WO2017188461A1 - Device for manufacturing organic fertilizer - Google Patents

Device for manufacturing organic fertilizer Download PDF

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Publication number
WO2017188461A1
WO2017188461A1 PCT/KR2016/004279 KR2016004279W WO2017188461A1 WO 2017188461 A1 WO2017188461 A1 WO 2017188461A1 KR 2016004279 W KR2016004279 W KR 2016004279W WO 2017188461 A1 WO2017188461 A1 WO 2017188461A1
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WIPO (PCT)
Prior art keywords
raw material
path
material input
drying
unit
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PCT/KR2016/004279
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French (fr)
Korean (ko)
Inventor
김우현
김상옥
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김우현
김상옥
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Application filed by 김우현, 김상옥 filed Critical 김우현
Priority to PCT/KR2016/004279 priority Critical patent/WO2017188461A1/en
Publication of WO2017188461A1 publication Critical patent/WO2017188461A1/en

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    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F9/00Fertilisers from household or town refuse
    • C05F9/02Apparatus for the manufacture
    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05FORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/90Apparatus therefor
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Definitions

  • the present invention relates to an apparatus for producing organic fertilizer, and more particularly, to an apparatus for producing organic fertilizer for recycling of organic waste resources.
  • wastewater generated from organic wastes such as food waste sludge, animal sludge, sewage sludge, and biogas plant sludge has also been mostly dumped in the ocean, causing pollution of fisheries resources and wasteland of fisheries. Polluting rivers threatens drinking water sources.
  • the reduction treatment technology is basically a process that cannot remove harmful substances, and it is a technique that minimizes waste by simply removing moisture from organic waste having a moisture content of 85% or more.
  • this method is a technique for producing compost and a technique for making a feed by mixing some of the general feed and organic sludge.
  • organic fertilizer (compost) production by dehydration, washing, and fermentation causes secondary pollution with leachate and wastewater during the treatment process, which damages the natural environment around the treatment plant, and harmful substances remain in the produced compost. After the application, secondary soil pollution occurs, and due to the excessive investment of facilities, there is no economic feasibility.
  • incineration technology of the existing method of treating organic waste is a deadly poison, such as dioxin when incinerated, threatening human life. Due to the excessive investment of facilities and disposal costs, the incineration of organic wastes has been stopped, but there is no special treatment method, and the situation is being sought to find an alternative.
  • organic wastes that are disposed of as garbage are separated and collected in significant quantities, but some are incinerated, landfilled and dumped at sea.
  • the characteristics of organic sludge wastes vary from region to region, and the specificity of their contents makes it difficult to recycle resources. Some of them are dehydrated and washed and then fermented and then composted. There is a situation.
  • An object of the present invention is to provide an apparatus for producing organic fertilizer for the recycling of organic waste resources.
  • the present invention in order to solve the above-mentioned problems raw material input unit; A raw material mixing part for mixing the raw materials introduced into the raw material input part; And a mixed raw material drying unit for drying the raw materials mixed in the raw material mixing unit, wherein the mixed raw material drying unit comprises: a chamber unit connected to the raw material mixing unit; It provides an organic fertilizer manufacturing apparatus including an internal raw material manufacturing apparatus including an internal drying path located inside the chamber portion and an external drying path located outside the mixed raw material drying unit.
  • the present invention includes a heating means located in the chamber portion, wherein the heating means is located in the lower portion of the chamber portion, the lower heating means for heating the inside of the chamber portion and the side of the chamber portion, Provided is an apparatus for producing organic fertilizer comprising side heating means for heating the inside of the chamber portion.
  • the raw material input unit includes a first raw material input unit and a second raw material input unit, the raw material input to the first raw material input unit is the main raw material, the raw material input to the second raw material input unit is a water content regulator An apparatus for producing phosphorus organic fertilizer is provided.
  • the raw material input unit includes a first raw material input unit and the second raw material input unit, the raw material introduced into the first raw material input unit is a water-conditioning regulator, the raw material introduced into the second raw material input unit is the main raw material
  • An apparatus for producing phosphorus organic fertilizer is provided.
  • the present invention may further include a first path raw material input part and a second path raw material input part separated from the first path raw material input part, and the first path raw material input part may include a first path first raw material input part. And a first path second raw material input part, wherein the second path raw material input part includes a second path first raw material input part and a second path second raw material input part, and enters the first path first raw material input part.
  • the raw material to be added is a secondary raw material
  • the raw material to be injected into the second raw material input part of the first path is a main raw material
  • the raw material to be injected into the first raw material input part of the second path is a water content regulator
  • the second raw material input part of the second path is a water content regulator
  • the raw material mixing unit, the first raw material mixing unit connected to the first path raw material input unit and the second raw material mixing unit is separated from the first raw material mixing unit, the second raw material mixing unit Including wealth
  • the chamber part includes a first drying path connected to the first raw material mixing part and a second drying path connected to the second raw material mixing part, wherein the internal drying path includes a first internal drying path and a second internal drying. And an external drying path, wherein the external drying path includes a first external drying path and a second external drying path, and the first drying path includes: the first internal drying path and the outside of the chamber part located in the chamber part.
  • the first drying path includes a first external drying path, wherein the second drying path is organic, including the second internal drying path located inside the chamber portion and the second external drying path located outside the chamber portion.
  • a fertilizer manufacturing apparatus is provided.
  • the first drying path further comprises a water content regulator discharge part connected to the first external drying path
  • the second drying path further includes a mixed raw material discharge part connected to the second external drying path
  • It provides an organic fertilizer manufacturing apparatus further comprising a water-containing regulator moving path for injecting the water-containing regulator discharged through the water-containing regulator discharge unit to the second raw material first feeder.
  • the present invention evenly contains nutrients necessary for the growth of crops, trees and crops, it is possible to produce a high-quality organic fertilizer of environmentally friendly by a relatively simple treatment method.
  • the present invention can produce an organic fertilizer that does not cause the problem of soil and water pollution due to the effect of recycling organic waste and leachate of secondary pollutants generated after landfill.
  • 1 is a flow chart showing a method for producing an organic fertilizer according to the present invention.
  • Figure 2 is a flow chart for explaining the step of producing a main raw material by treating the organic waste according to the present invention.
  • FIG 3 is a schematic view for explaining the organic waste treatment apparatus according to the present invention
  • Figure 4 is a schematic view for explaining the specific gravity separation unit in the organic waste treatment apparatus according to the present invention.
  • FIG. 5 is a flow chart for explaining the steps of producing a water modifier according to the present invention.
  • FIG. 6 is a flow chart for explaining the step of producing a mixed raw material according to the present invention.
  • FIG. 7 is a schematic perspective view showing a mixed raw material manufacturing apparatus according to a first embodiment of the present invention
  • Figure 8 is a schematic cross-sectional view showing a mixed raw material manufacturing apparatus according to a first embodiment of the present invention.
  • FIG. 9 is a schematic perspective view showing a mixed raw material manufacturing apparatus according to a second embodiment of the present invention.
  • FIG. 10 is a schematic perspective view showing a fermentation / maturation apparatus of a mixed raw material according to the present invention
  • FIG. 11 is a schematic sectional view showing another mixed raw material according to the present invention.
  • first, second, etc. are used to describe various components, these components are of course not limited by these terms. These terms are only used to distinguish one component from another. Therefore, of course, the first component mentioned below may be a second component within the technical spirit of the present invention.
  • spatially relative terms below “, “ beneath “, “ lower”, “ above “, “ upper” It can be used to easily describe a component's correlation with other components. Spatially relative terms are to be understood as including terms in different directions of components in use or operation in addition to the directions shown in the figures. For example, when flipping a component shown in the drawing, a component described as “below” or “beneath” of another component may be placed “above” the other component. Can be. Thus, the exemplary term “below” can encompass both an orientation of above and below. The components can be oriented in other directions as well, so that spatially relative terms can be interpreted according to the orientation.
  • 1 is a flow chart showing a method for producing an organic fertilizer according to the present invention.
  • the manufacturing method of the organic fertilizer according to the present invention includes the step of producing a main raw material by treating the organic waste (S110).
  • the organic waste means food waste sludge, condensed sludge, sewage sludge, biogas plant sludge and the like, but the present invention does not limit the type of the organic waste.
  • the method for producing an organic fertilizer according to the present invention includes the step of mixing the main raw material and a separate auxiliary raw material to prepare a water-conditioning agent (S120).
  • the secondary raw material may be masato, ocher, silt, raw soil, etc., but the type of the secondary raw material is not limited in the present invention.
  • the step of preparing the water-adjusting agent by mixing the main raw material and the additional auxiliary material will be described later.
  • the method for producing an organic fertilizer according to the present invention includes the step of preparing a mixed raw material by mixing the main raw material and the water-containing regulator (S130).
  • step S110 by mixing the main raw material prepared in step S110 and the water content regulator prepared in step S120, it is possible to produce a mixed raw material according to the present invention.
  • the step of preparing the mixed raw material by mixing the main raw material and the water-containing regulator will be described later.
  • the method for producing an organic fertilizer according to the present invention includes the step of producing an organic fertilizer by fermenting and ripening the mixed raw material (S140).
  • Fermenting and aging the mixed raw material may be a step of fermenting and ripening in a subsequent bath for 3 to 10 days at a temperature of 0 to 70 °C, except that, depending on the amount of the mixed raw material, the aging temperature and the aging The time can be adjusted appropriately, and therefore, the present invention does not limit the aging temperature condition and the aging time condition.
  • the aerobic microorganisms are Streptomyces (Streptomyces), Thermoactinomycetes (Thermoactinomycetes), Bacillus cereus (Bbacillus cereus), Arcanobacterium he Arcanobacterium haemolyticum, Lactobacillus delbrueckiilactis, Providencia stuartii, Staphylococcus kloosi, Vibrio haemolyticus at Vibrio haemolyticus
  • One or more microorganisms selected may be used, but the present invention does not limit the type of aerobic microorganisms.
  • the water content of the organic fertilizer may be 10% to 40%, preferably 15% to 30%, the water content of the organic fertilizer can be controlled by the mixing of the above-described main raw material and the moisture control agent.
  • Figure 2 is a flow chart for explaining the step of producing a main raw material by treating the organic waste according to the present invention.
  • the step of preparing the main raw material by treating the organic waste in accordance with the present invention comprising the step of removing the weight by putting the organic waste in the washing tank (S111).
  • Injecting the organic waste into the washing tank corresponds to a process for screening the organic material from the organic waste by a dipping method.
  • the dipping method in the present invention is to put organic waste into a washing tank, such as a container or a water tank containing a certain amount of water, by removing the floating matter or weight contained in the organic waste by the specific gravity difference, the organic material This is to sort out the bay.
  • a washing tank such as a container or a water tank containing a certain amount of water
  • a washing tank such as a container or a water tank containing water, iron products, glass products, etc., which are heavy materials, are precipitated in the lower portion of the container or the water tank, and vinyl products, Floats such as plastic products may be floated.
  • step S111 by the above-described dipping method, it is possible to remove the weight precipitated in the lower portion of the washing tank such as a container or a water tank.
  • removing the weight can be removed by a mechanical device or a manpower.
  • the organic waste, as well as the organic material may include a heavy material and suspended matter as described above, through the step S111, the heavy material can be removed.
  • the organic waste from which the weight is removed may include organic material and suspended solids.
  • the organic waste including the organic material and the suspended matter may be crushed through a separate crushing device, thereby minimizing the size of the organic material, and also crushing the suspended matter, thereby minimizing the size of the suspended matter.
  • the pulverized suspended matter is more easily floated on the upper portion of the storage tank such as a container or a water tank containing water.
  • the pulverized suspended matter is more easily floated on the upper portion of the storage tank such as a container or a water tank containing water, due to the specific gravity difference, the crushed suspended matter floated It can be easily removed.
  • the removal of the suspended matter can be removed by a mechanical device or attraction.
  • the crushed organic waste can be fermented and aged more easily in the above-described fermentation and ripening step.
  • aerobic microorganisms may be used in the present invention, and the aerobic microorganisms may include Streptomyces, Thermoactinomycetes, Bacillus cereus, and Arcanobacte.
  • Arcanobacterium haemolyticum, Lactobacillus delbrueckiilactis, Providencia stuartii, Staphylococcus kloosi, Vibrio haemolyticus One or more microorganisms selected from) may be used, but the present invention does not limit the type of aerobic microorganisms.
  • the first main material processing the preliminary main raw material includes a step (S115).
  • the first chemical treatment may use an inorganic reactant, and the inorganic reactant may be lime (CaO).
  • the lime is a limestone obtained by burning limestone such as ash, chalk, and shells, and limestone obtained by pouring water into quicklime, and also means white basic powder obtained by adding water to calcium oxide.
  • the step of treating the first drug is to remove the salt contained in the preliminary main material, when the first drug treatment on the preliminary main raw material, the first drug and the preliminary main raw material react, so that a certain precipitate is generated. do.
  • the present invention preferably further comprises the step of removing the precipitate generated by the first drug treatment, after the first drug treatment of the preliminary main raw material.
  • Removing the generated precipitate can be removed by a mechanical device or attraction.
  • the inorganic reactant may include 2 to 5 parts by weight relative to 100 parts by weight of the preliminary main raw material, due to the components of the inorganic reactant, the preliminary main raw material is exothermic reaction, the odor is removed and the moisture content
  • the salt contained in the preliminary main raw material can be removed.
  • the organic fertilizer When the organic fertilizer is manufactured in the state containing such a salt, and the prepared organic fertilizer is used in the soil, the salt is absorbed into the soil and accumulated continuously, resulting in serious soil contamination.
  • the salt contained in the preliminary main raw material can be removed by the first chemical treatment.
  • a second drug treatment of the first drug-treated preliminary main raw material includes a step (S116).
  • the second chemical treatment step may use a flocculant, the flocculant may use a known organic flocculant or inorganic flocculant, and by appropriately included in accordance with the amount of the preliminary main raw material, it is possible to aggregate the preliminary main raw material.
  • the flocculant includes iron or aluminum, and ferrous sulfate (Fe (SO 4 )), ferric sulfate (Fe 2 (SO 4 ) 3 ), aluminum sulfate (Al 2 (SO 4 ) 3 ), chloride It may be selected from ferrous iron (FeCl 2 ), ferric chloride (FeCl 3 ), the addition amount may be added to 0.05 to 2% by weight, but does not limit the type and amount of the flocculant in the present invention.
  • the step of precipitating the second drug-treated preliminary raw material (S117), and drying the precipitated preliminary main raw material through the step (S118) of manufacturing a main raw material can be prepared according to the present invention.
  • the moisture content of the main raw material may correspond to about 80 to 85%.
  • the step of preparing the main raw material in the present invention can be produced by treating the organic waste.
  • an organic fertilizer is prepared using such a main raw material, and thus, the step of preparing the main raw material according to the present invention may be understood as treating the organic waste.
  • the apparatus for producing the main raw material corresponds to the organic waste treatment apparatus.
  • FIG 3 is a schematic view for explaining the organic waste treatment apparatus according to the present invention
  • Figure 4 is a schematic view for explaining the specific gravity separation unit in the organic waste treatment apparatus according to the present invention.
  • the organic waste treating apparatus 100 includes a specific gravity separating unit 110 for removing a heavy substance from the organic waste, and removes the heavy substance from the specific gravity separating unit 110. It includes a preliminary main raw material manufacturing unit 120 for decomposing organic waste, and includes a main raw material manufacturing unit 130 for manufacturing a main raw material by chemical treatment of the preliminary main raw material.
  • the specific gravity separating unit 110 includes a washing tank 112 into which the organic waste is input and a heavy material collecting unit 111 positioned in a predetermined lower region of the washing tank.
  • the washing tank 112 is for sorting organic materials from organic waste by a dipping method, and the washing tank 112 is filled with a predetermined amount of water together with a predetermined amount of organic waste.
  • the present invention is characterized in that the organic material is selected from the organic waste by the dipping method, as shown in Figure 4, the top portion of the specific gravity separation unit 110, the floating material 11 is located, the specific gravity separation unit The lower part of the 110, the heavy material 13 is located, the organic material 12 is located in the middle of the specific gravity separation unit 110, depending on the specific gravity, it is possible to separate the suspended matter, organic material and heavy material.
  • washing tank 112 such as a container or a water tank containing water, iron products, glass products, etc., which are heavy products, are precipitated in the lower weight collection unit 111, and the washing tank 112 is disposed.
  • floats such as vinyl products, plastic products, etc. are floated.
  • a predetermined region of the washing tank 112 may include a first mixing device 113 for facilitating mixing of organic waste and water, provided that the first mixing in the present invention. It does not limit the presence or absence of the device 113.
  • the predetermined region of the washing tank 112 includes an organic material outlet 114 for discharging the organic waste from which the heavy material is removed, more specifically, the organic material, and the heavy material in the predetermined region of the heavy material collection unit 111. It may include a heavy discharge outlet 115 for discharging.
  • the organic material discharge path 114 may include an organic material movement path 116 connected to the organic matter discharge path 115, and may include a heavy material movement path 117 connected to the weight discharge port 115.
  • the organic material movement path 116 and the heavy material movement path 117 may be connected to a predetermined region of the preliminary main raw material manufacturing unit 120.
  • the preliminary main raw material manufacturing unit 120 includes a crushing unit 121 for crushing the organic waste from which the heavy material is removed.
  • the organic material movement path 116 is connected to the crushing unit 121, that is, the organic waste from which the heavy material is removed may be transferred to the crushing unit 121 through the organic material moving path.
  • the organic waste may include heavy materials and suspended solids in addition to organic materials, and the heavy materials may be removed by the specific gravity separation unit.
  • the organic waste from which the weight has been removed may include organic material and suspended solids.
  • the organic waste including the organic material and the suspended matter may be crushed through the crushing unit 121, so that not only the size of the organic material may be minimized, but also the suspended matter may be crushed, thereby minimizing the size of the suspended matter. have.
  • the preliminary main raw material manufacturing unit 120 includes a floating material removing unit 127 positioned below the crushing unit 121, and the floating material may be removed from the floating material removing unit 127.
  • the pulverized suspended matter is more easily floated on the upper portion of the storage tank such as a container or a water tank containing water.
  • the preliminary main raw material manufacturing unit 120 includes a float container 122 located on one side of the float removing unit 127, that is, the float removed from the float removing unit 127 is the float container ( 122, it is finally discharged through the float discharge portion (126).
  • the heavy material movement path 117 is connected to a predetermined region of the preliminary main raw material manufacturing unit 120, more specifically, the heavy material movement path 117 may be connected to the floating container 122. have.
  • the heavy material moved through the heavy material movement path 117 is introduced into the floating container 122, and finally discharged through the floating material discharge part 126.
  • the preliminary main raw material manufacturing unit 120 is located in the lower region of the floating material removing unit 127 and includes a decomposition tank 123 for decomposing the organic material.
  • the organic waste from which the suspended matter is removed that is, the organic material is decomposed to prepare a preliminary main raw material
  • the preliminary main raw material may be prepared and stored by decomposing the organic material in the decomposition tank 123.
  • aerobic microorganisms can be used in the present invention
  • the aerobic microorganisms are Streptomyces, Thermoactinomycetes, Bacillus cereus ), Arcanobacterium haemolyticum, Lactobacillus delbrueckiilactis, Providencia stuartii, Staphylococcus kloosi, Vibrio hemolytic
  • One or more microorganisms selected from Tibrio haemolyticus may be used, but the present invention does not limit the type of aerobic microorganisms.
  • the preliminary main raw material moving means 124 for moving the preliminary main raw material stored in the decomposition tank 123 and the preliminary main raw material moving path 125 for moving the preliminary main raw material by the preliminary main raw material moving means 124 are further included. can do.
  • the preliminary main raw material movement path 125 may be connected to a predetermined region of the main raw material manufacturing unit 130.
  • the decomposition tank 123 may further include a water discharge path, as shown in the figure, the water introduced into the decomposition tank 123 via the crushing unit 121 through the specific gravity separation unit 110. May be supplied to the specific gravity separator 110 again through the water discharge path.
  • the main raw material manufacturing unit 130 includes a first drug processing unit 131 for processing the first main material of the preliminary drug and is connected to the second drug processing unit 131. It includes a second drug processing unit 132 for processing the second main material preliminary.
  • the preliminary main raw material moving path 125 is connected to the first drug processing unit 131, that is, the preliminary main raw material may be transferred to the first drug processing unit 131 through the preliminary main raw material moving path.
  • the step of treating the first drug may use an inorganic reactant, and the inorganic reactant may be lime (CaO).
  • the step of treating the first drug is to remove the salt contained in the preliminary main material, when the first drug treatment on the preliminary main raw material, the first drug and the preliminary main raw material react, so that a certain precipitate is generated. do.
  • the present invention may further include the step of removing the precipitate generated by the first drug treatment, after the first drug treatment of the preliminary main raw material.
  • the main raw material manufacturing unit 130 may include a precipitation unit 137 located in a predetermined lower region of the first drug processing unit 131, that is, in the first drug processing unit 131
  • the generated sediment may be collected in the sedimentation unit 137 and finally discharged through the sediment discharge unit 138.
  • the second drug treatment of the first drug-treated preliminary main raw material may be a flocculant, which is the same as described above, and thus the detailed description thereof will be omitted.
  • a predetermined region of the first drug processing unit 131 may include a second mixing device 135 for facilitating mixing of the preliminary main raw material and the first drug, the schedule of the second drug processing unit 132
  • the region may include a third mixing device 136 for facilitating mixing of the first drug-treated preliminary raw material and the second drug, provided that the second mixing device 135 and the third in the present invention.
  • the presence or absence of the mixing device 136 is not limited.
  • the main raw material manufacturing unit 130 includes a precipitation tank 133 connected to the second chemical processing unit 132.
  • the present invention includes the step of precipitating the second drug-treated preliminary raw material, by precipitating and storing the second drug-treated preliminary raw material in the precipitation tank, to prepare a main raw material according to the present invention Can be.
  • the main raw material may further include a main raw material moving means 134 for moving the main raw material from the settling tank and settled, the main raw material moving means 134 may be transferred to the device of the next step .
  • the water content of the main raw material is preferably equivalent to about 80 to 85%, when the water content of the main raw material precipitated and stored in the precipitation tank 133 does not meet this range, by a separate drying means, the main raw material Can be dried.
  • the settling tank 133 may further include a water discharge path, as shown in the figure, is introduced into the decomposition tank 123 via the crushing unit 121 through the specific gravity separation unit 110, after In addition, the water may be supplied to the specific gravity separating unit 110 through the water discharge path through the water discharge path through the first chemical treatment unit 131 and the second chemical treatment unit 132.
  • the above-described main raw material can be produced in the present invention.
  • FIG. 5 is a flow chart for explaining the steps of producing a water modifier according to the present invention.
  • the step of preparing the water-containing regulator according to the present invention includes preparing a main raw material (S121).
  • the manufacturing of the main raw material (S121) may be prepared through the above-described step of FIG. 2, that is, in the present invention, the main raw material may be used in preparing the water-containing regulator.
  • the step of preparing a water-containing regulator according to the present invention includes the step of preparing a subsidiary material (S122).
  • the subsidiary materials may include masato, ocher, silt, raw soil, and the like, and the subsidiary materials may be manufactured by drying them alone or by mixing them.
  • the water content of the sub-material may be 10% to 20%, preferably 15%.
  • the step of preparing a water-containing regulator according to the invention the step of mixing the main raw material and the sub-material.
  • the secondary raw material may be 40 to 60 parts by weight relative to 100 parts by weight of the main raw material
  • the amount of the auxiliary raw material may be appropriately blended according to the addition amount and the water content of the main raw material, more preferably a function prepared by the drying step described below
  • An appropriate amount can be selected to control so that the water content of the modifier can be 10% to 20%.
  • step of preparing a water-containing regulator according to the present invention the step of drying the mixed main and secondary raw materials to prepare a water-containing regulator (S124).
  • the water content of the water content regulator may be 10% to 20%, preferably 15%, and through the water content adjustment agent, it is possible to easily control the water content of the mixed raw material to be described later.
  • the water-containing regulator according to the present invention is manufactured by using the main raw material in the mixed raw material, that is, the mixed raw material for producing the organic fertilizer described later, even in the case of the main raw material contained in the water-containing regulator
  • the water-containing regulator since it can function as the main raw material in the mixed raw material, the water-containing regulator can not only control the water content of the organic fertilizer, but also can be part of the organic fertilizer by itself.
  • the water-containing modifier according to the present invention can not only control the amount of water, but also control the amount of organic substances in the organic fertilizer.
  • FIG. 6 is a flow chart for explaining the step of producing a mixed raw material according to the present invention.
  • the step of preparing the mixed raw material according to the present invention includes preparing a main raw material (S131).
  • the manufacturing of the main raw material (S131) may be manufactured through the above-described step of FIG. 2. That is, in the present invention, in preparing the mixed raw material, the same main raw material as the main raw material for preparing the water-containing regulator may be used.
  • the step of preparing the mixed raw material according to the present invention includes the step of preparing a water-containing regulator (S132).
  • the step (S132) of preparing the water modifier may be prepared through the above-described step of FIG. 5, that is, in the present invention, in preparing the water modifier, the same main raw material as the main material for preparing the mixed raw material of this step is used. Can be used.
  • the step of preparing the mixed raw material according to the present invention may include mixing the main raw material and the water-containing regulator (S133).
  • the water regulator is to adjust the function of the main raw material, it may include 40 to 60 parts by weight compared to 100 parts by weight of the main raw material.
  • the moisture content of the main raw material may correspond to about 80 to 85%.
  • the water content of the main raw material is 80 to 85% may mean that the organic material in the main raw material is 15 to 20%.
  • controlling the function of the main raw material through the water modifier may mean increasing the content of the organic substance in the main raw material.
  • the step of preparing a mixed raw material according to the present invention by adjusting the function of the mixed main raw material and the function regulator, comprising the step of preparing a mixed raw material (S134).
  • the mixed raw material according to the present invention may be prepared, including the main raw material and the water-containing regulator, wherein the water-containing regulator is the same as the main raw material that is the main component of the mixed raw material according to the present invention It can be prepared using.
  • the water-containing regulator not only can control the water content of the organic fertilizer, but also by itself It can be part of organic fertilizers.
  • the water content of the mixed raw material may be 10% to 40%, preferably 15% to 30%, the water content of the mixed raw material can be controlled by the mixing of the above-described main raw material and the water regulator.
  • the present invention can produce an organic fertilizer by fermenting and ripening the mixed raw material.
  • the step of preparing the main raw material in the present invention can be produced by treating the organic waste.
  • such a main raw material and a secondary raw material may be mixed to produce a water-containing regulator.
  • an organic fertilizer is prepared by mixing the main raw material and the subsidiary material to produce a water-containing regulator, to prepare a mixed raw material by using the main raw material and the water-containing regulator, fertilizing and ripening the mixed raw material to produce an organic fertilizer.
  • the manufacturing apparatus of the will be described.
  • the manufacturing apparatus of the organic fertilizer in the present invention may include an organic waste treatment apparatus in the step of treating the organic waste described above.
  • the apparatus for treating organic waste in the present invention is, firstly, an apparatus for treating organic waste, second, a mixed raw material manufacturing apparatus for preparing a mixed raw material using a main raw material, and third, fermenting and ripening the mixed raw material. It may include a fermentation / aging device, and will be described in detail below for the second mixed raw material manufacturing apparatus and the third fermentation / ripening apparatus.
  • the apparatus for producing a mixed raw material for producing a mixed raw material using the second main raw material can be classified into two types.
  • the main raw material and the subsidiary raw material are mixed by one device to prepare a water content adjusting agent, and the other raw material may be mixed with the main raw material and the water adjusting agent to produce a mixed raw material.
  • a mixed raw material may be prepared by mixing the main raw material and the subsidiary raw material in one device to produce a water content regulator, and the mixed raw material and the water content regulator in the same device.
  • the mixed raw material manufacturing apparatus according to the first embodiment of the present invention may be a mixed raw material manufacturing apparatus for producing a mixed raw material by mixing the main raw material and the water content regulator, and also, a function for producing a water content regulator by mixing the main raw material and the sub-raw material It may be a regulator manufacturing apparatus.
  • the mixed raw material manufacturing apparatus of FIGS. 7 and 8 will be described as a device for producing a mixed raw material by mixing the main raw material and the water-reducing agent, except that the apparatus in FIGS. 7 and 8 shows the main raw material and the sub raw material. It can also be used as a device for mixing the water-soluble regulator.
  • a raw material mixture for mixing the raw material input unit 210 and the raw material introduced into the raw material input unit 210.
  • the unit 220 and the mixed raw material drying unit 230 for drying the raw materials mixed in the raw material mixing unit 220.
  • the raw material input part 210 may include a first raw material input part 211 and a second raw material input part 212, the first raw material may be a main raw material, and the second raw material may be a water content regulator.
  • the apparatus in Figures 7 and 8 is also used as a device for producing a water-conditioning agent by mixing the main raw material and the sub-raw material, in this case, the first raw material is the main raw material, the second raw material is the sub-raw material Can be.
  • the mixed raw material drying unit 230 includes a chamber part 231 connected to the raw material mixing part 220, and is located inside the chamber part 231. It includes an internal drying path 240, and includes an external drying path (250, 260) located outside the mixed raw material drying unit, wherein the external drying path (250, 260) is located on one side of the chamber portion And a first side external drying path 250 and a second side external drying path 260 positioned on the other side of the chamber part.
  • the internal drying path 240, the first side external drying path 250, and the second side external drying path 260 may each include a plurality, that is, a plurality of internal drying paths 240a to 240f, and a plurality of internal drying paths 240a to 240f, respectively. It may include a first side external drying path (250a ⁇ 250c) and a plurality of second side external drying path (260a ⁇ 260c), these drying paths may be arranged in a zigzag.
  • the internal drying path may be a horizontal drying path
  • the external drying path may be a vertical drying path
  • a heating means 280 is located inside the chamber portion 231, wherein the heating means 280 is located in the lower portion of the chamber portion, the lower heating means 280a for heating the interior of the chamber portion And located on the side of the chamber portion, may include a side heating means (280b) for heating the interior of the chamber portion.
  • the mixture may further include a mixed raw material discharge part 270 connected to the external drying path.
  • the mixed raw material mixed in the raw material mixing part 220 is discharged to the mixed raw material discharge part 270 through the internal drying path and the external drying path.
  • the mixed raw material is dried while passing through the internal drying path and the external drying path.
  • the mixed raw material is dried by the high temperature, and in the external drying path, the internal drying path. While the mixed raw material becomes hot while passing through a relatively low external drying path, moisture contained in the mixed raw material is dried in the process of being discharged as water vapor.
  • the present invention includes an internal drying path located inside the chamber part and an external drying path located outside the chamber part, wherein the mixed material is dried by a high temperature in the internal drying path.
  • drying is performed by evaporation of water in the form of water vapor due to the temperature difference between the mixed raw material and the outside air.
  • the apparatus in Figures 7 and 8 is also used as a device for producing a water-conditioning agent by mixing the main raw material and the sub-raw material, in this case, the first raw material is the main raw material, the second raw material is the sub-raw material And, therefore, what is produced in the apparatus may be a water content regulator.
  • FIG. 9 is a schematic perspective view showing a mixed raw material manufacturing apparatus according to a second embodiment of the present invention.
  • the apparatus for producing a mixed raw material according to the second embodiment of the present invention corresponds to an apparatus capable of simultaneously producing a water content regulator and a mixed raw material.
  • the mixed raw material manufacturing apparatus according to the second embodiment of the present invention may refer to the mixed raw material manufacturing apparatus of the first embodiment except as described below.
  • the mixed raw material manufacturing apparatus 400 according to the second embodiment of the present invention, a raw material mixing unit 421a for mixing the raw material input unit 410 and the raw material introduced into the raw material input unit 410 , 421b) and a mixed raw material drying unit 430 for drying the mixed raw materials in the raw material mixing units 421a and 421b.
  • the raw material input part 410 is a second path raw material input part separated from the first path raw material input parts 411 and 421b and the first path raw material input parts 411 and 421b. 412 and 422b.
  • the first path raw material input unit 411, 421b includes a first path first raw material input unit 411 and a first path second raw material input unit 421b
  • the second path raw material input unit 412, 422b includes a second path first raw material input part 412 and a second path second raw material input part 422b.
  • the raw material introduced into the first raw material input part 411 is a sub-material
  • the raw material introduced into the second raw material input part 421b of the first path is a main raw material
  • the first second raw material is supplied to the second raw material.
  • the raw material introduced into the raw material input unit 412 may be a water content regulator
  • the raw material introduced into the second path second raw material input unit 422b may be a main raw material.
  • the first raw material mixing unit 421a and the first raw material mixing unit connected to the first path raw material input units 411 and 421b are separated from the second path raw material.
  • a second raw material mixing part 422a connected to the input parts 412 and 422b.
  • the first path may be mixed with the main raw material and the subsidiary material, and in the second path, the water content regulator and the main raw material may be mixed.
  • the mixed raw material drying unit 430 includes a chamber part 431 connected to the first raw material mixing part 421a and the second raw material mixing part 422a.
  • the chamber part includes a first drying path connected to the first raw material mixing part 421a and a second drying path connected to the second raw material mixing part 421b.
  • the first drying path includes a first internal drying path 440 located inside the chamber part 431, and first external drying paths 450 and 460 located outside the chamber part 431. ).
  • the second drying path may include a second internal drying path (not shown) positioned inside the chamber part 431, and a second external drying path located outside the chamber part 431. 460 ').
  • the first drying path and the second drying path may be arranged in the same form, except that the water-adjusting agent is manufactured by the first drying path, and the mixed raw material may be manufactured by the second drying path. Therefore, according to the second embodiment of the present invention, therefore, the process of manufacturing the water-containing regulator and the process of manufacturing the mixed raw material can be implemented in one apparatus.
  • the first drying path may further include a water content regulator discharge unit 470 connected to the first external drying path
  • the second drying The path may further include a mixed raw material discharge part 470 ′ connected to the second external drying path
  • the second raw material may further include the moisture control agent discharged through the moisture control agent discharge part 470. It may further include a function adjuster movement path 480 for input to the input unit 412.
  • the preparation of the mixed raw material according to the second embodiment of the present invention as described above is as follows.
  • a subsidiary material input to the first raw material input part 411 is input, and a main raw material is input to the second raw material input part 421b of the first path, and the sub raw material and the main raw material are mixed with the first raw material. It is mixed in the part 421a.
  • the mixed main raw materials and the sub raw materials are a first drying path, that is, a first internal drying path 440 located inside the chamber part 431 and a first external drying path 450 located outside the mixed raw material drying part. It is dried while passing through, 460, is made of a water-containing regulator, the water-containing regulator is discharged through the water-containing regulator discharge unit 470.
  • the discharged water modifier is introduced into the second path first raw material input part 412 through the water modifier moving path 480, and the main raw material is added to the second raw material input part 422b.
  • the water content regulator and the main raw material are mixed in the second raw material mixing portion 422a.
  • the mixed main raw material and the water adjusting agent have a second drying path, that is, a second internal drying path (not shown) located inside the chamber part 431 and a second external drying path located outside the mixed raw material drying part. It is dried while going through the (460 '), and is made of a mixed raw material, the mixed raw material is discharged through the mixed raw material discharge portion (470').
  • FIG. 10 is a schematic perspective view showing a fermentation / maturation apparatus of a mixed raw material according to the present invention
  • FIG. 11 is a schematic sectional view showing another mixed raw material according to the present invention.
  • the fermentation / maturation device of the mixed raw material according to the present invention is a container portion 320 for storing the organic fertilizer manufactured and the fermentation / maturation portion 310 disposed surrounding the outside of the container portion ).
  • the fermentation / ripening unit 310 includes a mixed raw material input unit 311 for inputting the mixed raw material, the organic fertilizer discharge port 312 for discharging the organic fertilizer manufactured through the fermentation / ripening unit 310 Including a), the organic fertilizer for transporting the organic fertilizer discharged through the organic fertilizer outlet 312 and the organic fertilizer for delivering the organic fertilizer to the container portion connected to the moving means 330 Path 340.
  • the mixed raw material introduced through the mixed raw material input part 311 is fermented and aged through the fermentation / aging part 310 to be manufactured as an organic fertilizer, and manufactured organic Fertilizer can be stored and stored in the container unit 320.
  • the mixed raw material input portion 311 is located at the upper end of the container portion 320
  • the organic fertilizer discharge port 312 is located at the lower end of the container portion 320
  • the fermentation / maturation portion 310 Since the spiral is made, the mixed raw material injected into the mixed raw material input part 311 may naturally move to the organic fertilizer discharge port 312 by gravity.
  • Organic fertilizer manufacturing apparatus as described above can be largely divided into three types.
  • the organic fertilizer manufacturing apparatus first, the organic waste treatment apparatus in the step of treating the organic waste, second, the mixed raw material manufacturing apparatus using the main raw material, third, fermentation / maturation of fermenting and ripening the mixed raw material It may include a device.

Abstract

The present invention relates to a device for manufacturing an organic fertilizer, comprising: a raw material feeding part; a raw material mixing part for mixing raw materials fed from the raw material feeding part; and a mixed raw material drying part for drying the raw materials mixed in the raw material mixing part, wherein the mixed raw material drying part comprises: a chamber part connected to the raw material mixing part; and a mixed raw material manufacturing device including an inner drying path located inside the chamber part, and an outer drying path located outside the mixed raw material drying part. Organic waste resources can be recycled through the device for manufacturing an organic fertilizer.

Description

유기성 비료의 제조장치Organic Fertilizer Manufacturing Equipment
본 발명은 유기성 비료의 제조장치에 관한 것으로서, 더욱 상세하게는 유기성 폐기물 자원의 재활용화을 위한 유기성 비료의 제조장치에 관한 것이다.The present invention relates to an apparatus for producing organic fertilizer, and more particularly, to an apparatus for producing organic fertilizer for recycling of organic waste resources.
최근 신재생 에너지 자원의 육성과 더불어 바이오 가스 플랜트에서 혐기 발효된 액체 슬러지가 액비로 유용되고 있으나 과다 배출시 수요, 공급 및 적기 처리의 문제가 발생되기 때문에 이에 대한 대책 방안인 액비의 장기 보관 방법으로 고체 성형화가 절실히 요구되고 있다.Recently, anaerobic fermented liquid sludge from biogas plants has been used as liquid fertilizers as well as the development of renewable energy resources. However, excessive discharge causes problems in demand, supply, and timely disposal. Solid molding is urgently needed.
일반적으로 유기성 폐기물은 많은 양이 매일 발생하며, 이를 처리할 시설이 부족하고 완벽한 처리 기술이 없어 많은 양의 유기성 폐기물이 매립되거나 소각되고, 그 일부만 탈수 및 세척하여 발효 과정을 거친 후 퇴비 및 사료로 생산되고 있는 실정이다.In general, large amounts of organic waste are generated daily, and there is a lack of facilities to deal with them and there is no perfect treatment technology, so a large amount of organic waste is landfilled or incinerated, and only a part of it is dehydrated and washed to undergo fermentation and then compost and feed It is being produced.
또한, 음식물 쓰레기 슬러지, 축분 슬러지, 하수 슬러지, 바이오 가스 플랜트 슬러지 등과 같은 유기성 폐기물에서 발생하는 폐수도 대부분 해양에 투기되어 수산 자원의 오염 및 어장의 황폐화를 초래해 왔으며, 방출된 가축 분뇨는 지하수 및 하천을 오염시켜 식수원을 위협하고 있다.  In addition, wastewater generated from organic wastes such as food waste sludge, animal sludge, sewage sludge, and biogas plant sludge has also been mostly dumped in the ocean, causing pollution of fisheries resources and wasteland of fisheries. Polluting rivers threatens drinking water sources.
일부에서는 일정한 폐수 시설을 설치하여 폐수 처리 후 방류하는 방법을 채택하고 있으나, 이것 또한 약품 및 기타 부대 비용의 증가로 현실성 있는 대안이 되지 못하고 있다.Some have adopted a method of discharging the wastewater after discharging it by installing certain wastewater facilities, but this is not a viable alternative due to the increase of drugs and other incidental costs.
이처럼 매일 발생하는 유기성 폐기물을 종래의 방법으로 처리할 경우에는 2차 발생 오염의 방지가 매우 어려운 문제로 긴박히 대두된다. 따라서 많은 연구자와 개발자들이 이 문제를 효과적으로 처리하여 2차 오염 없이 유기성 폐기물 자원을 재활용할 수 있는 다양한 방법을 찾는 연구와 장치의 개발이 있으나, 근본적인 해결방법은 여전히 개발되지 않고 있다.When the organic waste generated daily is treated in a conventional manner, it is urgent to prevent secondary generation pollution. As a result, many researchers and developers have researched and developed devices to effectively deal with this problem and find various ways to recycle organic waste resources without secondary pollution, but the fundamental solution is still not developed.
더욱이, 하수 슬러지와 악성 폐수 등의 해양 투기가 2013년부터는 전면 금지되었다. 그동안 해양 투기가 허용되었던 음식물 쓰레기 슬러지, 축분 슬러지, 하수 슬러지, 바이오 가스 플랜트 슬러지 등과 같은 유기성 폐기물을 처리하기 위해서는 기존 처리 시설을 증설 및 개선한 처리 시스템을 설치해야 한다.Moreover, marine dumping, including sewage sludge and malignant wastewater, has been banned since 2013. In order to treat organic wastes such as food waste sludge, waste sludge, sewage sludge, and biogas plant sludge, which have been permitted for dumping at sea, existing treatment facilities have to be expanded and installed.
기존의 유기성 폐기물 처리 방법 중 감량화 처리 기술은 근본적으로 유해물질을 제거할 수 없다는 과정으로 함수율이 85% 이상인 유기성 폐기물에서 단지 수분을 제거하여 폐기물을 최소화하는 기술이며, 기타 방법으로 유해 물질을 제거하기 위하여 탈수 및 세척 후 톱밥 등을 혼합하여 그 유해 물질을 희석하는 방법이 있으며, 이러한 방법은 퇴비를 생산하는 기술과 일반 사료와 유기성 슬러지를 일부 혼합하여 사료를 만드는 기술이다.Among the existing organic waste treatment methods, the reduction treatment technology is basically a process that cannot remove harmful substances, and it is a technique that minimizes waste by simply removing moisture from organic waste having a moisture content of 85% or more. For this purpose, there is a method of diluting the harmful substances by mixing sawdust and the like after dehydration and washing, and this method is a technique for producing compost and a technique for making a feed by mixing some of the general feed and organic sludge.
이와 같은 종래의 감량화 기술에 의하면, 유기성 폐기물을 건조 및 발효시켜 최소화하며 잔량 폐기물을 매립하는 경우, 오수에 의해 침출수가 발생하여 지하수 및 토양을 오염시키며, 악취 및 병원균이 발생한다. 또한, 자원의 재활용화가 되지 않아 경제적인 손실이 막대하다 하겠다.According to such a conventional weight reduction technology, when organic wastes are dried and fermented to minimize the landfill wastes, leachate is generated by sewage to contaminate groundwater and soil, and odors and pathogens are generated. In addition, the economic loss is enormous because resources are not recycled.
또한, 탈수, 세척 및 발효에 의한 유기질 비료(퇴비) 생산은 그 처리과정에서 침출수 및 오폐수 등으로 2차 오염이 발생하여 처리 공장 주변의 자연 환경을 훼손하며, 생산된 퇴비에 유해 물질이 잔류하는 등 시비 후, 2차 토양 오염이 발생하며, 시설투자 비용의 과다로 경제성이 전혀 없어 설치 후 대개 정상적인 운영이 되고 있지 않다.In addition, organic fertilizer (compost) production by dehydration, washing, and fermentation causes secondary pollution with leachate and wastewater during the treatment process, which damages the natural environment around the treatment plant, and harmful substances remain in the produced compost. After the application, secondary soil pollution occurs, and due to the excessive investment of facilities, there is no economic feasibility.
한편, 기존의 유기성 폐기물의 처리방법 중 소각기술은 소각 시에 다이옥신과 같은 맹독이 발생하여 인류의 생명을 위협하고 있다. 시설투자비 및 처리비용의 과다로 인해 유기성 폐기물의 소각을 중지하려고 하나, 특별한 처리방법이 없어 대안을 찾고자 고심하고 있는 실정이다.On the other hand, incineration technology of the existing method of treating organic waste is a deadly poison, such as dioxin when incinerated, threatening human life. Due to the excessive investment of facilities and disposal costs, the incineration of organic wastes has been stopped, but there is no special treatment method, and the situation is being sought to find an alternative.
따라서, 종래 기술로서 유기성 폐기물에 함유된 유해물질의 제거를 어떻게 하는가에 따라 감량화, 탈수, 세척 및 발효 등의 처리방법이 개발되어 왔으나, 투자 비용, 처리 비용 및 재활용에 따른 경제성 여부와 처리 결과물의 유해물질 제거가 이루어지지 않는 등 많은 문제가 발생하고 있다. Therefore, as a conventional technique, treatment methods such as reduction, dehydration, washing and fermentation have been developed according to how to remove harmful substances contained in organic wastes. There are many problems such as no removal of harmful substances.
이러한 문제가 있음에도 매립 및 소각으로 많은 양의 유기성 폐기물이 처리되고 있어 근본적인 대책이 절박한 실정이다.Despite these problems, a large amount of organic waste is being disposed of by landfilling and incineration, which implies an urgent need for fundamental measures.
유기성 폐기물의 처리 기술은 근본적으로 처리 시에, 2차 오염이 발생하는 것은 바람직하지 않다. 또한, 처리 결과물도 자연 환경을 오염시켜서는 안 되는 자원 재활용 기술이어야 한다는 기본 원칙을 지켜야 한다. 그러나 종래의 처리 방법은 여러 가지 문제점이 노출되어 한계에 봉착했다.In the treatment of organic waste, it is not desirable that secondary pollution occurs in the treatment. In addition, basic principles should be observed that the result of treatment should be resource recycling technology that should not pollute the natural environment. However, the conventional treatment methods are exposed to various problems and have reached a limit.
매일 발생하는 유기성 폐기물을 매립 및 소각에 의존하고 있으나, 현재까지 이처럼 환경법에 의해 유기성 폐기물의 매립 및 소각을 금지하도록 되어 있으므로 지방 자치 단체 환경 담당자 뿐만 아니라 전 세계의 모든 국가가 이 같은 문제에 크게 고심하고 있다.Relying on landfills and incineration of organic wastes generated every day, but to date, the environmental law has banned landfilling and incineration of organic wastes. Doing.
특히, 쓰레기로 버려지는 유기성 폐기물은 상당한 양이 분리 및 수거되지만 일부 많은 양이 소각, 매립 및 해양 투기되고 있다. 유기성 슬러지 폐기물의 특성이 지역마다 다르고, 그 내용물의 특이성으로 인해 자원재활용에 어려운 문제가 있으므로 일부는 탈수 및 세척 후에 발효 과정을 거친 후 퇴비로 생산하여 처리하고, 극히 일부는 사료로 생성하여 처리하고 있는 실정이다.In particular, organic wastes that are disposed of as garbage are separated and collected in significant quantities, but some are incinerated, landfilled and dumped at sea. The characteristics of organic sludge wastes vary from region to region, and the specificity of their contents makes it difficult to recycle resources. Some of them are dehydrated and washed and then fermented and then composted. There is a situation.
이 중에서 유기성 폐기물의 매립 시에는 매립장 주변의 악취와 해충 등으로 인한 피해가 크고, 매립 후에 발생하는 2차 오염물질의 침출수로 인한 토양 및 수질 오염문제가 매우 심각하다. Among them, when organic waste is reclaimed, damage due to bad smells and pests around the landfill site is large, and soil and water pollution problems due to leachate of secondary pollutants occurring after reclamation are very serious.
주민들의 매립장 설치 반대로 인하여 매립장 자체를 구하기 힘든 직접적인 문제도 생기고, 매립장 설치장소도 점점 줄어들고 있다. 이와 같이 환경 오염의 문제를 근원적으로 해결할 수 없어 국내는 물론 전 세계적으로 유기성 폐기물의 처리가 환경 문제의 중요한 이슈로 대두되고 있다.Due to the opposition of the landfill site, residents have a direct problem that it is difficult to obtain the landfill site itself. As such, the problem of environmental pollution cannot be fundamentally solved. Therefore, the treatment of organic wastes is emerging as an important issue of environmental problems both domestically and globally.
기존의 탈수 및 세척 후의 발효 방식은 퇴비화를 가능하게 하는 이점은 있으나, 유해 물질의 근본적인 제거가 이루어지지 않고, 악취가 발생하는 등의 문제가 남는다. Existing dehydration and the fermentation method after washing has the advantage of enabling composting, but there is a problem such as fundamental removal of harmful substances is not made, odor occurs.
또한, 시비 후에 토양의 2차 오염이 발생함으로 불완전 처리에 불과하며, 사료화는 음식물 쓰레기의 특성인 부패가 빨라 제조된 사료에 독성이 남아 있게 되어 가축의 폐사가 발생하며, 또한 축산물에 누적된 잔류성 유해 물질로 인하여 국민 건강까지 위협하고 있다.In addition, secondary pollution of the soil occurs after fertilization, which is only an incomplete treatment. Feeding is rapidly decaying, which is a characteristic of food waste, resulting in toxic remains in the produced feed, resulting in death of livestock, and accumulated residue in livestock products. Toxic substances threaten national health.
따라서, 보다 현실적이고 근본적인 유기성 폐기물 자원의 재활용화가 가능한 신기술의 필요성이 절실히 요구되고 있다.Therefore, there is an urgent need for new technologies capable of recycling more realistic and fundamental organic waste resources.
본 발명이 해결하고자 하는 과제는 유기성 폐기물 자원의 재활용화를 위한 유기성 비료의 제조장치를 제공하는데 그 목적이 있다.An object of the present invention is to provide an apparatus for producing organic fertilizer for the recycling of organic waste resources.
본 발명의 목적들은 이상에서 언급한 목적으로 제한되지 않으며, 언급되지 않은 또 다른 목적들은 아래의 기재로부터 당업자에게 명확하게 이해될 수 있을 것이다.The objects of the present invention are not limited to the above-mentioned objects, and other objects which are not mentioned will be clearly understood by those skilled in the art from the following description.
상기 지적된 문제점을 해결하기 위해서 본 발명은 원료 투입부; 상기 원료 투입부로 투입된 원료를 혼합하기 위한 원료 혼합부; 및 상기 원료 혼합부에서 혼합된 원료를 건조하기 위한 혼합 원료 건조부를 포함하고, 상기 혼합 원료 건조부는, 상기 원료 혼합부와 연결되는 챔버부; 상기 챔버부의 내부에 위치하는 내부 건조경로 및 상기 혼합 원료 건조부의 외부에 위치하는 외부 건조경로를 포함하는 혼합 원료 제조장치를 포함하는 유기성 비료의 제조장치를 제공한다.The present invention in order to solve the above-mentioned problems raw material input unit; A raw material mixing part for mixing the raw materials introduced into the raw material input part; And a mixed raw material drying unit for drying the raw materials mixed in the raw material mixing unit, wherein the mixed raw material drying unit comprises: a chamber unit connected to the raw material mixing unit; It provides an organic fertilizer manufacturing apparatus including an internal raw material manufacturing apparatus including an internal drying path located inside the chamber portion and an external drying path located outside the mixed raw material drying unit.
또한, 본 발명은 상기 챔버부의 내부에 위치하는 가열 수단을 포함하며, 상기 가열 수단은 상기 챔버부의 하부에 위치하여, 상기 챔버부의 내부를 가열하는 하부 가열 수단 및 상기 챔버부의 측면에 위치하여, 상기 챔버부의 내부를 가열하는 측면 가열 수단을 포함하는 유기성 비료의 제조장치를 제공한다.In addition, the present invention includes a heating means located in the chamber portion, wherein the heating means is located in the lower portion of the chamber portion, the lower heating means for heating the inside of the chamber portion and the side of the chamber portion, Provided is an apparatus for producing organic fertilizer comprising side heating means for heating the inside of the chamber portion.
또한, 본 발명은 상기 원료 투입부는 제1원료 투입부 및 제2원료 투입부를 포함하며, 상기 제1원료 투입부에 투입되는 원료는 주원료이고, 상기 제2원료 투입부에 투입되는 원료는 함수조정제인 유기성 비료의 제조장치를 제공한다.In addition, the present invention, the raw material input unit includes a first raw material input unit and a second raw material input unit, the raw material input to the first raw material input unit is the main raw material, the raw material input to the second raw material input unit is a water content regulator An apparatus for producing phosphorus organic fertilizer is provided.
또한, 본 발명은 상기 원료 투입부는 제1원료 투입부 및 제2원료 투입부를 포함하며, 상기 제1원료 투입부에 투입되는 원료는 함수조정제이고, 상기 제2원료 투입부에 투입되는 원료는 주원료인 유기성 비료의 제조장치를 제공한다.In addition, the present invention, the raw material input unit includes a first raw material input unit and the second raw material input unit, the raw material introduced into the first raw material input unit is a water-conditioning regulator, the raw material introduced into the second raw material input unit is the main raw material An apparatus for producing phosphorus organic fertilizer is provided.
또한, 본 발명은 상기 원료 투입부는 제1경로 원료 투입부 및 상기 제1경로 원료 투입부와 분리되는 제2경로 원료 투입부를 포함하고, 상기 제1경로 원료 투입부는 제1경로 제1원료 투입부 및 제1경로 제2원료 투입부를 포함하며, 상기 제2경로 원료 투입부는 제2경로 제1원료 투입부 및 제2경로 제2원료 투입부를 포함하며, 상기 제1경로 제1원료 투입부에 투입되는 원료는 부원료이고, 상기 제1경로 제2원료 투입부에 투입되는 원료는 주원료이며, 상기 제2경로 제1원료 투입부에 투입되는 원료는 함수조정제이고, 상기 제2경로 제2원료 투입부에 투입되는 원료는 주원료인 유기성 비료의 제조장치를 제공한다.The present invention may further include a first path raw material input part and a second path raw material input part separated from the first path raw material input part, and the first path raw material input part may include a first path first raw material input part. And a first path second raw material input part, wherein the second path raw material input part includes a second path first raw material input part and a second path second raw material input part, and enters the first path first raw material input part. The raw material to be added is a secondary raw material, the raw material to be injected into the second raw material input part of the first path is a main raw material, the raw material to be injected into the first raw material input part of the second path is a water content regulator, and the second raw material input part of the second path. The raw material to be added to provides an apparatus for producing organic fertilizer which is a main raw material.
또한, 본 발명은 상기 원료 혼합부는, 상기 제1경로 원료 투입부와 연결되는 제1원료 혼합부 및 상기 제1원료 혼합부와 분리되고, 상기 제2경로 원료 투입부와 연결되는 제2원료 혼합부를 포함하고, In addition, the present invention, the raw material mixing unit, the first raw material mixing unit connected to the first path raw material input unit and the second raw material mixing unit is separated from the first raw material mixing unit, the second raw material mixing unit Including wealth,
상기 챔버부는, 상기 제1원료 혼합부와 연결되는 제1건조 경로 및 상기 제2원료 혼합부와 연결되는 제2건조 경로를 포함하고, 상기 내부 건조경로는 제1내부 건조경로 및 제2내부 건조경로를 포함하고, 상기 외부 건조경로는 제1외부 건조경로 및 제2외부 건조경로를 포함하며, 상기 제1건조 경로는, 상기 챔버부의 내부에 위치하는 상기 제1내부 건조경로 및 상기 챔버부의 외부에 위치하는 상기 제1외부 건조경로를 포함하고, 상기 제2건조 경로는, 상기 챔버부의 내부에 위치하는 상기 제2내부 건조경로 및 상기 챔버부의 외부에 위치하는 제2외부 건조경로를 포함하는 유기성 비료의 제조장치를 제공한다.The chamber part includes a first drying path connected to the first raw material mixing part and a second drying path connected to the second raw material mixing part, wherein the internal drying path includes a first internal drying path and a second internal drying. And an external drying path, wherein the external drying path includes a first external drying path and a second external drying path, and the first drying path includes: the first internal drying path and the outside of the chamber part located in the chamber part. The first drying path includes a first external drying path, wherein the second drying path is organic, including the second internal drying path located inside the chamber portion and the second external drying path located outside the chamber portion. Provided is a fertilizer manufacturing apparatus.
또한, 본 발명은 상기 제1건조 경로는 상기 제1외부 건조경로와 연결되는 함수조정제 배출부를 포함하, 상기 제2건조 경로는 상기 제2외부 건조경로와 연결되는 혼합 원료 배출부를 더 포함하며, 상기 함수조정제 배출부를 통해 배출된 함수조정제를 상기 제2경로 제1원료 투입부에 투입하기 위한 함수 조정제 이동경로를 더 포함하는 유기성 비료의 제조장치를 제공한다.In addition, the first drying path further comprises a water content regulator discharge part connected to the first external drying path, the second drying path further includes a mixed raw material discharge part connected to the second external drying path, It provides an organic fertilizer manufacturing apparatus further comprising a water-containing regulator moving path for injecting the water-containing regulator discharged through the water-containing regulator discharge unit to the second raw material first feeder.
상기한 바와 같은 본 발명에서는 상기 유기성 비료의 제조 장치를 통해, 유기성 폐기물 자원의 재활용화가 가능하다.In the present invention as described above, through the organic fertilizer production apparatus, it is possible to recycle the organic waste resources.
또한, 본 발명에서는 농작물, 수목과 작물의 성장에 필요한 영양소를 골고루 함유하고 있고, 비교적 간단한 처리 방법에 의하여 친환경적인 양질의 유기성 비료를 제조할 수 있다.In addition, the present invention evenly contains nutrients necessary for the growth of crops, trees and crops, it is possible to produce a high-quality organic fertilizer of environmentally friendly by a relatively simple treatment method.
또한, 본 발명에서는 유기성 페기물을 재활용하는 효과와 매립 후에 발생하는 2차 오염물질의 침출수로 인한 토양 및 수질 오염문제를 유발하지 않는 유기성 비료를 제조할 수 있다.In addition, the present invention can produce an organic fertilizer that does not cause the problem of soil and water pollution due to the effect of recycling organic waste and leachate of secondary pollutants generated after landfill.
도 1은 본 발명에 따른 유기성 비료의 제조방법을 도시한 흐름도이다.1 is a flow chart showing a method for producing an organic fertilizer according to the present invention.
도 2는 본 발명에 따른 유기성 폐기물을 처리하여 주원료를 제조하는 단계를 설명하기 위한 흐름도이다.Figure 2 is a flow chart for explaining the step of producing a main raw material by treating the organic waste according to the present invention.
도 3는 본 발명에 따른 유기성 폐기물 처리장치를 설명하기 위한 개략적인 도면이며, 도 4는 본 발명에 따른 유기성 폐기물 처리장치에서의 비중 분리부를 설명하기 위한 개략적인 도면이다.3 is a schematic view for explaining the organic waste treatment apparatus according to the present invention, Figure 4 is a schematic view for explaining the specific gravity separation unit in the organic waste treatment apparatus according to the present invention.
도 5는 본 발명에 따른 함수 조정제를 제조하는 단계를 설명하기 위한 흐름도이다.5 is a flow chart for explaining the steps of producing a water modifier according to the present invention.
도 6은 본 발명에 따른 혼합원료를 제조하는 단계를 설명하기 위한 흐름도이다.6 is a flow chart for explaining the step of producing a mixed raw material according to the present invention.
도 7은 본 발명의 제1실시예에 따른 혼합 원료 제조장치를 도시하는 개략적인 사시도이고, 도 8은 본 발명의 제1실시예에 따른 혼합 원료 제조장치를 도시하는 개략적인 단면도이다.7 is a schematic perspective view showing a mixed raw material manufacturing apparatus according to a first embodiment of the present invention, Figure 8 is a schematic cross-sectional view showing a mixed raw material manufacturing apparatus according to a first embodiment of the present invention.
도 9는 본 발명의 제2실시예에 따른 혼합 원료 제조장치를 도시하는 개략적인 사시도이다.9 is a schematic perspective view showing a mixed raw material manufacturing apparatus according to a second embodiment of the present invention.
도 10은 본 발명에 따른 혼합원료의 발효/숙성 장치를 도시하는 개략적인 사시도이고, 도 11은 본 발명에 다른 혼합원료를 도시하는 개략적인 단면도이다.10 is a schematic perspective view showing a fermentation / maturation apparatus of a mixed raw material according to the present invention, and FIG. 11 is a schematic sectional view showing another mixed raw material according to the present invention.
본 발명의 이점 및 특징, 그리고 그것들을 달성하는 방법은 첨부되는 도면과 함께 상세하게 후술되어 있는 실시예들을 참조하면 명확해질 것이다. 그러나 본 발명은 이하에서 개시되는 실시예들에 한정되는 것이 아니라 서로 다른 다양한 형태로 구현될 것이며, 단지 본 실시예들은 본 발명의 개시가 완전하도록 하며, 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자에게 발명의 범주를 완전하게 알려주기 위해 제공되는 것이며, 본 발명은 청구항의 범주에 의해 정의될 뿐이다.Advantages and features of the present invention and methods for achieving them will be apparent with reference to the embodiments described below in detail with the accompanying drawings. However, the present invention is not limited to the embodiments disclosed below, but will be implemented in various forms, and only the present embodiments are intended to complete the disclosure of the present invention, and the general knowledge in the art to which the present invention pertains. It is provided to fully convey the scope of the invention to those skilled in the art, and the present invention is defined only by the scope of the claims.
아래 첨부된 도면을 참조하여 본 발명의 실시를 위한 구체적인 내용을 상세히 설명한다. 도면에 관계없이 동일한 부재번호는 동일한 구성요소를 지칭하며, "및/또는"은 언급된 아이템들의 각각 및 하나 이상의 모든 조합을 포함한다.DETAILED DESCRIPTION Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings. Regardless of the drawings, the same reference numbers refer to the same components, and “and / or” includes each and every combination of one or more of the items mentioned.
비록 제1, 제2 등이 다양한 구성요소들을 서술하기 위해서 사용되나, 이들 구성요소들은 이들 용어에 의해 제한되지 않음은 물론이다. 이들 용어들은 단지 하나의 구성요소를 다른 구성요소와 구별하기 위하여 사용하는 것이다. 따라서, 이하에서 언급되는 제1 구성요소는 본 발명의 기술적 사상 내에서 제2 구성요소일 수도 있음은 물론이다.Although the first, second, etc. are used to describe various components, these components are of course not limited by these terms. These terms are only used to distinguish one component from another. Therefore, of course, the first component mentioned below may be a second component within the technical spirit of the present invention.
본 명세서에서 사용된 용어는 실시예들을 설명하기 위한 것이며 본 발명을 제한하고자 하는 것은 아니다. 본 명세서에서, 단수형은 문구에서 특별히 언급하지 않는 한 복수형도 포함한다. 명세서에서 사용되는 "포함한다(comprises)" 및/또는 "포함하는(comprising)"은 언급된 구성요소 외에 하나 이상의 다른 구성요소의 존재 또는 추가를 배제하지 않는다.The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. In this specification, the singular also includes the plural unless specifically stated otherwise in the phrase. As used herein, "comprises" and / or "comprising" does not exclude the presence or addition of one or more other components in addition to the mentioned components.
다른 정의가 없다면, 본 명세서에서 사용되는 모든 용어(기술 및 과학적 용어를 포함)는 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자에게 공통적으로 이해될 수 있는 의미로 사용될 수 있을 것이다. 또 일반적으로 사용되는 사전에 정의되어 있는 용어들은 명백하게 특별히 정의되어 있지 않는 한 이상적으로 또는 과도하게 해석되지 않는다.Unless otherwise defined, all terms (including technical and scientific terms) used in the present specification may be used in a sense that can be commonly understood by those skilled in the art. In addition, the terms defined in the commonly used dictionaries are not ideally or excessively interpreted unless they are specifically defined clearly.
공간적으로 상대적인 용어인 "아래(below)", "아래(beneath)", "하부(lower)", "위(above)", "상부(upper)" 등은 도면에 도시되어 있는 바와 같이 하나의 구성 요소와 다른 구성 요소들과의 상관관계를 용이하게 기술하기 위해 사용될 수 있다. 공간적으로 상대적인 용어는 도면에 도시되어 있는 방향에 더하여 사용시 또는 동작시 구성요소들의 서로 다른 방향을 포함하는 용어로 이해되어야 한다. 예를 들면, 도면에 도시되어 있는 구성요소를 뒤집을 경우, 다른 구성요소의 "아래(below)" 또는 "아래(beneath)"로 기술된 구성요소는 다른 구성요소의 "위(above)"에 놓여질 수 있다. 따라서, 예시적인 용어인 "아래"는 아래와 위의 방향을 모두 포함할 수 있다. 구성요소는 다른 방향으로도 배향될 수 있고, 이에 따라 공간적으로 상대적인 용어들은 배향에 따라 해석될 수 있다. The spatially relative terms " below ", " beneath ", " lower ", " above ", " upper " It can be used to easily describe a component's correlation with other components. Spatially relative terms are to be understood as including terms in different directions of components in use or operation in addition to the directions shown in the figures. For example, when flipping a component shown in the drawing, a component described as "below" or "beneath" of another component may be placed "above" the other component. Can be. Thus, the exemplary term "below" can encompass both an orientation of above and below. The components can be oriented in other directions as well, so that spatially relative terms can be interpreted according to the orientation.
이하, 첨부된 도면을 참조하여 본 발명의 바람직한 실시예를 상세히 설명하기로 한다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명에 따른 유기성 비료의 제조방법을 도시한 흐름도이다.1 is a flow chart showing a method for producing an organic fertilizer according to the present invention.
도 1을 참조하면, 본 발명에 따른 유기성 비료의 제조방법은 유기성 폐기물을 처리하여 주원료를 제조하는 단계를 포함한다(S110).Referring to Figure 1, the manufacturing method of the organic fertilizer according to the present invention includes the step of producing a main raw material by treating the organic waste (S110).
상기 유기성 폐기물은 음식물 쓰레기 슬러지, 축분 슬러지, 하수 슬러지, 바이오 가스 플랜트 슬러지 등을 의미하는 것으로, 다만, 본 발명에서 상기 유기성 폐기물의 종류를 제한하는 것은 아니다.The organic waste means food waste sludge, condensed sludge, sewage sludge, biogas plant sludge and the like, but the present invention does not limit the type of the organic waste.
유기성 폐기물을 처리하여 주원료는 제조하는 구체적인 방법에 대해서는 후술하기로 한다.A detailed method of preparing the main raw material by treating the organic waste will be described later.
다음으로, 본 발명에 따른 유기성 비료의 제조방법은 상기 주원료와 별도의 부원료를 혼합하여 함수조정제를 제조하는 단계를 포함한다(S120).Next, the method for producing an organic fertilizer according to the present invention includes the step of mixing the main raw material and a separate auxiliary raw material to prepare a water-conditioning agent (S120).
즉, 상기 S110 단계에서 제조된 주원료와 별도의 부원료를 이용하여, 본 발명에 따른 함수조정제를 제조할 수 있다.That is, using the main raw material manufactured in the step S110 and a separate auxiliary raw material, it is possible to manufacture a water-conditioning agent according to the present invention.
이때, 상기 부원료는 마사토, 황토, 미사, 생흙 등일 수 있으며, 다만, 본 발명에서 상기 부원료의 종류를 제한하는 것은 아니다.At this time, the secondary raw material may be masato, ocher, silt, raw soil, etc., but the type of the secondary raw material is not limited in the present invention.
상기 주원료와 별도의 부원료를 혼합하여 함수조정제를 제조하는 단계에 대해서는 후술하기로 한다.The step of preparing the water-adjusting agent by mixing the main raw material and the additional auxiliary material will be described later.
다음으로, 본 발명에 따른 유기성 비료의 제조방법은 상기 주원료와 상기 함수조정제를 혼합하여 혼합원료를 제조하는 단계를 포함한다(S130).Next, the method for producing an organic fertilizer according to the present invention includes the step of preparing a mixed raw material by mixing the main raw material and the water-containing regulator (S130).
즉, 상기 S110 단계에서 제조된 주원료와 S120 단계에서 제조된 함수조정제를 혼합하여, 본 발명에 따른 혼합원료를 제조할 수 있다.In other words, by mixing the main raw material prepared in step S110 and the water content regulator prepared in step S120, it is possible to produce a mixed raw material according to the present invention.
상기 주원료와 상기 함수조정제를 혼합하여 혼합원료를 제조하는 단계에 대해서는 후술하기로 한다.The step of preparing the mixed raw material by mixing the main raw material and the water-containing regulator will be described later.
다음으로, 본 발명에 따른 유기성 비료의 제조방법은 상기 혼합원료를 발효 및 숙성하여 유기성 비료를 제조하는 단계를 포함한다(S140).Next, the method for producing an organic fertilizer according to the present invention includes the step of producing an organic fertilizer by fermenting and ripening the mixed raw material (S140).
상기 혼합원료를 발효 및 숙성하는 것은 0 내지 70℃의 온도에서 3일 내지 10일 동안 후속조에서 발효 및 숙성하는 단계일 수 있으며, 다만, 상기 혼합원료의 양에 따라, 상기 숙성 온도 및 상기 숙성 시간은 적절히 조절할 수 있으며, 따라서, 본 발명에서 상기 숙성 온도 조건 및 상기 숙성 시간 조건을 제한하는 것은 아니다.Fermenting and aging the mixed raw material may be a step of fermenting and ripening in a subsequent bath for 3 to 10 days at a temperature of 0 to 70 ℃, except that, depending on the amount of the mixed raw material, the aging temperature and the aging The time can be adjusted appropriately, and therefore, the present invention does not limit the aging temperature condition and the aging time condition.
한편, 상기 발효 단계에서는 발효를 위한 호기성 미생물을 사용할 수 있으며, 상기 호기성 미생물은 스트렙토마이세스(Streptomyces), 써모액티노마이세테스(Thermoactinomycetes), 바실러스 세레우스(Bbacillus cereus), 아르카노박테리움 헤몰리티컴(Arcanobacterium haemolyticum), 락토바실러스 델브루엑키락티스(Lactobacillus delbrueckiilactis), 프로비덴시아 스투알티(Providencia stuartii), 스타필로코쿠스 클루시(Staphylococcus kloosi), 비브리오 헤몰리티쿠스(Vibrio haemolyticus)에서 선택되는 1종 이상의 미생물을 사용할 수 있으며, 다만, 본 발명에서 상기 호기성 미생물의 종류를 제한하는 것은 아니다.On the other hand, in the fermentation step can be used aerobic microorganisms for fermentation, the aerobic microorganisms are Streptomyces (Streptomyces), Thermoactinomycetes (Thermoactinomycetes), Bacillus cereus (Bbacillus cereus), Arcanobacterium he Arcanobacterium haemolyticum, Lactobacillus delbrueckiilactis, Providencia stuartii, Staphylococcus kloosi, Vibrio haemolyticus at Vibrio haemolyticus One or more microorganisms selected may be used, but the present invention does not limit the type of aerobic microorganisms.
이때 상기 유기성 비료의 함수율은 10% 내지 40%일 수 있고, 바람직하게는 15% 내지 30%일 수 있으며, 이러한 유기성 비료의 함수율은 상술한 주원료와 함수조정제의 혼합에 의해 제어될 수 있다.At this time, the water content of the organic fertilizer may be 10% to 40%, preferably 15% to 30%, the water content of the organic fertilizer can be controlled by the mixing of the above-described main raw material and the moisture control agent.
이하에서는 본 발명에 따른 유기성 비료의 제조방법의 각 단계를 상술하기로 한다.Hereinafter, each step of the manufacturing method of the organic fertilizer according to the present invention will be described in detail.
도 2는 본 발명에 따른 유기성 폐기물을 처리하여 주원료를 제조하는 단계를 설명하기 위한 흐름도이다.Figure 2 is a flow chart for explaining the step of producing a main raw material by treating the organic waste according to the present invention.
도 2를 참조하면, 본 발명에 따른 유기성 폐기물을 처리하여 주원료를 제조하는 단계는, 유기성 폐기물을 세척조에 투입하여 중량물을 제거하는 단계를 포함한다(S111).Referring to Figure 2, the step of preparing the main raw material by treating the organic waste in accordance with the present invention, comprising the step of removing the weight by putting the organic waste in the washing tank (S111).
상기 유기성 폐기물을 세척조에 투입하는 것은, 일정 양의 물이 함유된 컨테이너 또는 수조 등의 세척조에 유기성 폐기물을 투입하는 것으로, 딥핑 방식에 의하여 유기성 폐기물에서 유기성 물질을 선별하기 위한 공정에 해당한다.Injecting the organic waste into the washing tank, injecting the organic waste into a washing tank, such as a container or a water tank containing a certain amount of water, corresponds to a process for screening the organic material from the organic waste by a dipping method.
즉, 본 발명에서 딥핑 방식이라 함은 일정 량의 물이 함유된 컨테이너 또는 수조 등의 세척조에 유기성 폐기물을 투입하여, 비중차이에 의하여, 상기 유기성 폐기물에 포함된 부유물 또는 중량물을 제거하여, 유기성 물질만을 선별하기 위한 작업이다.That is, the dipping method in the present invention is to put organic waste into a washing tank, such as a container or a water tank containing a certain amount of water, by removing the floating matter or weight contained in the organic waste by the specific gravity difference, the organic material This is to sort out the bay.
상기 물이 함유된 컨테이너 또는 수조 등의 세척조에 유기성 폐기물을 투입하는 경우, 컨테이너 또는 수조의 하부로는 중량물인, 철제 제품, 유리 제품 등이 침전하게 되며, 컨테이너 또는 수조의 상부로는 비닐 제품, 플라스틱 제품 등과 같은 부유물이 부상하게 된다.When the organic waste is put into a washing tank such as a container or a water tank containing water, iron products, glass products, etc., which are heavy materials, are precipitated in the lower portion of the container or the water tank, and vinyl products, Floats such as plastic products may be floated.
즉, 본 S111단계에서는, 상술한 딥핑 방식에 의하여, 컨테이너 또는 수조 등의 세척조의 하부에 침전되는 중량물을 제거할 수 있다.That is, in the step S111, by the above-described dipping method, it is possible to remove the weight precipitated in the lower portion of the washing tank such as a container or a water tank.
이때, 상기 중량물을 제거하는 것은 기계적인 장치 또는 인력에 의해 제거할 수 있다.At this time, removing the weight can be removed by a mechanical device or a manpower.
다음으로, 중량물이 제거된 유기성 폐기물을 파쇄하는 단계를 포함한다(S112).Next, the step of crushing the organic waste from which the weight is removed (S112).
상술한 S111단계에서, 유기성 폐기물은, 유기성 물질 이외에도 중량물 및 부유물을 포함할 수 있음은 상술한 바와 같으며, S111단계를 통하여, 중량물을 제거할 수 있다.In the above-described step S111, the organic waste, as well as the organic material may include a heavy material and suspended matter as described above, through the step S111, the heavy material can be removed.
따라서, S112 단계에서, 중량물이 제거된 유기성 폐기물은 유기성 물질 및 부유물을 포함할 수 있다.Therefore, in step S112, the organic waste from which the weight is removed may include organic material and suspended solids.
즉, 유기성 물질과 부유물을 포함하는 유기성 폐기물은, 별도의 파쇄장치를 통해 파쇄됨으로써, 유기성 물질의 크기를 최소화할 수 있을 뿐만 아니라, 상기 부유물도 파쇄되어, 상기 부유물의 크기도 최소화될 수 있다.That is, the organic waste including the organic material and the suspended matter may be crushed through a separate crushing device, thereby minimizing the size of the organic material, and also crushing the suspended matter, thereby minimizing the size of the suspended matter.
이때, 비중 차이에 의하여, 상기 분쇄된 부유물은 물이 함유된 컨테이너 또는 수조 등의 저장조의 상부에 보다 용이하게 부상하게 된다.At this time, due to the difference in specific gravity, the pulverized suspended matter is more easily floated on the upper portion of the storage tank such as a container or a water tank containing water.
다음으로, 상기 파쇄된 유기성 폐기물로부터 부유물을 제거하는 단계를 포함한다(S113).Next, the step of removing the suspended matter from the crushed organic waste (S113).
즉, 상술한 바와 같이, S113단계에 의하여, 상기 분쇄된 부유물은 물이 함유된 컨테이너 또는 수조 등의 저장조의 상부에, 비중차이에 의하여, 보다 용이하게 부상하게 되며, 부상된 상기 분쇄된 부유물을 용이하게 제거할 수 있다.That is, as described above, by the step S113, the pulverized suspended matter is more easily floated on the upper portion of the storage tank such as a container or a water tank containing water, due to the specific gravity difference, the crushed suspended matter floated It can be easily removed.
이때, 상기 부유물을 제거하는 것은 기계적인 장치 또는 인력에 의해 제거할 수 있다.At this time, the removal of the suspended matter can be removed by a mechanical device or attraction.
한편, 상술한 S112단계에 의하여, 파쇄된 유기성 폐기물은 상술한 발효 및 숙성 단계에서, 보다 용이하게 발효 및 숙성될 수 있다.On the other hand, by the above-described step S112, the crushed organic waste can be fermented and aged more easily in the above-described fermentation and ripening step.
다음으로, 상기 부유물이 제거된 유기성 폐기물을 분해하여 예비 주원료를 제조하는 단계를 포함한다(S114).Next, a step of preparing a preliminary main raw material by decomposing the organic waste from which the suspended matter is removed (S114).
상기 유기성 폐기물을 분해함에 있어서, 본 발명에서는 호기성 미생물을 사용할 수 있으며, 상기 호기성 미생물은 스트렙토마이세스(Streptomyces), 써모액티노마이세테스(Thermoactinomycetes), 바실러스 세레우스(Bbacillus cereus), 아르카노박테리움 헤몰리티컴(Arcanobacterium haemolyticum), 락토바실러스 델브루엑키락티스(Lactobacillus delbrueckiilactis), 프로비덴시아 스투알티(Providencia stuartii), 스타필로코쿠스 클루시(Staphylococcus kloosi), 비브리오 헤몰리티쿠스(Vibrio haemolyticus)에서 선택되는 1종 이상의 미생물을 사용할 수 있으며, 다만, 본 발명에서 상기 호기성 미생물의 종류를 제한하는 것은 아니다.In decomposing the organic waste, aerobic microorganisms may be used in the present invention, and the aerobic microorganisms may include Streptomyces, Thermoactinomycetes, Bacillus cereus, and Arcanobacte. Arcanobacterium haemolyticum, Lactobacillus delbrueckiilactis, Providencia stuartii, Staphylococcus kloosi, Vibrio haemolyticus One or more microorganisms selected from) may be used, but the present invention does not limit the type of aerobic microorganisms.
다음으로, 상기 예비 주원료를 제1약품처리하는 단계를 포함한다(S115).Next, the first main material processing the preliminary main raw material includes a step (S115).
상기 제1약품처리하는 단계는 무기성 반응재를 사용할 수 있으며, 상기 무기성 반응재는 석회(CaO)일 수 있다.The first chemical treatment may use an inorganic reactant, and the inorganic reactant may be lime (CaO).
상기 석회는 횟돌이나 백악, 조개껍질 따위의 석회석을 태워 이산화탄소를 제거하여 얻는 생석회와 생석회에 물을 부어 얻는 소석회를 통틀어 이르는 것으로, 산화칼슘에 물을 가하여 얻는 흰색의 염기성 가루를 의미하기도 한다.The lime is a limestone obtained by burning limestone such as ash, chalk, and shells, and limestone obtained by pouring water into quicklime, and also means white basic powder obtained by adding water to calcium oxide.
이때, 상기 석회가 물에 녹아 포화되면 석회수가 되며, 값싼 공업용 염기로서, 암모니아 발생, 탄산나트륨의 가성화, 부식제 등으로 널리 쓰이고, 모르타르 등의 건축 재료, 산성 토양의 중화제로도 사용되고 있는 공지된 물질이다.At this time, when the lime is dissolved in water and saturated, it becomes lime water, and it is a cheap industrial base, which is widely used as ammonia generation, sodium causticization, caustic, etc. to be.
상기 제1약품처리하는 단계는, 상기 예비 주원료에 포함된 염분을 제거하기 위한 것으로, 상기 예비 주원료에 제1약품처리 하는 경우, 상기 제1약품과 상기 예비 주원료가 반응하여, 일정 침전물이 발생하게 된다.The step of treating the first drug is to remove the salt contained in the preliminary main material, when the first drug treatment on the preliminary main raw material, the first drug and the preliminary main raw material react, so that a certain precipitate is generated. do.
따라서, 본 발명에서는 상기 예비 주원료를 제1약품처리하는 단계 이후, 상기 제1약품 처리에 의해 발생된 침전물을 제거하는 단계를 더 포함하는 것이 바람직하다.Therefore, the present invention preferably further comprises the step of removing the precipitate generated by the first drug treatment, after the first drug treatment of the preliminary main raw material.
상기 발생된 침전물을 제거하는 것은, 기계적인 장치 또는 인력에 의해 제거할 수 있다.Removing the generated precipitate can be removed by a mechanical device or attraction.
한편, 상기 무기성 반응재는 상기 예비 주원료 100 중량부 대비 2 내지 5 중량부를 포함할 수 있으며, 상기 무기성 반응재의 성분으로 인해, 상기 예비 주원료는 발열 반응이 이루어지면서, 악취가 제거됨과 함께 수분 함량을 줄일 수 있고, 특히, 상술한 바와 같이, 예비 주원료에 포함된 염분을 제거할 수 있다.On the other hand, the inorganic reactant may include 2 to 5 parts by weight relative to 100 parts by weight of the preliminary main raw material, due to the components of the inorganic reactant, the preliminary main raw material is exothermic reaction, the odor is removed and the moisture content In particular, as described above, the salt contained in the preliminary main raw material can be removed.
이러한 염분을 포함한 상태로 유기성 비료를 제조하고, 제조된 유기성 비료를 토양에 사용하는 경우, 상기 염분이 토양에 흡수되고 계속적으로 축적됨으로써, 토양 오염이 심각해지게 된다.When the organic fertilizer is manufactured in the state containing such a salt, and the prepared organic fertilizer is used in the soil, the salt is absorbed into the soil and accumulated continuously, resulting in serious soil contamination.
따라서, 본 발명에서는 상기 제1약품처리에 의해 예비 주원료에 포함된 염분을 제거할 수 있다. Therefore, in the present invention, the salt contained in the preliminary main raw material can be removed by the first chemical treatment.
다음으로, 상기 제1약품처리된 예비 주원료를 제2약품처리하는 단계를 포함한다(S116).Next, a second drug treatment of the first drug-treated preliminary main raw material includes a step (S116).
상기 제2약품처리하는 단계는 응집제를 사용할 수 있으며, 상기 응집제는 공지된 유기 응집제 또는 무기 응집제를 사용할 수 있으며, 상기 예비 주원료의 양에 따라 적절히 포함함으로써, 상기 예비 주원료를 응집시킬 수 있다.The second chemical treatment step may use a flocculant, the flocculant may use a known organic flocculant or inorganic flocculant, and by appropriately included in accordance with the amount of the preliminary main raw material, it is possible to aggregate the preliminary main raw material.
예를 들어, 상기 응집제로는 철 또는 알루미늄을 함유하는 것으로서 황산제일철(Fe(SO4)), 황산제이철(Fe2(SO4)3), 황산알루미늄(Al2(SO4)3), 염화제일철(FeCl2), 염화제이철(FeCl3)에서 선택된 것을 사용할 수 있으며, 첨가량은 0.05 내지 2 중량%를 첨가할 수 있으며, 다만, 본 발명에서 상기 응집제의 종류 및 첨가량을 제한하는 것은 아니다.For example, the flocculant includes iron or aluminum, and ferrous sulfate (Fe (SO 4 )), ferric sulfate (Fe 2 (SO 4 ) 3 ), aluminum sulfate (Al 2 (SO 4 ) 3 ), chloride It may be selected from ferrous iron (FeCl 2 ), ferric chloride (FeCl 3 ), the addition amount may be added to 0.05 to 2% by weight, but does not limit the type and amount of the flocculant in the present invention.
다음으로, 상기 제2약품처리된 예비주원료를 침전시키는 단계(S117)를 포함하며, 상기 침전된 예비 주원료를 건조하여 주원료를 제조하는 단계(S118)를 거쳐 본 발명에 따른 주원료를 제조할 수 있다.Next, the step of precipitating the second drug-treated preliminary raw material (S117), and drying the precipitated preliminary main raw material through the step (S118) of manufacturing a main raw material can be prepared according to the present invention. .
이때, 상기 주원료의 함수율은 80 내지 85% 정도에 해당할 수 있다.At this time, the moisture content of the main raw material may correspond to about 80 to 85%.
이상에서 살펴본 바와 같이, 본 발명에서 주원료를 제조하는 단계는 유기성 폐기물을 처리하여 제조할 수 있다.As described above, the step of preparing the main raw material in the present invention can be produced by treating the organic waste.
후술할 바와 같이, 본 발명에서는 이러한 주원료를 이용하여 유기성 비료를 제조하며, 따라서, 본 발명에 따른 주원료를 제조하는 단계가 유기성 폐기물을 처리하는 단계로 이해될 수 있다.As will be described later, in the present invention, an organic fertilizer is prepared using such a main raw material, and thus, the step of preparing the main raw material according to the present invention may be understood as treating the organic waste.
이하에서는 주원료를 제조하는 단계, 달리 표현하면, 유기성 폐기물을 처리하는 단계에서의 유기성 폐기물 처리 장치를 설명하기로 한다.Hereinafter, the organic waste treatment apparatus in the step of preparing the main raw material, in other words, treating the organic waste will be described.
즉, 본 발명에서는 주원료를 제조하는 장치가 유기성 폐기물 처리 장치에 해당한다.That is, in the present invention, the apparatus for producing the main raw material corresponds to the organic waste treatment apparatus.
도 3는 본 발명에 따른 유기성 폐기물 처리장치를 설명하기 위한 개략적인 도면이며, 도 4는 본 발명에 따른 유기성 폐기물 처리장치에서의 비중 분리부를 설명하기 위한 개략적인 도면이다.3 is a schematic view for explaining the organic waste treatment apparatus according to the present invention, Figure 4 is a schematic view for explaining the specific gravity separation unit in the organic waste treatment apparatus according to the present invention.
먼저, 도 3를 참조하면, 본 발명에 따른 유기성 폐기물 처리장치(100)는 유기성 폐기물로부터 중량물을 제거하기 위한 비중 분리부(110)를 포함하고, 상기 비중 분리부(110)로부터 중량물이 제거된 유기성 폐기물을 분해하기 위한 예비 주원료 제조부(120)를 포함하며, 상기 예비 주원료를 약품처리하여 주원료를 제조하기 위한 주원료 제조부(130)를 포함한다.First, referring to FIG. 3, the organic waste treating apparatus 100 according to the present invention includes a specific gravity separating unit 110 for removing a heavy substance from the organic waste, and removes the heavy substance from the specific gravity separating unit 110. It includes a preliminary main raw material manufacturing unit 120 for decomposing organic waste, and includes a main raw material manufacturing unit 130 for manufacturing a main raw material by chemical treatment of the preliminary main raw material.
보다 구체적으로, 상기 비중 분리부(110)는 유기성 폐기물이 투입되는 세척조(112) 및 상기 세척조의 하부 일정 영역에 위치하는 중량물 수집부(111)를 포함한다.More specifically, the specific gravity separating unit 110 includes a washing tank 112 into which the organic waste is input and a heavy material collecting unit 111 positioned in a predetermined lower region of the washing tank.
상기 세척조(112)는 딥핑 방식에 의하여 유기성 폐기물에서 유기성 물질을 선별하기 위한 것으로, 상기 세척조(112)에는 일정 양의 유기성 폐기물과 함께 일정 양의 물이 투입된다.The washing tank 112 is for sorting organic materials from organic waste by a dipping method, and the washing tank 112 is filled with a predetermined amount of water together with a predetermined amount of organic waste.
즉, 본 발명에서는 딥핑 방식에 의해 유기성 폐기물에서 유기성 물질을 선별하는 것을 특징으로 하는 것으로, 도 4에 도시된 바와 같이, 비중 분리부(110)의 최상부에는 부유물(11)이 위치하고, 비중 분리부(110)의 최하부에는 중량물(13)이 위치하며, 비중 분리부(110)의 중간부에는 유기성 물질(12)이 위치함에 의하여, 비중에 다라, 부유물, 유기성 물질 및 중량물을 분리할 수 있다. That is, the present invention is characterized in that the organic material is selected from the organic waste by the dipping method, as shown in Figure 4, the top portion of the specific gravity separation unit 110, the floating material 11 is located, the specific gravity separation unit The lower part of the 110, the heavy material 13 is located, the organic material 12 is located in the middle of the specific gravity separation unit 110, depending on the specific gravity, it is possible to separate the suspended matter, organic material and heavy material.
즉, 상기 물이 함유된 컨테이너 또는 수조 등의 세척조(112)에 유기성 폐기물을 투입하는 경우, 하부의 중량물 수집부(111)에 중량물인, 철제 제품, 유리 제품 등이 침전하게 되며, 세척조(112)의 상부에는 비닐 제품, 플라스틱 제품 등과 같은 부유물이 부상하게 된다.That is, when the organic waste is put into a washing tank 112 such as a container or a water tank containing water, iron products, glass products, etc., which are heavy products, are precipitated in the lower weight collection unit 111, and the washing tank 112 is disposed. At the top of the) floats such as vinyl products, plastic products, etc. are floated.
계속해서, 도 3을 참조하면, 상기 세척조(112)의 일정 영역에는 유기성 폐기물과 물의 혼합을 용이하게 하기 위한 제1혼합장치(113)를 포함할 수 있으며, 다만, 본 발명에서 상기 제1혼합장치(113)의 유무를 제한하는 것은 아니다.Subsequently, referring to FIG. 3, a predetermined region of the washing tank 112 may include a first mixing device 113 for facilitating mixing of organic waste and water, provided that the first mixing in the present invention. It does not limit the presence or absence of the device 113.
또한, 상기 세척조(112)의 일정 영역에는 중량물이 제거된 유기성 폐기물, 보다 구체적으로 유기성 물질을 배출하기 위한 유기성 물질 배출구(114)를 포함하며, 상기 중량물 수집부(111)의 일정 영역에는 상기 중량물을 배출하기 위한 중량물 배출구(115)를 포함할 수 있다.In addition, the predetermined region of the washing tank 112 includes an organic material outlet 114 for discharging the organic waste from which the heavy material is removed, more specifically, the organic material, and the heavy material in the predetermined region of the heavy material collection unit 111. It may include a heavy discharge outlet 115 for discharging.
또한, 상기 유기성 물질 배출구(114)와 연결되는 유기성 물질 이동 경로(116)를 포함하고, 상기 중량물 배출구(115)와 연결되는 중량물 이동 경로(117)를 포함할 수 있다.In addition, the organic material discharge path 114 may include an organic material movement path 116 connected to the organic matter discharge path 115, and may include a heavy material movement path 117 connected to the weight discharge port 115.
이때, 상기 유기성 물질 이동 경로(116) 및 상기 중량물 이동 경로(117)는 예비 주원료 제조부(120)의 일정 영역과 연결될 수 있다.In this case, the organic material movement path 116 and the heavy material movement path 117 may be connected to a predetermined region of the preliminary main raw material manufacturing unit 120.
계속해서, 도 3을 참조하면, 상기 예비 주원료 제조부(120)는 중량물이 제거된 유기성 폐기물을 파쇄하기 위한 파쇄부(121)를 포함한다.Subsequently, referring to FIG. 3, the preliminary main raw material manufacturing unit 120 includes a crushing unit 121 for crushing the organic waste from which the heavy material is removed.
이때, 상기 유기성 물질 이동 경로(116)는 파쇄부(121)와 연결되며, 즉, 유기성 물질 이동 경로를 통해, 중량물이 제거된 유기성 폐기물이 파쇄부(121)로 전달될 수 있다.In this case, the organic material movement path 116 is connected to the crushing unit 121, that is, the organic waste from which the heavy material is removed may be transferred to the crushing unit 121 through the organic material moving path.
상술한 바와 같이, 유기성 폐기물은, 유기성 물질 이외에도 중량물 및 부유물을 포함할 수 있음은 상술한 바와 같으며, 상기 비중 분리부에 의해 중량물을 제거할 수 있다.As described above, the organic waste may include heavy materials and suspended solids in addition to organic materials, and the heavy materials may be removed by the specific gravity separation unit.
따라서, 중량물이 제거된 유기성 폐기물은 유기성 물질 및 부유물을 포함할 수 있다.Thus, the organic waste from which the weight has been removed may include organic material and suspended solids.
즉, 유기성 물질과 부유물을 포함하는 유기성 폐기물은, 상기 파쇄부(121)를 통해 파쇄됨으로써, 유기성 물질의 크기를 최소화할 수 있을 뿐만 아니라, 상기 부유물도 파쇄되어, 상기 부유물의 크기도 최소화될 수 있다.That is, the organic waste including the organic material and the suspended matter may be crushed through the crushing unit 121, so that not only the size of the organic material may be minimized, but also the suspended matter may be crushed, thereby minimizing the size of the suspended matter. have.
또한, 상기 예비 주원료 제조부(120)는 상기 파쇄부(121)의 하부에 위치하는 부유물 제거부(127)를 포함하며, 상기 부유물 제거부(127)에서 상기 부유물이 제거될 수 있다.In addition, the preliminary main raw material manufacturing unit 120 includes a floating material removing unit 127 positioned below the crushing unit 121, and the floating material may be removed from the floating material removing unit 127.
이때, 비중 차이에 의하여, 상기 분쇄된 부유물은 물이 함유된 컨테이너 또는 수조 등의 저장조의 상부에 보다 용이하게 부상하게 된다.At this time, due to the difference in specific gravity, the pulverized suspended matter is more easily floated on the upper portion of the storage tank such as a container or a water tank containing water.
또한, 상기 예비 주원료 제조부(120)는 상기 부유물 제거부(127)의 일측에 위치하는 부유물 컨테이너(122)를 포함하며, 즉, 상기 부유물 제거부(127)에서 제거된 부유물은 상기 부유물 컨테이너(122)에 투입되어, 최종적으로 부유물 배출부(126)를 통해 배출되게 된다.In addition, the preliminary main raw material manufacturing unit 120 includes a float container 122 located on one side of the float removing unit 127, that is, the float removed from the float removing unit 127 is the float container ( 122, it is finally discharged through the float discharge portion (126).
한편, 상술한 바와 같이, 상기 중량물 이동 경로(117)는 예비 주원료 제조부(120)의 일정 영역과 연결되는데, 보다 구체적으로, 상기 중량물 이동 경로(117)는 상기 부유물 컨테이너(122)와 연결될 수 있다.On the other hand, as described above, the heavy material movement path 117 is connected to a predetermined region of the preliminary main raw material manufacturing unit 120, more specifically, the heavy material movement path 117 may be connected to the floating container 122. have.
즉, 상기 중량물 이동 경로(117)를 통해 이동되는 중량물은 상기 부유물 컨테이너(122)에 투입되어, 최종적으로 부유물 배출부(126)를 통해 배출되게 된다.That is, the heavy material moved through the heavy material movement path 117 is introduced into the floating container 122, and finally discharged through the floating material discharge part 126.
계속해서, 도 3을 참조하면, 상기 예비 주원료 제조부(120)는 상기 부유물 제거부(127)의 하부 영역에 위치하고, 상기 유기성 물질을 분해하기 위한 분해조(123)를 포함한다.Subsequently, referring to FIG. 3, the preliminary main raw material manufacturing unit 120 is located in the lower region of the floating material removing unit 127 and includes a decomposition tank 123 for decomposing the organic material.
즉, 본 발명에서는 상기 부유물이 제거된 유기성 폐기물, 즉, 유기성 물질을 분해하여 예비 주원료를 제조하는데, 상기 분해조(123)에서 상기 유기성 물질을 분해하여 예비 주원료를 제조 및 저장할 수 있다.That is, in the present invention, the organic waste from which the suspended matter is removed, that is, the organic material is decomposed to prepare a preliminary main raw material, and the preliminary main raw material may be prepared and stored by decomposing the organic material in the decomposition tank 123.
상술한 바와 같이, 상기 유기성 물질을 분해함에 있어서, 본 발명에서는 호기성 미생물을 사용할 수 있으며, 상기 호기성 미생물은 스트렙토마이세스(Streptomyces), 써모액티노마이세테스(Thermoactinomycetes), 바실러스 세레우스(Bbacillus cereus), 아르카노박테리움 헤몰리티컴(Arcanobacterium haemolyticum), 락토바실러스 델브루엑키락티스(Lactobacillus delbrueckiilactis), 프로비덴시아 스투알티(Providencia stuartii), 스타필로코쿠스 클루시(Staphylococcus kloosi), 비브리오 헤몰리티쿠스(Vibrio haemolyticus)에서 선택되는 1종 이상의 미생물을 사용할 수 있으며, 다만, 본 발명에서 상기 호기성 미생물의 종류를 제한하는 것은 아니다.As described above, in the decomposition of the organic material, aerobic microorganisms can be used in the present invention, the aerobic microorganisms are Streptomyces, Thermoactinomycetes, Bacillus cereus ), Arcanobacterium haemolyticum, Lactobacillus delbrueckiilactis, Providencia stuartii, Staphylococcus kloosi, Vibrio hemolytic One or more microorganisms selected from Tibrio haemolyticus may be used, but the present invention does not limit the type of aerobic microorganisms.
또한, 상기 분해조(123)에 저장된 예비 주원료를 이동시키기 위한 예비 주원료 이동수단(124) 및 상기 예비 주원료 이동수단(124)에 의해 예비 주원료를 이동시키기 위한 예비 주원료 이동 경로(125)를 더 포함할 수 있다. In addition, the preliminary main raw material moving means 124 for moving the preliminary main raw material stored in the decomposition tank 123 and the preliminary main raw material moving path 125 for moving the preliminary main raw material by the preliminary main raw material moving means 124 are further included. can do.
이때, 상기 예비 주원료 이동 경로(125)는 상기 주원료 제조부(130)의 일정 영역과 연결될 수 있다.In this case, the preliminary main raw material movement path 125 may be connected to a predetermined region of the main raw material manufacturing unit 130.
한편, 상기 분해조(123)는 물 배출 경로를 더 포함할 수 있으며, 도면에 도시된 바와 같이, 비중 분리부(110)를 통해 파쇄부(121)를 거쳐 분해조(123)에 유입된 물은 상기 물 배출 경로를 통해, 다시 비중 분리부(110)로 공급될 수 있다.On the other hand, the decomposition tank 123 may further include a water discharge path, as shown in the figure, the water introduced into the decomposition tank 123 via the crushing unit 121 through the specific gravity separation unit 110. May be supplied to the specific gravity separator 110 again through the water discharge path.
계속해서, 도 3을 참조하면, 상기 주원료 제조부(130)는 예비 주원료를 제1약품처리 하기 위한 제1약품 처리부(131)를 포함하며, 상기 제2약품 처리부(131)와 연결되고, 상기 예비 주원료를 제2약품처리하기 위한 제2약품 처리부(132)를 포함한다.Subsequently, referring to FIG. 3, the main raw material manufacturing unit 130 includes a first drug processing unit 131 for processing the first main material of the preliminary drug and is connected to the second drug processing unit 131. It includes a second drug processing unit 132 for processing the second main material preliminary.
이때, 상기 예비 주원료 이동 경로(125)는 상기 제1약품 처리부(131)와 연결되며, 즉, 예비 주원료 이동 경로를 통해, 예비 주원료가 제1약품 처리부(131)로 전달될 수 있다.In this case, the preliminary main raw material moving path 125 is connected to the first drug processing unit 131, that is, the preliminary main raw material may be transferred to the first drug processing unit 131 through the preliminary main raw material moving path.
상술한 바와 같이, 상기 제1약품처리하는 단계는 무기성 반응재를 사용할 수 있으며, 상기 무기성 반응재는 석회(CaO)일 수 있다.As described above, the step of treating the first drug may use an inorganic reactant, and the inorganic reactant may be lime (CaO).
상기 제1약품처리하는 단계는, 상기 예비 주원료에 포함된 염분을 제거하기 위한 것으로, 상기 예비 주원료에 제1약품처리 하는 경우, 상기 제1약품과 상기 예비 주원료가 반응하여, 일정 침전물이 발생하게 된다.The step of treating the first drug is to remove the salt contained in the preliminary main material, when the first drug treatment on the preliminary main raw material, the first drug and the preliminary main raw material react, so that a certain precipitate is generated. do.
이에 따라, 본 발명에서는 상기 예비 주원료를 제1약품처리하는 단계 이후, 상기 제1약품 처리에 의해 발생된 침전물을 제거하는 단계를 더 포함할 수 있다.Accordingly, the present invention may further include the step of removing the precipitate generated by the first drug treatment, after the first drug treatment of the preliminary main raw material.
따라서, 본 발명에 따른 주원료 제조부(130)는 상기 제1약품 처리부(131)의 하부 일정 영역에 위치하는 침전부(137)를 포함할 수 있으며, 즉, 상기 제1약품 처리부(131)에서 발생된 침전물은 상기 침전부(137)에 수집되어, 최종적으로 침전물 배출부(138)를 통해 배출될 수 있다.Therefore, the main raw material manufacturing unit 130 according to the present invention may include a precipitation unit 137 located in a predetermined lower region of the first drug processing unit 131, that is, in the first drug processing unit 131 The generated sediment may be collected in the sedimentation unit 137 and finally discharged through the sediment discharge unit 138.
또한, 상기 제1약품처리된 예비 주원료를 제2약품처리하는 단계는 응집제를 사용할 수 있으며, 이는 상술한 바와 같으므로, 이하 구체적인 설명은 생략하기로 한다.In addition, the second drug treatment of the first drug-treated preliminary main raw material may be a flocculant, which is the same as described above, and thus the detailed description thereof will be omitted.
한편, 상기 제1약품 처리부(131)의 일정 영역에는 예비 주원료와 제1약품의 혼합을 용이하게 하기 위한 제2혼합장치(135)를 포함할 수 있고, 상기 제2약품 처리부(132)의 일정 영역에는 제1약품 처리된 예비 주원료와 제2약품의 혼합을 용이하게 하기 위한 제3혼합장치(136)를 포함할 수 있으며, 다만, 본 발명에서 상기 제2혼합장치(135) 및 상기 제3혼합장치(136)의 유무를 제한하는 것은 아니다.On the other hand, a predetermined region of the first drug processing unit 131 may include a second mixing device 135 for facilitating mixing of the preliminary main raw material and the first drug, the schedule of the second drug processing unit 132 The region may include a third mixing device 136 for facilitating mixing of the first drug-treated preliminary raw material and the second drug, provided that the second mixing device 135 and the third in the present invention. The presence or absence of the mixing device 136 is not limited.
계속해서, 도 3을 참조하면, 상기 주원료 제조부(130)는 상기 제2약품 처리부(132)와 연결되는 침전조(133)를 포함한다.Subsequently, referring to FIG. 3, the main raw material manufacturing unit 130 includes a precipitation tank 133 connected to the second chemical processing unit 132.
즉, 상술한 바와 같이, 본 발명에서는 상기 제2약품처리된 예비주원료를 침전시키는 단계를 포함하며, 상기 침전조에 제2약품처리된 예비주원료가 침전 및 저장됨으로써, 본 발명에 따른 주원료를 제조할 수 있다.That is, as described above, the present invention includes the step of precipitating the second drug-treated preliminary raw material, by precipitating and storing the second drug-treated preliminary raw material in the precipitation tank, to prepare a main raw material according to the present invention Can be.
한편, 상기 주원료가 침전 및 저장된 침전조로부터 상기 주원료를 이동시키기 위한 주원료 이동수단(134)을 더 포함할 수 있으며, 상기 주원료 이동수단(134)에 의해 상기 주원료는 다음 단계의 장치로 이송될 수 있다.On the other hand, the main raw material may further include a main raw material moving means 134 for moving the main raw material from the settling tank and settled, the main raw material moving means 134 may be transferred to the device of the next step .
이때, 상기 주원료의 함수율은 80 내지 85% 정도에 해당하는 것이 바람직하며, 상기 침전조(133)에 침전 및 저장된 상기 주원료의 함수율이 이러한 범위를 충족하지 않는 경우, 별도의 건조수단에 의해, 상기 주원료를 건조시킬 수 있다.At this time, the water content of the main raw material is preferably equivalent to about 80 to 85%, when the water content of the main raw material precipitated and stored in the precipitation tank 133 does not meet this range, by a separate drying means, the main raw material Can be dried.
한편, 상기 침전조(133)는 물 배출 경로를 더 포함할 수 있으며, 도면에 도시된 바와 같이, 비중 분리부(110)를 통해 파쇄부(121)를 거쳐 분해조(123)에 유입되고, 이후, 제1약품처리부(131) 및 제2약품처리부(132)를 거쳐 침전조(133)에 물은 상기 물 배출 경로를 통해, 다시 비중 분리부(110)로 공급될 수 있다.On the other hand, the settling tank 133 may further include a water discharge path, as shown in the figure, is introduced into the decomposition tank 123 via the crushing unit 121 through the specific gravity separation unit 110, after In addition, the water may be supplied to the specific gravity separating unit 110 through the water discharge path through the water discharge path through the first chemical treatment unit 131 and the second chemical treatment unit 132.
이상과 같은 유기성 폐기물 처리 장치를 통해, 본 발명에서는 상술한 주원료를 제조할 수 있다.Through the above organic waste treatment apparatus, the above-described main raw material can be produced in the present invention.
따라서, 본 발명에서는 상기 유기성 폐기물 처리 장치를 통해, 유기성 폐기물 자원의 재활용화가 가능하다.Therefore, in the present invention, through the organic waste treatment apparatus, it is possible to recycle the organic waste resources.
이하에서는, 본 발명에 따른 유기성 비료의 제조방법의 각 단계를 계속적으로 상술하기로 한다.Hereinafter, each step of the manufacturing method of the organic fertilizer according to the present invention will be described in detail continuously.
도 5는 본 발명에 따른 함수 조정제를 제조하는 단계를 설명하기 위한 흐름도이다.5 is a flow chart for explaining the steps of producing a water modifier according to the present invention.
도 5를 참조하면, 본 발명에 따른 함수 조정제를 제조하는 단계는, 주원료를 제조하는 단계를 포함한다(S121).Referring to FIG. 5, the step of preparing the water-containing regulator according to the present invention includes preparing a main raw material (S121).
상기 주원료를 제조하는 단계(S121)는 상술한 도 2의 단계를 통해 제조될 수 있으며, 즉, 본 발명에서는 함수 조정제를 제조함에 있어서, 주원료를 사용할 수 있다.The manufacturing of the main raw material (S121) may be prepared through the above-described step of FIG. 2, that is, in the present invention, the main raw material may be used in preparing the water-containing regulator.
다음으로, 본 발명에 따른 함수 조정제를 제조하는 단계는, 부원료를 제조하는 단계를 포함한다(S122).Next, the step of preparing a water-containing regulator according to the present invention includes the step of preparing a subsidiary material (S122).
상기 부원료는 마사토, 황토, 미사, 생흙 등을 포함할 수 있으며, 이들을 단독 또는 혼합하여 건조함으로써, 상기 부원료를 제조할 수 있다.The subsidiary materials may include masato, ocher, silt, raw soil, and the like, and the subsidiary materials may be manufactured by drying them alone or by mixing them.
이때 상기 부원료의 함수율은 10% 내지 20%일 수 있으며, 바람직하게는 15%일 수 있다.In this case, the water content of the sub-material may be 10% to 20%, preferably 15%.
다음으로, 본 발명에 따른 함수 조정제를 제조하는 단계는, 상기 주원료와 상기 부원료를 혼합하는 단계를 포함한다.Next, the step of preparing a water-containing regulator according to the invention, the step of mixing the main raw material and the sub-material.
이때, 상기 부원료는 상기 주원료 100 중량부 대비 40 내지 60 중량부일 수 있으며, 상기 부원료의 첨가량은 주원료의 첨가량 및 함수율에 따라 적절히 배합할 수 있으며, 보다 바람직하게는 후술하는 건조단계에 의해 제조된 함수 조정제의 함수율이 10% 내지 20%가 될 수 있도록 제어할 수 있는 적절한 양을 선택할 수 있다.In this case, the secondary raw material may be 40 to 60 parts by weight relative to 100 parts by weight of the main raw material, the amount of the auxiliary raw material may be appropriately blended according to the addition amount and the water content of the main raw material, more preferably a function prepared by the drying step described below An appropriate amount can be selected to control so that the water content of the modifier can be 10% to 20%.
다음으로, 본 발명에 따른 함수 조정제를 제조하는 단계는, 상기 혼합된 주원료와 부원료를 건조하여 함수 조정제를 제조하는 단계를 포함한다(S124).Next, the step of preparing a water-containing regulator according to the present invention, the step of drying the mixed main and secondary raw materials to prepare a water-containing regulator (S124).
이때 상기 함수 조정제의 함수율은 10% 내지 20%일 수 있고, 바람직하게는 15%일 수 있으며, 상기 함수 조정제를 통하여, 후술하는 혼합원료의 함수율을 용이하게 제어할 수 있다.At this time, the water content of the water content regulator may be 10% to 20%, preferably 15%, and through the water content adjustment agent, it is possible to easily control the water content of the mixed raw material to be described later.
한편, 상술한 바와 같이, 본 발명에 따른 함수 조정제는 후술하는 혼합원료, 즉, 유기성 비료를 제조하기 위한 혼합원료에서의 주원료를 사용하여 제조되는 것으로, 함수 조정제에 포함된 주원료의 경우도, 결국, 혼합원료에서의 주원료로 기능할 수 있으므로, 상기 함수 조정제는 유기성 비료의 함수양을 제어할 수 있을 뿐만 아니라, 그 자체로도 유기성 비료의 일부가 될 수 있다.On the other hand, as described above, the water-containing regulator according to the present invention is manufactured by using the main raw material in the mixed raw material, that is, the mixed raw material for producing the organic fertilizer described later, even in the case of the main raw material contained in the water-containing regulator In addition, since it can function as the main raw material in the mixed raw material, the water-containing regulator can not only control the water content of the organic fertilizer, but also can be part of the organic fertilizer by itself.
즉, 본 발명에 따른 함수조정제는 함수양을 제어할 뿐만아니라, 유기성 비료에서의 유기 물질의 양을 제어할 수 있다.That is, the water-containing modifier according to the present invention can not only control the amount of water, but also control the amount of organic substances in the organic fertilizer.
도 6은 본 발명에 따른 혼합원료를 제조하는 단계를 설명하기 위한 흐름도이다.6 is a flow chart for explaining the step of producing a mixed raw material according to the present invention.
도 6을 참조하면, 본 발명에 따른 혼합원료를 제조하는 단계는, 주원료를 제조하는 단계를 포함한다(S131).Referring to FIG. 6, the step of preparing the mixed raw material according to the present invention includes preparing a main raw material (S131).
상기 주원료를 제조하는 단계(S131)는 상술한 도 2의 단계를 통해 제조될 수 있으며, 즉, 본 발명에서는 혼합원료를 제조함에 있어서, 함수 조정제를 제조하기 위한 주원료와 동일한 주원료를 사용할 수 있다.The manufacturing of the main raw material (S131) may be manufactured through the above-described step of FIG. 2. That is, in the present invention, in preparing the mixed raw material, the same main raw material as the main raw material for preparing the water-containing regulator may be used.
다음으로, 본 발명에 따른 혼합원료를 제조하는 단계는, 함수 조정제를 제조하는 단계를 포함한다(S132).Next, the step of preparing the mixed raw material according to the present invention includes the step of preparing a water-containing regulator (S132).
상기 함수 조정제를 제조하는 단계(S132)는 상술한 도 5의 단계를 통해 제조될 수 있으며, 즉, 본 발명에서는 함수 조정제를 제조함에 있어서, 본 단계의 혼합원료를 제조하기 위한 주원료와 동일한 주원료를 사용할 수 있다.The step (S132) of preparing the water modifier may be prepared through the above-described step of FIG. 5, that is, in the present invention, in preparing the water modifier, the same main raw material as the main material for preparing the mixed raw material of this step is used. Can be used.
다음으로, 본 발명에 따른 혼합원료를 제조하는 단계는, 상기 주원료와 상기 함수 조정제를 혼합하는 단계를 포함할 수 있다(S133).Next, the step of preparing the mixed raw material according to the present invention may include mixing the main raw material and the water-containing regulator (S133).
상기 함수 조정제는 상기 주원료의 함수를 조절하기 위한 것으로, 상기 주원료 100 중량부 대비 40 내지 60 중량부를 포함할 수 있다.The water regulator is to adjust the function of the main raw material, it may include 40 to 60 parts by weight compared to 100 parts by weight of the main raw material.
즉, 상술한 바와 같이, 상기 주원료의 함수율은 80 내지 85% 정도에 해당할 수 있다. 주원료의 함수율이 80 내지 85%라 함은 주원료에서의 유기성 물질이 15 내지 20%임을 의미할 수 있다.That is, as described above, the moisture content of the main raw material may correspond to about 80 to 85%. The water content of the main raw material is 80 to 85% may mean that the organic material in the main raw material is 15 to 20%.
따라서, 상기 함수 조정제를 통하여 상기 주원료의 함수를 조절한다 함은, 상기 주원료에서의 유기성 물질의 함량을 증가시킴을 의미할 수 있다.Therefore, controlling the function of the main raw material through the water modifier may mean increasing the content of the organic substance in the main raw material.
즉, 상기 주원료 100 중량부 대비 40 내지 60 중량부의 함수 조정제를 포함함으로써, 상기 주원료의 함수율을 조절할 뿐만 아니라, 상기 주원료의 유기성 물질의 양을 조절할 수 있다.That is, by including a water content regulator of 40 to 60 parts by weight relative to 100 parts by weight of the main raw material, it is possible not only to adjust the moisture content of the main raw material, but also to adjust the amount of the organic material of the main raw material.
다음으로, 본 발명에 따른 혼합원료를 제조하는 단계는, 상기 혼합된 주원료와 함수 조정제의 함수를 조정하여, 혼합원료를 제조하는 단계를 포함한다(S134).Next, the step of preparing a mixed raw material according to the present invention, by adjusting the function of the mixed main raw material and the function regulator, comprising the step of preparing a mixed raw material (S134).
즉, 상술한 바와 같이, 본 발명에 따른 혼합원료는, 주원료와 함수 조정제를 포함하여 제조될 수 있으며, 이때, 상기 함수 조정제는, 본 발명에 따른 혼합원료의 주요 구성이 되는 주원료와 동일한 주원료를 사용하여 제조될 수 있다.That is, as described above, the mixed raw material according to the present invention may be prepared, including the main raw material and the water-containing regulator, wherein the water-containing regulator is the same as the main raw material that is the main component of the mixed raw material according to the present invention It can be prepared using.
따라서, 본 발명에 따른 함수 조정제에 포함된 주원료의 경우도, 결국, 혼합원료에서의 주원료로 기능할 수 있으므로, 상기 함수 조정제는 유기성 비료의 함수양을 제어할 수 있을 뿐만 아니라, 그 자체로도 유기성 비료의 일부가 될 수 있다.Therefore, even in the case of the main raw material contained in the water-containing regulator according to the present invention, after all, can function as the main raw material in the mixed raw material, the water-containing regulator not only can control the water content of the organic fertilizer, but also by itself It can be part of organic fertilizers.
이때, 상기 혼합원료의 함수율은 10% 내지 40%일 수 있고, 바람직하게는 15% 내지 30%일 수 있으며, 이러한 혼합 원료의 함수율은 상술한 주원료와 함수조정제의 혼합에 의해 제어될 수 있다.In this case, the water content of the mixed raw material may be 10% to 40%, preferably 15% to 30%, the water content of the mixed raw material can be controlled by the mixing of the above-described main raw material and the water regulator.
이후, 상술한 도 1에서와 같이, 본 발명에서는 상기 혼합원료를 발효 및 숙성하여 유기성 비료를 제조할 수 있다.Thereafter, as shown in FIG. 1, the present invention can produce an organic fertilizer by fermenting and ripening the mixed raw material.
이상에서 살펴본 바와 같이, 본 발명에서 주원료를 제조하는 단계는 유기성 폐기물을 처리하여 제조할 수 있다.As described above, the step of preparing the main raw material in the present invention can be produced by treating the organic waste.
또한, 본 발명에서는 이러한 주원료와 부원료를 혼합하여, 함수조정제를 제조할 수 있다.In addition, in the present invention, such a main raw material and a secondary raw material may be mixed to produce a water-containing regulator.
또한, 본 발명에서는 이러한 주원료를 함수조정제와 혼합하여 혼합원료를 제조한 이후에, 상기 혼합원료를 발효 및 숙성하여 유기성 비료를 제조할 수 있다.In addition, in the present invention, after mixing the main raw material with a water-containing regulator to prepare a mixed raw material, it is possible to ferment and mature the mixed raw material to produce an organic fertilizer.
따라서, 이하에서는, 상기 주원료와 부원료를 혼합하여 함수조정제를 제조하고, 상기 주원료와 상기 함수조정제를 이용하여 혼합원료를 제조하며, 상기 혼합원료를 발효 및 숙성하여 유기성 비료를 제조할 수 있는 유기성 비료의 제조장치에 대해 설명하기로 한다.Therefore, in the following, an organic fertilizer is prepared by mixing the main raw material and the subsidiary material to produce a water-containing regulator, to prepare a mixed raw material by using the main raw material and the water-containing regulator, fertilizing and ripening the mixed raw material to produce an organic fertilizer. The manufacturing apparatus of the will be described.
다만, 본 발명에서의 유기성 비료의 제조장치는, 상술한 유기성 폐기물을 처리하는 단계에서의 유기성 폐기물 처리 장치를 포함할 수 있다.However, the manufacturing apparatus of the organic fertilizer in the present invention may include an organic waste treatment apparatus in the step of treating the organic waste described above.
즉, 본 발명에서의 유기성 폐기물의 처리장치는, 첫째, 유기성 폐기물을 처리하는 유기성 폐기물의 처리장치, 둘째, 주원료를 이용한 혼합원료를 제조하는 혼합원료 제조장치, 셋째, 상기 혼합원료를 발효 및 숙성하는 발효/숙성 장치를 포함할 수 있으며, 이하에서는 상기 둘째의 혼합원료 제조장치 및 상기 셋째의 발효/숙성 장치에 대해 상술하기로 한다.That is, the apparatus for treating organic waste in the present invention is, firstly, an apparatus for treating organic waste, second, a mixed raw material manufacturing apparatus for preparing a mixed raw material using a main raw material, and third, fermenting and ripening the mixed raw material. It may include a fermentation / aging device, and will be described in detail below for the second mixed raw material manufacturing apparatus and the third fermentation / ripening apparatus.
한편, 상기 둘째의 주원료를 이용한 혼합원료를 제조하는 혼합원료의 제조장치는 2가지로 분류될 수 있다.On the other hand, the apparatus for producing a mixed raw material for producing a mixed raw material using the second main raw material can be classified into two types.
즉, 먼저, 혼합원료를 제조하는 것은, 하나의 장치에 의해, 주원료와 부원료를 혼합하여 함수조정제를 제조하고, 또 다른 하나의 장치에 의해 주원료와 함수조정제를 혼합하여 혼합원료를 제조할 수 있다.That is, first, in the preparation of the mixed raw material, the main raw material and the subsidiary raw material are mixed by one device to prepare a water content adjusting agent, and the other raw material may be mixed with the main raw material and the water adjusting agent to produce a mixed raw material. .
다음으로, 혼합원료를 제조하는 것은 하나의 장치에서 주원료와 부원료를 혼합하여 함수조정제를 제조하고, 동일한 장치에서 주원료와 함수조정제를 혼합하여 혼합원료를 제조할 수 있다.Next, to prepare a mixed raw material may be prepared by mixing the main raw material and the subsidiary raw material in one device to produce a water content regulator, and the mixed raw material and the water content regulator in the same device.
이하에서는 혼합원료의 제조장치를 이와 같이 2가지의 경우로 분류하여 설명하기로 한다.Hereinafter, the apparatus for preparing mixed raw materials will be described by dividing into two cases.
도 7은 본 발명의 제1실시예에 따른 혼합 원료 제조장치를 도시하는 개략적인 사시도이고, 도 8은 본 발명의 제1실시예에 따른 혼합 원료 제조장치를 도시하는 개략적인 단면도이다. 이때, 본 발명의 제1실시예에 따른 혼합원료 제조 장치는 주원료와 함수조정제를 혼합하여 혼합원료를 제조하는 혼합원료 제조장치일 수 있으며, 또한, 주원료와 부원료를 혼합하여 함수조정제를 제조하는 함수 조정제 제조장치일 수 있다.7 is a schematic perspective view showing a mixed raw material manufacturing apparatus according to a first embodiment of the present invention, Figure 8 is a schematic cross-sectional view showing a mixed raw material manufacturing apparatus according to a first embodiment of the present invention. At this time, the mixed raw material manufacturing apparatus according to the first embodiment of the present invention may be a mixed raw material manufacturing apparatus for producing a mixed raw material by mixing the main raw material and the water content regulator, and also, a function for producing a water content regulator by mixing the main raw material and the sub-raw material It may be a regulator manufacturing apparatus.
즉, 이하에서는 도 7 및 도 8의 혼합 원료 제조장치가 주원료와 함수조정제를 혼합하여 혼합 원료를 제조하는 장치인 것으로 설명하기로 하며, 다만, 도 7 및 도 8에서의 장치는 주원료와 부원료를 혼합하여 함수조정제를 제조하는 장치로도 사용될 수 있다.That is, hereinafter, the mixed raw material manufacturing apparatus of FIGS. 7 and 8 will be described as a device for producing a mixed raw material by mixing the main raw material and the water-reducing agent, except that the apparatus in FIGS. 7 and 8 shows the main raw material and the sub raw material. It can also be used as a device for mixing the water-soluble regulator.
도 7 및 도 8을 참조하면, 본 발명의 제1실시예에 따른 혼합 원료 제조장치(200)는, 원료 투입부(210) 및 상기 원료 투입부(210)로 투입된 원료를 혼합하기 위한 원료 혼합부(220) 및 상기 원료 혼합부(220)에서 혼합된 원료를 건조하기 위한 혼합 원료 건조부(230)를 포함한다.7 and 8, in the mixed raw material manufacturing apparatus 200 according to the first embodiment of the present invention, a raw material mixture for mixing the raw material input unit 210 and the raw material introduced into the raw material input unit 210. The unit 220 and the mixed raw material drying unit 230 for drying the raw materials mixed in the raw material mixing unit 220.
상기 원료 투입부(210)는 제1원료 투입부(211) 및 제2원료 투입부(212)를 포함할 수 있으며, 상기 제1원료는 주원료이고, 상기 제2원료는 함수조정제일 수 있다.The raw material input part 210 may include a first raw material input part 211 and a second raw material input part 212, the first raw material may be a main raw material, and the second raw material may be a water content regulator.
한편, 상술한 바와 같이, 도 7 및 도 8에서의 장치는 주원료와 부원료를 혼합하여 함수조정제를 제조하는 장치로도 사용될 있으며, 이 경우, 상기 제1원료는 주원료이고, 상기 제2원료는 부원료일 수 있다.On the other hand, as described above, the apparatus in Figures 7 and 8 is also used as a device for producing a water-conditioning agent by mixing the main raw material and the sub-raw material, in this case, the first raw material is the main raw material, the second raw material is the sub-raw material Can be.
계속해서, 도 7 및 도 8을 참조하면, 상기 혼합 원료 건조부(230)는 상기 원료 혼합부(220)와 연결되는 챔버부(231)를 포함하며, 상기 챔버부(231)의 내부에 위치하는 내부 건조경로(240)를 포함하고, 상기 혼합 원료 건조부의 외부에 위치하는 외부 건조경로(250, 260)를 포함하며, 이때, 상기 외부 건조경로(250, 260)는 상기 챔버부의 일측에 위치하는 제1측 외부 건조경로(250) 및 상기 챔버부의 타측에 위치하는 제2측 외부 건조경로(260)를 포함한다.7 and 8, the mixed raw material drying unit 230 includes a chamber part 231 connected to the raw material mixing part 220, and is located inside the chamber part 231. It includes an internal drying path 240, and includes an external drying path (250, 260) located outside the mixed raw material drying unit, wherein the external drying path (250, 260) is located on one side of the chamber portion And a first side external drying path 250 and a second side external drying path 260 positioned on the other side of the chamber part.
상기 내부 건조경로(240), 제1측 외부 건조경로(250) 및 제2측 외부 건조경로(260)는 각각 복수개로 이루어질 수 있으며, 즉, 복수개의 내부 건조경로(240a ~ 240f), 복수개의 제1측 외부 건조경로(250a ~ 250c) 및 복수개의 제2측 외부 건조경로(260a ~ 260c)를 포함할 수 있으며, 이들 건조 경로들이 지그재그로 배치될 수 있다.The internal drying path 240, the first side external drying path 250, and the second side external drying path 260 may each include a plurality, that is, a plurality of internal drying paths 240a to 240f, and a plurality of internal drying paths 240a to 240f, respectively. It may include a first side external drying path (250a ~ 250c) and a plurality of second side external drying path (260a ~ 260c), these drying paths may be arranged in a zigzag.
이때, 상기 내부 건조경로는 수평 건조경로일 수 있으며, 상기 외부 건조경로는 수직 건조경로일 수 있다.In this case, the internal drying path may be a horizontal drying path, and the external drying path may be a vertical drying path.
또한, 상기 챔버부(231)의 내부에 위치하는 가열 수단(280)을 포함하며, 이때, 상기 가열 수단(280)은 챔버부의 하부에 위치하여, 챔버부의 내부를 가열하는 하부 가열 수단(280a) 및 챔버부의 측면에 위치하여, 챔버부의 내부를 가열하는 측면 가열 수단(280b)을 포함할 수 있다.In addition, a heating means 280 is located inside the chamber portion 231, wherein the heating means 280 is located in the lower portion of the chamber portion, the lower heating means 280a for heating the interior of the chamber portion And located on the side of the chamber portion, may include a side heating means (280b) for heating the interior of the chamber portion.
또한, 상기 외부 건조경로와 연결되는 혼합 원료 배출부(270)를 더 포함할 수 있다.In addition, the mixture may further include a mixed raw material discharge part 270 connected to the external drying path.
상기 원료 혼합부(220)에서 혼합된 혼합 원료는 상기 내부 건조경로 및 상기 외부 건조경로를 거쳐 상기 혼합 원료 배출부(270)로 배출된다.The mixed raw material mixed in the raw material mixing part 220 is discharged to the mixed raw material discharge part 270 through the internal drying path and the external drying path.
한편, 상기 혼합 원료는 상기 내부 건조경로 및 상기 외부 건조경로를 거치면서 건조되게 된다.On the other hand, the mixed raw material is dried while passing through the internal drying path and the external drying path.
이때, 상기 내부 건조경로에서는 상기 가열수단(280)에 의해 챔버부(231)의 온도가 고온이 상태이므로, 고온의 온도에 의하여 상기 혼합 원료가 건조되며, 또한, 상기 외부 건조경로에서는 내부 건조경로를 거치면서 고온이 된 혼합원료가 상대적으로 저온인 외부 건조경로를 거치면서, 혼합원료에 포함된 수분이 수증기가 되어 배출되는 과정에서 건조되게 된다.In this case, since the temperature of the chamber part 231 is high by the heating means 280 in the internal drying path, the mixed raw material is dried by the high temperature, and in the external drying path, the internal drying path. While the mixed raw material becomes hot while passing through a relatively low external drying path, moisture contained in the mixed raw material is dried in the process of being discharged as water vapor.
즉, 상술한 바와 같이, 본 발명에서는 상기 챔버부의 내부에 위치하는 내부 건조경로 및 상기 챔버부의 외부에 위치하는 외부 건조경로를 포함하며, 상기 내부 건조경로에서는 고온에 의해 혼합원료의 건조가 이루어지고, 상기 외부 건조경로에서는 혼합원료와 외기의 온도차이에 의한 수증기 형태의 수분 증발에 의해 건조가 이루어진다.That is, as described above, the present invention includes an internal drying path located inside the chamber part and an external drying path located outside the chamber part, wherein the mixed material is dried by a high temperature in the internal drying path. In the external drying path, drying is performed by evaporation of water in the form of water vapor due to the temperature difference between the mixed raw material and the outside air.
이로써, 본 발명에 따른 혼합 원료를 제조할 수 있다.Thereby, the mixed raw material which concerns on this invention can be manufactured.
한편, 상술한 바와 같이, 도 7 및 도 8에서의 장치는 주원료와 부원료를 혼합하여 함수조정제를 제조하는 장치로도 사용될 있으며, 이 경우, 상기 제1원료는 주원료이고, 상기 제2원료는 부원료일 수 있고, 따라서, 본 장치에서 제조되는 것은 함수조정제일 수 있다.On the other hand, as described above, the apparatus in Figures 7 and 8 is also used as a device for producing a water-conditioning agent by mixing the main raw material and the sub-raw material, in this case, the first raw material is the main raw material, the second raw material is the sub-raw material And, therefore, what is produced in the apparatus may be a water content regulator.
이상에서는 함수조정제와 혼합원료를 각각 제조할 수 있는 장치를 설명하였다.In the above, the apparatus which can manufacture a water content regulator and a mixed raw material was demonstrated.
이하에서는 함수조정제와 혼합원료를 동시에 제조할 수 있는 장치를 설명하기로 한다.Hereinafter, an apparatus capable of simultaneously preparing a water content regulator and a mixed raw material will be described.
도 9는 본 발명의 제2실시예에 따른 혼합 원료 제조장치를 도시하는 개략적인 사시도이다. 이때, 본 발명의 제2실시예에 따른 혼합원료 제조 장치는 함수조정제와 혼합원료를 동시에 제조할 수 있는 장치에 해당한다.9 is a schematic perspective view showing a mixed raw material manufacturing apparatus according to a second embodiment of the present invention. At this time, the apparatus for producing a mixed raw material according to the second embodiment of the present invention corresponds to an apparatus capable of simultaneously producing a water content regulator and a mixed raw material.
본 발명의 제2실시예에 따른 혼합 원료 제조장치는 후술하는 바를 제외하고는 상기 제1실시예의 혼합 원료 제조장치를 참조할 수 있다.The mixed raw material manufacturing apparatus according to the second embodiment of the present invention may refer to the mixed raw material manufacturing apparatus of the first embodiment except as described below.
도 9를 참조하면, 본 발명의 제2실시예에 따른 혼합 원료 제조장치(400)는, 원료 투입부(410) 및 상기 원료 투입부(410)로 투입된 원료를 혼합하기 위한 원료 혼합부(421a, 421b) 및 상기 원료 혼합부(421a, 421b)에서 혼합된 원료를 건조하기 위한 혼합 원료 건조부(430)를 포함한다.9, the mixed raw material manufacturing apparatus 400 according to the second embodiment of the present invention, a raw material mixing unit 421a for mixing the raw material input unit 410 and the raw material introduced into the raw material input unit 410 , 421b) and a mixed raw material drying unit 430 for drying the mixed raw materials in the raw material mixing units 421a and 421b.
이때, 본 발명의 제2실시예에서는 상기 원료 투입부(410)는 제1경로 원료 투입부(411, 421b) 및 제1경로 원료 투입부(411, 421b)와 분리되는 제2경로 원료 투입부(412, 422b)를 포함한다.At this time, in the second embodiment of the present invention, the raw material input part 410 is a second path raw material input part separated from the first path raw material input parts 411 and 421b and the first path raw material input parts 411 and 421b. 412 and 422b.
상기 제1경로 원료 투입부(411, 421b)는 제1경로 제1원료 투입부(411) 및 제1경로 제2원료 투입부(421b)를 포함하며, 상기 제2경로 원료 투입부(412, 422b)는 제2경로 제1원료 투입부(412) 및 제2경로 제2원료 투입부(422b)를 포함한다.The first path raw material input unit 411, 421b includes a first path first raw material input unit 411 and a first path second raw material input unit 421b, and the second path raw material input unit 412, 422b) includes a second path first raw material input part 412 and a second path second raw material input part 422b.
이때, 상기 제1경로 제1원료 투입부(411)에 투입되는 원료는 부원료이고, 상기 제1경로 제2원료 투입부(421b)에 투입되는 원료는 주원료이며, 또한, 상기 제2경로 제1원료 투입부(412)에 투입되는 원료는 함수조정제이고, 상기 제2경로 제2원료 투입부(422b)에 투입되는 원료는 주원료일 수 있다.In this case, the raw material introduced into the first raw material input part 411 is a sub-material, and the raw material introduced into the second raw material input part 421b of the first path is a main raw material, and the first second raw material is supplied to the second raw material. The raw material introduced into the raw material input unit 412 may be a water content regulator, and the raw material introduced into the second path second raw material input unit 422b may be a main raw material.
또한, 본 발명의 제2실시예에서는, 상기 제1경로 원료 투입부(411, 421b)와 연결되는 제1원료 혼합부(421a) 및 상기 제1원료 혼합부와 분리되고, 상기 제2경로 원료 투입부(412, 422b)와 연결되는 제2원료 혼합부(422a)를 포함한다.In addition, in the second embodiment of the present invention, the first raw material mixing unit 421a and the first raw material mixing unit connected to the first path raw material input units 411 and 421b are separated from the second path raw material. And a second raw material mixing part 422a connected to the input parts 412 and 422b.
즉, 상기 제1경로에서는 주원료와 부원료과 혼합되며, 상기 제2경로에서는 함수조정제와 주원료가 혼합될 수 있다.That is, the first path may be mixed with the main raw material and the subsidiary material, and in the second path, the water content regulator and the main raw material may be mixed.
계속해서, 도 9를 참조하면, 상기 혼합 원료 건조부(430)는 상기 제1원료 혼합부(421a) 및 상기 제2원료 혼합부(422a)와 연결되는 챔버부(431)를 포함하며,9, the mixed raw material drying unit 430 includes a chamber part 431 connected to the first raw material mixing part 421a and the second raw material mixing part 422a.
상기 챔버부는 상기 제1원료 혼합부(421a)와 연결되는 제1건조 경로 및 상기 제2원료 혼합부(421b)와 연결되는 제2건조 경로를 포함한다.The chamber part includes a first drying path connected to the first raw material mixing part 421a and a second drying path connected to the second raw material mixing part 421b.
상기 제1건조 경로는, 상기 챔버부(431)의 내부에 위치하는 제1내부 건조경로(440)를 포함하고, 상기 챔버부(431)의 외부에 위치하는 제1외부 건조경로(450, 460)를 포함한다.The first drying path includes a first internal drying path 440 located inside the chamber part 431, and first external drying paths 450 and 460 located outside the chamber part 431. ).
또한, 상기 제2건조 경로는, 상기 챔버부(431)의 내부에 위치하는 제2내부 건조경로(미도시)를 포함하고, 상기 챔버부(431)의 외부에 위치하는 제2외부 건조경로(460')를 포함한다.In addition, the second drying path may include a second internal drying path (not shown) positioned inside the chamber part 431, and a second external drying path located outside the chamber part 431. 460 ').
상기 제1건조 경로 및 상기 제2건조 경로에서, 내부 건조경로 및 외부 건조경로를 두는 것은 상술한 바와 같으므로, 이하 구체적인 설명은 생략하기로 한다.In the first drying path and the second drying path, since the internal drying path and the external drying path are the same as described above, detailed descriptions thereof will be omitted.
이때, 상기 제1건조 경로와 상기 제2건조 경로는 동일한 형태로 배치될 수 있으며, 다만, 상기 제1건조 경로에 의해 함수조정제가 제조되고, 상기 제2건조 경로에 의해 혼합 원료가 제조될 수 있으므로, 따라서, 본 발명의 제2실시예에서는 함수조정제를 제조하는 공정과 혼합 원료를 제조하는 공정을 하나의 장치에서 구현할 수 있다.At this time, the first drying path and the second drying path may be arranged in the same form, except that the water-adjusting agent is manufactured by the first drying path, and the mixed raw material may be manufactured by the second drying path. Therefore, according to the second embodiment of the present invention, therefore, the process of manufacturing the water-containing regulator and the process of manufacturing the mixed raw material can be implemented in one apparatus.
한편, 본 발명의 제2실시예에 따른 혼합 원료 제조장치는, 상기 제1건조 경로는 상기 제1외부 건조경로와 연결되는 함수조정제 배출부(470)를 더 포함할 수 있고, 상기 제2건조 경로는 상기 제2외부 건조경로와 연결되는 혼합 원료 배출부(470')를 더 포함할 수 있으며, 또한, 상기 함수조정제 배출부(470)를 통해 배출된 함수조정제를 상기 제2경로 제1원료 투입부(412)에 투입하기 위한 함수 조정제 이동경로(480)를 더 포함할 수 있다.On the other hand, in the mixed raw material manufacturing apparatus according to the second embodiment of the present invention, the first drying path may further include a water content regulator discharge unit 470 connected to the first external drying path, the second drying The path may further include a mixed raw material discharge part 470 ′ connected to the second external drying path, and the second raw material may further include the moisture control agent discharged through the moisture control agent discharge part 470. It may further include a function adjuster movement path 480 for input to the input unit 412.
이상과 같은 본 발명의 제2실시예에 따른 혼합 원료의 제조를 설명하면 다음과 같다.The preparation of the mixed raw material according to the second embodiment of the present invention as described above is as follows.
먼저, 상기 제1경로 제1원료 투입부(411)에 투입되는 부원료가 투입되고, 상기 제1경로 제2원료 투입부(421b)에 주원료가 투입되어, 상기 부원료와 상기 주원료가 제1원료 혼합부(421a)에서 혼합된다.First, a subsidiary material input to the first raw material input part 411 is input, and a main raw material is input to the second raw material input part 421b of the first path, and the sub raw material and the main raw material are mixed with the first raw material. It is mixed in the part 421a.
상기 혼합된 주원료와 부원료는 제1건조 경로, 즉, 상기 챔버부(431)의 내부에 위치하는 제1내부 건조경로(440) 및 상기 혼합 원료 건조부의 외부에 위치하는 제1외부 건조경로(450, 460)를 거치면서 건조되어, 함수조정제로 제조되며, 상기 함수조정제는 함수조정제 배출부(470)를 통해 배출된다.The mixed main raw materials and the sub raw materials are a first drying path, that is, a first internal drying path 440 located inside the chamber part 431 and a first external drying path 450 located outside the mixed raw material drying part. It is dried while passing through, 460, is made of a water-containing regulator, the water-containing regulator is discharged through the water-containing regulator discharge unit 470.
배출된 함수 조정제는 함수 조정제 이동경로(480)를 통해, 상기 제2경로 제1원료 투입부(412)에 투입되고, 상기 제2경로 제2원료 투입부(422b)에 주원료가 투입되어, 상기 함수조정제와 상기 주원료가 제2원료 혼합부(422a)에서 혼합된다.The discharged water modifier is introduced into the second path first raw material input part 412 through the water modifier moving path 480, and the main raw material is added to the second raw material input part 422b. The water content regulator and the main raw material are mixed in the second raw material mixing portion 422a.
상기 혼합된 주원료와 함수조정제는 제2건조 경로, 즉, 상기 챔버부(431)의 내부에 위치하는 제2내부 건조경로(미도시) 및 상기 혼합 원료 건조부의 외부에 위치하는 제2외부 건조경로(460')를 거치면서 건조되어, 혼합 원료로 제조되며, 상기 혼합원료는 혼합 원료 배출부(470')를 통해 배출된다.The mixed main raw material and the water adjusting agent have a second drying path, that is, a second internal drying path (not shown) located inside the chamber part 431 and a second external drying path located outside the mixed raw material drying part. It is dried while going through the (460 '), and is made of a mixed raw material, the mixed raw material is discharged through the mixed raw material discharge portion (470').
이로써, 본 발명에 따른 혼합 원료를 제조할 수 있다.Thereby, the mixed raw material which concerns on this invention can be manufactured.
이하에서는 상기 혼합원료를 발효 및 숙성하는 발효/숙성 장치를 설명하기로 한다.Hereinafter, a fermentation / aging device for fermenting and aging the mixed raw material will be described.
도 10은 본 발명에 따른 혼합원료의 발효/숙성 장치를 도시하는 개략적인 사시도이고, 도 11은 본 발명에 다른 혼합원료를 도시하는 개략적인 단면도이다.10 is a schematic perspective view showing a fermentation / maturation apparatus of a mixed raw material according to the present invention, and FIG. 11 is a schematic sectional view showing another mixed raw material according to the present invention.
도 10 및 도 11을 참조하면, 본 발명에 따른 혼합원료의 발효/숙성 장치는 제조된 유기성 비료를 저장하기 위한 컨테이너부(320) 및 상기 컨테이너부의 외부를 둘러싸며 배치되는 발효/숙성부(310)를 포함한다.10 and 11, the fermentation / maturation device of the mixed raw material according to the present invention is a container portion 320 for storing the organic fertilizer manufactured and the fermentation / maturation portion 310 disposed surrounding the outside of the container portion ).
상기 발효/숙성부(310)는 상기 혼합 원료를 투입하기 위한 혼합 원료 투입부(311)를 포함하고, 상기 발효/숙성부(310)를 거쳐 제조된 유기성 비료를 배출하기 위한 유기성 비료 배출구(312)를 포함하며, 상기 유기성 비료 배출구(312)를 통해 배출된 유기성 비료를 이동하기 위한 이동수단(330) 및 상기 이동수단(330)과 연결되어 상기 유기성 비료를 상기 컨테이너부로 전달하기 위한 유기성 비료 전달 경로(340)를 포함한다.The fermentation / ripening unit 310 includes a mixed raw material input unit 311 for inputting the mixed raw material, the organic fertilizer discharge port 312 for discharging the organic fertilizer manufactured through the fermentation / ripening unit 310 Including a), the organic fertilizer for transporting the organic fertilizer discharged through the organic fertilizer outlet 312 and the organic fertilizer for delivering the organic fertilizer to the container portion connected to the moving means 330 Path 340.
즉, 도 10 및 도 11에 도시된 바와 같이, 혼합 원료 투입부(311)를 통해 투입된 혼합원료는 상기 발효/숙성부(310)를 거치면서 발효 및 숙성되어 유기성 비료로 제조되며, 제조된 유기성 비료는 상기 컨테이너부(320)에 저장 및 보관할 수 있다.That is, as shown in FIGS. 10 and 11, the mixed raw material introduced through the mixed raw material input part 311 is fermented and aged through the fermentation / aging part 310 to be manufactured as an organic fertilizer, and manufactured organic Fertilizer can be stored and stored in the container unit 320.
한편, 상기 혼합 원료 투입부(311)는 상기 컨테이너부(320)의 상단부에 위치하고, 상기 유기성 비료 배출구(312)는 상기 컨테이너부(320)의 하단부에 위치하며, 상기 발효/숙성부(310)는 나선형으로 이루어짐으로써, 상기 혼합 원료 투입부(311)에 투입된 혼합 원료는 중력에 의해 자연스럽게 유기성 비료 배출구(312)로 이동할 수 있다.On the other hand, the mixed raw material input portion 311 is located at the upper end of the container portion 320, the organic fertilizer discharge port 312 is located at the lower end of the container portion 320, the fermentation / maturation portion 310 Since the spiral is made, the mixed raw material injected into the mixed raw material input part 311 may naturally move to the organic fertilizer discharge port 312 by gravity.
이때, 도면에는 도시하지 않았으나, 발효 및 숙성의 효율을 높이기 위하여, 상기 발효/숙성부(310) 내에 로터리와 같은 기계적 장치를 두어, 발효/숙성부(310)에 투입된 혼합 원료를 뒤엎는 절차를 진행할 수 있다.At this time, although not shown in the drawing, in order to increase the efficiency of fermentation and maturation, by placing a mechanical device such as a rotary in the fermentation / maturation portion 310, to proceed with the procedure for overturning the mixed raw material injected into the fermentation / maturation portion (310). Can be.
이로써, 본 발명에 따른 유기성 비료를 제조할 수 있다.Thereby, the organic fertilizer which concerns on this invention can be manufactured.
이상과 같은 본 발명에 따른 유기성 비료의 제조장치는 크게 3가지로 구분될 수 있다.Organic fertilizer manufacturing apparatus according to the present invention as described above can be largely divided into three types.
즉, 본 발명에 따른 유기성 비료의 제조장치는, 첫째, 유기성 폐기물을 처리하는 단계에서의 유기성 폐기물 처리 장치, 둘째, 주원료를 이용하는 혼합원료 제조장치, 셋째, 혼합원료를 발효 및 숙성하는 발효/숙성 장치를 포함할 수 있다.That is, the organic fertilizer manufacturing apparatus according to the present invention, first, the organic waste treatment apparatus in the step of treating the organic waste, second, the mixed raw material manufacturing apparatus using the main raw material, third, fermentation / maturation of fermenting and ripening the mixed raw material It may include a device.
본 발명에서는 이러한 유기성 비료의 제조장치를 통하여, 유기성 폐기물 자원의 재활용화가 가능하다.In the present invention, through the production of such organic fertilizer, it is possible to recycle the organic waste resources.
이상과 첨부된 도면을 참조하여 본 발명의 실시예를 설명하였지만, 본 발명이 속하는 기술분야에서 통상의 지식을 가진 자는 본 발명이 그 기술적 사상이나 필수적인 특징을 변경하지 않고서 다른 구체적인 형태로 실시될 수 있다는 것을 이해할 수 있을 것이다. 그러므로 이상에서 기술한 실시예들은 모든 면에서 예시적인 것이며 한정적이 아닌 것으로 이해해야만 한다.Although embodiments of the present invention have been described above with reference to the accompanying drawings, those skilled in the art to which the present invention pertains may implement the present invention in other specific forms without changing the technical spirit or essential features thereof. You will understand that. Therefore, it should be understood that the embodiments described above are exemplary in all respects and not restrictive.

Claims (7)

  1. 원료 투입부;Raw material input unit;
    상기 원료 투입부로 투입된 원료를 혼합하기 위한 원료 혼합부; 및A raw material mixing part for mixing the raw materials introduced into the raw material input part; And
    상기 원료 혼합부에서 혼합된 원료를 건조하기 위한 혼합 원료 건조부를 포함하고, It includes a mixed raw material drying unit for drying the raw materials mixed in the raw material mixing unit,
    상기 혼합 원료 건조부는, 상기 원료 혼합부와 연결되는 챔버부; 상기 챔버부의 내부에 위치하는 내부 건조경로 및 상기 혼합 원료 건조부의 외부에 위치하는 외부 건조경로를 포함하는 혼합 원료 제조장치를 포함하는 유기성 비료의 제조장치.The mixed raw material drying unit may include a chamber unit connected to the raw material mixing unit; And a mixed raw material manufacturing apparatus including an internal drying path located inside the chamber part and an external drying path located outside the mixed raw material drying part.
  2. 제 1 항에 있어서,The method of claim 1,
    상기 챔버부의 내부에 위치하는 가열 수단을 포함하며,It includes a heating means located in the chamber portion,
    상기 가열 수단은 상기 챔버부의 하부에 위치하여, 상기 챔버부의 내부를 가열하는 하부 가열 수단 및 상기 챔버부의 측면에 위치하여, 상기 챔버부의 내부를 가열하는 측면 가열 수단을 포함하는 유기성 비료의 제조장치.The heating means is located in the lower portion of the chamber portion, the lower heating means for heating the inside of the chamber portion and the side of the chamber portion, the side heating means for heating the inside of the chamber portion comprises an apparatus for producing an organic fertilizer.
  3. 제 1 항에 있어서,The method of claim 1,
    상기 원료 투입부는 제1원료 투입부 및 제2원료 투입부를 포함하며,The raw material input unit includes a first raw material input unit and a second raw material input unit,
    상기 제1원료 투입부에 투입되는 원료는 주원료이고, 상기 제2원료 투입부에 투입되는 원료는 함수조정제인 유기성 비료의 제조장치.The raw material introduced into the first raw material input unit is a main raw material, the raw material introduced into the second raw material input unit is an organic fertilizer manufacturing apparatus.
  4. 제 1 항에 있어서,The method of claim 1,
    상기 원료 투입부는 제1원료 투입부 및 제2원료 투입부를 포함하며,The raw material input unit includes a first raw material input unit and a second raw material input unit,
    상기 제1원료 투입부에 투입되는 원료는 함수조정제이고, 상기 제2원료 투입부에 투입되는 원료는 주원료인 유기성 비료의 제조장치.The raw material to be introduced into the first raw material input unit is a water content regulator, the raw material to be injected into the second raw material input unit is an organic fertilizer manufacturing apparatus.
  5. 제 1 항에 있어서,The method of claim 1,
    상기 원료 투입부는 제1경로 원료 투입부 및 상기 제1경로 원료 투입부와 분리되는 제2경로 원료 투입부를 포함하고,The raw material input part includes a first path raw material input part and a second path raw material input part separated from the first path raw material input part,
    상기 제1경로 원료 투입부는 제1경로 제1원료 투입부 및 제1경로 제2원료 투입부를 포함하며, 상기 제2경로 원료 투입부는 제2경로 제1원료 투입부 및 제2경로 제2원료 투입부를 포함하며,The first path raw material input part includes a first path first raw material input part and a first path second raw material input part, and the second path raw material input part includes a second path first raw material input part and a second path second raw material input part. Includes wealth,
    상기 제1경로 제1원료 투입부에 투입되는 원료는 부원료이고, 상기 제1경로 제2원료 투입부에 투입되는 원료는 주원료이며, 상기 제2경로 제1원료 투입부에 투입되는 원료는 함수조정제이고, 상기 제2경로 제2원료 투입부에 투입되는 원료는 주원료인 유기성 비료의 제조장치.The raw material input to the first raw material input part of the first path is a subsidiary material, the raw material input to the second raw material input part of the first path is a main raw material, and the raw material input to the first raw material input part of the second path is a water content regulator. And a raw material introduced into the second raw material input part of the second path is an organic fertilizer manufacturing apparatus.
  6. 제 5 항에 있어서,The method of claim 5, wherein
    상기 원료 혼합부는, 상기 제1경로 원료 투입부와 연결되는 제1원료 혼합부 및 상기 제1원료 혼합부와 분리되고, 상기 제2경로 원료 투입부와 연결되는 제2원료 혼합부를 포함하고, The raw material mixing part includes a first raw material mixing part connected to the first path raw material input part and a second raw material mixing part separated from the first raw material mixing part and connected to the second path raw material input part,
    상기 챔버부는, 상기 제1원료 혼합부와 연결되는 제1건조 경로 및 상기 제2원료 혼합부와 연결되는 제2건조 경로를 포함하고,The chamber part includes a first drying path connected to the first raw material mixing part and a second drying path connected to the second raw material mixing part,
    상기 내부 건조경로는 제1내부 건조경로 및 제2내부 건조경로를 포함하고, 상기 외부 건조경로는 제1외부 건조경로 및 제2외부 건조경로를 포함하며,The inner drying path includes a first inner drying path and a second inner drying path, and the outer drying path includes a first outer drying path and a second outer drying path,
    상기 제1건조 경로는, 상기 챔버부의 내부에 위치하는 상기 제1내부 건조경로 및 상기 챔버부의 외부에 위치하는 상기 제1외부 건조경로를 포함하고,The first drying path includes the first internal drying path located inside the chamber part and the first external drying path located outside the chamber part.
    상기 제2건조 경로는, 상기 챔버부의 내부에 위치하는 상기 제2내부 건조경로 및 상기 챔버부의 외부에 위치하는 제2외부 건조경로를 포함하는 유기성 비료의 제조장치.The second drying path is an apparatus for producing organic fertilizer comprising the second internal drying path located inside the chamber portion and the second external drying path located outside the chamber portion.
  7. 제 6 항에 있어서,The method of claim 6,
    상기 제1건조 경로는 상기 제1외부 건조경로와 연결되는 함수조정제 배출부를 포함하, 상기 제2건조 경로는 상기 제2외부 건조경로와 연결되는 혼합 원료 배출부를 더 포함하며,The first drying path includes a water content regulator discharge part connected to the first external drying path, and the second drying path further includes a mixed raw material discharge part connected to the second external drying path.
    상기 함수조정제 배출부를 통해 배출된 함수조정제를 상기 제2경로 제1원료 투입부에 투입하기 위한 함수 조정제 이동경로를 더 포함하는 유기성 비료의 제조장치.The apparatus for producing organic fertilizer further comprises a water-containing regulator moving path for introducing the water-containing regulator discharged through the water-containing regulator discharge unit to the second raw material input unit.
PCT/KR2016/004279 2016-04-25 2016-04-25 Device for manufacturing organic fertilizer WO2017188461A1 (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR19980019962A (en) * 1996-09-04 1998-06-25 최홍림 Closed Layered Reactor Composting System for Livestock Manure
JP2003192475A (en) * 2001-12-25 2003-07-09 Katsuhiro Ito System for recycling domestic animal dung by drying, fermenting and carbonizing and method of manufacturing compost, dry fertilizer, carbonized fertilizer and carbonized product
KR200360330Y1 (en) * 2004-06-15 2004-08-25 김인수 A continuous automatic dry apparatus for scrapped material
KR20130008133A (en) * 2011-07-12 2013-01-22 (주)그린리소스 Electronic food waste composter using thermophilic microorganisms
KR20130102195A (en) * 2012-03-07 2013-09-17 지인철 Manufacturing method of the organic fertilizer using feces as a raw material and the equipment thereof
KR101616824B1 (en) * 2014-11-13 2016-05-09 김우현 A Manufacturing device of organic fertilizer

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR19980019962A (en) * 1996-09-04 1998-06-25 최홍림 Closed Layered Reactor Composting System for Livestock Manure
JP2003192475A (en) * 2001-12-25 2003-07-09 Katsuhiro Ito System for recycling domestic animal dung by drying, fermenting and carbonizing and method of manufacturing compost, dry fertilizer, carbonized fertilizer and carbonized product
KR200360330Y1 (en) * 2004-06-15 2004-08-25 김인수 A continuous automatic dry apparatus for scrapped material
KR20130008133A (en) * 2011-07-12 2013-01-22 (주)그린리소스 Electronic food waste composter using thermophilic microorganisms
KR20130102195A (en) * 2012-03-07 2013-09-17 지인철 Manufacturing method of the organic fertilizer using feces as a raw material and the equipment thereof
KR101616824B1 (en) * 2014-11-13 2016-05-09 김우현 A Manufacturing device of organic fertilizer

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