CN107655307A - Magnetic tape trailer recuperation of heat and the pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger - Google Patents

Magnetic tape trailer recuperation of heat and the pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger Download PDF

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Publication number
CN107655307A
CN107655307A CN201710924861.2A CN201710924861A CN107655307A CN 107655307 A CN107655307 A CN 107655307A CN 201710924861 A CN201710924861 A CN 201710924861A CN 107655307 A CN107655307 A CN 107655307A
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China
Prior art keywords
biogas
counter
drying tower
lacquer disk
gas explosion
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CN201710924861.2A
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Chinese (zh)
Inventor
向明翠
张思言
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Individual
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Priority to CN201710924861.2A priority Critical patent/CN107655307A/en
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/12—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft
    • F26B17/14—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas
    • F26B17/1433—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material
    • F26B17/1466—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material the members or bodies being in movement
    • F26B17/1475—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed solely by gravity, i.e. the material moving through a substantially vertical drying enclosure, e.g. shaft the materials moving through a counter-current of gas the drying enclosure, e.g. shaft, having internal members or bodies for guiding, mixing or agitating the material, e.g. imposing a zig-zag movement onto the material the members or bodies being in movement the movement being a vibration or oscillation
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00—Bioreactors or fermenters specially adapted for specific uses
    • C12M21/04—Bioreactors or fermenters specially adapted for specific uses for producing gas, e.g. biogas
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M23/00—Constructional details, e.g. recesses, hinges
    • C12M23/36—Means for collection or storage of gas; Gas holders
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
    • C12M27/02—Stirrer or mobile mixing elements
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
    • C12M29/24—Recirculation of gas
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
    • C12M33/16—Screw conveyor
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/12—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
    • C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
    • C12M41/48—Automatic or computerized control
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
    • F26B21/002—Drying-air generating units, e.g. movable, independent of drying enclosure heating the drying air indirectly, i.e. using a heat exchanger
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26—DRYING
    • F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B23/00—Heating arrangements
    • F26B23/001—Heating arrangements using waste heat
    • F26B23/007—Heating arrangements using waste heat recovered from the dried product
    • F26B23/008—Heating arrangements using waste heat recovered from the dried product using a heat pump cycle
    • 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
    • F26B25/005—Treatment of dryer exhaust gases
    • F26B25/007—Dust filtering; Exhaust dust filters
    • 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
    • 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 the pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger,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 upper right quarter passes through pipeline,Roots blower link slot bottom,Roots blower outlet connection biogas storage tank,Biogas storage tank passes through pipeline,Biogas combustion machine connects methane boiler,Methane boiler connects counter-current drying tower by steam fin air-heater,Counter-current drying tower upper left quarter is sequentially connected spiral and closes wind charger and sinusoidal roller,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,Sinusoidal roller and cosine lacquer disk(-sc) pulse the gas explosion device of the present invention all has distinguishing feature,Energy reliable collaborative realizes comprehensive development and utilization to the king-sized agricultural crop straw of moisture gradient and discarded object.

Description

Magnetic tape trailer recuperation of heat and the pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger
Technical field
The present invention relates to a kind of magnetic tape trailer recuperation of heat and the pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger.
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 pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger, the agricultural wastes for being adapted to moisture gradient big add Work.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 heat exchange The pulse gas explosion formula stalk Integrated Processing Unit of device.
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 pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger, 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, its feature exist In：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 agitating shaft Be connected with the stirring motor reductor at top, biogas fermentation groove top portion by pipeline connect feed water valve, top connection L-shaped hold one's breath into Expect auger, L-shaped is held one's breath feeding packing auger top connection feed well, and feed well top is provided with pulverizer, and biogas fermentation trench bottom is in boring Shape, pump inlet is connected by pipeline, transfusion control valve, biogas fermentation groove upper right quarter is controlled by biogas pipe, roots blower, air-blowing Valve connects biogas fermentation trench bottom pipeline, and roots blower outlet passes through pipeline, gas storage control valve, appendix and biogas storage tank top Connection, biogas tank top connection pressure gauge, bottom connect blowoff valve by pipeline, and biogas storage tank top passes through appendix, combustion Supply control valve, biogas combustion machine connection methane boiler are burnt, methane boiler top connects boiler exhaust gas pipe, and methane boiler top is logical Steam pipe, steam control valve connection steam fin air-heater are crossed, steam fin air-heater passes through pipeline and counter-current drying tower bottom Connection, is provided with stacking sieve-like cone bucket, cone disk inside counter-current drying tower, and cone disk diameter be slightly larger than cone bucket, and cone tray bottom have it is automatically controlled Wind charger and offgas duct are closed in bin gate, counter-current drying tower top provided with spiral, and spiral closes wind charger import top and is provided with sine Roller, sinusoidal roller surface are continuous sine surface, offgas duct by pipeline be sequentially connected tail gas air exhauster, cyclone separator and Evaporator, evaporator upper end are provided with air outlet, and evaporator top is sequentially connected heat pump main frame and condenser by refrigerant pipe, condensation Device one end is provided with condenser air inlet, and the other end connects blower inlet by pipeline, and blower outlet is through steam fin Air-heater is connected with counter-current drying tower bottom, 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 Pipe, baffle ring and pot shape spherical faced pan composition, thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is cosine curve, cosine Pot shape spherical faced pan is provided with below lacquer disk(-sc), cosine lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive expansion link to drive Cosine lacquer disk(-sc) moves up and down, and expansion link front hollow simultaneously connects compressed air hose and also connects cosine lacquer disk(-sc) inner chamber body；Processing unit 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 progress highly effective drying is squeezed to rubbing with the hands using steam.
Biogas fermentation groove maintains 2/3rds liquid level, water, material can be held one's breath as needed for supplementing feed water valve by L-shaped Feeding packing auger prevents gas from leaking using water seal closed-type feed, while is advantageous to slight positive pressure state in retention groove.Groove top portion is stirred Mix agitating paddle in motor reducer driver slot to rotate, 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.
Favorably the ferment liquid phase material thoroughly degraded of bottom land taper be used as naturally by pipeline, transfusion control valve, pump output Fertilizer application, biogas fermentation groove upper right quarter have biogas pipe output biogas is pressurized through roots blower, air-blowing control valve controls can be by natural pond Gas fermentation tank cone bottom, which imports, realizes that gas phase circulation collaboration promotion stirs, and can also be circulated and evacuated by gas when liquid phase exports Bore the material of bottom sedimentation.Roots blower energy automatic start supercharging output biogas passes through gas storage control when fermentation tank biogas produces pressure-fired It is temporary or provide combustion through burning supply control valve control for the biogas combustion machine of methane boiler that valve processed, appendix import biogas storage tank Material.Steam fin heat of the steam caused by methane boiler by steam control valve through steam pipe output for counter-current drying tower right lower quadrant Blower fan heat supply, or greenhouse provide thermal source.
Aqueous less agricultural crop straw through differential stranding fine groundization of sinusoidal roller extruding, be easy to subsequently to input inverse by such material Operation is dried in stream drying tower.Sinusoidal roller surface is continuous sine surface, corresponding bearing arrangement sealing and dustproof, is also adapted to Strongly extruding, can the particularly advantageous extruding by force of convenient adjusting roller spacing and roller differential pair turn stranding stone roller to turning and extruding differential pair turn Crush and promote stalk refinement, be easy to follow-up highly effective drying.Sinusoidal roller bites that continuous reliable, extruding compression ratio is special to material Greatly, the differential stranding of sinusoidal roller curved surface grinds reliable, durable, skimming over property is good, and 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 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；
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 three measures all have distinguishing feature, and energy reliable collaborative is to the king-sized agricultural crop straw of moisture gradient Comprehensive development and utilization is realized with discarded object, there is complete unexpected operation principle and effect, while design also has Extremely strong creative and good popularizing application prospect.
Brief description of the drawings
Fig. 1 is the planar structure schematic diagram of the present invention.
Fig. 2 is sinusoidal drum structure schematic diagram.
Fig. 3 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；D, computer control system；E heat pump main frames；1st, biogas fermentation Groove；2nd, biogas storage tank；3rd, counter-current drying tower；4th, methane boiler；5th, burning supply control valve；6th, biogas combustion machine；7th, steam control Valve processed；8th, steam pipe；9th, boiler exhaust gas pipe；10th, feed water valve；11st, stirring motor reductor；12nd, feed well；13rd, agitating paddle； 14th, biogas pipe；15th, roots blower；16th, transfusion control valve；17th, air-blowing control valve；18th, gas storage control valve；19th, L-shaped hold one's breath into Expect auger；20th, pressure gauge；21st, blowoff valve；22nd, horizon；23rd, appendix；24th, pulverizer；25th, mouse cage tubular heat exchanger； 30th, shield；31st, spiral closes wind charger；32nd, offgas duct；33rd, steam fin air-heater；34th, air blower；35th, wind discharging is closed Machine；36th, compressed air hose；37th, cylinder；38th, axle sleeve；39th, expansion link；40th, spherical faced pan；41st, 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, air outlet；74th, refrigerant pipe；75th, condense Device；76th, condenser air inlet.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
The pulse gas explosion formula stalk Integrated Processing Unit of a kind of magnetic tape trailer recuperation of heat and heat exchanger as shown in FIG. 1 to 3, 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, it is characterised in that：The middle part of biogas fermentation groove 1 is provided with mouse cage tubular heat exchanger 25, in biogas fermentation groove 1 Portion is provided with agitating paddle 13, and agitating paddle 13 is connected by the stirring motor reductor 11 at agitating shaft and top, the top of biogas fermentation groove 1 Feed water valve 10 is connected by pipeline, top connection L-shaped is held one's breath feeding packing auger 19, and L-shaped is held one's breath the connection charging of the top of feeding packing auger 19 Groove 12, the top of feed well 12 are provided with pulverizer 24, and the bottom of biogas fermentation groove 1 is tapered, are connected by pipeline, transfusion control valve 16 Pump inlet, the upper right quarter of biogas fermentation groove 1 connect the bottom of biogas fermentation groove 1 by biogas pipe 14, roots blower 15, air-blowing control valve 17 Portion's pipeline, the outlet of roots blower 15 are connected by pipeline, gas storage control valve 18, appendix 23 with the top of biogas storage tank 2, biogas storage The top of tank 2 connection pressure gauge 20, bottom connect blowoff valve 21 by pipeline, and the top of biogas storage tank 2 is supplied by appendix 23, burning Gas control valve 5, biogas combustion machine 6 connect methane boiler 4, the top of methane boiler 4 connection boiler exhaust gas pipe 9, the top of methane boiler 4 Steam fin air-heater 33 is connected by steam pipe 8, steam control valve 7, steam fin air-heater 33 is dry with adverse current by pipeline The dry bottom of tower 3 connection, the inside of counter-current drying tower 3 are provided with stacking sieve-like cone bucket 42, cone disk 43, and 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, wind charger 31 and offgas duct 32, spiral shell are closed in the top of counter-current drying tower 3 provided with spiral The import top of traling wind charger 31 is provided with sinusoidal roller A, and sinusoidal roller A surfaces are continuous sine surface, and offgas duct 32 passes through Pipeline 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, evaporation The top of device 72 is 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 dry with adverse current through steam fin air-heater 33 Wind discharging machine 35 is closed in the dry bottom of tower 3 connection, the connection of the bottom of counter-current drying tower 3, and the lower left quarter of counter-current drying tower 3 is provided with cosine lacquer disk(-sc) arteries and veins Burst device of air 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 36th, baffle ring 41 and pot shape spherical faced pan 40 form, and thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is cosine curve, Pot shape spherical faced pan 40 is provided with below cosine lacquer disk(-sc), cosine lacquer disk(-sc) connects extra-organismal cylinder 37 through expansion link 39, and cylinder 37 can drive Dynamic expansion link 39 drives cosine lacquer disk(-sc) to move up and down, and the front hollow of expansion link 39 simultaneously connects compressed air hose 36 and also connects cosine glue Disk inner chamber body；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 progress highly effective drying is squeezed to rubbing with the hands using steam.
Biogas fermentation groove 1 maintains 2/3rds liquid level, can supplement required water by feed water valve 10, material passes through L-shaped Feeding packing auger of holding one's breath 19 prevents gas from leaking using water seal closed-type feed, while is advantageous to slight positive pressure state in retention groove.Groove top Agitating paddle 13 rotates in the driver slot of stirring motor reductor 11 in portion, and 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.
Favorably the ferment liquid phase material thoroughly degraded of bottom land taper is used as day by pipeline, transfusion control valve 16, pump output Right Fertilizer application, the upper right quarter of biogas fermentation groove 1 has the output of biogas pipe 14, and biogas is pressurized through roots blower 15, air-blowing control valve 17 is controlled System can be bored bottom importing by biogas fermentation groove 1 and realize that gas phase circulation collaboration promotion stirs, and be able to can also be passed through when liquid phase exports The material of gas circulation evacuation cone bottom sedimentation.Roots blower 15 can automatic start supercharging output natural pond when fermentation tank biogas produces pressure-fired It is methane boiler that gas is imported biogas storage tank 2 and kept in or controlled through burning supply control valve 5 by gas storage control valve 18, appendix 23 4 biogas combustion machine 6 provides fuel.Steam caused by methane boiler 4 is adverse current through the output of steam pipe 8 by steam control valve 7 The heat supply of steam fin air-heater 33 of the right lower quadrant of drying tower 3, or greenhouse provide thermal source.
Aqueous less agricultural crop straw is easy to subsequently input through differential stranding fine groundization of sinusoidal roller A extruding, such material Operation is dried in counter-current drying tower 3.Sinusoidal roller A surfaces are continuous sine surface, corresponding bearing arrangement sealing and dustproof, Strength extruding is adapted to turning and extruding differential pair to turn, can the particularly advantageous strong extruding of convenient adjusting roller spacing and roller differential pair turn Rub with the hands to grind to crush and promote stalk refinement, be easy to follow-up highly effective drying.Sinusoidal roller A bites continuous reliable, extruding compression ratio to material Especially big, the sinusoidal differential stranding of roller A curved surfaces grinds reliable, durable, skimming over property is good, and crushing effect is especially good while energy consumption is also special It is 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 pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger, including sinusoidal 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 are held one's breath feeding packing auger top connection feed well, and feed well top is provided with pulverizer, and biogas fermentation trench bottom is in Taper, pump inlet is connected by pipeline, transfusion control valve, biogas fermentation groove upper right quarter passes through biogas pipe, roots blower, air-blowing control Valve processed connects biogas fermentation trench bottom pipeline, and roots blower outlet passes through on pipeline, gas storage control valve, appendix and biogas storage tank Portion connect, biogas tank top connection pressure gauge, bottom by pipeline connect blowoff valve, biogas storage tank top by appendix, Burning supply control valve, biogas combustion machine connection methane boiler, methane boiler top connection boiler exhaust gas pipe, methane boiler top Steam fin air-heater is connected by steam pipe, steam control valve, steam fin air-heater passes through under pipeline and counter-current drying tower Portion connects, and is slightly larger than cone bucket provided with stacking sieve-like cone bucket, cone disk, cone disk diameter inside counter-current drying tower, and bore tray bottom to have electricity Wind charger and offgas duct are closed in material controlling door, counter-current drying tower top provided with spiral, and spiral closes wind charger import top and is provided with just String roller, sinusoidal roller surface are continuous sine surface, and offgas duct is sequentially connected tail gas air exhauster, cyclone separator by pipeline And evaporator, evaporator upper end are provided with air outlet, evaporator top is sequentially connected heat pump main frame and condenser by refrigerant pipe, cold Condenser one end is provided with condenser air inlet, and the other end connects blower inlet by pipeline, and blower outlet is through steam wing Piece air-heater is connected with counter-current drying tower bottom, and wind discharging machine is closed in the connection of counter-current drying tower bottom, and counter-current drying tower lower left quarter is set There is cosine lacquer disk(-sc) pulse gas explosion device；Cosine lacquer disk(-sc) pulse gas explosion device is empty by cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compression Tracheae, 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 cosine curve, remaining Pot shape spherical faced pan is provided with below string lacquer disk(-sc), cosine lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive expansion link band Dynamic cosine lacquer disk(-sc) moves up and down, and expansion link front hollow simultaneously connects compressed air hose and also connects cosine lacquer disk(-sc) inner chamber body；Processing dress Put and controlled by computer control system.
2. the pulse gas explosion formula stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat and heat exchanger according to claim 1, its feature It 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 body by shield Outer 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 pulse gas explosion formula stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat and heat exchanger according to claim 1, its feature It is：Baffle ring is provided with above the pot shape spherical faced pan.
CN201710924861.2A 2017-10-02 2017-10-02 Magnetic tape trailer recuperation of heat and the pulse gas explosion formula stalk Integrated Processing Unit of heat exchanger Withdrawn CN107655307A (en)

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

Patent Citations (4)

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

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Application publication date: 20180202