CN114027166A - Novel organic matter water planting system - Google Patents
Novel organic matter water planting system Download PDFInfo
- Publication number
- CN114027166A CN114027166A CN202111515993.2A CN202111515993A CN114027166A CN 114027166 A CN114027166 A CN 114027166A CN 202111515993 A CN202111515993 A CN 202111515993A CN 114027166 A CN114027166 A CN 114027166A
- Authority
- CN
- China
- Prior art keywords
- water
- nitrification
- raw material
- reaction
- reactor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 179
- 239000005416 organic matter Substances 0.000 title claims abstract description 19
- 238000006396 nitration reaction Methods 0.000 claims abstract description 54
- 235000015097 nutrients Nutrition 0.000 claims abstract description 32
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 28
- 239000010959 steel Substances 0.000 claims abstract description 28
- 239000002994 raw material Substances 0.000 claims description 76
- 238000006243 chemical reaction Methods 0.000 claims description 74
- 230000001546 nitrifying effect Effects 0.000 claims description 44
- 230000001105 regulatory effect Effects 0.000 claims description 37
- 239000003337 fertilizer Substances 0.000 claims description 36
- 239000002002 slurry Substances 0.000 claims description 33
- 238000010248 power generation Methods 0.000 claims description 26
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 claims description 25
- 238000005273 aeration Methods 0.000 claims description 23
- 239000000618 nitrogen fertilizer Substances 0.000 claims description 22
- 238000000855 fermentation Methods 0.000 claims description 19
- 239000002918 waste heat Substances 0.000 claims description 18
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 241000894006 Bacteria Species 0.000 claims description 9
- 239000012295 chemical reaction liquid Substances 0.000 claims description 9
- 238000004321 preservation Methods 0.000 claims description 9
- 229910002651 NO3 Inorganic materials 0.000 claims description 8
- 150000001875 compounds Chemical class 0.000 claims description 8
- -1 nitrate ions Chemical class 0.000 claims description 8
- 235000013619 trace mineral Nutrition 0.000 claims description 8
- 239000011573 trace mineral Substances 0.000 claims description 8
- 239000010815 organic waste Substances 0.000 claims description 6
- 238000003860 storage Methods 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 239000010806 kitchen waste Substances 0.000 claims description 4
- 241001465754 Metazoa Species 0.000 claims description 3
- 210000003608 fece Anatomy 0.000 claims description 3
- 239000010871 livestock manure Substances 0.000 claims description 3
- 239000010908 plant waste Substances 0.000 claims description 3
- 239000003501 hydroponics Substances 0.000 claims 9
- 238000000034 method Methods 0.000 abstract description 15
- 230000005540 biological transmission Effects 0.000 description 9
- 230000008901 benefit Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 4
- 201000010099 disease Diseases 0.000 description 4
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 4
- 230000003203 everyday effect Effects 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 230000000813 microbial effect Effects 0.000 description 4
- 239000002689 soil Substances 0.000 description 4
- 241000607479 Yersinia pestis Species 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 208000037805 labour Diseases 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 235000013311 vegetables Nutrition 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- 238000012271 agricultural production Methods 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000011031 large-scale manufacturing process Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 239000011591 potassium Substances 0.000 description 2
- 229910052700 potassium Inorganic materials 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 208000035240 Disease Resistance Diseases 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 241000237502 Ostreidae Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000033558 biomineral tissue development Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000012272 crop production Methods 0.000 description 1
- 230000002354 daily effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- 239000002054 inoculum Substances 0.000 description 1
- 238000007130 inorganic reaction Methods 0.000 description 1
- 210000001503 joint Anatomy 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 235000020636 oyster Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002686 phosphate fertilizer Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
Images
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
- A01G31/00—Soilless cultivation, e.g. hydroponics
- A01G31/02—Special apparatus therefor
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
- A01G9/00—Cultivation in receptacles, forcing-frames or greenhouses; Edging for beds, lawn or the like
- A01G9/14—Greenhouses
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01G—HORTICULTURE; CULTIVATION OF VEGETABLES, FLOWERS, RICE, FRUIT, VINES, HOPS OR SEAWEED; FORESTRY; WATERING
- A01G9/00—Cultivation in receptacles, forcing-frames or greenhouses; Edging for beds, lawn or the like
- A01G9/22—Shades or blinds for greenhouses, or the like
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/25—Greenhouse technology, e.g. cooling systems therefor
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/12—Technologies relating to agriculture, livestock or agroalimentary industries using renewable energies, e.g. solar water pumping
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/20—Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2
- Y02P60/21—Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Environmental Sciences (AREA)
- Hydroponics (AREA)
Abstract
The invention discloses a novel organic matter water planting system which comprises a water planting facility, wherein the water planting facility comprises a steel pipe plastic greenhouse or a greenhouse, a plurality of steel pipe plastic greenhouses are arranged side by side, and a plurality of water planting grooves are formed in the steel pipe plastic greenhouse; the water planting facility is connected with an external nitration reaction system and a cogeneration generator set. The invention has the characteristics of low and stable source of the organic nutrient solution, low and stable energy source, seamless connection between the nutrient solution nitrification process and the planting process, and convenient and simple operation.
Description
Technical Field
The invention relates to the field of circular agricultural water culture production, in particular to a novel organic matter water culture planting system.
Background
Traditional agriculture adopts soil planting, often involves a large amount of soil ploughing in the operation process, need consume a large amount of labours, and labor efficiency is low. Moreover, the soil components are complex, and the growth of various harmful components and the large-area generation of soil-borne diseases and pests are caused due to the growth of the planting years, and the soil-borne diseases and pests can also become the generation places of the pests and the weeds. In order to control all factors in the whole planting process, various water culture technologies based on inorganic chemical nutrient solution are developed, the technology does not need to repeatedly turn over soil, the planting efficiency is greatly improved, the planting environment is uniform, and the quality of planted products is relatively standardized.
But also brings new problems, such as high cost of the nutrient solution itself, and if the nutrient solution is recycled, the pH environment, EC environment, microbial environment and nutrient change of the absorbed nutrient solution bring unpredictable adverse effects to planting. If the waste water is not recycled, the waste water is directly discharged into an environmental water area, and pollution pressure is brought to the environment. And the hydroponic planting is characterized in that the inorganic nutrient solution does not contain buffer components, factors including pH and the like easily change greatly, so that the water body generates diseases, the whole disease is easily enlarged, and the planting risk is extremely high, so that the requirements on the environmental control and the technical level of planting facilities are extremely high, the cost and the operation cost of the stably-produced hydroponic system and facilities are usually high, and the large-area popularization is difficult.
In order to overcome the problems of the conventional water culture planting technique using inorganic nutrient solution, patent 1 entitled "method for preparing inoculum of microorganism group optimized as catalyst for parallel multiple mineralization" in publication No. CN 102112598B; in patent 2, "preparation method of solid carrier and catalyst column fixed with microorganism group for parallel compound inorganic reaction, and solid culture medium for plant cultivation", granted publication No. CN 102112609B "discloses a hydroponic cultivation technique using organic nutrient solution as main nutrient. Compared with the traditional water culture system, the planting system has the advantages that nitrifying bacteria participate in the nutrient supply and root protection of crops, the disease resistance of the crops and the environment buffering capacity of the culture solution are improved, the harsh requirements of the culture process on the planting environment are reduced, and the hardware investment cost of facilities is also reduced.
However, this technique has the following problems: 1. a large amount of heat preservation energy is needed for a nitration reaction system and a water planting system, and the source of cheap energy is not clear; 2. because the nitrification system has strict requirements on the carbon-nitrogen ratio (C/N) of the organic nutrient solution, generally lower than 10, if the carbon-nitrogen ratio of the organic raw material is unstable, particularly the excessively high carbon-nitrogen ratio can cause the instability of the nitrification system, the problem that the cheap source of the high-quality organic nutrient solution is not clear exists; 3. although the scheme provided by the patent 2 solves the problem of the microbial reaction surface area, the adding operation flow of the materials is complex and is not suitable for large-scale production, and the economic applicability is not provided without large-scale agricultural production.
Disclosure of Invention
The purpose of the invention is as follows: aiming at the defects of the prior art, the invention provides a novel organic matter water planting system which has the characteristics of low and stable source of high-quality organic nutrient solution, low and stable energy source, capability of seamlessly butting the nitrification process and the planting process of the nutrient solution, and convenience and simplicity in operation.
The first technical scheme is as follows: the novel organic matter water planting system comprises a water planting facility, wherein the water planting facility comprises a steel pipe plastic greenhouse or a greenhouse, a plurality of steel pipe plastic greenhouses are arranged side by side, a plurality of water planting grooves are formed in the steel pipe plastic greenhouses, and the water planting facility is connected with an external nitration reaction system and a cogeneration generator set.
The nitrification reaction system comprises a nitrification reactor, an aeration pump and a nitrification raw material regulating tank, wherein the nitrification reactor is respectively connected with the nitrification raw material regulating tank and the water culture planting facility through pipelines; the cogeneration generator set is respectively connected with one or more of a nitrification raw material regulating tank, a nitrification reactor and a circulating reservoir of a water culture planting facility through pipelines.
Wherein, the nitration system is provided with an aeration pump to form an aerobic reaction environment, the reaction liquid contains nitrifying bacteria flora capable of converting organic matters into nitrate ions, and the reaction temperature is 15-37 ℃; after the components of organic matters serving as nitrifying raw materials are regulated in a nitrifying raw material regulating pond, the organic matters are injected into a nitrifying reactor, the ammoniation and nitrification of the organic matters are carried out in a parallel compound reaction mode, after fertilizer water containing nitrate nitrogen is generated, part of the fertilizer water flows into a water culture groove of a water culture planting facility through a pipeline for being used by the crops, and the rest of the fertilizer water is continuously left in the nitrifying reactor as strains to participate in the nitrifying reaction together with the subsequently injected raw materials; nitrate nitrogen fertilizer water enters the water culture tank through the water inlet pipeline, crops are planted on the water culture tank, and the nitrate nitrogen fertilizer water is discharged through the water outlet pipeline after the nutrients are absorbed by the crops; the fertilizer water after one-time use enters a circulating reservoir and can circularly flow into the water culture tank for crops to absorb for many times; the fertilizer water after being recycled can flow into the nitrifying raw material regulating tank for component regulation of the nitrifying raw material; the waste heat generated by the cogeneration generator set is input into one or more of a nitrification reactor, a nitrification raw material adjusting tank and a circulating reservoir in the form of hot water or steam through pipelines, so as to provide a heat source for nitrification reaction and plant heat preservation.
Wherein the reaction temperature of the nitration reaction system is 28 ℃; an aeration pump is arranged in the circulating reservoir to adjust the dissolved oxygen in the nutrient solution, and crop growth trace elements and a regulator for adjusting the pH value are added into the circulating reservoir.
The top of the steel pipe plastic greenhouse can be additionally provided with a sunshade net rack, photovoltaic power generation boards are arranged between the steel pipe plastic greenhouses, and the sunshade net rack and the photovoltaic power generation boards share a supporting column.
The second technical scheme is as follows: the novel organic matter water planting system comprises a water planting facility, wherein the water planting facility comprises a steel pipe plastic greenhouse or a greenhouse, a plurality of steel pipe plastic greenhouses are arranged side by side, and a plurality of water planting grooves are formed in the steel pipe plastic greenhouse. The water planting facility is connected with an external anaerobic reaction system, a nitration reaction system and a cogeneration generator set; the anaerobic reaction system comprises an anaerobic reactor and a biogas storage; the nitrification reaction system comprises a nitrification reactor, an aeration pump and a nitrification raw material regulating tank, wherein the nitrification reactor is respectively connected with the nitrification raw material regulating tank and the water culture planting facility through pipelines; the cogeneration generator set is connected with one or more of an anaerobic reactor, a nitrifying raw material regulating tank, a nitrifying reactor and a circulating reservoir of a water culture planting facility through pipelines; the nitrifying raw material regulating tank is respectively connected with the circulating reservoir and the anaerobic reactor through pipelines.
The anaerobic reaction system takes kitchen waste, animal manure and plant waste as main raw materials, and converts organic matters with high carbon-nitrogen ratio in the raw materials into biogas and biogas slurry as raw materials for nitration reaction through medium-temperature anaerobic fermentation at 37 ℃ or high-temperature anaerobic fermentation at 55 ℃; the biogas slurry after anaerobic fermentation is in a high-temperature state of 37 ℃ or 55 ℃, and the waste heat provides heat for a subsequent nitration reaction system; configuring an aeration pump in a nitration reaction system to form an aerobic reaction environment, wherein the reaction liquid contains nitrifying bacteria flora capable of converting organic matters into nitrate ions, and the reaction temperature is 15-37 ℃; the nitrification raw material regulating tank receives biogas slurry discharged after anaerobic fermentation of an external facility, the biogas slurry is subjected to component regulation and then is injected into the nitrification reactor, parallel compound reaction of ammoniation and nitrification of organic matters is carried out, after fertilizer water containing nitrate nitrogen is generated, part of the fertilizer water flows into a water culture tank of the water culture planting facility through a pipeline for crop utilization, and the rest part of the fertilizer water is continuously left in the nitrification reactor as a strain to participate in nitrification reaction together with the subsequently injected raw material; nitrate nitrogen fertilizer water enters the water culture tank through the water inlet pipeline, crops are planted on the water culture tank, and the nitrate nitrogen fertilizer water is discharged through the water outlet pipeline after the nutrients are absorbed by the crops; the fertilizer water after one-time use enters a circulating reservoir and can circularly flow into the water culture tank for crops to absorb for many times; the fertilizer water after recycling can flow into the nitrification raw material adjusting tank circularly and is used for adjusting the components of the biogas slurry raw material; the waste heat generated by the cogeneration generator set is input into one or more of an anaerobic fermentation tank, a nitration reactor, a nitration raw material adjusting tank and a circulating reservoir in the form of hot water or steam through pipelines, and a heat source is provided for anaerobic reaction, nitration reaction and planting heat preservation.
Wherein the reaction temperature of the nitration reaction system is 28 ℃; an aeration pump is arranged in the circulating reservoir to adjust the dissolved oxygen in the nutrient solution, and crop growth trace elements and a regulator for adjusting the pH value are added into the circulating reservoir; after partial carbon elements in the organic waste raw material are converted into biogas, the carbon-nitrogen ratio in the product biogas slurry is reduced to below 10.
The top of the steel pipe plastic greenhouse can be additionally provided with a sunshade net rack, photovoltaic power generation boards are arranged between the steel pipe plastic greenhouses, and the sunshade net rack and the photovoltaic power generation boards share a supporting column.
Has the advantages that: compared with the prior art, the invention has the following remarkable advantages:
1. in the first scheme, a water culture planting facility is connected with an external nitration reaction system and a cogeneration generator set; the cogeneration generator set provides a large amount of cheap waste heat energy sources for a nitration reaction system and a water planting facility, reduces the operation cost and improves the operation effect and the benefit.
2. In the second scheme, the water culture planting facility is connected with an external anaerobic reaction system and a nitration reaction system; the raw materials of the biogas project are wide in source and low in price, and the environment-friendly function is also considered, so that the product biogas slurry is subjected to harmless treatment along with various costs, and can be obtained freely. After the organic waste is subjected to anaerobic fermentation and carbon is extracted as the main component of the biogas, the carbon-nitrogen ratio of the organic waste is greatly reduced, and the organic waste can be used as an excellent raw material for nitration reaction, so that the biogas slurry is treated harmlessly, the source of the high-quality raw material is stable and reliable, and the raw material cost is greatly saved. Meanwhile, as the biogas slurry discharged after the reaction also contains a large amount of waste heat, the waste heat is added into the nitration reactor before the waste heat is dissipated and the temperature is reduced, so that extremely low-cost heat preservation energy can be provided for the subsequent nitration reaction, and the nitration reaction can be carried out under the condition of being closer to the optimal reaction temperature. In addition, the biogas slurry is directly supplied to the nitration engineering for use, so that a large biogas slurry storage facility which is conventionally configured in the biogas engineering is omitted, the construction cost is greatly reduced, and the problem of biogas slurry utilization which troubles the operation of the biogas engineering for a long time is solved;
3. because the biogas slurry contains not only digestible organic matters but also a large amount of various insoluble solid substances such as lignin, cellulose and the like, the substances can still remain in the reaction liquid after anaerobic reaction and nitration reaction and can become good attachments of nitrifying bacteria groups. When a large amount of suspended matters attached to nitrifying flora exist in the nitrifying reaction liquid, the reaction area of the nitrifying reaction is greatly increased and is far larger than that of a biological membrane attached to the wall of the container, so that the nitrifying reaction efficiency is improved, and meanwhile, a large amount of strains are continuously provided for subsequent reactions.
4. In the whole system, the processes from the addition of reaction raw materials to the conversion of nitrate nitrogen fertilizer water, absorption by the hydroponic crops and discharge are communicated by a pipeline or a water channel, the nutrient solution nitrification process and the planting process are in seamless butt joint, the working flow is smooth, and the operation is simple and convenient, so that the method is very suitable for large-scale production and large-scale planting. The popularization of the system can greatly improve the labor efficiency of agricultural production.
5. By recycling nitrate nitrogen fertilizer water, on one hand, nutrient elements in the nitrate nitrogen fertilizer water can be fully utilized, and on the other hand, the content of water quality pollution elements such as organic matters, nitrogen, phosphorus and the like in the nitrate nitrogen fertilizer water can be reduced, so that the nitrate nitrogen fertilizer water finally reaches the direct discharge standard.
6. The fertilizer water used for water culture can be acidified and various trace elements are deficient after long-term use, and the trace elements and the pH regulator are added, so that the fertilizer water can be recycled, the crop production is guaranteed, and the water source is saved.
7. The production system is combined with thermal power generation, and cooperative production is realized, so that the waste heat generated by the thermal power generation is fully utilized as the heat-insulating energy for system operation, the overall operation energy consumption cost is greatly reduced, the waste heat value of the thermal power generation is fully exerted, and the operation benefit is improved.
8. By combining with a thermal power station, the original characteristics of the power station such as: the investment cost of power transmission and grid connection of various power equipment such as transformers and grid-connected power transmission lines is greatly reduced, and the investment return rate is increased.
9. By installing the photovoltaic power generation equipment in the system, the photovoltaic power generation equipment and the sun shading equipment of the greenhouse can share the support frame, the construction cost of the sun shading equipment of the greenhouse is reduced, photovoltaic power generation grid connection can also share various power equipment of a thermal power station, and the investment cost of the whole hardware is reduced.
10. The power supply of the whole system can be supplied by thermal power generation, methane power generation and photovoltaic power generation, so that the power supply safety of the system is greatly improved, the loss caused by accidental power failure is avoided, and the power use cost can be reduced.
Drawings
FIG. 1 is a block diagram 1 of the present invention;
FIG. 2 is a block diagram 2 of the present invention;
FIG. 3 is a schematic side view of the steel pipe plastic greenhouse of the present invention;
FIG. 4 is a schematic top view of the steel pipe plastic greenhouse of the present invention;
in the figure, 1 is a steel pipe plastic greenhouse, 2 is a photovoltaic power generation board, 3 is a sunshade net rack, and 4 is a water culture tank.
Detailed Description
The technical solution of the present invention is further described with reference to the accompanying drawings and the detailed description.
The first scheme is as follows: the novel organic matter water planting system comprises a water planting facility, wherein the water planting facility comprises steel pipe plastic greenhouses 1 or greenhouses, a plurality of steel pipe plastic greenhouses 1 are arranged side by side, a plurality of water planting grooves 4 are formed in the steel pipe plastic greenhouses 1, a sunshade net rack 3 is arranged at the top of each steel pipe plastic greenhouse 1, and photovoltaic power generation boards 2 are arranged between the steel pipe plastic greenhouses 1; the water planting facility is connected with a nitration reaction system and a cogeneration generator set.
The water culture planting facility is connected with an external nitration reaction system and a cogeneration generator set; the nitrification reaction system comprises a nitrification reactor, an aeration pump and a nitrification raw material regulating tank, and the nitrification reactor is respectively connected with the nitrification raw material regulating tank and the water culture planting facility through pipelines; the cogeneration generator set is respectively connected with the nitrifying raw material regulating tank, the nitrification reactor and the circulating reservoir of the water planting facility through pipelines; the circulating reservoir is connected with the nitrifying raw material regulating tank through a pipeline. When in use, the nitrification reaction system is provided with an aeration pump to form an aerobic reaction environment, the reaction liquid contains nitrifying bacteria flora capable of converting organic matters into nitrate ions, and the reaction temperature is 15-37 ℃; after the components of organic matters serving as nitrifying raw materials are regulated in a nitrifying raw material regulating pond, the organic matters are injected into a nitrifying reactor, the ammoniation and nitrification of the organic matters are carried out in a parallel compound reaction mode, after fertilizer water containing nitrate nitrogen is generated, part of the fertilizer water flows into a water culture tank 4 of a water culture planting facility through a pipeline for being used by the crops, and the rest of the fertilizer water is continuously left in the nitrifying reactor as strains to participate in the nitrifying reaction together with the subsequently injected raw materials; nitrate nitrogen fertilizer water enters the water culture tank 4 through a water inlet pipeline, crops are planted on the water culture tank 4, and the nitrate nitrogen fertilizer water is discharged through a water outlet pipeline after the nutrients are absorbed by the crops; the fertilizer water after one-time use enters a circulating reservoir and can circularly flow into the water culture tank 4 for crops to absorb for many times; circularly flowing the fertilizer water after being recycled into the nitration raw material regulating tank for regulating the components of the nitration raw material; the waste heat generated by the cogeneration generator set is input into one or more of a nitrification reactor, a nitrification raw material adjusting tank and a circulating reservoir in the form of hot water or steam through pipelines, so as to provide a heat source for nitrification reaction and plant heat preservation. Wherein the reaction temperature of the nitration reaction system is 28 ℃; an aeration pump is arranged in the circulating reservoir to adjust the dissolved oxygen in the nutrient solution, and crop growth trace elements and a regulator for adjusting the pH value are added into the circulating reservoir.
Scheme II: the water culture planting facility is connected with an external anaerobic reaction system, a nitration reaction system and a cogeneration generator set; the anaerobic reaction system comprises an anaerobic reactor and a biogas storage; the nitrification reaction system comprises a nitrification reactor, an aeration pump and a nitrification raw material regulating tank, and the nitrification reactor is respectively connected with the nitrification raw material regulating tank and the water culture planting facility through pipelines; the cogeneration generator set is respectively connected with the anaerobic reactor, the nitrifying raw material regulating tank, the nitrifying reactor and the circulating reservoir of the water planting facility through pipelines; the nitrifying raw material regulating tank is respectively connected with the circulating reservoir and the anaerobic reactor through pipelines. When the anaerobic reaction system is used, kitchen waste, animal manure and plant waste are used as main raw materials, and high-carbon-nitrogen-ratio organic matters in the raw materials are converted into biogas and biogas slurry as raw materials for nitration reaction through medium-temperature anaerobic fermentation at 37 ℃ or high-temperature anaerobic fermentation at 55 ℃; the biogas slurry after anaerobic fermentation is in a high-temperature state of 37 ℃ or 55 ℃, and the waste heat provides heat for a subsequent nitration reaction system; configuring an aeration pump in a nitration reaction system to form an aerobic reaction environment, wherein the reaction liquid contains nitrifying bacteria flora capable of converting organic matters into nitrate ions, and the reaction temperature is 15-37 ℃; the nitrification raw material regulating tank receives biogas slurry discharged after anaerobic fermentation of an external facility, the biogas slurry is subjected to component regulation and then is injected into the nitrification reactor, parallel compound reaction of ammoniation and nitrification of organic matters is carried out, after fertilizer water containing nitrate nitrogen is generated, part of the fertilizer water flows into the water culture tank 4 of the water culture planting facility through a pipeline for crop utilization, and the rest of the fertilizer water is continuously left in the nitrification reactor as a strain to participate in nitrification reaction together with the subsequently injected raw material; nitrate nitrogen fertilizer water enters the water culture tank 4 through a water inlet pipeline, crops are planted on the water culture tank 4, and the nitrate nitrogen fertilizer water is discharged through a water outlet pipeline after the nutrients are absorbed by the crops; the fertilizer water after one-time use enters a circulating reservoir and can circularly flow into the water culture tank 4 for crops to absorb for many times; circularly flowing the fertilizer water after being recycled into the nitrification raw material adjusting tank for adjusting the components of the biogas slurry raw material; the waste heat generated by the cogeneration generator set is input into one or more of an anaerobic fermentation tank, a nitration reactor, a nitration raw material adjusting tank and a circulating reservoir in the form of hot water or steam through pipelines, and a heat source is provided for anaerobic reaction, nitration reaction and planting heat preservation. Wherein the reaction temperature of the nitration reaction system is 28 ℃; an aeration pump is arranged in the circulating reservoir to adjust the dissolved oxygen in the nutrient solution, and crop growth trace elements and a regulator for adjusting the pH value are added into the circulating reservoir; the carbon-nitrogen ratio of the organic waste raw material is more than 20, and after part of carbon elements are converted into biogas, the carbon-nitrogen ratio in the product biogas slurry is reduced to be less than 10. The fuel of the cogeneration generator set can use the biogas generated by anaerobic fermentation, and the generated power can be merged into the power grid through a common power transmission line. Preferably, the facility of the protected area in the water planting system can adopt a steel pipe plastic greenhouse 1, a water planting groove 4 is arranged in the greenhouse, the greenhouse is in the north-south direction, a photovoltaic power generation board is arranged between the greenhouses, the power generation board faces south, and the power generation board is supported by a support column. The panel support is used as a common support, the sunshade net rack is arranged at the upper part of the greenhouse, and the sunshade net is laid, so that the greenhouse can be planted in summer conveniently. The generated energy is merged into a power grid through an inverter, a transformer and a power transmission line, wherein the transformer and the power transmission line can be shared with a thermal generator set. The electric energy generated by the photovoltaic power generation can also be used for stirring power for anaerobic fermentation or nitration reaction in the system, aeration pump power for nitration reaction, and various water pumps in the system.
Example (b):
the hydroponic planting facility of this embodiment is connected with outside anaerobic reaction system, nitration reaction system, combined heat and power generation generating set, selects the technical content of scheme one, scheme two as required:
the water planting facility adopts a 1000-mu steel pipe plastic greenhouse 1 water planting base, 4 water planting grooves 4 are arranged in each mu of greenhouse, the length of each water planting groove 4 is 65 meters, the width of each water planting groove is 1.5 meters, the height of each water planting groove is 0.3 meter, the volume of each water planting groove is about 120 cubic meters, and the total volume of the base is 120000 cubic meters; the distance between the greenhouses is 2 meters, the photovoltaic power generation plates 2 are arranged between the greenhouses, the size is 2 meters multiplied by 2 meters, the power is 800 watts, 25 photovoltaic power generation plates 2 can be arranged between two greenhouses with the length of 70 meters, 25000 photovoltaic power generation plates 2 can be arranged between 1000 greenhouses, the installed total capacity can reach 20MW, the electric energy grid-connected transmission and the thermal generator set share a transformer and a power transmission line, the total investment amount of the electric energy grid-connected transmission and the thermal generator set can be greatly reduced, and the investment return rate of the electric energy grid-connected transmission and the thermal generator set can be increased. The generated power can also be used for a stirrer of an anaerobic reaction system, an aeration pump of a nitration reaction system, an automatic sun-shading net of a greenhouse, an automatic film rolling machine, an air circulation fan in the greenhouse, a culture solution circulation pump and the like. An automatic sunshade net rack 3 is arranged on the greenhouse and supported by the photovoltaic power generation panel 2 pillars, so that the equipment investment is reduced by more than 30%. The average daily requirement of nitrogen fertilizer for planting vegetables in the greenhouse is about 70 g per mu, and the total requirement of nitrogen fertilizer for 1000 mu is about 70 kg.
The anaerobic reaction system adopts kitchen waste or culture excrement as raw materials, adopts a high-temperature fermentation mode of a complete mixing anaerobic reaction tank (CSTR) at 55 ℃, has a total reaction capacity of 500 cubic meters, produces 500 cubic meters of methane every day, discharges 25 cubic meters of biogas slurry, and can provide 700Mcal heat preservation for digestion engineering reacting at 28 ℃ every day. The biogas slurry has about 5 percent of organic matter content, about 2 percent of total carbon content, about 0.3 percent of total nitrogen content, about 7 percent of carbon-nitrogen ratio, about 0.3 percent of total potassium content and about 0.08 percent of total phosphorus content, which is equivalent to providing 75kg of nitrogen fertilizer, 75kg of potassium fertilizer and 18kg of phosphate fertilizer every day, and is enough to supply the fertilizer water in the water culture planting area. The biogas slurry is directly supplied to the nitration engineering for use, so that a large biogas slurry storage facility which is conventionally configured in the biogas engineering is omitted, the construction cost is greatly reduced, and the problem of biogas slurry utilization which troubles the operation of the biogas engineering for a long time is solved.
The nitrification reaction system is provided with a reaction tank of 50 cubic meters, a 50KW aeration pump ensures that the dissolved oxygen in the reaction tank is kept above 3ppm, the nitrifying bacteria source is dry microbial powder, the dry microbial powder is added into biogas slurry diluent with 1% of organic matter concentration and then is subjected to aeration culture, parallel compound nitrification reaction is carried out, and 80% of reaction liquid discharged as nitrate nitrogen fertilizer water flows into a water culture tank for planting through a pipeline after the nitrate ion concentration reaches 200 mg/L. And adding the biogas slurry into the nitration reactor in batches again, keeping the concentration of organic matters at about 1%, performing aeration reaction, discharging the nitrate ions again according to the above mode after the concentration of the nitrate ions reaches 200mg/L, and repeating the steps. After being absorbed by crops, the nitrate nitrogen fertilizer water can selectively flow into a circulating reservoir or flow back to a nitrification raw material regulating tank or a biogas engineering raw material regulating tank for utilization according to the content of nutrient components. Under the condition that the dissolved oxygen of the fertilizer water in the circulating water storage tank is insufficient, oxygen can be increased through the oxygen increasing pump, oyster powder particles can be added to adjust under the conditions that the pH value is reduced and the trace components are insufficient, and the redundant fertilizer water can be directly discharged under the condition that the direct discharge standard is met after the nutrient components are completely absorbed.
The cogeneration generator set adopts a 20MW thermal power station, the generation waste heat is about 500GMcal every day, the power station, the water planting facility, the anaerobic reaction system, the nitration reactor and the circulating reservoir are all within 2 kilometers, and the waste heat of the cogeneration generator set of the thermal power station is input into a biogas project and the circulating reservoir through a hot water pipeline to preserve heat. The total water culture volume is 120000 cubic meters, the whole water temperature can be improved by more than 4 ℃, low-temperature-resistant vegetables are planted in the greenhouse at the far end area of the heat source, and normal-temperature vegetables are planted at the near end, so that the temperature of the water culture planting system can be fully guaranteed by the generated waste heat even in winter.
Claims (9)
1. The utility model provides a novel organic matter hydroponics system of planting which characterized in that: the water planting device comprises a water planting facility, wherein the water planting facility comprises a steel pipe plastic greenhouse (1) or a greenhouse, a plurality of steel pipe plastic greenhouses (1) are arranged side by side, and a plurality of water planting grooves (4) are arranged in the steel pipe plastic greenhouse (1); the water planting facility is connected with an external nitration reaction system and a cogeneration generator set.
2. A novel organic matter hydroponics growing system in accordance with claim 1, characterized in that: the water planting facility is connected with an external nitration reaction system and a cogeneration generator set; the nitrification reaction system comprises a nitrification reactor, an aeration pump and a nitrification raw material regulating tank, wherein the nitrification reactor is respectively connected with the nitrification raw material regulating tank and the water culture planting facility through pipelines; the cogeneration generator set is connected with one or more of a nitrifying raw material adjusting tank, a nitrifying reactor and a circulating reservoir of a water planting facility through pipelines.
3. A novel organic matter hydroponics growing system in accordance with claim 2, characterized in that: configuring an aeration pump in a nitration reaction system to form an aerobic reaction environment, wherein the reaction liquid contains nitrifying bacteria flora capable of converting organic matters into nitrate ions, and the reaction temperature is 15-37 ℃; after the components of organic matters serving as nitrifying raw materials are regulated in a nitrifying raw material regulating pond, the organic matters are injected into a nitrifying reactor, the ammoniation and nitrification of the organic matters are carried out in a parallel compound reaction mode, after fertilizer water containing nitrate nitrogen is generated, part of the fertilizer water flows into a water culture groove of a water culture planting facility through a pipeline for being used by the crops, and the rest of the fertilizer water is left in the nitrifying reactor as strains to participate in the nitrifying reaction together with the subsequently injected raw materials; nitrate nitrogen fertilizer water enters the water culture tank through the water inlet pipeline, crops are planted on the water culture tank, and the nitrate nitrogen fertilizer water is discharged through the water outlet pipeline after the nutrients are absorbed by the crops; the fertilizer water after one-time use enters a circulating reservoir and circularly flows into a water culture tank for crops to absorb for many times; the recycled fertilizer water flows into a nitrifying raw material regulating tank and is used for regulating the components of the raw materials; the waste heat generated by the cogeneration generator set is input into one or more of a nitrification reactor, a nitrification raw material adjusting tank and a circulating reservoir in the form of hot water or steam through pipelines, so as to provide a heat source for nitrification reaction and plant heat preservation.
4. A novel organic matter hydroponics growing system in accordance with claim 3, characterized in that: the reaction temperature of the nitration reaction system is 28 ℃; an aeration pump is arranged in the circulating reservoir to adjust the dissolved oxygen in the nutrient solution, and crop growth trace elements and a regulator for adjusting the pH value are added into the circulating reservoir.
5. A novel organic matter hydroponics growing system in accordance with claim 1, characterized in that: the water planting facility is connected with an external anaerobic reaction system, a nitration reaction system and a cogeneration generator set.
6. A novel organic matter hydroponics growing system in accordance with claim 5, characterized in that: the anaerobic reaction system comprises an anaerobic reactor and a biogas storage; the nitrification reaction system comprises a nitrification reactor, an aeration pump and a nitrification raw material regulating tank, wherein the nitrification reactor is respectively connected with the nitrification raw material regulating tank and the water culture planting facility through pipelines; the cogeneration generator set is respectively connected with one or more of an anaerobic reactor, a nitrifying raw material regulating tank, a nitrifying reactor and a circulating reservoir of a water culture planting facility through pipelines; the nitrifying raw material regulating tank is respectively connected with the circulating reservoir and the anaerobic reactor through pipelines.
7. A novel organic matter hydroponics growing system in accordance with claim 6, characterized in that: the anaerobic reaction system takes kitchen waste, animal manure and plant waste as main raw materials, and converts organic matters with high carbon-nitrogen ratio in the raw materials into biogas and biogas slurry through medium-temperature anaerobic fermentation at 37 ℃ or high-temperature anaerobic fermentation at 55 ℃, wherein the biogas slurry is used as a raw material for nitration reaction; the biogas slurry after anaerobic fermentation is in a high-temperature state of 37 ℃ or 55 ℃, and the waste heat provides heat for a subsequent nitration reaction system; configuring an aeration pump in a nitration reaction system to form an aerobic reaction environment, wherein the reaction liquid contains nitrifying bacteria flora capable of converting organic matters into nitrate ions, and the reaction temperature is 15-37 ℃; the nitrification raw material regulating tank receives biogas slurry discharged after anaerobic fermentation of an external facility, the biogas slurry is subjected to component regulation and then is injected into the nitrification reactor, parallel compound reaction of ammoniation and nitrification of organic matters is carried out, after fertilizer water containing nitrate nitrogen is generated, part of the fertilizer water flows into a water culture tank of the water culture planting facility through a pipeline for crop utilization, and the rest part of the fertilizer water is continuously left in the nitrification reactor as a strain to participate in nitrification reaction together with the subsequently injected raw material; nitrate nitrogen fertilizer water enters the water culture tank through the water inlet pipeline, crops are planted on the water culture tank, and the nitrate nitrogen fertilizer water is discharged through the water outlet pipeline after the nutrients are absorbed by the crops; the fertilizer water after one-time use enters a circulating reservoir and circularly flows into a water culture tank for crops to absorb for many times; the recycled fertilizer water flows into a nitrification raw material adjusting tank and is used for adjusting the components of the biogas slurry raw material; the waste heat generated by the cogeneration generator set is input into one or more of an anaerobic fermentation tank, a nitration reactor, a nitration raw material adjusting tank and a circulating reservoir in the form of hot water or steam through pipelines, and a heat source is provided for anaerobic reaction, nitration reaction and planting heat preservation.
8. A novel organic matter hydroponics growing system in accordance with claim 9, characterized in that: the reaction temperature of the nitration reaction system is 28 ℃; an aeration pump is arranged in the circulating reservoir to adjust the dissolved oxygen in the nutrient solution, and crop growth trace elements and a regulator for adjusting the pH value are added into the circulating reservoir; after part of carbon elements in the organic waste raw materials are converted into biogas, the carbon-nitrogen ratio in the biogas slurry product is reduced to below 10.
9. A novel organic matter hydroponics growing system in accordance with claim 1 or 5, characterised in that: the top of the steel pipe plastic greenhouse (1) is provided with a sunshade net rack (3), photovoltaic power generation boards (2) are arranged between the steel pipe plastic greenhouse (1), and the sunshade net rack (3) and the photovoltaic power generation boards (2) share a supporting column.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111515993.2A CN114027166A (en) | 2021-12-03 | 2021-12-03 | Novel organic matter water planting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202111515993.2A CN114027166A (en) | 2021-12-03 | 2021-12-03 | Novel organic matter water planting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN114027166A true CN114027166A (en) | 2022-02-11 |
Family
ID=80146774
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202111515993.2A Pending CN114027166A (en) | 2021-12-03 | 2021-12-03 | Novel organic matter water planting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114027166A (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102112598A (en) * | 2008-10-09 | 2011-06-29 | 独立行政法人农业·食品产业技术综合研究机构 | Method for production of seed material for microorganisms optimized as catalyst for parallel complex mineralization reaction |
| CN103194377A (en) * | 2013-04-10 | 2013-07-10 | 涂维浩 | Biogas engineering product and agricultural planting combined comprehensive utilization system |
| CN103373793A (en) * | 2012-04-27 | 2013-10-30 | 中国科学院城市环境研究所 | High-efficiency and low-consumption livestock and poultry breeding wastewater treatment and recycling technology |
| CN108934632A (en) * | 2018-06-07 | 2018-12-07 | 蒙城县京徽蒙农业科技发展有限公司 | Sprinkler irrigation technique promotes training device in a kind of agricultural soilless cultivation planting shed |
| CN109380101A (en) * | 2017-08-09 | 2019-02-26 | 南充智库汽车有限公司 | A kind of device and method of fish and vegetable symbiotic soilless cultivation capsicum |
| CN110015812A (en) * | 2019-04-11 | 2019-07-16 | 泰州学院 | A kind of high concentration livestock breeding wastewater processing method |
| CN113307369A (en) * | 2021-06-08 | 2021-08-27 | 上海市环境科学研究院 | Livestock and poultry farm manure recycling and ammonia-control carbon-reduction full-chain emission reduction system and method |
-
2021
- 2021-12-03 CN CN202111515993.2A patent/CN114027166A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102112598A (en) * | 2008-10-09 | 2011-06-29 | 独立行政法人农业·食品产业技术综合研究机构 | Method for production of seed material for microorganisms optimized as catalyst for parallel complex mineralization reaction |
| CN103373793A (en) * | 2012-04-27 | 2013-10-30 | 中国科学院城市环境研究所 | High-efficiency and low-consumption livestock and poultry breeding wastewater treatment and recycling technology |
| CN103194377A (en) * | 2013-04-10 | 2013-07-10 | 涂维浩 | Biogas engineering product and agricultural planting combined comprehensive utilization system |
| CN109380101A (en) * | 2017-08-09 | 2019-02-26 | 南充智库汽车有限公司 | A kind of device and method of fish and vegetable symbiotic soilless cultivation capsicum |
| CN108934632A (en) * | 2018-06-07 | 2018-12-07 | 蒙城县京徽蒙农业科技发展有限公司 | Sprinkler irrigation technique promotes training device in a kind of agricultural soilless cultivation planting shed |
| CN110015812A (en) * | 2019-04-11 | 2019-07-16 | 泰州学院 | A kind of high concentration livestock breeding wastewater processing method |
| CN113307369A (en) * | 2021-06-08 | 2021-08-27 | 上海市环境科学研究院 | Livestock and poultry farm manure recycling and ammonia-control carbon-reduction full-chain emission reduction system and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US5527464A (en) | Method and system for the treatment and utilization of waste products | |
| CN103210713A (en) | Method for improving soil fertility of greenhouse and preventing soil disease | |
| CN103194377B (en) | Biogas engineering product and agricultural planting combined comprehensive utilization system | |
| CN101798953B (en) | Medium-low pluripotential complementary methane generating system | |
| CN104152493A (en) | Method for improving yield of methane produced by anaerobic digestion of biomass raw materials | |
| CN101628841A (en) | Method for producing organic and inorganic compound fertilizer by utilizing duck dropping source | |
| CN108605863A (en) | A kind of livestock culture waste ecology synthesis utilizes system | |
| CN111996217A (en) | Straw bed-lying padding and livestock and poultry manure combined anaerobic fermentation method | |
| CN101892268A (en) | System for promoting fermentation of biogas from lignocellulose materials by utilizing microalgae | |
| CN105586362A (en) | Method for producing methane through high-temperature dry type anaerobic co-fermentation | |
| CN103342596A (en) | Tomato seedling medium and preparation method thereof | |
| CN102173897A (en) | Method for treating and utilizing agricultural solid waste through aerobic high-temperature hydrolysis and fermentation | |
| CN101314780A (en) | Method for producing methyl hydride and electricity with solar energy | |
| CN202717774U (en) | Anaerobic fermentation biogas fermentation broth and biogas slurry waste heat utilization system | |
| CN209468338U (en) | A kind of Agro-ecology circulatory system | |
| CN101445810A (en) | Method for preparing hydrogen by fermenting biologically pretreated straw | |
| CN204490868U (en) | Biomass energy bionethanation system | |
| CN202017008U (en) | Edible fungus dreg recycling treatment device | |
| CN112097312A (en) | Device and method for continuously extracting heat from composting system | |
| CN206452951U (en) | Environment-friendly type penkeeping is given up | |
| CN114027166A (en) | Novel organic matter water planting system | |
| CN207391302U (en) | A kind of methane/hydrogen coproduction organic fertilizer integration installation for fermenting | |
| CN114149895B (en) | Aerobic fermentation heat recycling equipment for agricultural and forestry waste coupled cultivation excrement | |
| CN205933570U (en) | System is used multipurposely to plant's excrement and urine step | |
| CN107460120A (en) | A kind of cellulose, micro- oxygen pretreatment unit of lignin fermentation methane production and method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20220211 |