JPS5864391A - Control mechanism for quantity of water in continuous type water electrolyzing device - Google Patents

Abstract

PURPOSE:To provide economy in continuous formation of water without waste of water by providing simple control mechanisms to water supply lines from electrical insulating means to electrolytic cells and controlling the production ratios between alkali ion water and acidic water. CONSTITUTION:The water released from the water separator 3 of the 1st insulating means 3 into a water receiving tank 3a enters an electrolytic cell 2 through a passage 5 from a water introducing port 2f. The alkali ion water and acidic water formed by receiving electrolysis and electric osmosis effect are brought into water supply nozzles 4f, 4f' as well through valve mechanisms 9, 9' then through pipelines 8, 8'. Here, both are treated with the 2nd electrical insulating means 4 and are received in respective water receiving tanks. In this case, the inflow rates of both passages in the cell 2 are controlled by controlling the openings of the valve discs of the mechanisms 9, 9'. At the same time the DC voltages to be applied are controlled. With such mechanism, the alkali ion water and the acidic water are formed according to the rates of consumption.

Description

DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water flow rate control mechanism in a continuous water electrolysis device for producing alkaline ionized water primarily for drinking.

In this type of continuous water electrolyzer, it is necessary to prevent the electric current for charging water from leaking to the water source (for example, a water pipe) or the end use port (faucet). For this reason, water is supplied to the electrolytic cell via electrically insulating means, and water is taken out from the electrolytic cell via electrically insulating means. In such a continuous water electrolysis device that takes safety precautions into consideration, a problem is that the amounts of alkaline ionized water and acidic water used vary depending on the time. If a large amount of alkaline ionized water is used and acidic water is not needed so much, it is desirable to reduce the amount of acidic water even if the paper value decreases significantly. Conversely, when a large amount of acidic water is required, it is desirable to reduce the amount of alkaline ionized water even if the paper value becomes significantly high.

In this way, it is important to control aquatic aoao in the above-mentioned continuous A decomposition device in order to avoid waste of water.

Jin's invention was made based on the above circumstances, and it is possible to control the generation ratio of alkaline ionized water and acidic water by providing a simple controller II'ft in the water supply path from the electrical insulation means to the electrolytic cell. The present invention aims to provide a water flow rate control mechanism in such a continuous water electrolysis device.

The present invention will be described below based on the illustrated embodiments.

I will explain in detail. In the figure, reference numeral 1 denotes an integral part of the water electrolyzer, and a long and narrow electrolytic cell 2, a first electrically insulating means 3, and a second electrically insulating means 4 are installed in one circle of the above-mentioned body.

Above 1 [s Hinoki 2 is I8 round II on its outer wall? ! It is composed of a cylindrical negative electrode 2a disposed at the wall, a positive electrode 2c of the negative electrode, and a top plate 2d and a bottom plate 2e provided at the upper and lower ends of the outer wall.

The bottom plate 26 is provided with in-filtrate inlets 2f and 2g located on the inside and outside of the unglazed partition wall 2b and communicating with the electrolytic cell 2, and the top plate 26 is also provided with infiltration inlets 2f and 2g. Water ring outlets 2h and 21 are provided on the inside and outside 114 of the thermal spacing 112b and communicated with the inside of the electrolytic cell 2.

The electrical insulation means 3 and 4 respectively include water tanks 3a and 4c%4m', and the water tanks 3a and 4c%4m' respectively.
rj and 4mb 4a'KFi, tilt axis 3b! and 4b,
Water separators 3C and 4c driven by 4b'
, 46' are arranged. The main separators 3eb and 4eb4c' are walls extending in the radial direction in the one-turn direction,
Separation chambers 3d, 4d, and 4dt are divided into a plurality of rt ratios (the number #i must be 3 or more), and mountain-shaped watershed members 3 and 4e are provided on the separation wall.
There is 14・'.

Above the water separators 3c and 4eb4c', water supply nozzles 3f and 4f%4f' are arranged above the inclined shafts 3b and 4b, 4b'.

In addition, in the water receiving tank 3 m s and 4 mb 4 m',
Paths 5 and 6 are provided respectively, and the path 5 is connected to the water inlet 2f of the electrolytic cell 2, and the path 6 is connected to the water inlet 2f of the electrolytic cell 2.
, Da is connected to the cram school, respectively Snake Roa, 1. The water supply nozzles 4f and 4f' are as follows.

Conduit 818: Water ring outlet 2h and 2 of electrolytic cell 2 via
It is connected to 1.

In addition, valve mechanisms 9 and q are provided at the inlet portions of the paths 6 and σ for controlling the respective flow cross-sectional areas. The valve mechanism 9 and the valve mechanism 9 are provided with two valve ports 9a-, g, / that communicate with the paths φ and σ, respectively.
%9b', and the valve bodies 9b, 9b' are pivoted to the pivots 9eb9c''t', and the upper 1e pivots 9c, 9
c' are in an interlocking relationship with each other, and when rotated, the valve body is controlled so as to decrease the opening degree of one of the valve ports 9am 9m' and increase the opening degree of the other.

Note that the water level 1- of the water tank 31 is set so that the water level in the pipe line 8 is lower than the water bell in the water tank 31.
, is located above the electrolytic cell 2.

In such a configuration, a DC voltage is applied between the electrodes 2a and 2c, water is brought onto the water separator 3c from the water supply nozzle 3f, and the rotation of the separator 3at and the inclined shaft 3b When the water is driven, the water that enters the separation chamber 34 sequentially moves to the lower side Kt of the inclined shaft 3b. - is released into the water tank 31. Water supply is not released and separated m3d
However, it is supplied across both sides,
Separation IIK is not injected during discharge, so it is electrically cut off, and even if the water received in the water receiving tank 3a is continuously brought to the electrolytic tank 2, there is no electrical leakage to the water supply nozzle 3f. There is no such thing as Jin. In particular, due to the function of the above-mentioned watershed member, the unit su
Since i is electrically disconnected from Kjllk, such an electrical insulation effect can be achieved.

The water that entered the water tank 3a passes through the path 5.5' to the room 2c' where the positive electrode 2c is located and the fi where the negative electrode 2a is located.
tBjll 2 m' ni so n statarasa n1 electrolytic tank 2
From bottom to top of circle edge i/cf11. % bisque partition wall 2 in the process of
It is subjected to electrolytic and electroosmotic effects via b. Then, alkaline ionized water is generated on the outside of the unglazed space 112b, and acidic water is generated on the 1-yen side. The generated alkaline ionized water and acidic water Fi, the valve mechanism 9 and Cat
- water supply nozzle 4f via line 8.8';

4 f' brought to n, hz electrically insulating means 4, treated as in the case of electrically insulating means 3 of that starvation 1 f'L
1 Receive water in the state of fL′fC, which is electrically disconnected from the turtle tank! #
I 4 am 4 m' respectively.

In this case, by manipulating the shafts 9c and 9C' to reduce the opening degree of the valve port 9a with the valve body 9b and increase the opening degree of the valve port 9&' with the valve body 9b', the opening degree of the valve port 9&' is increased. The flow cover decreases and the flow cover to room 2a/ increases.

When applying a direct current voltage commensurate with the increase in the flow rate to this room 2 m, the concentration of alkaline ionized water is slightly reduced, despite the flL control of the upper 1 pin valve mechanism 9. Keep it in place. On the other hand, the concentration of acidic water increases due to increased pressure and decreased flow velocity and sound.
This will increase significantly, but this is not needed at this point.
Since there is no problem, the amount of water that would be wasted will be saved. If the pivots 9c and 9c' are reversely operated to reduce the opening t of the valve port 9a' by the valve body 9b', the valve body 9
If the opening of the valve port 9a is increased by b, the flow rate of acidic water is increased and the flow rate of alkaline ionized water is decreased. Such control is preferably used when using acidic water.

Note that the conductivity of water t'i with less lEt increases as it deviates from the neutral point, so depending on the case, Fi,
Even without voltage regulation, it helps to reach the Beha value for water with a large flow rate at a predetermined at.

In addition, for such R sound control, 1. Valve mechanism 9 as described above
. It is also possible to create a relative head by raising or lowering only one of the pipes Th8 and Izun.

As detailed above, this invention is based on the JIIoIIC Kisinsute 1! Water is supplied to the electrolytic cell through the electrolytic cell, and the alkaline ionized water and acidic water produced from the top of the electrolytic cell are taken out through the electrically insulating means of %m1, respectively. The route for supplying water from the tank to the electrolytic tank is divided into two routes, each of which communicates with the cathode chamber and the anode chamber of the electrolytic tank, and a 9P machine Jk that is interlocked with each other is installed in the route, 15 on one route
When the flow rate is increased, the other flow rate is completely reduced, so the required amount of produced water can be obtained easily, and unnecessary waste is avoided. The advantages and effects of being able to eliminate waste and demonstrate great economic efficiency in continuous water generation VC are being underestimated□

[Brief explanation of drawings]

Figure 1 is a schematic system diagram showing one embodiment of this invention;
Figures 3 and 4 are vertical views of the electrolytic cell, Figures 3 and 4 are vertical views of the electrical insulation means, Figure 5 is a perspective view of the water content Mkm, and Figure 6 is the valve mechanism. It is a perspective view. 1...,... integral, 2...... electrolytic cell, 3.4
・・・・・・Electrical insulation means, 5, Tap... Route, 9.
... Valve mechanism, 919a' ... 0.9b
・Seal/valve plate.

Claims (1)

[Claims] Water is supplied to the electrolytic cell through the first electrically insulating means, and alkaline ionized water and acidic water generated from the top of the electrolytic cell are taken out through the t''LLth electrically insulating stage, respectively. In a pressurized trap, the path for supplying water from the electrically insulating means of 1!1 to the electrolytic cell communicates with the anode chamber and the anode chamber at the inlet of the electrolytic cell, and
Control is performed on the two paths that communicate with the top of each chamber and bring generated water to the second electrically insulating means so that when the flow rate of one path is increased, the flow rate of the other path is decreased. A water flow control mechanism in a continuous water electrolysis device characterized by having a flow control technique.