Provided is a first process of producing an anhydride of an organic mono-acid comprising performing a transanhydridization reaction of an organic mono-acid and a thermally regenerable anhydride to produce the anhydride of the organic mono-acid and an acid of the thermally regenerable anhydride, wherein at least one of the organic mono-acid and thermally regenerable anhydride is provided by a preprocess that is integrated with the first process. An anhydride production system that is integrated with at least one preprocess, a wood acetylation process coupled to an acetic anhydride production process, a process of supplying an acetic acid reactant feed to a transanhydridization reaction unit, and an integrated wood acetylation and anhydride production system also are provided.

Provided is a first process of producing an anhydride of an organic mono-acid comprising performing a transanhydridization reaction of an organic mono-acid and a thermally regenerable anhydride to produce the anhydride of the organic mono-acid and an acid of the thermally regenerable anhydride, wherein at least one of the organic mono-acid and thermally regenerable anhydride is provided by a preprocess that is integrated with the first process. An anhydride production system that is integrated with at least one preprocess, a wood acetylation process coupled to an acetic anhydride production process, a process of supplying an acetic acid reactant feed to a transanhydridization reaction unit, and an integrated wood acetylation and anhydride production system also are provided.

The invention relates to a process for distillative removal of a unsaturated carboxylic anhydride of the general formula (I) R—C(O)—O—C—(O)—R in which R is an unsaturated organic radical having 2 to 12 carbon atoms, wherein said unsaturated carboxylic anhydride is discharged in gaseous form from a sidestream take-off and is condensed in an atomized liquid circulating stream of said unsaturated carboxylic anhydride.

The invention relates to a process for distillative removal of a unsaturated carboxylic anhydride of the general formula (I) R—C(O)—O—C—(O)—R in which R is an unsaturated organic radical having 2 to 12 carbon atoms, wherein said unsaturated carboxylic anhydride is discharged in gaseous form from a sidestream take-off and is condensed in an atomized liquid circulating stream of said unsaturated carboxylic anhydride.

The invention relates to a process for distillative removal of a unsaturated carboxylic anhydride of the general formula (I) R—C(O)—O—C—(O)—R in which R is an unsaturated organic radical having 2 to 12 carbon atoms, wherein said unsaturated carboxylic anhydride is discharged in gaseous form from a sidestream take-off and is condensed in an atomized liquid circulating stream of said unsaturated carboxylic anhydride.

The present invention concerns a process for manufacturing a fraction comprising carboxylic acid anhydride by reaction of a fraction comprising carboxylic acid with a ketene, and the use of the fraction comprising carboxylic acid anhydride in a process for acylation of polysaccharides.

The present invention concerns a process for manufacturing a fraction comprising carboxylic acid anhydride by reaction of a fraction comprising carboxylic acid with a ketene, and the use of the fraction comprising carboxylic acid anhydride in a process for acylation of polysaccharides.

A method for chemical separation of cannabinoids includes: (i) providing a starting organic solvent solution that contains a mixture of cannabinoid acids, (ii) using an aqueous basic solution to remove a portion of the cannabinoid acids from the mixture of cannabinoid acids in the starting organic solvent solution by converting the portion of the cannabinoid acids to cannabinoid carboxylate salts that solubilize in the an aqueous basic solution, (iii) separating the aqueous basic solution in (ii) from the starting organic solvent, (iv) combining the aqueous solution from (iii) with new organic solvent to produce a combined solution, (v) acidifying the combined solution to extract the cannabinoid acids from the aqueous solution to the organic solvent, (vi) separating the organic solvent of (v) from the aqueous solution, and (vii) evaporating the organic solvent of (vi) to leave product cannabinoid acids.

Methods and systems for separating a desublimatable compound from hydrocarbons is disclosed. A feed fluid stream, consisting of a hydrocarbon and a desublimatable compound, is passed into an upper chamber of a vessel. The feed fluid stream is cooled in the upper chamber, thereby desublimating a portion of the desublimatable compound out of the feed liquid stream to form a product gas stream and a desublimatable compound snow which is collected in the lower chamber of the vessel. A lower portion of the desublimatable compound snow is melted to form a liquid desublimatable compound stream such that an upper portion of the solid desublimatable compound snow remains as an insulative barrier between the upper chamber and the liquid desublimatable compound stream. The liquid desublimatable compound stream is removed at a rate that matches a production rate of the solid desublimatable compound snow, thereby maintaining the insulative barrier.

The present invention relates to a process for the preparation of halogenated carboxylic anhydrides, e.g. for the preparation of trifluoroacetic anhydride. The preparation is achieved by reacting a halogenated carboxylic acid, e.g. trifluoroacetic acid, with sulfuric acid, oleum and/or disulfuric acid.