JPS61174990A - Water treatment - Google Patents
Water treatmentInfo
- Publication number
- JPS61174990A JPS61174990A JP1402985A JP1402985A JPS61174990A JP S61174990 A JPS61174990 A JP S61174990A JP 1402985 A JP1402985 A JP 1402985A JP 1402985 A JP1402985 A JP 1402985A JP S61174990 A JPS61174990 A JP S61174990A
- Authority
- JP
- Japan
- Prior art keywords
- water
- edta
- treatment
- scales
- deposition
- 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.)
- Pending
Links
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は用水特に水道水の脱色用水処理方法に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a water treatment method for decolorizing municipal water, particularly tap water.
[従来の技術]
用水の色に関するも規定とて、我が国においては飲料用
水においては、水道法用4条に、外観無色。工業用水に
おいては、色度20〜70と定められている。水道水と
なる原水の質は地域により大きく異なり、その脱色方法
としては化学的酸化、活性炭吸着、生物的酸化等が行な
われている。そして化学的酸化方法には、水道水への添
加が許可されている代表的な水処理剤としてリン酸塩系
の薬剤と、ケイ酸塩系の薬剤がある。又非飲料水系には
亜硝酸塩系の薬剤が使われている。[Prior Art] Regarding the color of drinking water, in Japan, Article 4 of the Water Supply Law stipulates that drinking water should be colorless in appearance. For industrial water, the chromaticity is defined as 20-70. The quality of the raw water that becomes tap water varies greatly depending on the region, and methods for decolorizing it include chemical oxidation, activated carbon adsorption, and biological oxidation. Regarding chemical oxidation methods, there are phosphate-based agents and silicate-based agents as typical water treatment agents that are permitted to be added to tap water. Nitrite-based chemicals are also used in non-potable water systems.
[発明が解決しようとする問題点]
しかるに従来の方法は、活性炭吸着、生物的酸化の三方
法とも高額な設備と運転経費を用し、最も経済的な化学
的酸化方法では、水処理剤としてのリン酸塩系の薬剤は
、硬度成分の少ない水質では効果が期待できなかったり
、ケイI[系の薬剤は微量添加では効果が少なく、多量
添加では配管にスウールの堆積をまねく等の問題点をも
っていた。[Problems to be solved by the invention] However, all three conventional methods, activated carbon adsorption and biological oxidation, require expensive equipment and operating costs, and the most economical chemical oxidation method does not work well as a water treatment agent. Phosphate-based chemicals have problems such as not being expected to be effective in water with low hardness components, and Kei I-based chemicals having little effect when added in small amounts, and causing swool to accumulate in pipes when added in large amounts. had.
したがってこれらの薬剤を水処理剤として使用する場合
は、水中の高度成分、スケール成分の管内堆積を防止す
るため、特に熱交換器においては伝熱性の低下を防ぐた
め管内の薬剤による洗浄や機械的な清掃を行う必要があ
り、それは又配管材料の損耗や排水処理によるコスト増
をまねいていた。Therefore, when using these chemicals as water treatment agents, cleaning the pipes with chemicals or mechanical treatment is necessary to prevent the accumulation of high-grade components and scale components in the water, especially in heat exchangers, to prevent a decrease in heat transfer. It is necessary to perform extensive cleaning, which also leads to increased costs due to wear and tear on piping materials and wastewater treatment.
本発明の目的は前記した従来技術の欠点を解消し処理経
費が少なくて済み、脱色効果が優れ、スケール堆積の心
配のない水処理方法を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a water treatment method that eliminates the drawbacks of the prior art described above, requires less treatment cost, has an excellent decolorizing effect, and is free from scale deposition.
[問題点を解決するための手段」
本発明の要旨は、用水中の金属イオン封鎖剤すなわち着
色防止剤として、エチレンジアミン四酢酸(以下EDT
Aという)又はその誘導体の薬剤を使用することにある
。[Means for Solving the Problems] The gist of the present invention is to use ethylenediaminetetraacetic acid (hereinafter referred to as EDT) as a metal ion sequestering agent, that is, a coloring preventive agent in service water.
A) or its derivatives.
即ち、用水の水処理方法において、金属イオンを含む用
水にエチレンジアミン四酢酸、又はその誘導体の薬剤を
使用することを特徴とする水処理方法であり、該薬剤の
使用量は用水1Jlに対して1u〜1.00010が効
果的であり、用水としては特に水道用水に於いて効果的
である。That is, the water treatment method is characterized by using a chemical such as ethylenediaminetetraacetic acid or its derivatives in the water containing metal ions, and the amount of the chemical used is 1 u per 1 Jl of the water. ~1.00010 is effective, and is particularly effective for tap water.
EDTAの誘導体として下記の薬剤がある。The following drugs are derivatives of EDTA.
エチレンジアミン四酢酸ナトリウム塩(EDTA−2N
a)、エチレンジアミン四酢酸カリウム塩(EDTA−
2K)、エチレンジアミン四酢酸カルシウム塩(EDT
A−2Ca)、エチレンジアミン四酢酸マグネシウムm
(EDTA−2Mg>等のEDTΔ金属塩。Ethylenediaminetetraacetic acid sodium salt (EDTA-2N
a), ethylenediaminetetraacetic acid potassium salt (EDTA-
2K), ethylenediaminetetraacetic acid calcium salt (EDT
A-2Ca), magnesium ethylenediaminetetraacetate m
(EDTA-2Mg> and other EDTΔ metal salts.
[作 用]
本発明に使用するEDTAは用水中のほとんどの金属イ
オンと反応し、安定なキレート化合物を形成する。この
キレート化合物は水に対する溶解度が非常に高く、用水
は脱色される。EDTAの構造式は
EDTAと金属イオンM2+どの反応は下記のとおり、
+
(EDTA)’ −+M2 M (EDTA)2−そ
の時の安定度定数には次式で与えられる金属キレート安
定度定数を表1に示す。[Function] EDTA used in the present invention reacts with most metal ions in water to form a stable chelate compound. This chelate compound has very high solubility in water and decolorizes water. The structural formula of EDTA is EDTA and metal ion M2+ Which reaction is as follows: + (EDTA)' - + M2 M (EDTA)2 - The stability constant at that time is the metal chelate stability constant given by the following formula. Table 1 Shown below.
表 −1
この様に全ての金属イオンと安定な化合物を作り水の着
色を防止する事がわかる。同様にEDTAの誘導体であ
る薬剤も同様の効果を示す。Table 1 In this way, it can be seen that stable compounds are created with all metal ions and water coloring is prevented. Similarly, drugs that are derivatives of EDTA exhibit similar effects.
し実施例]
(1) 深さ1mの白色の容器にF e3 + 、
Cu2 +’IrNN水をPH10にしそれぞれ1.2
,4.6゜B、10(llo/J)添加したもの中に、
その着色が消えるのに必要なEDTAの添加量1g/l
を求めた、第1図にその結果を示す。Example] (1) Fe3 + in a white container with a depth of 1 m,
Cu2 + 'IrNN water to pH 10 and 1.2 each
, 4.6°B, 10 (llo/J) was added,
The amount of EDTA added is 1 g/l necessary to eliminate the coloring.
The results are shown in Figure 1.
金属イオン1o/Jの場合EDTAは2〜5mg/l必
要となる金属イオンが1oppi+に程度になった場合
EDTAは40〜50 on必要であることを示した。It was shown that in the case of metal ions of 1 o/J, 2 to 5 mg/l of EDTA is required, but when the metal ions are about 1 oppi+, 40 to 50 on of EDTA is required.
なお、金属イオン濃度が1l1+II/J!程度の場合
、水の着色は通常感知できないが、アルカリ性成分であ
る洗剤が混入すると1l1l0/Jlの金属イオンでも
水酸化物を形成して肉眼でも色を感知することが出来る
本実験はこの点も加味し蒸留水をPH10とした。In addition, the metal ion concentration is 1l1+II/J! Normally, the coloration of water cannot be detected, but when detergent, which is an alkaline ingredient, is mixed in, even metal ions of 1l1l0/Jl form hydroxides, and the color can be detected with the naked eye.This experiment also shows this point. The pH of the distilled water was adjusted to 10.
■ Ca2+を50 ppn+含む水道水を鋼管の密閉
回路で循環させ、鋼管を外部から温水で加熱し、銅管内
部にCaを含むスケールが形成されやすい環境にしてお
く、この水道水にEDTAの無添加。■ Tap water containing 50 ppn+ of Ca2+ is circulated in a closed circuit of steel pipes, and the steel pipes are heated with hot water from the outside to create an environment where scale containing Ca is easily formed inside the copper pipes.This tap water is free of EDTA. Addition.
25.50,100,200.300 <llQ/I!
)のEDTAを添加したものの30日後の管内スケー
ル量を測定比較してみた。この場合の実験条件として、
鋼管サイズ外径15.88.厚さ0.7履、長さ500
履、管内平均流速0.5m/秒。25.50,100,200.300 <llQ/I!
) was measured and compared for the amount of scale in the tubes after 30 days with the addition of EDTA. In this case, the experimental conditions are:
Steel pipe size outer diameter 15.88. Thickness 0.7, length 500
Average flow velocity in the pipe is 0.5 m/sec.
加熱用温水温度60℃、PH7,5であった。第2図に
その結果を示す。EDTA無添加の条件では管内面積1
C12に200+noのスケールが付着したのに対し、
E D TA 300mg/Ilの添加ではスケールの
発生は皆無。そして、25+++o/Ilの添加でもス
ケール発生は半分以下となっている。この効果はEDT
Aが温度の高い条件下では鋼管内面に吸着し皮膜状とな
り、金属と無機系物質との直接の接触を妨げるインヒビ
ータとしての特性をもつことによる効果である。The temperature of the hot water for heating was 60°C, and the pH was 7.5. Figure 2 shows the results. Under conditions without EDTA, the inner tube area is 1
While 200+no scale was attached to C12,
No scale was generated when 300 mg/Il of EDTA was added. Even with the addition of 25+++o/Il, the scale generation was reduced to less than half. This effect is EDT
This effect is due to the fact that A adsorbs to the inner surface of the steel pipe under high temperature conditions and forms a film, which acts as an inhibitor that prevents direct contact between the metal and the inorganic substance.
[発明の効果J
本発明によれば、用水にEDTAを適用添加することだ
けにより、用水の着色の原因である用水中の金属イオン
が速やかにEDTAとキレート化合物を形成して脱色を
する。非常に経済的な方法である。尚、スケールの堆積
の心配がある熱交換器においてはEDTAを含んだ用水
を加熱することにより脱色のみならず又容易にスケール
堆積防止の効果も伴わせて得られる。[Effect of the Invention J According to the present invention, by simply adding EDTA to the water, the metal ions in the water, which are the cause of coloring the water, quickly form a chelate compound with EDTA to decolorize the water. This is a very economical method. In addition, in a heat exchanger where there is a concern about scale accumulation, by heating service water containing EDTA, not only decolorization but also the effect of preventing scale accumulation can be easily obtained.
第1図は金属イオン濃度に対する脱色に必要なEDTA
の濃度との関係を示す1実施例の図、第2図はEDTA
の濃度とスケール付着量の関係を示す1実施例の図であ
る。
第 1 目
児 2 口
EDTA不加f気>/。Figure 1 shows the EDTA required for decolorization depending on the metal ion concentration.
A diagram of one example showing the relationship with the concentration of EDTA.
FIG. 2 is a diagram of one example showing the relationship between the concentration of and the amount of scale deposited. 1st child: 2 mouths of EDTA not added>/.
Claims (3)
水にエチレンジアミン四酢酸、又はその誘導体の薬剤を
使用することを特徴とする水処理方法。(1) A water treatment method for industrial water, characterized in that a chemical agent such as ethylenediaminetetraacetic acid or a derivative thereof is used in water containing metal ions.
の使用量が、用水1lに対して1mg以上1,000m
g以下である特許請求の範囲第1項記載の水処理方法。(2) The amount of ethylenediaminetetraacetic acid or its derivatives used is 1 mg or more per 1 liter of water for 1,000 m
The water treatment method according to claim 1, wherein the water treatment amount is less than or equal to g.
第2項記載の水処理方法。(3) The water treatment method according to claims 1 and 2, wherein the water used is tap water.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1402985A JPS61174990A (en) | 1985-01-28 | 1985-01-28 | Water treatment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1402985A JPS61174990A (en) | 1985-01-28 | 1985-01-28 | Water treatment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61174990A true JPS61174990A (en) | 1986-08-06 |
Family
ID=11849734
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1402985A Pending JPS61174990A (en) | 1985-01-28 | 1985-01-28 | Water treatment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61174990A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4980077A (en) * | 1989-06-22 | 1990-12-25 | Mobil Oil Corporation | Method for removing alkaline sulfate scale |
US5084105A (en) * | 1989-04-03 | 1992-01-28 | Mobil Oil Corporation | Sulfate scale dissolution |
US5093020A (en) * | 1989-04-03 | 1992-03-03 | Mobil Oil Corporation | Method for removing an alkaline earth metal sulfate scale |
JPH04104032U (en) * | 1991-02-14 | 1992-09-08 | 関東自動車工業株式会社 | vehicle drink container holder |
US5200117A (en) * | 1989-04-03 | 1993-04-06 | Mobil Oil Corporation | Sulfate scale dissolution |
-
1985
- 1985-01-28 JP JP1402985A patent/JPS61174990A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5084105A (en) * | 1989-04-03 | 1992-01-28 | Mobil Oil Corporation | Sulfate scale dissolution |
US5093020A (en) * | 1989-04-03 | 1992-03-03 | Mobil Oil Corporation | Method for removing an alkaline earth metal sulfate scale |
US5200117A (en) * | 1989-04-03 | 1993-04-06 | Mobil Oil Corporation | Sulfate scale dissolution |
US4980077A (en) * | 1989-06-22 | 1990-12-25 | Mobil Oil Corporation | Method for removing alkaline sulfate scale |
JPH04104032U (en) * | 1991-02-14 | 1992-09-08 | 関東自動車工業株式会社 | vehicle drink container holder |
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