CN106360746A - Extraction system for dietary fibers and proteins - Google Patents
Extraction system for dietary fibers and proteins Download PDFInfo
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- CN106360746A CN106360746A CN201611049810.1A CN201611049810A CN106360746A CN 106360746 A CN106360746 A CN 106360746A CN 201611049810 A CN201611049810 A CN 201611049810A CN 106360746 A CN106360746 A CN 106360746A
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- reactor
- reaction kettle
- feed tube
- washer
- centrifuge
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- 235000013325 dietary fiber Nutrition 0.000 title claims abstract description 85
- 238000000605 extraction Methods 0.000 title claims abstract description 54
- 102000004169 proteins and genes Human genes 0.000 title claims abstract description 43
- 108090000623 proteins and genes Proteins 0.000 title claims abstract description 43
- 235000021245 dietary protein Nutrition 0.000 title claims abstract description 21
- 238000006243 chemical reaction Methods 0.000 claims abstract description 103
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 23
- 235000018102 proteins Nutrition 0.000 claims abstract description 22
- 239000002253 acid Substances 0.000 claims abstract description 16
- 238000000751 protein extraction Methods 0.000 claims abstract description 14
- 239000003513 alkali Substances 0.000 claims abstract description 11
- 238000005238 degreasing Methods 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 131
- 238000007599 discharging Methods 0.000 claims description 62
- 239000012528 membrane Substances 0.000 claims description 61
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 55
- 239000012530 fluid Substances 0.000 claims description 52
- 239000007921 spray Substances 0.000 claims description 45
- 238000005485 electric heating Methods 0.000 claims description 32
- 238000010438 heat treatment Methods 0.000 claims description 32
- 238000001914 filtration Methods 0.000 claims description 23
- 238000005859 coupling reaction Methods 0.000 claims description 22
- 238000003306 harvesting Methods 0.000 claims description 21
- 230000007246 mechanism Effects 0.000 claims description 21
- 238000002242 deionisation method Methods 0.000 claims description 19
- 239000002699 waste material Substances 0.000 claims description 16
- 239000002657 fibrous material Substances 0.000 claims description 14
- 239000007787 solid Substances 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 12
- GQWNECFJGBQMBO-UHFFFAOYSA-N Molindone hydrochloride Chemical compound Cl.O=C1C=2C(CC)=C(C)NC=2CCC1CN1CCOCC1 GQWNECFJGBQMBO-UHFFFAOYSA-N 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 10
- 230000003139 buffering effect Effects 0.000 claims description 9
- 239000002585 base Substances 0.000 claims description 8
- 239000000523 sample Substances 0.000 claims description 8
- 230000008878 coupling Effects 0.000 claims description 7
- 238000010168 coupling process Methods 0.000 claims description 7
- 239000004744 fabric Substances 0.000 claims description 7
- 238000002604 ultrasonography Methods 0.000 claims description 7
- 238000005452 bending Methods 0.000 claims description 6
- 239000000872 buffer Substances 0.000 claims description 6
- 239000000284 extract Substances 0.000 claims description 5
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 4
- 238000010298 pulverizing process Methods 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 2
- 238000004080 punching Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 239000002244 precipitate Substances 0.000 abstract description 52
- 239000000843 powder Substances 0.000 abstract description 32
- 239000006228 supernatant Substances 0.000 abstract description 27
- 235000010627 Phaseolus vulgaris Nutrition 0.000 abstract description 24
- 244000046052 Phaseolus vulgaris Species 0.000 abstract description 24
- 239000000243 solution Substances 0.000 description 25
- 238000005119 centrifugation Methods 0.000 description 15
- 239000008367 deionised water Substances 0.000 description 9
- 229910021641 deionized water Inorganic materials 0.000 description 9
- 241000196324 Embryophyta Species 0.000 description 7
- 238000001035 drying Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 235000010469 Glycine max Nutrition 0.000 description 3
- 244000068988 Glycine max Species 0.000 description 3
- 230000005540 biological transmission Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000011160 research Methods 0.000 description 3
- 235000013527 bean curd Nutrition 0.000 description 2
- 235000019197 fats Nutrition 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- GOMNOOKGLZYEJT-UHFFFAOYSA-N isoflavone Chemical compound C=1OC2=CC=CC=C2C(=O)C=1C1=CC=CC=C1 GOMNOOKGLZYEJT-UHFFFAOYSA-N 0.000 description 2
- CJWQYWQDLBZGPD-UHFFFAOYSA-N isoflavone Natural products C1=C(OC)C(OC)=CC(OC)=C1C1=COC2=C(C=CC(C)(C)O3)C3=C(OC)C=C2C1=O CJWQYWQDLBZGPD-UHFFFAOYSA-N 0.000 description 2
- 235000008696 isoflavones Nutrition 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- IMQLKJBTEOYOSI-GPIVLXJGSA-N Inositol-hexakisphosphate Chemical compound OP(O)(=O)O[C@H]1[C@H](OP(O)(O)=O)[C@@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@@H]1OP(O)(O)=O IMQLKJBTEOYOSI-GPIVLXJGSA-N 0.000 description 1
- IMQLKJBTEOYOSI-UHFFFAOYSA-N Phytic acid Natural products OP(O)(=O)OC1C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C1OP(O)(O)=O IMQLKJBTEOYOSI-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 235000015278 beef Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000000975 bioactive effect Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000019784 crude fat Nutrition 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 235000013410 fast food Nutrition 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008363 phosphate buffer Substances 0.000 description 1
- 235000002949 phytic acid Nutrition 0.000 description 1
- 229940068041 phytic acid Drugs 0.000 description 1
- 239000000467 phytic acid Substances 0.000 description 1
- 239000001397 quillaja saponaria molina bark Substances 0.000 description 1
- 229930182490 saponin Natural products 0.000 description 1
- 150000007949 saponins Chemical class 0.000 description 1
- 210000000582 semen Anatomy 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 235000013597 soy food Nutrition 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23J—PROTEIN COMPOSITIONS FOR FOODSTUFFS; WORKING-UP PROTEINS FOR FOODSTUFFS; PHOSPHATIDE COMPOSITIONS FOR FOODSTUFFS
- A23J1/00—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites
- A23J1/14—Obtaining protein compositions for foodstuffs; Bulk opening of eggs and separation of yolks from whites from leguminous or other vegetable seeds; from press-cake or oil-bearing seeds
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Abstract
The invention provides an extraction system for dietary fibers and proteins. The extraction system comprises a pretreatment device, a degreasing device, a dietary fiber extraction device I, a protein extraction device and a dietary fiber extraction device II which are connected sequentially. The system is mainly used for extracting the dietary fibers and the proteins from bean dregs, wherein wet bean dregs are put into the pretreatment device and are crushed into bean dreg powder by the pretreatment device, the bean dreg powder is baked, the baked bean dreg powder is fed into the degreasing device for degreasing so as to obtain degreased bean dreg powder, the degreased bean dreg powder is put into the dietary fiber extraction device I, alkali liquor is added into the dietary fiber extraction device I, a reaction is carried out so as to obtain supernatant I and precipitates I, the precipitates I are water-insoluble dietary fibers, the supernatant I is introduced into the protein extraction device, acid liquor is added into the protein extraction device, a reaction is carried out so as to obtain supernatant II and precipitates II, the precipitates II are the proteins, the supernatant II is introduced into the dietary fiber extraction device II, ethanol is added into the dietary fiber extraction device II so as to obtain precipitates III, and the precipitates III are water-soluble dietary fibers.
Description
Technical field
The invention belongs to field of mechanical technique, it is related to a kind of system extracting dietary fiber and protein.
Background technology
Bean dregs are the Main By products in the processing of the bean products such as bean curd, bean milk, account for the 15%-20% of full dried tofu weight,
According to incompletely statistics, if calculated according to the wet bean dregs that every processing 0.5kg Semen sojae atricolor produces 2kg, domestic soy food product industry at present
20,000,000 tons of wet bean dregs of annual about production.Research shows, in bean dregs, dietary fiber accounts for 50%-60%, thick protein 15%-
20%, crude fat 6%-12%, and the feature thing such as multivitamin, mineral, soybean isoflavone, soybean saponin and phytic acid
Matter.For a long time because its water content high (75-85%) and easily fermentation are rotten, mostly it is taken as feedstuff, the fertilizer of low value
Material is discarded.And be to preserve to transport the dried carrying out because expense is too greatly without forming good industry chain (supply chain).Right at present
The resources development and utilization of bean dregs still rests on to be prepared at the beginning of the food such as a beef ball, bakery, fast food using it as major ingredient
Processing interpolation or as feedstuff.Recently as the rise of the research to bioactive substance, a large amount of fibres containing in bean dregs
Dimension element and isoflavone, natural ve isoreactivity material are more and more taken seriously, but the extraction to its soybean dreg dietary fiber or protein
It is substantially single and do not carry out systematic research, still in laboratory stage, little for produce reality, extraction cost
Of a relatively high, equipment imperfection is it is impossible to meet actual production requirement.
Content of the invention
The purpose of the present invention is that there are the problems referred to above for existing technology it is proposed that a kind of extract dietary fiber and albumen
The system of matter, level of integrated system is high, can reduce extraction cost.
The purpose of the present invention can be realized by following technical proposal:
A kind of system extracting dietary fiber and protein, including the pretreating device being sequentially connected, degreasing plant, meals
Fiber extraction element one, Protein Extraction device and dietary fiber extraction apparatus two；Pretreating device includes pulverizer and conveying
Auger one, the discharging opening of pulverizer connects the charging aperture of conveying auger one；Degreasing plant includes reactor one and centrifuge one, instead
Kettle one is answered to have feed pipe one, feed tube one and discharge nozzle one, feed tube one is connected with extraction flow container, contains leaching in extraction flow container
Extract, the feed pipe one of the discharging opening coupled reaction kettle one of conveying auger one, the discharge nozzle one of reactor one connects centrifuge one
Charging aperture；Dietary fiber extraction apparatus one include reactor two, centrifuge two and washer one, and reactor two has feed pipe
2nd, feed tube two, feed tube three and discharge nozzle two, the solid outlet of centrifuge one passes through conveying auger two and reactor two
Feed pipe two is connected, and feed tube two is connected with buffering flow container, contains buffer, feed tube three and alkali liquid tank phase in buffering flow container
Even, alkali liquid tank contains naoh solution, and the discharge nozzle two of reactor two connects the charging aperture of centrifuge two, and the solid of centrifuge two goes out
Material mouth connects the charging aperture of washer one；Protein Extraction device includes reactor three, centrifuge three and washer two, reactor
Three have feed tube four, feed tube five and discharge nozzle three, and the liquid outlet of centrifuge two passes through the feed tube of pipeline and reactor three
Four are connected, and feed tube five is connected with acid solution tank, contain acid solution in acid solution tank, and the discharge nozzle three of reactor three connects centrifuge
Three charging aperture, the solid outlet of centrifuge three connects the charging aperture of washer two；Dietary fiber extraction apparatus two include instead
Answer kettle four, centrifuge four and washer three, reactor four has feed tube six, feed tube seven and discharge nozzle four, centrifuge three
Liquid outlet is connected with the feed tube six of reactor four by pipeline, and feed tube seven is connected with alcohol tank, contains ethanol, reaction in alcohol tank
The discharge nozzle four of kettle four connects the charging aperture of centrifuge four, and the solid outlet of centrifuge four connects the charging aperture of washer three.
This system is mainly used in extracting the dietary fiber in bean dregs and protein, and wet bean dregs are put to pretreating device
In, wet bean dregs are smashed into okara powder by pretreating device, and are dried, and the okara powder after drying is admitted in degreasing plant
Row defat obtains defatted bean-dregs powder, and defatted bean-dregs powder is put in dietary fiber extraction apparatus one, after adding alkaline reaction, obtains
Supernatant one and precipitate one, precipitate one is water insoluble dietary fiber, and supernatant one is passed through in Protein Extraction device,
After adding acid liquid reaction, obtain supernatant two and precipitate two, precipitate two is protein, and supernatant two is passed through dietary fiber
Extraction element two, adds ethanol, is precipitated thing three, and precipitate three is water soluble dietary fiber.
In the above-mentioned system extracting dietary fiber and protein, the discharging opening of pulverizer is located at the bottom of pulverizer,
This discharging opening is provided with outlet valve；Conveying auger one includes base, charging pipeline section and feeding pipeline section, and feeding pipeline section can by bearing
It is rotationally connected with base, charging pipeline section is connected with feeding pipeline section and is rotatably connected by flange bearing, and charging pipeline section erects
Directly it is arranged on the underface of pulverizer, the upper end opening of charging pipeline section is the charging aperture of conveying auger one, charging pipeline section
Upper end is connected with the outlet valve of pulverizer, and feeding pipeline section tilts to reactor one, the upper end of feeding pipeline section from bottom to up
Opening is the discharging opening of conveying auger one, and the upper end of feeding pipeline section is connected by flange with the feed pipe one of reactor one；Send
Expects pipe section includes delivery pipe body, is provided with screw-conveyer-shaft in delivery pipe body, and screw-conveyer-shaft is controlled by motor, the outer concentric gap set of delivery pipe body
It is provided with thermal sleeve, between delivery pipe body and thermal sleeve, forms heating chamber, heating intracavity compartment of terrain is provided with and is sequentially connected electrically
Electric heating piece, electric heating piece is attached to the outer surface of delivery pipe body.
In the above-mentioned system extracting dietary fiber and protein, removably it is provided with above the discharging opening of pulverizer
Screen cloth；Feeding pipeline section has air inlet, and air inlet is connected with pressure fan.
In the above-mentioned system extracting dietary fiber and protein, reactor one includes reaction kettle body one and lid one,
Lid one lid is located on reaction kettle body one, and feed pipe one and feed tube one are fixedly arranged on lid one, and respectively with reaction kettle body one even
Logical, discharge nozzle one is located at the bottom of reaction kettle body one；It is provided with temperature sensor, temperature sensor connects temperature in reaction kettle body one
Display, temperature indicator is installed in the outer surface of reaction kettle body one；Exhaustor is additionally provided with lid one, exhaustor is connected with
Relief valve.
In the above-mentioned system extracting dietary fiber and protein, reactor one also has rabbling mechanism, rabbling mechanism
Including the motor being installed on lid one and the shaft stretching in reaction kettle body one, shaft has multiple stirring vanes, stirs
Mixing axle is in bending, and the upper end of shaft is connected with the output through-drive of motor by shaft coupling；Conveying auger two and conveying
The structure of auger one is identical.
In the above-mentioned system extracting dietary fiber and protein, reactor two includes reaction kettle body two and lid two,
Lid two lid is located on reaction kettle body two, and feed pipe two, feed tube two and feed tube three are fixedly arranged on lid two, discharge nozzle two respectively
Located at the bottom of reaction kettle body two, the discharging opening of conveying auger two is connected with feed pipe two flange of reactor two；Reaction kettle body
Two are externally provided with supersonic generator, and supersonic generator connects ultrasound probe, and ultrasound probe is in reaction kettle body two, instead
Answer and in kettle two, be additionally provided with temperature sensor, temperature sensor connects temperature indicator, temperature indicator is installed in reaction kettle body
Two outer surface.
In the above-mentioned system extracting dietary fiber and protein, reaction kettle body two is additionally provided with air inlet pipe, air inlet pipe
Outer end be in outside reaction kettle body two, the inner of air inlet pipe is in reaction kettle body two, and the outer end of air inlet pipe is connected with intake valve,
Intake valve is connected with the relief valve of pressure fan or reactor one by pipeline, and the inner of air inlet pipe connects air jet pipe, air jet pipe
In bending, the side wall phase of air jet pipe and reaction kettle body two is fixed, and the bottom adjacent to reaction kettle body two, air jet pipe upper and lower
Both sides are respectively provided with row's nozzle；Liquid flowing tube one is additionally provided with reaction kettle body two；Dietary fiber extraction apparatus one also include fluid reservoir
One, fluid reservoir one has inlet and liquid outlet, and fluid reservoir one is arranged between centrifuge two and reactor three, on lid two also
It is provided with feed tube eight, the liquid outlet of centrifuge two is connected with the inlet of fluid reservoir one, and the liquid outlet of fluid reservoir one is provided with liquid pump
With three-way valve one, the one outlet of this three-way valve one passes through the feed tube eight of pipeline coupled reaction kettle two, this three-way valve one another
One outlet passes through the feed tube four of pipeline coupled reaction kettle three；Washer one introversion is tiltedly provided with filter membrane one, and filter membrane one passes through
Support is detachably secured to the inwall of washer one, and filter membrane one lower section is filtering area, and filter membrane one top is spray area, sprays area
Inwall be installed with multiple showers, shower is connected with deionization water pot, and the charging aperture of washer one is opened in spray area
Upper end, the discharging opening of washer one is opened on the side wall in spray area, and the bottom of filtering area offers liquid outlet；Washer one
Discharging opening connect the charging aperture of conveying auger three, conveying auger three includes delivery pipe body two, is provided with auger in delivery pipe body two
Axle, screw-conveyer-shaft is controlled by motor, and the outer concentric gap of delivery pipe body two is arranged with thermal sleeve two, delivery pipe body two and thermal sleeve
Form heating chamber, heating intracavity compartment of terrain is provided with the electric heating piece being sequentially connected electrically, and electric heating piece is attached to delivery pipe body two between two
Outer surface, the discharging opening of conveying auger three connects water insoluble dietary fiber Material collecting box for harvesting.
In the above-mentioned system extracting dietary fiber and protein, reactor three includes reaction kettle body three and lid three,
Lid three lid is located on reaction kettle body three, and feed tube four and feed tube five are fixedly arranged on lid three, and respectively with reaction kettle body three even
Logical, the side wall of reaction kettle body three is provided with liquid flowing tube two；Discharge nozzle three is located at the bottom of reaction kettle body three, the lower section of reaction kettle body three
For centrifuge three, Protein Extraction device also includes fluid reservoir two, and fluid reservoir two has inlet and liquid outlet, and fluid reservoir two sets
Put between centrifuge three and reactor four, the liquid outlet of centrifuge three is connected with the inlet of fluid reservoir two, fluid reservoir two
Liquid outlet is provided with liquid pump and three-way valve two, and the one outlet of three-way valve two passes through the feed tube four of pipeline coupled reaction kettle three, and three
Another outlet feed tube six by pipeline coupled reaction kettle four of port valve two；Washer two introversion is tiltedly provided with filter membrane two,
Filter membrane two is detachably secured to the inwall of washer two by support, and filter membrane two lower section is filtering area, and filter membrane two top is spray
Drench area, the inwall in spray area is installed with multiple showers, and shower is connected with deionization water pot, and the charging aperture of washer two opens up
In the upper end in spray area, the discharging opening of washer two is opened on the side wall in spray area, and the bottom of filtering area offers out liquid
Mouthful；The discharging opening of washer two connects the charging aperture of conveying auger four, and conveying auger four includes delivery pipe body two, delivery pipe body two
Inside it is provided with screw-conveyer-shaft, screw-conveyer-shaft is controlled by motor, the outer concentric gap of delivery pipe body two is arranged with thermal sleeve two, delivery pipe body two
Form heating chamber and thermal sleeve two between, heating intracavity compartment of terrain is provided with the electric heating piece being sequentially connected electrically, and electric heating piece is attached to
The outer surface of delivery pipe body two, the discharging opening of conveying auger four connects protein Material collecting box for harvesting.
In the above-mentioned system extracting dietary fiber and protein, reactor three also includes rabbling mechanism, rabbling mechanism
Including the motor being installed on lid three and the shaft stretching in reaction kettle body three, shaft has multiple stirring vanes, stirs
The upper end mixing axle is connected with the output through-drive of motor by shaft coupling.
In the above-mentioned system extracting dietary fiber and protein, a fixed dividing plate in reactor four, dividing plate will react
Kettle four separates as upper reative cell and lower reative cell, and upper reaction interior is provided with a filter bag, and filter bag is made up of filter membrane three, and filter bag top is opened
Mouthful, feed tube six is installed in the top of reactor four, and feed tube six penetrates the upper opening of filter bag, and the bottom of filter bag connects discharging
Pipe five, discharge nozzle five wears dividing plate and stretches into lower reative cell, and the side wall of upper reative cell is connected with discharging tube, discharging tube and liquid pump phase
Even；Feed tube seven is installed in the side wall of lower reative cell, and discharge nozzle four is located at the bottom of lower reative cell；Dietary fiber extraction apparatus two
Also include fluid reservoir three, the liquid outlet of centrifuge four is connected with the inlet of fluid reservoir three, and the liquid outlet of fluid reservoir three is provided with liquid
Pump and three-way valve three, the one outlet of three-way valve three connects the feed tube six of upper reative cell by pipeline, three-way valve three another
Individual outlet connects waste liquid pool by pipeline；Washer three introversion is tiltedly provided with filter membrane four, and it is removably solid that filter membrane four passes through support
Due to the inwall of washer three, filter membrane four lower section is filtering area, and filter membrane four top is spray area, and the inwall in spray area is installed with many
Individual shower, shower is connected with deionization water pot, and the charging aperture of washer three is opened in the upper end in spray area, washer three
Discharging opening be opened in spray area side wall on, the bottom of filtering area offers liquid outlet；The discharging opening of washer three connects defeated
Send the charging aperture of auger five, conveying auger five includes delivery pipe body two, is provided with screw-conveyer-shaft in delivery pipe body two, and screw-conveyer-shaft is controlled by
Motor, the outer concentric gap of delivery pipe body two is arranged with thermal sleeve two, forms heating between delivery pipe body two and thermal sleeve two
Chamber, heating intracavity compartment of terrain is provided with the electric heating piece being sequentially connected electrically, and electric heating piece is attached to the outer surface of delivery pipe body, conveying auger
Five discharging opening connects water soluble dietary fiber Material collecting box for harvesting.
Compared with prior art, the present invention has the advantage that
1st, the pulverizer of this system is connected by conveying auger one with reactor one, not only achieves the conveying of okara powder,
And it is provided with electric heating piece in conveying auger one, there is heating function, the okara powder after pulverizing can be dried, okara powder is not
Need to deliver in drying mechanism again and dried, directly realize drying in conveying, simplify system composition, and improve
Production efficiency；
2nd, reactor one only carries the required heat of defat reaction and is provided by conveying auger one, so that previous conveying process is produced
Heat is reused, and reactor one is not required to additional heating arrangements, simplifies the structure of reactor one, and improves
The utilization rate of the energy, beneficial to reducing production cost；
3rd, the exhaustor of reactor one connects with the air inlet pipe of reactor two, the excessive gas energy discharged in reactor one
For reactor two it is achieved that gas recycles, and the excessive gas that reactor one is discharged carry heat, enter reactor
Two can also provide heat for reactor two.
Brief description
Fig. 1 is the structural representation of the extraction system of the present invention.
Fig. 2 is the schematic enlarged-scale view of pretreating device and degreasing plant.
Fig. 3 is the schematic enlarged-scale view of dietary fiber extraction apparatus one.
Fig. 4 is the schematic enlarged-scale view of Protein Extraction device.
Fig. 5 is the schematic enlarged-scale view of dietary fiber extraction apparatus two.
In figure, 1, pulverizer；2nd, conveying auger one；3rd, reactor one；4th, centrifuge one；5th, feed pipe one；6th, feed tube
One；7th, discharge nozzle one；8th, extract flow container；9th, reactor two；10th, centrifuge two；11st, washer one；12nd, feed pipe two；13rd, enter
Liquid pipe two；14th, feed tube three；15th, discharge nozzle two；16th, conveying auger two；17th, buffer flow container；18th, alkali liquid tank；19th, reactor
Three；20th, centrifuge three；21st, washer two；22nd, feed tube four；23rd, feed tube five；24th, discharge nozzle three；25th, acid solution tank；26、
Reactor four；27th, centrifuge four；28th, washer three；29th, feed tube six；30th, feed tube seven；31st, discharge nozzle four；32nd, alcohol tank；
33rd, base；34th, feed pipeline section；35th, feeding pipeline section；36th, delivery pipe body；37th, screw-conveyer-shaft；38th, thermal sleeve；39th, electric heating piece；
40th, screen cloth；41st, pressure fan；42nd, reaction kettle body one；43rd, lid one；44th, temperature sensor；45th, temperature indicator；46th, aerofluxuss
Pipe；47th, rabbling mechanism；48th, reaction kettle body two；49th, lid two；50th, supersonic generator；51st, ultrasound probe；52nd, air inlet
Pipe；53rd, air jet pipe；54th, nozzle；55th, liquid flowing tube one；56th, fluid reservoir one；57th, feed tube eight；58th, three-way valve one；59th, filter membrane
One；60th, filtering area；61st, spray area；62nd, shower；63rd, deionization water pot；64th, conveying auger three；65th, delivery pipe body two；
66th, thermal sleeve two；67th, water insoluble dietary fiber Material collecting box for harvesting；68th, reaction kettle body three；69th, lid three；70th, liquid flowing tube two；
71st, fluid reservoir two；72nd, three-way valve two；73rd, filter membrane two；74th, conveying auger four；75th, protein Material collecting box for harvesting；76th, dividing plate；77th, on
Reative cell；78th, lower reative cell；79th, filter bag；80th, discharge nozzle five；81st, discharging tube；82nd, fluid reservoir three；83rd, three-way valve three；84、
Waste liquid pool；85th, filter membrane four；86th, conveying auger five；87th, water soluble dietary fiber Material collecting box for harvesting.
Specific embodiment
The following is the specific embodiment of the present invention and combine accompanying drawing, technical scheme is further described,
But the present invention is not limited to these embodiments.
As shown in Figures 1 to 5, the present invention provides a kind of system extracting dietary fiber and protein, is mainly used in extracting
Dietary fiber in bean dregs and protein, including the pretreating device being sequentially connected, degreasing plant, dietary fiber extraction apparatus
First, Protein Extraction device and dietary fiber extraction apparatus two, wet bean dregs are put in pretreating device, and pretreating device will
Wet bean dregs smash into okara powder, and are dried, and the okara powder after drying is admitted in degreasing plant and carries out defat and obtain defat
Okara powder, defatted bean-dregs powder is put in dietary fiber extraction apparatus one, after adding alkaline reaction, obtains supernatant one and precipitation
Thing one, precipitate one is water insoluble dietary fiber, and supernatant one is passed through in Protein Extraction device, adds acid liquid reaction
Afterwards, supernatant two and precipitate two are obtained, precipitate two is protein, and supernatant two is passed through dietary fiber extraction apparatus two,
Add ethanol, be precipitated thing three, precipitate three is water soluble dietary fiber.
Specifically, pretreating device includes pulverizer 1 and conveying auger 1, and the discharging opening of pulverizer 1 connects conveying auger
One 2 charging aperture.
Degreasing plant includes reactor 1 and centrifuge 1, and reactor 1 has feed pipe 1, feed tube 1 and goes out
Expects pipe one, feed tube 1 is connected with extraction flow container 8, contains lixiviating solution, lixiviating solution is preferably normal hexane, conveying in extraction flow container 8
The feed pipe 1 of the discharging opening coupled reaction kettle 1 of auger 1, the discharge nozzle one of reactor 1 connects entering of centrifuge 1
Material mouth, extraction flow container 8 connects liquid valve and liquid pump, and after liquid valve and liquid pump unlatching, lixiviating solution flows out from extraction flow container 8, and
It is passed through reactor 1 through feed tube 1, the okara powder after pulverizing falls in conveying auger 1 from pulverizer 1, and defeated
The conveying sending auger 1 falls in reactor 1, and okara powder and lixiviating solution extract reaction 6h in reactor 1 and taken off
Fat mixed liquor, defat mixed liquor is passed through in centrifuge 1, and centrifugal rotational speed is 4000r/min, and centrifugation time is 20min, is taken off
Fat okara powder.
Dietary fiber extraction apparatus one include reactor 29, centrifuge 2 10 and washer 1, and reactor 29 has
Feed pipe 2 12, feed tube 2 13, feed tube 3 14 and discharge nozzle 2 15, the solid outlet of centrifuge 1 is twisted by conveying
Dragon 2 16 is connected with the feed pipe 2 12 of reactor 29, and feed tube 2 13 is connected with buffering flow container 17, and buffering flow container 17 is provided with out
Liquid valve and liquid pump, contain buffer in buffering flow container 17, feed tube 3 14 is connected with alkali liquid tank 18, and alkali liquid tank 18 is provided with liquid valve
And liquid pump, alkali liquid tank 18 splendid attire 1mol/l naoh solution, the discharge nozzle 2 15 of reactor 29 connects the charging of centrifuge 2 10
Mouthful, the solid outlet of centrifuge 2 10 connects the charging aperture of washer 1；Under the transmission of conveying auger 2 16, defat bean
Ground-slag falls into reactor 29 through feed pipe 2 12, and after the liquid valve of buffering flow container 17 and liquid pump unlatching, buffer is through feed tube
After 2 13 inflow reactors 29, the liquid valve of alkali liquid tank 18 and liquid pump are opened, naoh solution flows into reaction through feed tube 3 14
Kettle 29, the ph value making solution in reactor 29 is 8～10.The obtained extraction in the presence of alkaline solution of defatted bean-dregs powder
Liquid mixture is passed through in centrifuge 2 10 through discharge nozzle 2 15 and is centrifuged, under the conditions of 5000～10000r/min centrifugation 10～
15min, obtains supernatant one and precipitate one, and precipitate one is rinsed with water in washer 1, obtains water after the later stage is dry
Insoluble dietary fiber.
Protein Extraction device includes reactor 3 19, centrifuge 3 20 and washer 2 21, reactor 3 19 have into
Liquid pipe 4 22, feed tube 5 23 and discharge nozzle 3 24, the liquid outlet of centrifuge 2 10 passes through the feed liquor of pipeline and reactor 3 19
Pipe 4 22 is connected, and feed tube 5 23 is connected with acid solution tank 25, contains acid solution in acid solution tank 25, and acid solution tank 25 is provided with liquid valve
And liquid pump, the charging aperture of the discharge nozzle 3 24 connection centrifuge 3 20 of reactor 3 19, the solid outlet of centrifuge 3 20 is even
Connect the charging aperture of washer 2 21；The supernatant one that centrifuge 2 10 centrifugation obtains is passed through reactor 3 19 from feed tube 4 22
Interior, acid solution is passed through in reactor 3 19 from feed tube 5 23, and it is 4～5 that solution in reactor 3 19 is adjusted ph value, standing
After 4～5 hours, open the discharge nozzle 3 24 of reactor 3 19, so that mixed liquor is entered in centrifuge 3 20,5000～
It is centrifuged 10～15min under the conditions of 10000r/min, obtain supernatant two and precipitate two, precipitate two is used in washer 2 21
Water rinses, and obtains protein after the later stage is dry.
Dietary fiber extraction apparatus two include reactor 4 26, centrifuge 4 27 and washer 3 28, and reactor 4 26 has
There are feed tube 6 29, feed tube 7 30 and discharge nozzle 4 31, the liquid outlet of centrifuge 3 20 passes through pipeline and reactor 4 26
Feed tube 6 29 is connected, and feed tube 7 30 is connected with alcohol tank 32, and alcohol tank 32 is provided with liquid valve and liquid pump, contains ethanol in alcohol tank 32
Solution, the discharge nozzle 4 31 of reactor 4 26 connects the charging aperture of centrifuge 4 27, and the solid outlet of centrifuge 4 27 connects
The charging aperture of washer 3 28.The supernatant two that centrifuge 3 20 centrifugation obtains is passed through reactor 4 26, second from feed tube 6 29
Alcoholic solution is passed through in reactor 4 26 from feed tube 7 30, stands 24 hours at room temperature, and that opens reactor 4 26 goes out liquid
Guan Si, makes mixed liquor enter in centrifuge 4 27, is centrifuged 10～15min, obtains supernatant under the conditions of 5000～10000r/min
Liquid three and precipitate three, precipitate three is rinsed with water in washer 3 28, obtains water soluble dietary fiber after the later stage is dry.Excellent
Selection of land, the discharging opening of pulverizer 1 is located at the bottom of pulverizer 1, and this discharging opening is provided with outlet valve, after outlet valve is opened, pulverizes
Okara powder in machine 1 falls in conveying auger 1.
Conveying auger 1 includes base 33, charging pipeline section 34 and feeding pipeline section 35, and it is rotatable that feeding pipeline section 35 passes through bearing
Be connected to base 33, charging pipeline section 34 is connected with feeding pipeline section 35 and is rotatably connected by flange bearing, charging pipeline section
34 underfaces being vertically situated at pulverizer 1, the upper end opening of charging pipeline section 34 is the charging aperture of conveying auger 1, enters
The upper end of expects pipe section 34 is connected with the outlet valve of pulverizer 1, and feeding pipeline section 35 tilts to reactor 1 from bottom to up, send
The upper end opening of expects pipe section 35 is the discharging opening of conveying auger 1, the charging of the upper end of feeding pipeline section 35 and reactor 1
Pipe 1 passes through flange and is connected；Okara powder first falls into the charging pipeline section 34 of conveying auger 1, then falls into from charging pipeline section 34 and send
Expects pipe section 35.
Feeding pipeline section 35 includes delivery pipe body 36, is provided with screw-conveyer-shaft 37 in delivery pipe body 36, and screw-conveyer-shaft 37 is controlled by motor,
Motor drive screw-conveyer-shaft 37 rotates, and the outer concentric gap of delivery pipe body 36 is arranged with thermal sleeve 38 to carry out thermal insulation, delivery pipe body
Form heating chamber, heating intracavity compartment of terrain is provided with the electric heating piece 39 being sequentially connected electrically, electric heating piece 39 between 36 and thermal sleeve 38
It is attached to the outer surface of delivery pipe body 36.Generate heat after electric heating piece 39 energising, thus heated transportation body 36, make in delivery pipe body 36
Temperature raises, and with the rotation of screw-conveyer-shaft 37, okara powder not only can be transferred into reactor 1, and okara powder is in transmission
During obtain drying, without using extra drying mechanism, simplify work with delivery pipe body 36 contact internal walls, wet okara powder
Sequence.
Preferably, above the discharging opening of pulverizer 1, screen cloth 40 is removably installed, okara powder is controlled by screen cloth 40
Grain size, screen cloth 40 is preferably 80 mesh sieves.Feeding pipeline section 35 has air inlet, and air inlet is connected with pressure fan 41, screw-conveyer-shaft
37 when conveying okara powder, can open pressure fan 41, introduces air, from inlet charge, air enters in delivery pipe body 36
When obtain heating, can accelerate after hot air okara powder okara powder be dried.
Reactor 1 includes reaction kettle body 1 and lid 1, and lid 1 lid is located on reaction kettle body 1, reaction
The upper end open of kettle, feed pipe 1 and feed tube 1 are fixedly arranged on lid 1, and connect with reaction kettle body 1 respectively, go out
Located at the bottom of reaction kettle body 1, the okara powder being dried is delivered to feed pipe 1 to expects pipe one by conveying auger 1, and passes through
Feed pipe 1 falls in reaction kettle body 1.It is provided with temperature sensor 44 in reaction kettle body 1, detect reactor for the moment
Temperature in one 3, temperature sensor 44 connects temperature indicator 45, and temperature indicator 45 is installed in the appearance of reaction kettle body 1
Face, operator can learn reaction temperature from temperature indicator 45.It is noted that the extraction temperature of reactor 1 is preferred
For 50 DEG C, the mode using conveying auger 1 to reactor 1 conveying heat is internally heated to reactor 1, that is,
After okara powder is delivered in reactor 1 conveying auger 1, electric heating piece 39 remains powered on, and continues heating to delivery pipe body 36,
Pressure fan 41 is passed through air into conveying auger 1, and air flows to reactor 1 along delivery pipe body 36, and heat is carried
Enter so that reactor 1 internal temperature raises in reactor 1, and the pressure of reactor 1 also raises, contribute to soaking
Propose reaction.
Exhaustor 46 is additionally provided with lid 1, exhaustor 46 is connected with relief valve, certain when reaching in reactor 1
During pressure, open relief valve, so that the gas in reactor 1 is discharged from exhaustor 46, carry out pressure release and avoid reacting
Kettle 1 temperature rises to too high.Reactor 1 also has rabbling mechanism 47, and rabbling mechanism 47 includes being installed on lid 1
Motor and the shaft stretching in reaction kettle body 1, shaft has multiple stirring vanes, and shaft is in bending, to increase
The contact area of stirring, the upper end of shaft is connected with the output through-drive of motor by shaft coupling, Motor drive shaft
Rotate；Conveying auger 2 16 is identical with the structure of conveying auger 1, also includes feeding pipeline section 34 and feeding pipeline section 35, wherein send
Expects pipe section 35 has heating function, and in addition to charging pipeline section 34 can not open up air inlet, other structures are all identical, centrifuge one
4 centrifugations obtain bean dregs grouts, after bean dregs grouts enter in conveying auger 2 16, are not only dried, and are broken up with rotating
Become defatted bean-dregs powder, be then transported into reactor 29.This system also includes waste liquid pool 84, and the liquid outlet of centrifuge 1 is even
Connect waste liquid pool 84, the liquid that centrifuge 1 centrifugation produces is directly discharged into waste liquid pool 84.
Reactor 29 includes reaction kettle body 2 48 and lid 2 49, and lid 2 49 lid is located on reaction kettle body 2 48, reaction
The upper end open of kettle 2 48, feed pipe 2 12, feed tube 2 13 and feed tube 3 14 are fixedly arranged on lid 2 49, discharge nozzle respectively
2 15 are connected with feed pipe 2 12 flange of reactor 29 located at the bottom of reaction kettle body 2 48, the discharging opening of conveying auger 2 16
Connect, buffer is phosphate buffer；Reaction kettle body 2 48 is externally provided with supersonic generator 50, and supersonic generator 50 connects ultrasonic
Ripple probe 51, ultrasound probe 51 is in reaction kettle body 2 48, and reactor 29 adopts ultrasonic assistant to extract, ultrasonic power
200-700w, is additionally provided with temperature sensor 44 in reaction kettle body 2 48, for detecting the reaction temperature of reactor 29, reaction temperature
Degree is preferably 30-70 DEG C, and temperature sensor 44 connects temperature indicator 45, and temperature indicator 45 is installed in reaction kettle body 2 48
Outer surface.
Air inlet pipe 52 is additionally provided with reaction kettle body 2 48, the outer end of air inlet pipe 52 is in outside reaction kettle body 2 48, air inlet pipe
52 the inner is in reaction kettle body 2 48, and the outer end of air inlet pipe 52 is connected with intake valve, and the inner of air inlet pipe 52 connects jet
Pipe 53, air jet pipe 53 is in bending, and the side wall phase of air jet pipe 53 and reaction kettle body 2 48 is fixed, and adjacent to reaction kettle body 2 48
Bottom, the both sides up and down of air jet pipe 53 are respectively provided with row's nozzle 54；Intake valve can be connected with pressure fan 41 by pipeline, air inlet
Valve is opened, and pressure fan 41 supplies, and gas is passed through air jet pipe 53 from air inlet pipe 52, in extraction process, the one of air jet pipe 53 upside
Gas is sprayed in mixed liquor so that mixed liquor is carried out with bubbling by row's nozzle 54 upwards, promotes the flowing up and down of mixed liquor, or enters
Air valve is connected with the relief valve of reactor 1 by pipeline, and the gas with heat discharged in reactor 1 is used for reacting
In kettle 29, not only promote the flowing of mixed liquor, and be carried along into heat, certain heating is served to reactor 29
Effect.When mixed liquor in reactor 29 is passed through centrifuge 1, using the row's nozzle 54 on the downside of exhaustor 5346 to mixed
Close liquid to be blown downwards, so that mixing liquid energy is all flowed in centrifuge 1.
Additionally, liquid flowing tube 1 is additionally provided with reaction kettle body 2 48, a certain amount of mixed liquor is taken out by liquid flowing tube 1,
The ph value of detection mixed liquor.
Dietary fiber extraction apparatus one also include fluid reservoir 1, and fluid reservoir 1 has inlet and liquid outlet, liquid storage
Tank 1 is arranged between centrifuge 2 10 and reactor 3 19, and lid 2 49 is additionally provided with feed tube 8 57, centrifuge 2 10
Liquid outlet be connected with the inlet of fluid reservoir 1, the liquid outlet of fluid reservoir 1 is provided with liquid pump and three-way valve 1, and this three
The one outlet of port valve 1 passes through the feed tube 8 57 of pipeline coupled reaction kettle 29, another outlet of this three-way valve 1
Feed tube 4 22 by pipeline coupled reaction kettle 3 19.The supernatant one producing after centrifuge 2 10 centrifugation is expelled to fluid reservoir
One 56 it is preferable that needing to be centrifuged through multiple, that is, open liquid pump and the three-way valve 1 of fluid reservoir 1, make three-way valve 1
Connect with feed tube 8 57, the supernatant one in fluid reservoir 1 is refilled in reactor 29 by feed tube 8 57, so
After be again introduced into centrifuge 2 10 and be centrifuged, improve centrifugal mass, improve the extracted amount of precipitate one.Finally, by three-way valve
One 58 are connected with feed tube 4 22, and the supernatant one of last centrifugation gained is injected in reactor 3 19 by feed tube 4 22
Carry out the extraction of protein.
Washer 1 introversion is tiltedly provided with filter membrane 1, and filter membrane 1 is detachably secured to washer one by support
11 inwall, filter membrane 1 lower section is filtering area 60, and filter membrane 1 top is spray area 61, and the inwall in spray area 61 is installed with many
Individual shower 62, shower 62 is connected with deionization water pot 63, and the charging aperture of washer 1 is opened in the upper end in spray area 61
Portion, the discharging opening of washer 1 is opened on the side wall in spray area 61, and the bottom of filtering area 60 offers liquid outlet, liquid outlet
Connect waste liquid pool 84；The aperture of filter membrane 1 is less than the particle diameter of precipitate one, can intercept precipitate one in spray area 61, but
Can pass through for deionized water.Centrifuge 2 10 centrifugation produce precipitate one enter washer 1 spray area 61 in, go from
Sub- water pot 63 is provided with liquid pump, and deionization water pot 63 provides deionized water to shower 62, after shower 62 is opened, by deionized water
On precipitate one, to rinse out the impurity substances of precipitate one remained on surface, deionization passes through filter membrane 1, stream to spray simultaneously
Enter filtering area 60, and be expelled to waste liquid pool 84 from liquid outlet.
The discharging opening of washer 1 connects the charging aperture of conveying auger 3 64, and conveying auger 3 64 includes delivery pipe body two
65, it is provided with screw-conveyer-shaft 37 in delivery pipe body 2 65, screw-conveyer-shaft 37 is controlled by motor, Motor drive screw-conveyer-shaft 37 rotates, delivery pipe
The outer concentric gap of body 2 65 is arranged with thermal sleeve 2 66, forms heating chamber between delivery pipe body 2 65 and thermal sleeve 2 66,
Heating intracavity compartment of terrain is provided with the electric heating piece 39 being sequentially connected electrically, and electric heating piece 39 is attached to the outer surface of delivery pipe body 2 65, defeated
The discharging opening sending auger 3 64 connects water insoluble dietary fiber Material collecting box for harvesting 67.After the completion of precipitate one rinses, open washer
One 11 discharging opening, because filter membrane 1 is to be obliquely installed, precipitate one is slid downwardly into conveying auger 3 64 along filter membrane 1
Interior, precipitate one is transmitted by screw-conveyer-shaft 37 to water insoluble dietary fiber Material collecting box for harvesting 67 direction, in transmit process, delivery pipe body
Electric heating piece 39 heating power on 2 65 surfaces, heats to delivery pipe body 2 65, thus by the precipitation in delivery pipe body 2 65
Thing one is dried, and the precipitate one falling into water insoluble dietary fiber Material collecting box for harvesting 67 is dry water insoluble dietary fiber.
Reactor 3 19 includes reaction kettle body 3 68 and lid 3 69, and lid 3 69 lid is located on reaction kettle body 3 68, instead
Answer the upper end open of kettle 3 68, feed tube 4 22 and feed tube 5 23 to be fixedly arranged on lid 3 69, and respectively with reaction kettle body three
68 connections, the side wall of reaction kettle body 3 68 is provided with liquid flowing tube 2 70, is easy to take out a certain amount of mixed liquor, to detect its ph value.
Reactor 3 19 also includes rabbling mechanism 47, the knot of the rabbling mechanism 47 of reactor 3 19 and the rabbling mechanism 47 of reactor 1
Structure can be identical, and rabbling mechanism 47 includes the motor being installed on lid 3 69 and the shaft stretching in reaction kettle body 3 68, stirs
Mixing has multiple stirring vanes on axle, the upper end of shaft is connected with the output through-drive of motor by shaft coupling.Discharge nozzle three
24 bottoms being provided with reaction kettle body 3 68, drain pipe are connected with liquid valve, the lower section of reaction kettle body 3 68 is centrifuge 3 20,
Reactor 3 19 also includes fluid reservoir 2 71, and fluid reservoir 2 71 has inlet and liquid outlet, and fluid reservoir 2 71 is arranged on centrifugation
Between machine 3 20 and reactor 4 26, the liquid outlet of centrifuge 3 20 is connected with the inlet of fluid reservoir 2 71, fluid reservoir 2 71
Liquid outlet be provided with liquid pump and three-way valve 2 72, the one outlet of three-way valve 2 72 passes through the feed liquor of pipeline coupled reaction kettle 3 19
Pipe 4 22, another outlet feed tube 6 29 by pipeline coupled reaction kettle 4 26 of three-way valve 2 72；Centrifuge 3 20 from
The supernatant two producing after the heart is expelled to fluid reservoir 2 71 it is preferable that needing to be centrifuged through multiple, that is, open fluid reservoir 2 71
Liquid pump and three-way valve 2 72, make three-way valve 2 72 connect with feed tube 4 22, by the supernatant two in fluid reservoir 2 71 pass through into
Liquid pipe 4 22 refills in reactor 3 19, is then again introduced into centrifuge 3 20 and is centrifuged, and improves centrifugal mass, improves
The extracted amount of precipitate two.Finally, three-way valve 2 72 is connected with feed tube 6 29, by the last supernatant two-way being centrifuged gained
Cross feed tube 6 29 and be injected into the extraction carrying out water soluble dietary fiber in reactor 4 26.
Washer 2 21 introversion is tiltedly provided with filter membrane 2 73, and filter membrane 2 73 is detachably secured to washer two by support
21 inwall, filter membrane 2 73 lower section is filtering area 60, and filter membrane 2 73 top is spray area 61, and the inwall in spray area 61 is installed with many
Individual shower 62, shower 62 is connected with deionization water pot 63, and the charging aperture of washer 2 21 is opened in the upper end in spray area 61
Portion, the discharging opening of washer 2 21 is opened on the side wall in spray area 61, and the bottom of filtering area 60 offers liquid outlet, liquid outlet
Connect waste liquid pool 84.Beyond the filter membrane 2 73 of washer 2 21 is different with the aperture of the filter membrane 1 of washer 1, washer
2 21 other structures all can be identical with the other structures of washer 1, and the aperture of filter membrane 2 73 is less than the grain of precipitate two
Footpath, can intercept precipitate two in spray area 61, but can pass through for deionized water.The precipitate that centrifuge 3 20 centrifugation produces
In the spray area 61 of two entrance washers 2 21, deionization water pot 63 is provided with liquid pump, and deionization water pot 63 provides to shower 62
Deionized water, after shower 62 is opened, deionized water is sprayed on precipitate two, to rinse out precipitate two remained on surface
Impurity substances, simultaneously deionization pass through filter membrane 2 73, flow into filtering area 60, and be expelled to waste liquid pool 84 from liquid outlet.
The discharging opening of washer 2 21 connects the charging aperture of conveying auger 4 74, and the structure of conveying auger 4 74 and conveying twist
The structure of dragon 3 64 is identical, and conveying auger 4 74 includes delivery pipe body 2 65, is provided with screw-conveyer-shaft 37, auger in delivery pipe body 2 65
Axle 37 is controlled by motor, and the outer concentric gap of delivery pipe body 2 65 is arranged with thermal sleeve 2 66, delivery pipe body 2 65 and collet
Form heating chamber, heating intracavity compartment of terrain is provided with the electric heating piece 39 being sequentially connected electrically, and electric heating piece 39 is attached to defeated between pipe 2 66
Send the outer surface of body 2 65, the discharging opening of conveying auger 4 74 connects protein Material collecting box for harvesting 75.After the completion of precipitate two rinses,
Open the discharging opening of washer 2 21, because filter membrane 2 73 is to be obliquely installed, precipitate two is slid downwardly into defeated along filter membrane 2 73
Send in auger 4 74, precipitate two is transmitted by screw-conveyer-shaft 37 to protein Material collecting box for harvesting 75 direction, in transmit process, delivery pipe body
Electric heating piece 39 heating power on 2 65 surfaces, heats to delivery pipe body 2 65, thus by the precipitation in delivery pipe body 2 65
Thing two is dried, and the precipitate one falling into protein fibre Material collecting box for harvesting is dry protein.
A fixed dividing plate 76 in reactor 4 26, dividing plate 76 separates reactor 4 26 for upper reative cell 77 and lower reative cell
78, be provided with a filter bag 79 in upper reative cell 77, filter bag 79 is made up of filter membrane three, the micropore on filter membrane three surface can only allow water and
Small-molecule substance passes through, and volume is trapped within filter bag 79 more than the macromolecular substances of micropore and becomes concentrated solution, on filter bag 79
Portion's opening, feed tube 6 29 is installed in the top of reactor 4 26, and feed tube 6 29 penetrates the upper opening of filter bag 79, filter bag 79
Bottom connect discharge nozzle 5 80, discharge nozzle 5 80 wears dividing plate 76 and stretches into lower reative cell 78, and the side wall of upper reative cell 77 is even
It is connected to discharging tube 81, discharging tube 81 is connected with liquid pump；Feed tube 7 30 is installed in the side wall of lower reative cell 78, drain pipe four located at
The bottom of lower reative cell 78, the supernatant two that centrifuge 3 20 produces is injected in filter bag 79 by feed tube 6 29, opens simultaneously
Discharging tube 81, the water passing from filter bag 79 and small-molecule substance are discharged from discharging tube 81, form concentrated solution, open in filter bag 79
Open the discharge nozzle 5 80 of filter bag 79 bottom, concentrated solution enters into lower reative cell 78 by discharge nozzle 5 80, is then turned on feed tube
7 30, it is passed through ethanol solution in downward reative cell 78, after standing 24 hours under room temperature, open drain pipe four, by lower reative cell 78
Interior mixed liquor is passed through centrifuge 4 27.
In lower reative cell 78, rabbling mechanism 47 can be set, rabbling mechanism 47 includes being fixedly arranged on the motor of reactor 4 26 side wall
With the shaft of horizontally set, one end of shaft is connected with motor by shaft coupling, can be to lower reaction by rabbling mechanism 47
Mixed liquor in room 78 carries out agitation as appropriate, promotes to extract.Dietary fiber extraction apparatus two also include fluid reservoir 3 82, centrifuge
4 27 liquid outlet is connected with the inlet of fluid reservoir 3 82, and the liquid outlet of fluid reservoir 3 82 is provided with liquid pump and three-way valve 3 83,
The one outlet of three-way valve 3 83 connects the feed tube 6 29 of upper reative cell 77, another outlet of three-way valve 3 83 by pipeline
Waste liquid pool 84 is connected by pipeline；The supernatant three producing after centrifuge 4 27 centrifugation is expelled to fluid reservoir 3 82 it is preferable that needing
To be centrifuged through multiple, that is, to open liquid pump and the three-way valve 3 83 of fluid reservoir 3 82, make three-way valve 3 83 with feed tube 6 29 even
Logical, the supernatant three in fluid reservoir 3 82 is refilled in reactor 4 26 by feed tube 6 29, be then again introduced into from
Scheming 4 27 is centrifuged, and improves centrifugal mass, improves the extracted amount of precipitate three.Finally, by three-way valve 3 83 and waste liquid pool
84 connections, the supernatant three of last centrifugation gained is entered waste liquid pool 84.
Washer 3 28 introversion is tiltedly provided with filter membrane 4 85, and filter membrane 4 85 is detachably secured to washer three by support
28 inwall, filter membrane 4 85 lower section is filtering area 60, and filter membrane 4 85 top is spray area 61, and the inwall in spray area 61 is installed with many
Individual shower 62, shower 62 is connected with deionization water pot 63, and the charging aperture of washer 3 28 is opened in the upper end in spray area 61
Portion, the discharging opening of washer 3 28 is opened on the side wall in spray area 61, and the bottom of filtering area 60 offers liquid outlet, liquid outlet
Connect waste liquid pool 84；Beyond the filter membrane 4 85 of washer 3 28 is different with the aperture of the filter membrane 1 of washer 1, washer
3 28 other structures all can be identical with the other structures of washer 1, and the aperture of filter membrane 4 85 is less than the grain of precipitate three
Footpath, can intercept precipitate three in spray area 61, but can pass through for deionized water.The precipitate that centrifuge 4 27 centrifugation produces
In the spray area 61 of three entrance washers 3 28, deionization water pot 63 is provided with liquid pump, and deionization water pot 63 provides to shower 62
Deionized water, after shower 62 is opened, deionized water is sprayed on precipitate three, to rinse out precipitate three remained on surface
Material, simultaneously deionization pass through filter membrane 4 85, flow into filtering area 60, and be expelled to waste liquid pool 84 from liquid outlet.
The discharging opening of washer 3 28 connects the charging aperture of conveying auger 5 86, and the structure of conveying auger 5 86 and conveying twist
The structure of dragon 3 64 is identical, and conveying auger 5 86 includes delivery pipe body 2 65, is provided with screw-conveyer-shaft 37, auger in delivery pipe body 2 65
Axle 37 is controlled by motor, and the outer concentric gap of delivery pipe body 2 65 is arranged with thermal sleeve 2 66, delivery pipe body 2 65 and collet
Form heating chamber, heating intracavity compartment of terrain is provided with the electric heating piece 39 being sequentially connected electrically, and electric heating piece 39 is attached to defeated between pipe 2 66
Send the outer surface of body 36, the discharging opening of conveying auger 5 86 connects water soluble dietary fiber Material collecting box for harvesting 87.Precipitate three rinses
After the completion of, open the discharging opening of washer 3 28, because filter membrane 4 85 is to be obliquely installed, precipitate three is downward along filter membrane 4 85
Slip in conveying auger 4 74, precipitate four-way water soluble dietary fiber Material collecting box for harvesting 87 direction is transmitted by screw-conveyer-shaft 37, in transmission
During, electric heating piece 39 heating power on delivery pipe body 2 65 surface, delivery pipe body 2 65 is heated, thus by delivery pipe
Precipitate three in body 2 65 is dried, and the precipitate one falling into water soluble dietary fiber Material collecting box for harvesting 87 is dry water solublity
Dietary fiber.
Specific embodiment described herein is only explanation for example to present invention spirit.The affiliated technology of the present invention is led
The technical staff in domain can be made various modifications or supplement or replaced using similar mode to described specific embodiment
Generation, but the spirit without departing from the present invention or surmount scope defined in appended claims.
Although more employing pulverizer 1 herein；Conveying auger 1；Reactor 1；Centrifuge 1；Feed pipe one
5；Feed tube 1；Discharge nozzle 1；Extraction flow container 8；Reactor 29；Centrifuge 2 10；Washer 1；Feed pipe 2 12；Enter
Liquid pipe 2 13；Feed tube 3 14；Discharge nozzle 2 15；Conveying auger 2 16；Buffering flow container 17；Alkali liquid tank 18；Reactor 3 19；From
Scheming 3 20；Washer 2 21；Feed tube 4 22；Feed tube 5 23；Discharge nozzle 3 24；Acid solution tank 25；Reactor 4 26；Centrifugation
Machine 4 27；Washer 3 28；Feed tube 6 29；Feed tube 7 30；Discharge nozzle 4 31；Alcohol tank 32；Base 33；Charging pipeline section 34；
Feeding pipeline section 35；Delivery pipe body 36；Screw-conveyer-shaft 37；Thermal sleeve 38；Electric heating piece 39；Screen cloth 40；Pressure fan 41；Reaction kettle body one
42；Lid 1；Temperature sensor 44；Temperature indicator 45；Exhaustor 46；Rabbling mechanism 47；Reaction kettle body 2 48；Lid two
49；Supersonic generator 50；Ultrasound probe 51；Air inlet pipe 52；Air jet pipe 53；Nozzle 54；Liquid flowing tube 1；Fluid reservoir one
56；Feed tube 8 57；Three-way valve 1；Filter membrane 1；Filtering area 60；Spray area 61；Shower 62；Deionization water pot 63；Defeated
Send auger 3 64；Delivery pipe body 2 65；Thermal sleeve 2 66；Water insoluble dietary fiber Material collecting box for harvesting 67；Reaction kettle body 3 68；Lid
Body 3 69；Liquid flowing tube 2 70；Fluid reservoir 2 71；Three-way valve 2 72；Filter membrane 2 73；Conveying auger 4 74；Protein Material collecting box for harvesting 75；
Dividing plate 76；Upper reative cell 77；Lower reative cell 78；Filter bag 79；Discharge nozzle 5 80；Discharging tube 81；Fluid reservoir 3 82；Three-way valve three
83；Waste liquid pool 84；Filter membrane 4 85；Conveying auger 5 86；Water soluble dietary fiber Material collecting box for harvesting 87 grade term, but be not precluded from using
The probability of other terms.It is used for the purpose of more easily describing and explaining the essence of the present invention using these terms；Them
It is all contrary with spirit of the present invention for being construed to any additional restriction.
Claims (10)
1. a kind of system extracting dietary fiber and protein is it is characterised in that include pretreating device, the defat being sequentially connected
Device, dietary fiber extraction apparatus one, Protein Extraction device and dietary fiber extraction apparatus two；Pretreating device includes pulverizing
Machine and conveying auger one, the discharging opening of pulverizer connects the charging aperture of conveying auger one；Degreasing plant include reactor one and from
Scheming one, reactor one has feed pipe one, feed tube one and discharge nozzle one, and feed tube one is connected with extraction flow container, lixiviating solution
Lixiviating solution, the feed pipe one of the discharging opening coupled reaction kettle one of conveying auger one is contained, the discharge nozzle one of reactor one is even in tank
Connect the charging aperture of centrifuge one；Dietary fiber extraction apparatus one include reactor two, centrifuge two and washer one, reactor two
There is feed pipe two, feed tube two, feed tube three and discharge nozzle two, the solid outlet of centrifuge one pass through conveying auger two with
The feed pipe two of reactor two is connected, and feed tube two is connected with buffering flow container, contains buffer in buffering flow container, feed tube three and
Alkali liquid tank is connected, and alkali liquid tank contains naoh solution, and the discharge nozzle two of reactor two connects the charging aperture of centrifuge two, centrifuge two
Solid outlet connect washer one charging aperture；Protein Extraction device includes reactor three, centrifuge three and washer
Two, reactor three has feed tube four, feed tube five and discharge nozzle three, and the liquid outlet of centrifuge two passes through pipeline and reactor three
Feed tube four be connected, feed tube five is connected with acid solution tank, contains acid solution, discharge nozzle three company of reactor three in acid solution tank
Connect the charging aperture of centrifuge three, the solid outlet of centrifuge three connects the charging aperture of washer two；Dietary fiber extraction apparatus
Two include reactor four, centrifuge four and washer three, and reactor four has feed tube six, feed tube seven and discharge nozzle four, from
The liquid outlet of scheming three is connected with the feed tube six of reactor four by pipeline, and feed tube seven is connected with alcohol tank, contains in alcohol tank
Ethanol, the discharge nozzle four of reactor four connects the charging aperture of centrifuge four, and the solid outlet of centrifuge four connects washer three
Charging aperture.
2. the system extracting dietary fiber and protein according to claim 1 is it is characterised in that the discharging opening of pulverizer
Positioned at the bottom of pulverizer, this discharging opening is provided with outlet valve；Conveying auger one includes base, charging pipeline section and feeding pipeline section,
Feeding pipeline section is rotatably connected at base by bearing, and charging pipeline section is connected with feeding pipeline section and passes through flange bearing and can turn
It is dynamically connected, charging pipeline section is vertically situated at the underface of pulverizer, and the upper end opening of charging pipeline section is conveying auger one
Charging aperture, the upper end of charging pipeline section is connected with the outlet valve of pulverizer, and feeding pipeline section tilts to reactor one from bottom to up,
The upper end opening of feeding pipeline section is the discharging opening of conveying auger one, the feed pipe one of the upper end of feeding pipeline section and reactor one
It is connected by flange；Feeding pipeline section includes delivery pipe body, is provided with screw-conveyer-shaft in delivery pipe body, and screw-conveyer-shaft is controlled by motor, conveying
The outer concentric gap of body is arranged with thermal sleeve, forms heating chamber, heat intracavity compartment of terrain between delivery pipe body and thermal sleeve
It is provided with the electric heating piece being sequentially connected electrically, electric heating piece is attached to the outer surface of delivery pipe body.
3. the system extracting dietary fiber and protein according to claim 2 is it is characterised in that the discharging opening of pulverizer
Top is removably provided with screen cloth；Feeding pipeline section has air inlet, and air inlet is connected with pressure fan.
4. the system of extraction dietary fiber according to claim 2 and protein is it is characterised in that reactor one includes instead
Answer kettle one and lid one, lid one lid is located on reaction kettle body one, and feed pipe one and feed tube one are fixedly arranged on lid one, and point
Do not connect with reaction kettle body one, discharge nozzle one is located at the bottom of reaction kettle body one；It is provided with temperature sensor, temperature in reaction kettle body one
Degree sensor connects temperature indicator, and temperature indicator is installed in the outer surface of reaction kettle body one；It is additionally provided with aerofluxuss on lid one
Pipe, exhaustor is connected with relief valve.
5. the system of extraction dietary fiber according to claim 4 and protein is it is characterised in that reactor one also has
Rabbling mechanism, rabbling mechanism includes the motor being installed on lid one and the shaft stretching in reaction kettle body one, on shaft
There are multiple stirring vanes, shaft is in bending, and the upper end of shaft is connected with the output through-drive of motor by shaft coupling；
Conveying auger two is identical with the structure of conveying auger one.
6. the system of extraction dietary fiber according to claim 4 and protein is it is characterised in that reactor two includes instead
Answer kettle two and lid two, lid two lid is located on reaction kettle body two, and feed pipe two, feed tube two and feed tube three are fixed respectively
In lid two, discharge nozzle two located at the bottom of reaction kettle body two, the feed pipe two of the discharging opening of conveying auger two and reactor two
Flange connects；Reaction kettle body two is externally provided with supersonic generator, and supersonic generator connects ultrasound probe, at ultrasound probe
In reaction kettle body two, in reaction kettle body two, it is additionally provided with temperature sensor, temperature sensor connects temperature indicator, temperature shows
Device is installed in the outer surface of reaction kettle body two.
7. the system extracting dietary fiber and protein according to claim 6 is it is characterised in that go back on reaction kettle body two
It is provided with air inlet pipe, the outer end of air inlet pipe is in outside reaction kettle body two, and the inner of air inlet pipe is in reaction kettle body two, air inlet pipe
Outer end is connected with intake valve, and intake valve is connected with the relief valve of pressure fan or reactor one by pipeline, the inner of air inlet pipe
Connect air jet pipe, air jet pipe is in bending, the side wall phase of air jet pipe and reaction kettle body two is fixed, and adjacent to reaction kettle body two
Bottom, the both sides up and down of air jet pipe are respectively provided with row's nozzle；Liquid flowing tube one is additionally provided with reaction kettle body two；Dietary fiber extracts dress
Put one and also include fluid reservoir one, fluid reservoir one has inlet and liquid outlet, fluid reservoir one is arranged on centrifuge two and reactor
Between three, lid two is additionally provided with feed tube eight, the liquid outlet of centrifuge two is connected with the inlet of fluid reservoir one, fluid reservoir one
Liquid outlet be provided with liquid pump and three-way valve one, the one outlet of this three-way valve one passes through the feed tube of pipeline coupled reaction kettle two
Eight, another outlet feed tube four by pipeline coupled reaction kettle three of this three-way valve one；Washer one introversion is tiltedly provided with
Filter membrane one, filter membrane one is detachably secured to the inwall of washer one by support, and filter membrane one lower section is filtering area, on filter membrane one
Side is spray area, and the inwall in spray area is installed with multiple showers, and shower is connected with deionization water pot, the charging of washer one
Mouth is opened in the upper end in spray area, and the discharging opening of washer one is opened on the side wall in spray area, and the bottom of filtering area opens up
There is liquid outlet；The discharging opening of washer one connects the charging aperture of conveying auger three, and conveying auger three includes delivery pipe body two, conveying
It is provided with screw-conveyer-shaft, screw-conveyer-shaft is controlled by motor, the outer concentric gap of delivery pipe body two is arranged with thermal sleeve two, conveying in body two
Form heating chamber, heating intracavity compartment of terrain is provided with the electric heating piece being sequentially connected electrically, electric heating piece between body two and thermal sleeve two
It is attached to the outer surface of delivery pipe body two, the discharging opening of conveying auger three connects water insoluble dietary fiber Material collecting box for harvesting.
8. the system of extraction dietary fiber according to claim 1 and protein is it is characterised in that reactor three includes instead
Answer kettle three and lid three, lid three lid is located on reaction kettle body three, and feed tube four and feed tube five are fixedly arranged on lid three, and point
Not and reaction kettle body tee joint, the side wall of reaction kettle body three is provided with liquid flowing tube two；Discharge nozzle three located at the bottom of reaction kettle body three,
The lower section of reaction kettle body three is centrifuge three, and Protein Extraction device also includes fluid reservoir two, fluid reservoir two have inlet and
Liquid outlet, fluid reservoir two is arranged between centrifuge three and reactor four, the feed liquor of the liquid outlet of centrifuge three and fluid reservoir two
Mouth connects, and the liquid outlet of fluid reservoir two is provided with liquid pump and three-way valve two, and the one outlet of three-way valve two passes through pipeline coupled reaction
The feed tube four of kettle three, another outlet feed tube six by pipeline coupled reaction kettle four of three-way valve two；In washer two
Obliquely it is provided with filter membrane two, filter membrane two is detachably secured to the inwall of washer two by support, and filter membrane two lower section is for filtering
Area, filter membrane two top is spray area, and the inwall in spray area is installed with multiple showers, and shower is connected with deionization water pot, punching
The charging aperture of washing machine two is opened in the upper end in spray area, and the discharging opening of washer two is opened on the side wall in spray area, filters
The bottom in area offers liquid outlet；The discharging opening of washer two connects the charging aperture of conveying auger four, and conveying auger four includes defeated
Send body two, in delivery pipe body two, be provided with screw-conveyer-shaft, screw-conveyer-shaft is controlled by motor, the outer concentric gap of delivery pipe body two be arranged with every
Thermal sleeve two, forms heating chamber between delivery pipe body two and thermal sleeve two, heating intracavity compartment of terrain is provided with and is sequentially connected electrically
Electric heating piece, electric heating piece is attached to the outer surface of delivery pipe body two, and the discharging opening of conveying auger four connects protein Material collecting box for harvesting.
9. the system of extraction dietary fiber according to claim 8 and protein is it is characterised in that reactor three also includes
Rabbling mechanism, rabbling mechanism includes the motor being installed on lid three and the shaft stretching in reaction kettle body three, on shaft
There are multiple stirring vanes, the upper end of shaft is connected with the output through-drive of motor by shaft coupling.
10. the system extracting dietary fiber and protein according to claim 1 is it is characterised in that consolidate in reactor four
If a dividing plate, reactor four is separated as upper reative cell and lower reative cell by dividing plate, and upper reaction interior is provided with a filter bag, and filter bag is by filtering
Film three forms, filter bag upper opening, and feed tube six is installed in the top of reactor four, and the top that feed tube six penetrates filter bag is opened
Mouthful, the bottom of filter bag connects discharge nozzle five, and discharge nozzle five wears dividing plate and stretches into lower reative cell, and the side wall of upper reative cell is connected with
Discharging tube, discharging tube is connected with liquid pump；Feed tube seven is installed in the side wall of lower reative cell, and discharge nozzle four is located at the bottom of lower reative cell
Portion；Dietary fiber extraction apparatus two also include fluid reservoir three, and the liquid outlet of centrifuge four is connected with the inlet of fluid reservoir three, storage
The liquid outlet of flow container three is provided with liquid pump and three-way valve three, and the one outlet of three-way valve three connects the feed liquor of upper reative cell by pipeline
Pipe six, another outlet of three-way valve three connects waste liquid pool by pipeline；Washer three introversion is tiltedly provided with filter membrane four, filter membrane four
It is detachably secured to the inwall of washer three by support, filter membrane four lower section is filtering area, filter membrane four top is spray area, spray
The inwall drenching area is installed with multiple showers, and shower is connected with deionization water pot, and the charging aperture of washer three is opened in spray
The upper end in area, the discharging opening of washer three is opened on the side wall in spray area, and the bottom of filtering area offers liquid outlet；Rinse
The discharging opening of machine three connects the charging aperture of conveying auger five, and conveying auger five includes delivery pipe body two, is provided with delivery pipe body two
Screw-conveyer-shaft, screw-conveyer-shaft is controlled by motor, and the outer concentric gap of delivery pipe body two is arranged with thermal sleeve two, delivery pipe body two and heat-insulated
Form heating chamber, heating intracavity compartment of terrain is provided with the electric heating piece being sequentially connected electrically, and electric heating piece is attached to delivery pipe between sleeve pipe two
The outer surface of body two, the discharging opening of conveying auger five connects water soluble dietary fiber Material collecting box for harvesting.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201611049810.1A CN106360746A (en) | 2016-11-23 | 2016-11-23 | Extraction system for dietary fibers and proteins |
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| CN201611049810.1A CN106360746A (en) | 2016-11-23 | 2016-11-23 | Extraction system for dietary fibers and proteins |
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Application publication date: 20170201 |