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PubMed2003

Adsorption of autoantibodies in the presence of LISS to detect alloantibodies underlying warm autoantibodies.

BACKGROUND: The safe transfusion of patients with warm autoimmune hemolytic anemia requires an efficient and time-saving assay to detect alloantibodies underlying autoantibodies. Methods used include RBCs treated with ZZAP reagent, proteolytic enzyme, or untreated RBCs in the presence of PEG. We propose a method using LISS, which presents some advantages over previous methods. STUDY DESIGN AND METHODS: We evaluated the effectiveness of autoantibody adsorption with papain-treated and untreated RBCs in the presence of LISS for removal of autoantibodies, without affecting alloantibodies. RESULTS: One-hundred twenty sera containing autoantibodies were adsorbed with our routine method, which uses papain-treated allogeneic RBCs. Seven-hundred twenty adsorptions (mean, 6 per sample) and 21,600 minutes (mean, 180 min per sample) were required to remove autoantibodies. Fifty sera were adsorbed with our routine method that uses papain-treated allogeneic RBCs in the presence of LISS. The number of adsorptions and the completion time were, respectively, 144 (mean, 2.9 per sample) and 2,880 minutes (mean, 57.6 min per sample). Twenty sera were evaluated with untreated autologous RBCs, in the presence of LISS; 58 adsorptions (mean, 2.9) and 1,160 minutes (mean, 58 min per sample) were required. Three adsorptions with antigen-negative allogeneic RBCs were performed on 8 sera containing alloantibodies with weak reactivity (anti-K [1], anti-D [1], anti-Fya[2], anti-S [2], anti-E [1], and anti-Jka[1]). Alloantibodies were detected with the LISS procedure with papain-treated and untreated RBCs and the routine papain method. Alloantibodies with weak reactivity, tested against the same antibody-detection RBCs, remained unchanged following adsorption of 5 sera. An anti-S, with very weak reactivity, was no longer detected, and an anti-Jka became weaker (1+), regardless of the procedure used. One anti-D became weaker only with the LISS adsorption method. CONCLUSION: Autoantibodies can be adsorbed more efficiently in the presence of LISS.

Autoantibodies↗
PubMed2004

Grand canonical Monte Carlo simulation of argon adsorption at the surface of silica nanopores: effect of pore size, pore morphology, and surface roughness.

Argon adsorption (77 K) in atomistic silica nanopores of various sizes and shapes has been studied by means of grand canonical Monte Carlo simulations (GCMC). We discuss the effects of confinement (pore size), pore morphology (ellipsoidal, hexagonal, constricted pore), and surface texture (rough/smooth) on the thickness variation of the adsorbed film with pressure onto the disordered inner surface of porous materials (usually called t-plot or t-curve). We show that no confinement effect occurs when the diameter of the regular cylindrical pore is larger than 10 nm. For pores smaller than 6 nm, we find that the film thickness increases as the pore size decreases. We show that the adsorption isotherm in the rough pore can be described as the sum of an adsorbed amount similar to that found for a smooth pore (of the same radius) and a constant contribution due to atoms "trapped" in the infractuosities of the rough surface which act as a microporous texture. Simulation snapshots for Ar adsorption in hexagonal and ellipsoidal smooth pores indicate that at low pressures the gas/adsorbate interface retains memory of the pore shape and becomes cylindrical prior to the capillary condensation of the fluid in the pore. The film thickness in the hexagonal pore is close to that obtained for a cylindrical pore having a similar dimension. By contrast, we find that the film thickness for an ellipsoidal pore is always larger than that for an equivalent cylindrical pore (having the same length and volume but a circular section). We show that this effect strengthens as the pore size decreases and/or the pore asymmetry increases. Ar adsorption in a cylindrical constricted pore shows that the presence of the narrower part considerably modifies the adsorption mechanism. Finally, we report GCMC simulations of Ar adsorption (77 K) on a plane silica reference substrate for different intermolecular potentials. We discuss the effect of the interaction on the shape of the adsorption isotherm and compare our results with experiments.

Journal Article↗
PubMed2004

Adsorption modes of cysteine on Au(111): thiolate, amino-thiolate, disulfide.

The adsorption of cysteine on the (111) surface of gold has been studied by means of periodic supercell density-functional theory calculations. A number of different adsorption modes are examined, including adsorption through the thiol group in either thiolate or disulfide form, and adsorption through both the thiol and amino functional groups. We find that at intermediate coverage densities the latter mode of adsorption is favored, followed by thiolate adsorption at the bridge (slightly displace toward fcc) site. The N-Au and S-Au bond strengths in the amino-thiolate adsorption are estimated to be of the order of 6 and 47 kcal/mol, respectively. The electronic structure of the different systems is analyzed, with focus on the total and projected density of states, as well as on the detailed character of the electronic states at the interface. States near the Fermi energy are found to have a metal-molecule antibonding character, whereas metal-molecule bonding states mostly occur near the lower edge of the Au-d band.

Journal Article↗
PubMed2004

Geometric view of the thermodynamics of adsorption at a line of three-phase contact.

We consider three fluid phases meeting at a line of common contact and study the linear excesses per unit length of the contact line (the linear adsorptions Lambda(i)) of the fluid's components. In any plane perpendicular to the contact line, the locus of choices for the otherwise arbitrary location of that line that makes one of the linear adsorptions, say Lambda(2), vanish, is a rectangular hyperbola. Two of the adsorptions Lambda(2) and Lambda(3) then both vanish when the contact line is chosen to pass through any of the intersections of the two corresponding hyperbolas Lambda(2)=0 and Lambda(3)=0. There may be two or four such real intersections. It is found most surprisingly, and confirmed in a numerical example, that Lambda(1(2,3)), the adsorption of component 1 in a frame of reference in which the adsorptions Lambda(2) and Lambda(3) are both 0, depends on which intersection of the hyperbolas Lambda(2)=0 and Lambda(3)=0 is chosen for the location of the contact line. This implies that what had long been taken to be the line analog of the Gibbs adsorption equation is incomplete; there must be additional, previously unanticipated terms in the relation, consistent with the invariance of the line tension to choice of location of the contact line. It is then not Lambda(1(2,3)) by itself but a related expression containing it that must be invariant, and this invariance is also confirmed in the numerical example. The presence of the additional terms in the adsorption equation is further confirmed and their origin clarified in a mean-field density-functional model. The supplemental terms vanish at a wetting transition, where one of the contact angles goes to 0.

Journal Article↗
PubMed2005

Monte Carlo simulations of hydrogen adsorption in alkali-doped single-walled carbon nanotubes.

Monte Carlo simulations and Widom's test particle insertion method have been used to calculate the solubility coefficients (S) and the adsorption equilibrium constants (K) in single-walled (10,10) armchair carbon nanotubes including single nanotubes, and nanotube bundles with various configurations with and without alkali dopants. The hydrogen adsorption isotherms at room temperature were predicted by following the Langmuir adsorption model using the calculated constants S and K. The simulation results were in good agreement with experimental data as well as the grand canonical Monte Carlo simulation results reported in the literature. The simulations of nanotube bundle configurations suggest that the gravimetric hydrogen adsorption increases with internanotube gap size. It may be attributed to favorable hydrogen-nanotube interactions outside the nanotubes. The effect of alkali doping on hydrogen adsorption was studied by incorporating K+ or Li+ ions into nanotube arrays using a Monte Carlo simulation. The results on hydrogen adsorption isotherms indicate hydrogen adsorption of 3.95 wt% for K-doping, and 4.21 wt% for Li-doping, in reasonable agreement with the experimental results obtained at 100 atm and room temperature.

Journal Article↗
PubMed2006

Simulated water adsorption in chemically heterogeneous carbon nanotubes.

Grand canonical Monte Carlo simulations are used to study the adsorption of water in single-walled (10:10), (12:12), and (20:20) carbon nanotubes at 298 K. Water is represented by the extended simple point charge model and the carbon atoms as Lennard-Jones spheres. The nanotubes are decorated with different amounts of oxygenated sites, represented as carbonyl groups. In the absence of carbonyl groups the simulated isotherms are characterized by negligible amounts of water uptake at low pressures, sudden and complete pore filling once a threshold pressure is reached, and wide adsorption-desorption hysteresis loops. In the presence of a few carbonyl groups the simulated adsorption isotherms are characterized by pore filling at lower pressures and by narrower adsorption-desorption hysteresis loops compared to the results obtained in the absence of carbonyl groups. Our results show that the distribution of the carbonyl groups has a strong effect on the adsorption isotherms. For carbonyl groups localized in a narrow section the adsorption of water may be gradual because a cluster of adsorbed water forms at low pressures and grows as the pressure increases. For carbonyl groups distributed along the nanotube the adsorption isotherm is of type V.

Journal Article↗
PubMed2001

[Elimination of carbendazim from fruit conditioning waters by adsorption on different materials].

The main aim of this work is to test different materials (activated carbon and other more "rustic" materials like clay and coal) as potential adsorbents in order to evaluate their adsorption capacity for carbendazime. The experiments were realized with certified carbendazim or with benlate solutions left to change long enough to suppose all the benomyl converted into carbendazim. The results were introduced through adsorption kinetic and isotherm forms or interpreted according to the Langmuir model. They pointed out that final elimination percentages of certified carbendazim don't exceed 55%. But even the activated carbon remains the most effective adsorbent, clay and coal present an interesting adsorption capacity, 45% for clay (but its performance is varied), 35% for coal. The presence of formulation additives has an inhibitive effect whatever the materials is. Some adsorption attempts with clay and coal mixtures (100 mg l(-1) of each one) were realized, there isn't a cumulative adsorption, final percentages of elimination are about 45%. Characterization attempts of the adsorbents pointed out that all the materials have a negative global surface charge. But clay possesses a surface charge far more negative than coal, sodipolary lap of carbendazim can further the adsorption. The measures of surface functions according to Boehm titration and capillary rising technique showed that coal differentiates from the other materials by its high capacity to establish Lifshitz-Van der Waals interactions. Carbendazim molecule can present a dipolary moment which could lead to the formation of hydrogen bonds. But results of capillary rising are to be considered by surface unities that could explain the superior adsorption capacity of clay (internal surface: 800m2 g(-1)).

Aluminum Silicates↗
PubMed2000

Statistical fractal adsorption isotherms, linear energy relations, and power-law trapping-time distributions in porous media

Drazer and Zanette [Phys. Rev. E 60, 5858 (1999)] have reported on interesting experiments which show that trapping-time distributions in porous media obey a scaling law of the negative power-law type. Unfortunately, their theoretical interpretation of the experimental data has physical and mathematical inconsistencies and errors. Drazer and Zanette assume the existence of a distribution of local adsorption isotherms for which the random parameter is not a thermodynamic function, but a kinetic parameter, the trapping time. Moreover, they mistakenly identify the reciprocal value of a rate coefficient with the instantaneous (fluctuating) value of the trapping time. Their approach leads to mathematically inconsistent probability densities for the trapping times, which they find to be non-normalizable. We suggest a different theory, which is physically and mathematically consistent. We start with the classical patch approximation, which assumes the existence of a distribution of adsorption heats, and introduce two linear energy relationships between the activation energies of the adsorption and desorption processes and the adsorption heat. If the distribution of the adsorption heat obeys the exponential law of Zeldovich and Roghinsky, then both the adsorption isotherm and the probability density of trapping times can be evaluated analytically in terms of the incomplete beta and gamma functions, respectively. Our probability density of the trapping times is mathematically consistent; that is, it is non-negative and normalized to unity. For large times it has a long tail which obeys a scaling law of the negative power-law type, which is consistent with the experimental data of Drazer and Zanette. By using their data we can evaluate the numerical values of the proportionality coefficients in the linear energy relations. The theory suggests that experimental study of the temperature dependence of the fractal exponents helps to elucidate the mechanism of the adsorption-desorption process.

Journal Article↗
PubMed1984

Adsorption of slow- and fast-growing rhizobia to soybean and cowpea roots.

Roots of soybean (Glycine max [L.] Merr. cv Hardee) and cowpea (Vigna unguiculata [L.] Walp. cv Pink Eye Purple Hull) were immersed in suspensions containing 10(4)Rhizobium cells per milliliter of a nitrogen-free solution. After 30 to 120 minutes the roots were rinsed, and the distal 2-centimeter segments excised and homogenized. Portions of the homogenates then were plated on a yeast-extract mannitol medium for bacterial cell counts. The adsorption capacities of four slow-growing rhizobia and a fast-growing R. meliloti strain varied considerably. Adsorption was independent of plant species and of the abilities of the Rhizobium strains to infect and nodulate. R. lupini 96B9 had the greatest adsorption capacity, and Rhizobium sp. 3G4b16 the least. Rhizobium sp. 229, R. japonicum 138, and R. meliloti 102F51 were intermediate, except on cowpea, where the adsorption of strain 102F51 was similar to that of strain 3G4b16. The initial adsorption rates of bacteria cultured in synthetic media and in the presence of soybean roots were about the same. Addition of soybean lectin to the bacterial inoculum failed to influence initial adsorption rates. Both treatments, however, reduced the numbers of bacteria that bound after incubation with roots for 120 minutes. The relationship between the logarithm of the number of strain 138 cells bound per soybean root segment and the logarithm of the density of bacteria in the inoculum was linear over five orders of magnitude. Binding of strain 138 to soybean roots was greatest at room temperature (27 degrees C) and substantially attenuated at both 4 and 37 degrees C. Although R. lupini 96B9 strongly rejected a model hydrophobic plastic surface, there were no simple correlations between bacterial binding to model hydrophobic and hydrophilic plastic surfaces and bacterial adsorption to roots.

Journal Article↗
PubMed2005

Suppression of inflammatory cytokine secretion by granulocyte/monocyte adsorptive apheresis in active ulcerative colitis.

To elucidate the molecular mechanisms involved in the therapeutic effects of granulocyte/monocyte adsorption apheresis, changes were investigated in the cytokine responses of peripheral blood mononuclear cells (PBMC) before and after granulocyte/monocyte adsorptive apheresis in ulcerative colitis (UC) patients. Four patients with active UC were enrolled. All patients responded to granulocyte/monocyte adsorptive apheresis. A total of 20 sessions of four patients were analyzed. Peripheral blood mononuclear cells were isolated from peripheral venous blood within 5 min before and after each session of granulocyte/monocyte adsorptive apheresis. The cells were stimulated with interleukin (IL)-1beta and tumor necrosis factor (TNF)-alpha for 24 h, and the secreted IL-8 and IL-6 levels were determined by enzyme-linked immunosorbent assay (ELISA). IL-1beta-induced IL-8 and IL-6 secretion was significantly decreased after granulocyte/monocyte adsorptive apheresis. TNF-alpha-induced IL-8 secretion was also significantly decreased after apheresis, but there was no significant difference in TNF-alpha-induced IL-6 secretion (P = 0.052). In conclusion, granulocyte/monocyte adsorptive apheresis down-regulates the IL-1beta- and TNF-alpha-induced inflammatory responses in PBMC. The induction of hyporesponsiveness to pro-inflammatory cytokines may be an important factor mediating the clinical effects of granulocyte/macrophage adsorptive apheresis in UC patients.

Adult↗
PubMed1995

Early Interactions of Rhizobium leguminosarum bv. phaseoli and Bean Roots: Specificity in the Process of Adsorption and Its Requirement of Ca(sup2+) and Mg(sup2+) Ions.

Roots of Phaseolus vulgaris L. were incubated with dilute suspensions (1 x 10(sup3) to 3 x 10(sup3) bacteria ml(sup-1)) of an antibiotic-resistant indicator strain of Rhizobium leguminosarum bv. phaseoli in mineral medium and washed four times by a standardized procedure prior to quantitation of adsorption (G. Caetano-Anolles and G. Favelukes, Appl. Environ. Microbiol. 52:371-376, 1986). The population of rhizobia remaining adsorbed on roots after washing was homogeneous, as indicated by the first-order course of its desorption by hydrodynamic shear. Rhizobia were maximally active for adsorption in the early stationary phase of growth. The process leading to adsorption was rapid, without an initial lag, and slowed down after 1 h. Adsorption of the indicator strain at 10(sup3) bacteria ml(sup-1) was inhibited to different extents in the presence of 10(sup3) to 10(sup8) antibiotic-sensitive competitor rhizobia ml(sup-1). After a steep rise above 10(sup4) bacteria ml(sup-1), inhibition by heterologous competitors in the concentration range of 10(sup5) to 10(sup7) bacteria ml(sup-1) was markedly less than by homologous strains, while at 10(sup8) bacteria ml(sup-1) it approached the high level of inhibition by the latter. At 10(sup7) bacteria ml(sup-1), all of the heterologous strains tested were consistently less inhibitory than homologous competitors (P < 0.001). These differences in competitive behavior indicate that in the process of adsorption of R. leguminosarum bv. phaseoli to its host bean roots, different modes of adsorption occur and that some of these modes are specific for the microsymbiont (as previously reported for the alfalfa system [G. Caetano-Anolles and G. Favelukes, Appl. Environ. Microbiol. 52:377-381, 1986]). Moreover, whereas the nonspecific process occurred either in the absence or in the presence of Ca(sup2+) and Mg(sup2+) ions, expression of specificity was totally dependent on the presence of those cations. R. leguminosarum bv. phaseoli bacteria adsorbed in the presence of Ca(sup2+) and Mg(sup2+) were more resistant to desorption by shear forces than were rhizobia adsorbed in their absence. These results indicate that (i) symbiotic specificity in the P. vulgaris-R. leguminosarum bv. phaseoli system is expressed already during the early process of rhizobial adsorption to roots, (ii) Ca(sup2+) and Mg(sup2+) ions are required by R. leguminosarum bv. phaseoli for that specificity, and (iii) those cations cause tighter binding of rhizobia to roots.

Journal Article↗
PubMed1991

Early recognition in the Rhizobium meliloti-alfalfa symbiosis: root exudate factor stimulates root adsorption of homologous rhizobia.

Adsorption of Rhizobium meliloti to alfalfa roots before their infection and nodule formation shows the specificity of the symbiotic association (G. Caetano-Anollés and G. Favelukes, Appl. Environ. Microbiol. 52:377-382, 1986). The time course of specific adsorption of R. meliloti (10(3) to 10(4) cells per ml) to roots shows an initial lag period of 3 h, suggesting that either or both symbionts must become conditioned for the adsorption process. Preincubation of R. meliloti L5-30 for 3 h with dialyzed alfalfa root exudate (RE) markedly increased early adsorption of rhizobia to alfalfa roots. The activity in RE was linked to a nondialyzable, thermolabile, trypsin-sensitive factor(s), very different from the root-exuded flavonoid compounds also involved in early Rhizobium-legume interactions. The lack of activity in the RE from plants grown in 5 mM NO3- suggested its negative regulation by the nitrogen nutritional status of the plant. Preincubation of R. meliloti with heterologous clover RE did not stimulate adsorption of rhizobial cells to roots. A short pretreatment of RE with homologous (but not heterologous) strains eliminated the stimulatory activity from solution. The stimulation of adsorption of R. meliloti to alfalfa roots was strongly dependent on the growth phase of the rhizobia, being greater at the late exponential stage. Nevertheless, the capacity of R. meliloti L5-30 to eliminate from solution the stimulatory activity in RE appeared to be constitutive in the rhizobia. The low concentration of rhizobial cells used in these experiments was critical to detect the stimulation of adsorption. The early interaction of spontaneously released alfalfa root macromolecular factor(s) and free-living R. meliloti, which shows the specificity and regulatory properties characteristic of infection and nodulation, would be an initial recognition event in the rhizosphere which triggers the process of symbiotic association.

Bacterial Adhesion↗
PubMed2005

Immobilized metal affinity beads for ferritin adsorption.

A new metal-chelate adsorbent utilizing N-methacryloyl-(L)-cysteine methyl ester (MAC) was prepared as a metal-chelating ligand. MAC was synthesized by using methacryloyl chloride and L-cysteine methyl ester dihydrochloride. Spherical beads with an average diameter of 150-200 microm were produced by suspension polymerization of 2-hydroxyethyl methacrylate (HEMA) and MAC carried out in an aqueous dispersion medium. Then, Fe(3+) ions were chelated directly on the beads. Properties such as specific surface area, specific pore volume and ligand occupation were determined. The specific surface area of the beads was found to be 18.9 m2/g. The total pore volume was 2.8 ml/g and represented a porosity over 52%. The average pore size of the poly(HEMA-MAC) beads was 620 nm. Fe(3+)-chelated beads were used in the adsorption of ferritin from aqueous solutions. Ferritin adsorption increased with increasing ferritin concentration. The maximum ferritin adsorption capacity of the Fe(3+)-chelated poly(HEMA-MAC) beads (Fe(3+) loading 0.81 mmol/g) was found to be 3.7 mg/g at pH 4.0 in acetate buffer. The non-specific ferritin adsorption on the poly(HEMA-MAC) beads were 0.4 mg/g. Adsorption behavior of ferritin could be modelled using both the Langmuir and Freundlich isotherms. Adsorption capacity decreased with increasing ionic strength of the binding buffer. Ferritin molecules could be adsorbed and desorbed five times with these adsorbents without noticeable loss in their ferritin adsorption capacity.

Cysteine↗
PubMed2003

Reversible and irreversible adsorption of surfactants at a hanging mercury drop electrode.

The adsorption-desorption phenomena of surfactants were studied by measuring differential capacity-potential curves in a static solution and differential capacity-time curves in a flowing solution. The surfactants investigated were Aerosol OT, cetylpyridinium chloride, Hyamin 1622, tetrabutylammonium bromide, Triton X-100 and trioctylphosphineoxide. The differential capacity-potential and differential capacity-time curves for these surfactants showed different shapes, with and without peaks. The differential capacity-time curves were used to study the adsorption reversibility of the surfactants at a mercury electrode. The adsorptions of Hyamin 1622 and Triton X-100 were irreversible at all the potentials investigated. The adsorptions of Aerosol OT and trioctylphosphineoxide were irreversible except at the potential more positive than -0.2 V. The adsorption of tetrabutylammonium bromide was almost reversible at any potential investigated. The adsorption of cetylpyridinium chloride was complicated, indicating different orientations of adsorption.

Journal Article↗
PubMed2004

Effects of hemoperfusion adsorption and/or plasma exchange in treatment of severe viral hepatitis: a comparative study.

AIM: Non-bioartificial liver has been applied to clinic for quite a long time, but the reported efficacy has been very different. The aim of this study was to compare the efficacy and safety of hemoperfusion adsorption, plasma exchange and plasma exchange plus hemoperfusion adsorption in treatment of severe viral hepatitis. METHODS: Seventy-five patients with severe viral hepatitis were treated with hemoperfusion adsorption therapy (24 cases), plasma exchange therapy (17 cases) and plasma exchange plus hemoperfusion adsorption therapy (34 cases). The data of liver function, renal function, blood routine test, prothrombin time (PT) and prothrombin activity (PTa) pre- and post-therapy were analyzed. RESULTS: Clinical symptoms of patients improved after treatment. The levels of aminotransferase, total bilirubin, direct bilirubin decreased significantly after 3 therapies (P<0.05 or P<0.01). PT, the level of total serum protein decreased significantly and PTa increased significantly after plasma exchange therapy and plasma exchange plus hemoperfusion adsorption therapy (P<0.05 or P<0.01). The side effects were few and mild in all patients. CONCLUSION: Three therapies were effective in the treatment of severe viral hepatitis. Plasma exchange therapy and plasma exchange plus hemoperfusion adsorption therapy are better than hemoperfusion adsorption therapy.

Adult↗
PubMed1988

The adsorption of metronidazole and tinidazole to activated charcoal and the effect of magnesium sulfate.

The effect of magnesium sulfate on the in vitro adsorption of metronidazole and tinidazole to activated charcoal was studied. Solutions of metronidazole and tinidazole were prepared at low concentrations of 6.25, 12.5, 25.0 and 50 micrograms/ml and at simulated toxic concentrations of 0.5, 1.0, 2.0, 5.0 and 10 mg/ml in distilled water. Drug charcoal slurries were vortex-mixed, centrifuged and analyzed for free drug. Metronidazole gave adsorption capacities of 62.2-82.7% with 50 and 200 mg activated charcoal. Fifty and 200 mg activated charcoal adsorbed 80-90% of tinidazole. Metronidazole at 0.5 mg/ml had 16.7, 30.0, 56.7, 75.0 and 83.3% adsorption with 12.5, 50, 125, 250 and 500 mg charcoal respectively. There was a corresponding increase in the adsorption of metronidazole and tinidazole at the increasing concentrations of activated charcoal. The adsorption of metronidazole and tinidazole also seemed to be dose dependent. Magnesium sulfate (7.5 mg/ml) enhanced the adsorption of metronidazole to activated charcoal, but had no effect on tinidazole-charcoal adsorption.

Charcoal↗
PubMed1995

Synthesis of thiophilic adsorbents, containing amine spacer arms, and adsorption of immunoglobulins from adult bovine serum.

In order to remove immunoglobulins from adult bovine serum (ABS), adsorptions were carried out in suspension with thiophilic adsorbents without (T-gel) and with (ST-gels) short amine spacer. The developed ST-gels could be cleaned in sodium hydroxide and specifically adsorbed immunoglobulins from ABS at a lower ionic strength of the adsorption buffer than a T-gel. The ST-gels are suited for the performance of adsorptions in a suspension with a high concentration of the adsorbent. For an almost complete removal of immunoglobulins from ABS in 0.5 M potassium sulfate and 0.1 M potassium phosphate (pH 7), up to 75 g ST-gel per 1 suspension may process up to 100 ml ABS. The synthesized ST-gels contained an equal amount of amine spacers and sulfone groups. The ratio between coupled 2-mercaptoethanol molecules and sulfone groups was about 0.4. In comparison with the T-gel, the chemical stability of the ST-gels in solutions of 0.1 to 1 M sodium hydroxide was higher. The capacity for adsorbing pure immunoglobulins of the T-gel was 0.329 g g-1 (10.9 g l-1) and of the ST2-gel, 0.677 g g1 (52.3 g l-1). The capacity for adsorbing IgG from ABS of the T-gel was 0.177 g g1 (5.88 g l-1) and of the ST2-gel, 0.152 g g-1 (11.7 g l-1). This reduced capacity was attributed to a low affinity binding to the adsorbents of other proteins from ABS. When an incubation of the adsorbent with ABS was performed in 0.5 M potassium sulfate and 0.1 M potassium phosphate (pH 7), the affinity constant (Ka) for IgG of the T-gel was 2.5 x 10(6) M-1 and of the ST-gel, 3.1 x 10(7) M-1. In this adsorption buffer at a protein concentration above 5 g l-1, salt-promoted precipitation of IgG took place. When an adsorption was performed at the minimal ionic strength of the adsorption buffer, the Ka of the T-gel for IgG was about 9 x 10(3) M-1 and of the ST-gel, about 2.3 x 10(5) M-1. In this case, the removal of Igs from ABS was achieved by means of a partition equilibrium, rather than by high affinity adsorption.

Amines↗
PubMed1994

Effect of denaturants and stabilisers on protein adsorption at solid-liquid interfaces.

The adsorption isotherms of different proteins from aqueous solution to the surface of different solids have been compared in the presence of additives such as urea, surfactants and high concentration of various neutral salts. The adsorption isotherms of lysozyme on alumina are not affected much in the presence of 8 M urea showing the rigid structure of lysozyme whereas isotherms of hemoglobin show surface coagulation even in presence of 2 M urea. In presence of 8 M urea, adsorption isotherms of BSA on alumina show two distinct steps. The extent of protein adsorption in the presence of surfactants depends on the nature of surfactants as well as of the underlying surface. The adsorption isotherms of BSA and lysozyme in presence of 2 M concentration of different neutral salts have also been compared with each other. In the presence of denaturants such as NaI and LiCl, the proteins are adsorbed in unfolded beta-conformation whereas in the presence of protein stabilizers such as NaCl, KCl and Na2SO4, amount of protein adsorbed at saturation is zero or extremely small showing that unfolding of proteins at the interface is necessary for initial stage of protein adsorption. The standard free energy change (delta G degrees) per square meter of the surface, signifying relative affinity of adsorption at the state of monolayer saturation, have been calculated. The magnitude of standard free energy of transfer (delta G degrees B) of one mole of protein to the surface in presence of all the additives was found close to 40 kJ/mole.

Absorption↗