CN207987056U - A kind of biological organic fertilizer production system - Google Patents
A kind of biological organic fertilizer production system Download PDFInfo
- Publication number
- CN207987056U CN207987056U CN201820029348.7U CN201820029348U CN207987056U CN 207987056 U CN207987056 U CN 207987056U CN 201820029348 U CN201820029348 U CN 201820029348U CN 207987056 U CN207987056 U CN 207987056U
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- Prior art keywords
- organic fertilizer
- powdery
- granular
- fermentation cabin
- fertilizer production
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- 239000003895 organic fertilizer Substances 0.000 title claims abstract description 72
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 69
- 238000000855 fermentation Methods 0.000 claims abstract description 121
- 230000004151 fermentation Effects 0.000 claims abstract description 121
- 239000002994 raw material Substances 0.000 claims abstract description 29
- 238000012216 screening Methods 0.000 claims abstract description 24
- 238000012856 packing Methods 0.000 claims abstract description 18
- 238000001816 cooling Methods 0.000 claims abstract description 15
- 238000003860 storage Methods 0.000 claims description 16
- 239000003054 catalyst Substances 0.000 claims description 10
- 238000005303 weighing Methods 0.000 claims description 9
- 239000000919 ceramic Substances 0.000 claims description 8
- 238000007789 sealing Methods 0.000 claims description 8
- 230000000694 effects Effects 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 description 15
- 108010066278 cabin-4 Proteins 0.000 description 12
- 238000005516 engineering process Methods 0.000 description 7
- 239000003337 fertilizer Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000000843 powder Substances 0.000 description 7
- 239000008187 granular material Substances 0.000 description 5
- 238000001035 drying Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 238000007873 sieving Methods 0.000 description 4
- 238000009434 installation Methods 0.000 description 3
- 238000013461 design Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 210000003608 fece Anatomy 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000669003 Aspidiotus destructor Species 0.000 description 1
- 206010054949 Metaplasia Diseases 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000015689 metaplastic ossification Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 239000000725 suspension 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 kind of biological organic fertilizer production system, including raw material chopper, fermentation tank, granular organic fertilizer production line and powdery Organic fertilizer production line, the discharge port of raw material chopper is connected with the feed inlet of fermentation tank, fermentation tank includes granular fermentation cabin and powdery fermentation cabin, granular organic fertilizer production line includes sequentially connected Squeezinggranulator, screening machine, cooling equipment and the first measuring packing machine, the first conveying device is equipped between the discharge port of Squeezinggranulator and the feed inlet of screening machine, powdery Organic fertilizer production line includes sequentially connected pulverizer, dryer and the second measuring packing machine, the fines mouth of screening machine is connected with the feed inlet of pulverizer, the discharge port of pulverizer is connected with the feed inlet of dryer, the utility model is capable of the production duration of effectively save biological organic fertilizer, whole production line area occupied is small.
Description
Technical field
The utility model belongs to organic fertilizer production technical field, more particularly, to a kind of biological organic fertilizer production system.
Background technology
Biological organic fertilizer refer to microorganisms with specific functions with mainly with plant and animal residues (such as feces of livestock and poultry, agricultural crop straw)
The one kind being combined for source and through harmless treatment, decomposed organic materials has both microbial manure and organic fertilizer effect
Fertilizer, compared with chemical fertilizer, biological organic fertilizer has nutrient complete, can effectively improve soil, improve the quality of crops,
It avoids that soil hardening caused by chemical fertilizer is commonly used.
The prior art is in the production process of biological organic fertilizer, raw material ferments after crushing into fermentation tank, has fermented
Cheng Houzai carries out screening process by screening machine, and entire production system needs multiple screening process, not only cause the production time it is long,
Complex steps, while causing entire process system production line huger, installation cost and area occupied are big, in addition, different grains
The organic fertilizer fermentation degree of diameter state is different, and prior art directly sends out the stalk of different-grain diameter in the same fermentation tank
Ferment processing, causes the total production time of biological organic fertilizer to lengthen.
Invention content
Problem to be solved in the utility model is to provide a kind of biological organic fertilizer production system, can effectively save biology have
The production duration of machine fertilizer, whole production line area occupied is small, and reaches good fermentation effect using new structural fermentation tank
Fruit.
In order to solve the above technical problems, the technical solution adopted in the utility model is：A kind of biological organic fertilizer production system,
Including raw material chopper, fermentation tank, granular organic fertilizer production line and powdery Organic fertilizer production line, the discharging of the raw material chopper
Mouthful it is connected with the feed inlet of the fermentation tank, the fermentation tank includes granular fermentation cabin and powdery fermentation cabin, and described granular have
Machine fertilizer production line includes Squeezinggranulator, screening machine, cooling equipment and the first measuring packing machine, the discharging of the granular fermentation cabin
Auger conveyor is equipped at mouthful, the discharge port of the auger conveyor is connected with the feed inlet of the Squeezinggranulator, described
The first conveying device is equipped between the discharge port of Squeezinggranulator and the feed inlet of the screening machine, the screening machine is equipped with coarse fodder
Mouthful and fines mouth, the coarse fodder mouth is connected with the feed inlet of the cooling equipment, the discharge port of the cooling equipment with it is described
First measuring packing machine is connected, and the powdery Organic fertilizer production line includes pulverizer, dryer and the second measuring packing machine, institute
State between the discharge port of powdery fermentation cabin and the feed inlet of dryer be equipped with the second conveying device, the discharge port of the dryer with
Second measuring packing machine is connected, and the fines mouth of the screening machine is connected with the feed inlet of the pulverizer, the powder
The discharge port of broken machine is connected with the feed inlet of the dryer.
Further, first conveying device and the second conveying device are belt conveyor.
Further, the cooling equipment is equipped with the Temperature Humidity Sensor of model SHT11, is set in the dryer
There are -2 type electronic type drimeters.
Further, the granular fermentation cabin is detachably mounted in the powdery fermentation cabin, the granular fermentation cabin
Side wall be equipped with several filter hole, the upper end of the granular fermentation cabin and powdery fermentation cabin is equipped with lid, runs through the lid
Body is equipped with the first agitating shaft, and the lid is equipped with the first driving motor and its output end is connected with first agitating shaft
It connects, the other end of first agitating shaft is located in the granular fermentation cabin and which is provided with screw type blade, described granular
The bottom end of fermentation cabin is equipped with weighing sensor, and the side wall of the powdery fermentation cabin is equipped with PTC ceramics heating plate and temperature sensing
The lower end of device, the powdery fermentation cabin is tapered, and the second agitating shaft is equipped with through the powdery fermentation cabin bottom side of the wall, and described the
One end bearing of two agitating shafts is connected on the side wall of the powdery fermentation cabin, and the other end of second agitating shaft is through described
The side wall of powdery fermentation cabin is connected with the second driving motor, and second agitating shaft is equipped with multiple template paddles, described
The discharge outlet activity of powdery fermentation cabin is plugged with sealing cover, and biologic ferment catalyst is additionally provided on the fermentation tank and is quantitatively conveyed
Device.
Further, the biologic ferment catalyst quantitative conveyer includes transparent storage box, is arranged described transparent
Scale on storage box side wall, the first discharge nozzle being connected with the upper end of the transparent storage box and with the transparent storage box
The second discharge nozzle for being connected of lower end, one end of first discharge nozzle is located at the inside of the transparent storage box, described
The other end of one discharge nozzle is arranged in the lid, and first discharge nozzle is equipped with multiple first nozzles, first spray
Head is respectively positioned on the upper end of the granular fermentation cabin, and first discharge nozzle is equipped with first pump housing, is set on second discharge nozzle
There are the first valve body and second pump housing, the outlet end of second discharge nozzle to be connect with the second nozzle, second nozzle is located at institute
It states in powdery fermentation cabin.
Further, controller is additionally provided on the outer wall of the fermentation tank, the controller is equipped with display screen, the title
It retransmits sensor and temperature sensor is electrically connected with the input terminal of the controller, the output end of the display screen and the controller
Electrical connection, the PTC ceramics heating plate are electrically connected by relay with the output end of the controller.
Further, the feed inlet of the discharge port Yu the auger conveyor of the granular fermentation cabin is fixed by flange and is connected
It connects, the second valve body is equipped at the feed inlet of the auger conveyor.
Compared with prior art, the utility model has the advantage that is with advantageous effect：
1, the production system of the biological organic fertilizer of the utility model includes powdery Organic fertilizer production line and granular organic fertilizer
Production line is carried out at the same time the production of different conditions biological organic fertilizer, and production efficiency is high, while in process of production crushing raw material
The technique for carrying out sieving in fermentation afterwards realizes granular feedstock and powder in fermentation process by the design to the jar structure that ferments
The separation and fermentation of shape raw material improves the fermentation efficiency of powder raw material, while effectively saving subsequent sieving technology flow, letter
While metaplasia production. art, the installation area occupied of entire biological organic fertilizer production line is made to reduce；
2, in the utility model by granular fermentation raw material extruder grain be organic fertilizer particles after sieve, grain will not met
The particle of shape organic fertilizer is further crushed, the organic fertilizer particles after crushing enter in dryer dried after powder is made
Shape organic fertilizer can be continual to not meeting granular organic fertilizer life on the basis of improving the production specification of granular organic fertilizer
The organic fertilizer particles of production specification are further processed, and improve the production efficiency of entire production technology.
Description of the drawings
Fig. 1 is a kind of flow chart of biological organic fertilizer production system of the utility model.
Fig. 2 is a kind of structural schematic diagram of the fermentation tank of biological organic fertilizer production system of the utility model.
In figure：1- raw material choppers；2- fermentation tanks；The granular fermentation cabins of 3-；4- powdery fermentation cabins；5- Squeezinggranulators；6-
Screening machine；7- cools down equipment；The first measuring packing machines of 8-；9- auger conveyors；10- pulverizers；11- dryers；12- second
Measuring packing machine；13- Temperature Humidity Sensors；14- drimeters；15- filter hole；16- lids；The first agitating shafts of 17-；18-
First driving motor；19- screw type blades；20- weighing sensors；21-PTC ceramic heating plates；22- temperature sensors；23-
Two agitating shafts；The second driving motors of 24-；25- template paddles；26- sealing covers；The transparent storage boxes of 27-；28- scales；29-
One discharge nozzle；The second discharge nozzles of 30-；The first nozzles of 31-；First pump housings of 32-；The first valve bodies of 33-；Second pump housings of 34-；35-
Two nozzles；36- controllers；The second valve bodies of 37-.
Specific implementation mode
It elaborates below in conjunction with the accompanying drawings to specific embodiment of the present utility model.
As depicted in figs. 1 and 2, a kind of biological organic fertilizer production system, including raw material chopper 1, fermentation tank 2, granular have
Machine fertilizer production line and powdery Organic fertilizer production line, the discharge port of the raw material chopper 1 are connected with the feed inlet of the fermentation tank 2
Logical, the fermentation tank 2 includes granular fermentation cabin 3 and powdery fermentation cabin 4, and the granular organic fertilizer production line includes Squeezinggranulator
5, screening machine 6,7 and first measuring packing machine 8 of cooling equipment, the discharge outlet of the granular fermentation cabin 3 are equipped with auger conveyor
9, the discharge port of the auger conveyor 9 is connected with the feed inlet of the Squeezinggranulator 5, and the Squeezinggranulator 5 goes out
The first conveying device is equipped between material mouth and the feed inlet of the screening machine 6, the three of S49 series may be used in the screening machine 6
Dimension spin vibration sieve extension set, the speed that this screening machine 6 replaces sieve is fast, can integrally provide production efficiency, the screening machine 6 is equipped with
Coarse fodder mouth and fines mouth, the coarse fodder mouth are connected with the feed inlet of the cooling equipment 7, the discharge port of the cooling equipment 7
It is connected with first measuring packing machine 8, the powdery Organic fertilizer production line includes pulverizer 10, the meter of dryer 11 and second
Packing machine 12 is measured, wherein dryer 11 is powdered rubber particle dedicated drying machine, the discharge port of the powdery fermentation cabin 4 and drying
The second conveying device, the discharge port of the dryer 11 and second measuring packing machine 12 are equipped between the feed inlet of machine 11
Be connected, the fines mouth of the screening machine 6 is connected with the feed inlet of the pulverizer 10, the discharge port of the pulverizer 10 with
The feed inlet of the dryer 11 is connected.
Further, first conveying device and the second conveying device are belt conveyor.
Further, the cooling equipment 7 is equipped with the Temperature Humidity Sensor 13 of model SHT11, the dryer 11
It is interior to be equipped with -2 type electronic type drimeters 14.
Further, the granular fermentation cabin 3 is detachably mounted in the powdery fermentation cabin 4, dismountable to connect
Mode includes being bolted or being connected by linking up with suspension, and convenient disassembly is conveniently replaceable the granular of different filtering specifications
The side wall of fermentation cabin, the granular fermentation cabin 3 is equipped with several filter hole 15, the granular fermentation cabin 3 and powdery fermentation cabin 4
Upper end be equipped with lid 16, through the lid 16 be equipped with the first agitating shaft 17, the lid 16 be equipped with the first driving motor
18 and its output end be connected with first agitating shaft 17, the other end of first agitating shaft 17 is located at the granular hair
In ferment storehouse 3 and screw type blade 19 is which is provided with, the bottom end of the granular fermentation cabin 3 is equipped with weighing sensor 20, convenient for note
Record initially enters the quality of the material of granular fermentation cabin 3, and biologic ferment catalyst, institute are proportionally added into be conveniently operated personnel
The side wall for stating powdery fermentation cabin 4 is equipped with PTC ceramics heating plate 21 and temperature sensor 22, realizes to temperature in fermentation tank 2
Control, the lower end of the powdery fermentation cabin 4 is tapered, and the second agitating shaft 23 is equipped with through 4 bottom side of the wall of powdery fermentation cabin,
One end bearing of second agitating shaft 23 is connected on the side wall of the powdery fermentation cabin 4, second agitating shaft 23 it is another
One end is connected through the side wall of the powdery fermentation cabin 4 with the second driving motor 24, and second agitating shaft 23 is equipped with more
The discharge outlet activity of a template paddle 25, the powdery fermentation cabin 4 is plugged with sealing cover 26, and the mode of activity grafting is：
The circumference of the discharge port of powdery fermentation cabin 4 is equipped with semicircle fixing groove, and the sealing cover 26 is plugged on described semicircle fixed
In slot, it is additionally provided with sealing ring on the upper surface of the sealing cover 26, the sealing performance of powdery fermentation cabin 4 is effectively ensured, prevents powder
Shape fermentation fertilizer leaks, and biologic ferment catalyst quantitative conveyer is additionally provided on the fermentation tank 2.
Further, the biologic ferment catalyst quantitative conveyer includes transparent storage box 27, is arranged described
Scale 28 on 27 side wall of bright storage box, the first discharge nozzle 29 being connected with the upper end of the transparent storage box 27 and with it is described
One end of the second discharge nozzle 30 that the lower end of transparent storage box 27 is connected, first discharge nozzle 29 is located at the transparent storage
The other end of the inside of case 27, first discharge nozzle 29 is arranged in the lid 16, and first discharge nozzle 29 is equipped with
Multiple first nozzles 31, first nozzle 31 are respectively positioned on the upper end of the granular fermentation cabin 3, are set on first discharge nozzle 29
There are first pump housing 32, second discharge nozzle 30 to be equipped with the first valve body 33 and second pump housing 34, second discharge nozzle 30
Outlet end is connect with the second nozzle 35, and second nozzle 35 is located in the powdery fermentation cabin 4.
Further, controller 36 is additionally provided on the outer wall of the fermentation tank 2, the controller 36 is XT-600w series
Intelligent digital temperature controller can effectively control the temperature in fermentation tank 2, and the controller is equipped with display screen, described
Weighing sensor 20 and temperature sensor 22 are electrically connected with the input terminal of the controller 36, the display screen and the control
The output end of device 36 is electrically connected, and the PTC ceramic heating plates 21 are electrically connected by relay with the output end of the controller.
Further, the feed inlet of the discharge port and the auger conveyor 9 of the granular fermentation cabin 3 is fixed by flange
It connects, the second valve body 37 is equipped at the feed inlet of the auger conveyor 9.
The production technology of the utility model includes the following steps：
Step (1)：Raw material crushes：Stalk is crushed to place in raw material chopper after weighing the weight of raw material stalk
Reason, the raw material after crushing enter in granular fermentation cabin, and the raw material for being partly less than filter hole in granular fermentation cabin enters powdery
In fermentation cabin；
Step (2)：Fermentation pretreatment：The weight in granular fermentation cabin weighed according to weighing sensor opens the first pump
Suitable biologic ferment catalyst is injected to by the first nozzle in granular fermentation cabin by body, while opening the first driving motor
10min is stirred to raw material, so that biologic ferment catalyst is sufficiently mixed with the raw material after crushing, and keep granular material further
The first starting weight for the stalk for entering in powdery fermentation cabin, while being weighed according to stalk initial weight and weighing sensor
The difference of amount is opened the first valve body and second pump housing, suitable biologic ferment catalyst is pumped into powdery fermentation cabin, simultaneously
The second driving motor is opened, powder raw material is stirred；
Step (3)：Fermentation：The first driving motor and the second driving motor are closed, opening temperature sensor and PTC ceramics add
Hot plate controls the temperature in fermentation tank at 70 DEG C -120 DEG C, after 2 hours of fermenting, starts the first driving motor, to granular hair
Raw material in fermentation tank stirs 0.5h, after so that granular material and granular material is completely separated, closes the first driving motor, opens second
Driving motor closes granular material stirring, ferments again after ten minutes；
Step (4)：The production of powdery organic fertilizer：In step (3) after powdery fermentation cabin fermentation 0.5h, powdery fermentation cabin is opened
Discharge port, open second conveyor structure, powdery fermentation raw material is delivered in dryer at 1200 DEG C and carries out drying and processing,
When the moisture that drimeter detects granular material is less than 20%, the discharge port of dryer is opened, powdery organic fertilizer is conveyed
It is packed in the second measuring packing machine, forms powdery organic fertilizer finished product；
Step (5)：The production of granular organic fertilizer：In step (3) after granular fermentation cabin fermentation 1h, the second valve body and spiral shell are opened
Conveyer is revolved, granular fermentation raw material is delivered to by auger conveyor in Squeezinggranulator and carries out granulation processing, is formed organic
Fertile particle, organic fertilizer particles are delivered in screening machine by the first conveying device and are sieved, the diameter of sieving plate in screening machine
For 6mm-7mm, organic fertilizer particles of the diameter more than 6mm-7mm, which enter in cooling equipment, to be cooled down, and Temperature Humidity Sensor is worked as
When detecting that the temperature of organic fertilizer particles is less than 40 DEG C, the discharge port of cooling equipment is opened, organic fertilizer particles are transported to first
It is packed in measuring packing machine, forms granular organic fertilizer finished product；
Step (6)：Organic fertilizer particles diameter entering in pulverizer less than 6mm-7mm in step (5) in screening machine
It crushes, is entered after crushing and carry out drying and processing in dryer.
Further, in step (1) filter hole a diameter of 8mm-10mm.
The production system of the biological organic fertilizer of the utility model includes powdery Organic fertilizer production line and granular organic fertilizer life
Producing line, is carried out at the same time the production of different conditions biological organic fertilizer, and production efficiency is high, while after in process of production crushing raw material
The technique sieved in fermentation realizes granular feedstock and powdery in fermentation process by the design to the jar structure that ferments
The separation and fermentation of raw material improves the fermentation efficiency of powder raw material, while effectively saving subsequent sieving technology flow, simplifies
While production technology, the installation area occupied of entire biological organic fertilizer production line is made to reduce.
Granular fermentation raw material extruder grain will not met granular to be sieved after organic fertilizer particles in the utility model
The particle of organic fertilizer is further crushed, the organic fertilizer particles after crushing enter in dryer dried after powdery is made
Organic fertilizer can be continual to not meeting granular organic fertilizer production on the basis of improving the production specification of granular organic fertilizer
The organic fertilizer particles of specification are further processed, and improve the production efficiency of entire production technology.
One embodiment of the utility model is described in detail above, but the content is only the utility model
Preferred embodiment should not be considered as limiting the scope of the present invention.It is all to be made according to application scope of the utility model
All the changes and improvements etc., should all still belong within the patent covering scope of the utility model.
Claims (7)
1. a kind of biological organic fertilizer production system, it is characterised in that：Including raw material chopper, fermentation tank, granular organic fertilizer production
Line and powdery Organic fertilizer production line, the discharge port of the raw material chopper are connected with the feed inlet of the fermentation tank, the hair
Fermentation tank includes granular fermentation cabin and powdery fermentation cabin, and the granular organic fertilizer production line includes Squeezinggranulator, screening machine, cooling
The discharge outlet of equipment and the first measuring packing machine, the granular fermentation cabin is equipped with auger conveyor, the auger conveyor
Discharge port is connected with the feed inlet of the Squeezinggranulator, the charging of the discharge port of the Squeezinggranulator and the screening machine
The first conveying device is equipped between mouthful, the screening machine is equipped with coarse fodder mouth and fines mouth, the coarse fodder mouth and the cooling equipment
Feed inlet be connected, the discharge port of the cooling equipment is connected with first measuring packing machine, the powdery organic fertilizer
Production line includes pulverizer, dryer and the second measuring packing machine, the charging of the discharge port and dryer of the powdery fermentation cabin
The second conveying device is equipped between mouthful, the discharge port of the dryer is connected with second measuring packing machine, the screening
The fines mouth of machine is connected with the feed inlet of the pulverizer, the feed inlet phase of the discharge port of the pulverizer and the dryer
Connection.
2. a kind of biological organic fertilizer production system according to claim 1, it is characterised in that：First conveying device and
Second conveying device is belt conveyor.
3. a kind of biological organic fertilizer production system according to claim 1, it is characterised in that：The cooling equipment is equipped with
The Temperature Humidity Sensor of model SHT11, the dryer is interior to be equipped with -2 type electronic type drimeters.
4. a kind of biological organic fertilizer production system according to claim 1, it is characterised in that：The granular fermentation cabin is removable
That unloads is fixed in the powdery fermentation cabin, and the side wall of the granular fermentation cabin is equipped with several filter hole, the granular hair
Ferment storehouse and the upper end of powdery fermentation cabin are equipped with lid, are equipped with the first agitating shaft through the lid, the lid is equipped with first
Driving motor and its output end is connected with first agitating shaft, the other end of first agitating shaft are located at described granular
In fermentation cabin and screw type blade is which is provided with, the bottom end of the granular fermentation cabin is equipped with weighing sensor, the powdery hair
The side wall in ferment storehouse is equipped with PTC ceramics heating plate and temperature sensor, and the lower end of the powdery fermentation cabin is tapered, through described
Powdery fermentation cabin bottom side of the wall is equipped with the second agitating shaft, and an end bearing of second agitating shaft is connected to the powdery fermentation cabin
Side wall on, the other end of second agitating shaft is connected through the side wall of the powdery fermentation cabin with the second driving motor,
Second agitating shaft is equipped with multiple template paddles, and the discharge outlet activity of the powdery fermentation cabin is plugged with sealing cover,
Biologic ferment catalyst quantitative conveyer is additionally provided on the fermentation tank.
5. a kind of biological organic fertilizer production system according to claim 4, it is characterised in that：The biologic ferment catalyst
Quantitative conveyer includes transparent storage box, is arranged on the transparent storage box side wall scale, with the transparent storage box
Upper end the first discharge nozzle being connected and the second discharge nozzle being connected with the lower end of the transparent storage box, described first goes out
One end of expects pipe is located at the inside of the transparent storage box, and the other end of first discharge nozzle is arranged in the lid, institute
It states the first discharge nozzle and is equipped with multiple first nozzles, first nozzle is respectively positioned on the upper end of the granular fermentation cabin, and described the
One discharge nozzle is equipped with first pump housing, and second discharge nozzle is equipped with the first valve body and second pump housing, second discharge nozzle
Outlet end connect with the second nozzle, second nozzle is located in the powdery fermentation cabin.
6. a kind of biological organic fertilizer production system according to claim 4, it is characterised in that：On the outer wall of the fermentation tank
It is additionally provided with controller, the controller is equipped with display screen, the weighing sensor and temperature sensor and the controller
Input terminal is electrically connected, and the display screen is electrically connected with the output end of the controller, and the PTC ceramics heating plate passes through relay
It is electrically connected with the output end of the controller.
7. a kind of biological organic fertilizer production system according to claim 1, it is characterised in that：The granular fermentation cabin goes out
Material mouth is fixedly connected with the feed inlet of the auger conveyor by flange, and second is equipped at the feed inlet of the auger conveyor
Valve body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820029348.7U CN207987056U (en) | 2018-01-09 | 2018-01-09 | A kind of biological organic fertilizer production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820029348.7U CN207987056U (en) | 2018-01-09 | 2018-01-09 | A kind of biological organic fertilizer production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207987056U true CN207987056U (en) | 2018-10-19 |
Family
ID=63819964
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820029348.7U Withdrawn - After Issue CN207987056U (en) | 2018-01-09 | 2018-01-09 | A kind of biological organic fertilizer production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207987056U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110015918A (en) * | 2018-01-09 | 2019-07-16 | 鑫宏润（天津）农业生物技术服务有限公司 | A kind of biological organic fertilizer production system and production technology |
-
2018
- 2018-01-09 CN CN201820029348.7U patent/CN207987056U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110015918A (en) * | 2018-01-09 | 2019-07-16 | 鑫宏润（天津）农业生物技术服务有限公司 | A kind of biological organic fertilizer production system and production technology |
| CN110015918B (en) * | 2018-01-09 | 2024-02-23 | 鑫宏润（天津）农业生物技术服务有限公司 | Bio-organic fertilizer production system and production process |
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