RU72690U1 - DEVICE FOR ELECTROCHEMICAL TREATMENT OF WATER OR AQUEOUS SOLUTIONS - Google Patents

Abstract

The utility model relates to the field of electrochemical treatment of water and / or aqueous solutions of salts in order to change their oxidizing, reducing and structural properties. The utility model can be used for purification, disinfection, structuring and conditioning of water, cathodic softening of water, as well as for obtaining disinfecting, washing, sterilizing, preserving, bleaching, preventive solutions and solutions that eliminate odors.

The device contains an inner electrode 1 with end blind axial holes 2 with an internal thread and an outer electrode coaxial to it 3. A semipermeable diaphragm 4 is installed between the electrodes, separating the annular cavity into the inner chamber 5 and the outer chamber 6. The outer chamber 6 has an input and output nozzles 7 ′ and 7 ″, which communicate with the camera 6 through the holes in this electrode. The inner chamber 5 has axial inlet and outlet nozzles 8 ′ and 8 ″ with internal axial through holes 9 ′ and 9 ″. At the closed end of the pipe 8 ′ (8 ″), facing the inside of the device, there is a cylindrical protrusion 10 with an external thread for interaction with a threaded hole 2 at the end of the inner electrode 1.

The device has end caps identical to each other at both ends. Each end cover consists of two parts 11, 12. The outward facing part 12 of the assembly cover is pressed by a protrusion (expanding part, flange) on the nozzle 8 ′ (8 ″), which acts as a bolt head, and washer 13. Between the washer 13 and the outer surface the lid is clamped to the current supply electrode 14. The second current supply electrode 15 is fixed to the outer electrode 3.

The inwardly facing portion of the lid 11 is a dielectric sleeve and has channels 16 through which axial holes in the nozzles 8 ′ (8 ″) communicate through the holes 17 in the side walls of the nozzles 5. The channels 16 are located in radial planes and are preferably oriented at an angle to the axis of the device.

Description

The utility model relates to the field of electrochemical treatment of water and / or aqueous solutions of salts in order to change their oxidizing, reducing and structural properties. The utility model can be used for purification, disinfection, structuring and conditioning of water, cathodic softening of water, as well as for obtaining disinfecting, washing, sterilizing, preserving, bleaching, preventive solutions and solutions that eliminate odors.

A device for electrochemical water treatment [Patent RF 2297981, publ. October 21, 2005, Figure 3], which incorporates an outer electrode in the form of a hollow cylinder and an inner rod composite electrode coaxial to it. The annular cavity between the electrodes is divided by a coaxial partition into external and internal chambers equipped with inlet and outlet nozzles. The design has a lower base and an upper end cover. The connection of the base with the electrodes is carried out using bolts. The upper end cover is connected to the inner electrode by means of a hollow bolt, which at the same time is the outlet pipe for the inner chamber, to which it is connected by channels radially passing through the inner electrode. The main drawback of the design is the lack of unification of the end elements, which complicates its manufacture.

The device is deprived of this drawback - a flowing electrochemical modular element for processing liquid [RF patent 2145940, publ. 02.27.2000], which incorporates, as in the analogue described above, an inner rod electrode, an outer electrode, a partition dividing the cavity into an inner and outer chamber, each of which has an inlet and outlet nozzles that are mounted on the end dielectric bushings , the same design for both ends. The assembly of the structure was carried out using bolts screwed into the ends of the internal electrode. Despite the relative unification, the main disadvantage remains the relative

design complexity, since the nodes for input / output of liquid into the inner chamber and the outer chamber are different from each other, and the design provides for additional end fastening elements. Another disadvantage is that the supply and removal of the processed fluid is carried out by radial lateral pipes, which necessitates additional supply using bent pipes (elbows) for installation in a linear highway.

As a prototype, a device for electrolytic water treatment was selected [RF Patent 2132821, publ. 07/10/1999]. The vertical flow-through electrolyzer incorporates an inner hollow electrode, an outer electrode and a baffle separating the annular cavity into the inner and outer chambers. At both ends of the device there is a dielectric sleeve, which is closed by a dielectric block, made similar to a union nut. The supply and removal of the processed fluid to the inner chamber is carried out by radial end pipes - fittings that are screwed onto the ends of the inner electrode. At the same time, these fittings are fasteners. The design of the prototype allows you to mount a flowing electrolyzer in the line of the processed fluid without the use of elbow bends. The main drawback of the design is the fragility of the internal electrode. This is because there are through holes in the wall of the inner electrode through which the cavity of the electrode communicates with the inner electrolysis chamber. In electrolyzers, two types of electrodes are usually used: metal with a coating of metals of the platinum-iridium group, or graphite. When an electrode is made of metal, the presence of holes violates the integrity of the protective coating on the inner electrode, which leads to electrochemical corrosion of the electrode body when it comes in contact with an aggressive environment. When the internal electrode is made of graphite, the presence of holes in the tubular structure increases the fragility of the electrode. In both cases, the service life of the internal electrode is significantly reduced in comparison with integral electrodes (without holes in the side walls).

Thus, there is a technical contradiction: some devices are reliable, but have an excessive number of structural elements - separately for supplying / discharging liquid and, separately, fasteners, for example, end bolts; other devices, for example, a prototype, are relatively simpler because they have elements combining the functions of fasteners and fluid inlet / outlet, but such devices have a limited service life and require frequent replacement of internal electrodes.

The utility model is based on the task of resolving this contradiction and creating a new device for the electrochemical treatment of water or aqueous solutions.

Achievable technical result - increased reliability (long-term operation of the device without replacing the internal electrode) while maintaining the possibility of coaxial connection to the processed fluid line without using elbow bends (direct connection).

The problem is solved in that the device for the electrochemical treatment of water or aqueous solutions includes end caps, an external tubular electrode, inside of which an internal electrode is coaxially located. The annular cavity between the electrodes is divided by a coaxial semipermeable diaphragm into an inner chamber and an outer chamber. Each chamber is equipped with inlet and outlet nozzles, while the inlet and outlet nozzles of the inner chamber are made axial. These nozzles are connected to the internal electrode by a threaded connection and fix the position of the end caps. The device differs from the prototype in that openings are made in the side walls of the axial nozzles, which communicate with the inner chamber through channels. These channels are made in the end caps and are oriented in radial planes. It is preferable that the inner electrode be formed with a rod electrode with blind threaded holes at the end to form a screw pair with an axial nozzle, which, in turn, is provided with a threaded portion on the outer surface.

More technologically advanced is the execution of end caps by prefabricated two-part assemblies and the execution of channels in the parts facing inward.

Channels oriented in radial planes can be perpendicular to the axis of the device, and can be oriented to it at an angle.

In more detail, the essence of the utility model is illustrated by the implementation example described below and is illustrated by the Figure, which shows a longitudinal section of the device.

The device comprises an internal electrode 1, for example, in the form of a rod of cylindrical shape with end blind axial holes 2 with internal thread. A hollow cylindrical (tubular) outer electrode 3 is installed coaxially with the inner electrode 1. A semipermeable diaphragm 4 is installed coaxially between the electrodes, separating the annular cavity into the inner chamber 5 and the outer chamber 6. The outer chamber 6 has an inlet and an outlet pipe 7 ′ and 7 ″, respectively which are radially mounted on the outer electrode 3 and communicate with the camera 6 through the holes in this electrode. The inner chamber 5 has axial inlet and outlet nozzles (fittings) 8 ′ and 8 ″ with internal axial through holes 9 ′ and 9 ″, respectively. At the closed end of the pipe 8 ′, facing the inside of the device, there is a cylindrical protrusion 10 with an external thread for interaction with the threaded hole 2 at the end of the inner electrode 1. A similar protrusion is available at the closed end of the pipe 8 ″.

The device has end caps identical to each other at both ends. More technologically advanced is the design in which each end cover consists of two parts 11, 12. The outward facing part 12 of the assembly cover is pressed by a protrusion (an expanding part, a flange) on the pipe 8 ′ (8 ″), which acts as a bolt head, and the washer 13 Between the washer 13 and the outer surface of the lid, a current-conducting electrode is clamped 14. A second current-conducting electrode 15 is mounted on the outer electrode 3.

The inwardly facing portion of the lid 11 is a dielectric sleeve and has channels 16 through which axial holes in the nozzles 8 ′ (8 ″) communicate through the holes 17 in the side walls of the nozzles 5. The channels 16 are located in radial planes and are preferably oriented at an angle to the axis of the device, and therefore to

the axis of the internal cavity and the axis of the hole 9 ′ (9 ″) of the nozzle, which reduces hydraulic losses. To prevent direct flow of liquids between chambers 5 and 6, O-rings 18 are installed at the ends of the diaphragm 4. The tightness of the device is generally achieved by means of O-rings 19 installed between the covers and in contact with the outer surface of the nozzles 8 ′ (8 ″) and on the other side with the inner surface of the outer electrode 3.

The operation of the device is illustrated by the following examples, in which the current supply is implemented in such a way that the inner electrode is the anode and the outer electrode is the cathode.

The processed fluid is supplied to the pipe 8 ′, from the pipe 8 ″ - the treated liquid (anolyte) is discharged. Depending on what properties the solution needs to be obtained, water and / or various saline solutions are supplied to the device. The pipe 7 ′ is intended for supplying a treatment fluid, for example, saline, pipe 7 ″ - for the removal of saline (catholyte). The nozzles 7 ′ and 7 ″ can be combined into a single external closed circuit (with replenishment of the active substance).

Example 1

To obtain anolyte and catholyte, a 1% solution of sodium chloride is fed into the pipe 8 ′. Through holes 17 and channels 16, the solution enters the inner electrode chamber 5. A voltage is applied to the electrodes. Under pressure, the solution through a semipermeable diaphragm 4 enters the external electrode chamber 6. During operation of the device, two oppositely charged ion flows form on the external and internal surfaces of the diaphragm 4, a potential difference arises between the flows, which leads to an increase in the electric field strength in the diaphragm, as a result the mobility of ions in the pores of the diaphragm increases and the electrical resistance of the device decreases. As a result, an electroactivated solution is formed - anolyte, which is discharged through the channels in the lid and 8 ″ pipe. A 1% sodium chloride solution may also be supplied through pipe 7 ′.

Example 2

To obtain a disinfectant solution, water is supplied through the pipe 8 ′, which enters the inner electrode chamber 5, as described above. At the same time, a 30% sodium chloride solution is supplied through pipe 7 ′, which circulates in an external closed circuit passing through an external electrode chamber 6. Water entering the internal (anode) electrode chamber is saturated by the redox processes in both chambers hypochlorous acid ions, short-lived oxygen radicals, a small amount of ozone and chlorine dioxide due to the migration of ions from the external (cathode) electrode chamber and is discharged through the 8 ″ pipe in the form of nfitsiruyuschego solution.

Example 3

To obtain a disinfecting solution, 1-20% sodium chloride solution is supplied through the pipe 7 ′, which enters the external cathode chamber, then the solution exits the pipe 7 ″ and through the pipe 8 ′ enters the internal electrode chamber. The solution entering the internal (anode) electrode chamber under the influence of redox processes occurring in both chambers is saturated with hypochlorous acid ions, short-lived oxygen radicals, a small amount of ozone and chlorine dioxide due to migration of ions from the external (anode) electrode chamber and is discharged through pipe 8 ″ in the form of a disinfectant solution.

Example 4

To process drinking water, water is supplied from the water supply pipe through the pipe 7 ′, which enters the external cathode chamber, then the water exits the pipe 7 ″ and through the pipe 8 ′ enters the internal electrode chamber. Water entering the inner (anode) electrode chamber, under the influence of redox processes occurring in both chambers, is disinfected, changes the redox potential and is discharged through pipe 8 ″ in the form of clean drinking water.

The examples given do not exhaust the scope of the claimed device, since, depending on the solutions used and the polarity of the electrodes, anolyte and catholyte with other desired properties can be obtained. The device can also be used for disinfecting water, changing the redox potential of water, cathodic softening of water and other purposes.

A device manufactured according to a utility model has been tested using known techniques. The table shows the performance of his work.

Table Name of indicator Value Volumetric flow rate, cm ³ / s 12-22 Linear flow velocity, cm / s 25-64 Water treatment time, s 0.3-1 Current strength, A 0.5-55 Voltage 30-120 Mineralization of water, g / l 0.05-2 Specific amount of electricity, C / l 22.5-135 Resource of continuous work, h 50,000 PH value 2-11 The value of redox potential, mV From (+990) to (-600) The frequency of washing the device from cathode deposits every 300-360 hours of operation

As can be seen from the drawing and the above description, the device has axial nozzles for supplying / discharging the processed fluid, which allows it to be connected directly to the line without the use of additional adapters - elbow bends. The same axial nozzles are simultaneously fasteners, as bolts are screwed into the end holes of the internal electrodes, clamping the electrodes between the end caps. The covers are made identical at both ends. Each can be made by the team and consist of two parts - one part facing outward, and the second part - the inner sleeve. Unlike the prototype, the channels for supplying / discharging the processed fluid are not made in the internal electrode, but in the dielectric sleeve 11 (or in the lid itself, if it is not prefabricated). This increases the overhaul periods for replacing the internal electrode, as it remains solid and

- a special coating protected from electro-corrosion, if it is made of metal,

- has no embrittling holes in it, if it is made of graphite.

With this design and when the channels are run at an angle to the axis of the device, stagnant zones and turbulent turbulence at the input / output of the inner chamber are not formed.

Claims (5)

1. A device for the electrochemical treatment of water or aqueous solutions, comprising end caps, an external tubular electrode, inside of which an inner electrode is coaxially located, the annular cavity between them is divided by a coaxial semipermeable diaphragm into an inner chamber and an outer chamber, each of which is provided with an input and outlet nozzles, while the inlet and outlet nozzles of the inner chamber are made axial, connected to the inner electrode using a threaded connection and fix of the end caps, characterized in that the side walls of the axial nozzle openings communicating with the internal chamber through the channels formed in the end covers, and oriented in radial planes. 2. The device according to claim 1, characterized in that the inner electrode is made of a rod, has a blind threaded hole at each end to form a screw pair with an axial pipe provided with a threaded section on the outer surface. 3. The device according to claim 1, characterized in that the end caps are prefabricated, consisting of two parts, while the channels are made in those parts of the cap that are facing inward. 4. The device according to claim 2, characterized in that the end caps are prefabricated, consisting of two parts, while the channels are made in those parts of the cap that are facing inward. 5. The device according to any one of claims 1 to 4, characterized in that the channels in the end caps are oriented at an angle to the axis of the device.