CN108329080A - Air energy waste harmless treatment and organic fertilizer fermentation equipment integrating and technique - Google Patents
Air energy waste harmless treatment and organic fertilizer fermentation equipment integrating and technique Download PDFInfo
- Publication number
- CN108329080A CN108329080A CN201810446814.6A CN201810446814A CN108329080A CN 108329080 A CN108329080 A CN 108329080A CN 201810446814 A CN201810446814 A CN 201810446814A CN 108329080 A CN108329080 A CN 108329080A
- Authority
- CN
- China
- Prior art keywords
- fermentation
- bearer network
- waste
- hot wind
- network band
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05D—INORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
- C05D1/00—Fertilisers containing potassium
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/90—Apparatus therefor
- C05F17/964—Constructional parts, e.g. floors, covers or doors
- C05F17/971—Constructional parts, e.g. floors, covers or doors for feeding or discharging materials to be treated; for feeding or discharging other material
- C05F17/979—Constructional parts, e.g. floors, covers or doors for feeding or discharging materials to be treated; for feeding or discharging other material the other material being gaseous
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/90—Apparatus therefor
- C05F17/989—Flow sheets for biological or biochemical treatment
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- 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
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse
Landscapes
- Chemical & Material Sciences (AREA)
- Molecular Biology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- General Chemical & Material Sciences (AREA)
- Microbiology (AREA)
- Inorganic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
The invention discloses air energy waste harmless treatment and organic fertilizer fermentation equipment integrating and technique, equipment includes body and air energy heat pump；At least provided with one transmitting waste fermentation materials and as the bearer network band in fermentation place in the body；The body is equipped with the feed inlet waste fermentation materials are imported the body and are placed on the bearer network band and the waste material after fermentation to be exported to the discharge port of the body；The body forms circulating air duct to adjust the yeasting of waste fermentation materials on the bearer network band with the air energy heat pump by blast pipe and discharge pipe.Present invention reduces energy consumption, reduce the pollution to environment, shorten fermentation period, improve work efficiency and dehumidifying rate, reduce operating cost, improve the convenience used, simple in structure, processing easy to repair is easy to use, is suitable for large-scale promotion and use.
Description
Technical field
The present invention relates to treatment for cow manure technical field more particularly to a kind of air energy waste harmless treatments and organic fertilizer to send out
Ferment equipment integrating and technique.
Background technology
A large amount of poultry waste is inevitably generated in the evolution of aquaculture.The accumulation of poultry waste not only can
Strong stink is generated, environmental pollution and the waste of resource can be also caused.Therefore the harmless treatment of waste and organic fertilizer are sent out
Ferment is particularly important.The composite bacteria that a kind of high-tech biotechnology of organic fertilizer fermentation strain system is developed, energy fast decoupled have
Machine matter has many advantages, such as that few additive amount, strength protein degradation matter, fermentation time are short, at low cost, fermentation temperature is unrestricted, can have
Effect kills harmful bacteria, worm, worm's ovum, grass-seed and antibiotic residue of degrading etc. in fermentate.Due to high temperature, quick-acting, fermentation
Period is short；Antibacterial evil of going out；Deodorization；It is enriched with nutrient；It is at low cost, effect is good；Improve germination percentage the advantages that, organic fertilizer fermentation technology and
Equipment has obtained quickly promoting the use of.
The hot wind for being passed through a large amount of certain temperatures is needed during current organic fertilizer fermentation.Inventor pays greatly in the field
The creative work of amount has also applied for that Patent No. 201720253669.0, a kind of entitled fowl and animal excrement are harmless before this
Change processing installation for fermenting, including fermentation seat, the fermentation tank being obliquely installed is rotatablely equipped on the fermentation seat, the fermentation seat
Side is provided with the fermentation platform for raising the fermentation tank open end, and the open end of the fermentation tank is equipped with and the fermentation tank
The ventilation device of inner cavity connection, the other end transmission of the fermentation tank are equipped with the rotation driving dress for driving the fermentation tank rotation
It sets, guide spiral is installed on the inner wall of the fermentation tank；Fermentation tank can provide good aerobic fermentation ring for feces of livestock and poultry
Border can accelerate course of fermentation, and the excrement after everfermentation can be as the green fertilizer for promoting crop growth to use, fertilizer efficiency
Significantly, efficiently using for feces of livestock and poultry is realized, excrement discharge is avoided to pollute the environment.
Inventor is in practice, it has been found that certain occasions need to carry out more continuous fermenting and producing, faster more renew
Fermentate, to improve the efficiency of fermentation.Moreover, the heating of hot wind needs to consume a large amount of energy, and the hot wind after use contains
A large amount of moistures, being passed directly into environment cannot be recycled；It can cause largely to pollute in fermentation process；Maintenance process etc. compared with
For complexity.
Therefore, a kind of air energy waste harmless treatment and organic fertilizer fermentation equipment integrating and technique are developed, is not only had
Urgent researching value, it may have good economic benefit and commercial application potentiality, this power that exactly present invention is accomplished
Place and basis.
Invention content
In order to overcome the defect of the prior art as indicated above, the present inventor to have made intensive studies this, paying
After a large amount of creative works, so as to complete the present invention.
Specifically, the technical problem to be solved by the present invention is to：Air energy waste harmless treatment and organic fertilizer are provided
Fermentation equipment integrating and technique are continuously fermented with realizing, shorten fermentation period.
In order to solve the above technical problems, the technical scheme is that：
In a first aspect, the present invention provides air energy waste harmless treatment and organic fertilizer fermentation equipment integrating, including machine
Body and air energy heat pump；
At least provided with one transmitting waste fermentation materials and as the bearer network band in fermentation place in the body；
The body is equipped with the charging waste fermentation materials are imported the body and are placed on the bearer network band
Mouthful and the waste material after fermentation is exported the discharge port of the body；
The body forms circulating air duct to adjust the carrying with the air energy heat pump by blast pipe and discharge pipe
The yeasting of waste fermentation materials on guipure.
As an improvement the equipment integrating further includes the feed inlet upstream position that sequentially arrangement is installed on the body
Biaxial rneader, beater, belt material-feeding machine, and be sequentially arranged in the product skin of the discharge port downstream position of the body
Band conveyer, drum-type screening machine.Wherein, biaxial rneader, beater, belt material-feeding machine, product belt conveyor, drum-type
Screening machine is all made of commercially available traditional equipment.
As an improvement being equipped with and the feed inlet and the matched spreader of bearer network band in the body
Structure.
As an improvement the mechanism of shakeouing includes rotation axis, the rotation axis is rotationally connected on the body, institute
It states and is arranged with two sections of oppositely oriented helical blades in rotation axis.
It will be apparent that shakeout mechanism, the equal be connected by power of bearer network band has driving equipment (such as motor), do not go to live in the household of one's in-laws on getting married herein
It states.
As an improvement being equipped with partition board in the body, the internal body is divided at least two layers heat by the partition board
Wind circulation cavity, hot wind flowing lumen road are matched with the blast pipe and the discharge pipe.
As an improvement material passing passage is formed between the partition board one end and the body far from the blast pipe,
It mutually accepts and sets at least provided with a bearer network band, between the two adjacent bearer network bands in every layer of hot wind flowing lumen road
It sets.
As an improvement being equipped with the two bearer network bands in every layer of hot wind flowing lumen road.
As an improvement being equipped with and the matched baffle of bearer network band in the body.
As an improvement the bottom end of the baffle is connected with sheet, the other end of the sheet and the carrying
Guipure contradicts connection.
As an improvement the discharge port is matched with the bearer network band of least significant end.
As an improvement the feed inlet is connected with feed hopper, the discharge port is connected with reclaiming plate.
Second aspect, the present invention provides air energy waste harmless treatment and organic fertilizer fermentation integrated techniques, using such as
The upper equipment integrating, includes the following steps：
S1, waste is mixed with fermenting microbe, is prepared into waste fermentation materials；
S2, waste fermentation materials are put into from the feed inlet of the equipment integrating to the body, and waste is fermented
Material shakeouts on the bearer network band；
S3, air energy heat pump is opened, 50-70 DEG C of hot wind, the bearer network is passed through into the body by blast pipe
Band ensures residence time of the waste fermentation materials in the body, to realize waste fermentation materials in the bearer network band
Upper completion is fermented, while the hot wind of discharge pipe being dehumidified, reuse；
S4, the discharge port that the waste material after fermentation is exported to the body.
As an improvement in step S1, the waste includes the mixing of feces of livestock and poultry, manioc waste, sawdust, plant ash
Object, weight ratio are preferably 7：2：1.3：0.7.Wherein, the preferred chicken manure of the feces of livestock and poultry or chicken manure content be 45wt% with
On.The sawdust preferably use pine, China fir sawdust, preferred pinus sylvestris var. mongolica, soft leaf China fir sawdust, weight ratio 5：2.
The fermenting microbe includes the mixture of purple nonsulfur bacteria, saccharomycete, bacillus, actinomyces, and weight ratio is 0.5：
1.7：1.3：0.2.
As an improvement the initial water content of the waste fermentation materials is 55-65wt%.
As an improvement being mixed with fermenting microbe to waste using biaxial rneader realization, using beater by waste
Fermentation materials are dispersed as thin pulverized powder.
As an improvement in step S2, using belt material-feeding machine by waste fermentation materials from the equipment integrating into
Material mouth is put into the body, and is shakeout waste fermentation materials on the bearer network band using mechanism is shakeout, the excrement
Thickness of the dirty fermentation materials on the bearer network band is 300-350mm, and most preferably 15-30 DEG C of processing temperature.
As an improvement in step S3, it is preferred to use be equipped with partition board in body, the partition board divides the internal body
Equipment at the two bearer network bands are equipped in two layers of hot wind flowing lumen road and every layer of hot wind flowing lumen road；
The driving motor for first turning on two bearer network bands in the hot wind flowing lumen road of upper layer, waste fermentation materials are contained in
On two bearer network bands, thickness 300-350mm stops two bearer network bands, is passed through 50-70 DEG C of hot wind, continuing fermentation 24-28 is small
When；
It is then turned on the driving motors of two bearer network bands in the hot wind flowing lumen road of upper layer, in lower layer's hot wind flowing lumen road
The driving motor of two bearer network bands, the material of initial fermentation is carried out in the hot wind flowing lumen road of upper layer can fall on lower layer's hot wind flowing lumen
On two bearer network bands in road, meanwhile, continue, to the two bearer networks band feeding in the hot wind flowing lumen road of upper layer, to stop four carryings
Guipure, is continually fed into 50-70 DEG C of hot wind, then continuing fermentation 24-28 hours.
In the present invention, the course of work of air energy heat pump is：15-30 DEG C of external environment air is introduced using air-introduced machine,
It is heated into 50-70 DEG C of hot wind by air compressor (dehumidifying), heat exchanger, is passed through in body by blast pipe using air blower,
So that material is fermented under the quick breeding effect of biological bacteria, and completes drying；The off-air for carrying moisture and fermentation gas passes through
Discharge pipe reenters air energy heat pump, returns again to heat exchanger after air compressor dehumidifies, passes through air inlet after reheating again
Pipe enters in body, and the air after extra cooling is discharged into environment.The energy needed for air energy heat pump comes from contained by surrounding air
Energy.The energy consumption of air energy heat pump is only that the energy of compressor compresses surrounding air (exhaust gas returned after fermenting containing drying materials)
Consumption, if the air energy consumption energy consumption of compressor of 10-30 DEG C of conventional compact is 1KW, the thermal energy generated is 3.5-3.8KW.In environment
Heat pump only needs the hot wind that one stage of compression generates 50-70 DEG C under conditions of 10-30 DEG C.
As an improvement in step S4, the waste material after fermentation is exported into the machine using product belt conveyor
The discharge port of body；And it is 35-45% to control the waste material moisture after fermentation；It opens cylinder round sifter to be sieved, not conform to
Lattice product return again to step S1 processing.
After using above-mentioned technical proposal, the beneficial effects of the invention are as follows：
Body provides place for the fermentation of material, and the air in working environment is introduced and carries out compression by air energy heat pump to be added
Hot wind after heating is passed by blast pipe in body by heat, and the hot wind in body provides suitable ring for the fermentation of material
Border temperature condition, while can accelerate material in order to the drying process of material, the heat that material fermentation generates in the process
Drying process is recovered to air energy heat pump, after being dehumidified containing damp and hot wind after material in body utilizes by discharge pipe
Continue to heat to enter in body and be recycled, it is time saving and energy saving, resource can be made full use of, the loss of resource is reduced
Waste reduces energy consumption, and the use of air energy reduces the pollution to environment, improves dehumidification efficiency, and feed inlet is convenient for object
Material imports in body, and innoxious and fermentation process will be carried out on material transportation to bearer network band, and the setting of bearer network band can be with
Material is carried and is transported, place is provided for the fermentation of material, the fermentation convenient for material is dry and will be after fermentation drying
Material discharges.
Be equipped in body with feed hopper and bearer network band is matched shakeouts mechanism, shakeouing the setting of mechanism can will pass through
The material that feed hopper enters body uniformly shakeouts on bearer network band, is convenient for the fermentation of material, improves material and contacted with hot wind
Area, improve ferment effect and fermentation efficiency.
It includes rotation axis to shakeout mechanism, and rotation axis is rotationally connected on body, and two sections of rotation direction phases are arranged in rotation axis
The rotation of anti-helical blade, rotation axis can drive helical blade to be rotated, after being fallen under material on bearer network band, two
To two end motion of rotation axis under the drive of oppositely oriented helical blade, to make material spread out on bearer network band.
Be equipped with partition board in body, internal body is divided at least two layers of hot wind flowing lumen road by partition board, hot wind flowing lumen road with
Blast pipe and discharge pipe match, and partition board separates blast pipe and discharge pipe in internal body, and hot wind is passed through from blast pipe
It after in body under the separation of partition board, is moved on along hot wind flowing lumen road, the run trace of hot wind can be increased, convenient for heat
Abundant flowing of the wind in body, improves the space availability ratio of material fermentation in body, and the setting in hot wind flowing lumen road makes heat
Wind is passed through from blast pipe in body, and body is left by discharge pipe after the flowing of hot wind flowing lumen road.
Partition board forms material passing passage between one end and body far from blast pipe, every layer of hot wind flowing lumen road is at least provided with one
Bearer network band mutually accepts setting between two adjacent bearer network bands, and the setting of material passing passage can be in order to the conveying of material, together
When pass through convenient for the walking of hot wind, the setting of bearer network band is matched with the walking passageway of hot wind, convenient for the fermentation of material and dry
Dry process, bearer network band mutually accept setting, and in adjacent two bearer networks band, the bearer network band of lower layer is along upper layer bearer network band
The direction of motion extends a segment length so that the bearer network band progress that material can fall on lower layer under the bearer network band on upper layer is defeated
It send.
Be equipped with two bearer network bands in every layer of hot wind flowing lumen road, bearer network band is equipped with four layers altogether, when in use, material from
Feed hopper can be transmitted to the 4th layer of bearer network band from first layer bearer network band successively after entering body, take full advantage of in body
Space, improve hot wind in the working efficiency of machine body-internal-circulation, ensure that working effect.
Be equipped in body with the matched baffle of bearer network band, the setting of baffle can stop material, prevent object
Material the situations such as falls in fermentation process and transmission process, while can be guided to hot wind so that hot wind is according to design
Path circulated, reduce thermal loss, improve work efficiency.
The bottom end of baffle is connected with sheet, and the other end of sheet is contradicted with bearer network band to be connected, and sheet is due to certainly
The physical characteristic of body can damage of the reduction to bearer network band when carrying out barrier effect to material, while baffle can be increased
Seal improves barrier effect of the baffle to hot wind.
Discharge port is matched with the bearer network band of least significant end, and the setting of discharge port can be in order to going out in material slave body
Material, improves the convenience used.
Feed inlet is connected with feed hopper, and discharge port is connected with reclaiming plate, and the setting of feed hopper, can be with convenient for the feeding of material
Play the role of accepting buffering to the conveying of material, reduces the loss that falls of material, the setting of reclaiming plate can be in material fermentation
Ensure the seal of body in the process.
Further include sequentially connected double-shaft mixing agitator and belt material-feeding machine, the discharge end of belt material-feeding machine with it is described into
Hopper matches, the reclaiming plate successively be equipped with belt conveyor and screening machine, the screening machine be equipped with collection material mouth, with it is described
The material return mechanism of double-shaft mixing agitator connection, the materials such as animal wastes and manioc waste, sawdust pass through double-shaft mixing agitator
Feeding is carried out by belt material-feeding machine after stirring evenly, internal body is entered by feed hopper and carries out fermentation drying, after fermentation
Material passes through reclaiming plate, is transported in screening machine and is sieved by belt conveyor, sieves qualified material and gathers materials, enters
Subsequent processing sieves underproof material and returns in double-shaft mixing agitator be mixed by material return mechanism and continues work
Make.
Body be equipped with shakeout the matched actuating unit of mechanism and with the matched transmission mechanism of bearer network band, power
Mechanism provides power to shakeout the operation of mechanism, and transmission mechanism provides power for the operation of bearer network band.
Technique provided by the invention has selected suitable fermentation materials, fermenting microbe and technique ginseng for specific equipment
Number, the step of carrying out primary fermentation in particular by two layers of hot wind flowing lumen road, sequence and ferment again so that material is replaced
Comparatively fast, it can be realized without shutting down, ensure that the sustainability of fermentation, shorten the period of fermentation, improve the efficiency of fermentation；
Meanwhile also being dried while fermentation, further shorten whole production procedure.
In conclusion present invention reduces energy consumption, reduces the pollution to environment, shorten fermentation period, improve work
Make efficiency and dehumidifying rate, reduce operating cost, improves the convenience used, simple in structure, processing easy to repair, user
Just, it is suitable for large-scale promotion and use.
Description of the drawings
Fig. 1 is the structural schematic diagram of embodiment one；
Fig. 2 is the structural schematic diagram of embodiment two；
Fig. 3 is the structural schematic diagram of embodiment three；
In figure：1, body, 2, air energy heat pump, 3, blast pipe, 4, discharge pipe, 5, feed hopper, 6, bearer network band, 7, shakeout
Mechanism, 8, baffle, 9, sheet, 10, reclaiming plate, 11, partition board, 12, feed inlet, 13, discharge port.
Specific implementation mode
With reference to specific embodiment, the present invention is further described.But the purposes and mesh of these exemplary embodiments
Be only used for enumerating the present invention, any type of any restriction not is constituted to the real protection scope of the present invention, it is more non-to incite somebody to action this
The protection domain of invention is confined to this.
Embodiment one
As shown in Figure 1, air energy waste harmless treatment and organic fertilizer fermentation equipment integrating, including body 1 and air energy
Heat pump 2；
One is equipped in body 1 to transmit waste fermentation materials and as the bearer network band 6 in fermentation place；
Body 1 be equipped with to by waste fermentation materials import body 1 and the feed inlet 12 that is placed on bearer network band 6 and
The discharge port 13 of body 1 is exported to the waste material after fermenting；
Body 1 forms circulating air duct by blast pipe 3 and discharge pipe 4 with air energy heat pump 2 and is applied manure to the fields with adjusting bearer network band 6
The yeasting of dirty fermentation materials.
Direction shown in arrow is the direction that hot wind moves in body 1 in Fig. 1.Body 1 provides place for the fermentation of material,
Air in working environment is introduced and is carried out compression heating by air energy heat pump 2, and the hot wind after heating is passed through by blast pipe 3
Into body 1, the hot wind in body 1 provides suitable ambient temperature conditions for the fermentation of material, while can be in order to material
Drying process, the heat that material fermentation generates in the process can accelerate the drying process of material, after material in body 1 utilizes
Be recovered to air energy heat pump 2 by discharge pipe 4 containing damp and hot wind, continue after being dehumidified heating enter body 1 in carry out
It recycles, it is time saving and energy saving, resource can be made full use of, reduces the loss waste of resource, reduces energy consumption, air energy makes
With the pollution reduced to environment, dehumidification efficiency is improved, feed inlet 12 is convenient for importing material in body 1, and material is transported
It is defeated that innoxious and fermentation process is carried out on bearer network band 6, the setting of bearer network band 6 can be carried and be transported to material,
Place is provided for the fermentation of material, the fermentation convenient for material is dry and material of the fermentation after dry discharges.
Air energy heat pump 2 collects surrounding air, and about 15-25 DEG C, 50-70 DEG C is heated to through compressor, condenser, heat exchanger,
Hot wind, which is entered by blast pipe 3 in body 1, makes material ferment under the quick breeding effect of biological bacteria, and completes drying；It carries
The off-air of moisture and fermentation gas reenters air energy heat pump 2 by discharge pipe 4, and heat exchange is returned again to after dehumidifier dehumidifies
Device is entered by air inlet pipe in body 1 again after reheating.
The energy needed for air energy heat pump 2 comes from the energy contained by surrounding air.The energy consumption of air energy heat pump 2 is only that pressure
The energy consumption of contracting machine compression environment air (exhaust gas returned after fermenting containing drying materials), the air energy consumption of 10-30 DEG C of conventional compact
If energy consumption of compressor is 1KW, the thermal energy generated is 3.5-3.8KW.Heat pump only needs level-one pressure under conditions of 10-30 DEG C of environment
Contracting generates 50-70 DEG C of hot wind.
It is equipped in body 1 and feed hopper 5 and bearer network band 6 are matched shakeouts mechanism 7, the setting for shakeouing mechanism 7 can be with
Will by feed hopper 5 enter body 1 material uniformly shakeout on bearer network band 6, be convenient for material fermentation, improve material with
The area of hot wind contact, improves ferment effect and fermentation efficiency.
It includes rotation axis to shakeout mechanism 7, and rotation axis is rotationally connected on body 1, and two sections of rotation directions are arranged in rotation axis
The rotation of opposite helical blade, rotation axis can drive helical blade to be rotated, after being fallen under material on bearer network band 6,
To two end motion of rotation axis under the drive of two oppositely oriented helical blades, to make material spread out on bearer network band 6.
Material can be stopped with 6 matched baffle 8 of bearer network band, the setting of baffle 8 by being equipped in body 1, be prevented
Only situations such as material falling in fermentation process and transmission process, while hot wind can be guided so that hot wind according to
The path of design is circulated, and thermal loss is reduced, and is improved work efficiency, and baffle 8 is from 1 inner wall of body to bearer network
Setting is tilted down with 6 top surface.
Baffle 8 uses PVC plastic plate in the present embodiment.
The bottom end of baffle 8 is connected with sheet 9, and the other end of sheet 9 is contradicted with bearer network band 6 to be connected, sheet 9 by
In the physical characteristic of itself can damage of the reduction to bearer network band 6 when carrying out barrier effect to material, while can increase
The seal of baffle 8 improves barrier effect of the baffle 8 to hot wind.
Discharge port 13 is matched with the bearer network band 6 of least significant end, and the setting of discharge port 13 can be in order to which material be out of body 1
Discharging, improve the convenience used.
Feed inlet 12 is connected with feed hopper 5, and discharge port 13 is connected with reclaiming plate 10, and the setting of feed hopper 5 is convenient for material
Feeding can play the role of the conveying of material to accept buffering, reduce the loss that falls of material, and the setting of reclaiming plate 10 can be with
Ensure the seal of body 1 during material fermentation.
Reclaiming plate 10 is articulated on body 1 in the present embodiment, and reclaiming plate 10 is equipped with and 1 matched sealing of body
Item.
Further include sequentially connected double-shaft mixing agitator and belt material-feeding machine, the discharge end of belt material-feeding machine with it is described into
Hopper 5 matches, the reclaiming plate 10 successively be equipped with belt conveyor and screening machine, the screening machine be equipped with collection material mouth, with
The material return mechanism of the double-shaft mixing agitator connection, the materials such as animal wastes and manioc waste, sawdust are mixed by twin shaft
Feeding is carried out by belt material-feeding machine after the stirring evenly of machine, is entered inside body 1 by feed hopper 5 and carries out fermentation drying, sent out
Material after ferment passes through reclaiming plate 10, is transported in screening machine and is sieved by belt conveyor, sieves qualified material and carries out
Gather materials, into subsequent processing, sieves underproof material by material return mechanism back to being mixed in double-shaft mixing agitator
Stirring works on.
Body 1 be equipped with shakeout 7 matched actuating unit of mechanism and with every matched transmission mechanism of bearer network band,
Actuating unit provides power to shakeout the operation of mechanism 7, and transmission mechanism provides power for the operation of bearer network band.
Bearer network band 6 uses 304 stainless (steel) wire bands, and the both sides of bearer network band 6 are equipped with chain, chain by lubrication oil guard,
The both ends of bearer network band 6 are respectively equipped with drive sprocket and transmission sprocket wheel, transmission sprocket wheel are rotatablely installed by rotation seat in body 1
Rack on, drive sprocket be sequentially connected in the transmission mechanism in rack.
Embodiment two
As shown in Fig. 2, being in place of the present embodiment and the difference of embodiment one：Partition board 11 is equipped in body 1, partition board 11 will
It is divided into two layers of hot wind flowing lumen road inside body 1, hot wind flowing lumen road is matched with blast pipe 3 and discharge pipe 4, and partition board 11 is separate
Form material passing passage between one end and body 1 of blast pipe 3, every layer of hot wind flowing lumen road is equipped with a bearer network band 6, and two adjacent hold
Setting is mutually accepted between contained network band 6.
Direction shown in arrow is the direction that hot wind moves in body 1 in Fig. 2.Partition board 11 is inside body 1 by blast pipe 3
Separate with discharge pipe 4, hot wind from blast pipe 3 be passed through in body 1 after under the separation of partition board 11, along hot wind flowing lumen road
It moves on, the run trace of hot wind can be increased, be convenient for abundant flowing of the hot wind in body 1, improve material hair in body 1
The setting of the space availability ratio of ferment, hot wind flowing lumen road makes hot wind be passed through in body 1 from blast pipe 3, along hot wind flowing lumen road
After flowing body 1 is left by discharge pipe 4.
The setting of material passing passage can be in order to the conveying of material, while passing through convenient for the walking of hot wind, and bearer network band 6 is set
It sets and is matched with the walking passageway of hot wind, the fermentation convenient for material and drying process, bearer network band 6 mutually accept setting, adjacent
In two bearer network bands 6, the bearer network band 6 of lower layer extends a segment length along the direction of motion of upper layer bearer network band 6 so that
The bearer network band 6 that material can fall on lower layer under the bearer network band 6 on upper layer is conveyed.
Embodiment three
As shown in figure 3, being in place of the present embodiment and the difference of embodiment two：It is equipped with two in every layer of hot wind flowing lumen road
Bearer network band 6, bearer network band 6 are equipped with four layers altogether, and direction shown in arrow is the direction that hot wind moves in body 1 in Fig. 3.Make
Used time, material can be transmitted to the 4th layer of bearer network band 6 from first layer bearer network band 6 successively after entering body 1 from feed hopper 5,
The space in body 1 is taken full advantage of, the working efficiency that hot wind recycles in body 1 is improved, ensure that working effect.
When in use, it opens biaxial mixing machine, belt conveyor, shakeout mechanism 7, first layer bearer network band 6 and the second layer
Bearer network band works, and material is entered by feed hopper 5 in body 1 after mixing, and is shakeout in first layer by shakeouing mechanism 7
Feeding is carried out on bearer network band and second layer bearer network band, third layer bearer network band and the 4th layer of bearer network band are opened after 24 hours
Feeding is carried out, reclaiming plate 10 is opened after 48 hours and opens belt conveyor, makes material discharging out of body 1, opens rotary screen
Extension set sieves material, and material stops air energy heat pump 2 after going out completely in all-in-one machine to the greatest extent, accordingly stops other equipment.
Present invention reduces energy consumption, reduce the pollution to environment, improve work efficiency and dehumidifying rate, reduces operation
Cost, because of the structure using air energy and circulating air duct so that the cost for the treatment of for cow manure is extremely low, the handling of poultry waste per ton
With only 20 yuan, comprehensive operating cost efficiently kills pathogenic microorganism for 30 hours or so, removes ovum less than 30 yuan, remove antibiotic and
Other harmful substances decompose macromolecular, are not necessarily to add auxiliary material after equipment operation, treatment in situ avoids the secondary dirt that transport generates
Dye, processing procedure are more closed, and no waste water, exhaust gas and stink exhaust emission, tunning have fragrant, organic matter, N P and K
Contents level is high, and moisture is down to 35% or so, complies fully with environmental impact assessment requirement, improves the convenience used, simple in structure, is convenient for
Maintenance process, it is easy to use, it is suitable for large-scale promotion and use.
Use the points for attention of, maintaining：
Maintaining：A. each power control cabinet associated appliance element, connection circuitry, switch, air energy heat pump, sky are checked before booting
Gas energy waste harmless treatment and organic fertilizer fermentation equipment integrating, batch mixer, charging belt, motor, wind turbine, cycloid speed reducer,
Whether guipure, chain, sprocket wheel etc. are in normal condition.B. lubricant housings (bearing, speed reducer, chain, sprocket wheel etc.) is respectively answered periodically to add
Note lubricating oil.
Troubleshooting：A. turbine being utilized (unclamping bolt, fastened after readjusting) b. temperature control instruments damage (replaces temperature
Degree instrument) to shut down and (analyzed reason by electrician and debugged) d. chain-looses, guipure caused by sideslip de- for c. motor reducers
It falls and (adjusts bearing block tensioning bolt)
Quality of material controls：It checks the just moisture of the material after batch mixing, should be 60%, check that discharging dry product moisture should reach and contain
Water 40%.
It is unqualified in product moisture, it should check hot blast temperature, hot blast rate, doses on material, first moisture, mixing
The uniformity, to be accordingly adjusted.
Overall process must monitor closely.
The conditions for equipment use condition：A. 20 DEG C or so of environment temperature；B. each specification under the conditions of material thickness 350mm
Air energy heat pump, equipment integrating yield be maximum production.
Example IV
The present embodiment includes body, the air energy heat pump that embodiment three provides, and further includes that sequentially arrangement is installed on the machine
Biaxial rneader, beater, the belt material-feeding machine of the feed inlet upstream position of body, and sequentially it is arranged in the discharging of the body
Product belt conveyor, the drum-type screening machine of mouth downstream position.Wherein, biaxial rneader, beater, belt material-feeding machine, production
Product belt conveyor, drum-type screening machine are all made of commercially available traditional equipment (being not shown in figure).
Process example 1
The technique is realized using the equipment as described in example IV, and using following steps：
S1, waste is mixed using biaxial rneader realization with fermenting microbe, is beaten waste fermentation materials using beater
Thin pulverized powder is dissipated into, waste fermentation materials are prepared into, the initial water content of the waste fermentation materials is 55-65wt%,
In, the waste includes the mixture of feces of livestock and poultry, manioc waste, sawdust, plant ash, weight ratio 7：2：1.3：0.7.Its
In, the feces of livestock and poultry is chicken manure.The sawdust is using pine, the sawdust of China fir.The fermenting microbe includes that Purple Non-sulfur is thin
Bacterium, saccharomycete, bacillus, actinomyces mixture, and weight ratio be 0.5：1.7：1.3：0.2；
S2, waste fermentation materials are put into from the feed inlet of the equipment integrating to the body, and waste is fermented
Material shakeouts on the bearer network band, is thrown waste fermentation materials from the feed inlet of the equipment integrating using belt material-feeding machine
Enter to the body, and is shakeout waste fermentation materials on the bearer network band using mechanism is shakeout, the waste fermentation
Thickness of the material on the bearer network band is 300mm, and most preferably 15 DEG C of processing temperature；
S3, the driving motor for first turning on two bearer network bands in the hot wind flowing lumen road of upper layer, waste fermentation materials are contained
Loaded on two bearer network bands, thickness 300mm stops two bearer network bands, is passed through 50 DEG C of hot wind, continuing fermentation 24 hours；
It is then turned on the driving motors of two bearer network bands in the hot wind flowing lumen road of upper layer, in lower layer's hot wind flowing lumen road
The driving motor of two bearer network bands, the material of initial fermentation is carried out in the hot wind flowing lumen road of upper layer can fall on lower layer's hot wind flowing lumen
On two bearer network bands in road, meanwhile, continue, to the two bearer networks band feeding in the hot wind flowing lumen road of upper layer, to stop four carryings
Guipure, is continually fed into 50 DEG C of hot wind, then continuing fermentation 24 hours；
S4, the discharge port that the waste material after fermentation is exported to the body using product belt conveyor；And control hair
Waste material moisture after ferment is 35%；It opens cylinder round sifter to be sieved, qualified product packaging, defective work returns again
Return step S1 processing.
Process example 2
The technique is realized using the equipment as described in example IV, and using following steps：
S1, waste is mixed using biaxial rneader realization with fermenting microbe, is beaten waste fermentation materials using beater
Thin pulverized powder is dissipated into, is prepared into waste fermentation materials, the initial water content of the waste fermentation materials is 65wt%, wherein
The waste includes the mixture of feces of livestock and poultry, manioc waste, sawdust, plant ash, and weight ratio is preferably 7：2：1.3：0.7.Its
In, chicken manure content is 45wt% or more in the feces of livestock and poultry.The sawdust using pinus sylvestris var. mongolica, soft leaf China fir mixing sawdust,
Weight ratio is 5：2.The fermenting microbe includes the mixture of purple nonsulfur bacteria, saccharomycete, bacillus, actinomyces, and again
Amount is than being 0.5： 1.7：1.3：0.2；
S2, waste fermentation materials are put into from the feed inlet of the equipment integrating to the body, and waste is fermented
Material shakeouts on the bearer network band, is thrown waste fermentation materials from the feed inlet of the equipment integrating using belt material-feeding machine
Enter to the body, and is shakeout waste fermentation materials on the bearer network band using mechanism is shakeout, the waste fermentation
Thickness of the material on the bearer network band is 350mm, and most preferably 30 DEG C of processing temperature；
S3, the driving motor for first turning on two bearer network bands in the hot wind flowing lumen road of upper layer, waste fermentation materials are contained
Loaded on two bearer network bands, thickness 350mm stops two bearer network bands, is passed through 70 DEG C of hot wind, continuing fermentation 28 hours；
It is then turned on the driving motors of two bearer network bands in the hot wind flowing lumen road of upper layer, in lower layer's hot wind flowing lumen road
The driving motor of two bearer network bands, the material of initial fermentation is carried out in the hot wind flowing lumen road of upper layer can fall on lower layer's hot wind flowing lumen
On two bearer network bands in road, meanwhile, continue, to the two bearer networks band feeding in the hot wind flowing lumen road of upper layer, to stop four carryings
Guipure, is continually fed into 70 DEG C of hot wind, then continuing fermentation 28 hours；
S4, the discharge port that the waste material after fermentation is exported to the body using product belt conveyor；And control hair
Waste material moisture after ferment is 45%；It opens cylinder round sifter to be sieved, qualified product packaging, defective work returns again
Return step S1 processing.
Process example 3
The technique is realized using the equipment as described in example IV, and using following steps：
S1, waste is mixed using biaxial rneader realization with fermenting microbe, is beaten waste fermentation materials using beater
Thin pulverized powder is dissipated into, is prepared into waste fermentation materials, the initial water content of the waste fermentation materials is 60wt%, wherein
The waste includes the mixture of feces of livestock and poultry, manioc waste, sawdust, plant ash, and weight ratio is preferably 7：2：1.3：0.7.Its
In, the feces of livestock and poultry uses chicken manure.The sawdust is using pinus sylvestris var. mongolica, the mixing sawdust of soft leaf China fir, weight ratio 5：2.Institute
The mixture that fermenting microbe includes purple nonsulfur bacteria, saccharomycete, bacillus, actinomyces is stated, and weight ratio is 0.5：1.7：
1.3：0.2；
S2, waste fermentation materials are put into from the feed inlet of the equipment integrating to the body, and waste is fermented
Material shakeouts on the bearer network band, is thrown waste fermentation materials from the feed inlet of the equipment integrating using belt material-feeding machine
Enter to the body, and is shakeout waste fermentation materials on the bearer network band using mechanism is shakeout, the waste fermentation
Thickness of the material on the bearer network band is 320mm, and most preferably 20 DEG C of processing temperature；
S3, the driving motor for first turning on two bearer network bands in the hot wind flowing lumen road of upper layer, waste fermentation materials are contained
Loaded on two bearer network bands, thickness 320mm stops two bearer network bands, is passed through 60 DEG C of hot wind, continuing fermentation 24 hours；
It is then turned on the driving motors of two bearer network bands in the hot wind flowing lumen road of upper layer, in lower layer's hot wind flowing lumen road
The driving motor of two bearer network bands, the material of initial fermentation is carried out in the hot wind flowing lumen road of upper layer can fall on lower layer's hot wind flowing lumen
On two bearer network bands in road, meanwhile, continue, to the two bearer networks band feeding in the hot wind flowing lumen road of upper layer, to stop four carryings
Guipure, is continually fed into 60 DEG C of hot wind, then continuing fermentation 24 hours；
S4, the discharge port that the waste material after fermentation is exported to the body using product belt conveyor；And control hair
Waste material moisture after ferment is 40%；It opens cylinder round sifter to be sieved, qualified product packaging, defective work returns again
Return step S1 processing.
Process example 4
The technique is realized using the equipment as described in example IV, and using following steps：
S1, waste is mixed using biaxial rneader realization with fermenting microbe, is beaten waste fermentation materials using beater
Thin pulverized powder is dissipated into, is prepared into waste fermentation materials, the initial water content of the waste fermentation materials is 57wt%, wherein
The waste includes the mixture of feces of livestock and poultry, manioc waste, sawdust, plant ash, weight ratio 7：2：1.3：0.7.Wherein, institute
It is 50wt% to state chicken manure content in feces of livestock and poultry.The sawdust is using pinus sylvestris var. mongolica, the sawdust of soft leaf China fir, weight ratio 5：2.Institute
The mixture that fermenting microbe includes purple nonsulfur bacteria, saccharomycete, bacillus, actinomyces is stated, and weight ratio is 0.5：1.7：
1.3：0.2；
S2, waste fermentation materials are put into from the feed inlet of the equipment integrating to the body, and waste is fermented
Material shakeouts on the bearer network band, is thrown waste fermentation materials from the feed inlet of the equipment integrating using belt material-feeding machine
Enter to the body, and is shakeout waste fermentation materials on the bearer network band using mechanism is shakeout, the waste fermentation
Thickness of the material on the bearer network band is 310mm, and most preferably 25 DEG C of processing temperature；
S3, the driving motor for first turning on two bearer network bands in the hot wind flowing lumen road of upper layer, waste fermentation materials are contained
Loaded on two bearer network bands, thickness 310mm stops two bearer network bands, is passed through 65 DEG C of hot wind, continuing fermentation 25 hours；
It is then turned on the driving motors of two bearer network bands in the hot wind flowing lumen road of upper layer, in lower layer's hot wind flowing lumen road
The driving motor of two bearer network bands, the material of initial fermentation is carried out in the hot wind flowing lumen road of upper layer can fall on lower layer's hot wind flowing lumen
On two bearer network bands in road, meanwhile, continue, to the two bearer networks band feeding in the hot wind flowing lumen road of upper layer, to stop four carryings
Guipure, is continually fed into 65 DEG C of hot wind, then continuing fermentation 25 hours；
S4, the discharge port that the waste material after fermentation is exported to the body using product belt conveyor；And control hair
Waste material moisture after ferment is 42%；It opens cylinder round sifter to be sieved, qualified product packaging, defective work returns again
Return step S1 processing.
Process example 5
The technique is realized using the equipment as described in example IV, and using following steps：
S1, waste is mixed using biaxial rneader realization with fermenting microbe, is beaten waste fermentation materials using beater
Thin pulverized powder is dissipated into, is prepared into waste fermentation materials, the initial water content of the waste fermentation materials is 55wt%, wherein
The waste includes the mixture of feces of livestock and poultry, manioc waste, sawdust, plant ash, and weight ratio is preferably 7：2：1.3：0.7.Its
In, the preferred chicken manure of feces of livestock and poultry.The sawdust is preferably using pine, the sawdust of China fir.The fermenting microbe includes purple
Non- sulfur bacteria, saccharomycete, bacillus, actinomyces mixture, and weight ratio be 0.5：1.7：1.3：0.2；
S2, waste fermentation materials are put into from the feed inlet of the equipment integrating to the body, and waste is fermented
Material shakeouts on the bearer network band, is thrown waste fermentation materials from the feed inlet of the equipment integrating using belt material-feeding machine
Enter to the body, and is shakeout waste fermentation materials on the bearer network band using mechanism is shakeout, the waste fermentation
Thickness of the material on the bearer network band is 350mm, and processing temperature is 18 DEG C；
S3, the driving motor for first turning on two bearer network bands in the hot wind flowing lumen road of upper layer, waste fermentation materials are contained
Loaded on two bearer network bands, thickness 350mm stops two bearer network bands, is passed through 50 DEG C of hot wind, continuing fermentation 27 hours；
It is then turned on the driving motors of two bearer network bands in the hot wind flowing lumen road of upper layer, in lower layer's hot wind flowing lumen road
The driving motor of two bearer network bands, the material of initial fermentation is carried out in the hot wind flowing lumen road of upper layer can fall on lower layer's hot wind flowing lumen
On two bearer network bands in road, meanwhile, continue, to the two bearer networks band feeding in the hot wind flowing lumen road of upper layer, to stop four carryings
Guipure, is continually fed into 50 DEG C of hot wind, then continuing fermentation 27 hours；
S4, the discharge port that the waste material after fermentation is exported to the body using product belt conveyor；And control hair
Waste material moisture after ferment is 38%；It opens cylinder round sifter to be sieved, qualified product packaging, defective work returns again
Return step S1 processing.
Comparative example 1
It is fermented using traditional stacking method, is not repeated specifically.
Comparative example 2
It is fermented, is selected using a kind of fowl and animal excrement harmless treatment installation for fermenting of Patent No. 201720253669.0
With the optimization process parameter for being suitble to the device.
The excrement of same quality, weight is handled, as a result such as following table：
| Discharge water content | Handle the deadline | |
| Process example 3 | 40% | 48 hours |
| Comparative example 1 | 71% | 127 hours |
| Comparative example 2 | 62% | 98 hours |
As can be seen from the above table, equipment and technique provided by the invention can shorten the time of processing, improve efficiency, together
When can also realize the drying of material, the water content of finished product is reduced, without being dried again.Inventor also uses process implementing
Example 1,2,4,5 carries out same contrast test, as a result unanimously.
It should be appreciated that the purposes of these embodiments is merely to illustrate the present invention and is not intended to limitation protection model of the invention
It encloses.In addition, it should also be understood that, after reading the technical contents of the present invention, those skilled in the art can make the present invention each
Kind change, modification and/or variation, all these equivalent forms equally fall within and are protected defined by the application the appended claims
Within the scope of shield.
Claims (10)
1. air energy waste harmless treatment and organic fertilizer fermentation equipment integrating, it is characterised in that：Including body and air energy thermal
Pump；
At least provided with one transmitting waste fermentation materials and as the bearer network band in fermentation place in the body；
The body be equipped with to waste fermentation materials are imported into the body and are placed on the bearer network band feed inlet, with
And the waste material after fermentation to be exported to the discharge port of the body；
The body forms circulating air duct to adjust the bearer network band with the air energy heat pump by blast pipe and discharge pipe
The yeasting of upper waste fermentation materials.
2. air energy waste harmless treatment as described in claim 1 and organic fertilizer fermentation equipment integrating, it is characterised in that：Also
Include biaxial rneader, beater, the belt material-feeding machine of the feed inlet upstream position for being installed on the body of sequentially arranging, and
Sequentially it is arranged in product belt conveyor, the drum-type screening machine of the discharge port downstream position of the body.
3. air energy waste harmless treatment as described in claim 1 and organic fertilizer fermentation equipment integrating, it is characterised in that：Institute
It states and is equipped in body and the feed inlet and bearer network band is matched shakeouts mechanism；The mechanism of shakeouing includes rotation
Axis, the rotation axis are rotationally connected on the body, and two sections of oppositely oriented helical blades are arranged in the rotation axis.
4. air energy waste harmless treatment as described in claim 1 and organic fertilizer fermentation equipment integrating, it is characterised in that：Institute
It states and is equipped with partition board in body, the internal body is divided at least two layers of hot wind flowing lumen road, the hot wind circulation by the partition board
Cavity is matched with the blast pipe and the discharge pipe；Between the partition board one end and the body far from the blast pipe
Form material passing passage, every layer of hot wind flowing lumen road at least provided with a bearer network band, the two adjacent bearer network bands it
Between mutually accept setting.
5. air energy waste harmless treatment as described in claim 1 and organic fertilizer fermentation equipment integrating, it is characterised in that：Institute
It states in body and is equipped with and the matched baffle of bearer network band；The bottom end of the baffle is connected with sheet, the sheet
The other end and the bearer network band contradict and connect.
6. air energy waste harmless treatment as described in claim 1 and organic fertilizer fermentation equipment integrating, it is characterised in that：Institute
Discharge port is stated to match with the bearer network band of least significant end；The feed inlet is connected with feed hopper, and the discharge port is connected with
Reclaiming plate.
7. air energy waste harmless treatment and organic fertilizer fermentation integrated technique, it is characterised in that：Appointed using such as claim 1-6
Equipment described in one, includes the following steps：
S1, waste is mixed with fermenting microbe, is prepared into waste fermentation materials；
S2, waste fermentation materials are put into from the feed inlet of the equipment integrating to the body, and by waste fermentation materials
It shakeouts on the bearer network band；
S3, air energy heat pump is opened, 50-70 DEG C of hot wind is passed through into the body by blast pipe, the bearer network band is true
Residence time of the waste fermentation materials in the body is protected, to realize that waste fermentation materials are complete on the bearer network band
At fermentation, while the hot wind of discharge pipe being dehumidified, reuse；
S4, the discharge port that the waste material after fermentation is exported to the body.
8. air energy waste harmless treatment as claimed in claim 7 and organic fertilizer fermentation integrated technique, it is characterised in that：Step
In rapid S1, the initial water content of the waste fermentation materials is 55-65wt%.
9. air energy waste harmless treatment as claimed in claim 7 and organic fertilizer fermentation integrated technique, it is characterised in that：Step
In rapid S2, waste fermentation materials are put into from the feed inlet of the equipment integrating to the body using belt material-feeding machine, and
Waste fermentation materials are shakeout on the bearer network band using mechanism is shakeout, the waste fermentation materials are in the bearer network band
On thickness be 300-350mm, and most preferably 15-30 DEG C of processing temperature.
10. air energy waste harmless treatment as claimed in claim 7 and organic fertilizer fermentation integrated technique, it is characterised in that：
In step S3, it is preferred to use be equipped with partition board in body, the partition board by the internal body be divided into two layers of hot wind flowing lumen road and
The equipment that the two bearer network bands are equipped in every layer of hot wind flowing lumen road；
Waste fermentation materials are contained in two and held by the driving motor for first turning on two bearer network bands in the hot wind flowing lumen road of upper layer
On contained network band, thickness 300-350mm stops two bearer network bands, is passed through 50-70 DEG C of hot wind, continuing fermentation 24-28 hours；
Two in the driving motors of two bearer network bands being then turned in the hot wind flowing lumen road of upper layer, lower layer's hot wind flowing lumen road hold
The driving motor of contained network band, the material of initial fermentation is carried out in the hot wind flowing lumen road of upper layer can fall in lower layer's hot wind flowing lumen road
Two bearer network bands on, meanwhile, continue in the hot wind flowing lumen road of upper layer two bearer networks band feeding, stop four bearer networks
Band, is continually fed into 50-70 DEG C of hot wind, then continuing fermentation 24-28 hours.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810446814.6A CN108329080A (en) | 2018-05-11 | 2018-05-11 | Air energy waste harmless treatment and organic fertilizer fermentation equipment integrating and technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810446814.6A CN108329080A (en) | 2018-05-11 | 2018-05-11 | Air energy waste harmless treatment and organic fertilizer fermentation equipment integrating and technique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108329080A true CN108329080A (en) | 2018-07-27 |
Family
ID=62935034
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810446814.6A Pending CN108329080A (en) | 2018-05-11 | 2018-05-11 | Air energy waste harmless treatment and organic fertilizer fermentation equipment integrating and technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108329080A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111943733A (en) * | 2020-08-25 | 2020-11-17 | 孙芳芳 | Equipment and method for preparing organic fertilizer by microbial fermentation of livestock and poultry manure |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101148309A (en) * | 2007-09-03 | 2008-03-26 | 张锦华 | Belt-type sludge drier |
| CN204128317U (en) * | 2014-10-23 | 2015-01-28 | 富源县益鸿农产品开发有限公司 | A kind of novel band slice food made from Amorphophallus rivieri drying device |
| CN204251519U (en) * | 2014-09-26 | 2015-04-08 | 大连晟农生态科技有限公司 | organic waste harmless processor |
| CN106220250A (en) * | 2016-09-27 | 2016-12-14 | 湖南绿捷环境科技有限公司 | A kind of method and system of excrement dirt quick fermentation production fertilizer |
| CN206709569U (en) * | 2017-04-24 | 2017-12-05 | 河南南洋环保机械有限公司 | Slurry electrical heating mesh belt type dryer |
| CN107647450A (en) * | 2017-10-25 | 2018-02-02 | 宁夏发途发蔬菜产业集团有限公司 | Multilayer chain combined type continuous drying system |
-
2018
- 2018-05-11 CN CN201810446814.6A patent/CN108329080A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101148309A (en) * | 2007-09-03 | 2008-03-26 | 张锦华 | Belt-type sludge drier |
| CN204251519U (en) * | 2014-09-26 | 2015-04-08 | 大连晟农生态科技有限公司 | organic waste harmless processor |
| CN204128317U (en) * | 2014-10-23 | 2015-01-28 | 富源县益鸿农产品开发有限公司 | A kind of novel band slice food made from Amorphophallus rivieri drying device |
| CN106220250A (en) * | 2016-09-27 | 2016-12-14 | 湖南绿捷环境科技有限公司 | A kind of method and system of excrement dirt quick fermentation production fertilizer |
| CN206709569U (en) * | 2017-04-24 | 2017-12-05 | 河南南洋环保机械有限公司 | Slurry electrical heating mesh belt type dryer |
| CN107647450A (en) * | 2017-10-25 | 2018-02-02 | 宁夏发途发蔬菜产业集团有限公司 | Multilayer chain combined type continuous drying system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111943733A (en) * | 2020-08-25 | 2020-11-17 | 孙芳芳 | Equipment and method for preparing organic fertilizer by microbial fermentation of livestock and poultry manure |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108033813A (en) | A kind of production technology and production equipment of feces of livestock and poultry rapid production of organic fertilizer | |
| CN216245414U (en) | Biomass fuel raw material drying device | |
| CN208791511U (en) | Air energy waste harmless treatment and organic fertilizer fermentation integrated equipment | |
| CN109809848A (en) | A kind of stalk and livestock and poultry feces fermentation are wrapped up in and pack fertile device and method | |
| CN2894872Y (en) | Food-beverage rubbish treating equipment | |
| CN108083872A (en) | Automate fermentation of organic wastes system | |
| CN111454084A (en) | Distributed rapid degradation integrated device and process for kitchen waste | |
| CN108329080A (en) | Air energy waste harmless treatment and organic fertilizer fermentation equipment integrating and technique | |
| CN207688597U (en) | A kind of biomass fertilizers drying unit | |
| CN1064595A (en) | Manure of livestock and poultry producing protein feed making method and equipment thereof | |
| KR100964081B1 (en) | Fermentation device for fish feed | |
| WO2021134526A1 (en) | Organic waste biological fermentation reaction device and organic fertilizer production line | |
| KR101634977B1 (en) | Fuel-axes systems | |
| CN115650781B (en) | Device and process for treating perishable garbage by biological drying and decomposition promotion | |
| CN107298594B (en) | Aerobic fermentation device for kitchen garbage | |
| KR101853206B1 (en) | high speed mixing fermentor and moisture and harmful gas removal method using it | |
| CN206408134U (en) | A kind of agricultural discharging device of microbial organic fertilizer fermenting tower | |
| CN110467486A (en) | A kind of automation integrated composting device | |
| CN110608598A (en) | Corn ear grain linkage drying production line | |
| CN203661652U (en) | High-efficiency drying/threshing/cleaning system for producing corn seeds | |
| CN114249611B (en) | Small-molecule organic protein fertilizer and preparation method thereof | |
| CN207119619U (en) | A kind of biogas residue regeneration application system | |
| CN212102621U (en) | Vertical composting device | |
| KR101212757B1 (en) | Method for producing closed anaerobic livestock manure | |
| CN212833364U (en) | Sludge aerobic fermentation equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180727 |