JP2003205291A - Liquid quality improvement method, its device and highly functional water production device using the same - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To obtain desired liquid by applying cleaning, activation and quality improvement to various kinds of liquid such as contaminated pond water to a required level, for example, a level at which the liquid is dischargeable, a level at which the liquid is usable for plant cultivation and breeding and culture of fishes and shell fishes and, moreover, a high level at which the liquid is drinkable and is profitable for human health. <P>SOLUTION: In this liquid quality improvement method, the liquid to be treated is subjected to quality improvement treatment S1... comprising filter medium treatment of passing the liquid through filter medium and magnetic treatment of passing the same through a magnetic field, the liquid subjected to the quality improvement treatment S1... is circulated to the filter medium, therein, the circulation is performed by jetting the liquid subjected to the quality improvement treatment and intense collision is caused between the liquids and between the liquid and the filter medium. <P>COPYRIGHT: (C)2003,JPO

Description

Detailed Description of the Invention

[0001]

TECHNICAL FIELD The present invention relates to water in ponds and lakes,
Various liquids such as domestic wastewater, industrial wastewater, rainwater, groundwater, night soil, seawater, and tap water can be discharged to a required level, for example, a level that can be discharged, a level that can be used for cultivating plants and raising and aquaculture of seafood, Further, the present invention relates to a technique for purifying, activating and modifying the substance to a high level which is good for human health by drinking it to obtain a desired liquid.

[0002]

2. Description of the Related Art As a technique for purifying sewage, there is, for example, an apparatus disclosed in Japanese Patent Laid-Open No. 9-327695. This purification device has a magnetic treatment device that magnetically treats raw water and a filter medium that allows microorganisms useful for water purification to live and filter, and the raw water activated by the magnetic treatment device is passed through the filter medium. It is a structure to return it to raw water after it is released.

In this apparatus, however, a filter is provided in front of the magnetic treatment device to remove visible dust from the raw water, but since the magnetic treatment is performed by itself, the effect of activating the water by the magnetic treatment is sufficient. Can not enjoy. Therefore, it is very dirty like lakes and marshes, and it is difficult to purify a large amount of raw water.

[0004] Further, the dust and the like captured by filtering reverses the water and returns it to the raw water, but it simply reverses it.
Although it depends on the degree of dirt, it is difficult to perform sufficient cleaning, and frequent backflow and replacement of the filter media are required.

Further, since the filter material is made of plastic, it does not positively improve the water quality, and relies solely on magnetism. Therefore, the dust and the like returned to the raw water are only affected by the water in an insufficiently activated state by the magnetic treatment, and the purification efficiency is poor.

[0006]

SUMMARY OF THE INVENTION Therefore, according to the present invention, the effect of magnetic treatment can be sufficiently exerted to efficiently purify a large amount of water such as lakes and marshes that are severely contaminated. Instead of that, the main issue is to modify various liquids, for example, to produce water that is useful for the natural world and the human body.

[0007]

[Means for Solving the Problems] A means for that purpose is to perform a modification treatment consisting of a filtration material treatment in which a liquid to be treated is passed through a filter medium and a magnetic treatment in which a fluid is passed through a magnetic field. The liquid reforming method is characterized in that the recirculation is performed by jetting the liquid to be treated after the reforming treatment, and the liquids to be treated and the liquid to be treated and the filter medium are violently collided with each other.

The filter medium treatment and the magnetic treatment in the above-mentioned modification treatment are
The treatment method, the sequence, and the stage are appropriately set according to the state of the liquid to be treated and the intended modification. That is, for example, when purifying water in a pond, a lake, or the like, it is preferable to perform the filter medium treatment and then the magnetic treatment. When reforming tap water, magnetic treatment can be directly performed.

For the above magnetic treatment, a permanent magnet is used to subdivide and activate clusters (groups of molecules) by passing water in a magnetic field. For example, it is disclosed in Registered Utility Model No. 3033968. It is preferable to use a well-known structure having such a structure. Further, for the filter material treatment, in addition to an appropriate filter such as a fiber filter for performing solid-phase filtration, a wire mesh filter, or a ceramic filter, it is preferable to use a porous granular filter material for releasing the active ingredient. In particular, when a far-infrared radiator is used as the filter medium, the energy level of the liquid to be treated can be increased, so that the activation effect by the magnetic treatment can be improved. The arrangement of the filter media is appropriately combined depending on the properties of the filter media. If you want to increase the mineral content,
For example, natural stone capable of eluting minerals may be used as the filter medium.

By subjecting the liquid to be treated to filter medium treatment,
If impurities such as dust are removed and a material that releases active ingredients such as natural minerals is used for the filter medium, the energy level is raised and activated, minerals are replenished, and the action depending on the filter medium is performed. . Further, when the liquid to be treated is subjected to magnetic treatment, the clusters of the liquid to be treated are subdivided into fine particles and activated, and the impurities dissolved in the clusters are discharged to enhance the cluster precision. Be affected. Since the filter material treatment and the magnetic treatment are carried out in the reforming treatment, the synergistic effect which cannot be obtained by only one of them is effective and the high-level reforming can be performed.

The liquid to be treated which has been reformed through the reforming treatment is
If necessary, it can be discharged for use, or returned to the portion where the liquid to be treated is collected to purify and activate the portion, and can also be returned to the filter medium for filter medium treatment to The liquid to be treated in the vicinity is purified and activated. That is, if the liquid is jetted at the time of reflux, the liquids to be treated collide with each other or the liquid to be treated and the filter medium violently collide with each other. As a result, a high degree of precision is obtained, and a higher level active state is entered.

[0012] It should be noted that, when it is refluxed to the filter medium, it is preferable to backwash the filter medium. That is, the back-cleaning is to remove dust and the like from the filter medium by flowing in a direction opposite to the direction in which the liquid to be treated flows during the reforming treatment, and this back-cleaning is performed by jetting as described above. When the treatment liquids or the treated liquid and the filter medium are violently collided with each other, the filter medium is cleaned cleanly, and is subjected to the action of the filter medium more than when the treated liquid simply flows in contact with the filter medium. In particular, a liquid in which clusters are subdivided and activated exhibits high fluidity and can dissolve many substances, so it is a natural stone that causes violent collisions, cleans the filter media, and causes the filter media to act on the liquid. In the case of the above, it is well dissolved to obtain the active ingredient positively. As a result, the clusters of the liquid to be treated are further atomized (activated) as compared with the case where a normal liquid simply collides.
The desired modification can be performed.

As described above, the liquid to be treated is highly activated, and can be activated to a state close to, for example, a supercritical liquid, and efficient reforming can be performed.

The fact that the cluster becomes smaller means that there is no extra substance in the cluster, and that the ultrafine particles make the purity higher, and if the water is water, the original function of water is restored. Such ultra-polymer magnetic water produces various effects due to its inherent high functionality. For example, activating the liquid in the injected part, suppressing scale and rust in water pipes, decomposing filtered impurities, suppressing the generation of scales, etc. Various effects can be obtained, such as shortening the boiling time by improving the thermal conductivity and removing organic substances and heavy metals. Drinking water, in particular, makes mellow and delicious water, makes tea and food delicious, and gives it to plants and animals to grow well.

If the above-mentioned reforming treatment is carried out in a plurality of stages, and the reforming treatment on the subsequent stage side is subjected to magnetic treatment with a stronger magnetic field, the stronger magnetic field acts according to the flow of treatment, so that the cluster of the liquid to be treated is higher. It is possible to reliably raise the energy state to a desired active state.

A large number of granular far-infrared radiators may be used as the filter medium. This is because, as described above, a synergistic effect is produced by combining the activation action by magnetism with the activation action by far infrared rays, and the liquid to be treated can be activated more efficiently. In particular, when the liquid to be treated that has undergone the reforming treatment is refluxed to be floatable, the liquid to be treated can collide with the filter medium and the liquid to be treated more vigorously and vigorously, so that the effect can be enhanced.

In addition to the far-infrared radiator, as a filter medium containing a natural mineral that releases an active ingredient and removes a harmful ingredient, for example, zeolite, barley stone, sodalite, soil of soft porous ancient humus, limestone By using (calcium), metamorphic granite (various kinds of minerals), iron sulfate (magnetic), etc., it is possible to obtain mineral water that is good for use as drinking water. As a matter of course, it is preferable to form a large number of particles as described above and fill them so that they can freely move around by the reflux of the liquid to be treated.

Another means is to provide a reforming processing section having a filter medium processing section for passing the liquid to be processed through a filter medium and a magnetic processing section for passing a magnetic field, and the processed liquid to be processed is provided at a stage subsequent to the reforming processing section. Is a liquid reforming apparatus which is provided with a recirculation path for recirculating the liquid to the filter medium processing section, and at the tip of the recirculation path is provided an injection means for injecting the liquid to be treated against the filter medium to strongly collide with it. And

That is, as in the above description, the filter medium treating section and the magnetic treating section in the reforming treating section are constructed according to the state of the liquid to be treated and the intended reforming, the treatment section structure, the order and the steps. Are appropriately set and performed. For example, when purifying water from a pond, a lake or the like, it is preferable to dispose the filter medium processing unit before the magnetic processing unit. When reforming tap water, it is also possible to directly perform magnetic treatment.

The magnetic processing section is formed by using a permanent magnet and subdivides and activates a cluster (group of molecules) by passing water through a magnetic field. For example, it is disclosed in Registered Utility Model No. 3033968. It is preferable to use a device having a well-known structure as described above. In addition, the filter material processing unit is a fiber filter or a wire mesh filter that performs solid-phase filtration,
In addition to a suitable filter such as a ceramic filter, it is preferable to use a porous granular filter medium that releases the active ingredient. Especially when a far infrared radiator is used as the filter medium,
Since the energy level of the liquid to be treated can be increased, the effect of activation by the magnetic treatment can be improved. The arrangement of the filter media is appropriately combined depending on the properties of the filter media. When it is desired to increase the mineral content, for example, natural stone capable of eluting minerals may be used as the filter medium. A mineral concentrate may be injected.

When the liquid to be treated passes through the filter medium treatment section, impurities such as dust are removed, and if a material releasing an active ingredient such as a natural mineral is used for the filter medium, the energy level is raised and activated. , Is replenished with minerals and is affected by the filter material. Also,
By passing the liquid to be processed through the magnetic processing section, the clusters of the liquid to be processed are subdivided into fine particles and activated,
Impurities dissolved in the clusters are discharged to improve the cluster precision and are affected by magnetism. Since the reforming treatment section has the filtering medium treating section and the magnetic treating section, the synergistic effect which cannot be obtained by only one of them enables efficient and high-level reforming.

The liquid to be treated which has been reformed through the reforming treatment section is discharged for use, if necessary, or returned to a portion where the liquid to be treated is accumulated to purify and activate the portion. In addition to liquefying, it is refluxed to the filter medium processing section through the reflux path and jetted by the jetting means. Then, the filter medium and the liquid to be treated in the vicinity thereof are purified and activated. That is, since the liquid is ejected when refluxed, the liquids to be treated, or the liquids to be treated and the filter medium violently collide with each other, and the clusters of the liquids to be finely divided are further subdivided into ultrafine particles. Higher precision will be obtained and a higher level of activation will be achieved.

It should be noted that when it is returned to the filter medium processing section, it is preferable to back-clean the filter medium. That is, the back-cleaning is to remove dust and the like from the filter medium by flowing in a direction opposite to the direction in which the liquid to be treated flows during the reforming treatment, and this back-cleaning is performed by jetting as described above. When the treatment liquids or the treated liquid and the filter medium are violently collided with each other, the filter medium is cleaned cleanly, and is subjected to the action of the filter medium more than when the treated liquid simply flows in contact with the filter medium. In particular, a liquid in which clusters are subdivided and activated exhibits high fluidity and can dissolve many substances, so it is a natural stone that causes violent collisions, cleans the filter media, and causes the filter media to act on the liquid. In the case of the above, it is well dissolved to obtain the active ingredient positively. As a result, the clusters of the liquid to be treated are further made into fine particles (activated) as compared with the case where a normal liquid simply collides, and desired modification can be performed.

As described above, the liquid to be treated is highly activated, and can be activated to a state close to, for example, a supercritical liquid, and efficient reforming can be executed.

The fact that the cluster becomes small means that there is no extra substance in the cluster, and that by making the particles ultrafine, the purity is increased, and in the case of water, the original function of water is restored. Such ultra-polymer magnetic water produces various effects due to its inherent high functionality. For example, activating the liquid in the injected part, suppressing scale and rust in water pipes, decomposing filtered impurities, suppressing the generation of scales, etc. Various effects can be obtained, such as shortening the boiling time by improving the thermal conductivity and removing organic substances and heavy metals. Drinking water, in particular, makes mellow and delicious water, makes tea and food delicious, and gives it to plants and animals to grow well.

The filter medium processing section may be formed by filling a number of granular far-infrared radiators. As mentioned above,
This is because a synergistic effect is produced by combining the activation action by magnetism with the activation action by far infrared rays, and the liquid to be treated can be activated more efficiently. In particular, when the liquid to be treated that has undergone the reforming treatment is refluxed to be floatable, the liquid to be treated can collide with the filter medium and the liquid to be treated more vigorously and vigorously, so that the effect is enhanced.

In addition to far-infrared radiators, as filter media containing natural minerals that release active ingredients and remove harmful ingredients, for example, zeolite, barley stone, sodalite, soil of soft porous ancient humus, limestone By using (calcium), metamorphic granite (various kinds of minerals), iron sulfate (magnetic), etc., it is possible to obtain mineral water that is good for use as drinking water. As a matter of course, it is preferable to form a large number of particles as described above and fill them so that they can freely move around by the reflux of the liquid to be treated.

This liquid reforming apparatus can be easily used by itself by placing it in a housing as a unit and providing an appropriate moving means such as casters on the lower surface of the housing. It becomes easy to use in combination with the apparatus as appropriate, and it can be easily used for reforming treatment of various liquids in various situations, and the availability of the liquid reforming apparatus can be expanded.

Still another means is to dispose a magnetic treatment device for passing a liquid to be treated in a magnetic field at a front stage and / or a rear stage of the liquid reforming device, and the magnetic treatment device and the magnetic treatment of the liquid reforming device. The magnetic field in the section is set stronger toward the rear side, and an auxiliary device that processes the liquid to be treated according to the target reforming state is connected to the front stage and / or the rear stage of the liquid reforming device. It is a liquid reforming system.

That is, by appropriately connecting the magnetic treatment device and the auxiliary device to the liquid treatment device having the reforming treatment portion having the filter medium treatment portion and the magnetic treatment portion, the reflux passage, and the injection means, various treatments can be performed. It can be used for various purposes in various situations. For example, if an apparatus having a filter medium treating section and a magnetic treating section is used as an auxiliary apparatus, a sterilizing apparatus is used, or a precipitation treating apparatus is used as an auxiliary apparatus, the apparatus can be used depending on the apparatus. A desired effect can be applied to the liquid to be treated. In addition, since the magnetic treatment device is connected so that the magnetic field becomes stronger toward the later stage, the liquid to be treated can be gradually changed to a higher active state, and the action of the auxiliary device can be efficiently performed.

Still another means is to provide a modification treatment section having a filter medium treatment section for passing the liquid to be treated through the filter medium and a magnetic treatment section for making a magnetic field act on the liquid to be treated which has passed through the filter medium treatment section. In the subsequent stage of the reforming treatment section, a discharge path for supplying the treatment target fluid that has passed through the reforming treatment section, a storage section for temporarily storing the treatment target solution before the treatment by the reforming treatment section, and the filter medium treatment section A high-performance water production method in which a reflux passage for returning to the filter material is provided It is a device.

That is, the liquid to be treated which has passed through the filter medium processing section and the magnetic processing section in this order and has exited the reforming processing section passes through the reflux channel except before being supplied through the discharge channel, before being processed by the reforming processing section. The liquid to be processed is refluxed to the storage part for temporarily storing it and the filter medium processing part.

Since the liquid to be treated passes through the magnetic treatment portion after passing through the filter medium treatment portion, the action of the magnetic treatment portion can be efficiently received. In other words, magnetically subdivides the cluster,
The impurities are removed and activated. Moreover, when the activated liquid to be treated is recirculated, a jetting means is provided at the tip of the recirculation path that recirculates to the filter medium processing unit, so that the liquid to be treated is strongly squirted against the filter medium. Due to this spraying, the liquids to be treated collide strongly with each other. By this collision, the water activated in the magnetic treatment unit is further atomized (activated) and the filter medium can be washed. Further, if the filter medium releases the active ingredient by strongly hitting the filter medium, the desired action of the filter medium can be efficiently received.

At this time, it is advisable to strongly flush the filter medium in a direction opposite to the normal direction so that the filter medium is backwashed. The filter medium can be actively washed. Further, by providing a jetting means on the side opposite to the backwashing and jetting the liquid to be treated from two opposite directions, not only the filter medium and the liquid to be treated but also violent collision between the liquids to be treated is positive. Therefore, the liquid to be treated can be more effectively activated.

It is preferable that the filter material treating section is composed of a granular material containing a natural mineral that releases an active ingredient as a filter material so as to be floatable. The filter medium containing a natural mineral that releases the active ingredient includes, for example, far-infrared emitting ceramics that emits far-infrared rays, iron sulfate that emits magnetism, and
There are a variety of other natural stones and soils, such as zeolite, barite, sodalite, limestone, metamorphic granite, and soft porous ancient humus. It may be appropriately selected according to the purpose and action. Such a filter medium is formed in a granular shape such as a sphere, and is filled so as to be freely floatable by the above reflux.

If a far-infrared radiator is used among the above examples, the liquid to be treated can be made to have a high energy level by far-infrared radiation, so that the treatment effect of the magnetic treatment section can be improved.

The liquid to be treated is filtered and reformed while passing through these filter materials alone or appropriately blended. Then, when it is refluxed, it collides violently with the liquid to be treated and the filter medium, and the filter medium is washed.

A magnetic processing unit for magnetically treating the liquid to be treated is provided in at least the return passage of the return passage that returns to the storage unit, and the magnetic field of the magnetic treatment unit is set to be greater than the magnetic field of the preceding magnetic treatment unit. Should be set to be strong. The liquid to be processed which returns to the storage part is activated to a higher level by the magnetic processing part and flows back in this state, so that the liquid to be processed in the storage part is highly modified.

Even when the liquid is recirculated to the storage portion, if it is jetted and recirculated, the liquid to be treated in the storage portion can also obtain a good reforming action due to the violent collision of molecules with each other.

In order to use the highly functional water obtained by reforming as drinking water, it is preferable to provide a sterilization treatment section constituted by using, for example, ozone or ultraviolet rays in order to sterilize the liquid to be treated. It is safe because it can sterilize surely.In particular, if this sterilization treatment part is provided in the preceding stage of the filter medium treatment part, the filter medium and magnetism can be acted after removing various bacteria, so the effect is enhanced and a better quality water can be obtained. To be

[0041]

BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is an explanatory diagram showing an outline of a liquid reforming system 1. As shown in this figure, liquids that have been subjected to a modification treatment after magnetically activating various liquids to be treated are modified. Is discharged or returned to the liquid to be treated to reform the liquid to be treated, and is also returned to the reforming processing sections S1 and Sn for performing the above-mentioned reforming treatment to further activate the liquid to be treated (improved). Quality) and the reforming processing units S1, SnM1, Mn, Mn +
Purify 1. In the figure, M1, Mn and Mn + 1 are magnetic processors for magnetic processing.

The above-mentioned reforming treatment sections S1 and Sn can be provided in a plurality of stages depending on the state of the liquid to be treated and the intended reforming state. At this time, the magnetic processors M1, Mn,
The strength of Mn + 1 is set higher on the rear side.

The recirculation is carried out by injecting the liquid to be treated which has passed through the reforming processing portions S1 and Sn, and causes a violent collision of the liquid to enhance the reforming effect. In other words, in the magnetically treated liquid, clusters, which are a group of molecules, are subdivided to have good fluidity, impurities are reduced, and the dissolving ability is increased to be in an activated state. As a result, further fragmentation occurs and ultrafine particles can be realized. As a result, the liquid can be reformed to a lively state as it should be, and a state in which it can act on itself as well as on others is created.

(Embodiment 1) FIG. 2 shows a river, a pond, a lake,
It is a block diagram of a liquid reforming system for purifying water such as groundwater and aquaculture pond. In the liquid reforming system 1, not only can the contaminated water be cleaned, but also the self-cleaning ability can be provided.

As shown in FIG. 2, the liquid reforming system 1
Is a first reforming treatment device 3 installed in a storage part 2 in which water to be purified is stored, and a second reforming treatment device 3 which can be installed in an appropriate place on the ground, for example, in the back of a garden, a warehouse, a storeroom, a factory, etc. And a processing device 4.

FIG. 3 shows the configuration of the first reforming treatment apparatus 3, and FIG.
FIG. 3 is an explanatory diagram systematically showing the configuration of the second reforming treatment device 4.

That is, in the first reforming treatment apparatus 3, the water pumped up by the pump 5 is passed through the first filter layer 6 and the first filter medium layer 7 corresponding to the filter medium in the present invention in this order, and The magnetic processing by the magnetic processing device 8 is performed.
The first reforming treatment device 3 may be formed in an appropriate shape to enter the storage portion 2, but in the illustrated example, it is formed in a rectangular parallelepiped box shape,
Water is pumped from four side surfaces, and the first filter layer 6 and the first filter medium layer 7 are provided along each side surface. The pump 5 is provided at the center so as to be surrounded by the first filter layer 6 and the first filter medium layer 7.

The first filter layer 6 is for separating dusts and agglomerated suspended matters from water, and is composed of a well-known filter such as a fibrous filter or a fine mesh stainless mesh filter.

The first filter material layer 7 is mainly for improving the property of water, and is made of far-infrared radiation ceramics.
It is formed by filling natural stones such as zeolite, barley stone, sodalite that release active ingredients and remove harmful elements. The filter medium may be composed of only the far-infrared emitting ceramics or only natural stone, but using both of them is effective in restoring the original state of water.

The far-infrared radiation ceramics and the natural stone are formed into a spherical shape having a diameter of about 1 cm. During the passage of water through the spherical shape, activation by heat absorption and activation of many pores on the surface of the natural stone are caused. Adsorption, separation, ion exchange, flocculation of suspended solids in water due to eluted components, sterilization, antibacterial, deodorizing, etc. are modified.

The first magnetic processor 8 has a well-known structure, is formed by using a permanent magnet, and is intended to subdivide and activate water clusters by passing water in a magnetic field.

A first directional switching valve 9 is provided at the subsequent stage of the first magnetic processing unit 8 so that the water passing through the first magnetic processing unit 8 is returned to the inside position of the first filter medium layer 7 in a reflux path. 10 and a delivery path 11 for sending to the second reformer 4. An injection member 12 that ejects water violently is provided at the tip of the return path 10 so that the first filter layer 6 and the first filter material layer 7 can be back-washed with the returned water. The jetting member 12 may be configured so that water can freely flow between the first filter medium layer 7 and the pump 5 and has a large number of small holes on the first filter medium layer 7 side.

In the second reforming treatment apparatus 4, as shown in FIG. 4, the water transferred by the pump 13 is the first filter layer 14,
Second filter layer 15, first filter medium layer 16, second filter medium layer 1
7 and the third filter layer 18 are sequentially passed to be magnetically processed by the second magnetic processor 19. Then, the magnetically treated water flows back to the filter layers 14, 15 and 18 and the filter material layers 16 and 17, and the first directional switching valve 20 and the second directional switching valve 21 are provided so as to backwash each part. Is provided.

The second reforming apparatus 4 is constructed by housing it entirely in a box-shaped casing 23 having a moving means 22 such as casters on the lower surface.

The housing 23 is roughly divided into three parts in the length direction, and the supply port 24 for connecting the delivery passage 11 from the first reforming treatment device 3 to the upper part of the first partition at the end. Is provided
At the position above the first section where the water supplied from the supply port 24 is received, for example, the first filter layer 1 composed of a stainless mesh basket or a fibrous filter or the like.
4 is provided. Then, below the first filter layer 14, the second filter layer 15 made of stainless steel mesh having a finer mesh than the first filter layer 14 is provided.

Below the second filter layer 15, the first filter medium layer 16 is formed. Similar to the first filter medium layer 7 in the first modification treatment device 3 described above, the first filter medium layer 16 is mainly for improving the property of water, and has a spherical shape of far-infrared radiation ceramics. It is configured by filling an appropriate natural stone as a filter medium. The filling is performed in a space of a certain size to the extent that the filter medium can float.

Next to the first filter medium layer 16, that is, in the lower part of the second compartment, the second filter medium layer 1 is connected through the communication port 25.
Form 7. This second filter medium layer 17 also includes the first filter medium layer 1
Similar to 6, a large number of granular far-infrared radiating ceramics and natural stones are filled as a filter medium, and the mixing ratio and the kind of contents may be the same as those of the first filter medium layer 16, but may be appropriately changed. Good.

The second filter material layer 17 is located on the second
A fresh water tank 26 is provided in the third section adjacent to the section. From the second filter material layer 17, water flows into the fresh water tank 26 from the communication port 27 formed on the upper side surface thereof through the third filter layer 18. The third filter layer 18 is also composed of, for example, a stainless mesh filter.

The fresh water tank 26 is provided with the pump 113 for pumping up the accumulated water and the second magnetic processor 19 for magnetically treating the water pumped up by the pump 13. The second magnetic processor 19 applies a stronger magnetic field than the first magnetic processor 8 of the first reforming treatment device 3.

The first directional switching valve 20 is provided in front of the second magnetic processor 19, and the return path 28 is returned to the storage section 2.
And a connection path 29 connected to the second directional control valve 21 is formed. From the second direction switching valve 21, two types of return passages 3
0, 31 are formed. One first return path 30 returns to each of the filter layers 14, 15 and 18 to return to each of the filter layers 14, 15.
15 and 18 are used for backwashing, while the second reflux passage 31 is refluxed to the filter medium layers 16 and 17 so that each filter medium layer 1
This is for performing back washing of Nos. 6 and 17.

The return passage 28 extending from the first directional control valve 20 extends toward the storage portion 2 to form a plurality of discharge passages 32. Each discharge channel 32 is provided with a third magnetic processor 33 and a flow rate adjusting valve 34, and an injection member 35 such as a well-known nozzle is attached to the tip.

As the third magnetic processor 33, one having a stronger magnetic field than that of the second magnetic processor 19 located in the preceding stage is used. In addition, the position of each of the ejection members 35 in the reservoir 2 is determined by the ejection of water from the ejection member 35.
The installation height and the positional relationship on the plane are appropriately set so that the water inside is well stirred.

In the above-mentioned back washing, water is drawn in the opposite direction to the normal direction.
It is performed by violently ejecting, and each part is provided with an ejecting member for ejecting.

The jet member 36 for backwashing the filter layers 14, 15, 18 may be formed as shown in FIG. 5, for example. That is, a frame 36a having the same size as or substantially the same size as the cleaning surface of the filter layers 14, 15 and 18 is provided,
A plurality of bridging portions 36b are formed inside the frame 36a. Both the frame 36a and the bridging portion 36b are hollow, and the frame 36
A large number of small holes 36c are formed on the upper surfaces of a and the bridging portion 36b. Further, a connecting portion 36d for connecting the tip of the first return path 30 is formed in a part of the frame body 36a. Connection part 3
The water that has entered the inside from 6d spouts out of the large number of small holes 36c, so that the filter layers 14, 15 and 18 are cleaned up to their fine meshes. Other suitable injection members may be used.

The jet member 37 for backwashing the filter medium layers 16 and 17 is composed of a frame 37a and a bridging portion 37b similarly to the jet member 36, and as shown in FIG.
A plurality of columnar portions 37e are provided on the upper surfaces of the plurality of bridging portions 37b.
Can be installed by standing. A large number of small holes 3 are formed on the upper surfaces of the frame body 37a and the bridging portion 37b and the peripheral surface of each columnar portion 37e.
7c is provided so that water spouts vigorously from these small holes 37c. Then, many floating filter media 16
a, 17a move violently due to the water flow, and the filter medium 16
While a collision occurs between a and 17a, and between the filter media 16a and 17a and water, the water also violently collides with each other.

A second device provided with such an injection member 37
A backwash tank 38 for backwashing is provided above the filter material layer 17. The backwash tank 38 is connected to the end of the branch channel 31a provided in the second reflux channel 31, and collects water flowing from the branch channel 31a to apply pressure to jet it downward. As shown in FIG. As described above, the first section has a function of pushing back the dust and suspended matter released from the filter media 16a and 17a by the back washing from the injection member 37.

An overflow port 39 is provided in the first section.
The water that has been pushed up is discharged together with dust and the like. The discharged water may be discharged as it is or may be supplied to the storage unit 2. Since the overflowed water and dust are activated, the water in the storage section 2 is not polluted,
On the contrary, help activation.

The overflow port 40 is connected to the fresh water tank 26.
Although it is also provided in the above, the water discharged from the overflow port 40 may be discharged as it is or may be flowed to the storage section 2 or the like.

In the liquid reforming system 1 thus constructed, water is reformed as follows. That is, the dirty water in the storage unit 2 enters the first reforming treatment device 3,
The first modification is made. Water that passes through the first filter layer 6 and the first filter medium layer 7 in order is first separated by the first filter layer 6 from dust and the like. Subsequently, the first filter medium layer 7 receives far-infrared radiation and causes water molecules to undergo a resonance reaction, so that the separation of water molecules is promoted and the activity is increased. In addition, elution of natural stone components causes various effects depending on the content of the filter medium, such as coagulation of impurities, release of minerals, and deodorization.

The water thus improved in water quality is then subjected to a magnetic treatment by the first magnetic treatment device 8. Due to the action of this magnetism, water clusters are subdivided into fine particles.
Further, when subdivided, impurities dissolved in the cluster are discharged, and the state becomes more pure and activated.

The water that has been subjected to the first-stage reforming is transferred to the second reforming treatment device 4 and also the injection member provided in the first reforming treatment device 3 through the reflux passage 10. Reflux to 12.

This reflux (backwashing) is appropriately performed, for example, every predetermined time or automatically when the first filter layer 6 is clogged. Both the first filter layer 6 and the first filter medium layer 7 are cleanly cleaned by the back washing, and the activated filter water violently collides with the filter medium in the first filter medium layer, so that the water is well affected by the filter medium.

The water transferred to the second reforming treatment device 4 passes through the first filter layer 14 and the second filter layer 15 in this order, is highly filtered, and then is collected in the first filter medium layer 16. In the first filter medium layer 16, water comes into contact with the filter medium,
By the action of the filter medium 16a, as described above, the separation of water molecules is promoted to increase the activity, the components of natural stone are eluted, the impurities are aggregated, the minerals are replenished, and the deodorization is performed. Various modifications are made. Similarly, the second filter medium layer 17 adjacent to the first filter medium layer 16 is also subjected to the modification treatment to be further purified and activated.

The water thus modified moves through the third filter layer 18 to the fresh water tank 26, and is pumped out by the pump 13. Second when pumped up
It is acted upon by the magnetic processor 19. The purified and activated water is further activated by a further magnetic treatment with a stronger magnetic field than is done in the first magnetic treatment device above. That is, the subdivision of the clusters further progresses and become ultrafine particles.

The water activated by the ultrafine particles is returned to the reservoir 2 through the reflux passage 28, and at the same time, each filter layer 14, 15, 18 and each filter medium layer 16, 1 for back washing.
Reflux to 7.

The water returned to the storage section 2 is further activated by the third magnetic processing unit 33 and jetted to the storage section 2. The jet stirs the water in the storage part 2 and, if soil is present in the storage part 2, stirs it until then. The vibrant jet of fresh water collides violently with the water and soil in the storage part 2 to promote the subdivision of its own clusters, activate the water in the storage part 2 and act on others. That is, various beneficial actions such as removal and decomposition of organic matter and heavy metals in soil, suppression of generation of scales and water-blooms, prevention of decay, and the like are performed.

As for the water which is backwashed through the two reflux passages 30 and 31, the purified and activated water is swiftly flowed in the opposite direction as in the case of the above-mentioned first reforming treatment apparatus. The filter layers 14 and 1518 and the filter material layers 16 and 17 are washed. When the filter media layers 16 and 17 are backwashed, a backwash tank 38 is provided, and water is flushed from the backwash tank 38. For this reason, the water is violently sprayed from both the upper and lower sides, so that the activation of the water is promoted and the filter medium can be effectively washed. In addition, since the dirt produced by the reverse cleaning can be discharged from the overflow port 39, it can be discharged to the outside of the apparatus and reformed again. In FIG. 2, reference numeral 41 is a replenishment water injection passage for supplying water discharged from the overflow port 39 at that time, and when a magnetic treatment device 42 is installed here, the water can be activated and the subsequent reforming treatment can be performed. It's good because it's easier to do. The same applies when the reservoir 2 is a pond or the like and there is water entering it.

As described above, the water in the reservoir 2 circulates through the first reforming treatment device 3 and the second reforming treatment device 4,
It is cleaned and returned. Further, not only is the water returned, but the returned water also acts to clean the water and sludge in the storage section 2. Moreover, the filter layer 1 for removing dirt
4, 15, 18 and the filter medium layers 16, 17 are also cleaned by refluxing the purified water.

Therefore, unlike the purifying action of simply removing dirt, the reforming work can be performed very efficiently, the vitality can be given to the reformed water, and the dirt never returns immediately. Absent. You can maintain a beautiful condition for a long time. Further, maintenance of each reforming treatment device can be eliminated. Moreover, since no chemicals are used, it is possible to preserve the natural environment.

It should be noted that, depending on the degree of contamination of the water in the storage section 2, as shown by the phantom line in FIG.
An appropriate auxiliary device 43 may be connected between the second reforming treatment device 4 and the second reforming treatment device 4. The auxiliary device 43 may have, for example, the same or similar configuration as the above-mentioned reforming treatment devices 3 and 4, and may be a device having a bactericidal action or a device for performing precipitation treatment, which is necessary. An appropriate device may be connected.

Further, the reforming treatment apparatus may be appropriately changed in form depending on the place of use. For example, when the storage part is deep and wide, the first processing device may be configured as shown in FIG. That is, the floating member 51 is attached so as to float on the water surface.

As in the case of the second reforming treatment device 4 described above, the housing 2
By using the liquid reforming apparatus 1a configured by putting it in No. 3, it is possible to achieve the effect that it can be easily installed at any place and the construction is simple. In particular, if the moving means 22 is provided in the housing 23, the effect can be further enhanced.

Although the range of use is very wide, for example, as shown in FIG. 9, if the liquid reforming apparatus 1a is installed in a water supply facility of a building or a house, the water becomes better as described above, and it is delicious when drinking. It feels mellow and improves the water in the water receiving layer 44, prevents red rust on the water pipe and boiler 45,
Various effects can be obtained, such as preventing the odor of the toilet 46 and the dirty water tank 47, and prolonging the life of the water heater.

FIG. 10 is an explanatory view showing an example in which a circulation cooler is connected. In the cooling tower 48, a pump 49 and a discharge passage 50 having a magnetic processor are provided, and these are connected to the second modified example of the above example. Similar to the quality treatment device 4, it may be connected to the water supply / drainage port of the reforming treatment device 1a surrounded by the casing.

In the cooling tower, usually, chemicals are added to the circulating cooling water in order to prevent protection from stopping due to the high pressure of the refrigerator, to wash the cooling water pipe, and to take measures against Legionella bacteria. However, this has the drawback of being costly.

However, as described above, the liquid reforming apparatus 1a
Incorporation of the above prevents the deterioration of water quality, suppresses or eliminates the growth of bacteria, removes scale and rust, and protects equipment and piping to prolong the life of the equipment. Stabilize, improve refrigeration capacity, shorten operating time to reduce costs, eliminate the need for maintenance, etc.
Various effects can be obtained.

In addition to this, it can be variously used for purification of human waste and industrial wastewater and production of highly functional drinking water.

(Embodiment 2) FIG. 11 is a perspective view of a high-performance water producing apparatus 101 which provides high-performance water that is delicious to drink and good for health. Also in the high-performance water producing apparatus 101, a better treatment is performed by performing a reforming treatment including a filter medium treatment and a magnetic treatment and injecting the reformed water.

FIG. 12 is a block diagram of the high-performance water producing apparatus 101. That is, the supplied purified water is passed through the first reforming treatment unit 103 having the first magnetic treatment unit 102, and this water is further passed through the second reforming treatment unit 105 having the second magnetic treatment unit 104. Then, this water is circulated to the first reforming processing unit 102 and the second reforming processing unit 105 to be activated by injection.

In the high-performance water producing device 101,
An overflow tank 106 is provided for each processing unit 102.
The water that overflows from the water supply tank and the water that has spilled on the support base 108 when supplied from the water supply cock 107 are collected so that they can be effectively used. In addition, the housing 10
A moving means 110 is attached to the lower surface of 9 for convenience of movement.

FIG. 13 shows the internal structure of the high-performance water producing apparatus 101. The high-performance water production device 101 is roughly divided into five compartments, and the first compartment, the second compartment, the third compartment, and the fourth compartment are arranged in parallel in the left-right direction, and a fifth compartment is formed under this compartment. ing.

First, the first section is the first reforming processing section.
That is, the supplied clean water is magnetically processed by the first magnetic processor 102, and the water is filtered and sterilized. The sterilization treatment may be performed by an appropriate method, but here, ozone is used.

The sterilization processing device 111 for performing ozone sterilization is
It may be configured as shown in FIG. The double structure allows for instant treatment in small areas and maximizes the effect of ozone. A cubic inner wall body 112 made of stainless steel mesh is provided, and this inner wall body 112 is formed of a plate-like outer wall body 113 also having a cubic shape and having a large number of small holes 113a on four side surfaces except the upper surface and the lower surface. Providing a double structure. Then, a discharge pipe 115 connected to an introduction pipe 114 that is erected to introduce water that has passed through the first magnetic processor 102 is provided in the inner wall body 112.

The discharge pipe 115 is T-shaped with both ends bent downward, and is formed in such a manner that water entering from below is divided into left and right and flows downward respectively. Two ozone emission pipes 116 for emitting ozone are provided on both lower side portions of the discharge pipe 115 in the inner wall body 112.

Ozone is generated by sending air to the ozone generator 119 through the air filter 118 by driving the pump 117, and sending it to the ozone discharge pipe 116. As shown in FIG. 15, the water discharged from the discharge pipe 115 is immediately subjected to sterilization treatment with ozone in a small space inside the inner wall body 112. Then, the water filtered by the inner wall body 112 is ejected from the small holes 113a of the outer wall body 113 and is collected in the storage tank 120 forming the first section.

Sterilization processing device 111 in the storage tank 120
A bypass tank 121 is provided in the vicinity of, and is connected to a third filter layer, which will be described later, via a bypass pipe.

Further, in the storage tank 120, a discharge port 122 for discharging the refluxed water, an overflow port 123 for discharging the water, a return water outlet 1 for returning the overflowed water.
24 is formed, and a communication port 1 is formed on the side surface of the upper second partition side.
25 are formed.

The second section, the third section, and the fourth section are the second reforming processing unit 105 and have substantially the same structure as the second reforming processing apparatus 4 in the first embodiment.

First, the communication port 125 above the second section.
Then, the first filter layer 126 is provided. The first filter layer 126 is composed of an appropriate filter such as a stainless mesh. The injection member 1 for backwashing the first filter layer 126 when the filtrate passes through the first filter layer 126.
27 are provided. The ejection member 127 may have the same configuration as the ejection member 36 in the first embodiment described above.

A finer second filter layer 128 is provided after the first filter layer 126, and a third filter layer 129 is provided below the second filter layer 128 so as to filter the water flowing down.

The third filter layer 129 is a rectangular parallelepiped cage made of stainless steel mesh, and the injection member 12 is also provided here.
7, 130 are provided to perform back washing. The ejection member 130 is provided on the lower surface and the side surface. The space below the third filter layer 129 is the first filter medium layer 131.

The first filter medium layer 131 is formed by filling a large number of spherical filter mediums, as in the first embodiment. The same thing is used for the injection member 132.

At the bottom of the first filter medium layer 131, the communication port 13
3 to the second filter medium layer 134 in the adjacent third section. The second filter medium layer 134 may be configured similarly to that of the first embodiment and may include the same ejection member 132.
Backwash tank 135 mounted on the second filter medium layer 134
The same as in the first embodiment.

A communication port 136 is formed on the side surface of the second filter medium layer 134 on the side of the fourth compartment so that water flows into the fresh water tank 138 of the fourth compartment via the fourth filter layer 137. There is. The fourth filter layer 137 may also be made of stainless mesh or the like, and the back-cleaning injection member 127 is also provided here.

A pump 139 is provided below the fresh water tank 138.
Is installed to pump up the accumulated water. The pumped water is supplied from the water supply cock 107 after being further magnetically processed through the second magnetic processor 104, and
Recirculation to the storage tank 120 by the three directional control valves 140, 141, 142, and the filter layers 126, 1 described above.
29, 136 and the filter medium layers 131, 134 are back-washed. The magnetic field of the second magnetic processor 104 is stronger than that of the first magnetic processor 102.

The top of the fresh water tank 138 and the first
At the upper part of the filter medium layer 131, overflow ports 143, 1
44 is provided.

FIG. 16 is an explanatory view showing the flow when reforming water. That is, it is sterilized in the storage tank 120,
The water that has passed through to the fresh water tank 138 in order is pump 13
9 is pumped up and flows through the first direction switching valve 140, the second direction switching valve 141, and the discharge passage 145 connected to the discharge port 122 provided in the storage tank 120. The discharge channel 145 is provided with a third magnetic processor 146 to perform further activation processing. The magnetic field of the third magnetic processor 146 is stronger than that of the second magnetic processor 104. An appropriate injection member is provided at the discharge port 122 so that the water in the storage tank 120 flows with stirring.

The back washing of the filter layers 126, 129, 136 and the filter material layers 131, 134 is performed as shown in FIG.

First filter layer 126, third filter layer 1
29, the back washing of the fourth filter layer 136 is performed by stopping the reflux of water by switching the first directional control valve 140. The backwashing of the third filter layer 1129 is performed by the third directional control valve 142 by switching the first directional control valve 140 from the above state, flowing it toward the second directional control valve 141. If the third directional control valve 142 is switched in this state in the reverse direction, the first filter medium layer 13
The first and second filter medium layers 134 can be backwashed, and the backwash tank 13
It is also possible to remove stains caused by 5. The action of the backwash tank 135 is the same as that of the first embodiment, and the second filter medium layer 13
Water is extruded from No. 4 to the first filter medium layer 131,
The water is drained from the overflow port 144 provided at the upper part of 1.

An overflow tank 1 is provided in the fifth section.
06, and each of the overflow ports 123, 143,
Water flowing into 144 and water spilled on the support 108 are collected.

The overflow tank 106 is divided into three sections, and a sterilization processing chamber 147 communicating with each other, a deodorization processing chamber 148 for eliminating the odor of ozone used for the sterilization processing, and a water for returning to the storage tank 120 are stored. The storage chamber 145 is formed.

An ozone discharge pipe 150 is provided in the sterilization chamber 147, and ozone is drawn from the ozone generator 119 to the ozone discharge pipe 150. All the water flowing into the overflow tank 106 enters the sterilization processing chamber 147.

The deodorizing chamber 148 may be filled with antibacterial balls, charcoal, bamboo charcoal, etc.

The storage chamber 149 is provided with a pump 151 and a float switch 152.

Further, the overflow port 153 is provided in each part.
Is provided to discharge overflowing water to the outside of the device.

[0116] The high-performance water producing apparatus 10 configured as described above.
In No. 1, high-performance water can be obtained by driving the pump 139 and performing the reforming treatment as shown in FIGS. 16 and 17. The backwashing is performed every time using a timer, or the flow and switch 15 provided in the overflow tank 106 are used.
2 may be used as appropriate.

The water, which has been made into fine particles by magnetism and far infrared rays and activated by normal circulation and back washing, is again jetted to the storage tank 120 and the filter material layers 131 and 134, and is further activated. That is, the clusters are further subdivided, and ultrafine particles are formed into water having higher functionality. The detailed operation has been described above, and will be omitted.

The high-performance water produced in this way is water having the high functionality inherent in water, and in addition to the action of natural stone, it also contains a large amount of minerals. So to speak, it becomes ultra-high molecular mineral magnetic ionized water and becomes mellow and extremely delicious. Not only does it taste good, but it also has the ability to activate the human body and other life.

The jetting member in the above description corresponds to the jetting means of the present invention, each filter layer and each filter medium layer correspond to the filter medium treating section, and each magnetic processor corresponds to the magnetic treating section. Is not limited to the above configuration.

[0120]

As described above, according to the present invention, the liquid to be treated, which has been subjected to the subdivision and activation of the clusters by magnetism, is refluxed to the reformed filter medium, Since the liquids to be treated or the liquids to be treated and the filter medium are violently collided by jetting, the liquid to be treated activated by magnetism is
It is further activated and modifies the liquid to be treated, the filter material, and the dust filtered on the filter material. That is, although the liquid to be processed activated by magnetism has small clusters, the liquid to be processed is further divided into smaller pieces by violent collision.
During this further subdivision, the liquid to be treated again discharges the impurities dissolved in the clusters, becomes a further pure state, and becomes ultrafine particles. Therefore, it has a high function as it should be, such as increased solubility and fluidity.

The function further enhanced by the modification by magnetism and, if necessary, the action of far infrared rays is further enhanced by the collision. As a result, a liquid having ultrafine particle clusters is obtained, and the liquid itself becomes in a highly functional state.

This highly functional liquid activates the liquid to be treated at the reflux destination. In addition, the filter medium is washed to remove stains to bring the filter medium into a clean state, and the stain is decomposed with high functionality. Furthermore, if the filter medium is one that releases active ingredients or removes harmful ingredients such as far infrared rays and minerals, it promotes its action and becomes a highly functional liquid by being positively affected by itself. Become.

Therefore, the liquid to be treated is efficiently modified, and maintenance such as washing and replacement of the filter medium is almost unnecessary.

Further, since the liquid to be treated is modified as described above, it is possible to purify sewage as well as industrial wastewater by devising the method of treating the filter medium, the structure of the filter medium treating section, the combination of the filter medium treatment and the magnetic treatment. It can be applied to the modification of various liquids as necessary, from the purification of human excrement to a level that can be discharged, to the production of delicious water for drinking.

Further, in the filter medium treatment, for example, a filter for mainly filtering a solid phase by forming it into a mesh shape and a filter medium for mainly modifying liquid components by being formed into a porous and granular form are appropriately used. Since it is possible to configure the liquid reforming device with a magnetic treatment that is well known in the art and a jetting means such as a well-known nozzle, it is possible to configure the liquid reforming device, so that a special device or a structure that is too complicated is required. The device for liquid reforming can be manufactured relatively inexpensively.

[Brief description of drawings]

FIG. 1 is an explanatory diagram showing an outline of a liquid reforming system.

FIG. 2 is a configuration diagram of a liquid reforming system.

FIG. 3 is an explanatory diagram of a first reforming treatment device.

FIG. 4 is an explanatory diagram of a second reforming treatment device.

FIG. 5 is a perspective view of an ejection member.

FIG. 6 is an explanatory view showing an ejection member and its operating state.

FIG. 7 is an explanatory view showing a cleaning state of the filter medium layer.

FIG. 8 is a structural diagram showing another example of the first reforming treatment device.

FIG. 9 is an explanatory diagram showing an example of use of the liquid reforming apparatus.

FIG. 10 is an explanatory diagram showing an example of use of the liquid reforming apparatus.

FIG. 11 is a perspective view of a high-performance water producing device.

FIG. 12 is an explanatory view showing the structure of a high-performance water producing device.

FIG. 13 is a sectional view showing the structure of a high-performance water producing device.

FIG. 14 is a partially cutaway perspective view of the sterilization apparatus.

FIG. 15 is an explanatory diagram showing an operating state in the storage tank.

FIG. 16 is an explanatory diagram showing the flow of a reforming process.

FIG. 17 is an explanatory diagram showing the flow of a reforming process.

[Explanation of symbols]

1 ... Liquid reforming system 1a ... Liquid reforming treatment device 3 ... First reforming treatment device 4 ... Second reforming treatment device 6 ... First filter layer 7 ... First filter medium layer 8 ... First magnetic processor 10 ... Return path 12 ... Injection member 14 ... First filter layer 15 ... Second filter layer 16 ... First filter medium layer 17 ... Second filter medium layer 18 ... Third filter layer 19 ... Second magnetic processor 28 ... Return path 30 ... First return path 31 ... Second return path 33 ... Third magnetic processor 35, 36, 37 ... Injection member 42 ... Magnetic processor 43 ... Auxiliary device 101 ... High-performance water production device 102 ... First magnetic processor 103 ... 1st modification processing part 104 ... Second magnetic processor 105 ... 2nd modification processing part 126 ... First filter layer 127, 130, 132 ... Injection member 128 ... Second filter layer 129 ... Third filter layer 131 ... First filter medium layer 134 ... Second filter medium layer 137 ... Fourth filter layer 146 ... Third magnetic processor

─────────────────────────────────────────────────── ───

[Procedure amendment]

[Submission date] February 4, 2002 (2002.2.4)

[Procedure Amendment 1]

[Document name to be amended] Statement

[Correction target item name] Full text

[Correction method] Change

[Correction content]

[Document name] Statement

Title: Liquid reforming method and apparatus, and high-performance water producing apparatus using the same

[Claims]

Detailed Description of the Invention

[0001]

TECHNICAL FIELD The present invention relates to water in ponds and lakes,
Various liquids such as domestic wastewater, industrial wastewater, rainwater, groundwater, night soil, seawater, and tap water can be discharged to a required level, for example, a level that can be discharged, a level that can be used for cultivating plants and raising and aquaculture of seafood, further to drink up the health better advanced level of the human body, performing clarified Ri activated or modified, to a technique for the desired liquid.

[0002]

2. Description of the Related Art As a technique for purifying sewage, there is, for example, an apparatus disclosed in Japanese Patent Laid-Open No. 9-327695. This purification device has a magnetic treatment device that magnetically treats raw water and a filter medium that allows microorganisms useful for water purification to live and filter, and the raw water activated by the magnetic treatment device is passed through the filter medium. It is a structure to return it to raw water after it is released.

In this apparatus, however, a filter is provided in front of the magnetic treatment device to remove visible dust from the raw water, but since the magnetic treatment is performed by itself, the effect of activating the water by the magnetic treatment is sufficient. Can not enjoy. Therefore, it is very dirty like lakes and marshes, and it is difficult to purify a large amount of raw water.

[0004] Further, the dust and the like captured by filtering reverses the water and returns it to the raw water, but it simply reverses it.
Although it depends on the degree of dirt, it is difficult to perform sufficient cleaning, and frequent backflow and replacement of the filter media are required.

Further, since the filter material is made of plastic, it does not positively improve the water quality, and relies solely on magnetism. Therefore, the dust and the like returned to the raw water are only affected by the water in an insufficiently activated state by the magnetic treatment, and the purification efficiency is poor.

[0006]

SUMMARY OF THE INVENTION Therefore, according to the present invention, the effect of magnetic treatment can be sufficiently exerted to efficiently purify a large amount of water such as lakes and marshes that are severely contaminated. Instead of that, the main issue is to modify various liquids, for example, to produce water that is useful for the natural world and the human body.

[0007]

[Means for Solving the Problems] A means for that purpose is to carry out a reforming treatment consisting of a filtering treatment for passing a liquid to be treated through a filter medium and a magnetic treatment for passing a magnetic field, and to subject the treated liquid after the reforming treatment to the above-mentioned filter medium. with refluxing, the above reflux, performed the injection of the liquid to be treated which has passed through the reforming process, characterized in that the liquid to be treated and between the liquid to be treated Toro material is a liquid reforming method for collision.

The filter medium treatment and the magnetic treatment in the above-mentioned modification treatment are
The treatment method, the sequence, and the stage are appropriately set according to the state of the liquid to be treated and the intended modification. That is, for example, when purifying water in a pond, a lake, or the like, it is preferable to perform the filter medium treatment and then the magnetic treatment. When reforming tap water, magnetic treatment can be directly performed.

For the above magnetic treatment, a permanent magnet is used to subdivide and activate clusters (groups of molecules) by passing water in a magnetic field. For example, it is disclosed in Registered Utility Model No. 3033968. It is preferable to use a well-known structure having such a structure. Further, for the filter material treatment, in addition to an appropriate filter such as a fiber filter for performing solid-phase filtration, a wire mesh filter, or a ceramic filter, it is preferable to use a porous granular filter material for releasing the active ingredient. In particular, when a far-infrared radiator is used as the filter medium, the energy level of the liquid to be treated can be increased, so that the activation effect by the magnetic treatment can be improved. The arrangement of the filter media is appropriately combined depending on the properties of the filter media. If you want to increase the mineral content,
For example, natural stone capable of eluting minerals may be used as the filter medium.

By subjecting the liquid to be treated to filter medium treatment,
If impurities such as dust are removed and a material that releases active ingredients such as natural minerals is used for the filter medium, the energy level is raised and activated, minerals are replenished, and the action depending on the filter medium is performed. . Further, when the liquid to be treated is subjected to magnetic treatment, the clusters of the liquid to be treated are subdivided into fine particles and activated, and the impurities dissolved in the clusters are discharged to enhance the cluster precision. Be affected. Since the filter material treatment and the magnetic treatment are carried out in the reforming treatment, the synergistic effect which cannot be obtained by only one of them is effective and the high-level reforming can be performed.

The liquid to be treated which has been reformed through the reforming treatment is
If necessary, it can be discharged for use, or returned to the portion where the liquid to be treated is collected to purify and activate the portion, and can also be returned to the filter medium for filter medium treatment to The liquid to be treated in the vicinity is purified and activated. That is, if the liquid is jetted at the time of reflux, the liquids to be treated collide with each other or the liquid to be treated and the filter medium violently collide with each other. As a result, a high degree of precision is obtained, and a higher level active state is entered.

[0012] It should be noted that, when it is refluxed to the filter medium, it is preferable to backwash the filter medium. That is, the back-cleaning is to remove dust and the like from the filter medium by flowing in a direction opposite to the direction in which the liquid to be treated flows during the reforming treatment, and this back-cleaning is performed by jetting as described above. When the treatment liquids or the treated liquid and the filter medium are violently collided with each other, the filter medium is cleaned cleanly, and is subjected to the action of the filter medium more than when the treated liquid simply flows in contact with the filter medium. In particular, a liquid in which clusters are subdivided and activated exhibits high fluidity and can dissolve many substances, so it is a natural stone that causes violent collisions, cleans the filter media, and causes the filter media to act on the liquid. In the case of the above, it is well dissolved to obtain the active ingredient positively. As a result, the clusters of the liquid to be treated are further atomized (activated) as compared with the case where a normal liquid simply collides.
The desired modification can be performed.

As described above, the liquid to be treated is highly activated, and can be activated to a state close to, for example, a supercritical liquid, and efficient reforming can be performed.

The fact that the cluster becomes smaller means that there is no extra substance in the cluster, and that the ultrafine particles make the purity higher, and if the water is water, the original function of water is restored. Such ultra-polymer magnetic water produces various effects due to its inherent high functionality. For example, activating the liquid in the injected part, suppressing scale and rust in water pipes, decomposing filtered impurities, suppressing the generation of scales, etc. Various effects can be obtained, such as shortening the boiling time by improving the thermal conductivity and removing organic substances and heavy metals. Drinking water, in particular, makes mellow and delicious water, makes tea and food delicious, and gives it to plants and animals to grow well.

If the above-mentioned reforming treatment is carried out in a plurality of stages, and the reforming treatment on the subsequent stage side is subjected to magnetic treatment with a stronger magnetic field, the stronger magnetic field acts according to the flow of treatment, so that the cluster of the liquid to be treated is higher. It is possible to reliably raise the energy state to a desired active state.

A large number of granular far-infrared radiators may be used as the filter medium. This is because, as described above, a synergistic effect is produced by combining the activation action by magnetism with the activation action by far infrared rays, and the liquid to be treated can be activated more efficiently. In particular, when the liquid to be treated that has undergone the reforming treatment is refluxed to be floatable, the liquid to be treated can collide with the filter medium and the liquid to be treated more vigorously and vigorously, so that the effect can be enhanced.

In addition to the far-infrared radiator, as a filter medium containing a natural mineral that releases an active ingredient and removes a harmful ingredient, for example, zeolite, barley stone, sodalite, soil of soft porous ancient humus, limestone By using (calcium), metamorphic granite (various kinds of minerals), iron sulfate (magnetic), etc., it is possible to obtain mineral water that is good for use as drinking water. As a matter of course, it is preferable to form a large number of particles as described above and fill them so that they can freely move around by the reflux of the liquid to be treated.

Another means is to provide a reforming processing section having a filter medium processing section for passing the liquid to be processed through a filter medium and a magnetic processing section for passing a magnetic field, and the processed liquid to be processed is provided at a stage subsequent to the reforming processing section. Is a liquid reforming apparatus which is provided with a recirculation path for recirculating the liquid to the filter medium processing section, and at the tip of the recirculation path is provided an injection means for injecting the liquid to be treated against the filter medium to strongly collide with it. And

That is, as in the above description, the filter medium treating section and the magnetic treating section in the reforming treating section are constructed according to the state of the liquid to be treated and the intended reforming, the treatment section structure, the order and the steps. Are appropriately set and performed. For example, when purifying water from a pond, a lake or the like, it is preferable to dispose the filter medium processing unit before the magnetic processing unit. When reforming tap water, it is also possible to directly perform magnetic treatment.

The magnetic processing section is formed by using a permanent magnet and subdivides and activates a cluster (group of molecules) by passing water through a magnetic field. For example, it is disclosed in Registered Utility Model No. 3033968. It is preferable to use a device having a well-known structure as described above. In addition, the filter material processing unit is a fiber filter or a wire mesh filter that performs solid-phase filtration,
In addition to a suitable filter such as a ceramic filter, it is preferable to use a porous granular filter medium that releases the active ingredient. Especially when a far infrared radiator is used as the filter medium,
Since the energy level of the liquid to be treated can be increased, the effect of activation by the magnetic treatment can be improved. The arrangement of the filter media is appropriately combined depending on the properties of the filter media. When it is desired to increase the mineral content, for example, natural stone capable of eluting minerals may be used as the filter medium. A mineral concentrate may be injected.

When the liquid to be treated passes through the filter medium treatment section, impurities such as dust are removed, and if a material releasing an active ingredient such as a natural mineral is used for the filter medium, the energy level is raised and activated. , Is replenished with minerals and is affected by the filter material. Also,
By passing the liquid to be processed through the magnetic processing section, the clusters of the liquid to be processed are subdivided into fine particles and activated,
Impurities dissolved in the clusters are discharged to improve the cluster precision and are affected by magnetism. Since the reforming treatment section has the filtering medium treating section and the magnetic treating section, the synergistic effect which cannot be obtained by only one of them enables efficient and high-level reforming.

The liquid to be treated which has been reformed through the reforming treatment section is discharged for use, if necessary, or returned to a portion where the liquid to be treated is accumulated to purify and activate the portion. In addition to liquefying, it is refluxed to the filter medium processing section through the reflux path and jetted by the jetting means. Then, the filter medium and the liquid to be treated in the vicinity thereof are purified and activated. That is, since the liquid is ejected when refluxed, the liquids to be treated, or the liquids to be treated and the filter medium violently collide with each other, and the clusters of the liquids to be finely divided are further subdivided into ultrafine particles. Higher precision will be obtained and a higher level of activation will be achieved.

It should be noted that when it is returned to the filter medium processing section, it is preferable to back-clean the filter medium. That is, the back-cleaning is to remove dust and the like from the filter medium by flowing in a direction opposite to the direction in which the liquid to be treated flows during the reforming treatment, and this back-cleaning is performed by jetting as described above. When the treatment liquids or the treated liquid and the filter medium are violently collided with each other, the filter medium is cleaned cleanly, and is subjected to the action of the filter medium more than when the treated liquid simply flows in contact with the filter medium. In particular, a liquid in which clusters are subdivided and activated exhibits high fluidity and can dissolve many substances, so it is a natural stone that causes violent collisions, cleans the filter media, and causes the filter media to act on the liquid. In the case of the above, it is well dissolved to obtain the active ingredient positively. As a result, the clusters of the liquid to be treated are further made into fine particles (activated) as compared with the case where a normal liquid simply collides, and desired modification can be performed.

As described above, the liquid to be treated is highly activated, and can be activated to a state close to, for example, a supercritical liquid, and efficient reforming can be executed.

The fact that the cluster becomes small means that there is no extra substance in the cluster, and that by making the particles ultrafine, the purity is increased, and in the case of water, the original function of water is restored. Such ultra-polymer magnetic water produces various effects due to its inherent high functionality. For example, activating the liquid in the injected part, suppressing scale and rust in water pipes, decomposing filtered impurities, suppressing the generation of scales, etc. Various effects can be obtained, such as shortening the boiling time by improving the thermal conductivity and removing organic substances and heavy metals. Drinking water, in particular, makes mellow and delicious water, makes tea and food delicious, and gives it to plants and animals to grow well.

The filter medium processing section may be formed by filling a number of granular far-infrared radiators. As mentioned above,
This is because a synergistic effect is produced by combining the activation action by magnetism with the activation action by far infrared rays, and the liquid to be treated can be activated more efficiently. In particular, when the liquid to be treated that has undergone the reforming treatment is refluxed to be floatable, the liquid to be treated can collide with the filter medium and the liquid to be treated more vigorously and vigorously, so that the effect can be enhanced.

In addition to far-infrared radiators, as filter media containing natural minerals that release active ingredients and remove harmful ingredients, for example, zeolite, barley stone, sodalite, soil of soft porous ancient humus, limestone By using (calcium), metamorphic granite (various kinds of minerals), iron sulfate (magnetic), etc., it is possible to obtain mineral water that is good for use as drinking water. As a matter of course, it is preferable to form a large number of particles as described above and fill them so that they can freely move around by the reflux of the liquid to be treated.

This liquid reforming apparatus can be easily used by itself by placing it in a housing as a unit and providing an appropriate moving means such as casters on the lower surface of the housing. It becomes easy to use in combination with the apparatus as appropriate, and it can be easily used for reforming treatment of various liquids in various situations, and the availability of the liquid reforming apparatus can be expanded.

Still another means is to dispose a magnetic treatment device for passing a liquid to be treated in a magnetic field at a front stage and / or a rear stage of the liquid reforming device, and the magnetic treatment device and the magnetic treatment of the liquid reforming device. The magnetic field in the section is set stronger toward the rear side, and an auxiliary device that processes the liquid to be treated according to the target reforming state is connected to the front stage and / or the rear stage of the liquid reforming device. It is a liquid reforming system.

That is, by appropriately connecting the magnetic treatment device and the auxiliary device to the liquid treatment device having the reforming treatment portion having the filter medium treatment portion and the magnetic treatment portion, the reflux passage, and the injection means, various treatments can be performed. It can be used for various purposes in various situations. For example, if an apparatus having a filter medium treating section and a magnetic treating section is used as an auxiliary apparatus, a sterilizing apparatus is used, or a precipitation treating apparatus is used as an auxiliary apparatus, the apparatus can be used depending on the apparatus. A desired effect can be applied to the liquid to be treated. In addition, since the magnetic treatment device is connected so that the magnetic field becomes stronger toward the later stage, the liquid to be treated can be gradually changed to a higher active state, and the action of the auxiliary device can be efficiently performed.

Still another means is to provide a modification treatment section having a filter medium treatment section for passing the liquid to be treated through the filter medium and a magnetic treatment section for making a magnetic field act on the liquid to be treated which has passed through the filter medium treatment section. In the subsequent stage of the reforming treatment section, a discharge path for supplying the treatment target fluid that has passed through the reforming treatment section, a storage section for temporarily storing the treatment target solution before the treatment by the reforming treatment section, and the filter medium treatment section a reflux passage for refluxing the provided at least at the tip of the return passage for returning the filter medium processing unit, producing high-function water in which a jet means for collision with sprayed liquid to be treated against the filter media out of the reflux passage It is a device.

That is, the liquid to be treated which has passed through the filter medium processing section and the magnetic processing section in this order and has exited the reforming processing section passes through the reflux channel except before being supplied through the discharge channel, before being processed by the reforming processing section. The liquid to be processed is refluxed to the storage part for temporarily storing it and the filter medium processing part.

Since the liquid to be treated passes through the magnetic treatment portion after passing through the filter medium treatment portion, the action of the magnetic treatment portion can be efficiently received. In other words, magnetically subdivides the cluster,
The impurities are removed and activated. Moreover, when the activated liquid to be treated is recirculated, a jetting means is provided at the tip of the recirculation path that recirculates to the filter medium processing unit, so that the liquid to be treated is strongly squirted against the filter medium. Due to this spraying, the liquids to be treated collide strongly with each other. By this collision, the water activated in the magnetic treatment unit is further atomized (activated) and the filter medium can be washed. Further, if the filter medium releases the active ingredient by strongly hitting the filter medium, the desired action of the filter medium can be efficiently received.

At this time, it is advisable to strongly flush the filter medium in a direction opposite to the normal direction so that the filter medium is backwashed. The filter medium can be actively washed. Further, by providing a jetting means on the side opposite to the backwashing and jetting the liquid to be treated from two opposite directions, not only the filter medium and the liquid to be treated but also violent collision between the liquids to be treated is positive. Therefore, the liquid to be treated can be more effectively activated.

It is preferable that the filter material treating section is composed of a granular material containing a natural mineral that releases an active ingredient as a filter material so as to be floatable. The filter medium containing a natural mineral that releases the active ingredient includes, for example, far-infrared emitting ceramics that emits far-infrared rays, iron sulfate that emits magnetism, and
There are a variety of other natural stones and soils, such as zeolite, barite, sodalite, limestone, metamorphic granite, and soft porous ancient humus. It may be appropriately selected according to the purpose and action. Such a filter medium is formed in a granular shape such as a sphere, and is filled so as to be freely floatable by the above reflux.

If a far-infrared radiator is used among the above examples, the liquid to be treated can be made to have a high energy level by far-infrared radiation, so that the treatment effect of the magnetic treatment section can be improved.

The liquid to be treated is filtered and reformed while passing through these filter materials alone or appropriately blended. Then, when it is refluxed, it collides violently with the liquid to be treated and the filter medium, and the filter medium is washed.

A magnetic processing unit for magnetically treating the liquid to be treated is provided in at least the return passage of the return passage that returns to the storage unit, and the magnetic field of the magnetic treatment unit is set to be greater than the magnetic field of the preceding magnetic treatment unit. Should be set to be strong. The liquid to be processed which returns to the storage part is activated to a higher level by the magnetic processing part and flows back in this state, so that the liquid to be processed in the storage part is highly modified.

Even when the liquid is recirculated to the storage portion, if it is jetted and recirculated, the liquid to be treated in the storage portion can also obtain a good reforming action due to the violent collision of molecules with each other.

In order to use the highly functional water obtained by reforming as drinking water, it is preferable to provide a sterilization treatment section constituted by using, for example, ozone or ultraviolet rays in order to sterilize the liquid to be treated. It is safe because it can sterilize surely.In particular, if this sterilization treatment part is provided in the preceding stage of the filter medium treatment part, the filter medium and magnetism can be acted after removing various bacteria, so the effect is enhanced and a better quality water can be obtained. To be

[0041]

BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is an explanatory diagram showing an outline of a liquid reforming system 1. As shown in this figure, liquids that have been subjected to a modification treatment after magnetically activating various liquids to be treated are modified. Is discharged or returned to the liquid to be treated to reform the liquid to be treated, and is also returned to the reforming processing sections S1 and Sn for performing the above-mentioned reforming treatment to further activate the liquid to be treated (improved). Quality) and purification of the reforming processing parts S1 and Sn .
In the figure, M1, Mn and Mn + 1 are magnetic processors for magnetic processing.

The above-mentioned reforming treatment sections S1 and Sn can be provided in a plurality of stages depending on the state of the liquid to be treated and the intended reforming state. At this time, the magnetic processors M1, Mn,
The strength of Mn + 1 is set higher on the rear side.

The recirculation is carried out by injecting the liquid to be treated which has passed through the reforming processing portions S1 and Sn, and causes a violent collision of the liquid to enhance the reforming effect. In other words, in the magnetically treated liquid, clusters, which are a group of molecules, are subdivided to have good fluidity, impurities are reduced, and the dissolving ability is increased to be in an activated state. As a result, further fragmentation occurs and ultrafine particles can be realized. As a result, the liquid can be reformed to a lively state as it should be, and a state in which it can act on itself as well as on others is created.

(Embodiment 1) FIG. 2 shows a river, a pond, a lake,
It is a block diagram of a liquid reforming system for purifying water such as groundwater and aquaculture pond. In the liquid reforming system 1, not only can the contaminated water be cleaned, but also the self-cleaning ability can be provided.

As shown in FIG. 2, the liquid reforming system 1
Is a first reforming treatment device 3 installed in a storage part 2 in which water to be purified is stored, and a second reforming treatment device 3 which can be installed in an appropriate place on the ground, for example, in the back of a garden, a warehouse, a storeroom, a factory, etc. And a processing device 4.

FIG. 3 shows the configuration of the first reforming treatment apparatus 3, and FIG.
FIG. 3 is an explanatory diagram systematically showing the configuration of the second reforming treatment device 4.

That is, in the first reforming treatment apparatus 3, the water pumped up by the pump 5 is passed through the first filter layer 6 and the first filter medium layer 7 corresponding to the filter medium in the present invention in this order, and The magnetic processing by the magnetic processing device 8 is performed.
The first reforming treatment device 3 may be formed in an appropriate shape to enter the storage portion 2, but in the illustrated example, it is formed in a rectangular parallelepiped box shape,
Water is pumped from four side surfaces, and the first filter layer 6 and the first filter medium layer 7 are provided along each side surface. The pump 5 is provided at the center so as to be surrounded by the first filter layer 6 and the first filter medium layer 7.

The first filter layer 6 is for separating dusts and agglomerated suspended matters from water, and is composed of a well-known filter such as a fibrous filter or a fine mesh stainless mesh filter.

The first filter material layer 7 is mainly for improving the property of water, and is made of far-infrared radiation ceramics.
It is formed by filling natural stones such as zeolite, barley stone, sodalite that release active ingredients and remove harmful elements. The filter medium may be composed of only the far-infrared emitting ceramics or only natural stone, but using both of them is effective in restoring the original state of water.

The far-infrared radiation ceramics and the natural stone are formed into a spherical shape having a diameter of about 1 cm. During the passage of water through the spherical shape, activation by heat absorption and activation of many pores on the surface of the natural stone are caused. Adsorption, separation, ion exchange, flocculation of suspended solids in water due to eluted components, sterilization, antibacterial, deodorizing, etc. are modified.

The first magnetic processor 8 has a well-known structure, is formed by using a permanent magnet, and is intended to subdivide and activate water clusters by passing water in a magnetic field.

A first directional switching valve 9 is provided at the subsequent stage of the first magnetic processing unit 8 so that the water passing through the first magnetic processing unit 8 is returned to the inside position of the first filter medium layer 7 in a reflux path. 10 and a delivery path 11 for sending to the second reformer 4. An injection member 12 that ejects water violently is provided at the tip of the return path 10 so that the first filter layer 6 and the first filter material layer 7 can be back-washed with the returned water. The jetting member 12 may be configured so that water can freely flow between the first filter medium layer 7 and the pump 5 and has a large number of small holes on the first filter medium layer 7 side.

In the second reforming treatment apparatus 4, as shown in FIG. 4, the water transferred by the pump 13 is the first filter layer 14,
Second filter layer 15, first filter medium layer 16, second filter medium layer 1
7 and the third filter layer 18 are sequentially passed to be magnetically processed by the second magnetic processor 19. Then, the magnetically treated water flows back to the filter layers 14, 15 and 18 and the filter material layers 16 and 17, and the first directional switching valve 20 and the second directional switching valve 21 are provided so as to backwash each part. Is provided.

The second reforming apparatus 4 is constructed by housing it entirely in a box-shaped casing 23 having a moving means 22 such as casters on the lower surface.

The housing 23 is roughly divided into three parts in the length direction, and the supply port 24 for connecting the delivery passage 11 from the first reforming treatment device 3 to the upper part of the first partition at the end. Is provided
At the position above the first section where the water supplied from the supply port 24 is received, for example, the first filter layer 1 composed of a stainless mesh basket or a fibrous filter or the like.
4 is provided. Then, below the first filter layer 14, the second filter layer 15 made of stainless steel mesh having a finer mesh than the first filter layer 14 is provided.

Below the second filter layer 15, the first filter medium layer 16 is formed. Similar to the first filter medium layer 7 in the first modification treatment device 3 described above, the first filter medium layer 16 is mainly for improving the property of water, and has a spherical shape of far-infrared radiation ceramics. It is configured by filling an appropriate natural stone as a filter medium. The filling is performed in a space of a certain size to the extent that the filter medium can float.

Next to the first filter medium layer 16, that is, in the lower part of the second compartment, the second filter medium layer 1 is connected through the communication port 25.
Form 7. This second filter medium layer 17 also includes the first filter medium layer 1
Similar to 6, a large number of granular far-infrared radiating ceramics and natural stones are filled as a filter medium, and the mixing ratio and the kind of contents may be the same as those of the first filter medium layer 16, but may be appropriately changed. Good.

The second filter material layer 17 is located on the second
A fresh water tank 26 is provided in the third section adjacent to the section. From the second filter material layer 17, water flows into the fresh water tank 26 from the communication port 27 formed on the upper side surface thereof through the third filter layer 18. The third filter layer 18 is also composed of, for example, a stainless mesh filter.

[0059] Shimizu tank 26 is provided with a said pump 1 3 for pumping water collected includes the second magnetic treatment device 19 for magnetically treating the water pumped by the pump 13. The second magnetic processor 19 applies a stronger magnetic field than the first magnetic processor 8 of the first reforming treatment device 3.

The first directional switching valve 20 is provided in front of the second magnetic processor 19, and the return path 28 is returned to the storage section 2.
And a connection path 29 connected to the second directional control valve 21 is formed. From the second direction switching valve 21, two types of return passages 3
0, 31 are formed. One first return path 30 returns to each of the filter layers 14, 15 and 18 to return to each of the filter layers 14, 15.
15 and 18 are used for backwashing, while the second reflux passage 31 is refluxed to the filter medium layers 16 and 17 so that each filter medium layer 1
This is for performing back washing of Nos. 6 and 17.

The return passage 28 extending from the first directional control valve 20 extends toward the storage portion 2 to form a plurality of discharge passages 32. Each discharge channel 32 is provided with a third magnetic processor 33 and a flow rate adjusting valve 34, and an injection member 35 such as a well-known nozzle is attached to the tip.

As the third magnetic processor 33, one having a stronger magnetic field than that of the second magnetic processor 19 located in the preceding stage is used. In addition, the position of each of the ejection members 35 in the reservoir 2 is determined by the ejection of water from the ejection member 35.
The installation height and the positional relationship on the plane are appropriately set so that the water inside is well stirred.

In the above-mentioned back washing, water is drawn in the opposite direction to the normal direction.
It is performed by violently ejecting, and each part is provided with an ejecting member for ejecting.

The jet member 36 for backwashing the filter layers 14, 15, 18 may be formed as shown in FIG. 5, for example. That is, a frame 36a having the same size as or substantially the same size as the cleaning surface of the filter layers 14, 15 and 18 is provided,
A plurality of bridging portions 36b are formed inside the frame 36a. Both the frame 36a and the bridging portion 36b are hollow, and the frame 36
A large number of small holes 36c are formed on the upper surfaces of a and the bridging portion 36b. Further, a connecting portion 36d for connecting the tip of the first return path 30 is formed in a part of the frame body 36a. Connection part 3
The water that has entered the inside from 6d spouts out of the large number of small holes 36c, so that the filter layers 14, 15 and 18 are cleaned up to their fine meshes. Other suitable injection members may be used.

The jet member 37 for backwashing the filter medium layers 16 and 17 is composed of a frame 37a and a bridging portion 37b similarly to the jet member 36, and as shown in FIG.
A plurality of columnar portions 37e are provided on the upper surfaces of the plurality of bridging portions 37b.
Can be installed by standing. A large number of small holes 3 are formed on the upper surfaces of the frame body 37a and the bridging portion 37b and the peripheral surface of each columnar portion 37e.
7c is provided so that water spouts vigorously from these small holes 37c. Then, many floating filter media 16
a, 17a move violently due to the water flow, and the filter medium 16
a, 17a to each other, also the filter medium 16a, along with the collision between 17a and the water takes place, water with each other even each other violently as collision.

A second device provided with such an injection member 37
A backwash tank 38 for backwashing is provided above the filter material layer 17. The backwash tank 38 is connected to the end of the branch channel 31a provided in the second reflux channel 31, and collects water flowing from the branch channel 31a to apply pressure to jet it downward. As shown in FIG. As described above, it functions to push back the dust and floating substances released from the filter media 16a and 17a by the back washing from the injection member 37 to the first partition side .

An overflow port 39 is provided in the first section.
The water that has been pushed up is discharged together with dust and the like. The discharged water may be discharged as it is or may be supplied to the storage unit 2. Since the overflowed water and dust are activated, the water in the storage section 2 is not polluted,
On the contrary, help activation.

The overflow port 40 is connected to the fresh water tank 26.
Although it is also provided in the above, the water discharged from the overflow port 40 may be discharged as it is or may be flowed to the storage section 2 or the like.

In the liquid reforming system 1 thus constructed, water is reformed as follows. That is, the dirty water in the storage unit 2 enters the first reforming treatment device 3,
The first modification is made. Water that passes through the first filter layer 6 and the first filter medium layer 7 in order is first separated by the first filter layer 6 from dust and the like. Subsequently, the first filter medium layer 7 receives far-infrared radiation and causes water molecules to undergo a resonance reaction, so that the separation of water molecules is promoted and the activity is increased. In addition, elution of natural stone components causes various effects depending on the content of the filter medium, such as coagulation of impurities, release of minerals, and deodorization.

The water thus improved in water quality is then subjected to a magnetic treatment by the first magnetic treatment device 8. Due to the action of this magnetism, water clusters are subdivided into fine particles.
Further, when subdivided, impurities dissolved in the cluster are discharged, and the state becomes more pure and activated.

The water that has been subjected to the first-stage reforming is transferred to the second reforming treatment device 4 and also the injection member provided in the first reforming treatment device 3 through the reflux passage 10. Reflux to 12.

This reflux (backwashing) is appropriately performed, for example, every predetermined time or automatically when the first filter layer 6 is clogged. Both the first filter layer 6 and the first filter medium layer 7 are cleanly cleaned by the back washing, and the activated filter water violently collides with the filter medium in the first filter medium layer, so that the water is well affected by the filter medium.

The water transferred to the second reforming treatment device 4 passes through the first filter layer 14 and the second filter layer 15 in this order, is highly filtered, and then is collected in the first filter medium layer 16. In the first filter medium layer 16, water comes into contact with the filter medium,
By the action of the filter medium 16a, as described above, the separation of water molecules is promoted to increase the activity, the components of natural stone are eluted, the impurities are aggregated, the minerals are replenished, and the deodorization is performed. Various modifications are made. Similarly, the second filter medium layer 17 adjacent to the first filter medium layer 16 is also subjected to the modification treatment to be further purified and activated.

The water thus modified moves through the third filter layer 18 to the fresh water tank 26, and is pumped out by the pump 13. Second when pumped up
It is acted upon by the magnetic processor 19. The purified and activated water is further activated by a further magnetic treatment with a stronger magnetic field than is done in the first magnetic treatment device above. That is, the subdivision of the clusters further progresses and become ultrafine particles.

The water activated by the ultrafine particles is returned to the reservoir 2 through the reflux passage 28, and at the same time, each filter layer 14, 15, 18 and each filter medium layer 16, 1 for back washing.
Reflux to 7.

The water returned to the storage section 2 is further activated by the third magnetic processing unit 33 and jetted to the storage section 2. The jet stirs the water in the storage part 2 and, if soil is present in the storage part 2, stirs it until then. The vibrant jet of fresh water collides violently with the water and soil in the storage part 2 to promote the subdivision of its own clusters, activate the water in the storage part 2 and act on others. That is, various beneficial actions such as removal and decomposition of organic matter and heavy metals in soil, suppression of generation of scales and water-blooms, prevention of decay, and the like are performed.

As for the water which is backwashed through the two reflux passages 30 and 31, the purified and activated water is swiftly flowed in the opposite direction as in the case of the above-mentioned first reforming treatment apparatus. The filter layers 14, 15, 18 and the filter material layers 16, 17 are washed. When the filter media layers 16 and 17 are backwashed, a backwash tank 38 is provided, and water is flushed from the backwash tank 38. For this reason, the water is violently sprayed from both the upper and lower sides, so that the activation of the water is promoted and the filter medium can be effectively washed. In addition, since the dirt produced by the reverse cleaning can be discharged from the overflow port 39, it can be discharged to the outside of the apparatus and reformed again. In FIG. 2, reference numeral 41 is a replenishment water injection passage for supplying water discharged from the overflow port 39 at that time, and when a magnetic treatment device 42 is installed here, the water can be activated and the subsequent reforming treatment can be performed. It's good because it's easier to do. The same applies when the reservoir 2 is a pond or the like and there is water entering it.

As described above, the water in the reservoir 2 circulates through the first reforming treatment device 3 and the second reforming treatment device 4,
It is cleaned and returned. Further, not only is the water returned, but the returned water also acts to clean the water and sludge in the storage section 2. Moreover, the filter layer 1 for removing dirt
4, 15, 18 and the filter medium layers 16, 17 are also cleaned by refluxing the purified water.

Therefore, unlike the purifying action of simply removing dirt, the reforming work can be performed very efficiently, the vitality can be given to the reformed water, and the dirt never returns immediately. Absent. You can maintain a beautiful condition for a long time. Further, maintenance of each reforming treatment device can be eliminated. Moreover, since no chemicals are used, it is possible to preserve the natural environment.

It should be noted that, depending on the degree of contamination of the water in the storage section 2, as shown by the phantom line in FIG.
An appropriate auxiliary device 43 may be connected between the second reforming treatment device 4 and the second reforming treatment device 4. The auxiliary device 43 may have, for example, the same or similar configuration as the above-mentioned reforming treatment devices 3 and 4, and may be a device having a bactericidal action or a device for performing precipitation treatment, which is necessary. An appropriate device may be connected.

Further, the reforming treatment apparatus may be appropriately changed in form depending on the place of use. For example, when the storage part is deep and wide, the first processing device may be configured as shown in FIG. That is, the floating member 51 is attached so as to float on the water surface.

As in the case of the second reforming treatment device 4 described above, the housing 2
By using the liquid reforming apparatus 1a configured by putting it in No. 3, it is possible to achieve the effect that it can be easily installed at any place and the construction is simple. In particular, if the moving means 22 is provided in the housing 23, the effect can be further enhanced.

Although the range of use is very wide, for example, as shown in FIG. 9, if the liquid reforming apparatus 1a is installed in a water supply facility of a building or a house, the water becomes better as described above, and it is delicious when drinking. It feels mellow and improves the water in the water receiving layer 44, prevents red rust on the water pipe and boiler 45,
Preventing malodor toilet 46 and sewage tank 47, such as extending the life of the boiler equipment, obtain a variety of effects.

FIG. 10 is an explanatory view showing an example in which a circulation cooler is connected. In the cooling tower 48, a pump 49 and a discharge passage 50 having a magnetic processor are provided, and these are connected to the second modified example of the above example. Similar to the quality treatment device 4, it may be connected to the water supply / drainage port of the reforming treatment device 1a surrounded by the casing.

In the cooling tower, usually, chemicals are added to the circulating cooling water in order to prevent protection from stopping due to the high pressure of the refrigerator, to wash the cooling water pipe, and to take measures against Legionella bacteria. However, this has the drawback of being costly.

However, as described above, the liquid reforming apparatus 1a
Incorporation of the above prevents the deterioration of water quality, suppresses or eliminates the growth of bacteria, removes scale and rust, and protects equipment and piping to prolong the life of the equipment. Stabilize, improve refrigeration capacity, shorten operating time to reduce costs, eliminate the need for maintenance, etc.
Various effects can be obtained.

In addition to this, it can be variously used for purification of human waste and industrial wastewater and production of highly functional drinking water.

(Embodiment 2) FIG. 11 is a perspective view of a high-performance water producing apparatus 101 which provides high-performance water that is delicious to drink and good for health. Also in the high-performance water producing apparatus 101, a better treatment is performed by performing a reforming treatment including a filter medium treatment and a magnetic treatment and injecting the reformed water.

FIG. 12 is a block diagram of the high-performance water producing apparatus 101. That is, the supplied clean water is passed through the first reforming treatment unit 103 having the first magnetic treatment unit 102, and this water is further passed through the second reforming treatment unit 105 having the second magnetic treatment unit 104. Then, this water is circulated to the first reforming processing unit 102 and the second reforming processing unit 105 to be activated by injection.

In the high-performance water producing device 101,
An overflow tank 106 is provided for each processing unit 102.
The water that overflows from the water supply tank and the water that has spilled on the support base 108 when supplied from the water supply cock 107 are collected so that they can be effectively used. In addition, the housing 10
A moving means 110 is attached to the lower surface of 9 for convenience of movement.

FIG. 13 shows the internal structure of the high-performance water producing apparatus 101. The high-performance water production device 101 is roughly divided into five compartments, and the first compartment, the second compartment, the third compartment, and the fourth compartment are arranged in parallel in the left-right direction, and a fifth compartment is formed under this compartment. ing.

First, the first section is the first reforming processing section.
That is, the supplied clean water is magnetically processed by the first magnetic processor 102, and the water is filtered and sterilized. The sterilization treatment may be performed by an appropriate method, but here, ozone is used.

The sterilization processing device 111 for performing ozone sterilization is
It may be configured as shown in FIG. The double structure allows for instant treatment in small areas and maximizes the effect of ozone. A cubic inner wall body 112 made of stainless steel mesh is provided, and this inner wall body 112 is formed of a plate-like outer wall body 113 also having a cubic shape and having a large number of small holes 113a on four side surfaces except the upper surface and the lower surface. Providing a double structure. Then, a discharge pipe 115 connected to an introduction pipe 114 that is erected to introduce water that has passed through the first magnetic processor 102 is provided in the inner wall body 112.

The discharge pipe 115 is T-shaped with both ends bent downward, and is formed in such a manner that water entering from below is divided into right and left and flows downward respectively. Two ozone emission pipes 116 for emitting ozone are provided on both lower side portions of the discharge pipe 115 in the inner wall body 112.

Ozone is generated by sending air to the ozone generator 119 through the air filter 118 by driving the pump 117, and sending it to the ozone discharge pipe 116. As shown in FIG. 15, the water discharged from the discharge pipe 115 is immediately subjected to sterilization treatment with ozone in a small space inside the inner wall body 112. Then, the water filtered by the inner wall body 112 is ejected from the small holes 113a of the outer wall body 113 and is collected in the storage tank 120 forming the first section.

Sterilization processing device 111 in the storage tank 120
A bypass tank 121 is provided in the vicinity of, and is connected to a third filter layer, which will be described later, via a bypass pipe.

Further, in the storage tank 120, a discharge port 122 for discharging the refluxed water, an overflow port 123 for discharging the water, a return water outlet 1 for returning the overflowed water.
24 is formed, and a communication port 1 is formed on the side surface of the upper second partition side.
25 are formed.

The second section, the third section, and the fourth section are the second reforming processing unit 105 and have substantially the same structure as the second reforming processing apparatus 4 in the first embodiment.

First, the communication port 125 above the second section.
Then, the first filter layer 126 is provided. The first filter layer 126 is composed of an appropriate filter such as a stainless mesh. The injection member 1 for backwashing the first filter layer 126 when the filtrate passes through the first filter layer 126.
27 are provided. The ejection member 127 may have the same configuration as the ejection member 36 in the first embodiment described above.

A finer second filter layer 128 is provided after the first filter layer 126, and a third filter layer 129 is provided below the second filter layer 128 so as to filter the water flowing down.

The third filter layer 129 is a rectangular parallelepiped cage made of stainless steel mesh, and the injection member 12 is also provided here.
7, 130 are provided to perform back washing. The ejection member 130 is provided on the lower surface and the side surface. The space below the third filter layer 129 is the first filter medium layer 131.

The first filter medium layer 131 is formed by filling a large number of spherical filter mediums, as in the first embodiment. The same thing is used for the injection member 132.

At the bottom of the first filter medium layer 131, the communication port 13
3 to the second filter medium layer 134 in the adjacent third section. The second filter medium layer 134 may be configured similarly to that of the first embodiment and may include the same ejection member 132.
Backwash tank 135 mounted on the second filter medium layer 134
The same as in the first embodiment.

A communication port 136 is formed on the side surface of the second filter medium layer 134 on the side of the fourth compartment so that water flows into the fresh water tank 138 of the fourth compartment via the fourth filter layer 137. There is. The fourth filter layer 137 may also be made of stainless mesh or the like, and the back-cleaning injection member 127 is also provided here.

A pump 139 is provided below the fresh water tank 138.
Is installed to pump up the accumulated water. The pumped water is supplied from the water supply cock 107 after being further magnetically processed through the second magnetic processor 104, and
Recirculation to the storage tank 120 by the three directional control valves 140, 141, 142, and the filter layers 126, 1 described above.
29, 136 and the filter medium layers 131, 134 are back-washed. The magnetic field of the second magnetic processor 104 is stronger than that of the first magnetic processor 102.

The top of the fresh water tank 138 and the first
At the upper part of the filter medium layer 131, overflow ports 143, 1
44 is provided.

FIG. 16 is an explanatory view showing the flow when reforming water. That is, it is sterilized in the storage tank 120,
The water that has passed through to the fresh water tank 138 in order is pump 13
9 is pumped up and flows through the first direction switching valve 140, the second direction switching valve 141, and the discharge passage 145 connected to the discharge port 122 provided in the storage tank 120. The discharge channel 145 is provided with a third magnetic processor 146 to perform further activation processing. The magnetic field of the third magnetic processor 146 is stronger than that of the second magnetic processor 104. An appropriate injection member is provided at the outlet 122 to allow the water in the storage tank 120 to flow while stirring.

The back washing of the filter layers 126, 129, 136 and the filter material layers 131, 134 is performed as shown in FIG.

First filter layer 126, third filter layer 1
29, the back washing of the fourth filter layer 136 is performed by stopping the reflux of water by switching the first directional control valve 140. The backwashing of the third filter layer 129 is performed by switching the first directional control valve 140 from the above state and flowing it toward the second directional control valve 141.
The third direction switching valve 142 is used. If the third directional control valve 142 is switched in this state in reverse, the first filter medium layer 131,
The second filter material layer 134 can be backwashed and the dirt can be removed by the backwash tank 135. The operation of the backwash tank 135 is the same as in the case of the first embodiment, water is extruded from the second filter medium layer 134 to the first filter medium layer 131, and is drained from the overflow port 144 provided in the upper portion of the first filter medium layer 131. .

An overflow tank 1 is provided in the fifth section.
06, and each of the overflow ports 123, 143,
Water flowing into 144 and water spilled on the support 108 are collected.

The overflow tank 106 is divided into three parts, and a sterilization processing chamber 147 communicating with each other, a deodorization processing chamber 148 for eliminating the odor of ozone used for the sterilization processing, and water for returning to the storage tank 120 are stored. The storage chamber 149 is formed.

An ozone discharge pipe 150 is provided in the sterilization chamber 147, and ozone is drawn from the ozone generator 119 to the ozone discharge pipe 150. All the water flowing into the overflow tank 106 enters the sterilization processing chamber 147.

The deodorizing chamber 148 may be filled with antibacterial balls, charcoal, bamboo charcoal, etc.

The storage chamber 149 is provided with a pump 151 and a float switch 152.

Further, the overflow port 153 is provided in each part.
Is provided to discharge overflowing water to the outside of the device.

[0116] The high-performance water producing apparatus 10 configured as described above.
In No. 1, high-performance water can be obtained by driving the pump 139 and performing the reforming treatment as shown in FIGS. 16 and 17. Backwashing is going to the each appropriate time using a timer, float switch 15 provided in the overflow tank 106
2 may be used as appropriate.

The water, which has been made into fine particles by magnetism and far infrared rays and activated by normal circulation and back washing, is again jetted to the storage tank 120 and the filter material layers 131 and 134, and is further activated. That is, the clusters are further subdivided, and ultrafine particles are formed into water having higher functionality. The detailed operation has been described above, and will be omitted.

The high-performance water produced in this way is water having the high functionality inherent in water, and in addition to the action of natural stone, it also contains a large amount of minerals. So to speak, it becomes ultra-high molecular mineral magnetic ionized water and becomes mellow and extremely delicious. Not only does it taste good, but it also has the ability to activate the human body and other life.

The jetting member in the above description corresponds to the jetting means of the present invention, each filter layer and each filter medium layer correspond to the filter medium treating section, and each magnetic processor corresponds to the magnetic treating section. Is not limited to the above configuration.

[0120]

According to the present invention as described above, according to the present invention, the liquid to be treated reformed to active activatable by subdividing the cluster magnetic is made and refluxed against a filter medium made the modification, since the Awa to collision between the filter medium liquid to be treated to each other and the liquid to be treated by injection, filtration with the liquid to be treated which has been activated by the magnetic is further activated, the liquid to be treated and the filter medium there, the filter medium It reforms the dust and the like. That is, although the liquid to be treated activated by magnetism has small clusters,
It is divided into smaller pieces by violent collision. During this further subdivision, the liquid to be treated again discharges the impurities dissolved in the clusters, becomes a further pure state, and becomes ultrafine particles. Therefore, it has a high function as it should be, such as increased solubility and fluidity.

The function further enhanced by the modification by magnetism and, if necessary, the action of far infrared rays is further enhanced by the collision. As a result, a liquid having ultrafine particle clusters is obtained, and the liquid itself becomes in a highly functional state.

This highly functional liquid activates the liquid to be treated at the reflux destination. In addition, the filter medium is washed to remove stains to bring the filter medium into a clean state, and the stain is decomposed with high functionality. Furthermore, if the filter medium is one that releases active ingredients or removes harmful ingredients such as far infrared rays and minerals, it promotes its action and becomes a highly functional liquid by being positively affected by itself. Become.

Therefore, the liquid to be treated is efficiently modified, and maintenance such as washing and replacement of the filter medium is almost unnecessary.

Further, since the liquid to be treated is modified as described above, it is possible to purify sewage as well as industrial wastewater by devising the method of treating the filter medium, the structure of the filter medium treating section, the combination of the filter medium treatment and the magnetic treatment. It can be applied to the modification of various liquids as necessary, from the purification of human excrement to a level that can be discharged, to the production of delicious water for drinking.

Further, in the filter medium treatment, for example, a filter for mainly filtering a solid phase by forming it into a mesh shape and a filter medium for mainly modifying liquid components by being formed into a porous and granular form are appropriately used. Since it is possible to configure the liquid reforming device with a magnetic treatment that is well known in the art and a jetting means such as a well-known nozzle, it is possible to configure the liquid reforming device, so that a special device or a structure that is too complicated is required. The device for liquid reforming can be manufactured relatively inexpensively.

[Brief description of drawings]

FIG. 1 is an explanatory diagram showing an outline of a liquid reforming system.

FIG. 2 is a configuration diagram of a liquid reforming system.

FIG. 3 is an explanatory diagram of a first reforming treatment device.

FIG. 4 is an explanatory diagram of a second reforming treatment device.

FIG. 5 is a perspective view of an ejection member.

FIG. 6 is an explanatory view showing an ejection member and its operating state.

FIG. 7 is an explanatory view showing a cleaning state of the filter medium layer.

FIG. 8 is a structural diagram showing another example of the first reforming treatment device.

FIG. 9 is an explanatory diagram showing an example of use of the liquid reforming apparatus.

FIG. 10 is an explanatory diagram showing an example of use of the liquid reforming apparatus.

FIG. 11 is a perspective view of a high-performance water producing device.

FIG. 12 is an explanatory view showing the structure of a high-performance water producing device.

FIG. 13 is a sectional view showing the structure of a high-performance water producing device.

FIG. 14 is a partially cutaway perspective view of the sterilization apparatus.

FIG. 15 is an explanatory diagram showing an operating state in the storage tank.

FIG. 16 is an explanatory diagram showing the flow of a reforming process.

FIG. 17 is an explanatory diagram showing the flow of a reforming process.

[Explanation of symbols] 1 ... Liquid reforming system 1a ... Liquid reforming treatment device 3 ... First reforming treatment device 4 ... Second reforming treatment device 6 ... First filter layer 7 ... First filter medium layer 8 ... First magnetic processor 10 ... Return path 12 ... Injection member 14 ... First filter layer 15 ... Second filter layer 16 ... First filter medium layer 17 ... Second filter medium layer 18 ... Third filter layer 19 ... Second magnetic processor 28 ... Return path 30 ... First return path 31 ... Second return path 33 ... Third magnetic processor 35, 36, 37 ... Injection member 42 ... Magnetic processor 43 ... Auxiliary device 101 ... High-performance water production device 102 ... First magnetic processor 103 ... 1st modification processing part 104 ... Second magnetic processor 105 ... 2nd modification processing part 126 ... First filter layer 127, 130, 132 ... Injection member 128 ... Second filter layer 129 ... Third filter layer 131 ... First filter medium layer 134 ... Second filter medium layer 137 ... Fourth filter layer 146 ... Third magnetic processor

[Procedure Amendment 2]

[Document name to be corrected] Drawing

[Name of item to be corrected] Figure 2

[Correction method] Change

[Correction content]

[Fig. 2]

[Procedure 3]

[Document name to be corrected] Drawing

[Name of item to be corrected] Fig. 13

[Correction method] Change

[Correction content]

[Fig. 13]

[Procedure amendment 4]

[Document name to be corrected] Drawing

[Correction target item name] Fig. 16

[Correction method] Change

[Correction content]

FIG. 16

[Procedure Amendment 5]

[Document name to be corrected] Drawing

[Name of item to be corrected] Fig. 17

[Correction method] Change

[Correction content]

FIG. 17

─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. ⁷ Identification code FI theme code (reference) C02F 1/50 531 C02F 1/50 531R 540 540B 550 550C 550H 560 560G 560Z 1/68 510 510/68 510B 510J 520 520K 520L 520N 520P 540 540F 540G 540Z ZAB ZAB 1/78 1/78 F term (reference) 4D037 AA05 AB03 BA17 BA18 CA02 CA05 CA13 4D050 CA05 FA06 FA12 CA15 FA06 CA12 DB12 CA15 CA07 CA11 CA12 CA06

Claims (9)

[Claims] 1. A reforming treatment comprising a filter medium treatment in which a liquid to be treated is passed through a filter medium and a magnetic treatment in which a magnetic field is passed, and the liquid to be treated which has undergone the reforming treatment is refluxed to the filter medium, and the reflux is performed. A liquid reforming method in which the liquids to be treated after the reforming treatment are jetted, and the liquids to be treated and the liquid to be treated and the filter medium are violently collided with each other. 2. The liquid reforming method according to claim 1, wherein the reforming treatment is performed in a plurality of stages, and the reforming treatment on the subsequent stage side is magnetically treated with a stronger magnetic field. 3. The liquid reforming method according to claim 1 or 2, wherein a large number of granular far-infrared radiators are used as the filter medium. 4. A reforming treatment section having a filtering medium treating section for passing a liquid to be treated through a filter medium and a magnetic treating unit for passing a magnetic field is provided, and the treated liquid to be treated is placed at a subsequent stage of the reforming treatment section. A liquid reforming apparatus having a reflux path for refluxing the treatment section, and an injection means for ejecting the liquid to be treated against the filter medium to strongly collide with the tip of the reflux path. 5. The liquid reforming apparatus according to claim 4, wherein the filter medium processing section is formed by filling a large number of granular far-infrared radiators. 6. A magnetic treatment device for passing a liquid to be treated through a magnetic field is disposed in a front stage and / or a rear stage of the liquid reforming device according to claim 4 or 5, and the magnetic treatment device and the liquid are provided. The magnetic field in the magnetic treatment unit of the reformer is set stronger toward the latter stage, and the liquid to be treated is treated in the former stage and / or the latter stage of the liquid reformer according to the target reforming state. Liquid reforming system to connect auxiliary equipment to. 7. A modification treatment section having a filter medium treatment section for allowing a liquid to be treated to pass through the filter medium and a magnetic treatment section for causing a magnetic field to act on the liquid to be treated having passed through the filter medium treatment section, and the modification treatment. In the latter part of the section, a discharge passage for supplying the liquid to be treated which has passed through the reforming treatment portion, a storage portion for temporarily accumulating the liquid to be treated before treatment by the reforming treatment portion, and a reflux passage for returning to the filter medium treatment portion. A high-performance water producing device, wherein a jetting means is provided, and a jetting means for jetting the liquid to be treated against the filter medium to strongly collide with the filter medium is provided at least at the tip of the reflux channel of the reflux channel that returns to the filter medium treating section. 8. The high-performance water producing device according to claim 7, wherein the filter medium treating section is configured by floatingly filling, as a filter medium, a granular material containing a natural mineral that releases an active ingredient. 9. The high-performance water producing apparatus according to claim 7, further comprising a sterilization treatment unit for sterilizing the liquid to be treated.