Enhanced expression of endoinulinase from Aspergillus niger by codon optimization in Pichia pastoris and its application in inulooligosaccharide production

In the present study, the endoinulinase gene (EnInu) from Aspergillus niger CICIM F0620 was optimized according to the codon usage of Pichia pastoris and both the native and the optimized gene were expressed in P. pastoris. Use of the optimized gene resulted in the secretion of recombinant endoinulinase activity that reached 1,349 U ml^?1, 4.18 times that observed using the native gene. This is the highest endoinulinase activity reported to date. The recombinant enzyme was optimally active at pH 6.0 and 60 °C. Moreover, inulooligosaccharides production from inulin was studied using the recombinant enzyme produced from the optimized gene. After 8 h under optimal conditions, which included 400 g l^?1 inulin, an enzyme concentration of 40 U g^?1 substrate, 50 °C and pH 6.0, the inulooligosaccharide yield was 91 %. The high substrate concentration and short reaction time described here should reduce production costs distinctly, compared with the conditions used in previous studies. Thus, this study may provide the basis for the industrial use of this recombinant endoinulinase for the production of inulooligosaccharides.     

Production of inulo-oligosaccharides from inulin by recombinant E. coli containing endoinulinase activity

To utilize intracellular endoinulinase for inulo-oligosaccharide (IOS) production from inulin, the endoinulinase gene (inu1) of Pseudomonas sp. was successfully cloned into the plasmid pBR322 by using EcoRI restriction endoinulinase and E. coli HB101 as a host strain. The endoinulinase from E. coli HB101/pKMG50 was constitutively expressed, showing similar reaction modes as compared to those of the original strain. However, some critical differences existed in optimal reaction conditions and oligosaccharide compositions between the two products catalyzed by the native enzyme of original strain and those by intact cells from recombinant cells. The IOS compositions produced by recombinant E. coli were quite different due to the diffusional restriction of the substrate and products within the cell wall. Optimal reaction conditions for batchwise production of IOS were as follow : optimum temperature, 55v°C; pH, 7.5; substrate concentration, 100 g/l inulin; enzyme dosage, 20 units/g substrate. Continuous production of IOS from inulin was also carried out at 50v°C using a bioreactor packed with the recombinant cells immobilized on calcium alginate gel. The optimal feed concentration and the feed flow rate were 100 g/l inulin and 0.6 h^у as a superficial space velocity, respectively. Under the optimum operation conditions, continuous production of IOS was successfully performed with productivity of 166.7 g/l·h for 15 days at 50v°C without significant loss of initial activity.     

Continuous production of inulo-oligosaccharides from chicory juice by immobilized endoinulinase

Several carrier materials were examined for endoinulinase immobilization. A polystyrene carrier material (UF93^®) gave the best immobilization capacity (217 units/g carrier) and operational stability. Carbohydrate compositions in the reaction product were quite similar irrespective of the support materials even though each carrier material has different pore structure associated with diffusional restriction. After immobilization the optimal pH for enzyme activity was shifted from 5.0 to 4.5, whereas optimal temperature (55v°C) was unaltered. Continuous production of inulo-oligosaccharides from chicory juice was carried out using the polystyrene-bound endoinulinase. The recommended operating conditions of the enzyme reactor for maximizing productivity were as follows: feed concentration, 100 g/l chicory juice; flow rate, as superficial space velocity 2.0 h^у; temperature, 55v°C. The enzyme reactor was run for 28 days at 55v°C achieving an oligosaccharide yield of 82% without any significant loss of initial enzyme activity, where the volumetric productivity was 200 g/l · h. Furthermore, there was no marked difference in operational stability between the two reactors fed with pure inulin solution and with chicory juice as a substrate even though chicory juice contains a lot of impurities.     

Purification and some properties of trehalase from Chaetomium aureum MS-27

The trehalase of Chaetomium aureum was purified about 196-fold with a yield of 51% from the culture filtrate by ammonium sulfate fractionation, DEAE-cellulose column chromatography, acetone fractionation, and Sephadex G-100 gel filtration. The enzyme preparation was homogeneous on disc electrophoresis. The enzyme was most active at pH 4.0 and 50°C. The enzyme was stable from pH 4.0 to 9.0 on 12 h incubation at 37°C. The molecular weight of the enzyme was estimated to be 450,000 by gel filtration on a column of Sepharose 6B, and 115,000 by SDS polyacrylamide gel electrophoresis. This indicated that the enzyme might consist of 4 subunits. The isoelectric point of the enzyme was pH 4.0. The enzyme was active specifically on trehalose and not active on the other disaccharides tested.     

Effects of Ionic Strength on Thermostability of Lactoperoxidase

An extracellular enzyme that produces di-D-fructofuranose 2′,1;2,1′-dianhydride (difructose anhydride I= DFA I) from inulin was purified from the culture broth of Streptomyces sp. MCI-2524. The purification enhanced the specific activity 7-fold with an overall yield of 17%. The purified enzyme, when electrophoresed on a SDS polyacrylamide gel, gave a single band corresponding to a molecular weight of 36 kDa. Gel filtration chromatography gave a single peak that eluted at a position corresponding to 70 kDa. The enzyme was active from pH 3.0 to pH 9.0, and at temperatures up to 65°C. Maximal activity was observed at pH 6.0, at 55°C. The enzyme was inhibited by Cu²⁺.     

Production of inulooligosaccharides from inulin by a novel endoinulinase from Xanthomonas sp.

A novel inulinolytic microorganism, Xanthomonas sp. produced an endoinulinase, to be used for inulooligosaccharide (IOS) formation from inulin, at an activity of 11 units ml^–1 (1.2 mg protein ml^–1). The endoinulinase was optimally active at 45°C and pH 6.0. Batchwise production of IOS was carried out by the partially purified endoinulinase with a maximum yield of about 86% on a total sugar basis with 10 g inulin l^–1. The major IOS components were DP (degree of polymerization) 5 and 6 with trace amount of smaller oligosaccharides.     

A thermophilic extracellular -amylase from Bacillus licheniformis

A strain of Bacillus licheniformis isolated from soil produced an extracellular α-amylase(s) with unusual characteristics. The enzyme was purified 126-fold by starch adsorption, DEAE-cellulose treatment, and CM-cellulose column chromatography. Four active protein bands were detected by disc electrophoresis in poly-acrylamide gel although the enzyme behaved as a single peak during both ultracen-trifugation and chromatography using CM-cellulose and Sephadex G-100. The enzyme showed a very broad pH-activity curve and had substantial activity in the alkaline range. The optimal temperature was 76 °C at pH 9.O. The enzyme was stable between pH 6 and 11 at 25 °C, and below 60 °C at pH 8.0. Using Sephadex G-100 gel filtration, a molecular weight of 22,500 was estimated for the enzyme. The action pattern on amylose and amylopectin is unique in that the predominant product during all stages of hydrolysis is maltopentaose.     

Semi-rational chemical modification of endoinulinase by pyridoxal 5′-phosphate and ascorbic acid

It is important to improve the quality of the enzyme inulinase used in industrial applications without allowing the treatment to have any adverse effects on enzyme activity. We achieved preferential chemical modification of the non-catalytic domain of endoinulinase (EC 3.2.1.7) to enhance the thermostability of the enzyme. We used pyridoxal 5′-phosphate (PLP) to modify the more accessible lysine residues at the surface of endoinulinase and then performed a necessary step of reduction with ascorbate. Endoinulinase was incubated in the presence of PLP at various concentrations; this step was followed by reduction of the resulting Schiff base and dialysis. The effects of different PLP concentrations and incubation times on enzyme modification were evaluated. Enzyme deactivation was observed immediately after treatment, even at low PLP concentrations, while reactivation was observed for samples treated with low PLP concentrations after a period of time. Structural analysis revealed that the α-helix content increased from 13.60% to 17.60% after applying the modification strategy; consequently, enzyme stabilization was achieved. The melting temperature (T_m) of the modified enzyme increased from 64.1 °C to 72.2 °C, and a comparative study of thermal stability at 25 °C, 45 °C, and 50 °C for 150 min confirmed that the enzyme was stabilized because of increase in its half-life (t_1/2) after PLP modification/ascorbate reduction. The modification process was optimized to achieve the optimum mole ratio for the PLP/endoinulinase (1.37). Excess moles of the modifier are thought to be responsible for enzyme deactivation through unwanted/nonspecific and noncovalent interactions, and the optimization ensured that there was no excess modifier after the desired covalent reaction was complete.     

Purification of Inulin Fructotransferase (DFA I-producing) from Arthrobacter MCI2493 and Production of DFA I from Inulin by the Enzyme

An extracellular enzyme that produces di-d-fructofuranose-2′, 1;2, 1′ dianhydride from inulin was purified from the culture broth cf Arthrobacter sp. MCI2493. The molecular weight of the enzyme was 40,000 by gel filtration and SDS polyacrylamide gel electrophoresis. The enzyme had maximum activity at pH 6.0 and 50°C. Using this purified enzyme, 100g/liter inulin was converted into 60 g/liter of DFA I, nystose, and 1-f-fructofuranosyl-nystose after incubation for 30 h.     

Production of Pentameric Hybrid Immunoglobulins Consisting of IgA and IgM

The amylomaltase from Escherichia coli IFO 3806 was purified to homogeneity seen by SDS- polyacrylamide gel electrophoresis after DEAE-Sephadex, Ultrogel AcA 44, hydroxylapatite, and 1,6- hexane-diamine-Sepharose 4B column chromatographies. The molecular weight of the purified enzyme was 93,000 by SDS-polyacrylamide gel electrophoresis. The enzyme was most active at pH 6.5 and at 35°C, and stable up to 45°C at pH 7.0 and from pH 6.0 —7.3 at 40°C on 30min incubation. The enzyme acted on maltotetraitol, maltopentaitol, and maltosylsucrose besides maltooligosaccharides, but did not act on maltitol, maltotriitol, glucosylsucrose, isomaltose, panose, isopanose, or isomaltosyl- maltose. This enzyme did not catalyze hydrolytic action on maltotetraitol, maltopentaitol, or maltosylsucrose.     

Purification and properties of an acidic β-glucosidase from Acidobacterium capsulatum

Acidobacterium capsulatum, an acidophilic, mesophilic and chemoorganotrophic bacterium, produced an inducible, acidic β-glucosidase in the cellobiose medium. The enzyme was successively purified 109 times by CM-Sepharose, Sephacryl S-200 chromatography and preparative discontinuous polyacrylamide gel electrophoresis. Polyacrylamide gel electrophoresis of the purified enzyme gave a single band at pH 4.3. The enzyme had an optimum pH of 3.0 and optimum reaction temperature of 55°C, being stable from pH 1.5 to 6.0 and at temperatures from 20 to 45°C. No activity was detected above pH 6.5 or above 65°C. The molecular weight of 90,000 was estimated by gel filtration and the enzyme had an isoelectric point of 7.0. The enzyme hydrolyzed aryl-β-glycosides and β-linked disaccharides.     

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.     

Purification and some properties of cellulose 1,4-β-cellobiosidase from a strain of Penicillium sp.

A cellulase was purified from the culture supernatant of a strain of Penicillium sp. The purified enzyme was homogenous on polyacrylamide disc gel electrophoresis. It was a glycoprotein with a molecular weight of 52,000 estimated by gel filtration. The optimum pH was about 4.0 and the optimum temperature was 60°C. The enzyme was stable in the pH range of 3.0–10.0 at 6°C for 48 h and on heating at 60°C for 10 min. The activity of the enzyme toward Avicel was about 3 times higher than toward carboxymethyl cellulose. The enzyme showed a low activity for cotton, newspaper, filter paper and cellulose powder. The main product from Avicel was cellobiose, with a trace of glucose.     

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.     

One-pot production of d-allulose from inulin by a novel identified thermostable exoinulinase from Aspergillus piperis and Dorea sp. d-allulose 3-epimerase

Inulin has been widely used as a cheap bioresource for producing many valuable products by enzymatic hydrolysis or microbial fermentation, such as high-fructose syrup and fructooligosaccharides. In this work, a one-pot two-enzyme reaction system was developed to produce d-allulose from inulin using A. piperis exoinulinase and Dorea sp. d-Allulose 3-epimerase. The exoinulinase that was identified from Aspergillus piperis CBS 112811 was cloned and intracellularly expressed in Escherichia coli. The enzyme displayed the maximal activity as 3750 U mg⁻¹ at pH 6.0 and 55 °C. For the effects of different cations, Mn²⁺ simulated the enzyme activity by 41 %. When 10 g L⁻¹ inulin was hydrolyzed by A. piperis exoinulinase, the conversion rate reached 98 % within 6 h. Furthermore, the optimum pH, temperature and the ratio of the two enzymes loaded for one-pot reaction were measured to be pH 6.0, 60 °C and 15/15 U mL⁻¹, respectively. The conversion rate of inulin to d-allulose reached 23.3 % after reaction for 4 h with 10 g L⁻¹ inulin. When adding 100 g L⁻¹ as a substrate, 21.4 g L⁻¹ d-allulose was produced using the two-enzyme system.     

Immobilization of luciferase from the firefly Luciola mingrelica — Catalytic properties and stability of the immobilized enzyme

Firefly (Luciola mingrelica) luciferase [Photinus luciferin 4-monooxygenase (ATP-hydrolysing); Photinus luciferin: oxygen 4-oxidoreductase (decarboxylating, ATP-hydrolysing), EC 1.13.12.7] has been immobilized on albumin and polyacrylamide gel, on AH-, CH- and CNBr-Sepharose 4B as well as on Ultragel, Ultradex and cellophane film activated by cyanogen bromide. Only immobilization on cyanogen bromide-activated polysaccharide carriers resulted in highly active immobilized luciferase. Kinetic properties of immobilized luciferase hardly differed from those of the soluble enzyme. The inactivation rate constants of soluble and immobilized luciferase were measured at pH 5.5–9.0 and 25°C as well as at pH 7.8 and 20–40°C. The ΔH^≠ and ΔS^≠ values for inactivation of soluble and immobilized luciferases were obtained. A 1000-fold stabilization effect was noted for the luciferase immobilized on CNBr-Sepharose 4B at pH 7.5 and 25°C. A stabilization mechanism for the immobilized luciferase is discussed.     

毛壳霉内切菊粉酶的纯化与性质

毛壳霉 (Chaetomiumsp .)C34发酵液经硫酸铵分级沉淀、DEAE 纤维素 11离子交换层析、Q SepharoseFastFlow离子交换层析、SephacrylS 2 0 0凝胶过滤、PhenolSepharoseTM HP疏水层析 ,得到电泳纯的内切菊粉酶组分 ,纯化倍数为 30 8倍 ,活力回收率为 7 7%。用SDS PAGE测得该酶亚基的分子量为 6 6kD。菊粉酶的最适pH为 6 0 ,最适温度为 5 0～ 5 5℃。菊粉酶在 5 0℃以下 ,pH5 0～ 8 0时较稳定。Cu2 完全抑制酶的活性 ,Mn2 、Zn2 、Fe2 、EDTA以及NBS(N bromosuccinimide ,N 溴代丁二酰亚胺 )对该酶有很强的抑制作用。该酶对菊粉有较强底物专一性 ,产物主要为低聚果糖 ,也可作用于蔗糖 ,I S值为 2 0。以菊粉为底物时 ,Km 为 0 199mmol L ,Vmax为 115 μmol (mg·min)。     

Characterization of a mutant glucose isomerase from <Emphasis Type="Italic">Thermoanaerobacterium saccharolyticum</Emphasis>

A series of site-directed mutant glucose isomerase at tryptophan 139 from Thermoanaerobacterium saccharolyticum strain B6A were purified to gel electrophoretic homogeneity, and the biochemical properties were determined. W139F mutation is the most efficient mutant derivative with a tenfold increase in its catalytic efficiency toward glucose compared with the native GI. With a maximal activity at 80 °C of 59.58 U/mg on glucose, this mutant derivative is the most active type ever reported. The enzyme activity was maximal at 90 °C and like other glucose isomerase, this mutant enzyme required Co²⁺ or Mg²⁺ for enzyme activity and thermal stability (stable for 20 h at 80 °C in the absence of substrate). Its optimum pH was around 7.0, and it had 86 % of its maximum activity at pH 6.0 incubated for 12 h at 60 °C. This enzyme was determined as thermostable and weak-acid stable. These findings indicated that the mutant GI W139F from T. saccharolyticum strain B6A is appropriate for use as a potential candidate for high-fructose corn syrup producing enzyme.     

Inulinase ofDebaryomyces cantarellii

Debaryomyces cantarellii excretes into a buffered medium an inulinase of β-fructofuranosidase type, its synthesis being induced by inulin. The enzyme has a pH optimum at 4 and its optimum temperature is 50°C. ItsK _m for inulin is 15mm.