CN103609714A - Production method for plant-based milk powder - Google Patents
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- 239000000843 powder Substances 0.000 title claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 15
- 235000020245 plant milk Nutrition 0.000 title abstract 5
- 235000013339 cereals Nutrition 0.000 claims abstract description 37
- 239000002994 raw material Substances 0.000 claims abstract description 17
- 239000006227 byproduct Substances 0.000 claims abstract description 13
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 11
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 10
- 108090000765 processed proteins & peptides Proteins 0.000 claims abstract description 6
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 claims abstract description 5
- 235000020985 whole grains Nutrition 0.000 claims abstract description 3
- 239000000463 material Substances 0.000 claims description 67
- 241000196324 Embryophyta Species 0.000 claims description 36
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 29
- 238000003756 stirring Methods 0.000 claims description 25
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- 235000013336 milk Nutrition 0.000 claims description 24
- 239000008267 milk Substances 0.000 claims description 24
- 210000004080 milk Anatomy 0.000 claims description 24
- 239000007853 buffer solution Substances 0.000 claims description 19
- 239000007788 liquid Substances 0.000 claims description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 235000011389 fruit/vegetable juice Nutrition 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 14
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 claims description 12
- 235000019750 Crude protein Nutrition 0.000 claims description 11
- 239000000839 emulsion Substances 0.000 claims description 11
- 239000007787 solid Substances 0.000 claims description 11
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 10
- 239000008367 deionised water Substances 0.000 claims description 10
- 229910021641 deionized water Inorganic materials 0.000 claims description 10
- 238000000227 grinding Methods 0.000 claims description 10
- 239000002245 particle Substances 0.000 claims description 10
- 239000002002 slurry Substances 0.000 claims description 10
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- 229910052799 carbon Inorganic materials 0.000 claims description 8
- 239000001103 potassium chloride Substances 0.000 claims description 8
- 235000011164 potassium chloride Nutrition 0.000 claims description 8
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims description 7
- 241000209140 Triticum Species 0.000 claims description 6
- 235000021307 Triticum Nutrition 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 6
- 239000001530 fumaric acid Substances 0.000 claims description 6
- 150000005677 organic carbonates Chemical class 0.000 claims description 6
- 159000000000 sodium salts Chemical class 0.000 claims description 6
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical compound [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 claims description 6
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims description 6
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 5
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 5
- 239000002028 Biomass Substances 0.000 claims description 5
- 229920001353 Dextrin Polymers 0.000 claims description 5
- 239000004375 Dextrin Substances 0.000 claims description 5
- 240000007594 Oryza sativa Species 0.000 claims description 5
- 235000007164 Oryza sativa Nutrition 0.000 claims description 5
- 244000082204 Phyllostachys viridis Species 0.000 claims description 5
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 5
- 229920002472 Starch Polymers 0.000 claims description 5
- 238000013019 agitation Methods 0.000 claims description 5
- 239000011425 bamboo Substances 0.000 claims description 5
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- 238000010298 pulverizing process Methods 0.000 claims description 5
- 235000009566 rice Nutrition 0.000 claims description 5
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- 239000008107 starch Substances 0.000 claims description 5
- 230000001954 sterilising effect Effects 0.000 claims description 5
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- 244000068988 Glycine max Species 0.000 claims description 4
- 235000010469 Glycine max Nutrition 0.000 claims description 4
- 244000061456 Solanum tuberosum Species 0.000 claims description 4
- 235000002595 Solanum tuberosum Nutrition 0.000 claims description 4
- 239000012141 concentrate Substances 0.000 claims description 4
- 244000046052 Phaseolus vulgaris Species 0.000 claims description 3
- 235000010627 Phaseolus vulgaris Nutrition 0.000 claims description 3
- 240000008042 Zea mays Species 0.000 claims description 3
- 235000002017 Zea mays subsp mays Nutrition 0.000 claims description 3
- 238000004945 emulsification Methods 0.000 claims description 3
- 210000001161 mammalian embryo Anatomy 0.000 claims description 3
- 230000008569 process Effects 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 108010068370 Glutens Proteins 0.000 claims description 2
- UEZVMMHDMIWARA-UHFFFAOYSA-N Metaphosphoric acid Chemical group OP(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-N 0.000 claims description 2
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims description 2
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims description 2
- 125000001931 aliphatic group Chemical group 0.000 claims description 2
- 235000021312 gluten Nutrition 0.000 claims description 2
- 235000009973 maize Nutrition 0.000 claims description 2
- 239000001508 potassium citrate Substances 0.000 claims description 2
- 229960002635 potassium citrate Drugs 0.000 claims description 2
- QEEAPRPFLLJWCF-UHFFFAOYSA-K potassium citrate (anhydrous) Chemical group [K+].[K+].[K+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O QEEAPRPFLLJWCF-UHFFFAOYSA-K 0.000 claims description 2
- 235000011082 potassium citrates Nutrition 0.000 claims description 2
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- 238000002203 pretreatment Methods 0.000 claims description 2
- 239000001632 sodium acetate Substances 0.000 claims description 2
- 235000017281 sodium acetate Nutrition 0.000 claims description 2
- 239000000047 product Substances 0.000 abstract description 7
- 102000006395 Globulins Human genes 0.000 abstract 2
- 108010044091 Globulins Proteins 0.000 abstract 2
- 235000020244 animal milk Nutrition 0.000 abstract 1
- 230000001804 emulsifying effect Effects 0.000 abstract 1
- MOMKYJPSVWEWPM-UHFFFAOYSA-N 4-(chloromethyl)-2-(4-methylphenyl)-1,3-thiazole Chemical compound C1=CC(C)=CC=C1C1=NC(CCl)=CS1 MOMKYJPSVWEWPM-UHFFFAOYSA-N 0.000 description 6
- -1 carbon fatty acids Chemical class 0.000 description 6
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- 239000000194 fatty acid Substances 0.000 description 6
- 229930195729 fatty acid Natural products 0.000 description 6
- 235000019983 sodium metaphosphate Nutrition 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 4
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- CEYULKASIQJZGP-UHFFFAOYSA-L disodium;2-(carboxymethyl)-2-hydroxybutanedioate Chemical compound [Na+].[Na+].[O-]C(=O)CC(O)(C(=O)O)CC([O-])=O CEYULKASIQJZGP-UHFFFAOYSA-L 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- UMPKMCDVBZFQOK-UHFFFAOYSA-N potassium;iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[K+].[Fe+3] UMPKMCDVBZFQOK-UHFFFAOYSA-N 0.000 description 3
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- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 210000002264 animal mammary gland Anatomy 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 235000020197 coconut milk Nutrition 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- XUJNEKJLAYXESH-UHFFFAOYSA-N cysteine Natural products SCC(N)C(O)=O XUJNEKJLAYXESH-UHFFFAOYSA-N 0.000 description 1
- 235000018417 cysteine Nutrition 0.000 description 1
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- 229910052739 hydrogen Inorganic materials 0.000 description 1
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- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
The invention relates to the production method for plant-based milk powder. According to the method, grain processed byproducts or whole grain seeds serve as raw materials. The method comprises the following steps: performing pretreatment on edible parts of plants, removing stench from the plants, depolymerizing plant globulin subunits, performing physical fracture on long peptide chains of plant globulin, binding small protein molecules with non-polar groups, performing ionization treatment on protein, and emulsifying to obtain the plant-based milk powder. By the method, an out-dated grain processing mode is changed; the utilization rate of grains is greatly improved; a whole ecological industry chain is created; moreover, the product, namely plant-based milk or plant-based milk powder, produced by the method is similar to animal milk.
Description
Technical field
The production method that the present invention relates to a kind of plant base milk powder, belongs to food processing field.
Background technology
The product such as current existing soymilk, cereal are with milk, still rest on the primary stage, to adding the element of cereal in the simple physical processing of soybean or milk, can not solve the problem of further processing of grains and comprehensive utilization completely, in grain processing, can produce some byproducts, in many byproducts, contain abundant nutritional labeling, these valuable resources are not well utilized, and in these byproducts, often contain more vitamin, mineral matter and the plant function factor.Byproduct after grain fine finishining is because the problems such as coarse, stench taste, structure indefinite form are used as feed mostly, and part byproduct deep processing degree is also very limited, and this has just caused great waste; Make the food after processing, nutritive value is had a greatly reduced quality.
Summary of the invention
In order significantly to improve grain utilization rate, present inventor has carried out a large amount of explorations and innovation in grain processing different aspects, a kind of production method of plant base milk powder is provided, really accomplish to get rid of the weed and keep the flower of the leek, make grain processing reduce the generation of byproduct as far as possible, nutritious composition is remained completely, changed the backward pattern of grain processing, greatly improve the utilization rate of grain, createed a complete ecological industrial chain
And the product that this method is produced shows with the form of class animal milk---plant base breast or plant base milk powder.
The technical scheme that the present invention solves the problems of the technologies described above is as follows: a kind of production method of plant base milk powder, comprising:
1) pre-treatment of plant edible part: take cereal processed side product or whole grain cereal seed is raw material, in above-mentioned raw materials, all contain abundant cereal crude protein, add water agitation grinding more than 30 minutes, the amount ratio of raw material and water is greater than 1:7, obtain the juice that contains cereal crude protein, again the juice that contains cereal crude protein is carried out to ultra-fine grinding, make particle diameter > 80 orders of raw material;
2) the stench taste of removal plant: rare alcohol buffer solution is joined to 1), in the juice after pulverizing, 30 ℃ are stirred 10～170 minutes, and the rare alcohol buffer solution of centrifugal removal obtains dry, adds the deionized water and stirring of 2～5 times of dry biomass even, obtains slurries;
3) in the slurries that the depolymerization of phytogloibulin subunit: to 2) obtain, add depolymerization liquid, 30～40 ℃ of insulated and stirred 5～40 minutes, it is 3～6.6 rear washing 2～3 times that deionized water regulates pH, is filtered dry standbyly, obtains material 1;
4) physical rupture of the long peptide chain of phytogloibulin: add water adjusting concentration to 10% in material 1, then add sodium acid carbonate adjust pH to 7.8～8.2, agitating heating, pumps into material 1 in high speed shear tank and carry out high speed shear, obtains material 2;
5) combination of small protein molecule and non-polar group: material 2 temperature are increased to 75 ℃, add organic carbonate and catalyst, stir insulation 15 minutes, obtain material 3;
6) protein ionize process: by material 3 Vacuum Concentrations to protein content 35%～45%, add sylvite or sodium salt, the addition of described sylvite or sodium salt accounts for 0.04%～0.08% of material 3 quality, at 30～40 ℃, stirs 10～80 minutes, obtains colloidal material 4;
7) emulsification treatment: according to required product specification, by adding wall material, adjust protein content in colloidal material 4, after homogeneous, sterilizing, become plant base emulsion, solid concentration is 30%～40%, plant base emulsion is the stable suspension liquid that the mixture of cereal various nutrients forms by self-emulsifying, plant base emulsion is spray dried to powdery lower than 160 ℃, obtains plant base milk powder.
On the basis of technique scheme, the present invention can also do following improvement.
Further, 1) in, described cereal processed side product is one or more the mixture in gluten, potato starch parting liquid, wheat embryo, dregs of beans, rice bran, maize germ, wheat, rice, soybean.
Further, 2) in, described rare alcohol buffer solution is (0.1～5) by mass ratio: (0.1～10): (0.01～0.5): the bamboo charcoal particle of (0.01～0.03), ethanol, NaOH and ferrate form.
The beneficial effect that adopts above-mentioned further scheme is to add rare alcohol buffer solution can eliminate little molecule aldehyde and the ketone relevant to the stench taste of plant.
Further, 3) in, described depolymerization liquid is (0.1～3) by mass ratio: (0.01～0.5): the fumaric acid of (0.01～0.2), sulphite and cysteine form.
The beneficial effect that adopts above-mentioned further scheme is with fumaric acid, sulphite and cysteine, to destroy the hydrogen bond of peptide interchain, makes peptide chain not in polymerization, reaches the effect of phytogloibulin matter subunit depolymerization.
Further, 4) in, described in be heated with stirring to 70～75 ℃;
The beneficial effect that adopts above-mentioned further scheme is in the time of 70～75 ℃, and peptide chain is opened and is wire;
Further, 4) in, the condition of described high speed shear: rotating speed is 1430～1500 revs/min, shear gap is 1～5 micron, at 70～75 ℃ of down cuts, stirs 20 minutes;
Further, 5) in, described organic carbonate is that carbon number is one or more the mixture in 8～26 aliphatic acid, the addition of described organic carbonate accounts for 0.1～0.8% of material 2 quality.
Further, 5) in, described catalyst is metaphosphoric acid salt, the addition of described catalyst accounts for 0.05%～0.3% of material 2 quality.
Further, 6) in, described sylvite is potassium citrate or potassium chloride, described sodium salt is sodium acid carbonate or sodium acetate;
Further, 7) in, described wall material is one or more mixture in dextrin, beta-schardinger dextrin-, converted starch;
The invention has the beneficial effects as follows:
The feature of the product utilization plants such as existing vegetable protein beverage itself is processed, and as coconut milk, soymilk, peanut milk etc., these products lack versatility, can not be as the raw material of industry as milk.Personal characteristics (mainly referring to local flavor aspect) how to remove plant itself retains its general character (nutrition aspect), and finally to form structure be great advantage of the present invention with stable components, the relative cheap bulk raw material of cost.We can produce same composition, constitutionally stable product with different vegetable raw materials; As ox, eat different feeds and only can extrude (this is milk and the milk powder prerequisite of doing the raw material of industry) milk.
Compared with prior art, the inventive method can be converted into plant edible part " milk ", also find no at present identical technology, and the present invention be take food processing byproducts as primary raw material (add and also can independently carry out production and processing man-hour at use raw grain), in process, reduced to greatest extent the personal characteristics of each Plants itself, the function of simulated animal mammary gland, by the even proportioning of Different Nutrition composition emulsification completely, directly produce milk or milk, finally make plant base breast or plant base milk powder.
The present invention has realized the preliminary industrialization phase that machinery is given milk.For the productive manpower, the mechanization of milk are laid a good foundation.
The specific embodiment
Below principle of the present invention and feature are described, example, only for explaining the present invention, is not intended to limit scope of the present invention.
Implementation column 1
1) by the 1:2:7 mixing in mass ratio of wheat, rice, soybean (raw grain), obtain maslin, add water agitation grinding 50 minutes, the amount ratio of maslin and water is 1:8, obtain the juice that contains cereal crude protein, again the juice that contains cereal crude protein is carried out to ultra-fine grinding, make particle diameter > 80 orders of raw material;
2) rare alcohol buffer solution being joined to 1) in juice after pulverizing, 30 ℃ are stirred 70 minutes, and the rare alcohol buffer solution of centrifugal removal obtains dry, adds the deionized water and stirring of 2 dry biomass even, obtains slurries; The bamboo charcoal particle that rare alcohol buffer solution is 2:1:0.02:0.02 by mass ratio, ethanol, solid sodium hydroxide and the solid potassium ferrate of 95% concentration form, and the addition of rare alcohol buffer solution is 1) in 3 times of cereal mixture quality.
3) to 2) add depolymerization liquid in the slurries that obtain, 30 ℃ of insulated and stirred 40 minutes, it is 5.6 rear washing 2 times that deionized water regulates pH, is filtered dry standbyly, obtains material 1; The fumaric acid that depolymerization liquid is 0.3:0.01:0.01 by mass ratio, sulphite and cysteine form, and the addition of depolymerization liquid is 1) in 3 times of cereal mixture quality.
4) in material 1, add water adjusting concentration to 10%, then add sodium acid carbonate adjust pH to 7.8, be heated with stirring to 70 ℃, material 1 is pumped in high speed shear tank and carries out high speed shear, and rotating speed is 1430 revs/min, and shear gap is 1 micron, at 70 ℃ of down cuts, stir 20 minutes, obtain material 2;
5) material 2 temperature are increased to 75 ℃, add 12 carbon fatty acids and sodium metaphosphate, the addition of 12 carbon fatty acids accounts for 0.1% of material 2 quality, and the addition of sodium metaphosphate accounts for 0.1% of material 2 quality, stirs insulation 15 minutes, obtains material 3;
6) by material 3 Vacuum Concentrations to protein content 35%～45%, add natrium citricum, addition accounts for 0.05%, 30 ℃ of material 3 quality and stirs 40 minutes, obtains colloidal material 4;
7) add wall material (dextrin: beta-schardinger dextrin-: the mass ratio=1:2:1 of converted starch) adjust protein content to 25% in colloidal material 4, after homogeneous, sterilizing, become plant base emulsion, solid concentration is 30%～40%, 150 ℃ of plant base emulsions are spray dried to powdery, obtain plant base milk powder.
Embodiment 2
1) by the 4:2:4 mixing in mass ratio of wheat embryo, corn, dregs of beans (food processing byproducts), obtain maslin, add water agitation grinding 50 minutes, the amount ratio of maslin and water is 1:8, obtain the juice that contains cereal crude protein, again the juice that contains cereal crude protein is carried out to ultra-fine grinding, make particle diameter > 80 orders of raw material;
2) rare alcohol buffer solution being joined to 1) in juice after pulverizing, 30 ℃ are stirred 70 minutes, and the rare alcohol buffer solution of centrifugal removal obtains dry, adds the deionized water and stirring of 3 times of dry biomass even, obtains slurries; The bamboo charcoal particle that rare alcohol buffer solution is 1:0.5:0.01:0.01 by mass ratio, 95% ethanol, solid sodium hydroxide and solid potassium ferrate form, and the addition of rare alcohol buffer solution is 1) in 3 times of cereal mixture quality.
3) to 2) add depolymerization liquid in the slurries that obtain, 30 ℃ of insulated and stirred 40 minutes, it is 5.6 rear washing 2 times that deionized water regulates pH, is filtered dry standbyly, obtains material 1; The fumaric acid that depolymerization liquid is 5:0.2:0.2 by mass ratio, sulphite and cysteine form, and the addition of depolymerization liquid is 1) in 3 times of cereal mixture quality.
4) in material 1, add water adjusting concentration to 10%, then add sodium acid carbonate adjust pH to 7.8, be heated with stirring to 75 ℃, material 1 is pumped in high speed shear tank and carries out high speed shear, and rotating speed is 1500 revs/min, and shear gap is 5 microns, at 75 ℃ of down cuts, stir 20 minutes, obtain material 2;
5) material 2 temperature are increased to 75 ℃, add 12 carbon fatty acids and sodium metaphosphate, the addition of 12 carbon fatty acids accounts for 0.1% of material 2 quality, and the addition of sodium metaphosphate accounts for 0.12% of material 2 quality, stirs insulation 15 minutes, obtains material 3;
6) by material 3 Vacuum Concentrations to protein content 35%～45%, add natrium citricum, addition accounts for 0.06%, 30 ℃ of material 3 quality and stirs 40 minutes, obtains colloidal material 4;
7) add wall material (dextrin: beta-schardinger dextrin-: the mass ratio=1:2:1 of converted starch) adjust protein content to 28% in colloidal material 4, after homogeneous, sterilizing, become plant base emulsion, solid concentration is 30%～40%, 150 ℃ of plant base emulsions are spray dried to powdery, obtain plant base milk powder.
Implementation column 3
1) Potato protein concentrate mud is added to water agitation grinding 50 minutes, the amount ratio of raw material and water is 1:8, obtains the juice that contains cereal crude protein, then the juice that contains cereal crude protein is carried out to ultra-fine grinding, makes particle diameter > 80 orders of raw material;
2) rare alcohol buffer solution being joined to 1) in juice after pulverizing, 30 ℃ are stirred 60 minutes, and the rare alcohol buffer solution of centrifugal removal obtains dry, adds the deionized water and stirring of 4 times of dry biomass even, obtains slurries; The bamboo charcoal particle that rare alcohol buffer solution is 1:0.5:0.01:0.01 by mass ratio, 95% ethanol, solid sodium hydroxide and solid potassium ferrate form, and the addition of rare alcohol buffer solution is 1) 3 times of Potato protein concentrate shale amount.
3) to 2) add depolymerization liquid in the slurries that obtain, 30 ℃ of insulated and stirred 40 minutes, it is 5.6 rear washing 2 times that deionized water regulates pH, is filtered dry standbyly, obtains material 1; The fumaric acid that depolymerization liquid is 3:0.1:0.1 by mass ratio, sulphite and cysteine form, and the addition of depolymerization liquid is 1) in 3 times of Potato protein concentrate shale amount.
4) in material 1, add water adjusting concentration to 10%, then add sodium acid carbonate adjust pH to 7.8, be heated with stirring to 70 ℃, material 1 is pumped in high speed shear tank and carries out high speed shear, and rotating speed is 1430 revs/min, and shear gap is 1 micron, at 70 ℃ of down cuts, stir 20 minutes, obtain material 2;
5) material 2 temperature are increased to 75 ℃, add 12 carbon fatty acids and sodium metaphosphate, the addition of 12 carbon fatty acids accounts for 0.1% of material 2 quality, and the addition of sodium metaphosphate accounts for 0.06% of material 2 quality, stirs insulation 15 minutes, obtains material 3;
6) by material 3 Vacuum Concentrations to protein content 35%～45%, add natrium citricum, addition accounts for 0.05%, 30 ℃ of material 3 quality and stirs 40 minutes, obtains colloidal material 4;
7) add wall material (dextrin: beta-schardinger dextrin-: the mass ratio=1:2:1 of converted starch) adjust protein content to 18% in colloidal material 4, after homogeneous, sterilizing, become plant base emulsion, solid concentration is 30%～40%, 150 ℃ of plant base emulsions are spray dried to powdery, obtain plant base milk powder.
Nutritional labeling to the plant base milk powder of the embodiment of the present application 1～3 preparation is measured, and result is as following table:
Table 1
| Project | Embodiment 1 | Embodiment 2 | Embodiment 3 |
| Protein | 25.4% | 28.2% | 18.6% |
| Fat | 21% | 18% | 23% |
| Dietary fiber | 3.2% | 2.6% | 4.1% |
| Moisture≤ | 5% | 4.8% | 4.7% |
The foregoing is only preferred embodiment of the present invention, in order to limit the present invention, within the spirit and principles in the present invention not all, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection scope of the present invention.
Claims (8)
1. a production method for plant base milk powder, is characterized in that, comprising:
1) pre-treatment of plant edible part: take cereal processed side product or whole grain cereal seed is raw material, add water agitation grinding more than 30 minutes, the amount ratio of raw material and water is greater than 1:7, obtain the juice that contains cereal crude protein, again the juice that contains cereal crude protein is carried out to ultra-fine grinding, make particle diameter > 80 orders of raw material;
2) the stench taste of removal plant: rare alcohol buffer solution is joined to 1), in the juice after pulverizing, 30 ℃ are stirred 10～170 minutes, and the rare alcohol buffer solution of centrifugal removal obtains dry, adds the deionized water and stirring of 2～5 times of dry biomass even, obtains slurries;
3) in the slurries that the depolymerization of phytogloibulin subunit: to 2) obtain, add depolymerization liquid, 30～40 ℃ of insulated and stirred 5～40 minutes, deionized water regulates the rear washing in pH to 3～6.6 2～3 times, is filtered dry standbyly, obtains material 1;
4) physical rupture of the long peptide chain of phytogloibulin: add water adjusting concentration to 10% in material 1, then add sodium acid carbonate to regulate pH value to 7.8～8.2, be heated with stirring to 70～75 ℃, material 1 is pumped in high speed shear tank and carries out high speed shear, obtain material 2;
5) combination of small protein molecule and non-polar group: material 2 temperature are increased to 75 ℃, add organic carbonate and catalyst, stir insulation 15 minutes, obtain material 3;
6) protein ionize process: by material 3 Vacuum Concentrations to protein content 35%～45%, add sylvite or sodium salt, the addition of described sylvite or sodium salt accounts for 0.04%～0.08% of material 3 quality, at 30～40 ℃, stirs 10～80 minutes, obtains colloidal material 4;
7) emulsification treatment: by adding wall material to adjust protein content in colloidal material 4, become plant base emulsion after homogeneous, sterilizing, solid concentration is 30%～40%, and plant base emulsion is spray dried to powdery lower than 160 ℃, obtains plant base milk powder.
2. production method according to claim 1, it is characterized in that, 1) in, described cereal processed side product is one or more the mixture in gluten, potato starch parting liquid, wheat embryo, wheat, dregs of beans, rice bran, rice, soybean, maize germ, Potato protein concentrate mud.
3. production method according to claim 1, it is characterized in that, 2) in, described rare alcohol buffer solution is (0.1～5) by mass ratio: (0.1～10): (0.01～0.5): the bamboo charcoal particle of (0.01～0.03), ethanol, NaOH and ferrate form.
4. production method according to claim 1, is characterized in that, 3) in, described depolymerization liquid is (0.1～3) by mass ratio: (0.01～0.5): the fumaric acid of (0.01～0.2), sulphite and cysteine form.
5. production method according to claim 1, is characterized in that, 4) in, the condition of described high speed shear: rotating speed is 1430～1500 revs/min, shear gap is 1～5 micron, at 70～75 ℃ of down cuts, stirs 20 minutes.
6. production method according to claim 1, is characterized in that, 5) in, described organic carbonate is that carbon number is one or more the mixture in 8～26 aliphatic acid, the addition of described organic carbonate accounts for 0.1～0.8% of material 2 quality; Described catalyst is metaphosphoric acid salt, and the addition of described catalyst accounts for 0.05%～0.3% of material 2 quality.
7. production method according to claim 1, is characterized in that, 6) in, described sylvite is potassium citrate or potassium chloride, described sodium salt is sodium acid carbonate or sodium acetate.
8. production method according to claim 1, is characterized in that, 7) in, described wall material is one or more mixture in dextrin, beta-schardinger dextrin-, converted starch.
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