CN107827481A - A kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device - Google Patents
A kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device Download PDFInfo
- Publication number
- CN107827481A CN107827481A CN201711310391.7A CN201711310391A CN107827481A CN 107827481 A CN107827481 A CN 107827481A CN 201711310391 A CN201711310391 A CN 201711310391A CN 107827481 A CN107827481 A CN 107827481A
- Authority
- CN
- China
- Prior art keywords
- fermentation
- bolt connection
- pipeline
- drying device
- livestock
- 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
- 238000000855 fermentation Methods 0.000 title claims abstract description 123
- 230000004151 fermentation Effects 0.000 title claims abstract description 122
- 238000001035 drying Methods 0.000 title claims abstract description 41
- 244000144977 poultry Species 0.000 title claims abstract description 28
- 244000144972 livestock Species 0.000 title claims abstract description 27
- 239000003895 organic fertilizer Substances 0.000 title claims abstract description 25
- 210000003608 fece Anatomy 0.000 title claims abstract description 23
- 230000001172 regenerating effect Effects 0.000 title claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 60
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 46
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 46
- 239000001301 oxygen Substances 0.000 claims abstract description 46
- 238000003860 storage Methods 0.000 claims abstract description 23
- 238000007599 discharging Methods 0.000 claims abstract description 19
- 229910001220 stainless steel Inorganic materials 0.000 claims abstract description 18
- 239000010935 stainless steel Substances 0.000 claims abstract description 17
- 238000009434 installation Methods 0.000 claims abstract description 11
- 238000007539 photo-oxidation reaction Methods 0.000 claims abstract description 11
- 230000001877 deodorizing effect Effects 0.000 claims abstract description 8
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 7
- 239000010959 steel Substances 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 238000005119 centrifugation Methods 0.000 claims description 14
- 239000000428 dust Substances 0.000 claims description 12
- 125000004122 cyclic group Chemical group 0.000 claims description 9
- 230000008878 coupling Effects 0.000 claims description 8
- 238000010168 coupling process Methods 0.000 claims description 8
- 238000005859 coupling reaction Methods 0.000 claims description 8
- 239000000446 fuel Substances 0.000 claims description 8
- 238000009413 insulation Methods 0.000 claims description 8
- 238000012856 packing Methods 0.000 claims description 7
- 238000010276 construction Methods 0.000 claims description 6
- 239000000498 cooling water Substances 0.000 claims description 6
- 239000000945 filler Substances 0.000 claims description 5
- 230000005540 biological transmission Effects 0.000 claims description 4
- 238000013519 translation Methods 0.000 claims description 4
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 3
- 241000486406 Trachea Species 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 239000010425 asbestos Substances 0.000 claims description 3
- 210000004907 gland Anatomy 0.000 claims description 3
- 229910052895 riebeckite Inorganic materials 0.000 claims description 3
- 210000003437 trachea Anatomy 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 2
- 239000003638 chemical reducing agent Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 description 22
- 239000010410 layer Substances 0.000 description 15
- 230000008569 process Effects 0.000 description 12
- 238000012545 processing Methods 0.000 description 9
- 238000005265 energy consumption Methods 0.000 description 8
- 238000013461 design Methods 0.000 description 7
- 244000005700 microbiome Species 0.000 description 7
- 102000004190 Enzymes Human genes 0.000 description 6
- 108090000790 Enzymes Proteins 0.000 description 6
- 230000007613 environmental effect Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 238000004332 deodorization Methods 0.000 description 4
- 239000011229 interlayer Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000002028 Biomass Substances 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 241001465754 Metazoa Species 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 230000001276 controlling effect Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 238000006213 oxygenation reaction Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 210000002700 urine Anatomy 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000010828 animal waste Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 235000013601 eggs Nutrition 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000002550 fecal effect Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 235000021049 nutrient content Nutrition 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000036316 preload Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F3/00—Fertilisers from human or animal excrements, e.g. manure
- C05F3/06—Apparatus for the manufacture
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/75—Multi-step processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/77—Liquid phase processes
- B01D53/78—Liquid phase processes with gas-liquid contact
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
-
- 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
Abstract
The invention discloses a kind of fermentation of livestock and poultry feces regenerating organic fertilizer and drying device, including installation for fermenting and drying device, installation for fermenting includes Zymolysis Equipment, temperature control system, expose oxygen system and exhaust treatment system, Zymolysis Equipment upper end is provided with feeding flood dragon, the other end of feeding flood dragon is provided with excrement dirt material storage container, the right-hand member bolt connection of Zymolysis Equipment has electronic stainless steel butterfly valve, bolt connection has discharging pipeline in the electronic stainless steel butterfly valve, the right-hand member of discharging pipeline is provided with material storage container after fermentation, Zymolysis Equipment includes bed frame, temperature control system includes fermentation boiler, exhaust treatment system includes air blower, photooxidation deodorizing device and washout tower, exposing oxygen system includes air compressor, Zymolysis Equipment also includes stair, stair are bolted to bed frame and steel platform, drying device includes base support and burning boiler.Service life of the present invention is long, energy-conserving and environment-protective, and automaticity is high, reduces cost of labor.
Description
Technical field
The present invention relates to installation for fermenting technical field, specifically a kind of livestock and poultry feces regenerating organic fertilizer fermentation and dry dress
Put.
Background technology
In recent years, China's animal husbandry sustainable and stable development, large-scale cultivation level significantly improve, and have ensured meat, eggs and milk confession
Give, but a large amount of breeding wastes are not effectively addressed and utilized, and turn into a great problem of Countryside Environment Rectification.It is estimated that
National annual 3800000000 tons of livestock and poultry feces of generation, comprehensive utilization ratio is less than 60%.Livestock and poultry feces are unprocessed or deal with improperly, arbitrarily
Place or discharge, not only waste of resource but also seriously pollute environment.Do a good job of it animal waste recycling, relation livestock products
Product effective supply, relation urban residents' production and living enhancement of environment, it is great people's livelihood engineering.
Domestic poultry excrement and urine disposal state-of-the-art
China's poultry excrement and urine disposal mode has a variety of, natural pile fermentation method:Fermentation time is long, it is necessary to which a large amount of soils disappear nearby
Receive, do not conform to suitable for intensive livestock and poultry farms.Dryness in the sun method:Floor space is big, and environmental pollution is serious, and product is relatively inaccessible to
Innoxious requirement.It is suitable for livestock and poultry decentralized household, is not suitable for intensive livestock and poultry farms.Direct flash baking method:Energy consumption is higher,
Drying tail gas easily causes secondary environmental pollution.When feces of livestock and poultry moisture content height or on the high ground of coal resources shortage, environmental requirement
Area, its usability are restricted.Biogas anaerobic fermentation method:Suitable for processing intensive livestock and poultry farms using flush-type (or bubble
Formula) cleaning up excrement technique liquid Animal fecal pollution.Disposable input is big, and middle-size and small-size scale raising is restricted.A generation is horizontal or vertical
Formula reactor composting process:Floor space is small, shortens fermentation period to 3-7 days;But this kind of processing mode can only select electrical heating
Mode, handles high energy consumption, and equipment can not accomplish hermetically sealed, need to add the mixing of a large amount of auxiliary materials with material leak-proof, and processing procedure
In have and arrange outside foul smell, it is impossible to accomplish complete environmental protection;And be difficult to be again started up if having a power failure in vertical reactor running,
In the presence of it is very big the drawbacks of.
Conventional process mode Problems Existing:
1st, auxiliary material addition is big
There is region limitation, increase operating cost, reduce treatment for cow manure efficiency in the unit interval, adjunct ingredient is with cellulose, wood
Based on quality etc., decomposed period extends, and nutrient content is low in auxiliary material, reduces the quality of organic fertilizer.
2nd, running environmental protection is not up to standard
It can not accomplish to be fully sealed, processing procedure tail gas easily causes secondary environmental pollution.
3rd, decomposed period is grown
Single type fermenting agent, fermentation maturity cycle length are not added or only added to conventional process mode.
4th, energy consumption cost is high
To ensure effective fermentation temperature in tank body, traditional approach can only select Electric heating, equipment operation energy because of equipment limitation
It is high to consume cost.
And also need to be dried after fermenting, to reach organic fertilizer moisture requirement, beneficial to the long-term storage of fertilizer.This
Device, which is particularly suitable for use in, does not add the material samples after the fermentation maturity that any auxiliary material is carried out is handled, and can largely improve
The production efficiency of organic fertilizer.
Conventional process mode Problems Existing:Conventional process mode is typically handled by natural drying or low temperature drying,
Natural drying mode has peculiar smell generation, can not accomplish green, environmental protection, low temperature drying mode process cycle is longer.
The content of the invention
It is an object of the invention to provide a kind of fermentation of livestock and poultry feces regenerating organic fertilizer and drying device, to solve the above-mentioned back of the body
The problem of being proposed in scape technology.
To achieve the above object, the present invention provides following technical scheme:
A kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device, including installation for fermenting and drying device, the installation for fermenting
Ground is placed in including Zymolysis Equipment, temperature control system, exposure oxygen system and exhaust treatment system, the Zymolysis Equipment, Zymolysis Equipment
Upper end is provided with feeding flood dragon, and the other end of the feeding flood dragon is provided with excrement dirt material storage container, and the excrement dirt material storage container is half ground
Following formula is built, and the right-hand member bolt connection of Zymolysis Equipment has an electronic stainless steel butterfly valve, bolt connection in the electronic stainless steel butterfly valve
There is discharging pipeline, the right-hand member for the pipeline that discharges is provided with material storage container after fermentation, and Zymolysis Equipment includes bed frame, the bed frame
End bolt connects threephase asynchronous machine, and the threephase asynchronous machine output shaft is provided with driving pulley, and the driving pulley leads to
V belt translation connection driven pulley is crossed, the driven pulley is connected by key connection with reductor input shaft, the deceleration machine bolt
Connect base frame, speed reducer output shaft are connected by shaft coupling with spindle nose, and the main shaft passes through double-row conical axle
Hold and be connected with bearing block, the bearing block bottom bolts connect base frame, and bearing block side bolt connecting ball head flange, institute
Bolt connection bearing door on the outside of bearing block is stated, the bearing door side is provided with fuel filler neck, and bearing rib outer side of lid is installed
There is a bearing baffle ring, stop washer and round nut are installed on the main shaft on the outside of the bearing baffle ring;The bulb flange bolt
Connection fermentation cylinder, bulb flange side is provided with pressure ring, asbestos is filled between the pressure ring, main shaft, bulb flange, described
Ferment cylinder bolt connection bed frame, is provided with rotating vane in the middle part of the main shaft, the rotating vane bolt connection is paired
It is installed on main shaft, the end of rotating blade bolt connection rotating vane scraper plate, the rotating vane scraper plate end bolt
Connection rubber flap, the main shaft other end bolt connection bearing gland, the fermentation cylinder body bottom bolt connection outlet pipeline,
The temperature control system includes fermentation boiler, ferments and states the delivery port bolt connection pipeline A of boiler, the pipeline A bolt connections
Flanged ball valve A, the flanged ball valve A bolt connection pipelines B, the pipeline B bolt connection Piping Centrifugal Pumps, the pipeline centrifugation
Pump bolt connection pipeline C, the pipeline C bolted flange check-valves, the flange check valve bolt connection fermentation cylinder
Cyclic water channel water inlet;Water inlet bolt connection pipeline D, the pipeline D bolted flanges ball valve B of the fermentation boiler,
The flanged ball valve B bolt connection pipelines E, the pipeline E bolt connections are fermented cylinder cyclic water channel delivery port, at the tail gas
Reason system includes air blower, and the air blower is bolted to fermentation cylinder, and ferment cylinder top gas outlet bolt connection tail gas
Pipeline B, tail gas pipeline B are bolted to photooxidation deodorizing device, and the photooxidation deodorizing device bolt connection tail gas pipeline A is described
Tail gas pipeline A bolt connection washout towers, exposing oxygen system includes air compressor, and the air compressor is connected to by PU tracheaes
Quick connector on the A of oxygen exposure tube road, the oxygen exposure tube road A are bolted to oxygen exposure tube road C, and oxygen exposure tube road C is bolted to hair
Oxygen exposure tube road B on ferment cylinder, magnetic valve is provided with the A of oxygen exposure tube road;The Zymolysis Equipment also includes stair, the stair
Bed frame and steel platform are bolted to, the steel platform is bolted to fermentation cylinder and support bar, the support bar
Fermentation cylinder is bolted to, chain-wales are installed, chain-wales include chain-wales A and chain-wales B, described small flat above fermentation cylinder
Platform A and chain-wales B are bolted to fermentation cylinder;
The drying device includes base support and burning boiler, symmetrical on the base support to be provided with the first roller
With the second roller, baking barrel body, the outside of the baking barrel body are provided with by the first roller and the second roller on base support
Middle part is provided with trundle, gear is engaged with the trundle, the gear is connected with reductor by connecting shaft, described to subtract
Fast machine is connected by shaft coupling with threephase asynchronous, baking barrel body be internally provided with moving tooth and centrifugation main shaft, it is described from
Heart main shaft is hollow structure, and centrifuge main shaft is internally provided with cooling water circulation passage, the centrifugation main shaft by driven pulley with
Driving wheel is connected with motor, is provided with material storage container feeding auger after the fermentation on material storage container, and the material storage container feeding twists
The other end of dragon is provided with feeding packing auger, and the feeding packing auger is connected with baking barrel body, the burning boiler and baking barrel body
Right-hand member connects, and is provided with staving blast pipe on baking barrel body, blast pipe is connected with the staving blast pipe, the blast pipe
The other end is provided with cyclone dust collectors, is provided with dedusting blast pipe on the cyclone dust collectors, the dedusting blast pipe it is another
End connection air-introduced machine, the air-introduced machine connect washout tower, are provided with washout tower blast pipe in the washout tower, under baking barrel body
Side right-hand member is provided with discharging opening, and discharging is provided with below the discharging opening and places pond, the discharging is placed and is provided with transmission on pond
Band.
As the further scheme of the present invention:The bulb flange is stainless steel 304 material.
As the further scheme of the present invention:The fermentation cylinder is double-decker, and internal layer is 6 millimeters thick stainless steel 304s,
Outer layer is 6 millimeters thick carbon steel Q235, and the cyclic water channel that gusset separates is designed between two layers.
As the further scheme of the present invention:Temperature of charge meter and water temperature meter are provided with the fermentation cylinder.
As the further scheme of the present invention:The fermenter volume surrounding sets insulation construction, and outer layer insulation construction uses
Alumina silicate needle punched blanket.
As the further scheme of the present invention:Stirrer paddle is set in the fermenter body.
As the further scheme of the present invention:The fermentation staving all-sealed structure is set.
As the further scheme of the present invention:Observation panel is provided with the fermentation staving.
As the further scheme of the present invention:The Zymolysis Equipment, temperature control system, exposure oxygen system and exhaust treatment system are equal
Using micro computer control.
As the further scheme of the present invention:The threephase asynchronous, motor and air-introduced machine use switch board control
System.
As further scheme of the invention:The centrifugation main shaft is hollow structure, centrifuges being internally provided with for main shaft
Cooling water circulation passage.
Compared with prior art, the beneficial effects of the invention are as follows:This covering device can be that microorganism preferably sends out with biology enzyme
The effect of waving provides suitable temperature and oxygen-supplying amount, realizes aerobic Rapid Fermentation;Fermentation can body in this covering device uses casing
Bucket, interlayer water/oily heating mode, and staving outermost layer is equipped with heat-insulation layer.This design can ensure that the material in staving is quick
The optimum temperature of microorganism and biology enzyme is warming up to, and the preference temperature can be maintained in whole fermentation process, reduces energy
Consumption;Fermentation can body internal layer staving in this covering device uses stainless steel, can reduce in excrement dirt fermentation process to equipment
Corrosion condition, while extension device service life, it ensure that the quality of organic fertilizer;Fermentation can body in this covering device is matched somebody with somebody
Apparatus of oxygen supply and oxygen exposure tube road are had, can be that microorganism and biology enzyme preferably play a role and provide suitable oxygen-supplying amount, realize
Aerobic Rapid Fermentation;Fermentation can body in this covering device is equipped with photooxidation odor removal and oxidation water spray system, to fermentation
During caused tail gas and dust carry out two stage treatment, make tail gas qualified discharge;This suit is set to total closed type processing, this kind
On the one hand design can ensure the possibility of high moisture material fermentation, be not in material leakage phenomenon, on the other hand can ensure excrement
Dirty green processing digest process, environmental protection, safety, non-secondary pollution thing produce;Thermal source supply all uses needed for this covering device
Biomass fuel or gas fuel, reduce energy consumption cost and the energy source tail-gas is safer to environment;The operation of this covering device uses
Microcomputer control system, real-time monitoring system running situation and reduction human cost input.By drying unit of the present invention, use
In feces of livestock and poultry harmless treatment, it is decomposed after change into the drying and processing of organic fertilizer raw material, the system can be with automatic feed, automatically
Drying, self-emptying, mitigate labor strength, realize that nobody automatically controls completely, improves production efficiency, makes automation journey
Du Genggao.And the system running is green, operation tail gas can qualified discharge.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention.
Fig. 2 is Fig. 1 top view.
Fig. 3 is the structural representation of Zymolysis Equipment.
Fig. 4 is Fig. 3 top view.
Fig. 5 is the partial enlarged drawing at X in Fig. 3.
Fig. 6 is the partial enlarged drawing at Y in Fig. 3.
Fig. 7 is the structural representation of temperature control system.
Fig. 8 is Fig. 7 side view.
Fig. 9 is Fig. 7 top view.
Figure 10 is the partial enlarged drawing at X in Fig. 8.
Partial enlarged drawing in Figure 11 bitmaps 9 at Y.
Partial enlarged drawing in Figure 12 bitmaps 9 at Z.
Figure 13 is the structural representation for exposing oxygen system and exhaust treatment system.
Figure 14 is Figure 13 side view.
Figure 15 is Figure 13 top view.
Figure 16 is the cut-away view of the drying system of drying device;
Figure 17 is assembling graph structure figure outside drying device.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, those of ordinary skill in the art are obtained every other under the premise of creative work is not made
Embodiment, belong to the scope of protection of the invention.
Refer to Fig. 1~17, in the embodiment of the present invention, a kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device, bag
Installation for fermenting and drying device are included, the installation for fermenting includes Zymolysis Equipment 1, temperature control system, aerating system and vent gas treatment system
System, the Zymolysis Equipment 1 are placed in ground, and the upper end of Zymolysis Equipment is provided with feeding flood dragon 2, the other end of the feeding flood dragon 2
It is provided with excrement dirt material storage container 3, the excrement dirt material storage container 3 is semi-underground type building, and the right-hand member bolt connection of Zymolysis Equipment 1 has electronic
Stainless steel butterfly valve 4, bolt connection has discharging pipeline 5 in the electronic stainless steel butterfly valve 4, and the right-hand member of discharging pipeline 5 is provided with hair
Material storage container 6 after ferment, Zymolysis Equipment 1 include bed frame 7, and the end bolt of bed frame 7 connects threephase asynchronous machine 8, institute
State the output shaft of threephase asynchronous machine 8 and driving pulley 9 is installed, the driving pulley 9 connects driven pulley 10, institute by V belt translation
State driven pulley 10 by key connection with the input shaft of reductor 11 to be connected, the bolt connection bed frame 1 of reductor 11, slow down
The output shaft of machine 11 is connected by shaft coupling 29 with the end of main shaft 12, and the main shaft 12 passes through double-row conical bearing 13 and bearing
Seat 14 is connected, the bottom bolts connect base frame 7 of bearing block 14, and the side bolt connecting ball head flange 15 of bearing block 14,
The outside bolt connection bearing door 16 of bearing block 14, the side of bearing door 16 is provided with fuel filler neck 17, and bearing rib
The outside of lid 16 is provided with bearing baffle ring 18, and stop washer 19 and circle spiral shell are provided with the main shaft 12 in the outside of bearing baffle ring 18
Mother 20;The bolt connection of bulb flange 15 is fermented cylinder 22, and the side of bulb flange 15 is provided with pressure ring 21, the pressure ring 21,
Asbestos 28, the fermentation bolt connection bed frame 1 of cylinder 22, the main shaft 12 are filled between main shaft 12, bulb flange 15
Middle part is provided with rotating vane 23, and the bolt connection mounted in pairs of rotating vane 23 is on main shaft 12, the rotating vane
23 end bolts connection rotating vane scraper plate 24, the end bolt of rotating vane scraper plate 24 connects rubber flap 25, the master
The other end bolt connection bearing gland 26 of axle 12, the fermentation cylinder 22 bottom bolts connection outlet pipeline 27, the temperature control system
System includes the boiler 30 that ferments, and ferments and states the delivery port bolt connection pipeline A31 of boiler 30, the pipeline A31 bolted-on connections
Blue ball valve A32, the flanged ball valve A32 bolt connection pipelines B33, the pipeline B33 bolt connections Piping Centrifugal Pumps 34 are described
The bolt connection pipeline C35 of Piping Centrifugal Pumps 34, the pipeline C35 bolted flanges check-valves 36, the flange check valve 36
The cyclic water channel water inlet of bolt connection fermentation cylinder 22;The water inlet bolt connection pipeline D37 of the fermentation boiler 30, it is described
Pipeline D37 bolted flange ball valves B38, the flanged ball valve B38 bolt connection pipelines E39, the pipeline E39 bolt connections
Ferment the cyclic water channel delivery port of cylinder 22, and the exhaust treatment system includes air blower 52, and the air blower 52 is bolted to
Ferment cylinder 22, and fermentation cylinder 22 top gas outlet bolt connection tail gas pipeline B57, tail gas pipeline B57 are bolted to photooxidation
Deodorizing device 58, the bolt connection tail gas pipeline A47 of photooxidation deodorizing device 58, the tail gas pipeline A47 bolt connections water leaching
Tower 48, exposing oxygen system includes air compressor 53, and the air compressor 53 is connected on the A44 of oxygen exposure tube road by PU tracheaes 56
Quick connector 55, the oxygen exposure tube road A44 is bolted to oxygen exposure tube road C51, and oxygen exposure tube road C51 is bolted to fermentation cylinder
Oxygen exposure tube road B49 on body 22, magnetic valve 54 is provided with the A44 of oxygen exposure tube road;The Zymolysis Equipment 1 also includes stair 42,
The stair 42 are bolted to bed frame 7 and steel platform 43, the steel platform 43 be bolted to fermentation cylinder 22 and
Support bar 50, the support bar 50 are bolted to fermentation cylinder 22, the top installation chain-wales of fermentation cylinder 22, and chain-wales include
Chain-wales A45 and chain-wales B46, the chain-wales A45 and chain-wales B46 are bolted to fermentation cylinder 22.
Drying device includes base support 70 and burning boiler 61, symmetrical setting on the base support 70
There are the first roller 68 and the second roller 69, baking barrel body is provided with by the first roller 68 and the second roller 69 on base support 70
84, the outer middle side part of the baking barrel body 84 is provided with trundle 71, and gear 72, the gear are engaged with the trundle 71
72 are connected with reductor 74 by connecting shaft 73, and the reductor 74 is connected by shaft coupling 85 with threephase asynchronous 75,
Baking barrel body 84 is internally provided with moving tooth 66 and centrifugation main shaft 65, and the centrifugation main shaft 65 passes through driven pulley 87 and driving wheel 86
Motor 67 is connected with, material drying is broken up, prevents from luming;And material is made again by the rotation of baking barrel body 84
Form irregular graininess;Material storage container feeding auger 63 is installed, the material storage container feeding twists after the fermentation on material storage container 6
Dragon 63 the other end be provided with feeding packing auger 64, the feeding packing auger 64 is connected with baking barrel body 84, the burning boiler 61 and
The right-hand member connection of baking barrel body 84, the choosing multiple fuel of burning boiler 61 are supplied as thermal source:Coal, biomass, energy oil, day
Right gas etc..Heat is provided to baking barrel body 84, the humidity of the materials inside of baking barrel body 84 is changed into gas evaporation, baking barrel body
Staving blast pipe 78 is provided with 84, blast pipe 83, the other end of the blast pipe 83 are connected with the staving blast pipe 78
Be provided with cyclone dust collectors 77, be provided with dedusting blast pipe 81 on the cyclone dust collectors 77, the dedusting blast pipe 81 it is another
One end connects air-introduced machine 80, and the air-introduced machine 80 connects washout tower 79, washout tower blast pipe 82 is provided with the washout tower 79,
Washout tower 79 sets blower unit, and traction hot blast is migrated from discharging opening to charging aperture, and hot gas and tail gas are discharged by charging aperture;And enter
Material mouth high humidity, dust content in discharge tail gas can be reduced;Such design makes heat utilization ratio height.Exhaust emissions is set to reach state
Family's standard, vapour content is 99.9% in emission, and the downside right-hand member of baking barrel body 84 is provided with discharging opening 88, it is described go out
The lower section of material mouth 88 is provided with discharging and places pond 76, and the discharging is placed and is provided with transmission belt 60 on pond 76.
The centrifugation main shaft 65 is hollow structure, and centrifugation main shaft 65 is internally provided with cooling water circulation passage 89.To keep away
Exempt from long-time hot environment and run damage to dispersing device, centrifugation main shaft 65 uses hollow structure, in equipment running process in
Hollow structure persistent loop cooling water, ensure the good running status of equipment.
The bulb flange 15 is stainless steel 304 material.
The fermentation cylinder 22 is double-decker, and internal layer is 6 millimeters thick stainless steel 304s, and outer layer is 6 millimeters thick carbon steels
Q235, the cyclic water channel that gusset separates is designed between two layers.
Temperature of charge meter 40 and water temperature meter 41 are provided with the fermentation cylinder 22.
Fermentation staving 22 all-sealed structure is set.
Observation panel is provided with the fermentation staving 22.The Zymolysis Equipment 1, temperature control system, expose at oxygen system and tail gas
Reason system uses micro computer control.
Fermentation process:Fig. 1-Fig. 3 is referred to, reaching 15-18 in the excrement dirt that feeding flood dragon 2 is delivered in Zymolysis Equipment 1 stands
Zymolysis Equipment starts and starts to ferment during square rice, drives driving pulley 9, and driving pulley 9 drives driven pulley 10 by V belt translation, from
Movable belt pulley 10 drives the input shaft of reductor 11, and then the output shaft of reductor 11 drives shaft coupling 29, and shaft coupling 29 drives main shaft 12
Rotate, main shaft 12 drives rotating vane 23 to be rotated, by the rotating vane scraper plate 24 on rotating vane 23 and
Rubber flap 25 is stirred to the excrement dirt in Zymolysis Equipment 1, is carried out always in whole fermentation process stirring action;It is different three
Temperature control system, exposure oxygen system, exhaust treatment system start simultaneously while step motor 8 starts, and treat that temperature of charge reaches setting temperature
When spending, fermenting agent is added by being arranged on three observation panels above Zymolysis Equipment.
The working method of temperature control system:The excrement dirt in being fermented to the inside of fermentation cylinder 22 is needed to protect during the fermentation
Temperature, control system by be arranged on fermentation cylinder 22 on temperature of charge meter 40 and water temperature meter 41 know temperature of charge and
Recirculated water water temperature, when temperature of charge is less than setting value and recirculated water water temperature is more than setting value, control system starts fermentation boiler
30, fermentation boiler 30 heats its internal heat recirculated water, then starts Piping Centrifugal Pumps 34 and recirculated water is circulated, recirculated water leads to
Cross circulation line to bring heat inside fermentation cylinder 22 into, when temperature of charge reaches setting value, Piping Centrifugal Pumps 34 is closed, hair
Ferment boiler 30 is flame-out.Outlet pipeline is installed in fermentation cylinder 22 bottom, effect is for a long time when not in use will fermentation in equipment
Recirculated water in the cyclic water channel of cylinder 22 is released, and prevents that recirculated water freezes when temperature is low.
Expose the working method of oxygen system:Need to provide aerobic environment for fermentative microorganism during the fermentation, it is phase asynchronous
When motor 8 starts, air compressor 53 starts, and compressed air is stored in the air accumulator of air compressor 53, in air accumulator
Interior pressure starts the magnetic valve 13 being arranged on oxygen exposure tube road when reaching setting value, and compressed air enters under the effect of the pressure
Among oxygen exposure tube road, material bottom is then entered by the oxygen exposure tube road B inside the cylinder 22 that ferments, then mixed under gas pressure
In material and material liquid surface is floated up to, fermentation materials are supplied oxygen in this process, exposes oxygen in whole fermentation process
Systems stay is run.
The working method of exhaust treatment system:Can produce foul smell in fermentation process, exhaust treatment system to foul smell at
Reason, the air blower 52 above fermentation cylinder 22 start, gas ullage and exposure oxygen system being filled with inside material
Body is blown out, and gas enters photooxidation deodorizing device 58 by tail gas pipeline B49 and carries out deodorization, is then entered by tail gas pipeline A47
Washout tower 48, secondary deodorization is carried out by aoxidizing water circulation spray in washout tower 48.The vent gas treatment in whole fermentation process
Systems stay is run.
Control system opens electronic stainless steel butterfly valve 4 after the fermentation has been completed, and material is entered by the pipeline that discharges after fermentation
Material storage container 6 after fermentation, fermentation process are completed.
Bearing block assembles:Bearing block rotation-fixed manner twin fixed guide-vane, one is integrally fixed above bed frame, second, fixed
On cylinder flange bulb, fixed effect is more preferable, and precision is higher.Bearing uses double-row conical bearing, double row tapered roller
Sub- bearing can bear heavy load, and rigidity is strong.They are adapted to bear compound(Radial direction and axial direction)Load, can axle in both direction
To positioning, with certain end-play or certain preload.
The staving that ferments is hermetically sealed:Heating pipe is set to carry out material heating using casing bucket, twin-tub interlayer;Internal layer staving is adopted
With 30408 stainless steels, prevent slant acidity and the high excrement of salt content is for the corrosiveness of equipment, ensure the use of equipment
Life-span;Hermetically sealed design ensure that the secondary dirt such as feasibility, no material leakage, waste liquid directly fermented to the fresh excrement of high moisture content
Thing is contaminated to produce.
Fermenter volume surrounding sets insulation construction:Using alumina silicate needle punched blanket as outer layer insulation construction, high insulating effect,
And high temperature resistant;The design reduces the loss of heat, reduces equipment operation energy consumption.
Stirrer paddle is set in fermenter body:It ensure that fermentation materials fully mix, fully contacted with supply oxygen.
Expose oxygen system:Expose oxygen system and be equipped with an air compressor, equipment air inlet pipe is connected by magnetic valve, air inlet pipe is led to
Cross eight pipes and enter Zymolysis Equipment, the material in fermentation tank is exposed oxygen completely, and then material is reached after fermenting 20 hours
Completely decomposed degree.
Observation panel:Three observation panels are set above staving, monitor material fermentation situation at any time.
Temperature monitoring:In fermentation materials and fermentation tank interlayer, temperature sensor, the temperature that thermal module will detect are set
Degree signal compares with predetermined temperature higher limit with lower limit, and by controlling opening for boiler fan and substance feeds
Stop, the temperature of fermentation materials is maintained in the upper offline temperature of setting.
Vent gas treatment:Tail gas, dust etc. caused by heat supplying process use photooxidation deodoration system and 200mm filler oxygenation water
Spray equipment(Washout tower)Deodorization.
Whole micro computer control:There are multiple interlocking and restriction relation in the wiring of component and the programming of program, each control
Circuit processed is provided with multiple protective electric elements, can be protected in time when equipment runs into overload, phase shortage or maloperation in operation
And can automatic alarm, while in touch-screen set alarm the page can show guilty culprit position, to prompt operating personnel
Find and fix a breakdown rapidly with attendant.
This covering device can be that microorganism and biology enzyme preferably play a role and provide suitable temperature and oxygen-supplying amount, realize
Oxygen Rapid Fermentation;Fermentation can body in this covering device is using casing bucket, interlayer water/oily heating mode, and staving outermost layer is matched somebody with somebody
Have heat-insulation layer.This design can ensure the optimum temperature that the material in staving is rapidly heated to microorganism and biology enzyme,
And the preference temperature can be maintained in whole fermentation process, reduce energy consumption;Fermentation can body internal layer staving in this covering device is adopted
With stainless steel, it can reduce in excrement dirt fermentation process to the corrosion condition of equipment, while extension device service life, protect
The quality of organic fertilizer is demonstrate,proved;Fermentation can body in this covering device equipped with apparatus of oxygen supply and oxygen exposure tube road, can be microorganism with
Biology enzyme, which preferably plays a role, provides suitable oxygen-supplying amount, realizes aerobic Rapid Fermentation;Fermentation can body in this covering device
Equipped with photooxidation odor removal and oxidation water spray system, two stage treatment is carried out to caused tail gas in fermentation process and dust,
Make tail gas qualified discharge;This suit is set to total closed type processing, on the one hand this kind design can ensure high moisture material fermentation
Possibility, be not in material leakage phenomenon, on the other hand can ensure the dirty green processing digest process of excrement, environmental protection, safety, nothing two
Secondary pollutant produces;Thermal source supply needed for this covering device all using biomass fuel or gas fuel, reduction energy consumption cost,
And the energy source tail-gas is safer to environment;This covering device, which is run, uses microcomputer control system, real-time monitoring system running situation,
And reduce human cost input.
The threephase asynchronous 75, motor 67 and air-introduced machine 80 are controlled using switch board.
Dryer uses " self-aligning riding wheel apparatus ", the cooperation of support roller and rolling ring is linearly contacted forever, so as to significantly
Reduce abrasion and kinetic equation loss.
It is real by regulating and controlling to operational factors such as material charging rate, the rotating speed of baking barrel body, heat source response device temperature
Reveal controllableization of material humidity.
Dedusting deodoration system:Coagulation is carried out to dust caused by drying course by cyclone dust collectors first, then
Deodorization two stage treatment is carried out to tail gas caused by drying course by 400mm filler oxygenation water spray systems.
Drying device when in use, when expect on the material storage container feeding auger 63 feeding packing auger 64 make material enter drying
Staving 84, burning boiler 61 starts conveying heat while material enters baking barrel body 84, while centrifuges main shaft 65 and connect motor 9
After startup operating makes the rotation of centrifugation main shaft 65 baking barrel body 84 is rotated through certain time with the startup of threephase asynchronous 75
Discharging opening 88 is discharged, and organic fertilizer is transported to specified location by the transmission belt 60 in the placement pond 76 that discharges, and improves production
Efficiency, whole process realize Automated condtrol by the switch board.
It is obvious to a person skilled in the art that the invention is not restricted to the details of above-mentioned one exemplary embodiment, Er Qie
In the case of without departing substantially from spirit or essential attributes of the invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, embodiment all should be regarded as exemplary, and be nonrestrictive, the scope of the present invention is by appended power
Profit requires rather than described above limits, it is intended that all in the implication and scope of the equivalency of claim by falling
Change is included in the present invention.Any reference in claim should not be considered as to the involved claim of limitation.
Moreover, it will be appreciated that although the present specification is described in terms of embodiments, not each embodiment is only wrapped
Containing an independent technical scheme, this narrating mode of specification is only that those skilled in the art should for clarity
Using specification as an entirety, the technical solutions in the various embodiments may also be suitably combined, forms those skilled in the art
It is appreciated that other embodiment.
Claims (11)
1. a kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device, including installation for fermenting and drying device, it is characterised in that
The installation for fermenting includes Zymolysis Equipment, temperature control system, exposure oxygen system and exhaust treatment system, the Zymolysis Equipment and is placed in ground
Face, the upper end of Zymolysis Equipment are provided with feeding flood dragon, and the other end of the feeding flood dragon is provided with excrement dirt material storage container, and the excrement is dirty
Material storage container is built for semi-underground type, and the right-hand member bolt connection of Zymolysis Equipment has electronic stainless steel butterfly valve, the electronic stainless steel butterfly
Bolt connection has discharging pipeline on valve, and the right-hand member for the pipeline that discharges is provided with material storage container after fermentation, and Zymolysis Equipment includes bed frame,
The bed frame end bolt connects threephase asynchronous machine, and the threephase asynchronous machine output shaft is provided with driving pulley, institute
State driving pulley and driven pulley is connected by V belt translation, the driven pulley is connected by key connection with reductor input shaft, institute
Reductor bolt connection bed frame is stated, speed reducer output shaft is connected by shaft coupling with spindle nose, and the main shaft passes through double
Row tapered roller bearing is connected with bearing block, the bearing block bottom bolts connect base frame, and bearing block side bolt connects
Receive head flange, bolt connection bearing door on the outside of the bearing block, the bearing door side is provided with fuel filler neck, and bearing
Bearing baffle ring is installed on the outside of door, stop washer and round nut are installed on the main shaft on the outside of the bearing baffle ring;It is described
Bulb flange bolt connection fermentation cylinder, bulb flange side is provided with pressure ring, filled out between the pressure ring, main shaft, bulb flange
Filled with asbestos, the fermentation cylinder bolt connection bed frame, the main shaft middle part is provided with rotating vane, the rotating vane
Bolt connection mounted in pairs is on main shaft, the end of rotating blade bolt connection rotating vane scraper plate, the rotating vane
Scraper plate end bolt connects rubber flap, the main shaft other end bolt connection bearing gland, the fermentation cylinder body bottom bolt
Outlet pipeline is connected, the temperature control system includes fermentation boiler, ferments and states the delivery port bolt connection pipeline A of boiler, described
Pipeline A bolted flange ball valves A, the flanged ball valve A bolt connection pipelines B, the pipeline B bolt connections pipeline centrifugation
Pump, the Piping Centrifugal Pumps bolt connection pipeline C, the pipeline C bolted flange check-valves, the flange check valve bolt
The cyclic water channel water inlet of connection fermentation cylinder;The water inlet bolt connection pipeline D of the fermentation boiler, the pipeline D bolts
Adpting flange ball valve B, the flanged ball valve B bolt connection pipelines E, the pipeline E bolt connections fermentation cylinder recirculated water are said
The mouth of a river, the exhaust treatment system include air blower, and the air blower is bolted to fermentation cylinder, fermentation cylinder top outlet
Mouth bolt connection tail gas pipeline B, tail gas pipeline B are bolted to photooxidation deodorizing device, the photooxidation deodorizing device bolt connection
Tail gas pipeline A, the tail gas pipeline A bolt connection washout towers, exposing oxygen system includes air compressor, and the air compressor leads to
The quick connector that PU tracheaes are connected on the A of oxygen exposure tube road is crossed, the oxygen exposure tube road A is bolted to oxygen exposure tube road C, oxygen exposure tube road
C is bolted to the oxygen exposure tube road B on fermentation cylinder, and magnetic valve is provided with the A of oxygen exposure tube road;The Zymolysis Equipment also includes
Stair, the stair are bolted to bed frame and steel platform, and the steel platform is bolted to fermentation cylinder and support
Bar, the support bar are bolted to fermentation cylinder, installation chain-wales above fermentation cylinder, chain-wales include chain-wales A with it is small
Platform B, the chain-wales A and chain-wales B are bolted to fermentation cylinder;
The drying device includes base support and burning boiler, symmetrical on the base support to be provided with the first roller
With the second roller, baking barrel body, the outside of the baking barrel body are provided with by the first roller and the second roller on base support
Middle part is provided with trundle, gear is engaged with the trundle, the gear is connected with reductor by connecting shaft, described to subtract
Fast machine is connected by shaft coupling with threephase asynchronous, baking barrel body be internally provided with moving tooth and centrifugation main shaft, it is described from
Heart main shaft is hollow structure, and centrifuge main shaft is internally provided with cooling water circulation passage, the centrifugation main shaft by driven pulley with
Driving wheel is connected with motor, is provided with material storage container feeding auger after the fermentation on material storage container, and the material storage container feeding twists
The other end of dragon is provided with feeding packing auger, and the feeding packing auger is connected with baking barrel body, the burning boiler and baking barrel body
Right-hand member connects, and is provided with staving blast pipe on baking barrel body, blast pipe is connected with the staving blast pipe, the blast pipe
The other end is provided with cyclone dust collectors, is provided with dedusting blast pipe on the cyclone dust collectors, the dedusting blast pipe it is another
End connection air-introduced machine, the air-introduced machine connect washout tower, are provided with washout tower blast pipe in the washout tower, under baking barrel body
Side right-hand member is provided with discharging opening, and discharging is provided with below the discharging opening and places pond, the discharging is placed and is provided with transmission on pond
Band.
2. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that described
Bulb flange is stainless steel 304 material.
3. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that described
Fermentation cylinder is double-decker, and internal layer is 6 millimeters thick stainless steel 304s, and outer layer is 6 millimeters thick carbon steel Q235, is designed between two layers
There is the cyclic water channel that gusset separates.
4. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that described
Temperature of charge meter and water temperature meter are provided with fermentation cylinder.
5. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that described
Fermenter volume surrounding sets insulation construction, and outer layer insulation construction uses alumina silicate needle punched blanket.
6. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that described
Stirrer paddle is set in fermenter body.
7. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that described
The staving all-sealed structure that ferments is set.
8. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that described
Observation panel is provided with fermentation staving.
9. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that described
Zymolysis Equipment, temperature control system, exposure oxygen system and exhaust treatment system use micro computer control.
10. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that institute
Threephase asynchronous, motor and air-introduced machine is stated to control using switch board.
11. a kind of livestock and poultry feces regenerating organic fertilizer fermentation according to claim 1 and drying device, it is characterised in that institute
It is hollow structure to state centrifugation main shaft, and centrifuge main shaft is internally provided with cooling water circulation passage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711310391.7A CN107827481A (en) | 2017-12-11 | 2017-12-11 | A kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201711310391.7A CN107827481A (en) | 2017-12-11 | 2017-12-11 | A kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107827481A true CN107827481A (en) | 2018-03-23 |
Family
ID=61642747
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201711310391.7A Pending CN107827481A (en) | 2017-12-11 | 2017-12-11 | A kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107827481A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108424178A (en) * | 2018-06-01 | 2018-08-21 | 方高健 | A kind of livestock and poultry feces fermentation heap extensive use of chemical fertilizer equipment |
CN108716293A (en) * | 2018-05-17 | 2018-10-30 | 华中科技大学 | It is a kind of that the intelligent lavatory glowed is mixed based on rural area human and animal excreta and biomass |
CN110508062A (en) * | 2019-09-02 | 2019-11-29 | 江西永发科技有限公司 | Integrated livestock and poultry excrement, urine, biogas slurry treatment system |
CN112673897A (en) * | 2020-12-09 | 2021-04-20 | 福建省荣佳菇业有限公司 | High-recycling preparation equipment and method for agaricus bisporus nutrient |
CN114671717A (en) * | 2022-04-20 | 2022-06-28 | 李玉社 | Fermenting installation is used in bio-organic fertilizer production |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102506567A (en) * | 2011-11-18 | 2012-06-20 | 山东天力干燥股份有限公司 | Double-scattering structure-type rotary cylinder dryer with shaft cooling |
CN102757270A (en) * | 2011-04-26 | 2012-10-31 | 汪深 | Horizontally-arranged cylinder rolling type aerobic fermentation apparatus with heat exchange function |
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 |
CN106673398A (en) * | 2017-03-15 | 2017-05-17 | 临朐中谷生物科技有限公司 | Harmless treatment production equipment for animal dung |
CN106882981A (en) * | 2017-04-18 | 2017-06-23 | 刘军林 | A kind of aquaculture excrement is dirty to concentrate method for innocent treatment |
CN206310860U (en) * | 2016-12-16 | 2017-07-07 | 杭州年丰有机肥有限公司 | Drying unit |
CN207632712U (en) * | 2017-12-11 | 2018-07-20 | 山东菏泽三仪生物工程有限公司 | A kind of fermentation of livestock and poultry feces regenerating organic fertilizer and drying device |
-
2017
- 2017-12-11 CN CN201711310391.7A patent/CN107827481A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102757270A (en) * | 2011-04-26 | 2012-10-31 | 汪深 | Horizontally-arranged cylinder rolling type aerobic fermentation apparatus with heat exchange function |
CN102506567A (en) * | 2011-11-18 | 2012-06-20 | 山东天力干燥股份有限公司 | Double-scattering structure-type rotary cylinder dryer with shaft cooling |
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 |
CN206310860U (en) * | 2016-12-16 | 2017-07-07 | 杭州年丰有机肥有限公司 | Drying unit |
CN106673398A (en) * | 2017-03-15 | 2017-05-17 | 临朐中谷生物科技有限公司 | Harmless treatment production equipment for animal dung |
CN106882981A (en) * | 2017-04-18 | 2017-06-23 | 刘军林 | A kind of aquaculture excrement is dirty to concentrate method for innocent treatment |
CN207632712U (en) * | 2017-12-11 | 2018-07-20 | 山东菏泽三仪生物工程有限公司 | A kind of fermentation of livestock and poultry feces regenerating organic fertilizer and drying device |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108716293A (en) * | 2018-05-17 | 2018-10-30 | 华中科技大学 | It is a kind of that the intelligent lavatory glowed is mixed based on rural area human and animal excreta and biomass |
CN108424178A (en) * | 2018-06-01 | 2018-08-21 | 方高健 | A kind of livestock and poultry feces fermentation heap extensive use of chemical fertilizer equipment |
CN110508062A (en) * | 2019-09-02 | 2019-11-29 | 江西永发科技有限公司 | Integrated livestock and poultry excrement, urine, biogas slurry treatment system |
CN112673897A (en) * | 2020-12-09 | 2021-04-20 | 福建省荣佳菇业有限公司 | High-recycling preparation equipment and method for agaricus bisporus nutrient |
CN114671717A (en) * | 2022-04-20 | 2022-06-28 | 李玉社 | Fermenting installation is used in bio-organic fertilizer production |
CN114671717B (en) * | 2022-04-20 | 2024-01-09 | 陕西肥沃田地生态农牧有限公司 | Fermenting installation is used in bio-organic fertilizer production |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107827481A (en) | A kind of livestock and poultry feces regenerating organic fertilizer fermentation and drying device | |
CN106119105B (en) | A kind of solid high-temperature aerobic fermentation reaction system and method | |
CN102617204B (en) | Aerobic fermentation reaction system and method | |
CN203999292U (en) | A kind of device of intelligent high-temperature aerobic fermentation sludge treatment | |
CN202558745U (en) | High efficiency intelligent aerobic fermentation reaction system | |
CN204265656U (en) | Intelligence high-temperature environmental-protection composting all-in-one | |
CN206046638U (en) | A kind of Large-scale pig farm breeding pollution comprehensive treatment system | |
CN214327587U (en) | Kitchen waste aerobic composting equipment | |
CN206736115U (en) | A kind of pin-connected panel fowl and animal excrement installation for fermenting | |
CN210001795U (en) | Oxygenating device and fermentation equipment thereof | |
CN106892687A (en) | A kind of discarded object installation for fermenting based on hot pipe technique | |
CN205347262U (en) | Integrated form OAR processing apparatus | |
CN111362738B (en) | High-efficient drum-type aerobic composting reaction device who returns muddy | |
KR20060054264A (en) | The process assembly and operation of the multi-staged vertical composter for the recycling of food wastes | |
CN106399079A (en) | Dry type anaerobic system | |
CN207483633U (en) | A kind of livestock and poultry feces regenerating organic fertilizer installation for fermenting | |
CN103641538B (en) | A kind of Hydrothermal roller high temperature compost reactor | |
CN207632712U (en) | A kind of fermentation of livestock and poultry feces regenerating organic fertilizer and drying device | |
CN212425907U (en) | Tower fermentation equipment of fertilizer | |
CN206127311U (en) | Solid high -ternperature aerobic zymolysis reaction system | |
CN112410174A (en) | Laminar flow fermentation device and fermentation method thereof | |
CN202519253U (en) | Circulating water system for aerobic fermentation reaction | |
CN107651991A (en) | A kind of livestock and poultry feces regenerating organic fertilizer installation for fermenting | |
CN111729922A (en) | Kitchen waste treatment system | |
CN206799637U (en) | A kind of multifunctional integrated solid-state fermentation installation |
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: 20180323 |