Non-live bacterium type whey milk-containing drink and preparation method thereof
A technology for milk-containing beverages and whey, applied in whey, dairy products, Streptococcus/Lactococcus, etc., can solve the problems of product taste improvement, low protein content, complicated process, etc., to achieve shelf life, reduce production costs, good stability
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Embodiment 1
[0057] A preparation method of non-viable whey milk-containing beverage includes the following steps:
[0058] (1) Preparation of whey, the following parts are parts by weight:
[0059] Skim the raw milk to make the fat content between 1.2% and 1.5%. Take part of the skim milk and heat it up to 52°C. Add 40 parts of white sugar and cut for 5 minutes. Add the remaining skim milk to make the volume up to 1000 parts. Filter and homogenize, homogenization temperature is 60℃, homogenization pressure 15-16Mpa, sterilization, sterilization temperature 95℃, sterilization time 300s, after sterilization, cool to 38℃, inoculate starter A, terminate pH 4.6, demulsify and stir for 200s After passing through the separator, the separator has a flow rate of 3.0 tons / hour and a smoothing pump speed of 20%. The obtained Greek yogurt is cooled to 23°C and enters into a tank for filling. The outlet temperature during whey separation is 35°C, and the whey is directly converted into feed.
[0060] The pr...
Embodiment 2
[0074] A preparation method of non-viable whey milk-containing beverage includes the following steps:
[0075] (1) Preparation of whey, the following parts are parts by weight:
[0076] The raw milk is skimmed to make the fat content 1.8%-2.0%. Take part of the skim milk and heat it to 54°C. Add 50 parts of white sugar and cut for 10 minutes. Add the remaining skim milk to make the volume to 1000 parts, then filter, Homogenization, homogenization temperature is 70℃, homogenization pressure 15-16Mpa, sterilization, sterilization temperature 94℃, sterilization time 300s, after sterilization, cool to 40℃, inoculate starter A, terminate pH 4.7, demulsify and stir for 200s, after Separator, the separator has a flow rate of 2.8 tons / hour and a smoothing pump speed of 20%. The obtained Greek yogurt is cooled to 23°C and put into cans. The outlet temperature during whey separation is 40°C, and the whey is directly fed into the whey tank for later use.
[0077] The protein content of the ra...
Embodiment 3
[0091] A preparation method of non-viable whey milk-containing beverage includes the following steps:
[0092] (1) Preparation of whey, the following parts are parts by weight:
[0093] The raw milk is skimmed to make the fat content between 1.5% and 1.7%. Take part of the skim milk and heat it to 55°C. Add 40 parts of white sugar and cut for 5 minutes. Add the remaining skim milk to make the volume up to 1000 parts, then filter, Homogenize, homogenization temperature is 65℃, homogenization pressure 15-16Mpa, sterilization, sterilization temperature 95±2℃, sterilization time 300s, after sterilization, cool to 40℃, inoculate starter A, terminate pH 4.6, demulsify and stir for 200s After passing through the separator, the separator has a flow rate of 3.1 tons / hour and a smoothing pump speed of 20%. The Greek yogurt is cooled to 23°C and placed in the tank. The temperature of the whey separation is 33°C, and the whey is directly fed into the whey tank.
[0094] The protein content of t...
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