KR100407473B1 - A disposal method for stoch rasing waste water availing leaf mould and apparatus therefor - Google Patents

Abstract

The present invention relates to a method for treating livestock wastewater and its apparatus,

Wastewater treatment system consists of high speed separator, vibrating screen tank, aeration tank, circulation circuit drop tank, sand gravel filter, jet (Z) magnetization reaction tank, low temperature plasma reactor, substitution stone reaction, carbon filter tank and discharge water tank. By adding the coarse soil, the aerobic and anaerobic properties of the coarse soil maximize the purification effect while minimizing the cost, and easy to maintain, without the risk of secondary environmental pollution, eliminating harmful insects, and purifying It is possible to produce fertilizer so that it can make big economic profit.

Description

A disposal method for stoch rasing waste water availing leaf mold and apparatus therefor}

The present invention relates to a method for purifying livestock wastewater and a device therefor, in particular, to maximize the removal of odor and sterilization effect by inputting the foliar soil during purification, as well as by configuring a purification device with a high-speed separator, vibrating screen, circulation circuit dropping tank, etc. Livestock wastewater treatment method and apparatus using flounder soil, which can minimize the cost by purifying wastewater, and are easy to maintain and excellent in purifying action, and can produce high-quality fertilizer during the purification process, which can bring economic benefits. It is about.

In recent years, serious environmental pollution is caused by various wastewater discharged from livestock farms, etc., which is a serious social problem.

Therefore, a method for purifying livestock wastewater using a chemical treatment method or an activated sludge treatment method is widely used.

However, conventional livestock wastewater treatment methods such as chemical treatment methods and activated sludge treatment methods are expensive and have a high economic burden, are difficult to maintain, and may cause secondary pollution by chemical substances. As the purification effect is greatly different depending on the temperature, there is a problem that the purification effect is lowered.

The present invention has been made to solve the above problems,

The wastewater treatment system consists of a high-speed separator, a vibrating screen tank, an aeration tank, a circulation circuit drop tank, and a sand gravel filter. By adding wastewood through the wastewater, it maximizes the purification cost by maximizing the purification effect by the aerobic and anaerobic properties of the soil. Livestock wastewater treatment method using foliar soil that can minimize economics, maintain easy, have no secondary pollution, eliminate harmful insects, produce high quality fertilizer and produce economical fertilizer. And an apparatus thereof.

1 is a schematic view showing a livestock wastewater treatment apparatus of the present invention.

Figure 2 is a cross-sectional view showing a high speed separator of the livestock wastewater treatment apparatus of the present invention.

Figure 3 is a sectional view showing a vibrating screen tank of the present invention livestock wastewater treatment apparatus.

Figure 4 is a perspective view showing an aeration tank of the livestock wastewater treatment apparatus of the present invention.

5 is a cross-sectional view showing a circulation circuit drop tank of the livestock wastewater treatment apparatus of the present invention.

Figure 6 is a cross-sectional view showing a sand gravel filter of the livestock wastewater treatment apparatus of the present invention.

7 is a cross-sectional view showing a Z-type magnetization reaction tank of the livestock wastewater treatment apparatus of the present invention.

8 is an overall configuration diagram showing a low temperature plasma reaction tank of the livestock wastewater treatment apparatus of the present invention.

9 is a cross-sectional view showing the flow of wastewater and oxygen in the low temperature plasma reaction tank of the livestock wastewater treatment apparatus of the present invention.

<Explanation of symbols for the main parts of the drawings>

1: collection tank 2: high speed separator

3: primary vibrating screen tank 4: aeration tank

5: secondary vibration screen tank 6: circulation circuit drop tank

7: aeration tank 8: stabilization tank

9: sand gravel filter 10: jet (Z) shaped magnetization reactor

11: low temperature plasma reactor 12: substitution stone reaction and carbon filter tank

13: discharge tank

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

1 is a schematic view showing a livestock wastewater treatment apparatus of the present invention.

The present invention comprises the steps of collecting the wastewater in the sump (1) and adding the subleaf soil to it;

Separating the wastewater into water molecules and sludge with a high speed separator (2);

Removing sludge of about 0.09 mm or more of the sludge not separated in the high speed separator by the primary vibrating screen 3;

Generating a wavelength between the water molecules by the aeration tank 4 and causing the movement;

Separating fine sludge having a size of about 0.03 to 0.05 mm out of the water molecules and foreign substances dissolved in the aeration tank with a secondary vibrating screen (5);

Applying self-cleaning force and pressurization to the wastewater by a circulation circuit dropping tank (6), so as to generate a strong drop due to pressurization, and finely separating the water molecules and each molecule to relax the water molecules and suspended solids;

Amplifying the oxygen content in the water molecules dissolved in the aeration tank (7) to increase the self-cleaning force and at the same time completely releasing fine residual suspended matter from the linkages of the water molecules;

Separating the fine residual suspended matters separated from the aeration tank by causing the homogeneous suspended matters to precipitate or float by the specific gravity difference with the water molecules in the stabilization tank 8;

Passing through the sand gravel filter tank 9 further enhances the self-cleaning force in the water molecules and once again filtering the suspended particles;

Passing a jet (Z) shaped localization reactor (10) to apply a strong hydraulic pressure to promote water deflection (hexagonal water) by magnetic force and to remove iron-like substances;

Removing and sterilizing malignant substances, odors, and residual colors by introducing deuterium into the treatment gas using the low temperature plasma reactor 11;

Substituted stone reaction and carbon filter tank substituted stone and carbon to satisfy the minerals (germanium, sodium, calcium, magnesium, helium, etc.) in the water quality, and to remove residual toxic color.

A wastewater treatment apparatus for treating wastewater in the same manner as described above includes a water collecting tank 1, a high speed separator 2, a primary vibrating screen tank 3, an aeration tank 4, a secondary vibrating screen tank 5, and circulation. Circuit free fall tank (6), aeration tank (7), stabilizer (8), sand gravel filter (9), Z type magnetization reaction tank (10), low temperature plasma reaction tank (11), substitution stone reaction and carbon filter tank (12) , But configured to connect the discharge tank 13,

As shown in FIG. 2, the high speed separator 2 has a screw 18, which is rotated by the rotation of the rotary shaft 17, which is rotated by the motor 21, inside the cylindrical network 19, and has a waterproof tube at the lower side thereof. (24) is installed, on one side is installed waste water inlet pipe 15 is provided with a control valve 14, the other side is configured by installing the sludge discharge port 23 in the direction of the conveyor (22).

Reference numeral 16 in the drawings is a bearing.

As shown in FIG. 3, the vibration screens 3 and 5 are provided with a wastewater inlet pipe 27 having a control valve 25 and a sump 26 installed thereon, and overlapping a plurality of vibration screens 28 up and down. Spaced apart installation, and fixed to the spring 29 to install the installation installed vibrating screen 28, the motor 31 is installed in the lower portion to allow a plurality of vibrating screen 28 to flow, vibrating screen 28 installation Consists of connecting the waterproof tube 30 to the lower portion of the.

Reference numeral 32 in the drawings is a conveyor.

The aeration tanks 4 and 7 constitute an aeration tank body 37 in which a plurality of diffusers 39 in which a plurality of aeration stones 38 are protruded, as shown in FIG. 4, constitute an air compressor 33 and an air pressure gauge. (35), the air supply pipe 36 in which the air tank 34 is installed is configured by connecting with a plurality of electric diffusers (39).

The circulation circuit drop tank 6 is provided with a waste water inlet 40 at the lower side, a pressurized water pump 41 and a motor 43 at the outer upper portion, and a plurality of magnets 42 therein. It is configured to install the injector 44 on the inner upper surface.

As shown in FIG. 6, the sand gravel filter 9 is provided with a wastewater inlet pipe 45 at an upper portion thereof, and a fine powder layer 46 and a gravel layer 47 from an upper portion in a main body on a body having a discharge tube 50 installed at a lower portion thereof. ), The sand layer 48, and the subfloor layer 49 is laminated.

The jet (Z) magnetization reaction tank 10 is bent in a zigzag shape at 90 ° angle to the pipe body in which the wastewater inlet pipe 51 is formed at one side as shown in FIG. 7, and a plurality of magnets 52 are installed therein. And it is configured by filling the gravel (53).

The low temperature plasma reactor 11 is as shown in FIG.

The low-temperature plasma reactor 11 is a low-temperature plasma medium oxygen in which a compressor 54, an air tank 55, a plurality of air filters 56, 58, 60, air dryers 57, and air coolers 59 are connected. The generator 61 is connected to the discharge pipe 62, and the oxygen-generating capacity of the oxygen-oxygener is determined by the preliminary test results according to the amount and property of each wastewater.

A plurality of unit reaction tanks 70, each of which has an oxygen oxygen pipe 66 installed therein, are connected to each other by a stepped discharge pipe opening passage 67, and an upper portion of each unit reaction tank 70 has a medium oxygen inlet pipe 64 and The surplus oxygen on one side is re-injected into the drainage water of the wastewater inlet pipe of the first unit reactor through the surplus filter tube, and the surplus oxygen is connected to be treated through the final deuterium discharge pipe in which the treatment filter 69 is installed. The unit reactor 70 is configured by connecting the wastewater inlet pipe 63 to the upper portion and the discharge pipe 68 to the lower portion.

Hereinafter, the operation of the present invention.

In order to purify the raw wastewater, it is collected in the sump tank (1), and the subleaf soil is put into it, and the sludge and water molecules are connected by activating by the aerobic and anaerobic characteristics of the wastewater under any adverse conditions, climate, and temperature by the intrinsic characteristics of the subleaf soil. It breaks the ring and removes ammonia gas and odors.

In this way, the wastewater activated by the collection tank 1 and the ammonia gas and odors are removed is introduced into the inner cylindrical network 19 through the wastewater inlet pipe 15 of the high speed separator 2 and the cylindrical network is a high speed motor ( Since the liquid is rotated at high speed by the operation of 21), the liquid flows out through the through hole of the cylindrical network by centrifugal force and flows out to the waterproof tube 24 at the lower side, and the sludge discharge port is controlled by the motor rotation speed of the screw according to the amount of sludge. It is conveyed to 23 and discharged, which is conveyed by the conveyor 22.

The sludge selected here is automatically transported to the collecting place by the conveyor 22, and the organic fertilizer (compost) of the excellent quality from which the odor has already been removed by the foliar soil is produced.

Wastewater flowing out through the waterproof tube 24 of the high-speed separator 2 is collected in the collecting tank 26 of the primary vibrating screen tank 3 again, and the vibrating screen 28 located at the top through the wastewater inflow pipe 27. Will be dropped in.

The wastewater dropped on the uppermost vibrating screen 28 is dropped onto the conveyor 32 on the inclined surface sludged by the inclined vibrating screen 28, and only the liquid passes sequentially through the vibrating screen 28 to provide a lower water resistance. It flows out through the pipe.

The operation of the vibrating screen tank 3 is possible by vibrating the vibrating screen 28 installed in the inclined shape so as to flow into the spring 29 and by the operation of the motor 31.

In addition, the vibrating screen 28 is a plurality of stacked is installed in order to filter the sludge particles of 0.09mm, 0.04mm, 0.01mm size from the top side.

The wastewater waterproofed from the primary vibrating screen tank 3 flows into the main body 37 of the aeration tank 4 to supply air from the air tank 34 to the diffuser 39 by the operation of the air compressor 33. High-pressure injection into a large number of protruding aeration stones (38) causes the wavelength between the molecules to move, thereby increasing the oxygen demand in the water and unstable ionization of various floating components to break the cohesion between each molecule and molecules.

Water molecules and various foreign matters disintegrated in the aeration tank 4 are again subjected to the same operation as the first vibration screen tank 3, which was passed through the second vibration screen tank 5, again, fine sludge having a size of 0.03 mm to 0.05 mm. The separated sludge is collected at the sludge outlet.

Wastewater that has passed through the secondary vibrating screen tank (5) flows into the wastewater inlet (40) of the circulation circuit dropping tank (6) and is raised by the operation of the motor (43) and the pressure pump (41), and the injector (44) therein. As it is high pressure spraying, it meets abundant oxygen demand by applying unbalanced magnetic force in circular circuit and finely decomposes water molecules and molecules by powerful drop by press and at the same time by material change by electromagnetic energy. It loosens water molecules and suspended solids by causing dissociation reactions between water molecules and slowing cohesion between small and large molecules of water.

In this case, since the side leaf component contained in the waste water is made to be more stable, it will act as a catalyst to be completely separated in the next aeration tank (7).

The wastewater passing through the free fall tank (6) of the circulation circuit is fed back into the aeration tank (7) and amplifies the oxygen content in the water molecules dissolved by the same operation as the aeration tank (4). The fine residual suspended matter is finally aerated to completely relax at the linkage of water molecules, and the foliated soil contained in the wastewater is actively purged by abundant free oxygen.

Wastewater passing through the aeration tank (7) is a fine residual suspended matter in the stabilization tank (8) due to the difference in specific gravity with water molecules, homogeneous suspended solids are aggregated, precipitated or floated to separate, where the stable water is odor and sterilized The fine wastewater, which is close to the atomic water with tack and separated in the stabilization tank 8, is reduced to the original wastewater.

Wastewater that has passed through the stabilization tank (8) is introduced into the interior through the wastewater inlet pipe (45) of the sand gravel filter (9), and the fine layer (46), the gravel layer (47), the sand layer (48), and the sublayer soil layer (49). Since it is passed through the discharge tube 50 in order to sequentially, to enhance the self-cleaning force to the water molecules, and once again to filter the suspended solids and to promote the activity of the flounder soil and at the same time to impose a water component.

The wastewater discharged through the discharge tube 50 of the stabilizer tank 8 flows into the wastewater input tube 51 of the jet Z-shaped magnetization reaction tank 10 and is provided with a plurality of magnets 52 and gravel 53 installed therein. ) Through strong water pressure, it promotes water decay (hexagonal water) by magnetic force and finally removes iron foreign substances.

Wastewater that has passed through the jet (Z) -shaped magnetization reaction tank 10 is introduced into the waste water inlet tube 63 of the low temperature plasma reactor 11, and the compressor 54 and the air tank 55 as shown in FIG. , Malignant substances and odors present in the wastewater by receiving the oxygen generated from the low temperature plasma oxygen generator 61 connected to the air filters 56, 58, 60, the air dryer 57, and the air cooler 59. It is then removed and sterilized to completely remove the residual chromaticity.

Here, the wastewater is introduced through the wastewater inlet pipe 63 connected to one side of the unit reaction tank 70 as illustrated in FIG. 9, and circulates the plurality of unit reaction tanks 70 through the pipe opening passage 67 and then discharges the pipe ( 68) is discharged to the unit reaction tank 70 through the oxygen oxygen feed pipe 64 at the same time is supplied to the wastewater through the oxygen oxygen acid pipe 66, the remaining oxygen is supplied to the waste water and remaining acid It is discharged from each unit reactor 70 through the small discharge pipe 65 is discharged to the outside through the excess deuterium treatment filter.

As such, the wastewater that has passed through the low temperature plasma reaction tank 11 is introduced into the substitution stone reaction and the carbon filter tank 12, and the minerals in the water quality (germanium, sodium, calcium, magnesium, and yeast) are replaced by the substitution stones (macbanite, zeolite) and carbon. Etc.), to remove residual toxic chromaticity, and the purified effluent does not cause any secondary pollution, but rather has a self-cleaning power to purify other contaminated water.

Hereinafter, the efficacy and components of the sidelobe soil added in purifying wastewater in the present invention will be described.

GSO-BIO (GSO-BIO) is a special bio ingredient that occurs when a high temperature of 130 ℃ or higher occurs on the surface of the volcano or earth, and it has the characteristics of coexisting with aerobic and anaerobic characteristics. By doing so, it is possible to improve water quality, remove odor, and sterilize smoothly.

Moreover, the high quality organic fertilizers and liquid fertilizers, which have no odor obtained by using 100% pure natural ingredients, without any chemical treatment, can not only improve acidified soils to neutral or alkaline soils, but also save enormous expenses. It is even more meaningful to improve and preserve it as soft soil for excellent crop cultivation.

In addition, foliar soil is more active than any bio-active and grows rapidly, and it is a product that has been aged for a certain period of time by mixing grains, vegetables, wood, fallen leaves, sawdust, etc., which are easily obtained around us. Direct testing has been confirmed by the relevant authorities.

As a result of spraying such foliar soil on our soil, after 7 days, the ammonia gas and odor were already removed, and the pests such as flies and mosquitoes were almost eliminated. COD 272,000, BOD The value of 96,690 PPM dropped to COD 148,000 and BOD 58,600 PPM, and in one month, the effect decreased to 6,700 COD and 5,600 POD BOD.

As described above, the present invention constitutes a wastewater treatment device with a high-speed separator, a vibrating screen tank, an aeration tank, a circulation circuit drop tank, a sand gravel filter, and adds the subleaf soil while passing the wastewater therethrough, thereby purifying the effect by the aerobic and anaerobic properties of the leaflet soil. While minimizing the cost, minimizing maintenance, easy to maintain, there is no risk of secondary environmental pollution, it is possible to get rid of harmful insects, clean up and produce high-quality fertilizer, which can bring big economic benefits. .

Claims (2)

Collecting the wastewater in the sump (1) and adding the subleaf soil to it; Separating the wastewater into water molecules and sludge with a high speed separator (2); Removing sludge having a diameter larger than 0.09 mm among sludges not separated in the high-speed separator by the primary vibrating screen 3; Generating a wavelength between the water molecules by the aeration tank 4 and causing the movement; Separating fine sludge having a diameter of 0.03 to 0.05 mm among water molecules and foreign matters disintegrated in the aeration tank by the secondary vibrating screen (5); Applying self-cleaning force and pressurization to the wastewater by a circulation circuit dropping tank (6), so as to generate a strong drop due to pressurization, and finely separating the water molecules and each molecule to relax the water molecules and suspended solids; Amplifying the oxygen content in the water molecules dissolved in the aeration tank (7) to increase the self-cleaning force and at the same time completely releasing fine residual suspended matter from the linkages of the water molecules; Separating the fine residual suspended matters separated from the aeration tank by causing the homogeneous suspended matters to precipitate or float by the specific gravity difference with the water molecules in the stabilization tank 8; Passing through the sand gravel filter tank 9 further enhances the self-cleaning force to the water molecules and once again filtering the suspended matter; Passing a jet (Z) -shaped magnetization reaction tank (10) to apply strong hydraulic pressure to promote water deflection (hexagonal water) by magnetic force and to remove iron-like substances; Using a low temperature plasma reaction tank (11) to remove and sterilize malignant substances, odors, and residual colors by adding oxygen to treated water; Substitutive stone reaction and livestock using carbonaceous water to satisfy the minerals (germanium, sodium, calcium, magnesium, and helium) content in the water quality by substituting stones and carbon, and removing residual toxic chromaticity. Wastewater treatment method. Collection tank (1), high speed separator (2), primary vibrating screen tank (3), aeration tank (4), secondary vibrating screen tank (5), circulation circuit drop tank (6), aeration tank (7), stabilizer tank ( 8), sand gravel filter (9), Z-type magnetization reaction tank (10), low temperature plasma reaction tank (11), substitution stone reaction and carbon filter tank (12), discharge water tank (13), The high speed separator 2 has a screw 18, which is rotated by the rotation of the rotary shaft 17 rotated by the motor 21, in the cylindrical network 19, and a waterproof tube 24 is installed at the lower side thereof. On one side, the waste water inlet pipe 15 is provided with a control valve 14, the other side is configured by installing the sludge outlet 23 in the direction of the conveyor 22, The vibrating screen (3) (5) is installed in the waste water inlet pipe 27, the control valve 25 and the sump (26) is installed on the top, and installed a plurality of vibrating screens 28 overlapping the top and bottom, the vibration screen Fixing the installation (28) is installed to flow by the spring 29, the motor 31 is installed in the lower portion to allow a plurality of vibration screen 28 to flow, the waterproof tube (below the installation of the vibration screen 28) 30) to connect and configure, The aeration tanks 4 and 7 constitute an aeration tank body 37 provided with a plurality of diffusers 39 protruding from a plurality of aeration stones 38, and include an air compressor 33, an air pressure gauge 35, and an air tank. It is configured to connect the air supply pipe (36) (34) is installed with a plurality of diffusers (39), The circulation circuit drop tank 6 is provided with a waste water inlet 40 at the lower side, a pressurized water pump 41 and a motor 43 at the outer upper portion, and a plurality of magnets 42 are installed inside the inner upper surface. Injector 44 is installed in the configuration, The sand gravel filter 9 is provided with a wastewater inlet pipe 45 at an upper portion thereof, and a fine layer 46, a gravel layer 47, and a sand layer 48 from the upper portion in a main body on the body provided with a discharge tube 50 at a lower portion thereof. , Stacking the sublayer soil layer (49), Jet (Z) -shaped magnetization reaction tank 10 is bent in a zigzag shape pipe body formed with wastewater inlet pipe 51 on one side at a 90 ° angle, a plurality of magnets 52 are installed inside, gravel 53 Charge to configure The low-temperature plasma reactor 11 is a low-temperature plasma medium oxygen in which a compressor 54, an air tank 55, a plurality of air filters 56, 58, 60, air dryers 57, and air coolers 59 are connected. It is configured to be connected to the generator 61 and the discharge pipe 62, A plurality of unit reaction tanks 70, each of which has an oxygen oxygen pipe 66 installed therein, are connected to each other by a stepped discharge pipe opening passage 67, and an upper portion of each unit reaction tank 70 has a medium oxygen inlet pipe 64 and The remaining heavy oxygen discharge pipe (65) is installed on one side of the excess oxygen treatment filter 69, the wastewater inlet pipe (63) is connected to the upper portion of the unit reaction tank (70) on one side and the discharge pipe (68) on the lower side. Livestock wastewater treatment apparatus using a foliar soil characterized in that configured by connecting.