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WO2020009073A1 - Method for modifying aquaculture tank, and aquaculture method - Google Patents

Method for modifying aquaculture tank, and aquaculture method Download PDF

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Publication number
WO2020009073A1
WO2020009073A1 PCT/JP2019/026168 JP2019026168W WO2020009073A1 WO 2020009073 A1 WO2020009073 A1 WO 2020009073A1 JP 2019026168 W JP2019026168 W JP 2019026168W WO 2020009073 A1 WO2020009073 A1 WO 2020009073A1
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Prior art keywords
aquaculture
sediment
fulvic acid
modifying
aquatic products
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French (fr)
Japanese (ja)
Inventor
充日児 ▲高▼味
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T&g KK
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T&g KK
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    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01KANIMAL HUSBANDRY; AVICULTURE; APICULTURE; PISCICULTURE; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
    • A01K61/00Culture of aquatic animals
    • A01K61/50Culture of aquatic animals of shellfish
    • A01K61/59Culture of aquatic animals of shellfish of crustaceans, e.g. lobsters or shrimps
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01KANIMAL HUSBANDRY; AVICULTURE; APICULTURE; PISCICULTURE; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
    • A01K63/00Receptacles for live fish, e.g. aquaria; Terraria
    • A01K63/04Arrangements for treating water specially adapted to receptacles for live fish

Definitions

  • the present invention relates to a method for modifying a culture tank and a method for modifying a culture tank.
  • Patent Literature 1 and the like are disclosed as a technique for culturing shrimp and the like, which is a typical marine product to be cultivated.
  • Patent Literature 1 discloses that an aquarium into which prawns are put is covered with a light-shielding house so that the illuminance on the water surface of the aquarium is 100 lux or less, and beneficial bacteria that grow regardless of illuminance dominantly proliferate in the aquarium.
  • a method for cultivating a prawn which comprises maintaining the prawn and cultivating the prawn in the water tank.
  • Patent Literature 2 discloses a fish and shellfish cultivation apparatus characterized in that a plurality of cultured fish beds are vertically provided in a breeding aquarium at intervals, and vibration means are attached to the cultured fish beds.
  • Patent Literature 3 is a culture method for purifying and adjusting water in a process of circulating water in a culture tank for culturing fish and shellfish through a circulation path as appropriate, wherein a denitrification apparatus and an activated carbon adsorption apparatus are provided in the circulation path.
  • the present invention discloses a water circulation type aquaculture method, wherein denitrification of circulating water and removal of organic hardly decomposable substances are performed through at least a part of the circulating water through the apparatus.
  • Patent Document 4 discloses a method of implanting or magnetically adsorbing microorganisms that have absorbed iron ions to a strain of a granular iron-type artificial zeolite carrying ferromagnetic iron powder, and eluted organic substances, oxidatively decomposed microorganisms, and antibacterial and antiviral microorganisms. It discloses a biofilter characterized in that the groups can coexist.
  • Patent Document 5 discloses that a nanofiber sheet having an antibacterial function is spread on the ground surface, a super-water-repellent nanofiber sheet is spread thereon, and further, breeding water is poured into a culture pond formed by stacking slag thereon.
  • the present invention discloses a method for purifying a closed-circulation onshore aquaculture farm, wherein aquacultured fish and shellfish such as shrimp are cultured.
  • aquaculture is repeatedly performed in a certain place from the viewpoint of securing a place for aquaculture and production controllability. Also, during aquaculture, aquatic products grow at a higher density than the natural environment. Therefore, every time aquaculture is carried out, organic matter such as excretion of fishery products, carcasses, and remains of food is produced, and the effects are produced and accumulated in the place where the fish are cultured.
  • An object of the present invention is to provide a method for purifying and reforming organic substances and nitrogen components in such repeatedly used culture tanks. Another object of the present invention is to stably cultivate aquatic products in a modified culture tank.
  • the present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, have found that the following inventions meet the above-mentioned objects, and have reached the present invention. That is, the present invention relates to the following inventions.
  • a method for modifying a culture tank for aquatic products including a mixing step of modifying a sediment by mixing a modifier containing a humic substance and a silicate compound with the sediment of the culture tank.
  • Tank reforming method ⁇ 2> The method for reforming a culture tank according to ⁇ 1>, further including a tilling step of tilling the sediment mixed with the modifying agent after the mixing step.
  • ⁇ 4> A method for culturing aquatic products using a culture tank modified by the modification method according to any one of the above ⁇ 1> to ⁇ 3>, wherein breeding water is supplied to the modified culture tank.
  • ⁇ 6> A method for cultivating aquatic products, comprising a reforming step of mixing a modifying agent containing humic substances and a silicate compound into breeding water supplied to the aquaculture tank.
  • ⁇ 7> By having an oxygen supply means to the breeding water and controlling the amount of oxygen by the oxygen supply means, A low oxygen period for controlling the dissolved oxygen concentration of the breeding water to a low concentration, The method for cultivating aquatic products according to any of the above ⁇ 4> to ⁇ 6>, further comprising a dissolved oxygen concentration control step having a high oxygen period in which the dissolved oxygen concentration of the breeding water is controlled to a high concentration.
  • ⁇ 8> The culture method according to any one of ⁇ 4> to ⁇ 7>, wherein the aquatic product is a crustacean.
  • a method for modifying a culture tank for aquatic products wherein the bottom substance of the culture tank contains humic substances and silicate compounds containing fulvic acid, which is a hydrophobic-like substance, according to the method of the International Society for Humic Substances (IHSS).
  • a mixing step of modifying the sediment by mixing a modifying agent wherein the amount of the sediment mixed with the sediment in the mixing step is 100 mg / 1000 m 2 or more as the humic substance equivalent to 5, 000 mg / 1000 m 2 or less, and the silicate compound is 1 kg / 1000 m 2 or more and 100 kg / 1000 m 2 or less.
  • ⁇ A2> The method according to ⁇ A1>, wherein the humic substance is a fulvic acid solution having a fulvic acid concentration of 10 mg / L to 2,500 mg / L.
  • ⁇ A3> The method for modifying a culture tank according to ⁇ A1> or ⁇ A2>, wherein the silicate compound is a silicate compound containing aluminum oxide in an amount of 10% by mass or more and 30% by mass or less.
  • ⁇ A4> A method for modifying an aquaculture tank for aquatic products, comprising a humic substance containing fulvic acid, which is a hydrophobic-like substance, according to the method of the International Humic Society (IHSS) in the bottom of the aquaculture tank.
  • IHSS International Humic Society
  • the mixing amount of the humic substances in the mixing step is 100 mg / 1000 m 2 or more as fulvic acid equivalent to 5,000 mg / 1000 m. 2 or less, the method of reforming the culture tank.
  • ⁇ A7> A method of cultivating aquatic products using a culture tank modified by the modification method of any one of ⁇ A1> to ⁇ A6>, wherein breeding water is supplied to the modified culture tank.
  • a fulvic acid solution having a fulvic acid concentration of 10 mg / L to 2,500 mg / L, which is a hydrophobic-like substance, according to the method of the International Humic Society (IHSS) was added to breeding water supplied to a culture tank for aquatic products.
  • a method for cultivating aquatic products comprising a modifying step of mixing a modifying agent containing a silicate compound containing 10% by mass or more and 30% by mass or less of aluminum oxide.
  • ⁇ A10> Having an oxygen supply means to the breeding water and controlling the amount of oxygen by the oxygen supply means, the dissolved oxygen concentration of the breeding water is continuously reduced to a low concentration of 0.5 ppm or more and 3.5 ppm or less.
  • ⁇ A11> The aquaculture method according to any one of ⁇ A7> to ⁇ A10>, wherein the aquatic product is a crustacean.
  • the present invention it is possible to purify and reform organic substances and nitrogen components in the culture tank, and to stably grow aquatic products in the modified culture tank.
  • the method for modifying a culture tank according to the present invention is a method for modifying a culture tank for aquatic products, and the method for modifying the bottom substance by mixing a modifier containing humic substances into the bottom substance of the culture tank. Having a process.
  • the modifier preferably contains a silicate compound. In this way, by mixing the modifying agent with the bottom material of the culture tank, the bottom material is improved, and the organic substance removing function and the like as the culture tank are improved.
  • the present invention assumes the following mechanism of action.
  • an aquaculture environment for marine products although marine products are bred at a high density as an economic act, the purification function of the natural world is not exhibited. This is thought to be due to the fact that soil microorganisms living in artificial structures such as aquaculture tanks and breeding water are not aware that the purification ability has been lost by abandoning the metabolic function acquired in the natural environment. .
  • the present inventors have obtained such knowledge from empirical rules.
  • Soil microorganisms are a general term for microorganisms mainly composed of soil bacteria.However, microorganisms with metabolic functions that function on organic substances and microorganisms with metabolic functions that function on nitrogen components coexist. . For example, when raising aquatic products in a closed aquaculture tank, the most problem is how to deal with organic matter and nitrogen components contained in residual foods and excrement.
  • the present invention purifies these.
  • organic matter organic matter that cannot be decomposed into carbon dioxide and water by only soil microorganisms in an environment of an artificial structure will rot.
  • the microorganisms are induced to activate the metabolism of soil microorganisms in the natural environment, are activated, suppress rot, and promote humification.
  • Nitrogen bacteria and denitrifying bacteria have also abandoned their metabolic functions in the natural environment, just as soil microorganisms in the environment of man-made structures have abandoned the metabolic functions of nitrogen components. This is because the nitrification reaction does not occur in the organic nitrogen and the ammonia nitrogen, and the nitrogen remains as it is.
  • nitrifying bacteria and denitrifying bacteria which are soil microorganisms inhabiting the aquaculture cultivation, are induced to natural metabolic functions and activated by intentionally utilizing humic substances generated by the soil microorganisms themselves.
  • organic nitrogen and ammonia nitrogen are transformed into nitrite nitrogen / nitrate nitrogen, and nitrite nitrogen / nitrate nitrogen reacts with a hydrogen donor to denitrify.
  • the hydrogen donor organic matter contained in the residual food and excrement is utilized. As a result, it is possible to simultaneously remove the organic matter and the nitrogen component, which are the two major factors that worsen the habitat environment in the culture.
  • including a silicate compound is also useful for generating phytoplankton and algae because iron fulvicate functions.
  • excessive consumption of carbon dioxide due to the photosynthesis reaction and provision of natural oxygen in water also occur, and phytoplankton and algae themselves can also feed on aquatic products.
  • the marine product is a fish, a marine mammal, a marine invertebrate, a seaweed, or the like, which is used for food or life.
  • the present invention can improve the cultivation environment of cultivated aquatic products, and the aquatic products to be cultivated can be widely targeted such as freshwater fish, saltwater fish, shellfish, and crustaceans.
  • Aquaculture techniques include pond aquaculture, paddy aquaculture, inland water aquaculture such as aquaculture in tidal flats and rivers, onshore aquaculture ponds and salt ponds aquaculture, compartmental aquaculture divided by dikes and nets, hanging aquaculture, and geodistribution.
  • Various aquatic products cultivated in marine aquaculture such as aquaculture can be targeted.
  • cultured aquatic products include carp, rainbow trout, sweetfish, dace, eel, goldfish, tropical fish, turtle, bullfrog, loach, mullet, crucian carp, sea bream, prawn, yellowtail, red sea bream, tiger puffer, oyster, oyster, sea squirt , Seaweed, seaweed, clams, clams, scallops and the like.
  • the present invention is for modifying a culture tank.
  • the aquaculture tank is a place used when artificially breeding and rearing aquatic products in a relatively narrow water area. For example, aquaculture ponds and paddy fields, partitioned tidal flats, rivers, seas, and onshore facilities.
  • the method for modifying a culture tank of the present invention is particularly directed to a culture tank having bottom sediment in order to fix the effect of the modification.
  • the term “sediment” refers to soil, sand, gravel, stone, sand mud, and the like provided mainly on the bottom of the culture tank. These sediments contribute to the food chain for breeding aquatic products, contribute to the growth of phytoplankton, etc., which feed on aquatic products, and contribute to the purification of residual food and dead bodies of aquatic products. I do. For this reason, sediment is provided at the bottom of the culture tank or the like in various culture techniques.
  • the reforming method of the present invention has a mixing step of modifying the bottom by mixing a modifier containing humic substances into the bottom of the culture tank.
  • the modifier may include a silicate compound.
  • This mixing is a state in which the modifying agent is dispersed on the sediment, mixed with stirring or plowing to disperse and contact the sediment.
  • the sediment is reformed by the mixing step.
  • This reforming in particular, purifies the organic matter and the like accumulated in the sediment, promotes humification, and purifies the humus, making the environment of the aquaculture tank suitable for aquaculture of aquatic products.
  • fulvic acid derived from humic substances and iron (iron ions) derived from silicate compounds are supplied to the sediment.
  • iron fulvicate is produced and supplied from the sediment to the culture tank.
  • algae such as cyanobacteria and diatoms, phytoplankton, and the like also easily proliferate, and phytoplankton and the like, which are food for aquatic products, are easily supplied in the culture tank.
  • iron contained in silicate compounds is oxidized in seawater to become granular iron and precipitates on sediment, but when it comes into contact with fulvic acid, the antioxidant power of fulvic acid changes it from ferrous iron to ferrous iron.
  • Ferrous iron is reduced to fulvic acid to form colloidal iron fulvic acid, which is used for phytoplankton and the like.
  • These phytoplanktons also contribute to photosynthesis and have the effect of supplying oxygen into the culture tank.
  • humic substances are supplied in the mixing step, thereby activating nitrifying bacteria and denitrifying bacteria resident in the culture tank.
  • denitrifying bacteria which particularly require anaerobic conditions, have abandoned their metabolic functions under the natural environment due to oxygen supply for growing aquatic products in the aquaculture tank, and have lost their functions.
  • the decrease in the activity of the denitrifying bacterium is overlooked in the conventional aquaculture, and the aquaculture efficiency is reduced, and the operation management is complicated though an additional device is provided for the denitrification.
  • such a denitrifying bacterium which originally existed in a culture tank or the like, is activated by humic substances so that the denitrifying bacterium or the like readily acts.
  • the modifier one containing humic substances is used.
  • the modifier may include a silicate compound.
  • the modifier may further include a pH adjuster, a viscosity adjuster, a salt for adjusting a salt concentration, and the like, as appropriate.
  • Humic substances are said to be a generic term for "organic substances whose chemical structures are not specified (non-living organic substances)" in which biological organisms are destroyed by microbial or chemical action after the death of the organism. It has been empirically known that some humic substances show functionality and others do not.This is because the organic matter, which is an organic substance in the natural world, tries to return to the soil. It is considered that the influence of whether or not an intermediate product is contained is large. Humid substances containing this intermediate product, that is, functional humic substances, are sometimes referred to as humic precursors.
  • humin, fulvic acid, humic acid, and the like are contained in the humic precursor or humic substance (humus) as the humification degree (polycondensation reaction degree) of the component.
  • the weight ratio of fulvic acid to humic acid is about 2: 8.
  • the humic substances of the present invention contain fulvic acid.
  • Fulvic acid itself is humic acid because of its solubility in acids and alkalis among humic substances (particularly humic precursors) produced by reacting metabolites containing phenol and / or compounds having a phenol-exposed group with organic substances and the like. , But a mixture of organic substances having various structures.
  • a fulvic acid solution contains fulvic acid at a higher ratio than general humus, and has a lower content of humic acid and the like.
  • fulvic acid solution fulvic acid iron is generated more efficiently.
  • a lead-up by T & G Corporation can be used.
  • fulvic acid and humic acid in the present application are based on the classification of the International Society of Humic Substances to which the Japanese Society of Humic Substances belongs, and the chemical structure of biological organisms that are disrupted by microbial and chemical actions has not been identified.
  • classification is based on solubility in alkalis and acids. That is, fulvic acid is a component that is soluble in alkali and soluble in acid.
  • humic acid is a component that is soluble in alkali but insoluble in acid.
  • Humin is a component that is insoluble in alkali and insoluble in acid.
  • a hydrophobic-like substance is separated and purified from the fulvic acid extract in accordance with the method of the International Society of Humic Substances (IHSS), and this substance is physically and chemically similar to the standard fulvic acid distributed by the Japan Humic Society (JHSS). It has been confirmed that it has characteristics (absorption, FTIR, 3D fluorescence spectrum, solid-state NMR, etc.).
  • the concentration of the fulvic acid can be determined by using a 3D fluorescence spectrum as an index for the degree of the fulvic acid activity.
  • the 3D fluorescence spectrum is determined based on the wavelength of the excitation light-fluorescence and the distribution of the intensity thereof using light in the range from UV to visible light. It is confirmed whether the tendency of the distribution is that of fulvic acid, and if a characteristic peak is observed near 310 nm to 410 nm (excitation light wavelength-fluorescence wavelength), it is determined that the fulvic acid activity is high (the fulvic acid concentration is high). Is determined.
  • the fulvic acid concentration can be simply calculated as an estimated concentration by creating a calibration curve based on the fluorescence wavelength at the peak near 410 nm.
  • the estimated concentration of the fulvic acid solution is about 10 mg / L to 2,500 mg / L, depending on the organic substance used as a raw material and the production conditions. It is preferable to use a fulvic acid solution having a fulvic acid concentration of 20 mg / L or more, 30 mg / L or more, 100 mg / L or more, and 500 mg / L or more. These can be used as stock solutions with appropriate dilution.
  • the fulvic acid content of a currently sold fulvic solution (trade name “Lead Up” (T & G)) is estimated to be about 1000 ppm.
  • the fulvic acid activity is simply expressed as a ratio of the fluorescence intensity at the wavelength that becomes the peak of the 3D fluorescence spectrum to the absorbance at the wavelength of the excitation light, the fluorescence intensity peak value around 410 nm / the excitation light around 310 nm. From the intensity peak value (fluorescence intensity (If) at the fluorescence wavelength / absorbance (Abs) at the excitation light wavelength), it can be determined as “fulvic acid-fluorescence spectrum ratio”. For example, in the case of a fulvic acid solution, the fulvic acid-fluorescence spectrum ratio shows a value of about 5,000 to 30,000.
  • the fulvic acid activity may be arbitrarily determined, as long as fulvic acid is sufficiently supplied. It is possible to expect a reforming effect such as an effect obtained by the above, an effect obtained for a long time, and an excellent organic substance purifying function. For this reason, the fulvic acid-fluorescence spectrum ratio of the humic substances used in the mixing step may have a lower limit such as 100 or more, 500 or more, 1000 or more, 2000 or more, 3000 or more, 5000 or more, and 8000 or more. On the other hand, there is no particular upper limit, but for example, an upper limit of 100,000 or less, 80000 or less, 50000 or less, or 30000 or less may be provided.
  • the fulvic acid-fluorescence spectrum ratio is almost a value close to zero. Note that this ratio is not a value indicating the concentration but an index of the quality or activity of fulvic acid, and greatly increases or decreases due to a reaction caused by contact with an organic substance.
  • the content of humic acid can be determined based on the concentration of humic acid by performing purification or analysis for specifying humic acid.
  • the wavelength of the excitation light-fluorescence and the distribution of the intensity thereof are determined by using the light in the range from UV to visible light using the 3D fluorescence spectrum when performing the above-described measurement of fulvic acid. It can be determined based on this.
  • humic acid is present, a peak is observed around 450 nm / 530 nm (excitation light / fluorescence).
  • the blackness of the solution increases, and in the above-mentioned fulvic acid-fluorescence spectrum ratio, the absorbance (Abs) of the excitation light wavelength around 310 nm increases, and the fluorescence intensity (If) of the fluorescence wavelength around 410 nm decreases.
  • the fulvic acid-fluorescence spectrum ratio is hardly in a preferable range for a fulvic acid solution. Therefore, the fulvic acid solution of the present invention does not show a double peak similar to that of a humic acid solution of fulvic acid: humic acid equivalent to 2: 8, which is a normal humic substance, or has a peak corresponding to humic acid.
  • An index lower than a general double peak value can be used as an index.
  • the fulvic acid-fluorescence spectrum ratio may be used as an index.
  • the fulvic acid and fulvic acid solution used in the present invention can be used with reference to the technology disclosed in Japanese Patent No. 6026631.
  • the present invention can be used by mixing a silicate compound for modifying bottom sediment or supplying the silicate compound to breeding water in a culture tank.
  • the silicate compound used in the present invention refers to a compound in which activated silicic acid derived from diatomaceous earth or the like contains aluminum or iron.
  • activated silicic acid derived from diatomaceous earth or the like contains aluminum or iron.
  • those derived from andesitic or rhyolite rocks can be suitably used.
  • a mixture of active silicic acid, which is an artificial product, and a metal such as iron or aluminum in a ratio equal to or higher than that of a natural product may be used.
  • the amount of aluminum contained in the silicate compound is preferably at least 5% by mass as aluminum oxide (Al 2 O 3 ).
  • the amount of aluminum oxide is more preferably 10% by mass or more, and may be 11% by mass or more and 12% by mass or more.
  • the upper limit of the amount of aluminum oxide may not be limited within a range that sufficiently contains activated silicic acid and iron, but may be 30% by mass or less, 25% by mass or less, or 20% by mass or less.
  • the amount of iron contained in the silicate compound is preferably 3% by mass or more as iron oxide (total amount of ferrous oxide and ferric oxide).
  • the amount of iron oxide is more preferably 4% by mass or more, and may be 4.5% by mass or more and 5.0% by mass or more.
  • the upper limit of the amount of iron oxide may not be limited within a range that sufficiently includes active silicic acid and aluminum oxide, but may be 30% by mass or less, 25% by mass or less, 20% by mass or less, or 15% by mass or less.
  • the silicate compound also contains components that become mineral components such as iron and aluminum, and the silicate compound is a growth environment for soil microorganisms, mainly soil bacteria that inhabit the sediment and breeding water in the culture tank. It is effective as a stabilizer. In addition, it functions as a catalyst for promoting humification of organic matter contained in the bottom material of the aquaculture tank and breeding water. It is also effective as a nutrient for photosynthetic organisms such as phytoplankton and algae that inhabit the bottom of culture tanks and breeding water. It is also useful as a raw material for producing iron fulvicate in a state contributing to these.
  • silicate compound when aluminum or iron is contained as the silicate compound, these aluminum or iron are supported on the silicate of diatomaceous earth and are easily stabilized. At the same time, it is considered that such a silicate compound is also useful as a place for carrying bacteria contributing to purification of a culture tank such as denitrifying bacteria activated with humic substances.
  • the amount of these modified substances should be set as appropriate in consideration of the type of the culture tank, the breeding period of the aquatic products, the conditions of use of the culture tank, etc., as long as the bottom material of the culture tank can be modified. Can be.
  • the mixing amount can be set based on the size of the bottom surface of the culture tank in which the sediment is disposed. By setting the content in these preferable ranges, it is possible to exert effects of activating denitrifying bacteria and the like and improving effects such as growth of phytoplankton.
  • the mixing amount of the humic substance is preferably 50 mg / 1000 m 2 or more as the fulvic acid equivalent contained in the humic substance.
  • 1 L 50 mg fulvic acid equivalent
  • 1 L 50 mg fulvic acid equivalent
  • Mixing amount of humic substances as fulvic acid equivalent weight 80 mg / 1000 m 2 or more and, 100 mg / 1000 m 2 or more and, more preferably to higher concentrations and 150 mg / 1000 m 2 or more.
  • An upper limit may not be set because there is no adverse effect of increasing the concentration of humic substances. However, an upper limit may be set in consideration of the amount of raw materials, the application time, etc., and 10,000 mg / 1000 m 2 or less, It may be 5,000 mg / 1000 m 2 or less.
  • the mixing amount of the silicate compound is preferably 1 kg / 1000 m 2 or more.
  • the mixing amount of the silicate compound is more preferably set to a higher concentration of 3 kg / 1000 m 2 or more, 5 kg / 1000 m 2 or more, or 10 kg / 1000 m 2 or more. Since there is no adverse effect of increasing the concentration of the silicate compound, there is no need to set the upper limit. However, the upper limit may be set in consideration of the limitation of the amount of the raw material, the spraying time, etc., and 100 kg / 1000 m 2 or less, 50 kg / It may be 1000 m 2 or less.
  • the reforming method of the present invention is preferably performed at the time of refilling the breeding water in the aquaculture tank in order to reform the sediment.
  • the breeding water in the aquaculture tank is such that after the aquatic products have sufficiently grown and the aquatic products in the tank have been collected and shipped, the used breeding water is discharged and replaced with new breeding water.
  • Aquaculture ponds, paddy fields, shore facilities, etc. which are particularly easy to make artificial adjustments, discharge almost all breeding water when switching. It is preferable to spray and mix the modifier on the sediment of the culture tank from which the breeding water has been discharged. Since the breeding water is discharged, the concentration of the modifier directly mixed with the sediment is improved, and an excellent reforming effect is easily obtained. Even when the breeding water is discharged, the sediment may be in a wet state or may have an extremely shallow water level. The bottom sediment may be appropriately sun-dried or plowed as described below.
  • the reforming method of the present invention preferably includes a tilling step of tilling the sediment mixed with the modifying agent after the mixing step.
  • the modifier is more uniformly mixed with the sediment.
  • This tilling digs the bottom of the culture tank and swells it softly.
  • This tilling may be performed on the sediment in a state where the breeding water is stretched, or may be performed on the sediment in a state where the breeding water is discharged. It is preferable to perform the cultivation in a state where the breeding water is discharged so as to reduce the influence of water resistance and weight at the time of tilling work and to efficiently cultivate a deeper range.
  • By cultivating it is possible to supply oxygen to the inside of the bottom sediment to more efficiently purify the deposited organic matter, etc., and to maintain the state where iron fluvic acid etc. contained in the modifier is maintained more widely. it can.
  • the reforming method of the present invention has a ripening step of ripening the tilled sediment in a drainage state after the tilling step.
  • the ripening is to allow the marine products to be cultured to stand without being charged, or to stir appropriately.
  • the aging step may be performed using wet bottom sediment. It is preferable to carry out the process without being filled with water. Aging is for the purpose of solving problems that cannot be solved by solar disinfection of sediment, for example, to prevent decay due to a humification reaction of residual organic substances and to control various bacteria such as spoilage bacteria.
  • the breeding water is aged, it can be made to conform to the aging of the sediment.
  • This aging step can be performed by appropriately setting the time according to the state of the culture tank and the like. For example, it is preferably performed for 6 hours or more.
  • the aging time may be 10 hours or longer, 20 hours or longer, 40 hours or longer, 60 hours or longer. There is no adverse effect of performing aging for a long time, but since the function of mixing humic substances and silicate compounds may be reduced, such as within 60 days, within 45 days, within 30 days, within 20 days, within 10 days An upper limit of the aging time may be set.
  • the culture method of the present invention includes a culture step of supplying breeding water to a culture tank modified by the modification method of the present invention and culturing.
  • the equipment in the bottom of the culture tank has been sufficiently purified, so contamination is unlikely to occur, and the fluctuation of dissolved oxygen concentration due to the purification of organic matter in the bottom, etc. Can be suppressed.
  • phytoplankton such as algae also breed, and contribute to purification of residual food and excrement of aquatic products cultured in the culture tank. Therefore, aquaculture efficiency of aquatic products is improved. For example, the survival rate of aquatic products is improved, higher-density breeding than before is possible, the growing period is shortened, and the aquatic products with excellent palatability in which the astringency of the aquatic products is suppressed are obtained. be able to.
  • Aquaculture techniques include pond aquaculture, paddy aquaculture, inland water aquaculture such as aquaculture in tidal flats and rivers, onshore aquaculture ponds and salt ponds aquaculture, compartmental aquaculture divided by dikes and nets, hanging aquaculture, and geodistribution.
  • sea surface culture such as in aquaculture
  • a culture method for culturing various aquatic products can be employed.
  • the breeding water is seawater or freshwater suitable for breeding aquatic products to be cultured, or water whose salt content is appropriately adjusted.
  • the breeding water is supplied to the culture tank so as to have a capacity corresponding to the stage of the culture.
  • the reforming method of the present invention is preferably carried out in a state where breeding water is discharged in order to reform the sediment. After completion, when used, cultivation is performed with breeding water supplied.
  • the method may have a reforming step of mixing a humic substance and a modifier containing a silicate compound with the breeding water supplied to the aquaculture tank for aquatic products.
  • This is a culture tank modified by the method for modifying a culture tank of the present invention, that is, a modified culture water containing humic substances and a silicate compound, which is used in combination with one having a modified sediment. It may have a reforming step of mixing agents.
  • breeding water is provided with the same water purification function as when the sediment is modified according to the present invention, and cultivation is performed.
  • the mixing amount and the like can be the same conditions as the mixing when performing the above-described bottom sediment reforming.
  • the water depth is set according to the specifications of the aquaculture tank, the type of aquatic product to be cultured, the timing of the aquaculture, and the like. For example, the water depth is appropriately set from about 1 to 5 m or about 2 to 4 m. This water depth is not always constant within a range in which aquatic products can be cultured, and fluctuates depending on the weather, time zone, culture time, and the like. For this reason, the mixture amount of humic substances and silicate compounds can be set and managed by using the size of the cultivation tank as an index instead of the amount of breeding water.
  • the mixing of the modifying agent into the breeding water may be performed a plurality of times with a predetermined period after the start of aquaculture.
  • the period after the start of aquaculture or after the mixing of the modifier may be additionally mixed after a period of 3 days or more, 1 week or more, 2 weeks or more, 3 weeks or more.
  • the upper limit of this period may be additionally mixed within a range such as within 3 months, within 2 months, or within 6 weeks as appropriate.
  • the stirring means a submersible pump, submersible paddle, blower or the like can be used.
  • the stirring time can be set within a range of about 72 hours or less before the introduction of the marine product in consideration of aging.
  • the agitation time may be determined by the activity of aquatic products during aquaculture or by normal agitation of the aquaculture tank. In consideration of aging and the like, the time for actively maintaining the stirring state may be determined as 1 hour or more, 6 hours or more, 12 hours or more, 24 hours or more.
  • the upper limit of the aging time may be set within 48 hours or 36 hours.
  • the cultivation method of the present invention has an oxygen supply means for the breeding water, and controls the amount of oxygen by the oxygen supply means, thereby controlling a dissolved oxygen concentration of the breeding water to a low concentration, and a low oxygen period. It is preferable to have a dissolved oxygen concentration control step having a high oxygen period for controlling the dissolved oxygen concentration of the breeding water to a high concentration.
  • nitrifying bacteria and denitrifying bacteria can be activated. Thereby, it is possible to perform advanced treatment for sufficiently reducing nitrogen-containing organic matter in the culture tank. In addition, since both aerobic and anaerobic treatments can be performed in the culture tank, the entire organic matter can be sufficiently removed in the culture tank.
  • nitrification is performed, dissolved oxygen is required, so that the breeding water has a high oxygen period in which the dissolved oxygen concentration is controlled to a high concentration.
  • the high oxygen period is a period in which the oxygen concentration is equal to or higher than a predetermined dissolved oxygen concentration.
  • the lower limit of the dissolved oxygen concentration which is an index of the high oxygen period is preferably 4.5 ppm or more, more preferably 5 ppm or more, and particularly preferably 6 ppm or more.
  • the upper limit of the dissolved oxygen is not particularly limited, but may be high by supplying oxygen itself or a gas having a high oxygen concentration.If the effect of excessively supplying oxygen is limited, the apparatus load or the low oxygen period may be reduced.
  • the upper limit may be 14 ppm or less, 12 ppm or less, or 10 ppm or less in consideration of the switching efficiency or the like.
  • the high oxygen period during which the oxygen concentration is equal to or higher than the predetermined dissolved oxygen concentration is preferably set to 1 hour or more / day. More preferably, it is at least 2 hours / day or at least 3 hours / day.
  • the high oxygen period can be achieved by installing a pump or the like that supplies air or oxygen to the breeding water in the aquaculture tank and supplying air or oxygen using them to increase the dissolved oxygen concentration.
  • the dissolved oxygen concentration can be controlled by, for example, setting the number of operations while measuring the dissolved oxygen concentration by attaching a plurality of air supply means.
  • the low oxygen period is a period in which the oxygen concentration is equal to or lower than a predetermined dissolved oxygen concentration.
  • the upper limit of the dissolved oxygen concentration which is an index of the low oxygen period is preferably less than 4.5 ppm, more preferably 4 ppm or less, and particularly preferably 3.5 ppm or less.
  • the lower limit of the dissolved oxygen concentration in the low oxygen period may not be particularly defined. However, if it is too low, the activity of the marine product may decrease or the survival rate may decrease. Therefore, the lower limit of the dissolved oxygen concentration during the low oxygen period may be set, and may be set to 0.5 ppm or more, 1.0 ppm or more, or 1.5 ppm or more.
  • the low oxygen period during which the oxygen concentration is equal to or lower than the predetermined dissolved oxygen concentration is preferably 1 hour or more / day. More preferably, it is at least 2 hours / day or at least 3 hours / day.
  • Aquaculture tanks generally breed aquatic products at a higher density than the natural environment. For this reason, in many cases, the dissolved oxygen concentration tends to decrease due to the use of dissolved oxygen accompanying the growth activity of aquatic products or the aerobic purification of organic substances in the culture tank.
  • the low oxygen period can be achieved by stopping the supply of oxygen (air) to the breeding water in the aquaculture tank, thereby lowering the dissolved oxygen concentration.
  • the concentration of dissolved oxygen may be positively reduced by supplying an inert gas such as nitrogen gas to the breeding water in the culture tank.
  • the cycle of performing the high oxygen period and the low oxygen period can be performed at a cycle of about 0.5 cycle / day (that is, one cycle for two days) to about three cycles / day.
  • This cycle can be appropriately set according to the type of the culture tank, the type of the marine product, the breeding time, and the like.
  • Aquatic products are roughly classified into nocturnal and nocturnal products. Oxygen is required during periods of active activity, and less likely during periods of low activity. From this characteristic, when breeding nocturnal aquatic products, it is preferable to have a high oxygen period during the night and a low oxygen period during the day. In breeding daytime aquatic products, it is preferable to have a high oxygen period during the day and a low oxygen period at night.
  • the nitric acid reaction and the denitrification reaction are repeatedly performed in these dissolved oxygen concentration control steps to highly treat organic substances and nitrogen components.
  • the humic substance fulvic acid is supported on the sediment. Residual food, dead bodies, etc. settle and accumulate on the sediment. In purifying these organic substances, the bottom sediment greatly influences the maintenance of the environment of the culture tank.
  • the sediment is in a state in which fulvic acid is carried, and furthermore, with a certain periodicity, there is an aerobic environment and an anaerobic environment, and in the sediment, humic acid in which fulvic acid dominates is also present. It is thought to proceed.
  • Such humic acid superiority in fulvic acid improves the purification function and the breeding effect of aquatic products.
  • the dissolved oxygen concentration can be measured by a dissolved oxygen concentration meter. Based on the measured dissolved oxygen concentration, the number and output of the operated oxygen supply means may be set, or may be controlled automatically.
  • water temperature, pH, salt concentration, transparency, and the like can be further operated as management items.
  • FIG. 1 is a view for explaining a first embodiment according to the culture tank of the present invention.
  • the aquaculture tank 10 has a water storage tank 100 including breeding water 101 and bottom sediment 102.
  • the cultivation of the present invention can be carried out by appropriately mixing humic substances and silicate compounds in the breeding water 101.
  • a humic substance or a silicate compound is mixed with the sediment 102, aged appropriately, and the breeding water 101 is supplied to form the aquaculture tank 10, and the aquatic products to be cultured are released into the breeding water 101 to start aquaculture. be able to.
  • the culture tank 10 is provided with air supply pumps 211, 221, and 231 and air supply means by the air supply pipes 212, 222, and 232.
  • the switching valves 213, 223, and 233 can be used to switch the presence or absence of air supply to the culture tank.
  • the air supply pumps 211, 221, and 231 are also connected to the control unit 30, and can control the presence / absence of air supply and the amount of air supply.
  • the control by the control means 30 may be such that the operation according to the time zone is programmed in advance, the control may be performed based on monitoring by the monitoring means 40 as described later in part, or the control may be based on input information from the input means 60. Can be.
  • Monitoring means 40 is attached to the culture tank 10 so that the condition of the breeding water 101 can be monitored. Items to be monitored include water temperature, pH, DO, various indicators such as organic substances and nitrogen (TC, TOC, COD, BOD, TN, NH 4 + , NO 2 , NO 3 ), etc. it can.
  • the monitoring means 40 is connected to the control means 30, and the control means 30 can control the operation of the air supply pumps 211, 221, and 231 based on the items of the monitoring means, the operation time, and the like.
  • the control status of the control unit 30 and various parameters monitored by the monitoring unit 40 can be displayed on the display unit 50.
  • control of the control means 30 and the items to be monitored by the monitoring means 40 and the display on the display means 50 can be processed based on the signal input from the input means 60, and can be selected or changed.
  • a storage means (not shown) is also provided to store various parameters and appropriately call and confirm them, or to store data of control conditions of the control means in the storage means, and to use the data to control the control means 30. Control may be performed.
  • a culture tank 10 is a culture device suitable for the culture method of the present invention.
  • the green tough fine powder contains 13.7% by mass of aluminum oxide, 1.0% by mass of iron oxide (ferrous), and 5.0% by mass of iron oxide (ferric).
  • the green tough fine powder was sprayed evenly over the culture pond (5070 m 2 ).
  • the reform start date is February 1. [2.2 Plowing and ripening]
  • the above-mentioned lead-up and green tough were sprayed and mixed, and then plowed with a cultivator. Then, it left still for 5 days as a ripening period. As a result, a culture pond with modified sediment was obtained.
  • Table 1 shows the measurement results of the management index after the start of the aquaculture.
  • Culture was carried out using river water as breeding water, and feeding was carried out in accordance with the usual method of shrimp culture.
  • the aquaculture tank is equipped with three air pumps to control the concentration of dissolved oxygen in the breeding water to a low level based on the breeding conditions, weather, shrimp size, and DO measurements. During the low oxygen period, only one air pump should be operated, and during the high oxygen period during which the dissolved oxygen concentration in the breeding water is controlled to a high level, three air pumps should be operated at the same time. Aquaculture was performed as an indicator.
  • the management index indicates that the night time (PM 6:00 to AM 6:00) is a high oxygen period and DO is 5 to 6 mg / L.
  • the daytime AM 6:00 to PM 6:00
  • aquaculture was performed using the low oxygen period during the day and a DO of 3 to 4 mg / L as a management index because the amount of activity decreased and oxygen consumption was small.
  • FIGS. 2 to 9 are photographs for explaining the cultivation state and the like.
  • FIG. 2 is a photograph showing river water used for breeding water.
  • FIG. 3 shows the sediment before the reforming of the sediment. In the sediment, repeated use of the cultivation pond shows decay and sludge.
  • FIG. 4 shows a period in which a sheet is stretched on the sediment after the mixing of the modifying agent so as to ensure a daily minimum water temperature of 20 ° C. or higher in preparation for breeding.
  • FIG. 5 shows a state in which the culture pond is filled with water after the ripening period is completed.
  • FIG. 6 shows the state of shrimp 30 days after the start of the culture.
  • FIG. 7 shows the state of shrimp 45 days after the start of the culture.
  • 8 and 9 show the state of shrimp 63 days after the start of aquaculture.
  • FIG. 8 shows five shrimp harvested on the 63rd day of breeding start, which is the harvest date, and it was confirmed that the body length was 13 cm to 15 cm.
  • the present invention can be used for aquaculture of aquatic products, and contributes to the improvement of the quantity and quality of aquatic products to be cultured by reforming aquaculture tanks and managing during aquaculture, and is industrially useful.

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Abstract

Provided is a method for purifying organic matter and nitrogen components in an aquaculture tank that is repeatedly used, and modifying the aquaculture tank. Also provide is a method for performing aquaculture of aquatic life in a stable manner using a reformed aquaculture tank. A method for reforming an aquaculture tank for aquatic life, wherein the method has a mixing step for mixing a modifier containing a humic substance and a silicate compound into the bottom material of the aquaculture tank, and thereby reforming the bottom material. A method for performing aquaculture of aquatic life using a reformed aquaculture tank, wherein the method has an aquaculture step for supplying breeding water into the reformed aquaculture tank and performing aquaculture.

Description

養殖槽の改質方法、および養殖方法Aquaculture tank reforming method and aquaculture method

 本発明は養殖槽の改質方法、および養殖槽を改質して用いる養殖方法に関する。 (4) The present invention relates to a method for modifying a culture tank and a method for modifying a culture tank.

 水産生物は、海や川、池、陸上設備などを用いた種々の養殖手法により生産されている。例えば、代表的な養殖対象となる水産生物であるエビ等の養殖技術として、特許文献1などが開示されている。特許文献1には、クルマエビが投入される水槽を遮光性のハウスで覆って前記水槽の水面における照度を100ルクス以下にし、照度と関係なく増殖する有益細菌を前記水槽内で優占的に増殖維持し、前記水槽内にクルマエビを投入して該クルマエビを養殖することを特徴とするクルマエビの養殖方法が開示されている。 Aquatic products are produced by various aquaculture techniques using the sea, rivers, ponds, onshore facilities and the like. For example, Patent Literature 1 and the like are disclosed as a technique for culturing shrimp and the like, which is a typical marine product to be cultivated. Patent Literature 1 discloses that an aquarium into which prawns are put is covered with a light-shielding house so that the illuminance on the water surface of the aquarium is 100 lux or less, and beneficial bacteria that grow regardless of illuminance dominantly proliferate in the aquarium. There is disclosed a method for cultivating a prawn, which comprises maintaining the prawn and cultivating the prawn in the water tank.

 養殖池などを用いる水産生物の養殖では、養殖中や、繰り返し養殖をおこなうときの有機物等の処理が問題となる場合がある。このような養殖環境に関する技術として、例えば、特許文献2~5などが開示されている。 養 In aquaculture of aquatic products using a pond or the like, treatment of organic substances during aquaculture or during repeated aquaculture may become a problem. As techniques related to such a culture environment, for example, Patent Documents 2 to 5 and the like are disclosed.

 特許文献2は、飼育水槽内に養殖魚床を複数個間隔を設けて垂設すると共に、前記養殖魚床に加振手段を取り付けたことを特徴とする魚貝養殖装置を開示するものである。特許文献3は、魚介類を養殖するための養殖槽内の水を適宜循環経路を介して循環させる過程において浄化、調整する養殖方法であって、前記循環経路内に脱窒装置と活性炭吸着装置を設け、該装置に循環水の少なくとも一部を通して循環水の脱窒と有機難分解物質の除去を行うことを特徴とする水循環式養殖方法を開示するものである。 Patent Literature 2 discloses a fish and shellfish cultivation apparatus characterized in that a plurality of cultured fish beds are vertically provided in a breeding aquarium at intervals, and vibration means are attached to the cultured fish beds. . Patent Literature 3 is a culture method for purifying and adjusting water in a process of circulating water in a culture tank for culturing fish and shellfish through a circulation path as appropriate, wherein a denitrification apparatus and an activated carbon adsorption apparatus are provided in the circulation path. The present invention discloses a water circulation type aquaculture method, wherein denitrification of circulating water and removal of organic hardly decomposable substances are performed through at least a part of the circulating water through the apparatus.

 特許文献4は、強磁性鉄粉を坦持した粒状鉄型人工ゼオライトの菌株に鉄イオンを吸収した微生物群を着床または磁気吸着し、溶出有機物質・酸化分解微生物群および抗菌・抗ウイルス微生物群が共生できることを特徴とするバイオフィルターを開示するものである。特許文献5は、地盤面に抗菌機能を有するナノファイバーシートを敷き詰め、その上に超撥水性ナノファイバーシートを敷き詰め、さらに、その上にスラグを積み上げて形成した養殖池に飼育水を注水して、エビなどの養殖魚介類を養殖するようにしたことを特徴とする閉鎖循環式陸上養殖場の浄化方法を開示するものである。 Patent Document 4 discloses a method of implanting or magnetically adsorbing microorganisms that have absorbed iron ions to a strain of a granular iron-type artificial zeolite carrying ferromagnetic iron powder, and eluted organic substances, oxidatively decomposed microorganisms, and antibacterial and antiviral microorganisms. It discloses a biofilter characterized in that the groups can coexist. Patent Document 5 discloses that a nanofiber sheet having an antibacterial function is spread on the ground surface, a super-water-repellent nanofiber sheet is spread thereon, and further, breeding water is poured into a culture pond formed by stacking slag thereon. The present invention discloses a method for purifying a closed-circulation onshore aquaculture farm, wherein aquacultured fish and shellfish such as shrimp are cultured.

特開2006-217895号公報JP 2006-217895 A 特開2010-239956号公報JP 2010-239956 A 特開昭64-63325号公報JP-A-64-63325 特開2012-183051号公報JP 2012-183051 A 特開2016-178917号公報JP 2016-178917 A

 特許文献1~5等にも一部開示されているように、養殖は、養殖するための場の確保や生産管理性の観点から、一定の場所で繰り返し行われる。また、養殖時に、水産生物は自然環境よりも高密度で生育される。このため、養殖を行うたびに、水産生物の排せつ物や死骸、餌の残存物等の有機物が生じ、養殖する場所にはその影響が生じ蓄積する。 一部 As partially disclosed in Patent Documents 1 to 5, etc., aquaculture is repeatedly performed in a certain place from the viewpoint of securing a place for aquaculture and production controllability. Also, during aquaculture, aquatic products grow at a higher density than the natural environment. Therefore, every time aquaculture is carried out, organic matter such as excretion of fishery products, carcasses, and remains of food is produced, and the effects are produced and accumulated in the place where the fish are cultured.

 しかしながら、養殖する場所となる池や海等による有機物の分解浄化能力には限界がある。このため、水や二酸化炭素等に分解されなかった有機物は、養殖槽の池底などに堆積したり、一部は飼育に用いられた水の排出時に公の海域、河川等に排出され環境汚染の原因にもなっている。 能力 However, there is a limit to the ability to decompose and purify organic matter by ponds and seas that serve as aquaculture sites. For this reason, organic matter that has not been decomposed into water, carbon dioxide, etc., accumulates on the bottom of the pond in the aquaculture tank, and part of the organic matter is discharged into public waters and rivers when the water used for breeding is discharged, causing environmental pollution. It is also the cause.

 特に、飼育する水産生物の排出物に含まれる有機物及び有機態窒素、アンモニア態窒素である窒素成分の除去機能は、養殖環境の池や海等自体が十分な機能を備えることが難しい。 Especially, it is difficult for ponds and seas in aquaculture environments to have sufficient functions to remove organic matter and organic nitrogen contained in the effluent of bred aquatic products and nitrogen components such as ammonia nitrogen.

 これらの処理のために薬剤や資材を使用する場合もあるが、十分な分解や浄化効果が得られておらず、養殖されるエビなどの水産生物の生育が遅くなったり、生残率が低下したり、病気が発生したりする場合がある。また、脱窒素反応のための装置を取り付けることも提案されているが、養殖環境によっては設置環境の設備的な問題や資金的な問題等から、それらの装置を取り付けることが困難であったり、運転するための管理等が煩雑となり十分に活用できていない場合もあった。 In some cases, chemicals and materials are used for these treatments, but they do not have sufficient decomposition and purification effects, resulting in slow growth of aquacultured shrimp and other aquatic products and a decrease in survival rate. Or develop illness. Also, it has been proposed to attach a device for denitrification reaction, but depending on the aquaculture environment, it is difficult to install those devices due to the installation environment's equipment problems or financial problems, In some cases, management for driving was complicated and could not be fully utilized.

 本発明は、このような繰り返し使用される養殖槽の有機物及び窒素成分を浄化し、改質する手法を提供することを目的とする。また、改質された養殖槽で、安定した水産生物の養殖を行うことを目的とする。 An object of the present invention is to provide a method for purifying and reforming organic substances and nitrogen components in such repeatedly used culture tanks. Another object of the present invention is to stably cultivate aquatic products in a modified culture tank.

 本発明者は、上記課題を解決すべく鋭意研究を重ねた結果、下記の発明が上記目的に合致することを見出し、本発明に至った。すなわち、本発明は、以下の発明に係るものである。 The present inventors have conducted intensive studies to solve the above-mentioned problems, and as a result, have found that the following inventions meet the above-mentioned objects, and have reached the present invention. That is, the present invention relates to the following inventions.

 <1> 水産生物の養殖槽の改質方法であって、養殖槽の底質に腐植物質およびシリケイト化合物を含む改質剤を混合することで前記底質を改質する混合工程を有する、養殖槽の改質方法。
 <2> 前記混合工程のあと、前記改質剤を混合した前記底質を耕耘する耕耘工程を有する前記<1>記載の養殖槽の改質方法。
 <3> 前記耕耘工程のあと、前記耕耘された前記底質を熟成する熟成工程を有する前記<2>記載の改質方法。
<1> A method for modifying a culture tank for aquatic products, the method including a mixing step of modifying a sediment by mixing a modifier containing a humic substance and a silicate compound with the sediment of the culture tank. Tank reforming method.
<2> The method for reforming a culture tank according to <1>, further including a tilling step of tilling the sediment mixed with the modifying agent after the mixing step.
<3> The reforming method according to <2>, further comprising, after the plowing step, a maturing step of maturing the plowed bottom sediment.

 <4> 前記<1>~<3>のいずれかの改質方法により改質された養殖槽を用いる水産生物の養殖方法であって、前記改質された養殖槽に飼育水を給水し水産生物を養殖する養殖工程を有する水産生物の養殖方法。
 <5> 前記飼育水に、腐植物質およびシリケイト化合物を含む改質剤を混合する改質工程を有する前記<4>記載の水産生物の養殖方法。
 <6> 水産生物の養殖槽に給水された飼育水に、腐植物質およびシリケイト化合物を含む改質剤を混合する改質工程を有する水産生物の養殖方法。
 <7> 前記飼育水への酸素供給手段を有し、酸素供給手段による酸素量を制御することで、
 前記飼育水の溶存酸素濃度を低濃度に管理する低酸素期間と、
 前記飼育水の溶存酸素濃度を高濃度に管理する高酸素期間とを有する溶存酸素濃度制御工程を有する前記<4>~<6>のいずれかに記載の水産生物の養殖方法。
 <8> 前記水産生物が、甲殻類である前記<4>~<7>のいずれかに記載の養殖方法。
<4> A method for culturing aquatic products using a culture tank modified by the modification method according to any one of the above <1> to <3>, wherein breeding water is supplied to the modified culture tank. A method for cultivating a marine product having a culturing step for culturing an organism.
<5> The method for cultivating aquatic products according to <4>, further comprising a modifying step of mixing a modifying agent containing humic substances and a silicate compound with the breeding water.
<6> A method for cultivating aquatic products, comprising a reforming step of mixing a modifying agent containing humic substances and a silicate compound into breeding water supplied to the aquaculture tank.
<7> By having an oxygen supply means to the breeding water and controlling the amount of oxygen by the oxygen supply means,
A low oxygen period for controlling the dissolved oxygen concentration of the breeding water to a low concentration,
The method for cultivating aquatic products according to any of the above <4> to <6>, further comprising a dissolved oxygen concentration control step having a high oxygen period in which the dissolved oxygen concentration of the breeding water is controlled to a high concentration.
<8> The culture method according to any one of <4> to <7>, wherein the aquatic product is a crustacean.

 <A1> 水産生物の養殖槽の改質方法であって、養殖槽の底質に国際腐植物質学会(IHSS)の方法に従う疎水性様物質であるフルボ酸を含有する腐植物質およびシリケイト化合物を含む改質剤を混合することで前記底質を改質する混合工程を有し、前記混合工程における前記底質への混合量が、前記腐植物質がフルボ酸相当量として100mg/1000m2以上5,000mg/1000m2以下であり、前記シリケイト化合物が1kg/1000m2以上100kg/1000m2以下である、養殖槽の改質方法。
 <A2> 前記腐植物質が、フルボ酸濃度が、10mg/L~2,500mg/Lのフルボ酸液である前記<A1>記載の養殖槽の改質方法。
 <A3> 前記シリケイト化合物が、酸化アルミニウムを10質量%以上30質量%以下含有するシリケイト化合物である前記<A1>または<A2>記載の養殖槽の改質方法。
 <A4> 水産生物の養殖槽の改質方法であって、養殖槽の底質に国際腐植物質学会(IHSS)の方法に従う疎水性様物質であるフルボ酸を含有する腐植物質を含む改質剤を混合することで前記底質を改質する混合工程を有し、前記混合工程における前記底質への混合量が、前記腐植物質がフルボ酸相当量として100mg/1000m2以上5,000mg/1000m2以下である、養殖槽の改質方法。
 <A5> 前記混合工程のあと、前記改質剤を混合した前記底質を耕耘する耕耘工程を有する前記<A1>~<A4>のいずれかに記載の養殖槽の改質方法。
 <A6> 前記耕耘工程のあと、前記耕耘された前記底質を熟成する熟成工程を有する前記<A5>記載の改質方法。
 <A7> 前記<A1>~<A6>のいずれかの改質方法により改質された養殖槽を用いる水産生物の養殖方法であって、前記改質された養殖槽に飼育水を給水し水産生物を養殖する養殖工程を有する水産生物の養殖方法。
 <A8> 前記飼育水に、フルボ酸を含有する腐植物質およびシリケイト化合物を含む改質剤を混合する改質工程を有する前記<A7>記載の水産生物の養殖方法。
 <A9> 水産生物の養殖槽に給水された飼育水に、国際腐植物質学会(IHSS)の方法に従う疎水性様物質であるフルボ酸濃度が10mg/L~2,500mg/Lのフルボ酸液および酸化アルミニウムを10質量%以上30質量%以下含有するシリケイト化合物を含む改質剤を混合する改質工程を有する水産生物の養殖方法。
 <A10> 前記飼育水への酸素供給手段を有し、酸素供給手段による酸素量を制御することで、前記飼育水の溶存酸素濃度を0.5ppm以上3.5ppm以下の低濃度に連続して2時間以上となるように管理する低酸素期間と、前記飼育水の溶存酸素濃度を4.5ppm以上10.0ppm以下の高濃度に連続して2時間以上となるように管理する高酸素期間とを有し、高酸素期間と低酸素期間とを0.5周期/日~3周期/日の周期で行う溶存酸素濃度制御工程を有する前記<A7>~<A9>のいずれかに記載の水産生物の養殖方法。
 <A11> 前記水産生物が、甲殻類である前記<A7>~<A10>のいずれかに記載の養殖方法。
<A1> A method for modifying a culture tank for aquatic products, wherein the bottom substance of the culture tank contains humic substances and silicate compounds containing fulvic acid, which is a hydrophobic-like substance, according to the method of the International Society for Humic Substances (IHSS). A mixing step of modifying the sediment by mixing a modifying agent, wherein the amount of the sediment mixed with the sediment in the mixing step is 100 mg / 1000 m 2 or more as the humic substance equivalent to 5, 000 mg / 1000 m 2 or less, and the silicate compound is 1 kg / 1000 m 2 or more and 100 kg / 1000 m 2 or less.
<A2> The method according to <A1>, wherein the humic substance is a fulvic acid solution having a fulvic acid concentration of 10 mg / L to 2,500 mg / L.
<A3> The method for modifying a culture tank according to <A1> or <A2>, wherein the silicate compound is a silicate compound containing aluminum oxide in an amount of 10% by mass or more and 30% by mass or less.
<A4> A method for modifying an aquaculture tank for aquatic products, comprising a humic substance containing fulvic acid, which is a hydrophobic-like substance, according to the method of the International Humic Society (IHSS) in the bottom of the aquaculture tank. And the mixing amount of the humic substances in the mixing step is 100 mg / 1000 m 2 or more as fulvic acid equivalent to 5,000 mg / 1000 m. 2 or less, the method of reforming the culture tank.
<A5> The method for reforming an aquaculture tank according to any one of <A1> to <A4>, further comprising a tilling step of tilling the sediment mixed with the modifying agent after the mixing step.
<A6> The reforming method according to <A5>, further including a ripening step of ripening the plowed sediment after the tilling step.
<A7> A method of cultivating aquatic products using a culture tank modified by the modification method of any one of <A1> to <A6>, wherein breeding water is supplied to the modified culture tank. A method for cultivating a marine product having a culturing step for culturing an organism.
<A8> The method for cultivating aquatic products according to <A7>, further including a modifying step of mixing a humic substance containing fulvic acid and a modifier containing a silicate compound with the breeding water.
<A9> A fulvic acid solution having a fulvic acid concentration of 10 mg / L to 2,500 mg / L, which is a hydrophobic-like substance, according to the method of the International Humic Society (IHSS) was added to breeding water supplied to a culture tank for aquatic products. A method for cultivating aquatic products, comprising a modifying step of mixing a modifying agent containing a silicate compound containing 10% by mass or more and 30% by mass or less of aluminum oxide.
<A10> Having an oxygen supply means to the breeding water and controlling the amount of oxygen by the oxygen supply means, the dissolved oxygen concentration of the breeding water is continuously reduced to a low concentration of 0.5 ppm or more and 3.5 ppm or less. A low oxygen period in which the dissolved oxygen concentration is controlled to be 2 hours or more, and a high oxygen period in which the dissolved oxygen concentration of the breeding water is continuously controlled to a high concentration of 4.5 ppm or more and 10.0 ppm or less for 2 hours or more. The marine product according to any one of <A7> to <A9>, further comprising a dissolved oxygen concentration control step of performing a high oxygen period and a low oxygen period at a cycle of 0.5 cycles / day to 3 cycles / day. How to cultivate organisms.
<A11> The aquaculture method according to any one of <A7> to <A10>, wherein the aquatic product is a crustacean.

 本発明によれば、養殖槽の有機物及び窒素成分等を浄化し、改質することができ、改質された養殖槽で、安定した水産生物の養殖を行うことができる。 According to the present invention, it is possible to purify and reform organic substances and nitrogen components in the culture tank, and to stably grow aquatic products in the modified culture tank.

本発明に用いられる養殖槽の第一の実施形態を示す図である。It is a figure showing a first embodiment of a culture tank used for the present invention. 実施例に係る飼育水に用いた河川水の写真である。It is a photograph of river water used for breeding water concerning an example. 実施例の対象とした養殖池の改質前の底質を示す写真である。It is a photograph which shows the sediment before reforming of the culture pond targeted for the Example. 実施例の対象とした養殖池の底質を改質するための熟成状態を示す写真である。It is a photograph which shows the ripening state for improving the sediment of the culture pond targeted for the Example. 実施例の養殖池に水を張った状態を示す写真である。It is a photograph which shows the state where the pond was filled with water. 実施例で養殖したエビの飼育開始から30日時の写真である。It is a photograph 30 days after the breeding start of the shrimp cultivated in the Example. 実施例で養殖したエビの飼育開始から45日時の写真である。It is a photograph of the date and time 45 days after the breeding start of the shrimp cultivated in the Example. 実施例で養殖したエビの飼育開始から63日時の写真である。It is a photograph of 63 days after the breeding start of the shrimp cultivated in the Example. 実施例で養殖したエビの飼育開始から63日時の写真である。It is a photograph of 63 days after the breeding start of the shrimp cultivated in the Example.

 以下に本発明の実施の形態を詳細に説明するが、以下に記載する構成要件の説明は、本発明の実施態様の一例(代表例)であり、本発明はその要旨を変更しない限り、以下の内容に限定されない。なお、本明細書において「~」という表現を用いる場合、その前後の数値を含む表現として用いる。 Hereinafter, embodiments of the present invention will be described in detail. However, the description of the constituent requirements described below is an example (representative example) of an embodiment of the present invention, and the present invention is described below unless the gist is changed. It is not limited to the content of. In this specification, the expression “to” is used to include the numerical values before and after it.

[養殖槽の改質方法]
 本発明の養殖槽の改質方法は、水産生物の養殖槽の改質方法であって、養殖槽の底質に腐植物質を含む改質剤を混合することで前記底質を改質する混合工程を有する。前記改質剤はシリケイト化合物を含むことが好ましい。このようにして、養殖槽の底質に改質剤を混合することで、底質が改善され、養殖槽としての有機物除去機能等が向上する。
[Aquaculture tank reforming method]
The method for modifying a culture tank according to the present invention is a method for modifying a culture tank for aquatic products, and the method for modifying the bottom substance by mixing a modifier containing humic substances into the bottom substance of the culture tank. Having a process. The modifier preferably contains a silicate compound. In this way, by mixing the modifying agent with the bottom material of the culture tank, the bottom material is improved, and the organic substance removing function and the like as the culture tank are improved.

 本発明は、次のような作用機序を想定したものである。まず、自然界の海や湖沼などでは、そこに流れ込む汚水・汚物が浄化され、清澄な自然が保たれているように、自然環境の底質や水等には、浄化機能を持った土壌微生物が常在し棲息している。一方、水産生物の養殖環境では、経済行為として水産生物を高密度に飼育しているものの、自然界の浄化機能が発揮されていない。これは、人工的構造物である養殖槽や飼育水に棲息する土壌微生物が自然界の環境で獲得した代謝機能を放棄することで浄化能力が喪失していることに気づいていないことによると考えられる。本発明者らは、経験則からこのような知見を得ている。 The present invention assumes the following mechanism of action. First, in the oceans and lakes in the natural world, sewage and sewage flowing into these areas are purified, and soil microorganisms with a purifying function are found in the sediment and water of the natural environment, so that clear nature is maintained. Resident and resident. On the other hand, in an aquaculture environment for marine products, although marine products are bred at a high density as an economic act, the purification function of the natural world is not exhibited. This is thought to be due to the fact that soil microorganisms living in artificial structures such as aquaculture tanks and breeding water are not aware that the purification ability has been lost by abandoning the metabolic function acquired in the natural environment. . The present inventors have obtained such knowledge from empirical rules.

 この対策として、土壌微生物が自ら生成する腐植物質を意図的に活用することで、土壌微生物の代謝機能を自然界の代謝機能へと誘導できることを発見した。土壌微生物とは、土壌細菌を主とする微生物群の総称であるが、有機物を対象として機能する代謝機能の微生物群と窒素成分を対象として機能する代謝機能の微生物群などが共棲混在している。例えば、閉鎖性の養殖槽で水産生物を飼育する際に最も問題となるのが、残餌及び排泄物等に含まれる有機物及び窒素成分への対応である。 (4) As a countermeasure, we discovered that the metabolic function of soil microorganisms can be induced to the metabolic function of nature by intentionally utilizing humic substances generated by soil microorganisms. Soil microorganisms are a general term for microorganisms mainly composed of soil bacteria.However, microorganisms with metabolic functions that function on organic substances and microorganisms with metabolic functions that function on nitrogen components coexist. . For example, when raising aquatic products in a closed aquaculture tank, the most problem is how to deal with organic matter and nitrogen components contained in residual foods and excrement.

 本発明はこれらを浄化するものである。まず有機物に対しては、人工的構造物の環境下の土壌微生物のみでは、炭酸ガスと水に分解されない有機物は腐敗してしまう。この対策として、土壌微生物が自ら生成する腐植物質を意図的に活用することにより、自然環境下の土壌微生物代謝機能へと誘導し活性化を図り、腐敗を抑制して腐植化を促進する。また、窒素成分に対しても、人工的構造物の環境下の土壌微生物は自然界の環境で機能させる代謝機能を放棄するように、硝化菌及び脱窒菌も自然界での代謝機能を放棄しており有機態窒素及びアンモニア態窒素も硝化反応が惹起されず、そのままの形で残存するからである。この対策として、養殖増内に棲息する土壌微生物である硝化菌、脱窒菌も土壌微生物が自ら生成する腐植物質を意図的に活用することで自然界の代謝機能へと誘導され活性化する。また、硝化反応を惹起することで有機態窒素及びアンモニア態窒素は、亜硝酸態窒素・硝酸態窒素へと変性し、亜硝酸態窒素・硝酸態窒素は水素供与体と反応して脱窒反応を惹起する。この水素供与体としては、残餌及び排せつ物に含まれる有機物を活用する。このことにより、養殖増内の棲息環境を悪化させる二大要因の有機物及び窒素成分を同時に除去することが可能となるのである。なお、シリケイト化合物も含むことは、フルボ酸鉄が機能することで植物プランクトンや藻類の発生にも有用である。また、光合成反応による過剰な二酸化炭素の消費や、水中での自然な酸素の供与も生じ、植物プランクトンや藻類自体が、水産生物の餌にもなりうる。 The present invention purifies these. First, as for organic matter, organic matter that cannot be decomposed into carbon dioxide and water by only soil microorganisms in an environment of an artificial structure will rot. As a countermeasure, by intentionally utilizing the humic substances generated by the soil microorganisms themselves, the microorganisms are induced to activate the metabolism of soil microorganisms in the natural environment, are activated, suppress rot, and promote humification. Nitrogen bacteria and denitrifying bacteria have also abandoned their metabolic functions in the natural environment, just as soil microorganisms in the environment of man-made structures have abandoned the metabolic functions of nitrogen components. This is because the nitrification reaction does not occur in the organic nitrogen and the ammonia nitrogen, and the nitrogen remains as it is. As a countermeasure, nitrifying bacteria and denitrifying bacteria, which are soil microorganisms inhabiting the aquaculture cultivation, are induced to natural metabolic functions and activated by intentionally utilizing humic substances generated by the soil microorganisms themselves. In addition, by inducing a nitrification reaction, organic nitrogen and ammonia nitrogen are transformed into nitrite nitrogen / nitrate nitrogen, and nitrite nitrogen / nitrate nitrogen reacts with a hydrogen donor to denitrify. Cause. As the hydrogen donor, organic matter contained in the residual food and excrement is utilized. As a result, it is possible to simultaneously remove the organic matter and the nitrogen component, which are the two major factors that worsen the habitat environment in the culture. In addition, including a silicate compound is also useful for generating phytoplankton and algae because iron fulvicate functions. In addition, excessive consumption of carbon dioxide due to the photosynthesis reaction and provision of natural oxygen in water also occur, and phytoplankton and algae themselves can also feed on aquatic products.

[水産生物]
 水産生物は、魚類、水産哺乳類、水産無脊椎動物、海藻類などで、食品もしくは生活に利用されるものである。本発明は養殖される水産生物の養殖環境の改質を行うことができ、その養殖対象となる水産生物は、淡水魚や海水魚、貝類、甲殻類など広く対象とすることができる。養殖手法は、池中養殖や、水田養殖、干潟・河川での養殖などの内水面養殖や、陸上の養殖池や塩田の池中養殖、堤防や網で仕切る区画養殖、垂下式養殖、地撒式養殖などの海面養殖で養殖される各種水産生物を対象とすることができる。養殖される水産生物を例示すると、コイ、ニジマス、アユ、ウグイ、ウナギ、キンギョ、熱帯魚、スッポン、ウシガエル、ドジョウ、ボラ、フナ、クロダイ、スズキ、クルマエビ、ブリ、マダイ、トラフグ、カキ、アコヤガイ、ホヤ、ワカメ、ノリ、アサリ、ハマグリ、ホタテ貝などがあげられる。
[Aquatic products]
The marine product is a fish, a marine mammal, a marine invertebrate, a seaweed, or the like, which is used for food or life. INDUSTRIAL APPLICABILITY The present invention can improve the cultivation environment of cultivated aquatic products, and the aquatic products to be cultivated can be widely targeted such as freshwater fish, saltwater fish, shellfish, and crustaceans. Aquaculture techniques include pond aquaculture, paddy aquaculture, inland water aquaculture such as aquaculture in tidal flats and rivers, onshore aquaculture ponds and salt ponds aquaculture, compartmental aquaculture divided by dikes and nets, hanging aquaculture, and geodistribution. Various aquatic products cultivated in marine aquaculture such as aquaculture can be targeted. Examples of cultured aquatic products include carp, rainbow trout, sweetfish, dace, eel, goldfish, tropical fish, turtle, bullfrog, loach, mullet, crucian carp, sea bream, prawn, yellowtail, red sea bream, tiger puffer, oyster, oyster, sea squirt , Seaweed, seaweed, clams, clams, scallops and the like.

[養殖槽]
 本発明は、養殖槽を改質するものである。養殖槽は、比較的狭い水域で水産生物を人工的に繁殖飼育するときに用いる場をいう。例えば、養殖池や水田、区画された干潟・河川・海、陸上設備などである。
[Aquaculture tank]
The present invention is for modifying a culture tank. The aquaculture tank is a place used when artificially breeding and rearing aquatic products in a relatively narrow water area. For example, aquaculture ponds and paddy fields, partitioned tidal flats, rivers, seas, and onshore facilities.

[底質]
 本発明の養殖槽の改質方法は、特に、改質の効果を定着させるために、底質を有する養殖槽を対象とする。底質とは、養殖槽の主に底に設けられる土や砂、砂利、石、砂泥等をいう。これらの底質は、水産生物の飼育のための食物連鎖等に寄与し、水産生物の餌となる植物プランクトン等の増殖等に寄与していたり、水産生物の残餌や死骸の浄化等に寄与する。このため、各種養殖手法にあたって養殖槽の底等に底質が設けられている。
[Sediment]
The method for modifying a culture tank of the present invention is particularly directed to a culture tank having bottom sediment in order to fix the effect of the modification. The term “sediment” refers to soil, sand, gravel, stone, sand mud, and the like provided mainly on the bottom of the culture tank. These sediments contribute to the food chain for breeding aquatic products, contribute to the growth of phytoplankton, etc., which feed on aquatic products, and contribute to the purification of residual food and dead bodies of aquatic products. I do. For this reason, sediment is provided at the bottom of the culture tank or the like in various culture techniques.

[混合工程]
 本発明の改質方法は、養殖槽の底質に腐植物質を含む改質剤を混合することで底質を改質する混合工程を有する。前記改質剤はシリケイト化合物を含むものとしてもよい。この混合は、底質に改質剤を散布したり、撹拌や耕耘して混ぜたりして、底質に改質剤が分散して接した状態である。
 本発明では、混合工程により、底質を改質する。この改質は、特に、底質に蓄積した有機物等の浄化及び腐植化促進や、その浄化も合わせて、養殖槽の環境を水産生物の養殖に適したものとするものである。
[Mixing process]
The reforming method of the present invention has a mixing step of modifying the bottom by mixing a modifier containing humic substances into the bottom of the culture tank. The modifier may include a silicate compound. This mixing is a state in which the modifying agent is dispersed on the sediment, mixed with stirring or plowing to disperse and contact the sediment.
In the present invention, the sediment is reformed by the mixing step. This reforming, in particular, purifies the organic matter and the like accumulated in the sediment, promotes humification, and purifies the humus, making the environment of the aquaculture tank suitable for aquaculture of aquatic products.

 特に、腐植物質由来のフルボ酸と、シリケイト化合物由来の鉄(鉄イオン)が底質に供給された状態となる。これにより底質から、養殖槽にフルボ酸鉄が生成し供給される。フルボ酸鉄が生成し供給されることでラン藻類や珪藻類などの藻類や植物プランクトン等も増殖しやすくなり、養殖槽内で水産生物の餌となる植物プランクトン等が供給されやすい状態となる。一般的にシリケイト化合物に含まれる鉄分は、海水中で酸化されて粒状の鉄となり底質に沈殿するが、フルボ酸と接触することでフルボ酸の持つ抗酸化力により三価鉄から二価鉄へ還元され、二価鉄はフルボ酸と結合してコロイド状のフルボ酸鉄となり、植物プランクトンなどに利用される。また、これらの植物プランクトン等は、光合成にも寄与し養殖槽内に酸素供給する効果も生じる。 Particularly, fulvic acid derived from humic substances and iron (iron ions) derived from silicate compounds are supplied to the sediment. Thus, iron fulvicate is produced and supplied from the sediment to the culture tank. By generating and supplying iron fulvic acid, algae such as cyanobacteria and diatoms, phytoplankton, and the like also easily proliferate, and phytoplankton and the like, which are food for aquatic products, are easily supplied in the culture tank. In general, iron contained in silicate compounds is oxidized in seawater to become granular iron and precipitates on sediment, but when it comes into contact with fulvic acid, the antioxidant power of fulvic acid changes it from ferrous iron to ferrous iron. Ferrous iron is reduced to fulvic acid to form colloidal iron fulvic acid, which is used for phytoplankton and the like. These phytoplanktons also contribute to photosynthesis and have the effect of supplying oxygen into the culture tank.

 また、混合工程により腐植物質を供給することで、養殖槽内に常在している硝化菌、脱窒菌を活性化する。一般的な養殖において、特に嫌気的条件を必要とする脱窒菌は養殖槽で水産生物を生育するための酸素供給等によって自然環境下の代謝機能を放棄し、その機能性を喪失している。この脱窒菌の活性が低下していることを従来の養殖では見落として養殖効率が低下したり、脱窒のために追加の装置等を設けるものの運転管理が複雑化したりしている。本発明では、このような脱窒菌について、養殖槽等にそもそも常在していたものを腐植物質により活性化し、脱窒菌等が活発に作用しやすい状態とする。 腐 Furthermore, humic substances are supplied in the mixing step, thereby activating nitrifying bacteria and denitrifying bacteria resident in the culture tank. In general aquaculture, denitrifying bacteria, which particularly require anaerobic conditions, have abandoned their metabolic functions under the natural environment due to oxygen supply for growing aquatic products in the aquaculture tank, and have lost their functions. In the conventional aquaculture, the decrease in the activity of the denitrifying bacterium is overlooked in the conventional aquaculture, and the aquaculture efficiency is reduced, and the operation management is complicated though an additional device is provided for the denitrification. In the present invention, such a denitrifying bacterium, which originally existed in a culture tank or the like, is activated by humic substances so that the denitrifying bacterium or the like readily acts.

[改質剤]
 改質剤は、腐植物質を含むものを用いる。前記改質剤はシリケイト化合物を含むものとしてもよい。この改質剤は、さらに、適宜、pH調整材や粘度調整材、塩分濃度を調整する塩等を含むものでもよい。
[Modifier]
As the modifier, one containing humic substances is used. The modifier may include a silicate compound. The modifier may further include a pH adjuster, a viscosity adjuster, a salt for adjusting a salt concentration, and the like, as appropriate.

[腐植物質]
 腐植物質は、生物の死後、生物体有機物が微生物的・化学的作用を受けて崩壊した「化学構造が特定されない有機物(非生体有機物)」の総称と言われている。この腐植物質についても、機能性を示すものと、機能性を示さないものとがあることが経験的に知られており、これは、その自然界の有機物である生物体有機物が、土へ還ろうとするときの中間生成物が含まれるか否かの影響が大きいものと考えられる。この中間生成物を含むとき、すなわち機能性を示す腐植物質については、腐植前駆物質と呼ばれることがある。(内水護「自然と輪廻 土・自然・人間・社会ベーシック文明論」18-28頁,漫画社,1986)
 ここで腐植前駆物質や腐植物質(腐植物)には、その成分の腐植化度合(重縮合反応化度合)として、ヒュミンやフルボ酸、フミン酸等が含まれていることが知られている。そして、一般的な腐植物質において、フルボ酸とフミン酸との比率は2:8程度の重量比で含まれている。本発明の腐植物質はフルボ酸を含むものを用いる。
[Humic substances]
Humic substances are said to be a generic term for "organic substances whose chemical structures are not specified (non-living organic substances)" in which biological organisms are destroyed by microbial or chemical action after the death of the organism. It has been empirically known that some humic substances show functionality and others do not.This is because the organic matter, which is an organic substance in the natural world, tries to return to the soil. It is considered that the influence of whether or not an intermediate product is contained is large. Humid substances containing this intermediate product, that is, functional humic substances, are sometimes referred to as humic precursors. (Uchimizu, "Basic Civilization of Nature, Nature, Humans, and Society", pages 18-28, Manga-Sha, 1986)
It is known that humin, fulvic acid, humic acid, and the like are contained in the humic precursor or humic substance (humus) as the humification degree (polycondensation reaction degree) of the component. In general humic substances, the weight ratio of fulvic acid to humic acid is about 2: 8. The humic substances of the present invention contain fulvic acid.

 フルボ酸自体は、フェノール及び/又はフェノール露出基のある化合物を含む代謝産物を、有機物等と反応させることで生じる腐植物質(特に腐植前駆物質)の内、酸およびアルカリへの溶解性からフミン酸と区別されるものの、様々な構造を有する有機物等の混合物である。 Fulvic acid itself is humic acid because of its solubility in acids and alkalis among humic substances (particularly humic precursors) produced by reacting metabolites containing phenol and / or compounds having a phenol-exposed group with organic substances and the like. , But a mixture of organic substances having various structures.

[フルボ酸液]
 本発明にはフルボ酸液を用いることが好ましい。フルボ酸液は、一般的な腐植よりもフルボ酸が高比率で含有されており、フミン酸等の含有量が低いものである。フルボ酸液を用いることで、フルボ酸鉄生成がより効率的に行われる。このようなフルボ酸液としては、例えば、株式会社T&Gのリードアップなどを用いることができる。
[Fulvic acid solution]
In the present invention, it is preferable to use a fulvic acid solution. The fulvic acid solution contains fulvic acid at a higher ratio than general humus, and has a lower content of humic acid and the like. By using the fulvic acid solution, fulvic acid iron is generated more efficiently. As such a fulvic acid solution, for example, a lead-up by T & G Corporation can be used.

[フルボ酸およびフミン酸]
 なお、本願におけるフルボ酸およびフミン酸は、日本腐植物質学会の属する国際腐植物質学会の分類に基づき、生物体有機物が微生物的・化学的作用を受けて崩壊して生じる化学構造が特定されていない有機物(非生体有機物)である腐植物のうち、アルカリ・酸に対する溶解性での分類を行う。すなわち、フルボ酸は、アルカリに可溶であり、かつ、酸に可溶な成分である。一方、フミン酸は、アルカリに可溶であるが、酸に不溶な成分である。なお、ヒュミンは、アルカリに不溶であり、かつ、酸に不溶な成分である。
[Fulvic acid and humic acid]
In addition, fulvic acid and humic acid in the present application are based on the classification of the International Society of Humic Substances to which the Japanese Society of Humic Substances belongs, and the chemical structure of biological organisms that are disrupted by microbial and chemical actions has not been identified. Among humic substances that are organic substances (non-organic organic substances), classification is based on solubility in alkalis and acids. That is, fulvic acid is a component that is soluble in alkali and soluble in acid. On the other hand, humic acid is a component that is soluble in alkali but insoluble in acid. Humin is a component that is insoluble in alkali and insoluble in acid.

[フルボ酸濃度・活性の測定例]
 フルボ酸液等に含まれているフルボ酸の程度は、フルボ酸が混合物質であり、かつ他の有機物の有無の影響も大きいため具体的な成分ごとの濃度で規定することが適切ではなく、具体的な数値では規定できない場合がある。
[Example of measuring fulvic acid concentration and activity]
The degree of fulvic acid contained in the fulvic acid solution, etc., is not appropriate to be specified by the concentration of each specific component because fulvic acid is a mixed substance, and the influence of other organic substances is large, There are cases where it cannot be specified with specific numerical values.

 フルボ酸抽出液より、国際腐植物質学会(IHSS)の方法に従い疎水性様物質を分離・精製し、この物質が日本腐植物質学会(JHSS)より頒布されている標準フルボ酸と類似した物理化学的特性(吸収、FTIR、3D蛍光スペクトル、固体NMR等)をもつことが確認されている。 A hydrophobic-like substance is separated and purified from the fulvic acid extract in accordance with the method of the International Society of Humic Substances (IHSS), and this substance is physically and chemically similar to the standard fulvic acid distributed by the Japan Humic Society (JHSS). It has been confirmed that it has characteristics (absorption, FTIR, 3D fluorescence spectrum, solid-state NMR, etc.).

 このフルボ酸の濃度は、そのフルボ酸活性の程度に関する、3D蛍光スペクトルを指標とすることができる。この3D蛍光スペクトルはUV~可視光範囲程度の光を用いて、励起光-蛍光の波長と、その強度の分布に基づいて判断する。この分布の傾向がフルボ酸のものかを確認し、その特徴的なピークが310nm-410nm(励起光波長-蛍光波長)付近にみられればフルボ酸活性が高い(フルボ酸濃度が高い)ものと判断される。 濃度 The concentration of the fulvic acid can be determined by using a 3D fluorescence spectrum as an index for the degree of the fulvic acid activity. The 3D fluorescence spectrum is determined based on the wavelength of the excitation light-fluorescence and the distribution of the intensity thereof using light in the range from UV to visible light. It is confirmed whether the tendency of the distribution is that of fulvic acid, and if a characteristic peak is observed near 310 nm to 410 nm (excitation light wavelength-fluorescence wavelength), it is determined that the fulvic acid activity is high (the fulvic acid concentration is high). Is determined.

 そして、そのフルボ酸濃度は、簡易的には、410nm付近のピークにおける蛍光波長に基づく検量線を作成し、推定濃度として算出することができる。この推定濃度として、フルボ酸液は、原料となる有機物質や製造条件にもよるが、およそ10mg/L~2,500mg/Lとなる。フルボ酸濃度が、20mg/L以上や、30mg/L以上、100mg/L以上、500mg/L以上のフルボ酸液を用いることが好ましい。これらを原液として、適宜希釈しながら用いることができる。例えば、現在販売されているフルボ液(商品名「リードアップ」(株式会社T&G))のフルボ酸含有量は約1000ppmと評価されている。 Then, the fulvic acid concentration can be simply calculated as an estimated concentration by creating a calibration curve based on the fluorescence wavelength at the peak near 410 nm. The estimated concentration of the fulvic acid solution is about 10 mg / L to 2,500 mg / L, depending on the organic substance used as a raw material and the production conditions. It is preferable to use a fulvic acid solution having a fulvic acid concentration of 20 mg / L or more, 30 mg / L or more, 100 mg / L or more, and 500 mg / L or more. These can be used as stock solutions with appropriate dilution. For example, the fulvic acid content of a currently sold fulvic solution (trade name “Lead Up” (T & G)) is estimated to be about 1000 ppm.

 また、そのフルボ酸活性は、簡易的には3D蛍光スペクトルのピークとなる波長での蛍光強度と、その励起光波長の吸光度との比として、410nm付近の蛍光強度ピーク値/310nm付近の励起光強度ピーク値(蛍光波長の蛍光強度(If)/励起光波長の吸光度(Abs))から、「フルボ酸-蛍光スペクトル比」として求めることができる。例えば、フルボ酸液の場合、このフルボ酸-蛍光スペクトル比が、5,000~30,000程度の値を示す。本発明においては、フルボ酸が十分に供給されればよいため、フルボ酸活性は任意でよいが、フルボ酸活性が高いほど少量の腐植物質の混合で改質効果等を得ることや、短時間で効果を得たり、長時間効果を得たり、有機物浄化機能が優れたりといった改質効果等が期待できる。このため、混合工程に用いる腐植物質のフルボ酸-蛍光スペクトル比は、100以上や、500以上、1000以上、2000以上、3000以上、5000以上、8000以上のように下限を設けてもよい。一方、上限は特に定めはないが、例えば、100000以下や、80000以下、50000以下、30000以下のような上限を設けてもよい。 In addition, the fulvic acid activity is simply expressed as a ratio of the fluorescence intensity at the wavelength that becomes the peak of the 3D fluorescence spectrum to the absorbance at the wavelength of the excitation light, the fluorescence intensity peak value around 410 nm / the excitation light around 310 nm. From the intensity peak value (fluorescence intensity (If) at the fluorescence wavelength / absorbance (Abs) at the excitation light wavelength), it can be determined as “fulvic acid-fluorescence spectrum ratio”. For example, in the case of a fulvic acid solution, the fulvic acid-fluorescence spectrum ratio shows a value of about 5,000 to 30,000. In the present invention, the fulvic acid activity may be arbitrarily determined, as long as fulvic acid is sufficiently supplied. It is possible to expect a reforming effect such as an effect obtained by the above, an effect obtained for a long time, and an excellent organic substance purifying function. For this reason, the fulvic acid-fluorescence spectrum ratio of the humic substances used in the mixing step may have a lower limit such as 100 or more, 500 or more, 1000 or more, 2000 or more, 3000 or more, 5000 or more, and 8000 or more. On the other hand, there is no particular upper limit, but for example, an upper limit of 100,000 or less, 80000 or less, 50000 or less, or 30000 or less may be provided.

 なお、一般的な汚水等の有機性物質含有液の腐植化が進まない段階では、このフルボ酸-蛍光スペクトル比は、ほとんど0に近い値である。なお、この比は濃度を示す値ではなくフルボ酸の質や活性の指標であり、有機性物質との接触による反応等で大きく増減する。 で は At a stage where humification of a liquid containing an organic substance such as general sewage does not proceed, the fulvic acid-fluorescence spectrum ratio is almost a value close to zero. Note that this ratio is not a value indicating the concentration but an index of the quality or activity of fulvic acid, and greatly increases or decreases due to a reaction caused by contact with an organic substance.

 一方、フミン酸の含有については、フミン酸を特定する精製や分析を行ってその濃度を基に判断することができる。この判断を簡易的に行う場合、前述したフルボ酸の測定を行うときの、3D蛍光スペクトルによって、UV~可視光範囲程度の光を用いて、励起光-蛍光の波長と、その強度の分布に基づいて判断することができる。フミン酸が存在する場合、450nm/530nm(励起光/蛍光)付近に、ピークがみられる。また、液の黒色度が高くなり、前述したフルボ酸-蛍光スペクトル比において、310nm付近の励起光波長の吸光度(Abs)が高くなったり、410nm付近の蛍光波長の蛍光強度(If)が低くなったりして、フルボ酸-蛍光スペクトル比が、フルボ酸液として好ましい範囲となりにくい。よって、本発明のフルボ酸液は、通常の腐植物質である、フルボ酸:フミン酸が2:8相当の腐植物質溶液と同様のダブルピークがみられない、またはフミン酸に相当するピークがこの一般的なダブルピークの値より低いことを指標とすることができる。または、フルボ酸-蛍光スペクトル比を指標としてもよい。なお、本発明に用いるフルボ酸やフルボ酸液については、特許第6026631号公報に開示の技術も参照して、利用することができる。 On the other hand, the content of humic acid can be determined based on the concentration of humic acid by performing purification or analysis for specifying humic acid. When this determination is simply performed, the wavelength of the excitation light-fluorescence and the distribution of the intensity thereof are determined by using the light in the range from UV to visible light using the 3D fluorescence spectrum when performing the above-described measurement of fulvic acid. It can be determined based on this. When humic acid is present, a peak is observed around 450 nm / 530 nm (excitation light / fluorescence). Further, the blackness of the solution increases, and in the above-mentioned fulvic acid-fluorescence spectrum ratio, the absorbance (Abs) of the excitation light wavelength around 310 nm increases, and the fluorescence intensity (If) of the fluorescence wavelength around 410 nm decreases. In some cases, the fulvic acid-fluorescence spectrum ratio is hardly in a preferable range for a fulvic acid solution. Therefore, the fulvic acid solution of the present invention does not show a double peak similar to that of a humic acid solution of fulvic acid: humic acid equivalent to 2: 8, which is a normal humic substance, or has a peak corresponding to humic acid. An index lower than a general double peak value can be used as an index. Alternatively, the fulvic acid-fluorescence spectrum ratio may be used as an index. The fulvic acid and fulvic acid solution used in the present invention can be used with reference to the technology disclosed in Japanese Patent No. 6026631.

[シリケイト化合物]
 本発明は、シリケイト化合物を、底質の改質のために混合したり、養殖槽の飼育水に供給したりして用いることができる。本発明に用いるシリケイト化合物とは、珪藻土など由来の活性珪酸に、アルミニウムや鉄を含んだものをいう。例えば、安山岩質もしくは流紋岩質の岩石に由来したものを好適に用いることができる。また、人工物である活性硅酸に鉄、アルミニウムなどの金属を天然物に含まれているものと同等以上の割合となるように混合したものを用いることもできる。
[Silicate compound]
INDUSTRIAL APPLICABILITY The present invention can be used by mixing a silicate compound for modifying bottom sediment or supplying the silicate compound to breeding water in a culture tank. The silicate compound used in the present invention refers to a compound in which activated silicic acid derived from diatomaceous earth or the like contains aluminum or iron. For example, those derived from andesitic or rhyolite rocks can be suitably used. In addition, a mixture of active silicic acid, which is an artificial product, and a metal such as iron or aluminum in a ratio equal to or higher than that of a natural product may be used.

 このシリケイト化合物に含まれるアルミニウム量は、酸化アルミニウム(Al23)として、5質量%以上が好ましい。酸化アルミニウム量として、10質量%以上がより好ましく、11質量%以上、12質量%以上としてもよい。酸化アルミニウム量として、十分に活性珪酸や鉄を含む範囲で上限を定めなくてもよいが、30質量%以下や、25質量%以下、20質量%以下としてもよい。
 このシリケイト化合物に含まれる鉄量は、酸化鉄(酸化第一鉄および酸化第二鉄の総量)として、3質量%以上が好ましい。酸化鉄量として、4質量%以上がより好ましく、4.5質量%以上、5.0質量%以上としてもよい。酸化鉄量として、十分に活性珪酸や酸化アルミニウムも含む範囲で上限を定めなくてもよいが、30質量%以下や、25質量%以下、20質量%以下、15質量%以下としてもよい。
The amount of aluminum contained in the silicate compound is preferably at least 5% by mass as aluminum oxide (Al 2 O 3 ). The amount of aluminum oxide is more preferably 10% by mass or more, and may be 11% by mass or more and 12% by mass or more. The upper limit of the amount of aluminum oxide may not be limited within a range that sufficiently contains activated silicic acid and iron, but may be 30% by mass or less, 25% by mass or less, or 20% by mass or less.
The amount of iron contained in the silicate compound is preferably 3% by mass or more as iron oxide (total amount of ferrous oxide and ferric oxide). The amount of iron oxide is more preferably 4% by mass or more, and may be 4.5% by mass or more and 5.0% by mass or more. The upper limit of the amount of iron oxide may not be limited within a range that sufficiently includes active silicic acid and aluminum oxide, but may be 30% by mass or less, 25% by mass or less, 20% by mass or less, or 15% by mass or less.

 シリケイト化合物は、鉄や、アルミニウム等のミネラル成分となる成分も含んでいることで、シリケイト化合物は、養殖槽内の底質や飼育水等に棲息する土壌細菌を中心とする土壌微生物の生育環境安定剤として有効である。また、養殖槽の底質や飼育水等に含まれる有機物の腐植化を促進する触媒としても機能する。また、養殖槽の底質や飼育水等に棲息する植物プランクトンや藻類などの光合成生物の栄養塩としても有効である。また、これらに寄与する状態のフルボ酸鉄を生成する原料としても有用である。さらに、シリケイト化合物として、アルミニウムや鉄を含むことで、珪藻土のケイ酸塩にこれらのアルミニウムや鉄が担持され安定化しやすくなると考えられる。また、同時に、このようなシリケイト化合物は腐植物質で活性化された脱窒菌等の養殖槽の浄化に寄与する菌を担持する場としても有用と考えられる。 The silicate compound also contains components that become mineral components such as iron and aluminum, and the silicate compound is a growth environment for soil microorganisms, mainly soil bacteria that inhabit the sediment and breeding water in the culture tank. It is effective as a stabilizer. In addition, it functions as a catalyst for promoting humification of organic matter contained in the bottom material of the aquaculture tank and breeding water. It is also effective as a nutrient for photosynthetic organisms such as phytoplankton and algae that inhabit the bottom of culture tanks and breeding water. It is also useful as a raw material for producing iron fulvicate in a state contributing to these. Further, it is considered that when aluminum or iron is contained as the silicate compound, these aluminum or iron are supported on the silicate of diatomaceous earth and are easily stabilized. At the same time, it is considered that such a silicate compound is also useful as a place for carrying bacteria contributing to purification of a culture tank such as denitrifying bacteria activated with humic substances.

[混合量]
 これらの改質物質は、養殖槽の底質を改質することができる範囲で、養殖槽の種類、水産生物の飼育期間、養殖槽の使用条件等を鑑み、適宜その混合量を設定することができる。混合量は、底質が配置される養殖槽の底面の広さを基準として設定することができる。これらの好適範囲とすることでより脱窒菌等の活性化や植物プランクトンの生育等の改質効果を奏することができる。
[Mixing amount]
The amount of these modified substances should be set as appropriate in consideration of the type of the culture tank, the breeding period of the aquatic products, the conditions of use of the culture tank, etc., as long as the bottom material of the culture tank can be modified. Can be. The mixing amount can be set based on the size of the bottom surface of the culture tank in which the sediment is disposed. By setting the content in these preferable ranges, it is possible to exert effects of activating denitrifying bacteria and the like and improving effects such as growth of phytoplankton.

 腐植物質の混合量は、腐植物質に含まれるフルボ酸相当量として、50mg/1000m2以上とすることが好ましい。例えば、フルボ酸相当量として50mg/L含むフルボ酸液を原液として用いる場合、1L(フルボ酸相当量50mg分)を、適宜、水等で希釈し、1000m2に散布することで腐植物質を混合することができる。腐植物質の混合量はフルボ酸相当量として、80mg/1000m2以上や、100mg/1000m2以上や、150mg/1000m2以上とより高濃度にすることがより好ましい。腐植物質を高濃度とする弊害はないため上限を定めなくてもよいが、原料の量の制限や、散布時間等を考慮して上限を定めてもよく、10,000mg/1000m2以下や、5,000mg/1000m2以下としてもよい。 The mixing amount of the humic substance is preferably 50 mg / 1000 m 2 or more as the fulvic acid equivalent contained in the humic substance. For example, when a fulvic acid solution containing 50 mg / L as a fulvic acid equivalent is used as a stock solution, 1 L (50 mg fulvic acid equivalent) is appropriately diluted with water or the like and sprayed to 1000 m 2 to mix humic substances. can do. Mixing amount of humic substances as fulvic acid equivalent weight, 80 mg / 1000 m 2 or more and, 100 mg / 1000 m 2 or more and, more preferably to higher concentrations and 150 mg / 1000 m 2 or more. An upper limit may not be set because there is no adverse effect of increasing the concentration of humic substances. However, an upper limit may be set in consideration of the amount of raw materials, the application time, etc., and 10,000 mg / 1000 m 2 or less, It may be 5,000 mg / 1000 m 2 or less.

 シリケイト化合物の混合量は、1kg/1000m2以上とすることが好ましい。シリケイト化合物の混合量は、3kg/1000m2以上や、5kg/1000m2以上や、10kg/1000m2以上とより高濃度にすることがより好ましい。シリケイト化合物を高濃度とする弊害はないため上限を定めなくてもよいが、原料の量の制限や、散布時間等を考慮して上限を定めてもよく、100kg/1000m2以下や、50kg/1000m2以下としてもよい。 The mixing amount of the silicate compound is preferably 1 kg / 1000 m 2 or more. The mixing amount of the silicate compound is more preferably set to a higher concentration of 3 kg / 1000 m 2 or more, 5 kg / 1000 m 2 or more, or 10 kg / 1000 m 2 or more. Since there is no adverse effect of increasing the concentration of the silicate compound, there is no need to set the upper limit. However, the upper limit may be set in consideration of the limitation of the amount of the raw material, the spraying time, etc., and 100 kg / 1000 m 2 or less, 50 kg / It may be 1000 m 2 or less.

 本発明の改質方法は、底質を改質するため、養殖槽の飼育水の張り替えの時に行うことが好ましい。養殖槽の飼育水は、水産生物が十分に成育し、その槽内の水産生物が回収・出荷されたあと、使用した飼育水を排出して、新しい飼育水に入れ替えられる。特に人工的な調整が行いやすい、養殖池や水田、陸上設備などは、切り替え時に飼育水をほぼ全量排出する。この飼育水が排出された状態の養殖槽の底質に、改質剤を散布し、混合することが好ましい。飼育水が排出されていることで、底質に直接混合される改質剤の濃度が向上し優れた改質効果を得やすい。なお、飼育水が排出された状態でも底質は湿潤状態であったり、極めて浅い水位を有する場合がある。この底質は、適宜、天日干しや、後述する耕耘等が行われる場合がある。 改 質 The reforming method of the present invention is preferably performed at the time of refilling the breeding water in the aquaculture tank in order to reform the sediment. The breeding water in the aquaculture tank is such that after the aquatic products have sufficiently grown and the aquatic products in the tank have been collected and shipped, the used breeding water is discharged and replaced with new breeding water. Aquaculture ponds, paddy fields, shore facilities, etc., which are particularly easy to make artificial adjustments, discharge almost all breeding water when switching. It is preferable to spray and mix the modifier on the sediment of the culture tank from which the breeding water has been discharged. Since the breeding water is discharged, the concentration of the modifier directly mixed with the sediment is improved, and an excellent reforming effect is easily obtained. Even when the breeding water is discharged, the sediment may be in a wet state or may have an extremely shallow water level. The bottom sediment may be appropriately sun-dried or plowed as described below.

[耕耘工程]
 本発明の改質方法は、混合工程のあと、改質剤を混合した底質を耕耘する耕耘工程を有するものであることが好ましい。この耕耘工程を行うことで、改質剤が底質により均質に混合される。この耕耘は、養殖槽の底質を掘り返して軟らかく膨らませるものである。この耕耘は、飼育水が張られた状態の底質で行っても良いし、飼育水が排出された状態の底質で行っても良い。耕耘作業時の水の抵抗や重さの影響を低減し、より深い範囲まで効率よく耕耘できるように飼育水が排出された状態で行うことが好ましい。耕耘することで、底質の内部まで酸素供給して、堆積した有機物等をより効率よく浄化したり、改質剤に含まれるフルボ酸鉄などがより広範に維持された状態としたりすることができる。
[Tilling process]
The reforming method of the present invention preferably includes a tilling step of tilling the sediment mixed with the modifying agent after the mixing step. By performing this tilling process, the modifier is more uniformly mixed with the sediment. This tilling digs the bottom of the culture tank and swells it softly. This tilling may be performed on the sediment in a state where the breeding water is stretched, or may be performed on the sediment in a state where the breeding water is discharged. It is preferable to perform the cultivation in a state where the breeding water is discharged so as to reduce the influence of water resistance and weight at the time of tilling work and to efficiently cultivate a deeper range. By cultivating, it is possible to supply oxygen to the inside of the bottom sediment to more efficiently purify the deposited organic matter, etc., and to maintain the state where iron fluvic acid etc. contained in the modifier is maintained more widely. it can.

[熟成工程]
 本発明の改質方法は、耕耘工程のあと、前記耕耘された前記底質を排水状態で熟成する熟成工程を有することが好ましい。熟成とは、養殖対象となる水産生物を投入せずに静置や、適宜、撹拌等するものである。この熟成工程を底質にする場合、飼育水の影響による熟成時間の長時間化を防止するために、湿潤状態の底質で行ってもよいが、養殖槽として使用するときに相当するような満水状態とせずに行うことが好ましい。熟成は、底質の天日消毒で解決できない問題点の解決を目的として、例えば残存有機物の腐植化反応による腐敗防止、腐敗菌等の雑菌類の抑制を行うものである。なお、後述する養殖方法において、飼育水を熟成する場合もこの底質の熟成に準じるものとすることができる。
[Aging process]
It is preferable that the reforming method of the present invention has a ripening step of ripening the tilled sediment in a drainage state after the tilling step. The ripening is to allow the marine products to be cultured to stand without being charged, or to stir appropriately. When the aging step is performed as bottom sediment, in order to prevent the ripening time from being lengthened by the influence of the breeding water, the aging step may be performed using wet bottom sediment. It is preferable to carry out the process without being filled with water. Aging is for the purpose of solving problems that cannot be solved by solar disinfection of sediment, for example, to prevent decay due to a humification reaction of residual organic substances and to control various bacteria such as spoilage bacteria. In the aquaculture method described below, when the breeding water is aged, it can be made to conform to the aging of the sediment.

 この熟成工程は、養殖槽の状態等に応じて、適宜その時間を定めて行うことができる。例えば、6時間以上行うことが好ましい。熟成時間は、10時間以上や、20時間以上、40時間以上、60時間以上行ってもよい。熟成を長時間行う弊害は特にないが、腐植物質やシリケイト化合物を混合した機能が低下する場合があるため、60日以内や、45日以内、30日以内、20日以内、10以内のような熟成時間の上限を定めてもよい。 熟 This aging step can be performed by appropriately setting the time according to the state of the culture tank and the like. For example, it is preferably performed for 6 hours or more. The aging time may be 10 hours or longer, 20 hours or longer, 40 hours or longer, 60 hours or longer. There is no adverse effect of performing aging for a long time, but since the function of mixing humic substances and silicate compounds may be reduced, such as within 60 days, within 45 days, within 30 days, within 20 days, within 10 days An upper limit of the aging time may be set.

[本発明の養殖方法]
 本発明の養殖方法は、本発明の改質方法により改質された養殖槽に飼育水を給水し養殖する養殖工程を有する。
 改質された養殖槽を用いることで、養殖槽の底質の機物等を十分に浄化した状態のため、汚染が生じにくく、底質中の有機物の浄化等による溶存酸素濃度の大幅な変動を抑制することができる。また、養殖槽の底質からフルボ酸や鉄等を供給することで、藻類などの植物プランクトンも繁殖し、養殖槽において養殖される水産生物の残餌や排泄物等の浄化等にも寄与するため、水産生物の養殖効率が向上する。例えば、水産生物の生残率が向上したり、従来以上の高密度飼育を可能としたり、生育期間を短縮したり、水産生物の雑味などが抑制された嗜好性に優れた水産生物を得ることができる。
[Aquaculture method of the present invention]
The culture method of the present invention includes a culture step of supplying breeding water to a culture tank modified by the modification method of the present invention and culturing.
By using the modified culture tank, the equipment in the bottom of the culture tank has been sufficiently purified, so contamination is unlikely to occur, and the fluctuation of dissolved oxygen concentration due to the purification of organic matter in the bottom, etc. Can be suppressed. In addition, by supplying fulvic acid, iron, and the like from the bottom of the culture tank, phytoplankton such as algae also breed, and contribute to purification of residual food and excrement of aquatic products cultured in the culture tank. Therefore, aquaculture efficiency of aquatic products is improved. For example, the survival rate of aquatic products is improved, higher-density breeding than before is possible, the growing period is shortened, and the aquatic products with excellent palatability in which the astringency of the aquatic products is suppressed are obtained. be able to.

[養殖]
 養殖手法は、池中養殖や、水田養殖、干潟・河川での養殖などの内水面養殖や、陸上の養殖池や塩田の池中養殖、堤防や網で仕切る区画養殖、垂下式養殖、地撒式養殖などの海面養殖のように、各種水産生物を養殖する養殖手法とすることができる。養殖池や水田、陸上設備などは、切り替え時に飼育水をほぼ全量排出する養殖手法を対象とすることが好ましい。
[Aquaculture]
Aquaculture techniques include pond aquaculture, paddy aquaculture, inland water aquaculture such as aquaculture in tidal flats and rivers, onshore aquaculture ponds and salt ponds aquaculture, compartmental aquaculture divided by dikes and nets, hanging aquaculture, and geodistribution. As in the case of sea surface culture such as in aquaculture, a culture method for culturing various aquatic products can be employed. For aquaculture ponds, paddy fields, land facilities, and the like, it is preferable to target aquaculture techniques that discharge almost all breeding water when switching.

[飼育水]
 飼育水は、養殖対象となる水産生物の飼育に適した海水や淡水、また適宜塩分調整された水である。飼育水は、養殖槽に、養殖の段階に応じた容量となるように供給される。一部前述したように、本発明の改質方法は、底質を改質するため、飼育水を排出した状態で実施することが好ましく、これらの飼育水が排出された状態で改質等を終えたのち、使用時には、飼育水が給水された状態で養殖を行う。
[Breeding water]
The breeding water is seawater or freshwater suitable for breeding aquatic products to be cultured, or water whose salt content is appropriately adjusted. The breeding water is supplied to the culture tank so as to have a capacity corresponding to the stage of the culture. As described above in part, the reforming method of the present invention is preferably carried out in a state where breeding water is discharged in order to reform the sediment. After completion, when used, cultivation is performed with breeding water supplied.

[飼育水への混合]
 本発明の第二の水産生物の養殖方法として、水産生物の養殖槽に給水された飼育水に、腐植物質およびシリケイト化合物を含む改質剤を混合する改質工程を有するものとすることができる。これは、本発明の養殖槽の改質方法により改質された養殖槽、すなわち、改質された底質を有するものと併用するような、飼育水に、腐植物質およびシリケイト化合物を含む改質剤を混合する改質工程を有するものとすることもできる。
[Mixing with breeding water]
As the second method for cultivating aquatic products of the present invention, the method may have a reforming step of mixing a humic substance and a modifier containing a silicate compound with the breeding water supplied to the aquaculture tank for aquatic products. . This is a culture tank modified by the method for modifying a culture tank of the present invention, that is, a modified culture water containing humic substances and a silicate compound, which is used in combination with one having a modified sediment. It may have a reforming step of mixing agents.

 底質が少ない養殖や底質を用いない養殖、底質の改質が行えない満水の期間等に、養殖槽の改質を行うときに、このような第二の水産生物の養殖方法等は特に有用である。これは、養殖槽(養殖池等)に、飼育水を貯め、底質同様に腐植物質、シリケイト化合物を投入し、撹拌手段によって緩やかな撹拌を必要に応じて行い、腐植物質、シリケイト化合物を池全体に作用する状態として、飼育水に、本発明により底質を改質したときと同様の水質浄化の機能を付与して、養殖を行うものである。 When the aquaculture tank is reformed during aquaculture with low sediment, culture without the sediment, or when the sediment cannot be reformed, such as the second aquaculture method, Especially useful. This is done by storing breeding water in a culture tank (culture pond, etc.), charging humic substances and silicate compounds as well as bottom sediment, and performing gentle stirring as needed using stirring means to remove humic substances and silicate compounds from the pond. As a state that acts on the whole, breeding water is provided with the same water purification function as when the sediment is modified according to the present invention, and cultivation is performed.

 飼育水に腐植物質やシリケイト化合物を供給することで、これらを混合するとき、その混合量等は、前述の底質の改質を行うときの混合と同様の条件とすることができる。養殖槽において、その水深は養殖槽の仕様や、養殖する水産生物の種類、養殖時期等に応じて設定される。この水深を例示すると、1~5mや、2~4m程度から適宜設定される。この水深は水産生物を養殖することが出来る範囲で必ずしも一定とされるものではなく、天候や時間帯、養殖時期等にもよって変動する。このため、腐植物質やシリケイト化合物の混合量は、飼育水の液量に代え、養殖槽の広さ等を指標として設定し、管理することができる。 腐 By supplying humic substances and silicate compounds to the breeding water, when mixing these, the mixing amount and the like can be the same conditions as the mixing when performing the above-described bottom sediment reforming. In the aquaculture tank, the water depth is set according to the specifications of the aquaculture tank, the type of aquatic product to be cultured, the timing of the aquaculture, and the like. For example, the water depth is appropriately set from about 1 to 5 m or about 2 to 4 m. This water depth is not always constant within a range in which aquatic products can be cultured, and fluctuates depending on the weather, time zone, culture time, and the like. For this reason, the mixture amount of humic substances and silicate compounds can be set and managed by using the size of the cultivation tank as an index instead of the amount of breeding water.

 飼育水への改質剤の混合は、養殖開始後に所定の期間をあけて複数回行うものとしてもよい。例えば、養殖開始後や改質剤混合してからの期間を、3日以上や、1週以上、2週以上、3週以上のような期間をおいて追加で混合してもよい。また、この期間の上限は、適宜、3月以内や、2月以内、6週以内のような範囲内で追加で混合するものでもよい。 (4) The mixing of the modifying agent into the breeding water may be performed a plurality of times with a predetermined period after the start of aquaculture. For example, the period after the start of aquaculture or after the mixing of the modifier may be additionally mixed after a period of 3 days or more, 1 week or more, 2 weeks or more, 3 weeks or more. The upper limit of this period may be additionally mixed within a range such as within 3 months, within 2 months, or within 6 weeks as appropriate.

 撹拌手段は、水中ポンプ、水中パドル、ブロワー等を用いることができる。撹拌を行う時間は、熟成も考慮して水産生物の投入前に72時間以内程度の範囲で行うこともできる。撹拌時間は、養殖中に水産生物の活動や、養殖槽の通常の撹拌等によるものとすることができるため、時間を定めずおこなってもよい。熟成等を考慮すると、1時間以上や、6時間以上、12時間以上、24時間以上と積極的に撹拌状態を維持する時間を定めておこなってもよい。熟成時間の上限は、48時間以内や、36時間以内のように上限を設定してもよい。 As the stirring means, a submersible pump, submersible paddle, blower or the like can be used. The stirring time can be set within a range of about 72 hours or less before the introduction of the marine product in consideration of aging. The agitation time may be determined by the activity of aquatic products during aquaculture or by normal agitation of the aquaculture tank. In consideration of aging and the like, the time for actively maintaining the stirring state may be determined as 1 hour or more, 6 hours or more, 12 hours or more, 24 hours or more. The upper limit of the aging time may be set within 48 hours or 36 hours.

[溶存酸素濃度制御工程]
 本発明の養殖方法は、前記飼育水への酸素供給手段を有し、酸素供給手段による酸素量を制御することで、前記飼育水の溶存酸素濃度を低濃度に管理する低酸素期間と、前記飼育水の溶存酸素濃度を高濃度に管理する高酸素期間とを有する溶存酸素濃度制御工程を有することが好ましい。このような溶存酸素濃度制御工程を行うことで、養殖槽内の各種有機物等を効率よく除去することができ、水産生物の飼育を効率よく行うことができる。
[Dissolved oxygen concentration control step]
The cultivation method of the present invention has an oxygen supply means for the breeding water, and controls the amount of oxygen by the oxygen supply means, thereby controlling a dissolved oxygen concentration of the breeding water to a low concentration, and a low oxygen period. It is preferable to have a dissolved oxygen concentration control step having a high oxygen period for controlling the dissolved oxygen concentration of the breeding water to a high concentration. By performing such a dissolved oxygen concentration control step, various organic substances and the like in the culture tank can be efficiently removed, and breeding of aquatic products can be efficiently performed.

 溶存酸素濃度制御工程を行うことで、硝化菌および脱窒菌を活性化することができる。これにより、養殖槽内の窒素を含む有機物を十分に低減する高度処理を行うことができる。また、好気的処理と、嫌気的処理との双方を養殖槽内で行うことができるため、有機物全般を養殖槽内でも十分に除去できる。 硝 By performing the dissolved oxygen concentration control step, nitrifying bacteria and denitrifying bacteria can be activated. Thereby, it is possible to perform advanced treatment for sufficiently reducing nitrogen-containing organic matter in the culture tank. In addition, since both aerobic and anaerobic treatments can be performed in the culture tank, the entire organic matter can be sufficiently removed in the culture tank.

(高酸素期間)
 水産生物の排泄物や残餌などに含まれる窒素成分の有機態窒素(org-N)およびアンモニア態窒素(NH4-N)は硝化菌の働きで、亜硝酸態窒素(NO2-N)及び硝酸態窒素(NO3-N)に硝化される。この硝化をおこなうとき、溶存酸素が必要なため、飼育水の溶存酸素濃度を高濃度に管理する高酸素期間を有する。
(High oxygen period)
Organic nitrogen (org-N) and ammonia nitrogen (NH 4 -N), which are nitrogen components contained in excretions and residual foods of aquatic products, are acted by nitrifying bacteria, and nitrite nitrogen (NO 2 -N) And nitrate to nitrate nitrogen (NO 3 -N). When nitrification is performed, dissolved oxygen is required, so that the breeding water has a high oxygen period in which the dissolved oxygen concentration is controlled to a high concentration.

 高酸素期間は、所定の溶存酸素濃度以上の酸素濃度となっている期間である。この高酸素期間の指標となる溶存酸素濃度の下限は、4.5ppm以上が好ましく、5ppm以上がより好ましく、6ppm以上が特に好ましい。溶存酸素の上限は特に定めなくてもよいが、酸素そのものや酸素濃度が高い気体を供給して高いものとしてもよく、過剰に酸素供給する効果が限られる場合等は、装置負荷や低酸素期間への切替効率等も考慮して14ppm以下や、12ppm以下、10ppm以下を上限としてもよい。
 この所定の溶存酸素濃度以上の酸素濃度となっている高酸素期間は、1時間以上/日とすることが好ましい。より好ましくは、2時間以上/日以上や、3時間以上/日以上である。
The high oxygen period is a period in which the oxygen concentration is equal to or higher than a predetermined dissolved oxygen concentration. The lower limit of the dissolved oxygen concentration which is an index of the high oxygen period is preferably 4.5 ppm or more, more preferably 5 ppm or more, and particularly preferably 6 ppm or more. The upper limit of the dissolved oxygen is not particularly limited, but may be high by supplying oxygen itself or a gas having a high oxygen concentration.If the effect of excessively supplying oxygen is limited, the apparatus load or the low oxygen period may be reduced. The upper limit may be 14 ppm or less, 12 ppm or less, or 10 ppm or less in consideration of the switching efficiency or the like.
The high oxygen period during which the oxygen concentration is equal to or higher than the predetermined dissolved oxygen concentration is preferably set to 1 hour or more / day. More preferably, it is at least 2 hours / day or at least 3 hours / day.

 高酸素期間は、養殖槽の飼育水に、空気や酸素を供給するポンプ等を取り付けて、それらを用いて空気や酸素を供給することで溶存酸素濃度を上昇させることで達成することができる。空気供給手段を複数台取り付けて、溶存酸素濃度を測定しながら、運転する数を設定するなどの運用により、溶存酸素濃度を制御できる。 The high oxygen period can be achieved by installing a pump or the like that supplies air or oxygen to the breeding water in the aquaculture tank and supplying air or oxygen using them to increase the dissolved oxygen concentration. The dissolved oxygen concentration can be controlled by, for example, setting the number of operations while measuring the dissolved oxygen concentration by attaching a plurality of air supply means.

(低酸素期間)
 そして、硝化菌の働きによって変性した亜硝酸態窒素(NO2-N)及び硝酸態窒素(NO3-N)は脱窒菌の働きで排泄物及び残餌等の有機物と化学的に反応し窒素ガスとなり、無害化する。この脱窒をおこなうとき、溶存酸素を低減する必要がある。
(Low oxygen period)
The nitrite nitrogen (NO 2 -N) and the nitrate nitrogen (NO 3 -N) denatured by the action of nitrifying bacteria chemically react with organic substances such as excreta and residual food by the action of denitrifying bacteria to form nitrogen. It becomes gas and detoxifies. When performing this denitrification, it is necessary to reduce dissolved oxygen.

 低酸素期間は、所定の溶存酸素濃度以下の酸素濃度となっている期間である。この低酸素期間の指標となる溶存酸素濃度の上限は、4.5ppm未満が好ましく、4ppm以下がより好ましく、3.5ppm以下が特に好ましい。なお、低酸素期間の溶存酸素濃度の下限は特に定めなくても良いが、低すぎる場合、水産生物の活動が低下したり、生残率が低下する場合がある。このため、低酸素期間の溶存酸素濃度の下限を設定してもよく、0.5ppm以上や、1.0ppm以上、1.5ppm以上とすることができる。この所定の溶存酸素濃度以下の酸素濃度となっている低酸素期間は、1時間以上/日とすることが好ましい。より好ましくは、2時間以上/日以上や、3時間以上/日以上である。 The low oxygen period is a period in which the oxygen concentration is equal to or lower than a predetermined dissolved oxygen concentration. The upper limit of the dissolved oxygen concentration which is an index of the low oxygen period is preferably less than 4.5 ppm, more preferably 4 ppm or less, and particularly preferably 3.5 ppm or less. In addition, the lower limit of the dissolved oxygen concentration in the low oxygen period may not be particularly defined. However, if it is too low, the activity of the marine product may decrease or the survival rate may decrease. Therefore, the lower limit of the dissolved oxygen concentration during the low oxygen period may be set, and may be set to 0.5 ppm or more, 1.0 ppm or more, or 1.5 ppm or more. The low oxygen period during which the oxygen concentration is equal to or lower than the predetermined dissolved oxygen concentration is preferably 1 hour or more / day. More preferably, it is at least 2 hours / day or at least 3 hours / day.

 養殖槽は、一般的に、自然環境よりも水産生物を高密度飼育している。このため、水産生物の生長活動に伴い溶存酸素を利用したり、養殖槽内の有機物の好気的浄化等により、溶存酸素濃度は低下しやすい環境の場合が多い。この環境を利用し、低酸素期間は、養殖槽の飼育水への酸素(空気)供給を停止することで、溶存酸素濃度を低下させて達成することができる。また、窒素ガスなどの不活性ガスを養殖槽の飼育水に供給することで積極的に溶存酸素濃度を低下させてもよい。 Aquaculture tanks generally breed aquatic products at a higher density than the natural environment. For this reason, in many cases, the dissolved oxygen concentration tends to decrease due to the use of dissolved oxygen accompanying the growth activity of aquatic products or the aerobic purification of organic substances in the culture tank. Using this environment, the low oxygen period can be achieved by stopping the supply of oxygen (air) to the breeding water in the aquaculture tank, thereby lowering the dissolved oxygen concentration. Alternatively, the concentration of dissolved oxygen may be positively reduced by supplying an inert gas such as nitrogen gas to the breeding water in the culture tank.

 これらの高酸素期間と低酸素期間とを行う周期は、0.5周期/日(すなわち、2日で1周期)~3周期/日程度の周期で行うことができる。この周期は、養殖槽の種類や、水産生物の種類、飼育時期等に応じて適宜設定することができる。水産生物は、夜行性か、昼行性に大別され、活発に活動する時間帯は酸素を必要とし、活動が低下する時間帯は酸素を必要としにくい。この特徴から、夜行性の水産生物の飼育にあたっては、夜間を高酸素期間とし、日中を低酸素期間とすることが好ましい。昼行性の水産生物の飼育にあたっては、日中を高酸素期間とし、夜間を低酸素期間とすることが好ましい。 周期 The cycle of performing the high oxygen period and the low oxygen period can be performed at a cycle of about 0.5 cycle / day (that is, one cycle for two days) to about three cycles / day. This cycle can be appropriately set according to the type of the culture tank, the type of the marine product, the breeding time, and the like. Aquatic products are roughly classified into nocturnal and nocturnal products. Oxygen is required during periods of active activity, and less likely during periods of low activity. From this characteristic, when breeding nocturnal aquatic products, it is preferable to have a high oxygen period during the night and a low oxygen period during the day. In breeding daytime aquatic products, it is preferable to have a high oxygen period during the day and a low oxygen period at night.

 前述のように、これらの溶存酸素濃度制御工程により、硝化反応・脱窒反応を繰り返して有機物および窒素成分を高度処理している。さらに、本発明では、底質が腐植物質を含む改質剤で改質されていることから、底質に腐植物質のフルボ酸が担持された状態となっている。底質には、残餌や死骸等が沈殿し堆積する。これらの有機物の浄化等にあたって底質が、養殖槽の環境を維持するために寄与する影響は大きい。そして、底質は、フルボ酸が担持された状態となっており、さらに一定の周期性をもって、好気的環境と、嫌気的環境が存在することで、底質ではフルボ酸優位な腐植化も進行すると考えられる。このようなフルボ酸優位な腐植化により、浄化機能や、水産生物の飼育効果も向上する。 (4) As described above, the nitric acid reaction and the denitrification reaction are repeatedly performed in these dissolved oxygen concentration control steps to highly treat organic substances and nitrogen components. Furthermore, in the present invention, since the sediment is modified with the modifier containing humic substances, the humic substance fulvic acid is supported on the sediment. Residual food, dead bodies, etc. settle and accumulate on the sediment. In purifying these organic substances, the bottom sediment greatly influences the maintenance of the environment of the culture tank. In addition, the sediment is in a state in which fulvic acid is carried, and furthermore, with a certain periodicity, there is an aerobic environment and an anaerobic environment, and in the sediment, humic acid in which fulvic acid dominates is also present. It is thought to proceed. Such humic acid superiority in fulvic acid improves the purification function and the breeding effect of aquatic products.

 溶存酸素濃度は、溶存酸素濃度計により測定することができる。測定された溶存酸素濃度を基に、運転する酸素供給手段の数や出力を設定してもよいし、自動で制御するものとしてもよい。 The dissolved oxygen concentration can be measured by a dissolved oxygen concentration meter. Based on the measured dissolved oxygen concentration, the number and output of the operated oxygen supply means may be set, or may be controlled automatically.

 本発明の養殖においては、さらに、水温や、pH、塩分濃度、透視度などを管理項目として運用することができる。 養 In the aquaculture of the present invention, water temperature, pH, salt concentration, transparency, and the like can be further operated as management items.

[実施形態]
 図1は、本発明の養殖槽に係る第一の実施形態を説明するための図である。養殖槽10は、飼育水101と底質102を含む貯水槽100を有している。飼育水101に適宜腐植物質やシリケイト化合物を混合して本発明の養殖を行うことができる。底質102に腐植物質やシリケイト化合物を混合し、適宜熟成しておき、飼育水101を供給して養殖槽10として、飼育水101内に、養殖対象の水産生物を放流して養殖を開始することができる。
[Embodiment]
FIG. 1 is a view for explaining a first embodiment according to the culture tank of the present invention. The aquaculture tank 10 has a water storage tank 100 including breeding water 101 and bottom sediment 102. The cultivation of the present invention can be carried out by appropriately mixing humic substances and silicate compounds in the breeding water 101. A humic substance or a silicate compound is mixed with the sediment 102, aged appropriately, and the breeding water 101 is supplied to form the aquaculture tank 10, and the aquatic products to be cultured are released into the breeding water 101 to start aquaculture. be able to.

 また、養殖槽10には、送気ポンプ211,221,231とそれらの送気配管212,222、232による送気手段が取り付けられている。送気手段からの送気はそれぞれ切換弁213,223、233により養殖槽への送気の有無を切り替えることができる。送気ポンプ211,221,231は制御手段30にも接続され、送気の有無や送気量等を制御することができる。制御手段30による制御は、予め時間帯による運転をプログラムしたものとしたり、一部後述するように監視手段40によるモニタリングに基づいて制御したり、入力手段60による入力情報に基づくものなどとすることができる。 養 Further, the culture tank 10 is provided with air supply pumps 211, 221, and 231 and air supply means by the air supply pipes 212, 222, and 232. As for the air supply from the air supply means, the switching valves 213, 223, and 233 can be used to switch the presence or absence of air supply to the culture tank. The air supply pumps 211, 221, and 231 are also connected to the control unit 30, and can control the presence / absence of air supply and the amount of air supply. The control by the control means 30 may be such that the operation according to the time zone is programmed in advance, the control may be performed based on monitoring by the monitoring means 40 as described later in part, or the control may be based on input information from the input means 60. Can be.

 養殖槽10には監視手段40が取り付けられており、飼育水101の状況をモニタリングすることができる。モニタリングの対象項目としては、水温やpH、DO、有機物や窒素等の各種指標(T-C、TOC、COD、BOD、T-N、NH4 +、NO2、NO3)等とすることができる。監視手段40は制御手段30に接続され、監視手段の各項目や、運転時間等に基づいて、制御手段30が送気ポンプ211,221,231の運転等を制御するものとすることができる。また、制御手段30による制御状況や、監視手段40がモニタリングした各種パラメータ等を表示手段50に表示することもできる。制御手段30の制御や、監視手段40がモニタリングする項目、それらの表示手段50への表示を、入力手段60から入力した信号に基づいて処理し、選択や変更等することもできる。また、このとき、記憶手段(図示せず)も設けて、各種パラメータを記憶させ、適宜呼び出して確認したり、記憶手段に制御手段の制御条件のデータを記憶させてこのデータにより制御手段30の制御をおこなってもよい。このような養殖槽10は、本発明の養殖方法に適した養殖装置である。 Monitoring means 40 is attached to the culture tank 10 so that the condition of the breeding water 101 can be monitored. Items to be monitored include water temperature, pH, DO, various indicators such as organic substances and nitrogen (TC, TOC, COD, BOD, TN, NH 4 + , NO 2 , NO 3 ), etc. it can. The monitoring means 40 is connected to the control means 30, and the control means 30 can control the operation of the air supply pumps 211, 221, and 231 based on the items of the monitoring means, the operation time, and the like. In addition, the control status of the control unit 30 and various parameters monitored by the monitoring unit 40 can be displayed on the display unit 50. The control of the control means 30 and the items to be monitored by the monitoring means 40 and the display on the display means 50 can be processed based on the signal input from the input means 60, and can be selected or changed. At this time, a storage means (not shown) is also provided to store various parameters and appropriately call and confirm them, or to store data of control conditions of the control means in the storage means, and to use the data to control the control means 30. Control may be performed. Such a culture tank 10 is a culture device suitable for the culture method of the present invention.

 以下、実施例により本発明を更に詳細に説明するが、本発明は、その要旨を変更しない限り以下の実施例に限定されるものではない。 Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited to the following examples unless the gist is changed.

[養殖槽の改質と養殖試験]
 エビを養殖する養殖池で以下の実験を行った。
[1.養殖槽]
 養殖池は、河川水を利用する中国広東省中山市のエビの養殖に利用している養殖池である。養殖池の広さ:5070m2。図2は、飼育水に用いた河川水である。
[Aquaculture tank modification and culture test]
The following experiment was conducted in a pond for cultivating shrimp.
[1. Culture tank]
The pond is used for shrimp cultivation in Zhongshan, Guangdong, China, using river water. The size of the aquaculture pond: 5070 m 2 . FIG. 2 shows river water used for breeding water.

[2.底質の改質]
[2.1 混合]
 水を抜いた養殖池に、株式会社T&G社製の「リードアップ(登録商標)」(Lot.No“7k12”)(フルボ酸液)5L分を散布した。リードアップ1Lあたりのフルボ酸相当量は、1,000mg/Lである。リードアップ5Lは、水で約100倍に薄めて500L程度とし、養殖池(5070m2)に満遍なく散布した。フルボ酸相当量としての散布量は、1mg/1m2である。
 さらに、シリケイト化合物として、株式会社サンクロック科学研究所製「グリーンタフ微粉末(医王石)」を50kg散布した。グリーンタフ微粉末は、酸化アルミニウムを13.7質量%含有し、酸化鉄(第一鉄)を1.0質量%、酸化鉄(第二鉄)を5.0質量%含有している。グリーンタフ微粉末は、そのまま、養殖池(5070m2)に満遍なく散布した。なお、改質開始日は2月1日である。
[2.2 耕耘・熟成]
 前述のリードアップとグリーンタフを散布して混合した後、耕運機で耕耘した。その後、熟成期間として5日間静置した。これにより、底質を改質した養殖池を得た。
[2. Sediment reforming]
[2.1 Mixing]
5 L of “Lead Up (registered trademark)” (Lot. No. “7k12”) (fulvic acid solution) manufactured by T & G Co., Ltd. was sprayed on the culture pond from which water had been drained. The equivalent amount of fulvic acid per liter of read-up is 1,000 mg / L. 5 L of the lead-up was diluted about 100 times with water to about 500 L, and was spread evenly over a pond (5070 m 2 ). The application amount as the equivalent amount of fulvic acid is 1 mg / 1 m 2 .
Further, as a silicate compound, 50 kg of “Green Tough Fine Powder (Ioishi)” manufactured by Sun Clock Science Laboratories was sprayed. The green tough fine powder contains 13.7% by mass of aluminum oxide, 1.0% by mass of iron oxide (ferrous), and 5.0% by mass of iron oxide (ferric). The green tough fine powder was sprayed evenly over the culture pond (5070 m 2 ). The reform start date is February 1.
[2.2 Plowing and ripening]
The above-mentioned lead-up and green tough were sprayed and mixed, and then plowed with a cultivator. Then, it left still for 5 days as a ripening period. As a result, a culture pond with modified sediment was obtained.

[3.養殖]
[3.1 管理項目]
「透明度」 透視度計 ST-50を用いて、透明度を測定した。
「溶存酸素濃度」(株)堀場製作所製「ハンディpHメーター D-55」の溶存酸素濃度測定用電極を取り付けて測定した。
「ORP」(株)堀場製作所製「ハンディpHメーター D-55」のORP測定用電極を取り付けて測定した。
「pH」(株)堀場製作所製「ハンディpHメーター D-55」のpH測定用電極を取り付けて測定した。
「T-N」JIS K0102(2013)「45.4 銅カドミウムカラム還元法」に則って測定した。
「NH4 +」(株)共立理化学研究所製 「パックテストWAK―NH4」を用いて測定した。
「NO2」(株)共立理化学研究所製 「パックテストWAK―NO2」を用いて測定した。
「NO3」(株)共立理化学研究所製 「パックテストWAK―NO3」を用いて測定した。
「COD」(株)共立理化学研究所製 「パックテストWAK―COD」を用いて測定した。
[3. Aquaculture]
[3.1 Management items]
"Transparency" Transparency was measured using a penetrometer ST-50.
"Dissolved oxygen concentration" was measured by attaching a dissolved oxygen concentration measurement electrode of "Handy pH Meter D-55" manufactured by Horiba, Ltd.
The measurement was performed by attaching an ORP measurement electrode of "ORP""Handy pH Meter D-55" manufactured by Horiba, Ltd.
"PH" was measured by attaching a pH measuring electrode of "Handy pH Meter D-55" manufactured by Horiba, Ltd.
"TN" was measured in accordance with JIS K0102 (2013) "45.4 Copper Cadmium Column Reduction Method".
It was measured using the "NH 4 +" (Ltd.) Kyoritsu Institute of Physical and Chemical Research, Ltd., "Pack Test WAK-NH4".
Was measured using the "NO 2" (Ltd.) Kyoritsu Institute of Physical and Chemical Research, Ltd., "Pack Test WAK-NO2".
“NO 3 ” was measured using “Pack Test WAK-NO3” manufactured by Kyoritsu Riken Co., Ltd.
"COD" was measured using "Pack Test WAK-COD" manufactured by Kyoritsu Riken Co., Ltd.

[3.2 養殖条件]
・養殖品種:Vannamei
・投下量(養殖開始時):450,000尾(5070m2あたり)
[3.2 Aquaculture conditions]
・ Aquaculture variety: Vannamei
・ Dropping volume (at the start of aquaculture): 450,000 fish (per 5070m 2 )

[3.3 養殖]
 養殖開始後の管理指標の測定結果を、表1に示す。養殖は飼育水として河川水を用い、エビ養殖の常法に則って給餌等をおこなった。なお、養殖槽には3基の空気の送気ポンプが設置されており、飼育状態や天候、エビの大きさ、DOの実測値等に基づいて、飼育水の溶存酸素濃度を低濃度に管理する低酸素期間とする時間帯は送気ポンプを1基のみ運転し、飼育水の溶存酸素濃度を高濃度に管理する高酸素期間とする時間帯は送気ポンプを3基同時に運転することを指標として養殖を行った。より具体的には、エビが夜行性であり夜間活発に活動し酸素消費量が多いことから夜間(PM6時~AM6時)を高酸素期間としDOを5~6mg/Lとすることを管理指標とし、日中(AM6時~PM6時)は活動量が低下し酸素消費量が少ないことから日中を低酸素期間としDOを3~4mg/Lとすることを管理指標として養殖を行った。
[3.3 Aquaculture]
Table 1 shows the measurement results of the management index after the start of the aquaculture. Culture was carried out using river water as breeding water, and feeding was carried out in accordance with the usual method of shrimp culture. The aquaculture tank is equipped with three air pumps to control the concentration of dissolved oxygen in the breeding water to a low level based on the breeding conditions, weather, shrimp size, and DO measurements. During the low oxygen period, only one air pump should be operated, and during the high oxygen period during which the dissolved oxygen concentration in the breeding water is controlled to a high level, three air pumps should be operated at the same time. Aquaculture was performed as an indicator. More specifically, since the shrimp are nocturnal, active at night, and have a large amount of oxygen consumption, the management index indicates that the night time (PM 6:00 to AM 6:00) is a high oxygen period and DO is 5 to 6 mg / L. During the daytime (AM 6:00 to PM 6:00), aquaculture was performed using the low oxygen period during the day and a DO of 3 to 4 mg / L as a management index because the amount of activity decreased and oxygen consumption was small.

 養殖期間中の主な状況等を以下に述べる。飼育水は河川水を導入した。養殖水中のNH4-N、NO2-N濃度から、硝化、脱窒反応が顕著であることが確認される。飼育開始63日目に収穫した。収穫時の日数で、従来の同時期の養殖よりもエビの生残率は高く、体長も大きかった。稚蝦の期間は、蝦による酸素消費が少ない。一方、20日経過頃から蝦の生長に伴い酸素消費量が大きくなり、40日経過頃から蝦の生長が顕著になり酸素消費量も大きくなる。このような酸素消費状況も鑑み、運転する酸素供給機(エアーポンプ)の稼働台数を変更して酸素濃度の管理を行った。 The main situations during the aquaculture period are described below. River water was introduced as breeding water. The concentrations of NH 4 —N and NO 2 —N in the culture water confirm that the nitrification and denitrification reactions are remarkable. Harvested 63 days after breeding. In terms of the number of days at harvest, the survival rate of shrimp was higher and the body length was larger than that of conventional simultaneous farming. During the period of the shrimp, the oxygen consumption by the shrimp is small. On the other hand, the oxygen consumption increases with the growth of the shrimp around 20 days, and the growth of the shrimp becomes remarkable and the oxygen consumption increases around 40 days. In consideration of such an oxygen consumption situation, the number of operating oxygen feeders (air pumps) to be operated was changed to manage the oxygen concentration.

 図2~9は養殖状態等を説明するための写真である。図2は飼育水に用いた河川水を示す写真である。図3は、底質の改質を行う前の底質であり、養殖池の繰り返し利用により腐敗等がみられ汚泥化している部分が見受けられる。図4は、飼育準備のために改質剤混合後の底質の上に日間最低水温が20℃以上を確保できるようにシートを張って熟成している期間である。図5は熟成期間完了後、養殖池に水を張る様子を示したものである。図6は、養殖開始から30日時点でのエビの状態を観察したものである。図7は養殖開始45日時点でのエビの状態を観察したものである。図8、図9は養殖開始63日時点でのエビの状態を観察したものである。図8は収穫日である飼育開始63日時に収穫した5尾のエビであり、体長は13cm~15cmであることを確認した。 FIGS. 2 to 9 are photographs for explaining the cultivation state and the like. FIG. 2 is a photograph showing river water used for breeding water. FIG. 3 shows the sediment before the reforming of the sediment. In the sediment, repeated use of the cultivation pond shows decay and sludge. FIG. 4 shows a period in which a sheet is stretched on the sediment after the mixing of the modifying agent so as to ensure a daily minimum water temperature of 20 ° C. or higher in preparation for breeding. FIG. 5 shows a state in which the culture pond is filled with water after the ripening period is completed. FIG. 6 shows the state of shrimp 30 days after the start of the culture. FIG. 7 shows the state of shrimp 45 days after the start of the culture. 8 and 9 show the state of shrimp 63 days after the start of aquaculture. FIG. 8 shows five shrimp harvested on the 63rd day of breeding start, which is the harvest date, and it was confirmed that the body length was 13 cm to 15 cm.

Figure JPOXMLDOC01-appb-T000001
Figure JPOXMLDOC01-appb-T000001

 本発明は、水産生物の養殖に利用することができ、養殖槽の改質や、養殖中の管理により、養殖される水産生物の量や質の向上に寄与し、産業上有用である。 The present invention can be used for aquaculture of aquatic products, and contributes to the improvement of the quantity and quality of aquatic products to be cultured by reforming aquaculture tanks and managing during aquaculture, and is industrially useful.

 10 養殖槽
 100 貯水槽
 101 飼育水
 102 底質
 211、221、231 送気ポンプ
 212、222、232 送気配管
 213、223、233 切換弁
 30 制御手段
 40 監視手段
 50 表示手段
 60 入力手段
DESCRIPTION OF SYMBOLS 10 Culture tank 100 Reservoir 101 Breeding water 102 Sediment 211,221,231 Air supply pump 212,222,232 Air supply piping 213,223,233 Switching valve 30 Control means 40 Monitoring means 50 Display means 60 Input means

Claims (11)

 水産生物の養殖槽の改質方法であって、
 養殖槽の底質に国際腐植物質学会(IHSS)の方法に従う疎水性様物質であるフルボ酸を含有する腐植物質およびシリケイト化合物を含む改質剤を混合することで前記底質を改質する混合工程を有し、
 前記混合工程における前記底質への混合量が、前記腐植物質がフルボ酸相当量として100mg/1000m2以上5,000mg/1000m2以下であり、前記シリケイト化合物が1kg/1000m2以上100kg/1000m2以下である、養殖槽の改質方法。
A method of reforming a culture tank for aquatic products,
Mixing for modifying the sediment by mixing a humic substance containing fulvic acid, which is a hydrophobic-like substance, and a silicate compound according to the method of the International Humic Substances Society (IHSS) with the sediment of an aquaculture tank Process
The amount of the humic substance mixed with the sediment in the mixing step is 100 mg / 1000 m 2 or more and 5,000 mg / 1000 m 2 or less as fulvic acid equivalent, and the silicate compound is 1 kg / 1000 m 2 or more and 100 kg / 1000 m 2. The following is a method for modifying a culture tank.
 前記腐植物質が、フルボ酸濃度が、10mg/L以上2,500mg/L以下のフルボ酸液である請求項1記載の養殖槽の改質方法。 (2) The method according to claim 1, wherein the humic substance is a fulvic acid solution having a fulvic acid concentration of 10 mg / L to 2,500 mg / L.  前記シリケイト化合物が、酸化アルミニウムを10質量%以上30質量%以下含有するシリケイト化合物であり、酸化鉄(酸化第一鉄および酸化第二鉄の総量)を3質量%以上30質量%以下含有する請求項1または2記載の養殖槽の改質方法。 The said silicate compound is a silicate compound containing 10 mass% or more and 30 mass% or less of aluminum oxide, and contains 3 mass% or more and 30 mass% or less of iron oxide (total amount of ferrous oxide and ferric oxide). Item 3. The method for modifying a culture tank according to Item 1 or 2.  水産生物の養殖槽の改質方法であって、養殖槽の底質に国際腐植物質学会(IHSS)の方法に従う疎水性様物質であるフルボ酸を含有する腐植物質を含む改質剤を混合することで前記底質を改質する混合工程を有し、前記混合工程における前記底質への混合量が、前記腐植物質がフルボ酸相当量として100mg/1000m2以上5,000mg/1000m2以下である、養殖槽の改質方法。 A method of modifying a culture tank for aquatic products, comprising mixing a humic substance containing fulvic acid, which is a hydrophobic-like substance, according to the method of the International Humic Society of Japan (IHSS) into the bottom of the culture tank. A mixing step of modifying the sediment by mixing the sediment with the sediment in the mixing step, wherein the humic substance is 100 mg / 1000 m 2 or more and 5,000 mg / 1000 m 2 or less as a fulvic acid equivalent. There is a method of modifying aquaculture tanks.  前記混合工程のあと、前記改質剤を混合した前記底質を耕耘する耕耘工程を有する請求項1~4のいずれかに記載の養殖槽の改質方法。 The method according to any one of claims 1 to 4, further comprising a tilling step of tilling the sediment mixed with the modifying agent after the mixing step.  前記耕耘工程のあと、前記耕耘された前記底質を熟成する熟成工程を有する請求項5記載の改質方法。 6. The reforming method according to claim 5, further comprising, after the plowing step, a ripening step of ripening the cultivated sediment.  請求項1~6のいずれかの改質方法により改質された養殖槽を用いる水産生物の養殖方法であって、
 前記改質された養殖槽に飼育水を給水し水産生物を養殖する養殖工程を有する水産生物の養殖方法。
A method for cultivating aquatic products using a culture tank modified by the modification method according to any one of claims 1 to 6,
A method for cultivating aquatic products, comprising a culturing step of supplying breeding water to the modified aquaculture tank and culturing aquatic products.
 前記飼育水に、フルボ酸を含有する腐植物質およびシリケイト化合物を含む改質剤を混合する改質工程を有する請求項7記載の水産生物の養殖方法。 8. The method for cultivating aquatic products according to claim 7, further comprising a modifying step of mixing a humic substance containing fulvic acid and a modifying agent containing a silicate compound with the breeding water.  水産生物の養殖槽に給水された飼育水に、国際腐植物質学会(IHSS)の方法に従う疎水性様物質であるフルボ酸濃度が10mg/L以上2,500mg/L以下のフルボ酸液および酸化アルミニウムを10質量%以上30質量%以下含有するシリケイト化合物を含む改質剤を混合する改質工程を有する水産生物の養殖方法。 A fulvic acid solution having a fluvic acid concentration of 10 mg / L to 2,500 mg / L, which is a hydrophobic-like substance, according to the method of the International Humic Substances Society (IHSS) and aluminum oxide are added to the breeding water supplied to the aquaculture tank. A method for culturing aquatic products, comprising a modifying step of mixing a modifying agent containing a silicate compound containing 10% by mass or more and 30% by mass or less.  前記飼育水への酸素供給手段を有し、酸素供給手段による酸素量を制御することで、
 前記飼育水の溶存酸素濃度を0.5ppm以上3.5ppm以下の低濃度に連続して2時間以上となるように管理する低酸素期間と、
 前記飼育水の溶存酸素濃度を4.5ppm以上10.0ppm以下の高濃度に連続して2時間以上となるように管理する高酸素期間とを有し、高酸素期間と低酸素期間とを0.5周期/日~3周期/日の周期で行う溶存酸素濃度制御工程を有する請求項7~9のいずれかに記載の水産生物の養殖方法。
By having an oxygen supply means to the breeding water, by controlling the amount of oxygen by the oxygen supply means,
A low oxygen period in which the dissolved oxygen concentration of the breeding water is controlled so as to be continuously at a low concentration of 0.5 ppm or more and 3.5 ppm or less for 2 hours or more;
A high oxygen period for controlling the dissolved oxygen concentration of the breeding water to a high concentration of 4.5 ppm or more and 10.0 ppm or less continuously for 2 hours or more; The method for cultivating aquatic products according to any one of claims 7 to 9, further comprising a dissolved oxygen concentration control step performed at a cycle of 5 cycles / day to 3 cycles / day.
 前記水産生物が、甲殻類である請求項7~10のいずれかに記載の養殖方法。 殖 The aquaculture method according to any one of claims 7 to 10, wherein the marine product is a crustacean.
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