CN107698292A - A kind of environment-friendly high-efficiency composite fertilizer synthesis production line - Google Patents
A kind of environment-friendly high-efficiency composite fertilizer synthesis production line Download PDFInfo
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- CN107698292A CN107698292A CN201711075689.4A CN201711075689A CN107698292A CN 107698292 A CN107698292 A CN 107698292A CN 201711075689 A CN201711075689 A CN 201711075689A CN 107698292 A CN107698292 A CN 107698292A
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- drying
- fine screen
- thermostatic tube
- screen
- discharging opening
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G1/00—Mixtures of fertilisers belonging individually to different subclasses of C05
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C3/00—Fertilisers containing other salts of ammonia or ammonia itself, e.g. gas liquor
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- 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
-
- 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
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/02—Applications of driving mechanisms, not covered by another subclass
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/04—Agitating, stirring, or scraping devices
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Pest Control & Pesticides (AREA)
- Fertilizers (AREA)
Abstract
The invention discloses a kind of environment-friendly high-efficiency composite fertilizer synthesis production line, it includes, material bin, the first spiral feed mechanism, the second spiral feed mechanism, granulation bowl, dilute sulfuric acid atomization gas container, ammonium aerosolization gas container, vapor body container, three gas input pipes, hydrate delivery pipe, hyrate container, the first drying mechanism, the 3rd spiral feed mechanism, first screen-dividing machine, disintegrating machine, the 5th spiral feed mechanism, the 3rd delivery pipe, the 4th spiral feed mechanism, fine screen thermostatic tube, the second drying mechanism；Fine screen thermostatic tube includes the first fine screen thermostatic tube and coating thermostatic tube；The present invention provides a kind of environment-friendly high-efficiency composite fertilizer synthesis production line, ingenious in design, easy to use, whole system is totally-enclosed system, not by natural environment influence, space is few, practical, saves energy consumption, production procedure realizes full-automation, cost is reduced, high yield rate, reduces the pollution to environment.
Description
Technical field
The present invention relates to a kind of production line, specially a kind of environment-friendly high-efficiency composite fertilizer synthesis production line.
Background technology
Existing composite fertilizer production line takes up an area about 1000 square meters, and working link is not the mode of operation of closing, in production process
Temperature, humidity by natural environment are influenceed greatly；Each link is banned using concentration and sends hot blast by pipeline after bituminous coal fired boiler heats
And vapor, all compounds for discharging gas are dispersed wantonly, particularly especially prominent in sunlight weather, so in production
Staff does not only exist major safety risks, can also be damaged to the body of staff；Traditional granulation cylinder only has one
Level roller and volume is big, diameter is in 1.2-1.5 rice, and for its utilization space 0.1% or so, wasting space is big, and cylinder is heavy, only limits
In a kind of constant rotating speed；Traditional Drying diameter length 18-20 rice, makes motor flog a dead horse mostly in 1.5-1.8 rice,
Cause cost high, both ends temperature difference is especially big in cylinder, and high temperature can be by product agglomerate, and low temperature causes dewatered drying not thorough, leads
Cause qualified products rate low；Because the opening of screening plant is to open wide upward, the not only dust containing toxin in screening process
It is uncontrollable to dance in the air also noise all over the sky, not still Manufacturing Worker's body damage, can also influence the normal life of neighbouring resident；
Whole equipment carrying and installation is extremely difficult, consumes a large amount of manpower, material resources and financial resources.
For disadvantages described above, a kind of environment-friendly high-efficiency composite fertilizer synthesis production line is designed.
The content of the invention
The purpose of the present invention is to be directed to problem above, there is provided a kind of environment-friendly high-efficiency composite fertilizer synthesis production line, solves biography
The composite fertilizer production line space of system is big, is controlled by the problem of natural environment influence is big, efficiency is low, production procedure hardly possible, cost
Height, yield rate is low, and environmental pollution is serious.
To realize object above, the technical solution adopted by the present invention is：A kind of environment-friendly high-efficiency composite fertilizer synthesis production line, it
Including material bin, the material bin connects with the first spiral feed mechanism, and the first spiral feed mechanism passes through pipeline
Connected with the second spiral feed mechanism；The second spiral feed mechanism passes through pipeline communication granulation bowl；The granulation
Three gas input pipes, the three gas input pipe and reservoir are communicated with roller, the container holds including dilute sulfuric acid atomization gas
Gas mixing enters granulation rolling simultaneously in device, ammonium aerosolization gas container, vapor body container, raw material and three gas input pipes
Cylinder；One end bottom of the granulation bowl is communicated with the first drying mechanism, first drying mechanism by the first delivery pipe with
3rd spiral feed mechanism connection；The 3rd spiral feed mechanism connects with first screen-dividing machine；The first screen-dividing machine
The second clout discharging opening connected with the feeding mouth of disintegrating machine, the discharging opening of disintegrating machine connects with the 5th spiral feed mechanism,
The 5th spiral feed mechanism connects with the first spiral feed mechanism；Second discharging opening of the first screen-dividing machine passes through
3rd delivery pipe connects with the 4th spiral feed mechanism, and the 4th spiral feed mechanism connects with fine screen thermostatic tube, institute
Stating fine screen thermostatic tube includes the first fine screen thermostatic tube and coating thermostatic tube；The first fine screen thermostatic tube is combined with coating thermostatic tube
Hydrate delivery pipe, the hydrate delivery pipe and hydrate reservoir, the coating thermostatic tube are connected with place
Connected with the second drying mechanism, second drying mechanism is identical, second drying with the first drying mechanism structure setting
Mechanism connects with finished product discharging opening.
Further, the granulation bowl includes the 3rd turbine worm reducer structure, the 3rd turbine worm reducer
Structure connects drum central axis, and first rotated together with drum central axis is disposed with from outside to inside on the drum central axis
Level roller, second level roller, third level roller, roller are provided with space from each other；The first order roller, second level rolling
Slow back-up ring during multiple granulations is provided with cylinder, third level roller；The first order roller, second level roller, third level roller
Into setting is tilted down, angle of inclination is 2 ° ~ 3 °；The first order roller, second level roller, the feed end of third level roller
Material separating disc is provided with, the material separating disc is along the circumferential direction divided into the sub-material room of three 120 ° of angles, three sub-materials by dividing plate
Room connects with space in first order roller, second level roller, third level roller respectively；The feed(raw material)inlet of the granulation bowl and remaining
Material clean-up port is separately positioned on the upper and lower side of material separating disc；Sky between the first order roller, second level roller, third level roller
Between connected after the other end is interconnected with the first discharging opening, the opposite end of first discharging opening is provided with the first suction opeing.
Further, first drying mechanism includes reducing motor, is connected with central principal axis on the reducing motor, institute
State and be provided with master gear on central principal axis at the both ends of the first drying mechanism, the master gear at both ends drives two driving cogs respectively
Wheel is rotated, and two travelling gears with one end are turned on the contrary, the travelling gear is arranged on the gear at the first drying mechanism both ends
In case, the travelling gear drives the Drying central rotating shaft being attached thereto to rotate respectively, is set on the Drying central rotating shaft
Drying shovel board telescopic shaft is equipped with, Drying shovel board is provided with the Drying shovel board telescopic shaft；Four Drying centers turn
The first Drying, the second Drying, the 3rd Drying, the 4th Drying are respectively arranged with axle；First Drying, second
Drying, the 3rd Drying, the 4th Drying are arranged on centered on central principal axis in four angles of square gearbox end surfaces, institute
The upper end for stating the first Drying is provided with semi-finished product entrance, and described first Drying one end connects one end of the second Drying, institute
One end that the second Drying other end connects the 3rd Drying is stated, the other end of the 3rd Drying connects the 4th Drying,
The bottom of 4th Drying is provided with woollen outlet；First Drying, the second Drying, the 3rd Drying, the 4th
The top of Drying is provided with for the hot air flow inlet tube toward heat air delivery stream in cylinder, the hot air flow inlet tube and hot blast
Flow input pipe connection；First Drying, the top of the second Drying are provided with the first exhaust column.
Further, the Drying shovel board telescopic shaft includes mandrel, and the Basolateral of the mandrel is provided with sleeve, institute
State and spring is provided with sleeve, the other end of the spring contacts with the bottom of mandrel；Distinguish with bottom on the top of the sleeve
It is provided with the first hex nut and the second hex nut.
Further, the first screen-dividing machine includes the first motor, and the output end of first motor is connected with the first whirlpool
Worm and gear reducing gear, central shaft is provided with the first turbine worm reducer structure；The other end of the central shaft is set
There is the first feeding pipe, the first pan feeding window is provided with first feeding pipe；The central shaft is in the first turbine worm reducer
Warm wind delivery pipe and warm wind porthole window are respectively arranged with structure end and center；Circular drum is provided with the outside of the central shaft,
One end of the roller is provided with the second discharging opening, and the other end is provided with the second clout discharging opening, and the inner side of the roller is set
There is taper fine screen mesh, the fine screen mesh taper small end is arranged on the second clout discharging opening side, taper is provided with the fine screen mesh
Wide-meshed screen, the wide-meshed screen taper small end are arranged on the second discharging opening side, and the big end of taper and the second clout of the wide-meshed screen go out
Material mouth connects, and the space between the circular drum and fine screen mesh also connects with the second clout discharging opening, second discharging opening
Connected with the big end of the taper of fine screen mesh；The second clout discharging opening opposite end is provided with the 3rd suction opeing.
Further, the first fine screen thermostatic tube includes the second motor, and the output end of second motor is connected with
Two turbine worm reducer structures, fine screen central shaft is provided with the second turbine worm reducer structure；The fine screen central shaft
Inside it is provided with hot blast conveying pipe；The other end of the fine screen central shaft is provided with the second feeding pipe, is set on second feeding pipe
It is equipped with the second pan feeding window；Second feeding pipe is arranged on one end of the first fine screen thermostatic tube；In the first fine screen thermostatic tube
Taper fine screen net is provided with, the taper small end of the fine screen net is arranged on the second feeding pipe side；The first fine screen thermostatic tube with
Coating thermostatic tube connects into an entirety by connecting baffle plate, and the big end of taper of the fine screen net is arranged on connection baffle plate；Institute
The top and bottom for stating the first fine screen thermostatic tube and the junction of coating thermostatic tube are respectively arranged with hyrate atomization entrance and powder
Last discharging opening；One end of the coating thermostatic tube is respectively arranged with the second suction opeing and the 3rd discharging opening up and down.
Further, the granulation bowl, the first drying mechanism, first screen-dividing machine, the first fine screen thermostatic tube, coating constant temperature
Cylinder is connected by exhaust column with air exhauster, and the exhaust column connects with clearing machine.
Further, the granulation bowl, the first drying mechanism, first screen-dividing machine, the first fine screen thermostatic tube, coating constant temperature
Cylinder is connected by pipeline with hot blast conveyer.
Further, the dilute sulfuric acid atomization gas container, ammonium aerosolization gas container, vapor body container, hydrate
The structure setting of thing container is identical；The dilute sulfuric acid atomization gas container includes long chamber and short cavity, and the side of the long chamber is set
Entrance is equipped with, the upper and lower side of the entrance is provided with level sensor；The long chamber is connected with short cavity by connecting hole, described
The lower end of short cavity is provided with electromagnetism furnace chamber, and the lower end of the long chamber is provided with hot-fluid cavity, and the top of the short cavity sets outlet
Mouthful；The electromagnetic oven intracavitary is provided with electromagnetic oven；Two opposite ends of the electromagnetism furnace chamber and hot-fluid cavity are respectively arranged with first
Thermovent and the second thermovent.
Further, high-temperature electromagnetic air valve and temperature control sensing contactor are each equipped with shunt conduit.
Beneficial effects of the present invention：
1st, present invention employs multistage granulation bowl, by the form of a traditional roller, three jacket casings has been changed to and have been combined
Form, add three times raw material granulation capacity, space is fully utilized.
2nd, present invention employs the transferring raw material of classification feed table to enter granulation cylinder, ensure that raw material in every one-level granulation cylinder
Uniform conveying.
3rd, present invention employs the mode that four Dryings are dried successively, material carrying system to convey for S-shaped, changes existing
There is the structure that single Drying is very long in technology.
4th, fine screen cylinder of the prior art and coating cylinder are merged into an entirety by the present invention, have saved space, are increased and decreased
Working procedure.
5th, the present invention uses totally-enclosed system, and each cylinder is provided with extractor fan, ensure that the gas circulation in cylinder, together
When can uniformly take waste gas away purified treatment.
6th, the finished product after coating of the present invention is dried again by drying mechanism, it is ensured that finished product does not have moisture, significantly
Extend the resting period of finished product.
7th, screeding device is provided with Drying of the present invention, screeding device has the function that transferring raw material, and scraper plate is being scraped
Flexible during cylinder, it is ensured that the removing of barrel slagging, effectively prevent from drying caking phenomenon.
8th, the present invention is ingenious in design, and easy to use, whole system is Full-enclosed constant-temp system, not by natural environment influence,
Space is few, practical, saves energy consumption, whole production procedure is realized full-automation, reduce cost, yield rate
Height, space about 38m2, bituminous coal fired boiler heating mode is banned completely, so as to reduce to pollution caused by environment.
Brief description of the drawings
Fig. 1 is first schematic three dimensional views of structure of the present invention.
Fig. 2 is second schematic three dimensional views of structure of the present invention.
Fig. 3 is 3rd schematic three dimensional views of structure of the present invention.
Fig. 4 is 4th schematic three dimensional views of structure of the present invention.
Fig. 5 is structure granulation bowl D profile schematic diagram of the present invention.
Fig. 6 is structure granulation bowl cross-section front view of the present invention.
Fig. 7 is the schematic three dimensional views of material separating disc in structure granulation bowl of the present invention.
Fig. 8 is the drying mechanism of structure first of the present invention（After 4th Drying removes）Schematic three dimensional views.
Fig. 9 is the first drying mechanism of structure cross-section front view of the present invention.
Figure 10 is Drying shovel board telescopic shaft cross-section front view in the drying mechanism of structure first of the present invention.
Figure 11 is the first screen-dividing machine schematic three dimensional views of structure of the present invention.
Figure 12 is the first screen-dividing machine three-dimensional cutaway view of structure of the present invention.
Figure 13 is the first screen-dividing machine cross-section front view of structure of the present invention.
Figure 14 is structure fine screen thermostatic tube schematic three dimensional views of the present invention.
Figure 15 is structure fine screen thermostatic tube cross-section front view of the present invention.
Figure 16 is structural container schematic three dimensional views of the present invention.
In figure：1st, material bin；2nd, the first spiral feed mechanism；3rd, the second spiral feed mechanism；4th, granulation bowl；5、
Container；6th, three gas input pipe；7th, three-way pipe；8th, the first drying mechanism；9th, the 3rd spiral feed mechanism；10th, first screen-dividing machine；
11st, the 3rd delivery pipe；12nd, hot blast conveyer；13rd, the 4th spiral feed mechanism；14th, fine screen thermostatic tube；15th, the 5th is spiral
Feed mechanism；16th, high-temperature electromagnetic air valve；17th, the second drying mechanism；18th, pipeline；19th, air exhauster；20th, exhaust column；21st, finished product
Discharging opening；22nd, hydrate container；23rd, hydrate delivery pipe；24th, the first delivery pipe；25th, disintegrating machine；401st, the 3rd turbine
Worm gear box；402nd, feed(raw material)inlet；403rd, material separating disc；40301st, dividing plate；40302nd, sub-material room；404th, clout clean-up port；
405th, drum central axis；Slow back-up ring when the 406th, pelletizing；407th, first order roller；408th, second level roller；409th, third level roller；
4010th, the first discharging opening；4011st, the first suction opeing；501st, sulfuric acid atomization gas container；502nd, ammonium aerosolization gas container；
503rd, vapor body container；50101st, entrance；50102nd, long chamber；50103rd, connecting hole；50104th, electromagnetic oven；50105th, short cavity；
50106th, gas outlet；50107th, the first thermovent；50108th, level sensor；50109th, the second thermovent；50110th, type of thermal communication
Chamber；50111st, electromagnetism furnace chamber；801st, reducing motor；802nd, master gear；803rd, semi-finished product entrance；804th, hot air flow inlet tube；
805th, Drying shovel board；806th, Drying central rotating shaft；807th, the first exhaust column；808th, travelling gear；809th, Drying shovel board
Telescopic shaft；80901st, mandrel；80902nd, the first hex nut；80903rd, the second hex nut；80904th, spring；80905th, cover
Cylinder；8010th, hot air flow input pipe；8011st, woollen exports；8012nd, the first Drying；8013rd, the second Drying；8014th, the 3rd
Drying；8015th, the 4th Drying；8016th, gear-box；8017th, central principal axis；1001st, the first feeding pipe；1002nd, first enters
Expect window；1003rd, roller；1004th, fine screen mesh；1005th, wide-meshed screen；1006th, central shaft；1007th, the first turbine worm reducer structure；
1008th, warm wind delivery pipe；1009th, the first motor；1010th, warm wind porthole window；1011st, the second discharging opening；1012nd, the second clout goes out
Material mouth；1013rd, the 3rd suction opeing；1401st, the second feeding pipe；1402nd, the first fine screen thermostatic tube；1403rd, hyrate atomization entrance；
1404th, the second pan feeding window；1405th, the second suction opeing；1406th, hot blast conveying pipe；1407th, the 3rd discharging opening；1408th, coating constant temperature
Cylinder；1409th, fine screen central shaft；14010th, baffle plate is connected；14011st, powder discharging opening；14012nd, fine screen net；14013rd, the second electricity
Machine；14014th, the second turbine worm reducer structure.
Embodiment
In order that those skilled in the art more fully understand technical scheme, the present invention is entered below in conjunction with the accompanying drawings
Row is described in detail, and the description of this subdivision is only exemplary and explanatory, should not there is any limitation to protection scope of the present invention
Effect.
As shown in Fig. 1-Figure 16, concrete structure of the invention is：
It includes material bin 1, and the material bin 1 connects with the first spiral feed mechanism 2, the first spiral feed mechanism
2 connect with the second spiral feed mechanism 3；The second spiral feed mechanism 3 connects granulation bowl 4；The granulation bowl 4
On be communicated with three gas input pipes 6, the three gas input pipe 6 connects with container 5, the container 5 include dilute sulfuric acid atomization gas hold
Device 501, ammonium aerosolization gas container 502, vapor body container 503, raw material enter simultaneously with gas mixing in three gas input pipes 6
Enter to granulation bowl 4；One end bottom of the granulation bowl 4 is communicated with the first drying mechanism 8, and first drying mechanism 8 is logical
The first delivery pipe 24 is crossed to connect with the 3rd spiral feed mechanism 9；The 3rd spiral feed mechanism 9 and first screen-dividing machine 10
Connection；Second clout discharging opening 1012 of the first screen-dividing machine 10 connects with the feeding mouth of disintegrating machine 25, and disintegrating machine 25 goes out
Material mouth connects with the 5th spiral feed mechanism 15, the 5th spiral 15 and first spiral feed mechanism 2 of feed mechanism
Connection；Second discharging opening 1011 of the first screen-dividing machine 10 is connected by the 3rd delivery pipe 11 and the 4th spiral feed mechanism 13
Logical, the 4th spiral feed mechanism 13 connects with fine screen thermostatic tube 14, and it is permanent that the fine screen thermostatic tube 14 includes the first fine screen
Warm cylinder 1402 and coating thermostatic tube 1408；The first fine screen thermostatic tube 1402 on the junction of coating thermostatic tube 1408 with being connected with
Hydrate delivery pipe 23, the hydrate delivery pipe 23 connect with hydrate container 22, the coating thermostatic tube 1408
Connected with the second drying mechanism 17, second drying mechanism 17 and the structure setting of the first drying mechanism 8 be it is identical, described second
Drying mechanism 17 connects with finished product discharging opening 21.
Preferably, the granulation bowl 4 includes the 3rd turbine worm reducer structure 401, and the 3rd turbine and worm slows down
Mechanism 401 connects drum central axis 405, is disposed with from outside to inside and drum central axis 405 on the drum central axis 405
First order roller 407, second level roller 408, the third level roller 409 rotated together, roller is provided with space from each other；Institute
Slow back-up ring 406 when stating first order roller 407, second level roller 408, multiple granulations are provided with third level roller 409；It is described
Into setting is tilted down, angle of inclination is 2 ° ~ 3 ° for first order roller 407, second level roller 408, third level roller 409；Institute
State first order roller 407, second level roller 408, the feed end of third level roller 409 and be provided with material separating disc 403, the material separating disc
403 are along the circumferential direction divided into the sub-material room 40302 of three 120 ° of angles by dividing plate 40301, and three sub-material rooms 40302 are distinguished
Connected with space in first order roller 407, second level roller 408, third level roller 409；The feed(raw material)inlet of the granulation bowl 4
402 and clout clean-up port 404 be separately positioned on the upper and lower side of material separating disc 403；The first order roller 407, second level roller
408th, the space between third level roller 409 connects after the other end is interconnected with the first discharging opening 4010, and described first goes out
The opposite end of material mouth 4010 is provided with the first suction opeing 4011.
Preferably, first drying mechanism 8 includes reducing motor 801, and center master is connected with the reducing motor 801
Axle 8017, master gear 802, the master gear at both ends are provided with the both ends of the first drying mechanism 8 on the central principal axis 8017
802 drive two travelling gears 808 to rotate respectively, and two travelling gears 808 with one end are turned on the contrary, the travelling gear
808 are arranged in the gear-box 8016 at the both ends of the first drying mechanism 8, and the travelling gear 808 drives the baking being attached thereto respectively
Dry cylinder central rotating shaft 806 is rotated, and Drying shovel board telescopic shaft 809, the drying are provided with the Drying central rotating shaft 806
Drying shovel board 805 is provided with cylinder shovel board telescopic shaft 809；The first baking is respectively arranged with four Drying central rotating shafts 806
Dry cylinder 8012, the second Drying 8013, the 3rd Drying 8014, the 4th Drying 8015；First Drying 8012, second
Drying 8013, the 3rd Drying 8014, the 4th Drying 8015 are arranged on square gear-box centered on central principal axis 8017
In four angles of 8016 end faces, the upper end of first Drying 8012 is provided with semi-finished product entrance 803, first Drying
8012 one end connect one end of the second Drying 8013, and the other end of the second Drying 8013 connects the 3rd Drying 8014
One end, the other end of the 3rd Drying 8014 connect the 4th Drying 8015, and the bottom of the 4th Drying 8015 is set
It is equipped with woollen outlet 8011；First Drying 8012, the second Drying 8013, the 3rd Drying 8014, the 4th Drying
8015 top is provided with for the hot air flow inlet tube 804 toward heat air delivery stream in cylinder, the hot air flow inlet tube 804 with
Hot air flow input pipe 8010 connects；First Drying 8012, the top of the second Drying 8013 are provided with the first exhausting
Pipe 807.
Preferably, the Drying shovel board telescopic shaft 809 includes mandrel 80901, and the Basolateral of the mandrel 80901 is set
Sleeve 80905 is equipped with, spring 80904, the other end and the mandrel 80901 of the spring 80904 are provided with the sleeve 80905
Bottom contact；The top of the sleeve 80905 is respectively arranged with the first hex nut 80902 and the second hex nut with bottom
80903。
Preferably, the first screen-dividing machine 10 includes the first motor 1009, the output end connection of first motor 1009
There is the first turbine worm reducer structure 1007, central shaft 1006 is provided with the first turbine worm reducer structure 1007；Institute
The other end for stating central shaft 1006 is provided with the first feeding pipe 1001, and the first pan feeding window is provided with first feeding pipe 1001
1002；The central shaft 1006 is respectively arranged with warm wind delivery pipe at the end of the first turbine worm reducer structure 1007 and center
1008 and warm wind porthole window 1010；The outside of the central shaft 1006 is provided with circular drum 1003, and the one of the roller 1003
End is provided with the second discharging opening 1011, and the other end is provided with the second clout discharging opening 1012, and the inner side of the roller 1003 is set
There is taper fine screen mesh 1004, the taper small end of fine screen mesh 1004 is arranged on the side of the second clout discharging opening 1012, the fine screen mesh
Taper wide-meshed screen 1005 is provided with 1004, the taper small end of wide-meshed screen 1005 is arranged on the side of the second discharging opening 1011, described
The big end of taper of wide-meshed screen 1005 connects with the second clout discharging opening 1012, between the circular drum 1003 and fine screen mesh 1004
Space also connected with the second clout discharging opening 1012, the big end of taper of second discharging opening 1011 and fine screen mesh 1004 connects
It is logical；The opposite end of second clout discharging opening 1012 is provided with the 3rd suction opeing 1013.
Preferably, the first fine screen thermostatic tube 1402 includes the second motor 14013, second motor 14013 it is defeated
Go out end and be connected with the second turbine worm reducer structure 14014, fine screen is provided with the second turbine worm reducer structure 14014
Central shaft 1409；Hot blast conveying pipe 1406 is provided with the fine screen central shaft 1409；The fine screen central shaft 1409 it is another
End is provided with the second feeding pipe 1401, and the second pan feeding window 1404 is provided with second feeding pipe 1401；Second pan feeding
Pipe 1401 is arranged on one end of the first fine screen thermostatic tube 1402；Taper fine screen net is provided with the first fine screen thermostatic tube 1402
14012, the taper small end of the fine screen net 14012 is arranged on the side of the second feeding pipe 1401；The first fine screen thermostatic tube 1402
An entirety is connected into by being connected baffle plate 14010 with coating thermostatic tube 1408, the big end of taper of the fine screen net 14012 is set
On connection baffle plate 14010；The first fine screen thermostatic tube 1402 and the top and bottom of the junction of coating thermostatic tube 1408
It is respectively arranged with hyrate atomization entrance 1403 and powder discharging opening 14011；One end of the coating thermostatic tube 1408 is divided up and down
The second suction opeing 1405 and the 3rd discharging opening 1407 are not provided with.
Preferably, the granulation bowl 4, the first drying mechanism 8, first screen-dividing machine 10, the first fine screen thermostatic tube 1402, bag
Film thermostatic tube 1408 is connected by exhaust column 20 with air exhauster 19, and the exhaust column 20 connects with clearing machine.
Preferably, the granulation bowl 4, the first drying mechanism 8, first screen-dividing machine 10, the first fine screen thermostatic tube 1402, bag
Film thermostatic tube 1408 is connected by pipeline 18 with hot blast conveyer 12.
Preferably, the dilute sulfuric acid atomization gas container 501, ammonium aerosolization gas container 502, vapor body container 503,
The structure setting of hydrate container 22 is identical；The dilute sulfuric acid atomization gas container 501 includes long chamber 50102 and short cavity
50105, the side of the long chamber 50102 is provided with entrance 50101, and the upper and lower side of the entrance 50101 is provided with water level biography
Sensor 50108；The long chamber 50102 is connected with short cavity 50105 by connecting hole 50103, and the lower end of the short cavity 50105 is set
There is electromagnetism furnace chamber 50111, the lower end of the long chamber 50102 is provided with hot-fluid cavity 50110, and the top of the short cavity 50105 is set
Put gas outlet 50106；Electromagnetic oven 50104 is provided with the electromagnetism furnace chamber 50111；The electromagnetism furnace chamber 50111 and type of thermal communication
Two opposite ends of chamber 50110 are respectively arranged with the first thermovent 50107 and the second thermovent 50109.
Preferably, high-temperature electromagnetic air valve 16 and temperature control sensing contactor are each equipped with shunt conduit.
When specifically used, a variety of solid feeds of composite fertilizer enter the first spiral feed mechanism 2 by material bin 1；By
Closed spiral pushing pattern is used in feed mechanism, makes raw material in course of conveying with raw material stirs, without weight
If agitating procedure.Raw material is sent into the second spiral feed mechanism 3 by the first spiral feed mechanism 2 in succession；It is spiral by second
Mixed material is sent into granulation bowl 4 by feed mechanism 3 in succession, while by dilute sulfuric acid atomization gas container 501, ammonium aerosolization gas
Container 502, vapor body container 503 are sent into dilute sour atomization gas of stream, ammonium aerosolization gas by three gas input pipes 6 and three-way pipe 7
Body and vapor body are to granulation bowl 4, and dilute sour atomization gas of stream, ammonium aerosolization gas and vapor body enter simultaneously with raw material
Granulation bowl 4, by setting the operating of timeliness and granulation bowl 4, mixed material is contained into glomeration particle.Due to granulation bowl
The 4 rotations inclination angle that granulation bowl 4 is installed in addition is combined with movement of falling object rule, particle is entered the first drying from top to bottom
Mechanism 8.First drying and dewatering is carried out to particle by setting time and temperature.First drying mechanism 8 is stretched using Drying shovel board
Contracting axle 809 connects Drying shovel board 805 and is used as power with reducing motor 801, and particle is stirred to rolling without a break makes particle as early as possible
Reach primary drying and dewatering purpose.Meanwhile particle is passed through into calmly the first Drying 8012, second in drying mechanism in an orderly manner
Enter the first delivery pipe 24 after Drying 8013, the 3rd Drying 8014, the 4th Drying 8015 and enter the using principle is slid
Three spiral feed mechanisms 9.Woollen is sent into first screen-dividing machine 10 and carries out first sub-sieve by the 3rd spiral feed mechanism 9, is passed through
First sub-sieve, finished product and defective work are separated.Defective work is sent to after the progress powder of disintegrating machine 25 by the 5th spiral immediately
Formula feed mechanism 15 is sent in the first spiral feed mechanism 2 of raw material material bin 1 again, again production granulation.Finished product is immediately
It is sent to the 3rd delivery pipe 11 of conveying and enters the 4th screw conveyer structure 13, first is pushed to by the 4th spiral feed mechanism 13
Fine screen thermostatic tube 1402 separates finished product and powder.Powder flows into the 5th spiral middle part of feed mechanism 15 in company with disintegrating machine immediately
Powder caused by 25 is sent to the first spiral feed mechanism 2 simultaneously；Finished product enters coating thermostatic tube 1408, while injects by aquation
Steam in the molten device 22 of compound delivers to coating thermostatic tube 1408 processed by hydrate delivery pipe 23 and carries out uniform coating, and coating is permanent
The warm rotation of cylinder 1408 makes finished particle rolling enter the second drying mechanism 17 so as to reach after atomization gas covers uniformly, dries again
Finished product after dry is packed.
The operation principle of granulation bowl 4：Such as Fig. 5, Fig. 6, shown in Fig. 7, the 3rd turbine worm reducer structure 401 drives roller
Central shaft 405 rotates, so as to drive first order roller 407, second level roller 408, third level roller 409 to rotate；Mixed material
The first order is respectively enterd by feed(raw material)inlet 402, material separating disc 403 with dilute sulfuric acid atomization gas, ammonium aerosolization gas, vapor body
Roller 407, second level roller 408, third level roller 409 carry out classification granulation；By the fortune for setting timeliness and granulation bowl 4
Turn, mixed material is contained into glomeration particle；Delay back-up ring 406 during granulation and extend particle time in cylinder；Lead to while granulation
The first suction opeing 4011 is crossed, exhaust column 20 connects with air exhauster 19, so as to ensure that the circulation of the gas in roller cylinder, extraction
Gas is unified in clearing machine and purified；Spherical particle after completing flows out from the first discharging opening 4010, accumulates over a long period
Dust then stay in clout clean-up port 404, later stage periodic maintenance cleaning, so as to complete whole pelletization.
The operation principle of first drying mechanism 8：As shown in Fig. 8, Fig. 9, Figure 10, reducing motor 801 drives 802 turns of master gear
Dynamic, the master gear 802 at both ends rotates together with drum central axis 405, then drives the travelling gear 808 at both ends to rotate, so as to
Drive Drying central rotating shaft 806 to rotate, realize the first Drying 8012, the second Drying 8013, the 3rd Drying 8014, the
The rotation of four Dryings 8015；Spherical particle enters the first Drying 8012 from semi-finished product entrance 803, in an orderly manner calmly by the
Two Dryings 8013, the 3rd Drying 8014, the 4th Drying 8015；The bottom of Drying shovel board telescopic shaft 809 is provided with bullet
Spring 80904, it is achieved thereby that Drying shovel board 805 is flexibly flexible, reaches flexibly to root out and be bonded at the first Drying 8012, the
Two Dryings 8013, the 3rd Drying 8014, the particle on the inwall of the 4th Drying 8015；Hot blast passes through hot air flow inlet tube
804th, hot air flow input pipe 8010 flows into the first Drying 8012, the second Drying 8013, the drying of the 3rd Drying the 8014, the 4th
In cylinder 8015；Particle after drying then flows into next process from woollen outlet 8011, and the first exhaust column 807 connects with air exhauster 19
It is logical, and the first Drying 8012 and the second Drying 8013 are connected, so as to realize to the first Drying 8012, the second Drying
8013rd, the circulation of the 3rd Drying 8014, gas in the 4th Drying 8015, the gas of extraction are uniformly sent to clearing machine progress
Evolution is handled.
The operation principle of first screen-dividing machine 10：As shown in Figure 11, Figure 12, Figure 13, the first motor 1009 and the first turbine snail
Bar reducing gear 1007 drives central shaft 1006 to rotate after connecting, so as to drive roller 1003 to rotate；The particle of last process from
First feeding pipe 1001 enters in roller 1003, and particle is screened for the first time by fine screen mesh 1004, wide-meshed screen 1005；Pass through
Warm wind delivery pipe 1008 conveys warm wind toward roller 1003 is interior.Qualified product is sieved between fine screen mesh 1004 and wide-meshed screen 1005
Space in, screen qualified particle for the first time and next process then flowed into by the second discharging opening 1011, sieved by fine screen mesh 1004
The particle in dust and wide-meshed screen 1005 divided then out enters disintegrating machine 25, air exhauster by the second clout discharging opening 1012
19 the 3rd suction opeings 1013 of connection.
The operation principle of fine screen thermostatic tube 14：As shown in Figure 14, Figure 15, the second motor 14013 subtracts with the second turbine and worm
Fast mechanism 14014 drives fine screen central shaft 1409 to rotate after connecting, so as to drive the first fine screen thermostatic tube 1402, coating thermostatic tube
1408 rotate；The particle of last process enters in the first fine screen thermostatic tube 1402 from the second feeding pipe 1401, passes through fine screen net
Entering coating thermostatic tube 1408 after 14012 fine screens choosing makes particle complete processing and fabricating.Pass through water in coating thermostatic tube 1408
Compound atomization entrance 1403 flows into hydrate steam, realizes coating；Connected by the air exhauster 19 of the second suction opeing 1405, so as to
The circulation to the gas in the first fine screen thermostatic tube 1402, coating thermostatic tube 1408 is realized, the gas of extraction is unified to enter purification
Machine carries out purified treatment；By hot blast conveying pipe 1406 to conveying warm wind, the first fine screen thermostatic tube 1402 in fine screen thermostatic tube 14
Sift out powder discharging opening 14011 and flow into the 5th spiral feed mechanism 15, finished product flows into the second drying from the 3rd discharging opening 1407
Mechanism 17.
The operation principle of container 5：As shown in figure 16, the aqueous solution enters long chamber 50102 by entrance 50101, passes through connection
Hole 50103 flow into short cavity 50105, electromagnetic oven 50104 to the aqueous solution in short cavity 50105 carry out heating produce steam, finally from
Flow out gas outlet 50106；Level sensor 50108 can detection reaches intelligent control in real time to water level in long chamber 50102；First dissipates
Hot mouth 50107, the second thermovent 50109 facilitate the circulation of intracavitary heat.
It should be noted that herein, term " comprising ", "comprising" or its any other become it should be noted that
Herein, term " comprising ", "comprising" or any other variant thereof is intended to cover non-exclusive inclusion, so that bag
To include process, method, article or the equipment of a series of elements not only include those key elements, but also including being not expressly set out
Other element, or also include for this process, method, article or the intrinsic key element of equipment.
Specific case used herein is set forth to the principle and embodiment of the present invention, the explanation of above example
It is only intended to help the method and its core concept for understanding the present invention.Described above is only the preferred embodiment of the present invention, should
When pointing out due to the finiteness of literal expression, and unlimited concrete structure objectively be present, for the common skill of the art
For art personnel, under the premise without departing from the principles of the invention, some improvement, retouching or change can also be made, can also incited somebody to action
Above-mentioned technical characteristic is combined by rights；These improve retouching, change or combination, or the not improved structure by invention
Think and technical scheme directly applies to other occasions, be regarded as protection scope of the present invention.
Claims (10)
1. a kind of environment-friendly high-efficiency composite fertilizer synthesis production line, it is characterised in that it includes material bin（1）, the material bin（1）With
First spiral feed mechanism（2）Connection, the first spiral feed mechanism（2）With the second spiral feed mechanism（3）Even
It is logical；The second spiral feed mechanism（3）Connect granulation bowl（4）；The granulation bowl（4）On be communicated with three gas input pipes
（6）, the three gas input pipe（6）With container（5）Connection, the container（5）Including dilute sulfuric acid atomization gas container（501）, ammonium
Aerosolization gas container（502）, vapor body container（503）, raw material and three gas input pipes（6）Interior gas mixing enters simultaneously
To granulation bowl（4）；The granulation bowl（4）One end bottom be communicated with the first drying mechanism（8）, first drying mechanism
（8）Pass through the first delivery pipe（24）With the 3rd spiral feed mechanism（9）Connection；The 3rd spiral feed mechanism（9）With
First screen-dividing machine（10）Connection；The first screen-dividing machine（10）The second clout discharging opening（1012）With disintegrating machine（25）Pan feeding
Mouth connection, disintegrating machine（25）Discharging opening and the 5th spiral feed mechanism（15）Connection, the 5th spiral feed mechanism
（15）With the first spiral feed mechanism（2）Connection；The first screen-dividing machine（10）The second discharging opening（1011）Pass through the 3rd
Delivery pipe（11）With the 4th spiral feed mechanism（13）Connection, the 4th spiral feed mechanism（13）With fine screen thermostatic tube
（14）Connection, the fine screen thermostatic tube（14）Including the first fine screen thermostatic tube（1402）With coating thermostatic tube（1408）；Described
One fine screen thermostatic tube（1402）With coating thermostatic tube（1408）Hydrate delivery pipe is connected with junction（23）, the aquation
Compound delivery pipe（23）With hydrate container（22）Connection, the coating thermostatic tube（1408）With the second drying mechanism（17）Even
It is logical, second drying mechanism（17）With the first drying mechanism（8）Structure setting is identical, second drying mechanism（17）With
Finished product discharging opening（21）Connection.
A kind of 2. environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 1, it is characterised in that the granulation rolling
Cylinder（4）Including the 3rd turbine worm reducer structure（401）, the 3rd turbine worm reducer structure（401）Connect centre of the drum
Axle（405）, the drum central axis（405）On be disposed with from outside to inside and drum central axis（405）Rotated together
One-level roller（407）, second level roller（408）, third level roller（409）, roller leaves space from each other；Described first
Level roller（407）, second level roller（408）, third level roller（409）Inside it is provided with slow back-up ring during multiple granulations（406）；Institute
State first order roller（407）, second level roller（408）, third level roller（409）Into setting is tilted down, angle of inclination is
2°~3°；The first order roller（407）, second level roller（408）, third level roller（409）Feed end be provided with material separating disc
（403）, the material separating disc（403）Pass through dividing plate（40301）Along the circumferential direction it is divided into the sub-material room of three 120 ° of angles
（40302）, three sub-material rooms（40302）Respectively with first order roller（407）, second level roller（408）, third level roller
（409）Interior space connection；The granulation bowl（4）Feed(raw material)inlet（402）With clout clean-up port（404）It is separately positioned on sub-material
Disk（403）Upper and lower side；The first order roller（407）, second level roller（408）, third level roller（409）Between space
In interconnected rear and the first discharging opening of the other end（4010）Connection, first discharging opening（4010）Opposite end be provided with
One suction opeing（4011）.
3. a kind of environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 1, it is characterised in that described first dries
Dry mechanism（8）Including reducing motor（801）, the reducing motor（801）On be connected with central principal axis（8017）, the center master
Axle（8017）On in the first drying mechanism（8）Both ends be provided with master gear（802）, the master gear at both ends（802）Band respectively
Move two travelling gears（808）Rotate, with two travelling gears of one end（808）Turn on the contrary, the travelling gear（808）If
Put in the first drying mechanism（8）The gear-box at both ends（8016）It is interior, the travelling gear（808）The baking being attached thereto is driven respectively
Dry cylinder central rotating shaft（806）Rotate, the Drying central rotating shaft（806）On be provided with Drying shovel board telescopic shaft（809）, institute
State Drying shovel board telescopic shaft（809）On be provided with Drying shovel board（805）；Four Drying central rotating shafts（806）Upper difference
It is provided with the first Drying（8012）, the second Drying（8013）, the 3rd Drying（8014）, the 4th Drying（8015）；Institute
State the first Drying（8012）, the second Drying（8013）, the 3rd Drying（8014）, the 4th Drying（8015）With center master
Axle（8017）Centered on be arranged on square gear-box（8016）In four angles of end face, first Drying（8012）Upper end
It is provided with semi-finished product entrance（803）, first Drying（8012）One end connects the second Drying（8013）One end, it is described
Second Drying（8013）The other end connects the 3rd Drying（8014）One end, the 3rd Drying（8014）The other end
Connect the 4th Drying（8015）, the 4th Drying（8015）Bottom be provided with woollen outlet（8011）；Described first
Drying（8012）, the second Drying（8013）, the 3rd Drying（8014）, the 4th Drying（8015）Top be provided with
For the hot air flow inlet tube toward heat air delivery stream in cylinder（804）, the hot air flow inlet tube（804）With hot air flow input pipe
（8010）Connection；First Drying（8012）, the second Drying（8013）Top be provided with the first exhaust column
（807）.
A kind of 4. environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 3, it is characterised in that the Drying
Shovel board telescopic shaft（809）Including mandrel（80901）, the mandrel（80901）Basolateral be provided with sleeve（80905）, institute
State sleeve（80905）Inside it is provided with spring（80904）, the spring（80904）The other end and mandrel（80901）Bottom connect
Touch；The sleeve（80905）Top and bottom be respectively arranged with the first hex nut（80902）With the second hex nut
（80903）.
5. a kind of environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 1, it is characterised in that described first point
Screen(ing) machine（10）Including the first motor（1009）, first motor（1009）Output end be connected with the first turbine worm reducer
Structure（1007）, the first turbine worm reducer structure（1007）Inside it is provided with central shaft（1006）；The central shaft（1006）
The other end be provided with the first feeding pipe（1001）, first feeding pipe（1001）On be provided with the first pan feeding window（1002）；
The central shaft（1006）In the first turbine worm reducer structure（1007）Warm wind delivery pipe is respectively arranged with end and center
（1008）With warm wind porthole window（1010）；The central shaft（1006）Outside be provided with circular drum（1003）, the roller
（1003）One end be provided with the second discharging opening（1011）, the other end is provided with the second clout discharging opening（1012）, the roller
（1003）Inner side be provided with taper fine screen mesh（1004）, the fine screen mesh（1004）Taper small end is arranged on the discharging of the second clout
Mouthful（1012）Side, the fine screen mesh（1004）Inside it is provided with taper wide-meshed screen（1005）, the wide-meshed screen（1005）Taper small end
It is arranged on the second discharging opening（1011）Side, the wide-meshed screen（1005）The big end of taper and the second clout discharging opening（1012）Even
It is logical, the circular drum（1003）With fine screen mesh（1004）Between space also with the second clout discharging opening（1012）Connection, institute
State the second discharging opening（1011）With fine screen mesh（1004）The connection of taper big end；The second clout discharging opening（1012）Opposite end
It is provided with the 3rd suction opeing（1013）.
A kind of 6. environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 1, it is characterised in that first essence
Sieve thermostatic tube（1402）Including the second motor（14013）, second motor（14013）Output end be connected with the second turbine snail
Bar reducing gear（14014）, the second turbine worm reducer structure（14014）Inside it is provided with fine screen central shaft（1409）；Institute
State fine screen central shaft（1409）Inside it is provided with hot blast conveying pipe（1406）；The fine screen central shaft（1409）The other end be provided with
Second feeding pipe（1401）, second feeding pipe（1401）On be provided with the second pan feeding window（1404）；Second feeding pipe
（1401）It is arranged on the first fine screen thermostatic tube（1402）One end；The first fine screen thermostatic tube（1402）Inside it is provided with taper essence
Screen cloth（14012）, the fine screen net（14012）Taper small end be arranged on the second feeding pipe（1401）Side；First fine screen
Thermostatic tube（1402）With coating thermostatic tube（1408）By connecting baffle plate（14010）Connect into an entirety, the fine screen net
（14012）The big end of taper be arranged on connection baffle plate（14010）On；The first fine screen thermostatic tube（1402）With coating thermostatic tube
（1408）Junction top and bottom be respectively arranged with hyrate atomization entrance（1403）With powder discharging opening（14011）；
The coating thermostatic tube（1408）One end up and down be respectively arranged with the second suction opeing（1405）With the 3rd discharging opening（1407）.
A kind of 7. environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 1, it is characterised in that the granulation rolling
Cylinder（4）, the first drying mechanism（8）, first screen-dividing machine（10）, the first fine screen thermostatic tube（1402）, coating thermostatic tube（1408）It is logical
Cross exhaust column（20）With air exhauster（19）Connection, the exhaust column（20）Connected with clearing machine.
A kind of 8. environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 1, it is characterised in that the granulation rolling
Cylinder（4）, the first drying mechanism（8）, first screen-dividing machine（10）, the first fine screen thermostatic tube（1402）, coating thermostatic tube（1408）It is logical
Piping（18）With hot blast conveyer（12）Connection.
A kind of 9. environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 1, it is characterised in that the dilute sulfuric acid
Atomization gas container（501）, ammonium aerosolization gas container（502）, vapor body container（503）, hydrate container（22）'s
Structure setting is identical；The dilute sulfuric acid atomization gas container（501）Including long chamber（50102）And short cavity（50105）, the length
Chamber（50102）Side be provided with entrance（50101）, the entrance（50101）Upper and lower side be provided with level sensor
（50108）；The long chamber（50102）And short cavity（50105）Pass through connecting hole（50103）Connection, the short cavity（50105）Under
End is provided with electromagnetism furnace chamber（50111）, the long chamber（50102）Lower end be provided with hot-fluid cavity（50110）, the short cavity
（50105）Top set gas outlet（50106）；The electromagnetism furnace chamber（50111）Inside it is provided with electromagnetic oven（50104）；It is described
Electromagnetism furnace chamber（50111）With hot-fluid cavity（50110）Two opposite ends be respectively arranged with the first thermovent（50107）Dissipated with second
Hot mouth（50109）.
10. a kind of environment-friendly high-efficiency composite fertilizer synthesis production line according to claim 1, it is characterised in that in shunt conduit
It is each equipped with high-temperature electromagnetic air valve（16）Sense contactor with temperature control.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711075689.4A CN107698292A (en) | 2017-11-06 | 2017-11-06 | A kind of environment-friendly high-efficiency composite fertilizer synthesis production line |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711075689.4A CN107698292A (en) | 2017-11-06 | 2017-11-06 | A kind of environment-friendly high-efficiency composite fertilizer synthesis production line |
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| CN107698292A true CN107698292A (en) | 2018-02-16 |
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ID=61177874
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Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203639360U (en) * | 2013-12-31 | 2014-06-11 | 湖北鄂中化工有限公司 | Slow/controlled-release fertilizer production system |
| CN104211547A (en) * | 2014-08-11 | 2014-12-17 | 武汉中农国际贸易有限公司 | Compound fertilizer production system and production process thereof |
| CN204699781U (en) * | 2015-06-15 | 2015-10-14 | 四川省眉山益稷农业科技有限公司 | A kind of fertilizer cylinder granulation dispensing apparatus |
| CN206104315U (en) * | 2016-08-25 | 2017-04-19 | 湖北鄂东肥业有限公司 | Fertilizer divides sieve equipment |
-
2017
- 2017-11-06 CN CN201711075689.4A patent/CN107698292A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203639360U (en) * | 2013-12-31 | 2014-06-11 | 湖北鄂中化工有限公司 | Slow/controlled-release fertilizer production system |
| CN104211547A (en) * | 2014-08-11 | 2014-12-17 | 武汉中农国际贸易有限公司 | Compound fertilizer production system and production process thereof |
| CN204699781U (en) * | 2015-06-15 | 2015-10-14 | 四川省眉山益稷农业科技有限公司 | A kind of fertilizer cylinder granulation dispensing apparatus |
| CN206104315U (en) * | 2016-08-25 | 2017-04-19 | 湖北鄂东肥业有限公司 | Fertilizer divides sieve equipment |
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