Kinetics of the H-ATPase in chromatophores from Rhodospirillum rubrum: Effect of the electrical transmembrane potential on the rate constants

The effect of the electrical potential on the H⁺-ATPase of Rhodospirillum rubrum is examined. It is shown that the forward reaction rate (ATP synthesis) is increased by a factor of 10 during illumination while the reversed rate is only slightly decreased. This indicates that the electrical potential across the membrane affects the rate constants mainly by increasing the forward rate constants rather than decreasing the reversed rate constants in order to go from net hydrolysis to net synthesis.     

Nucleotide exchange and control of ATPase activity in Rhodospirillum rubrum chromatophores

(1) Light-activated ‘dark’ ATPase in Rhodospirillum rubrum chromatophores is inhibited by preincubation with ADP or ATP (in the absence of Mg²⁺). I₅₀ values were 0.5 and 6 μM, respectively, after 20 s of preincubation. (2) In the absence of MgATP, the rate constant for dissociation of ADP or ATP from the inhibitory site was less than 0.2 min^?1 in deenergized membranes. Illumination in the absence of MgATP caused an increase of over 60-fold in both rate constants. (3) In some experiments hydrolysis was performed in the presence of 10 μM Mg²⁺ and 0.2 mM MgATP. Under these conditions, the ADP or ATP inhibition was reversed within about 20 or about 80 s, respectively, after the onset of hydrolysis. This suggests that recovery from ADP or ATP inhibition (i.e., release of tightly bound ADP or ATP) in the dark is induced by MgATP binding to a second nucleotide-binding site on the enzyme. (4) Results obtained with variable concentrations of uncoupler suggest that in the absence of bound Mg²⁺ (see below), MgATP-induced release of tightly bound ADP or ATP does not require a transmembrane . This, together with the inhibitor/substrate ratios prevalent during hydrolysis, suggests that these reactivation reactions involve MgATP binding to a high-affinity binding site (Kd < 2 μM). (5) At high concentrations of uncoupler, a time-dependent inhibition of hydrolysis occurred in the control chromatophores as well as in the nucleotide-pretreated chromatophores. This deactivation was dependent on Mg²⁺. In addition, MgATP-dependent reversal of ADP inhibition in the dark was inhibited by Mg²⁺ at concentrations above 20–30 μM. By contrast, MgATP-dependent reversal of ADP inhibition occurs within 3–4 s, despite the presence of high concentrations of Mg²⁺ if the chromatophores are illuminated during contact with the nucleotides. Uncoupler abolishes the effect of illumination. A reaction scheme incorporating these findings is proposed. (6) The implications of these findings for the mechanism of lightactivation of ATP hydrolysis (Slooten, L. and Nuyten, A., (1981) Biochim. Biophys. Acta 638, 305–312) are discussed.     

Partition of polysaccharide-coated liposomes in aqueous two-phase systems

Hydrophobized polysaccharides such as cholesterol-bearing pullulan (CHP), dextran (CHD) and mannan (CHM) effectively coat the liposomal surface. Partition of the hydrophobized polysaccharide-coated liposomes in an aqueous two-phase system (PEO (top)/pullulan (bottom) or PEO (top)/dextran (bottom)) was investigated (PEO = poly(ethylene oxide)). Conventional liposomes without a polysaccharide coat mostly locate at the interface between the two polymer phases. The polysaccharide-coated liposomes, on the other hand, were partly partitioned to the bottom polysaccharide phase depending on the structure of the hydrophobized polysaccharide on the liposomal surface. The affinity between the polysaccharide on the liposomal surface and that in the bulk bottom phase controls the efficiency of partition. The sequence of interaction strength between the two carbohydrates as the following: for the PEO/dextran two-phase system, dextran_(liposome)-dextran_(bulk) > mannan_(liposome)-dextran_(bulk) > pullulan_(liposome)-dextran_(bulk); while for the PEO/pullulan system, the sequence of interaction strength was pullulan_(liposome)-pullulan_(bulk) > dextran_(liposome)-pullulan_(bulk) ≈ mannan_(liposome)-pullulan_(bulk).     

两相法分离纯化橡胶树树皮质膜

橡胶树树皮质膜H~+-ATPase在橡胶树产排胶过程中扮演着重要角色,制备高纯度及高活性的质膜是研究质膜H~+-ATPase特性和功能的必要条件。该研究以一年生巴西橡胶树(Hevea brasiliensis)树皮为材料,利用差速离心法获得粗膜微粒体,通过两相分配法分离纯化质膜,并研究两相体系中不同浓度聚合物(5.9%、6.1%、6.3%、6.5%、6.7%,W/W)和KCl(2、5、8、11、14 mmol·L~(-1))对质膜蛋白得率和纯化效率的影响。通过Bradford法对质膜蛋白得率进行检测,同时采用酶活性检测法对质膜纯度进行检测,分析结果表明选用6.4%(W/W)聚合物浓度和5mmol·L~(-1)KCl组成的两相体系可获得较高纯度和得率的橡胶树树皮质膜。通过电镜观察法在形态学上对质膜纯度进一步评价,利用铅铀能侵染全部膜组分使其染色,而磷钨酸只能专一性地侵染质膜并使其染色这一特性,分别使用铅铀和磷钨酸对切片进行染色,并通过透射电镜对切片染色程度进行直接观察,结果表明提取的粗膜微粒体中质膜组分较少,存在大量的细胞器膜污染,而纯化后的质膜膜组分较单一,其他膜组分污染较少,而且质膜大小较均一,可以用于进行后续橡胶树树皮质膜H~+-ATPase特性和功能的研究。     

Dissociation and isolation of chromatin proteins in salt solutions by an aqueous two-phase system

An aqueous two-phase system containing 7% Dextran T 500-5% polyethylene glycol (PEG) 6000 has been adopted for rapid selective stepwise extractions of high-mobility-group proteins and histones from both isolated chromatin and intact nuclei of calf thymus. After the dissociated proteins in the PEG phase were precipitated with 20% trichloroacetic acid at 4 degrees C, proteins were recovered from this phase by solubilization of PEG with acidified acetone at room temperature. This method allows preparation of nuclei depleted of histone H1.     

Extraction of peptide tagged cutinase in detergent-based aqueous two-phase systems

Detergent-based aqueous two-phase systems have the advantage to require only one auxiliary chemical to induce phase separation above the cloud point. In a systematic study the efficiency of tryptophan-rich peptide tags was investigated to enhance the partitioning of an enzyme to the detergent-rich phase using cutinase as an example. Up to 90% enzyme activity could be extracted in a single step from whole broth of recombinant Saccharomyces cerevisiae expressing cutinase variants carrying a (WP)₄ tag. In contrast, the extraction yield of wild type cutinase was 2–3% only. The detergent concentration and the temperature are the main parameters to optimize the extraction yield. Considering availability, extraction yields, and price the detergent Agrimul NRE 1205 served best for enzyme recovery.     

Simultaneous biosynthesis and purification of two extracellular Bacillus hydrolases in aqueous two-phase systems

Thermostable a-amylase with temperature optimum at 80 °C, molecular mass 58 kDa and pI point 6.9 was purified from a catabolite resistant Bacillus licheniformis strain. The enzyme was sensitive to inhibition by metal ions and N-bromosuccinimide. The partition behaviour of this enzyme in aqueous two-phase systems (ATPS) of the polymer-polymer-water type was investigated and some effects of type, molecular weight and concentration of phase components were studied. Up to 100% retention in the bottom phase of polyethylene glycol 10,000—20,000/dextran 200 system was reached. Best partition conditions were obtained in PEG 10,000—20,000/polyvinyl alcohol 200 systems, where the partition coefficient K increased 750 times to 7.5. Simultaneous production and purification of a-amylase and serine proteinase in PEG-polymer-water ATPS were examined. In the system PEG 6,000/ficoll, up to 90% of the amylase was retained in the bottom phase, whereas about 95% of the total protein (K = 22.8) and 60—75% of the proteinase were in the top phase. Similar separation of the enzymes from laboratory supernatant was obtained in system PEG/Na₂SO₄.     

Purification of lipase derived from Burkholderia pseudomallei with alcohol/salt-based aqueous two-phase systems

Alcohol/salt-based aqueous two-phase systems (ATPSs) were used to recover lipase derived from Burkholderia pseudomallei (B. pseudomallei). Nine biphasic systems, comprised of an alcohol-based top phase (ethanol, 2-propanol and 1-propanol) and a salt-based bottom phase (ammonium sulfate, potassium phosphate and sodium citrate), were evaluated for their effectiveness in lipase recovery. The stability of lipase in each of the solutions was tested, and phase diagrams were constructed for each system. The optimum partition efficiency for the purification of lipase was obtained in an ATPS of 16% (w/w) 2-propanol and 16% (w/w) phosphate in the presence of 4.5% (w/v) NaCl. The purified lipase had a purification factor of 13.5 and a yield of 99%.     

Photooxidase activity of Rhodospirillum rubrum chromatophores and reaction center complexes. The role of non-cyclic electron transfer in generation of the membrane potential

The mechanism of light-induced O₂ uptake by chromatophores and isolated P-870 reaction center complexes from Rhodospirillum rubrum has been investigated.The process is inhibited by o-phenanthroline and also by an extraction of loosely bound quinones from chromatophores. Vitamin K-3 restored the o-phenanthroline-sensitive light-induced O₂ uptake by the extracted chromatophores and stimulated the O₂ uptake by the reaction center complexes. It is believed that photooxidase activity of native chromatophores is due to an interaction of loosely bound photoreduced ubiquinone with O₂. Another component distinguishable from the loosely bound ubiquinone is also oxidized by O₂ upon the addition of detergents (lauryldimethylamine oxide or Triton X-100) to the illuminated reaction center complexes and to the extracted or native chromatophores treated by o-phenanthroline. Two types of photooxidase activity are distinguished by their dependence on pH.The oxidation of chromatophore redox chain components due to photooxidase activity as well as the over-reduction of these components in chromatophores, incubated with 2,3,5,6-tetramethyl-p-phenylenediamine (Me₄Ph(NH₂)₂) or N,N,N′,N′-tetramethyl-p-phenylenediamine (TMPD) (plus ascorbate) in the absence of exogenous electron acceptors, leads to an inhibition of the membrane potential generation, as measured by the light-induced uptake of penetrating phenyldicarbaundecaborane anions (PCB^?) and tetraphenylborate anions. The inhibition of the penetrating anion responses observed under reducing conditions is removed by oxygen, 1,4-naphthoquinone, fumarate, vitamin K-3 and methylviologen, but not by NAD⁺ or benzylviologen. Since methylviologen does not act as an electron acceptor with the extracted chromatophores, it is believed that this compound, together with fumarate and O₂, gains electrons at the level of the loosely bound ubiquinone. Data on the relationship between photooxidase activity and membrane potential generation by the chromatophores show that non-cyclic electron transfer from reduced Me₄Ph(NH₂)₂ to the exogenous acceptors is an electrogenic process, whereas non-cyclic electron transfer from reduced TMPD is non-electrogenic.Being oxidized, Me₄Ph(NH₂)₂ and TMPD are capable of the shunting of the cyclic redox chain of the chromatophores. Experiments with extracted chromatophores show that the mechanisms of the shunting by Me₄Ph(NH₂)₂ and TMPD are different.     

Continuous purification of antibodies from cell culture supernatant with aqueous two-phase systems: From concept to process

An aqueous two-phase extraction (ATPE) process based on a PEG/phosphate system was developed for the capture of human immunoglobulin G and successfully applied to a Chinese hamster ovary and a PER.C6® cell supernatant. A continuous ATPE process incorporating three different steps (extraction, back-extraction, and washing) was set up and validated in a pump mixer-settler battery. Most of the higher molecular weight cell supernatant impurities were removed during the extraction step, while most of the lower molecular weight impurities were removed during the subsequent steps. A global recovery yield of 80% and a final protein purity of more than 99% were obtained for the IgG purification from a CHO cell supernatant, representing a 155-fold reduction in the protein/IgG ratio. For the purification of IgG from a PER.C6® cell supernatant, a global recovery yield of 100%, and a host cell protein purity were attained, representing a 22-fold reduction in the host cell protein/IgG ratio. These results, thus, open promising perspectives for the application of the developed ATPE process as a platform for the capture of antibodies. In fact, this new process has shown the ability to successfully recover and purify different antibodies from distinct cell culture supernatants. This technology can also overcome some of the limitations encountered using the typical chromatographic processes, besides inherent advantages of scalability, process integration, capability of continuous operation, and economic feasibility.     

Optimization of bovine serum albumin partition coefficient in aqueous two-phase systems

Partitioning of proteins in aqueous two-phase systems has been shown to provide a powerful method for separating and purifying mixtures of biomolecules by extraction. These systems are composed of aqueous solutions of either two water-soluble polymers, usually polyethylene glycol (PEG) and dextran (Dx), or a polymer and a salt, usually PEG and phosphate or sulfate. There are many factors which influence the partition coefficient K, the ratio of biomolecule concentration in the top phase to that in the bottom phase, in aqueous two-phase systems. The value of the partition coefficient relies on the physico-chemical properties of the target biomolecule and other molecules and their interactions with those of the chosen system. In this work, the partition behavior of pure bovine serum albumin in aqueous two-phase systems was investigated in order to see the effects of changes in phase properties on the partition coefficient K. The concentration of NaCl and pH were considered to be the factors having influence on K. Optimal conditions of these factors were obtained using the Box-Wilson experimental design. The optimum value of K was found as 0.0126 when NaCl concentration and pH were 0.14 M and 9.8, respectively, for a phase system composed of 8% (w/w) polyethylene glycol 3,350 - 9 (% w/w) dextran 37,500 - 0.05 M phosphate at 20 °C.     

Improved method for isolation of plasma membrane on cationic beads. Membranes from Dictyostelium discoideum

The plasma membrane from Dictyostelium discoideum was routinely purified 35-fold by an improved technique using beads coated with positively charged polymers. Cells were attached to the beads and bare regions between the cells were neutralized with a polyanion. The neutralization decreased contamination of the bare regions by intracellular proteins released when cells were disrupted to leave behind beads coated by plasma membrane. The neutralization increased the purification as measured by membrane-bound ¹²⁵I-labeled concanavalin A. Contamination by markers for various intracellular components was markedly decreased. Various bare-site neutralization reagents were evaluated and gave different results depending upon their charge density and molecular weight. The pH of the neutralization was critical. The optimum pH for cell attachment to beads, 5.0, had little effect as regards bare-site neutralization. A new procedure is given that optimizes the essential features for the plasma membrane isolation on beads.     

Partitioning of recombinant human granulocyte-macrophage colony stimulating factor (hGM-CSF) from plant cell suspension culture in PEG/sodium phosphate aqueous two-phase systems

Partitioning of human granulocyte-macrophage colony stimulating factor (hGM-CSF) was achieved in the aqueous two-phase systems (ATPSs) using a crude extract of transgenic tobacco cell suspension culture. This study examined the effects of polyethylene glycol (PEG) molecular weight and concentration and the effects of sodium phosphate concentration in different PEG/sodium phosphate systems on the partition coefficient,K. The best ATPS system was 5% PEG 8,000/1.6 M sodium phosphate after 2 h of incubation at room temperature. In this system, hGM-CSF was partitioned in the PEG-rich phase with a yield of 57.99% andK _hGM-CSF of 8.12. In another system, 3% PEG 10,000/1.6 M sodium phosphate, hGM-CSF was also partitioned primarily in the top phase with a yield of 45.66% andK _hGM-CSF of 7.64 after 2 h of incubation at room temperature.     

Extraction of β-galactosidase fused protein a in aqueous two-phase systems

A method for the purification of proteins hybridized with β-galactosidase and produced in Escherichia coli is suggested. The method is based on the dominating properties of the β-galactosidase part of the molecule that are utilized for extraction in a poly(ethylene glycol) 4000/potassium phosphate aqueous two-phase system. The purification of the hybrid protein Staphylococcal protein A-Escherichia coli-β-galactosidase (SpA-βgal) produced in Escherichia coli is described. The partitioning of the cell debris and SpA-βgal depended on the distance to the critical point, i.e., the length of the tie line. A poly(ethylene glycol) top phase and an interface free from cell debris were obtained for a composition close to the binodial with a relatively short tie line. At this composition no Spa-βgal partitioned to the interface. When the length of the tie line was increased, more of the SpA-βgal was caught by the interface. The partitioning of SpA-βgal to the top phase was also affected by the salts present during the extraction. The utilization of SpA-βgal for affinity extraction has been investigated. Experiments with SpA-βgal and fluorescence-labeled human IgG(hIgG-F) in a poly(ethylene glycol) 4000/potassium phosphate aqueous two-phase system showed that the complex SpA-βgal-hlgG-F was partitioned to the interface, probably as a precipitate.     

Trapping, loss and annihilation of excitations in a photosynthetic system: II. Experiments with the purple bacteria Rhodospirillum rubrum and Rhodopseudomonas capsulata

In this paper a number of experiments with the purple bacteria Rhodospirillum rubrum and Rhodopseudomonas capsulata is described in which the total fluorescence yield and/or the total fraction of reaction centers closed after a picosecond laser pulse were measured as a function of the pulse intensity. The conditions were such that the reaction centers were either all in the open or all in the closed state before the pulse arrived. These experiments are analysed using the theoretical formalism discussed in the preceding paper (Den Hollander, W.T.F., Bakker J.G.C., and Van Grondelle, R., Biochim. Biophys. Acta 725, 492–507). From the experimental results the number of connected photosynthetic units, λ, the rate of energy transfer between neighboring antenna molecules, k_h, and the rate of trapping by an open reaction center, k^o_t, can be estimated. For R. rubrum it is found that λ = 14−17, k_h = (1−2)·10¹² s⁻¹ and k^o_t = (4−6)·10¹¹ s⁻¹, for Rps. capsulata λ ≈ 30, k_h ≈ 4·10¹¹ s⁻¹ and k^o_t ≈ 3·10¹¹ s⁻¹. The findings are discussed in terms of current models for the structure of the antenna and the kinetic properties of the decay processes occurring in these purple bacteria.     

Effect of salts and surfactants on the partitioning of Fusarium solani pisi cutinase in aqueous two-phase systems of thermoseparating ethylene oxide/propylene oxide random copolymer and hydroxypropyl starch

An aqueous two-phase system composed by a thermoseparating random copolymer of ethylene oxide/propylene oxide 50/50 (%w/w), Breox, and hydroxypropyl starch – Reppal PES 100 was evaluated for the partitioning of Fusarium solani pisi recombinant cutinase. The effect of several additives on the partitioning of pure cutinase was evaluated. Micelles of sodium dodecanoate provided a ten-fold increase of the partitioning coefficient (K=9) and recovery yields of 60-75%. The phase diagrams of the systems composed of Breox, Reppal and sodium dodecanoate were determined and it was found that in systems with high surfactant concentrations, the binodal was moved to lower polymer concentrations, enabling a two-phase system with 6% (w/w) of each polymer.     

On the use of mild hydrophobic interaction chromatography for "method scouting" protein purification strategies in aqueous two-phase systems: a study using model proteins

The behavior of a series of pure proteins partitioned in aqueous two-phase systems is compared with their behavior during mild hydrophobic interaction chromatography (HIC). A simple theoretical rationale for this comparison is presented based upon solvophobic theory. Similarities were found in the behavior of the model proteins in the two forms of partition chromatography. This indicates that HIC may be employed as a rapid instrumental technique for the broad characterization of protein behavior, which may be of benefit in the development of liquid-liquid partitioning strategies. However, it has proved difficult to completely account for this behavior on the basis of the known physical and structural properties of the proteins used. The variety in the detailed partitioning behavior of this small sample of protein types suggests that partition in aqueous two-phase systems is uniquely sensitive to subtle differences in surface properties of complex macromolecules. (c) 1994 John Wiley & Sons, Inc.     

Continuous extraction of β-d-galactosidase from Escherichia coli in an aqueous two-phase system: effects of biomass concentration on partitioning and mass transfer

High concentrations of Escherichia coli disintegrate move the binodial of a poly(ethylene glycol) (PEG) 4000/potassium phosphate aqueous two-phase system towards lower concentrations. It has also been shown that the yield and purification factor of β-d-galactosidase (β-d-galactoside galactohydrolase, EC 3.2.1.23) in the PEG phase was gradually improved by moving the experimental system to a composition closer to the binodial. The mass transfer rates of cell debris, total protein, β-d-galactosidase and DNA have been studied and were found to be fast enough to reach equilibrium between the phases after 1.9 s of mixing in a static mixer with 24 mixing elements. A continuous extraction process for β-d-galactosidase from E. coli has been designed on the basis of these studies with a mean residence time of 6.3 min from the disintegrator inlet to the β-d-galactosidase containing PEG-phase outlet of the centrifuge. This PEG phase contained 83.5% of the total β-d-galactosidase with a purification factor of 13.6, and only 2.8% of the total protease activity of the disintegrate. All cell debris and almost all DNA were confined to the potassium phosphate phase.     

Magnetic field-stimulated luminescence and a matrix model for energy transfer. A new method for determining the redox state of the first quinone acceptor in the reaction center of whole cells of Rhodospirillum rubrum

In whole cells of Rhodospirillum rubrum the light-induced absorbance difference spectrum of the reduction of the first quinone electron acceptor Q₁ was determined in order to relate the emission yield ф and the magnetic field-induced emission increase Δф to the redox state of Q₁. It was found that Δф/ф² is a linear function of the number of reaction centers, in which Q₁ is reduced, independent of the fraction of reaction centers in the oxidized state. The emission yield is a hyperbolic function of the fraction of reaction centers closed, either by reduction of the acceptor Q₁ or by oxidation of the primary electron donor P. Apparently, in whole cells of R. rubrum a matrix model for energy transfer between various photosynthetic units can be applied. A model is presented, which is a generalization of theoretical considerations reported before (Duysens, L.N.M. (1978) in Chlorophyll Organization and Energy Transfer in Photosynthesis, Ciba Found. Symp. 61 (New Series), pp. 323–340, Elsevier/North-Holland, Amsterdam) and which is in excellent agreement with the experiments. From simultaneous measurements of Δф and ф the redox state of the reaction center can relatively easily be determined. So far, this is the only method for simultaneously measuring the fractions P⁺ and Q⁻₁ in intact cells under steady-state conditions.     

A Process for large-scale isolation of beta-galactosidase from E. coli in an aqueous two-phase system

A method suitable for large-scale isolation of beta-galactosidase from a suspension of disintegrated E. coli cells has been developed. In an aqueous two-phase system consiting of PEG 6000 and potassium phosphate, all cell debris and the major part of the proteins and nucleic acids were partitioned to the denser salt phase. Seventy-five percent of the beta-galactosidase was recovered in the lighter PEG phase, giving a purification ratio of about 12.