Use of modified diatomaceous earth for removal and recovery of viruses in water.

Diatomaceous earth was modified by in situ precipitation of metallic hydroxides. Modification decreased the negative charge on the diatomaceous earth and increased its ability to adsorb viruses in water. Electrostatic interactions were more important than hydrophobic interactions in virus adsorption to modified diatomaceous earth. Filters containing diatomaceous earth modified by in situ precipitation of a combination of ferric chloride and aluminum chloride adsorbed greater than 80% of enteroviruses (poliovirus 1, echovirus 5, and coxsackievirus B5) and coliphage MS2 present in tap water at ambient pH (7.8 to 8.3), even after filtration of 100 liters of tap water. Viruses adsorbed to the filters could be recovered by mixing the modified diatomaceous earth with 3% beef extract plus 1 M NaCl (pH 9).     

Use of modified diatomaceous earth for removal and recovery of viruses in water.

Diatomaceous earth was modified by in situ precipitation of metallic hydroxides. Modification decreased the negative charge on the diatomaceous earth and increased its ability to adsorb viruses in water. Electrostatic interactions were more important than hydrophobic interactions in virus adsorption to modified diatomaceous earth. Filters containing diatomaceous earth modified by in situ precipitation of a combination of ferric chloride and aluminum chloride adsorbed greater than 80% of enteroviruses (poliovirus 1, echovirus 5, and coxsackievirus B5) and coliphage MS2 present in tap water at ambient pH (7.8 to 8.3), even after filtration of 100 liters of tap water. Viruses adsorbed to the filters could be recovered by mixing the modified diatomaceous earth with 3% beef extract plus 1 M NaCl (pH 9).     

Purification of rat renal renin from crude kidney extracts by diaminohexamethylene-Sepharose chromatography

Renin from rat kidney extracts was adsorbed to diaminohexamethylene-sepharose columns at extremely low ionic strength and neutral pH. Renin was retarded while the column was developed in 1 mM sodiumpyrophosphate and extraneous proteins were removed. Elution of renin was performed using a linear gradient of sodiumpyrophosphate, 1 – 17 mM at pH 6.8. Renin was purified in a yield up to approx. 60 per cent of the applied activity and a purification factor between 5 – 122 depending on the specific activity of the applied sample. The specific activity after this single chromatography of crude rat kidney homogenate on diaminohexamethylene-sepharose showed a median of 11.3 Goldblatt units per mg protein in a range of 5.3 – 42.0 Goldblatt units per mg protein. The renin binding capacity of the column was 1 Goldblatt unit per ml wet gel. The purified renin was subjected to G-100 Sephadex chromatography demonstrating two molecular weight forms of 44000 and 50000 dalton. Polyacrylamide gel electrophoresis demonstrated three separate fractions of renin.     

High-performance hydrophobic interaction chromatography of proteins

A new, weakly hydrophobic, high-performance liquid chromatography column has been developed for the separation of native proteins based on their relative hydrophobicities. Starting with a covalently bound, hydrophilic polyamine matrix, packing materials were synthesized through acylation with anhydrides and acid chlorides of increasing chain length to obtain increasingly hydrophobic surfaces. Proteins in aqueous buffers were induced to bind hydrophobically to the columns by the use of high salt concentrations in the mobile phase. Elution was achieved by decreasing the ionic strength of the solvent in a linear gradient. A mixture of cytochrome c, conalbumin, and beta-glucosidase was used as a standard to test the resolving power of newly synthesized columns. On a 4-cm butyrate column, baseline resolution was achieved in 20 min with a gradient of 3.0 mu sodium sulfate in 0.1 M potassium phosphate buffer, pH 7.0, to water. The static loading capacity for each column was determined using a hemoglobin binding assay. Capacities normally ranged between 150 and 180 mg of hemoglobin per gram of support. Since proteins are not denatured in hydrophobic interaction chromatography, enzymes eluted from the column retained enzymatic activity. Samples of alpha-amylase and beta-glucosidase ranging in size from 10 to 200 micrograms were recovered from the butyrate column with greater than 92% enzymatic activity in all cases. In a single trial, the enzyme citrate synthase was recovered from the benzoate column with 92% retention of enzymatic activity.     

Fibrinogen-sepharose interaction with prothrombin, prethrombin 1, prethrombin 2 and thrombin

Binding of prothrombin, prethrombin 1, prethrombin 2 and thrombin to fibrinogen-Sepharose was studied. Thrombin and prethrombin 2 bound to fibrinogen-Sepharose, while prethrombin 1 and prothrombin did not. Bound thrombin and prethrombin 2 were recovered from the column by eluting with 0.1 M NaCl/0.05 M Tris-HCl buffer (pH 7.4). The affinity of thrombin and prethrombin 2 to fibrinogen-Sepharose depended on ionic strength and reached a maximum at 50 mm concentration. Prethrombin 2 interacts with fibrinogen as well as thrombin; and prothrombin fragment 1.2 is not important in the formation of this complex. Thus, prethrombin 2, which is a precursor of thrombin without measurable enzymatic activity and which lacks the single cleavage at Arg-322-Ile-323 present in thrombin, has the same or very similar structural conformation as thrombin and has the same macromolecular substrate recognition site. These results confirm the earlier results that active center is not necessary in fibrinogen-thrombin interaction.     

Determination of heterocyclic aromatic amines (HAs) content in samples of household-prepared meat dishes

Aminoazaarene content was investigated in 10 meat samples (including pork, beef, turey and chicken) thermally processed at home according to common recipes used by residents of Upper Silesia region in Poland. The clean-up procedure included tandem solid-phase extraction (SPE) using Extrelut-type columns filled with diatomaceous earth, propylsulphonic acid and chemically bounded phase-C18. Identification and quantitative analysis of HAs fraction was carried out using a HPLC system with DAD-type detector. Separation was achieved using TSK-gel ODS 80-TM column and a mixture of 5% acetonitrile and 95% triethylamine phosphate buffer (pH 3.3) as a mobile phase. The results of qualitative determinations were confirmed by GC-MS method. To achieve this, HAs fractions were derivatized to pentafluoropropionic acid (PFPA) amide derivatives. The summary content of five aminoazaarenes determined in investigated meat samples, i.e. 2-amino-3-methylimidazo [4,5-f]quinoline (IQ), 2-amino-3,8-dimethylimidazo[4,5-f]quinoxaline (MeIQx), 2-amino-3,4-dimethylimidazo[4,5-f]quinoline (MeIQ), 2-amino-3,4,8-trimethylimidazo[4,5-f]quinoxaline (4,8-DiMeIQx), 2-amino-1-methyl-6-phenyl-imidazo[4,5-b]pyridine (PhIP) falls within the range of 1.9-77.4 ng/g of sample. The calculated values of theoretically daily human exposure to five determined HAs were in the range of 0.2-7.7 microg per day per person.     

Effect of column dimensions and flow rates on size-exclusion refolding of beta-lactamase

We have investigated the effect of changing the column diameter and length on the size exclusion chromatography (SEC) refolding of beta-lactamase from Escherichia coli-derived inclusion bodies (IBs). Inclusion bodies were recovered and solubilised in 6 M GdnHCl and 5 mM DTT. Up to 16 mg of denatured, solubilised beta-lactamase was loaded onto size exclusion columns packed with Sephacryl S-300 media (fractionation range: 10(4)-1.5 x 10(6) Da). beta-Lactamase was refolded by eluting the loaded sample with 1 M urea in 0.05 M phosphate buffer, pH 7 at 23 degrees C. The following columns were studied: 26 x 400, 16 x 400 and 26 x 200 mm, with a range of mobile phase flow rates from 0.33 to 4.00 ml/min. beta-Lactamase was successfully refolded in all three columns and at all flow rates studied. The beta-lactamase activity peak coincided with the major protein peak. Reducing the column diameter had little effect on refolding performance. The enzyme activity recovered was relatively independent of the mobile phase linear velocity. Reducing the column length gave a poorer resolution of the protein peaks, but the enzyme activity peaks were well resolved. Calculation of the partition coefficients for beta-lactamase activity showed that the 26 x 400 column gave the greatest refolding performance.     

Chromatography of human prothrombin from Nitschmann fraction III on Q Sepharose Fast Flow using axial and radial flow column

An axial column (Hitrap Q 5 ml, 2.5 2 1.6 cm) and a radial flow column (3.5 2 5 cm) packed with Q Sepharose Fast Flow media had been evaluated for the separation of human prothrombin. Nitschmann fraction III dissolved in buffered saline (0.10 M sodium chloride buffered with 0.06 M Tris/HCl to pH 7.5) was the starting material. Effects of sample flow rate of the two columns were screened. Under radial flow conditions using the radial column, sample flow rate up to 15 ml/min (i.e. 18 bed volumes/h) was achieved and the operating pressure was below 0.2 MPa eventhough the elution velocity was 30 ml/min. Breakthrough capacity was determined by analyzing the total protein and prothrombin activity of the target protein-containing fraction under subsaturating conditions and both columns had almost the same breakthrough capacity per ml media, indicating that the sample loading was independent of radial column geometry. It was concluded that the radial column is an attractive alternate to traditional axial packed bed column, exhibiting very good potential for use in the separation of human prothrombin.     

Affinity purification of mouse monoclonal IgE using a protein A mimetic ligand (TG19318) immobilized on solid supports

A synthetic ligand (TG19318), deduced from the screening of a combinatorial peptide library, has been previously characterized by our group for its applicability in affinity chromatography for polyclonal and monoclonal IgG purification from crude sources. In this study we have extended the characterization of its recognition properties for other immunoglobulin classes, evaluating its ability to purify mouse monoclonal IgE from ascitic fluid. TG19318 affinity columns proved useful for a very convenient one-step purification of IgE directly from crude ascites, by loading the samples on the columns equilibrated with 50 mM sodium phosphate at pH 7 and eluting and adsorbed IgE by a buffer change to 0.1 M acetic acid. Antibody purity after affinity purification was very high and no albumin traces were detected, as determined by SDS-PAGE analysis. Antibody activity was fully recovered after purification, as determined by immunoassays on antigen-coated plates, and up to 5 mg of IgEs could be purified on a 1 ml column in a single run.     

Effect of blood thrombokinase,as influenced by soy bean trypsin inhibitor,ultracentrifugation, and accessory factors

1. Crystallized soy bean trypsin inhibitor, at a concentration of 100 microg./ml., suppressed the production of thrombin from a mixture of prothrombin and blood thrombokinase. The experiment was performed in the presence of 0.011 M oxalate, in order to minimize the possibility of participation by accessory factors which require ionic calcium. The results are in accord with the view that thrombokinase is a trypsin-like enzyme. 2. When a solution of blood thrombokinase was centrifuged at 85,000 g for 120 minutes, almost all the activity remained in the supernate. This supernate activated the supernate from a prothrombin solution which had been similarly centrifuged. The activation of prothrombin by thrombokinase can proceed in the absence of material completely sedimentable in 120 minutes at 85,000 g. 3. An "accelerator" reagent was prepared by treating bovine serum with barium carbonate, and then passing the serum through a column of diatomaceous earth. This "accelerator" was used together with prothrombin, blood thrombokinase, Howell's cephalin, and calcium chloride to compose a five-reagent thrombin-producing system. In this system, no thrombin was produced without thrombokinase. On the other hand, thrombin was produced from prothrombin and thrombokinase, even when all the other reagents were omitted. When calcium was omitted, thrombokinase was able to function; but cephalin and the "accelerator" reagent were ineffective. 4. Quantitative tests indicated that the "accelerator" reagent exerted an effect distinct from those of thrombokinase and cephalin. However, it is not certain whether the "accelerator" reagent functioned as an accessory factor, as a potential source of more thrombokinase, or both. In the experiments reported, thrombokinase was primary to, or necessary for, the effect of "accelerator." 5. The effectiveness of thrombokinase was multiplied a hundred times or more, when complemented by calcium, cephalin, and "accelerator" reagent. Ionic calcium was a necessary component of this complementing system. This may help to explain why removal of calcium ions keeps blood fluid, even though thrombokinase, by itself, is little influenced either by calcium ions or by oxalate.     

Preparation of thrombokinase from bovine plasma

Thrombokinase is prepared from bovine plasma by a procedure involving: treatment with diatomaceous silica, adsorption on barium sulfate, flowing elution with two successive phosphate buffers, ammonium sulfate fractionation, "spontaneous" activation in concentrated solution, and isoelectric precipitation. The yield of nitrogen is 0.002 per cent, corresponding to 1.2 mg. protein per liter of plasma. When diluted back to the volume of parent plasma, and complemented by calcium plus cephalin, the product causes appreciable activation of prothrombin in 1 minute. Thus, the quantity of thrombokinase obtainable is compatible with a physiologic role. In the more complex system used for routine assay, thrombokinase can be supplied by crude plasma at a dilution of 1/500. In parallel tests, the product appears to be more active than its parent plasma, although it contains only 0.002 per cent of the nitrogen. However, the thrombokinase of the product has been activated, whereas the thrombokinase of the plasma is probably in an inactive precursor state. When diluted back to the volume of parent plasma, to a concentration of 0.2 microgram nitrogen per ml., thrombokinase can slowly activate prothrombin in the presence of oxalate, and without the addition of accessory factors. Activation of prothrombin in the presence of oxalate is faster with higher concentrations of thrombokinase.     

Analytical method for the quantitative determination of cyanuric acid as the degradation product of sodium dichloroisocyanurate in urine by liquid chromatography mass spectrometry

A simple and selective analytical method for the quantitative determination of cyanuric acid, the degradation product of sodium dichloroisocyanurate (NaDCC), in human urine is reported herein. The sample preparation involved the use of diatomaceous earth extraction columns. Quantification was achieved by liquid chromatography mass spectrometry using negative ion electrospray with a cyano (CN) column. Between day relative standard deviation less than 10% (n=6) was obtained at the 5 mg L(-1) level. The assay was linear over the investigated range 0-20 mg L(-1) and the limit of detection (LOD) was confirmed to be 0.1 mg L(-1). The method was applied to monitoring levels of cyanuric acid in healthcare workers using disinfectants products containing NaDCC.     

Acetylated prothrombin as a substrate in the measurement of the procoagulant activity of platelets: elimination of the feedback activation of platelets by thrombin.

Human prothrombin was acetylated to produce a modified prothrombin that upon activation by platelet-bound prothrombinase generates a form of thrombin that does not activate platelets but retains its amidolytic activity on a chromogenic peptide substrate. If normal prothrombin is used in such an assay, the thrombin that is generated activates the platelets in a feedback manner, accelerating the rate of thrombin generation and thereby preventing accurate measurement of the initial platelet procoagulant activity. Acetylation of prothrombin was carried out over a range of concentrations of sulfo-N-succinimidyl acetate (SNSA). Acetylation by 3 mM SNSA at room temperature for 30 min at pH 8.2 in the absence of metal ions produced a modified prothrombin that has <0.1% clotting activity (by specific prothrombin clotting assay), but it is activated by factor Xa (in the presence of either activated platelets or factor Va + anionic phospholipid) to produce thrombin activity that is measurable with a chromogenic substrate. Because the feedback action on the platelets is blocked, thrombin generation is linear, allowing quantitative measurement of the initial platelet activation state.     

Modification of histidines in human prothrombin. Effect on the interaction of fibrinogen with thrombin from diethyl pyrocarbonate-modified prothrombin

Diethyl pyrocarbonate (ethoxyformic anhydride) was used to modify histidyl residues in prothrombin. Diethyl pyrocarbonate inactivated the potential fibrinogen-clotting activity of prothrombin with a second-order rate constant of 70 M-1 min-1 at pH 6.0 and 25 degrees C. The difference spectrum of the modified protein had a maximum absorption at 240 nm which is characteristic of N-carbethoxyhistidine. The pH dependence for inactivation suggested the participation of a residue with a pKa of 6.2. Addition of hydroxylamine to ethoxyformylated prothrombin reversed the loss of fibrinogen-clotting activity. No structural differences were detected between the native and modified proteins using fluorescence emission and high-performance size-exclusion chromatography. The tyrosine and tryptophan content was not altered, but approximately 1-2 amino groups were modified. Statistical analysis of residual enzyme activity and extent of modification indicates that among 7 histidyl residues modified per molecule, there is 1 essential histidine (not in the active site) involved in the potential fibrinogen-clotting activity of prothrombin. To further examine its properties, the modified prothrombin was activated to thrombin using Echis carinatus venom protease. There was no difference in the catalytic activity of thrombin obtained from either native or ethoxyformylated prothrombin, as measured by H-D-Phe-pipecolyl-Arg-p-nitroanilide (D-Phe-Pip-Arg-NA) hydrolysis. However, thrombin produced from the modified protein showed a loss of fibrinogen-clotting activity but had a comparable apparent Ki value (about 20 microM) to thrombin from native prothrombin when fibrinogen was used as a competitive inhibitor during D-Phe-Pip-Arg-NA hydrolysis. The similarity in Ki values indicated that thrombin derived from diethyl pyrocarbonate-modified prothrombin does not have an altered fibrinogen-binding site. Although the histidyl residue involved during inactivation has not been identified, the results suggest that a histidyl residue in the thrombin portion of prothrombin is essential for interaction with fibrinogen.     

A study of histone-histone interactions by affinity chromatography

Homologous whole histone from calf thymus was adsorbed on Sepharose 4B columns with covalently coupled histone fractions H2a, H2b, H3 or H4 in 0.01 M phosphate buffer, pH 6.7–1 M NaCl. The adsorbed histones were eluted from the columns with 5 M urea in the same buffer. Electrophoretic analysis has shown that the different columns exhibit selective affinity to the histone fractions: the H2b column to histone H2b and H2a (with only weak affinity to histones H3 and H4), the H2a column to histones H2b and H3 (moderate affinity to histones H2a and H4), the H3 column to histones H3, H4, H2a (moderate affinity to histone H2b), and the H4 column to histone H3, H4 and H2b (weak affinity to histone H2a). Histone H1 displayed no fixation by either of the columns tested.     

Glyphosate degradation by immobilized bacteria: laboratory studies showing feasibility for glyphosate removal from waste water.

To evaluate immobilized bacteria technology for the removal of low levels of glyphosate (N-phosphonomethylglycine) from aqueous industrial effluents, microorganisms with glyphosate-degrading activity obtained from a fill and draw enrichment reactor inoculated with activated sludge were first exposed to glyphosate production wastes containing 500-2000 mg glyphosate/L. The microorganisms were then immobilized by adsorption onto a diatomaceous earth biocarrier contained in upflow Plexiglas columns. The columns were aerated, maintained at pH 7.0-8.0, incubated at 25 degrees C, supplemented with NH4NO3 (50 mg/L), and exposed to glyphosate process wastes pumped upflow through the biocarrier. Glyphosate degradation to aminomethylphosphonic acid was initially > 96% for 21 days of operation at flows yielding hydraulic residence times (HRTs) as short as 42 min. Higher flow rate studies showed > 98% removal of 50 mg glyphosate/L from the waste stream could be achieved at a HRT of 23 min. Glyphosate removal of > 99% at a 37-min HRT was achieved under similar conditions with a column inoculated with a pure culture of Pseudomonas sp. strain LBr, a bacterium known to have high glyphosate-degrading activity. After acid shocking (pH 2.8 for 18 h) of a column of immobilized bacteria, glyphosate-degrading activity was regained within 4 days without reinoculation. Although microbial growth and glyphosate degradation were not maintained under low organic nutrient conditions in the laboratory, the low levels of degradable carbon (45-94 mg/L) in the industrial effluent were sufficient to support prolonged glyphosate-degrading activity. The results demonstrated that immobilized bacteria technology is effective in removing low levels of glyphosate in high-volume liquid waste streams.     

Adsorption-desorption of recombinant hepatitis B surface antigen (r-HBsAg) from P. pastoris on a diatomaceous earth matrix: Optimization of parameters for purification

Recombinant hepatitis B surface antigen (r-HBsAg) produced in yeast is adsorbed on a diatomaceous earth matrix for purification purposes. A pH dependence in the adsorption-elution behavior was found. The capacity of celite (Hyflo Super Cei) for adsorbing r-HBsAg increased with decreasing pH. Nonspecific proteins were also adsorbed, but a low pH dependence was found. Elution from the matrix was performed using a basic pH buffer, in which r-HBsAg is more specifically adsorbed/desorbed than contaminant proteins, permitting the purification of the r-HBsAg. A pH of 4.0 was used for adsorption and pH 8.2 was used for desorption. The described protocol allows a purification factor between three- and fivefold with respect to contaminant proteins and sixfold with respect to contaminant DNA. Finally, the adsorption step was successfully scaled-up for production purposes. (c) 1993 John Wiley & Sons, Inc.     

Outstanding Characteristics of Thrombokinase Isolated from Bovine Plasma

Thrombokinase has been isolated from bovine plasma by a procedure which begins with the highly purified product of a previously described method, chromatographs it on DEAE-cellulose, and then fractionates it by continuous flow electrophoresis, yielding 0.2 mg per liter of oxalated plasma. The electrophoretic fraction has shown a single boundary in the ultracentrifuge; and its esterase activity on toluenesulfonylarginine methyl ester has been about the same as that of thrombokinase previously isolated by repeated electrophoretic fractionations. Thrombokinase is a euglobulin with minimum solubility near pH 5.0. It is most stable within the pH range 7.5 to 9.5; but there is also a peak in the stability curve near pH 1.8. A few micrograms of thrombokinase per milliliter can activate prothrombin in the presence of EDTA. A few thousandths of a microgram causes rapid production of thrombin in the system: prothrombin, thrombokinase, calcium chloride, phosphatide, "accelerator." But, thrombokinase has less than 1/175 the proteolytic activity of crystallized trypsin.     

Membrane-bound choline acetyltransferase from human brain: Purification and properties

Choline acetyltransferase (ChAT; EC 2.3.1.6) was separated from human caudate/putamen into three fractions by successive extractions into apotassium phosphate buffer, a high salt (NaCl) buffer and a buffer containing 0.6% Triton X-100. The Triton-X-solubilized fraction is the membrane-bound ChAT (mChAT) and represents about 40% of the total ChAT. After centrifugation, mChAT was precipitated by ammonium sulfate at 35–65% saturation. The crude enzyme preparation was fractionated in turn on a DEAE-Sepharose, a hydroxylapatite and a phosphocellulose columns. Finally, mChAT was applied to a CoA-Sepharose column equilibrated with buffer containing 100 mM choline chloride and was specifically eluted with buffer containing acetyl-CoA. The presence of both substrates greatly stabilized the enzyme and ChAT was recovered almost quantitatively. The final preparation of mChAT has a specific activity of 37.2 mol of acetylcholine synthesized per min-mg protein. The purified mChAT has a pH optimum of 8.3. It migrated as two bands on SDS-PAGE with molecular weights of 67,000 and 62,000 daltons, respectively. Immunoblot autoradiography showed that an antiserum prepared previously against soluble ChAT also cross-reacted with both bands of mChAT, indicating that both forms of this enzyme are related. Furthermore, as previously reported for soluble ChAT, Fab-Sepharose chromatography could be used for the purification of mChAT and this preparation also resolved into two bands of 10% SDS gel.Special Issue dedicated to Prof. Eduardo De Robertis.     

Effect of varying static and changing moisture levels during incubation on extractability of soil phosphate

Summary A sandy loam (pH 6.5) was incubated at 28°C at static moisture levels, ranging from 10 per cent saturation to 133 per cent saturation (waterlogging), for 6 and 12 weeks; other samples covering the same moisture range were first incubated for 6 weeks, and after changing all moisture levels to 50 per cent saturation were incubated for a further 6 weeks.With increasing static soil moisture level during incubation there was a slight reduction in Morgan-extractable phosphate up to 70 per cent saturation, but thereafter, due to anaerobic effects, there were considerable increases in extractable phosphate with increasing moisture level.With changing moisture level during incubation the effects of anaerobiosis became apparent where original moisture level was greater than 50 per cent saturation; extractable phosphate was reduced to levels lower than those occurring where the soil was maintained continuously at 50 per cent saturation. The extent of reduction in extractable phosphate increased with original soil saturation level.