TW310347B - - Google Patents

Description

310347 Α7 Β7 5. Description of the invention (1) The present invention relates to an electrolyzed water generation which can be used for electrolysis of water to produce useful acidic water for K ion efficiency as a cleaning and killing, and the ageable water can be used as beverage water The method and its device, especially related to a kind of acidic water that can control the electrolysis to generate the desired degree of dissociation efficiency or even residual water. In the field of food and food, it is generally known that low pH value mildew can be used Water is used as water for cleaning or disinfection and sugar killing, but it is not easy to make strong acid water stable and produced by Dong. The conventional device for generating mildew water is generally divided into a cathode chamber and an anode chamber by an ion-permeable membrane, and a dangerous electrode and an anode pole are filled in it, and the raw water is placed in the chamber In order to make the rollers flow between the two electrodes and cause electrolysis through the diaphragm, the PH value of the indoor water is increased to form test water, and the f »H value in the anode room becomes lower to become acidic water. However, in such a conventional electrolyzed water device, it is difficult to produce acidic water or even superficial water with desired electrolysis degree. Printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs «. ----------- ^ ^ 1 (Please read the precautions on the back before filling out this page) Typically used as a pure tap water for drinks Is slightly neutral with a conductivity of about 100 to 200 μ / cm (EC) and a pH of about 6.5 to 8. In order to generate a large amount of dewatering water, the energizing current can be increased. However, the usual drinking water, as before, has a very low conductivity, so it is difficult to flow between the electrodes. The large electric roller * must be lifted off to apply the pressure , Resulting in the disadvantage of increased power consumption. In addition, in the conventionally widely-used water dehydration generating device, the acidic water obtained from the anode chamber subjected to the water dehydration treatment in the electrolytic cell has a weakly acidic pH value of at most about 40 to 5.0, which is also difficult To fully obtain the desired cleaning, the paper size is applicable to the Chinese National Standard (CNS) A4 specification (2 丨 0X297mm) Λ · — 4 一 Α7 87 ^ 10347 5. Description of the invention (2) The shortcomings of the sterilization effect t This The purpose of the invention is to provide a method and a device for generating II hydrolyzed water that can generate stable acidic water and superficial water by electrolysis with a low amount of power and high efficiency. Another object of the present invention is to provide an efficient car that can easily generate killing effect below 03, which is best? ! 〇.5 ~ 2.6 strong acidic water electrolysis water generation method and device. Still another object of the present invention is to provide an electrolyzed water generation method and apparatus that can generate acidic water or sickle water of desired electrolysis degree and electrolysis degree at a high efficiency depending on the flow rate and even the degree of electrolysis of the decomposed water. Another object of the present invention is to provide an electrolysis water generation method and device that can generate acidic water or alkaline water with a desired pH value according to the pH value of the generated hydrolyzed water or even the gasification potential. In order to achieve the above purpose, the composition of the electrolyzed water generation method of the present invention is as follows: a galvanic electrode and a cathode electrode are provided in the chamber and the anode chamber separated by the M diaphragm to form a small solution tank, and "Supplying Raw Water" will be applied between the aforementioned anode and cathode electrodes, and the electrolyte will be added to the front of the raw water to add electrolyte fluid flow, while measuring the degree of mycolysis of the raw water and even the electrolyzed water and controlling the electrolysis according to the predetermined electrolysis degree. Thus, acidic water and alkaline water with adjusted electrolysis degree can be obtained. In addition, the electrolysis generating device of the present invention is constituted as follows: the anode electrode and the cathode electrode chamber partitioned by the M diaphragm are provided with kuma electrode and cathode electrode to form an electrolytic cell; and the anode chamber and the cathode chamber are respectively connected Discharge water discharge path; raw water can be supplied to the original water supply path of the aforementioned electrolyzer; set in this paper standard is applicable to China National Standards (CNS) Α4 specifications (210X297 mm) (please read note f on the back before filling in this Page) Order the S10347 A7 B7 by Beigong Consumer Cooperation of the Central Bureau of Standards of the Ministry of Economy V. Description of the invention (3) At least one flow regulating device of the aforementioned raw water supply channel; inject electrolyte aqueous solution into the aforementioned raw water supply channel Tuck injection device; a device for detecting the degree of electrolysis of at least one of the raw water supply path and the electrolysis water discharge path of the engraving tank; it can accept the detection number from the aforementioned sensor and at least one test A control unit that controls the at least one of the clarification function, the raw water supply path, and the electrolysis discharge amount based on the known signal. The aforementioned degree of defrost of the measured object of the electrolyzed water refers to at least one of pH value, conductivity, oxidative potential and ion susceptibility. Raw water such as drinking water is supplied to the electrolytic cell, and energized between the cathode and anode electrodes can cause the original water to be electrolyzed. K turns over to generate aging water in the shade chamber in the electrolysis chamber and acid water in the kuma pole chamber *. Can be suitably used. For the injection of the electrolyte aqueous solution added to the raw water, a gas strip electrolyte aqueous solution such as saline can be used. By adding this aqueous solution of solution, the conductivity of the plateau water can be increased, and the low II pressure can be used to form the circulation of the big mold. M produces a strong «solution effect, and an effective 11 solution is achieved. Measure the conductivity of the raw water and even the decomposed water and even the oxidation potential, and control the mildew hydrolysis according to the detected signal, which can effectively control the acidic water from the carved pole chamber and the alkaline water from the shade chamber At least one of the pH value of the enzymatic hydrolysis water and even the amount of production. In addition, the electrolysis state in the electrolysis right or the electrolysis situation of the electrolyzed discharge water can be measured to control the flow ratio of the basal water and the acidic water discharged from the electrolyzer to control the amount of frost decompression load in the anode chamber and the cathode chamber. Solution intensity. By moving the diaphragm of the tank, the capacity of the anode chamber and the cathode chamber is roughened, and the flow ratio of sexual water to acidic water can be changed. And • Even if it is set by the paper standard from the anode, it is suitable for China National Crushing Rate (CNS) Α4 specification (210Χ297 mm) ---.-- Ί ---- J4 ------- order (please read first Note on the back and then fill out this page) Printed by the Ministry of Economic Affairs, Central Bureau of Standards, Employee Consumer Cooperative Printed by the Ministry of Economic Affairs, Central Bureau of Standards-Industry and Consumer Cooperatives i. Invention Description (4) The flow of the electrolyzed water from the chamber and cathode chamber is most regulated Device • It can also change the rolling ratio of salty water to acidic water. Other objects and features of the present invention can be described in detail in accordance with the attached drawings. The first circle is a schematic diagram of the device used to explain the principle of the generation of water solution according to the method of the present invention. The second plaque represents the outline of the first embodiment of the «water generation device of the present invention. No. 3_ shows the outline of the second embodiment of the electrolyzed water generating device 1. The fourth circle shows the outline of the third embodiment of the electrolytic water generator. The fifth circle shows the outline of the fourth embodiment that can show the variation example of the electrolytic cell in No. 4_. Section 6_ shows the outline of Figure 5. Picture 7 shows the flow circle of the flow control principle of the device in Figure 6. The 8th series is a schematic diagram of a sixth embodiment of another modification of the electrolytic cell. Preferred embodiment: The present invention relates to an electrolysis which can effectively control electrolysis according to the electrolysis degree of the generated hydrolyzed water, pH value, conductivity (EC value), oxidation primitive potential (ORP value) and mule concentration, etc. The electrolysis water generation method and device for efficiently generating acidic water and sexual water with a desired pH value, and referring to the conceptual drawing of FIG. 1, the principle of generating and controlling water of the present invention will be described below. As shown in FIG. 1, the electrolyzed water generation device of the present invention is composed of the following: the Chinese chamber standard (OJS & gt) is used in the dimensions of the solar chamber la and the negative paper separated by the ion-permeable membrane 3 ; A4 specifications (210'〆297 g (please read the precautions on the back before filling in this page) " * 3i〇347 a? B7 Printed by the Beigong Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy V. Invention Instructions (5) The electrode chamber 1b is provided with a closed structure electrolytic cell 1 having an anode electrode 5a and a cathode mildew electrode 5b; raw water W0 can be supplied to the raw water supply path 7 of the chamber 1a and the cathode chamber 1b; and can be stored in the water tank 9a The electrolyte aqueous solution SS is injected into the injection device 9 of the raw water supply path 7; the measuring device 11 for measuring the EC value and / or (and / or) the amount of raw water provided in the raw water supply path with M is provided on at least one roller of the raw water supply path 7. Dong regulating device 13; the mold solution water discharge paths 15a, 15b respectively discharged from the anode chamber la and the cathode chamber lb of the decomposed water Wl, W2; the flow rate of dehydrated water even at the electrolytic discharge path 15a provided on at least one side is measured by M Sensing device 17 for the degree of resolution; spit out at least one or two of the «solution water discharge path Amount adjustment device 19; a storage water tank 21 that retains the enzymatic water W1 flowing out from the electrolyzed water discharge path 15a. Use relatively pure drinking water such as tap water as raw water W0, which can be supplied to the anode chamber 1a and the cathode via the raw water supply path 7 respectively Room 1 b. Electrolyte water dissolving SS can use gas strip electrolyte water Panye such as NaCl, KC1, HCI, HC10, HC103, fiC10a, NaCIO, etc. The electrolyte aqueous solution SS can be added to the raw water to increase the conductivity of the raw water, It can also circulate a large current with a low voltage and a strong electrolysis effect. The electrolysis current can be supplied from the power supply 23 to the anode electrode 5a and the cathode electrode 5b of the Kuma electrode chamber U and the cathode honey lb respectively installed in the electrolytic cell The installation positions of the quantity adjustment devices 13 and 19 provided in the raw water supply path 7 and the electrolyzed water discharge paths 15a and 15b can be set at appropriate positions on the path respectively. In the figure, 25 is the control unit * which is set in the raw water Check the measuring device 11 on the supply path 7 and the sensing and tearing device 17 installed in the "Water Discharge Outlet 15a" (please read the note $ item on the back and fill in this page) 1

A. The size of the paper is in accordance with the Chinese National Standard (CNS) A4 specification (210X297 mm). ΒΙ〇347 λ, D 1 ~~ I 'Ministry of Economy, Central Standards Bureau, Beige Consumer Cooperation Du Printing

5. Description of the invention (6) The detection signals of the raw water volume and conductivity, the flow rate and conductivity of the electrolyzed water, the oxidation potential, etc. are carried out, and the aforementioned flow regulating device 13 or even is controlled according to at least one detection signal 19. The spoiled water splashing liquid injection device 9 〇 The objects monitored by the control unit 25 (that is, the raw water roll and conductivity, the flow rate and conductivity of the electrolyzed water, the gasification potential), and the objects of control (ie The flow regulating devices 13, 19 and the electrolyte water dissolving and injecting device 9> have different states, and depending on the desired degree of electrolysis of electrolyzed water, there are some differences in the composition of the electrolyzed water generating device. Some specific configurations of the electrolyzed water generating device of the present invention. The first embodiment shown in Fig. 2 is to control the anode while detecting the electrolysis state in m solution or electrolysis degree of electrolyzed water discharged from the electrolysis building. The amount of electrolytic frost in the chamber and the cathode chamber M controls the electrolytic strength. The control of the electrolytic charge current can be controlled by the ratio of the amount of surface water and acidic water discharged from the electrolytic cell. By this, a predetermined amount of M is obtained It produces acidic water with the expected pH. In the anode chamber la and the cathode chamber lb separated by the diaphragm 3, there is a decoupling tank 1 for the electrolysis 5a and the cathode electrode 5b, and it is provided in a place where it can be electrolyzed. The flow rate adjusting device of the raw water supply path 107 of the tank 1 includes a pressure reducing valve 113a, a water stop valve 113b, and a flow control valve 113c. In addition, a pressure gauge 108a and a roll gauge 108b are provided at appropriate positions of the raw water supply path 107. These devices can be adjusted to control the flow of raw water. The electrolyte aqueous solution injection device 109 here is composed of the following: It is installed under the flow meter 108b to flow copper; can store the decomposed aqueous solution SS {please read the notes on the back first Please fill in this page for more details) 1 4 The standard paper size is based on the Chinese National Standard (CNS) A4 regulations (210X297mm) ^ 10347 A7 B7 5. The invention description (7) of the water tank 109a; can be sent for solution The quantitative pump 109b of the aqueous solution SS; the injector 109c that can inject the electrolyte aqueous solution SS into the raw water supply path 107; the mixing device 109d that can mix the injected delyzed aqueous solution SS with the raw water W0. In order to adjust the conductivity, the electrolyte aqueous solution SS used may be a nitrogen strip electrolyte aqueous solution. Here, edible mussel is used as an example of mycoplasma, and saline solution with a concentration of about 10% M is suitable. Such salt water is stored in the water tank 109a. The electrolyte aqueous solution SS can be quantitatively supplied to the raw water W> flowing through the raw water supply path 107 by the pump 109b and stirred and mixed by the mixing device 109d, and the fully mixed raw water can be supplied to the electrolytic cell 1. An electric conductivity detector (EC detector) 111 for measuring the conductivity of the raw water is provided on the downstream side of the injection device 109 as a sensing device for the raw water supply side of musk. The EC sensor can output the conductivity signal (EC signal) 1 c 1 detected from the raw water. The electric roller is applied to the anode electrode 5a and the cathode electrode 5b from the power source 23, and the raw water W0 flowing into the electrolytic cell 1 will be decomposed. The electrolytic waters W1 and W2 obtained as a result of mildew hydrolysis can be discharged from the discharge channels 115a and 115b. The acid water W1 from the anode chamber la rolled out by the electrolytic water spit 115a printed by the Beigong Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs can be sent to the storage tank 21 through the three-way 119a, but it can be punished according to the pain The three-way valve 119a provided in the middle of the discharge path 115a discharges the acid water W1 through the discharge path 115c only to a proper amount to the discharge path 115b. The acidic water W1 stored in the storage tank 21 can be used as water for washing and sterilization. A discharge volume regulating valve 119b is provided on the discharge path 115b, and the age water W2 generated in the cathode chamber lb can be blown out through the valve 1: 19b. This sickle water can be supplied as a drink. In addition, the sensing device 117 provided on the discharge path 115a is equipped with: Measurable 10 (please read the precautions on the back and then fill out this page) This paper standard is applicable to China National Standard (CNS> A4 specification (210X297 public)) Printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A? B7 _ V. Description of the invention (8) The conductivity of the acidic water W1 generated in the anode chamber la (EC :) Μ _ the conductivity sense of EC times I c2 Sensor < EC sensor), and, can measure the redox potential M of acidic water W1 _Oxidation original potential multiple (ORP 傕 号)> IP redox potential sensor (ORP sensor) 117b. The EC multiple Icl from the EC sensor 111 provided in the original waterway 107, and the EC signal U2 from the EC sensor 117a provided in the discharge path 115a are sent to the comparator 25a of the control unit 25 for comparison Electrolysis degree, 1 degree difference signal Id passes through the amplifier 25b and is sent to the CPU 25c. In addition, the CPU 25c can receive the 0RP 傕 号 IP from the 0RP sensor 117b. Respectively, the reference values of the electrical conductivity of the eel and the gasification potential, according to the aforementioned difference number Id, or, 0ΡΒ No. 丨 p and other pull-out signals, and various control signals are sent from the CPU 25c to the control object respectively. According to the aforementioned difference times Id and (or / or) acidic water W1 gasification reduction position, adjust the raw water The maximum supply or the injection amount of the electrolyte aqueous solution * or the control of the discharge roll amount set at the discharge path 115b is adjusted to 119b. That is, compared with the raw water W0, if the result is that the electrolysis degree of the acidic water W1 obtained is not Sufficient (the difference between the electrolysis degree of the raw water and the acidic water is very small), the pump 109b can be controlled to increase the injection of the pyrolysate aqueous solution SS, and at the same time, the flow regulating valve 113c can be narrowed. If the electrolysis degree is high, the injection amount of the aqueous solution SS of mildew can be suppressed, and the flow can be adjusted to increase the flow rate of the raw water by 113cM. Therefore, the acid water W1 with a predetermined degree of decomposition can be generated. The size of the original potential is used to control the flow rate of the refining device or the injection of the aqueous solution of mildew, which can easily generate «water solution with the expected PH value. Moreover, the paper standard of M« solution solution is suitable for the Chinese national rubbing rate (CN S) Α4 specifications (210X297 mm) 11 (please read the notes on the back before filling in this page) Order 3 # 3 # A7 B7 i, invention description (9) ss Injecting a strong m solution can increase the oxidative entanglement of water and obtain strong acidic electrolyzed water with a strong sterilization effect. The Ding Dong pump 109b is driven to inject the enzymolysis aqueous solution SS into the raw water supply path 107, but, The neck of the raw water supply path 107 is provided with a venturi tube, and the supply tube of the defrosted aqueous solution from the water tank 109a is connected to this neck, and the raw water rolling on the raw water supply path 107 accelerates the rolling speed at the neck. The supply pipe applies a negative pressure, and M dissolves the dissolved water in the raw water supply channel 107 to supply it. At this time, a sluice valve is provided on the electrolyte aqueous solution supply pipe from the water tank 109 to the raw water supply path 107, and the control and adjustment threshold can be adjusted according to the pH value of the decomposed water or vaporization. In either case, by adjusting the electrolyte aqueous solution supplied to the raw water, the raw water with a predetermined conductivity can be led to the tank. The raw water whose conductivity has been adjusted is introduced into the electrolytic cell 1 * Immunity is applied between the electrodes 5a and 5b to produce the ion permeability of electrolysis * «The cations in this raw water will be concentrated in the cathode chamber lb, _ion through the diaphragm 3 It will be concentrated in the anode chamber la, and low pH acidic water containing anions such as Da Dong Cr and the like is obtained in the anode chamber U. The adjustment control of the pH value of the acidic water W1 caused by the discharge flow regulating valve 119b is 1 conductivity can be implemented as follows. The acidic water W1 generated in the anode chamber is subjected to electrolysis with a large average flow rate, which increases the degree of mildew and forms strong acidic water with a low pH value. In addition, salt water W2 is generated in the shade chamber lb and is discharged through the discharge path 115b. The discharge flow halo adjustment valve 119b provided in the discharge passage 115b controls the flow rate. The pH value of the acid water W1 discharged from the discharge passage 115a of the sun chamber la can be controlled. This paper uses the Chinese National Standard (CNS) A4 specification (210X297mm) ^ Wood Order- * (#Read the precautions on the back and then fill out this page) 12 A7 B7 Ministry of Economic Affairs Central Bureau of Industry and Customs Consumer Cooperation Du Yinzhi V. Description of Invention (Μ) That is, the flow rate of the acidic water generated by controlling the flow of sexual water is also related to change. Therefore, the amount of frost per unit flow can also be controlled to complete the control of electrical conductivity and oxidation. Therefore, in the calculation processing circuit (CPU) 25c of the control unit 25, the raw water and the conductivity of the decomposed water and even the gasification potential are further preset. The control base data of the setting, changing, and applying current values are discharged, and the M control corresponds to the adjustment system according to the control signal (comparing the detection value from each sensor). The state of the detection signal from each sensor and the control state of each adjustment device to be controlled can be easily monitored and confirmed by a person indicated by the display device 25d of the control unit 25. Secondly * explain the experimental results that can show the special effects of the present invention. Relative to 100 liters of raw water, the ratio of 1 liter of 10% saline solution was mixed, and the raw water of this mixed salt solution was supplied to the decoction for engraving and digestion. When a current of 16V and 30A was applied to the engraving tank M, and the discharge flow of sickle water was controlled, pH 2.6 acidic water in an amount of about 3.6 liters per minute was obtained. In addition, when controlling the decompression voltage to generate acidic water, it takes about 1 kw to generate 1 liter of acidic water. Also, after changing the rolling volume to electrolyze the raw water containing NaH 1000 ppb, can it be obtained by Η 16 丫 父 3 (^ (4801 |))? 112.6 of junior water 3.6 liters "With the method of not changing the flow rate, without adding NaCl and controlling the electric calendar to conduct electrolysis, you can consume electricity to get 1 liter of acidic water. In this way, according to the present invention, it is possible to easily generate low-pH Dadongqiang acidic water required for low-level coal mines. In addition, the pH value of the acidic water to be generated should be 2.6 (please read the precautions on the back before filling this page) ---- 1 Pack ---

* tT ϋ—fn · — —Bn UK— 4 This paper scale adopts China ’s national standard rate (CNS > A4 specification (2 丨 OX297mm) A7 B7 Printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs V. Invention description (11) When it is lifted to about pH 3, it can further reduce the mixing amount of edible water, while controlling the drainage of alkaline water, while the same electrical energy increases the amount of acidic water produced by 0. Although it has been explained that M acidic water is the main The generation control of chrysanthemum, however, the discharge flow suspension control valve 119b can also be set to the discharge path 115a of acidic water, and the pH of the acidic water W1 is controlled by M to control the pH of the salty water W2. At this time, the M It is easy to broadcast a large amount of aging water. In addition, the control of the ratio of mineral water to acidic water can also be set by a fixed distribution valve with a certain total II distribution flow rate on both lake roads. As mentioned above, the present invention can easily promote the enzymatic hydrolysis of water by the addition of the mildew hydrolyzate solution, while effectively suppressing the consumption of frost power while efficiently producing a large amount of electrolytic water. In addition, the mildew conductivity, PH value, It can easily generate stable and strong acidic water with PH3 Μ under the control of the amount ratio. Furthermore, it can be mixed with gas to generate a kind of cleaning and high killing gas containing a lot of chlorine, hypochlorous acid or highly killing gas in the water. It is an acidic water. It is outlined in the electrolysis water generating device of the second embodiment of the third embodiment, which is provided with a three-way valve 213 and a fixed ft distribution outlet 217 in the raw water supply path 107. The other elements shown in the description are omitted because of their equivalent construction. The fixed valve 2Π is composed of two separate supply pipes 207a and 207b which are respectively connected to the anode chamber la and the negative chamber lb. The flow can be distributed in a certain total position. The M distribution valve 217 controls the director fed to the electrolytic cell 1, and is respectively fed into the hibiscus chamber la of the mildew cell and the raw water WO of the cathode chamber lb via the supply pipes 207a and 207b. Related, however, if the total amount supplied to the electrolytic cell 1 is based on the paper standard, the Chinese National Standard (CNS) A4 specification (21〇X2W public publication) 14 ------ ^ --- ^ ^- ------- ^ Order (please read the precautions on the back before filling in this page) Printed 3103 by the Ministry of Economic Affairs, Central Standard Staff Employee Consumer Cooperative 47 at ίΡ 5. Description of the invention (12) At a certain time, in other words * the amount of raw water supplied to the anode chamber U is private, and the amount of raw water Qb supplied to the shade chamber lb has the following relationship: K * Qa + (-10 · Qb =-fixed < 1 (from 0 to the maximum value) .. (1) The electrolysis of the raw water measured by the EC sensor 111 and the electrolysis from the conductivity sensor (EC sensor) 117a The electrolysis of water is known to be poor, or the MEC sensor 117a or even the 0RP sensor 117b detects the conductivity of the electrolyzed water W1 and even the original data, which can be controlled by the control unit 25 after calculation. 217, to separately adjust the raw water supply amount of the separation chamber la and the dangerous chamber lb of the decoupling tank. The adjustment is the same as the aforementioned first embodiment. For example, if the acidity of the acidic water W1 from the anode chamber la is too low, it is possible to distribute Lang 217 to reduce the amount of raw water supplied to the anode chamber la. As a result, the electrolysis of the electrode compartment la becomes thicker, and the acidity of the electrolyzed water W1 discharged from the anode compartment la increases. If the acidity of the acidic water W1 is too high, the opposite treatment is sufficient. In the illustrated embodiment, although the two valves 217a and 217b form a distribution valve 217, of course, a three-way valve with a single rotor that can be quantitatively distributed, or, well-known Distributing device of the sowing chrysanthemum, etc. 0 The third * embodiment shown in the fourth circle has a volume of the limiting chamber 30la and the cathode chamber 301b which can make the small solution tank 301, that is, the spit out of the water The variable volume of the hydrolyzation tank volume variable device to control the degree of decomposition of the electrolytic water produced by the electrolytic cell. In this embodiment, the support film 303 is tiltably provided on the side with a support stick 303a on the bottom surface of the electrolytic cell 301. The upper paddle of the tilting diaphragm 303a is endowed with the paper size applicable to the Chinese National Standard (CNS) A4 specification (210X297.mm) ---------- 4 :. 水 丨 — (please read the back first (Notes to fill out this page) Order 15 The Ministry of Economic Affairs, Central Bureau of Industry and Commerce, Beigong Consumer Co., Ltd. Du Printed A7 B7 V. Description of Invention (13) It can be used to position the barrier in the center under normal conditions by means of a spring. The volume control device 310 is composed of a swinging member 312 that is rotatably held by the M fulcrum 312a, and an electromagnetic driving device 314 that can swingably drive the swinging member 312. The lower end of the rocking member 312 is connected to the aforementioned tilting diaphragm 303, and the upper end thereof is provided with a magnetic roller 312b. The plural magnets MGK of the magnetic roller 312b at the time when the rocking member 312 rotates and shakes are set to draw an arc shape. If any of the electromagnets MG of the electromagnetic drive device 314 is excited to attract the roller 312b at the upper end of the rocking member 312, the yoke 312b rotates and tilts around the support 312a: the diaphragm 303. As a result, the volumes of the kuma electrode chamber 301a and the cathode chamber 303b of the electrolytic cell 301 are correlated with each other and change. Therefore, if the raw water WO Μ acidity sensor 311 detects the acidity, at the same time, the acidic water W1 discharged from the «solution tank 301 is a sensing device composed of the acidity sensor 317a and even the ORP sensor 3 17b After detecting the acidity in 317, the control unit 325 can perform the calculation process in the same way as the previous embodiment to control the volume control device 310. That is, when the acidity of the generated acidic water W1 is lower than the expected value, the left side electromagnet MG of the electromagnetic actuation device 314 is magnetized in 阄 4 to lure the yoke 312 to the left, and the fulcrum 312a Rotating the shaking member 312 as the center, thereby moving the upper end of the diaphragm 303 to the right, as a result, not only can the volume of the anode chamber 30la be reduced, but also the acidity of the etheric water W1 generated in the hibiscus chamber 301a can be increased degree. When the acidity of the acidic water W1 is too high, it is only necessary to increase the volume of the compartment 301a by the opposite method. By changing the contents of the anode chamber 301a and the yin chamber 301b to change the pH values of the decomposed water W1 and W2, and at the same time as the above embodiment, the paper size of the electric paper is suitable for China National Standard (CNS ) A4 specification (210X29? Mm) (please read the notes on the back before filling in this page) Binding-Order 16 A7 B7 i, invention description (14) printed by decontamination solution The injection device 309, a three-way valve 313 for flow * adjustment, can make the raw water of the Weiwei, which has been adjusted to flow into the electrolytic cell 301, and can control the electrolysis. Fifth Frontier is «Variation of the variable tank-relieving device (the fourth example)). Its structure is that the movable side wall 421 is provided in the seed chamber 401a of the electrolytic cell 1 to drive the movable side wall forward and backward Μ changes the volume of the carved pole chamber 40 U. The movable side wall 421 is a gasket 423 provided around it to maintain watertightness, and the movable side wall 421K of the focus chamber 401a is moved forward and backward according to the acidity change of the raw water and the acidic water W1 detected by each sensor. The volume of the amp chamber 401 a is changed. Here, the pole electrode 4053 is fixed to the movable side wall 421 and the cathode electrode 405b is fixed to the outer wall surface of the cathode chamber 40lb. In this embodiment, the third embodiment shown in section 4_ also changes the capacity of the anode chamber 40la. It can generate acidic water W1 or even aging water W2 having a desired pH value. The sixth type is an embodiment having a control bar that automatically adjusts the generated acidic water and sickle water to the desired degree of resolution by electrolysis. In this embodiment, the raw water W0 is a system that meets the filter 507a, the reduction valve 507b, the pressure gauge 507c, the flow control valve 507d, the tumbler 5076, and the device 507f with the solution of decomposing aqueous solution, etc. The raw water supply path 507 * is supplied to the engraving tank 1. The storage solution 510 sends the electrolytic aqueous solution SS to the injection device 507f via a stationary pump 509g. The electrolytic 1 series M diaphragm 5CB is divided into an anode chamber 501a and a cathode chamber 50lb, and a broadcast electrode 505a is provided in the anode chamber 501a, and, in the _ pole chamber, the paper size is common to the Chinese national rate (CNS) A4 Specifications (210X297mm) ------------ γ Packing ------ Ordered -------- * (Please read the precautions on the back before filling in this page) Central Ministry of Economic Affairs Bureau of Standards Consumer Labor Cooperative Printed Bag A? B 'V. Description of the invention (15) A cathode electrode 505b is provided in 50lb. The acidic water W1 generated in the separator chamber 50la is discharged from the discharge path 515a, and the sickle water W2 generated in the cathode chamber 501b is discharged from the discharge path 515b. The acid discharge channel 515a is provided with a 0PR sensor 517 and a roll gauge 518, and the acid water is sent to the calculation processing circuit (CPU) 525. The acid water discharge channel 515a and brewing water discharge channel 515b are provided with three-way valves 519a and 519b respectively. The ST can be used as a calculus processing reverse circuit 525 to control the opening and closing of the discharge flow regulating valve. It is connected to the confluence pipe 520c. In the figure, 512 is a water level gauge for measuring the storage amount of the aqueous solution in the tank 510 of the degraded aqueous solution, and 514 is a display device that displays each measured value and control status. 523 is a source for supplying electrolytic electric rollers to one frost solution 505a, 5051 >. In the above-mentioned eaves formation, according to the oxidation level of the acid water W1 generated by the ORP sensor 517, the three-way thresholds 519a and 519b can be opened and closed by the arithmetic processing circuit 525. If the oxidation water source of acidic water is too large, if the three-way valve 519a is opened and the three-way valve 519b is narrowed at the same time, the passage of the dehydration water in the anode chamber 501a will be faster to inhibit the oxidation of the source. Thereby, the oxidation of acid water W1 can be reduced, and the acidity of acid water W1 can be reduced. The proper control of the acidity of mildew solution water can be measured by the flow meter 518 to adjust the flow rate of the water solution to adjust the amount of control 507d, and, according to the gasification of the original potential and the three-way control 519a, 519b to entangle Implementation. That is, as shown in the flow chart shown in the seventh plaque, the lower limit of the ^ Qv ratio of the electrolyzed water W1 measured by the M-liquid meter 518. This paper scale is applicable to the Chinese National Standard (CNS} A4 specification (2! 〇X29 * 7 Gonghua ) 1 2 (Please read the precautions on the back before filling in this page)-* A7 —B7 ____ 'Invention description (16) Value til hours (QKQ \ 〇 is M processing I shrink roll * control valve 507d, than the upper limit When Q2 is large, Uli ^ tiv> is H treatment I to open the valve 507d. At the following stage, the oxidation potential Qv is lower than the lower limit value οι hour (ου hour (οι > 〇v) is to open the valve 507d by treatment I, if 01 >; Ον, is the κ treatment IV to reduce the Langmen 507d, M makes the acidity scorching. So, if the enzymatic water is optimized by the degree of hydration, then the electrolyzed water can be used through the three-way valve 519a. The measurement of the original position 517 and the opening of the three-way valve 519a to allow the acidic water to flow out can set the electrolysis degree within the predetermined range, and only the expected water can be stabilized and taken out. Also, the above-mentioned electrolytic water is generated The control method also includes: according to a kind of raw water or spitting water which is controlled by the measurement of the flow meter 518, The setting is rolling, and the raw water is injected into the electrolyte water dissolution, and, according to the detection number of the 0RP sensor 517, it is possible to cancel the fine adjustment of the previous rolling amount control, so that the above-mentioned electrolysis situation of spitting out the decomposed water becomes constant. Ministry of Central Prototyping Bureau Beigong Consumer Cooperative Printing Co., Ltd. That is, the rolling volume control of raw water or spit water is controlled according to the measured value of the rolling volume meter, and the predetermined rolling volume is controlled in advance. Inject, and apply a predetermined set voltage to control the electrolysis electrical. In addition, by using the detector to detect the electrolysis state of the electrolysis water in the generation of electrolysis water or the electrolysis situation of the electrolysis spouted water, the number can be detected accordingly. To carry out precise and precise rolling volume control to maintain the conductivity, pH value, gasification level, etc. of the electrolysis degree at a predetermined predetermined tuna. Furthermore, by controlling the raw water roll, the electrolysis water can be controlled at will. The adjustment of conductivity and pH value, therefore, strong acidic water at pH 3 Μ can also be generated stably and easily and continuously. In addition, the use of acidic water or sickle water generated by mildew can be set 19 --- „--- ^- --One pack-- (Please read the precautions on the back before filling in this page) This paper scale is applicable to China National Standard Rate (CNS) Α4 specification (210Χ297mm) Printed by the Employee Consumer Cooperative of the Central Bureau of Economics of the Ministry of Economic Affairs A. 7 B7 V. Description of the invention (17) The set flow setter 527 of the set flow set is set in the CPU processing circuit (CPU) to switch the flow rate of the raw water and mildewed water set in the flow setter Control, and supply control of electrolyte water dissolution can also be adjusted according to different controls. In this way, according to acid water or salty The supply of the aqueous solution is switched, and the setting of the engraving source «Pressing and cutting, can often keep the defrosting situation of the electrolytic water constant, and it is easy to generate any desired lake * solution without changing the electrolysis shape. The eighth lap is the engraved groove 1 in the previous embodiment and the replaceable cylindrical tubular engraved groove 601, and the diaphragm 603 separates the concentric outer cathode chamber 601b and the inner kumbo chamber 601a. Then, the cathode electrode 605b and the anode mildew electrode 605a are installed in each room. The raw water supply channel 607 which can supply the raw water controlled by the roller is divided into technical tubes 607a and 607b, and the raw water is distributed and supplied to the anode chamber 601a and Cathode chamber 601b. In this embodiment, a supply tank 609 for injecting a solution of aqueous solution of magma, such as water and water, into the cathode chamber 601b is connected to the middle of the branching tube 607b. The valve 609a opens and closes, and the injector 609b can be used A predetermined amount of the enzymolysis aqueous solution is injected into the branch pipe 607b. According to this embodiment, by adding a water solution such as saline solution to the shadow chamber 601b of the electrolytic cell 601 from the sub-tube 607b, the reaction of the water dissociation in the cathode dissolution tank can be promoted, while in the anode chamber 60la Μ separation efficiency generates strong acidic water. In addition, since only the raw water is supplied to the _ electrode chamber 601a, the consumption of electricity can be greatly reduced, and the electrolysis efficiency can be improved. The raw water volume control supplied to the engraving tank is based on the paper size set in the calculation process. The Chinese National Standard (CNS) A4 specification (210x 297 mm) is applied. 20 ------- ^ --- M ------ Subscribe ------ f. (Please read the precautions on the back before filling in this page) A7 B7 Fifth, the invention description (18) The reference value of the circuit is carried out, for example, for the Jiji room 601a Reducing rolling, Μ increases the amount of electricity in the average rolling amount of raw water, thereby increasing the amount of electricity can improve the solution strength, and obtain strong acid water with high conductivity and low pH. In this way, the flow rate control can obtain acid water with any degree of resolution. As for the aging water generated in the cathode chamber 601b, the three-way valve 609b can be opened to take out only the required amount of pH-entrained water according to the same control. It can be used for drinking water. In addition, during the generation of sickle water *, a saline water discharge path 515b or a flow meter K may be provided to control the 0RP sensor. As mentioned above, according to the present invention, the solution of water can be easily achieved by «mixing of decomposed substances *, which reduces consumption and is cheap, and even generates suspicion in the mining area. Moreover, through the control of the electrolysis in the electrolytic cell, the supply control of the degraded aqueous solution, and the roll volume control of the raw water, the electrolysis of the generated electrolytic water can be accurately managed and controlled, and the pH and conductivity can be easily controlled (EC value), oxide potential (0RP value) and ion concentration «solution degree is controlled within a predetermined setting range. --- η --- I ---- ^ * clothing-- (please read the note Ϋ on the back before filling in this page) Printed paper ruler of the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs Λ applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 21 310347 A 7 B7 Printed by the Consumer Consumer Cooperative of the Central Prototype Bureau of the Ministry of Economic Affairs V. Invention description (19) [A brief description of the main component symbols] I, 301, 601 ... Electrolyzers la, 301a, 401a, 50] a, 601a ... Yangyang chamber lb, 301b, 401b, 501b, 601b ..., shade chamber 3, 303, 503, 603-ion permeability barrier隳 5a, 405a, 505a, 605a__ 隈 极 轚 棰 5b, 405b, 505b, 605b__ Cathode electrode 7, 107, 307, 507, 607 .... Raw water supply path 9, 109, 309 9a, 109a ---- Sink II, 117, 317, 517--sensing device 13 ... flow rate adjusting device 15a, 15b, 515a, 515b .. .. Rolling M adjusting device 21____ water tank 25, 325 .... Control unit W0 .... Raw water Wl, W2... «Jieshui 23, 523 ---- Xiaoyuan 25a. .. Comparator 25b____Amplifier 25c, 525 ____CPU 25d, 514 ... Display device This paper standard is applicable to the Chinese National Standard (CNS) Α4 Youge (210X297mm) (Please read the precautions on the back before filling this page)

, 1T 22 Ministry of Economic Affairs Central Standards Bureau employee consumption cooperation Du Yinju 310347 at B7 V. Description of the invention (2〇) I08a, 507c: pressure gauge 108b, 507e-flowmeter 109b, 509b-quantitative pump 111. .. EC sensor 113a, 113b, 113c, 507d-flow adjustment threshold 115a, 115b, 115c-discharge path 119a, 313, 519a, 519b-three-way valve 119b ... discharge flow adjustment valve 207a, 207b-supply pipe 217.... Quantitative distribution valves 217a, 217b-linkage valve 310-volume control device 311 ... acidity detector 312 ... shaking eaves 312a- -Fulcrum 312b-Magnetic Lanwan 314 ... Electromagnetic drive device 421-Movable side wall 423-Gasket 507a .. Overblower 512-Water level gauge 520a, 520b____ Discharge pipe 520c. ... Confluence tube 527 ... Rolling setter (please read the precautions on the back before filling in this page) ml nn n HD m · nn ml ^ in · --4 ... water-- iT-- ---- This paper scale is applicable to China National Standards (CNS) A4 specifications (210 to 297 mm) 23 A7 5. Description of the invention (21) 609 ... Electrolytic water supply tank 609a ... Valve 609b. ... injector ------. 1 ^ --- -1 --- (Please read the precautions on the back before filling in this page) Order Printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs This paper is based on China National Standards (CNS) A4 (210X297mm) 24

Claims (1)

Printed bags of the Consumer Labor Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 6. Scope of patent application 1. A device for generating electrolyzed water with a degree of electrolysis using Μ, which includes a decoupling tank (301) with at least one prepared pole ( 5a > anode chamber (30 la >) and at least one cathode chamber (301b) provided with a cathode (5b), the anode chamber and the cathode chamber are separated by at least-ion-permeable barrier (303);-raw water supply path (307), use M to supply raw water to the lyolysis tank * at least one roll adjustment device U13), which is provided on the raw water supply path; the injection device (309), injects the mycolytic aqueous solution (SS) into the rolling raw water supply The raw water of the road; the majority of the discharge channels (15a, 15b), which are connected to the anode and cathode chambers of each distillation column respectively; at least one flow rate device (19), which is installed on at least one of the plurality of discharge channels; sensing device (311, 317), installed on at least one of the raw water supply path and the majority of the spitting path, using M to detect the degree of hygrolysis of at least one of the raw water and the water solution; M and a control unit (325) , Based on at least one round of the sensing device No. K controls at least one of the enzymatic dissolution tank, the supply volume of the raw water and the «dissolution water discharge flow rate; wherein, the diaphragm (303) can move according to the electrolysis degree of the entrained water discharged from the electrolytic cell ΜChange the content of each anode chamber and cathode chamber. The paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 public daughter) --- J_ 丨 ^ --------- order * · (please first Read the precautions on the back and fill in this page) 25 A8 B8 C8 D8 printed by the Employee Consumer Cooperative of the Central Bureau of Economic Development of the Ministry of Economic Affairs 6. The amount of patent application 2. 2. A device for generating electrolytic water with a degree of electrolysis * It includes an electrolytic cell (301>) with at least one Kuma electrode chamber (30 a) equipped with an anode (5a) and at least one cathode chamber (301 b) equipped with a cathode < 5b > The shade chamber is separated by at least one ion-permeable membrane (303); a raw water supply path (307), which supplies raw water to the electrolytic cell with Μ * at least one roll-up ironing device (313), which is provided in the raw water On the supply road; injection device (309), the electrolyte solution (SS) is injected and rolled through the raw water supply Raw water; multiple discharge channels (15a, 15b) connected to the anode and cathode chambers of each americium; at least one roller volume adjustment device U9>, which is provided on at least one value of the multiple discharge channels; sensing device (311 , 317>, installed on at least one of the raw water supply path and the majority of the discharge path, using K to detect the electrolysis degree of at least one of the raw water and the electrolyzed water; and a control unit < 325), according to At least one of the measuring devices _ outputs a signal to control at least one of the mold dissolution tank, the supply of the raw water «M and the discharge flow of the electrolyzed water: wherein the diaphragm (303> regret M is provided in a 蟵 will be a majority The size of this paper is applicable to the Chinese National Standard (CNS) Α4 specification (210X297mm) --- Ί .------ ^ installed-- (please read the precautions on the back before filling this page) Order 26 310347 g D8 #, The scope of patent application «magnet (MG > one of the electromagnetically attracted magnetic ray drying (312b) rocking member (312) movably supported in the rolling cell (30U, and according to the spit out from the cell« The electrolysis degree of water is dissolved to move, Μ changes each Too accommodating the electrode and cathode compartments. 3. A device for generating enzymatic dehydration with an electrolyzer, comprising an electrolyzer (1), at least one Kuma electrode chamber (401a) with at least one pole (405a) and at least one with cathode (405b) the shade chamber < 401b), the anode chamber and the shade chamber are separated by at least one impenetrable membrane (3 >; a raw water supply path (7), the raw water is supplied to the electrolysis with Μ Tank; at least one flow regulating device (13), which is provided on the raw water supply path; an injection device (9>, which injects an electrolyte aqueous solution (SS) into the raw water rolling through the raw water supply path; most of the discharge paths (15a, 15b), Separately connect each of the exposure and cathode chambers of the Quanzhou; printed by the Male Industry Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs i In ml m · ml nfl »0 ^ ^^^ 1 mV —man in«, JJ ', " 1 No (please read note i on the back and then fill in this page) At least one flow regulating device (19) is installed on at least one of the multiple spit discharge paths; the sensing device (11, 17) is installed on the raw water On at least one of the supply path and the majority of the discharge path, use Μ to detect at least one of the raw water and the «solution water The degree of solution; M and a control unit (25), according to at least one _ output signal of the measuring device to control the electrolytic cell, the supply volume of the dirty water and the mildew solution water (CNS) Α4 specification (210X297 mm) Printed by the Employees ’Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs-A8 B8 eg 1) 8 6. At least one of the spit flow rates applying for patents; One is equipped with a movable side wall (421), which moves the wall to change the volume of the chamber, and then control the electrolysis degree of the electrolyzed water discharged from the electrolytic cell. This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X 297 Mm) --- Ί --.---- j 士 衣 ------ tT ------.--- »1 (please read the precautions on the back before filling this page) 28