A mobile phase including a lithium salt flows through a stationary phase including an oxygenated metal compound with affinity to the lithium salt through a Lewis acid-Lewis base interaction so that the oxygenated metal compound captures the lithium salt through the Lewis acid-Lewis base interaction. An eluent flows through the stationary phase to release the lithium salt captured by the oxygenated metal compound into the eluent. The eluent includes a Lewis base or a Lewis acid that disrupts the Lewis acid-Lewis base interaction between the lithium salt and the oxygenated metal compound. The eluent including the released lithium salt is collected after the eluent flows through the stationary phase.

Provided are an apparatus and a method for refining pyrolysis oil in which a dechlorination reaction is performed at a first temperature under a first hydrotreating catalyst, denitrification reaction is performed at a second temperature higher than the first temperature under a second hydrotreating catalyst, and chlorine adsorption by an adsorbent is performed after the dechlorination reaction, thereby preventing production of an ammonium salt (NH.sub.4Cl), and providing refined oil which is excellent in prevention of corrosion of a reactor, improvement of durability, occurrence of differential pressure, and process efficiency, has very low contents of impurities such as chlorine, nitrogen, and metal and olefin, and has excellent quality.

An ion exchange resin rejuvenation system includes a vessel, a source of a first cleaning solution including an enzyme fluidly connected to the vessel, a source of a second cleaning solution fluidly connected to the vessel, a source of rinse solution connected to the vessel, and a source of a resin regeneration solution fluidly connected to the vessel.

A method of producing lithium phosphate from a lithium source includes the step of (a) concentrating the lithium to produce a lithium concentrate, with an ion exchange sorbent, and (b) reacting the lithium concentrate with phosphate anions to produce lithium phosphate. The lithium phosphate may then be converted to lithium hydroxide or lithium 5 carbonate by reaction with calcium hydroxide or by electrolysis.

A method for reducing a contaminating DNA content of a preparation containing AAV capsids and contaminating DNA, comprising the steps of a) Performing an extraction of DNA with a solid phase bearing positive charges at its surface said solid phase is contacted with the preparation at a pH of 7.0±1.0, and a salt concentration of 10 mM to 200 mM yielding a first fraction, (b) Diafiltering the first fraction by a first tangential flow filtration to obtain a second fraction, (c) Treating the second fraction with DNase, (d) Diafiltering the DNase treated second fraction obtained by step c) by a second tangential flow, (e) filtration to a buffer with pH of 7.0±1.0, and a salt concentration of 10 mM to 20 mM to yield a third fraction, and optionally (f) Concentrating the third fraction by tangential flow filtration before supplemental chromatography.

A system for the treatment of a liquid plastic-derived oil having a pretreating section that includes a pretreating system having one or more reactors that may receive the liquid plastic-derived oil having one or more contaminants and a first contamination level. The one or more reactors includes a sorbent material having a faujasite (FAU) crystal framework type zeolitic molecular sieve and that may remove a first portion of the one or more contaminants from the liquid plastic-derived oil and generate a treated liquid plastic-derived oil having a second contamination level that is less than the first contamination level. The liquid plastic-derived oil is derived from a solid plastic waste (SPW), and the first portion of the one or more contaminants includes a halogen.

An apparatus and method for softening water are provided. The water softening system comprises a water softener apparatus comprising a tank designed to contain a resin bed and a water softener head coupled to the tank. The water softener head comprises at least one inlet, at least one outlet, a first channel in fluid communication with the first outlet, and a second channel in fluid communication with the first inlet. The water softening system includes at least one inlet water line for hard water and one outlet water line for softened water. A controller is provided and is configured to detect a first operating state of the water softening system, monitor the performance of the water softening system, and send instructions to at least one of the first valve and the second valve to change from a first operational state to a second operational state.

A purification system for separating a molecule of interest from a solution is provided and generally includes a plurality of resin processing sections, wherein each of the resin processing sections is controllably separated from each other via a configurable valve, wherein the configurable valve is configured to introduce or evacuate a fluid/resin into/out of a proximately located processing section, a plurality of inlets configured to introduce fluid and/or resin into one or more of the plurality of resin processing sections.

The invention relates to a new process for the purification of oligonucleotides which comprises the removal of an acid labile 5′hydroxy protecting group at the 5′-O-oligonucleotide terminus of the oligonucleotide by means of an on-column de-protection with an acid.

An alternating cascaded system for high-salinity wastewater treatment includes a pollutant removal system and an alternating cascaded water conveyance system embedded in the pollutant removal system. The pollutant removal system includes four partition plates, a pollutant removal zone and a discharge sump; and the alternating cascaded water conveyance system includes feed water distribution channels disposed under a feed water conveyer pipe and on an outer wall of a first pollutant removal subzone, cleaning water distribution channels disposed on an outer wall of a third pollutant removal subzone and located under a cleaning water pipe, and a purified water discharge pipe and a cleaning water discharge pipe that are located in the discharge sump and axially have a same discharge direction from top to bottom.