Effect of extraction temperature on the diffusion coefficient of polysaccharides from Spirulina and the optimal separation method

The extraction temperature had a significant impact on the concentration of polysaccharides derived from solid-liquid extraction of Spirulina. The polysaccharide concentration was significantly higher when the extraction was performed at 90°C than when it was performed at 80, 70, and 50°C. This result is related to the diffusion coefficients of the polysaccharides, which increased from 1.07 × 10^?12 at 50°C to 3.02 × 10^?12 m²/sec at 90°C. Using the Arrhenius equation, the pre-exponential factor (D ₀ ) and the activation energy (E _a ) for Spirulina polysaccharide extraction were calculated as 7.958 × 10^?9 m²/sec and 24.0 kJ/mol, respectively. Among the methods used for the separation of Spirulina polysaccharides, cetyltrimethylammonium bromide (CTAB, method I) and organic solvent (ethanol, in methods II and III) provided similar yields of polysaccharides. However, the separation of polysaccharides using an ultrafiltration (UF) process (method III) and ethanol precipitation was superior to separation via CTAB or vacuum rotary evaporation (method II). The use of a membrane with a molecular weight cut-off (MWCO) of 30 kDa and an area of 0.01 m² at a feed pressure of 103 kPa with a mean permeate flux of 39.3 L/m²/h and a retention rate of 95% was optimal for the UF process. The addition of two volumes (v/v) of ethanol, which gave a total polysaccharide content of approximately 4% dry weight, was found to be most suitable for polysaccharide precipitation. The results of a Sepharose 6B column separation showed that the molecular weights of the polysaccharides in fractions I and II were 212 and 12.6 kDa, respectively.     

Influence of pH and salt concentration on the cross-flow microfiltration of BSA through a ceramic membrane

In this paper, the influence of pH in the 4–8 interval and NaCl concentration up to 25 mM on the cross-flow microfiltration of BSA was investigated. A tubular ceramic membrane with a pore size of 0.14 μm was employed and its point of zero charge was calculated. The evolution of permeate flow and BSA transmission with time was determined at 45 °C, a cross-flow velocity of 3.5 m/s and a transmembrane pressure of 100 kPa. The curves of permeate flow were explained according to the resistances in series model. Maximum protein transmission was obtained at the isoelectric point of BSA (4.9), with significant transmission also at the point of zero charge of the membrane and null transmission at pH 4 and 8. The highest permeate flow was observed at pH 7 and the lowest at 4.9. Finally, the addition of salt resulted to some extent in an improvement of both protein transmission and permeate flow.     

Effects of by-products of fermentation of banana pseudostem on ethanol separation by pervaporation

In this work, we performed recovery of ethanol from a fermentation broth of banana pseudostem by pervaporation (PV) as a lower-energy-cost alternative to traditional separation processes such as distillation. As real fermentation systems generally contain by-products, it was investigated the effects of different components from the fermentation broth of banana pseudostem on PV performance for ethanol recovery through commercial flat sheet polydimethylsiloxane (PDMS) membrane. The experiments were compared to a binary solution (ethanol/water) to determine differences in the results due to the presence of fermentation by-products. A real fermented broth of banana pseudostem was also used as feed for the PV experiments. Seven by-products from fermented broth were identified: propanol, isobutanol, methanol, isoamyl alcohol, 1-pentanol, acetic acid, and succinic acid. Moreover, the residual sugar content of 3.02 g/L¹ was obtained. The presence of methanol showed the best results for total permeate flux (0.1626 kg·m⁻²·h⁻¹) and ethanol permeate flux (0.0391 kg·m⁻²·h⁻¹) during PV at 25°C and 3 wt% ethanol, also demonstrated by the selectivity and enrichment factor. The lowest total fluxes of permeate were observed in the experiments containing the acids. Better permeance of 0.1171 from 0.0796 kg·m⁻²·h⁻¹ and membrane selectivity of 9.77 from 9.30 were obtained with real fermentation broth than with synthetic solutions, possibly due to the presence of by-products in the multicomponent mixtures, which contributed to ethanol permeation. The results of this work indicate that by-products influence pervaporation of ethanol with hydrophobic flat sheet membrane produced from the fermented broth of banana pseudostem.     

Pretreatment with alum or powdered activated carbon reduces bacterial predation-associated irreversible fouling of membranes

This study evaluated the co-application of bacterial predation by Bdellovibrio bacteriovorus and either alum coagulation or powdered activated carbon adsorption to reduce fouling caused by Escherichia coli rich feed solutions in dead-end microfiltration tests. The flux increased when the samples were predated upon or treated with 100 ppm alum or PAC, but co-treatment with alum and predation gave the best flux results. The total membrane resistance caused by the predated sample was reduced six-fold when treated with 100 ppm PAC, from 11.8 to 1.98 × 10¹¹ m^?1, while irreversible fouling (R_p) was 2.7-fold lower. Treatment with 100 ppm alum reduced the total resistance 14.9-fold (11.8 to 0.79 × 10¹¹ m^?1) while the R_p decreased 4.25-fold. SEM imaging confirmed this, with less obvious fouling of the membrane after the combined process. This study illustrates that the combination of bacterial predation and the subsequent removal of debris using coagulation or adsorption mitigates membrane biofouling and improves membrane performance.     

Phosphate transport in Ehrlich ascites tumor cells and the effect of arsenate

The effect of extracellular Pi and arsenate on Pi-transport in Ehrlich ascites tumor cells has been studied. Pi-transport can be described by Michaelis-Menten kinetics; the maximal flux equal to 44 mmoles (kg cell water)^?1 hour^?1 and K_m equal to 3.3 × 10^?4 M . Arsenate is a competitive inhibitor of Pi-transport with an inhibition constant (K_i) equal to 2.41 × 10^?3 M . The data support the hypothesis that cellular Pi is regulated by the cell membrane through the mediation of a carrier system.     

Liposomes modulate docetaxel-induced lipid oxidization and membrane damage in human hepatoma cells

The aim of this study was to investigate the effect of liposomes on docetaxel-induced lipid oxidization and membrane damage in human hepatoma cells. Cytotoxicity of free docetaxel and docetaxel-containing liposomes was evaluated by 3-(4,5-dimethylthiazol-2-yl)-2,5-diphenyltetrazolium (MTT) assay in human hepatoma cell lines HepG2 and SMMC-7721. To the cell lines, blank liposomes prepared with soybean phosphatidylcholine (SPC), dimyristoylphosphocholine (DMPC), and dioleoylphosphocholine (DOPC) did not show any significant toxicity below a 0.02-mg/mL phospholipid concentration. On the other hand, free docetaxel showed IC₅₀ values of 9.13?×?10^?6?±?1.54?×?10^?5 and 1.58?×?10^?2?±?2.71?×?10^?2 mg/mL in HepG2 cells and SMMC-7721 cells, respectively, after of 24 hours of incubation. IC₅₀ values of docetaxel-encapsulating liposomes, measured in terms of total docetaxel concentration, were at least 1.5-fold higher than those of free docetaxel. SPC liposomes reduced cellular damage caused by free docetaxel, as evidenced by the attenuation of docetaxel-induced lactate dehydrogenase (LDH) leakage by over 11% after liposome encapsulation at each dosage. Docetaxel-induced oxidative membrane damage was monitored by the formation of the lipid peroxidation product, malondialdehyde (MDA), and the antioxidative property of SPC liposome was monitored by the suppression of superoxide dismutase (SOD). These data demonstrated that free docetaxel facilitated MDA formation and suppressed SOD, and that these membrane-damaging effects were reduced by SPC liposomes.     

A one-step procedure for immobilising the thermostable carbonic anhydrase (SspCA) on the surface membrane of Escherichia coli

The carbonic anhydrase superfamily (CA, EC 4.2.1.1) of metalloenzymes is present in all three domains of life (Eubacteria, Archaea, and Eukarya), being an interesting example of convergent/divergent evolution, with its seven families (α-, β-, γ-, δ-, ζ-, η-, and θ-CAs) described so far. CAs catalyse the simple, but physiologically crucial reaction of carbon dioxide hydration to bicarbonate and protons. Recently, our groups characterised the α-CA from the thermophilic bacterium, Sulfurihydrogenibium yellowstonense finding a very high catalytic activity for the CO₂ hydration reaction (k_cat?=?9.35?×?10⁵?s^?1 and k_cat/K_m?=?1.1?×?10⁸?M^?1?s^?1) which was maintained after heating the enzyme at 80?°C for 3?h. This highly thermostable SspCA was covalently immobilised within polyurethane foam and onto the surface of magnetic Fe₃O₄ nanoparticles. Here, we describe a one-step procedure for immobilising the thermostable SspCA directly on the surface membrane of Escherichia coli, using the INPN domain of Pseudomonas syringae. This strategy has clear advantages with respect to other methods, which require as the first step the production and the purification of the biocatalyst, and as the second step the immobilisation of the enzyme onto a specific support. Our results demonstrate that thermostable SspCA fused to the INPN domain of P. syringae ice nucleation protein (INP) was correctly expressed on the outer membrane of engineered E. coli cells, affording for an easy approach to design biotechnological applications for this highly effective thermostable catalyst.     

Extraction of laminarin from Saccharina latissima seaweed using cross-flow filtration

Laminarin is a low-molecular-weight polysaccharide found in seaweed (kelp), often in equal concentrations to that in the commercially important hydrocolloid alginate. However, while alginate can be easily recovered by dissolution followed by acid precipitation, for laminarin, there is no such straightforward way of recovering it. Laminarin can be used as dietary fiber and, if efficiently extracted, it may be used for functional food/feed applications and as a component in plant defense stimulants for agriculture. One way of concentrating laminarin from dilute solutions is to press the solution through ultrafine membranes that the molecules cannot pass through. When alginate is extracted, an acid pretreatment step is used and the dilute acid residue from that process also contains laminarin. We used cross-flow filtration to concentrate laminarin from Saccharina latissima, retrieving it from the dilute acid solution of the acid pretreatment of an alginate extraction. Three ceramic membranes with 5, 15, and 50 kDa molecular weight cutoffs were used, and the pressure, temperature, and feed velocity were altered to reveal which parameters controlled the flow through the membrane and how efficiently laminarin was concentrated. The effects on laminarin extraction for fresh vs. frozen biomass were evaluated showing that frozen biomass releases more laminarin with a similar biomass homogenization technique. Thermal and microbial degradation of the feed components was studied during the course of the filtrations, showing that microbial degradation can affect the laminarin concentration, while the temperature of the process ~ 65 °C had little impact on laminarin. The techniques used to monitor the components in the feed and permeate during filtration were nuclear magnetic resonance, ¹H-NMR, and size exclusion chromatography. The filtrations were performed in a pilot-size filtration unit with ceramic membranes (ZrO₂/TiO₂, TiO₂-Al₂O support, 0.08 m²). To be able to operate without quick membrane fouling, the most important parameter was to have a high liquid velocity over the membrane, 4.7 m?s^?1. A good technique to concentrate laminarin was to prefilter it through a 50-kDa membrane using 2 bar liquid pressure and to concentrate it over a 5-kDa membrane using 5-bar liquid pressure. With these settings, the liquid flux through the filter became 60–80 and 30–40 L?m^?2?h^?1 over the 50-kDa and 5-kDa membrane.

     

Spectroscopic Studies on the Interaction of Fluorine Containing Triazole with Bovine Serum Albumin

The binding of one fluorine including triazole (C₁₀H₉FN₄S, FTZ) to bovine serum albumin (BSA) was studied by spectroscopic techniques including fluorescence spectroscopy, UV–Vis absorption, and circular dichroism (CD) spectroscopy under simulative physiological conditions. Fluorescence data revealed that the fluorescence quenching of BSA by FTZ was the result of forming a complex of BSA–FTZ, and the binding constants (K _a) at three different temperatures (298, 304, and 310 K) were 1.516?×?10⁴, 1.627?×?10⁴, and 1.711?×?10⁴?mol L^?1, respectively, according to the modified Stern–Volmer equation. The thermodynamic parameters ΔH and ΔS were estimated to be 7.752 kJ mol^?1 and 125.217 J?mol^?1?K^?1, respectively, indicating that hydrophobic interaction played a major role in stabilizing the BSA–FTZ complex. It was observed that site I was the main binding site for FTZ to BSA from the competitive experiments. The distance r between donor (BSA) and acceptor (FTZ) was calculated to be 7.42 nm based on the Förster theory of non-radioactive energy transfer. Furthermore, the analysis of fluorescence data and CD data revealed that the conformation of BSA changed upon the interaction with FTZ.     

Potassium Channels in Eremosphaera viridis: Modulation of Channel Opening,Conductance and Inhibition*

I/V relationships were performed by the voltage clamp technique in the sphaerical green alga Eremosphaera viridis de Bary. We focused on the course of the transient potential (TP) found in light-off experiments when specific potassium channels open. I/V measurements done during this period show a N-shaped curve. The shape depended on external potassium. TPs could be released by light-off and by addition of barium, strontium, or α-naphthyl phosphate. We calculated the number of specific potassium channels to be between 1750 and 34 825 channels per cell. Barium (1 mol × m^?3) and tetraethylammonium (10 mol × m^?3) inhibited TPs. I/V relationships demonstrated, when N-shaped, that potassium channels start to close at voltages more negative than ?195 mV (0.1 mol × m^?3 K⁺), ?160 mV (1 mol × m^?3 K⁺) and ?148 mV (10 mol × m^?3 K⁺). In the region of ?300 mV conditions similar to those at rest are reached. External sodium suppressed the development of N-shaped I/V relationships and reduced the membrane conductance during a TP between 8 % and 29 %. This indicates an influence of external sodium on potassium channels.     

Life cycle assessment of a large,thin ceramic tile with advantageous technological properties

Purpose

Ceramic tiles play a strategic role in the Italian market; currently, the Italian production is of 367.2 million m² (Confindustria Ceramica 2012). In 2009, Italy was positioned as the world’s fourth largest producer of ceramic tiles, producing 368 million m² of the world’s total production of 1,735 million m² Giacomini (Ceram World Rev 88:52–68, 2010). Therefore, there is an ongoing effort to create innovations in the products offered and their manufacturing processes, in order to better compete on the market and to create eco-friendly products. Recently, the Italian Ceramic District has increased its focus on environmental issues with the aim of protecting natural resources and reducing the energy and material consumption. For this reason, a new product was born in the Italian Ceramic District, namely, a large thin ceramic tile (dimensions 1,000 mm?×?3,000 mm?×?3.5 mm) reinforced with a fibreglass backing, which gives the product excellent resistance and flexibility properties. The aim was to manufacture a new product with lower environmental impact than the traditional one. The production of a large thin ceramic tile requires, in fact, a lower quantity of materials, transports and energy consumptions comparing to the same metres square of traditional ceramic tile. At the present, no comparative life cycle assessment (LCA) studies have been performed between traditional and innovative ceramic stoneware tiles. This study analyses, for the first time, a life cycle of the innovative ceramic product (porcelain stoneware) developed by a company of the Italian Ceramic District.

Methods

The analysis is performed using the LCA methodology, in order to identify environmental impacts, energy consumption and CO₂ equivalent emissions that occur during extraction of raw materials, transportation, production, material handling, distribution and end-of-life stages within a cradle to grave perspective.

Results and conclusions

LCA analysis indicates that the highest environmental impact mainly affects the respiratory inorganics impact category due to base slip production (27.62 %), caused by the transport of the raw materials and by non-renewable impact category due to both the pasting phase (21.31 %) and the two-component adhesive manufacture. The major greenhouse gas (GHG) emissions are related to the production of polyurethane, a component of the adhesive used in the pasting stage, and to the natural gas consumption in the firing process.     

Anaerobic digestion by a ceramic membrane enclosed reactor

A reactor with an external pressure type ceramic membrane module was designed to complete a compact system which brings about a reduction of permeability power requirements. The applicability of the reactor to methane fermentation was examined using heat-treated liquor obtained from sewage sludge. The experiments were carried out at 3 steps of CODcr-loading (Run 1; 4.53, Run 2; 7.98, Run 3; 15.4 kg CODcr/m³·d). The permeation flux stabilized at 0.06 in Run 1 and 0.11 m³/m²·d in Run 2, where the membrane surface was backwashed with N₂ gas. In Run 3, the membrane surface was additionally washed by circulating the gas yielded by the fermentation to increase the permeation flux, which stabilized at 0.2 m³/m²·d. The CODcr removal was 79.3 in Run 1, 83.2 in Run 2, and 80.2% in Run 3, respectively. In all cases, the BOD removal exceeded 95%, and there was no significant difference in the gas yield, which was 0.41 to 0.43 (l/g CODcr supplied) and 0.50 to 0.54 (l/g CODcr decomposed). Since the BOD could be greatly reduced even at 0.6 d of HRT and the microbiol cell concentration could be easily controlled, it seems possible to that the effciency of this reactor can be further improved.     

Simulation of carbon nanotube welding through Ar bombardment

Single-walled carbon nanotubes show promise as nanoscale transistors for nanocomputing applications. This use will require appropriate methods for creating electrical connections between distinct nanotubes, analogous to welding of metallic wires at larger length scales, but methods for performing nanoscale chemical welding are not yet sufficiently understood. This study examines the effect of Ar bombardment on the junction of two crossed single-walled carbon nanotubes, to understand the value and limitations of this method for generating connections between nanotubes. A geometric criterion was used to assess the quality of the junctions formed, with the goal of identifying the most productive conditions for experimental ion bombardment. In particular, the effects of nanotube chirality, Ar impact kinetic energy, impact particle flux and fluence, and annealing temperature were considered. The most productive bombardment conditions, leading to the most crosslinking of the tubes with the smallest loss of graphitic (i.e., conductive) character, were found to be at relatively mild impact energies (100 eV), with low flux and high-temperature (3000 K) annealing. Particularly noteworthy for experimental application, a high junction quality is maintained for a relatively broad range of fluences, from 3?×?10¹⁹ m^?2 to at least 1?×?10²⁰ m^?2.     

Butanol production from concentrated lactose/whey permeate: Use of pervaporation membrane to recover and concentrate product

In these studies, butanol (acetone butanol ethanol or ABE) was produced from concentrated lactose/whey permeate containing 211 g L^?1 lactose. Fermentation of such a highly concentrated lactose solution was possible due to simultaneous product removal using a pervaporation membrane. In this system, a productivity of 0.43 g L^?1 h^?1 was obtained which is 307 % of that achieved in a non-product removal batch reactor (0.14 g L^?1 h^?1) where approximately 60 g L^?1 whey permeate lactose was fermented. The productivity obtained in this system is much higher than that achieved in other product removal systems (perstraction 0.21 g L^?1 h^?1 and gas stripping 0.32 g L^?1 h^?1). This membrane was also used to concentrate butanol from approximately 2.50 g L^?1 in the reactor to 755 g L^?1. Using this membrane, ABE selectivities and fluxes of 24.4–44.3 and 0.57–4.05 g m^?2 h^?1 were obtained, respectively. Pervaporation restricts removal of water from the reaction mixture thus requiring significantly less energy for product recovery when compared to gas stripping.     

A mechanistic study of in situ chemical cleaning-in-place for a PTFE flat sheet membrane: fouling mitigation and membrane characterization

This study aimed at unfolding the role and mechanisms of chemically enhanced cleaning-in-place (CIP) regimes in fouling control of polytetrafluoroethylene (PTFE) made flat sheet (FS) membrane bio-reactors (MBRs). The trans-membrane pressure (TMP) was successfully maintained below 10 kPa using a daily CIP regime consisting of 100 to 600 mg l^?1 of NaOCl and cake layer resistance control was shown to be critical for effective high-flux MBR operation. In contrast, in the control unit without the CIP, the TMP exceeded 35 kPa at a flux of 40 LMH. The extracellular polymeric substances associated with proteins (EPS_protein) were also controlled effectively with a daily application of the CIP to the fouled membrane. Moreover, the CIP prompted a thinner and looser bio-cake layer on the membrane surface, suggesting that in situ CIP can be a favorable method to control FS membrane fouling at high-flux MBR operation.     

Spatiotemporal Variation of Bacterial Assemblages in a Shallow Subtropical Coastal Lagoon in Southern Brazil

A study on the bacterioplankton of Conceição Lagoon (27°34′ S–48°27′ W), Southern Brazil, was carried out in July 2005 (austral winter) and January 2006 (austral summer) to characterize the bacterial spatiotemporal distribution and to determine the heterotrophic and photoautotrophic bacterial dominance in hypoxic/oxic stratified waters. Bacterial abundance increased significantly (p?5 (winter) to 3.21?×?10⁶ cells mL^?1 (summer), heterotrophic coccus/rod-shaped (HCR) cells from 7.00?×?10⁴ to 3.60?×?10⁶ cells mL^?1, and heterotrophic filamentous (HF) bacteria from 2.90?×?10³ to 2.74?×?10⁵ cells mL^?1. Bacterial biovolumes also increased in summer with mean biovolumes of CCY ranging from 0.38 to 1.37 μm³, HCR cells from 0.31 to 1.12 μm³, and HF from 3.32 to 11.34 μm³. Principal component analysis showed that salinity, temperature, and light were the abiotic factors that better explained the temporal variability of bacterial assemblages. Bacterial heterotrophy dominated in the lagoon, excepted by the southern and part of central sector in January 2006, when autotrophic-dominated microbial community occurred. Spatially, bacterial assemblages were influenced by nutrient gradient, oxygen, and salinity with a positive relationship between biovolumes and nutrients and a negative relationship between abundance of coccus cyanobacteria and nutrients. area revealed a singular temporal pattern with hypoxic bottom waters in winter and oxygen-rich waters appearing in summer related with the availability of light and predominant microbes. Thus, oxygen consumption/production is likely to be regulated by the amount of light reaching the bottom, stimulating the production of oxygen by oxygenic phototrophs.     

The cyanobacterium Synechococcus R-2 (Anacystis nidulans, S. leopoliensis) PCC 7942 has a sodium-dependent chloride transporter

Synechococcus R-2 (PCC 7942) actively accumulated Cl^? in the light and dark, under control conditions (BG-11 media: pH_o, 7·5; [Na⁺]_o, 18 mol m^?3; [Cl^?]_o, 0·508 molm^?3). In BG-11 medium [Cl^?], was 17·2±0·848 mol m^?3 (light), electrochemical potential of Cl^? (ΔμCl^?_i,o) =+211±2mV; [Cl^?]_i= 1·24±0·11 mol m^?3(dark), ΔμCl^?_i,o=+133±4mV. Cl^? fluxes, but not permeabilities, were much higher in the light: ?Cl^?_i,o= 4·01±5·4 nmol m^?2 s^?1, ^PCl^?_i,o= 47±5pm s^?1 (light); ?Cl^?_i,o= 0·395±0·071 nmol m^?2 s^?1, _PCl^?_i,o= 69±14 pm s^?1 (dark). Chloride fluxes are inhibited by acid pH_o (pH_o 5; ?Cl^?_i,o= 0·14±0·04 nmol m^?2 s^?1); optimal at pH_o 7·5 and not strongly inhibited by alkaline pH_o (pH_o 10; ?Cl^?1_i,o= 1·7±0·14 nmol m^?2 s^?1). A Cl^?_in/2H⁺_in coporter could not account for the accumulation of Cl^? alkaline pH_o. Permeability of Cl^? is very low, below 100pm s^?1 under all conditions used, and appears to be maximal at pH_o 7·5 (50–70 pm s^?1) and minimal in acid pH_o (20pm s^?1). DCCD (dicyclohexyl-carbodiimide) inhibited ?Cl^?_i,o in the light about 75% and [Cl^?]_i fell to 2·2±0·26 (4) mol m^?3. Valinomycin had no effect but monensin severely inhibited Cl^? uptake ([Cl^?]_i= 1·02±0·32 mol m^?3; ?Cl^?_i,o= 0·20±0·1 nmol m^?2 s^?1). Vanadate (200 mmol m^?3) accelerated the Cl^? flux (?Cl^?_i,o= 5·28±0·64 nmol m^?2 s^?1) but slightly decreased accumulation of Cl^? ([Cl^?], = 13·9±1·3 mol m^?3) in BG-11 medium but had no significant effect in Na⁺-free media. DCMU (dichlorophenyldimethylurea) did not reduce [Cl^?], or ?Cl^?_i,o to that found in the dark ([Cl^?]_i= 8·41±0·76 mol m^?3; ?Cl^?_i,o= 2·06±0·36 nmol m^?2 s^?1). Synechococcus also actively accumulated Cl^? in Na⁺-free media, [Cl^?]_i was lower but ΔΨ_i,o hyperpolarized in Na⁺-free media and so the ΔμCl^?_i,o was little changed ([Cl^?]_i= 7·98±0·698 mol m^?3; ΔμCl^?_i,o=+203±3 mV). Net Cl^? uptake was stimulated by Na⁺; Li⁺ acted as a partial analogue for Na⁺. Synechococcus has a Na⁺ activated Cl^? transporter which is probably a primary 2Cl^?/ATP pump. The Cl^? pump is voltage sensitive. ΔμCl^?_i,o is directly proportional to ΔΨ_i,o(P»0·01%): ΔμCl^?_i,o= -1·487 (±0·102) ×ΔΨ_i,o, r= -0·983, n= 31. The ΔμCl^?_i,o increased (more positive) as the Δμ_i,o became more negative. The ΔμCl^?_i,o has no known function, but might provide a driving force for the uptake of micronutrients.     

Performance of an anaerobic membrane bioreactor in which granular sludge and dynamic filtration are integrated

To alleviate the fouling of a filter, simple substrates, dynamic filtration, and granular sludge were applied in an anaerobic membrane bioreactor (AnMBR). The results showed that under a transmembrane pressure < 20 kPa, the filter flux ranged between 15 and 20 l (m^?2 h)^?1 for a period of 30 days. The flux was higher than the typical flux of AnMBRs with conventional membranes and most current dynamic filters. In addition, the low cost of the filter avoided the need for a higher flux. Moreover, a stable granular sludge bed, which consumed all volatile fatty acids, was maintained. A compact fouling/filtration layer formed on the filter, which contributed to low effluent chemical oxygen demand concentrations and turbidity. In addition, substrate scarcity in the filtration zone resulted in the evolution of diverse bacteria on the filter.     

Triton X-100 inhibition of yeast plasma membrane associated NADH-dependent redox activities

Plasma membrane (PM) vesicles isolated from the yeast Saccharomyces cerevisiae (wild-type NCIM 3078, and a MG 21290 mutant pma 1-1) were used to monitor the effect of the detergents, 3-[(3-cholamidopropyl) dimethylammonio]-1-propane sulfonate (Chaps) and Triton X-100, on H⁺-ATPase (E.C. 3.6.1.35), NADH oxidase and NADH- hexacynoferrate (III)[HCF (III)] oxidoreductase (E.C. 1.6.99.3) activities. The results obtained show that Triton X-100 inhibited both membrane bound and solubilized NADH-dependent redox activities. The nature of this inhibition as determined for NADH–HCF(III) oxidoreductase was non-competitive and the Ki values for wild and mutant enzymes were 1.2?×?10^?5?M and 8.0?×?10^?6?M, respectively. The findings are interpreted, in view of the established reports, that the active site architecture of PM bound NADH-dependent oxidoreductase in yeast is likely to be different than in other eukaryotes.     

Determination on the binding of chlortetracycline to bovine serum albumin using spectroscopic methods

In this work, the interaction of chlortetracycline with bovine serum albumin (BSA) was investigated by fluorescence spectroscopy, circular dichroism (CD) spectroscopy, and molecular docking. Results indicated that chlortetracycline quenches BSA fluorescence mainly by a static quenching mechanism. The quenching constants (K_SV) were obtained as 5.64 × 10⁴, 4.49 × 10^4/, and 3.44 × 10^4/ M_?1 at 283, 295, and 307 K, respectively. The thermodynamic parameters of enthalpy change Δ H°, entropy change Δ S°, and free energy change Δ G° were ?5.12 × 10^4/ J mol?1, ?97.6 J mol?1 K?1, and ?2.24 × 10^4/ J mol?1 (295 K), respectively. The association constant (K_A) and the number of binding sites (n) were 9.41 × 10^3/ M?1 and 0.86, respectively. The analysis results suggested that the interaction was spontaneous, and van der Waals force and hydrogen‐bonding interactions played key roles in the reaction process. In addition, CD spectra proved secondary structure alteration of BSA in the presence of chlortetracycline. © 2012 Wiley Periodicals, Inc. J Biochem Mol Toxicol 26:331–336, 2012; View this article online at wileyonlinelibrary.com . DOI 10:1002/jbt.21424