Stanol composition and the use thereof
a technology of stanol and composition, which is applied in the direction of edible oils/fats with aqeous phase, organic active ingredients, metabolism disorders, etc., can solve the problems of limited absorption of sterols from healthy subjects' intestines, impaired elimination from the body via the biliary route, and not always well documented sterol composition of tested preparations
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example 1
Hydrogenation of Sterol Mixtures
[0050] A commercially available sterol mixture obtained from vegetable oil distillate (composition: brassicasterol 2.7%, campesterol 26.7%, stigmasterol 18.4% sitosterol 49.1% and sitostanol 2.9% ) was hydrogenated in a pilot scale reactor (25 l). 26 g of a fibrous Pd catalyst (Smop-20; Pd content 10 weight-%, Smoptech, Turku, Finland), 26 g distilled water for the activation of the catalyst and 11.7 kg propanol was feed into the reactor. The reactor was flushed with nitrogen and the activation of the catalyst was carried out under hydrogen gas at a pressure of 1 bar and at a temperature of 65° C. for 30 min. After the activation the blend was cooled to 40° C., after which 1.3 kg of the sterol blend was added.
[0051] The propanol sterol mixture was heated under nitrogen atmosphere to 65° C., after which nitrogen was displaced by hydrogen. After that a thorough flushing with hydrogen was done, the hydrogenation reaction was carried out at a hydrogen p...
example 2
Preparation of Stanol Fatty Acid Esters
[0053] A stanol fatty acid ester mixture was prepared on a pilot scale. 6 kg stanols obtained by combining several batches obtained by the hydrogenating procedure given in example 1 was dried overnight at 60° C. and esterified with a 8.6 kg low erucic acid rapeseed oil methyl ester mixture. The sterol composition of the stanol blends used was as follows: Campesterol 0.4%, campestanol (+24β-methyl cholestanol) 29.7%, stigmasterol 0.1%, sitosterol 0.4% and sitostanol 68.0%. The stanol content of the blend was 98.2%. The esterification was carried out as follows:
[0054] A mixture of stanols and low erucic rapeseed oil fatty acid methyl ester was heated in a reactor vessel at 90-120° C. under a vacuum of 5-15 mmHg. After drying for 1 hour, 21 g Na-ethylate was added and the reaction was continued for about 2 hours. The catalyst was destroyed by the addition of 30% water (by weight) at 90° C. After phase separation the water phase was removed and a...
example 3
Production of Margarines for the Clinical Studies
[0056] 80% margarines with tall oil stanol fatty acid esters and vegetable oil based stanol fatty esters were produced on a Gerstenberg & Agger 3×57 pilot scale perfector. Tall oil stanol fatty acid esters were obtained from the normal production of Benecol® margarine by Raision Margariini, Finland. A normal trans fatty acid free fat blend (composition: 30% non-hydrogenated interesterified vegetable fat and 70% liquid LEAR oil) to wich the stanol fatty acid mixtures were added was used. The stanol content of the final product was targeted to be 12 g / 100 g product, which would provide a daily intake of 3 g stanols at usage level of 25 g / day. The products were produced according to following recipe:
Fat blend including the stanol fatty acid esters80%Water19%Salt0.5%Emulsifier, Dimodan BPNa-bicarbonate and citric acid as pH-regulating agentsβ-carotene as colouring agentFlavours.
[0057] The obtained margarines were packed into 250 g poly...
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