CN206519201U - A kind of feed addictive reducing mechanism - Google Patents
A kind of feed addictive reducing mechanism Download PDFInfo
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- CN206519201U CN206519201U CN201720132456.2U CN201720132456U CN206519201U CN 206519201 U CN206519201 U CN 206519201U CN 201720132456 U CN201720132456 U CN 201720132456U CN 206519201 U CN206519201 U CN 206519201U
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- crushing
- cavity
- feed addictive
- pulverizer body
- reducing mechanism
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Abstract
The utility model discloses a kind of feed addictive reducing mechanism, including pulverizer body, outgoing be provided with above frame, pulverizer body of pulverizer body is provided with charging aperture, is provided with below pulverizer body in discharging opening, pulverizer body provided with two crushing cavitys；Described crushing cavity is divided into the first crushing cavity for being arranged on top and sets the second of bottom to crush cavity, provided with crushing rod in first crushing chamber body, rod is crushed to be arranged on the first crushing shaft, provided with crushing wing in second crushing chamber body, crush wing to be arranged on the second crushing shaft, the first crushing shaft and the second crushing shaft are all connected with crushing motor.The utility model is by setting two crushing cavitys, and two crushing cavitys can be divided into two by dividing plate and individually crush cavitys, can also remove dividing plate, and two cavitys realize continuous crushing, improve effect, improve crushing effect, cost-effective.
Description
Technical field
The utility model is related to feed addictive manufacture field, is exactly a kind of feed addictive reducing mechanism.
Background technology
The production Technology of feed addictive, which can be concluded, is divided into following several big classifications；Chemistry or biological synthesis process production
Technique；Refer to the preparation and production that feed addictive is carried out using chemistry or the method for biosynthesis, wherein chemical synthesis again
It is divided into organic synthesis and the major class of Inorganic synthese two, such as vitamin A, E, organic acid (salt), mineral matter, trace element etc., all it is
Prepared using chemical synthesis.Biological synthesis process refers to that selection biology enzyme is catalyst, carries out the synthetically prepared of related substances,
Such as galactooligosaccharicomposition, γ-aminobutyric acid, prepared using biological synthesis process.The process characteristic of chemical synthesis is as follows；
Quick extensive consecutive production can be carried out；Production process is influenceed small by extraneous natural environmental condition；The purity of product is high, component
It is clear；Production batch and product specification uniformity are strong；Relatively it is adapted to the preparation that product is small molecule or molecular structure simple material；It is raw
Production process requires high to equipment, technological process and condition, and the requirement to safe class is also higher.Weak point：To environment energy structure
Into a certain degree of pollution.The process characteristic of biological synthesis process is as follows；Extensive consecutive production can be carried out；Production process is by outer
Boundary's natural environmental condition influence is small；The purity of product is high, and component understands；Production batch and product specification uniformity are strong；Relatively it is adapted to
Product is the preparation of medium molecule structural material；Production process condition requires gentleer.Weak point：Need to be adapted to industrial metaplasia
The biology enzyme of production, application field is currently not too extensive.Chemistry or bio-enzyme degradation method production technology；Refer to using chemistry or raw
The method of thing enzyme degraded prepares and produced the process of feed addictive.Major part oligosaccharides and oligopeptides feed addictive are basic at present
Select such technical method.Such as manna oligosacchride, wood oligose, chitosan oligosaccharide, soybean protein oligopeptides.The process characteristic of chemical degradation method
It is as follows：Extensive consecutive production can be carried out；Production process is influenceed small by extraneous natural environmental condition.Weak point：Product
Purity is reported to the leadship after accomplishing a task, complicated components；Production batch and product specification uniformity are poor；Separation and purification of products process complexity is cumbersome；Produced
Journey condition requires harsher.The process characteristic of bio-enzyme degradation method is as follows；Extensive consecutive production can be carried out；Production process by
Extraneous natural environmental condition influence is small；The purity of product is high, and component understands；Production batch and product specification uniformity are strong；Production
Process condition requires gentleer.Weak point：Need the biology enzyme of suitable industrialized production.Biological fermentation process prepares production work
Skill；Refer to the process of prepare using the method for microbial fermentation and production feed addictive.Such as lysine, vitamin B2, enzyme
Preparation and active bacteria formulation etc..The process characteristic of biological fermentation process is；Can consecutive production on a large scale, the cycle is long；Production process by
Extraneous natural environmental condition influence is larger；Direct products purity is low, complicated components；Production batch and product specification uniformity compared with
Difference；The production cost of product is relatively low, can use natural material；Production process is to production equipment, technological process and condition
And clean level requires high.Weak point：Need the microbial strains of suitable industrialized production.Use biological fermentation process at present
The feedstuff additive product of production is concentrated mainly on the products such as enzyme preparation, amino acid and some vitamin.According to production process
The fermentation method of middle application, selects the technique of several feedstuff additive products of representative use biological fermentation process production to make
For example.Extraction method prepares production technology；Refer to using solvent such as water or organic solvent under certain condition by raw material can
The process separated as the composition of feed addictive.Such as astragalus polyose, Flos Tagetis Erectae extract.The spy of extraction process
Point：Using natural materials as raw material；Crude extract is made up of target component and association composition；Continuous production can be industrialized.Weak point：
Production cost is higher.Post-processing method manufacturing process：Refer to carry out physical behavior to some feed addictives using physical method
Improve the special requirement so as to fit feed manufacturing and aquaculture.Such as coated vitamin C, vitamin ad3 E micro-capsules, post-processing
Technique mainly has dilution, coating, granulation, emulsification etc..The necessity for carrying out feedstuff additive product post-processing is embodied in
Below two aspect：One is to improve the stability of feedstuff additive product in itself, the i.e. ordinary temperature stability (shelf-life) of product, high temperature
Stability (hot-working character) and the volatility for reducing product；Two be the processing characteristics for improving downstream product, is such as changed
Become the form (liquid, crystallization, powdery, particle, instant/dispersion powder) of product, improve its mobility, unit weight, granularity and shape
Shape, reduces the generation of dust, convenient addition, weak point：The lifting of cost can be caused.The crushing of raw material, the work that feed is crushed
Skill flow is granularity as requested, depending on the condition such as kind of feed.Number of times is crushed by raw material, a disintegrating process can be divided into
With circulation disintegrating process or separating twice technique.It can be divided into disintegrating process and elder generation after first dispensing by the combining form with burden process
Proportioning process after crushing.1st, a disintegrating process：It is a kind of most simple, the most frequently used, most original disintegrating process, it is either single
Raw material, mixed material, after once crushing, can be divided into unit by the number of units using pulverizer and crush and crushing side by side,
Small-sized feed-processing plant is crushed using unit mostly, and the medium-sized useful two or more pulverizers of feed-processing plant make side by side
With having the disadvantage that granularity is uneven, power consumption is higher.2nd, separating twice technique have three kinds of process forms, i.e. simple subprogram disintegrating process,
Stage size reduction technique and tissue disintegrating process.(1) simple subprogram separating twice technique is laggard by crushing material with a pulverizer
Row screening, oversize is back to original pulverizer and crushed again again.(2) the stage separating twice technique technique is basic
Setting is respectively to set one of classifying screen on the pulverizer for using two sieves different, two pulverizers, and material is first sieved through first of sieve
Reason, the screenings for meeting granularity requirements directly carries out mixer, and oversize enters First pulverizer, and the material of crushing is entered back into
Classifying screen carries out screen.The material for meeting granularity requirements enters mixer, and remaining oversize enters second pulverizer and crushed,
Enter mixer after crushing.(3) the combination separating twice technique technique is that different types of pulverizer is used in crushing twice,
Pair roller pulverizer is used for the first time, after classifying screen screen, screenings enters mixer, and oversize enters beater disintegrating machine
Second is carried out to crush.3rd, after first dispensing disintegrating process by feed formula advanced design row dispensing and mixed, Ran Houjin
Enter pulverizer to be crushed.4th, this technique of proportioning process will first treat that powder is crushed, and respectively enters batch bin, so after first crushing
Carry out dispensing and mixing again afterwards.
Utility model content
The technical problems to be solved in the utility model is that separating twice is generally two independent size reduction machineries, powder in the prior art
Broken effect is bad, it is necessary to which a large amount of hand fit's crushed works, improve cost, influence crushing effect.
In order to solve the above technical problems, the utility model uses following technological means：
A kind of feed addictive reducing mechanism, including pulverizer body, pulverizer body is outgoing to be provided with frame, pulverizer sheet
It is provided with above body below charging aperture, pulverizer body and is provided with discharging opening, provided with two crushing cavitys in pulverizer body；Described
Crushing cavity is divided into the first crushing cavity for being arranged on top and sets the second of bottom to crush to be set in cavity, the first crushing chamber body
There is crushing rod, crush rod and be arranged on the first crushing shaft, provided with wing is crushed in the second crushing chamber body, crush wing and be arranged on the second powder
On broken axle, the first crushing shaft and the second crushing shaft are all connected with crushing motor.
Preferably, the utility model further technical scheme is：
Controlled valve is provided between the first described crushing shaft and the second crushing shaft and crushing motor.Common size reduction machinery
The crushing shaft of connection receives crushing motor control, starts simultaneously, simultaneously closes off, and the utility model can individually control crushing shaft
Start and close, reduce unnecessary waste.
Described charging aperture is inverted funnel shaped.
Described first is crushed and is provided with dividing plate between cavity and the second crushing cavity, and dividing plate two ends are provided with hook, pulverizer
Body madial wall is provided with link.
Described crushing wing is provided with rotating blade.
Described discharge outlet is provided with screen pack.The setting of screen pack, it is possible to achieve to crushing halfway clout, again
Reclaim, crush again, improve product quality.
The utility model is by setting two crushing cavitys, and two can be divided into individually by dividing plate by crushing cavity for two
Crushing cavity, can also remove dividing plate, two cavitys realize it is continuous crush, improve effect, improve crushing effect, save into
This.It is how red, red by the dynamic guarantor's product of above-mentioned manufacturing machine processing and fabricating, including happy polyacid, happy sour, origanum oil plus easy chromium, egg
The types such as bright health, mould clear, the strength element of speed, dynamic product of protecting is after antibiotic, with probiotic, enzyme preparation, probiotics etc.
Important additives arranged side by side, are a kind of noresidue, the environment protection additive acted on without the resistance to the action of a drug, nonhazardous.Produce feed addition
Agent product is found pleasure in sour, Yi Xianbao, methylpartricin sodium laurylsulfate plus easily fresh, and feed addictive refers in Feed Manufacturing processing, added during use
A small amount of or micro substance, consumption is seldom in feed but effect is notable.Feed addictive is that modern feed industry is necessarily used
Raw material, to reinforcing basal feed nutritive value, improve breeding performonce fo animals, it is ensured that animal health, save feed cost, improve
There is obvious effect in terms of livestock products quality.
Brief description of the drawings
Fig. 1 is a kind of structural representation of embodiment of the present utility model.
Fig. 2 is the structural representation of the second crushing shaft of the present utility model.
Fig. 3 is the structural representation of the utility model dividing plate.
Fig. 4 is the utility model feed additive production process chart
Description of reference numerals：1- frames；2- dividing plates；3- crushes rod；The crushing shafts of 4- first；5- charging apertures；6-
Two crush cavity；7- crushes motor；8- first crushes cavity；9- rotating blades；The crushing shafts of 10- second；11- crushes wing；
12- discharging openings；13- is linked up with.
Embodiment
With reference to embodiment, the utility model is further illustrated.
It can be seen from Fig. 1, a kind of feed addictive reducing mechanism of the utility model, including pulverizer body, pulverizer sheet
Go out in vitro provided with frame 1, pulverizer body top, which is provided with below charging aperture 5, pulverizer body, is provided with discharging opening 12, pulverizer sheet
In vivo provided with two crushing cavitys；Described crushing cavity is divided into the first crushing cavity 8 for being arranged on top and sets bottom
Second crushes cavity 6, and first crushes in cavity 8 provided with rod 3 is crushed, and crushes rod 3 and is arranged on the first crushing shaft 4, second crushes
Provided with wing 11 is crushed in cavity 6, crush wing 11 and be arranged on the second crushing shaft 10, the first crushing shaft 4 and the second crushing shaft 10 are equal
Motor 7 is crushed in connection, is provided with controlled valve between the first crushing shaft 4 and the second crushing shaft 10 and crushing motor 7, charging aperture 5 is
Inverted funnel shaped, the first crushing cavity 8 and second is provided with dividing plate 2 between crushing cavity 6, and the two ends of dividing plate 2 are provided with hook 13,
Pulverizer body madial wall is provided with link, crushes wing 11 and is provided with rotating blade 9, discharging opening 12 provided with screen pack.
Due to the foregoing is only embodiment of the present utility model, but protection not limited to this of the present utility model,
Any those skilled in the art it is contemplated that the equivalent change of the technical program technical characteristic or replacement, all cover
Within protection domain of the present utility model.
Claims (6)
1. a kind of feed addictive reducing mechanism, including pulverizer body, pulverizer body is outgoing to be provided with frame, pulverizer body
Top, which is provided with below charging aperture, pulverizer body, is provided with discharging opening, provided with two crushing cavitys in pulverizer body；Its feature exists
In：Described crushing cavity is divided into the first crushing cavity for being arranged on top and sets the second of bottom to crush cavity, the first powder
Provided with rod is crushed in broken cavity, crush rod and be arranged on the first crushing shaft, provided with wing is crushed in the second crushing chamber body, crush wing and set
Put on the second crushing shaft, the first crushing shaft and the second crushing shaft are all connected with crushing motor.
2. a kind of feed addictive reducing mechanism according to claim 1, it is characterised in that：Described the first crushing shaft and
Controlled valve is provided between second crushing shaft and crushing motor.
3. a kind of feed addictive reducing mechanism according to claim 1, it is characterised in that：Described charging aperture is inversion
Funnel shaped.
4. a kind of feed addictive reducing mechanism according to claim 1, it is characterised in that：Described first crushes cavity
And second crush cavity between be provided with dividing plate, dividing plate two ends provided with hook, pulverizer body madial wall be provided with link.
5. a kind of feed addictive reducing mechanism according to claim 1, it is characterised in that：Described crushing wing is provided with rotation
Rotor piece.
6. a kind of feed addictive reducing mechanism according to claim 1, it is characterised in that：Described discharge outlet is provided with
Screen pack.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720132456.2U CN206519201U (en) | 2017-02-14 | 2017-02-14 | A kind of feed addictive reducing mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720132456.2U CN206519201U (en) | 2017-02-14 | 2017-02-14 | A kind of feed addictive reducing mechanism |
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| Publication Number | Publication Date |
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| CN206519201U true CN206519201U (en) | 2017-09-26 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201720132456.2U Active CN206519201U (en) | 2017-02-14 | 2017-02-14 | A kind of feed addictive reducing mechanism |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108176488A (en) * | 2017-12-28 | 2018-06-19 | 郑州赫恩电子信息技术有限公司 | A kind of humidification dust-protection type building castoff grinding equipment |
-
2017
- 2017-02-14 CN CN201720132456.2U patent/CN206519201U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108176488A (en) * | 2017-12-28 | 2018-06-19 | 郑州赫恩电子信息技术有限公司 | A kind of humidification dust-protection type building castoff grinding equipment |
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