Abstract: Provided are a liquid seasoning in which degradation of taste and flavor due to storage is suppressed, and a method of producing the same. The method of producing a liquid seasoning comprises the following steps (1), (2), and (3): (1) at a temperature of 80° C. or less, adding an aqueous solution of at least one selected from the group consisting of ascorbic acid, hydroxyacid, and salts thereof to a fat or oil and stirring the mixture; (2) bringing the fat or oil after the step (1) into contact with water vapor under reduced pressure; and (3) bringing the fat or oil obtained in the step (2) as an oil phase component into contact with an aqueous phase.

Abstract: Provided are a liquid seasoning in which degradation of taste and flavor due to storage is suppressed, and a method of producing the same. The method of producing a liquid seasoning comprises the following steps (1), (2), and (3): (1) at a temperature of 80° C. or less, adding an aqueous solution of at least one selected from the group consisting of ascorbic acid, hydroxyacid, and salts thereof to a fat or oil and stirring the mixture; (2) bringing the fat or oil after the step (1) into contact with water vapor under reduced pressure; and (3) bringing the fat or oil obtained in the step (2) as an oil phase component into contact with an aqueous phase.

Abstract: A method for manufacturing a refined fat or oil, including: carrying out a first steam treatment of bringing a fat or oil into contact with water vapor; and subsequently carrying out a second steam treatment of bringing the fat or oil having a temperature lower by 10° C. or more than a temperature of the fat or oil in the first steam treatment into contact with water vapor in the presence of an organic acid.

Abstract: Provided is a method for manufacturing refined fats and oils. Here fats and oils are brought into contact with an adsorbent and subsequently treated with water vapor under at least one condition of the following conditions. In condition I, the time for which the fats and oils are brought into contact with the water vapor in a temperature range of 175° C. to 205° C. for from 5 to 110 minutes. In condition 2, the fats and oils are brought into contact with the water vapor in a temperature range of 205° C. to 215° C. for from 5 to 50 minutes. In condition 3, the fats and oils are brought into contact with the water vapor in a temperature range of 215° C. to 230° C. for from 5 to 30 minutes.

Abstract: Provided is an oil or fat composition, which has an MCPD-FS content (ppm) of 13 ppm or less, the content being measured by a Deutsche Gesellschaft für Fettwissenschaft (DGF) standard method C-III 18(09), has a diacylglycerol content of 15 mass % or more, and is subjected to deodorization treatment.

Abstract: A method for manufacturing a refined fat or oil, including: carrying out a first steam treatment of bringing a fat or oil into contact with water vapor; subsequently carrying out a treatment of bringing the fat or oil into contact with an adsorbent; and further carrying out a second steam treatment of bringing the fat or oil having a temperature lower by 10° C. or more than a temperature of the fat or oil in the first steam treatment into contact with water vapor.

Abstract: A method for manufacturing a refined fat or oil, including: carrying out a first steam treatment of bringing a fat or oil into contact with water vapor; and subsequently carrying out a second steam treatment of bringing the fat or oil having a temperature lower by 10° C. or more than a temperature of the fat or oil in the first steam treatment into contact with water vapor in the presence of an organic acid.

Abstract: A method for manufacturing a refined fat or oil, including: carrying out a first steam treatment of bringing a fat or oil into contact with water vapor; subsequently carrying out a treatment of bringing the fat or oil into contact with an adsorbent; and further carrying out a second steam treatment of bringing the fat or oil having a temperature lower by 10° C. or more than a temperature of the fat or oil in the first steam treatment into contact with water vapor.

Abstract: Provided is an oil or fat composition, which has an MCPD-FS content (ppm) of 13 ppm or less, the content being measured by a Deutsche Gesellschaft für Fettwissenschaft (DGF) standard method C-III 18(09), has a diacylglycerol content of 15 mass % or more, and is subjected to deodorization treatment.

Abstract: Provided is a method for manufacturing refined fats and oils, including: treating fats and oils by bringing the fats and oils into contact with an adsorbent; and subsequently treating the fats and oils by bringing the fats and oils into contact with water vapor under at least one condition selected from the following conditions: (condition 1) the time for which the fats and oils are brought into contact with the water vapor in a temperature range of 175° C. or more and 205° C. or less is from 5 to 110 minutes; (condition 2) the time for which the fats and oils are brought into contact with the water vapor in a temperature range of more than 205° C. and 215° C. or less is from 5 to 50 minutes; and (condition 3) the time for which the fats and oils are brought into contact with the water vapor in a temperature range of more than 215° C. and 230° C. or less is from 5 to 30 minutes.

Abstract: Provided is a method of producing an immobilized lipolytic enzyme which has almost the same ability as that of an unused immobilized enzyme by effectively utilizing an immobilization carrier in a used immobilized enzyme which has been used in an esterification reaction. The method of producing an immobilized lipolytic enzyme includes: mixing an immobilized lipolytic enzyme that has been used in an esterification reaction with a solvent to wash the immobilized lipolytic enzyme so that the residual oil content in the immobilized lipolytic enzyme is reduced to 50 parts by mass or less based on 100 parts by mass of an immobilization carrier; bringing the immobilized lipolytic enzyme into contact with an alkali solution; collecting the immobilization carrier; and adsorbing a lipolytic enzyme on the immobilization carrier.