Transport of phenylalanine into vacuoles isolated from barley mesophyll protoplasts

The energy-dependent transport of phenylalanine into isolated vacuoles of barley (Hordeum vulgare L.) mesophyll protoplasts has been studied by silicone-layer floatation filtering. The uptake of this aromatic amino acid into the vacuolar compartment is markedly increased by MgATP, showing saturation kinetics; the K _m values were 0.5 mM for MgATP and 1.2 mM for phenylalanine. V _max for phenylalanine transport was estimated to 140 nmol phenylalanine·(mg·Chl)^-1·h^-1. The transport shows a distinct pH optimum at 7.3 and is markedly inhibited by 40 mM nitrate. Azide (1 mM) and vanadate (400 M) had no or little effect on rates of transport while p-fluorophenylalanine seemed to be an effective inhibitor, indicating a possible competition at an amino-acid carrier. Ionophores such as valinomycin, nigericin or gramicidin were strong inhibitors of phenylalanine transport, indicating that this process is coupled to both the transmembrane pH gradient (pH) and the transmembrane potential ().Abbreviations and symbols BSA bovine serum albumin - Chl chlorophyll - Hepes 4-(2-hydroxyethyl)-1-piperazineethanesulfonic acid - pH transmembrane pH gradient - transmembrane potential     

Transient state characteristics of adaptation to changes in light conditions for the cyanobacterium Oscillatoria agardhii

Transitions in growth irradiance level from 92 to 7 Em^-2 s^-1 and vice versa caused changes in the pigment contents and photosynthesis of Oscillatoria agardhii. The changes in chlorophyll a and C-phycocyanin contents during the transition from high to low irradiance (HL) were reflected in photosynthetic parameters. In the LH transition light utilization efficiencies of the cells changed faster than pigment contents. This appeared to be related to the lowering of light utilization efficiencies of photosynthesis. As a possible explanation it was hypothesized that excess photosynthate production led to feed back inhibition of photosynthesis. Time-scales of changes in the maximal rate of O₂ evolution were discussed as changes in the number of reaction centers of photosystem II in relation to photosynthetic electron transport. Parameters that were subject to change during irradiance transitions obeyed first order kinetics, but hysteresis occurred when comparing HL with LH transients. Interpretation of first order kinetic analysis was discussed in terms of adaptive response vs changes in growth rate.Non-standard abbreviations Chla chlorophyll a - CPC C-phycocyanin - PS II photosystem II - PS I photosystem I - RC II reaction center of photosystem II - P photosynthetic O₂-evolution - I irradiance, Em^-2 s^-1 - light utilization efficiency of cells, mmol O₂·mg dry wt^-1·h^-1/Em^-2 s^-1 - light utilization efficiency of photosynthetic apparatus, mol O₂·mol Chla ^-1·h^-1/Em^-2 s^-1 - P_max maximal rate of O₂ evolution by cells, mol O₂·mg dry wt^-1·h^-1 - P_max maximal rate of O₂ evolution by photosynthetic apparatus, mol O₂·mol·Chla ^-1·h^-1 - LL low light, E m^-2 s^-1 - HL high light, E m^-2 s^-1 - LH low to high light transition - HL high to low light transition - k specific rate of adaptation, h^-1 - specific growth rate, h^-1 - Q pool size of cell constituent, mol·mg dry wt^-1 - q net synthesis rate of cell constituent, mol·mg dry wt^-1·h^-1     

Purification and properties of the ATP: adenylylsulphate 3′-phosphotransferase from Chlamydomonas reinhardii

APS-kinase (ATP: adenylylsulphate 3-phosphotransferase, EC 2.7.1.25) has been purified from the alga Chlamydomonas reinhardii, strain CW 15 by means of chromatofocussing and affinity chromatography. The isolated protein showed an apparent molecular mass of 44,000 upon sodium dodecylsulphate polyacrylamide gel electrophoresis. The transfer of phosphate groups from ATP onto APS required a pH of 6.8, the presence of Mg²⁺ ions and a reducing thiol. Its catalytical activity was destroyed by sulphhydryl group inhibitors (phenyl-mercuri compounds, dithiopyridine) and alkylating reagents.The purified enzyme attained a V _max of 360 pkat under optimal reaction conditions declining to v _limit of 260 pkat in the presence of excess substrate APS. This sensitivity towards changes in substrate concentrations was parallelled by a high affinity and specificity: apparent K _m APS: 2 · 10^-6 mol · l^-1, and K _m ATP: 7 · 10^-6 mol · l^-1. The enzyme was found specific for ATP, d-ATP and CTP, while UTP, ITP and GTP showed marginal activity. The Hill coefficients suggested 4 binding sites for APS and 1 for ATP. Excessive APS resulted in a negative slope indicating 3 inhibiting sites of the substrate.Abbreviations APS Adenosine 5-phosphosulphate - dATP 2-deoxyadenosine 5-triphosphate - p-CMB p-chloromercuribenzoate - DTE dithioerythritol - DTT dithiothreitol - -MSH -mercaptoethanol - PAPS 3-phosphoadenosine 5-phosphosulphate - PAP 3-phosphoadenosine 5-phosphate - SDS sodium dodecyl sulphate This work is part of a dissertation submitted by H. G. J., Bochum 1982     

Lactic acid production by batch fermentation of whey permeate: A mathematical model

Summary The batch fermentation of whey permeate to lactic acid was improved by supplementing the broth with enzyme-hydrolyzed whey protein. A mathematical model based on laboratory results predicts to a 99% confidence limit the kinetics of this fermentation. Cell growth, acid production and protein and sugar use rates are defined in quantifiable terms related to the state of cell metabolism. The model shows that the constants of the Leudeking-Piret model are not true constants, but must vary with the medium composition, and especially the peptide average molecular weight. The kinetic mechanism on which the model is based also is presented.Nomenclature K _i lactic acid inhibition constant (g/l) - K _pr protein saturation constant during cell growth (g/l) - K _pr protein saturation constant during maintenance (g/l) - K _s lactose saturation constant (g/l) - [LA] lactic acid concentration (g/l) - [PR] protein concentration (g/l) - [S] lactose concentration (g/l) - t time (h) - [X] cell mass concentration (g/l) - , fermentation constants of Leudeking and Piret - specific growth rate (l/h) - Y _{g, LA/S} acid yield during cell growth (g acid/g sugar) - Y _{m, LA/S} acid yield during maintenance (g acid/g sugar) - Y _x/pr yield (g cells/g protein) - specific sugar use rate during cell growth (g sugar/h·g cell) - specific sugar use rate during maintenance (g sugar/h·cell)     

Purification and characterization of an extracellular β-glucosidase from the anaerobic fungus Piromyces sp. strain E2

An extracellular -glucosidase (EC 3.2.2.21) from the anaerobic fungus Piromyces sp. strain E2 was purified. The enzyme is a monomer with a molecular mass of 45 kDa and a pI of 4.15. The enzyme readily hydrolyzes p-nitrophenyl--d-glycoside, p-nitrophenyl--d-fucoside, cellobiose, cellotriose, cellotetraose and cellopentaose but is not active towards Avicel, carboxymethylcellulose, xylan, p-nitrophenyl--d-galactoside and p-nitrophenyl--d-xyloside. To cleave p-nitrophenyl--d-glucoside the maximum activity is reached at pH 6.0 and 55°C, and the enzyme is stable up to 72 h at 40°C. Activity is inhibited by d-glucurono--lactone, cellobiose, sodium dodecyl sulfate, Hg²⁺ and Cu²⁺ cations. With p-nitrophenyl--d-glycoside, p-nitrophenyl--d-fucoside, and. cellobiose as enzyme substrates, the K _m and V _max balues are 1.5 mM and 25.5 IU·mg^-1, 1.1. mM and 133 IU·mg^-1, and 0.05 mM and 55.6 IU·mg^-1, respectively.     

Basal oxygen consumption,ventilatory frequency,and heart rate during the protracted spawning run of the Southern Hemisphere lamprey Geotria australis

Summary Basal oxygen consumption, ventilatory frequency, and heart rate were recorded at four different times during the unusually protracted 15–16-month spawning run of the Southern Hemisphere lamprey Geotria australis. At 15°C, the mean basal oxygen consumption of G. australis caught immediately after they had left the sea and embarked on the spawning run (45 l · g^-1 · h^-1) was less than in young adults about to commence their marine feeding phase (64 l · g^-1 · h^-1), but greater than in large ammocoetes (26.5 l · g^-1 · h^-1). Basal oxygen consumption fell progressively during the spawning-run of to 33 l · g^-1 · h^-1 after 5 months and 25 l · g^-1 · h^-1 after 10 months, before rising to 35 l · g^-1 · h^-1 after 15 months when the animals were approaching sexual maturity. The downwards trend in basal oxygen consumption contrasts with that recorded during the spawning run of Lampetra fluviatilis. Furthermore, these values for spawning-run of G. australis are far lower than those measured at any time during the upstream migration of L. fluviatilis or during the parasitic phase of landlocked Petromyzon marinus. A low and declining metabolic rate during much of the spawning run of G. australis would facilitate the conservation of energy reserves during this very long non-feeding period. Trends shown by ventilatory frequency and heart rate essentially parallel those of basal oxygen consumption. The Q₁₀s for basal oxygen consumption, ventilatory frequency and heart rate over the temperature range 5–25°C were 1.6, 1.6, and 1.7, respectively. The trends shown by basal oxygen consumption during metamorphosis and the upstream migration did not parallel those exhibited by circulating thyroid hormones.     

Some regulatory aspects of [14C]methylamine influx intoPisum sativum L. cv. Feltham First seedlings

[¹⁴C]Methylamine influx intoPisum sativum L. cv. Feltham First seedlings showed Michaelis-Menten-type kinetics with apparentV _max=49.2 mol·g^-1 FW·h^-1 and apparentK _m=0.51 mM. The competitive interactions between ammonium and methylamine were most obvious when biphasic kinetics were assumed with saturation of the first phase at 0.05 mM. The inhibitor constant for ammonium (K _i)=0.027 mM. When [¹⁴C]methylamine was used in trace amounts with ammonium added as substrate, the influx of tracer showed Michaelis-Menten-type kinetics with apparentV _max=3.46 mol·g^-1 FW·h^-1 and apparentK _m=0.15 mM. The initial rate of net ammonium uptake corresponded with that found when [¹⁴C]methylamine was used to trace ammonium influx. The latter was also stimulated by high pH_o and inhibited by nitrate. Ammonium pretreatment±methionine sulphoximine or glutamine pretreatment of the seedlings inhibited subsequent [¹⁴C]methylamine influx, while methylamine or asparagine pretreatment stimulated [¹⁴C]methylamine influx. There was also a stimulatory effect of prior inoculation withRhizobium. The results are discussed in terms of current models for the regulation of ammonium uptake in plants.     

Sodium influx in isolated gills of the freshwater mussel,Ligumia subrostrata

Summary Isolated gills of the freshwater mussel,Ligumia subrostrata, accumulate Na from a pondwater bathing medium. The rate of Na transport by the isolated gill is 13.2±1.1 mol (g dry gill·10 min)^–1 which equals or exceeds the estimated Na transport rate of intact animals. Sodium influx is saturable with aV _max of 13.6±1.2 mol (g dry gill·10 min)^–1 and an affinity (K _s) of 0.17 mM Na/l. The isolated gills survive prolonged exposure to pondwater with a constant of 890 l O₂ (g dry gill·h)^–1 over a 4 h period. Sodium transport in the isolated gills is stimulated 80% above control values by 10^–4 M serotonin, 60% by 0.5 mM cAMP and 60% by 12.5 g/ml nystatin. Sodium influx is inhibited by 0.5 mM amiloride and 1 mM lithium.     

Enhancement of protein precipitate strength and density by low-frequency conditioning

The use of a continuous, low-frequency conditioning process to alter the structure of protein precipitate aggregates is examined. An increase in the density of aggregates is correlated with the levels of fluid acceleration and hence hydrodynamic stress to which the aggregates are exposed during conditioning. A combination of low-frequency conditioning followed by shear break-up (as in the feed zone to a high-speed disk-stack centrifuge) is shown to result in a precipitate suspension of increased particle size at the fine end of the distribution, and having a greater sedimentation velocity. The resistance of large aggregates to shear disruption is increased by low-frequency conditioning.List of Symbols CR conditioning ratio - CRS conditioning ratio after shearing - d m amplitude of displacement - D m particle size - D _c m critical size for centrifuge recovery - f s^–1 frequency of vibration - G s^–1 mean velocity gradient - Q m³/s volumetric throughput - SR shear ratio - t s ageing time Greek Symbols s^–1 mass-average shear rate - K sedimentation shape factor - _a kg/m³ aggregate density - _f kg/m³ fluid density - _s kg/m³ solids density - kg/m³ aggregate-suspension density difference - Ns/m² kinematic viscosity - amplitude of pulse ratio (ref. 23, 9) - s mean residence time - _s solids volume fraction     

Accumulation of alkaloids in plant vacuoles does not involve an ion-trap mechanism

Alkaloid uptake into vacuoles isolated from a Fumaria capreolata L. cell suspension culture was investigated. The uptake is carrier-mediated as shown by its substrate saturation, its sensitivity to metabolic inhibitors and especially by its exclusive preference for the (S)-forms of reticuline and scoulerine while the (R)-enantiomers which do not occur in this plant species were strictly discriminated. The carrier has a high affinity for (S)-reticuline with a K _m=0.3 M. The rate of alkaloid uptake was 6 pmol·h^-1·l^-1 vacuole, and 0.03 mg alkaloid·mg^-1 vacuolar protein were taken up. Transport was stimulated five-to seven-fold by ATP and was inhibited by the ATPase inhibitors N,N-dicyclohexylcarbodiimide and 4-4-diisothiocyanatostilbene-2,2 disulfonic acid, as well as by the protonophore carbonyl cyanide m-chlorophenylhydrazone. A number of alkaloids did not compete with labelled (S)-reticuline for uptake into vacuoles. The uptake system is absolutely specific for alkaloids indigenous to the plant from which the vacuoles were isolated. Slight modifications of the topography of an alkaloid molecule even with full retention of its electrical charge results in its exclusion. Alkaloid efflux was also shown to be mediated by a highly specific energy-dependent carrier. These results contradict the previously proposed ion-trap mechanism for alkaloid accumulation in vacuoles. A highly specific carrier-mediated and energy-dependent proton antiport system for alkaloid uptake and release is postulated.Abbreviations CCCP carbonylcyanide m-chlorophenylhydrazone - DCCD N,N-dicyclohexylcarbodiimide - DIDS 4-4-diisothiocyanatostilbene-2,2 disulfonic acid Dedicated to Professor Harry Beevers, Santa Cruz, on the occasion of his 60^th birthday     

Effect of time delay in specific growth rate on the periodic operation of bioreactors with input multiplicities

The effect of time delay in specific growth rate () on the periodic operation of bioreactors with input multiplicities is theoretically analyzed for productivity improvement. A periodic rectangular pulse is applied either in feed substrate concentration (S_f) or in dilution rate (D). Periodic operation under feed substrate concentration cycling gives improvement in productivity at lower value of ¯S_f of the two steady-state multiplicities of S_f only when the time delay in is larger. Whereas the larger value of ¯S_f gives improvement in average productivity for all values of time delay. Dilution rate (D) cycling gives an improvement in average productivity particularly for larger time delay in . This improvement in average productivity is obtained only at smaller value of dilution rate out of the two steady-state input multiplicities of D.List of Symbols D 1/h dilution rate - F memory function - g dummy variable - K_i g/l substrate inhibition constant - K_m g/l substrate saturation constant - P g/l product concentration - P_m g/l product saturation constant - Q g/(hl) product cell produced per unit time - S g/l substrate concentration - S_f g/l feed substrate concentration - S_f,p g/l feed substrate concentration during fraction of a period - X g/l biomass concentration - Y_X/S g/g cell mass yield - w variable either S or Z - Z g/l weighted average of substrate concentration Greek Letters 1/h time delay parameter - ₁ , ₂ product yield parameters, g/g and 1/h - pulse width expressed as a fraction of a period - 1/h specific growth rate - _m 1/h maximum specific growth rate - h period of oscillation - – average value     

Ein Verfahren zur näherungsweisen Berechnung des Fruchtvolumens bei Äpfeln

Zusammenfassung Unter Berücksichtigung des Fruchtformindexes h/Ø der einzelnen Frucht kann man den Volumzuwachs beliebig zusammengesetzter Gruppen von Früchten an verschiedenen Bäumen vergleichen. Bei der Berechnung der Zuwachsraten des Fruchtvolumens braucht man nur Durchmesser und Höhe der Früchte zu kennen, um das tatsächliche Volumen in guter Annäherung zu berechnen. Die Daten der Regression des Korrekturfaktors für das Volumen (K ) auf den Fruchtformindex werden für vier Sorten stark unterschiedlicher Fruchtform angegeben. Das Volumen der Frucht wird nach folgender Formel berechnet: V = 4/3 · · r ³ · K . Vergleichende Untersuchungen über die Zuwachsrate verschiedener Sorten können bei Verwendung der sortentypischen Regressionen durchgeführt werden.

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A method for approximate calculation of fruit volume in apples

Summary Growth rates of fruit volume can be determined more precisely by using the index h/Ø (length of fruit/diameter) than by simply calculating the volume of a sphere based on the measured diameter. Fruit volume is to be calculated by: V = 4/3 · · r ³ · K K is the factor of deviation of fruit shape from a sphere. K is given for 4 different varieties with varying shape of fruits (Echter Winterglockenapfel, Golden Delicious, Cox Orange Pippin and Ingrid Marie). The increase in volume of any group of apples within one variety or of different varieties can be compared by means of the specific regression of h/Ø to K .

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Obstbauversuchsanstalt des Alten Landes in Jork     

Kinetics of yeast growth and enzyme syntheses in a phosphate-limited continuous culture

Summary The effect of a deficiency of inorganic phosphate on the growth rate and on the invertase and phosphatase activities inSaccharomyces carlsbergensis was studied in a chemostat culture using a synthetic medium in which ethanol was the sole carbon source.The kinetic relationship between the growth rate and both the rates of phosphate uptake and the ethanol consumption agreed well with the threshold model but not the multicative model. The invertase activity of the yeast increased as the dilution rate decreased. As the phosphate concentration in the feed was reduced, the enzyme synthesis increased remarkably. Acid phosphatase activity was repressed completely above a critical molecular ratio, 0.015, of monopotassium phosphate to ethanol in the feed medium. As the phosphate concentration in the feed decreased, the maximum specific enzyme activity increased and the corresponding optimum dilution rate decreased. These experimental changes in enzyme synthesis were expressed mathematically using the modified operon models for enzyme regulation in terms of two fractions of limited inorganic phosphate; one which affects growth and the other which is incorporated in excess by the cells.Nomenclature A ethanol concentration in the culture (mM) - a, b, c, d exponents in the operon model - D dilution rate (h^–1) - E enzyme concentration in the culture (enzyme unit l^–1) - K_a, K_b, K_c, K_d, k equilibrium constants used in the operon model, see Toda (1976b) - o operator gene - P inorganic phosphate concentration in the culture (mM) - Pi limited inorganic phosphate concentration in the cells (mmole inorganic phosphate/g dry weight of cell) - Q specific enzyme activity, no units: (E/X)/(E/X)_max - Q_c, Q_d as defined in Eq. 12 - R repressor - r regulator gene - X cell concentration in the culture (dry cell weight l^–1) Greek Letters molecular ratio of inorganic phosphate to ethanol in the feed medium (mole/mole) - specific growth rate (h^–1) - A specific uptake rate of ethanol (mmole/g cell·h) - P specific uptake rate of inorganic phosphate (mmole/g cell·h) Suffix crit critical value - f feed - max maximum - min minimum - t total - 1, 2 number of species Superfix eff effective for cell growth - exc excess - str structural     

Biotransformation of cephalosporin C to 7-aminocephalosporanic acid with coimmobilized biocatalyst in a batch bioreactor

Biotransformation of cephalosporin C (CPS-C) to 7-aminocephalosporanic acid (7-ACA) was carried out with coimmobilized permeabilized cells of Trigonopsis variabilis and Pseudomonas species entrapped in Ca-pectate gel beads. Good aeration and stirring during the process was assured. The analysis of this complicated biochemical process in a heterogeneous system was based on the identification of individual effects (internal diffusion, reaction) running simultaneously. A spectrophotometric method was proposed for the determination of 7-(-ketoadipyl amido) cephalosporanic acid (CO-GL-7-ACA) and 7-ACA. The reaction-diffusion model containing dimensionless partial differential equations was solved by using the orthogonal collocation method. A good agreement between experimental values and values predicted by the mathematical model was obtained. Numerical simulations were performed on the basis of following the two assumptions:- several times higher activity of both cells,- hydrogen peroxide was continuously supplied in the bioreactor.List of Symbols A m² surface of the bead - c _i mol/dm³ concentration of component in the bead and/or in the solution - c _i0 mol/dm³ initial concentration of component in the solution - c _l0 mol/dm³ initial concentration of CPS-C in the solution - C _jl orthogonal collocation weights of the first derivation - D _ei m²/s effective diffusion coefficient of the components - D _jl orthogonal collocation weights of the second derivation - k ₅ dm³/(mol · s) kinetic parameter of non-enzyme reaction - K _inh mol/dm³ inhibition parameter for the first enzyme reaction - K _i dimensionless Michaelis constant for the first and second enzyme reaction, defined in Eq. (7) - K _l dimensionless inhibition parameter for the first enzyme reaction, defined in Eq. (7) - K _mi mol/dm³ Michaelis constant for the first and second enzyme reaction - n number of beads - P( _i ) symbol of dimensionless reaction rate, defined in Eq. (13) - r m radial coordinate inside the bead - R m radius of the bead - R(c _i ) mol/(dm³ · s) symbol for reaction rate, defined in Eq. (6) - t s time - V _max mol/(dm³ · s) max. reaction rate for the first and second enzyme reaction - V _L dm³ volume of solution excluding the space occupied by beads - voidage in batch bioreactor - _P porosity of the bead - i dimensionless effective diffusion coefficient of the components, defined in Eq. (7) - dimensionless time, defined in Eq. (7) - _mi Thiele modulus, defined in Eq. (7) - _i dimensionless concentration, defined in Eq. (7) - dimensionless radial position inside the bead, defined in Eq. (7) - _l0 initial dimension concentration of CPS-C, defined in Eq. (9), (10) - _i0 initial dimension concentration of component, defined in Eq. (9), (10) The authors wish to thank Dr. P. Gemeiner of Slovak Academy of Sciences for rendering of pectate gel. This work is supported by Ministry of Education (Grant No. 1/990 935/93).     

Product inhibition during the feeding phasein fed-batch ethanol fermentation of sugar-cane blackstrap molasses

Summary The following equations represent the influence of the ethanol concentration (E) on the specific growth rate of the yeast cells () and on the specific production rate of ethanol () during the reactor filling phase in fed-batch fermentation of sugar-cane blackstrap molasses: = ₀ - k · E and v = v ₀ · K/(K +E) Nomenclature E ethanol concentration in the aqueous phase of the fermenting medium (g.L^–1) - E_m value of E when = 0 or = 0 (g.L^–1) - F medium feeding rate (L.h^–1) - k empirical constant (L.g^–1.h^–1) - K empirical constant (g.L^–1) - M_as mass of TRS added to the, reactor (g) - M_cs mass of consumed TRS (g) - M_e mass of ethanol in the aqueous phase of the fermenting medium (g) - M_s mass of TRS in the aqueous phase of the fermenting medium (g) - M_x mass of yeast cells (dry matter) in the fermenting medium (g) - r correlation coefficient - S TRS concentration in the aqueous phase of the fermenting medium (g.L^–1) - S_m TRS concentration of the feeding medium (g.L^–1) - t time (h) - T temperature (° C) - TRS total reducing sugars calculated as glucose - V volume of the fermenting medium (L) - V₀ volume of the inoculum (L) - X yeast cells concentration (dry matter) in the fermenting medium (g.L^–1) - filling-up time (h) - specific growth rate of the yeast cells (h^–1) - ₀ value of when E=0 - specific production rate of ethanol (h^–1) - ₀ value of when E=0 - density of the yeast cells (g.L^–1) - dry matter content of the yeast cells     

Hormonal regulation of hepatic glycogenolysis inAmphibolurus nuchalis,the western netted dragon: an in vitro study

Summary In mammals hepatic glycogenolysis is controlled by several hormones using cyclicAMP, Ca²⁺ and/or diacylglycerol as intracellular messengers. In contrast, in teleost fish, lungfish and amphibians fewer hormones promote hepatic glycogenolysis, and cyclicAMP is the sole intra-cellular messenger. This suggests that the -adrenergic mechanism became associated with the liver after amphibians separated from the vertebrate line. Reptiles separated later, and the aim of this study is to elucidate the hormonal control of hepatic glycogenolysis in a reptile,Amphibolurus nuchalis, and especially to determine which adrenergic receptor system is operative.InA. nuchalis liver pieces cultured in vitro, adrenaline and glucagon stimulated glycogen breakdown and glucose release, glycogen phosphorylase activity and accumulation of cyclicAMP in the tissue. Neurohypophysial peptides did not affect these parameters. These actions of adrenaline were completely blocked by the -adrenergic antagonist, propranolol and slightly reduced by the -adrenergic antagonist, phentolamine. Removal of Ca²⁺ from the medium and addition of the Ca²⁺ chelator, EGTA, did not block the actions of adrenaline, and the Ca²⁺ ionophore A23187 did not mimic these actions.The -adrenegic ligand [¹²⁵I]-iodocyanopindolol (ICP) bound specifically to an isolated membrane preparation fromA. nuchalis liver with a calculated K_D of 100 pM and a Bmax of 37.6 fmol·mg protein^–1. The adrenergic ligands propranolol, isoprenaline, adrenaline, noradrenaline, phenylephrine and phentolamine displaced ICP with K_D's of 20 nM, 1 M, 4.5 M, 32 M, 35 M and 500 M, respectively. The ₂-adrenergic ligand yohimbine did not bind specifically to the membrane, but at 1 nM and 100 pM, specific binding of the ₁-adrenergic ligand prazosin was 45% of total with a mean of 11.3 fmoles·mg protein^–1 specifically bound.These findings indicate that the glycogenolytic actions of adrenaline are mediated primarily via -adrenergic receptors inA. nuchalis, but that -adrenergic receptors may also play some role in the control of hepatic metabolism.     

Valine inhibition of β-isopropylmalate dehydrogenase takes part in the regulation of leucine biosynthesis inCandida maltosa

The -isopropylmalate (IPM) dehydrogenase (EC 1.1.1.85) ofCandida maltosa, the third pathway-specific enzyme of leucine biosynthesis, was purified, some properties of the enzyme were studied and a novel regulatory pattern was found. The K_m values of the enzyme were estimated to be 0.42 mM for -IPM and 0.34 mM for NAD⁺. It is demonstrated that the enzyme can be regulated by L-valine. The inhibition was competitive with respect to -IPM (K_i=1.84 mM) and non-competitive with respect to NAD⁺ (K_i=5.67 mM). Exogenous addition of L-valine toC. maltosa cells increased the intracellular pool of some intermediates of leucine biosynthesis (-ketoisovalerate, -IPM, -IPM), but has hardly influence on the leucine pool.     

Activation of fatty acids by non-glyoxysomal peroxisomes

Ethylene treatment (approx. 20 l ·1^-1 in air for 2 d) of tobacco (Nicotiana tabacum L. cv. Havana 425) plants markedly increases the endo--1,3-glucanase (EC 3.2.1.39) content of leaves. The antigenic form of the enzyme induced is the same one whose production is blocked by treating cultured cells with combinations of auxin (1.1 · 10^-5 M -naphthaleneacetic acid) and cytokinin (1.4 · 10^-6 M kinetin). Evidence is presented that cultured tobacco cells require ethylene for -1,3-glucanase accumulation: i) ethylene treatment increased the accumulation of \-1,3-glucanase in callus tissues >10 d after subculturing and in cell-suspension cultures; ii) callus tissues can produce ethylene; iii) conditions known to inhibit ethylene production (1 mM CoCl₂; 33° C treatment) or ethylene action (approx. 1.6 mmol · 1^-1 norbornadiene in air) inhibited -1,3-glucanase accumulation by callus tissues treated for 4 d following subculturing; and, these inhibitory effects were prevented by exogenous ethylene. Combinations of auxin and cytokinin blocked ethylene-induced accumulation of -1,3-glucanase by cell-suspension cultures. The results favor a model in which ethylene induces results favor a model in which ethylene induces 1,3-glucanase accumulation, and auxin and cytokinin inhibit this induction process.Abbreviations NAA -naphthaleneacetic acid - NDE norbornadiene     

Caecal water and electrolyte absorption and the effects of acetate and glucose, in dehydrated, low-NaCl diet hens

Summary In vivo electrolyte transport and water absorption from the caeca of dehydrated, low-NaCl diet hens are reported. In the absence of luminal glucose or acetate, net electrolyte transport rates and water absorption are small. When physiological concentrations of acetate (40 mM) are included in the perfusate, Na⁺ transport and water absorption increase significantly (P<0.01): 38±7 eqNa⁺/caecum kg·h and 256±33 l H₂O/caecum · kg · h.A similar increase in water absorption occurs with the inclusion of 15 mM glucose in the perfusate (219±30 l H₂O/caecum · kg · h), however both net Na⁺ and Cl^– absorption increase: 28±6 eq Na⁺/caecum · kg · h and 21±5 eq Cl^–/caecum kg · h.These pronounced increases in electrolyte and water absorption are not accompanied by any significant increase in transmural potential difference.The data presented establish caeca as important sites in the recuperation of water and electrolytes in dehydrated, low-NaCl diet hens.Abbreviations ECPD electrochemical potential difference - PD (transmural) potential difference - PEG polyethylene glycol     

Integral kinetics of the cleavage of maltose catalysed by α-glucosidase fromSaccharomyces carlsbergensis

Summary A new, sensitive and continuous assay for -glucosidase is described exploiting the different angles of rotation for the substrate maltose and the product glucose. Kinetic experiments revealed a very pronounced product inhibition of -glucosidase fromSaccharomyces carlsbergensis with a K_i of 4.85·10^–3 M for glucose.The K_M of maltose was found to be 37.8·10^–3 M. Taking these values, an integral kinetic curve for the enzymatic hydrolysis of maltose was calculated, which is shown to fit the experimental data.Symbols used k₁ (min^–1) pseudo first-order rate constant (for enzymatic cleavage) - k₂ (min^–1) rate constant (for mutarotation reaction) - I, P (mol/1) inhibitor (product) concentration - k_i (mmol/1) inhibitor constant - K_M (mmol/l) Michaelis constant - [M] ₅₈₉ ³⁰ (degree/m · l/mol) molecular rotation at 30°C and 589 nm - s (mmol/l) substrate concentration - R (mmol/mg · min) reaction rate - V_max (mmol/mg · min) maximal rate - U (mol/min) activity unit (here at 30°C and pH=6.8) Indices O initial value - max maximal value