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PubMed1995

Microcalorimetric characterization of the anion-exchange adsorption of recombinant cytochrome b5 and its surface-charge mutants.

The adsorption of recombinant soluble tryptic fragment of rat cytochrome b5 on the strong anion exchanger Mono Q was studied using isothermal titration calorimetry and differential scanning calorimetry (DSC). Titration calorimetry results obtained at low levels of adsorbed protein show increasingly endothermic (unfavorable) enthalpies of binding with increasing surface coverage, confirming the heterogeneous nature of binding. The enthalpy of adsorption declines toward zero at higher loadings. At low surface coverage, enthalpies increase linearly with temperature, giving rise to a positive value of delta Cp. Enthalpies of adsorption depend strongly on the history of the adsorbent. DSC is used to show that cytochrome b5 is stable in both free and adsorbed states at all temperatures used in the titration calorimetric experiments. Site-directed mutants of recombinant cytochrome b5 carrying single charge-neutralizing substitutions are used to test the contributions of particular residues to the thermodynamics of adsorption. Like those derived from van't Hoff analysis of equilibrium adsorption isotherms and HPLC retention data, calorimetric enthalpies of adsorption are positive, confirming the dominant role of entropic effects in ion-exchange adsorption in this system.

Adsorption↗
PubMed1985

The adsorption of thrombin to polypropylene tubes: the effect of polyethylene glycol and bovine serum albumin.

The adsorption of 125I-thrombin to polypropylene tubes has been studied with thrombin dissolved in tris-buffered saline (TBS), TBS with 0.66% polyethylene glycol (PEG), and TBS with 0.01% or 0.20% bovine serum albumin (BSA). Adsorption stabilized over time from all three solutions, increased with increasing concentrations of unadsorbed thrombin, and was reversible by repetitive washing. At equilibrium, more thrombin adsorbed from TBS-PEG than from TBS. The difference was attributable to an increased amount of thrombin deposited by evaporation during aspiration of the polypropylene tubes. Adsorption equilibrium and capacity were otherwise relatively unaffected by the presence of PEG. However, PEG was effective in retarding thrombin adsorption by markedly reducing the adsorption rate. Reduction of adsorption in the presence of BSA, on the other hand, was explained by competitive inhibition. Pretreatment of the tubes with PEG or BSA was also shown to be effective in reducing thrombin adsorption from TBS.

Adsorption↗
PubMed1988

Adsorption of thrombin from buffer and modified plasma to polystyrene resins containing sulphonate and sulphamide arginyl methyl ester groups.

The adsorption of albumin and thrombin to insoluble modified polystyrene resins bearing sulphonate (PSSO3) and L-arginyl methyl ester groups (PAOM) was investigated in both purified and plasma systems. Radioiodinated proteins were used to follow adsorption in a 'minicolumn' experiment. Albumin adsorption was found to follow the Langmuir model and specific surface areas of the various resins were evaluated from plateau albumin adsorption data. The adsorption isotherms of thrombin both in buffer and in antithrombin III/fibrinogen-free plasma were also found to be Langmuir-like, and the quantities adsorbed at the isotherm plateaux are in the monolayer range. Analysis of the isotherms at 4 degrees and 37 degrees C for the purified system shows that adsorption is endothermic. Adsorption capacities in plasma remain high (30-50% of those in the purified system) despite competition from the other plasma proteins. These data confirm the strong affinity and selectivity of these resins for thrombin.

Adsorption↗
PubMed1994

Use of enhanced chemiluminescence to quantify protein adsorption to calcium phosphate materials and microcarrier beads.

The adsorption of serum proteins to calcium phosphate bone substitute materials, positively-charged dextrose and negatively-charged polystyrene microcarrier beads was compared by SDS-PAGE (sodium dodecyl sulphate-polyacrylamide gel electrophoresis). Protein adsorption to hydroxyapatite (HA)-based materials was influenced by chemical composition. Surface charge sign, distribution and/or functional group affected protein adsorption to microcarrier beads. Enhanced chemiluminescence was used to quantify adsorption of fibronectin and vitronectin following Western blotting, and to monitor the kinetics of adsorption of these two proteins to HA and Biosilon. Relative to total protein, fluctuating levels of fibronectin were detected on both materials. In contrast, vitronectin adsorption increased over the course of the incubation period with maximal relative adsorption detected after 30 min on Biosilon and 60 min on HA.

Adsorption↗
PubMed1978

The cleavage and adsorption of parathyroid hormone at high dilution: implications for receptor binding studies.

Like other polypeptide hormones, purified intact parathyroid hormone (1-84)parathyroid hormone is notoriously unstable and is subject to large adsorptive losses in routine laboratory manipulation. The present studies were undertaken with 125I-labeled hormone to quantitate the problem and to develop preventative measures, particularly with concentrations of physiological interest, 1 . 10(-10) M. It was found that spontaneous cleavage of the hormone takes place upon its incubation in air or oxygen. This can be prevented by the presence of mercaptoethanol or by plasma levels of cysteine and ascorbate. Under non-cleavage conditions, adsorption was found to be extensive on all materials tested. This adsorption increased with time up to 2 h, was independent of ionic strength, increased with increasing temperature and was presumed to involve hydrophobic interactions. Under given conditions, adsorption was proportional to concentration (constant percentage). However, at very high concentrations, 1 . 10(-6) M, adsorption was markedly reduced. Adsorption was minimized at low pH (2). Bovine serum albumin reduced adsorption under all conditions when present at concentrations of 2 mg/ml or more. Coating laboratory ware with cetyl alcohol also was helpful. Using optimal conditions, cleavage is prevented and losses are less than 5% at neutral pH, and under 2% at pH 2.

Adsorption↗
PubMed2005

Removal of molybdate from water by adsorption onto ZnCl2 activated coir pith carbon.

Removal and recovery of molybdate from aqueous solution was investigated using ZnCl2 activated carbon developed from coir pith. Studies were conducted to delineate the effects of contact time, adsorbent dose, molybdate concentration, pH and temperature. Two theoretical adsorption isotherms, namely, Langmuir and Freundlich were used to describe the experimental results. The Langmuir adsorption capacity (Q0) was found to be 18.9 mg molybdate/g of the adsorbent. Adsorption followed second order kinetics. Studies were performed at different pH values to find out the pH at which maximum adsorption occurred. The pH effect and desorption studies showed that ion exchange and chemisorption mechanism were involved in the adsorption process. Thermodynamic parameters such as DeltaG0, DeltaH0 and DeltaS0 for the adsorption were evaluated. Effect of foreign ions on adsorption of molybdate has been examined. The results showed that ZnCl2 activated coir pith carbon was effective for the removal and recovery of molybdate from water.

Adsorption↗
PubMed2006

Adsorption of heavy metals from electroplating wastewater by wood sawdust.

Poplar wood sawdust was examined for adsorption as a replacement for current, more expensive methods of removing copper, zinc and cadmium from electroplating wastewater. Langmuir, Freundlich, BET and competitive Langmuir (two competing ions) isotherms were fitted to experimental data and the goodness of their fit for adsorption was compared. The shapes of isotherms obtained fitted well with multilayer adsorption. This was established and confirmed through solid correspondence between the BET equation and experimental data, in contrast to an observed monolayer adsorption of metal ions on poplar sawdust in single metal-water solutions. The adsorption of copper ions from a mixture (in wastewater) was better than that from a single metal solution. The adsorptions of zinc ions from wastewater and from model water were approximately equal, while that of cadmium ions was significantly lower from the wastewater than from model water. The aforementioned suggests that the presence of other ions in wastewater hindered adsorption of cadmium ions.

Adsorption↗
PubMed2006

Ammonia adsorption in a fixed bed of activated carbon.

The rise in atmospheric pollution caused by gases such as ammonia has led many researchers to conduct studies aimed at decreasing or treating the emissions of such polluting gases. The present work attempted to study the adsorption of ammonia in the fixed bed of activated carbon as a means to treat its emissions. The effects of the initial concentration of ammonia (C0) and of the bed temperature (TL) on the adsorption of ammonia by the activated carbon were also considered. Adsorption capacity of activated carbon was determined using data from the breakthrough curves and from a balance of mass in the bed. Adsorption capacities were obtained employing the Langmuir and Freudlich isotherms. The results showed that within the NH3 concentration range of 600-2400 ppm, adsorption capacity varied from 0.6 to 1.8 mg NH3/g carbon at 40 degrees C, from 0.2 to 0.7 mg NH3/g carbon at 80 degrees C and from 0.15 to 0.35 mg NH3/g carbon at 120 degrees C. These numbers highlight the tendency toward a lower adsorption capacity with the decrease in temperature. As to mass of the bed, this latter variable had no significant influence over adsorption capacity.

Adsorption↗
PubMed2006

Adsorption of 125I-labeled immunoglobulin G, its F(ab')2 and Fc fragments onto plasma-polymerized films.

Plasma-polymerized films were formed on flat glass plates using allylamine, acrylic acid, acrolein, and allylcyanide as monomers. Adsorption of (125)I-labeled-proteins such as immunoglobulin G (IgG), its F(ab')(2) and Fc fragments, and human serum albumin (HSA) was measured on these plasma-polymerized (PP) films covering the glass plates and on commercially available polymer plates. The adsorption isotherm followed the Langmuir equation, from which the binding constant and amount of saturation binding were estimated. We found that, in general, a cationic surface had higher affinity for protein adsorption than an anionic surface. Among the surfaces examined, the PP-allylamine surface showed the highest binding capacity (264.2 nmol/m(2)) for F(ab')(2) fragment: it was remarkably high. Of the surfaces examined, the PP-acrylic acid surface showed the lowest binding capacity (12.8 nmol/m(2)) for F(ab')(2) fragment. The PP-acrylic acid surface also indicated the lowest protein binding capacity for IgG (16.5 nmol/m(2)), Fc-IgG (32.4 nmol/m(2)) and HSA (16.7 nmol/m(2)), respectively. These imply that the PP-acrylic acid film is useful to fabricate as a low protein adsorption material which expected to decrease cell adhesion. Results of our investigation indicate that the plasma-polymerization technique is promising for fabrication of a smart NanoBio-interface which can control the protein adsorption on a solid-phase substrate using a suitable monomer such as allylamine for the large adsorption and acrylic acid for the small adsorption.

Adsorption↗
PubMed2006

Adsorption of synthetic homo- and hetero-oligodeoxynucleotides onto highly oriented pyrolytic graphite: atomic force microscopy characterization.

DNA adsorption on electrode surfaces is of fundamental interest for the development of DNA-based biosensors. The free adsorption of 10-mer synthetic oligodeoxynucleotides (ODNs) onto highly oriented pyrolytic graphite (HOPG) surfaces was studied using Magnetic AC mode atomic force microscopy (MAC Mode AFM). The mechanism of interaction of nucleic acids with carbon electrode surfaces was elucidated, using 10-mer synthetic homo- and hetero-ODNs sequences of known base sequences, because they allow clear interpretation of the experimental data. AFM images in air revealed different adsorption patterns and degree of HOPG surface coverage for the ODNs, and correlation with the individual structure and base sequence of each ODN molecule will be presented. The results demonstrated that the hydrophobic interactions with the HOPG hydrophobic surface explain the main adsorption mechanism, although other effects such as electrostatic and Van der Waals interactions may contribute to the free adsorption process. The ODNs interacted differently with the HOPG surface, according to the ODN sequence hydrophobic characteristics, being directly depending on the molecular mass, the hydrophobic character of the individual bases and on the secondary structure of the molecule. The importance of the type of base existent at the ODN chain extremities on the adsorption process was investigated and different adsorption patterns were obtained with ODN sequences composed by the same group of bases aligned in a different order.

Adsorption↗
PubMed2005

Multi-component behavior of fixed-bed adsorption of dioxins by activated carbon fiber.

The multi-component behavior of fixed-bed adsorption of dioxins (DXNs) was examined through detailed analyses of the concentration profiles of isomers in fixed-bed activated carbon fiber (ACF). Regularities in both adsorption rates and strengths were clarified. (1) The rate of transfer in the adsorption of polychlorinated dibenzo-p-dioxins and polychlorinated dibenzofurans (PCCDs/DFs) tends to increase with decreasing number of chlorine substituents. Axial dispersion also tends to increase with a decreasing number of chlorine substituents under our experimental conditions. (2) Homologues with the same number of chlorine substituents in PCDDs/DFs have similar adsorption strengths. The adsorption strength of PCDD/DF isomers is probably greater than that of co-planar polychlorinated biphenyls (co-PCB) isomers when the number of chlorine substituents is identical. (3) The adsorption strength of isomers depends on their molecular structure. In PCDDs/DFs the toxic isomers, all of which have vicinal chlorine substituents at the 2, 3, 7 and 8 positions, are relatively strong. It is clear, especially in TeCDDs, that isomers with vicinal chlorine substituents are stronger than isomers without. In co-PCBs, isomers without chlorine substituents at ortho positions are stronger than those with, and (4) A close analogy exists between the adsorption strength order for ACF and the elution order in gas chromatography (GC).

Adsorption↗
PubMed2005

Competitive adsorption of dye metanil yellow and RB15 in acid solutions on chemically cross-linked chitosan beads.

One kind of adsorbent with a high adsorption capacity for anionic dyes was prepared using ionically and chemically cross-linked chitosan beads. A batch system was applied to study the adsorption behavior of one acid dye (MY, metanil yellow) and one reactive dye (RB15, reactive blue 15) in aqueous solutions by the cross-linked chitosan beads. The adsorption capacities was 3.56 mmol g(-1) (1334 mg g(-1)) for dye MY and 0.56 mmol g(-1) (722 mg g(-1)) for dye RB15 at pH4, 30 degrees C. The Langmuir model agreed very well with the experimental data (R(2)>0.996). The kinetics of adsorption for a single dye and the kinetics of removal of ADMI color value in mixture solutions at different initial dye concentrations were evaluated by the nonlinear first-order and second-order models. The first-order kinetic model fits well with the dynamical adsorption behavior of a single dye for lower initial dye concentrations, while the second-order kinetic model fits well for higher initial dye concentrations. The competitive adsorption favored the dye RB15 in the mixture solution (initial conc. (mM): MY=1.34; RB15=1.36); while it favored the dye MY in the mixture solution (initial conc. (mM): MY=3.00; RB15=1.34) and the adsorption kinetics for dye RB15 has the tendency to shift to a slower first order model.

Adsorption↗
PubMed2006

Determination of gas phase adsorption isotherms--a simple constant volume method.

Single and ternary solute gas phase adsorption isotherms were conducted in this study to evaluate the effectiveness of a simple constant volume method, which was utilized by using Tedlar gas sampling bags as a constant volume batch reactor. For this purpose, gas phase adsorption of toluene, methyl ethyl ketone (MEK), and methyl isobutyl ketone (MIBK) on two types of activated carbons, BPL-bituminous base and OVC--coconut base, were investigated. For the single solute adsorption, the experimental adsorption data were found to be well correlated with Freundlich and Myers adsorption equations. The pore size distribution of adsorbents was found to affect their adsorption capacities; its effect was dependant on the solute concentration. The ternary adsorption experimental isotherms were accurately predicted by using the well-known model, i.e., ideal adsorbed solution theory (IAST).

Adsorption↗
PubMed2006

Adsorption of Acid Red 73 on copper dithiocarbamate precipitate-type solid wastes.

Three solid wastes, copper N,N'-bis(dithiocarboxy)piperazine ([CuBDP](n)), copper diethyldithiocarbamate (Cu(DDTC)(2)) and copper dimethyldithiocarbamate (Cu(DMTC)(2)), were prepared and tested as adsorbents to remove Acid Red 73 from wastewater. It was found that the three precipitates all could effectively adsorb the dye but their adsorption abilities were rather different. The maximum adsorption amounts of the coordination polymer precipitate [CuBDP](n) reached as high as 364mg g(-1), much greater than those of Cu(DDTC)(2) and Cu(DMTC)(2) (42.9 and 37.8mg g(-1), respectively). The investigation of adsorption models showed these adsorption processes followed the pseudo-second-order kinetic equation and the adsorption balances could be described with both Langmuir and Freundlich isotherms, but the latter seemed to be more suitable. Their adsorption nature was inferred to be physical adsorption and mainly depended on the hydrophobic interaction between these precipitates and Acid Red 73. This is the first example for the reutilization of metal dithiocarbamate precipitates as solid wastes to date.

Adsorption↗
PubMed2005

Comparative study on the gas-phase adsorption of hexane over zeolites by calorimetry and inverse gas chromatography.

The scope of this work is to carry out a systematic comparison of inverse gas chromatography (IGC) and microcalorimetry as tools for the study of the gas-phase adsorption of organic vapours (using hexane as model compound) on zeolitic materials (using different Mn, Co and Fe-exchanged NaX and CaA zeolites). Adsorption isotherms were recorded using both techniques in the temperature range of 150-250 degrees C, being observed that the shape of the isotherms obtained with the dynamic (IGC) and static (microcalorimetry) techniques was surprisingly similar in the pressure range at which both techniques are applicable (low surface coverages). Concerning to the measurement of the strength of the adsorption, calorimetric data provide two parameters related to the adsorption enthalpy: the initial differential heat and the isosteric adsorption enthalpy. A great coincidence was found between the last one and the adsorption enthalpy determined by IGC (4-20% of difference, depending on the studied material). The behaviour of the initial differential heat depends strongly on the studied material, being in some cases closely related to the other two parameters and temperature-independent (in the case on Mn-exchanged zeolites), whereas for the Co-CaA and Fe-CaA zeolites, it is temperature-dependent, being not correlated with the other parameters in this case. The main conclusion of this work is that IGC is an attractive alternative to the static microcalorimetric data for obtaining information on the adsorption of organic compounds on microporous materials.

Adsorption↗
PubMed2005

Predictive modeling of protein adsorption along the bed height by taking into account the axial nonuniform liquid dispersion and particle classification in expanded beds.

Expanded bed adsorption (EBA) is a special chromatography technique with perfect classification of adsorbent particles in the column, thus the performance of protein adsorption in expanded beds is particular, obviously nonuniform and complex along the column. Detailed description of the complex adsorption kinetics of proteins in expanded bed is essential for better analyzing of adsorptive mechanisms, the design of chromatographic processes and the optimization of operation parameters of EBA processes. In this work, a theoretical model for the prediction of protein adsorption kinetics in expanded beds was developed by taking into account the classified distribution of adsorbent particles along the bed height, the nonuniform behaviors of axial liquid dispersion, the axial variation of local bed voidage as well as the axial changes of target component mass transfer. The model was solved using the implicit finite difference scheme combining with the orthogonal collocation method, and then applied to predict the breakthrough behaviors of bovine serum albumin (BSA) on Streamline DEAE and lysozyme on Streamline SP along the bed height in expanded beds under various conditions. In addition, the experiments of front adsorption of BSA on Streamline DEAE at different axial column positions were carried out to reveal the adsorption kinetics of BSA along the bed height in a 20 mm I.D. expanded bed, and the influences of liquid velocity and feed concentration on the breakthrough behaviors were also analyzed. The breakthrough behaviors predicted by the present model were compared with the experimental data obtained in this work and in the literature published. The agreement between the prediction and the experimental breakthrough curves is satisfied.

Adsorption↗
PubMed2005

Effect of temperature on competitive adsorption of the solute and the organic solvent in reversed-phase liquid chromatography.

In analysis of the temperature effect on chromatographic separations the influence of the adsorption of organic solvent on the retention properties of solute is generally not taken into account. In fact, adsorption behavior of solutes is strongly affected by competitive adsorption of organic solvents, which is temperature dependent. In this work changes of adsorption equilibrium of an organic solvent as well as a solute with temperature have been analyzed. Data of the excess adsorption of methanol from aqueous solutions on octadecyl-bonded silica have been acquired at different temperature. Experiments have been performed over a relatively narrow temperature range corresponding to typical chromatographic conditions, i.e., 10-50 degrees C. The competitive adsorption equilibria of model solutes (i.e., two homologous compounds: cyclopentanone and cyclohexanone) have been measured at different temperature and composition of the mobile phase. Temperature alterations to the retention properties were found to result from combined effects of changes in adsorption behavior of the organic solvent and of the solute. The influence of temperature on the separation selectivity has been considered.

Adsorption↗
PubMed2006

Incorporating water-release and lateral protein interactions in modeling equilibrium adsorption for ion-exchange chromatography.

The equilibrium adsorption of two albumin proteins on a commercial ion exchanger has been studied using a colloidal model. The model accounts for electrostatic and van der Waals forces between proteins and the ion exchanger surface, the energy of interaction between adsorbed proteins, and the contribution of entropy from water-release accompanying protein adsorption. Protein-surface interactions were calculated using methods previously reported in the literature. Lateral interactions between adsorbed proteins were experimentally measured with microcalorimetry. Water-release was estimated by applying the preferential interaction approach to chromatographic retention data. The adsorption of ovalbumin and bovine serum albumin on an anion exchanger at solution pH>pI of protein was measured. The experimental isotherms have been modeled from the linear region to saturation, and the influence of three modulating alkali chlorides on capacity has been evaluated. The heat of adsorption is endothermic for all cases studied, despite the fact that the net charge on the protein is opposite that of the adsorbing surface. Strong repulsive forces between adsorbed proteins underlie the endothermic heat of adsorption, and these forces intensify with protein loading. It was found that the driving force for adsorption is the entropy increase due to the release of water from the protein and adsorbent surfaces. It is shown that the colloidal model predicts protein adsorption capacity in both the linear and non-linear isotherm regions, and can account for the effects of modulating salt.

Adsorption↗