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.     

Hydrolysis of inulin from Jerusalem artichoke by inulinase immobilized on aminoethylcellulose

Purified inulinase (inulase, 2,1-β-d-fructan fructanohydrolase, EC 3.2.1.7) of Kluyveromyces fragilis has been immobilized on 2-aminoethyl-cellulose by treatment with 2% glutaraldehyde in 0.05 m phosphate buffer, pH 7.0, for 2 h at room temperature. The immobilized enzyme preparation had 39.3 units inulinase activity per gram dried matrix, with 53.4% recovery yield of activity, and showed good operational stability in the presence of substrate, inulin or the tuber extract of Jerusalem artichoke. Optimum pH and temperature were 5.5 and 45°C, respectively. In a batch reactor, the conversion was 90% ($\text{d}\text{-fructose/}\text{d}\text{-glucose}\text{= 76/24}$) and 34 mg d-fructose per ml was produced from the artichoke tuber extract by the immobilized inulinase in 20 h. In column reactor packed with 28 ml immobilized enzyme, the following conditions were found to be optimal: height/diameter ratio of column, 10.3; space time, 3.8 h; temperature, 40°C. Operation under these conditions gave 90% conversion of a 7% inulin solution and the productivity was 102 mmol l^?1 h^?1.     

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.     

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.     

Inulin hydrolysis by the Debaryomyces phaffii inulinase immobilized on Deae cellulose

Debaryomyces phaffii inulinase was immobilized by adsorption on DEAE-cellulose. The immobilization caused a drop in optimum pH, a slight increase in optimum temperature and an important increase in the thermal stability of the system. The activity yield of immobilized inulinase was 75%.A continuous reactor operation was carried out. The utilization of this system permited the production of fructose syrup from inulin.     

Direct conversion of inulin and extract of tubers of Jerusalem artichoke into single cell oil by co-cultures of Rhodotorula mucilaginosa TJY15a and immobilized inulinase-producing yeast cells

In this study, it was found that the immobilized inulinase-producing cells of Pichia guilliermondii M-30 could produce 169.3 U/ml of inulinase activity while the free cells of the same yeast strain only produced 124.3 U/ml of inulinase activity within 48 h. When the immobilized inulinase-producing yeast cells were co-cultivated with the free cells of Rhodotorula mucilaginosa TJY15a, R. mucilaginosa TJY15a could accumulate 53.2% oil from inulin in its cells and cell dry weight reached 12.2 g/l. Under the similar conditions, R. mucilaginosa TJY15a could accumulate 55.4% (w/w) oil from the extract of Jerusalem artichoke tubers in its cells and cell dry weight reached 12.8 g/l within 48 h. When the co-cultures were grown in 2 l fermentor, R. mucilaginosa TJY15a could accumulate 56.6% (w/w) oil from the extract of Jerusalem artichoke tubers in its cells and cell dry weight reached 19.6 g/l within 48 h. Over 90.0% of the fatty acids from the yeast strain TJY15a grown in the extract of Jerusalem artichoke tubers was C_16:0, C_18:1 and C_18:2, especially C_18:1 (50.6%).     

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.     

The State of the Art in the Production of Fructose from Inulin Enzymatic Hydrolysis

ABSTRACT

The present work reviews the main advancements achieved in the last decades in the study of the fructose production process by inulin enzymatic hydrolysis. With the aim of collecting and clarifying the majority of the knowledge in this area, the research on this subject has been divided in three main parts: a) the characteristics of inulin (the process reactant); b) the properties of the enzyme inulinase and its hydrolytic action; c) the advances in the study of the applications of inulinases in bioreactors for fructose production.

Many vegetable sources of inulin are reported, including information about their yields in terms of inulin. The properties of inulin that appear relevant for the process are also summarized, with reference to their vegetable origin.

The characteristics of the inulinase enzyme that catalyzes inulin hydrolysis, together with the most relevant information for a correct process design and implementation, are described in the paper. An extended collection of data on microorganisms capable of producing inulinase is reported. The following characteristics and properties of inulinase are highlighted: molecular weight, mode of action, activity and stability with respect to changes in temperature and pH, kinetic behavior and effect of inhibitors. The paper describes in detail the main aspects of the enzyme hydrolysis reaction; in particular, how enzyme and reactant properties can affect process performance. The properties of inulinase immobilized on various supports are shown and compared to those of the enzyme in its native state.

Finally, a number of applications of free and immobilized inulinases and whole cells in bioreactors are reported, showing the different operating procedures and reactor types adopted for fructose production from inulin on a laboratory scale.     

Immobilization of Brevibacterium flavum with carrageenan and its application for continuous production of l-malic acid

Extensive experiments were carried out to improve the productivity ofl-malic acid from fumaric acid using Brevibacterium flavum immobilized with carrageenan. The most favourable preparation for the continuous production ofl-malic acid was obtained when 16 g of B. flavum cells was entrapped in 100 ml 3.4% carrageenan gel. However, the immobilized cells produced an unwanted by-product, succinic acid. Treatment of the immobilized cells with 0.6% bile extract suppressed the side reaction and gave the highest operational stability of fumarase activity. By the immobilization of intact cells, the optimal temperature of the enzyme reaction shifted to 10°C higher, the optimal pH became broader, and the operational stability of fumarase activity increased. The effect of temperature on the stability of fumarase activity in the immobilized cell column was investigated under conditions of continuous enzyme reaction. The decay of fumarase activity during continuous enzyme reaction was expressed by an exponential relationship. The productivity of the immobilized B. flavum using carrageenan was as high as 5.2 times that of the conventional immobilized B. ammoniagenes using polyacrylamide.     

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.     

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。     

Inulin hydrolysis and citric acid production from inulin using the surface-engineered Yarrowia lipolytica displaying inulinase

The INU1 gene encoding exo-inulinase cloned from Kluyveromyces marxianus CBS 6556 was ligated into the surface display plasmid and expressed in the cells of the marine-derived yeast Yarrowia lipolytica which can produce citric acid. The expressed inulinase was immobilized on the yeast cells. The activity of the immobilized inulinase with 6 × His tag was found to be 22.6 U mg^?1 of cell dry weight after cell growth for 96 h. The optimal pH and temperature of the displayed inulinase were 4.5 and 50 °C, respectively and the inulinase was stable in the pH range of 3–8 and in the temperature range of 0–50 °C. During the inulin hydrolysis, the optimal inulin concentration was 12.0% and the optimal amount of added inulinase was 181.6 U g^?1 of inulin. Under such conditions, over 77.9% of inulin was hydrolyzed within 10 h and the hydrolysate contained main monosaccharides and disaccharides, and minor trisaccharides. During the citric acid production in the flask level, the recombinant yeast could produce 77.9 g L^?1 citric acid and 5.3 g L^?1 iso-citric acid from inulin while 68.9 g L^?1 of citric acid and 4.1 g L^?1 iso-citric acid in the fermented medium were attained within 312 h of the 2-L fermentation, respectively.     

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.     

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.     

Purification, Immobilization, and Some Properties of Glucose Isomerase from Streptomyces flavogriseus

Glucose isomerase (EC 5.3.1.5) produced from Streptomyces flavogriseus was purified by fractionation with (NH₄)₂SO₄ and chromatography on diethylaminoethyl (DEAE)-cellulose and DEAE-Sephadex A-50 columns. The purified enzyme was homogeneous as shown by ultracentrifugation and sodium dodecyl sulfate-polyacrylamide gel electrophoresis. Benzyl DEAE-cellulose, triethylaminoethyl-cellulose, and DEAE-cellulose were effective in the immobilization of partially purified glucose isomerase. Several differences in properties were found between purified soluble enzyme, immobilized enzyme (DEAE-cellulose-glucose isomerase), and heat-treated whole cells. Glucose and xylose served as substrate for the enzyme. Whole cells had the highest K_m values for glucose and xylose; the soluble enzyme had the lowest values. The optimum temperature for activity of the soluble and immobilized enzymes was 70°C; that for whole cells was 75°C. The pH optimum for the three enzyme preparations was 7.5. Magnesium ion or Co²⁺ was required for enzyme activity; an addition effect resulted from the presence of both Mg²⁺ and Co²⁺. The enzyme activity was inhibited by Hg²⁺, Ag⁺, or Cu²⁺. The conversion ratio of the enzyme for isomerization was about 50%. The soluble and immobilized enzymes showed a greater heat stability than whole cells. The soluble enzyme was stable over a slightly wider pH (5.0 to 9.0) range than the immobilized enzyme and whole cells (pH 5.5 to 9.0). The molecular weight of the enzyme determined by the sedimentation equilibrium method was 171,000. A tetrameric structure for the enzyme was also indicated. After operating at 70°C for 5 days, the remaining enzyme activity of the immobilized enzyme and whole cells, which were used for the continuous isomerization of glucose in a plug-flow type of column in the presence of Mg²⁺ and Co²⁺, was 75 and 55%, respectively. Elimination of Co²⁺ decreased operational stability.     

Immobilized inulinase: a new horizon of paramount importance driving the production of sweetener and prebiotics

In recent times, inulinase has emerged as one the most prominent and industrially upcoming enzymes applied to meet the ever increasing demand of d-fructose and fructooligosaccharides (FOS) as sweetener and prebiotics in the food and pharmaceutical industry, respectively. This review deals with types of inulinase and the attempts made to modify it for better thermal stability and shelf life. The ease of immobilization of inulinase has led us to the path of experimenting with different methods of enzyme immobilization since 1979. Several modes of immobilization ranging from simple cross-linking of enzymes onto a polymer support to nanoparticles have been applied over the years. The approach and concept of this review provide a yet unexplored focus on pioneering advances for the development of white biotechnology, for instance production of immobilized inulinase-based reusable biocatalysts and bioreactors designed for their use and for the continuous production of fructose and FOS.     

Enhanced bioconversion of colchicine to regiospecific 3-demethylated colchicine (3-DMC) by whole cell immobilization of recombinant E. coli harboring P450 BM-3 gene

Biotransformation of colchicine into regiospecific 3-demethylated colchicine (3-DMC) which is pharmacologically active and a potent anti-cancer drug, mediated by immobilization of recombinant microbial monooxygenases is a novel and promising strategy for its production. In the present study, recombinant Escherichia coli expressing P450 BM-3 was immobilized in calcium-alginate beads and its ability to catalyze colchicine into 3-DMC was investigated. Characteristics of immobilized system showed that optimum conditions for activity of microbial cells were not affected due to immobilization. The optimum pH and temperature for both free and immobilized cells were found to be 7.5 and 37.5 °C, respectively. Experimental variables under consideration such as Ca²⁺ concentration, alginate concentration, P450 BM-3 enzyme activity and colchicine concentration were optimized using response surface methodology. The immobilized cells exhibited a markedly improved thermal stability as compared to free cells. The yield of 3-DMC with immobilized microbial cells was found to be an average of 69%, with 82, 73 and 52% across three independent batches in succession as against bioconversion by free cells, which indicated improved operational stability and reusability of immobilized cells in batch processes. Additionally, a packed bed reactor has been proposed for the immobilized biocatalytic system for bioconversion of colchicine and other biochemicals.     

Cloning,characterization and heterelogous expression of the INU1 gene from Cryptococcus aureus HYA

The INU1 gene (Accession number: JX073660) encoding exo-inulinase from Cryptococcus aureus HYA was cloned and characterized. The gene had an open reading frame (ORF) of 1653 bp long encoding an inulinase. The coding region of the gene was not interrupted by any intron. It encoded 551 amino acid residues of a protein with a putative signal peptide of 23 amino acids and the calculated molecular mass of 59.5 kDa. The protein sequence deduced from the inulinase structural gene contained the inulinase consensus sequences (WMNDPNGL), (RDP), ECP, FS and Q. It also had two conserved putative N-glycosylation sites. The inulinase from C. aureus HYA was found to be closely related to that from Kluyveromyces marxianus and Pichia guilliermondii. The inulinase gene without the signal sequence was subcloned into pPICZaA 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 inulinase activity of 16.3 ± 0.24 U/ml was obtained from the culture supernatant of P. pastoris X-33 harboring the inulinase gene. The optimal temperature and pH for action of the enzyme were 50 °C and 5.0, respectively. A large amount of monosaccharides were detected after the hydrolysis of inulin with the purified recombinant inulinase.     

High-level secretory expression and characterization of the recombinant Kluyveromyces marxianus inulinase

Inulinase is an important enzyme used in the high fructose syrup and other related industries. A more cost-effective approach is required for producing highly active inulinase. In this study, the gene encoding inulinase of the yeast Kluyveromyces marxianus CBS 6556 was expressed in methylotrophic host Pichia pastoris and secretory production of recombinant inulinase (rKmINU) in the yeast under methanol induction was achieved. The purified rKmINU showed a specific activity of 2714 U/mg, which is over 12-fold higher than those of other inulinases described previously. It displayed excellent stability from 30 to 50 °C and pH 3.0-5.0, and the half-life of rKmINU was over 96 h under these conditions. Moreover, rKmINU saccharified Jerusalem artichoke tuber juice effectively.