CN209152319U - A kind of feed production system - Google Patents
A kind of feed production system Download PDFInfo
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- CN209152319U CN209152319U CN201820631648.2U CN201820631648U CN209152319U CN 209152319 U CN209152319 U CN 209152319U CN 201820631648 U CN201820631648 U CN 201820631648U CN 209152319 U CN209152319 U CN 209152319U
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- rotary distributor
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- bucket elevator
- powder
- batch bin
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Abstract
The utility model belongs to Feed Manufacturing processing technique field, and in particular to a kind of feed production system.The system include be sequentially connected setting raw material reception workshop section is mixed with Chu Qing workshop section, break section, ingredient, pelletize workshop section and bale room.All feeds and raw materials of feed additives are uniformly mixed by feed production system provided by the utility model using the mixed characteristic of mixing machine, and the material of certain granules is made of granulator.According to the needs of factory formula, all feeds and raw materials of feed additives can be mixed into concentrated feed or mixed feed, and particle is made.To intermediate mixed process, more hybrid mode is provided, the applicability of system is extended, so as to be suitable for the production of birds or aquatic feeds.
Description
Technical field
The utility model belongs to Feed Manufacturing processing technique field, and in particular to a kind of feed production system.
Background technique
Birds or aquatic feeds are an important factor for influencing birds or aquatic products quality.General bird feed production system is pressed
Carry out according to such as under type: burden balance weigh each raw material in proportion, these raw materials are crushed machine and crush later, finally in mixing machine
It is mixed.Since the particle diameter of raw material is different, and crushing process is necessary environment so that certain little particle raw materials also by
Unnecessary crushing, waste of resource, and particle diameter difference is larger in final mixture.In addition, due to the development of feed, it is raw
Production system is also required to match.
Utility model content
To solve the deficiencies in the prior art, the utility model provides a kind of feed production system.The production system can be with
All feeds and raw materials of feed additives are uniformly mixed, and the feed material of certain granules is made.
Technical solution provided by the utility model is as follows:
A kind of feed production system, the raw material including being sequentially connected setting receive mixed with Chu Qing workshop section, break section, ingredient
Close workshop section, granulation workshop section and bale room.
Based on the above-mentioned technical proposal, raw material can be mixed, pelletized and is packaged by clear, crushing, ingredient, be prepared into feeding
Material.
Specifically, it includes powder feeding port, particulate material feeding port, the first bucket lifting that the raw material, which is received with Chu Qing workshop section,
Machine and the second elevator, the powder feeding port connect first bucket elevator, described in the particulate material feeding port connection
Second elevator.
Based on the above-mentioned technical proposal, the production line of powder and particle can be distinguished.
Further, the powder feeding port is provided with the first pulse dust collector, and the particulate material feeding port is provided with
Two pulse dust collectors.
Pulse dust collector can prevent dust pollution.
Specifically, the break section includes particulate material receiving sieve, the first pipe magnetic separator, the first rotary distributor, at least two
A storehouse to be comminuted, the first scroll feeder, the second scroll feeder, pulverizer, micronizer, third bucket elevator and
Four bucket elevators, second elevator, the particulate material receiving sieve, first pipe magnetic separator and the first rotation distribution
Device is sequentially connected setting, and first rotary distributor is separately connected each storehouse to be comminuted, to be comminuted described at least one
Storehouse connects first scroll feeder, and first scroll feeder connects the pulverizer, described at least one to powder
Broken storehouse connects second scroll feeder, and second scroll feeder connects micronizer, and the pulverizer connects institute
Third bucket elevator is stated, the micronizer connects the 4th bucket elevator.
Based on the above-mentioned technical proposal, particulate material can be crushed.
Specifically, ingredient mixing workshop section include powder receiving sieve, the second rotary distributor, third rotary distributor,
Powder rotary distributor, several batch bins, the first burden balance, the second burden balance, Manual material feeding mouth, double-shaft mixer, scraper plate,
5th bucket elevator, first bucket elevator connect the powder receiving sieve, and the powder receiving sieve connects the powder
Expect that rotary distributor, the powder rotary distributor are separately connected batch bin described in part, the third bucket elevator connects
Second rotary distributor is connect, second rotary distributor is separately connected batch bin device described in part, the 4th bucket
Formula elevator connects the third rotary distributor, and the third rotary distributor is separately connected batch bin device described in part,
Batch bin described in part connects first burden balance jointly, is left the batch bin and connects second ingredient jointly
Scale, first burden balance, second burden balance and the Manual material feeding mouth connect the double-shaft mixer jointly, described double
Axis mixing machine connects the scraper plate, and the scraper plate connects the 5th bucket elevator.
Based on the above-mentioned technical proposal, powder and smashed particulate material can be subjected to ingredient mixing.In mixed process, by
Have in the second rotary distributor, third rotary distributor, powder rotary distributor and each batch bin different public and independent
Second rotary distributor, third rotary distributor and powder rotary distributor can be combined by the connection type of connection, from
And the different material of combination is obtained in the first burden balance and the second burden balance.
Specifically, batch bin at least there are six, the powder rotary distributor be separately connected at least two described in ingredient
Storehouse, second rotary distributor be separately connected at least three described in batch bin, the third rotary distributor is separately connected
Batch bin described at least four, the powder rotary distributor and the third rotary distributor at least share described in one
Batch bin, the powder rotary distributor at least individually connect one described in batch bin, the third rotary distributor and institute
State the second rotary distributor at least share two described in batch bin, the third rotary distributor at least individually connect an institute
The batch bin stated, second rotary distributor at least individually connect one described in batch bin.
Specifically, at least one described second rotary distributor individually connect the batch bin, described at least one
The batch bin and at least one described third that third rotary distributor and second rotary distributor share rotate
The batch bin that distributor individually connects connects first burden balance jointly；At least one described third rotary distributor
The batch bin, at least one described powder rotary distributor and the third shared with second rotary distributor is revolved
Turn the ingredient that the shared batch bin of distributor and at least one described powder rotary distributor individually connect
Storehouse connects second burden balance jointly.
Specifically, the granulation workshop section includes the second pipe magnetic separator, the 4th rotary distributor and distributes with the 4th rotation
Device connection at least two granulation lines, each granulation line include the storehouse to be pelletized for being sequentially connected setting, feeder, modulator,
Granulator, cooling blower, counterflow cooler, crusher and the 6th bucket elevator, the 5th bucket elevator connect institute
The second pipe magnetic separator is stated, the second pipe magnetic separator connects the 4th rotary distributor.
Based on the above-mentioned technical proposal, the mixed material of ingredient can be pelletized in batches.
Specifically, the bale room include at least two pack threads, the pack thread include revolution classifying screen, respectively with
At least two finished bins of the revolution classifying screen connection setting, the first packing for connecting setting jointly with each finished bin
Scale and the seam packet conveying combination machine that setting is connect with first packaging scale, the corresponding connection of each revolution classifying screen
6th bucket elevator described in one.
Based on the above-mentioned technical proposal, the material after granulation can be packaged, obtains finished product.
Further, it is provided with the first threeway between the third bucket elevator and second rotary distributor,
First threeway be also connected with one described in storehouse to be comminuted.
Based on the above-mentioned technical proposal, it is the material sufficiently crushed by pulverizer, re-starts crushing.
Further, it is additionally provided with the second threeway between the 5th bucket elevator and second pipe magnetic separator, institute
It states the second threeway and is also connected with the batch bin that a powder rotary distributor individually connects.
Based on the above-mentioned technical proposal, matching in batch bin can be participated in again using the mixed material of ingredient as mixture
Material process.
Further, the 4th rotary distributor be also connected with one described in finished bin.
Based on the above-mentioned technical proposal, the material after material that ingredient is mixed to get and granulation can be mixed in finished bin
It closes.Further, feed production system is additionally provided with third pulse dust collector, and the third pulse dust collector is separately connected described
First bucket elevator, the second bucket elevator, third bucket elevator, the 4th bucket elevator, the 5th bucket elevator and
Each 6th bucket elevator.
Based on the above-mentioned technical proposal, each bucket elevator can be dusted.
Further, the bale room is additionally provided with the second packaging scale, described in the finished bin described in one and one
The first packaging scale between be provided with third threeway, the third threeway is also connected with second packaging scale.
Further, feed production system is additionally provided with several 4th pulse dust collectors, each first packaging scale and institute
State the second packaging scale be connected separately with one described in the 4th pulse dust collector.
Based on the above-mentioned technical proposal, each packaging scale can be dusted.
Further, feed production system is additionally provided with grease addition equipment, and the grease addition equipment connection is described double
Axis mixing machine.
Based on the above-mentioned technical proposal, it can need to add grease according to what feed configured.
Feed production system provided by the utility model, using the mixed characteristic of mixing machine, by all feeds and feed
Additive raw material is uniformly mixed, and the material of certain granules is made of granulator.It, can will be various according to the needs of factory formula
Feed and raw materials of feed additives are mixed into concentrated feed or mixed feed, and particle is made.To intermediate mixed process, provide
More hybrid mode, extends the applicability of system, so as to be suitable for the production of birds or aquatic feeds.
Detailed description of the invention
Fig. 1 is the system diagram of feed production system provided by the utility model.
In attached drawing 1, structure list representated by each label is as follows:
101, powder feeding port, the 102, first pulse dust collector, the 103, first bucket elevator, 104, powder receiving sieve,
105, powder rotary distributor, 201, particulate material feeding port, the 202, second pulse dust collector, the 203, second elevator, 204,
Pellet receiving sieve, the 205, first pipe magnetic separator, the 206, first rotary distributor, 207, storehouse to be comminuted, 301, pulverizer, 302, third
Bucket elevator, the 303, first threeway, the 304, second rotary distributor, 401, micronizer, the 402, the 4th bucket lifting
Machine, 403, third rotary distributor, 404, batch bin, the 501, first burden balance, the 502, second burden balance, 503, Manual material feeding
Mouthful, 504, double-shaft mixer, 505, scraper plate, the 506, the 5th bucket elevator, the 507, second threeway, the 508, second pipe magnetic separator,
509, the 4th rotary distributor, 510, storehouse to be pelletized, 601, granulator, 602, modulator, 603, feeder, 604, reverse-flow cold
But device, 605, cooling blower, 606, crusher, the 607, the 6th bucket elevator, 608, revolution classifying screen, 609, finished bin,
610, third pulse dust collector, the 701, first packaging scale, 702, seam packet conveying combination machine, the 703, the 4th pulse dust collector.
Specific embodiment
The principles of the present invention and feature are described below, illustrated embodiment is served only for explaining the utility model,
It is not intended to limit the scope of the utility model.
In a specific embodiment, as described in Figure 1, feed production system includes the raw material reception for being sequentially connected setting
Workshop section, granulation workshop section and bale room are mixed with Chu Qing workshop section, break section, ingredient.
It includes powder feeding port 101, particulate material feeding port 201, the first bucket elevator 103 that raw material, which is received with Chu Qing workshop section,
Second elevator 203, powder feeding port 101 connect the first bucket elevator 103, and the connection of particulate material feeding port 201 second is promoted
Machine 203, powder feeding port 101 are provided with the first pulse dust collector 102, and particulate material feeding port 201 is provided with the second pulse dust removal
Device 202.
Break section includes particulate material receiving sieve 204, the first pipe magnetic separator 205, the first rotary distributor 206, four to powder
Broken storehouse 207, the first scroll feeder, the second scroll feeder, pulverizer 301, micronizer 401, third bucket elevator
302 and the 4th bucket elevator 402.Second elevator 203, particulate material receiving sieve 204, the first pipe magnetic separator 205 and the first rotation
Distributor 206 is sequentially connected setting.First rotary distributor 206 is separately connected each storehouse to be comminuted 207, two storehouses 207 to be comminuted
The first scroll feeder is connected, the first scroll feeder connects pulverizer 301.Two storehouses 207 to be comminuted connect the second spiral and feed
Glassware, the second scroll feeder connect micronizer 401, and pulverizer 301 connects third bucket elevator 302, pulverize
Machine 401 connects the 4th bucket elevator 402.
It includes powder receiving sieve 104, the second rotary distributor 304, third rotary distributor 403, powder that ingredient, which mixes workshop section,
Expect 105,18 batch bins 404 of rotary distributor, it is the first burden balance 501, the second burden balance 502, Manual material feeding mouth 503, double
Axis mixing machine 504, scraper plate 505, the 5th bucket elevator 506.First burden balance 501, the second burden balance 502 and Manual material feeding
Connection double-shaft mixers 504, double-shaft mixer 504 connect scraper plate 505 to mouth 503 jointly, and scraper plate 505 connects the 5th bucket elevator
506.The first threeway 303 is provided between third bucket elevator 302 and the second rotary distributor 304, the first threeway 303 is also
The storehouse to be comminuted 207 of connection one
First bucket elevator 103 connects powder receiving sieve 104, and powder receiving sieve 104 connects powder rotary distributor
105, powder rotary distributor 105 is separately connected six batch bins 404.
Third bucket elevator 302 connects the second rotary distributor 304, and the second rotary distributor 304 is separately connected ten
404 device of batch bin.
4th bucket elevator 402 connects third rotary distributor 403, and third rotary distributor 403 is separately connected eight
404 device of batch bin.
Powder rotary distributor 105 and third rotary distributor 403 share three batch bins 404, powder rotation distribution
Device 105 individually connects three batch bins 404.
Third rotary distributor 403 and the second rotary distributor 304 share three batch bins 404, third rotation distribution
Device 403 individually connects two batch bins 404.
Second rotary distributor 304 individually connects seven batch bins 404.
404, third rotary distributors 403 and second of batch bin that seven the second rotary distributors 304 individually connect
The batch bin 404 that the shared batch bin 404 of rotary distributor 304 and two third rotary distributors 403 individually connect
The first burden balance 501 of common connection.
404, three powders of batch bin that two third rotary distributors 403 and the second rotary distributor 304 share revolve
Turn the batch bin 404 shared with third rotary distributor 403 of distributor 105 and three powder rotary distributors 105 are independent
The batch bin 404 of connection connects the second burden balance 502 jointly.
Granulation workshop section includes the second pipe magnetic separator 508, the 4th rotary distributor 509 and connect with the 4th rotary distributor 509
Two granulation lines, each line of pelletizing includes the storehouse to be pelletized 510 for being sequentially connected setting, feeder 603, modulator 602, granulator
601, cooling blower 605, counterflow cooler 604, crusher 606 and the 6th bucket elevator 607, the 5th bucket elevator
506 the second pipe magnetic separators 508 of connection.The second threeway is additionally provided between the 5th bucket elevator 506 and the second pipe magnetic separator 508
507, the second threeway 507 is also connected with the batch bin 404 that a powder rotary distributor 105 individually connects.4th rotary distributor
509 are also connected with one finished bin 609.
Bale room includes two pack threads, and pack thread connects including revolution classifying screen 608, respectively with revolution classifying screen 608
Connect two finished bins 609 of setting, with each finished bin 609 jointly connect setting the first packaging scale 701 and with first dozen
The seam packet conveying combination machine 702 of the connection setting of packet scale 701, each the 6th bucket for turning round the corresponding connection one of classifying screen 608
Formula elevator 607.Bale room is additionally provided with the second packaging scale, in one finished bin 609 and one the first packaging scale 701
Between be provided with third threeway, third threeway is also connected with the second packaging scale.
Feed production system is additionally provided with 610, three the 4th pulse dust collectors 703 and one of a third pulse dust collector
A grease adds equipment.Third pulse dust collector 610 is separately connected the first bucket elevator 103, the second bucket elevator, third
Bucket elevator 302, six bucket elevator 607 of the 4th bucket elevator 402, the 5th bucket elevator 506 and Ge.Each first
Packaging scale 701 and the second packaging scale are connected separately with one the 4th pulse dust collector 703.It is mixed that grease adds equipment connection twin shaft
Conjunction machine 504.
The workflow of this system is as follows:
1, raw material receives and Chu Qing workshop section:
It is not required to the raw material crushed to be put at powder feeding port 101, mention through the first bucket elevator 103 to highest point,
After powder receiving sieve 104 is just clear, through powder rotary distributor 105, enter in batch bin 13-18.
The raw material for needing to crush through at particulate material feeding port 201 put into, mention through the second elevator 203 to highest point, through
Pellet receiving sieve 204 just clearly after the first pipe magnetic separator 205, through the first rotary distributor 206, enters in storehouse 1-4 to be comminuted.
2, break section:
The raw material for entering storehouse 1-2 to be comminuted is sent in pulverizer 301 through the first scroll feeder, crushing rear material warp
Third bucket elevator 302 is promoted, can be into 1-8 or 11-12 batch bin through the first threeway 303, can also be into be comminuted
Again through pulverizing in storehouse 4.The raw material for entering storehouse 3-4 to be comminuted is sent to micronizer through the second scroll feeder
In 401, crushing rear material is promoted through the 4th bucket elevator 402, into 8-15 batch bin.
3, ingredient mixes workshop section:
When production, bulk raw material from 1-10 batch bin through 501 ingredient of the first burden balance, match from No. 11-18 by a small amount of raw material
Feed bin feeds intake, grease is through liquid after additive premix ingredient from artificial adding mouth 503 through 502 ingredient of the second burden balance
Body add-on system adds, and after ingredient, is added in mixing machine, automatic to release after mixing a period of time, by 505 water of scraper plate
Flat to be transferred to the 5th bucket elevator 506, ingredient mixes substandard product and is back to No. 18 batch bins through the second threeway 507, matches
After 508 de-iron of the second pipe magnetic separator, the product for needing to pelletize can enter material mixing qualified products through the 4th rotary distributor 509
Into storehouse 510 to be pelletized, powder product can be entered in finished bin 1 with the 4th rotary distributor 509.
4, pelletize workshop section:
The product in batch bin is entered, through 603 feeding of feeder, is cured into modulator 602, into granulator 601
Granulation, cooling in counterflow cooler 604 under the action of high pressure blower 605, boosted machine 607 broken through crusher 606
It is promoted and isolates the product of suitable granularity in revolution classifying screen and enter in finished bin 609；The product of improper granularity can divide
It does not enter in granulator and is crushed in granulation or crusher.
5, bale room:
Powder is picked out from finished bin 1, and pellet is picked out from finished bin 1,2,3,4.
Implementation result:
The product mix uniformity: concentrated feed, the mixed feed mixture homogeneity coefficient of variation are not more than 7%.
Dust concentration: (1) concentration of emission :≤150mg/m3；(2) other regions :≤10mg/m3
The above is only the preferred embodiment of the present invention, is not intended to limit the utility model, all practical at this
Within novel spirit and principle, any modification, equivalent replacement, improvement and so on should be included in the guarantor of the utility model
Within the scope of shield.
Claims (7)
1. a kind of feed production system, which is characterized in that the raw material including being sequentially connected setting receives and Chu Qing workshop section, grinders
Section, ingredient mixing workshop section, granulation workshop section and bale room；
It includes powder feeding port (101), particulate material feeding port (201), the first bucket lifting that the raw material, which is received with Chu Qing workshop section,
Machine (103) and the second elevator (203), the powder feeding port (101) connects first bucket elevator (103), described
Particulate material feeding port (201) connects second elevator (203)；
The break section includes particulate material receiving sieve (204), the first pipe magnetic separator (205), the first rotary distributor (206), extremely
Few two storehouses (207) to be comminuted, the first scroll feeder, the second scroll feeder, pulverizer (301), micronizer
(401), third bucket elevator (302) and the 4th bucket elevator (402), second elevator (203), the particulate material
Receiving sieve (204), first pipe magnetic separator (205) and first rotary distributor (206) are sequentially connected setting, and described first
Rotary distributor (206) is separately connected each storehouse (207) to be comminuted, and the storehouse to be comminuted (207) described at least one connects institute
The first scroll feeder is stated, first scroll feeder connects the pulverizer (301), the storehouse to be comminuted described at least one
(207) second scroll feeder is connected, second scroll feeder connects micronizer (401), the pulverizer
(301) the third bucket elevator (302) is connected, the micronizer (401) connects the 4th bucket elevator
(402)；
Ingredient mixing workshop section includes powder receiving sieve (104), the second rotary distributor (304), third rotary distributor
(403), powder rotary distributor (105), several batch bins (404), the first burden balance (501), the second burden balance (502),
Manual material feeding mouth (503), double-shaft mixer (504), scraper plate (505), the 5th bucket elevator (506), first bucket type mention
It rises machine (103) and connects the powder receiving sieve (104), the powder receiving sieve (104) connects the powder rotary distributor
(105), the powder rotary distributor (105) is separately connected batch bin described in part (404), the third bucket elevator
(302) second rotary distributor (304) is connected, second rotary distributor (304), which is separately connected described in part, matches
Feed bin (404) device, the 4th bucket elevator (402) connect the third rotary distributor (403), the third rotation point
Orchestration (403) is separately connected batch bin described in part (404) device, and batch bin (404) described in part connects described jointly
One burden balance (501) are left the batch bin (404) and connect second burden balance (502), first burden balance jointly
(501), second burden balance (502) and the Manual material feeding mouth (503) connect the double-shaft mixer (504), institute jointly
It states double-shaft mixer (504) and connects the scraper plate (505), the scraper plate (505) connects the 5th bucket elevator (506).
2. feed production system according to claim 1, it is characterised in that: the powder feeding port (101) is provided with
One pulse dust collector (102), the particulate material feeding port (201) are provided with the second pulse dust collector (202).
3. feed production system according to claim 2, it is characterised in that: batch bin (404) at least there are six, the powder
Material rotary distributor (105) be separately connected at least two described in batch bin (404), second rotary distributor (304) point
Not Lian Jie batch bin (404) described at least three, the third rotary distributor (403) is separately connected at least described in four
Batch bin (404), the powder rotary distributor (105) and the third rotary distributor (403) at least share described in one
Batch bin (404), the powder rotary distributor (105) at least independent batch bin (404) described in connection one, described the
Three rotary distributors (403) and second rotary distributor (304) at least share two described in batch bin (404), it is described
Batch bin (404) described in at least independent connection one of third rotary distributor (403), second rotary distributor (304)
Batch bin (404) described at least individually connecting one.
4. feed production system according to claim 3, it is characterised in that: at least one described second rotary distributor
(304) batch bin (404), at least one described third rotary distributor (403) and second rotation individually connected
Turn distributor (304) shared described batch bin (404) and at least one described third rotary distributor (403) individually connects
The batch bin (404) connect connects first burden balance (501) jointly；At least one described third rotary distributor
(403) batch bin (404), at least one the described powder shared with second rotary distributor (304) rotates and divides
The batch bin (404) and at least one described powder that orchestration (105) and the third rotary distributor (403) share
The batch bin (404) that rotary distributor (105) individually connects connects second burden balance (502) jointly.
5. feed production system according to claim 4, it is characterised in that: the granulation workshop section includes the second pipe magnetic separator
(508), the 4th rotary distributor (509) and at least two bars granulation lines being connect with the 4th rotary distributor (509), each institute
State granulation line include the storehouse to be pelletized (510) for being sequentially connected setting, feeder (603), modulator (602), granulator (601),
Cooling blower (605), counterflow cooler (604), crusher (606) and the 6th bucket elevator (607), the 5th bucket type
Elevator (506) connects second pipe magnetic separator (508), and second pipe magnetic separator (508) connects the 4th rotary distributor
(509)。
6. feed production system according to claim 5, it is characterised in that: the bale room is packaged including at least two
Line, the pack thread connect at least two of setting including revolution classifying screen (608), respectively with revolution classifying screen (608)
Finished bin (609) connect the first packaging scale (701) of setting with each finished bin (609) and with described first jointly
The seam packet conveying combination machine (702) of packaging scale (701) connection setting, the corresponding connection of each revolution classifying screen (608)
6th bucket elevator (607) described in one.
7. feed production system according to claim 6, it is characterised in that:
The first threeway is provided between the third bucket elevator (302) and second rotary distributor (304)
(303), first threeway (303) be also connected with one described in storehouse (207) to be comminuted；
The second threeway (507) are additionally provided between the 5th bucket elevator (506) and second pipe magnetic separator (508),
Second threeway (507) is also connected with the batch bin (404) that a powder rotary distributor (105) individually connects；
4th rotary distributor (509) be also connected with one described in finished bin (609)；
Feed production system is additionally provided with third pulse dust collector (610), and the third pulse dust collector (610) is separately connected institute
State the first bucket elevator (103), the second bucket elevator, third bucket elevator (302), the 4th bucket elevator (402),
5th bucket elevator (506) and each 6th bucket elevator (607)；
The bale room is additionally provided with the second packaging scale, first dozen described in the finished bin (609) described in one and one
Third threeway is provided between packet scale (701), the third threeway is also connected with second packaging scale；
Feed production system is additionally provided with several 4th pulse dust collectors (703), each first packaging scale (701) and described
Two packaging scales be connected separately with one described in the 4th pulse dust collector (703)；
Feed production system is additionally provided with grease addition equipment, and the grease addition equipment connects the double-shaft mixer (504).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820631648.2U CN209152319U (en) | 2018-04-28 | 2018-04-28 | A kind of feed production system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820631648.2U CN209152319U (en) | 2018-04-28 | 2018-04-28 | A kind of feed production system |
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| Publication Number | Publication Date |
|---|---|
| CN209152319U true CN209152319U (en) | 2019-07-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201820631648.2U Active CN209152319U (en) | 2018-04-28 | 2018-04-28 | A kind of feed production system |
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| CN (1) | CN209152319U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113455680A (en) * | 2021-05-26 | 2021-10-01 | 河南广安生物科技股份有限公司 | High-efficient fodder production line |
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2018
- 2018-04-28 CN CN201820631648.2U patent/CN209152319U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113455680A (en) * | 2021-05-26 | 2021-10-01 | 河南广安生物科技股份有限公司 | High-efficient fodder production line |
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Effective date of registration: 20191121 Address after: Room 8, room 803-809, golden code Hotel, No. 100083, Haidian District, Beijing Co-patentee after: Hubei North Agricultural University Biotechnology Co., Ltd. Patentee after: Nongda Polytron Technologies Inc Address before: 432624 Wanqiao Village, Yandian Town, Anlu City, Xiaogan City, Hubei Province (No. 1 Xiaoxiang Road, New Street) Patentee before: Hubei North Agricultural University Biotechnology Co., Ltd. |