CN207285158U - A kind of high-performance bio fermentation liquid diets production line - Google Patents

A kind of high-performance bio fermentation liquid diets production line Download PDF

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Publication number
CN207285158U
CN207285158U CN201720964584.3U CN201720964584U CN207285158U CN 207285158 U CN207285158 U CN 207285158U CN 201720964584 U CN201720964584 U CN 201720964584U CN 207285158 U CN207285158 U CN 207285158U
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feed
particulate
comminuted
level detector
elevators
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王玲玲
刘建华
朱玉华
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Shenzhen One Hundred Fly Biological Technology Co Ltd
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Shenzhen One Hundred Fly Biological Technology Co Ltd
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Abstract

The utility model discloses a kind of high-performance bio fermentation liquid diets production line, including particulate material conditioning department, particulate material break section, powder raw material conditioning department, feed proportioning workshop section, mixing crushing section, liquid addition workshop section.The utility model mechanization degree is high, and the degree of automation is high, and production process control is accurate, product quality stability is high, and adaptability to raw material is wide, and the mixture homogeneity of wet fermentation feed and dry and wet mixed fodder is high, it is good for the applicability of various various trait raw materials, it is possible to achieve a variety of production processing need.

Description

A kind of high-performance bio fermentation liquid diets production line
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 high-performance bio Ferment liquid diets production line.
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.
There is the type of two kinds of mainstreams in fermented feed product, a kind of is the fermented feed after drying process, and another kind is not With dry wet fermentation feed.
Because wet fermentation feed does not have to drying process, the larger drying cost of energy consumption is eliminated, while because without drying Processing, the high activity beneficial bacterium in product can be fully retained, will not caused by drying process partial loss.But due to wet hair Ferment feed product water content is larger, in use, adds easy conglomeration in other dry feedstuffs, causes mixing uneven Even, end product quality is unstable, and the application effect of cultivating link is difficult to control.
Meanwhile production fermented feed is more by semi-automatic equipment production and processing at present, manual labor amount is big, produces Journey is difficult accurately to control, the unstable product quality produced, and simple and crude processing combination is for the suitable of various various trait raw materials It is poor with property, it is impossible to make full use of the local abundant special feedstuff resource of producer, this will seriously affect the height of fermented feed Imitate industrialized production.
The content of the invention
The purpose of this utility model is to provide a kind of high-performance bio fermentation liquid diets production line, which possesses Mechanization degree is high, and the degree of automation is high, and production process control is accurate, and product quality stability is high, and adaptability to raw material is wide, wet hair The mixture homogeneity of ferment feed and dry and wet mixed fodder is high, good for the applicability of various various trait raw materials, it is possible to achieve more The advantages of kind production processing needs.
To achieve the above object, the solution of the utility model is:A kind of high-performance bio fermentation liquid diets production line, It is broken including particulate material conditioning department, particulate material break section, powder raw material conditioning department, feed proportioning workshop section, mixing Workshop section, liquid addition 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 Material scale, claim feed intake blanking hole, hand of door, hand to feed intake deduster composition, and the feed inlet of the 1# distributors is carried by 2# threeways with 2# The discharge port connection of the machine of liter, the feed inlet of the 2# distributors are connected with the discharge port of 2# pipe magnetic separators, and the batch bin quantity has Multiple batch bins multiple, that 1# distributors and 2# distributors are connected respectively, each batch bin are respectively provided with level detector, blanking Position device and material blending auger, material blending auger discharge port are flexible coupling with burden balance, are set below burden balance and claim door, above burden balance It is provided with that hand feeds intake blanking hole and hand feeds intake deduster;
The mixing crushing section is made of mixer, mixture surge bunker, material scattering machine, finished product discharging machine, is mixed Machine lower part sets mixture surge bunker, and material scattering machine is set between mixture surge bunker and finished product discharging machine;
Liquid add workshop section by bacterium solution tank, flowmeter, bacterium solution pump, solenoid valve block into, bacterium solution tank by pipeline and flowmeter, Bacterium solution pump, solenoid valve connection, and finally it is switched to mixer.
Preferably, the feed bin quantity to be comminuted has 2.
Preferably, the batch bin quantity has 6.
Preferably, the finished product discharging machine is double-shaft paddle formula conveyer.
Preferably, the finished product discharging machine from feed inlet to discharge outlet in the state set from high to low.
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.
Start inoculation mixing before, by microbial inoculum add bacterium solution tank in, will according to the specified combined amount of mixer every batch of, Burden balance every batch of dispensing inventory is set, sets every batch of bacterium solution additive amount.
When starting inoculation mixing, the material that dispensing is completed is released the mixer fallen into operating condition by burden balance from title door It is interior, open bacterium solution and pump, the microbial inoculum in bacterium solution tank flows through flowmeter, is pumped by bacterium solution, sprays into mixer, when flowmeter is real When measuring the microbial bacteria liquid measure that flows through and being equal to setting additive amount, feedback control stops bacterium solution pump and closes solenoid valve.Mixing Machine continuous service, microbial inoculum are sufficiently mixed with feedstuff.
Inoculation material is discharged into mixture surge bunker, mixer is further continued for repeating by mixer after material mixing is completed As above feed the process that hydrojet is inoculated with.
Start finished product discharging machine material scattering machine, inoculation material is broken up, most when flowing through material scattering machine by Mechanical Crushing The material of homogeneous no agglomerate is discharged from the double-shaft paddle formula finished product discharging machine being obliquely installed afterwards, since discharging machine is to be obliquely installed Double-shaft paddle formula set, using material gravity flow act on, inoculation material can smoothly be discharged from discharging machine, discharge at the same time Double-shaft paddle in machine further will mix inoculation material while material is conveyed, and ensure the mixed of inoculation material The uniformity is closed, the inoculation material of discharge can be entered in fermentation tank or other containers by transfer tool to ferment.The mode of fermentation Can flexibly it choose as needed.
After the completion of wet fermentation feed fermentation, it is necessary to be added mixed in other dry materials when, can need to Dry material to be processed is put into from powder raw material blanking hole, is lifted through 2# elevators, and material enters batch bin from 1# distributors It is interior, after material blending auger and the accurate batch of burden balance weigh, scale door is opened, dry material enters in mixer.Since wet fermentation is raised Expect that the ratio of addition is generally little, the adding proportion of dry material is added according to wet fermentation feed, weighs the weight that meets the requirements by hand Wet fermentation feed, from hand feed intake blanking hole in put into, open hand feed intake deduster carry out dust removal process.
Wet fermentation feed enters in mixer, and dry material is sufficiently mixed with wet fermentation finished feed in mixer, mixing Dry and wet mixture is discharged into mixture surge bunker by machine after material mixing is completed, and mixer is further continued for repeating as above dry and wet thing Expect mixed process.
Start finished product discharging machine and material scattering machine, dry and wet mixture are beaten when flowing through material scattering machine by Mechanical Crushing Dissipate, this step eliminates the dry and wet material agglomerate that mixed process produces in mixer, and the material of last homogeneous no agglomerate is from inclining Discharge in the double-shaft paddle formula finished product discharging machine tiltedly set, since discharging machine is that the double-shaft paddle formula being obliquely installed is set, utilize The gravity flow effect of material, dry and wet mixture can be discharged smoothly from discharging machine, while the double-shaft paddle in discharging machine is defeated While sending material, further dry and wet material will be mixed, and ensure the mixture homogeneity of dry and wet material.Such a material Shape is homogeneous, and the high material of mixture homogeneity meets the raising need of raiser.
The beneficial effects of the utility model are:
(1)Production system mechanization degree is high, it is possible to reduce manual labor, reduces human cost, improves work production Rate.
(2)Production process control is accurate.Proportioning materials are weighed to be claimed using electronic proportioning, and material weighing proportioning accuracy is high.Bacterium Liquid inoculation is controlled using flowmeter, and bacterium solution additive amount is more accurate, and the material homogeneity of every batch of combined inoculation is controllable, and mixing connects The each batch material of kind is consistent, and product quality stability is high.
(3)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.
(4)The mixture homogeneity of wet fermentation feed and dry and wet mixed fodder is high, and product quality is stablized.By setting material to beat Dissipate machine and mechanical examination carried out to material, crush the agglomerate in wet fermentation Feed Manufacturing and dry and wet material mixture manufacturing material, make by It is more homogeneous to handle material.Handled by the double-shaft paddle formula finished product discharging machine being obliquely installed, wet fermentation feed can be promoted to give birth to Production it is homogeneous, the homogeneity of dry and wet material mixture manufacturing can also be promoted, the quality of wet fermentation feed and dry and wet mixture is opposite The situation of other simple and crude processing combinations productions, the product quality produced is more secure, at the same the utility model for it is various not Applicability with character raw material is good, it is possible to achieve a variety of production processing need.
Brief description of the drawings
Fig. 1 is the production technological process of the utility model.
Fig. 2 is the schematic cross-section of finished product discharging machine in the utility model.
Fig. 3 is the top view of finished product discharging machine inlet 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;309- hands feed intake blanking hole;310- hands feed intake deduster;
401- mixers;402- mixture surge bunkers;403- material scattering machines;404- finished product discharging machines;
501- bacterium solution tanks;502- flowmeters;503- bacterium solutions pump;504- solenoid valves.
Embodiment
The utility model is described in detail below in conjunction with the accompanying drawings.
As shown in FIG. 1 to 3, a kind of high-performance bio fermentation liquid diets production line of the embodiment of the utility model, including Particulate material conditioning department, particulate material break section, powder raw material conditioning department, feed proportioning workshop section, mixing crushing section, Liquid adds 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, hand blanking hole 309, the hand deduster 310 that feeds intake that feeds intake to form, the 1# The feed inlet of distributor 301 is connected by 2# threeways 109 with the discharge port of 2# elevators 211, the charging of the 2# distributors 302 Mouth is connected with the discharge port of 2# pipe magnetic separators 111, and 304 quantity of batch bin has multiple, 1# distributors 301 and 2# distributors 302 The multiple batch bins 304 being connected respectively, each batch bin 304 are respectively provided with level detector 303, lower level detector 305 and dispensing Auger 306,306 discharge port of material blending auger are flexible coupling with burden balance 307, and the lower section of burden balance 307, which is set, claims door 308, dispensing The top of scale 307 is provided with that hand feeds intake blanking hole 309 and hand feeds intake deduster 310;
The mixing crushing section is by mixer 401, mixture surge bunker 402, material scattering machine 403, finished product discharging machine 404 compositions, 401 lower part of mixer sets mixture surge bunker 402, between mixture surge bunker 402 and finished product discharging machine 404 Material scattering machine 403 is set;
Liquid adds workshop section and is made of bacterium solution tank 501, flowmeter 502, bacterium solution pump 503, solenoid valve 504, and bacterium solution tank 501 is logical Piping connects with flowmeter 502, bacterium solution pump 503, solenoid valve 504, and is finally switched to mixer 401.
Preferably, 202 quantity of feed bin to be comminuted has 2.
Preferably, 304 quantity of batch bin has 6.
Preferably, the finished product discharging machine 404 is double-shaft paddle formula conveyer.
Preferably, the finished product discharging machine 404 from feed inlet to discharge outlet in the state set from high to low.
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 501, will be specified according to 401 every batch of of mixer Combined amount, sets 307 every batch of dispensing inventory of burden balance, sets every batch of bacterium solution additive amount.
When starting inoculation mixing, the material that dispensing is completed is released and fallen into operating condition by burden balance 307 from title door 308 In mixer 401, bacterium solution pump 503 is opened, the microbial inoculum in bacterium solution tank 501 flows through flowmeter 501, pumps 503 by bacterium solution, spray Enter in mixer 401, when flowmeter 502 measures the microbial bacteria liquid measure flowed through equal to setting additive amount in real time, feedback control Stop bacterium solution pump 503 and close solenoid valve 504.401 continuous service of mixer, microbial inoculum are sufficiently mixed with feedstuff.
Inoculation material is discharged into mixture surge bunker 402, mixer 401 is again by mixer 401 after material mixing is completed Continue to repeat the process that hydrojet is inoculated with that as above feeds.
Start finished product discharging machine 404 and material scattering machine 403, inoculation material is mechanical when flowing through material scattering machine 403 Broken to break up, the material of last homogeneous no agglomerate is discharged from the double-shaft paddle formula finished product discharging machine 404 being obliquely installed, due to going out Material machine 404 is that the double-shaft paddle formula being obliquely installed is set, and is acted on using the gravity flow of material, inoculation material can be smoothly from discharging Discharged in machine 404, while the double-shaft paddle in discharging machine 404 further will carry out inoculation material while material is conveyed Mixing, has ensured the mixture homogeneity of inoculation material, the inoculation material of discharge can be entered by transfer tool fermentation tank or its He ferments in container.The mode of fermentation can flexibly be chosen as needed.
After the completion of wet fermentation feed fermentation, it is necessary to be added mixed in other dry materials when, can need to Dry material to be processed from powder raw material blanking hole 107 in put into, lifted through 2# elevators 211, material from 1# distributors 301 into Enter in batch bin 304, after material blending auger 306 and 307 accurate batch of burden balance weigh, open scale door 308, dry material enters mixed In conjunction machine 401.Since the ratio of wet fermentation feed addition is generally little, the addition ratio of dry material is added according to wet fermentation feed Example, weighs the wet fermentation feed of the weight that meets the requirements by hand, is put into feeding intake blanking hole 309 from hand, opens hand and feeds intake deduster 310 carry out dust removal process.
Wet fermentation feed enters in mixer 401, and dry material is fully mixed with wet fermentation finished feed in mixer 401 Close, mixer 401 complete material mixing after, dry and wet mixture is discharged into mixture surge bunker 402, mixer 401 followed by Continuous repetition as above dry and wet material mixed process.
Start finished product discharging machine 404 and material scattering machine 403, dry and wet mixture is when flowing through material scattering machine 403, by machine Tool, which crushes, to be broken up, this step eliminates the dry and wet material agglomerate that mixed process produces in mixer 401, last homogeneous no agglomerate Material discharged from the double-shaft paddle formula finished product discharging machine 404 being obliquely installed, since discharging machine 404 is the twin shaft that is obliquely installed Oar blade type is set, and is acted on using the gravity flow of material, dry and wet mixture can smoothly be discharged from discharging machine 404, discharged at the same time Double-shaft paddle in machine 404 further will mix dry and wet material while material is conveyed, and ensure dry and wet material Mixture homogeneity.Such a combustion is homogeneous, and the high material of mixture homogeneity meets the raising need of raiser.
The above, is only the preferred embodiment of the utility model, is not intended to limit the utility model, every according to this Any trickle amendment, equivalent substitution and the improvement that the technical spirit of utility model makees above example, should be included in this Within the protection domain of utility model technical solution.

Claims (5)

  1. The liquid diets production line 1. a kind of high-performance bio ferments, it is characterised in that:Including particulate material conditioning department, particulate material Break section, powder raw material conditioning department, feed proportioning workshop section, mixing crushing section, liquid addition 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, Feed intake blanking hole, hand of door, hand is claimed to feed intake deduster composition, the feed inlet of the 1# distributors passes through 2# threeways and 2# elevators Discharge port connects, and the feed inlet of the 2# distributors is connected with the discharge port of 2# pipe magnetic separators, and the batch bin quantity has multiple, 1# Multiple batch bins that distributor and 2# distributors are connected respectively, each batch bin be respectively provided with level detector, lower level detector and Material blending auger, material blending auger discharge port are flexible coupling with burden balance, are set below burden balance and claim door, are provided with above burden balance Hand feeds intake blanking hole and hand feeds intake deduster;
    The mixing crushing section is made of mixer, mixture surge bunker, material scattering machine, finished product discharging machine, under mixer Portion sets mixture surge bunker, and material scattering machine is set between mixture surge bunker and finished product discharging machine;
    Liquid adds workshop section by bacterium solution tank, flowmeter, bacterium solution pump, solenoid valve block into bacterium solution tank passes through pipeline and flowmeter, bacterium solution Pump, solenoid valve connection, and finally it is switched to mixer.
  2. A kind of 2. high-performance bio fermentation liquid diets production line as claimed in claim 1, it is characterised in that:The material to be comminuted Storehouse quantity has 2.
  3. A kind of 3. high-performance bio fermentation liquid diets production line as claimed in claim 1, it is characterised in that:The batch bin number Amount has 6.
  4. A kind of 4. high-performance bio fermentation liquid diets production line as claimed in claim 1, it is characterised in that:The finished product discharging Machine is double-shaft paddle formula conveyer.
  5. 5. such as a kind of high-performance bio fermentation liquid diets production line of Claims 1-4 any one of them, it is characterised in that:Institute Finished product discharging machine is stated from feed inlet to discharge outlet in the state set from high to low.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110449248A (en) * 2019-09-07 2019-11-15 广州穗粮实业有限公司 A kind of wheat bran processing technology
CN110934317A (en) * 2019-12-18 2020-03-31 安徽五粮泰生物工程股份有限公司 Manufacturing method of special mixing equipment for fermented feed

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110449248A (en) * 2019-09-07 2019-11-15 广州穗粮实业有限公司 A kind of wheat bran processing technology
CN110934317A (en) * 2019-12-18 2020-03-31 安徽五粮泰生物工程股份有限公司 Manufacturing method of special mixing equipment for fermented feed

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