Characterization and inhibition of invertases in sugar cane juice

(NH₄)₂SO₄ fractionation followed by Sephadex G-200 chromatography of sugar cane juice gave an acid invertase with MW of 380 000 and 23.5% carbohydrate and a neutral invertase with MW of 66 000 and 22% carbohydrate. For acid invertase, K_m is 2.8 mM and V_max is 2.7 μmol sucrose hydrolysed/hr/mg protein. For neutral invertase, K_m and V_max are 0.32 mM and 2.8 μmol hydrolysed/hr/mg protein, respectively. Inhibition of both invertases by either lauryl sulfate or metasilicate is not competitive.     

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).     

Characterization of the co-purified invertase and β-glucosidase of a multifunctional extract from Aspergillus terreus

The filamentous fungus Aspergillus terreus secretes both invertase and β-glucosidase when grown under submerged fermentation containing rye flour as the carbon source. The aim of this study was to characterize the co-purified fraction, especially the invertase activity. An invertase and a β-glucosidase were co-purified by two chromatographic steps, and the isolated enzymatic fraction was 139-fold enriched in invertase activity. SDS-PAGE analysis of the co-purified enzymes suggests that the protein fraction with invertase activity was heterodimeric, with subunits of 47 and 27 kDa. Maximal invertase activity, which was determined by response surface methodology, occurred in pH and temperature ranges of 4.0–6.0 and 55–65 °C, respectively. The invertase in co-purified enzymes was stable for 1 h at pH 3.0–10.0 and maintained full activity for up to 1 h at 55 °C when diluted in water. Invertase activity was stimulated by 1 mM concentrations of Mn²⁺ (161 %), Co²⁺ (68 %) and Mg²⁺ (61 %) and was inhibited by Al³⁺, Ag⁺, Fe²⁺ and Fe³⁺. In addition to sucrose, the co-purified enzymes hydrolyzed cellobiose, inulin and raffinose, and the apparent affinities for sucrose and cellobiose were quite similar (K_M = 22 mM). However, in the presence of Mn²⁺, the apparent affinity and V_max for sucrose hydrolysis increased approximately 2- and 2.9-fold, respectively, while for cellobiose, a 2.6-fold increase in V_max was observed, but the apparent affinity decreased 5.5-fold. Thus, it is possible to propose an application of this multifunctional extract containing both invertase and β-glucosidase to degrade plant biomass, thus increasing the concentration of monosaccharides obtained from sucrose and cellobiose.     

Transport of glucose,fructose and sucrose by Streptanthus tortuosus suspension cells

Streptanthus tortuosus Kell. suspension cells will grow in a medium with sucrose as carbohydrate source. It was investigated whether the cells are able to take up sucrose or whether sucrose has to be hydrolyzed to glucose and fructose which eventually are taken up. The detailed quantitative analysis of sugar-uptake rates in the low concentration range up to 1 mM showed the following features: (i) There is definitely no sucrose-uptake system working in the low concentration range; any uptake of radioactivity from labelled sucrose proceeds via hydrolysis of sucrose by cell-wallbound invertase. (ii) Hexoses are taken up by two systems, a glucose-specific system with a K _m of 45 M and a high V _max for glucose and a K _m of 6 mM and a low V _max for fructose, and a fructosespecific system with a K _m of 500 M and high a V _max for fructose and a K _m of 650 M and a low V _max for glucose. (iii) There is a more than tenfold preference for uptake of the fructose derived from sucrose versus uptake of free fructose, with the result that the kinetic disadvantage of the fructoseuptake system compared to the glucose-uptake system is diminished if sucrose is supplied as the carbon source. It is speculated that invertase might work as an enzyme aiding in fructose transport.Abbreviations FCCP carbonylcyanide-p-trifluoromethoxyphenylhydrazone - FW fresh weight     

Kinetics of invertase immobilised on poly(phe-lys) coated polystyrene beads

Summary Surface of polystyrene beads was modified by poly(phe-lys) for invertase immobilisation. The optimum immobilisation conditions of invertase were; 0.01% (w/v) poly(phe-lys), 2% (v/v) glutaraldehyde at 25 °C and pH 4.5. The kinetics of sucrose hydrolysis by free and immobilised invertase in a batch reactor at pH 4.5 and 55 °C gave K_m and V_max values for sucrose with free and immobilised invertase of 81, 114 mM and 10.1, 9.2 mol glucose/min.mg enzyme, respectively. The deactivation rate constants of free and immobilised invertase were 0.0347 and 0.0098 min^–1, respectively.     

Kinetic characterization of unspecific alkaline phosphatase at different villus sites of rat jejunum

Summary A quantitative histochemical method to determine the apparent Km and V _max values of rat intestinal unspecific alkaline phosphatase at different sites of the villi is described. Naphthol-As-Bi-phosphate (0.025–1.5 mM) is employed as substrate and Fast Blue B as coupling reagent, and the resulting azo-dye in the brush border membrane has an absorbance maximum at 550 nm. The ratio between the absorbance at 550 and 500 nm is constant as calculated from automatically recorded spectra at different intense dye deposits. Its absorbance is a linear function of incubation time up to 3 min and thickness of the slices up to 10 m both with medium (0.5 mM) and high (1.5 mM) substrate concentrations. Using the histochemical assay under comparable conditions in test tube experiments with homogenates of intestinal mucosa an app. Km of 0.26±0.081 mM (weighted regression analysis) and 0.28–0.084 mM (direct linear plotting) is determined, demonstrating an affinity to the histochemical substrate, which is about 10 times higher than for p-Nitro-phenyl-phosphate with the purified enzyme.The results obtained by scanning the total dye deposits along jejunal villi show considerable differences in enzymatic activity between single villi and an increase from the villus base up to the transition between medium and apical villus third. As well in the apical region as at the villus base saturation curves are obtained by determining the relationship between the absorbance and the substrate concentration under standard conditions (slice thickness 10 m, incubation time 3 min, 37°C, pH 8.3). Calculated by weighted regression analysis and direct linear plotting from the absorbance data of six female rats the medium app. kinetic data ±SD from the jejunal villi read as follows. Apical: Km=0.81±0.438 mM, V _max=3.99±1.217 absorbance units (A) and Km=0.87±0.428 mM, V _max=4.02±1.191 A, respectively. Basal: Km=0.82±0.261 mM, V _max=3.26±0.719 A and Km=0.77±0.184 mM, V _max=3.04±0.518 AU, respectively. As demonstrated by factorial analysis of variance only V _max is influenced by the villus position.Supported by the Deutsche Forschungsgemeinschaft GU 184/1     

Simple and inexpensive Flow Injection Analysis for determination of sucrose using invertase and glucose oxidase immobilised on glass beads

A Flow Injection Analysis (FIA) for sucrose using invertase (E.C. 3.2.1.26), mutarotase (E.C.5.1.3.3) and glucose oxidase (E.C.1.1.3.4) was developed. The enzymes were immobilised on glass beads using glutaraldehyde. The sucrose concentration was related to oxygen saturation. Fall in O₂ concentration, as a result of sucrose oxidation, was detected by a low cost, home-made O₂ electrode. The system was able to measure sucrose from 0.025 to 100mM with a response time of 6min using 200 l of sample, with an apparent Km of 42mM of sucrose. The system has been operated satisfactorily for 50 days without loss any initial activity.     

Effect of pH,aeration and sucrose feeding on the invertase activity of intactS. cerevisiae cells grown in sugarcane blackstrap molasses

S. cerevisiae was grown in a blackstrap molasses containing medium in batch and fed-batch cultures. The following parameters were varied: pH (from 4.0 to 6.5), dissolved oxygen (DO) (from 0 to 5.0 mg O₂L^–1) and sucrose feeding rate. When glucose concentration (S) was higher than 0.5 g L^–1 a reduction in the specific invertase activity of intact cells (v) and an oscillatory behavior of v values during fermentation were observed. Both the invertase reduction and the oscillatory behavior of v values could be related to the glucose inhibitory effect on invertase biosynthesis. The best culture conditions for attainingS. cerevisiae cells suitable for invertase production were: temperature=30°C; pH=5.0; DO=3.3 mg O₂L^–1; (S)=0.5 g L^–1 and sucrose added into the fermenter according to the equations: (V–V_o)=t²/16 or (V–V_o)=(V_f–V_o)·(e^0.6t–1)/10.This work was supported by FAPESP     

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 %.     

Kinetic and thermodynamic properties of wall bound invertase in heat tolerant and susceptible cultivars of wheat

We have identified two types of invertases, one bound ionically and the other covalently to the particulate fraction in grains of heat tolerant C 306 and heat susceptible WH 542 cultivars of wheat (Triticum aestivum L.). The cell walls contained a high level of invertase activity, of which 79.2–72.8% was extractable by 2 M NaCl and 14.9–21.1% by 0.5% EDTA in C 306 and WH 542, respectively. The NaCl-released invertase constituted the predominant fraction. Using 5–100 mM sucrose and pH range of 4.0–7.0, the apparent Michaelis constant (K _m, enzyme substrate affinity measure) of enzyme ranged from 5.73 to 16.06 mM for C 306 and from 6.08 to 19.86 mM for WH 542. The V _max (maximum catalytic rate) values at these pH were higher in C 306 (0.63–11.04 μg sucrose hydrolysed min⁻¹) than WH 542 (0.51–8.73 μg sucrose hydrolysed min⁻¹). By employing photo-oxidation and by studying the effect of pH on K _m and V _max, the involvement of histidine and α-carboxyl groups at the active site of the enzyme was indicated. The two cultivars also showed differential response in terms of thermodynamic properties of the enzyme i.e. energy of activation (E _a), enthalpy change (ΔH) and entropy change (ΔS). NaCl-released invertase showed differential response to metal ions in two cultivars suggesting their distinctive nature. Mn²⁺, Cu²⁺, Hg²⁺, Mg²⁺, Zn²⁺ and Cd²⁺ were strong inhibitors in WH 542 as compared to C 306 while K⁺, Ca²⁺ were stimulators in both the cultivars. Overall the results suggest that genetic differences exist in wall bound invertase properties of wheat grains as evident in its altered kinetic behaviour.     

Formaldehyde activating enzyme (Fae) and hexulose-6-phosphate synthase (Hps) in <Emphasis Type="Italic">Methanosarcina barkeri</Emphasis>: a possible function in ribose-5-phosphate biosynthesis

Formaldehyde activating enzyme (Fae) was first discovered in methylotrophic bacteria, where it is involved in the oxidation of methanol to CO₂ and in formaldehyde detoxification. The 18 kDa protein catalyzes the condensation of formaldehyde with tetrahydromethanopterin (H₄MPT) to methylene-H₄MPT. We describe here that Fae is also present and functional in the methanogenic archaeon Methanosarcina barkeri. The faeA homologue in the genome of M. barkeri was heterologously expressed in Escherichia coli and the overproduced purified protein shown to actively catalyze the condensation reaction: apparent V _max=13 U/mg protein (1 U=μmol/min); apparent Km for H₄MPT=30 μM; apparent Km for formaldehyde=0.1 mM. By Western blot analysis the concentration of Fae in cell extracts of M. barkeri was determined to be in the order of 0.1% of the soluble cell proteins. Besides the faeA gene the genome of M. barkeri harbors a second gene, faeB-hpsB, which is shown to code for a 42 kDa protein with both Fae activity (3.6 U/mg) and hexulose-6-phosphate synthase (Hps) activity (4.4 U/mg). The results support the recent proposal that in methanogenic archaea Fae and Hps could have a function in ribose phosphate synthesis.     

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     

Sucrose translocation and storage in the sugar beet

Several physiological processes were studied during sugar beet root development to determine the cellular events that are temporally correlated with sucrose storage. The prestorage stage was characterized by a marked increase in root fresh weight and a low sucrose to glucose ratio. Carbon derived from ¹⁴C-sucrose accumulation was partitioned into protein and structural carbohydrate fractions and their amino acid, organic acid, and hexose precursors. The immature root contained high soluble acid invertase activity (V_max 20 micromoles per hour per milligram protein; K_m 2 to 3 millimolar) which disappeared prior to sucrose storage. Sucrose storage was characterized by carbon derived from ¹⁴C-sucrose uptake being partitioned into the sucrose fraction with little evidence of further metabolism. The onset of storage was accompanied by the appearance of sucrose synthetase activity (V_max 12 micromoles per hour per milligram protein; K_m 7 millimolar). Neither sucrose phosphate synthetase nor alkaline invertase activities were detected during beet development. Intact sugar beet plants (containing a 100-gram beet) exported 70% of the translocate to the beet, greater than 90% of which was retained as sucrose with little subsequent conversions.     

Pathway of Phloem unloading of sucrose in corn roots

The pathway of phloem unloading and the metabolism of translocated sucrose were determined in corn (Zea mays) seedling roots. Several lines of evidence show that exogenous sucrose, unlike translocated sucrose, is hydrolyzed in the apoplast prior to uptake into the root cortical cells. These include (a) presence of cell wall invertase activity which represents 20% of the total tissue activity; (b) similarity in uptake and metabolism of [¹⁴C]sucrose and [¹⁴C]hexoses; and (c) randomization of ¹⁴C within the hexose moieties of intracellular sucrose following accumulation of [¹⁴C] (fructosyl)sucrose. Conversely, translocated sucrose does not undergo apoplastic hydrolysis during unloading. Asymmetrically labeled sucrose ([¹⁴C](fructose)sucrose), translocated from the germinating kernels to the root, remained intact indicating a symplastic pathway for unloading. In addition, isolated root protoplasts and vacuoles were used to demonstrate that soluble invertase activity (V_max = 29 micromoles per milligram protein per hour, K_m = 4 millimolar) was located mainly in the vacuole, suggesting that translocated sucrose entered via the symplasm and was hydrolyzed at the vacuole prior to metabolism.     

Changes in glycine and leucine transport during red cell maturation in the rat

Both glycine and leucine transport in rat red blood cells have been studied. The glycine uptake showed two different components, one sodium-dependent and another diffusion-like process. In contrast, leucine uptake was sodium independent. Both, Na⁺-dependent glycine and the overall leucine uptake in red blood cells showed a saturable pattern. Kinetic parameters in reticulocytes were: i) glycine: apparent Km 0.16 mM; V_max 100.2 nmol/ml ICW/min; ii) leucine: apparent Km 2.11 mM; V_max 3.88 mol/ml ICW/min. The erythrocytes kinetic parameters were: i) glycine: apparent Km 0.17 mM; V_max 9.47 nmol/ml ICW/min; leucine; apparent Km 4.77 mM; V_max 7.42 mol/ml ICW/min. The Kd values (sodium independent glycine uptake) were similar in both kind of cells, but the importance of this component in total glycine uptake in erythrocytes was much higher than in reticulocytes. Our results confirm that rat red blood cells have both saturable leucine and Na⁺-dependent glycine uptake, but some important changes occur during cell maturation.     

Immobilization of yeast cells in hydroxyethylmethacrylate gels

Summary Whole cells of Saccharomyces cerevisiae were entrapped in polymers of 2-hydroxyethylmetha-crylate and sucrose hydrolysis catalysed by its invertase was investigated.Analysis of the experimental results confirmed that diffusional resistance to mass transfer of reactant and product was not induced by immobilization.For the yeast cells in the hydrogel, invertase activity obeyed a Michaelis-Menten kinetic and the value of Km (40 mM) was the same as that for yeast cells in bulk phase.The recovery of biocatalyst activity ranged between 17% and 23%, depending on immobilization temperature; the optimum pH range was found to be slightly wider.Storage stability at refrigerator temperature was quite satisfactory; invertase half-life was 267 days. Operational stability of immobilized cells at 45°C (half-life 110 days) was almost twice that of free cells.Finally, cell distribution in the polymer, observed with a scanning electron microscope, was found to be uniform.Symbols C Active cell concentration, g/mg - Ea Activation energy, cal/mol - Kd kinetic constant of the enzyme deactivation reaction, h - Km Michaelis constant, mM - Nc Active cell amount, mg - r Enzymatic reaction rate, mol/min - S Substrate concentration, mM - t Reaction time, h or days - T Reaction temperature, °C or °K - Tp Polymerization temperature, °C - V _max Kinetic constant of enzymatic reaction, mol/min     

Invertases in young and mature leaves of Citrus sinensis

The sucrose catabolic enzymes acid invertase (EC 3.2.1.26) and alkaline invertase (EC 3.2.1.27) were studied in young and mature Citrus sinensis leaf tissue. In young, expanding leaves (60 % final length) soluble acid invertase activity predominated, while soluble alkaline invertase activity predominated in mature leaves. The acid and alkaline invertase activities were separated on Sephadex G-200. The acid invertase had an M_r of approximately 60 000, pH maximum of 4.5 and apparent K_m of 3.3 mM sucrose. The alkaline invertase had an M_r of approximately 200 000, pH maxima of 6.8 and an apparent K_m of 20 mM sucrose. Alkaline invertase was strongly inhibited by 10 mM Tris while acid invertase was not. Possible physiological roles for the two invertases are discussed.     

Synthesis of wall glucan from sucrose by enzyme preparations from Pisum sativum

Radioactive sucrose, supplied through the cut base to Pisum sativum epicotyls, was transported to the growing apex (plumule and hook) and used there for the synthesis mainly of uridine diphosphoglucose (UDP- glucose), fructose and cell wall glucan. Enzyme extracts of the apical tissue contained sucrose synthetase activity which was freely reversible, i.e. formed UDP-glucose and fructose from sucrose (pH optimum = 6·6 for the cleavage reaction, K_m for sucrose = 63 mM). Particulate fractions of the same tissue contained a β-glucan synthetase which utilized UDP-glucose for formation of alkali-soluble and -insoluble products (pH optimum = 8·4, K_m for UDP-glucose = 1·9 mM). Values for V_max and yields of these two synthetase activities were sufficient to account for observed rates of cellulose deposition during epicotyl growth (15–25 μg/hr/epicotyl). When soluble pea enzyme was supplied with sucrose and UDP at pH 6·6 and then the preparation was supplemented with particles bearing β-glucan synthetase at pH 8·4, the glucose moiety of sucrose was converted to glucan in vitro. The results indicate that it is feasible for these synthetases to co-operate in vivo to generate β-glucan for expanding cell walls.     

The influence of phosphate concentration on the kinetics of uptake by maize roots

In an experiment with native maize roots depending on different phosphorus concentration in the external solution (0.001 … 50 mM P), the multiphasic character of the kinetics of phosphate uptake has been stated. The single phases are characterized by the different values of K_m and V_max. In the wide range of concentrations the isotherm of the phosphate uptake has five evident phases. The character of kinetics for the uptake of phosphate is analogical to the kinetics of the enzymatic reactions described by the Michaelis-Menten equation. On the other hand the linear dependence for the inactivated root was determined,i.e. the uptake of phosphate versus different phosphorus concentration in the external solution. The graphic representation of the logarithmic values for the phosphorus taken up versus the different phosphorus concentration in the external solution gives the biphasic course including concentration less than 1.0 mM P and more than 1.0 mM P. Within the framework of the concentration range the following values of V_max, K_m and ϕ_in were calculated under the conditions if the concentration of phosphorus is less than 1.0mMP: V_max = 1.705 μmol P × g^-1h^-1, K_m = 0.057 mM P and ϕ_in = 0.83,i.e. if the concentration of phosphorus is more than 1.0mM P: V_max = 40 μmol P × g^-1 h^-1, K_m = 16.66 mM and ϕ_in = 20. According to these results, the phosphate concentration in the external solution influences the activity of the transport mechanisms concerning their conformative changes which discretely change their working regime of membrane transport. This is also demonstrated in the change of values V_max, K_m and ϕ_in.     

Kinetics and bioreactor studies of immobilized invertase on polyurethane rigid adhesive foam

A new support, polyurethane rigid adhesive foam (PRAF), which can be used to cover internal surface of metallic tubes, was used to immobilize invertase for application in an enzymatic bioreactor. The kinetic parameters were: K_m - 46.5 ± 1.9 mM (PRAF-invertase) and 61.2 ± 0.1 mM (free enzyme) and V_max 42.0 ± 4.3 U/mg protein/min (PRAF-invertase) and 445.3 ± 24.0 U/mg protein/min (free invertase). The PRAF-invertase derivative maintained 50.1% of initial activity (69.17 U/g support) for 8 months (4 °C) and was not observed microbial contamination. The bioreactor showed the best production of inverted sugar syrup using up-flow rate (0.48 L/h) with average conversion of 10.64 ± 1.5% h⁻¹ at feeding rate (D) of 104 h⁻¹. The operational inactivation rate constant (k_opi) and half-life were 1.92 × 10⁻⁴ min⁻¹ and 60 h (continue use). The PRAF spray support looks promising as a new alternative to produce immobilized derivatives on reactor surfaces.