Bean protein composition and preparation method thereof
阅读说明：本技术 豆类蛋白组合物及其制备方法 (Bean protein composition and preparation method thereof ) 是由 王凯 郑妍 杨武林 于 2019-11-29 设计创作，主要内容包括：本发明涉及豆类蛋白组合物及其制备方法。本发明的豆类蛋白组合物,其中以重量比计,皂苷B与DDMP皂苷比例为25:1～150:1,所述DDMP皂苷是2,3-二氢-2,5-二羟基-6-甲基-4h-吡喃-4-酮皂苷。本发明的豆类蛋白组合物的制备方法,包括依次进行以下的步骤：添加盐的步骤：使豆类蛋白源与强碱弱酸盐接触,和酶解步骤：使豆类蛋白源与糖苷酶接触。本发明的豆类蛋白组合物的高溶解性、高乳化性且苦味显著减弱,具有良好的口感和加工特性,且变性程度底,无可溶性蛋白损失,保持了含量较高的高分子豆类蛋白。(The invention relates to a pulse protein composition and a preparation method thereof. The bean protein composition comprises, by weight, 25: 1-150: 1 of saponin B and DDMP saponin, wherein the DDMP saponin is 2,3-dihydro-2,5-dihydroxy-6-methyl-4h-pyran-4-one saponin. The preparation method of the pulse protein composition comprises the following steps of: step of salt addition: contacting a pulse protein source with a strong base and a weak acid salt, and an enzymatic hydrolysis step: contacting a pulse protein source with a glycosidase. The pulse protein composition has high solubility, high emulsibility, obviously reduced bitter taste, good mouthfeel and processing characteristics, low denaturation degree, no loss of soluble protein and high-molecular pulse protein content.)
1. A bean protein composition comprises, by weight, 25: 1-150: 1 of saponin B and DDMP saponin, wherein the DDMP saponin is 2,3-dihydro-2,5-dihydroxy-6-methyl-4h-pyran-4-one saponin.
2. The composition according to claim 1, wherein the ratio of saponin B to DDMP saponin is 30: 1-140: 1 by weight, preferably the ratio of saponin B to DDMP saponin is 40: 1-120: 1 by weight, and/or the content of saponin B is 10-100 mg/kg, preferably the content of saponin B is 15-80 mg/kg, preferably the content of saponin B is 20-60 mg/kg.
3. The composition according to any one of claims 1 to 2, wherein the protein content of the supernatant is 60 to 85% by weight,
wherein the protein content in the supernatant is calculated by the following formula,
NSI = (protein content in supernatant)/(total protein content of sample) × 100%,
wherein the protein content is determined according to the Kjeldahl method described in the national standard GB5009.5-2016 of the people's republic of China, preferably the protein content in the supernatant is 60-83 wt%, preferably the protein content in the supernatant is 65-80 wt%, and/or the protein content is 40-70 wt% based on the total amount of the composition, preferably the protein content is 42-65 wt% based on the total amount of the composition, preferably the protein content is 45-60 wt% based on the total amount of the composition.
4. According to the claimsObtaining a composition having an emulsifying activity index of 12 to 18m in any one of 1 to 32The emulsifying activity index is expressed by EAI and is obtained by calculation according to the following formula,
where EAI is the emulsified area of 1g of sample in m2/g；A500The light absorption value is measured at the wavelength of 500 nm; n is the dilution factor; theta is the proportion of the oil phase; c is the concentration of the sample water solution, the unit is g/mL, and the preferred emulsifying activity index is 12.2-17 m2Preferably, the emulsifying activity index is 12.5-16 m2(ii) a/g, and/or,
the emulsion stability index is 14-25 min and is expressed by ESI and is obtained by calculating according to the following formula,
wherein, A0: absorbance value At 0min, At: tmin-time absorbance value, Δ T: and the difference value of tmin and 0min is preferably 15-24 min, preferably 16-23 min, and/or the beans are selected from at least one of peas, black beans, mung beans, red beans, cowpeas, lentils, broad beans or chickpeas.
5. A method for preparing a pulse protein composition, comprising the steps of sequentially:
step of salt addition: contacting the pulse protein source with a strong base and a weak acid salt, and
an enzymolysis step: contacting a pulse protein source with a glycosidase.
6. The method according to claim 5, wherein the pH of the strong base constituting the weak acid salt of strong base is 12 to 14, and/or the pKa of the weak acid constituting the weak acid salt of strong base is 4.5 to 6.5, and/or the weak acid salt of strong base is selected fromAt least one of organic acid salt or inorganic acid salt, preferably the strong base weak acid salt is selected from carbonate, bicarbonate or acetate, preferably the strong base weak acid salt is selected from at least one of alkali metal salt or alkaline earth metal salt, preferably the strong base weak acid salt is selected from Na2CO3、K2CO3、NaHCO3、CH3And the concentration of at least one of COONa and/or the strong alkali and weak acid salt is 0.001-0.1 mol/L.
7. The production method according to any one of claims 5 to 6, wherein the step of adding a salt comprises contacting the pulse protein source with the strong base weak acid salt at a temperature of 45 to 60 ℃, and/or the step of adding a salt comprises dispersively dissolving the pulse protein source in water, and/or the weight ratio of the pulse protein source to water is 1:8 to 1:20, and/or the strong base weak acid salt is added in an amount of 0.001 to 1 wt% relative to the pulse protein source aqueous dispersion, and/or the step of adding a salt comprises stirring for 10 to 30min after the addition of a salt, and/or the step of enzymatically hydrolyzing comprises a glycosidase to pulse protein source weight ratio of 1:2000 to 1:20, preferably the step of enzymatically hydrolyzing comprises a glycosidase to pulse protein source weight ratio of 1:1500 to 1:30, preferably the step of enzymatically hydrolyzing, the weight ratio of the glycosidase to the bean protein source is 1: 1000-1: 50.
8. The preparation method according to any one of claims 5 to 7, wherein in the enzymolysis step, the enzymolysis temperature is 45 to 60 ℃, and/or in the enzymolysis step, the glycosidase is selected from beta-glucosidase, xylosidase and rhamnosidase or a compound enzyme of the three glycosidases, and/or in the enzymolysis step, the reaction time is 0.5 to 12 hours, and/or in the enzymolysis step, pH adjustment is not performed, and/or a sterilization step is further included after the enzymolysis step, and/or a drying step is further included after the sterilization step, and/or in the drying step, the enzymolysis reaction solution is sterilized and then spray-dried or freeze-dried, and/or the spray-drying condition is that the air inlet temperature is 160 to 190 ℃, the air outlet temperature is 75 to 95 ℃, and/or the bean protein source is selected from peas, At least one of black beans, mung beans, red beans, cowpeas, lentils, broad beans or chickpeas, and/or the pulse protein source is obtained by peeling pulses, and/or the peeled pulses are pulverized and air-stream classified by dry classification.
9. A pulse protein composition produced by the production method according to any one of claims 5 to 8.
10. Use of the pulse protein composition according to any one of claims 1 to 4 and the pulse protein composition prepared by the preparation method according to any one of claims 5 to 8 for preparing a food, preferably the food is selected from at least one of a baked food, a beverage, a sauce, an energy bar, an extruded food, a meat and a meat product.
Technical Field
The invention relates to a pulse protein composition and a preparation method thereof.
Background
Pea protein is hypoallergenic plant protein, has balanced nutrition, is rich in multiple essential amino acids required by human bodies, and has an amino acid composition close to the FAO/WHO recommended value. At present, pea protein is extracted industrially by two ways, namely a wet extraction process and a dry classification process, the wet extraction process is commonly used, pea protein concentrate and pea protein isolate are extracted mainly by means of acid dissolution, alkali dissolution, centrifugation, spray drying and other process means, the process consumes a large amount of energy in production, generates a large amount of waste water and causes serious environmental pollution, and the pea protein obtained by the wet process is seriously denatured, so that the functional characteristics of solubility, emulsibility and the like are poor, and the application of the pea protein is influenced. The dry-method classification process mainly utilizes the crushing and airflow classification modes to enrich the pea protein, the protein obtained by the process has low denaturation degree, no wastewater is generated in the production process, and the process accords with the production concept of nature and environmental protection.
The saponin is an oligosaccharide glycoside with a complex structure, widely exists in various plants, and has biological activities of resisting inflammation, oxidation and tumor, enhancing the body immunity regulation and the like. The content of total saponins in peas is generally 0.8-2.5 g/kg, two most common oleanane type saponins such as DDMP saponin and saponin B are used as main saponins, wherein the content ratio of DDMP saponin to saponin B is about 4:1, and the DDMP saponin takes soyasapogenol B as an aglucone and is combined with 2,3-dihydro-2,5-dihydroxy-6-methyl-4h-pyran-4-one (DDMP) on a C-22 position. Both DDMP saponin and saponin B have bitter taste, wherein the bitter taste of DDMP saponin is extremely strong and much stronger than that of saponin B.
At present, in order to improve the problem of poor functional properties of pea protein, modification methods such as physical methods and enzymatic methods are often adopted to achieve the goal of improving solubility and other functional properties by modifying the molecular structure of protein or reducing the particle size of protein particles, for example, the jagil corporation (CN 107950748A) adds high-pressure homogenization in a pea extraction process to obtain a pea protein composition with a nitrogen solubility index of greater than or equal to 88%; the southern China university (CN 102250201B) utilizes carbohydrase combined jet cooking treatment to obtain high-solubility pea protein; protein modification is carried out by using transglutaminase at the university of south China (CN 101703147A) to obtain pea protein with better emulsibility. While less research has been done on improving the bitterness of pea proteins, there are only a few studies on reducing bitterness by physical means, such as: frederick William comber (US 4022919A) reduces the bitterness of pea protein flour by heat steaming.
At present, most of patent methods modify pea proteins with high denaturation degree extracted by a wet method to improve the functionality of the pea proteins, however, researches on further improving the functionality of the pea proteins extracted by the dry method while reducing the bitter taste of the pea proteins are rarely reported.
Disclosure of Invention
The inventor unexpectedly finds that the content of saponin B in pea protein and the proportion of the saponin B to DDMP saponin can be controlled by strong alkali weak acid salt and glycosidase when researching and removing the bitter taste of the bean protein subjected to dry fractionation, and obtains the bean protein composition with high solubility, high emulsibility and remarkably reduced bitter taste.
The bean protein composition comprises, by weight, 25: 1-150: 1 of saponin B and DDMP saponin, wherein the DDMP saponin is 2,3-dihydro-2,5-dihydroxy-6-methyl-4h-pyran-4-one saponin.
The bean protein composition provided by the invention has the advantages that the ratio of the saponin B to the DDMP saponin is 30: 1-140: 1 in terms of weight ratio.
The bean protein composition provided by the invention has the advantages that the ratio of the saponin B to the DDMP saponin is 40: 1-120: 1 in terms of weight ratio.
The bean protein composition provided by the invention has the saponin B content of 10-100 mg/kg.
The bean protein composition provided by the invention has the saponin B content of 15-80 mg/kg.
The bean protein composition provided by the invention has the saponin B content of 20-60 mg/kg.
The legume protein composition of the present invention comprises a supernatant having a protein content of 60 to 85 wt%,
wherein the protein content in the supernatant is calculated by the following formula,
NSI = (protein content in supernatant)/(total protein content of sample) × 100%,
wherein the protein content is determined according to Kjeldahl method described in national standard GB5009.5-2016 of the people's republic of China.
The legume protein composition of the present invention comprises 60 to 83 wt% of protein in the supernatant.
The legume protein composition of the present invention comprises 65-80 wt% protein in the supernatant.
The legume protein composition according to the present invention has a protein content of 40 to 70 wt% based on the total amount of the composition.
The legume protein composition according to the present invention has a protein content of 42 to 65 wt% based on the total amount of the composition.
The bean protein composition has the protein content of 45-60 wt% based on the total weight of the composition.
The bean protein composition has the emulsifying activity index of 12-18 m2The emulsifying activity index is expressed by EAI and is obtained by calculation according to the following formula,
where EAI is the emulsified area of 1g of sample in m2/g；A500The light absorption value is measured at the wavelength of 500 nm; n is the dilution factor; theta is the proportion of the oil phase; c is the concentration of the aqueous sample solution in g/mL.
The bean protein composition has the emulsifying activity index of 12.2-17 m2/g。
According to the inventionThe bright bean protein composition has the emulsifying activity index of 12.5-16 m2/g。
The legume protein composition has an emulsion stability index of 14-25 min, wherein the emulsion stability index is expressed by ESI and is calculated by the following formula,
wherein, A0: absorbance value At 0min, At: tmin-time absorbance value, Δ T: difference between tmin and 0 min.
The bean protein composition has an emulsification stability index of 15-24 min.
The bean protein composition has an emulsification stability index of 16-23 min.
The bean protein composition according to the invention is at least one of peas, black beans, mung beans, red beans, cowpeas, lentils, broad beans or chickpeas.
The preparation method of the pulse protein composition comprises the following steps of:
step of salt addition: contacting the pulse protein source with a strong base and a weak acid salt, and
an enzymolysis step: contacting a pulse protein source with a glycosidase.
The preparation method of the bean protein composition comprises the step of forming a strong base of the strong base and weak acid salt at a pH of 12-14.
The preparation method of the bean protein composition comprises the step of forming the weak acid of the strong base weak acid salt with pKa 4.5-6.5.
The preparation method of the pulse protein composition according to the invention, wherein the strong base and weak acid salt is at least one of organic acid salt or inorganic acid salt.
The preparation method of the bean protein composition according to the invention is characterized in that the strong base and weak acid salt is selected from carbonate, bicarbonate or acetate.
The method for preparing the pulse protein composition according to the present invention, wherein the strong and weak acid salt is at least one selected from alkali metal salts and alkaline earth metal salts.
The preparation method of the bean protein composition according to the invention, wherein the strong alkali and weak acid salt is selected from Na2CO3、K2CO3、NaHCO3、CH3And (4) COONa.
The preparation method of the pulse protein composition comprises the step of preparing a pulse protein composition, wherein the concentration of the strong alkali and the weak acid salt is 0.001-0.1 mol/L.
The preparation method of the pulse protein composition comprises the step of contacting the pulse protein source with the strong base and weak acid salt at the temperature of 45-60 ℃ in the salt adding step.
The method for preparing a leguminous protein composition according to the present invention, wherein the step of adding a salt, the leguminous protein source is dispersedly dissolved in water.
The preparation method of the pulse protein composition comprises the step of mixing a pulse protein source and water in a weight ratio of 1: 8-1: 20.
The preparation method of the leguminous protein composition according to the present invention includes adding the strong alkali and weak acid salt in an amount of 0.001 to 1 wt% based on the aqueous dispersion of the leguminous protein source.
The preparation method of the pulse protein composition comprises the step of adding salt, and stirring for 10-30 min after adding the salt.
According to the preparation method of the bean protein composition, in the enzymolysis step, the weight ratio of glycosidase to bean protein source is 1: 2000-1: 20.
According to the preparation method of the bean protein composition, in the enzymolysis step, the weight ratio of glycosidase to bean protein source is 1: 1500-1: 30.
According to the preparation method of the bean protein composition, in the enzymolysis step, the weight ratio of glycosidase to bean protein source is 1: 1000-1: 50.
According to the preparation method of the bean protein composition, in the enzymolysis step, the enzymolysis temperature is 45-60 ℃.
The preparation method of the bean protein composition according to the invention, wherein in the enzymolysis step, the glycosidase is selected from beta-glucosidase, xylosidase and rhamnosidase or a complex enzyme of the three glycosidases.
According to the preparation method of the bean protein composition, in the enzymolysis step, the reaction time is 0.5-12 hours.
The method for preparing the legume protein composition according to the present invention, wherein the enzymatic hydrolysis step is performed without pH adjustment.
The preparation method of the legume protein composition according to the present invention further comprises a sterilization step after the enzymatic hydrolysis step.
The method for preparing the pulse protein composition according to the present invention further comprises a drying step after the sterilization step.
The preparation method of the pulse protein composition according to the present invention, wherein the drying step is to sterilize the enzymolysis reaction solution and then spray-dry or freeze-dry the enzymolysis reaction solution.
According to the preparation method of the bean protein composition, the spray drying condition is that the air inlet temperature is 160-190 ℃ and the air outlet temperature is 75-95 ℃.
The method for preparing the bean protein composition according to the invention, wherein the bean protein source is at least one selected from peas, black beans, mung beans, red beans, cowpeas, lentils, broad beans or chickpeas.
The method for preparing a pulse protein composition according to the present invention, wherein the pulse protein source is obtained by peeling a pulse.
The method for preparing a pulse protein composition according to the present invention, wherein dehulled pulses are pulverized and air-classified by dry classification.
A pulse protein composition prepared by the method for preparing a pulse protein composition of the present invention.
The invention relates to a pulse protein composition and application of the pulse protein composition prepared by the pulse protein composition preparation method in preparing food.
According to the use of the present invention, the food is selected from at least one of a baked good, a beverage, a sauce, an energy bar, an extruded food, a meat and a meat product.
Effects of the invention
The pulse protein composition of the invention has high solubility and emulsibility, and the bitterness is obviously reduced. Compared with the bean protein concentrate obtained by dry classification, the bean protein composition has good mouthfeel and processing characteristics. The bean protein composition has low denaturation degree, no loss of soluble protein, and high-molecular bean protein content compared with the processes of preparing bean protein by protease enzymolysis and the like.
Detailed Description
Leguminous protein compositions
In the present invention, it is sometimes referred to as "pulse protein composition of the present invention" or "pulse protein composition".
The bean protein composition comprises, by weight, 25: 1-150: 1 of saponin B and DDMP saponin. The DDMP saponin is 2,3-dihydro-2,5-dihydroxy-6-methyl-4h-pyran-4-one saponin.
In a preferred embodiment of the pulse protein composition of the present invention, the ratio of saponin B to DDMP saponin is 30:1 to 140:1 by weight, and more preferably, the ratio of saponin B to DDMP saponin is 40:1 to 120:1 by weight.
In a specific embodiment of the pulse protein composition of the present invention, the ratio of saponin B to DDMP saponin is 30: 1. 46: 1. 52: 1. 55: 1. 59: 1. 64: 1. 78: 1. 85: 1. 94: 1. 101: 1.
in the bean protein composition, the content of the saponin B is 10-100 mg/kg.
In a preferred embodiment of the present invention, the content of saponin B is 15-80 mg/kg, and more preferably 20-60 mg/kg.
In a particular embodiment of the pulse protein composition of the invention, the saponin B content is 10.115mg/kg, 17.084mg/kg, 23.677mg/kg, 32.687mg/kg, 47.811mg/kg, 49.192mg/kg, 49.796mg/kg, 52.928mg/kg, 55.935mg/kg, 79.892 mg/kg.
The bean protein composition of the invention has a protein content of 40-70 wt% based on the total weight of the composition.
In a preferred embodiment of the pulse protein composition of the present invention, the protein content is 42 to 65 wt% based on the total amount of the composition, and more preferably 45 to 60 wt% based on the total amount of the composition.
In a particular embodiment of the pulse protein composition of the invention, the protein content is 45.8 wt.%, 50.8 wt.%, 51.9 wt.%, 52.3 wt.%, 53.5 wt.%, 54.4 wt.%, 55.1 wt.%, 55.8 wt.%, 59.7 wt.%, based on the total composition.
In the present invention, the "protein content" is sometimes referred to as "concentrated protein content".
In the bean protein composition, the protein content in the supernatant is 60-85 wt%,
wherein the protein content in the supernatant is calculated by the following formula,
NSI = (protein content in supernatant)/(total protein content of sample) × 100%,
wherein the protein content is determined according to Kjeldahl method described in national standard GB5009.5-2016 of the people's republic of China.
In a preferred embodiment of the pulse protein composition of the present invention, the protein content of the supernatant is 60 to 83 wt%, and more preferably, the protein content of the supernatant is 65 to 80 wt%.
In a particular embodiment of the pulse protein composition of the invention, the protein content in the supernatant is 69.8 wt.%, 70.2 wt.%, 7.03 wt.%, 70.7 wt.%, 71.6 wt.%, 73.8 wt.%, 75.4 wt.%, 76.4 wt.%, 79.7 wt.%, 82.3 wt.%.
The bean protein composition has the emulsifying activity index of 12-18 m2The emulsifying activity index is expressed by EAI and is obtained by calculation according to the following formula,
where EAI is the emulsified area of 1g of sample in m2/g；A500The light absorption value is measured at the wavelength of 500 nm; n is the dilution factor; theta is the proportion of the oil phase; c is the concentration of the aqueous sample solution in g/mL.
In a preferred embodiment of the present legume protein composition, the legume protein composition has an emulsifying activity index of 12.2 to 17m2The bean protein composition has an emulsifying activity index of 12.5-16 m2/g。
In a particular embodiment of the pulse protein composition of the invention, the pulse protein composition has an emulsifying activity index of 12.4m2/g、12.7m2/g、13.9m2/g、14.0m2/g、15.1m2/g、15.7m2/g、15.9m2/g、16.4m2/g、17.8m2/g。
The bean protein composition has an emulsion stability index of 14-25 min, wherein the emulsion stability index is expressed by ESI and is obtained by calculation according to the following formula,
wherein, A0: absorbance value At 0min, At: tmin-time absorbance value, Δ T: difference between tmin and 0 min.
In a preferred embodiment of the present invention, the pulse protein composition has an emulsion stability index of 15 to 24min, more preferably 16 to 23 min.
In the present invention, the beans are selected from at least one of peas, black beans, mung beans, red beans, cowpeas, lentils, broad beans or chickpeas.
The pulse protein composition of the invention can be used for preparing food.
Preparation method of bean protein composition
The preparation method of the pulse protein composition comprises the following steps of:
step of salt addition: contacting the pulse protein source with a strong base and a weak acid salt, and
an enzymolysis step: contacting a pulse protein source with a glycosidase.
In the preparation method of the bean protein composition, the pH value of the strong base forming the strong base and weak acid salt is 12-14.
In the method for producing a leguminous protein composition of the present invention, the weak acid constituting the strong base and weak acid salt has a pKa of 4.5 to 6.5.
In the method for preparing the pulse protein composition, the strong base and weak acid salt is at least one selected from organic acid salt or inorganic acid salt.
In the present invention, the strong base and weak acid salt is selected from carbonate, bicarbonate or acetate.
In the present invention, the weak acid and strong base salt is at least one selected from alkali metal salts and alkaline earth metal salts.
In the method for preparing the pulse protein composition of the invention, the strong alkali and weak acid salt is selected from Na2CO3、K2CO3、NaHCO3、CH3And (4) COONa.
In the preparation method of the pulse protein composition, the concentration of the strong alkali and the weak acid salt is 0.001 mol/L-0.1 mol/L.
In the method for preparing the pulse protein composition, in the step of adding salt, the pulse protein source is contacted with the strong base and weak acid salt at the temperature of 45-60 ℃.
In the method for producing a leguminous protein composition of the present invention, in the step of adding a salt, the leguminous protein source is dispersedly dissolved in water.
In the preparation method of the pulse protein composition, the weight ratio of the pulse protein source to water is 1: 8-1: 20. Specifically, the weight ratio of the leguminous protein source to water is 1:8, 1:10, 1:15 and 1: 20.
In the method for producing a leguminous protein composition of the present invention, the strong base and weak acid salt is added in an amount of 0.001 to 1 wt% based on the aqueous dispersion of a leguminous protein source.
In the preparation method of the pulse protein composition, in the step of adding salt, the mixture is stirred for 10-30 min after the salt is added.
In the preparation method of the bean protein composition, in the enzymolysis step, the weight ratio of glycosidase to bean protein source is 1: 2000-1: 20, preferably, in the enzymolysis step, the weight ratio of glycosidase to bean protein source is 1: 1500-1: 30, and more preferably, in the enzymolysis step, the weight ratio of glycosidase to bean protein source is 1: 1000-1: 50. Specifically, in the enzymolysis step, the weight ratio of the glycosidase to the bean protein source is 1:20, 1:50, 1:100, 1:200, and 1: 1000.
In the preparation method of the bean protein composition, in the enzymolysis step, the enzymolysis temperature is 45-60 ℃.
In the preparation method of the bean protein composition, in the enzymolysis step, the glycosidase is selected from beta-glucosidase, xylosidase and rhamnosidase or a complex enzyme of the three glycosidases.
In the preparation method of the bean protein composition, in the enzymolysis step, the reaction time is 0.5-12 h.
In the method for preparing the pulse protein composition of the invention, in the enzymolysis step, pH adjustment is not carried out.
In the preparation method of the pulse protein composition, a sterilization step is further included after the enzymolysis step.
In the method for preparing the pulse protein composition of the present invention, a drying step is further included after the sterilization step.
In the preparation method of the pulse protein composition, the drying step is to sterilize the enzymolysis reaction solution and then spray-dry or freeze-dry the enzymolysis reaction solution.
In the preparation method of the bean protein composition, the spray drying condition is that the air inlet temperature is 160-190 ℃ and the air outlet temperature is 75-95 ℃.
In the method for preparing the bean protein composition of the present invention, the bean protein source is at least one selected from peas, black beans, mung beans, red beans, cowpeas, lentils, broad beans or chickpeas.
The above-mentioned pulse protein source may be used as it is in the present invention, and may be used after the following pretreatment. The pretreatment is, for example, to subject the legume protein source to dehulling of the legume, followed by crushing and air-classifying of the dehulled legume by dry classification.
Specifically, for example, the pulse protein source is first dry-pulverized, and then air-flow classified to obtain a fraction with smaller particles, i.e., a pulse protein concentrate, which is used as a pulse protein source after pretreatment.
The above-mentioned pulse protein composition of the present invention can be prepared by the method for preparing the pulse protein composition of the present invention.
The pulse protein composition prepared by the method for preparing the pulse protein composition of the present invention can be used for preparing foods. The food is not particularly limited, and for example, at least one of a baked food, a beverage, a sauce, an energy bar, an extruded food, meat, and a meat product.
The following detailed description of various aspects of the present invention is provided in connection with examples to provide a better understanding of the present invention, but the scope of the present invention is not limited thereto.
In the present invention, the technical means in the respective embodiments, preferred embodiments and specific embodiments may be arbitrarily combined, and the technical means obtained by combining them are within the scope of the present invention.
The following examples use instrumentation conventional in the art. The experimental procedures, in which specific conditions are not noted in the following examples, are generally carried out under conventional conditions or conditions recommended by the manufacturers. In the following examples, various starting materials were used, and unless otherwise specified, conventional commercially available products were used. In the description of the present invention and the following examples, "%" represents weight percent unless otherwise specified.
Examples
1. Materials:
in all embodiments of the invention the peas are yellow peas.
2. The experimental method comprises the following steps:
2.1 the protein content in all embodiments of the invention can be determined according to Kjeldahl method of national standard GB5009.5-2016 (determination of protein in food safety national standard food) of the people's republic of China.
2.2 the NSI value of the protein in all embodiments of the invention can be determined according to the following method.
A 0.5g protein sample was accurately weighed, dispersed in 40mL of distilled water (buffer solution of pH = 7.2), shaken at room temperature for 1h, centrifuged at 4500 rpm for 10min, and the protein content in the supernatant and the protein content of the sample were measured.
NSI = (protein content in supernatant)/(total protein content of sample) × 100%
Wherein the protein content is determined according to Kjeldahl method in national standard GB5009.5-2016 determination of protein in food safety national standard food.
2.3 protein EAI and ESI values described in all embodiments of the invention can be determined according to the following methods.
Taking 45mL of 1% (W/V) sample water solution (the sample is dissolved in 0.1mol/L phosphate buffer solution with pH value of 7.0), adding 15mL of soybean oil, shearing at room temperature for 1min at 10000rpm with a high-speed shearing machine, quickly sampling from the bottom, diluting with 0.1% (W/V) Sodium Dodecyl Sulfate (SDS) solution by 100 times, and measuring the absorbance A at 500nm500This value is the absorbance at time 0. After 10min, samples were taken from the bottom and diluted with SDS and the procedure was repeated, and the value determined was the absorbance at 10min, while SDS solution was used as a blank.
EAI (emulsifying activity index) indicates emulsifiability:
where EAI is the emulsified area of 1g of sample in m2(ii)/g; n is the dilution factor; theta is the proportion of the oil phase; c is the concentration of the aqueous sample solution,the unit is g/mL.
ESI (emulsion stability index) indicates emulsion stability:
wherein, A0: absorbance value At 0min, At: tmin-time absorbance value, Δ T: difference between tmin and 0 min.
2.4 in all embodiments of the invention the saponin content may be determined by HPLC-ELSD as follows.
Sample pretreatment:
defatting pea protein powder with n-hexane for 6 hr, air drying overnight in fume hood, dispersing and dissolving 1g defatted pea protein powder with 70% (v/v) ethanol (100 mL), extracting in a gas bath shaker at 25 deg.C under oscillation at 200 rpm for 1 hr, filtering the crude extract with slow speed filter paper, volatilizing residual ethanol in the filtrate at 27 deg.C (15 min), diluting the ethanol volatilized filtrate with distilled water to 40mL, then centrifuging for 10min at 10 deg.C and 15000g, passing the obtained supernatant through Sep-Pak C18 solid phase extraction column, then washing with 15mL of clear water to remove non-adhered substances, eluting with 10 mL of methanol, air drying the eluate, dissolving the dried saponin sample in 1 mL of 50% (v/v) ethanol, centrifuging at 15000g for 10min, and collecting supernatant for measuring saponin content.
Pea manufacturers: linyi city nalun trade limited, glycosidase manufacturers: qingdao blue biological corporation, sodium carbonate manufacturer: the Shanghai pharmaceutical reagent group and other chemical reagents are all from the Shanghai pharmaceutical reagent group.
Chromatographic conditions for measuring saponin by HPLC-ELSD:
a chromatographic column: kromasil C18(150 mm. times.4.6 mm, 5.0 μm) chromatography column
Mobile phase: 0.1% acetic acid (A) -acetonitrile (B)
Gradient elution: 0 → 8min, 40 → 50% B
8→10min，50→100% B
10→15min，100% B
15→20 min，100%→40% B
Operating time: 25 min;
flow rate: 1.0 to 1.0 m L/min,
sample introduction amount: 20 μ L
Column temperature: 25 deg.C
Evaporation photodetector drift tube temperature: 40 deg.C
Atomizing: n is a radical of2
Gas flow rate: 2.5L/min
And (3) taking soybean saponin Bb, alpha g and beta g standard products (the purity is more than or equal to 98%) as reference products to calibrate the content of the pea saponin B and the DDMP saponin. (method reference: Simultaneous quantification of differential glycosylated, acetylated, and 2,3-dihydro-2, 5-dihydroxy-6-methyl-4H-pyran-4-one-connected soybean milk production conversion-phase high-performance chromatography with improved light scattering detection).
2.5 evaluation of bitterness in the present invention the sensory evaluation was carried out by tissue tasters, all of which were sensitive to bitterness, scored from 1 to 5 for bitterness, 1 for no bitterness and 5 for strong bitterness. Sensory evaluation was carried out at 0.5g per sample, and the results were scored on an average scale.
2.6 the "pea protein concentrate" of the present invention was obtained by the following crushing apparatus and classifying apparatus under the following conditions.
Crushing equipment: a graded impact mill (Sichuan sun flow energy powder equipment Co., Ltd.);
grading equipment: an air classifier (Sichuan Mianyang powder plant Co., Ltd.);
and (3) crushing conditions: the frequency of a grinder is 50Hz, the frequency of a grader is 50Hz, the frequency of an induced draft fan is 30Hz, the grinding temperature is lower than 40 ℃, the grinding treatment capacity is 20kg/h, and the grinding particle size D90= 34-40 μm;
grading conditions: the frequency of a classifier is 50Hz, the frequency of an induced draft fan is 35Hz, the classifying treatment capacity is 10kg/h, and the enriched and thin part crushed particle size D90= 18-22 μm.
Examples 1 to 4
The pea protein concentrate is obtained by classifying peas by a dry method, 4 parts of dispersed suspension substrate are respectively prepared according to the feed-liquid ratio of the pea protein concentrate to water of 1:8, 1:10, 1:15 and 1:20, 0.001mol/L of sodium carbonate is added, the mixture is stirred for 30min at the temperature of 50 ℃, glycosidase is added (the mass ratio of the glycosidase to the pea protein concentrate is 1:200), the pH is not regulated, the temperature is kept at 50 ℃, enzymolysis is carried out for 1h, high-temperature steam at the temperature of 140 ℃ is used for carrying out instantaneous sterilization for 15s after the enzymolysis is finished, finally, spray drying is carried out, the air inlet temperature of the spray drying is 190 ℃, and the air outlet temperature is 95 ℃, so that the pea protein concentrate powder.
The results are shown in table 1 below.
TABLE 1
Examples
Ratio of material to liquid
Pea protein concentrate content
Saponin B content (mg/kg)
Saponin B is DDMP saponin
NSI
EAI(m2/g)
ESI(min)
Bitterness score
1
1:8
52.3%
55.935
46:1
70.7%
12.4
18.4
1.4
2
1:10
55.1%
49.796
59:1
73.8%
15.9
20.3
0.9
3
1:15
45.8%
49.192
52:1
69.8%
12.7
17.6
1.7
4
1:20
51.9%
52.928
55:1
70.2%
14.0
18.1
1.0
Example 5 to example 7
The preparation method comprises the steps of carrying out dry classification on peas to obtain pea protein concentrates, preparing 3 parts of a dispersed suspension substrate according to the feed liquid ratio of the pea protein concentrates to water of 1:10, adding 1% of 0.001mol/L sodium carbonate, stirring for 10min at 45 ℃, adding glycosidase (the mass ratio of the glycosidase to the pea protein concentrates is 1:1000, 1:100 and 1:20), adjusting pH, keeping the temperature at 45 ℃, carrying out enzymolysis for 0.5h, carrying out pasteurization after the enzymolysis is finished, and finally carrying out spray drying at the air inlet temperature of 160 ℃ and the air outlet temperature of 75 ℃ to obtain the pea protein concentrate powder.
The results are shown in table 2 below.
TABLE 2
Examples
Glycosidase addition amount
Pea protein concentrate content
Saponin B content (mg/kg)
Saponin B is DDMP saponin
NSI
ESI(m2/g)
EAI(min)
Bitterness score
5
1:50
50.8%
32.687
78:1
75.4%
16.4
19.2
1.3
6
1:100
53.5%
47.811
64:1
71.6%
13.9
15.9
1.7
7
1:1000
52.3%
79.892
30:1
70.3%
12.7
14.7
2.4
Examples 8 to 10
The pea protein concentrate is obtained by dry classification of peas, 3 parts of dispersed suspension substrate is prepared according to the feed-liquid ratio of the pea protein concentrate to water of 1:10, 0.01mol/L sodium carbonate is added for 0.5 percent, the mixture is stirred for 30min at the temperature of 60 ℃, glycosidase is added (the mass ratio of the glycosidase to the pea protein concentrate is 1:50), the pH is not regulated, the temperature is kept at 60 ℃, the enzymolysis is carried out for 4h/8h/12h, high-temperature steam at the temperature of 140 ℃ is used for carrying out instant sterilization for 15s after the enzymolysis is finished, finally, the spray drying is carried out, the air inlet temperature of the spray drying is 180 ℃, and the air outlet temperature is 90 ℃.
The results are shown in table 3 below.
TABLE 3
Examples
Enzymolysis time of glycosidase
Pea protein concentrate content
Saponin B content (mg/kg)
Saponin B is DDMP saponin
NSI
EAI(m2/g)
ESI(min)
Bitterness score
8
4h
55.8%
23.677
85:1
79.7%
15.7
25.2
0.7
9
8h
59.7%
17.084
101:1
82.3%
17.8
21.5
0.5
10
12h
54.4%
10.115
94:1
76.4%
15.1
17.9
0.2
Comparative example 1
Pea is classified by a dry method to obtain pea protein concentrate, 1 part of dispersed suspension substrate is prepared according to the feed-liquid ratio of the pea protein concentrate to water of 1:20, the pH value is adjusted to 9.0 by 0.1mol/L sodium hydroxide, and the pea protein concentrate is leached for 0.5h at the temperature of 45 ℃. Centrifuging at 3000r/min for 30min, collecting supernatant, adjusting pH of the supernatant to 4.5 with 0.1mol/L hydrochloric acid for acid precipitation, centrifuging at 3500r/min for 30min, collecting precipitate, washing with distilled water for 2-3 times, adjusting pH to 7.0 with 0.1mol/L sodium hydroxide, performing instantaneous sterilization with 140 deg.C high temperature steam for 15s, spray drying at 180 deg.C, air outlet temperature of 90 deg.C, and drying to obtain pea protein powder.
Comparative example 2
Pea is classified by a dry method to obtain pea protein concentrate, pea starch (with the purity of 95%) is added according to the mass ratio of 4:1 for blending to obtain a pea protein mixture (with the protein content of 39.3%), 1 part of dispersed suspension substrate is prepared according to the feed-liquid ratio of the pea protein mixture to water of 1:10, 0.01mol/L sodium carbonate is added for 0.5%, the mixture is stirred for 30min at the temperature of 60 ℃, glycosidase is added (the mass ratio of the glycosidase to the pea protein concentrate is 1:50), the pH is not regulated, the temperature is kept at 60 ℃, the enzymolysis is carried out for 1h, high-temperature steam at the temperature of 140 ℃ is used for carrying out instantaneous sterilization for 15s after the enzymolysis is finished, finally, spray drying is carried out, the air inlet temperature of the spray drying is 180 ℃, and the.
Comparative example 3
And (3) classifying peas by a dry method to obtain pea protein enrichment, adding water according to the material-liquid ratio of 1:3 to prepare pea protein slurry, carrying out damp-heat reaction at 110 ℃ for 30min, carrying out dry-heat sterilization at 140 ℃ after the reaction is finished, and drying to obtain the pea protein.
Comparative example 4
Carrying out dry classification on peas to obtain pea protein concentrate, preparing 31 parts of dispersed suspension substrate according to the feed-liquid ratio of the pea protein concentrate to water of 1:10, stirring for 30min at 80 ℃, adding glycosidase (the mass ratio of the glycosidase to the pea protein concentrate is 1:100), adjusting pH, keeping the temperature at 80 ℃, carrying out enzymolysis for 1h, carrying out instantaneous sterilization for 3min by using high-temperature steam at 140 ℃ after the enzymolysis is finished, finally carrying out spray drying, wherein the air inlet temperature of the spray drying is 180 ℃, and the air outlet temperature is 90 ℃ to obtain the pea protein concentrate powder.
Comparative example 5
Carrying out dry classification on peas to obtain pea protein concentrate, preparing 1 part of dispersed suspension substrate according to the feed-liquid ratio of the pea protein concentrate to water of 1:10, stirring for 30min at the temperature of 30 ℃, instantly sterilizing for 30s by using high-temperature steam at the temperature of 140 ℃, finally carrying out spray drying, and carrying out spray drying at the air inlet temperature of 180 ℃ and the air outlet temperature of 90 ℃ to obtain the pea protein concentrate powder.
Comparative example 6
The method comprises the steps of carrying out dry classification on peas to obtain pea protein concentrates, preparing 1 part of a dispersed suspension substrate according to the feed-liquid ratio of the pea protein concentrates to water of 1:10, adding 0.01mol/L of sodium sulfate 0.5%, stirring for 30min at 60 ℃, adding glycosidase (mass ratio of glycosidase to pea protein concentrates is 1:50), adjusting pH, keeping the temperature at 60 ℃, carrying out enzymolysis for 6h, carrying out instantaneous sterilization for 15s by using high-temperature steam at 140 ℃ after the enzymolysis is finished, and finally carrying out spray drying at the air inlet temperature of 180 ℃ and the air outlet temperature of 90 ℃ to obtain the pea protein concentrate powder.
Comparative example 7
The pea protein concentrate is obtained by dry classification of peas, 1 part of dispersed suspension substrate is prepared according to the feed-liquid ratio of the pea protein concentrate to water of 1:10, 0.01mol/L sodium bisulfite of 0.5 percent is added, the mixture is stirred for 30min at the temperature of 60 ℃, glycosidase (the mass ratio of the glycosidase to the pea protein concentrate is 1:50) is added, the pH is not regulated, the temperature is kept at 60 ℃, the enzymolysis is carried out for 6h, after the enzymolysis is finished, high-temperature steam of 140 ℃ is used for carrying out instant sterilization for 15s, finally, the spray drying is carried out, the air inlet temperature of the spray drying is 180 ℃, and the air outlet temperature is 90 ℃, so.
Comparative example 8
The method comprises the steps of carrying out dry classification on peas to obtain pea protein concentrates, preparing 1 part of dispersed suspension substrate according to the feed liquid ratio of the pea protein concentrates to water of 1:10, stirring for 30min at 80 ℃, adding glycosidase (the mass ratio of the glycosidase to the pea protein concentrates is 1:100), adjusting pH, keeping the temperature at 60 ℃, carrying out enzymolysis for 1h, carrying out instantaneous sterilization for 3min by using high-temperature steam at 140 ℃ after the enzymolysis is finished, finally carrying out spray drying, wherein the air inlet temperature of the spray drying is 180 ℃, and the air outlet temperature is 90 ℃ to obtain the pea protein concentrate powder.
The results are shown in Table 4 below.
TABLE 4
Comparative examples
Pea protein concentrate content
Saponin B content (mg/kg)
Saponin B is DDMP saponin
NSI
EAI(m2/g)
ESI(min)
Bitterness score
1
78.3%
12.334
36:1
14.9%
7.7
11.4
3.5
2
38.9%
10.217
31:1
45.3%
8.9
13.7
3.6
3
53.9%
25.436
28:1
56.5%
10.3
12.1
3.0
4
49.2%
11.237
105:1
47.4%
10.4
13.1
3.2
5
52.6%
7.154
37:1
56.3%
10.7
14.7
3.8
6
53.9%
87.356
32:1
54.5%
11.3
12.5
3.2
7
53.0%
85.557
34:1
51.3%
10.4
12.1
3.8
8
52.1%
37.127
23:1
53.5%
10.3
13.6
3.1
- 上一篇：一种医用注射器针头装配设备
- 下一篇：一种玉米水溶性蛋白的制备工艺