CN107816879A - Stalk Integrated Processing Unit with break process - Google Patents
Stalk Integrated Processing Unit with break process Download PDFInfo
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- CN107816879A CN107816879A CN201710924851.9A CN201710924851A CN107816879A CN 107816879 A CN107816879 A CN 107816879A CN 201710924851 A CN201710924851 A CN 201710924851A CN 107816879 A CN107816879 A CN 107816879A
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- biogas
- drying tower
- lacquer disk
- counter
- current drying
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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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- 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
- 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
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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
- F26B21/00—Arrangements for supplying or controlling air or other gases for drying solid materials or objects
- F26B21/001—Air generating units, e.g. movable or independent of drying enclosure
- F26B21/002—Air generating units, e.g. movable or independent of drying enclosure with means for indirect air heating, i.e. using heat exchangers
-
- 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
-
- 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 goods
- F26B2200/02—Biomass, e.g. waste vegetative matter, straw
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Abstract
The invention discloses a kind of 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,Counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device,The sinusoidal 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
Technical field
The present invention relates to a kind of 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
Stalk Integrated Processing Unit with break process, it is adapted to the agricultural wastes processing that moisture gradient is big.This is for improving agricultural
Industrialization circulation economies of scale has especially important meaning.
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 stalk with break process
Integrated Processing Unit.
For overcome the deficiencies in the prior art, the present invention takes following technical scheme：
A kind of stalk Integrated Processing Unit with break process, including sinusoidal roller, biogas fermentation groove, biogas storage tank, adverse current are dry
Dry tower, biogas combustion machine and methane boiler, it is characterised in that：Agitating paddle is provided with inside biogas fermentation groove, agitating paddle passes through stirring
Axle and the stirring motor reductor at top are connected, and biogas fermentation groove top portion connects feed water valve by pipeline, and top connection L-shaped is held one's breath
Feeding packing auger, L-shaped hold one's breath feeding packing auger top connection feed well, feed well top is provided with pulverizer, biogas fermentation groove lower left quarter
Provided with sinusoidal ultrasound wave vibrator, biogas fermentation trench bottom is tapered, and pump inlet, biogas are connected by pipeline, transfusion control valve
Fermentation tank upper right quarter connects biogas fermentation trench bottom pipeline, roots blower outlet by biogas pipe, roots blower, air-blowing control valve
Connected by pipeline, gas storage control valve, appendix and biogas storage tank top, biogas tank top connection pressure gauge, bottom passes through
Pipeline connects blowoff valve, and biogas storage tank top connects methane boiler by appendix, burning supply control valve, biogas combustion machine,
Methane boiler top connects boiler exhaust gas pipe, passes through steam pipe, steam control valve connection steam fin hot blast at the top of methane boiler
Machine, steam fin air-heater are connected by pipeline with counter-current drying tower bottom, be provided with inside counter-current drying tower stacking sieve-like cone bucket,
Disk is bored, cone disk diameter is slightly larger than cone bucket, and cone tray bottom has automatically controlled bin gate, and wind charger is closed in counter-current drying tower top provided with spiral
And offgas duct, spiral close wind charger import top and be provided with sinusoidal roller, sinusoidal roller surface is continuous sine surface, air blower
Air outlet is connected through steam fin air-heater with counter-current drying tower bottom, and wind discharging machine is closed in the connection of counter-current drying tower bottom, adverse 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 cosine lacquer disk(-sc), cylinder, flexible
Bar, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan composition, the thick edge in cosine lacquer disk(-sc) section centre is slightly thin, general shape
For cosine curve, cosine lacquer disk(-sc) lower section is provided with pot shape spherical faced pan, and cosine lacquer disk(-sc) connects extra-organismal cylinder, cylinder energy through expansion link
Expansion link is driven to drive cosine lacquer disk(-sc) to move up and down, expansion link front hollow simultaneously connects compressed air hose and also connected in cosine lacquer disk(-sc)
Cavity；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.
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 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.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：
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；
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 sinusoidal 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, sinusoidal 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 stalk Integrated Processing Unit with break process as shown in Fig. 1~Fig. 8, 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：Set inside biogas fermentation groove 1
There is agitating paddle 13, agitating paddle 13 is connected by the stirring motor reductor 11 at agitating shaft and top, and the top of biogas fermentation groove 1 passes through
Pipeline connects feed water valve 10, 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 connection feed well 12,
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, the bottom of biogas fermentation groove 1
Portion 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, Luo Cifeng
Machine 15, air-blowing control valve 17 connect the bottom pipe of biogas fermentation groove 1, the outlet of roots blower 15 by pipeline, gas storage control valve 18,
Appendix 23 is connected with the top of biogas storage tank 2, and the top of biogas storage tank 2 connection pressure gauge 20, bottom connects blowoff valve by pipeline
21, the top of biogas storage tank 2 connects methane boiler 4, biogas pot by appendix 23, burning supply control valve 5, biogas combustion machine 6
The top of stove 4 connection boiler exhaust gas pipe 9, the top of methane boiler 4 connects steam fin air-heater by steam pipe 8, steam control valve 7
33, steam fin air-heater 33 is connected by pipeline with the bottom of counter-current drying tower 3, and the inside of counter-current drying tower 3 is provided with 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, the top of counter-current drying tower 3 are arranged at cone disk 43 bottom
Wind charger 31 and offgas duct 32 are closed provided with spiral, spiral closes the import top of wind charger 31 and is provided with sinusoidal roller A, sinusoidal roller
A surfaces are continuous sine surface, and the air outlet of air blower 34 is connected through steam fin air-heater 33 with the bottom of counter-current drying tower 3, inverse
Wind discharging machine 35 is closed in the connection of stream drying tower 3 bottom, 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 hose 36, baffle ring 41 and pot shape
Spherical faced pan 40 forms, and thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is cosine curve, is provided with below cosine lacquer disk(-sc)
Pot shape spherical faced pan 40, cosine lacquer disk(-sc) connect extra-organismal cylinder 37 through expansion link 39, and it is remaining that cylinder 37 can drive expansion link 39 to drive
String lacquer disk(-sc) moves up and down, and the front hollow of expansion link 39 simultaneously connects compressed air hose 36 and also connects cosine lacquer disk(-sc) inner chamber body；Sine is super
Sound wave vibrator C is driven by actuating unit, and the speed governing rotation of energy high speed, 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.
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 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.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 stalk Integrated Processing Unit with break process, including sinusoidal roller, biogas fermentation groove, biogas storage tank, adverse current
Drying tower, biogas combustion machine and methane boiler, it is characterised in that：Agitating paddle is provided with inside biogas fermentation groove, agitating paddle is by stirring
The stirring motor reductor for mixing axle and top is connected, and biogas fermentation groove top portion connects feed water valve by pipeline, and top connection L-shaped is closed
Gas feeding packing auger, L-shaped hold one's breath feeding packing auger top connection feed well, feed well top is provided with pulverizer, biogas fermentation groove lower-left
Portion is provided with sinusoidal ultrasound wave vibrator, and biogas fermentation trench bottom is tapered, and pump inlet, natural pond are connected by pipeline, transfusion control valve
Gas fermentation tank upper right quarter connects biogas fermentation trench bottom pipeline by biogas pipe, roots blower, air-blowing control valve, and roots blower goes out
Mouth is connected by pipeline, gas storage control valve, appendix and biogas storage tank top, and biogas tank top connection pressure gauge, bottom leads to
Piping connects blowoff valve, and biogas storage tank top connects biogas pot by appendix, burning supply control valve, biogas combustion machine
Stove, methane boiler top connection boiler exhaust gas pipe, methane boiler top passes through steam pipe, steam control valve connects steam fin heat
Blower fan, steam fin air-heater are connected by pipeline with counter-current drying tower bottom, and stacking sieve-like cone is provided with inside counter-current drying tower
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 wind provided with spiral and entered
Material machine and offgas duct, spiral close wind charger import top and are provided with sinusoidal roller, and sinusoidal roller surface is continuous sine surface, drum
Fan outlet is connected through steam fin air-heater with counter-current drying tower bottom, and wind discharging machine is closed in the connection of counter-current drying tower bottom,
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 by cosine lacquer disk(-sc), cylinder,
Expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan composition, the thick edge in cosine lacquer disk(-sc) section centre is slightly thin, substantially
Cosine curve is shaped as, pot shape spherical faced pan is provided with below cosine lacquer disk(-sc), cosine lacquer disk(-sc) connects extra-organismal cylinder, gas through expansion link
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 hose and also connects cosine glue
Disk inner chamber body；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.
2. the stalk Integrated Processing Unit with break process according to claim 1, it is characterised in that：The cosine lacquer disk(-sc) arteries and veins
Burst and shield is provided with above device of air, cosine lacquer disk(-sc) pulse gas explosion device is stretched out extra-organismal part and covered by shield, makes adverse current
Drying tower associative perception is preferable, and the convenient maintenance of gas explosion device can be carried out by removing shield.
3. the stalk Integrated Processing Unit with break process according to claim 1, it is characterised in that：The pot shape spherical faced pan
Top is provided with baffle ring.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710924851.9A CN107816879A (en) | 2017-10-02 | 2017-10-02 | Stalk Integrated Processing Unit with break process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710924851.9A CN107816879A (en) | 2017-10-02 | 2017-10-02 | Stalk Integrated Processing Unit with break process |
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| Publication Number | Publication Date |
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| CN107816879A true CN107816879A (en) | 2018-03-20 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201710924851.9A Withdrawn CN107816879A (en) | 2017-10-02 | 2017-10-02 | Stalk Integrated Processing Unit with break process |
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| CN (1) | CN107816879A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN109059274A (en) * | 2018-07-25 | 2018-12-21 | 安徽辰宇机械科技有限公司 | A kind of hot-blast stove of fermenting organism mass-energy heated type |
| CN113899192A (en) * | 2021-10-28 | 2022-01-07 | 江苏正昌粮机股份有限公司 | Gas heating system of belt dryer |
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| 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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| Publication number | Priority date | Publication date | Assignee | Title |
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| 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 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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