CN106579504A - Production equipment for biological fermented feed and production method - Google Patents
Production equipment for biological fermented feed and production method Download PDFInfo
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- CN106579504A CN106579504A CN201611123574.3A CN201611123574A CN106579504A CN 106579504 A CN106579504 A CN 106579504A CN 201611123574 A CN201611123574 A CN 201611123574A CN 106579504 A CN106579504 A CN 106579504A
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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
Abstract
The invention provides production equipment for biological fermented feed. The production equipment comprises a fist cleaning section, a raw material smashing section, a batching section, a bacterial liquor adding and mixing section, a constant temperature fermentation section, a low temperature drying section, a cooling section, a finished product smashing section, and a finished product packaging section connected in sequence. The batching section is also connected with a second cleaning section. The invention also provides a production method for the biological fermented feed. The production equipment for biological fermented feed and the production method can realize full-automatic production of fermented feed, and the production equipment is suitable for different kinds of fermented raw materials. A constant temperature fermentation chamber is used for fermentation, and controllability of fermentation temperature and humidity can be ensured, so as to ensure quality of fermentation products. After fermentation, low temperature drying and cold air forced cooling are used in sequence, preventing warming phenomenon of products after fermentation, ensuring activity of fermentation products not to be damaged by high temperature, and further ensuring high stability and high quality of the fermentation products.
Description
Technical field
The present invention relates to feed production equipment field, and in particular to a kind of biological fermentation feed production equipment and producer
Method.
Background technology
With the fast development of animal husbandry, the supply of high-quality feed raw material resources tends to all the more nervous, and feedstuff cost is occupied
It is high not under, while resident is popular for the quality requirements of healthy animal products are further raised, the use of antibiotic in aquaculture
Gradually it is limited, so exploitation low production cost, highly effective and safe feedstuff become the trend of following animal husbandry development.
What biological fermentation feed exactly arose at the historic moment in this context, by the low unconventional protein money of a large amount of digestibilities
Source is changed into the microprotein of high-quality, fermented feed good palatability, be of high nutritive value, rich in microorganism beneficial metabolic product,
Digestive utilization ratio is high, can improve the immunity of livestock and poultry animal, the use of antibiotic is reduced, so as to improve livestock meat egg product
Quality, and the extensive production cost of raw material sources is relatively low, can make full use of agricultural byproducts and leftover bits and pieces, for animal husbandry and
Feed industry, can significantly alleviate the problem of protein feed resources shortage, with very big development potentiality.But, at this stage
It is primarily present the quality-improving that three below problem restricts fermented feed：
(1) adopt in many medium and small producer's fermented feed production processes or semiautomatic production equipment, manually operates ring
Section is more, is unfavorable for the stable production of high-quality, low production efficiency；
(2) fermentation technology is most or using trough type fermentation is stacked, and this mode is excessively extensive, and external environment was for fermenting
The interference of journey is excessive, it is difficult to which production process is controlled, and material easily contaminates environment miscellaneous bacteria and causes finished product unqualified；
(3) fermented feed dried adopts high temperature drying mode to destroy larger, thing after high temperature drying for product quality
Material temperature degree is still higher；Material material temperature in crushing process can also heat up, and cause product high temperature to be destroyed.
The content of the invention
To overcome technological deficiency present in existing fermented feed production, it is an object of the invention to provide a kind of biofermentation
Feed production equipment.
It is a further object of the present invention to provide a kind of biological fermentation feed production method.
The biological fermentation feed production equipment that the present invention is provided includes the first conditioning department, the raw material pulverizing work being sequentially connected
Section, ingredient station, bacterium solution addition mixing workshop section, ferment at constant temperature workshop section, cold drying workshop section, cooling workshop section, finished product break section
And finished product packing workshop section, the ingredient station is also associated with the second conditioning department.
In the biological fermentation feed production equipment of the present invention, first conditioning department includes the first pulse being sequentially connected
Cleaner unit, the first elevator, the first pipe magnetic separator and the first receiving sieve；Second conditioning department includes the second arteries and veins being sequentially connected
Rush cleaner unit, the second elevator and the second receiving sieve.
In the biological fermentation feed production equipment of the present invention, the raw material pulverizing workshop section includes that the raw material being sequentially connected treats powder
Broken storehouse, raw material feeding device, raw material chopper, ingredient conveyor and the 3rd elevator, the ingredient conveyor is also associated with
Three pulse dust collectors.
In the biological fermentation feed production equipment of the present invention, the ingredient station includes allotter, the dispensing being sequentially connected
Storehouse, discharging machine and burden balance, the allotter includes comminuting matter allotter and non-comminuting matter allotter, respectively with it is described
Raw material pulverizing workshop section and second conditioning department are connected.
In the biological fermentation feed production equipment of the present invention, the bacterium solution addition mixing workshop section includes the bacterium solution being sequentially connected
Activation pot, electromagnetic valve, electronic scale and mixer, the mixer is connected with the ingredient station and send mixed material
Enter the ferment at constant temperature workshop section.
In the biological fermentation feed production equipment of the present invention, the ferment at constant temperature workshop section includes multiple fermentation casings and constant temperature
Fermenting cellar, the fermentation casing is used for the accommodating material for adding mixing workshop section from the bacterium solution, and in the ferment at constant temperature room
In fermented.
In the biological fermentation feed production equipment of the present invention, the height of the fermentation casing is 50～120cm, and its top sets
Opening is equipped with, sealer is provided with the opening during fermentation.
In the biological fermentation feed production equipment of the present invention, temperature when fermenting in the ferment at constant temperature room is 35～45
℃。
In the biological fermentation feed production equipment of the present invention, the cold 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 produces are delivered to the low temperature boiling by the high inclination angle conveyer
Rise fluid bed to be dried.Baking temperature can be 50～60 DEG C.
In the biological fermentation feed production equipment of the present invention, the cooling workshop section includes the air conveying whirlwind being sequentially connected
Cleaner unit, air conveying supporting pulse dust collector, air-flow cooler and the 4th elevator, the air-flow cooler is connected with gas
The supporting pulse dust collector of stream cooler.
In the biological fermentation feed production equipment of the present invention, the finished product break section includes the second permanent magnetism being sequentially connected
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 associated with the 4th pulse dust collector.
In the biological fermentation feed production equipment of the present invention, the finished product packing workshop section includes successively finished bin and packaging
Scale.
The biological fermentation feed production method that the present invention is provided is to be set using the production described in above any one of technical scheme
It is standby to produce the biological fermentation feed.
The biological fermentation feed production equipment and production method of the present invention has the advantage that：
(1) whole production process is capable of achieving full-automation, and each link adopts do mechanization operation, is suitable for scale, collection
Reduction is produced.
(2), there is raw material pulverizing path and raw material do not crush path in fermentation raw material wide adaptability, send out simultaneously in process equipment
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 casing is moved to
Ferment at constant temperature indoor storage ferments, and yeasting epidemic disaster is controllable, and material fermentation and transhipment are in the space of closing, are sent out
Ferment process control degree is high, can seriality it is good, material is difficult microbiological contamination, and fermentation quality is more stable, it is to avoid traditional biological fermentation
Adopt heap fermentation, sweat occupied ground is more more, pollute it is big the problems such as.
(4) in drying section, using the process of low-temperature boiling bed, dried material gas flow temperature is relatively low, ensures for dry materials
Material material temperature is unlikely to too high, by rapid cooling the rising of whole process stream temperature is controlled, and realizes high humility, high-moisture
Fermented product is dried rapidly at low ambient temperatures, it is to avoid high temperature drying is destroyed to the quality of fermented product.
(5) in cooling workshop section, drying terminates rear material and immediately enters in air-flow cooler, with cold air to dried material
Pressure cooling is carried out, temperature of charge can further decline, cold air forces the ingenious cooperation cold drying of cooling, it is to avoid fermented
The warming phenomenon of product afterwards, fully ensures that temperature of charge is sufficiently low before crushing so that fermented product from high temperature, further
Ensure that fermentation materials activity, from insulation destruction, ensures that the high stable and high-quality of fermented feed.
Description of the drawings
Fig. 1 is the schematic diagram of the biological fermentation feed production equipment of the present invention；
Wherein, description of reference numerals is as follows：
11st, the first pulse dust collector；12nd, the first elevator；13rd, the first pipe magnetic separator；14th, the first receiving sieve；15th, the second arteries and veins
Rush cleaner unit；16th, the second elevator；17th, the second receiving sieve；
21st, raw material storehouse to be comminuted；22nd, raw material feeding device；23rd, raw material chopper；24th, the 3rd pulse dust collector；25th, raw material
Conveyer；26th, the 3rd elevator；
31st, comminuting matter allotter；32nd, non-comminuting matter allotter；33rd, batch bin；34th, discharging machine；35th, burden balance；
41st, bacterium liquid activation tank；42nd, electromagnetic valve；43rd, electronic scale；44th, mixer；
45th, ferment casing；50th, ferment at constant temperature room；
61st, high inclination angle conveyer；62nd, low-temperature boiling fluid bed；
71st, air conveying cyclone dust extractor；72nd, air-flow cooler；73rd, the supporting pulse dust collector of air-flow cooler；74th, gas
Power conveys supporting pulse dust collector；75th, the 4th elevator；
81st, the second pipe magnetic separator；82nd, finished product storehouse to be comminuted；83rd, finished product feeder；84th, finished product grinder；85th, the 4th pulse
Cleaner unit；86th, finished product conveyer；87th, the 5th elevator；
91st, finished bin；92nd, packing scale.
Specific embodiment
To make the object, technical solutions and advantages of the present invention clearer, the example of the present invention is will be further described below
The technical scheme of property embodiment.
The invention provides a kind of biological fermentation feed production equipment, according to the handling process of fermentation raw material, including successively
First conditioning department of connection, raw material pulverizing workshop section, ingredient station, bacterium solution addition mixing workshop section, ferment at constant temperature workshop section, low temperature are done
Dry workshop section, cooling workshop section, finished product break section and finished product packing workshop section, ingredient station therein is also associated with the second fettler
Section.
According to the difference in fermentation raw material source, the production equipment of the present invention is applicable to plurality of raw materials, such as needs to crush, raw material
Jing after the cleaning of the first conditioning department, further ingredient station can be entered after the crushing of raw material pulverizing workshop section, such as without the need for crushing, then
Be directly entered ingredient station after being cleared up by the second conditioning department, two paths can be used separately, also can be combined and use, i.e., two kinds
Raw material doping is used.
As shown in figure 1, the first conditioning department includes successively the first pulse dust collector 11, the first elevator 12, the first permanent magnetism
The receiving sieve 14 of cylinder 13 and first, needs dog-house input of the fermentation raw material crushed from the first pulse dust collector 11, by first
Elevator 12 is delivered to eminence, and to remove irony therein miscellaneous for the first pipe magnetic separators of Jing 13 after then falling from the first elevator 12
Matter, then the impurity such as block, the rope in raw material are removed through the first receiving sieve 14, the first conditioning department is thus completed, material is most
The charging aperture of raw material pulverizing workshop section is flowed into afterwards.
Second conditioning department includes successively the second pulse dust collector 15, the second elevator 16 and the second receiving sieve 17, for
The fermentation raw material that need not be crushed puts into from the dog-house of the second pulse dust collector 15, is conveyed by the second elevator 16 paramount
Place, then removes the impurity such as block, the rope in raw material through the second receiving sieve 17, thus completes the second conditioning department, material
Flow directly into the charging aperture of ingredient station.
Raw material pulverizing workshop section includes successively raw material storehouse 21 (F1) to be comminuted, raw material feeding device 22, raw material chopper 23, raw material
The elevator 26 of conveyer 25 and the 3rd, ingredient conveyor 25 is also associated with the 3rd 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, and then Jing raw material feedings device 22 is even added to
Required granularity, the pulse dust collector 24 of raw material chopper 23 and the 3rd and ingredient conveyor 25 are ground in raw material chopper 23
Support the use, ensure the work efficiency and work quality of raw material chopper 23, the elevators 26 of material Jing the 3rd after crushing are conveyed
To eminence and then the charging aperture of inflow ingredient station, raw material pulverizing workshop section is thus completed.
Ingredient station includes successively allotter, batch bin 33, discharging machine 34 and burden balance 35, and allotter includes comminuting matter
Allotter 31 and non-comminuting matter allotter 32, from raw material pulverizing workshop section material by comminuting matter allotter 31, come
The batch bin 33 specified is entered by non-comminuting matter allotter 32 from the material of the second conditioning department and stores (including P1-P6),
According to the material formula gravimetric value of automatic setting, in burden balance 35, thus the material in batch bin 33 is added by discharging machine 34
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 includes successively bacterium liquid activation tank 41, electromagnetic valve 42, electronic scale 43 and mixer 44, from
Material after ingredient station burden balance 35 are weighed is fallen in mixer 44, while the zymocyte liquid in bacterium liquid activation tank 41 is by pipe
Road is flowed in electronic scale 43, and when the weighing value of electronic scale 43 reaches setting value, electromagnetic valve 42 is closed, and bacterium solution is weighed and terminated
Afterwards bacterium solution is put in mixer 44, and bacterium solution is mixed homogeneously with the material in mixer 44, thus completes bacterium solution addition mixing workshop section,
The discharging opening alignment fermentation casing 45 of mixer 44, mixes the material for finishing 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 is used for accommodating from bacterium solution
The mixed material of addition mixing workshop section, and is fermented in ferment at constant temperature room, the height of the casing that ferments typically can for 50～
120cm, top is provided with opening, and for receiving the material from mixer 44, and fermentation heel row goes out fermentation materials, ferments
When, sealer is also provided with opening, for the yeasting that strain provides a relative closure, each fermentation casing can be filled
0.8～1.6 ton of fermentation materials, and can run on automatization's track, so as to be capable of achieving continuous prodution.Ferment at constant temperature room adopts
Insulation material, fermentation temperature general control is at 35～45 DEG C, it is possible to achieve ambient temperature is controllable, so as to ensure growth
Steady-state conditionss, and ensure optimum temperature of fermenting, after fermentation ends, fermentation casing 45 is transferred out of into ferment at constant temperature room 50, it is thus complete
Into ferment at constant temperature workshop section, the fermentation materials in fermentation casing 45 are taken out and enters cold drying workshop section.
Cold drying workshop section includes high inclination angle conveyer 61 and low-temperature boiling fluid bed 62, the thing that ferment at constant temperature workshop section produces
Material is delivered to low-temperature boiling fluid bed 62 by high inclination angle conveyer 61 carries out cold drying, dry run material Contact Temperature one
As not higher than 60 DEG C, typically 50～60 DEG C, thus complete cold drying workshop section, dried material enters follow-up cold
But workshop section.
Cooling workshop section includes that successively air conveying cyclone dust extractor 71, air conveying supporting pulse dust collector 74, air-flow are cold
But the elevator 75 of device 72 and the 4th, air-flow cooler 72 is connected with the supporting pulse dust collector 73 of air-flow cooler.From low temperature
The gas of the air conveying cyclone dust extractors 71 of material Jing and air conveying supporting pulse dust collector 74 composition after the drying of drying section
Power induction system is delivered in air-flow cooler 72, Jing pressure cold air cooling treatments, the near room temperature level of material temperature of material, by
This completes to cool down workshop section, and by the 4th elevator 75 follow-up finished product break section, the cooling that air-flow cooler 72 is discharged are sent into
Air is entered in air Jing after the supporting dust removal process of pulse dust collector 73.The outlet of pulse dust collector 73 and pulse dust collector 74
Also it is connected with the discharging opening of the air-flow cooler 72, collects discharge material and send into follow-up finished product break section together.
Finished product break section includes successively the second pipe magnetic separator 81, finished product storehouse 82 (F2) to be comminuted, finished product feeder 83, finished product
Pulverizer 84, the elevator 87 of finished product conveyer 86 and the 5th, finished product conveyer 86 is also associated with the 4th pulse dust collector 85.Come
Sent in pipe magnetic separator 81 by the 4th elevator 75 from the material of cooling workshop section, remove the irony impurity in material, later fallen into
Finished product storehouse 82 to be comminuted, the material stored in finished product storehouse 82 to be comminuted is uniformly added into finished product grinder 84 by finished product feeder 83
In, by crushing material to desired particle size, finished product grinder 84 is supported the use with the 4th pulse dust collector 85, finished product conveyer 86,
The work efficiency and work quality of finished product grinder 84 are ensured, the finished product after crushing sends into finished product packing by the 5th elevator 87
Workshop section, thus completes finished product break section.
Finished product packing workshop section includes successively finished bin 91 (C1) and packing scale 92.Send out after the crushing of 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 through packing scale 92
Amount is packaged into bagged product.
The biological fermentation feed production equipment of the present invention can realize the full-automatic production of fermented feed, can be for not
Congener fermentation raw material, regardless of whether needing to crush, is applied both to the production equipment of the present invention.Additionally, the life of the present invention
Product equipment adopts ferment at constant temperature room, it is ensured that fermentation temperature, the controllability of humidity, so as to ensure fermented product quality, has fermented
After finishing successively cooling forced using cold drying and cold air, it is to avoid the warming phenomenon of product after fermentation, it is ensured that fermentation
Product Activity further ensures the quality and stability of fermented product from high temperature.
Although in order to illustrate the present invention, having been disclosed for the preferred embodiments of the invention, those skilled in the art
Member to the present invention it should be appreciated that in the case of the present inventive concept and scope limited without departing from claims, can do
Go out various modifications, addition and replace.
Claims (12)
1. a kind of biological fermentation feed production equipment, it is characterised in that including the first conditioning department, the raw material pulverizing that are sequentially connected
Workshop section, ingredient station, bacterium solution addition mixing workshop section, ferment at constant temperature workshop section, cold drying workshop section, cooling workshop section, finished product grinders
Section and finished product packing workshop section, the ingredient station is also associated with the second conditioning department.
2. production equipment according to claim 1, it is characterised in that first conditioning department include being sequentially connected the
One pulse dust collector, the first elevator, the first pipe magnetic separator and the first receiving sieve；Second conditioning department includes what is be sequentially connected
Second pulse dust collector, the second elevator and the second receiving sieve.
3. production equipment according to claim 1, it is characterised in that the raw material pulverizing workshop section includes the original being sequentially connected
Expect storehouse to be comminuted, raw material feeding device, raw material chopper, ingredient conveyor and the 3rd elevator, the ingredient conveyor also connects
It is connected to the 3rd pulse dust collector.
4. production equipment according to claim 1, it is characterised in that the ingredient station includes the distribution being sequentially connected
Device, batch bin, discharging machine and burden balance, the allotter includes comminuting matter allotter and non-comminuting matter allotter, point
It is not connected with the raw material pulverizing workshop section and second conditioning department.
5. production equipment according to claim 1, it is characterised in that the bacterium solution addition mixing workshop section includes being sequentially connected
Bacterium liquid activation tank, electromagnetic valve, electronic scale and mixer, the mixer is connected with the ingredient station and will be mixed
Material sends into the ferment at constant temperature workshop section.
6. production equipment according to claim 1, it is characterised in that the ferment at constant temperature workshop section includes multiple fermentation casings
And ferment at constant temperature room, the fermentation casing is used for the accommodating material for adding mixing workshop section from the bacterium solution, and in the constant temperature
Fermented in fermenting cellar.
7. production equipment according to claim 6, it is characterised in that the height of the fermentation casing is 50～120cm, its
Top is provided with opening, and sealer is provided with the opening during fermentation；In the ferment at constant temperature room ferment when temperature be 35～
45℃。
8. production equipment according to claim 1, it is characterised in that the cold drying workshop section includes high inclination angle conveyer
And low-temperature boiling fluid bed, the fermentation materials that the ferment at constant temperature workshop section produces are delivered to described by the high inclination angle conveyer
Low-temperature boiling fluid bed is dried, and baking temperature is 50～60 DEG C.
9. production equipment according to claim 1, it is characterised in that the cooling workshop section includes the pneumatic transporting being sequentially connected
Cyclone dust extractor, air conveying supporting pulse dust collector, air-flow cooler and the 4th elevator, the air-flow cooler is sent to connect
It is connected to the supporting pulse dust collector of air-flow cooler.
10. production equipment according to claim 1, it is characterised in that the finished product break section includes what is be sequentially connected
Second pipe magnetic separator, finished product storehouse to be comminuted, finished product feeder, finished product grinder, finished product conveyer and the 5th elevator, it is described into
Product conveyer is also associated with the 4th pulse dust collector.
11. production equipments according to claim 1, it is characterised in that the finished product packing workshop section includes successively finished bin
And packing scale.
12. a kind of biological fermentation feed production methods, it is characterised in that with the production equipment described in any one of claim 1-11
Produce the biological fermentation feed.
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| Application Number | Priority Date | Filing Date | Title |
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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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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| 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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| CN106579504A true CN106579504A (en) | 2017-04-26 |
| CN106579504B CN106579504B (en) | 2019-09-20 |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN109536365A (en) * | 2018-11-22 | 2019-03-29 | 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 |
| 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 |
| CN109999955A (en) * | 2019-04-18 | 2019-07-12 | 广西扬翔股份有限公司 | Essence feeds mill |
| CN109999954A (en) * | 2019-04-18 | 2019-07-12 | 广西扬翔股份有限公司 | Essence feeds mill |
| CN110038686A (en) * | 2019-04-18 | 2019-07-23 | 广西扬翔股份有限公司 | Essence feeds mill |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201995556U (en) * | 2011-01-19 | 2011-10-05 | 浙江国茂饲料有限公司 | Fodder production line |
| CN104126857A (en) * | 2014-07-31 | 2014-11-05 | 福建龙岩金和动物饲料有限公司 | Automatic production device of environmental protection antibiotic-free fermented feed |
| CN205161844U (en) * | 2015-11-12 | 2016-04-20 | 无锡华诺威动物保健品有限公司 | Automatic fat powder production facility of totally enclosed |
-
2016
- 2016-12-08 CN CN201611123574.3A patent/CN106579504B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201995556U (en) * | 2011-01-19 | 2011-10-05 | 浙江国茂饲料有限公司 | Fodder production line |
| CN104126857A (en) * | 2014-07-31 | 2014-11-05 | 福建龙岩金和动物饲料有限公司 | Automatic production device of environmental protection antibiotic-free fermented feed |
| CN205161844U (en) * | 2015-11-12 | 2016-04-20 | 无锡华诺威动物保健品有限公司 | Automatic fat powder production facility of totally enclosed |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
| CN109536365A (en) * | 2018-11-22 | 2019-03-29 | 广州博善生物科技股份有限公司 | Fermented feed device, system and method |
| 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 |
| CN109999955A (en) * | 2019-04-18 | 2019-07-12 | 广西扬翔股份有限公司 | Essence feeds mill |
| CN109999954A (en) * | 2019-04-18 | 2019-07-12 | 广西扬翔股份有限公司 | Essence feeds mill |
| CN110038686A (en) * | 2019-04-18 | 2019-07-23 | 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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|---|---|
| CN106579504B (en) | 2019-09-20 |
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Inventor after: Liu Jianhua Inventor after: Zhou Jianliang Inventor after: Wang Lingling Inventor after: Zhu Qinhao Inventor before: Liu Jianhua Inventor before: Wei Hong Inventor before: Zhou Jianliang Inventor before: Wang Lingling Inventor before: Zhu Qinhao |
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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. |