CN107860205A - Tendons pulley type stalk Integrated Processing Unit with break process - Google Patents

Tendons pulley type stalk Integrated Processing Unit with break process Download PDF

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Publication number
CN107860205A
CN107860205A CN201710924835.XA CN201710924835A CN107860205A CN 107860205 A CN107860205 A CN 107860205A CN 201710924835 A CN201710924835 A CN 201710924835A CN 107860205 A CN107860205 A CN 107860205A
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China
Prior art keywords
biogas
counter
lacquer disk
drying tower
tendons
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CN201710924835.XA
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Chinese (zh)
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祖慧楠
熊敏
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Individual
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Priority to CN201710924835.XA priority Critical patent/CN107860205A/en
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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
    • 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
    • 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
    • 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
    • C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02—Stirrer or mobile mixing elements
    • 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
    • C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/24—Recirculation of gas
    • 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
    • C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
    • C12M33/16—Screw conveyor
    • 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
    • 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
    • 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
    • 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
    • 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
    • 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

Abstract

The invention discloses a kind of tendons pulley type stalk Integrated Processing Unit with break process,Including tendons 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 tendons roller,Counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device,The tendons roller of the present invention,Cosine lacquer disk(-sc) pulse gas explosion device and sinusoidal ultrasound wave vibrator all have distinguishing feature,Energy reliable collaborative realizes comprehensive development and utilization to the king-sized agricultural crop straw of moisture gradient and discarded object.

Description

Tendons pulley type stalk Integrated Processing Unit with break process
Technical field
The present invention relates to a kind of tendons 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 Tendons 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 tendons 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 tendons pulley type stalk Integrated Processing Unit with break process, including the storage of tendons 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 tendons roller, and tendons roller surface is provided with axially even The tendons of cloth, blower outlet are connected through steam fin air-heater with counter-current drying tower bottom, the connection of counter-current drying tower bottom Wind discharging machine is closed, counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device；Cosine lacquer disk(-sc) pulse gas explosion device is by remaining String lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan composition, cosine lacquer disk(-sc) section centre are thick Edge is slightly thin, and general shape is cosine curve, and pot shape spherical faced pan is provided with below cosine lacquer disk(-sc), and cosine lacquer disk(-sc) connects machine through expansion link External cylinder, cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compressed air Pipe also connects cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator is driven by actuating unit, the speed governing rotation of energy high speed, and sine is super The structure of sound wave vibrator is spherical cap shape, and spherical cap edge is smooth continuous sine curve, has ripple from spherical cap center to edge Peak, trough progressively expand continuous diverging feature.
Shield is provided with above the cosine lacquer disk(-sc) pulse gas explosion device, cosine lacquer disk(-sc) pulse gas explosion device is stretched out machine by shield External part is covered, and makes counter-current drying tower associative perception preferable, and the convenient maintenance of gas explosion device can be carried out by removing shield.
Baffle ring is provided with above the pot shape spherical faced pan.
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 tendons roller extruding, be easy to subsequently to input inverse by such material Operation is dried in stream drying tower.Tendons roller surface is provided with the tendons of axially even cloth, corresponding bearing arrangement sealing and dustproof, Strength extruding is also 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 to rub with the hands to grind to crush and promote stalk refinement, be easy to follow-up highly effective drying.Tendons roller bites continuous reliable, extruding compression ratio to material Especially big, the differential stranding of tendons roller 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.Counter-current drying tower lower left quarter has cosine lacquer disk(-sc) pulse gas explosion Device, energy explosion type release compressed air produce the pulsation of gas explosion material, and collaboration tower type counterflow drying obtains unthinkable drying Effect.
Rational insulation processing is carried out to apparatus system, reduces radiation loss.
Core component cosine lacquer disk(-sc), the thick edge in lacquer disk(-sc) section centre is slightly thin, and general shape is cosine curve, and lacquer disk(-sc) compresses Pot shape spherical faced pan forms airtight cavity, to wherein inputting compressed air, when air pressure is increasing reaches certain value, and lacquer disk(-sc) It can produce and be flipped up suddenly, explosion type release is produced to the compressed air wherein stored, explosion vibration shock wave can be produced, it is special Not favorably material gas explosion is promoted to stir and counter-current drying.
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 connects Logical lacquer disk(-sc) inner chamber body, and realized by axle sleeve with body and isolate airtight connection, and can flexibly stretch, when expansion link drives lacquer disk(-sc) pressure Airtight cavity can be formed during tight pot shape spherical faced pan, at this moment by compressed air hose to wherein inputting compressed air, in air pressure The triggering until cosine lacquer disk(-sc) rim pressure transfinites is risen, it is empty to produce the compression for being flipped up internally storing under the effect of lacquer disk(-sc) integral pressure Gas produces explosion type release, and at this moment expansion link bounces back again, lacquer disk(-sc) just can automatic elastic reply and be flipped back to original initial state, can be with Repetitive cycling action is carried out again, and baffle ring can assist the upset of cosine lacquer disk(-sc) to reset in case of need.
Compared with prior art, beneficial effects of the present invention also reside in：
Tendons roller material, which bites continuously reliable, extruding and rubbed with the hands, grinds material thinning effect brilliance, while energy consumption is also especially low；
Cosine lacquer disk(-sc) pulse gas explosion device can be simulated effectively, produce macroscopical discontinuous blast, and excitation drying tower gas phase is pulsed by force punching Hit, the collaboration of gas explosion turning over materials promotes adverse current highly effective drying；
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.
Above three measures 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 tendons drum structure schematic diagram.
Fig. 8 is the partial enlargement structural representation of cosine lacquer disk(-sc) pulse gas explosion device.
Each label represents in figure：
A, tendons roller；B, cosine lacquer disk(-sc) pulse gas explosion device；C, sinusoidal ultrasound wave vibrator；1st, biogas fermentation groove；2nd, biogas Storage tank；3rd, counter-current drying tower；4th, methane boiler；5th, burning supply control valve；6th, biogas combustion machine；7th, steam control valve；8th, steam Steam pipe；9th, boiler exhaust gas pipe；10th, feed 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；20、 Pressure gauge；21st, blowoff valve；22nd, horizon；23rd, appendix；24th, pulverizer；30th, shield；31st, spiral closes wind charger；32、 Offgas duct；33rd, steam fin air-heater；34th, air blower；35th, wind discharging machine is closed；36th, compressed air hose；37th, cylinder；38th, axle Set；39th, expansion link；40th, spherical faced pan；41st, baffle ring；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 tendons pulley type stalk Integrated Processing Unit with break process as shown in Fig. 1~Fig. 8, including tendons 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 tendons roller Cylinder A, tendons roller A surfaces are provided with the tendons of axially even cloth, and the air outlet of air blower 34 is through steam fin air-heater 33 and adverse current The bottom of drying tower 3 connects, and wind discharging machine 35 is closed in the connection of the bottom of counter-current drying tower 3, and the lower left quarter of counter-current drying tower 3 is provided with cosine lacquer disk(-sc) Pulse gas explosion device B；Cosine lacquer disk(-sc) pulse gas explosion device B is by cosine lacquer disk(-sc), cylinder 37, expansion link 39, axle sleeve 38, compressed air Pipe 36, baffle ring 41 and pot shape spherical faced pan 40 form, and thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is that cosine is bent Line, cosine lacquer disk(-sc) lower section are provided with pot shape spherical faced pan 40, and cosine lacquer disk(-sc) connects extra-organismal cylinder 37, the energy of cylinder 37 through expansion link 39 Expansion link 39 is driven to drive cosine lacquer disk(-sc) to move up and down, the front hollow of expansion link 39 simultaneously connects compressed air hose 36 and also connects cosine Lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator C is driven by actuating unit, the speed governing rotation of energy high speed, sinusoidal ultrasound wave vibrator C Structure be spherical cap shape, and spherical cap edge is smooth continuous sine curve, has crest, trough from spherical cap center to edge progressively Expand continuous diverging feature.
It is provided with shield 30 above the cosine lacquer disk(-sc) pulse gas explosion device B, shield 30 is by cosine lacquer disk(-sc) pulse gas explosion device B Stretch out extra-organismal part to cover, make the associative perception of counter-current drying tower 3 preferable, the convenient dimension of gas explosion device can be carried out by removing shield Shield.
The top of pot shape spherical faced pan 40 is provided with baffle ring 41.
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 tendons roller A extruding, such material Operation is dried in counter-current drying tower 3.Tendons roller A surfaces are provided with the tendons of axially even cloth, corresponding bearing arrangement sealing It is dust-proof, it is also adapted to strength extruding and turns to turning and extruding differential pair, can the particularly advantageous strong extruding of convenient adjusting roller spacing and roller Differential pair, which turns to rub with the hands to grind to crush, promotes stalk refinement, is easy to follow-up highly effective drying.Tendons roller A bites continuous reliable, crowded to material Press compression ratio especially big, tendons roller A is differential rub with the hands grind reliable, durable, skimming over property is good, separating twice effect is especially good while energy consumption Also it is especially 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.Adverse current is dry The dry lower left quarter of tower 3 has cosine lacquer disk(-sc) pulse gas explosion device B, and energy explosion type release compressed air produces the pulsation of gas explosion material, collaboration Tower type counterflow, which is dried, obtains unthinkable drying effect.
Rational insulation processing is carried out to apparatus system, reduces radiation loss.
Core component cosine lacquer disk(-sc) B, the thick edge in lacquer disk(-sc) section centre is slightly thin, and general shape is cosine curve, and lacquer disk(-sc) B is pressed Tight pot shape spherical faced pan 40 forms 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, is produced explosion type release to the compressed air wherein stored, can be produced explosion vibration impact Ripple, particularly advantageous promotion material gas explosion is stirred and counter-current drying.
Cylinder 37 can drive expansion link 39 to drive cosine lacquer disk(-sc) B to move up and down, and the connection compression of the front hollow of expansion link 39 is empty Tracheae 36 also connects lacquer disk(-sc) B inner chamber bodies, and is realized by axle sleeve 38 with body 3 and isolate airtight connection, and can flexibly stretch, when stretching Contracting bar 39 drives lacquer disk(-sc) B to form airtight cavity when compressing pot shape spherical faced pan 40, at this moment by compressed air hose 36 to wherein defeated Enter compressed air, air pressure rises the triggering until cosine lacquer disk(-sc) B rim pressures transfinite, produce under lacquer disk(-sc) integral pressure acts on to The upper compressed air internally stored that overturns produces explosion type release, and at this moment expansion link 39 bounces back again, and just energy automatic elastic returns lacquer disk(-sc) B Original initial state is flipped back to again, can carry out repetitive cycling action again, and baffle ring 41 can assist cosine in case of need Lacquer disk(-sc) B upset resets.
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 (3)

1. a kind of tendons pulley type stalk Integrated Processing Unit with break process, including tendons 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 tendons roller, and tendons roller surface is provided with axle To the tendons of even cloth, blower outlet is connected through steam fin air-heater with counter-current drying tower bottom, counter-current drying tower bottom Wind discharging machine is closed in connection, and counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device；Cosine lacquer disk(-sc) pulse gas explosion device It is made up of cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan, among cosine lacquer disk(-sc) section Thick edge is slightly thin, and general shape is cosine curve, is provided with pot shape spherical faced pan below cosine lacquer disk(-sc), cosine lacquer disk(-sc) connects through expansion link Extra-organismal cylinder is connect, cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compression Air hose also connects cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator is driven by actuating unit, the speed governing rotation of energy high speed, just The structure of string ultrasonic wave excitation device is spherical cap shape, and spherical cap edge is smooth continuous sine curve, from spherical cap center to edge There are crest, trough progressively to expand continuous diverging feature.
2. the tendons pulley type stalk Integrated Processing Unit with break process according to claim 1, it is characterised in that：It is described Shield is provided with above cosine lacquer disk(-sc) pulse gas explosion device, cosine lacquer disk(-sc) pulse gas explosion device is stretched out extra-organismal component cover by shield Firmly, make counter-current drying tower associative perception preferable, the convenient maintenance of gas explosion device can be carried out by removing shield.
3. the tendons pulley type stalk Integrated Processing Unit with break process according to claim 1, it is characterised in that：It is described Baffle ring is provided with above pot shape spherical faced pan.
CN201710924835.XA 2017-10-02 2017-10-02 Tendons pulley type stalk Integrated Processing Unit with break process Withdrawn CN107860205A (en)

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102517199A (en) * 2011-11-17 2012-06-27 西安建筑科技大学 Multi-cycle stirring egg-shaped anaerobic fermentation system
CN105021012A (en) * 2015-08-14 2015-11-04 吉首大学 Hot-air drying machine capable of utilizing waste heat and achieving penetrating countercurrent fluidization
CN105621849A (en) * 2016-01-21 2016-06-01 江苏兆盛环保股份有限公司 Air shockwave crushing sludge drying device and sludge shockwave drying system
CN106895414A (en) * 2017-01-06 2017-06-27 湖州南太湖环保能源有限公司 Kitchen castoff cooperates with handling process with domestic garbage burning electricity generation

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102517199A (en) * 2011-11-17 2012-06-27 西安建筑科技大学 Multi-cycle stirring egg-shaped anaerobic fermentation system
CN105021012A (en) * 2015-08-14 2015-11-04 吉首大学 Hot-air drying machine capable of utilizing waste heat and achieving penetrating countercurrent fluidization
CN105621849A (en) * 2016-01-21 2016-06-01 江苏兆盛环保股份有限公司 Air shockwave crushing sludge drying device and sludge shockwave drying system
CN106895414A (en) * 2017-01-06 2017-06-27 湖州南太湖环保能源有限公司 Kitchen castoff cooperates with handling process with domestic garbage burning electricity generation

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Application publication date: 20180330