Characterization of molecular-sieve-bound inulinase

The enzyme inulinase (2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7), prepared from Kluyveromyces marxianus has been immobilized using an inorganic solid support, molecular sieve 4A via the metal link method. The immobilized enzyme had around 22 units of inulinase activity per g of the support with retention of 72% of the original activity. The optimum protein to molecular sieve ratio for the maximum retention of inulinase activity was 9 mg/g molecular sieve. The properties of soluble and immobilized enzyme differed in many respects. The optimum pH of the enzyme shifted from 6 to 5 and the optimum temperature of enzyme activity changed from 50 to 55°C. K_m values were 6.7 mM for soluble enzyme and 10 mM for immobilized enzyme. The heat stability of the enzyme was improved by immobilization. Immobilized enzyme retained about 76% of the original activity after 40 days of storage at room temperature (30±2°C).     

Biocatalytic properties of immobilized inulinase

A heterogeneous biocatalyst based on inulinase immobilized on a nonionic sorbent of Stirosorb series was proposed. Thermal and acid inactivation of free and immobilized inulinase was examined and the corresponding inactivation constants were calculated. An increase in the thermal stability of the immobilized enzyme in comparison to the free one was found. The possibility of using the immobilized enzyme in the hydrolysis of inulin for ten cycles was determined.     

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.     

Immobilization of Kluyveromyces marxianus cells containing inulinase activity in open pore gelatin matrix: 1. Preparation and enzymatic properties

Kluyveromyces marxianus cells with inulinase (2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7) activity have been immobilized in open pore gelatin pellets with retention of > 90% of the original activity. The open pore gelatin pellets with entrapped yeast cells were obtained by selective leaching out of calcium alginate from the composite matrix, followed by crosslinking with glutaraldehyde. Enzymatic properties of the gelatin-entrapped cells were studied and compared with those of the free cells. The immobilization procedure did not alter the optimum pH of the enzymatic preparation; the optimum for both free and immobilized cells was pH 6.0. The optimum temperature of inulin hydrolysis was 10°C higher for immobilized cells. Activation energies for the reaction with the free and immobilized cells were calculated to be 6.35 and 2.26 kcal mol^?1, respectively. K_m values were 8 mM inulin for the free cells and 9.52 mM for the immobilized cells. The thermal stability of the enzyme was improved by immobilization. Free and immobilized cells showed fairly stable activities between pH 4 and 7, but free cell inulinase was more labile at pH values below 4 and above 7 compared to the immobilized form. There was no loss of enzyme activity of the immobilized cells on storage at 4°C for 30 days. Over the same period at room temperature only 6% of the original activity was lost.     

Inulinase immobilization on polyethylene glycol/polypyrrole multiwall carbon nanotubes producing a catalyst with enhanced thermal and operational stability

This paper describes the development of a simple method for mixed non‐covalent and covalent bonding of partially purified inulinase on functionalized multiwall carbon nanotubes (f‐MWCNTs) with polypyrrole (PPy). The pyrrole (Py) was electrochemically polymerized on MWCNTs in order to fabricate MWCNTs/PPy nanocomposite. Two multiple forms of enzyme were bound to N‐H functional groups from PPy and ‐COO^? from activated MWCNTs to yield a stable MWCNTs/PPy/PEG immobilized preparation with increased thermal stability. Fourier transform infrared (FTIR) spectroscopy and scanning electron microscopy (SEM) were used to confirm functionalization of nanoparticles and immobilization of the enzyme. The immobilization yield of 85% and optimal enzyme load of 345 μg protein onto MWCNTs was obtained. The optimum reaction conditions and kinetic parameters were established using the UV‐Vis analytical assay. The best functional performance for prepared heterogeneous catalyst has been observed at pH 3.6 and 10, and at the temperatures of 60 and 80ºC. The half‐life (t_1/2) of the immobilized inulinase at 60 and 80ºC was found to be 231 and 99 min, respectively. The reusability of the immobilized formulation was evaluated based on a method in which the enzyme retained 50% of its initial activity, which occurred after the eighteenth operation cycle.     

Immobilization of inulinase obtained by solid-state fermentation using spray-drying technology

Abstract

This work focuses on the immobilization of a crude inulinase extract obtained by solid-state fermentation using spray-drying technology. Maltodextrin and arabic gum were used as immobilizing agents. The effects of inlet air temperature, maltodextrin/arabic gum ratio and mass fraction of crude enzyme extract on the activity of immobilized inulinase were assessed using a central composite rotatable design (CCRD) (2³). The optimum operational conditions for the immobilization of inulinase by spray-drying was obtained at an inlet air temperature of 200°C, mass fraction of crude enzyme extract of 0.5 wt% and using only arabic gum as immobilizing agent. The immobilized enzyme had good thermostability, comparable with other inulinases obtained from different microorganisms. The method used gave good enzyme activity after immobilization and could be applied to other enzymes which have good thermal stability.     

Thermal inactivation of free and immobilized inulinase

Thermal inactivation of the Kluyveromyces marxianus inulinase in a free form and immobilized on VION KN-1 cation exchange fiber was studied. Atomic force microscopy demonstrated an oligomeric structure of this enzyme, composed of two subunits differing in their size. It was assumed that the intersubunit contacts were destroyed at 60°C, and the inulinase molecule dissociated into two monomers located separately.     

The effect of urea, gamma- and UV-irradiation on physico-chemical characteristics of native and immobilized inulinase

The immobilization of inulinase by ionexchange AB-26 and AB-17-2P has been made by adsorbtion and glutaraldehyde methods. The effect of UV-radiation, carbamide and gamma-rays on the stability of native and immobilized enzyme has been investigated. The stability of inulinase in relation to denaturation agents has been shown to increase with the immobilization of ionexchange. The character of binding with the matrix affects greatly the stability of immobilized enzyme to physical factors.     

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.     

Production and properties of inulinase from Penicillium sp. NFCC 2768 grown on inulin-rich vegetal infusions

Inulinase production by Penicillium sp. NFCC 2768 isolated from the rhizosphere soil of dahlia was studied on media containing inulin-rich plant extracts. The maximum inulinase activity (64.54 nkat/ml) was observed with the tuber extract of dahlia (Dahlia pinnata). The fungus produced substantial inulinase activity on asparagus root powder (45.23 nkat/ml) and garlic extracts (41.32 nkat/ml). The apparent molecular weight of the purified inulinase was 68 kDa. The optimum pH and temperature for enzyme activity were 5.0 and 50°C, respectively. Mn²⁺ and Ca²⁺ were found to enhance the inulinase activity, while Hg²⁺ was found to be a strong inhibitor. Inulinase liberated fructose, glucose, sucrose, kestose (GF₂), nystose (GF₃), and inulooligosaccharides (IOS). This study suggested the use of dahlia tuber extract and asparagus root powder as suitable substrates for inulinase production by the newly isolated Penicillium sp. NFCC 2768, and its application in the generation of fructose and IOS.     

高产菊粉酶酵母筛选、发酵和酶学性质研究

筛选到1株菊粉酶高产克鲁维酵母菌株,采用酵母高密度细胞发酵方法,最高菊粉酶产量达到288.78u/mL,比80～90年代国际上报道的克鲁维酵母菊粉酶最高产量高6.8倍。该酶的菊粉酶/转化酶活性比为1/24.72;菊糖m=13.3mmol/L,蔗糖Km=62.6mmol/L;最适反应pH值为4.4,但在pH3.8～5.6的范围内均保持了较高的活性,相当于最适pH值下活性的90%;最适反应温度为55℃,在50～575℃范围内能够保持较高活性,50℃下酶的半衰期约为16h;外加Mg2+提高酶活性11.28%。     

Continuous production of gluconic acid and sorbitol from Jerusalem artichoke and glucose using an oxidoreductase of Zymomonas mobilis and inulinase

Gluconic acid and sorbitol were simultaneously produced from glucose and Jerusalem artichoke using a glucose-fructose oxidoreductase of Zymomonas mobilis and inulinase. Inulinase was immobilized on chitin by cross-linking with glutaraldehyde. Cells of Z. mobilis permeabilized with toluene were coimmobilized with chitin-immobilized inulinase in alginate beads. The optimum amounts of both chitin-immobilized inulinase and permeabilized cells for coimmobilization were determined, and operational conditions were optimized. In a continuous stirred tank reactor operation, the maximum productivities for gluconic acid and sorbitol were about 19.2 and 21.3 g/L/h, respectively, at the dilution rate of 0.23 h(-1) and the substrate concentration of 20%, but operational stability was low because of the abrasion of the beads. As an approach to increase the operational stability, a recycle packed-bed reactor (RPBR) was employed. In RPBR operation, the maximum productivities for gluconic acid and sorbitol were found to be 23.4 and 26.0 g/L/h, respectively, at the dilution rate of 0.35 h(-1) and the substrate concentration of 20% when the recirculation rate was fixed at 900 mL/h. Coimmobilized enzymes were stable for 250 h in a recycle packed-bed reactor without any loss of activity, while half-life in a continuous stirred tank reactor (CSTR) was observed to be about 150 h.     

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.     

固定化克鲁维酵母Y-179外切菊粉酶的研究

鹰嘴豆孢克鲁维酵母(Kluveromyces cicerisporus Y-179)分泌的糖基化菊粉外切酶经高碘酸钠氧化其分子表面的糖链产生醛基,再共价结合于氨基型固定化载体ZH-HA上,固定化酶活力达到4 000 U/g湿载体。所制备的固定化酶在pH 3.5和70℃温度下表现出最大反应活性,该固定化酶pH稳定性和热稳定性较游离酶明显提高。固定化酶在分批式反应器中重复水解菊粉50批次,活力没有明显损失,表现出良好的工作稳定性。     

Improvement of inulinase stability of calcium alginate immobilized Kluyveromyces marxianus cells by treatment with hardening agents

To improve the inulinase (2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7) stability of calcium alginate-immobilized Kluyveromyces marxianus cells, treatment with hardening agents has been investigated. Treatment of immobilized cells with some polycationic polymers resulted in little decrease in volumetric reactor productivity, but was most effective in increasing the inulinase stability of the immobilized cells. Inulinase stability of glutaraldehyde-hardened immobilized cells increased two-fold, and for hexamethylenediamine + glutaraldehyde and polyethyleneimine + glutaraldehyde-hardened cells increased six-fold compared with that of the unhardened cells.     

Isolation of an inulinase derepressed mutant of Pichia polymorpha for the production of fructose

Pichia polymorpha has inulinase activity and could be used for the production of fructose syrup from inulin. The application of immobilized P. polymorpha whole cells for the continuous hydrolysis of inulin is, however, limited since the biosynthesis of this enzyme system is repressed by the reaction products, dextrose and fructose. A derepressed mutant hyperproducer of inulinase was isolated after treatment with EMS followed by a selection step with deoxyglucose.     

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     

Production of an endoinulinase from Aspergillus niger AUMC 9375, by solid state fermentation of agricultural wastes,with purification and characterization of the free and immobilized enzyme

Two different substrates, sunflower (Helianthus annuus L.) tubers and lettuce (Lactuca sativa) roots, were tested. Using a mixture of both wastes resulted in higher production of endoinulinase than either waste alone. Also, ten fungal species grown on these substrates as inexpensive, carbon sources were screened for the best production of endoinulinase activities. Of these, Aspergillus niger AUMC 9375 was the most productive, when grown on the mixture using a 6:1 w/w ratio of sun flower: lettuce, and yielded the highest levels of inulinase at 50% moisture, 30°C, pH 5.0, with seven days of incubation, and with yeast extract as the best nitrogen source. Inulinase was purified to homogeneity by ion-exchange chromatography and gel-filtration giving a 51.11 fold purification. The mixture of sunflower tubers and lettuce roots has potential to be an effective and economical substrate for inulinase production. Inulinase was successfully immobilized with an immobilization yield of 71.28%. After incubation for 2 h at 60°C, the free enzyme activity decreased markedly to 10%, whereas that of the immobilized form decreased only to 87%. A reusability test demonstrated the durability of the immobilized inulinase for 10 cycles and in addition, that it could be stored for 32 days at 4°C. These results indicate that this inulinase, in the immobilized form, is a potential candidate for large-scale production of high purity fructose syrups.     

Cloning and characterization of the inulinase gene from a marine yeast <Emphasis Type="Italic">Pichia guilliermondii</Emphasis> and its expression in <Emphasis Type="Italic">Pichia pastoris</Emphasis>

The extracellular inulinase structural gene was isolated from the genomic DNA of the marine yeast Pichia guilliermondii strain 1 by PCR. The gene had an open reading frame of 1,542 bp long encoding an inulinase. The coding region of the gene was not interrupted by any intron. It encoded 514 amino acid residues of a protein with a putative signal peptide of 18 amino acids and the calculated molecular mass of 58.04 kDa. The protein sequence deduced from the inulinase structural gene contained the inulinase consensus sequences (WMNXPNGL) and (RDPKVF). It also had ten conserved putative N-glycosylation sites. The inulinase from P. guilliermondii strain 1 was found to be closely related to that from Kluyveromyces marxianus. The inulinase gene without the signal sequence was subcloned into pPICZαA expression vector and expressed in Pichia pastoris X-33. The expressed fusion protein was analyzed by SDS-PAGE and western blotting and a specific band with molecular mass of about 60 kDa was found. Enzyme activity assay verified the recombinant protein as an inulinase. A maximum activity of 58.7 ± 0.12 U/ml was obtained from the culture supernatant of P. pastoris X-33 harboring the inulinase gene. A large amount of monosaccharides, disaccharides and oligosaccharides were detected after the hydrolysis of inulin with the crude recombinant inulinase.     

Inulinase biosynthesis using immobilized mycelium of Aspergillus niger

Conidia of Aspergillus niger 20 Osm producing extracellular inulinase were immobilized on pumice stones or polyurethane sponge and used in repeated-batch processes. Some factors affecting inulinase biosynthesis by the mycelium A. niger immobilized on pumice stones were investigated. Maximal inulinase production occurred in 50 ml of medium containing 0.5 g of carrier at 30 °C, pH 6.0 and at an agitation speed of 200 rpm. This procedure enabled repeated-batch enzyme production and as many as six subsequent 24 h batches could be fermented by using the same carrier. This is the first report on inulinase biosynthesis by mycelium of A. niger immobilized on polyurethane sponge using unconventional oxygenation of culture which ensures that the dissolved oxygen concentration remains constant.