CN205974299U - Banana bio -feritlizer fermentation system - Google Patents
Banana bio -feritlizer fermentation system Download PDFInfo
- Publication number
- CN205974299U CN205974299U CN201620826843.1U CN201620826843U CN205974299U CN 205974299 U CN205974299 U CN 205974299U CN 201620826843 U CN201620826843 U CN 201620826843U CN 205974299 U CN205974299 U CN 205974299U
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- China
- Prior art keywords
- fermentation
- tank
- bio
- feritlizer
- stirring
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- 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.)
- Expired - Fee Related
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- 238000000855 fermentation Methods 0.000 title claims abstract description 72
- 230000004151 fermentation Effects 0.000 title claims abstract description 72
- 235000018290 Musa x paradisiaca Nutrition 0.000 title abstract 2
- 241000234295 Musa Species 0.000 title 1
- 238000010438 heat treatment Methods 0.000 claims abstract description 18
- 238000003756 stirring Methods 0.000 claims abstract description 18
- 239000000463 material Substances 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims description 16
- 238000002156 mixing Methods 0.000 claims description 16
- 230000008569 process Effects 0.000 claims description 16
- 239000011229 interlayer Substances 0.000 claims description 11
- 238000007789 sealing Methods 0.000 claims description 3
- 239000003638 chemical reducing agent Substances 0.000 claims description 2
- 230000005611 electricity Effects 0.000 claims 1
- 239000003337 fertilizer Substances 0.000 abstract description 9
- 239000002994 raw material Substances 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 244000005700 microbiome Species 0.000 abstract description 5
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 abstract description 4
- 231100000572 poisoning Toxicity 0.000 abstract description 4
- 230000000607 poisoning effect Effects 0.000 abstract description 4
- 238000001035 drying Methods 0.000 abstract description 3
- 238000009423 ventilation Methods 0.000 abstract description 3
- 241000894006 Bacteria Species 0.000 abstract description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract 2
- 230000001580 bacterial effect Effects 0.000 abstract 2
- 240000005561 Musa balbisiana Species 0.000 abstract 1
- 230000009849 deactivation Effects 0.000 abstract 1
- 230000002349 favourable effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- 229910052742 iron Inorganic materials 0.000 abstract 1
- 239000002689 soil Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 230000000844 anti-bacterial effect Effects 0.000 description 3
- 239000003895 organic fertilizer Substances 0.000 description 3
- 235000018291 probiotics Nutrition 0.000 description 3
- FGRBYDKOBBBPOI-UHFFFAOYSA-N 10,10-dioxo-2-[4-(N-phenylanilino)phenyl]thioxanthen-9-one Chemical compound O=C1c2ccccc2S(=O)(=O)c2ccc(cc12)-c1ccc(cc1)N(c1ccccc1)c1ccccc1 FGRBYDKOBBBPOI-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000009335 monocropping Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007850 degeneration Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000008635 plant growth Effects 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 230000031068 symbiosis, encompassing mutualism through parasitism Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- Fertilizers (AREA)
Abstract
The utility model provides a banana bio -feritlizer fermentation system, mix unit and fermentation unit including raw material handling unit, batching. Adopt steam drum right at the raw material handling unit the treatment tank is sterilized, exterminates the bacterium in the raw materials completely, avoids the murder by poisoning to the microorganism for fermentation finished product steady quality, the quality is higher. Setting up the many blast pipes of being connected and extending to fermented inner chamber bottom with the air pump in the fermentation cylinder of fermentation unit, having guaranteed the interior good ventilation of intracavity of fermentation, be favorable to the bacterial to survive, the while can help moisture content upwards to volatilize fast to passing through gases stir the fermentation that rolls, make it reach abundant fermentation, prevent that the iron rust that the mixer produced from making the bacterial deactivation. The layer with thermal clip is established to the fermentation cylinder, heating and drying, and fermentation, stirring and stoving step combine, and the fermented stirring stoving of fertilizer material has been realized to a machine, and stirring is thorough, and it is even to dry, and the production efficiency height is easy and simple to handle, saves the usage space.
Description
Technical field
This utility model is related to a kind of fermentation system, especially relates to a kind of Fructus Musae bio-feritlizer fermentation system.
Background technology
Biological organic fertilizer nutrient is complete, can improved soil, improve the soil compaction that causes using chemical fertilizer, improve soil
Earth physicochemical character, strengthens soil water-retaining, fertilizer conservation, the ability of fertilizer.Beneficial microbe in biological organic fertilizer enter after soil with
Soil Microorganism forms mutual symbiosis Relationship With Proliferation, and the harmful bacteria growing of suppression is simultaneously converted into probioticss, interacts, phase
Mutually promote, play the synergism of colony, probioticss produce substantial amounts of metabolite during growth and breeding, promote Organic substance
Decomposition and inversion, directly or indirectly can provide multiple nutrition and pungent for crop, promote and regulation and control plant growth, improve
Soil porosity, penetrating commutativity and plant survival rate, increase probioticss and soil microorganism and population.Meanwhile, in root of the crop
The advantage profitable strain that system is formed can suppress harmful pathogen procreation, strengthen the degeneration-resistant resistances against diseases of crop, reduce continuous cropping crop
Disease index, apply year after year and can significantly alleviate continuous cropping obstacle, reduce environmental pollution, to people, animal, Environmental security, nontoxic, be one
Plant environment-friendly type fertilizer.
At present, produce in the fermentation system of bio-feritlizer and equipment to accelerate fermenting speed, need the fermented product that rolls, make
It reaches abundant fermentation, is all to realize stirring by increasing blender, the rust that blender produces is easy in existing technology
So that strain is inactivated, affect strain fermentation, thus the bio-feritlizer impact on fermentation is very big.And existing Organic fertilizer production line
In, the fermentation stirring of fertilizer and fertilizer dry generally extension set device operation step by step, waste time and energy, production efficiency is not high.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of Fructus Musae bio-feritlizer fermentation system,
Its structure is simple, and stirring stirring thoroughly, is dried uniformly, production efficiency is high, easy and simple to handle.
This utility model is realized in：
A kind of Fructus Musae bio-feritlizer fermentation system, including material processing unit, dispensing mixed cell and fermentation unit.Described
Material processing unit includes process tank and vapor can, and described vapor can is connected with described process tank, and for described process tank
Sterilized, and described vapor can be provided with heat ray filter.Described dispensing mixed cell includes blending tank and motor, described
Motor is located at the top of described blending tank, and is connected with the rotating shaft in described blending tank by reducer output shaft, described turn
Stirring vane is provided with axle；Described process tank is connected by pipeline with described blending tank.Described fermentation unit include fermentation tank,
Base, support and air pump, described fermentation tank is installed on described base, and described support is arranged on below described base；Described fermentation
Tank includes heating interlayer and fermentation inner chamber, described fermentation tank is provided with multiple electric heaters, described electric heater extend into institute
State in heating interlayer；Described heating interlayer is sealing structure, is filled with heating medium；In described fermentation, intracavity is provided with many and send
Airduct, described ajutage one end extends close to the position of the bottom of inner chamber of fermenting, and the other end extends to from the top of fermentation tank
Outside is simultaneously connected with air pump.Described blending tank is connected with the feeding mouth of described fermentation tank by batching pipe.
Preferably, the side wall of described fermentation tank is provided with overfall.
Preferably, described overfall is connected with described batching pipe by overflow pipe.
Preferably, the control system that described fermentation tank is provided with temperature sensor and controls temperature sensor.
The beneficial effects of the utility model are as follows：
(1) material in process tank is sterilized using vapor can, kill the antibacterial in raw material completely, it is to avoid to micro- life
So that fermented product steady quality, quality is higher for the murder by poisoning of thing.
(2) many of setting is connected ajutage with air pump, and makes ajutage extend close to the position of the bottom of inner chamber of fermenting,
On the one hand ensure that the good ventilation of intracavity in fermentation, be conducive to strain to survive, moisture content can be helped simultaneously quickly to volatilize upwards,
On the other hand fermented product is rolled so as to reach abundant fermentation by Gas Stirring, prevent the rust that blender produces from so that strain is gone out
Live.
(3) heating, drying of heating interlayer, fermentation, stirring and baking step is combined, a machine achieves fertilizer
The fermentation stirring of material is dried, and stirring stirring thoroughly, is dried uniformly, production efficiency is high, easy and simple to handle, saved and use space.
Brief description
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of vapor can；
Fig. 3 is the structural representation of dispensing mixed cell.
Specific embodiment
With reference to the accompanying drawings, in conjunction with specific embodiments this utility model is made with the explanation of a progressive step, with more preferably geographical
Solution this utility model.
As Figure 1-3, Fructus Musae bio-feritlizer fermentation system of the present utility model, mixes including material processing unit, dispensing
Close unit and fermentation unit.
Described material processing unit includes process tank 1.It is connected with the steam that process tank 1 is sterilized under process tank 1
Tank 7 (with reference to Fig. 2).Vapor can 7 wall is provided with heat ray filter.Vapor can 7 is used for pre-stored tank 2 sterilized, it is to avoid straight
Connect heating, meanwhile, sterilization process in three times, kills the antibacterial in raw material, it is to avoid the murder by poisoning to microorganism is so that be fermented into completely
Quality is stable, and quality is higher.Vapor can 7 includes body 7-1, and its top is provided with outlet 7-2, and bottom is provided with heater 7-3,
Inside is provided with two water-level gauge 7-4, is arranged inside body 7-1 one on the other, control device and water-level gauge 7-4 and heater
7-3 connects respectively, and the body 7-1 wall of described vapor can is provided with heat ray filter.Inject liquid into vapor can 7, water level need to be reached
At meter 7-4, then discharge from outlet 7-2 after heater 7-3 is thermally formed vapor, when water level is less than lower water-level gauge 7-
Transmit a signal to control device when 4, reported to the police and controlled by control device heater 7-3 to quit work.To in process tank 1
Material is sterilized using vapor can 7, kills the antibacterial in raw material completely, it is to avoid murder by poisoning to microorganism is so that fermented product
Steady quality, quality is higher.
Described dispensing mixed cell includes blending tank 2 and motor, and motor 3 is located at the top of blending tank 2, and passes through to subtract
Fast device output shaft is connected with the rotating shaft 3-1 in blending tank 2, and rotating shaft 3-1 is provided with stirring vane 3-2.Process tank 1 and blending tank
2 are connected by pipeline 4, such that it is able to be delivered to the material in process tank 1 in blending tank 2, in described dispensing mixed cell energy
It is sufficiently mixed.
Described fermentation unit includes fermentation tank 5, base 6, support 11 and air pump (not shown), and fermentation tank 5 is installed on
Base 6, support 11 is arranged on below base 6.Blending tank 2 is connected with the feeding mouth of fermentation tank 5 by batching pipe 10.
Fermentation tank 5 includes heating interlayer and fermentation inner chamber, and fermentation tank 5 is provided with multiple electric heaters 8.Electric heater 8
It extend in described heating interlayer.Described heating interlayer is sealing structure, is filled with heating medium.Pass through after the completion of fermentation to send out
The heating interlayer of ferment bucket 5 carries out heating, drying, completes the baking step of fertilizer.
In described fermentation, intracavity is provided with many ajutages 9 (for simplification figure, only illustrating 1 in Fig. 1), ajutage 9 one end
Extend close to the position of the bottom of inner chamber of fermenting, the other end extends to outside from the top of fermentation tank 5 and (in figure is not with air pump
Illustrate) it is connected.The good ventilation of intracavity in fermentation be ensure that by ajutage 9 one aspect, be conducive to strain to survive, simultaneously permissible
Help moisture content quickly to volatilize upwards, on the other hand fermented product is rolled so as to reach abundant fermentation by Gas Stirring, prevent from stirring
The rust that machine produces makes strain inactivate.
In one preferred embodiment, the side wall of fermentation tank 5 is provided with overfall 5-1, and overfall 5-1 passes through overflow
Pipe 12 is connected with batching pipe 10.In fermentation, when there is overflow, the overfall 5-1 of the fermented tank of the liquid that overflow goes out 5 side is through passing
Send overflow pipe 12 and batching pipe 10 to deliver to fermentation tank 5, reuse.
In one preferred embodiment, the control that described fermentation tank is provided with temperature sensor and controls temperature sensor
System.The temperature in fermentation can be controlled by control system.
Above specific embodiment of the utility model is described in detail, but it has been intended only as example, this practicality is new
Type is not restricted to particular embodiments described above.To those skilled in the art, any this utility model is carried out
Equivalent modifications and substitute also all among category of the present utility model.Therefore, without departing from spirit of the present utility model and model
Enclose lower made impartial conversion and change, all should cover in the range of this utility model.
Claims (4)
1. a kind of Fructus Musae bio-feritlizer fermentation system is it is characterised in that include material processing unit, dispensing mixed cell and fermentation
Unit；
Described material processing unit includes process tank and vapor can, and described vapor can is connected with described process tank, and for institute
State process tank to be sterilized, and described vapor can be provided with heat ray filter；
Described dispensing mixed cell includes blending tank and motor, and described motor is located at the top of described blending tank, and passes through
Reducer output shaft is connected with the rotating shaft in described blending tank, and described rotating shaft is provided with stirring vane；Described process tank and institute
State blending tank to connect by pipeline；
Described fermentation unit includes fermentation tank, base, support and air pump, and described fermentation tank is installed on described base, described support
It is arranged on below described base；
Described fermentation tank includes heating interlayer and fermentation inner chamber, and described fermentation tank is provided with multiple electric heaters, and described electricity adds
Hot device extend in described heating interlayer；Described heating interlayer is sealing structure, is filled with heating medium；Described fermentation inner chamber
Inside it is provided with many ajutages, described ajutage one end extends close to the position of the bottom of inner chamber of fermenting, and the other end is from fermentation tank
Top extend to outside and be connected with air pump；
Described blending tank is connected with the feeding mouth of described fermentation tank by batching pipe.
2. Fructus Musae bio-feritlizer fermentation system according to claim 1 is it is characterised in that set on the side wall of described fermentation tank
There is overfall.
3. Fructus Musae bio-feritlizer fermentation system according to claim 2 is it is characterised in that described overfall passes through overflow pipe
It is connected with described batching pipe.
4. the Fructus Musae bio-feritlizer fermentation system according to any one in claim 1-3 is it is characterised in that described fermentation
The control system that tank is provided with temperature sensor and controls temperature sensor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620826843.1U CN205974299U (en) | 2016-07-30 | 2016-07-30 | Banana bio -feritlizer fermentation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620826843.1U CN205974299U (en) | 2016-07-30 | 2016-07-30 | Banana bio -feritlizer fermentation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205974299U true CN205974299U (en) | 2017-02-22 |
Family
ID=58029903
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620826843.1U Expired - Fee Related CN205974299U (en) | 2016-07-30 | 2016-07-30 | Banana bio -feritlizer fermentation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205974299U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112142503A (en) * | 2020-09-30 | 2020-12-29 | 青州乙木农业科技有限公司 | System and method for preparing fertilizer by continuous fermentation of kitchen waste centrifugate |
-
2016
- 2016-07-30 CN CN201620826843.1U patent/CN205974299U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112142503A (en) * | 2020-09-30 | 2020-12-29 | 青州乙木农业科技有限公司 | System and method for preparing fertilizer by continuous fermentation of kitchen waste centrifugate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170222 |