CN106083239A - A kind of novel organic bio-fertilizer production system - Google Patents
A kind of novel organic bio-fertilizer production system Download PDFInfo
- Publication number
- CN106083239A CN106083239A CN201610687461.XA CN201610687461A CN106083239A CN 106083239 A CN106083239 A CN 106083239A CN 201610687461 A CN201610687461 A CN 201610687461A CN 106083239 A CN106083239 A CN 106083239A
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- Prior art keywords
- fertilizer
- bio
- production system
- novel organic
- fertilizer production
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 103
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 33
- 238000001035 drying Methods 0.000 claims abstract description 33
- 229920002456 HOTAIR Polymers 0.000 claims abstract description 24
- 241000894006 Bacteria Species 0.000 claims abstract description 20
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 20
- 239000002028 Biomass Substances 0.000 claims abstract description 16
- 210000003128 Head Anatomy 0.000 claims description 29
- 238000004062 sedimentation Methods 0.000 claims description 27
- 239000000463 material Substances 0.000 claims description 19
- 239000002068 microbial inoculum Substances 0.000 claims description 12
- 238000007599 discharging Methods 0.000 claims description 11
- 239000003034 coal gas Substances 0.000 claims description 8
- 238000005453 pelletization Methods 0.000 claims description 5
- 230000004323 axial length Effects 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims description 3
- 238000009434 installation Methods 0.000 claims description 3
- 238000004134 energy conservation Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 23
- 239000008187 granular material Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 230000000694 effects Effects 0.000 description 5
- 238000000855 fermentation Methods 0.000 description 5
- 230000004151 fermentation Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 238000007873 sieving Methods 0.000 description 4
- 235000013339 cereals Nutrition 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000000813 microbial Effects 0.000 description 2
- 230000000116 mitigating Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000001172 regenerating Effects 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 210000003608 Feces Anatomy 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 230000001580 bacterial Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000002054 inoculum Substances 0.000 description 1
- 230000000749 insecticidal Effects 0.000 description 1
- 239000002917 insecticide Substances 0.000 description 1
- 238000002372 labelling Methods 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/90—Apparatus therefor
- C05F17/989—Flow sheets for biological or biochemical treatment
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B11/00—Machines or apparatus for drying solid materials or objects with movement which is non-progressive
- F26B11/02—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
- F26B11/04—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis
- F26B11/0404—Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis with internal subdivision of the drum, e.g. for subdividing or recycling the material to be dried
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/003—Supply-air or gas filters
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/12—Manure
-
- 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
Abstract
The invention discloses a kind of novel organic bio-fertilizer production system, device, biomass energy hot air generator, drying unit, exhaust apparatus and burnishing device is manufactured including the online quantitative adding device of fertilizer bacteria agent, bio-fertilizer, the online quantitative adding device of fertilizer bacteria agent manufactures device by conveyer belt with bio-fertilizer and is connected, described bio-fertilizer manufactures device, biomass energy hot air generator is connected with drying unit charging aperture, air inlet respectively, and the tail end of drying unit is connected with burnishing device and exhaust apparatus respectively.The technical purpose of the present invention be to provide a kind of can produce continuously organic bio-fertilizer, realize bacteria agent online quantitatively add, novel organic bio-fertilizer production system more environmentally-friendly, energy-conservation, in hgher efficiency, novel organic bio-fertilizer production system utilizes biomass energy to produce bio-fertilizer, the production cost making enterprise is lower, and more preferable to environment.
Description
Technical field
The present invention relates to field of fertilizer production, a kind of novel organic bio-fertilizer production system.
Background technology
Bio-fertilizer is by microbial life activity, makes crops obtain the goods of specific fertilizer effect, also referred to as
Inoculant or bacterial manure.Now, how all advocate " ecological agriculture ", be intended to be done step-by-step in farmland few with or without chemical fertilizer and chemistry
Insecticide, and use organic biofertilizer and use microbial process prevention and elimination of disease and pests.A large amount of uses of chemical fertilizer so that soil
Ground structure is destroyed, and pollutes agricultural product and environment, reduces the quality of agricultural product, and therefore bio-fertilizer is must to use in a large number future
Green fertilizer.
The production of bio-fertilizer now can expend the substantial amounts of energy, particularly during manufacturing, drying so that Ben Yingqi
To environment amenable bio-fertilizer, and during manufacturing, expend mass energy just become drawback.It is right to strengthen now
The materials such as straw produce regenerative resource, and Appropriate application regenerative resource produces environment amenable bio-fertilizer, it is achieved
Sustainable development, and reduce production cost for enterprise.Biomass can be utilized, just produce the production system of organic bio-fertilizer continuously
Become particularly significant.
Summary of the invention
For the deficiency of above-mentioned existence, the technical purpose of the present invention is to provide one can produce organic-biological continuously
Fertile, realize bacteria agent online quantitatively add, novel organic bio-fertilizer production system more environmentally-friendly, energy-conservation, in hgher efficiency,
Novel organic bio-fertilizer production system utilizes biomass energy to produce bio-fertilizer so that the production cost of enterprise is lower, and right
Environment is more preferable.
The present invention is achieved through the following technical solutions: including: the online quantitative adding device of fertilizer bacteria agent, bio-fertilizer
Manufacturing device, biomass energy hot air generator, drying unit, exhaust apparatus and burnishing device, fertilizer bacteria agent exists
Line quantitative adding device manufactures device by conveyer belt with bio-fertilizer and is connected, and described bio-fertilizer manufactures device, biomass energy heat
Wind generation apparatus is connected with drying unit charging aperture, air inlet respectively, drying unit tail end be connected with respectively burnishing device and
Exhaust apparatus.
In technique scheme, the online quantitative adding device of fertilizer bacteria agent can be continuously, efficiently bio-fertilizer system
Manufacturing apparatus feeds, and it is more uniform to make to feed, and manufactures device by bio-fertilizer and bio-fertilizer carries out producing fermentation, and
Carry out sieving, pelletize, the bio-fertilizer after pelletize enters into drying dress by biomass energy hot air generator hot blast out
Putting, dried the bio-fertilizer of granule by drying unit, the bio-fertilizer granule after drying is polished by burnishing device,
Becoming finished product, the tail gas with steam is repelled by exhaust apparatus, and the bio-fertilizer contained in tail gas can be entered by exhaust apparatus
Row sedimentation, the tail gas after sedimentation empties again.
Further, the described online quantitative adding device of fertilizer bacteria agent includes reducing mechanism, the sieve being sequentially connected with
Separating device and screening material transmitting device composition, described screening material transmitting device is provided with continuous feeding, described screening material
Transmitting device is ribbon conveyer.
In technique scheme, compared to traditional direct scheme adding bacteria agent in organic matter, will originally enter
Row is pulverized and screening, only qualified organic matter is carried out microbial inoculum interpolation so that the interpolation of microbial inoculum is more uniform, and also can save
Saving bacteria agent, compared to traditional feed postition, it is possible to reduce and turn over equal operation, in hgher efficiency, the material after screening leads to simultaneously
Cross ribbon conveyer can quickly, be sent to formulate place.
Further, described continuous feeding includes body, and described body is provided with feed hopper and discharging opening, described
Feed hopper is connected by cavity with discharging opening, is provided with rotating shaft in described cavity, and described rotating shaft is provided with spiral along axial length direction
Blade, the helical blade back side is provided with reinforcement, and the work surface of helical blade is through nitrogen treatment, and the material of helical blade is stainless
Steel, described rotating shaft is driven by the motor coordinated；Obconic microbial inoculum disperser it is provided with in discharging opening.
In technique scheme, carried out the conveying of bacteria agent by helical blade, can be by controlling the rotating speed of motor
Control the load of bacteria agent, be suitable for the organic bio-fertilizer of different formulations, there is discharging uniform, stable, and helical-blade
Sheet is rustless steel, and work surface is through nitrogen treatment, it is possible to corrosion-resistant, and uses the time longer, and hardness is higher, can add durable；
The microbial inoculum disperser being provided with enables to microbial inoculum and can be dispersed on material.
Further, described drying unit is multiple rollers exsiccator, and described multiple rollers exsiccator includes being respectively arranged on
In the middle part of multiple rollers exsiccator head end with air inlet and the exhaust outlet on tail end top, be respectively arranged on multiple rollers exsiccator head end
The charging aperture of top and tail end bottom and discharge gate, air inlet is connected with hot air blower, and exhaust outlet is provided with hot air draft machine；Many
Level drum dryer includes chopped-off head cylinder and secondary cylinder, and described chopped-off head cylinder is arranged on the front portion of secondary cylinder, chopped-off head cylinder
And the angle of inclination that secondary cylinder is installed is 5 °～10 °, it can be 6 °, 7 °, 8 °, 9 °.
In technique scheme, it is filled with hot blast by the air inlet on multiple rollers exsiccator, is dried by multiple rollers
The rolling of device so that hot blast fully contacts with bio-fertilizer granule, is baked to, owing to this multiple rollers exsiccator is longer, resistance
Relatively big, including chopped-off head cylinder and secondary cylinder, therefore need to be provided with hot air blower at air inlet, exhaust outlet is provided with hot blast take out
Blower fan so that hot blast can circulate smoothly, quickly dries bio-fertilizer, is discharged by steam in time, by by chopped-off head cylinder and
The angle of inclination that secondary cylinder is installed is 5 °～10 °, so that bio-fertilizer granule can have a stable speed from charging
Mouth is transported to discharging opening.
Further, described biomass energy hot air generator includes bio-coal gas producer, the mistake being sequentially connected with
Filter and combustor, the pipeline between filter and combustor is connected with air-blaster.
In technique scheme, bio-coal gas producer is used for producing coal gas, after production with the material such as straw, wood flour
The contaminant filter that coal gas is contained by coal gas by filter, and it is mixed with coal gas to be connected to air-blaster on conveying gas pipe
Close, fully burn in being jointly transported to combustor, simultaneously the most also for drying the air providing enough so that drying in hgher efficiency.
Further, described bio-fertilizer manufactures device and includes: the installation for fermenting that is sequentially connected with, screening plant, pelletizing drum,
Grain cylinder is connected with charging aperture by transmission belt.
In technique scheme, the powdery bio-fertilizer after fermentation is sieved by screening plant, screens out satisfactory
Powder, the bio-fertilizer of powdery made graininess by pelletizing drum by the bio-fertilizer of powdery, and pelletizing drum is wet type pelletize, therefore
It is transported to the charging aperture of drying unit by conveyer belt again dry.
Further, described exhaust apparatus includes the mud chamber being connected with the exhaust outlet of multiple rollers exsiccator, mud chamber
It is connected with evacuated tube.
In technique scheme, mud chamber can settle being contained in the bio-fertilizer dried in exhaust gas flow so that biological
Fertile powder will not be discharged in air, periodically clears up mud chamber such that it is able to the bio-fertilizer of deposition in mud chamber again
Utilize.
Further, described chopped-off head cylinder is uniformly provided with lifting blade, described lifting blade cross section with secondary inner wall of rotary drum
For " umbrella " type, lifting blade is screw type, and chopped-off head cylinder and the lifting blade in secondary cylinder stagger setting, described lifting blade
Height be chopped-off head cylinder/secondary cylinder internal diameter~。
In technique scheme, by lifting blade cross section being set to " umbrella " type, the height of lifting blade be chopped-off head cylinder/
Secondary cylinder internal diameter~, it is possible to the both sides in drying drum sagittal plane are formed expects curtain uniformly, and in cylinder
The heart will not form material curtain, and the gas for also moisture is discharged, and improves the efficiency dried, chopped-off head cylinder and carrying in secondary cylinder
Material blade staggers settings, so that chopped-off head cylinder can be dried successively by the air-flow dried with the bio-fertilizer in secondary cylinder,
Drying efficiency improves.
Further, described mud chamber includes 3～6 sedimentation units, and each sedimentation unit is respectively equipped with inlet port and discharge
Mouthful, the inlet port of each sedimentation unit connects with outlet successively head and the tail, and forms the gas phase loop of " S " type, the deposition of afterbody
The outlet of unit is connected with evacuated tube.
In technique scheme, by the gas phase loop of " S " type, it is possible to the flowing velocity of mitigation of gases, and increase gas
The length of flow of stream, by the effect of gravity, has the sufficient time to settle bio-fertilizer.
Further, the inlet port of described sedimentation unit and outlet are respectively arranged on the vertical metope of sedimentation unit,
Inlet port is arranged with the roof of the adjacent sedimentation unit of outlet.
In technique scheme, by the roof of inlet port with the adjacent sedimentation unit of outlet is arranged so that gas
Bio-fertilizer bottom mud chamber, all on the top of mud chamber, will not be kicked up by flowing.
The invention has the beneficial effects as follows:
1, the online quantitative adding device of fertilizer bacteria agent can manufacture device charging continuously, efficiently for bio-fertilizer, and makes
Must feed more uniform, manufacture device by bio-fertilizer and bio-fertilizer carries out producing fermentation, and carry out sieving, pelletize, make
Bio-fertilizer after Li enters into drying unit, by drying unit pair by biomass energy hot air generator hot blast out
The bio-fertilizer of granule is dried, and the bio-fertilizer granule after drying is polished by burnishing device, becomes finished product, steams with water
The tail gas of gas is repelled by exhaust apparatus, and the bio-fertilizer contained in tail gas can be settled by exhaust apparatus, the tail after sedimentation
Gas empties again.
2, compared to traditional direct scheme adding bacteria agent in organic matter, will originally pulverize and sieved,
Only qualified organic matter is carried out microbial inoculum interpolation so that the interpolation of microbial inoculum is more uniform, and also can save bacteria agent, phase
Ratio is in traditional feed postition, it is possible to reduces and turns over equal operation, in hgher efficiency, and the material after screening is by belt conveying function simultaneously
The most quickly, it is sent to formulate place.
3, bio-fertilizer manufactures device bio-fertilizer carries out producing fermentation, and carry out sieving, pelletize, the biology after pelletize
Fertile enter into drying unit, by the drying unit biology to granule by biomass energy hot air generator hot blast out
Fertilizer is dried, and the bio-fertilizer granule after drying is polished by burnishing device, becomes finished product, and the tail gas with steam leads to
Crossing exhaust apparatus to repel, the bio-fertilizer contained in tail gas can be settled by exhaust apparatus, and the tail gas after sedimentation empties again.
4, it is filled with hot blast by the air inlet on multiple rollers exsiccator, by the rolling of multiple rollers exsiccator so that
Hot blast fully contacts with bio-fertilizer granule, is baked to, and owing to this multiple rollers exsiccator is longer, resistance is relatively big, including chopped-off head
Cylinder and secondary cylinder, therefore need to be provided with hot air blower at air inlet, be provided with hot air draft machine on exhaust outlet so that hot blast
Can circulate smoothly, quickly bio-fertilizer be dried, in time steam be discharged, by what chopped-off head cylinder and secondary cylinder were installed
Angle of inclination is 5 °～10 °, so that bio-fertilizer granule can have a stable speed to be transported to discharging opening from charging aperture.
5, the gas phase loop of mud chamber " S " type, it is possible to the flowing velocity of mitigation of gases, and the flowing increasing air-flow is long
Degree, by the effect of gravity, has the sufficient time to settle bio-fertilizer.
Accompanying drawing explanation
Fig. 1 is the overview flow chart of the present invention；
Fig. 2 is the structural representation of multiple rollers exsiccator；
Fig. 3 is the structural representation of lifting blade；
The structural representation of Tu4Shi mud chamber；
Fig. 5 is the structural representation of the online quantitative adding device of fertilizer bacteria agent；
Fig. 6 is the structural representation of continuous feeding.
Labelling in figure: 1.1 be hot air blower, 1.2 for charging aperture, 1.3 for air inlet, 1.4 for discharge gate, 1.5 for row
Air port, 1.6 be hot air draft machine, 1.7 for lifting blade, 10 for mud chamber, 10.1 for sedimentation unit, 20 for reducing mechanism, 21
For screening plant, 22 for screening material transmitting device, 23 be continuous feeding, 23.1 for feed hopper, 23.2 be discharge bucket, 23.3
For rotating shaft, 23.4 be helical blade, 23.5 for microbial inoculum disperser.
Detailed description of the invention
The present invention is described in detail below in conjunction with the accompanying drawings.
Novel organic bio-fertilizer production system as shown in Figure 1, including: fertilizer bacteria agent the most quantitatively adds dress
Put, bio-fertilizer manufactures device, biomass energy hot air generator, drying unit, exhaust apparatus and burnishing device, and fertilizer is raw
The online quantitative adding device of thing microbial inoculum manufactures device by conveyer belt with bio-fertilizer and is connected, and described bio-fertilizer manufactures device, biology
Mass-energy source hot air generator is connected with drying unit charging aperture, air inlet respectively, drying unit tail end be connected with throwing respectively
Electro-optical device and exhaust apparatus.
The online quantitative adding device of fertilizer bacteria agent as described in Figure 5, including: the reducing mechanism 20 that is sequentially connected with,
Screening plant 21 and screening material transmitting device 22 form, and described screening material transmitting device 22 is provided with continuous feeding 23,
Described screening material transmitting device 22 is ribbon conveyer.
Continuous feeding (23) as described in Figure 6 includes body, and described body is provided with feed hopper 23.1 and discharging
Mouthfuls 23.2, described feed hopper 23.1 is connected by cavity with discharging opening 23.2, is provided with rotating shaft 23.3 in described cavity, described turn
Axle 23.3 is provided with helical blade 23.4 along axial length direction, and described rotating shaft 23.3 is driven by the motor coordinated；Discharging opening 23.2
Inside it is provided with obconic microbial inoculum disperser 23.5.
Drying unit is multiple rollers exsiccator, as in figure 2 it is shown, multiple rollers exsiccator includes being respectively arranged on multiple rollers
In the middle part of exsiccator head end with the air inlet 1.3 on tail end top and exhaust outlet 1.5, be respectively arranged on the upper of multiple rollers exsiccator head end
The charging aperture 1.2 of portion and tail end bottom and discharge gate 1.4, air inlet 1.3 is connected with hot air blower 1.1, and exhaust outlet 1.5 is provided with
Hot air draft machine 1.6；Multiple rollers exsiccator includes chopped-off head cylinder and secondary cylinder, and described chopped-off head cylinder is arranged on secondary cylinder
Front portion, the angle of inclination that chopped-off head cylinder and secondary cylinder are installed is 5 °～10 °, usually 6 °.
Described biomass energy hot air generator includes bio-coal gas producer, filter and the burning being sequentially connected with
Room, the pipeline between filter and combustor is connected with air-blaster, and the pipeline between filter and combustor is provided with explosion-proof
Valve, the air vent of air-blaster goes out to be provided with flow control valve.
Described bio-fertilizer manufactures device and includes: the installation for fermenting that is sequentially connected with, screening plant, pelletizing drum, and grain cylinder leads to
Cross transmission belt to be connected with charging aperture 1.2.
Described exhaust apparatus includes the mud chamber 10 that the exhaust outlet 1.5 with multiple rollers exsiccator is connected, mud chamber 10 with
Evacuated tube connects.
Described chopped-off head cylinder is uniformly provided with lifting blade 1.7 with secondary inner wall of rotary drum, and described lifting blade 1.7 cross section is
" umbrella " type, lifting blade 1.7 is distributed on chopped-off head cylinder and secondary inner wall of rotary drum as shown in Figure 3, and quantity is 10, lifting blade
1.7 is screw type, and chopped-off head cylinder and the lifting blade in secondary cylinder stagger setting, headed by the height of described lifting blade 1.7
Level cylinder/secondary cylinder internal diameter~, the height of usual lifting blade 1.7 be chopped-off head cylinder/secondary cylinder internal diameter be,
Chopped-off head cylinder internal diameter is identical with secondary cylinder internal diameter.
Described mud chamber 10 includes 4 sedimentation units 10.1, and as shown in Figure 4, each sedimentation unit 10.1 is respectively equipped with entrance
Mouth and outlet, the inlet port of each sedimentation unit 10.1 connects with outlet successively head and the tail, and the gas phase forming " S " type is returned
Road, the outlet of the sedimentation unit 10.1 of afterbody is connected with evacuated tube.
The inlet port of sedimentation unit 10.1 and outlet are respectively arranged on the vertical metope of sedimentation unit 10.1, inlet port
The roof of sedimentation unit 10.1 adjacent with outlet is arranged, and mud chamber 10 makes for mixed clay structure.
Manufacture device by bio-fertilizer and bio-fertilizer carry out producing fermentation, and carry out sieving, pelletize, the life after pelletize
Thing fertilizer enters into drying unit, by the drying unit life to granule by biomass energy hot air generator hot blast out
Thing fertilizer is dried, and the bio-fertilizer granule after drying is polished by burnishing device, becomes finished product, with the tail gas of steam
Being repelled by exhaust apparatus, the bio-fertilizer contained in tail gas can be settled by exhaust apparatus, and the tail gas after sedimentation empties again.
Claims (10)
1. a novel organic bio-fertilizer production system, it is characterised in that including: fertilizer bacteria agent the most quantitatively adds dress
Put, bio-fertilizer manufactures device, biomass energy hot air generator, drying unit, exhaust apparatus and burnishing device, and fertilizer is raw
The online quantitative adding device of thing microbial inoculum manufactures device by conveyer belt with bio-fertilizer and is connected, and described bio-fertilizer manufactures device, biology
Mass-energy source hot air generator is connected with drying unit charging aperture, air inlet respectively, drying unit tail end be connected with throwing respectively
Electro-optical device and exhaust apparatus.
Novel organic bio-fertilizer production system the most according to claim 1, it is characterised in that described fertilizer bacteria agent
Online quantitative adding device includes reducing mechanism (20), screening plant (21) and screening material transmitting device (22) group being sequentially connected with
Becoming, described screening material transmitting device (22) is provided with continuous feeding (23), described screening material transmitting device (22) is band
Formula conveyer.
Novel organic bio-fertilizer production system the most according to claim 2, it is characterised in that described continuous feeding
(23) include body, described body is provided with feed hopper (23.1) and discharging opening (23.2), described feed hopper (23.1) and going out
Material mouth (23.2) is connected by cavity, is provided with rotating shaft (23.3) in described cavity, and described rotating shaft (23.3) sets along axial length direction
Being equipped with helical blade (23.4), described rotating shaft (23.3) is driven by the motor coordinated；Discharging opening is provided with rounding in (23.2)
The microbial inoculum disperser (23.5) of taper.
Novel organic bio-fertilizer production system the most according to claim 1, it is characterised in that described drying unit is multistage
Drum dryer, described multiple rollers exsiccator include being respectively arranged in the middle part of multiple rollers exsiccator head end with the entering of tail end top
Air port (1.3) and exhaust outlet (1.5), it is respectively arranged on the top of multiple rollers exsiccator head end and the charging aperture of tail end bottom
(1.2) and discharge gate (1.4), air inlet (1.3) is connected with hot air blower (1.1), and exhaust outlet (1.5) is provided with hot air draft machine
(1.6)；Multiple rollers exsiccator includes chopped-off head cylinder and secondary cylinder, and described chopped-off head cylinder is arranged on the front portion of secondary cylinder,
The angle of inclination that chopped-off head cylinder and secondary cylinder are installed is 5 °～10 °.
Novel organic bio-fertilizer production system the most according to claim 1, it is characterised in that described biomass energy hot blast
Generating means includes bio-coal gas producer, filter and the combustor being sequentially connected with, the pipe between filter and combustor
Road is connected with air-blaster.
Novel organic bio-fertilizer production system the most according to claim 1, it is characterised in that described bio-fertilizer manufactures device
Including: the installation for fermenting that is sequentially connected with, screening plant, pelletizing drum, grain cylinder is connected with charging aperture (1.2) by transmission belt.
Novel organic bio-fertilizer production system the most according to claim 1, it is characterised in that described exhaust apparatus include with
The mud chamber (10) that the exhaust outlet (1.5) of multiple rollers exsiccator connects, mud chamber (10) are connected with evacuated tube.
Novel organic bio-fertilizer production system the most according to claim 4, it is characterised in that described chopped-off head cylinder is with secondary
Inner wall of rotary drum is uniformly provided with lifting blade (1.7), and described lifting blade (1.7) cross section is " umbrella " type, and lifting blade (1.7) is spiral shell
Rotation type, chopped-off head cylinder and the lifting blade in secondary cylinder stagger settings, and the height of described lifting blade (1.7) is that chopped-off head rolls
Cylinder/secondary cylinder internal diameter~。
Novel organic bio-fertilizer production system the most according to claim 1, it is characterised in that described mud chamber (10) include
3～6 sedimentation units (10.1), each sedimentation unit (10.1) is respectively equipped with inlet port and outlet, each sedimentation unit (10.1)
Inlet port and outlet head and the tail successively connect, and form the gas phase loop of " S " type, the row of the sedimentation unit (10.1) of afterbody
Outlet is connected with evacuated tube.
Novel organic bio-fertilizer production system the most according to claim 7, it is characterised in that described sedimentation unit
(10.1) inlet port and outlet are respectively arranged on the vertical metope of sedimentation unit (10.1), and inlet port is adjacent with outlet
The roof of sedimentation unit (10.1) is arranged.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610687461.XA CN106083239A (en) | 2016-08-19 | 2016-08-19 | A kind of novel organic bio-fertilizer production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610687461.XA CN106083239A (en) | 2016-08-19 | 2016-08-19 | A kind of novel organic bio-fertilizer production system |
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| CN106083239A true CN106083239A (en) | 2016-11-09 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN106905015A (en) * | 2017-04-06 | 2017-06-30 | 贵州赤天化桐梓化工有限公司 | It is a kind of with dealing with earthworm mixed-matrix and the devices and methods therefor that is dried |
| CN112410175A (en) * | 2020-11-30 | 2021-02-26 | 杭州小鲤工业设计有限公司 | Adjustable quantitative microbial inoculum adding device for biological fermentation |
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| CN102430563A (en) * | 2011-12-12 | 2012-05-02 | 张华民 | Alcohol vinasse waste slag treatment system and treatment method |
| CN203451394U (en) * | 2013-09-13 | 2014-02-26 | 张共敏 | System for producing bio-organic fertilizer through airtight aerobic fermentation of municipal sludge or kitchen residues |
| CN104446728A (en) * | 2014-11-28 | 2015-03-25 | 四川凯尔丰农业科技有限公司 | Online quantitative addition device for organic fertilizer biological agents |
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| CN102430563A (en) * | 2011-12-12 | 2012-05-02 | 张华民 | Alcohol vinasse waste slag treatment system and treatment method |
| CN203451394U (en) * | 2013-09-13 | 2014-02-26 | 张共敏 | System for producing bio-organic fertilizer through airtight aerobic fermentation of municipal sludge or kitchen residues |
| CN104446728A (en) * | 2014-11-28 | 2015-03-25 | 四川凯尔丰农业科技有限公司 | Online quantitative addition device for organic fertilizer biological agents |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106905015A (en) * | 2017-04-06 | 2017-06-30 | 贵州赤天化桐梓化工有限公司 | It is a kind of with dealing with earthworm mixed-matrix and the devices and methods therefor that is dried |
| CN106905015B (en) * | 2017-04-06 | 2020-05-15 | 贵州赤天化桐梓化工有限公司 | Device and method for treating and drying mixed matrix by using earthworms |
| CN112410175A (en) * | 2020-11-30 | 2021-02-26 | 杭州小鲤工业设计有限公司 | Adjustable quantitative microbial inoculum adding device for biological fermentation |
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