CN107815403A - Magnetic tape trailer recuperation of heat and the stalk Integrated Processing Unit for cutting section processing - Google Patents

Magnetic tape trailer recuperation of heat and the stalk Integrated Processing Unit for cutting section processing Download PDF

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Publication number
CN107815403A
CN107815403A CN201710925012.9A CN201710925012A CN107815403A CN 107815403 A CN107815403 A CN 107815403A CN 201710925012 A CN201710925012 A CN 201710925012A CN 107815403 A CN107815403 A CN 107815403A
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China
Prior art keywords
biogas
counter
drying tower
lacquer disk
current drying
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CN201710925012.9A
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Chinese (zh)
Inventor
杨胜辉
张思言
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Individual
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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
    • C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/24—Recirculation of gas
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
    • C12M33/16—Screw conveyor
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12—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
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/40—Means for regulation, monitoring, measurement or control, e.g. flow regulation of pressure
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M43/00—Combinations of bioreactors or fermenters with other apparatus
    • C12M43/04—Bioreactors or fermenters combined with combustion devices or plants, e.g. for carbon dioxide removal
    • 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
    • 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
    • F26B17/001—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement the material moving down superimposed floors
    • F26B17/006—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement the material moving down superimposed floors the movement being imparted by oscillation or vibration
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
    • F26B21/002—Drying-air generating units, e.g. movable, independent of drying enclosure heating the drying air indirectly, i.e. using a heat exchanger
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/001—Handling, e.g. loading or unloading arrangements
    • F26B25/002—Handling, e.g. loading or unloading arrangements for bulk goods
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/04—Agitating, stirring, or scraping devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
    • F26B2200/02—Biomass, e.g. waste vegetative matter, straw
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • 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
    • Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

The invention discloses a kind of magnetic tape trailer recuperation of heat and cut section processing stalk Integrated Processing Unit,Including sinusoidal 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 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,Sinusoidal 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 sinusoidal 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

Magnetic tape trailer recuperation of heat and the stalk Integrated Processing Unit for cutting section processing
Technical field
The present invention relates to a kind of magnetic tape trailer recuperation of heat and cut section processing stalk Integrated Processing Unit.
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 stalk Integrated Processing Unit for cutting section processing, it is adapted to the agricultural wastes processing that moisture gradient is big.This is right There is especially important meaning in improving agriculture industrialization circulation economies of scale.
The content of the invention
The technical problem to be solved in the present invention is exactly overcome the deficiencies in the prior art, there is provided a kind of magnetic tape trailer recuperation of heat and cuts section The stalk Integrated Processing Unit of processing.
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 stalk Integrated Processing Unit for cutting section processing, including the storage of sinusoidal roller, biogas fermentation groove, biogas Tank, counter-current drying tower, biogas combustion machine, methane boiler, heat pump main frame and computer control system, it is characterised in that：Biogas is sent out Be provided with mouse cage tubular heat exchanger in the middle part of ferment groove, biogas fermentation groove inside is provided with agitating paddle, and agitating paddle passes through agitating shaft and top Stirring motor reductor is 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 Shape is held one's breath feeding packing auger top connection feed well, and feed well top is provided with pulverizer, and biogas fermentation groove lower left quarter is provided with sinusoidal surpass Sound wave vibrator, biogas fermentation trench bottom is tapered, and pump inlet, biogas fermentation groove upper right are connected by pipeline, transfusion control valve Portion by biogas pipe, roots blower, air-blowing control valve connect biogas fermentation trench bottom pipeline, roots blower outlet by pipeline, Gas storage control valve, appendix and biogas storage tank top are connected, and biogas tank top connection pressure gauge, bottom is connected by pipeline and arranged Dirty valve, biogas storage tank top supplies control valve by appendix, burning, biogas combustion machine connects methane boiler, on methane boiler Portion connects boiler exhaust gas pipe, passes through steam pipe, steam control valve connection steam fin air-heater, steam fin at the top of methane boiler Air-heater is connected by pipeline with counter-current drying tower bottom, and stacking sieve-like cone bucket, cone disk are provided with inside counter-current drying tower, and cone disk is straight Footpath is slightly larger than cone bucket, and cone tray bottom has automatically controlled bin gate, and wind charger and offgas duct, spiral shell are closed in counter-current drying tower top provided with spiral Traling wind charger import top is provided with sinusoidal roller, and sinusoidal roller surface is continuous sine surface, and sinusoidal roller top is provided with Segment cutter, offgas duct are sequentially connected tail gas air exhauster, cyclone separator and evaporator by pipeline, and evaporator upper end is provided with air-out Mouthful, evaporator top is sequentially connected heat pump main frame and condenser by refrigerant pipe, and condenser one end is provided with condenser air inlet, separately One end connects blower inlet by pipeline, and blower outlet connects through steam fin air-heater and counter-current drying tower bottom Connect, wind discharging machine is closed in the connection of counter-current drying tower bottom, and counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device；Cosine Lacquer disk(-sc) pulse gas explosion device is made up of cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan, Thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is cosine curve, and pot shape spherical faced pan is provided with below cosine lacquer disk(-sc), remaining String lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, before expansion link Portion is hollow and connects compressed air hose and also connects cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator is driven by actuating unit, The speed governing rotation of energy high speed, the structure of sinusoidal ultrasound wave vibrator is spherical cap shape, and spherical cap edge is smooth continuous sine curve, There are crest, trough progressively to expand continuous diverging feature from spherical cap center to edge；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.
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 sinusoidal roller is differential, this Sample material, which is easy to subsequently to input counter-current drying tower, is dried operation.Sinusoidal roller surface is continuous sine surface, corresponding axle It is dust-proof to hold system sealing, is also adapted to strength extruding to turning and extruding differential pair turns, can convenient adjusting roller spacing it is 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.Sinusoidal roller is to thing Material bites that continuous reliable, extruding compression ratio is especially big, sinusoidal roller curved surface is differential rub with the hands grind reliable, durable, skimming over property is good, two wheat-middlings Broken 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.Recovery circulation carried out to the tail heat utilization heat pump of counter-current drying tower discharge, the evaporator of heat pump is arranged in inverse The upper right side of drying tower is flowed, the tail gas that offgas duct is discharged is sent into cyclone separator by tail gas air exhauster through pipeline, through cyclonic separation The damp-heat stream of device purification is reclaimed through evaporator with heat pump, heat energy, heat pump main frame by refrigerant pipe connect evaporator and under The condenser in portion, air blower certain driving air-flow pass through condenser, while are able to transferred cold in evaporator recovery by heat pump main frame The tail heat of condenser release is preheated, and the temperature into steam fin air-heater air can so be substantially improved, and is effectively reduced and is steamed Vapour fin air-heater heats the consumption of 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：
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；
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 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；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；70th, cyclone separator；71st, tail gas air exhauster；72nd, evaporator；73rd, go out Air port；74th, refrigerant pipe；75th, condenser；76th, condenser air inlet.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
A kind of magnetic tape trailer recuperation of heat and the stalk Integrated Processing Unit of section processing is cut 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, methane boiler 4, heat pump main frame E and computer control System D processed, it is characterised in that：The middle part of biogas fermentation groove 1 is provided with mouse cage tubular heat exchanger 25, and the inside of biogas fermentation groove 1, which is provided with, to be stirred Oar 13 is mixed, 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 Feed water valve 10 is connected, 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, charging The top of groove 12 is provided with pulverizer 24, and the lower left quarter of biogas fermentation groove 1 is provided with sinusoidal ultrasound wave vibrator C, and the bottom of biogas fermentation groove 1 is in Taper, pump inlet is connected by pipeline, transfusion control valve 16, the upper right quarter of biogas fermentation groove 1 passes through biogas pipe 14, roots blower 15th, air-blowing control valve 17 connects the bottom pipe of biogas fermentation groove 1, and the outlet of roots blower 15 passes through pipeline, gas storage control valve 18, defeated Tracheae 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 21 by pipeline, The top of biogas storage tank 2 connects methane boiler 4, methane boiler 4 by appendix 23, burning supply control valve 5, biogas combustion machine 6 Top connection boiler exhaust gas pipe 9, the top of methane boiler 4 connects steam fin air-heater 33 by steam pipe 8, steam control valve 7, 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 42nd, disk 43 is bored, 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, and the top of counter-current drying tower 3 is provided with Spiral closes wind charger 31 and offgas duct 32, and spiral closes the import top of wind charger 31 and is provided with sinusoidal roller A, sinusoidal roller A tables Face is continuous sine surface, and sinusoidal roller A tops are provided with segment cutter 29, and offgas duct 32 is sequentially connected tail gas air exhauster by pipeline 71st, cyclone separator 70 and evaporator 72, the upper end of evaporator 72 are provided with air outlet 73, the top of evaporator 72 by refrigerant pipe 74 according to Secondary connection heat pump main frame E and condenser 75, the one end of condenser 75 are provided with condenser air inlet 76, and the other end is connected by pipeline and roused The air inlet of blower fan 34, the air outlet of air blower 34 are connected through steam fin air-heater 33 with the bottom of counter-current drying tower 3, counter-current drying tower Wind discharging machine 35 is closed in the connection of 3 bottoms, 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 Composition, the thick edge in cosine lacquer disk(-sc) section centre is slightly thin, and general shape is cosine curve, and pot shape sphere is provided with below cosine lacquer disk(-sc) Disk 40, cosine lacquer disk(-sc) connect extra-organismal cylinder 37 through expansion link 39, and cylinder 37 can drive expansion link 39 to drive on cosine lacquer disk(-sc) Lower motion, the front hollow of expansion link 39 simultaneously connect compressed air hose 36 and also connect cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave exciting Device C is driven by actuating unit, can high speed speed governing rotation, sinusoidal ultrasound wave vibrator C structure is spherical cap shape, and spherical cap edge For the continuous sine curve of smoothness, there are crest, trough progressively to expand continuous diverging feature from spherical cap center to edge；Processing unit 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.
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 sinusoidal roller A extruding is differential, So material, which is easy to subsequently to input counter-current drying tower 3, is dried operation.Sinusoidal roller A surfaces are continuous sine surface, accordingly Bearing arrangement sealing and dustproof, be also adapted to strength extruding to turn and extruding differential pair turn, can convenient adjusting roller spacing especially have Sharp 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.Sinusoidal roller A Bite that continuous reliable, extruding compression ratio is especially big to material, sinusoidal roller A curved surfaces are differential rub with the hands grind reliable, durable, skimming over property is 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 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.The tail heat utilization heat pump discharged to counter-current drying tower 3 returns Circulation is received, the evaporator 72 of heat pump is arranged in the upper right side of counter-current drying tower 3, and tail gas air exhauster 71 discharges offgas duct 32 Tail gas through pipeline be sent into cyclone separator 70, through cyclone separator 70 purify damp-heat stream through evaporator with heat pump 72, heat It can be reclaimed, heat pump main frame E connects evaporator 72 and the condenser 75 of bottom, the certain driving air-flow of air blower 34 by refrigerant pipe 74 Through condenser 75, while it is able to reclaim the transferred tail heat progress discharged in condenser 75 in evaporator 72 by heat pump main frame E Preheating, can so be substantially improved the temperature into the air of steam fin air-heater 33, effectively reduce steam fin air-heater 33 and add The consumption of vapours.
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 stalk Integrated Processing Unit for cutting section processing, including sinusoidal roller, biogas fermentation groove, biogas Storage tank, counter-current drying tower, biogas combustion machine, methane boiler, heat pump main frame and computer control system, it is characterised in that：Biogas Mouse cage tubular heat exchanger is provided with the middle part of fermentation tank, is provided with agitating paddle inside biogas fermentation groove, agitating paddle passes through agitating shaft and top Stirring motor reductor connection, biogas fermentation groove top portion by pipeline connect feed water valve, top connection L-shaped hold one's breath charging twist Dragon, L-shaped are held one's breath feeding packing auger top connection feed well, and feed well top is provided with pulverizer, and biogas fermentation groove lower left quarter is provided with just String ultrasonic wave excitation device, biogas fermentation trench bottom is tapered, and pump inlet, biogas fermentation groove are connected by pipeline, transfusion control valve Upper right quarter connects biogas fermentation trench bottom pipeline by biogas pipe, roots blower, air-blowing control valve, and roots blower outlet passes through pipe Road, gas storage control valve, appendix and biogas storage tank top are connected, and biogas tank top connection pressure gauge, bottom is connected by pipeline Blowoff valve is connect, biogas storage tank top connects methane boiler, biogas pot by appendix, burning supply control valve, biogas combustion machine Stove top connects boiler exhaust gas pipe, passes through steam pipe, steam control valve connection steam fin air-heater, steam at the top of methane boiler Fin air-heater is connected by pipeline with counter-current drying tower bottom, and stacking sieve-like cone bucket, cone disk, cone are provided with inside counter-current drying tower Disk diameter is slightly larger than cone bucket, and cone tray bottom has automatically controlled bin gate, and wind charger and tail gas are closed in counter-current drying tower top provided with spiral Pipe, spiral close wind charger import top and are provided with sinusoidal roller, and sinusoidal roller surface is continuous sine surface, sinusoidal roller top Provided with segment cutter, offgas duct is sequentially connected tail gas air exhauster, cyclone separator and evaporator by pipeline, and evaporator upper end is provided with Air outlet, evaporator top are sequentially connected heat pump main frame and condenser by refrigerant pipe, and condenser one end is provided with condenser air intake Mouthful, the other end connects blower inlet by pipeline, and blower outlet is through under steam fin air-heater and counter-current drying tower Portion connects, and wind discharging machine is closed in the connection of counter-current drying tower bottom, and counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device； Cosine lacquer disk(-sc) pulse gas explosion device is by cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan group Into thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is cosine curve, and pot shape sphere is provided with below cosine lacquer disk(-sc) Disk, cosine lacquer disk(-sc) connect extra-organismal cylinder through expansion link, and cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and stretch Bar 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 Dynamic, the speed governing rotation of energy high speed, the structure of sinusoidal ultrasound wave vibrator is spherical cap shape, and spherical cap edge is smooth continuous sinusoidal song Line, there are crest, trough progressively to expand continuous diverging feature from spherical cap center to edge；Processing unit is by computer control system control System.
2. according to claim 1 magnetic tape trailer recuperation of heat and cut section processing stalk Integrated Processing Unit, it is characterised in that：It is described Shield is provided with above cosine lacquer disk(-sc) pulse gas explosion device, cosine lacquer disk(-sc) pulse gas explosion device is stretched out extra-organismal component cover by shield Firmly, make counter-current drying tower associative perception preferable, the convenient maintenance of gas explosion device can be carried out by removing shield.
3. according to claim 1 magnetic tape trailer recuperation of heat and cut section processing stalk Integrated Processing Unit, it is characterised in that：It is described Baffle ring is provided with above pot shape spherical faced pan.
CN201710925012.9A 2017-10-02 2017-10-02 Magnetic tape trailer recuperation of heat and the stalk Integrated Processing Unit for cutting section processing Withdrawn CN107815403A (en)

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CN201710925012.9A CN107815403A (en) 2017-10-02 2017-10-02 Magnetic tape trailer recuperation of heat and the stalk Integrated Processing Unit for cutting section processing

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Application Number Priority Date Filing Date Title
CN201710925012.9A CN107815403A (en) 2017-10-02 2017-10-02 Magnetic tape trailer recuperation of heat and the stalk Integrated Processing Unit for cutting section processing

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CN107815403A true CN107815403A (en) 2018-03-20

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