Disclosed is an oxidation process to produce a crude carboxylic acid product carboxylic acid product. The process comprises oxidizing a feed stream comprising at least one oxidizable compound to generate a crude carboxylic acid slurry comprising furan-2,5-dicarboxylic acid (FDCA) and compositions thereof. Also disclosed is a process to produce a dry purified carboxylic acid product by utilizing various purification methods on the crude carboxylic acid.

Methods of priming a plasma processing system are disclosed. The plasma processing system has a number of different fluid flow circuits that are defined by sources of fluid, fluid flow paths, waste containers, a mixer, a separator, valves and a pump. A first fluid circuit is flushed, where the first fluid circuit is defined by a source of a first fluid, a first valve positioned between the source of the first fluid and the first fluid flow path, a second valve positioned between the first fluid flow path and the second fluid flow path, a first pump positioned between the second fluid flow path and the third fluid flow path, and a first waste container in fluid communication with the third fluid flow path. A second fluid circuit is then flushed by closing and opening certain valves.

The present specification discloses plasma processing systems that include a number of different fluid flow circuits that are defined by sources of fluid, fluid lines, fluid flow paths, waste containers, a mixer, a separator, valves, and a pump. The systems also include a connector tube and a solvent extraction device, wherein the connector tube and solvent extraction device are configured to be alternatively inserted in a same position along a fluid flow line. In addition, the systems include a controller that is configured to execute a plurality of programmatic instructions to open and close each of a first fluid flow line valve, a second fluid flow line valve, a third fluid flow line valve, and a fourth fluid flow line valve in a predetermined sequence to either enable or prevent a flow of fluid through various fluid flow lines.

The present specification discloses plasma processing systems that include a number of different fluid flow circuits that are defined by sources of fluid, fluid lines, fluid flow paths, waste containers, a mixer, a separator, valves, and a pump. The systems also include a connector tube and a solvent extraction device, wherein the connector tube and solvent extraction device are configured to be alternatively inserted in a same position along a fluid flow line. In addition, the systems include a controller that is configured to execute a plurality of programmatic instructions to open and close each of a first fluid flow line valve, a second fluid flow line valve, a third fluid flow line valve, and a fourth fluid flow line valve in a predetermined sequence.

A supercritical water separation process and system is disclosed for the removal of metals, minerals, particulate, asphaltenes, and resins from a contaminated organic material. The present invention takes advantage of the physical and chemical properties of supercritical water to effect the desired separation of contaminants from organic materials and permit scale-up. At a temperature and pressure above the critical point of water (374 C., 22.1 MPa), nonpolar organic compounds become miscible in supercritical water (SCW) and polar compounds and asphaltenes become immiscible. The process and system disclosed continuously separates immiscible contaminants and solids from the supercritical water and clean oil product solution. The present invention creates a density gradient that enables over 95% recovery of clean oil and over 99% reduction of contaminants such as asphaltenes and particulate matter depending on the properties of the contaminated organic material.

A process is provided for removing a heavy polynuclear aromatic (HPNA) compound from a hydrocarbon oil. The process includes contacting the hydrocarbon oil containing the HPNA compound with a lean hydrocarbon-immiscible liquid stream to produce a mixture comprising the hydrocarbon oil and a rich hydrocarbon-immiscible liquid containing the HPNA compound; and separating the mixture to produce a hydrocarbon oil effluent having a reduced level of the HPNA compound and a hydrocarbon-immiscible liquid effluent containing the HPNA compound. The hydrocarbon-immiscible liquid can be a halometallate ionic liquid, a liquid coordination complex, or a combination thereof.

Provided is a method of inhibiting degradation of an extractant by an anhydrous environment avoiding and metal stripping, the method including the steps of: (a) stopping the addition of soda ash (Na.sub.2CO.sub.3) to an extracting reaction tank; (b) starting solution recirculation and stopping solvent recirculation of a settler; (c) supplying a solvent from a loaded organic tank to a scrubbing reaction tank, in which the scrubbing reaction tank, stripping reaction tank and extracting reaction tank are connected for circulation and operating stirrers of the scrubbing reaction tank, stripping reaction tank and extracting reaction tank; (d) supplying a sulfuric acid solution having a controlled concentration with a diluting solution to the stripping reaction tank; (e) transferring the solvents of the settler, the loaded organic tank and all the pipes to the scrubbing reaction tank; and (f) stopping the step (e) and initiating solvent recirculation.

The invention relates to a process for purifying a lithium bis(fluorosulfonyl)imide salt. The present invention relates to a process for purifying a lithium bis(fluorosulfonyl)imide salt in a solution in at least one solvent S1, said process comprising at least one purification step carried out in:a piece of silicon carbide-based or fluorinated polymer-based equipment; ora piece of metal or glass equipment comprising an inner surface, said inner surface, which can come into contact with the lithium bis(fluorosulfonyl)imide salt, being covered with a polymer coating or with a silicon carbide coating.

The present invention relates to a method for the chlorination of a sucrose-6-acylate to produce a 4,1,6-trichloro-4,1,6-trideoxy-galactosucrose-6-acylate wherein said method includes steps of: (i) combining the sucrose-6-acylate with a chlorinating agent in a reaction vehicle comprising a tertiary amide to afford a mixture; (ii) heating said mixture for a heating period in order to provide chlorination of sucrose-6-acylate at the 4,1 and 6 positions thereof; and (iii) quenching the product stream of (ii) to produce a 4,1,6-trichloro-4,1,6-trideoxy-galactosucrose-6-acylate;
wherein before said quenching, a portion of said tertiary amide is removed by extraction into a solvent in which said tertiary amide is at least partially soluble.

Disclosed is an oxidation process to produce a crude carboxylic acid product carboxylic acid product. The process comprises oxidizing a feed stream comprising at least one oxidizable compound to generate a crude carboxylic acid slurry comprising furan-2,5-dicarboxylic acid (FDCA) and compositions thereof. Also disclosed is a process to produce a dry purified carboxylic acid product by utilizing various purification methods on the crude carboxylic acid.