阅读说明：本技术 一种低黄色值豌豆蛋白的生产方法 (Production method of pea protein with low yellow value ) 是由 时玉强 鲁绪强 许建 于 2021-09-14 设计创作，主要内容包括：一种低黄色值豌豆蛋白生产方法,包括：粉碎、浸提、离心分离、酸沉、离心分离、中和、杀菌、真空脱气、保温、喷雾干燥。所制得的豌豆蛋白分散速度快,水溶后不易结团,便于产品的加工使用；杀菌彻底,耐热菌及菌落总数低；分散性高NSI高,蛋白溶液稳定性好；蛋白溶液颜色白,蛋白水合液体或浆体黄色值低。(A method for producing pea protein with low yellow value comprises the following steps: crushing, leaching, centrifugal separation, acid precipitation, centrifugal separation, neutralization, sterilization, vacuum degassing, heat preservation and spray drying. The prepared pea protein has high dispersion speed, is not easy to agglomerate after being dissolved in water, and is convenient for processing and using products; the sterilization is thorough, and the total number of thermotolerant bacteria and bacterial colonies is low; the dispersibility is high, NSI is high, and the stability of the protein solution is good; the protein solution has white color and the protein hydration liquid or slurry has low yellow value.)

1. A method for producing pea protein with low yellow value comprises the following steps:

(1) crushing: pulverizing semen Pisi Sativi to obtain powder of 80-100 mesh;

(2) leaching: mixing pea powder with water according to the weight ratio of 1:15-20, stirring for a certain time at the water temperature of 50-55 ℃, then crushing by using wet crushing equipment, conveying to a storage tank, carrying out sterilization treatment, and then storing for a period of time to obtain a first mixture;

(3) centrifugal separation: centrifuging the first mixture obtained in the step (2) to obtain primary pea residues and primary pea milk, washing the primary pea residues with water to obtain secondary pea residues and secondary pea milk, and mixing the primary pea milk and the secondary pea milk to obtain a pea milk mixture;

(4) acid precipitation: adjusting the pH value of the pea milk mixture to 4.5-4.8, and settling to obtain an acid settling solution;

(5) centrifugal separation: carrying out centrifugal separation on the acid precipitation solution obtained in the step (4) to obtain acidic solid-phase protein slurry;

(6) neutralizing: diluting the acidic solid-phase protein slurry with 1.5-2.5 times of water, homogenizing, continuously neutralizing the diluted acidic protein solution and the diluted food-grade alkali by a static mixer, and adjusting the pH to 6.0-7.3; brix is 12.0-14.5;

(7) and (3) sterilization: carrying out high-temperature instantaneous sterilization on the protein slurry obtained in the step (6);

(8) vacuum degassing: carrying out vacuum degassing on the protein slurry obtained in the step (7) to remove beany flavor;

(9) and (3) heat preservation: placing the protein slurry obtained in the step (8) in a heat-preservation tank, and preserving heat for 30-45 minutes at 70-75 ℃;

(10) spray drying: and (4) carrying out spray drying on the protein slurry obtained in the step (9) to prepare protein powder, and spraying a food-grade surfactant on the elbow.

2. The method for producing pea proteins with low yellow value according to claim 1, wherein the raw material pea used has a maturation period of 10-20 months.

3. The method for producing pea proteins with low yellow value according to claim 1, wherein in the step (2), the stirring time is 25-45 min.

4. The method for producing pea proteins with low yellow value according to claim 1, wherein in the step (2), the sterilization treatment is performed by using microwave, ultrasonic wave or microwave and ultrasonic wave combined treatment.

5. The method for producing pea proteins with low yellow value according to claim 1, wherein in the step (2), the storage time is 30-50 min.

6. The method for producing pea proteins with low yellow value according to claim 1 to 5, wherein in step (4), the precipitation is isoelectric precipitation.

7. The method for producing pea proteins with low yellow value according to claim 1, wherein in the step (6), the homogenizing pressure is 5-30 MPa.

8. The method for producing pea proteins with low yellow value according to claim 1, wherein in the step (7), the sterilization temperature is 125-149 ℃, and the sterilization time is 3-8 seconds.

9. The method for producing pea proteins with low yellow value according to claim 1, wherein the vacuum degree of vacuum degassing in the step (8) is 60-70 kPa.

10. The production method of pea proteins with low yellow value as claimed in claim 1, wherein in the step (10), the addition amount of the food grade surfactant is 0.5-2% o of the weight of the protein powder; the food grade surfactant includes a water soluble phospholipid.

Technical Field

The invention relates to a production method of pea protein with low yellow value, in particular to a production method of pea protein with low yellow value by taking peas as main raw materials; the pea protein with low yellow value prepared by the production method can be applied to neutral liquid beverages and solid beverages, and can also be applied to various foods with higher requirements on yellow of liquid or slurry after hydration.

Background

The vegetable protein beverage is a milky liquid beverage mainly containing vegetable protein, which is prepared from main raw materials (such as peas, peanuts, almonds, walnut kernels, coconuts, sticks and the like) including vegetable nuts and fruit pulp. It is popular with consumers because of its advantages of no or less cholesterol content, rich protein and amino acid, proper amount of unsaturated fatty acid, complete nutrients, etc.

The outstanding defects of the food structure in China are that the protein is low, the milk source is seriously lacked, and the occupancy of the cow milk is insufficient in 1/10 of developed countries. In addition, milk powder accounts for about 75% of dairy products, and new fields are urgently to be developed. The development of new protein products of milk-containing beverages is suitable for the taste of consumers in China, enriches the market of dairy products, and is an important task in the food industry. Protein beverages are rapidly developed in China in the last decade, and the main reason is that with the continuous improvement of living standard and the continuous enhancement of health consciousness in large and medium-sized cities, consumers gradually turn to the requirements of nutrition, health care and functions from simply meeting carbonated beverages for relieving summer heat and quenching thirst, which is necessary for the development of soft beverages.

With the increase of consumption level of people, the requirements on the beverage tend to be nutritional, health-care, safe and sanitary and return to nature. Therefore, according to local conditions and reasonable layout, the development of the milk-containing beverage and the rapid development of the vegetable protein beverage are important industrial policies for the development of beverage industry in China. And the plant protein resources in China are rich from north to south, so the development of the plant protein beverage is a supplementary measure suitable for the national situation and improving the protein intake of China. On the other hand, the vegetable protein beverage (such as soymilk) has rich nutrition, reasonable nutrient composition and special color, aroma and taste, is suitable for consumers in China, and is a healthy nutritional beverage with high quality and low price.

Therefore, in recent years, vegetable protein beverages have begun to show up in the corners in the beverage market in our country. At present, the vegetable protein beverage in China is increased at a speed of 30% every year, and the vegetable protein beverage is in the best development period. Since the introduction of the first soymilk production line in Guangdong in the early 80 s, thousands of soymilk processing factories exist in China.

Pea protein is used as an important component of liquid beverage and is widely applied to various vegetable protein beverages. Pea protein has the advantage of comprehensive amino acid composition, particularly, the content of 8 essential amino acids meets the complete protein standard, and the pea protein is a plant protein capable of replacing animal protein. Meanwhile, the pea protein does not contain cholesterol substances, has positive effects on cardiovascular and cerebrovascular diseases, has certain prevention effects on obesity and cancer, and does not contain an allergen and does not have transgenic risks compared with the soybean protein. However, the pea protein is easy to be light yellow after being dissolved in water due to the existence of pigments such as pea isoflavone and the like, and does not meet the requirements of the pea protein in liquid beverages, solid beverages and other protein beverages with higher requirements on color.

In the prior art, CN102250201B discloses a preparation method of high-solubility pea protein powder, which takes pea starch processing waste liquid as a raw material, combines carbohydrase enzymolysis and continuous hydrothermal treatment to prepare the high-solubility pea protein powder, firstly reclaims pea protein in the waste water by a spray drying method, then prepares a pea protein solution and adjusts the pH value; stirring the obtained protein dispersion, adding carbohydrase, and performing enzymolysis at 50-95 deg.C and pH 4.5-7.0 for 0.5-5 hr; adjusting pH value, continuous hydrothermal treatment, and spray drying. The disadvantages of this method are: the raw material is waste liquid produced by pea starch, the waste liquid is a byproduct of starch processing, long-time soaking (8-12 hours) is needed during starch production, and pea protein reacts with corresponding enzyme and is hydrolyzed during the soaking process, so that the functional maintenance of the pea protein is not facilitated. Meanwhile, microorganisms are excessively propagated in the process of long-time soaking, secondary metabolites of colored microorganisms are generated, and the color of pea protein is not favorably maintained. In addition, the method needs spray concentration, and after the spray drying is carried out once, the conditioning is carried out again, and the treatment is carried out again by the spray drying, so the energy consumption is large, the processing process is long, the reaction of the polyphenol compounds and the carbonyl ammonia is enhanced, and the white value of the pea egg is poor and the pea egg is yellow.

Therefore, a new production method of pea protein with low yellow value is needed to solve the technical problem.

Disclosure of Invention

The invention provides a production method of pea protein with a low yellow value, which comprises the following steps:

(1) crushing: pulverizing semen Pisi Sativi to obtain powder of 80-100 mesh;

(2) leaching: mixing pea powder with water according to the weight ratio of 1:15-20, stirring for a certain time at the water temperature of 50-55 ℃, then crushing by using wet crushing equipment, conveying to a storage tank, sterilizing, and then storing for a period of time to obtain a first mixture;

(3) centrifugal separation: centrifuging the first mixture obtained in the step (2) to obtain primary pea residues and primary pea milk, washing the primary pea residues with water to obtain secondary pea residues and secondary pea milk, and mixing the primary pea milk and the secondary pea milk to obtain a pea milk mixture;

(4) acid precipitation: adjusting the pH value of the pea milk mixture to 4.5-4.8, and settling to obtain an acid settling solution;

(5) centrifugal separation: carrying out centrifugal separation on the acid precipitation solution obtained in the step (4) to obtain acidic solid-phase protein slurry;

(6) neutralizing: diluting the acidic solid-phase protein slurry with 1.5-5 times (preferably 2 times) volume of water, homogenizing, continuously neutralizing the diluted acidic protein solution and diluted food-grade alkali by a static mixer, and adjusting pH to 6.0-7.3; brix is 12.0-14.5;

(7) and (3) sterilization: carrying out high-temperature instantaneous sterilization on the protein slurry obtained in the step (6);

(8) vacuum degassing: carrying out vacuum degassing on the protein slurry obtained in the step (7) to remove beany flavor;

(9) and (3) heat preservation: placing the protein slurry obtained in the step (8) in a heat-preservation tank, and preserving heat for 30-45 minutes at 70-75 ℃;

(10) spray drying: and (4) carrying out spray drying on the protein slurry obtained in the step (9) to prepare protein powder, and spraying a food-grade surfactant on the elbow.

Wherein the mature period of the adopted raw material pea is 10-20 months.

Wherein in the step (2), the stirring time is 25-45 min; the wet grinding equipment is a multi-stage homogenizing pump; the sterilization treatment is carried out by utilizing microwave, ultrasonic wave or microwave and ultrasonic wave combined treatment; the sterilization treatment time is 2-8 min; the storage time is 30-50 min.

And (3) recovering fiber and pea starch from the primary pea residues and the secondary pea residues.

Wherein, in the step (4), the sedimentation is isoelectric point sedimentation.

Wherein in the step (6), the homogenizing pressure is 5-30 MPa; the food grade alkali is sodium hydroxide and/or potassium hydroxide.

Wherein, in the step (7), the sterilization temperature is 125-149 ℃, and the sterilization time is 3-8 seconds.

Wherein in the step (8), the vacuum degree of vacuum degassing is 60-70 kPa.

Wherein in the step (10), the addition amount of the food-grade surfactant is 0.5-2 per mill of the mass of the protein powder; the food grade surfactant includes a water soluble phospholipid.

The invention also provides pea proteins having a low yellow value (i.e., b-value of 14 to 15.0) produced by the low yellow value pea protein production process.

The invention also provides a beverage comprising the low-yellow-value pea protein.

The invention has the following beneficial technical effects:

(1) the maturation period of the raw material pea is 10-20 months, which ensures the stability of pea protein molecules and compact structure.

(2) In the step (1), the pea protein powder is crushed to the fineness of 80-100 meshes, which is helpful for ensuring the water dissolving speed of the pea protein and is convenient for separating the pea protein.

(3) In the step (2), water is used as an extracting agent, so that the isomerization and yellow color development of pea isoflavone under high pH are avoided; microwave, ultrasonic wave or microwave combined ultrasonic wave treatment is utilized to promote extraction of pea protein and simultaneously inactivate enzyme, so that the functionality of the protein is ensured, the activity of a trypsin inhibitor is reduced, and the nutritional value is improved; the microorganism is controlled at a high temperature of 50-55 ℃ to avoid yellow and other secondary metabolites.

(4) In the step (6), the pH time of the protein slurry is ensured to be less than or equal to 7.3 by continuously adding alkali, so that the conversion of pea isoflavone and the conversion of related pigments are avoided, and further, the generation of yellow and other pigments is avoided, and the color is white.

(5) In the step (7), the process sterilization is achieved through sterilization.

(6) In the step (9), the globular protein is stretched by heat preservation, so that the globular protein is conveniently dispersed in water; and the pigment is damaged, and yellow and other miscellaneous colors are reduced.

(7) In the step (10), the dispersibility is improved by adding a food grade surfactant.

(8) The pea protein prepared by the invention has high dispersion speed, is not easy to agglomerate after being dissolved in water, and is convenient for processing and using products; the sterilization is thorough, and the total number of thermotolerant bacteria and bacterial colonies is low; the dispersibility is high, NSI is high, and the stability of the protein solution is good; the protein solution has white color and the protein hydration liquid or slurry has low yellow value. The b value in an LAB color difference detection system is adopted to indicate the degree of yellow, the higher the b value is, the more yellow the color is, and the b value of the pea protein prepared by the invention is 14.0-15.0.

Detailed Description

In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail with reference to the following embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.

Example 1

(1) Crushing: pulverizing semen Pisi Sativi to 80 mesh.

(2) Leaching: mixing pea powder with water at a weight ratio of 1:15, stirring at 50 deg.C for 25min, pulverizing with a multi-stage homogenizing pump, transferring to a storage tank, sterilizing with microwave for 2min, storing for 30min, and separating; the maturation period of the raw material pea is 10 months, which ensures the stability and compact structure of the pea protein molecules. Water was used as the extractant to avoid yellow coloration of pea isoflavones by isomerization at high PH. The microwave promotes the extraction of pea protein and simultaneously inactivates, ensures the functionality of the protein, reduces the activity of trypsin inhibitor and improves the nutritive value. High temperature controls microorganisms, avoids yellow and other color secondary metabolites.

(3) Centrifugal separation: performing centrifugal separation on the liquid phase subjected to sterilization treatment in the step (2) to obtain primary pea residues and primary pea milk, washing the primary pea residues with water to obtain secondary pea residues and secondary pea milk, and mixing the primary pea milk and the secondary pea milk to obtain a pea milk mixture; the fiber and the pea starch can be recovered from the primary pea residues and the secondary pea residues.

(4) Acid precipitation: adjusting the pH value of the pea milk mixture to 4.5, and performing isoelectric point precipitation to obtain an acid precipitation solution.

(5) Centrifugal separation: carrying out centrifugal separation on the acid precipitation solution in the step (4) to obtain acidic solid-phase protein slurry;

(6) neutralizing: diluting the acidic solid-phase protein slurry with 2 times of water, homogenizing under 5MPa, continuously neutralizing the diluted acidic protein solution and the diluted food-grade alkali by a static mixer, and adjusting pH to 6.0; brix 12.0. The pH time of the protein slurry is ensured to be lower than or equal to 7.3 by continuously adding alkali, so that the conversion of pea isoflavone and the conversion of related pigments are avoided, and further, the generation of yellow and other pigments is avoided, and the color is white.

(7) And (3) sterilization: instantly sterilizing the protein pulp at high temperature, wherein the sterilization temperature is 125 ℃ for 3 seconds; achieving the process sterilization;

(8) vacuum degassing: vacuum degassing is carried out after sterilization, and the vacuum degree is controlled to be 60 kPa; the beany flavor is removed through vacuum degassing,

(9) and (3) heat preservation: placing the degassed protein slurry in a heat-preserving tank, and preserving the heat for 30 minutes at 70 ℃ to ensure that the spherical protein is stretched and is convenient to disperse in water; and the pigment is damaged, and yellow and other miscellaneous colors are reduced.

(10) Spray drying: the albumen powder is prepared by spray drying, and meanwhile, the elbow is sprayed with water-soluble phospholipid, and the addition amount of the water-soluble phospholipid is 0.5 per mill of the mass of the albumen powder;

as a result: the color of the hydrated slurry was measured by dark LAB color difference, the b value was 14, and the color was white.

Example 2

(1) Crushing: pulverizing semen Pisi Sativi to 100 mesh. Ensures the water dissolving speed of the pea protein and is convenient for separating the pea protein.

(2) Leaching: mixing pea powder with water at a weight ratio of 1:20, stirring at 55 deg.C for 45min, pulverizing with a multi-stage homogenizing pump, transferring to a storage tank, sterilizing with microwave for 8min, storing for 50min, and separating; the maturation period of the raw material pea is 20 months, which ensures the stability and compact structure of the pea protein molecules. Water was used as the extractant to avoid yellow coloration of pea isoflavones by isomerization at high PH. The microwave promotes the extraction of pea protein and simultaneously inactivates, ensures the functionality of the protein, reduces the activity of trypsin inhibitor and improves the nutritive value. High temperature controls microorganisms, avoids yellow and other color secondary metabolites.

(3) Centrifugal separation: performing centrifugal separation on the liquid phase subjected to sterilization treatment in the step (2) to obtain primary pea residues and primary pea milk, washing the primary pea residues with water to obtain secondary pea residues and secondary pea milk, and mixing the primary pea milk and the secondary pea milk to obtain a pea milk mixture; the fiber and the pea starch can be recovered from the primary pea dregs and the secondary pea dregs.

(4) Acid precipitation: adjusting the pH value of the pea milk mixture to 4.8, and performing isoelectric point precipitation to obtain an acid precipitation solution.

(5) Centrifugal separation: carrying out centrifugal separation on the acid precipitation solution in the step (4) to obtain acidic solid-phase protein slurry;

(6) neutralizing: diluting the acidic solid-phase protein slurry with 2 times of water, homogenizing under the homogenizing pressure of 30MPa, continuously neutralizing the diluted acidic protein solution and the diluted food-grade alkali through a static mixer, and adjusting the pH to 7.3; brix 14.5. The pH time of the protein slurry is ensured to be lower than or equal to 7.3 by continuously adding alkali, so that the conversion of pea isoflavone and the conversion of related pigments are avoided, and further, the generation of yellow and other pigments is avoided, and the color is white.

(7) And (3) sterilization: instantly sterilizing the protein pulp at high temperature, wherein the sterilization temperature is 149 ℃ for 8 seconds; achieving the process sterilization;

(8) vacuum degassing: vacuum degassing after sterilization, wherein the vacuum degree is controlled to 70 kPa; the beany flavor is removed through vacuum degassing,

(9) and (3) heat preservation: placing the degassed protein slurry in a heat-preserving tank, preserving the heat for 45 minutes at 75 ℃ to ensure that the spherical protein is stretched and is convenient to disperse in water; and the pigment is damaged, and yellow and other miscellaneous colors are reduced.

(10) Spray drying: the albumen powder is prepared by spray drying, and meanwhile, the elbow is sprayed with water-soluble phospholipid, and the addition amount of the water-soluble phospholipid is 2 per mill of the mass of the albumen powder;

as a result: the color of the hydrated slurry was measured by dark LAB color difference and the b value was 15.

Example 3

(1) Crushing: pulverizing semen Pisi Sativi to 90 mesh. Ensures the water dissolving speed of the pea protein and is convenient for separating the pea protein.

(2) Leaching: mixing pea powder with water at a weight ratio of 1:18, stirring at 53 deg.C for 29min, pulverizing with multi-stage homogenizing pump, transferring to storage tank, sterilizing with microwave for 6min, and storing for 38min for separation; the maturation period of the raw material pea is 15 months, which ensures the stability and compact structure of the pea protein molecules. Water was used as the extractant to avoid yellow coloration of pea isoflavones by isomerization at high PH. The microwave promotes the extraction of pea protein and simultaneously inactivates, ensures the functionality of the protein, reduces the activity of trypsin inhibitor and improves the nutritive value. High temperature controls microorganisms, avoids yellow and other color secondary metabolites.

(3) Centrifugal separation: performing centrifugal separation on the liquid phase subjected to sterilization treatment in the step (2) to obtain primary pea residues and primary pea milk, washing the primary pea residues with water to obtain secondary pea residues and secondary pea milk, and mixing the primary pea milk and the secondary pea milk to obtain a pea milk mixture; the fiber and the pea starch can be recovered from the primary pea dregs and the secondary pea dregs.

(4) Acid precipitation: adjusting the pH value of the pea milk mixture to 4.6, and performing isoelectric point precipitation to obtain an acid precipitation solution.

(5) Centrifugal separation: carrying out centrifugal separation on the acid precipitation solution in the step (4) to obtain acidic solid-phase protein slurry;

(6) neutralizing: diluting the acidic solid-phase protein slurry with 2 times of water, homogenizing under 260MPa, continuously neutralizing the diluted acidic protein solution and the diluted food-grade alkali by a static mixer, and adjusting the pH to 6.5; brix 13.5. The pH time of the protein slurry is ensured to be lower than or equal to 7.3 by continuously adding alkali, so that the conversion of pea isoflavone and the conversion of related pigments are avoided, and further, the generation of yellow and other pigments is avoided, and the color is white.

(7) And (3) sterilization: instantly sterilizing the protein pulp at high temperature, wherein the sterilization temperature is 129 ℃ for 6 seconds; the sterilization achieves the process sterilization.

(8) Vacuum degassing: vacuum degassing is carried out after sterilization, and the vacuum degree is controlled to be 67 kPa; the beany flavor is removed by vacuum degassing.

(9) And (3) heat preservation: placing the degassed protein slurry in a heat-preserving tank, and preserving the heat for 35 minutes at 75 ℃ to ensure that the spherical protein is stretched and is convenient to disperse in water; and the pigment is damaged, and yellow and other miscellaneous colors are reduced.

(10) Spray drying: the protein powder is prepared by spray drying, and meanwhile, the elbow is sprayed with water-soluble phospholipid, and the addition amount of the water-soluble phospholipid is 1 per mill of the mass of the protein powder.

As a result: the hydrated slurry was dark in color as measured by LAB color difference and had a b value of 14.5.

Example 4

(1) Crushing: pulverizing semen Pisi Sativi to 88 mesh. Ensures the water dissolving speed of the pea protein and is convenient for separating the pea protein.

(2) Leaching: mixing pea powder and water according to the weight ratio of 1:18, stirring for 35min at the water temperature of 53 ℃, crushing by using a multi-stage homogenizing pump, conveying to a storage tank, sterilizing by using microwave for 6min, and storing for 40min for waiting for separation; the maturation period of the raw material pea is 18 months, which ensures the stability and compact structure of the pea protein molecules. Water was used as the extractant to avoid yellow coloration of pea isoflavones by isomerization at high PH. The microwave promotes the extraction of pea protein and simultaneously inactivates, ensures the functionality of the protein, reduces the activity of trypsin inhibitor and improves the nutritive value. High temperature controls microorganisms, avoids yellow and other color secondary metabolites.

(3) Centrifugal separation: performing centrifugal separation on the liquid phase subjected to sterilization treatment in the step (2) to obtain primary pea residues and primary pea milk, washing the primary pea residues with water to obtain secondary pea residues and secondary pea milk, and mixing the primary pea milk and the secondary pea milk to obtain a pea milk mixture; the fiber and the pea starch can be recovered from the primary pea dregs and the secondary pea dregs.

(4) Acid precipitation: adjusting the pH value of the pea milk mixture to 4.7, and performing isoelectric point precipitation to obtain an acid precipitation solution.

(5) Centrifugal separation: and (4) carrying out centrifugal separation on the acid precipitation solution in the step (4) to obtain the acidic solid-phase protein slurry.

(6) Neutralizing: diluting the acidic solid-phase protein slurry with 2 times of water, homogenizing under 9MPa, continuously neutralizing the diluted acidic protein solution and the diluted food-grade alkali by a static mixer, and adjusting the pH to 6.7; brix 12.9. The pH time of the protein slurry is ensured to be lower than or equal to 7.3 by continuously adding alkali, so that the conversion of pea isoflavone and the conversion of related pigments are avoided, and further, the generation of yellow and other pigments is avoided, and the color is white.

(7) And (3) sterilization: instantly sterilizing the protein pulp at high temperature at 139 deg.C for 6 s; achieving the process sterilization;

(8) vacuum degassing: vacuum degassing after sterilization, wherein the vacuum degree is controlled to 64 kPa; the beany flavor is removed by vacuum degassing.

(9) And (3) heat preservation: placing the degassed protein slurry in a heat-preserving tank, and preserving the heat for 42 minutes at 73 ℃ to ensure that the spherical protein is stretched and is convenient to disperse in water; and the pigment is damaged, and yellow and other miscellaneous colors are reduced.

(10) Spray drying: the albumen powder is prepared by spray drying, and meanwhile, the elbow is sprayed with water-soluble phospholipid, and the addition amount of the water-soluble phospholipid is 1.2 per mill of the mass of the albumen powder.

As a result: the hydrated slurry was dark in color as measured by LAB color difference and had a b value of 14.8.

Example 5

(1) Crushing: pulverizing semen Pisi Sativi to 88 mesh. Ensures the water dissolving speed of the pea protein and is convenient for separating the pea protein.

(2) Leaching: mixing pea powder with water at a weight ratio of 1:16, stirring at 52 deg.C for 35min, pulverizing with multi-stage homogenizing pump, transferring to storage tank, sterilizing with microwave for 2-8min, storing for 30-50min, and separating; the maturation period of the raw material pea is 13 months, so that the stability and the compact structure of the pea protein molecule are ensured. Water was used as the extractant to avoid yellow coloration of pea isoflavones by isomerization at high PH. The microwave promotes the extraction of pea protein and simultaneously inactivates, ensures the functionality of the protein, reduces the activity of trypsin inhibitor and improves the nutritive value. High temperature controls microorganisms, avoids yellow and other color secondary metabolites.

(3) Centrifugal separation: performing centrifugal separation on the liquid phase subjected to sterilization treatment in the step (2) to obtain primary pea residues and primary pea milk, washing the primary pea residues with water to obtain secondary pea residues and secondary pea milk, and mixing the primary pea milk and the secondary pea milk to obtain a pea milk mixture; the fiber and the pea starch can be recovered from the primary pea dregs and the secondary pea dregs.

(4) Acid precipitation: adjusting the pH value of the pea milk mixture to 4.7, and performing isoelectric point precipitation to obtain an acid precipitation solution.

(5) Centrifugal separation: and (4) carrying out centrifugal separation on the acid precipitation solution in the step (4) to obtain the acidic solid-phase protein slurry.

(6) Neutralizing: diluting the acidic solid-phase protein slurry with 2 times of water, homogenizing under 22MPa, continuously neutralizing the diluted acidic protein solution and the diluted food-grade alkali by a static mixer, and adjusting the pH to 7.0; brix 13.9. The pH time of the protein slurry is ensured to be lower than or equal to 7.3 by continuously adding alkali, so that the conversion of pea isoflavone and the conversion of related pigments are avoided, and further, the generation of yellow and other pigments is avoided, and the color is white.

(7) And (3) sterilization: instantly sterilizing the protein pulp at high temperature, wherein the sterilization temperature is 132 ℃ for 7 seconds; achieving the process sterilization.

(8) Vacuum degassing: vacuum degassing after sterilization, wherein the vacuum degree is controlled to be 66 kPa; the beany flavor is removed by vacuum degassing.

(9) And (3) heat preservation: placing the degassed protein slurry in a heat-preserving tank, preserving the heat for 39 minutes at 74 ℃ to stretch the globular protein, so that the globular protein is conveniently dispersed in water; and the pigment is damaged, and yellow and other miscellaneous colors are reduced.

(10) Spray drying: the albumen powder is prepared by spray drying, and meanwhile, the elbow is sprayed with water-soluble phospholipid, and the addition amount of the water-soluble phospholipid is 1.2 per mill of the mass of the albumen powder.

As a result: the hydrated slurry was dark in color as measured by LAB color difference and had a b value of 14.4.

Comparative example 1

(1) Crushing: pulverizing semen Pisi Sativi to 55 mesh.

(2) Leaching: mixing pea powder with water at a weight ratio of 1:19, stirring at 30 deg.C for 145min, pulverizing with a multi-stage homogenizing pump, transferring to a storage tank, sterilizing with microwave for 6min, storing for 70min, and separating; the maturation period of the raw material pea is 29 months, so that the stability and the compact structure of the pea protein molecule are ensured.

(3) Centrifugal separation: performing centrifugal separation on the extracting solution in the step (2) to obtain primary pea residues and primary pea milk, washing the primary pea residues with water to obtain secondary pea residues and secondary pea milk, and mixing the primary pea milk and the secondary pea milk to obtain a pea milk mixture;

(4) acid precipitation: adjusting the pH value of the pea milk mixture to 4.3, and performing isoelectric point precipitation to obtain an acid precipitation solution.

(5) Centrifugal separation: and (4) carrying out centrifugal separation on the acid precipitation solution in the step (4) to obtain the acidic solid-phase protein slurry.

(6) Neutralizing: diluting the acidic solid-phase protein slurry with 2 times of water, homogenizing under 22MPA, continuously neutralizing the diluted acidic protein slurry and the diluted food-grade alkali by a static mixer, and adjusting the pH to 7.9; brix 15.

(7) And (3) sterilization: instantly sterilizing the protein pulp at high temperature, wherein the sterilization temperature is 125 ℃ for 22 seconds; achieving the process sterilization.

(8) Vacuum degassing: vacuum degassing is carried out after sterilization, and the vacuum degree is controlled to be 70 kpa; the beany flavor is removed by vacuum degassing.

(9) And (3) heat preservation: placing the degassed protein slurry in a heat preservation tank, and preserving the heat at 70 ℃ for 45 minutes.

(10) Spray drying: the protein powder is prepared by spray drying, and meanwhile, the elbow is sprayed with water-soluble phospholipid, and the addition amount of the water-soluble phospholipid is 2 per mill of the mass of the protein powder.

Compared with the production method of the invention, the grinding fineness of the comparative example 1 is too large, the extraction water temperature is too low, the extraction stirring time is too long, the storage time after microwave sterilization treatment is too long, the pea maturation period is too long, the pH value of the pea milk mixture in the acid precipitation step is too low, the pH value in the neutralization step is too high, the Brix is too high, the sterilization time is too long, and the results are as follows: the hydrated slurry was dark in color as measured by LAB color difference, with a b value of 22, yellow in color, an a value of 5, and red in color.

It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. And obvious variations or modifications therefrom are within the scope of the invention.