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 PDF

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Publication number
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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China
Prior art keywords
parts
thread
screw extruder
area
double screw
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CN201710262180.4A
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Inventor
张德林
张世齐
邓飞
韩高升
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Henan Standard Food Technology Co Ltd
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Henan Standard Food Technology Co Ltd
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Priority to CN201710262180.4A priority Critical patent/CN106974296A/en
Publication of CN106974296A publication Critical patent/CN106974296A/en
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    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23VINDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00Food compositions, function of food ingredients or processes for food or foodstuffs

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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

A kind of preparation method of the thread histone of use various plants protein production
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.
CN201710262180.4A 2017-04-20 2017-04-20 A kind of preparation method of the thread histone of use various plants protein production Pending CN106974296A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
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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Publication number Priority date Publication date Assignee Title
CN101120757A (en) * 2007-09-10 2008-02-13 林鸿仿 Vegetarian meat five cereals food
CN102630806A (en) * 2012-04-26 2012-08-15 北京金地三福膨化机制造(大厂)有限公司 Twin screw extrusion device and extrusion type expansion machine
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

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101120757A (en) * 2007-09-10 2008-02-13 林鸿仿 Vegetarian meat five cereals food
CN102630806A (en) * 2012-04-26 2012-08-15 北京金地三福膨化机制造(大厂)有限公司 Twin screw extrusion device and extrusion type expansion machine
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

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
CN115104725B (en) * 2021-03-18 2023-06-27 华南农业大学 Plant-based artificial meat based on full components of flammulina velutipes fruiting bodies and preparation method thereof
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

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