A novel method to determine residual detergent in biological samples post endotoxin reduction treatment and evaluation of strategies for subsequent detergent removal.

Endotoxin removal using detergent washes and extractions are well-established, efficient, and cost-effective methods; however, removing residual detergent post treatment has been shown to be a challenge. In this communication, we show a simple and fast method for determining the detergent concentration in a protein solution post treatment and highlight strategies for detergent removal to achieve levels below the critical micelle concentration (CMC), the minimum concentration at which detergent micelles form.

The removal of Triton X-100 by dialysis is feasible!

Triton X-100 has been widely used in many analytical and preparative protocols for a long time. Nevertheless, mass spectrometry, chromatographic separation, and spectrophotometric readout may be considerably hampered by this detergent due to signal suppression, complex formation, and high blank values, respectively. Additionally, Triton X-100 is not safe to remove prior to analytics. Here, microdialysis is introduced as a parallelizable, high-throughput method to clean samples from Triton X-100 with high efficacy and precision. To achieve this, we exploit the potential to considerably increase the critical micellar concentration of Triton X-100 by alteration of matrix properties. To that end, addition of several chaotropic compounds and organic solvents has been shown to increase the critical micellar concentration as well as the removal rate of the detergent. For application, matrix additives can be selected for analyte stability requirements out of a variety of compounds. Conveniently, all these additives are removable subsequently using the same microdialysis tool for downstream analytics requirements. Applicability and protocols are shown with proteomic sample preparation of purified proteins and complex protein mixtures prior to matrix-assisted laser desorption ionization (MALDI) mass spectrometry.

Degradation and toxicity assessment of the nonionic surfactant Triton™ X-45 by the peroxymonosulfate/UV-C process.

The degradation and mineralization of the nonionic surfactant octylphenol ethoxylate (OPEO), commercially known as Triton™ X-45, by the peroxymonosulfate (PMS)/UV-C process were investigated. Three different toxicity tests (Daphnia magna, Vibrio fischeri and Pseudokirchneriella subcapitata) as well as the Yeast Estrogen Screen (YES) bioassay were undertaken to evaluate the potential toxic and estrogenic effects of OPEO and its oxidation products. OPEO removal was very fast and complete after 7 min via PMS/UV-C treatment under the investigated reaction conditions (OPEO = 20 mg L(-1) (47 µM); TOC = 12 mg L(-1); PMS = 2.5 mM; initial reaction pH = 6.5; applied UV-C dose = 21 Wh L(-1)). TOC removal also proceeded rapidly; a gradual decrease was observed resulting in an overall TOC removal of 84%. The toxic responses of PMS/UV-C treated OPEO solutions varied according to the test organism used in the bioassay. Daphnia magna was found to be most sensitive to aqueous OPEO, whereas Pseudokirchneriella subcapitata appeared to be the least sensitive one. Daphnia magna and Vibrio fischeri tests revealed that the inhibitory effect of OPEO decreased significantly during the course of treatment. On the other hand, PMS/UV-C oxidation products exhibited a high toxic effect towards Pseudokirchneriella subcapitata (around 60%). YES test results underlined the need for improving the PMS/UV-C treatment performance to remove the estrogenic activity of OPEO and its oxidation products.

Presence and removal of a contaminating NADH oxidation activity in recombinant maltose-binding protein fusion proteins expressed in Escherichia coli.

We observed the presence of contaminating NADH oxidation activity in maltose binding protein (MBP) fusion proteins expressed in Escherichia coli and purified using conventional amylose resin-based affinity chromatography. This contaminating NADH oxidation activity was detectable with at least four different enzymes from Cryptosporidium parvum expressed as MBP-fusion proteins (i.e., an enoyl-reductase domain from a type I fatty acid synthase, a fatty acyl-CoA binding protein, the acyl-ligase domain from a polyketide synthase, and a putative thioesterase), regardless of their NADH dependence. However, contaminating NADH oxidation activity was not present when fusion proteins were engineered to contain a His-tag and were purified using a Ni-NTA resin-based protocol. Alternatively, for proteins containing only an MBP-tag, the contaminating activity could be eliminated through the addition of 0.1% Triton X-100 and 2% glycerol to the column buffer during homogenization of bacteria and first column wash, followed by an additional wash and elution with regular column and elution buffers. Removal of the artifactual activity is very valuable in the study of enzymes using NADH as a cofactor, particularly when the native activity is low or the recombinant proteins are inactive.

Removal of nonionic surfactants from wastewater using a constructed wetland.

Removal of nonionic surfactants from municipal wastewater using a constructed wetland with a horizontal subsurface flow was studied in 2009 and 2010. Extraction spectrophotometry with 3',3″,5',5″-tetrabromophenolphthalein ethyl ester and KCl served to determine the analyte concentrations. Triton(®) X-100 was used as a standard to express the nonionic-surfactant concentrations. Anionic and cationic surfactants were shown not to interfere during the determination. Nonionic surfactants were degraded (to products undeterminable by the method) with a high average efficiency that reached 98.1% in 2009 and 99.1% in 2010, respectively. The average concentration of nonionic surfactants at the inflow was 0.978 mg/l, while it was close to the limit of quantification at the outflow (0.014 mg/l). A significant fraction of nonionic surfactants (38.7%) was already degraded during the pretreatment, and only 14.0% of the nonionic surfactants remained in the interstitial H(2) O taken in the vegetation bed at a distance of 1 m from the inflow zone at a 50-cm depth. Nonionic surfactants were degraded both under aerobic and anaerobic conditions.

Strategies for the purification of membrane proteins.

Although membrane proteins account for 20-30% of the coding regions of all sequenced genomes and play crucial roles in many fundamental cell processes, there are relatively few membranes proteins with known 3D structure. This is likely due to technical challenges associated with membrane protein extraction, solubilisation, and purification. Membrane proteins are classified based on the level of interaction with membrane lipid bilayers, with peripheral membrane proteins associating non-covalently with the membrane, and integral membrane proteins associating more strongly by means of hydrophobic interactions. Generally speaking, peripheral membrane proteins can be purified by milder techniques than integral membrane proteins, whose extraction requires phospholipid bilayer disruption by detergents. Here, important criteria for strategies of membrane protein purification are addressed, with a focus on the initial stages of membrane protein solublilisation, where problems are most frequently encountered. Protocols are outlined for the successful extraction of peripheral membrane proteins, solubilisation of integral membrane proteins, and detergent removal which is important not only for retaining native protein stability and biological functions, but also for the efficiency of later purification techniques.

Practical aspects of using methacrylate-ester-based monolithic columns in capillary electrochromatography.

Methacrylate-ester-based monoliths containing quaternary ammonium groups were prepared in situ in capillary columns and in simultaneous experiments in vials, employing thermal initiation. The chromatographic properties of the monoliths were determined with capillary electrochromatography (CEC), and their morphology was studied with mercury-intrusion porosimetry on the bulk materials. Materials with different, well repeatable pore-size distributions could be prepared. A satisfactory column-to-column and run-to-run repeatability was obtained for the electro-osmotic mobility, the retention characteristics (k-values) and the efficiency on the columns prepared and tested in the CEC mode. A relatively high electro-osmotic flow was observed in the direction of the positive electrode. The electro-osmotic mobility was found to be influenced only marginally by mobile-phase parameters such as the pH, ionic strength, and acetonitrile content. The retention behavior of the monolithic columns was similar to that of columns packed with C18-modified silica particles. Columns could be prepared with optimum plate heights ranging from 6 microm for unretained compounds to 20 microm for well retained (k=2.5) polyaromatic hydrocarbons. However, for specific analytes a - still unexplained - lower chromatographic column efficiency was observed.

Activated carbons application to remove nonionic surfactants from wastewater produced by an Italian metallurgic plant.

The performance of different activated carbons for the removal of nonionic surfactants from metallurgic wastewater was assessed through lab scale experiments. Two different matrices were used: a simple one, obtained by dissolving different amounts of a single nonionic surfactant (Triton X100) in distilled water, and a complex matrix, prepared as above but using surfactants-free wastewater from an Italian metallurgic plant as solvent. In this way the main operative parameters that affect the adsorption process in the simple matrix have been studied avoiding the interference due to the complex matrix: then the results were utilized to define and optimize the tests carried out on the complex matrix. The adsorption equilibrium experimental data were best fitted with a Langmuir isotherm, allowing defining the contact time and the proper design parameters for the adsorption column. The different tests were performed on four different activated carbon types, and the removal efficiency and the treatment cycle duration for each of the tested carbons were discussed and compared. The experimental results showed that the saturation adsorption capacity is not notably correlated either with the pH value or with the water matrix, whereas the slope of the isotherm, defined by the Henry constant, is sensibly higher at strong acidic or alcaline conditions, with a minimum value at nearly neutral pH. Therefore, it was concluded that the removal efficiency is maximized when the operative pH was in the 2-4-unit value range. The best activated carbon, in terms of removal efficiency, resulted to be a mineral activated carbon, characterized by the highest iodine number, and thus with the largest porosity. Removal efficiencies were in the 60 to 80% range.

Capillary electrochromatography of Triton X-100.

Nonionic surfactants such as Triton X-100 (TX-100) are comprised of a mixture of oligomers with a varying degree of length in the ethoxylate chain. The development of chromatographic methods for resolution of the various oligomers of TX-100 is of environmental importance, and can be useful for quality control and characterization in industrial manufacture. Capillary electrochromatography (CEC) is fast becoming a capable separation technique that combines the benefits of both high-performance liquid chromatography (HPLC) and capillary electrophoresis (CE). This report presents a novel CEC method for separation of the various TX-100 oligomers. A comparison of monomeric vs. polymeric stationary phases for separation of TX-100 was conducted. Since the oligomers of TX-100 were better resolved on a monomeric phase as compared to polymeric phase, a systematic mobile phase tuning was performed utilizing a monomeric CEC-C18-3 microm-100 A stationary phase. Various mobile phase parameters such as acetonitrile (ACN) content, Tris concentration, pH, voltage, and temperature were manipulated in order to achieve the optimum separation of oligomers in less than 30 min.

Characterization of biodegradation intermediates of nonionic surfactants by MALDI-MS. 2. Oxidative biodegradation profiles of uniform octylphenol polyethoxylate in 18O-labeled water.

This paper reports the characterization of the biodegradation intermediates of octylphenol octaethoxylate (OP(8)EO) by means of matrix-assisted laser desorption/ionization mass spectrometry (MALDI-MS). The biodegradation test study was carried out in a pure culture (Pseudomonas putida S-5) under aerobic conditions using OP(8)EO as the sole carbon source and (18)O-labeled water as an incubation medium. In the MALDI-MS spectra of biodegraded samples, a series of OP(n)EO molecules with n = 2-8 EO units and their corresponding carboxylic acid products (OP(n)EC) were observed. The use of purified OP(8)EO enabled one to distinguish the shortened OPEO molecules as biodegradation intermediates. Furthermore, the formation of OP(8)EC (the oxidized product of OP(8)EO) supported the notion that terminal oxidation is a step in the biodegradation process. When biodegradation study was carried out in (18)O-labeled water, incorporation of (18)O atoms into the carboxyl group was observed for OPEC, while no incorporation was observed for the shortened OPEO products. These results could provide some rationale to the biodegradation mechanism of alkylphenol polyethoxylates.

Assessment of polycrystalline graphites as sorbents for solid-phase microextraction of nonionic surfactants.

Two polycrystalline graphites (pencil lead and glassy carbon) were used as sorbents for solid-phase microextraction of a nonionic alkylphenol ethoxylate surfactant (Triton X-100). Analyses were performed by reversed-phase HPLC-fluorescence detection. The presence of the benzene ring in the congeners of Triton X-100 also allowed their direct detection at lambda(ex) = 230 nm and lambda(em) = 310 nm. Variables such as time of adsorption, time of desorption and concentration of surfactant in water were evaluated. The method limit of detection was found to be 0.5 microg/l for Triton X-100, with a linear dynamic range of 0.5-150 microg/l. Results were compared to those obtained using polymeric fibers such as PDMS/DVB and Carbowax/TPR. The chemical resistance and low cost of the polycrystalline graphites are advantageous over commercially available SPME fibers.

Quantitative determination of zwitterionic detergents using salt-induced phase separation of Triton X-100.

Zwitterionic detergents interfere with the salt-induced phase separation for nonionic detergents in a concentration-dependent manner by shifting the normal cloud point of nonionic detergents to a higher ionic strength at room temperature. This phenomenon was used to determine the concentration of the zwitterionic detergents CHAPS, CHAPSO, and sulfobetaine SB-12 in solution by titration with ammonium sulfate in the presence of Triton X-100. Among the ionic detergents tested, the method was only applicable to sodium cholate. The assay can be used to control the removal of zwitterionic detergents during the reconstitution of membrane proteins in liposomes. However, it cannot be used to determine the specific binding of zwitterionic detergents to highly diluted, pure membrane proteins because of the limited sensitivity. Neither proteins nor phospholipids interfered with this method at concentrations up to 20 mg/ml of test solution (human serum albumin) or 10 mg/ml (phospholipids), respectively. Since the assay is based on the competition between salts and nonionic detergents for water molecules, it is important to equalize the ionic strength of samples and calibration standards.

Quantitative determination of cardiolipin in mitochondrial electron transferring complexes by silicic acid high-performance liquid chromatography.

Quantitative determination of cardiolipin from two mitochondrial electron-transferring complexes was achieved using a rapid and sensitive silicic acid HPLC method combined with digital analysis of the elution profile. Phospholipid samples containing as little as 0. 01 nmol of cardiolipin were accurately analyzed. Phospholipids from detergent-solubilized cytochrome bc1 (EC 1.10.2.2) and cytochrome c oxidase (EC 1.9.3.1) were extracted by an organic two-phase system and analyzed by isocratic normal-phase HPLC after dissolving the dried sample in the mobile phase (cyclohexane:2-propanol:5 mM phosphoric acid, 50:50:2.9, v/v/v). Analysis was performed by the method of standard addition in which increasing amounts of cardiolipin (0 to 5 nmol) are added to a constant amount of phospholipid extract containing an unknown amount of cardiolipin. By determining the slope and intercept of a plot of the HPLC elution peak area as a function of the amount of standard cardiolipin added, the amount of cardiolipin in the unknown is determined. By this analysis, purified, detergent-solubilized bovine heart cytochrome bc1 and cytochrome c oxidase contained 9.2 +/- 0.7 and 3.05 +/- 0.05 mol cardiolipin per mole of enzyme, respectively. The method was also used to prove that cardiolipin could be completely removed from each complex by digestion with Crotalus atrox phospholipase A2, i.e., each delipidated complex contained less than 0.05 mol cardiolipin per mole of complex. The rapidity and high sensitivity of this method make it very useful for analysis of cardiolipin in other biological samples.

Octoxynol presence in bear-bile.

The presence of octoxynol from dried bear-bile was examined. Octoxynol was coextracted when glycolipids by Folch-Suzuki partition method. Octoxynol formed mixed-micelles with glycosphingolipids. The glycolipids were purified by DEAE-Sephadex A-25 column chromatography. The fractions containing mixed micelles were obtained from linear gradient solvent of 0.05M-0.5M ammonium acetate in methanol. HPLC ( Bondapak-NH(2) - linked to a Bondapak-C(18) column) chromatogram showed five peaks. Two possible structures for the fourth peak fraction were proposed as (CH(3))(3)C-CH(2)-C(CH(3))(2)-C(6)H(4)-OR and (CH(3))(3)C-C(CH(3))(2)-CH(2)-C(6)H(4)-OR by NMR spectroscopy. The structure was further confirmed by electrospray tandem mass spectrometry (ESI MS/MS). The spectrum showed a protonated molecule at m/z 559 and three different series of ions with mass difference of 44 were detected in the MS/MS spectrum. Therefore, the structure of the fourth peak fraction from HPLC was confirmed as octoxynol, (CH(3))(3)C-CH(2)-C(CH(3))(2)-C(6)H(4)-(OCH(2)-CH(2))n-OH, based on mass spectrometry and NMR spectroscopy.

Extraction of Triton X-100 and its determination in virus-inactivated human plasma by the solvent--detergent method.

For inactivation of lipid-enveloped viruses during the production of fresh frozen and lyophilized human plasma, the solvent-detergent method was applied. In this process, the solvent tri-n-butyl phosphate is removed by extraction with castor oil. The removal of the non-ionic detergent Triton X-100 is performed by solid-phase extraction using reversed-phase supports. For this purpose, different polymer- and silica-based supports were tested. The highest capacity for Triton X-100 was achieved with C18 silica gels. These supports can bind more than 0.1 ml of Triton X-100 per ml of support. None of the proteins, e.g., clotting factors, bind to the support and therefore they pass through the column and their biological activity is hardly affected. The determination of detergent during the production process was also studied. The application of special columns allowing direct sample injection was introduced. This is a simple method for the rapid in-process determination of Triton X-100 in human plasma by reversed-phase chromatography under isocratic conditions. Using the method developed here, less than 1.0 ppm of Triton X-100 can be detected in less than 12 min without any sample pretreatment.