Inulinase production by a marine yeast <Emphasis Type="Italic">Pichia guilliermondii</Emphasis> and inulin hydrolysis by the crude inulinase

Marine yeast strain 1, isolated from the surface of a marine alga, was found to secrete a large amount of inulinase into the medium. This marine yeast was identified as a strain of Pichia guilliermondii according to the results of routine yeast identification and molecular methods. The crude inulinase produced by this marine yeast worked optimally at pH 6.0 and 60°C. The optimal medium for inulinase production was seawater containing 4.0% (w/v) inulin and 0.5% (w/v) yeast extract, while the optimal cultivation conditions for inulinase production were pH 8.0, 28°C and 170 rpm. Under the optimal conditions, over 60 U ml⁻¹ of inulinase activity was produced within 48 h of fermentation in shake flasks. A large amount of monosaccharides and a trace amount of oligosaccharides were detected after the hydrolysis, indicating that the crude inulinase had a high exoinulinase activity.     

Alkaline inulinase production by a newly isolated bacterium Marinimicrobium sp. LS–A18 and inulin hydrolysis by the enzyme

To date, all of microbial inulinases reported showed optimal activity at pH values ranging from 3.5 to 7.0. A bacterial strain, Marinimicrobium sp. LS-A18, showing high extracellular inulinolytic activity was isolated from a marine solar saltern of the Yellow Sea in China. Maximum enzyme activity was obtained at 55°C and pH 9.0, respectively. The inulinase activity was induced by inulin, but not by the other carbon sources employed. Under the optimal medium and culture condition, the highest inulinase activity, 14.6 U/ml, was obtained after 96 h of incubation at shake flask level. The optimal medium for inulinase production was MHI medium containing 4% inulin, 1% peptone and 5% NaCl, while the optimal culture condition for inulinase production were pH 7.5, temperature 37°C, agitation speed 210 rpm, medium volume 40 ml in 250 ml shake flask, and incubation time 96 h. A large amount of monosaccharides was released after inulin hydrolysis by the inulinase from strain LS-A18. This is the first report on alkaline inulinase production from microorganism.     

Inulinase production by the marine yeast Cryptococcus aureus G7a and inulin hydrolysis by the crude inulinase

The marine yeast strain G7a isolated from sediment of China South Sea was found to secrete a large amount of inulinase into the medium. This marine yeast strain was identified to be a strain of Cryptococcus aureus according to the results of routine yeast identification and molecular methods. The crude inulinase produced by this marine yeast showed the highest activity at pH 5.0 and 50 °C. The optimal medium for inulinase production was artificial seawater containing inulin 4.0% (w/v), K₂HPO₄ 0.3% (w/v), yeast extract 0.5% (w/v), KCl 0.5% (w/v), CaCl₂ 0.12% (w/v), NaCl 4.0% (w/v) and MgCl₂·6H₂O 0.6% (w/v), while the optimal cultivation conditions for inulinase production were pH 5.0, a temperature of 28 °C and a shaking speed of 170 rpm. Under the optimal conditions, over 85.0 U/ml of inulinase activity was produced within 42 h of fermentation at shake flask level. This is very high level of inulinase activity produced by yeasts. A large amount of monosaccharides and oligosaccharides were detected after inulin hydrolysis by the crude inulinase.     

Enhanced fructooligosaccharides and inulinase production by a <Emphasis Type="Italic">Xanthomonas campestris</Emphasis> pv. <Emphasis Type="Italic">phaseoli</Emphasis> KM 24 mutant

Xanthomonas campestris pv phaseoli produced an extracellular endoinulinase (9.24 ± 0.03 U mL⁻¹) in an optimized medium comprising of 3% sucrose and 2.5% tryptone. X. campestris pv. phaseoli was further subjected to ethylmethanesulfonate mutagenesis and the resulting mutant, X. campestris pv. phaseoli KM 24 demonstrated inulinase production of 22.09 ± 0.03 U mL⁻¹ after 18 h, which was 2.4-fold higher than that of the wild type. Inulinase production by this mutant was scaled up using sucrose as a carbon source in a 5-L fermenter yielding maximum volumetric (21,865 U L⁻¹ h⁻¹) and specific (119,025 U g⁻¹ h⁻¹) productivities of inulinase after 18 h with an inulinase/invertase ratio of 2.6. A maximum FOS production of 11.9 g L⁻¹ h⁻¹ and specific productivity of 72 g g⁻¹ h⁻¹ FOS from inulin were observed in a fermenter, when the mutant was grown on medium containing 3% inulin and 2.5% tryptone. The detection of mono- and oligosaccharides in inulin hydrolysates by TLC analysis indicated the presence of an endoinulinase. This mutant has potential for large-scale production of inulinase and fructooligosaccharides.     

Continuous production of fructose-syrups from inulin by immobilized inulinase from recombinantSaccharomyces cerevisiae

Recombinant exoinulinase was partially purified from the culture supernatant ofS. cerevisiae by (NH₄)₂SO₄ precipitation and PEG treatment. The purified inulinase was immobilized onto Amino-cellulofine with glutaraldehyde as a cross-linking agent. Immobilization yield based on the enzyme activity was about 15%. Optimal pH and temperature of immobilized enzyme were found to be 5.0 and 60°C, respectively. The enzyme activity was stably maintained in the pH ranges of 4.5 to 6.0 at 60°C. 100% of enzyme activity was observed even after incubation for 24 hr at 60°C. In the operation of a packed-bed reactor containing 412 U inulinase, dahalia inulin of 7.5%(w/v) concentration was completely hydrolyzed at flow rate of 2.0 mL/min at 60°C, resulting in a volumetric productivity of 693 g-reducing sugars/L/h. Under the reaction conditions of 1.0 mL/min flow rate with 2.5% inulin at 60°C, the reactor was successfully operated over 30 days without loss of inulinase activity.     

Characterization and properties of an inulinase from a thermophilic bacteria

The inulinase of the thermophilic bacterial strain LCB41 (Bacillus sp.) was produced in fermentor using a mineral medium containing inulin as carbon source. The enzyme content was as high as the known inulinase producers and most of the activity was found in the culture medium. The enzyme was stable at high temperature and active at neutral and slightly basic pH. Fructose is liberated as the sole reaction product of inulin hydrolysis, classifying the enzyme as an exoinulinase. Inulin and sucrose were both hydrolyzed at appreciable rates with an (I/S) ratio of 0·40 and (V_m/K_m)₁/(V_m/K_m)_S = 9·9. The enzyme was less inhibited than yeast invertase or Kluyveromyces fragilis inulinase at high sucrose concentrations. The inulinase of strain LCB41 is a good candidate for industrial hydrolysis of inulin or sucrose.     

Considerazioni su Gelsi Ingialliti per Fame

Jerusalem artichoke (Helianthus tuberosus L.), an important crop, containing over 50% inulin in its tubers on a dry weight basis is an agricultural and industrial crop with a great potential for production of ethanol and industrial products. Inulin is a good substrate for bioethanol production. Saccharomyces cerevisiae 6525 can produce high concentrations of ethanol, but it cannot synthesize inulinase. In this study, a new integration vector carrying inuA1 gene encoding exoinulinase was constructed and transformed into 18SrDNA site of industrial strain S. cerevisiae 6525. The obtained transformant, BR8, produced 1.1 U mL^? 1 inulinase activity within 72 h and the dry cell weight reached 12.3 g L^? 1 within 48 h. In a small-scale fermentation, BR8 produced 9.5% (v/v) ethanol, with a productivity rate of 0.385 g ethanol per gram inulin, while wild-type S. cerevisiae 6525 produced only 3.3% (v/v) ethanol in the same conditions. In a 5-L fermentation, BR8 produced 14.0% (v/v) ethanol in fermentation medium containing inulin and 1% (w/v) (NH4)₂SO₄. The engineered S. cerevisiae 6525 carrying inuA1 converted pure nonhydrolyzed inulin directly into high concentrations of ethanol.     

Inulinase production and mathematical modeling from carob extract by using Aspergillus niger

The main objectives of the study were to produce inulinase from carob extract by Aspergillus niger A42 (ATCC 204447) and to model the inulinase fermentation in the optimum carob extract-based medium. In the study, carob extract was used as a novel and renewable carbon source in the production of A. niger inulinase. For medium optimization, eight different variables including initial sugar concentration (°Bx), (NH₄)₂HPO₄, MgSO₄.7H₂O, KH₂PO₄, NH₄NO₃, yeast extract, peptone, and ZnSO₄.7H₂O were employed. After fermentations, optimum medium composition contained 1% yeast extract in 5°Bx carob extract. As a result of the fermentation, the maximum inulinase activity, maximum invertase-type activity, I/S ratio, maximum inulinase- and invertase-type activity rates, maximum sugar consumption rate, and sugar utilization yield were 1507.03 U/ml, 1552.86 U/ml, 0.97, 175.82 and 323.76 U/ml/day, 13.26 g/L/day, and 98.52%, respectively. Regarding mathematical modeling, the actual inulinase production and sugar consumption data were successfully predicted by Baranyi and Cone models based on the model evaluation and validation results and the predicted kinetic values, respectively. Consequently, this was the first report in which carob extract was used in the production of inulinase as a carbon source. Additionally, the best-selected models can serve as universal equations in modeling the inulinase production and sugar consumption in shake flask fermentation with carob extract medium.     

Immobilization of thermostable exo-inulinase from mutant thermophilic Aspergillus tamarii-U4 using kaolin clay and its application in inulin hydrolysis

In this study, attempts were made to immobilize purified exo-inulinase from mutant thermophic Aspergillus tamarii-U4 onto Kaolinite clay by covalent bonding cross-linked with glutaraldehyde with an immobilization yield of 66% achieved. The free and immobilized inulinases were then characterized and characterization of the enzymes revealed that temperature and pH optima for the activity of the free and immobilized enzymes were both 65?°C and pH 4.5 respectively. The free inulinase completely lost its activity after incubation at 65?°C for 6 h while the immobilized inulinase retained 16.4% of its activity under the same condition of temperature and incubation time. The estimated kinetic parameters K_m and V_max for the free inulinase as estimated from Lineweaver-Burk plots were 0.39?mM and 4.21?µmol/min for the free inulinase and 0.37?mM and 4.01?µmol/min for the immobilized inulinase respectively. Inulin at 2.5% (w/v) and a flow rate of 0.1?mL was completely hydrolysed for 10?days at 60?°C in a continuous packed bed column and the operational stability of the system revealed that the half-life of the immobilized inulinase was 51?days. These properties make the immobilized exo-inulinase from Aspergillus tamarii-U4 a potential candidate for the production of fructose from inulin hydrolysis.     

Expression of the inulinase gene from the marine‐derived Pichia guilliermondii in Saccharomyces sp. W0 and ethanol production from inulin

It has been confirmed that Saccharomyces sp. W0 can produce high concentration of ethanol. In this study, the INU1 gene cloned from the marine-derived Pichia guilliermondii was transformed into uracil mutant of Saccharomyces sp. W0. The positive transformant Inu-66 obtained could produce 34.2 U ml⁻¹ of extracellular inulinase within 72 h of cultivation. It was found that 15.2 U of inulinase activity per one gram of inulin was suitable for inulin hydrolysis and ethanol production by the transformant Inu-66. During the small-scale fermentation, 13.7 ml of ethanol in 100 ml of medium was produced and 99.1% of the added inulin was utilized by the transformant. During the 2 l fermentation, 14.9% (v/v) of ethanol was produced from inulin and 99.5% of the added inulin was converted into ethanol, CO₂ and cell mass.     

Expression of exo‐inulinase gene from Aspergillus niger 12 in E. coli strain Rosetta‐gami B (DE3) and its characterization

Inulin is a linear carbohydrate polymer of fructose subunits (2‐60) with terminal glucose units, produced as carbon storage in selected plants. It cannot directly be taken up by most microorganisms due to its large size, unless prior hydrolysis through inulinase enzymes occurs. The hydrolyzed inulin can be taken up by microbes and/or recovered and used industrially for the production of high fructose syrup, inulo‐oligosaccharides, biofuel, and nutraceuticals. Cell‐free enzymatic hydrolysis would be desirable for industrial applications, hence the recombinant expression, purification and characterization of an Aspergillus niger derived exo‐inulinase was investigated in this study. The eukaroyototic exo‐inulinase of Aspergillus niger 12 has been expressed, for the first time, in an E. coli strain [Rosetta‐gami B (DE3)]. The molecular weight of recombinant exo‐inulinase was estimated to be ～81 kDa. The values of K_m and V_max of the recombinant exo‐inulinase toward inulin were 5.3 ± 1.1 mM and 402.1 ± 53.1 µmol min^?1 mg^?1 protein, respectively. Towards sucrose the corresponding values were 12.20 ± 1.6 mM and 902.8 ± 40.2 µmol min^?1 mg^?1 protein towards sucrose. The S/I ratio was 2.24 ± 0.7, which is in the range of native inulinase. The optimum temperature and pH of the recombinant exo‐inulinase towards inulin was 55°C and 5.0, while they were 50°C and 5.5 towards sucrose. The recombinant exo‐inulinase activity towards inulin was enhanced by Cu²⁺ and reduced by Fe²⁺, while its activity towards sucrose was enhanced by Co²⁺ and reduced by Zn²⁺. © 2016 American Institute of Chemical Engineers Biotechnol. Prog., 32:629–637, 2016     

Studies on a beta-fructosidase (inulinase) produced bySaccharomyces fragilis

Summary A study was made of a β-fructosidase, which is produced extracellularly and intracellularly bySaccharomyces fragilis. The enzyme catalyzes the hydrolysis of inulin, bacterial levans, sucrose, and the fructose portion of raffinose, by splitting off terminal fructosyl units. It attacks β-2,1 as well as β-2,6 linkages. The enzyme content of inulin-grown cells is sufficient to allow fermentation of inulin at the same rate as glucose. The ratio of hydrolysis rates with sucrose and inulin was about 25 for the β-fructosidase ofS. fragilis and about 14,000 for invertase.S. fragilis does not contain significant amounts of invertase and it ferments inulin, sucrose and raffinose with the aid of a related, but different enzyme, inulinase. Conditions of growth were established which favor inulinase synthesis. Highest yields were obtained with inulin as the carbon source, and somewhat lower yields with raffinose. Glucose, fructose and sucrose were poor inducers of inulinase. The pH of the medium during growth on inulin had to be in the range where inulinase could act, otherwise growth was tardy and poor. In an inulin containing medium aeration favored enzyme production as a result of stimulation of growth. The inulinase content of the cells in a unit volume was generally greater than that in the culture medium. The intracellular inulinase could be solubilized quantitatively by autolysis. The intra-and extracellular inulinases were concentrated and purified to the same extent. Comparison of the two preparations with respect to substrate specificity, rate of inactivation by heat, pH optima with sucrose (4.2) and with inulin (5.0), and elution patterns from a column of diethylaminoethyl cellulose, indicated that the intra-and extracellular enzymes were identical.     

Utilization of Leek (Allium ampeloprasum var. porrum) for Inulinase Production

Inulinase production by Rhodotorula glutinis was carried out in this study, using leek (Allium ampeloprasum var. porrum) as an alternative carbon source due to its high inulin content and easy availability. Taguchi orthogonal array (OA) design of experiment (DOE) was used to optimize fermentation conditions. For this purpose, five influential factors (leek concentration, pH, incubation temperature, agitation speed, and fermentation time) related to inulinase production were selected at four convenient levels. The results showed that maximum inulinase activity was obtained as 30.89 U/mL, which was close to the predicted result (30.24 U/mL). To validate the obtained results, analysis of variance (ANOVA) was employed. Consequently, leek has a great potential as an effective and economical carbon source for inulinase production, and the use of Taguchi DOE enhanced enzyme activity about 2.87-fold when compared with the unoptimized condition.     

Optimization of simultaneously enzymatic fructo- and inulo-oligosaccharide production using co-substrates of sucrose and inulin from Jerusalem artichoke

Prebiotic substances are extracted from various plant materials or enzymatic hydrolysis of different substrates. The production of fructo-oligosaccharide (FOS) and inulo-oligosaccharide (IOS) was performed by applying two substrates, sucrose and inulin; oligosaccharide yields were maximized using central composite design to evaluate the parameters influencing oligosaccharide production. Inulin from Jerusalem artichoke (5–15% w/v), sucrose (50–70% w/v), and inulinase from Aspergillus niger (2–7 U/g) were used as variable parameters for optimization. Based on our results, the application of sucrose and inulin as co-substrates for oligosaccharide production through inulinase hydrolysis and synthesis is viable in comparative to a method using a single substrate. Maximum yields (674.82?mg/g substrate) were obtained with 5.95% of inulin, 59.87% of sucrose, and 5.68 U/g of inulinase, with an incubation period of 9?hr. The use of sucrose and inulin as co-substrates in the reaction simultaneously produced FOS and IOS from sucrose and inulin. Total conversion yield was approximately 67%. Our results support the high value-added production of oligosaccharides using Jerusalem artichoke, which is generally used as a substrate in prebiotics and/or bioethanol production.     

Production, purification and characterization of an extracellular inulinase from Kluyveromyces marxianus var. bulgaricus

The yeast Kluyveromyces marxianus var. bulgaricus produced large amounts of extracellular inulinase activity when grown on inulin, sucrose, fructose and glucose as carbon source. This protein has been purified to homogeneity by using successive DEAE-Trisacryl Plus and Superose 6HR 10/30 columns. The purified enzyme showed a relative molecular weight of 57 kDa by sodium dodecyl sulfate polyacrylamide gel electrophoresis (SDS-PAGE) and 77 kDa by gel filtration in Superose 6 HR 10/30. Analysis by SDS-PAGE showed a unique polypeptide band with Coomassie Blue stain and nondenaturing PAGE of the purified enzyme obtained from media with different carbon sources showed the band, too, when stained for glucose oxidase activity. The optimal hydrolysis temperature for sucrose, raffinose and inulin was 55°C and the optimal pH for sucrose was 4.75. The apparent K _m values for sucrose, raffinose and inulin are 4.58, 7.41 and 86.9 mg/ml, respectively. Thin layer chromatography showed that inulinase from K. marxianus var. bulgaricus was capable of hydrolyzing different substrates (sucrose, raffinose and inulin), releasing monosaccharides and oligosaccharides. The results obtained suggest the hypothesis that enzyme production was constitutive. Journal of Industrial Microbiology & Biotechnology (2000) 25, 63–69. Received 17 November 1999/ Accepted in revised form 30 May 2000     

Increase in extracellular inulinase production for a new Rhizoctonia ssp. strain by using buckwheat (Fagopyrum esculentum) flour as a single carbon source

Aims: A newly isolated strain of Rhizoctonia ssp. was used for the production of extracellular inulinase. Previously, the qualitative effects of some carbon and nitrogen sources from fermentative media and the physicochemical parameters for growth were established by Plackett–Burman analysis, and the main parameters that affect extracellular inulinase yield were identified. In this study, the quantitative effect of the carbon to nitrogen ratio in the fermentative medium and the growth temperature were studied and optimized using central composite design and response surface methodology. Methods and results: On the basis of optimization, the maximum extracellular inulinase activity was achieved when 2·5–6·5% buckwheat flour was used as a single carbon source and 4·6–5·0% yeast extract was used as nitrogen source, by submerged cultivation, after 48 h at an incubation temperature between 15 and 27·5°C. Conclusions: Under the fermentative conditions established in this study, a maximum extracellular inulinase yield of 1·8 UI ml^?1 was achieved. Rhizoctonia ssp. strain can be used for extracellular inulinase production. Also, buckwheat flour proved to be an inexpensive and abundant substrate suitable for obtaining inulinase. Significance and impact of the study: Inulinases are versatile tools for biotechnology as they can be used for a wide range of applications, including production of bioethanol, fructose syrup and inulo‐oligosaccharides, lactic acid, citric acid and butanediol.     

Bioconversion of inulin to 2,3-butanediol by a newly isolated Klebsiella pneumoniae producing inulinase

Inulin could be converted to bio-based chemicals by an inulinase producer without external inulinase, and the production of 2,3-butanediol was less than 50 g/L. In this work, a novel inulinase producer of Klebsiella pneumoniae H3 was isolated, and inulinase catalytic properties as well as 2,3-butanediol fermentation were investigated. The enzyme was an intracellular inulinase with an optimal pH of 6 ∼ 7 and a temperature of 30 °C. The use of inulin by H3 was dependent on the degree of polymerization (DP), and the average DP of inulin in fermentation broth increased from 2.82 to 8.08 in 24-h culture of batch fermentation. Acidic pretreatment was developed to increase inulin utilization by adjusting medium pH to 3.0 prior to sterilization. In batch fermentation with optimized medium and fermentation conditions, the concentration of target product (2,3-butanediol and acetoin) was 80.4 g/L with a productivity of 2.23 g/(L⋅h), and a yield of 0.426 g/g inulin.     

降解菊粉担子菌的分离鉴定及其酶的产生

从菊芋地的腐木上分离到一株在以菊粉为唯一碳源和能源的培养基上生长良好,具有较高菊粉酶活性的担子菌菌株,经鉴定为采绒革盖菌（Ｃｏｒｉｏｌｕｓｖｅｒｓｉｏｌｏｒ）。该菌的菊粉酶大部分是胞外酶,此酶对菊粉的专一性高,其Ｉ／Ｓ比值在发酵过程中不断变化。菊粉酶活性平行地随菌体生长而增加。该酶的合成受菊粉诱导,受果糖抑制。当果糖浓度大于２．７ｍｇ／ｍｌ时,菊粉酶活性为零。菌体的匀质化可使生长加快从而获得大量菊粉酶。     

Enhanced production of an alkaline pectinase from Streptomyces sp. RCK-SC by whole-cell immobilization and solid-state cultivation

An alkalophilic Streptomyces sp. RCK-SC, which produced a thermostable alkaline pectinase, was isolated from soil samples. Pectinase production at 45 °C in shaking conditions (200 rev min⁻¹) was optimal (76,000 IU l⁻¹) when a combination of glucose (0.25% w/v) and citrus pectin (0.25% w/v) was added along with urea (0.25% w/v) in the basal medium devoid of yeast extract and peptone. All the tested amino acids and vitamins greatly induced pectinase production and increased the specific productivity of pectinase up to 550%. In an immobilized cell system containing polyurethane foam (PUF), the pectinase production was enhanced by 32% (101,000 IU l⁻¹) compared to shake flask cultures. In solid-state cultivation (SSC) conditions, using wheat bran as solid substrate, pectinase yield of 4857 IU g⁻¹ dry substrate was obtained at substrate-to-moisture ratio of 1:5 after 72 h of incubation. The partially purified pectinase was optimally active at 60 °C and retained 80% of its activity at 50 °C after 2 h of incubation. The half life of pectinase was 3 h at 70 °C. Pectinase was stable at alkaline pH ranging from 6.0 to 9.0 for more than 8 h at room temperature retaining more than 50% of its activity. This revised version was published online in August 2006 with corrections to the Cover Date.     

The Influence of n-Propanol on the Growth and Conidiation of Pestalotia rhododendri

Pestalotia rhododendri was exposed to vapours from 1 ml propanol solution in water and linear growth, formation of aerial hyphae and production of conidia were determined. A special Petri dish technique was used and maximum stimulation of conidial formation was induced by the vapours from a propanol concentration of 3–4 % (v/v) at 25°C. When propanol was added directly to the medium, a concentration of 1.2 × 10^?2M was optimal for growth and sporulation at 30°C. Sporulation stimulated by propanol was observed at temperatures from 20–32°C, with an optimum at 30°C. Certain observations indicated that an exposure to propanol for 24 hours was enough to induce a stimulated spore production. The stimulation was noticed on different media at 25°C, and was more pronounced at 30°C. One exception was observed. Propanol did not promote sporulation when the fungus was grown on maltagar at 30°C. Propanol 3 ° (v/v) in combination with the standard medium containing (NH₄)₂-tartrate as sole nitrogen source, inhibited the linear growth at 15–20°C, was inactive at 22.5° and 25°C, and stimulated growth at 27.5–31°C. The stimulatory effect was maximal at 30°C. Other media were tested at 25° and 30°C. At both temperatures stimulations of linear growth caused by propanol were observed with a medium containing KNO₃ as sole nitrogen source, and inhibitions with maltagar and another medium containing l -asparaginc as sole nitrogen source. The linear growth could be either inhibited or stimulated while the sporulation was stimulated.