Embodiments of the present disclosure generally relate to processes for converting disulfides to conversion products and to processes for producing cysteic acid. In an embodiment, a process for converting cystine to a conversion product is provided. The process include introducing an organic peroxide and water to cystine to form a mixture. The process further includes reacting the mixture, under conversion conditions, to form the conversion product, wherein the conversion product comprises cysteic acid, an amount of cysteic acid in the conversion product is greater than about 90 wt % based on a total weight of the conversion product, and the conversion conditions comprise a conversion temperature from about 15° C. to about 50° C. The process further includes heating the conversion product to remove the organic peroxide.

Embodiments of the present disclosure generally relate to processes for converting disulfides to conversion products and to processes for producing cysteic acid. In an embodiment, a process for converting cystine to a conversion product is provided. The process include introducing an organic peroxide and water to cystine to form a mixture. The process further includes reacting the mixture, under conversion conditions, to form the conversion product, wherein the conversion product comprises cysteic acid, an amount of cysteic acid in the conversion product is greater than about 90 wt % based on a total weight of the conversion product, and the conversion conditions comprise a conversion temperature from about 15° C. to about 50° C. The process further includes heating the conversion product to remove the organic peroxide.

Embodiments of the present disclosure generally relate to processes for converting disulfides to conversion products and to processes for producing cysteic acid. In an embodiment, a process for converting cystine to a conversion product is provided. The process include introducing an organic peroxide and water to cystine to form a mixture. The process further includes reacting the mixture, under conversion conditions, to form the conversion product, wherein the conversion product comprises cysteic acid, an amount of cysteic acid in the conversion product is greater than about 90 wt % based on a total weight of the conversion product, and the conversion conditions comprise a conversion temperature from about 15° C. to about 50° C. The process further includes heating the conversion product to remove the organic peroxide.

A process for producing a surfactant having two head groups and a single tail group per molecule, including steps of: producing a compound of Formula (1) from ethanol and carbon disulfide; producing a compound of Formula (2) from a carboxylic acid and bromine; producing a compound of Formula (3) from the compound of Formula (2) and methanol; producing a compound of Formula (4) from the compound of Formula (1) and the compound of Formula (3); and producing a compound of Formula (5) from the compound of Formula (4) by a direct oxidation process or by a peracid oxidation process. The surfactant produced by the process has lower critical micelle concentration and enables a lower surface tension of a liquid as compared with prior surfactants with two head groups per molecule, thereby enabling the amount of surfactant required and thus the cost to be substantially reduced.

A process for producing a surfactant having two head groups and a single tail group per molecule, including steps of: producing a compound of Formula (1) from ethanol and carbon disulfide; producing a compound of Formula (2) from a carboxylic acid and bromine; producing a compound of Formula (3) from the compound of Formula (2) and methanol; producing a compound of Formula (4) from the compound of Formula (1) and the compound of Formula (3); and producing a compound of Formula (5) from the compound of Formula (4) by a direct oxidation process or by a peracid oxidation process. The surfactant produced by the process has lower critical micelle concentration and enables a lower surface tension of a liquid as compared with prior surfactants with two head groups per molecule, thereby enabling the amount of surfactant required and thus the cost to be substantially reduced.

Embodiments of the present disclosure generally relate to processes for converting disulfides to conversion products and to processes for producing cysteic acid. In an embodiment, a process for converting cystine to a conversion product is provided. The process include introducing an organic peroxide and water to cystine to form a mixture. The process further includes reacting the mixture, under conversion conditions, to form the conversion product, wherein the conversion product comprises cysteic acid, an amount of cysteic acid in the conversion product is greater than about 90 wt % based on a total weight of the conversion product, and the conversion conditions comprise a conversion temperature from about 15° C. to about 50° C. The process further includes heating the conversion product to remove the organic peroxide.

Embodiments of the present disclosure generally relate to processes for converting disulfides to conversion products and to processes for producing cysteic acid. In an embodiment, a process for converting cystine to a conversion product is provided. The process include introducing an organic peroxide and water to cystine to form a mixture. The process further includes reacting the mixture, under conversion conditions, to form the conversion product, wherein the conversion product comprises cysteic acid, an amount of cysteic acid in the conversion product is greater than about 90 wt % based on a total weight of the conversion product, and the conversion conditions comprise a conversion temperature from about 15° C. to about 50° C. The process further includes heating the conversion product to remove the organic peroxide.

Embodiments of the present disclosure generally relate to processes for converting disulfides to conversion products and to processes for producing cysteic acid. In an embodiment, a process for converting cystine to a conversion product is provided. The process include introducing an organic peroxide and water to cystine to form a mixture. The process further includes reacting the mixture, under conversion conditions, to form the conversion product, wherein the conversion product comprises cysteic acid, an amount of cysteic acid in the conversion product is greater than about 90 wt % based on a total weight of the conversion product, and the conversion conditions comprise a conversion temperature from about 15° C. to about 50° C. The process further includes heating the conversion product to remove the organic peroxide.

A process for producing a surfactant having two head groups and a single tail group per molecule, including steps of: producing a compound of Formula (1) from ethanol and carbon disulfide; producing a compound of Formula (2) from a carboxylic acid and bromine; producing a compound of Formula (3) from the compound of Formula (2) and methanol; producing a compound of Formula (4) from the compound of Formula (1) and the compound of Formula (3); and producing a compound of Formula (5) from the compound of Formula (4) by a direct oxidation process or by a peracid oxidation process. The surfactant produced by the process has lower critical micelle concentration and enables a lower surface tension of a liquid as compared with prior surfactants with two head groups per molecule, thereby enabling the amount of surfactant required and thus the cost to be substantially reduced.

A process for producing a surfactant having two head groups and a single tail group per molecule, including steps of: producing a compound of Formula (1) from ethanol and carbon disulfide; producing a compound of Formula (2) from a carboxylic acid and bromine; producing a compound of Formula (3) from the compound of Formula (2) and methanol; producing a compound of Formula (4) from the compound of Formula (1) and the compound of Formula (3); and producing a compound of Formula (5) from the compound of Formula (4) by a direct oxidation process or by a peracid oxidation process. The surfactant produced by the process has lower critical micelle concentration and enables a lower surface tension of a liquid as compared with prior surfactants with two head groups per molecule, thereby enabling the amount of surfactant required and thus the cost to be substantially reduced.