JP2003112187A - Liquid treatment apparatus and liquid treatment system containing the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a liquid treatment apparatus which can carry out a suitable fractionization and electrification treatment of filth in foul water flowing through a mixer pipe according to the properties of the foul water by improving the structure of a fractionization and electrification treatment means. SOLUTION: The liquid treatment apparatus has a mixer pipe 71 which comprises a fin 75 spirally formed in a pipe 72 and magnets 92 having N and S poles and embedded in the fin 75 and an electromagnet 100 which applies a magnetic field to the magnets 92 to impart torque to the fin 75. By rotating the fin in the magnetic field applied by the electromagnet 100 to generate an electromotive force in the mixer pipe, liquid molecules and suspended matter molecules are electrically charged and arranged in lines. The magnetic filed applied by the electromagnet 100 to the magnets 92 is made reversible according to the properties of the liquid.

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid treatment device and a liquid treatment system having the liquid treatment device, and more particularly to efficient treatment of subdivision and charging of various substances such as liquid molecules and colloidal particles contained in treated water. TECHNICAL FIELD The present invention relates to a liquid processing apparatus and a liquid processing system having the same.

[0002]

2. Description of the Related Art Conventionally, there have been proposed methods and systems for purifying livestock wastewater containing manure from cattle, pigs, etc., or industrial wastewater containing chemical substances such as cleaning liquids and factory waste liquids.

[0003] Such conventional liquid treatment system will be described by taking pig effluent drainage treatment as an example. In the conventional water treatment system for pig effluent, filtration for removing solid suspended matters by passing raw water through a screen or the like. Treatment means, activated sludge treatment means for decomposing water-soluble organic substances and the like by aerobic microorganisms, and precipitation decomposition treatment for precipitating water-soluble organic substances separated from raw water by this decomposition to separate water and precipitates And means for dehydrating and removing water from the precipitate.

More specifically, each of these processing means will be described. In the filtration processing means, when raw water containing solid suspended matter such as manure and urine passes through the screen, the suspended matter is captured and removed by the screen. . The raw water from which the suspended solids have been removed is temporarily stored in a storage tank, then transferred to a measuring 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 sedimentation tank as a sedimentation decomposition treatment means, and in this sedimentation tank, water-soluble organic substances and the like are precipitated at the bottom of the sedimentation tank to separate from water, and this water is disinfected. After being discharged into a river or the like, the precipitate is transferred to the dehydration treatment means. In this dehydration processing means, it is dehydrated by a dehydrator to be solidified and discharged.

Here, in the conventional water treatment system, the washing water of the dehydrator is introduced into the storage tank in order to avoid an increase in the site and construction cost due to the large size of the activated sludge treatment tank. It was like this.

Therefore, with the washing water of the dehydrator,
Since so-called high-concentration raw water having a high organic matter load is diluted, the burden of aerobic microorganisms for decomposing organic matter in the activated sludge treatment means has been reduced.

However, in the conventional water treatment system, the high-concentration raw water cannot be sufficiently diluted with only the washing water for the dehydrator, and a larger amount of water is required. In addition, as the amount of water for diluting raw water increases, the amount of water to be purified also increases, so that the water treatment facility eventually becomes large in scale, and initial costs such as construction costs and power consumption for water treatment and water supply are required. There has been a problem that running costs such as fees increase.

Further, when biological treatment of high-concentration wastewater is difficult, maintenance is difficult, and once the treatment system collapses, it takes several months to recover. There was a risk of environmental pollution because it would be released to the sea.

In order to solve such a problem, a treatment method has been proposed in which a chemical agent such as a polymer flocculant is used to chemically aggregate and separate the organic matter of the polymer in the raw water to reduce the concentration. However, there is a problem in that it is difficult to follow changes in concentration and the like, because the type of drug and the setting of the dose are delicate with respect to the concentration of organic substances.

In view of these problems, the present inventor has already made it possible to reduce the size of the liquid processing facility, reduce the initial cost and running cost, and at the same time, the water-soluble organic substance in the liquid can be easily operated. We have developed and applied for a liquid treatment method, liquid treatment device, and liquid treatment system that can reliably remove odors, microorganisms, etc., and can perform deodorization, decolorization, sterilization, liquid fragmentation treatment, and redox treatment. The invention is disclosed in JP-A Nos. 11-90420 and 2000-263056.

Here, the invention disclosed in the above-mentioned two publications describes a mixer tube used in the step of liquid subdivision processing.

This mixer pipe is constructed so that the liquid can be subdivided and charged when the treated water flowing in the pipe is mixed with a mixer. As shown in FIG. 90 Ga at the top and bottom
A uss neodymium plate 91 is arranged,
Inside the pipe 90, 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. The neodymium fin 93 is formed of a flat plate that is twisted in a spiral shape, and the neodymium magnet 92 is provided at the end portion in the width direction of the fin along the direction in which the treated water flows, by "N.
, NSSNNSS ... "are alternately buried in the order.

When the treated water is circulated in the mixer tube constructed as described above, the liquid molecules in the treated water are subdivided by the action of the magnetic field of the neodymium plate 91 and the mixer of the neodymium fin 93 to divide the negative electrons. Can be charged (ionized) to each other, and the colloidal particles of the dissolved substance in the treated water can be subdivided and charged with positive electrons to be aligned, respectively. It becomes possible to efficiently perform the treatment in the separation treatment step of fine liquid molecules and colloidal particles, which is a step after the subdivision charging treatment.

[0014]

As described above, the liquid processing apparatus which realizes the liquid processing method and the liquid processing system developed by the present inventor has solved the problems of the previous apparatus. As a further matter of concern, it is possible to flexibly carry out an appropriate subdivision charging treatment according to the properties of the suspended matter molecules of the liquid flowing in the mixer tube.

Therefore, the present invention improves the structure of the subdivision electrification treatment means for the waste in the treated water including the mixer pipe used for the subdivision electrification treatment, and is suitable for the property of the treated water flowing in the mixer pipe. An object of the present invention is to provide a liquid processing apparatus capable of performing a subdivision charging process.

[0016]

In order to achieve the above-mentioned object, the liquid treatment apparatus according to the first aspect of the present invention is characterized in that a spiral shape is formed in a tubular pipe along the longitudinal direction of the tubular pipe. The formed fins are rotatably arranged in the circumferential direction, and a mixer pipe in which N-pole and S-pole magnets are alternately embedded in the fins along the spiral direction, and the mixer pipe is provided outside the mixer pipe. An electromagnet capable of imparting a rotational force to the fins by applying a magnetic field to the magnets embedded in the fins, and the fins are rotated in the magnetic field generated by the electromagnets so as to be generated in the mixer tube. Electric power is generated, and the electromotive force is caused to act on the liquid subdivided by the mixer tube to charge-align the liquid molecules and the floating molecule, and, By the electromagnet depending on the nature of the serial liquid in that it is capable inverting the magnetic field applied to the magnet of the fin.

By adopting such a configuration, the fins are applied by the electromagnet in accordance with the liquid properties such as the polarities (positive / negative) of the ions of suspended matter molecules such as colloidal particles contained in the liquid. The direction of rotation of the fins can be reversed by reversing the magnetic field applied to the magnet of, so that the charge state of the suspended matter molecules can be unified,
It is possible to appropriately and flexibly perform the subdivision charging treatment of the liquid according to the property of the liquid.

The liquid treatment apparatus according to a second aspect is characterized in that, in the first aspect, the strength of the magnetic field applied to the magnet of the fin by the electromagnet can be changed according to the property of the liquid. is there.

By adopting such a constitution, it is possible to carry out 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.

The liquid treatment system according to claim 3 of the present invention is characterized in that the subdivision electrification treatment means is provided in a tubular pipe.
The fins formed in a spiral shape along the longitudinal direction of the tubular pipe are rotatably arranged in the circumferential direction, and N-pole and S-pole magnets are alternately embedded in each fin along the spiral direction. The mixer tube, and an electromagnet capable of imparting a rotational force to the fin by applying a magnetic field to the magnet embedded in the fin on the outside of the mixer tube. In (1), by rotating the fin, an electromotive force is generated in the mixer tube, and the electromotive force is applied to the liquid subdivided by the mixer tube to charge and align the liquid molecules and the floating molecule. And
It is possible to reverse the magnetic field applied to the magnet of the fin by the electromagnet according to the property of the liquid.

By adopting such a configuration, the magnetic field applied to the magnet of the fin by the electromagnet is reversed according to the property of the liquid such as the polarity of the ions in the liquid to change the direction of rotation of the fin. Since it can be reversed, the liquid can be appropriately and flexibly subjected to the subdivision charging treatment according to the property of the liquid, and the liquid treatment effect can be improved throughout the system.

The 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 by the electromagnet can be varied according to the property of the liquid. is there.

By adopting such a configuration, it is possible to perform more appropriate subdivision charging processing according to the properties of the liquid such as the concentration of suspended matter molecules contained in the liquid,
Further effective liquid purification can be provided throughout the liquid processing system.

[0024] [Detailed Description of the Invention]

[0025]

BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of a liquid processing apparatus 70 according to the present invention will be described below with reference to FIGS.

As shown in FIGS. 1 and 2, the liquid processing apparatus 70 in this embodiment has a mixer tube 71. The mixer tube 71 has a tubular pipe 72 made of ceramics or resin as a main body, and the inner surface of the tubular pipe 72 has an N pole neodymium magnet 7
3a and S-pole neodymium magnets 73b are arranged alternately so that rows of two neodymium magnets 73 are buried flush with the inner surface of the tubular pipe 72 so that the opposite polarities face each other. There is. In the present embodiment, as shown in FIG. 4, the row of the neodymium magnets 73 is embedded in the upper and lower positions inside the tubular pipe 72, and the neodymium magnets 73 are approximately 10,000 Gauss.
Shall have the magnetic force of.

In the tubular pipe 72, about 11
A neodymium magnet 75 having a magnetic force of 000 Gauss and a neodymium fin 75 made of a ceramic material embedded in the surface thereof is disposed rotatably in the circumferential direction.

The neodymium fin 75 acts as a fin for stirring on the treated water flowing in the cylindrical pipe 72. More specifically, in the present embodiment, it is a flat plate twisted in a substantially spiral shape. There are two types of shapes: a first fin 75a formed so as to rotate clockwise when receiving a flow of liquid flowing through the mixer pipe, and a second fin 75b formed so as to rotate counterclockwise. The fins are formed by alternately arranging them in the axial direction of the tubular pipe 72. As described above, the neodymium fins 75 are configured by alternately arranging the first fins 75a and the second fins 75b whose rotation directions are opposite to each other, whereby the treated water can be stirred more efficiently and the liquid The liquid molecules and the suspended solids therein can be effectively subdivided.

The first fin 75a and the second fin 75a
On the surface of the fin 75b, as shown in FIG. 4, the N pole neodymium magnets 74a and S are arranged along the direction in which the liquid flows.
The pole neodymium magnets 74b are alternately embedded.

On the outside of the mixer pipe 71,
A pair of electromagnets 100 for applying a magnetic field to the neodymium magnets 74a and 74b of the pair of neodymium fins 75 arranged in the mixer tube 71 are arranged so as to face each other with the mixer tube 71 interposed therebetween. It is set up.

Therefore, since the magnetic field of the electromagnet 100 can exert a magnetic force which is a repulsive force or an attractive force on the neodymium magnets 74a and 74b, the magnetic force can rotate the neodymium fins 75 in the circumferential direction. It is like this.

As described above, when the neodymium fins 75 rotate in the circumferential direction, the number of magnetic flux linkages passing through the neodymium fins 75 among the magnetic fluxes between the pair of electromagnets 100 changes abruptly. An induced electromotive force is generated in the neodymium fin 75 due to the change in the number of alternating electrodes.

Under the influence of this electromotive force, liquid molecules subdivided by the rotation of the neodymium fin 75 are charged as negative ions, and suspended matter molecules such as colloid particles are charged as positive ions or negative ions. It has become so.

The polarity of the charge of the floating substance molecules depends on the direction of the electromotive force generated by the neodymium fin 75.

Here, as a liquid, particularly in artificially produced industrial wastewater and the like, as floating substance molecules surrounding water molecules, those having positive ions and those having negative ions are mixed. If the polarities of the ions of the suspended matter molecules are not unified, it is difficult to efficiently perform the subsequent aggregation and separation. However, in the present embodiment, the floating material molecules can be uniformly charged to either positive or negative charges by using the neodymium fin 75. The water molecules are negatively charged.

Therefore, in this embodiment, it is possible to improve the efficiency of the coagulation and separation following the subdivision charging process by the mixer tube 71 and the electromagnet 100.

Further, in the present embodiment, the electromagnet 100 is adapted to reverse the magnetic field applied to the neodymium fin 75 according to the properties of the liquid such as the polarities of suspended matter molecules.

When reversing the magnetic field, the neodymium fin 75 switches its rotation in the opposite direction to the original rotation direction. Therefore, the switching of this rotation causes the direction of the electromotive force generated by the neodymium fin 75 to be opposite to the original direction. It is designed to switch in the direction.

When the electromotive force is switched, it is possible to reverse the charge polarity of the floating substance molecules.

For this reason, for example, since many floating ions have positive ions, the negative ions in the raw water are increased while those in which the electromotive force is applied in the direction of uniformly charging the floating molecule to positive ions. In this case, the electromotive force generated by the neodymium fin 75 is switched by the reversal of the magnetic field so that the suspended matter can be uniformly charged with negative ions.

Therefore, it is possible to flexibly perform an appropriate subdivision charging process according to the property of the liquid.

Further, in this embodiment, the electromagnet 1 is
00 is capable of varying the strength of the magnetic field applied to the neodymium fin 75 in accordance with the ion concentration of floating substance molecules contained in the liquid.

As a result, even when the ion concentration of the 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 properly performed. ing.

Further, an automatic controller 101 for controlling the magnetic field of the electromagnet is connected to the electromagnet.

A sensor 102 for measuring the polarity of ions in the treated water and the concentration of suspended matter molecules in real time is connected to the automatic control unit 101. This sensor 102
Is, for example, one in which a pair of electrodes (not shown) are brought into contact with the treated water, and the property of the liquid is automatically detected based on the current value or electric resistance value flowing between the electrodes. Good.

As described above, if the automatic controller 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.

Further, the electromotive force generated by the electromagnet 100 and the neodymium fin 75 acts on the microorganisms and bacteria in the treated water to kill them.
Alternatively, since the proliferation can be suppressed, the liquid can be purified more appropriately.

The arrangement position and the number of the sensors 102 described above can be variously changed according to the design concept. For example, the sensors are used to store the raw water supplied to the mixer pipe 71. Raw water tank 1 described later
6 or a first aggregating treatment tank 26, which will be described later, or the like.

Next, a concrete example of a liquid processing system using the mixer tube 71 having the above-described effects will be shown, and the operation and effects of the mixer tube 71 of the present embodiment will be further described.

FIG. 5 shows a specific example of the liquid treatment system, which is a filtration treatment means 1 for removing a solid suspended matter having a large specific gravity from raw water containing urine of pigs by a screen or the like.
Then, a microwave of an electromagnetic wave is oscillated in the still turbid raw water after filtration, and the electric field generated by the oscillates the first separation treatment means 2 for separating the colloidal particles and the liquid molecules, and the raw water after the separation is low. The first aggregating treatment means 3 for oscillating ultrasonic waves in the peripheral region to aggregate the colloidal particles and disperse the colloidal particles from the liquid molecules, and the liquid molecules in the raw water and the colloidal particles are subdivided by being mixed in the magnetic field. And a subdivided charging processing means 4 for aligning the charging while being subdivided,
In addition, the second separation treatment means 5 for oscillating the microwave of the electromagnetic wave again into the charged and treated treated water to separate it into fine colloidal particles and liquid molecules, and the treated water after the separation has a high frequency range. Deodorizing treatment means 6 for oscillating electromagnetic ultrasonic waves to remove a bad odor from the treated water, and ultrasonic waves in a low frequency region are oscillated into the treated water after the deodorizing treatment to agglomerate the colloidal particles and liquid molecules A second aggregating treatment means 7 for dispersing the treated water, and a decolorization and sterilization treatment of the treated water by applying a high voltage pulse to the treated water to separate and remove nitrogen from the treated water and generate ozone. High-voltage pulse processing means 8 of the above, aggregate discharge processing means 9 for absorbing and precipitating and discharging aggregates containing a metal substance such as heavy metal of the colloidal particles by magnetic force, and also referred to as clusters by the action of magnetic field. Liquid molecules refining treatment means 1 for generating an activated active water with finer liquid molecules that
0, a redox treatment means 11 for redox-reacting the treated water ionized by the charging treatment to return it to a stable state, a dehydration treatment means 12 for dehydrating the precipitate composed of the colloidal particles, It is composed of a centralized control means 13 which is connected to each of the processing means and controls each processing operation.

More specifically, each of the above-mentioned means will be described. The filtration processing means 1 is, as shown in FIG. 5, a filter body 14 such as a screen or a filter for filtering raw water, and a suspended matter after filtration. Dust residue receiver 15 for discharging
And a raw water tank 16 for storing the raw water after filtration.

Then, the filtering means 1 passes the raw water through the filter body 14 to filter out the solid suspended matter which has been separated from the water and is floating in the raw water, and the scrap residue receiver 15 It is designed to be discharged to. The raw water filtered by the filter body 14 is temporarily stored in a raw water tank 16 and then transferred by a 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 at its upper part with an inflow pipe 18 for inflowing the filtered raw water, and at the lower portion of the side surface, the first transfer pipe 18 is provided. The pipe 19a is connected so that the raw water is transferred to the next treatment stage by the suction force of the raw water transfer pump 17.

A first discharge pipe 20a for discharging the precipitate is connected to the bottom of the raw water tank 16, and the precipitate is transferred to the dehydration processing means 12 through the first discharge pipe 20a. It is supposed to be done.

In the raw water tank 16, the water dehydrated from the precipitate by the dehydrator 56 of the dehydrating means 12 described below and the water after cleaning the dehydrator 56 are allowed to flow. And is used for diluting raw water.

Next, the first separation processing means 2 will be described.

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 19a. An electromagnetic coil 23 is wound around the outer circumference of the processing pipe 22, and the first microwave oscillating tube body 2 has a circular tubular shape.
4 are provided. This first microwave oscillating tube 24
Is composed of a magnet such as a neodymium plate, the upper side of which is an N pole and the lower side of which is an S pole. And
From the first microwave oscillating tube 24, a frequency of 300 MHz to 16 GHz, more preferably 2.4 G to 10.
A microwave having a frequency of 5 GHz, more preferably 10.5 GHz, is oscillated. Such permanent magnets, electromagnets, and microwaves, which are electromagnetic waves, form a combined field of a magnetic field and an electric field, thereby separating colloidal particles and liquid molecules in raw water.

Here, as shown in FIG. 11, the microwave is considered to have an action mainly in which the raw water is destroyed to charge the colloidal particles and the liquid molecules and disperse them in pieces.

Then, the dispersed treated water is supplied to the second separation pipe 19 connected to the first separation treatment pipe 22.
It is transferred to the first aggregation processing means 3 through b.

Next, the first aggregation processing means 3 will be described.

As shown in FIGS. 5 to 7, the first aggregating treatment means 3 is provided with a first aggregating treatment tank 26, and the second aggregating treatment tank 26 is provided at the bottom thereof.
The transfer pipe 19b is connected to allow treated water to flow from the first separation treatment pipe 22.

In the first flocculation tank 26, as shown in FIGS. 7 and 8, a plurality of first low frequency ultrasonic waves are oscillated in a frequency range of 100 kHz or less according to the concentration of raw water. 1. A low-frequency ultrasonic oscillator 27 is provided. In this specific example, the first low-frequency ultrasonic oscillator 27 includes a first low-frequency ultrasonic oscillator 27a that oscillates an ultrasonic wave of 28 kHz or 40 kHz as a transverse wave, and 48 k.
The first low-frequency ultrasonic oscillating body 27b that oscillates ultrasonic waves of Hz or 100 kHz as transverse waves.
By the cavitation effect 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 disperses the aggregating colloidal particles and liquid molecules. Have a role. In addition, these ultrasonic output is 300W-
It is set to 1.2 kW.

A permanent magnet 28a such as neodymium is laid on the inner surface of the bottom of the first flocculation tank 26, and the second discharge pipe 20b is provided on the bottom.
Are connected. Therefore, the agglomerates of the colloidal particles in the charged state are attracted to the permanent magnet 28a and settled, and the deposits pass through the second discharge pipe 20b to the dehydration processing means 12. It is supposed to be transferred.

The treated water which has been subjected to the first stage coagulation treatment passes through the third transfer pipe 19c connected to the upper portion of the side surface of the first coagulation treatment tank 26 to the subdivision charging means 4. Be transferred. The third transfer pipe 19c
A pressurizing pump 29 is provided in the middle of the process, so that the treated water to be made to flow into the subdivision charging means 4 is made to flow in at an appropriate pressure.

An air discharge port 49 for discharging the air contained in the raw water is provided above the first flocculation tank 26.

Next, the subdivision charging means 4 will be described.

The subdivision charging means 4 has the same structure as the liquid processing apparatus 70 according to the present invention described above, and the subdivision charging means 4 includes the third transfer pipe 1
A subdivision charging pipe 30 connected to 9c is provided.

FIG. 3 shows an essential part of the constitution of the subdivision charging means 4, and the nozzle 2 of the pressurizing pump 29.
An appropriate pressure is applied by way of 9a and the diffuser 30, and the treated water whose flow velocity is increased is the element part 3
It is configured to flow through the mixer pipe arranged in No. 1.

In the element portion 31, cavitation phenomenon occurs in the tubular pipe 72 in the treated water supplied at a high flow rate. When this cavitation phenomenon occurs, hot spots are formed in the treated water, and places of ultra-high pressure and vacuum 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 fins 7 constituting the neodymium fins 75 disposed inside the mixer pipe 71.
The 5a and the second fin 75b act to vigorously stir the treated water to decompose liquid molecules and colloidal particles in the treated water, and promote uniform size. Further, neodymium magnets 73, 7 embedded in the inner surface of the tubular pipe 72 constituting the mixer pipe 71 and the neodymium fin 75.
No. 4 acts to generate electromotive force in the treated water rotating at high speed and increase the magnetization efficiency. Then, the generated electromotive force acts to uniformly charge the homogenized colloidal particles and align the ions.

Further, the neodymium magnet 7 of the pair of neodymium fins 75 arranged in the mixer tube 71.
A pair of electromagnets 100 for applying a magnetic field to 4a and 74b are arranged so as to face each other with the mixer tube 71 interposed therebetween. Therefore, due to the magnetic field of the electromagnet 100, the neodymium magnets 74a, 74a
Since a magnetic force which is a repulsive force or an attractive force can be applied to b, this magnetic force can rotate the neodymium fin 75 in the circumferential direction.

As described above, when the neodymium fins 75 rotate in the circumferential direction, the number of magnetic flux linkages penetrating the neodymium fins among the magnetic fluxes between the pair of electromagnets 100 changes abruptly. An induced electromotive force is generated in the neodymium fin 75 due to the change in the number.

Under the influence of this electromotive force, liquid molecules subdivided by the rotation of the neodymium fin 75 are charged as negative ions, and suspended matter molecules such as colloid particles are charged as positive ions or negative ions. It has become.

The polarity of the charge of the floating substance molecules depends on the direction of the electromotive force generated by the neodymium fin 75. Here, as the liquid, particularly in the suspended matter molecules contained in the artificially generated industrial wastewater and the like, those containing many positive ions and those containing many negative ions are mixed. If the polarities are not uniform, it is difficult to efficiently perform the subsequent coagulation separation treatment. However, in the present embodiment, the neodymium fin 75 is used to make the suspended matter molecules positive or negative. One side can be uniformly charged.

Therefore, in the present embodiment, it is possible to improve the efficiency of the coagulation separation subsequent to the subdivision charging process by the mixer tube 71 and the electromagnet 100.

Further, the electromagnet 100 is adapted to reverse the magnetic field applied to the neodymium fin 75 in accordance with the properties of the liquid such as the polarities of suspended matter molecules.
When reversing the magnetic field, the neodymium fin 75
Changes the rotation in the opposite direction to the original rotation direction.
The direction of the electromotive force generated by is switched to the opposite direction.

When the electromotive force is switched, it is possible to reverse the charge polarity of the floating substance molecules.

For this reason, since many floating ions are positive ions, when an electromotive force is applied in a direction to uniformly charge the floating molecules to positive ions, when the number of negative ions increases, Neodymium fin 7 by reversing the magnetic field
By changing the electromotive force generated by 5, the floating substance molecules can be uniformly charged with negative ions.

Therefore, it is possible to flexibly perform a proper subdivision charging process according to the property of the liquid.

Further, in the present embodiment, the electromagnet 1
00 is capable of varying the strength of the magnetic field applied to the neodymium fin 75 in accordance with the ion concentration of floating substance molecules contained in the liquid.

As a result, even when the ion concentration of the suspended matter molecules is low, an effective electromotive force can be obtained by increasing the strength of the magnetic field, and the subsequent subdivision charging process can be appropriately performed. It has become.

Further, the electromagnet 100 is connected with an automatic control section 101 for controlling the magnetic field of the electromagnet 100.

A sensor 102 for measuring the polarities and ion concentrations of the suspended matter molecules in real time is connected to the automatic control unit 101. The sensor 102 may be, for example, a device that brings a pair of electrodes (not shown) into contact with the liquid and automatically detects the property of the liquid based on the current value flowing between the electrodes. .

Further, for example, a pair of electrodes are brought into contact with a liquid, and a reference signal for measurement, which is an AC signal in an audible sound band, is oscillated from one electrode to the other electrode through the liquid, and this oscillation is performed. A signal is received by the other electrode through the liquid, and the received signal is
By performing synchronous detection based on the same signal as the measurement reference signal, the phase change of the signal received through the liquid is detected, and the ion concentration of the suspended molecule in the liquid is detected based on the detection result. You may make it measure. In addition,
In this case, the impedance of the liquid may be obtained from the phase change of the signal received by the electrode on the receiving side via the liquid, and the ion concentration may be calculated based on this impedance. In such a case, since the electric signal applied between the electrodes is an alternating current, it is possible to prevent deposits from accumulating on the electrodes and reduce the number of times of maintenance.

As described above, if the automatic controller 101 can automatically control the magnetization of the electromagnet based on the property of the liquid, the efficiency of the subdivision charging process can be further improved.

As described above, in the subdivided charging treatment means 4, finer colloidal particles which could not be removed by the first separating and aggregating treatment are ion-aligned and easily treated in the subsequent second separating and aggregating treatment step. You can prepare for this.

Next, the second separation processing means 5 will be described.

The second separation processing means 5 is the first separation processing means described above.
It has substantially the same configuration as the separation processing means 2. 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 subdivision charging processing pipe 30. An electromagnetic coil 34 is wound around the outer periphery of the pipe 33, and a second microwave oscillating tube body 35 is arranged. The second microwave oscillating tube body 35 is composed of a magnet such as a neodymium plate, and has an upper pole as an N pole and a lower pole as an S pole. Then, depending on the concentration of the treated water that flows in, a frequency of 300 M to 16 GHz, and more preferably 2.4 G from the viewpoint of performing separation treatment of colloidal particles.
~ 10.5 GHz frequency, more preferably 10.5
Microwaves in the frequency range of GHz are oscillated for about 1 μsec. When such microwaves are oscillated into treated water, the treated water is destroyed and finer colloidal particles and liquid molecules are formed. Will be scattered apart.

Thereafter, the dispersed treated water is transferred from the second separation treatment pipe 33 to the next deodorizing treatment means 6.

Next, the deodorizing means 6 will be described.

The deodorization processing means 6 is provided with a deodorization processing box 37 which is a high frequency electromagnetic ultrasonic oscillator, and the inside of the deodorization processing box 37 is connected to the second separation processing pipe 33 for deodorization. The processing pipe 38 is arranged so as to penetrate therethrough. As shown in FIG. 12, external magnets 39a having polarities of N pole and S pole are arranged at the upper and lower positions on the outside of the deodorization processing pipe 38, and at the axial center position of the deodorization processing pipe 38. Is arranged such that the rod-shaped internal magnet 39b has a polarity opposite to that of the external magnet 39a. In the first embodiment, the outer magnet 39a is formed of an electromagnet, and the inner magnet 39b is formed of a permanent magnet. Further, on the left and right side surfaces of the deodorization processing pipe 38,
Depending on the concentration of treated water, 3M to 300 MHz, more effectively, a longitudinal ultrasonic wave having a frequency of 100 MHz is applied for about 0.5 s.
A high-frequency ultrasonic oscillator 40 that oscillates in a cycle of ec is provided.

The treated water is the deodorizing treatment pipe 38.
In the first embodiment, the deodorizing process pipe 3 is used.
A nozzle (not shown) disposed in the nozzle 8 is provided with a vibrating plate (not shown) in the vicinity of the outlet of the nozzle. ing.

In addition, the external magnet 38a and the internal magnet 38
b and the high frequency ultrasonic oscillator 40 form a combined field by a magnetic field and an electric field, so that a so-called electromagnetic ultrasonic wave is generated. This electromagnetic ultrasonic wave crushes the amino acids of the colloidal particles and completely It is designed to remove odors from treated water.

The treated water deodorized by the deodorizing treatment pipe 38 is transferred to the second aggregating treatment means 7 which is the next treatment stage.

Next, the second aggregation processing means 7 will be described.

A second aggregating treatment pipe 41 is disposed in the second aggregating treatment means 7, and an electromagnetic coil 42 is wound around the outer periphery of the second aggregating treatment pipe 41 and the treatment is performed. A second low-frequency ultrasonic oscillator 43 that oscillates low-frequency ultrasonic waves in a frequency range of 50 kHz or less according to the concentration of water is provided.

When the second low-frequency ultrasonic oscillator 43 oscillates the low-frequency ultrasonic waves into the treated water, it negatively charges the liquid molecules and colloidal particles that are irregularly arranged. The liquid molecules present in the second agglomeration processing pipe 41
Colloidal particles that have been attracted to the wall surface side of and flow along the wall surface and are charged with positive ions.
The liquid molecules and the colloidal particles are dispersed and the colloidal particles are agglomerated with each other.

The treated water thus subjected to the second coagulation treatment is transferred to the next high voltage pulse treatment means 8.

The high voltage pulse processing means 8 is about 10 k
By applying a high voltage of ˜60 kV at different cycles, plasma is generated to remove nitrogen molecules in the treated water.

Therefore, as shown in FIG. 13, the high voltage pulse processing means 8 includes a high voltage pulse processing pipe 45.
Are arranged so as to be connected to the second coagulation processing pipe 41, and the high voltage pulse processing pipe 45 has a plurality of electrode bodies 46A as high voltage pulse generators applied at different periods. 46A ', 46B, 46B',
46C and 46D are arranged.

Between these electrode bodies 46A-46A 'and between electrode bodies 46B-46B', as shown in FIG.
20 μs when a voltage of 10 k to 30 kV is applied for 20 μs
After a lapse of time, the voltage is applied again for 20 μs, and after a lapse of 5 μs, the application of the voltage of the same pattern is repeated again.

On the other hand, between the electrode bodies 46C-46D, as shown in FIG.
As shown in 3, the voltage of about 60 kV is 5
It is applied for μs.

FIG. 16 shows the electrode bodies 46A, 46A.
The state changes of liquid molecules and colloidal particles when a voltage is applied are shown by ', 46B, 46B', 46C, and 46D. The large circle in FIG. 16 is a liquid molecule, and the small circle bound to it is a colloid particle. First, between the electrode bodies 46A-46A 'and between the electrode bodies 46B-46B'.
The high voltage pulse in between charges the liquid molecules to a negative charge and the nitrogen molecules to a positive charge. And the electrode body 46A
A high voltage pulse between -46B 'and between electrode bodies 46A'-46B causes an action of separating liquid molecules and nitrogen molecules, and a high voltage pulse between electrode bodies 46C-46D completely removes nitrogen molecules from the liquid molecules. Torn. At the same time as the nitrogen molecules are blown off, ozone molecules are generated by the bonding of the oxygen molecules being processed. This ozone decolorizes the treated water,
Moreover, it has a sterilizing effect.

Therefore, the high voltage pulse processing means 8
As a result, the treated water can remove nitrogen and can be decolorized and sterilized.

The fourth transfer pipe 1 is provided on the outflow side of the high voltage pulse processing pipe 45 of the high voltage pulse processing means 8.
9d are connected, and the treated water is transferred to the discharge treatment tank 48 which is the aggregate discharge treatment means 9 which is the next treatment stage.

Next, the aggregate discharge processing means 9 will be described.

The agglomerate discharge processing means 9 adsorbs and discharges downward the colloidal particles that have been agglomerated by the second separating and aggregating process by the permanent magnet 28b such as neodymium.

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 the treated water. At the bottom of the discharge processing tank 48, the fourth transfer pipe 1
9d is connected so that treated water containing agglomerates can flow in, and a permanent magnet such as neodymium 2
8b is laid so that the charged agglomerates of the treated water that has flowed in through the fourth transfer pipe 19d are attracted by the magnetic force of the permanent magnet 28b and settle to the bottom.

The sediment collected at the bottom of the discharge treatment tank 48 is discharged to the dehydration treatment means 12 through the third discharge pipe 20c connected to the bottom of the discharge treatment tank 48. Has become.

The magnetic force of the permanent magnet 28b is determined according to the organic matter concentration of the treated water.
Therefore, when treating 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. On the contrary, when treating low-concentration raw water, the magnetic force of the electromagnet is set to be small.

An air exhaust port 49 and an ozone exhaust port 50 are provided above the exhaust treatment tank 48 to exhaust the air such as nitrogen and ozone generated by the high voltage pulse process to the outside. It is like this.

The treated water from which aggregates and the like have been removed in the discharge treatment tank 48 passes through the fifth transfer pipe 19e connected to the upper portion of the side surface of the discharge treatment tank 48 to the next liquid molecule fragmentation. Transferred to the processing means 10.

Next, the liquid molecule subdivision processing means 10 will be described.

The liquid molecule subdivision processing means 10 is further adapted to subdivide the liquid molecules of the water purified by the above-mentioned respective treatments into active water by the action of a strong magnetic force.

Therefore, the liquid molecule subdivision processing means 1
As shown in FIGS. 5, 6 and 10, a subdivision processing tank 51 is disposed in the No. 0, and a cylindrical body 52 made of an insulating material such as ceramic is provided in the subdivision processing tank 51.
Are arranged such that the vertical direction is the longitudinal direction. The fifth transfer pipe 19e is connected to the upper side surface of the subdivision processing tank 51, and
An in-cylinder transfer pipe 53 that connects the fifth transfer pipe 19e and the cylindrical body 52 is provided. For this reason,
The water subjected to the liquid molecule subdivision processing is the fifth transfer pipe 1 described above.
9e and the tubular body 5 through the tubular body transfer pipe 53
It is designed to flow into the inside of 2.

The bottom 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. Therefore, when a current is applied to the electromagnetic coil, a force acting downward is generated inside the cylindrical body 52, and the inflowing treatment water is transferred toward the bottom of the liquid molecule subdivision treatment tank 51. It is like this.

On the other hand, the liquid molecule subdivision processing tank 51.
The inner surface of the top and bottom of the
Permanent magnets 28c and 28d such as aus neodymium are laid as magnetic field forming bodies, and a strong magnetic field is formed in the liquid molecule subdivision processing tank 51. Due to this strong magnetic force, the treated water becomes the liquid molecule subdivision treatment tank 5
When it passes through 1, the liquid molecules, so-called clusters, are further subdivided to generate activated water.

Therefore, the water after this treatment can exert a remarkable effect on its growth when it is used as drinking water for animals or when given to plants.

Further, the treated water in which the liquid molecules have been subdivided is discharged from the discharge pipe 54 connected to the upper portion of the side surface of the liquid molecule subdivision processing tank 51 and discharged as it is to a river or the like. Or, it can be used as water for animals and plants.

The liquid molecule subdivision processing tank 51 is used.
A fourth discharge pipe 20d is connected to the bottom of the
The final colloidal particles and the like adsorbed by the permanent magnet 28d laid on the bottom surface are discharged to the dehydration processing means 12.

Further, the liquid molecule subdivision processing tank 51.
An air outlet 49 and an ozone outlet 50 for discharging the air such as nitrogen and ozone remaining in the treated water are formed in the upper part of the.

Next, the redox processing means 11 will be described.

The oxidation-reduction processing means 11 is shown in FIGS.
And as shown in FIG. 10, it is comprised by the electrode member 55 which has four suitable electric potentials. On the surfaces of these electrode members 55, the treated water ionized by the above-described treatments exchanges electrons to cause a redox reaction. By this redox reaction, the treated water is returned from an ionized state where chemical reaction easily occurs to a stable state where chemical reaction hardly occurs.

In the first embodiment, the redox reaction is carried out as an electrode reaction via the electrode member 55, but an appropriate oxidizing agent or reducing agent may be used depending on the case.

Next, the dehydration processing means 12 will be described.

The dehydrating means 12 is provided with a dehydrator 56, which removes the water contained in the precipitate discharged from each treating means by the action of centrifugal separation or the like. There is. The dehydrator 56 can reduce the water content of the precipitate from about 98% to about 80%. For this reason, it becomes possible to perform the treatment more efficiently in the composting plant.

Further, as described above, the dehydrator 56 includes the water generated by the dehydration action and the dehydrator 56.
A pipe 57 for diluting raw water for transferring the wash water to the raw water tank 16 to dilute the raw water is connected.

On the other hand, the solid matter dehydrated by the dehydrator 56 is discharged to the solid matter receiving portion 58. After that, the solid matter is conveyed to the composting plant together with the solid matter filtered by the above-mentioned filtration treatment means 1, is composted as a compost raw material, and is reused as agricultural fertilizer.

Next, the centralized control means 13 will be described.

The centralized control means 13 is oscillated by the first separation processing means 2 as shown in the block diagram of FIG.
1st to control the output of microwave of 00M-16GHz
The microwave control unit 60, the first low-frequency ultrasonic control unit 61 for controlling the output of low-frequency ultrasonic waves of 100 kHz or less oscillated in the first aggregation processing unit 3, and the second separation processing unit 5 Second microwave control unit 62 for controlling the output of the microwave of 300 M to 16 GHz oscillated in
And 50 kHz oscillated in the second aggregation processing means 7.
The second low-frequency ultrasonic wave control unit 63 that controls the output of the following low-frequency ultrasonic waves, and 3 that is oscillated in the deodorization processing unit 6
A high frequency electromagnetic ultrasonic controller 64 for controlling the output of the high frequency electromagnetic ultrasonic waves of M to 300 MHz, and a high voltage pulse controller 65 for controlling the output of the high voltage pulse applied in the high voltage pulse processing means 8. And a voltage control unit 66 that controls the voltage applied to the electrode member 55 in the oxidation-reduction processing unit 11, and a dehydration control unit 67 that controls the operation of the dehydrator 56 of the dehydration processing unit 12. Each of these control units can be easily controlled by a switch (not shown) of the centralized control panel 68, and is normally automatically controlled.

Next, a liquid processing method using the above liquid processing system will be described.

First, raw water containing swine effluent, industrial effluent, etc. is passed through the screen of the filtration treatment means 1 to be filtered to remove the colloidal particles separated in the raw water, and the colloidal particles are discharged to the residue receiver 15. At the same time, the filtered raw water is temporarily stored in the raw water tank 16.

Then, the raw water transfer pump 17 sucks the raw water from the raw water tank 16 and transfers it to the first separation treatment pipe 22 of the first separation treatment means 2. Under the control of the first microwave control unit 60, the first separation processing means 2 oscillates a microwave of 10.5 GHz from the first microwave oscillating tube 24 to the raw water, and liquids the raw water. Separate into molecules and colloidal particles. The separated treated water is transferred to the first flocculation processing means 3 through the second transfer pipe 19b. The first coagulation processing means 3 controls the treated water by the control of the first low-frequency ultrasonic controller 61.
28 kHz from the first low-frequency ultrasonic oscillators 27a and 27b
An ultrasonic wave of any one of z, 40 kHz, 48 kHz and 100 kHz is oscillated to agglomerate the colloidal particles and disperse them from the liquid molecules. And the first
A permanent magnet 28a arranged on the bottom surface of the aggregating tank 26 adsorbs and agglomerates the agglomerated colloidal particles and discharges them to the second exhaust pipe 20b.

On the other hand, the treated water is transferred to the subdivision charging means 4 with a proper pressure by the pressurizing pump 29 through the third transfer pump. In the subdivision charging processing means 4, the floating material molecules in the raw water are subdivided by rotation of the mixer tube 71 of the neodymium fin 75, and a magnetic field is applied to the neodymium fin 75 by the electromagnet 100 to generate an electromotive force. Then, the electromotive force charges the liquid molecules and the floating molecules surrounding the liquid molecules. As a result, the polarities of the ions of suspended matter molecules such as fine colloid are unified to either positive or negative, the liquid molecules are negatively charged, and the subdivision charging process of the treated water is completed.

At this time, the automatic control unit 101 determines that the sensor 1
Since the magnetic field of the electromagnet can be reversed or the strength of the magnetic field can be changed according to the property of the treated water based on the detection result of No. 2, an appropriate subdivision charging process can be performed according to the property of the treated water.

Subsequently, the water that has been subjected to the subdivision charging treatment is transferred to the second separation treatment means 5. This second separation processing means 5
Is the second microwave controller 62 of the centralized control means 13.
By the control, the second microwave oscillating tube 35 oscillates a microwave of 10.5 GHz to the treated water to separate the treated water into liquid molecules and colloidal particles. The separated treated water is transferred to the deodorizing means 6.

The deodorization processing means 6 is controlled by the high frequency electromagnetic ultrasonic wave control section 64 of the centralized control means 13 to drive the high frequency ultrasonic oscillator 40 to about 100 MHz in a magnetic field.
The ultrasonic waves of are oscillated into the treated water, and the odor is removed from the treated water by this electromagnetic ultrasonic wave.

The deodorized treated water is treated by the second flocculating means 7
Be transferred to. The second aggregating treatment means 7 applies the second low-frequency ultrasonic controller 6 of the centralized control means 13 to the treated water.
By the control of 3, the second low-frequency ultrasonic oscillators 43 to 50
Ultrasonic waves of kHz or less are oscillated to aggregate the colloidal particles and disperse them from the liquid molecules.

Then, the treated water which has been subjected to the second flocculation treatment is transferred to the high voltage pulse treatment means 8. The high voltage pulse processing means 8 is controlled by the high voltage pulse control section 65 of the centralized control means 13, and the electrode bodies 46A-46 are controlled.
10 between A ′ and between electrode bodies 46B-46B ′
While applying a voltage of k to 30 kV, the electrode body 46C
A voltage of about 60 kV is applied between −46 D to generate plasma to separate and remove nitrogen contained in the treated water. Further, ozone generated at this time decolorizes and sterilizes the treated water.

The water from which nitrogen has been removed is supplied to the fourth transfer pipe 1
It is transferred to the discharge processing tank 48 of the aggregate discharge processing means 9 through 9d.

In the discharge treatment tank 48, the permanent magnet 28b adsorbs the aggregate of colloidal particles by magnetic force and precipitates it at the bottom of the discharge treatment tank 48, and the third discharge pipe 20c to the dehydration treatment means 12. Transfer.

The treated water from which the agglomerates have been removed is transferred from the supernatant through the fifth transfer pipe 19e to the liquid molecule fragmentation processing tank 51 of the liquid molecule fragmentation processing means 10. The liquid molecule subdivision 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 subdivision processing tank 51 to further subdivide the liquid molecules of the inflowing treatment water. Generates active water.

Also, the liquid molecule subdivision processing tank 51.
In the inside, the electrode member 55 of the oxidation-reduction treatment means 11 performs a treatment for performing an oxidation-reduction reaction on the treated water ionized on its surface to return it to stable treated water.

After that, the water that has been subjected to the subdivision processing and the redox processing is discharged from the discharge pipe 54 and discharged to the river, or is used as drinking water for animals or nutrient water to be given to plants.

On the other hand, the precipitates of colloidal particles discharged in each processing stage are the first discharge pipe 20a, the second discharge pipe 20b, the third discharge pipe 20c and the fourth discharge pipe 2.
It is transferred to the dehydrator 56 of the dehydration processing means 12 through 0d respectively. In this dehydrator 56, the solid matter is subjected to a centrifugal action under the control of the dehydration controller 67 of the central control means 13 to remove water from the precipitate.

Then, the water removed by the dehydrator 56 is used together with the wash water for the dehydrator 56 to dilute the raw water pipe 57.
The raw water is transferred to the raw water tank 16 and used for diluting the raw water. On the other hand, the dehydrated solid matter is stored in the solid matter receiving portion 58 and then transported to the composting plant to be used as agricultural compost.

As described above, according to the liquid treatment method using the liquid treatment apparatus of this example, colloid particles (including heavy metals) and nitrogen contained in raw water such as swine effluent and industrial chemical effluent can be reliably discharged. In addition to being deodorized, decolorized, and sterilized, it is possible to generate stable water that is active water composed of extremely finely divided liquid molecules, and the liquid treatment apparatus 70 of the present invention can perform the liquid treatment. In the method, for example,
Depending on the properties of the liquid, such as the polarity of the ions of the suspended matter molecules contained in the liquid and the ion concentration, the magnetic field applied to the magnet of the fin by the electromagnet can be reversed to reverse the direction of rotation of the fin. It is possible to unify the charged state of the object molecules, and perform the subdivided charging treatment of the liquid appropriately and flexibly according to the property of the liquid.

The present invention is not limited to the above-mentioned embodiment, and various modifications can be made if necessary.

[0147]

As described above, according to the liquid treatment apparatus and the liquid treatment system having the same according to the present invention, various substances such as liquid molecules and colloidal particles contained in treated water are subdivided and charged. Can be processed properly and efficiently according to the properties of the liquid, and by using this mixer pipe in the liquid processing system, the liquid processing system can be downsized and the initial cost and running cost can be reduced. In addition, by making the liquid molecules finer, it is possible to reliably remove suspended matter in the liquid and improve the quality by deodorizing, decolorizing and sterilizing, and it can be used in a wider range of fields. Become.

[Brief description of drawings]

FIG. 1 is a sectional view showing an embodiment of a liquid processing apparatus according to the present invention.

FIG. 2 is a sectional view showing an embodiment of a liquid processing apparatus according to the present invention.

FIG. 3 is an explanatory diagram showing a main part of a subdivision charging processing means in an embodiment of a liquid processing system according to the present invention.

FIG. 4 is a sectional view showing the structure of a mixer tube according to the present invention.

FIG. 5 is a flow chart 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 line I-I of FIG.

FIG. 8 is an explanatory view seen from the direction II-II in FIG. 6.

9 is an explanatory view seen from the direction III-III in FIG.

10 is a sectional view taken along 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 diagram showing a main part of a deodorizing treatment means in the embodiment of the liquid treatment 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 a 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 an embodiment of a liquid processing system according to the present invention.

FIG. 18 is a 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 processing means 7 Second agglomeration processing means 8 High voltage pulse processing means 9 Aggregate discharge processing means 10 Water molecule subdivision processing means 11 Redox treatment means 12 Dehydration treatment means 13 Centralized control means 14 Filter 15 Screen residue receiver 16 Raw water tank 17 Raw water transfer pump 18 Inflow pipe 19 Transfer pipe 20 First discharge pipe 22 First separation processing pipe 26 First flocculation tank 27 1st low frequency ultrasonic oscillator 29 Pressurizing pump 30 Subdivision charging pipe 33 Second separation processing pipe 38 Deodorizing pipe 41 Second flocculation pipe 43 Second low frequency ultrasonic oscillator 45 high voltage pulse processing pipe 48 Emission treatment tank 49 Air outlet 50 Ozone outlet 51 Subdivision processing tank 52 cylinder 54 Discharge pipe 56 dehydrator 58 Solid receiving part 68 Central control panel 70 Liquid treatment equipment 71 mixer tube 72 Cylindrical 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 Second fin 100 electromagnet 101 Automatic control unit 102 sensor

─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. ⁷ Identification code FI theme code (reference) C02F 1/78 C02F 1/78 F term (reference) 4D037 AA11 AB04 BA26 CA04 CA05 CA12 4D050 AA13 AA14 AB03 AB04 BB02 BC10 CA07 CA10 4D061 DA08 DB01 DB16 DC03 DC04 EA13 EA19 EB01 EB07 EB39 EC05 EC19 GC11 GC20

Claims (4)

[Claims] 1. A liquid containing a floating substance is mixed in a magnetic field, and liquid molecules in the liquid and floating substance molecules are subdivided and charged and aligned, thereby separating the liquid molecules from the floating substance molecules. In a liquid processing device for facilitating operation, a fin formed in a spiral shape along the longitudinal direction of the tubular pipe is arranged in a tubular pipe so as to be rotatable in the circumferential direction, and the fin has an N pole. A mixer tube in which magnets of S and S poles are alternately embedded along the spiral direction, and a rotational force can be applied to the fin by applying a magnetic field to the magnet embedded in the fin on the outside of the mixer tube. And a generated electromagnet, by causing the electromotive force in the mixer tube by rotating the fin in a magnetic field by the electromagnet,
The electromotive force is applied to the liquid atomized by the mixer tube to charge and align the liquid molecules and the floating substance molecules, and the electromagnet causes the liquid molecules and the floating substance molecules to be aligned. A liquid processing apparatus, wherein a magnetic field applied to a fin magnet is reversible. 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. 3. Separation treatment means for oscillating microwaves into treated water containing at least suspended matter to separate suspended matter molecules and liquid molecules, and a liquid after separating the suspended matter molecules to a liquid having a low frequency range. Aggregation treatment means for oscillating a sound wave to aggregate the floating substance molecules, subdivision charging treatment means for charging and aligning while subdividing the liquid molecules and the floating substance molecules in the liquid by mixing in a magnetic field, and a liquid Deodorization processing means that oscillates electromagnetic ultrasonic waves in the high frequency range to deodorize the liquid, and decolorization of the liquid by applying a high-pressure pulse to the liquid to separate and remove nitrogen from the liquid and generate ozone. And a liquid treatment system having a high-pressure pulse treatment means for sterilization and an aggregate discharge treatment means for adsorbing and ejecting aggregates of the suspended matter molecules by magnetic force, wherein the subdivision charging means is Fins spirally formed along the longitudinal direction of the tubular pipe are arranged in the tubular pipe so as to be rotatable in the circumferential direction, and magnets of N pole and S pole are provided in the fins in the helical direction. A mixer tube alternately embedded along the outer side of the mixer tube, and an electromagnet capable of imparting a rotational force to the fin by applying a magnetic field to the magnet embedded in the fin on the outside of the mixer tube. Generating an electromotive force in the mixer tube by rotating the fin in a magnetic field by the electromagnet,
The electromotive force is applied to the liquid atomized by the mixer tube to charge and align the liquid molecules and the floating substance molecules, and the electromagnet causes the liquid molecules and the floating substance molecules to be aligned. A liquid treatment system characterized in that a magnetic field applied to a magnet of a fin can be reversed. 4. 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.