CN106974296A - A kind of preparation method of the thread histone of use various plants protein production - Google Patents
A kind of preparation method of the thread histone of use various plants protein production Download PDFInfo
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- CN106974296A CN106974296A CN201710262180.4A CN201710262180A CN106974296A CN 106974296 A CN106974296 A CN 106974296A CN 201710262180 A CN201710262180 A CN 201710262180A CN 106974296 A CN106974296 A CN 106974296A
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- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- 108010033040 Histones Proteins 0.000 title claims abstract description 18
- 230000014616 translation Effects 0.000 title claims abstract description 15
- 239000000463 material Substances 0.000 claims abstract description 126
- 235000018102 proteins Nutrition 0.000 claims abstract description 23
- 108090000623 proteins and genes Proteins 0.000 claims abstract description 23
- 102000004169 proteins and genes Human genes 0.000 claims abstract description 23
- 241000196324 Embryophyta Species 0.000 claims abstract description 14
- 239000008367 deionised water Substances 0.000 claims abstract description 9
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 108010068370 Glutens Proteins 0.000 claims abstract description 6
- 238000001125 extrusion Methods 0.000 claims abstract description 6
- 235000021312 gluten Nutrition 0.000 claims abstract description 6
- 235000012054 meals Nutrition 0.000 claims abstract description 6
- 235000017060 Arachis glabrata Nutrition 0.000 claims abstract description 5
- 244000105624 Arachis hypogaea Species 0.000 claims abstract description 5
- 235000010777 Arachis hypogaea Nutrition 0.000 claims abstract description 5
- 235000018262 Arachis monticola Nutrition 0.000 claims abstract description 5
- 235000009496 Juglans regia Nutrition 0.000 claims abstract description 5
- 108010084695 Pea Proteins Proteins 0.000 claims abstract description 5
- 239000012141 concentrate Substances 0.000 claims abstract description 5
- 235000019702 pea protein Nutrition 0.000 claims abstract description 5
- 235000020232 peanut Nutrition 0.000 claims abstract description 5
- 235000020234 walnut Nutrition 0.000 claims abstract description 5
- 240000007049 Juglans regia Species 0.000 claims abstract 2
- 239000000835 fiber Substances 0.000 claims description 34
- 230000000694 effects Effects 0.000 claims description 13
- 230000008859 change Effects 0.000 claims description 9
- 238000004898 kneading Methods 0.000 claims description 8
- 230000015572 biosynthetic process Effects 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 5
- 238000000465 moulding Methods 0.000 claims description 4
- 238000005491 wire drawing Methods 0.000 claims description 4
- 108010064851 Plant Proteins Proteins 0.000 claims 1
- 235000021118 plant-derived protein Nutrition 0.000 claims 1
- 238000005516 engineering process Methods 0.000 abstract description 9
- 235000016709 nutrition Nutrition 0.000 abstract description 7
- 230000035764 nutrition Effects 0.000 abstract description 7
- 238000000034 method Methods 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 5
- 239000000654 additive Substances 0.000 abstract description 4
- 230000000996 additive effect Effects 0.000 abstract description 4
- 238000010606 normalization Methods 0.000 abstract description 3
- 235000010469 Glycine max Nutrition 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 108010073771 Soybean Proteins Proteins 0.000 description 4
- 241000758789 Juglans Species 0.000 description 3
- 235000019710 soybean protein Nutrition 0.000 description 3
- 108010082495 Dietary Plant Proteins Proteins 0.000 description 2
- 244000068988 Glycine max Species 0.000 description 2
- 238000010959 commercial synthesis reaction Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229940001941 soy protein Drugs 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
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- Meat, Egg Or Seafood Products (AREA)
Abstract
The present invention relates to a kind of preparation method of the thread histone of use various plants protein production, it is that protein concentrate is mixed by 20 30 parts of low temperature soy meal, 25 40 parts of protein isolate, 10 15 parts of Gluten, 5 10 parts of peanut protein, 5 10 parts of pea protein, 35 parts of walnut protein, surplus, then after deionized water is infiltrated, extrusion molding is carried out to mixed material by double screw extruder, extruding force release finally is carried out so as to obtain finished product to the material of extrusion molding.The preparation method automaticity that the present invention is provided is high, technological process normalization is good, it is easy to learn, and the control of machined parameters data is convenient, the stability and reliability of processing technology are favorably improved, and reaches the purpose for improving product quality and quality, while the preparation method that the present invention is provided also contributes to the nutrition content of product, it is in good taste, and be that can obtain the thread histone product of high-quality without any additive.
Description
Technical field
The present invention relates to a kind of silk-like proteins production technology, belong to food processing technology field.
Background technology
Current people increasingly pay attention to the development and utilization technology to vegetable protein, but are found in actual work, when
It using Gluten, soy meal is raw material or this soybean protein isolate etc. for raw material that preceding nematophyte histone, which is, by stirring
Mix, extrude and the machinery such as expanded and Equipment for Heating Processing processing prepare production, although can meet the needs of production to a certain degree, but
Production technology is relative complex, process parameter control precision extreme difference, so as to have a strong impact on the stability and reliability of technique, simultaneously
Also easily cause the loss of nutrition in soybean fiber, while also influence whether the eating mouth feel of product, while it is current in order to
Long fibre soybean protein is obtained, in process of production, often also needs to add substantial amounts of additive in the feed, so that in increase
While product cost, separately cause commercial synthesis product etc. to be mixed into soy protein products, had a strong impact on product it is edible can
By property and security, while nutrition mostlys come from the nutrients of soybean itself in current thread textured soybean protein
Matter, therefore nutrition is relatively single, reaches the nutritive value of vegetable protein, using effect and is applicable so as to significantly limit
Scope, therefore for this present situation, in the urgent need to developing a kind of brand-new composite plant egg rich in polytype nutrition
White product, the need for meeting actual use.
The content of the invention
In view of the shortcomings of the prior art, the present invention, which provides one kind, uses the thread tissue egg of various plants protein production
White preparation method.
To achieve these goals, the present invention is to realize by the following technical solutions:
A kind of preparation method of the thread histone of use various plants protein production, comprises the following steps:
The first step, material is mixed to form by the raw material of following parts by weight, wherein:Temperature is -10 DEG C -0 DEG C of low temperature soy meal
20-30 parts, 25-40 parts of protein isolate, 10-15 parts of Gluten, 5-10 parts of peanut protein, 5-10 parts of pea protein, walnut protein
3-5 parts, surplus be protein concentrate mixed;
Second step, it is 8-12 parts of deionized water to add parts by weight in the material that the first step is mixed to form, and infiltrates 5-10
Minute;
3rd step, after second step operation is completed, continuously adds parts by weight and is 5-10 parts of deionized water, and infiltrate 5-10 points
Clock;
4th step, at a temperature of 5-30 DEG C, is stirred by double-screw agitator to material, while by material spiral forward
Conveying;
5th step, at a temperature of 40-60 DEG C, carries out tentatively extruding and stirring by the area of double screw extruder first to material,
So as to improve the viscosity of material, wherein extruding force is 1-3kg/cm2;
6th step, at a temperature of 100-125 DEG C, is extruded material by the area of double screw extruder second, is crushed, so that
The viscosity of material is further improved, extruding force is 3-5 kg/cm2;
7th step, at a temperature of 125-140 DEG C, is extruded material, kneading by the area of double screw extruder the 3rd, makes thing
Material preliminarily forms fibre structure, and extrusion force is 3-5 kg/cm2;
8th step, at a temperature of 140-170 DEG C, material is extruded by area to the SECTOR-SEVEN of double screw extruder the 3rd,
Kneading, makes material fully cure, and extruding force is 5-8 kg/cm2;
9th step, at a temperature of 140-160 DEG C, fiber weight is carried out by double screw extruder Section Eight to the tenth area to material
Group, extruding force is 8-10kg/cm2;
Tenth step, at a temperature of 140-190 DEG C, by the area of double screw extruder the 11st and No.12 District it is thread to material enter
Row restructuring, make material it is thread it is orderly arranged, extruding force is 4-10kg/cm2;
11st step, at a temperature of 150-170 DEG C, is extruded material by double screw extruder, is heated, make material shape
Into thread density in 0.5-2g/ centimetres of m3 fibre structure, extruding force is 3-12.5 kg/cm2;
12nd step, by material by internal diameter progressively or the increased passage of gradient, and progressively discharge the extruding force to material;
13rd step, discharges material with uniform extruding force by the passage of constant inner diameter by material, makes the protein point of material
Mutually bonding preliminarily forms 10mm-100mm fiber to son under forward thrust effect, and material of the filamentary fibers below is pushed away
Power and vias inner walls frictional force effect under along direction of advance ordered arrangement be linear pattern meat-like filament;
14th step, the passage that material is progressively reduced by internal diameter and the extruding force for being stepped up being applied to material, later
Under the frictional force effect of material thrust and vias inner walls, linear pattern filamentary fibers are made to be gradually formed along direction of advance moulding fixed
Type, and wire drawing is finally extruded into the long filamentary fibers of 10mm-100mm, you can obtain finished product product.
Further, in described the 12nd step and the 13rd step, the material speed of service is:350rpm-600rpm materials
Rate of pressure release is:5500g/min—6100g/min
Further, in the 12nd described step, channel internal diameter scaling up is:75mm:78mm:80mm:75mm
Further, the tenth described step, material formation fibre structure density be:0.3-0.7g/cm³
Further, in the 13rd and the 14th described step, the thrust of subsequent material is:1.6N/min materials and vias inner walls
Kinetic force of friction be:1.2-2.3μ
Further, the pitch and screw slotting and double screw extruder in the described area of double screw extruder second to the 5th area
Pitch and spiral the change ratio in one area are 20mm:18mm.
Further, the pitch and spiral and double screw extruder in the area of described double screw extruder the 3rd to the 5th area
Pitch and spiral the change ratio in 2 area are 25mm:20mm.
Compared with prior art, the advantages of the present invention are:
The preparation method automaticity that the present invention is provided is high, and technological process normalization is good, easy to learn, and machined parameters data
Control is convenient, is favorably improved the stability and reliability of processing technology, and reaches the purpose for improving product quality and quality, together
When the preparation method that provides of the present invention also contribute to product nutrition and mouthfeel, and be that can obtain without any additive
The thread histone product of high-quality.
Embodiment
To be easy to understand the technical means, the inventive features, the objects and the advantages of the present invention, with reference to specific
Embodiment, is expanded on further the present invention.
Embodiment 1
A kind of preparation method of the thread histone of use various plants protein production, comprises the following steps:
The first step, material is mixed to form by the raw material of following parts by weight, wherein:Temperature is -10 DEG C of low temperature soy meal 20 part, point
30 parts from albumen, 11 parts of Gluten, 8 parts of peanut protein, 6 parts of pea protein, 4 parts of walnut protein, surplus be protein concentrate carry out
Mixing;
Second step, adds the deionized water that parts by weight are 10 parts, and infiltrate 6 minutes in the material that the first step is mixed to form;
3rd step, after second step operation is completed, continuously adds the deionized water that parts by weight are 8 parts, and infiltrate 10 minutes;
4th step, at a temperature of 25 DEG C, is stirred by double-screw agitator to material, while material spiral is defeated forward
Send;
5th step, at a temperature of 50 DEG C, carries out tentatively extruding and stirring by the area of double screw extruder first to material, so that
The viscosity of material is improved, wherein extruding force is 3kg/cm2;
6th step, at a temperature of 110 DEG C, is extruded material by the area of double screw extruder second, is crushed, so as to enter one
Step improves the viscosity of material, and extruding force is 4 kg/cm2;
7th step, at a temperature of 130 DEG C, is extruded material, kneading by the area of double screw extruder the 3rd, at the beginning of making material
Step forms fibre structure, and extrusion force is 4 kg/cm2;
8th step, at a temperature of 160 DEG C, is extruded material, kneading by area to the SECTOR-SEVEN of double screw extruder the 3rd,
Material is set fully to cure, extruding force is 6 kg/cm2;
9th step, at a temperature of 150 DEG C, fiber restructuring is carried out by double screw extruder Section Eight to the tenth area to material,
Extruding force is 10kg/cm2;
Tenth step, at a temperature of 180 DEG C, passes through the area of double screw extruder the 11st and No.12 District carry out weight thread to material
Group, make material it is thread it is orderly arranged, extruding force is 8kg/cm2;
11st step, at a temperature of 160 DEG C, is extruded material by double screw extruder, is heated, and makes material formation silk
Shape density is in 1g/ centimetres of m3 fibre structure, and extruding force is 4.5 kg/cm2;
12nd step, by material by internal diameter progressively or the increased passage of gradient, and progressively discharge the extruding force to material;
13rd step, discharges material with uniform extruding force by the passage of constant inner diameter by material, makes the protein point of material
Sub mutually bonding preliminarily forms 50mm fiber under forward thrust effect, and the filamentary fibers are in material thrust below and lead to
Road inwall frictional force effect under along direction of advance ordered arrangement be linear pattern meat-like filament;
14th step, the passage that material is progressively reduced by internal diameter and the extruding force for being stepped up being applied to material, later
Under the frictional force effect of material thrust and vias inner walls, linear pattern filamentary fibers are made to be gradually formed along direction of advance moulding fixed
Type, and wire drawing is finally extruded into the long filamentary fibers of 100mm, you can obtain finished product product.
In the present embodiment, in the 12nd described step and the 13rd step, the material speed of service is:600rpm material pressures are released
Putting speed is: 6100g/min
In the present embodiment, in the 12nd described step, channel internal diameter scaling up is:75mm:78mm:80mm:75mm
In the present embodiment, the tenth described step, material formation fibre structure density be:0.5g/cm³
In the present embodiment, in the 13rd and the 14th described step, the thrust of subsequent material is:In 1.6N/min materials and passage
The kinetic force of friction of wall is:1.5μ
In the present embodiment, the pitch and screw slotting and double screw extruder in the described area of double screw extruder second to the 5th area
Pitch and spiral the change ratio in the first area are 20mm:18mm.
In the present embodiment, the pitch and spiral and double screw extruder in the described area of double screw extruder the 3rd to the 5th area
Pitch and spiral the change ratio in the second area are 25mm:20mm.
Embodiment 2
A kind of preparation method of the thread histone of use various plants protein production, comprises the following steps:
The first step, material is mixed to form by the raw material of following parts by weight, wherein:Temperature is 0 DEG C of 25 parts of low temperature soy meal, separation
35 parts of albumen, 10 parts of Gluten, 5 parts of peanut protein, 5 parts of pea protein, 3 parts of walnut protein, surplus are that protein concentrate is mixed
Close
Second step, adds the deionized water that parts by weight are 8 parts, and infiltrate 6 minutes in the material that the first step is mixed to form;
3rd step, after second step operation is completed, continuously adds the deionized water that parts by weight are 5 parts, and infiltrate 10 minutes;
4th step, at a temperature of 20 DEG C, is stirred by double-screw agitator to material, while material spiral is defeated forward
Send;
5th step, at a temperature of 40 DEG C, carries out tentatively extruding and stirring by the area of double screw extruder first to material, so that
The viscosity of material is improved, wherein extruding force is 2kg/cm2;
6th step, at a temperature of 110 DEG C, is extruded material by the area of double screw extruder second, is crushed, so as to enter one
Step improves the viscosity of material, and extruding force is 4 kg/cm2;
7th step, at a temperature of 130 DEG C, is extruded material, kneading by the area of double screw extruder the 3rd, at the beginning of making material
Step forms fibre structure, and extrusion force is 3-5 kg/cm2;
8th step, at a temperature of 150 DEG C, is extruded material, kneading by area to the SECTOR-SEVEN of double screw extruder the 3rd,
Material is set fully to cure, extruding force is 8 kg/cm2;
9th step, at a temperature of 160 DEG C, fiber restructuring is carried out by double screw extruder Section Eight to the tenth area to material,
Extruding force is 9kg/cm2;
Tenth step, at a temperature of 190 DEG C, passes through the area of double screw extruder the 11st and No.12 District carry out weight thread to material
Group, make material it is thread it is orderly arranged, extruding force is 8kg/cm2;
11st step, at a temperature of 170 DEG C, is extruded material by double screw extruder, is heated, and makes material formation silk
Shape density is in 2g/ centimetres of m3 fibre structure, and extruding force is 11.5 kg/cm2;
12nd step, by material by internal diameter progressively or the increased passage of gradient, and progressively discharge the extruding force to material;
13rd step, discharges material with uniform extruding force by the passage of constant inner diameter by material, makes the protein point of material
Sub mutually bonding preliminarily forms 30mm fiber under forward thrust effect, and the filamentary fibers are in material thrust below and lead to
Road inwall frictional force effect under along direction of advance ordered arrangement be linear pattern meat-like filament;
14th step, the passage that material is progressively reduced by internal diameter and the extruding force for being stepped up being applied to material, later
Under the frictional force effect of material thrust and vias inner walls, linear pattern filamentary fibers are made to be gradually formed along direction of advance moulding fixed
Type, and wire drawing is finally extruded into the long filamentary fibers of 50mm, you can obtain finished product product.
In the present embodiment, in the 12nd described step and the 13rd step, the material speed of service is:500rpm material pressures are released
Putting speed is:6000g/min
In the present embodiment, in the 12nd described step, channel internal diameter scaling up is:75mm:78mm:80mm:75mm
In the present embodiment, the tenth described step, material formation fibre structure density be:0.4g/cm³
In the present embodiment, in the 13rd and the 14th described step, the thrust of subsequent material is:In 1.6N/min materials and passage
The kinetic force of friction of wall is:1.2μ
In the present embodiment, the pitch and screw slotting and double screw extruder in the described area of double screw extruder second to the 5th area
Pitch and spiral the change ratio in the first area are 20mm:18mm.
In the present embodiment, the pitch and spiral and double screw extruder in the described area of double screw extruder the 3rd to the 5th area
Pitch and spiral the change ratio in the second area are 25mm:20mm.
Compared with prior art, the advantages of the present invention are:
The preparation method automaticity that the present invention is provided is high, and technological process normalization is good, easy to learn, and machined parameters data
Control is convenient, is favorably improved the stability and reliability of processing technology, and reaches the purpose for improving product quality and quality, together
When the preparation method that provides of the present invention also contribute to after product nutrition, mouthfeel, and can be obtained without any additive
To the thread histone product of high-quality.
The general principle and principal character and advantages of the present invention of the present invention has been shown and described above.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the simply explanation described in above-described embodiment and specification is originally
The principle of invention, without departing from the spirit and scope of the present invention, various changes and modifications of the present invention are possible, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (7)
1. a kind of preparation method of the thread histone of use various plants protein production, it is characterised in that:Described use is more
The preparation method for planting the thread histone of plant protein production comprises the following steps:
The first step, material is mixed to form by the raw material of following parts by weight, wherein:Temperature is -10 DEG C -0 DEG C of low temperature soy meal
20-30 parts, 25-40 parts of protein isolate, 10-15 parts of Gluten, 5-10 parts of peanut protein, 5-10 parts of pea protein, walnut protein
3-5 parts, surplus be protein concentrate mixed;
Second step, it is 8-12 parts of deionized water to add parts by weight in the material that the first step is mixed to form, and infiltrates 5-10
Minute;
3rd step, after second step operation is completed, continuously adds parts by weight and is 5-10 parts of deionized water, and infiltrate 5-10 points
Clock;
4th step, at a temperature of 5-30 DEG C, is stirred by double-screw agitator to material, while by material spiral forward
Conveying;
5th step, at a temperature of 40-60 DEG C, carries out tentatively extruding and stirring by the area of double screw extruder first to material,
So as to improve the viscosity of material, wherein extruding force is 1-3kg/cm2;
6th step, at a temperature of 100-125 DEG C, is extruded material by the area of double screw extruder second, is crushed, so that
The viscosity of material is further improved, extruding force is 3-5 kg/cm2;
7th step, at a temperature of 125-140 DEG C, is extruded material, kneading by the area of double screw extruder the 3rd, makes thing
Material preliminarily forms fibre structure, and extrusion force is 3-5 kg/cm2;
8th step, at a temperature of 140-170 DEG C, material is extruded by area to the SECTOR-SEVEN of double screw extruder the 3rd,
Kneading, makes material fully cure, and extruding force is 5-8 kg/cm2;
9th step, at a temperature of 140-160 DEG C, fiber weight is carried out by double screw extruder Section Eight to the tenth area to material
Group, extruding force is 8-10kg/cm2;
Tenth step, at a temperature of 140-190 DEG C, by the area of double screw extruder the 11st and No.12 District it is thread to material enter
Row restructuring, make material it is thread it is orderly arranged, extruding force is 4-10kg/cm2;
11st step, at a temperature of 150-170 DEG C, is extruded material by double screw extruder, is heated, make material shape
Into thread density in 0.5-2g/ centimetres of m3 fibre structure, extruding force is 3-12.5 kg/cm2;
12nd step, by material by internal diameter progressively or the increased passage of gradient, and progressively discharge the extruding force to material;
13rd step, discharges material with uniform extruding force by the passage of constant inner diameter by material, makes the protein point of material
Mutually bonding preliminarily forms 10mm-100mm fiber to son under forward thrust effect, and material of the filamentary fibers below is pushed away
Power and vias inner walls frictional force effect under along direction of advance ordered arrangement be linear pattern meat-like filament;
14th step, the passage that material is progressively reduced by internal diameter and the extruding force for being stepped up being applied to material, later
Under the frictional force effect of material thrust and vias inner walls, linear pattern filamentary fibers are made to be gradually formed along direction of advance moulding fixed
Type, and wire drawing is finally extruded into the long filamentary fibers of 10mm-100mm, you can obtain finished product product.
2. a kind of its feature of the preparation method of thread histone of use various plants protein production according to claim 1
It is:In the 12nd described step and the 13rd step, the material speed of service is:350rpm-600rpm material pressure rate of release
For:5500g/min—6100g/min.
3. a kind of preparation method of thread histone of use various plants protein production according to claim 1, it is special
Levy and be:In the 12nd described step, channel internal diameter scaling up is:75mm:78mm:80mm:75mm.
4. a kind of preparation method of thread histone of use various plants protein production according to claim 1, it is special
Levy and be:The tenth described step, material formation fibre structure density be:0.3-0.7g/cm³.
5. a kind of preparation method of thread histone of use various plants protein production according to claim 1, it is special
Levy and be:In the 13rd and the 14th described step, the thrust of subsequent material is:1.6N/min, material and vias inner walls it is dynamic
Frictional force is:1.2-2.3μ.
6. a kind of preparation method of thread histone of use various plants protein production according to claim 1, it is special
Levy and be:The pitch and screw slotting in the described area of double screw extruder second to the 5th area and the area of double screw extruder first
It is 20mm that pitch and spiral, which change ratio,:18mm.
7. a kind of preparation method of thread histone of use various plants protein production according to claim 1, it is special
Levy and be:The pitch and spiral and the pitch in the area of double screw extruder second in the described area of double screw extruder the 3rd to the 5th area
It is 25mm with spiral change ratio:20mm.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113826756A (en) * | 2021-09-28 | 2021-12-24 | 宁波市素莲食品有限公司 | Plant protein meat preparation device and method based on high-humidity extrusion cold-pressed oil bean pulp |
CN115104725A (en) * | 2021-03-18 | 2022-09-27 | 华南农业大学 | Plant-based meat analogue based on whole components of needle mushroom sporocarp and preparation method of plant-based meat analogue |
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CN101120757A (en) * | 2007-09-10 | 2008-02-13 | 林鸿仿 | Vegetarian meat five cereals food |
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CN104957607A (en) * | 2015-06-08 | 2015-10-07 | 杭州福百嘉生物科技有限公司 | Wet recombination method of vegetable protein |
CN105660989A (en) * | 2016-04-13 | 2016-06-15 | 河南曙光生物科技有限公司 | Preparation method of filiform tissue protein |
CN105724727A (en) * | 2016-04-13 | 2016-07-06 | 河南曙光生物科技有限公司 | Preparation method of textured soybean protein concentrate |
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