JPS6235059B2 - - Google Patents
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- Publication number
- JPS6235059B2 JPS6235059B2 JP54006575A JP657579A JPS6235059B2 JP S6235059 B2 JPS6235059 B2 JP S6235059B2 JP 54006575 A JP54006575 A JP 54006575A JP 657579 A JP657579 A JP 657579A JP S6235059 B2 JPS6235059 B2 JP S6235059B2
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- Prior art keywords
- acid
- concentration
- ions
- fluorine
- ion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Description
【発明の詳細な説明】
本発明は、金属材料の酸洗に使用する弗酸と硝
酸、硫酸、塩酸等の強酸との混酸(以下単に混酸
と記す)、酸洗液の酸濃度、鉄イオン濃度、及び
総弗素イオン濃度測定方法に関するものである。Detailed Description of the Invention The present invention relates to a mixed acid (hereinafter simply referred to as mixed acid) of hydrofluoric acid and a strong acid such as nitric acid, sulfuric acid, or hydrochloric acid used for pickling metal materials, acid concentration of the pickling solution, and iron ion. The present invention relates to a method for measuring concentration and total fluorine ion concentration.
金属材料の酸洗に使用中の混酸中には、水素イ
オン、弗素イオン、強酸の陰イオン、弗酸分子、
強酸の分子の他、金属イオン、金属イオンと弗素
イオンで作る種々の錯イオン、金属と弗素の化合
物等が存在している。例えば、弗酸と硝酸の混酸
で、鉄鋼材料を酸洗する場合の酸洗液中には、次
式の反応で生ずるイオンあるいは分子が存在す
る。 The mixed acid used for pickling metal materials contains hydrogen ions, fluorine ions, strong acid anions, hydrofluoric acid molecules,
In addition to strong acid molecules, there are metal ions, various complex ions made of metal ions and fluorine ions, and compounds of metal and fluorine. For example, when pickling steel materials with a mixed acid of hydrofluoric acid and nitric acid, ions or molecules produced by the following reaction are present in the pickling solution.
HNO3→H++NO− 3 ……(1)
HF〓H++F- ……(2)
HF+F-〓HF− 2 ……(3)
2Fe+6H+→2Fe3++2H2↑ ……(4)
Fe3++HF〓FeF2++H+ ……(5)
FeF2++HF〓FeF+ 2+H+ ……(6)
FeF+ 2+HF〓FeF3↓+H+ ……(7)
これらのイオン、分子のうちで、酸洗に有効な
のは弗素イオン(F-)、硝酸イオン(NO− 3)およ
びこれらと平衡する水素イオン(H+)である。酸
洗が進行すると混酸中に鉄イオンが溶解して(4)式
の反応が進むとともに共存する弗素イオンによつ
て鉄−弗素錯体を生成する(5)(6)式の反応が進み、
ついには(7)式の反応によつて弗化鉄が生成、沈殿
する。前記(1)〜(7)式のうち、酸洗に有効な反応は
(1)及び(4)式であり、このため常に酸洗中の弗酸及
び硝酸の濃度を測定してこれらを管理する必要が
ある。HNO 3 →H + +NO − 3 ……(1) HF〓H + +F - ……(2) HF+F - 〓HF − 2 ……(3) 2Fe+6H + →2Fe 3+ +2H 2 ↑ ……(4) Fe 3+ +HF〓FeF 2+ +H + …(5) FeF 2+ +HF〓FeF + 2 +H + …(6) FeF + 2 +HF〓FeF 3 ↓+H + …(7) These ions and molecules Among them, fluorine ions (F - ), nitrate ions (NO - 3 ), and hydrogen ions (H + ) that are in equilibrium with these ions are effective for pickling. As the pickling progresses, iron ions are dissolved in the mixed acid, and the reaction of equation (4) progresses, and the reactions of equations (5) and (6), which generate an iron-fluorine complex by the coexisting fluorine ions, proceed.
Finally, iron fluoride is produced and precipitated by the reaction of equation (7). Among the above formulas (1) to (7), the reaction effective for pickling is
(1) and (4), and therefore it is necessary to constantly measure and control the concentrations of hydrofluoric acid and nitric acid during pickling.
一方、弗酸及び硝酸を補給して酸濃度調整を行
いつつ酸洗処理を継続すると、酸洗液中では(7)式
にしめす弗化鉄が沈殿し始める。これは単に酸洗
液中の弗素イオン即ち弗酸を消費するだけでな
く、槽内に堆積し酸洗処理の妨げとなる。この弗
化鉄の生成を抑えるには、第1図に示すように全
弗素イオン60g/以下、全鉄イオン30g/以
下となるように酸洗液濃度を管理する必要があ
る。 On the other hand, if the pickling process is continued while adjusting the acid concentration by replenishing hydrofluoric acid and nitric acid, iron fluoride shown by formula (7) begins to precipitate in the pickling solution. This not only consumes fluorine ions, ie, hydrofluoric acid, in the pickling solution, but also accumulates in the tank, interfering with the pickling process. In order to suppress the production of iron fluoride, it is necessary to control the concentration of the pickling solution so that the total fluoride ions are 60 g/or less and the total iron ions are 30 g/or less, as shown in FIG.
従来、この酸濃度を測定するには、水酸化ナト
リウム等のアルカリ溶液による滴定が行われてい
る。しかし、この方法では、共存する金属イオン
の影響で、電導度滴定の場合には電導度変化の彎
曲点が、又指示薬を利用した中和滴定の場合には
色の変化点が不明確であり正確な値が得られな
い。又、弗素イオン、水素イオンを直接測定して
弗酸及び硝酸の測定を行うイオン選択性電極を使
用する方法(特開昭49−83492)が提案されてい
るが分析精度が良くない。また、酸洗液中の金属
イオン濃度及び全弗素イオン濃度を同時に測定す
る方法及び装置はみあたらない。 Conventionally, to measure this acid concentration, titration with an alkaline solution such as sodium hydroxide has been performed. However, in this method, due to the influence of coexisting metal ions, the point of curvature of conductivity change is unclear in the case of conductivity titration, and the point of color change is unclear in the case of neutralization titration using an indicator. I can't get accurate values. Furthermore, a method using an ion-selective electrode for measuring hydrofluoric acid and nitric acid by directly measuring fluorine ions and hydrogen ions has been proposed (Japanese Patent Laid-Open No. 49-83492), but the analytical accuracy is not good. Furthermore, no method or apparatus has been found for simultaneously measuring the metal ion concentration and total fluorine ion concentration in the pickling solution.
本発明は、弗酸を含む混酸酸洗液中の弗酸、強
酸、鉄イオン及び全弗素イオンの各濃度を迅速か
つ精確に測定する方法を提供することを目的とす
る。 An object of the present invention is to provide a method for quickly and accurately measuring the concentrations of hydrofluoric acid, strong acid, iron ions, and total fluorine ions in a mixed acid pickling solution containing hydrofluoric acid.
本発明の方法は、
1 陰イオン交換膜により、混酸酸洗液中の弗素
イオン、強酸の陰イオン及び水素イオンを拡散
透析させ、この溶液に弱酸と強塩基又は強酸と
弱塩基の中和によつて生じた塩溶液を加えて希
釈し、弗素イオン、強酸の陰イオンそれぞれの
イオン選択性電極により、それぞれのイオン濃
度を測定し、この値をもとに、混酸の酸濃度を
求める。 The method of the present invention is as follows: 1. Fluorine ions, strong acid anions, and hydrogen ions in the mixed acid pickling solution are subjected to diffusion dialysis using an anion exchange membrane, and this solution is subjected to diffusion dialysis to neutralize the weak acid and the strong base or the strong acid and the weak base. The resulting salt solution is added and diluted, and the ion concentrations of fluorine ions and strong acid anions are measured using ion-selective electrodes, and based on these values, the acid concentration of the mixed acid is determined.
2 比重計により、混酸酸洗液の比重を測定し、
予め作成してある比重−鉄イオン濃度相関曲線
から鉄イオン濃度を求め、さらにこの値をもと
に鉄イオンと化合している弗素イオンを求め、
別に測定した弗素イオンとの和を求めて全弗素
イオンを測定することを特徴とする。2 Measure the specific gravity of the mixed acid pickling solution using a hydrometer,
Determine the iron ion concentration from the specific gravity-iron ion concentration correlation curve created in advance, and then determine the fluorine ion combined with the iron ion based on this value.
The method is characterized in that total fluorine ions are measured by calculating the sum with fluorine ions measured separately.
以下に、本発明を図面により詳細に説明する。
第2図において1は金属イオンを含んだ混酸を金
属イオンを含まない新混酸(以下回収酸と記す)
として回収する回収槽である。 The present invention will be explained in detail below with reference to the drawings.
In Figure 2, 1 is a mixed acid containing metal ions and a new mixed acid containing no metal ions (hereinafter referred to as recovered acid).
This is a collection tank that collects wastewater as waste.
弗素イオン選択性電極で弗素イオン濃度を測定
する際、イオン強度バツフアーとPHバツフアーを
兼ねたくえん酸ナトリウム溶液を使用するが、金
属イオンを含んだ混酸をそのまま試料とすると
(5)、(6)式で示す鉄−弗素錯体が解離して弗素を遊
離するため過剰の弗素イオンを測定するので真の
弗素イオンを測定出来ない。このために、本回収
槽を用い、遊離の弗素イオンのみを回収する。回
収槽は陰イオン交換膜2により仕切られている。
左側には酸洗に使用中の混酸を入れ、右側には水
を入れておく。この回収槽の容量は、右側に比べ
左側を充分に大きくしておく。こうすることによ
つて左側の混酸中の弗素イオン(F-)および強酸
の陰イオンが、陰イオン交換膜2中を拡散透析し
て右側の水中に移行する。このとき陽イオンであ
る水素イオン(H+)もイオン半径が小さいため移
行する。陰イオン交換膜2の左右で弗素イオン、
強酸の陰イオンおよび水素イオンの各濃度が等し
くなつたところで平衡に達する。このときの濃度
は、左側の容積をVA、右側の容積をVBとする
と、
W=VA/VA+VB・C ……(8)
W:平衡に対する濃度
C:左側に入れた混酸の濃度
で求まる。また右側の濃度が時間(t)とともに
増加する割合(t)は
(t)=W(1−E-〓) ……(9)
t:時間
T:時定数
で求まる。(8)式を(9)式に代入し
(t)=VA/VA+VB・C・(1−E-〓)……
(10)
となる。従つて使用中の混酸中の錯イオンのバラ
ンスをくずすことなく、混酸と濃度と(10)式に示す
関係をもつた酸濃度を有する金属イオンを含まな
い回収酸を回収槽の右側に得ることができる。な
お陰イオン交換膜中のイオンの拡散透析に時間を
要する場合には、超音波振動を付与して時間短縮
することができる。 When measuring fluoride ion concentration with a fluoride ion-selective electrode, a sodium citrate solution that serves as an ionic strength buffer and a PH buffer is used, but if a mixed acid containing metal ions is used as a sample.
Since the iron-fluorine complexes shown in formulas (5) and (6) dissociate to liberate fluorine, excess fluorine ions are measured, and true fluorine ions cannot be measured. For this purpose, this recovery tank is used to recover only free fluorine ions. The recovery tank is partitioned by an anion exchange membrane 2.
Put the mixed acid used for pickling on the left side, and water on the right side. The capacity of this recovery tank is made sufficiently larger on the left side than on the right side. By doing this, the fluorine ions (F - ) in the mixed acid on the left and the anions of the strong acid undergo diffusion dialysis through the anion exchange membrane 2 and migrate into the water on the right. At this time, hydrogen ions (H + ), which are cations, also migrate because their ionic radius is small. Fluorine ions on the left and right sides of the anion exchange membrane 2,
Equilibrium is reached when the concentrations of anions and hydrogen ions of the strong acid are equal. The concentration at this time is, assuming that the volume on the left side is V A and the volume on the right side is V B , W = V A / V A + V B・C ... (8) W: Concentration relative to equilibrium C: Mixed acid added to the left side It is determined by the concentration of Also, the rate (t) at which the concentration on the right side increases with time (t) is determined by (t)=W(1-E - 〓)...(9) t: time T: time constant. Substitute equation (8) into equation (9) (t)=V A /V A +V B・C・(1-E - 〓)...
(10) becomes. Therefore, without destroying the balance of complex ions in the mixed acid being used, it is possible to obtain recovered acid free of metal ions and having an acid concentration that has the relationship between the mixed acid and the concentration shown in equation (10) on the right side of the recovery tank. I can do it. Note that if it takes time to perform diffusion dialysis of ions in the anion exchange membrane, the time can be shortened by applying ultrasonic vibration.
以上のようにして得られた回収酸も弗酸と強酸
の混酸であるため弗素イオンの量に比して水素イ
オンの量が多く弗酸はほとんど解離していない為
このままでは弗素イオン選択性電極による弗酸の
濃度測定は困難である。この為第2図に示すよう
に回収酸を混合槽3に導き希釈溶液用タンク4に
入つている希釈液で希釈する。希釈液は回収酸の
水素イオンを中和させ弗酸を解離させるとともに
イオン強度バツフアとしても作用するものでなけ
ればならない。水素イオンを中和させるために、
加水分解して微アルカリとなる塩つまり、弱酸と
強塩基又は強酸と弱塩基で中和して得られる塩の
水溶液である必要がある。またイオン強度バツフ
アとしても使えるために電離して電価の多い塩で
あることが必要である。このような希釈液の一例
としてくえん酸ナトリウムを使用した場合につい
て説明する。弗酸は水素イオン濃度が10-5モル/
以下程度になると、ほぼ完全に解離する為、回
収酸をくえん酸ナトリウム溶液で希釈して水素イ
オン濃度が10-5モル/以下になるように、希釈
率とくえん酸ナトリウム溶液の濃度を決めてお
く。例えば硝酸濃度最大1モル/で弗酸濃度最
大1モル/の回収酸では1モル/のくえん酸
ナトリウム溶液で回収酸の濃度を1/10に希釈す
ると水素イオン濃度は10-5モル/以下になる。
第2図の混合槽3において回収酸を希釈し、希釈
された回収酸について検出槽5で、弗素イオン選
択性電極6と強酸の陰イオン選択性電極7により
弗素イオン濃度及び強酸の陰イオン濃度を検知す
る。各イオン濃度はそれぞれの電圧計8,9によ
り電極の起電力として測定され、この値から混酸
濃度を知ることができる。また混合槽3は検出槽
5をかねてもよい。このようにすることにより金
属イオンを含んだ混酸の濃度を金属イオンの影響
を受けず、しかもイオン選択性電極を用いて測定
することができるため、自動化が容易で、比較的
短い時間で正確に硝酸及び弗酸の濃度を測定する
ことができる。 The recovered acid obtained in the above manner is also a mixed acid of hydrofluoric acid and a strong acid, so the amount of hydrogen ions is large compared to the amount of fluorine ions, and the hydrofluoric acid is hardly dissociated. Measuring the concentration of hydrofluoric acid is difficult. For this purpose, as shown in FIG. 2, the recovered acid is introduced into a mixing tank 3 and diluted with a diluent contained in a dilute solution tank 4. The diluent must neutralize hydrogen ions in the recovered acid and dissociate hydrofluoric acid, and must also act as an ionic strength buffer. To neutralize hydrogen ions,
It needs to be an aqueous solution of a salt that becomes slightly alkaline upon hydrolysis, that is, a salt obtained by neutralizing a weak acid and a strong base or a strong acid and a weak base. In addition, since it can also be used as an ionic strength buffer, it needs to be a salt with a high charge value when ionized. A case where sodium citrate is used as an example of such a diluent will be described. Hydrofluoric acid has a hydrogen ion concentration of 10 -5 mol/
If the concentration is below, it will almost completely dissociate, so determine the dilution rate and the concentration of the sodium citrate solution so that the recovered acid is diluted with a sodium citrate solution and the hydrogen ion concentration becomes 10 -5 mol/or less. put. For example, if the recovered acid has a maximum concentration of 1 mol/nitric acid and a maximum concentration of 1 mol/fluoric acid, and the concentration of the recovered acid is diluted to 1/10 with a 1 mol/mol sodium citrate solution, the hydrogen ion concentration will be 10 -5 mol/or less. Become.
The recovered acid is diluted in the mixing tank 3 of FIG. Detect. The concentration of each ion is measured as the electromotive force of the electrode by the respective voltmeters 8 and 9, and the mixed acid concentration can be determined from this value. Further, the mixing tank 3 may also serve as the detection tank 5. In this way, the concentration of a mixed acid containing metal ions can be measured using an ion-selective electrode without being affected by metal ions, making it easy to automate and accurately measure in a relatively short time. The concentration of nitric acid and hydrofluoric acid can be measured.
10は比重測定のための槽で混酸を導入する。
11は液体比重計で、12はインターフエイスで
ある。混酸中の鉄イオンが増加するにしたがい、
第3図に示すように液体の比重が増加する。この
関係は相関があるので、混酸の比重を測定すれば
鉄イオン濃度が測定出来る。全弗素イオンは弗酸
中の弗素イオンと(5)(6)式にしめす鉄−弗素錯体中
の弗素イオンの合量によつて求まるが、第4図に
示すように鉄−弗素錯体中の弗素は、鉄と弗酸濃
度によつて化合型態が異なるので、計算によつて
容易に求めることが出来る。13は濃度測定用の
計算機、14はデイスプレーである。計算機は弗
素イオン、強酸イオン比重の各測定値の情報から
弗酸、強酸、鉄イオン及び全弗素イオンの各濃度
の算出を行う。又、鉄イオン濃度及び全弗素イオ
ン濃度が第1図の曲線A以下の範囲内であれば、
弗化鉄は沈殿しないし、図中の斜線内となるよう
全弗素イオン及び鉄イオン濃度を調整すれば酸洗
効果が大きいことを確認している。このため、こ
れら全弗素イオン、鉄イオン、弗酸及び強酸の濃
度を測定することが重要である。 10 is a tank for measuring specific gravity, into which mixed acid is introduced.
11 is a liquid hydrometer, and 12 is an interface. As the iron ions in the mixed acid increase,
As shown in FIG. 3, the specific gravity of the liquid increases. Since this relationship is correlated, the iron ion concentration can be measured by measuring the specific gravity of the mixed acid. The total fluorine ion is determined by the total amount of fluorine ions in hydrofluoric acid and the fluorine ions in the iron-fluorine complex according to equations (5) and (6). Since the compound form of fluorine differs depending on the concentration of iron and hydrofluoric acid, it can be easily determined by calculation. 13 is a calculator for concentration measurement, and 14 is a display. The calculator calculates the concentrations of hydrofluoric acid, strong acid, iron ions, and total fluorine ions from the information on the measured values of fluorine ions and strong acid ion specific gravity. Also, if the iron ion concentration and total fluorine ion concentration are within the range below curve A in Figure 1,
It has been confirmed that iron fluoride does not precipitate, and that if the total fluoride ion and iron ion concentrations are adjusted to fall within the diagonal lines in the figure, the pickling effect will be great. Therefore, it is important to measure the concentrations of total fluorine ions, iron ions, hydrofluoric acid, and strong acids.
濃度測定を行う必要が生じた場合は、図示して
いない水源から水シヤワー39,40,41に水
を一定時間供給し、液槽24,25,26の内部
とこれらを結ぶ導管を洗浄する。このとき電磁弁
43,46,47を開いておき、洗浄水は、電磁
弁43,47を通つて排出される。洗浄水が完全
に排出された後ポンプ36を駆動し電磁弁44を
開くと共に電磁弁43,46,47を閉じ、標準
液タンク34より液槽24に濃度のわかつている
標準液を一定量供給し、これと同時に液槽25に
水シヤワー40から水を一定量供給し、この状態
で一定時間保持する。すると液槽24と25はそ
の間を陰イオン交換膜48によつてしきられてい
る為、液槽25の酸濃度が増加する。こうして一
定時間経過した後電磁弁46を開き、液槽25の
液を液槽26に移すとともに、ポンプ37を駆動
し電磁弁45を開き希釈液タンク33から希釈液
を一定量供給し希釈するとともにスターラー42
でかくはんしながら弗素イオン選択性電極27
と、被検液中の強酸の陰イオンに選択性をもつイ
オン選択性電極28(例えば硝酸イオン電極)
と、この2つの電極電位の基準となる電圧を発生
する比較電極29により各濃度を検出し電圧計3
0にて起電力を測定し演算部31に記憶する。こ
の測定が完了すると電磁弁47を開き液槽26の
液を排出する。 When it becomes necessary to measure the concentration, water is supplied from a water source (not shown) to the water showers 39, 40, 41 for a certain period of time to clean the insides of the liquid tanks 24, 25, 26 and the conduits connecting them. At this time, the solenoid valves 43, 46, 47 are kept open, and the cleaning water is discharged through the solenoid valves 43, 47. After the cleaning water is completely drained, the pump 36 is driven to open the solenoid valve 44 and close the solenoid valves 43, 46, and 47, and a constant amount of standard solution of known concentration is supplied from the standard solution tank 34 to the liquid tank 24. At the same time, a certain amount of water is supplied to the liquid tank 25 from the water shower 40, and this state is maintained for a certain period of time. Then, since the liquid tanks 24 and 25 are separated by the anion exchange membrane 48, the acid concentration in the liquid tank 25 increases. After a certain period of time has elapsed, the solenoid valve 46 is opened and the liquid in the liquid tank 25 is transferred to the liquid tank 26, and the pump 37 is driven and the solenoid valve 45 is opened to supply a certain amount of diluent from the diluent tank 33 and dilute it. Stirrer 42
Fluorine ion selective electrode 27 while stirring
and an ion-selective electrode 28 (for example, a nitric acid ion electrode) that is selective for strong acid anions in the test solution.
Each concentration is detected by the reference electrode 29 that generates a voltage that serves as a reference for these two electrode potentials, and the voltmeter 3
0, the electromotive force is measured and stored in the calculation unit 31. When this measurement is completed, the electromagnetic valve 47 is opened and the liquid in the liquid tank 26 is discharged.
以上で標準液の濃度が測定されたことになり続
いて被検液の濃度測定を行う。 Now that the concentration of the standard solution has been measured, the concentration of the test solution is then measured.
まず水シヤワー38,39,40,41に水を
一定時間供給し液槽21、フイルター22、温度
調整器23、液槽24,25,26及びこれらを
結ぶ導管を洗浄する。このときポンプ35を駆動
するとともに電磁弁43,46,47を開いてお
き、洗浄水は電磁弁43,47を通して排出す
る。洗浄が一定時間続き洗浄水が完全に排出され
た後電磁弁43,46,47を閉じ図示していな
いサンプリング装置で被検液をサンプリングし、
液槽21に入れ、フイルター22、温度調整器2
3を通り、バルプ51及び52の開閉によつて液
槽24及び53に一定量供給する。これと同時に
水シヤワー40から液槽25に水を一定量供給す
る。後は前に説明した標準液の濃度測定と同じ方
法で濃度を検出し、演算部31にこの結果を入力
する。演算部31では、標準液を測定した時の電
圧をVs、被検液を測定した時の電圧をViとし
Ci=Cs×10Vs−Vi/K
Cs:標準液の濃度
Ci:被検液の濃度
K:係数
を計算する。なお係数Kは前もつて濃度のわかつ
ている混酸で実験により求めておく。一方液槽5
3に液比重計49を入れインターフエイス50を
通して演算部31にこの結果を入力する。演算部
31では液比重測定値をもとに、予め実験により
求めてある係数Kを利用し、
CFe=k×Sg
CFe:鉄イオン濃度
k:係数
Sg:液比重
を計算する。 First, water is supplied to the water showers 38, 39, 40, and 41 for a certain period of time to clean the liquid tank 21, the filter 22, the temperature regulator 23, the liquid tanks 24, 25, and 26, and the conduits connecting these. At this time, the pump 35 is driven and the solenoid valves 43, 46, 47 are kept open, and the cleaning water is discharged through the solenoid valves 43, 47. After the cleaning continues for a certain period of time and the cleaning water is completely discharged, the solenoid valves 43, 46, and 47 are closed, and the test liquid is sampled with a sampling device (not shown).
Put it in the liquid tank 21, filter 22, temperature regulator 2
3, and is supplied in fixed amounts to the liquid tanks 24 and 53 by opening and closing valves 51 and 52. At the same time, a certain amount of water is supplied from the water shower 40 to the liquid tank 25. After that, the concentration is detected by the same method as the concentration measurement of the standard solution described above, and this result is input to the calculation section 31. In the calculation unit 31, the voltage when the standard solution is measured is Vs , and the voltage when the test solution is measured is Vi , and Ci= Cs × 10Vs − Vi / Kcs : Concentration of the standard solution C i : Concentration of test liquid K: Calculate the coefficient. The coefficient K is determined by experiment using a mixed acid whose concentration is known in advance. On the other hand, liquid tank 5
3, a liquid hydrometer 49 is inserted, and the result is input to the calculation section 31 through the interface 50. The calculation unit 31 calculates the liquid specific gravity based on the liquid specific gravity measurement value, using a coefficient K determined in advance through experiments, as follows: C Fe =k×S g C Fe : iron ion concentration k : coefficient S g : liquid specific gravity.
さらにCFe、CHFをもとに予め実験によつて求
めてある係数k1を利用し
CF=k1×CFe
CF:鉄イオンと化合する弗素
k1:係数
CFe:鉄濃度
を計算し、CFとCiasHFからCTFを求める。これ
らの演算結果を表示部32で表示し、測定を全て
終了する。以上の流れをリレーシーケンス又はシ
ーケンサー又はマイクロコンピユーター等で制御
することにより自動的に混酸濃度、鉄イオン濃
度、全弗素イオン濃度の測定を行うことが出来
る。 Furthermore, using the coefficient k 1 which has been experimentally determined in advance based on C Fe and C HF , CF = k 1 ×C Fe CF : Fluorine that combines with iron ions k 1 : Coefficient C Fe : Iron concentration Calculate and find C TF from C F and C iasHF . The results of these calculations are displayed on the display section 32, and all measurements are completed. By controlling the above flow using a relay sequence, a sequencer, a microcomputer, etc., it is possible to automatically measure the mixed acid concentration, iron ion concentration, and total fluorine ion concentration.
以上述べたごとく、本発明方法により弗酸と硝
酸、硫酸、塩酸等の強酸との混酸を用いて金属材
料を酸洗する際に、酸濃度、鉄イオン濃度及び全
弗素イオン濃度を随時、正確にかつ迅速に測定出
来、弗酸の余分の消費を防ぐ混酸等の濃度管理を
的確に行うことが出来る。 As described above, when pickling metal materials using a mixed acid of hydrofluoric acid and strong acids such as nitric acid, sulfuric acid, and hydrochloric acid according to the method of the present invention, the acid concentration, iron ion concentration, and total fluorine ion concentration can be accurately determined at any time. It can be measured easily and quickly, and the concentration of mixed acids, etc. can be accurately controlled to prevent excess consumption of hydrofluoric acid.
第1図は鉄−弗素系の状態図、第2図は本発明
を行うための原理図、第3図は混酸比重−鉄イオ
ン濃度の関係図、第4図は鉄−弗酸系における鉄
−弗素錯体の状態図、第5図は本発明の一実施例
を示す装置の系統図である。
Figure 1 is a phase diagram of the iron-fluorine system, Figure 2 is a principle diagram for carrying out the present invention, Figure 3 is a relationship between mixed acid specific gravity and iron ion concentration, and Figure 4 is iron in the iron-fluorine system. - Phase diagram of fluorine complex; FIG. 5 is a system diagram of an apparatus showing an embodiment of the present invention.
Claims (1)
ン、強酸の陰イオン及び水素イオンを透析させ、
この透析液に弱酸と強塩基又は強酸と弱塩基の中
和によつて生じた塩溶液を加えて希釈したのち、
イオン選択性電極により弗素イオンおよび強酸の
陰イオン濃度を測定し、一方比重計により酸洗液
の比重を測定し、これらの測定値から弗酸、強
酸、鉄イオン、総弗素イオンの各濃度を求めるこ
とを特徴とする弗酸を含む酸洗液の濃度測定方
法。1 Dialyze fluorine ions, strong acid anions, and hydrogen ions in the pickling solution using an anion exchange membrane,
After diluting this dialysate by adding a salt solution generated by neutralizing a weak acid and a strong base or a strong acid and a weak base,
The fluorine ion and strong acid anion concentrations are measured using an ion-selective electrode, while the specific gravity of the pickling solution is measured using a hydrometer, and the concentrations of hydrofluoric acid, strong acid, iron ions, and total fluorine ions are determined from these measured values. A method for measuring the concentration of a pickling solution containing hydrofluoric acid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP657579A JPS5599062A (en) | 1979-01-25 | 1979-01-25 | Concentration measurement of pickling solution containing hydrofluoric acid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP657579A JPS5599062A (en) | 1979-01-25 | 1979-01-25 | Concentration measurement of pickling solution containing hydrofluoric acid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5599062A JPS5599062A (en) | 1980-07-28 |
| JPS6235059B2 true JPS6235059B2 (en) | 1987-07-30 |
Family
ID=11642121
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP657579A Granted JPS5599062A (en) | 1979-01-25 | 1979-01-25 | Concentration measurement of pickling solution containing hydrofluoric acid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5599062A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3413905A1 (en) * | 1984-04-13 | 1985-10-24 | Metallgesellschaft Ag, 6000 Frankfurt | METHOD FOR MONITORING FLUORIDE-CONTAINING BATHS FOR THE SURFACE TREATMENT OF METALS |
| JP5260446B2 (en) * | 2009-08-26 | 2013-08-14 | 株式会社クレハ環境 | Fluorine concentration automatic measuring method and fluorine concentration automatic measuring device |
-
1979
- 1979-01-25 JP JP657579A patent/JPS5599062A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5599062A (en) | 1980-07-28 |
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