KR102666275B1 - Liquid fertilizer manufacturing method using gas-selective generators and microbubble generating device - Google Patents
Liquid fertilizer manufacturing method using gas-selective generators and microbubble generating device Download PDFInfo
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- KR102666275B1 KR102666275B1 KR1020210033743A KR20210033743A KR102666275B1 KR 102666275 B1 KR102666275 B1 KR 102666275B1 KR 1020210033743 A KR1020210033743 A KR 1020210033743A KR 20210033743 A KR20210033743 A KR 20210033743A KR 102666275 B1 KR102666275 B1 KR 102666275B1
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- gas
- generator
- nitrogen
- water
- oxygen
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 65
- 239000007788 liquid Substances 0.000 title claims abstract description 33
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 24
- 239000007789 gas Substances 0.000 claims abstract description 229
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 192
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 169
- 238000000034 method Methods 0.000 claims abstract description 136
- 230000008569 process Effects 0.000 claims abstract description 122
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 106
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 106
- 239000001301 oxygen Substances 0.000 claims abstract description 106
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 96
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 59
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 48
- 238000003860 storage Methods 0.000 claims abstract description 45
- 230000012010 growth Effects 0.000 claims abstract description 44
- 239000012298 atmosphere Substances 0.000 claims abstract description 41
- XLYOFNOQVPJJNP-DYCDLGHISA-N deuterium hydrogen oxide Chemical compound [2H]O XLYOFNOQVPJJNP-DYCDLGHISA-N 0.000 claims abstract description 28
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 26
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 24
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 24
- 238000004090 dissolution Methods 0.000 claims abstract description 16
- 239000003463 adsorbent Substances 0.000 claims description 14
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 10
- 238000002347 injection Methods 0.000 claims description 9
- 239000007924 injection Substances 0.000 claims description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 8
- 239000001257 hydrogen Substances 0.000 claims description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims description 8
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 7
- 238000006555 catalytic reaction Methods 0.000 claims description 7
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 7
- -1 nitric acid ions Chemical class 0.000 claims description 6
- 229910002651 NO3 Inorganic materials 0.000 claims description 4
- 238000001514 detection method Methods 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 241000894006 Bacteria Species 0.000 abstract description 30
- 244000005700 microbiome Species 0.000 abstract description 18
- 239000002689 soil Substances 0.000 abstract description 18
- 230000001965 increasing effect Effects 0.000 abstract description 15
- 230000021749 root development Effects 0.000 abstract description 15
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 11
- 230000002786 root growth Effects 0.000 abstract description 11
- 238000003306 harvesting Methods 0.000 abstract description 10
- 102000039446 nucleic acids Human genes 0.000 abstract description 10
- 108020004707 nucleic acids Proteins 0.000 abstract description 10
- 150000007523 nucleic acids Chemical class 0.000 abstract description 10
- 102000004169 proteins and genes Human genes 0.000 abstract description 10
- 108090000623 proteins and genes Proteins 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 9
- 241000233866 Fungi Species 0.000 abstract description 8
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 abstract description 7
- 239000008103 glucose Substances 0.000 abstract description 7
- 230000035755 proliferation Effects 0.000 abstract description 6
- 241000238631 Hexapoda Species 0.000 abstract description 5
- 241000700605 Viruses Species 0.000 abstract description 5
- 238000010521 absorption reaction Methods 0.000 abstract description 5
- 230000003213 activating effect Effects 0.000 abstract description 5
- 230000001580 bacterial effect Effects 0.000 abstract description 5
- 239000001569 carbon dioxide Substances 0.000 abstract description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 5
- 238000009313 farming Methods 0.000 abstract description 5
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 5
- 230000001939 inductive effect Effects 0.000 abstract description 5
- 230000001546 nitrifying effect Effects 0.000 abstract description 5
- 239000000618 nitrogen fertilizer Substances 0.000 abstract description 5
- 230000000243 photosynthetic effect Effects 0.000 abstract description 5
- 238000005507 spraying Methods 0.000 abstract description 5
- 230000009286 beneficial effect Effects 0.000 abstract description 4
- 230000002538 fungal effect Effects 0.000 abstract description 4
- 239000005431 greenhouse gas Substances 0.000 abstract description 4
- 238000003973 irrigation Methods 0.000 abstract description 4
- 230000002262 irrigation Effects 0.000 abstract description 4
- 230000001902 propagating effect Effects 0.000 abstract description 4
- 230000009229 glucose formation Effects 0.000 abstract description 3
- 230000001590 oxidative effect Effects 0.000 abstract description 2
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 9
- 238000001179 sorption measurement Methods 0.000 description 8
- 239000000126 substance Substances 0.000 description 8
- 241000196324 Embryophyta Species 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000000813 microbial effect Effects 0.000 description 5
- 239000011259 mixed solution Substances 0.000 description 5
- 239000005445 natural material Substances 0.000 description 5
- 235000015097 nutrients Nutrition 0.000 description 5
- 229910052717 sulfur Inorganic materials 0.000 description 5
- 239000011593 sulfur Substances 0.000 description 5
- 239000006227 byproduct Substances 0.000 description 4
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 3
- 241000245665 Taraxacum Species 0.000 description 3
- 235000005187 Taraxacum officinale ssp. officinale Nutrition 0.000 description 3
- 235000011941 Tilia x europaea Nutrition 0.000 description 3
- 239000012190 activator Substances 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 238000000855 fermentation Methods 0.000 description 3
- 230000004151 fermentation Effects 0.000 description 3
- 239000004571 lime Substances 0.000 description 3
- 239000000575 pesticide Substances 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 235000003261 Artemisia vulgaris Nutrition 0.000 description 2
- 240000006891 Artemisia vulgaris Species 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 208000035240 Disease Resistance Diseases 0.000 description 2
- 240000000691 Houttuynia cordata Species 0.000 description 2
- 235000013719 Houttuynia cordata Nutrition 0.000 description 2
- 241000124033 Salix Species 0.000 description 2
- 239000004115 Sodium Silicate Substances 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000002361 compost Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 229910000160 potassium phosphate Inorganic materials 0.000 description 2
- 235000011009 potassium phosphates Nutrition 0.000 description 2
- 235000019795 sodium metasilicate Nutrition 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- 244000301850 Cupressus sempervirens Species 0.000 description 1
- 241001632410 Eleutherococcus senticosus Species 0.000 description 1
- 206010061291 Mineral deficiency Diseases 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 244000205939 Rhizopus oligosporus Species 0.000 description 1
- 235000000471 Rhizopus oligosporus Nutrition 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 230000003042 antagnostic effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000015165 citric acid Nutrition 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000004009 herbicide Substances 0.000 description 1
- 239000003864 humus Substances 0.000 description 1
- 239000010903 husk Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 235000015816 nutrient absorption Nutrition 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 235000011181 potassium carbonates Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 235000015170 shellfish Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/10—Addition or removal of substances other than water or air to or from the material during the treatment
- C05F17/15—Addition or removal of substances other than water or air to or from the material during the treatment the material being gas
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/231—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids by bubbling
- B01F23/23105—Arrangement or manipulation of the gas bubbling devices
- B01F23/2312—Diffusers
- B01F23/23121—Diffusers having injection means, e.g. nozzles with circumferential outlet
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
- C01B13/0248—Physical processing only
- C01B13/0259—Physical processing only by adsorption on solids
- C01B13/0262—Physical processing only by adsorption on solids characterised by the adsorbent
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/10—Preparation of ozone
- C01B13/11—Preparation of ozone by electric discharge
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/02—Preparation of nitrogen
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/04—Purification or separation of nitrogen
- C01B21/0405—Purification or separation processes
- C01B21/0433—Physical processing only
- C01B21/045—Physical processing only by adsorption in solids
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/20—Nitrogen oxides; Oxyacids of nitrogen; Salts thereof
- C01B21/38—Nitric acid
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C11/00—Other nitrogenous fertilisers
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
- C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
- C05F17/90—Apparatus therefor
- C05F17/964—Constructional parts, e.g. floors, covers or doors
- C05F17/971—Constructional parts, e.g. floors, covers or doors for feeding or discharging materials to be treated; for feeding or discharging other material
- C05F17/979—Constructional parts, e.g. floors, covers or doors for feeding or discharging materials to be treated; for feeding or discharging other material the other material being gaseous
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G5/00—Fertilisers characterised by their form
- C05G5/20—Liquid fertilisers
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Analytical Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Microbiology (AREA)
- Molecular Biology (AREA)
- Biotechnology (AREA)
- Biochemistry (AREA)
- Health & Medical Sciences (AREA)
- Pest Control & Pesticides (AREA)
- Fertilizers (AREA)
Abstract
본 발명은 기체선택발생장치(A)의 제어부(A1)를 통해 전원을 인가하고, 제어부(A1)에서 포집하여 저장시킬 기체를 산소, 질소, 대기, 오존 중 어느 하나 또는 둘 이상을 선택하면서 수조가동횟수와 시간을 설정하여 그 기체의 포집과 저장을 수조가동횟수만큼 실행하도록 설정하는 포집기체선택설정과정(10);
상기 포집기체선택설정과정(10)의 제어부(A1)에서 산소, 질소, 대기, 오존 중 선택된 어느 하나를 생성하기 위하여 상기 기체선택발생장치(A)로 주변의 공기를 필터를 통해 흡입압축하고 흡입압축된 공기 중 상기 포집기체선택설정과정(10)에서 선택된 기체만을 남기고 나머지 기체는 분리배출시켜 선택된 기체만을 생성시키는 선택기체포집생성과정(20);
상기 선택기체포집생성과정(20)을 통해서 생성된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나를 기체보관탱크(A5)에 압축보관하는 선택기체보관과정(30);
상기 선택기체보관과정(30)을 통해 기체보관탱크(A5)에 보관중인 기체를 일정압력으로 공급관(A7)을 통해 물(D)이 가득찬 수조(C) 내부에 위치된 마이크로버블생성장치(B)로 공급하는 선택기체압력공급과정(40);
상기 선택기체압력공급과정(40)을 통해 산소, 질소, 대기, 오존 중 선택된 어느 하나를 공급받은 마이크로버블생성장치(B)가 물(D)이 가득찬 수조(C) 내부에서 공급된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나로 마이크로버블을 생성시켜 수조(C) 내부의 물(D)에 빠르게 용존처리하는 마이크로버블생성용존과정(50); 및
상기 마이크로버블생성용존과정(50)을 거친 수조(C) 내부의 용존수(D1)를 펌프(P)를 통해 농장의 액비로 사용하는 용존수액비투입과정(60)으로 이루어짐을 특징으로 하는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법에 관한 것이다.
이러한 본 발명은 기체선택발생장치와 마이크로버블생성장치를 사용하여 용존산소가 풍부한 산소용존수를 작물에게 관주 및 옆면살포로 공급하여 호기성 미생물의 증식을 원활하게 유도하고, 유해균 및 협기성 미생물을 억제시켜 토양 및 배지 또는 수경재배 및 아쿠아포닉스 농법에 균류의 균형을 이루며, 작물 성장시 작물의 뿌리 발육이 좋아지고, 작물 수확시 호기성 미생물의 증식율을 높여 작물의 뿌리 발육 및 생육성장이 활성화되어 작물 수확량을 보다 증대시킬 수 있으며, 용존질소가 풍부한 질소용존수를 작물에게 공급하여 잔 뿌리로부터 수관 및 체관을 이용하여 잎의 광합성 작용을 통한 수확량을 보다 원활하게 증대되도록 유도함으로써 생육성장 및 작물 수확량을 보다 증대시킬 수 있고, 용존암모니아가 풍부한 암모늄용존수를 작물에게 공급하여 뿌리혹박테리아로 부터 질소고정세균을 얻은 잔뿌리는 질소비료 흡수 효과를 극대화 할 수 있게 하고 작물이 포도당 생성에 필요한 단백질, 핵산 도움을 주며 잔뿌리성장에 유익하도록 세균 번식을 해 비옥한 땅 조성에 기여를 하며, 용존대기가 풍부한 대기용존수는 온실가스 이산화탄소를 이온화시켜 작물에게 공급하여 작물 생육성장의 균형이 잘 이루어진 상태에서 지속적으로 성장할 수 있도록 유도하며, 용존질산이 풍부한 질산염용존수를 작물에게 공급하여 질소동화작용에 중요한 질화세균의 호기성 균 류 증식을 유발하며 수확을 증대하기위한 포도당, 단백질, 핵산의 식물 기반 조건을 더 극대화하는 중요한 세균 번식의 균형을 유지하는 역할을 하고 탈질소 작용에 의한 기체상태 대기로 반복되는 자연 친화적 순환 방법이 되며, 용존오존이 풍부한 오존용존수를 작물에게 공급하여 곰팡이 균류나 벌레 충류 및 박테리아나 바이러스를 사멸시키거나 억제 및 기피처리하고, 중금속을 산화분해시켜 작물의 뿌리 발육과 생육성장을 활성화시키면서 작물 수확량을 저렴한 비용으로 지속가능하게 증대시킬 수 있는 효과가 있다.In the present invention, power is applied through the control unit (A1) of the gas selection generator (A), and the control unit (A1) selects one or more of oxygen, nitrogen, atmosphere, and ozone to collect and store the gas in the water tank. A collection gas selection setting process (10) that sets the number of operations and time to capture and store the gas as many times as the number of tank operations;
In the control unit (A1) of the capture gas selection setting process (10), the surrounding air is sucked and compressed through the filter by the gas selection generator (A) to generate any one selected among oxygen, nitrogen, atmosphere, and ozone. A selective gas collection and generation process (20) in which only the gas selected in the capture gas selection and setting process (10) is left in the compressed air and the remaining gases are separated and discharged to generate only the selected gas;
A selective gas storage process (30) of compressing and storing any one of oxygen, nitrogen, atmosphere, and ozone, which are gases generated through the selective gas collection and generation process (20), in a gas storage tank (A5);
Through the selective gas storage process (30), the gas stored in the gas storage tank (A5) is supplied at a constant pressure through the supply pipe (A7), and a microbubble generator located inside the water tank (C) filled with water (D) ( Select gas pressure supply process (40) supplied to B);
The microbubble generator (B), which receives any one selected from oxygen, nitrogen, atmosphere, and ozone through the selective gas pressure supply process (40), is supplied with the gas supplied from inside the water tank (C) filled with water (D). A microbubble generation and dissolution process (50) in which microbubbles are generated with one selected from oxygen, nitrogen, atmosphere, and ozone and quickly dissolved in the water (D) inside the water tank (C); and
A gas characterized in that it consists of a dissolved sap fertilizer input process (60) in which the dissolved water (D1) inside the water tank (C) that has undergone the microbubble generation dissolved process (50) is used as a liquid fertilizer for the farm through a pump (P). This relates to a method of manufacturing liquid fertilizer using a selective generator and a microbubble generator.
The present invention uses a gas selective generator and a microbubble generator to supply oxygenated water rich in dissolved oxygen to crops by irrigation and side spraying, thereby smoothly inducing the growth of aerobic microorganisms and suppressing harmful bacteria and aerobic microorganisms. It achieves a balance of fungi in the soil and medium or in hydroponic and aquaponics farming methods, improves root development of crops during crop growth, and increases the proliferation rate of aerobic microorganisms when harvesting crops, thereby activating crop root development and growth. Yields can be further increased, and nitrogen-dissolved water rich in dissolved nitrogen is supplied to crops to increase yield more smoothly through the photosynthetic action of leaves using crowns and phloem from fine roots, thereby improving growth growth and crop yield. By supplying ammonium-dissolved water rich in dissolved ammonia to crops, fine roots that obtain nitrogen-fixing bacteria from root nodule bacteria can maximize the effect of nitrogen fertilizer absorption and help crops with proteins and nucleic acids necessary for glucose production. It contributes to the creation of fertile land by propagating bacteria beneficial to the growth of fine roots, and dissolved atmospheric water, which is rich in dissolved air, ionizes the greenhouse gas carbon dioxide and supplies it to crops, allowing crops to grow continuously in a well-balanced state. By supplying nitrate-dissolved water 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 for glucose, protein, and nucleic acid to increase harvest. It plays a role in maintaining the balance of important bacterial reproduction and becomes a nature-friendly circulation method that is repeated in the gaseous atmosphere through denitrification, and supplies ozone-dissolved water rich in dissolved ozone to crops, eliminating mold, insects, bacteria, and viruses. It has the effect of killing, suppressing, and avoiding treatment, oxidizing and decomposing heavy metals, activating root development and growth of crops, and sustainably increasing crop yield at low cost.
Description
본 발명은 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법에 관한 것으로서, 보다 상세하게는 기체선택발생장치와 마이크로버블생성장치를 사용하여 용존산소가 풍부한 산소용존수를 작물에게 관주 및 옆면살포로 공급하여 호기성 미생물의 증식을 원활하게 유도하고, 유해균 및 협기성 미생물을 억제시켜 토양 및 배지 또는 수경재배 및 아쿠아포닉스 농법에 균류의 균형을 이루며, 작물 성장시 작물의 뿌리 발육이 좋아지고, 작물 수확시 호기성 미생물의 증식율을 높여 작물의 뿌리 발육 및 생육성장이 활성화되어 작물 수확량을 보다 증대시킬 수 있으며, 용존질소가 풍부한 질소용존수를 작물에게 공급하여 잔 뿌리로부터 수관 및 체관을 이용하여 잎의 광합성 작용을 통한 수확량을 보다 원활하게 증대되도록 유도함으로써 생육성장 및 작물 수확량을 보다 증대시킬 수 있고, 용존암모니아가 풍부한 암모늄용존수를 작물에게 공급하여 뿌리혹박테리아로 부터 질소고정세균을 얻은 잔뿌리는 질소비료 흡수 효과를 극대화 할 수 있게 하고 작물이 포도당 생성에 필요한 단백질, 핵산 도움을 주며 잔뿌리성장에 유익하도록 세균 번식을 해 비옥한 땅 조성에 기여를 하며, 용존대기가 풍부한 대기용존수는 온실가스 이산화탄소를 이온화시켜 작물에게 공급하여 작물 생육성장의 균형이 잘 이루어진 상태에서 지속적으로 성장할 수 있도록 유도하며, 용존질산이 풍부한 질산염용존수를 작물에게 공급하여 질소동화작용에 중요한 질화세균의 호기성 균 류 증식을 유발하며 수확을 증대하기위한 포도당, 단백질, 핵산의 식물 기반 조건을 더 극대화하는 중요한 세균 번식의 균형을 유지하는 역할을 하고 탈질소 작용에 의한 기체상태 대기로 반복되는 자연 친화적 순환 방법이 되며, 용존오존이 풍부한 오존용존수를 작물에게 공급하여 곰팡이 균류나 벌레 충류 및 박테리아나 바이러스를 사멸시키거나 억제 및 기피처리하고, 중금속을 산화분해시켜 작물의 뿌리 발육과 생육성장을 활성화시키면서 작물 수확량을 저렴한 비용으로 지속가능하게 증대시킬 수 있는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법에 관한 것이다. The present invention relates to a method of manufacturing liquid fertilizer using a gas selective generator and a microbubble generator. More specifically, the present invention relates to a method of irrigating crops with oxygenated water rich in dissolved oxygen using a gas selective generator and a microbubble generator. By supplying it through side spraying, it smoothly induces the growth of aerobic microorganisms, suppresses harmful bacteria and aerobic microorganisms, achieves a balance of fungi in soil and media, or in hydroponic and aquaponics farming methods, and improves root development of crops when growing crops. By increasing the proliferation rate of aerobic microorganisms when harvesting crops, the root development and growth of crops are activated, thereby increasing crop yield. By supplying nitrogen-dissolved water rich in dissolved nitrogen to crops, they use crowns and phloem from fine roots. By inducing the yield to increase more smoothly through the photosynthetic action of the leaves, growth growth and crop yield can be further increased, and by supplying ammonium-dissolved water rich in dissolved ammonia to the crops, fine roots obtain nitrogen-fixing bacteria from root nodule bacteria. It maximizes the effect of nitrogen fertilizer absorption, helps crops with the proteins and nucleic acids needed to produce glucose, and propagates bacteria beneficial to the growth of fine roots, contributing to the creation of fertile land. By ionizing gas carbon dioxide and supplying it to crops, it induces continuous growth in a well-balanced state of crop growth and growth, and by supplying nitrate-dissolved water rich in dissolved nitric acid to crops, aerobic fungi of nitrifying bacteria, which are important in nitrogen assimilation, are used. It plays a role in maintaining the balance of important bacterial reproduction that further maximizes the plant-based conditions of glucose, proteins, and nucleic acids to induce proliferation and increase harvest, and is a natural and friendly circulation method that is repeated into the gaseous atmosphere by denitrification. By supplying ozone-dissolved water rich in dissolved ozone to crops, it kills, suppresses, and evades mold, insects, bacteria, and viruses, and oxidizes and decomposes heavy metals to activate root development and growth of crops, thereby increasing crop yield. This relates to a method of manufacturing liquid fertilizer using a gas selective generator and a microbubble generator that can be sustainably increased at low cost.
일반적으로 유기질 비료라 함은 무기질 비료(화학비료)와의 상대적 개념으로서, 유기물을 주원료로 하는 유기질비료와 부산물을 주원료로 하는 부산물비료를 포함하며, 이러한 유기질 또는 부산물 비료의 원료에는 부숙겨, 재, 분뇨잔사, 부엽토, 아미노산발효부산비료, 부숙왕겨, 톱밥 또는 토양 미생물제제 등이 있다. In general, organic fertilizer is a relative concept with inorganic fertilizer (chemical fertilizer), and includes organic fertilizers made from organic matter as the main raw material and by-product fertilizers made from by-products as the main raw material. Raw materials for such organic or by-product fertilizers include boiled bran, ash, These include manure residue, humus soil, amino acid fermentation by-product fertilizer, composted rice husk, sawdust, or soil microbial agents.
이중에서 화학비료는 대부분 토양에 시비되면 한번에 빨리 녹는 속효성이며, 시비 직후 일시적으로 토양에 영양분이 풍부해진다. 하지만 식물은 단기간에 시비된 영양분을 한꺼번에 흡수하거나 이용할 수 없다. 그 결과 식물이 흡수 못하고 남은 영양분이 토양으로 스며들어 토양, 지하수, 및 하천을 오염시키는 원인이 되기도 한다. Among them, most chemical fertilizers are fast-acting, dissolving quickly when applied to the soil, and the soil is temporarily enriched with nutrients immediately after application. However, plants cannot absorb or utilize nutrients applied in a short period of time all at once. As a result, the remaining nutrients that plants cannot absorb seep into the soil, causing contamination of soil, groundwater, and rivers.
우리 나라의 토양은 장기간에 걸친 화학비료 위주의 시비(施肥), 농약과 화학제초제의 과다한 사용, 한 가지 작물의 연작(連作) 등으로 인하여 작물의 생육불량, 품질 저하, 내병성(耐病性) 저하, 농작물 오염, 수확량 감소, 생산성 저하 등을 야기하고 있다. Our country's soil suffers from poor crop growth, poor quality, and reduced disease resistance due to long-term fertilization with chemical fertilizers, excessive use of pesticides and chemical herbicides, and continuous cultivation of one crop. , causing crop contamination, reduced yield, and decreased productivity.
또한, 농후 화학비료와 농약의 사용은 심각한 염류집적 현상을 유발하기도 하고, 과다하게 살포된 영양분 간의 길항작용으로 인해 미네랄 결핍 등에 의한 연쇄적인 장애가 발생하기도 해 농작물의 내병성이 저하되고, 생육불량 등으로 수확이 감소하며, 품질과 맛이 저하되는 등의 문제가 발생되기도 하였다. In addition, the use of concentrated chemical fertilizers and pesticides can cause serious salt accumulation, and the antagonistic effect between excessively sprayed nutrients can cause chain disorders due to mineral deficiencies, etc., resulting in reduced disease resistance of crops and poor growth. Problems such as decreased harvest and decreased quality and taste also occurred.
최근에는 환경오염 문제와 함께 이러한 농작물 오염문제가 심각하게 대두되면서 화학비료나 농약을 사용하기보다는 양질의 유기질 비료나 완숙퇴비를 사용하는 농법개발이 확산되어, 많은 유기질 비료의 개발이 지속적으로 시도되고 있다.Recently, as agricultural pollution problems have become more serious along with environmental pollution problems, the development of agricultural methods that use high-quality organic fertilizers or mature compost rather than chemical fertilizers or pesticides has spread, and the development of many organic fertilizers has been continuously attempted. there is.
그러나 이런 노력에도 불구하고, 화학비료의 대안으로서 사용되는 유기질 비료 및 퇴비의 집중적 사용은 재료학적으로만 차이가 있을 뿐 화학제와 비슷한 또 다른 문제점을 심화시키고 있다. 토양 산도는 토양 자체의 특성이나 영양분의 유효성, 미생물 활성 등 여러 가지에 영향을 미치고 있으며, 특히 농작물의 생육과 밀접한 영양분흡수에 크게 영향을 주고 있다. However, despite these efforts, the intensive use of organic fertilizers and compost, which are used as alternatives to chemical fertilizers, is deepening another problem that is similar to chemical agents, with only material differences. Soil acidity affects many things, including the characteristics of the soil itself, the availability of nutrients, and microbial activity, and especially has a significant impact on nutrient absorption, which is closely related to the growth of crops.
따라서, 농작물의 생육을 향상시키기 위하여 산성화된 농토를 알칼리성화된 농토를 중성(PH6.5~7)화된 농토로 교정하고자 많은 시도가 이루어지고 있으며, 일반적으로 생석회비료, 소석회 비료, 돌로마이트비료(고토비료), 석고비료 및 조개가루비료(패화석 분말비료) 등 칼슘 및 유황을 함유하고 있는 석회계, 유황계 물질등을 다량 토양개량제 비료로 사용되고 있다. Therefore, in order to improve the growth of crops, many attempts are being made to change acidic farmland to alkaline farmland to neutral (PH 6.5~7) farmland. In general, quicklime fertilizer, slaked lime fertilizer, and dolomite fertilizer (gosoil) are used. A large amount of lime-based and sulfur-based substances containing calcium and sulfur, such as fertilizers), gypsum fertilizers, and shellfish fertilizers (shell powder fertilizers), are used as soil improvement fertilizers.
그러나 석회계, 유황계 비료에 함유된 칼슘(Ca), 황(S)이 토양을 경화(硬化)시킬 수 있기에, 석회계나 유황계 단독비료의 대량 사용은 점차 기피되고 있다. 따라서, 이와 같은 부작용을 해결하면서도 농작물의 성장을 증진시키는 효과가 있는 비료 개발의 필요성이 제기되고 있으며, 특히, 천연물을 이용한 비료의 수요가 증가하고 있는 추세이다.However, because the calcium (Ca) and sulfur (S) contained in lime-based and sulfur-based fertilizers can harden the soil, the large-scale use of lime-based or sulfur-based fertilizers alone is gradually being avoided. Accordingly, there is a need to develop fertilizers that have the effect of improving the growth of crops while solving these side effects. In particular, the demand for fertilizers using natural products is increasing.
이런 문제점을 해결하기 위하여, "물에 메타규산소다, 인산칼륨, 탄산칼륨 및 구연산을 포함하는 재료들을 용해하여 혼합액을 제조하는 혼합액 제조 단계(S100); 버드나무, 도꼬마리, 참쑥, 순비기나무, 소리쟁이, 민들레 및 어성초를 포함하는 천연재료를 준비한 후 혼합하는 천연재료 준비 및 혼합 단계(S200); 상기 혼합된 천연재료를 발효시키는 천연재료 발효 단계(S300); 상기 발효된 천연재료와 상기 혼합액을 혼합한 후 발효를 더 진행시켜 천연추출물을 제조하는 천연추출물 제조단계(S400); 미생물 활성화제를 제조하는 미생물 활성화제 제조 단계(S500); 및 상기 천연추출물과 미생물 활성화제를 혼합하여 액상비료를 제조하는 액상비료 제조 단계(S600)를 포함하고, 상기 혼합액 제조 단계(S100)에서 상기 혼합액은 물 전체 1000 중량부에 대해 메타규산소다 70 내지 100 중량부, 인산칼륨 60 내지 90 중량부, 탄산칼륨 15 내지 25 중량부 및 구연산 1 내지 2 중량부의 중량 비율로 혼합한 후 교반하여 제조되고, 상기 천연재료 준비 및 혼합 단계(S200)에서 상기 준비된 천연재료는 버드나무, 도꼬마리, 참쑥, 순비기나무, 소리쟁이, 민들레 및 어성초가 각각 1:1:1:1:1:1:1의 중량 비율로 혼합되며, 상기 천연재료 발효 단계(S300)에서 상기 미생물로는 리조푸스 올리고스포러스(Rhizopus oligosporus) 또는 사카로마이세스 세레비지에(Saccharomyces cerevisiae) 중에서 선택되는 어느 하나 이상의 미생물이 사용되고, 상기 미생물은 상기 혼합된 천연재료 100 중량부에 대해 1 내지 3 중량부의 중량 비율로 혼합되며, 상기 천연추출물 제조 단계(S400)에서는 상기 혼합액 전체 100 중량부에 대해 상기 발효된 천연재료 30 내지 50 중량부의 중량 비율로 혼합한 후 45 내지 50℃의 온도에서 5 내지 10일 동안 발효를 더 진행시켜 천연추출물을 제조하고, 상기 액상비료 제조 단계(S600)에서 상기 액상비료는 상기 액상비료는 천연추출물 100 내지 200 중량부 및 미생물 활성화제 10 내지 30 중량부의 중량 비율로 혼합되어 제조된 것을 특징으로 하는 식물 뿌리 생육 촉진용 액상비료의 제조방법."이 특허등록 제10-2118923호(2020.06.04. 공고)로 개시된바 있었다.In order to solve this problem, "mixed solution preparation step (S100) of preparing a mixed solution by dissolving materials including sodium metasilicate, potassium phosphate, potassium carbonate, and citric acid in water; willow, orientalis, mugwort, and citric acid, A natural material preparation and mixing step (S200) of preparing and mixing natural materials including dandelion, dandelion, and Houttuynia cordata (S300); fermenting the mixed natural materials (S300); A natural extract manufacturing step (S400) of mixing and then further fermenting to produce a microbial activator (S500) and mixing the natural extract and the microbial activator to produce a liquid fertilizer; It includes a liquid fertilizer manufacturing step (S600) of preparing a liquid fertilizer, and in the mixed solution manufacturing step (S100), the mixed solution contains 70 to 100 parts by weight of sodium metasilicate, 60 to 90 parts by weight of potassium phosphate, and carbonic acid for 1000 parts by weight of the total water. It is prepared by mixing 15 to 25 parts by weight of potassium and 1 to 2 parts by weight of citric acid and then stirring, and in the natural material preparation and mixing step (S200), the prepared natural materials are willow, cypress, mugwort, and Siberian ginseng. , dandelion, and Houttuynia cordata are mixed at a weight ratio of 1:1:1:1:1:1:1, respectively, and in the natural material fermentation step (S300), the microorganism is Rhizopus oligosporus. ) or Saccharomyces cerevisiae, one or more microorganisms selected from among are used, the microorganisms are mixed at a weight ratio of 1 to 3 parts by weight based on 100 parts by weight of the mixed natural material, and the natural extract In the manufacturing step (S400), the fermented natural material is mixed at a weight ratio of 30 to 50 parts by weight with respect to the total 100 parts by weight of the mixed solution, and then fermentation is further performed for 5 to 10 days at a temperature of 45 to 50 ° C. to produce a natural extract. In the liquid fertilizer manufacturing step (S600), the liquid fertilizer is prepared by mixing 100 to 200 parts by weight of natural extract and 10 to 30 parts by weight of microbial activator. Plant root growth. “Method for manufacturing liquid fertilizer for promotion.” Patent registration No. 10-2118923 (2020.06.04. It had been commenced with a notice).
그러나 이런 종래의 액상비료는, 많은 종류의 천연재료를 구입 및 채취하여 발효시키는 과정에서 많은 시간과 많은 비용이 추가적으로 소요되므로 실질적으로 농가에서 보편적으로 사용하기에는 시간과 비용이 많은 부담되는 금적적인 문제점이 있었다. However, these conventional liquid fertilizers require a lot of additional time and money in the process of purchasing and collecting many types of natural ingredients and fermenting them, so they have financial problems that make it difficult to use them universally in farms. there was.
본 발명은 상기와 같은 문제점을 해결하기 위한 것으로서, 기체선택발생장치와 마이크로버블생성장치를 사용하여 용존산소가 풍부한 산소용존수를 작물에게 관주 및 옆면살포로 공급하여 호기성 미생물의 증식을 원활하게 유도하고, 유해균 및 협기성 미생물을 억제시켜 토양 및 배지 또는 수경재배 및 아쿠아포닉스 농법에 균류의 균형을 이루며, 작물 성장시 작물의 뿌리 발육이 좋아지고, 작물 수확시 호기성 미생물의 증식율을 높여 작물의 뿌리 발육 및 생육성장이 활성화되어 작물 수확량을 보다 증대시킬 수 있으며, 용존질소가 풍부한 질소용존수를 작물에게 공급하여 잔 뿌리로부터 수관 및 체관을 이용하여 잎의 광합성 작용을 통한 수확량을 보다 원활하게 증대되도록 유도함으로써 생육성장 및 작물 수확량을 보다 증대시킬 수 있고, 용존암모니아가 풍부한 암모늄용존수를 작물에게 공급하여 뿌리혹박테리아로 부터 질소고정세균을 얻은 잔뿌리는 질소비료 흡수 효과를 극대화 할 수 있게 하고 작물이 포도당 생성에 필요한 단백질, 핵산 도움을 주며 잔뿌리성장에 유익하도록 세균 번식을 해 비옥한 땅 조성에 기여를 하며, 용존대기가 풍부한 대기용존수는 온실가스 이산화탄소를 이온화시켜 작물에게 공급하여 작물 생육성장의 균형이 잘 이루어진 상태에서 지속적으로 성장할 수 있도록 유도하며, 용존질산이 풍부한 질산염용존수를 작물에게 공급하여 질소동화작용에 중요한 질화세균의 호기성 균 류 증식을 유발하며 수확을 증대하기위한 포도당, 단백질, 핵산의 식물 기반 조건을 더 극대화하는 중요한 세균 번식의 균형을 유지하는 역할을 하고 탈질소 작용에 의한 기체상태 대기로 반복되는 자연 친화적 순환 방법이 되며, 용존오존이 풍부한 오존용존수를 작물에게 공급하여 곰팡이 균류나 벌레 충류 및 박테리아나 바이러스를 사멸시키거나 억제 및 기피처리하고, 중금속을 산화분해시켜 작물의 뿌리 발육과 생육성장을 활성화시키면서 작물 수확량을 저렴한 비용으로 지속가능하게 증대시킬 수 있는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법을 제공함에 그 목적이 있다.The present invention is intended to solve the above problems, and uses a gas selective generator and a microbubble generator to smoothly induce the growth of aerobic microorganisms by supplying oxygenated water rich in dissolved oxygen to crops through irrigation and side spraying. By suppressing harmful bacteria and aerobic microorganisms, it achieves a balance of fungi in soil and media or hydroponic and aquaponics farming methods, improves root development of crops when growing crops, and increases the proliferation rate of aerobic microorganisms when harvesting crops, thereby improving crop growth. By activating root development and growth, crop yield can be further increased, and by supplying nitrogen-dissolved water rich in dissolved nitrogen to crops, the yield can be more smoothly increased through the photosynthetic action of leaves using crowns and phloem from fine roots. By inducing it as much as possible, growth growth and crop yield can be further increased, and by supplying ammonium-dissolved water rich in dissolved ammonia to crops, fine roots obtained from nitrogen-fixing bacteria from root nodule bacteria can maximize the effect of nitrogen fertilizer absorption, and the crop can It provides proteins and nucleic acids necessary for glucose production and contributes to the creation of fertile land by propagating bacteria to benefit the growth of fine roots. Dissolved atmospheric water, which is rich in dissolved air, ionizes the greenhouse gas carbon dioxide and supplies it to crops, contributing to crop growth and growth. It induces continuous growth in a well-balanced state, supplies crops with nitrate-dissolved water rich in dissolved nitric acid, induces aerobic fungal growth of nitrifying bacteria important for nitrogen assimilation, and provides glucose, protein, and It plays a role in maintaining the balance of important bacterial reproduction that further maximizes the plant-based conditions of nucleic acids, and becomes a nature-friendly circulation method that is repeated into the gaseous atmosphere by denitrification, and supplies ozone-dissolved water rich in dissolved ozone to crops. Selective gas generation that kills, suppresses, and repels fungi, insects, bacteria, and viruses, oxidizes and decomposes heavy metals, and activates root development and growth of crops while sustainably increasing crop yield at low cost. The purpose is to provide a method for manufacturing liquid fertilizer using a device and a microbubble generator.
본 발명이 해결하고자 하는 과제는 이상에 언급한 과제들에 제한되지 않으며, 언급되지 않는 또 다른 과제들은 아래의 기재로부터 당업자에게 명확하게 이해될 수 있을 것이다.The problems to be solved by the present invention are not limited to the problems mentioned above, and other problems not mentioned will be clearly understood by those skilled in the art from the description below.
이와 같은 목적을 달성하기 위하여, 본 발명은, 기체선택발생장치(A)의 제어부(A1)를 통해 전원을 인가하고, 제어부(A1)에서 포집하여 저장시킬 기체를 산소, 질소, 대기, 오존 중 어느 하나 또는 둘 이상을 선택하면서 수조가동횟수와 시간을 설정하여 그 기체의 포집과 저장을 수조가동횟수만큼 실행하도록 설정하는 포집기체선택설정과정(10);In order to achieve this purpose, the present invention applies power through the control unit (A1) of the gas selection generator (A), and collects and stores the gas in the control unit (A1) among oxygen, nitrogen, atmosphere, and ozone. A collection gas selection setting process (10) of selecting one or more than two and setting the number of tank operations and time to capture and store the gas as many times as the number of tank operations;
상기 포집기체선택설정과정(10)의 제어부(A1)에서 산소, 질소, 대기, 오존 중 선택된 어느 하나를 생성하기 위하여 상기 기체선택발생장치(A)로 주변의 공기를 필터를 통해 흡입압축하고 흡입압축된 공기 중 상기 포집기체선택설정과정(10)에서 선택된 기체만을 남기고 나머지 기체는 분리배출시켜 선택된 기체만을 생성시키는 선택기체포집생성과정(20);In the control unit (A1) of the capture gas selection setting process (10), the surrounding air is sucked and compressed through the filter by the gas selection generator (A) to generate any one selected among oxygen, nitrogen, atmosphere, and ozone. A selective gas collection and generation process (20) in which only the gas selected in the capture gas selection and setting process (10) is left in the compressed air and the remaining gases are separated and discharged to generate only the selected gas;
상기 선택기체포집생성과정(20)을 통해서 생성된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나를 기체보관탱크(A5)에 압축보관하는 선택기체보관과정(30);A selective gas storage process (30) of compressing and storing any one of oxygen, nitrogen, atmosphere, and ozone, which are gases generated through the selective gas collection and generation process (20), in a gas storage tank (A5);
상기 선택기체보관과정(30)을 통해 기체보관탱크(A5)에 보관중인 기체를 콤프레샤(A6)의 일정압력으로 공급관(A7)을 통해 물(D)이 가득찬 수조(C) 내부에 위치된 마이크로버블생성장치(B)로 공급하는 선택기체압력공급과정(40);Through the selected gas storage process (30), the gas stored in the gas storage tank (A5) is placed inside the water tank (C) filled with water (D) through the supply pipe (A7) at a constant pressure of the compressor (A6). Selective gas pressure supply process (40) supplied to the microbubble generating device (B);
상기 선택기체압력공급과정(40)을 통해 산소, 질소, 대기, 오존 중 선택된 어느 하나를 공급받은 마이크로버블생성장치(B)가 물(D)이 가득찬 수조(C) 내부에서 공급된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나로 마이크로버블을 생성시켜 수조(C) 내부의 물(D)에 빠르게 용존처리하는 마이크로버블생성용존과정(50); 및The microbubble generator (B), which receives any one selected from oxygen, nitrogen, atmosphere, and ozone through the selective gas pressure supply process (40), is supplied with the gas supplied from inside the water tank (C) filled with water (D). A microbubble generation and dissolution process (50) in which microbubbles are generated with one selected from oxygen, nitrogen, atmosphere, and ozone and quickly dissolved in the water (D) inside the water tank (C); and
상기 마이크로버블생성용존과정(50)을 거친 수조(C) 내부의 용존수(D1)를 펌프(P)를 통해 농장의 액비로 사용하는 용존수액비투입과정(60)으로 이루어짐을 특징이 있다.It is characterized by a dissolved sap fertilizer injection process (60) in which the dissolved water (D1) inside the water tank (C) that has undergone the microbubble generation and dissolution process (50) is used as liquid fertilizer for the farm through a pump (P).
상기 기체선택발생장치(A)로는, 산소발생기(A2)를 사용하고, 주변의 공기를 흡입압축하여 흡착베드로 이송하고 흡착베드 내에서 산소만을 90%이상의 농도로 기체보관탱크(A5)로 공급하면서 질소를 포함한 그 외의 기체는 별도로 분리배출되는 특징이 있다.The gas selective generator (A) uses an oxygen generator (A2), sucks in and compresses the surrounding air, transfers it to the adsorption bed, and supplies only oxygen in the adsorption bed to the gas storage tank (A5) at a concentration of 90% or more. Other gases, including nitrogen, have the characteristic of being discharged separately.
상기 기체선택발생장치(A)로 산소발생기(A2)를 사용시, 산소생성 후 남은 질소를 포함하는 기체에서 질소만을 포집하여 별도로 질소탱크에 저장하는 특징이 있다.When using the oxygen generator (A2) as the gas selective generator (A), only nitrogen is collected from the nitrogen-containing gas remaining after oxygen generation and stored separately in a nitrogen tank.
상기 기체선택발생장치(A)로는, 질소발생기(A3)를 사용하고, 주변의 공기를 흡입압축하여 산소흡착제(CMS)로 가득찬 탱크를 통과하면서 90%이상의 농도로 질소만을 기체보관탱크(A5)로 공급하면서 산소흡착제(CMS)에 흡착된 산소는 별도로 분리배출되는 특징이 있다.As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked in and compressed to pass through a tank full of oxygen adsorbent (CMS), and only nitrogen at a concentration of 90% or more is stored in the gas storage tank (A5). ), the oxygen adsorbed on the oxygen adsorbent (CMS) has the characteristic of being separated and discharged separately.
상기 기체선택발생장치로 질소발생기를 사용시, 질소생성 후 산소흡착제(CMS)에 흡착된 산소만을 포집하여 별도의 산소탱크에 저장하는 특징이 있다.When using a nitrogen generator as the gas selective generator, only the oxygen adsorbed on the oxygen adsorbent (CMS) is collected after nitrogen is generated and stored in a separate oxygen tank.
상기 기체선택발생장치(A)로는, 질소발생기(A3)를 사용하고, 주변의 공기를 흡입압축하여 산소흡착제(CMS)로 가득찬 탱크를 통과하면서 90%이상의 농도로 질소만을 기체보관탱크(A5)로 공급하면서 산소흡착제(CMS)에 흡착된 산소는 별도로 분리배출되며, 암모니아(A12a) 선택시 수조(C)내의 수소발생장치(A12aa)에 의해 전기분해되어 +에서 나오는 산소는 공기중으로 방출하고 촉매반응(A12ba)으로 인해 암모늄이온질소가 생성되는 특징이 있다.As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked in and compressed to pass through a tank full of oxygen adsorbent (CMS), and only nitrogen at a concentration of 90% or more is stored in the gas storage tank (A5). ), the oxygen adsorbed on the oxygen adsorbent (CMS) is separated and discharged separately, and when ammonia (A12a) is selected, the oxygen coming from + is electrolyzed by the hydrogen generator (A12aa) in the water tank (C) and released into the air. It has the characteristic of producing ammonium ion nitrogen due to a catalytic reaction (A12ba).
상기 기체선택발생장치(A)로는, 콤프레샤(A6)를 사용하고, 주변의 공기를 흡입압축하여 기체보관탱크(A5)로 공급하는 특징이 있다.The gas selective generator (A) uses a compressor (A6), sucks in and compresses surrounding air, and supplies it to the gas storage tank (A5).
상기 기체선택발생장치(A)로는, 콤프레샤(A6)를 사용하고, 주변의 공기를 흡입압축하여 기체보관탱크(A5)로 공급하며, 질산(A13a) 선택시 공중방전(번개)처럼 고온고압이 생성되는 플라즈마발생장치(A13aa)로 삼중결합으로 이루어진 질소 연결고리를 분리하여 질산이온질소가 생성되는 특징이 있다.The gas selection generator (A) uses a compressor (A6), sucks in and compresses the surrounding air, and supplies it to the gas storage tank (A5). When nitric acid (A13a) is selected, high temperature and high pressure are generated like an aerial discharge (lightning). It has the characteristic of generating nitrate ion nitrogen by separating the nitrogen chain consisting of a triple bond using the plasma generator (A13aa).
상기 기체선택발생장치(A)로는, 산소발생기(A2)를 사용하여 주변의 공기를 흡입압축하여 흡착베드로 이송하고 흡착베드 내에서 산소만을 90%이상의 농축된 산소를 생성하고, 이렇게 생성된 농축된 산소를 받아 오존발생기(A4)를 사용하여 무성방전 작용을 통해서 산소를 오존으로 변화시켜 공급하는 특징이 있다.The gas selective generator (A) uses an oxygen generator (A2) to suction and compress the surrounding air, transfers it to the adsorption bed, and generates oxygen concentrated to more than 90% of oxygen in the adsorption bed. It has the characteristic of receiving oxygen and converting it into ozone through a silent discharge using an ozone generator (A4).
상기 기체선택발생장치(A)의 제어부(A1)는, 사용자가 작물의 필요에 의해 수조(C)의 용량을 수위감지센서(S1,S2)에 의해 설정하고, 그 수조(C)의 설정된 용량에 따라 물(D)을 가득 채우고 이를 각종 용존수(D1)로 만들어 작물에게 모두 공급하는 1싸이클의 수조가동횟수를 설정할 수 있는 산소횟수버튼(A11), 질소횟수버튼(A12), 대기횟수버튼(A13), 오존횟수버튼(A14)을 각각 더 구비하여, 작물 생육의 필요에 따라서 수조가동회수를 미리 "0 ~ 20"으로 설정함으로써, "0"으로 수조가동횟수가 설정된 버튼의 가동은 제외하고, 그 설정된 수조가동횟수에 따라서, 수조(C) 내부의 용존수(D1)를, 산소발생기(A2), 질소발생기(A3), 콤프레샤(A6), 오존발생기(A4)에 의해 각각 산소용존수, 질소용존수, 대기용존수, 오존용존수로 수조가동횟수만큼 순차적으로 채워서 수조(C) 내부의 각 용존수(D1)를 펌프(P)로 작물에게 순차적으로 수조가동횟수만큼 공급시키는 특징이 있다.The control unit (A1) of the gas selection generator (A) allows the user to set the capacity of the water tank (C) according to the needs of the crops using the water level detection sensors (S1 and S2), and the set capacity of the water tank (C) The oxygen count button (A11), nitrogen count button (A12), and standby count button allow you to set the number of tank operations for one cycle, which fills water (D), turns it into various dissolved water (D1), and supplies it to the crops. (A13) and an ozone count button (A14) are further provided to set the water tank operation number in advance to "0 to 20" according to the needs of crop growth, excluding the operation of the button whose water tank operation number is set to "0". And, according to the set number of water tank operations, the dissolved water (D1) inside the water tank (C) is converted into dissolved oxygen by the oxygen generator (A2), nitrogen generator (A3), compressor (A6), and ozone generator (A4). The feature is that the tank is sequentially filled with water, nitrogen dissolved water, atmospheric dissolved water, and ozone dissolved water as many times as the tank is operated, and each dissolved water (D1) inside the tank (C) is sequentially supplied to the crops by the pump (P) as many times as the tank is operated. There is.
상기 기체선택발생장치(A)의 제어부(A1)는, The control unit (A1) of the gas selection generator (A),
암모니아횟수버튼(A12a), 질산횟수버튼(A13a)을 각각 더 구비하고, Further equipped with an ammonia count button (A12a) and a nitric acid count button (A13a),
암모니아횟수버튼(A12a)으로 암모니아 선택시 수조(C)내의 수소발생장치(A12aa)에 의해 전기분해되어 +에서 나오는 산소는 공기중으로 방출하고 촉매반응(A12ba)으로 인해 암모늄이온질소가 생성되어 수조(C) 내부에 암모늄용존수가 형성되며, 질산횟수버튼(A13a)으로 질산 선택시 공중방전(번개)처럼 고온고압이 생성되는 플라즈마발생장치(A13aa)로 삼중결합으로 이루어진 질소 연결고리를 분리하여 질산이온질소가 생성되어 수조(C) 내부에 질산염용존수가 형성되는 특징이 있다.When ammonia is selected with the ammonia number button (A12a), it is electrolyzed by the hydrogen generator (A12aa) in the water tank (C), and the oxygen from + is released into the air, and ammonium ion nitrogen is generated through the catalytic reaction (A12ba) and the water tank (C) C) Ammonium dissolved water is formed inside, and when nitric acid is selected with the nitric acid number button (A13a), a high temperature and high pressure is generated like an air discharge (lightning) using the plasma generator (A13aa), which separates the nitrogen chain consisting of a triple bond to produce nitric acid ions. Nitrogen is produced and nitrate dissolved water is formed inside the water tank (C).
본 발명은, 기체선택발생장치(A)의 제어부(A1)를 통해 전원을 인가하고, 제어부(A1)에서 포집하여 저장시킬 기체를 산소, 질소, 대기, 오존 중 어느 하나 또는 둘 이상을 선택하면서 수조가동횟수와 시간을 설정하여 그 기체의 포집과 저장을 수조가동횟수만큼 실행하도록 설정하는 포집기체선택설정과정(10);In the present invention, power is applied through the control unit (A1) of the gas selection generator (A), and the control unit (A1) selects one or more of oxygen, nitrogen, atmosphere, and ozone as the gas to be collected and stored. A collection gas selection setting process (10) of setting the number and time of water tank operations to capture and store the gas as many times as the number of water tank operations;
상기 포집기체선택설정과정(10)의 제어부(A1)에서 산소, 질소, 대기, 오존 중 선택된 어느 하나를 생성하기 위하여 상기 기체선택발생장치(A)로 주변의 공기를 필터를 통해 흡입압축하고 흡입압축된 공기 중 상기 포집기체선택설정과정(10)에서 선택된 기체만을 남기고 나머지 기체는 분리배출시켜 선택된 기체만을 생성시키는 선택기체포집생성과정(20);In the control unit (A1) of the capture gas selection setting process (10), the surrounding air is sucked and compressed through the filter by the gas selection generator (A) to generate any one selected among oxygen, nitrogen, atmosphere, and ozone. A selective gas collection and generation process (20) in which only the gas selected in the capture gas selection and setting process (10) is left in the compressed air and the remaining gases are separated and discharged to generate only the selected gas;
상기 선택기체포집생성과정(20)을 통해서 생성된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나의 기체를 일정압력으로 공급관(A7)을 통해 물(D)이 가득찬 수조(C) 내부에 위치된 마이크로버블생성장치(B)로 공급하는 선택기체압력공급과정(40);Inside the water tank (C) filled with water (D) through the supply pipe (A7) at a constant pressure with one of the gases selected from oxygen, nitrogen, atmosphere, and ozone, which are gases generated through the selective gas collection and generation process (20). Selective gas pressure supply process (40) supplied to the microbubble generating device (B) located in;
상기 선택기체압력공급과정(40)을 통해 산소, 질소, 대기, 오존 중 선택된 어느 하나를 공급받은 마이크로버블생성장치(B)가 물(D)이 가득찬 수조(C) 내부에서 공급된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나로 마이크로버블을 생성시켜 수조(C) 내부의 물(D)에 빠르게 용존처리하는 마이크로버블생성용존과정(50); 및The microbubble generator (B), which receives any one selected from oxygen, nitrogen, atmosphere, and ozone through the selective gas pressure supply process (40), is supplied with the gas supplied from inside the water tank (C) filled with water (D). A microbubble generation and dissolution process (50) in which microbubbles are generated with one selected from oxygen, nitrogen, atmosphere, and ozone and quickly dissolved in the water (D) inside the water tank (C); and
상기 마이크로버블생성용존과정(50)을 거친 수조(C) 내부의 용존수(D1)를 펌프(P)를 통해 농장의 액비로 사용하는 용존수액비투입과정(60)으로 이루어지는 특징이 있다.It is characterized by a dissolved sap fertilizer injection process (60) in which the dissolved water (D1) inside the water tank (C) that has undergone the microbubble generation and dissolution process (50) is used as liquid fertilizer for the farm through a pump (P).
이와 같이, 본 발명은 기체선택발생장치와 마이크로버블생성장치를 사용하여 용존산소가 풍부한 산소용존수를 작물에게 관주 및 옆면살포로 공급하여 호기성 미생물의 증식을 원활하게 유도하고, 유해균 및 협기성 미생물을 억제시켜 토양 및 배지 또는 수경재배 및 아쿠아포닉스 농법에 균류의 균형을 이루며, 작물 성장시 작물의 뿌리 발육이 좋아지고, 작물 수확시 호기성 미생물의 증식율을 높여 작물의 뿌리 발육 및 생육성장이 활성화되어 작물 수확량을 보다 증대시킬 수 있으며, 용존질소가 풍부한 질소용존수를 작물에게 공급하여 잔 뿌리로부터 수관 및 체관을 이용하여 잎의 광합성 작용을 통한 수확량을 보다 원활하게 증대되도록 유도함으로써 생육성장 및 작물 수확량을 보다 증대시킬 수 있고, 용존암모니아가 풍부한 암모늄용존수를 작물에게 공급하여 뿌리혹박테리아로 부터 질소고정세균을 얻은 잔뿌리는 질소비료 흡수 효과를 극대화 할 수 있게 하고 작물이 포도당 생성에 필요한 단백질, 핵산 도움을 주며 잔뿌리성장에 유익하도록 세균 번식을 해 비옥한 땅 조성에 기여를 하며, 용존대기가 풍부한 대기용존수는 온실가스 이산화탄소를 이온화시켜 작물에게 공급하여 작물 생육성장의 균형이 잘 이루어진 상태에서 지속적으로 성장할 수 있도록 유도하며, 용존질산이 풍부한 질산염용존수를 작물에게 공급하여 질소동화작용에 중요한 질화세균의 호기성 균 류 증식을 유발하며 수확을 증대하기위한 포도당, 단백질, 핵산의 식물 기반 조건을 더 극대화하는 중요한 세균 번식의 균형을 유지하는 역할을 하고 탈질소 작용에 의한 기체상태 대기로 반복되는 자연 친화적 순환 방법이 되며, 용존오존이 풍부한 오존용존수를 작물에게 공급하여 곰팡이 균류나 벌레 충류 및 박테리아나 바이러스를 사멸시키거나 억제 및 기피처리하고, 중금속을 산화분해시켜 작물의 뿌리 발육과 생육성장을 활성화시키면서 작물 수확량을 저렴한 비용으로 지속가능하게 증대시킬 수 있는 효과가 있다.In this way, the present invention uses a gas selective generator and a microbubble generator to supply oxygenated water rich in dissolved oxygen to crops by irrigation and side spraying, thereby smoothly inducing the growth of aerobic microorganisms and eliminating harmful bacteria and aerobic microorganisms. It suppresses the balance of fungi in soil and media or hydroponic and aquaponics farming methods, improves root development of crops when growing, and increases the proliferation rate of aerobic microorganisms when harvesting crops, activating root development and growth of crops. It is possible to further increase crop yield, and by supplying nitrogen-dissolved water rich in dissolved nitrogen to crops, it is induced to increase the yield more smoothly through the photosynthetic action of leaves using crowns and phloem from fine roots, thereby improving the growth and growth of crops. Yields can be further increased, and by supplying ammonium-dissolved water rich in dissolved ammonia to crops, fine roots obtained with nitrogen-fixing bacteria from root nodule bacteria can maximize the effect of nitrogen fertilizer absorption, and proteins and nucleic acids necessary for crops to produce glucose. It contributes to the creation of fertile soil by propagating bacteria beneficial to the growth of fine roots, and dissolved atmospheric water, which is rich in dissolved air, ionizes greenhouse gas carbon dioxide and supplies it to crops, maintaining a well-balanced growth and growth of crops. By supplying nitrate-dissolved water rich in dissolved nitric acid to crops, it induces aerobic fungal growth of nitrifying bacteria, which are important for nitrogen assimilation, and provides 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 is a nature-friendly circulation method that is repeated in the gaseous atmosphere through denitrification, and supplies ozone-dissolved water rich in dissolved ozone to crops to prevent fungi, insects, and bacteria. It has the effect of killing, suppressing, and avoiding viruses, oxidizing and decomposing heavy metals, activating root development and growth of crops, and sustainably increasing crop yield at a low cost.
본 발명은 상술한 특정의 바람직한 실시 예에 한정되지 아니하며, 청구범위에서 청구하는 본 발명의 요지를 벗어남이 없이 당해 발명이 속하는 기술분야에서 통상의 지식을 가진 자라면 누구든지 다양한 변형 실시가 가능한 것은 물론이고, 그와 같은 변경은 청구범위 기재의 범위 내에 있게 된다.The present invention is not limited to the specific preferred embodiments described above, and various modifications can be made by anyone skilled in the art without departing from the gist of the invention as claimed in the claims. Of course, such changes are within the scope of the claims.
도 1은 본 발명 실시 예인 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법을 시간차에 의해 나열한 순서도,
도 2는 본 발명 실시 예인 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법의 작동 개요를 나타낸 설명도,
도 3은 본 발명 실시 예인 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법 중 콤프레샤를 사용않을 시의 작동 개요를 나타낸 설명도.Figure 1 is a flow chart listing the liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, which are embodiments of the present invention, by time difference;
Figure 2 is an explanatory diagram showing the operation outline of a liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, which is an embodiment of the present invention;
Figure 3 is an explanatory diagram showing the operation outline when a compressor is not used in the liquid fertilizer manufacturing method using the gas selective generator and the microbubble generator, which is an embodiment of the present invention.
이하, 본 발명을 첨부된 도면에 의해 보다 상세하게 설명하면 다음과 같다.Hereinafter, the present invention will be described in more detail with the accompanying drawings.
이하, 첨부한 도면을 참조하여 본 발명의 실시 예에 대하여 본 발명에 속하는 기술분야에서 통상의 지식을 가진 자가 용이하게 실시할 수 있도록 상세히 설명한다. 본 발명은 여러 가지 상이한 형태로 구현될 수 있으며 여기에서 설명하는 실시 예에 한정되지 않는다.Hereinafter, with reference to the attached drawings, embodiments of the present invention will be described in detail so that those skilled in the art can easily implement the present invention. The present invention may be implemented in many different forms and is not limited to the embodiments described herein.
도면에서 본 발명을 명확하게 설명하기 위해서 설명과 관계없는 부분은 생략하였으며, 명세서 전체를 통하여 동일 또는 유사한 구성요소에 대해서는 동일한 참조부호를 붙였다. 본 발명의 권리범위는 본문에 설명된 실시 예에 의하여 제한되는 것으로 해석되어서는 아니되며, 실시 예는 다양한 변경이 가능하고 여러 가지 형태를 가질 수 있으므로 본 발명의 권리범위는 기술적 사상을 실현할 수 있는 균등물들을 포함하는 것으로 이해되어야 한다. In order to clearly explain the present invention in the drawings, parts not related to the description are omitted, and identical or similar components are given the same reference numerals throughout the specification. The scope of rights of the present invention should not be construed as being limited by the embodiments described in the text, and since the embodiments can be modified in various ways and may have various forms, the scope of rights of the present invention should not be construed as limited by the embodiments described in the text. It should be understood to include equivalents.
본 발명의 명세서 전체에서, 어떤 부분이 다른 부분과 "연결"되어 있다고 할 때, 이는 "직접적으로 연결"되어 있는 경우 뿐만 아니라, 다른 부재를 사이에 두고 "간접적으로 연결"된 것도 포함한다. 또한, 어떤 부분이 어떤 구성요소를 "포함"한다고 할 때, 이는 특별히 반대되는 기재가 없는 한 다른 구성요소를 제외하는 것이 아니라 다른 구성요소를 더 포함할 수 있는 것을 의미한다.Throughout the specification of the present invention, when a part is said to be “connected” to another part, this includes not only “directly connected” but also “indirectly connected” through another member. Additionally, when a part is said to “include” a certain component, this means that it may further include other components, rather than excluding other components, unless specifically stated to the contrary.
본 발명에서 사용되는 용어들은 본 발명에서의 기능을 고려하여 정의된 용어들로서, 이는 사용자, 운용자의 의도 또는 관례에 따라 달라질 수 있으므로, 이러한 용어들에 대한 정의는 본 발명의 기술적 사항에 부합되는 의미와 개념으로 해석되어야 할 것이다.The terms used in the present invention are terms defined in consideration of the functions in the present invention, and may vary depending on the intention or custom of the user or operator, so the definitions of these terms are defined in accordance with the technical details of the present invention. It should be interpreted as a concept.
그리고, 아래 실시 예에서의 선택적인 용어는 하나의 구성요소를 다른 구성요소로부터 구별하기 위해 사용되는 것으로서, 구성요소가 상기 용어들에 의해 제한되는 것은 아니다. 이하, 본 발명을 설명함에 있어서, 본 발명의 요지를 불필요하게 흐릴 수 있는 관련된 공지기술에 대한 상세한 설명은 생략한다.Additionally, optional terms in the examples below are used to distinguish one component from another component, 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.
본 발명의 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법은, 포집기체선택설정과정(10)과, 선택기체포집생성과정(20)과, 선택기체보관과정(30)과, 선택기체압력공급과정(40)과, 마이크로버블생성용존과정(50)과, 용존수액비투입과정(60)으로 이루어진다.The liquid fertilizer manufacturing method using the gas selection generator and the microbubble generator of the present invention includes a capture gas selection and setting process (10), a selection gas collection and generation process (20), a selection gas storage process (30), and a selection process. It consists of a gas pressure supply process (40), a microbubble generation and dissolution process (50), and a dissolved sap injection process (60).
상기 포집기체선택설정과정(10)은, 기체선택발생장치(A)의 제어부(A1)를 통해 전원을 인가하고, 제어부(A1)에서 포집하여 저장시킬 기체를 산소, 질소, 암모니아, 대기, 질산, 오존 중 어느 하나 또는 둘 이상을 선택하면서 수조가동횟수를 설정하여 그 기체의 포집과 저장을 수조가동횟수만큼 수동 또는 자동으로 실행하도록 설정하는 과정이다. 이를 자동적으로 수행하는 것이 바람직하나, 이를 선택적으로 수동으로 수행할 수도 있음은 물론이다. 이를 위해서 자동선택스위치와 수동선택스위치를 별도로 형성함이 바람직하다.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 in the control unit (A1) is selected as oxygen, nitrogen, ammonia, atmosphere, and nitric acid. , It is a process of selecting one or more of ozone and setting the number of tank operations to capture and store the gas manually or automatically according to the number of tank operations. It is desirable to perform this automatically, but of course it can also be optionally performed manually. For this purpose, it is desirable to form an automatic selection switch and a manual selection switch separately.
상기 선택기체포집생성과정(20)은, 상기 포집기체선택설정과정(10)의 제어부(A1)에서 산소, 질소, 암모니아, 대기, 질산, 오존을 선택하여 생성하기 위하여 상기 기체선택발생장치(A)로 주변의 공기를 필터를 통해 흡입압축하고 흡입압축된 공기 중 상기 포집기체선택설정과정(10)에서 선택된 기체만을 남기고 나머지 기체는 분리배출시켜 선택된 기체만을 생성시키는 과정이다.The selective gas collection and generation process (20) is performed by the control unit (A1) of the capture gas selection and setting process (10) to select and generate oxygen, nitrogen, ammonia, atmosphere, nitric acid, and ozone. ) is a process of suctioning and compressing the surrounding air through a filter, leaving only the gas selected in the capture gas selection setting process (10) among the suctioned and compressed air, and separating and discharging the remaining gases to generate only the selected gas.
상기 선택기체보관과정(30)은, 상기 선택기체포집생성과정(20)을 통해서 생성된 기체인 산소, 질소, 암모니아, 대기, 질산, 오존 중 선택된 어느 하나 또는 둘 이상을 공급받아 기체보관탱크(A5)에 압축보관하는 과정이다.The selective gas storage process 30 receives any one or two or more selected from oxygen, nitrogen, ammonia, atmosphere, nitric acid, and ozone, which are gases generated through the selective gas collection and generation process 20, and stores them in a gas storage tank ( This is the process of compressing and storing it in A5).
상기 선택기체압력공급과정(40)은, 상기 선택기체보관과정(30)을 통해 기체보관탱크(A5)에 보관중인 기체를 콤프레샤(A6)의 일정압력으로 공급관(A7)을 통해 물(D)이 가득찬 수조(C) 내부에 위치된 마이크로버블생성장치(B)로 공급하는 과정이다. The selected gas pressure supply process (40) is to supply water (D) to the gas stored in the gas storage tank (A5) through the supply pipe (A7) at a constant pressure of the compressor (A6) through the selected gas storage process (30). This is the process of supplying to the microbubble generator (B) located inside the filled water tank (C).
상기 마이크로버블생성용존과정(50)은, 상기 선택기체압력공급과정(40)을 통해 산소, 질소, 암모니아, 대기, 질산, 오존 중 선택 공급받은 마이크로버블생성장치(B)가 물(D)이 가득찬 수조(C) 내부에서 공급된 기체인 산소, 질소, 암모니아, 대기, 질산, 오존 중 선택된 마이크로버블을 생성시켜 수조(C) 내부의 물(D)에 빠르게 용존처리하는 과정이다. 이때, 용존처리의 효율을 높이기 위해서 수조(C) 내부에 별도의 수중모터(도시않음)를 설치하여 용존수(D1)가 서로 섞이도록 함이 바람직하다.In the microbubble generation and dissolution process (50), the microbubble generating device (B) supplied with a selection of oxygen, nitrogen, ammonia, atmosphere, nitric acid, and ozone through the selective gas pressure supply process (40) is supplied with water (D). This is a process of generating microbubbles selected from oxygen, nitrogen, ammonia, atmosphere, nitric acid, and ozone, which are gases supplied inside a full water tank (C), and quickly dissolving them in the water (D) inside the water tank (C). At this time, in order to increase the efficiency of the dissolved treatment, it is desirable to install a separate submersible motor (not shown) inside the water tank (C) to mix the dissolved water (D1) with each other.
상기 용존수액비투입과정(60)은, 상기 마이크로버블생성용존과정(50)을 거친 수조(C) 내부의 용존수(D1)를 펌프(P)를 통해 농장 작물의 액비로 사용하는 과정이다.The dissolved sap fertilizer 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 a liquid fertilizer for farm crops through a pump (P).
상기 기체선택발생장치(A)로 산소발생기(A2)를 사용하면, 주변의 공기를 흡입압축하여 흡착베드(도시않음)로 이송하고 흡착베드 내에서 산소만을 90%이상의 농도로 기체보관탱크(A5)로 공급하면서 질소를 포함한 그 외의 기체는 별도로 분리배출시킨다.When the oxygen generator (A2) is used as the gas selection generator (A), the surrounding air is sucked and compressed and transferred to the adsorption bed (not shown), and only oxygen is stored in the gas storage tank (A5) at a concentration of 90% or more in the adsorption bed. ), other gases including nitrogen are separated and discharged separately.
상기 기체선택발생장치(A)로 산소발생기(A2)를 사용시, 산소생성 후 남은 질소를 포함하는 기체에서 질소만을 포집하여 별도로 질소탱크(도시않음)에 저장할 수도 있음은 물론이다. Of course, when using the oxygen generator (A2) as the gas selective generator (A), only nitrogen can be collected from the nitrogen-containing gas remaining after oxygen generation and stored separately in a nitrogen tank (not shown).
상기 기체선택발생장치(A)로 질소발생기(A3)를 사용하면, 주변의 공기를 흡입압축하여 산소흡착제(CMS)로 가득찬 탱크를 통과하면서 90%이상의 농도로 질소만을 기체보관탱크(A5)로 공급하면서 산소흡착제(CMS)에 흡착된 산소는 별도로 분리배출 시킨다.When the nitrogen generator (A3) is used as the gas selection device (A), the surrounding air is sucked in and compressed to pass through a tank filled with oxygen adsorbent (CMS), and only nitrogen at a concentration of 90% or more is stored in the gas storage tank (A5). The oxygen adsorbed on the oxygen adsorbent (CMS) is separated and discharged separately.
상기 기체선택발생장치(A)로 질소발생기(A3) 사용시, 질소생성 후 산소흡착제(CMS)에 흡착된 산소만을 포집하여 별도의 산소탱크(도시않음)에 저장할 수도 있음은 물론이다.Of course, when using the nitrogen generator (A3) as the gas selective generator (A), only the oxygen adsorbed on the oxygen adsorbent (CMS) after nitrogen generation can be collected and stored in a separate oxygen tank (not shown).
상기 기체선택발생장치(A)로 질소발생기(A3)를 사용하면, 주변의 공기를 흡입압축하여 산소흡착제(CMS)로 가득찬 탱크를 통과하면서 90%이상의 농도로 질소만을 기체보관탱크(A5)로 공급하면서 산소흡착제(CMS)에 흡착된 산소는 별도로 분리배출되며, 암모늄이온(A12a) 선택시 수조내의 수소발생장치(A12aa)에 의해 전기분해되어 +에서 나오는 산소는 공기중으로 방출하고 촉매반응(A12ba)으로 인해 암모늄이온질소가 생성된다.When the nitrogen generator (A3) is used as the gas selection device (A), the surrounding air is sucked in and compressed to pass through a tank filled with oxygen adsorbent (CMS), and only nitrogen at a concentration of 90% or more is stored in the gas storage tank (A5). The oxygen adsorbed on the oxygen adsorbent (CMS) is separated and discharged separately, and when ammonium ions (A12a) are selected, it is electrolyzed by the hydrogen generator (A12aa) in the water tank, and the oxygen coming from + is released into the air and catalytic reaction ( A12ba) produces ammonium ion nitrogen.
상기 기체선택발생장치(A)로 콤프레샤(A6)를 사용하면, 주변의 공기를 흡입압축하여 기체보관탱크(A5)로 공급한다.When the compressor (A6) is used as the gas selective generator (A), surrounding air is sucked in and compressed and supplied to the gas storage tank (A5).
상기 기체선택발생장치(A)로 콤프레샤(A6)를 사용시, 질산이온(A13a) 선택시 공중방전(번개)처럼 고온이 생성되는 플라즈마발생장치(A13aa)로 삼중결합으로 이루어진 질소 연결고리를 분리하여 질산이온질소가 생성된다.When using the compressor (A6) as the gas selection generator (A), the nitrogen link consisting of a triple bond is separated using the plasma generator (A13aa), which generates high temperature like an air discharge (lightning) when nitrate ions (A13a) are selected. Nitrate ion nitrogen is produced.
상기 기체선택발생장치(A)로 산소발생기(A2)를 사용하여 주변의 공기를 흡입압축하여 흡착베드(도시않음)로 이송하고 흡착베드 내에서 산소만을 90%이상의 농축된 산소를 생성하며, 이렇게 생성되어 농축된 산소를 받아 오존발생기(A4)를 사용하여 무성방전 작용을 통해서 산소를 오존으로 변화시켜 기체보관탱크(A5)로 공급한다.Using the oxygen generator (A2) as the gas selection generator (A), the surrounding air is sucked and compressed, transferred to an adsorption bed (not shown), and oxygen concentrated to more than 90% of oxygen is generated in the adsorption bed. It receives the generated and concentrated oxygen, changes it into ozone through silent discharge using an ozone generator (A4), and supplies it to the gas storage tank (A5).
상기 기체선택발생장치(A)의 제어부(A1)는, 사용자가 작물의 필요에 의해 수조(C)의 용량을 수위감지센서(S1,S2)에 의해 설정하고, 그 수조(C)의 설정된 용량에 따라 물(D)을 가득 채우고 이를 각종 용존수(D1)로 만들어 작물에게 모두 공급하는 1싸이클의 수조가동횟수를 설정할 수 있는 산소횟수버튼(A11), 질소횟수버튼(A12), 암모니아횟수버튼(A12a), 대기횟수버튼(A13), 질산횟수버튼(A13a), 오존횟수버튼(A14)을 각각 더 구비하여, 작물 생육의 필요에 따라서 수조가동회수를 미리 "0 ~ 20"으로 설정함으로써, "0"으로 수조가동횟수가 설정된 버튼의 가동은 제외하고, 그 설정된 수조가동횟수에 따라서, 수조(C) 내부의 용존수(D1)를, 산소발생기(A2), 질소발생기(A3), 콤프레샤(A6), 오존발생기(A4), 수소발생기(A12aa), 플라즈마발생기(A13aa), 에 의해 각각 산소용존수, 질소용존수, 암모늄용존수, 대기용존수, 질산염용존수, 오존용존수로 수조가동횟수만큼 순차적으로 채워서 수조(C) 내부의 각 용존수(D1)를 펌프(P)로 작물에게 순차적으로 수조가동횟수만큼 공급시킨다.The control unit (A1) of the gas selection generator (A) allows the user to set the capacity of the water tank (C) according to the needs of the crops using the water level detection sensors (S1 and S2), and the set capacity of the water tank (C) Oxygen count button (A11), nitrogen count button (A12), and ammonia count button allow you to set the number of tank operations for one cycle, which fills water (D), turns it into various dissolved water (D1), and supplies it to the crops. (A12a), a standby number button (A13), a nitric acid number button (A13a), and an ozone number button (A14) are each further provided, and the water tank operation number is set to "0 to 20" in advance according to the needs of crop growth, Excluding the operation of the button whose water tank operation count is set to "0", the dissolved water (D1) inside the water tank (C), oxygen generator (A2), nitrogen generator (A3), and compressor are operated according to the set water tank operation number. (A6), ozone generator (A4), hydrogen generator (A12aa), and plasma generator (A13aa), respectively, create a water tank with oxygen dissolved water, nitrogen dissolved water, ammonium dissolved water, atmospheric dissolved water, nitrate dissolved water, and ozone dissolved water. It is sequentially filled according to the number of operations, and each dissolved water (D1) inside the tank (C) is sequentially supplied to the crops by the pump (P) according to the number of tank operations.
즉, 사용자가 작물의 필요량에 따라 수조(C) 내부의 용량을 수위감지센서(S1,S2)의 높낮이에 의해 설정하면, 제어부(A1)는 수조(C) 내부를 물(D)로 가득 채우게 되고, 사용자가 상기 기체선택발생장치(A)의 제어부(A1)에서 산소횟수버튼(A11)은 "3", 질소횟수버튼(A12)은 "1", 암모니아횟수버튼(A12a), "0", 대기횟수버튼(A13)은 "1", 질산횟수버튼(A13a), "0", 오존횟수버튼(A14)은 "1"이라 설정하는 포집기체선택설정과정(10)을 거치면, 기체선택발생장치(A)의 제어부(A1)는 산소횟수버튼(A11)의 "3" 수조가동횟수에 따라서, 산소를 포집하는 선택기체포집생성과정(20), 포집된 산소를 기체보관탱크(A5)로 압축저장하는 선택기체보관과정(30), 압축저장된 산소를 마이크로버블발생장치(B)로 공급하는 선택기체압력공급과정(40), 산소용존수(D1)를 생성하는 마이크로버블생성용존과정(50), 산소용존수(D1)를 펌프(P)로 작물에 공급하는 용존수액비투입과정(60)을 1싸이클로 진행한다. 이런 상기 과정을 상기 설정한 수조가동횟수 만큼 3번 모두 반복적으로 실행하게 된다.In other words, when the user sets the capacity inside the water tank (C) according to the required amount of crops by adjusting the height of the water level sensor (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 user sets the oxygen number button (A11) to "3", the nitrogen number button (A12) to "1", and the ammonia number button (A12a) to "0". , the standby count button (A13) is set to “1,” the nitric acid count button (A13a) is set to “0,” and the ozone count button (A14) is set to “1.” After going through the collection gas selection setting process (10), gas selection occurs. The control unit (A1) of the device (A) performs a selective gas collection generation process (20) to collect oxygen according to the “3” water tank operation number of the oxygen number button (A11), and transfers the captured oxygen to the gas storage tank (A5). A selective gas storage process (30) of compressed storage, a selective gas pressure supply process (40) of supplying the compressed and stored oxygen to the microbubble generator (B), and a microbubble generation dissolved process (50) of generating oxygen dissolved water (D1). ), the dissolved sap injection process (60), in which oxygen dissolved water (D1) is supplied to the crop using a pump (P), is performed in one cycle. This process is repeated three times for the number of water tank operations set above.
그 다음, 제어부(A1)에 의해 수조(C)는 내부를 물(D)로 가득 채우게 되고, 기체선택발생장치(A)의 제어부(A1)는, 질소횟수버튼(A12)의 "1" 수조가동횟수에 따라서, 질소를 포집하는 선택기체포집생성과정(20), 포집된 질소를 기체보관탱크(A5)로 압축저장하는 선택기체보관과정(30), 압축저장된 질소를 마이크로버블발생장치(B)로 공급하는 선택기체압력공급과정(40), 질소용존수(D1)를 생성하는 마이크로버블생성용존과정(50), 질소용존수(D1)를 펌프(P)로 작물에 공급하는 용존수액비투입과정(60)을 1싸이클로 진행한다.Next, 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) sets the water tank (C) to “1” on the nitrogen number button (A12). Depending on the number of operations, there is a selective gas collection process (20) to collect nitrogen, a selective gas storage process (30) to compress and store the captured nitrogen in the gas storage tank (A5), and a microbubble generator (B) to compress and store the compressed stored nitrogen. ), a selective gas pressure supply process (40), a microbubble generation dissolved process (50) that generates nitrogen dissolved water (D1), and a dissolved sap ratio that supplies nitrogen dissolved water (D1) to crops through a pump (P). The input process (60) is performed in one cycle.
그 다음, 제어부(A1)에 의해 수조(C)는 내부를 물(D)로 가득 채우게 되고, 기체선택발생장치(A)의 제어부(A1)는, 암모니아횟수버튼(A12a), "0", 이면 수조가동횟수가 설정된 버튼의 가동은 제외하고 다음 설정구간으로 진행한다.Next, 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) sets the ammonia count button (A12a) to "0", If this is the case, proceed to the next setting section, excluding the operation of the button for which the number of water tank operations has been set.
그 다음, 제어부(A1)에 의해 수조(C)는 내부를 물(D)로 가득 채우게 되고, 기체선택발생장치(A)의 제어부(A1)는, 대기횟수버튼(A13)의 "1" 수조가동횟수에 따라서, 대기를 포집하는 선택기체포집생성과정(20), 포집된 대기를 기체보관탱크(A5)로 압축저장하는 선택기체보관과정(30), 압축저장된 대기를 마이크로버블발생장치(B)로 공급하는 선택기체압력공급과정(40), 대기용존수(D1)를 생성하는 마이크로버블생성용존과정(50), 대기용존수(D1)를 펌프(P)로 작물에 공급하는 용존수액비투입과정(60)을 1싸이클로 진행한다.Next, 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) sets the water tank (C) to “1” on the standby number button (A13). Depending on the number of operations, there is a selective gas collection generation process (20) that collects the atmosphere, a selective gas storage process (30) that compresses and stores the captured atmosphere in the gas storage tank (A5), and a microbubble generator (B) that compresses and stores the compressed atmosphere. ), a selective gas pressure supply process (40), a microbubble generation dissolved process (50) that generates atmospheric dissolved water (D1), and a dissolved sap ratio that supplies atmospheric dissolved water (D1) to crops through a pump (P). The input process (60) is performed in one cycle.
그 다음, 제어부(A1)에 의해 수조(C)는 내부를 물(D)로 가득 채우게 되고, 기체선택발생장치(A)의 제어부(A1)는, 질산횟수버튼(A13a), "0", 이면 수조가동횟수가 설정된 버튼의 가동은 제외하고 다음 설정구간으로 진행한다.Next, 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) turns on the nitric acid number button (A13a), "0", If this is the case, proceed to the next setting section, excluding the operation of the button for which the number of water tank operations has been set.
그 다음, 제어부(A1)에 의해 수조(C)는 내부를 물(D)로 가득 채우게 되고, 기체선택발생장치(A)의 제어부(A1)는, 오존횟수버튼(A14)의 "1" 수조가동횟수에 따라서, 산소발생기(A2)에 의해 산소를 포집하는 선택기체포집생성과정(20), 포집된 산소를 오존발생기(A4)를 사용하여 오존으로 변화시켜 기체보관탱크(A5)로 압축저장하는 선택기체보관과정(30), 압축저장된 오존을 마이크로버블발생장치(B)로 공급하는 선택기체압력공급과정(40), 오존용존수(D1)를 생성하는 마이크로버블생성용존과정(50), 오존용존수(D1)를 펌프(P)로 작물에 공급하는 용존수액비투입과정(60)을 1싸이클로 진행한다.Next, the control unit (A1) fills the inside of the water tank (C) with water (D), and the control unit (A1) of the gas selection device (A) sets the “1” tank of the ozone count button (A14). Depending on the number of operations, a selective gas collection 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) that supplies the compressed and stored ozone to the microbubble generator (B), a microbubble generation and dissolution process (50) that generates ozone dissolved water (D1), The dissolved sap injection process (60) of supplying ozone-dissolved water (D1) to crops using a pump (P) is performed in one cycle.
이렇게 제어부(A1)에서 산소횟수버튼(A11)은 "3", 질소횟수버튼(A12)은 "1", 암모니아횟수버튼(A12a), "0", 대기횟수버튼(A13)은 "1", 질산횟수버튼(A13a), "0", 오존횟수버튼(A14)은 "1"이라 설정된 수조가동횟수 만큼 모두 실행시킨다.In this way, in the control unit (A1), the oxygen count button (A11) is set to "3", the nitrogen count button (A12) is set to "1", the ammonia count button (A12a) is set to "0", and the standby count button (A13) is set to "1". The nitric acid count button (A13a) is set to "0", and the ozone count button (A14) is set to "1" so that they all run as many times as the set water tank operation count.
이와 같은 본 발명은, 기체선택발생장치(A)와 마이크로버블생성장치(B)를 사용하여 용존산소가 풍부한 산소용존수(D1)를 작물에게 관주 및 옆면살포로 공급하여 호기성 미생물의 증식을 원활하게 유도하고, 유해균 및 협기성 미생물을 억제시켜 토양 및 배지 또는 수경재배 및 아쿠아포닉스 농법에 균류의 균형을 이루며, 작물 성장시 작물의 뿌리 발육이 좋아지고, 작물 수확시 호기성 미생물의 증식율을 높여 작물의 뿌리 발육 및 생육성장이 활성화되어 작물 수확량을 보다 증대시킬 수 있게 된다.The present invention uses a gas selective generator (A) and a microbubble generator (B) to supply oxygenated water (D1) rich in dissolved oxygen to crops by irrigation and side spraying, thereby facilitating the growth of aerobic microorganisms. By suppressing harmful bacteria and aerobic microorganisms, it achieves a balance of fungi in soil and media or hydroponic and aquaponics farming methods, improves root development of crops when growing crops, and increases the proliferation rate of aerobic microorganisms when harvesting crops. Root development and growth of crops are activated, making it possible to further increase crop yield.
또한, 용존질소가 풍부한 질소용존수(D1)를 작물에게 공급하여 잔뿌리로부터 수관 및 체관을 이용하여 잎의 광합성 작용을 통한 수확량을 보다 원활하게 증대되도록 유도함으로써 생육성장 및 작물 수확량을 보다 증대시킬 수 있게 된다.In addition, by supplying nitrogen-dissolved water (D1), which is rich in dissolved nitrogen, to crops, growth growth and crop yield can be further increased by inducing a smoother increase in yield through photosynthetic action of leaves using crowns and phloem from fine roots. There will be.
또한, 용존암모니아가 풍부한 암모늄용존수(D1)를 작물에게 공급하여 뿌리혹박테리아로 부터 질소고정세균을 얻은 잔뿌리는 질소비료 흡수 효과를 극대화 할 수 있게 하고 작물이 포도당 생성에 필요한 단백질, 핵산 도움을 주며 잔뿌리성장에 유익하도록 세균 번식을 해 비옥한 땅 조성에 기여 한다.In addition, by supplying ammonium dissolved water (D1), which is rich in dissolved ammonia, to crops, fine roots that have obtained nitrogen-fixing bacteria from root nodule bacteria can maximize the effect of nitrogen fertilizer absorption and help crops with proteins and nucleic acids necessary for glucose production. It contributes to the creation of fertile soil by propagating bacteria beneficial to the growth of fine roots.
또한, 용존대기가 풍부한 대기용존수(D1)는 온실가스 이산화탄소를 이온화시켜 작물에게 공급하여 작물 생육성장의 균형이 잘 이루어진 상태에서 지속적으로 성장할 수 있도록 유도하게 된다.In addition, atmospheric dissolved water (D1), which is rich in dissolved air, ionizes the greenhouse gas carbon dioxide and supplies it to crops, thereby encouraging them to grow continuously in a well-balanced state of crop growth and growth.
또한, 용존질산이 풍부한 질산염용존수(D1)를 작물에게 공급하여 질소동화작용에 중요한 질화세균의 호기성 균 류 증식을 유발하며 수확을 증대하기위한 포도당, 단백질, 핵산의 식물 기반 조건을 더 극대화하는 중요한 세균 번식의 균형을 유지하는 역할을 하며 탈질소 작용에 의한 기체상태 대기로 반복되는 자연 친화적 순환 방법이 된다.In addition, by supplying nitrate-dissolved water (D1), which is rich in dissolved nitric acid, to crops, it induces aerobic fungal growth of nitrifying bacteria, which are important for nitrogen assimilation, and further maximizes plant-based conditions for glucose, protein, and nucleic acids to increase harvest. It plays a role in maintaining the balance of important bacterial reproduction and becomes a nature-friendly circulation method that is repeated in the gaseous atmosphere through denitrification.
또한, 용존오존이 풍부한 오존용존수(D1)를 작물에게 공급하여 곰팡이 균류나 벌레 충류 및 박테리아나 바이러스를 사멸시키거나 억제 및 기피처리하고, 중금속을 산화분해시켜 작물의 뿌리 발육과 생육성장을 활성화시키면서 작물 수확량을 저렴한 비용으로 지속가능하게 증대시킬 수 있게 된다. In addition, by supplying ozone-dissolved water (D1), which is rich in dissolved ozone, to crops, it kills, suppresses, and wards off mold, insects, bacteria, and viruses, and oxidizes and decomposes heavy metals to activate root development and growth of crops. This makes it possible to sustainably increase crop yield at low cost.
본 실시예 및 본 명세서에 첨부된 도면은 본 발명에 포함되는 기술적 사상의 일부를 명확하게 나타내고 있는 것에 불과하며, 본 발명의 명세서 및 도면에 포함된 기술적 사상의 범위 내에서 당업자가 용이하게 유추할 수 있는 변형예와 구체적인 실시예는 모두 본 발명의 기술적 사상의 범위에 포함되는 것은 자명하다.This embodiment and the drawings attached to this specification only clearly show a part of the technical idea included in the present invention, and those skilled in the art can easily infer within the scope of the technical idea included in the specification and drawings of the present invention. It is obvious that all possible modifications and specific embodiments are included within the scope of the technical idea of the present invention.
본 발명의 범위는 상세한 설명보다는 후술하는 특허청구범위에 의하여 나타내어지며, 특허청구범위의 의미 및 범위 그리고 등가 개념으로부터 도출되는 모든 변경 또는 변형된 형태가 본 발명의 범위에 포함되는 것으로 해석되어야 한다.The scope of the present invention is indicated by the claims described later rather than the detailed description, and all changes or modified forms derived from the meaning and scope of the claims and the equivalent concept should be construed as being included in the scope of the present invention.
10 : 포집기체선택설정과정
20 : 선택기체포집생성과정
30 : 선택기체보관과정
40 : 선택기체압력공급과정
50 : 마이크로버블생성용존과정
60 : 용존수액비투입과정
A : 기체선택발생장치
A1 : 제어부
A11 : 산소횟수버튼
A12 : 질소횟수버튼
A12a ; 암모니아횟수버튼
A12aa ; 수소발생기
A12ba ; 촉매반응
A13 : 대기횟수버튼
A13a : 질산횟수버튼
A13aa ; 플라즈마발생기
A14 : 오존횟수버튼
A2 : 산소발생기
A3 : 질소발생기
A4 : 오존발생기
A5 : 기체보관탱크
A6 : 콤프레샤
A7 : 공급관
B : 마이크로버블발생장치
C : 수조
D : 물
D1 : 용존수
P : 펌프
S1,S2 : 수위감지센서
S/W : 전원스위치
T : 타이머10: Collection gas selection setting process
20: Selected gas capture generation process
30: Selected gas storage process
40: Selected gas pressure supply process
50: Microbubble generation and dissolution process
60: Dissolved sap cost input process
A: Gas selection generator
A1: Control unit
A11: Oxygen count button
A12: Nitrogen count button
A12a ; Ammonia count button
A12aa; hydrogen generator
A12ba; catalytic reaction
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: Microbubble generator
C: water tank
D: water
D1: dissolved water
P: pump
S1,S2: Water level sensor
S/W: Power switch
T: Timer
Claims (17)
상기 포집기체선택설정과정(10)은, 기체선택발생장치(A)의 제어부(A1)를 통해 전원을 인가하고, 제어부(A1)에서 포집저장할 기체를 선택하고 수조가동횟수와 시간을 설정하여 그 기체의 포집과 저장을 수조가동횟수만큼 실행하도록 설정하며;
상기 선택기체포집생성과정(20)은, 상기 포집기체선택설정과정(10)의 제어부(A1)에서 산소, 질소, 대기, 오존 중 선택된 어느 하나를 생성하기 위하여 상기 기체선택발생장치(A)로 주변의 공기를 필터를 통해 흡입압축하고 흡입압축된 공기 중 상기 포집기체선택설정과정(10)에서 선택된 기체만을 남기고 나머지 기체는 분리배출시켜 선택된 기체만을 생성시키고;
상기 선택기체보관과정(30)은, 상기 선택기체포집생성과정(20)을 통해서 생성된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나를 기체보관탱크(A5)에 압축보관하고;
상기 선택기체압력공급과정(40)은, 상기 선택기체보관과정(30)을 통해 기체보관탱크(A5)에 보관중인 기체를 일정압력으로 공급관(A7)을 통해 물(D)이 가득찬 수조(C) 내부에 위치된 마이크로버블생성장치(B)로 공급하며;
상기 마이크로버블생성용존과정(50)은, 상기 선택기체압력공급과정(40)을 통해 산소, 질소, 대기, 오존 중 선택된 어느 하나를 공급받은 마이크로버블생성장치(B)가 물(D)이 가득찬 수조(C) 내부에서 공급된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나로 마이크로버블을 생성시켜 수조(C) 내부의 물(D)에 빠르게 용존처리하고;
상기 용존수액비투입과정(60)은, 상기 마이크로버블생성용존과정(50)을 거친 수조(C) 내부의 용존수(D1)를 펌프(P)를 통해 농장의 액비로 사용하는 것을 특징으로 하는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법.A capture gas selection setting process (10) for selecting one or more of oxygen, nitrogen, atmosphere, and ozone as the gas to be captured and stored, and a selective gas collection and generation process for generating one selected from oxygen, nitrogen, atmosphere, and ozone. A process (20), a selective gas storage process (30) in which one of oxygen, nitrogen, atmosphere, and ozone is stored in the gas storage tank (A5), and the gas stored in the gas storage tank (A5) is maintained at a constant pressure. A selective gas pressure supply process (40), a microbubble generation dissolution process (50) that generates microbubbles, and the dissolved water (D1) inside the water tank (C) is used as a liquid fertilizer for the farm through the pump (P). In the dissolved sap injection process 60, the user sets the capacity of the water tank (C) according to the needs of the crop using the water level detection sensors (S1, S2) and water (D) according to the set capacity of the water tank (C). ) and a gas selective generator (A) having a control unit (A1) that turns it into various dissolved water (D1) and supplies it to crops. A liquid fertilizer manufacturing method using a gas selective generator (A) and a microbubble generator. Because,
In the capture gas selection setting process (10), power is applied through the control unit (A1) of the gas selection generator (A), the gas to be captured and stored is selected in the control unit (A1), and the number and time of water tank operation are set. Set the collection and storage of gas to be performed as many times as the water tank is operated;
The selective gas collection and generation process (20) is performed by the control unit (A1) of the capture gas selection and setting process (10) to the gas selection generator (A) to generate any one selected among oxygen, nitrogen, atmosphere, and ozone. Suctioning and compressing the surrounding air through a filter, leaving only the gas selected in the capture gas selection setting process (10) among the suctioned and compressed air, and separating and discharging the remaining gases to generate only the selected gas;
The selective gas storage process (30) compresses and stores any one of oxygen, nitrogen, atmosphere, and ozone, which are gases generated through the selective gas collection and generation process (20), in a gas storage tank (A5);
The selected gas pressure supply process 40 is a water tank filled with water (D) through the supply pipe A7 at a constant pressure to the gas stored in the gas storage tank A5 through the selected gas storage process 30 ( C) supplied to the microbubble generating device (B) located inside;
The microbubble generation and dissolution process (50) is performed when the microbubble generator (B), which has received any one selected from oxygen, nitrogen, atmosphere, and ozone through the selective gas pressure supply process (40), is filled with water (D). Microbubbles are generated from one of oxygen, nitrogen, atmosphere, and ozone, which are gases supplied from the cold water tank (C), and are quickly dissolved in the water (D) inside the water tank (C);
The dissolved sap fertilizer injection process (60) is characterized in that the dissolved water (D1) inside the water tank (C) that has undergone the microbubble generation and dissolution process (50) is used as a liquid fertilizer for the farm through a pump (P). Liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator.
상기 기체선택발생장치(A)로는, 질소발생기(A3)를 사용하고, 주변의 공기를 흡입압축하여 산소흡착제(CMS)로 가득찬 탱크를 통과하면서 90%이상의 농도로 질소만을 기체보관탱크(A5)로 공급하면서 산소흡착제(CMS)에 흡착된 산소만을 포집하여 별도의 산소탱크에 저장하며, 암모니아(A12a) 선택시 수조(C)내의 수소발생장치(A12aa)에 의해 전기분해되어 +에서 나오는 산소는 공기중으로 방출하고 촉매반응(A12ba)으로 인해 암모늄이온질소가 생성되는 것을 특징으로 하는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법.According to claim 1,
As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked in and compressed to pass through a tank full of oxygen adsorbent (CMS), and only nitrogen at a concentration of 90% or more is stored in the gas storage tank (A5). ), only the oxygen adsorbed on the oxygen adsorbent (CMS) is collected and stored in a separate oxygen tank. When ammonia (A12a) is selected, oxygen is electrolyzed by the hydrogen generator (A12aa) in the water tank (C) and released from +. A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that it is released into the air and ammonium ion nitrogen is generated due to a catalytic reaction (A12ba).
상기 기체선택발생장치(A)로는, 콤프레샤(A6)를 사용하고, 주변의 공기를 흡입압축하여 기체보관탱크(A5)로 공급하며, 질산(A13a) 선택시 공중방전(번개)처럼 고온고압이 생성되는 플라즈마발생장치(A13aa)로 삼중결합으로 이루어진 질소 연결고리를 분리하여 질산이온질소가 생성되는 특징으로 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법.According to claim 1,
The gas selection generator (A) uses a compressor (A6), sucks in and compresses the surrounding air, and supplies it to the gas storage tank (A5). When nitric acid (A13a) is selected, high temperature and high pressure are generated like an aerial discharge (lightning). A method of manufacturing liquid fertilizer using a gas selective generator and a microbubble generator, with the characteristic of generating nitrate ion nitrogen by separating the nitrogen chain consisting of a triple bond using the plasma generator (A13aa).
상기 기체선택발생장치(A)의 제어부(A1)는, 수조(C)의 설정된 용량에 따라 물(D)을 가득 채우고 이를 각종 용존수(D1)로 만들어 작물에게 모두 공급하는 1싸이클의 수조가동횟수를 설정할 수 있는 산소횟수버튼(A11), 질소횟수버튼(A12), 대기횟수버튼(A13), 오존횟수버튼(A14)을 각각 더 구비하여, 작물 생육의 필요에 따라서 수조가동회수를 미리 "0 ~ 20"으로 설정함으로써, "0"으로 수조가동횟수가 설정된 버튼의 가동은 제외하고, 그 설정된 수조가동횟수에 따라서, 수조(C) 내부의 용존수(D1)를, 산소발생기(A2), 질소발생기(A3), 콤프레샤(A6), 오존발생기(A4)에 의해 각각 산소용존수, 질소용존수, 대기용존수, 오존용존수로 수조가동횟수만큼 순차적으로 채워서 수조(C) 내부의 각 용존수(D1)를 펌프(P)로 작물에게 순차적으로 수조가동횟수만큼 공급시키는 것을 특징으로 하는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법.According to claim 1,
The control unit (A1) of the gas selection generator (A) operates the water tank for one cycle by filling it with water (D) according to the set capacity of the water tank (C), turning it into various dissolved water (D1) and supplying it to the crops. It is further equipped with an oxygen count button (A11), a nitrogen count button (A12), a standby count button (A13), and an ozone count button (A14) that can set the number of times, so that the number of tank operations can be set in advance according to the needs of crop growth. By setting it to "0 ~ 20", excluding the operation of the button whose water tank operation number is set to "0", the dissolved water (D1) inside the water tank (C) is transferred to the oxygen generator (A2) according to the set water tank operation number. , the nitrogen generator (A3), compressor (A6), and ozone generator (A4) are sequentially filled with oxygen-dissolved water, nitrogen-dissolved water, atmospheric dissolved water, and ozone-dissolved water, respectively, according to the number of tank operations, and each inside the water tank (C) A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, characterized in that dissolved water (D1) is sequentially supplied to crops using a pump (P) as many times as the water tank is operated.
상기 기체선택발생장치(A)의 제어부(A1)는,
암모니아횟수버튼(A12a), 질산횟수버튼(A13a)을 각각 더 구비하고,
암모니아횟수버튼(A12a)으로 암모니아 선택시 수조(C)내의 수소발생장치(A12aa)에 의해 전기분해되어 +에서 나오는 산소는 공기중으로 방출하고 촉매반응(A12ba)으로 인해 암모늄이온질소가 생성되어 수조(C) 내부에 암모늄용존수가 형성되며, 질산횟수버튼(A13a)으로 질산 선택시 공중방전(번개)처럼 고온고압이 생성되는 플라즈마발생장치(A13aa)로 삼중결합으로 이루어진 질소 연결고리를 분리하여 질산이온질소가 생성되어 수조(C) 내부에 질산염용존수가 형성되는 것을 특징으로 하는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법.According to claim 10,
The control unit (A1) of the gas selection generator (A),
Further equipped with an ammonia count button (A12a) and a nitric acid count button (A13a),
When ammonia is selected with the ammonia number button (A12a), it is electrolyzed by the hydrogen generator (A12aa) in the water tank (C), and the oxygen from + is released into the air, and ammonium ion nitrogen is generated through the catalytic reaction (A12ba) and the water tank (C) C) Ammonium dissolved water is formed inside, and when nitric acid is selected with the nitric acid number button (A13a), a high temperature and high pressure is generated like an air discharge (lightning) using the plasma generator (A13aa), which separates the nitrogen chain consisting of a triple bond to produce nitric acid 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).
상기 포집기체선택설정과정(10)은, 기체선택발생장치(A)의 제어부(A1)를 통해 전원을 인가하고, 제어부(A1)에서 포집저장할 기체를 선택하고 수조가동횟수와 시간을 설정하여 그 기체의 포집과 저장을 수조가동횟수만큼 실행하도록 설정하며;
상기 선택기체포집생성과정(20)은, 상기 포집기체선택설정과정(10)의 제어부(A1)에서 산소, 질소, 대기, 오존 중 선택된 어느 하나를 생성하기 위하여 상기 기체선택발생장치(A)로 주변의 공기를 필터를 통해 흡입압축하고 흡입압축된 공기 중 상기 포집기체선택설정과정(10)에서 선택된 기체만을 남기고 나머지 기체는 분리배출시켜 선택된 기체만을 생성시키고;
상기 선택기체압력공급과정(40)은, 상기 선택기체포집생성과정(20)을 통해서 생성된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나의 기체를 일정압력으로 공급관(A7)을 통해 물(D)이 가득찬 수조(C) 내부에 위치된 마이크로버블생성장치(B)로 공급하며;
상기 마이크로버블생성용존과정(50)은, 상기 선택기체압력공급과정(40)을 통해 산소, 질소, 대기, 오존 중 선택된 어느 하나를 공급받은 마이크로버블생성장치(B)가 물(D)이 가득찬 수조(C) 내부에서 공급된 기체인 산소, 질소, 대기, 오존 중 선택된 어느 하나로 마이크로버블을 생성시켜 수조(C) 내부의 물(D)에 빠르게 용존처리하고;
상기 용존수액비투입과정(60)은, 상기 마이크로버블생성용존과정(50)을 거친 수조(C) 내부의 용존수(D1)를 펌프(P)를 통해 농장의 액비로 사용하는 것을 특징으로 하는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법.A capture gas selection setting process (10) for selecting one or more of oxygen, nitrogen, atmosphere, and ozone as the gas to be captured and stored, and a selective gas collection and generation process for generating one selected from oxygen, nitrogen, atmosphere, and ozone. A process (20), a selective gas pressure supply process (40) for supplying the generated gas at a constant pressure, a microbubble generation dissolution process (50) for generating microbubbles, and dissolved water (D1) inside the water tank (C). ) is used as a liquid fertilizer on the farm through a pump (P) (60), and the user sets the capacity of the water tank (C) according to the needs of the crop using the water level sensor (S1, S2) Gas selection generator including a gas selection generator (A) with a control unit (A1) that fills the water tank (C) with water (D) according to the set capacity, turns it into various dissolved water (D1), and supplies it to the crops. In the method of manufacturing liquid fertilizer using a device and a microbubble generating device,
In the capture gas selection setting process (10), power is applied through the control unit (A1) of the gas selection generator (A), the gas to be captured and stored is selected in the control unit (A1), and the number and time of water tank operation are set. Set the collection and storage of gas to be performed as many times as the water tank is operated;
The selective gas collection and generation process (20) is performed by the control unit (A1) of the capture gas selection and setting process (10) to the gas selection generator (A) to generate any one selected among oxygen, nitrogen, atmosphere, and ozone. Suctioning and compressing the surrounding air through a filter, leaving only the gas selected in the capture gas selection setting process (10) among the suctioned and compressed air, and separating and discharging the remaining gases to generate only the selected gas;
The selective gas pressure supply process (40) is performed by supplying water at a constant pressure to one of the gases selected from oxygen, nitrogen, atmosphere, and ozone, which are gases generated through the selective gas collection and generation process (20), through the supply pipe (A7). (D) is supplied to the microbubble generator (B) located inside the full water tank (C);
The microbubble generation and dissolution process (50) is performed when the microbubble generator (B), which has received any one selected from oxygen, nitrogen, atmosphere, and ozone through the selective gas pressure supply process (40), is filled with water (D). Microbubbles are generated from one of oxygen, nitrogen, atmosphere, and ozone, which are gases supplied from the cold water tank (C), and are quickly dissolved in the water (D) inside the water tank (C);
The dissolved sap fertilizer injection process (60) is characterized in that the dissolved water (D1) inside the water tank (C) that has undergone the microbubble generation and dissolution process (50) is used as a liquid fertilizer for the farm through a pump (P). Liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator.
상기 기체선택발생장치(A)로는, 질소발생기(A3)를 사용하고, 주변의 공기를 흡입압축하여 산소흡착제(CMS)로 가득찬 탱크를 통과하면서 90%이상의 농도로 질소만을 공급관(A7)으로 공급하면서 산소흡착제(CMS)에 흡착된 산소는 별도로 분리배출되며, 암모니아(A12a) 선택시 수조(C)내의 수소발생장치(A12aa)에 의해 전기분해되어 +에서 나오는 산소는 공기중으로 방출하고 촉매반응(A12ba)으로 인해 암모늄이온질소가 생성되고, 질산(A13a) 선택시 공중방전(번개)처럼 고온고압이 생성되는 플라즈마발생장치(A13aa)로 삼중결합으로 이루어진 질소 연결고리를 분리하여 질산이온질소가 생성되는 것을 특징으로 하는 기체선택발생장치와 마이크로버블생성장치를 이용한 액상비료 제조방법.According to claim 12,
As the gas selective generator (A), a nitrogen generator (A3) is used, and the surrounding air is sucked in and compressed to pass through a tank filled with oxygen adsorbent (CMS), and only nitrogen at a concentration of 90% or more is supplied to the supply pipe (A7). The oxygen adsorbed on the oxygen adsorbent (CMS) during supply is separated and discharged separately, and when ammonia (A12a) is selected, it is electrolyzed by the hydrogen generator (A12aa) in the water tank (C), and the oxygen coming from + is released into the air and undergoes a catalytic reaction. Ammonium ion nitrogen is generated by (A12ba), and when nitric acid (A13a) is selected, nitrate ion nitrogen is created by separating the nitrogen chain consisting of a triple bond with the plasma generator (A13aa), which generates high temperature and high pressure like an air discharge (lightning). A liquid fertilizer manufacturing method using a gas selective generator and a microbubble generator, which is characterized in that it is generated.
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