KR100411804B1 - Wastewater Physical Treatment Device - Google Patents

Abstract

The present invention relates to a wastewater treatment apparatus capable of treating a variety of highly concentrated wastewater, the first decomposition including an ultrasonic wave generator, a microwave generator, a far infrared ray generator, an activation energy reduction device, a perlite electron accelerator in the wastewater treatment equipment facility A reaction tank and a secondary decomposition reaction tank are installed between the settling tanks to decompose and redefine the supernatant introduced from the first settling tank in the first decomposition reaction tank, and in the secondary decomposition reaction tank, dissolved residual organic matter not decomposed in the first decomposition reaction tank. Decomposition of nitrogen compounds, hardly decomposable substances, and stabilization of water molecules for stabilizing the treated water after the removal of suspended solids from the pressure flotation tank are installed. Self-cleaning activator is installed to remove and make active water. Due to the sludge reduction device installed, the hardly decomposable substance can be decomposed in a short time, and the pollution of river water can be prevented by the decomposition treatment of chromatic components of dyeing wastewater and high concentration wastewater, and dissolved inorganic substances, nutrients, It can completely remove colloidal substances, and it can completely remove nutrients such as nitrogen, phosphorus, hardly degradable wastewater such as landfill leachate, livestock wastewater, heavy metal-containing wastewater, which are high concentration wastewater, It is a very useful invention that can reduce the lake and rivers to the natural state where the midnight powers are restored by the discharge of active water.

Description

Wastewater Physical Treatment Unit {.}

The present invention relates to a wastewater treatment apparatus capable of treating a variety of highly concentrated wastewater, and in particular, in the existing wastewater treatment plant by decomposing hardly decomposable substances and nutrients which are not removed by chemical and biological treatment using far infrared rays and physical treatment devices. The present invention relates to a wastewater treatment apparatus capable of preventing secondary pollution of water quality by discharged effluent.

In general, when treating wastewater, large particles of sludge are separated from the pretreatment in the treatment device, that is, in the sedimentation tank using the screening device or the gravity sedimentation method.

Waste water from which sludge of large particles is removed as described above is chemically treated to adjust pH, and then chemically aggregated to separate and collect contaminants (organic substances), and then, activated sludge treatment (aerator) to decompose residual organic matter. )do.

When a proper air is aerated in the wastewater introduced into the aeration tank, as time passes, aerobic microorganisms multiply to form flocs (FLOCs), which cause sedimentation and decomposition of residual organic matter.

The above problems of chemical and biological treatment include, firstly, a pretreatment facility that requires materials harmful to microorganisms, strong acid and strong alkaline waste water; Second, hardly decomposable materials are almost impossible to decompose and require a long residence time even if decomposed; Third, the chromatic components of the dyeing wastewater and the high concentration wastewater cannot be decomposed and removed; Fourth, dissolved inorganic substances, salts, and colloidal substances are impossible to remove; Fifth, in the removal of total nitrogen and total phosphorus, it can be removed to some extent by the long-term aeration method and the denitrification process using anoxic tank, but high concentration wastewater (garbage landfill leachate, livestock wastewater, plating wastewater containing heavy metals) is difficult to decompose. It is demonstrated that there is a technical limitation in the removal of nutrients such as nitrogen, phosphorus and phosphorus.

In addition, although there is a wastewater treatment apparatus using an electron beam accelerator, not only the technical stability has not been verified, but also requires a lot of construction and maintenance costs, and has a problem in that the decomposition treatment efficiency of nitrogen, phosphorus, or hardly decomposable materials is lowered.

In order to solve the above problems, the structural improvement of the wastewater treatment apparatus has to be made urgently, and for this purpose, the wastewater treatment apparatus has been developed.

The present invention devised to solve the above-mentioned disadvantages of the conventional wastewater treatment method, the first wastewater treatment facility comprising an ultrasonic generator, a microwave generator, a far infrared radiation device, an activation energy reduction device, a perlite electron accelerator A secondary decomposition reaction tank and a secondary decomposition reaction tank are installed between the settling tanks so that the supernatant water introduced from the first sedimentation tank is decomposed and reduced in the first decomposition reaction tank, and the dissolved residual organic matter which is not decomposed in the primary decomposition reaction tank in the secondary decomposition reaction tank. Decomposition and nitrogen compounds, hardly decomposable substances, and water molecular decomposition stabilization tank is installed to stabilize the treated water after the removal of suspended solids from the pressure flotation tank, residual hardly decomposable substances and contaminants present in the stabilized decomposed water Self-cleaning activator is installed to remove water and make water into active water. Sludge as been the reduction device laid, first, as in the prior art the raw contaminants and I it is possible to prevent secondary pollution of river water caused by materials decomposable; Second, the physical treatment of wastewater that can reduce lakes and rivers to the natural state where the self-cleaning ability is restored by discharging active water given the self-cleaning ability by providing a substance capable of raising natural self-cleaning ability and activating mineral components. To provide.

1 is a process diagram of the physical treatment of wastewater according to the present invention.

2 is a system diagram of a physical treatment apparatus for wastewater according to the present invention.

Figure 3 is a plan view illustrating the arrangement of the components constituting the primary decomposition reaction tank according to the present invention.

Figure 4 is a cross-sectional configuration of one side of the first decomposition reaction tank according to the present invention.

5 is an exemplary cross-sectional view of FIG. 4 viewed from another direction.

Figure 6 is a cross-sectional configuration of one side of the secondary decomposition reaction tank according to the present invention.

Figure 7 is a side cross-sectional view of the first degassing apparatus according to the present invention.

Figure 8 is a side cross-sectional view of the secondary degassing apparatus according to the present invention.

Figure 9 is a side cross-sectional view showing a water molecular decomposition stabilization adjustment tank according to the present invention.

10 is a perspective configuration diagram of a self-cleaning capacity activation tank according to the present invention.

FIG. 11 is a cross-sectional view taken along the line A-A of FIG. 10; FIG.

Figure 12 is a side cross-sectional view of the sludge reduction apparatus according to the present invention.

※ Explanation of symbols used in the main part of the drawing ※

100: pretreatment unit 200: decomposition treatment unit

210: first decomposition reaction tank 240: second decomposition reaction tank

211,241: Article 212,242: Natural media

213,243 Membrane 214,244 Ultrasonic generator

215,245 Electromagnetic wave generator 216,246 Far infrared ray generator

217,247 Activation energy reduction device 218,248 Perlite electronic accelerator

220: first degassing apparatus 250: second degassing apparatus

221,251 Joe 222,252 Membrane

223,253: ultrasonic wave generator 224,254: electromagnetic wave generator

225,255: far infrared radiation device 226,256: activated energy reduction device

227,257: Perlite Electronic Accelerator 228,258: Decomposition

229,259: rotational aberration 229a, 259a: plate

229b: piston pumps 229c, 259c: baffle plate

229d, 259d: Hole 300: Pressurized injury

400: decomposition recovery processing unit 410: water molecule decomposition stability adjustment tank

411 Joe 412 Membrane

413: Far infrared ray generator 414: Perlite electronic accelerator

420: self-cleaning tank 421: filtering network

422: tourmaline 423: zeolite

424 Germanium 425 Ocher

426: Illite 427: Bio-Ceramic

428 activated carbon 429 collection pipe

429a: pump 500: aftertreatment

550: sludge reduction device 551: tank

552 Membrane 553 ultrasonic generator

554: electromagnetic wave generator 555: far infrared ray generator

556: Activation energy reduction device 557: Perlite electronic acceleration device

558: decomposition processor 559: rotation aberration

559a: plate 559b: hole

559c: baffle plate 559d: monopump

The present invention for achieving the object of the present invention, the pre-treatment unit 100 for the first treatment of the generated wastewater; A decomposition treatment unit 200 for decomposing and redoxing the supernatant treated in the pretreatment unit, atomizing particles, and decomposing dissolved residual organic substances, nitrogen compounds, and hardly decomposable substances; A self-cleaning capacity restoring unit 400 for removing residual hardly decomposable substances and contaminants from the decomposed water and making it active water; It is composed of a post-processing unit 500 to minimize the amount of sludge to cut and decompose the sludge molecules using potential energy.

The pretreatment unit 100 is to remove the sludge of the large particles from the wastewater introduced into the inlet 110, 120 and the fine sand and suspended matter in the wastewater source water treated by the contaminant treatment unit to remove the activated carbon. A flocculant is added to the sedimentation tank 130 and the wastewater introduced from the sedimentation tank to reduce the repulsive force due to electric neutralization, and the particles are largely aggregated to form a floc, and then the dewatering solution is degassed with a centrifuge. It is introduced into the secondary agglomeration reactor 140, a flocculant is formed from the first agglomeration reactor and the centrifuge 150 for dewatering the sludge precipitated in the wastewater source and the first sedimentation tank, and agglomeration in the first agglomeration reactor At the same time, the first sedimentation tank 160 into which the desorption fluid generated while dewatering the sludge sedimented on the bottom of the first sedimentation tank and the sedimentation tank in which the floc is formed is introduced.

Decomposition processing unit 200 for decomposing the wastewater source treated first in the pre-treatment unit, an ultrasonic generator, a microwave generator, a far infrared radiation device, an activation energy reduction device, an electron acceleration device using a perrite electromagnet and a permanent magnet. The first decomposition reactor 210 for decomposing and redoxing the supernatant water introduced from the first settling tank 160 in the pretreatment step and the decomposed treated water in which the decomposition reaction is completed in the first decomposition reaction tank are ultra-fine particles so that the low specific gravity particles are brought into the atmosphere. The first degassing apparatus 220 for releasing and agglomerating the particles having a high specific gravity, and a second agglomeration reactor for aggregating (aggregating) suspended solid particles in the decomposed treated water which has been treated in the first degassing apparatus to increase precipitation efficiency. (260) and the decomposition process raw water in which the conditions for forming the floc in the second flocculation reactor are matured is introduced to form a huge floc. The second sedimentation tank 230 in which the heavy sludge is precipitated, and the supernatant is introduced from the second sedimentation tank to decompose dissolved residual organic substances, nitrogen compounds, and hardly decomposable substances that were not decomposed in the first decomposition reaction tank 210. The second decomposition reactor 240, the second degassing apparatus 250 for degassing ammonia nitrogen dissolved in the decomposed treatment water decomposed in the secondary decomposition reaction tank, and the sludge degassed from the decomposed decomposed treatment water The third flocculation reactor 270 to stabilize, and the sludge which is heavy due to the formation of a huge floc is formed while the decomposition water introduced from the third flocculation reactor stays for about 3 to 5 hours, and the supernatant is pressurized. It consists of a third settling tank 280 to be transferred to the device.

The decomposition treatment water treated in the decomposition treatment unit 200 is subjected to the third process while passing through the self-cleaning capacity restoring unit 400, and the self-cleaning capacity restoring unit 400 is a process in which the removal of suspended solids is completed in the pressure flotation tank 300. Water molecular decomposition stabilization tank 410 for stabilizing the water, and the remaining hard-decomposable substances and contaminants present in the decomposed treated water stabilized in the water molecular decomposition stabilization adjustment tank to remove the self-determination ability to activate the third Blocking the recombination in advance and goes through the activation tank is composed of a self-cleaning capacity activation tank 420 to be combined with the natural media embedded in the tank to make the active water rich in mineral rich self-cleaning ability.

The treated water that has passed through the midnight capacity restoring unit 400 is finally processed by the aftertreatment unit. The aftertreatment unit 500 is not removed by precipitation at the same time the midnight capacity is activated in the midnight capacity activation tank 420. The upstream filtration device 510 for filtration of the decomposed treated water as well as the removal of residual suspended solids in the decomposed water, and the final discharge tank for discharging the decomposed treated water that has passed through the upflow filtration system for a certain period of time for stabilization. 520, and the sludge deposited on the bottom of the first and third settling tank, the sludge molecular link chain has an ultrasonic generator, an electromagnetic wave generator, a far-infrared radiation device, the concentration tank 530 made of an activated energy reducer, The sludge reduction device 550 which cuts and disassembles sludge by rotating aberration, a baffle plate, and a collection tank, and removes the water in the sludge reduced by the sludge reduction device. Which is characterized in that the sludge consisting of the high-pressure dehydrator 560.

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

Referring to Figure 1, the raw water generated in the factory, livestock farm, household, etc. will be treated in the pre-treatment unit (100).

First, coarse contaminants (3 to 5 mm) and sand and seeds are removed from the contaminant treatment unit 120 in the wastewater source introduced through the inlet 110.

In other words, the introduced wastewater is first removed through the rotary screen, and the coarse contaminants are removed, and the removed coarse contaminants are transferred to the screw conveyor and discharged. After the solid-liquid separation using the centrifugal force and specific gravity difference by entering into the cyclone apparatus, the supernatant is introduced into the sedimentation tank 130, and the sediments sedimented at the bottom are introduced into the centrifuge 150 to remove seeds and sand. The desorption liquid separated from the seeds and sand is introduced into the settling tank 130.

The contaminant treatment unit 120 is the most important equipment in the pretreatment unit 100, the wastewater source water from which the coarse contaminants are removed is introduced into the sedimentation tank 130 to remove fine sand, suspended matter.

Wastewater source water introduced into the sedimentation tank 130 from the contaminant treatment unit 120 is settled on the bottom by injecting activated carbon while staying about 1hr to 3hr to cause gravity sedimentation due to the specific gravity difference. Sludge is removed by the transfer to 150, the desorption liquid at this time is introduced into the first settling tank 160, the supernatant is transferred to the first flocculation reaction tank 140, agglomerated by the flocculant and the first settling tank 160 again. Flows into.

The first agglomeration reaction tank 140, the first centrifugation tank 150 and the first sedimentation tank by agglomerating the supernatant water in the sedimentation tank 130 in accordance with the concentration of suspended solids in the wastewater source flowing into the sedimentation tank 130 (160) It acts to inflow into the waste water, it is very stable in the waste water and charges such as positive or negative charge between the charge and it is difficult to settle and precipitate each other, it is added to the ZETA potential such as electrical repulsive force, attraction force, gravity, etc. To reduce the repulsive force by electric neutralization and collide the particles so that the particles agglomerate to each other to form flocs (Floc) to settle and settle the centrifugal separator after aggregating the wastewater source flowing from the sedimentation tank 130. 150 and the first settling tank 160 is introduced.

As described above, the centrifuge 150 for dewatering the sludge is agglomerated in the first flocculation reactor 140 according to the concentration of suspended solids in the wastewater source water introduced from the sedimentation tank 130 to the centrifuge 150. Dewatering sludge deposited on the surface of the incoming wastewater and the first sedimentation tank 160 is a facility to remove the floating fine particles of the floating material floating.

The centrifugal separator 150 tends to fall from the inside to the outside when rotating by high speed rotation. By applying this method, the solids are forcibly transferred to the inner circumferential surface of the perforated horizontal cylinder to separate and dehydrate the solids liquid. It is supposed to be. The cake dehydrated by the second high speed rotation is transferred to the dewatering cake hopper 540 by the conveyor and the desorbing liquid is introduced into the first settling tank 160.

The first settling tank 160 is agglomerated in the first flocculation reaction tank 140, the floc formed wastewater and the desorption liquid generated while dehydrating in the centrifuge 150 is introduced, the secondary flocculation is introduced into the secondary flocculation tank The floc is formed while floc is formed and is settled on the bottom of the first settling tank 160. At this time, the settled sludge is transferred to the centrifuge 150 by a pump and dewatered, and the supernatant is the first decomposition reaction tank 210. The desorbing liquid generated in the centrifuge 150 is recycled and flows into the first settling tank 160.

As described above, the supernatant treated by the pretreatment unit 100 is secondaryly processed by the decomposition treatment unit 200.

The decomposition treatment unit 200 is the first decomposition reaction tank 210, the first degassing apparatus 220, the second precipitation tank 230, the second decomposition reaction tank 240, the second secondary degassing apparatus 250, The second agglomeration reaction tank 260, the third agglomeration reaction tank 270 is composed of.

The supernatant is introduced into the first decomposition reaction tank 210 from the first settling tank 160 of the pretreatment unit 100.

As described above, when the supernatant introduced from the first settling tank 160 is introduced into the first decomposition reaction tank 210, the electromagnetic wave generating device, the far infrared radiation device, the activation energy reduction device, the ferrite electron acceleration device, in particular, the rod type, are placed on the inlet pipe. As the cavitation phenomenon is generated by the pulse energy irradiated by the ultrasonic generator (20Mhz) 214, a large number of bubbles are generated and a synergistic effect of pressure and temperature is generated, generating a large vibration energy, anion oxygen generator (membrane) At 213, it combines with the anion oxygen particles introduced through the aeration device, and a strong redox effect occurs beyond the oxidation of ozone to start decomposition of water molecules.

On the other hand, electrons are actively moved by vibration energy when cavitation occurs in the electromagnetic wave generator, the far-infrared radiation device, the activated energy reduction device, especially the ferrite electron acceleration device (three-radius magnet) 218 installed inside the inflow pipe. Polarization of the electrons by the vibration energy generated by resonance and resonance movement causes the electrons to enter into the tank 211 and gives tremendous disturbance to the propagation angle of the electrons, thereby increasing the bending angle of the electrons. It matures the conditions so that the decomposition rate in (211) can proceed faster.

The physical processing apparatuses installed in the tank 211 of the first decomposition reaction tank 210 are as follows. The first decomposition reaction tank 210 is provided with a physical decomposition treatment device as described below to decompose organic materials, hardly decomposable substances, nitrogen compounds and the like. In the physical decomposition processing apparatus, the ultrasonic wave generator 214, the electromagnetic wave generator 215, the far-infrared radiation device 216, the activation energy reduction device 21, the perlite electromagnetic acceleration device (the device using an electromagnet and a permanent magnet) 218 )) Is installed.

Referring to the function of the devices installed in the first decomposition reaction tank 210 as follows.

The ultrasonic wave generator 214 is installed inside the jaw 211 in the upper (under the water) bottom portion zigzag installation inlet pipe, both sides.

The raw water introduced as described above and introduced into the tank 211 generates huge pulse energy by irradiating sound waves. At this time, an increase in pressure temperature occurs and a negative pressure is generated at the decompression side when the pressure amplitude reaches a positive pressure or more.

Since this negative pressure does not actually exist, a force for dividing the liquid is applied to generate a cavity of the vacuum. These cavities will break down again in the next compression phase at vacuum or near low pressure. At this time, the liquids collide with each other strongly, generating huge shock pressures and strong mechanical disturbances (cavitation cavitation).

When the cavitation occurs, strong oxidation (H2O2, HNO3, HNO2) reduction action occurs to decompose the water molecule linking chain polymerization ring and organic substance hardly decomposable substances, and the anion oxygen supplied from the anion oxygen generator 213 is the OH- ions, which are intermediate products, are produced in large quantities to promote redox reactions in combination with pulsed energy from sound waves irradiated from the ultrasonic generator 214. Accelerate

The electromagnetic wave (microwave) generator 215 is provided as an upper side (more than 8 places) side part (45 degree inclination) of the tank 211.

The electromagnetic wave (microwave 2,450Mhz ~ 5,000Mhz) generator 215 by a plurality of magnetrons is installed on the upper and side surfaces of the tank 211. A huge vibration is generated by the microwaves irradiated from the electromagnetic wave generator 215. The kinetic energy is generated by rapid disturbance and vibration, which accelerates the electrons further to promote the decomposition of the water molecular chain chain, and the electromagnetic wave generators are irradiated across the electromagnetic wave generator by the timer through the feedback control to progress the electrons. In order to increase the vibration width by disturbing the direction, the kinetic energy is converted into thermal energy by the rapid disturbance of the water molecules, and thermal energy, which is a condition in which far infrared rays can be radiated to the natural media 212 installed in a square in the tank 211. It serves to supply the circle.

Far infrared ray (4 ~ 20um) radiation device 216 is installed in a number of squares inside the tank 211.

Far-infrared radiation device 216, the plastic processing of the bio-ceramic + illite, there is a heating wire inside the tubing, the tube is made of stainless steel tube, it is configured so that the far-infrared radiation can be constantly radiated by adopting a temperature sensor.

When power is supplied, the heat generated from the heating wire is transferred to the tube, and the far infrared rays are radiated first from the ceramic coated on the tube, and the far infrared rays are radiated secondly as heat is transferred to the bio-ceramic and illite plastics by radiant heat and heat conduction.

The far-infrared radiation is 4 ~ 20um and the emissivity is over 95%. It breaks down and breaks the water chain linking polymer ring, and the huge vibration occurs by the resonance resonance motion to accelerate the electrons and decomposes the hardly decomposable substance to prevent recombination. Hard-decomposable substances are usually bonded 180 ° by using the atom as a bridge. By making the bond angle densely (30 ~ 40 °), they weaken the binding force and make it impossible to bind. It combines with energy and microwaves to further promote the decomposition of organic compounds and nitrogen compounds.

The activating energy reduction device 217 is installed at the six upper portions of the tank 211 and the four side portions.

The activation energy reduction device 217 was manufactured by using tourmaline, and is a device for reducing decomposition energy to promote decomposition and applying energy to tourmaline using instant back electromotive force between about 1 second and 3 seconds to generate a surface active material. When the counter electromotive force is generated, a voltage of several hundred volts is applied to the tourmaline stone. At this time, the electric energy applied to the tourmaline is heated and the tourmaline is heated to emit the far infrared rays absorbed inside the tourmaline stone.

At this time, the emitted far infrared rays are combined with physical water molecule-linked chain decomposition devices to rapidly accelerate electrons by resonance resonance motion, and further accelerate the decomposition of water-molecule-linked chain polymerization rings and organic materials, nitrogen compounds and hard-decomposable materials. Let's do it.

The counter electromotive force is generated when the current is supplied to the coil, the electromotive force is generated, the electromotive force generated in the coil is always generated only in the opposite direction, that is, the reverse direction of the current supplied from the outside. It is called back electromotive force because current is generated in the reverse direction

Perlite electron accelerator 218 (using electromagnets and three-way permanent magnets) is installed at various points in the center of the inner tank 211 in the side inlet pipe of the tank 211.

The perlite electro-accelerator 218 becomes an electromagnet while generating magnetic force when a current flows through the coil.

In general, electromagnets have an iron core, and coils are wound around the core to increase the strength of the magnet. However, the electroaccelerator 218 using this perlite has an electromagnet formed by inserting a magnetic material called perlite instead of the iron core.

This electromagnet is installed on the side of the tank 211 using direct current and alternating current to bend the direction of movement of the accelerated electrons in the physical decomposition device, causing huge vibrations. Decomposition is accelerated further, in combination with existing physical decomposers to increase the decomposing efficiency.

On the other hand, electromagnets are grouped with three-way permanent magnets and installed in the center of the tank (211) to bend the progress angle of the electrons to promote disassembly, and three-way permanent magnets (5,000 Gaus) form strong magnetic fields in three directions. Disturbing the acceleration and progression cycles of the electrons, especially raw water, which stays about 104hr ~ 24hr depending on the concentration in the tank 211, and decomposes organic materials, nitrogen compounds, and hardly decomposable substances at the same time as the water-molecule link chain polymerization ring is decomposed. .

The raw water treated in the first furnace decomposition reactor 210 is treated again in the tank 221 of the first secondary degassing apparatus 200 having the same devices as the first decomposition furnace described above, and then the first primary degassing apparatus. The high pressure piston pump 229d (80 Kg / cm 2 to 100 Kg / cm 2) of the 220 is suctioned and the pressure that impinges on the rotational aberration 229 as the discharge diameter change is 130 Kg / cm 2 or more and the second obstruction plate 229c. Ultrasonic generator is installed in the suction line, which causes oxidation and reduction reactions once again to decompose water molecule link chain polymerization, residual organic materials and hardly decomposable materials.

As mentioned above, the water molecules are broken into small pieces while colliding with the rotary aberration 229 and the baffle plate 229c, and the atomized particles include residual toxic gases, ammonia nitrogen, nitrogen compounds, and hardly decomposable substances. As the particles collide with each other, the bonding angle between the molecules is ideally combined at 104,5 °, and the particles are densely packed so that ammonia nitrogen, organic hardly decomposable substances, and toxic gases cannot be re-adhered to the water molecule linking chain. The lighter particles are sucked into the exhaust fan installed above the decomposition processor 228 and discharged into the atmosphere. The treated water collected by the lower collection tank 229e is sent to the second agglomeration reactor 260 to stay in the reactor for about 1 hr. Agglomeration reaction is performed to the second and then sent to the second settling tank 230 to be precipitated.

On the bottom of the first decomposition reaction tank 210, a square is formed with a natural filter (ceramic, elite, ocher germanium, zeolite tourmaline), and a cavity phenomenon is generated by pulse energy irradiated from the ultrasonic generator 214. As the temperature rises and heat energy generated by the thermal energy activated energy reduction device 217, which is conducted in the far-infrared radiation device 216, is amplified, it acts as an energy source to the natural media and radiates far infrared rays (4 to 14um). As resonant motion occurs, huge vibration energy is generated, which promotes the decomposition of water molecule link chain polymerization and non-decomposable nitrogen compounds by vibration energy, and is combined with physical decomposition devices to combine water molecule link chain, nitrogen compound, and egg. It acts to increase the decomposition effect of degradable substances, etc.

Particularly, when natural filter media (bioceramic, germanium, elite, ocher, zeolite, activated carbon) and powder filter media were introduced into the primary decomposition reaction tank 210 through a feeder (H +), (OH By dissociating into-), instead of hydrogen ions, the natural media particles combine with (OH-) ions to dehydrogenate (H +) ions and settle by adsorbing nitrogen compounds and hardly decomposable substances. It acts as a catalyst to accelerate the decomposition reaction.

As mentioned above, the first degassing apparatus 220 is introduced into the decomposition treatment water in which the decomposition reaction is completed in the first decomposition reaction tank 210, and a physical treatment device installed in the tank 221, that is, an ultrasonic wave generator ( 223), the electromagnetic wave generator 224, the far infrared ray generator 225, the activating energy reduction device 226, and the like, and the nitrogen molecules, the hardly decomposable substances, the toxic gases, etc. adhered to the water molecule connecting chains. The resonance energy is generated by the resonance energy caused by the pulse ring irradiated from the ultrasonic wave generator 223 and the microwaves irradiated from the electromagnetic wave generator 224 and the far infrared ray radiated from the far infrared ray generator 225. By cutting the molecular link chain polymerization ring, the water molecule link chain polymerization structure is densely bonded (104.5 °), which makes nitrogen compounds, hardly decomposable substances, and toxic gases not re-adhesive.

As can be seen from the physical treatment apparatus, the decomposed treated water in the tank 221 of the first degassing apparatus 220 is sucked by the high pressure piston pump 229d, which is installed on the suction pipe passage. After reprocessing by ultrasonic generator (20Mhz), electromagnetic wave generator, far-infrared radiation device, etc., it is made into fine particles and sucked and discharged by high pressure piston pump 22d. At this time, the pressure is about 80 ~ 130Kg / ㎠ The discharge pressure is increased by changing the injection angle of the nozzle.

On the other hand, the discharged treated water firstly decomposes the water molecules by hitting the rotary aberration 229 and the second obstruction plate 229c to decompose water molecules, toxic gases, nitrogen compounds, and eggs that were previously adhered to the water-molecule linking chain. Suction exhaust pen installed at the top of the decomposition processor 228 without being able to re-adhesive to the water molecule connecting chain because the decomposable substance is ideally bonded at 104.5 °, which is a water molecule bonding angle that cannot be reattached to the water molecule connecting chain. Particles that have been sucked by and lighter in specific gravity are released into the atmosphere, and particles condensed by heavy condensation due to collision with the rotary aberration 229 and the baffle plate 229c aggregate the sludge streams such as nitrogen compounds and non-degradable substances. Remove it.

The decomposed treated water in which the decomposition degassing treatment is completed in the first degassing apparatus 220 flows into the second agglomeration reaction tank 260, and unlike the first agglomeration reaction tank 140, it is decomposed in the first decomposition reaction tank 210. As the treated water passes through the first degassing apparatus 220, the binding angle of the sludge molecules is densified by the activation energy reduction device 226 and the far infrared rays, and the sludge is stabilized early as the activation energy decreases.

The secondary agglomeration reactor 260 is very stable in the waste water, and the charges such as positive or negative charges are charged with each other is difficult to settle by causing a repulsion to each other, such a coagulant is added to the ZETA potential such as electrical repulsive force, gravity, gravity Therefore, the repulsive force caused by electric neutralization is reduced, and particles collide with each other to form a floc (Floc) to precipitate.

In the second flocculation reactor 260, a natural filter powder was used as the coagulant in addition to the flocculant, thereby improving the efficiency of the precipitation tank in the second precipitation tank 230.

Decomposed raw water transferred from the second agglomeration reaction tank 260 and introduced into the second sedimentation tank 230 stays for about 4 hours, and a large floc while staying in the second sedimentation tank 230. Sludge is heavy gravity formed as it is formed is to be settled on the bottom of the secondary sedimentation tank 230, the supernatant is introduced into the secondary decomposition reaction tank 240.

The sludge deposited on the bottom of the second sedimentation tank 230 is transferred to the concentrating tank 530, and the sludge connection chain for sludge reduction by physical processing devices installed in the concentrating tank 530, and the like, destroying cells. The decomposition reaction of starts.

The supernatant water flows into the secondary decomposition reaction tank 240 from the secondary sedimentation tank 230, and the secondary decomposition reaction tank 240 has a decomposition process similar to that of the primary decomposition reaction tank 210. Do.

The secondary decomposition reaction tank 240 decomposes dissolved residual organic substances, nitrogen compounds, and hardly decomposable materials that are not decomposed in the primary decomposition reaction tank 210.

The decomposed treated water introduced into the second decomposition reaction tank 240 is to stay for 24 to 36 hours, and the residence time is longer than that of the first decomposition reaction tank 210.

The secondary decomposition reaction tank 240 has a large number of physical treatment apparatuses in which the far-infrared generator 246 using bioceramic and illite and the activation energy reduction device 247 using tourmaline are 30% or more in the tank 241. It is installed to accelerate the decomposition of water molecule linking chain polymerization ring, nitrogen compound and hardly decomposable substance.

In addition, the anion oxygen supplied from the anion generator (membrane) 243 reacts with the natural filter 242 in the tank 241 and the filter filter supplied from the powder filter injector to increase the amount of dissolved oxygen and promote dehydrogenation. To accelerate the redox reaction.

The difference between the second decomposition reaction tank 240 and the first decomposition reaction tank 210 is far-infrared generator 246 among the physical treatment devices installed in the first decomposition reaction tank 210, and the activation energy reduction device 247 ), More than 30% of the electron acceleration device 248 using the ferrite rod-type electromagnet decomposes the water-molecule linking chain polymerization ring, a hardly decomposable substance, a nitrogen compound, and the like.

The decomposed treated water completed by the second decomposition reaction tank 240 is introduced into the secondary degassing apparatus 250.

The second degassing apparatus 240 is a process of degassing the decomposed treated water introduced after completion of the decomposition treatment in the secondary decomposition reaction tank 240 and has the same function as the first degassing apparatus 220, and the toxic gas ammonia Degassing of the nitrogen.

The second degassing apparatus 250 has the same physical processing apparatus as the first degassing apparatus, and in the second degassing apparatus 250, raw water treated by being decomposed and reacted in the secondary decomposition reaction tank 240 is treated as a third. Degassing and sludge reduction before flowing into the secondary flocculation reactor 270 to decompose the link chains of nitrogen compounds and sludge molecules to make the molecular structure dense and dense so that the nitrogen compounds, toxic gases, etc. adhered to the link chains Is released into the atmosphere, and vibration energy is generated by resonance resonance motion by the physical processing devices and far infrared rays installed inside the tank 251 to destroy the cell walls of the sludge molecules, thereby removing the intracellular moisture. At the same time, it plays a role of maturing conditions that can stabilize the sludge at an early stage. The floc is formed by a flocculating agent while flowing into the reactor 270.

The decomposed treated water in which the first decomposition degassing treatment is completed in the second degassing apparatus 250 flows into the third agglomeration reaction tank 270, and unlike the first agglomeration reaction tank 140, the treated water decomposed in the decomposition reaction tank is treated. Through the degassing device, the activation energy reduction device and the far-infrared radiation reduce the binding angle of the sludge molecules and stabilize the sludge at an early stage while the activation energy decreases.It is very stable in the wastewater to charge the charges such as positive or negative charges. Therefore, it is difficult to settle due to repulsion, and it adds flocculating agent to ZETA potential such as electric repulsive force, attraction force and gravity to reduce the repulsive force by electric neutralization and collide the particles to make the particles aggregate together. It forms and precipitates.

The decomposition treatment raw water treated in the third agglomeration reaction tank 270 is introduced into the third sedimentation tank 280, and the introduced decomposition treatment water stays about 3 hours.

During the stay in the third settled sedimentation tank 280, a large floc is formed, and the heavy sludge becomes sedimented on the bottom surface, and the supernatant flows into the pressure flotation device 300, and the sludge on the bottom surface is mono Decomposition reaction such as cutting of sludge connecting chain for sludge reduction and breaking of cells is started by the physical processing apparatuses transferred to the concentration tank 530 by the pump and installed in the concentration tank 530. At this time, the supernatant is transferred to the pressure flotation device (300).

The supernatant flows from the third settling tank 280 into the pressurized flotation tank, and attaches a myriad of bubbles to the solids to lower the specific gravity to float to the upper side. When atmospheric pressure is reached, oxygen is released by the pressure difference. After saturating the air through the aeration under atmospheric pressure, it is released to the flotation tank to float and remove the floating material. The treated water from which the floating material is removed from the pressurization tank 300 is introduced into the water molecular decomposition stabilization adjustment tank 410.

The supernatant flowed into the primary from the pressurized flotation device 300 is to stay at about 8 hrs in the water molecular decomposition stabilization tank 410. In the tank 411 of the water molecule decomposition stabilization adjustment tank 410, a far infrared ray generator 413 In addition to the electron acceleration device 414 using a ferrite electromagnet, the bottom of the tank 411 is provided with physical processing devices and anion generating device (membrane) (412).

Powder natural media (ocher, germanium, ceramics, zeolites) and the like are introduced into the tank 411 of the water molecular decomposition stability adjusting tank 410 to stabilize the treated water.

The far-infrared ray (4 ~ 20㎛) emitted from the far-infrared generator 413 decomposes the residual organic substance and the hardly decomposable substance, and the chain chain polymerization of molecules. It will be adsorbed and settle on the bottom.

At this time, the bonding angle is ideally densely coupled to 104.5 ° in which organic and hardly decomposable substances cannot be recombined in the water-molecule linking chain ring, thereby reducing the load of the subsequent process. Meanwhile, an electron accelerator using a ferrite electromagnet The magnetic field formed at 414 causes the electrons to be polarized, resulting in tremendous disturbances as the electrons accelerate, further accelerating the decomposition of the molecules.

The water molecules are sedimented on the bottom surface by the particles of the powder filter media instead of H + ions by the powder filters introduced into the water molecular decomposition stability adjusting tank 410 and the anionic oxygen supplied from the negative ion generator 412.

In particular, the anion oxygen supplied from the anion generator 412 can be over-aerated, so that the dissolved oxygen in the tank 411 can be adjusted to be maintained at 10 or more to stabilize the water molecules early to reduce the load of subsequent processes.

In addition, the treated water in which the stabilization of the molecules is completed in the water molecular decomposition stabilization adjustment tank 410 is introduced into the self-cleaning capacity activation tank 420.

The treated water in which the stabilization of the molecules is completed in the water molecular decomposition stabilization tank 410 is introduced into the self-cleaning capacity activation tank 420, the residual hardly decomposable substance present in the decomposed treated water flows in the self-cleaning capacity activation tank 420 It completely removes contaminants and activates the self-cleaning ability to block the recombination with the third hardly decomposable substance in advance, and the mineral-rich self-cleaning ability is combined with the natural media embedded during the self-cleaning activating tank 420. It is made with improved active water.

The self-cleaning capacity activation tank 420 is divided into several sections so as to pass the decomposition treatment water in several stages to make the active water, and the tourmaline stone 422 while going upward from the filter network (strainer) 421 formed therein. ), Zeolite 423, germanium 424, ocher 425, illite 426, bio-ceramic 427, and activated carbon 428 are stacked in this order, and the bottom of the section forming a layer as described above. A collection pipe 429 is formed to collect the active water passing through the inside, and is configured as a pump 429a to the collection pipe 429 to transfer the active water collected to the collection pipe 429 to the next step, The natural media (bioceramic, elite, germanium, ocher, zeolite, activated carbon) is activated at mid stage through the multi-step.

Decomposed water after several steps of the self-cleaning capacity activation tank 420 is converted to water having excellent self-cleaning ability to act as a catalyst for activating the self-cleaning ability when discharged in lakes and rivers. The decomposed treated water given the midnight power in the midnight power activation tank 420 is introduced into the upflow filtration device 510.

In the self-cleaning capacity activating tank 420, the decomposed treated water having completed the activation of the self-cleaning capacity passes through the upflow filtration device 510 to remove the residual suspended solids, and the shape of the influent is very diverse and the solid load of the influent changes frequently. It was applied to remove fine particles that were not removed by precipitation. Decomposed treated water passing through the upflow filtration device 510 is introduced into the final discharge tank (520).

The decomposed treated water passing through the upflow filtration device 510 is stabilized while staying in the final discharge tank 520 for a predetermined time and then discharged.

The thickening tank 530 serves to cut and decompose the sludge connection chain loop using far-infrared rays and a physical treatment device while introducing and storing sludge deposited on the bottoms of the second and third sedimentation tanks 230 and 280. Joe, the thickening tank 530 is already well known technology, so a detailed description will be omitted.

The sludge introduced into the thickening tank 530 is processed by the sludge reduction apparatus 550. The sludge reducing apparatus 550 is collected in the center as a device for reducing the sludge introduced into the thickening tank 530. Membrane 552 is installed to blow the anion into the bottom of the tank 511 forming the inclined surface to activate the decomposed water, and the water molecules are irradiated with water waves on the bottom and the top of the tank 551 and irradiated with water. An ultrasonic generator 553 is provided to decompose the linking chain polymerization ring and the organic material hardly decomposable substance. A plurality of ultrasonic wave generators are formed at a predetermined inclined angle to the upper part of the ultrasonic generator 553 and are interposed between molecules by irradiation of electromagnetic waves. An electromagnetic wave generating device 554 is provided, which causes rapid disturbance and vibration to promote decomposition of the water-molecule linking chain polymerization ring, and has a rectangular shape at the top of the tank 551. The water chain is decomposed by the far-infrared rays which are emitted and radiated.The huge vibration is generated by the resonance resonance motion to accelerate the electrons, and to prevent the recombination of the hardly decomposable materials and prevent them from recombining. By making the bonding angle densely (30 ~ 40 °), it weakens the bonding force and makes the conditions impossible to combine. In particular, it combines with the pulse energy of the ultrasonic wave and microwave to promote the decomposition of organic compounds such as nitrogen compounds. 555 is installed, and a plurality of them are disposed above the tank 551 and emit instantaneous electromotive force to radiate far infrared rays by the generated thermal energy, thereby physically linking the polymer chain and the organic material, nitrogen compound, and hardly decomposable. Activation energy reducer to accelerate the decomposition of materials Activation energy reduction device 556 made of tourmaline is installed, which accelerates electrons by resonance resonance motion in combination with the chisels and further accelerates the decomposition of water molecule-linked chain polymerization ring and organic substance nitrogen compound hardly decomposable substance. Inserting a coil into a magnetic ferrite material to pass a current through this coil to become an electromagnet to form a triangular band, consisting of a single body is installed in the center of the tank 551 and combined with the above-described water molecule decomposing devices to resolve the decomposition of water molecules. A perlite electron accelerator 557 for accelerating is provided, and the decomposed treated water atomized in the tank 551 is sucked out by the mono pump 559d and has a plate 559a having a plurality of perforated holes 559b. Ultra-fine atomization against the aberration plate 559c, which firstly struck the rotation aberration 559, and zigzag-installed on the deodorization facility transport path second Decomposition processor (558e) consisting of a collection tank (559e), which decomposes toxic gases, nitrogen compounds, and hardly decomposable substances adhering to the polymerization chain of water molecules, and releases lighter particles into the atmosphere and collects heavy particles. ), The sludge deposited on the bottom surface of the first to the third settling tank is pumped into the facility consisting of the concentration tank 530 and the sludge reduction device 560, and then the physical treatment device (ultrasonic generator, electromagnetic wave). Combined with systems consisting of generators, far-infrared radiation devices, and activated energy reduction devices), the decomposition and vibration energy of the sludge molecular linking chain penetrates into the cell and breaks down the cell wall to escape the intracellular moisture and cytoplasm while staying about 6HR to 16HR. To make the bond angle of the sludge molecules dense, Such that purging is done to give the composition the best condition to be given to enhance the agglomeration efficiency in the flocculation reaction tank significantly improve the dewatering efficiency (50 ± 5%) in a high pressure dewatering device.

The sludges transferred from the settling tank stay at least 8HR-16HR in the thickening tank 530, and the decomposition and vibration energy of the sludge molecules penetrate into the cell and destroy the cell membrane by the physical processing devices installed in the thickening tank 530 to destroy the intracellular moisture and cytoplasm. By making it escape, it creates conditions to increase the dehydration efficiency due to the decrease of the water content of sludge and to stabilize the sludge at an early stage.The physical device (ultrasound) which establishes the conditions for improving the water content of the sludge and stabilizing the sludge at an early stage. Decomposition and cutting are performed by the generator, the electromagnetic wave generator, the far-infrared radiation device, and the activated energy reduction device. The sludge that has been decomposed is introduced into the high-pressure sludge dewatering facility (560) to reduce the volume of the cake hopper ( It is caked by 540 and the wastewater treatment is completed.

As described above, in the wastewater treatment apparatus according to the present invention, the sludge of the large particles from the generated wastewater is first treated by the pretreatment unit 100, and the ultrasonic wave generator and the treated water treated by the pretreatment unit in the tank. Decomposition processing unit consisting of the first and second decomposition powder coagulation unit and the first and the second degassing device consisting of electromagnetic wave generation device, far-infrared radiation device, activated energy reduction device, perlite electron accelerator, cloth filter, anion generator (membrane) After the secondary reaction by the decomposition reaction in the 200, and the third step in the self-cleaning capacity recovery processing unit 400 consisting of the water molecule stability adjustment tank and the self-cleaning capacity activation tank after the decomposition treatment water treated in the decomposition processing unit 200, sludge reduction apparatus It is possible to complete the treatment in the after-treatment unit having a, which can decompose the hardly decomposable material in a short time, and remains by decomposing the chromatic components of dyeing wastewater and high concentration wastewater. It can prevent contamination of river water by the discharge of degradable materials, and can completely remove dissolved inorganic materials, salts, and colloidal materials, and leachate from landfill leachate, livestock wastewater and heavy metal-plated wastewater which are high concentration wastewater. It has the effect of completely removing nutrients such as hardly degradable wastewater, nitrogen and phosphorus.

By completely removing the secondary pollution, it is a very useful invention that can not only increase the natural self-cleaning ability, but also reduce the lake and river to the natural state by the discharge of active water.

Claims (8)

A sediment treatment unit 120 for removing large particles of sludge from the wastewater introduced into the raw water inlet 110, and an immersion tank 130 for removing fine sand and suspended matter in the wastewater source water treated by the contaminant treatment unit by adding activated carbon and flocculant. ), And a first flocculation reactor (140) in which a coagulant is added to the wastewater source introduced from the sedimentation tank to reduce the repulsive force due to electrical neutralization and the particles are largely aggregated to precipitate, and the wastewater source is introduced into the centrifuge and the first precipitation tank (140). ), And the centrifuge 150 for dewatering the wastewater introduced from the first flocculation reactor and the sludge settled in the first sedimentation tank, and the dehydrated in the flocculation wastewater and the centrifuge, in which the flocculation is flocculated in the first flocculation reactor. The wastewater source water is primarily processed by the pretreatment unit 100 including the first settling tank 160 into which the generated desorption liquid flows; First decomposition that consists of ultrasonic generator, microwave generator, far-infrared generator, activation energy reduction device, electron acceleration device using perrite electromagnet and permanent magnet to deoxidize and reduce supernatant water flowing from the first settling tank 160 in the pretreatment stage. The first degassing apparatus 220 for ultra-atomizing the decomposition treatment water in which the decomposition reaction is completed in the first decomposition reaction tank and releasing particles with low specific gravity into the atmosphere and agglomerated and removing the specific gravity particles with the reactor 210, and The second flocculation reactor 260 which aggregates (flocculates) the suspended solids in the decomposed treated water by the first degassing unit to increase the settling efficiency, and the conditions under which flocs may be formed in the second flocculation reactor. The second settling tank 230 and a second settling tank, in which mature sludge treated raw water is introduced and a large floc is formed to precipitate sludge with heavy gravity. The second decomposition reaction tank 240 decomposes dissolved residual organic substances, nitrogen compounds, and hardly decomposable substances which have not been decomposed in the first decomposition reaction tank 210 due to the inflow of water, and the decomposed treatment water decomposed in the secondary decomposition reaction tank. A second degassing apparatus 250 for degassing ammonia nitrogen, a third flocculation reactor 270 for stabilizing the sludge degassed from the cracked degassed decomposed treated water, and the raw water decomposed from the third flocculation reactor Sludge is formed by a large floc (heavy floc) is formed while staying for about 3 to 5 hours, the supernatant is secondary treatment in the decomposition treatment unit 200 consisting of a third settling tank 280 to transfer to the pressure flotation apparatus; Water molecular decomposition stabilization adjustment tank 410 for stabilizing the treated water in which the floating material is removed in the pressure flotation tank 300, and residual hardly decomposable substances and contaminants present in the decomposition treatment water stabilized in the water molecule decomposition stabilization adjustment tank. To activate the self-cleaning ability to remove the third hardly decomposable substance and recombination in advance, and to combine with the natural media contained in the tank to make the mineral-rich active water with enhanced self-cleaning ability. It is the third process while going through the self-cleaning capacity recovery processing unit 400 made of 420; At the same time, the activation of the self-cleaning capacity in the self-cleaning capacity activating tank 420 removes the residual suspended solids of the decomposed treated water which is not removed by sedimentation, as well as the upward filtration device 510 for discharging the decomposed processed water, and the upflow filtration The final discharge tank 520 is discharged after stabilizing the decomposed treated water that has passed through the facility for a certain time, and the sludge deposited on the bottom of the first and third sedimentation tanks is stored in an ultrasonic generator, A sludge reduction device 550 having a concentration tank 530 formed of an electromagnetic wave generator, a far infrared ray generator, and an activated energy reducer, which is a rotary aberration, a baffle plate, and a collection tank to cut and decompose sludge, and the sludge reduced in the sludge reduction device. Physical treatment device for wastewater, characterized in that consisting of a post-treatment unit 500 consisting of a high pressure sludge dehydrator (560) for dehydrating water. According to claim 1, wherein the primary decomposition reaction tank 210, the bottom surface of the tank 211 forming the inclined surface collected in the center of the plurality of natural media 212 and far-infrared radiation is blown anion between the decomposition treatment water Membrane 213 to activate the is installed, The ultrasonic generator 214 is disposed on the side wall, bottom, and top of the bath 211 to irradiate sound waves to decompose the water molecule connecting chain polymerization ring and the organic material hardly decomposable material. At the same time, it is installed on the upper side of the adjacent sidewall of the ultrasonic generator 214 at a predetermined inclination angle, and at the same time, it is installed on the upper side, which causes rapid disturbance and vibration between molecules by irradiation of electromagnetic waves, thereby facilitating decomposition of the chain of water molecule chains. Electromagnetic wave generator 215 for generating conditions under which far-infrared rays can be radiated from the natural media 212 installed in a square inside the tank 211 by converting kinetic energy generated by rapid disturbance of water molecules into heat energy. Installed, Decomposition of the water-molecule link chain polymerized by the far-infrared rays installed in a rectangular shape on the top of the tank 211, and a huge vibration occurs by the resonance resonance movement to accelerate the electrons, decompose the hard-decomposable material to recombine It makes it impossible to bond by weakening the bonding force by making the bonding angle of hardly decomposable material (30 ~ 40 °) densely by using hydrogen atom as a bridge. Especially, it is combined with ultrasonic pulse energy and microwave Far-infrared ray generator 216 is installed to accelerate the decomposition of substance nitrogen compounds. The plurality of tanks 211 is disposed above, and emits far-infrared rays by thermal energy generated by generating instant back electromotive force to promote the decomposition of the physical water molecule connection chain polymerization ring and organic materials, nitrogen compounds, hard-decomposable materials The activation energy reducing device 217 is combined with the decomposing devices to generate a ringing phenomenon due to resonance resonance movement, thereby rapidly accelerating electrons and further promoting the decomposition of the water molecule linking chain polymerization ring and organic nitrogen compound hardly decomposable substances. Activated energy reduction device 217 manufactured by the installation is installed, Inserting a coil into a magnetic ferrite body, which becomes an electromagnet by passing AC and DC currents to the coil, which forms a triangular band and crosses the central side of the tank 211 and is installed in a single body. And a perlite electron accelerator 218 for accelerating electrons by polarizing water molecules by a magnetic field formed in the electron accelerator. According to claim 1, The secondary decomposition reaction tank 240, the bottom surface of the tank 241 forming the inclined surface collected in the center of the plurality of natural media 242 and far-infrared radiation is blown anion between the decomposition treatment water Membrane (243) for activating is installed, The ultrasonic generator 244 is disposed on the side wall, bottom, and top of the bath 241 to irradiate sound waves to decompose the water molecule connecting chain polymerization ring and the organic material hardly decomposable material. At the same time, it is installed on the upper side of the adjacent sidewall of the ultrasonic generator 244 at a predetermined inclination angle, and at the same time, it is installed on the upper side, which causes rapid disturbance and vibration between molecules by irradiation of electromagnetic waves, thereby facilitating decomposition of the chain of water molecule chains. Electromagnetic wave generator 245 for generating conditions under which far-infrared rays can be radiated from the natural media 212 installed in a square inside the tank 241 by converting kinetic energy generated by rapid disturbance of water molecules into heat energy. Installed, Decomposes the water-molecule connection chain polymerization ring by the far-infrared rays radiated from the upper part of the tank 241, and a huge vibration is caused by the ringing phenomenon generated by the resonance resonance movement to accelerate the electrons, non-degradable material Prevents recombination by decomposing ions, makes the bonding angle of hardly decomposable materials densely (30-40 °) by using hydrogen atoms as a bridge, weakens the binding force and makes it impossible to bind. And a far infrared ray generator 246, which is combined with microwaves and promotes decomposition of organic substances, nitrogen compounds, etc., A plurality of tanks are arranged on the upper part of the tank 241, which generates instant back electromotive force to radiate far infrared rays by the generated thermal energy, thereby promoting physical water molecule connection chain polymerization and decomposition of organic materials, nitrogen compounds, and hardly decomposable materials. Activated energy abatement device 247 is combined with decomposers to generate ringing by resonance resonance motion to rapidly accelerate electrons and further accelerate the decomposition of water molecule link chain polymerization and organic nitrogen compounds. Activation energy reduction device 247 is manufactured is installed, Inserting a coil into a magnetic ferrite material to pass a current through this coil to become an electromagnet to form a triangular band and consists of a single body is installed in the center of the tank 241, in combination with the water molecule decomposition devices described above in the electron accelerator Physical treatment device for wastewater, characterized in that consisting of a perlite electron accelerator (248) to accelerate the electrons by polarizing the water molecules by the magnetic field formed. According to claim 1, The first degassing device 220, a membrane 222 for activating the decomposition treatment water by blowing negative ions in the bottom of the tank 221 forming the inclined surface collected in the center is provided, The ultrasonic generator 223 is disposed on the bottom and top of the bath 221 to irradiate sound waves to decompose the water molecule connection chain polymerization ring and the organic material hardly decomposable material. Electromagnetic wave generator 224 is installed to form a plurality of inclined angles in the upper portion adjacent to the ultrasonic wave generator 223, which causes rapid disturbance and vibration between molecules by irradiation of electromagnetic waves, thereby facilitating decomposition of the water-molecule link chain polymerization ring. It is, Decomposition of the water-molecule connecting chain polymerization ring by the far-infrared radiation installed and installed in the upper part of the tank 221, the ringing phenomenon is generated by the resonance resonance movement to accelerate the electrons and accelerate the hard-decomposable material It prevents recombination and recombination, and makes the bonding angle of hardly decomposable material densely (30 ~ 40 °) by using hydrogen atom as a bridge, weakens the coupling force and makes it impossible to combine. In combination there is a far-infrared ray generator 225 for promoting the decomposition of organic substances nitrogen compounds, etc., The plural number is disposed above the tank 221 and generates instantaneous back electromotive force to radiate far infrared rays by the generated heat energy, thereby activating physical water molecule connection chain polymerization ring and decomposition of organic material, nitrogen compound, and hardly decomposable material. Activated energy made of tourmaline, which combines with decomposing devices to accelerate electrons rapidly by ringing phenomena generated by resonance resonant motion and further accelerates the decomposition of water molecule link chain polymerization and organic nitrogen compounds. An abatement device 226 is installed, The coil is inserted into a magnetic ferrite material, and an electric current is applied to the coil to form a triangular band, which consists of a single body, is installed in the center of the tank, and is matched with the above-described water molecule decomposing devices to produce water by a magnetic field formed in the electron accelerator. A perlite electron accelerator 227 is installed to polarize molecules to accelerate electrons, The decomposed treated water atomized in the tank 221 is sucked and discharged by the piston pump 229d, and the degassing facility transfer path is driven secondly to the rotary aberration 229 having the plate 229a having the plurality of holes 229b. The microparticles are crushed on the blockage plate (229c) installed in a zigzag on the top to cut the chains of toxic gas, nitrogen compound, and hardly decomposable substance that adhered to the water-molecule linking chain. Physical treatment apparatus for wastewater, characterized in that composed of a decomposition processor 228 consisting of a water collecting tank (229e) is a collection of heavy particles. According to claim 1, The second degassing apparatus 250, a membrane 252 for activating the decomposition treatment water by blowing negative ions are provided on the bottom of the tank 251 forming the inclined surface collected in the center, The ultrasonic generator 253 is disposed on the bottom and top of the tank 251 to irradiate sound waves to decompose the water molecule connecting chain polymerization ring and the organic material hardly decomposable material. A plurality of electromagnetic wave generators 254 are installed to form a predetermined inclination angle to the upper portion adjacent to the ultrasonic wave generator 253 to cause rapid disturbances and vibrations between molecules by irradiation of electromagnetic waves, thereby promoting decomposition of the water-molecule link chain polymerization ring. It is, Decomposition of the water-molecule connection chain polymerization ring by the far-infrared rays installed and installed in the upper portion of the tank 251, the ringing phenomenon is generated by the resonance resonance movement to accelerate the electrons and accelerate the hard-decomposable material It prevents recombination and recombination, and makes the bonding angle of hardly decomposable material densely (30 ~ 40 °) by using hydrogen atom as a bridge, weakens the coupling force and makes it impossible to combine. In combination there is a far-infrared ray generator 255 that facilitates the decomposition of organic compounds, nitrogen compounds, etc., The plural number is disposed above the tank 251 and generates instant back electromotive force to radiate far infrared rays by the generated thermal energy to promote physical water molecule connection chain polymerization ring and decomposition of organic material, nitrogen compound, and hardly decomposable material. Activated energy made of tourmaline, which combines with decomposing devices to accelerate electrons rapidly by ringing phenomena generated by resonance resonant motion and further accelerates the decomposition of water molecule link chain polymerization and organic nitrogen compounds. An abatement device 256 is installed, The coil is inserted into a magnetic ferrite material, and an electric current is applied to the coil to form a triangular band, which consists of a single body, is installed in the center of the tank, and is matched with the above-described water molecule decomposing devices to produce water by a magnetic field formed in the electron accelerator. A perlite electron accelerator 257 is installed to polarize molecules to accelerate electrons, The decomposed treatment water atomized in the tank 251 is suction-discharged by the piston pump 259d, and the deodorization facility transport path is driven on the second aberration 259 having a plate 259a having a plurality of holes 259b. Ultra-fine particles are squeezed onto the zigzag block (259c) on the top to decompose toxic gases, nitrogen compounds, and hardly decomposable substances adhering to the polymerization chain of water molecules. At the same time, lighter particles are released into the atmosphere and heavy specific gravity is released. Physical treatment apparatus for waste water, characterized in that consisting of a decomposition treatment unit (258) consisting of a collecting tank (259e) in which particles are collected. The method of claim 1, wherein the water molecular decomposition stabilization adjustment tank 410, the powder natural media (ocher, germanium, A plurality of membranes (anion generators) 412 for stabilizing the decomposed treated water into which ceramics, zeolites, etc. are introduced, Rectangle is installed in the upper portion of the tank 411 to decompose the link chain polymerization ring of the molecules of the residual organic material and hardly decomposable, and at the same time, a portion of the powder natural filter material is adsorbed with the residual organic material and the hardly decomposable material to precipitate on the bottom surface. At this time, the bonding angle is 104.5 °, which is impossible to recombine organic material and hardly decomposable material to the water molecule linking chain, ideally densely coupled to reduce the load of the subsequent process far infrared (4 ~ 20㎛) It has a far-infrared radiation device 413 that radiates, By forming a magnetic field formed in the electron accelerator using a perlite electromagnet, the electrons are polarized, causing a great disturbance according to the acceleration of the electrons. Processing equipment According to claim 1, wherein the self-cleaning capacity activation tank 420 is divided into a number of sections so as to make the active water by passing the decomposed treated water stabilized molecules in several stages from the water molecular decomposition stabilization adjustment tank 410 into The tourmaline 422, zeolite 423, germanium 424, loess 425, illite 426, bio ceramics 427, and activated carbon 428 while moving upward from the formed filter net (strainer) 421. ) Are stacked in this order, and a collection pipe 429 is formed at the bottom of which collection of the active water passing through the inside of the layered section is carried out, and the active water collected in the collection pipe 429 is transferred to the next step. Physical treatment apparatus for wastewater, characterized in that the pump (429a) is installed in the collection pipe (429). According to claim 1, The sludge reduction apparatus 550 is a device for reducing the sludge first introduced into the thickening tank 530, the negative ion is blown to the bottom surface of the tank 511 forming the inclined surface collected in the center decomposition treatment Membrane 552 is installed to activate the water, The ultrasonic generator 553 is disposed on the bottom and top of the tank 551 to irradiate sound waves to decompose water-molecule-linked chain polymerization rings and organic material hardly decomposable materials. A plurality of electromagnetic wave generators 554 are installed to form an inclined angle in the upper portion of the ultrasonic generator 553 in close proximity to each other, thereby causing rapid disturbance and vibration between the molecules by irradiation of electromagnetic waves, thereby facilitating the decomposition of the water-molecule link chain polymerization ring. It is, Decomposition of the water-molecule connection chain polymerization ring by the far-infrared rays installed and installed in the upper part of the tank 551, ringing phenomenon is generated by the resonance resonance movement to accelerate the electrons and decompose the hardly decomposable substance Prevents recombination, and makes the bond angle of hardly decomposable material densely (30 ~ 40 °) by using hydrogen atom as a bridge, weakens the bond force and makes it impossible to bond. Especially, it is combined with ultrasonic pulse energy and microwave Far-infrared ray generator 555 is installed to accelerate the decomposition of organic substances, nitrogen compounds, etc. A plurality of tanks are arranged on top of the tank 551, and instantaneous electromotive force is generated to radiate far-infrared rays by heat energy generated, thereby promoting physical water molecule connection chain polymerization and decomposition of organic materials, nitrogen compounds, and hardly decomposable materials. Activated energy made of tourmaline, which combines with decomposing devices to accelerate electrons rapidly by ringing phenomena generated by resonance resonant motion and further accelerates the decomposition of water molecule link chain polymerization and organic nitrogen compounds. An abatement device 556 is installed, The coil is inserted into a magnetic ferrite material, and the current flows through the coil to become an electromagnet. The triangular band is formed into a single body and is installed in the center of the tank 551. The water molecule decomposing device is formed in the electron accelerator. A perlite electron accelerator 557 is installed to polarize water molecules by a magnetic field to accelerate electrons. The deaerated water in the tank 551 is suctioned and discharged by the monopump 559d to primarily face the rotational aberration 559 having the plate 559a having a plurality of holes 559b, and the second degassing facility transfer path The microparticles are crushed on the zigzag block (559c) installed on the top to decompose toxic gases, nitrogen compounds, and hardly decomposable substances adhering to the water-molecule linking chain, and light particles are released into the atmosphere. Physical treatment apparatus of wastewater, characterized in that consisting of a decomposition processor 558 consisting of a collecting tank (559e) in which heavy particles are collected