JP5584869B1 - Sterilization treatment apparatus and sterilization treatment method - Google Patents

Abstract

A sterilization apparatus and a sterilization process that can perform sterilization and antibacterial treatment of a liquid to be processed, can easily remove a minute object to be removed from the liquid to be processed, and can reduce costs compared to conventional methods. Provide a method.
SOLUTION: A flowing water pipe 2, a liquid speed adjusting means 4 for adjusting a flow rate of a liquid to be treated provided in the flowing water pipe, and an upstream side provided in the flowing water pipe are arranged in parallel from the downstream side. A swirling flow reversing unit 7 composed of two or more swirling flow generating fixed blades, a decompression unit 8 for depressurizing the liquid to be treated supplied from the swirling flow reversing unit, the liquid speed adjusting means and the swirling flow reversing unit. Or a gas supply unit 3 for supplying a gas provided in at least one place between the swirl flow reversing unit and the decompression unit, and a water collecting tank 9 for sterilizing the liquid to be treated supplied from the decompression unit In the water collection tank, the clay mineral 11 and the heavy metal 12 are disposed at a position where the liquid can be contacted with the liquid to be treated.
[Selection] Figure 1

Description

  The present invention relates to a sterilization treatment apparatus and a sterilization treatment method, and more specifically, sterilization and antibacterial bacteria contained in a liquid to be treated, and microscopic removal of microorganisms, organic substances, metals (cadmium, arsenic, etc.), etc. The present invention relates to a sterilization processing apparatus and a sterilization processing method that can aggregate a target object and easily perform flotation removal (removal target object is attached to bubbles to be removed).

  Treatment technology to remove the removal target in the liquid to be treated includes circulating water such as pools and bathtubs, desalination of seawater, purification of medical or industrial water, treatment of ballast water mounted on ships, livestock sewage Treatment, purification of well water and river water to obtain drinking water for livestock, treatment of cleaning water for fisheries and agriculture, drainage treatment of food factories, removal of harmful substances such as plankton in coastal fishing grounds, water for hydroponics It is performed in various fields such as processing.

  The said processing technique is performed by various apparatuses, such as an apparatus using various filters and an ultrafiltration membrane, or a sand filtration apparatus. In general, the type of membrane used in these apparatuses, the pore size thereof, or the particle size of sand is selected according to the size of the target object to be removed. In particular, with the advancement of membrane technology, attempts have been made to remove minute objects to be removed such as microorganisms, organic substances and metals with a filtration separation apparatus.

  For example, generally, zooplankton has a size of about 50 μm or more, phytoplankton has a size of 10 μm or more and less than 50 μm, and bacteria are smaller than phytoplankton and have a size of about 0.1 μm to several μm. Therefore, the pore diameter of the membrane is determined according to the plankton or bacteria to be removed. More specifically, an ultrafiltration membrane having a pore diameter of 2 nm or more and 200 nm or less, a microfiltration membrane having a pore diameter of 50 nm or more and less than 10 μm, and the like are usually used.

In addition to micro organisms such as plankton and microorganisms, an invention of an apparatus for removing metals such as iron in a liquid to be treated has been developed (Patent Document 1 below). The apparatus disclosed in Patent Document 1 uses a hollow fiber membrane having a pore diameter of 1 μm or less and 0.03 μm or more in order to remove iron and manganese in the liquid to be treated.
JP 2006-192418 A

  As shown in the above prior art, according to the size of the object to be removed, using a filtration membrane having a pore size equal to or smaller than the size enables physical separation of the membrane. However, the smaller the size of the object to be removed, the more clogging between the pores of the separation membrane and the sand particles, and the backwashing of the separation device and replacement of the separation membrane must be performed frequently. In addition, the running cost was a problem. In particular, a separation device for filtering and removing objects to be removed having a size of 10 μm or less, such as phytoplankton and bacteria, is generally high in cost and requires a lot of time for washing and the like, and the running cost is high.

  The present invention has been made in view of the above problems, and can perform sterilization and antibacterial treatment of a liquid to be treated, and can easily remove a minute object to be removed from the liquid to be treated. An object of the present invention is to provide a sterilization treatment apparatus and a sterilization treatment method capable of reducing the above.

The sterilization apparatus of the first invention is
A water pipe for supplying the liquid to be treated;
Liquid speed adjusting means for adjusting the flow rate of the liquid to be treated provided in the water flow pipe;
Two or more swirl flow generating fixed wing bodies arranged in parallel from the upstream side to the downstream side provided in the water flow pipe , wherein the adjacent swirl flow generation fixed wing bodies are arranged in a spiral direction opposite to each other in the horizontal direction. A swirl flow reversing unit comprising a fixed wing having an inclination ;
A decompression unit for decompressing the liquid to be treated supplied from the swirl flow reversing unit;
A gas supply unit for supplying a gas which is provided to each of at least one place between the pressure reducing portion, and between the swirling flow reversal portions of the swirling flow reversal portions and the liquid velocity adjusting means,
It consists of a water collection tank that sterilizes the liquid to be treated supplied from the decompression unit, and
The water collecting tank is characterized in that clay minerals and heavy metals are arranged at positions where they can come into contact with the liquid to be treated.

The sterilization apparatus of the second invention is
The invention according to claim 1 is characterized in that the water collecting tank is provided with at least one circulating means for circulating the liquid to be treated.

The sterilization apparatus of the third invention is
The invention according to claim 1 or 2 is characterized in that the liquid speed adjusting means is a cascade pump or a centrifugal pump.

The sterilization apparatus of the fourth invention is
The invention according to any one of claims 1 to 3 , wherein the heavy metal is a fiber-shaped metal containing at least copper.

The sterilization treatment method of the fifth invention is
Pass the liquid to be treated through the water pipe,
Next, the liquid to be processed is passed through a liquid speed adjusting means for adjusting the flow rate of the liquid to be processed provided in the flow pipe,
Next, two or more swirl flow generating fixed wing bodies paralleling the liquid to be treated from the upstream side to the downstream side provided in the water flow pipe , the adjacent swirl flow generating fixed wing bodies are mutually, Through a swirl flow reversing part comprising a fixed wing having an inclination in the opposite spiral direction ;
Next, the liquid to be treated supplied from the swirl flow reversing unit is passed through a decompression unit that decompresses the liquid to be treated.
The gas from the injector provided in each of at least one place between the pressure reducing portion, and between the swirling flow reversal portions of the swirling flow reversing section the liquid velocity adjusting means is supplied to the liquid to be treated,
Pass the liquid to be treated supplied from the decompression section through a water collection tank for sterilization,
and,
In the water collecting tank, the liquid to be treated is brought into contact with the clay mineral and the heavy metal.

The sterilization treatment method of the sixth invention comprises
The invention according to claim 5 is characterized in that in the water collecting tank, the supplied liquid to be treated is circulated by a circulation means provided at least at one place.

The sterilization treatment method of the seventh invention is
The invention according to claim 5 or 6 is characterized in that the liquid speed adjusting means is a cascade pump or a centrifugal pump.

The sterilization treatment method of the eighth invention is
The invention according to any one of claims 5 to 7 , wherein the heavy metal is a fiber-shaped metal containing at least copper.

  In the present invention and this specification, “upstream side” means a side closer to the supply side of the liquid flowing in the apparatus, and “downstream side” means a side farther from the supply side of the liquid flowing in the apparatus. means.

  Further, in the present invention and the present specification, “first swirl flow generating fixed wing body” and “second swirl flow generating fixed wing body” are two upstream swirl flow generating fixed wing bodies in the upstream side. The swirl flow generating fixed wing body located at the position is called the first swirl flow generating fixed wing body, and the second swirl flow generating fixed blade adjacent to the downstream side is the second swirl flow generating fixed blade. The body. Further, in the present invention having more than two fixed flow wings for generating swirl flow, a fixed flow wing for swirl flow installed in parallel to the second fixed flow wing for swirl flow is provided. , Third, fourth,... N-th swirl flow generating fixed wing body.

According to the first invention and the fifth invention,
When gas is supplied from the gas supply unit and passed through the swirl flow reversing unit to the liquid to be processed accelerated by the liquid speed adjusting means, two or more swirl flow generating fixed blades swirling in opposite directions are used. A torsional shear force can be applied to the treatment liquid, and a large amount of fine bubbles can be generated.
Next, by reducing the pressure of the liquid to be processed in the pressure reducing part, a gas dissolved in the liquid to be processed is generated, and bubbles generated in the swirl flow reversing part are further refined.
Next, in the water collection tank, the liquid to be treated is brought into contact with heavy metal to generate metal ions, thereby killing bacteria in the liquid to be treated and exhibiting an excellent sterilization / antibacterial action. In addition, by bringing the liquid to be treated into contact with the clay mineral and generating metal ions from the metal in the clay mineral, fine particles (algae, microorganisms, mold, metal, etc.) of about 10 to 1000 nm in the liquid to be treated are aggregated. Can be removed.

  By using an injector for the gas supply unit, the gas can be easily supplied to the liquid to be processed which is pressurized by the liquid speed adjusting means and is in an accelerated state.

According to the second and sixth inventions,
By providing one or more circulation means in the water collection tank, the liquid to be treated can be efficiently circulated in the water collection tank, and the chances of contact with clay minerals and heavy metals can be increased.

According to the third and seventh inventions,
By using a cascade pump or a centrifugal pump as the liquid speed adjusting means, in addition to accelerating the liquid to be treated, the bubbles in the liquid to be treated can be sheared by the impeller of the centrifugal pump to refine the bubbles. .

According to the fourth and eighth inventions,
As a heavy metal, at least copper-containing metal has a fiber shape, which increases the contact area between the liquid to be treated and the surface of copper, generates more copper ions, and has better sterilization and antibacterial action. Can be obtained.

It is a schematic sectional drawing which shows one Embodiment of the sterilization processing apparatus of this invention. 2a is a reference diagram showing how to attach the injector. 2b is an explanatory diagram showing the mechanism of the injector. It is a schematic sectional drawing which shows one Embodiment of a swirl flow reverse part. It is a fracture perspective view showing one embodiment of a fixed wing body for generating a swirl flow in parallel. 5a is a front view of a disk used for forming the swirl flow generating fixed wing body shown in FIG. 4, and 5b and 5c are front views of the swirl flow generating fixed wing body shown in FIG. It is a perspective view which shows the different embodiment of the fixed wing | blade for a swirl | vortex flow generation used for this invention. It is a schematic sectional drawing which shows the Example of the sterilization processing apparatus of this invention.

[About the sterilization apparatus of the present invention]
Hereinafter, the sterilization apparatus of the present invention will be described with reference to the drawings.
FIG. 1 is a sterilization treatment apparatus 1 showing an embodiment of the present invention, and is a schematic cross-sectional view cut in a direction in which a liquid to be treated flows in the apparatus.

In the sterilizing apparatus 1, a vortex pump 4 is installed as a liquid speed adjusting means in a flowing water pipe 2 in which a liquid to be processed flows in the direction of an arrow A.
Next, the gas supply unit 3 is installed in the flowing water pipe 2.
Next, a swirling flow generating fixed wing body 5 is installed in the flowing water pipe 2 from the upstream side, and a swirling flow generating fixed wing body 6 is installed in parallel to the downstream side. The region of the swirl flow generating fixed wings 5 and 6 becomes the swirl flow reversing unit 7.
Next, the gas supply unit 3 is installed in the flowing water pipe 2.
Next, a decompression unit 8 for decompressing the liquid to be treated is provided.
Next, a water collection tank 9 for sterilizing the liquid to be treated supplied from the decompression unit is installed. The water collection layer has a circulation pump 10 for circulating the supplied liquid to be treated, and clay minerals 11 and fibrous copper 12 are arranged at positions where the circulating liquid to be treated can be contacted. ing.

Flowing water pipe:
Below, the structure of the sterilization processing apparatus 1 of this invention is demonstrated in detail. First, the flowing water pipe 2 in the sterilization apparatus 1 will be described. The water flow pipe 2 is a water distribution pipe for securing a liquid flow path. In general, it may be a resin pipe or metal pipe with a circular cross section, but the shape and material are not particularly limited, taking into consideration the type of liquid flowing and the desired flow rate, etc. Can be designed as appropriate.

Liquid to be treated:
The liquid to be treated is not particularly limited as long as it exhibits fluidity capable of flowing in the flowing water pipe. Ballast water mounted on ships, circulating water such as pools and bathtubs, seawater, well water, river water, medical or industrial water, fishery / agricultural cleaning water, livestock sewage, food factory wastewater, aquaculture fisheries Examples include purification of irrigation water and removal of harmful substances such as plankton in coastal fishing grounds, but are not limited thereto, and any liquid that requires sterilization and removal of heavy metals may be used.

Gas supply part:
In the gas supply unit 3, the gas communicated from the gas supply pipe 23 is supplied to the liquid to be processed flowing through the flowing water pipe 2. Examples of the gas supply unit 3 include, but are not limited to, an injector that is a device that mixes liquid and gas, a porous ceramic filter that can supply gas in the form of fine bubbles, and a mesh filter. In order to supply the gas to the liquid to be treated which is accelerated and pressurized, it is preferable to use an injector as the gas supply unit. Further, examples of the gas to be supplied include ozone, oxygen, air, carbon dioxide, nitrogen and the like, but are not limited thereto. Ozone having a high sterilizing effect is preferable.
As shown in FIG. 2 (2 a), the injector 26 is provided in the flowing water pipe 3 through the bypass 25. The injector 26 applies the venturi effect. That is, when the cross-sectional area of the fluid flow is reduced and the flow velocity is increased, a portion where the pressure is low is created (FIG. 2 (2b)). Supply of the gas D from the part where this pressure became low can be performed easily.

  In the present embodiment, the gas supply unit 3 is provided between the centrifugal pump 4 and the swirling flow reversing unit 7 and between the swirling flow reversing unit 7 and the decompression unit 8, but may be provided only in either one. Good. That is, the gas supply unit 3 may be provided at least at one place between the centrifugal pump 4 and the swirling flow reversing unit 7 or between the swirling flow reversing unit 7 and the decompression unit 8.

  In the liquid to be treated used in the present invention, a special advantage is obtained by supplying a gas that is not dissolved or a gas having a small dissolved amount from the gas supply unit and generating a large amount of fine bubbles of the gas in the liquid. Some examples of enjoying this are described below.

  For example, when the present invention is carried out using water from a tank for raising fish or water poured into a farm and using oxygen or a gas having an oxygen concentration of 60% or more as a gas supplied from a gas supply unit In this case, water having a high oxygen concentration and maintaining the high oxygen concentration for a long time is provided to an aquarium or a farm, which is very advantageous for fish breeding.

  As another example, in the purification of the liquid to be treated, the sterilization apparatus of the present invention can be used for the purpose of killing aerobic bacteria that survive in the liquid to be treated. Specifically, an unpurified liquid is used as the liquid to be flowed in the present invention, and nitrogen or a gas containing 60% or more of nitrogen is supplied from the gas supply unit to carry out the present invention. Then, oxygen dissolved in the liquid to be treated is replaced with fine nitrogen, and the liquid to be treated can be made rich in nitrogen. Moreover, since nitrogen is in the form of fine bubbles, it is not easily released from the liquid to be treated, but dissolves in the liquid to be treated for a long time, so that aerobic bacteria in the liquid to be treated can be sufficiently killed. Is possible.

  Alternatively, as another example, conventionally, there is a purification method in which a specific aerobic bacterium is supported on a carrier and the liquid to be treated is caused to flow therethrough, whereby the microorganisms in the liquid to be treated are killed by the action of the aerobic bacteria. As is known, when such a treatment system is implemented, if the liquid to be treated is filled with oxygen fine bubbles in advance using the sterilization treatment apparatus of the present invention, the aerobic bacteria carried on the carrier are removed. Since it can be activated, the killing action of microorganisms can be improved.

  As described above, the sterilization apparatus of the present invention can exert very advantageous effects in various fields depending on the liquid selected and the type of gas supplied. Moreover, since a large amount of fine bubbles can be generated in a short time in the present invention, the amount of gas contained in the liquid can be easily increased, so that the device of the present invention is only passed once. Thus, it is possible to generate desired fine bubbles, or it is possible to significantly reduce the number of circulations compared to the conventional method and to shorten the processing time.

Liquid speed adjusting means (vortex pump):
In the centrifugal pump 4, pressure is applied to the liquid to be processed by an impeller (impeller), and the liquid to be processed is accelerated. In addition, when bubbles (gas) are included in the liquid to be processed, the bubbles in the liquid to be processed are sheared and refined by the impeller of the centrifugal pump 4. By adjusting the centrifugal pump 4, it is possible to freely accelerate and decelerate the liquid to be processed. In this embodiment, a spiral pump is used as the liquid speed adjusting means. However, the present invention is not limited to this, and various types of liquids other than various pumps such as cascade pumps (vortex pumps), turbine pumps, gear pumps, and piston pumps are used. Speed adjusting means can be used. A pump having an impeller is preferable because it can generate fine bubbles by shearing the bubbles in the liquid to be treated. Further, the cascade pump (vortex pump) is preferable because of its structure, since the impeller is less damaged by the liquid to be treated containing bubbles and is excellent in durability. In addition, in order to accelerate a to-be-processed liquid, although the pressure applied to the to-be-processed liquid may be suitably adjusted according to the flow velocity of a desired to-be-processed liquid, generally about 0.1-9.8 MPa It is preferable that

Swirl reverse part:
In the swirling flow reversing unit 7, first, the liquid to be treated flowing through the flowing water pipe 1 is pressurized by the centrifugal pump 4 and the flow velocity is increased, and first contacts the swirling flow generating fixed wing body 5. The plurality of fixed wings constituting the swirling flow generating fixed wing body 5 has an inclination in the spiral direction, and is guided to the fixed wing to rotate the liquid to be treated in a direction indicating the spiral direction. Next, the liquid to be treated that swirls in this direction contacts the swirl flow generating fixed wing body 6. Here, the swirl flow generating fixed wing body 6 includes fixed wings inclined in the spiral direction opposite to the left and right of the fixed wing body 5 in the swirl flow generating fixed wing body 5. It turns in the direction which shows the spiral direction which is opposite direction.

The generation of the liquid to be processed and the fine bubbles that pass through the swirling flow reversing part will be described in more detail with reference to FIG. As described above, the liquid to be treated comes into contact with the fixed blade in the swirl flow generating fixed blade body 5 while being accelerated by the centrifugal pump as the liquid speed adjusting means and the flow velocity is increased. Fine bubbles are generated by the collision force at this time.
Next, the liquid to be treated that swirls in the direction of arrow B contacts the fixed wings in the swirl flow generating fixed wing body 6 including the generated fine bubbles. By the contact with the second fixed blade, the bubble diameter of the gas contained in the liquid can be further reduced.

Further, the liquid to be treated is guided by the inclination of the fixed blade in the swirling flow generating fixed blade body 6 and the flow direction swirls from the direction of arrow B to the direction of arrow C, that is, the direction opposite to 360 degrees. Due to this rapid change in the flow direction, a torsional shearing force can be applied to the liquid, whereby a larger amount of fine bubbles can be generated. Moreover, the microorganisms in water can be crushed with the shear force by a swirl flow.
As a result, the liquid to be treated that has passed through the swirl flow reversal section contains a large amount of microbubbles or nanobubble-sized fine bubbles. The bubbles include both gases such as air that have been dissolved in the liquid from the beginning and gases supplied by the gas supply unit, both of which have very fine bubble diameters and are dissolved in the liquid to be treated. To do. In this way, a large amount of fine bubbles can be generated in the liquid to be processed that passes through the swirl flow reversing part for a short time.

  In the present invention, the “fine bubbles” can be adjusted in size according to the fixed angle of the fixed blade, the flow rate of the liquid, etc., but generally, the microbubbles having a bubble diameter of about 10 μm to several hundred μm, Alternatively, it means nanobubbles having a bubble diameter of several tens of nm to less than 10 μm, or a mixture thereof. Bubbles of these sizes are known to exhibit different physical and chemical effects than bubbles of several millimeters. Taking advantage of these properties, purification, dust adhesion, dissolution in liquids, desorption Various actions such as oxygen action (gas displacement action) can be usefully used in each technical field depending on the purpose.

Fixed wing for swirl flow generation:
The swirl flow generating fixed wing bodies 5 and 6 are for swirling the flow direction of the liquid flowing through the water flow pipe 2 in a specific direction, and are configured to include a plurality of fixed wings inclined in a spiral direction. . Here, “fixed” in the fixed wing body or the fixed wing means that it does not rotate itself by a driving force like a rotating propeller, but is fixed in the flowing water pipe and maintains a certain posture. . By installing the fixed wing body and the fixed wing in the flowing water pipe as described above, the driving force for rotating the wing is not necessary, and the energy cost is reduced. In addition, when a liquid collides with a rotating wing, the wing may be damaged or destroyed depending on the collision force. However, in the present invention, the wing is fixed in the water pipe, and such a concern is caused. There is no.

The characteristic feature of the swirling flow generating fixed wing body in the present invention is that two or more swirling flow generating fixed wing bodies are provided in parallel in the flowing water pipe and two adjacent swirling flow generations. The fixed wing included in the fixed wing body for use is inclined in the spiral directions opposite to each other. Therefore, the liquid that passes through the swirl flow reversing portion formed of the swirl flow generating fixed wing body is changed from a substantially straight flow to a swirl flow first, and then the flow direction is reversed so as to always swirl in the opposite direction.
As described above, the swirling flow generating fixed wing body and the fixed wing provided therein according to the present invention can guide the liquid in the swirling direction and be fixed in the flowing water pipe. For example, there is no particular limitation, and for example, a generally known propeller shape, which is fixed inside the flowing water, can be used as the fixed wing body for generating swirl flow of the present invention. The method of fixing the swirl flow generating fixed wing body and the fixed wing in the water pipe is not particularly limited and is arbitrary. The number of fixed blades in one swirling flow generating fixed blade body is not particularly limited as long as it is two or more.

  One embodiment of the preferred swirl flow generating fixed wing bodies 5 and 6 is shown in FIG. FIG. 4 is a cutaway perspective view for showing one embodiment of the swirl flow generating fixed wing bodies 5 and 6 in the swirl flow reversing unit 7. The fixed flow body 5 for swirl flow generation shown in FIG. 4 is composed of four fixed wings 13 and a ring 14. The four fixed wings 13 are coupled to each other at the center of the wing, and the outer edges of the fixed wing bodies 5 are ring rings. 14 is joined to the inner wall surface. The outer wall surface of the ring 14 is joined to the inner wall surface of the water pipe 2, whereby the swirl flow generating fixed wing body 5 is fixed inside the water pipe 2. Each of the four fixed blades 13 has an inclination in the same spiral direction, and the passing liquid can be swung in the direction of arrow B shown in FIG. On the other hand, the swirl flow generating fixed wing body 6 includes four fixed wings 15, and each of the fixed wings 15 has an inclination in a spiral direction opposite to the fixed wing 13. The configuration is the same as that of the swirl flow generating fixed wing body 5. Therefore, as shown in FIG. 3, the swirl flow generating fixed wing body 6 can reverse the flow direction of the liquid passing therethrough from the arrow B direction to the arrow C direction.

  As shown in FIG. 5A, for example, the swirl flow generating fixed wing bodies 5 and 6 shown in FIG. 4 use a metal disc 17 that can withstand the flow velocity of the liquid, and the outer periphery of the disc 17 is directed toward the center of the circle. It can be configured using four cuts 18. In the case of this mode, the region between the adjacent cuts 18 corresponds to the fixed wing 13 or 15. That is, the fixed wing 13 or the fixed wing 15 having a desired angle can be formed by twisting so that the region surface between the notches 18 is inclined in a spiral shape of a desired angle.

  FIG. 5 b is a front view of the swirl flow generating fixed wing body 5 formed using the disk 17, and is a front view of the swirl flow generating fixed wing body 5 shown in FIG. The fixed wing of the sheet is continuous at the center of the wing, the outer edge of the fixed wing is welded to the inner wall surface of the ring 14, and the outer wall surface of the ring 14 is joined and fixed to the inner wall surface of the water flow pipe 2. ing. 5c is a front view of the swirl flow generating fixed wing body 6 shown in FIG. 4, except that the torsional direction of the region between the notches 18 is swirled in a spiral shape opposite to the fixed wing 13. It is comprised similarly to the fixed wing | blade body 5 for a flow generation. Although not shown, instead of forming a swirl flow generating fixed wing body using a disk as described above, a desired number of independent wings for the fixed wing are prepared in advance and welded at the center of each other. Alternatively, the swirl flow generating fixed wing body may be created by welding the outer edges of the respective wings to the inner wall surface of the ring.

  FIG. 6 shows another embodiment of the swirl flow generating fixed wing body of the present invention. FIG. 6 a is a perspective view showing the swirl flow generating fixed wing body 5 having a plurality of independent fixed wings 19 fixed to the inner wall surface of the water flow pipe 2. The independent fixed wings 19 are arranged in the circumferential direction in the same direction and in a spirally inclined posture, and the outer edges thereof are fixed to the inner wall surface of the water flow pipe 2, whereby the swirl flow generating fixed wings are arranged. The body 5 is constituted. 6b is a front view showing the swirl flow generating fixed wing body 6 having a plurality of independent fixed wings 20 fixed to the inner wall surface of the water flow pipe 2, and is a spiral shape of the fixed wing 19 shown in FIG. 6a. The configuration is the same as that of the swirl flow generating fixed wing body 5 except that the fixed wing 20 is tilted to the side opposite to the tilt. As described above, the swirling flow generating fixed wing body used in the present invention is not particularly limited in shape and configuration, and is for guiding the liquid passing through the swirling flow generating fixed wing body to swirl. It is only necessary to have fixed wings.

  In the above description, the swirl flow reversing unit using two parallel swirl flow generating fixed blades has been described as an example. This is not to exclude using the body in parallel. In the present invention, the number of swirl flow generating fixed blades is two or more and is arbitrary. However, it is important that the fixed wing bodies for generating the swirl flow adjacent to each other are configured such that the fixed wings of the fixed wing bodies are inclined in opposite spiral directions. This is because the flow direction of the liquid can be rotated in the opposite direction by 360 degrees, and at this time, a torsional shearing force can be applied to the liquid.

  As described above, it is important that the fixed wings in the present invention have spiral inclinations that are opposite to each other so that the liquid swirls in opposite directions in adjacent swirl flow generating fixed wing bodies. The specific angle may be designed as appropriate. However, in the adjacent swirl flow generating fixed wings, when a liquid collides with the first swirl flow generating fixed wing located on the upstream side and the second swirl flow generating fixed wings located on the downstream side. In order to obtain the impact force more advantageously, the pitch of the first swirl flow generating fixed wing body is preferably equal to or greater than the pitch of the second swirl flow generating fixed wing body.

  Here, in the present invention, the “pitch of the swirl flow generating fixed wing body” means a distance that the swirl flow of the liquid that contacts the swirl flow generating fixed wing body travels in the downstream direction in one swirl. That is, when it is desired to design a large pitch, each fixed wing is tilted and fixed to the horizontal direction with respect to the flow direction of the flowing water pipe. What is necessary is just to incline and fix to the perpendicular direction side with respect to the flow path direction of a pipe | tube. In other words, when the pitch is designed to be large, the resistance force when the fixed wing and the liquid come into contact with each other becomes small, and the liquid flows a larger distance during one turn while slowly drawing a spiral, while the pitch is reduced. In the case of a small design, the resistance force when the fixed wing comes into contact with the liquid increases, and the distance that flows during one turn of the spiral decreases.

Pressure reducing part:
The decompression unit 8 is provided by enlarging the inner diameter of the flowing water pipe from the upstream side to the downstream side. The liquid to be treated that is accelerated and pressurized from the swirling flow reversing unit 7 enters the flowing water pipe having a small inner diameter and is reduced in pressure through the flowing water pipe that expands. By reducing the pressure of the liquid to be processed, gas dissolved in the liquid to be processed is generated, and bubbles generated in the swirl flow reversing unit 7 become finer.

Catch tank:
The water collection tank 9 is provided with a circulation path 22 having a circulation pump 10 as a circulation means on the side surface thereof, and the liquid to be treated flowing from the decompression section 8 is circulated in the water collection tank 9. Note that when the liquid to be treated supplied from the decompression unit has a flow rate sufficient to circulate in the water collection tank, the circulation means (circulation pump) may not be provided. Moreover, it arrange | positions in the water-collecting tank 9, and arrange | positions the fibrous copper 12 so that it may contact with the to-be-processed liquid to circulate. Fibrous copper has a large contact area with the liquid to be treated, and copper ions are eluted into the liquid to be treated, killing bacteria in the liquid to be treated and exhibiting an excellent sterilizing / antibacterial action. Further, the clay mineral 11 is disposed in the water collection tank 9 and is configured to come into contact with the liquid to be circulated. By such contact, fine particles (algae, microorganisms, mold, metal, etc.) of about 10 to 1000 nm in the liquid to be treated can be aggregated and removed. Copper and clay minerals can be provided in any part of the water collection tank as long as they can contact the circulating liquid to be treated.

Circulation means:
In this embodiment, a circulation path 22 having a circulation pump 10 is provided as a circulation means. In the present invention, at least one circulation means is provided in the water collection tank. The circulation pump 10 only needs to circulate the liquid to be treated in the water collection tank, and examples thereof include a vortex pump, a cascade pump (vortex pump), a turbine pump, a gear pump, and a piston pump. Moreover, although the installation location of the circulation means is provided in the side surface portion of the water collection tank 9 in this embodiment, it may be provided anywhere as long as the liquid to be treated can be circulated in the water collection tank. Examples of other circulation means include a circulation path for bypassing the liquid to be treated. The fine bubbles contained in the liquid to be treated have a very small bubble diameter and a fine bubble volume, so that they remain long without floating in the liquid to be treated. Therefore, the liquid to be treated containing the object to be removed in the fine bubbles is circulated and raised by the circulating means, and is removed by flotation from the water distribution pipe 21. Further, by circulating the liquid to be treated in the water collection tank 9, the chances of contact between the clay mineral 11 and the copper 12 can be increased.
The liquid to be treated by flotation removal from the water distribution pipe 21 may be discarded as it is, but after removing the object to be removed through a removal means 27 such as a filter, it is returned to the water flow pipe 2 upstream of the centrifugal pump 4. Then, the sterilization treatment can be performed again by the sterilization treatment apparatus 1 of the present invention.
The liquid to be treated that has been sterilized moves to the next step through the water distribution pipe 24, but a harmful metal treatment means 28 may be provided in the water distribution pipe 24. Providing a toxic metal treatment means is preferable because the liquid to be treated can be further purified. The harmful metal treatment means is not particularly limited as long as it is a means for removing harmful metals in addition to various filters such as a mesh filter, a nonwoven fabric filter, and a heavy metal adsorbent-containing filter.

Heavy metal (copper):
In this embodiment, fibrous copper 12 is used as the heavy metal. The diameter of the fiber is 1 mm or less. Preferably, it is about 20-150 micrometers. More preferably, it is about 80 μm. This is because the effective contact area is ensured and the strength can withstand contact with the liquid to be treated. Furthermore, it is more preferable that the fibrous copper is made into a cotton shape in order to secure an effective contact area and strength capable of withstanding the contact. In addition, the shape is not limited to the fibrous shape as long as the contact area with the liquid to be processed is large. Examples of other shapes include powders and meshes. As the heavy metal, one having a bactericidal action by generating metal ions is used. For example, copper, silver, mercury, gold, lead, platinum, nickel, chromium, aluminum, tin, zinc, iron and the like can be mentioned. A metal containing at least copper having strong sterilizing power is preferable. For example, pure copper, brass (brass), high steel alloy, bronze, copper nickel alloy and the like can be mentioned.

Clay minerals:
The clay mineral 11 can be appropriately selected and used as long as it is generally understood as a clay mineral. More specifically, in the present invention, the clay mineral means a compound mainly composed of a crystalline inorganic component generated when the clay component is subjected to very high heat and pressure in the ground. As the clay mineral, a layered silicate mineral is common. The layered silicate mineral includes a tetrahedron sheet formed by secondary connection of tetrahedrons (Si-O tetrahedrons) composed of silicon and oxygen, and an octahedron sheet obtained by further bonding various metal oxides thereto. And mainly consists of There are various metals such as aluminum, magnesium, iron, potassium, etc. that are bonded to the tetrahedron. These metals are generally present in clay minerals in the form of metal oxides. Since the composition of clay minerals is determined by the environment in which they are formed and the soil components of the land, even if they are classified as the same family, the types of compositions are very diverse.

  As a more specific example of the clay mineral in the present invention, kaolinite, smectite, montmorillonite, sericite (sericite), illite, sea green stone (groconite), chlorite (chlorite), Amphibolite, talc, zeolite (zeolite), Wakkanai siliceous shale, diatomaceous earth, and the like.

  In the present invention, the mechanism by which minute removal objects existing in the liquid to be treated aggregate due to the liquid to be treated coming into contact with the clay mineral is not clear. However, the present inventors have found that the agglomeration is caused by the metal component contained in the clay mineral eluting in the state of ions in the liquid to be treated, and the minute objects to be removed are attracted to the charge of the metal ions. This is a phenomenon, and the minute removal object having a charge opposite to the charge on the surface of the aggregate formed by using metal ions as nuclei (that is, the same charge as the above nuclei) is further attracted, resulting in secondary aggregation. I guess that can happen. In addition, following the above-described secondary aggregation, similarly, tertiary and quaternary aggregation in which a minute removal target having a charge opposite to the charge on the aggregate surface is attracted to the aggregate surface may occur. It is guessed.

  Therefore, the “aggregation” observed in the practice of the present invention refers to a nucleus that is a metal ion having a positive or negative charge contained as a composition component of clay mineral, and a treatment liquid having a charge opposite to that of the nucleus. It is inferred that this is a phenomenon in which a minute object to be removed is bonded by van der Waals force, and a minute object to be removed having a charge opposite to that on the surface of the aggregate formed thereby is the surface of the aggregate. It is considered that the phenomenon of being further attracted to and bound to is also included in the above aggregation.

  From the above viewpoint, particularly, a metal ion serving as a nucleus is preferably an aluminum ion having a large charge. Therefore, among various clay minerals, a clay mineral containing aluminum is preferably used in the present invention. Examples of desirable clay minerals containing aluminium include, for example, chlorite, kaolinite, montmorillonite, sericite, glauconite, amphibole, zeolite (zeolite), Examples include smectite, Wakkanai siliceous shale, and diatomaceous earth.

  Furthermore, the present inventors have obtained the knowledge that the clay mineral having potassium in the composition has a high effect of aggregating the minute objects to be removed. In particular, it has been found that a clay mineral containing the above-described aluminum having a high aggregating action in its composition and further a clay mineral containing potassium as a composition component exhibits a very good aggregating action. At present, this mechanism is not clear. However, potassium existing in natural products is a mixture of nuclides of potassium-39, potassium-40, and potassium-41. Among the different nuclides, potassium-40 has a very small abundance ratio. Although it is a radioisotope, it is known to emit higher gamma rays than cobalt-60. The present inventors activate the metal ions eluted from the clay mineral into the liquid to be treated by the excitation action of the gamma rays emitted from the potassium-40, thereby increasing the ion exchange efficiency. As a result, the metal ions from the clay mineral are increased. It is presumed that the eluate is actively dissolved and becomes a nucleus, and the cohesiveness of the minute removal object in the liquid to be treated is enhanced.

  Examples of various clay minerals have been given as examples of the clay mineral in the present invention described above. By the study of the present inventors, by using chlorite in particular, the object to be finely removed from the liquid to be treated is the gist of the present invention. It was found that the agglomeration of the objects was performed effectively.

  Chlorite generally has a flaky or plate-like form, and is characterized by a monoclinic crystal structure. It is a clay mineral with remarkable cleavage in one direction. It is a metamorphic rock that has been melted in the state of 3000, temperature 2500 °, oxygen-free state, and recrystallized after undergoing metamorphism. In particular, it is abundant in metamorphic rocks generated at low temperatures. Chlorite may also occur when biotite, pyroxene, amphibole, olivine, etc. are altered. Chlorite is generally green in color, but may be colorless, light brown, or yellow. The polychromaticity is weak. As for the optical properties, the optical property is biaxial, and the refractive indexes are α = 1.57-1.67, β = 1.57-1.69, γ = 1.57-1.69. It is known that the birefringence is 0.000 to 0.0200.

In addition, even clay minerals classified as chlorite are very diverse in chemical composition and cannot be specified by one chemical composition, but those classified as chlorite are generally aluminum. One of the characteristics is that there are many in the composition. As an example of the chemical composition formula of chlorite having aluminum in the composition,
(Mg, Fe, Al) ₆ (Si, Al) ₄ O ₁₀ (OH) ₆
Or
(Mg, Fe, Al) ₁₂ (Si, Al) ₈ O ₂₀ (OH) ₁₆
Etc. The above chemical composition formula is just one example of what is classified as chlorite, and different from the composition ratio of the nuclear component, or in place of some or all of the above metals aluminum, magnesium, iron, potassium, Some contain other metal components such as calcium, manganese and titanium. For example, in the case of chlorite having a composition similar to the chemical composition formula described above and containing other metals such as potassium, potassium ions may be contained by replacing some of the metals such as aluminum. It is.

  As described above, potassium-40, which is a part of potassium that may be present in clay minerals, is expected to activate other metal ions and increase their ion exchange efficiency. There are those in which potassium is included in the composition, and chlorite containing such potassium in the composition is very preferably used as the clay mineral in the present invention.

The clay ore used in the present invention may be a clay mineral as specifically exemplified in the above, particularly one kind of clay mineral having aluminum or further potassium in its composition, or a combination of two or more kinds of clay minerals. it can. Especially, it is preferable that chlorite is contained in the ratio of 50 to 100 weight%. The chlorite used preferably contains 5% or more by weight of aluminum oxide (Al ₂ O ₃ ) in its composition, and more preferably 8% or more by weight. Furthermore, in the composition of chlorite, potassium oxide (K ₂ O) is preferably contained in an amount of 0.5% by weight or more, more preferably 0.7% by weight or more, It is particularly desirable that the content is 9% by weight or more. The concentration (%) of the composition in the present invention means the concentration of each composition obtained by fluorescent X-ray analysis.

  When chlorite is 50% by weight or more and less than 100% by weight, the clay mineral of the present invention is a combination of the chlorite and any other one kind of clay mineral or any other two or more kinds of clay minerals. Can be configured. Other arbitrary clay minerals are appropriately selected in consideration of various circumstances such as the action unique to the clay minerals, availability, and cost. For example, clay minerals such as smectite, zeolite, Wakkanai siliceous shale, and diatomaceous earth are inferior to chlorite in terms of the amount of metal ions generated, but have a high adsorption effect on fine removal objects in the liquid to be treated. A combination of these clay minerals and chlorite is mentioned as one of the preferable combinations. Zeolite is known to have a specific action of having a high adsorptive power for heavy metal ions such as cadmium ions and copper ions in the liquid to be treated, or ammonium ions. Therefore, in the present invention, in addition to the function of agglomerating and removing fine objects to be removed in the liquid to be treated, when it is desired to add a function of adsorbing and removing heavy metal ions and ammonium ions in the liquid to be treated. The clay mineral in the present invention may be constituted using chlorite and zeolite, Wakkanai siliceous shale, or diatomaceous earth.

  In the present invention, when two or more kinds of clay minerals such as a combination of chlorite and other clay minerals are used, the clay minerals may be mixed and filled in one container. Good. Alternatively, two or more kinds of clay minerals used in combination as clay minerals in the present invention can be used separately. For example, each room of a container having a plurality of separated rooms may be filled with each clay mineral, or each container is filled with each clay mineral, and these containers are continuously arranged. It may be arranged. Whether clay minerals used in combination of two or more are mixed or separated is mainly determined in consideration of the period of use (exchange period) of those clay minerals. For example, in a clay mineral composed of a combination of chlorite and zeolite, the zeolite is shorter than chlorite when the zeolite is expected to act to adsorb and remove the object to be removed in the liquid to be treated. It is desirable to exchange at a period. Therefore, in order to easily exchange only the zeolite, it is desirable to use them separately in a separate room or a separate container.

  The shape and dimensions of the clay mineral used in the present invention are not particularly limited, and the scale of the sterilization treatment apparatus or the like can be obtained as long as it can exhibit an effect of significantly agglomerating the minute removal object in the liquid to be treated. It may be determined appropriately in consideration of the degree of purification or the type of removal object expected to be contained in the liquid to be treated.

  Moreover, it does not specifically limit about the method of processing the extract | collected natural clay mineral into a desired shape. For example, the collected natural clay mineral mass may be crushed by an appropriate method, or may be processed into a powder, and further, the powder is formed into a pellet shape and baked and hardened by baking. The chlorite desirably used in the present invention can be obtained by pulverizing a collected natural mass to an appropriate size and using it as it is. For example, a soft clay mineral such as zeolite is calcined at about 500 ° C. It is preferable to use after baking through the process.

When seeking higher agglomeration, it is desirable to reduce the size of the crushed clay mineral and increase the overall surface area. However, if the average particle size is less than 0.5 cm in powder form, the clay mineral itself is dispersed in the liquid to be treated and flows with the liquid to be treated, so it must be replenished periodically. Running cost increases. On the other hand, even if the clay mineral itself is not dispersed in the liquid to be treated, the clay mineral having a certain size or more is placed in the water collection tank, and the liquid to be treated is brought into contact with the metal ions from the clay mineral. And the aggregating action can be sufficiently exerted by the presence of the metal ions. From the above viewpoint, the clay mineral used in the present invention is obtained by pulverization so that the average particle size of the massive clay mineral is 0.5 cm or more, preferably 1.0 cm or more, more preferably 1.5 cm or more. It is preferable that the crushed clay mineral is produced.
As described above, by installing clay minerals that are not in powder form and have a certain size in the water collection tank, metal ions can be eluted from the installed clay minerals little by little. The reduction in quantity is significantly slower than in the case of powder. Therefore, if it is a powdery clay mineral, it needs to be replenished continuously, and if it is a crushed clay mineral of the above preferred dimensions, it can be replaced at regular intervals, which is very expensive in terms of cost and maintenance labor. It is advantageous. In addition, the half-life of the effect of the aggregating action of the clay mineral in the liquid to be treated varies depending on the size of the lump and the type of the clay mineral, but is about 5 to 20 years. Depending on the type of liquid to be treated and the concentration and content of the object to be removed, the crushed clay mineral once installed in the sterilization apparatus of the present invention can be used continuously for a maximum of several years. It is.

  On the other hand, the upper limit of the size of the crushed clay mineral is not particularly limited. However, in order to sufficiently agglomerate minute removal objects in the liquid to be processed and not to disturb the flow of the liquid to be processed, 1 The average particle size of each crushed clay mineral is desirably 10 cm or less, more desirably 5 cm or less, and particularly desirably 3 cm or less. If it is the range of the desirable average particle diameter mentioned above, the magnitude | size of the clay mineral used for this invention may be uniform, and the crushed clay mineral of a different average particle diameter may be mixed.

  The contact between the crushed clay mineral and the liquid to be treated may be performed by filling the container in which the liquid to be treated can pass with the crushed stone clay mineral and placing it in a position where the liquid can be contacted. Examples of the container include a bag having a pore size that does not allow passage of the crushed clay mineral, a case in which at least a part of the side surface is formed of a mesh that does not allow passage of the crushed clay mineral, or a liquid to be treated. An inlet and a drain outlet are provided, and the liquid to be treated that has entered the container through the inlet can flow through the container while being in contact with the clay mineral in the container and be drained from the drain outlet. Can be used. The description regarding the aspect of the said container does not limit the container used for this invention, The container of a various aspect can be used for this invention in the range which does not deviate from the meaning of this invention.

[About the sterilization treatment method of the present invention]
The sterilization treatment method of the present invention is a sterilization treatment performed using the sterilization treatment apparatus 1 described above. The sterilization treatment method of the present invention will be described with reference to FIG.
FIG. 1 is a sterilization treatment apparatus 1 showing an embodiment of the present invention, and is a schematic cross-sectional view cut in a direction in which a liquid to be treated flows in the apparatus.
Pass the liquid to be treated through the flowing water pipe 2,
Increasing the flow rate of the liquid to be treated by the centrifugal pump 4 installed in the flowing water pipe 2;
Next, gas is supplied to the liquid to be processed from the gas supply unit 3 installed in the flowing water pipe 2, and bubbles contained in the liquid to be processed are refined.
Next, the bubbles contained in the liquid to be treated are further refined by the swirling flow reversing unit 7 installed inside the flowing water pipe 2.
Next, gas is supplied to the liquid to be treated from the gas supply unit 3 provided between the swirling flow reverse unit 7 and the decompression unit 8.
Next, the decompression unit 8 decompresses the liquid to be treated to further refine the bubbles contained in the liquid to be treated.
Next, the liquid to be treated supplied from the decompression unit 8 is stored in a water collection tank 9 for sterilization. In the water collecting tank 9, the supplied liquid to be treated is circulated in the water collecting tank 9 by the circulation pump 10, and the circulating liquid to be treated is brought into contact with the clay mineral 11 and the fibrous copper 12.
The to-be-processed liquid sterilized moves from the water distribution pipe 24 to the next process. When the hazardous substance removing means 28 is provided in the water distribution pipe 24, after the harmful metal is removed by the means, the process proceeds to the next step.
Objects to be removed such as microorganisms, metals and organic substances are aggregated and discharged from the waste water pipe 21 (flotation removal). The liquid to be treated which has been removed by flotation from the waste water pipe 21 may be discarded as it is, but after removing the removal target through a removing means 27 such as a filter, it is returned to the flowing water pipe 2 upstream of the centrifugal pump 4. Then, the sterilization treatment can be performed again by the sterilization treatment apparatus 1 of the present invention.
Through the above steps, the liquid to be processed can be sterilized.
The description of each part is the same as that of the sterilization apparatus of the present invention.

  A step of supplying gas to the liquid to be treated from the gas supply unit 3 installed in the flowing water pipe 2, a step of supplying the liquid to be treated containing gas to the swirling flow reversing unit 7 installed in the flowing water pipe 2, As the process of supplying gas to the liquid to be processed from the gas supply unit 3 installed between the reversing unit 7 and the pressure reduction part 8 and the process of supplying the liquid to be processed containing gas to the pressure reduction part 8 are sequentially performed, the liquid to be processed The gas bubbles contained in the gas become finer. That is, as the gas becomes finer, the contact area with the liquid to be processed increases, and a sterilizing effect due to the contact between the liquid to be processed and the gas can be obtained.

  In the water collection tank 9, when the liquid to be treated comes into contact with the clay mineral 11 and the fibrous copper 12, a further bactericidal effect can be obtained.

[Example]
This will be described with reference to FIG. FIG. 7 is a schematic sectional view showing an embodiment of the sterilization apparatus of the present invention.
A water pipe 2 having an inner diameter of 20 mm was prepared as the water pipe. The water flow pipe 2 was connected with a centrifugal pump 4 (“Self-priming self-priming pump for seawater” manufactured by Tsurumi Seisakusho, model: 40TPSPZ-4031A) as a liquid speed adjusting means. On the upstream side of the centrifugal pump 4, a porous ceramic filter (SPG membrane manufactured by SPG Techno Co., Ltd., pore diameter 0.1 μm) was provided as a gas supply part at one place.

Next, a swirl flow reverse portion was provided in the water flow pipe 2.
Prepare a disc of 1.0 mm thick stainless steel (SUS304) cut into a circle with a diameter of 24 mm and insert four 1.15 cm cuts at equal intervals from the circumference toward the center of the circle. A propeller A having four fixed wings was prepared by twisting about 30 degrees from the disk surface so as to incline in the spiral direction. Next, a stainless steel (SAS304) ring having a thickness of 3 mm, an inner diameter of 21.2 mm, and a width of 12 mm was prepared, and the outer edge of the fixed wing was joined to the inner wall surface of the ring, and the swirling flow generating fixed wing body A was obtained. Obtained.
Further, a swirl flow generating fixed wing body is prepared in the same manner as the swirl flow generating fixed wing body A, except that the twisting direction between the cuts is the left and right direction opposite to the fixed wing in the swirl flow generating fixed wing body A. This was designated as a swirl flow generating fixed wing body B.
Next, a flowing water pipe having an inner diameter of 27.2 mm is prepared, the outer wall surface of the ring of the swirling flow generating fixed wing body A is fixed to the inner wall surface of the flowing water pipe, and then downstream of the swirling flow generating fixed wing body A. At the position of 10 cm on the side, the outer wall surface of the ring of the swirling flow generating fixed wing body B was fixed to the inner wall surface of the water flow pipe to form a swirling flow reversing portion.

From the position 20 cm further downstream of the swirling flow generating fixed wing body B, the inner system of the flowing water pipe was enlarged to 70.3 mm, and a decompression section having a length of 10 cm was provided.
The water collection tank 9 had a capacity of 80 L, and 750 g of copper fibers (fiber diameter 80 μm, component ratio: copper 65%, zinc 35%) and 2.5 kg of chlorite were placed inside. The water collection tank 9 is provided with a water distribution pipe 24 and a waste water pipe 21.
(Test 1)
The sterilization test was conducted as follows using the examples.
Liquid used: Seawater (raw water) in Shinagawa City
Liquid flow rate: 2000 kg / h
Supply gas: Ozone ozone introduction amount: 10 g / h
Under the above conditions, after the raw water is injected from the flowing water pipe 2 and ozone is supplied from the gas supply unit while the apparatus is filled with the raw water, the swirl pump is operated and the preliminary operation is performed for about 5 minutes. The test was started.

  As a result, at the start of the test, clear raw water without white turbidity was visually confirmed to be clouded to the extent that the whole became opaque 60 seconds after the start of the test, and a large amount of fine bubbles were generated in the liquid. It was confirmed.

After operating the above example for about 60 minutes, the gas supply and circulation pump were stopped and the operation of the example was terminated. The raw water in the water collecting tank was left as it was, and was observed with the naked eye one hour later. As a result, the raw water in the water collection tank is maintained in a turbid state with bubbles, and the bubbles in the liquid generated by the examples are bubbles with a very small bubble diameter of microbubbles or less, and for a long time. It was confirmed that it was maintained in the raw water.
After starting the test, after 3 minutes and 60 minutes, the liquid to be treated after sterilization was collected from the water distribution pipe as a sample, and the number of viable bacteria in the sample was analyzed. The above test was performed twice, and the analysis results are shown in Table 1. The unit of the viable cell count in Table 1 is the viable cell count / ml, and ND represents 1.0 × 10 ³ cells / ml or less.

  As shown in Table 1, bacteria contained in the liquid to be treated are easily sterilized and antibacterial in a short time, and minute removal objects such as microorganisms, organic substances and metals (cadmium, arsenic, etc.) are aggregated. It was shown in the above test that it can be easily removed by flotation.

DESCRIPTION OF SYMBOLS 1 Sterilization processing apparatus 2 Flowing water pipe 3 Gas supply part 4 Centrifugal pump 5, 6 Swirling flow generation fixed wing body 7 Swirling flow reverse part 8 Decompression part 9 Catchment tank 10 Circulation pump 11 Clay mineral 12 Copper 13, 15 Fixed wing 14, 16 Ring 17 Disk 18 Notches 19, 20 Fixed wing 21 Waste water pipe 22 Circulation path 23 Gas supply pipe 24 Water distribution pipe 25 Bypass 26 Injector 27 Removal means 28 Toxic metal treatment means

Claims (8)

A water pipe for supplying the liquid to be treated;
Liquid speed adjusting means for adjusting the flow rate of the liquid to be treated provided in the water flow pipe;
Two or more swirl flow generating fixed wing bodies arranged in parallel from the upstream side to the downstream side provided in the water flow pipe , wherein the adjacent swirl flow generation fixed wing bodies are arranged in a spiral direction opposite to each other in the horizontal direction. A swirl flow reversing unit comprising a fixed wing having an inclination ;
A decompression unit for decompressing the liquid to be treated supplied from the swirl flow reversing unit;
And an injector for feeding a gas that is provided to each of at least one place between the pressure reducing portion, and between the swirling flow reversal portions of the swirling flow reversal portions and the liquid velocity adjusting means,
It consists of a water collection tank that sterilizes the liquid to be treated supplied from the decompression unit, and
In the water collecting tank, a sterilization treatment apparatus is characterized in that clay minerals and heavy metals are arranged at positions where the liquid can be contacted. The current water tank, sterilizing apparatus according to claim 1, characterized by providing at least one location circulating means for circulating the liquid to be treated. The sterilization apparatus according to claim 1 or 2, wherein the liquid speed adjusting means is a cascade pump or a centrifugal pump. The sterilization apparatus according to any one of claims 1 to 3 , wherein the heavy metal is a fiber-shaped metal containing at least copper. Pass the liquid to be treated through the water pipe,
Next, the liquid to be processed is passed through a liquid speed adjusting means for adjusting the flow rate of the liquid to be processed provided in the flow pipe,
Next, two or more swirl flow generating fixed wing bodies paralleling the liquid to be treated from the upstream side to the downstream side provided in the water flow pipe , the adjacent swirl flow generating fixed wing bodies are mutually, Through a swirl flow reversing part comprising a fixed wing having an inclination in the opposite spiral direction ;
Next, the liquid to be treated supplied from the swirl flow reversing unit is passed through a decompression unit that decompresses the liquid to be treated.
The gas from the injector provided in each of at least one place between the pressure reducing portion, and between the swirling flow reversal portions of the swirling flow reversing section the liquid velocity adjusting means is supplied to the liquid to be treated,
Pass the liquid to be treated supplied from the decompression section through a water collection tank for sterilization,
and,
A sterilization treatment method comprising contacting a liquid to be treated with clay mineral and heavy metal in the water collecting tank.   6. The sterilization method according to claim 5, wherein in the water collection tank, the supplied liquid to be treated is circulated by a circulation means provided at least at one place.   The sterilization method according to claim 5 or 6, wherein the liquid speed adjusting means is a cascade pump or a centrifugal pump.   The sterilization treatment method according to any one of claims 5 to 7, wherein the heavy metal is a fiber-shaped metal containing at least copper.

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