KR101144827B1 - Method for making granule feed and apparatus thereof - Google Patents

Abstract

The present invention relates to a granulated feed manufacturing method and apparatus, the manufacturing method comprising the steps of mixing all the ingredients for making the granular feed and filtered through a screen and then granulating process; Spraying the conveyed materials at medium temperature with a binder solution using a high pressure air atomizer to form granules; Drying and cooling the granular feed having the granular shape at high temperature; Re-screening the dried and cooled granulated feed to pulverize the excessively sized feed selected; And feeding the dust collected in the drying / cooling step and the pulverizing step back to the granulation step to repeat the granulation process, thereby completing the granular feed. Therefore, by preparing the granule feed material by granulating the material using a binder solution and then drying and cooling and screening, the feed solubility can be obtained, as well as decomposition of the component by coating the binder solution. And moisture penetration is prevented to improve the reliability of the product, and also to feed back the dust generated in the drying and cooling and screening step to the granulation step to produce granular feed, thereby greatly improving the production efficiency, etc. Gets the effect.

Granule feed manufacturing method and apparatus, binder solution, dextrin, screen, crushing

Description

Method for making granule feed and apparatus {Method for making granule feed and apparatus

The present invention relates to a method and apparatus for producing granular feed, and more particularly, to produce a desired granular feed through a drying and cooling step and a screening step after the feed is made into granular granules through a binder solution containing dextrin. According to the characteristics of the granular feed in which the fine powders are weakly bound to each other, it is possible to obtain a feed having improved solubility because there is a lot of space where water can penetrate upon dissolution, and also by coating the binder solution. The product's reliability is improved by preventing decomposition and moisture penetration, and because it's granule type, it is easy to flow in the farm feeder, which saves labor for feeding management, reduces feed loss and improves feed efficiency and pellets. Consists of small particles compared to the shape, etc. And, also, it relates to a granular food production method and apparatus for feedback to the dust generated in the drying and cooling step and screening step to step so that the screen again grains, production efficiency is greatly enhanced by making it possible to produce a granular feed.

In general, feed refers to food for the purpose of supplying nutrients to animals, such as livestock, poultry, and silkworms, and is the basic production data required for livestock, sheep breeding, and aquaculture fishing. Account for more than half of the market.

These feeds are classified into rich feeds and irradiated foods according to their nutritional value. The rich feeds are feeds with low fiber content and high energy and protein, while the feeds are rich with crude fiber and low energy and protein. In particular, herbivores are essential for the maintenance of health as a basic feed, the importance is high in the livestock industry.

In addition, the feed can be divided into a maintenance feed and a production feed in order to calculate the feed amount, which is a feed necessary for the livestock to maintain only life without any production activity, and the production feed is analogy. It is a feed necessary for production activities such as, fattening, motherhood, spawning, pregnancy, development, and ministry.

In terms of marketability of feed, it is classified into self-supply feed and purchased feed. In addition, there are cattle feed, pig feed and chicken feed according to the target livestock, and livestock breeding, stock raising, breeding stock etc. You can subdivide again.

Since the start of breeding animals, many studies have highlighted the importance of liquid substitutes or bitter feeds to maximize their growth potential. The genetic growth potential of piglets is much higher than generally thought.

In the UK, targets for weaning pig growth rates that are achievable on conventional farms are given at 100 g in the first week, 200 g in the second week and 400 g in the third week after weaning. However, this goal is far lower than the herd's genetic growth potential.

In the literature published so far, the highest growth rate was recorded in pigs fed unlimitedly using recombinant substitute oil for one day after birth, and these piglets grew by 571 g per day from 10 days to 30 days of age. From 30 to 50 days of age, 832 g per day were reported.

The test was made in the early 1970s and is expected to grow even higher if the same test is conducted using current genetically advanced pigs. Interest in feed for food has increased since the early 1990s, when studies showed that breast milk was not sufficient to meet the genetic growth potential of piglets.

Accordingly, since the early 1990s, substitute oils have been manufactured using dairy products and high quality raw materials available to have similar components to sows' dairy components. However, as the size of farms grow and the management of farms is automated, substitute oils containing large amounts of dairy products need to be dissolved in water. Difficulties were not exposed.

As such, it is very important for farmers to provide suitable and appropriate feed for livestock such as pigs.

On the other hand, with reference to Figure 1, as a schematic look at the conventional substitute milk feed, it is in the form of fine powder powder, and looking at the manufacturing method, the step of the user to manually input all the raw material in the powder shape into the inlet and Collecting the input raw materials in the hopper and transferring them to the upper end of the mixer; adding and mixing a predetermined amount of soybean oil to the materials transferred to the mixer; and storing the mixed feed before screening, and mixing is completed. The material has been manufactured by replacing the foreign matter or lumps through a vibrating screen, etc., and packaging and shipping the finished feed.

However, when the substitute feed of the prior art is used as a liquid substitute, some protein sources used in the substitute feed have a property of not being easily dissolved in water, and thus, it takes a long time to prepare a liquid substitute.

In addition, in the case of solid feed, most of the raw materials used in the substitute oil feed are fine particles and have high hygroscopic tendency to stick easily in the feeder. It takes a lot of labor, such as having to push to the bottom of the feed, as well as a problem that the amount of loss caused by sticking easily by the saliva around the mouth every time the animal is ingested.

In addition, since the powder feed is commercialized immediately after the screening, there is a problem that the productivity is greatly reduced, resulting in a waste of the product, since no special function for collecting the powder is provided in the screening process.

The present invention has been made to solve the problems of the prior art, through the binder solution containing the dextrin made to feed the granules in the form of granules, through the drying and cooling step and the screening step can produce the desired granular feed As a result, the granular feed has a weak binding of fine powders, so that water can penetrate during dissolution, thereby improving feed solubility as well as decomposing components by coating a binder solution. And it is an object of the present invention to provide a granulated feed manufacturing method and apparatus to prevent moisture penetration to improve the reliability of the product.

In addition, as it is a granule type, it is easy to flow in farm feeder, thus reducing labor for feeding management, reducing feed loss, improving feed efficiency, and mixing additives if necessary, consisting of small particles compared to pellets. Another object of the present invention is to provide a method and apparatus for preparing granular feed, which facilitates the following.

In addition, there is another object to provide a granulated feed manufacturing method and apparatus for greatly improving the production efficiency by feeding back the dust generated in the drying and cooling step and the screening step to the granulation step to produce a granulated feed. .

The granular feed production method of the present invention for achieving the above object comprises the steps of mixing all the ingredients for making the granular feed and filtered through a screen and then granulating process; Spraying the conveyed materials at medium temperature with a binder solution using a high pressure air atomizer to form granules; Drying and cooling the granular feed having the granular shape at high temperature; Re-screening the dried and cooled granulated feed to pulverize the excessively sized feed selected; And feeding the dust collected in the drying / cooling step and the pulverizing step back to the granulation step to repeat the granulation process, thereby completing the granular feed.

In addition, in the granulated feed manufacturing method according to the invention, the size of all the material to be transferred to the granulation process preferably has a size of 70 ~ 90mesh / inch.

In addition, in the granulated feed manufacturing method according to the present invention, it is preferable that the water content of the final feed produced through the granulation process has a content of 1 to 10% by weight.

In addition, in the granulated feed manufacturing method according to the present invention, it is preferable that the coating of the binder solution in the granulation process is performed until the outer peripheral surface of the granules is completely wrapped through the nozzle spraying.

In addition, in the method of manufacturing granular feed according to the present invention, the binder solution is a dextrin equivalent (DE: Dextrin Equivalent) of about 6 to 12 dextrin mixed with water at a predetermined ratio, the concentration of dextrin in the dextrin solution It is preferable that it is 15-20 weight%.

In addition, in the granulated feed manufacturing method according to the present invention, it is preferable to increase the palatability of the feed prepared by mixing 0.5 to 1% by weight of the total feed amount of saccharin and general sweetener in the binder solution.

In addition, in the granular feed manufacturing method according to the invention, the dextrin is preferably included in the range of 3 to 15% by weight, depending on the type of material and the process conditions.

And, the granular feed manufacturing apparatus of the present invention is a mixer for mixing all the ingredients to make the granular feed; A first screen for filtering out foreign substances, etc. of materials mixed in the mixer; A feeding hopper for storing the sorted material through the first screen; A granulator for forming granules by spraying a binder solution after forming a fluidized bed under medium temperature of the materials transferred from the feeding hopper; A dry cooler for drying and cooling the granular feed having a granular shape manufactured in the granulator at a high temperature; A second screen for re-screening the dried and cooled granulated feed to select an oversized feed; A grinder for crushing an excessively sized feed picked up from the second screen and feeding it back to the granulator; A dust collector for collecting foreign matter and collecting only dust from the air forming the fluidized bed in the granulator; And a filter for filtering the dust collected in the dust collector and transporting the dust back to the granulator.

In addition, in the granular feed manufacturing apparatus according to the present invention, the granulator, a housing having a space therein and a material inlet and a granule discharge port are formed on both sides, respectively, the upper and lower ends of the housing having a circulating gas outlet and an air inlet; An air distribution plate disposed at a lower end of the housing to isolate the upper and lower spaces and have a plurality of nozzles protruding upward; And a plurality of flow rate distribution rods having a heat exchanger function for supplying thermal energy to form a fluidized bed in the upper space part of the upper and lower spaced spaces spaced apart from each other in a zigzag state by a predetermined distance. It is preferable to be configured.

As described above, the granulated feed manufacturing method of the present invention by using the binder solution containing the dextrin to make the feed granule-like granules to produce the desired granular feed through the drying and cooling step and the screening step, Depending on the characteristics of granular feeds in which fine powders are weakly bound, there is a lot of space for water to penetrate during dissolution, so that feed can be obtained with improved solubility, and decomposition of components and moisture penetration by coating of binder solution. Is prevented to obtain the effect of improving the reliability of the product.

In addition, as it is a granule type, it is easy to flow in farm feeder, thus reducing labor for feeding management, reducing feed loss, improving feed efficiency, and mixing additives if necessary, consisting of small particles compared to pellets. The effect which becomes easy to do is obtained.

In addition, by feeding back the dust generated in the drying and cooling step and the screening step to the granulation step to produce granular feed, it is possible to obtain the effect of greatly improving the production efficiency.

Hereinafter, the present invention will be described with reference to the accompanying drawings.

As shown in Figures 2 to 6, the mixer 10 for mixing all the materials to make a granulated feed according to an embodiment of the present invention, and filtering foreign matters of the mixed material in the mixer 10, etc. After forming the fluidized bed under medium temperature the first screen 20 for, the feeding hopper 30 for storing the material selected through the first screen 20, and the materials transferred from the feeding hopper 30 Granulator 40 for spraying the binder solution to produce a granule shape, a dry cooler 50 for drying and cooling the granule feed having a granule shape manufactured by the granulator 40, and the drying and cooling Re-screening the finished granule feed to the second screen 60 to pick out the oversized feed, and the crusher for crushing the feed of the excessive size selected from the second screen 60 to feed back to the granulator 40 70, In the air forming the fluidized bed in the granulator 40, foreign matters are collected and dust is collected only in the dust collector 80, and the dust collected in the dust collector 80 filters the filter (90) and transports it back to the granulator 40. ) Is configured to include.

Here, the first and second screens 20 and 60 have a vibrating reticulated structure that separates and filters materials or feeds and foreign substances more efficiently.

The granulator 40 has a space formed therein, and a material inlet 41a and a granule outlet 41b are formed at both sides, respectively, and the circulating gas outlet 41c and the air inlet 41d are respectively formed at upper and lower ends thereof. An air distribution plate 42 and an upper portion of the air distribution plate 42 having a housing 41 having a plurality of nozzles 42a which are disposed at a lower end of the housing 41 to isolate the upper and lower spaces and protrude upward. A plurality of flow distribution rods 43 having a heat exchanger function for supplying thermal energy as needed while at the same time spaced up and down spaced apart and arranged in a zigzag layer to the fluidized layer of the material in the upper space portion It is composed.

Here, the air distribution plate 42 is disposed below the material inlet 41a and the granules outlet 41b, and the material inlet 41a is disposed above the granules outlet 41b, when viewed in positional structure, The granulated feed is produced and discharged smoothly in a state where a fluid phase of the material is formed.

The dust collector 80 is preferably configured to collect dust through a cyclone function causing air vortex.

In addition, the filter 90 is provided with a predetermined bag filtering member (not shown) for filtering the dust, and after the dust of the dust collector 80 is filtered to some extent, the filtering member. It is preferable that a separate blow member (not shown) is provided to shake off the dust by hitting.

Reference numeral 95 denotes a blower for supplying air to the granulator 40.

In addition, the granulated feed manufacturing method according to the present invention is a step of mixing all the ingredients for making the granular feed and filtered through the screen and then transferred to the granulation process, by spraying the binder solution at medium temperature to form a granular shape Forming a granular feed, drying and cooling the granular feed having a granular shape, and re-screening the granulated feed having been dried and cooled to pulverize an excessively sized feed selected; And feeding the dust collected in the drying / cooling step and the pulverizing step back to the granulation step to repeat the granulation process, thereby completing the granular feed.

Here, the size of all the materials transferred to the granulation process has a size of 70 ~ 90 mesh / inch, most preferably it should have a size of 80 mesh / inch.

In addition, the water content of the final feed produced through the granulation process is preferably less than 10% by weight, that is, having a content of 1 to 10% by weight.

The process adopted in the present invention is a wet granulation method, among which a liquid spray granulation method is applied, and in this wet granulation process, the binder solution is used to promote the aggregation process, and this binder solution It is important to select an element (material) that can be easily aggregated by the first one. The first requirement is that the size of the material is 80 mesh / inch as described above.

By this liquid spray method, after the materials are evenly mixed in the mixing process, the liquid spray is sprayed to the materials in the granulation step through the screening and feeding step.

Here, the granulation step is performed in a granulator, and in the granulation step, after forming the fluidized bed under medium temperature air conditions, the mixed particles are sprayed with a binder solution to form a predetermined granular form.

On the other hand, the binder solution to be sprayed is preferably such that the binder solution is sprayed with a number of fine droplets so that the volume ratio to mass as large as possible.

FIG. 5 is an example of a high-pressure air atomizer for spraying a binder solution into fine particles, and shows an atomizer for miniaturizing a binder solution using kinetic energy of a high speed jet flow ejected from a nozzle.

When the high-pressure air is ejected, the shock wave and the expansion wave are repeatedly formed as shown in the drawing to finely atomize the binder solution. As an example of the preferred atomizer, the above-mentioned high pressure air atomizer is proposed, but a general orifice type spray structure or other spray structure may be adopted.

Here, the spraying is made by a high-pressure nozzle spraying method, as shown in Figure 6, the sprayed binder solution 100 is sprayed on the particles 200 to promote granular shape aggregation, particles in contact with each other in a low humidity situation The particles adhere to each other by the formation of a so-called liquid connection path 300, which connects the particles to each other, and finally, granular granules are formed when the liquid binder solution completely wraps around the connected particles. will be.

Meanwhile, the binder solution is a mixture of dextrin having a dextrin equivalent (DE) of about 6 to 12 and water at a predetermined ratio, and the concentration of dextrin in the dextrin solution is preferably 15 to 20% by weight. , The dextrin is preferably included in the range of 3 to 15% by weight depending on the type of material and the process conditions.

Here, the saccharin and the general sweetener in the binder solution may increase the palatability of the prepared feed by mixing 0.5 to 1% by weight of the total feed amount.

The granules thus formed are dried and cooled again by hot air, and lumps produced in excessive sizes during the process are collected through a screen and then crushed through a so-called pin mill grinder, which is a grinder, and then granulated again. It will be moved.

In addition, the dust generated during the cooling process is transferred to the granulator, which is a granulation step.

This basic granular feed is produced and at the same time the feedback process is repeatedly circulated to finally obtain the desired granular feed.

1 is a schematic flowchart showing a substitute milk feed manufacturing process of the prior art.

Figure 2 is a schematic flowchart showing a granule feed manufacturing process according to an embodiment of the present invention.

Figure 3 is a schematic diagram showing an apparatus for producing granular feed according to an embodiment of the present invention.

Figure 4 is a cutaway perspective view showing a granulator of the granular feed manufacturing apparatus according to an embodiment of the present invention.

Figure 5 is a schematic diagram showing the main part showing a state in which the binder solution is a high-pressure spraying during the granulation feed manufacturing process according to an embodiment of the present invention.

Figure 6 is a schematic diagram showing a process in which the particles are granulated by being connected to each other through a binder solution of the granular feed manufacturing method according to an embodiment of the present invention.

DESCRIPTION OF REFERENCE NUMERALS

10: mixer 20: first screen

30: feeding hopper 40: granulator

41: housing 41a: material inlet

41b: granule outlet 41c: circulating gas outlet

41d: air inlet 42: air distribution plate

42a: nozzle 43: flow distribution rod

50: dry cooler 60: second screen

70: grinder 80: dust collector

90 filter 95 blower

100 binder solution 200 particles

300: liquid connection

Claims (9)

Mixing all the ingredients for making the granulated feed, filtering through the screen and then transferring to the granulation process; Forming the fluidized bed under medium temperature air, and then introducing the micronized binder solution into the fluidized bed by introducing into a jet flow of high pressure air to form a granular shape; Drying and cooling the granular feed having the granular shape at high temperature; Screening the dried and cooled granulated feed again to select granular feed having an excessive size, and pulverizing the selected granulated feed of excessive size; And Feeding the dust collected in the drying and cooling steps and the pulverizing step back into the granulation step to repeat the granulation process, thereby completing granulated feed; Granule feed manufacturing method comprising a. The method of claim 1, All the size of the material transferred to the granulation process granule feed manufacturing method characterized in that it has a size of 70 ~ 90mesh / inch. The method of claim 1, Moisture content of all materials produced through the granulation process is characterized in that it has a content of 1 to 10% by weight. The method of claim 1, The method of granulating feed, characterized in that the coating of the binder solution in the granulation process is performed until the outer peripheral surface of the granules is completely wrapped through the nozzle spraying. The method of claim 1, The binder solution is a dextrin equivalent (DE: Dextrin Equivalent) is a mixture of dextrin and water of about 6 to 12 in a predetermined ratio, the concentration of dextrin in the dextrin solution is characterized in that the granule feed, characterized in that 15 to 20% by weight Way. The method of claim 5, Method for producing a granular feed, characterized in that to increase the palatability of the feed prepared by mixing 0.5 to 1% by weight of the total feed amount of saccharin and general sweetener in the binder solution. The method of claim 5, The dextrin is granule feed manufacturing method characterized in that the inclusion degree is in the range of 3 to 15% by weight depending on the type and process conditions of the material. A mixer 10 for mixing all materials to make granular feed; A first screen 20 for filtering foreign matters of the material mixed in the mixer 10; A feeding hopper 30 for storing the sorted material through the first screen 20; A granulator 40 for forming granules by spraying the materials transferred from the feeding hopper 30 under medium temperature air and then spraying the finely divided binder solution into the fluidized bed by introducing into a jet flow of high pressure air; A dry cooler 50 for drying and cooling the granular feed having a granular shape manufactured by the granulator 40 at a high temperature; A second screen 60 for re-screening the dried and cooled granulated feed to select an oversized feed; A grinder 70 for pulverizing feed of excessive size selected from the second screen 60 and feeding it back to the granulator 40; A dust collector (80) for filtering foreign matters from the air forming the fluidized bed in the granulator (40) and collecting only dust; And A filter (90) for filtering the dust collected by the dust collector (80) and feeding it back to the granulator (40); Granular feed manufacturing device comprising a. The method of claim 8, The granulator 40, A housing 41 having a space formed therein, a material inlet 41a and a granule outlet 41b formed on both sides thereof, respectively, having a circulating gas outlet 41c and an air inlet 41d at the upper and lower ends thereof; An air distribution plate 42 disposed at a lower end of the housing 41 to isolate the upper and lower spaces and have a plurality of nozzles 42a protruding upward; And A plurality of flow distribution rods having a heat exchanger function for supplying thermal energy to form a fluidized bed of a material in the upper space part of the air distribution plate 42 is spaced up and down spaced apart in a zigzag state at a predetermined distance. (43); Granular feed production apparatus characterized in that comprises a.

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