Process for preparing sterol ester of fatty acid for food
A technology of fatty acid ester and manufacturing method, which is applied in the direction of fatty acid esterification, edible oil/fat, fatty acid production, etc., can solve the problems of unoptimized safety, high price, no consideration of quality and safety, etc.
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Embodiment 1
[0200] 100 g of water was added to 200 g of soybean deodorized scum oil (sterol content 13% by weight), and while mixing at 40° C., lipase powder (360,000 units / g) derived from Candida was added (Lipase OF, Meito Sangyo Co., Ltd.) 2.0 g. After performing the reaction while stirring at 40° C. for 24 hours, enzyme inactivation was performed by stirring at 80° C. for 30 minutes. After performing dehydration treatment at 80° C. under reduced pressure, 1.0 g of diatomaceous earth was added, stirred, and filtered to remove enzyme protein. Next, molecular distillation was carried out using a centrifugal molecular distillation apparatus with a vacuum degree of 1.5 Pa, an evaporation surface temperature of 230° C., and a flow rate of 2.0 L / hour to remove impurities mainly composed of free fatty acids to obtain 33 g of sterol fatty acid esters. Then, as an adsorbent treatment, hexane in an amount 5 times the amount of the remaining components was added, mixed, 20% of activated clay was...
Embodiment 2
[0203] 50 g of water was added to 200 g of soybean deodorized scum oil (sterol content 13% by weight), and while mixing at 40° C., heat-resistant lipase powder (10,000 units / g) derived from Rhizopus was added (タリパゼ, Tian Bian Pharmaceutical Co., Ltd.) 3.0 g. After performing the reaction while stirring at 50° C. for 24 hours, the enzyme was inactivated by stirring at 90° C. for 30 minutes. After performing dehydration treatment at 80° C. under reduced pressure, 1.0 g of diatomaceous earth was added, stirred, and filtered to remove enzyme protein. Next, molecular distillation was performed using a centrifugal molecular distillation apparatus with a vacuum degree of 1.5 Pa, an evaporation surface temperature of 230° C., and a flow rate of 2.0 L / hour to remove impurities mainly including free fatty acids to obtain 31 g of sterol fatty acid esters. Then, as an adsorbent treatment, hexane in an amount 5 times the amount of the remaining components was added, mixed, 20% of silica g...
Embodiment 3
[0205] 100 g of water was added to 200 g of rapeseed deodorized scum oil (sterol content 8%), and while mixing at 40° C., lipase powder (360,000 units / g) derived from Candida was added (Lipase OF, Meito Sangyo Co., Ltd.) 2.0 g. After performing the reaction while stirring at 40° C. for 24 hours, enzyme inactivation was performed by stirring at 80° C. for 30 minutes. After performing dehydration treatment at 80° C. under reduced pressure, 1.0 g of diatomaceous earth was added, stirred, and filtered to remove enzyme protein. Next, molecular distillation was carried out using a centrifugal molecular distillation apparatus at a vacuum degree of 1.5 Pa, an evaporation surface temperature of 230° C., and a flow rate of 2.0 L / hour to remove impurities mainly composed of free fatty acids to obtain 28 g of sterol fatty acid esters. Then, as an adsorbent treatment, hexane in an amount 5 times the amount of the remaining components was added, mixed, 20% of activated carbon relative to t...
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