Composition for non-dairy creamer, non-dairy creamer as well as preparation method and application of non-dairy creamer
A technology of non-dairy creamer and its composition, which is applied in the field of non-dairy creamer and its preparation and composition of non-dairy creamer, to achieve the effects of preventing health risks, smooth taste and flavor, and reducing fat intake
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Embodiment 1
[0057] Weigh raw materials according to the following weights: (grams)
[0058] Sucrose polyester 35g; palm oil 0.5g; glucose syrup 55.6g; sodium caseinate 3.5g; monoglyceride fatty glyceride 2g; diglyceride fatty glyceride 2g; sodium stearoyl lactylate 0.5g; Sodium hexametaphosphate 0.3g; essence 0.45g.
[0059] The preparation method of non-dairy creamer:
[0060] The raw materials are mixed according to the above ratio and dissolved in 500g of distilled water, homogenized, pasteurized, pasteurized usually at 75°C, sterilized for 20s, flavored, spray-dried, the product is aseptically vacuum-packed to obtain non-dairy creamer . Among them, the homogenization pressure is 20MP, the temperature is 65°C, and the number of homogenization is 2 times. And spray drying is carried out under the process conditions of feed rate 460mL / h, inlet air temperature 160°C, outlet air temperature 84°C, and spray pressure 25Mpa.
Embodiment 2
[0062] Weigh raw materials according to the following weights: (grams)
[0063] Sucrose polyester 30g; palm oil 3g; glucose syrup 58.5g; sodium caseinate 3g; monoglyceride fatty glyceride 4g; diglyceride fatty glyceride 0.1g; sodium stearoyl lactylate 0.2g; Sodium metaphosphate 0.4g; essence 0.3g.
[0064] The preparation method of non-dairy creamer:
[0065] The raw materials are mixed according to the above ratio and dissolved in 590 g of distilled water. After homogenization, pasteurization, flavoring and spray drying, the product is subjected to aseptic vacuum packaging to obtain non-dairy creamer. Among them, the homogenization pressure is 15MP, the temperature is 80°C, and the number of homogenization times is 1 time. And spray drying is carried out under the process conditions of feed rate 400mL / h, inlet air temperature 120°C, outlet air temperature 90°C, and spray pressure 20Mpa.
Embodiment 3
[0067] Weigh raw materials according to the following weights: (grams)
[0068] Sucrose polyester 10g; corn oil 15g; glucose syrup 30g; sodium caseinate 2g; monoglyceride fatty glyceride 5g; diglyceride fatty glyceride 4g; sodium stearoyl lactylate 0.1g; Sodium 0.2g; essence 0.5g.
[0069] The preparation method of non-dairy creamer:
[0070] The raw materials are mixed according to the above ratio and dissolved in 270 g of distilled water. After homogenization, pasteurization, flavoring and spray drying, the product is subjected to aseptic vacuum packaging to obtain non-dairy creamer. Among them, the homogenization pressure is 30MP, the temperature is 60°C, and the number of homogenization times is 3 times. And spray drying is carried out under the process conditions of feed rate 500mL / h, inlet air temperature 180°C, outlet air temperature 80°C, and spray pressure 30Mpa.
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