JP3616922B2 - Liquid processing apparatus and liquid processing system having the same - Google Patents

Description

[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a liquid processing apparatus and a liquid processing system having the same, and in particular, can efficiently perform subdivision and charging of various substances such as liquid molecules and colloidal particles contained in treated water. The present invention relates to a liquid processing apparatus and a liquid processing system having the same.
[0002]
[Prior art]
Conventionally, methods and systems have been proposed for purifying livestock wastewater containing manure such as cattle and pigs, or industrial wastewater containing chemical substances such as washing liquid and factory waste liquid.
[0003]
Such a conventional liquid treatment system will be described by taking pig farm wastewater treatment as an example. A conventional water treatment system for pig farm wastewater and the like includes a filtration treatment means for passing raw water through a screen or the like to remove solid suspended matters. Activated sludge treatment means for decomposing water-soluble organic substances by aerobic microorganisms, precipitation decomposition treatment means for precipitating water-soluble organic substances separated from raw water by this decomposition and separating into water and precipitates, And dehydrating means for dehydrating and removing water from the precipitate.
[0004]
More specifically, each of the processing means will be described. In the filtration processing means, when the raw water containing solid suspended matter such as manure passes through the screen, the suspended matter is captured by the screen and removed. The raw water from which the suspended matter has been removed is once stored in a storage tank, then transferred to a metering tank, and flows into an activated sludge treatment tank as activated sludge treatment means for each amount of water that can be treated with activated sludge. In this activated sludge treatment tank, aerobic microorganisms biodegrade water-soluble organic substances such as nitrogen in raw water. The raw water biodegraded by this treatment means is sent to a precipitation tank as a precipitation decomposition treatment means. In this precipitation tank, water-soluble organic substances are precipitated at the bottom of the precipitation tank and separated from the water. After being discharged into a river or the like, the precipitate is transferred to a dehydrating means. In this dehydration processing means, it is dehydrated by a dehydrator to be a solid and discharged.
[0005]
Here, in the conventional water treatment system, in order to avoid enlarging the site and construction costs due to the increase in the size of the activated sludge treatment tank, the dehydrator washing water flows into the storage tank. It was.
[0006]
Therefore, because the washing water of the dehydrator dilutes so-called high-concentration raw water having a high organic matter load, the burden of aerobic microorganisms on organic matter decomposition in the activated sludge treatment means is reduced.
[0007]
However, in the conventional water treatment system, the high-concentration raw water cannot be sufficiently diluted with only the washing water of the dehydrator, and a larger amount of water is required. In addition, if the amount of raw water dilution increases, the amount of water to be purified increases, resulting in an increase in the size of the water treatment facility, resulting in initial costs such as construction costs and power consumption fees and water for liquid treatment. There has been a problem that running costs such as fees increase.
[0008]
In addition, when biological treatment of high-concentration sewage is performed, maintenance is difficult, and once the treatment system breaks down, it takes several months to recover. As a result, there was a risk of environmental pollution.
[0009]
In order to deal with such problems, a treatment method has been proposed in which chemicals such as a polymer flocculant are used to chemically agglomerate and separate high molecular organic substances in raw water to reduce the concentration. However, there is a problem that it is difficult to follow a change in concentration and the like because the setting of the type and dosage of the drug with respect to the concentration of the organic substance is delicate.
[0010]
In view of these problems, the present inventor has already been able to reduce the size of the liquid processing equipment to reduce the initial cost and the running cost, and to perform water-soluble organic matters and microorganisms in the liquid by a simple operation. Has been developed and applied for a liquid processing method, a liquid processing apparatus, and a liquid processing system capable of reliably removing water, and capable of performing deodorization, decolorization, sterilization, liquid subdivision processing, and oxidation-reduction processing. Are disclosed in Japanese Patent Application Laid-Open No. 11-90420 and Japanese Patent Application Laid-Open No. 2000-263056.
[0011]
Here, in the invention disclosed in the above-mentioned two publications, a mixer tube used in the liquid subdividing process is described.
[0012]
This mixer pipe is configured so that the liquid can be subdivided and charged when the mixer is applied to the treated water flowing in the pipe, and as shown in FIG. A neodymium plate 91 of about 10,000 Gauss is arranged in the part, and a neodymium fin 93 made of a ceramic material in which a neodymium magnet 92 having a magnetic force of about 11000 Gauss is embedded is arranged in the pipe 90. And the said neodymium fin 93 is formed by the flat plate twisted helically, and the neodymium magnet 92 is the width direction edge part of a fin along the direction through which treated water distribute | circulates, in order of "NNSSNNNSS ...". It is configured to be buried alternately.
[0013]
Then, when the treated water is circulated in the mixer tube thus configured, the liquid molecules in the treated water are subdivided and charged to negative electrons by the magnetic field of the neodymium plate 91 and the action of the mixer of the neodymium fin 93 ( And the colloidal particles of the dissolved substance in the treated water can be subdivided and charged to positive electrons to be aligned, respectively. By this subdivision and charging, the subdivision charging process of the liquid processing in the liquid processing apparatus In the subsequent process, which is a process for separating fine liquid molecules and colloidal particles, it is possible to efficiently perform the process.
[0014]
[Problems to be solved by the invention]
As described above, the liquid processing apparatus that realizes the liquid processing method and the liquid processing system developed by the present inventor solves the problems of the previous apparatus, but as a further concern, In accordance with the properties of the floating molecules of the liquid flowing through the liquid, an appropriate subdivided charging process is performed flexibly.
[0015]
Therefore, the present invention improves the structure of the subdivision charging means for the filth in the treated water including the mixer pipe used for the subdivision charging process, and is suitable for the subdivision charging process according to the properties of the treated water flowing in the mixer pipe. It is an object of the present invention to provide a liquid processing apparatus capable of performing the above.
[0016]
[Means for Solving the Problems]
In order to achieve the above-mentioned object, a feature of the liquid processing apparatus according to claim 1 of the present invention is that a fin formed in a spiral shape along the longitudinal direction of the cylindrical pipe is provided in the circumferential direction in the cylindrical pipe. A mixer tube that is rotatably arranged and in which the N-pole and S-pole magnets are alternately embedded along the spiral direction in the fin, and the magnet embedded in the fin outside the mixer tube An electromagnet capable of applying a rotational force to the fin by applying a magnetic field, and generating an electromotive force in the mixer tube by rotating the fin in the magnetic field of the electromagnet. The liquid molecules and the suspended matter molecules are charged and aligned by acting on the liquid subdivided by the mixer tube, and the electric current is selected according to the properties of the liquid. The stones in that it is capable inverting the magnetic field applied to the magnet of the fin.
[0017]
And, by adopting such a configuration, for example, depending on the properties of the liquid such as the polarity (positive or negative) of ions of suspended matter molecules such as colloidal particles contained in the liquid, the electromagnet causes the fin magnet to The direction of rotation of the fins can be reversed by reversing the applied magnetic field, so that the charge state of the suspended matter molecules can be unified, and the liquid can be subdivided appropriately and flexibly according to the properties of the liquid. Can do.
[0018]
The liquid processing apparatus according to claim 2 is characterized in that, in claim 1, the strength of the magnetic field applied to the fin magnet by the electromagnet can be varied according to the properties of the liquid.
[0019]
Further, by adopting such a configuration, it is possible to perform a more appropriate subdivision charging process according to the properties of the liquid such as the concentration of suspended matter molecules contained in the liquid.
[0020]
The liquid processing system according to claim 3 of the present invention is characterized in that the subdivided charging means includes fins formed in a spiral shape along the longitudinal direction of the cylindrical pipe in the circumferential direction. A mixer tube in which N-pole and S-pole magnets are alternately embedded in each fin along the spiral direction, and a magnet embedded in the fin outside the mixer tube. An electromagnet capable of applying a rotational force to the fin by applying a magnetic field, and generating an electromotive force in the mixer tube by rotating the fin in a magnetic field generated by the electromagnet. The liquid molecules and the suspended matter molecules are charged and aligned by acting on the liquid subdivided by the mixer tube, and the electric current is selected according to the properties of the liquid. The stones in that it is capable inverting the magnetic field applied to the magnet of the fin.
[0021]
And by adopting such a configuration, the rotation direction of the fin is reversed by reversing the magnetic field applied to the magnet of the fin by the electromagnet according to the properties of the liquid such as the polarity of ions in the liquid, for example. Therefore, according to the properties of the liquid, the liquid can be subdivided appropriately and flexibly, and as a result, the liquid processing effect throughout the system can be improved.
[0022]
A feature of the liquid processing system according to claim 4 is that, in claim 3, the strength of the magnetic field applied to the magnet of the fin can be varied by the electromagnet according to the property of the liquid.
[0023]
And by adopting such a configuration, it is possible to perform a more appropriate subdivision charging process according to the properties of the liquid such as the concentration of suspended matter molecules contained in the liquid, and a more effective liquid throughout the liquid processing system. Can be used for purification.
[0024]
[0025]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of a liquid processing apparatus 70 according to the present invention will be described with reference to FIGS. 1 to 4.
[0026]
As shown in FIGS. 1 and 2, the liquid processing apparatus 70 in this embodiment has a mixer tube 71. The mixer pipe 71 has a cylindrical pipe 72 made of ceramics or resin as a main body. On the inner surface of the cylindrical pipe 72, N-pole neodymium magnets 73a and S-pole neodymium magnets 73b are alternately arranged. The rows of the two neodymium magnets 73 arranged in this manner are buried flush with the inner surface of the cylindrical pipe 72 so that the opposite polarities are opposed to each other. In the present embodiment, as shown in FIG. 4, the row of the neodymium magnets 73 is embedded in the vertical position inside the cylindrical pipe 72, and the neodymium magnet 73 has a magnetic force of about 10,000 Gauss. And
[0027]
Further, in the cylindrical pipe 72, a neodymium fin 75 made of a ceramic material having a neodymium magnet 74 having a magnetic force of about 11000 Gauss embedded in its surface is rotatably arranged in the circumferential direction.
[0028]
The neodymium fin 75 acts on the treated water flowing through the cylindrical pipe 72 as a stirring fin. Specifically, in the present embodiment, the neodymium fin 75 includes a flat plate twisted in a spiral shape in the mixer pipe. Two types of fins, a first fin 75a formed to rotate in the clockwise direction in response to the flow of the liquid flowing through the second fin 75b formed to rotate in the counterclockwise direction, The cylindrical pipes 72 are alternately arranged in the axial direction. As described above, the first fin 75a and the second fin 75b in which the rotation directions of the neodymium fin 75 are opposite to each other are alternately arranged, so that the treatment water can be stirred more efficiently, and the liquid The liquid molecules and suspended matter inside can be subdivided effectively.
[0029]
As shown in FIG. 4, the first fin 75a and the second fin 75b are alternately arranged with N-pole neodymium magnets 74a and S-pole neodymium magnets 74b along the liquid flow direction. Buried.
[0030]
A pair of electromagnets 100 for applying a magnetic field to the neodymium magnets 74a and 74b of the pair of neodymium fins 75 disposed in the mixer tube 71 are provided outside the mixer tube 71. It arrange | positions so that the pipe | tube 71 may be pinched | interposed so that it may mutually oppose.
[0031]
Accordingly, a magnetic force, which is a repulsive force or an attractive force, can be applied to the neodymium magnets 74a and 74b by the magnetic field of the electromagnet 100, so that the neodymium fin 75 can be rotated in the circumferential direction by this magnetic force. ing.
[0032]
Thus, when the neodymium fin 75 rotates in the circumferential direction, the number of magnetic flux linkages penetrating the neodymium fin 75 among the magnetic fluxes between the pair of electromagnets 100 changes abruptly. Due to the change, an induced electromotive force is generated in the neodymium fin 75.
[0033]
Due to the influence of this electromotive force, the liquid molecules subdivided by the rotation of the neodymium fin 75 are charged as negative ions, and suspended matter molecules such as colloidal particles are charged as positive ions or negative ions. It has become.
[0034]
Note that the polarity of the charge of the floating molecule depends on the direction of the electromotive force generated by the neodymium fin 75.
[0035]
Here, in the industrial waste water etc. produced | generated especially as a liquid, the thing which has a positive ion and the thing which has a negative ion are mixed as a floating substance molecule surrounding a water molecule, but this floating substance If the polarities of the molecular ions are not uniform, it is difficult to perform subsequent agglomeration separation efficiently. However, in this embodiment, the neodymium fin 75 can be used to uniformly charge floating molecules to either positive or negative charges. Water molecules are negatively charged.
[0036]
Therefore, in the present embodiment, it is possible to improve the efficiency of the agglomeration separation subsequent to the subdivision charging process by the mixer tube 71 and the electromagnet 100.
[0037]
Furthermore, in this embodiment, the electromagnet 100 reverses the magnetic field applied to the neodymium fin 75 according to the properties of the liquid such as the polarity of suspended matter molecules.
[0038]
When the magnetic field is reversed, the neodymium fin 75 switches its rotation in the direction opposite to the original rotation direction, and thus the direction of the electromotive force generated by the neodymium fin 75 is switched in the opposite direction to the original by switching this rotation. It is like that.
[0039]
When this electromotive force is switched, the charge polarity of the suspended molecule can be reversed.
[0040]
For this reason, for example, because there are many positive ions in the suspended matter, what applied the electromotive force in the direction to uniformly charge the suspended matter molecules to positive ions, By switching the electromotive force generated by the neodymium fin 75 by the reversal of the magnetic field, the suspended matter can be uniformly charged to negative ions.
[0041]
Accordingly, it is possible to flexibly perform an appropriate subdividing charging process according to the properties of the liquid.
[0042]
In the present embodiment, the electromagnet 100 can change the strength of the magnetic field applied to the neodymium fin 75 according to the ion concentration of suspended matter molecules contained in the liquid.
[0043]
As a result, even when the ion concentration of suspended matter molecules is low, an effective electromotive force can be obtained by increasing the strength of the magnetic field, and the subdivision charging process can be performed appropriately.
[0044]
Furthermore, an automatic control unit 101 that controls the magnetic field of the electromagnet is connected to the electromagnet.
[0045]
The automatic control unit 101 is connected to a sensor 102 that measures the polarity of ions in the treated water and the concentration of suspended matter molecules in real time. The sensor 102, for example, makes a pair of electrodes (not shown) contact the treated water and automatically detects the property of the liquid based on a current value or an electric resistance value flowing between the electrodes. It may be.
[0046]
As described above, if the automatic control unit can automatically control the magnetization of the electromagnet based on the properties of the liquid, it is possible to further improve the efficiency of the subdivision charging process.
[0047]
Furthermore, since the electromotive force generated by the electromagnet 100 and the neodymium fin 75 acts on microorganisms, bacteria, etc. in the treated water to kill them or suppress their growth, the liquid can be further purified. It can be done properly.
[0048]
In addition, the arrangement | positioning position and arrangement | positioning number of the sensor 102 mentioned above can be variously changed according to a design concept, For example, the said sensor is mentioned later for storing the raw | natural water supplied to the said mixer pipe | tube 71. You may make it arrange | position to the raw | natural water tank 16, the 1st aggregation process tank 26 etc. which are mentioned later.
[0049]
Next, a specific example of a liquid processing system using the mixer tube 71 having the above-described effect will be shown, and the operation and effect of the mixer tube 71 of this embodiment will be further described.
[0050]
FIG. 5 shows a specific example of the liquid processing system, and filtration processing means 1 for removing solid suspended solids having a large specific gravity from raw water including urine of pigs with a screen, etc., and raw water still turbid after filtration A first separation processing means 2 for oscillating microwaves of electromagnetic waves to separate the colloidal particles from the liquid molecules, and a low-frequency ultrasonic wave is oscillated in the raw water after the separation. First aggregation processing means 3 for aggregating and dispersing the particles from the liquid molecules, and subdivided charging processing means 4 for charging and aligning the liquid molecules and the colloidal particles in the raw water while being subdivided by being mixed in a magnetic field. And a second separation processing means 5 for oscillating microwaves of electromagnetic waves again into the subdivided and charge-aligned treated water to separate into fine colloidal particles and liquid molecules, The deodorizing treatment means 6 for oscillating high-frequency electromagnetic ultrasonic waves in the treated water after separation to remove bad odors from the treated water, and low-frequency ultrasonic waves in the treated water after the deodorizing treatment are oscillated. Second aggregating treatment means 7 for aggregating the colloidal particles and dispersing them from the liquid molecules, and applying high voltage pulses to the treated water to separate and remove nitrogen from the treated water and generate ozone. High-voltage pulse processing means 8 for performing decolorization and sterilization of treated water, and aggregate discharge treatment means 9 for adsorbing and discharging aggregates containing metal substances such as heavy metals of the colloidal particles by magnetic force; Liquid molecule fragmentation treatment means 10 for generating activated water obtained by further refining and activating liquid molecules, also called clusters, by the action of a magnetic field, and oxidizing treated water ionized by charging treatment An oxidation-reduction treatment means 11 for returning to a stable state by an original reaction, a dehydration treatment means 12 for dehydrating the precipitate made of the colloidal particles, and each treatment means are connected to control each treatment operation. Centralized control means 13 for this purpose.
[0051]
More specifically, each of the means will be described. As shown in FIG. 5, the filtration means 1 is for discharging a filter 14 such as a screen or a filter for filtering raw water, and a suspended matter after filtration. 2 and a raw water tank 16 for storing raw water after filtration.
[0052]
The filtration means 1 passes the raw water through the filter body 14 to filter out the solid suspended matter that has already separated from the water and suspended in the raw water, and discharges it to the residue receiving unit 15. It is like that. The raw water filtered by the filter body 14 is once stored in the raw water tank 16 and then transferred by the raw water transfer pump 17 to the first separation processing means 2 which is the next processing stage. Therefore, as shown in FIGS. 6 and 7, the raw water tank 16 is connected with an inflow pipe 18 for allowing the raw water after filtration to flow into the upper part thereof, and the first transfer is provided at the lower part of the side surface. A pipe 19a is connected, and the raw water is transferred to the next treatment stage by the suction force of the raw water transfer pump 17.
[0053]
The bottom of the raw water tank 16 is connected to a first discharge pipe 20a for discharging the precipitate, and the precipitate is transferred to the dehydration processing means 12 through the first discharge pipe 20a. It has become.
[0054]
The raw water tank 16 is supplied with water dehydrated from the precipitate by a dehydrator 56 (to be described later) of the dehydrating means 12 and water after the dehydrator 56 is washed. Has been used for dilution.
[0055]
Next, the first separation processing unit 2 will be described.
[0056]
As shown in FIGS. 5 and 6, the first separation processing means 2 is provided with a first separation processing pipe 22 connected to the first transfer pipe 19 a, and the first separation processing pipe 22. An electromagnetic coil 23 is wound around the outer periphery of the first and a cylindrical first microwave oscillation tube body 24 is disposed. The first microwave oscillating tube 24 is composed of a magnet such as a neodymium plate, and the upper side is an N pole and the lower side is an S pole. And from this 1st microwave oscillation tube body 24, the frequency of 300 MHz-16 GHz according to the density | concentration of raw | natural water, More preferably, the frequency of 2.4 G-10.5 GHz from the viewpoint of isolate | separating a colloid particle, More preferably, 10 A microwave with a frequency of .5 GHz is oscillated. A magnetic field and an electric field synthesis field are formed by such permanent magnets, electromagnets, and microwaves as electromagnetic waves, thereby separating colloidal particles and liquid molecules in the raw water.
[0057]
Here, as shown in FIG. 11, the microwave is considered to have an action of mainly dispersing the raw water when the colloidal particles and the liquid molecules are charged and broken apart.
[0058]
The dispersed treated water is transferred to the first aggregating treatment means 3 through the second transfer pipe 19b connected to the first separation treatment pipe 22.
[0059]
Next, the first aggregation processing means 3 will be described.
[0060]
As shown in FIGS. 5 to 7, the first aggregating treatment unit 3 is provided with a first aggregating treatment tank 26. The bottom of the first aggregating treatment tank 26 has the second transfer pipe 19b. Are connected so that treated water flows from the first separation processing pipe 22.
[0061]
Then, in the first agglomeration treatment tank 26, as shown in FIGS. 7 and 8, a plurality of first low frequency oscillations that oscillate low frequency ultrasonic waves in a frequency range of 100 kHz or less according to the concentration of raw water. A region ultrasonic oscillator 27 is disposed. In this specific example, the first low-frequency ultrasonic oscillator 27 is a first low-frequency ultrasonic oscillator 27a that oscillates with a 28 kHz or 40 kHz ultrasonic wave as a transverse wave, and a 48 kHz or 100 kHz ultrasonic wave is a transverse wave. And the first low-frequency ultrasonic oscillator 27b that oscillates as follows. Due to the cavitation action by these ultrasonic waves, the low-frequency ultrasonic wave of 28 kHz or 40 kHz has a role of aggregating the dispersed colloidal particles, and the low-frequency ultrasonic wave of 48 kHz or 100 kHz is agglomerated. It has a role to disperse colloidal particles and liquid molecules. These ultrasonic outputs are set to 300 W to 1.2 kW.
[0062]
A permanent magnet 28a such as neodymium is laid on the inner surface of the bottom of the first agglomeration treatment tank 26, and a second discharge pipe 20b is connected to the bottom. For this reason, the aggregate of colloidal particles in the charged state is attracted by the permanent magnet 28a and settles, and this precipitate passes through the second discharge pipe 20b to the dehydration processing means 12. It is supposed to be transferred.
[0063]
Then, the treated water that has been subjected to the first stage agglomeration treatment is transferred to the subdivided charging means 4 through the third transfer pipe 19c connected to the upper part of the side surface of the first agglomeration treatment tank 26. . A pressurizing pump 29 is disposed in the middle of the third transfer pipe 19c, so that the treated water that flows into the subdivided charging processing means 4 flows in at an appropriate pressure.
[0064]
Note that an air discharge port 49 for discharging the air contained in the raw water is disposed in the upper portion of the first aggregating treatment tank 26.
[0065]
Next, the subdivided charging processing means 4 will be described.
[0066]
The subdivided charging means 4 has the same configuration as the liquid processing apparatus 70 according to the present invention described above, and the subdivided charging means 4 includes a subdivided charging pipe connected to the third transfer pipe 19c. 30 is disposed.
[0067]
FIG. 3 shows a main part of the configuration of the sub-charging unit 4, and treated water having an increased flow velocity by applying an appropriate pressure through the nozzle 29 a and the diffuser 30 of the pressurizing pump 29. The mixer pipe disposed in the element portion 31 is circulated.
[0068]
In the element portion 31, a cavitation phenomenon occurs in the cylindrical pipe 72 in the treated water supplied at a high flow rate. When this cavitation phenomenon occurs, a hot spot is formed in the treated water, and an ultra-high pressure and a vacuum state are formed. In this state, the colloidal particles and the like in the treated water are once separated and then made uniform in size. At that time, the first fin 75a and the second fin 75b constituting the neodymium fin 75 disposed in the mixer tube 71 vigorously agitate the treated water to decompose the liquid molecules and colloidal particles in the treated water. It acts to promote uniformity of thickness. Further, the neodymium magnets 73 and 74 embedded in the inner surface of the cylindrical pipe 72 constituting the mixer tube 71 and the neodymium fin 75 generate electromotive force in the treated water rotating at a high speed so as to increase the magnetization efficiency. Act on. Then, the generated electromotive force acts to uniformly charge the colloidal particles that have been made uniform and to perform ion alignment.
[0069]
Further, a pair of electromagnets 100 for applying a magnetic field to the neodymium magnets 74 a and 74 b of the pair of neodymium fins 75 disposed in the mixer tube 71 are opposed to each other with the mixer tube 71 interposed therebetween. It is arranged. Accordingly, a magnetic force, which is a repulsive force or an attractive force, can be applied to the neodymium magnets 74a and 74b by the magnetic field of the electromagnet 100, so that the neodymium fin 75 can be rotated in the circumferential direction by this magnetic force. ing.
[0070]
Thus, when the neodymium fin 75 rotates in the circumferential direction, among the magnetic fluxes between the pair of electromagnets 100, the number of magnetic flux linkages penetrating the neodymium fin changes rapidly, and the change in the number of magnetic flux linkages. As a result, an induced electromotive force is generated in the neodymium fin 75.
[0071]
Due to the influence of this electromotive force, the liquid molecules subdivided by the rotation of the neodymium fin 75 are charged as negative ions, and suspended matter molecules such as colloidal particles are charged as positive ions or negative ions. Yes.
[0072]
Note that the polarity of the charge of the floating molecule depends on the direction of the electromotive force generated by the neodymium fin 75. Here, in particular, suspended matter molecules contained in liquids such as artificially produced industrial wastewater contain a mixture of many positive ions and many negative ions. If the polarities of the particles are not unified, it is difficult to efficiently perform the subsequent aggregating and separating process. However, in the present embodiment, the neodymium fin 75 is used to convert the suspended molecule to either a positive or negative charge. Either one can be charged uniformly.
[0073]
Therefore, in the present embodiment, it is possible to improve the efficiency of the agglomeration separation subsequent to the subdivision charging process by the mixer tube 71 and the electromagnet 100.
[0074]
Further, the electromagnet 100 reverses the magnetic field applied to the neodymium fin 75 in accordance with the properties of the liquid such as the polarity of suspended matter molecules. When reversing the magnetic field, the neodymium fin 75 switches its rotation in the direction opposite to the original rotation direction, so that the direction of the electromotive force generated by the neodymium fin 75 is switched in the reverse direction by switching this rotation. ing.
[0075]
When this electromotive force is switched, the charge polarity of the suspended molecule can be reversed.
[0076]
For this reason, since there are a lot of positive ions among the suspended matter molecules, an electromotive force is applied in the direction in which the suspended matter molecules are uniformly charged to the positive ions. By switching the electromotive force generated by the neodymium fin 75 by the inversion, the floating molecules can be uniformly charged to negative ions.
[0077]
Accordingly, it is possible to flexibly perform an appropriate subdividing charging process according to the properties of the liquid.
[0078]
In the present embodiment, the electromagnet 100 can change the strength of the magnetic field applied to the neodymium fin 75 according to the ion concentration of suspended matter molecules contained in the liquid.
[0079]
As a result, even when the ion concentration of suspended matter molecules is small, an effective electromotive force can be obtained by increasing the strength of the magnetic field, and the subsequent sub-charging process can be performed appropriately. Yes.
[0080]
Further, an automatic control unit 101 that controls the magnetic field of the electromagnet 100 is connected to the electromagnet 100.
[0081]
The automatic control unit 101 is connected to a sensor 102 that measures the polarity and ion concentration of the suspended molecule in real time. The sensor 102 may be, for example, such that a pair of electrodes (not shown) are brought into contact with the liquid and the property of the liquid is automatically detected based on a current value flowing between the electrodes. .
[0082]
Further, for example, a pair of electrodes are brought into contact with the liquid, and a measurement reference signal that is an AC signal in the audible sound band is oscillated from the one electrode to the other electrode via the liquid, and the oscillated signal is converted into the liquid. The phase difference of the signal received via the liquid is detected by synchronously detecting the received signal based on the same signal as the measurement reference signal. And based on this detection result, you may make it measure the ion concentration of the suspended | floating matter molecule | numerator in a liquid. In this case, the impedance of the liquid may be obtained from the phase change of the signal received by the receiving electrode via the liquid, and the ion concentration may be calculated based on this impedance. In such a case, since the electrical signal applied between the electrodes is alternating current, it is possible to prevent deposits from accumulating on the electrodes and to reduce the number of times maintenance is performed.
[0083]
As described above, if the automatic control unit 101 can automatically control the magnetization of the electromagnet based on the property of the liquid, it is possible to further improve the efficiency of the subdivision charging process.
[0084]
As described above, the fine charge processing means 4 performs ion alignment of finer colloidal particles that could not be removed by the first separation / aggregation process, and easily processed in the next second separation / aggregation process step. Preparations can be made.
[0085]
Next, the second separation processing unit 5 will be described.
[0086]
The second separation processing unit 5 has substantially the same configuration as the first separation processing unit 2 described above. That is, as shown in FIGS. 6 and 9, the second separation processing means 5 is provided with a second separation processing pipe 33 connected to the subdivided charging processing pipe 30, and this second separation processing. An electromagnetic coil 34 is wound around the outer periphery of the pipe 33 and a second microwave oscillating tube 35 is disposed. The second microwave oscillating tube 35 is composed of a magnet such as a neodymium plate, and the upper side is an N pole and the lower side is an S pole. And from the viewpoint of performing a separation treatment of colloidal particles according to the concentration of treated water flowing in, more preferably from 2.4 G to 10.5 GHz, and even more preferably from 10.5 GHz. The wave oscillates for about 1 μsec. When such a microwave is oscillated in the treated water, the treated water is destroyed and finer colloidal particles and liquid molecules are formed and dispersed separately. It will be.
[0087]
Thereafter, the dispersed treated water is transferred from the second separation treatment pipe 33 to the next deodorization treatment means 6.
[0088]
Next, the deodorizing means 6 will be described.
[0089]
The deodorization processing means 6 is provided with a deodorization processing box 37 which is a high-frequency electromagnetic ultrasonic oscillator, and a deodorization processing pipe 38 connected to the second separation processing pipe 33 in the deodorization processing box 37. Is arranged so as to be penetrated. As shown in FIG. 12, external magnets 39a having polarities of N pole and S pole are respectively disposed at the upper and lower positions outside the deodorizing pipe 38, and at the axial position of the deodorizing pipe 38. The bar-shaped inner magnet 39b is arranged so that the polarity opposite to that of the outer magnet 39a is opposed. In the first embodiment, the external magnet 39a is formed of an electromagnet, and the internal magnet 39b is formed of a permanent magnet. Further, on the left and right side surfaces of the deodorizing pipe 38, a high-frequency wave that oscillates longitudinal ultrasonic waves with a frequency of 3 MHz to 300 MHz, more effectively 100 MHz depending on the concentration of treated water, with a period of about 0.5 sec. A region ultrasonic oscillator 40 is provided.
[0090]
The treated water passes through the deodorizing pipe 38 while being vibrated with a mixer or in the first embodiment, and is ejected from a nozzle (not shown) disposed in the deodorizing pipe 38 in the first embodiment. A diaphragm (not shown) is disposed near the outlet of the nozzle, and vibrates vigorously when the treated water collides with the diaphragm.
[0091]
The external magnet 38a, the internal magnet 38b, and the high-frequency ultrasonic oscillator 40 form a synthetic field by a magnetic field and an electric field so that a so-called electromagnetic ultrasonic wave is generated. The amino acids in the colloidal particles are pulverized to completely remove the odor from the treated water.
[0092]
The treated water deodorized by the deodorized treatment pipe 38 is transferred to the second aggregating treatment means 7 which is the next treatment stage.
[0093]
Next, the second aggregation processing means 7 will be described.
[0094]
The second agglomeration treatment means 7 is provided with a second agglomeration treatment pipe 41, and an electromagnetic coil 42 is wound around the outer periphery of the second agglomeration treatment pipe 41, and the concentration of the treated water. Accordingly, a second low-frequency ultrasonic oscillator 43 that oscillates low-frequency ultrasonic waves in a frequency range of 50 kHz or less is disposed.
[0095]
When low-frequency ultrasonic waves are oscillated in the treated water by the second low-frequency ultrasonic wave oscillating body 43, liquid molecules that are charged with negative ions among irregularly arranged liquid molecules and colloidal particles. Is attracted to the wall surface side of the second agglomeration pipe 41 and flows along the wall surface, and colloidal particles charged to positive ions flow through the center side of the second agglomeration pipe 41, and the liquid molecules And colloidal particles are dispersed so that the colloidal particles are aggregated.
[0096]
The treated water that has been subjected to the second aggregating treatment in this way is transferred to the next high voltage pulse processing means 8.
[0097]
The high voltage pulse processing means 8 generates plasma by applying a high voltage of about 10 k-60 kV at different periods to remove nitrogen molecules in the treated water.
[0098]
For this reason, as shown in FIG. 13, the high voltage pulse processing means 8 is provided with a high voltage pulse processing pipe 45 connected to the second aggregation processing pipe 41. The pulse processing pipe 45 is provided with a plurality of electrode bodies 46A, 46A ′, 46B, 46B ′, 46C, 46D as high voltage pulse generators applied at different periods.
[0099]
Between these electrode bodies 46A-46A 'and between the electrode bodies 46B-46B', as shown in FIG. 12, a voltage of 10 to 30 kV is applied for 20 .mu.s, 20 .mu.s is applied again, and after 20 .mu.s, 5 .mu.s are passed. The application of the voltage with the same pattern is repeated again.
[0100]
On the other hand, between the electrode bodies 46C and 46D, as shown in FIG. 13, a voltage of about 60 kV is applied for 5 μs with a period of 5 μs.
[0101]
FIG. 16 shows changes in the state of liquid molecules and colloidal particles when a voltage is applied by the electrode bodies 46A, 46A ′, 46B, 46B ′, 46C, and 46D. The large circle in FIG. 16 is a liquid molecule, and the small circle bonded to this is a colloidal particle. First, the liquid molecules are charged to a negative charge and the nitrogen molecules are charged to a positive charge by a high voltage pulse between the electrode bodies 46A-46A 'and between the electrode bodies 46B-46B'. The high voltage pulse between the electrode bodies 46A-46B 'and between the electrode bodies 46A'-46B causes an action of separating liquid molecules and nitrogen molecules, and the high voltage pulses between the electrode bodies 46C-46D cause nitrogen molecules to be separated. It is completely torn from the liquid molecules. Simultaneously with the skipping of the nitrogen molecules, the oxygen molecules being processed are combined to generate ozone. This ozone has the effect of decolorizing and sterilizing the treated water.
[0102]
Therefore, the high-voltage pulse processing means 8 is capable of removing nitrogen from the treated water and decolorizing and sterilizing the treated water.
[0103]
A fourth transfer pipe 19d is connected to the outflow side of the high voltage pulse processing pipe 45 of the high voltage pulse processing means 8 so that the treated water is discharged from the aggregate discharge processing means 9 which is the next processing stage. It will be transferred to the processing tank 48.
[0104]
Next, the aggregate discharge processing means 9 will be described.
[0105]
The agglomerate discharge processing means 9 adsorbs and discharges colloidal particles that have been agglomerated by the second separation and agglomeration process downward by a permanent magnet 28b such as neodymium.
[0106]
Therefore, as shown in FIGS. 5, 6 and 10, the aggregate discharge treatment means 9 is provided with a discharge treatment tank 48 for storing treated water. At the bottom of the discharge treatment tank 48, the fourth transfer pipe 19d is connected so that treated water containing agglomerates flows in, and a permanent magnet 28b such as neodymium is laid. Among the treated water flowing in from the fourth transfer pipe 19d, agglomerated particles in a charged state are attracted by the magnetic force of the permanent magnet 28b and settled to the bottom.
[0107]
The sediment collected at the bottom of the discharge processing tank 48 is discharged from the third discharge pipe 20c connected to the bottom of the discharge processing tank 48 to the dehydration processing means 12. .
[0108]
The magnetic force of the permanent magnet 28b is determined according to the organic matter concentration of the treated water. For this reason, when processing high concentration raw water, that is, raw water containing a large amount of colloidal particles, it is necessary to adsorb a large amount of aggregates, so that the magnetic force of the electromagnet is set to be large. Conversely, when processing low concentration raw water, the magnetic force of the electromagnet is set to be small.
[0109]
In addition, an air discharge port 49 and an ozone discharge port 50 are disposed above the discharge processing tank 48, and air such as nitrogen and ozone generated by the high voltage pulse processing are discharged to the outside. ing.
[0110]
Then, the treated water from which the aggregates and the like are removed in the discharge treatment tank 48 passes through the fifth transfer pipe 19e connected to the upper part of the side surface of the discharge treatment tank 48, and the next liquid molecule fragmentation treatment means 10 is used. It is transferred to.
[0111]
Next, the liquid molecule fragmentation processing means 10 will be described.
[0112]
The liquid molecule subdivision processing means 10 generates active water by further subdividing the liquid molecules of water purified by the above-described processes by the action of a strong magnetic force.
[0113]
For this reason, as shown in FIGS. 5, 6 and 10, the liquid molecule fragmentation processing means 10 is provided with a fragmentation treatment tank 51, and a ceramic or the like is provided in the fragmentation treatment tank 51. A cylindrical body 52 made of an insulating material is disposed so that the vertical direction is the longitudinal direction. The fifth transfer pipe 19e is connected to the upper part of the side surface of the subdivision processing tank 51, and a cylinder transfer pipe 53 that connects the fifth transfer pipe 19e and the cylinder 52 is provided. Has been. For this reason, the water subjected to the liquid molecular fragmentation process flows into the cylinder 52 through the fifth transfer pipe 19e and the cylinder transfer pipe 53.
[0114]
The bottom surface side of the cylindrical body 52 is opened, and an electromagnetic coil (not shown) is wound around the outer peripheral surface of the cylindrical body 52. For this reason, when a current flows through the electromagnetic coil, a force acting downward is generated inside the cylindrical body 52, and the treated water that flows in is transferred toward the bottom of the liquid molecule fragmentation processing tank 51. It is like that.
[0115]
On the other hand, permanent magnets 28c and 28d such as neodymium of about 10000 Gauss are laid as magnetic field forming bodies on the inner surfaces of the top and bottom of the liquid molecule fragmentation processing tank 51, respectively. A strong magnetic field is formed. When the treated water passes through the liquid molecule fragmentation treatment tank 51 by this strong magnetic force, activated water is generated by further subdividing the liquid molecules, so-called clusters, and activating them.
[0116]
Therefore, the water after this treatment can be used as drinking water for animals or can exert a remarkable effect on its growth when given to plants.
[0117]
The treated water that has been subjected to the liquid molecule fragmentation process flows out of the discharge pipe 54 connected to the upper part of the side surface of the liquid molecule fragmentation tank 51 and is discharged as it is to a river or the like, or animals and plants. It can be used as water to give
[0118]
A fourth discharge pipe 20d is connected to the bottom of the liquid molecule fragmentation processing tank 51, and the final colloidal particles and the like adsorbed by the permanent magnet 28d laid on the bottom surface are dehydrated. It is designed to discharge to 12.
[0119]
Further, an air discharge port 49 and an ozone discharge port 50 for discharging air such as nitrogen remaining in the treated water and ozone are formed in the upper part of the liquid molecule fragmentation processing tank 51.
[0120]
Next, the redox treatment means 11 will be described.
[0121]
As shown in FIGS. 5, 6 and 10, the oxidation-reduction processing means 11 is composed of four electrode members 55 having appropriate potentials. On the surfaces of these electrode members 55, the treated water ionized by the above-described treatments exchanges electrons to cause an oxidation-reduction reaction. By this oxidation-reduction reaction, the treated water is returned from an ionized state where chemical reaction is likely to occur to a stable state where chemical reaction is difficult.
[0122]
In the first embodiment, the oxidation-reduction reaction is performed as an electrode reaction via the electrode member 55, but an appropriate oxidizing agent or reducing agent may be used depending on circumstances.
[0123]
Next, the dehydration processing means 12 will be described.
[0124]
The dehydrating means 12 is provided with a dehydrator 56 for removing moisture contained in the sediment discharged from the processing means by the action of centrifugation or the like. The dehydrator 56 can reduce the moisture content of the precipitate from about 98% to about 80%. For this reason, it becomes possible to process more efficiently in the composting plant.
[0125]
In addition, as described above, the dehydrator 56 is supplied with the raw water dilution pipe 57 for diluting the raw water by transferring the water generated by the dehydration action and the washing water of the dehydrator 56 to the raw water tank 16. Are connected.
[0126]
On the other hand, the solid after being dehydrated by the dehydrator 56 is discharged to the solid receiver 58. Thereafter, this solid matter is transported to the composting plant together with the solid matter filtered by the filtration means 1 described above, composted as a compost raw material, and reused as an agricultural fertilizer.
[0127]
Next, the central control means 13 will be described.
[0128]
As shown in the block diagram of FIG. 17, the central control unit 13 includes a first microwave control unit 60 that controls the output of a 300 M to 16 GHz microwave oscillated by the first separation processing unit 2, and a first aggregation. The first low-frequency ultrasonic control unit 61 that controls the output of the low-frequency ultrasonic wave of 100 kHz or less oscillated in the processing means 3 and the 300 M to 16 GHz microwave oscillated in the second separation processing means 5. A second microwave control unit 62 that controls the output of the low-frequency ultrasonic wave of 50 kHz or less oscillated in the second aggregation processing means 7, A high-frequency electromagnetic ultrasonic control unit 64 that controls the output of 3M to 300 MHz high-frequency electromagnetic ultrasonic waves oscillated in the deodorization processing means 6, and a high-voltage pulse applied in the high-voltage pulse processing means 8. The high voltage pulse control unit 65 for controlling the output of the gas, the voltage control unit 66 for controlling the voltage applied to the electrode member 55 in the oxidation-reduction processing unit 11, and the operation of the dehydrator 56 of the dehydration processing unit 12 are controlled. And a dehydration control unit 67. Each of these control units can be easily controlled by each switch (not shown) of the centralized control panel 68, and is normally automatically controlled.
[0129]
Next, a liquid processing method using the above-described liquid processing system will be described.
[0130]
First, raw water including pig farm wastewater and industrial wastewater is filtered through the screen of the filtration means 1 to remove colloidal particles separated in the raw water and discharged to the residue receiving unit 15 and filtered. The raw water is temporarily stored in the raw water tank 16.
[0131]
Then, the raw water transfer pump 17 sucks the raw water from the raw water tank 16 and transfers it to the first separation processing pipe 22 of the first separation processing means 2. The first separation processing unit 2 oscillates a 10.5 GHz microwave from the first microwave oscillation tube body 24 to the raw water under the control of the first microwave control unit 60, and the raw water is liquidized. Separate into molecules and colloidal particles. The separated treated water is transferred to the first aggregating treatment means 3 through the second transfer pipe 19b. The first agglomeration treatment means 3 is controlled by the first low-frequency region ultrasonic control unit 61 with respect to the treated water from 28 kHz, 40 kHz, 48 kHz and 100 kHz from the first low-frequency region ultrasonic oscillators 27a and 27b. One of the ultrasonic waves is oscillated to aggregate the colloidal particles and disperse them from the liquid molecules. Then, the agglomerated permanent colloid 28a disposed on the bottom surface of the first agglomeration treatment tank 26 adsorbs and precipitates the agglomerated colloidal particles and discharges them to the second discharge pipe 20b.
[0132]
On the other hand, the treated water passes through the third transfer pump and is transferred to the subdivided charging processing means 4 with an appropriate pressure by the pressure pump 29. In this subdivision charging means 4, the floating molecules in the raw water are subdivided by rotation of the mixer tube 71 of the neodymium fin 75, and an electromotive force is generated by applying a magnetic field to the neodymium fin 75 by the electromagnet 100. The electromotive force causes the liquid molecules and the floating molecules surrounding them to be charged. As a result, the polarity of ions of suspended matter molecules such as fine colloids is unified to either positive or negative, and liquid molecules are negatively charged, whereby the subdivided charging process of the treated water is completed.
[0133]
At this time, since the automatic control unit 101 can reverse the magnetic field of the electromagnet or change the strength of the magnetic field according to the property of the treated water based on the detection result of the sensor 12, the appropriateness according to the property of the treated water Can be performed with a finely divided charging process.
[0134]
Subsequently, the water subjected to the subdivided charging process is transferred to the second separation processing unit 5. The second separation processing unit 5 oscillates a 10.5 GHz microwave from the second microwave oscillation tube 35 to the treated water under the control of the second microwave control unit 62 of the central control unit 13. The treated water is separated into liquid molecules and colloidal particles. The separated treated water is transferred to the deodorizing treatment means 6.
[0135]
The deodorizing treatment means 6 oscillates about 100 MHz ultrasonic waves from the high-frequency ultrasonic oscillator 40 in the magnetic field into the treated water under the control of the high-frequency electromagnetic ultrasonic control unit 64 of the central control means 13. Remove malodor from treated water by electromagnetic ultrasonic waves.
[0136]
The deodorized treated water is transferred to the second aggregation treatment means 7. The second agglomeration treatment unit 7 controls the ultrasonic waves of 50 kHz or less from the second low-frequency ultrasonic wave oscillator 43 by controlling the second low-frequency ultrasonic control unit 63 of the concentration control unit 13 with respect to the treated water. The colloidal particles are aggregated and dispersed from the liquid molecules.
[0137]
Then, the treated water subjected to the second aggregating treatment is transferred to the high voltage pulse processing means 8. The high voltage pulse processing means 8 applies a voltage of 10 k-30 kV between the electrode bodies 46A-46A 'and between the electrode bodies 46B-46B' under the control of the high voltage pulse control section 65 of the central control means 13. At the same time, a voltage of about 60 kV is applied between the electrode bodies 46C-46D to generate plasma, thereby separating and removing nitrogen contained in the treated water. The ozone generated at this time decolorizes and sterilizes the treated water.
[0138]
The water from which nitrogen has been removed is transferred to the discharge processing tank 48 of the aggregate discharge processing means 9 through the fourth transfer pipe 19d.
[0139]
In the discharge processing tank 48, the permanent magnet 28b adsorbs the aggregate of colloidal particles by magnetic force, precipitates it on the bottom of the discharge processing tank 48, and transfers it from the third discharge pipe 20c to the dehydration processing means 12.
[0140]
The treated water from which the aggregates have been removed is transferred to the liquid molecule fragmentation processing tank 51 of the liquid molecule fragmentation processing means 10 through the fifth transfer pipe 19e in order from the supernatant. The liquid molecule fragmentation processing means 10 forms a strong magnetic field by the permanent magnets 28c and 28d laid on the upper and lower surfaces of the liquid molecule fragmentation processing tank 51, and further subdivides the liquid molecules of the inflowing treated water. Generate active water.
[0141]
In the liquid molecule fragmentation treatment tank 51, the electrode member 55 of the oxidation-reduction treatment means 11 performs a treatment to cause the treated water ionized on the surface thereof to undergo oxidation-reduction reaction and return to stable treated water.
[0142]
Thereafter, the water subjected to the subdivision treatment and the oxidation-reduction treatment is discharged from the discharge pipe 54 and discharged into the river, or used as nutrient water for animal drinking water or plants.
[0143]
On the other hand, the colloidal particle precipitate discharged in each processing stage passes through the first discharge pipe 20a, the second discharge pipe 20b, the third discharge pipe 20c, and the fourth discharge pipe 20d, respectively. It is transferred to the dehydrator 56. In the dehydrator 56, the solid matter is subjected to centrifugal separation action under the control of the dehydration control unit 67 of the central control means 13, and moisture is removed from the precipitate.
[0144]
The water removed by the dehydrator 56 is transferred to the raw water tank 16 through the raw water dilution pipe 57 together with the washing water of the dehydrator 56, and is used to dilute the raw water. On the other hand, after the dehydrated solid is stored in the solid receiver 58, it is transported to a composting plant and used as agricultural compost.
[0145]
Thus, according to the liquid processing method using the liquid processing apparatus of this example, colloidal particles (including heavy metals) and nitrogen contained in raw water such as swine effluent and industrial chemical effluent can be reliably removed. Deodorizing, decolorizing and sterilizing can also be performed, and active water composed of extremely finely divided liquid molecules can be generated and stable water can be generated. Thus, for example, the rotation direction of the fin can be reversed by reversing the magnetic field applied to the magnet of the fin by the electromagnet according to the properties of the liquid such as the ion polarity and ion concentration of suspended matter molecules contained in the liquid. Therefore, it is possible to unify the charged state of the suspended molecule, and to perform the liquid fine charging process appropriately and flexibly according to the properties of the liquid.
[0146]
In addition, this invention is not limited to embodiment mentioned above, A various change is possible as needed.
[0147]
【The invention's effect】
As described above, according to the liquid processing apparatus and the liquid processing system having the liquid processing apparatus according to the present invention, it is possible to subdivide and charge various substances such as liquid molecules and colloidal particles contained in the processing water. It can be carried out appropriately and efficiently according to the properties, and by using this mixer tube in the liquid processing system, the liquid processing system can be reduced in scale, the initial cost and running cost can be reduced, By further miniaturizing the liquid molecules, it is possible to reliably remove suspended matters in the liquid and to improve the quality by deodorizing, decolorizing and sterilizing, and it is possible to use in a wider range of fields.
[Brief description of the drawings]
FIG. 1 is a cross-sectional view showing an embodiment of a liquid processing apparatus according to the present invention.
FIG. 2 is a cross-sectional view showing an embodiment of a liquid processing apparatus according to the present invention.
FIG. 3 is an explanatory diagram showing the main part of the subdivision charging processing means in the embodiment of the liquid processing system according to the present invention.
FIG. 4 is a sectional view showing the structure of a mixer pipe according to the present invention.
FIG. 5 is a flowchart showing an embodiment of a liquid processing system according to the present invention.
FIG. 6 is a plan view showing a main part of an embodiment of a liquid processing system according to the present invention.
7 is a cross-sectional view taken along the line II of FIG.
FIG. 8 is an explanatory diagram viewed from the II-II direction in FIG.
FIG. 9 is an explanatory diagram viewed from the III-III direction of FIG.
10 is a cross-sectional view taken along the line IV-IV in FIG.
FIG. 11 is a schematic diagram showing first separation processing means and first aggregation processing means in the embodiment of the liquid processing system according to the present invention.
FIG. 12 is an explanatory view showing the main part of the deodorizing means in the embodiment of the liquid processing system according to the present invention.
FIG. 13 is an explanatory view showing high voltage pulse processing means in the embodiment of the liquid processing system according to the present invention.
FIG. 14 is an explanatory diagram showing a voltage pattern applied in the high voltage pulse processing means in the embodiment of the liquid processing system according to the present invention.
FIG. 15 is an explanatory diagram showing a voltage pattern applied in the high voltage pulse processing means in the embodiment of the liquid processing system according to the present invention.
FIG. 16 is an explanatory diagram showing the molecular state of treated water by the treatment of the high voltage pulse treatment means in the embodiment of the liquid treatment system according to the present invention.
FIG. 17 is a block diagram showing centralized control means in the embodiment of the liquid processing system according to the present invention.
FIG. 18 is a cross-sectional view showing the structure of a conventional mixer tube
[Explanation of symbols]
1 Filtration processing means
2 First separation processing means
3 First aggregation processing means
4 Subdivision charging means
5 Second separation processing means
6 Deodorization treatment means
7 Second aggregation processing means
8 High voltage pulse processing means
9 Aggregate discharge treatment means
10 Water molecule fragmentation treatment means
11 Redox treatment means
12 Dehydration means
13 Central control means
14 Filter body
15 Residue receiving part
16 Raw water tank
17 Raw water transfer pump
18 Inflow pipe
19 Transfer pipe
20 First discharge pipe
22 First separation pipe
26 1st aggregation processing tank
27 First low-frequency ultrasonic oscillator
29 Pressure pump
30 Finely charged pipe
33 Second separation pipe
38 Deodorized pipe
41 Second coagulation treatment pipe
43 Second low-frequency ultrasonic oscillator
45 High voltage pulse processing pipe
48 Discharge treatment tank
49 Air outlet
50 Ozone outlet
51 Subdivision processing tank
52 cylinder
54 Discharge pipe
56 Dehydrator
58 Solid receiving part
68 Centralized control panel
70 Liquid processing equipment
71 mixer tube
72 Tubular pipe
73 Neodymium magnet
73a N pole
73b S pole
74 Neodymium magnet
74a N pole
74b S pole
75 neodymium fin
75a First fin
75b 2nd fin
100 electromagnet
101 Automatic control unit
102 sensor

Claims (4)

Liquid processing that facilitates separation of liquid molecules and suspended matter molecules by mixing liquids containing suspended matter in a magnetic field, and charging and aligning the liquid molecules and suspended matter molecules in the liquid while subdividing them In the device
A fin formed in a spiral shape along the longitudinal direction of the cylindrical pipe is disposed in the cylindrical pipe so as to be rotatable in the circumferential direction, and N-pole and S-pole magnets are spirally arranged on the fin. Mixer tubes buried alternately along
Outside the mixer tube, an electromagnet capable of applying a rotational force to the fin by applying a magnetic field to the magnet embedded in the fin,
An electromotive force is generated in the mixer tube by rotating the fin in a magnetic field by the electromagnet, and the electromotive force is applied to the liquid subdivided by the mixer tube, whereby the liquid molecule and the suspended matter molecule are generated. And is charged and aligned
In addition, the liquid processing apparatus is characterized in that the magnetic field applied to the magnet of the fin can be reversed by the electromagnet according to the property of the liquid. 2. The liquid processing apparatus according to claim 1, wherein the strength of the magnetic field applied to the magnet of the fin can be changed by the electromagnet according to the property of the liquid. At least a separation processing means that oscillates microwaves in treated water containing suspended matter to separate suspended molecules and liquid molecules, and oscillates low-frequency ultrasonic waves in the liquid after separating these suspended molecules. Aggregation treatment means for aggregating the suspended matter molecules, subdivided charging treatment means for charging and aligning the liquid molecules and the suspended matter molecules in the liquid while being subdivided by mixing in a magnetic field; Deodorization processing means for deodorizing the liquid by oscillating ultrasonic waves, and high pressure for decolorizing and sterilizing the liquid by applying high pressure pulses to the liquid to separate and remove nitrogen from the liquid and generate ozone In a liquid processing system having a pulse processing means and an aggregate discharge processing means for adsorbing and discharging aggregates of the suspended matter molecules by magnetic force, the fine charge processing means includes:
In the cylindrical pipe, fins spirally formed along the longitudinal direction of the cylindrical pipe are rotatably arranged in the circumferential direction, and N-pole and S-pole magnets are spirally arranged in each fin. Mixer tubes buried alternately along
Outside the mixer tube, an electromagnet capable of applying a rotational force to the fin by applying a magnetic field to the magnet embedded in the fin,
An electromotive force is generated in the mixer tube by rotating the fin in a magnetic field generated by the electromagnet, and the electromotive force is applied to the liquid subdivided by the mixer tube, whereby the liquid molecule and the suspended matter molecule are generated. And is charged and aligned
The liquid processing system is characterized in that the magnetic field applied to the fin magnet can be reversed by the electromagnet according to the properties of the liquid. The liquid processing system according to claim 3, wherein the strength of the magnetic field applied to the magnet of the fin can be changed by the electromagnet according to the property of the liquid.

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