CN107606921A - The stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester - Google Patents
The stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester Download PDFInfo
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- CN107606921A CN107606921A CN201710942061.3A CN201710942061A CN107606921A CN 107606921 A CN107606921 A CN 107606921A CN 201710942061 A CN201710942061 A CN 201710942061A CN 107606921 A CN107606921 A CN 107606921A
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- biogas
- sinusoidal
- spark arrester
- lacquer disk
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- 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
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- 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, the stalk Integrated Processing Unit of heat exchanger and sinusoidal spark arrester, including sinusoidal roller, biogas fermentation groove, biogas storage tank, counter-current drying tower, biogas combustion machine, methane boiler, heat pump main frame and computer, biogas fermentation groove lower left quarter is provided with sinusoidal ultrasound wave vibrator, upper right quarter passes through pipeline, roots blower link slot bottom, roots blower outlet connection biogas storage tank, biogas storage tank passes through pipeline, 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 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.Sinusoidal roller, cosine lacquer disk(-sc) pulse gas explosion device and the sinusoidal ultrasound wave vibrator of the present invention all has distinguishing feature, and 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 the stalk Integrated Processing Unit of a kind of magnetic tape trailer recuperation of heat, heat exchanger and 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 magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester, it is adapted to the big agricultural wastes of moisture gradient
Processing.This has especially important meaning for improving agriculture industrialization circulation economies of scale.
The content of the invention
The technical problem to be solved in the present invention is exactly overcome the deficiencies in the prior art, there is provided a kind of magnetic tape trailer recuperation of heat, heat exchange
The stalk Integrated Processing Unit of device and sinusoidal spark arrester.
For overcome the deficiencies in the prior art, the present invention takes following technical scheme：
The stalk Integrated Processing Unit of a kind of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester, including sinusoidal roller, biogas
Fermentation tank, biogas storage tank, counter-current drying tower, biogas combustion machine, methane boiler, heat pump main frame and computer control system, biogas
Mouse cage tubular heat exchanger is provided with the middle part of fermentation tank, is provided with agitating paddle inside biogas fermentation groove, agitating paddle passes through agitating shaft and top
The connection of stirring motor reductor, biogas fermentation groove top portion is communicated with feed water valve, and biogas fermentation groove top connection L-shaped is held one's breath charging
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 groove lower left quarter is provided with
Sinusoidal ultrasound wave vibrator, biogas fermentation trench bottom is tapered, and biogas fermentation trench bottom connects pump inlet by control valve of infusing,
Biogas fermentation groove upper right quarter connects biogas fermentation trench bottom pipeline, roots blower by biogas pipe, roots blower, air-blowing control valve
Outlet is connected by pipeline, gas storage control valve, appendix and biogas storage tank top, biogas tank top connection pressure gauge, bottom
Blowoff valve is connected by pipeline, biogas storage tank top is connected by appendix, spark arrester, burning supply control valve, biogas combustion machine
Logical methane boiler, methane boiler top connection boiler exhaust gas pipe, methane boiler top passes through steam pipe, steam control valve connection is steamed
Vapour fin air-heater, steam fin air-heater are connected by pipeline with counter-current drying tower bottom, and layer is provided with inside counter-current drying tower
Folded sieve-like cone bucket, cone disk, cone disk diameter is more than cone bucket, and cone tray bottom has automatically controlled bin gate, and cone disk is in below cone bucket；Adverse current is dry
Wind charger and offgas duct are closed in dry tower top provided with spiral, and spiral closes wind charger import top and is provided with sinusoidal roller, sinusoidal roller
Cylinder surface is continuous sine surface, and offgas duct is sequentially communicated tail gas air exhauster, cyclone separator and evaporator, and evaporator upper end is set
There is air outlet, evaporator top is sequentially connected heat pump main frame and condenser by refrigerant pipe, and condenser one end is entered provided with condenser
Air port, other end connection blower inlet, blower outlet are connected through steam fin air-heater with counter-current drying tower bottom,
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 glue
Disk pulse gas explosion device is made up of cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape spherical faced pan, remaining
String lacquer disk(-sc) section thick middle thin edge, cosine lacquer disk(-sc) section are cosine curve shape, and pot shape spherical faced pan is provided with below cosine lacquer disk(-sc), remaining
String lacquer disk(-sc) connects extra-organismal cylinder through expansion link, and cylinder can drive expansion link to drive cosine lacquer disk(-sc) to move up and down, before expansion link
Portion is hollow and connects compressed air hose and cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator is driven by actuating unit, can be high
Velocity modulation speed rotation, the structure of sinusoidal ultrasound wave vibrator is spherical cap shape, and spherical cap edge is smooth continuous sine curve, from ball
Lid center has crest, trough progressively to expand continuous diverging feature to edge；Spark arrester is tubular heat exchanger formula spark arrester, spark arrester
Shell side remains full of water.
It is further to improve, it is provided with shield above the cosine lacquer disk(-sc) pulse gas explosion device, shield is by cosine lacquer disk(-sc) pulse
Gas explosion device stretches out extra-organismal part and covered, and makes counter-current drying tower associative perception preferable, gas explosion device can be carried out by removing shield
Convenient maintenance.
It is further to improve, it is provided with baffle ring above the pot shape spherical faced pan.
Further to improve, the offgas duct is set through biogas storage tank.
Further to improve, the biogas tubulation in the tubular heat exchanger formula spark arrester is micro- diameter tube and tubular heat exchanger
The sinusoidal sharp wave shape inner fin of copper material manufacture is provided with formula spark arrester.
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.
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 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：
1st, 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；
2nd, cosine lacquer disk(-sc) pulse gas explosion device can effectively simulate, produce macroscopical discontinuous blast, and excitation drying tower gas phase is strong
Pulsatile impact, the collaboration of gas explosion turning over materials promote adverse current highly effective drying；
3rd, sinusoidal ultrasound wave vibrator is rotated by the speed governing of actuating unit kinetic energy high speed in the liquid phase, produces similar ultrasound
The strong cavitation effect of ripple, effectively facilitates mass transfer process, and collaboration promotes fermentation to realize efficient Quick material degraded；
4th, dry tower counter-flow highly effective drying can an air blast, also can steam heating dry, convenient can also realize tail heat driven heat pump
Recycling, energy consumption for drying can drop to especially low.
Above four main measures all have distinguishing feature, and energy reliable collaborative is to the king-sized agricultural crop straw of moisture gradient
Comprehensive development and utilization is realized with discarded object, there is complete unexpected operation principle and effect, while design also has
Extremely strong creative and good popularizing application prospect.
Brief description of the drawings
Fig. 1 is the planar structure schematic diagram of the present invention.
Fig. 2 is the main structure diagram of sinusoidal ultrasound wave vibrator.
Fig. 3 is the overlooking the structure diagram of sinusoidal ultrasound wave vibrator.
Fig. 4 is the present invention looks up structural representation of sinusoidal ultrasound wave vibrator.
Fig. 5 is the strabismus structural representation of bowing of sinusoidal ultrasound wave vibrator.
Fig. 6 is the oblique present invention looks up structural representation of sinusoidal ultrasound wave vibrator.
Fig. 7 is 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；D, computer control system
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；8th, steam pipe；9th, boiler exhaust gas pipe；10th, feed water valve；11st, stirring motor slows down
Machine；12nd, feed well；13rd, agitating paddle；14th, biogas pipe；15th, roots blower；16th, transfusion control valve；17th, air-blowing control valve；18、
Gas storage control valve；19th, L-shaped is held one's breath feeding packing auger；20th, pressure gauge；21st, blowoff valve；22nd, horizon；23rd, appendix；24th, crush
Machine；25th, mouse cage tubular heat exchanger；26th, spark arrester；30th, shield；31st, spiral closes wind charger；32nd, offgas duct；33rd, steam wing
Piece air-heater；34th, air blower；35th, wind discharging machine is closed；36th, compressed air hose；37th, cylinder；38th, axle sleeve；39th, expansion link；40、
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, steam
Send out device；73rd, air outlet；74th, refrigerant pipe；75th, condenser；76th, condenser air inlet.
Embodiment
In conjunction with accompanying drawing, the present invention is further elaborated with.
The stalk Integrated Processing Unit of a kind of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester as shown in Fig. 1~Fig. 9, bag
Include 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
With computer control system D, it is characterised in that：The middle part of biogas fermentation groove 1 is provided with mouse cage tubular heat exchanger 25, biogas fermentation groove 1
Inside is provided with agitating paddle 13, and agitating paddle 13 is connected by the stirring motor reductor 11 at agitating shaft and top, and biogas fermentation groove 1 pushes up
Portion connects feed water valve 10 by pipeline, and top connection L-shaped is held one's breath feeding packing auger 19, L-shaped hold one's breath the top of feeding packing auger 19 connect into
Hopper 12, the top of feed well 12 are provided with pulverizer 24, and the lower left quarter of biogas fermentation groove 1 is provided with sinusoidal ultrasound wave vibrator C, biogas hair
The bottom of ferment groove 1 is tapered, connects pump inlet by pipeline, transfusion control valve 16, the upper right quarter of biogas fermentation groove 1 passes through biogas pipe
14th, roots blower 15, air-blowing control valve 17 connect the bottom pipe of biogas fermentation groove 1, and the outlet of roots blower 15 passes through pipeline, gas storage
Control valve 18, appendix 23 are connected with the top of biogas storage tank 2, and the top of biogas storage tank 2 connection pressure gauge 20, bottom is connected by pipeline
Blowoff valve 21 is connect, the top of biogas storage tank 2 is connected by appendix 23, spark arrester 26, burning supply control valve 5, biogas combustion machine 6
Methane boiler 4, the top of methane boiler 4 connection boiler exhaust gas pipe 9, the top of methane boiler 4 is connected by steam pipe 8, steam control valve 7
Steam fin air-heater 33 is connect, steam fin air-heater 33 is connected by pipeline with the bottom of counter-current drying tower 3, counter-current drying tower 3
Inside is provided with stacking sieve-like cone bucket 42, cone disk 43, bores the diameter of disk 43 and is slightly larger than cone bucket 42, and bores the bottom of disk 43 to have automatically controlled bin gate
44, wind charger 31 and offgas duct 32 are closed in the top of counter-current drying tower 3 provided with spiral, and spiral closes the import top of wind charger 31 and is provided with
Sinusoidal roller A, sinusoidal roller A surfaces are continuous sine surface, and offgas duct 32 is sequentially connected tail gas air exhauster 71, rotation by pipeline
Wind separator 70 and evaporator 72, the upper end of evaporator 72 are provided with air outlet 73, and the top of evaporator 72 is connected successively by refrigerant pipe 74
Heat pump main frame E and condenser 75 are met, the one end of condenser 75 is provided with condenser air inlet 76, and the other end connects air blower by pipeline
34 air inlets, the air outlet of air blower 34 are connected through steam fin air-heater 33 with the bottom of counter-current drying tower 3, the bottom of counter-current drying tower 3
Wind discharging machine 35 is closed in portion's connection, and the lower left quarter of counter-current drying tower 3 is provided with cosine lacquer disk(-sc) pulse gas explosion device B；Cosine lacquer disk(-sc) pulse is quick-fried
Device of air B is by 40 groups of 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
Into thick edge is slightly thin among cosine lacquer disk(-sc) section, and general shape is cosine curve, and pot shape spherical faced pan is provided with below cosine lacquer disk(-sc)
40, cosine lacquer disk(-sc) connects extra-organismal cylinder 37 through expansion link 39, and cylinder 37 can drive expansion link 39 to drive above and below cosine lacquer disk(-sc)
Motion, the front hollow of expansion link 39 simultaneously connect compressed air hose 36 and also connect cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator C
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, there are crest, trough progressively to expand continuous diverging feature from spherical cap center to edge；Spark arrester 26 is
Tubular heat exchanger formula spark arrester, spark arrester shell side remain full of water, and it is micro- diameter tube and large number of, copper that tube side, which leads to biogas tubulation,
Material manufacture has sinusoidal sharp wave shape inner fin；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.
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 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 (5)
1. the stalk Integrated Processing Unit of a kind of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester, 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 connect, and biogas fermentation groove top portion is communicated with feed water valve, biogas fermentation groove top connection L-shaped
Hold one's breath feeding packing auger, L-shaped is held one's breath feeding packing auger top connection feed well, and feed well top is provided with pulverizer, a biogas fermentation groove left side
Bottom is provided with sinusoidal ultrasound wave vibrator, and biogas fermentation trench bottom is tapered, and biogas fermentation trench bottom is connected by control valve of infusing
Logical pump inlet, biogas fermentation groove upper right quarter connect biogas fermentation trench bottom pipe by biogas pipe, roots blower, air-blowing control valve
Road, roots blower outlet are connected by pipeline, gas storage control valve, appendix and biogas storage tank top, the connection of biogas tank top
Pressure gauge, bottom connect blowoff valve by pipeline, and biogas storage tank top passes through appendix, spark arrester, burning supply control valve, natural pond
Gas combustor connects methane boiler, and methane boiler top connection boiler exhaust gas pipe, methane boiler top passes through steam pipe, steam control
Valve processed connects steam fin air-heater, and steam fin air-heater is connected by pipeline with counter-current drying tower bottom, counter-current drying tower
Inside bores disk diameter and is more than cone bucket provided with sieve-like cone bucket, cone disk is laminated, and bores tray bottom to have automatically controlled bin gate, bores disk and is in cone bucket
Lower section；Wind charger and offgas duct are closed in 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, and offgas duct is sequentially communicated tail gas air exhauster, cyclone separator and evaporator,
Evaporator upper end is provided with air outlet, and evaporator top is sequentially connected heat pump main frame and condenser, condenser one end by refrigerant pipe
It is dry with adverse current through steam fin air-heater provided with condenser air inlet, other end connection blower inlet, blower outlet
Wind discharging machine is closed in dry tower bottom connection, the connection of counter-current drying tower bottom, and it is quick-fried that counter-current drying tower lower left quarter is provided with cosine lacquer disk(-sc) pulse
Device of air；Cosine lacquer disk(-sc) pulse gas explosion device is by cosine lacquer disk(-sc), cylinder, expansion link, axle sleeve, compressed air hose, baffle ring and pot shape
Spherical faced pan forms, cosine lacquer disk(-sc) section thick middle thin edge, and cosine lacquer disk(-sc) section is cosine curve shape, is provided with below cosine lacquer disk(-sc)
Pot shape spherical faced pan, cosine lacquer disk(-sc) connect extra-organismal cylinder through expansion link, and cylinder can drive expansion link to drive above and below cosine lacquer disk(-sc)
Motion, expansion link front hollow simultaneously connect compressed air hose and cosine lacquer disk(-sc) inner chamber body；Sinusoidal ultrasound wave vibrator passes through power
Mechanism drives, the speed governing rotation of energy high speed, and the structure of sinusoidal ultrasound wave vibrator is spherical cap shape, and spherical cap edge is the continuous of smoothness
Sine curve, there are crest, trough progressively to expand continuous diverging feature from spherical cap center to edge；Spark arrester is tubular heat exchanger formula
Spark arrester, spark arrester shell side remain full of water.
2. the stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester 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 stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester according to claim 1, its feature
It is：Baffle ring is provided with above the pot shape spherical faced pan.
4. the stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester according to claim 1, its feature
It is：The offgas duct is set through biogas storage tank.
5. the stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester according to claim 1, its feature
It is：Biogas tubulation in the tubular heat exchanger formula spark arrester is interior setting in micro- diameter tube and tubular heat exchanger formula spark arrester
There is the sinusoidal sharp wave shape inner fin that copper material manufactures.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710942061.3A CN107606921A (en) | 2017-10-11 | 2017-10-11 | The stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710942061.3A CN107606921A (en) | 2017-10-11 | 2017-10-11 | The stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107606921A true CN107606921A (en) | 2018-01-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710942061.3A Pending CN107606921A (en) | 2017-10-11 | 2017-10-11 | The stalk Integrated Processing Unit of magnetic tape trailer recuperation of heat, heat exchanger and sinusoidal spark arrester |
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| CN (1) | CN107606921A (en) |
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| CN102517199A (en) * | 2011-11-17 | 2012-06-27 | 西安建筑科技大学 | Multi-cycle stirring egg-shaped anaerobic fermentation system |
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| 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 |
| CN105066653A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Heat pump type tail heat recovery and penetrating counterflow fluidized drying machine |
| 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 |
| CN206428268U (en) * | 2017-01-17 | 2017-08-22 | 临沂友康生物科技有限公司 | A kind of zymotic fluid bacterial cell disruption tank |
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|---|---|---|---|---|
| CN102553697A (en) * | 2010-10-07 | 2012-07-11 | 通用电气公司 | Pressure wave pulverizer for gasificatin applications |
| 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 |
| CN105066653A (en) * | 2015-08-14 | 2015-11-18 | 吉首大学 | Heat pump type tail heat recovery and penetrating counterflow fluidized drying machine |
| 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 |
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