Increased levansucrase production by a genetically modified Acetobacter diazotrophicus strain in shaking batch cultures

Acetobacter diazotrophicus levansucrase (LsdA) is a potential new candidate enzyme for kestose production from sucrose. Culture conditions for maximal LsdA yield were investigated. Variations in the medium pH had the most significant influence on LsdA production. The highest yield (32 mg l⁻¹) was achieved at an initial pH of 8·0, although optimal growth occurred under acidic conditions. The introduction of extrachromosomal copies of the levansucrase gene increased the enzyme yield to 72 mg l⁻¹. In the genetically modified A. diazotrophicus strain, levansucrase represented more than 95% of total secreted proteins showing an overall activity of 189 units ml⁻¹.     

Structural analysis and optimised production of fructo- oligosaccharides by levansucrase from Acetobacter diazotrophicus SRT4

Major fructo-oligosaccharides (FOS) produced by levansucrase (EC 2.4.1.10) from Acetobacter diazotrophicus SRT4 were characterised as 1-kestose and nystose by acid hydrolysis and 13C-NMR spectroscopy. The highest yields of 1-kestose (481 mM; 241 g/l) and nystose (81 mM; 54 g/l) were achieved at initial sucrose concentration of 1754 mM (600 g/l), pH 5.5 and 40°C. The synthesized FOS reached 50% (w/w) of total sugars in the reaction mixture, with a conversion efficiency over 70% (w/w) based on the amount of sucrose converted to 1-kestose.     

Sugarcane molasses and yeast powder used in the Fructooligosaccharides production by Aspergillus japonicus-FCL 119T and Aspergillus niger ATCC 20611

Different concentrations of sucrose (3–25% w/v) and peptone (2–5% w/v) were studied in the formulation of media during the cultivation of Aspergillus japonicus-FCL 119T and Aspergillus niger ATCC 20611. Moreover, cane molasses (3.5–17.5% w/v total sugar) and yeast powder (1.5–5% w/v) were used as alternative nutrients for both strains’ cultivation. These media were formulated for analysis of cellular growth, β-Fructosyltransferase and Fructooligosaccharides (FOS) production. Transfructosylating activity (U _t ) and FOS production were analyzed by HPLC. The highest enzyme production by both the strains was 3% (w/v) sucrose and 3% (w/v) peptone, or 3.5% (w/v) total sugars present in cane molasses and 1.5% (w/v) yeast powder. Cane molasses and yeast powder were as good as sucrose and peptone in the enzyme and FOS (around 60% w/w) production by studied strains.     

Characterization of a beta-fructofuranosidase from Schwanniomyces occidentalis with transfructosylating activity yielding the prebiotic 6-kestose

beta-Fructofuranosidases are powerful tools in industrial biotechnology. We have characterized an extracellular beta-fructofuranosidase from the yeast Schwanniomyces occidentalis. The enzyme shows broad substrate specificity, hydrolyzing sucrose, 1-kestose, nystose and raffinose, with different catalytic efficiencies (k(cat)/K(m)). Although the main reaction catalysed by this enzyme is sucrose hydrolysis, it also produces two fructooligosaccharides (FOS) by transfructosylation. A combination of (1)H, (13)C and 2D-NMR techniques shows that the major product is the prebiotic trisaccharide 6-kestose. The 6-kestose yield obtained with this beta-fructofuranosidase is, to our concern, higher than those reported with other 6-kestose-producing enzymes, both at the kinetic maximum (76gl(-1)) and at reaction equilibrium (44gl(-1)). The total FOS production in the kinetic maximum was 101gl(-1), which corresponded to 16.4% (w/w) referred to the total carbohydrates in the reaction mixture.     

游离及固定化果糖基转移酶部分酶学性质的比较研究

 从诱变、筛选的米曲霉GX0 0 10菌株所产生的果糖基转移酶 ,经过纯化和固定化操作分别制备游离酶和固定化酶 ,对两者的酶学性质进行了比较研究 .结果表明 ,两者在蔗糖转化为蔗果低聚糖的酶促反应中 ,最适pH为 5 5,在pH5 0～ 7 5之间酶活性相对稳定 .游离酶和固定化酶的适宜温度范围分别是 4 5～ 52℃和 4 0～ 55℃ .在 55℃保温 60min ,酶活性保存率分别是 61 6%和 87 5% .固定化酶的热稳定性提高 .0 1mmol LHg2 +和 1mmol LAg+能完全抑制游离酶的活性 ,但只能部分抑制固定化酶的活性 ,1mmol L的Ti2 +能完全抑制两者的活性 .以蔗糖为底物时 ,游离酶的米氏常数Km=2 15mmol L ,而固定化酶Km =386mmol L .游离酶只能使用一次 ,固定化酶反复使用 54次后 ,剩余活力为 55 2 % .用 55% (W V)蔗糖溶液与固定化酶在pH5 0 ,4 6℃下作用 12h ,可获得61 5% (总低聚糖 总糖 )产物 ,其中蔗果五糖含量达到 7 2 % .     

High levan accumulation in transgenic tobacco plants expressing the Gluconacetobacter diazotrophicus levansucrase gene

Bacterial levansucrase (EC 2.4.1.10) converts sucrose into non-linear levan consisting of long β(2,6)-linked fructosyl chains with β(2,1) branches. Bacterial levan has wide food and non-food applications, but its production in industrial reactors is costly and low yielding. Here, we report the constitutive expression of Gluconacetobacter diazotrophicus levansucrase (LsdA) fused to the vacuolar targeting pre-pro-peptide of onion sucrose:sucrose 1-fructosyltransferase (1-SST) in tobacco, a crop that does not naturally produce fructans. In the transgenic plants, levan with degree of polymerization above 10⁴ fructosyl units was detected in leaves, stem, root, and flowers, but not in seeds. High levan accumulation in leaves led to gradual phenotypic alterations that increased with plant age through the flowering stage. In the transgenic lines, the fructan content in mature leaves varied from 10 to 70% of total dry weight. No oligofructans were stored in the plant organs, although the in vitro reaction of transgenic LsdA with sucrose yielded β(2,1)-linked FOS and levan. Transgenic lines with levan representing up to 30 mg g⁻¹ of fresh leaf weight produced viable seeds and the polymer accumulation remained stable in the tested T1 and T2 progenies. The lsdA-expressing tobacco represents an alternative source of highly polymerized levan.     

Expression of an Aspergillus niger glucose oxidase in saccharomyces cerevisiae and its use to optimize fructo-oligosaccharides synthesis

Fructo-oligosaccharides (FOS) represent the most abundantly supplied and utilized group of nondigestible oligosaccharides as food ingredients. These prebiotics can be produced from sucrose using the transglycosylating activity of beta-fructofuranosidases (EC 3.2.1.26) at high concentrations of the starting material. The main problem during FOS synthesis is that the activity of the enzyme is inhibited by the glucose generated during the reaction, and therefore the maximum FOS content in commercial products reaches up to 60% on a dry substance basis. The glucose oxidase (gox) gene from Aspergillus niger BT18 was cloned and integrated, as part of an expression cassette, into the ribosomal DNA of a Saccharomyces cerevisiae host strain. One of the recombinant strains with a high copy number of the gox gene and showing a high GOX specific activity was used to produce the enzyme. Addition of the extracellular glucose oxidase to the FOS synthesis reaction helped to remove the glucose generated, avoiding the inhibition of the fungal beta-fructofuranosidase. As a result, a final syrup containing up to 90% of FOS was obtained.     

Kinetics of sucrose conversion to fructo-oligosaccharides using enzyme (invertase) under free condition

The study reports the synthesis of fructo-oligosaccharide (FOS) from sucrose using invertase derived from Saccharomyces cerevisiae. The reaction was conducted in a batch mode under free enzyme condition. Fructo-oligosaccharide formation was detected at a high sucrose concentration of over 200 g/L. The investigation was extended to study the effect of different parameters such as initial sucrose concentration (ISC), pH, and enzyme concentration. A maximum FOS yield of 10 % (dry basis) was observed using 525 g/L of ISC, with 6 U/mL of the enzyme, and pH 5.5 at 40 °C. 1-Kestose was the major product of among different forms of FOS. The FOS yield increased with an increase in sucrose concentration up to 525 g/L, beyond which it started to decrease. However, the maximum FOS yield was not affected by the increasing concentration of the enzyme beyond a certain level (2 U/mL). Furthermore, the activity of enzyme slightly increased with an increase in the pH up to 6, and thereafter it declined. Addition of glucose decreased the FOS yield because of enzyme inhibition. A five-step, ten-parameter model was developed, for which the simulation was performed in COPASI. The results predicted by the model were consistent with the experimental data.     

Structural levansucrase gene (lsdA) constitutes a functional locus conserved in the species Gluconacetobacter diazotrophicus

Levansucrase (EC 2.4.1.10) was identified as a constitutive exoenzyme in 14 Gluconacetobacter diazotrophicus strains recovered from different host plants in diverse geographical regions. The enzyme, consisting of a single 60-kDa polypeptide, hydrolysed sucrose to synthesise oligofructans and levan. Sugar-cane-associated strains of the most abundant genotype (electrophoretic type 1) showed maximal values of levansucrase production. These values were three-fold higher than those of the isolates recovered from coffee plants. Restriction fragment length polymorphism analysis revealed a high degree of conservation of the levansucrase locus (IsdA) among the 14 strains under study, which represented 11 different G. diazotrophicus genotypes. Targeted disruption of the lsdA gene in four representative strains abolished their ability to grow on sucrose, indicating that the endophytic species G. diazotrophicus utilises plant sucrose via levansucrase.     

Synthesis of Fructooligosaccharides by IslA4, a truncated inulosucrase from Leuconostoc citreum

Background

IslA4 is a truncated single domain protein derived from the inulosucrase IslA, which is a multidomain fructosyltransferase produced by Leuconostoc citreum. IslA4 can synthesize high molecular weight inulin from sucrose, with a residual sucrose hydrolytic activity. IslA4 has been reported to retain the product specificity of the multidomain enzyme.

Results

Screening experiments to evaluate the influence of the reactions conditions, especially the sucrose and enzyme concentrations, on IslA4 product specificity revealed that high sucrose concentrations shifted the specificity of the reaction towards fructooligosaccharides (FOS) synthesis, which almost eliminated inulin synthesis and led to a considerable reduction in sucrose hydrolysis. Reactions with low IslA4 activity and a high sucrose activity allowed for high levels of FOS synthesis, where 70% sucrose was used for transfer reactions, with 65% corresponding to transfructosylation for the synthesis of FOS.

Conclusions

Domain truncation together with the selection of the appropriate reaction conditions resulted in the synthesis of various FOS, which were produced as the main transferase products of inulosucrase (IslA4). These results therefore demonstrate that bacterial fructosyltransferase could be used for the synthesis of inulin-type FOS.     

Biochemical characterization of a β-fructofuranosidase from Rhodotorula dairenensis with transfructosylating activity

An extracellular β-fructofuranosidase from the yeast Rhodotorula dairenensis was characterized biochemically. The enzyme molecular mass was estimated to be 680 kDa by analytical gel filtration and 172 kDa by sodium dodecyl sulfate-polyacrylamide gel electrophoresis, of which the N -linked carbohydrate accounts for 16% of the total mass. It displays optimum activity at pH 5 and 55–60 °C. The enzyme shows broad substrate specificity, hydrolyzing sucrose, 1-kestose, nystose, leucrose, raffinose and inulin. Although the main reaction catalyzed by this enzyme is sucrose hydrolysis, it also exhibits transfructosylating activity that, unlike other microbial β-fructofuranosidases, produces a varied type of prebiotic fructooligosaccharides containing β-(2→1)- and β-(2→6)-linked fructose oligomers. The maximum concentration of fructooligosaccharides was reached at 75% sucrose conversion and it was 87.9 g L⁻¹. The 17.0% (w/w) referred to the total amount of sugars in the reaction mixture. At this point, the amounts of 6-kestose, neokestose, 1-kestose and tetrasaccharides were 68.9, 10.6, 2.6 and 12.7 g L⁻¹, respectively.     

Continuous production of high-content fructooligosaccharides by a complex cell system

A complex biocatalyst system with a bioreactor equipped with a microfiltration (MF) module was employed to produce high-content fructooligosaccharides (FOS) in a continuous process initiated by a batch process. The system used mycelia of Aspergillus japonicus CCRC 93007 or Aureobasidium pullulans ATCC 9348 with beta-fructofuranosidase activity and Gluconobacter oxydans ATCC 23771 with glucose dehydrogenase activity. Calcium carbonate slurry was used to control pH to 5.5, and gluconic acid in the reaction mixture was precipitated as calcium gluconate. Sucrose solution with an optimum concentration of 30% (w/v) was employed as feed for the complex cell system, and high-content FOS was discharged continuously from a MF module. The complex cell system was run at 30 degrees C with an aeration rate of 5 vvm and produced more than 80% FOS with the remainder being 5-7% glucose and 8-10% sucrose on a dry weight basis, plus a small amount of calcium gluconate. The system worked for a 7-day continuous production process with a dilution rate of 0.04 h(-1), and the volumetric productivity for total FOS was more than 160 g L(-1) h(-1).     

Cloning,expression and functional validation of a β-fructofuranosidase from Lactobacillus plantarum

Fructooligosaccharides (FOS) are prebiotics that selectively stimulate the growth and activity of lactobacilli and bifidobacteria. These strains metabolize FOS with endogenous β-fructofuranosidase. In this study, a β-fructofuranosidase gene from Lactobacillus plantarum ST-III designated sacA was cloned into Escherichia coli, and the properties of the recombinant protein (SacA) were examined. The sacA gene encodes a peptide of 501 amino acids with a predicted molecular weight of 56.7 kDa. Sequence alignment revealed the presence of three highly conserved motifs, NDPNG, RDP and EC, indicating that the enzyme belongs to glycoside hydrolase family 32. The predicted three-dimensional structure of the SacA enzyme was similar to β-fructofuranosidases of bifidobacteria, such that it contained a five-blade β-propeller module and a β-sandwich domain with one additional N-terminal α-helix. The optimal reaction temperature and pH of the enzyme were 37 °C and 6.0, respectively. Substrate hydrolysis and kinetic parameters demonstrated that β-fructofuranosidase from L. plantarum ST-III liberated fructosyl residues from the non-reducing terminus of fructans, such as sucrose, FOS, levan or inulin, and FOS was the preferred substrate. The expression of the sacA gene in a non-FOS-fermenting strain, Lactobacillus rhamnosus GG, enabled the recombinant strain to metabolize FOS and sucrose.     

Characterization of a novel fructosyltransferase from Lactobacillus reuteri that synthesizes high-molecular-weight inulin and inulin oligosaccharides

Fructosyltransferase (FTF) enzymes produce fructose polymers (fructans) from sucrose. Here, we report the isolation and characterization of an FTF-encoding gene from Lactobacillus reuteri strain 121. A C-terminally truncated version of the ftf gene was successfully expressed in Escherichia coli. When incubated with sucrose, the purified recombinant FTF enzyme produced large amounts of fructo-oligosaccharides (FOS) with beta-(2-->1)-linked fructosyl units, plus a high-molecular-weight fructan polymer (>10(7)) with beta-(2-->1) linkages (an inulin). FOS, but not inulin, was found in supernatants of L. reuteri strain 121 cultures grown on medium containing sucrose. Bacterial inulin production has been reported for only Streptococcus mutans strains. FOS production has been reported for a few bacterial strains. This paper reports the first-time isolation and molecular characterization of (i) a Lactobacillus ftf gene, (ii) an inulosucrase associated with a generally regarded as safe bacterium, (iii) an FTF enzyme synthesizing both a high molecular weight inulin and FOS, and (iv) an FTF protein containing a cell wall-anchoring LPXTG motif. The biological relevance and potential health benefits of an inulosucrase associated with an L. reuteri strain remain to be established.     

Production of a novel transfructosylating enzyme from Bacillus macerans EG-6

A new bacterium producing a novel transfructosylating enzyme was isolated from soil and designated as Bacillus macerans EG-6. Various culture conditions for enzyme production were optimized in a flask culture. 1% (w/v) sucrose as a carbon source and a mixed nitrogen source (1% yeast extract, 1% polypeptone, and 0.5% ammonium chloride) gave the best enzyme production. Addition of phosphate and magnesium ion into the medium enhanced the enzyme yield. Optimum culture pH and temperature were 7.0 and 37?°C, respectively. Under optimal culture conditions, transfructosylating enzyme was rapidly produced in the early growth period, thereafter invertase activity was predominant as the culture proceeded. Using the culture filtrate, production of fructooligosaccharides from sucrose was preliminarily carried out. In a low sucrose concentration (200?g/l), transfructosylating activity competes with invertase activity in sucrose utilization. Subsequently, low fructooligosaccharide yield (20%) was achieved due to liberation of high amounts of glucose and fructose. The best oligosaccharide yield (43%) was achieved when 500?g/l sucrose was utilized.     

Production of fructooligosaccharides by crude enzyme preparations of β-fructofuranosidase from <Emphasis Type="Italic">Aureobasidium pullulans</Emphasis>

Fructooligosaccharides (FOS) were produced from sucrose by using crude enzyme preparations of β-fructofuranosidases (FFases) obtained from sucrose-cultured cells of Aureobasidium pullulans DSM 2404. When the preparation mainly consisted of FFase I, that has high transfructosylating activity, the FOS yield was 62%. When the reaction was carried out with additional commercial glucose isomerase (GI) at an activity ratio of FFase and GI of 1:2, the maximum FOS yield reached 69%. This value was higher than those obtained previously using other Aureobasidium spp. (53–59%).     

Aspergillus niger inulinase immobilized in polyurethane foam and treated in pressurized LPG: A potential catalyst for enzymatic synthesis of fructooligosaccharides

Inulinase from Aspergillus niger was immobilized in polyurethane foam (PU). Immobilized catalyst was treated in pressurized liquefied petroleum gas (LPG) system. This biocatalyst was used in the fructooligosaccharide production using sucrose as substrate in aqueous system. The main objective of this study was to evaluate the reaction yield and productivity by using polyurethane foam as a low-cost support for enzyme immobilization in an alternative processes for fructooligosaccharide production in pressurized LPG system with potential for industrial application. The total FOS concentration obtained were 31% as a result of sucrose concentration reduction, and formation of FOS long chain (GF3 and GF4) from kestose (GF2). FOS concentrations of 5%, 22%, and 3% were obtained for GF2, GF3, and GF4, respectively. The methodology suggested in this research work, enzyme immobilization in a low-cost support, and treatment in LPG, showed potential technology for fructooligosaccharide synthesis.     

Immobilization of <Emphasis Type="Bold">β</Emphasis>-fructofuranosidase from <Emphasis Type="Italic">Aspergillus japonicus</Emphasis> on chitosan using tris(hydroxymethyl)phosphine or glutaraldehyde as a coupling agent

A partially purified -fructofuranosidase from Aspergillus japonicus was covalently immobilized on to chitosan beads using either glutaraldehyde or tris(hydroxymethyl)phosphine (THP) as a coupling agent. Compared with the glutaraldehyde-immobilized and the free enzyme, the THP-immobilized enzyme had the highest thermal stability with 78% activity retained after 12 days at 37 ° C. The THP-immobilized enzyme also had higher reusability than that immobilized by glutaraldehyde, 75% activity was retained after 11 batches (or 11 days) at 37° C for the THP immobilized enzyme system. Less yield (48%) of fructooligosaccharides (FOS) were produced by the THP-immobilized enzyme compared with the free enzyme system (58%) from 50 (w/v) sucrose at 50 ° C.