Rotating simplex method of optimization of physical parameters for higher production of extracellular pectinases in bioreactor

Rotating simplex method of optimization has been successfully used to determine the optimal conditions for extracellular pectinase production by Aspergillus niger in batch bioreactor. Maximum production of 1.132 U of polymethylgalacturonase, 1.313 U of polygalacturonase and 0.0091 U of pectinlyase was obtained at pH (controlled). 3.38; agitation rate, 483 rpm and aeration rate, 2.12 vvm. These conditions were found to be more suitable for pectinase production.     

Pongamia pinnata seed cake: a promising and inexpensive substrate for production of protease and lipase from Bacillus pumilus SG2 on solid-state fermentation

The production of a protease and a lipase from Bacillus pumilus SG2 on solid-state fermentation using Pongamia pinnata seed cake as substrate was studied. The seed cake was proved to be a promising substrate for the bacterial growth and the enzyme production. The initial pH, incubation time and moisture content were optimized to achieve maximal enzyme production. Maximum protease production was observed at 72 h and that of the lipase at 96 h of incubation. The production of protease (9840 U/g DM) and lipase (1974 U/g DM) were maximum at pH 7.0 and at 60% moisture content. Triton X-100 (1%) was proved to be an effective extractant for the enzymes and their optimal activity was observed at alkaline pH and at 60 C. The molecular mass of the protease and lipase was 24 and 40 kDa, respectively. Both the enzymes were found to be stable detergent additives. The study demonstrated that inexpensive and easily available Pongamia seed cake could be used for production of industrially important enzymes, such as protease and lipase.     

Production of pectolytic enzymes – a review

Pectolytic enzymes play an important role in food processing industries and alcoholic beverage industries. These enzymes degrade pectin and reduce the viscosity of the solution so that it can be handled easily. These enzymes are mainly synthesized by plants and microorganisms. Aspergillus niger is used for industrial production of pectolytic enzymes. This fungus produces polygalacturonase, polymethylgalacturonase and pectinlyase. This review mainly concerns with the production of pectolytic enzymes using different carbon sources. It also deals with the effect of operating parameters such as temperature, aeration rate, agitation and type of fermentation on the production of these enzymes.     

High-speed pectic enzyme fractionation by immobilised metal ion affinity membranes

Immobilised metal ion affinity polysulfone hollow-fibre membranes, with a high capacity for protein adsorption, were prepared and their utilisation for commercial pectic enzyme fractionation was studied. The pass-through fraction containing pectinlyase is useful for fruit-juice clarification without methanol production on account of pectinesterase being retained by the IDA-Cu²⁺ membrane.     

Protease production by fermentation of fish solubles from salmon canning processes

Production of protease by fermentation, using Sorangium 495, of a substrate based on condensed fish solubles is demonstrated. The effects of carbohydrate addition, pH, fish solubles concentration, scale-up, agitation, and air flow rate on protease yields are described. While the fish solubles medium alone could give rise to measurable yields of protease, these were, at worst, doubled when 1% glucose was added to the medium. pH 7 was optimal for protease yield. Although the concentration of fish solubles in the basic medium showed no significant effect on cell yield, maximum protease yield was observed at a protein concentration equivalent to 3.85 mg/mL of bovine serum albumin. Protease production rates decreased as medium protein fermentor showed no significant effect on maximum protease yields. The effects of agitator speed and air flow rate on protease yield suggested that the rate of O2 transfer from air to medium could limit the rate of protease production. It was also noted that protease production is not growth associated.     

Influence of carbon source on production of a heat stable protease from Thermomonospora fusca YX

Summary Thermomonospora fusca YX produced a very active heat stable protease when incubated in media containing cellulose as the substrate. Cultures grown on Solka-floc generated the highest amount of protease whereas the protease was produced at significantly lower levels when T. fusca YX was grown on cellobiose or glucose. Negligible growth or protease production was observed when protein was used as a carbon source. The production of the protease did not appear to be constitutive. While rapid growth was observed on either cellobiose or glucose, protease levels were at least two to fourfold lower than for the T. fusca YX cultures grown on Solka-floc wich generated 33% less cell mass. Protease production was four times lower in cultures which employed casein hydrolysate (tryptone) or xylan as carbon sources than for cellulose.     

Physical factors affecting the production of organic solvent-tolerant protease by Pseudomonas aeruginosa strain K

The physical factors affecting the production of an organic solvent-tolerant protease from Pseudomonas aeruginosa strain K was investigated. Growth and protease production were detected from 37 to 45 degrees C with 37 degrees C being the optimum temperature for P. aeruginosa. Maximum enzyme activity was achieved at static conditions with 4.0% (v/v) inoculum. Shifting the culture from stationary to shaking condition decreased the protease production (6.0-10.0% v/v). Extracellular organic solvent-tolerant protease was detected over a broad pH range from 6.0 to 9.0. However, the highest yield of protease was observed at pH 7.0. Neutral media increased the protease production compared to acidic or alkaline media.     

Plasmodium berghei: effect of protease inhibitors during gametogenesis and early zygote development

Plasmodium berghei: The effect of five protease inhibitors, TPCK, TLCK, PMSF, leupeptin, and 1,10-phenanthroline on in vitro gametogenesis and early zygote development of P. berghei was investigated. PMSF and leupeptin showed no effect. Cysteine/serine protease inhibitors TPCK/TLCK at concentrations of 75 and 100 microM were effective on inhibiting exflagellation center formation, and this effect was reversible with the addition of l-cysteine. Exflagellation center formation was most effectively blocked by 1,10-phenanthroline (1mM), and exflagellation center numbers were restored by the addition of Zn(2+). A reduction of ookinete production was observed when TPCK/TLCK (100 microM) was added at 2h after gametogenesis, but no effect was observed with 1,10-phenanthroline (1mM). Our results suggest that proteolysis is important in both gametocyte activation and sexual development of P. berghei.     

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.     

Optimization of Alkaline Protease Production from Bacillus sp. by Response Surface Methodology

High yields (1939 U/ml) of an alkaline protease were obtained in batch fermentation of a Bacillus sp. using a response surface methodology. The interaction of four variables, viz., starch, peptone, incubation time, and inoculum density, suggested inoculum density to be an insignificant variable. However, incubation time had a profound effect on protease yields at all the concentrations of carbon and nitrogen used. The response surface raised and flattened with increase in time of incubation, and maximum protease production up to 1939 U/ml was obtained after 96 h of incubation. The model equation obtained was validated experimentally at maximum starch (15 mg/ml) and peptone (7.5 mg/ml) concentration with increased incubation time up to 144 h in the presence of minimum inoculum density (1%). An overall 2.6-fold increase in protease production was obtained as compared with mean observed response (750 U/ml) at zero level of all variables. Received: 19 July 2001 / Accepted: 15 August 2001     

An organic solvent-, detergent-, and thermo-stable 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 degrees 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 abroad range of temperatures (45-70 degrees C) and pH (8-10) range with an optimum activity at pH 10 and 65 degrees C. It was comparatively stable in the presence ofa relatively high concentration (35% (v/v)) of organic solvents and various types of detergents even at a relatively high temperature (45 degrees 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.     

Optimization of culture conditions for the production of haloalkaliphilic thermostable protease from an extremely halophilic archaeon Halogeometricum sp. TSS101

AIMS: Isolation and screening of extreme halophilic archaeon producing extracellular haloalkaliphilic protease and optimization of culture conditions for its maximum production. METHODS AND RESULTS: Halogeometricum sp. TSS101 was isolated from salt samples and screened for the secretion of protease on gelatin and casein plates containing 20% NaCl. The archaeon was grown aerobically in a 250 ml flask containing 50 ml of (w/v) NaCl 20%; MgCl(2) 1%; KCl 0.5%; trisodium citrate 0.3%; and peptone 1%; pH 7.2 at 40 degrees C on rotary shaker. The production of enzyme was investigated at various pH, temperatures, NaCl concentrations, metal ions and different carbon and nitrogen sources. The partially purified protease had activity in a broad pH range (7.0-10.0) with optimum activity at pH 10.0 and a temperature (60 degrees C). The enzyme was thermostable and retained 70% initial activity at 80 degrees C. Maximum protease production occurred at 40 degrees C in a medium containing 20% NaCl (w/v) and 1% skim milk powder after 84 h in shaking culture. Enzyme secretion was observed at a broad pH range of 7.0-10.0. Addition of CaCl(2) (200 mmol) to the culture medium enhanced the production of protease. Protein rich flours proved to be cheap and good alternative source for enzyme production. Different osmolytes were tested for the growth and production of haloalkaliphilc protease and found that betaine and glycerol enhanced growth without secretion of the protease. Immobilization studies showed that whole cells immobilized in 2% alginate beads were stable up to 10 batches and able to secrete the protease, which attained maximum production within 60 h under shaking conditions. CONCLUSIONS: Halogeometricum sp. TSS101 secreted an extracellular haloalkaliphilic and thermostable protease. The optimum conditions required for maximum production are 20% NaCl, 1% skim milk powder and temperature at 40 degrees C. Addition of CaCl(2) (200 mmol) enhanced the enzyme production. Immobilization of whole cells in absence of NaCl proved to be useful for continuous production of haloalkaliphilic protease. SIGNIFICANCE AND IMPACT OF THE STudy: The low cost protein rich flours were used as an alternative carbon and nitrogen sources for enzyme production. Immobilization of halophilic cells in alginate beads can be used in continuous production of halophilic enzyme. The halophilic and thermostable protease from Halogeometricum sp. TSS101 is good source for industrial applications and can be a suitable source for preparation of fish sauce.     

Mutation of Bacillus subtilis causing hyperproduction of alpha-amylase and protease, and its synergistic effect.

Mutants that had a genetic lesion increasing the production of alpha-amylase and protease simultaneously were isolated from a transformable strain of Bacillus subtilis Marburg by N-methyl-N'-nitro-N-nitrosoguanidine treatment. These mutants produced two to three times more alpha-amylase and five to 16 times more protease than their parent and were tentatively referred to as AP mutants. As this mutation seems to have occurred at a single gene of the bacterial chromosome and was not located near the alpha-amylase structural gene, the gene was designated as "pap." When pap- and amyR2 (an alpha amylase regulator gene) or pap- and ProH coexisted in the same cell, synergistic effects of the two genetic characters were observed on the alpha-amylase and protease production, respectively. Upon introduction of the pap mutation, the following phenotypic changes were observed in addition to changes in alpha-amylase and protease productivity. (i) Mutants lost the character of competence for the transformation. (ii) When cells were cultured at 30 C for 30 h, mutant cells became filament owing to the formation of chains of cells. (iii) Autolysis of cells was decreased in the mutants. When pap- was transferred to the wild strain by deoxyribonucleic acid-mediated transformation, the transformants showed all these phenotypic alterations simultaneously.     

烷烃溶剂对耐有机溶剂极端微生物地衣芽孢杆菌YP1产胞外蛋白酶的影响

考察了添加5%(V/V)浓度的正庚烷、正辛烷、正癸烷、十二烷、十四烷、十六烷等烷烃溶剂对耐有机溶剂极端微生物地衣芽孢杆菌(Bacillus licheniformis)YP1的生长及产胞外蛋白酶的影响.结果表明5%(V/V)浓度的各种烷烃溶剂对YP1蛋白酶的稳定性及菌体生物量均无显著影响,正庚烷、正辛烷、正癸烷等溶剂显著抑制YP1产蛋白酶,而十二烷、十四烷,十六烷能提高YP1产蛋白酶1倍以上.发酵液中十四烷的浓度(1%-8%,VIV)与蛋白酶的活力呈正相关性,添加十四烷后发酵过程中蛋白酶活力的显著增加出现在菌体生长的对数后期.培养过程中添加十四烷能导致YP1菌体形态显著变小.首次报道了烷烃溶剂对极端微生物产蛋白酶的影响.     

烷烃溶剂对耐有机溶剂极端微生物地衣芽孢杆菌YP1产胞外蛋白酶的影响

考察了添加5％(V/V)浓度的正庚烷、正辛烷、正癸烷、十二烷、十四烷、十六烷等烷烃溶剂对耐有机溶剂极端微生物地衣芽孢杆菌(Bacillus licheniformis)YP1的生长及产胞外蛋白酶的影响。结果表明5％(V/V)浓度的各种烷烃溶剂对YP1蛋白酶的稳定性及菌体生物量均无显著影响, 正庚烷、正辛烷、正癸烷等溶剂显著抑制YP1产蛋白酶, 而十二烷、十四烷、十六烷能提高YP1产蛋白酶1倍以上。发酵液中十四烷的浓度(1％－8％, V/V)与蛋白酶的活力呈正相关性, 添加十四烷后发酵过程中蛋白酶活力的显著增加出现在菌体生长的对数后期。培养过程中添加十四烷能导致YP1菌体形态显著变小。首次报道了烷烃溶剂对极端微生物产蛋白酶的影响。     

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.     

Optimization of culture conditions for the production of halothermophilic protease from halophilic bacterium <Emphasis Type="Italic">Chromohalobacter</Emphasis> sp. TVSP101

An extremely halophilic Chromohalobacter sp. TVSP101 was isolated from solar salterns and screened for the production of extracellular halothermophilic protease. Identification of the bacterium was done based upon biochemical tests and the 16S rRNA sequence. The partially purified enzyme displayed maximum activity at pH 8 and required 4.5 M of NaCl for optimum proteolytic activity. In addition, this enzyme was thermophilic and active in broad range of temperature 60–80°C with 80°C as optimum. The Chromohalobacter sp. required 4 M NaCl for its optimum growth and protease secretion and no growth was observed below 1 M of NaCl. The initial pH of the medium for growth and enzyme production was in the range 7.0–8.0 with optimum at pH 7.2. Various cations at 1 mM concentration in the growth medium had no significant effect in enhancing the growth and enzyme production but 0.5 M MgCl₂ concentration enhanced enzyme production. Casein or skim milk powder 1% (w/v) along with 1% peptone proved to be the best nitrogen sources for maximum biomass and enzyme production. The carbon sources glucose and glycerol repressed the protease secretion. Immobilization of whole cells in absence of NaCl proved to be useful for continuous production of halophilic protease.     

Induction of shikonin biosynthesis by endogenous polysaccharides in Lithospermum erythrorhizon cell suspension cultures

Endogenous polysaccharides capable of inducing shikonin biosynthesis in a growth medium were isolated from shikonin-producing Lithospermum cells cultured in a production medium. Chemical analysis showed that these active polysaccharides consist of galacturonic acid, galactose, arabinose and glucose. Their activity, however, was lost by a treatment with pectinlyase. Addition of a small amount of pectinase to cell cultures in the growth medium induced shikonin formation. This is the first report that endogenous polysaccharides participate in inducing normal secondary metabolism of higher plants.     

Production of Extracellular Halo-alkaline Protease from a Newly Isolated Haloalkaliphilic Bacillus sp. Isolated from Seawater in Western India

Summary Haloalkaliphilic, gram positive, aerobic, coccoid Bacillus sp. Po2 was isolated from a seawater sample in Gujarat, India. On the basis of 16s rRNA gene homology, Po2 was 95% related to Bacillus pseudofirmus. A substantial level of extracellular alkaline protease was produced by Po2, which corresponded with the growth and reached a maximum level (264 U/ml) during the stationary phase at 24 h. The production thereafter remained nearly static at optimal level till 36 h. Po2 could grow in the range of 0–20% NaCl (w/v) and pH 7–9, optimally at 10% NaCl (w/v) and pH 8. The protease production was salt-dependent and optimum production required 15% NaCl (w/v) and pH 8. Among the organic nitrogen sources, optimum growth and protease production (260 U/ml) were supported by the combination of peptone and yeast extract. However, growth and protease production were highly suppressed by the inorganic nitrogen sources used; with the exception of potassium nitrate, which supported both growth and protease production to limited extent (24 U/ml). Strong inhibition of enzyme production was observed at above 1% glucose (w/v). Wheat flour served as both carbon and nitrogen source supporting growth and protease production.