Investigation of Bovine Serum Albumin (BSA) Attachment onto Self-Assembled Monolayers (SAMs) Using Combinatorial Quartz Crystal Microbalance with Dissipation (QCM-D) and Spectroscopic Ellipsometry (SE)

Understanding protein adsorption kinetics to surfaces is of importance for various environmental and biomedical applications. Adsorption of bovine serum albumin to various self-assembled monolayer surfaces including neutral and charged hydrophilic and hydrophobic surfaces was investigated using in-situ combinatorial quartz crystal microbalance with dissipation and spectroscopic ellipsometry. Adsorption of bovine serum albumin varied as a function of surface properties, bovine serum albumin concentration and pH value. Charged surfaces exhibited a greater quantity of bovine serum albumin adsorption, a larger bovine serum albumin layer thickness, and increased density of bovine serum albumin protein compared to neutral surfaces at neutral pH value. The quantity of adsorbed bovine serum albumin protein increased with increasing bovine serum albumin concentration. After equilibrium sorption was reached at pH 7.0, desorption of bovine serum albumin occurred when pH was lowered to 2.0, which is below the isoelectric point of bovine serum albumin. Our data provide further evidence that combinatorial quartz crystal microbalance with dissipation and spectroscopic ellipsometry is a sensitive analytical tool to evaluate attachment and detachment of adsorbed proteins in systems with environmental implications.     

Isotherm for Adsorption of Agrobacterium tumefaciens to Susceptible Potato (Solanum tuberosum L.) Tissues

Potato tuber disks were submerged in suspensions containing 10¹ to 10⁹ cells of Agrobacterium tumefaciens B6 per ml. After 60 min, the disks were rinsed and homogenized, and portions of the homogenates were plated to measure the number of adsorbed bacteria. At low initial bacterial concentrations (10⁵/ml), 5 to 23% of the bacteria adsorbed. At higher bacterial concentrations, the corresponding value was approximately 1.2%. Adsorption was a reversible equilibrium process. Binding saturation was not achieved, and adsorbed bacteria were confined to monolayers on the surfaces of tissue prepared for scanning electron microscopy. Adsorption of strain B6 to potato tuber tissues is described accurately by the Freundlich adsorption isotherm and may be a nonspecific phenomenon.     

Batch removal of chromium(VI) from aqueous solution by Turkish brown coals

The ability of using low-rank Turkish brown coals (Ilgın: BC₁, Beyşehir: BC₂, and Ermenek: BC₃) to remove Cr(VI) from aqueous solutions was studied as a function of contact time, solution pH, temperature, concentration of metal solutions and amount of adsorbent. Their sorption properties were compared with the activated carbon from Chemviron (AQ-30). Adsorption of Cr(VI) uptake is in all cases pH-dependent showing a maximum at equilibrium pH values between 2.0 and 3.2, depending on the biomaterial, that correspond to initial pH values of 2.3 units for BC₁, 3.0 units for BC₂ and 3.2 units for BC₃ and AQ-30. Batch equilibrium tests showed that the Cr(VI) removal was fitted with Freundlich isotherm and the adsorption reached equilibrium in 80 min. It was proceeding effectively into a short acid pH interval (2.0–3.2) where processes of Cr(VI) sorption are maximized. It was observed that the maximum adsorption capacity of 11.2 mM of Cr(VI)/g for Ilgın (BC₁), 12.4 mM of Cr(VI)/g for Beyşehir (BC₂), 7.4 mM of Cr(VI)/g for Ermenek (BC₃) and 6.8 mM of Cr(VI)/g for activated carbon (AQ-30) was achieved at pH of 3.0. The rise in temperature caused a slight decrease in the value of the equilibrium constant (K_c) for the sorption of Cr(VI) ion. The Cr(VI) sorption capacities of Beyşehir and Ilgın brown coals were the same. Ermenek brown coals and activated carbon (AQ-30) showed a similar sorption capacity.     

Thermodynamic equilibrium in reversibly interacting ribosomal systems of E. coli and Bac. coagulans

The results which strongly confirm the existence of dynamic equilibrium 50S-30S ? 50S + 30S in ribosomal systems of E. Coli and Bac. coagulans are presented. A method has been devised which permitted to determine quantitatively the detailed composition of the reaction mixture of ribosomal subparticles and evaluate the equilibrium constant.The analysis of equilibrium ribosomal systems of E. coli and Bac. coagulans at different temperatures allowed evaluation of appropriate thermodynamic parameters. In particular, the free energy of dissociation was shown to be higher in the case of thennophilic Bac. coagulans rihosomes.     

Biosorption of uranium by magnetically modified Rhodotorula glutinis

Adsorption of uranium from aqueous solution onto the magnetically modified yeast cell, Rhodotorula glutinis, was investigated in a batch system. Factors influencing sorption such as initial solution pH, biomass dosage, contact time, temperature, initial uranium concentration and other common cations were analyzed. Sorption isotherm, kinetic and thermodynamic studies of uranium on magnetically modified R. glutinis were also carried out. The temperature dependent equilibrium data agreed well with the Langmuir model. Kinetic data obtained at different temperatures were simulated using pseudo-first-order and pseudo-second-order kinetic models, the pseudo-second-order kinetic model was found to describe the data better with correlation coefficients near 1.0. The thermodynamic parameters, ΔH°, ΔS° and ΔG° were calculated from the sorption data gained at different temperatures. These thermodynamic parameters showed that the sorption process was endothermic and spontaneous. All results indicated that magnetically modified R. glutinis can be a potential sorbent for uranium wastewater treatment.     

Adsorption of metal ions on yeast cells at varied cell concentrations

Adsorption isotherms for adsorption of metal ions on yeast cellswere determined at varied cell concentrations. The mass of adsorbedmetal per unit weight of the cells at an equilibrium metal concentrationwas largely dependent on the cell concentration. An experimentalequation was presented, relating the included parameters. (Received August 19, 1975; )     

A study of E. coli and T. maritima ribosomes by atomic force microscopy

Whole 70S ribosomes and 50S and 30S ribosomal subunits of E. coli and T. maritima were studied by atomic force microscopy. Adsorption of the ribosomal subunits on a substrate revealed considerable heterogeneity of their structures. Analysis of the geometric size of the particles demonstrated essential difference between the heights of E. coli and T. maritima ribosomes 9.4 ± 0.01 nm and 10.35 ± 0.02 nm, respectively. Presumably, the difference in size is determined by the difference in organization of the mobile ribosomal domain, the L7/L12 stalk.     

Drin pesticides removal from aqueous solutions using acid-treated date stones

This work describes the potential applicability of chemically and thermally treated date stones for removing drin pesticides (aldrin, dieldrin and endrin) from aqueous solutions. The effect of several parameters, such as sorbent particle size, adsorbent dose, shaking speed, shaking time, concentration of pesticide solution and temperature, was evaluated by batch experiments. Pesticide determination was carried out using stir bar sorptive extraction and gas chromatography coupled with mass spectroscopy. Maximum removal efficiency (93%) was reached using 0.1 g of acid-treated date stones (ATDS) (63–100 μm) and 100 mL of aldrin (0.5 mg L⁻¹). The removal efficiency of drin pesticides decreased in the order of aldrin, dieldrin and endrin, and decreased as the temperature rose. Adsorption data were processed according to various kinetic models. Lagergren and Morris-Weber equations were applied to fit the kinetic results. The second order model was the most suitable on the whole, and intra-particle diffusion was found to be the rate-controlling the adsorption process. According to adsorption kinetic data, 3.5 h were considered as the equilibrium time for determining adsorption isotherms. Adsorption data were analyzed by the Langmuir, Freundlich and Dubinin–Radushkevich adsorption approaches. Experimental results showed that the Freundlich isotherm model best described the adsorption process. In addition, thermodynamic parameters such as ΔH, ΔS and ΔG were calculated. Negative values of ΔH and ΔG indicate the exothermic and spontaneous nature of pesticide adsorption on ATDS.     

Interaction of human immunoglobulin G with l-histidine immobilized onto poly(ethylene vinyl alcohol) hollow-fiber membranes

l-Histidine as pseudobiospecific ligand was immobilized onto poly(ethylene vinyl alcohol) hollow-fiber membranes to obtain an affinity support for immunoglobulin G (IgG) purification. The interaction of human IgG with the affinity membranes was studied by chromatography and equilibrium binding analysis. Adsorption was possible over a broad pH range and was found to depend strongly on the nature of the buffer ions rather than on ionic strength. With zwitterionic buffers like morpholinopropanesulfonic acid (Mops) and hydroxyethylpiperazineethanesulfonic acid (Hepes), much higher adsorption capacities were obtained than with other buffers like Tris-HCl and phosphate buffers. An inhibition analysis revealed that non-zwitterionic buffers competitively inhibit IgG binding, whereas Mops and Hepes in their zwitterionic form do not. By choosing the appropriate buffer system, it was possible to adsorb specifically different IgG subsets. The IgG molecules were found to adsorb on membrane immobilized histidine via their F_ab part. Determination of dissociation constants at different temperatures allowed calculation of thermodynamic adsorption parameters. Decrease in K_D with increasing temperature and a positive entropy value between 20 and 35°C (in Mops buffer) indicated that adsorption is partially governed by hydrophobic forces in that temperature range, whereas at lower temperatures, electrostatic forces are more important for adsorption.     

Effect of pretreatment and enzymatic hydrolysis of wheat straw on cell wall composition, hydrophobicity and cellulase adsorption

The present study aimed to determine the impact of cell wall composition and lignin content on enzyme adsorption and degradability. Thioacidolysis analysis of residual lignins in wheat straw after steam-explosion or organosolv pretreatment revealed an increase in lignin condensation degree of 27% and 33%, respectively. Surface hydrophobicity assessed through wettability tests decreased after the pretreatments (contact angle decrease of 20-50%), but increased with enzymatic conversion (30% maximum contact angle increase) and correlatively to lignin content. Adsorption of the three major cellulases Cel7A, Cel6A and Cel7B from Trichoderma reesei decreased with increasing hydrolysis time, down to 7%, 31% and 70% on the sample with the highest lignin content, respectively. The fraction of unspecifically bound enzymes was dependent both on the enzyme and the lignin content. Adsorption and specific activity were shown to be inversely proportional to lignin content and hydrophobicity, suggesting that lignin is one of the factors restricting enzymatic hydrolysis.     

Nickel(II) adsorption onto biomass based activated carbon obtained from sugarcane bagasse pith

Bioavailability of Nickel in the form of hydrated Nickel(II) attributes to its toxicological effects and hence its removal from aqueous solution is of great concern. Adsorption is used as an efficient technique for the removal of Nickel(II), hereafter Ni(II), from water and wastewaters. Activated carbon obtained from sugarcane bagasse pith (SBP-AC), a waste biomass collected from juice shops in Sarkara Devi Temple, Chirayinkeezhu, Trivandrum, India during annual festival, is used as adsorbent in the study. The process of adsorption is highly dependent on solution pH, and maximum removal occurs in the pH range of 4.0-8.0. Moreover, the amount of Ni(II) adsorbed onto SBP-AC increased with the time increase and reached equilibrium at 4h. Adsorption kinetic and equilibrium data were analyzed for determining the best fit kinetic and isotherm models. The overall study reveals the potential value of steam pyrolysed SBP-AC as a possible commercial adsorbent in wastewater treatment strategies.     

Binding of the protoxin and toxin proteins ofBacillus thuringiensis subsp.kurstaki on clay minerals

The equilibrium adsorption and binding of the delta-endotoxin proteins, i.e., the protoxins (M_r=132 kDa) and toxins (M_r=66 kDa), fromBacillus thuringiensis subsp.kurstaki were greater on montmorillonite than on kaolinite (five-fold more protoxin and three-fold more toxin were adsorbed on montmorillonite). Approximately two- to three-fold more toxin than protoxin was adsorbed on these clay minerals. Maximum adsorption occurred within 30 min (the shortest interval measured), and adsorption was not significantly affected by temperatures between 7° and 50°C. The proteins were more easily desorbed from kaolinite than from montmorillonite; they could not be desorbed from montmorillonite with water or 0.2% Na₂CO₃, but they could be removed with Tris-SDS (sodium dodecyl sulfate) buffer. Adsorption was higher at low pH and decreased as the pH increased. Adsorption on kaolinite was also dependent on the ionic nature of the buffers. The molecular mass of the proteins was unaltered after adsorption on montmorillonite, as shown by SDS-PAGE (polyacrylamide gel electrophoresis) of the desorbed proteins; no significant modifications occurred in their structure as the result of binding on the clay, as indicated by infrared analysis; and there was no significant expansion of the clay by the proteins, as shown by x-ray diffraction analysis. The bound proteins appeared to retain their insecticidal activity against the third instar larvae ofTrichoplusia ni.     

Use of Phanerochaete chrysosporium biomass for the removal of textile dyes from a synthetic effluent

Summary The use of Phanerochaete chrysosporium biomass for the removal of Reactofix Golden Yellow from aqueous solution and eight textile dyes (four azo and four anthraquinone) from a synthetic effluent (0.6 g/l) at different pH, temperature and biomass concentrations was studied. Adsorption was maximum at pH 2.0 and 40 °C using 2.45 g mycelial biomass. The rate constant of adsorption was 1.95×10⁻¹/min for Reactofix Golden Yellow and 1.64×10⁻¹/min for synthetic effluent. In both cases, the equilibrium data fitted well in the Langmuir but not the Freundlich model of adsorption, and the adsorption was biphasic. Adsorption decreased the COD of Reactofix Golden Yellow and synthetic effluent by 54 and 57%, respectively. Desorption (80–84%) of dyes from P. chrysosporium mycelial surface occurred as the pH increased from 2 to 10.     

THE INFLUENCE OF ACIDITY ON THE MULTIPLICATION OF LACTIC STREPTOCOCCAL BACTERIOPHAGE IN LIQUID MEDIA

SUMMARY: Mass lysis of lactic streptococci infected with baeteriophage at 30° was prevented at pH 5·10. At lower pH values no multiplication of phage followed infection, and prolonged incubation at 30° resulted in loss of phage particles from unlysed samples. Adsorption of phage particles on host cells was unaffected by acidity, but no phage penetration of host cells took place. Host cell properties were apparently unchanged by adsorption of phage particles in acid whey.     

The influence of temperature on the binding of AMP to phosphorylase b

Equilibrium dialysis measurements have been performed at several temperatures, ranging from 5 to 30°C, to calculate the binding constants of AMP to phosphorylase b (EC 2.4.1.1). ΔH = ?10 kcal/mol and ΔS = ?6.4 e.u. have been obtained for the binding process. Measurements of enzymatic activity have been performed in the same temperature range. An activation energy of 16 kcal has been calculated for the enzyme-catalysed reaction. Absorption difference spectra induced by AMP in phosphorylace b when AMP is bound to its high affinity site have also been carried out at these temperatures. The equilibrium constant for the binding of AMP to phosphorylase b, the enzyme activity as well as the molar absorption coefficient of the absorption difference spectra studied show no discontinuity with temperature from 5 to 30°C.     

The characteristics of Escherichia coli adsorption of arsenic(III) from aqueous solution

The potential of using Escherichia coli (E. coli) as adsorbent for the adsorption of As(III) from aqueous solution was assessed. Various parameters like pH, initial concentration and temperature have been investigated. It is found that the adsorption of As(III) is pH dependent and the optimum value was 2.0. Kinetics studies revealed that the equilibrium of the adsorption of As(III) on to E. coli was obtained within 30 min and the process was followed with the pseudo-2nd-order kinetic model. The equilibrium adsorption data obtained at different temperatures were fitted better with Langmuir than Freundich isotherm. The adsorption capacity of E. coli for As(III) is increased with the increasing of temperature and the maximum adsorption capacity is 1.111 mg/g which obtained at 40°C. Potentiometric titration and Fourier transform infra-red spectroscopy were applied to reveal the mechanisms of the As(III) binding. Amino, amide, amine group and C–H of the alkane are determined to be involved in As(III) binding based on the results.     

CO2 adsorption on polar surfaces of ZnO

Physical and chemical adsorption of CO₂ on ZnO surfaces were studied by means of two different implementations of periodic density functional theory. Adsorption energies were computed and compared to values in the literature. In particular, it was found that the calculated equilibrium structure and internuclear distances are in agreement with previous work. CO₂ adsorption was analyzed by inspection of the density of states and electron localization function. Valence bands, band gap and final states of adsorbed CO₂ were investigated and the effect of atomic displacements analyzed. The partial density of states (PDOS) of chemical adsorption of CO₂ on the ZnO(0001) surface show that the p orbitals of CO₂ were mixed with the ZnO valence band state appearing at the top of the valence band and in regions of low-energy conduction band.

EST-SSR markers from Heterodera glycines Ichinohe

The soybean cyst nematode Heterodera glycines Ichinohe is a severe agricultural pest for which genetic resources are limited. In this study, 295 simple sequence repeats (SSRs) were identified from 259 expressed sequenced tags (ESTs), which were selected from 9,443 unigenes. The successful primer pairs were designed against six regions. In total, 30 alleles were identified from 30 individuals using the six markers, with an average of five alleles per locus (range, 4–7). The observed and expected heterozygosities were 0.074–0.900 and 0.266–0.775, respectively. Significant departure from Hardy-Weinberg equilibrium was found at three of the six loci. The EST-based SSR markers developed in this study may contribute to better under-standing of the genetic structure of H. glycines populations.     

Sucrose density gradient sedimentation of E. coli ribosomes.

The behavior of E. coli ribosomes during sedimentation on sucrose gradients is predicted under a variety of conditions by computer simulations. Since numerous recent kinetic studies indicate equilibration in times short compared to the time of sedimentation, these simulations assume that the system attains local reaction equilibrium at every point in the gradient at all times. For any type of homogeneous equilibrating ribosome population, governed by a single formation constant at one atmosphere pressure for 70S couples, no more than two clearly defined zones will be resolved, although the presence of large dissociating effects due to pressure gradients in high speed experiments will spread the subunit zone. Normally the pattern will consist of a 30S zone and a so-called “70S” zone, which is in reality a mixture of 70S couples and 30S and 50S subunits in local equilibrium. The greater the dissociation into subunits, the more the “70S” zone will be slowed below the nominal rate of 70 Svedberg units. If ribosomes have been collected from the “70S” zone in several successive cycles of purification, the repeated deletion of resolved 30S subunits can result in a preparation with so large a molar excess of 50S subunits that the ensuing sucrose density gradient sedimentation pattern may exhibit a “70S” zone followed by zone of 50S subunits, insteadof a zone of 30S subunits. Our most important conclusion is that whenever a well-resolved 50S zone is present in a sucrose density gradient sedimentation experiment on E. coli ribosomes, in addition to a 30S and a “70S” zone, under conditions where ribosomes and subunits should be in reversible equilibrium, the preparation must be microheterogeneous, containing a mixture of “tight” and “loose” couples. Moreover in such cases the content of large subunits in the 50S zone must be derived entirely from “loose” couples whereas the 30S zone must contain small subunits derived from both “tight” and “loose” couples. Sedimentation patterns predicted for various mixtures of “tight” and “loose” couples display all the major characteristics of published experimental patterns for E. coli ribosomes, including the partial or complete resolution into three zones, depending on rotor velocity and level of Mg²⁺.