A synergistic polymerization inhibitor composition, the composition having a copper salt, and a manganese salt; a copper salt or a manganese salt, and a cationic polymer; or a phenothiazine and a manganese salt. A method for inhibiting polymerization of unsaturated polymerizable monomers, the method providing adding a synergistic polymerization inhibitor composition to an methacrylic acid manufacturing system or component thereof, the composition having a copper salt, and a manganese salt; a copper salt or a manganese salt, and a cationic polymer; or a phenothiazine and a manganese salt.

A process for making a high purity salt comprises the steps of providing an organic compound, providing a metal salt, adding the metal salt and organic compound to an aqueous medium, heating the reaction mixture to react the organic compound and the metal salt to form an organic salt, collecting the organic salt, and directly contacting the collected organic salt with a heated gas stream while agitating the collected organic salt to reduce the moisture content of the dried organic salt to about 7% or less.

A process for making a high purity salt comprises the steps of providing an organic compound, providing a metal salt, adding the metal salt and organic compound to an aqueous medium, heating the reaction mixture to react the organic compound and the metal salt to form an organic salt, collecting the organic salt, and directly contacting the collected organic salt with a heated gas stream while agitating the collected organic salt to reduce the moisture content of the dried organic salt to about 7% or less.

The purpose of the present invention is to provide a method for producing a 3-hydroxy-3-methylbutyrate or salt thereof, the method being capable of efficiently producing a highly pure 3-hydroxy-3-methylbutyrate or salt thereof. The highly pure 3-hydroxy-3-methylbutyrate or salt thereof can be efficiently produced by performing at least one of the following operations (a) to (d) on a solution containing 3-hydroxy-3-methylbutyrate and impurities exposed to environments of pH 6.0 or less. (a) Hypochlorous acid or salt thereof is added to the solution. (b) The solution is maintained at 40 to 200° C. for 30 minutes or more, provided that the solution contains hypochlorous acid or salt thereof. (c) Calcium salt is added to the solution, and the precipitated calcium 2,3-dihydroxy-3-methylbutanoate is separated from the liquid phase in which 3-hydroxy-3-methylbutyrate and/or the salt is dissolved. (d) A base is added to the solution to separate the liquid phase in which the salt of 2,3-dihydroxy-3-methylbutanoic acid formed is dissolved and the liquid phase in which 3-hydroxy-3-methylbutyrate and/or salt thereof is dissolved.

The purpose of the present invention is to provide a method for producing a 3-hydroxy-3-methylbutyrate or salt thereof, the method being capable of efficiently producing a highly pure 3-hydroxy-3-methylbutyrate or salt thereof. The highly pure 3-hydroxy-3-methylbutyrate or salt thereof can be efficiently produced by performing at least one of the following operations (a) to (d) on a solution containing 3-hydroxy-3-methylbutyrate and impurities exposed to environments of pH 6.0 or less. (a) Hypochlorous acid or salt thereof is added to the solution. (b) The solution is maintained at 40 to 200° C. for 30 minutes or more, provided that the solution contains hypochlorous acid or salt thereof. (c) Calcium salt is added to the solution, and the precipitated calcium 2,3-dihydroxy-3-methylbutanoate is separated from the liquid phase in which 3-hydroxy-3-methylbutyrate and/or the salt is dissolved. (d) A base is added to the solution to separate the liquid phase in which the salt of 2,3-dihydroxy-3-methylbutanoic acid formed is dissolved and the liquid phase in which 3-hydroxy-3-methylbutyrate and/or salt thereof is dissolved.

The purpose of the present invention is to provide a method for producing a 3-hydroxy-3-methylbutyrate or salt thereof, the method being capable of efficiently producing a highly pure 3-hydroxy-3-methylbutyrate or salt thereof. The highly pure 3-hydroxy-3-methylbutyrate or salt thereof can be efficiently produced by performing at least one of the following operations (a) to (d) on a solution containing 3-hydroxy-3-methylbutyrate and impurities exposed to environments of pH 6.0 or less. (a) Hypochlorous acid or salt thereof is added to the solution. (b) The solution is maintained at 40 to 200° C. for 30 minutes or more, provided that the solution contains hypochlorous acid or salt thereof. (c) Calcium salt is added to the solution, and the precipitated calcium 2,3-dihydroxy-3-methylbutanoate is separated from the liquid phase in which 3-hydroxy-3-methylbutyrate and/or the salt is dissolved. (d) A base is added to the solution to separate the liquid phase in which the salt of 2,3-dihydroxy-3-methylbutanoic acid formed is dissolved and the liquid phase in which 3-hydroxy-3-methylbutyrate and/or salt thereof is dissolved.

Provided herein are methods of producing acrylic acid from beta-propiolactone. Such methods may involve the use of a heterogeneous catalyst, such as a zeolite.

Provided herein are methods of producing acrylic acid from beta-propiolactone. Such methods may involve the use of a heterogeneous catalyst, such as a zeolite.

The present invention relates to methods of extracting cannabinoid acids from cannabis plant material by combining the plant material with an aqueous solution having a high pH to solubilize cannabinoid acid anions, followed by precipitation of the cannabinoid acids at low pH and filtration. The method provides yields of up to 97%, while high pH purification of ethanol extracted oils yielded purities up to 86%.

The present invention relates to methods of extracting cannabinoid acids from cannabis plant material by combining the plant material with an aqueous solution having a high pH to solubilize cannabinoid acid anions, followed by precipitation of the cannabinoid acids at low pH and filtration. The method provides yields of up to 97%, while high pH purification of ethanol extracted oils yielded purities up to 86%.