CN106278435A - A kind of solid organic matters aerobic pressurized high-temperature fermentation tank - Google Patents
A kind of solid organic matters aerobic pressurized high-temperature fermentation tank Download PDFInfo
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- CN106278435A CN106278435A CN201610898065.1A CN201610898065A CN106278435A CN 106278435 A CN106278435 A CN 106278435A CN 201610898065 A CN201610898065 A CN 201610898065A CN 106278435 A CN106278435 A CN 106278435A
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- 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
- C05F17/95—Devices in which the material is conveyed essentially vertically between inlet and discharge means
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N17/00—Apparatus specially adapted for preparing animal feeding-stuffs
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N17/00—Apparatus specially adapted for preparing animal feeding-stuffs
- A23N17/004—Apparatus specially adapted for preparing animal feeding-stuffs for treating by application of heat, e.g. by means of potato cookers
-
- 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
- C05F17/30—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation using irradiation, e.g. solar or nuclear radiation; using electric or magnetic fields
-
- 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
- C05F17/60—Heating or cooling during the 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- 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
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Microbiology (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Molecular Biology (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Toxicology (AREA)
- Physics & Mathematics (AREA)
- High Energy & Nuclear Physics (AREA)
- Sustainable Development (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses a kind of solid organic matters aerobic pressurized high-temperature fermentation tank, including tank body, feed system, fixing axle, material-feeding mechanism, Material moving device, discharging mechanism, leakage port, discharging opening and inside heat exchanger；Feed system is located at tank deck, fixing is located in tank body, and for hollow structure, two ends bearing respectively connects tank deck and tank bottoms, fixing axle bottom end seal and stretch out tank bottoms connection hydraulic motor；Material-feeding mechanism, Material moving device and discharging mechanism are arranged on fixing axle the most successively；Leakage port is located at tank deck；Discharging opening is located at tank bottoms；Inside heat exchanger is located at inner tank wall, and air inlet connects oxygenation compression system, and gas outlet connects fixing axle top.The fermentation tank of the present invention has ensured the oxygen needed for fermentation, the temperature that inside and outside two set heat exchangers can effectively utilize biofermentation to produce, ensure that fermentation temperature is stable, heat up quickly, become thoroughly decomposed and innoxious the most thorough, control to make moisture content rapid evaporation by pressure differential, shorten fermentation period, improve efficiency.
Description
Technical field
The invention belongs to fermentation tank technical field, specifically a kind of solid organic matters aerobic pressurized high-temperature fermentation tank.
Technical background
At present, China's agricultural efficient, intensive and farming industry obtain and develop rapidly, and bring a large amount of solid equally
Organic resources is idle, abandon, and also result in the waste of organic resources, and a lot of places also create the pollution to environment.
Solid organic matters includes straw, Chinese herb residues, manioc waste, bagasse, animal dung slag, filter pressing bacterium mud etc., pre-through pulverizing etc.
After process, it is possible to use biotechnology, transform under conditions of anaerobism or aerobic fermentation rich in abundant humic acids matter and move
The nutrient product of plant available, comes back in modern agricultural production, reduces the agricultural production usage amount to chemical fertilizer, is conducive to
Improve the organic matter of soil, improve soil activation, raising agricultural product quality, it is also possible to as the feedstuff of its feeding, minimizing is raised
Material cost of investment.But, at present, owing to solid organic matters quality is light, volume is big, packs difficult, and general distance is concentrated
After fermentation process makes product, distance scattered distribution again, causes cost of transportation high.Solid organic matters resource is exactly
To realize the dehydration of material by the way of biofermentation, become thoroughly decomposed and innoxious, conventional strip stamps formula, the solid organic matters of slot type is sent out
Ferment technique, ferments in mostly being outdoor or workshop, is restricted by the factor such as ambient temperature, Odor control, and exist occupation of land big,
The problems such as technology controlling and process difficulty, moisture slow, the fermentation period length of evaporation.
Summary of the invention
The technical problem to be solved is to provide a kind of solid organic matters aerobic pressurized high-temperature fermentation tank, solves to pass
System mode is taken up an area greatly, exhaust-gas treatment difficulty, fermentation temperature and technique are difficult to control, moisture evaporation is slow, fermentation period length, collect fortune
Defeated problem with high costs, it is achieved system equipmentization, solid organic matters can recycling, beneficially technology and equipment on the spot
Popularization and application.
The present invention solves above-mentioned technical problem by the following technical programs:
A kind of solid organic matters aerobic pressurized high-temperature fermentation tank, including tank body, feed system, fixing axle, material-feeding mechanism, shifting
Material mechanism, discharging mechanism, leakage port, discharging opening and inside heat exchanger；
Feed system is located at tank deck, and including storage bin and charging hatch door, charging hatch door is located at bottom storage bin；
Fixing being located in tank body, for hollow structure, two ends bearing respectively connects tank deck and tank bottoms, fixing axle bottom end seal
And stretching out tank bottoms connection hydraulic motor, hydraulic motor connects hydraulic oil pump；Tank deck is stretched out on fixing axle top；
Material-feeding mechanism, Material moving device and discharging mechanism are stainless steel or carbon steel preservative treatment, all tie in scissor-shaped
Structure, is arranged on fixing axle the most successively；
Leakage port is located at tank deck；Discharging opening is located at tank bottoms；
Inside heat exchanger is located at inner tank wall, and the air inlet of inside heat exchanger is opened in the middle part of tank body or middle and lower part, gives vent to anger
Mouth is located at tank body top or top and pipeline connects fixing axle top.
Described tank body is cylinder, and ratio of height to diameter is 1.0～3.5.
Also include fixed support；Tank body is placed on fixed support.
Described charging hatch door is formed around sealing gasket, and the hatch door plate of charging hatch door is fixed with tank body by movable ear；Hatch door
Plate connects cylinder, and cylinder is arranged on storage bin top.
Described material-feeding mechanism includes: upper peeling knife and lower peeling knife are that scissor-shaped is connected on fixing axle, upper peeling knife and
Two guide plates it are respectively provided with on lower peeling knife；
Material moving device includes: upper peeling knife and lower peeling knife are that scissor-shaped is connected on fixing axle, and upper peeling knife is at blade
Respectively setting two guide plates in the middle part of tail end, blade, lower peeling knife respectively sets on two guide plates, and the knife back equal in the middle part of blade tail end, blade
It is provided with pore, in the fixing axle of pore connection；
Discharging mechanism includes: lower peeling knife is connected with fixing axle, is respectively equipped with in the middle part of the blade tail end of lower peeling knife, blade
Two guide plates, the edge of a knife has multi-disc blade uniformly at intervals.
The air inlet of described inside heat exchanger connects oxygenation compression system, and oxygenation compression system includes high pressure blower, storage
Gas tank, outer heat-exchanger and heating system, high pressure blower connects air accumulator, and air accumulator pipeline connects the air inlet of outer heat-exchanger
Mouthful, the gas outlet pipeline of outer heat-exchanger connects the air inlet of inside heat exchanger；Heating system connects outer heat-exchanger.
Described heating system be electrical heating, solar energy heating, heat pump, biogas heating, steam-heated one or
Several.
Described leakage port connects air releasing device, and air releasing device includes high pressure exhaust blower, and high pressure exhaust blower one end pipeline connects
With leakage port, other end pipeline connects biological aeration tower.
Also include in storehouse material induction apparatus, oxygen sensor, pressure transducer and temperature sensing in material induction apparatus, tank
Device；In storehouse in material induction apparatus, tank material induction apparatus, oxygen sensor, pressure transducer and hygrosensor respectively with control
Center connects；In storehouse, material induction apparatus is located in storage bin, and in tank, material induction apparatus, oxygen sensor and pressure transducer are respectively
Being located in tank body, hygrosensor is upper, middle and lowers that are multiple, that be respectively arranged in tank body.
The invention has the beneficial effects as follows:
(1) needed for solid organic matters of the present invention aerobic pressurized high-temperature fermentation tank utilizes oxygenation compression system to ensure fermentation
Oxygen, is respectively provided with inside and outside two set heating systems, effectively utilizes the temperature that biofermentation produces, it is ensured that fermentation temperature is stable, rise
Temperature quickly, become thoroughly decomposed and innoxious faster, more thorough, utilize pressurization negative pressure alternate cycles evaporation technique, by pressure differential control, make
Moisture content rapid evaporation, shortens fermentation period, improves efficiency；
(2) solid organic matters aerobic pressurized high-temperature installation for fermenting achieves modularized design, uses pot type equipment configuration, accounts for
Ground is little, and equipmentization, automaticity are high, reduce labor intensity；
(3) can organize used in parallel more, meet the production requirement of various treating capacity.
Accompanying drawing explanation
Fig. 1 is solid organic matters of the present invention aerobic pressurized high-temperature fermentation tank structural representation.
Fig. 2 is the material-feeding mechanism structural representation in Fig. 1.
Fig. 3 is the Material moving device structural representation in Fig. 1.
Fig. 4 is the discharging mechanism structural representation in Fig. 1.
In figure: 5-tank body, 510-storage bin, 511-feeds hatch door, material induction apparatus in 512-storehouse, material sense in 513-tank
Answer device, 515-cylinder, 516-activity ear, 517-hydraulic motor, 518-hydraulic oil pump, 519-fixed support, 52-leakage port,
520-discharging opening, 521-high pressure exhaust blower, 53-oxygen sensor, 54-pressure transducer, 55-upper bearing (metal), 56-lower bearing,
571-high pressure blower, 572-air accumulator, 573-outer heat-exchanger, 574-inside heat exchanger, 575-heating system, 58-cloth
Mechanism, the upper peeling knife of 581-, peeling knife under 582-, 583-guide plate, 584-fixes axle, 585-flange, 586-pore, 588-cutter
Sheet, 59-Material moving device, 60-discharging mechanism, 7-hygrosensor, 6-biology aeration tower, 9-control centre.
Detailed description of the invention
Below in conjunction with example, accompanying drawing, the invention will be further described, and the enforcement of the present invention is not limited to the following example.
As it is shown in figure 1, a kind of solid organic matters aerobic pressurized high-temperature fermentation tank, main body is stainless steel or carbon steel anticorrosion
Process, including tank body 5, feed system, fixing axle 584, material-feeding mechanism 58, Material moving device 59, discharging mechanism 60, leakage port 52,
Discharging opening 520 and inside heat exchanger 574；
Feed system is located at tank body 5 top, and including storage bin 510 and charging hatch door 511, charging hatch door 511 is located at storing
Bottom storehouse 510, it is used for controlling material and enters in tank body 5 from storage bin 510；Charging hatch door 511 is formed around sealing gasket, feeds cabin
The hatch door plate of door 511 is connected by movable ear 516 is fixing with tank body 5；Hatch door plate connects cylinder 515, and cylinder 515 is arranged on storing
On Cang510Ding.Controlled the opening and closing of charging hatch door 511 by cylinder 515, the material controlling material storage feed bin 510 enters tank body 5.
Fixing axle 584 is located in tank body 5, for hollow structure.Tank deck is stretched out and by upper bearing (metal) 55 in the upper end of fixing axle 584
Connecting tank deck, lower end is stretched out tank bottoms and connects tank bottoms by lower bearing 56, and lower end is also connected with hydraulic motor 517, hydraulic motor 517
Connect hydraulic oil pump 518；The bottom end seal of fixing axle 584.
Material-feeding mechanism 58, Material moving device 59 and discharging mechanism 60 are stainless steel or carbon steel preservative treatment, all in cutting
The each one group of upper and lower being connected to fix axle 584 of knife-like structure, material-feeding mechanism 58 and discharging mechanism 60, Material moving device
59 helically arrange be fixed in the middle part of fixing axle 584 for some groups.
Can also be: material-feeding mechanism 58, Material moving device 59, discharging mechanism 60 respectively connect a hollow stub shafts and formed whole respectively
Body structure, then it is concatenated into fixing axle 584 successively by flange 585.
As in figure 2 it is shown, material-feeding mechanism 58 includes peeling knife 581 and lower peeling knife 582, upper peeling knife 581 and lower rotary-cut
Cutter 582 is connected in scissor-shaped on fixing axle 584, and upper peeling knife 581 and lower peeling knife 582 are respectively provided with two guide plates 583.
As it is shown on figure 3, Material moving device 59 includes peeling knife 581 and lower peeling knife 582, upper peeling knife 581 and lower rotary-cut
Cutter 582 is connected in scissor-shaped on fixing axle 584, and upper peeling knife 581 respectively sets two guide plates 583 in the middle part of blade tail end, blade,
Lower peeling knife 582 respectively sets two guide plates 583 in the middle part of blade tail end, blade, and is equipped with pore 586 on the knife back, and pore 586 is even
In logical fixing axle 584.
As shown in Figure 4, discharging mechanism 60 includes that lower peeling knife 582, lower peeling knife 582 are connected with fixing axle 584, lower rotary-cut
It is respectively equipped with two guide plates 583 in the middle part of the blade tail end of cutter 582, blade, the edge of a knife has multi-disc blade 588 uniformly at intervals.
Leakage port 52 is located at tank deck, and leakage port 52 connects air releasing device, and air releasing device includes high pressure exhaust blower 521, high pressure
Exhaust blower 521 one end pipeline connects and leakage port 52, and other end pipeline connects biological aeration tower 6.Discharging opening 520 is located at tank bottoms；
Inside heat exchanger 574 is located at tank body 5 inwall, the air inlet of inside heat exchanger 574 be opened in the middle part of tank body 5 or under
Portion, inside heat exchanger 574 body along tank body 5 inwall up around, the gas outlet of inside heat exchanger 574 is opened in tank body 5 top
And pipeline connects fixing axle 584 top.The air inlet of inside heat exchanger 574 connects oxygenation compression system, oxygenation compression system bag
Including high pressure blower 571, air accumulator 572, outer heat-exchanger 573 and heating system 575, high pressure blower 571 connects air accumulator
572, air accumulator 572 pipeline connects the air inlet of outer heat-exchanger 573, and the gas outlet pipeline of outer heat-exchanger 573 connects interior-heat
The air inlet of exchanger 574；Heating system 575 connects outer heat-exchanger 573.Described heating system 575 is electrical heating, the sun
Can heating, heat pump, biogas heat, steam-heated one or more.
Described tank body 5 is cylinder, and ratio of height to diameter is 1.0～3.5.
Also include fixed support 519；Tank body 5 is placed on fixed support 519.
Also include that in material induction apparatus 512, tank, material induction apparatus 513, oxygen pass in the storehouse being connected with control centre 9 respectively
Sensor 53, pressure transducer 54 and hygrosensor 7；In in storehouse, material induction apparatus 512 is located at storage bin 510, material sense in tank
Answering device 513, oxygen sensor 53 and pressure transducer 54 to be respectively arranged in tank body 5, hygrosensor 7 is multiple, is respectively arranged on
Upper, middle and lower in tank body 5.
The solid organic matters pulverization process such as including straw, Chinese herb residues, manioc waste, bagasse, animal dung slag, filter pressing bacterium mud
Rear feeding batch mixer, is added fermenting agent, N nutritive salt and water to batch mixer respectively by proportioning machine and mixes, after mix homogeneously
Send into storage bin 510, storage bin 510 be fed into aerobic pressurized high-temperature fermentation cylinder for fermentation 5-12 days, at aerobic pressurized high-temperature
In fermentation tank, the signal instruction according to control centre 9 circulates realization charging, cloth, oxygenation pressurization, moves material, disappointing, the work of discharging
Sequence processes, and utilizes pressurization negative pressure alternate cycles method of evaporating, improves the water evaporates speed of solid organic matters, and biofermentation makes solid
Body Organic substance is rapidly converted into rich in abundant humic acids matter and animals and plants absorbable nutrient product, reaches solid organic matters resource
Changing the requirement utilized, discharging material can use as feedstuff, it is also possible to use as organic fertilizer, biological organic fertilizer.Aerobic
The waste gas that pressurized high-temperature fermentation tank is discharged purifies via biological aeration tower 6 and discharges, solves exhaust pollution problems.
Feed intake, discharging is batch-type pattern, and oxygenation pressurization, pressure release are batch-type pattern, are formed from top to down in fermentation tank
Heating zone 50-60 DEG C, 60-72 DEG C, high-temperature region, three gradients in 45-60 DEG C, cooling area, moisture successively decreases from 60%-70% from top to bottom
For forming malleation, negative pressure state, rapid evaporation moisture in 30%-45%, fermentation tank.
In storehouse, material induction apparatus 512 feeds back to control centre 9 according to the bank height signal of storage bin 510, controls to feed intake
To storage bin 510；After material is discharged in tank, forming certain material potential difference, in tank, material induction apparatus 513 feeds back signal to control
Center 9, control cylinder 515 is opened charging hatch door 511 and is dosed in tank, starts air releasing device simultaneously.Charging hatch door 511 is closed,
Air releasing device stops, and has fed intake, and hydraulic motor 517 drives fixing axle 584 to rotate clockwise, 58 solid materials of material-feeding mechanism
Being evenly arranged in tank, Material moving device 59 is simultaneously material horizontal displacement in tank, and plays brokenly bridge, immixture, and temperature passes
Sensor 7, oxygen sensor 53, pressure transducer 54 feed back detection signal respectively to control centre 9, management oxygenation compression system
Start and stop.After fermentation materials temperature reaches design temperature, heating zone temperature reaches 55 DEG C or high-temperature region reaches 65 DEG C, hydraulic oil
Pump, oxygenation compression system start；Or after oxygen concentration is less than the setting concentration of 18%, hydraulic-driven, oxygenation compression system start；
Or after fermentation tank air pressure reaches malleation 0.08MPa setting pressure, air releasing device and high pressure exhaust blower 521 start, fermentation tank air pressure
Reaching negative pressure 0.07MPa and set pressure, air releasing device and high pressure exhaust blower 521 are closed down；Reservoir pressure is less than setting pressure
2MPa, high pressure blower 571 starts, and pressure reaches to set pressure 4MPa, and high pressure blower 571 stops.
Claims (9)
1. a solid organic matters aerobic pressurized high-temperature fermentation tank, is characterized in that: include tank body, feed system, fixing axle, cloth
Mechanism, Material moving device, discharging mechanism, leakage port, discharging opening and inside heat exchanger；
Feed system is located at tank deck, and including storage bin and charging hatch door, charging hatch door is located at bottom storage bin；
Fixing being located in tank body, for hollow structure, two ends bearing respectively connects tank deck and tank bottoms, fixing axle bottom end seal and stretching
Going out tank bottoms connection hydraulic motor, hydraulic motor connects hydraulic oil pump；Tank deck is stretched out on fixing axle top；
Material-feeding mechanism, Material moving device and discharging mechanism are stainless steel or carbon steel preservative treatment, all in en scissors-like construction, from
Upper and under be arranged in successively on fixing axle；
Leakage port is located at tank deck；Discharging opening is located at tank bottoms；
Inside heat exchanger is located at inner tank wall, and the air inlet of inside heat exchanger is opened in the middle part of tank body or middle and lower part, and gas outlet sets
Fixing axle top is connected in tank body top or top and pipeline.
2. a kind of solid organic matters aerobic pressurized high-temperature fermentation tank as claimed in claim 1, is characterized in that: described tank body is circle
Cylinder, ratio of height to diameter is 1.0～3.5.
3. a kind of solid organic matters aerobic pressurized high-temperature fermentation tank as claimed in claim 1, is characterized in that: also include fixing
Frame；Tank body is placed on fixed support.
4. a kind of solid organic matters aerobic pressurized high-temperature fermentation tank as claimed in claim 1, is characterized in that: described charging hatch door
Being formed around sealing gasket, the hatch door plate of charging hatch door is fixed with tank body by movable ear；Hatch door plate connects cylinder, and cylinder is arranged on
On storage bin top.
5. a kind of solid organic matters aerobic pressurized high-temperature fermentation tank as claimed in claim 1, is characterized in that: described material-feeding mechanism
Including: upper peeling knife and lower peeling knife are that scissor-shaped is connected on fixing axle, and upper peeling knife and lower peeling knife are respectively provided with two
Guide plate；
Material moving device includes: upper peeling knife and lower peeling knife are that scissor-shaped is connected on fixing axle, upper peeling knife blade tail end,
Respectively setting two guide plates in the middle part of blade, lower peeling knife respectively sets in the middle part of blade tail end, blade and is equipped with gas on two guide plates, and the knife back
Hole, in the fixing axle of pore connection；
Discharging mechanism includes: lower peeling knife is connected with fixing axle, is respectively equipped with two in the middle part of the blade tail end of lower peeling knife, blade
Guide plate, the edge of a knife has multi-disc blade uniformly at intervals.
6. a kind of solid organic matters aerobic pressurized high-temperature fermentation tank as claimed in claim 1, is characterized in that: described interior heat exchange
The air inlet of device connects oxygenation compression system, and oxygenation compression system includes high pressure blower, air accumulator, outer heat-exchanger and heating
System, high pressure blower connects air accumulator, and air accumulator pipeline connects the air inlet of outer heat-exchanger, the gas outlet of outer heat-exchanger
Pipeline connects the air inlet of inside heat exchanger；Heating system connects outer heat-exchanger.
7. a kind of solid organic matters aerobic pressurized high-temperature fermentation tank as claimed in claim 6, is characterized in that: described heating system
System for electrical heating, solar energy heating, heat pump, biogas heating, steam-heated one or more.
8. a kind of solid organic matters aerobic pressurized high-temperature fermentation tank as claimed in claim 1, is characterized in that: described leakage port is even
Connecing air releasing device, air releasing device includes high pressure exhaust blower, and high pressure exhaust blower one end pipeline connects and leakage port, and other end pipeline is even
Deliver a child thing aeration tower.
9. a kind of solid organic matters aerobic pressurized high-temperature fermentation tank as claimed in claim 1, is characterized in that: also include thing in storehouse
Material induction apparatus, oxygen sensor, pressure transducer and hygrosensor in material induction apparatus, tank；In storehouse in material induction apparatus, tank
Material induction apparatus, oxygen sensor, pressure transducer and hygrosensor are connected with control centre respectively；Material induction apparatus in storehouse
Being located in storage bin, in tank, material induction apparatus, oxygen sensor and pressure transducer are respectively arranged in tank body, and hygrosensor is
Upper, middle and lowers that are multiple, that be respectively arranged in tank body.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610898065.1A CN106278435A (en) | 2016-10-15 | 2016-10-15 | A kind of solid organic matters aerobic pressurized high-temperature fermentation tank |
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| CN201610898065.1A CN106278435A (en) | 2016-10-15 | 2016-10-15 | A kind of solid organic matters aerobic pressurized high-temperature fermentation tank |
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| CN106278435A true CN106278435A (en) | 2017-01-04 |
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Cited By (3)
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| CN107827507A (en) * | 2017-11-17 | 2018-03-23 | 巴东隆生生物科技有限公司 | A kind of biomass fertilizers process units |
| CN108998352A (en) * | 2018-09-14 | 2018-12-14 | 山东沃禾生物科技有限公司 | Humic acid solution prepares equipment |
| CN109400239A (en) * | 2018-10-25 | 2019-03-01 | 湖北鸟王智能装备股份有限公司 | A kind of cultivation waste fermentation turning machine |
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| CN203715524U (en) * | 2014-03-12 | 2014-07-16 | 潍坊鹤来饲料有限公司 | Solid fermentation tank with depressurization system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107827507A (en) * | 2017-11-17 | 2018-03-23 | 巴东隆生生物科技有限公司 | A kind of biomass fertilizers process units |
| CN108998352A (en) * | 2018-09-14 | 2018-12-14 | 山东沃禾生物科技有限公司 | Humic acid solution prepares equipment |
| CN109400239A (en) * | 2018-10-25 | 2019-03-01 | 湖北鸟王智能装备股份有限公司 | A kind of cultivation waste fermentation turning machine |
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Application publication date: 20170104 |