Fatty acid component microcapsule and preparation method thereof
A fatty acid and microcapsule technology, which is applied in the field of fatty acid component microcapsules and its preparation, can solve problems such as limitations and general adaptability, and achieve the effect of improving biodigestibility
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Embodiment 1
[0029] Mix 3.89 kg of sodium caseinate, 5.89 kg of maltodextrin, 1.08 kg of sucrose esters, and 0.36 kg of sodium ascorbate into 32.0 kg of pure water, keep the water temperature at 55°C and stir for 55 minutes until completely mixed and dissolved to obtain the aqueous phase Standby; all manipulations were performed under an inert gas atmosphere.
[0030] Take by weighing 1.30 kilograms of 68.5% palmitic acid, 2.19 kilograms of 99.2% oleic acid, 2.33 kilograms of 90% linoleic acid, 0.41 kilogram of 85% alpha-linolenic acid, 0.07 kilogram of fish oil (wherein DHA+EPA content ≥ 80%) mix as crude oil and 0.48 kg of vitamin E was miscible at a temperature of 35° C. to obtain an oil phase for use; all operations were carried out under an inert gas environment.
[0031] Slowly add the oil phase obtained in step 2) into the aqueous phase obtained in step 1) to obtain a mixture, and use a high-speed shearer to perform high-speed shearing on the mixture at a rate of 7000r / min, the shea...
Embodiment 2
[0035] Take by weighing 6.29 kilograms of gum arabic, 4.82 kilograms of glucose syrup, 4.98 kilograms of maltodextrin, 0.40 kilograms of glyceryl monostearate, 1.61 kilograms of sucrose esters, add 0.5 kilograms of sodium ascorbate to 46.56 kilograms of pure water after mixing, and keep the water temperature at 70 °C and stirred for 60 minutes until completely mixed and dissolved to obtain an aqueous phase for later use; all operations were performed under an inert gas environment.
[0036] Weigh 2.51 kg 72.4% palm oil, 4.72 kg 90.7% oleic acid, 5.96 kg 85% linoleic acid, 0.96 kg 80.8% α-linolenic acid, 0.16 kg algal oil mixed as crude oil with 0.20 kg ascorbyl palmitate and 0.33 kg The lecithin is miscible at a temperature of 25° C., and the oil phase is prepared for use; all operations are carried out under an inert gas environment.
[0037] Slowly add the oil phase obtained in step 2) into the aqueous phase obtained in step 1) to obtain a mixture, and use a high-speed shear...
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