The present invention relates to a process for treating aqueous effluents containing formaldehyde by distillation in the presence of acetic acid, in particular to a process for treating aqueous solutions resulting from the synthesis of acrylic acid. The invention also relates to the use of the purified aqueous solution in a process for producing acrylic acid by catalytic oxidation of propylene and/or propane in steam dilution.

The present invention relates to a process for treating aqueous effluents containing formaldehyde by distillation in the presence of acetic acid, in particular to a process for treating aqueous solutions resulting from the synthesis of acrylic acid. The invention also relates to the use of the purified aqueous solution in a process for producing acrylic acid by catalytic oxidation of propylene and/or propane in steam dilution.

The present invention relates to a process for treating aqueous effluents containing formaldehyde by distillation in the presence of acetic acid, in particular to a process for treating aqueous solutions resulting from the synthesis of acrylic acid. The invention also relates to the use of the purified aqueous solution in a process for producing acrylic acid by catalytic oxidation of propylene and/or propane in steam dilution.

A production process of acetic acid according to the present invention inhibits concentration of hydrogen iodide and improves a liquid-liquid separation of an overhead from a distillation column. Acetic acid is produced by distilling a mixture containing hydrogen iodide, water, acetic acid and methyl acetate in a first distillation column (3) to form an overhead and a side cut stream or bottom stream containing acetic acid, cooling and condensing the overhead in a condenser (C3) to form separated upper and lower phases in a decanter (4). According to this process, a zone having a high water concentration is formed in the distillation column above the feed position of the mixture by feeding a mixture having a water concentration of not less than an effective amount to not more than 5% by weight (e.g., 0.5 to 4.5% by weight) and a methyl acetate concentration of 0.5 to 9% by weight (e.g., 0.5 to 8% by weight) as the mixture to the distillation column and distilling the mixture. In the zone having a high water concentration, hydrogen iodide is allowed to react with methyl acetate to produce methyl iodide and acetic acid.

A production process of acetic acid according to the present invention inhibits concentration of hydrogen iodide and improves a liquid-liquid separation of an overhead from a distillation column. Acetic acid is produced by distilling a mixture containing hydrogen iodide, water, acetic acid and methyl acetate in a first distillation column (3) to form an overhead and a side cut stream or bottom stream containing acetic acid, cooling and condensing the overhead in a condenser (C3) to form separated upper and lower phases in a decanter (4). According to this process, a zone having a high water concentration is formed in the distillation column above the feed position of the mixture by feeding a mixture having a water concentration of not less than an effective amount to not more than 5% by weight (e.g., 0.5 to 4.5% by weight) and a methyl acetate concentration of 0.5 to 9% by weight (e.g., 0.5 to 8% by weight) as the mixture to the distillation column and distilling the mixture. In the zone having a high water concentration, hydrogen iodide is allowed to react with methyl acetate to produce methyl iodide and acetic acid.

A production process of acetic acid according to the present invention inhibits concentration of hydrogen iodide and improves a liquid-liquid separation of an overhead from a distillation column. Acetic acid is produced by distilling a mixture containing hydrogen iodide, water, acetic acid and methyl acetate in a first distillation column (3) to form an overhead and a side cut stream or bottom stream containing acetic acid, cooling and condensing the overhead in a condenser (C3) to form separated upper and lower phases in a decanter (4). According to this process, a zone having a high water concentration is formed in the distillation column above the feed position of the mixture by feeding a mixture having a water concentration of not less than an effective amount to not more than 5% by weight (e.g., 0.5 to 4.5% by weight) and a methyl acetate concentration of 0.5 to 9% by weight (e.g., 0.5 to 8% by weight) as the mixture to the distillation column and distilling the mixture. In the zone having a high water concentration, hydrogen iodide is allowed to react with methyl acetate to produce methyl iodide and acetic acid.

The present disclosure provides a method for extracting alpha-ketoglutarate and pyruvate simultaneously from microbial fermentation broth or enzyme transformation solution, which is related to the technical field of biological separation and extraction. The method comprises the following steps: centrifuging the microbial fermentation broth or enzymatic conversion solution containing α-KG and PA to remove the cells and other visible solids; removing the macromolecular impurities by ultrafiltration; evaporating and concentrating under reduced pressure conditions; extracting with the water-insoluble extraction after acidification; separating crude crystals of α-KG and crude liquid of PA by evaporation crystallization method (if concentration of PA is great higher than that of α-KG, crystallization separation should be conducted after distilling partial pure pyruvate); washing the crude crystal of α-KG with water-insoluble organic solvent as ethyl acetate or butyl acetate, drying and crushing to obtain qualified α-KG; distilling to gain qualified PA product applying high vacuum distillation (or molecular distillation).

The present disclosure provides a method for extracting alpha-ketoglutarate and pyruvate simultaneously from microbial fermentation broth or enzyme transformation solution, which is related to the technical field of biological separation and extraction. The method comprises the following steps: centrifuging the microbial fermentation broth or enzymatic conversion solution containing α-KG and PA to remove the cells and other visible solids; removing the macromolecular impurities by ultrafiltration; evaporating and concentrating under reduced pressure conditions; extracting with the water-insoluble extraction after acidification; separating crude crystals of α-KG and crude liquid of PA by evaporation crystallization method (if concentration of PA is great higher than that of α-KG, crystallization separation should be conducted after distilling partial pure pyruvate); washing the crude crystal of α-KG with water-insoluble organic solvent as ethyl acetate or butyl acetate, drying and crushing to obtain qualified α-KG; distilling to gain qualified PA product applying high vacuum distillation (or molecular distillation).

The present disclosure provides a method for extracting alpha-ketoglutarate and pyruvate simultaneously from microbial fermentation broth or enzyme transformation solution, which is related to the technical field of biological separation and extraction. The method comprises the following steps: centrifuging the microbial fermentation broth or enzymatic conversion solution containing α-KG and PA to remove the cells and other visible solids; removing the macromolecular impurities by ultrafiltration; evaporating and concentrating under reduced pressure conditions; extracting with the water-insoluble extraction after acidification; separating crude crystals of α-KG and crude liquid of PA by evaporation crystallization method (if concentration of PA is great higher than that of α-KG, crystallization separation should be conducted after distilling partial pure pyruvate); washing the crude crystal of α-KG with water-insoluble organic solvent as ethyl acetate or butyl acetate, drying and crushing to obtain qualified α-KG; distilling to gain qualified PA product applying high vacuum distillation (or molecular distillation).

A method for purification and extraction of cannabinoids includes: providing a cannabis oil including phospholipids and cannabinoid acids; contacting the cannabis oil with a degumming solvent, wherein the degumming solvent and cannabis oil are substantially immiscible; and separating an aqueous phase including the degumming solvent and at least a portion of the phospholipids from an oil phase including the cannabis oil. The method may further include contacting the oil phase with an extraction solvent, where the extraction solvent and oil phase are substantially immiscible; and separating an aqueous phase including the extraction solvent and at least a portion of the cannabinoid acids from a second oil solvent phase including the oil phase and/or simply the liberated cannabinoids following acidification of the extraction solvent.