Method for separating sterols from tall oil
AssigneeArizona Chemical Company
InventorsDerk T. A. Huibers, Andrew M. Robbins, David H. Sullivan
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AssigneeArizona Chemical Company
InventorsDerk T. A. Huibers, Andrew M. Robbins, David H. Sullivan
Estimating the term…
A method is set forth for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil into a residue fraction and a volatile fraction, wherein the temperature of the residue fraction does not exceed about 290.degree. C., and wherein the residue fraction includes the sterol or sterol ester. By application of this method, which can be implemented in existing fractionating equipment or in specially designed pitch collecting apparatuses disclosed herein, the yield of sterols can exceed 50% with respect to the sterols present in crude tall oil. A method is also provided for separating unsaponifiable material from a tall oil stream comprising saponifying the stream with a mixture of sodium hydroxide and potassium hydroxide to form sodium and potassium salts of fatty acid, rosin acids, or both; evaporating the unsaponifiable material; and acidulating the unevaporated sodium and potassium salts.
A method for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil into a residue fraction and a volatile fraction, wherein the temperature of the residue fraction during the fractionation is between about 250.degree. C. and about 290.degree. C., and wherein the residue fraction includes the sterol or sterol ester.
A method for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil into a residue fraction and a volatile fraction, wherein the temperature of the residue fraction during the fractionation does not exceed about 290.degree. C., wherein the residue fraction includes the sterol or sterol ester, and wherein the temperature of the crude tall oil fractionation feed is between about 300.degree. C., and 310.degree. C.
A method for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil into a residue fraction and a volatile fraction, wherein the temperature of the residue fraction during the fractionation does not exceed about 290.degree. C., wherein the residue fraction includes the sterol or sterol ester, and wherein the time of separating the residue fraction from the volatile fraction does not exceed about one hour, after which the residue fraction is allowed to cool.
A method for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil into a residue fraction and a volatile fraction, wherein the temperature of the residue fraction during the fractionation does not exceed about 290.degree. C., wherein the residue fraction includes the sterol or sterol ester, and wherein the residue fraction comprises at least about 15% rosin acids.
A method for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil into a residue fraction and a volatile fraction, wherein the temperature of the residue fraction during the fractionation does not exceed about 290.degree. C., wherein the residue fraction includes the sterol or sterol ester, the method further comprising esterifying the sterols in the crude tall oil prior to or during fractionation.
A method for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil into a residue fraction and a volatile fraction, wherein the temperature of the residue fraction during the fractionation does not exceed about 290.degree. C., wherein the residue fraction includes the sterol or sterol ester, the method further comprising substantially separating the sterols from the non-sterol components of the residue fraction.
A method for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil into a residue fraction and a volatile fraction, wherein the temperature of the residue fraction during the fractionation does not exceed about 290.degree. C., wherein the residue fraction includes the sterol or sterol ester, the method further comprising saponifying the residue fraction to recover free sterols.
A method for separating a sterol or sterol ester from crude tall oil comprising fractionating the crude tall oil in a thin film evaporator at a temperature below about 250.degree. C., into a residue fraction and a volatile fraction, and wherein the residue fraction includes the sterol or sterol ester.
A residue fraction comprising at least about 15% rosin acids.
Dependencies are inferred from the claim text.