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Method for continuously separating and preparing functional lactoprotein in raw and fresh milk

A fresh milk and functional technology, applied in the field of food processing, can solve the problems of immunoglobulins that cannot be mass-produced, expensive to purchase, and limited in industrial development, and achieve improved bioavailability, good effect, and easy operation. The effect of simple method

Active Publication Date: 2020-04-07
JILIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The separation and preparation of milk base materials is one of the key research issues in the development of special dietary foods. In particular, immunoglobulin, lactoferrin and α-lactalbumin are widely used, but in actual production, immunoglobulins are faced with inability to The problem of large-scale production, and the production technology of α-lactalbumin and lactoferrin is monopolized by foreign countries, so they can only rely on imports, the purchase price is expensive, and the industrial development is very limited

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] (1) Separation of milk fat: take 1000g of fresh milk, pasteurize it, and quickly lower it to 40°C, and use a milk fat separator to centrifuge at a speed of 3000r / min to remove fat;

[0018] (2) Chymosin precipitation method combined with acid precipitation method to separate casein: add 0.1g rennet to skim milk, react at 35°C for 0.5 hours, adjust the pH of the emulsion to 4.8 with lactic acid solution, and The solution is centrifuged at a speed of 7000r / min to obtain a casein precipitate and a supernatant, the supernatant is whey protein, and the supernatant is recovered for use;

[0019] (3) Sterilization by microfiltration: sterilize the whey protein obtained in step (2) through a 0.1 μm microfiltration membrane, and take the permeate for later use;

[0020] (4) Separation and purification of lactoferrin: recover crude lactoferrin by isoelectric point precipitation, adjust the pH of whey obtained in step (3) to 8.0 with edible sodium hydroxide solution, add 60% (w / ...

Embodiment 2

[0027] (1) Milk fat separation: 2000g of fresh goat milk is pasteurized and rapidly lowered to 41°C, and centrifuged at a speed of 5000r / min by a milk fat separator to remove fat;

[0028] (2) Chymosin precipitation method combined with acid precipitation method to separate casein: Add 2g of chymosin to skim milk, react at 36°C for 0.8 hours, adjust the pH of the emulsion to 4.7 with citric acid solution, and The solution is centrifuged at a speed of 8000r / min to obtain a casein precipitate and a supernatant, the supernatant is whey protein, and the supernatant is recovered for use;

[0029] (3) Sterilization by microfiltration: sterilize the whey protein obtained in step (2) through a 0.45 μm microfiltration membrane, and take the permeate for later use;

[0030] (4) Separation and purification of lactoferrin: recover crude lactoferrin by isoelectric point precipitation, adjust the pH of the whey obtained in step (3) to 8.3 with edible sodium hydroxide solution, add 70% (w / ...

Embodiment 3

[0037] (1) Separation of milk fat: Take 3000g of fresh milk, pasteurize it, and quickly lower it to 42°C, use a milk fat separator to centrifuge at a speed of 7000r / min to remove fat;

[0038] (2) Chymosin precipitation method combined with acid precipitation method to separate casein: Add 6g of chymosin to skim milk, react at 37°C for 1 hour, adjust the pH of the emulsion to 4.6 with acetic acid solution, and dissolve the solution Centrifuge at a speed of 10000r / min to obtain a casein precipitate and a supernatant, the supernatant is whey protein, and the supernatant is recovered for use;

[0039] (3) Sterilization by microfiltration: sterilize the whey protein obtained in step (2) through a 0.1 μm microfiltration membrane, and take the permeate for later use;

[0040] (4) Separation and purification of lactoferrin: recover crude lactoferrin by isoelectric point precipitation, adjust the pH of whey obtained in step (3) to 8.5 with edible sodium hydroxide solution, add 80% (w / ...

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Abstract

The invention discloses a method for continuously separating and preparing functional lactoprotein in raw and fresh milk. The method mainly comprises the following steps: step one, separating and recovering milk fat by adopting a centrifugal method; step two, separating casein by combining a chymosin precipitation method with an acid precipitation method; step three, centrifuging a solution to obtain a supernatant being whey protein, carrying out microfiltration sterilization, and recovering permeate liquid for later use; step three, recovering a lactoferrin crude product by adopting an isoelectric point method; step three, recycling trapped fluid by an ultrafiltration method to obtain a crude immunoglobulin product; step five, removing lactose components from the ultrafiltration permeateto obtain an alpha-lactalbumin crude product; and step six, carrying out chromatographic purification on the alpha-lactalbumin crude product to obtain high-purity protein. According to the invention,the casein is separated by adopting the chymosin precipitation method combined with the acid precipitation method, so that the whey protein yield is increased; the subsequent separation of three different functional lactoproteins is facilitated; the protein crude product and the high-purity protein can be respectively obtained; and the requirements of the food industry on different raw materials are met.

Description

technical field [0001] The invention belongs to the technical field of food processing, relates to a method for continuous separation and preparation of functional milk protein in fresh milk, and is a new separation method. Background technique [0002] The separation and preparation of milk bases is one of the key research issues in the development of special dietary foods, especially immunoglobulin, lactoferrin and α-lactalbumin are widely used, but in actual production, immunoglobulins are faced with inability to The problem of large-scale production, and the production technology of α-lactalbumin and lactoferrin is monopolized by foreign countries, so they can only rely on imports, the purchase price is expensive, and the industrial development is very limited. [0003] Separation and preparation of immunoglobulin, lactoferrin and α-lactalbumin from raw milk firstly prepare skim milk, separate casein from the skim milk to obtain whey protein, and then continuously separa...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07K14/47C07K14/79C07K14/76C07K16/02C07K1/14C07K1/36C07K1/34C07K1/30C07K1/18
CPCC07K14/4732C07K14/76C07K14/79C07K16/02
Inventor 张铁华刁梦雪陈思如杨婉露
Owner JILIN UNIV
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