CN109393233A - A kind of trout feed production method - Google Patents
A kind of trout feed production method Download PDFInfo
- Publication number
- CN109393233A CN109393233A CN201811565410.5A CN201811565410A CN109393233A CN 109393233 A CN109393233 A CN 109393233A CN 201811565410 A CN201811565410 A CN 201811565410A CN 109393233 A CN109393233 A CN 109393233A
- Authority
- CN
- China
- Prior art keywords
- production method
- machine
- raw material
- trout
- trout feed
- 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.)
- Withdrawn
Links
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K50/00—Feeding-stuffs specially adapted for particular animals
- A23K50/80—Feeding-stuffs specially adapted for particular animals for aquatic animals, e.g. fish, crustaceans or molluscs
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/20—Animal feeding-stuffs from material of animal origin
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/20—Animal feeding-stuffs from material of animal origin
- A23K10/22—Animal feeding-stuffs from material of animal origin from fish
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/20—Animal feeding-stuffs from material of animal origin
- A23K10/24—Animal feeding-stuffs from material of animal origin from blood
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/30—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/30—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms
- A23K10/37—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms from waste material
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K10/00—Animal feeding-stuffs
- A23K10/30—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms
- A23K10/37—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms from waste material
- A23K10/38—Animal feeding-stuffs from material of plant origin, e.g. roots, seeds or hay; from material of fungal origin, e.g. mushrooms from waste material from distillers' or brewers' waste
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23K—FODDER
- A23K40/00—Shaping or working-up of animal feeding-stuffs
- A23K40/10—Shaping or working-up of animal feeding-stuffs by agglomeration; by granulation, e.g. making powders
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/80—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management
- Y02A40/81—Aquaculture, e.g. of fish
- Y02A40/818—Alternative feeds for fish, e.g. in aquacultures
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Polymers & Plastics (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Food Science & Technology (AREA)
- Animal Husbandry (AREA)
- Physiology (AREA)
- Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Biotechnology (AREA)
- Mycology (AREA)
- Botany (AREA)
- Biomedical Technology (AREA)
- Marine Sciences & Fisheries (AREA)
- Insects & Arthropods (AREA)
- Birds (AREA)
- Fodder In General (AREA)
Abstract
The invention discloses a kind of trout feed production methods, with the raw material of following parts by weight: corn flour 6%, brewex's grains 3%, earthworm powder 0.28%, fish meal 26%, pig blood 0.2%, dandelion 0.2%, purslane 0.25%, rapeseed cake 8%, duckweed 16%, mulberry leaf 16%, seaweed 2%, egg pupa powder 4%, glycine betaine 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula 10%, pass through conveying, cleaning, it crushes, mixing, it is quenched, the preparation of the processes such as extrusion, cost of material of the invention is low, but nutrition is balanced for finished product, feeding effect is good, and there is diseases prevention, promote the effect digested and assimilated.
Description
Technical field
The present invention relates to aquatic feeds fields, and in particular to a kind of trout feed production method.
Background technique
Trout meat thorniness is few, Fresh & Tender in Texture, and smoother taste is full of nutrition, to have been favored by people, trout cultivation by
It is formed on the development of trout feed production technology, trout feed is a kind of slow sinking feed, production technology production currently on the market
Trout feed existing for main problem be: cost of material is high, efficiency of feed utilization is low, and generates a large amount of dust but in production process
There is no explosion precaution, there are security risks;Trout is poor to general plant feed digestibility and utilization ability, affects nutriment
It digests and assimilates, how to reduce cost of material using plant and nutrition equilibrium, suitable trout feeding habits can be produced and be conducive to digestion and inhale
The trout feed of receipts is a problem to be solved.
Summary of the invention
The purpose of the present invention is to solve above-mentioned technical problems, provide a kind of trout feed production method, utilize original
The complementation of material makes original by secondary quenched, mixing, maturation process accordingly matched smashing fineness and suitable temperature, moisture
Material reaches the glutinous degree of most good soft, prepares that nutrition is balanced, palatability is good, feed system by extrusion and unique auxiliary process
The low feed of number, yields is high, abundant raw material, cheap, select everywhere can target-seeking plant as basic raw material, be greatly reduced
Cost of material, but nutrition is balanced for resulting trout feed, and feeding effect is good, has good diseases prevention, promotes digestion,
And improve efficiency of feed utilization, reduce residual bait, water quality is improved, ultramicro grinding process is eliminated in production method, further
Production cost is reduced, is controlled by refining temperature etc., product effect but has same effect, and production method of the invention
With explosion prevention function, the hidden danger of dust explosion in Feed Manufacturing is prevented.
It is provided by the invention the specific scheme is that
A kind of trout feed production method, which is characterized in that the trout feed is made of following component by weight percentage:
Corn flour 6%, brewex's grains 3%, earthworm powder 0.28%, fish meal 26%, pig blood 0.2%, dandelion 0.2%, purslane 0.25%, rapeseed cake
8%, duckweed 16%, mulberry leaf 16%, seaweed 2%, egg pupa powder 4%, glycine betaine 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula
10%;
The production method include the following steps: 1), by rapeseed cake 8%, duckweed 16%, mulberry leaf 16%, 2% raw material of seaweed with 6~
The ribbon conveyer that installation is tilted on 15 degree is sent into receiving sieve impurity elimination cleaning, then after magnetic separator de-iron, through spiral ribbon mixer into
Row imports wind-force through double-vane flow deflector after mixing for the first time and removes stone feeder, then feeds vertical crusher and crushes to obtain smashing fineness
Raw material for 60~70 mesh is stand-by;
2) pig blood 0.2%, dandelion 0.2%, purslane 0.25%, brewex's grains 3%, are used into hammering crushing after cleaning screen clears up impurity elimination
Machine crushes to obtain raw material and first step gained raw material and corn flour 6%, earthworm powder 0.28%, fish meal 26%, egg pupa powder 4%, beet
After alkali 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula 10% carries out secondary mixing, kettle is fallen into through vibration discharger discharging
Formula quality-adjusting device is simultaneously passed through 62 DEG C~66 DEG C of steam, mixes quenched, keep 18~after twenty minutes, it is dry into after-ripening fluidized dryer
Crushed again through vertical crusher afterwards, smashing fineness be 90~100 mesh after through helix emptying machine be discharged again through dextrorotation variable-pitch auger
Feeder enters the adjustable screw blade formula quality-adjusting device of barrel temperature, adds 24~25% moisture, in 82 DEG C~87 DEG C of temperature
Degree is lower carry out quenched 32~38 seconds after, through screw blade formula retainer 78 DEG C~88 DEG C at a temperature of heat preservation 100~200 seconds it is ripe
Change sterilization, by dextrorotation variable-pitch auger feeder by bulking machine feed hopper feeding single screw squeezing expansion machine squeeze it is swollen
Change, temperature control is at 123~140 DEG C before depanning for extruding product, and pressure is controlled in 33~36kg/cm2, and the extruding product goes out
In 470~500kg/m3, the die throat diameter of the single screw squeezing expansion machine is Φ 1.8, major diameter for grain density control after mould
Than being 1.8, the bulking machine feed hopper gradient is greater than 72 degree, and two sides are symmetrically each provided with a gas butterfly, and the single screw rod is squeezed
The speed of mainshaft for pressing bulking machine is 500~550rpm, and the secondary mixing opens greatly two-door mixing machine using oar blade type, step 1) and
Hammer crusher described in step 2, vertical crusher, micronizer discharge port be all rectangular or rectangle, be connected separately with
One section of 30mm~130mm high is rectangular or the changeover portion of rectangle, and the other end of changeover portion is just connect with respective lower road equipment, institute
The one side for stating changeover portion is both provided with the safety plate with extinguishing device, and another plane of symmetry, which is both provided with, leads to outdoor pilot guarantor
Dangerous piece and pipeline;
3) puffed material obtained by step 3) is transported to through self-cleaning type bucket elevator, and is arranged in high-rise included evaporation and aqueous
Through vibration separation screen after conical air duct is dry in the double belt drying machines of the cross-flow type of rate control module, screening gained finished product into
Row is packaged stacking, is equipped with dust pelletizing system, the dust pelletizing system setting at each charging and discharging in the production method steps
There is pressure relief opening, and pressure relief opening is led to by outdoor using elongnated building conduit, the length of the elongnated building conduit is less than 3m, institute
State the turning that cannot have in the setting of elongnated building conduit scene less than 138 degree.
Preferably, pulse bag type dust collector of the dust pelletizing system using configuration antistatic filter bag, the impulse bag
Circle transition conduit is arranged in the ejection air port of deduster, and the round transition conduit other end and blower direct connection, the blower direct connection have
Muffler, the muffler is horizontal positioned, and the round transition length of tube is not more than 0.8m.
Preferably, the dextrorotation variable-pitch auger feeder installation gradient is no more than 10 °.
Preferably, the grain density of the extruding product is controlled using density controller.
Preferably, autoclave quality-adjusting device inner cavity uses stainless steel material.
The invention has the following advantages:
Compared with prior art, the invention has the advantages that significantly reducing cost of material, but nutrition is equal for resulting trout feed
Weighing apparatus, feeding effect is good, has good diseases prevention, promotes digestion, and improve efficiency of feed utilization, reduce residual bait, improves
Water quality eliminates ultramicro grinding process in production method, further reduced production cost, controlled by refining temperature etc.,
Product effect but has same effect, and in addition production method of the invention has explosion prevention function, has prevented dust in Feed Manufacturing
The hidden danger of explosion.
Below by way of specific embodiment, the invention will be further described, but it should not be construed as protecting the present invention
The limitation of range.
Embodiment 1
A kind of trout feed production method, which is characterized in that the trout feed is made of following component by weight percentage:
Corn flour 6%, brewex's grains 3%, earthworm powder 0.28%, fish meal 26%, pig blood 0.2%, dandelion 0.2%, purslane 0.25%, rapeseed cake
8%, duckweed 16%, mulberry leaf 16%, seaweed 2%, egg pupa powder 4%, glycine betaine 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula
10%;
1), by rapeseed cake 8%, duckweed 16%, mulberry leaf 16%, 2% raw material of seaweed the production method includes the following steps: with 6 degree
The ribbon conveyer of upper inclination installation is sent into receiving sieve impurity elimination cleaning, then after magnetic separator de-iron, carries out the through spiral ribbon mixer
After mixed once through double-vane flow deflector import wind-force remove stone feeder, then feed vertical crusher crush smashing fineness be 60
Purpose raw material is stand-by;
2) pig blood 0.2%, dandelion 0.2%, purslane 0.25%, brewex's grains 3%, are used into hammering crushing after cleaning screen clears up impurity elimination
Machine crushes to obtain raw material and first step gained raw material and corn flour 6%, earthworm powder 0.28%, fish meal 26%, egg pupa powder 4%, beet
After alkali 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula 10% carries out secondary mixing, kettle is fallen into through vibration discharger discharging
Formula quality-adjusting device is simultaneously passed through 62 DEG C of steam, mix it is quenched, after being kept for 18 minutes, into after-ripening fluidized dryer it is dry after again through vertical
Formula pulverizer crushes, and smashing fineness enters barrel through dextrorotation variable-pitch auger feeder again to be discharged after 90 mesh through helix emptying machine
The adjustable screw blade formula quality-adjusting device of temperature, adds 24% moisture, 82 DEG C at a temperature of carry out quenched 32 seconds after, through spiral shell
Oar blade type retainer is revolved in 78 DEG C of the at a temperature of heat preservation sterilization of curing in 100 seconds, is passed through by dextrorotation variable-pitch auger feeder swollen
Change machine feed hopper feeds single screw squeezing expansion machine and carries out extrusion, and temperature control is at 123 DEG C before depanning for extruding product, pressure
In 470kg/m3, the single screw rod squeezes swollen for grain density control of the power control after 33kg/cm2, the extruding product depanning
The die throat diameter of change machine is Φ 1.8, and draw ratio 1.8, greater than 72 degree, two sides are symmetrically respectively set the bulking machine feed hopper gradient
It is equipped with a gas butterfly, the speed of mainshaft of the single screw squeezing expansion machine is 500rpm, and the secondary mixing is big using oar blade type
Open two-door mixing machine, hammer crusher described in step 1) and step 2, vertical crusher, micronizer discharge port be all
Rectangular or rectangle, is connected separately with rectangular or rectangle the changeover portion of one section of 30mm high, the other end of changeover portion just with it is respective
The connection of lower road equipment, the one side of the changeover portion are both provided with the safety plate with extinguishing device, and another plane of symmetry is both provided with
Lead to outdoor pilot safety plate and pipeline;
3) puffed material obtained by step 3) is transported to through self-cleaning type bucket elevator, and is arranged in high-rise included evaporation and aqueous
Through vibration separation screen after conical air duct is dry in the double belt drying machines of the cross-flow type of rate control module, screening gained finished product into
Row is packaged stacking, is equipped with dust pelletizing system, the dust pelletizing system setting at each charging and discharging in the production method steps
There is pressure relief opening, and pressure relief opening is led to by outdoor using elongnated building conduit, the length of the elongnated building conduit is less than 3m, institute
State the turning that cannot have in the setting of elongnated building conduit scene less than 138 degree.
In real work, pulse bag type dust collector of the dust pelletizing system using configuration antistatic filter bag, the pulse packet
Circle transition conduit, the round transition conduit other end and blower direct connection, the blower direct connection is arranged in the ejection air port of formula deduster
There is muffler, the muffler is horizontal positioned, and the round transition length of tube is not more than 0.8m.
In real work, the dextrorotation variable-pitch auger feeder installation gradient is no more than 10 °.
In real work, the grain density of the extruding product is controlled using density controller.
In real work, autoclave quality-adjusting device inner cavity uses stainless steel material.
Embodiment 2
A kind of trout feed production method, which is characterized in that the trout feed is made of following component by weight percentage:
Corn flour 6%, brewex's grains 3%, earthworm powder 0.28%, fish meal 26%, pig blood 0.2%, dandelion 0.2%, purslane 0.25%, rapeseed cake
8%, duckweed 16%, mulberry leaf 16%, seaweed 2%, egg pupa powder 4%, glycine betaine 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula
10%;
1), by rapeseed cake 8%, duckweed 16%, mulberry leaf 16%, 2% raw material of seaweed the production method includes the following steps: with 7 degree
The ribbon conveyer of upper inclination installation is sent into receiving sieve impurity elimination cleaning, then after magnetic separator de-iron, carries out the through spiral ribbon mixer
After mixed once through double-vane flow deflector import wind-force remove stone feeder, then feed vertical crusher crush smashing fineness be 63
Purpose raw material is stand-by;
2) pig blood 0.2%, dandelion 0.2%, purslane 0.25%, brewex's grains 3%, are used into hammering crushing after cleaning screen clears up impurity elimination
Machine crushes to obtain raw material and first step gained raw material and corn flour 6%, earthworm powder 0.28%, fish meal 26%, egg pupa powder 4%, beet
After alkali 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula 10% carries out secondary mixing, kettle is fallen into through vibration discharger discharging
Formula quality-adjusting device is simultaneously passed through 64 DEG C of steam, mix it is quenched, after being kept for 19 minutes, into after-ripening fluidized dryer it is dry after again through vertical
Formula pulverizer crushes, and smashing fineness enters barrel through dextrorotation variable-pitch auger feeder again to be discharged after 96 mesh through helix emptying machine
The adjustable screw blade formula quality-adjusting device of temperature, adds 24.5% moisture, 83 DEG C at a temperature of carry out quenched 36 seconds after, warp
Screw blade formula retainer passes through in 79 DEG C of the at a temperature of heat preservation sterilization of curing in 130 seconds by dextrorotation variable-pitch auger feeder
Bulking machine feed hopper feeds single screw squeezing expansion machine and carries out extrusion, and extruding product temperature before depanning is controlled at 133 DEG C,
In 480kg/m3, the single screw rod is squeezed for grain density control of the pressure control after 34kg/cm2, the extruding product depanning
The die throat diameter of bulking machine is Φ 1.8, and draw ratio 1.8, for the bulking machine feed hopper gradient greater than 72 degree, two sides are symmetrically each
It is provided with a gas butterfly, the speed of mainshaft of the single screw squeezing expansion machine is 520rpm, and the secondary mixing uses oar blade type
Open two-door mixing machine greatly, hammer crusher described in step 1) and step 2, vertical crusher, micronizer discharge port all
For rectangular or rectangle, be connected separately with rectangular or rectangle the changeover portion of one section of 70mm high, the other end of changeover portion just with it is respective
The connection of lower road equipment, the one side of the changeover portion is both provided with the safety plate with extinguishing device, and another plane of symmetry is all arranged
Have and leads to outdoor pilot safety plate and pipeline;
3) puffed material obtained by step 3) is transported to through self-cleaning type bucket elevator, and is arranged in high-rise included evaporation and aqueous
Through vibration separation screen after conical air duct is dry in the double belt drying machines of the cross-flow type of rate control module, screening gained finished product into
Row is packaged stacking, is equipped with dust pelletizing system, the dust pelletizing system setting at each charging and discharging in the production method steps
There is pressure relief opening, and pressure relief opening is led to by outdoor using elongnated building conduit, the length of the elongnated building conduit is less than 3m, institute
State the turning that cannot have in the setting of elongnated building conduit scene less than 138 degree.
In real work, pulse bag type dust collector of the dust pelletizing system using configuration antistatic filter bag, the pulse packet
Circle transition conduit, the round transition conduit other end and blower direct connection, the blower direct connection is arranged in the ejection air port of formula deduster
There is muffler, the muffler is horizontal positioned, and the round transition length of tube is not more than 0.8m.
In real work, the dextrorotation variable-pitch auger feeder installation gradient is no more than 10 °.
In real work, the grain density of the extruding product is controlled using density controller.
In real work, autoclave quality-adjusting device inner cavity uses stainless steel material.
Embodiment 3
A kind of trout feed production method, which is characterized in that the trout feed is made of following component by weight percentage:
Corn flour 6%, brewex's grains 3%, earthworm powder 0.28%, fish meal 26%, pig blood 0.2%, dandelion 0.2%, purslane 0.25%, rapeseed cake
8%, duckweed 16%, mulberry leaf 16%, seaweed 2%, egg pupa powder 4%, glycine betaine 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula
10%;
1), by rapeseed cake 8%, duckweed 16%, mulberry leaf 16%, 2% raw material of seaweed the production method includes the following steps: with 15 degree
The ribbon conveyer of upper inclination installation is sent into receiving sieve impurity elimination cleaning, then after magnetic separator de-iron, carries out the through spiral ribbon mixer
After mixed once through double-vane flow deflector import wind-force remove stone feeder, then feed vertical crusher crush smashing fineness be 70
Purpose raw material is stand-by;
2) pig blood 0.2%, dandelion 0.2%, purslane 0.25%, brewex's grains 3%, are used into hammering crushing after cleaning screen clears up impurity elimination
Machine crushes to obtain raw material and first step gained raw material and corn flour 6%, earthworm powder 0.28%, fish meal 26%, egg pupa powder 4%, beet
After alkali 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula 10% carries out secondary mixing, kettle is fallen into through vibration discharger discharging
Formula quality-adjusting device is simultaneously passed through 66 DEG C of steam, mix it is quenched, keep after twenty minutes, into after-ripening fluidized dryer it is dry after again through vertical
Formula pulverizer crushes, and smashing fineness enters cylinder through dextrorotation variable-pitch auger feeder again to be discharged after 100 mesh through helix emptying machine
The adjustable screw blade formula quality-adjusting device of wall temperature, adds 25% moisture, 87 DEG C at a temperature of carry out quenched 38 seconds after, warp
Screw blade formula retainer passes through in 88 DEG C of the at a temperature of heat preservation sterilization of curing in 200 seconds by dextrorotation variable-pitch auger feeder
Bulking machine feed hopper feeds single screw squeezing expansion machine and carries out extrusion, and extruding product temperature before depanning is controlled at 140 DEG C,
In 500kg/m3, the single screw rod is squeezed for grain density control of the pressure control after 36kg/cm2, the extruding product depanning
The die throat diameter of bulking machine is Φ 1.8, and draw ratio 1.8, for the bulking machine feed hopper gradient greater than 72 degree, two sides are symmetrically each
It is provided with a gas butterfly, the speed of mainshaft of the single screw squeezing expansion machine is 550rpm, and the secondary mixing uses oar blade type
Open two-door mixing machine greatly, hammer crusher described in step 1) and step 2, vertical crusher, micronizer discharge port all
For rectangular or rectangle, be connected separately with rectangular or rectangle the changeover portion of one section of 130mm high, the other end of changeover portion just with it is respective
The connection of lower road equipment, the one side of the changeover portion is both provided with the safety plate with extinguishing device, and another plane of symmetry is all arranged
Have and leads to outdoor pilot safety plate and pipeline;
3) puffed material obtained by step 3) is transported to through self-cleaning type bucket elevator, and is arranged in high-rise included evaporation and aqueous
Through vibration separation screen after conical air duct is dry in the double belt drying machines of the cross-flow type of rate control module, screening gained finished product into
Row is packaged stacking, is equipped with dust pelletizing system, the dust pelletizing system setting at each charging and discharging in the production method steps
There is pressure relief opening, and pressure relief opening is led to by outdoor using elongnated building conduit, the length of the elongnated building conduit is less than 3m, institute
State the turning that cannot have in the setting of elongnated building conduit scene less than 138 degree.
In real work, pulse bag type dust collector of the dust pelletizing system using configuration antistatic filter bag, the pulse packet
Circle transition conduit, the round transition conduit other end and blower direct connection, the blower direct connection is arranged in the ejection air port of formula deduster
There is muffler, the muffler is horizontal positioned, and the round transition length of tube is not more than 0.8m.
In real work, the dextrorotation variable-pitch auger feeder installation gradient is no more than 10 °.
In real work, the grain density of the extruding product is controlled using density controller.
In real work, autoclave quality-adjusting device inner cavity uses stainless steel material.
The specific implementation of the invention is not to be limited to these illustrations for above embodiments, for technology belonging to the present invention
For the those of ordinary skill in field, without departing from the inventive concept of the premise, several simple deductions can also be made or replaced
It changes, all shall be regarded as belonging to present invention scope of patent protection determined by the appended claims.
Claims (5)
1. a kind of trout feed production method, which is characterized in that the trout feed is by weight percentage by following component group
At: corn flour 6%, brewex's grains 3%, earthworm powder 0.28%, fish meal 26%, pig blood 0.2%, dandelion 0.2%, purslane 0.25%, vegetable seeds
Cake 8%, duckweed 16%, mulberry leaf 16%, seaweed 2%, egg pupa powder 4%, glycine betaine 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava are raw
Powder 10%;
The production method include the following steps: 1), by rapeseed cake 8%, duckweed 16%, mulberry leaf 16%, 2% raw material of seaweed with 6~
The ribbon conveyer that installation is tilted on 15 degree is sent into receiving sieve impurity elimination cleaning, then after magnetic separator de-iron, through spiral ribbon mixer into
Row imports wind-force through double-vane flow deflector after mixing for the first time and removes stone feeder, then feeds vertical crusher and crushes to obtain smashing fineness
Raw material for 60~70 mesh is stand-by;
2) pig blood 0.2%, dandelion 0.2%, purslane 0.25%, brewex's grains 3%, are used into hammering crushing after cleaning screen clears up impurity elimination
Machine crushes to obtain raw material and first step gained raw material and corn flour 6%, earthworm powder 0.28%, fish meal 26%, egg pupa powder 4%, beet
After alkali 0.06%, bile salt 0.01%, wheat-middlings 8%, cassava fecula 10% carries out secondary mixing, kettle is fallen into through vibration discharger discharging
Formula quality-adjusting device is simultaneously passed through 62 DEG C~66 DEG C of steam, mixes quenched, keep 18~after twenty minutes, it is dry into after-ripening fluidized dryer
Crushed again through vertical crusher afterwards, smashing fineness be 90~100 mesh after through helix emptying machine be discharged again through dextrorotation variable-pitch auger
Feeder enters the adjustable screw blade formula quality-adjusting device of barrel temperature, adds 24~25% moisture, in 82 DEG C~87 DEG C of temperature
Degree is lower carry out quenched 32~38 seconds after, through screw blade formula retainer 78 DEG C~88 DEG C at a temperature of heat preservation 100~200 seconds it is ripe
Change sterilization, by dextrorotation variable-pitch auger feeder by bulking machine feed hopper feeding single screw squeezing expansion machine squeeze it is swollen
Change, temperature control is at 123~140 DEG C before depanning for extruding product, and pressure is controlled in 33~36kg/cm2, and the extruding product goes out
In 470~500kg/m3, the die throat diameter of the single screw squeezing expansion machine is Φ 1.8, major diameter for grain density control after mould
Than being 1.8, the bulking machine feed hopper gradient is greater than 72 degree, and two sides are symmetrically each provided with a gas butterfly, and the single screw rod is squeezed
The speed of mainshaft for pressing bulking machine is 500~550rpm, and the secondary mixing opens greatly two-door mixing machine using oar blade type, step 1) and
Hammer crusher described in step 2, vertical crusher, micronizer discharge port be all rectangular or rectangle, be connected separately with
One section of 30mm~130mm high is rectangular or the changeover portion of rectangle, and the other end of changeover portion is just connect with respective lower road equipment, institute
The one side for stating changeover portion is both provided with the safety plate with extinguishing device, and another plane of symmetry, which is both provided with, leads to outdoor pilot guarantor
Dangerous piece and pipeline;
3) puffed material obtained by step 3) is transported to through self-cleaning type bucket elevator, and is arranged in high-rise included evaporation and aqueous
Through vibration separation screen after conical air duct is dry in the double belt drying machines of the cross-flow type of rate control module, screening gained finished product into
Row is packaged stacking, is equipped with dust pelletizing system, the dust pelletizing system setting at each charging and discharging in the production method steps
There is pressure relief opening, and pressure relief opening is led to by outdoor using elongnated building conduit, the length of the elongnated building conduit is less than 3m, institute
State the turning that cannot have in the setting of elongnated building conduit scene less than 138 degree.
2. a kind of trout feed production method according to claim 1, which is characterized in that the dust pelletizing system is using configuration
Circle transition conduit, the circle is arranged in the pulse bag type dust collector of antistatic filter bag, the ejection air port of the pulse bag type dust collector
Transition conduit other end and blower direct connection, the blower direct connection have muffler, and the muffler is horizontal positioned, the round coupling tube
Length is not more than 0.8m.
3. a kind of trout feed production method according to claim 1, which is characterized in that the dextrorotation variable-pitch auger is fed
Glassware installs gradient no more than 10 °.
4. a kind of trout feed production method according to claim 1, which is characterized in that the particle of the extruding product is close
Degree is controlled using density controller.
5. a kind of trout feed production method according to claim 1, which is characterized in that adopt autoclave quality-adjusting device inner cavity
Use stainless steel material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811565410.5A CN109393233A (en) | 2018-12-20 | 2018-12-20 | A kind of trout feed production method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811565410.5A CN109393233A (en) | 2018-12-20 | 2018-12-20 | A kind of trout feed production method |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109393233A true CN109393233A (en) | 2019-03-01 |
Family
ID=65460085
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811565410.5A Withdrawn CN109393233A (en) | 2018-12-20 | 2018-12-20 | A kind of trout feed production method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109393233A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2793466C1 (en) * | 2022-08-03 | 2023-04-04 | федеральное государственное бюджетное образовательное учреждение высшего образования "Волгоградский государственный аграрный университет" (ФГБОУ ВО Волгоградский ГАУ) | Trout production feed |
-
2018
- 2018-12-20 CN CN201811565410.5A patent/CN109393233A/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2793466C1 (en) * | 2022-08-03 | 2023-04-04 | федеральное государственное бюджетное образовательное учреждение высшего образования "Волгоградский государственный аграрный университет" (ФГБОУ ВО Волгоградский ГАУ) | Trout production feed |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109393253A (en) | A kind of tilapia feed processing technology | |
CN109393224A (en) | A kind of Bullfrog feedstuff production method | |
CN109430586A (en) | A kind of chum salmon feed production method | |
CN109393250A (en) | A kind of salmon feed production method | |
CN109393225A (en) | A kind of Bullfrog feedstuff processing technology | |
CN109393223A (en) | A kind of ricefield el fodder processing technology | |
CN109393248A (en) | A kind of sturgeon feed production method | |
CN109393213A (en) | A kind of ricefield el fodder production method | |
CN109393247A (en) | A kind of prawn feed processing technology | |
CN109430590A (en) | A kind of chum salmon feed processing technology | |
CN109393233A (en) | A kind of trout feed production method | |
CN109393218A (en) | A kind of catfish feed production method | |
CN109393239A (en) | A kind of perch feed production method | |
CN109430523A (en) | A kind of loach feed production method | |
CN109393241A (en) | A kind of crucian carp feed production method | |
CN109430581A (en) | A kind of feed of grass carp production method | |
CN109393234A (en) | A kind of trout feed processing technology | |
CN109393220A (en) | A kind of black carp feed production method | |
CN109393236A (en) | A kind of bream feed production method | |
CN109430584A (en) | A kind of carp feed production method | |
CN109393212A (en) | A kind of chub feed production method | |
CN109430587A (en) | A kind of fresh water fish feed production method | |
CN109430588A (en) | A kind of fresh water fish feed processing technology | |
CN109393232A (en) | A kind of catfish feed processing technology | |
CN109393243A (en) | A kind of tongue sole feed production method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20190301 |