Modelling complexation and electrostatic attraction in heavy metal biosorption by Sargassum biomass

Biosorption, the passive accumulation of metal ions by biomass, can be used for purifying metal bearing wastewater. Seaweeds represent a readily available source of biosorbent material that possesses a high metal binding capacity. For example, Sargassum can accumulate 2 mequiv of Cd per gram of biomass i.e. 10% of its dry weight. Binding of Cd and Cu by Sargassum is an ion exchange process involving both covalent and ionic bonds. The amount of cations bound covalently or by complexation can be predicted using multi-component sorption isotherms involving 2 types of binding sites, carboxyl and sulphate. A Donnan model was used to account for the effect of ionic strength and electrostatic attraction. The use of a multi-component isotherm that included one term for Na binding was less appropriate than the Donnan model for modelling ionic strength effects. It was possible to predict metal and proton binding as a function of the pH value, metal concentration and ionic strength of the solution. This revised version was published online in June 2006 with corrections to the Cover Date.     

Performance of electron acceptors in catholyte of a two-chambered microbial fuel cell using anion exchange membrane

The performance of the cathodic electron acceptors (CEA) used in the two-chambered microbial fuel cell (MFC) was in the following order: potassium permanganate (1.11 V; 116.2 mW/m²) > potassium persulfate (1.10 V; 101.7 mW/m²) > potassium dichromate, K₂Cr₂O₇ (0.76 V; 45.9 mW/m²) > potassium ferricyanide (0.78 V; 40.6 mW/m²). Different operational parameters were considered to find out the performance of the MFC like initial pH in aqueous solutions, concentrations of the electron acceptors, phosphate buffer and aeration. Potassium persulfate was found to be more suitable out of the four electron acceptors which had a higher open circuit potential (OCP) but sustained the voltage for a much longer period than permanganate. Chemical oxygen demand (COD) reduction of 59% was achieved using 10 mM persulfate in a batch process. RALEX™ AEM-PES, an anion exchange membrane (AEM), performed better in terms of power density and OCP in comparison to Nafion®117 Cation Exchange Membrane (CEM).     

Transport of vanadium (V) in saturated porous media: effects of pH,ionic-strength and clay mineral

Vanadium, a hazardous pollutant, has been frequently detected in soil and groundwater, however, its transport behavior in porous media were not clearly understood. In this study, the effects of solution pH, ionic strength (IS) and the effect of clay mineral on the transport of vanadium in saturated porous media were investigated. Laboratory experiments using a series of columns packed with quartz sand were carried out to explore the retention and transport of vanadium with a range of ionic-strength (0.001–0.1 M) and pH (4–8) and two different types of clay minerals montmorillonite and kaolinite. Results of the breakthrough experiments showed that vanadium was highly mobile in the saturated porous media. The increase in pH rendered a higher transport of vanadium in saturated porous media. The study also indicated an easier transfer of vanadium with an increase in IS. Montmorillonite enhanced the mobility of vanadium in the column when compared to kaolinite. A mathematical model based on advection-dispersion equation coupled with equilibrium and kinetic reactions was used to describe the retention and transport of vanadium in the columns very well.     

Influence of Short-Chain Aliphatic Acids on the Phenanthrene Desorption and Mobilization from Contaminated Soil

This study was performed to investigate the influence of short-chain aliphatic acids (SCAAs) on the desorption of phenanthrene from artificially contaminated soils with this polycyclic aromatic hydrocarbon. Five SCAAs examined, including acetic acid, oxalic acid, malic acid, tartaric acid and citric acid, were related to the increase of phenanthrene desorption from two kinds of soil. Citric acid and oxalic acid enhanced phenanthrene desorption to a more significant extent than other organic acids. The effects of pH, SCAA concentration, and ionic strength were further evaluated. The phenanthrene desorption was enhanced as the pH increased. An increase in desorbed phenanthrene from pH 3 to pH 8 was observed, but that was followed by a slight decrease above pH 8 for most SCAAs. The phenanthrene desorption performance showed increments with increasing organic acid concentrations. However, the increase of phenanthrene desorption became less remarkable when SCAA concentrations were above 100 mmol/L. Moreover the results suggested that high ionic strength hindered the desorption of phenanthrene in the presence of SCAAs.     

The effects of pH and ionic strength on the partitioning of four proteins in reverse micelle systems

Four proteins with different physicochemical properties have been partitioned in reversed micelle systems: thaumatin, ribonuclease A, soybean trypsin inhibitor, and alpha-lactalbumin. The organic phase was formed by sodium salt (AOT) in isooctane, and the aqueous phase contained KCl, KBr, MgCl(2), or NaCl. Aqueous phase pH was varied between 2 and 13 and ionic strength from 0.1 to 1.0 M. Small changes in pH [around the isoelecric point (pl)] were found to influence the solubilization of ribonuclease A and trypsin inhibitor, but for thaumatin the pH change necessary to affect partition was much greater as a consequence of the difference in net charge (titration curves) of these protein molecules as pH changes. The type of ions present in the system was also a determining factor for partition; the larger ions (K(+)) produced more electrostatic screening and hence less protein solubilization than the smaller ions (Na(+)). With changes in ionic strength surface hydrophobicity was a dominant factor affecting solubilization of thaumatin in NaCl-containing systems at high pH. Charge distribution and hydrophobicity are thought to be important parameters when partitioning the protein alpha-lactalbumin. (c) 1994 John Wiley & Sons, Inc.     

Transport of natural soil nanoparticles in saturated porous media: effects of pH and ionic strength

To understand the effects of ionic strength and pH on the transport of natural soil nanoparticles (NS) in saturated porous media, aeolian sandy soil nanoparticles (AS), cultivated loessial soil nano particles (CS), manural loessial soil nanoparticles (MS) and red soil nanoparticles (RS) were leached with solutions of varying pH and ionic strength. The recovery rate of soil nanoparticles decreased in the order AS > RS > MS > CS. Transport of soil nanoparticles was enhanced with increasing pH and decreasing ionic strength and was attributable to changes in the Zeta potential of NS. Deposition of NS was also affected by the composition of soil nanoparticles and the surface charge. Column experiments showed that the interaction between soil nanoparticles and saturated quartz sand was mainly due to the physical and chemical properties of soil nanoparticles. The Derjaguin–Landau–Verwey–Overbeek interaction energies between NS and sand were affected by pHs and ionic strengths. Soil nanoparticles transport through saturated porous media could be accurately simulated by the one-dimensional advection-dispersion-reaction equation.     

Dynamic approach to predict pH profiles of biologically relevant buffers

Recently, dynamic approach has been applied to determine the steady state concentrations of multiple ionic species present in complex buffers at equilibrium. Here, we have used the dynamic approach to explicitly model the pH profiles of biologically relevant phosphate buffer and universal buffer (a mixture of three tri-protic acids such as citric acid, boric acid and phosphoric acid). The results from dynamic approach are identical to that of the conventional algebraic approach, but with an added advantage that the dynamic approach, allow for the modelling of complex buffer systems relatively easy compared to that of algebraic method.     

Characterization of glucoamylase adsorption to raw starch

The adsorption of Aspergillus niger glucoamylase forms (GA-I and GA-II) to raw corn starch was studied as a function of pH, ionic strength, and temperature. A three-parameter model was developed to account for the specific and nonspecific adsorption of GA-I to starch. The adsorption of the GA-II form to raw starch was weak and independent of the pH and ionic strength of the mixture. GA-I was bound strongly to the starch surface, with association constant values ranging from 2 to 5 × 10⁶ M⁻¹. Maximum adsorption capacities (saturation concentrations) Q_max for GA-I were affected by pH, inonic strength, and temperature and varied between 1.6 and 4.3 mg protein g⁻¹ starch. The tightly bound GA-I could be specifically eluted from the starch surface with maltose, maltodextrin, or soluble starch. The adsorption of GA-II to starch in the presence of acarbose (glucoamylase activity inhibitor) indicated that the active site participates minimally in the adsorption process. The comparison of the distribution coefficients of GA-I and GA-II showed that the starch-binding domain, present only in GA-I, increases the affinity of GA-I for starch by two orders of magnitude.     

An alternate diafiltration strategy to mitigate protein precipitation for low solubility proteins

Application of the minimum diafiltration (DF) time solution for a monoclonal antibody resulted in a 20‐h process time rather than the expected 12 h. Further investigation indicated high turbidity associated with a product solubility issue that caused a flux decline. As a result, the gel flux model and the associated minimum DF time were not predictive. Multiwell plate solubility screening confirmed that the protein passed through a region of low solubility during the ultrafiltration step. Multiple approaches to address this issue were considered and a new strategy involving variable volume diafiltration (VVDF) was developed. Process modeling and simulation were used to predict performance and to select a value of the DF ratio control parameter (buffer flow/permeate flow = 0.65). Feasibility testing at the bench and pilot scales confirmed that the new strategy reduced solubility issues, fit within existing manufacturing tank volume and system area constraints, matched model predictions, and did not present significant implementation issues. Recommendations are made regarding the general value of this strategy, when it should be used, and how to implement it. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 30:646–655, 2014     

Evaluation of Escherichia coli proteins that burden nonaffinity-based chromatography as a potential strategy for improved purification performance

Escherichia coli is a favored host for rapid, scalable expression of recombinant proteins for academic, commercial, or therapeutic use. To maximize its economic advantages, however, it must be coupled with robust downstream processes. Affinity chromatography methods are unrivaled in their selectivity, easily resolving target proteins from crude lysates, but they come with a significant cost. Reported in this study are preliminary efforts to integrate downstream separation with upstream host design by evaluating co-eluting host proteins that most severely burden two different nonaffinity-based column processes. Phosphoenolpyruvate carboxykinase and peptidase D were significant contaminants during serial purification of green fluorescent protein (GFP) by hydrophobic interaction and anion exchange chromatography. Ribosomal protein L25 dominated non-target binding of polyarginine-tagged GFP on cation exchange resin. Implications for genetic knockout or site-directed mutagenesis resulting in diminished column retention are discussed for these and other identified contaminants.     

Computation of pH evolution versus ionic products concentration in a fermentation broth

An algorithm developed for pH computation has been tested to calculate the theoretical pH changes in a culture medium during the course of a fermentation. A divergence between the computed pH value and the value measured with the electrode allows us to highlight the presence of undetected ionic products. The calculation with the algorithm by means of a computer requires only the knowledge of the ionic properties of the substrates and detected products and existing thermodynamic constants. (c) 1993 Wiley & Sons, Inc.     

Protein composition of nuclear ribonucleoprotein particles isolated from liver of rats in the early stages of feeding of 3'-methyl-4-dimethylaminoazobenzene and from hepatoma induced by the same carcinogen.

The feeding of carcinogenic 3'-methyl-4-dimethylaminoazobenzene (3'-MeDAB) in the early stages results in a change in the protein composition of the nuclear ribonucleoprotein particles of the rat liver. These particles are associated with newly synthesized RNA and it is assumed that they are involved in the processing and in the transport of this RNA. After 6 weeks of feeding of this azocarcinogen, the amount of one of the main polypeptides (apparent molecular weight 42 000) is decreased and after 10 weeks of feeding the particles are devoid of this polypeptide completely. Feeding of the non-carcinogenic p-aminoazobenzene (AB) is without any effect. The loss of this polypeptide is not characteristic for the malignant transformation. In the nuclear ribonucleoprotein particles isolated from hepatoma which has been induced by 3'-MeDAB this polypeptide is present in even higher proportion to other polypeptides than it is in particles isolated from liver cells of control animals. The 3'-MeDAB binds to the proteins of the liver nuclear ribonucleoprotein particles and interferes with the RNA processing. It is proposed that the changes in the composition of the protein moiety of the particles reflect changes in the population of liver cells leading finally to the selection of hepatoma cells which are resistant to the toxic effect of 3'-MeDAB on RNA processing.