UA87342C2 - Biological fertilizer, process for preparation of biological fertilizer and plant for preparation thereof (variants) - Google Patents

Abstract

A biological fertilizer contains biohumus, containing nitrogen, phosphorous, potassium, calcium, magnesium, iron, mangenese, copper, water-soluble humates and agronomically useful biohumus bioflora. A method for preparation of biological fertilizer and variants of a plant for preparation of biological fertilizer comprise, in general, accumulative reservoir, screw extruder, biorector, jet aerator, turbine pump and hydrodynamic cavitation mixer of rotor-pulsation apparatus.

Description

the flow pipeline is connected to the inlet pipeline of product clarification, in addition, the installation of a screw extruder with water, and through the jet, additionally equipped with a buffer tank, a fine aerator - with a bioreactor, which is equipped with a tip-dispersed suspension, the inlet pipeline of which is the bottom with the installed in in it, the distribution is connected to the output pipeline by a dispersing device, while the upper part of the bioreactor, and the output pipeline to the inlet pipe of the reactor, is connected to two interconnected water bioreactors.

The invention relates to agricultural production (spraying) of plants. Considering the fact that it is intended for the production of liquid ecologics, the treatment of plants by the spraying method is one of the purest complex fertilizers based on biorubber, one of the most effective and inexpensive methods, stable. It will be most widely used because suspension is a mandatory factor for successful foliar feeding of plants, processing of our agricultural work. haying, soaking of tree seedlings and root- The stability conditions are met by a suspension that can be introduced into the soil by spraying. satisfactory fluidity with minimal viscosity.

The use of chemical fertilizers and various nutrients are introduced into the composition of liquid pesticides, which has become widespread, to meet these conditions. modern agriculture, leads to So, for example, in (a.s. Me1708806 MPKU: СО5С1/06, soil pollution and slowing down of the process of pri- publ. in Byul. Me4, 1992 | described mineral native revival of their fertility. In connection in this regard, the fertilizer, which as a suspension stabilizer is of special relevance, is the production and tying gel. The gel is a mixture of extract from tor- the use of environmentally friendly fertilizers based on fu, potassium metasilicate, phosphoric acid and natural materials that not only do not harm salts of polyvalent cations of metals. The gel of the soil, but also nourishes the plants and provides them, the component of this fertilizer allows you to retain biologically active substances that help solid insoluble particles of salts in the suspended become resistant to diseases and negative effects, but at the same time its ingredients anthropogenic load has little effect on increasing the productivity of agricultural

In this aspect, it is widely distributed as some cultures. In addition, biohumus acquired insoluble particles of highly effective fertilizer salts. It has too large sizes, which, although it is produced by processing industrial popu- in a gel environment, can get stuck in the lation of red California worms in the pipes and nozzles of sprayers. It is known that waste of various origins: manure, liquid humic fertilizer, which is animal, vegetable, household, food waste and liquid suspension of biohumus and agricultural etc. Biohumus fertilizer is rich in humic substances from river wastes, which include potassium (patent wines, macro- and microelements, amino acids, enzymes, plant hormones, as well as 2005.10.27| . The suspension also contains an extract of rubber with antibiotics and living agronomically useful bio- new acids and products of decay of organic flora. The presence of a significant content of calcium humates in biohumus contributes to the formation of water-resistant silt. It should be noted that almost any grain structure of the soil, which helps the collected suspension, which is used as fertilizer, to harvest soil moisture in the root zone. oder- produces biologically active substances, chewing this fertilizer increases. It is easily sprayed, resistance of plants to diseases and pests. Biohumus, but its biological effectiveness is low eye significantly affects the acidity of the soil and has the property of changing it towards the optimum. One of the ways to increase the biological value. A unique property of fertilizer is its microbiological fermentation. properties of this product formed the basis of the development. Yes, in (application of RF Mo20021296660/12 IPKZ: various solid and liquid forms of fertilizers, in СО5Е11/02, publ. , which contains crushed

To date, numerical measurements of lignite particles and an additive - aqueous bactericides and equipment for the production of complex biohumus suspension have been developed. Fertilizer enrichment of liquid fertilizers based on biohumus, each with microorganisms, increases its consumer qualities, which have specific characteristics for its species - in particular, ensures the regulation of plant growth, but ki. The liquid form of fertilizer is a dispersed system with at the same time operational properties of fertilizer, liquid dispersion medium and solid dis- are related to its application, preservation and suspension phase (or suspension). new characteristics of liquid fertilizers, except for agrochymus in aqueous suspension tend to octamic, includes such an important indicator as giving, they can get stuck in the nozzles and the stability of the suspension before it is introduced into the soil. bags of sprayers.

It is this indicator that determines consumer qualities. In the field of modern crop production, liquid fertilizer is counted, many methods for the production of liquid forms depend on it to a large extent, both the efficiency of processing and the reliability of functional complex fertilizers, which include bionization of equipment, which is used when ob- humus. Yes, in (patent of Ukraine Mebb173 IPC:

СО5011/02, publ. in Bul. Me4, 2004 | described The production of liquid organic fertilizers will require a method of obtaining biofertilizer with fungicidal and there is creation of a reliable, economical and simple in bactericidal properties. The method includes maintenance of the equipment. The improvement of the existing preparation of water extract of biohumus, scraping technologies and the creation of new ones necessarily by processing with red Californian- is connected with the creation of new types of installations and the worm of organic waste, to the composition of devices. which includes 50-8095 plants infected with fungi. Yes, the well-known installation for the production of mines

To obtain fertilizer, biohumus is placed in a commercialized organic fertilizer, described in the (patent of the centrifuge) and mixed with water, after which RF Mo2254699 MPK8: А0О1С3/00, СОБ5ЕЗ/06, the resulting mixture is drained and settled until complete СО5Е11/04, publ. 2005.06.27 |, which is equipped with re-sedimentation of solid particles. The settled liquid in a reservoir with inlet and outlet pipelines is the finished product. The disadvantage of this additive for mixing the liquid medium and the stream is the low content of living beneficial microflora by the injector. The disadvantage of this installation is that that of biohumus, because in the process of processing in a centrifuge, it is not able to ensure sustainable production, most of it loses its viability.

In addition, the mixture mixed in a centrifuge retains the sludge, which can cause clogging of spray nozzles due to its homogeneity within a relatively short period of time, and the settled liquid can destratify devices. to hide A well-known installation for the production of liquid or

A similar technology for the production of liquid humic fertilizer based on raw materials containing a new fertilizer is described in RF patent Mo2263092 humic compound, which is mixed with biomass at

MIC: СО5Е11/02, publ. 2005.10.27|. Fertilizer is obtained by constantly bubbling with air currents by preparing an aqueous suspension (patent of the Russian Federation Me2040516, MPKU: СО5Е11/02, publ. in biohumus, with the addition of an active substance to it Bull. Me21, 1995). This installation contains an auger of mineral fertilizers, treatment of the mixture with alkali , a raw material shredder connected to the tank, mixing of the resulting suspension and its isolated pipeline with a storage tank. The technological cycle of preparing this biomass, which is fed into the tank with fertilizer, is long-term -for example, the process of a centrifugal pump. A tank equipped with a means of stirring the mixture takes about 10-12 hours, and mixing of crushed raw materials with biomass. settling of the suspension takes 2-2.5 days. But the main installation is also equipped with a compressor, which is a drawback of the technology , that it is not able to ensure the bubbling of the mixing mixture - to ensure the production of a product resistant to dissolution. This installation has the same disadvantages as the above ezga- layering. given, because of which the final product, which it produces

An example of the production of liquid fertilizer is a liquid kefir-like mass, which has an increased content of plant growth regulators (contains solid inclusions that can clog active metabolites) can be the method described in spraying equipment.

I(patent of Ukraine Me47304 MPKU: СО5Е11/08, publ. A similar plant for ecological production in Bull. Mob, 2002|. According to this method of fine fertilizer is described in (patent of Ukraine) peat is mixed with cultural liquid - Meb4092 МИК: СО5Е11 /04, published in Bul. Me2, with a bacterial suspension and add water extract- 2004|. It includes a bioreactor in which there is a layer of biohumus. This technology is complicated by the need for in feeding organic waste into the bioreactor and removing it from it, as well as a device for mixing

A method of obtaining biofertilizer, a mixture in a bioreactor is also known. With the help of this installation, which includes the following operations: fertilizer, which is a liquid fraction, is added to the sieved biohumus, the biomass of red Californian chertium is added to the fermented mass of shredded waste, and the mixture is crushed until it is homogeneous, the points of which are incompatible with the dimensional parameters of the mass, which is mixed with water and whisked to the spraying equipment. Thus, obtaining a suspension (patent of Ukraine Mob7514, structural construction of this installation is also not

IPC: C0509/02, publ. in Bul. Mob, 2004 |. Su- creates conditions for obtaining a finely dispersed and suspension is defended, separated from solid stable suspension. particles and an aqueous solution are used as fertilizers. This technology, thanks to the use of straw biomass containing biohumus, which includes earworms, ensures the saturation of the fertilizer with valuable nitrogen, phosphorus, potassium, calcium, magnesium, iron, components that increase the immune properties of manganese, copper, water-soluble humates and plant agronomy. But, as it was noted above, a relatively insignificant amount of nutrients passes into the settled human-useful bioflora of biohumus (patent of the Russian Federation), while the bulk of them 2002.04.27|. always remains in the settled fraction. In addition, this Fertilizer contains nitrogen, potassium, phosphorus and humic technology requires considerable costs for growing acids and is a settled and filtered biomass of worms, the composition of which is a crushed peat suspension and of biohumus, which in the case of a non-mixture reaches 4095. Thus, the considered circumstance adds additional nutrients, the technology is not effective enough, and from the position - copper, boron, zinc, selenium, silicon oxide. Disadvantages - emotional perception, it can be called inhumane the low content of this product is agronomic - because the production of biomass requires the useful bioflora of biohumus, which significantly reduces the efficiency of the fertilizer. The reason for the low content bioflora has the fact that in the process of mixing the mixture The set task is achieved due to biohumus and peat in the reactor a significant amount of mikgo, that in biological fertilizer containing biohumus, roorganisms simply die, and a large number of vital nitrogen, phosphorus, potassium, ca- able microflora remains in the sediment. lithium, magnesium, iron, manganese, copper, water-soluble

Particles of solid humates and agronomically useful bioflora of biohumus and peat moss are present in the finished product. In addition, they can settle to the bottom of the container in which fertilizer is stored - nitrogen 0.0084-3.0; in Thus, the physical state of the fertilizer can be phosphorus 0.0053-3.0; present as a suspension with a low degree of potassium 0.036-3.0; firmness and stability, the use of which is from calcium 0.0047-1.0; spraying plants is problematic. magnesium 0.0037-0.37;

The invention is based on the problem of sub-iron 0.00025-0.025; improving the agrochemical efficiency of biological fertilizer - manganese 0.000011-0.001; ryva by optimizing qualitative and quantitative copper 0.000045-0.0045; of its nutritional elements and minimization of the size of water-soluble humates 0.00016-0.6; of solid inclusions that are part of the fertilizer, the remaining water, which allows to increase the agrochemical value of the fertilizer - at the same time, the fertilizer contains agro-fertilizer, to increase the total area of solid particles, the beneficial bioflora of biohumus in the amount of 15.56 - on which microorganisms are immobilized , which results in 15.52 colonies in 1Tml, and the size of the solid particles leads to their intensive development, as a result, the volume is 3-10 μm. which not only restores the bacterial flora. In the composition of the proposed fertilizer, the nutrients lost in the process of carrying out technological operations, the elements of biohumus are present in a much greater number of cycles of the work cycle, but also significantly replenishes its bones than in the fertilizer described in the invention, the content in to the finished product, in addition, they are created as a prototype. This is evidenced by the following data: the conditions for the unhindered passage of fertilizer through the channels of spraying installations. 11111111 Inventionbu6 | Prototype, in the (Middle) pity 777777111111111111111111111117777717171717171711111111111111002222222222222222227777771111 /-/-/./ 00000021 o vodasreshta.і////777711111111Ї11

The increased content in the proposed fertilizer. In addition, the solid particles of biohumus are finely dispersed, almost dust-like, in a balanced amount and in easily accessible forms, including nitrogen - improves the synthesis of amino acids, from which proteins and polypeptides are formed from the suspended solids; phosphorus - stimulates without forming sediment. Such a suspension even during the processes of respiration and photosynthesis; potassium - increases during long-term storage does not delaminate, preserves the hydration of the protoplasm and its water-holding capacity, giving its stability, and is the most acceptable tness and activates the supply of plastic substances for the treatment of plants by the spraying method. from leaves to reproductive organs; calcium - A significant advantage of the biological fertilizer is that it contributes to the better development of the root system, its significant content of active (living) agronomic-optimizes the reaction of the soil-absorbing complex; beneficial bacterial flora, which makes it magnesium and iron - improves the formation of chlorophyll in the leaves; also an effective microbiological fertilizer; manganese - has a positive effect on carbon - is an excellent regulator of plant growth, contributes to the water, nucleic and protein exchange of plants, activates the restoration of soils even after many years of exposure and enhances photosynthesis; the use of water-soluble rubbers and inhibits pathogenic microflora - activates and accelerates the processes of growth and development (see Table 1). plants, reduces the influence of stressful natural factors.

Table 1 (Spore-forming bacteria, millions of

Azotobacter, million |11116 100

A high content of agronomically useful bioflora is more acceptable for ensuring both high is the result of the presence of finely dispersed agrochemical and high operational characteristic solid inclusions in the fertilizer. Taking into account the fact that micro-teristic fertilizers. Fertilizer, the quantitative composition of biohumus organisms are immobilized on the outside of the living elements, which will be smaller than the surface of the solid carrier substrate, it is obvious that with the invention, has too low a biological reduction in the size of solid particles, increasing the activity and treatment of plants with it is little the area for their "inhabitation" - microorganisms on their development - will be marked. The use of fertilizer, the content of which will provide favorable conditions for the active communication elements of which will exceed the specified amount. This process is also intensified by the quantitative interval in the invention, in some cases due to the fact that the development of bacteria occurs in the biological presence of oxygen can cause oversaturation of plants. active substances, which leads to depression

As a result of conducting a series of studies, their growth and deterioration of product quality. It has been established that the content of nutrients, which Shredding in a biohumus dispersant is sometimes included in the composition of biological fertilizer in quantities whose size will exceed 10 μm, in the interval proposed by this technical solution leads to their getting stuck in the nozzles of the spraying solution, is optimally balanced for seeds, and obtaining particles with a size smaller than Zμm is a very difficult technical operation to ensure full nutrition of plants. throughout the entire period of their development and taking into account their Table 2 presents the results of the stimulus-biological features. Likewise, the size of the solidifying effect on the growth and development of plant bioreactive particles of fertilizer in the range of 3-10 μm is the most tested.

Table 2

DE or other NN VN. tip

Options for activating the troll role

Control - water

Table C shows the results of the tests proposed by the invention. In the experiment conducted on the plot planted with tomatoes, MeZ - in an amount equal to the minimum content of ingram, with the use of specific compositions of biological agents proposed by the invention. In the research of fertilizer. In the Me1 experiment, the ingredients of the Me4 fertilizer - in an amount equal to the maximum content, were selected in an amount smaller than the minimum required ingredients proposed by the invention. In addition to this invention. In the experiment Me2 - in the lead Me5 and Mob - in the amount that is in the amount that exceeds the maximum content of ing within the limits of the proposed interval.

Table C

Mo. Number of plants that are n/p Composition of ingredients, wt. 9o survived per 100 planted pieces nitrogen - 0.0080, phosphorus - 0.0050, potassium - 0.030, calcium - 0.0042, magnesium - 0.0032, 1 | iron - 0.00020, manganese - 0.000009, copper - 0.000040, water-soluble humates - 76 0.00012, water - the rest, agronomically useful bioflora - 15'col/ml nitrogen - 5.0, phosphorus - 5, 0, potassium - 5.0, calcium - 2.0, magnesium - 0.40, iron - 0.030, 2 | manganese - 0.003, copper - 0.0050, water-soluble humates - 0.7, water - the rest, agronomically useful bioflora - 15 "col/ml, nitrogen - 0.0084, phosphorus - 0.0053, potassium - 0.036, calcium - 0.0047, magnesium - 0.0037,

With | iron - 0.00025, manganese - 0.000011, copper - 0.000045, water-soluble humates - 0.00016, water - the rest, agronomically useful bioflora - 15 bcol/ml nitrogen - 3.0, phosphorus - 3.0, potassium - 3.0, calcium - 1.0, magnesium - 0.37, iron - 0.025, 4 | manganese - 0.001, copper - 0.0045, water-soluble humates - 0.6, water - the rest, agronomically useful bioflora - 152 kol/ml nitrogen - 1.5, phosphorus - 1.5, potassium - 1.6, calcium - 0.55, magnesium - 0.01, iron - |0.00080, manganese - 0.000099, copper - 0.000099, water-soluble humates - 0.00085, 91 water - the rest, agronomically useful bioflora - 158 kol/ml nitrogen - 2.5, phosphorus - 2.5, potassium - 2.5, calcium - 0.80, magnesium - 0.12, iron - 0.010, manganese - 0.000080, copper - 0.000085, water-soluble humates - 0 ,00095, water - 94 rest, agronomically useful bioflora - 15 Injection/ml

According to the results of the table, it can be seen that the greatest increase in biological fertilizer by processing and the highest indicator of plant survival occurs in crushed raw materials with the help of the case of using fertilizers under MoMo 5, 6. snail cavitation disperser and optimal

The prototype of the invention also adopted the conditions for microbiological fermentation to obtain a complex liquid organic tation of an aqueous suspension, which ensures the minimization of fertilizer, which includes diluting biohumus to the size of solid particles of biohumus to a state, adding, mixing and microbiological fermentation of water suspension that contains these particles, the resulting mixture with continuous it is stable, homogeneous, resistant to oxygen depletion (patent of the Russian Federation Meo2107054, IPC: layering of the substance, and also increases

СО5Е11/00, СО5Е17/00, publ. 1998.03.201. total area of solid particles on which immo-

According to this method, the raw materials are inactivated by microorganisms, which leads to their being pressed into the fermenter, heated water is added and intensive development, in addition, microbiological fermentation is carried out under conditions for unhindered passage of the fertilizer - constant mixing. To provide water through the channels of spraying units. optimal fermentation conditions, the temperature is maintained at the expense of the suspension in the range of 25-30" and during that, in the method of obtaining biological fertilizer, the reaction mass is enriched with oxygen, which includes diluting the biohumus with water, by blowing the fermenter heated to mixing and microbiological fermentation at a temperature of 25-307"C with air. At the end of the obtained mixture during its continuous enrichment process, the suspension is settled and not oxygenated, according to the invention, the biohumus is subjected to separate the liquid phase, which is then evaporated during dispersion using a hydrodynamic temperature of 25-30"C. The resulting dry fraction of the cavitation disperser before obtaining a shallow - dilute with water and thus obtain a dispersed aqueous suspension with the size of solid final product - liquid humic fertilizer. particles of biohumus 3-10 μm, after which

The disadvantage of this technology is that it does not involve microbiological bacterial fermentation and the operation of fine grinding by biohumus flora. raw materials, due to which the efficiency of micro- The proposed method of making good- biological fermentation is not high enough. va provides the possibility of grinding biohumus

And, taking into account the fact that the fermented vessel is subjected to dehydration at a temperature of 10 µm to the state of microdispersed particles with a size of 3. This effect is achieved thanks to the recirculation mixer. Solid particles of biohumus, produced

It should also be noted that the complete technological process of making several "turns" through the cavitation cycle of this fertilizer is a long mixer or a rotary-pulsation apparatus, which is long and complicated. So, for example, to carry out cavitation effects, they are crushed. On such days of fermentation, the suspension must be heated to form sediment-resistant particles suspended at a temperature of 25-30"C, and the enzyme (emulsion) process itself. And, as mentioned above, it takes at least 160 hours to reduce the size of the particles. surface area

The basis of the invention is the problem of the soil, on which microorganisms can be immobilized and the efficiency of the odesma method can be increased, due to which the content of the bioflora of biohumus in the liquid fertilizer produced according to the proposed second variant of the invention technology is much higher than in the well-known invention has been given the task of increasing operational efficiency. This is also facilitated by the fact that the contact of micro-arable facilities for the production of ganisms with miluodispersible inclusions of bio-biological fertilizer by improving its slurry occurs under the action of airlift flows of a constructive design, in particular, equipped with air bubbles that contain oxygen. by a disperser with an external circuit reciprocating

A significant advantage of the method is also the fact that culation, optimization of the connections between the main suspensions for fermentation are not used as structural elements, and also equipped with a separately grown population of microorganisms (as in the case of the installation with a buffer tank of finely dispersed, this is the case in the prototype), and the bacterial flora suspension and two tanks for clarification of the product, raw material - biohumus. This significantly increases the minimization of solids, increases the biological value of the fertilizer and reduces its biohumus points to a state in which the water-dry value. suspension, which contains these particles, is

The combination of such factors as the presence of finely dispersed particles in a stable, homogeneous, layer-resistant suspension and their contact with the substance, as well as an increase in the total area of solid particles by the bioflora of biohumus in an oxygen atmosphere, on which the technological cycle of fertilizer production occurs in bilising microorganisms, which leads to their comparison with the known process. So, for example, intensive development, in addition, the necessary concentration of biohumus is created in the finished condition for the unhindered passage of fertilizer - the product, which is manufactured by the proposed method through the channels of spraying installations and this method, is achieved in 5-7 minutes, at that time, it is ensured the continuity of the technological as in the known method, this operation takes close to the process. for 160 hours. The set task is achieved by the fact that

The method can also be used for the installation for the production of biological fertilizers of liquid forms of biologically active fertilizers, which includes a storage container and feed additives. ity associated with the screw extruder and bio-

Implementation of the proposed method with a reactor connected to a jet aerator, pouring biological fertilizer in a general view - according to the first version of the implementation, the initial work and a specific example of its implementation - the screw extruder is connected to the distruing work described below installation, a pergator, equipped with an external contour intended for the implementation of this method. recirculation, which includes centrifugal

Also accepted as a prototype of the invention is an inline pump and hydrodynamic cavitation mixer for the production of a complex liquid tank or a rotary-pulsation device, which through organic fertilizer, which includes an outlet pipeline connected to an inlet pipe-accumulating tank, connected connected to the screw extruder wire of the screw extruder, and through the extruder and the bioreactor connected to the jet mine aerator - with the bioreactor, which is equipped with an aerator (patent of the Russian Federation Mo2056393, IPC: conical bottom with installed in it

СО5ЕЗ3/06, publ. in Bul. Mov, 1996 |. distribution device, while the upper time-

In this installation, the aqueous solution of the crushed sludge of the bioreactor is connected to the clarification tank of the raw material and is fermented in the bioreactor - the product. methane tank, to which it enters through an airlift. The task is also achieved with a military aerator. Among the disadvantages of the installation is the fact that in the installation for the production of biota it lacks structural elements, logical fertilizer, which includes a container capable of ensuring the grinding of raw materials into a fine-dispersed state, connected to the auger. This factor is the reason for the extruder and the bioreactor connected to the jet, that the fermentation process in the bioreactor with a decompression aerator, according to the second option, is not sufficiently intense. feeding, the output pipeline of the screw extrusion

The basis of the invention is the task of a sub-separator connected to a disperser equipped with an external recirculation circuit, which includes a centrifugal pump and hydrodynamic improvement of its design, a cavitation mixer or a rotary-pulsation mixer, in particular, equipment for the production of biological fertilizer a disperser with an external device, which is connected through the outlet pipeline to the recirculation circuit, as well as optimization with the input pipeline of the screw extrusion connections between the main structural elements, and through a jet aerator - with the bioreactors of the installation, which ensures minimization size, which is equipped with a conical bottom from the moat of solid particles of biohumus to a state where, with a distribution device installed in it, the aqueous suspension containing these particles, while the upper part of the bioreactor is connected to represents a stable, homogeneous, stable to the two interconnected tanks and clarification of the substance layering, as well as providing the product, in addition to this, the installation is equipped to increase the total area of solid particles, on the buffer tank of a finely dispersed suspension, the input of which is immobilized microorganisms, the call pipeline of which is connected to the output works to of their intensive development, in addition, the dispersant pipeline, and the outlet pipeline, conditions for unobstructed passage - with the bioreactor inlet pipeline. Fertilizer delivery through the channels of sprayers Equipping the installation with a disperser, connectors. equipped with an external recirculation circuit, ensures the possibility of formation in the disperser of

of co-dispersed suspension of biohumus, solid incl. product 18 and valves ВЗ and В4, which connect the tank 15 and 18 with bioreactor 11. Illumination tanks of the bioflora of biohumus on them. The positives of the product 15 and 18 allow you to combine the results of this described above in time. processes of filling tanks and lightening the product in

It should be noted that the rotary-pulsation one tank with the process of pouring the product from the dru-apparatus is an alternative to the cavitation mixer of the gogo tank. For this purpose, they are additionally equipped - both devices perform the same function with valves B5 and Bb, the outputs of which are connected as part of the external recirculation circuit, and in the filling pipeline. designs of the proposed installation can be used interchangeably. phase, which is biologically active

In the composition of the installation described in the second part of the product, which is separated in the lightening tanks of the invention, a shallow product buffer tank is introduced, the installation can be equipped with an additional dispersed suspension and two interconnected pipelines with valves B7 and B8, the entrances of the lightening tanks product This ensures safe connected to the nozzles installed in the rarity of the technological cycle of preparation of the lower part, respectively, of the first 15 and additional fertilizers due to the combination in time of the process 18 tanks of lightening of the product. The output of the pipe preparation of finely dispersed emulsion and reduction pipeline through pump 19 is connected to the bottom of the biological flora: made in the disperser of the part of the bioreactor tank 11. a portion of the suspension before entering the bioreactor The installation works in the following way. tore accumulates in the buffer tank, and during this In the initial state, the dispersant b is filled, the dispersant processes the next portion of product water, and the conical part of the bioreactor 11 closes. At the same time, it does not need to be halted by the initial biologically active product. riod of operation of the bioreactor, as it happens when the valve B1 is open, and the valve B2 is closed. of the installation described in the first version of it For the preparation of a liquid biologically active performance. The product includes a centrifugal pump 7 and

The presence of two tanks for lightening the product is a screw extruder 2. At the same time, the output prevents the combination during the filling process, the duct is crushed by the extruder 2 and enters the tanks and the product lightening process in one outlet chamber 3, from where the water flow of the tank circuit with the process of filling the product with of the second barrecirculation is carried out into the disperser 6. Rough. the dispersed phase of the initial product, settling in

The invention is explained by the drawings on which the dispersant b is absorbed by the hydrodynamic brew: by a cavitation mixer (or a rotary - in Fig. 1 - the block diagram of the first version of the pulsation apparatus) 9, where under the action of cavitation-tanovka; of these effects is crushed, forming a resistance to - in Fig. 2 - a block diagram of the second version of the suspension suspension (emulsion). newcomers The working time of screw extruder 2 is determined by

The proposed installation for the production of the required concentration of the initial pro-complex liquid fertilizer (Fig. 1) contains the product in the finished mixture. After obtaining the necessary storage tank 1, connected to the screw extruder 2 with the help of the extruder 2, the pre-shredding of the original product and the mixture through hydrodynamic cavitation mixing, separation of extraneous impurities from it is switched off and the recirculation process takes place. The outlet of the drum (or rotary-pulsation apparatus) 9 to the single-screw extruder 2 is equipped with the outlet of a homogenous suspension resistant to stratification. The chamber 3 is equipped with outlet 4 and inlet 5. The recirculation time is determined by the volume of pipelines. The outlet pipeline 4 of the chamber of the disperser 6 of the screw extruder 2 is connected to the dispersant during the dispersion process of the bacterial rum 6, which in the initial state is filled with water. the flora of the initial product dies. For its restoration

The disperser 6 is equipped with an external circuit, after the end of the process of dispersing the recirculation, which contains a venter pump 7. the valve VI1 closes, and the valve B2 opens

Suction pipeline 8 centrifugal. This leads to the supply of the resulting pump 7 connected to the disperser 6, and its finely dispersed suspension into the bioreactor 11 through the pressure pipeline connected to the inlet of the hydrojet aerator 12. The flow of the finely dispersed dynamic cavitation mixer (or suspension rotor, saturated with small bubbles of - no-pulsation apparatus) 9. The inlet of the suction in the jet aerator 12, entering through the nozzle 10 of the cavitation mixer (or the distribution device 13 in the output layer of the bio-rotor-pulsation apparatus) 9 is connected to the dynamically active product, pushes the latter . the lower part of the disperser 6, and the exit through the Construction of the distribution device 13 is the VI valve with the inlet pipeline 5 screw-ensures the distributed tangential introduction of the extruder 2 and with the bioreactor 11 through the suspension flow into the bioreactor 11, and the saturation of the tail B2 and jet aerator 12 The bioreactor flow tank with air bubbles leads to the ra 11 is made with a conical bottom, in which the formation of airlift flows in the bioreactor 11, the distribution device 13 is installed. 14 with a product lightening tank 15. As a result of contact with biologically active

The installation according to the second version of the initial product in a finely dispersed suspension (Fig. 2) is equipped with an additional lighting tank, the active development of the bacterial flora takes place, which reaches the optimal concentration by the concentration of the initial product in the finished amount - within a certain time. Based on this, the entrance time, which is about 5-7 minutes. After one flow of finely dispersed suspension into the bioreactor, the required concentration of the screw solution solution is selected, the volume of the bioreactor is selected with the orientation, the extruder is turned off and comes into contact during this time period. This is the process of recirculation of the mixture through the hydrodynamic cavitation mixer from the upper level of the bioreactor 11 (or the finished product through the pipeline 14 into the bubulation apparatus) to obtain a homogeneous product clarification tank 15 for subsequent suspension resistant to stratification . The time of recirculating filling in a transport container. lation is determined by the volume of the dispersant and for

The coarse-dispersed part of the initial product, which is the biologically active phase of an operating installation with a capacity of up to 1 ton of product, can be removed in an hour for 40-45 minutes. It is optimal to convert to bioreactor 11 for re-cultivation of bacterial flora in the bioreactor. It takes 35-40 minutes. Based on this, enter

During the operation of the second version of the installation (Fig. 2), the daily flow of finely dispersed suspension into the bioreactor, which provides a continuous process and the volume of the bioreactor is selected based on a 40-cycle calculation, there is a continuous process of pre-minute contact. In the operating installation, when the fine-dispersed suspension is added and the last flow of the suspension is supplied, the volume of the bioreactor is first in the buffer tank 16, and then by the pump 17 - 0.8 m3. From the upper level of the bioreactor, it is ready for bioreactor 11. During the time that one portion of suspension product is removed through the pipeline in the buffer and processed in bioreactor 11, the disperser 6th tank of product clarification has time to prepare the second portion of the product for the next one. This is pouring into a transport container. Coarse-dispersed allows to combine the process of preparation of flour - part of the initial product can be returned to the co-dispersed suspension and the process of recovery of the bio-bioreactor for reuse. logical flora. Biological fertilizer manufactured according to

From the bioreactor 11, the suspension enters the proposed technical solution, it is a sodium product clarification tank 18, where it fights a finely dispersed stable water suspension that settles for a certain time, which is supplied by balanced compounds of nitrogen, potassium, phosphorus for filling tank 15. After filling the head, trace elements and active bacterial tank 15, the finished product from tank 18 of biohumus flora has already been illuminated. The liquid form of complex fertilizer can be sent to packaging. riva allows to reduce the costs of its introduction,

An example of fertilizer production using the spraying method. In addition,

The raw material for the production of bio-liquid form allows to optimize the dosage of logical fertilizer is biohumus, qualitative and quantitative introduction of fertilizer by diluting the initial composition of which is determined by TUU 3336496.001-94. product with water to the required concentration.

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Ministry of Education and Science of Ukraine

State Department of Intellectual Property, str. Urytskogo, 45, Kyiv, MSP, 03680, Ukraine

SE "Ukrainian Institute of Industrial Property", str. Glazunova, 1, Kyiv - 42, 01601