CN108813639A - A kind of preparation method of high dietary-fiber wire-drawing protein - Google Patents

A kind of preparation method of high dietary-fiber wire-drawing protein Download PDF

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Publication number
CN108813639A
CN108813639A CN201810467676.XA CN201810467676A CN108813639A CN 108813639 A CN108813639 A CN 108813639A CN 201810467676 A CN201810467676 A CN 201810467676A CN 108813639 A CN108813639 A CN 108813639A
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CN
China
Prior art keywords
protein
dietary
fiber wire
soybean
gluten
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810467676.XA
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Chinese (zh)
Inventor
刘有文
牛念念
张森
田翔
刘建建
史翠翠
管西建
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shandong Wan De Fu Biotechnology Co Ltd
SHANDONG WONDERFUL INDUSTRIAL GROUP Co Ltd
Original Assignee
Shandong Wan De Fu Biotechnology Co Ltd
SHANDONG WONDERFUL INDUSTRIAL GROUP Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shandong Wan De Fu Biotechnology Co Ltd, SHANDONG WONDERFUL INDUSTRIAL GROUP Co Ltd filed Critical Shandong Wan De Fu Biotechnology Co Ltd
Priority to CN201810467676.XA priority Critical patent/CN108813639A/en
Publication of CN108813639A publication Critical patent/CN108813639A/en
Pending legal-status Critical Current

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    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A23L33/17—Amino acids, peptides or proteins
    • A23L33/185—Vegetable proteins
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/20—Reducing nutritive value; Dietetic products with reduced nutritive value
    • A23L33/21—Addition of substantially indigestible substances, e.g. dietary fibres
    • A23L33/22—Comminuted fibrous parts of plants, e.g. bagasse or pulp

Abstract

The present invention relates to a kind of preparation method of high dietary-fiber wire-drawing protein, raw material group becomes：Soybean protein isolate, soy protein concentrate, defatted soybean meal, wheaten starch, Gluten, fresh bean dreg, He Shui；Include the following steps：（1）Fresh bean dreg and water 1：4 mixing, colloid mill crushes, high-pressure homogeneous that bean dregs suspension is made；（2）Soybean protein isolate, defatted soybean meal, wheaten starch, Gluten, is uniformly mixed soy protein concentrate；（3）Uniformly mixed material dosing is sent into twin-screw extruder, simultaneous quantitative injects fresh bean dreg suspension after homogeneous, carries out extrusion dissection sizing；（4）It is dry to be conveyed into drying box；（5）Finished product holding tank is cooling；（6）Product quantitative package storage.Advantage is：The elasticity of Protein filament, good toughness after wire-drawing protein good forming effect produced by the invention, rehydration；Meanwhile dietary fiber content is high, nutritive value is high.

Description

A kind of preparation method of high dietary-fiber wire-drawing protein
Technical field
The present invention relates to food processing fields, and in particular to a kind of preparation method of high dietary-fiber wire-drawing protein.
Background technique
Bean dregs are soybean further process field by-products, long containing higher dietary fiber and the soybean protein not extracted It is easily putrid and deteriorated since bean dregs moisture content is big since phase, it is not easy to save and with compared with beany and anti-nutrition because Son exists, and most of bean dregs substantially reduce bean dregs added value as feed even soil fertility quality.Small part enterprise is used to extract meals Fiber is eaten, but existing production technology can generate a large amount of waste water, increases soybean processing industry wastewater treatment burden.
Bean dregs can be used as good dietary fiber and protein source, but bean dregs cannot directly be eaten, present soybean Deep processing industry.
Summary of the invention
A kind of preparation side of high dietary-fiber wire-drawing protein is provided present invention aims at the deficiencies in the prior art are avoided Method.
The technical solution adopted by the present invention is that：
A kind of preparation method of high dietary-fiber wire-drawing protein, raw material group become（Mass percent）：
Soybean protein isolate 5%-20%,
Soy protein concentrate 25%-45%,
Defatted soybean meal 10%-20%,
Wheaten starch 4%-8%,
Gluten 20%-35%,
Fresh bean dreg 5%-15%,
Water；
Its making step is：
1）Fresh bean dreg and water are according to mass ratio 1：4 are sufficiently swollen in stirring in-tank mixing, incorporation time 15-20min, bean dregs, then It is crushed by colloid mill, bean dregs suspension is made in high pressure homogenizer, injects in agitator tank and keeps in；
2）Soybean protein isolate, soy protein concentrate, 4 defatted soybean meal of right, wheaten starch, Gluten are according to raw material group Proportional investment mixing machine is mixed, and time 15min, the strict control time, overlong time can destroy raw tissue structure Influence extrusion effect；
3）Uniformly mixed material dosing is sent into twin-screw extruder, while quantifying injection step in extruder Mixed Zone 1）In fresh bean dreg suspension carry out extrusion, extruder totally three sections of heating zones, the first 95-105 DEG C of heating zone, the second heating zone 115-125 DEG C, 125-135 DEG C of third heating zone, material is in the case where screw mixes squeeze conveying effect through three sections of heating zones, material Become molten condition, in the mold by outlet, expanded molding, cutter is divided into predetermined size；
4）The wire-drawing protein of well cutting is conveyed into drying box and is dried, and temperature controls moisture content 9%-11% less than 110 DEG C；
5）Dried finished product is delivered to holding tank and is cooled to room temperature；
6）Product quantitative package storage.
The raw material optimal proportion is（Mass percent）：Soybean protein isolate 10%, soy protein concentrate 35%, low temperature are de- Rouge dregs of beans 15%, wheaten starch 4%, Gluten 26%, fresh bean dreg 10%, appropriate amount of water.
The fresh bean dreg generated bean dregs, water content 75%-85%, egg when being same day online production soybean protein isolate Bai Hanliang 15%-20%.
It is 100 mesh 30%-40% that the defatted soybean meal, which need to be crushed to fineness degree,.
The step（1）The temperature of middle water is controlled at 25-35 DEG C.
The step（1）Middle colloid mill grinding particle size is 100 mesh.
The step（1）Middle homogenizer homogenization pressure 20-30Mpa.
The step（2）Middle mixing machine feeding sequence is the defatted soybean meal crushed, soy protein concentrate, glutelin Powder, soybean protein isolate, wheaten starch.
The step（3）Middle material and bean dregs suspension mass ratio are 10:3.
The step（3）Middle mold controls 100-110 DEG C of temperature.
The present invention has the following advantages that：Bean dregs are by crushing, the high-pressure homogeneous bean dregs suspension that becomes instead of wire-drawing protein production With water for producing, bean dregs are quickly and effectively utilized, considerably increase bean dregs added value, reduce under bean dregs processing at This；The wire-drawing protein dietary fiber content with higher produced simultaneously, good forming effect, albumen flexible after rehydration, Elasticity, nutritive value are high.
Detailed description of the invention
Fig. 1 is the process flow chart of the preparation method of high dietary-fiber wire-drawing protein.
Specific embodiment
A kind of preparation method of high dietary-fiber wire-drawing protein, raw material group become（Mass percent）：
Soybean protein isolate 5%-20%,
Soy protein concentrate 25%-45%,
Defatted soybean meal 10%-20%,
Wheaten starch 4%-8%,
Gluten 20%-35%,
Fresh bean dreg 5%-15%,
Water；
Its making step is：
1）Fresh bean dreg and water are according to mass ratio 1：4 are sufficiently swollen in stirring in-tank mixing, incorporation time 15-20min, bean dregs, then It is crushed by colloid mill, bean dregs suspension is made in high pressure homogenizer, injects in agitator tank and keeps in；
2）Soybean protein isolate, soy protein concentrate, 4 defatted soybean meal of right, wheaten starch, Gluten are according to raw material group Proportional investment mixing machine is mixed, and time 15min, the strict control time, overlong time can destroy raw tissue structure Influence extrusion effect；
3）Uniformly mixed material dosing is sent into twin-screw extruder, while quantifying injection step in extruder Mixed Zone 1）In fresh bean dreg suspension carry out extrusion, extruder totally three sections of heating zones, the first 95-105 DEG C of heating zone, the second heating zone 115-125 DEG C, 125-135 DEG C of third heating zone, material is in the case where screw mixes squeeze conveying effect through three sections of heating zones, material Become molten condition, in the mold by outlet, expanded molding, cutter is divided into predetermined size；
4）The wire-drawing protein of well cutting is conveyed into drying box and is dried, and temperature controls moisture content 9%-11% less than 110 DEG C；
5）Dried finished product is delivered to holding tank and is cooled to room temperature；
6）Product quantitative package storage.
The raw material optimal proportion is（Mass percent）：Soybean protein isolate 10%, soy protein concentrate 35%, low temperature are de- Rouge dregs of beans 15%, wheaten starch 4%, Gluten 26%, fresh bean dreg 10%, appropriate amount of water.
The fresh bean dreg generated bean dregs, water content 75%-85%, egg when being same day online production soybean protein isolate Bai Hanliang 15%-20%.
It is 100 mesh 30%-40% that the defatted soybean meal, which need to be crushed to fineness degree,.
The step（1）The temperature of middle water is controlled at 25-35 DEG C.
The step（1）Middle colloid mill grinding particle size is 100 mesh.
The step（1）Middle homogenizer homogenization pressure 20-30Mpa.
The step（2）Middle mixing machine feeding sequence is the defatted soybean meal crushed, soy protein concentrate, glutelin Powder, soybean protein isolate, wheaten starch.
The step（3）Middle material and bean dregs suspension mass ratio are 10:3.
The step（3）Middle mold controls 100-110 DEG C of temperature.
Embodiment one：
Take 100 mesh granularity, 30% defatted soybean meal 50kg after crushing, soy protein concentrate 115kg, Gluten 90kg, big Beans protein isolate 30kg, starch 15kg are successively put into blending tank, and unlatching is stirred 15 minutes, strict control incorporation time, Overlong time, which can destroy raw tissue structure, influences extrusion effect, and the material mixed is put into raw material cabin and keeps in.
The bean dregs Weighing of soybean protein isolate workshop new life output is delivered in agitator tank, while 4 times of water is added, Water temperature requires 25-30 DEG C, is mixed 15 minutes, and it is 100 mesh that pipeline, which is delivered to colloid mill grinding particle size, by high-pressure homogeneous Machine, homogenization pressure 20-30Mpa are delivered to that agitator tank is temporary, and speed of agitator is 300 revs/min after homogeneous.
Uniformly mixed material dosing is sent into twin-screw extruder, while quantitatively being injected in extruder Mixed Zone Fresh bean dreg suspension carries out extrusion after matter, and bean dregs suspension additive amount is the 30% of material, extruder totally three sections of heating zones, and first 105 DEG C of heating zone, the second 125 DEG C of heating zone, 125 DEG C of third heating zone, material pass through in the case where screw mixes squeeze conveying effect Three sections of heating zones, material become molten condition, and in the mold by outlet, expanded molding, mold controls 100 DEG C of temperature, cutter It is divided into predetermined size.
The wire-drawing protein of well cutting is conveyed into drying box and is dried, and temperature is less than 110 DEG C, by adjusting drying box crawler belt Revolving speed and hot blast temperature control moisture content 9%-11%, and dried finished product is delivered to holding tank by elevator and is cooled to room temperature, Product quantitative package storage.
Embodiment two
It takes and crushes 100 mesh granularity, 40% defatted soybean meal 30kg, soy protein concentrate 135kg, Gluten 60kg, soybean Protein isolate 60kg, starch 15kg are successively put into blending tank, and unlatching is stirred 15 minutes, strict control incorporation time.
The bean dregs 20kg of soybean protein isolate workshop new life output is delivered in agitator tank, while 4 times of water, water temperature is added It is required that 25-30 DEG C, it being mixed 15 minutes, it is 100 mesh that pipeline, which is delivered to colloid mill grinding particle size, passing through high pressure homogenizer, Homogenization pressure is 25Mpa, and agitator tank is delivered to after homogeneous and is kept in, and speed of agitator is 300 revs/min.
Uniformly mixed material dosing is sent into twin-screw extruder, while quantitatively being injected in extruder Mixed Zone Fresh bean dreg suspension carries out extrusion after matter, and bean dregs suspension additive amount is the 30% of material, extruder totally three sections of heating zones, and first 100 DEG C of heating zone, the second 120 DEG C of heating zone, 135 DEG C of third heating zone, material pass through in the case where screw mixes squeeze conveying effect Three sections of heating zones, material become molten condition, and in the mold by outlet, expanded molding, mold controls 110 DEG C of temperature, cutter It is divided into predetermined size.
The wire-drawing protein of well cutting is conveyed into drying box and is dried, and 100 DEG C of temperature, by adjusting drying box crawler belt revolving speed Moisture content 9%-11% is controlled with hot blast temperature.Dried finished product is delivered to holding tank by elevator and is cooled to room temperature.Product Quantitative package storage.
Embodiment three
It takes and crushes 100 mesh granularity, 30% defatted soybean meal 60kg, soy protein concentrate 85kg, Gluten 105kg, soybean Protein isolate 36kg, starch 24kg are successively put into blending tank, and unlatching is stirred 15 minutes, strict control incorporation time.
The bean dregs 20kg of soybean protein isolate workshop new life output is delivered in agitator tank, while 4 times of water, water temperature is added It is required that 25-30 DEG C, it being mixed 15 minutes, it is 100 mesh that pipeline, which is delivered to colloid mill grinding particle size, passing through high pressure homogenizer, Homogenization pressure is 25Mpa, and agitator tank is delivered to after homogeneous and is kept in, and speed of agitator is 300 revs/min.
Uniformly mixed material dosing is sent into twin-screw extruder, while quantitatively being injected in extruder Mixed Zone Fresh bean dreg suspension carries out extrusion after matter, and bean dregs suspension additive amount is the 30% of material, extruder totally three sections of heating zones, and first 105 DEG C of heating zone, the second 120 DEG C of heating zone, 130 DEG C of third heating zone, material pass through in the case where screw mixes squeeze conveying effect Three sections of heating zones, material become molten condition, and in the mold by outlet, expanded molding, mold controls 110 DEG C of temperature, cutter It is divided into predetermined size.
The wire-drawing protein of well cutting is conveyed into drying box and is dried, and 100 DEG C of temperature, by adjusting drying box crawler belt revolving speed Moisture content 9%-11% is controlled with hot blast temperature.Dried finished product is delivered to holding tank by elevator and is cooled to room temperature.Product Quantitative package storage.
The above case study on implementation is merely a preferred embodiment of the present invention, and is not intended to restrict the invention.Although referring to reality It applies example to describe the invention in detail, it will be understood by those of skill in the art that carrying out technical solution of the present invention each Kind combination, modification or equivalent replacement should all cover without departure from the spirit and scope of technical solution of the present invention of the invention In scope of the claims.

Claims (10)

1. a kind of preparation method of high dietary-fiber wire-drawing protein, it is characterised in that：
Its raw material group becomes（Mass percent）：
Soybean protein isolate 5%-20%,
Soy protein concentrate 25%-45%,
Defatted soybean meal 10%-20%,
Wheaten starch 4%-8%,
Gluten 20%-35%,
Fresh bean dreg 5%-15%,
Water；
Its making step is：
1）Fresh bean dreg and water are according to mass ratio 1：4 are sufficiently swollen in stirring in-tank mixing, incorporation time 15-20min, bean dregs, then It is crushed by colloid mill, bean dregs suspension is made in high pressure homogenizer, injects in agitator tank and keeps in；
2）Soybean protein isolate, soy protein concentrate, 4 defatted soybean meal of right, wheaten starch, Gluten are according to raw material group Proportional investment mixing machine is mixed, and time 15min, the strict control time, overlong time can destroy raw tissue structure Influence extrusion effect；
3）Uniformly mixed material dosing is sent into twin-screw extruder, while quantifying injection step in extruder Mixed Zone 1）In fresh bean dreg suspension carry out extrusion, extruder totally three sections of heating zones, the first 95-105 DEG C of heating zone, the second heating zone 115-125 DEG C, 125-135 DEG C of third heating zone, material is in the case where screw mixes squeeze conveying effect through three sections of heating zones, material Become molten condition, in the mold by outlet, expanded molding, cutter is divided into predetermined size；
4）The wire-drawing protein of well cutting is conveyed into drying box and is dried, and temperature controls moisture content 9%-11% less than 110 DEG C；
5）Dried finished product is delivered to holding tank and is cooled to room temperature；
6）Product quantitative package storage.
2. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：The raw material Optimal proportion is（Mass percent）：Soybean protein isolate 10%, soy protein concentrate 35%, defatted soybean meal 15%, wheat form sediment Powder 4%, Gluten 26%, fresh bean dreg 10%, appropriate amount of water.
3. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：Described is fresh Bean dregs generated bean dregs, water content 75%-85%, protein content 15%-20% when being same day online production soybean protein isolate.
4. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：Described is low It is 100 mesh 30%-40% that warm defatted soybean meal, which need to be crushed to fineness degree,.
5. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：The step Suddenly（1）The temperature of middle water is controlled at 25-35 DEG C.
6. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：The step Suddenly（1）Middle colloid mill grinding particle size is 100 mesh.
7. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：The step Suddenly（1）Middle homogenizer homogenization pressure 20-30Mpa.
8. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：The step Suddenly（2）Middle mixing machine feeding sequence is the defatted soybean meal crushed, soy protein concentrate, Gluten, soybean protein isolate, small Wheat starch.
9. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：The step Suddenly（3）Middle material and bean dregs suspension mass ratio are 10:3.
10. a kind of preparation method of high dietary-fiber wire-drawing protein according to claim 1, it is characterised in that：Described Step（3）Middle mold controls 100-110 DEG C of temperature.
CN201810467676.XA 2018-05-16 2018-05-16 A kind of preparation method of high dietary-fiber wire-drawing protein Pending CN108813639A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110915981A (en) * 2019-11-28 2020-03-27 江苏全盈生物科技有限公司 High rehydration rate tissue protein and preparation method thereof
CN112205579A (en) * 2020-10-28 2021-01-12 威海世纪博康海藻有限公司 Soybean vegetarian meat raw material containing seaweed dietary fibers, product and preparation method thereof
WO2021254412A1 (en) * 2020-06-19 2021-12-23 江南大学 Automatic production line for manufacturing and processing vegetable protein meat

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101874587A (en) * 2009-11-17 2010-11-03 刘继明 Vegetarian lunch meat and preparation method and equipment thereof
CN102283309A (en) * 2010-06-18 2011-12-21 青岛太阳石食品有限公司 Preparation process of fibre wiredrawing protein
CN104186914A (en) * 2014-07-29 2014-12-10 吉林农业大学 High-dietary-fiber textured soy protein and production 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
CN106962591A (en) * 2017-04-13 2017-07-21 安徽瑞福祥食品有限公司 A kind of full wheat wire-drawing protein and its industrialized process for preparing

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101874587A (en) * 2009-11-17 2010-11-03 刘继明 Vegetarian lunch meat and preparation method and equipment thereof
CN102283309A (en) * 2010-06-18 2011-12-21 青岛太阳石食品有限公司 Preparation process of fibre wiredrawing protein
CN104186914A (en) * 2014-07-29 2014-12-10 吉林农业大学 High-dietary-fiber textured soy protein and production 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
CN106962591A (en) * 2017-04-13 2017-07-21 安徽瑞福祥食品有限公司 A kind of full wheat wire-drawing protein and its industrialized process for preparing

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110915981A (en) * 2019-11-28 2020-03-27 江苏全盈生物科技有限公司 High rehydration rate tissue protein and preparation method thereof
WO2021254412A1 (en) * 2020-06-19 2021-12-23 江南大学 Automatic production line for manufacturing and processing vegetable protein meat
CN112205579A (en) * 2020-10-28 2021-01-12 威海世纪博康海藻有限公司 Soybean vegetarian meat raw material containing seaweed dietary fibers, product and preparation method thereof

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