CN207285156U - A kind of no-antibiotics feed mechanized production system - Google Patents
A kind of no-antibiotics feed mechanized production system Download PDFInfo
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- CN207285156U CN207285156U CN201720964170.0U CN201720964170U CN207285156U CN 207285156 U CN207285156 U CN 207285156U CN 201720964170 U CN201720964170 U CN 201720964170U CN 207285156 U CN207285156 U CN 207285156U
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 28
- 239000003242 anti bacterial agent Substances 0.000 title claims abstract description 10
- 229940088710 antibiotic agent Drugs 0.000 title claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 40
- 239000000843 powder Substances 0.000 claims abstract description 39
- 239000011236 particulate material Substances 0.000 claims abstract description 35
- 238000011081 inoculation Methods 0.000 claims abstract description 31
- 238000002156 mixing Methods 0.000 claims abstract description 27
- 230000003750 conditioning effect Effects 0.000 claims abstract description 14
- 239000000463 material Substances 0.000 claims description 126
- 241000894006 Bacteria Species 0.000 claims description 40
- 239000000428 dust Substances 0.000 claims description 28
- 239000000203 mixture Substances 0.000 claims description 25
- 238000007599 discharging Methods 0.000 claims description 22
- 239000006148 magnetic separator Substances 0.000 claims description 19
- 238000006243 chemical reaction Methods 0.000 claims description 16
- 239000006185 dispersion Substances 0.000 claims description 14
- 230000003139 buffering effect Effects 0.000 claims description 13
- 238000012856 packing Methods 0.000 claims description 12
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 230000005611 electricity Effects 0.000 claims description 3
- 239000004615 ingredient Substances 0.000 claims description 3
- 241000273930 Brevoortia tyrannus Species 0.000 description 19
- 238000000034 method Methods 0.000 description 11
- 239000000047 product Substances 0.000 description 11
- 230000008569 process Effects 0.000 description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- 239000012535 impurity Substances 0.000 description 8
- 239000000654 additive Substances 0.000 description 7
- 230000000996 additive effect Effects 0.000 description 7
- 238000000855 fermentation Methods 0.000 description 7
- 230000004151 fermentation Effects 0.000 description 7
- 238000012545 processing Methods 0.000 description 6
- 241001465754 Metazoa Species 0.000 description 5
- 238000004140 cleaning Methods 0.000 description 4
- 229910052742 iron Inorganic materials 0.000 description 4
- 244000144972 livestock Species 0.000 description 4
- 239000002068 microbial inoculum Substances 0.000 description 4
- 230000003115 biocidal effect Effects 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 238000011161 development Methods 0.000 description 3
- 230000036541 health Effects 0.000 description 3
- 238000010298 pulverizing process Methods 0.000 description 3
- 230000000433 anti-nutritional effect Effects 0.000 description 2
- 238000009360 aquaculture Methods 0.000 description 2
- 244000144974 aquaculture Species 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 235000013601 eggs Nutrition 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000009472 formulation Methods 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 230000001360 synchronised effect Effects 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 210000001367 artery Anatomy 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000001079 digestive effect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 235000021393 food security Nutrition 0.000 description 1
- 210000001035 gastrointestinal tract Anatomy 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 230000036039 immunity Effects 0.000 description 1
- 239000002054 inoculum Substances 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 235000019629 palatability Nutrition 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
Abstract
The utility model discloses a kind of no-antibiotics feed mechanized production system, including particulate material conditioning department, particulate material break section, powder raw material conditioning department, feed proportioning workshop section, inoculation mixing workshop section.The utility model possesses the advantages of mechanization degree height, production process control exact automatic, adaptability to raw material is extensive, and product quality is stablized.
Description
Technical field
A kind of feed production equipment is the utility model is related to, belongs to feed manufacturing machine field, more particularly to a kind of nonreactive fermentation
Feed mechanized production system.
Background technology
In recent years, the animal husbandry in China is fast-developing, and livestock products yield increases year by year, while China's high-quality feed raw material
Resource provisioning but tends to be all the more nervous, and feedstuff cost remains high.
China is agricultural planting big country, and the yield of annual various agricultural and sideline products is up to several ten million tons, but most agriculture
The various anti-nutritional factors contained in byproduct sources can be to generations such as animal intestinal tract health, growth and development and breedings significantly not
Good influence, feed conversion are restricted, therefore cannot efficiently be utilized.Grain and feeding are striven in face of increasingly serious animal husbandry and people
The situation of the industrial quality raw materials insufficient supply of material, develops the agricultural and sideline product feed resource of China's abundant, improves feed conversion
Rate is extremely urgent.
On the other hand, aquaculture industry of China large-scale degree is very high, raiser's economic damage caused by order to reduce animal epidemic
Lose, largely antibiotic is generally used in aquaculture.As the herdings such as the raising of society Consciousness of food security, meat, eggs and milk are produced
The universal exceeded shade that has become people's health and can't get rid of of product antibiotic residue, nonreactive health livestock products have become this
The direction of a epoch inevitable development.
Commercial fermenting and producing fermented feed carries out agricultural and sideline product by microbial fermentation technology, can greatly degrade feeding
Expect the anti-nutritional factors in raw material, improve the nutritive value for improving feedstuff, fermented feed has good palatability, is rich in
Microorganism beneficial metabolic product, digestive utilization ratio is high, can improve the immunity of livestock and poultry animal, reduce the use of antibiotic, change
The quality of kind livestock meat egg product, the extensive production cost of raw material sources is relatively low, has very big development potentiality.
Fermented feed is more at present is produced and processed by semi-automatic equipment, and manual labor amount is big, and production process is difficult essence
Really control, it is more difficult to realize standardization, the unstable product quality produced, simple and crude processing combination is for various various traits original
The applicability of material is poor, it is impossible to makes full use of the local abundant special feedstuff resource of producer, this will seriously affect fermentation and raise
The efficient industrialized production of material.
The content of the invention
The purpose of this utility model is to provide a kind of no-antibiotics feed mechanized production system, which possesses
The advantages of mechanization degree is high, production process control exact automatic, adaptability to raw material is extensive, and product quality is stablized.
To achieve the above object, the solution of the utility model is：A kind of no-antibiotics feed mechanized production system,
Including particulate material conditioning department, particulate material break section, powder raw material conditioning department, feed proportioning workshop section, inoculation mixing
Workshop section, wherein：
The particulate material conditioning department by particulate material blanking hole, 1# pulse dust collectors, 1# elevators, 1# receiving sieves,
1# pipe magnetic separators, 1# threeways composition, 1# pulse dust collectors, which cheat particulate material blanking, carries out dedusting, particulate material blanking hole connection 1#
Machine inlet is lifted, 1# elevator discharge ports are sequentially connected 1# receiving sieves, 1# pipe magnetic separators and 1# threeways；
The particulate material break section is by upper level detector, feed bin to be comminuted, lower level detector, pneumatic gate valve, buffering bucket, change
Frequency rotary feeder, pulverizer, expansion chamber, material conveyor, auxiliary air draught pulse dust collector, 2# elevators composition, it is described to treat
The feed inlet for crushing feed bin is connected with the discharge port of 1# threeways, and the feed bin quantity to be comminuted has multiple, each feed bin to be comminuted
It is respectively provided with and installs level detector, lower level detector, pneumatic gate valve, the discharge port of feed bin to be comminuted is pooled to buffering bucket, buffering bucket
It is connected with frequency conversion rotary feeder, frequency conversion rotary feeder is arranged on above pulverizer and carries out uniform feeding, crushing to pulverizer
Machine, material conveyor, auxiliary air draught pulse dust collector are connected with expansion chamber respectively, and the material that pulverizer crushes is conveyed via material
Machine is delivered to the feed inlet of 2# elevators；
The powder raw material conditioning department by powder raw material blanking hole, 2# pulse dust collectors, 2# threeways, circular cone Powder screen,
2# pipe magnetic separators, 2# elevators composition, the 2# pulse dust collectors, which cheat powder raw material blanking, carries out dedusting, powder raw material blanking hole
2# lifting machine inlets are connected, 2# elevator discharge ports are sequentially connected 2# threeways, circular cone Powder screen, 2# pipe magnetic separators；
The ingredient station by 1# distributors, 2# distributors, upper level detector, batch bin, lower level detector, material blending auger, match somebody with somebody
Expect scale, claim door composition, the feed inlet of the 1# distributors is connected by 2# threeways with the discharge port of 2# elevators, the 2# distribution
The feed inlet of device is connected with the discharge port of 2# pipe magnetic separators, and the batch bin quantity has multiple, 1# distributors and 2# distributors difference
Multiple batch bins of corresponding connection, each batch bin are respectively provided with level detector, lower level detector and material blending auger, material blending auger discharging
Mouth is flexible coupling with burden balance, is set below burden balance and claims door；
The inoculation mixing workshop section is by dispensing surge bunker, apron quantitive conveyor, mixer, mixture surge bunker, inoculation material
Discharging machine, conical material dispersion cap, bacterium solution tank, flowmeter, bacterium solution pump, solenoid valve, disk jet head composition, the dispensing buffering
The title door of storehouse feed inlet connection burden balance, the apron quantitive conveyor are arranged on dispensing surge bunker lower part, and apron quantitive conveyor can be determined
When control, the feed inlet of the discharge port of apron quantitive conveyor and mixer connects, and the lower part of mixer sets mixture surge bunker,
Mixture surge bunker lower part sets inoculation material discharging machine, and the underface of mixer inside feed inlet sets conical material to disperse
Cap, conical material dispersion cap underface set disk jet head, the bacterium solution tank by pipeline successively with flowmeter, bacterium solution
Pump, solenoid valve are connected with disk jet head.
Preferably, automatic packing balance, the discharging of the feed inlet and inoculation material discharging machine of the automatic packing balance are further included
Mouth connection.
Preferably, the feed bin quantity to be comminuted has 2.
Preferably, the batch bin quantity has 6.
The utility model is using process：
When needing the particulate material of pulverization process in the raw material that production uses, particulate material is cheated from particulate material blanking
Cast, 1# pulse dust collectors cheat particulate material blanking and carry out dedusting, and particulate material to be comminuted is conveyed by 1# elevators, from 1#
Fallen into after discharging in elevator in 1# receiving sieves and clear up impurity, then material enters 1# pipe magnetic separators cleaning iron impurities, last clear
Manage clean material and fall into feed bin to be comminuted by 1# threeways, material is sent when the bed of material reaches level detector position in feed bin to be comminuted
Position alarm, switches 1# threeways at this time, and the material for making to clean out falls into another feed bin to be comminuted.Have in feed bin to be comminuted certain
During material stock, you can open 2# elevators, material conveyor, auxiliary air draught pulse dust collector, pulverizer, frequency conversion impeller feeding successively
Device, opens the pneumatic gate valve under feed bin to be comminuted, and material is fallen into frequency conversion rotary feeder by buffering bucket, is fed by frequency conversion impeller
Glassware uniformly feeds pulverizer, and pulverizer completes crushing material processing, and comminuting matter is fallen into expansion chamber, and material conveyor will
Comminuting matter is delivered in 2# elevators, and final comminuting matter enters after 2# threeways reach 1# distributors specifies in batch bin.
Aid in air draught pulse dust collector to carry out auxiliary air draught in the pulverizer course of work, improve the yield of pulverizer.
The utility model feed bin quantity preferably to be comminuted is 2, facilitates and is switched fast when reloading in production process, together
When also increase the capacity in storehouse to be comminuted, more materials can be stored, improve the work efficiency of pulverizer, save electricity consumption.
When having powder raw material in the raw material that production uses, switch 2# threeways, make 2# elevators discharge port and circular cone powder
The feed inlet of sieve is connected, and powder raw material is cast from powder raw material blanking hole, 2# pulse dust collectors powder raw material blanking is cheated into
Row dedusting, powder raw material are conveyed by 2# elevators, are fallen into after discharging from 2# elevators in circular cone Powder screen and are cleared up impurity, then
Material enters 2# pipe magnetic separators cleaning iron impurities, and the material finally cleaned out enters in 2# distributors, is then dispensed into
In the batch bin specified.
The utility model preferred formulations storehouse quantity is 6, while batch bin quantity obtains control reduction construction investment, 1#
The batch bin quantity that distributor and 2# distributors correspond to connection is enough.
According to the material formula gravimetric value set in dispensing scale control system, batch weigher control system automatically controls batch bin
In material successively by material blending auger add burden balance in, successively respectively reach setting into the weight of the various materials of batch weigher
Opened after value and claim door, material is fallen into dispensing surge bunker.
Before starting inoculation mixing, microbial inoculum is added in bacterium solution tank, according to the specified combined amount of mixer every batch of, if
Determine the time and the duration of runs of every batch of bacterium solution additive amount or bacterium solution pump of apron quantitive conveyor every batch of mixing cycle operating.
The duration of runs of every batch of apron quantitive conveyor determines the additive amount of material, and every batch of bacterium solution additive amount can be by flowing through
The stopping of the real-time traffic signal feedback control bacterium solution pump of flowmeter, can also be controlled by the duration of runs for controlling bacterium solution to pump.
Synchronous to open apron quantitive conveyor and bacterium solution pump when mixer starts running, feedstuff is quantitatively delivered machine and adds
Enter to mix in machine inlet, just fall in conical material dispersion cap, material is dispersed into along conical material dispersion cap edge
Cylindrical shape material curtain.
At this time, microbial inoculum is acted on by bacterium solution pump, is extracted from bacterium solution tank, and flows through flowmeter and solenoid valve,
Finally sprayed from disk jet head, the bacterium solution of ejection is rounded to scatter, and just even application disperses bacterium solution from conical material
On the cylindrical shape material curtain that cap edge is fallen, material is uniformly inoculated with.The time that apron quantitive conveyor has arrived setting stops conveying
Material, bacterium solution pump also stop, solenoid valve also close synchronously.Mixer is discharged into mixing after material mixing is completed, by inoculation material
Expect in surge bunker, mixer is further continued for repeating the process that hydrojet is inoculated with that as above feeds.
Start inoculation material discharging machine, inoculation material is vaccinated material discharging machine discharge mixture surge bunker.
Inoculation material discharging machine material is fallen into automatic packing balance, can carry out packing processing to material.Also it is extensible automatic
Packing scale, inoculation material is entered in fermentation tank or other containers by transfer tool to ferment.The mode of fermentation can be as needed
Flexibly choose.
The beneficial effects of the utility model are：
（1）Whole production system mechanization degree is high, it is possible to reduce manual labor, reduces human cost, improves work
Productivity.
（2）The inoculation control of production material dispensing is accurate.Proportioning materials are weighed to be claimed using electronic proportioning, material weighing dispensing essence
Degree is high.Bacterium solution inoculation can use timing and flowmeter feedback control two methods accurately to control bacterium solution additive amount, and every batch of is mixed
The material homogeneity of splice grafting kind is controllable, and each batch material of combined inoculation is consistent, and product quality stability is high.
（5）Adaptability to raw material is wide.The processing of the particulate material and powder raw material that need pulverization process is provided with process equipment
Process, and there is provided multiple batch bins, raw material composition can have more selection collocation, a variety of originals of selection that can be without misgivings
Material production.
Brief description of the drawings
Fig. 1 is the production equipment process flow chart of the utility model.
Fig. 2 is the artwork of inoculation mixing workshop section in the utility model.
Description of symbols in figure：
The blanking of 101- particulate materials is cheated；102-1# pulse dust collectors；103-1# elevators；104-1# receiving sieves；105-1#
Pipe magnetic separator；106-1# threeways；The blanking of 107- powder raw materials is cheated；108-2# pulse dust collectors；109-2# threeways；110- circular cone powders
Sieve；111-2# pipe magnetic separators；
The upper level detectors of 201-；202- feed bins to be comminuted；Level detector under 203-；204- pneumatic gate valves；205- buffering buckets；206-
Frequency conversion rotary feeder；207- pulverizers；208- expansion chambers；209- material conveyors；210- aids in air draught pulse dust collector；
211-2# elevators；
301-1# distributors；302-2# distributors；The upper level detectors of 303-；304- batch bins；Level detector under 305-；306- matches somebody with somebody
Expect auger；307- burden balance；308- claims door；
401- dispensing surge bunkers；402- apron quantitive conveyors；403- mixers；404- mixture surge bunkers；405- inoculums
Expect discharging machine；406- conical material dispersion caps；407- bacterium solution tanks；408- flowmeters；409- bacterium solutions pump；410- solenoid valves；411-
Disk jet head；
501- automatic packing balances.
Embodiment
The utility model is described in detail below in conjunction with the accompanying drawings.
As shown in Fig. 1~Fig. 2, a kind of no-antibiotics feed mechanized production system of embodiment of the utility model, including
Particulate material conditioning department, particulate material break section, powder raw material conditioning department, feed proportioning workshop section, inoculation mixing workshop section,
Wherein：
The particulate material conditioning department by particulate material blanking hole 101,1# pulse dust collectors 102,1# elevators 103,
1# receiving sieves 104,1# pipe magnetic separators 105,1# threeways 106 form, and 1# pulse dust collectors 102 carry out particulate material blanking hole 101
Dedusting, 101 connection 1# elevators of particulate material blanking hole, 103 feed inlet, 103 discharge port of 1# elevators are sequentially connected 1# receiving sieves
104th, 1# pipe magnetic separators 105 and 1# threeways 106；
The particulate material break section is by upper level detector 201, feed bin to be comminuted 202, lower level detector 203, pneumatic gate valve
204th, buffering bucket 205, frequency conversion rotary feeder 206, pulverizer 207, expansion chamber 208, material conveyor 209, auxiliary air draught arteries and veins
Rush deduster 210,2# elevators 211 form, the feed inlet of the feed bin 202 to be comminuted is connected with the discharge port of 1# threeways 106,
202 quantity of feed bin to be comminuted has multiple, and each feed bin 202 to be comminuted, which is respectively provided with, installs level detector 201, lower level detector
203rd, pneumatic gate valve 204, the discharge port of feed bin 202 to be comminuted are pooled to buffering bucket 205, and buffering bucket 205 is fed with frequency conversion impeller
Glassware 206 connects, frequency conversion rotary feeder 206 is arranged on the top of pulverizer 207 and carries out uniform feeding, crushing to pulverizer 207
Machine 207, material conveyor 209, auxiliary air draught pulse dust collector 210 are connected with expansion chamber 208 respectively, what pulverizer 207 crushed
Material is delivered to the feed inlet of 2# elevators 211 via material conveyor 209；
The powder raw material conditioning department is by powder raw material blanking hole 107,2# pulse dust collectors 108,2# threeways 109, circle
Cone Powder screen 110,2# pipe magnetic separators 111,2# elevators 211 form, and the 2# pulse dust collectors 108 cheat powder raw material blanking
107 carry out dedusting, 107 connection 2# elevators of powder raw material blanking hole, 211 feed inlet, and 211 discharge port of 2# elevators is sequentially connected
2# threeways 109, circular cone Powder screen 110,2# pipe magnetic separators 111；
The ingredient station is by 1# distributors 301,2# distributors 302, upper level detector 303, batch bin 304, lower level detector
305th, material blending auger 306, burden balance 307, claim door 308 to form, the feed inlets of the 1# distributors 301 by 2# threeways 109 with
The discharge port connection of 2# elevators 211, the feed inlet of the 2# distributors 302 is connected with the discharge port of 2# pipe magnetic separators 111, described
304 quantity of batch bin has multiple, 1# distributors 301 and 2# distributors 302 are connected respectively multiple batch bins 304, each
Batch bin 304 is respectively provided with level detector 303, lower level detector 305 and material blending auger 306,306 discharge port of material blending auger and burden balance
307 are flexible coupling, and the lower section of burden balance 307, which is set, claims door 308；
The inoculation mixing workshop section is by dispensing surge bunker 401, apron quantitive conveyor 402, mixer 403, mixture surge bunker
404th, material discharging machine 405, conical material dispersion cap 406, bacterium solution tank 407, flowmeter 408, bacterium solution pump 409, solenoid valve are inoculated with
410th, disk jet head 411 forms, the title door 308 of 401 feed inlet of the dispensing surge bunker connection burden balance 307, described quantitative
Conveyer 402 is arranged on 401 lower part of dispensing surge bunker, and apron quantitive conveyor 402 can be gone out with timing controlled, apron quantitive conveyor 402
Material mouth is connected with the feed inlet of mixer 403, and the lower part of mixer 403 sets mixture surge bunker 404, in mixture surge bunker
404 lower parts set inoculation material discharging machine 405, and the underface of 403 inside feed inlet of mixer sets conical material dispersion cap
406, disk jet head 411 is set in the underface of conical material dispersion cap 406, the bacterium solution tank 407 by pipeline successively with
Flowmeter 408, bacterium solution pump 409, solenoid valve 410 are connected with disk jet head 411.
Preferably, automatic packing balance 501, feed inlet and the inoculation material discharging machine of the automatic packing balance 501 are further included
405 discharge port connection.
Preferably, 202 quantity of feed bin to be comminuted has 2.
Preferably, 304 quantity of batch bin has 6.
The utility model is using process：
When needing the particulate material of pulverization process in the raw material that production uses, particulate material is cheated from particulate material blanking
101 cast, and 1# pulse dust collectors 102 carry out dedusting to particulate material blanking hole 101, and particulate material to be comminuted is by 1# elevators
103 conveyings, fall into 1# receiving sieves 104 after discharging from 1# elevators 103 and clear up impurity, then material enters 1# pipe magnetic separators
105 cleaning iron impurities, the material finally cleaned out fall into feed bin 202 to be comminuted, feed bin to be comminuted by 1# threeways 106
Material position alarm is sent when the bed of material reaches 201 position of level detector in 202, switches 1# threeways 106 at this time, makes the material cleaned out
Fall into another feed bin 202 to be comminuted.When having certain material stock in feed bin 202 to be comminuted, you can open successively 2# elevators 211,
Material conveyor 209, auxiliary air draught pulse dust collector 210, pulverizer 207, frequency conversion rotary feeder 206, open material to be comminuted
Pneumatic gate valve 204 under storehouse 202, material are fallen into frequency conversion rotary feeder 206 by buffering bucket 205, by frequency conversion impeller feeding
Device 206 uniformly feeds pulverizer 207, and pulverizer 207 completes crushing material processing, and comminuting matter is fallen into expansion chamber 208, thing
Comminuting matter is delivered in 2# elevators 211 by material conveyer 209, and final comminuting matter reaches 1# distributors through 2# threeways 109
Enter after 301 and specify in batch bin 304.Air draught pulse dust collector 210 is aided in carry out auxiliary suction in 207 course of work of pulverizer
Wind, improves the yield of pulverizer 207.
The utility model 202 quantity of feed bin preferably to be comminuted is 2, facilitates and is quickly cut when reloading in production process
Change, while also increase the capacity in storehouse 202 to be comminuted, more materials can be stored, improve the work effect of pulverizer 207
Rate, saves electricity consumption.
When having powder raw material in the raw material that production uses, switching 2# threeways 109, make 211 discharge port of 2# elevators and circle
The feed inlet for boring Powder screen 110 is connected, and powder raw material is cast from powder raw material blanking hole 107,2# pulse dust collectors 108 are to powder
Shape raw material blanking hole 107 carries out dedusting, and powder raw material is conveyed by 2# elevators 211, and circle is fallen into after discharging from 2# elevators 211
Impurity is cleared up in cone Powder screen 110, then material enters the cleaning iron impurities of 2# pipe magnetic separators 111, the material finally cleaned out
Into in 2# distributors 302, then it is dispensed into the batch bin 304 specified.
304 quantity of the utility model preferred formulations storehouse is 6, and 304 quantity of batch bin obtains control and reduces construction investment
Meanwhile 1# distributors 301 and 304 quantity of batch bin of the correspondence connection of 2# distributors 302 are enough.
According to the material formula gravimetric value set in 307 control system of burden balance, 307 control system of batch weigher automatically controls
Material in batch bin 304 is successively added in burden balance 307 by material blending auger 306, successively into the various materials of batch weigher 307
Weight respectively reach to open after setting value and claim door 308, material is fallen into dispensing surge bunker 401.
Before starting inoculation mixing, microbial inoculum is added in bacterium solution tank 407, it is specified mixed according to 403 every batch of of mixer
Resultant, the time of setting apron quantitive conveyor 402 every batch of mixing cycle operating and every batch of bacterium solution additive amount or bacterium solution pump 409
The duration of runs.
The duration of runs of every batch of apron quantitive conveyor 402 determines the additive amount of material, and every batch of bacterium solution additive amount can be by
The stopping of the real-time traffic signal feedback control bacterium solution pump 409 of flowmeter 408 is flowed through, also can be by controlling bacterium solution to pump 409 fortune
Turn the time to control.
When mixer 403 starts running, synchronous to open apron quantitive conveyor 402 and bacterium solution pump 409, feedstuff is quantified
Conveyer 402 is added in 403 feed inlet of mixer, is just fallen in conical material dispersion cap 406, material is dispersed into along taper
The cylindrical shape material curtain at 406 edge of material dispersion cap.
At this time, microbial inoculum is extracted, and flow through flowmeter 408 by the effect of bacterium solution pump 409 from bacterium solution tank 407
With solenoid valve 410, finally sprayed from disk jet head 411, the bacterium solution of ejection is rounded to scatter, and just even application exists bacterium solution
From the cylindrical shape material curtain that 406 edge of conical material dispersion cap is fallen, material is uniformly inoculated with.Apron quantitive conveyor 402 arrives
The time of setting stops conveying material, and bacterium solution pump 409 also stops, the also close synchronously of solenoid valve 410.Mixer 403 is completed
After material mixing, inoculation material is discharged into mixture surge bunker 404, mixer is further continued for repeating the hydrojet inoculation that as above feeds
Process.
Start inoculation material discharging machine 405, inoculation material is vaccinated material discharging machine 405 and discharges mixture surge bunker 404.
405 material of inoculation material discharging machine is fallen into automatic packing balance 501, can carry out packing processing to material.Also it is removable
Go out automatic packing balance 501, inoculation material is entered in fermentation tank or other containers by transfer tool to ferment.The mode of fermentation can be with
Flexibly choose as needed.
Claims (4)
- A kind of 1. no-antibiotics feed mechanized production system, it is characterised in that：Including particulate material conditioning department, particulate material Break section, powder raw material conditioning department, feed proportioning workshop section, inoculation mixing workshop section, wherein：The particulate material conditioning department by particulate material blanking hole, 1# pulse dust collectors, 1# elevators, 1# receiving sieves, 1# forever Magnetic cylinder, 1# threeways composition, 1# pulse dust collectors, which cheat particulate material blanking, carries out dedusting, particulate material blanking hole connection 1# liftings Machine inlet, 1# elevator discharge ports are sequentially connected 1# receiving sieves, 1# pipe magnetic separators and 1# threeways；The particulate material break section is by upper level detector, feed bin to be comminuted, lower level detector, pneumatic gate valve, buffering bucket, frequency conversion leaf Feeder, pulverizer, expansion chamber, material conveyor, auxiliary air draught pulse dust collector, 2# elevators composition are taken turns, it is described to be comminuted The feed inlet of feed bin is connected with the discharge port of 1# threeways, and the feed bin quantity to be comminuted has multiple, and each feed bin to be comminuted is all provided with Put and install level detector, lower level detector, pneumatic gate valve, the discharge port of feed bin to be comminuted is pooled to buffering bucket, and buffering bucket is with becoming The connection of frequency rotary feeder, frequency conversion rotary feeder are arranged on above pulverizer and carry out uniform feeding, pulverizer, thing to pulverizer Material conveyer, auxiliary air draught pulse dust collector are connected with expansion chamber respectively, and the material that pulverizer crushes is defeated via material conveyor Send to the feed inlet of 2# elevators；The powder raw material conditioning department by powder raw material blanking hole, 2# pulse dust collectors, 2# threeways, circular cone Powder screen, 2# forever Magnetic cylinder, 2# elevators composition, the 2# pulse dust collectors, which cheat powder raw material blanking, carries out dedusting, the connection of powder raw material blanking hole 2# lifts machine inlet, and 2# elevator discharge ports are sequentially connected 2# threeways, circular cone Powder screen, 2# pipe magnetic separators；The ingredient station by 1# distributors, 2# distributors, upper level detector, batch bin, lower level detector, material blending auger, burden balance, Claim door composition, the feed inlet of the 1# distributors is connected by 2# threeways with the discharge port of 2# elevators, the 2# distributors Feed inlet is connected with the discharge port of 2# pipe magnetic separators, and the batch bin quantity has multiple, and 1# distributors and 2# distributors correspond to respectively Multiple batch bins of connection, each batch bin are respectively provided with level detector, lower level detector and material blending auger, material blending auger discharge port with Burden balance are flexible coupling, and are set below burden balance and claim door；The inoculation mixing workshop section is by dispensing surge bunker, apron quantitive conveyor, mixer, mixture surge bunker, inoculation material discharging Machine, conical material dispersion cap, bacterium solution tank, flowmeter, bacterium solution pump, solenoid valve, disk jet head composition, the dispensing surge bunker into Material mouth connects the title door of burden balance, and the apron quantitive conveyor is arranged on dispensing surge bunker lower part, and apron quantitive conveyor can be with timing control System, the discharge port of apron quantitive conveyor and the feed inlet of mixer connect, and the lower part of mixer sets mixture surge bunker, is mixing Expect that surge bunker lower part sets inoculation material discharging machine, the underface of mixer inside feed inlet sets conical material dispersion cap, The underface of conical material dispersion cap sets disk jet head, and the bacterium solution tank is pumped with flowmeter, bacterium solution successively by pipeline, electricity Magnet valve is connected with disk jet head.
- A kind of 2. no-antibiotics feed mechanized production system as claimed in claim 1, it is characterised in that：Further include automatic bag Scale is filled, the feed inlet of the automatic packing balance is connected with being inoculated with the discharge port of material discharging machine.
- A kind of 3. no-antibiotics feed mechanized production system as claimed in claim 1, it is characterised in that：The material to be comminuted Storehouse quantity has 2.
- A kind of 4. no-antibiotics feed mechanized production system as claimed in claim 1, it is characterised in that：The batch bin number Amount has 6.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201720964170.0U CN207285156U (en) | 2017-08-03 | 2017-08-03 | A kind of no-antibiotics feed mechanized production system |
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| CN201720964170.0U CN207285156U (en) | 2017-08-03 | 2017-08-03 | A kind of no-antibiotics feed mechanized production system |
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| CN207285156U true CN207285156U (en) | 2018-05-01 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110089771A (en) * | 2019-06-06 | 2019-08-06 | 湖南良平农牧发展有限公司 | A kind of dregs of beans crushing hybrid system |
-
2017
- 2017-08-03 CN CN201720964170.0U patent/CN207285156U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110089771A (en) * | 2019-06-06 | 2019-08-06 | 湖南良平农牧发展有限公司 | A kind of dregs of beans crushing hybrid system |
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Effective date of registration: 20211222 Address after: 518101 Building 2, row 3, Shasan shangxiawei third industrial zone, Shajing street, Bao'an District, Shenzhen City, Guangdong Province Patentee after: RONGHUA UNITED BIOLOG SCIENCE Address before: 518106 No. 1, shangshijia Shangnan Industrial Zone, Gongming street, Guangming New District, Shenzhen, Guangdong Patentee before: SHENZHEN BAIAOFEI BIOTECHNOLOGY CO.,LTD. |
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Granted publication date: 20180501 |