KR101036181B1 - Apparatus for ship ballast water using electrolysis - Google Patents

Abstract

PURPOSE: An electrolytic disinfection apparatus is provided to have maximized disinfection efficiency by increasing the contact area with water. CONSTITUTION: An electrolytic disinfection apparatus comprises the following: a reaction tank(90) including an inlet cap(92) with an inlet hole(92a), and an outlet cap(94) with an outlet hole(94a) for processing water; a pair of crossbars(70,75) combined with the reaction tank; a hydraulic pressure controlling plate(80) controlling the flow of water; and an electrode module(10) in an annular form to wind a positive electrode wire and a negative electrode wire in parallel.

Description

Electrolytic Disinfection Equipment {Apparatus for ship ballast water using electrolysis}

The present invention disinfects water to be disinfected, such as food materials, sterilized water from various medical devices, sterilized washing water from vessels, drinking water from containers, and drinking water from home or catering (hereinafter referred to as 'water to be treated'). The present invention relates to an electrolytic sterilization apparatus which can be sterilized or sterilized. More specifically, the electrode module installed inside the reactor is increased or decreased in accordance with the amount of water to be sterilized to generate sterilized water within a short time. In addition, the present invention relates to an electrolytic disinfection apparatus which maximizes the contact area with the target water to be disinfected, while maximizing the treatment efficiency of disinfection, while making it easy to increase or decrease the electrode module and simplify the structure.

In general, in order to use tap water as drinking water, chlorine is added and disinfected at each water treatment plant. At this time, chlorine has a strong sterilizing power, which contributes to the microbial safety of tap water and has greatly contributed to maintaining safety. Subjects are chlorine susceptible bacteria that have recently caused a mass outbreak of microbial infections caused by tap water, and have been identified as protozoa such as Giardia and Cryptosporidium. This has been taken. In particular, because the spores are the smallest among pathogenic protozoa and have the highest resistance to disinfectant, the disinfection system capable of coping with the spores can function well with other pathogenic protozoa. Cryptosporidium has been detected in various concentrations to be Abbey ... which there is confirmed that the sewage which is discharged humans and animals is a major source of contamination, the highest concentration at the point of water intake has been reported to be up to 10 ³ / 100ℓ. Warping spores are very difficult to inactivate by conventional chlorine disinfection because they are very resistant to chlorine disinfectants or viability.

In addition, large group restaurants, large restaurants, hospitals, etc. require a treatment device capable of instant sterilization so that many people can continuously and safely use food, facilities, and machinery without controversy.

Therefore, in connection with a device for disinfecting fungi, viruses, pathogens, protozoa in water, and the like, the disinfecting water may be disinfected by various techniques such as ozone method, ultraviolet ray method, and high temperature treatment method by applying heat. Treatment research is actively progressed and commercialized, and as an example, Korean Patent Publication No. 2005-100092, Korean Patent Publication No. 2002-39265, Korean Patent Publication No. 2003-73130, the specifications of the disinfection treatment of water by electrolysis Methods of doing this are disclosed.

In the case of Korea Patent Publication No. 2002-39265 (water electrolytic sterilization method and electrolytic sterilization device), it is characterized in that the target water is disinfected by putting it in water to disinfect the hypochlorous acid contained in the electrolyzed water. In this technique, the treated water and the sterilized water are separated, and hypochlorous acid and radicals contained in the electrolyzed sterilized water are put into the treated water to be disinfected, so the lifetime of radicals generated during electrolysis is extremely short. There is a limitation in disinfection efficiency because there is a problem of not only decomposing before reaching the water to be treated, but also utilizing the disinfection effect due to the potential difference formed near the electrode surface and controversial hazards such as excessive hypochlorous acid after sterilization.

In Korean Patent Laid-Open Publication No. 2003-73130, platinum is used as an anode and a cathode by using water characteristics, and water is used as a switching medium, and the platinum wire is wound around the frame to realize virtual mesh electrode points to realize self-destruction of water. And self-healing phenomena to generate free radicals and ozone through continuous repeated underwater discharge, but also due to electrode points intersecting platinum wires due to the winding of platinum wires on the frame in an alternating manner. The adverse effect of the increase is generated, the contact area with water during the electrolysis is limited to only the electrode points have a problem that the ozone generation efficiency is greatly reduced.

In Korean Patent Laid-Open Publication No. 2005-100092 (an ozone generator in which an electrolysis generating core is connected in parallel), the platinum wire of the positive electrode and the platinum wire of the negative electrode are wound on the frame of the electrolysis generating core in the same direction to face each other. However, the present invention is characterized in that the efficiency of ozone generation is improved by maximizing the opposing contact area with water during electrolysis in water, but such a technique includes a plurality of first and second winding supports for winding and supporting the anode line and the cathode line. Since the first and second winding auxiliary supports are used, and in particular, the anode wire and the cathode wire must be connected using separate parallel connection wires, they have a very complicated structure in terms of construction. Of course, there is a risk of defects.

In addition, the first winding support and the first winding support is formed integrally with the plate-shaped partition wall to limit the flow of water, thereby disinfecting the electrostatic method only in a stagnant state, that is, in water. When the amount of water to be treated is large, the flow of water is restricted by the plate-shaped partition wall described above, and the efficiency of treatment of disinfectant water which is desired to be sterilized momentarily is greatly reduced.

In the conventional case, while recognizing the above-mentioned problems, it is not possible to prepare a specific countermeasure.

Therefore, the present invention was devised under the above-mentioned background, and an object of the present invention is to simplify the structure and to directly pass the treated water directly to the electrode module of the reaction tank regardless of the water pressure, flow rate, and flow rate of the groundwater including tap water, so that ozone, The present invention provides an electrolytic disinfecting apparatus capable of instantaneous disinfection of viruses, pathogens, protozoa and bacteria in water due to the generation of hypochlorous acid and potential difference. In contrast, in order not to limit the flow of water in the reaction tank, several electrode modules wound around the anode line and the cathode line are vertically spaced at regular intervals, thereby maximizing the contact area with water.

Another object of the present invention is to provide an electrolytic disinfecting apparatus which can freely increase or decrease the electrode module installed inside the reactor according to the water to be treated and its inflow rate, and the electrolytic disinfecting apparatus is a desired number of pairs of crossbars. It is achieved by binding the electrode module of each other by fitting together without a separate fixing member, by sliding in a sliding manner along the longitudinal direction of the reaction tank or detached from it.

Other objects of the present invention will become more apparent from the following detailed description and the accompanying drawings.

According to the electrolytic disinfection apparatus according to the present invention for achieving the above object, in the electrolytic disinfection apparatus for disinfecting and supplying various viruses, pathogens, bacteria and the like remaining in the water to be treated, such as tap water or ground water; A cylindrical reaction tank having a constant volume and tightly coupled with an inlet cap and an outlet cap having inlets and outlets of water to be treated at both ends; A pair of crossbars having a long width groove and a short width groove at equal intervals along a longitudinal direction and inserted along both inner circumferential surfaces of the reactor to be coupled to the inflow cap and the discharge cap; A disk having a plurality of apertures, having at least two shortening fastening grooves at opposite sides of the mutually opposite edges, and fitted with no flow in the short width grooves of the pair of crossbars, when the pair of crossbars is inserted, the flow direction of the water to be treated; At least one hydraulic pressure control plate that is orthogonally installed orthogonally in the reactor; And an annular cross-sectional shape such that thin anode wires and cathode wires can be wound in parallel with each other at a predetermined interval therebetween, and are inserted so that there is no flow in the long width grooves of the pair of crossbars when the pair of crossbars are inserted. It characterized in that it comprises at least one electrode module orthogonally installed orthogonally in the reaction tank with respect to the flow direction of the water to be treated.

Optionally, the electrode module has an annular cross-sectional shape having a predetermined diameter and thickness, and along the arc direction so that any one of the anode line and the cathode line can be wound in parallel to each other on the front, rear, and outer circumferential surfaces facing each other. A first winding wheel having a winding groove at equal intervals and a pair of long width fastening grooves formed at both edges facing each other such that there is no flow in the long width grooves of the pair of crossbars; And an annular cross-section having a thickness thinner than the diameter of the first winding wheel, wherein the other poles are wound in parallel with the poles wound on the first winding wheel at opposite front, rear and outer circumferential surfaces. Winding grooves are formed at equal intervals along the arc direction, and a pair of long width fastening grooves are formed at both sides of the pair of crossbars to prevent flow. It characterized in that it comprises a second, third winding wheel to be in close contact.

Optionally, one of the upper and the front or rear of the first winding wheel and the second and third winding wheels so that each of the positive and negative wires wound on the first to third winding wheels are wound to be alternately wound. A semicircular arc-shaped parallel binding groove is formed in the upper portion of the front or rear side of the winding wheel, and the anode and cathode parallel lines are formed through the parallel binding groove without being wound up to a limited length from the distal end of the anode and cathode lines. At both ends of the binding groove, a plurality of holes are formed to determine the start of winding and the finishing of winding so that the transverse pole lines can be wound to the outer circumferential surface of the winding wheels.

Optionally, long axis grooves formed along the lengthwise direction of the pair of crossbars so as to cross contact with the electrode module; And a power supply line fitted into the long shaft groove and electrically connected to the wound anode and cathode wires, respectively, when the electrode module is fitted.

As such, several electrode modules wound around the anode line and the cathode line are vertically installed at regular intervals so as not to restrict the flow of water in the reactor, thereby maximizing the contact area with the water, thereby increasing the efficiency of electrolysis. By attaching the desired number of electrode modules to each other's crossbar without fitting a separate fixing member and sliding them along the longitudinal direction of the reactor, the electrode modules can be easily increased or decreased depending on the number of objects to be treated and their inflow. In particular, it is possible to instantaneously disinfect the aquatic organisms and bacteria remaining in the water to be treated regardless of the water pressure, flow rate, and flow rate of the water to be treated. There is an advantage that can generate disinfectant water.

According to the electrolytic disinfection apparatus of the present invention, regardless of the water pressure, flow rate and flow rate of the water to be treated, the water to be treated is directly passed through the electrode module of the reaction tank to generate the virus, aquatic organisms, and the like by generating ozone, hypochlorous acid, and potential difference. Bacteria such as Staphylococcus aureus, Salmonella, flagella, coccyx, toxic Vibrio cholena, Escherichia coli, Norovirus and the like can be instantaneously killed. In addition, when disinfecting various food materials, cooking utensils, sanitary facilities, medical instruments, etc. using electrolytic sterilization water (including ozone, hypochlorous acid, hydrogen peroxide, etc.) that have been instantaneously sterilized by a potential difference, the effect may be maintained for a long time. And, the material produced by electrolysis is naturally reduced to water (H ₂ O) and oxygen (O ₂ ) after a certain period of time is natural-friendly and beneficial to the human body.

In addition, the electrode module of the reaction vessel can be easily increased or changed according to the water to be treated or the amount of water to be treated, so that it can be used for drinking water of large facilities, ships, etc. Not only can be usefully applied to treatment, but also has a large contact area with water, which greatly improves sterilization efficiency during electrolysis.

In addition, since the structure is simplified, bad factors are eliminated during production, and the labor cost is drastically reduced, thereby improving productivity and reducing the unit cost of the product.

1 is a perspective view showing an exploded electrode module of the electrolytic disinfection device according to the present invention,
FIG. 2 is a perspective view illustrating a state in which a cathode wire is wound around a first winding wheel of the electrode module illustrated in FIG. 1;
3 is a perspective view illustrating a state in which the second and third winding wheels are coupled to the first winding wheel of FIG. 2 and a cathode wire is wound;
4 is a perspective view illustrating the electrode module, the crossbar, and the hydraulic pressure control plate of the electrolytic disinfecting apparatus of FIG.
5 is an exploded perspective view illustrating a state in which an electrode module and a hydraulic pressure control plate coupled to the crossbar of FIG. 4 are inserted into a reaction tank,
6 is a cross-sectional view showing a combination of the electrolytic disinfection device of FIG.

Hereinafter, preferred embodiments of the electrolytic disinfecting apparatus according to the present invention with reference to the accompanying drawings will be described in detail.

1 to 5, the electrolytic disinfection device according to the present embodiment is a pair of crossbars that are largely inserted into a reaction tank 90 having a constant volume and length and are inserted into surface contact with both inner peripheral surfaces of the reaction tank. (70) (75), a couple of crossbars (70) and a couple of crossbars (70) and a couple of crossbars (70) for controlling the hydraulic pressure and the flow rate of the water to be treated by being fitted to the pair (75) is coupled to fit and is installed between the hydraulic pressure control plate 80 is composed of a combination of several electrode modules 10 to kill aquatic organisms or bacteria by electrolysis.

At this time, the reaction vessel 90 satisfies the strength condition to withstand the strong hydraulic pressure and the condition that is not corroded or soluble by oxidizing substances such as ozone, hypochlorous acid, etc. generated during salt and electrolysis, and the condition of the non-conductor through the current Material, for example, polypropylene (PP), polyethylene (PE), ABS, and the material is implemented in a cylindrical shape.

Both ends of the cylindrical reaction tank 90 are screwed inlet cap 92 and the discharge cap 94 having an inlet (92a) for the treatment water is introduced and the outlet (94a) for disinfecting water is discharged.

Meanwhile, a plurality of electrode modules 10 and a plurality of hydraulic pressure control plates 80 as shown in FIGS. 3 and 4 are respectively spaced by a pair of crossbars 70 and 75 inside the reactor 90. They are alternately placed, stand up, and installed.

The pair of crossbars 70 and 75 are implemented in the same material as the reactor 90, for example, and are manufactured in a rectangular cross-sectional shape having a predetermined length.

4, the crossbars 70 and 75 of the rectangular cross-sectional shape are arranged in the short width grooves 70a and 75a and the long width grooves 70b and 75b at equal intervals along the longitudinal direction, respectively. Longitudinal grooves 70c and 75c are formed in the longitudinal direction, respectively. In addition, a power supply line (not shown) is inserted into the long shaft grooves 70c and 75c for electrical connection with the electrode modules 10. For example, a positive power supply line is fitted in the long axis groove 70c of the crossbar 70 and a negative power supply line is inserted in the long axis groove 75c of the other crossbar 75.

On the other hand, the long width grooves 70b and 75b and the short width grooves 70a and 75a of the pair of crossbars 70 and 75 have a plurality of electrode modules 10 and a plurality of hydraulic pressure interruptions as shown in FIGS. 3 and 4. The plates 80 are alternately arranged and coupled to each other at regular intervals.

The hydraulic pressure control plate 80, for example, is made of the same material as the reaction vessel 90, and is made of a disc shape, such disc-shaped hydraulic pressure control plate 80, as shown in Figure 4, a plurality of through holes (80a) The densely arranged fastening grooves 82 and 84 are centered so as to be fitted into the short edge grooves 70a and 75a of the pair of crossbars 70 and 75 at both edges thereof. It is recessed and provided.

In this way, the short width fastening grooves 82 and 84 are fitted to the short width grooves 70a and 75a of the crossbars 70 and 75, that is, intersected with each other, so that the hydraulic pressure control plates 80 are crossbars ( 70 and 75 are stably coupled without flow and are inserted into the reactor 90 as shown in FIG. 6, so that the hydraulic pressure control plate 80 stands in the reactor 90, that is, the number of objects to be treated. By dispersing and controlling the water pressure or flow rate of the water to be treated flowing into the reaction vessel 90 in the state standing upright with respect to the flow direction through the through holes 80a, the electrode installed at the rear end of the hydraulic pressure control plate 80. The impact on the modules 10 is minimized.

On the other hand, the above-described plurality of electrode modules 10 is large, made of a combination of the first to third winding wheels 20, 30, 40 and the thin anode wire 50 and the cathode ray 55, in detail later In the reactor 90 to be described, electrolysis kills various viruses and bacteria such as noroviruses, flagella worms, coccyx worms, toxic vibrio kolena, E. coli, etc. remaining in the treated water.

The first winding wheel 20 of the electrode module 10 is made of, for example, the same material as the reaction tank 90 and has an annular cross-sectional shape having a predetermined diameter and thickness. As shown in FIGS. 1 and 2, the first winding wheel 20 having an annular cross-section is wound in parallel with the slender anode wire 50 made of the predetermined material, for example, platinum, on the front, rear, and outer circumferential surfaces thereof facing each other. Winding grooves 20a are arranged at equal intervals along the arc direction so as to be fitted to each other, and are coupled to the long width grooves 70b and 75b of a pair of crossbars 70 and 75 at mutually opposite edges. The long width fastening grooves 26 and 28 are recessed in the center direction so as to be provided.

In the center of the inner circumferential surface of the first winding wheel 20, the first winding guide 22 and the first reinforcing bar 24 are formed to cross each other in a horizontal and vertical direction in the form of an annular space portion. And before and after the first winding support 22, the winding auxiliary grooves 22a are formed in the vertical direction at equal intervals along the longitudinal direction so as to match the winding grooves 20a, and the amount of the first reinforcing table 24 Fasteners 24a and 24b are formed at the ends.

In addition, a semicircular arc-shaped parallel binding groove 20b is formed on either side of the front side or the rear side such that the anode wires 50 wound on the first winding wheel 20 are alternately wound and connected in parallel. On both ends of the parallel binding grooves 20b, a plurality of holes 20c to 20f are formed to determine the start of the winding of the anode wire 50 and the finish of the winding.

In the annular first winding wheel 20 having such a structure, first, a thin platinum wire 50 is wound. At this time, as shown in FIG. 2, a hole formed at one end side of the parallel binding groove 20b. Insert the tip of the anode wire (50) from the front to the rear (20c) and then knot the back so that the anode wire (50) does not fall out. And the rear end of the anode wire 50 is guided to be fitted into the long width fastening groove 28 and the semi-circular parallel binding groove (20b) to form a parallel parallel line and then a hole (20d) perforated at the end of the parallel binding groove (20b) ) And discharge it backwards. Here, the anode parallel line defines from the tip of the anode line 50 to a limited length, that is, to the length of the parallel binding groove 20b. Subsequently, the windings 20a are wound along the winding grooves continuously from the winding groove 20a on one side to the winding groove on the other side so that the anode wires 50 passing through the hole 20d can be wound in parallel with each other. When given, that is, starting from the right to continue winding to the left, the anode wire 50 is wound around the anode line 50, that is, the anode parallel line via the parallel binding groove 20b of the semi-circular arc type is connected to be wound. Are not only electrically connected in parallel, they are also fitted into the winding auxiliary grooves 22a of the first winding guide 22 and are wound by close coupling with the second and third winding wheels 30 and 40 which will be described later. It is to maintain the stabilization of, thereby preventing the sagging of the water to be treated flowing into the reaction vessel 90 during electrolysis, the sagging of the anode wire 50 due to the water pressure and flow rate or the flow of left and right.

In the same manner as described above, when the winding of the anode wire 50 is completed, the knot is inserted into the hole 20e so that the anode wire 50 does not fall out.

Meanwhile, the second and third winding wheels 30 and 40 of the above-described electrode module 10 are made of the same material as the reaction tank 90 and have an annular shape that is thinner and thicker than the diameter of the first winding wheel 20. It is manufactured in the form of cross section.

As shown in FIGS. 1 and 2, the second and third winding wheels 30 and 40 have parallel slender cathode wires 55 made of a predetermined material, for example, platinum, on the front, rear, and outer circumferential surfaces thereof facing each other. The winding grooves 30a and 40a are arranged at equal intervals along the arc direction so as to be wound, and the long width grooves 70b and 75b of the pair of crossbars 70 and 75 are formed at opposite edges of each other. The long width fastening grooves 36, 38, 46 and 48 are recessed in the center direction so as to be fitted in the fitting.

In addition, in the center of the inner circumferential surface of the second and third winding wheels 30 and 40, the second and third winding guides 32 and 42 and the second and third reinforcing rods 34 are formed in the form of an annular space portion. (44) are formed to cross each other in the horizontal and vertical directions. And before and after the second and third winding guides 32 and 42, the winding guide grooves 32a and 42a are vertically spaced at equal intervals along the longitudinal direction to match the winding grooves 30a and 40a. Fasteners 34a, 34b, 44a, 44b are formed at both ends of the second and third reinforcing rods 34, 44, respectively.

In addition, one of the second and third winding wheels (30, 40) of the semi-circular arc shape on any one surface of the front or rear surface, that is, the upper side of the front surface so that the cathode wires 55 are wound around the winding wheels alternately. Parallel binding groove 30b and a plurality of holes 30c to 30e are formed.

Before winding the cathode ray 55 to the second and third winding wheels 30 and 40 having such a structure, first, a second portion is formed before and after the first winding wheel 20 on which the anode wire 50 is wound. , The surface of the third winding wheel (30), 40 and then contact the fasteners (34a) (34b), 44a, 44b by engaging the coupling pins (60) (65) to couple as shown in Figure 3 .

In addition, a thin cathode ray 55 of the platinum is wound around the second and third winding wheels 30 and 40 coupled to the first winding wheel 20. In this case, as shown in FIGS. 2, the ends of the cathode ray 55 are inserted into the holes 30c and 40c of the third winding wheels 30 and 40 in turn, and then knotted at the rear of the third winding wheel 40 so that the cathode ray 55 does not fall out. To form. And the rear end of the cathode ray 55 is guided to be fitted into the long width fastening groove 36 and the semi-circular parallel binding groove 30b of the second winding wheel 30 to form a cathode parallel line and then the parallel binding groove (30b) ) Is inserted into the hole 30d perforated at the end of the), the hole 20f of the first winding wheel 20, and the hole 40d of the third winding wheel 40, and then discharged backward. Here, as described above, the cathode parallel line defines the length from the tip of the cathode ray 55 to the length of the parallel binding groove 30b. Subsequently, the second and third winding wheels 30 and 40 can be wound from this time so that the cathode rays 55 passing through the hole 40d of the third winding wheel 40 can be wound in parallel with each other. When the winding grooves 30a and 40a on one side of the winding grooves are continuously wound along the winding grooves on the other side of the winding grooves, that is, starting from the left side and continuing to the right side, the cathode ray 55 is the second winding wheel 30. Cathode wires 55, which are wound and intersected with the cathode parallel line via the parallel binding grooves 30b of the wires, are not only electrically connected in parallel but also wound of the second and third winding aids 32 and 42. Since it is inserted into the auxiliary grooves 32a and 42a to maintain the stabilization of the winding, as described above, the cathode ray 55 is drooped due to the fluctuation or the water pressure and the flow rate of the object to be introduced into the reaction vessel 90 during the electrolysis. However, flow to the left and right is prevented.

In the same manner as described above, when the winding of the cathode ray 55 is completed, the hole 30e of the second winding wheel 30 and the hole 20g of the first winding wheel 20 are again removed so that the cathode ray 55 does not fall out. And it passes through the hole 40e of the third winding wheel 40 in order to form a knot in the rear.

On the other hand, the plurality of pressure interruption plate 80 and the plurality of electrode modules 10 made as described above, as described above, the short width grooves 70a and 75a and the long width grooves (a pair of crossbars 70 and 75). 70b) and 75b are combined to fit. At this time, a pair of long shaft grooves 70c and 75c are fitted with a positive power supply line and a negative power supply line, respectively, and the long width fastening grooves 28 and 36 of the first and second winding wheels 20 and 30, respectively. The anode wire 50 and the cathode ray 55 pass through. Therefore, when the plurality of electrode modules 10 is fitted, the positive power supply line is connected to the positive electrode line 50 and the negative power supply line is connected to the negative electrode line 55 to supply power.

As described above, the pair of crossbars 70 and 75 coupled with the plurality of hydraulic pressure control plates 80 and the plurality of electrode modules 10 are brought into contact with the inner peripheral surfaces of both sides of the reaction tank 90 to be pushed in a sliding manner, and then discharged. By coupling the cap 94 to the reaction vessel 90, as shown in FIG. 6, the plurality of hydraulic pressure control plates 80 and the plurality of electrode modules 10 are standing up in the reaction vessel 90, and a pair of crossbars 70 is provided. One end of the (75) is coupled to the inlet cap 92, the other end is in close contact with the discharge cap (94).

In such a state, when power is applied to the electrode modules 10 of the reaction vessel 90 through the power supply line, the water to be treated is electrolyzed. At this time, the water pressure is lowered through the through hole 80a of the hydraulic pressure control plate 80. The sodium chloride (Nacl) component in the treated water, which has a low flow rate, is replaced with hypochlorite ions (OCL ^_ , HClO) by electrolysis, and passes between the anode line 50 and the cathode line 55 of the electrode module 10. In addition to killing aquatic organisms and bacteria, in addition to electrolysis, OH-radicals, ozone (O ₃ ), H ₂ O _2, etc. are generated to act as sterilization and disinfection. It is reduced to harmless water (H ₂ O) and oxygen (O ₂ ). In addition, due to the potential difference between the anode wire 50 and the cathode ray 55, aquatic organisms and bacteria remaining in the water to be treated burst the cell membranes to instantly sterilize microorganisms such as bacteria.

On the other hand, as a comparative example, since the conventional technique, that is, the treatment target water is sterilized only in the stagnant water by electrolysis, the efficiency of the treatment of the sterilized water which is desired to be sterilized is greatly reduced. By placing several electrode modules wound around the cathode line vertically at regular intervals with respect to the flow direction of the water and installing them in the reactor, the contact area with the flowing water is maximized and the electrode module can be easily increased or decreased depending on the number of objects to be treated. It can be seen that.

As a result, according to the present invention, there is an advantage that a simple structure can be used to instantaneously disinfect aquatic organisms and bacteria remaining in the water to be treated regardless of the water pressure, flow rate and flow rate of the water to be treated.

In addition, although specific embodiments of the present invention have been described and illustrated above, it is obvious that the present invention may be variously modified and implemented by those skilled in the art.

Such modified embodiments should not be individually understood from the technical spirit or the prospect of the present invention, and such modified embodiments should fall within the appended claims of the present invention.

10: electrode module 20: first winding wheel
20a: winding groove 20b: parallel binding groove
30: 2nd winding wheel 36, 38: long width fastening groove
40: third winding wheel 42: third winding support
50: anode line 55: cathode line
70, 75: crossbar 80: hydraulic intermittent plate
90 reactor

Claims (4)

An electrolytic disinfecting apparatus for disinfecting and supplying bacteria or the like remaining in tap water or groundwater;
(1) a cylindrical reaction tank having a constant volume and having an inlet cap and an outlet cap tightly coupled at both ends with an inlet and an outlet of the water to be treated;
(2) a pair of crossbars having a rectangular cross section having a long width groove and a short width groove at equal intervals along the longitudinal direction and inserted into surface contact on both inner circumferential surfaces of the reactor and coupled to the inlet cap and the discharge cap;
(3) A disk type having a plurality of through holes, having at least two shortening fastening grooves at opposite sides of the mutually opposing edges, and inserted into the short width grooves of the pair of crossbars so that there is no flow, when the pair of crossbars are inserted. At least one hydraulic pressure control plate which is installed in an orthogonal state in the reaction tank with respect to a flow direction of the at least one hydraulic control plate; And
(4) when the pair of crossbars is inserted into the long width grooves of the pair of crossbars with an annular cross-sectional shape so that the thin positive and negative wires can be wound in parallel with each other at regular intervals; Electrolytic disinfection device, characterized in that it comprises at least one electrode module standing up in the state orthogonal to the flow direction of the water to be treated.
The method according to claim 1,
The electrode module,
An annular cross-section having a predetermined diameter and thickness, wherein the winding grooves are wound at equal intervals along the arc direction so that the polar lines of any one of the anode line and the cathode line are wound parallel to each other on the front, rear, and outer circumferential surfaces thereof which face each other. A first winding wheel having a pair of width fastening grooves formed at both edges facing each other such that there is no flow in the long width grooves of the pair of crossbars; And
An annular cross-sectional shape larger than the diameter of the first winding heel and thinner, and along the circular arc direction so that the other poles can be wound in parallel with the wound poles at opposite front, rear and outer circumferential surfaces. Winding grooves at equal intervals, and a pair of long width fastening grooves are formed at both sides of the pair of crossbars so as not to flow so as to be tightly coupled to the front and rear of the first winding wheel by a coupling pin. 2, electrolytic disinfection device comprising a third winding wheel.
The method according to claim 2,
The front or rear of the front or rear of the first winding wheel and the winding wheel of any one of the second and third winding wheels so that each polar wire wound on the first to third winding wheels are wound in parallel and connected in parallel. A semi-circular arc-shaped parallel binding groove is formed on the upper portion of the upper and lower ends of the anode line and the cathode line so as not to be wound up to a limited length and passing through the parallel binding groove to form a parallel line between the anode and the cathode, and both ends of the parallel binding grooves. And a plurality of holes for determining the start of the winding and the finishing of the winding so that the transverse pole lines can be wound to the outer circumferential surface of the winding wheels.
The method according to claim 2,
A long axis groove formed in the pair of crossbars along a lengthwise direction thereof so as to cross-contact with the electrode module; And
A power supply line electrically connected to the wound positive and negative wires, respectively, when the electrode modules are coupled to the long shaft grooves; Electrolytic disinfection device characterized in that it further comprises.

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