CN106539097A - The water-soluble method with Water insoluble dietary fiber is produced simultaneously using bagasse - Google Patents
The water-soluble method with Water insoluble dietary fiber is produced simultaneously using bagasse Download PDFInfo
- Publication number
- CN106539097A CN106539097A CN201610852063.9A CN201610852063A CN106539097A CN 106539097 A CN106539097 A CN 106539097A CN 201610852063 A CN201610852063 A CN 201610852063A CN 106539097 A CN106539097 A CN 106539097A
- Authority
- CN
- China
- Prior art keywords
- water
- bagasse
- dietary fiber
- filter residue
- insoluble 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.)
- Pending
Links
- 235000013325 dietary fiber Nutrition 0.000 title claims abstract description 45
- 241000609240 Ambelania acida Species 0.000 title claims abstract description 44
- 239000010905 bagasse Substances 0.000 title claims abstract description 44
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 44
- 238000000034 method Methods 0.000 title claims abstract description 21
- 102000004190 Enzymes Human genes 0.000 claims abstract description 24
- 108090000790 Enzymes Proteins 0.000 claims abstract description 22
- 239000011261 inert gas Substances 0.000 claims abstract description 18
- 239000000706 filtrate Substances 0.000 claims description 33
- 230000000694 effects Effects 0.000 claims description 27
- 239000007787 solid Substances 0.000 claims description 25
- 108091005804 Peptidases Proteins 0.000 claims description 22
- 239000004365 Protease Substances 0.000 claims description 22
- 239000007788 liquid Substances 0.000 claims description 22
- 235000019419 proteases Nutrition 0.000 claims description 22
- 229940088598 enzyme Drugs 0.000 claims description 21
- 239000003513 alkali Substances 0.000 claims description 20
- 238000000926 separation method Methods 0.000 claims description 20
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- 241000194108 Bacillus licheniformis Species 0.000 claims description 17
- 150000001875 compounds Chemical class 0.000 claims description 16
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 13
- 230000002255 enzymatic effect Effects 0.000 claims description 12
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 11
- 239000002253 acid Substances 0.000 claims description 10
- 102000004139 alpha-Amylases Human genes 0.000 claims description 10
- 108090000637 alpha-Amylases Proteins 0.000 claims description 10
- 229940024171 alpha-amylase Drugs 0.000 claims description 10
- 108090000765 processed proteins & peptides Proteins 0.000 claims description 10
- 108010067770 Endopeptidase K Proteins 0.000 claims description 8
- 108010059378 Endopeptidases Proteins 0.000 claims description 8
- 102000005593 Endopeptidases Human genes 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 8
- 235000015097 nutrients Nutrition 0.000 claims description 8
- 239000002002 slurry Substances 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 8
- 238000010792 warming Methods 0.000 claims description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 claims description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 6
- 241000894006 Bacteria Species 0.000 claims description 5
- 241000196324 Embryophyta Species 0.000 claims description 5
- 238000007605 air drying Methods 0.000 claims description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 4
- 230000003321 amplification Effects 0.000 claims description 4
- 230000008030 elimination Effects 0.000 claims description 4
- 238000003379 elimination reaction Methods 0.000 claims description 4
- 239000012535 impurity Substances 0.000 claims description 4
- 230000000937 inactivator Effects 0.000 claims description 4
- 238000009413 insulation Methods 0.000 claims description 4
- 238000003199 nucleic acid amplification method Methods 0.000 claims description 4
- 238000001556 precipitation Methods 0.000 claims description 4
- 230000028327 secretion Effects 0.000 claims description 4
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 3
- 239000006210 lotion Substances 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 229910052786 argon Inorganic materials 0.000 claims description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 2
- 239000000920 calcium hydroxide Substances 0.000 claims description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 2
- 238000004108 freeze drying Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 claims description 2
- 238000000227 grinding Methods 0.000 claims description 2
- 239000001307 helium Substances 0.000 claims description 2
- 229910052734 helium Inorganic materials 0.000 claims description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 2
- 230000006698 induction Effects 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 238000001694 spray drying Methods 0.000 claims description 2
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 claims 6
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims 1
- 238000001816 cooling Methods 0.000 claims 1
- 229910017604 nitric acid Inorganic materials 0.000 claims 1
- 238000009835 boiling Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000004880 explosion Methods 0.000 abstract description 2
- 238000002955 isolation Methods 0.000 abstract description 2
- 102000035195 Peptidases Human genes 0.000 description 16
- 229920002472 Starch Polymers 0.000 description 7
- 239000000463 material Substances 0.000 description 7
- 239000008107 starch Substances 0.000 description 7
- 235000019698 starch Nutrition 0.000 description 7
- 102000004169 proteins and genes Human genes 0.000 description 6
- 108090000623 proteins and genes Proteins 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 5
- 230000003301 hydrolyzing effect Effects 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 229920002488 Hemicellulose Polymers 0.000 description 4
- 239000001913 cellulose Substances 0.000 description 4
- 229920002678 cellulose Polymers 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 230000007062 hydrolysis Effects 0.000 description 4
- 238000006460 hydrolysis reaction Methods 0.000 description 4
- 229920005610 lignin Polymers 0.000 description 4
- 229920001221 xylan Polymers 0.000 description 4
- 150000004823 xylans Chemical class 0.000 description 4
- 241000193830 Bacillus <bacterium> Species 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000007086 side reaction Methods 0.000 description 3
- OWEGMIWEEQEYGQ-UHFFFAOYSA-N 100676-05-9 Natural products OC1C(O)C(O)C(CO)OC1OCC1C(O)C(O)C(O)C(OC2C(OC(O)C(O)C2O)CO)O1 OWEGMIWEEQEYGQ-UHFFFAOYSA-N 0.000 description 2
- 206010013786 Dry skin Diseases 0.000 description 2
- 241000726221 Gemma Species 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- GUBGYTABKSRVRQ-PICCSMPSSA-N Maltose Natural products O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 description 2
- 240000000111 Saccharum officinarum Species 0.000 description 2
- 235000007201 Saccharum officinarum Nutrition 0.000 description 2
- 125000002777 acetyl group Chemical group [H]C([H])([H])C(*)=O 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 2
- GUBGYTABKSRVRQ-QUYVBRFLSA-N beta-maltose Chemical compound OC[C@H]1O[C@H](O[C@H]2[C@H](O)[C@@H](O)[C@H](O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@@H]1O GUBGYTABKSRVRQ-QUYVBRFLSA-N 0.000 description 2
- 239000008280 blood Substances 0.000 description 2
- 210000004369 blood Anatomy 0.000 description 2
- 210000000170 cell membrane Anatomy 0.000 description 2
- 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 description 2
- 238000004939 coking Methods 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 235000005911 diet Nutrition 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 230000032050 esterification Effects 0.000 description 2
- 238000005886 esterification reaction Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 230000008595 infiltration Effects 0.000 description 2
- 238000001764 infiltration Methods 0.000 description 2
- 238000010297 mechanical methods and process Methods 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 102000004196 processed proteins & peptides Human genes 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 1
- 206010010774 Constipation Diseases 0.000 description 1
- 208000005016 Intestinal Neoplasms Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- SRBFZHDQGSBBOR-LECHCGJUSA-N alpha-D-xylose Chemical compound O[C@@H]1CO[C@H](O)[C@H](O)[C@H]1O SRBFZHDQGSBBOR-LECHCGJUSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000012000 cholesterol Nutrition 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 206010012601 diabetes mellitus Diseases 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 230000000378 dietary effect Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 208000007784 diverticulitis Diseases 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 201000002313 intestinal cancer Diseases 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 229920001206 natural gum Polymers 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 210000000496 pancreas Anatomy 0.000 description 1
- 239000001814 pectin Substances 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 239000003053 toxin Substances 0.000 description 1
- 231100000765 toxin Toxicity 0.000 description 1
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 1
- 229960003487 xylose Drugs 0.000 description 1
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
The invention discloses a kind of utilization bagasse produces the water-soluble method with Water insoluble dietary fiber simultaneously, belong to biological technical field.The present invention is improved to conventional steam explosion isolation technics, using relatively low boiling temperature and elevated pressures(Inert gas is provided)Condition, and digested using special biology enzyme, it is ensured that high efficiency that bagasse is utilized, high-quality, high yield.The present invention obtains water-soluble and Water insoluble dietary fiber simultaneously using bagasse, and gained dietary fiber purity is high, and process is simple;Simultaneously present invention reduces production cost, improves economic benefit, it is easy to industrialized production.
Description
Technical field
The present invention relates to biological technical field, it is more particularly to a kind of using bagasse produce simultaneously it is water-soluble with it is water-insoluble
The method of dietary fiber.
Background technology
Dietary fiber can be divided into two fundamental types whether to be dissolved in water:Water-soluble dietary fiber(SDF)With non-aqueous
Property dietary fiber(IDF).Cellulose, lignin are modal Water insoluble dietary fibers, and pectin, natural gum etc. belong to water-soluble
Dietary fiber.The two not only species have difference, and physiologically active also has difference.It was found that water-soluble dietary fiber is more non-aqueous
Soluble dietary fiber has higher physiologically active.Water-soluble dietary fiber can slow down digestion rate and most rapid drainage courage is solid
Alcohol, so the blood sugar that can be allowed in blood and cholesterol are controlled in optimal level, may also help in diabetic reduces pancreas
Island element and triglyceride.Water insoluble dietary fiber can reduce the risk for suffering from intestinal cancer, at the same can by assimilating food in have
Noxious material Constipation and diverticulitis, and lower the toxin of bacterium discharge in alimentary canal.Most plants all contain water solubility
With Water insoluble dietary fiber, so balanced intake water solubility could obtain different benefits from Water insoluble dietary fiber in diet
Place.
Hemicellulose containing mass fraction 15-35% in grass, the overwhelming majority are xylan.Xylan be with
Isosorbide-5-Nitrae-β-D- pyranoid forms wood sugar constitute main chain, with 4- oxygen methyl-glucopyranose aldehydic acid as side chain, be difficult to be disappeared
The heteroglycan of change, is excellent dietary fibre.Xylan has good hydrophilicity, than dietary cellulosic be easier aquation,
Absorption, profit rise.Due to the otherness of side chain, dissolubility of the xylan in water is also variant, wherein there are about mass fraction 40%
For water-soluble dietary fiber, mass fraction 60% for Water insoluble dietary fiber.
Bagasse is sugarcane remaining Main By product Jing after mechanical expression, extraction, accounts for sugarcane squeezing amount mass fraction
24-27%.Bagasse main chemical is cellulose(Mass fraction 46%), hemicellulose(Mass fraction 26%), lignin
(Mass fraction 23%)Deng macromolecular substances, in addition with a small amount of(Mass fraction 5%)Ash content, wax etc..Due to cane milling
When operate fully according to food standard, the crude fibre containing up to 95% mass fraction in bagasse, thus bagasse is to prepare meals
The high-quality raw material of fiber.
But have no in prior art using bagasse while producing the water-soluble report with Water insoluble dietary fiber, shadow
The performance of bagasse economic benefit is rung.
The content of the invention
In order to make up the deficiencies in the prior art, the invention provides it is a kind of using bagasse produce simultaneously it is water-soluble with it is non-aqueous
The method of soluble dietary fiber.
The technical scheme is that:
A kind of utilization bagasse produces the water-soluble method with Water insoluble dietary fiber, including step simultaneously:
1)Cooker is inserted after bagasse impurity elimination;
2)The water of bagasse quality 1-20 times is added in cooker, adds alkali to alkali lye mass concentration to be 1-10%;It is passed through steam
To cooker, stop logical steam after being warming up to 60-100 DEG C, inert gas is passed through in cooker, air in cooker is arranged
Only;Then intermittence is passed through steam and inert gas into cooker, maintaining in hydrolytic decomposition pot temperature as 60-100 DEG C and
Pressure is 0.1-1MPa, heat-insulation pressure keeping 10-120 minutes;
3)By the substance release in cooker out, and in being transferred to grinding mill grind;
4)Step 3)Gained slurry is placed in enzymatic vessel, and the water of slurry quality 1-10 times is added in enzymatic vessel, adds compound
Protease, interval 1-3 minute, is passed through inert gas, digests 10-80 minutes;Normal temperature type AMS is subsequently added, 10- is digested
80 minutes;Then pass to steam and be warming up to 60-70 DEG C, be incubated the activity of 2-20 minute inactivators;The compound protease is by having
The alkali protease of standby endopeptidase activity and the Proteinase K for possessing peptide ending enzyme activity are constituted;The normal temperature type AMS is by micro-
Ripple induction gained variation bacillus licheniformis secretion gained AMS, the preference temperature of the normal temperature type AMS is 22-
35℃;
5)Go out after enzyme, separation of solid and liquid obtains filter residue one and filtrate one by the substance release in enzymatic vessel out;
6)The gained sig water of filter residue one is washed several times, separation of solid and liquid, and centralized collection washing lotion is to filtrate one, obtains two He of filter residue
Filtrate two;
7)Diluted acid being added in filtrate two, pH being adjusted to 4-6, after stirring, stable 1-5 hours, separate out precipitation, and separation of solid and liquid is obtained
Filter residue three and filtrate three;
8)The liquid that adds dilute alkali in filter residue three dissolves, then acid out again;Repeat 2-3 time, separation of solid and liquid obtains filter residue four and filtrate four;
9)Four drying of filter residue, crushing, obtain water-soluble dietary fiber;
10)The ethanol of 1-10 times of volume is added in filtrate three, after stirring, stable 1-3 hours are separated out and precipitated, separation of solid and liquid,
Obtain filter residue five and filtrate five;
11)Filter residue five and two drying of filter residue, crushing, obtain Water insoluble dietary fiber.
Preferably, step 4)In, the obtaining step of the microwave induced gained variation bacillus licheniformis is concrete
For:The nutrient solution of bacillus licheniformis is placed in into microwave generator, setting microwave power is 850-950W, pulse frequency is
2300MHz, microwave treatment 20s cool down 20s, reciprocal 25-35 time according to this;Nutrient solution after microwave treatment is coated on into solid training
On foster base, cultivate 1-2 days under the conditions of 30 DEG C, by the high ground of alpha-amylase activity under four plants of normal temperature of screening in the bacterium colony for surviving
The dissociant of clothing bacillus.
Further, the dissociant Amplification Culture of alpha-amylase activity highest bacillus licheniformis under normal temperature is selected,
So as to obtain the normal temperature type AMS.The normal temperature type AMS obtained using the method, at normal temperatures can efficient enzyme
Solution starch, had both reduced energy consumption, turn avoid the generation of side reaction.
Preferably, possess the alkali protease of endopeptidase activity in the compound protease and possess peptide ending enzyme work
Property Proteinase K ratio be 1:1-3;The addition of the compound protease meets every kilogram of butt bagasse 400-800U,
The addition of the normal temperature type AMS meets every kilogram of butt bagasse 300-700U.
Preferably, the alkali is NaOH, potassium hydroxide, ammoniacal liquor or calcium hydroxide;The acid is hydrochloric acid, nitre
Acid or acetic acid.
Preferably, the inert gas is nitrogen, helium or argon gas.
Preferably, step 9), step 11)Described in be dried for spray drying, heated-air drying, fluidized bed drying or
Freeze-drying;Baking temperature is less than 120 DEG C.
Preferably, step 10)In the volume fraction of ethanol used be 95%.
Beneficial effects of the present invention are:
The present invention is improved to conventional steam explosion isolation technics, using relatively low boiling temperature and elevated pressures(Inert gas
There is provided)Condition, and digested using special biology enzyme, it is ensured that high efficiency that bagasse is utilized, high-quality, high yield.The present invention
Water-soluble and Water insoluble dietary fiber is obtained simultaneously using bagasse, and gained dietary fiber purity is high, and process is simple.
Present invention reduces production cost, improves economic benefit, it is easy to industrialized production.
Specific embodiment
Embodiment 1
A kind of utilization bagasse produces the water-soluble method with Water insoluble dietary fiber, including step simultaneously:
1)Bagasse impurity elimination(Reject big material)After insert cooker;
2)The water of 10 times of bagasse quality is added in cooker, adds potassium hydroxide to alkali lye mass concentration to be 7%;It is passed through steaming
Vapour stops logical steam to cooker, after being warming up to 90 DEG C, is passed through inert nitrogen gas, by air in cooker in cooker
Emptying, sealing;Then intermittence is passed through steam and inert gas into hydrolytic decomposition pot, with maintain in hydrolytic decomposition pot temperature as 95 DEG C with
And pressure be 0.8MPa, heat-insulation pressure keeping 50 minutes;
In the step, adopt relatively low boiling temperature to avoid decomposition reaction, the dehydration of each component(Coking)Reaction, peeling reaction
Deng using elevated pressures(By being passed through inert gas realization)Ensure that alkali lye, to the effective infiltration between bagasse cell membrane, is adopted
Use inert environments(It is passed through inert gas realization)Avoid oxidation reaction, the esterification of acetyl group of each component molecular radical
Deng so as to ensure that integrality, high yield pulp1 and the high-quality of each material;This step diluted alkaline can extract hemicellulose simultaneously
Extract the most of siliceous grade inorganic salts in ash content;
3)By the substance release in cooker out, and in being transferred to mill grind 30min;Part macromolecular is cracked with Mechanical Method
Between it is chemical bonded, be fully contacted beneficial to next step enzyme system and material;
4)Step 3)Gained slurry is placed in enzymatic vessel, and the water of 6 times of slurry quality is added in enzymatic vessel, adds compound protein
Enzyme(500U/ kilogram of butt bagasse), intermittently 1 minute, inert gas is passed through, is digested 40 minutes;It is subsequently added normal temperature type α-shallow lake
Powder enzyme(400U/ kilogram of butt bagasse), digest 30 minutes;Then pass to steam and be warming up to 65 DEG C, be incubated 12 minutes inactivators
Activity;
Wherein, compound protease is made up of the alkali protease for possessing endopeptidase activity and the Proteinase K for possessing peptide ending enzyme activity,
It is 1 to possess the alkali protease of endopeptidase activity in compound protease with the ratio of the Proteinase K for possessing peptide ending enzyme activity: 1;
The compound protease can effectively hydrolyzing protein at normal temperatures;
Normal temperature type AMS is by microwave induced gained variation bacillus licheniformis secretion gained AMS;Microwave induced gained
The obtaining step of variation bacillus licheniformis is specially:The nutrient solution of bacillus licheniformis is placed in into microwave generator, is arranged micro-
Wave power is 900W, and pulse frequency is 2300MHz, microwave treatment 20s, cools down 20s, reciprocal 30 times according to this;After microwave treatment
Nutrient solution be coated on solid medium, under the conditions of 30 DEG C cultivate 1-2 days, by the bacterium colony for surviving screen four plants of normal temperature
The dissociant of the high bacillus licheniformis of lower alpha-amylase activity.Select alpha-amylase activity highest lichens gemma under normal temperature
The dissociant Amplification Culture of bacillus, so as to obtain normal temperature type AMS;Normal temperature type AMS is high at a temperature of 22-35 DEG C
Efficient hydrolysis starch, it is not necessary to as the thermal-stable α-amylase for adopting mostly at present needs high temperature(80-90℃)Condition, thus subtract
Energy consumption is lacked and has also reduced the requirement to equipment, while greatly reducing the generation of side reaction;Herein can be mildly with enzyme process
Protein, Starch Hydrolysis are entered in filtrate, so as to successfully remove into the peptides of small molecule, amino acid, maltose, glucose etc.
Protein and starch;
5)Go out after enzyme, separation of solid and liquid obtains filter residue one and filtrate one by the substance release in enzymatic vessel out;
6)Gained filter residue one is washed several times with 2% potassium hydroxide solution, and separation of solid and liquid obtains filter residue two and filtrate two;
7)Acetic acid,diluted is added in filtrate two, pH is adjusted to 5, after stirring, low temperature(6℃)Lower standing, stablizes 4 hours, separates out
Precipitation, separation of solid and liquid obtain filter residue three and filtrate three;
8)The potassium hydroxide solution dissolving for Jia 2% in filter residue three, then acid out again;Repeat 2-3 time, separation of solid and liquid obtains four He of filter residue
Filtrate four;
9)Filter residue four is spray-dried, crushing, obtains water-soluble dietary fiber(Water soluble pentosan), high purity 98%;Spraying is dry
Dry room temperature is less than 60 DEG C;
10)The 95% of 4 times of volumes ethanol is added in filtrate three, after stirring, is stablized 2 hours, separated out and precipitate, separation of solid and liquid,
Obtain filter residue five and filtrate five;
11)Filter residue Five Classics heated-air drying(Less than 60 DEG C), crush, obtain part Water insoluble dietary fiber(Water-insoluble half fiber
Element), high purity 95%;Two Jing fluidized bed dryings of filter residue(Less than 60 DEG C), crush, obtain another part Water insoluble dietary fiber
(Cellulose and lignin)High purity 96%.
Embodiment 2
A kind of utilization bagasse produces the water-soluble method with Water insoluble dietary fiber, including step simultaneously:
1)Bagasse impurity elimination(Reject big material)After insert cooker;
2)The water of 12 times of bagasse quality is added in cooker, adds ammoniacal liquor to alkali lye mass concentration to be 5%;It is passed through steam extremely
In cooker, stop logical steam after being warming up to 85 DEG C, inert nitrogen gas are passed through in cooker, air in cooker is arranged
Only, seal;Then intermittence is passed through steam and inert gas into cooker, maintaining in cooker temperature as 90 DEG C and
Pressure is 0.6MPa, heat-insulation pressure keeping 60 minutes;
In the step, adopt relatively low boiling temperature to avoid decomposition reaction, the dehydration of each component(Coking)Reaction, peeling reaction
Deng using elevated pressures(By being passed through inert gas realization)Ensure that alkali lye, to the effective infiltration between bagasse cell membrane, is adopted
Use inert environments(It is passed through inert gas realization)Avoid oxidation reaction, the esterification of acetyl group of each component molecular radical
Deng so as to ensure that integrality, high yield pulp1 and the high-quality of each material;This step diluted alkaline can extract hemicellulose simultaneously
Extract the most of siliceous grade inorganic salts in ash content;
3)By the substance release in cooker out, and in being transferred to colloid mill grind 30min;Big point of part is cracked with Mechanical Method
It is chemical bonded between son, it is fully contacted beneficial to next step enzyme system and material;
4)Step 3)Gained slurry is placed in enzymatic vessel, and the water of 4 times of slurry quality is added in enzymatic vessel, adds compound protein
Enzyme(600U/ kilogram of butt bagasse), intermittently 1 minute, inert gas is passed through, is digested 30 minutes;It is subsequently added normal temperature type α-shallow lake
Powder enzyme(500U/ kilogram of butt bagasse), digest 25 minutes;Then pass to steam and be warming up to 70 DEG C, be incubated 10 minutes inactivators
Activity;
Wherein, compound protease is made up of the alkali protease for possessing endopeptidase activity and the Proteinase K for possessing peptide ending enzyme activity,
It is 1 to possess the alkali protease of endopeptidase activity in compound protease with the ratio of the Proteinase K for possessing peptide ending enzyme activity: 2;
The compound protease can effectively hydrolyzing protein at normal temperatures;
Normal temperature type AMS is by microwave induced gained variation bacillus licheniformis secretion gained AMS;Microwave induced gained
The obtaining step of variation bacillus licheniformis is specially:The nutrient solution of bacillus licheniformis is placed in into microwave generator, is arranged micro-
Wave power is 900W, and pulse frequency is 2300MHz, microwave treatment 20s, cools down 20s, reciprocal 30 times according to this;After microwave treatment
Nutrient solution be coated on solid medium, under the conditions of 30 DEG C cultivate 1-2 days, by the bacterium colony for surviving screen four plants of normal temperature
The dissociant of the high bacillus licheniformis of lower alpha-amylase activity.Select alpha-amylase activity highest lichens gemma under normal temperature
The dissociant Amplification Culture of bacillus, so as to obtain normal temperature type AMS;Normal temperature type AMS is high at a temperature of 22-35 DEG C
Efficient hydrolysis starch, it is not necessary to as the thermal-stable α-amylase for adopting mostly at present needs high temperature(80-90℃)Condition, thus subtract
Energy consumption is lacked and has also reduced the requirement to equipment, while greatly reducing the generation of side reaction;Herein can be mildly with enzyme process
Protein, Starch Hydrolysis are entered in filtrate, so as to successfully remove into the peptides of small molecule, amino acid, maltose, glucose etc.
Protein and starch;
5)Go out after enzyme, separation of solid and liquid obtains filter residue one and filtrate one by the substance release in enzymatic vessel out;
6)Gained filter residue one is washed several times with 3% ammonia spirit, separation of solid and liquid, and centralized collection washing lotion is to filtrate one, must filter
Slag two and filtrate two;
7)Watery hydrochloric acid is added in filtrate two, pH is adjusted to 4.5, after stirring, low temperature(5℃)Lower standing, stablizes 4 hours, analysis
Go out precipitation, separation of solid and liquid obtains filter residue three and filtrate three;
8)The ammonia spirit dissolving for Jia 3% in filter residue three, then acid out again;Repeat 3 times, separation of solid and liquid obtains filter residue four and filtrate
Four;
9)Four Jing heated-air dryings of filter residue, crushing, obtain water-soluble dietary fiber(Water soluble pentosan), high purity 97%;It is dried temperature
Degree is less than 60 DEG C;
10)The 95% of 5 times of volumes ethanol is added in filtrate three, after stirring, is stablized 2 hours, separated out and precipitate, separation of solid and liquid,
Obtain filter residue five and filtrate five;
11)Filter residue Five Classics heated-air drying(Less than 60 DEG C), crush, obtain part Water insoluble dietary fiber(Water-insoluble half fiber
Element), high purity 96%;Two Jing fluidized bed dryings of filter residue(Less than 60 DEG C), crush, obtain another part Water insoluble dietary fiber
(Cellulose and lignin), high purity 97%.
Claims (8)
1. a kind of utilization bagasse produces the water-soluble method with Water insoluble dietary fiber simultaneously, it is characterised in that including step
Suddenly:
1)Cooker is inserted after bagasse impurity elimination;
2)The water of bagasse quality 1-20 times is added in cooker, adds alkali to alkali lye mass concentration to be 1-10%;It is passed through steam
Be warming up to cooker after 60-100 DEG C and stop logical steam, inert gas is passed through in cooker, air in cooker is arranged
Only;Then intermittence is passed through steam and inert gas into cooker, maintaining in cooker temperature as 60-100 DEG C and
Pressure is 0.1-1MPa, heat-insulation pressure keeping 10-120 minutes;
3)By the substance release in cooker out, and in being transferred to grinding mill grind;
4)Step 3)Gained slurry is placed in enzymatic vessel, and the water of slurry quality 1-10 times is added in enzymatic vessel, adds compound
Protease, interval 1-3 minute, is passed through inert gas, digests 10-80 minutes;Normal temperature type AMS is subsequently added, 10- is digested
80 minutes;Then pass to steam and be warming up to 60-70 DEG C, be incubated the activity of 2-20 minute inactivators;The compound protease is by having
The alkali protease of standby endopeptidase activity and the Proteinase K for possessing peptide ending enzyme activity are constituted;The normal temperature type AMS is by micro-
Ripple induction gained variation bacillus licheniformis secretion gained AMS, the preference temperature of the normal temperature type AMS is 22-
35℃;
5)Go out after enzyme, separation of solid and liquid obtains filter residue one and filtrate one by the substance release in enzymatic vessel out;
6)The gained sig water of filter residue one is washed several times, separation of solid and liquid, and centralized collection washing lotion is to filtrate one, obtains two He of filter residue
Filtrate two;
7)Diluted acid being added in filtrate two, pH being adjusted to 4-6, after stirring, stable 1-5 hours, separate out precipitation, and separation of solid and liquid is obtained
Filter residue three and filtrate three;
8)The liquid that adds dilute alkali in filter residue three dissolves, then acid out again;Repeat 2-3 time, separation of solid and liquid obtains filter residue four and filtrate four;
9)Four drying of filter residue, crushing, obtain water-soluble dietary fiber;
10)The ethanol of 1-10 times of volume is added in filtrate three, after stirring, stable 1-3 hours are separated out and precipitated, separation of solid and liquid,
Obtain filter residue five and filtrate five;
11)Filter residue five and two drying of filter residue, crushing, obtain Water insoluble dietary fiber.
2. the water-soluble method with Water insoluble dietary fiber, its feature are produced simultaneously using bagasse as claimed in claim 1
It is, step 4)In, the obtaining step of the microwave induced gained variation bacillus licheniformis is specially:By bacillus licheniformis
Nutrient solution be placed in microwave generator, setting microwave power is 850-950W, and pulse frequency is 2300MHz, microwave treatment 20s,
Cooling 20s, it is reciprocal 25-35 time according to this;Nutrient solution after microwave treatment is coated on solid medium, is cultivated under the conditions of 30 DEG C
1-2 days, by the dissociant that the high bacillus licheniformis of alpha-amylase activity under four plants of normal temperature is screened in the bacterium colony for surviving.
3. the water-soluble method with Water insoluble dietary fiber, its feature are produced simultaneously using bagasse as claimed in claim 2
It is:The dissociant Amplification Culture of alpha-amylase activity highest bacillus licheniformis under normal temperature is selected, it is described so as to obtain
Normal temperature type AMS.
4. the water-soluble method with Water insoluble dietary fiber is produced simultaneously using bagasse, which special as claimed in claim 1 or 2
Levy and be:Possess the alkali protease and the Proteinase K for possessing peptide ending enzyme activity of endopeptidase activity in the compound protease
Ratio is 1:1-3;The addition of the compound protease meets every kilogram of butt bagasse 400-800U, the normal temperature type α-shallow lake
The addition of powder enzyme meets every kilogram of butt bagasse 300-700U.
5. the water-soluble method with Water insoluble dietary fiber, its feature are produced simultaneously using bagasse as claimed in claim 1
It is:The alkali is NaOH, potassium hydroxide, ammoniacal liquor or calcium hydroxide;The acid is hydrochloric acid, nitric acid or acetic acid.
6. the water-soluble method with Water insoluble dietary fiber, its feature are produced simultaneously using bagasse as claimed in claim 1
It is:The inert gas is nitrogen, helium or argon gas.
7. the water-soluble method with Water insoluble dietary fiber, its feature are produced simultaneously using bagasse as claimed in claim 1
It is:Step 9), step 11)Described in be dried as spray drying, heated-air drying, fluidized bed drying or freeze-drying;It is dried temperature
Degree is less than 120 DEG C.
8. the water-soluble method with Water insoluble dietary fiber, its feature are produced simultaneously using bagasse as claimed in claim 1
It is:Step 10)In the volume fraction of ethanol used be 95%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610852063.9A CN106539097A (en) | 2016-09-27 | 2016-09-27 | The water-soluble method with Water insoluble dietary fiber is produced simultaneously using bagasse |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610852063.9A CN106539097A (en) | 2016-09-27 | 2016-09-27 | The water-soluble method with Water insoluble dietary fiber is produced simultaneously using bagasse |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106539097A true CN106539097A (en) | 2017-03-29 |
Family
ID=58368133
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610852063.9A Pending CN106539097A (en) | 2016-09-27 | 2016-09-27 | The water-soluble method with Water insoluble dietary fiber is produced simultaneously using bagasse |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106539097A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107129542A (en) * | 2017-07-10 | 2017-09-05 | 桂林融通科技有限公司 | A kind of method for extracting bagasse polysaccharide |
CN107692243A (en) * | 2017-08-07 | 2018-02-16 | 云南肠和健康科技股份有限公司 | The preparation method and sugarcane dietary fiber of a kind of sugarcane dietary fiber |
CN110074418A (en) * | 2019-05-21 | 2019-08-02 | 山东探克生物科技股份有限公司 | A kind of extracting method of seaweed diet fiber |
CN110574934A (en) * | 2019-10-16 | 2019-12-17 | 广西马中粮油有限公司 | Method for producing dietary fiber by using rice hull as raw material |
CN110652014A (en) * | 2019-10-16 | 2020-01-07 | 梁乐 | Method for preparing dietary fiber from zedoary turmeric leaves |
CN113016950A (en) * | 2021-04-20 | 2021-06-25 | 哈尔滨求真生物科技有限公司 | Series products prepared from bagasse, preparation method and comprehensive utilization method of bagasse |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1335097A (en) * | 2001-08-18 | 2002-02-13 | 广西大学 | Deep bagasse processing method of producing edible fibre |
CN103976369A (en) * | 2014-04-04 | 2014-08-13 | 浙江恒乐粮食有限公司 | Production method for high-activity rice bran dietary fiber |
CN104404803A (en) * | 2014-08-29 | 2015-03-11 | 济南米铎碳新能源科技有限公司 | Straw component separation and straw component full utilization method |
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 |
-
2016
- 2016-09-27 CN CN201610852063.9A patent/CN106539097A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1335097A (en) * | 2001-08-18 | 2002-02-13 | 广西大学 | Deep bagasse processing method of producing edible fibre |
CN103976369A (en) * | 2014-04-04 | 2014-08-13 | 浙江恒乐粮食有限公司 | Production method for high-activity rice bran dietary fiber |
CN104404803A (en) * | 2014-08-29 | 2015-03-11 | 济南米铎碳新能源科技有限公司 | Straw component separation and straw component full utilization method |
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 |
Non-Patent Citations (3)
Title |
---|
张建春等: "《汉麻籽综合利用加工技术》", 31 December 2010 * |
车云波: "《功能食品加工技术》", 31 January 2013 * |
颜贤仔等: "微波对枯草芽孢杆菌诱变效应的研究", 《江西农业大学学报》 * |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107129542A (en) * | 2017-07-10 | 2017-09-05 | 桂林融通科技有限公司 | A kind of method for extracting bagasse polysaccharide |
CN107692243A (en) * | 2017-08-07 | 2018-02-16 | 云南肠和健康科技股份有限公司 | The preparation method and sugarcane dietary fiber of a kind of sugarcane dietary fiber |
CN110074418A (en) * | 2019-05-21 | 2019-08-02 | 山东探克生物科技股份有限公司 | A kind of extracting method of seaweed diet fiber |
CN110574934A (en) * | 2019-10-16 | 2019-12-17 | 广西马中粮油有限公司 | Method for producing dietary fiber by using rice hull as raw material |
CN110652014A (en) * | 2019-10-16 | 2020-01-07 | 梁乐 | Method for preparing dietary fiber from zedoary turmeric leaves |
CN113016950A (en) * | 2021-04-20 | 2021-06-25 | 哈尔滨求真生物科技有限公司 | Series products prepared from bagasse, preparation method and comprehensive utilization method of bagasse |
CN113016950B (en) * | 2021-04-20 | 2024-03-05 | 中粮崇左糖业有限公司 | Series products prepared from bagasse, preparation method and bagasse comprehensive utilization method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106539097A (en) | The water-soluble method with Water insoluble dietary fiber is produced simultaneously using bagasse | |
CN106638089B (en) | The method for preparing dissolving pulp and other high value added products using crop material | |
CN106519066A (en) | Method for production of dietary fiber and combined production of pectin by utilizing fruit branches and fruit peels (residues) | |
CN106509915A (en) | Method of producing dietary fibers and co-producing xylose and furfural from corn stalks | |
CN102187984A (en) | Preparation method for soluble dietary fiber with apple pomace as raw material | |
CN106072672A (en) | A kind of production technology activating wheat-bran dietary fiber | |
Wagner et al. | Valorization of brewer's spent grain by different strategies of structural destabilization and enzymatic saccharification | |
CN109527601A (en) | The preparation method of seaweed diet fiber | |
CN106617110A (en) | Preparation method of tea dietary fiber | |
CN109576324A (en) | A kind of astragalus polyose and its biological extraction method | |
CN103243138A (en) | Method for preparing corncob xylooligosaccharide by a complex enzyme method | |
CN106509914A (en) | Method for preparing dietary fibers by use of crop straws | |
CN112920285B (en) | Preparation method and application of rice bran polysaccharide | |
CN106381320B (en) | The preparation method of cellooligosaccharide | |
CN110628846B (en) | Method for preparing xylooligosaccharide by high-temperature high-pressure treatment | |
CN100532396C (en) | Process for preparing high purity pectin by using apple pomace | |
CN106632581A (en) | Multilayer separation and refining method for straw components | |
CN106519065A (en) | Method for preparing pectin, hemicelluloses, chemimechanical pulp and wood-plastic composite material by utilizing cotton straws | |
CN106519258B (en) | The preparation method of high-purity lignin with complete molecular structure | |
CN101665534B (en) | Preparation method of concentrated protein of cottonseeds | |
De Menezes et al. | Fungal cellulases as an aid for the saccharification of cassava | |
CN106509912A (en) | Preparation method of whole straw nutritional powder | |
Guerfali et al. | Hydrolytic potential of Talaromyces thermophilus β-xylosidase and its use for continuous xylose production | |
CN101828628A (en) | Biological treatment method for effectively extracting rapeseed protein | |
CN101843329B (en) | Method for preparing dietary fiber by adopting corn bran hydrolyzed by multifunctional enzyme |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170329 |