CN107312888A - With feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units - Google Patents
With feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units Download PDFInfo
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- CN107312888A CN107312888A CN201710738197.2A CN201710738197A CN107312888A CN 107312888 A CN107312888 A CN 107312888A CN 201710738197 A CN201710738197 A CN 201710738197A CN 107312888 A CN107312888 A CN 107312888A
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- lacquer disk
- bagasse
- centrifuge
- drying machine
- turning kun
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- 241000609240 Ambelania acida Species 0.000 title claims abstract description 35
- 239000010905 bagasse Substances 0.000 title claims abstract description 35
- 238000001035 drying Methods 0.000 title claims abstract description 17
- 238000012545 processing Methods 0.000 title claims abstract description 12
- 239000004922 lacquer Substances 0.000 claims abstract description 50
- 230000000694 effects Effects 0.000 claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 238000004880 explosion Methods 0.000 claims abstract description 17
- 238000001704 evaporation Methods 0.000 claims abstract description 14
- 230000008020 evaporation Effects 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims description 33
- 239000012141 concentrate Substances 0.000 claims description 19
- 238000007789 sealing Methods 0.000 claims description 8
- 230000006835 compression Effects 0.000 claims description 5
- 238000007906 compression Methods 0.000 claims description 5
- 238000002386 leaching Methods 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 10
- 230000001737 promoting effect Effects 0.000 abstract description 3
- 239000007791 liquid phase Substances 0.000 description 20
- 240000000111 Saccharum officinarum Species 0.000 description 10
- 235000007201 Saccharum officinarum Nutrition 0.000 description 10
- 238000012546 transfer Methods 0.000 description 10
- 230000005484 gravity Effects 0.000 description 9
- 239000012071 phase Substances 0.000 description 8
- 230000009194 climbing Effects 0.000 description 5
- 238000001914 filtration Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 238000009834 vaporization Methods 0.000 description 4
- 230000008016 vaporization Effects 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 241000906629 Cimicifugeae Species 0.000 description 2
- 241001504664 Crossocheilus latius Species 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000003139 buffering effect Effects 0.000 description 2
- 239000008358 core component Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000000149 penetrating effect Effects 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 230000007306 turnover Effects 0.000 description 2
- 230000003245 working effect Effects 0.000 description 2
- 208000004350 Strabismus Diseases 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 210000001367 artery Anatomy 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 230000001351 cycling effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000003340 mental effect Effects 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 230000000541 pulsatile effect Effects 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 230000003252 repetitive effect Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 238000009923 sugaring Methods 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B10/00—Production of sugar juices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/80—Destroying solid waste or transforming solid waste into something useful or harmless involving an extraction step
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B10/00—Production of sugar juices
- C13B10/02—Expressing juice from sugar cane or similar material, e.g. sorghum saccharatum
- C13B10/025—Treatment of sugar cane before extraction
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B10/00—Production of sugar juices
- C13B10/02—Expressing juice from sugar cane or similar material, e.g. sorghum saccharatum
- C13B10/06—Sugar-cane crushers
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B20/00—Purification of sugar juices
- C13B20/16—Purification of sugar juices by physical means, e.g. osmosis or filtration
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B25/00—Evaporators or boiling pans specially adapted for sugar juices; Evaporating or boiling sugar juices
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B25/00—Evaporators or boiling pans specially adapted for sugar juices; Evaporating or boiling sugar juices
- C13B25/02—Details, e.g. for preventing foaming or for catching juice
-
- C—CHEMISTRY; METALLURGY
- C13—SUGAR INDUSTRY
- C13B—PRODUCTION OF SUCROSE; APPARATUS SPECIALLY ADAPTED THEREFOR
- C13B5/00—Reducing the size of material from which sugar is to be extracted
- C13B5/04—Shredding sugar cane
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B20/00—Combinations of machines or apparatus covered by two or more of groups F26B9/00 - F26B19/00
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Centrifugal Separators (AREA)
Abstract
The invention discloses it is a kind of with feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units, bagasse feed well is provided with above the body of leaching device；Internal body, to turning Kun, is cylinder to turning Kun, every grade is equipped with bagasse guide groove to turning Kun lower sections, and afterbody guide groove connects the hopper of bagasse elevator, and the blow tank of elevator connects drying machine through dewatering centrifuge provided with three-level；Elevator is provided with water intaking valve, and body upper is provided with filter and drain pipe, drain pipe connection triple effect long tube climbing-film evaporation enrichment facility；Cosine lacquer disk(-sc) pulse gas explosion device is provided with body, the body lower left corner is provided with mechanical ultrasonic vibrator.The three-level of the present invention is to turning Kun, cosine lacquer disk(-sc) pulse gas explosion device and mechanical ultrasonic vibrator be all with distinguishing feature, the leaching for promoting sugar can be cooperateed with to extract, operation principle and the technique effect for being difficult to predict with those skilled in the art, possess stronger actual application value.
Description
Technical field
The present invention relates to it is a kind of with feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units.
Background technology
By sugar cane crushing and to carry out sugaring be very important food basic industry, in general sugar enterprise is all in south
The square especially convenient place of traffic, and it is nearer apart from sugarcane producing region, be so conducive to saving logistics cost and development scale warp
Ji.
The first step of sugar enterprise's working process is sugar cane crushing, but it is difficult thoroughly to realize sugar that traditional sugar cane crushing, which is,
Separation and Extraction, squeezed and counterflow leaching innovative design so carrying out continuous rub with the hands to the fiber after sugar cane crushing, and leachate is entered
Row low energy consumption is concentrated, and to realizing depth extraction sugared in bagasse, the energy efficiency level of lifting sucrose enterprise is all with important
Meaning.
The content of the invention
The technical problem to be solved in the present invention is exactly to overcome the deficiencies in the prior art there is provided a kind of simple and practical, energy
Sugar to turning Kun cartridge type bagasse processing units in enough energy efficiencies to greatest extent and to greatest extent extraction bagasse.
To overcome the deficiencies in the prior art, the present invention takes following technical scheme：
It is a kind of to exist with feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units, including body, its feature
In：Bagasse feed well is provided with above body；Internal body, to turning Kun, is cylinder to turning Kun, every grade right provided with three-level
Turn Kun lower sections and be equipped with bagasse guide groove, afterbody guide groove connects the hopper of bagasse elevator, the blow tank of elevator
Drying machine is connected through dewatering centrifuge；Elevator is provided with water intaking valve, and body upper is provided with filter and drain pipe, drain pipe warp
Dashpot connects filter press, and filter press connects triple effect long tube climbing-film evaporation enrichment facility through pipeline, and triple effect long tube climbing-film evaporation is dense
The concentrated liquid temporary tank connection concentrate efferent duct of compression apparatus；Cosine lacquer disk(-sc) pulse gas explosion device, cosine lacquer disk(-sc) are provided with body
Pulse gas explosion device is made up of cosine lacquer disk(-sc), cylinder, expansion link, compressed air hose, baffle ring and pot shape spherical faced pan, and cosine lacquer disk(-sc) is cut
Face thick middle thin edge, is shaped as below cosine curve, cosine lacquer disk(-sc) being provided with pot shape spherical faced pan, cosine lacquer disk(-sc) is connected through expansion link
Extra-organismal cylinder, cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compression sky
Tracheae also UNICOM's cosine lacquer disk(-sc) inner chamber body；The body lower left corner is provided with mechanical ultrasonic vibrator, by actuating unit kinetic energy at a high speed
Rotation, the structure of mechanical ultrasonic vibrator is spherical cap shape, and spherical cap edge is smooth continuous cosine curve, from spherical cap center
There is the feature that crest, trough progressively expand and continuously dissipated to edge.
Clean-up port is provided with below the body.
Baffle ring is provided with above the pot shape spherical faced pan.
The body is connected as one with elevator by flange, is sealing structure and easy to disassemble.
Bagasse delivers into device top by feed well, and transfer roller cylinder is extruded by three-level, passes through elevator afterwards
Output.Body is integrally connected with elevator by flange, is that sealing structure also allows for demolition and maintenance；Device liquid level is maintained during work
Certain position, device supplements water and filled into by water intaking valve control, is overflowed by drain pipe, reaches liquid phase turnover balance, so sweet
Bagasse is able to realize that counter current contacting is leached with liquid phase water in the case where entering device and three-level squeezing effect, because strong extruding promotes strong inhale
Water, realizes the adverse current sugar leaching for most penetrating by force, permeating, reaches Increasing Production and Energy Saving emission reduction.
Bagasse is exported by the blow tank of elevator, is dried again through drying machine by centrifuge dewatering and is easy to later use
Processing, the relatively concentrated sugar liquid of counterflow leaching is filtered by filter, is overflowed and conveyed by drain pipe, carries out triple effect long tube climbing-film evaporation dense
Contracting is handled.
The concentration of triple effect long tube climbing-film evaporation is exactly briefly three Long-Tube Rising-Film Evaporators tandem workings, and Boiler Steam supplies one
Long-Tube Rising-Film Evaporators are imitated as thermal source, an effect indirect steam is used as triple effect thermal source, work as two effect thermals source, two effect indirect steams
Bagasse leachate inputs temporary dashpot by drain pipe when making, then carries out press filtration purification through pump, pipeline to filter press；
Pressing filtering liquid is again through pump, pipeline to an effect tribe Cimicifugeae device bottom, and tribe Cimicifugeae device is one kind of tubular heat exchanger in fact, row
Pipe caliber lesser amt is numerous, possesses enough pipe surfaces externally and internally products, and pipe with small pipe diameter is easy to intraluminal fluid mutually heated explosive vaporization vaporization
Drive liquid phase to pull up a liter film forming in pipe, Boiler Steam is connected by steam control valve between shell side and tube side, by drain valve certainly
The cavity of dynamic discharge steam condensate (SC), tube side and shell side is heated full of suitable pressure steam to tubulation outer wall, promote pipe interior by
Heat；Sugar-cane juice liquid inlet control valve controls sugarcane liquid input flow rate, makes to have in tubulation relatively suitable liquid level, while continuous feed liquor.Liquid phase
Heated acutely boiling, gas-liquid mixture gas phase expansion in tubulation drives liquid phase to gush upwards jointly and drawn high into liquid in pipe
Film, there is heat transfer area inside and outside king-sized pipe, and pipe is outer to be heated by steam condensateization, the heated continuous vaporization of intraluminal fluid phase film forming,
Gas-liquid mixture is gushed into gravity gas-liquid catch-all, and gravity gas-liquid catch-all water conservancy diversion cross section is larger, and air velocity of gushing can drop
Low, such drop produces sedimentation because being affected by gravity, and is concentrated by pipe and is transported to concentrate buffer groove buffering；Gravity vapour-liquid
The indirect steam of catch-all is by the tangentially connected cyclonic separation foam of central upper portion pipe, and indirect steam carries a small amount of drop in whirlwind point
Screw is produced in foam device to decline, and backflows to form inside spin ascending air in bottom, last indirect steam is led by central tube
Stream conveying concentrates shell side thermal source as next effect；Drop is also rotated at a high speed because gas phase drives, and gas phase is departed under the action of the centrifugal force
In whirlwind catch-all glue wall be captured, drop enrichment along wall decline be concentrated through pipe concentrate be transported to concentrate temporary tank delay
Punching, temporary tank lower liquid phase carries out two effect concentrations, similar carry out triple effect concentration again through pump, pipeline to the second effect concentration again.
Triple effect indirect steam enters condenser through pipeline connection, and condenser connects vacuum machine, shell side connection by pipeline
Low temperature water-circulating pipe；Vacuum machine extracts incondensable gas, and condensable vapours condensed water connects condensed water temporary tank by pipeline, dense
Contracting liquid connects concentrate temporary tank by pipeline, can enter next process procedure by pump, pipeline output.Condensed water temporary tank and
The general length of vertical straight tube of concentrate temporary tank connection is more than 10 meters, for overcoming atmospheric pressure liquid phase to export automatically, is commonly called as big
Air leg.
It is cylinder to transfer roller cylinder, corresponding bearing arrangement is easy to seal waterproof, adapts to strength extruding poor to turning and extruding
Dynamic to turning, particularly advantageous strong extruding is crushed with rubbing with the hands to grind, the sugared dissolution of counterflow leaching for promoting bagasse and water.
Core component is that thick edge is slightly thin in the middle of cosine lacquer disk(-sc), lacquer disk(-sc) section, and general shape is cosine curve, lacquer disk(-sc) pressure
Tight pot shape spherical faced pan constitutes airtight cavity, and to wherein inputting compressed air, when air pressure reaches certain value, lacquer disk(-sc) can be produced
It is flipped up suddenly, explosion type release is produced to the compressed air wherein stored, explosion vibration shock wave can be produced, it is particularly advantageous
Material gas explosion is promoted to stir with leaching mass transfer.
Cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow connection compressed air hose also joins
Logical lacquer disk(-sc) inner chamber body, and by axle sleeve and body realization isolate it is closed prevent leakage, and can flexibly stretch；When expansion link drives glue
Disk can form airtight cavity when compressing pot shape spherical faced pan, at this moment by compressed air hose to wherein inputting compressed air, air pressure
Power rises, the triggering until cosine lacquer disk(-sc) rim pressure transfinites, and produces and is flipped up what is internally stored under the effect of lacquer disk(-sc) integral pressure
Compressed air produces explosion type release, and at this moment expansion link bounces back again, and just the reply of energy automatic elastic is flipped back to original starting shape to lacquer disk(-sc)
State, may be repeated do action, and baffle ring can assist the upset of cosine lacquer disk(-sc) to reset in case of need.
Mechanical ultrasonic vibrator is rotated at a high speed, axle sleeve can realize liquid in the lower left corner of device by actuating unit kinetic energy
Mutually simultaneously favourable vibrator rotates at a high speed for sealing.
The structure of mechanical ultrasonic vibrator is spherical cap shape, and spherical cap edge is smooth continuous cosine curve, from spherical cap
Center has crest, trough progressively to expand continuous diverging feature to edge.Such structure has good bulk strength, when machinery is super
Sound wave vibrator is driven by actuating unit in the liquid phase to be rotated at a high speed, it is clear that can produce the strong cavitation effect of similar ultrasonic wave
Should, strength promotes the mass transport process of counterflow leaching, and collaboration promotes the dissolving of sugar to leach.
Compared with prior art, beneficial effects of the present invention are also resided in：
1st, continuous reliable, extruding compression ratio is bitten to transfer roller tin material especially big, differential stone roller separating twice effect of rubbing with the hands is especially good, three
The strong extruding of level realizes most perfect adaptation with counterflow leaching；
2nd, cosine lacquer disk(-sc) pulse gas explosion device can effectively simulate, produce macroscopical discontinuous blast, encourage the strong pulsatile impact of liquid phase；
3rd, mechanical ultrasonic vibrator C rotates at a high speed in the liquid phase, can the ingenious strong cavitation for producing the similar ul-trasonic irradiation of high frequency
Effect.
4th, the present apparatus bagasse leachate is carried out triple effect climbing-film evaporation concentration it is especially reliable, efficiently, unit steam raising
Water is big；Two-stage vapor-liquid separation is taken to carry out purified treatment to indirect steam, vapor-liquid separation is reliable, efficient；Carried out after press filtration dense
Contracting operating procedure is smooth, and condenser collaboration vacuum machine work is particularly advantageous to be concentrated in vacuo；Long tube barometric pipe reliable design, it is simple,
It is durable, automatic to overcome atmospheric pressure liquid phase to export.
Above four main measures all have distinguishing feature, can cooperate with and promote the leaching of sugar to extract and save energy consumption, with ability
Field technique personnel are difficult to the operation principle predicted and technique effect, possess stronger actual application value.
Brief description of the drawings
Fig. 1 is the planar structure schematic diagram of the present invention.
Fig. 2 is the planar structure schematic diagram of triple effect climbing-film evaporation enrichment facility.
Fig. 3 is the partial enlargement structural representation of cosine lacquer disk(-sc) pulse gas explosion device.
Fig. 4 is the main structure diagram of mechanical ultrasonic vibrator.
Fig. 5 is the overlooking the structure diagram of mechanical ultrasonic vibrator.
Fig. 6 is the present invention looks up structural representation of mechanical ultrasonic vibrator.
Fig. 7 is the strabismus structural representation of bowing of mechanical ultrasonic vibrator.
Fig. 8 is the oblique present invention looks up structural representation of mechanical ultrasonic vibrator.
Each label is represented in figure：
A, to transfer roller cylinder；B, cosine lacquer disk(-sc)；C, mechanical ultrasonic vibrator；1st, body；2nd, filter；3rd, drain pipe；4th, liquid level；
5th, guide groove；6th, hopper；7th, clean-up port；8th, elevator；9th, cylinder；10th, expansion link；11st, compressed air hose；12nd, baffle ring；13rd, ball
Face；14th, actuating unit；15th, blow tank；16th, water intaking valve；20th, feed well；31st, dewatering centrifuge；32nd, drying machine；41st, delay
Jet-bedding；42nd, filter press；43rd, pipeline；44th, drain valve；45th, climbing film evaporator；46th, Boiler Steam control valve；47th, gravity gas-liquid
Catch-all；48th, 50 be secondary steam pipe；49th, whirlwind catch-all；51st, concentrate dashpot；52nd, condensed water temporary tank；53、
Concentrate temporary tank；54th, concentrate efferent duct；55th, condenser；56th, low temperature water-circulating pipe；57th, vacuum machine.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
As Figure 1-Figure 8 with feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units, including machine
Body 1, the top of body 1 is provided with bagasse feed well 20；Internal body, to turning Kun A, is cylinder to turning Kun, often provided with three-level
Level is equipped with bagasse guide groove 5 to turning Kun lower sections, and afterbody guide groove connects the hopper 6 of bagasse elevator 8, elevator
Blow tank 15 connects drying machine 32 through dewatering centrifuge 31；Elevator is provided with water intaking valve 16, and body upper is provided with the He of filter 2
Drain pipe 3, the buffered groove of drain pipe 3 connection filter press, filter press connects triple effect long tube climbing-film evaporation enrichment facility, three through pipeline
Imitate the concentrated connection concentrate of liquid temporary tank 53 efferent duct 54 of long tube climbing-film evaporation enrichment facility；Cosine lacquer disk(-sc) arteries and veins is provided with body
Device of air is burst, cosine lacquer disk(-sc) pulse gas explosion device is by cosine lacquer disk(-sc) B, cylinder 9, expansion link 10, compressed air hose 11, baffle ring 12
Constituted with pot shape spherical faced pan 13, cosine lacquer disk(-sc) B-section thick middle thin edge, be shaped as being provided with below cosine curve, cosine lacquer disk(-sc)
Pot shape spherical faced pan 13, cosine lacquer disk(-sc) B connects extra-organismal cylinder 9 through expansion link 10, and cylinder 9 can drive expansion link 10 to drive cosine
Lacquer disk(-sc) B moves up and down, and the front hollow of expansion link 10 simultaneously connects the also UNICOM's cosine lacquer disk(-sc) inner chamber body of compressed air hose 11；Body lower-left
Angle is provided with mechanical ultrasonic vibrator C, is rotated at a high speed by actuating unit kinetic energy, and mechanical ultrasonic vibrator C structure is ball
Cap-shaped, and spherical cap edge is smooth continuous cosine curve, has crest, trough progressively to expand and continuous from spherical cap center to edge
The feature of diverging.
The lower section of body 1 is provided with clean-up port 7.
The top of pot shape spherical faced pan 13 is provided with baffle ring 12.
The body 1 is connected as one with elevator 8 by flange, is sealing structure and easy to disassemble.
Bagasse delivers into device top by feed well 20, and transfer roller cylinder A is extruded by three-level, passes through lifting afterwards
Machine 8 is exported.Body 1 is integrally connected with elevator 8 by flange, is that sealing structure also allows for demolition and maintenance；One is maintained during work
Fixed liquid level, device supplements water and filled into by the control of valve 16, is overflowed by drain pipe 3 and reaches liquid phase turnover balance, such sugarcane
Slag is able to realize that counter current contacting is leached with liquid phase water in the case where entering device and three-level squeezing effect, because strong extruding promotes strong inhale
Water, realizes the adverse current sugar leaching for most penetrating by force, permeating, reaches Increasing Production and Energy Saving emission reduction.
Bagasse is exported by the blow tank 15 of elevator 8, is dehydrated to dry through drying machine 32 again by centrifuge 31 and is easy to
Later use is processed, and the relatively concentrated sugar liquid of counterflow leaching is filtered by filter 2 overflows conveying by drain pipe 3, carries out triple effect long tube
Climbing-film evaporation concentration.
The concentration of triple effect long tube climbing-film evaporation is exactly briefly three tandem workings of climbing film evaporator 45 herein, and Boiler Steam is supplied
One effect climbing film evaporator 45 is as thermal source, and an effect indirect steam is used as triple effect thermal source, work as two effect thermals source, two effect indirect steams
Bagasse leachate inputs temporary dashpot 41 by drain pipe 3 when making, then carries out press filtration through pump, pipeline to filter press 42
Purification；Pressing filtering liquid is transported to the bottom of an effect climbing film evaporator 45 through pump, pipeline 43 again, and climbing film evaporator 45 is tubulation heat exchange in fact
One kind of device, tubulation caliber lesser amt is numerous, possesses enough pipe surfaces externally and internally products, and pipe with small pipe diameter is easy to intraluminal fluid by popular drama
Strong carburation by evaporation drives liquid phase to pull up a liter film forming in pipe, and boiler is connected by Boiler Steam control valve 46 between shell side and tube side
Steam, steam condensate (SC) is automatically drained out by drain valve 44, and the cavity of tube side and shell side is carried out full of suitable pressure steam to tubulation outer wall
Heating, promotes to be heated in pipe；Sugar-cane juice liquid inlet control valve controls sugarcane liquid input flow rate, makes to have in tubulation relatively suitable liquid level, together
Shi Lianxu feed liquors.The heated violent boiling of liquid phase, gas-liquid mixture gas phase expansion in tubulation drives liquid phase to gush upwards jointly
Liquid in pipe draws high film forming, there is heat transfer area inside and outside king-sized pipe, and pipe is outer to be heated by steam condensateization, intraluminal fluid phase film forming
Heated constantly vaporization, gas-liquid mixture is gushed into gravity gas-liquid catch-all 47, and gravity gas-liquid 47 water conservancy diversion cross sections of catch-all are larger,
Air velocity of gushing can be reduced, and such drop produces sedimentation because being affected by gravity, and concentrated by pipe and be transported to concentrate dashpot
51 bufferings；The indirect steam of gravity vapour-liquid catch-all 47 is carried by the tangentially connected whirlwind catch-all 49 of pipeline 48, indirect steam
A small amount of drop produces screw in whirlwind catch-all 49 and declined, and backflows to form inside spin ascending air in bottom, and last two
Secondary steam is used as next effect concentration shell side thermal source by the conveying of the water conservancy diversion of pipeline 50；Drop because gas phase drive also at a high speed rotate, from
Depart from gas phase viscous wall in whirlwind catch-all 49 under mental power function to be captured, drop is enriched with along along wall drop set, passes through pipe collection
In be transported to concentrate dashpot 51 and buffer, the lower liquid phase of concentrate dashpot 51 is concentrated through pump, pipeline to the second effect again
Two effect concentrations, similar carry out triple effect concentration are carried out again.
Triple effect indirect steam enters condenser 55 through pipeline connection, and condenser 55 connects vacuum machine 57, shell by pipeline
Journey connection low temperature water-circulating pipe 56；Vacuum machine 57 extracts incondensable gas, and condensable vapours condensed water is connected by pipeline and condensed
Water temporary tank 52, concentrate connects concentrate temporary tank 53 by pipeline, under being entered by pump, the output of concentrate efferent duct 54
One process procedure.Condensed water temporary tank 52 and concentrate temporary tank connection the general length of vertical straight tube be more than 10 meters, for gram
Take atmospheric pressure liquid phase to export automatically, be commonly called as barometric pipe.
It is cylinder to transfer roller cylinder A, it is poor to turning and extruding that corresponding bearing arrangement is easy to sealing waterproof to adapt to strength extruding
Move to turning, the sugared dissolution of counterflow leaching for promoting bagasse and water is crushed in particularly advantageous strong extruding with stranding stone roller.
Thick edge is slightly thin in the middle of core component cosine lacquer disk(-sc) B, lacquer disk(-sc) section, and general shape is cosine curve, lacquer disk(-sc) B pressures
Tight pot shape spherical faced pan 13 constitutes airtight cavity, to wherein inputting compressed air, when air pressure is increasing reaches certain value,
Lacquer disk(-sc) B can be produced to be flipped up suddenly, and explosion type release is produced to the compressed air wherein stored, can produce explosion vibration impact
Ripple, particularly advantageous promotion material gas explosion is stirred with leaching mass transfer.
Cylinder 9 can drive expansion link 10 to drive cosine lacquer disk(-sc) B to move up and down, the front hollow of expansion link 10 connection compressed air
The also UNICOM's lacquer disk(-sc) B inner chamber bodies of pipe 11；And realized by axle sleeve and body 1 isolate it is closed prevent leakage, and can flexibly stretch；When stretching
The driving lacquer disk(-sc) of contracting bar 10 B can form airtight cavity when compressing pot shape spherical faced pan 13, at this moment wherein defeated by 11 pairs of compressed air hose
Enter compressed air, air pressure rises the triggering until cosine lacquer disk(-sc) B rim pressures transfinite, produce under lacquer disk(-sc) integral pressure is acted on to
The upper compressed air internally stored that overturns produces explosion type release, and at this moment expansion link 10 bounces back again, and just energy automatic elastic is returned lacquer disk(-sc) B
Original initial state is flipped back to again, repetitive cycling action can be carried out again, and baffle ring 12 can assist cosine in case of need
Lacquer disk(-sc) B upset resets.
Mechanical ultrasonic vibrator C is rotated at a high speed, axle sleeve can be realized in the lower left corner of device by the kinetic energy of actuating unit 14
Liquid phase sealing and favourable vibrator C rotations at a high speed.
Mechanical ultrasonic vibrator C structure is spherical cap shape, and spherical cap edge is smooth continuous cosine curve, from spherical cap
Center has crest, trough progressively to expand continuous diverging feature to edge.
Such structure has good bulk strength, when mechanical ultrasonic vibrator C passes through actuating unit 14 in the liquid phase
Drive and rotate at a high speed, the strong cavitation effect of similar ultrasonic wave can be produced, strength promotes the mass transport process of counterflow leaching, and collaboration promotees
The dissolving of sugar entering is leached.
Above-mentioned simply presently preferred embodiments of the present invention, not makees any formal limitation to the present invention.It is any to be familiar with sheet
The technical staff in field, in the case where not departing from technical solution of the present invention scope, all using the technology contents of the disclosure above
Many possible variations and modification are made to technical solution of the present invention, or is revised as the equivalent embodiment of equivalent variations.Therefore, it is all
It is the content without departing from technical solution of the present invention, any is simply repaiied to made for any of the above embodiments according to the technology of the present invention essence
Change, equivalent variations and modification, all should fall in the range of technical solution of the present invention protection.
Claims (4)
1. a kind of exist with feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units, including body, its feature
In：Bagasse feed well is provided with above body；Internal body, to turning Kun, is cylinder to turning Kun, every grade right provided with three-level
Turn Kun lower sections and be equipped with bagasse guide groove, afterbody guide groove connects the hopper of bagasse elevator, the blow tank of elevator
Drying machine is connected through dewatering centrifuge；Elevator is provided with water intaking valve, and body upper is provided with filter and drain pipe, drain pipe warp
Dashpot connects filter press, and filter press connects triple effect long tube climbing-film evaporation enrichment facility through pipeline, and triple effect long tube climbing-film evaporation is dense
The concentrated liquid temporary tank connection concentrate efferent duct of compression apparatus；Cosine lacquer disk(-sc) pulse gas explosion device, cosine lacquer disk(-sc) are provided with body
Pulse gas explosion device is made up of cosine lacquer disk(-sc), cylinder, expansion link, compressed air hose, baffle ring and pot shape spherical faced pan, and cosine lacquer disk(-sc) is cut
Face thick middle thin edge, is shaped as below cosine curve, cosine lacquer disk(-sc) being provided with pot shape spherical faced pan, cosine lacquer disk(-sc) is connected through expansion link
Extra-organismal cylinder, cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compression sky
Tracheae also UNICOM's cosine lacquer disk(-sc) inner chamber body；The body lower left corner is provided with mechanical ultrasonic vibrator, by actuating unit kinetic energy at a high speed
Rotation, the structure of mechanical ultrasonic vibrator is spherical cap shape, and spherical cap edge is smooth continuous cosine curve, from spherical cap center
There is the feature that crest, trough progressively expand and continuously dissipated to edge.
2. according to claim 1 with feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units, it is special
Levy and be：Clean-up port is provided with below the body.
3. according to claim 2 with feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units, it is special
Levy and be：Baffle ring is provided with above the pot shape spherical faced pan.
4. according to claim 3 with feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units, it is special
Levy and be：The body is connected as one with elevator by flange, is sealing structure and easy to disassemble.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710738197.2A CN107312888A (en) | 2017-08-25 | 2017-08-25 | With feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710738197.2A CN107312888A (en) | 2017-08-25 | 2017-08-25 | With feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units |
Publications (1)
| Publication Number | Publication Date |
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| CN107312888A true CN107312888A (en) | 2017-11-03 |
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|---|---|---|---|
| CN201710738197.2A Withdrawn CN107312888A (en) | 2017-08-25 | 2017-08-25 | With feed well, centrifuge and drying machine to turning Kun cartridge type bagasse processing units |
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| CN (1) | CN107312888A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111059865A (en) * | 2019-11-27 | 2020-04-24 | 秦子媛 | Continuous processing device of silage |
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2017
- 2017-08-25 CN CN201710738197.2A patent/CN107312888A/en not_active Withdrawn
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111059865A (en) * | 2019-11-27 | 2020-04-24 | 秦子媛 | Continuous processing device of silage |
| CN111059865B (en) * | 2019-11-27 | 2023-07-14 | 秦子媛 | Continuous processing device for silage |
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Application publication date: 20171103 |
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