CN115636979A - Method for enhancing fiber degradation of sweet potato residue - Google Patents
Method for enhancing fiber degradation of sweet potato residue Download PDFInfo
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- CN115636979A CN115636979A CN202211226538.5A CN202211226538A CN115636979A CN 115636979 A CN115636979 A CN 115636979A CN 202211226538 A CN202211226538 A CN 202211226538A CN 115636979 A CN115636979 A CN 115636979A
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
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Abstract
The invention relates to the field of animal nutrition and feed resource development, in particular to a method for strengthening degradation of sweet potato residue fiber 3 Processing, and performing extrusion puffing operation to enhance the degradation of sweet potato residue fiber,in the extrusion process, naHCO is used synergistically 3 And glycerine to enhance the extrusion effect by heating NaHCO 3 CO produced 2 The internal pressure is improved, and the glycerol with high boiling point and specific heat performance is used for improving the extrusion temperature, so that the degradation capability of cellulose and hemicellulose can be obviously improved, the yield of glucose and xylose is obviously improved, the additional value of sweet potato residue is improved, and the extrusion puffing effect is obviously improved.
Description
Technical Field
The invention relates to the field of animal nutrition and feed resource development, in particular to a method for enhancing the degradation of sweet potato residue fibers.
Background
Sweet potato is one of food crops in China, the planting area and the yield of the sweet potato are in the top of the world, sweet potato residues are byproducts generated in the sweet potato starch extraction process, account for 10% -14% of the total amount of the sweet potato starch, are discharged along with wastewater by many enterprises, contain a large amount of nutrient substances including starch, dietary fiber, protein and the like, wherein the starch content accounts for 48.26%, the dietary fiber accounts for 26.73%, and the protein accounts for 3.35%, and deep processing and comprehensive utilization of the sweet potato residues can reduce environmental pollution, increase the economic value of the sweet potato residues and realize sustainable utilization of resources.
The sweet potato is used as an important food crop in China, is mainly used for producing starch, can generate a large amount of sweet potato residues (1000 ten thousand tons/year), contains rich fiber resources, but is used for animal feeding in a small amount (within 10 percent), and most of the sweet potato residues are directly discarded, so that serious environmental pollution and resource waste are caused. Obviously, the efficient development and utilization of the sweet potato residues are an important way for solving the energy and environmental crisis. The sweet potato residue is composed of cellulose, hemicellulose and lignin, and the cellulose forms a three-dimensional network structure with the lignin and the hemicellulose due to strong hydrogen bonds, high polymerization degree and high crystallinity, so that how to efficiently hydrolyze the cellulose and the hemicellulose is the key of utilizing sweet potato residue fiber resources.
The sweet potato residue fiber degradation method in the prior art mainly comprises acidolysis, alkaline hydrolysis, thermochemical treatment, ionic liquid and the like, but the methods have the defects of toxic compound generation, long processing time, serious corrosion to production equipment and the like in the pretreatment process, so that the application of the pretreatment method is limited, and on the basis, the sweet potato residue fiber degradation method which is simple and convenient to operate, large in processing scale and free of pollution is needed.
Disclosure of Invention
Aiming at the defects of the prior art, the invention aims to provide a method for enhancing the fiber degradation of sweet potato residues.
In order to solve the technical problems, the invention adopts the following technical scheme:
a method for enhancing degradation of sweet potato residue fiber comprises subjecting sweet potato residue fiber to glycerol and NaHCO 3 Processing, and performing extrusion puffing operation in cooperation to enhance the degradation of the sweet potato residue fiber;
preferably, the method for enhancing the fiber degradation of the sweet potato residue comprises the following steps:
(1) Sequentially carrying out purification, drying and crushing pretreatment on the sweet potato residues to obtain treated sweet potato residues;
(2) Adding sweet into the sweet potato residue treated in the step (1)Oil, naHCO 3 Mixing with water, and stirring to obtain mixed sweet potato residue;
wherein the sweet potato residue contains 20-30% of water, 1-10% of glycerol and NaHCO 3 The mass to water volume ratio of (1-2 g): 1L;
(3) And (3) treating the mixed sweet potato residues by using a double-screw extrusion bulking machine, jointly hydrolyzing the sweet potato residues before extrusion and after extrusion by using cellulase and hemicellulase, and performing post-treatment to obtain the degraded sweet potato residue fiber.
Preferably, the sweet potato residue contains 25% of water, 5% of glycerin by mass and NaHCO 3 The mass to water volume ratio of (2) is 1g/L.
Preferably, the pretreatment of the sweet potato residue in the step (1) comprises the following specific steps: cleaning the sweet potato residue with water, drying to constant weight, crushing, and sieving to obtain a sweet potato residue sample.
Preferably, the screw rotating speed of the twin-screw extrusion bulking machine in the step (3) is 100-140rpm, the extrusion temperature is 110-150 ℃, and the feeding speed is 15-19Hz.
Preferably, the storage post-treatment method in step (3) comprises: drying to constant weight, sieving, sealing, drying and storing.
Preferably, the drying temperature in the step (1) and the drying time in the step (3) are both 50-70 ℃, the drying time is 24-72 hours, and the drying temperature and the drying time are both screened by adopting a 30-50 mesh screen.
Compared with the prior art, the invention has the beneficial effects that:
1. the invention uses NaHCO synergistically in the extrusion process 3 And glycerine to enhance the extrusion effect by heating NaHCO 3 CO produced 2 The internal pressure is increased, and the glycerol with high boiling point and specific heat performance is used for increasing the extrusion temperature, so that the degradation capability of cellulose and hemicellulose is obviously improved, the yield of glucose and xylose is obviously increased, the additional value of sweet potato residue is obviously increased, and the extrusion puffing effect is obviously improved;
2. compared with the traditional chemical fiber degradation process, the extrusion and puffing process obviously improves the reduction of the cellulose and the hemicellulase to the sweet potato residue fiberThe dissolving capacity, namely the spatial network structure of cellulose and hemicellulose is destroyed through extrusion and puffing; meanwhile, the grain size of the sweet potato residue after the extrusion and expansion treatment is reduced, the specific surface area contacted with the enzyme is increased, and more enzyme digestion sites are released, so that the hydrolysis rate of the enzyme is improved; by glycerol and NaHCO 3 The extrusion puffing process is synergistically enhanced, the yield of monosaccharide is improved, the energy consumption is reduced, the production cost is saved, the environmental pollution is reduced, the additional value of the sweet potato residue is obviously improved, and the extrusion puffing effect is obviously improved;
3. when the water content of the sweet potato residue is 30%, the puffing effect is good, and if the water content is low, the puffing of a sample is influenced, so that a discharge port is easily blocked; the water content is too high, the instant pressure of sample expansion can be reduced, the expansion effect can be influenced, the production cost is increased, meanwhile, the glycerol with the replacement mass fraction of 5 percent also has the best expansion effect, and NaHCO is used for replacing 3 The difference between 1 and 2g/L is not significant, so 1g/L is taken.
Drawings
Fig. 1 is a thermal stability curve a for the sweet potato residue samples of example 1, comparative example 1 and comparative example 2: comparative example 2; b: comparative example 1; c: example 1;
fig. 2 is a scanning electron micrograph a of the sweet potato residue samples of example 1, comparative example 1 and comparative example 2: comparative example 2; b: comparative example 1; c: example 1;
FIG. 3 is an infrared spectrum of a sample of sweet potato residue of example 1, comparative example 1 and comparative example 2;
FIG. 4 is an X-ray diffraction pattern of samples of sweet potato residue of example 1, comparative example 1 and comparative example 2;
fig. 5 is a graph of glucose (a) and xylose (B) yields for the sweet potato residue samples of example 1, comparative example 1 and comparative example 2.
Detailed Description
The following detailed description is provided to best modes for carrying out the invention and is to be read in connection with the accompanying drawings.
Example 1
A method for enhancing fiber degradation of sweet potato residue comprises the following steps:
(1) Thoroughly cleaning sweet potato residue with water, drying at 60 deg.C for 48 hr to constant weight, pulverizing, and sieving with 40 mesh sieve to obtain treated sweet potato residue, which is named as SPRs;
(2) Adding 25 percent of distilled water, 5 percent of glycerin and 1g/LNaHCO into the sweet potato residues treated by the SPRs in the step (1) 3 And mixing and stirring uniformly to obtain mixed sweet potato residues named as SPRs-DW-GNa;
(3) And (3) extruding the SPRs-DW-GNa sweet potato residue sample obtained in the step (2) by using a double-screw extrusion and expansion machine, wherein the rotating speed of a screw is 120rpm, the extrusion temperature is 130 ℃, the feeding speed is 17Hz, the extruded sweet potato residue sample is dried at 60 ℃ for 48h to constant weight, and the dried sweet potato residue sample is screened by a 40-mesh screen to obtain the degraded sweet potato residue fiber.
Example 2
A method for enhancing fiber degradation of sweet potato residue comprises the following steps:
(1) Thoroughly washing sweet potato residue with water, drying at 50 deg.C for 24 hr to constant weight, pulverizing, and sieving with 30 mesh sieve to obtain processed sweet potato residue;
(2) Adding 20% of distilled water, 1% of glycerol and 1g/LNaHCO into the sweet potato residue treated in the step (1) 3 And mixing and stirring uniformly to obtain mixed sweet potato residues;
(3) And (3) extruding the mixed sweet potato residue sample obtained in the step (2) by using a double-screw extrusion puffing machine, wherein the rotating speed of a screw is 100rpm, the extrusion temperature is 110 ℃, the feeding speed is 15Hz, the extruded sweet potato residue sample is dried for 24 hours at 50 ℃ to constant weight, and the sample is sieved by a 30-mesh screen to obtain the degraded sweet potato residue.
Example 3
A method for enhancing fiber degradation of sweet potato residue comprises the following steps:
(1) Thoroughly cleaning sweet potato residue with water, drying at 60 deg.C for 48 hr to constant weight, pulverizing, and sieving with 40 mesh sieve;
(2) Adding 30 mass percent of distilled water, 10 mass percent of glycerin and 2g/LNaHCO into the SPRs sweet potato residue sample in the step (1) 3 And mixing and stirring uniformly to obtain mixed sweet potato residues;
(3) And (3) extruding the mixed sweet potato residue sample obtained in the step (2) by using a double-screw extrusion puffing machine, wherein the rotating speed of a screw is 140rpm, the extrusion temperature is 150 ℃, the feeding speed is 19Hz, drying the extruded sweet potato residue sample at 70 ℃ for 72h to constant weight, and screening the dried sweet potato residue sample by using a 50-mesh screen to obtain the degraded sweet potato residue.
Comparative example 1
30% distilled water, named as SPRs-DW, was added to the sweet potato residue sample of step (1) in example 1, and the sample was processed using a twin-screw extrusion-expansion machine, and then subjected to sample testing using the same testing method as in example 1.
Comparative example 2
The same procedure as in example 1 was followed, except that the detection was carried out using the samples of SPRs obtained in step (1) of example 1.
The characterization method of the invention comprises the following steps:
research on physicochemical characteristics of sweet potato residues before and after extrusion
1. Particle size analysis
And analyzing the particle size of the sweet potato residue sample before and after extrusion by using a Malvern 3000 particle size analyzer, and evaluating the uniformity of the sweet potato residue through particle span.
2. Chemical composition
The crude protein content of the sweet potato residue sample before and after extrusion is determined by adopting an AOAC 920.87 method, the crude fat content is determined by adopting an AACC 30-25 method, and the crude ash content is determined by adopting an AOAC 923.03 method.
3. Thermogravimetric analysis (TG)
And (3) placing the sweet potato residue samples before and after extrusion in an instrument, setting the flow of protective gas nitrogen at 20mL/min, heating the furnace body from 25 ℃ to 800 ℃ at a heating rate of 20 ℃/min, and deducting a blank curve to obtain a thermogravimetric experiment curve (TG) and a micro-entropy thermogravimetric curve (DTG).
4. Differential Scanning Calorimetry (DSC)
And (3) placing the sweet potato residue sample before and after extrusion into an instrument, setting the flow of protective gas nitrogen at 20mL/min, heating the furnace body from 25 ℃ to 800 ℃ at a heating rate of 20 ℃/min, and deducting a blank curve to obtain a thermogravimetric experiment curve (TG) and a microentropy thermogravimetric curve (DTG).
Research on structural characteristics of sweet potato residues before and after extrusion
1. Scanning electron microscope
And (3) putting the sweet potato residue samples before and after extrusion into an ion sputtering coating instrument, coating a layer of gold film with the thickness of about 100nm on the surface of the sample under vacuum, and observing the morphological characteristic change of the sweet potato residue samples before and after extrusion by using a scanning electron microscope.
2. Fourier infrared spectroscopy
The method comprises the following steps of (1) placing sweet potato residue samples before and after extrusion under an infrared lamp, avoiding the samples from absorbing moisture, and mixing the sweet potato residue samples with dry KBr powder according to a mass ratio of 1:100 are mixed in an agate mortar, ground evenly and finely until no granular sensation exists, added into a pressing die and pressed into a sheet and immediately placed in a light path for scanning, and the scanning interval is 400-4000 cm -1 。
X-ray diffraction analysis
The crystal structure of the sweet potato residue samples before and after extrusion was determined using an X' Pert 3 Powedr X-ray diffractometer. The experimental condition parameters are as follows: the voltage is 40kV, and the current is 40mA; the starting angle is 5 deg., and the ending angle is 70 deg..
Research on enzymolysis effect of sweet potato residues before and after extrusion
1. Enzymatic analysis
Hydrolyzing the sweet potato residues before and after extrusion by using cellulase (10000U/g) and hemicellulase (10000U/g), adding sodium azide with the mass concentration of 0.02% to inhibit the growth of microorganisms by using a 250mL conical flask with the pH =4.8 and containing 50mL of sodium acetate buffer solution, adding 1g of sweet potato residues into each conical flask, wherein the enzyme loading amount is 15FPU/g dry weight, oscillating the conical flask at 50 ℃ and 150rpm for 72h, taking 5mL of enzymatic hydrolysate to determine the contents of glucose and xylose at intervals of 12h, carrying out enzymolysis, filtering the sweet potato residues, washing the sweet potato residues with distilled water for 5 times, drying the sweet potato residues at 80 ℃ to constant weight, and determining the contents of cellulose, hemicellulose and lignin in the sweet potato residues after the enzymolysis by using a fiber analyzer.
2. Glucose and xylose production assays
The enzymatic hydrolysate was centrifuged at 12000g at 4 ℃ for 10min, and the glucose and xylose yields in the supernatant were determined by high performance liquid chromatography with a differential refractometer (HPLC, HPX-87H column, 300mm. Times.7.8 mm), HPLC conditions: the mobile phase was 5mM H 2 SO 4 The flow rate is 0.6mL/min, the temperature is 35 ℃, the sample loading amount is 20uL, and the sample solution is filtered by a 0.22um filter membrane before sample loading.
Results and analysis
Analysis of physicochemical Properties of sweet Potato residue samples before and after extrusion
1. Particle size analysis
The average particle size and specific surface area of the sweet potato residue samples before and after extrusion are shown in Table 1, compared with the groups of the SPRs, the surface area average particle size (D3, 2) and the volume average particle size (D4, 3) of the groups of the SPRs-DW and the SPRs-DW-GNa are respectively reduced, and the specific surface area is obviously increased, which indicates that the extrusion treatment reduces the particle size of the sweet potato residue and improves the specific surface area of the sample, and the reason is that the macromolecular polymer of the sweet potato residue is degraded due to the extrusion treatment.
TABLE 1 analysis of mean particle size and specific surface area of sweet potato residue samples before and after extrusion
Sample (I) | D3,2(μm) | D4,3(μm) | Specific surface area (m) 2 /g) |
SPRs | 37.643 | 173.005 | 0.159 |
SPRs-DW | 34.716 | 165.973 | 0.173 |
SPRs-DW-Gna | 34.794 | 153.441 | 0.172 |
2. Chemical composition analysis
Chemical components of the sweet potato residue sample before and after extrusion are shown in Table 2, cellulose contents of different sweet potato residue samples after extrusion are respectively 13.5% (SPRs-DW) and 13% (SPRs-DW-GNa), and compared with an original sweet potato residue sample (13.9%), the cellulose contents are respectively reduced by 2.87% and 6.5%; in addition, the hemicellulose content of the sweet potato residue sample is reduced from 9.2 percent (SPRs) to 8.4 percent (SPRs-DW) and 7.7 percent (SPRs-DW-GNa), respectively by 8.7 percent (SPRs-DW) and 16.3 percent (SPRs-DW-GNa), and the lignin content of the sweet potato residue sample is reduced from 4.6 percent (SPRs) to 4.3 percent (SPRs-DW) and 4.0 percent (SPRs-DW-GNa), respectively by 6.5 percent (SPRs-DW) and 13 percent (SPRs-DW-GNa), so that the cellulose, hemicellulose and lignin components in the sweet potato residue sample can be remarkably degraded by extrusion and expansion treatment, wherein 25 percent of distilled water, 5 percent of glycerol and 1g/L of NaHCO are added into the sweet potato residue sample 3 The treatment group (SPRs-DW-GNa) performed best.
TABLE 2 chemical composition (%, dry basis) of sweet potato residue samples before and after extrusion
Sample (I) | Cellulose, process for producing the same, and process for producing the same | Hemicellulose | Lignin | Starch | Crude fat | Crude protein | Coarse ash content |
SPRs | 13.9 | 9.2 | 4.6 | 54.28 | 0.84 | 3.6 | 2.54 |
SPRs-DW | 13.5 | 8.4 | 4.3 | 53.82 | 0.72 | 3.1 | 3.37 |
SPRs-DW-GNA | 13 | 7.7 | 4.0 | 52.93 | 0.54 | 3.29 | 7.68 |
3. Analysis of thermal stability
The TG curve shows the presence of multi-stage thermal degradation of the sample of the sweet potato residue before and after extrusion (fig. 1), wherein the sweet potato residue before and after extrusion shows a first degradation peak at 58.19-66.18 ℃, at this stage, the moisture loss of the sweet potato residue may be the main cause of mass loss, and as the temperature rises, the carbohydrates begin to degrade, and the final products are C, CO and combustible volatile substances, thereby causing endothermic degradation to be converted into exothermic process, in the DSC spectrum, the peak is endothermic upward and the peak is downward; compared with the untreated sweet potato residue, the sweet potato residue after extrusion has smaller endothermic peak and exothermic peak, which indicates that the extrusion enhances the thermal stability of the polymer.
Analysis of structural characteristics of sweet potato residue samples before and after extrusion
1. Scanning electron microscope
The microstructure of the sweet potato residue sample before and after extrusion is shown in figure 2 (2000 times), the surface of the untreated sweet potato residue sample is flaky, which shows that the structure and the fiber structure of the sweet potato residue are kept intact (figure 2A), the fiber particles of the SPRs-DW become smaller and the cracks increase (figure 2B) after the sample is added with 30% of distilled water and is extruded, and when 25% of distilled water, 5% of glycerol and 1g/L of NaHCO are used 3 When extrusion treatment is carried out, the SpRs-DW-GNa fibers are finely crushed and have rough surfaces (figure 1C), and the observation results show that the extrusion treatment effectively breaks the stubborn structure of the sweet potato residue and is beneficial to subsequent enzymolysis, in addition, macromolecules can change into smaller soluble molecules in the extrusion process, and certain honeycomb appearance is presented, because of the cracking of glycosidic bonds and the degradation of IDF macromolecules under the extrusion action, in a word, the crushing effect of the SPRs-DW-GNa on the sweet potato residue fibers is better than that of the SPRs-DW and the SPRs.
2. Fourier infrared spectrum
Fourier infrared spectroscopy is utilized to analyze the difference of the functional group compositions of the sweet potato residue sample before and after extrusion (figure 3), and the difference is 3000cm -1 The absorption peak at (C-H) was probably due to stretching of = C-H in cellulose, at 3000cm for the groups of SPRs-DW and SPRs-DW-GNa compared to the untreated sweet potato residue group -1 The absorption peak is reduced, which shows that the cellulose content in the sweet potato residue sample is reduced after the extrusion treatment, and the cellulose reduction of the SPRs-DW-GNa treatment group is most obvious, and in addition, 1300cm -1 The absorption peak at (A) represents C-O vibration in lignin, 1376cm -1 The absorption peak at (A) may be related to C-H vibration is related, and compared with untreated sweet potato residue group, the groups of the SPRs-DW and the SPRs-DW-GNa are 1376cm -1 The absorption peak is reduced, which shows that the content of hemicellulose in the sweet potato residue sample is reduced after extrusion treatment, and the reduction effect of the SPRs-DW-GNa group is more obvious, which is consistent with the chemical composition result of the sweet potato residue in the table 2.
X-ray diffraction analysis
The X-ray diffraction spectra of the sweet potato residue samples before and after extrusion are shown in figure 4, and compared with the untreated sweet potato residue group, the diffraction peaks of the SPRs-DW and the SPRs-DW-GNa groups show a descending trend at about 20 degrees, which indicates that the crystallization index of the sweet potato residue after extrusion treatment is reduced, and the X-ray diffraction spectra are mainly related to the damage of hydrogen bonds in cellulose and the breakage of a compact structure of hemicellulose in the extrusion process, and the damage effect of the SPRs-DW-GNa group is more obvious, which is consistent with the chemical composition result of the sweet potato residue in the table 2.
4. Research on enzymolysis effect of sweet potato residues before and after extrusion
In the invention, the glucose yield of an untreated sweet potato residue sample after 48 hours of enzymolysis is 19.749g/L (figure 5A), the glucose yield of the untreated sweet potato residue sample after 72 hours of enzymolysis reaches 31.588g/L, the glucose yields of the groups SPRs-DW and SPRs-DW-GNa after extrusion are respectively 28.794 and 35.251g/L at 48 hours, the glucose yields of the groups SPRs-DW and SPRs-DW-GNa are respectively improved by 45.8% and 78.5% compared with the untreated sweet potato residue sample, the glucose yields of the groups SPRs-DW and SPRs-DW-GNa after 72 hours are respectively 43.936 and 44.925g/L, the xylose yields of the groups SPRs, SPRs-DW and SPDW-GNa are respectively improved by 39% and 42.2% compared with the untreated sweet potato residue sample, and the xylose yields of the groups SPRs, SPRs-DW and SPRs, SPDW-GNa and SPRs, 48.221 g and 10.8% compared with the glucose yields of the groups after 72 hours of enzymolysis, the glucose yields of the groups are respectively improved by 48.438 g/L and 48 h; and the glucose yield of the groups of the SPRs-DW and the SPRs-DW-GNa is 11.696 and 12.668g/L respectively at 72h, which are respectively improved by 34.2 percent and 45.3 percent compared with an untreated sweet potato residue sample.
In conclusion, 25% of distilled water, 5% of glycerol and 1g/LNaHCO are added into the sweet potato residue sample 3 After the treatment (SPRs-DW-GNa), the degradation effect on cellulose, hemicellulose and lignin of the sweet potato residue is optimal, and at the moment, the grain size of a sweet potato residue sample is reduced, the specific surface area is increased, the crystallinity is reduced, the thermal stability is enhanced, and the enzymolysis effect is optimal.
It will be apparent to those skilled in the art that various changes and modifications may be made in the present invention without departing from the spirit and scope of the invention. Thus, if such modifications and variations of the present invention fall within the scope of the claims of the present invention and their equivalents, the present invention is also intended to include such modifications and variations.
Claims (7)
1. A method for strengthening the degradation of sweet potato residue fiber is characterized in that the sweet potato residue fiber is firstly treated by adopting glycerol and NaHCO 3 And (4) processing, and performing extrusion and puffing operation in cooperation to strengthen the degradation of the sweet potato residue fiber.
2. The method for enhancing fiber degradation of sweet potato residue as claimed in claim 1, comprising the steps of:
(1) Sequentially carrying out purification, drying and crushing pretreatment on the sweet potato residue to obtain treated sweet potato residue;
(2) Adding glycerol and NaHCO into the sweet potato residue treated in the step (1) 3 Mixing with water, and stirring to obtain mixed sweet potato residue;
wherein the sweet potato residue contains 20-30% of water, 1-10% of glycerol and NaHCO 3 1-2g of mass to volume ratio of water: 1L;
(3) And (3) processing the mixed sweet potato residue obtained in the step (2) by using a double-screw extrusion puffing machine, and storing and post-processing the extruded sweet potato residue to obtain the degraded sweet potato residue fiber.
3. The method for enhancing fiber degradation of sweet potato residue according to claim 2, wherein the sweet potato residue of step (2) contains 25% water, 5% glycerin, and NaHCO 3 The mass to volume ratio of water of (1) to (1 g/L).
4. The method for enhancing fiber degradation of sweet potato residue according to claim 2, wherein the pretreatment of the sweet potato residue in the step (1) comprises the following specific steps: cleaning the sweet potato residue with water, drying to constant weight, crushing, and sieving to obtain a sweet potato residue sample.
5. The method for enhancing fiber degradation of sweet potato residue according to claim 2, wherein in the step (3), the rotation speed of the screw of the twin-screw extrusion-expansion machine is 100-140rpm, the extrusion temperature is 110-150 ℃, and the feeding speed is 15-19Hz.
6. The method for enhancing fiber degradation of sweet potato residue according to claim 2, wherein the post-storage treatment method in step (3) is as follows: drying to constant weight, sieving, sealing, drying and storing.
7. The method for enhancing the fiber degradation of the sweet potato residue as claimed in claim 6, wherein the drying temperature in step (1) and the drying time in step (3) are 50-70 ℃, the drying time is 24-72 hours, and the drying temperature and the drying time are both sieved by a 30-50 mesh sieve.
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CN105011021A (en) * | 2014-04-30 | 2015-11-04 | 湖南农业大学 | Sweet potato and bean pulp extrusion expansion flour food |
CN106509627A (en) * | 2016-10-13 | 2017-03-22 | 张家界天湘薯业有限公司 | Efficient utilization method of sweet potato residue |
CN110074419A (en) * | 2019-05-17 | 2019-08-02 | 山东理工大学 | Squeeze the method that enzymatic hydrolysis pea slag prepares soluble dietary fiber |
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CN105011021A (en) * | 2014-04-30 | 2015-11-04 | 湖南农业大学 | Sweet potato and bean pulp extrusion expansion flour food |
CN106509627A (en) * | 2016-10-13 | 2017-03-22 | 张家界天湘薯业有限公司 | Efficient utilization method of sweet potato residue |
US20190249107A1 (en) * | 2016-12-30 | 2019-08-15 | Jiangnan University | Method for Co-Production and Processing of Biological Energy Sources by Oil Crops |
CN110074419A (en) * | 2019-05-17 | 2019-08-02 | 山东理工大学 | Squeeze the method that enzymatic hydrolysis pea slag prepares soluble dietary fiber |
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