The inhibitory effect of benzenethiol on the cresolase and catecholase activities of mushroom tyrosinase

The inhibitory effect of benzenethiol on the cresolase and catecholase activities of mushroom tyrosinase (MT) have been investigated at two temperatures of 20 and 30 degrees C in 10 mM phosphate buffer solution, pHs 5.3 and 6.8. The results show that benzenethiol can inhibit both activities of mushroom tyrosinase competitively. The inhibitory effect of benzenethiol on the cresolase activity is more than the catecholase activity of MT. The inhibition constant (K(i)) value at pH 5.3 is smaller than that at pH 6.8 for both enzyme activities. However, the K(i) value increases in cresolase activity and decreases in catecholase activity due to the increase of temperature from 20 to 30 degrees C at both pHs. Moreover, the effect of temperature on K(i) value is more at pH 6.8 for both cresolase and catecholase activities. The type of binding process is different in the two types of MT activities. The binding process for catecholase inhibition is only entropy driven, which means that the predominant interaction in the active site of the enzyme is hydrophobic, meanwhile the electrostatic interaction can be important for cresolase inhibition due to the enthalpy driven binding process. Fluorescence and circular studies also show a minor change in the tertiary structure, without any change in the secondary structure, of the enzyme due to the electrostatic interaction in cresolase inhibition by benzenethiol at acidic pH.     

Effects of temperature on the hydrolysis of lactose by immobilized beta-galactosidase in a capillary bed reactor

The effects of temperature on the hydrolysis of lactose by immobilized beta-galactosidase were studied in a continuous flow capillary bed reactor. Temperature affects the rates of enzymatic reactions in two ways. Higher temperatures increase the rate of the hydrolysis reaction, but also increase the rate of thermal deactivation of the enzyme. The effect of temperature on the kinetic parameters was studied by performing lactose hydrolysis experiments at 15, 20, 25, 30, and 40 degrees C. The kinetic parameters were observed to follow an Arrhenius-type temperature dependence. Galactose mutarotation has a significant impact on the overall rate of lactose hydrolysis. The temperature dependence of the mutarotation of galactose was effectively modelled by first-order reversible kinetics. The thermal deactivation characteristics of the immobilized enzyme reactor were investigated by performing lactose hydrolysis experiments at 52, 56, 60, and 64 degrees C. The thermal deactivation was modelled effectively as a first order decay process. Based on the estimated thermal deactivation rate constants, at an operating temperature of 40 degrees C, 10% of the enzyme activity would be lost in one year.     

Effects of temperature on cell growth and xanthan production in batch cultures of Xanthomonas campestris

Batch xanthan fermentations by Xanthomonas campestris NRRL B-1459 at various temperatures ranging between 22 degrees C and 35 degrees C were studied. At 24 degrees C or lower, xanthan formation lagged significantly behind cell growth, resembling typical secondary metabolism. However, at 27 degrees C and higher, xanthan biosynthesis followed cell growth from the beginning of the exponential phase and continued into the stationary phase. Cell growth at 35 degrees C was very slow; the specific growth rate was near zero. The specific growth rate had a maximum value of 0.26 h(-1) at temperatures between 27 degrees C and 31 degrees C. Cell yield decreased from 0.53 g/g glucose at 22 degrees C to 0.28 g/g glucose at 33 degrees C, whereas xanthan yield increased from 54% at 22 degrees C to 90% at 33 degrees C. The specific xanthan formation rate also increased with increasing temperature. The pyruvate content of xanthan produced at various temperatures ranged between 1.9% and 4.5%, with the maximum occurring between 27 degrees C and 30 degrees C. These results suggest that the optimal temperatures for cell growth are between 24 degrees C and 27 degrees C, whereas those for xanthan formation are between 30 degrees C and 33 degrees C. For single-stage batch fermentation, the optimal temperature for xanthan fermentation is thus dependent on the design criteria (i. e., fermentation rate, xanthan yield, and gum qualities). However, a two-stage fermentation process with temperature shift-up from 27 degrees C to 32 degrees C is suggested to optimize both cell growth and xanthan formation, respectively, at each stage, and thus to improve overall xanthan fermentation.     

Product deactivation in recombinant Streptomyces

The production of tyrosinase by Streptomyces antibioticus (p1J7O2) was investigated as a model system for recombinant protein production by Streptomyces. Product deactivation was found to have a severe effect on the levels of tyrosinase obtained. Tyrosinase deactivation was detected during all phases of batch cultures, with higher specific deactivation rates observed during the stationary phase. The specific deactivation rate exhibited an Arrhenius dependence on temperature, with approximately a twofold increase in the deactivation rate between 25 degrees C and 30 degrees C. The effect of deactivation on the determination of tyrosinase production kinetics is discussed. A strategy was implemented to increase tyrosinase productivity by enriching the growth medium and reducing the culture temperature during the period of maximum tyrosinase production. This strategy resulted in a shorter culture time and a 2.5-fold increase in tyrosinase activity compared to a culture grown at 25 degrees C using a standard growth medium.     

Enhancement of monascus pigment production by the culture of Monascus sp. J101 at low temperature

In general, high broth viscosity is a key factor to be considered in a submerged fermentation of filamentous fungi. High broth viscosity was also observed in a batch fermentation of Monascus sp. J101 at 30 degrees C. In a batch culture at 30 degrees C, most cell growth was accomplished within 48 h, which induced highly entangled clumps. The resultant high viscosity induced heterogeneity inside the fermentor, poor oxygen transfer, and low pigment yield. However, these problems could be overcome by reducing fungal growth rate through culture at low temperature (25 degrees C). Cell growth was moderate and continued for 120 h, and low viscosity was maintained. The DO levels remained at 50% or higher with good mixing. As a result, the pigment yield at 25 degrees C was 10 times greater than at 30 degrees C.     

Adenylate energy charge in Escherichia coli CR341T28 and properties of heat-sensitive adenylate kinase

Escherichia coli strain CR341T28 will not grow at temperatures above 34 degrees C in liquid medium, and the adenylate kinase of this strain is heat sensitive. When a culture was shifted from a permissive (30 degrees C) to a nonpermissive (36 degrees C) temperature, the adenylate energy charge fell from 0.9 to 0.2, with a concurrent decrease in the number of viable cells and in the specific activity of adenylate kinase. When cultures of the temperature-sensitive strain were grown at temperatures above 30 degrees C, the adenylate energy charge, the specific activity of adenylate kinase, and the growth rate were lower than the corresponding parameters for the parental strain. By isotopic labeling of the adenine nucleotides in vivo, it was determined that increasing growth temperatures between 30 and 34 degrees C for the heat-sensitive strain resulted in a decrease in the adenosine triphosphate-to-adenosine monophosphate and adenosine triphosphate-to-adenosine diphosphate ratios. Between 26 and 30 degrees C the adenosine triphosphate-to-adenosine diphosphate ratio was essentially normal in the temperature-sensitive strain, but the adenosine triphosphate-to-adenosine diphosphate ratio was decreased. The adenylate ratios in the parental strain did not change between 30 and 34 degrees C. The adenylate kinase mass action ratio for each strain was essentially constant under all growth conditions. When assayed at 30 degrees C, the affinities of the enzyme from the mutant strain were somewhat lower than those of the parent adenylate kinase. The mutant enzyme also did not exhibit the substrate inhibition that was observed at high adenosine monophosphate concentrations with the parental enzyme. An increase in the assay temperature from 30 degrees to 40 degrees C had little or no effect on the Km values determined for the parental adenylate kinase, but caused the Km values determined for the mutant adenylate kinase to increase by a factor of two or more.     

Rate of deactivation of nitric oxide-stimulated soluble guanylate cyclase: influence of nitric oxide scavengers and calcium

Soluble guanylate cyclase (sGC) is highly activated by nitric oxide (NO) and is the known mediator of the effects of NO on a variety of physiological processes. The rates at which sGC is activated and deactivated are therefore of wide interest since they determine the duration of a tissue's response to NO. The effect of NO on smooth muscle dissipates in 1-2 min, suggesting that both activation and deactivation are fast. In vitro measurements show that the activation of sGC occurs in less than a second, while the deactivation takes several hours at 20 degrees C. However, recent reports indicate that Mg-GTP, oxyhemoglobin, and reducing and oxidizing agents could deactivate the cyclase in several seconds to minutes, though the effectiveness of each of these agents is in dispute. We investigated the lifetime of NO-sGC in the cytosol of retina by monitoring its enzymatic activity at 20 degrees C. Our results show that Mg-GTP, the substrate of NO-sGC, has no influence on the deactivation. Similarly, reducing agents glutathione and dithiothreitol shortened the half-life of NO-sGC only by about 30%. The greatest effect on the deactivation was caused by scavengers of NO: oxyhemoglobin reduced the half-life of NO-sGC from 106 min to 18 s; another NO scavenger, 2-(4-carboxyphenyl)-4,4,5, 5-tetramethylimidazoline-1-oxyl-3-oxide (CPTIO), reduced it to 42 s (20 degrees C). Similarly rapid deactivation was observed with the enzyme from bovine lung, immunoprecipitated enzyme from bovine retina, and heme-deficient enzyme from bovine retina reconstituted with heme. On the other hand, YC-1, an activator of sGC, stabilized the activated enzyme, preventing NO dissociation, as was evident from the inability of oxyhemoglobin or CPTIO to deactivate NO-sGC. Calcium, which is known to inhibit NO-sGC, also inhibited the effects of oxyhemoglobin and CPTIO, slowing down the deactivation of the enzyme. Lithium, which is also known to inhibit NO-sGC, had no effect on the deactivation rate of the enzyme. These results, taken together, suggest that two factors with major impact on the lifetime of NO-sGC are the proximity to NO scavengers and the calcium concentration in the cell.     

Influence of polymolecular events on inactivation behavior of xylose isomerase from Thermotoga neapolitana 5068

The inactivation behavior of the xylose isomerase from Thermotoga neapolitana (TN5068 XI) was examined for both the soluble and immobilized enzyme. Polymolecular events were involved in the deactivation of the soluble enzyme. Inactivation was biphasic at 95 degrees C, pH 7.0 and 7.9, the second phase was concentration-dependent. The enzyme was most stable at low enzyme concentrations, however, the second phase of inactivation was 3- to 30-fold slower than the initial phase. Both phases of inactivation were more rapid at pH 7.9, relative to 7.0. Differential scanning calorimetry of the TN5068 XI revealed two distinct thermal transitions at 99 degrees and 109 degrees C. The relative magnitude of the second transition was dramatically reduced at pH 7.9 relative to pH 7.0. Approximately 24% and 11% activity were recoverable after the first transition at pH 7.0 and 7.9, respectively. When the TN5068 XI was immobilized by covalent attachment to glass beads, inactivation was monophasic with a rate corresponding to the initial phase of inactivation for the soluble enzyme. The immobilized enzyme inactivation rate corresponded closely to the rate of ammonia release, presumably from deamidation of labile asparagine and/or glutamine residues. A second, slower inactivation phase suggests the presence of an unfolding intermediate, which was not observed for the immobilized enzyme. The concentration dependence of the second phase of inactivation suggests that polymolecular events were involved. Formation of a reversible polymolecular aggregate capable of protecting the soluble enzyme from irreversible deactivation appears to be responsible for the second phase of inactivation seen for the soluble enzyme. Whether this characteristic is common to other hyperthermophilic enzymes remains to be seen.     

Expression of xyloglucan endotransglycosylases of Gerbera hybrida and Betula pendula in Pichia pastoris

The plant enzyme xyloglucan endotransglycosylase (XET; EC 2.4.1.207, xyloglucan:xyloglucosyl transferase) participates in selective modification of plant cell walls during cell growth. XETs are potential catalysts in various applications. Here, sequences encoding two XETs from Gerbera hybrida and Betula pendula are reported. The encoded proteins, which are 51% identical at the amino acid level, were expressed in the yeast Pichia pastoris in secreted form with the aid of mating factor alpha signal sequence. XET production in shake flask cultivations was better at 22 degrees C than at 30 degrees C. Both the yield of protein of expected molecular mass and the XET activity improved at the lower temperature. Under all cultivation conditions studied, higher amounts of XET from B. pendula (BXET) were expressed than XET from G. hybrida (GXET). Both XET enzymes were produced in 16l fed-batch bioreactor cultures. GXET was produced in methanol-limited fed-batch cultivation in minimal medium, and BXET in temperature-limited fed-batch (TLFB) in minimal or complex medium. Production was highest in TLFB in complex medium. BXET was purified from the culture filtrate and characterized. Based on the specific activity of the purified protein, 60-70 mg l(-1) BXET was produced in the TLFB in complex medium.     

Characterization of an Agrobacterium tumefaciens D-psicose 3-epimerase that converts D-fructose to D-psicose

The noncharacterized gene previously proposed as the D-tagatose 3-epimerase gene from Agrobacterium tumefaciens was cloned and expressed in Escherichia coli. The expressed enzyme was purified by three-step chromatography with a final specific activity of 8.89 U/mg. The molecular mass of the purified protein was estimated to be 132 kDa of four identical subunits. Mn2+ significantly increased the epimerization rate from D-fructose to D-psicose. The enzyme exhibited maximal activity at 50 degrees C and pH 8.0 with Mn2+. The turnover number (k(cat)) and catalytic efficiency (k(cat)/Km) of the enzyme for D-psicose were markedly higher than those for d-tagatose, suggesting that the enzyme is not D-tagatose 3-epimerase but D-psicose 3-epimerase. The equilibrium ratio between D-psicose and D-fructose was 32:68 at 30 degrees C. D-Psicose was produced at 230 g/liter from 700-g/liter D-fructose at 50 degrees C after 100 min, corresponding to a conversion yield of 32.9%.     

Production and characterization of a thermostable glucoamylase from Streptosporangium sp. endophyte of maize leaves

Thermostable amylolytic enzymes are currently investigated to improve industrial processes of starch degradation. Streptosporangium sp. an endophytic actinomycete isolated from leaves of maize (Zea mays L.) showed glucoamylase production, using starch-Czapek medium, and the highest rate was obtained in the initial growth phase, after incubation for 24 h at pH 8.0. Maximum glucoamylase activity (158 U mg(-1) protein) was obtained at pH 4.5 and 70 degrees C. The isolated enzyme exhibited thermostable properties as indicated by retention of 100% of residual activity at 70 degrees C for 30 min with total inhibition at 100 degrees C. Extracellular enzyme from Streptosporangium sp. was purified by fractionated precipitation with ammonium sulphate. After 60% saturation produced 421 U mg(-1) protein, and yield was 74% with purification 2.7 fold. The enzyme produced by Streptosporangium sp. has potential for industrial applications.     

Isomaltulose production using free cells: optimisation of a culture medium containing agricultural wastes and conversion in repeated-batch processes

The enzyme glucosyltransferase is an industrially important enzyme since it produces non-cariogenic isomaltulose (6-O-alpha-D-glucopyronosyl-1-6-D-fructofuranose) from sucrose by intramolecular transglucosylation. The experimental designs and response surface methodology (RSM) were applied for the optimisation of the nutrient concentrations in the culture medium for the production of glucosyltransferase by Erwinia sp. D12 in shaken flasks at 200 rpm and 30 degrees C. A statistical analysis of the results showed that, in the range studied, the factors had a significant effect (P < 0.05) on glucosyltransferase production and the highest enzyme activity (10.84 U/ml) was observed in culture medium containing sugar cane molasses (150 g l(-1)), corn steep liquor (20 g l(-1)), yeast extract Prodex Lac SD (15 g l(-1)) and K2HPO4 (0.5 g l(-1)) after 8 h at 30 degrees C. The production of cell biomass by the strain of Erwinia sp. D12 was carried out in a 6.6-l fermenter with a mixing rate of 200 rpm and an aeration rate of 1 vvm. Fermentation time, cellular growth, medium pH and glucosyltransferase production were observed. The greatest glucosyltransferase activity was 22.49 U/ml, obtained after 8 h of fermentation. The isomaltulose production from sucrose was performed using free Erwinia sp. D12 cells in a batch process using an orbital shaker. The influence of the parameters sucrose concentration, temperature, pH, and cell concentration on the conversion of sucrose into isomaltulose was studied. The free cells showed a high conversion rate of sucrose into isomaltulose using batch fermentation, obtaining an isomaltulose yield of 72.11% from sucrose solution 35% at 35 degrees C.     

The inhibitory effect of benzenethiol on the cresolase and catecholase activities of mushroom tyrosinase

The inhibitory effect of benzenethiol on the cresolase and catecholase activities of mushroom tyrosinase (MT) have been investigated at two temperatures of 20 and 30°C in 10 mM phosphate buffer solution, pHs 5.3 and 6.8. The results show that benzenethiol can inhibit both activities of mushroom tyrosinase competitively. The inhibitory effect of benzenethiol on the cresolase activity is more than the catecholase activity of MT. The inhibition constant (K_i) value at pH 5.3 is smaller than that at pH 6.8 for both enzyme activities. However, the K_i value increases in cresolase activity and decreases in catecholase activity due to the increase of temperature from 20 to 30°C at both pHs. Moreover, the effect of temperature on K_i value is more at pH 6.8 for both cresolase and catecholase activities. The type of binding process is different in the two types of MT activities. The binding process for catecholase inhibition is only entropy driven, which means that the predominant interaction in the active site of the enzyme is hydrophobic, meanwhile the electrostatic interaction can be important for cresolase inhibition due to the enthalpy driven binding process. Fluorescence and circular studies also show a minor change in the tertiary structure, without any change in the secondary structure, of the enzyme due to the electrostatic interaction in cresolase inhibition by benzenethiol at acidic pH.     

Temperature-dependent kinetic model for nitrogen-limited wine fermentations

A physical and mathematical model for wine fermentation kinetics was adapted to include the influence of temperature, perhaps the most critical factor influencing fermentation kinetics. The model was based on flask-scale white wine fermentations at different temperatures (11 to 35 degrees C) and different initial concentrations of sugar (265 to 300 g/liter) and nitrogen (70 to 350 mg N/liter). The results show that fermentation temperature and inadequate levels of nitrogen will cause stuck or sluggish fermentations. Model parameters representing cell growth rate, sugar utilization rate, and the inactivation rate of cells in the presence of ethanol are highly temperature dependent. All other variables (yield coefficient of cell mass to utilized nitrogen, yield coefficient of ethanol to utilized sugar, Monod constant for nitrogen-limited growth, and Michaelis-Menten-type constant for sugar transport) were determined to vary insignificantly with temperature. The resulting mathematical model accurately predicts the observed wine fermentation kinetics with respect to different temperatures and different initial conditions, including data from fermentations not used for model development. This is the first wine fermentation model that accurately predicts a transition from sluggish to normal to stuck fermentations as temperature increases from 11 to 35 degrees C. Furthermore, this comprehensive model provides insight into combined effects of time, temperature, and ethanol concentration on yeast (Saccharomyces cerevisiae) activity and physiology.     

Lactate dehydrogenase from the extreme halophilic archaebacterium Halobacterium marismortui

D-Lactate dehydrogenase from the extreme halophilic archaebacterium Halobacterium marismortui has been partially purified by ammonium-sulfate fractionation, hydrophobic and ion exchange chromatography. Catalytic activity of the enzyme requires salt concentrations beyond 1M NaCl: optimum conditions are 4M NaCl or KCl, pH 6-8, 50 degrees C. Michaelis constants for NADH and pyruvate under optimum conditions of enzymatic activity are 0.070 and 4.5mM, respectively. As for other bacterial D-specific lactate dehydrogenases, fructose 1,6-bisphosphate and divalent cations (Mg2+, Mn2+) do not affect the catalytic activity of the enzyme. As shown by gel-filtration and ultracentrifugal analysis, the enzyme under the conditions of the enzyme assay is a dimer with a subunit molecular mass close to 36 kDa. At low salt concentrations (less than 1M), as well as high concentrations of chaotropic solvent components and low pH, the enzyme undergoes reversible deactivation, dissociation and denaturation. The temperature dependence of the enzymatic activity shows non-linear Arrhenius behavior with activation energies of the order of 90 and 25 kJ/mol at temperatures below and beyond ca. 30 degrees C. In the presence of high salt, the enzyme exhibits exceptional thermal stability; denaturation only occurs at temperatures beyond 55 degrees C. The half-time of deactivation at 70 and 75 degrees C is 300 and 15 min, respectively. Maximum stability is observed at pH 7.5-9.0.     

Increased thermostability of Asn182 --> Ala mutant Aspergillus awamori glucoamylase

Asn182 --> Ala Aspergillus awamori glucoamylase expressed in Saccharomyces cerevisiae had a first-order thermodeactivation coefficient 40% that of wild-type glucoamylase at pH 4.5 between 60 degrees and 65 degrees C, caused by the elimination of an Asn-Gly sequence subject to deamidation and eventual chain breakage. Above 70 degrees C, and at pHs 3.5 and 5.5, thermodeactivation coefficients of wild-type and mutant enzymes were roughly equal, because the fastest deactivation mechanism was no longer deamidation. The mutation had little effect on the enzyme's optimal pH for activity and subsite map, or on the glucose yield from starch dextrin hydrolysis. During enzyme production by yeast fermentation, highest cell densities and activities of wild-type and mutant glucoamylases were attained after a period of glucose starvation, followed by a second addition of glucose. (c) 1994 John Wiley & Sons, Inc.     

Host cell variations resulting from F plasmid-controlled replication of the Escherichia coli chromosome.

Cell size and DNA concentration were measured in Escherichia coli K-12 ET64. This strain carries a dnaA (Ts) mutation that has been suppressed by the insertion of the F plasmid into the chromosome. ET64 can grow in a balanced steady state of exponential growth at the restrictive temperature for its dnaA allele (39 degrees C), in which chromosome replication is controlled by the F plasmid, and at the permissive temperature (30 degrees C), in which chromosome replication is controlled by dnaA-oriC. When cells grown at the indicated temperatures were compared, it was observed that at 39 degrees C, the cell mass increased and the amount of cellular DNA decreased slightly; therefore, the DNA concentration was strongly reduced. These changes can neither be explained by the reduction of the generation time (which is only 10-15%) nor from observed changes in the replication time and in the time between DNA synthesis termination and cell division. Variations were mainly due to the increase in cell mass per origin of replication, at initiation, in cells grown at 39 degrees C. Control of chromosome replication by the F plasmid appears to be the reason for the increase in the initiation mass. Other possible causes, such as the modification of growth temperature, the generation time, or both, were discarded. These observations suggest that at one growth rate, the F plasmid replicates at a particular cell mass to F particle number ratio, and that this ratio is higher than the cell mass to oriC ratio at the initiation of chromosome replication. This fact might be significant to coordinate the replication of two different replicons in the same cell.     

Optimization of maltodextrin hydrolysis by glucoamylase in a batch reactor

The hydrolysis of maltodextrins (10 DE) by glucoamylase was studied in a batch reactor at temperatures between 40 and 80 degrees C and substrate concentration range from 17 to 300 kg/m(-3). The experimental data were fitted to a model including thermal deactivation of the enzyme. In the model, the reaction rate was correlated with an extended Michaelis-Menten equation including inhibition by product, and the thermal deactivation of glucoamylase was fitted with a first-order reaction. The dependence of rate parameters on temperature was correlated using the Arrhenius equation. The differential equation of the model was integrated and the optimal enzyme demand and temperature were determined for isothermal operation.     

The calmodulin-dependent activation and deactivation of the phosphoprotein phosphatase, calcineurin, and the effect of nucleotides, pyrophosphate, and divalent metal ions. Identification of calcineurin as a Zn and Fe metalloenzyme

Studies on the interaction of calcineurin with its activator, calmodulin, showed that the 1:1 complex is the activated species. Concomitant with activation, a time-dependent deactivation of the phosphatase was observed. The process followed first order kinetics and was dependent on the presence of both Ca2+ and calmodulin. The deactivation rate constant at pH 7.6 and 30 degrees C was 0.06 min-1, which was increased by the substrate, p-nitrophenylphosphate (Km = 11 mM), to 0.47 min-1. PPi and nucleotides inhibited the enzyme competitively and accelerated the deactivation. The first order rate constant was increased to 2.3 min-1 by PPi (Ki = 55 microM) and to 8.0 min-1 by ADP (Ki = 0.94 mM). A theory dealing with the deactivation (applicable to chemical modification, etc.) of an enzyme in the absence and presence of various ligands is presented. The deactivated enzyme remained bound to calmodulin and was not reactivated by dissociation-reassociation of the calcineurin-calmodulin complex. Calcineurin was found to contain covalently bound phosphate; however, no difference in its content was detected upon deactivation, indicating that self-dephosphorylation was not involved. The deactivation could be reversed, as well as prevented, by divalent metal ions such as Ni2+ and Mn2+. Atomic absorption spectroscopy revealed nearly stoichiometric amounts of tightly bound Fe and Zn (but little other ions) on purified calcineurin, which remained bound during the calmodulin-dependent deactivation; removal of tightly bound metals is, therefore, not the cause of deactivation. Our results indicate that calcineurin is a metallophosphatase and not simply a Ca2+- and calmodulin-stimulated enzyme. In addition to the nondissociable Zn and Fe and the Ca2+ bound to the B subunit and calmodulin, the enzyme requires a divalent metal ion for structural stability and full activity.     

Physarum thymidine kinase. A step or a peak enzyme depending upon temperature of growth.

The variations of thymidine kinase or ATP:thymidine 5'-phosphotransferase (EC 2.7.1.21) during the cell cycle of Physarum polycephalum plasmodia have been studied at two extreme physiological temperatures: 22 degrees C and 32 degrees C. At 22 degrees C the enzyme activity increases near mitosis and stays constant during late S and G2 phases, exhibiting the typical pattern of a 'step enzyme'. But at 32 degrees C thymidine kinase activity goes through a maximum 1 h 30 min after mitosis and decreases during the subsequent phases as expected for a 'peak enzyme'. The rate of enzyme degradation and/or inactivation, measured in the presence of metabolic poisons (cycloheximide or dinitrophenol), appears to follow a simple exponential function with a half-life of approximately 3 h and 1 h at 22 degrees C and 32 degrees C respectively. The effect of growth temperature on the decrease of thymidine kinase activity can account entirely for the differences in the pattern of enzyme activity at the two extreme temperatures. Tentative calculations indicate that the rate of enzyme synthesis is nearly constant during the cell cycle except near mitosis, where it is temporarily increased. The results suggest the existence of a regulatory mechanism able to modulate the rate of synthesis of thymidine kinase during the cell cycle.