enzyme production by Phanerochaete chrysosporium. Optimization of the corncob SSF medium caused a significant reduction in fermentation time to give maximum lignin peroxidase yield. Supplementation of the SSF medium by low concentrations of peptone, yeast extract and Tween-80 enhanced lignin peroxidase production. Maximum yield of lignin peroxidase was 13.7 U/gds (units per gram dry substrate) noted after 5 days of SSF with 70% moisture and 20% (v/w) inoculum.     

Medium optimization of a hydrophilic solvent‐stable protease from Serratia sp. SYBC H

Two statistical methods were used for medium optimization for a hydrophilic solvent‐stable protease production by Serratia sp. SYBC H with duckweed as the nitrogen source. Orthogonal design was applied to find the significant variables, then response surface methodology (RSM), including Box–Behnken central composite experiments, was used to determine the optimal concentrations and interaction of the significant variables. Results demonstrated that duckweed powder, wheat flour, Tween 80, sodium chloride had significant effects on the solvent‐stable protease production. The interaction between duckweed and wheat flour was significant. The optimal level of the variables for the maximum protease production was duckweed 43.9 g/L, wheat flour 20 g/L, sodium chloride 0.08 M, Tween 80 1% v/v, initial pH 11.0, and inoculum size 7% v/v. The maximum protease activity reached 1922.8 U/mL in the optimized medium, with about 18.3‐fold higher than that in the unoptimized medium. Most importantly, the protease from Serratia sp. SYBC H has successfully catalyzed the specific acylation of sucrose in a two‐solvent medium consisting of pyridine and n‐hexane (1:1, v/v), and non‐specific acylation of sucrose in anhydrous DMSO. These results demonstrated that the protease from Serratia sp. SYBC H is a solvent‐stable protease and it could be an ideal biocatalyst for sugar esters syntheses in non‐aqueous media.     

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.     

Enhanced production and characterization of a highly thermostable alkaline protease from Bacillus sp. P-2

An obligatory alkalophilic Bacillus sp. P-2, which produced a thermostable alkaline protease was isolated by selective screening from water samples. Protease production at 30 °C in static conditions was highest (66 U/ml) when glucose (1% w/v) was used with combination of yeast extract and peptone (0.25% w/v, each), in the basal medium. Protease production by Bacillus sp. P-2 was suppressed up to 90% when inorganic nitrogen sources were supplemented in the production medium. Among the various agro-byproducts used in different growth systems (solid state, submerged fermentation and biphasic system), wheat bran was found to be the best in terms of maximum enhancement of protease yield as compared to rice bran and sunflower seed cake. The protease was optimally active at pH 9.6, retaining more than 80% of its activity in the pH range of 7–10. The optimum temperature for maximum protease activity was 90 °C. The enzyme was stable at 90 °C for more than 1h and retained 95 and 37% of its activity at 99 °C and 121 °C, respectively, after 1 h. The half-life of protease at 121 °C was 47 min.     

An organic solvent-, detergent-, and thermostable alkaline protease from the mesophilic, organic solvent-tolerant Bacillus licheniformis 3C5

Bacillus licheniformis 3C5, isolated as mesophilic bacterium, exhibited tolerance towards a wide range of non-polar and polar organic solvents at 45°C. It produced an extracellular organic solvent-stable protease with an apparent molecular mass of approximately 32 kDa. The inhibitory effect of PMSF and EDTA suggested it is likely to be an alkaline serine protease. The protease was active over a broad range of temperatures (45–70°C) and pH (8–10) range with an optimum activity at pH 10 and 65°C. It was comparatively stable in the presence of a relatively high concentration (35% (v/v)) of organic solvents and various types of detergents even at a relatively high temperature (45°C). The protease production by B. licheniformis 3C5 was growth-dependent. The optimization of carbon and nitrogen sources for cell growth and protease production revealed that yeast extract was an important medium component to support both cell growth and the protease production. The overall properties of the protease produced by B. licheniformis 3C5 suggested that this thermo-stable, solvent-stable, detergent-stable alkaline protease is a promising potential biocatalyst for industrial and environmental applications.     

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.     

Comparative study of protease production in solid substrate fermentation versus submerged fermentation

Attempts have been made to compare solid substrate fermentation (SSF) with submerged fermentation for the production of proteases by Bacillus amyloliquefaciens. In submerged fermentation it produced 800,000 units of enzyme under optimal conditions in a 20-litre fermentor whereas in solid substrate, it produced 250,000 units/g. Owing to the simplicity and easiness of operation of SSF and for applications like unhairing, biodetergents and bating the former would be advantageous for the production of proteases.     

Alkaline protease from Thermoactinomyces sp. RS1 mitigates industrial pollution

Proteases have found a wide application in the several industrial processes, such as laundry detergents, protein recovery or solubilization, prion degradation, meat tenderizations, and in bating of hides and skins in leather industries. But the main hurdle in industrial application of proteases is their economical production on a large scale. The present investigation aimed to exploit the locally available inexpensive agricultural and household wastes for alkaline protease production using Thermoactinomyces sp. RS1 via solid-state fermentation (SSF) technique. The alkaline enzyme is potentially useful as an additive in commercial detergents to mitigate pollution load due to extensive use of caustic soda-based detergents. Thermoactinomyces sp. RS1 showed good protease production under SSF conditions of 55 °C, pH 9, and 50 % moisture content with potato peels as solid substrate. The presented findings revealed that crude alkaline protease produced by Thermoactinomyces sp. RS1 via SSF is of potential application in silver recovery from used X-ray films.     

Laccase production in solid‐state and submerged fermentation by Pleurotus ostreatus

A solid‐state fermentation (SSF) system for production of an industrially important enzyme laccase by Pleurotus ostreatus was developed by using potato dextrose yeast extract medium and polyurethane foam as a supporting material. The maximum laccase production in the SSF system was as high as 3×10⁵ U/L. Addition of inducers, such as copper and ferulic acid, further enhanced the laccase production in SSF. Moreover, the time required for the maximum laccase production was reduced to 6 days compared to 10 days reported earlier. The improvement achieved by the SSF system was investigated by comparing it to a submerged fermentation system (SmF), both experimentally and by using a standard theoretical model along with a parameter sensitivity analysis. Laccase production in SSF was found to be twice of that in SmF. One of the main reasons for higher laccase production in SSF compared to SmF was possibly due to the presence of higher proteolytic activity in SmF. Strong proteolytic activity in SmF presumably caused subsequent laccase degradation, which lowered the ultimate laccase production in SmF compared to SSF.     

Production of multiple extracellular enzyme activities by novel submerged culture of <Emphasis Type="Italic">Aspergillus kawachii</Emphasis> for ethanol production from raw cassava flour

Cassava is a starch-containing root crop that is widely used as a raw material in a variety of industrial applications, most recently in the production of fuel ethanol. In the present study, ethanol production from raw (uncooked) cassava flour by simultaneous saccharification and fermentation (SSF) using a preparation consisting of multiple enzyme activities from Aspergillus kawachii FS005 was investigated. The multi-activity preparation was obtained from a novel submerged fermentation broth of A. kawachii FS005 grown on unmilled crude barley as a carbon source. The preparation was found to consist of glucoamylase, acid-stable α-amylase, acid carboxypeptidase, acid protease, cellulase and xylanase activities, and exhibited glucose and free amino nitrogen (FAN) production rates of 37.7 and 118.7 mg/l/h, respectively, during A. kawachii FS005-mediated saccharification of uncooked raw cassava flour. Ethanol production from 18.2% (w/v) dry uncooked solids of raw cassava flour by SSF with the multi-activity enzyme preparation yielded 9.0% (v/v) of ethanol and 92.3% fermentation efficiency. A feasibility study for ethanol production by SSF with a two-step mash using raw cassava flour and the multi-activity enzyme preparation manufactured on-site was verified on a pilot plant scale. The enzyme preparation obtained from the A. kawachii FS005 culture broth exhibited glucose and FAN production rates of 41.1 and 135.5 mg/l/h, respectively. SSF performed in a mash volume of about 1,612 l containing 20.6% (w/v) dry raw cassava solids and 106 l of on-site manufactured A. kawachii FS005 culture broth yielded 10.3% (v/v) ethanol and a fermentation efficiency of 92.7%.     

Inoculation effect of thermophilic microorganisms on protease production through solid-state fermentation under non-sterile conditions at lab and bench scale (SSF)

The production of protease enzyme was evaluated through the solid state fermentation (SSF) of soy fibre, a waste product that acted as a sole substrate for the fermentation, at a laboratory and bench scale using a 500-mL (batch size 115 g) and 10-L (batch size 2300 g) bioreactors. The objective was to assess the effect of the inoculation of the thermophilic bacteria Thermus sp. on the production of the enzyme when working at laboratory and bench scale under non-sterile conditions, since scaling-up and the need of sterilization are the main challenges of SSF, preventing its industrial development. Results revealed that the inoculation led to a substantial increase in the protease obtained on both scales when compared to non-inoculated fermentation. The maximum protease activities increased as a result of the inoculation from 500 to 800 and from 350 to 670 U/g dry matter of soy fibre in the lab and bench scale bioreactors, respectively. Finally, a very good correlation was found between the protease activities obtained and the fermentation most relevant parameters: oxygen uptake rate (R ² = 0.81) and temperature (R ² = 0.82). In this work, we have demonstrated that inoculation is effective even under non-sterile conditions at the kg scale and that this strain is able to compete with autochthonous microbiota and increase the protease production to levels higher than those previously reported in literature.     

Production of protease and lipase by solvent tolerant Pseudomonas aeruginosa PseA in solid-state fermentation using Jatropha curcas seed cake as substrate

Deoiled Jatropha seed cake was assessed for its suitability as substrate for enzyme production by solid-state fermentation (SSF). Solvent tolerant Pseudomonas aeruginosa PseA strain previously reported by us was used for fermentation. The seed cake supported good bacterial growth and enzyme production (protease, 1818 U/g of substrate and lipase, 625 U/g of substrate) as evident by its chemical composition. Maximum protease and lipase production was observed at 50% substrate moisture, a growth period of 72 and 120 h, and a substrate pH of 6.0 and 7.0, respectively. Enrichment with maltose as carbon source increased protease and lipase production by 6.3- and 1.6-fold, respectively. Nitrogen supplementation with peptone for protease and NaNO(3) for lipase production also enhanced the enzyme yield reaching 11,376 U protease activity and 1084 U lipase activity per gram of Jatropha seed cake. These results demonstrated viable approach for utilization of this huge biomass by solid-state fermentation for the production of industrial enzymes. This offers significant benefit due to low cost and abundant availability of cake during biodiesel production.     

A novel nonionic surfactant- and solvent-stable alkaline serine protease from <Emphasis Type="Italic">Serratia</Emphasis> sp. SYBC H with duckweed as nitrogen source: production,purification, characteristics and application

A novel nonionic surfactant- and hydrophilic solvent-stable alkaline serine protease was purified from the culture supernatant of Serratia sp. SYBC H with duckweed as nitrogen source. The molecular mass of the purified protease is about 59 kDa as assayed via SDS-PAGE. The protease is highly active over the pH range between 5.0 and 11.0, with the maximum activity at pH 8.0. It is also fairly active over the temperature range between 30 and 80°C, with the maximum activity at 40°C. The protease activity was substantially stimulated by Mn²⁺ and Na⁺ (5 mM), up to 837.9 and 134.5% at 40°C, respectively. In addition, Mn²⁺ enhanced the thermostability of the protease significantly at 60°C. Over 90% of its initial activity remained even after incubating for 60 min at 40°C in 50% (v/v) hydrophilic organic solvents such as DMF, DMSO, acetone and MeOH. The protease retained 81.7, 83.6 and 76.2% of its initial activity in the presence of nonionic surfactants 20% (v/v) Tween 80, 25% (v/v) glycerol and Triton X-100, respectively. The protease is strongly inhibited by PMSF, suggesting that it is a serine protease. Washing experiments revealed that the protease has an excellent ability to remove blood stains.     

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).     

Laccase, cellulase and xylanase activities during growth ofPleurotus sajor-caju on sagohampas

Sagohampas, the fibrous pith residue left after starch extraction from sago palm, is abundant at sago-processing factories and can be used as a substrate for the production of laccase by solid substrate fermentation (SSF) withPleurotus sajorcaju, an edible mushroom. The fungus grown onhampas with an adjusted carbon : nitrogen ratio of 35:1, exhibited high laccase activity together with variable cellulase (0.3-2.8 U/g) and xylanase (0.9-10.1 U/g) activity. The maximum amount of laccase produced was approximately 17.7 U/g after 6 days of SSF using 4-week-old inoculum at a density of 10%. With the mature four-week inoculum, laccase activity increased 12-fold compared to that achieved with two-week-old inoculum. The optimum pH and temperature of the crude laccase were 6.0 and 50‡C, respectively. The apparent K_m and V_max values obtained were 0.073 mM and 0.962 U/min, respectively. The maximum laccase activity could be almost doubled after 6 days of fermentation by addition of 0.2 mM vanillin or ferulic acid; the cellulose to lignin ratio increased significantly during the 12 days of SSF, from 2.74 in the control to 3.3, when 0.2 mM of either vanillin or ferulic acid was added to the substrate.     

Solid‐state fermentation for the production of debittering enzyme naringinase using Aspergillus niger MTCC 1344

Aspergillus niger produced high levels of naringinase using easily available, inexpensive industrial waste residues such as rice bran, wheat bran, sugar cane bagasse, citrus peel, and press mud in solid‐state fermentation (SSF). Among these, rice bran was found to be the best substrate. Naringinase production was highest after 96 h of incubation at 27°C and at a substrate‐to‐moisture ratio of 1:1 w/v. Supplementation of the medium with 10% naringin caused maximum induction. An inoculum age of 72 h and an inoculum level of 15% resulted in maximum production of naringinase. Enzyme production was stimulated by the addition of nutrients such as naringin and peptone. Thus, A. niger produced a very high level of naringinase within a short time in solid‐state fermentation using inexpensive agro‐residues, a level that is much higher than reported for any other microbes.     

Production and Regulation of Lipase Activity from <Emphasis Type="Italic">Penicillium restrictum</Emphasis> in Submerged and Solid-State Fermentations

Different carbon (C) sources, mainly carbohydrates and lipids, have been screened for their capacity to support growth and lipase production by Penicillium restrictum in submerged fermentation (SmF) and in solid-state fermentation (SSF). Completely different physiological behaviors were observed after the addition of easily (oleic acid and glucose) and complex (olive oil and starch) assimilable C sources to the liquid and solid media. Maximal lipolytic activities (12.1 U/mL and 17.4 U/g) by P. restrictum were obtained with olive oil in SmF and in SSF, respectively. Biomass levels in SmF (12.2–14.1 mg/mL) and SSF (7.0–8.0 mg/g) did not varied greatly with the distinct C sources used. High lipase production (12.3 U/g) using glucose was only attained in SSF, perhaps due to the ability of this fermentation process to minimize catabolite repression.     

Production,partial characterization,and immobilization in alginate beads of an alkaline protease from a new thermophilic fungus <Emphasis Type="Italic">Myceliophthora</Emphasis> sp.

Thermophilic fungi produce thermostable enzymes which have a number of applications, mainly in biotechnological processes. In this work, we describe the characterization of a protease produced in solidstate (SSF) and submerged (SmF) fermentations by a newly isolated thermophilic fungus identified as a putative new species in the genus Myceliophthora. Enzyme-production rate was evaluated for both fermentation processes, and in SSF, using a medium composed of a mixture of wheat bran and casein, the proteolytic output was 4.5-fold larger than that obtained in SmF. Additionally, the peak of proteolytic activity was obtained after 3 days for SSF whereas for SmF it was after 4 days. The crude enzyme obtained by both SSF and SmF displayed similar optimum temperature at 50°C, but the optimum pH shifted from 7 (SmF) to 9(SSF). The alkaline protease produced through solid-state fermentation (SSF), was immobilized on beads of calcium alginate, allowing comparative analyses of free and immobilized proteases to be carried out. It was observed that both optimum temperature and thermal stability of the immobilized enzyme were higher than for the free enzyme. Moreover, the immobilized enzyme showed considerable stability for up to 7 reuses.     

Economic production of Lysinibacillus sphaericus under solid state fermentation

A highly active mosquitocidal Lysinibacillus sphaericus namely Ls 9B24 was isolated from soil of Alexandria governorate in Egypt. It was more active than the standard strain, L. sphaericus 2362. The sporulation and toxin formation of both cultures grown on different leguminous seeds and by-products under solid state fermentation (SSF) were studied. Among the tested substrates, 6% cotton seed meal enhanced sporulation and the mosquitocidal activity of L. sphaericus 2362, while 6% fodder yeast enhanced sporulation and the mosquitocidal activity of Ls 9B24. The optimum SSF growth conditions for maximum mosquitocidal activity by both cultures were using coarse wheat bran as a carrier material, 50% initial moisture content, 4–64 × 10⁶ colony forming units (CFU)/g solid medium inoculum and 6 days’ incubation period at 30°C. Addition of 0.5% yeast extract enhanced toxicity about 2.2 and 1.8 fold for L. sphaericus 2362 and Ls 9B24, respectively.