KR20220129191A - Liquid fertilizer manufacturing method using gas-selective generators and microbubble generating device - Google Patents

Abstract

The present invention relates to a method for manufacturing a liquid fertilizer using a gas selective generator and a microbubble generator, wherein the method comprises: a collection gas selection setting process (10); a selection gas collection generation process (20); a selective gas storage process (30); a selective gas pressure supply process (40); a microbubble generation dissolution process (50); and a dissolved sap non-injection process (60). The present invention has the effect of smoothly inducing the growth of aerobic microorganisms by supplying dissolved oxygen-rich oxygen-dissolved water to crops.

Description

Liquid fertilizer manufacturing method using gas-selective generators and microbubble generating device

The present invention relates to a method for manufacturing a liquid fertilizer using a gas selective generator and a microbubble generator, and more particularly, to a crop using a selective gas generator and a microbubble generator to irrigate a crop with oxygen dissolved water rich in dissolved oxygen and It is supplied by side spraying to smoothly induce the growth of aerobic microorganisms, suppress harmful bacteria and aerobic microorganisms to balance fungi in the soil and medium or hydroponics and aquaponics farming methods. By increasing the growth rate of aerobic microorganisms during crop harvesting, root growth and growth of crops are activated, thereby further increasing crop yields, and supplying dissolved nitrogen-rich water to crops using canopies and sieves from small roots. Thus, by inducing a more smooth increase in yield through photosynthesis of leaves, growth growth and crop yield can be further increased. can maximize the absorption effect of nitrogen fertilizer, help crops with protein and nucleic acids necessary for glucose production, and contribute to the creation of fertile soil by breeding bacteria to be beneficial for root growth. An aerobic fungus of nitrifying bacteria important for nitrogen assimilation by ionizing gaseous carbon dioxide and supplying it to crops to induce continuous growth in a well-balanced state of crop growth and growth. It plays a role in maintaining the balance of important bacterial reproduction that further maximizes plant-based conditions of glucose, protein, and nucleic acid to induce proliferation and increase harvest, and becomes a nature-friendly circulation method that is repeated into a gaseous atmosphere by denitrification. , By supplying ozone-dissolved water rich in dissolved ozone to crops, it kills, suppresses, and evades molds, fungi, worms, bacteria, and viruses, and oxidizes and decomposes heavy metals to activate root growth and growth of crops while increasing crop yields. Gas selection that can be increased sustainably at low cost It relates to a liquid fertilizer manufacturing method using a device and a microbubble generating device.

In general, organic fertilizer is a relative concept with inorganic fertilizers (chemical fertilizers), and includes organic fertilizers with organic substances as main raw materials and by-product fertilizers with by-products as main raw materials. There are excrement residues, humus, amino acid fermented byproducts, husk husks, sawdust, or soil microbial preparations.

Among them, most of the chemical fertilizers are fast-acting, which dissolves quickly when applied to the soil, and temporarily enriches the soil with nutrients immediately after fertilization. However, plants cannot absorb or utilize nutrients that are fertilized in a short period of time. As a result, nutrients that remain unabsorbed by plants seep into the soil, causing contamination of soil, groundwater, and rivers.

The soil of our country is poor in growth, quality, and disease resistance due to long-term fertilization centered on chemical fertilizers, excessive use of pesticides and chemical herbicides, and continuous cropping of one crop. , crop pollution, yield reduction, and lower productivity.

In addition, the use of concentrated chemical fertilizers and pesticides may cause serious salt accumulation, and chain disorders due to mineral deficiency may occur due to the antagonistic action between excessively sprayed nutrients, resulting in reduced disease resistance of crops, poor growth, etc. There were also problems such as a decrease in harvest and deterioration of quality and taste.

Recently, as this crop pollution problem has been seriously raised along with the environmental pollution problem, the development of farming methods using high-quality organic fertilizers or mature compost rather than using chemical fertilizers or pesticides has spread, and the development of many organic fertilizers is continuously attempted. have.

However, despite these efforts, the intensive use of organic fertilizers and composts used as alternatives to chemical fertilizers is only different in material, and aggravates another problem similar to chemical agents. Soil acidity affects various factors such as the characteristics of the soil itself, the effectiveness of nutrients, and microbial activity, and in particular, has a great influence on the nutrient absorption closely related to the growth of crops.

Therefore, in order to improve the growth of crops, many attempts are being made to correct the acidified agricultural soil to the neutralized (PH6.5-7) agricultural soil, and generally quicklime fertilizer, slaked lime fertilizer, dolomite fertilizer (goto Fertilizer), gypsum fertilizer and shellfish powder fertilizer (shell fossil powder fertilizer), lime-based and sulfur-based substances containing calcium and sulfur are used in large amounts as soil improver fertilizers.

However, since calcium (Ca) and sulfur (S) contained in lime-based and sulfur-based fertilizers can harden the soil, the mass use of lime-based or sulfur-based fertilizers is gradually being avoided. Therefore, the need for the development of fertilizers that have the effect of enhancing the growth of crops while solving these side effects has been raised, and in particular, the demand for fertilizers using natural products is increasing.

In order to solve this problem, "a mixed solution preparation step of dissolving materials containing sodium metasilicate, potassium phosphate, potassium carbonate and citric acid in water (S100); Natural material preparation and mixing step (S200) of preparing and mixing the natural materials including the sagebrush, dandelion and eoseongcho; Natural material fermentation step (S300) of fermenting the mixed natural material; The fermented natural material and the mixture solution A natural extract manufacturing step (S400) of preparing a natural extract by further fermenting after mixing the microbial activator manufacturing step (S500) of preparing a microbial activator; And a liquid fertilizer by mixing the natural extract and the microbial activator and a liquid fertilizer manufacturing step (S600) for preparing It is prepared by mixing after mixing in a weight ratio of 15 to 25 parts by weight of potassium and 1 to 2 parts by weight of citric acid, and the prepared natural material in the natural material preparation and mixing step (S200) is willow, sagebrush, mugwort, sagebrush. , Sorijae, dandelion and Eosongcho are mixed in a weight ratio of 1:1:1:1:1:1:1, respectively, and as the microorganism in the natural material fermentation step (S300), Rhizopus oligosporus (Rhizopus oligosporus) ) or Saccharomyces cerevisiae, any one or more microorganisms selected from among are used, and the microorganisms are mixed in a weight ratio of 1 to 3 parts by weight with respect to 100 parts by weight of the mixed natural material, and the natural extract In the manufacturing step (S400), after mixing in a weight ratio of 30 to 50 parts by weight of the fermented natural material with respect to 100 parts by weight of the total mixture, fermentation is further performed at a temperature of 45 to 50° C. for 5 to 10 days to obtain a natural extract. manufactured, and in the liquid fertilizer manufacturing step (S600), the liquid fertilizer is a method for producing a liquid fertilizer for promoting plant root growth, characterized in that the liquid fertilizer is prepared by mixing 100 to 200 parts by weight of a natural extract and 10 to 30 parts by weight of a microbial activator. No. 2118923 (2020.06.04. announcement) was initiated.

However, this conventional liquid fertilizer requires a lot of time and a lot of money in the process of purchasing, collecting, and fermenting many kinds of natural materials, so it is practically time-consuming and costly to be universally used in farms. there was.

(Patent Document 1) (KR) Korean Patent Registration No. 10-2118923 (2020.06.04. Announcement)

The present invention is to solve the above problems, and by using a gas selective generator and a microbubble generator, oxygen-dissolved water rich in dissolved oxygen is supplied to crops by irrigation and side spraying to smoothly induce the proliferation of aerobic microorganisms. Inhibits harmful bacteria and aerobic microorganisms to balance fungi in soil and medium or hydroponics and aquaponics, improves root growth during crop growth, and increases the growth rate of aerobic microorganisms when harvesting crops Root growth and growth can be activated to further increase crop yield, and nitrogen-rich water rich in dissolved nitrogen is supplied to crops to more smoothly increase yield through photosynthesis of leaves by using canopy and phloem from fine roots. By inducing it to be possible, the growth growth and crop yield can be further increased, and the fine roots obtained with nitrogen-fixing bacteria from root-knot bacteria by supplying ammonium-dissolved water rich in dissolved ammonia to the crops can maximize the effect of absorbing nitrogen fertilizers, and It helps proteins and nucleic acids necessary for glucose production, and contributes to the creation of fertile soil by breeding bacteria to be beneficial for root growth. It induces continuous growth in a well-balanced condition, and supplies nitrate dissolved water rich in dissolved nitric acid to crops to induce aerobic fungal growth of nitrifying bacteria, which is important for nitrogen assimilation. It plays a role in maintaining the balance of important bacterial reproduction that further maximizes the plant-based condition of nucleic acid, and becomes a nature-friendly circulation method that is repeated to the gaseous atmosphere by denitrification, and supplies ozone-dissolved water rich in dissolved ozone to crops. It kills, suppresses and repels molds, fungi, worms, and bacteria or viruses, and oxidizes and decomposes heavy metals to activate root growth and growth of crops, while generating gas selection that can increase crop yields sustainably at low cost Liquid fertilizer manufacturing method using device and microbubble generator Its purpose is to provide

The problem to be solved by the present invention is not limited to the problems mentioned above, and other problems not mentioned will be clearly understood by those skilled in the art from the following description.

In order to achieve this object, the present invention applies power through the control unit A1 of the gas selective generator A, and the gas to be collected and stored in the control unit A1 is selected from among oxygen, nitrogen, air, and ozone. a collection gas selection setting process (10) of selecting any one or two or more and setting the number and time of operation of the tank to execute the collection and storage of the gas as many times as the number of operation of the tank;

In order to generate any one selected from among oxygen, nitrogen, atmosphere, and ozone in the control unit A1 of the collection gas selection setting process 10, the surrounding air is sucked and compressed with the gas selective generator A through a filter and sucked. a selective gas collection and generation process (20) in which only the gas selected in the collection gas selection setting process (10) is left in the compressed air and the remaining gas is separated and discharged to generate only the selected gas;

a selective gas storage process (30) of compressing and storing any one selected from oxygen, nitrogen, air, and ozone, which are gases generated through the selective gas collection and generation process (20), in a gas storage tank (A5);

The gas stored in the gas storage tank (A5) through the selective gas storage process (30) is placed inside the water tank (C) filled with water (D) through the supply pipe (A7) at a constant pressure of the compressor (A6). a selective gas pressure supply process (40) for supplying to the microbubble generating device (B);

The microbubble generating device (B) supplied with any one selected from oxygen, nitrogen, air, and ozone through the selective gas pressure supply process (40) is a gas supplied from inside the water tank (C) filled with water (D). a microbubble generation and dissolution process (50) of rapidly dissolving and processing microbubbles in water (D) inside the water tank (C) by generating microbubbles with any one selected from oxygen, nitrogen, air, and ozone; and

It is characterized in that it consists of a non-dissolved sap non-injection process (60) in which the dissolved water (D1) inside the water tank (C), which has undergone the microbubble generation and dissolution process (50), is used as the liquid manure of the farm through the pump (P).

As the gas selective generator (A), an oxygen generator (A2) is used, the surrounding air is sucked and compressed to be transferred to the adsorption bed, and only oxygen in the adsorption bed is supplied to the gas storage tank (A5) at a concentration of 90% or more. Other gases, including nitrogen, are separately discharged.

When the oxygen generator A2 is used as the gas selective generator A, only nitrogen is collected from the gas containing nitrogen remaining after oxygen generation and stored in a separate nitrogen tank.

As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked and compressed to pass through a tank filled with oxygen adsorbent (CMS) and only nitrogen at a concentration of 90% or more in a gas storage tank (A5) ), the oxygen adsorbed to the oxygen adsorbent (CMS) is separately discharged.

When a nitrogen generator is used as the gas selective generator, only oxygen adsorbed to an oxygen adsorbent (CMS) is collected and stored in a separate oxygen tank after nitrogen is generated.

As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked and compressed to pass through a tank filled with oxygen adsorbent (CMS) and only nitrogen at a concentration of 90% or more in a gas storage tank (A5) ), the oxygen adsorbed on the oxygen adsorbent (CMS) is separately discharged, and when ammonia (A12a) is selected, it is electrolyzed by the hydrogen generator (A12aa) in the water tank (C) and the oxygen from + is released into the air. There is a characteristic that ammonium ion nitrogen is generated due to the catalytic reaction (A12ba).

As the gas selective generating device (A), a compressor (A6) is used, and the surrounding air is sucked and compressed to be supplied to the gas storage tank (A5).

As the gas selective generator (A), a compressor (A6) is used, the surrounding air is sucked and compressed and supplied to the gas storage tank (A5), and when nitric acid (A13a) is selected, high temperature and high pressure like air discharge (lightning) The generated plasma generating device (A13aa) is characterized in that nitrogen nitrate ions are generated by separating the nitrogen linkage made of a triple bond.

As the gas selective generator (A), the oxygen generator (A2) is used to suck and compress the surrounding air and transport it to the adsorption bed, and only oxygen in the adsorption bed generates oxygen that is more than 90% concentrated. It receives oxygen and uses an ozone generator (A4) to change oxygen into ozone and supply it through silent discharge.

The control unit A1 of the gas selection generator A sets the capacity of the water tank C according to the needs of the crop by the user by the water level sensors S1 and S2, and the set capacity of the water tank C Oxygen number button (A11), nitrogen number button (A12), standby number button that can set the number of times of operation of the tank in one cycle to fill the water (D) and supply it all to the crops by filling it with water (D1) (A13), the ozone frequency button (A14) is further provided, respectively, and the number of times of operation of the tank is set in advance to "0 ~ 20" according to the need for crop growth, and operation of the button with the number of times of operation of the tank set to "0" is excluded And, according to the set number of operation of the water tank, the dissolved water (D1) inside the water tank (C) is dissolved in oxygen by the oxygen generator (A2), the nitrogen generator (A3), the compressor (A6), and the ozone generator (A4), respectively. Water, nitrogen-dissolved water, atmospheric dissolved water and ozone-dissolved water are sequentially filled as many times as the number of tank operations, and each dissolved water (D1) inside the tank (C) is sequentially supplied to the crops as many times as the number of tank operations with the pump (P). There is this.

The control unit (A1) of the gas selection generator (A),

Each of an ammonia count button (A12a) and a nitric acid count button (A13a) is further provided,

When ammonia is selected with the ammonia count button (A12a), it is electrolyzed by the hydrogen generator (A12aa) in the water tank (C), and oxygen from + is released into the air and ammonium ion nitrogen is generated due to the catalyst reaction (A12ba). C) Ammonium dissolved water is formed inside, and when nitric acid is selected with the nitric acid number button (A13a), a plasma generator (A13aa) that generates high temperature and high pressure like air discharge (lightning) separates the nitrogen link made of triple bonds to nitrate ions Nitrogen is generated and nitrate dissolved water is formed inside the tank (C).

The present invention applies power through the control unit (A1) of the gas selection generator (A), and selects any one or two or more of oxygen, nitrogen, air, and ozone as the gas to be collected and stored in the control unit (A1). a collection gas selection setting process (10) of setting the number and time of operation of the tank to set the collection and storage of the gas to be executed as many times as the number of times of operation of the tank;

In order to generate any one selected from among oxygen, nitrogen, atmosphere, and ozone in the control unit A1 of the collection gas selection setting process 10, the surrounding air is sucked and compressed with the gas selective generator A through a filter and sucked. a selective gas collection and generation process (20) in which only the gas selected in the collection gas selection setting process (10) is left in the compressed air and the remaining gas is separated and discharged to generate only the selected gas;

The inside of the water tank (C) filled with water (D) through the supply pipe (A7) at a constant pressure of any one gas selected among oxygen, nitrogen, air, and ozone, which is the gas generated through the selective gas collection and generation process (20) Selective gas pressure supply process 40 for supplying to the microbubble generating device (B) located in the;

The microbubble generating device (B) supplied with any one selected from oxygen, nitrogen, air, and ozone through the selective gas pressure supply process (40) is a gas supplied from inside the water tank (C) filled with water (D). a microbubble generation and dissolution process (50) of rapidly dissolving and processing microbubbles in water (D) inside the water tank (C) by generating microbubbles with any one selected from oxygen, nitrogen, air, and ozone; and

It is characterized in that it consists of a non-dissolved sap non-injection process (60) in which the dissolved water (D1) inside the water tank (C), which has undergone the microbubble generation and dissolution process (50), is used as a liquid manure of the farm through the pump (P).

As described above, the present invention uses a gas selective generator and a microbubble generator to supply oxygen-rich water rich in dissolved oxygen to crops by irrigation and side spraying to smoothly induce the proliferation of aerobic microorganisms, harmful bacteria and aerobic microorganisms to balance fungi in the soil and medium or hydroponics and aquaponics farming methods, improve root growth during crop growth, and increase the growth rate of aerobic microorganisms during crop harvest to activate root and growth growth of crops It is possible to further increase the crop yield by supplying nitrogen-dissolved water rich in dissolved nitrogen to the crops, using the canopy and phloem from the fine roots to more smoothly increase the yield through the photosynthetic action of leaves. It is possible to further increase the yield, and by supplying ammonium-dissolved water rich in dissolved ammonia to the crops, the fine roots obtained with nitrogen-fixing bacteria from the root-knot bacteria can maximize the absorption effect of nitrogen fertilizers, and proteins and nucleic acids necessary for the production of glucose by the crops. It helps and contributes to the creation of fertile soil by propagating bacteria to be beneficial to the growth of fine roots. Dissolved water in the atmosphere, rich in dissolved atmosphere, ionizes carbon dioxide in the greenhouse gas and supplies it to crops, providing continuous growth in a well-balanced state of crop growth and growth. It induces aerobic fungal growth of nitrifying bacteria, which is important for nitrogen assimilation by supplying nitrate dissolved water rich in dissolved nitric acid to crops, and adds plant-based conditions of glucose, protein, and nucleic acid to increase harvest. It plays a role in maintaining the balance of the reproduction of important bacteria that maximizes, and becomes a nature-friendly circulation method that is repeated to the gaseous atmosphere by denitrification action. It has the effect of killing, suppressing and avoiding viruses, and oxidatively decomposing heavy metals to activate root growth and growth of crops, while increasing crop yields sustainably at low cost.

The present invention is not limited to the specific preferred embodiments described above, and various modifications are possible by anyone with ordinary skill in the art to which the invention pertains without departing from the gist of the invention as claimed in the claims. Of course, such modifications are intended to be within the scope of the claims.

1 is a flowchart in which a liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator according to an embodiment of the present invention is listed by time difference;
2 is an explanatory view showing the outline of the operation of the liquid fertilizer manufacturing method using the gas selective generator and the microbubble generator according to the embodiment of the present invention;
Figure 3 is an explanatory view showing the outline of the operation when the compressor is not used in the liquid fertilizer manufacturing method using the gas selective generator and the microbubble generator according to the embodiment of the present invention.

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

Hereinafter, embodiments of the present invention will be described in detail with reference to the accompanying drawings so that those of ordinary skill in the art can easily implement them. The present invention may be embodied in several different forms and is not limited to the embodiments described herein.

In order to clearly explain the present invention in the drawings, parts irrelevant to the description are omitted, and the same reference numerals are assigned to the same or similar components throughout the specification. The scope of the present invention should not be construed as being limited by the embodiments described in the text, and since the embodiments are capable of various changes and may have various forms, the scope of the present invention is intended to provide a way to realize the technical idea. It should be understood to include equivalents.

Throughout the specification of the present invention, when a part is "connected" with another part, it includes not only the case where it is "directly connected" but also the case where it is "indirectly connected" with another member interposed therebetween. In addition, when a part "includes" a certain component, this means that other components may be further included, rather than excluding other components, unless otherwise stated.

The terms used in the present invention are terms defined in consideration of the functions in the present invention, which may vary depending on the intention or custom of the user or operator, so the definitions of these terms correspond to the technical matters of the present invention and should be interpreted as a concept.

In addition, optional terms in the following embodiments are used to distinguish one component from other components, and the components are not limited by the terms. Hereinafter, in describing the present invention, detailed descriptions of related known technologies that may unnecessarily obscure the gist of the present invention will be omitted.

The liquid fertilizer manufacturing method using the gas selective generating device and the microbubble generating device of the present invention includes a collection gas selection setting process (10), a selective gas collection and generation process (20), a selective gas storage process (30), and a selection It consists of a gas pressure supply process (40), a microbubble generation dissolved process (50), and a dissolved sap non-injection process (60).

In the collection gas selection setting process 10, power is applied through the control unit A1 of the gas selection generator A, and the gas to be collected and stored by the control unit A1 is oxygen, nitrogen, ammonia, air, nitric acid It is a process of setting the number of tank operation while selecting any one or two or more of ozone, and setting the collection and storage of the gas to be performed manually or automatically as many times as the number of operation of the tank. It is preferable to perform this automatically, but it goes without saying that this can optionally be performed manually. For this purpose, it is preferable to separately form the automatic selection switch and the manual selection switch.

In the selective gas collection and generation process (20), the gas selective generator (A) selects and generates oxygen, nitrogen, ammonia, air, nitric acid, and ozone in the control unit (A1) of the collection gas selection setting process (10). ), the surrounding air is suction-compressed through a filter, and only the gas selected in the collection gas selection setting process (10) is left among the suction-compressed air, and the remaining gas is separated and discharged to generate only the selected gas.

The selective gas storage process 30 is a gas storage tank ( This is the process of compressing and storing in A5).

In the selective gas pressure supply process 40, the gas stored in the gas storage tank A5 through the selective gas storage process 30 is subjected to a constant pressure of the compressor A6 through the supply pipe A7 through the water (D) This is the process of supplying to the microbubble generating device (B) located inside the full tank (C).

In the microbubble generating and dissolving process 50, the microbubble generating device B selectively supplied from oxygen, nitrogen, ammonia, air, nitric acid, and ozone through the selective gas pressure supply process 40 is water (D) It is a process of rapidly dissolving in the water (D) inside the tank (C) by generating microbubbles selected from among the gases supplied from the inside of the tank (C), which are oxygen, nitrogen, ammonia, air, nitric acid, and ozone. At this time, it is preferable to install a separate submersible motor (not shown) inside the water tank (C) in order to increase the efficiency of the dissolved water treatment so that the dissolved water (D1) is mixed with each other.

The dissolved sap non-injection process (60) is a process of using the dissolved water (D1) inside the water tank (C) that has undergone the microbubble generation and dissolution process (50) as liquid fertilizer of farm crops through the pump (P).

When an oxygen generator (A2) is used as the gas selective generator (A), the surrounding air is sucked and compressed and transferred to an adsorption bed (not shown), and only oxygen in the adsorption bed is contained in a gas storage tank (A5) with a concentration of 90% or more. ), other gases including nitrogen are separately discharged.

Of course, when the oxygen generator A2 is used as the gas selective generator A, only nitrogen may be collected from the gas containing nitrogen remaining after oxygen generation and stored in a separate nitrogen tank (not shown).

When a nitrogen generator (A3) is used as the gas selective generator (A), the surrounding air is sucked and compressed and passes through a tank filled with oxygen adsorbent (CMS) while only nitrogen at a concentration of 90% or more gas storage tank (A5) The oxygen adsorbed on the oxygen adsorbent (CMS) is separately discharged while being supplied to the

Of course, when the nitrogen generator A3 is used as the gas selective generator A, only oxygen adsorbed to the oxygen adsorbent (CMS) after nitrogen generation may be collected and stored in a separate oxygen tank (not shown).

When a nitrogen generator (A3) is used as the gas selective generator (A), the surrounding air is sucked and compressed and passes through a tank filled with oxygen adsorbent (CMS) while only nitrogen at a concentration of 90% or more gas storage tank (A5) Oxygen adsorbed to the oxygen adsorbent (CMS) while being supplied to the CMS is separately discharged, and when ammonium ion (A12a) is selected, it is electrolyzed by the hydrogen generator (A12aa) in the water tank. A12ba) produces ammonium ion nitrogen.

When the compressor (A6) is used as the gas selective generator (A), the surrounding air is sucked and compressed and supplied to the gas storage tank (A5).

When using the compressor (A6) as the gas selective generator (A), when selecting nitrate ions (A13a), the plasma generator (A13aa) generates a high temperature like air discharge (lightning) by separating the nitrogen linkage made of a triple bond Nitrate ion nitrogen is produced.

As the gas selective generator (A), the oxygen generator (A2) is used to suck and compress the surrounding air, and transfer it to an adsorption bed (not shown), and only oxygen in the adsorption bed generates oxygen enriched by 90% or more. Receives the generated and concentrated oxygen and uses the ozone generator (A4) to change the oxygen into ozone through silent discharge and supply it to the gas storage tank (A5).

The control unit A1 of the gas selection generator A sets the capacity of the water tank C according to the needs of the crop by the user by the water level sensors S1 and S2, and the set capacity of the water tank C Oxygen number button (A11), nitrogen number button (A12), ammonia number button that can set the number of times of operation of the water tank in one cycle to fill the water (D) according to (A12a), standby number button (A13), nitric acid number button (A13a), ozone number button (A14), respectively, by setting the number of times of operation of the tank to "0 ~ 20" in advance according to the needs of crop growth, Except for the operation of the button whose water tank operation frequency is set to “0”, the dissolved water (D1) inside the water tank (C) is converted to the oxygen generator (A2), nitrogen generator (A3), compressor according to the set number of tank operation times. (A6), an ozone generator (A4), a hydrogen generator (A12aa), and a plasma generator (A13aa), respectively, in a tank with dissolved oxygen water, nitrogen dissolved water, ammonium dissolved water, atmospheric dissolved water, nitrate dissolved water, and ozone dissolved water Each of the dissolved water (D1) inside the water tank (C) is sequentially filled as many times as the number of operation and is supplied to the crops sequentially as many times as the number of operation of the water tank (C) with the pump (P).

That is, when the user sets the capacity inside the water tank (C) according to the required amount of crops by the height of the water level sensors (S1, S2), the control unit (A1) fills the inside of the water tank (C) with water (D). In the control unit A1 of the gas selection generator A, the oxygen number button A11 is “3”, the nitrogen number button A12 is “1”, the ammonia number button A12a, “0” , gas selection occurs when the collection gas selection setting process (10) in which the standby number button (A13) is set to “1”, the nitric acid number button A13a, “0”, and the ozone number button A14 to “1” The control unit A1 of the device A performs a selective gas capture and generation process 20 for collecting oxygen, according to the number of operation of the water tank “3” of the oxygen number button A11, and transfers the captured oxygen to the gas storage tank A5. Selective gas storage process 30 for compression and storage, Selective gas pressure supply process 40 for supplying compressed and stored oxygen to the microbubble generating device B, Microbubble generating dissolved process 50 for generating oxygen dissolved water D1 ), and a process (60) of supplying oxygen-dissolved water (D1) to the crops by means of a pump (P) is performed in one cycle. This process is repeated all three times as many as the set number of operation of the water tank.

Then, the water tank C is filled with water D by the control unit A1, and the control unit A1 of the gas selection generator A is set to “1” water tank of the nitrogen count button A12. Depending on the number of operations, the selective gas collection and generation process (20) for collecting nitrogen, the selective gas storage process (30) for compressing and storing the collected nitrogen into the gas storage tank (A5), and a microbubble generator (B) for the compressed and stored nitrogen ) in the selective gas pressure supply process (40), the microbubble generation dissolved process (50) for generating nitrogen dissolved water (D1), and the dissolved sap ratio for supplying the nitrogen dissolved water (D1) to the crops with the pump (P) The input process (60) proceeds in one cycle.

Then, the water tank C is filled with water D by the control unit A1, and the control unit A1 of the gas selection generator A is configured to include the ammonia count button A12a, “0”, In this case, it proceeds to the next setting section except for the operation of the button for which the number of times of operation of the tank is set.

Then, the water tank C is filled with water D by the control unit A1, and the control unit A1 of the gas selection generator A is set to the “1” water tank of the standby number button A13. Depending on the number of operations, the selective gas collection and generation process (20) for collecting the atmosphere, the selective gas storage process (30) for compressing and storing the collected air into the gas storage tank (A5), and a microbubble generating device (B) for the compressed and stored atmosphere ) in the selective gas pressure supply process (40), the microbubble generation dissolved process (50) for generating atmospheric dissolved water (D1), and the dissolved sap ratio for supplying the atmospheric dissolved water (D1) to the crops with the pump (P). The input process (60) proceeds in one cycle.

Then, the inside of the water tank C is filled with water D by the control unit A1, and the control unit A1 of the gas selection generator A is configured to the nitric acid number button A13a, “0”, In this case, it proceeds to the next setting section except for the operation of the button for which the number of times of operation of the tank is set.

Then, the water tank C is filled with water D by the control unit A1, and the control unit A1 of the gas selective generating device A controls the tank “1” of the ozone count button A14. Depending on the number of operations, the selective gas collection and generation process (20) in which oxygen is captured by the oxygen generator (A2), the captured oxygen is converted into ozone using the ozone generator (A4), and compressed and stored in the gas storage tank (A5) a selective gas storage process 30, a selective gas pressure supply process 40 for supplying compressed and stored ozone to the microbubble generating device B, a microbubble generating and dissolving process 50 for generating ozone-dissolved water D1, A non-dissolved sap non-injection process (60) of supplying ozone-dissolved water (D1) to crops with a pump (P) is performed in one cycle.

In this way, in the control unit A1, the oxygen count button A11 is “3”, the nitrogen count button A12 is “1”, the ammonia count buttons A12a and “0”, the standby count button A13 is “1”, The nitric acid frequency button (A13a), "0", and ozone frequency button A14 are all executed as many times as the number of operation of the water tank set to "1".

As described above, the present invention uses a gas selective generator (A) and a microbubble generator (B) to supply oxygen-rich water (D1) rich in dissolved oxygen to crops by irrigation and side spraying to facilitate the proliferation of aerobic microorganisms. Induces fertility and inhibits harmful bacteria and aerobic microorganisms to balance fungi in soil and medium or hydroponic and aquaponics farming methods, improves root growth during crop growth, and increases the growth rate of aerobic microorganisms during crop harvest Root development and growth growth of crops are activated, and thus crop yield can be further increased.

In addition, by supplying nitrogen-dissolved water (D1) rich in dissolved nitrogen to the crops to more smoothly increase the yield through photosynthesis of the leaves using the canopy and phloem from the fine roots, the growth growth and crop yield can be further increased. there will be

In addition, by supplying ammonium-dissolved water (D1) rich in dissolved ammonia to crops, the fine roots obtained with nitrogen-fixing bacteria from root-knot bacteria can maximize the absorption effect of nitrogen fertilizers and help crops produce glucose and proteins and nucleic acids. It contributes to the creation of fertile soil by breeding bacteria to be beneficial to the growth of fine roots.

In addition, atmospheric dissolved water (D1) rich in dissolved atmosphere ionizes greenhouse gas carbon dioxide and supplies it to crops to induce continuous growth in a well-balanced state of crop growth and growth.

In addition, by supplying nitrate dissolved water (D1) rich in dissolved nitric acid to crops, it induces aerobic fungal growth of nitrifying bacteria important for nitrogen assimilation and further maximizes plant-based conditions of glucose, protein, and nucleic acid to increase harvest. It plays a role in maintaining the balance of important bacterial reproduction, and it becomes a nature-friendly circulation method that is repeated into the gaseous atmosphere by denitrification.

In addition, by supplying ozone-dissolved water (D1) rich in dissolved ozone to crops, it kills, suppresses, and avoids molds, fungi, worms, bacteria, and viruses, and oxidizes and decomposes heavy metals to activate the root growth and growth of crops. It is possible to increase crop yields sustainably at low cost.

This embodiment and the drawings attached to this specification merely clearly show some of the technical ideas included in the present invention, and those skilled in the art can easily infer within the scope of the technical ideas included in the specification and drawings of the present invention. It is obvious that all possible modifications and specific embodiments are included in the scope of the technical spirit of the present invention.

The scope of the present invention is indicated by the following claims rather than the detailed description, and all changes or modifications derived from the meaning and scope of the claims and equivalent concepts should be construed as being included in the scope of the present invention.

10: Capture gas selection setting process
20: Selective gas capture and generation process
30: Selective gas storage process
40: Selective gas pressure supply process
50: microbubble generation dissolution process
60: Dissolved sap non-injection process
A: Gas selective generator
A1: Control
A11 : Oxygen count button
A12 : Nitrogen count button
A12a; Ammonia Count Button
A12aa ; hydrogen generator
A12ba ; catalysis
A13 : Wait count button
A13a : Nitric acid count button
A13aa; plasma generator
A14 : Ozone count button
A2 : Oxygen generator
A3 : Nitrogen generator
A4 : Ozone generator
A5 : Gas storage tank
A6 : Compressor
A7: supply pipe
B: Micro bubble generator
C: water tank
D: water
D1: dissolved water
P: pump
S1, S2: water level sensor
S/W: Power switch
T: timer

Claims (17)

Power is applied through the control unit (A1) of the gas selection generator (A), and the number of water tank operation and a collection gas selection setting process (10) of setting a time to execute the collection and storage of the gas as many times as the number of times of operation of the tank;
In order to generate any one selected from among oxygen, nitrogen, atmosphere, and ozone in the control unit A1 of the collection gas selection setting process 10, the surrounding air is sucked and compressed with the gas selective generator A through a filter and sucked. a selective gas collection and generation process (20) in which only the gas selected in the collection gas selection setting process (10) is left in the compressed air and the remaining gas is separated and discharged to generate only the selected gas;
a selective gas storage process (30) of compressing and storing any one selected from oxygen, nitrogen, air, and ozone, which are gases generated through the selective gas collection and generation process (20), in a gas storage tank (A5);
A microbubble generating device ( B) a selective gas pressure supply process (40);
The microbubble generating device (B) supplied with any one selected from oxygen, nitrogen, air, and ozone through the selective gas pressure supply process (40) is a gas supplied from inside the water tank (C) filled with water (D). a microbubble generation and dissolution process (50) of rapidly dissolving in water (D) inside the water tank (C) by generating microbubbles with any one selected from oxygen, nitrogen, air, and ozone; and
Gas characterized in that it consists of a dissolved sap non-injection process (60) in which the dissolved water (D1) inside the water tank (C), which has undergone the microbubble generation and dissolution process (50), is used as the liquid manure of the farm through the pump (P). A liquid fertilizer manufacturing method using a selective generator and a microbubble generator. The method of claim 1,
As the gas selective generator (A), an oxygen generator (A2) is used, the surrounding air is sucked and compressed and transferred to the adsorption bed, and only oxygen in the adsorption bed is supplied to the gas storage tank (A5) at a concentration of 90% or more. A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that other gases including nitrogen are separately discharged. 3. The method of claim 2,
When the oxygen generator (A2) is used as the gas selective generator (A), the gas selective generator and the microbubble generator, characterized in that only nitrogen is collected from the gas containing nitrogen remaining after oxygen generation and stored in a separate nitrogen tank A method of manufacturing liquid fertilizer using The method of claim 1,
As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked and compressed to pass through a tank filled with oxygen adsorbent (CMS) and only nitrogen at a concentration of 90% or more in a gas storage tank (A5) ), the oxygen adsorbed on the oxygen adsorbent (CMS) is separately discharged and discharged separately. 5. The method of claim 4,
When the nitrogen generator (A3) is used as the gas selective generator (A), only oxygen adsorbed to the oxygen adsorbent (CMS) is collected and stored in a separate oxygen tank after nitrogen is generated. A method for manufacturing liquid fertilizer using a device. 5. The method of claim 4,
As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked and compressed to pass through a tank filled with oxygen adsorbent (CMS) and only nitrogen at a concentration of 90% or more in a gas storage tank (A5) ), the oxygen adsorbed on the oxygen adsorbent (CMS) is separately discharged, and when ammonia (A12a) is selected, it is electrolyzed by the hydrogen generator (A12aa) in the water tank (C) and the oxygen from + is released into the air. A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that ammonium ion nitrogen is produced by the catalytic reaction (A12ba). The method of claim 1,
As the gas selective generator (A), a compressor (A6) is used, and the surrounding air is compressed by suction and supplied to the gas storage tank (A5). A liquid phase using a gas selective generator and a microbubble generator Fertilizer manufacturing method. 8. The method of claim 7,
As the gas selective generator (A), a compressor (A6) is used, the surrounding air is sucked and compressed and supplied to the gas storage tank (A5), and when nitric acid (A13a) is selected, high temperature and high pressure like air discharge (lightning) A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that nitrogen nitrate ions are generated by separating a nitrogen link made of a triple bond with the generated plasma generator (A13aa). The method of claim 1,
As the gas selective generator (A), the oxygen generator (A2) is used to suck and compress the surrounding air and transport it to the adsorption bed, and only oxygen in the adsorption bed generates oxygen that is more than 90% concentrated. A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that receiving oxygen and using an ozone generator (A4) to change oxygen into ozone and supply it through a silent discharge action. The method of claim 1,
The control unit A1 of the gas selection generator A sets the capacity of the water tank C according to the needs of the crop by the user by the water level sensors S1 and S2, and the set capacity of the water tank C Oxygen number button (A11), nitrogen number button (A12), standby number button that can set the number of times of operation of the tank in one cycle to fill the water (D) and supply it all to the crops by filling it with water (D1) (A13), the ozone frequency button (A14) is further provided, respectively, and the number of times of operation of the tank is set in advance to "0 ~ 20" according to the need for crop growth, and operation of the button with the number of times of operation of the tank set to "0" is excluded And, according to the set number of operation of the water tank, the dissolved water (D1) inside the water tank (C) is dissolved in oxygen by the oxygen generator (A2), the nitrogen generator (A3), the compressor (A6), and the ozone generator (A4), respectively. Water, nitrogen-dissolved water, atmospheric dissolved water, ozone-dissolved water is sequentially filled as many times as the number of tank operations, and each dissolved water (D1) inside the tank (C) is supplied to the crops sequentially as many times as the number of tank operations with the pump (P). A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator. 11. The method of claim 10,
The control unit (A1) of the gas selection generator (A),
Each of an ammonia count button (A12a) and a nitric acid count button (A13a) is further provided,
When ammonia is selected with the ammonia count button (A12a), it is electrolyzed by the hydrogen generator (A12aa) in the water tank (C), and oxygen from + is released into the air and ammonium ion nitrogen is generated due to the catalyst reaction (A12ba). C) Ammonium dissolved water is formed inside, and when nitric acid is selected with the nitric acid number button (A13a), a plasma generator (A13aa) that generates high temperature and high pressure like air discharge (lightning) separates the nitrogen link made of triple bonds to nitrate ions A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that nitrogen is generated and nitrate dissolved water is formed inside the water tank (C). Power is applied through the control unit (A1) of the gas selection generator (A), and the number of water tank operation and a collection gas selection setting process (10) of setting a time to execute the collection and storage of the gas as many times as the number of times of operation of the tank;
In order to generate any one selected from among oxygen, nitrogen, atmosphere, and ozone in the control unit A1 of the collection gas selection setting process 10, the surrounding air is sucked and compressed with the gas selective generator A through a filter and sucked. a selective gas collection and generation process (20) in which only the gas selected in the collection gas selection setting process (10) is left in the compressed air and the remaining gas is separated and discharged to generate only the selected gas;
The inside of the water tank (C) filled with water (D) through the supply pipe (A7) at a constant pressure of any one gas selected among oxygen, nitrogen, air, and ozone, which is the gas generated through the selective gas collection and generation process (20) Selective gas pressure supply process 40 for supplying to the microbubble generating device (B) located in the;
The microbubble generating device (B) supplied with any one selected from oxygen, nitrogen, air, and ozone through the selective gas pressure supply process (40) is a gas supplied from inside the water tank (C) filled with water (D). a microbubble generation and dissolution process (50) of rapidly dissolving and processing microbubbles in water (D) inside the water tank (C) by generating microbubbles with any one selected from oxygen, nitrogen, air, and ozone; and
Gas characterized in that it consists of a non-dissolved sap non-injection process (60) in which the dissolved water (D1) inside the water tank (C), which has undergone the microbubble generation and dissolution process (50), is used as the liquid manure of the farm through the pump (P). A liquid fertilizer manufacturing method using a selective generator and a microbubble generator. 13. The method of claim 12,
As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked and compressed to pass through a tank filled with oxygen adsorbent (CMS) and only nitrogen at a concentration of 90% or more to the supply pipe (A7). A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that the oxygen adsorbed to the oxygen adsorbent (CMS) is separately discharged while supplying. 14. The method of claim 13,
As the gas selective generator (A), when ammonia (A12a) is selected, oxygen generated from + is electrolyzed by the hydrogen generator (A12aa) in the water tank (C) and released into the air and ammonium ions due to the catalytic reaction (A12ba) A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that nitrogen is generated. 14. The method of claim 13,
As the gas selective generator (A), when nitric acid (A13a) is selected, a plasma generator (A13aa) that generates high-temperature and high-pressure like air discharge (lightning) separates a nitrogen link made of a triple bond to generate nitrate ion nitrogen A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator as a feature. 13. The method of claim 12,
As the gas selective generator (A), an oxygen generator (A2) is used, the surrounding air is sucked and compressed and transferred to the adsorption bed, and only oxygen in the adsorption bed is supplied to the supply pipe (A7) at a concentration of 90% or more while nitrogen is supplied. A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that other gases, including those, are separately discharged. 13. The method of claim 12,
As the gas selective generator (A), the oxygen generator (A2) is used to suck and compress the surrounding air and transport it to the adsorption bed, and only oxygen in the adsorption bed generates oxygen that is more than 90% concentrated. A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that receiving oxygen and using an ozone generator (A4) to change oxygen into ozone and supply it through a silent discharge action.

Images