Continuous D-tagatose production by immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

D-Tagatose was continuously produced using thermostable L-arabinose isomerase immobilized in alginate with D-galactose solution in a packed-bed bioreactor. Bead size, L/D (length/diameter) of reactor, dilution rate, total loaded enzyme amount, and substrate concentration were found to be optimal at 0.8 mm, 520/7 mm, 0.375 h(-1), 5.65 units, and 300 g/L, respectively. Under these conditions, the bioreactor produced about 145 g/L tagatose with an average productivity of 54 g tagatose/L x h and an average conversion yield of 48% (w/w). Operational stability of the immobilized enzyme was demonstrated, with a tagatose production half-life of 24 days.     

Bioconversion of D-galactose to D-tagatose: continuous packed bed reaction with an immobilized thermostable L-arabinose isomerase and efficient purification by selective microbial degradation

The continuous enzymatic conversion of D-galactose to D-tagatose with an immobilized thermostable L-arabinose isomerase in packed-bed reactor and a novel method for D-tagatose purification were studied. L-arabinose isomerase from Thermoanaerobacter mathranii (TMAI) was recombinantly overexpressed and immobilized in calcium alginate. The effects of pH and temperature on D-tagatose production reaction catalyzed by free and immobilized TMAI were investigated. The optimal condition for free enzyme was pH 8.0, 60°C, 5 mM MnCl(2). However, that for immobilized enzyme was pH 7.5, 75°C, 5 mM MnCl(2). In addition, the catalytic activity of immobilized enzyme at high temperature and low pH was significantly improved compared with free enzyme. The optimum reaction yield with immobilized TMAI increased by four percentage points to 43.9% compared with that of free TMAI. The highest productivity of 10 g/L h was achieved with the yield of 23.3%. Continuous production was performed at 70°C; after 168 h, the reaction yield was still above 30%. The resultant syrup was then incubated with Saccharomyces cerevisiae L1 cells. The selective degradation of D-galactose was achieved, obtaining D-tagatose with the purity above 95%. The established production and separation methods further potentiate the industrial production of D-tagatose via bioconversion and biopurification processes.     

Characterization of a mutated Geobacillus stearothermophilus L-arabinose isomerase that increases the production rate of D-tagatose

AIMS: Characterization of a mutated Geobacillus stearothermophilus L-arabinose isomerase used to increase the production rate of D-tagatose. METHODS AND RESULTS: A mutated gene was obtained by an error-prone polymerase chain reaction using L-arabinose isomerase gene from G. stearothermophilus as a template and the gene was expressed in Escherichia coli. The expressed mutated L-arabinose isomerase exhibited the change of three amino acids (Met322-->Val, Ser393-->Thr, and Val408-->Ala), compared with the wild-type enzyme and was then purified to homogeneity. The mutated enzyme had a maximum galactose isomerization activity at pH 8.0, 65 degrees C, and 1.0 mM Co2+, while the wild-type enzyme had a maximum activity at pH 8.0, 60 degrees C, and 1.0-mM Mn2+. The mutated L-arabinose isomerase exhibited increases in D-galactose isomerization activity, optimum temperature, catalytic efficiency (kcat/Km) for D-galactose, and the production rate of D-tagatose from D-galactose. CONCLUSIONS: The mutated L-arabinose isomerase from G. stearothermophilus is valuable for the commercial production of D-tagatose. SIGNIFICANCE AND IMPACT OF THE STUDY: This work contributes knowledge on the characterization of a mutated L-arabinose isomerase, and allows an increased production rate for D-tagatose from D-galactose using the mutated enzyme.     

Tagatose production by immobilized recombinant Escherichia coli cells containing Geobacillus stearothermophilus l-arabinose isomerase mutant in a packed-bed bioreactor

Using immobilized recombinant Escherichia coli cells containing Geobacillus stearothermophilus l-arabinose isomerase mutant (Gali 152), we found that the galactose isomerization reaction was maximal at 70 degrees C and pH 7.0. Manganese ion enhanced galactose isomerization to tagatose. The immobilized cells were most stable at 60 degrees C and pH 7.0. The cell and substrate concentrations and dilution rate were optimal at 34 g/L, 300 g/L, and 0.05 h(-1), respectively. Under the optimum conditions, the immobilized cell reactor with Mn2+ produced an average of 59 g/L tagatose with a productivity of 2.9 g/L.h and a conversion yield of 19.5% for the first 20 days. The operational stability of immobilized cells with Mn2+ was demonstrated, and their half-life for tagatose production was 34 days. Tagatose production was compared for free and immobilized enzymes and free and immobilized cells using the same mass of cells. Immobilized cells produced the highest tagatose concentration, indicating that cell immobilization was more efficient for tagatose production than enzyme immobilization.     

High production of D-tagatose by the addition of boric acid

An L-arabinose isomerase mutant enzyme from Geobacillus thermodenitrificans was used to catalyze the isomerization of D-galactose to D-tagatose with boric acid. Maximum production of D-tagatose occurred at pH 8.5-9.0, 60 degrees C, and 0.4 molar ratio of boric acid to D-galactose, and the production increased with increasing enzyme concentration. Under the optimum conditions, the enzyme (10.8 units/mL) converted 300 g/L D-galactose to 230 g/L D-tagatose for 20 h with a yield of 77% (w/w); the production and conversion yield with boric acid were 1.5-fold and 24% higher than without boric acid, respectively. In 24 h, the enzyme produced 370 g/L D-tagatose from 500 g/L D-galactose with boric acid, corresponding to a conversion yield of 74% (w/w) and a production rate of 15.4 g/L.h. The production and yield of D-tagatose obtained in this study are unprecedented.     

Metabolic engineering of Lactobacillus plantarum for production of L-ribulose

L-Ribulose is a rare and expensive sugar that can be used as a precursor for the production of other rare sugars of high market value such as L-ribose. In this work we describe a production process for L-ribulose using L-arabinose, a common component of polymers of lignocellulosic materials, as the starting material. A ribulokinase-deficient mutant of the heterofermentative lactic acid bacterium Lactobacillus plantarum NCIMB8826 was constructed. Expression of araA, which encodes the critical enzyme L-arabinose isomerase, was repressed by high glucose concentrations in batch cultivations. A fed-batch cultivation strategy was therefore used to maximize L-arabinose isomerase production during growth. Resting cells of the ribulokinase-deficient mutant were used for the production of L-ribulose. The isomerization of L-arabinose to L-ribulose was very unfavorable for L-ribulose formation. However, high L-ribulose yields were obtained by complexing the produced L-ribulose with borate. The process for L-ribulose production in borate buffer by resting cells was optimized using central composite designs. The experiment design suggested that the process has an optimal operation point around an L-arabinose concentration of 100 g liter(-1), a borate concentration of 500 mM, and a temperature of 48 degrees C, where the statistical software predicted an initial L-ribulose production rate of 29.1 g liter(-1) h(-1), a best-achievable process productivity of 14.8 g liter(-1) h(-1), and a conversion of L-arabinose to L-ribulose of 0.70 mol mol(-1).     

A feasible enzymatic process for D-tagatose production by an immobilized thermostable L-arabinose isomerase in a packed-bed bioreactor

To develop a feasible enzymatic process for d-tagatose production, a thermostable l-arabinose isomerase, Gali152, was immobilized in alginate, and the galactose isomerization reaction conditions were optimized. The pH and temperature for the maximal galactose isomerization reaction were pH 8.0 and 65 degrees C in the immobilized enzyme system and pH 7.5 and 60 degrees C in the free enzyme system. The presence of manganese ion enhanced galactose isomerization to tagatose in both the free and immobilized enzyme systems. The immobilized enzyme was more stable than the free enzyme at the same pH and temperature. Under stable conditions of pH 8.0 and 60 degrees C, the immobilized enzyme produced 58 g/L of tagatose from 100 g/L galactose in 90 h by batch reaction, whereas the free enzyme produced 37 g/L tagatose due to its lower stability. A packed-bed bioreactor with immobilized Gali152 in alginate beads produced 50 g/L tagatose from 100 g/L galactose in 168 h, with a productivity of 13.3 (g of tagatose)/(L-reactor.h) in continuous mode. The bioreactor produced 230 g/L tagatose from 500 g/L galactose in continuous recycling mode, with a productivity of 9.6 g/(L.h) and a conversion yield of 46%.     

l-Xylose and l-lyxose production from xylitol using Alcaligenes 701B strain and immobilized l-rhamnose isomerase enzyme

Xylitol was used as a raw material for production of l-xylose and l-lyxose using Alcaligenes 701B strain and immobilized l-rhamnose isomerase enzyme. Alcaligenes 701B converted xylitol to l-xylulose with a yield of 34% in the bioreactor. l-Xylulose was converted to l-xylose and l-lyxose using immobilized l-rhamnose isomerase enzyme. The final equilibrium between l-xylulose, l-xylose and l-lyxose was 53:26:21. The enzyme assays indicated that Alcaligenes 701B strain has an NAD-dependent xylitol dehydrogenase enzyme responsible for l-xylulose production. Furthermore, NAD(P)H-dependent l-xylulose reductase enzyme was active during conversion of xylitol to l-xylulose. The highest l-xylulose production rate corresponded with the highest growth rate. The Alcaligenes 701B strain used d-xylose for biomass growth, but xylitol was used only for l-xylulose production during conversion phase.     

A method for the production of D-tagatose using a recombinant Pichia pastoris strain secreting ß-D-galactosidase from Arthrobacter chlorophenolicus and a recombinant L-arabinose isomerase from

ABSTRACT: BACKGROUND: D-Tagatose is a natural monosaccharide which can be used as a low-calorie sugar substitute in food, beverages and pharmaceutical products. It is also currently being tested as an anti-diabetic and obesity control drug. D-Tagatose is a rare sugar, but it can be manufactured by the chemical or enzymatic isomerization of D-galactose obtained by a beta-D-galactosidase-catalyzed hydrolysis of milk sugar lactose and the separation of D-glucose and D-galactose. L-Arabinose isomerases catalyze in vitro the conversion of D-galactose to D-tagatose and are the most promising enzymes for the large-scale production of D-tagatose. RESULTS: In this study, the araA gene from psychrotolerant Antarctic bacterium Arthrobacter sp. 22c was isolated, cloned and expressed in Escherichia coli. The active form of recombinant Arthrobacter sp. 22c L-arabinose isomerase consists of six subunits with a combined molecular weight of approximately 335 kDa. The maximum activity of this enzyme towards D-galactose was determined as occurring at 52[DEGREE SIGN]C; however, it exhibited over 60% of maximum activity at 30[DEGREE SIGN]C. The recombinant Arthrobacter sp. 22c L-arabinose isomerase was optimally active at a broad pH range of 5 to 9. This enzyme is not dependent on divalent metal ions, since it was only marginally activated by Mg2+, Mn2+ or Ca2+ and slightly inhibited by Co2+ or Ni2+. The bioconversion yield of D-galactose to D-tagatose by the purified L-arabinose isomerase reached 30% after 36 h at 50[DEGREE SIGN]C. In this study, a recombinant Pichia pastoris yeast strain secreting beta-D-galactosidase Arthrobacter chlorophenolicus was also constructed. During cultivation of this strain in a whey permeate, lactose was hydrolyzed and D-glucose was metabolized, whereas D-galactose was accumulated in the medium. Moreover, cultivation of the P. pastoris strain secreting beta-D-galactosidase in a whey permeate supplemented with Arthrobacter sp. 22c L-arabinose isomerase resulted in a 90% yield of lactose hydrolysis, the complete utilization of D-glucose and a 30% conversion of D-galactose to D-tagatose. CONCLUSIONS: The method developed for the simultaneous hydrolysis of lactose, utilization of D-glucose and isomerization of D-galactose using a P. pastoris strain secreting beta-D-galactosidase and recombinant L-arabinose isomerase seems to offer an interesting alternative for the production of D-tagatose from lactose-containing feedstock.     

Porins of Pseudomonas fluorescens MFO as fibronectin-binding proteins

Gene araA encoding an L-arabinose isomerase (AraA) from the hyperthermophile, Thermotoga neapolitana 5068 was cloned, sequenced, and expressed in Escherichia coli. The gene encoded a polypeptide of 496 residues with a calculated molecular mass of 56677 Da. The deduced amino acid sequence has 94.8% identical amino acids compared with the residues in a putative L-arabinose isomerase of Thermotoga maritima. The recombinant enzyme expressed in E. coli was purified to homogeneity by heat treatment, ion exchange chromatography and gel filtration. The thermophilic enzyme had a maximum activity of L-arabinose isomerization and D-galactose isomerization at 85 degrees C, and required divalent cations such as Co(2+) and Mn(2+) for its activity and thermostability. The apparent K(m) values of the enzyme for L-arabinose and D-galactose were 116 mM (v(max), 119 micromol min(-1) mg(-1)) and 250 mM (v(max), 14.3 micromol min(-1) mg(-1)), respectively, that were determined in the presence of both 1 mM Co(2+) and 1 mM Mn(2+). A 68% conversion of D-galactose to D-tagatose was obtained using the recombinant enzyme at the isomerization temperature of 80 degrees C.     

Expression of E. coli araBAD operon encoding enzymes for metabolizing L-arabinose in Saccharomyces cerevisiae

The Escherichia coli araBAD operon consists of three genes encoding three enzymes that convert L-arabinose to D-xylulose-5 phosphate. In this paper we report that the genes of the E. coli araBAD operon have been expressed in Saccharomyces cerevisiae using strong promoters from genes encoding S. cerevisiae glycolytic enzymes (pyruvate kinase, phosphoglucose isomerase, and phosphoglycerol kinase). The expression of these cloned genes in yeast was demonstrated by the presence of the active enzymes encoded by these cloned genes and by the presence of the corresponding mRNAs in the new host. The level of expression of L-ribulokinase (araB) and L-ribulose-5-phosphate 4-epimerase (araD) in S. cerevisiae was relatively high, with greater than 70% of the activity of the enzymes in wild type E. coli. On the other hand, the expression of L-arabinose isomerase (araA) reached only 10% of the activity of the same enzyme in wild type E. coli. Nevertheless, S. cerevisiae, bearing the cloned L-arabinose isomerase gene, converted L-arabinose to detectable levels of L-ribulose during fermentation. However, S. cerevisiae bearing all three genes (araA, araB, and araD) was not able to produce detectable amount of ethanol from L-arabinose. We speculate that factors such as pH, temperature, and competitive inhibition could reduce the activity of these enzymes to a lower level during fermentation compared to their activity measured in vitro. Thus, the ethanol produced from L-arabinose by recombinant yeast containing the expressed BAD genes is most likely totally consumed by the cell to maintain viability.     

微生物来源的L-阿拉伯糖异构酶的研究进展及应用前景

L-阿拉伯糖异构酶(L-AI)能分别催化L-阿拉伯糖和D-半乳糖异构为L-核酮糖和D-塔格糖,它是目前生物法生产新型功能性因子D-塔格糖最为有效的酶.近年来,L-AI的结构已被揭晓,其基因已获得克隆、测序和过量表达,经过蛋白质工程改造的L-AI将是未来工业化生产D-塔格糖的主要用酶.本文综述了近年来国外对L-AI的结构与功能、催化机理、酶学性质及应用于D-塔格糖生产方面的研究状况,并展望了其发展前景.     

Development of a selection system for the detection of L-ribose isomerase expressing mutants of <Emphasis Type="Italic">Escherichia coli</Emphasis>

L-Arabinose isomerase (E.C. 5.3.1.14) catalyzes the reversible isomerization between L-arabinose and L-ribulose and is highly selective towards L-arabinose. By using a directed evolution approach, enzyme variants with altered substrate specificity were created and screened in this research. More specifically, the screening was directed towards the identification of isomerase mutants with L-ribose isomerizing activity. Random mutagenesis was performed on the Escherichia coli L-arabinose isomerase gene (araA) by error-prone polymerase chain reaction to construct a mutant library. To enable screening of this library, a selection host was first constructed in which the mutant genes were transformed. In this selection host, the genes encoding for L-ribulokinase and L-ribulose-5-phosphate-4-epimerase were brought to constitutive expression and the gene encoding for the native L-arabinose isomerase was knocked out. L-Ribulokinase and L-ribulose-5-phosphate-4-epimerase are necessary to ensure the channeling of the formed product, L-ribulose, to the pentose phosphate pathway. Hence, the mutant clones could be screened on a minimal medium with L-ribose as the sole carbon source. Through the screening, two first-generation mutants were isolated, which expressed a small amount of L-ribose isomerase activity.     

Production of acrylamide using immobilized cells of<Emphasis Type="Italic">Rhodococcus rhodochrous</Emphasis> M33

The cellsof Rhodococcus rhodochrous M33, which produce a nitrile hydratase enzyme, were immobilized in acrylamide-based polymer gels. The optimum pH and temperature for the activity of nitrile hydratase in both the free and immobilized cells were 7.4 and 45°C, respectively, yet the optinum temperature for acrylamide production by the immobilized cells was 20°C. The nitrile hydratase of the immobilized cells was more stable with acrylamide than that of the free cells. Under optimal conditions, the final acrylamide concentration reached about 400 g/L with a conversion yield of almost 100% after 8 h of reaction when using 150 g/L of immobilized cells corresponding to a 1.91 g-dry cell weight/L. The enzyme activity of the immobilized cells rapidly decreased with repeated use. However, the quality of the acrylamide produced by the immobilized cells was much better than that produced by the free cells in terms of color, salt content, turbidity, and foam formation. The quality of the aqueous acrylamide solution obtained was found to be of commercial use without further purification.     

Bacillus Stearothermophilus IAM 11001 L-阿拉伯糖异构酶在大肠杆菌中的表达、纯化及活性研究

L-阿拉伯糖异构酶是生物法生产新型功能性因子D-塔格糖最为有效的酶。本文获得了一种新型耐热L-阿拉伯糖异构酶的编码基因araA,来源于Bacillus stearothermophilis IAM 11001,经NCBI Blastn分析,与GenBank中Thermus sp. IM6501 araA序列的同源性为95%,并将该新基因提交到GenBank,获得登陆号：EU394214。以pET-22b(+)为载体质粒,E. coli BL21(DE3)为宿主细胞,构建了基因重组菌,IPTG可诱导目的蛋白的过量表达;经亲和层析纯化的重组蛋白样品进行SDS-PAGE电泳分析,约在59 kDa处出现显著的特征蛋白条带;同时对重组L-AI的活性进行了初步研究,全细胞反应24小时D-塔格糖的转化率为39.8%。     

海栖热袍菌葡萄糖异构酶基因xylA的克隆、表达及酶学性质

海栖热袍菌(Thermotoga maritima)是嗜极端高温的厌氧细菌,其产生的葡萄糖异构酶由于其出色的耐热性有着潜在的工业应用价值.由于海栖热袍菌苛刻的培养条件导致其葡萄糖异构酶产量较低.通过PCR方法克隆编码T. maritima MSB8葡萄糖异构酶基因xylA,构建重组质粒pHsh-xylA,转入Escherichia coli JM109,通过热激诱导表达.通过热处理和离子交换层析纯化两步得到电泳纯的酶制品,纯化倍数和回收率分别为8.02和49.02.对酶学性质研究表明,该重组酶为金属离子激活性酶,Mg2 ,Co2 对相对酶活有很强的激活作用,其最适pH为7.0,最适反应温度为95℃,且在pH 6～8之间有着较好的稳定性,在95℃下半衰期长达5 h以上.以葡萄糖为底物时的表观Km和Vmax分别为105 mmol/L和45.2 mol/min·mg.     

Bioproduction of ethylenediamine-N,N'-disuccinic acid using immobilized fumarase-free EDDS lyase

Ethylenediamine-N,N'-disuccinic acid (EDDS) is a promising chelating agent for the remediation of heavy metal-contaminated soil. In general, EDDS is produced through a chemical method. In this study, we report an efficient biotechnological approach for EDDS production using an immobilized enzyme. We expressed the EDDS lyase in E. coli and obtained 19.8 g/L of EDDS through a reaction catalyzed by crude enzymes, containing EDDS lyase and fumarase. After performing metal affinity chromatography-mediated purification, we thoroughly eliminated the fumarase activity, which could result in the unnecessary formation of malate. Then, the purified EDDS lyase was immobilized on a glutaraldehyde-activated amino carrier, and the immobilized enzyme was used in 11 batches (864.5 h). After optimization, 209.3 g/L EDDS was obtained in a 100 mL reaction system, resulting in 20.2 g of EDDS product with a purity of 99.8 % after isolation. The yields of reaction and isolation were 94.0 % and 91.8 %, respectively. In conclusion, this study describes a promising bioproduction process for industrial-level EDDS production.     

Production of D-tagatose, a low caloric sweetener during milk fermentation using L-arabinose isomerase

Lactobacillusdelbrueckii subsp. bulgaricus and Streptococcus thermophilus are used for the biotransformation of milk in yoghurt. During milk fermentation, these lactic acid bacteria (LAB) hydrolyze lactose producing a glucose moiety that is further metabolized and a galactose moiety that they are enable to metabolize. We investigated the ability of L. bulgaricus and S. thermophilus strains expressing a heterologous L-arabinose isomerase to convert residual D-galactose to D-tagatose. The Bacillus stearothermophilus US100l-arabinose isomerase (US100l-AI) was expressed in both LAB, using a new shuttle vector where the araA US100 gene is under the control of the strong and constitutive promoter of the L. bulgaricus ATCC 11842 hlbA gene. The production of L-AI by these LAB allowed the bioconversion of D-galactose to D-tagatose during fermentation in laboratory media and milk. We also established that the addition of L-AI to milk also allowed the conversion of D-galactose into D-tagatose during the fermentation process.     

Cloning, expression, and characterization of bacterial L-arabinose 1-dehydrogenase involved in an alternative pathway of L-arabinose metabolism

Azospirillum brasiliense converts L-arabinose to alpha-ketoglutarate via five hypothetical enzymatic steps. We purified and characterized L-arabinose 1-dehydrogenase (EC 1.1.1.46), catalyzing the conversion of L-arabinose to L-arabino-gamma-lactone as an enzyme responsible for the first step of this alternative pathway of L-arabinose metabolism. The purified enzyme preferred NADP+ to NAD+ as a coenzyme. Kinetic analysis revealed that the enzyme had high catalytic efficiency for both L-arabinose and D-galactose. The gene encoding L-arabinose 1-dehydrogenase was cloned using a partial peptide sequence of the purified enzyme and was overexpressed in Escherichia coli as a fully active enzyme. The enzyme consists of 308 amino acids and has a calculated molecular mass of 33,663.92 Da. The deduced amino acid sequence had some similarity to glucose-fructose oxidoreductase, D-xylose 1-dehydrogenase, and D-galactose 1-dehydrogenase. Site-directed mutagenesis revealed that the enzyme possesses unique catalytic amino acid residues. Northern blot analysis showed that this gene was induced by L-arabinose but not by D-galactose. Furthermore, a disruptant of the L-arabinose 1-dehydrogenase gene did not grow on L-arabinose but grew on D-galactose at the same growth rate as the wild-type strain. There was a partial gene for L-arabinose transport in the flanking region of the L-arabinose 1-dehydrogenase gene. These results indicated that the enzyme is involved in the metabolism of L-arabinose but not D-galactose. This is the first identification of a gene involved in an alternative pathway of L-arabinose metabolism in bacterium.