CN106820232B - A kind of mixed feed production system and its production method - Google Patents
A kind of mixed feed production system and its production method Download PDFInfo
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- CN106820232B CN106820232B CN201710268503.0A CN201710268503A CN106820232B CN 106820232 B CN106820232 B CN 106820232B CN 201710268503 A CN201710268503 A CN 201710268503A CN 106820232 B CN106820232 B CN 106820232B
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- spray
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Classifications
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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
-
- 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
- A23N17/004—Apparatus specially adapted for preparing animal feeding-stuffs for treating by application of heat, e.g. by means of potato cookers
-
- 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
- A23N17/005—Apparatus specially adapted for preparing animal feeding-stuffs for shaping by moulding, extrusion, pressing, e.g. pellet-mills
-
- 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
- A23N17/007—Apparatus specially adapted for preparing animal feeding-stuffs for mixing feeding-stuff components
Abstract
The invention discloses a kind of mixed feed production system and its production methods, the preliminary storage that feed prepares raw material is carried out by raw material transfer tank, material through raw material transfer tank lower part discharge port output is delivered in pulverizer by second conveyer to be crushed, so that the operational safety of production process is higher, in addition after the solid-liquid separator I that the material that pulverizer crushes also passes through pulverizer discharge port is separated by solid-liquid separation, branch, which be delivered in quenched tank, carries out modifier treatment, the solid-liquid separator II of conditioned treated material conditioned tank lower part feed opening connection again is separated by solid-liquid separation again, wherein liquid phase material is spray-dried to obtain granule materials, solid-phase material is granulated by pelletizer, the material after the granule materials of spray drying and pelletizer are granulated is stirred again and is mixed into required finished feed , so that production cost reduce and improve material recycle degree, realize the secondary economic value of production byproduct.
Description
Technical field
The present invention relates to pannage preparation field, especially a kind of compound pig feed production system and its production method.
Background technique
Pannage is as one of indispensable food in pork pig breeding process, due to the difference of cost and raw material, so that
Pannage needs whether, material mixing whether rotten to raw material sufficiently monitors in real time in production preparation process, this is not only
Consume a large amount of human and material resources, and but also the human cost of production preparation process is higher, and since pannage is producing
In the process usually can because of the liquid phase material separated solid content it is lower and the problem of lead to application difficult, lead to this part
Liquid phase material can neither outlet, treatment for reuse need to expend a large amount of fund again so that the secondary spending of this part is all the year round
Month after month become no small expenditure afterwards, if can production handle during in time by liquid phase material carry out processing and by its
In nutrient make full use of if, that can not only reduce the additive amount of Feed Manufacturing raw material, but also can take into account
Under the premise of finished feed quality, save the cost.
Summary of the invention
In order to make up for the deficiencies of the prior art, the purpose of the present invention is to provide a kind of materials using abundant, control is simple
Mixed feed production system and its production method convenient, product preparation quality is high.
In order to realize above-mentioned technical purpose, the technical solution of the present invention is as follows:
A kind of mixed feed production system comprising the raw material transfer tank that is set in sequence, pulverizer, quenched tank, pelletizer,
It is spray-dried tank, agitator tank, the feed inlet of the raw material transfer tank is set to top, and the discharge port of raw material transfer tank lower part passes through the
The discharge port of the connection of the feed inlet of one transmission device and pulverizer, pulverizer is equipped with solid-liquid separator I, the solid-liquid separator I
Solid-phase outlet connect with the first charging aperture on quenched tank top by second conveyer, the liquid-phase outlet of solid-liquid separator I
It is connect by pump I with quenched tank upper pipeline, the discharge port of quenched tank lower part is equipped with solid-liquid separator II, the separation of solid and liquid
II liquid-phase outlet of device is by pump II and is spray-dried tank piping connection, the solid-phase outlet of solid-liquid separator II and the charging of pelletizer
The discharge port of mouth connection, the spray drying tank and pelletizer is connect with the feed inlet on agitator tank top.
Further, the feed inlet of the raw material transfer tank is connected with the tubaeform material guiding hopper of auxiliary blanking.
Further, the spray drying tank top is equipped with the steam (vapor) outlet I for steam discharge, the steam (vapor) outlet
I connect with the second charging aperture of quenched tank top setting.
Preferably, the steam (vapor) outlet I on the connecting line of quenched tank second charging aperture also sequentially be equipped with for steaming
The heat exchanger I and pump III of vapour condensation.
Further, the gaseous phase outlet that steam is taken when being equipped at the top of the agitator tank for stirring, the gas phase go out
Mouthful second charging aperture piping connection being arranged with quenched tank top, is additionally provided with roots blower on the connecting line.
Further, the pelletizer discharge port is connect by third transmission device with the feed inlet on agitator tank top.
Preferably, the second conveyer, second conveyer and third transmission device are conveyer belt.
A kind of production method of mixed feed production system, it is characterised in that: it includes the following steps:
(1) pretreatment of raw material: by feedstuff from the feed inlet of raw material transfer tank be sequentially added in raw material transfer tank into
Row prestores, and then carries out smashing place by setting period quantitative material is delivered in pulverizer from the discharge port of raw material transfer tank
Reason, by the discharge port output of pulverizer, the solid-phase material wherein generated after pulverization process passes through the feedstuff through smashing processing
It is input in quenched tank after filter by the first charging aperture on quenched tank top, filters the liquid phase material of generation by pumping I from quenched tank
Pipeline spray in portion's is delivered in quenched tank；
(2) quenched: temperature in the tank of quenched tank to be set in 75~90 DEG C, and periodically by the material in quenched tank by quenched
The discharge port of tank lower part is exported, and is separated by solid-liquid separation by the solid-liquid separator II that quenched tank lower part discharge port connects, wherein
Fixed material is transported in pelletizer, and liquid phase material is spray-dried by pumping II Pipeline transport into spray dryer；
(3) prepared by crude product: being delivered to the material of pelletizer in pelletizer with 75~85 DEG C by quenched tank discharge port
Temperature is granulated, and the crude product after granulation is conveyed in agitator tank by the discharge port of pelletizer from the feed inlet above agitator tank,
Into the liquid phase material in spray dryer in spray dryer spray-dried obtained granule materials, wherein being spray-dried
Inlet temperature is 130~150 DEG C, wherein be spray-dried the steam of generation by the steam (vapor) outlet at the top of spray dryer by the road from
The second charging aperture of quenched tank top inputs in quenched tank, it is spray-dried after granule materials from the discharge port of spray dryer
It is stirred and mixes with the material after granulation from the feed inlet conveying agitator tank above agitator tank；
(4) prepared by finished product: agitator tank carries out the material of input with the revolving speed of 60~70 DEG C of temperature, 200~300rmp
Stir process, the agitated tank top of the steam wherein generated in whipping process are transported to quenched tank, the material after the completion of stirring
It is packed by the discharge hole for discharge of stirring pot bottom, the preparation of mixed feed can be completed.
Further, the material particular diameter in the step (3) after pelletizer is granulated is 300~600 microns.
Further, the material moisture after the completion of agitator tank stirring is 11%~15%.
Using above-mentioned technical solution, the invention has the benefit that by setting raw material transfer tank come the feed system of progress
Standby raw material tentatively stores the addition for being conducive to facilitate and carrying out the control and auxiliary additive of the feed in production process, through in raw material
The material for turning tank lower part discharge port output is delivered in pulverizer by second conveyer to be crushed, and uses set as far as possible
Standby to substitute the mode manually shifted, so that the operational safety of production process is higher, the safety for being more advantageous to producers is protected
Shield, can rub into fine grained, especially medicine for the material of bulky grain and the higher material of fiber content by pulverizer
These relative hardness of slag, corn ear, sweet potato are higher, biggish material can be sufficiently ground into disintegrating slag and be produced, and in addition pass through
Cross pulverizer crushing material also pass through pulverizer discharge port solid-liquid separator I be separated by solid-liquid separation after, branch is conveyed
To carrying out modifier treatment in quenched tank, the solid-liquid separator of conditioned treated material conditioned tank lower part feed opening connection again
II is separated by solid-liquid separation again, and wherein liquid phase material is spray-dried to obtain granule materials, and solid-phase material is carried out by pelletizer
Be granulated, then the material after the granule materials of spray drying and pelletizer are granulated is stirred be mixed into required feed at
Product not only make the liquid phase material in production process be fully used, also by that will be spray-dried and the steam of stir process
It is transmitted back in quenched tank and is recycled, reduce production cost and improve material recycles degree, realize production
The secondary economic value of byproduct.
Detailed description of the invention
The present invention is further elaborated with reference to the accompanying drawings and detailed description:
Fig. 1 is the implementation diagram of production system of the present invention.
Specific embodiment
As shown in Figure 1, the present invention includes the raw material transfer tank 1 being set in sequence, pulverizer 2, quenched tank 3, pelletizer 5, spray
The feed inlet of mist drying chamber 4, agitator tank 6, the raw material transfer tank 1 is set to top, it is preferred that the feed inlet of raw material transfer tank 1
Be also connected with the tubaeform material guiding hopper 11 of auxiliary blanking, the discharge port of 1 lower part of raw material transfer tank by second conveyer 71 with
The feed inlet of pulverizer 2 connects, and the discharge port of pulverizer 2 is equipped with solid-liquid separator I 21, the solid phase of the solid-liquid separator I 21
Outlet is connect by second conveyer 72 with the first charging aperture on quenched 3 top of tank, and the liquid-phase outlet of solid-liquid separator I 21 is logical
It crosses pump I 91 to connect with quenched 3 upper pipeline of tank, the discharge port of quenched 3 lower part of tank is equipped with solid-liquid separator II 33, the solid-liquid
II 33 liquid-phase outlet of separator by pump II 92 with spray drying 4 piping connection of tank, the solid-phase outlet of solid-liquid separator II 33 with
The feed inlet of pelletizer 5 connects, feed inlet of the discharge port of the spray drying tank 3 and pelletizer 5 with 6 top of agitator tank
Connection.
In order to enable the processing steam of spray drying tank 4 and agitator tank 6 can be fully utilized, and further, the spray
The steam (vapor) outlet I for steam discharge is equipped at the top of mist drying chamber 4, the be arranged at the top of the steam (vapor) outlet I and quenched tank 3
Two feed inlets connection, it is preferred that be also sequentially equipped on the steam (vapor) outlet I and the connecting line of quenched 3 second charging aperture of tank
For the heat exchanger I 8 and pump III 93 of steam condensation, is inputted after being condensed steam using heat exchanger in quenched tank, add quenched tank 3
The material entered will not because vapor (steam) temperature is too high and make material occur protein denaturation the problems such as, influence the nutriture value of material
Value, further, at the top of the agitator tank 6 is equipped with the gaseous phase outlet taken of steam when for stirring, the gaseous phase outlet with
The second charging aperture piping connection being arranged at the top of quenched tank 3 is additionally provided with roots blower 94 on the connecting line, utilizes Roots
Blower 94 can be convenient the transmission speed of steam in control agitator tank 6, keep production management more convenient.
Further, 5 discharge port of pelletizer is connected by third transmission device 73 and the feed inlet on 6 top of agitator tank
It connects, it is preferred that second conveyer 71, second conveyer 72 and the third transmission device 73 is conveyer belt.
A kind of production method of mixed feed production system, it is characterised in that: it includes the following steps:
(1) pretreatment of raw material: from the tubaeform material guiding hopper 11 above 1 feed inlet of raw material transfer tank sequentially by feedstuff
It is added in raw material transfer tank 1 and is prestored, then quantitatively convey material from the discharge port of raw material transfer tank 1 by the setting period
Smashing processing is carried out into pulverizer 2, is smashed the feedstuff of processing by the discharge port output of pulverizer 2, wherein at crushing
The solid-phase material generated after reason is input in quenched tank 3 by the first charging aperture 31 on quenched 3 top of tank after filtering, and filtering generates
Liquid phase material by pump I 91 from quenched 3 upper pipeline of tank spray be delivered in quenched tank 3, utilize the spray thrower 32 in quenched tank
Liquid phase material is set sufficiently to be contacted with solid-phase material；
(2) quenched: temperature in the tank of quenched tank 3 to be set in 75~90 DEG C, and periodically by the material in quenched tank 3 by adjusting
The discharge port of 3 lower part of matter tank is exported, and carries out solid-liquid point by the solid-liquid separator II 32 of quenched 3 lower part discharge port of tank connection
From wherein fixed material is transported in pelletizer 5, liquid phase material is carried out by pumping II 92 Pipeline transports into spray dryer 4
Spray drying；
(3) prepared by crude product: being delivered to the material of pelletizer 5 in pelletizer 5 with 75~85 DEG C by quenched 3 discharge port of tank
Temperature be granulated, the crude product after granulation by pelletizer 5 discharge port from above agitator tank 6 feed inlet convey agitator tank
In 6, into the liquid phase material in spray dryer 4 in spray dryer 4 spray-dried obtained granule materials, wherein spraying
The inlet temperature of dry spray thrower 41 is 130~150 DEG C, wherein being spray-dried the steam of generation by 4 top of spray dryer
Steam (vapor) outlet inputted in quenched tank from the second charging aperture at 3 top of quenched tank by the road, it is spray-dried after granule materials
It is stirred from the feed inlet conveying agitator tank 6 above agitator tank 6 with the material after granulation from the discharge port of spray dryer 4
Mixing；
(4) prepared by finished product: agitator tank 6 carries out the material of input with the revolving speed of 60~70 DEG C of temperature, 200~300rmp
Stir process is transported to quenched tank 3, the object after the completion of stirring at the top of the agitated tank 6 of the steam wherein generated in whipping process
Material is packed by the discharge hole for discharge of 6 bottom of agitator tank, and the preparation of mixed feed can be completed.
Further, the material particular diameter in the step (3) after pelletizer is granulated is 300~600 microns.
Further, the material moisture after the completion of agitator tank stirring is 11%~15%.
The present invention uses above-mentioned technical solution, carries out the preliminary storage that feed prepares raw material by setting raw material transfer tank
There is the addition for being conducive to facilitate and carrying out the control and auxiliary additive of the feed in production process, through raw material transfer tank lower part discharge port
The material of output is delivered in pulverizer by second conveyer to be crushed, and substitutes artificial turn using equipment as far as possible
The mode of shifting is more advantageous to the safeguard protection of producers so that the operational safety of production process is higher, can by pulverizer
With by the material of bulky grain and the higher material of fiber content rub into fine grained, the especially dregs of a decoction, corn ear, sweet potato this
A little relative hardness are higher, biggish material can be sufficiently ground into disintegrating slag and be produced, the object in addition crushed by pulverizer
After material is also separated by solid-liquid separation by the solid-liquid separator I of pulverizer discharge port, branch be delivered in quenched tank and is adjusted
The solid-liquid separator II of matter processing, the conditioned tank lower part feed opening connection again of conditioned treated material carries out solid-liquid point again
From wherein liquid phase material is spray-dried to obtain granule materials, and solid-phase material is granulated by pelletizer, then will be by spraying
Material after dry granule materials and pelletizer granulation, which is stirred, is mixed into required finished feed, not only to produce
Liquid phase material in journey is fully used, and is also carried out by the way that the steam of spray drying and stir process to be transmitted back in quenched tank
It recycles, reduces production cost and improve material recycles degree, realize the secondary economic valence of production byproduct
Value.
The above is the embodiment of the present invention, for the ordinary skill in the art, religion according to the present invention
Lead, without departing from the principles and spirit of the present invention all equivalent changes done according to scope of the present invention patent, repair
Change, replacement and variant, is all covered by the present invention.
Claims (10)
1. a kind of mixed feed production system, it is characterised in that: it includes the raw material transfer tank being set in sequence, pulverizer, quenched
Tank, pelletizer, spray drying tank, agitator tank, the feed inlet of the raw material transfer tank are set to top, and raw material transfer tank lower part goes out
Material mouth is connected by the feed inlet of second conveyer and pulverizer, and the discharge port of pulverizer is equipped with solid-liquid separator I, described solid
The solid-phase outlet of liquid/gas separator I is connect by second conveyer with the first charging aperture on quenched tank top, solid-liquid separator I
Liquid-phase outlet is connect by pump I with quenched tank upper pipeline, and the discharge port of quenched tank lower part is equipped with solid-liquid separator II, described
II liquid-phase outlet of solid-liquid separator passes through pump II and spray drying tank piping connection, the solid-phase outlet and granulation of solid-liquid separator II
The feed inlet of machine connects, and the discharge port of the spray drying tank and pelletizer is connect with the feed inlet on agitator tank top.
2. a kind of mixed feed production system according to claim 1, it is characterised in that: the charging of the raw material transfer tank
Mouth is connected with the tubaeform material guiding hopper of auxiliary blanking.
3. a kind of mixed feed production system according to claim 1, it is characterised in that: the spray drying tank top
Equipped with the steam (vapor) outlet I being discharged for steam, the steam (vapor) outlet I is connect with the second charging aperture that quenched tank top is arranged.
4. a kind of mixed feed production system according to claim 3, it is characterised in that: the steam (vapor) outlet I and tune
The heat exchanger I and pump III for steam condensation are also sequentially equipped on the connecting line of matter tank second charging aperture.
5. a kind of mixed feed production system according to claim 1, it is characterised in that: be equipped at the top of the agitator tank
The second charging aperture pipeline of the gaseous phase outlet that steam is taken when for stirring, the gaseous phase outlet and the setting of quenched tank top connects
It connects, is additionally provided with roots blower on the connecting line between gaseous phase outlet and quenched tank.
6. a kind of mixed feed production system according to claim 1, it is characterised in that: the pelletizer discharge port is logical
Third transmission device is crossed to connect with the feed inlet on agitator tank top.
7. a kind of mixed feed production system according to claim 6, it is characterised in that: the second conveyer,
Second conveyer and third transmission device are conveyer belt.
8. a kind of production method of mixed feed production system according to any of the above-described claim, it is characterised in that: its
Include the following steps:
(1) pretreatment of raw material: feedstuff is sequentially added in raw material transfer tank from the feed inlet of raw material transfer tank and is carried out in advance
It deposits, then carries out smashing processing by setting period quantitative material is delivered in pulverizer from the discharge port of raw material transfer tank, pass through
Smash processing feedstuff by the discharge port output of pulverizer, the solid-phase material wherein generated after pulverization process after filtering by
The first charging aperture on quenched tank top is input in quenched tank, filters the liquid phase material of generation by pumping I from quenched tank upper pipeline
Spray is delivered in quenched tank；
(2) quenched: temperature in the tank of quenched tank to be set in 75~90 DEG C, and periodically by the material in quenched tank by under quenched tank
The discharge port in portion is exported, and is separated by solid-liquid separation by the solid-liquid separator II that quenched tank lower part discharge port connects, wherein fixing
Material is transported in pelletizer, and liquid phase material is spray-dried by pumping II Pipeline transport into spray dryer；
(3) prepared by crude product: being delivered to the material of pelletizer in pelletizer with 75~85 DEG C of temperature by quenched tank discharge port
It is granulated, the crude product after granulation from the feed inlet conveying agitator tank above agitator tank, is entered by the discharge port of pelletizer
Liquid phase material in the spray dryer spray-dried obtained granule materials in spray dryer, wherein the import being spray-dried
Temperature is 130~150 DEG C, wherein being spray-dried the steam of generation by the steam (vapor) outlet at the top of spray dryer by the road from quenched
The second charging aperture of tank top inputs in quenched tank, it is spray-dried after granule materials from the discharge port of spray dryer from stirring
It mixes to be stirred in the feed inlet conveying agitator tank above tank with the material after granulation and mix；
(4) prepared by finished product: agitator tank is stirred the material of input with the revolving speed of 60~70 DEG C of temperature, 200~300rmp
Processing, the agitated tank top of the steam wherein generated in whipping process are transported to quenched tank, and the material after the completion of stirring is by stirring
The discharge hole for discharge packaging for mixing pot bottom, can be completed the preparation of mixed feed.
9. a kind of production method of mixed feed production system according to claim 8, it is characterised in that: its feature exists
In: the material particular diameter in the step (3) after pelletizer is granulated is 300~600 microns.
10. a kind of production method of mixed feed production system according to claim 8, it is characterised in that: its feature exists
In: the material moisture after the completion of the agitator tank stirring is 11%~15%.
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| CN201710268503.0A CN106820232B (en) | 2017-04-23 | 2017-04-23 | A kind of mixed feed production system and its production method |
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| CN201710268503.0A CN106820232B (en) | 2017-04-23 | 2017-04-23 | A kind of mixed feed production system and its production method |
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| CN106820232B true CN106820232B (en) | 2019-03-26 |
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Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107373730A (en) * | 2017-08-25 | 2017-11-24 | 黄贤飞 | One boar food production comminutor |
| CN108840119A (en) * | 2018-07-27 | 2018-11-20 | 安徽天行健农业股份有限公司 | Black bone sheep greenfeed stores handling system |
| CN111227284A (en) * | 2019-12-17 | 2020-06-05 | 长治学院 | Device and method for preparing special feed for laying hens in laying period by using vinasse |
| CN116462559A (en) * | 2023-05-09 | 2023-07-21 | 浏阳象形精品烟花出口制造有限公司 | Novel safe and environment-friendly smokeless colloid spray anther |
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| US4166839A (en) * | 1974-03-19 | 1979-09-04 | Norsk Hydro A.S | Method for producing calcium phosphates |
| CN203290222U (en) * | 2013-05-24 | 2013-11-20 | 山东佑润生物技术有限公司 | Raw material pretreatment device for low-temperature water soluble creep feed |
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| CN106820232A (en) | 2017-06-13 |
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