CN102028095B - Organized wiredrawing protein and preparation method thereof - Google Patents
Organized wiredrawing protein and preparation method thereof Download PDFInfo
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- CN102028095B CN102028095B CN 200910177467 CN200910177467A CN102028095B CN 102028095 B CN102028095 B CN 102028095B CN 200910177467 CN200910177467 CN 200910177467 CN 200910177467 A CN200910177467 A CN 200910177467A CN 102028095 B CN102028095 B CN 102028095B
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Abstract
The invention discloses organized wiredrawing protein and a preparation method thereof, belonging to the technical field of organized protein and organized protein processing. The preparation method comprises the following steps of: crushing low-temperature defatted soybean meal and collecting; mixing the collected low-temperature defatted soybean meal with a mixture to form a mixed product containing grain protein, isolating protein and starch; adding water in the mixture and tempering; enabling the mixture to pass through an extruded bulking machine provided with a wiredrawing outlet die; and cutting, drying and cooling the product output by the extruded bulking machine to obtain the organized wiredrawing protein. After being rehydrated, the organized wiredrawing protein has the perception and characteristics similar to animal muscles and can be drawn into wires.
Description
Technical field
The present invention relates to textured protein and preparation method thereof, especially relate to a kind of organized wiredrawing protein and preparation method thereof.
Background technology
Produce good to eat and with the real histone product of animal muscle vision be the work that a lot of food enterprises are constantly explored.
Application number is 93103902.9, the application for a patent for invention prospectus that open day is on November 10th, 1993 discloses a kind of textured soybean protein and preparation method thereof, and its production process is to be processed into textured soybean protein take soybean as raw material through operations such as screening, degreasing, abrasive dust, batching, heating, extruding.
Application number 200510046353.6, the application for a patent for invention prospectus that open day is on September 28th, 2005 discloses a kind of processing technology of nutrient reinforcing soybean tissue protein, its production technology is that low temperature soy meal is through pulverizing, mix with the fortification material, the mixture extrusion, oven dry, cooling obtains textured soybean protein.
The patent No. is 98126298.8, Granted publication day is that the patent of invention specification in June 27 calendar year 2001 discloses cultivate peanut histone and processing technology and a special equipment, its production technology be with shelled peanut through degreasing, systematism in kneading compactor obtains the peanut histone again.
The histone that above-mentioned three explained hereafter go out all has common shortcoming: the source of (one) albumen is single; (2) content of albumen is not high; (3) the histone finished product can not really realize tearing the effect of drawwing wire, the goods of meat as an alternative, and mouthfeel and outward appearance are all immature.
Summary of the invention
The purpose of this invention is to provide a kind of dietary protein origin various, protein content is high, has simultaneously the organoleptic attribute of similar animal muscle, the tearable histone product that draws wire.
One aspect of the present invention provides a kind of method for preparing organized wiredrawing protein, and described method comprises the steps:
1) defatted soybean meal of pulverizing is puddled formation with a mixture and puddle product, wherein, based on the described weight of puddling product, described defatted soy flour is 10-60% weight, and described mixture is 40-90% weight; And, the starch of the corn gluten protein that it is 25-65% weight that described mixture comprises based on described mixture total weight amount, the protein isolate of 20%-65% weight and 0-15% weight;
2) puddle product to add water modified described, and by being equipped with the extruding puffing machine of wire drawing outlet mould, the amount of the described water that adds in described modified step and the described weight ratio of puddling product are 25: 100 to 45: 100, the rotating speed of described extruding puffing machine is 350rpm-600rpm, and the temperature in the described extruding puffing machine is 130-180 ℃;
3) to the product by the output of described extruding puffing machine cut, dry, cooling, obtain organized wiredrawing protein.
Another aspect of the present invention provides the organized wiredrawing protein of above-described method preparation.
The detailed description of invention
The defatted soybean meal NSI (nitrogen soluble index) of one of raw material of puddling product of the present invention is higher, is conducive to the formation of product institutional framework, and the defatted soybean meal color is faint yellow simultaneously, is conducive to guarantee the color and luster of final products.
When corn gluten protein Jia Shui when becoming dough, can consist of the network structure as sponge, form the skeleton of gluten, other compositions all contain among the network of gluten skeleton such as fat, carbohydrate, starch and water, this is with regard to so that gluten has elasticity and plasticity.Puddling among the present invention adds corn gluten protein in the product can strengthen viscosity, elasticity, extensibility, film forming and the emulsibility of puddling product, thereby realize that products obtained therefrom of the present invention has the sense organ of similar animal muscle, and have simultaneously tearable feature of drawwing wire.Corn gluten protein among the present invention can be any corn gluten protein of selling on the market, as is known rice grains albumen, wheat grain albumen, corn corn gluten protein, oat grain albumen, Chinese sorghum corn gluten protein etc. can serve the same role and realize identical effect.
For the protein content that improves organized wiredrawing protein and promote final products organize the matter structure, in puddling product, add protein isolate.Along with the increase of puddling protein content in the product, the situation of the melting when puddling product and being squeezed in bulking machine is better, and this will be conducive to realize that products obtained therefrom of the present invention has the sense organ of similar animal muscle, and have simultaneously tearable feature of drawwing wire.Protein isolate among the present invention can be any protein isolate of selling on the market, such as soybean protein isolate, peanut protein isolate etc., can serve the same role and realizes identical effect.
Employed starch can be the starch of any kind of selling on the market among the present invention.
Prepare in the preferred embodiment of method of organized wiredrawing protein in the present invention, described protein isolate is soybean protein isolate.
Prepare in another preferred embodiment of method of organized wiredrawing protein in the present invention, described soybean protein isolate is group or its combination that gel-type soybean protein isolate, Injectable soy protein isolate, high-dispersibility isolated soy protein form.
Prepare in the another preferred embodiment of method of organized wiredrawing protein the starch of the corn gluten protein that it is 25-60% weight that described mixture comprises based on described mixture total weight amount, the protein isolate of 30%-65% weight and 0-15% weight in the present invention.
Prepare in another preferred embodiment of method of organized wiredrawing protein in the present invention, described drying is heated-air drying, and temperature is 65-85 ℃.
Prepare in the another preferred embodiment of method of organized wiredrawing protein, in step 3 in the present invention) in, after cutting, the product of described extruding puffing machine output enters dry run by blast system.
Prepare in the again preferred embodiment of method of organized wiredrawing protein in the present invention, described extruding puffing machine is the twin-screw extruding puffing machine.
Employed bulking machine is Switzerland Bu Leer extruded type bulking machine among the present invention, and the wire drawing outlet mould with elongated cavity that internal diameter reduces gradually by means of the present inventor is equipped with can obtain organized wiredrawing protein of the present invention.Be in the utility application of 200920216995.X detailed description to be arranged at the application number of the application that the applicant submitted on September 28th, 2009 relevant for the optimization of described wire drawing outlet mould, the content of this application all is incorporated herein by reference.
Obtain for the mould for preparing organized wiredrawing protein at extruding puffing machine by optimization, comprise body, described body comprises entrance point, the port of export, and the elongated cavity from described entrance point to described port of export perforation, described elongated cavity comprises the first cone cavity part that is reduced to gradually D2 from described entrance point to described port of export extension and diameter from entrance point diameter D1, the outlet of described entrance point diameter D1 and described extruding puffing machine is complementary, and the cylindrical cavity part that is essentially port of export diameter D3 from the described port of export to described entrance point extension and diameter, wherein, D1＞D2＞D3.
Preferably, described elongated cavity comprises that also the diameter that is arranged between described the first cone cavity part and the described cylindrical cavity part is reduced to the second cone cavity part of entrance point diameter D3 gradually from D2.
Preferably, described the first cone cavity length is 40-60mm.
Preferably, described cylindrical cavity diameter is 8-12mm, and length is 5-20mm.
Preferably, described the second cone cavity length is 300-1000mm.
Preferably, described the second cone cavity cone angle is 2-6 °.
Preferably, the elongated cavity periphery of described perforation is provided with the sheath with inlet and liquid outlet.
Preferably, the periphery of described the second cone cavity and described cylindrical cavity is provided with the sheath with inlet and liquid outlet.
Organoleptic indicator, physical and chemical index according to the organized wiredrawing protein of preparation method's preparation of the described organized wiredrawing protein of the inventive method preparation are as follows:
Technical performance index sees attached list.
Table 1 organoleptic properties index
| Project | Requirement |
| Color and luster | Milky or light yellow |
| Tissue morphology | Column or sheet |
| Taste, smell | Has the intrinsic smell of this product, pure taste, free from extraneous odour |
Table 2 voltinism can index
| Project | Requirement |
| Crude protein (in butt, N * 6.25), % 〉= | 60.0 |
| Crude fat (in butt), %≤ | 1.5 |
| Crude fibre (in butt), %≤ | 5.0 |
| Moisture, %≤ | 12.0 |
| Ash content (in butt), %≤ | 6.5 |
| Plumbous (in Pb), mg/kg≤ | 1.0 |
| Total arsenic (in As), mg/kg≤ | 0.5 |
| Copper (in Cu), (mg/kg)≤ | 20.0 |
| Total plate count, cfu/g≤ | 30000 |
| Coliform, MPN/100g≤ | 30 |
| Mould/cfu/g≤ | 25 |
| Yeast/cfu/g≤ | 25 |
| Pathogenic bacteria (salmonella, Shigella, staphylococcus aureus) | Must not detect |
This product belongs to a kind of fibrous vegetable protein meat with similar meat fiber texture.Have sense organ, the characteristic of similar animal muscle through this histone after the rehydration, tearable drawwing wire therefore can the Substitute For Partial animal muscle in meat products, also is the present domestic and international new generation product of the most comprehensive, the pure natural of function in the former batching of meat products.
Description of drawings
Fig. 1 is the flow chart for preparing the method for organized wiredrawing protein.
Fig. 2 is the extruding puffing machine structural representation.
Fig. 3 is the schematic diagram of optimizing structure of extruding puffing machine wire drawing outlet mould.
Embodiment
The defatted soybean meal that adopts in the present embodiment is available from Ha Gaoke grease Co., Ltd; Employed soybean protein isolate is that our company oneself produces; The wheat grain albumen of employed corn gluten protein (trade name is " tanimoto powder "), corn corn gluten protein, starch are available from Tableland in Fufeng County, Shaanxi Province county corn gluten protein factory.
Employed bulking machine is Switzerland Bu Leer extruded type bulking machine in the present embodiment, technical parameter respectively explanation in following preparation example of the wire drawing outlet mould that this extruded type bulking machine is equipped with.The material of preparation mould is high temperature resistant and high voltage bearing evanohm.
Preparation example 1: the preparation of wire drawing outlet mould (mould 1):
In an embodiment of the structure of the homemade wire drawing outlet mould of our company of the present invention, the structure of the wire drawing outlet mould 1 of extruding puffing machine is as follows: mould cone cavity 103 links to each other with a cylindrical cavity 105 orders, wherein the upper outlet along 11 diameter D1 and extruding puffing machine of cone cavity 103 is complementary, the length L 1 of described cone cavity 103 is 740mm, upper along 13 (diameter D3) along 12 (diameter D2) connecting cylinder chamber 105 of described cone cavity 103 lower, the diameter D3 of described cylindrical cavity 105 is 12mm, the length L 3 of described cylindrical cavity 105 is 5mm, the upper edge of described cylindrical cavity 105 is 13, lower edge is 14, upper along 13 and lower diameter along 14 be D3.
Preparation example 2: the preparation of wire drawing outlet mould (mould 2):
In an embodiment of the structure of the homemade wire drawing outlet mould of our company of the present invention, the structure of the wire drawing outlet mould 2 of extruding puffing machine is as follows: mould has two continuous cone cavity 103,104 link to each other with a cylindrical cavity 105 order, the upper outlet along 11 diameter D1 and extruding puffing machine of the cone cavity that wherein diameter is larger (the first cone cavity) 103 is complementary, the length L 1 of the cone cavity 103 that described diameter is larger is 50mm, upper along 12 (diameter D2) along 12 (diameter D2) cone cavity that connection diameter is less (the second cone cavity) 104 of the cone cavity 103 that described diameter is larger lower, the taper angle theta of the cone cavity 104 that described diameter is less is 4 °, the length L 2 of the cone cavity 104 that described diameter is less is 800mm, the cone cavity 104 that described diameter is less lower to 13 connecting cylinder chambeies 105, the diameter D3 of described cylindrical cavity 105 is 12mm, the length L 3 of described cylindrical cavity 105 is 5mm, the upper edge of described cylindrical cavity 105 is 13, lower edge is 14, upper along 13 and lower diameter along 14 be D3.
The structure of preparation example 3,4 wire drawing outlet mould is identical with the structure of the wire drawing outlet mould of preparation example 2, clear for stating, succinct, preparation example 3,4 key dimensions that mark out mould.
Preparation example 3: the preparation of wire drawing outlet mould (mould 3):
As shown in Figure 3, specifically be of a size of:
D1: be complementary with the outlet of the extruding puffing machine of twin-screw;
D3：10mm；
L1：50mm；
L2：600mm；
L3：15mm；
θ：5°；
The cone cavity 104 that the diameter of mould is less in addition and the periphery of cylindrical cavity 105 are provided with the sheath 106 with inlet 1061 and liquid outlet 1062.
Preparation example 4: the preparation of wire drawing outlet mould (mould 4):
As shown in Figure 3, specifically be of a size of:
D1: be complementary with the outlet of the extruding puffing machine of twin-screw;
D3：12mm；
L1：40mm；
L2：700mm；
L3：10mm；
θ：2°；
The cone cavity 104 that the diameter of mould is less in addition and the periphery of cylindrical cavity 105 are provided with the sheath 106 with inlet 1061 and liquid outlet 1062.
Embodiment one:
20 kilograms defatted soybean meals are pulverized, filter collection through cloth envelop collector, then with 80 kilograms tanimoto powder, 80 kilograms gel-type soybean protein isolate, 20 kilograms starch is puddled in agitator evenly, obtain 200 kilograms the product of puddling, then will puddle product is shipped in the quality-adjusting device, add 60 kilograms in water modified, the product of puddling of modified rear one-tenth semi-solid is delivered in the extruding puffing machine that is equipped with wire drawing outlet mould (mould 1), in the rotating speed of 600rpm, carry out systematism, expanded built-in temperature is controlled at 130-180 ℃, obtain the systematism product, this systematism product is cut into difformity, enter drying in the drier by blast system, baking temperature is 65-85 ℃, obtains 200 kilograms of products.
Embodiment two:
80 kilograms defatted soybean meals are pulverized, filter collection through cloth envelop collector, then with 42 kilograms corn corn gluten protein, 60 kilograms Injectable soy protein isolate, 18 kilograms starch is puddled in agitator evenly, obtain 200 kilograms the product of puddling, then will puddle product is shipped in the quality-adjusting device, add 80 kilograms in water modified, the product of puddling of modified rear one-tenth semi-solid is delivered in the extruding puffing machine that is equipped with wire drawing outlet mould (mould 2), in the rotating speed of 600rpm, carry out systematism, expanded built-in temperature is controlled at 130-180 ℃, obtain the systematism product, this systematism product is cut into difformity, enter drying in the drier by blast system, baking temperature is 65-85 ℃, obtains 200 kilograms of products.
Embodiment three:
50 kilograms defatted soybean meals are pulverized, filter collection through cloth envelop collector, then with 45 kilograms tanimoto powder, 95 kilograms high-dispersibility isolated soy protein, 10 kilograms starch is puddled in agitator evenly, obtain 200 kilograms the product of puddling, then will puddle product is shipped in the quality-adjusting device, add 70 kilograms in water modified, the product of puddling of modified rear one-tenth semi-solid is delivered in the twin-screw extruding puffing machine that is equipped with wire drawing outlet mould (mould 3), in the rotating speed of 450rpm, carry out systematism, temperature is controlled at 130-180 ℃ in the twin-screw Bulking Machine, obtain the systematism product, this systematism product is cut into difformity, enter drying in the drier by blast system, baking temperature is 65-85 ℃, obtains 200 kilograms of products.
Embodiment four:
40 kilograms defatted soybean meals are pulverized, filter collection through cloth envelop collector, then with 80 kilograms tanimoto powder, 60 kilograms gel-type soybean protein isolate, 20 kilograms starch is puddled in agitator evenly, obtain 200 kilograms the product of puddling, then will puddle product is shipped in the quality-adjusting device, add 70 kilograms in water modified, the product of puddling of modified rear one-tenth semi-solid is delivered in the twin-screw extruding puffing machine that is equipped with wire drawing outlet mould (mould 4), in the rotating speed of 400rpm, carry out systematism, temperature is controlled at 130-180 ℃ in the twin-screw Bulking Machine, obtain the systematism product, this systematism product is cut into difformity, enter drying in the drier by blast system, baking temperature is 65-85 ℃, obtains 200 kilograms of products.
Embodiment five:
60 kilograms defatted soybean meals are pulverized, filter collection through cloth envelop collector, then with 90 kilograms tanimoto powder, 50 kilograms gel-type soybean protein isolate, 0 kilogram starch is puddled in agitator evenly, obtain 200 kilograms the product of puddling, then will puddle product is shipped in the quality-adjusting device, add 80 kilograms in water modified, the product of puddling of modified rear one-tenth semi-solid is delivered in the twin-screw extruding puffing machine that is equipped with wire drawing outlet mould (mould 3), in the rotating speed of 500rpm, carry out systematism, temperature is controlled at 130-180 ℃ in the twin-screw Bulking Machine, obtain the systematism product, this systematism product is cut into difformity, enter drying in the drier by blast system, baking temperature is 65-85 ℃, obtains 200 kilograms of products.
Relevant experimental data is as follows:
Experimental result and evaluation
★ ★ ★ ★ ★ fibre tension or voluptuousness degree, star more multilist show that pulling force is stronger or voluptuousness is stronger.
Claims (8)
1. method for preparing organized wiredrawing protein, described method comprises the steps:
1) defatted soybean meal of pulverizing is puddled formation with a mixture and puddle product, wherein, based on the described weight of puddling product, described defatted soybean meal is 10-60% weight, and described mixture is 40-90% weight; And, the starch of the corn gluten protein that it is 25-65% weight that described mixture comprises based on described mixture total weight amount, the protein isolate of 20%-65% weight and 0-15% weight;
2) puddle product to add water modified described, and by being equipped with the extruding puffing machine of wire drawing outlet mould, the amount of the described water that adds in described modified step and the described weight ratio of puddling product are 25:100 to 45:100, the rotating speed of described extruding puffing machine is 350rpm-600rpm, and the temperature in the described extruding puffing machine is 130-180 ℃; Wherein said wire drawing outlet mould comprises body, described body comprises entrance point, the port of export, and the elongated cavity from described entrance point to described port of export perforation, described elongated cavity comprises the first cone cavity part that is reduced to gradually D2 from described entrance point to described port of export extension and diameter from entrance point diameter D1, the outlet of described entrance point diameter D1 and described extruding puffing machine is complementary, and the cylindrical cavity part that is essentially port of export diameter D3 from the described port of export to described entrance point extension and diameter, wherein, D1〉D2〉D3;
3) to the product by the output of described extruding puffing machine cut, dry, cooling, obtain described organized wiredrawing protein;
Wherein, described organized wiredrawing protein has the water content less than 12%.
2. method according to claim 1 is characterized in that, described protein isolate is soybean protein isolate.
3. method according to claim 2 is characterized in that, described soybean protein isolate is selected from the group by gel-type soybean protein isolate, Injectable soy protein isolate, high-dispersibility isolated soy protein or combinations thereof.
4. the described method of any one is characterized in that according to claim 1-3, the starch of the corn gluten protein that it is 25-60% weight that described mixture comprises based on described mixture total weight amount, the protein isolate of 30%-65% weight and 0-15% weight.
5. method according to claim 1 is characterized in that, described drying is that temperature is 65-85 ℃ heated-air drying.
6. method according to claim 1 is characterized in that, in step 3), the product of described extruding puffing machine output enters dry run by blast system after cutting.
7. method according to claim 1 is characterized in that, described extruding puffing machine is the twin-screw extruding puffing machine.
8. the organized wiredrawing protein of the described method of one of claim 1-7 preparation.
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| CN105249178A (en) * | 2015-11-17 | 2016-01-20 | 青海省农林科学院 | Broad bean protein meat and preparation method thereof |
| CN105379943A (en) * | 2015-12-07 | 2016-03-09 | 嘉兴市鸿翔食品有限公司 | Process using organized soybean drawing protein to prepare meat analogue |
| CN107006676A (en) * | 2016-01-27 | 2017-08-04 | 百川生物科技有限公司 | A kind of soybean wire-drawing protein and its production technology |
| CN107006675A (en) * | 2016-01-27 | 2017-08-04 | 百川生物科技有限公司 | A kind of production technology of wire-drawing protein |
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| CN107251986B (en) * | 2017-06-15 | 2018-08-14 | 中国农业科学院原子能利用研究所 | A kind of polysaccharide improvement high-moisture peanut wire-drawing protein quality method |
| CN107319096B (en) | 2017-06-15 | 2018-12-18 | 中国农业科学院农产品加工研究所 | A kind of high-moisture peanut wire-drawing protein and preparation method thereof |
| CN113016932A (en) * | 2019-12-06 | 2021-06-25 | 丰益(上海)生物技术研发中心有限公司 | Composition for preparing wiredrawing protein, wiredrawing protein and preparation method thereof |
| CN112704149B (en) * | 2020-12-29 | 2022-11-04 | 浙江庆源顺生物科技有限公司 | Vegetable protein production system |
| CN113016934B (en) * | 2021-04-21 | 2023-02-03 | 齐鲁工业大学 | Processing method for improving rehydration of plant tissue protein |
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