CN106579504B - A kind of biological fermentation feed production equipment and production method - Google Patents
A kind of biological fermentation feed production equipment and production method Download PDFInfo
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- CN106579504B CN106579504B CN201611123574.3A CN201611123574A CN106579504B CN 106579504 B CN106579504 B CN 106579504B CN 201611123574 A CN201611123574 A CN 201611123574A CN 106579504 B CN106579504 B CN 106579504B
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N17/00—Apparatus specially adapted for preparing animal feeding-stuffs
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- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
Abstract
The present invention provides a kind of biological fermentation feed production equipments, the second conditioning department is also connected with including sequentially connected first conditioning department, raw material break section, ingredient station, bacterium solution addition mixing workshop section, ferment at constant temperature workshop section, low temperature drying workshop section, cooling workshop section, finished product break section and finished product packing workshop section, ingredient station therein.The present invention also provides a kind of biological fermentation feed production methods.The full-automatic production of fermented feed may be implemented in biological fermentation feed production equipment of the invention and production method, different types of fermentation raw material is suitable for production equipment of the invention, using ferment at constant temperature room ferment certifiable fermentation temperature, humidity controllability, to guarantee fermented product quality, it successively forces to cool down using low temperature drying and cold air after having fermented, avoid the warming phenomenon of product after fermenting, it ensure that fermented product activity from high temperature, further ensures the high stability and high quality of fermented product.
Description
Technical field
The present invention relates to feed production equipment fields, and in particular to a kind of biological fermentation feed production equipment and producer
Method.
Background technique
With the fast development of animal husbandry, the supply of high-quality feed raw material resources more tends to be nervous, and feedstuff cost occupies
It is high not under, while resident masses further increase the quality requirements of healthy animal products, the use of antibiotic in aquaculture
It is gradually limited, so exploitation low production cost, highly effective and safe feed become the trend of the following animal husbandry development.
What biological fermentation feed exactly came into being in this context, the low unconventional protein of a large amount of digestibilities is provided
Source becomes good microprotein, fermented feed palatability is good, nutritive value is high, rich in microorganism beneficial metabolic product,
Digestive utilization ratio is high, and the immunity of livestock and poultry animal can be improved, reduce the use of antibiotic, so as to improve livestock meat egg product
Quality, and extensive lower production costs of raw material sources can make full use of agricultural and sideline product and leftover bits and pieces, for animal husbandry and
Feed industry can alleviate the problem of protein feed resources shortage significantly, have very big development potentiality.But at this stage
It is primarily present the quality-improving that following three problems restrict fermented feed:
(1) used in many medium and small producer's fermented feed production processes or semiautomatic production equipment, manual operation ring
It saves more, is unfavorable for the stable production of high quality, production efficiency is low；
(2) zymotechnique is most or using trough type fermentation is stacked, this mode is excessively extensive, and external environment was for fermenting
The interference of journey is excessive, it is difficult to control production process, material easily contaminates environment miscellaneous bacteria and causes finished product unqualified；
(3) fermented feed, which is dried, destroys larger, object after high temperature drying for product quality using high temperature drying mode
Material temperature degree is still higher；Material material temperature in crushing process can also heat up, and product high temperature is caused to be destroyed.
Summary of the invention
To overcome technological deficiency present in existing fermented feed production, the object of the present invention is to provide a kind of biofermentations
Feed production equipment.
It is a further object of the present invention to provide a kind of biological fermentation feed production methods.
Biological fermentation feed production equipment provided by the invention includes sequentially connected first conditioning department, raw material grinders
Section, ingredient station, bacterium solution addition mixing workshop section, ferment at constant temperature workshop section, low temperature drying workshop section, cooling workshop section, finished product break section
And finished product packing workshop section, the ingredient station are also connected with the second conditioning department.
In biological fermentation feed production equipment of the invention, first conditioning department includes sequentially connected first pulse
Deduster, the first elevator, the first pipe magnetic separator and the first receiving sieve；Second conditioning department includes sequentially connected second arteries and veins
Rush deduster, the second elevator and the second receiving sieve.
In biological fermentation feed production equipment of the invention, the raw material break section includes that sequentially connected raw material waits for powder
Broken storehouse, raw material feeding device, raw material chopper, ingredient conveyor and third elevator, the ingredient conveyor are also connected with
Three pulse dust collectors.
In biological fermentation feed production equipment of the invention, the ingredient station includes sequentially connected distributor, ingredient
Storehouse, discharging machine and burden balance, the distributor include comminuting matter distributor and non-comminuting matter distributor, respectively with it is described
Raw material break section and second conditioning department are connected.
In biological fermentation feed production equipment of the invention, the bacterium solution addition mixing workshop section includes sequentially connected bacterium solution
Activation pot, solenoid valve, electronic scale and mixing machine, the mixing machine are connected with the ingredient station and send mixed material
Enter the ferment at constant temperature workshop section.
In biological fermentation feed production equipment of the invention, the ferment at constant temperature workshop section includes multiple fermentation casings and constant temperature
Fermenting cellar, the fermentation casing are used to accommodate the material for adding mixing workshop section from the bacterium solution, and in the ferment at constant temperature room
In ferment.
In biological fermentation feed production equipment of the invention, the height of the fermentation casing is 50~120cm, and top is set
It is equipped with opening, is provided with sealer in when fermentation opening.
In biological fermentation feed production equipment of the invention, temperature when fermenting in the ferment at constant temperature room is 35~45
℃。
In biological fermentation feed production equipment of the invention, the low temperature drying workshop section includes high inclination angle conveyer and low temperature
Fluidizing fluid-bed, the fermentation materials that the ferment at constant temperature workshop section generates are delivered to the low temperature by the high inclination angle conveyer and boil
Fluidized bed is risen to be dried.Drying temperature can be 50~60 DEG C.
In biological fermentation feed production equipment of the invention, the cooling workshop section includes sequentially connected pneumatic conveying whirlwind
The mating pulse dust collector of deduster, pneumatic conveying, air-flow cooler and the 4th elevator, the air-flow cooler are connected with gas
Flow the mating pulse dust collector of cooler.
In biological fermentation feed production equipment of the invention, the finished product break section includes sequentially connected second permanent magnetism
Cylinder, finished product storehouse to be comminuted, finished product feeder, finished product grinder, finished product conveyer and the 5th elevator, the finished product conveyer
It is also connected with the 4th pulse dust collector.
In biological fermentation feed production equipment of the invention, the finished product packing workshop section successively includes finished bin and packaging
Scale.
Biological fermentation feed production method provided by the invention is to be set using the described in any item productions of above technical scheme
It is standby to produce the biological fermentation feed.
Biological fermentation feed production equipment of the invention and production method have the advantage that
(1) entire production process can realize full-automation, and each link is all made of do mechanization operation, be suitable for scale, collection
Reduction production.
(2) fermentation raw material wide adaptability, exists simultaneously that raw material crushes path and raw material does not crush path in process equipment, sends out
The raw material of ferment can select larger class.
(3) fermenting step contains the material of inoculation bacterium solution using fermentation casing as junior unit, and the cabinet is moved to
The fermentation of ferment at constant temperature indoor storage, yeasting epidemic disaster is controllable, and material fermentation and transhipment are in closed space, hair
Ferment process control degree is high, can continuity it is good, material is not easy microbiological contamination, and fermentation quality is more stable, avoids traditional biological fermentation
Heap fermentation is mostly used, fermentation process occupied ground is more, pollutes the problems such as big.
(4) in drying section, dry materials are handled using low-temperature boiling bed, and dried material gas flow temperature is lower, are ensured
Material material temperature is unlikely to excessively high, by the rising of cooling control whole process stream temperature rapidly, realizes high humility, high-moisture
Fermented product is dried rapidly at low ambient temperatures, is avoided high temperature drying and is destroyed to the quality of fermented product.
(5) in cooling workshop section, material is immediately entered in air-flow cooler after drying, with cold air to dried material
Pressure cooling is carried out, temperature of charge can further decline, and cold air forces cooling ingenious cooperation low temperature drying, avoid and fermented
The warming phenomenon of product afterwards sufficiently ensures that temperature of charge is sufficiently low before crushing, so that fermented product is from high temperature, further
It ensure that fermentation materials activity is destroyed from heat preservation, ensure that the high stable and high quality of fermented feed.
Detailed description of the invention
Fig. 1 is the schematic diagram of biological fermentation feed production equipment of the invention；
Wherein, the reference numerals are as follows:
11, the first pulse dust collector；12, the first elevator；13, the first pipe magnetic separator；14, the first receiving sieve；15, the second arteries and veins
Rush deduster；16, the second elevator；17, the second receiving sieve；
21, raw material storehouse to be comminuted；22, raw material feeding device；23, raw material chopper；24, third pulse dust collector；25, raw material
Conveyer；26, third elevator；
31, comminuting matter distributor；32, non-comminuting matter distributor；33, batch bin；34, discharging machine；35, burden balance；
41, bacterium liquid activation tank；42, solenoid valve；43, electronic scale；44, mixing machine；
45, fermentation casing；50, ferment at constant temperature room；
61, high inclination angle conveyer；62, low-temperature boiling fluidized bed；
71, pneumatic conveying cyclone dust collectors；72, air-flow cooler；73, the mating pulse dust collector of air-flow cooler；74, gas
Power conveys mating pulse dust collector；75, the 4th elevator；
81, the second pipe magnetic separator；82, finished product storehouse to be comminuted；83, finished product feeder；84, finished product grinder；85, the 4th pulse
Deduster；86, finished product conveyer；87, the 5th elevator；
91, finished bin；92, packing scale.
Specific embodiment
To make the object, technical solutions and advantages of the present invention clearer, it will be further described below example of the invention
The technical solution of property embodiment.
The present invention provides a kind of biological fermentation feed production equipments, according to the process flow of fermentation raw material, including successively
The first conditioning department, raw material break section, ingredient station, bacterium solution addition mixing workshop section, ferment at constant temperature workshop section, the low temperature of connection are dry
Dry workshop section, cooling workshop section, finished product break section and finished product packing workshop section, ingredient station therein are also connected with the second fettler
Section.
According to the difference in fermentation raw material source, production equipment of the invention is applicable to plurality of raw materials, if you need to crush, raw material
After the cleaning of the first conditioning department, ingredient station is entered after can further crushing by raw material break section, such as without crushing, then
It is directly entered ingredient station after being cleared up by the second conditioning department, two paths can be used separately, also can be used in combination, i.e., and two kinds
Raw material doping uses.
As shown in Figure 1, the first conditioning department successively includes the first pulse dust collector 11, the first elevator 12, the first permanent magnetism
Cylinder 13 and the first receiving sieve 14, feeding port investment of the fermentation raw material for needing to crush from the first pulse dust collector 11, by first
Elevator 12 is delivered to eminence, then falls that remove irony therein by the first pipe magnetic separator 13 miscellaneous from the first elevator 12
Matter removes the impurity such as block, the rope in raw material using the first receiving sieve 14, thus completes the first conditioning department, material is most
The feed inlet of raw material break section is flowed into afterwards.
Second conditioning department successively includes the second pulse dust collector 15, the second elevator 16 and the second receiving sieve 17, for
The fermentation raw material for not needing to crush is put into from the feeding port of the second pulse dust collector 15, is conveyed by the second elevator 16 supreme
Then place removes the impurity such as block, the rope in raw material by the second receiving sieve 17, thus completes the second conditioning department, material
Flow directly into the feed inlet of ingredient station.
Raw material break section successively includes raw material storehouse 21 (F1) to be comminuted, raw material feeding device 22, raw material chopper 23, raw material
Conveyer 25 and third elevator 26, ingredient conveyor 25 are also connected with third pulse dust collector 24.From the first fettler
The material of section initially enters storage in raw material storehouse 21 to be comminuted and waits pulverization process, is then even added to through raw material feeding device 22
Required granularity, raw material chopper 23 and third pulse dust collector 24 and ingredient conveyor 25 are ground into raw material chopper 23
It matches, ensures that the working efficiency and work quality of raw material chopper 23, smashed material are conveyed through third elevator 26
The feed inlet that ingredient station is then flowed into eminence, thus completes raw material break section.
Ingredient station successively includes distributor, batch bin 33, discharging machine 34 and burden balance 35, and distributor includes comminuting matter
Distributor 31 and non-comminuting matter distributor 32, the material from raw material break section by comminuting matter distributor 31, come
Specified batch bin 33 is entered by non-comminuting matter distributor 32 from the material of the second conditioning department and stores (including P1-P6),
According to the material formula weight value set automatically, the material in batch bin 33 is added in burden balance 35 by discharging machine 34, thus
Ingredient station is completed, material flows into bacterium solution addition mixing workshop section after the weighing of burden balance 35.
Bacterium solution addition mixing workshop section successively includes bacterium liquid activation tank 41, solenoid valve 42, electronic scale 43 and mixing machine 44, is come from
Material after ingredient station burden balance 35 weigh is fallen into mixing machine 44, while the zymocyte liquid in bacterium liquid activation tank 41 passes through pipe
Road flows into electronic scale 43, and when the weighing value of electronic scale 43 reaches setting value, solenoid valve 42 is closed, and bacterium solution weighing terminates
Bacterium solution is put into mixing machine 44 afterwards, and bacterium solution is uniformly mixed with the material in mixing machine 44, thus completes bacterium solution addition mixing workshop section,
The discharge port of mixing machine 44 is directed at fermentation casing 45, mixes the material finished and enters in fermentation casing 45 hence into ferment at constant temperature
Workshop section.
Ferment at constant temperature workshop section includes multiple fermentation casings 45 and ferment at constant temperature room 50, and fermentation casing comes from bacterium solution for accommodating
The mixed material of addition mixing workshop section, and ferments in ferment at constant temperature room, the height of fermentation casing generally can for 50~
120cm, top are provided with opening, and for receiving the material from mixing machine 44, and fermentation heel row goes out fermentation materials, ferments
When, sealer is also provided in opening, provides the yeasting of a relative closure for strain, each fermentation casing can fill
0.8~1.6 ton of fermentation materials, and can be run on automation track, so that continuous production can be realized.Ferment at constant temperature room uses
Thermal insulation material, fermentation temperature general control may be implemented that environment temperature is controllable at 35~45 DEG C, to can guarantee growth
Stable condition, and guarantee that fermentation casing 45 is transferred out of ferment at constant temperature room 50 after fermentation by fermentation optimum temperature, it is thus complete
At ferment at constant temperature workshop section, the fermentation materials in fermentation casing 45 are taken out and enter low temperature drying workshop section.
Low temperature drying workshop section includes high inclination angle conveyer 61 and low-temperature boiling fluidized bed 62, the object that ferment at constant temperature workshop section generates
Material is delivered to low-temperature boiling fluidized bed 62 by high inclination angle conveyer 61 and carries out low temperature drying, drying process material Contact Temperature one
As be not higher than 60 DEG C, typically 50~60 DEG C, thus complete low temperature drying workshop section, it is dry after material enter it is subsequent cold
But workshop section.
Cooling workshop section successively includes that pneumatic conveying cyclone dust collectors 71, the mating pulse dust collector 74 of pneumatic conveying, air-flow are cold
But device 72 and the 4th elevator 75, air-flow cooler 72 are connected with the mating pulse dust collector 73 of air-flow cooler.From low temperature
The gas that material is formed through pneumatic conveying cyclone dust collectors 71 and the mating pulse dust collector 74 of pneumatic conveying after the drying of drying section
Power transportation system is delivered in air-flow cooler 72, is forced cold air cooling treatment, and the near room temperature of the material temperature of material is horizontal, by
This completes cooling workshop section, is sent into subsequent finished product break section, the cooling that air-flow cooler 72 is discharged by the 4th elevator 75
Air is discharged into atmosphere after matched 73 dust removal process of pulse dust collector.The outlet of pulse dust collector 73 and pulse dust collector 74
Also it is connected with the discharge port of the air-flow cooler 72, collects discharge material and be sent into subsequent finished product break section together.
Finished product break section successively includes the second pipe magnetic separator 81, finished product storehouse 82 (F2) to be comminuted, finished product feeder 83, finished product
Pulverizer 84, finished product conveyer 86 and the 5th elevator 87, finished product conveyer 86 are also connected with the 4th pulse dust collector 85.Come
It is sent into pipe magnetic separator 81 from the material of cooling workshop section by the 4th elevator 75, removes the iron impurities in material, later fall into
Finished product storehouse 82 to be comminuted, the material stored in finished product storehouse 82 to be comminuted are uniformly added into finished product grinder 84 by finished product feeder 83
In, by crushing material to required granularity, finished product grinder 84 is matched with the 4th pulse dust collector 85, finished product conveyer 86,
Ensure that the working efficiency and work quality of finished product grinder 84, smashed finished product are sent into finished product packing by the 5th elevator 87
Thus workshop section completes finished product break section.
Finished product packing workshop section successively includes finished bin 91 (C1) and packing scale 92.It is sent out after crushing from finished product break section
Ferment material is delivered in finished bin 91 by the 5th elevator 87 and is stored, and the finished product in final finished storehouse 91 claims by packing scale 92
Amount is packaged into bagged product.
The full-automatic production of fermented feed may be implemented in biological fermentation feed production equipment of the invention, can be for not
Congener fermentation raw material is applied both to production equipment of the invention regardless of whether needing to crush.In addition, life of the invention
It produces equipment and uses ferment at constant temperature room, it is ensured that the controllability of fermentation temperature, humidity has been fermented to guarantee fermented product quality
It successively forces to cool down using low temperature drying and cold air after complete, avoids the warming phenomenon of product after fermenting, ensure that fermentation
Product Activity further ensures the quality and stability of fermented product from high temperature.
Although the preferred embodiments of the invention, those skilled in the art has been disclosed in order to illustrate the present invention
Member can be the present invention it should be appreciated that in the case where not departing from present inventive concept defined by claims and range
Various modifications, addition and replacement out.
Claims (10)
1. a kind of biological fermentation feed production equipment, which is characterized in that crushed including sequentially connected first conditioning department, raw material
Workshop section, ingredient station, bacterium solution addition mixing workshop section, ferment at constant temperature workshop section, low temperature drying workshop section, cooling workshop section, finished product grinders
Section and finished product packing workshop section, the ingredient station are also connected with the second conditioning department；
The ferment at constant temperature workshop section includes multiple fermentation casings and ferment at constant temperature room, and the fermentation casing is for accommodating from described
The material of bacterium solution addition mixing workshop section, and ferment in the ferment at constant temperature room；
The low temperature drying workshop section includes high inclination angle conveyer and low-temperature boiling fluidized bed, the hair that the ferment at constant temperature workshop section generates
Ferment material is delivered to the low-temperature boiling fluidized bed by the high inclination angle conveyer and is dried, and drying temperature is 50~60
℃。
2. production equipment according to claim 1, which is characterized in that first conditioning department includes sequentially connected
One pulse dust collector, the first elevator, the first pipe magnetic separator and the first receiving sieve；Second conditioning department includes sequentially connected
Second pulse dust collector, the second elevator and the second receiving sieve.
3. production equipment according to claim 1, which is characterized in that the raw material break section includes sequentially connected original
Expect that storehouse, raw material feeding device, raw material chopper, ingredient conveyor and third elevator to be comminuted, the ingredient conveyor also connect
It is connected to third pulse dust collector.
4. production equipment according to claim 1, which is characterized in that the ingredient station includes sequentially connected distribution
Device, batch bin, discharging machine and burden balance, the distributor include comminuting matter distributor and non-comminuting matter distributor, are divided
It is not connected with the raw material break section and second conditioning department.
5. production equipment according to claim 1, which is characterized in that the bacterium solution addition mixing workshop section includes being sequentially connected
Bacterium liquid activation tank, solenoid valve, electronic scale and mixing machine, the mixing machine is connected with the ingredient station and will be mixed
Material is sent into the ferment at constant temperature workshop section.
6. production equipment according to claim 1, which is characterized in that the height of the fermentation casing is 50~120cm,
Top is provided with opening, is provided with sealer in when fermentation opening；In the ferment at constant temperature room ferment when temperature be 35~
45℃。
7. production equipment according to claim 1, which is characterized in that the cooling workshop section includes sequentially connected pneumatic transporting
The mating pulse dust collector of cyclone dust collectors, pneumatic conveying, air-flow cooler and the 4th elevator are sent, the air-flow cooler connects
It is connected to the mating pulse dust collector of air-flow cooler.
8. production equipment according to claim 1, which is characterized in that the finished product break section includes sequentially connected
Two pipe magnetic separators, finished product storehouse to be comminuted, finished product feeder, finished product grinder, finished product conveyer and the 5th elevator, the finished product
Conveyer is also connected with the 4th pulse dust collector.
9. production equipment according to claim 1, which is characterized in that the finished product packing workshop section successively include finished bin and
Packing scale.
10. a kind of biological fermentation feed production method, which is characterized in that with the described in any item production equipments of claim 1-9
Produce the biological fermentation feed.
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| CN201611123574.3A CN106579504B (en) | 2016-12-08 | 2016-12-08 | A kind of biological fermentation feed production equipment and production method |
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| CN107048449A (en) * | 2017-06-09 | 2017-08-18 | 镇江东方生物工程设备技术有限责任公司 | A kind of mushroom bran fermented feed fermenter equipment and its application |
| CN109266541A (en) * | 2018-10-16 | 2019-01-25 | 临沂希来利生物饲料有限公司 | A kind of fermented feed fermentation unit and fermentation process |
| CN109536365B (en) * | 2018-11-22 | 2021-08-24 | 广州博善生物科技股份有限公司 | Fermented feed device, system and method |
| CN109777717A (en) * | 2019-01-22 | 2019-05-21 | 云南东道饲料有限公司 | A kind of novel biological fermentation feed equipment |
| CN109938160A (en) * | 2019-03-04 | 2019-06-28 | 路德环境科技股份有限公司 | The process system and process of biological feedstuff are prepared using vinasse |
| CN109999954A (en) * | 2019-04-18 | 2019-07-12 | 广西扬翔股份有限公司 | Essence feeds mill |
| CN109999955A (en) * | 2019-04-18 | 2019-07-12 | 广西扬翔股份有限公司 | Essence feeds mill |
| CN110038686B (en) * | 2019-04-18 | 2024-03-26 | 广西扬翔股份有限公司 | Fine feeding mill |
| CN109965325A (en) * | 2019-04-22 | 2019-07-05 | 广东广垦畜牧工程研究院有限公司 | A kind of device and method using ground source feed resource production fermented feed |
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| CN201995556U (en) * | 2011-01-19 | 2011-10-05 | 浙江国茂饲料有限公司 | Fodder production line |
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Effective date of registration: 20211224 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. |