CN117101180B - Reverse driving opposite-impact type homogeneous leaching device and application thereof in purification of konjaku flour - Google Patents
Reverse driving opposite-impact type homogeneous leaching device and application thereof in purification of konjaku flour Download PDFInfo
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- CN117101180B CN117101180B CN202311389431.7A CN202311389431A CN117101180B CN 117101180 B CN117101180 B CN 117101180B CN 202311389431 A CN202311389431 A CN 202311389431A CN 117101180 B CN117101180 B CN 117101180B
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- 229920002752 Konjac Polymers 0.000 title claims abstract description 114
- 238000002386 leaching Methods 0.000 title claims abstract description 40
- 235000013312 flour Nutrition 0.000 title claims abstract description 31
- 238000000746 purification Methods 0.000 title claims abstract description 16
- 239000000843 powder Substances 0.000 claims abstract description 82
- 238000002156 mixing Methods 0.000 claims abstract description 26
- 230000007246 mechanism Effects 0.000 claims abstract description 13
- 239000000463 material Substances 0.000 claims abstract description 10
- 238000003756 stirring Methods 0.000 claims description 52
- 238000011010 flushing procedure Methods 0.000 claims description 45
- 239000006185 dispersion Substances 0.000 claims description 4
- 235000010485 konjac Nutrition 0.000 abstract description 78
- 230000000694 effects Effects 0.000 description 17
- 238000000034 method Methods 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 244000309464 bull Species 0.000 description 7
- 230000009471 action Effects 0.000 description 6
- 230000004913 activation Effects 0.000 description 2
- LUEWUZLMQUOBSB-FSKGGBMCSA-N (2s,3s,4s,5s,6r)-2-[(2r,3s,4r,5r,6s)-6-[(2r,3s,4r,5s,6s)-4,5-dihydroxy-2-(hydroxymethyl)-6-[(2r,4r,5s,6r)-4,5,6-trihydroxy-2-(hydroxymethyl)oxan-3-yl]oxyoxan-3-yl]oxy-4,5-dihydroxy-2-(hydroxymethyl)oxan-3-yl]oxy-6-(hydroxymethyl)oxane-3,4,5-triol Chemical compound O[C@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@@H](O[C@@H]2[C@H](O[C@@H](OC3[C@H](O[C@@H](O)[C@@H](O)[C@H]3O)CO)[C@@H](O)[C@H]2O)CO)[C@H](O)[C@H]1O LUEWUZLMQUOBSB-FSKGGBMCSA-N 0.000 description 1
- 229920002581 Glucomannan Polymers 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 229940046240 glucomannan Drugs 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0215—Solid material in other stationary receptacles
- B01D11/0223—Moving bed of solid material
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
- A23L19/10—Products from fruits or vegetables; Preparation or treatment thereof of tuberous or like starch containing root crops
- A23L19/115—Konjak; Konntaku
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0215—Solid material in other stationary receptacles
- B01D11/0223—Moving bed of solid material
- B01D11/0234—Moving bed of solid material using other slow rotating arms or elements, whereby the general transport direction of the solids is not parallel to the rotation axis, e.g. perpendicular
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
Abstract
The invention relates to the field of konjak powder purification, in particular to a reverse-drive opposite-impact type homogeneous leaching device which comprises an upper bin body and a lower bin body which are fixed, wherein the leaching device comprises an opposite-impact mixing mechanism, the opposite-impact mixing mechanism is provided with opposite-impact pipelines, the opposite-impact mixing mechanism is also provided with a centrifugal dispersing assembly, a plurality of centrifugal stirrers are uniformly arranged in the upper bin body around the opposite-impact pipelines, a flow chamber is formed between the upper bin body and the opposite-impact pipelines, and a centrifugal material port communicated with each flow chamber is formed on the surface of the opposite-impact pipeline. The invention also relates to application of the reverse-drive opposite-impact type homogeneous leaching device in purification of konjaku flour.
Description
Technical Field
The invention relates to the field of konjaku flour purification, in particular to a reverse-drive opposite-impact type homogeneous leaching device and an application of the reverse-drive opposite-impact type homogeneous leaching device in konjaku flour purification.
Background
For konjaku flour, the higher the content of konjaku glucomannan therein, the larger the molecular weight and the better the quality, so that the konjaku flour needs to be purified in the process of processing the konjaku into the powder, and in order to improve the purification efficiency, a stirring device with a single-rod structure is usually arranged in a leaching tank, but the efficiency of the existing single-rod structure is limited, the stirring is uneven, and the purification effect is poor.
The utility model provides a leaching device is used in purification of chinese patent CN214808578U konjaku flour that present disclosure, includes the jar body and fixes the fixed box at jar body top, the inside of jar body is provided with holds the chamber, the feed inlet has all been seted up to the top both sides that hold the chamber, the bottom that holds the chamber is provided with the discharging pipe, the inside of fixed box is provided with the symmetrical and drive arrangement that turns to the opposite, the output of drive arrangement is connected with the pivot, the outer end of pivot is connected with the gear, the below of gear is provided with the fluted disc with gear engagement, is connected with the diameter that runs through first bull stick and second bull stick and first bull stick to hold the intracavity portion on two fluted discs respectively, and the length of first bull stick is less than the length of second bull stick, first bull stick and second bull stick are located the body of rod surface that holds the intracavity portion all are fixed with a plurality of stirring vane.
According to the above patent, the stirring device of the patent is capable of performing cross stirring on the materials in the tank body due to the opposite directions of the two driving devices, so that the materials in the tank body can be subjected to cross stirring, and compared with single-rod stirring, the stirring of the materials can be more uniform, however, the stirring device of the patent has the effect of improving uniform stirring in a mode of reversely stirring the two rotating rods, but the konjak powder at the bottom of the tank still cannot be sufficiently stirred, and the konjak powder still cannot be sufficiently and uniformly stirred, so that in order to improve the effect of uniformly and sufficiently stirring the konjak powder, a konjak powder homogenizing leaching device capable of performing dispersion stirring and counter-flushing mixing stirring on the konjak powder is needed.
Disclosure of Invention
According to the invention, konjak powder is dispersed through the centrifugal dispersing component, so that the konjak powder is enabled to flow into each flow chamber in a scattered manner, the konjak powder is led to flow along with the guidance of the centrifugal stirrer in the flow chamber, the konjak powder enters the opposite-flushing pipeline under the action of centrifugal force, and the dispersed konjak powder is mixed in an opposite-flushing manner, so that the purification effect of the konjak powder is improved.
In order to solve the problems in the prior art, the invention provides a reverse-drive opposite-flushing type homogeneous leaching device which comprises an upper bin body and a lower bin body which are fixedly connected together, wherein the leaching device is arranged in the upper bin body and the lower bin body, a bin cover is arranged at the top of the upper bin body, a cavity is formed between the bin cover and the upper bin body, a feeding funnel communicated with the cavity is arranged at the center of the top of the bin cover, a discharge opening is formed at the bottom of the lower bin body and near the edge of the lower bin body, the leaching device comprises an opposite-flushing mixing mechanism for mixing konjak powder together in an opposite-flushing mode, the opposite-flushing mixing mechanism is provided with an opposite-flushing pipeline with a closed upper end and an open lower end, the opposite-flushing pipeline is coaxial and fixedly arranged in the upper bin body, the opposite-flushing mixing mechanism is also provided with a centrifugal dispersing assembly, a plurality of centrifugal stirrers are uniformly arranged around the opposite-flushing pipeline in the upper bin body, a flow chamber for driving konjak powder to flow is formed between the upper bin body and the opposite-flushing pipeline, a centrifugal dispersing assembly communicated with the centrifugal stirrer is formed on the surface of the opposite-flushing pipeline along the axial direction of the centrifugal stirring pipeline, the centrifugal stirring assembly is arranged between the upper bin body and the centrifugal dispersing assembly and the upper bin body in the flow chamber after the centrifugal dispersing assembly falls into the cavity in the cavity when the cavity is started.
Preferably, the inside of the flushing pipeline is coaxially provided with a central shaft, the upper end of the central shaft is rotatably arranged at the top of the flushing pipeline, the lower end of the central shaft extends to the bottom of the flushing pipeline, the upper end of the central shaft is provided with a push rod extending upwards into the feeding funnel, and a primary stirrer is arranged on the push rod and positioned in the small opening end of the feeding funnel.
Preferably, the centrifugal dispersing assembly is provided with an upper centrifugal disc, the upper centrifugal disc is coaxially and fixedly sleeved on the central shaft, the upper centrifugal disc is located between the primary stirrer and the opposite flushing pipeline, the top of each centrifugal stirrer is provided with a lower centrifugal disc, a plurality of lower centrifugal discs are evenly distributed around the upper centrifugal disc, the lower centrifugal discs are located below the upper centrifugal disc, and a plurality of centrifugal strips evenly distributed around the axle center are arranged on the top surfaces of the upper centrifugal disc and the lower centrifugal disc.
Preferably, a first blanking channel is formed between the edge of the upper centrifugal disc and the inner wall of the bin cover and at the position corresponding to each lower centrifugal disc, a second blanking channel is formed between the edge of each lower centrifugal disc and the inner wall of the upper bin body, and each second blanking channel is respectively communicated with the corresponding flow chamber.
Preferably, the centrifugal stirrer is provided with a rotary column, the rotary column is rotationally arranged in the flow chamber, the axial direction of the rotary column is parallel to the axial direction of the central shaft, a rotating shaft rotationally connected with the bin cover is coaxially arranged at the top of the rotary column, the lower centrifugal disc is coaxially and fixedly sleeved on the rotating shaft, a plurality of centrifugal blades are uniformly arranged on the edge of the rotary column along the axial direction of the rotary column, and the side of each centrifugal blade is contacted with the edge of the flow chamber.
Preferably, the edge of the bin cover is fixedly provided with a rotating motor, a first belt is connected between an output shaft of the rotating motor and one of the rotating shafts, a second belt is connected between every two adjacent rotating shafts, and after the rotating motor is started, the rotating columns are in a rotating motion state.
Preferably, the primary stirrer is provided with a plurality of first stirring blades uniformly distributed around the ejector rod, the side of each first stirring blade is provided with a notch extending inwards, the inner wall of the small opening end of the feeding funnel is uniformly provided with a plurality of second stirring blades along the axial direction of the small opening end of the feeding funnel, and when the central shaft rotates, the second stirring blades pass through the notches and are in a staggered motion state with the first stirring blades.
Preferably, the lower bin body is internally provided with a first spiral auger, the upper end of the first spiral auger is coaxial with the lower end of the central shaft and is fixedly connected with the lower end of the central shaft, the lower end of the first spiral auger is rotationally connected with the bottom of the lower bin body, and the bottom of the lower bin body is provided with a stirring motor for driving the first spiral auger to rotate.
Preferably, a second spiral auger is arranged in the lower bin body corresponding to each centrifugal stirrer, the upper end of the second spiral auger is coaxial with and fixedly connected with the lower end of the rotary column, and the lower end of the second spiral auger is rotationally connected with the bottom of the lower bin body.
The invention also provides application of the reverse-drive opposite-impact type homogeneous leaching device in purification of konjaku flour, and the reverse-drive opposite-impact type homogeneous leaching device is adopted.
Compared with the prior art, the beneficial effects of this application are:
1. according to the invention, the konjaku flour is dispersed by the centrifugal dispersing assembly, so that the konjaku flour is caused to flow into each flowing cavity in a scattered manner, the konjaku flour in the flowing cavities is uniformly stirred along with the guidance of the centrifugal stirrer, the konjaku flour in all flowing cavities is thrown into a counter-flushing pipeline together under the action of centrifugal force, the konjaku flour is mixed with the counter-flushing pipeline, the konjaku flour is homogenized and leached, and the purification effect of the konjaku flour is improved;
2. according to the invention, the primary stirrer in the small opening end of the feeding funnel is used for stirring konjak powder in the sliding process, so that the konjak powder is primarily stirred, and the centrifugal stirrer guides the konjak powder to enter the opposite flushing pipeline in a centrifugal way along with the dispersion of the konjak powder into a plurality of flow chambers, so that the konjak powder is impacted on the surface of the central shaft to be dispersed, the dispersed konjak powder achieves a mixing effect, the opposite flushing type konjak powder mixing is realized, and the uniform stirring effect of the konjak powder is improved;
3. according to the invention, the konjak powder is thrown out in a centrifugal way through the rotation of the upper centrifugal disk, so that the konjak powder is scattered and falls on the surface of each lower centrifugal disk, and is thrown out in a centrifugal way along with the rotation of the lower centrifugal disk, so that the konjak powder falls on one side of the flow chamber far away from the opposite flushing pipeline, the centrifugal stirrer is promoted to generate fluidity in the process of guiding the konjak powder, the flow stroke of the konjak powder is increased, the konjak powder is ensured to enter the opposite flushing pipeline in a throwing way under the action of centrifugal force, uniform stirring of the konjak powder is realized, and the purification effect is improved.
Drawings
FIG. 1 is a schematic perspective view of a counter-drive, counter-current, homogeneous leaching apparatus;
FIG. 2 is a partial perspective sectional view of a counter-drive, opposite-impact, homogeneous leaching apparatus;
FIG. 3 is a cross-sectional view of a counter-drive, counter-current, homogeneous leaching apparatus;
FIG. 4 is a partial cross-sectional view I of a counter-drive, counter-current, homogeneous leaching apparatus;
FIG. 5 is a perspective view in partial cross-section of a reverse drive counter-current homogeneous leaching apparatus;
FIG. 6 is a partial cross-sectional view II of a counter-drive, opposite-impact, homogeneous leaching apparatus;
FIG. 7 is a partial cross-sectional view III of a counter-drive, counter-impact, homogeneous leaching apparatus;
FIG. 8 is a schematic perspective view of a centrifugal agitator and centrifugal dispersing assembly of a counter-drive, counter-current, homogeneous leaching apparatus;
FIG. 9 is a top view of a centrifugal agitator and centrifugal dispersing assembly of a counter-drive, counter-current, homogeneous leaching apparatus;
fig. 10 is an enlarged schematic view at a of fig. 3.
The reference numerals in the figures are: 1-loading a bin body; 11-a flow chamber; 2-lower bin body; 21-a discharge port; 3-bin cover; 31-a first blanking channel; 32-a second blanking passage; 4-a feeding funnel; 5-opposite-impact mixing mechanism; 51-a flush line; 511-centrifuging the feed opening; 512-central axis; 5121-a push rod; 52-centrifuging the dispersion assembly; 521-upper centrifuge disk; 5211-centrifuge strips; 522-lower centrifuge disk; 53-centrifugal stirrer; 531-spin column; 5311-a spindle; 5312-centrifuging the blades; 532-a rotating electric machine; 5321-a first belt; 5322 a second belt; 6-a primary stirrer; 61-a first stirring blade; 62-a second stirring blade; 7-a first spiral auger; 71-a stirring motor; 8-a second spiral auger.
Detailed Description
The invention will be further described in detail with reference to the drawings and the detailed description below, in order to further understand the features and technical means of the invention and the specific objects and functions achieved.
Referring to fig. 1-9, a counter-drive hedging homogeneous leaching device comprises an upper bin body 1 and a lower bin body 2 which are fixedly connected together, wherein the leaching device is arranged in the upper bin body 1 and the lower bin body 2, a bin cover 3 is arranged at the top of the upper bin body 1, a cavity is formed between the bin cover 3 and the upper bin body 1, a feeding funnel 4 communicated with the cavity is arranged at the center of the top of the bin cover 3, a discharge opening 21 is formed at the position, close to the edge, of the bottom of the lower bin body 2, of the leaching device, the leaching device comprises a hedging mixing mechanism 5 for mixing konjaku powder together in a hedging mode, the hedging mixing mechanism 5 is provided with a hedging pipeline 51 with a closed upper end and an open lower end, the hedging pipeline 51 is coaxial and fixedly arranged in the upper bin body 1, the hedging mixing mechanism 5 is also provided with centrifugal dispersing components 52, a plurality of centrifugal stirrers 53 are uniformly arranged around the inside the hedging pipeline 51, a flow cavity 11 for each centrifugal stirrer 53 is formed between the upper bin body 1 and the hedging pipeline 51, the centrifugal stirrer 53 drives the konjaku powder to flow, and the centrifugal dispersing components 11 fall into the cavity 52 along the direction of the flow cavity 11 along the axis 11, and the flow dispersing components are arranged in the cavity 11 and the cavity 11 is in the flow cavity after the cavity is in the flow state of the cavity 11.
When konjak powder is purified, konjak powder and leaching liquor are mixed first, and then the konjak powder is thrown into a charging hopper 4, the konjak powder slides onto a centrifugal dispersing assembly 52, the centrifugal dispersing assembly 52 disperses the konjak powder in a centrifugal manner and throws the konjak powder out to the periphery along with the activation of the centrifugal dispersing assembly 52 until the konjak powder impacts on the inner wall of an upper bin body 1 and then falls into flow chambers 11, part of konjak powder is contained in each flow chamber 11, then a centrifugal stirrer 53 in each flow chamber 11 is activated, the konjak powder is caused to be guided to a centrifugal material opening 511 of a flushing pipeline 51, the konjak powder enters the flushing pipeline 51 from the centrifugal material opening 511 under the action of centrifugal force, the konjak powder in each flow chamber 11 is caused to flow towards the centrifugal material opening 511 due to the synchronous activation of the plurality of the centrifugal stirrers 53, the konjak powder in the plurality of flow chambers 11 is collided in the flushing pipeline 51, the konjak powder is mixed along with the inner wall of the upper bin body 1, and the mixed konjak powder freely falls down along the flushing pipeline 51, and falls into a lower bin body 2 for storage.
Referring to fig. 2-8, a central shaft 512 is coaxially disposed in the opposite flushing pipe 51, the upper end of the central shaft 512 is rotatably disposed at the top of the opposite flushing pipe 51, the lower end of the central shaft 512 extends to the bottom of the opposite flushing pipe 51, a top rod 5121 extending upward into the feeding funnel 4 is disposed at the upper end of the central shaft 512, and a primary stirrer 6 is disposed on the top rod 5121 and located in the small mouth end of the feeding funnel 4.
When the konjak powder is mixed with the leaching solution and then put into the charging hopper 4, the konjak powder slides into the small mouth end of the charging hopper 4, and as the central shaft 512 rotates, the primary stirrer 6 rotates relative to the charging hopper 4, so that the konjak powder is primarily stirred until the konjak powder enters each flow chamber 11 after being dispersed, the konjak powder in the plurality of flow chambers 11 enters the opposite flushing pipeline 51 through the centrifugal material holes 511 under the action of centrifugal force, and then the konjak powder and the konjak powder are opposite-flushed with each other on the surface of the central shaft 512, so that the konjak powder is dispersed and slides down the opposite flushing pipeline 51 into the lower bin body 2, and finally the konjak powder is mixed.
Referring to fig. 2, 3, 6 and 7, the centrifugal dispersing assembly 52 is provided with an upper centrifugal disk 521, the upper centrifugal disk 521 is coaxially and fixedly sleeved on the central shaft 512, the upper centrifugal disk 521 is located between the primary stirrer 6 and the opposite flushing pipeline 51, a lower centrifugal disk 522 is arranged at the top of each centrifugal stirrer 53, a plurality of lower centrifugal disks 522 are uniformly distributed around the upper centrifugal disk 521, the lower centrifugal disk 522 is located below the upper centrifugal disk 521, and a plurality of centrifugal strips 5211 uniformly distributed around the axle center are arranged on the top surfaces of the upper centrifugal disk 521 and the lower centrifugal disk 522.
When the konjak powder falls on the surface of the upper centrifugal plate 521, the konjak powder is thrown outwards under the centrifugal force along with the rotation of the upper centrifugal plate 521, the konjak powder is scattered in four directions, and slides downwards along with the inner wall of the bin cover 3, and slides on the surface of each lower centrifugal plate 522 along with the impact of the konjak powder, and the konjak powder is thrown outwards again under the centrifugal force along with the rotation of the lower centrifugal plate 522, and slides downwards into the flow chamber 11 along with the impact of the inner wall of the upper bin body 1, and then the konjak powder is driven to flow through the centrifugal stirrer 53, so that the konjak powder flows in the dispersing process, the stirring effect is achieved, and the stirring of the konjak powder is more uniform.
Referring to fig. 3 to 9, a first blanking passage 31 is formed between the edge of the upper centrifugal disk 521 and the inner wall of the bin cover 3 at a position corresponding to each of the lower centrifugal disks 522, and a second blanking passage 32 is formed between the edge of each of the lower centrifugal disks 522 and the inner wall of the upper bin 1, and each of the second blanking passages 32 communicates with the corresponding flow chamber 11, respectively.
After the konjak powder is thrown out in a scattering manner on the surface of the upper centrifugal plate 521, the konjak powder slides down through the first blanking channel 31 corresponding to each lower centrifugal plate 522, and as the plurality of lower centrifugal plates 522 are uniformly distributed around the upper centrifugal plate 521 and the lower centrifugal plates 522 are positioned below the upper centrifugal plate 521, the konjak powder slides down to the surface of the lower centrifugal plates 522 along the first blanking channel 31, and along with the rotation of the lower centrifugal plates 522, the konjak powder is guided to the second blanking channel 32, and as the second blanking channel 32 is opposite to the area of the side of the flow chamber 11, which is far away from the flushing pipeline 51, the flow stroke of the konjak powder in the flow chamber 11 is effectively increased, so that the konjak powder is stirred more uniformly, the konjak powder in each flow chamber 11 is impacted in a flushing manner, and the purification effect after the mixing is improved.
Referring to fig. 3-6, the centrifugal stirrer 53 is provided with a rotary column 531, the rotary column 531 is rotatably disposed in the flow chamber 11, the axial direction of the rotary column 531 is parallel to the axial direction of the central shaft 512, a rotary shaft 5311 rotatably connected with the bin cover 3 is coaxially disposed at the top of the rotary column 531, the lower centrifugal disk 522 is coaxially and fixedly sleeved on the rotary shaft 5311, a plurality of centrifugal blades 5312 are uniformly disposed at the edge of the rotary column 531 along the axial direction thereof, and the side of each centrifugal blade 5312 is in contact with the edge of the flow chamber 11.
When the centrifugal stirrer 53 is started, the rotating shaft 5311 rotates to drive the rotating column 531 to rotate, and as the surface of the rotating column 531 is provided with a plurality of centrifugal blades 5312 which are in contact with the inner wall of the upper bin body 1, the konjaku flour flows along the inner wall of the upper bin body 1 along with the guidance of the centrifugal blades 5312, so that the konjaku flour generates fluidity and achieves a uniform stirring effect, until the konjaku flour is guided to the centrifugal material openings 511 of the opposite flushing pipelines 51, and is thrown outwards by the centrifugal blades 5312 under the high-speed rotation of the rotating shaft 5311, so that the konjaku flour enters the opposite flushing pipelines 51 to collide with the central shaft 512 and is dispersed, and the konjaku flour entering the opposite flushing pipelines 51 is mixed with each other after being dispersed, so that the homogenizing leaching effect is improved.
Referring to fig. 1-3, a rotating motor 532 is fixedly arranged at the edge of the bin cover 3, a first belt 5321 is connected between an output shaft of the rotating motor 532 and one of the rotating shafts 5311, a second belt 5322 is connected between every two adjacent rotating shafts 5311, and when the rotating motor 532 is started, the rotating columns 531 are in a rotating motion state.
When the rotating shafts 5311 of the centrifugal agitators 53 simultaneously rotate, the rotating motor 532 drives one of the rotating shafts 5311 to rotate through the first belt 5321, and as one rotating shaft 5311 rotates, the plurality of rotating shafts 5311 are driven to rotate together under the connection of the second belt 5322 between every two adjacent rotating shafts 5311, so that the konjak powder dispersed in each flow chamber 11 flows simultaneously, the collision effect between the konjak powder and the konjak powder in the opposite flushing pipeline 51 is effectively achieved, the dispersed konjak powder is gathered together, the complete mixing is achieved, the purifying effect is improved, and the uniformity of the konjak powder in the stirring process is improved.
Referring to fig. 2, 3 and 10, the primary mixer 6 is provided with a plurality of first mixing blades 61 uniformly distributed around the ejector pin 5121, each first mixing blade 61 is provided with a notch extending inwards on a side thereof, the inner wall of the small opening end of the charging hopper 4 is uniformly provided with a plurality of second mixing blades 62 along the axial direction thereof, and when the central shaft 512 rotates, the second mixing blades 62 pass through the notches and are in a staggered movement state with the first mixing blades 61.
In the process of rotating the central shaft 512, the central shaft 512 drives the upper centrifugal disk 521 to rotate, and the primary stirrer 6 also rotates in the small opening end of the feeding funnel 4, and the central shaft 512 drives the ejector rod 5121 to rotate together, because the surface of the ejector rod 5121 is provided with the first stirring blades 61, and the inner wall of the small opening end of the feeding funnel 4 is provided with the second stirring blades 62 which are distributed in a staggered manner with the first stirring blades 61, the ejector rod 5121 rotates relative to the feeding funnel 4, and the first stirring blades 61 and the second stirring blades 62 perform a staggered motion, so that the effect of primary stirring on konjaku flour is achieved in the process of sliding the konjaku flour along the feeding funnel 4, and the subsequent efficiency of uniformly stirring konjaku flour is improved.
Referring to fig. 2, 3 and 8, a first spiral auger 7 is disposed in the lower bin 2, an upper end of the first spiral auger 7 is coaxially and fixedly connected with a lower end of the central shaft 512, a lower end of the first spiral auger 7 is rotatably connected with a bottom of the lower bin 2, and a stirring motor 71 for driving the first spiral auger 7 to rotate is disposed at the bottom of the lower bin 2.
After the konjaku flour falls into the lower bin 2, the stirring motor 71 drives the first screw auger 7 to rotate, and the first screw auger 7 is fixedly connected with the central shaft 512, so that the central shaft 512 is driven to rotate together by the rotation of the first screw auger 7, and the first screw auger 7 performs final overall mixing and stirring on the konjaku flour in the lower bin 2 to ensure uniform stirring.
Referring to fig. 2, 3 and 8, a second spiral auger 8 is disposed in the lower bin 2 corresponding to each centrifugal stirrer 53, the upper end of the second spiral auger 8 is coaxially and fixedly connected with the lower end of the rotary column 531, and the lower end of the second spiral auger 8 is rotatably connected with the bottom of the lower bin 2.
When each centrifugal stirrer 53 is started, each second spiral auger 8 connected with the centrifugal stirrer 53 also rotates along with the centrifugal stirrer, a plurality of second spiral augers 8 surround the periphery of the first spiral auger 7 and stir konjaku flour together with the second spiral augers, so that the stirring effect is improved, the stirring uniformity is improved, and the purity of the konjaku flour is ensured to meet the requirement.
An application of a reverse-drive opposite-impact type homogeneous leaching device in purifying konjaku flour.
According to the invention, the konjak powder is dispersed by the centrifugal dispersing assembly 52, so that the konjak powder is caused to flow into each flow chamber 11 in a scattered manner, the konjak powder in the flow chambers 11 is uniformly stirred in the flowing process along with the guidance of the centrifugal stirrer 53, the konjak powder in all the flow chambers 11 is thrown into the opposite-flushing pipeline 51 under the action of the centrifugal force along with the centrifugal stirrer, and the konjak powder is mixed along with the centrifugal stirrer, so that the purification effect of the konjak powder is improved.
The foregoing examples merely illustrate one or more embodiments of the invention, which are described in greater detail and are not to be construed as limiting the scope of the invention. It should be noted that it will be apparent to those skilled in the art that several variations and modifications can be made without departing from the spirit of the invention, which are all within the scope of the invention. Accordingly, the scope of the invention should be assessed as that of the appended claims.
Claims (6)
1. The utility model provides a reverse drive is to dashing homogeneity leaching device, including fixed connection's last storehouse body (1) and lower storehouse body (2) together, leaching device sets up in last storehouse body (1) and lower storehouse body (2), the top of last storehouse body (1) is equipped with storehouse lid (3), form the cavity between storehouse lid (3) and last storehouse body (1), the top center of storehouse lid (3) is equipped with material throwing funnel (4) with cavity intercommunication, the bottom of lower storehouse body (2) and be close to edge position department has seted up bin outlet (21), characterized in that, leaching device includes be used for konjaku powder to mix together with the form of dashing in mixing mechanism (5), dashing mixing mechanism (5) are equipped with upper end and are open-ended dashing pipeline (51), inside at last storehouse body (1) is coaxial and fixed the setting, dashing mixing mechanism (5) still are equipped with centrifugal dispersion subassembly (52), the inside of last storehouse body (1) evenly is equipped with a plurality of centrifugal mixer (53) around dashing pipeline (51), the centrifuge mixer (11) of each is equipped with the centrifuge mixer (11) of mouth forms between each pipeline (11) and each pipeline (11) of mouth that are connected with the flow channel (11) along the direction of the flow of dashing pipeline (11), the centrifugal dispersing assembly (52) is arranged in a cavity formed between the bin cover (3) and the upper bin body (1), after the centrifugal dispersing assembly (52) is started, konjaku flour is in a flowing state of dispersing and falling into each flowing cavity (11), a central shaft (512) is coaxially arranged in the opposite flushing pipeline (51), an ejector rod (5121) which extends upwards into the feeding funnel (4) is arranged at the upper end of the central shaft (512), a primary stirrer (6) is arranged on the ejector rod (5121) and positioned in the small opening end of the feeding funnel (4), a first spiral auger (7) is arranged in the lower bin body (2), the upper end of the first spiral auger (7) is coaxially and fixedly connected with the lower end of the central shaft (512), and a second spiral auger (8) is arranged in the lower bin body (2) corresponding to each centrifugal stirrer (53);
the centrifugal dispersing assembly (52) is provided with an upper centrifugal disc (521), the upper centrifugal disc (521) is coaxially and fixedly sleeved on the central shaft (512), the upper centrifugal disc (521) is positioned between the primary stirrer (6) and the opposite flushing pipeline (51), the top of each centrifugal stirrer (53) is provided with a lower centrifugal disc (522), a plurality of lower centrifugal discs (522) are uniformly distributed around the upper centrifugal disc (521), the lower centrifugal discs (522) are positioned below the upper centrifugal disc (521), and a plurality of centrifugal strips (5211) uniformly distributed around the axle center are arranged on the top surfaces of the upper centrifugal disc (521) and the lower centrifugal disc (522);
a first blanking channel (31) is formed between the edge of the upper centrifugal disc (521) and the inner wall of the bin cover (3) and corresponds to the position of each lower centrifugal disc (522), a second blanking channel (32) is formed between the edge of each lower centrifugal disc (522) and the inner wall of the upper bin body (1), and each second blanking channel (32) is respectively communicated with the corresponding flow chamber (11);
the centrifugal stirrer (53) is provided with a rotating column (531), the rotating column (531) is rotationally arranged in the flow chamber (11), the axial direction of the rotating column (531) is parallel to the axial direction of the central shaft (512), the top of the rotating column (531) is coaxially provided with a rotating shaft (5311) rotationally connected with the bin cover (3), the lower centrifugal disc (522) is coaxially and fixedly sleeved on the rotating shaft (5311), the edge of the rotating column (531) is uniformly provided with a plurality of centrifugal blades (5312) along the axial direction of the rotating column, and the side of each centrifugal blade (5312) is contacted with the edge of the flow chamber (11);
the primary stirrer (6) is provided with a plurality of first stirring blades (61) which surround the ejector rod (5121) and are uniformly distributed, the side of each first stirring blade (61) is provided with a notch which extends inwards, the inner wall of the small opening end of the feeding funnel (4) is uniformly provided with a plurality of second stirring blades (62) along the axial direction of the small opening end, and when the central shaft (512) rotates, the second stirring blades (62) penetrate through the notches and are in a staggered motion state with the first stirring blades (61).
2. A counter-drive, counter-flushing, homogeneous leaching apparatus according to claim 1, characterized in that the upper end of the central shaft (512) is rotatably arranged at the top of the counter-flushing pipe (51), and that the lower end of the central shaft (512) extends to the bottom of the counter-flushing pipe (51).
3. A counter-drive hedging homogeneous leaching device according to claim 1, characterized in that the edge of the lid (3) is fixedly provided with a rotating electric machine (532), a first belt (5321) is arranged between the output shaft of the rotating electric machine (532) and one of the rotating shafts (5311) between the rotating electric machines (532), a second belt (5322) is arranged between each two adjacent rotating shafts (5311), and when the rotating electric machine (532) is started, the rotating columns (531) are in a co-rotating motion.
4. The reverse-drive opposite-impact type homogeneous leaching device according to claim 1, wherein the lower end of the first spiral auger (7) is rotatably connected with the bottom of the lower bin body (2), and a stirring motor (71) for driving the first spiral auger (7) to rotate is arranged at the bottom of the lower bin body (2).
5. The reverse-drive opposite-impact type homogeneous leaching device according to claim 1, wherein the upper end of the second spiral auger (8) is coaxially and fixedly connected with the lower end of the rotary column (531), and the lower end of the second spiral auger (8) is rotatably connected with the bottom of the lower bin body (2).
6. Use of a counter-drive, opposite-impact, homogeneous leaching device according to any one of claims 1 to 5 in the purification of konjaku flour.
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| CN202311389431.7A CN117101180B (en) | 2023-10-25 | 2023-10-25 | Reverse driving opposite-impact type homogeneous leaching device and application thereof in purification of konjaku flour |
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| CN202311389431.7A CN117101180B (en) | 2023-10-25 | 2023-10-25 | Reverse driving opposite-impact type homogeneous leaching device and application thereof in purification of konjaku flour |
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| CN117101180B true CN117101180B (en) | 2024-03-19 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1034089A (en) * | 1965-05-19 | 1966-06-29 | Microcyclomat Co | Extraction apparatus and method |
| CN214319190U (en) * | 2020-12-14 | 2021-10-01 | 西北师范大学 | Anthocyanin extraction, separation and concentration integrated device |
| CN113634012A (en) * | 2021-10-14 | 2021-11-12 | 江苏京牧生物技术有限公司 | Chinese herbal medicine component purification device as feed additive |
| CN214763452U (en) * | 2021-03-25 | 2021-11-19 | 云南农业大学 | Low temperature preparation dendrobe polysaccharide draws jar |
| CN113893574A (en) * | 2021-09-03 | 2022-01-07 | 韩青芬 | Plant polypeptide extraction equipment |
-
2023
- 2023-10-25 CN CN202311389431.7A patent/CN117101180B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1034089A (en) * | 1965-05-19 | 1966-06-29 | Microcyclomat Co | Extraction apparatus and method |
| CN214319190U (en) * | 2020-12-14 | 2021-10-01 | 西北师范大学 | Anthocyanin extraction, separation and concentration integrated device |
| CN214763452U (en) * | 2021-03-25 | 2021-11-19 | 云南农业大学 | Low temperature preparation dendrobe polysaccharide draws jar |
| CN113893574A (en) * | 2021-09-03 | 2022-01-07 | 韩青芬 | Plant polypeptide extraction equipment |
| CN113634012A (en) * | 2021-10-14 | 2021-11-12 | 江苏京牧生物技术有限公司 | Chinese herbal medicine component purification device as feed additive |
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