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.     

Biochemical characterization and evaluation of invertases produced from Saccharomyces cerevisiae CAT-1 and Rhodotorula mucilaginosa for the production of fructooligosaccharides

Abstract

Invertases are used for several purposes; one among these is the production of fructooligosaccharides. The aim of this study was to biochemically characterize invertase from industrial Saccharomyces cerevisiae CAT-1 and Rhodotorula mucilaginosa isolated from Cerrado soil. The optimum pH and temperature were 4.0 and 70?°C for Rhodotorula mucilaginosa invertase and 4.5 and 50?°C for Saccharomyces cerevisiae invertase. The pH and thermal stability from 3.0 to 10.5 and 75?°C for R. mucilaginosa invertase, respectively. The pH and thermal stability for S. cerevisiae CAT-1 invertase from 3.0 to 7.0, and 50?°C, respectively. Both enzymes showed good catalytic activity with 10% of ethanol in reaction mixture. The hydrolysis by invertases occurs predominantly when sucrose concentrations are ≤5%. On the other hand, the increase in the concentration of sucrose to levels above 10% results in the highest transferase activity, reaching about 13.3?g/L of nystose by S. cerevisiae invertase and 12.6?g/L by R. mucilaginosa invertase. The results demonstrate the high structural stability of the enzyme produced by R. mucilaginosa, which is an extremely interesting feature that would enable the application of this enzyme in industrial processes.     

Development of food-grade expression system for d-allulose 3-epimerase preparation with tandem isoenzyme genes in Corynebacterium glutamicum and its application in conversion of cane molasses to D-allulose

D -Allulose 3-epimerase (DAE) has been applied to produce D -allulose, a low-calorie and functional sweetener. In this study, a new DAE from Paenibacillus senegalensis was characterized in Escherichia coli. Furthermore, we presented a tandem isoenzyme gene expression strategy to express multiple DAEs in one cell and construct food-grade expression systems based on Corynebacterium glutamicum. Seventeen expression cassettes based on three DAE genes from different organisms were constructed. Among all recombinant strains, DAE16 harboring three DAE genes in an expression vector exhibited the highest enzyme activity with 22.7 U/mg. Whole-cell transformation of DAE16 produced 225 g/L D -allulose with a volumetric productivity of 353 g·g ⁻¹·hr ⁻¹. The catalytic efficiency of strain C-DAE9 integrating total 11 DAE genes in chromosome was 16.4-fold higher than strains carrying one DAE. Fed-batch culture of C-DAE9 gave enzyme activity of 44,700 U/L. We also expressed a thermostable invertase in C. glutamicum and obtained enzyme activity of 29 U/mg. Immobilized cells expressing DAE or invertase exhibited 80% of retained activity after 30 cycles of catalytic reactions. Those immobilized cells were coupled to produce 61.2 g/L D -allulose from cane molasses in a two-step reaction process. This study provided an efficient approach for enzyme preparation and allowed access to produce D -allulose from other abundant and low-cost feedstock enriched with sucrose.     

Production of high fructose syrup from <Emphasis Type="Italic">Asparagus</Emphasis> inulin using immobilized exoinulinase from <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> YS-1

Extracellular exoinulinase from Kluyveromyces marxianus YS-1, which hydrolyzes inulin into fructose, was immobilized on Duolite A568 after partial purification by ethanol precipitation and gel exclusion chromatography on Sephadex G-100. Optimum temperature of immobilized enzyme was 55 °C, which was 5 °C higher than the free enzyme and optimal pH was 5.5. Immobilized biocatalyst retained more than 90% of its original activity after incubation at 60 °C for 3 h, whereas in free form its activity was reduced to 10% under same conditions, showing a significant improvement in the thermal stability of the biocatalyst after immobilization. Apparent K _m values for inulin, raffinose and sucrose were found to be 3.75, 28.5 and 30.7 mM, respectively. Activation energy (E _a) of the immobilized biocatalyst was found to be 46.8 kJ/mol. Metal ions like Co²⁺ and Mn²⁺ enhanced the activity, whereas Hg²⁺ and Ag²⁺ were found to be potent inhibitors even at lower concentrations of 1 mM. Immobilized biocatalyst was effectively used in batch preparation of high fructose syrup from Asparagus racemosus raw inulin and pure inulin, which yielded 39.2 and 40.2 g/L of fructose in 4 h; it was 85.5 and 92.6% of total reducing sugars produced, respectively.     

Rapid ethanol production from sucrose without by-product formation

Summary Non-sorbitol-producing Zymomonas mobilis ACM 3963 was developed from Z. mobilis UQM 2716. This strain was co-immobilised with invertase in alginate and incubated on sucrose-based media. This combination allowed theoretical yields of ethanol to be produced from 100 and 150 g/l sucrose, using both semi-defined media and sugar-cane syrup. No sorbitol or fructo-oligosaccharides were formed in either fermentation. Increased biomass concentrations immobilised in alginate reduced the batch fermentation times of 100 and 150 g/l sucrose by 50–70%, to 3 and 5 hours respectively. This strain also improved the efficiency of the fed-batch fermentation of sucrose.     

Lactic acid production using two food processing wastes,canned pineapple syrup and grape invertase,as substrate and enzyme

Canned pineapple syrup, a food processing waste, was utilized as a substrate for lactic acid production by Lactococcus lactis. To improve the utilization of sucrose from the syrup, grape invertase from grape juice derived from wine production was used for sucrose hydrolysis. The highest lactic acid concentrations achieved were 20 and 92 g l^–1 from 20 and 100 g total sugars l^–1, respectively, without a lag period for sucrose consumption.     

Immobilized Sclerotinia sclerotiorum invertase to produce invert sugar syrup from industrial beet molasses by product

The fungus Sclerotinia sclerotiorum produces invertase activity during cultivation on many agroindustrial residues. The molasses induced invertase was purified by DEAE-cellulose chromatography. The molecular mass of the purified enzyme was estimated at 48 kDa. Optimal temperature was determined at 60 °C and thermal stability up to 65 °C. The enzyme was stable between pH 2.0 and 8.0; optimum pH was about 5.5. Apparent K_m and V_max for sucrose were estimated to be respectively 5.8 mM and 0.11 μmol/min. The invertase was activated by β-mercaptoethanol. Free enzyme exhibited 80 % of its original activity after two month’s storage at 4 °C and 50 % after 1 week at 25 °C. In order to investigate an industrial application, the enzyme was immobilized on alginate and examined for invert sugar production by molasses hydrolysis in a continuous bioreactor. The yield of immobilized invertase was about 78 % and the activity yield was 59 %. Interestingly the immobilized enzyme hydrolyzed beet molasses consuming nearly all sucrose. It retained all of its initial activity after being used for 4 cycles and about 65 % at the sixth cycle. Regarding productivity; 20 g/l of molasses by-product gave the best invert sugar production 46.21 g/day/100 g substrate related to optimal sucrose conversion of 41.6 %.     

Purification and characterization of extracellular invertase from the hypocotyls of mung bean (Phaseolus radiatus L.)

The extracellular invertase (β-D-fructofuranoside fructohydrolase, EC 3.2.1.26) was isolated and characterized from the hypocotyls of mung bean (Phaseolus radiatus L.). The enzyme was purified to apparent homogeneity by ammonium sulfate fractionation and sequential chromatography over diethylaminoethyl (DEAE)-cellulose anion exchange, Concanavalin (Con) A-Sepharose 4B affinity and Sephadex G-200. The overall purification was about 77-fold with a recovery of about 11%. The finally purified enzyme exhibited a specific activity of about 113 μmol of glucose produced mg^-1 protein min^-1 at pH 5.0 and appeared to be a single protein by nondenaturing polyacrylamide gel electrophoresis (PAGE) and sodium dodecyl sulfate (SDS)-PAGE. The enzyme had the native molecular mass of 134 kD and subunit molecular weight of 67 kD as estimated by Sephadex G-200 chromatography and SDS-PAGE, respectively, suggesting that the enzyme was composed of homodimeric proteins. On the other hand, the enzyme appeared to be a glycoprotein containing mannosyl residues on the basis of its ability to interact specifically with the immobilized Con A and the separability of invertase-Con A complex by methyl-α-D-mannopyranoside. The enzyme had a K_m for sucrose of 3.4 mM and its pH optimum of 4.0. The enzyme showed highest enzyme activity with sucrose as substrate. Raffinose and cellobiose were hydrolyzed at a low rate, maltose and lactose were not cleaved by the enzyme. These results indicate the extracellular invertase is a β-fructofuranosidase.     

Immobilization of enzymes on magnetic particles

Trypsin (EC 3.4.4.4) was immobilized in low yield on aminoalkylsilylated magnetite (Fe₃O₄). Better results were obtained when trypsin was immobilized by crosslinking with glutaraldehyde on magnetite. The preparation contained 36 mg protein/g magnetite and the enzyme retained 46% and 11% of esterase and proteolytic activity. Immobilized trypsin was more heat stable than trypsin. Invertase (β-D -fructofuranoside fructohydrolase, EC 3.2.1.26) was cross-linked on magnetite with glutaraldehyde in low yield due to the inactivation of the enzyme. However in the presence of 1% sucrose, the total activity recovered was 79% of the initial activity and the preparation contained 4.4 mg/g of active invertase. Immobilized invertase was less active than invertase when acting on oligosaccharides of the raffinose family. The immobilized enzymes could be easily recovered, from solutions or suspensions, magnetically.     

A novel method for immobilization of invertase from the thermophilic fungus, Thermomyces lanuginosus

An invertase from the thermophilic fungus, Thermomyces lanuginosus was immobilized on phenyl-Sepharose and its properties were studied. Between the soluble and immobilized forms of the invertase, there were not much difference in their optimum pH, K _M and V _max for sucrose. In contrast, the K _M and V _max for raffinose changed significantly. The optimum temperature for the immobilized invertase was lower by 10 C. The immobilized invertase showed remarkable stability at 50 C and was less sensitive to inhibition by metal ions. There was no leaching of the enzyme for at least a month when stored in the refrigerator. The method is novel and specific for the thermophilic invertase as a mesophilic invertase (from yeast) did not bind to phenyl-Sepharose.     

Simultaneous production of citric acid and invertase by Yarrowia lipolytica SUC+ transformants

Simultaneous production of citric acid (CA) and invertase by Yarrowia lipolytica A-101-B56-5 (SUC⁺ clone) growing from sucrose, mixture of glucose and fructose, glucose or glycerol was investigated. Among the tested substrates the highest concentration of CA was reached from glycerol (57.15 g/L) with high yield (Y_CA/S = 0.6 g/g). When sucrose was used, comparable amount of CA was secreted (45 g/L) with slightly higher yield (Y_CA/S = 0.643 g/g). In all cultures amount of isocitrate (ICA) was below 2% of total citrates. Considering invertase production, the best carbon source appeared to be sucrose (72 380 U/L). The highest yield of CA and invertase biosynthesis calculated for 1 g of biomass was obtained for cells growing from glycerol (9.9 g/g and 4325 U/g, respectively). Concentrates of extra- and intracellular invertase of the highest activity were obtained from sucrose as substrate (0.5 and 1.8 × 10⁶ U/L, respectively).     

Active protein and substrate flow effects in a tubular immobilized invertase reactor

Investigations of invertase (EC 3.2.1.26) immobilized inside modified nylon tubes showed that between 4% and 20% (w/w) of the protein exposed to binding sites on the tube was immobilized. An enhanced activity consistent with enzyme purification during immobilization was also evident, suggesting that, in scaled-up commercial applications, nylon tube invertase would be a more economical converter of sucrose than the free enzyme. The quantity and specific activity of the immobilized protein were not stochiometrical with the amount used in the coupling solution and, in the system studied, a concentration of 2 mg ml^?1 was optimal. K_m and V_max values confirmed higher rates of immobilized invertase catalysis when the rates of substrate flow through the reactor were higher. Higher rates of substrate flow imply a shortened residence time in the reactor and would lower the fractional conversion per pass of the substrate, reducing the efficiency of the reactor in flow-through situations. Thus, these higher catalysis rates, attributable at the higher flow rates to a reduction of the diffusion barrier between enzyme and substrate, would not translate into improved economy in the commercial flow-through processes at which the reactor is aimed.     

Isolation and characterization of a cDNA clone from Lolium temulentum L. encoding for a sucrose hydrolytic enzyme which shows alkaline/neutral invertase activity

A novel cDNA clone, functionally expressed in E. coli, was isolated from a L. temulentum L. cDNA library. The expressed protein hydrolysed sucrose with an apparent Km of approximately 18 mM, and produced equi-molar concentrations of glucose and fructose. Optimum activity was observed at pH 7-7.5; there was little or no activity at pH 5.5. The expressed protein did not hydrolyse raffinose, stachyose or maltose. The activity of the expressed protein was inhibited by fructose (50% at 15 mM) and TRIS (50% at 2.5 mM), but was not affected by MgCl2, CaCl2 or MnCl2. These findings suggest that this cDNA clone encodes for an alkaline/neutral invertase. Sequence analysis revealed little homology with published sequences for acid invertase, however the invertase motif (NDPN) identified in other invertases was present. Expression studies show that the gene encoding for this enzyme is not regulated by sucrose accumulation in leaf tissue.     

Continuous production of fructooligosaccharides using fructosyltransferase immobilized on ion exchange resin

A continuous production of fructooligosaccharides from sucrose was investigated by fructosyltransferase immobilized on a high porous resin, Diaion HPA 25. The optimum pH (5.5) and temperature (55°C) of the enzyme for activity was unaltered by immobilization, and the immobilized enzyme became less sensitive to the pH change. The optimal operation conditions of the immobilized enzyme column for maximizing the productivity were as follows: 600 g/L of sucrose feed concentration, flow rate of superficial space velocity 2.7 h^?1. When the enzyme column was run at 50°C, about 8% loss of the initial activity of immobilized enzyme was observed after 30 days of continuous operation, during which high productivity of 1174 g/L·h was achieved. The kinds of products obtained using the immobilized enzyme were almost the same as those using soluble enzymes or free cells.     

Method of measuring invertase activity in soils

Summary Invertase (-D-fructofuranoside fructohydrolase, EC [Enzyme Commission] 3.2.1.26) is the enzyme that catalyzes the hydrolysis of sucrose and yields glucose and fructose. The activity of this enzyme was monitored by systematically developing a sensitive and rapid method to detect reducing sugars with the precision of 1.4 to 6.1% C.V. The method involves the colorimetric determination of reducing sugars which react with 3,5-dinitrosalicylic acid when soil is incubated with buffered sucrose solution and toluene at 37°C for 24 h. The detection limit for the method described is 100 g of reducing sugar per ml of soil extract. The color intensity remained constant up to 24 h. Comparative studies showed that the method described was in good agreement to other invertase assay procedures reported in the literature.Studies on the stability and distribution of invertase in soils by using the method described showed that air-drying of field-moist soil samples resulted in decreased activity ranging from 15.3 to 23.7% (avg.=19.8%). Statistical analyses indicated that invertase activity was significantly correlated with total N (r=0.78^***) and organic C (r=0.70^***) in the topsoil of 19 diverse samples. There was no significant correlation between invertase activity and soil pH, cation exchange capacity, percentage of clay and percentage of sand. The activity of this enzyme was concentrated in surface soils and decreased with profile depth. Regression analyses showed that invertase activity was significantly correlated with organic carbon content of three soil profiles examined.     

Production of l-rhamnulose,a rare sugar,from l-rhamnose using commercial immobilized glucose isomerase

Abstract

A commercial immobilized d-glucose isomerase from Streptomyces murines (Sweetzyme) was used to produce l-rhamnulose from l-rhamnose in a packed-bed reactor. The optimal conditions for l-rhamnulose production from l-rhamnose were determined as pH 8.0, 60?°C, 300?g L^?1 l-rhamnose as a substrate, and 0.6?h^?1 dilution rate. The half-life of the immobilized enzyme at 60?°C was 809?h. Under the optimal conditions, the immobilized enzyme produced an average of 135?g L^?1 l-rhamnulose from 300?g L^?1 l-rhamnose after 16 days at pH 8.0, 60?°C, and 0.6?h^?1 dilution rate, with a productivity of 81?g/L/h and a conversion yield of 45% in a packed-bed reactor.     

Continuous production of fructooligosaccharides from sucrose by immobilized fructosyltransferase

The productivity of the continuous production of fructooligosaccharides from sucrose was investigated by fructosyltransferase immobilized onto a high-porous ion exchange resin was optimal with 600 g sucrose/l at a flow rate of 2.7 h^–1 expressed as a superficial space velocity. When the column was operated at 50 °C, about 8% loss of the initial activity of immobilized enzyme was observed after 30 days continuous operation, achieving high productivity of 1174 g/l · h.     

Purification and Characterization of Invertase from Lactobacillus reuteri CRL 1100

The invertase of Lactobacillus reuteri CRL 1100 is a glycoprotein composed by a single subunit with a molecular weight of 58 kDa. The enzyme was stable below 45°C over a wide pH range (4.5–7.0) with maximum activity at pH 6.0 and 37°C. The invertase activity was significantly inhibited by bivalent metal ions (Ca⁺⁺, Cu⁺⁺, Cd⁺⁺, and Hg⁺⁺), β-mercaptoethanol, and dithiothreitol and partially improved by ethylenediaminetetraacetic acid. The enzyme was purified 32 times over the crude extract by gel filtration and ion-exchange chromatography with a recovery of 17%. The K _m and V_max values for sucrose were 6.66 mM and 0.028 μmol/min, respectively. An invertase is purified and characterized for the first time in Lactobacillus, and it proved to be a β-fructofuranosidase. Received: 13 August 1999 / Accepted: 15 September 1999     

Homofermentative production of optically pure <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid from sucrose and mixed sugars by batch fermentation of <Emphasis Type="Italic">Enterococcus faecalis</Emphasis> RKY1

In the present study, lactic acid fermentation was carried out by batch culture of Enterococcus faecalis RKY1 using sucrose and mixed sugars as the major substrate. Maximum lactic acid productivity (5.2 g/L/h) was recorded when 50 and 100 g/L of sucrose were used as a carbon source. Sucrose concentration higher than 150 g/L resulted in the decrease of lactic acid productivity due to inhibition by high substrate concentration, but lactic acid productivity was remained > 3.0 g/L/h until the sucrose used for lactic acid fermentation increased up to 150 g/L. L-Lactic acid content of the total lactic acid produced from sucrose and mixed sugars was higher than 98%. When the fermentation media contained sucrose, the kinetic parameters showing specific rates such as μ, qS, and qP were relatively lower than those of fermentation using glucose as a sole carbon source, which might be due to additional time requirement to induce invertase enzyme for utilization of sucrose. There was no carbon catabolite repression observed when the sugar mixtures containing sucrose, glucose, and/ or fructose were used as a carbon source for lactic acid fermentation by E. faecalis RKY1.     

Influence of growth factor supplements on butyric acid production from sucrose byClostridium butyricum

During batch fermentation of sucrose to butyric acid byClostridium butyricum the effect of growth factor supplementation was determined: addition of yeast extract (5 g/L) stimulated most. Using biotin as the sole growth factor, average productivity was definitely lower. Beet molasses as a combined source of carbon and growth factor were effective only at a high concentration (150 g/L). The optimal butyric acid production (45 g/L, yield 45%) was achieved with sucrose concentration of 100 g/L in a medium supplemented with yeast extract (5 g/L). It represents an average productivity of 0.90 gL⁻¹ h⁻¹ and relative butyric acid concentration of 91%.