Hydrational and intrinsic compressibilities of globular proteins

Partial compressibilities of globular proteins in water are reviewed. Contribution of hydrational and of intrinsic compressibilities to experimental partial quantity have been evaluated from ultrasonic data using two independent methods: (a) additive calculation of the hydrational contributions of the surface atomic groups and (b) an analysis of correlation between partial compressibility and molecular surface area. The value (14 ± 3) × 10^?6 bar ^?1 for the isothermal compressibility coefficient of the protein interior at 25°C was obtained as an average value for variety of globular proteins. This value is similar to that of solid organic polymers. Possible relaxation contribution to partial compressibility is roughly estimated from comparison of thermodynamic with x-ray data on protein compressibility. The average compressibility of water in the hydration shell of proteins was found to be 35 × 10^?6 bar ^?1, which is 20% less than that of pure water. © 1993 John Wiley & Sons, Inc.     

Über die Adsorption von DNS in der Grenzfläche Quecksilber–Elektrolyt

The adsorption of deoxyribonucleic acid (DNA) in the mercury–electrolyte interface has been investigated. The effect of this adsorption on the differential capacity of the electrical double layer between a polarized mercury surface and an 0.15M NaCl solution containing DNA was measured by means of the alternating current polarography (Breyer polarography). The effective alternating current ? under actual conditions (adsorption processes only, small electrolytic resistance, small alternating current frequency, and alternating current amplitude) is directly proportional to the differential double layer capacity. The combination of this method with the application of a stationary mercury drop electrode allows the coverage of the electrode to be followed, continuously in the range 0.2 sec, to about 60 sec. The diffusion is the rate-controlled step of the adsorption kinetics. Therefore the lowering of the alternating current ? by the adsorbed DNA is proportional to the surface concentration for partly covered surface and reaches a constant value after the surface becomes fully covered. Adsorption of further layers does not affect the differential capacity. This makes it possible to determine the maximum surface concentration of the DNA. For that it is necessary to determine the diffusion coefficient of DNA. This was done directly by Strassburger and Reinert in our institute. The surface concentrations of the native DNA and the relative surface concentrations of the denatured DNA in dependence on the potential of the polarized mercury surface was estimated. Both surface concentrations show a pronounced dependence on the potential with a minimum of the surface concentration around ?0.4 V with respect to the normal calomel electrode. This property may be caused by the structure of the adsorption layer depending on the potential. That means that only several segments at the rigid DNA molecules are adsorbed and the other ones remain in the solution near the surface. The adsorption in the neighborhood of the electrocapillary zero potential at ?0.4 V is strongest, and therefore the fraction of the adsorbed segments has a maximum. At these potentials consequently the maximum coverage is already reached at relatively low surface concentrations. Opposite to this is Miller's hypothesis, that native DNA preserves its double helical structure when adsorbed on a negatively charged mercury surface, whereas unfolding occurs on a positively charged mercury surface. Miller's hypothesis is supported by facts that the surface concentration of the denatured DNA should be independent of the potential and should be equal to the surface concentration of the native DNA at a positively charged mercury surface. But an evaluation of Miller's diagrams by no means gives an independence on the potential of the surface concentration of the denatured DNA and no accordance between the surface concentrations of denatured and of native DNA's at the positively charged mercury surface. Moreover Miller compared different DNA samples with different moleculer weights and possibly with different molecular weight distributions. Both the molecular weight and the molecular weight distribution have a pronounced influence on the surface concentration. Therefore this accordance mentioned above is not evident. The critical inspection of Miller's work and the own investigation lead to the conclusion that an unfolding or denaturation of native DNA does not take place in the mercury–electrolyte interface.     

Potential and structure controlled interfacial behavior of uracil derivatives

The adsorption and related interfacial behavior of uracil, various methylated uracil derivatives, uridine, uridine-5'-monophosphate and uridine-3'5'-cyclic monophosphate has been studied by surface electrochemical measurements at a mercury electrode. All uracil derivatives exhibit an initial "dilute" adsorption region where the virtually flat uracil residue is absorbed flat on the electrode surface. In the case of uracil and its methylated derivatives the area occupied by one molecule is about 60-70 A2. Uracil, thymine and 1,5-dimethyluracil exhibit a second adsorption region where they rearrange on the surface and adopt a perpendicular orientation and occupy about 40 A2 per molecule. In this perpendicular orientation the uracils are bound to the electrode through the N(3)-H or perhaps N(1)-H functions in a manner similar to their Watson-Crick bonding in nucleic acids. When in the perpendicular orientation the adsorbed molecules undergo extensive stacking (association) interactions, again similar to those observed between adjacent bases in nucleic acids. The ability of a uracil derivative to undergo a surface reorientation is critically dependent on electrode potential, bulk-solution concentration and molecular structure.     

Functional Tat transport of unstructured, small, hydrophilic proteins

The twin-arginine translocation (Tat) system is a protein translocation system that is adapted to the translocation of folded proteins across biological membranes. An understanding of the folding requirements for Tat substrates is of fundamental importance for the elucidation of the transport mechanism. We now demonstrate for the first time Tat transport for fully unstructured proteins, using signal sequence fusions to naturally unfolded FG repeats from the yeast Nsp1p nuclear pore protein. The transport of unfolded proteins becomes less efficient with increasing size, consistent with only a single interaction between the system and the substrate. Strikingly, the introduction of six residues from the hydrophobic core of a globular protein completely blocked translocation. Physiological data suggest that hydrophobic surface patches abort transport at a late stage, most likely by membrane interactions during transport. This study thus explains the observed restriction of the Tat system to folded globular proteins on a molecular level.     

Adsorption of bacteriophage on bacterial surface and on the surface of Hg dropping electrode

Summary The influence of the ionic strength of the medium on the adsorption of bacteriophage T 2 to the surfaces of a mercury dropping electrode on one hand and ofbacteria E. coli B on the other hand was studied. The adsorption on the mercury surface was determined by measurement of the differential capacity of the electrode double layer, the adsorption to bacteria was estimated from the decrease of free phage particles in a bacterial suspension with time. The adsorption to the mercury electrode increases with increasing ionic strength of the medium, but adsorption to the surface of bacteria increases at first, has a maximum at concentrations between 0,1 to 0,5 M and decreases with further increase of ionic strength. The decrease of adsorption of phage to the bacterial surface is assumed to be caused by the blocking of specific sites on the bacterial surface by adsorbed ions which sterically prevent the adsorption of the phage. Such specific sites are not present on the electrode surface, therefore adsorption increases further with increasing ionic strength probably due to the neutralization of surface charges of the phage and of the electrode. The saturated surface-concentration of the phage _s was calculated from the dependence of the differential capacity on the concentration. It is concluded from _s value obtained that the phage particles are scattered with wide intervals on the electrode surface with a degree of coverage of approximately 140.Abbreviations used DNA deoxyribonucleic acid - N Avogadro number The authors wishes to express their gratitude to the late Prof.Ferdinand Hercík, director of the Institute of Biophysics, for the initiation of this work and stimulating interest. The authors are also indebted to Dr. J.Koudelka for his kind gift of phage T 2 sample and to Dr. M.Vízdalová for her valuable comments during preparation of this article.     

Adsorption of peptide nucleic acid and DNA decamers at electrically charged surfaces.

Adsorption behavior of peptide nucleic acid (PNA) and DNA decamers (GTAGATCACT and the complementary sequence) on a mercury surface was studied by means of AC impedance measurements at a hanging mercury drop electrode. The nucleic acid was first attached to the electrode by adsorption from a 5-microliter drop of PNA (or DNA) solution, and the electrode with the adsorbed nucleic acid layer was then washed and immersed in the blank background electrolyte where the differential capacity C of the electrode double layer was measured as a function of the applied potential E. It was found that the adsorption behavior of the PNA with an electrically neutral backbone differs greatly from that of the DNA (with a negatively charged backbone), whereas the DNA-PNA hybrid shows intermediate behavior. At higher surface coverage PNA molecules associate at the surface, and the minimum value of C is shifted to negative potentials because of intermolecular interactions of PNA at the surface. Prolonged exposure of PNA to highly negative potentials does not result in PNA desorption, whereas almost all of the DNA is removed from the surface at these potentials. Adsorption of PNA decreases with increasing NaCl concentration in the range from 0 to 50 mM NaCl, in contrast to DNA, the adsorption of which increases under the same conditions.     

Molecular basis of cooperativity in protein folding IV. Core: A general cooperative folding model

The cooperative nature of the protein folding process is independent of the characteristic fold and the specific secondary structure attributes of a globular protein. A general folding/unfolding model should, therefore, be based upon structural features that transcend the peculiarities of α-helices, β-sheets, and other structural motifs found in proteins. The studies presented in this paper suggest that a single structural characteristic common to all globular proteins is essential for cooperative folding. The formation of a partly folded state from the native state results in the exposure to solvent of two distinct regions: (1) the portions of the protein that are unfolded; and (2) the “complementary surfaces,” located in the regions of the protein that remain folded. The cooperative character of the folding/unfolding transition is determined largely by the energetics of exposing complementary surface regions to the solvent. By definition, complementary regions are present only in partly folded states; they are absent from the native and unfolded states. An unfavorable free energy lowers the probability of partly folded states and increases the cooperativity of the transition. In this paper we present a mathematical formulation of this behavior and develop a general cooperative folding/unfolding model, termed the “complementary region” (CORE) model. This model successfully reproduces the main properties of folding/unfolding transitions without limiting the number of partly folded states accessible to the protein, thereby permitting a systematic examination of the structural and solvent conditions under which intermediates become populated. It is shown that the CORE model predicts two-state folding/unfolding behavior, even though the two-state character is not assumed in the model. © 1993 Wiley-Liss, Inc.     

Polarography of polynucleotides. IV. Effect of the molecular weight of poly(U) on its adsorption at a charged surface

Effects of molecular size on the adsorption properties of poly(U) were studied using alternating current polarography as a technique and a dropping mercury electrode (d.m.e.) as a model interface. The measurements were carried out on fractions (by molecular weight) of poly(U) characterized by sedimentation and viscosity measurements. The data indicate that the rate of poly(U) adsorption is controlled by diffusion. The adsorption equilibrium can be established during the drop-life at higher concentrations of poly(U) where the electrode is fully covered, while at low concentrations corresponding to the linearized isotherm, the time τ for the establishment of the adsorption equilibrium is much longer than can be obtained with d.m.e. The time τ increases with increasing chain length, n (in monomeric units). From the concentration dependence of the course of current time, I ～t, curves, or of the current values at the end of the drop life, a constant K was calculated which depends on n. In the range of molecular weights studied (25 × 10³ to 564 × 10³) the data obeys the relationship log n = a + b log K (where a and b are constants). Area, A, occupied by the monomer of an adsorbed poly(U) molecule was calculated from experimental values of K and D (diffusion coefficient). The decrease of A with increasing n was explained in terms of the looping of longer poly(U) chains out from the electrode surface.     

Molecularly imprinted cryogels for human interferon‐alpha purification from human gingival fibroblast culture

Interferons are important proteins for the immune system because of their antiviral, anti‐proliferating and immunomodulatory activities. Therapeutic value of these proteins against certain types of tumors caused interest and investigations aimed to obtain highly purified interferons. Molecular imprinting is an efficient method for purification with high selectivity, specificity and good reproducibility. In this study, we utilized advantages of molecular imprinting technique for the purification of interferon from human gingival fibroblast culture. For this purpose, interferon α‐2b imprinted poly(hydroxyethyl methacrylate) cryogel (hIFN‐α‐MIP) was prepared. Optimum adsorption conditions were determined, and maximum adsorption capacity of hIFN‐α‐MIP cryogel was found as 254.8 × 10⁴ IU/g from aqueous solution. All interferon measurements are expressed as International Unit (IU), which is a unit measurement used to quantify biologically active substances like interferon based on their biological activity or effect. Selectivity experiments were performed using competitive proteins and repeated adsorption–desorption studies showed that the adsorption capacity maintained almost at a constant value after ten cycles. For the purification of interferon from human gingival fibroblast culture, fast protein liquid chromatography was used and the specific activity of the purified interferon α‐2b on HeLa cell line was found between the values 3.45 × 10⁸ IU/mg and 3.75 × 10⁸ IU/mg. The results are promising, and the molecular imprinting technique is effective for the purification of interferon α‐2b. Copyright © 2013 John Wiley & Sons, Ltd.     

Interaction of nucleic acids with electrically charged surfaces. VII. The effect of ionic strength of neutral medium on the conformation of dna adsorbed on the mercury electrode

Triangular-wave direct current (d.c.) voltammetry at a hanging mercury drop electrode and phase-selective alternating current (a.c.) polarography at a dropping mercury electrode were used for the investigation of adsorption of double-helical (ds) DNA at mercury electrode surfaces from neutral solutions of 0.05-0.4 M HCOONH4. It was found for the potential region T (from -0.1 V up to ca. -1.0 V) that the height of voltammetric peaks of ds DNA is markedly influenced by the initial potential only at relatively low ionic strength (mu) (from 0.05 up to ca. 0.3). Also a decrease of differential capacity (measured by means of a.c. polarography) in the region T depended markedly on the electrode potential only at relatively low ionic strength. The following conclusions were made concerning the interaction of ds DNA with a mercury electrode charged to potentials of the region T in neutral medium of relatively low ionic strength mu < 0.3). (i) When ds DNA is adsorbed, a significantly higher number of DNA segments is anchored in the positively charged electrode surface than in the surface bearing a negative charge, (ii) In the region T, especially adsorbed labile regions of ds DNA are opened in the electrode surface, which are present in ds DNA already in the bulk of the solution, (iii) In the narrow region of potentials in the Vicinity of the zero charge potential a higher number of ds DNA segments can be opened, probably as a consequence of the strain which could act on the ds DNA molecule in the course of the segmental adsorption/desorption process.     

Electrocatalytic four-electron reduction of oxygen at the cytochrome c3-adsorbed electrode

The electrocatalytic activity of cytochrome c3 for the reduction of molecular oxygen was characterized from the studies of the adsorption of cytochrome c3 and the co-adsorption of cytochrome cs with cytochrome c on the mercury electrode by the a.c. polarographic technique. The adsorption of cytochrome c3 on the mercury electrode is irreversible and is diffusion-controlled. The maximum amount of cytochrome c3 absorbed was 0.92 . 10(-11) mol . cm-2 at -0.90 V. The amount of cytochrome c3 in the mixed adsorbed layer with cytochrome c was determined from the differential capacitance measurement. It was shown that the fractional coverage of cytochrome c3 can be estimated from its bulk concentration and the diffusion coefficient (1.05 . 10(-6) cm2 . s-1). Cytochrome c3 catalyzes the electrochemical reduction of molecular oxygen from the two-electron pathways via hydrogen peroxide to the four-electron pathway at the mercury electrode in neutral phosphate buffer solution. The catalytic activity varies with the bulk concentration of cytochrome c3. The highest catalytic activity for the oxygen reduction (no hydrogen peroxide formation) is attained when one-half of the mercury electrode surface is covered by cytochrome c3. The addition of cytochrome c or bovine serum albumin to the cytochrome c3 solution inhibits the catalytic activity of cytochrome c3. The reversible polarographic behavior of cytochrome c3 through the mixed adsorbed layer of cytochrome c3 and cytochrome c was also investigated.     

Compressibility of protein transitions

We review the results of compressibility studies on proteins and low molecular weight compounds that model the hydration properties of these biopolymers. In particular, we present an analysis of compressibility changes accompanying conformational transitions of globular proteins. This analysis, in conjunction with experimental compressibility data on protein transitions, were used to define the changes in the hydration properties and intrinsic packing associated with native-to-molten globule, native-to-partially unfolded, and native-to-fully unfolded transitions of globular proteins. In addition, we discuss the molecular origins of predominantly positive changes in compressibility observed for pressure-induced denaturation transitions of globular proteins. Throughout this review, we emphasize the importance of compressibility data for characterizing protein transitions, while also describing how such data can be interpreted to gain insight into role that hydration and intrinsic packing play in modulating the stability of and recognition between proteins and other biologically important compounds.     

Specific adsorption of phosphate ions on proteins evidenced by capillary electrophoresis and reversed-phase high-performance liquid chromatography

Specific adsorption of phosphate ions at pH=7.0 was studied on different proteins, either counter-ions of phosphate (lysozyme, lactoferrin) or co-ion of phosphate (α-lactalbumin). The theoretical electrophoretic mobility of globular proteins lysozyme and α-lactalbumin (apo and holo (+1 calcium per molecule) forms) was compared with those measured by capillary electrophoresis in phosphate at pH 7.0, versus the ionic strength (I) in the range 0–0.775 mol L⁻¹. The specific adsorption of phosphate ions was evidenced by difference. From the experimental charge number (Z^eff) of protein in phosphate medium, a phosphate content per protein molecule was determined at pH=7.0.

• •For lactoferrin (pI=8–9), the electrophoretic mobility (μ) was constant and negative, highlighting a charge reversal due to phosphate adsorption.
• •For α-lactalbumin (holo form) experimental μ was roughly constant and more negative than predicted. Z^eff increased continuously from −4 to −11 in the ionic strength range from 0.005 to 0.775 mol l⁻¹, respectively. Accordingly, one to six phosphates were bound per molecule, respectively.
• •For lysozyme, experimental electrophoretic mobility was positive but lower than predicted. Z^eff was only discrete values +5 for I in the range 0.001–0.020 mol l⁻¹ and about +3 in the range 0.050–0.500 mol l⁻¹, whereas the theoretical Z value was +7 at pH=7.0. Lysozyme bounds one phosphate at low ionic strength and about two — three at higher ionic strength.

Reversed-phase HPLC confirms that adsorption of phosphate is different for the three proteins.     

Kinetics of adsorption of proteins at interfaces: role of protein conformation in diffusional adsorption

To elucidate the role of protein conformation in the kinetics of adsorption at interfaces, seven structural intermediates of bovine serum albumin were prepared and their adsorption at the air/water interface was studied. Molecular area calculations indicated two distinct molecular processes, the first being the creation of an area, delta A1, for anchoring the molecule during the initial phase of adsorption and the second being the delta A2 cleared during subsequent reorientation and rearrangement of adsorbed molecules at the interface. The delta A1 values for all the albumin intermediates were the same, indicating that the initial work pi delta A1 needed to anchor the molecule at the interface was independent of solution conformation of the protein. Unlike delta A1, delta A2 exhibited a bell-shaped relationship with the extent of refolded state of the intermediates. Calculation of diffusion coefficients indicated that greater the unfolded state of the albumin intermediate, the greater was the diffusion coefficient. It is shown that the simple diffusion theory is inadequate to explain quantitatively the kinetics of protein adsorption. Specific, conformation-dependent, solute-solvent and solute-interface interactions also seem to influence the kinetics of adsorption of proteins.     

Kinetics of adsorption of globular proteins at an air-water interface.

Adsorption of globular proteins at an air-water interface from an infinite stagnant medium was modeled as one-dimensional diffusion in a potential field. The interaction potential experienced by an adsorbing molecule consisted of contributions from electrostatic interactions, work done against the surface pressure to clear area at the interface in order to anchor the adsorbed segments, and the change in the free energy due to exposure of penetrated surface hydrophobic functional groups to air. The assumption of irreversible adsorption is employed in the present analysis. The energy barrier to adsorption, present at sufficiently large surface pressures, was found to be higher for smaller surface hydrophobicities, larger surface pressures, larger size molecules, and oblate orientation of an ellipsoidal molecule. Consequently, more adsorption occurred at larger surface hydrophobicities, smaller size molecules, and for prolate orientation of ellipsoidal molecules. The subphase concentration has been shown to be zero at short times, increasing with time at larger times, and eventually becoming close to the bulk concentration as a result of increasing energy barrier to adsorption. The predicted evolution of surface concentration with time for adsorption of lysozyme at an air-water interface agreed well with the experimental data of Graham and Phillips (1979a).     

Electrocatalytic four-electron reduction of oxygen at the cytochrome c3-adsorbed electrode

The electrocatalytic activity of cytochrome c₃ for the reduction of molecular oxygen was characterized from the studies of the adsorption of cytochrome c₃ and the co-adsorption of cytochrome c₃ with cytochrome c on the mercury electrode by the a.c. polarographic technique. The adsorption of cytochrome c₃ on the mercury electrode is irreversible and is diffusion-controlled. The maximum amount of cytochrome c₃ adsorbed was 0.92 · 10^?11 mol · cm^?2 at ?0.90 V. The amount of cytochrome c₃ in the mixed adsorbed layer with cytochrome c was determined from the differential capacitance measurement. It was shown that the fractional coverage of cytochrome c₃ can be estimated from its bulk concentration and the diffusion coefficient (1.05 · 10^?6 cm² · s^?1). Cytochrome c₃ catalyzes the electrochemical reduction of molecular oxygen from the two-electron pathways via hydrogen peroxide to the four-electron pathway at the mercury electrode in neutral phosphate buffer solution. The catalytic activity varies with the bulk concentration of cytochrome c₃. The highest catalytic activity for the oxygen reduction (no hydrogen peroxide formation) is attained when one-half of the mercury electrode surface is covered by cytochrome c₃. The addition of cytochrome c or bovine serum albumin to the cytochrome c₃ solution inhibits the catalytic activity of cytochrome c₃. The reversible polarographic behavior of cytochrome c₃ through the mixed adsorbed layer of cytochrome c₃ and cytochrome c was also investigated.     

Leaf expansion and carbon assimilation in cotton leaves grown at two photosynthetic photon flux densities

Increasing photosynthetic photon flux density (PPFD) received during development from 5.5 to 31.2 mol m^-2 d^-1 resulted in greater leaf and mesophyll cell surface areas in cotton (Gossypium hirsutum L.). The relationships between the amounts of these surface areas and potential CO₂ assimilation by these leaves were evaluated. Leaf area (epidermal surface area of one side of a leaf), mesophyll cell surface area, and net rate of CO₂ uptake (P_n) were measured from the time leaves first unfolded until P., was substantially reduced. At the higher PPFD, leaf and mesophyll surface areas increased more rapidly during expansion, and P_n per unit leaf area was greater than at the lower PPFD. Although leaves at the higher PPFD reached the maximum P., per unit mesophyll cell surface area 4 to 5 days earlier than leaves at the lower PPFD, the maxima for these P., were similar. Leaves grown at the higher PPFD had the potential to assimilate 2.2, 3.5, or 5.8 times the amount of CO₂ as leaves from the lower PPFD when P., was expressed per unit mesophyll surface, per unit leaf surface, or per whole leaf, respectively. Greater and earlier development of both P., and mesophyll cell surface area at higher PPFD apparently had a compounding effect on the potential for carbon assimilation by a leaf.     

Prediction of "hot spots" of aggregation in disease-linked polypeptides

Background  

The polypeptides involved in amyloidogenesis may be globular proteins with a defined 3D-structure or natively unfolded proteins. The first class includes polypeptides such as β2-microglobulin, lysozyme, transthyretin or the prion protein, whereas β-amyloid peptide, amylin or α-synuclein all belong to the second class. Recent studies suggest that specific regions in the proteins act as "hot spots" driving aggregation. This should be especially relevant for natively unfolded proteins or unfolded states of globular proteins as they lack significant secondary and tertiary structure and specific intra-chain interactions that can mask these aggregation-prone regions. Prediction of such sequence stretches is important since they are potential therapeutic targets.     

Strategy combining separation of isotope-labeled unfolded proteins and matrix-assisted laser desorption/ionization mass spectrometry analysis enables quantification of a wide range of serum proteins

A novel strategy for the quantitative profiling of serum proteome is described. It includes an ammonium sulfate depletion of the serum, an affordable stable isotope labeling chemistry for samples with a large amount of protein, separation of the unfolded proteins, and relative quantification by matrix-assisted laser desorption/ionization (MALDI) mass spectrometry (MS). Labeling of unfolded proteins was performed using normal (D₀) acrylamide and deuterated (D₃) acrylamide. The workflow for separating the unfolded proteins includes whole gel elution and ion exchange liquid chromatography, and it combines electrophoretic separation based on the protein molecular weight followed by chromatographic separation in the presence of 8 M urea based on protein charge. This was followed by trypsinolysis and MALDI MS analysis, leading to the quantification of a large number of serum proteins, including those with an abundance of 10^-5 less than albumin. This robust and inexpensive workflow is suitable for the quantitative profiling of protein changes in serum associated with preanalytical variables.     

Mathematical modeling of the integrated process of mercury bioremediation in the industrial bioreactor

The mathematical model of the integrated process of mercury contaminated wastewater bioremediation in a fixed-bed industrial bioreactor is presented. An activated carbon packing in the bioreactor plays the role of an adsorbent for ionic mercury and at the same time of a carrier material for immobilization of mercury-reducing bacteria. The model includes three basic stages of the bioremediation process: mass transfer in the liquid phase, adsorption of mercury onto activated carbon and ionic mercury bioreduction to Hg(0) by immobilized microorganisms. Model calculations were verified using experimental data obtained during the process of industrial wastewater bioremediation in the bioreactor of 1 m³ volume. It was found that the presented model reflects the properties of the real system quite well. Numerical simulation of the bioremediation process confirmed the experimentally observed positive effect of the integration of ionic mercury adsorption and bioreduction in one apparatus.