Abstract: The present invention relates to a method for separating a sample comprising a nucleic acid, the method comprising: (a) loading a sample comprising a nucleic acid onto an anion-exchange column; and (b) eluting the sample from the anion-exchange column using a salt gradient, wherein a mobile phase used in the eluting step comprises a mild ion-pairing cation, and wherein a column temperature of the anion-exchange column is greater than 30° C. The present invention also relates to a method for determining one or more calorimetric properties of a nucleic acid using anion-exchange chromatography.

Abstract: Provided herein chiral derivatization reagents for use in separating and detecting of amine containing enantiomers. The said chiral derivatization reagents provide a combination of improved detectable properties to facilitate various downstream analyses. In particular, the chiral derivatization reagents include at least one chiral carbon atom; at least one strongly basic moiety; at least one chromophore moiety or at least one fluorophore moiety; and at least one reactive group. The present disclosure further provides methods for analyzing amine-containing enantiomeric isomers using a chromatographic separation device and a mass spectroscopy.

Abstract: Methods for quenching a nuclease digestion of a target nucleic acid prior to downstream analysis of the target nucleic acid are disclosed herein. Particularly, methods for controlling the end point of a nuclease digestion prior to sequence analysis of a target nucleic acid is provided. Quenching of a nuclease digestion in the present disclosure employs at least one non-ionic or anionic denaturant combined with an optional reducing agent. The methods presented in this disclosure aids preserving the sample comprising the target nucleic acid or fragments thereof for long term storage and ensures that the effect of contaminating nucleases is eliminated during pretreatment step.

Abstract: A system capable of performing both single and multidimensional liquid chromatography includes a solvent delivery system, a sample injection system, a first dimension column path configured to perform a separation process in a first dimension, a second dimension column path configured to perform a separation process in a second dimension that is different than the first dimension, a valve system; and a sample injection system fluidically connected to the valve system. The valve system is configured to direct flow from a sample injection system to a first dimension column path when the valve system is in a first position, and to direct flow from the sample injection system to the second dimension column path without the flow path flowing through the first dimension column path in the chromatography system when the valve system is in a second position.

Abstract: In various embodiments, the present disclosure pertains to core-shell particles that comprise a porous hybrid organic-inorganic shell disposed on a surface-modified non-porous polymer particle core. In some embodiments, the present disclosure pertains to chromatographic separation devices that comprise such core-shell particles. In some embodiments, the present disclosure pertains to chromatographic methods that comprise: (a) loading a sample onto a chromatographic column comprising such core-shell particles and (b) flowing a mobile phase through the column.

Abstract: An immobilized enzymatic reactor can include a wall defining a chamber having an inlet and an outlet; a solid stationary phase covalently linked to an enzyme and disposed within the chamber; and a pressure modulator in a fluid communication with the chamber and adapted to support continuous flow of a liquid sample comprising a polymer analyte through the inlet, over the solid stationary phase, and out of the outlet under a pressure between about 2,500 and 35,000 psi. In one example, the solid stationary phase includes inorganic/organic hybrid particles in an ultra performance liquid chromatography system, the enzyme is a protease, and the polymer analyte is a polypeptide. The immobilized enzymatic reactor can prepare an analyte for applications such as for hydrogen deuterium exchange mass spectrometry.

Abstract: The present disclosure discusses a method of separating a sample (e.g., pharmaceutical drug, genotoxic impurity, biomarker, and/or biological metabolite) including coating a metallic flow path of a chromatographic system; injecting the sample into the chromatographic system; flowing the sample through the chromatographic system; separating the sample; and analyzing the separated sample using mass spectroscopy. In some examples, the coating applied to the surfaces defining the flow path is non-binding with respect to the sample—and the separated sample. Consequently, the sample does not bind to the low-binding surface of the coating of the flow path. The applied coating can increase the chromatographic peak area for the sample of the chromatographic system.

Abstract: In various aspects, the present disclosure pertains to methods of performing a sample enrichment procedure, which comprise: adding a sample fluid that comprises at least one phospholipid and at least one target analyte to a sorbent that comprises a hydrophobic component and a cation exchange component, thereby resulting in sorbent with bound phospholipid and bound target analyte; adding an aqueous solution comprising an acidic compound and a salt; adding an organic solution to the sorbent thereby desorbing at least a portion of the bound phospholipid from the sorbent; and adding an elution solution to the sorbent, thereby desorbing at least a portion of the bound target analyte from the sorbent and forming a solution of the target analyte in the elution solution. In other aspects, the present disclosure pertains to kits, which may be used in conjunction with such methods.

Abstract: Exemplary embodiments are directed to methods and systems for controlling fluid parameters within a detector. A first and second fluid pump manager control the flow of a first and second fluid to one or more heating/cooling devices, and a mixer receives and mixes the first and second fluids. An optical detector flow cell receives the fluid mixture from the mixer, and a pressure regulator controls the pressure at the optical detector flow cell. Thus, the composition, temperature, and pressure of a fluid mixture entering an optical detector flow cell can be controlled in real time.

Abstract: In various embodiments, the present disclosure pertains to organic polymer core-shell particles that comprise a non-porous organic polymer core (i.e., having a pore volume of less than 0.1 cc/g) and a porous organic polymer shell (i.e., having a pore volume of greater than 0.1 cc/g), in which the porous organic polymer shell has a pore size ranging from 100 ? to 3000 ?. In some embodiments, the present disclosure pertains to chromatographic separation devices that comprise such organic polymer core-shell particles. In some embodiments, the present disclosure pertains to chromatographic methods that comprise: (a) loading a sample onto a chromatographic column comprising such organic polymer core-shell particles and (b) flowing a mobile phase through the column.

Abstract: The invention relates to poly-amide bonded hydrophilic interaction chromatography (HILIC) stationary phases and novel HILIC methods for use in the characterization of large biological molecules modified with polar groups, known to those skilled in the art as glycans. The invention particularly provides novel, poly-amide bonded materials designed for efficient separation of large biomolecules, e.g. materials having a large percentage of larger pores (i.e. wide pores). Furthermore, the invention advantageously provides novel HILIC methods that can be used in combination with the stationary phase materials described herein to effectively separate protein and peptide glycoforms by eliminating previously unsolved problems, such as on-column aggregation of protein samples, low sensitivity of chromatographic detection of the glycan moieties, and low resolution of peaks due to restricted pore diffusion and long intra/inter-particle diffusion distances.

Abstract: The present invention provides methods for performing supercritical fluid chromatography comprising loading a sample to be separated by supercritical fluid chromatography onto a stationary phase comprising a spherical, monodisperse, core-shell particulate material comprising a nonporous core and one or more layers of a porous shell material surrounding the core, wherein the particles are sized less than 2 microns; and performing supercritical fluid chromatography to separate the sample.

Abstract: The present invention provides novel chromatographic materials, e.g., for chromatographic separations, processes for its preparation and separations devices containing the chromatographic material; separations devices, chromatographic columns and kits comprising the same; and methods for the preparation thereof. The chromatographic materials of the invention are chromatographic materials comprising having a narrow particle size distribution.

Abstract: Described is a dual mode sample manager for a liquid chromatography system. The dual mode sample manager includes a sample needle, a sample loop, a metering pump, a needle seat and first and second valves. Each valve is configurable in two valve states to enable two modes of operation. In one mode, sample acquired and stored in the sample needle is injected into a chromatography system flow and, in the other mode, sample acquired through the sample needle and stored in the sample loop is injected into the chromatography system flow. The automated switching of the sample manager between the two modes of operation avoids the need for maintaining two separate liquid chromatography systems or manual reconfiguration of a chromatography system for users desiring the capability of both modes of operation.

Abstract: A liquid chromatography system includes a solvent delivery system, a sample manager including a sample delivery system in fluidic communication with the solvent delivery system, the sample delivery system configured to inject a sample from a sample-vial into a chromatographic flow stream, a liquid chromatography column located downstream from the sample delivery system, and a detector located downstream from the liquid chromatography column. The sample delivery system further includes a first needle drive including a first sample needle configured to extract the sample from the sample-vial and deliver the sample to the liquid chromatography column, and a first syringe in communication with the first sample needle configured to meter extraction of the sample from the sample-vial. The sample manager further includes a sample automation system that includes a second needle drive including a second sample needle configured to add a volume of reagent to the sample-vial.

Abstract: A method of capturing human immunoglobulin Fc domains in a biofluid sample is provided. The method includes providing an affinity capture device. The affinity capture device includes a surface having an aptamer that is at least 80% identical to SEQ ID NO 1 immobilized onto the surface of the affinity capture device. The biofluid sample is diluted with a binding buffer. The binding buffer includes (A) tris(hydroxymethyl)aminomethane (Tris), trimethylamine (TES), 2-ethanesulfonic acid (MES), or 4-(2-hydroxyethyl)-1-piperazineethanesulfonic acid (HEPES); (B) a magnesium cation at a concentration between about 10 ?M to about 20 mM; and (C) a total monovalent cation concentration from 0 to no greater than 100 mM. The human immunoglobulin Fc domains in the biofluid sample are adsorbed to the aptamer with the binding buffer.

Abstract: A methodology scales supercritical fluid chromatography (SFC) and/or carbon dioxide based chromatography methods between different system and/or column configurations. The methodology includes measuring an average mobile phase density during a first separation utilizing C02 as a mobile phase component and substantially duplicating the average density profile for a second separation. Substantial duplication of the average mobile phase density (e.g., within about 10%, 5%, 2.5%, 1%, 0.5%, 0.1 %, 0.05%) results in chromatography for both system and/or column configurations having similar selectivity and retention factors. Average mobile phase density may be, either measured directly, calculated, or approximated using average pressure or density measurements. The average pressure profile may be used as a close approximation to duplicate average density profiles between separations.

Abstract: The present disclosure relates to a method for using chemical tags which have two or more sites for ionization to improve quantification and identification of components of interest from a complex mixture. This method relies on first selectively reacting one or more component in a sample with a chemical tag having two or more sites for ionization, followed by separation of components based on charge status, and finally characterization of each component to identify the same. Additionally disclosed are compounds useful as chemical tags in the disclosed methods.

Abstract: A liquid chromatography system including a solvent delivery system, a sample delivery system in fluidic communication with solvent delivery system, a liquid chromatography column located downstream from the solvent delivery system and the sample delivery system, a detector located downstream from the liquid chromatography column, a thermal chamber housing at least one of the solvent delivery system, the sample delivery system, the liquid chromatography column and the detector, an engine configured to control the temperature in the thermal chamber, a heatsink operably connected to the engine, a first temperature sensor in the thermal chamber, a second temperature sensor, and a computer system configured to receive temperature information from each of the first and second temperature sensors, and implement a method for controlling temperature in the thermal chamber.

Abstract: Described is a mixer for a chromatography system. The mixer includes an inlet manifold channel, an outlet manifold channel and a plurality of transfer channels. The inlet manifold channel has an inlet at a proximal end of the inlet manifold channel for receiving an inlet flow. The transfer channels are fluidly connected between the inlet and outlet manifold channels. The respective fluid connections are distributed along each of the inlet and outlet manifolds channels. The transfer channels have different volumes. The mixer may be formed of a plurality of layer and the layers may be diffusion bonded to each other.