Surface Energetics to Assess Microbial Adhesion onto Fluidized Chromatography Adsorbents

Cell‐to‐support interaction and cell‐to‐cell aggregation phenomena have been studied in a model system composed of intact yeast cells and agarose‐based chromatography adsorbent surfaces. Biomass components and beaded adsorbents were characterized by contact angle determinations with three diagnostic liquids and, complementarily, by zeta potential measurements. Such experimental characterization of the interacting surfaces has allowed the calculation of interfacial free energy of interaction in aqueous media vs. distance profiles. The extent of biomass adhesion was inferred from calculations performed assuming standard chromatographic conditions, but different adsorption modes. Several stationary support/mobile phase systems were considered, i.e., ion exchange, hydrophobic interaction, and pseudo‐affinity. The calculated interaction energy minima revealed marginal attraction between cells and cation exchangers or agarose‐matrix beads (U ≤ |10–20| kT) but strong attraction with anion exchangers (U ≥ |200–1000| kT). Other systems including hydrophobic interaction and chelating beads showed intermediate energy minimum values (U <$>\approx<$> |40–100| kT) for interaction with biological particles. However, the calculations also showed that working conditions in the presence of salt can promote cell aggregation apart from cell‐to‐support interaction. Predictions based on the application of the XDLVO approach were confirmed by independent experimental methods, e.g., biomass deposition experiments and laser diffraction spectroscopy. The understanding of biomass attachment onto chromatographic supports can help in alleviating process limitations normally encountered during direct (primary) sequestration of bioproducts.     

Surface energetics to assess biomass attachment onto immobilized metal-ion chromatography adsorbents in expanded beds

Cell-to-support interaction and cell-to-cell agglomeration phenomena have been studied in a model system composed of intact yeast cells and Chelating-Streamline™ adsorbents. Biomass components and beaded adsorbents were mainly characterized by contact angle determinations with three diagnostic liquids. Complementarily, zeta potential measurements were performed. These experimental values were employed to calculate free energy of interaction versus distance profiles in aqueous media. The effect of immobilized metal-ion type and buffer pH on the interaction energy was evaluated. Calculations indicated that moderate interaction between cell particles and adsorbent beads can develop due to the presence of Cu²⁺ ions onto the solid phase. The strength of interaction increased with buffer pH, within the range 6.0 to 8.3 e.g. secondary energy pockets increased from |15| to |60| kT. Cell-to-cell secondary energy minimum was ≥ |14| kT showing low-to-moderate tendencies to aggregate, particularly at pH ≥ 8. Extended DLVO predictions were generally confirmed by biomass deposition experiments. However, an exception was found when working with immobilized Cu²⁺ at pH 8 since yeast cells were able to sequestrate such immobilized ions. Therefore, lower-than-expected values for the depositions coefficient (α) were observed. Understanding biomass attachment onto Chelating supports can help in better design and operate expanded bed adsorption of bioproducts.     

Eco-physiological characteristics of alfalfa seedlings in response to various mixed salt-alkaline stresses

Soil salinization and alkalization frequently co-occur in nature, but little is known about the mixed effects of salt-alkaline stresses on plants. An experiment with mixed salts （NaCI, Na2SO4, NaHCO3 and Na2CO3） and 30 salt-alkaline combinations （salinity 24-120 mmollL and pH 7.03-10.32） treating Medicago sativa seedlings was conducted. The results demonstrated that salinity and alkalinity significantly affected total biomass and biomass components of seedlings. There were interactive effects of salt composition and concentration on biomass （P 〈 0.001）. The interactions between salinity and alkalinity stresses led to changes in the root activity along the salinity gradient （P 〈 0.001）. The effects of alkalinity on seedling survival rate were more significant than those of salinity, and the seedlings demonstrated some physiological responses （leaf electrolyte leakage rate and proline content） in order to adapt to mixed salt-alkaline stresses. It was concluded that the mixed salt-alkaline stresses, which differ from either salt or alkali stress, emphasize the significant interaction between salt concentration （salinity） and salt component （alkalinity）. Further, the effects of the interaction between high alkalinity and salinity are more severe than those of either salt or alkali stress, and such a cooperative interaction results in more sensitive responses of ecological and physiological characteristics in plants.     

Hydrophobicity of lectins. I. The hydrophobic character of concanavalin A.

The hydrophobicity of Concanavalin A has been estimated by its tendency to adsorb to hydrophobic adsorbents. Experiments varying temperature, salt concentration and hydrophobicity of the absorbent were consistent with accepted criteria of hydrophobic interaction between biomolecules and hydrophobic ligands. The biological significance of the hydrophobic character of Concanavalin A is also discussed.     

溶剂环境对乙肝表面抗原(HBsAg)结构的影响

HBsAg作为乙肝疫苗的主要成分,是一种病毒样颗粒,由蛋白质和脂类通过非共价键作用形成。HBsAg保持完整结构对其功能非常重要,而目前未见对其在溶液中结构变化的研究。考察了不同溶剂环境(温度、pH值、离子类型和盐浓度)对HBsAg结构的影响。实验发现,HBsAg在常温下比较稳定,但在温度超过60℃时稳定性明显下降;pH值小于4.0时引起不可逆聚集,但在pH5.0时的聚集部分可逆;不同离子对HBsAg的影响基本符合Hofmeister序列,不同之处是SO42-比F-更易引起HBsAg颗粒的聚集,在所考察的盐中,(NH4)2SO4对HBsAg有着较大的影响,0.4mol/L时就会引起HBsAg聚集,随着浓度增加,聚集现象更加严重,所以在HBsAg的疏水层析中要谨慎使用(NH4)2SO4。     

Characterization and isolation of intermediates in beta-lactoglobulin heat aggregation at high pH

The early stages of heat induced aggregation at 67.5 degrees C of beta-lactoglobulin were studied by combined static light scattering and size exclusion chromatography. At all conditions studied (pH 8.7 without salt and pH 6.7 with or without 60 mM NaCl) we observe metastable heat-modified dimers, trimers, and tetramers. These oligomers reach a maximum in concentration at about the time when large aggregates (1000-4000 kg/mol) appear, after which they decline in concentration. By isolating the oligomers it was demonstrated that they rapidly form aggregates upon heating in the absence of monomeric protein, showing that these species are central to the aggregation process. To our knowledge this is the first time that intermediates in protein aggregation have been isolated. At all stages of aggregation the dominant oligomer was the heat-modified dimer. Whereas the heat-modified oligomers are formed at a higher rate at pH 8.7 than at pH 6.7, the opposite is the case for the formation of aggregates from the metastable oligomers indicating cross-linking via disulfide bridges for the oligomers and noncovalent interaction in the formation of the aggregates. The data suggest that an aggregate nucleus is formed from four oligomers. For protein concentrations of 10 or 20 g/l a heat-modified monomer can be observed until about the time when the maximum in concentration appears of the heat-modified dimer. The disappearance of this heat-modified monomer correlates to the formation of dimers (trimers and tetramers).     

Adsorption of radium-226 by biological origin absorbents

Selected samples of waste microbial biomass used in industrial fermentation processes and wastewater biological treatment plants have been studied for their radium biosorption ability from aqueous solutions. Equilibrium biosorption isotherms have been used to quantify the radium uptake capacity of the various types of biomass which were also compared to two types of activated carbon. Solution pH affected the observed uptake significantly. In general, the biomass types that showed appreciable sorption capacity exhibited maximum uptake between pH 7 and 10. The uptake was reduced considerably at pH 4 and little or no uptake was observed at pH 2. Radium biosorptive uptake capacities of the order of 4.5 x 10(4) nCi/g, at pH 7 and at an equilibrium radium concentration of 1000 pCi/L, were determined for a mixed culture, while the biomass of Penicillium chrysogenum adsorbed 5 x 10(4) nCi/g radium under the same conditions. The highest uptake value for a sample of F-400 granular activated carbon was 3600 nCi/g at pH 7 and 1000 pCi/L radium concentration. The biosorptive radium uptake of microbial biomass is compared to literature values for other types of adsorbents. The most effective biomass types studied exhibited radium removals in excess of 99% of the radium in solution.     

Zeta potential as a diagnostic tool to evaluate the biomass electrostatic adhesion during ion-exchange expanded bed application

Expanded bed adsorption is an integrative technology in downstream processing allowing the direct capture of target proteins from biomass (cells or cell debris) containing feedstocks. Potential adhesion of biomass on the surface of adsorbent, however, may hamper the application of this technique. Since the electrostatic forces dominate the interactions between biomass and adsorbent, the concept of zeta potential was introduced to characterize the biomass/adsorbent electrostatic interactions during expanded bed application. The criterion of zeta potential evaluation proposed in the previous paper (Biotechnol Bioeng, 83(2):149-157, 2003) was verified further with the experimental validation. The zeta potential of intact cells and homogenates of four microorganisms (Escherichia coli, Bacillus subtilis, Pichia pastoris, and S. cerevisiae) were measured under varying pH and salt concentration, and two ion-exchange adsorbents (Streamline DEAE and Streamline QXL) were investigated. The biomass transmission index (BTI) from the biomass pulse response experiments was used as the indicator of biomass adhesion in expanded bed. Combining the influences from zeta potential of adsorbent (zeta(a)), zeta potential of biomass (zeta(b)) and biomass size (d), a good relationship was established between the zeta potential parameter (-zeta(a)zeta(b)d) and BTI for all experimental conditions. The threshold value of parameter (-zeta(a)zeta(b)d) can be defined as 120 mV2 microm for BTI above 0.9. This means that the systems with (-zeta(a)zeta(b)d) < 120 show neglectable electrostatic bio-adhesion, and would have a considerable probability of forming stable expanded beds in a biomass suspension under the particular experimental conditions.     

Heat-induced aggregation of recombinant erythropoietin in the intact and deglycosylated states as monitored by gel permeation chromatography combined with a low-angle laser light scattering technique.

Aggregate formation of recombinant human erythropoietin (r-EPO) on heat-treatment was followed by gel permeation chromatography combined with a low-angle laser light scattering technique under various conditions with respect to pH and salt concentration in order to provide basic knowledge about the change strictly required to be monitored for medicinal proteins. When heated at 60 degrees C at neutral pH, an aggregate with a limited size consisting of about 20 r-EPO molecules was formed. On heating at 50 degrees C at acidic pH, aggregation was unlimited. The aggregation proceeded non-covalently in acidic pH, but in alkaline pH covalent bond formation was also involved. Increase in salt concentration enhanced the aggregation. Deglycosylation of the N-linked oligosaccharides made r-EPO remarkably susceptible to aggregation on heat-treatment, indicating that the carbohydrate chains are essential to the stability of r-EPO.     

Kinetic growth parameters of different amylolytic and non-amylolytic Lactobacillus strains under various salt and pH conditions

Four Lactobacillus species were studied for their ability to grow at high NaCl concentrations and different initial pH values. Lactobacillus plantarum 541 and A6 could ferment glucose and produce lactic acid in the presence of 8% salt in the medium. For strain 541, the specific rate of lactate production (q(lac)) and the yield of lactic acid relative to substrate (Y(p/s)) remained constant, whereas the yield of biomass relative to substrate (Y(x/s)) decreased up to 6% salt. In contrast, for strain A6, Y(p/s) decreased up to 6% salt whereas Y(x/s) did not vary markedly. Combined effects of salt and pH studied through a factorial design did not show significant interaction between salt and pH. The pH was the dominant factor in glucose fermentation for both the strains. Considering overall performance, 4% salt and pH between 6.0 and 6.6 can be taken as appropriate conditions, for the use of both strains as starters in processes where higher salt concentrations are required.     

Preferential interactions determine protein solubility in three-component solutions: the MgCl2 system

The correlation between protein solubility and the preferential interactions of proteins with solvent components was critically examined with aqueous MgCl2 as the solvent system. Preferential interaction and solubility measurements with three proteins, beta-lactoglobulin, bovine serum albumin, and lysozyme, resulted in similar patterns of interaction. At acid pH (pH 2-3) and lower salt concentrations (less than 2 M), the proteins were preferentially hydrated, while at higher salt concentrations, the interaction was either that of preferential salt binding or low salt exclusion. At pH 4.5-5, all three proteins exhibited either very low preferential hydration or preferential binding of MgCl2. These results were analyzed in terms of the balance between salt binding and salt exclusion attributed to the increase in the surface tension of water by salts, which is invariant with conditions. It was shown that the increase in salt binding at high salt concentration is a reflection of mass action, while its decrease at acid pH is due to the electrostatic repulsion between Mg2+ ions and the high net positive charge on the protein. The preferential interaction pattern was paralleled by the variation of protein solubility with solvent conditions. Calculation of the transfer free energies from water to the salt solutions for proteins in solution and in the precipitate showed dependencies on salt concentration. This indicates that the nature of interactions between proteins and solvent components is the same in solution and in the solid state, which implies no change in protein structure during precipitation. Analysis of the transfer free energies and preferential interaction parameter in terms of the salting-in, salting-out, and weak ion binding contributions has led to the conclusions that, when the weak ion binding contribution is small, the predominant protein-salt interaction must be that of preferential salt exclusion most probably caused by the increase of the surface tension of water by addition of the salt. A necessary consequence of this is salting-out of the protein, if the protein structure is to remain unaltered.     

Use of the industrial yeastCandida utilis for cadmium sorption

The sorption ability of Candida utilis biomass for cadmium ions with accumulating competence of dried cells and cells in alginate was compared. After an optimization of process conditions (pH 5.5, biomass concentration 1 g/L and c0 50 mg/L), the cadmium sorption capacity of dried yeast biomass was perceptibly higher than that of the other tested adsorbents. Considering the sorption of the dried yeast biomass equal to 100 %, the cells in alginate reached 86 % while native cells showed only 42 %.     

The use of multifunctional adsorbents to purify membrane-bound phosphatases from Zymomonas mobilis. Purification of acid phosphatase, alkaline phosphatase and ATPase.

The purification of detergent-solubilized membrane-bound phosphatases from Zymomonas mobilis using novel adsorbents is described. The prepared adsorbents have a hydrophobic core with functional groups attached. These functional groups may either increase or decrease the hydrophobicity of the adsorbent, or participate in other forms of interactions. Adsorption of acid phosphatase (ACP), alkaline phosphatase (ALP) and ATPase to these adsorbents was salt-promoted. Desorption was achieved by decreasing the salt concentration or by displacement with increasing concentration of Triton X-100. The results indicate that chromatography on multifunctional adsorbents that are predominantly hydrophobic in character is a procedure that can have a general applicability in purification of membrane proteins.     

Investigation into the mechanism of (-)-epigallocatechin-3-gallate-induced precipitation of insulin

The molecular interactions between EGCG and insulin were investigated to probe the mechanism of EGCG-induced insulin precipitation. The results indicated that 1-5mM EGCG induced insulin into reversible globular precipitates of 185-365 nm. The formation of precipitates was facilitated at high salt concentration and pH values close to insulin's isoelectric point, indicating that hydrophobic interaction was the main driving force. The precipitation was positively related to insulin concentration, but for EGCG, there was a suitable concentration (2 mM at 2 mg/mL of insulin) at which the precipitate content reached maximum. Mass spectroscopy analysis indicated that EGCG formed clusters in the aqueous solution and the clusters correlate with the insulin precipitation. Based on extensive investigation, a physical model was proposed to explain the molecular interactions between EGCG and insulin. Namely, EGCG monomers and clusters first bound to insulin dimers via hydrophobic interaction, leading to the reduction of the thickness of the hydration layer and the partial denaturation of insulin. Then, EGCG clusters acted as bridges to induce the aggregation and precipitation of insulin.     

Negative chromatography: Progress,applications and future perspectives

In negative chromatography, the impurities bind on the adsorbent, and the product is allowed to flow through the chromatographic column. Negative chromatography is an alternative to positive chromatography under certain circumstances and has been used to purify various biomolecules. For this review, a detailed survey of the performance of reported studies on negative chromatography was conducted. The applications of negative chromatography in the capture and intermediate purification steps for biomolecules (e.g., plasmid DNA, antibodies, enzymes, hemoglobin, virus particles and cells) are reviewed. The negative chromatographic adsorbents adsorb the impurities through surface charge, hydrophobic interaction at specific sites on the surface, hydrophobic interaction, hydrogen bonding and functional groups. Examples of applications of negative chromatography according to the type of chromatography matrix used are summarized and discussed. In addition, the effects of operating conditions (initial protein concentration, buffer ions, pH and salt concentration) are discussed, and the criteria for choosing negative or positive chromatography are summarized. The literature survey showed that there will be future limitations and challenges ahead in implementation of negative chromatography. Possible solutions to the limitations and challenges of negative chromatography and future trends for developing negative chromatography are discussed.     

The mechanism of the steric exclusion of cells brought about by proteoglycans]

The effect of amount of rabbit erythrocytes and concentration of sodium hyaluronate and sodium salt of protein--chondroitin-keratan-sulfate were studied on aggregation of erythrocytes suspended in 0.15 M NaCL, pH 7.4. It was shown that the rate of steric exclusion of erythrocytes depends on relationship between amount of erythrocytes and concentrations of these proteoglycans.     

The kinetics of aggregation of poly-glutamic acid based polypeptides

The aggregation of two negatively-charged polypeptides, poly-L-glutamic acid (PE) and a copolymer of poly-glutamic acid and poly-alanine (PEA), has been studied at different peptide and salt concentrations and solution pH conditions. The kinetics of aggregation were based on Thioflavin T (ThT) fluorescence measurements. The observed lag phase shortened and the aggregation was faster as the pH approached the polypeptides' isoelectric points. While the initial polypeptide structures of PE and PEA appeared identical as determined from circular dichroism spectroscopy, the final aggregate morphology differed; PE assumed large twisted lamellar structures and the PEA formed typical amyloid-like fibrils, although both contained extensive beta-sheet structure. Differences in aggregation behavior were observed for the two polypeptides as a function of salt concentration; aggregation progressed more slowly for PE and more quickly for PEA with increasing salt concentration. Several models of aggregation kinetics were fit to the data. No model yielded consistent rate constants or a critical nucleus size. A modified nucleated polymerization model was developed based on that of Powers and Powers [E.T. Powers, D.L. Powers, The kinetics of nucleated polymerizations at high concentrations: Amyloid fibril formation near and above the "supercritical concentration", Biophys. J. 91 (2006) 122-132], which incorporated the ability of oligomeric species to interact. This provided a best fit to the experimental data.     

Modulation of the interactions of isolated ryanodine receptors of rabbit skeletal muscle by Na+ and K+

Ryanodine receptors (RyRs) of skeletal muscle, as calcium release channels, have been found to form semicrystalline arrays in the membrane of sarcoplasmic reticulum. Recently, both experimental observations and theoretical simulations suggested cooperative coupling within interlocking RyRs. To better understand the interactions between RyRs and their modulation, the aggregation and dissociation of isolated RyRs in aqueous medium containing various Na(+) and K(+) concentrations were investigated using photon correlation spectroscopy (PCS) and atomic force microscopy (AFM). RyRs aggregated readily at low salt concentrations. However, a different behavior was observed in the presence of Na(+) or K(+). Detectable aggregates were formed in 5 microg/mL RyR sample when the concentration of Na(+) and K(+) was reduced from 1 M to below 0.28 and 0.23 M, respectively. The dissociation of RyR aggregates was also examined when raising the salt concentration. While aggregates formed in 0.15 M NaCl medium could reverse almost completely, those formed in 0.15 M KCl medium only dissolved partly. When keeping the total salt concentration at 0.15 M, the aggregation and dissociation of RyRs were seen to evidently depend on the relative concentration of Na(+) and K(+). The interaction between RyRs was strengthened with increasing Na(+)/K(+) ratios in the mixed medium. Accompanying this, a decrease of [(3)H]ryanodine binding occurred. The results obtained with PCS and AFM provide further evidence for the interaction between RyRs and suggest the importance of Na(+), K(+), and their relative composition in modulating the interaction and cooperation between RyRs in vivo.     

Heparin and Concanavalin A interaction: isolation of fraction with higher anticoagulant activity

Heparin and Concanavalin A complexes were studied under different conditions. Interaction was measured by reading the turbidity at 420 nm. The influence of the pH, heparin, and salt concentration was measured. In the presence of salts pH was very critical, and above pH 5.4 the interaction was practically negligible. At pH 4.6 or 5.2 and the lowest salt concentration compatible with buffering, heparin fractions with different anticoagulant specific activities were detected in the precipitate and in the supernatant, after the interaction. In all cases a significative difference was observed in favor of the heparin isolated from the precipitate. Possibility of an artifact was eliminated by using adequate blanks and running the coagulation tests in the presence of an excess of Concanavalin A.     

Hydrophobic interaction chromatography in alkaline pH

Hydrophobic interaction chromatography is a very powerful protein purification technique which is dependent on strong salting-out salts to increase the hydrophobic interactions between the protein and the ligand. Ammonium sulfate is the salt most commonly used for this purpose, but it cannot be used at very alkaline pH. Monosodium glutamate was therefore tested as a salt for hydrophobic interaction chromatography at pH 9.5. When ribonuclease A, ovalbumin, and beta-lactoglobulin were individually applied to a phenyl superose column in 2 M monosodium glutamate, all three proteins bound to the column and could be subsequently eluted by decreasing the salt concentration. Using this salt, it was possible to separate commercially obtained beta-lactoglobulin into authentic protein and contaminants and to purify the individual proteins from a mixture of ovalbumin and beta-lactoglobulin. These results demonstrate that monosodium glutamate is a useful salt for hydrophobic interaction chromatography. Guanidine and sodium sulfate and sodium aspartate were also examined at the same pH, demonstrating that they also resulted in the binding and elution of the proteins examined.