Simultaneous nitrification and denitrification in a mixed methanotrophic culture

Simultaneous nitrification and denitrification using a mixed methanotrophic culture was investigated. When both NO₃ ^–-N (108 mg l^–1) and NH₃-N (59 mg l^–1) were added into batch reactors, nitrate removal was complete within 10 h at the rate of 47 mg NO₃ ^–-N g VSS^–1 day^–1 when dissolved oxygen (DO) concentration was maintained at 2 mg DO l^–1. Ammonia removal started simultaneously with nitrate removal at a slower rate of 14 NH₃-N g VSS^–1 day^–1. No significant accumulation of nitrite or nitrate during ammonia utilization suggested the occurrence of simultaneous nitrification and denitrification.     

Effects of a plume front on the distribution of inorganic and organic matter off the Rhône River

Hydrological and chemical structures off the Rhône River estuary resulting from the introduction of the river flow into the Mediterranean Sea are described. The effect of the fresh-water/sea-water interface on the distribution of inorganic and organic matter off the Rhône river is investigated. Strong vertical gradients of inorganic and dissolved organic matter such as lipids characterized the first few meters in this area (from 83.7 to 0.6 N-NO₃ µgat l^–1, from 6.39 to 0.92 N-NH₄ µgat l^–1 and from 299 to 73 µg l^–1 of total dissolved lipids). At the interface, substantial increases of particulate organic (PON: from 45 µg l^–1 at surface to 118 µg l^–1 at the interface, POC: from 462 to 876 µg l^–1, total particulate lipids: from 33 to 648 µg l^–1) and suspended matter in general (from 18 to 22.2 mg l^–1) were observed. High phytoplanktonic production may account for some of this enrichment, although passive accumulation might also be involved.     

Protein production from whey usingPenicillium cyclopium; growth parameters and cellular composition

Summary The growth parameters ofPenicillium cyclopium have been evaluated in a continuous culture system for the production of fungal protein from whey. Dilution rates varied from 0.05 to 0.20 h^–1 under constant conditions of temperature (28°C) and pH (3.5). The saturation coefficients in the Monod equation were 0.74 g l^–1 for lactose and 0.14 mg l^–1 for oxygen, respectively. For a wide range of dilution rates, the yield was 0.68 g g^–1 biomass per lactose and the maintenance coefficient 0.005 g g^–1 h^–1 lactose per biomass, respectively. The maximum biomass productivity achieved was 2 g l^–1 h^–1 biomass at dilution rates of 0.16–0.17 h^–1 with a lactose concentration of 20 g l^–1 in the feed. The crude protein and total nucleic acid contents increased with a dilution rate, crude protein content varied from 43% to 54% and total nucleic acids from 6 to 9% in the range of dilution rates from 0.05 to 0.2 h^–1, while the Lowry protein content was almost constant at approximately 37.5% of dry matter.Nomenclature (mg l^–1) C_o initial concentration of dissolved oxygen - (h^–1) D dilution rate - (mg l^–1) K₀₂ saturation coefficient for oxygen - (g l^–1) K_s saturation coefficient for substrate - (g g^–1 h^–1) lactose per biomass) m maintenance energy coefficient - (mM g^–1 h^–1O₂ per biomass) Q₀₂ specific oxygen uptake rate - (g l^–1) S residual substrate concentration at steady state - (g l^–1) S_o initial substrate concentration in feed - (min) t_1/2 time when C_o is equal to C_o/2 - (g l^–1) X biomass concentration - (g l^–1) X biomass concentration at steady state - (g g^–1 biomass per lactose) Y_G yield coefficient for cell growth - (g g^–1 biomass per lactose) Y_x/s overall yield coefficient - (h^–1) specific growth rate     

Studies on the variables and kinetics of SCP production from nopal fruit juice

Summary Submerged batch cultivation under controlled environmental conditions of pH 3.8, temperature 30°C, and K_La200 h^–1 (above 180 mMO₂ l ^–1 h^–1 oxygen supply rate) produced a maximum (12.0 g·l ^–1) SCP (Candida utilis) yield on the deseeded nopal fruit juice medium containing C/N ratio of 7.0 (initial sugar concentration 25 g·l ^–1) with a yield coefficient of 0.52 g cells/g sugar. In continuous cultivation, 19.9 g·l ^–1 cell mass could be obtained at a dilution rate (D) of 0.36 h^–1 under identical environmental conditions, showing a productivity of 7.2 g·l ^–1·h^–1. This corresponded to a gain of 9.0 in productivity in continuous culture over batch culture. Starting with steady state values of state variables, cell mass (C_X–19.9 g·l ^–1), limiting nutrient concentration (C_ln–2.5 g·l ^–1) and sugar concentration (C_S–1.5 g·l ^–1) at control variable conditions of pH 3.8, 30°C, and K_La 200 h^–1 keeping D=0.36 h^–1 as reference, transient response studies by step changes of these control variables also showed that this pH, temperature and K_La conditions are most suitable for SCP cultivation on nopal fruit juice. Kinetic equations obtained from experimental data were analysed and kinetic parameters determined graphically. Results of SCP production from nopal fruit juice are described.Nomenclature C_ln concentration of ammonium sulfate (g·l ^–1) - C_S concentration of total sugar (g·l ^–1) - C_X cell concentration (g·l ^–1) - D dilution rate (h^–1) - K_ln Monod's constant (g·l ^–1) - m maintenance coefficient (g ammonium sulfate cell^–1 h^–1) - m_(S) maintenance coefficient (g sugar g cell^–1 h^–1) - t time, h - Y yield coefficient (g cells/g ammonium sulfate) - Y_m maximum of Y - Y_S yield coefficient based on sugar consumed (g cells · g sugar^–1) - Y_S(m) maximum value of Y_S - ^µm maximum specific growth rate constant (h^–1)     

Sequential kinetic parameter estimation of anaerobic fluidized bed bioreactor using an optimization technique

Mathematical model parameters for the methanogenic degradation of propylene glycol were estimated in a sequential manner by means of an optimization technique. Model parameters determined from an initial experimental data set using one bioreactor were then verified with the results from a second bioreactor. The proposed methodology is a useful tool to obtain model parameters for continuous flow reactors with completely mixed regime. Abbrevations: S – substrate concentration (mg COD l^–1); S _in – influent substrate concentration (mg COD l^–1); D _L – dilution rate (day^–1); – stoichiometric coefficients (ND); nx – number of microbial species (ND); X _S – fixed biomass concentration (mg biomass l^–1); X _L – suspended biomass concentration of (mg biomass l^–1); k _d – decay rate of biomass (day^–1); b _S – specific detachment rate of biofilm (day^–1); – specific growth rate of biomass (day^–1); _m – maximum specific growth rate of biomass (day^–1); K _S – half saturation constant (mg COD l^–1); K _I – inhibition constant (mg COD l^–1).     

Organic reduction of tapioca wastewaters using modified RBC

A modified Rotating Biological Contactor (RBC) was used for the treatability studies of synthetic tapioca wastewaters. The RBC used was a four stage laboratory model and the discs were modified by attaching porous nechlon sheets to enhance biofilm area. Synthetic tapioca wastewaters were prepared with influent concentrations from 927 to 3600 mg/l of COD. Three hydraulic loads were used in the range of 0.03 to 0.09 m³·m^–2·d^–1 and the organic loads used were in the range of 28 to 306 g COD· m^–2·d^–1. The percentage COD removal were in the range from 97.4 to 68. RBC was operated at a rotating speed of 18 rpm which was found to be the optimal rotating speed. Biokinetic coefficients based on Kornegay and Hudson models were obtained using linear analysis. Also, a mathematical model was proposed using regression analysis.List of Symbols A m² total surface area of discs - d m active depth of microbial film onany rotating disc - K _s mg ·l^–1 saturation constant - P mg·m^–2·^–1 area capacity - Q l·d^–1 hydraulic flow rate - q m³·m^–2·d^–1 hydraulic loading rate - S ₀ mg·l^–1 influent substrate concentration - S _e mg·l^–1 effluent substrate concentration - w rpm rotational speed - V m³ volume of the reactor - X _f mg·l^–1 active biomass per unit volume ofattached growth - X _s mg·l^–1 active biomass per unit volume ofsuspended growth - X mg·l^–1 active biomass per unit volume - Y _s yield coefficient for attachedgrowth - Y _A yield coefficient for suspendedgrowth - Y yield coefficient, mass of biomass/mass of substrate removed Greek Symbols hr mean hydraulic detention time - (_max)_A d^–1 maximum specific growth rate forattached growth - (_max)_s d^–1 maximum specific growth rate forsuspended growth - _max d^–1 maximum specific growth rate - d^–1 specific growth rate - _v mg·l^–1·hr^–1 maximum volumetric substrateutilization rate coefficient     

Conversion of cellulose into fungal cell mass

Summary Chaetomium cellulolyticum (ATCC 32319) was cultivated on glucose, Avicel and/or Sigmacell in a 20-1 stirred tank batch reactor. The substrate (cellulose) concentration, the cell mass concentration (through protein and/or nitrogen content), reducing sugar concentration, the enzyme activity, the alkali consumption rate, the dissolved O₂ and CO₂ concentrations in the outlet gas were measured. The specific growth rate, the substrate yield coefficient, cell productivity, the oxygen consumption rate, the CO₂ production rate and the volumetric mass transfer coefficient were determined. At the beginning of the growth phase the oxygen utilization rate exhibits a sharp maximum. This maximum could be used to start process control. Because of the long lag phase periodic batch operation is recommended.Symbols CP cell protein concentration (g l^–1) - FPA FP enzyme activity (IU l^–1) - GP dissolved protein concentration (g l^–1) - IU international unit of enzyme activity - k_La volumetric mass tranfer coefficient (h^–1) - LG alkali (1 n NaOH) consumption (ml) - LGX specific alkali consumption rate per cell mass (ml g^–1 h^–1) - P cell mass productivity (g l^–1 h^–1) - specific oxygen consumption rate per cell mass (g g^–1 h^–1) - Q aeration rate (volumetric gas flow rate per volume of medium, vvm) (min^–1) - N impeller speed (revolution per minute, rpm) (min^–1) - S substrate concentration (g l^–1) - S⁰ S at t_F=0 (g l^–1) - S₀ S in feed (g l^–1) - SR acid consumption (ml) - TDW total dry weight (g l^–1) - T temperature (° C) - t_F cultivation time (h) - U substrate conversion - X cell mass concentration (g l^–1) - Y_X/S vield coefficient - specific growth rate (h^–1) - _m maximum specific growth rate (h^–1)     

Mixed inhibitions by methanol, furfural and acetic acid on xylitol production by Candida guilliermondii

Xylose production by Candida guilliermondii FTI 20037 was carried out in a synthetic medium in the presence of 0–100 g methanol l^–1, 0–0.7 g furfural l^–1 or 0–1.3 g acetic acid l^–1. Kinetic results show a mixed inhibition mechanism in all three cases. Maximum specific productivity and saturation constant for product formation were, in the absence of inhibition, 3.6 g_P g_X ^–1 h^–1 and 232 g_S l^–1, respectively, while the inhibition constants, K _i and K _i, were 17 and 50 g methanol l^–1, 0.62 and 7.0 g furfural l^–1, 0.69 and 3.5 g acetic acid l^–1, which suggests the following order of inhibition: furfural > acetic acid > methanol.     

Limitations in substrate utilization efficiency by Zymomonas mobilis

Summary Optimal growth conditions for Zymomonas mobilis have been established using continuous cultivation methods. Optimal substrate utilization efficiency occurs with 2.5 g l^–1 yeast extract, 2.0 g l^–1 ammonium sulfate and 6.0 g l^–1 magnesium sulfate in the media. Catabolic activity is at its maximum with glucose uptake rates of 16–18 g l^–1 h^–1 and ethanol production rates of 8–9 g l^–1 h^–1, Q_g values of 22–26 and Q_p values between 11 and 13, which results in 40 g l^–1 h^–1 ethanol yields using a 100 g l^–1 substrate feed. Any increase in these parameters goes on cost of substrate utilization efficiency. Calcium pantothenate can not substitute yeast extract.Abbreviations G Glucose (%) - Pant Calcium pantothenate (mg l^–1) - D Dilution rate (h^–1) - NH₄ Ammonium sulfate (%) - M_g Magnesium sulfate (%) - S₁ Residual glucose in the fermenter (g l^–1) - S₀ Glucose feed (g l^–1) - Eth Ethanol concentration (g l^–1) - GUR Glucose uptake rate (g l^–1 h^–1) - Q_g Specific glucose uptake rate (g g^–1 h^–1) - Q_p Specific ethanol production rate (g g^–1 h^–1) - EPR Ethanol production rate (g l^–1 h^–1) - Y_g Yield coefficient for glucose (g g^–1) - Y_p Conversion efficiency (%) - C Biomass concentration (g l^–1) Present address: (Until June 1982) Institut für Mikrobiologie, TH Darmstadt, 6100 Darmstdt, Federal Republic of Germany     

Effects of growth temperature on maximal specific growth rate,yield, maintenance,and death rate in glucose-limited continuous culture of the thermophilic Bacillus caldotenax

Summary The influence of temperature on the growth of the theromophilic Bacillus caldotenax was investigated using chemostat techniques and a chemically defined minimal medium. All determined growth constants, that is maximal specific growth rate, yield and maintenance, were temperature dependent. It was striking that the very large maintenance requirement was about 10 times higher than for mesophilic cells under equivalent conditions. A death rate, which was very substantial at optimal and supraoptimal growth temperatures, was estimated by comparing the maintenance for substrate and oxygen. There was no indication for a thermoadaptation as postulated by Haberstich and Zuber (1974).Symbols D Dilution rate (h^–1) - D_c=_max Critical dilution rate (h^–1) - E Temperature characteristic (J mol^–1) - k Organism constant - k_d Death rate coefficient (h^–1) - k_m Maintenance substrate coefficient estimated from M_O (h^–1) - M_O Maintenance respiration, mmol O₂ per g dry biomass and h (mmol g^–1h^–1) - M_O Maintenance respiration, taking k_d into account - m_S Maintenance substrate coefficient, g glucose per g dry biomass and h (h^–1) - OD Optical density at 546 nm - QO₂ Specific O₂-uptake rate (mmol g^–1h^–1) - Q _O2 ^V Specific O₂-uptake rate for viable portion of biomass (mmol g^–1 h^–1) - Q_S Specific glucose uptake rate (h^–1) - Q _S ^V Specific glucose uptake rate for viable portion of biomass (h^–1) - R Gas constant 8.28 J mol^–1K^–1 - S Substrate concentration in reactor (g l^–1) - S_O Influent substrate concentration (g l^–1) - T_max Maximal growth temperature (°C) - T_min Minimal growth temperature (°C) - X Dry biomass (g l^–1) - X_tOt=X Dry biomass containing dead and viable cells - X_v Viable portion of biomass - Y _O ^m Potential yield for O₂ corrected for maintenance respiration (g mol^–1) - Y _S ^m Potential yield for substrate corrected for maintenance requirement, g biomass per g glucose (–) - Specific growth rate (h^–1) - _max Maximal specific growth rate (h^–1)     

Effects of solar radiation,humic substances and nutrients on phytoplankton biomass and distribution in Lake Solumsjö, Sweden

Impacts of solar radiation, humic substances and nutrients on phytoplankton abundance at different depths were investigated in a temperate dimictic lake, Lake Solumsjö. Penetration of solar radiation profiles at different depths, represented as light attenuation coefficient (K _d) were examined. Water sampling and downward irradiance of photosynthetically active radiation (PAR), ultraviolet-A (UV-A, 320–400 nm) and ultraviolet-B (UV-B, 280–320 nm) radiation were performed once a week and at three different times of the day (08.00, 12.00 and 16.00 hrs, local time) between September 13 and November 1, 1999. During the period of investigation, solar radiation above the water surface declined from 474 to 94 mol m^–2 s^–1 for PAR, from 1380 to 3.57 W m^–2 for UV-A and from 13.1 to 0.026 W m^–2 for UV-B, respectively. The attenuation coefficient (K _d) for UV-B radiation ranged from 3.7 to 31 m^–1 and UV-B radiation could not be detected at depths greater than 0.25 m. Humic substances measured at 440 nm ranged from 35.5 to 57.7 Pt mg l^–1. Mean values of biomass, estimated from chlorophyll a, in the whole water column (0–10 m) varied between 2.3 and 5.6 g l^–1 and a diel fluctuation was observed. During stratified conditions, high levels of iron (1.36 mg l^–1) and manganese (4.32 mg l^–1) were recorded in the hypolimnion, suggesting that the thermocline played a major role in the vertical distribution of phytoplankton communities in Lake Solumsjö. The high levels of iron and manganese stimulated the growth of Trachelomonas volvocinopsis in the hypolimnion at a depth of 10 m. Negative impacts of UV-B radiation on phytoplankton in lake Solumsjö are reduced due to the high levels of humic substances and the high degree of solar zenith angle at the latitude studied.     

Mechanism of Na+/proline symport inEscherichia coli: Reappraisal of the effect of cation binding to the Na+/proline symport carrier

Summary Recently we proposed that cytoplasmic acidification of low K⁺ (LK) sheep erythrocytes may stimulate ouabain-resistant Cl^–-dependent K⁺ flux (K⁺Cl^– cotransport), also known to be activated by cell swelling, treatment with N-ethylmaleimide (NEM), or removal of cellular bivalent cations. Here we studied the dependence of K⁺ transport on intracellular and extracellular pH (pH _i , pH _o ) varied either simultaneously or independently using the Cl^–/HCO ₃ ^– exchange inhibitor 4,4, diisothiocyanatostilbene-3,2-disulfonic acid (DIDS). In both control and NEM-treated LK cells volumes were kept near normal by varying extracellular sucrose. Using DIDS as an effective pH clamp, both K⁺ efflux and influx of Rb⁺ used as K⁺ congener were strongly activated at acid pH _i and alkaline pH _o . A small stimulation of K⁺ (Rb⁺) flux was also seen at acid pH _i in the absence of DIDS, i.e., when pH _i pH _o . Anti-L _l serum, known to inhibit K⁺Cl^– cotransport, prevented the pH _i -stimulated K⁺ (Rb⁺) fluxes. Subsequent to NEM treatment at pH 6, K⁺ (Rb⁺) fluxes were activated only by raising pH, and thus were similar to the pH activation profile of K⁺ (Rb⁺) fluxes in DIDS-treated cells with pH _o varied at constant physiologic pH _i . Anti-L _l , which inhibited NEM-stimulated K⁺ (Rb⁺) fluxes, failed to do so in NEM-plus DIDS-treated cells. Thus, NEM treatment interferes with the internal but not with the external pH-sensitive site.     

Gill (Na+,K+)-ATPase from the blue crab Callinectes danae: modulation of K+-phosphatase activity by potassium and ammonium ions

The kinetic properties of a microsomal gill (Na⁺,K⁺)-ATPase from the blue crab Callinectes danae were analyzed using the substrate p-nitrophenylphosphate. The (Na⁺,K⁺)-ATPase hydrolyzed PNPP obeying cooperative kinetics (n=1.5) at a rate of V=125.4±7.5 U mg⁻¹ with K_0.5=1.2±0.1 mmol l⁻¹; stimulation by potassium (V=121.0±6.1 U mg⁻¹; K_0.5=2.1±0.1 mmol l⁻¹) and magnesium ions (V=125.3±6.3 U mg⁻¹; K_0.5=1.0±0.1 mmol l⁻¹) was cooperative. Ammonium ions also stimulated the enzyme through site–site interactions (n_H=2.7) to a rate of V=126.1±4.8 U mg⁻¹ with K_0.5=13.7±0.5 mmol l⁻¹. However, K⁺-phosphatase activity was not stimulated further by K⁺ plus NH₄⁺ ions. Sodium ions (K_I=36.7±1.7 mmol l⁻¹), ouabain (K_I=830.3±42.5 μmol l⁻¹) and orthovanadate (K_I=34.0±1.4 nmol l⁻¹) completely inhibited K⁺-phosphatase activity. The competitive inhibition by ATP (K_I=57.2±2.6 μmol l⁻¹) of PNPPase activity suggests that both substrates are hydrolyzed at the same site on the enzyme. These data reveal that the K⁺-phosphatase activity corresponds strictly to a (Na⁺,K⁺)-ATPase in C. danae gill tissue. This is the first known kinetic characterization of K⁺-phosphatase activity in the portunid crab C. danae and should provide a useful tool for comparative studies.     

Biodegradation of 4-aminobenzenesulphonate by a newly isolated bacterial strain PNS-1

A bacterial strain PNS-1, isolated from activated sludge derived from a domestic wastewater treatment unit, could utilize 4-aminobenzenesulphonate (4-ABS) as a sole organic carbon and energy source under aerobic conditions. Degradation rate varied with the initial concentration of 4-ABS and maximum specific substrate removal rate was observed at 400mg 4-ABS l^–1 (2.3mM). Average biomass yield was 0.31mg/mg 4-ABS degraded. Biokinetic parameters for the degradation, determined using the Haldane relationship, were 0.26h^–1 (_max), 6mg\,l^–1 (K_S) and 4020mg\,l^–1 (K_i). Strain PNS-1 could not utilize other isomers of benzenesulphonate and 5-sulphosalicylate as growth substrates whereas protocatechuate, pyrocatechuate and p-hydroxybenzoate could be degraded. In mixed substrate batch cultivations, where 4-ABS was one of the component, protocatechuate and 4-ABS were simultaneously utilized. Presence of 2- or 3-ABS decreased the growth and substrate degradation rates of 4-ABS. With 4-ABS and pyrocatechuate, although a lag phase was observed prior to pyrocatechuate degradation, a diauxic growth pattern was not seen.     

Denitrification kinetics of simulated fish processing wastewater at different ratios of nitrate to biomass

Denitrification was studied in anoxic batch cultures of a simulated fish processing wastewater at 37 r C and pH 7.5, using a denitrifying enrichment culture from fishery wastewater. Different initial nitrate to biomass ratios (So/Xo) were used: nitrate and biomass varied from 7.5 to 94.7 mg NO₃-N l^–1, and from 20 to 4300 mg volatile suspended solids l^–1, respectively. The specific maximum denitrification rate (r _m) and the cell yield (Y _{X / S}) depended on the So/Xo ratio under anoxic conditions: r _m increased from 1.2 to 1584 mg NO₃-N g^–1 VSS h^–1 and Y _{X / S} decreased from 42 to 0.03 mg VSS mg^–1 NO₃-N when So/Xo varied from 5.5 10^{– 3} to 9.3 mg NO₃-N/mg VSS. Nomenclature C_{NO3 – N} nitrate concentration, mg NO₃-N l^–1 K _S saturation constant, mg NO₃-N l^–1 r _m specific maximum denitrification rate, mg NO₃-N g^–1 VSS h^–1 So initial substrate concentration, mg l^–1 t time, h TOC total organic carbon VSS volatile suspended solids x biomass concentration, g VSS l^–1 Xo initial biomass concentration, g VSS l^–1 Y _X/S substrate to biomass cell yield, mg VSS/mg N Greek symbols: _m maximum specific growth rate of the anoxic microbial population, 1 h^–1     

Growth ofPhormidium sp. in aerobic secondary piggery waste-water

The potential of a cyanobacteriumPhormidium sp., for the tertiary treatment of piggery waste-water chemical oxygen demand , 3000 mg·1^–1, using an aerobically stabilized secondary effluent, was studied. Batch cultures were carried out in 2-1 glass reactors and in a 30-1 glass-fibre carousel reactor. The nutrient removal efficiency as well as biomass production were compared in synthetic mineral medium and in different concentrations of aerobically stabilized piggery effluent. The best performance ofPhormidium sp. ocurred in diluted stabilized secondary effluent (1:1). Removal efficiencies were 100% for P-PO₄ ^–3, 50% for N-NH₄ ^–1 and 35% for N-NO₃ ^– in small-volume cultures; and 31% for P-PO₄ ^–3, 100% for N-NH₄ ^– and 70% for N-NO₃ ^– in an open carousel reactor. Biomass production on the aerobically stabilized effluent was six times higher in the 2-1 reactors and 1.7 times higher in the carousel reactor when compared to the synthetic medium.     

Intracellular potassium activity and the role of potassium in transepithelial salt transport in the human reabsorptive sweat duct

Summary We have measured the intracellular potassium activity, [K⁺]_i and the mechanisms of transcellular K⁺ transport in reabsorptive sweat duct (RSD) using intracellular ion-sensitive microelectrodes (ISMEs). The mean value of [K⁺]_i in RSD is 79.8±4.1mm (n=39). Under conditions of microperfusion, the [K⁺]_i is above equilibrium across both the basolateral membrane, BLM (5.5 times) and the apical membrane, APM (7.8 times). The Na⁺/K⁺ pump inhibitor ouabain reduced [K⁺]_i towards passive distribution across the BLM. However, the [K⁺]_i is insensitive to the Na⁺/K⁺/2 Cl^– cotransport inhibitor bumetanide in the bath. Cl^– substitution in the lumen had no effect on [K⁺]_i. In contrast, Cl^– substitution in the bath (basolateral side) depolarized BLM from –26.0±2.6 mV to –4.7^*±2.4 mV (n=3;^* indicates significant difference) and decreased [K⁺]_i from 76.0±15.2mm to 57.7^* ±12.7mm (n=3). Removal of K⁺ in the bath decreased [K⁺]_i from 76.3±15.0mm to 32.3^*±7.6mm (n=4) while depolarizing the BLM from –32.5±4.1 mV to –28.3^*±3.0 mV (n=4). Raising the [K⁺] in the bath by 10-fold increased [K⁺]_i from 81.7±9.0mm to 95.0^*±13.5mm and depolarized the BLM from –25.7±2.4 mV to –21.3^*±2.9 mV (n=4). The K⁺ conductance inhibitor, Ba²⁺, in the bath also increased [K⁺]_i from 85.8±6.7mm to 107.0^*±11.5mm (n=4) and depolarized BLM from –25.8±2.2 mV to –17.0^*±3.1 mV (n=4). Amiloride at 10^–6 m increased [K⁺]_i from 77.5±18.8mm to 98.8^*±21.6mm (n=4) and hyperpolarized both the BLM (from –35.5±2.6 mV to –47.8^*±4.3 mV) and the APM (from –27.5±1.4 mV to –46.0^* ±3.5 mV,n=4). However, amiloride at 10^–4 m decreased [K⁺]_i from 64.5±0.9mm to 36.0^*±9.9mm and hyperpolarized both the BLM (from –24.7±1.4 mV to –43.5^*±4.2 mV) and APM (from –18.3±0.9 mV to –43.5^*±4.2 mV,n=6). In contrast to the observations at the BLM, substitution of K⁺ or application of Ba²⁺ in the lumen had no effect on the [K⁺]_i or the electrical properties of RSD, indicating the absence of a K⁺ conductance in the APM. Our results indicate that (i) [K⁺]_i is above equilibrium due to the Na⁺/K⁺ pump; (ii) only the BLM has a K⁺ conductance; (iii) [K⁺]_i is subject to modulation by transport status; (iv) K⁺ is probably not involved in carrier-mediated ion transport across the cell membranes; and (v) the RSD does not secrete K⁺ into the lumen.     

Intracellular K+ activities and cell membrane potentials in a K+-transporting epithelium,the midgut of tobacco hornoworm (Manduca sexta)

Summary Transbasal electrical potential (V _b) and intraepithelial potassium chemical activity ((K⁺) _i ) were measured in isolated midgut epithelium of tobacco hornworm (Manduca sexta) using double-barrelled glass microelectrodes. Values ofV _b ranging from +8 to –48 mV (relative to blood side) were recorded. For all sites, (K⁺) _i is within a few millivolts of electrochemical equilibrium with the blood side bathing solution. Sites more negative than –20 mV show relatively high sensitivity ofV _b to changes in blood side K⁺ concentration: 43% of these sites can be marked successfully with iontophoresed Lucifer yellow CH dye and shown to represent epithelial cells of all three types present in the midgut. In about half of successful marks, dye-coupling of several adjacent cells is seen. Low potential sites — those withV _b less negative than –20 mV —typically do not show high sensitivity ofVb to changes of external K⁺, but rather (K⁺) _i rapidly approaches the K⁺ activity of blood side bathing solution. These sites can seldom be marked with Lucifer yellow (4% success). The mean (K⁺) _i of the high potential sites is 95±29 (sd)mm under standard conditions, a value which is in accord with published values for the whole tissue.     

Sequential liquid-liquid extraction of d-amino acid oxidase from Trigonopsis variabilis

A method for isolation of d-amino acid oxidase (DAAO) from disrupted Trigonopsis variabilis cells has been developed. In an aqueous two-phase system consisting of PEG6000 (220 g l^–1), potassium phosphate (110 g l^–1, K₂HPO₄ + KH₂PO₄ = 10.1:1, mol mol^–1) and dl-methionine (11 g l^–1), the major portion of cellular proteins (87%) was partitioned into the salt phase. By sequential extraction, 48% of DAAO was recovered in PEG phase, giving a yield of 211 U mg protein^–1.