CN101664167A - Peanut water-soluble dietary fiber enzymatic extracting method - Google Patents
Peanut water-soluble dietary fiber enzymatic extracting method Download PDFInfo
- Publication number
- CN101664167A CN101664167A CN200910178414A CN200910178414A CN101664167A CN 101664167 A CN101664167 A CN 101664167A CN 200910178414 A CN200910178414 A CN 200910178414A CN 200910178414 A CN200910178414 A CN 200910178414A CN 101664167 A CN101664167 A CN 101664167A
- Authority
- CN
- China
- Prior art keywords
- filter residue
- peanut
- water
- dietary fiber
- soluble dietary
- 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.)
- Granted
Links
- 235000017060 Arachis glabrata Nutrition 0.000 title claims abstract description 97
- 241001553178 Arachis glabrata Species 0.000 title claims abstract description 97
- 235000010777 Arachis hypogaea Nutrition 0.000 title claims abstract description 97
- 235000018262 Arachis monticola Nutrition 0.000 title claims abstract description 97
- 235000020232 peanut Nutrition 0.000 title claims abstract description 97
- 235000013325 dietary fiber Nutrition 0.000 title claims abstract description 49
- 238000000034 method Methods 0.000 title claims abstract description 22
- 230000002255 enzymatic effect Effects 0.000 title claims abstract description 14
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 57
- 235000019441 ethanol Nutrition 0.000 claims abstract description 44
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000000843 powder Substances 0.000 claims abstract description 34
- 239000004365 Protease Substances 0.000 claims abstract description 26
- 108091005804 Peptidases Proteins 0.000 claims abstract description 22
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 claims abstract description 22
- 238000001035 drying Methods 0.000 claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 9
- 230000001376 precipitating effect Effects 0.000 claims abstract description 9
- 230000007062 hydrolysis Effects 0.000 claims abstract description 3
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 3
- 239000012141 concentrate Substances 0.000 claims description 95
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 84
- 239000000706 filtrate Substances 0.000 claims description 72
- 238000000967 suction filtration Methods 0.000 claims description 58
- 230000010355 oscillation Effects 0.000 claims description 46
- 102000004190 Enzymes Human genes 0.000 claims description 41
- 108090000790 Enzymes Proteins 0.000 claims description 41
- 229940088598 enzyme Drugs 0.000 claims description 41
- 238000001556 precipitation Methods 0.000 claims description 41
- 239000006228 supernatant Substances 0.000 claims description 32
- 108010059892 Cellulase Proteins 0.000 claims description 28
- 229940106157 cellulase Drugs 0.000 claims description 28
- 125000005909 ethyl alcohol group Chemical group 0.000 claims description 24
- 238000002390 rotary evaporation Methods 0.000 claims description 24
- 235000019419 proteases Nutrition 0.000 claims description 21
- 238000009835 boiling Methods 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 16
- 239000002994 raw material Substances 0.000 claims description 13
- 239000000047 product Substances 0.000 claims description 12
- 206010013786 Dry skin Diseases 0.000 claims description 10
- 241000196324 Embryophyta Species 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 9
- 238000012216 screening Methods 0.000 claims description 9
- 239000012153 distilled water Substances 0.000 claims description 8
- 239000000284 extract Substances 0.000 claims description 8
- 238000012545 processing Methods 0.000 claims description 8
- 101000693530 Staphylococcus aureus Staphylokinase Proteins 0.000 claims description 6
- 238000001291 vacuum drying Methods 0.000 claims description 6
- 108090000526 Papain Proteins 0.000 claims description 5
- 239000003513 alkali Substances 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 238000004108 freeze drying Methods 0.000 claims description 4
- 229940055729 papain Drugs 0.000 claims description 4
- 235000019834 papain Nutrition 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 238000010129 solution processing Methods 0.000 claims description 2
- 201000010099 disease Diseases 0.000 abstract description 5
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 102000007330 LDL Lipoproteins Human genes 0.000 abstract description 4
- 108010007622 LDL Lipoproteins Proteins 0.000 abstract description 4
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 abstract description 4
- 229920002678 cellulose Polymers 0.000 abstract description 3
- 239000001913 cellulose Substances 0.000 abstract description 3
- 150000004676 glycans Chemical class 0.000 abstract description 3
- 229920001282 polysaccharide Polymers 0.000 abstract description 3
- 239000005017 polysaccharide Substances 0.000 abstract description 3
- 239000008280 blood Substances 0.000 abstract description 2
- 210000004369 blood Anatomy 0.000 abstract description 2
- 235000012000 cholesterol Nutrition 0.000 abstract description 2
- 239000000835 fiber Substances 0.000 abstract description 2
- 235000013376 functional food Nutrition 0.000 abstract description 2
- 208000024891 symptom Diseases 0.000 abstract description 2
- 208000024172 Cardiovascular disease Diseases 0.000 abstract 1
- 229920002472 Starch Polymers 0.000 abstract 1
- 102000004139 alpha-Amylases Human genes 0.000 abstract 1
- 108090000637 alpha-Amylases Proteins 0.000 abstract 1
- 229940024171 alpha-amylase Drugs 0.000 abstract 1
- 210000001035 gastrointestinal tract Anatomy 0.000 abstract 1
- 230000003301 hydrolyzing effect Effects 0.000 abstract 1
- 239000006041 probiotic Substances 0.000 abstract 1
- 235000018291 probiotics Nutrition 0.000 abstract 1
- 239000008107 starch Substances 0.000 abstract 1
- 235000019698 starch Nutrition 0.000 abstract 1
- 235000013305 food Nutrition 0.000 description 9
- 241000238631 Hexapoda Species 0.000 description 7
- 241000607479 Yersinia pestis Species 0.000 description 7
- 238000010298 pulverizing process Methods 0.000 description 5
- 238000012827 research and development Methods 0.000 description 4
- 235000012054 meals Nutrition 0.000 description 3
- 235000016709 nutrition Nutrition 0.000 description 3
- 230000035764 nutrition Effects 0.000 description 3
- 239000000470 constituent Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 206010009944 Colon cancer Diseases 0.000 description 1
- 229920000832 Cutin Polymers 0.000 description 1
- 229920002488 Hemicellulose Polymers 0.000 description 1
- 206010020772 Hypertension Diseases 0.000 description 1
- 238000009098 adjuvant therapy Methods 0.000 description 1
- 101150039403 ams gene Proteins 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 208000029742 colonic neoplasm Diseases 0.000 description 1
- 238000012790 confirmation Methods 0.000 description 1
- 239000007799 cork Substances 0.000 description 1
- 208000029078 coronary artery disease Diseases 0.000 description 1
- 206010012601 diabetes mellitus Diseases 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 235000006694 eating habits Nutrition 0.000 description 1
- 230000002526 effect on cardiovascular system Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 229920001542 oligosaccharide Polymers 0.000 description 1
- 150000002482 oligosaccharides Chemical class 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
The invention discloses a peanut water-soluble dietary fiber enzymatic extracting method which comprises the steps of: pretreating the prepared peanut powder by acetone, alcohol, protease and alpha-amylase, and hydrolyzing by using cellulose for three times; and concentrating hydrolysis liquid and then precipitating by absolute ethyl alcohol, centrifuging and drying to obtain the water-soluble dietary fiber. The product prepared by the invention contains 30-60% of non-starch polysaccharide, can reduce the content of low density lipoprotein (LDL) cholesterol in the blood, promotes the growth and the propagation of probiotics group in the intestinal tract, and can be taken as functional food for preventing and alleviating symptom as well as treating diseases such as cardiovascular diseases and the like in an auxiliary way. The method is low in production cost, high in fiber content and suitable for industrialized production.
Description
Technical field
The present invention relates to a kind of peanut water-soluble dietary fiber enzymatic extracting method, belong to food processing field.
Background technology
Dietary fiber is meant in the food summation of plant cell, polysaccharide, lignin and other material that can not be digested and assimilated by the human body endogenous enzymes, and this definition comprises in the food a large amount of constituents such as cellulose, hemicellulose, lignin, colloid, modified cellulose, cement, oligosaccharides, pectin and other constituent such as wax, cutin, cork matter in a small amount.Though dietary fiber is not had a nutritive value, can treat and prevent many modern civilization diseases, the eubolism of human body is absolutely necessary.Therefore, dietary fiber has been subjected to the expert from different field, comprise physician, nutritionist, meals man, Food Science man, biochemist, and the relevant science decision person's of alimentary codex and nutrition education extensive attention, and classify it as after carbohydrate, protein, fat, water, minerals and vitamins " the seventh-largest nutrient ".Western developed country just sets about dietary fiber is carried out research and development as far back as twentieth century the seventies.And China's tradition meals can not lack dietary fiber based on plant food, thereby research and development utilizes not enough to dietary fiber.We can say that China still is in the starting stage to the research and development of dietary fiber at present, does not form the processing enterprise of scale.But along with improving constantly of people's living standard, great changes have taken place in eating habit, lack cellulosic situation in the meals and are on the rise, and rich man's diseases such as the disease of causeing fat, hypertension, coronary heart disease, diabetes, colon cancer are more and more general.Therefore, actively develop dietary fiber research and utilization and have extremely great realistic significance improving China people general level of the health.China's peanut annual production is big, and the byproduct of peanut industry is potential dietary fiber resource.The peanut dietary fiber has nutrition, health care and physiologic effect, can add in the numerous food, to improve nutrition, the health-care efficacy of food.Research and development peanut dietary fiber is extremely important to health, also has huge social benefit and economic benefit simultaneously.
In order to improve and to improve national diet structure, improve national physique holistic health level, and utilization rationally has the natural agriculture resource now to large extent, improve the food resource benefit, will develop dietary fiber food, and preparation technology provided by the present invention can process the peanut water-soluble dietary fiber product, can satisfy above-mentioned needs.
Summary of the invention
The purpose of this invention is to provide the extracting method that a kind of cost is low, the product dietary fiber content is high.
For achieving the above object, the present invention adopts following steps:
With the peanut powder that makes after acetone, ethanol, protease and AMS preliminary treatment, again through three hydrolysis of cellulase, hydrolyzate through concentrate, absolute ethyl alcohol precipitation, centrifugal, drying obtain water-soluble dietary fiber.
Specifically, described method is as follows:
(1) preparation of peanut powder;
(2) gained peanut powder is added acetone, water bath with thermostatic control oscillation treatment certain hour, suction filtration is abandoned filtrate, keeps filter residue 1, and filter residue 1 adds ethanol, water bath with thermostatic control oscillation treatment certain hour, suction filtration is abandoned filtrate, keeps filter residue 2;
(3) mixed enzyme solution of adding protease and AMS in the filter residue 2, water bath with thermostatic control oscillation treatment certain hour, suction filtration keeps filtrate 1, obtains filter residue 3.The washing of filter residue 3 usefulness distilled water, suction filtration keeps filtrate 2, obtains filter residue 4;
(4) filter residue 4 is divided into 2.5 parts, get a filter residue 4 and add cellulase solution, water bath with thermostatic control vibration enzymolysis certain hour, suction filtration, keep filtrate 3, obtain filter residue 5, add a filter residue 4 in the filter residue 5, add the cushioning liquid of identical pH value again with cellulase solution, water bath with thermostatic control oscillation treatment certain hour, suction filtration keeps filtrate 4, obtains filter residue 6;
(5) add moiety filter residue 4 in the filter residue 6, add the above-mentioned cellulase solution of a half strength again, water bath with thermostatic control vibration enzymolysis certain hour, suction filtration keeps filtrate 5;
(6) filtrate 1-filtrate 5 is merged together, and behind the enzyme 10min that goes out in boiling water bath, rotary evaporation in vacuo concentrates, obtain concentrate 1, add 4 times of volume absolute ethyl alcohols of concentrate 1 in the concentrate 1, standing over night, centrifugal, keep precipitation 1, obtain supernatant 1, supernatant 1 concentrates through rotary evaporation in vacuo, obtain concentrate 2, add 4 times of volume absolute ethyl alcohols of concentrate 2 in the concentrate 2, standing over night, centrifugal, keep precipitation 2;
(7) be dissolved in the boiling water after precipitation 1 and precipitation 2 merge, centrifugal, obtain supernatant 2, supernatant 2 concentrates through rotary evaporation in vacuo, obtains concentrate 3, adds 4 times of volume absolute ethyl alcohols of concentrate 3 in the concentrate 3, standing over night, centrifugal, obtain precipitating 3, precipitate 3 dryings, pulverize and to obtain the peanut water-soluble dietary fiber product.
Preferably, the described peanut powder, preparation method thereof of step (1) is that raw material is cleaned up with flowing water, 80 ℃ of dryings in air dry oven, and dried raw material is pulverized with the plant pulverizer, crushed material is crossed 50 mesh sieves, collects screenings as the peanut powder that extracts water-soluble dietary fiber;
Described raw material does not go rotten for having, peanut shell, peanut bar and the peanut root of free from insect pests; Described peanut powder is the powder behind peanut shell, peanut bar and the peanut root crushing screening.
Preferably, the described acetone addition of step (2) is 3~5 times (peanut opaque amount and acetone volume ratios) of peanut powder, and the temperature of handling the peanut powder is 30~50 ℃, and the processing time is 30~90min;
Preferably, described amount of alcohol added is 3~5 times (peanut opaque amount and ethanol volume ratios) of peanut powder.
Preferably, the described protease of step (3) is any or several in papain, neutral proteinase and the alkali protease;
Preferably, the quality percentage composition of protease is 0.2%~1.0% in the described mixed enzyme solution, and the quality percentage composition of AMS is 0.2%~1.0%, the pH value 6.0~8.0 of mixed enzyme solution, the mixed enzyme solution processing time is 1.0~3.0h, and treatment temperature is 40~60 ℃.
Preferably, the concentration of the described cellulase solution of step (4) is 0.05~2.0mg/ml, and the pH value is 4.0~6.0, and treatment temperature is 35~60 ℃, and the processing time is 0.5~8.0h.
Preferably, the water bath with thermostatic control oscillation treatment certain hour described in step (2), (3) and (4) is meant that the temperature of handling the peanut powder is 40~60 ℃, and the processing time is 20~60min.
Preferably, the drying means of described precipitation 3 is any in freeze drying and the vacuum drying.
Suction filtration described in the said method is to adopt suction filtration method well known in the art to operate.
The water-soluble dietary fiber product is a kind of khaki powder, wherein contains non-starchiness polysaccharide 30%~60%, swelling in 100 ℃ of water of pH6.0~7.0, and the dissolving back is a brown yellow solution, has a small amount of insoluble matter to exist.The water-soluble dietary fiber product can reduce low-density lipoprotein in the blood (LDL) content of cholesterol, promotes beneficial flora growth and breeding in the enteron aisle, can be used as the functional food of diseases such as prevention, mitigation symptoms, adjuvant therapy of cardiovascular.Method production cost of the present invention is low, fiber content is high owing to adopt, and is fit to suitability for industrialized production.
The specific embodiment
Present embodiment is to be used for understanding, rather than restriction the present invention.The inventor is tested confirmation, and step that method of the present invention adopted and parameter all can realize purpose of the present invention.
Embodiment 1
Get do not have to go rotten, peanut shell, peanut bar and the peanut root of free from insect pests clean up with flowing water, 80 ℃ of dryings in air dry oven, dried raw material is pulverized with the plant pulverizer, and crushed material is crossed 50 mesh sieves, collects screenings as the peanut powder that extracts water-soluble dietary fiber; The peanut powder adds 3 times of (peanut opaque amount and acetone volume ratio) acetone, 30 ℃ of water bath with thermostatic control oscillation treatment 30min, suction filtration, abandon filtrate, keep filter residue 1, filter residue 1 adds 3 times of (peanut opaque amount and ethanol volume ratio) ethanol, 30 ℃ of water bath with thermostatic control oscillation treatment 30min, suction filtration is abandoned filtrate, keeps filter residue 2; The mixed enzyme solution that adds papain and AMS in the filter residue 2, the quality percentage composition of protease is 0.2% in the mixed enzyme solution, and the quality percentage composition of AMS is 0.2%, the pH value 6.0 of mixed enzyme solution, 40 ℃ of water bath with thermostatic control oscillation treatment of mixed enzyme solution 1.0h, suction filtration keeps filtrate 1, obtains filter residue 3, filter residue 3 usefulness distilled water wash, suction filtration keeps filtrate 2, obtains filter residue 4; Filter residue 4 is divided into 2.5 parts, getting a filter residue 4 adding concentration is 0.05mg/ml, the pH value is 4.0 cellulase solution,, 35 ℃ of water bath with thermostatic control oscillation treatment 0.5h, suction filtration, keep filtrate 3, obtain filter residue 5, add a filter residue 4 in the filter residue 5, the cushioning liquid that adds identical pH value again with cellulase solution, 35 ℃ of water bath with thermostatic control oscillation treatment 0.5h, suction filtration keeps filtrate 4, obtain filter residue 6, add moiety filter residue 4 in the filter residue 6, add the cellulase solution of a half strength again, temperature is 35 ℃ of water bath with thermostatic control oscillation treatment 0.5h, suction filtration keeps filtrate 5; Filtrate 1-filtrate 5 is merged together, and behind the enzyme 10min that goes out in boiling water bath, rotary evaporation in vacuo concentrates, obtain concentrate 1, add 4 times of volume absolute ethyl alcohols of concentrate 1 in the concentrate 1, standing over night, centrifugal, keep precipitation 1, obtain supernatant 1, supernatant 1 concentrates through rotary evaporation in vacuo, obtain concentrate 2, add 4 times of volume absolute ethyl alcohols of concentrate 2 in the concentrate 2, standing over night, centrifugal, keep precipitation 2; After merging, precipitation 1 and precipitation 2 be dissolved in the boiling water, centrifugal, obtain supernatant 2, supernatant 2 concentrates through rotary evaporation in vacuo, obtains concentrate 3, adds 4 times of volume absolute ethyl alcohols of concentrate 3 in the concentrate 3, standing over night, centrifugal, obtain precipitating 3, precipitation 3 obtains the peanut water-soluble dietary fiber product through freeze drying, pulverizing.
Embodiment 2
Get do not have to go rotten, peanut shell, peanut bar and the peanut root of free from insect pests clean up with flowing water, 80 ℃ of dryings in air dry oven, dried raw material is pulverized with the plant pulverizer, and crushed material is crossed 50 mesh sieves, collects screenings as the peanut powder that extracts water-soluble dietary fiber; The peanut powder adds 5 times of (peanut opaque amount and acetone volume ratio) acetone, 50 ℃ of water bath with thermostatic control oscillation treatment 90min, suction filtration, abandon filtrate, keep filter residue 1, filter residue 1 adds 5 times of (peanut opaque amount and ethanol volume ratio) ethanol, 50 ℃ of water bath with thermostatic control oscillation treatment 90min, suction filtration is abandoned filtrate, keeps filter residue 2; The mixed enzyme solution that adds alkali protease and AMS in the filter residue 2, the quality percentage composition of protease is 1.0% in the mixed enzyme solution, and the quality percentage composition of AMS is 1.0%, the pH value 8.0 of mixed enzyme solution, 60 ℃ of water bath with thermostatic control oscillation treatment of mixed enzyme solution 3.0h, suction filtration keeps filtrate 1, obtains filter residue 3, filter residue 3 usefulness distilled water wash, suction filtration keeps filtrate 2, obtains filter residue 4; Filter residue 4 is divided into 2.5 parts, getting a filter residue 4 adding concentration is 2.0mg/ml, the pH value is 6.0 cellulase solution, 60 ℃ of water bath with thermostatic control oscillation treatment 8.0h, suction filtration keeps filtrate 3, obtain filter residue 5, add a filter residue 4 in the filter residue 5, add the cushioning liquid of identical pH value again, 60 ℃ of water bath with thermostatic control oscillation treatment 8.0h with cellulase solution, suction filtration, keep filtrate 4, obtain filter residue 6, add moiety filter residue 4 in the filter residue 6, the cellulase solution that adds a half strength again, temperature is 60 ℃ of water bath with thermostatic control oscillation treatment 8.0h, and suction filtration keeps filtrate 5; Filtrate 1-filtrate 5 is merged together, and behind the enzyme 10min that goes out in boiling water bath, rotary evaporation in vacuo concentrates, obtain concentrate 1, add 4 times of volume absolute ethyl alcohols of concentrate 1 in the concentrate 1, standing over night, centrifugal, keep precipitation 1, obtain supernatant 1, supernatant 1 concentrates through rotary evaporation in vacuo, obtain concentrate 2, add 4 times of volume absolute ethyl alcohols of concentrate 2 in the concentrate 2, standing over night, centrifugal, keep precipitation 2; After merging, precipitation 1 and precipitation 2 be dissolved in the boiling water, centrifugal, obtain supernatant 2, supernatant 2 concentrates through rotary evaporation in vacuo, obtains concentrate 3, adds 4 times of volume absolute ethyl alcohols of concentrate 3 in the concentrate 3, standing over night, centrifugal, obtain precipitating 3, precipitation 3 obtains the peanut water-soluble dietary fiber product through vacuum drying, pulverizing.
Embodiment 3
Get do not have to go rotten, peanut shell, peanut bar and the peanut root of free from insect pests clean up with flowing water, 80 ℃ of dryings in air dry oven, dried raw material is pulverized with the plant pulverizer, and crushed material is crossed 50 mesh sieves, collects screenings as the peanut powder that extracts water-soluble dietary fiber; The peanut powder adds 4 times of (peanut opaque amount and acetone volume ratio) acetone, 40 ℃ of water bath with thermostatic control oscillation treatment 60min, suction filtration, abandon filtrate, keep filter residue 1, filter residue 1 adds 4 times of (peanut opaque amount and ethanol volume ratio) ethanol, 40 ℃ of water bath with thermostatic control oscillation treatment 60min, suction filtration is abandoned filtrate, keeps filter residue 2; The mixed enzyme solution that adds protease neutral proteinase and AMS in the filter residue 2, the quality percentage composition of protease is 0.6% in the mixed enzyme solution, and the quality percentage composition of AMS is 0.6%, the pH value 7.0 of mixed enzyme solution, 50 ℃ of water bath with thermostatic control oscillation treatment of mixed enzyme solution 2.0h, suction filtration keeps filtrate 1, obtains filter residue 3, filter residue 3 usefulness distilled water wash, suction filtration keeps filtrate 2, obtains filter residue 4; Filter residue 4 is divided into 2.5 parts, getting a filter residue 4 adding concentration is 0.95mg/ml, the pH value is 5.0 cellulase solution,, 48 ℃ of water bath with thermostatic control oscillation treatment 4.0h, suction filtration, keep filtrate 3, obtain filter residue 5, add a filter residue 4 in the filter residue 5, the cushioning liquid that adds identical pH value again with cellulase solution, 48 ℃ of water bath with thermostatic control oscillation treatment 4.0h, suction filtration keeps filtrate 4, obtain filter residue 6, add moiety filter residue 4 in the filter residue 6, add the cellulase solution of a half strength again, temperature is 48 ℃ of water bath with thermostatic control oscillation treatment 4.0h, suction filtration keeps filtrate 5; Filtrate 1-filtrate 5 is merged together, and behind the enzyme 10min that goes out in boiling water bath, rotary evaporation in vacuo concentrates, obtain concentrate 1, add 4 times of volume absolute ethyl alcohols of concentrate 1 in the concentrate 1, standing over night, centrifugal, keep precipitation 1, obtain supernatant 1, supernatant 1 concentrates through rotary evaporation in vacuo, obtain concentrate 2, add 4 times of volume absolute ethyl alcohols of concentrate 2 in the concentrate 2, standing over night, centrifugal, keep precipitation 2; After merging, precipitation 1 and precipitation 2 be dissolved in the boiling water, centrifugal, obtain supernatant 2, supernatant 2 concentrates through rotary evaporation in vacuo, obtains concentrate 3, adds 4 times of volume absolute ethyl alcohols of concentrate 3 in the concentrate 3, standing over night, centrifugal, obtain precipitating 3, precipitate 3 drying freeze dryings, pulverize and to obtain the peanut water-soluble dietary fiber product.
Embodiment 4
Get do not have to go rotten, peanut shell, peanut bar and the peanut root of free from insect pests clean up with flowing water, 80 ℃ of dryings in air dry oven, dried raw material is pulverized with the plant pulverizer, and crushed material is crossed 50 mesh sieves, collects screenings as the peanut powder that extracts water-soluble dietary fiber; The peanut powder adds 3.5 times of (peanut opaque amount and acetone volume ratio) acetone, 35 ℃ of water bath with thermostatic control oscillation treatment 45min, suction filtration, abandon filtrate, keep filter residue 1, filter residue 1 adds 3.5 times of (peanut opaque amount and ethanol volume ratio) ethanol, 35 ℃ of water bath with thermostatic control oscillation treatment 45min, suction filtration is abandoned filtrate, keeps filter residue 2; The mixed enzyme solution that adds papain, neutral proteinase and AMS in the filter residue 2, the quality percentage composition of protease is 0.4% in the mixed enzyme solution, and the quality percentage composition of AMS is 0.4%, the pH value 6.5 of mixed enzyme solution, 45 ℃ of water bath with thermostatic control oscillation treatment of mixed enzyme solution 1.5h, suction filtration keeps filtrate 1, obtains filter residue 3, filter residue 3 usefulness distilled water wash, suction filtration keeps filtrate 2, obtains filter residue 4; Filter residue 4 is divided into 2.5 parts, getting a filter residue 4 adding concentration is 0.6mg/ml, the pH value is 4.5 cellulase solution, 40 ℃ of water bath with thermostatic control oscillation treatment 2.0h, suction filtration keeps filtrate 3, obtain filter residue 5, add a filter residue 4 in the filter residue 5, add the cushioning liquid of identical pH value again, 40 ℃ of water bath with thermostatic control oscillation treatment 2.0h with cellulase solution, suction filtration, keep filtrate 4, obtain filter residue 6, add moiety filter residue 4 in the filter residue 6, the cellulase solution that adds a half strength again, temperature is 40 ℃ of water bath with thermostatic control oscillation treatment 2.0h, and suction filtration keeps filtrate 5; Filtrate 1-filtrate 5 is merged together, and behind the enzyme 10min that goes out in boiling water bath, rotary evaporation in vacuo concentrates, obtain concentrate 1, add 4 times of volume absolute ethyl alcohols of concentrate 1 in the concentrate 1, standing over night, centrifugal, keep precipitation 1, obtain supernatant 1, supernatant 1 concentrates through rotary evaporation in vacuo, obtain concentrate 2, add 4 times of volume absolute ethyl alcohols of concentrate 2 in the concentrate 2, standing over night, centrifugal, keep precipitation 2; After merging, precipitation 1 and precipitation 2 be dissolved in the boiling water, centrifugal, obtain supernatant 2, supernatant 2 concentrates through rotary evaporation in vacuo, obtains concentrate 3, adds 4 times of volume absolute ethyl alcohols of concentrate 3 in the concentrate 3, standing over night, centrifugal, obtain precipitating 3, precipitation 3 obtains the peanut water-soluble dietary fiber product through vacuum drying, pulverizing.
Embodiment 5
Getting raw material (not having peanut shell, peanut bar and peanut root mildew and rot, free from insect pests) cleans up with flowing water, 80 ℃ of dryings in air dry oven, dried raw material is pulverized with the plant pulverizer, and crushed material is crossed 50 mesh sieves, collects screenings as the peanut powder that extracts water-soluble dietary fiber; The peanut powder adds 4.5 times of (peanut opaque amount and acetone volume ratio) acetone, 45 ℃ of water bath with thermostatic control oscillation treatment 75min, suction filtration, abandon filtrate, keep filter residue 1, filter residue 1 adds 4.5 times of (peanut opaque amount and ethanol volume ratio) ethanol, 45 ℃ of water bath with thermostatic control oscillation treatment 75min, suction filtration is abandoned filtrate, keeps filter residue 2; The mixed enzyme solution that adds protease neutral proteinase, alkali protease and AMS in the filter residue 2, the quality percentage composition of protease is 0.8% in the mixed enzyme solution, and the quality percentage composition of AMS is 0.8%, the pH value 7.5 of mixed enzyme solution, 55 ℃ of water bath with thermostatic control oscillation treatment of mixed enzyme solution 2.5h, suction filtration keeps filtrate 1, obtains filter residue 3, filter residue 3 usefulness distilled water wash, suction filtration keeps filtrate 2, obtains filter residue 4; Filter residue 4 is divided into 2.5 parts, getting a filter residue 4 adding concentration is 1.5mg/ml, the pH value is 5.5 cellulase solution, 55 ℃ of water bath with thermostatic control oscillation treatment 6.0h, suction filtration keeps filtrate 3, obtain filter residue 5, add a filter residue 4 in the filter residue 5, add the cushioning liquid of identical pH value again, 55 ℃ of water bath with thermostatic control oscillation treatment 6.0h with cellulase solution, suction filtration, keep filtrate 4, obtain filter residue 6, add moiety filter residue 4 in the filter residue 6, the cellulase solution that adds a half strength again, temperature is 55 ℃ of water bath with thermostatic control oscillation treatment 6.0h, and suction filtration keeps filtrate 5; Filtrate 1-filtrate 5 is merged together, and behind the enzyme 10min that goes out in boiling water bath, rotary evaporation in vacuo concentrates, obtain concentrate 1, add 4 times of volume absolute ethyl alcohols of concentrate 1 in the concentrate 1, standing over night, centrifugal, keep precipitation 1, obtain supernatant 1, supernatant 1 concentrates through rotary evaporation in vacuo, obtain concentrate 2, add 4 times of volume absolute ethyl alcohols of concentrate 2 in the concentrate 2, standing over night, centrifugal, keep precipitation 2; After merging, precipitation 1 and precipitation 2 be dissolved in the boiling water, centrifugal, obtain supernatant 2, supernatant 2 concentrates through rotary evaporation in vacuo, obtains concentrate 3, adds 4 times of volume absolute ethyl alcohols of concentrate 3 in the concentrate 3, standing over night, centrifugal, obtain precipitating 3, precipitation 3 obtains the peanut water-soluble dietary fiber product through vacuum drying, pulverizing.
Embodiment 6
Getting raw material (not having peanut shell, peanut bar and peanut root mildew and rot, free from insect pests) cleans up with flowing water, 80 ℃ of dryings in air dry oven, dried raw material is pulverized with the plant pulverizer, and crushed material is crossed 50 mesh sieves, collects screenings as the peanut powder that extracts water-soluble dietary fiber; The peanut powder adds 3 times of (peanut opaque amount and acetone volume ratio) acetone, 50 ℃ of water bath with thermostatic control oscillation treatment 90min, suction filtration, abandon filtrate, keep filter residue 1, filter residue 1 adds 5 times of (peanut opaque amount and ethanol volume ratio) ethanol, 30 ℃ of water bath with thermostatic control oscillation treatment 30min, suction filtration is abandoned filtrate, keeps filter residue 2; Add protease papain, neutral proteinase and alkali protease in the filter residue 2, and the mixed enzyme solution of AMS, the quality percentage composition of protease is 0.9% in the mixed enzyme solution, the quality percentage composition of AMS is 0.3%, the pH value 6.2 of mixed enzyme solution, 42 ℃ of water bath with thermostatic control oscillation treatment of mixed enzyme solution 1.8h, suction filtration, keep filtrate 1, obtain filter residue 3, the washing of filter residue 3 usefulness distilled water, suction filtration, keep filtrate 2, obtain filter residue 4; Filter residue 4 is divided into 2.5 parts, getting a filter residue 4 adding concentration is 1.8mg/ml, the pH value is 4.5 cellulase solution, 58 ℃ of water bath with thermostatic control oscillation treatment 1.0h, suction filtration keeps filtrate 3, obtain filter residue 5, add a filter residue 4 in the filter residue 5, add the cushioning liquid of identical pH value again, 37 ℃ of water bath with thermostatic control oscillation treatment 7.0h with cellulase solution, suction filtration, keep filtrate 4, obtain filter residue 6, add moiety filter residue 4 in the filter residue 6, the cellulase solution that adds a half strength again, temperature is 50 ℃ of water bath with thermostatic control oscillation treatment 3.0h, and suction filtration keeps filtrate 5; Filtrate 1-filtrate 5 is merged together, and behind the enzyme 10min that goes out in boiling water bath, rotary evaporation in vacuo concentrates, obtain concentrate 1, add 4 times of volume absolute ethyl alcohols of concentrate 1 in the concentrate 1, standing over night, centrifugal, keep precipitation 1, obtain supernatant 1, supernatant 1 concentrates through rotary evaporation in vacuo, obtain concentrate 2, add 4 times of volume absolute ethyl alcohols of concentrate 2 in the concentrate 2, standing over night, centrifugal, keep precipitation 2; After merging, precipitation 1 and precipitation 2 be dissolved in the boiling water, centrifugal, obtain supernatant 2, supernatant 2 concentrates through rotary evaporation in vacuo, obtains concentrate 3, adds 4 times of volume absolute ethyl alcohols of concentrate 3 in the concentrate 3, standing over night, centrifugal, obtain precipitating 3, precipitation 3 obtains the peanut water-soluble dietary fiber product through vacuum drying, pulverizing.
Claims (10)
1, a kind of peanut water-soluble dietary fiber enzymatic extracting method may further comprise the steps:
With the peanut powder that makes after acetone, ethanol, protease and AMS preliminary treatment, again through three hydrolysis of cellulase, hydrolyzate through concentrate, absolute ethyl alcohol precipitation, centrifugal, drying obtain water-soluble dietary fiber.
2, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1 is characterized in that, may further comprise the steps:
(1) preparation of peanut powder;
(2) gained peanut powder is added acetone, water bath with thermostatic control oscillation treatment certain hour, suction filtration is abandoned filtrate, keeps filter residue 1, and filter residue 1 adds ethanol, water bath with thermostatic control oscillation treatment certain hour, suction filtration is abandoned filtrate, keeps filter residue 2;
(3) mixed enzyme solution of adding protease and AMS in the filter residue 2, water bath with thermostatic control oscillation treatment certain hour, suction filtration keeps filtrate 1, obtains filter residue 3, the washing of filter residue 3 usefulness distilled water, suction filtration keeps filtrate 2, obtains filter residue 4;
(4) filter residue 4 is divided into 2.5 parts, get a filter residue 4 and add cellulase solution, water bath with thermostatic control vibration enzymolysis certain hour, suction filtration, keep filtrate 3, obtain filter residue 5, add a filter residue 4 in the filter residue 5, add the cushioning liquid of identical pH value again with cellulase solution, water bath with thermostatic control oscillation treatment certain hour, suction filtration keeps filtrate 4, obtains filter residue 6;
(5) add moiety filter residue 4 in the filter residue 6, add the above-mentioned cellulase solution of a half strength again, water bath with thermostatic control vibration enzymolysis certain hour, suction filtration keeps filtrate 5;
(6) filtrate 1-filtrate 5 is merged together, and behind the enzyme 10min that goes out in boiling water bath, rotary evaporation in vacuo concentrates, obtain concentrate 1, add 4 times of absolute ethyl alcohols, standing over night in the concentrate 1, centrifugal, keep precipitation 1, obtain supernatant 1, supernatant 1 concentrates through rotary evaporation in vacuo, obtain concentrate 2, add 4 times of absolute ethyl alcohols, standing over night in the concentrate 2, centrifugal, keep precipitation 2;
(7) be dissolved in the boiling water after precipitation 1 and precipitation 2 merge, centrifugal, obtain supernatant 2, supernatant 2 concentrates through rotary evaporation in vacuo, obtains concentrate 3, adds 4 times of absolute ethyl alcohols in the concentrate 3, standing over night, centrifugal, obtain precipitating 3, precipitate 3 dryings, pulverize and to obtain the peanut water-soluble dietary fiber product.
3, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1, it is characterized in that, the described peanut powder, preparation method thereof of step (1) is that raw material is cleaned up with flowing water, 80 ℃ of dryings in air dry oven, dried raw material is pulverized with the plant pulverizer, crushed material is crossed 50 mesh sieves, collects screenings as the peanut powder that extracts water-soluble dietary fiber.
4, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1 is characterized in that, the described acetone addition of step (2) is long-pending 3~5 times of peanut powder, and the temperature of handling the peanut powder is 30~50 ℃, and the processing time is 30~90min.
5, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1 is characterized in that, the described amount of alcohol added of step (2) is long-pending 3~5 times of peanut powder.
6, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1 is characterized in that, the described protease of step (3) is any or several in papain, neutral proteinase and the alkali protease.
7, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1, it is characterized in that, the quality percentage composition of protease is 0.2%~1.0% in the described mixed enzyme solution, the quality percentage composition of AMS is 0.2%~1.0%, the pH value 6.0~8.0 of mixed enzyme solution, the mixed enzyme solution processing time is 1.0~3.0h, and treatment temperature is 40~60 ℃.
8, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1, it is characterized in that the concentration of the described cellulase solution of step (4) is 0.05~2.0mg/ml, the pH value is 4.0~6.0, treatment temperature is 35~60 ℃, and the processing time is 0.5~8.0h.
9, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1, it is characterized in that, water bath with thermostatic control oscillation treatment certain hour described in step (2), (3) and (4) is meant that the temperature of handling the peanut powder is 40~60 ℃, and the processing time is 20~60min.
10, peanut water-soluble dietary fiber enzymatic extracting method according to claim 1 is characterized in that, the drying means of described precipitation 3 is freeze drying or vacuum drying.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009101784142A CN101664167B (en) | 2009-09-24 | 2009-09-24 | Peanut water-soluble dietary fiber enzymatic extracting method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2009101784142A CN101664167B (en) | 2009-09-24 | 2009-09-24 | Peanut water-soluble dietary fiber enzymatic extracting method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN101664167A true CN101664167A (en) | 2010-03-10 |
CN101664167B CN101664167B (en) | 2012-08-22 |
Family
ID=41801072
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2009101784142A Expired - Fee Related CN101664167B (en) | 2009-09-24 | 2009-09-24 | Peanut water-soluble dietary fiber enzymatic extracting method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101664167B (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101990965A (en) * | 2010-09-26 | 2011-03-30 | 华侨大学 | Method for preparing dietary fiber micropowder by tea stem and tea dust enzyme method |
CN102187984A (en) * | 2011-06-27 | 2011-09-21 | 成都大学 | Preparation method for soluble dietary fiber with apple pomace as raw material |
CN102224907A (en) * | 2011-05-25 | 2011-10-26 | 东北农业大学 | Method for extracting dietary fiber from pods |
CN103361395A (en) * | 2013-08-07 | 2013-10-23 | 山东省花生研究所 | Solid-state fermentation preparation method for peanut non-starch polysaccharides |
CN105533760A (en) * | 2015-12-09 | 2016-05-04 | 重庆三零三科技有限公司 | Preparation of mulberry pomace water-soluble dietary fiber |
CN104757564B (en) * | 2015-04-30 | 2016-08-17 | 马健 | A kind of method utilizing Pericarppium arachidis hypogaeae to prepare dietary fiber |
CN106072171A (en) * | 2016-06-28 | 2016-11-09 | 河南天纤益康科技有限公司 | A kind of preparation method of RHIIZOMA DIOSCOREAE fr0m Henan of China dietary fiber |
CN106723090A (en) * | 2016-11-28 | 2017-05-31 | 胜利 | A kind of preparation method of Dietary Fiber from Wheat Straw |
CN106993810A (en) * | 2017-04-25 | 2017-08-01 | 中国科学院过程工程研究所 | A kind of Chinese yam soluble dietary fiber and preparation method thereof |
CN107616508A (en) * | 2017-09-30 | 2018-01-23 | 江苏农林职业技术学院 | A kind of preparation method of leaf of bamboo soluble dietary fiber |
CN108159070A (en) * | 2018-03-14 | 2018-06-15 | 广东省微生物研究所(广东省微生物分析检测中心) | Purposes of the ovum spore Aode mushroom dietary fiber extract in treatment and/or prevention intestinal bacilli illness relevant disease preparation is prepared |
CN108719958A (en) * | 2018-05-30 | 2018-11-02 | 北京林业大学 | A kind of rose slag modified dietary fiber plural gel |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1483349A (en) * | 2002-09-22 | 2004-03-24 | 于铁梁 | Method for preparing soluble dietary fibre |
CN1179658C (en) * | 2002-10-18 | 2004-12-15 | 湘潭工学院 | Enzymatic Extraction Technology of Peanut Protein and Oil |
CN101401658B (en) * | 2008-07-18 | 2012-05-23 | 江南大学 | A Pilot Test Method for Extracting Oil and Hydrolyzed Protein from Peanuts by Aqueous Enzyme |
-
2009
- 2009-09-24 CN CN2009101784142A patent/CN101664167B/en not_active Expired - Fee Related
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101990965A (en) * | 2010-09-26 | 2011-03-30 | 华侨大学 | Method for preparing dietary fiber micropowder by tea stem and tea dust enzyme method |
CN102224907A (en) * | 2011-05-25 | 2011-10-26 | 东北农业大学 | Method for extracting dietary fiber from pods |
CN102224907B (en) * | 2011-05-25 | 2012-09-26 | 东北农业大学 | Method for extracting dietary fibers from bean pods |
CN102187984A (en) * | 2011-06-27 | 2011-09-21 | 成都大学 | Preparation method for soluble dietary fiber with apple pomace as raw material |
CN102187984B (en) * | 2011-06-27 | 2013-01-30 | 成都大学 | A method for preparing soluble dietary fiber from apple pomace |
CN103361395A (en) * | 2013-08-07 | 2013-10-23 | 山东省花生研究所 | Solid-state fermentation preparation method for peanut non-starch polysaccharides |
CN103361395B (en) * | 2013-08-07 | 2015-10-14 | 山东省花生研究所 | A kind of solid state fermentation prepares the method for peanut non-starch polysaccharide |
CN104757564B (en) * | 2015-04-30 | 2016-08-17 | 马健 | A kind of method utilizing Pericarppium arachidis hypogaeae to prepare dietary fiber |
CN105533760A (en) * | 2015-12-09 | 2016-05-04 | 重庆三零三科技有限公司 | Preparation of mulberry pomace water-soluble dietary fiber |
CN106072171A (en) * | 2016-06-28 | 2016-11-09 | 河南天纤益康科技有限公司 | A kind of preparation method of RHIIZOMA DIOSCOREAE fr0m Henan of China dietary fiber |
CN106723090A (en) * | 2016-11-28 | 2017-05-31 | 胜利 | A kind of preparation method of Dietary Fiber from Wheat Straw |
CN106993810A (en) * | 2017-04-25 | 2017-08-01 | 中国科学院过程工程研究所 | A kind of Chinese yam soluble dietary fiber and preparation method thereof |
CN107616508A (en) * | 2017-09-30 | 2018-01-23 | 江苏农林职业技术学院 | A kind of preparation method of leaf of bamboo soluble dietary fiber |
CN107616508B (en) * | 2017-09-30 | 2020-11-03 | 江苏农林职业技术学院 | Preparation method of soluble dietary fiber of bamboo leaves |
CN108159070A (en) * | 2018-03-14 | 2018-06-15 | 广东省微生物研究所(广东省微生物分析检测中心) | Purposes of the ovum spore Aode mushroom dietary fiber extract in treatment and/or prevention intestinal bacilli illness relevant disease preparation is prepared |
CN108719958A (en) * | 2018-05-30 | 2018-11-02 | 北京林业大学 | A kind of rose slag modified dietary fiber plural gel |
CN108719958B (en) * | 2018-05-30 | 2022-03-04 | 北京林业大学 | Rose flower residue modified dietary fiber composite gel |
Also Published As
Publication number | Publication date |
---|---|
CN101664167B (en) | 2012-08-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101664167B (en) | Peanut water-soluble dietary fiber enzymatic extracting method | |
CN103719880B (en) | Preparation method of high-activity purple sweet potato dietary fiber | |
CN104256584B (en) | A kind of Moringa ferment and preparation method thereof | |
CN102524698B (en) | Method for preparing pumpkin dietary fiber | |
CN103815415A (en) | High-quality functional alga dietary fiber | |
CN102121036A (en) | Method for preparing peanut dietary fibers by using microbial fermentation method | |
CN101946891A (en) | Method for preparing water-soluble dietary fiber of corn peels | |
CN106343410A (en) | Production method of kelp extract | |
CN103265614A (en) | Method for extracting soy protein, oligosaccharide and isoflavone from soybean wastewater by one-step process | |
CN114847494B (en) | Method for extracting dietary fibers from reed shoots | |
CN104719753A (en) | Making method of soluble cereal dietary fibers | |
CN105124134B (en) | Method of preparing feed dietary fibers | |
CN109957040A (en) | Method for extracting Tremella polysaccharide by enzyme-assisted wet beating | |
CN101569387B (en) | Method for producing water chestnut sheet jelly | |
CN101028101A (en) | Production of sweet potato prandial fibre containing sweet-potato resistance starch | |
CN105533760A (en) | Preparation of mulberry pomace water-soluble dietary fiber | |
CN106993810A (en) | A kind of Chinese yam soluble dietary fiber and preparation method thereof | |
CN107114801B (en) | High-content oat dietary fiber preparation and preparation method thereof | |
CN105831775A (en) | Method for improving soluble meal fiber content of lotus rhizome slag | |
CN105031289A (en) | Dendrobium officinale and lucid ganoderma capsules and preparation method thereof | |
CN118633750A (en) | Composite dietary fiber with the function of improving intestinal health and preparation method thereof | |
CN111700279B (en) | Preparation method of wheat bran dietary fiber | |
CN111743065A (en) | Asparagus beverage and preparation method thereof | |
CN106805242A (en) | A kind of selenium-enriched cordceps militaris piece and preparation method thereof | |
CN107258915B (en) | Cordyceps militaris, corn and peanut compound beverage |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C17 | Cessation of patent right | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120822 Termination date: 20130924 |