JP2938815B2 - Method for displaying pH value of electro-generated water and pH display device for electro-generated water - Google Patents
Method for displaying pH value of electro-generated water and pH display device for electro-generated waterInfo
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- JP2938815B2 JP2938815B2 JP25557796A JP25557796A JP2938815B2 JP 2938815 B2 JP2938815 B2 JP 2938815B2 JP 25557796 A JP25557796 A JP 25557796A JP 25557796 A JP25557796 A JP 25557796A JP 2938815 B2 JP2938815 B2 JP 2938815B2
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Description
【0001】[0001]
【発明の属する技術分野】本発明は、水道水、井戸水、
海水などの原水を隔膜を介して電気分解し、陽極側から
酸性水を、陰極側からアルカリ性水を製造する方法及び
その装置にかかり、陽極側から製造される酸性水又はア
ルカリ性水のpHを的確に、リアルタイムに表示する方
法及びその装置に関するものである。The present invention relates to tap water, well water,
Raw water such as seawater is electrolyzed through a diaphragm, and a method and apparatus for producing acidic water from the anode side and alkaline water from the cathode side, and accurately determine the pH of the acidic water or alkaline water produced from the anode side. And a method for real-time display.
【0002】[0002]
【従来の技術】本願発明者らは、原水を電気分解し、陽
極側から酸性水を、陰極側からアルカリ性水を製造する
方法及びその装置に関し、既に、特願昭63−3790
号(特開平1−180293号)、特願昭63−517
65号(特開平1−228589号)、特願昭63−1
49861号(特開平1−317592号)にて、電解
槽内を隔膜で陽極室と陰極室で仕切り、両極室に導入し
た水道水などの原水を電気分解することで無菌の処理水
を生成することを発明した。2. Description of the Related Art The present inventors have disclosed a method and an apparatus for producing an acidic water from the anode side and an alkaline water from the cathode side by electrolyzing raw water, and have already disclosed Japanese Patent Application No. 63-3790.
No. (JP-A-1-180293), Japanese Patent Application No. 63-517.
No. 65 (Japanese Patent Application Laid-Open No. 1-228589), Japanese Patent Application No. 63-1
According to Japanese Patent No. 49861 (JP-A-1-317592), the inside of an electrolytic cell is partitioned by a diaphragm into an anode chamber and a cathode chamber, and raw water such as tap water introduced into the bipolar chambers is electrolyzed to produce aseptic treated water. That was invented.
【0003】[0003]
【発明が解決しようとする課題】ところが、この種の従
来の処理水の製造には、安定したpH値を有する酸性水
およびアルカリ水を生成する必要があり、この種の従来
の方法および装置においては、生成の最中に、そのpH
値を測定することは困難であった。すなわち、pH値を
測定するには、イオン電極法などのpH計測器によるの
が一般的であり、この計測に際しては、被測定箇所を必
ず電場内において行わなければならず、このため、強い
電圧を印加する電解の場合には、その処理の途中でpH
値を測定すること自体ができなかった。殊に、リアルタ
イムに、そのpH値を計測することは及びもつかなかっ
た。However, the production of this type of conventional treated water requires the production of acidic water and alkaline water having a stable pH value. During its formation, its pH
It was difficult to measure the value. That is, in order to measure the pH value, it is general to use a pH meter such as an ion electrode method. In this measurement, the measurement target must always be performed in an electric field. In the case of electrolysis where
The value itself could not be measured. In particular, measuring its pH value in real time has been unsuccessful.
【0004】本発明は、上記従来の事情に鑑みてなされ
たもので、陽極と陰極間を隔膜で仕切って陽極室と陰極
室とを形成した電解槽内に原水を流して電気分解し、前
記原水の電解前の電気伝導度と電解後の処理水の電気伝
導度との差を求め、所定の手順に従って、リアルタイム
に電解生成水pHを計測し、表示する電解生成処理水の
pH値を表示する方法および電解生成水pH表示装置を
提供することを目的とする。The present invention has been made in view of the above-mentioned conventional circumstances, and raw water is flowed into an electrolytic cell in which an anode and a cathode are partitioned by a diaphragm to form an anode chamber and a cathode chamber, and electrolysis is performed. Find the difference between the electric conductivity of raw water before electrolysis and the electric conductivity of treated water after electrolysis, measure the pH of electrolyzed water in real time according to a predetermined procedure, and display the pH value of electrolyzed water to be displayed It is an object of the present invention to provide a method and a pH indicator for electrolytically produced water.
【0005】[0005]
【課題を解決するための手段】本発明は、上記目的を達
成するために、請求項1には、陽極と陰極間を隔膜で仕
切って陽極室と陰極室とを形成した電解槽内に原水を流
して電気分解をするとともに、所望のpH値の処理水を
製造する方法において、上記原水の電解前の電気伝導度
と電解後の処理水の電気伝導度との差(EC差)を測定
し、次式(A)、(B)により電解生成処理水のpH値
を算出し、表示することを特徴とする。pH値が4.1
1末満の場合は Y=5.43−0.94X(A) 〔Y=log(EC差)、X=pH値〕 pH値が4.11以上場合は Y=2.84−0.31X(B) 〔Y=log(EC差)、X=pH値〕According to the present invention, in order to achieve the above-mentioned object, according to the present invention, raw water is contained in an electrolytic cell in which an anode chamber and a cathode chamber are formed by partitioning an anode and a cathode with a diaphragm. And a method for producing treated water having a desired pH value by measuring the difference (EC difference) between the electric conductivity of the raw water before electrolysis and the electric conductivity of the treated water after electrolysis. The pH value of the electrolyzed water is calculated by the following equations (A) and (B) and displayed. pH value of 4.1
Y = 5.43-0.94X (A) [Y = log (EC difference), X = pH value] If the pH value is 4.11 or more, Y = 2.84-0.31X (B) [Y = log (EC difference), X = pH value]
【0006】また、本願請求項2に係る発明は、前記請
求項1に記載の電解生成処理水のpH値を表示する方法
において用いる装置であって、陽極と陰極間を隔膜で仕
切って陽極室と陰極室とが形成された電解槽と、その電
解槽の陽極室と陰極室に原水を供給する原水供給手段
と、電解槽の陽極と陰極間に電圧を印加する電源手段
と、原水の入口側電気伝導度と陽極室の出口側の処理水
の電気伝導度との差を測定し、次式(A)、(B)によ
り電解生成処理水のpH値を算出し、表示する手段とを
有することを特徴とする。 pH値が4.11末満の場合は Y=5.43−0.94X(A) 〔Y=log(EC差)、X=pH値〕 pH値が4.11以上場合は Y=2.84−0.31X(B) 〔Y=log(EC差)、X=pH値〕According to a second aspect of the present invention, there is provided an apparatus used in the method for displaying the pH value of the electrolytically produced treated water according to the first aspect, wherein the anode and the cathode are separated by a diaphragm. And a cathode chamber formed therein, raw water supply means for supplying raw water to the anode chamber and cathode chamber of the electrolytic cell, power supply means for applying a voltage between the anode and cathode of the electrolytic cell, and an inlet for raw water Means for measuring the difference between the side electric conductivity and the electric conductivity of the treated water on the outlet side of the anode chamber, calculating the pH value of the electrolytically produced treated water by the following formulas (A) and (B), and displaying the pH value.
It is characterized by having . When the pH value is less than 4.11, Y = 5.43-0.94X (A) [Y = log (EC difference), X = pH value] When the pH value is 4.11 or more, Y = 2. 84-0.31X (B) [Y = log (EC difference), X = pH value]
【0007】[0007]
【発明の実施の形態】上記構成によれば、生成した酸性
水及びアルカリ性水のpH値を直接測定する代わりに出
入口の電気伝導度差を検出し、その差に基づいてpH値
をリアルタイムに表示することができる。According to the above configuration, instead of directly measuring the pH value of the generated acidic water and alkaline water, the difference in electric conductivity between the entrance and the exit is detected, and the pH value is displayed in real time based on the difference. can do.
【0008】[0008]
【実施例】以下本発明の実施例を添付図面に基づいて説
明する。図1(a)において、1は電解槽で、隔膜2で
陽極室3と陰極室4とに仕切られると共にその3、4に
それぞれ内壁と一体または別個に陽極5及び陰極6が設
けられる。この陽極室3と陰極室4には、水道水、井戸
水などの原水を供給する原水供給手段7が接続される。
すなわち、陰極室4の下部に原水供給管8が接続され、
その分岐管10が陽極室4の下部に接続されて原水供給
手段7が形成される。Embodiments of the present invention will be described below with reference to the accompanying drawings. In FIG. 1 (a), reference numeral 1 denotes an electrolytic cell, which is partitioned by a diaphragm 2 into an anode chamber 3 and a cathode chamber 4, and the anodes 5 and the cathodes 6 are provided integrally with or separately from the inner walls of the chambers 3, 4, respectively. Raw water supply means 7 for supplying raw water such as tap water and well water is connected to the anode chamber 3 and the cathode chamber 4.
That is, the raw water supply pipe 8 is connected to the lower part of the cathode chamber 4,
The branch pipe 10 is connected to the lower part of the anode chamber 4 to form the raw water supply means 7.
【0009】陽極室3と陰極室の上部にはそれぞれ陽極
処理水(酸性水)の排出管11と陰極処理水(アルカリ
性水)の排出管12が接続される。陽極5と陰極6には
原水を電気分解するための出力電圧可変な直流電源13
が接続され、原水供給手段7より、電解槽1内の陽極室
3と、陰極室4内に原水が供給され、直流電源13より
陽極5と陰極6との間に直流電圧が印加されて、原水が
電気分解され、酸性の処理水が陽極排水管11より排水
され、また、アルカリ性の処理水が陰極排水管12より
排水される。A discharge pipe 11 for anodized water (acidic water) and a discharge pipe 12 for cathodically treated water (alkaline water) are connected to the upper portions of the anode chamber 3 and the cathode chamber, respectively. The anode 5 and the cathode 6 have a variable output voltage DC power supply 13 for electrolyzing raw water.
Is connected, and raw water is supplied from the raw water supply means 7 into the anode chamber 3 in the electrolytic cell 1 and into the cathode chamber 4, and a DC voltage is applied between the anode 5 and the cathode 6 from the DC power supply 13, raw water is electrolyzed, treated water acidity is drained from the anode exhaust water pipe 11, also alkaline treated water is drained from the cathode discharge pipe 12.
【0010】また、前記原水供給管8には、原水の電気
伝導度を測定するEC電極14が設けられ、また陽極処
理水の配管11には、陽極処理水の電気伝導度を測定す
るEC電極15が設けられ、本実施例においては、これ
ら二つのEC電極14、15を設けることによって、そ
の電解槽に供給される原水の電気伝導度と、陽極室から
排水される処理水の電気伝導度を測定、比較することに
より、電気分解しながらも、生成される酸性水またはア
ルカリ性水のpH値をリアルタイムに表示する方法およ
びその装置を提供せんとするものである。The raw water supply pipe 8 is provided with an EC electrode 14 for measuring the electric conductivity of the raw water, and the anodized water pipe 11 is provided with an EC electrode 14 for measuring the electric conductivity of the anodized water. In this embodiment, by providing these two EC electrodes 14 and 15, the electric conductivity of raw water supplied to the electrolytic cell and the electric conductivity of treated water discharged from the anode chamber are provided. It is intended to provide a method and an apparatus for displaying the pH value of generated acidic water or alkaline water in real time while electrolysis while measuring and comparing the pH values.
【0011】次に、このようなEC電極を用いた場合
に、pH値とEC値との関係を説明する。原水の電気伝
導度(EC)値を測定する。そして、その原水を前記電
解槽1で電気分解すると、電解後陽極室3より吐水され
る処理水(酸性水)のpH値は、原水のpH値より低下
し、EC値は、原水のEC値より、上昇する。したがっ
て、この関係に着目すると、電解処理において、pH値
とEC値との関係を下記のように関連式を導くことによ
り、pH値に換算することができる。原水と電解生成水
においてのEC値とpH値との関連式は次のようにな
る。すなわち、原水の電気伝導率Kは、式15で示され
る。Next, the relationship between the pH value and the EC value when such an EC electrode is used will be described. Measure the electrical conductivity (EC) value of the raw water. When the raw water is electrolyzed in the electrolytic cell 1, the pH value of the treated water (acidic water) discharged from the anode chamber 3 after electrolysis is lower than the pH value of the raw water, and the EC value is the EC value of the raw water. More to rise. Therefore, focusing on this relationship, in the electrolytic treatment, the relationship between the pH value and the EC value can be converted into a pH value by deriving a related equation as follows. The relational expression between the EC value and the pH value in the raw water and the electrolyzed water is as follows. That is, the electric conductivity K of the raw water is represented by Expression 15.
【0012】[0012]
【式1】 (Equation 1)
【0013】そして、これは、原水中の電解質物質の電
離によって生ずるイオン種とその濃度により決定され
る。原水のpH値は、いわゆる中性領域にあるので、H
=OH=10−7M/lで求められ、したがって、この
イオン濃度では、原水のEC値は、電解質物質の電離に
よるイオンのものといえる。次に原水を電解するとする
と、この電解においては、電解に必要な通電量Q(クロ
ーン)は、次式に示すように電流iと時間tの積で表さ
れる。 Q=i・t (2) また、電流iは式2のようにも表される。[0013] This is determined by the ion species generated by ionization of the electrolyte substance in the raw water and its concentration. Since the pH value of the raw water is in the so-called neutral range,
= OH = 10 −7 M / l. Therefore, at this ion concentration, the EC value of the raw water can be said to be that of ions due to ionization of the electrolyte substance. Next, when raw water is electrolyzed, in this electrolysis, the amount of current Q (clone) required for electrolysis is represented by the product of current i and time t as shown in the following equation. Q = i · t (2) Further, the current i is also expressed by Expression 2.
【0014】[0014]
【式2】 (Equation 2)
【0015】また、当量イオン伝導率λiとイオン移動
度Uiとの関係は次式で表され、 Ui=λi/F (4) 原水の電気伝導率Kは(1)式に(4)式を代入して、
式3に表すことができ、The relationship between the equivalent ionic conductivity λi and the ion mobility Ui is expressed by the following equation: Ui = λi / F (4) The electric conductivity K of the raw water is expressed by the following equation (1). Substitute,
Which can be expressed in equation 3,
【0016】[0016]
【式3】 (Equation 3)
【0017】(3)式と(5)式より関数Kの変数は、From the equations (3) and (5), the variable of the function K is
【0018】[0018]
【式4】 (Equation 4)
【0019】となり、電極間の電圧と電流によって決ま
ることになる。また、変数Σ|Zi|Ci・λiのう
ち、陽イオン部分(式5で示す。)は、隔膜を通して、
陰極側に、陰イオン部分(式6で示す。)は、陽極側に
移動するが、各種イオンの当量イオン伝導率とイオン移
動度は、陰イオンの方が僅かに高い値を示すが、原水に
含まれていると考えられるイオン種は、OHイオンを除
いた場合は、ほぼ同じ値になる。Thus, the voltage is determined by the voltage and current between the electrodes. Further, of the variable 式 | Zi | Ci · λi, the cation portion (shown by equation 5) passes through the diaphragm,
On the cathode side, the anion portion (indicated by Equation 6) moves to the anode side, but the equivalent ion conductivity and ion mobility of various ions show slightly higher values for anions, but the raw water The ionic species considered to be contained in the above have substantially the same value when OH ions are excluded.
【0020】[0020]
【式5】 (Equation 5)
【0021】[0021]
【式6】 (Equation 6)
【0022】よって、式7が成り立ち、電解前と電解後
でのEC値が異なるのは、陽極側ではH+の濃度、陰極
側ではOH+濃度の変化によることがわかる。Therefore, it can be understood that the equation 7 holds, and the EC values before and after electrolysis are different due to changes in the concentration of H + on the anode side and the OH + concentration on the cathode side.
【0023】[0023]
【式7】 Equation 7
【0024】それゆえに、電解前のEC値をK1とし、
電解後のEC値をK2とすると、式8が成り立つ。Therefore, the EC value before electrolysis is defined as K1,
Assuming that the EC value after electrolysis is K2, Expression 8 holds.
【0025】[0025]
【式8】 (Equation 8)
【0026】つまり、K2−K1をEC差とすると、E
C差とHは相関性があるので式9が成立する。That is, assuming that K2-K1 is the EC difference, E
Equation 9 holds because the C difference and H have a correlation.
【0027】[0027]
【式9】 [Equation 9]
【0028】なお、いくつかの計測をした結果、陽極室
より吐出される処理水のEC差と、pH値との間には、
一定の相関性があることを知りえた。すなわち、図1の
電解槽を用いて、水道水(EC68μs/cm、pH
6.65)を電解して、EC差とその時のpH値のデー
タを表1に示し、また、このデータを図2のグラフに示
した。As a result of several measurements, the difference between the EC difference between the treated water discharged from the anode chamber and the pH value is as follows.
We knew that there was a certain correlation. That is, using the electrolytic cell of FIG. 1, tap water (EC 68 μs / cm, pH
6.65) was electrolyzed, and the data of the EC difference and the pH value at that time are shown in Table 1, and this data is shown in the graph of FIG.
【0029】[0029]
【表1】 [Table 1]
【0030】この際の試験方法としては、電解前の前記
水道水のECを市販されているEC計で測定し、その値
を電解前の原水のEC値とし、電解槽で電解した後(電
解槽1に負荷する電解電流を可変することにより)、陽
極室3から吐水された処理水のpH値を市販のpH計で
測定し、その値を、生成された処理水のEC値をEC計
で測定し、この値を電解後のEC値とした。そして、電
解後のECから電解前のECを引いた値をEC差とし
た。このような測定および所定の関係を導くことによ
り、pH値とEC値とは、一定の相関性があることが知
りえた。As a test method at this time, the EC of the tap water before the electrolysis was measured by a commercially available EC meter, and the value was used as the EC value of the raw water before the electrolysis. The pH value of the treated water discharged from the anode chamber 3 is measured with a commercially available pH meter, and the EC value of the generated treated water is measured by an EC meter (by varying the electrolytic current applied to the tank 1). And this value was taken as the EC value after electrolysis. Then, a value obtained by subtracting EC before electrolysis from EC after electrolysis was defined as EC difference. By deriving such a measurement and a predetermined relationship, it was found that there is a certain correlation between the pH value and the EC value.
【0031】また、次に、水道水(EC68μs/c
m、pH6.65)で、硫酸を希釈し、各pH値におい
てのEC値及びEC差を調べた。すなわち、電解溶液
(例えば硫酸等)を、水道水で希釈して、各pH値にお
けるEC値とEC差を表2にし、図3に、このデータを
グラフで示した。Next, tap water (EC 68 μs / c)
m, pH 6.65), and the EC value and EC difference at each pH value were examined. That is, an electrolytic solution (for example, sulfuric acid or the like) was diluted with tap water, and the EC value and EC difference at each pH value were shown in Table 2, and this data is shown in a graph in FIG.
【0032】[0032]
【表2】 [Table 2]
【0033】上記の試験例1、2のデータを比較し、知
り得ることは、水道水及び電解溶液おけるEC差は、p
H3.0と2.0との間では、ほとんど差のない同数値
で表され、また、pH3.0以上では、近似的数値で表
されることが知り得た。また、水道水、井戸水、海水
(食塩等を含んだ水)等を電解し、生成された水のpH
値は、電解前のEC値と、電解後のEC値とを測定する
ことにより、生成水のpH値を求めることができること
を知りえた。By comparing the data of Test Examples 1 and 2 above, what can be known is that the EC difference between tap water and electrolytic solution is p
It was found that between H3.0 and 2.0, the values were expressed by almost the same values with almost no difference, and that at pH 3.0 or higher, they were expressed by approximate values. It also electrolyzes tap water, well water, seawater (water containing salt, etc.), and produces a pH value of the generated water.
As for the value, it was found that the pH value of the produced water can be determined by measuring the EC value before electrolysis and the EC value after electrolysis.
【0034】また、図3において、直線A及び直線Bを
数式化すると、直線Aは、式(A)で、直線Bは、式
(B)で示される。 Y=5.43−0.94X (A) 〔Y=log(EC差),X=pH値〕 直線Bは、 Y=2.84−0.31X (B) となり、A線とB線の交点は(4.11,1.57)と
なり、pH値を算出する場合には、pH4.11を分岐
点として、pH4.11以上の場合は、上記(B)式を
用いて、近似的なlog(EC差)を算出し、電解後の
EC値を知ることができる。また、pH4.11未満で
は、pH2.0程度までは、上記(A)式を用いて、l
og(EC差)を算出し、電解後のEC値を知ることが
できる。In FIG. 3, when the straight line A and the straight line B are mathematically expressed, the straight line A is expressed by the equation (A), and the straight line B is expressed by the equation (B). Y = 5.43-0.94X (A) [Y = log (EC difference), X = pH value] The straight line B becomes Y = 2.84-0.31X (B). The intersection is (4.11, 1.57), and when calculating the pH value, the pH 4.11 is taken as the branch point, and when the pH is 4.11 or more, the approximate value is calculated using the above equation (B). By calculating log (EC difference), the EC value after electrolysis can be known. In addition, when the pH is less than 4.11, up to about pH 2.0, using the above formula (A),
og (EC difference) can be calculated, and the EC value after electrolysis can be known.
【0035】このことから、上記(A)式(B)式を用
いてEC差を知ることができれば、電解後の処理水のp
H値は、容易に算出できることとなる。したがって、上
記の算出方法を用いれば、電解の最中であっても容易に
生成される処理水のpH値を求めることができる。From the above, if the EC difference can be obtained by using the above equations (A) and (B), the p of the treated water after electrolysis can be obtained.
The H value can be easily calculated. Thus, using the above method of calculation, it is possible to determine the pH value of the treated water even during the electrolysis are easily generated.
【0036】次に原水と処理水の電気伝導度差(EC
差)から処理水のpHを表示する装置を図4により説明
する。図4において原水のEC電極16と処理水のEC
電極17とで発振器20に接続した交流ブリッヂ21を
形成し、その出力を電位差増幅器22に入力し、この電
位差を直流電流電圧変換回路23にて直流電圧に変換す
る。得られた出力24をコントロール回路25に入力す
る。コントロール回路25には、上述した試験例1、2
のデータを計算し、求められた電圧値からpH値を表示
回路26に出力し、その時点の処理水のpH値をアナロ
グ表示やデジタル表示で表示することができる。Next, the difference in electric conductivity between raw water and treated water (EC
An apparatus for displaying the pH of the treated water from the difference will be described with reference to FIG. In FIG. 4, EC electrode 16 of raw water and EC of treated water are shown.
An AC bridge 21 connected to an oscillator 20 is formed by the electrode 17 and the output is input to a potential difference amplifier 22, and this potential difference is converted into a DC voltage by a DC current / voltage conversion circuit 23. The obtained output 24 is input to the control circuit 25. The control circuit 25 includes the test examples 1 and 2 described above.
Is calculated, the pH value is output from the obtained voltage value to the display circuit 26, and the pH value of the treated water at that time can be displayed by analog display or digital display.
【0037】[0037]
【発明の効果】以上説明してきたように本発明によれ
ば、原水と処理水の電気伝導度(EC)差を測定するこ
とにより、電場内でのpH測定を可能にし、電解の最中
であっても、リアルタイムに、生成される処理水のpH
値を表示することができる。As described above, according to the present invention, by measuring the difference in electric conductivity (EC) between raw water and treated water, it is possible to measure pH in an electric field, and during electrolysis, Even if the pH of the generated treated water is real-time
Values can be displayed.
【図1】本発明の一実施例を示す装置図である。FIG. 1 is an apparatus diagram showing one embodiment of the present invention.
【図2】本発明において処理水のpH値とEC値との関
係を示す説明図である。FIG. 2 is an explanatory diagram showing a relationship between a pH value of treated water and an EC value in the present invention.
【図3】本発明において処理水のpH値とEC値との関
係を示す説明図である。FIG. 3 is an explanatory diagram showing a relationship between a pH value of treated water and an EC value in the present invention.
【図4】本発明における直流電流の電源回路図である。FIG. 4 is a power supply circuit diagram of a direct current according to the present invention.
1・・・電解槽 2・・・隔膜 3・・・陽極室 4・・・陰極室 5・・・陽極 6・・・陰極 7・・・原水供給手段 13・・直流電源 14、15・・EC電極 16、17・・EC測定槽 DESCRIPTION OF SYMBOLS 1 ... Electrolyzer 2 ... Diaphragm 3 ... Anode chamber 4 ... Cathode chamber 5 ... Anode 6 ... Cathode 7 ... Raw water supply means 13. DC power supply 14, 15 ... EC electrodes 16, 17 ... EC measuring tank
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平1−180293(JP,A) 特開 昭51−82802(JP,A) 特開 昭58−131193(JP,A) 特開 昭57−57248(JP,A) 実公 昭63−10867(JP,Y2) 「電気化学」、第11巻(昭和18年11 月)、第324−329頁 (58)調査した分野(Int.Cl.6,DB名) G01N 27/06 - 27/10 C02F 1/46 - 1/469 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-1-180293 (JP, A) JP-A-51-82802 (JP, A) JP-A-58-131193 (JP, A) JP-A-57-131 57248 (JP, a) the actual public Akira 63-10867 (JP, Y2) "electrochemical", Vol. 11 (1943 November), pp. 324-329 (58) investigated the field (Int.Cl. 6 , DB name) G01N 27/06-27/10 C02F 1/46-1/469
Claims (2)
陰極室とを形成した電解槽内に原水を流して電気分解を
するとともに、所望のpH値の処理水を製造する方法に
おいて、上記原水の電解前の電気伝導度と電解後の処理
水の電気伝導度とのEC差を測定し、次式(A)、
(B)により電解生成処理水のpH値を算出し、表示す
る方法。 pH値が4.11末満の場合は Y=5.43−0.94X(A) 〔Y=log(EC差)、X=pH値〕 pH値が4.11以上の場合は Y=2.84−0.31X(B) 〔Y=log(EC差)、X=pH値〕1. A method for producing raw water having a desired pH value by flowing raw water into an electrolytic cell having an anode chamber and a cathode chamber formed by partitioning an anode and a cathode with a diaphragm to form electrolyzed water. The EC difference between the electric conductivity of the raw water before electrolysis and the electric conductivity of the treated water after electrolysis was measured, and the following equation (A) was obtained.
A method of calculating and displaying the pH value of the electrolytically generated treated water according to (B). When the pH value is less than 4.11, Y = 5.43-0.94X (A) [Y = log (EC difference), X = pH value] When the pH value is 4.11 or more, Y = 2 .84-0.31X (B) [Y = log (EC difference), X = pH value]
陰極室とが形成された電解槽と、その電解槽の陽極室と
陰極室に原水を供給する原水供給手段と、電解槽の陽極
と陰極間に電圧を印加する電源手段と、原水の入口側電
気伝導度と陽極室の出口側の処理水の電気伝導度とのE
C差を測定し、次式(A)、(B)により電解生成処理
水のpH値を算出し、表示する手段とを有することを特
徴とする電解生成水pH表示装置。 pH値が4.11末満の場合は Y=5.43−0.94X(A) 〔Y=log(EC差)、X=pH値〕 pH値が4.11以上の場合は Y=2.84−0.31X(B) 〔Y=log(EC差)、X=pH値〕2. An electrolytic cell in which an anode chamber and a cathode chamber are formed by partitioning an anode and a cathode with a diaphragm, raw water supply means for supplying raw water to the anode chamber and the cathode chamber of the electrolytic cell, A power supply means for applying a voltage between the anode and the cathode; and E of the electric conductivity of the raw water at the inlet side and the electric conductivity of the treated water at the outlet side of the anode chamber.
Means for measuring the C difference and calculating and displaying the pH value of the electrolyzed treated water by the following formulas (A) and (B). When the pH value is less than 4.11, Y = 5.43-0.94X (A) [Y = log (EC difference), X = pH value] When the pH value is 4.11 or more, Y = 2 .84-0.31X (B) [Y = log (EC difference), X = pH value]
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25557796A JP2938815B2 (en) | 1996-09-05 | 1996-09-05 | Method for displaying pH value of electro-generated water and pH display device for electro-generated water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP25557796A JP2938815B2 (en) | 1996-09-05 | 1996-09-05 | Method for displaying pH value of electro-generated water and pH display device for electro-generated water |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23422389A Division JP2885841B2 (en) | 1989-09-08 | 1989-09-08 | Method and apparatus for producing treated water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09119911A JPH09119911A (en) | 1997-05-06 |
| JP2938815B2 true JP2938815B2 (en) | 1999-08-25 |
Family
ID=17280659
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP25557796A Expired - Lifetime JP2938815B2 (en) | 1996-09-05 | 1996-09-05 | Method for displaying pH value of electro-generated water and pH display device for electro-generated water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2938815B2 (en) |
-
1996
- 1996-09-05 JP JP25557796A patent/JP2938815B2/en not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| 「電気化学」、第11巻(昭和18年11月)、第324−329頁 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09119911A (en) | 1997-05-06 |
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