KR102063413B1 - Manufacturing factory system having complex equipment of far infrared dry apparatus and magnetic separating apparatus for eco agricultural and marineproducts of organic processed food and manufacturing method for powder using thesame - Google Patents

Abstract

The present invention relates to an eco-friendly agricultural and marine product organic processed food preparing factory system having a complex production facility including a far-infrared dryer and a cascade magnetic sorter; and a powder preparing method using the same. The eco-friendly agricultural and marine product organic processed food preparing factory system of the present invention comprises: a far-infrared dryer system (100); a first sorter (210); a washer (300); a hot air dryer (400); a second sorter (220); a hyper-grinder (500); and a cascade magnetic sorter (600). Therefore, a loss expected in a drying process can be fundamentally prevented while preserving unique nutrients of raw ingredients.

Description

MANUFACTURING FACTORY SYSTEM HAVING COMPLEX EQUIPMENT OF FAR INFRARED DRY APPARATUS AND MAGNETIC SEPARATING APPARATUS FOR ECO AGRICULTURAL AND MARINEPRODUCTS OF ORGANIC PROCESSED FOOD AND MANUFACTURING METHOD FOR POWDER USING THESAME}

The present invention relates to an environment-friendly agricultural and aquatic products organic food manufacturing plant system having a complex production equipment including a far-infrared drying device and cascade magnetic screening device, and to a powder powder manufacturing method using the same. The present invention relates to an eco-friendly agricultural and aquatic product manufacturing plant system and a powder powder manufacturing method using the cascade continuous movement type self-selection device to effectively verify the safety of agricultural and marine products received.

In the case of organic agricultural and marine products, they are naturally exposed to various environments due to the nature of harvesting. Therefore, when various kinds of foreign matters, especially metallic foreign matters, are added during the cultivation or transportation process, they may adversely affect the human body. Various efforts have been made to remove foreign substances.

In addition, organic processed foods using agricultural products harvested in nature has a problem that a lot of manpower and a number of drying processes and a long time is used when drying in natural light such as the sun because the raw material contains a lot of moisture.

In order to overcome these problems, various efforts have been made to dry raw materials harvested in nature in large quantities. However, most of them use high-temperature drying methods using electric heaters, so they are dried when applied to various kinds of agricultural and fish products uniformly. There was a problem that the production efficiency is sharply lowered due to the loss of material in the process.

In addition, when performing a process requiring low temperature drying in order to prevent the nutrients of the raw material is destroyed during the drying process, the drying time is excessively excessive, resulting in a manufacturing cost increase. When the hot air drying method of directly transferring heat to the nutrients are destroyed, there is a problem that the quality is sharply reduced after production.

In addition, in recent years, in order to produce a large amount of agricultural and marine products processed foods represented by organic processed foods due to a diet craze due to a change in consumers' perception, it is possible to quickly process materials such as leafy vegetables that are difficult to grind. There is a need for a manufacturing system.

Therefore, the manufacturing of eco-friendly organic processed foods that can not only remove metal foreign substances that can flow into the manufacturing process or transportation process, but also prevent material loss and nutrient destruction during the drying process and effectively crush various materials during powder processing. There is an urgent need for realistic and applicable technologies related to technology.

Korean Utility Model Publication KR 20-2008-0005986 (Publication date 2008.12.04.)

The present invention has been made in order to solve the above problems, the present invention, eco-friendly agricultural and aquatic products organic processing equipped with a far-infrared drying device and a magnetic sorting device of the cascade continuous movement method for effectively verifying the safety of the certified organic agricultural products An object of the present invention is to provide a food manufacturing plant system and a powder powder manufacturing method using the same.

Eco-friendly agricultural and aquatic products organic food manufacturing plant system equipped with a composite production facility according to an embodiment of the present invention, in an organic processed food manufacturing plant system having a complex production facility, can be installed and relocated at various locations according to the type of raw materials It is formed to be assembled in a modular form so that the moisture content of raw materials harvested from nature is less than 7% by simultaneously implementing a far-infrared drying method using a planar heating element, a cooling drying method using a cooler, and a vacuum drying method using a vacuum pump. A far-infrared drying apparatus system of a triple hybrid method capable of performing a pretreatment process; A first sorter 210 for removing foreign substances by using a wind separator and an LED vision separator in units of 100 kg per unit of raw material passing through the far infrared drying apparatus system 100; Washing machine 300 to clean the foreign matter including four minutes, dirt, straw, and strings by washing at room temperature up to 3 tons per 100kg units of the material that needs to be washed out of the material passed through the first sorter 210 at a time ; 5% to 6 hours of hot air drying at a temperature between 60 and 70 degrees Celsius using a rectangular box that can accommodate 500 kg of the material that has passed through the washer 300 at a time of 5% moisture content of the raw material Hot air dryer 400 to be below; A second sorter 220 for sorting the material that has passed through the hot air dryer 400 up to 3 tons per day in the same manner as the first sorter; A hyper grinder 500 including at least one grinder for collecting the material passing through the second sorter 220 and feeding it into the upper hopper and then treating the material at a processing speed of 200 kg per one time to a predetermined particle size; And it is formed to be implemented in a modular form so that it can be installed and repositioned at various locations according to the type of raw materials, processing the metal foreign matter of the powder powder passing through the hyper-crusher 500 by cascade continuous movement method 100kg each time Cascade magnetic separation device 600 that can be; may be provided.

The organic processed food manufacturing plant system may further include a cutter 700 for cutting to 5 cm or less when the size of the material passing through the washer 300 exceeds 5 cm.

Cascade magnetic separator device 600 constituting the organic processed food manufacturing plant system, the hopper portion having a rectangular shape of a light beam narrowing so that the material can be injected into the upper side; An inclined screw conveyor unit 602 for transferring the material introduced into the hopper unit 601 to the uppermost end of the magnetic force selection device 600; Square housing 603 having a receiving space for accommodating the plurality of magnetic rods so that the material conveyed to the uppermost through the inclined screw conveyor 602 can pass through the plurality of magnetic rods while moving in the lower vertical direction ); A cylindrical vibrator 604 disposed under the rectangular housing 603 and having a mesh network therein for passing only powder powder of a predetermined size; And a driving unit 605 for transmitting the vibration to the cylindrical vibrator 604 so that the powder powder of a predetermined size is discharged.

The hot air dryer 400 constituting the organic processed food manufacturing plant system is formed in a box shape having a size of 160 cm, 300 cm, and 90 cm in length and length, respectively, and the inside and the outside of the wall are formed of a material of the sun. A hot air drying housing 410 having a thermal insulation metal wall having a thickness of 5 cm therein and equipped with a drying tray inside the box; A heat generating device 420 having a length of horizontal length and height of 96 cm, 122 cm, and 122 cm at one end in a longitudinal direction of the hot air drying housing 410 to generate heat by heating the hot air drying housing 410; And a hot air dry control box 430 for controlling the temperature of the hot air dry housing 410 by controlling the heat generating device 420 while displaying the temperature of the hot air dry housing 410.

The organic processed food manufacturing plant system may use a stirrer instead of a hot air dryer when the material passed through the washing machine is grains such as beans and sesame seeds.

The hyper grinder 500 constituting the organic processed food manufacturing plant system includes a raw material input hopper 511, a transfer screw 512a communicating with a lower portion of the raw material input hopper 511, and the transfer screw 512a. A raw material conveying part 510 installed in the longitudinal direction and inclined at an upper diagonal and having a screw housing tube 512 for conveying a material to be crushed into the raw material input hopper 511; It is provided with a connecting hopper 521 of the upper and lower narrow shape for accommodating the raw material discharged from the end of the screw housing 512 constituting the raw material transfer unit 510, and pulverizes the raw material flowing through the connecting hopper 521 A first mill 520 having a milling housing 522 to be formed; The centrifugal hopper 532 and the dust collecting means which are formed by extending the lower portion of the cylindrical body 531 and the cylindrical body 531 that is air-pneumatically accommodated by the blower is blown by the primary crusher 520 A plurality of cyclone powder collectors 530 having air discharge parts 533 connected to the plurality of cyclone powder collectors 530; A plurality of secondary grinders 540 disposed to be in communication with each of the plurality of cyclone powder collectors 530 to further grind the powder mass discharged by the cyclone powder collectors 530; A horizontal housing part 550 for horizontally transferring powder powder discharged to the plurality of secondary grinders 540 under a single feed pipe; A vibrating body 560 having a mesh network therein for allowing only a predetermined particle size to pass through the powder powder introduced from the horizontal housing 550; And a driving unit 570 for transmitting the vibration to the vibrating body 560 to discharge powder powder of a predetermined size.

The cyclone powder collector 530 of the hyper grinder constituting the organic processed food manufacturing plant system is formed on the outer circumferential surface of the centrifugal hopper 532 which extends below the cylindrical body 531. By forming the pulse generating means (532a) for transmitting the shock wave on the inner wall surface it can prevent the powder powder is stuck to the inner surface of the centrifugal hopper (532).

The first grinder 520 and the second grinder 540 of the hyper grinder constituting the organic processed food manufacturing plant system, the projections of a predetermined size on the cylindrical inner wall surface constituting the housing 521 of the grinder ( A crushing rotary blade 522 formed to form 521a and closely spaced with the uneven protrusion 521a at a minute interval may be rotatably installed on the central rotation shaft 523 of the cylindrical housing.

The triple hybrid type far-infrared drying device system constituting the organic processed food manufacturing plant system is an agent for evaporating moisture of a material introduced into a drying chamber with water vapor in the air using a planar heating element 111a providing far infrared rays and radiant heat. 1 drying means 111 and the water vapor of the raw material evaporated by the first drying means 111 not only discharges to the outside of the drying chamber 110a while circulating in the air inside each drying chamber 110a, Second drying means 112 that can additionally provide heat to the air inside each drying chamber 110a to maintain a constant temperature of the drying chamber 110a from which steam is discharged, and the first drying means. Third drying means 113 for quickly discharging the water vapor in the drying chamber (110a) relative to the 111 and the second drying means 112; Ratio, and a drying housing (110) having a three drying chamber (110a) for drying the interior temperature at the same time various kinds of agricultural and marine products, while maintaining the low temperature of below 55 ° C; And operating the three drying chambers 110a and the first drying means 111 to the third drying means 113 constituting the drying housing 110, and the three drying chambers 110a and the first drying means 111. ) To a control panel 120 for displaying the operating state of the third drying means 113 and a vacuum control unit 130 for controlling the three vacuum chamber internal vacuum state, wherein the control panel 120 The temperature of the planar heating element can be adjusted so that the internal temperatures of the three drying chambers 110a are 45 degrees Celsius, 50 degrees Celsius, and 55 degrees Celsius, respectively, and when the raw materials are put into the drying chamber 110a, the vacuum control unit 130 By using the vacuum pump 113a constituting the third drying means 113 until the internal temperature reaches a specific temperature set in advance to quickly discharge the moisture in the drying chamber (110a), the first Gun using the drying means 111 and the second drying means 112 Chamber (110a) it is possible to maintain the internal temperature.

The second drying means constituting the triple-infrared far-infrared drying apparatus system includes: a blowing air fan (112a) for circulating water vapor in the drying chamber (110a); A cooler (112b) which cools the water contained in the water vapor circulating in the drying chamber (110a) by the blowing air fan (112a) and discharges it to the outside; And an auxiliary heater part 112c capable of maintaining the internal temperature by receiving heat from the driving motor part constituting the cooler 112b and supplying the inside of the drying room 110a to further heat the air inside the drying room 110a. It may be provided.

The third drying means 113 constituting the triple hybrid type far-infrared drying apparatus system sucks steam vapor condensed through the cooler 112b and rapidly discharges it to the outside to vacuum the inside of the drying chamber 110a. And a vacuum pump 113a. When the internal temperature of the drying chamber 110a reaches a predetermined temperature, external air may be introduced.

Powdered powder manufacturing method using a hyper grinder of an eco-friendly agricultural and aquatic products organic food manufacturing plant system according to an embodiment of the present invention, the step of inputting a large amount of material through the input hopper 511 of the raw material transfer unit 510 (S7100); The material to be crushed into the hopper 511 through the screw housing tube 512 of the raw material transfer part 510 is installed in the longitudinal direction in the conveying screw 512a is communicated with the lower portion of the hopper 511. Is transferred (S7200); When the material to be pulverized discharged from the end of the screw housing 512 constituting the raw material transfer part 510 through the connection hopper 501 of the ordinary light strait shape is introduced into the cylindrical inner wall surface of the irregular protrusion 521a Forming and crushing the primary blade through the first grinder 510 rotatably installed on the central axis 523, the crushing rotary blade 522 is disposed in close proximity to the uneven protrusion (521a) (S7300) ); Powder powder pulverized by the primary crusher 510 is air-feeded using a blow and accommodated in a plurality of cylindrical bodies 531 constituting a plurality of cyclone powder collectors 530 (S7400); Discharging the powder mass by operating the centrifugal hopper 532 extending downward of the cylindrical body to configure the plurality of cyclone powder collectors 531 (S7500); Further pulverizing and pulverizing the powder mass discharged by the cyclone powder collector 531 through a plurality of secondary grinders 540 respectively disposed in communication with the lower side of the plurality of cyclone powder collectors 531 ( S7600); Step (S7700) to horizontally convey the powder powder discharged to the lower side of the plurality of secondary grinder 540 through a horizontal housing 550 consisting of a single transport pipe; And a powder mesh provided therein to collect powder powder having a predetermined particle size by selecting powder powder introduced from the horizontal housing 550 using a vibrating body 560 vibrated by the driving unit 560. Step S7800; may be provided.

The step of discharging the powder mass by operating the centrifugal hopper extending to the lower side of the cylindrical body to constitute the plurality of cyclone powder collector, the vortex in the centrifugal hopper 532 to separate and collect the pulverized powder by applying a centrifugal force As the phenomenon occurs, the powder powder contained in the cylindrical body 531 is collected in a lump and rapidly rotates, and the air introduced together with the powder powder inside the cylindrical body 531 is an air discharge part 533 connected to the dust collecting means. Discharged through; And when the shock wave is transmitted to the inner wall surface of the centrifugal hopper 532 by using the pulse generating means (532a) formed on the outer circumferential surface of the centrifugal hopper 532, powder powder stuck to the inner surface of the centrifugal hopper 532 falls It may include;

As described above, the present invention, in the construction of a far-infrared drying device by applying a triple hybrid drying method that implements a cooling drying method and a vacuum drying method at the same time, while preserving the inherent nutrients of the raw materials while reducing the expected loss in the drying process There is an effect to provide an eco-friendly agricultural and aquatic product dryers equipped with a triple-infrared infrared drying apparatus that can not only block the source but also minimize the water content in a short time, and a method for manufacturing organic aquatic products using the same.

In addition, the present invention has the effect of shortening the drying time by increasing the surface area to which the radiant heat is transmitted while evenly transmitting far infrared rays to the drying target material introduced into the drying chamber by using the radiant heat of the planar heating element.

In addition, the present invention can provide a function to remove only moisture without destroying the nutrients of the material by discharging the water vapor filled in the closed space inside the drying chamber using the cooler to the outside, in the drive unit for driving the cooler By providing an auxiliary heater to transfer the generated heat into the drying chamber there is an effect of maintaining a constant drying temperature required in the drying chamber while minimizing power consumption.

In addition, the present invention is to vacuum the inside of the drying chamber by using a vacuum pump can rapidly discharge the moisture in the drying chamber has the effect of shortening the drying time.

In addition, the present invention can be adjusted to have a different temperature in the configuration of a plurality of drying chambers, there is an effect to actively respond to the material to be put into the drying chamber.

In addition, the present invention has an effect that the drying process can be efficiently carried out by providing a drying process system that can process from washing to drying process in a predetermined unit zone.

In addition, the present invention, an eco-friendly agricultural and aquatic products manufacturing plant system and a powder powder manufacturing method using a far-infrared drying device and a cascade continuous movement magnetic separation device to secure the safety of the certified organic agricultural and aquatic products modularly equipped Has the effect of providing.

In addition, the present invention, by implementing a far-infrared drying system and a hot air dryer at the same time has the effect of providing an organic processed food manufacturing plant system that can reduce the drying time as possible while preserving the nutrients of the raw materials.

In addition, the present invention has an effect of facilitating the pulverization of leafy vegetables, which are difficult to pulverize, by forming a hyper-pulverizer capable of simultaneously implementing medium and fine grinding.

In addition, the present invention comprises a single machine in which a magnetic body passing means having a plurality of magnetic rods and a vibration means having a mesh network therein in a vertical structure, in the construction of a magnetic force selection device, inclined screw conveyor By implementing automation equipment in a limited space using wealth, the area of the entire factory system can be effectively used.

In addition, the present invention has a cyclone powder collector and a pulse generating means in the pulverizing process to configure the hyper-pulverizer has the effect of minimizing the loss of the powdered material and preventing malfunction due to the powder mass during the manufacturing process .

1 is a view for schematically showing the configuration of a manufacturing plant system according to an embodiment of the present invention.
2 is a view for schematically showing a drying system according to an embodiment of the present invention.
3 is a view for schematically showing a configuration of a far infrared ray drying apparatus according to an embodiment of the present invention.
4 is a flow chart showing a manufacturing method using a drying system according to an embodiment of the present invention.
FIG. 5 is a view schematically showing the casecade magnetic separator shown in FIG. 1.
FIG. 6 is a diagram schematically showing a single magnetic separator constituting the cascade magnetic separator shown in FIG.
FIG. 7 is a diagram schematically illustrating a configuration of the hypercrusher illustrated in FIG. 1.
8 is a view for explaining a raw material transfer unit of the hyper-crusher shown in FIG.
9 is a view for explaining the cyclone powder collector of the hyper-crusher shown in FIG.
FIG. 10 is a view for explaining a grinder constituting the hyper-crusher shown in FIG.
FIG. 11 is a flowchart schematically illustrating a method of preparing powder powder using the hyper grinder illustrated in FIG. 7.
12 is a view for explaining the pre-processing grinder shown in FIG.
FIG. 13 is a view for explaining the hot air dryer shown in FIG. 1.
14 is a view for explaining the washing machine shown in FIG.
FIG. 15 is a diagram for describing the cutter illustrated in FIG. 1.
FIG. 16 is a flowchart schematically illustrating a powder manufacturing method using the manufacturing plant system shown in FIG. 1.

Description of the present invention is only an embodiment for structural or functional description, the scope of the present invention should not be construed as limited by the embodiments described in the text. That is, since the embodiments may be variously modified and may have various forms, the scope of the present invention should be understood to include equivalents capable of realizing the technical idea.

On the other hand, the meaning of the terms described in the present invention will be understood as follows.

Terms such as "first" and "second" are intended to distinguish one component from another component, and the scope of rights should not be limited by these terms. For example, the first component may be named a second component, and similarly, the second component may also be named a first component.

When a component is referred to as being "connected" to another component, it should be understood that there may be other components in between, although it may be directly connected to the other component. On the other hand, when a component is referred to as being "directly connected" to another component, it should be understood that there is no other component in between. On the other hand, other expressions describing the relationship between the components, such as "between" and "immediately between" or "neighboring to" and "directly neighboring to", should be interpreted as well.

Singular expressions should be understood to include plural expressions unless the context clearly indicates otherwise, and terms such as "comprise" or "have" refer to features, numbers, steps, operations, components, parts, or parts thereof described. It is to be understood that the combination is intended to be present and does not exclude in advance the possibility of the presence or addition of one or more other features or numbers, steps, operations, components, parts or combinations thereof.

In each step, an identification code (e.g., a, b, c, etc.) is used for convenience of description, and the identification code does not describe the order of the steps, and each step clearly indicates a specific order in context. Unless stated otherwise, they may occur out of the order noted. That is, each step may occur in the same order as specified, may be performed substantially simultaneously, or may be performed in the reverse order.

All terms used herein have the same meaning as commonly understood by one of ordinary skill in the art unless otherwise defined. Generally, the terms defined in the dictionary used are to be interpreted as being consistent with the meanings in the context of the related art, and should not be interpreted as having ideal or excessively formal meanings unless clearly defined in the present invention.

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

1 is a view for schematically showing the configuration of a manufacturing plant system according to an embodiment of the present invention.

As shown in the drawings, a manufacturing plant system according to an embodiment of the present invention relates to an organic processed food manufacturing plant system having a complex production facility.

Manufacturing plant system according to an embodiment of the present invention, the far-infrared drying apparatus system 100, the first sorter 210, the washing machine 300, the hot air dryer 400, the second sorter 220, hyper grinder 500 , The cascade magnetic separator 600, a cutter 700, a pretreatment grinder 800, a packing and stacking machine 900 may be provided.

Referring to the drawings in more detail the manufacturing plant system according to an embodiment of the present invention.

As shown in the figure, the far-infrared drying apparatus system 100 is formed to be implemented in a modular form that can be assembled and relocated by installing at various locations according to the type of raw material, the far-infrared drying method using a planar heating element and a cooler Simultaneous implementation of the cooling drying method and the vacuum drying method using a vacuum pump may be performed to pre-treat the water content of the raw material harvested in nature to be less than 7%, the detailed description thereof will be described above with reference to FIGS. See the configuration of FIG. 3.

In addition, the first sorter 210 may be a configuration for removing foreign substances using a wind separator and an LED vision separator in units of 100 kg per raw material that has passed through the far-infrared drying apparatus system 100, and the present invention. In the case of using leafy vegetables such as barley leaf as in the embodiment of the LED vision sorter is preferable, compared to the wind selector, in the case of using bulbs such as carrots and radishes as a material can also be used wind turbines.

In addition, the washer 300, washing the material that needs to be washed out of the material passed through the first sorter 210 at room temperature up to 3 tons in units of 100kg per time, including four minutes, dust, straw, and strings. Foreign matter can be removed cleanly.

In addition, the hot air dryer 400, 5 hours to 6 hours hot air drying at a temperature between 60 degrees Celsius and 70 degrees Celsius using a rectangular box that can accommodate 500kg of the material passed through the washer 300 once. The water content of the raw material can be carried out to 5% or less.

In addition, the second sorter 220 may sort the material passed through the hot air dryer 400 up to 3 tons per day in the same manner as the first sorter.

In addition, the hyper-pulverizer 500, may be provided with at least one grinder for processing at a processing speed of 200kg per one time to put the material passed through the second sorter 220 and then to a predetermined particle size. have.

In addition, the cascade magnetic force selection device 600 is formed to be implemented in a modular form that can be installed and repositioned at various locations according to the type of raw material, the metal foreign matter of powder powder passing through the hyper-crusher 500. Can be processed 100kg per time by cascade continuous movement method.

In addition, as shown in the drawings, the manufacturing plant system according to an embodiment of the present invention, the cutter 700 for cutting to less than 5cm when the size of the material passing through the washing machine 300 exceeds 5cm further. It can be provided. Here, the cutter 700 may be selected and used in various ways at the moment required in the manufacturing process of the manufacturing plant system.

2 is a view for schematically showing a drying system according to an embodiment of the present invention.

As shown in the figure, the drying system according to an embodiment of the present invention, may include a drying housing 110, a control panel 120, a vacuum control unit 130.

More specifically, the drying housing 110 may be provided with three drying chambers 110a for simultaneously drying various kinds of agricultural and aquatic products while maintaining a low temperature of 55 degrees Celsius or less.

Here, the drying chamber (110a), the first drying means 111 for evaporating the water of the material introduced into the drying chamber with water vapor in the air by using the planar heating element (111a) that provides far infrared rays and radiant heat, respectively, 1 The internal temperature of the drying chamber 110a in which the steam of the raw material evaporated by the drying means 111 is not only discharged to the outside of the drying chamber 110a while circulating in the air inside each drying chamber 110a, but at the same time, the heated steam is discharged. In order to maintain a constant without dropping the second drying means 112 that can additionally provide heat in the air inside each drying chamber (110a), and the first drying means 111 and the second drying means ( Compared with 112, it may be provided with a third drying means 113 for quickly discharging the water vapor in the drying chamber (110a).

In addition, the control panel 120 operates the three drying chambers 110a and the first drying means 111 to the third drying means 113 constituting the drying housing 110, and the three drying chambers ( 110a) and the operating states of the first drying means 111 to the third drying means 113 can be displayed.

 Here, the control panel 120 may adjust the temperature of the planar heating element such that the internal temperatures of the three drying chambers 110a are 45 degrees Celsius, 50 degrees Celsius, and 55 degrees Celsius, respectively.

In addition, the vacuum control unit 130 may control the vacuum state inside the three drying chambers.

That is, when raw materials are introduced into the drying chamber 110a, the vacuum pump 113a constituting the third drying means 113 until the internal temperature reaches a predetermined temperature preset by the vacuum control unit 130. Water may be quickly discharged inside the drying chamber 110a, and the internal temperature of the drying chamber 110a may be maintained using the first drying means 111 and the second drying means 112 thereafter.

In addition, as shown in the drawings, the drying system according to an embodiment of the present invention, automatic washing machine 101, horizontal conveyor belt unit 102, grinder 103, sorting conveying conveyor 104, screw conveyor ( 105, a dewatering part 106, and a discharge part 107 may be provided.

Here, the automatic washing machine 101 is configured to perform the washing process at regular intervals when the material is continuously supplied.

In addition, the horizontal conveyor belt unit 102 may serve to horizontally transport in the direction in which the workbench for pretreatment of the material passing through the automatic washer 101 is installed.

In addition, the grinder 103 is configured to grind the material passed through the horizontal conveyor belt 102 to a predetermined size.

In addition, the sorting conveying conveyor 104 may be composed of a plurality of rollers having a predetermined interval so that the material of a small size falls below and the material of a certain size or more to pass through.

In addition, the screw conveyor 105, the front end may be disposed at the end of the sorting transfer conveyor 104, the rear end may be inclined on the upper side of the point where the collecting bag is installed.

In addition, the dehydration unit 106 may remove the moisture of the material before performing the drying process.

In addition, the discharge unit 107 may be configured to discharge the material selected or moved through the sorting transfer conveyor 104 and the screw conveyor 105 to the conveying means.

3 is a view for schematically showing a configuration of a far infrared ray drying apparatus according to an embodiment of the present invention.

Referring to the drawings in more detail the detailed configuration of the far-infrared drying device constituting the drying system according to an embodiment of the present invention.

As shown in the drawings, the triple-hybrid far-infrared drying apparatus according to the embodiment of the present invention relates to a far-infrared drying apparatus for drying the agricultural and marine products harvested in nature at low temperature.

As described above, the far-infrared drying apparatus may include a drying housing 110, a first drying means 111, a second drying means 112, and a third drying means 114.

In more detail, the drying housing 110 may adjust the final moisture content of the drying target in three or more steps in correspondence with the type of raw materials to be put into the drying chamber 110a while controlling the internal temperature of 55 degrees Celsius or less. A plurality of drying chambers may be provided for drying at the same time while maintaining a low temperature.

In addition, the first drying means 111 is installed in each drying chamber 110a constituting the drying housing 110 to be introduced into the drying chamber using a planar heating element 111a that provides far infrared rays and radiant heat. It may serve to evaporate the moisture of the material with water vapor in the air.

In addition, the second drying means 112 not only discharges water vapor of the raw material evaporated by the first drying means 111 to the outside of the drying chamber while circulating in the air inside the respective drying chambers 110a, but also simultaneously heats it. In order to maintain a constant temperature without lowering the internal temperature of the drying chamber 110a from which the steam is discharged, heat may be additionally provided in the air inside each of the drying chambers 110a.

In addition, the third drying means 113, the discharge rate of the water vapor discharged to the outside of the drying chamber (110a) relative to the type of each raw material introduced into the plurality of drying chamber (110a) can be adjusted more than three stages. The water vapor in the drying chamber 110a may be discharged faster than the first drying means 111 and the second drying means 112.

In addition, in the embodiment of the present invention, the first drying means 111, the final moisture content of the drying target corresponding to the material to be put into the drying chamber (110a) is relatively adjusted in three stages, the most The temperature of the planar heating element 111 is controlled so that the internal temperature of the drying chamber 110a is 55 degrees Celsius in the case of requiring a high final moisture content, and the interior of the drying chamber 110a in the case of requiring a relatively low final moisture content. The temperature of the planar heating element 111 is controlled so that the temperature is 45 degrees Celsius, and when the relatively high or low final moisture content is required, the interior temperature of the planar heating element 111 is 50 degrees Celsius. The temperature can be adjusted.

On the other hand, the drying chamber 110a may be formed of three drying chambers 110a that maintain different temperatures of the planar heating elements 111a in response to the final moisture content controlled in the three steps.

In addition, as shown in the figure, the second drying means 112 may be provided with a blowing air fan 112a, a cooler 112b, and an auxiliary heater part 112c.

Here, the blowing air fan 112a may be configured to circulate water vapor in the drying chamber 110a.

In addition, the cooler 112b may cool the water contained in the water vapor circulating in the drying chamber 110a by the blowing air fan 112a and discharge the water to the outside.

In addition, the auxiliary heater 112c may maintain the internal temperature by receiving heat from the driving motor unit constituting the cooler 112b and supplying the inside of the drying chamber to further heat the air inside the drying chamber.

In addition, as shown in the figure, the third drying means 113, a vacuum pump for evacuating the interior of the drying chamber (111a) by sucking the steam condensed through the cooler (112b) and rapidly discharged to the outside. 113a may be provided.

At this time, the third drying means 113, it is preferable to configure a predetermined inlet means so as to introduce the outside air when the internal temperature of the drying chamber (111a) reaches a predetermined temperature.

As such, the far-infrared ray drying apparatus according to the embodiment of the present invention uses a vacuum chamber constituting the third drying means 1113 until the internal temperature of the drying chamber 111a reaches a predetermined temperature. After the inside of the drying chamber 111a is quickly discharged and the internal temperature of the drying chamber 111a reaches a preset temperature, the first drying unit 111 and the second drying unit 112 are used to form the inside of the drying chamber. Temperature can be maintained.

On the other hand, the drying system having a far infrared ray drying apparatus according to an embodiment of the present invention, as shown in the drawing, any of radishes, carrots, parsley, wheat germ, barley green leaves (sprouts), cabbage, fresh vinegar, and kale In the case of drying a single material, a plurality of drying trays 1 are placed in a drying chamber 110a at regular intervals and vertically stacked, and each drying chamber 110a is formed using the drying tray 1. Injected weight to 690kg to 710kg, the set temperature may be 55 degrees Celsius, humidity 6%, operating time may be 18 to 23 hours.

At this time, according to an embodiment of the present invention, the material to be put into the drying chamber 110a may use barley leaf.

4 is a flow chart showing a manufacturing method using a drying system according to an embodiment of the present invention.

Detailed description of the same configuration described above in the drawings will be omitted.

As shown in the drawings, the manufacturing method using a drying system according to an embodiment of the present invention, the automatic washing step using an automatic washing machine (S2100), the horizontal conveying step using a horizontal conveyor belt (S2200), the grinding unit 103 Crushing step (S2300), size selection step (S2400) using a sorting transfer conveyor, out-of-standard product discharge step (S2500) using a screw conveyor, water removal step (S2600) using a dehydrator, drying chamber input using a drying tray A step S2700 and a drying step S2800 using a far infrared ray drying device may be provided.

More specifically, first, the automatic washing step using the automatic washing machine (S2100), using the automatic washing machine 101, any one of radish, carrot, parsley, wheat germ, barley green leaf, cabbage, fresh vinegar, and kale material When continuously supplied may be a step of performing a washing process at regular intervals.

Next, the horizontal conveying step (S2200) using the horizontal conveyor belt, the horizontal conveyor belt unit 102 by using a horizontal conveying step horizontally in the direction in which the work table for pre-processing the material passed through the automatic washing machine 101 is installed Can be.

Next, the grinding step (S2300) using the grinding unit 103, when the material passed through the horizontal conveyor belt unit 102 by using the grinding unit 103 is put into the upper hopper to discharge the crushed to a certain size. It may be a step.

Next, the size selection step using the sorting conveying conveyor (S2400), the sorting conveying conveyor 104 consisting of a plurality of rollers having a predetermined interval so that the material of a small size falls below and the material of a certain size or more passes. It may be a step of sorting the material crushed to a predetermined size by passing through the crushing unit 103 according to the size.

Next, the out-of-standard product discharge step (S2500) using a screw conveyor, the front end is located at the end of the sorting transfer conveyor 104 and the rear end is screw conveyor 105 is disposed inclined on the upper side of the point where the collecting bag is installed. It may be a step of collecting and discharging the material of a specific size or more passed through the sorting transfer conveyor 104 using.

Next, the water removal step (S2600) using the dehydrator, may be a step of collecting the material dropped to the bottom of the sorting transfer conveyor 104 by using the dehydration unit 106 to remove the water.

Next, the drying chamber input step (S2700) using the drying tray may be a step of putting the material passed through the dehydration unit 106 in the step of removing the water in a plurality of drying tray 1 and put it into the drying chamber. have.

Next, in the drying step (S2800) using the far-infrared drying apparatus, a low temperature of 55 degrees Celsius or less using an drying chamber 110a provided with the first to third drying means 111, 112, and 113 described above. It may be a step of drying while maintaining.

FIG. 5 is a diagram schematically showing the casecade magnetic separator shown in FIG. 1, and FIG. 6 is a diagram schematically showing a single magnetic separator constituting the cascade magnetic separator shown in FIG. 5.

As shown in the figure, the cascade magnetic separator device 600 constituting the manufacturing plant system according to an embodiment of the present invention, it can be seen that at least three consecutive magnetic separators 610 are arranged.

In addition, the magnetic separator may include a hopper unit 601, an inclined screw conveyor unit 602, a rectangular housing 603, a cylindrical vibrator 604, and a cylindrical vibrator driving unit 605.

In more detail, the hopper 601 may be configured as a housing having a rectangular shape in the form of a light-low light narrowing so that the material can be injected into the upper side.

In addition, the inclined screw conveyor unit 602 may be configured to transfer the material injected into the hopper unit 601 to the top of the magnetic separators 610, 620, and 630.

In addition, the rectangular housing 603 accommodates the plurality of magnetic rods such that the material conveyed to the uppermost through the inclined screw conveyor 602 can pass through the plurality of magnetic rods while moving in the lower vertical direction. It may be provided with a receiving space, in this case, in the embodiment of the present invention may be 70 magnet rods, the unit of the magnet may be 11,000 gauss.

In addition, the cylindrical vibrating body 604 may be disposed below the rectangular housing 603 and may have a mesh network therein to allow only powder powder of a predetermined size to pass therethrough.

In addition, the cylindrical vibrator drive unit 605 is configured to transmit the vibration to the cylindrical vibrator 604 to discharge the powder of a certain size.

7 is a view schematically showing the configuration of the hyper-crusher shown in Figure 1, Figures 8 to 10 are views for explaining the raw material conveying unit, the cyclone powder collector, the grinder constituting the hyper-crusher, respectively.

As shown in the figure, the hyper-pulverizer 500 constituting the manufacturing plant system according to an embodiment of the present invention, the raw material transfer unit 510, the primary mill 520, the cyclone powder collector 530, the second The car grinder 540, the horizontal housing 550, the hypervibrator 560, and the hyperdrive unit 570 may be provided.

In more detail, the raw material transfer part 510 has a raw material input hopper 511, a transfer screw 512a communicating with a lower portion of the raw material input hopper 511, and the transfer screw 512a to an inner side thereof. It may be provided in a direction and is inclined diagonally to the upper side may be provided with a screw housing pipe 512 for transferring the material to be crushed is injected into the raw material input hopper 511.

Here, referring to FIG. 8, the raw material conveying part 510 includes a material input hopper 511, a transfer screw 512a communicating with a lower portion of the raw material input hopper 511, and the transfer screw 512a inside. It may be provided in the longitudinal direction and is inclined diagonally to the upper side may be provided with a screw housing pipe 512 for transferring the material to be crushed is injected into the raw material input hopper 511.

In addition, the primary crusher 520 is provided with a connecting hopper 521 of a normal light narrowing shape for accommodating the raw material discharged from the end of the screw housing 512 constituting the raw material conveying unit 510, A grinding housing 522 may be provided to grind raw materials introduced through the connection hopper 521.

In addition, the cyclone powder collector 530 extends below the cylindrical body 531 and the cylindrical body 531 in which powder powder pulverized by the primary crusher 520 is air-fed and accommodated using a blower. It may be provided with a plurality of centrifugal hopper 532 and the air discharge portion (533) connected to the dust collecting means.

Here, referring to FIG. 9, the cyclone powder collector 530 is a shock wave on the inner wall surface of the centrifugal hopper 532 on the outer circumferential surface of the centrifugal hopper 532 which extends below the cylindrical body 531. By forming a pulse generating means (532a) for transmitting the powder can be prevented from sticking to the inner surface of the centrifugal hopper (532).

In addition, the second pulverizer 540, the plurality of the cyclone powder collector 530 is arranged in communication with each other to form a plurality so as to further grind the powder mass discharged by the cyclone powder collector 530. Can be.

At this time, referring to Figure 10, in the embodiment of the present invention, the first grinder 520 and the second grinder 540, irregularities of a predetermined size on the cylindrical inner wall surface constituting the housing 521 of the grinder. The protrusion 521a may be configured to be rotatably installed on the center rotation shaft 523 of the cylindrical housing crushing blade 522 disposed in close proximity to the uneven protrusions 521a at a fine interval.

In addition, the horizontal housing 550, the powder powder discharged to the lower side of the plurality of secondary grinder 540 can be horizontally transferred using a single feed pipe.

In addition, the hypervibrator 560 may be provided with a mesh network to allow only the particle size set in advance to pass through the powder powder flowing from the horizontal housing 550.

In addition, the hyper drive unit 570 may be configured to transmit the vibration to the hyper vibrating body 560 to discharge the powder of a predetermined size.

FIG. 11 is a flowchart schematically illustrating a method of preparing powder powder using the hyper grinder illustrated in FIG. 7.

Detailed description of the same configuration of the hyper-crusher described in the above drawings will be omitted.

As shown in the drawings, the powder powder manufacturing method using a hyper crusher of the manufacturing plant system according to an embodiment of the present invention, the material input grinding step (S7100), the material transfer step (S7200), the primary grinding process Step (S7300), air blower feeding step (S7400), cyclone powder collector operation step (S7500), secondary grinding process step (S7600), horizontal transfer step (S7700), and the collecting step (S7800) can be provided.

More specifically, first, the grinding material input step (S7100) may be a step in which a large amount of material is introduced through the input hopper 511 of the raw material transfer unit 510.

Next, the grinding material transfer step (S7200), the screw housing tube 512 of the raw material transfer unit 510 is installed in the longitudinal direction in which the transfer screw 512a communicating with the lower portion of the input hopper 511. Through the input hopper 511 may be a step of conveying the material to be crushed.

Next, the primary grinding process step (S7300), the material to be pulverized discharged from the end of the screw housing 512 constituting the raw material transfer unit 510 through the connection hopper 501 of the ordinary light strait shape inflow When the first surface is formed with a convex convex protrusion (521a) on a cylindrical inner wall surface and is disposed rotatably on the central axis 523, the crushing rotary blade 522 is disposed in close proximity to the convex convex protrusion (521a). Primary grinding may be performed through the tea grinder 510.

Next, the air blower feeding step (S7400), the powder powder pulverized by the primary crusher 510 is air-feeded using a blow to form a plurality of cylindrical bodies constituting a plurality of cyclone powder collector 530 ( 531).

Next, the cyclone powder collector operation step (S7500), by operating the centrifugal hopper extending to the lower side of the cylindrical body to constitute the plurality of cyclone powder collector 531 to discharge the powder mass It may be a step.

Next, the secondary crushing process step (S7600), by the cyclone powder collector 531 through a plurality of secondary grinder 540 which is arranged in communication with each of the plurality of cyclone powder collector 531, respectively. The pulverized powder mass may be further pulverized.

Next, the horizontal transfer step (S7700) may be a step of horizontally conveying the powder powder discharged to the lower side of the plurality of secondary grinder 540 through a horizontal housing 550 consisting of a single transport pipe. have.

Next, in the collecting step (S7800), the powder is introduced from the horizontal housing 550 using a vibrating body 560 which is provided with a mesh network and vibrated by the driving unit 560 in advance. It may be a step of collecting the powder of the set particle size.

In addition, the step of discharging the powder mass by operating the centrifugal hopper extending to the lower side of the cylindrical body to configure the plurality of cyclone powder collector, centrifugal hopper to separate and collect the pulverized powder by applying a centrifugal force In the vortex phenomenon occurs, the powder powder accommodated in the cylindrical body 531 is collected in a lump and rapidly rotates and the air introduced together with the powder powder inside the cylindrical body 531 is an air discharge unit connected to the dust collecting means ( 533), and when the shock wave is transmitted to the inner wall surface of the centrifugal hopper 532 by using the pulse generating means 532a formed on the outer circumferential surface of the centrifugal hopper 532, the inner surface of the centrifugal hopper 532. It may include a step of falling powder powder stuck to.

On the other hand, according to an embodiment of the present invention, when the material using the hyper grinder is a leaf vegetable, such as a barley green leaf, the input hopper of the raw material transport unit to facilitate the primary grinding process in the first grinder 520 It may further include a pretreatment milling process by the pretreatment mill 800 to crush the barley leaves to a suitable size before the material is introduced through.

12 is a view for explaining the pre-processing grinder.

As shown in the drawing, the pretreatment grinder according to the embodiment of the present invention includes a loading unit 810 for loading pretreatment material (barley leaf), and a conveyor with an upper portion of the loading unit 810 open. The pretreatment transfer unit 820 having a non-slip partition wall at regular intervals so as not to slip the material evenly inclined through the pretreatment grinding unit 830 for accommodating and conveying the material transferred through the pretreatment transfer unit 820, the pretreatment grinding unit And a pretreatment orthogonal transfer unit 840 for transferring the material crushed and separated through the 830 to be inclined in a screw conveyor manner with respect to the orthogonal direction of the pretreatment transfer unit, and a pretreatment driving unit 850 for providing a driving force of the orthogonal transfer unit. Can be.

In this case, the pretreatment grinding step before the first grinder 520 performs a medium grinding step of the particle size of the barley lining leaf is 1 cm or less, and the primary grinding step of the first grinder 520 is the particle size. A general grinding process of 1 mm or less, and the secondary grinding process by the second secondary mill 540 after the first mill 520 is to perform a fine grinding process having a particle size of 10 μm or less Can be.

FIG. 13 is a view for explaining the hot air dryer shown in FIG. 1.

Hot air dryer 400 according to an embodiment of the present invention, by using a rectangular box that can accommodate 500kg per material, hot air drying for 5 hours to 6 hours at a temperature between 60 degrees to 70 degrees Celsius The water content of can be made 5% or less.

Here, as shown in the figure, the hot air dryer 400 may be provided with a hot air drying housing 410, a heat generating device 420, a hot air drying control box 430.

In more detail, the hot air drying housing 410 is formed in a box shape having a length of 160 cm, 300 cm, and 90 cm in length and length, respectively, and the inside and the outside of the wall are formed of a material of material and 5 cm inside. Built-in thick metal wall for insulation, drying tray may be mounted inside the box. In addition, a mesh cloth 401 may be further provided to easily contain and discharge the material.

In addition, the heat generating device 420, the length of the vertical length of the hot air drying housing 410 is arranged in the length of 96cm, 122cm, 122cm, respectively, and the hot air drying housing 410 by heating It can generate heat.

In addition, the hot air drying control box 430 may control the heat generating device 420 while controlling the temperature of the hot air drying housing 410 while displaying the temperature of the hot air drying housing 410.

On the other hand, according to the present invention, when the material is grains such as beans and sesame, it is preferable to use a stirrer instead of a hot air dryer.

14 is a view for explaining the washing machine shown in Figure 1, Figure 15 is a view for explaining the cutter shown in FIG.

Washing machine 300 according to the embodiment of the present invention, by washing the material that needs to be washed at room temperature up to 3 tons in units of 100kg per time to remove the foreign matter, including dust, dust, straw, and strings. .

As shown in the figure, it is divided into an automatic washer and a bulbous washer, the automatic washer mainly washes vegetables and bulbous washer can wash bulbs such as radishes and carrots.

Here, the automatic washing machine 310 may include a washing water supply means 311, a washing housing 312, a washing material catching network 313, a washing stand control unit 314, and the bulb washing machine 322 is a washing housing. 321 and the washing control panel 322 may be provided.

In addition, the embodiment of the present invention may further include a cutter 700 for cutting to less than 5cm when the size of the material passed through the washing machine 300 exceeds 5cm, wherein the cutter 700 is In the manufacturing process of the manufacturing plant system, it can be variously selected and used at the moment required.

The cutting machine 700 may include a material input part 710 for inputting material, a support housing 720 for supporting the cutter, and a cutting part 730 having a cutting blade.

FIG. 16 is a flowchart schematically illustrating a powder manufacturing method using the manufacturing plant system shown in FIG. 1.

As shown in the drawings, the powder manufacturing method using the manufacturing plant system according to the present invention, cutting the raw material (S1000), pre-treatment drying step (S2000), pre-treatment screening step (S3000), washing step (S4000), It may include a hot air drying step (S5000), after drying the sorting step (S6000), the crushing process performing step (S7000), metal foreign matter removal step (S8000), and packaging and loading step (S9000).

In more detail, first, the step of cutting the raw material (S1000) may be a step of cutting the barley vine leaf harvested in nature using a cutter to have a length of 5 cm or less.

Next, the pre-treatment drying step (S2000), using a far-infrared drying apparatus system 100, low temperature of 55 degrees Celsius or less so that the moisture content of the barley lining leaves cut to a size of 5 cm or less can be 7% or less It may be a step of performing a pre-treatment drying process in a state, a detailed description thereof will be referred to Figures 2 to 4.

Next, the pre-treatment screening step (S3000), the step of removing the foreign matter in a unit of 100kg once from the material passed through the far-infrared drying apparatus system 100 by using a first vision sorter 210 installed with a plurality of LED lights. Can be.

Next, the washing step (S4000), using a washing machine 300 to wash the material that needs to be washed out of the material passed through the pre-treatment screening step at room temperature up to 3 tons per day in 100kg units per quarter, dirt, It may be a step of removing the foreign matter including the straw and the string.

Next, the hot air drying step (S5000), the material passed through the washer 300 using a hot air dryer 400 having a rectangular box capable of accommodating 500 kg per one time between 60 to 70 degrees Celsius Drying at a temperature of 5 hours to 6 hours may be a step of performing a hot air drying process until the moisture content is 5% or less.

Next, the drying and sorting step (S6000) may be a step of sorting the material passed through the hot air dryer 400 up to 3 tons per day using a second sorter 220 having a plurality of LED lights. .

Next, in the grinding process performing step (S7000), using a hyper grinder 500, the material passed through the second sorter 220 is ground at a processing speed of 200 kg per one time so as to be a powder having a predetermined particle size. The process may be performed.

Next, the metal foreign matter removing step (S8000), the hyper-crusher by using the cascade magnetic screening device 600 for multi-selecting in a manner of successively passing through a plurality of magnetic screening machines (610, 620, 630) that can process 100kg per one time It may be a step of performing a process for removing the foreign matter of the barley leaf powder powder passed through 500.

Next, the packaging and loading step (S9000), may be provided with a step (S9000) for packing and loading the barley leaf powder in 20kg units.

On the other hand, according to an embodiment of the present invention, in the case of producing a barley lean leaf powder, the barley vine leaf after the step of performing the pre-treatment drying step of the low temperature state below 55 degrees Celsius packed in 20kg units until loading 24 Can be processed in time.

As described above, the present invention, in the construction of a far-infrared drying apparatus by applying a triple hybrid drying method that implements a cooling drying method and a vacuum drying method at the same time, while preserving the inherent nutrients of the raw materials, the loss expected in the drying process at the source It is effective to provide an eco-friendly agricultural and aquatic product drying system equipped with a triple-hybrid far-infrared drying device that can not only block but also minimize moisture content in a short time, and a method of manufacturing organic aquatic products using the same.

The present invention has been described in detail so far, but the embodiments mentioned in the process are only illustrative and are not intended to be limiting, and the present invention is provided by the following claims and the technical spirit and field of the present invention. Within the scope not departing from the scope of the present invention, changes in the components that can be coped evenly will fall within the scope of the present invention.

1: drying group
100: far infrared drying system
101: automatic washing machine
102: horizontal conveyor belt
103: grinder
104: Transfer conveyor for sorting
105: screw conveyor
106: dehydration unit
110 (110a): Drying Housing (Drying Room)
111 (111a): first drying means (planar heating element)
112: second drying means
112a: Blowing air fan
112b: cooler
112c: auxiliary heater
113: third drying means
113a: vacuum pump
120: control panel
130: vacuum control unit
210: first sorter
220: second sorter
300: Washer
400: hot air dryer
410 hot air drying housing
420: heat generating device
430: hot air drying control box
500: Hyper Crusher
510: raw material transfer unit
520: the first grinder
530: Cyclone Powder Collector
531: cylindrical body
532 centrifugal hopper
532a: pulse generating means
540: second mill
550: horizontal housing
560 hypervibration
570: hyper drive unit
600: magnetic separator
601 hopper section
602: inclined screw conveyor
603: square housing
604 cylindrical cylindrical body
605: drive unit
700: Cutter
800: pretreatment grinder
900: Packers and Stackers

Claims (13)

In organic processed food manufacturing plant system with complex production facilities,
It is formed to be assembled in modular form so that it can be installed and relocated at various positions according to the kinds of raw materials.At the same time, it implements a far-infrared drying method using a planar heating element, a cooling drying method using a cooler, and a vacuum drying method using a vacuum pump. A triple hybrid type far-infrared drying apparatus system 100 capable of performing a pretreatment process so that the moisture content of raw materials harvested from nature is 7% or less;
A first sorter 210 for removing foreign substances by using a wind separator and an LED vision separator in units of 100 kg per raw material having passed through the far infrared drying apparatus system 100;
Washing machine 300 to clean the foreign matter including four minutes, dirt, straw, and strings by washing at room temperature up to 3 tons per 100kg units of the material that needs to be washed out of the material passed through the first sorter 210 at a time ;
5% to 6 hours of hot air drying at a temperature between 60 and 70 degrees Celsius using a rectangular box that can accommodate 500 kg of the material that has passed through the washer 300 at a time of 5% moisture content of the raw material Hot air dryer 400 to be below;
A second sorter 220 for sorting the material that has passed through the hot air dryer 400 up to 3 tons per day in the same manner as the first sorter;
A hyper grinder 500 including at least one grinder for collecting the material passing through the second sorter 220 and feeding it into the upper hopper and then treating the material at a processing speed of 200 kg per one time to a predetermined particle size; And
It is formed to be assembled in a modular form so that it can be installed and relocated at various locations according to the type of raw materials, and 100 kg of powdered metal foreign matter that has passed through the hyper grinder 500 can be processed by cascade continuous movement method at a time. Cascade magnetic screening device 600 that can; eco-friendly agricultural and aquatic products organic food manufacturing plant system with a composite production equipment characterized in that it comprises a
The method according to claim 1, wherein the organic food manufacturing plant system,
Eco-friendly agricultural and aquatic products manufacturing plant system with a complex production facility characterized in that it further comprises a cutter 700 for cutting to less than 5cm when the size of the material passed through the washing machine 300cm more than 5cm

The method according to claim 2, Cascade magnetic separator device 600 constituting the organic processed food manufacturing plant system,
A hopper portion 601 having a quadrangular shape in the form of a light beam narrowing so that a material can be introduced into the upper side;
An inclined screw conveyor unit 602 for transferring the material introduced into the hopper unit 601 to the uppermost end of the magnetic force selection device 600;
Square housing 603 having a receiving space for accommodating the plurality of magnetic rods so that the material conveyed to the uppermost through the inclined screw conveyor 602 can pass through the plurality of magnetic rods while moving in the lower vertical direction );
A cylindrical vibrator 604 disposed under the rectangular housing 603 and having a mesh network therein for passing only powder powder of a predetermined size; And
Complex production, characterized in that the magnetic force selector 610 having at least three consecutively disposed; the drive unit 605 for transmitting the vibration to the cylindrical vibrating body 604 to discharge the powder of a predetermined size Eco-Friendly Agricultural Products Organic Processed Food Manufacturing Plant System
The method of claim 3, wherein the hot air dryer 400 constituting the organic processed food manufacturing plant system,
It is formed in the shape of a box having a length of 160cm, 300cm, and 90cm in height and width, and the inside and the outside of the wall are formed of a material of heat, and a 5cm thick thermal insulation metal wall is built in the inside, and dried inside the box. Hot air drying housing 410 is installed;
A heat generating device 420 having a length of horizontal length and height of 96 cm, 122 cm, and 122 cm at one end in a longitudinal direction of the hot air drying housing 410 to generate heat by heating the hot air drying housing 410; And
And a hot air drying control box 430 for controlling the temperature of the hot air drying housing 410 by controlling the heat generating device 420 while displaying the temperature of the hot air drying housing 410. Eco-Friendly Agricultural Products Organic Processed Food Manufacturing Plant System

The method according to claim 3, wherein the organic food manufacturing plant system,
Eco-friendly agricultural and aquatic products organic food manufacturing plant system equipped with a composite production equipment, characterized in that the use of a stirrer instead of the hot air dryer when the material passed through the washing machine is grains such as beans and sesame seeds
The method according to claim 5, Hyper grinder 500 constituting the organic food manufacturing plant system,
The raw material input hopper 511, the transfer screw 512a communicating with the lower portion of the raw material input hopper 511, and the transfer screw 512a is installed in the longitudinal direction inwardly and inclined diagonally above the raw material input hopper A raw material transfer part 510 having a screw housing tube 512 for transferring the material to be crushed to be put into the 511;
It is provided with a connecting hopper 521 of the upper and lower narrow shape for accommodating the raw material discharged from the end of the screw housing 512 constituting the raw material transfer unit 510, and pulverizes the raw material flowing through the connecting hopper 521 A first mill 520 having a milling housing 522 to be formed;
The centrifugal hopper 532 and the dust collecting means which are formed by extending the lower portion of the cylindrical body 531 and the cylindrical body 531 that is air-pneumatically accommodated by the blower is blown by the primary crusher 520 A plurality of cyclone powder collectors 530 having air discharge parts 533 connected to the plurality of cyclone powder collectors 530;
A plurality of secondary grinders 540 disposed to be in communication with each of the plurality of cyclone powder collectors 530 to further grind the powder mass discharged by the cyclone powder collectors 530;
A horizontal housing part 550 for horizontally transferring powder powder discharged to the plurality of secondary grinders 540 under a single feed pipe;
A hypervibrator 560 having a mesh network therein for allowing only a predetermined particle size to pass through the powder powder introduced from the horizontal housing 550; And
Eco-friendly agricultural and aquatic products organic food manufacturing plant system with a complex production facility, characterized in that it comprises a; hyper drive unit 570 for transmitting the vibration to the vibrating body 560 to discharge a powder of a certain size
The cyclone powder collector 530 of the hyper grinder constituting the organic processed food manufacturing plant system,
On the outer circumferential surface of the centrifugal hopper 532 extending downward of the cylindrical body 531, a pulse generating means 532a for transmitting shock waves to the inner wall surface of the centrifugal hopper 532 is formed so that the powder is centrifugal hopper. Eco-friendly agricultural and aquatic products organic food manufacturing plant system equipped with a composite production equipment, characterized in that to prevent sticking to the inner surface of (532)
The method according to claim 7, wherein the first grinder 520 and the second grinder 540 of the hyper grinder constituting the organic processed food manufacturing plant system,
The crushing rotary blade 522 is formed in the cylindrical inner wall surface constituting the housing 521 of the crusher, and the crushing rotary blade 522 is disposed in close proximity to the uneven protrusion 521a at a fine interval. Eco-friendly agricultural and aquatic products organic food manufacturing plant system with a composite production equipment, characterized in that rotatably installed on the rotating shaft 523
The method of claim 8, wherein the triple-infrared far infrared drying device system constituting the organic food processing manufacturing plant system,
First drying means 111 for evaporating the moisture of the material introduced into the drying chamber with water vapor in the air by using the planar heating element 111a providing far infrared rays and radiant heat, and the evaporated by the first drying means 111. In addition to circulating the steam of the raw material in the air inside the respective drying chamber (110a) to the outside of the drying chamber (110a), at the same time additionally to maintain a constant temperature without lowering the temperature inside the drying chamber (110a) from which the heated steam is discharged Compared with the second drying means 112 that can provide heat to the air inside the respective drying chambers 110a, and the first drying means 111 and the second drying means 112, the drying chamber 110a. And a third drying means 113 for quickly discharging the water vapor therein, and simultaneously drying various kinds of agricultural and aquatic products while keeping the internal temperature at a low temperature of 55 degrees Celsius or less. A drying housing 110 having three drying chambers 110a for growing; And
The three drying chambers 110a and the first drying means 111 to the third drying means 113 constituting the drying housing 110 are operated to operate the three drying chambers 110a and the first drying means 111. And a control panel 120 for displaying an operating state of the third to third drying means 113 and a vacuum control unit 130 for controlling the three vacuum states inside the drying chambers.
The control panel 120,
The temperature of the planar heating element can be adjusted so that the internal temperatures of the three drying chambers 110a are 45 degrees Celsius, 50 degrees Celsius, and 55 degrees Celsius, respectively.
When raw materials are introduced into the drying chamber 110a, the vacuum control unit 130 uses the vacuum pump 113a constituting the third drying means 113 until the internal temperature reaches a predetermined temperature. Quickly drain the moisture inside the drying chamber (110a),
The internal temperature of the drying chamber 110a is maintained by using the first drying means 111 and the second drying means 112.
The second drying means may include an air blower fan 112a for circulating water vapor in the drying chamber 110a; A cooler (112b) which cools the water contained in the water vapor circulating in the drying chamber (110a) by the blowing air fan (112a) and discharges it to the outside; And an auxiliary heater part 112c capable of maintaining the internal temperature by receiving heat from the driving motor part constituting the cooler 112b and supplying the inside of the drying room 110a to further heat the air inside the drying room 110a. And
The third drying means 113, the vacuum pump 113a for evacuating the interior of the drying chamber (110a) by sucking the steam condensed through the cooler (112b) and rapidly discharged to the outside; Eco-friendly agricultural and aquatic products organic food manufacturing plant system equipped with a complex production facility characterized in that when the internal temperature of the drying chamber (110a) reaches a predetermined temperature set in advance
delete delete In the powder flour manufacturing method using a hyper grinder of an eco-friendly agricultural and marine products organic processed food manufacturing plant system,
Inputting a large amount of material through the input hopper 511 of the raw material transfer unit 510 (S7100);
The material to be crushed into the hopper 511 through the screw housing tube 512 of the raw material transfer part 510 is installed in the longitudinal direction in the conveying screw 512a is communicated with the lower portion of the hopper 511. Is transferred (S7200);
When the material to be pulverized discharged from the end of the screw housing 512 constituting the raw material transfer part 510 through the connection hopper 501 of the ordinary light strait shape is introduced into the cylindrical inner wall surface of the irregular protrusion 521a Forming and crushing the primary blade through the first grinder 510 rotatably installed on the central axis 523, the crushing rotary blade 522 is disposed in close proximity to the uneven protrusion (521a) (S7300) );
Powder powder pulverized by the primary crusher 510 is air-feeded using a blow and accommodated in a plurality of cylindrical bodies 531 constituting a plurality of cyclone powder collectors 530 (S7400);
Discharging the powder mass by operating the centrifugal hopper 532 extending downward of the cylindrical body to configure the plurality of cyclone powder collectors 531 (S7500);
Further pulverizing and pulverizing the powder mass discharged by the cyclone powder collector 531 through a plurality of secondary grinders 540 respectively disposed in communication with the lower side of the plurality of cyclone powder collectors 531 ( S7600);
Step (S7700) to horizontally convey the powder powder discharged to the lower side of the plurality of secondary grinder 540 through a horizontal housing 550 consisting of a single transport pipe; And
Steps to collect the powder powder of a predetermined particle size by selecting the powder powder flowing from the horizontal housing 550 using a vibrating body 560 having a mesh network therein and vibrating by the driving unit 560. (S7800); powder powder manufacturing method using a hyper crusher comprising
The method of claim 12, wherein the step of discharging the powder mass by operating the centrifugal hopper extending to the lower side of the cylindrical body to constitute the plurality of cyclone powder collector,
In the centrifugal hopper 532 which separates and collects the pulverized powder by centrifugal force, vortex phenomena occur, and the powder powder contained in the cylindrical body 531 is collected into a lump, which quickly rotates and falls into the inside of the cylindrical body 531. The air introduced with the powder is discharged through the air discharge unit 533 connected to the dust collecting means; And
When the shock wave is transmitted to the inner wall surface of the centrifugal hopper 532 by using the pulse generating means 532a formed on the outer circumferential surface of the centrifugal hopper 532, powder powder stuck to the inner surface of the centrifugal hopper 532 falls. Powder flour manufacturing method using a hyper crusher comprising a;

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