CN107881097A - Magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed - Google Patents
Magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed Download PDFInfo
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- CN107881097A CN107881097A CN201710924970.4A CN201710924970A CN107881097A CN 107881097 A CN107881097 A CN 107881097A CN 201710924970 A CN201710924970 A CN 201710924970A CN 107881097 A CN107881097 A CN 107881097A
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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
- 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
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- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/36—Means for collection or storage of gas; Gas holders
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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
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
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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
- 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
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- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
- C12M41/18—Heat exchange systems, e.g. heat jackets or outer envelopes
- C12M41/24—Heat exchange systems, e.g. heat jackets or outer envelopes inside the vessel
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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- 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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- 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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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
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- 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
- 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
- F26B17/1441—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 stationary, e.g. fixed panels, baffles, grids, the position of which may be adjustable
- F26B17/1458—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 stationary, e.g. fixed panels, baffles, grids, the position of which may be adjustable consisting of perforated panels or baffles; consisting of grids
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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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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
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Abstract
The invention discloses a kind of magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed,Including tendons roller,Biogas fermentation groove,Biogas storage tank,Counter-current drying tower,Biogas combustion machine,Methane boiler,Heat pump main frame and computer,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 connects 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,Tendons roller and segment cutter,Offgas duct connects heat pump,Counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device,Processing unit is controlled by computer,The tendons roller of the present invention,Cosine lacquer disk(-sc) pulse gas explosion device and sinusoidal ultrasound wave vibrator energy reliable collaborative realize 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 magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed.
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
Magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed, it is adapted to the big agricultural wastes of moisture gradient
Processing.This has especially important meaning for 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 magnetic tape trailer recuperation of heat and system are given birth to
The tendons pulley type straw treating device of biomass fuel.
For overcome the deficiencies in the prior art, the present invention takes following technical scheme：
A kind of magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed, including tendons roller, biogas hair
Ferment groove, biogas storage tank, counter-current drying tower, biogas combustion machine, methane boiler, heat pump main frame and computer control system, its feature
It is：Mouse cage tubular heat exchanger is provided with the middle part of biogas fermentation groove, is provided with agitating paddle 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 tendons roller, tendons roller surface is provided with the tendons of axially even cloth,
Tendons roller top is provided with segment cutter, and offgas duct is sequentially connected tail gas air exhauster, cyclone separator and evaporator by pipeline, steams
Hair device upper end is provided with air outlet, and evaporator top is sequentially connected heat pump main frame and condenser by refrigerant pipe, and condenser one end is set
Have a condenser air inlet, the other end connects blower inlet by pipeline, blower outlet through steam fin air-heater with
Counter-current drying tower bottom connects, counter-current drying tower bottom Amenorrhea wind discharging machine connection biological substance fuel forming machine, 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 cosine lacquer disk(-sc), cylinder, expansion link, axle
Set, 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, and general shape is remaining
Chord curve, cosine lacquer disk(-sc) lower section are provided with pot shape spherical faced pan, and cosine lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive
Expansion link drives cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compressed air hose and also connects cosine lacquer disk(-sc) inner chamber
Body；Sinusoidal ultrasound wave vibrator is driven by actuating unit, and the speed governing rotation of energy high speed, the structure of sinusoidal ultrasound wave vibrator is ball
Cap-shaped, and spherical cap edge is smooth continuous sine curve, has crest, trough progressively to expand continuous hair from spherical cap center to edge
Dissipate feature；Processing unit is controlled by computer control system.
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 are squeezed to segment, stranding using steam and carry out highly effective drying, the qualified stalk material profit of moisture
Shaping is processed with biological substance fuel forming machine, production biomass fuel carries out sale extra earning.
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, the mouse cage tubular heat exchanger in the middle part of groove can be directed respectively into cold and hot media implementation groove
Interior heating and cooling regulation and control are beneficial to fermentation, and 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 can rub fine groundization with the hands by segment cutter segment, then through the extruding of tendons roller is differential, this
Sample material, which is easy to subsequently to input counter-current drying tower, is dried operation.Tendons roller surface is provided with the tendons of axially even cloth, phase
The bearing arrangement sealing and dustproof answered, be also adapted to strength extruding to turn and extruding differential pair turn, can convenient adjusting roller spacing it is special
Favourable strong extruding turns to rub with the hands to grind to crush with roller differential pair promotes segment stalk to refine once again, is easy to follow-up highly effective drying.Tendons roller
Cylinder bites that continuous reliable, extruding compression ratio is especially big to material, tendons roller is differential rub with the hands grind reliable, durable, skimming over property is good, secondary
Crushing 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 imports biological substance fuel forming machine by closing the output of wind discharging machine
Carry out processing and forming.Air blower blasts air and is heated to be high temperature air through steam fin air-heater passes through drying tower from bottom to top.
Counter-current drying tower lower left quarter has cosine lacquer disk(-sc) pulse gas explosion device, and energy explosion type release compressed air produces the pulsation of gas explosion material,
Cooperate with tower type counterflow to dry and obtain unthinkable drying effect.The tail heat utilization heat pump of counter-current drying tower discharge is carried out
Recovery circulation, the evaporator of heat pump are arranged in the upper right side of counter-current drying tower, the tail that tail gas air exhauster discharges offgas duct
Gas is sent into cyclone separator through pipeline, and the damp-heat stream through cyclone separator purification is reclaimed through evaporator with heat pump, heat energy,
Heat pump main frame connects evaporator by refrigerant pipe and the condenser of bottom, air blower certain driving air-flow pass through condenser, be able to simultaneously
Preheated, can be so substantially improved into steam in the transferred tail heat in condenser release of evaporator recovery by heat pump main frame
The temperature of fin air-heater air, effectively reduce the consumption of steam fin air-heater heating steam.
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.
Processing unit can collectively form the intelligence system of coordination with computer control system simultaneously, can intelligent, program
Change and control each device collaborative work, continuous monitoring creation data, realize automation Continuous maching, improve product quality, save people
Work.
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；
Dry tower counter-flow highly effective drying can an air blast, also can steam heating dry, convenient can also realize that the recovery of tail heat driven heat pump follows
Ring utilizes, and energy consumption for drying can drop to especially low.
Above four main 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；D, computer control system；E heat
Pump main frame；1st, biogas fermentation groove；2nd, biogas storage tank；3rd, counter-current drying tower；4th, methane boiler；5th, burning supply control valve；6th, natural pond
Gas combustor；7th, steam control valve；8th, steam pipe；9th, boiler exhaust gas pipe；10th, feed water valve；11st, stirring motor reductor；12nd, enter
Hopper；13rd, agitating paddle；14th, biogas pipe；15th, roots blower；16th, transfusion control valve；17th, air-blowing control valve；18th, gas storage controls
Valve；19th, L-shaped is held one's breath feeding packing auger；20th, pressure gauge；21st, blowoff valve；22nd, horizon；23rd, appendix；24th, pulverizer；25th, mouse
Cage tubular heat exchanger；29th, segment cutter；30th, shield；31st, spiral closes wind charger；32nd, offgas duct；33rd, steam fin air-heater；
34th, air blower；35th, wind discharging machine is closed；36th, compressed air hose；37th, cylinder；38th, axle sleeve；39th, expansion link；40th, spherical faced pan；41、
Baffle ring；42nd, cone bucket；43rd, disk is bored；44th, automatically controlled bin gate；45th, biological substance fuel forming machine；70th, cyclone separator；71st, tail gas is taken out
Blower fan；72nd, evaporator；73rd, air outlet；74th, refrigerant pipe；75th, condenser；76th, condenser air inlet.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
The tendons pulley type straw treating device of a kind of magnetic tape trailer recuperation of heat and biomass fuel processed as shown in Fig. 1~Fig. 8, bag
Include tendons roller A, biogas fermentation groove 1, biogas storage tank 2, counter-current drying tower 3, biogas combustion machine 6, methane boiler 4, heat pump main frame E
With computer control system D, it is characterised in that：The middle part of biogas fermentation groove 1 is provided with mouse cage tubular heat exchanger 25, biogas fermentation groove 1
Inside is provided with agitating paddle 13, and agitating paddle 13 is connected by the stirring motor reductor 11 at agitating shaft and top, and biogas fermentation groove 1 pushes up
Portion connects feed water valve 10 by pipeline, and top connection L-shaped is held one's breath feeding packing auger 19, L-shaped hold one's breath the top of feeding packing auger 19 connect into
Hopper 12, the top of feed well 12 are provided with pulverizer 24, and the lower left quarter of biogas fermentation groove 1 is provided with sinusoidal ultrasound wave vibrator C, biogas hair
The bottom of ferment groove 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
14th, 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, gas storage
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 is connected by pipeline
Blowoff valve 21 is connect, the top of biogas storage tank 2 connects methane boiler by appendix 23, burning supply control valve 5, biogas combustion machine 6
4, the top of methane boiler 4 connection boiler exhaust gas pipe 9, the top of methane boiler 4 connects steam wing by steam pipe 8, steam control valve 7
Piece air-heater 33, steam fin air-heater 33 are connected by pipeline with the bottom of counter-current drying tower 3, and the inside of counter-current drying tower 3 is provided with
Sieve-like cone bucket 42, cone disk 43 are laminated, 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, countercurrently dry
Wind charger 31 and offgas duct 32 are closed in the dry top of tower 3 provided with spiral, and spiral closes the import top of wind charger 31 and is provided with tendons roller
A, tendons roller A surface are provided with the tendons of axially even cloth, and tendons roller A tops are provided with segment cutter 29, and offgas duct 32 passes through pipe
Road is sequentially connected tail gas air exhauster 71, cyclone separator 70 and evaporator 72, and the upper end of evaporator 72 is provided with air outlet 73, evaporator
72 tops are sequentially connected heat pump main frame E and condenser 75 by refrigerant pipe 74, and the one end of condenser 75 is provided with condenser air inlet 76,
The other end connects the air inlet of air blower 34 by pipeline, and the air outlet of air blower 34 is through steam fin air-heater 33 and counter-current drying tower
3 bottoms connect, the bottom Amenorrhea wind discharging machine 35 of counter-current drying tower 3 connection biological substance fuel forming machine 45, the lower-left of counter-current drying tower 3
Portion is provided with cosine lacquer disk(-sc) pulse gas explosion device B；Cosine lacquer disk(-sc) pulse gas explosion device B 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 form, and thick edge is slightly thin among cosine lacquer disk(-sc) section, greatly
Shape is cosine curve, is provided with pot shape spherical faced pan 40 below cosine lacquer disk(-sc), cosine lacquer disk(-sc) connects extra-organismal through expansion link 39
Cylinder 37, cylinder 37 can drive expansion link 39 to drive cosine lacquer disk(-sc) to move up and down, and the front hollow of expansion link 39 simultaneously connects compression sky
Tracheae 36 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 is spherical cap shape, and spherical cap edge is smooth continuous sine curve, from spherical cap center to side
Edge has crest, trough progressively to expand continuous diverging feature；Processing unit is controlled by computer control system D.
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 are squeezed to segment, stranding using steam and carry out highly effective drying, the qualified stalk material profit of moisture
Shaping is processed with biological substance fuel forming machine, production biomass fuel carries out sale extra earning.
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 the mouse cage tubular heat exchanger 25 in the middle part of groove can be directed respectively into cold
Thermal medium realizes that heating and cooling regulation and control are beneficial to fermentation in groove, 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 can rub fine groundization with the hands by the segment of segment cutter 29, then through tendons roller A extruding is differential,
So material, which is easy to subsequently to input counter-current drying tower 3, is dried operation.Tendons roller A surfaces are provided with the prominent of the even cloth in axial direction
Muscle, corresponding bearing arrangement sealing and dustproof, it is also adapted to strength extruding and turns to turning and extruding differential pair, can convenient adjusting roller spacing
Particularly advantageous strong extruding turns to rub with the hands to grind to crush with roller differential pair promotes segment stalk to refine once again, is easy to follow-up highly effective drying.It is prominent
Muscle roller A bites that continuous reliable, extruding compression ratio is especially big to material, and differential rub with the hands of tendons roller A grinds reliable, durable, skimming over property
Good, separating twice effect is especially good while energy consumption is also 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 exported by closing wind discharging machine 35
Import biological substance fuel forming machine 45 and carry out processing and forming.Air blower 34 blasts air and is heated to be height through steam fin air-heater 33
Warm air passes through drying tower from bottom to top.The lower left quarter of counter-current drying tower 3 has cosine lacquer disk(-sc) pulse gas explosion device B, and energy explosion type is released
Put compressed air and produce the pulsation of gas explosion material, collaboration tower type counterflow, which is dried, obtains unthinkable drying effect.To counter-current drying
The tail heat utilization heat pump that tower 3 is discharged carries out recovery circulation, and the evaporator 72 of heat pump is arranged in the right side of counter-current drying tower 3
Top, the tail gas that offgas duct 32 is discharged is sent into cyclone separator 70 by tail gas air exhauster 71 through pipeline, net through cyclone separator 70
The damp-heat stream of change is reclaimed through evaporator with heat pump 72, heat energy, heat pump main frame E by refrigerant pipe 74 connect evaporator 72 and
The condenser 75 of bottom, the certain driving air-flow of air blower 34 pass through condenser 75, while are able to be reclaimed in evaporator 72 by heat pump main frame E
The transferred tail heat discharged in condenser 75 is preheated, and the temperature into the air of steam fin air-heater 33 can so be substantially improved
Degree, effectively reduce the consumption that steam fin air-heater 33 heats steam.
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.
Processing unit can collectively form the intelligence system of coordination with computer control system D simultaneously, can intelligent, program
Change and control each device collaborative work, continuous monitoring creation data, realize automation Continuous maching, improve product quality, save people
Work.
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 magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed, including tendons roller, biogas
Fermentation tank, biogas storage tank, counter-current drying tower, biogas combustion machine, methane boiler, heat pump main frame and computer control system, it is special
Sign is：Mouse cage tubular heat exchanger is provided with the middle part of biogas fermentation groove, is provided with agitating paddle 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 tendons roller, and tendons roller surface is provided with the even cloth in axial direction
Tendons, tendons roller top are provided with segment cutter, and offgas duct is sequentially connected tail gas air exhauster, cyclone separator and evaporation by pipeline
Device, evaporator upper end are provided with air outlet, and evaporator top is sequentially connected heat pump main frame and condenser, condenser one by refrigerant pipe
End is provided with condenser air inlet, and the other end connects blower inlet by pipeline, and blower outlet is through steam fin hot blast
Machine is connected with counter-current drying tower bottom, counter-current drying tower bottom Amenorrhea wind discharging machine connection biological substance fuel forming machine, and adverse current is dry
Dry 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；Processing unit is controlled by computer control system.
2. the tendons pulley type straw treating device of magnetic tape trailer recuperation of heat and biomass fuel processed according to claim 1, it is special
Sign is：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.
3. the tendons pulley type straw treating device of magnetic tape trailer recuperation of heat and biomass fuel processed according to claim 1, it is special
Sign is：Baffle ring is provided with above the pot shape spherical faced pan.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710924970.4A CN107881097A (en) | 2017-10-02 | 2017-10-02 | Magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201710924970.4A CN107881097A (en) | 2017-10-02 | 2017-10-02 | Magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed |
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| CN107881097A true CN107881097A (en) | 2018-04-06 |
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| CN201710924970.4A Withdrawn CN107881097A (en) | 2017-10-02 | 2017-10-02 | Magnetic tape trailer recuperation of heat and the tendons pulley type straw treating device of biomass fuel processed |
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| CN108977246A (en) * | 2018-08-03 | 2018-12-11 | 蚌埠市昊源压缩机制造有限公司 | The method that a kind of pair of natural gas is compressed |
| CN111306925A (en) * | 2020-03-27 | 2020-06-19 | 周全红 | Petrochemical environmental protection drying equipment |
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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 |
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| CN111306925B (en) * | 2020-03-27 | 2021-11-02 | 东营联合石化有限责任公司 | Petrochemical environmental protection drying equipment |
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