Isomaltose formation by free and immobilized dextransucrase

The acceptor reaction of dextransucrase from Leuconostoc mesenteroides NRRL-B512F with glucose as acceptor is of technical interest for isomaltooligosaccharide (IMOs) synthesis. Different experimental conditions were investigated for free and immobilized enzyme. The data for oligosaccharide formation up to a degree of polymerization 4 were correlated with a model developed earlier, and optimal reaction conditions for immobilized dextransucrase design and application were identified for later continuous application. Furthermore, stability was investigated for free and immobilized enzyme including stabilization by sugars.     

Isomaltose formation by free and immobilized dextransucrase

The acceptor reaction of dextransucrase from Leuconostoc mesenteroides NRRL-B512F with glucose as acceptor is of technical interest for isomaltooligosaccharide (IMOs) synthesis. Different experimental conditions were investigated for free and immobilized enzyme. The data for oligosaccharide formation up to a degree of polymerization 4 were correlated with a model developed earlier, and optimal reaction conditions for immobilized dextransucrase design and application were identified for later continuous application. Furthermore, stability was investigated for free and immobilized enzyme including stabilization by sugars.     

Properties of Leuconostoc mesenteroides B-512FMC constitutive dextransucrase

Leuconostoc mesenteroides B-512FMC, a constitutive mutant for dextransucrase, was grown on glucose, fructose, or sucrose. The amount of cell-associated dextransucrase was about the same for the three sugars at different concentrations (0.6% and 3%). Enzyme produced in glucose medium was adsorbed on Sephadex G-100 and G-200, but much less enzyme was adsorbed when it was produced in sucrose medium. Sephadex adsorption decreased when the glucose-produced enzyme was preincubated with dextrans of molecular size greater than 10 kDa. The release of dextransucrase activity from Sephadex by buffer (20 mM acetate, pH 5.2) was the highest at 28°–30°C. The addition of dextran to the enzyme stimulated dextran synthesis but had very little effect on the temperature or pH stability. Dextransucrase purified by ammonium sulfate precipitation, hydroxyapatite chromatography, and Sephadex G-200 adsorption did not contain any carbohydrate, and it synthesized dextran, showing that primers are not necessary to initiate dextran synthesis. The purified enzyme had a molecular size of 184 kDa on SDS-PAGE. On standing at 4°C for 30 days, the native enzyme was dissociated into three inactive proteins of 65, 62, and 57 kDa. However, two protein bands of 63 and 59 kDa were obtained on SDS-PAGE after heat denaturation of the 184-kDa active enzyme at 100°C. The amount of 63-kDa protein was about twice that of 59-kDa protein. The native enzyme is believed to be a trimer of two 63-kDa and one 59-kDa monomers.     

Co-immobilization of dextransucrase and dextranase for the facilitated synthesis of isomalto-oligosaccharides: Preparation, characterization and modeling

Co-Immobilization of dextransucrase (DS) and dextranase (DN) into calcium alginate includes the co-entrapment of soluble DS and adsorbed DN. DS converts sucrose into dextran, which is the substrate for DN, so that isomalto-oligosaccharides (IMOs) are follow-up products of dextran hydrolysis. The boundary conditions for the successful preparation are investigated with respect to choice of DN adsorbate, surface modifications using blotting agents and optimal enzyme activity ratios. Further, repetitive batch experiments suggest the selection of medium activity ratios for continuous use (0.3 U(DN)U(-1) (DS), e.g.). Product formation at various cosubstrate:substrate concentrations as well as at different DN:DS ratios are discussed. Moreover, the complexity of the bi-enzymatic system can be reduced considering the molar ratios of cosubstrate:substrate (glucose:sucrose). Based on these factors, a mechanistic kinetic model is developed, which distinguishes the corresponding contributions of the two enzymes upon overall product formation. In general, at low glucose:sucrose ratios isomaltose synthesis is featured primarily by DN action. Yet with increasing amounts of glucose both the quantity and quality of DN substrate changes, so that its contribution to product formation decreases in an exponential manner; still the overall product yield continuously increases due to enhanced DS contribution.     

Reactor optimization for alpha-1,2 glucooligosaccharide synthesis by immobilized dextransucrase

The immobilization of dextransucrase in Ca-alginate beads relies on the close association between dextran polymer and dextransucrase. However, high amounts of dextran in the enzyme preparation drastically limit the specific activity of the immobilized enzyme (4 U/mL of alginate beads). Moreover, even in the absence of diffusion limitation at the batch conditions used, the enzyme behavior is modified by entrapment so that the dextran yield increases and the alpha-1,2 glucooligosaccharides (GOS) are produced with a lower yield (46.6% instead of 56.7%) and have a lower mean degree of polymerization than with the free dextransucrase. When the immobilized catalyst is used in a continuous reaction, the reactor flow rate necessary to obtain high conversion of the substrates is very low, leading to external diffusion resistance. As a result, dextran synthesis is even higher than in the batch reaction, and its accumulation within the alginate beads limits the operational stability of the catalyst and decreases glucooligosaccharide yield and productivity. This effect can be limited by using reactor columns with length to diameter ratio > or =20, and by optimizing the substrate concentrations in the feed solution: the best productivity obtained was 3.74 g. U(-1). h(-1), with an alpha-1,2 GOS yield of 36%.     

重组大肠杆菌右旋糖酐蔗糖酶的表达条件优化

通过设计正交实验,考察了培养基中各组分及其浓度对右旋糖酐蔗糖酶工程菌Escherichia coli BL21(DE3)/pET28-dexYG诱导产酶结果的影响。在获得最佳培养条件的基础上,考察温度、蔗糖浓度和pH值对右旋糖酐产量的影响。结果表明:菌浓OD600达到2.0时,加入异丙基硫代-β-D-呋喃半乳糖苷(IPTG)至0.25mmol/L,25°C诱导培养4h,产酶活力最高,达到110.16U/mL,蔗糖浓度对产量的影响比较显著。研究结果得到高效表达的培养条件,为实现该酶的工业化应用打下了基础。     

Factors affecting alpha,-1,2 glucooligosaccharide synthesis by Leuconostoc mesenteroides NRRL B-1299 dextransucrase

The optimization of alpha-1,2 glucooligosaccharide (GOS) synthesis from maltose and sucrose by Leuconostoc mesenteroides NRRL B-1299 dextransucrase was achieved using experimental design and consecutive analysis of the key parameters. An increase of the pH of the reaction from 5.4 to 6.7 and of the temperature from 25 to 40 degrees C significantly favored alpha-1,2 GOS synthesis, thanks to a significant decrease of the side reactions, i.e., dextran and leucrose synthesis. These positive effects were not sufficient to compensate for the decrease of enzyme stability caused by the use of high pH and temperature. However, the critical parameters were the sucrose to maltose concentration ratio (S/M) and the total sugar concentration (TSC). Alpha1,2 GOS synthesis was favored at high S/M ratios. But using these conditions also led to an increase of side reactions which could be modulated by choosing the appropriate TSC. Finally, with S/M = 4 and TSC = 45% w/v, dextran and leucrose productions were limited and the final alpha-1,2 GOS yield reached 56.7%, the total GOS yield being 88%.     

重组大肠杆菌右旋糖酐蔗糖酶的纯化及其性质

[目的]研究工程菌E.coli BL21(DE3)/pET28-dexYG产右旋糖酐蔗糖酶的纯化和酶学性质.[方法]工程菌经过IPTG诱导后生产含His-tag融合蛋白的右旋糖酐蔗糖酶,通过硫酸铵沉淀、Ni-NTA亲和层析纯化,得到纯度较高的酶蛋白,并对纯酶进行了酶学性质及动力学研究.[结果]经过SDS-PAGE测得该酶的分子量约为170 kDa,与理论推测值基本相同.以蔗糖为底物,酶促反应的最适温度为25～30℃,最适pH值为5.4,动力学常数Km值为10.43 mmol/L;酶活在pH 5.0～8.0较为稳定,在室温(25 ℃)保藏4天仍有59%的酶活力,4℃保存7周酶活力仅下降一半,但在35℃以上失活很快;Ca2 对催化作用有较大的促进,Mg2 有微弱的促进作用,K 对催化反应无影响,Cu2 的抑制作用最强.其他试剂对重组酶的活性有不同程度的影响,其中SDS抑制作用很强.[结论]研究为重组右旋糖酐蔗糖酶纯酶的获取、得到稳定性好、活性高的酶反应体系及利用该酶进行催化反应和工业化应用提供了重要参数.     

Investigation of production of dextran and dextransucrase by Leuconostoc mesenteroides immobilized within porous stainless steel

Cells of Leuconostoc mesenteroides were immobilized within porus, stainless-steel (SS) supports and used for dextransucrase (DS) and dextran production. The pore size of the support significantly affected the dextran yields, which were greatest with average pore sizes of 2-5 mum. All immobilized-cell biocatalysts in porous stainless steel produced higher yields than free cells, with the exception of cells confined in submicrometer pores (0.5 mum). Coating supports of larger pore size (40 and 100 mum) with calcium alginate enhanced the cell-loading capacity of the supports and increased dextran and fructose yields in the cell-free broth. Controlled, fed-batch, DS production (activation), as a step preliminary to dextran production, significantly improved the subsequent dextran and fructose yields and shortened the time required to attain the maximum such yields. Scanning electron microscopy (SEM) of immobilized L. mesenteroides in stainless steel shows an irregular pattern of the microorganism inside the pores of the solid supports. Coating the porous solid supports with a cell-free calcium alginate layer led to an increase in the cell density inside the support. Cell growth inside the coated, porous stainless steel had no distinct growth form. (c) 1992 John Wiley & Sons, Inc.     

基于右旋糖酐蔗糖酶转糖基作用的槲皮素葡萄糖苷的合成研究

右旋糖酐蔗糖酶是一种以蔗糖为唯一底物,将蔗糖分子中D-葡萄糖基催化转移到受体分子上的葡萄糖基转移酶。利用右旋糖酐蔗糖酶的转糖基作用,以蔗糖为葡萄糖糖基供体,槲皮素为糖基受体,对槲皮素糖苷的酶法合成进行了探索。通过对该酶催化反应体系、催化反应条件及产物分析的研究,结果表明：在25℃下,右旋糖酐蔗糖酶能够在30％DMSO-70％乙酸-乙酸钙（0.02 mol/L,pH值5.4）的反应体系中催化合成一种槲皮素葡萄糖苷,在这个反应体系下,以10％的蔗糖作为糖基供体,槲皮素为糖基受体,右旋糖酐蔗糖酶活力为40 U/mL,转速为150 r/min,槲皮素糖苷的转化率最高,可达39.5％。通过质谱分析确定是一种槲皮素单糖苷,分子量为464。该研究结果为黄酮类物质的糖基化修饰奠定了基础。     

Biosynthesis of dextrans with different molecular weights by selecting the concentration of Leuconostoc mesenteroides B-512FMC dextransucrase, the sucrose concentration, and the temperature

Leuconostoc mesenteroides B-512FMC dextransucrase was found to synthesize dextrans of varying molecular weights by selecting the concentrations of dextransucrase and sucrose, as well as the temperature. Four enzyme concentrations (50, 10, 1.0, and 0.1 U/mL), five sucrose concentrations (20, 50, 100, 200 and 1000 mM), and two temperatures (20 °C and 30 °C) were studied. The highest amount of enzyme (50 U/mL), with the lowest concentration of sucrose (20 mM), and the lower temperature of 20 °C gave the lowest number-average molecular weight (MW_n) of 20,630 Da, respectively. As the sucrose concentration was increased, 50 mM, 100 mM, and 200 mM, the MW_n was 49,240 Da, 63,350 Da, and 126,720 Da, respectively. The next enzyme concentration (10 U/mL) gave a similar upward trend, starting at 73,130 Da and ending at 237,870 Da at 20 °C and 130,040 Da and ending at 415,770 Da at 30 °C. The upward trend continued for the 1.0 and 0.1 U/mL enzyme concentrations. An increase in the temperature had the overall effect of increasing the MW_n for each decreasing concentration of enzyme and increasing concentration of sucrose. For 0.1 U/mL and 1000 mM sucrose at 30 °C, the MW_n was 1,645,700 Da. The results of the study show that the molecular weights of the synthesized dextrans were inversely proportional to the concentration of the enzyme and directly proportional to the concentration of sucrose and the temperature.     

High-level production and purification of a fully active recombinant dextransucrase from Leuconostoc mesenteroides NRRL B-512F

Recombinant expression of the dextransucrase dsrS gene by Escherichia coli was optimized to produce 5850 U L(-1) (culture) of DSR-S, corresponding to a 30-fold increase compared with previous studies. Rational deletions of the signal peptide, the beginning of the variable region and the last four repeats of the C-terminal end caused no loss of activity. This new variant successfully purified was remarkably stable. With a k(cat) of 584 s(-1), it is the most efficient recombinant glucansucrase described to date. The synthesized polymer possesses more than 95% of alpha-1,6 links, like the dextran produced by the native enzyme, and innovative gel properties were obtained.     

Synthesis of isomaltooligosaccharides and oligodextrans in a recycle membrane bioreactor by the combined use of dextransucrase and dextranase

A recycle ultrafiltration membrane reactor was used to develop a continuous synthesis process for the production of isomaltooligosaccharides (IMO) from sucrose, using the enzymes dextransucrase and dextranase. A variety of membranes were tested and the parameters affecting reactor stability, productivity, and product molecular weight distribution were investigated. Enzyme inactivation in the reactor was reduced with the use of a non-ionic surfactant but its use had severe adverse effects on the membrane pore size and porosity. During continuous isomaltooligosaccharide synthesis, dextransucrase inactivation was shown to occur as a result of the dextranase activity and it was dependent mainly on the substrate availability in the reactor and the hydrolytic activity of dextranase. Substrate and dextranase concentrations (50-200 mg/mL(-1) and 10-30 U/mL(-1), respectively) affected permeate fluxes, reactor productivity, and product average molecular weight. The oligodextrans and isomaltooligosaccharides formed had molecular weights lower than in batch synthesis reactions but they largely consisted of oligosaccharides with a degree of polymerization (DP) greater than 5, depending on the synthesis conditions. No significant rejection of the sugars formed was shown by the membranes and permeate flux was dependent on tangential flow velocity.     

Entrapment of purified novel dextransucrase obtained from newly isolated Acetobacter tropicalis and its comparative study of kinetic parameters with free enzyme

Abstract

Purified Acetobacter tropicalis dextransucrase was immobilized in different matrices viz. calcium-alginate, κ-carrageenan, agar, agarose and polyacrylamide. Calcium-alginate was proved to be superior to the other matrices for immobilization of dextransucrase enzyme. Standardization of immobilization conditions in calcium-alginate resulted in 99.5% relative activity of dextransucrase. This is the first report with such a large amount of relative activity as compared to the previous reports. The immobilized enzyme retained activity for 11 batch reactions without a decrease in activity which suggested that enzyme can be used repetitively for 11 cycles. The dextransucrase was also characterized, which revealed that enzyme worked best at pH 5.5 and 37?°C for 30?min in both the free as well as immobilized state. Calcium-alginate immobilized dextransucrase of A. tropicalis showed the K_m and V_max values of 29?mM and 5000?U/mg, respectively. Free and immobilized enzyme produced 5.7?mg/mL and 2.6?mg/mL of dextran in 2?L bench scale fermenter under optimum reaction conditions. This immobilization method is very unconventional for purified large molecular weight dextran-free dextransucrase of A. tropicalis as this method is used usually for cells. Such reports on entrapment of purified enzyme are rarely documented.     

Structure modeling and functional analysis of recombinant dextransucrase from Weissella confusa Cab3 expressed in Lactococcus lactis

The dextransucrase gene from Weissella confusa Cab3, having an open reading frame of 4.2?kb coding for 1,402?amino acids, was amplified, cloned, and expressed in Lactococcus lactis. The recombinant dextransucrase, WcCab3-rDSR was expressed as extracellular enzyme in M17 medium with a specific activity of 1.5?U/mg which after purification by PEG-400 fractionation gave 6.1?U/mg resulting in 4-fold purification. WcCab3-rDSR was expressed as soluble and homogeneous protein of molecular mass, approximately, 180?kDa as analyzed by SDS-PAGE. It displayed maximum enzyme activity at 35°C at pH 5.0 in 50?mM sodium acetate buffer. WcCab3-rDSR gave K_m of 6.2?mM and V_m of 6.3?µmol/min/mg. The characterization of dextran synthesized by WcCab3-rDSR by Fourier transform infrared and nuclear magnetic resonance spectroscopic analyses revealed the structural similarities with the dextran produced by the native dextransucrase. The modeled structure of WcCab3-rDSR using the crystal structures of dextransucrase from Lactobacillus reuteri (protein data bank, PDB id: 3HZ3) and Streptococcus mutans (PDB id: 3AIB) as templates depicted the presence of different domains such as A, B, C, IV, and V. The domains A and B are circularly permuted in nature having (β/α)₈ triose phosphate isomerase-barrel fold making the catalytic core of WcCab3-rDSR. The structure superposition and multiple sequence alignment analyses of WcCab3-rDSR with available structures of enzymes from family 70 GH suggested that the amino acid residue Asp510 acts as a nucleophile, Glu548 acts as a catalytic acid/base, whereas Asp621 acts as a transition-state stabilizer and these residues are found to be conserved within the family.     

One-step synthesis of isomalto-oligosaccharide syrups and dextrans of controlled size using engineered dextransucrase

Isomalto-oligosaccharides and dextrans of controlled molecular weight of about 10 and 40 kDa were produced using a simple one-step process using engineered L. mesenteroides NRRL B-512F dextransucrase variants. Isomalto-oligosaccharides were produced in a 58% yield by the acceptor reaction with glucose, and reached a degree of polymerization of at least 27 glucosyl units. Reaction conditions for optimal synthesis of dextrans of controlled molecular weight were defined, in respect of initial sucrose concentration and reaction temperature. Thus, we achieved synthesis with impressive yields of 69 and 75% for the 40 and 10 kDa dextran species, respectively. These two dextran sizes are particularly suitable for clinical applications, and are of great industrial demand. Compared with the traditional processes based on chemical hydrolysis and fractionation, which achieve only low yields, the new enzymatic methods offer improvement in quantity, quality and efficiency.     

Production and secretion of recombinant Leuconostoc mesenteroides dextransucrase DsrS in Bacillus megaterium

Leuconostoc mesenteroides dextransucrase DsrS was recombinantly produced in Bacillus megaterium and exported into the growth medium. For this purpose a plasmid-based xylose-inducible gene expression system was optimized via introduction of a multiple cloning site and an encoded optimal B. megaterium ribosome binding site. A cre mediating glucose-dependent catabolite repression was removed. Recombinant DsrS was found in the cytoplasm and exported via its native leader sequence into the growth medium. Elimination of the extracellular protease NprM increased extracellular DsrS concentrations by a factor of 4 and stabilized the recombinant protein for up to 12 h. Cultivation in a semi-defined medium resulted in a further doubling of extracellular DsrS concentration up to an activity of 65 Units/L. To develop an industrial process a high cell density cultivation of B. megaterium was established yielding cell dry weights of up to 80 g/L. After induction of dsrS expression high specific (362 Units/g) and volumetric (28,600 Units/L) activities of dextran free DsrS were measured. However, using high cell density cultivation, most DsrS was found cell-associated indicating current limitations of the production process. A protease accessibility assay identified the major limitation of DsrS production at the level of protein folding. Intracellular misfolding of DsrS hampered DsrS export via the SEC pathway at high cell densities. The subsequent use of a semi-defined mineral medium and the induction of DsrS production at lower cell densities increased protein export efficiency remarkably, but also led to extracellular DsrS aggregation. Further optimization strategies for the production of recombinant DsrS in B. megaterium are discussed.     

One-step synthesis of isomalto-oligosaccharide syrups and dextrans of controlled size using engineered dextransucrase

Isomalto-oligosaccharides and dextrans of controlled molecular weight of about 10 and 40 kDa were produced using a simple one-step process using engineered L. mesenteroides NRRL B-512F dextransucrase variants. Isomalto-oligosaccharides were produced in a 58% yield by the acceptor reaction with glucose, and reached a degree of polymerization of at least 27 glucosyl units. Reaction conditions for optimal synthesis of dextrans of controlled molecular weight were defined, in respect of initial sucrose concentration and reaction temperature. Thus, we achieved synthesis with impressive yields of 69 and 75% for the 40 and 10 kDa dextran species, respectively. These two dextran sizes are particularly suitable for clinical applications, and are of great industrial demand. Compared with the traditional processes based on chemical hydrolysis and fractionation, which achieve only low yields, the new enzymatic methods offer improvement in quantity, quality and efficiency.     

An overview of purification methods of glycoside hydrolase family 70 dextransucrase

The enzyme dextransucrase (sucrose:1, 6-α-D-glucan 6-α-glucosyltransferase, EC 2.4.1.5) catalyses the synthesis of exopolysaccharide, dextran from sucrose. This class of polysaccharide has been extensively exploited in pharmaceutical industry as blood volume expander, as stabiliser in food industry and as a chromatographic medium in fine chemical industry because of their nonionic nature and stability. Majority of the dextrans are synthesized from sucrose by dextransucrase secreted mainly by bacteria belonging to genera Leuconostoc, Streptococcus and Lactobacillus. Bulk of the information on purification of extracellular dextransucrase has been generated from Leuconostoc species. Various methods such as precipitation by ammonium sulphate, ethanol or polyethylene glycol, phase partitioning, ultrafiltration and chromatography have been used to purify the enzyme. Purification of dextransucrase is rendered difficult by the presence of viscous dextran in the medium. However, processes like ultra-filtration, salt and PEG precipitation, chromatography and phase partitioning have been standardized and successfully used for higher scale purification of the enzyme. A recombinant dextransucrase from Leuconostoc mesenteroides B-512F with a histidine tag has been expressed in E. coli cells and purifi ed by immobilized metal ion chromatography. This review reports the available information on purifi cation methods of dextransucrase from Leuconostoc mesenteroides strains.