CN101444254B - Method for removing flaxseed gum from flaxseed meal by extrusion and expanding - Google Patents

Method for removing flaxseed gum from flaxseed meal by extrusion and expanding Download PDF

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Publication number
CN101444254B
CN101444254B CN2008102475601A CN200810247560A CN101444254B CN 101444254 B CN101444254 B CN 101444254B CN 2008102475601 A CN2008102475601 A CN 2008102475601A CN 200810247560 A CN200810247560 A CN 200810247560A CN 101444254 B CN101444254 B CN 101444254B
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flax
rice
flaxseed
dregs
extrusion
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CN101444254A (en
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李栋
吴敏
汪立君
毛志怀
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China Agricultural University
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
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    • Y02P60/87Re-use of by-products of food processing for fodder production

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Abstract

The invention discloses a method for removing flaxseed gum from flaxseed meal by extrusion and expanding, which belongs to the technical field of agricultural products processing. The method uses waste residual flaxseed meal produced during flaxseed oil production in a flaxseed oil processing plant as a raw martial, and removes flaxseed gum in the flaxseed meal, which may impact on digestion and absorption of animals, by extrusion and expanding technology. The specific process comprises the steps of removing flaxseed gum from flaxseed meal at an extrusion temperature of 80-160 DEG C, a rotation speed of 60-80rpm and a feeding speed of 30-35 kg/h, and the one-step removal rate of flaxseed gum from flaxseed meal is 52.0-83.2%. The process proposed in the invention can realize gum removal and aging at the same time and can effectively improve the feed efficiency of flaxseed meal; and has the advantages simple equipment, convenient operation, low cost, rapidness, high profit, etc.

Description

A kind of extrusion is removed the method for flax glue in flax dregs of rice
Technical field
The present invention relates to a kind of extruding and puffing technology and remove the method for flax glue in flax dregs of rice, belong to technical field of agricultural product process.
Background technology
Linseed claims flaxseed again, is the seed of flax family (Linaceae) plant flax.World's linseed output increased sharply in nearly ten years, and China has become and is only second to Canadian second-biggest-in-the-world linseed and produces state, and the output of Chinese linseed accounts for 20% of world's total amount.Wherein, linseed oil is rich in about 73% polyunsaturated fatty acid, 18% monounsaturated fatty acids and become the edible oil and fat source of high-quality.Will certainly produce a large amount of degreasing dregs of rice like this, be rich in protein, lignanoid, Soluble Fiber, mineral matter and vitamins and other nutritious components in flax dregs of rice, it is available valuable source, as not recycled, not only cause the wasting of resources, also can be corrupt owing to piling up, cause serious environmental to pollute.In addition, it contains the breach that rich in protein can replenish protein feed on the market well.But,,, and then reduce the trophism of flax dregs of rice as animal feed because of it influences the absorption of nutritional labeling in the feed comprising flax glue owing to there are some ANFs in flax dregs of rice.The existence of flax glue can influence the deep processing of flax dregs of rice equally, and for example, microbial fermentation flax dregs of rice can also just can't carry out for the fermentation of flax dregs of rice fully because the existence of flax glue makes microorganism to grow fully.
The extrusion process technology is that collection mixing, stirring, fragmentation, heating, boiling, sterilization, expanded and moulding etc. are the new and high technology of one, is widely used in food and feed processing industry.In extrusion pressing puffing process, powder or granular material are converted to face dough plasticising, thickness; Boiomacromolecule is after high temperature, high pressure, instantaneous extruding, and destroyed, the secondary bond fission of space structure, peptide bond are loose, and protein molecule rearranges; The biopolymer structure then can be redirected slabbing or filamentary structure, thereby finishes the matter structure reorganization of natural polymer, protein and the devolatilization of harmful substance, more is of value to its value.If the place allows material temperature, pressure discharge suddenly at the extruding die orifice, also can form the puff of porosity and looseness, help digestion and sweat.
According to above-mentioned principle, flax glue is a kind of polysaccharide mixture, reduce by the high temperature of extrusion, the polysaccharide molecular weight that high shear forces can make flax glue, be degraded to the little polysaccharide of monose or molecular weight, show as the viscosity of the water-soluble glue that has reduced flax dregs of rice effectively, reach the purpose of removing flax glue.
Summary of the invention
The purpose of this invention is to provide a kind of extruding and puffing technology and remove the method for flax glue in flax dregs of rice.
Described extrusion is removed the method for flax glue in flax dregs of rice, is that the waste residue flax dregs of rice that produced during with linolein process plants linseed oil are raw material, adopts extruding and puffing technology to remove flax glue in flax dregs of rice, and concrete technology is:
1) with after sheet flax dregs of rice raw material handling impurity elimination, handles or roll with pulverizer, make flax dregs of rice pulverize and be powder by grease pulverizer or feed;
2) in above-mentioned flax dregs of rice powder, add corn flour, and it is sprayed, when spraying, constantly stir, to regulate the mixture moisture content by a water mist spray device;
3) utilize twin-screw extruder that flax dregs of rice are carried out the extrusion processing of coming unstuck then;
4) at last expanded back material is carried out drying processing, after the gained drying expanded sample after testing the flax glue clearance be 52.0~73.2%.
Described flax dregs of rice are high temperature flax dregs of rice or low temperature flax dregs of rice, and moisture content is 6.07%~6.23%, and total polyoses content is 121.59mg/g, and flax glue extract viscosity is 142.0mpas.
Described flax dregs of rice powder size is 20~120 orders.
Described corn flour adding proportion accounts for 5~20% of mixture gross mass.
Described mixture moisture content is 18.8~35.1%.
The described extrusion treatment conditions of coming unstuck are: the extrusion temperature is 80~160 ℃, and screw speed is 60~180 commentaries on classics/min, and rate of feeding is 30~35kg/h.
Described drying is treated to 60~70 ℃ of oven dry or normal temperature dries.
The inventive method is simple and reliable, easy to operate, cost is low, speed is fast, flax glue clearance height.Technology of the present invention is compared with biological degumming method with existing chemistry, has not only improved a clearance of flax glue, and has made the nutrition digestion of flax dregs of rice significantly improve, and has reduced because the waste liquid that chemistry and bioanalysis come unstuck and produced.Realized coming unstuck and maturing process of flax dregs of rice simultaneously, can produce protein feed into a kind of high-quality.
The specific embodiment
Following examples are used to illustrate the present invention, but are not used for limiting the scope of the invention.
Embodiment 1
One, flax dregs of rice roll or pulverize
After sheet flax dregs of rice raw material 3kg cleaning impurity elimination, pulverize or roll by the grease pulverizer and be the powder of granularity in 20-120 order scope.
Two, flax dregs of rice powder adds corn flour and moisture content adjusting
Get flax dregs of rice 2kg after the pulverizing, adding corn flour (by mixture gross mass percentage) is 5%, and fully mixes.The mixture moisture content of flax dregs of rice and corn flour is regulated by a water mist spray device, when spraying, constantly stirs, and be 35.1% to carry out moisture content and regulate according to mass ratio.
Three, extrusion is handled
Utilize twin-screw extruder (SLG67-18.5, Beijing generation connection machinery plant) to carry out the extrusion processing in flax dregs of rice and the corn flour mixture that regulate moisture content, the extrusion temperature is 80 ℃, and screw speed is 180 commentaries on classics/min, and rate of feeding is 35kg/h.
Four, expanded sample drying and detection
Collect expanded back sample at the baking oven inner drying, temperature is 60-70 ℃.Expanded sample is pulverized back adding 100mL deionized water after getting the 10g drying, and at room temperature (22 ℃) utilize magnetic stirring apparatus to extract flax glue 3h.With turbid solution under 5000 commentaries on classics/min conditions centrifugal 20 minutes, get supernatant and be used for viscosity measurement after extract finishing.Viscosity measurement uses flow graph (AR2000ex, U.S. TA instrument company) to carry out under constant shear rate and uniform temp, obtains the viscosity of extract, and utilizes following formula to calculate the clearance of flax glue:
Figure G2008102475601D00041
Triplicate according to the method described above, averaging is designated as the flax glue clearance.After testing, the flax glue clearance is 52.0% ± 1.35% (mean+SD), and expanded sample shows as loose porous outward appearance, fragrant odour.
Embodiment 2
One, flax dregs of rice roll or pulverize
After sheet flax dregs of rice raw material 3kg cleaning impurity elimination, pulverize or roll by the grease pulverizer and be the powder of granularity in 20-120 order scope.
Two, flax dregs of rice powder adds corn flour and moisture content adjusting
Get flax dregs of rice 2kg after the pulverizing, adding corn flour (by mixture gross mass percentage) is 10%, and fully mixes.The mixture moisture content of flax dregs of rice and corn flour is regulated by a water mist spray device, when spraying, constantly stirs, and be 35.1% to carry out moisture content and regulate according to mass ratio.
Three, extrusion is handled
Utilize twin-screw extruder (SLG67-18.5, Beijing generation connection machinery plant) to carry out the extrusion processing in flax dregs of rice and the corn flour mixture that regulate moisture content, the extrusion temperature is 100 ℃, and screw speed is 140 commentaries on classics/min, and rate of feeding is 34kg/h.
Four, expanded sample drying and detection
Collect expanded back sample at the baking oven inner drying, temperature is 60~70 ℃.Expanded sample is pulverized back adding 100mL deionized water after getting the 10g drying, and at room temperature (22 ℃) utilize magnetic stirring apparatus to extract flax glue 3h.With turbid solution under 5000 commentaries on classics/min conditions centrifugal 20 minutes, get supernatant and be used for viscosity measurement after extract finishing.Viscosity measurement uses flow graph (AR2000ex, U.S. TA instrument company) to carry out under constant shear rate and uniform temp, obtains the viscosity of extract, and utilizes following formula to calculate the clearance of flax glue:
Figure G2008102475601D00051
Triplicate according to the method described above, averaging is designated as the flax glue clearance.After testing, the flax glue clearance is 59.4% ± 1.50% (mean+SD), and expanded sample shows as loose porous outward appearance, fragrant odour.
Embodiment 3
One, flax dregs of rice roll or pulverize
After sheet flax dregs of rice raw material 3kg cleaning impurity elimination, pulverize or roll by the grease pulverizer and be the powder of granularity in 20-120 order scope.
Two, flax dregs of rice powder adds corn flour and moisture content adjusting
Get flax dregs of rice 2kg after the pulverizing, adding corn flour (by mixture gross mass percentage) is 15%, and fully mixes.The mixture moisture content of flax dregs of rice and corn flour is regulated by a water mist spray device, when spraying, constantly stirs, and be 31.8% to carry out moisture content and regulate according to mass ratio.
Three, extrusion is handled
Utilize twin-screw extruder (SLG67-18.5, Beijing generation connection machinery plant) to carry out the extrusion processing in flax dregs of rice and the corn flour mixture that regulate moisture content, the extrusion temperature is 120 ℃, and screw speed is 100 commentaries on classics/min, and rate of feeding is 33kg/h.
Four, expanded sample drying and detection
Collect expanded back sample at the baking oven inner drying, temperature is 60~70 ℃.Expanded sample is pulverized back adding 100mL deionized water after getting the 10g drying, and at room temperature (22 ℃) utilize magnetic stirring apparatus to extract flax glue 3h.With turbid solution under 5000 commentaries on classics/min conditions centrifugal 20 minutes, get supernatant and be used for viscosity measurement after extract finishing.Viscosity measurement uses flow graph (AR2000ex, U.S. TA instrument company) to carry out under constant shear rate and uniform temp, obtains the viscosity of extract, and utilizes following formula to calculate the clearance of flax glue:
Figure G2008102475601D00061
Triplicate according to the method described above, averaging is designated as the flax glue clearance.After testing, the flax glue clearance is 68.9% ± 0.95% (mean+SD), and expanded sample shows as loose porous outward appearance, fragrant odour.
Embodiment 4
One, flax dregs of rice roll or pulverize
After sheet flax dregs of rice raw material 3kg cleaning impurity elimination, pulverize or roll by the grease pulverizer and be the powder of granularity in 20-120 order scope.
Two, flax dregs of rice powder adds corn flour and moisture content adjusting
Get flax dregs of rice 2kg after the pulverizing, adding corn flour (by mixture gross mass percentage) is 20%, and fully mixes.The mixture moisture content of flax dregs of rice and corn flour is regulated by a water mist spray device, when spraying, constantly stirs, and be 18.8% to carry out moisture content and regulate according to mass ratio.
Three, extrusion is handled
Utilize twin-screw extruder (SLG67-18.5, Beijing generation connection machinery plant) to carry out the extrusion processing in flax dregs of rice and the corn flour mixture that regulate moisture content, the extrusion temperature is 140 ℃, and screw speed is 100 commentaries on classics/min, and rate of feeding is 31kg/h.
Four, expanded sample drying and detection
Collect expanded back sample at the baking oven inner drying, temperature is 60~70 ℃.Expanded sample is pulverized back adding 100mL deionized water after getting the 10g drying, and at room temperature (22 ℃) utilize magnetic stirring apparatus to extract flax glue 3h.With turbid solution under 5000 commentaries on classics/min conditions centrifugal 20 minutes, get supernatant and be used for viscosity measurement after extract finishing.Viscosity measurement uses flow graph (AR2000ex, U.S. TA instrument company) to carry out under constant shear rate and uniform temp, obtains the viscosity of extract, and utilizes following formula to calculate the clearance of flax glue:
Figure G2008102475601D00071
Triplicate according to the method described above, averaging is designated as the flax glue clearance.After testing, the flax glue clearance is 69.8% ± 1.41% (mean+SD), and expanded sample shows as loose porous outward appearance, fragrant odour.
Embodiment 5
One, flax dregs of rice roll or pulverize
After sheet flax dregs of rice raw material 3kg cleaning impurity elimination, pulverize or roll by the grease pulverizer and be the powder of granularity in 20-120 order scope.
Two, flax dregs of rice powder adds corn flour and moisture content adjusting
Get flax dregs of rice 2kg after the pulverizing, adding corn flour (by mixture gross mass percentage) is 10%, and fully mixes.The mixture moisture content of flax dregs of rice and corn flour is regulated by a water mist spray device, when spraying, constantly stirs, and be 25.1% to carry out moisture content and regulate according to mass ratio.
Three, extrusion is handled
Utilize twin-screw extruder (SLG67-18.5, Beijing generation connection machinery plant) to carry out the extrusion processing in flax dregs of rice and the corn flour mixture that regulate moisture content, the extrusion temperature is 140 ℃, and screw speed is 60 commentaries on classics/min, and rate of feeding is 33kg/h.
Four, expanded sample drying and detection
Collect expanded back sample at the baking oven inner drying, temperature is 60~70 ℃.Expanded sample is pulverized back adding 100mL deionized water after getting the 10g drying, and at room temperature (22 ℃) utilize magnetic stirring apparatus to extract flax glue 3h.With turbid solution under 5000 commentaries on classics/min conditions centrifugal 20 minutes, get supernatant and be used for viscosity measurement after extract finishing.Viscosity measurement uses flow graph (AR2000ex, U.S. TA instrument company) to carry out under constant shear rate and uniform temp, obtains the viscosity of extract, and utilizes following formula to calculate the clearance of flax glue:
Figure G2008102475601D00081
Triplicate according to the method described above, averaging is designated as the flax glue clearance.After testing, the flax glue clearance is 73.20% ± 1.14% (mean+SD), and expanded sample shows as loose porous outward appearance, fragrant odour.
Above embodiment is only unrestricted in order to technical scheme of the present invention to be described, although the present invention is had been described in detail with reference to preferred embodiment, those of ordinary skill in the art is to be understood that, can make amendment or be equal to replacement technical scheme of the present invention, and not breaking away from the spirit and scope of technical solution of the present invention, it all should be encompassed in the middle of the claim scope of the present invention.

Claims (2)

1. an extrusion is removed the method for flax glue in flax dregs of rice, is that the waste residue flax dregs of rice that produced during with linolein process plants linseed oil are raw material, adopts extruding and puffing technology to remove flax glue in flax dregs of rice, it is characterized in that concrete technology is:
1) with after sheet flax dregs of rice raw material handling impurity elimination, handle or roll with pulverizer by grease pulverizer or feed, making flax dregs of rice be crushed to granularity is 20~120 purpose flax dregs of rice powder;
2) add 5~20% the corn flour account for the mixture gross mass in above-mentioned flax dregs of rice powder, and by a water mist spray device it is sprayed, constantly stir when spraying, regulating the mixture moisture content is 18.8~35.1%;
3) utilize twin-screw extruder that flax dregs of rice are carried out the extrusion processing of coming unstuck, extrusion then
Temperature is 80~160 ℃, and screw speed is 60~180 commentaries on classics/min, and rate of feeding is 30~35kg/h;
4) at last expanded back material is carried out drying and handle, dry treatment temperature is that 60~70 ℃ of oven dry or normal temperature dry; After the gained drying expanded sample after testing the flax glue clearance be 52.0~73.2%.
2. method according to claim 1 is characterized in that, described flax dregs of rice are high temperature flax dregs of rice or low temperature flax dregs of rice, and moisture content is 6.07%~6.23%, and total polyoses content is 121.59mg/g, and flax glue extract viscosity is 142.0mpas.
CN2008102475601A 2008-12-30 2008-12-30 Method for removing flaxseed gum from flaxseed meal by extrusion and expanding Expired - Fee Related CN101444254B (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2647506C1 (en) * 2017-04-26 2018-03-16 Общество с ограниченной ответственностью Научно-Технический Центр "Химинвест" Method of production of extruded fodder additives
RU2741101C1 (en) * 2020-06-09 2021-01-22 Общество с ограниченной ответственностью Научно-Технический Центр "Химинвест" Method for production of extruded fodder additive
RU2745610C1 (en) * 2020-10-08 2021-03-29 Общество с ограниченной ответственностью Научно-Технический Центр "Химинвест" Method for preparing expanded feed additive

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103583827A (en) * 2013-11-10 2014-02-19 河南科技学院 Method for preparing feed additive by honeysuckle decoction dreg puffed material
CN107568566B (en) * 2017-08-16 2020-12-22 新疆农垦科学院 Method for removing lint and phenol from cottonseed meal
CN113288838A (en) * 2021-06-24 2021-08-24 烟台新时代健康产业日化有限公司 Preparation method of linseed meal extract and application of linseed meal extract in hair care products
KR102598344B1 (en) * 2021-11-29 2023-11-06 농업회사법인 주식회사 가야바이오 Method of producing livestock feed to prevent rancidity of fatty acids and reduce cyanide in flaxseed through special processing

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
宋春芳 等.挤压膨化工艺参数对亚麻籽体外消化率的影响.《农业机械学报》.2008,第39卷(第3期),75-78. *
黄显南 等.膨化处理胶粘物的红外光谱分析.《中国造纸学报》.2005,第20卷(第2期),106-108. *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2647506C1 (en) * 2017-04-26 2018-03-16 Общество с ограниченной ответственностью Научно-Технический Центр "Химинвест" Method of production of extruded fodder additives
RU2741101C1 (en) * 2020-06-09 2021-01-22 Общество с ограниченной ответственностью Научно-Технический Центр "Химинвест" Method for production of extruded fodder additive
RU2745610C1 (en) * 2020-10-08 2021-03-29 Общество с ограниченной ответственностью Научно-Технический Центр "Химинвест" Method for preparing expanded feed additive

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