CN207252502U - A kind of pig farm liquid reactive fermented feed feeds system - Google Patents
A kind of pig farm liquid reactive fermented feed feeds system Download PDFInfo
- Publication number
- CN207252502U CN207252502U CN201720964588.1U CN201720964588U CN207252502U CN 207252502 U CN207252502 U CN 207252502U CN 201720964588 U CN201720964588 U CN 201720964588U CN 207252502 U CN207252502 U CN 207252502U
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- China
- Prior art keywords
- solenoid valve
- feed
- blending tank
- feeder
- flowmeter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- 239000007788 liquid Substances 0.000 title claims abstract description 20
- 238000002156 mixing Methods 0.000 claims abstract description 58
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 239000000463 material Substances 0.000 claims description 79
- 238000003756 stirring Methods 0.000 claims description 30
- 238000000034 method Methods 0.000 claims description 8
- 238000012935 Averaging Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 2
- 238000009434 installation Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 6
- 238000013459 approach Methods 0.000 abstract description 4
- 238000002360 preparation method Methods 0.000 abstract description 4
- 238000012545 processing Methods 0.000 abstract description 4
- 238000001514 detection method Methods 0.000 abstract description 3
- 230000003670 easy-to-clean Effects 0.000 abstract description 3
- 238000004801 process automation Methods 0.000 abstract description 3
- 208000023504 respiratory system disease Diseases 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 2
- 238000004140 cleaning Methods 0.000 description 5
- 238000009413 insulation Methods 0.000 description 5
- 230000002950 deficient Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 238000000855 fermentation Methods 0.000 description 3
- 230000004151 fermentation Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000003111 delayed effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000012840 feeding operation Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 235000011837 pasties Nutrition 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 238000011001 backwashing Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000021050 feed intake Nutrition 0.000 description 1
- 230000003031 feeding effect Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000036039 immunity Effects 0.000 description 1
- 230000007413 intestinal health Effects 0.000 description 1
- 239000000320 mechanical mixture Substances 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- Feeding And Watering For Cattle Raising And Animal Husbandry (AREA)
Abstract
The utility model discloses a kind of pig farm liquid reactive fermented feed to feed system, including the hole that feeds intake, conveyer, feed bin, feeder, blending tank, the first solenoid valve, product pump, first flowmeter, feeding trough, water inlet pipe, second flowmeter, second solenoid valve, backwash water pipe, the 3rd solenoid valve, controller.The utility model makes full use of the value characteristic and combustion characteristic of high-activity fermented feed, the technological approaches fed using liquid, use process automation, control levels of precision high, feed processing preparation cost is low, and Viable detection is high, reduces porcine respiratory disease incidence, reduce feed waste, it is easy to clean during the system use.
Description
Technical field
A kind of pig farm feed feeding system is the utility model is related to, belongs to cultivation feeding equipment field, is specifically related to one
Kind pig farm liquid reactive fermented feed feeding system.
Background technology
Not only nutritive value enriches high-activity fermented feed, can be supplied to the nutriment needed for raising pig, at the same time
Again because of the beneficial viable bacteria containing high level, the intestinal health for raising pig has significant application effect, feeding high living
Property fermented feed can improve the growth performance of pig, strengthen immunity, improves many beneficial effects such as efficiency of feed utilization.
At present, fermented feed generally has two kinds of application approaches, and one kind is to be added in mixed feed that sizing is made by feed factory
Compound feed products, then it is sold to pig farm use；Another kind is to be added in other raw materials to match somebody with somebody when from dispensing by pig farm
Conventional daily ration is made to be fed.Both the above approach, being limited by fermented feed will be just easy to use by drying process so that hair
The viable bacteria of high level is greatly affected in ferment feed, and feeding effect is deteriorated, and feed processing cost also improves.
If a kind of new feeding application method can be provided, the value characteristic of high-activity fermented feed can be made full use of,
It is of low cost that preparation is processed at the same time, it will for pig raising, enterprise brings more economic values.
The content of the invention
In view of the above-mentioned problems, the utility model aims to provide a kind of pig farm liquid reactive fermented feed feeding system, this is
System makes full use of the value characteristic and combustion characteristic of high-activity fermented feed, and the technological approaches fed using liquid, is used
Process automation, control levels of precision is high, and feed processing preparation cost is low, and Viable detection is high, reduces porcine respiratory disease hair
Sick rate, reduces feed waste, easy to clean during the system use.
To realize the technical purpose, the embodiment of the utility model is：A kind of pig farm liquid reactive fermented feed feeds system,
Including the hole that feeds intake, conveyer, feed bin, feeder, blending tank, the first solenoid valve, product pump, first flowmeter, feeding trough, water inlet
Pipe, second flowmeter, second solenoid valve, backwash water pipe, the 3rd solenoid valve, controller, the feed bin is by conveyer with throwing
Material hole is connected, and the bin bottom installs feeder, and the discharge port of feeder is stretched into blending tank, the lower part of the blending tank
Discharge port is connected with the first solenoid valve, product pump, first flowmeter and feeding trough successively by material delivery pipe, the recoil
Wash water pipe is accessed on the material conveying pipe between the first solenoid valve and product pump, and the 3rd solenoid valve is installed on backwashing water
Guan Shang, the water inlet pipe are communicated with blending tank, and second flowmeter and second solenoid valve are set in water inlet pipe, the feeder, the
One solenoid valve, product pump, first flowmeter, second flowmeter, second solenoid valve and the 3rd solenoid valve Method of Averaging Controller are electrically connected.
Preferably, deduster is further included, deduster is arranged on the top in the hole that feeds intake.
Preferably, the conveyer is has one's face covered with formula screw conveyor, and conveyer from feed inlet to discharge port pitch successively
Increase.
Preferably, vibrator is further included, the vibrator is arranged on the outer bulkhead of feed bin.
Preferably, the variable-pitch auger conveyer that the feeder is sequentially increased from feed inlet to discharge port for pitch.
Preferably, discharge gate is further included, the discharge gate is arranged on the discharge port of feeder.
Preferably, the blending tank includes mixing tank body, water-bath chuck, electrothermal tube, agitating shaft, stirring motor, inside spin
Ribbon, external spiral stirring ribbon, temperature sensor are stirred, the water-bath chuck is arranged on outside blending tank body, and electrothermal tube is set
In water-bath chuck, the temperature sensor is arranged in blending tank body, the electrothermal tube and temperature sensor and controller electricity
Connection, inside spin stirring ribbon and external spiral the stirring ribbon are arranged on agitating shaft, the agitating shaft and stirring motor
It is connected.
The operation principle of the utility model：
Before use, the batch operating duration of feeder is set on the controller, sets the batch flow control of second flowmeter
Value processed, the material insulating value for setting blending tank, the startup run time point and corresponding material flow of each time point for setting product pump
Amount, the time point of the 3rd electromagnetism valve timing start and stop of setting.
When starting from liquid reactive fermented feed, start conveyer and deduster, deduster ensures that production environment is not produced
Fecula dirt.Wet fermentation feed is delivered in feed bin from the hole input that feeds intake, material by conveyer.Since conveyer is formula spiral shell of having one's face covered with
Conveyer is revolved, and the pitch of conveyer is sequentially increased from feed inlet to discharge port pitch, particularly suitable for the wet of various water content
Fermented feed, no matter whether transported material material has viscosity, and conveyer can avoid material from extruding, make thing during conveying
Material keeps loose condition (of surface), is conducive to material conveying.
Start the stirring motor on blending tank, agitating shaft, which is opened, to be rotated.Start feeder operating from controller, shake at the same time
Dynamic device is started to work, while discharge gate is opened.Feeder, vibrator and discharge gate are chain control, when feeder operates,
Vibrator is started to work, and discharge gate is opened；When feeder stops, vibrator is stopped, and discharge gate is closed.Feeder will
Material in feed bin is uniformly delivered in blending tank, when the batch operating duration of feeder reaches the setting value on controller,
Feeder shuts down, and vibrator is stopped, and discharge gate is closed.Due to the cooperation of vibrator, feeder and discharge gate
Work allow feeder to discharge stabilization, secures the operating duration of feeder, that is, controls batches additive amount, discharging
Material caused by gate also further avoid vibration equipment is additionally spilled into blending tank out of feeder, and the batch of material adds
Dosage can be more accurate with control ratio.
Feeder charging is completed after stopping, and is controlled by the controller, and second solenoid valve is opened, because water inlet pipe water inlet accesses
Water source is cleaned, clean clear water flows through second flowmeter and second solenoid valve enters in blending tank, when the reality for flowing through second flowmeter
When Shi Liuliang is equal to the batch flow control value set on controller, second solenoid valve is controlled by the controller and closes immediately, stops
Add water.
Material and water in blending tank are acted on by inside spin stirring ribbon on agitating shaft and external spiral stirring ribbon, equal
Even stirring.Inside spin stirs the oppositely oriented setting of ribbon and external spiral stirring ribbon, and mixed material is subject to stronger machine
Tool mixes shear action, and material can be made into homogeneous slurry.
When agitating shaft starts running in blending tank, being controlled by controller, electrothermal tube begins to warm up the water in water-bath chuck,
Water-bath chuck carries out indirectly heat and insulation to blending tank.
Temperature sensor is stretched into blending tank, measures the material temperature of the mixture in blending tank in real time.When temperature sensor is real
When measuring material temperature in blending tank and being equal to the blending tank material insulating value that controller has been set, controller control electrothermal tube stops
Heating.According to the process of thermometric-heating and thermal insulation as above, temperature control is carried out to the material in blending tank, makes material material temperature constant.
When setting the run time point of material pump startup on time is up controller, it is controlled by the controller, the first electromagnetism
Valve is opened, material pump startup, and homogeneous pasty material flows through the first solenoid valve, product pump and first-class from pipeline in blending tank
Gauge is reached in feeding trough.When the real-time material flow value for flowing through first flowmeter is equal to the setting value on controller, first
Solenoid valve is closed immediately, and product pump stops immediately.
Because setting the time point of the 3rd electromagnetism valve timing start and stop, the time of the 3rd solenoid valve time opening on the controller
Point is routed in feeding trough after material terminates substantially by pig feeding, and the time point that the timing of the 3rd solenoid valve is closed is peace
Come after the 3rd solenoid valve is opened and be delayed a period of time, this time can flexibly be grasped according to the needs of use site.
When terminate to one batch feeding operation of feeding trough and in feeding trough material by pig feeding it is basic after, the time
To the time point of the 3rd solenoid valve time opening, the 3rd solenoid valve, product pump are controlled by the controller unlatching, backwash in water pipe
Cleaning water source washings pipe material, product pump, first flowmeter, and will rinse in defective material water injection feeding trough, pig can be with
Residue has been searched for food.While making full use of the residue material in pipeline, maintenance is rinsed to material pipe and equipment, is avoided
It is solid and rotten after material long-time in pipeline, ensure that the performance of equipment is unaffected.
3rd solenoid valve and product pump can also be opened and closed by way of manually controlling controller, flexibly right
Material pipe and equipment are rinsed attended operation.
The beneficial effects of the utility model are：
（1）Process automation is operated with, material adds and adds water to be automatically performed.
（2）Blending tank has automatic heat insulating function, is uniformly mixed, and the homogeneous quality of quality of material of preparation is high.
（3）It is high to operate control accuracy.Add materials and lead to water, mixed material insulation, mixed material addition by controller
The component such as overcurrent gauge or temperature sensor completes accurate control.
（4）Feed formulation cost is low.Operating process whole process needs the place of manual control to lack, and pole can be obtained by preparing cost
Big control.
（5）Viable detection is high.Fermented feed avoids high temperature drying processing, and blending tank has automatic heat insulating function,
Viable bacteria can be effectively retained.
（6）By the way of liquid feeding, material dust will not produce during feeding, reduce porcine respiratory disease incidence,
Feed is not easy to be dug feeding trough, and the cleaning defective material slag of pipeline is all utilized effectively, and substantially reduces feed waste.
（7）It is easy to clean after use.Backwash water pipe is added in the system of the utility model, has been controlled by controller
Into the cleaning of material conveying pipe and conveying equipment, ejected wash water and defective material slag are directly entered in feeding trough.
Brief description of the drawings
Fig. 1 is that a kind of pig farm liquid reactive fermented feed of the utility model feeds the flow diagram of system.
Fig. 2 is the structure diagram of blending tank in the utility model.
Fig. 3 is the cross-sectional view of feeding trough in the utility model.
Description of reference numerals：
1- feed intake hole, 2- dedusters, 3- conveyers, 4- feed bins, 5- vibrators, 6- feeders, 7- discharge gates, 8- mixing
Tank, the first solenoid valves of 9-, 10- product pumps, 11- first flowmeters, 12- feeding troughs, 13- water inlet pipes, 14- second flowmeters, 15-
Second solenoid valve, 16- backwashes water pipe, the 3rd solenoid valves of 17-, 18- controllers；
801- mixing tank body, 802- water-baths chuck, 803- electrothermal tubes, 804- agitating shafts, 805- stirring motors, spiral shell in 806-
Rotation stirring ribbon, 807- external spirals stirring ribbon, 808- temperature sensors.
Embodiment
This and specific embodiment are described in further details the utility model below in conjunction with the accompanying drawings.
As shown in FIG. 1 to 3, a kind of pig farm liquid reactive fermented feed feeding system of the utility model embodiment, bag
Include the hole 1 that feeds intake, conveyer 3, feed bin 4, feeder 6, blending tank 8, the first solenoid valve 9, product pump 10, first flowmeter 11, adopt
Crib 12, water inlet pipe 13, second flowmeter 14, second solenoid valve 15, backwash water pipe 16, the 3rd solenoid valve 17, controller 18,
The feed bin 4 is connected by conveyer 3 with the hole 1 that feeds intake, and feeder 6, the discharge port of feeder 6 are installed in 4 bottom of feed bin
Stretch into blending tank 8, the lower part discharge port of the blending tank 8 by material delivery pipe successively with the first solenoid valve 9, product pump
10th, first flowmeter 11 is connected with feeding trough 12, and the backwash water pipe 16 is accessed between the first solenoid valve 9 and product pump 10
Material conveying pipe on, the 3rd solenoid valve 17 be installed on backwash water pipe 16 on, the water inlet pipe 13 and 8 phase of blending tank
It is logical, in water inlet pipe 13, second flowmeter 14 and second solenoid valve 15 be set, the feeder 6, the first solenoid valve 9, product pump 10,
First flowmeter 11, second flowmeter 14, second solenoid valve 15 and 17 Method of Averaging Controller 18 of the 3rd solenoid valve are electrically connected.
Preferably, deduster 2 is further included, deduster 2 is arranged on the top in the hole 1 that feeds intake.
Preferably, the conveyer 3 is has one's face covered with formula screw conveyor, and conveyer 3 from feed inlet to discharge port pitch according to
Secondary increase.
Preferably, vibrator 5 is further included, the vibrator 5 is arranged on the outer bulkhead of feed bin 4.
Preferably, the variable-pitch auger conveyer that the feeder 6 is sequentially increased from feed inlet to discharge port for pitch.
Preferably, discharge gate 7 is further included, the discharge gate 7 is arranged on the discharge port of feeder 6.
Preferably, the blending tank 8 includes mixing tank body 801, water-bath chuck 802, electrothermal tube 803, agitating shaft 804, stirs
Motor 805, inside spin stirring ribbon 806, external spiral stirring ribbon 807, temperature sensor 808 are mixed, the water-bath chuck 802 is set
Put outside mixing tank body 801, electrothermal tube 803 is arranged in water-bath chuck 802, and the temperature sensor 808 is arranged on mixing
In tank body 801, the electrothermal tube 803 and temperature sensor 808 are electrically connected with controller 18, and the inside spin stirs ribbon 806
It is arranged at external spiral stirring ribbon 807 on agitating shaft 804, the agitating shaft 804 is connected with stirring motor 805.
The operation principle of the utility model：
Before use, the batch operating duration of feeder 6 is set on controller 18, sets the batch stream of second flowmeter 14
It is corresponding to measure controlling value, the material insulating value for setting blending tank 8, the startup run time point of setting product pump 10 and each time point
Mass flow, the time point for setting the 17 timing start and stop of the 3rd solenoid valve.
When starting from liquid reactive fermented feed, start conveyer 3 and deduster 2, deduster 2 ensures production environment not
Produce dust.Wet fermentation feed is delivered in feed bin 4 from the input of hole 1 that feeds intake, material by conveyer 3.Since conveyer 3 is full
Face formula screw conveyor, and the pitch of conveyer 3 is sequentially increased from feed inlet to discharge port pitch, particularly suitable for various aqueous
The wet fermentation feed of amount, no matter whether transported material material has viscosity, and conveyer 3 can avoid material from squeezing during conveying
Pressure, makes material keep loose condition (of surface), is conducive to material conveying.
Start the stirring motor 805 on blending tank 8, agitating shaft 804, which is opened, to be rotated.Start feeder 6 from controller 12
Operating, while vibrator 5 is started to work, while discharge gate 7 is opened.Feeder 6, vibrator 5 and discharge gate 7 are chain control
System, when feeder 6 operates, vibrator 5 is started to work, and discharge gate 7 is opened；When feeder 6 stops, vibrator 5 is stopped,
Discharge gate 7 is closed.Material in feed bin 4 is uniformly delivered in blending tank 8 by feeder 6, when the batch operating of feeder 6
When length reaches the setting value on controller 18, feeder 6 shuts down, and vibrator 5 is stopped, and discharge gate 7 is closed.Due to
The cooperating of vibrator 5, feeder 6 and discharge gate 7 allows feeder to discharge stabilization, secures the fortune of feeder 6
Turn duration, that is, control batches additive amount, material caused by discharge gate 7 also further avoid vibration equipment is from feeding
Additionally it is spilled into blending tank 8 in device 6, the batch additive amount of material can be more accurate with control ratio.
The charging of feeder 6 is completed after stopping, and is controlled by controller 18, second solenoid valve 15 is opened, because water inlet pipe 13 is intake
Mouth has accessed cleaning water source, and clean clear water flows through second flowmeter 14 and second solenoid valve 15 enters in blending tank 8, when flowing through the
When the real-time traffic of two flowmeters 14 is equal to the batch flow control value set on controller 18, second solenoid valve 15 is by controller
18 controls are closed immediately, stop adding water.
Material and water in blending tank 8 are stirred ribbon 807 by inside spin stirring ribbon 806 and external spiral on agitating shaft 804
Effect, by uniform stirring.Inside spin stirs the oppositely oriented setting of ribbon 806 and external spiral stirring ribbon 807, mixed material
It is subject to stronger mechanical mixture shear action, material can be made into homogeneous slurry.
When agitating shaft 804 starts running in blending tank 8, by the control of controller 18, electrothermal tube 803 begins to warm up water-bath folder
Water in set 802, water-bath chuck 802 carry out indirectly heat and insulation to blending tank 8.
Temperature sensor 808 is stretched into blending tank 8, measures the material temperature of the mixture in blending tank 8 in real time.Work as temperature sensing
When the material temperature that device 808 measures in blending tank 8 in real time is equal to the 8 material insulating value of blending tank that controller 18 has been set, controller 18
Electrothermal tube 803 is controlled to stop heating.According to the process of thermometric-heating and thermal insulation as above, the material in blending tank 8 is controlled
Temperature, makes material material temperature constant.
When setting the run time point that product pump 10 starts on time is up controller 18, controlled by controller 18, the
One solenoid valve 9 is opened, and product pump 10 starts, and homogeneous pasty material flows through the first solenoid valve 9, thing from pipeline in blending tank 8
Material pump 10 and first flowmeter 11 are reached in feeding trough 12.When the real-time material flow value for flowing through first flowmeter 11 is equal to control
During setting value on device 18, the first solenoid valve 9 is closed immediately, and product pump 10 stops immediately.
Because setting the time point of 17 timing start and stop of the 3rd solenoid valve, 17 time opening of the 3rd solenoid valve on controller 18
Time point be routed in feeding trough 12 after material terminates substantially by pig feeding, what the 3rd solenoid valve 17 was periodically closed
Time point is routed in after the 3rd solenoid valve 17 is opened and is delayed a period of time, this time can need spirit according to use site
It is living to grasp.
When terminate to 12 1 batch feeding operation of feeding trough and in feeding trough 12 material by pig feeding it is basic after,
The time point of time is up 17 time opening of the 3rd solenoid valve, the 3rd solenoid valve 17, product pump 10 are controlled by controller 18 and opened,
Cleaning water source washings pipe material, product pump 10 in backwash water pipe 16, first flowmeter 11, and the injection of defective material water will be rinsed
In feeding trough 12, pig can search for food residue.While making full use of the residue material in pipeline, to material pipe and set
It is standby to be rinsed maintenance, avoid solid and rotten after material long-time in pipeline, ensure that the performance of equipment is unaffected.
3rd solenoid valve 17 and product pump 10 can also be opened and closed by way of manually controlling controller 18,
Attended operation flexibly is rinsed to material pipe and equipment.
The above, is only the preferred embodiment of the utility model, is not intended to limit the utility model, every according to this
Any trickle amendment, equivalent substitution and the improvement that the technical spirit of utility model makees above example, should be included in this
Within the protection domain of utility model technical solution.
Claims (7)
1. a kind of pig farm liquid reactive fermented feed feeds system, it is characterised in that：Including the hole that feeds intake, conveyer, feed bin, feeding
It is device, blending tank, the first solenoid valve, product pump, first flowmeter, feeding trough, water inlet pipe, second flowmeter, second solenoid valve, anti-
Wash tub pipe, the 3rd solenoid valve, controller, the feed bin are connected by conveyer with the hole that feeds intake, the bin bottom installation
Feeder, the discharge port of feeder are stretched into blending tank, the lower part discharge port of the blending tank by material delivery pipe successively with
First solenoid valve, product pump, first flowmeter are connected with feeding trough, and the backwash water pipe accesses the first solenoid valve and material
On material conveying pipe between pump, the 3rd solenoid valve is installed on backwash water pipe, the water inlet pipe and blending tank phase
It is logical, in water inlet pipe, second flowmeter and second solenoid valve, the feeder, the first solenoid valve, product pump, first flow are set
Meter, second flowmeter, second solenoid valve and the 3rd solenoid valve Method of Averaging Controller are electrically connected.
A kind of 2. pig farm liquid reactive fermented feed feeding system as claimed in claim 1, it is characterised in that：Further include dedusting
Device, deduster are arranged on the top in the hole that feeds intake.
A kind of 3. pig farm liquid reactive fermented feed feeding system as claimed in claim 1, it is characterised in that：The conveyer
For formula screw conveyor of having one's face covered with, and conveyer is sequentially increased from feed inlet to discharge port pitch.
A kind of 4. pig farm liquid reactive fermented feed feeding system as claimed in claim 1, it is characterised in that：Further include vibration
Device, the vibrator are arranged on the outer bulkhead of feed bin.
A kind of 5. pig farm liquid reactive fermented feed feeding system as claimed in claim 1, it is characterised in that：The feeder
The variable-pitch auger conveyer being sequentially increased from feed inlet to discharge port for pitch.
A kind of 6. pig farm liquid reactive fermented feed feeding system as claimed in claim 1, it is characterised in that：Further include discharging
Gate, the discharge gate are arranged on the discharge port of feeder.
A kind of 7. pig farm liquid reactive fermented feed feeding system as claimed in claim 1, it is characterised in that：The blending tank
Including mixing tank body, water-bath chuck, electrothermal tube, agitating shaft, stirring motor, inside spin stirring ribbon, external spiral stirring ribbon, temperature
Sensor is spent, the water-bath chuck is arranged on outside blending tank body, and electrothermal tube is arranged in water-bath chuck, the temperature sensor
It is arranged in blending tank body, the electrothermal tube and temperature sensor are electrically connected with the controller, inside spin stirring ribbon and outer
Auger ribbon is arranged on agitating shaft, and the agitating shaft is connected with stirring motor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720964588.1U CN207252502U (en) | 2017-08-03 | 2017-08-03 | A kind of pig farm liquid reactive fermented feed feeds system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720964588.1U CN207252502U (en) | 2017-08-03 | 2017-08-03 | A kind of pig farm liquid reactive fermented feed feeds system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207252502U true CN207252502U (en) | 2018-04-20 |
Family
ID=61928099
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720964588.1U Expired - Fee Related CN207252502U (en) | 2017-08-03 | 2017-08-03 | A kind of pig farm liquid reactive fermented feed feeds system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207252502U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113682613A (en) * | 2021-08-27 | 2021-11-23 | 广东智源机器人科技有限公司 | Food sealed storage device |
-
2017
- 2017-08-03 CN CN201720964588.1U patent/CN207252502U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113682613A (en) * | 2021-08-27 | 2021-11-23 | 广东智源机器人科技有限公司 | Food sealed storage device |
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Effective date of registration: 20211222 Address after: 518101 Building 2, row 3, Shasan shangxiawei third industrial zone, Shajing street, Bao'an District, Shenzhen City, Guangdong Province Patentee after: RONGHUA UNITED BIOLOG SCIENCE Address before: 518106 No. 1, shangshijia Shangnan Industrial Zone, Gongming street, Guangming New District, Shenzhen, Guangdong Patentee before: SHENZHEN BAIAOFEI BIOTECHNOLOGY CO.,LTD. |
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Granted publication date: 20180420 |