CN107858280A - The stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester - Google Patents
The stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester Download PDFInfo
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- CN107858280A CN107858280A CN201710929407.6A CN201710929407A CN107858280A CN 107858280 A CN107858280 A CN 107858280A CN 201710929407 A CN201710929407 A CN 201710929407A CN 107858280 A CN107858280 A CN 107858280A
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- biogas
- sinusoidal
- counter
- drying tower
- lacquer disk
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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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/44—Solid fuels essentially based on materials of non-mineral origin on vegetable substances
- C10L5/445—Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M23/00—Constructional details, e.g. recesses, hinges
- C12M23/36—Means for collection or storage of gas; Gas holders
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M33/00—Means for introduction, transport, positioning, extraction, harvesting, peeling or sampling of biological material in or from the apparatus
- C12M33/16—Screw conveyor
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—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
-
- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/32—Molding or moulds
-
- 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
- Y02E50/10—Biofuels, e.g. bio-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
- 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
Abstract
The invention discloses a kind of band biomass fuel and the stalk Integrated Processing Unit of sinusoidal spark arrester,Including sinusoidal roller,Biogas fermentation groove,Biogas storage tank,Counter-current drying tower,Biogas combustion machine and methane boiler,Biogas fermentation groove lower left quarter is provided with sinusoidal ultrasound wave vibrator,Upper right quarter passes through pipeline,Roots blower link slot bottom,Roots blower outlet connection biogas storage tank,Biogas storage tank passes through pipeline,Spark arrester,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,Counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse gas explosion device,The sinusoidal roller of the present invention,Cosine lacquer disk(-sc) pulse gas explosion device and sinusoidal ultrasound wave vibrator all have distinguishing feature,Energy reliable collaborative realizes comprehensive development and utilization to the king-sized agricultural crop straw of moisture gradient and discarded object.
Description
Technical field
The present invention relates to a kind of band biomass fuel and the stalk Integrated Processing Unit of sinusoidal spark arrester.
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
The stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester, 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 band biomass fuel and
The stalk Integrated Processing Unit of sinusoidal spark arrester.
For overcome the deficiencies in the prior art, the present invention takes following technical scheme：
A kind of stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester, including sinusoidal roller, biogas fermentation groove,
Biogas storage tank, counter-current drying tower, biogas combustion machine and methane boiler, it is characterised in that：Mouse cage is provided with the middle part of biogas fermentation groove to arrange
Heat exchange of heat pipe, biogas fermentation groove inside are provided with agitating paddle, and agitating paddle is connected by agitating shaft and the stirring motor reductor at top,
Biogas fermentation groove top portion connects feed water valve by pipeline, and top connection L-shaped is held one's breath feeding packing auger, and L-shaped is held one's breath feeding packing auger top
Feed well is connected, feed well top is provided with pulverizer, and biogas fermentation groove lower left quarter is provided with sinusoidal ultrasound wave vibrator, biogas fermentation
Trench bottom is tapered, connects pump inlet by pipeline, transfusion control valve, biogas fermentation groove upper right quarter passes through biogas pipe, Luo Cifeng
Machine, air-blowing control valve connection biogas fermentation trench bottom pipeline, roots blower outlet by pipeline, gas storage control valve, appendix with
Biogas storage tank top connects, and biogas tank top connection pressure gauge, bottom connects blowoff valve by pipeline, and biogas storage tank top leads to
Cross appendix, spark arrester, burning supply control valve, biogas combustion machine connection methane boiler, methane boiler top connection boiler tail
Tracheae, methane boiler top connect steam fin air-heater by steam pipe, steam control valve, and steam fin air-heater passes through pipe
Road is connected with counter-current drying tower bottom, stacking sieve-like cone bucket, cone disk is provided with inside counter-current drying tower, cone disk diameter is slightly larger than cone
Bucket, and cone tray bottom has automatically controlled bin gate, wind charger and offgas duct are closed in counter-current drying tower top provided with spiral, and spiral closes wind charging
Machine import top is provided with sinusoidal roller, and sinusoidal roller surface is continuous sine surface, and sinusoidal roller top is provided with segment cutter, air blast
Machine air outlet is connected through steam fin air-heater with counter-current drying tower bottom, the connection life of counter-current drying tower bottom Amenorrhea wind discharging machine
Biomass fuel forming machine, counter-current drying tower lower left quarter are provided with cosine lacquer disk(-sc) pulse gas explosion device；Cosine lacquer disk(-sc) pulse gas explosion device
It is made up of cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan, among cosine lacquer disk(-sc) section
Thick edge is slightly thin, and general shape is cosine curve, is provided with pot shape spherical faced pan below cosine lacquer disk(-sc), cosine lacquer disk(-sc) connects through expansion link
Extra-organismal cylinder is connect, cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compression
Air hose also connects cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator is driven by actuating unit, the speed governing rotation of energy high speed, just
The structure of string ultrasonic wave excitation device is spherical cap shape, and spherical cap edge is smooth continuous sine curve, from spherical cap center to edge
There are crest, trough progressively to expand continuous diverging feature；Spark arrester is tubular heat exchanger formula spark arrester, and spark arrester shell side remains full of
Water, tube side leads to biogas tubulation has sinusoidal sharp wave shape inner fin for micro- diameter tube and large number of, copper material manufacture.
Shield is provided with above the cosine lacquer disk(-sc) pulse gas explosion device, cosine lacquer disk(-sc) pulse gas explosion device is stretched out machine by shield
External part is covered, and makes counter-current drying tower associative perception preferable, and the convenient maintenance of gas explosion device can be carried out by removing shield.
Baffle ring is provided with above the pot shape spherical faced pan.
Its prevailing technology of Integrated Processing Unit process system is to handle agricultural waste material respectively by moisture height,
The higher fresh waste delivery of cumulative water-oil ratio enters fermentation tank and carries out high-efficiency fermenting degraded producing methane, and biogas is used to drive methane boiler to produce
Raw steam, aqueous relatively low agricultural wastes are squeezed to segment, stranding using steam and carry out highly effective drying, the qualified stalk material profit of moisture
Shaping is processed with biological substance fuel forming machine, production biomass fuel carries out sale extra earning.
Biogas fermentation groove maintains 2/3rds liquid level, water, material can be held one's breath as needed for supplementing feed water valve by L-shaped
Feeding packing auger prevents gas from leaking using water seal closed-type feed, while is advantageous to slight positive pressure state in retention groove.Groove top portion is stirred
Mix agitating paddle in motor reducer driver slot to rotate, the mouse cage tubular heat exchanger in the middle part of groove can be directed respectively into cold and hot media implementation groove
Interior heating and cooling regulation and control are beneficial to fermentation, and bottom land taper is easy to material to export.
The sinusoidal ultrasound wave vibrator of cell body lower left quarter is driven by actuating unit, and the speed governing rotation of energy high speed, axle sleeve can be real
Simultaneously favourable sinusoidal ultrasound wave vibrator rotates at a high speed for existing liquid phase sealing.The structure of sinusoidal ultrasound wave vibrator is spherical cap shape, and ball
Lid edge is smooth continuous sine curve, has crest, trough progressively to expand continuous diverging feature from spherical cap center to edge.This
The structure of sample has good bulk strength, when sinusoidal ultrasound wave vibrator passes through actuating unit kinetic energy high speed speed governing in the liquid phase
Rotation, it is clear that the strong cavitation effect of similar ultrasonic wave can be produced, effectively facilitate mass transfer process, collaboration air-blowing, temperature control, stirring promote
Enter fermentation, realize that efficient fast microbiological effect makes material fermentation degrade.
Favorably the ferment liquid phase material thoroughly degraded of bottom land taper be used as naturally by pipeline, transfusion control valve, pump output
Fertilizer application, biogas fermentation groove upper right quarter have biogas pipe output biogas is pressurized through roots blower, air-blowing control valve controls can be by natural pond
Gas fermentation tank cone bottom, which imports, realizes that gas phase circulation collaboration promotion stirs, and can also be circulated and evacuated by gas when liquid phase exports
Bore the material of bottom sedimentation.Roots blower energy automatic start supercharging output biogas passes through gas storage control when fermentation tank biogas produces pressure-fired
It is temporary or provide combustion through burning supply control valve control for the biogas combustion machine of methane boiler that valve processed, appendix import biogas storage tank
Material.Steam fin heat of the steam caused by methane boiler by steam control valve through steam pipe output for counter-current drying tower right lower quadrant
Blower fan heat supply, or greenhouse provide thermal source.Effectively to prevent biogas to be tempered issuable explosive fire accident hidden danger, tubulation is designed
Heat exchanger type spark arrester, spark arrester shell side remain full of water, and it is micro- diameter tube and large number of, copper material that tube side, which leads to biogas tubulation,
Material manufacture has sinusoidal sharp wave shape inner fin, and such structure possesses splendid heat conduction, cooling back-fire relief function.Intuitively retouched with reduction to absurdity
State, it is assumed that high-temperature fuel gas is full of in tempering tube, but sinusoidal sharp wave fin to circumference due to cutting in special structure design, its center
The heat flow of face unit section is that hot-fluid is close more uniform, thus fin temperature field does not have big thermograde change, especially has
Sharp moment reduces the performance that fuel gas temperature knock down the flame realizes back-fire relief function.
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 imports biological substance fuel forming machine by closing the output of wind discharging machine
Carry out processing and forming.Air blower blasts air and is heated to be high temperature air through steam fin air-heater passes through drying tower from bottom to top.
Counter-current drying tower lower left quarter has cosine lacquer disk(-sc) pulse gas explosion device, and energy explosion type release compressed air produces the pulsation of gas explosion material,
Cooperate with tower type counterflow to dry and obtain unthinkable drying effect.
Rational insulation processing is carried out to apparatus system, reduces radiation loss.
Core component cosine lacquer disk(-sc), the thick edge in lacquer disk(-sc) section centre is slightly thin, and general shape is cosine curve, and lacquer disk(-sc) compresses
Pot shape spherical faced pan forms airtight cavity, to wherein inputting compressed air, when air pressure is increasing reaches certain value, and lacquer disk(-sc)
It can produce and be flipped up suddenly, explosion type release is produced to the compressed air wherein stored, explosion vibration shock wave can be produced, it is special
Not favorably material gas explosion is promoted to stir and counter-current drying.
Cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow connection compressed air hose also connects
Logical lacquer disk(-sc) inner chamber body, and realized by axle sleeve with body and isolate airtight connection, and can flexibly stretch, when expansion link drives lacquer disk(-sc) pressure
Airtight cavity can be formed during tight pot shape spherical faced pan, at this moment by compressed air hose to wherein inputting compressed air, in air pressure
The triggering until cosine lacquer disk(-sc) rim pressure transfinites is risen, it is empty to produce the compression for being flipped up internally storing under the effect of lacquer disk(-sc) integral pressure
Gas produces explosion type release, and at this moment expansion link bounces back again, lacquer disk(-sc) just can automatic elastic reply and be flipped back to original initial state, can be with
Repetitive cycling action is carried out again, and baffle ring can assist the upset of cosine lacquer disk(-sc) to reset in case of need.
Compared with prior art, beneficial effects of the present invention also reside in：
Sinusoidal roller material, which bites continuously reliable, extruding and rubbed with the hands, grinds material thinning effect brilliance, while energy consumption is also especially low；
Cosine lacquer disk(-sc) pulse gas explosion device can be simulated effectively, produce macroscopical discontinuous blast, and excitation drying tower gas phase is pulsed by force punching
Hit, the collaboration of gas explosion turning over materials promotes adverse current highly effective drying；
Sinusoidal ultrasound wave vibrator is rotated by the speed governing of actuating unit kinetic energy high speed in the liquid phase, produces the strong of similar ultrasonic wave
Cavitation effect, effectively facilitates mass transfer process, and collaboration promotes fermentation to realize efficient Quick material degraded.
Above three measures all have distinguishing feature, and energy reliable collaborative is to the king-sized agricultural crop straw of moisture gradient
Comprehensive development and utilization is realized with discarded object, there is complete unexpected operation principle and effect, while design also has
Extremely strong creative and good popularizing application prospect.
Brief description of the drawings
Fig. 1 is the planar structure schematic diagram of the present invention.
Fig. 2 is the main structure diagram of sinusoidal ultrasound wave vibrator.
Fig. 3 is the overlooking the structure diagram of sinusoidal ultrasound wave vibrator.
Fig. 4 is the present invention looks up structural representation of sinusoidal ultrasound wave vibrator.
Fig. 5 is the strabismus structural representation of bowing of sinusoidal ultrasound wave vibrator.
Fig. 6 is the oblique present invention looks up structural representation of sinusoidal ultrasound wave vibrator.
Fig. 7 is micro- diameter tube section structure diagram.
Fig. 8 is sinusoidal drum structure schematic diagram.
Fig. 9 is the partial enlargement structural representation of cosine lacquer disk(-sc) pulse gas explosion device.
Each label represents in figure：
A, sinusoidal roller；B, cosine lacquer disk(-sc) pulse gas explosion device；C, sinusoidal ultrasound wave vibrator；1st, biogas fermentation groove；2nd, biogas
Storage tank；3rd, counter-current drying tower；4th, methane boiler；5th, burning supply control valve；6th, biogas combustion machine；7th, steam control valve；8th, steam
Steam pipe；9th, boiler exhaust gas pipe；10th, feed water valve；11st, stirring motor reductor；12nd, feed well；13rd, agitating paddle；14th, biogas pipe；
15th, roots blower；16th, transfusion control valve；17th, air-blowing control valve；18th, gas storage control valve；19th, L-shaped is held one's breath feeding packing auger；20、
Pressure gauge；21st, blowoff valve；22nd, horizon；23rd, appendix；24th, pulverizer；25th, mouse cage tubular heat exchanger；26th, spark arrester；
29th, segment cutter；30th, shield；31st, spiral closes wind charger；32nd, offgas duct；33rd, steam fin air-heater；34th, air blower；35、
Close wind discharging 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；45th, biological substance fuel forming machine.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
The stalk Integrated Processing Unit of a kind of band biomass fuel and sinusoidal spark arrester as shown in Fig. 1~Fig. 9, including just
String roller A, biogas fermentation groove 1, biogas storage tank 2, counter-current drying tower 3, biogas combustion machine 6 and methane boiler 4, it is characterised in that：
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 is provided with agitating paddle 13, and agitating paddle 13 passes through
Agitating shaft and the stirring motor reductor 11 at top connect, and the top of biogas fermentation groove 1 connects feed water valve 10 by pipeline, and top connects
Connect L-shaped to hold one's breath feeding packing auger 19, L-shaped is held one's breath the top of feeding packing auger 19 connection feed well 12, and the top of feed well 12 is provided with pulverizer
24, 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 tapered, passes through pipeline, transfusion
Control valve 16 connects pump inlet, and the upper right quarter of biogas fermentation groove 1 is connected by biogas pipe 14, roots blower 15, air-blowing control valve 17
The bottom pipe of biogas fermentation groove 1, the outlet of roots blower 15 pass through on pipeline, gas storage control valve 18, appendix 23 and biogas storage tank 2
Portion connects, and the top of biogas storage tank 2 connection pressure gauge 20, bottom connects blowoff valve 21 by pipeline, and the top of biogas storage tank 2 passes through defeated
Tracheae 23, spark arrester 26, burning supply control valve 5, biogas combustion machine 6 connect methane boiler 4, the top of methane boiler 4 connection pot
Furnace exhaust gas pipe 9, the top of methane boiler 4 connect steam fin air-heater 33, steam fin heat by steam pipe 8, steam control valve 7
Blower fan 33 is connected by pipeline with the bottom of counter-current drying tower 3, and the inside of counter-current drying tower 3 is provided with stacking sieve-like cone bucket 42, cone disk 43,
The cone diameter of disk 43 is slightly larger than cone bucket 42, and automatically controlled bin gate 44 is arranged at cone disk 43 bottom, and the top of counter-current drying tower 3 is closed wind provided with spiral and entered
Material machine 31 and offgas duct 32, spiral close the import top of wind charger 31 and are provided with sinusoidal roller A, sinusoidal roller A surfaces for it is continuous just
String curved surface, sinusoidal roller A tops are provided with segment cutter 29, and the air outlet of air blower 34 is through steam fin air-heater 33 and counter-current drying tower
3 bottoms connect, the bottom Amenorrhea wind discharging machine 35 of counter-current drying tower 3 connection biological substance fuel forming machine 45, the lower-left of counter-current drying tower 3
Portion is provided with cosine lacquer disk(-sc) pulse gas explosion device B；Cosine lacquer disk(-sc) pulse gas explosion device B by cosine lacquer disk(-sc), cylinder 37, expansion link 39,
Axle sleeve 38, compressed air hose 36, baffle ring 41 and pot shape spherical faced pan 40 form, and thick edge is slightly thin among cosine lacquer disk(-sc) section, greatly
Shape is cosine curve, is provided with pot shape spherical faced pan 40 below cosine lacquer disk(-sc), cosine lacquer disk(-sc) connects extra-organismal through expansion link 39
Cylinder 37, cylinder 37 can drive expansion link 39 to drive cosine lacquer disk(-sc) to move up and down, and the front hollow of expansion link 39 simultaneously connects compression sky
Tracheae 36 also connects cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator C is driven by actuating unit, the speed governing rotation of energy high speed,
Sinusoidal ultrasound wave vibrator C structure is spherical cap shape, and spherical cap edge is smooth continuous sine curve, from spherical cap center to side
Edge has crest, trough progressively to expand continuous diverging feature；Spark arrester 26 is tubular heat exchanger formula spark arrester, and spark arrester shell side is kept
Full of water, tube side leads to biogas tubulation has sinusoidal sharp wave shape inner fin for micro- diameter tube and large number of, copper material manufacture.
It is provided with shield 30 above the cosine lacquer disk(-sc) pulse gas explosion device B, shield 30 is by cosine lacquer disk(-sc) pulse gas explosion device B
Stretch out extra-organismal part to cover, make the associative perception of counter-current drying tower 3 preferable, the convenient dimension of gas explosion device can be carried out by removing shield
Shield.
The top of pot shape spherical faced pan 40 is provided with baffle ring 41.
Its prevailing technology of Integrated Processing Unit process system is to handle agricultural waste material respectively by moisture height,
The higher fresh waste delivery of cumulative water-oil ratio enters fermentation tank and carries out high-efficiency fermenting degraded producing methane, and biogas is used to drive methane boiler to produce
Raw steam, aqueous relatively low agricultural wastes are squeezed to segment, stranding using steam and carry out highly effective drying, the qualified stalk material profit of moisture
Shaping is processed with biological substance fuel forming machine, production biomass fuel carries out sale extra earning.
Biogas fermentation groove 1 maintains 2/3rds liquid level, can supplement required water by feed water valve 10, material passes through L-shaped
Feeding packing auger of holding one's breath 19 prevents gas from leaking using water seal closed-type feed, while is advantageous to slight positive pressure state in retention groove.Groove top
Agitating paddle 13 rotates in the driver slot of stirring motor reductor 11 in portion, and the mouse cage tubular heat exchanger 25 in the middle part of groove can be directed respectively into cold
Thermal medium realizes that heating and cooling regulation and control are beneficial to fermentation in groove, and bottom land taper is easy to material to export.
The sinusoidal ultrasound wave vibrator C of cell body lower left quarter is driven by actuating unit, and the speed governing rotation of energy high speed, axle sleeve can be real
Simultaneously favourable sinusoidal ultrasound wave vibrator C rotates at a high speed for existing liquid phase sealing.Sinusoidal ultrasound wave vibrator C structure is spherical cap shape, and
Spherical cap edge is smooth continuous sine curve, has crest, trough progressively to expand continuous diverging feature from spherical cap center to edge.
Such structure has good bulk strength, when sinusoidal ultrasound wave vibrator C passes through actuating unit kinetic energy high speed in the liquid phase
Speed governing rotates, it is clear that can produce the strong cavitation effect of similar ultrasonic wave, effectively facilitate mass transfer process, collaboration air-blowing, temperature control, stir
Promotion fermentation is mixed, realizes that efficient fast microbiological effect makes material fermentation degrade.
Favorably the ferment liquid phase material thoroughly degraded of bottom land taper is used as day by pipeline, transfusion control valve 16, pump output
Right Fertilizer application, the upper right quarter of biogas fermentation groove 1 has the output of biogas pipe 14, and biogas is pressurized through roots blower 15, air-blowing control valve 17 is controlled
System can be bored bottom importing by biogas fermentation groove 1 and realize that gas phase circulation collaboration promotion stirs, and be able to can also be passed through when liquid phase exports
The material of gas circulation evacuation cone bottom sedimentation.Roots blower 15 can automatic start supercharging output natural pond when fermentation tank biogas produces pressure-fired
It is methane boiler that gas is imported biogas storage tank 2 and kept in or controlled through burning supply control valve 5 by gas storage control valve 18, appendix 23
4 biogas combustion machine 6 provides fuel.Steam caused by methane boiler 4 is adverse current through the output of steam pipe 8 by steam control valve 7
The heat supply of steam fin air-heater 33 of the right lower quadrant of drying tower 3, or greenhouse provide thermal source.Effectively to prevent that biogas tempering may
Caused explosive fire accident hidden danger, design tubular heat exchanger formula spark arrester 26, the shell side of spark arrester 26 remains full of water, and tube side leads to biogas
Tubulation is micro- diameter tube and large number of, copper material manufacture has sinusoidal sharp wave shape inner fin, and such structure possesses splendid
Heat conduction, cooling back-fire relief function.With reduction to absurdity directviewing description, it is assumed that be full of high-temperature fuel gas in tempering tube, but sinusoidal sharp wave fin by
In special structure design, the heat flow in its center to the cross-sectional unit section of circumference is that hot-fluid is close more uniform, thus fin temperature
Degree field does not have big thermograde change, and particularly advantageous moment reduces the hair that fuel gas temperature knock down the flame realizes back-fire relief function
Wave.
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 exported by closing wind discharging machine 35
Import biological substance fuel forming machine 45 and carry out processing and forming.Air blower 34 blasts air and is heated to be height through steam fin air-heater 33
Warm air passes through drying tower from bottom to top.The lower left quarter of counter-current drying tower 3 has cosine lacquer disk(-sc) pulse gas explosion device B, and energy explosion type is released
Put compressed air and produce the pulsation of gas explosion material, collaboration tower type counterflow, which is dried, obtains unthinkable drying effect.
Rational insulation processing is carried out to apparatus system, reduces radiation loss.
Core component cosine lacquer disk(-sc) B, the thick edge in lacquer disk(-sc) section centre is slightly thin, and general shape is cosine curve, and lacquer disk(-sc) B is pressed
Tight pot shape spherical faced pan 40 forms airtight cavity, to wherein inputting compressed air, when air pressure is increasing reaches certain value,
Lacquer disk(-sc) B can be produced to be flipped up suddenly, is produced explosion type release to the compressed air wherein stored, can be produced explosion vibration impact
Ripple, particularly advantageous promotion material gas explosion is stirred and counter-current drying.
Cylinder 37 can drive expansion link 39 to drive cosine lacquer disk(-sc) B to move up and down, and the connection compression of the front hollow of expansion link 39 is empty
Tracheae 36 also connects lacquer disk(-sc) B inner chamber bodies, and is realized by axle sleeve 38 with body 3 and isolate airtight connection, and can flexibly stretch, when stretching
Contracting bar 39 drives lacquer disk(-sc) B to form airtight cavity when compressing pot shape spherical faced pan 40, at this moment by compressed air hose 36 to wherein defeated
Enter compressed air, air pressure rises the triggering until cosine lacquer disk(-sc) B rim pressures transfinite, produce under lacquer disk(-sc) integral pressure acts on to
The upper compressed air internally stored that overturns produces explosion type release, and at this moment expansion link 39 bounces back again, and just energy automatic elastic returns lacquer disk(-sc) B
Original initial state is flipped back to again, can carry out repetitive cycling action again, and baffle ring 41 can assist cosine in case of need
Lacquer disk(-sc) B upset resets.
Above-mentioned simply presently preferred embodiments of the present invention, not makees any formal limitation to the present invention.It is any to be familiar with sheet
The technical staff in field, in the case where not departing from technical solution of the present invention scope, all using the technology contents of the disclosure above
Many possible changes and modifications are made to technical solution of the present invention, or are revised as the equivalent embodiment of equivalent variations.Therefore, it is all
It is the content without departing from technical solution of the present invention, any is simply repaiied to made for any of the above embodiments according to the technology of the present invention essence
Change, equivalent variations and modification, all should fall in the range of technical solution of the present invention protection.
Claims (3)
1. the stalk Integrated Processing Unit of a kind of band biomass fuel and sinusoidal spark arrester, including sinusoidal roller, biogas fermentation
Groove, biogas storage tank, counter-current drying tower, biogas combustion machine and methane boiler, it is characterised in that：Mouse cage is provided with the middle part of biogas fermentation groove
Tubular heat exchanger, biogas fermentation groove inside are provided with agitating paddle, and agitating paddle passes through agitating shaft and the stirring motor reductor at top connects
Connect, biogas fermentation groove top portion connects feed water valve by pipeline, and top connection L-shaped is held one's breath feeding packing auger, and L-shaped is held one's breath in feeding packing auger
Portion connects feed well, and feed well top is provided with pulverizer, and biogas fermentation groove lower left quarter is provided with sinusoidal ultrasound wave vibrator, biogas hair
Ferment trench bottom is tapered, connects pump inlet by pipeline, transfusion control valve, biogas fermentation groove upper right quarter passes through biogas pipe, Roots
Blower fan, air-blowing control valve connection biogas fermentation trench bottom pipeline, roots blower outlet passes through pipeline, gas storage control valve, appendix
It is connected with biogas storage tank top, biogas tank top connection pressure gauge, bottom connects blowoff valve, biogas storage tank top by pipeline
Methane boiler, methane boiler top connection boiler are connected by appendix, spark arrester, burning supply control valve, biogas combustion machine
Offgas duct, methane boiler top connect steam fin air-heater by steam pipe, steam control valve, and steam fin air-heater passes through
Pipeline is connected with counter-current drying tower bottom, stacking sieve-like cone bucket, cone disk is provided with inside counter-current drying tower, cone disk diameter is slightly larger than cone
Bucket, and cone tray bottom has automatically controlled bin gate, wind charger and offgas duct are closed in counter-current drying tower top provided with spiral, and spiral closes wind charging
Machine import top is provided with sinusoidal roller, and sinusoidal roller surface is continuous sine surface, and sinusoidal roller top is provided with segment cutter, air blast
Machine air outlet is connected through steam fin air-heater with counter-current drying tower bottom, the connection life of counter-current drying tower bottom Amenorrhea wind discharging machine
Biomass fuel forming machine, counter-current drying tower lower left quarter are provided with cosine lacquer disk(-sc) pulse gas explosion device；Cosine lacquer disk(-sc) pulse gas explosion device
It is made up of cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan, among cosine lacquer disk(-sc) section
Thick edge is slightly thin, and general shape is cosine curve, is provided with pot shape spherical faced pan below cosine lacquer disk(-sc), cosine lacquer disk(-sc) connects through expansion link
Extra-organismal cylinder is connect, cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, and expansion link front hollow simultaneously connects compression
Air hose also connects cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator is driven by actuating unit, the speed governing rotation of energy high speed, just
The structure of string ultrasonic wave excitation device is spherical cap shape, and spherical cap edge is smooth continuous sine curve, from spherical cap center to edge
There are crest, trough progressively to expand continuous diverging feature；Spark arrester is tubular heat exchanger formula spark arrester, and spark arrester shell side remains full of
Water, tube side leads to biogas tubulation has sinusoidal sharp wave shape inner fin for micro- diameter tube and large number of, copper material manufacture.
2. the stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester, its feature exist according to claim 1
In：Shield is provided with above the cosine lacquer disk(-sc) pulse gas explosion device, shield stretches out cosine lacquer disk(-sc) pulse gas explosion device outside body
Part cover, make counter-current drying tower associative perception preferable, the convenient maintenance of gas explosion device can be carried out by removing shield.
3. the stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester, its feature exist according to claim 1
In：Baffle ring is provided with above the pot shape spherical faced pan.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710929407.6A CN107858280A (en) | 2017-10-09 | 2017-10-09 | The stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710929407.6A CN107858280A (en) | 2017-10-09 | 2017-10-09 | The stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107858280A true CN107858280A (en) | 2018-03-30 |
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ID=61698407
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710929407.6A Withdrawn CN107858280A (en) | 2017-10-09 | 2017-10-09 | The stalk Integrated Processing Unit of band biomass fuel and sinusoidal spark arrester |
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| Country | Link |
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| CN (1) | CN107858280A (en) |
Citations (4)
| 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 |
| CN206500626U (en) * | 2017-02-16 | 2017-09-19 | 锦州宏达新材料有限公司 | Horizontal metal powder dryer |
-
2017
- 2017-10-09 CN CN201710929407.6A patent/CN107858280A/en not_active Withdrawn
Patent Citations (4)
| 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 |
| CN206500626U (en) * | 2017-02-16 | 2017-09-19 | 锦州宏达新材料有限公司 | Horizontal metal powder dryer |
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Application publication date: 20180330 |