CN201640417U - Curing granulator - Google Patents
Curing granulator Download PDFInfo
- Publication number
- CN201640417U CN201640417U CN201020001517XU CN201020001517U CN201640417U CN 201640417 U CN201640417 U CN 201640417U CN 201020001517X U CN201020001517X U CN 201020001517XU CN 201020001517 U CN201020001517 U CN 201020001517U CN 201640417 U CN201640417 U CN 201640417U
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- feed
- granulator
- raw material
- slaking
- curing
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- Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)
Abstract
The utility model relates to a curing granulator which comprises a raw material storing and distributing groove, a rationing feeder, a double-shaft speed-difference conditioner, a curing extrusion granulator, a vacuum pressure relief system and a feed forming system, wherein the double-shaft speed-difference conditioner is provided with a raw material inlet and a raw material outlet; two converse speed-difference rotation shafts with different sizes are arranged inside the double-shaft speed-difference conditioner; the two rotation shafts are respectively provided with a plurality of stirring paddles with adjustable angles; the curing extrusion granulator is provided with a feed inlet and a feed outlet; and a feed extrusion screw rod and an outer-lining internal-thread sleeve are arranged inside the curing extrusion granulator so as to enable the rationing feeder to send raw materials in the raw material storing and distributing groove to the double-shaft speed-difference conditioner quantificationally; and vapour, water, oil, seriflux and the like are injected to ensure that the raw material is heated, humidified, kneaded and stirred for complete and uniform drenching and starch curing.
Description
Technical field
The utility model relates to a kind of expanded granulator, the particularly a kind of slaking granulator that can produce organism in water or the land fowl poultry feed that pet ate.
Background technology
Generally be used to make the expanded granulator of feed, it is for providing organisms in water such as fish, shrimp, or the feed manufacturing of land fowl, poultry, cat, dog etc.But, general fish can be divided into shallow-layer fish, midwater fishes and deep layer fish according to its life habit, therefore, in the manufacture process of feed, must possess two machines and can make different fishes and shrimps feeds or land fowl poultry feed for pet according to the habit of fishes and shrimps or fowl poultry.
And, because organism in water is neither identical with build, eating habit and the life style of land fowl poultry pet, make that organism in water and the land fowl poultry feed that pet ate is also inequality.But generally be used to produce the feed that organism in water eats and can't be used for the feed that production land fowl poultry pet is used, the manufacturer that makes must use many machines could produce different types of feed, causes the production of fodder cost to improve relatively.
In No. 557676 patent case of TaiWan, China, disclosed a kind of structural improvement of extruder, its primary structure is: extruder machine thorax is established an exhaust pumped vacuum systems, this vacuum system is provided with a CD-ROM drive motor, CD-ROM drive motor connects establishes a screw rod, this screw rod left side cutter is established a vacuum and is extracted mouth out, when the vacuum motor vacuumizes by vacuum extraction mouth, this CD-ROM drive motor drives screw rod and rotates, the rotation of the raw material mat screw rod in the extrusion machine barrel is kept out makes it can't run out of and enter in the vacuum system, moreover this raw material adds the expanded bubble that produces behind the steam because of adding water, but the spiral space of mat screw rod and extracting out, and reach the density of control material, make the feed that produces reach the density specific gravity control then, and can float in the water or be sunken to function in the water, be the utility model of a tool practicality and progressive in fact.
Yet, though the structural improvement of above-mentioned extruder can be controlled feed density proportion, and produce different fishes and shrimps feeds, but can't be used for the feed that production land fowl poultry pet is used.
This shows, problem and deficiency that the expanded granulator that known manufacturing feed is used is derived, real non-one kindhearted design, and demand urgently being improved.
Every problem and deficiency that designer of the present utility model derives in view of the expanded granulator that above-mentioned manufacturing feed is used are urgently to think to be improved innovation, and after concentrating on studies through taking great pains to attain one's goal for many years, successfully this part slaking granulator is finished in research and development finally.
Summary of the invention
A purpose of the present utility model provides a kind of slaking granulator, relies on twin shaft differential quality controling machine provided by the utility model and curing extruded granulator, can produce organism in water or the land fowl poultry feed that pet ate.
Another purpose of the present utility model provides a kind of slaking granulator, relies on vacuum pressure relieving system provided by the utility model, can control the weight density of feed according to the habit of various biologies in the water or land fowl poultry pet, and make different types of feed.
For reaching above-mentioned purpose, a kind of slaking granulator of the utility model, it comprises:
One twin shaft differential quality controling machine, have a feed(raw material)inlet and a material outlet, and be provided with two reverse differential rotating shafts of size in this twin shaft differential quality controling machine inside, these two rotating shafts are respectively arranged with the paddle of a plurality of angle adjustables, with so that raw material is sent into from this feed(raw material)inlet, via the paddle of this rotating shaft raw material is crumpled and stirred, and in the heating and moistening process, evenly modified make raw material finish slaking after, sent from this material outlet;
One curing extruded granulator, have feed inlet and feed outlet, and be provided with a feed extrusion spiral bar and an outer lining inner thread sleeve in this curing extruded granulator inside, this feed inlet is connected in the material outlet of this twin shaft differential quality controling machine, with entering this curing extruded granulator so that the feed that this twin shaft differential quality controling machine is sent enters the mouth from this feed, via this feed extrusion spiral bar and outer lining inner thread sleeve feed is pushed after moment produces the complete slaking of high pressure-temperature, sent from this feed outlet;
One vacuum pressure relieving system is arranged at the top and a side of this curing extruded granulator, and is adjacent to the port of export of this curing extruded granulator, regulates discharging in order to high-temperature gas in should curing extruded granulator thorax is an amount of automatically, with control feed weight density;
One feed formation system; be incorporated into the feed outlet of this curing extruded granulator; this feed formation system comprises a feed finishing die panel seat and a cutting knife group; this feed finishing die panel seat offers a plurality of feed extrusion cavities; with so that feed from this feed extrusion cavities extrusion molding, and cuts into graininess by this cutting knife group.
Described slaking granulator wherein, more comprises the equal hopper of a raw material, is arranged at the feed(raw material)inlet of this twin shaft differential quality controling machine, in order to the storage of raw materials.
Described slaking granulator wherein, more comprises a certain amount of supply machine, is arranged between the equal hopper of this raw material and this twin shaft differential quality controling machine, is delivered to this twin shaft differential quality controling machine quantitatively in order to the raw material with the equal hopper of this raw material storage.
Described slaking granulator, wherein, this vacuum pressure relieving system comprises a vacuum valve, a vacuum collecting device and a vavuum pump.
Described slaking granulator, wherein, this cutting knife group comprises a CD-ROM drive motor and a Cutter apron; this Cutter apron is provided with a plurality of cutoff knife racks; this cutoff knife rack locks respectively a cutting edge, by this Cutter apron rotation of this drive motor, makes the cutting edge of this cutoff knife rack that feed is cut into graininess.
Described slaking granulator, wherein, the cutting knife of this cutoff knife rack locking is hard blade or soft blade.
Described slaking granulator, wherein, this paddle is arranged at rotating shaft with different angles respectively.
Via the technological means that the utility model adopted, because twin shaft differential quality controling machine of the present utility model has the modified slaking effect of preferable stirring, and can mix at feed and add water and steam when stirring, make the evenly drenched and slaking of raw material, can add simultaneously the prescription additives that the bait feeding habits are strong, heat energy is high such as fish oil, salad oil, the molten slurry of fish, molasses again, solve to overcome in the common production processes and add high grease, heavy bodied predicament.
Secondly, curing extruded granulator of the present utility model has bigger mechanical shearing and rubbing energy, can efficiently material be pushed moment to reach the high pressure-temperature slaking and be shaped, and makes production capacity promote more than 40%.
In addition, vacuum release of pressure gas extraction system of the present utility model can effectively be controlled the feed weight density, with this, can produce floating forage, slow falling forage or heavy soon forage according to the life habit of organism in water, and all can control the rate of swimming or heavy water rate 100% for highly difficult nano sized particles feed, digestibility height, resistance to water are good.
On the other hand, the utility model can be raiseeed feed for pet by production land fowl, also can produce the feed of organism in water, as long as change needn't be changed internal screw or sleeve assembly through operating parameter, just can produce various variety classes feeds, and the utility model institute production land fowl poultry feed for pet is an innovation, and product quality spy is good, uniform particles, high slaking, no powder, meat change rate height, grow up quick.Shortcomings such as the high grease feed of tradition granulator can't be produced, curing degree deficiency, particle inequality, powder is many, meat change rate is low, the utility model all can overcome solution.
Description of drawings
Fig. 1 shows the schematic diagram of the utility model slaking granulator;
Fig. 2 shows the internal structure schematic diagram of twin shaft differential quality controling machine;
Fig. 3 shows the pivot structure schematic diagram of twin shaft differential quality controling machine;
Fig. 4 shows that twin shaft differential quality controling machine stirs the action schematic diagram of raw material;
Fig. 5 shows the structural representation of curing extruded granulator and feed formation system;
Fig. 6 shows the schematic diagram that separates of curing extruded granulator and feed formation system;
Fig. 7 shows the schematic diagram of feed formation system;
Fig. 8 shows the separation schematic diagram of cutting knife group;
Fig. 9 shows the action schematic diagram of curing extruded granulator and feed formation system;
Figure 10 shows the schematic diagram of vacuum system.
Description of reference numerals: 100-slaking granulator; 1-twin shaft differential quality controling machine; The equal hopper of 11-raw material; 12-weight feed machine; The 13-feed(raw material)inlet; The 14-material outlet; 15,16-rotating shaft; 151,161-paddle; The curing extruded granulator of 2-; 21-feed inlet; 22-feed extrusion spiral bar; 23-outer lining inner thread sleeve; The outlet of 24-feed; 3-vacuum pressure relieving system; The 31-vacuum valve; 32-vacuum collecting device; The 33-vavuum pump; 4-feed formation system; 41-feed finishing die panel seat; 411-feed extrusion cavities; 42-cutting knife group; The 421-CD-ROM drive motor; The 422-Cutter apron; The 423-cutoff knife rack; The 424-cutting edge; The 5-raw material; The 6-feed.
The specific embodiment
Your auditor is convenient to understand other features of the present utility model and advantage in order to make, and the effect of being reached can more manifest, and with the utility model conjunction with figs., is described in detail as follows now:
See also Fig. 1, it shows the schematic diagram of the utility model slaking granulator.As shown in the figure, the utility model slaking granulator 100 comprises a twin shaft differential quality controling machine 1, one curing extruded granulator 2, a vacuum pressure relieving system 3 and a feed formation system 4; Twin shaft differential quality controling machine 1 front end is provided with equal hopper 11 of a raw material and a certain amount of supply machine 12; the equal hopper 11 of raw material is in order to place raw material; and via weight feed machine 12 raw material is all measured quantitatively enter twin shaft differential quality controling machine 1 mix, stir modified after; be sent to curing extruded granulator 2 raw material is given squeezing, maturing; and via vacuum pressure relieving system 3 with gas in the machine thorax automatically an amount of regulate discharging after; with the feed extrusion molding, and cut into graininess by feed formation system 4.
Please consult Fig. 2 to Fig. 4 simultaneously, Fig. 2 shows the internal structure schematic diagram of twin shaft differential quality controling machine, and Fig. 3 shows the big or small reverse differential pivot structure schematic diagram of twin shaft differential quality controling machine, and Fig. 4 shows that twin shaft differential quality controling machine stirs the action schematic diagram of raw material.As shown in the figure, twin shaft differential quality controling machine 1 of the present utility model comprises a feed(raw material)inlet 13, a material outlet 14 and two reverse differential rotating shafts 15,16 of size; Feed(raw material)inlet 13 usefulness are so that raw material is inserted twin shaft differential quality controling machine 1, material outlet 14 is sent in order to the feed after will mixing and stir, two reverse differential rotating shafts 15,16 of size are respectively arranged with the paddle 151,161 of a plurality of angle adjustables, and are modified in order to raw material is mixed, stirs.Wherein, the paddle 151 of rotating shaft 15 and the length of the paddle 161 of rotating shaft 16 and inequality, and a plurality of paddles 151 of rotating shaft 15 are arranged at rotating shaft 15 with different angles respectively, and a plurality of paddles 161 of rotating shaft 16 also are arranged at rotating shaft 16 with different angles respectively.
When desiring to carry out raw material 5 mixture operations, raw material 5 13 is inserted twin shaft differential quality controling machine 1 from the feed(raw material)inlet, drive paddles 151,161 rotations by the rotating shaft in the rotation 15,16, with so that raw material 5 carries out the stirring of reverse differential and the action of mixing.And, can when stirring and mix, raw material 5 add entry, grease and steam etc., and make raw material 5 when mixing, stirring, form gelatinization gradually, and the starch of raw material 5 is finished slaking.Secondly, because a plurality of paddles 151,161 of rotating shaft 15,16 are arranged at rotating shaft 15,16 with different angles respectively, therefore, when raw material 5 stirs in twin shaft differential quality controling machine 1, the paddle 151,161 that is adjacent to feed(raw material)inlet 13 can push raw material 5 forward when stirring, and fully crumples stirring to promote raw material 5 propelling movement processes; And the paddle 151,161 that is adjacent to material outlet 14 can be sent raw material 5 from material outlet 14, be arranged at rotating shaft 15,16 by paddle 151,161 with different reverse differentials and angle, make that raw material 5 can evenly modified in twin shaft differential quality controling machine 1, starch slaking; And after raw material 5 is finished slaking, by the paddle 151,161 of rear end raw material 5 is sent to material outlet 14 and sends, not only accelerate operating speed, also shorten the activity duration.
In addition, also can solve to overcome on the conventional process flow process and add high grease, heavy bodied predicament with prescription additives that the bait feeding habits are strong, heat energy is high such as fish oil, lecithin and the molten slurries of fish when raw material 5 stirs.
Please consult Fig. 5 to Figure 10 simultaneously; Fig. 5 shows the structural representation of curing extruded granulator and feed formation system; Fig. 6 shows the schematic diagram that separates of curing extruded granulator and feed formation system; Fig. 7 shows the schematic diagram of feed formation system; Fig. 8 shows the separation schematic diagram of feed formation system; Fig. 9 shows the action schematic diagram of curing extruded granulator and feed formation system, and Figure 10 shows the schematic diagram of vacuum pressure relieving system.Curing extruded granulator 2 comprises feed inlet 21, one feed extrusion spiral bar 22, an outer lining inner thread sleeve 23 and feed outlet 24, with so that feed 6 is inserted curing extruded granulator 2 from feed inlet 21, and this feed inlet 21 is connected in the material outlet 14 of this twin shaft differential quality controling machine 1,, sent after feed 6 extrusions via feed extrusion spiral bar 22 and outer lining inner thread sleeve 23 from feed outlet 24; Vacuum pressure relieving system 3 is arranged at the top and a side of curing extruded granulator 2, vacuum pressure relieving system 3 comprises a vacuum valve 31, a vacuum collecting device 32 and a vavuum pump 33, vacuum pressure relieving system 3 discharges in order to an amount of automatically adjusting of the high-temperature gas in the extruder thorax that will push granulator 2, with the weight density of control feed 6; This feed formation system 4 is incorporated into the feed outlet 24 of this curing extruded granulator 2; and this feed formation system 4 comprises a feed finishing die panel seat 41 and a cutting knife group 42; feed finishing die panel seat 41 offers a plurality of feed extrusion cavities 411; in order to feed 6 extrusion moldings; cutting knife group 42 comprises a CD-ROM drive motor 421 and a Cutter apron 422; CD-ROM drive motor 421 is in order to drive Cutter apron 422 rotations; Cutter apron 422 is provided with a plurality of cutoff knife racks 423; cutoff knife rack 423 locks respectively a cutting edge 424; drive Cutter apron 422 rotations by CD-ROM drive motor 421, cut into graininess in order to the feed 6 that feed extrusion cavities 411 is extruded.Wherein, cutting edge 424 can be that hard blade also can be soft blade.
When feed 6 when feed inlet 21 enters curing extruded granulator 2; by feed extrusion spiral bar 22 and outer lining inner thread sleeve 23 feed 6 is pushed and the instantaneous pressure high-temperature maturing after; be sent to the feed finishing die panel seat 41 of feed formation system 4 from feed outlet 24; by a plurality of feed extrusion cavities 411 of feed finishing die panel seat 41 with feed 6 extrusion moldings; CD-ROM drive motor 421 by cutting knife group 42 drives Cutter apron 422 rotations then; drive cutoff knife racks 423 rotations by Cutter apron 422 again, feed 6 is cut into graininess by the cutting edge 424 of cutoff knife rack 423.
In addition, when the desire manufacturing feed 6 that organism in water ate, can the high-temperature gas of feed 6 in the extruder thorax be expelled to vacuum collecting device 32 automatically in right amount by the vacuum valve 31 of vacuum pressure relieving system 3, by vavuum pump 33 moisture and the gas of vacuum collecting device 32 are discharged again, thus, can be according to the weight density of the habit control feed 6 of organism in water and land fowl poultry pet, and floating forage, slow falling forage, heavy forage or fowl poultry feed for pet are soon produced in decision.
The above person only, it only is preferred embodiment of the present utility model, when not limiting the scope that the utility model is implemented with this, so the change of numerical value or displacement of equivalent elements such as, or, all should still belong to the category that the utility model patent contains according to equalization variation and modification that the utility model claim is done.
Claims (7)
1. a slaking granulator is characterized in that, comprising:
One twin shaft differential quality controling machine, have a feed(raw material)inlet and a material outlet, and be provided with two reverse differential rotating shafts of size in this twin shaft differential quality controling machine inside, these two rotating shafts are respectively arranged with the paddle of a plurality of angle adjustables, with so that raw material send into from this feed(raw material)inlet, paddle via this rotating shaft stirs the raw material rubbing, is sent from this material outlet;
One curing extruded granulator, have feed inlet and feed outlet, and be provided with a feed extrusion spiral bar and an outer lining inner thread sleeve in this curing extruded granulator inside, this feed inlet is connected in the material outlet of this twin shaft differential quality controling machine, with entering this curing extruded granulator so that the feed that this twin shaft differential quality controling machine is sent enters the mouth from this feed, via this feed extrusion spiral bar and outer lining inner thread sleeve feed is pushed after moment produces the complete slaking of high pressure-temperature, sent from this feed outlet;
One vacuum pressure relieving system is arranged at the top and a side of this curing extruded granulator, and is adjacent to the port of export of this curing extruded granulator, regulates discharging in order to high-temperature gas in should curing extruded granulator thorax is an amount of automatically, with control feed weight density;
One feed formation system; be incorporated into the feed outlet of this curing extruded granulator; this feed formation system comprises a feed finishing die panel seat and a cutting knife group; this feed finishing die panel seat offers a plurality of feed extrusion cavities; with so that feed from this feed extrusion cavities extrusion molding, and cuts into graininess by this cutting knife group.
2. slaking granulator as claimed in claim 1 is characterized in that, more comprises the equal hopper of a raw material, is arranged at the feed(raw material)inlet of this twin shaft differential quality controling machine, in order to the storage of raw materials.
3. slaking granulator as claimed in claim 2 is characterized in that, more comprises a certain amount of supply machine, is arranged between the equal hopper of this raw material and this twin shaft differential quality controling machine, is delivered to this twin shaft differential quality controling machine quantitatively in order to the raw material with the equal hopper of this raw material storage.
4. slaking granulator as claimed in claim 1 is characterized in that, this vacuum pressure relieving system comprises a vacuum valve, a vacuum collecting device and a vavuum pump.
5. slaking granulator as claimed in claim 1; it is characterized in that; this cutting knife group comprises a CD-ROM drive motor and a Cutter apron; this Cutter apron is provided with a plurality of cutoff knife racks; this cutoff knife rack locks respectively a cutting edge; by this Cutter apron rotation of this drive motor, make the cutting edge of this cutoff knife rack that feed is cut into graininess.
6. slaking granulator as claimed in claim 5 is characterized in that, the cutting knife of this cutoff knife rack locking is hard blade or soft blade.
7. slaking granulator as claimed in claim 1 is characterized in that this paddle is arranged at rotating shaft with different angles respectively.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201020001517XU CN201640417U (en) | 2010-01-11 | 2010-01-11 | Curing granulator |
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CN201020001517XU CN201640417U (en) | 2010-01-11 | 2010-01-11 | Curing granulator |
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CN201020001517XU Expired - Lifetime CN201640417U (en) | 2010-01-11 | 2010-01-11 | Curing granulator |
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Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102599620A (en) * | 2011-02-08 | 2012-07-25 | 国立大学法人鸟取大学 | Apparatus and method for manufacturing pet food |
CN102845817A (en) * | 2012-09-10 | 2013-01-02 | 江苏牧羊集团有限公司 | Conditioning and granulating device for shrimp feed |
CN103156267A (en) * | 2013-01-31 | 2013-06-19 | 温特牧(北京)科技有限公司 | Bulking machine |
CN103169000A (en) * | 2013-01-31 | 2013-06-26 | 温特牧(北京)科技有限公司 | Regeneration rice production apparatus |
CN103169142A (en) * | 2013-03-14 | 2013-06-26 | 牧羊有限公司 | Bulking machine vacuumizing device |
CN105192568A (en) * | 2015-10-17 | 2015-12-30 | 晋江市恒松机械制造有限公司 | Automatic forming device for grain particle materials |
CN106923362A (en) * | 2017-03-03 | 2017-07-07 | 安徽安丰堂动物药业有限公司 | A kind of mixed fodder production stirring device for making |
CN108936772A (en) * | 2018-09-10 | 2018-12-07 | 广州天地实业有限公司 | A kind of quality-adjusting device |
CN108940122A (en) * | 2018-08-10 | 2018-12-07 | 明毅强 | A kind of granulation device of health food processing |
CN112515058A (en) * | 2020-12-11 | 2021-03-19 | 福建天马科技集团股份有限公司 | Penaeus vannamei boone puffed feed and puffing method thereof |
RU2783914C2 (en) * | 2021-04-13 | 2022-11-22 | Федеральное государственное бюджетное образовательное учреждение высшего образования «Пензенский государственный технологический университет» | Unit for thermal-vacuum extrusion of plant raw materials |
-
2010
- 2010-01-11 CN CN201020001517XU patent/CN201640417U/en not_active Expired - Lifetime
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102599620A (en) * | 2011-02-08 | 2012-07-25 | 国立大学法人鸟取大学 | Apparatus and method for manufacturing pet food |
CN102845817A (en) * | 2012-09-10 | 2013-01-02 | 江苏牧羊集团有限公司 | Conditioning and granulating device for shrimp feed |
CN103156267A (en) * | 2013-01-31 | 2013-06-19 | 温特牧(北京)科技有限公司 | Bulking machine |
CN103169000A (en) * | 2013-01-31 | 2013-06-26 | 温特牧(北京)科技有限公司 | Regeneration rice production apparatus |
CN103156267B (en) * | 2013-01-31 | 2017-09-15 | 温特牧(北京)科技有限公司 | Bulking machine |
CN103169142A (en) * | 2013-03-14 | 2013-06-26 | 牧羊有限公司 | Bulking machine vacuumizing device |
CN105192568A (en) * | 2015-10-17 | 2015-12-30 | 晋江市恒松机械制造有限公司 | Automatic forming device for grain particle materials |
CN106923362A (en) * | 2017-03-03 | 2017-07-07 | 安徽安丰堂动物药业有限公司 | A kind of mixed fodder production stirring device for making |
CN108940122A (en) * | 2018-08-10 | 2018-12-07 | 明毅强 | A kind of granulation device of health food processing |
CN108936772A (en) * | 2018-09-10 | 2018-12-07 | 广州天地实业有限公司 | A kind of quality-adjusting device |
CN112515058A (en) * | 2020-12-11 | 2021-03-19 | 福建天马科技集团股份有限公司 | Penaeus vannamei boone puffed feed and puffing method thereof |
RU2783914C2 (en) * | 2021-04-13 | 2022-11-22 | Федеральное государственное бюджетное образовательное учреждение высшего образования «Пензенский государственный технологический университет» | Unit for thermal-vacuum extrusion of plant raw materials |
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