High-buffering capacity, hydrolytically stable, low-pI isoelectric membranes for isoelectric trapping separations

Proteomic analysis of 3T3-L1 adipocyte mitochondria during differentiation and enlargement

The increase in adipose tissue mass arises in part from progressive lipid loading and triglyceride accumulation in adipocytes. Enlarged adipocytes produce the highest levels of pro-inflammatory molecules and reactive oxygen species (ROS). Since mitochondria are the site for major metabolic processes (e.g., TCA cycle) that govern the extent of triglyceride accumulation as well as the primary site of ROS generation, we quantitatively investigated changes in the adipocyte mitochondrial proteome during different stages of differentiation and enlargement. Mitochondrial proteins from 3T3-L1 adipocytes at different stages of lipid accumulation (days 0-18) were digested and labeled using the iTRAQ 8-plex kit. The labeled peptides were fractionated using a liquid phase isoelectric fractionation system (MSWIFT) to increase the depth of proteome coverage and analyzed using LC-MS/MS. A total of 631 proteins in the mitochondrial fraction, including endoplasmic reticulum-associated and golgi-related mitochondrial proteins, were identified and classified into 12 functional categories. A total of 123 proteins demonstrated a statistically significant change in expression in at least one of the time points over the course of the experiment. The identified proteins included enzymes and transporters involved in the TCA cycle, fatty acid oxidation, and ATP synthesis. Our results indicate that cultured adipocytes enter a state of metabolic-overdrive where increased flux through the TCA cycle and increased fatty acid oxidation occur simultaneously. The proteomic data also suggest that accumulation of reduced electron carriers and the resultant oxidative stress may be attractive targets for modulating adipocyte function in metabolic disorders.

Concentration and fractionation by isoelectric trapping in a micropreparative-scale multicompartmental electrolyzer having orthogonal pH gradients. Part 1

A multicompartmental electrolyzer called ConFrac has been developed and tested for micropreparative-scale isoelectric trapping separations. ConFrac contains n separate, minimalistic isoelectric trapping core units, each with a separate anode compartment, anodic flow-through compartment, collection compartment, cathodic flow-through compartment and a shared cathode compartment. The collection compartments are all isolated from each other and have volumes of 100 μL each. The liquid held in the collection compartments is stagnant. The respective anodic and cathodic flow-through compartments are hydraulically serially connected to each other by flexible, minimum-length, narrow internal diameter tubes. The respective feed solutions whose volumes are larger and variable are recirculated through the serially connected flow-through compartments. Poly(vinyl alcohol)-based buffering membranes are placed between the anode compartments, anodic flow-through compartments, collection compartments, cathodic flow-through compartments and cathode compartment. The membranes establish two orthogonal pH gradients in ConFrac. The primary pH gradient is parallel with the direction of the recirculating flows and orthogonal to that of the electric field. The secondary pH gradient is parallel with the direction of the electric field and orthogonal to that of the recirculating flows. Since the recirculating liquids are kept in thermostated reservoirs and the residence times in the flow-through compartments are shorter than 2 s, ConFrac can tolerate power loads as high as 2 W without overheating the solutions. The operation and performance of ConFrac has been quantitatively characterized: four 25 μM ampholytic components were isolated from 5 mL of feed solution in 20 min and their concentration increased approximately 50-fold.

Combining isoelectric point-based fractionation, liquid chromatography and mass spectrometry to improve peptide detection and protein identification

The off-line coupling of an isoelectric trapping device termed membrane separated wells for isoelectric focusing and trapping (MSWIFT) to mass spectrometry-based proteomic studies is described. The MSWIFT is a high capacity, high-throughput, mass spectrometry-compatible isoelectric trapping device that provides isoelectric point (pI)-based separations of complex mixtures of peptides. In MSWIFT, separation and analyte trapping are achieved by migrating the peptide ions through membranes having fixed pH values until the peptide pI is bracketed by the pH values of adjacent membranes. The pH values of the membranes can be tuned, thus affording a high degree of experimental flexibility. Specific advantages of using MSWIFT for sample prefractionation include: (1) small sample volumes (approximately 200 microL), (2) customized membranes over a large pH range, (3) flexibility in the number of desired fractions, (4) membrane compatibility with a variety of solvents systems, and (5) resulting fractions do not require sample cleanup before MS analysis. Here, we demonstrate the utility of MSWIFT for mass spectrometry-based detection of peptides in improving dynamic range and the reduction of ion suppression effects for high-throughput separations of tryptic peptides.

The Biflow: An instrument for transfer-loop mediated, continuous, preparative-scale isoelectric trapping separations

The Biflow, a new isoelectric trapping instrument was designed to obtain a narrow DeltapI fraction from a complex feed in one step. The Biflow contains two identical separation units, each unit houses: an anode and cathode compartment, an anodic and cathodic membrane, an anodic and cathodic separation compartment, and a separation membrane. The separation units are connected to independent power supplies. The anodic membranes in Units 1 and 2 typically buffer at the same pH value and so do the cathodic membranes. The separation membranes in Units 1 and 2 buffer at different pH values, these determine the pI range (DeltapI) of the product. The cathodic separation compartments in Units 1 and 2 contain the feed and harvest streams. The two anodic separation compartments, connected through an electrically insulating air gap, form the transfer loop through which the transfer stream is recirculated between Units 1 and 2. Ampholytic components in the feed, with pI values lower than the pH of the buffering membrane in Unit 1, pass into the transfer stream and are shuttled into Unit 2. In Unit 2, components in the transfer stream which have pI values higher than the pH of the buffering membrane in Unit 2, pass into the harvest stream. This double transfer of the target component, oppositely directed, guarantees the complete exclusion of products outside the desired DeltapI range from the harvest stream. The utility of the Biflow unit was demonstrated by isolating carnosine from a mixture of UV-absorbing ampholytes and ovalbumin isoforms as well as 4.4 <pI <4.5 and 5.4 <pI <5.5 minor constituents from chicken egg white.

Use of a preparative-scale, recirculating isoelectric trapping device for the isolation and enrichment of acidic proteins in bovine serum

A recirculating, preparative-scale isoelectric trapping device, developed for the binary isoelectric trapping separation of proteins has been used to desalt, isolate and enrich the pI<4 protein fraction from a 150 mL sample of bovine serum. Subsequent re-separation of the 2<pI<4 fraction with pH 3.0, 3.5 and 3.9 buffering membranes resulted in distinct, narrow pI fractions whose components could be readily analyzed by reversed-phase HPLC, even though they were below the detection limit in the original bovine serum sample. The entire isoelectric trapping process (from desalting to collection of the final, narrow pI fractions) took only 7h, indicating the potential of the recirculating, preparative-scale isoelectric trapping device as a front-end component in the proteomic work-flow when sufficiently large samples are available.

Rapid isoelectric trapping in a micropreparative-scale multicompartment electrolyzer

A multicompartmental electrolyzer called membrane-separated wells for isoelectric focusing and trapping (MSWIFT) has been developed and tested for micropreparative-scale isoelectric trapping separations. In the MSWIFT, the length of the heat conduction path from the center of the compartments to the wall is less than 1 mm. The compartments are made from 99.8% nonporous alumina that has a high heat conductivity and a high specific heat capacity, leading to adequate Joule heat dissipation even at power loads as high as 5 W. The length of any compartment parallel to the electric field (the intermembrane distance) can be selected to be multiples of 1.5 mm, leading to compartment volumes that are multiples of about 60 muL. A maximum of 20 (1.5 mm long) separation compartments can be readily assembled in the current version of MSWIFT. The MSWIFT has been used to desalt samples, isolate small ampholytic components (amino acids, peptides, and dyes), prefractionate complex protein mixtures and enrich minor components; these separations were achieved in 20-60 min.

pH transients during salt removal in isoelectric trapping separations: A curse revisited

The pH transients that occur during isoelectric trapping separations as a result of the removal of nonampholytic ionic components have been re-examined. Salts containing strong electrolyte anions and cations, both with equal and dissimilar mobilities, have been studied using anodic and cathodic buffering membranes whose pH values were both equidistant and nonequidistant from pH 7. The direction and magnitude of the pH transient (acidic or basic) was found to depend on both the mobilities of the anion and cation (mu(anion)/mu(cation)) and the pH difference between pH 7 and the pH of the buffering membranes (|pH(memb) (anodic) - 7|/|7 - pH(memb) (cathodic)|). When |pH(memb) (anodic) - 7|/|7 - pH(memb) (cathodic)| = 1, mu(anion)/mu(cation)<1 leads to an acidic pH transient, mu(anion)/mu(cation) = 1 eliminates the pH transient and mu(anion)/mu(cation)>1 leads to a basic pH transient. When mu(anion)/mu(cation) = 1, |pH(memb) (anodic) - 7|/|7 - pH(memb) (cathodic)|<1 leads to a basic pH transient, |pH(memb) (anodic) - 7|/|7 - pH(memb) (cathodic)| = 1 eliminates the pH transient and |pH(memb) (anodic) - 7|/|7 - pH(memb) (cathodic)|>1 leads to an acidic pH transient. By selecting appropriate anodic and cathodic buffering membranes to adjust the |pH(memb) (anodic) - 7|/|7 - pH(memb) (cathodic)| value, pH transients caused by dissimilar anion and cation mobilities can be avoided.

Characterization of discontinuous buffer junctions using pH indicators in capillary electrophoresis for protein preconcentration

An effective sample preconcentration technique for proteins and peptides was recently developed using capillary electrophoresis (CE) with discontinuous buffers [C.A. Nesbitt, J.T.-M. Lo, K.K.-C. Yeung, J. Chromatogr. A 1073 (2005) 175]. Two buffers of different pH created a junction to trap the sample molecules at their isoelectric points and resulted in over 1000-fold preconcentration for myoglobin within 30 min. To study the formation of pH junctions in CE, a pH indicator, bromothymol blue, is used in this work to reveal the pH changes at the discontinuous buffer boundary. Bromothymol blue (BTB) exhibits a drastic change in its visible absorption spectrum (300-600 nm) going from the acidic to basic pH conditions, and is therefore ideal for visualizing the changes in pH at the junctions created by various buffer combinations. Preconcentration of myoglobin was performed in discontinuous buffers containing BTB. Major differences in the BTB absorption profiles were identified from buffer systems that differ significantly in preconcentration performance, which in turn, allowed for the identification of ideal buffers for sample preconcentration. Up to 2000-fold preconcentrations of myoglobin were achieved in the buffer systems studied in this work. In addition, the role of the electroosmotic flow (EOF) on the preconcentration performance was investigated. A low EOF was found to be desirable, as the pH junction could stay longer in the capillary for accumulation of proteins. The pH junction also displayed characteristics to resist bandbroadening. Potential laminar flow resulted from the mismatched residual EOFs under the two pH conditions within the discontinuous buffers appeared to have minimal effect on the preconcentration. In fact, external applied pressure can be used to control the migration of the pH junction without compromising the protein preconcentration.

Synthesis of UV-absorbing and fluorescent carrier ampholyte mixtures and their application for the determination of the operational pH values of buffering membranes used in isoelectric trapping separations

Success in isoelectric trapping separations critically depends on the knowledge of the accurate operational pH value of the buffering membranes used. Currently, due to a lack of easy, rapid, accurate methods that can be used for the post-synthesis determination of the operational pH value of a buffering membrane, only nominal pH values calculated from the amounts of the reagents used in the synthesis of the membranes and their acid-base dissociation constants are available. To rectify this problem, UV-absorbing and fluorescent carrier ampholyte mixtures were prepared by alkylating pentaethylenehexamine with a chromophore and a fluorophore, followed by Michael addition of acrylic acid and itaconic acid to the resulting oligoamine. Carrier ampholyte mixtures, with evenly distributed absorbance values across the 3<pI<10 range, were prepared by blending. The master blend served as the feed mixture in binary isoelectric trapping separations that used the buffering membrane to be characterized. The pI value of the most basic UV-absorbing or fluorescent carrier ampholyte collected in the anodic separation compartment, determined by full-column imaging capillary isoelectric focusing analysis, indicates the operational pH value of the separation membrane.

Effects of increased voltage on resolution in preparative isoelectric focusing of myoglobin varia

IEF is a powerful technique which separates proteins and other amphoteric solutes in a pH gradient according to their pI's. The current work evaluates the effect on resolution of increasing electric fields in a novel preparative, vortex-stabilized electrophoresis device. In shallow gradients spanning one pH unit, the variants of myoglobin were separated at applied voltages from 10 to 15 kV. Digital imaging of these separations indicated a 20% reduction in bandwidth and a 60% increase in resolution as the electric field strength is varied across this range. These results were confirmed by IEF-PAGE and ion-exchange chromatography.

Hydrolytically stable, diaminocarboxylic acid-based membranes buffering in the pH range from 6 to 8.5 for isoelectric trapping separations

Diaminocarboxylic acid carrier ampholytes, such as L-histidine, 2,3-diaminopropionic acid, L-ornithine, and L-lysine, were reacted with glycerol-1,3-diglycidyl ether (GDGE) and poly(vinyl alcohol) (PVA) in the presence of sodium hydroxide to produce hydrolytically and mechanically stable hydrogels, supported on a PVA substrate, for use as buffering membranes in isoelectric trapping (IET) separations. The pH values of the DACAPVA membranes were determined with the help of small-molecule pI markers and proteins and were found to be in the 6 < pH < 8.5 range. The membranes were successfully used to isoelectrically trap small ampholytes, desalt ampholyte solutions in IET mode, and effect the binary separation of chicken egg white proteins.

Synthesis and characterization of quaternary ammonium dicarboxylic acid isoelectric buffers and their use in pH-biased isoelectric trapping separations

Two approaches are described in this paper for the synthesis of isoelectric buffers that have pI values in the 1.5 < pI < 4.3 range. The first synthesis relies on the alkylation of existing aminodicarboxylic acids and recovery of the ampholyte as an inner salt. The second synthesis method forms low-pI ampholytes by reacting a secondary amine with two equivalents of an alkylester of a haloalkanecarboxylic acid, followed by hydrolysis of the intermediate in an alkaline solution and recovery of the ampholyte as an inner salt. The new ampholytes have been analytically characterized by capillary electrophoresis, high-resolution electrospray ionization-mass spectrometry, one- and two-dimensional nuclear magnetic resonance (NMR) spectroscopy, and X-ray crystallography. The isoionic solutions of the new ampholytes have high buffering capacity and conductivity, making them good pH biasers in the receiving stream in preparative-scale pH-biased isoelectric trapping separations.

How to Bring the “Unseen” Proteome to the Limelight via Electrophoretic Pre-Fractionation Techniques

The present review reports a panoply of electrophoretic methods as pre-fractionation tools in proteomic investigations in preparation for mass spectrometry or two-dimensional electrophoresis map analysis. Such electrophoretic pre-fractionation protocols include all those electrokinetic methodologies which are performed in free solution, most of them relying on isoelectric focusing steps (although some approaches based on gels and granulated media are also discussed). Devices associated with electrophoretic separations are multi-chamber apparatuses, such as the multi-compartment electrolyzers equipped with either isoelectric membranes or with isoelectric beads, Off-Gel electrophoresis in a multi-cup device and the Rotofor, an instrument also based on a multi-chamber system but exploiting the conventional technique of carrier-ampholyte-focusing. Other free-flow systems, as well as miniaturized chambers, are also described.

A family of high-buffering capacity diamino sulfate isoelectric buffers for pH-biased isoelectric trapping separations

pH-biased isoelectric trapping separations are hindered by the lack of suitable isoelectric buffers with pI values in the 5.8 < pI range. Two generic approaches are described here for the cost-effective synthesis of a family of diamino sulfate buffers that have high buffering capacities in their isoelectric state: the first approach relies on the sulfation of existing, commercially available diamino alcohol intermediates, the second approach calls for the synthesis of diamino alcohols from epichlorohydrin and widely available secondary amines, and subsequent sulfation of the new diamino alcohol. The diamino sulfate buffers are recovered in isoelectric state, in high purity. Four members of the family having pI values in the 5.8 < pI < 8.9 range have been synthesized, analytically characterized by capillary electrophoresis (CE), electrospray ionization-time of flight-mass spectrometry (ESI-TOF-MS), 1-D and 2-D nuclear magnetic resonance (NMR) spectroscopy, and X-ray crystallography. All four diamino sulfates have been successfully used as pH biasers in the receiving stream in preparative-scale pH-biased isoelectric trapping protein separations.