A method for manufacturing 1,4-bis(4-phenoxybenzoyl)benzene, including: reacting terephthaloyl chloride with diphenyl ether in a reaction solvent and in the presence of a Lewis acid, so as to obtain a product mixture including a 1,4-bis(4-phenoxybenzoyl)benzene-Lewis acid complex; contacting the product mixture with a protic solvent, so as to obtain a first phase containing the Lewis acid and a second phase containing 1,4-bis(4-phenoxybenzoyl)benzene; heating at least the second phase up to a maximum temperature, followed by cooling the second phase down to a separation temperature; subjecting at least the second phase to a solid/liquid separation step at the separation temperature, so as to recover solid 1,4-bis(4-phenoxybenzoyl)benzene.

Methods of purifying crude 4-hydroxyacetophenone using one or more solvents as well as products comprising or consisting of crystallized 4-hydroxyacetophenone and one, two or more solvent(s). The products may be obtained or obtainable from the methods for purifying crude 4-hydroxyacetophenone.

Methods of purifying crude 4-hydroxyacetophenone using one or more solvents as well as products comprising or consisting of crystallized 4-hydroxyacetophenone and one, two or more solvent(s). The products may be obtained or obtainable from the methods for purifying crude 4-hydroxyacetophenone.

Methods of purifying crude 4-hydroxyacetophenone using one or more solvents as well as products comprising or consisting of crystallized 4-hydroxyacetophenone and one, two or more solvent(s). The products may be obtained or obtainable from the methods for purifying crude 4-hydroxyacetophenone.

Methods and systems for preparing acetone from cumene hydroperoxide (CHP) are disclosed. The methods and systems involve an acetone purification column configured to separate acetone from other components of the product/reactant stream. The acetone purification column is equipped with a side draw configured to route a portion of the column contents to a caustic treating vessel where the contents are reacted with a dilute aqueous alkaline solution to remove aldehydes from the acetone product. The contents of the caustic treating vessel are then routed back to the acetone purification column. Using a separate caustic treating vessel for the aldehydes removal provides increased contact time between the acetone product and the alkaline solution, thereby affording greater aldehydes removal.

Methods and systems for preparing acetone from cumene hydroperoxide (CHP) are disclosed. The methods and systems involve an acetone purification column configured to separate acetone from other components of the product/reactant stream. The acetone purification column is equipped with a side draw configured to route a portion of the column contents to a caustic treating vessel where the contents are reacted with a dilute aqueous alkaline solution to remove aldehydes from the acetone product. The contents of the caustic treating vessel are then routed back to the acetone purification column. Using a separate caustic treating vessel for the aldehydes removal provides increased contact time between the acetone product and the alkaline solution, thereby affording greater aldehydes removal.

An example method for extracting phytochemical oil from plant parts includes freezing plant parts from at least one of Cannabis sativa, Curcuma longa, Panax ginseng, and Panax quinquefolius. The frozen plant parts are reduced to a plant powder, which is suspended in an aqueous buffer. The aqueous buffer containing the suspended plant powder is incubated with at least one pectinase and at least one cellulase. An aqueous phase of the incubated aqueous buffer is evaporated through steam heating to obtain a steam dried product. Phytochemical oil, which includes at least one of cannabinoids, curcuminoids, and ginsenosides, is extracted from the steam dried product.

An example method for extracting phytochemical oil from plant parts includes freezing plant parts from at least one of Cannabis sativa, Curcuma longa, Panax ginseng, and Panax quinquefolius. The frozen plant parts are reduced to a plant powder, which is suspended in an aqueous buffer. The aqueous buffer containing the suspended plant powder is incubated with at least one pectinase and at least one cellulase. An aqueous phase of the incubated aqueous buffer is evaporated through steam heating to obtain a steam dried product. Phytochemical oil, which includes at least one of cannabinoids, curcuminoids, and ginsenosides, is extracted from the steam dried product.

An example method for extracting phytochemical oil from plant parts includes freezing plant parts from at least one of Cannabis sativa, Curcuma longa, Panax ginseng, and Panax quinquefolius. The frozen plant parts are reduced to a plant powder, which is suspended in an aqueous buffer. The aqueous buffer containing the suspended plant powder is incubated with at least one pectinase and at least one cellulase. An aqueous phase of the incubated aqueous buffer is evaporated through steam heating to obtain a steam dried product. Phytochemical oil, which includes at least one of cannabinoids, curcuminoids, and ginsenosides, is extracted from the steam dried product.

Methods of purifying crude 4-hydroxyacetophenone using one or more solvents as well as products comprising or consisting of crystallized 4-hydroxyacetophenone and one, two or more solvent(s). The products may be obtained or obtainable from the methods for purifying crude 4-hydroxyacetophenone.