A method for the determination of estrogen receptor concentration in calf uterus and other tissues using an aqueous two-phase system

An assay for the cytoplasmic estrogen receptor in calf, human and rat uterus has been developed. The method is based on partial separation of free and bound estradiol (E2) by means of an aqueous two-phase system containing dextran and poly(ethylene glycol), respectively, in the two phases. Low-speed supernatant from uterus homogenate is equilibrated with E2 and [3H]E2. A two-phase mixture is then added and bound E2 will partition into the lower phase while free E2 is distributed in both phases according to its partition coefficient. The amounts of bound and free E2 are calculated and the receptor concentration and association constant are obtained from a Scatchard plot. No dissociation of bound E2 in the phase system could be demonstrated at 4 degrees C. The interassay coefficient of variation for receptor concentration at 4 degrees C was 20 and 14% for calf and human uterus, respectively. The intraassay variation for receptor concentration in calf uterus determined at 4 degrees C and 23 degrees C was 7.1 and 4.1%, respectively. The influence of freezing the tissue and supernatant preparation was examined and results from supernatant preparations obtained with different centrifugations were compared. The method is simple and rapid, permitting large numbers of samples to be handled efficiently by a single technician.     

Kinetics and in vitro origin of the temperature-dependent transition of the estrogen receptor monomer

Partitioning of estrogen receptors in aqueous two-phase polymer systems has provided the basis for a detailed kinetic analysis of the effects of temperature on estrogen receptor (ER) structure in vitro. Exposure to temperatures of 0-30 degrees C increased the rate of change in ER partition coefficients by up to 100-fold but did not affect the final extent of the process. The temperature-dependent change in ER partition coefficients was characterized by a linear Arrhenius plot and an activation energy of 25 kcal/mol. The rate of the temperature-dependent ER transition (28 degrees C) was found to be unaffected by greater than 50-fold changes in receptor concentration, which indicates that the temperature-dependent change in partition coefficients reflects a first-order process. The partition coefficients of heated ER were unaffected by subsequent 18-h incubations at 0 degree C, indicating that the temperature-dependent ER transition is irreversible in vitro. Direct heating of the unoccupied ER resulted in both a change in ER partition coefficients and a loss of ER binding sites. The temperature-dependent change in unoccupied ER partition coefficients was complete within 30 min at 28 degrees C and yielded a first-order rate constant that was the same as that obtained for heating the receptor-estradiol complex at 28 degrees C. In contrast, the loss of unoccupied ER binding sites that occurred during 28 degrees C incubations did not reach completion after 150 min of heating and was found to behave as a second-order process.(ABSTRACT TRUNCATED AT 250 WORDS)     

Enzymatic hydrolysis of cellulose in aqueous two-phase systems. I. Partition of cellulases from Trichoderma reesei

The partitioning of endo-beta-glucanase, exo-beta-glucanase, and beta-glucosidase from Trichoderma reesei QM 9414 in aqueous two-phase systems has been studied with the object of designing a phase system for continuous bioconversion of cellulose. The partitioning of the enzymes in two-phase systems composed of various water soluble polymeric compounds were studied. Systems based on dextran and polyethylene glycol (PEG) were optimal for one-sidedly partitioning the enzymes to the bottom phase. The influence of polymer molecular weights, polymer concentration, ionic composition of the medium, pH, temperature, and adsorption of the enzymes to cellulose on the enzyme partition coefficients (K) were studied. By combining the effects of polymer molecular weight and adsorption to cellulose, K values could be reduced for endo-beta-glucanase to 0.02 and for beta-glucosidase to 0.005 at 20 degrees C in a phase system of Dextran 40-PEG 40000 in the presence of excess cellulose, At 50 degrees C, K values were increased by a factor of two. In a phase system based on inexpensive crude dextran and PEG, the partition coefficient for endo-beta-glucanase was 0.16 and for beta-glucosidase was 0.14 at 20 degrees C with excess cellulose present.     

Partitioning of acid proteases in aqueous two-phase systems containing a charged polymer

Summary A preparation of DEAE-dextran was described, which can form an aqueous two-phase system with hydroxypropyldextran. Acid proteases showed strong partition in this system due to its large interfacial electrical potential. Partition coefficients of the enzymes changed rapidly when salts were added.     

Steroid bioconversion in a novel aqueous two-phase system

A novel aqueous two-phase system, based on polyethyleneglycol (PEG) and monosodium glutamate, was tested for the 1-dehydrogenation of hydrocortisone-based substrates. This system led to higher substrate solubilities and biocatalyst/steroid separation levels when compared with alternative systems. The addition of short-chain monohydric alcohols resulted in higher solubilities and more favourable partition coefficients for the tested substrates. Bioconversion activities in PEG/glutamate systems with 2,5% (v/v) methanol were comparable to those measured in monophasic buffer-methanol medium.     

Partition of isomeric dipeptides in poly(ethylene glycol)/magnesium sulfate aqueous two-phase systems

A series of isomeric dipeptides, i.e., those containing identical residues but in different order such as Trp-Gly versus Gly-Trp, was partitioned in a poly(ethylene glycol) (PEG)/magnesium sulfate (MgSO4) aqueous two-phase system. Dipeptides having a more hydrophobic character favored the upper (PEG) phase. Moreover, the partition coefficients for isomeric dipeptides are different, with the partition coefficients for dipeptides containing the more hydrophobic residue in the C-terminal position being, in general, greater than the partition coefficients for corresponding isomers which contain the more hydrophobic residue in the N-terminal position. These observations can be attributed to the different interactions that the isomers have with specific two-phase systems.     

Aqueous two-phase protein partitioning using textile dyes as affinity ligands.

A simple and inexpensive aqueous two-phase system for the affinity partitioning of proteins is introduced. An aqueous solution consisting of maltodextrin (M100; molecular mass, 1800) and polyvinylpyrrolidone (PVP360; molecular mass, 360,000) formed two phases at 4 degrees C when the concentration of the polymers was 22.5% (w/w) and 4.0% (w/w), respectively. When the amino derivatives of chlorotriazine textile dyes or other azo textile dyes were added to the two-phase system they partitioned asymmetrically, favoring the upper, less dense, PVP360-rich phase. The association of the textile dyes with PVP360 did not prevent them from acting as affinity ligands for proteins. Three of the dyes screened increased the partition coefficient of purified lysozyme nearly 50-fold over a control containing no dye. Parameters such as pH, ionic strength, and dye concentration modulated the affinity-partitioning effect of the system. The partition coefficient of lysozyme in an egg white protein mixture increased severalfold as the total protein content of the system approached 4% (w/w), indicating that protein concentration is also important in determining the partitioning characteristics of this two-phase system. Proteins were efficiently freed of PVP360 and textile dye by recovery in a high-salt solution when another two-phase system was formed upon the addition of a solution of concentrated potassium phosphate to the isolated upper phase of a PVP360/M100/textile dye two-phase system. The affinity-partitioning system presented here allows one to screen large numbers of potentially useful protein ligands to optimize protein separation, followed by direct scaleup to a system size determined by the user.     

Cutinase purification on poly(ethylene glycol)–hydroxypropyl starch aqueous two-phase systems

The partition behaviour of cutinase on poly(ethylene glycol) (PEG)–hydroxypropyl starch aqueous two-phase systems was characterized. The effect of molecular mass of PEG, the pH of the system and tie-line length on cutinase partition coefficient and cutinase yield to the top phase was investigated for systems prepared with a purified hydroxypropyl starch (Reppal PES 100) and a crude one (HPS). The effect of the presence of different salts, such as sodium chloride, sodium sulphate and ammonium sulphate, on cutinase partition was also studied. The results lead to the conclusion that aqueous two-phase systems composed of PEG and hydroxypropyl starch are not efficient in the purification of cutinase. In the majority of cases, the partition coefficients were very close to 1, with pH being the factor which affects most cutinase partition. Partition coefficients were significantly improved when salts were added to the systems. For PEG 4000–Reppal PES 100 [at pH 4.0; 0.5 M (NH₄)₂SO₄], the partition coefficient for cutinase was 3.7, while a value of 12 was obtained for PEG 4000–HPS (at pH 4.0; 1 M NaCl). An isoelectric point (pI) of 7.8 was confirmed for cutinase by constructing a cross partition graphic from the results obtained in the experiments with different salts.     

Understanding viral partitioning in two-phase aqueous nonionic micellar systems: 1. Role of attractive interactions between viruses and micelles

The partitioning behavior of viruses in the two-phase aqueous nonionic n-decyl tetra(ethylene oxide) (C10E4) micellar system cannot be fully explained by considering solely the repulsive, steric, excluded-volume interactions that operate between the viruses and the nonionic C10E4 micelles. Specifically, an excluded-volume theory developed recently by our group is not able to quantitatively predict the observed viral partition coefficients, even though this theory is capable of providing reasonable quantitative predictions of protein partition coefficients. To shed light on the discrepancy between the theoretically predicted and the experimentally measured viral partition coefficients, a central assumption underlying the excluded-volume theory that the viruses and the C10E4 micelles interact solely through repulsive, excluded-volume interactions was challenged in this study. In particular, utilizing bacteriophage P22 as a model virus, a competitive inhibition test and a partitioning study of the capsids of bacteriophage P22 were conducted. Based on the results of these two experimental studies, it was concluded that any attractive interactions between the tailspikes of bacteriophage P22 and the C10E4 micelles are negligible. Another experimental study was carried out wherein the partition coefficients of the model viruses, bacteriophages P22 and T4, were measured at various temperatures, and compared with those previously obtained for bacteriophage phiX174. This comparison also indicated that possible attractive, electromagnetic-induced interactions between the bacteriophage particles and the C10E4 micelles cannot be invoked to rationalize the observed discrepancy between the theoretically predicted and the experimentally measured viral partition coefficients.     

A model for the prediction of partition coefficients in aqueous two-phase systems.

A mathematical model has been developed to predict partition coefficients for aqueous two-phase systems. The model is based on a previously-developed equation for partitioning which arises from an osmotic pressure viral expansion. The model suggests that the properties of importance are the concentration difference of one of the phase-forming components, such as a polymer, and the hydrophobicity of the solute relative to the hydrophobic-hydrophilic difference between the two phases. Several two-phase systems have been studied, with a particular emphasis on the poly(ethylene glycol)/magnesium sulfate system. Numerous solutes, including peptides, were used in this system and their partition coefficients show good agreement with the model.     

Dependence of the kinetics of forming phases of a two-phase polymeric system on actin state

New analytical possibilities of biological macromolecule partition in a two-phase polymer system (dextran-500/polyethyleneglycol-6000) were investigated. The technical principles were based on the fact that optical density of the system changes during phase formation. Various actin forms were investigated. Unlike G-actin, F-actin increases the speed of phase formation. Different actin isoforms exert different influence on this process. The kinetics of the partition system into phases makes it possible to figure out the picture of native G-actin damage. The two-phase polymer system has been shown to be capable of supporting the native properties of actin for not less than 6 days at 20 degrees C. An assumption is made that two-phase systems can be used for imitating the intracellular medium in studies on actin functional characteristics.     

Partition behaviour of a cultured mouse mammary cancer cell line in aqueous two-phase polymer systems.

Cell surface-associated changes in behaviour of cultured cells on partition in an aqueous two-phase polymer system were studied using FM3A cell line (a cultured mammary cancer of mouse) with respect to aging. The aqueous polymer system consisted of dextran, polyethyleneglycol and sodium phosphate, equilibrated at 6 degrees C to separate into two phases. Enzyme treatment of cells with neuraminidase reduced cell electrophoretic mobility, as well as the cell partition ratio. Hyaluronidase produced no observable effects on partition and cell electrophoretic mobility, suggesting that the partition is related to culture time was similar for both cell electrophoretic mobility and cell partition, showing a rise and fall of charge-associated cell surface change during cell growth, the maxium occurring at the beginning of exponential growth. This change was reflected in the pattern of countercurrent distribution of the cells in respective stages of growth. Countercurrent distribution with our two-phase system is expected to be capable of fractionating cell populations according to cell surface properties.     

Glucose-6-phosphate dehydrogenase partitioning in two-phase aqueous mixed (nonionic/cationic) micellar systems

The enzyme glucose-6-phosphate dehydrogenase (G6PD) plays an important role in maintaining the level of NADPH and in producing pentose phosphates for nucleotide biosynthesis. It is also of great value as an analytical reagent, being used in various quantitative assays. In searching for new strategies to purify this enzyme, the partitioning of G6PD in two-phase aqueous mixed (nonionic/cationic) micellar systems was investigated both experimentally and theoretically. Our results indicate that the use of a two-phase aqueous mixed micellar system composed of the nonionic surfactant C(10)E(4) (n-decyl tetra(ethylene oxide)) and the cationic surfactant C(n)TAB (alkyltrimethylammonium bromide, n = 8, 10, or 12) can improve significantly the partitioning behavior of G6PD relative to that obtained in the two-phase aqueous C(10)E(4) micellar system. This improvement can be attributed to electrostatic attractions between the positively charged mixed (nonionic/cationic) micelles and the net negatively charged enzyme G6PD, resulting in the preferential partitioning of G6PD to the top, mixed micelle-rich phase of the two-phase aqueous mixed micellar systems. The effect of varying the cationic surfactant tail length (n = 8, 10, and 12) on the denaturation and partitioning behavior of G6PD in the C(10)E(4) /C(n)TAB/buffer system was investigated. It was found that C(8)TAB is the least denaturing to G6PD, followed by C(10)TAB and C(12)TAB. However, the C(10)E(4)/C(12)TAB/buffer system generated stronger electrostatic attractions with the net negatively charged enzyme G6PD than the C(10)E(4)/C(10)TAB/buffer and the C(10)E(4)/C(8)TAB/buffer systems, when using the same amount of cationic surfactant. Overall, the two-phase aqueous mixed (C(10)E(4)/C(10)TAB) micellar system yielded the highest G6PD partition coefficient of 7.7, with a G6PD yield in the top phase of 71%, providing the optimal balance between the denaturing effect and the electrostatic attractions for the three cationic surfactants examined. A recently developed theoretical framework to predict protein partition coefficients in two-phase aqueous mixed (nonionic/ionic) micellar systems was implemented, and the theoretically predicted G6PD partition coefficients were found to be in reasonable quantitative agreement with the experimentally measured ones.     

Differences in the surface properties of the mating types of Physarum polycephalum

In the slime mold Physarum polycephalum, formation of a diploid plasmodium occurs when compatible haploid amoebae fuse. To study cell surface changes associated with the fusion process, a non-destructive method known as aqueous, two-phase partitioning was employed. Using a two-phase system of dextran and polyethylene glycol, we observed that the two mating types (RSD4 and MA185) have different partition coefficients and hence different surface properties. Based on their partitioning behavior, MA185 cells appear to have a more hydrophobic surface than RSD4 amoeba. The partition coefficient of both cell types decreased with time. If amoebae were maintained in culture until they encysted, differences in their surface were not detectable.     

Protein sorption and recovery by hydrogels using principles of aqueous two-phase extraction

Use of the thermodynamic principles of aqueous two-phase extraction (ATPE) to drive protein into a crosslinked gel is developed as a protein isolation and separation technique, and as a protein loading technique for drug delivery applications. A PEG/dextran gel system was chosen as a model system because PEG/dextran systems are widely used in aqueous two-phase extraction and dextran gels (Sephadex(R)) are common chromatographic media. The effects of polymer concentrations and molecular weights, salts, and pH on the partitioning of ovalbumin matched ATPE heuristics and data trends. Gel partition coefficients (Cgel/Csolution) increased with increasing PEG molecular weight and concentration and decreasing dextran concentration (increased gel swelling). The addition of PEG to the buffer solution yielded partition coefficients more than an order of magnitude greater than those obtained in systems with buffer alone, or added salt. A combined salt/PEG system yielded an additional order of magnitude increase. For example, when ovalbumin solution (2.3 mg/mL) was equilibrated with Sephadex(R) G-50 at pH 6.75, the partition coefficients were 0.13 in buffer, 0.11 in buffer with 0.22M KI, 2.3 in 12 wt% PEG-10,000 and 32.0 in 12 wt% PEG-10, 000 with 0.22M KI. The effect of anions and cations as well as ionic strength and pH on the partitioning of ovalbumin also matched ATPE heuristics. Using the heuristics established above, partition coefficients as high as 80 for bovine serum albumin and protein recoveries over 90% were achieved. In addition, the wide range of partition coefficients that were obtained for different proteins suggests the potential of the technique for separating proteins. Also, ovalbumin sorption capacities in dextran were as high as 450 mg/g dry polymer, and the sorption isotherms were linear over a broad protein concentration range.     

Extraction of cephalosporin C from whole broth and separation of desacetyl cephalosporin C by aqueous two-phase partition

Cephalosporin C was extracted from diluted or whole broth by PEG/salt aqueous two-phase systems. Parameters such as PEG molecular weight, salt type, pH, and salt concentration were investigated for finding a suitable extraction system. In PEG 600/ammonium sulfate or phosphate systems, K(c) (partition coefficienct of cephalosporin C) was observed to be larger than 1, with K(d) (partition coefficient of desacetyl cephalosporin C) being smaller than 1. The particular values of these coefficients would imply that the difficult separation of cephalosporin C and desacetyl cephalosporin C could possibly be achieved via the aqueous two-phase extraction. The addition of surfactants, water-miscible solvents, and neutral salts for enhancement of the separation efficiency was also investigated. The addition of surfactants to the system did not affect the separation efficiency substantially. K(c) would increase whereas K(d) decreased as a result of the addition of acetone, MeOH, EtOH, IPA, and n-BuOH. Meanwhile both K(c) and K(d) would decrease whenever neutral salts, NaCl, KCl, Kl, or KSCN, were added. The partitioning behavior of cephalosporin C and desacetyl cephalosporin C in filtered, whole, and different batches of broth was notably quite similar to that of diluted broth. The recovery yield of cephalosporin C in whole broth extraction was observed to be a function of centrifugal force used in phase separation. (c) 1994 John Wiley & Sons, Inc.     

Fundamental studies of biomolecule partitioning in aqueous two-phase systems

Phase diagram data at 4 degrees C was determined for the aqueous two-phase systems composed of polyethylene glycol, dextran, and water. The Flory-Huggins theory of polymer thermodynamics was used to correlate partitioning of biomolecules in these aqueous two-phase systems resulting in a simple linear relationship between the natural logarithm of the partition coefficient and the concentration of polymers in the two phases. This relationship was verified by partitioning a series of dipeptides which differ from one another by the addition of a CH(2) group on the c-terminal amino acid residue and by utilizing a set of low-molecular-weight proteins. The slope of the line could be expressed in terms of the interactions of the biomolecule with the phase forming polymers and water. The main result for the dipeptides was that knowledge of the partition coefficient in any of the PEG/dextran/water systems, regardless of polymer molecular weight, enabled prediction of the coefficient in all of the systems. The dipeptides were also used for determination of the Gibbs free energy of transfer of a CH(2) group between the phases. This quantity was correlated with polymer concentration, thus establishing a hydrophobicity profile for the PEG/ dextran/water systems. The methodology for predicting dipeptide partition coefficients was extended to proteins, where it was found that low-molecular-weight proteins gave a linear relationship with the tie line compositions of a phase diagram.     

Temperature dependence of the partition coefficient of proteins in aqueous two-phase systems.

We report the partition coefficients of lysozyme, chymotrypsinogen-A, albumin and catalase in sixty four Polyethyleneglycol/Dextran/Water systems at 4, 25 and 40 degrees C. We found that the partition coefficients of the four proteins generally increase with increasing temperature. The influence of temperature on the partition coefficient seems to be highly dependent on the kind of protein which is partitioned and on the total polymer concentration, but does not, in general, depend on the molecular weight of the polymers. The partition coefficients of small and hydrophilic proteins like lysozyme and chymotrypsinogen-A are only slightly affected by changes in temperature, while the partition coefficients of bigger and more hydrophobic proteins like albumin and catalase are strongly affected by changes in temperature. The results suggest the incorporation of attractive forces (possible electrostatic) into a model previously reported by us.     

Ovomucoid partitioning in aqueous two-phase systems

This study evaluated the partitioning of ovomucoid from egg white, in aqueous two-phase systems (ATPS) composed of PEG 1500 and inorganic salt (lithium sulfate, sodium sulfate, magnesium sulfate, sodium carbonate or sodium citrate) at 25 °C. The results showed a great effect of the electrolyte nature on the partition coefficient. The partition coefficient value ranges from 0.02 to 6.0. The highest partition coefficients were obtained from systems composed of sodium carbonate and the lowest in systems composed of magnesium sulfate. In the system containing magnesium sulfate, a recovery percentage greater than 90% was obtained.