A portable fluidic platform for rapid and flexible end-to-end production of recombinant protein biologics includes a bioreactor system hosting stable and robust cell-free translation systems that is fluidically integrated with modular protein separation functionalities (e.g., size exclusion, ion exchange or affinity chromatography systems) for purification of the cell-free expressed product and which are configurable for process-specific isolation of different proteins, as well as for formulation. The bioreactor utilizes lysates from engineered eukaryotic (e.g., yeast) or prokaryotic (e.g., bacterial) strains that contain factors for protein folding and posttranslational modifications. Combination of various purification modules on the same fluidic platform allows flexibility of re-routing for purification of different proteins depending on specific target requirements. Protein synthesis and purification modules are integrated into self-contained disposable fluidic cartridge that eliminates cross-contamination between runs. The platform allows for flexible production of protein biologics within 24 hours (from DNA to purified product).

The present disclosure discloses a 1-carboxy-2-hydroxy-3-iminopropane and an extraction method thereof, and belongs to the technical fields of food, health food and medicine. A method for extracting the 1-carboxy-2-hydroxy-3-iminopropane of the present disclosure includes the following steps: (1) adding a diaphragma juglandis fructus powder into an ethanol solution for extraction and filtration to obtain a supernatant, and conducting concentration on the supernatant under reduced pressure to obtain a walnut alcohol extract; (2) adding a filter residue of step (1) into water for extraction and filtration to obtain a supernatant, and conducting concentration on the supernatant under reduced pressure to obtain a walnut water extract; and (3) mixing the walnut alcohol extract and the water extract to obtain a diaphragma juglandis fructus mixed extract, sequentially conducting elution through an AB-8 type macroporous resin column, an MCI column and an ODS column, and conducting separation to obtain a precipitate, namely the 1-carboxy-2-hydroxy-3-iminopropane. In the present disclosure, the 1-carboxy-2-hydroxy-3-iminopropane in diaphragma juglandis fructus is found for the first time and has great sedation and hypnosis activity.

A method for simultaneous determination of nitrogen and oxygen isotope compositions of natural nitrate and nitrite, which quantitatively converts natural nitrate and nitrite into an organic ester and a nitro-compounds respectively, and then nitrate and nitrite δ.sup.18O and δ.sup.15N are simultaneously determined by adopting a gas chromatography/pyrolysis/gas chromatography/isotope ratio mass spectrometry coupling technology (GC/Py/GC/IRMS). According to the method for simultaneously determining the nitrogen and oxygen isotope compositions of the natural nitrate salt and nitrite salt, the small amount of sample does not result in the loss, acquisition, exchange and fractionation of nitrogen and oxygen.

A solvent supply for a chromatography system includes a mobile phase drive and a separation unit. The mobile phase drive is configured for driving a mobile phase through the separation unit, and the separation unit is configured for chromatographically separating compounds of a sample fluid in the mobile phase. The solvent supply comprises a tubing having a tubing end configured to couple to a solvent container to supply solvent contained in the solvent container via the tubing to the chromatography system. The tubing is configured in a flexible manner to allow the tubing end to be movable. A tubing arm supports the tubing to allow positioning the tubing end into a first resting position, such that the tubing end is at least substantially held in position and distantly situated beyond a reference to prevent physical contact with the reference.

A solvent supply for a chromatography system includes a mobile phase drive and a separation unit. The mobile phase drive is configured for driving a mobile phase through the separation unit, and the separation unit is configured for chromatographically separating compounds of a sample fluid in the mobile phase. The solvent supply comprises a tubing having a tubing end configured to couple to a solvent container to supply solvent contained in the solvent container via the tubing to the chromatography system. The tubing is configured in a flexible manner to allow the tubing end to be movable. A tubing arm supports the tubing to allow positioning the tubing end into a first resting position, such that the tubing end is at least substantially held in position and distantly situated beyond a reference to prevent physical contact with the reference.

Example implementations relate to techniques for thermal fluid conditioning and delivery. A technique may involve coupling a container of heat transfer fluid to an input and removing moisture from the heat transfer fluid via a molecular sieve. A pressure source is configured to push the heat transfer fluid out of the container and through the molecular sieve. Subsequent to removing the moisture from the heat transfer fluid, the technique involves separating, via an orifice coupled to a tank, the heat transfer fluid into liquid and gas particles within the tank and removing, via a vacuum coupled to the tank, the gas particles from the tank. The liquid can then be supplied into a fluid system via additional pressure by the pressure source. The technique may be performed by a portable device that houses the various components used to condition and delivery the thermal fluid.

This invention relates generally to a process for selective adsorption and recovery of lithium from natural and synthetic brines, and more particular to a process for recovering lithium from a natural or synthetic brine solution by passing the brine solution through a lithium selective adsorbent in a continuous countercurrent adsorption and desorption circuit.

Disclosed herein is a method for obtaining compounds and compositions from plant and fungus materials by thermal treatment, affinity capture, filtration, and release through multi-phasic transitions between gas, solid, and liquid states. The compounds of interest are obtained by manipulating the temperature and pressure of the heating chamber. The compounds in gas phase are passed through an affinity medium which captures the compounds of interest in either solid or liquid phase by exposing the compound of interest to the localized micro-affinity environment of the medium. The compounds are separated from the medium using direct competition with solvent or buffers optimized for the specific chemical properties of compounds.

Disclosed herein is a method for obtaining compounds and compositions from plant and fungus materials by thermal treatment, affinity capture, filtration, and release through multi-phasic transitions between gas, solid, and liquid states. The compounds of interest are obtained by manipulating the temperature and pressure of the heating chamber. The compounds in gas phase are passed through an affinity medium which captures the compounds of interest in either solid or liquid phase by exposing the compound of interest to the localized micro-affinity environment of the medium. The compounds are separated from the medium using direct competition with solvent or buffers optimized for the specific chemical properties of compounds.

The disclosure describes a method for simultaneous determination of nitrogen and oxygen isotope compositions of natural nitrate and nitrite, which quantitatively converts natural nitrate and nitrite into an organic ester and a nitro-compounds respectively, and then nitrate and nitrite δ.sup.18O and δ.sup.15N are simultaneously determined by adopting a gas chromatography/pyrolysis/gas chromatography/isotope ratio mass spectrometry coupling technology (GC/Py/GC/IRMS). According to the method for simultaneously determining the nitrogen and oxygen isotope compositions of the natural nitrate salt and nitrite salt, the small amount of sample does not result in the loss, acquisition, exchange and fractionation of nitrogen and oxygen.