WO2022139714A1 - Preparation unit before dryer for flake feed products - Google Patents
Preparation unit before dryer for flake feed products Download PDFInfo
- Publication number
- WO2022139714A1 WO2022139714A1 PCT/TR2021/050139 TR2021050139W WO2022139714A1 WO 2022139714 A1 WO2022139714 A1 WO 2022139714A1 TR 2021050139 W TR2021050139 W TR 2021050139W WO 2022139714 A1 WO2022139714 A1 WO 2022139714A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- flake
- product
- unit
- vibrating table
- preparation unit
- Prior art date
Links
- 238000002360 preparation method Methods 0.000 title claims abstract description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000005265 energy consumption Methods 0.000 claims abstract description 9
- 229940095709 flake product Drugs 0.000 claims description 47
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 230000005540 biological transmission Effects 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 230000006835 compression Effects 0.000 claims description 5
- 238000007906 compression Methods 0.000 claims description 5
- 238000003892 spreading Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 230000000694 effects Effects 0.000 claims description 2
- 235000013339 cereals Nutrition 0.000 abstract description 25
- 238000001035 drying Methods 0.000 abstract description 22
- 235000007319 Avena orientalis Nutrition 0.000 abstract description 3
- 244000075850 Avena orientalis Species 0.000 abstract description 3
- 240000005979 Hordeum vulgare Species 0.000 abstract description 3
- 235000007340 Hordeum vulgare Nutrition 0.000 abstract description 3
- 241000209140 Triticum Species 0.000 abstract description 3
- 235000021307 Triticum Nutrition 0.000 abstract description 3
- 240000008042 Zea mays Species 0.000 abstract 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 abstract 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 abstract 1
- 235000005822 corn Nutrition 0.000 abstract 1
- 239000000047 product Substances 0.000 description 23
- 238000010411 cooking Methods 0.000 description 3
- 238000009395 breeding Methods 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000011868 grain product Nutrition 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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
- A23K50/10—Feeding-stuffs specially adapted for particular animals for ruminants
-
- 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
- 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
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B1/00—Preliminary treatment of solid materials or objects to facilitate drying, e.g. mixing or backmixing the materials to be dried with predominantly dry solids
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/06—Grains, e.g. cereals, wheat, rice, corn
Definitions
- Invention relates to preliminary preparation unit before dryer (3), where grains such as com, oats, wheat, barley cooked with high pressure steam in the steam tower (1 ) and flaked with flake roller mill (2) are transferred after leaving the flake roller mill (2), before being transferred into the dryer (3) for drying process.
- the preparation unit (4) before dryer (3) the energy consumption required for the drying process is reduced and the flake drying efficiency is increased by separating the moisture, steam and water carried by the flaked grains, coming out of the flake roller mill (2), from the product flow before the drying process.
- the importance of flake feed production is gradually increasing in the feed sector in order to obtain high efficiency feed in fattening feed production.
- the flake feed product is obtained by drying the remaining steam and moisture after the grains such as com, barley, wheat, oats are crushed in flake (leaf) form by means of the flake roller mill after the cooking process with superheated steam.
- flake feed production the grains cooked with high pressure steam in the steam tower before the flake roller mill are flaked by means of the crushing cylinders in the flake roller mill, and then flake fattening feed is obtained by enabling that this grain flow in the form of flake is transferred to the dryer and the moisture and water contained in it are separated from the product.
- flake feed processes there is a high energy consumption for the drying process due to both the steam and moisture remaining from the steam cooking process and the water released from the grains crushed in the flake roller mill.
- the grain cooked with superheated steam in the steam boiler is transferred directly to the dryer after being crushed in the flake roller mill.
- the crushed grain coming out of the flake roller mill is passed through the dryer in order to separate the excess moisture and water from the product and then the feed product is obtained. There is no improvement here to separate the steam, moisture or water contained in the grain from the grain flow at the flake roller mill outlet.
- the preparation unit (4) has been developed for preparation before the dryer (3) in order to remove the free- steam, moisture and condensed water in the grain, which is cooked with high pressure steam in the steam tower (1 ) and crushed into flake in the flake roller mill (2), from the flow before the dryer (3) and to increase the flake drying efficiency.
- the developed preparation unit (4) enables that the excess steam, moisture and condensed water in the crushed grain coming out of the flake roller mill (2) is separated from the grain before entering the dryer (3) by positioning it between the flake roller mill (2) and the dryer (3).
- the developed preparation unit (4) enables the crushed grain flakes coming out of the flake roller mill (2) to be separated from each other and the water to be removed from the flakes by means of the Vibrating Table (4.2) on it.
- the air suction duct (4.4) on the developed preparation unit (4) ensures that the free-steam and hot air in the crushed grain flow coming out of the flake roller mill (2) to be evacuated from the unit (4).
- the developed pre-preparation unit (4) it is ensured that the energy consumption, i.e. the amount of energy required for drying in the dryer (3) is reduced and the drying efficiency is increased by ensuring that the steam and hot air in the grain coming out of the flake roller mill (2) in the form of flake is removed with air suction before entering the dryer (3).
- the energy consumption i.e. the amount of energy required for drying is reduced and the drying efficiency is increased by preventing the grains coming out of the flake roller mill (2) in the form of flakes sticking to each other before entering the dryer (3), and by spreading the product over the width of the dryer before entering the dryer (3) thanks to the Vibrating Table.
- the developed preparation unit (4) ensures the energy consumption, i.e. the amount of energy required for drying in the dryer (3) to be reduced and the drying efficiency to be increased by allowing the condensed water in the grain coming out of the flake roller mill (2) in the form of flakes to be accumulated in the vibrating table and discharged through the discharge channel (4) before entering the dryer (3).
- Preparation unit (4) which is the subject of the invention, developed for preparation before dryer (3) in order to remove free-steam, moisture and condensed water in the grain, which is cooked with high pressure steam in the steam tower (1 ) and crushed into flake in the flake roller mill (2), from the flow before being transferred to the dryer (3) with the intention of reducing the energy consumption of the dryer (3), contains at least one flake product inlet (4.1), where crushed product coming out of the flake roller mill (2) is fed into the unit (4), at least one vibrating table (4.2) that allows the flake product to be spread over a large surface with vibration effect, at least one vibration motor (4.3) that drives the vibrational motion of the vibrating table (4.2), at least one air suction duct (4.4) that allows free-steam and hot air inside the flake product fed into the unit (4) to be evacuated outside the unit, at least one product outlet (4.5) where the flake product passed over the vibrating table (4.2) is taken out of the unit (4) for transfer to the dryer (3), at least one compression spring (4.6
- the preparation unit (4) which is the subject of the invention, is a device positioned between the flake roller mill (2) and the dryer (3) in a way to provide pre-cooling and removal of excess steam, hot air, moisture and condensed water before the flake product coming out of the flake roller (2) as crushed product enters into the dryer (3) during the flake feed production process.
- the flake product inlet (4.1 ) developed in the preparation unit (4), which is subject of the invention, is the section that enables the flake product crushed in the flake roller mill (2) to enter into the preparation unit (4) in a way to be directed to the vibrating table (4.2).
- the vibrating table (4.2) developed in the preparation unit (4), which is subject of the invention, is the section that the flake product fed through the flake product inlet (4.1) is spread on it and allows both the cooling of the flake product by separating it and draining of the water into the tray (4.2) on it due to the vibrational motion.
- the vibrating table (4.2) is preferably manufactured in an inclined structure so that the water drained from the flake can be directed on the table (4.2).
- the vibration motor (4.3) developed in the preparation unit (4), which is the subject of the invention, is the part connected to the vibrating table (4.2) by means of the vibration transmission profile (4.7) so as to drive the vibrational motion of the vibrating table (4.2).
- the air suction duct (4.4) developed in the preparation unit (4) which is the subject of the invention, is the section connected to the unit (4) in a way to create suction, preferably by means of an air suction equipment, in order to ensure that the free steam and hot air flow in the flake product transferred into the unit (4) are removed from the flake product before the dryer (3).
- the air suction duct (4.4) is the section that preferably contains filter equipment inside it so as to prevent the leakage of product outside the unit (4).
- the product outlet (4.5) developed in the preparation unit (4), which is subject of the invention, is the section that allows the flake product, separated by spreading on the vibrating table (4.2) and the free-steam, hot air, moisture and water inside it removed, to exit the unit (4) in order to be transferred to the dryer (3).
- the compression spring (4.6) developed in the preparation unit (4), which is the subject of the invention, is the part that ensures the connection of the vibrating table (4.2), vibrational motion of which driven by the vibration motor (4.3), with the unit (4) in a way to prevent the deformation of the table (4.2) induced by the mechanical forces caused by vibration.
- the vibration transmission profile (4.7) developed in the preparation unit (4), which is the subject of the invention, is the connecting piece that enables vibrational motion provided by the vibration motor (4.3) is transmitted to the vibrating table (4.2).
- the discharge channel (4.8) developed in the preparation unit (4) which is the subject of the invention, is the section that is formed preferably as inclined and preferably in the form of a channel, where water inside the flake product drained to the surface of the vibrating table (4.2) after the flake product fed into the unit (4) being laid on the vibrating table (4.2) is transferred into the table (4.2) due to its preferably inclined structure and from here directed outside the unit (4).
- the product spreader (4.9) developed in the preparation unit (4), which is subject of the invention, is the section where the product entering from the flake product inlet (4.1 ) first contacts and preferably formed in a conical structure so as to ensure that the flake product is spread over a wide area on the vibrating table (4.2).
- the level adjustment mechanism (4.10) developed in the preparation unit (4), which is the subject of the invention, is the section connected to the vibrating table (4.2) so as to allow the adjustment of the product flow rate after the flake product fed into the unit (4) is laid on the vibrating table (4.2).
- the preparation unit (4) which is the subject of the invention, while the free-steam, moisture and hot air inside the cereal product, which has been turned into flake feed in the flake roller mill (2), is removed and discharged from the unit (4) through the air suction channel (4.4) after the entrance of the flake product through the flake product inlet (4.1 ) and being laid on the vibrating table (4.2) by means of the product spreader (4.9); whereas the liquid water inside it accumulates on the surface of the table (4.2) and is directed to the discharge channel (4.8) and from there to the outside of the unit (4).
- the energy consumption of the dryer (3) for the drying process will be low, since some of the steam, moisture and water in the flake feed exiting the unit outlet (4.5) being removed from the product before the dryer (3).
- the drying efficiency of the dryer (3) is increased, production costs can be reduced and the shelf life of the final product can be extended.
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Polymers & Plastics (AREA)
- Food Science & Technology (AREA)
- Zoology (AREA)
- Animal Husbandry (AREA)
- Biotechnology (AREA)
- Health & Medical Sciences (AREA)
- Botany (AREA)
- Molecular Biology (AREA)
- Mycology (AREA)
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- Drying Of Solid Materials (AREA)
- Cereal-Derived Products (AREA)
Abstract
Invention relates to preliminary preparation unit before dryer (3), where grains such as corn, oats, wheat, barley cooked with high pressure steam in the steam tower (1) and flaked with flake roller mill (2) are transferred after leaving the flake roller mill (2), before being transferred into the dryer (3) for drying process. With the preparation unit (4) before dryer (3), the energy consumption required for the drying process is reduced and the flake drying efficiency is increased by separating the moisture, steam and water carried by the flaked grains, coming out of the flake roller mill (2), from the product flow before the drying process.
Description
PREPARATION UNIT BEFORE DRYER FOR FLAKE FEED PRODUCTS
TECHNICAL FIELD
Invention relates to preliminary preparation unit before dryer (3), where grains such as com, oats, wheat, barley cooked with high pressure steam in the steam tower (1 ) and flaked with flake roller mill (2) are transferred after leaving the flake roller mill (2), before being transferred into the dryer (3) for drying process. With the preparation unit (4) before dryer (3), the energy consumption required for the drying process is reduced and the flake drying efficiency is increased by separating the moisture, steam and water carried by the flaked grains, coming out of the flake roller mill (2), from the product flow before the drying process.
PRIOR ART
The importance of flake feed production is gradually increasing in the feed sector in order to obtain high efficiency feed in fattening feed production. The flake feed product is obtained by drying the remaining steam and moisture after the grains such as com, barley, wheat, oats are crushed in flake (leaf) form by means of the flake roller mill after the cooking process with superheated steam.
It is also proven by scientific studies that the digestion of starch and similar ingredients in the content of grains increases after the formation of flake, and thus important elements for stock-breeding such as live weight and milk yield of livestock increase at high rates and stock-breeding productivity increases.
In flake feed production, the grains cooked with high pressure steam in the steam tower before the flake roller mill are flaked by means of the crushing cylinders in the flake roller mill, and then flake fattening feed is obtained by enabling that this grain flow in the form of flake is transferred to the dryer and the moisture and water contained in it are separated from the product. However,
in flake feed processes, there is a high energy consumption for the drying process due to both the steam and moisture remaining from the steam cooking process and the water released from the grains crushed in the flake roller mill.
In the systems used for flake feed production in the current technique, the grain cooked with superheated steam in the steam boiler is transferred directly to the dryer after being crushed in the flake roller mill. As mentioned in the document No.TR200908671, the crushed grain coming out of the flake roller mill is passed through the dryer in order to separate the excess moisture and water from the product and then the feed product is obtained. There is no improvement here to separate the steam, moisture or water contained in the grain from the grain flow at the flake roller mill outlet.
In the document No.TR201703707, the flaked grain in the flake roller mill after being subjected to superheated steam cooking in the steam tower, comes out directly from the roller mill and transferred to the dryer. Again, there is no improvement in the separation of steam, moisture and water in the crushed grain at the flake roller mill outlet.
Also in documents NO.US4126946 and CN107940939 and similar documents, in the drying units used in grain processing processes, the products subjected to pre-drying processes (washing, cleaning, grinding, etc.) are transferred directly to the dryers, and the drying steps are carried out in this unit. However, there is no intermediate process step before the dryer.
BRIEF DESCRIPTION OF THE INVENTION
In the production of flake fattening feed, the preparation unit (4) has been developed for preparation before the dryer (3) in order to remove the free- steam, moisture and condensed water in the grain, which is cooked with high pressure steam in the steam tower (1 ) and crushed into flake in the flake roller mill (2), from the flow before the dryer (3) and to increase the flake drying efficiency.
The developed preparation unit (4) enables that the excess steam, moisture and condensed water in the crushed grain coming out of the flake
roller mill (2) is separated from the grain before entering the dryer (3) by positioning it between the flake roller mill (2) and the dryer (3).
The developed preparation unit (4) enables the crushed grain flakes coming out of the flake roller mill (2) to be separated from each other and the water to be removed from the flakes by means of the Vibrating Table (4.2) on it.
The air suction duct (4.4) on the developed preparation unit (4) ensures that the free-steam and hot air in the crushed grain flow coming out of the flake roller mill (2) to be evacuated from the unit (4).
With the developed pre-preparation unit (4), it is ensured that the energy consumption, i.e. the amount of energy required for drying in the dryer (3) is reduced and the drying efficiency is increased by ensuring that the steam and hot air in the grain coming out of the flake roller mill (2) in the form of flake is removed with air suction before entering the dryer (3).
With the developed preparation unit (4), the energy consumption, i.e. the amount of energy required for drying is reduced and the drying efficiency is increased by preventing the grains coming out of the flake roller mill (2) in the form of flakes sticking to each other before entering the dryer (3), and by spreading the product over the width of the dryer before entering the dryer (3) thanks to the Vibrating Table.
With the developed preparation unit (4), ensures the energy consumption, i.e. the amount of energy required for drying in the dryer (3) to be reduced and the drying efficiency to be increased by allowing the condensed water in the grain coming out of the flake roller mill (2) in the form of flakes to be accumulated in the vibrating table and discharged through the discharge channel (4) before entering the dryer (3).
MEANING OF THE FIGURES
Figure 1. Preparation Unit General Layout View
Figure 2. Preparation Unit General View
Figure 3. Preparation Unit Sectional View
Figure 4. Preparation Unit Vibrating Table General View
The part numbers given in the figures are provided below.
1. Steam Tower
2. Flake Roller Mill
3. Dryer
4. Preparation Unit
4.1. Flake Product Inlet
4.2. Vibrating Table
4.3. Vibration Motor
4.4. Air Suction Duct
4.5. Product Outlet
4.6. Compression Spring
4.7. Vibration Transfer Profile
4.8. Discharge Channel
4.9. Product Spreader
4.10. Level Adjustment Mechanism
DETAILED DESCRIPTION OF THE INVENTION
Preparation unit (4), which is the subject of the invention, developed for preparation before dryer (3) in order to remove free-steam, moisture and condensed water in the grain, which is cooked with high pressure steam in the steam tower (1 ) and crushed into flake in the flake roller mill (2), from the flow before being transferred to the dryer (3) with the intention of reducing the energy consumption of the dryer (3), contains at least one flake product inlet (4.1), where crushed product coming out of the flake roller mill (2) is fed into the unit (4), at least one vibrating table (4.2) that allows the flake product to be spread over a large surface with vibration effect, at least one vibration motor (4.3) that drives the vibrational motion of the vibrating table (4.2), at least one air suction duct (4.4) that allows free-steam and hot air inside the flake product fed into the unit (4) to be evacuated outside the unit, at least one product outlet (4.5) where the flake product passed over the vibrating table (4.2) is taken out of the unit (4) for transfer to the dryer (3), at least one compression spring (4.6)
on the vibrating table (4.2) to counteract the force that will occur due to vibration, at least one vibration transmission profile (4.7) that provides the connection of the vibration motor (4.3) to the vibrating table (4.2), at least one discharge channel (4.8) on the vibrating table (4.2) that enables the liquid water separated from the flake product to be directed out of the unit (4) through the table (4.2), at least one product spreader (4.9) that allows spreading of the product transferred into the unit (4) through the flake product inlet (4.1 ) to a wide area on the vibrating table (4.2) and the parts and sections of the level adjustment mechanism (4.10), which allows the adjustment of product flow rate after the flake product is laid on the vibrating table (4.2).
The preparation unit (4), which is the subject of the invention, is a device positioned between the flake roller mill (2) and the dryer (3) in a way to provide pre-cooling and removal of excess steam, hot air, moisture and condensed water before the flake product coming out of the flake roller (2) as crushed product enters into the dryer (3) during the flake feed production process.
The flake product inlet (4.1 ) developed in the preparation unit (4), which is subject of the invention, is the section that enables the flake product crushed in the flake roller mill (2) to enter into the preparation unit (4) in a way to be directed to the vibrating table (4.2).
The vibrating table (4.2) developed in the preparation unit (4), which is subject of the invention, is the section that the flake product fed through the flake product inlet (4.1) is spread on it and allows both the cooling of the flake product by separating it and draining of the water into the tray (4.2) on it due to the vibrational motion. The vibrating table (4.2) is preferably manufactured in an inclined structure so that the water drained from the flake can be directed on the table (4.2).
The vibration motor (4.3) developed in the preparation unit (4), which is the subject of the invention, is the part connected to the vibrating table (4.2) by means of the vibration transmission profile (4.7) so as to drive the vibrational motion of the vibrating table (4.2).
The air suction duct (4.4) developed in the preparation unit (4), which is the subject of the invention, is the section connected to the unit (4) in a way to
create suction, preferably by means of an air suction equipment, in order to ensure that the free steam and hot air flow in the flake product transferred into the unit (4) are removed from the flake product before the dryer (3). The air suction duct (4.4) is the section that preferably contains filter equipment inside it so as to prevent the leakage of product outside the unit (4).
The product outlet (4.5) developed in the preparation unit (4), which is subject of the invention, is the section that allows the flake product, separated by spreading on the vibrating table (4.2) and the free-steam, hot air, moisture and water inside it removed, to exit the unit (4) in order to be transferred to the dryer (3).
The compression spring (4.6) developed in the preparation unit (4), which is the subject of the invention, is the part that ensures the connection of the vibrating table (4.2), vibrational motion of which driven by the vibration motor (4.3), with the unit (4) in a way to prevent the deformation of the table (4.2) induced by the mechanical forces caused by vibration.
The vibration transmission profile (4.7) developed in the preparation unit (4), which is the subject of the invention, is the connecting piece that enables vibrational motion provided by the vibration motor (4.3) is transmitted to the vibrating table (4.2).
The discharge channel (4.8) developed in the preparation unit (4), which is the subject of the invention, is the section that is formed preferably as inclined and preferably in the form of a channel, where water inside the flake product drained to the surface of the vibrating table (4.2) after the flake product fed into the unit (4) being laid on the vibrating table (4.2) is transferred into the table (4.2) due to its preferably inclined structure and from here directed outside the unit (4).
The product spreader (4.9) developed in the preparation unit (4), which is subject of the invention, is the section where the product entering from the flake product inlet (4.1 ) first contacts and preferably formed in a conical structure so as to ensure that the flake product is spread over a wide area on the vibrating table (4.2).
The level adjustment mechanism (4.10) developed in the preparation unit (4), which is the subject of the invention, is the section connected to the vibrating table (4.2) so as to allow the adjustment of the product flow rate after the flake product fed into the unit (4) is laid on the vibrating table (4.2).
With the preparation unit (4), which is the subject of the invention, while the free-steam, moisture and hot air inside the cereal product, which has been turned into flake feed in the flake roller mill (2), is removed and discharged from the unit (4) through the air suction channel (4.4) after the entrance of the flake product through the flake product inlet (4.1 ) and being laid on the vibrating table (4.2) by means of the product spreader (4.9); whereas the liquid water inside it accumulates on the surface of the table (4.2) and is directed to the discharge channel (4.8) and from there to the outside of the unit (4). Thus, the energy consumption of the dryer (3) for the drying process will be low, since some of the steam, moisture and water in the flake feed exiting the unit outlet (4.5) being removed from the product before the dryer (3). Thus, while the drying efficiency of the dryer (3) is increased, production costs can be reduced and the shelf life of the final product can be extended.
Claims
CLAIMS It is the preparation unit (4), which is the subject of the invention, developed for preparation before the dryer (3) in order to remove free-steam, moisture and condensed water in the grain, which is cooked with high pressure steam in the steam tower (1 ) and crushed into flake in the flake roller mill (2), from the flow before the dryer (3) with the intention of reducing the energy consumption of the dryer, and it is characterized by containing at least one flake product inlet
(4.1 ) where the crushed product coming out of the flake roller mill (2) is fed into the unit (4), at least one vibrating table (4.
2) that allows the flake product to be spread over a large surface with the effect of vibration, at least one vibration motor (4.
3) that drives the vibrational motion of the vibrating table (4.2), at least one air suction duct (4.
4) that enables the transfer of free steam and hot air in the flake product fed into the unit (4) to the outside of the unit, at least one product outlet (4.
5) where the flake product passed over the vibrating table
(4.2) is taken out of the unit (4) in order to be transferred to the dryer (3), At least one compression spring (4.
6) to counteract the force that will occur on the vibrating table (4.2) due to vibration, at least one vibration transmission profile (4.
7) that enables the connection of the vibration motor (4.3) to the vibrating table (4.2), at least one discharge channel (4.
8) that enables the liquid water separated from the flake product on the vibrating table (4.2) to be directed to the outside of the unit (4) over the table (4.2), at least one product spreader (4.9) that enables the spreading of the product transferred into the unit (4) from the flake product inlet (4.1) to a wide area on the vibrating table (4.2) and level adjustment mechanism (4.10) parts and sections that enables the adjustment of the product flow rate after the flake product being laid on the vibrating table (4.2).
- 8 -
It is a preparation unit (4) as per Claim 1 , and it is characterized by the said preparation unit (4) being the unit positioned between the flake roller mill (2) and the dryer (3) so as to provide a pre-cooling and removal of excess steam, hot air, moisture and condensed water before the flake product coming out of the flake roller (2) as crushed enters the dryer (3) in the process of flake feed production. It is a preparation unit (4) as per Claim 1 , and it is characterized by the said flake product inlet (4.1) being the section that enables the flake product, which is crushed in the flake roller mill (2), to enter into the preparation unit (4) in a way that it is directed to the vibrating table (4.2). It is a preparation unit (4) as per Claim 1 , and it is characterized by the said vibrating table (4.2) being the section that the flake product fed from the flake product inlet (4.1 ) is laid on it and enables the flake product laid on it both to be cooled and leave the water inside it on the table (4.2) by separating the flake product with vibrational motion. It is a preparation unit (4) as per Claim 1 , and it is characterized by the said vibrating table (4.2) being the section produced preferably as an inclined structure in order to be able to direct the water separated from the flake product on the table (4.2). It is a preparation unit (4) as per Claim 1 , and it is characterized by the said vibration motor (4.3) being the part connected to the vibrating table (4.2) via the vibration transmission profile (4.7) so as to drive the vibrational motion of the vibrating table (4.2). It is a preparation unit (4) as per Claim 1 , and it is characterized by the said air suction duct (4.4) being the section connected to the unit (4) so as to create suction preferably by means of an air suction equipment in order to ensure that the free steam and hot air flow in the flake product transferred into the unit (4) are removed from the flake product before the dryer (3). It is a preparation unit (4) as per Claim 1 , and it is characterized by the said air suction duct (4.4) being the section preferably having
- 9 -
filter equipment inside it so as to prevent leakage of product to the outside of the unit (4).
9. It is a preparation unit (4) as per Claim 1 , and it is characterized by the said product outlet (4.5) being the section that allows the flake product, which is separated and the steam, hot air, moisture and water inside it removed by laying it on the vibrating table (4.2), to exit the unit (4) in order to be transferred to the dryer (3)..
10. It is a preparation unit (4) as per Claim 1 , and it is characterized by the said compression spring (4.6) being the part that enables the connection of the vibrating table (4.2) driven by the vibration motor (4.3) with the unit (4) in a way to prevent the deformation of the table (4.2) induced by the mechanical forces caused by vibration..
11. It is a preparation unit (4) as per Claim 1 , and it is characterized by the said vibration transmission profile (4.7) being a connection part that enables the transmission of the vibrational motion driven by the vibration motor (4.3) to the vibrating table (4.2).
12. It is a preparation unit (4) as per Claim 1 , and it is characterized by the said discharge channel (4.8) being the section, preferably formed as inclined and preferably as a channel, where the water inside the flake product fed into the unit (4) drained down to the surface of the table (4.2) is transferred into the table (4.2) after the flake product fed into the unit (4) is laid on the vibrating table (4.2), and from there it is directed to the outside of the unit (4) depending on the preferably inclined structure of the table (4.2).
13. It is a preparation unit (4) as per Claim 1 , and it is characterized by the said product spreader (4.9) being the section, where the product entering from the flake product inlet (4.1 ) first comes into contact with and preferably formed in a conical structure so as to ensure that the flake product is spread over a wide area on the vibrating table (4.2).
14. It is a preparation unit (4) as per Claim 1 , and it is characterized by the said level adjustment mechanism (4.10) is the section connected to the vibrating table (4.2) in such a way that the product flow rate
- 10 -
can be adjusted after the flake product fed into the unit (4) is laid on the vibrating table (4.2).
- 11 -
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TR2020/21667A TR202021667A2 (en) | 2020-12-25 | 2020-12-25 | Pre-dryer preparation unit for flake feed product |
TR2020/21667 | 2020-12-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2022139714A1 true WO2022139714A1 (en) | 2022-06-30 |
Family
ID=75576709
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/TR2021/050139 WO2022139714A1 (en) | 2020-12-25 | 2021-02-16 | Preparation unit before dryer for flake feed products |
Country Status (2)
Country | Link |
---|---|
TR (1) | TR202021667A2 (en) |
WO (1) | WO2022139714A1 (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4810513A (en) * | 1986-10-30 | 1989-03-07 | Merle Van Liere | Process for treating raw soybeans |
CN102519233A (en) * | 2011-12-13 | 2012-06-27 | 山东禹王实业有限公司 | Equipment specially used for ventilating and drying low-temperature soybean meal |
RU2013123295A (en) * | 2013-05-21 | 2014-11-27 | Открытое акционерное общество "Всероссийский научно-исследовательский институт комбикормовой промышленности" (ОАО "ВНИИКП") | CEREAL FLAKES PRODUCTION LINE |
CN204128325U (en) * | 2014-09-18 | 2015-01-28 | 常州恒诚富士特干燥设备有限公司 | Vibratingfluidbeddrier |
-
2020
- 2020-12-25 TR TR2020/21667A patent/TR202021667A2/en unknown
-
2021
- 2021-02-16 WO PCT/TR2021/050139 patent/WO2022139714A1/en active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4810513A (en) * | 1986-10-30 | 1989-03-07 | Merle Van Liere | Process for treating raw soybeans |
CN102519233A (en) * | 2011-12-13 | 2012-06-27 | 山东禹王实业有限公司 | Equipment specially used for ventilating and drying low-temperature soybean meal |
RU2013123295A (en) * | 2013-05-21 | 2014-11-27 | Открытое акционерное общество "Всероссийский научно-исследовательский институт комбикормовой промышленности" (ОАО "ВНИИКП") | CEREAL FLAKES PRODUCTION LINE |
CN204128325U (en) * | 2014-09-18 | 2015-01-28 | 常州恒诚富士特干燥设备有限公司 | Vibratingfluidbeddrier |
Also Published As
Publication number | Publication date |
---|---|
TR202021667A2 (en) | 2021-02-22 |
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