CN107841456A - Sinusoidal pulley type stalk Integrated Processing Unit with break process - Google Patents
Sinusoidal pulley type stalk Integrated Processing Unit with break process Download PDFInfo
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- CN107841456A CN107841456A CN201710924829.4A CN201710924829A CN107841456A CN 107841456 A CN107841456 A CN 107841456A CN 201710924829 A CN201710924829 A CN 201710924829A CN 107841456 A CN107841456 A CN 107841456A
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M21/00—Bioreactors or fermenters specially adapted for specific uses
- C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/36—Means for collection or storage of gas; Gas holders
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/24—Recirculation of gas
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/16—Screw conveyor
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/40—Means for regulation, monitoring, measurement or control, e.g. flow regulation of pressure
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M43/00—Combinations of bioreactors or fermenters with other apparatus
- C12M43/04—Bioreactors or fermenters combined with combustion devices or plants, e.g. for carbon dioxide removal
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M45/00—Means for pre-treatment of biological substances
- C12M45/02—Means for pre-treatment of biological substances by mechanical forces; Stirring; Trituration; Comminuting
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/12—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
- F26B17/14—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas
- F26B17/1433—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material
- F26B17/1466—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material the members or bodies being in movement
- F26B17/1475—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material the members or bodies being in movement the movement being a vibration or oscillation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
- F26B21/002—Drying-air generating units, e.g. movable, independent of drying enclosure heating the drying air indirectly, i.e. using a heat exchanger
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/001—Handling, e.g. loading or unloading arrangements
- F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/04—Agitating, stirring, or scraping devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/02—Biomass, e.g. waste vegetative matter, straw
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Abstract
The invention discloses a kind of sinusoidal pulley type stalk Integrated Processing Unit with break process, including sinusoidal roller, biogas fermentation groove, biogas storage tank, counter-current drying tower, biogas combustion machine and methane boiler, biogas fermentation groove lower left quarter is provided with sinusoidal ultrasound wave vibrator, upper right quarter passes through pipeline, roots blower link slot bottom, roots blower outlet connection biogas storage tank, biogas storage tank passes through pipeline, biogas combustion machine connects methane boiler, methane boiler connects counter-current drying tower by steam fin air-heater, counter-current drying tower upper left quarter is sequentially connected spiral and closes wind charger and sinusoidal roller, sinusoidal roller and the sinusoidal ultrasound wave vibrator of the present invention all has distinguishing feature, energy reliable collaborative realizes comprehensive development and utilization to the king-sized agricultural crop straw of moisture gradient and discarded object.
Description
Technical field
The present invention relates to a kind of sinusoidal pulley type stalk Integrated Processing Unit with break process.
Background technology
Agricultural crop straw and agricultural wastes are the major garbage of agricultural production industry, waste, and agricultural wastes are typically adopted now
Crushing straw returning to the field, burning and the processing mode for manufacturing biomass fuel are taken, but straw-returning can not make the energy reality that it is rich in
Existing effect utilizes, and manufacture biomass fuel has high requirements again to the moisture of agricultural wastes, burns again especially pollution environment, because
And it is difficult the different agricultural waste of efficient integrated treatment moisture height and carries out efficient twice laid.If it can design more advanced
Sinusoidal pulley type stalk Integrated Processing Unit with break process, it is adapted to the agricultural wastes processing that moisture gradient is big.This is right
There is especially important meaning in improving agriculture industrialization circulation economies of scale.
The content of the invention
The technical problem to be solved in the present invention is exactly overcome the deficiencies in the prior art, there is provided a kind of sine with break process
Pulley type stalk Integrated Processing Unit.
For overcome the deficiencies in the prior art, the present invention takes following technical scheme:
A kind of sinusoidal pulley type stalk Integrated Processing Unit with break process, including the storage of sinusoidal roller, biogas fermentation groove, biogas
Tank, counter-current drying tower, biogas combustion machine and methane boiler, it is characterised in that:Agitating paddle, agitating paddle are provided with inside biogas fermentation groove
Connected by agitating shaft and the stirring motor reductor at top, biogas fermentation groove top portion connects feed water valve by pipeline, and top connects
Connect L-shaped to hold one's breath feeding packing auger, L-shaped is held one's breath feeding packing auger top connection feed well, and feed well top is provided with pulverizer, biogas fermentation
Groove lower left quarter is provided with sinusoidal ultrasound wave vibrator, and biogas fermentation trench bottom is tapered, and connecting pump by pipeline, transfusion control valve enters
Mouthful, biogas fermentation groove upper right quarter connects biogas fermentation trench bottom pipeline, Roots by biogas pipe, roots blower, air-blowing control valve
Fan outlet is connected by pipeline, gas storage control valve, appendix and biogas storage tank top, biogas tank top connection pressure gauge,
Bottom connects blowoff valve by pipeline, and biogas storage tank top connects natural pond by appendix, burning supply control valve, biogas combustion machine
Gas boiler, methane boiler top connection boiler exhaust gas pipe, methane boiler top passes through steam pipe, steam control valve connects steam wing
Piece air-heater, steam fin air-heater are connected by pipeline with counter-current drying tower bottom, and stacking sieve is provided with inside counter-current drying tower
Shape cone bucket, cone disk, cone disk diameter is slightly larger than cone bucket, and cone tray bottom has automatically controlled bin gate, and counter-current drying tower top is closed provided with spiral
Wind charger and offgas duct, spiral close wind charger import top and are provided with sinusoidal roller, and sinusoidal roller surface is continuous sinusoidal bent
Face, blower outlet are connected through steam fin air-heater with counter-current drying tower bottom, and the connection of counter-current drying tower bottom is closed wind and gone out
Material machine;Sinusoidal ultrasound wave vibrator is driven by actuating unit, the speed governing rotation of energy high speed, and the structure of sinusoidal ultrasound wave vibrator is
Spherical cap shape, and spherical cap edge is smooth continuous sine curve, has crest, trough progressively to expand continuously from spherical cap center to edge
Dissipate feature.
Its prevailing technology of Integrated Processing Unit process system is to handle agricultural waste material respectively by moisture height,
The higher fresh waste delivery of cumulative water-oil ratio enters fermentation tank and carries out high-efficiency fermenting degraded producing methane, and biogas is used to drive methane boiler to produce
Raw steam, aqueous relatively low agricultural wastes progress highly effective drying is squeezed to rubbing with the hands using steam.
Biogas fermentation groove maintains 2/3rds liquid level, water, material can be held one's breath as needed for supplementing feed water valve by L-shaped
Feeding packing auger prevents gas from leaking using water seal closed-type feed, while is advantageous to slight positive pressure state in retention groove.Groove top portion is stirred
Mix agitating paddle in motor reducer driver slot to rotate, bottom land taper is easy to material to export.
The sinusoidal ultrasound wave vibrator of cell body lower left quarter is driven by actuating unit, and the speed governing rotation of energy high speed, axle sleeve can be real
Simultaneously favourable sinusoidal ultrasound wave vibrator rotates at a high speed for existing liquid phase sealing.The structure of sinusoidal ultrasound wave vibrator is spherical cap shape, and ball
Lid edge is smooth continuous sine curve, has crest, trough progressively to expand continuous diverging feature from spherical cap center to edge.This
The structure of sample has good bulk strength, when sinusoidal ultrasound wave vibrator passes through actuating unit kinetic energy high speed speed governing in the liquid phase
Rotation, it is clear that the strong cavitation effect of similar ultrasonic wave can be produced, effectively facilitate mass transfer process, collaboration air-blowing, temperature control, stirring promote
Enter fermentation, realize that efficient fast microbiological effect makes material fermentation degrade.
Favorably the ferment liquid phase material thoroughly degraded of bottom land taper be used as naturally by pipeline, transfusion control valve, pump output
Fertilizer application, biogas fermentation groove upper right quarter have biogas pipe output biogas is pressurized through roots blower, air-blowing control valve controls can be by natural pond
Gas fermentation tank cone bottom, which imports, realizes that gas phase circulation collaboration promotion stirs, and can also be circulated and evacuated by gas when liquid phase exports
Bore the material of bottom sedimentation.Roots blower energy automatic start supercharging output biogas passes through gas storage control when fermentation tank biogas produces pressure-fired
It is temporary or provide combustion through burning supply control valve control for the biogas combustion machine of methane boiler that valve processed, appendix import biogas storage tank
Material.Steam fin heat of the steam caused by methane boiler by steam control valve through steam pipe output for counter-current drying tower right lower quadrant
Blower fan heat supply, or greenhouse provide thermal source.
Aqueous less agricultural crop straw through differential stranding fine groundization of sinusoidal roller extruding, be easy to subsequently to input inverse by such material
Operation is dried in stream drying tower.Sinusoidal roller surface is continuous sine surface, corresponding bearing arrangement sealing and dustproof, is also adapted to
Strongly extruding, can the particularly advantageous extruding by force of convenient adjusting roller spacing and roller differential pair turn stranding stone roller to turning and extruding differential pair turn
Crush and promote stalk refinement, be easy to follow-up highly effective drying.Sinusoidal roller bites that continuous reliable, extruding compression ratio is special to material
Greatly, the differential stranding of sinusoidal roller curved surface grinds reliable, durable, skimming over property is good, and separating twice effect is especially good while energy consumption is also especially low.
Counter-current drying tower top has spiral to close wind charger and offgas duct, and there are stacking sieve-like cone bucket, cone disk in inside, it is straight to bore disk
Footpath is slightly larger than cone bucket, and cone tray bottom has electric controlled door, and cone bucket, cone disk energy controlled vibration coordinate electric controlled door opening and closing to be easy to material to expand
Scattered, stop drying also can be moved downward successively, and such material can be realized inverse with the heat transfer of thermal updrafts composition counter current contacting, mass transfer
Drying is flowed, damp and hot tail gas is discharged by offgas duct, and dried material then exports by closing wind discharging machine.Air blower blasts air through steam
Fin air-heater is heated to be high temperature air and passes through drying tower from bottom to top.
Rational insulation processing is carried out to apparatus system, reduces radiation loss.
Compared with prior art, beneficial effects of the present invention also reside in:
Sinusoidal roller material, which bites continuously reliable, extruding and rubbed with the hands, grinds material thinning effect brilliance, while energy consumption is also especially low;
Sinusoidal ultrasound wave vibrator is rotated by the speed governing of actuating unit kinetic energy high speed in the liquid phase, produces the strong of similar ultrasonic wave
Cavitation effect, effectively facilitates mass transfer process, and collaboration promotes fermentation to realize efficient Quick material degraded.
Two measures of the above all have distinguishing feature, and energy reliable collaborative is to the king-sized agricultural crop straw of moisture gradient
Comprehensive development and utilization is realized with discarded object, there is complete unexpected operation principle and effect, while design also has
Extremely strong creative and good popularizing application prospect.
Brief description of the drawings
Fig. 1 is the planar structure schematic diagram of the present invention.
Fig. 2 is the main structure diagram of sinusoidal ultrasound wave vibrator.
Fig. 3 is the overlooking the structure diagram of sinusoidal ultrasound wave vibrator.
Fig. 4 is the present invention looks up structural representation of sinusoidal ultrasound wave vibrator.
Fig. 5 is the strabismus structural representation of bowing of sinusoidal ultrasound wave vibrator.
Fig. 6 is the oblique present invention looks up structural representation of sinusoidal ultrasound wave vibrator.
Fig. 7 is sinusoidal drum structure schematic diagram.
Each label represents in figure:
A, sinusoidal roller;C, sinusoidal ultrasound wave vibrator;1st, biogas fermentation groove;2nd, biogas storage tank;3rd, counter-current drying tower;4th, biogas
Boiler;5th, burning supply control valve;6th, biogas combustion machine;7th, steam control valve;8th, steam pipe;9th, boiler exhaust gas pipe;10th, supply water
Valve;11st, stirring motor reductor;12nd, feed well;13rd, agitating paddle;14th, biogas pipe;15th, roots blower;16th, transfusion control valve;
17th, air-blowing control valve;18th, gas storage control valve;19th, L-shaped is held one's breath feeding packing auger;20th, pressure gauge;21st, blowoff valve;22nd, horizon;
23rd, appendix;24th, pulverizer;31st, spiral closes wind charger;32nd, offgas duct;33rd, steam fin air-heater;34th, air blower;
35th, wind discharging machine is closed;42nd, cone bucket;43rd, disk is bored;44th, automatically controlled bin gate.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
A kind of sinusoidal pulley type stalk Integrated Processing Unit with break process as shown in Fig. 1~Fig. 7, including sinusoidal roller
A, biogas fermentation groove 1, biogas storage tank 2, counter-current drying tower 3, biogas combustion machine 6 and methane boiler 4, it is characterised in that:Biogas is sent out
The inside of ferment groove 1 is provided with agitating paddle 13, and agitating paddle 13 is connected by the stirring motor reductor 11 at agitating shaft and top, biogas fermentation
The top of groove 1 connects feed water valve 10 by pipeline, and top connection L-shaped is held one's breath feeding packing auger 19, and L-shaped is held one's breath the top of feeding packing auger 19 company
Hopper 12 is tapped into, the top of feed well 12 is provided with pulverizer 24, and the lower left quarter of biogas fermentation groove 1 is provided with sinusoidal ultrasound wave vibrator C, natural pond
The bottom of gas fermentation tank 1 is tapered, connects pump inlet by pipeline, transfusion control valve 16, the upper right quarter of biogas fermentation groove 1 passes through biogas
Pipe 14, roots blower 15, air-blowing control valve 17 connect the bottom pipe of biogas fermentation groove 1, and the outlet of roots blower 15 passes through pipeline, storage
Gas control valve 18, appendix 23 are connected with the top of biogas storage tank 2, and the top of biogas storage tank 2 connection pressure gauge 20, bottom passes through pipeline
Blowoff valve 21 is connected, the top of biogas storage tank 2 connects biogas pot by appendix 23, burning supply control valve 5, biogas combustion machine 6
Stove 4, the top of methane boiler 4 connection boiler exhaust gas pipe 9, the top of methane boiler 4 connects steam by steam pipe 8, steam control valve 7
Fin air-heater 33, steam fin air-heater 33 are connected with the bottom of counter-current drying tower 3 by pipeline, set inside counter-current drying tower 3
There are stacking sieve-like cone bucket 42, cone disk 43, the cone diameter of disk 43 is slightly larger than cone bucket 42, and automatically controlled bin gate 44 is arranged at cone disk 43 bottom, adverse current
Wind charger 31 and offgas duct 32 are closed in the top of drying tower 3 provided with spiral, and spiral closes the import top of wind charger 31 and is provided with sinusoidal roller
Cylinder A, sinusoidal roller A surfaces are continuous sine surface, and the air outlet of air blower 34 is through steam fin air-heater 33 and counter-current drying tower 3
Bottom connects, and wind discharging machine 35 is closed in the connection of the bottom of counter-current drying tower 3;Sinusoidal ultrasound wave vibrator C is driven by actuating unit, energy
High speed speed governing rotates, and sinusoidal ultrasound wave vibrator C structure is spherical cap shape, and spherical cap edge is smooth continuous sine curve,
There are crest, trough progressively to expand continuous diverging feature from spherical cap center to edge.
Its prevailing technology of Integrated Processing Unit process system is to handle agricultural waste material respectively by moisture height,
The higher fresh waste delivery of cumulative water-oil ratio enters fermentation tank and carries out high-efficiency fermenting degraded producing methane, and biogas is used to drive methane boiler to produce
Raw steam, aqueous relatively low agricultural wastes progress highly effective drying is squeezed to rubbing with the hands using steam.
Biogas fermentation groove 1 maintains 2/3rds liquid level, can supplement required water by feed water valve 10, material passes through L-shaped
Feeding packing auger of holding one's breath 19 prevents gas from leaking using water seal closed-type feed, while is advantageous to slight positive pressure state in retention groove.Groove top
Agitating paddle 13 rotates in the driver slot of stirring motor reductor 11 in portion, and bottom land taper is easy to material to export.
The sinusoidal ultrasound wave vibrator C of cell body lower left quarter is driven by actuating unit, and the speed governing rotation of energy high speed, axle sleeve can be real
Simultaneously favourable sinusoidal ultrasound wave vibrator C rotates at a high speed for existing liquid phase sealing.Sinusoidal ultrasound wave vibrator C structure is spherical cap shape, and
Spherical cap edge is smooth continuous sine curve, has crest, trough progressively to expand continuous diverging feature from spherical cap center to edge.
Such structure has good bulk strength, when sinusoidal ultrasound wave vibrator C passes through actuating unit kinetic energy high speed in the liquid phase
Speed governing rotates, it is clear that can produce the strong cavitation effect of similar ultrasonic wave, effectively facilitate mass transfer process, collaboration air-blowing, temperature control, stir
Promotion fermentation is mixed, realizes that efficient fast microbiological effect makes material fermentation degrade.
Favorably the ferment liquid phase material thoroughly degraded of bottom land taper is used as day by pipeline, transfusion control valve 16, pump output
Right Fertilizer application, the upper right quarter of biogas fermentation groove 1 has the output of biogas pipe 14, and biogas is pressurized through roots blower 15, air-blowing control valve 17 is controlled
System can be bored bottom importing by biogas fermentation groove 1 and realize that gas phase circulation collaboration promotion stirs, and be able to can also be passed through when liquid phase exports
The material of gas circulation evacuation cone bottom sedimentation.Roots blower 15 can automatic start supercharging output natural pond when fermentation tank biogas produces pressure-fired
It is methane boiler that gas is imported biogas storage tank 2 and kept in or controlled through burning supply control valve 5 by gas storage control valve 18, appendix 23
4 biogas combustion machine 6 provides fuel.Steam caused by methane boiler 4 is adverse current through the output of steam pipe 8 by steam control valve 7
The heat supply of steam fin air-heater 33 of the right lower quadrant of drying tower 3, or greenhouse provide thermal source.
Aqueous less agricultural crop straw is easy to subsequently input through differential stranding fine groundization of sinusoidal roller A extruding, such material
Operation is dried in counter-current drying tower 3.Sinusoidal roller A surfaces are continuous sine surface, corresponding bearing arrangement sealing and dustproof,
Strength extruding is adapted to turning and extruding differential pair to turn, can the particularly advantageous strong extruding of convenient adjusting roller spacing and roller differential pair turn
Rub with the hands to grind to crush and promote stalk refinement, be easy to follow-up highly effective drying.Sinusoidal roller A bites continuous reliable, extruding compression ratio to material
Especially big, the sinusoidal differential stranding of roller A curved surfaces grinds reliable, durable, skimming over property is good, and separating twice effect is especially good while energy consumption is also special
It is not low.
The top of counter-current drying tower 3 has spiral to close wind charger 31 and offgas duct 32, and there are stacking sieve-like cone bucket 42, cone disk in inside
43, the cone diameter of disk 43 is slightly larger than cone bucket 42, and electric controlled door 44 is arranged at cone disk 43 bottom, and cone bucket, cone disk energy controlled vibration coordinate automatically controlled
The opening and closing of door 44 is easy to material diffusion, stop drying also can successively move downward, and such material can form adverse current with thermal updrafts
Transmission of heat by contact, mass transfer realize counter-current drying, and damp and hot tail gas is discharged by offgas duct, and dried material is then defeated by closing wind discharging machine 35
Go out.Air blower 34 blasts air and is heated to be high temperature air through steam fin air-heater 33 passes through drying tower from bottom to top.
Rational insulation processing is carried out to apparatus system, reduces radiation loss.
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 changes and modifications are made to technical solution of the present invention, or are 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 (1)
1. a kind of sinusoidal pulley type stalk Integrated Processing Unit with break process, including sinusoidal roller, biogas fermentation groove, biogas
Storage tank, counter-current drying tower, biogas combustion machine and methane boiler, it is characterised in that:Agitating paddle is provided with inside biogas fermentation groove, is stirred
Oar is connected by agitating shaft and the stirring motor reductor at top, and biogas fermentation groove top portion connects feed water valve, top by pipeline
Connection L-shaped is held one's breath feeding packing auger, and L-shaped is held one's breath feeding packing auger top connection feed well, and feed well top is provided with pulverizer, and biogas is sent out
Ferment groove lower left quarter is provided with sinusoidal ultrasound wave vibrator, and biogas fermentation trench bottom is tapered, and pump is connected by pipeline, transfusion control valve
Import, biogas fermentation groove upper right quarter connect biogas fermentation trench bottom pipeline, sieve by biogas pipe, roots blower, air-blowing control valve
Thatch fan outlet is connected by pipeline, gas storage control valve, appendix and biogas storage tank top, biogas tank top connection pressure
Table, bottom connect blowoff valve by pipeline, and biogas storage tank top is connected by appendix, burning supply control valve, biogas combustion machine
Methane boiler is connect, methane boiler top connection boiler exhaust gas pipe, methane boiler top passes through steam pipe, steam control valve connection is steamed
Vapour fin air-heater, steam fin air-heater are connected by pipeline with counter-current drying tower bottom, and layer is provided with inside counter-current drying tower
Folded sieve-like cone bucket, cone disk, cone disk diameter is slightly larger than cone bucket, and cone tray bottom has automatically controlled bin gate, and counter-current drying tower top is provided with spiral shell
Traling wind charger and offgas duct, spiral close wind charger import top and are provided with sinusoidal roller, sinusoidal roller surface for it is continuous just
String curved surface, blower outlet are connected through steam fin air-heater with counter-current drying tower bottom, and the connection of counter-current drying tower bottom is closed
Wind discharging machine;Sinusoidal ultrasound wave vibrator is driven by actuating unit, the speed governing rotation of energy high speed, the knot of sinusoidal ultrasound wave vibrator
Structure is spherical cap shape, and spherical cap edge is smooth continuous sine curve, has crest, trough progressively to expand from spherical cap center to edge
Continuous diverging feature.
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CN201710924829.4A CN107841456A (en) | 2017-10-02 | 2017-10-02 | Sinusoidal pulley type stalk Integrated Processing Unit with break process |
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Application Number | Priority Date | Filing Date | Title |
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CN201710924829.4A CN107841456A (en) | 2017-10-02 | 2017-10-02 | Sinusoidal pulley type stalk Integrated Processing Unit with break process |
Publications (1)
Publication Number | Publication Date |
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CN107841456A true CN107841456A (en) | 2018-03-27 |
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CN201710924829.4A Withdrawn CN107841456A (en) | 2017-10-02 | 2017-10-02 | Sinusoidal pulley type stalk Integrated Processing Unit with break process |
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2017
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