JP2705813B2 - Activated carbon treatment method - Google Patents

Activated carbon treatment method

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Publication number
JP2705813B2
JP2705813B2 JP28258588A JP28258588A JP2705813B2 JP 2705813 B2 JP2705813 B2 JP 2705813B2 JP 28258588 A JP28258588 A JP 28258588A JP 28258588 A JP28258588 A JP 28258588A JP 2705813 B2 JP2705813 B2 JP 2705813B2
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JP
Japan
Prior art keywords
activated carbon
water
aqueous solution
treated
treating
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Expired - Fee Related
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JP28258588A
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Japanese (ja)
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JPH02131183A (en
Inventor
勇 堀口
勉 坂本
貞男 矢澤
守弘 蓮見
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Organo Corp
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Organo Corp
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Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は、地下水あるいは上水を活性炭濾過器で濾過
し、その濾過水を電解式塩素発生器で処理することによ
り、遊離塩素を含む水を製造する処理装置において、前
記活性炭濾過器に充填する活性炭の前処理方法に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION <Industrial application field> The present invention relates to water containing free chlorine by filtering groundwater or tap water with an activated carbon filter and treating the filtered water with an electrolytic chlorine generator. The present invention relates to a method for pre-treating activated carbon to be charged in the activated carbon filter in a processing apparatus for producing an activated carbon.

<従来の技術> 従来からたとえばコーヒー、紅茶、清涼飲料水等の自
動販売機においては、当該販売機内に、濾過手段、殺菌
手段、加熱およびまたは冷却手段、目的とする飲料の原
料を水に溶解する手段、あるいは炭酸溶解手段、カップ
等が内設されており、コインの投入と希望する飲料の選
択ボタンを押すことにより、前記各手段の働きにより希
望する飲料がカップに入り、取り出されるようになって
いる。
<Conventional technology> Conventionally, in vending machines for coffee, tea, soft drinks, etc., for example, filtration means, sterilization means, heating and / or cooling means, and raw materials of a desired beverage are dissolved in water in the vending machine. Means, or carbonic acid dissolving means, a cup, etc. are provided internally, and by pressing a coin and pressing the select button of the desired beverage, the desired beverage enters the cup by the action of each of the means and is taken out. Has become.

当該自動販売機には供給原水として飲料適である地下
水あるいは上水が用いられ、当該原水はまず前述した濾
過手段によって濾過される。
The vending machine uses groundwater or tap water suitable for drinking as supply raw water, and the raw water is first filtered by the above-mentioned filtering means.

濾過手段としては、粒状あるいは粉末状の活性炭を使
用する活性炭濾過器が用いられることが多く、当該濾過
器で原水を濾過することにより、原水中に含まれる懸濁
物、有機物、色度等の不純物が除去される。
As the filtering means, an activated carbon filter using granular or powdered activated carbon is often used. By filtering raw water with the filter, a suspension, organic matter, chromaticity, etc. contained in the raw water can be used. The impurities are removed.

また当該濾過水が自動販売機内に設置された水槽内
で、ある程度滞留するので、この滞留中に細菌が発生し
ないように、濾過器から流出した直後の濾過水は殺菌手
段により殺菌される。
In addition, since the filtered water stays to some extent in a water tank installed in the vending machine, the filtered water immediately after flowing out of the filter is sterilized by a sterilizing means so that bacteria are not generated during the stay.

当該殺菌手段としては、次亜塩素酸ソーダ溶液を注入
ポンプにて濾過水に注入するものもあるが、濾過水を電
解式塩素発生器で処理する方式も採用されている。
As the sterilizing means, there is a method in which a sodium hypochlorite solution is injected into filtered water by an injection pump, but a method of treating the filtered water with an electrolytic chlorine generator is also employed.

当該電解式塩素発生器は原水に含まれている塩化物イ
オンの一部を電解により遊離塩素とするものであり、原
水中に存在する塩化物の量に応じて、通電時間や電流を
あらかじめ決定し、遊離塩素が0.2ppm前後〜1ppm程度含
む水となすものである。
The electrolytic chlorine generator converts part of the chloride ions contained in the raw water into free chlorine by electrolysis, and determines the energization time and current in advance according to the amount of chloride present in the raw water. Water containing about 0.2 ppm to about 1 ppm of free chlorine.

一方前述した活性炭は新品のものをそのまま用いる
と、当初の濾過水のpHは10前後のアルカリ性となること
が知られており、当該pHの値が飲料不適となることか
ら、上述したような自動販売機に用いる場合は、従来か
ら塩酸で処理してから用いられていた。
On the other hand, if the above-mentioned activated carbon is used as it is, it is known that the pH of the initial filtered water becomes alkaline at around 10, and the pH value becomes unsuitable for beverages. When used in a vending machine, it has been used after being treated with hydrochloric acid.

当該塩酸処理は、新品の活性炭を塩酸の水溶液に浸漬
したり、あるいは活性炭充填層に塩酸の水溶液を通液し
た後、脱塩水で充分に洗浄する操作である。
The hydrochloric acid treatment is an operation in which new activated carbon is immersed in an aqueous solution of hydrochloric acid, or an aqueous solution of hydrochloric acid is passed through an activated carbon packed bed and then sufficiently washed with demineralized water.

このような塩酸処理を施した活性炭の場合は、これを
前記活性炭濾過器に用いてもその濾過水のpHが上昇し飲
料不適となることはない。
In the case of activated carbon subjected to such a hydrochloric acid treatment, even if the activated carbon is used in the activated carbon filter, the pH of the filtered water does not increase and the beverage is not unsuitable.

しかしながら自動販売機に用いられる殺菌手段が、前
述した電解式塩素発生器の場合は、上述した塩酸処理し
た活性炭を用いると以下のような不具合が生じることが
判明した。
However, when the sterilizing means used in the vending machine is the above-mentioned electrolytic chlorine generator, it has been found that the following problems occur when the above-mentioned activated carbon treated with activated carbon is used.

すなわちあらかじめ測定してある原水の塩化物イオン
の量に応じて、電解式塩素発生器の処理水の遊離塩素濃
度が0.2ppm前後から1ppm程度となるように、当該発生器
の通電時間や電流を調整し、原水を活性炭濾過器、次い
で電解式塩素発生器で処理すると、処理開始からしばら
くの間は処理水の遊離塩素濃度が異常に上昇し、甚だし
い塩素臭が発生する。
That is, depending on the amount of chloride ions in the raw water that has been measured in advance, the energizing time and current of the electrolytic chlorine generator are adjusted so that the free chlorine concentration in the treated water of the electrolytic chlorine generator becomes about 0.2 ppm to about 1 ppm. When the raw water is adjusted and treated with an activated carbon filter and then with an electrolytic chlorine generator, the concentration of free chlorine in the treated water rises abnormally for a while from the start of the treatment, and an extreme chlorine odor is generated.

当該活性炭濾過器と電解式塩素発生器が自動販売機に
組み込まれている場合は、前述の塩素臭が製品の飲料に
移行し、製品の価値を損なうので好ましくない。
When the activated carbon filter and the electrolytic chlorine generator are incorporated in a vending machine, the chlorine odor described above is transferred to the beverage of the product, which is not preferable because the value of the product is lost.

処理開始からしばらくの間、処理水の遊離塩素が異常
に上昇する原因を調査した結果、塩酸処理した活性炭で
原水を濾過すると濾過水の塩化物イオンが原水のそれよ
り大幅に増加するためと判明した。
After investigating the cause of the abnormal increase of free chlorine in treated water for a while from the start of treatment, it was found that filtering raw water with activated carbon treated with hydrochloric acid significantly increased the chloride ion of filtered water from that of raw water. did.

たとえば原水の塩化物イオンが30mg/の原水を塩酸
処理した活性炭で濾過すると、当初の濾過水の塩化物イ
オンは原水の全カチオン量によっても相違するが、時に
は200mg/にまで達し、次いで濾過処理を続行するにし
たがって徐々に低下してくるのである。
For example, if raw water containing 30 mg / chloride of raw water is filtered with activated carbon treated with hydrochloric acid, the chloride ion in the initial filtered water will vary depending on the total amount of cations in the raw water, but sometimes reaches up to 200 mg /. As it continues, it gradually decreases.

たとえば電解式塩素発生器を、原水塩化物イオン濃度
30mg/の時に遊離塩素発生量が0.2ppm前後〜1ppm程度
となるように調整した場合、塩化物イオンが200mg/に
増加した水を当該塩素発生器で処理した場合、遊離塩素
濃度は5ppm前後となる。
For example, using an electrolytic chlorine generator,
When the amount of generated free chlorine is adjusted to be about 0.2 ppm to about 1 ppm at the time of 30 mg /, when the water in which the chloride ion is increased to 200 mg / is treated with the chlorine generator, the free chlorine concentration is about 5 ppm. Become.

活性炭を塩酸処理する場合、塩酸処理後に洗浄廃水が
中性になるまで脱塩水で洗浄するが、このように充分に
洗浄した活性炭を使用するにもかかわらず、通水当初に
塩化物イオンの量が増加するのは、活性炭に少量の陰イ
オン交換基が存在しているためと考えられる。
When activated carbon is treated with hydrochloric acid, it is washed with demineralized water until the washing wastewater becomes neutral after the hydrochloric acid treatment. Is thought to be due to the presence of a small amount of anion exchange groups in the activated carbon.

すなわち塩酸処理することにより、当該陰イオン交換
基が塩化物イオン形となり、通水の当初に当該塩化物イ
オンが選択性の強い陰イオンに交換されることにより塩
化物イオンが増加し、また通水の続行により当該陰イオ
ン交換基が他のイオン形になるにしたがって、塩化物イ
オンの増加量が低下し、原水のイオン組成に平衡な点に
達した時点で活性炭濾過水の塩化物イオン量は原水のそ
れと等しくなる。
That is, the treatment with hydrochloric acid converts the anion exchange group into a chloride ion form, and the chloride ion is exchanged for a highly selective anion at the beginning of the flow of water, thereby increasing the chloride ion. As the anion exchange group becomes another ion form by the continuation of the water, the amount of increase in chloride ion decreases, and at the point when the ion composition of the raw water reaches an equilibrium point, the amount of chloride ion in the activated carbon filtered water Is equal to that of raw water.

したがって、このように変化する活性炭濾過水の塩化
物イオンの量に応じて電解式塩素発生器の通電時間や電
流を変化させれば、常に一定の遊離塩素を発生させるこ
とができるが、この操作は甚だしく煩雑であり、たとえ
ば無人運転である自動販売機の場合は、これを手動にて
行うのは不可能である。
Therefore, if the energization time and current of the electrolytic chlorine generator are changed in accordance with the amount of chloride ions in the activated carbon filtered water which changes in this manner, a constant free chlorine can always be generated. Is extremely complicated, for example, in the case of a vending machine which is operated unattended, it is impossible to do this manually.

なお、電解式塩素発生器に供給される水の塩化物イオ
ンを自動的に計測し、当該計測値に応じて通電時間や電
流を自動的に可変することも考えられるが、これに要す
るコストは甚大であって、実用化が困難である。
In addition, it is conceivable to automatically measure the chloride ion of the water supplied to the electrolytic chlorine generator and automatically vary the energization time and current according to the measured value, but the cost required for this is It is enormous and difficult to put to practical use.

<発明が解決しようとする問題点> 本発明は地下水あるいは上水を活性炭濾過器で濾過
し、その濾過水を電解式塩素発生器で処理することによ
り、遊離塩素を含む水を製造する処理装置における上述
した欠点を解決するもので、通水の当初から塩化物イオ
ンの量が増加することなく、かつpHが上昇しない濾過水
を得ることができる活性炭の処理方法を提供することを
目的とするものである。
<Problems to be Solved by the Invention> The present invention is a treatment apparatus for producing water containing free chlorine by filtering groundwater or tap water with an activated carbon filter and treating the filtered water with an electrolytic chlorine generator. It is an object of the present invention to provide a method for treating activated carbon that can obtain filtered water without increasing the amount of chloride ions from the beginning of passing water and without increasing pH, from the beginning of passing water. Things.

<問題点を解決するための手段> 本発明は、地下水あるいは上水を活性炭濾過器で濾過
し、その濾過水を電解式塩素発生器で処理することによ
り、遊離塩素を含む水を製造する処理装置において、前
記活性炭濾過器に用いる活性炭をあらかじめ、リン酸お
よび硫酸から選ばれる一種以上の酸の水溶液で処理する
ことを特徴とする活性炭の処理方法であり、また上述の
処理装置において、前記活性炭濾過器に用いる活性炭を
あらかじめ塩酸の水溶液で処理した後、次いでリン酸お
よび硫酸から選ばれる一種以上の酸あるいは塩の水溶液
で処理することを特徴とする活性炭の処理方法である。
<Means for Solving the Problems> The present invention provides a process for producing water containing free chlorine by filtering groundwater or clean water with an activated carbon filter and treating the filtered water with an electrolytic chlorine generator. In the apparatus, there is provided a method for treating activated carbon, wherein the activated carbon used in the activated carbon filter is previously treated with an aqueous solution of one or more acids selected from phosphoric acid and sulfuric acid. This is a method for treating activated carbon, wherein the activated carbon used in the filter is treated in advance with an aqueous solution of hydrochloric acid, and then treated with an aqueous solution of one or more acids or salts selected from phosphoric acid and sulfuric acid.

<作用> 活性炭を塩酸処理したままでは、前述したように活性
炭に少量存在する陰イオン交換基が塩化物イオン形とな
り、当該塩化物イオンが濾過処理中に当該交換基に対し
てより選択性の強い陰イオンと交換されることにより、
上述のような問題を生ずる。
<Action> When activated carbon is treated with hydrochloric acid, as described above, the anion exchange group present in a small amount in the activated carbon becomes a chloride ion form, and the chloride ion becomes more selective for the exchange group during the filtration treatment. By being exchanged for strong anions,
The above-described problem occurs.

したがって、本発明はこれを回避するため以下の二つ
の処理方法の内、いずれかを行う。
Therefore, the present invention performs one of the following two processing methods to avoid this.

その一つは、新品活性炭濾過水のpH上昇を防ぐための
酸洗浄として、従来の塩酸水溶液にかえて、リン酸水溶
液、硫酸水溶液あるいはリン酸と硫酸の混合水溶液を用
いるものである。
One of them is to use a phosphoric acid aqueous solution, a sulfuric acid aqueous solution or a mixed aqueous solution of phosphoric acid and sulfuric acid instead of the conventional hydrochloric acid aqueous solution as an acid washing for preventing a pH rise of the new activated carbon filtered water.

すなわち上述した酸水溶液で洗浄することにより、活
性炭に存在する陰イオン交換基を塩化物イオン形とする
ことなく、リン酸型およびまたは硫酸形とすることがで
き、これによって通水初期における濾過水の塩化物イオ
ンの増加を確実に回避し得る。
That is, by washing with the above-mentioned acid aqueous solution, the anion exchange group present in the activated carbon can be converted into a phosphoric acid type and / or a sulfuric acid type without being converted into a chloride ion type. Can be reliably prevented from increasing.

なお上記陰イオン交換基に対するリン酸イオンあるい
は硫酸イオンの選択性は、塩化物イオンよりかなり強い
ので、上記処理後の活性炭で原水を濾過しても原水中の
塩化物イオンがほとんどイオン交換されることはなく、
したがって濾過水中の塩化物イオン量は原水のそれとほ
ぼ同じ値となる。
Since the selectivity of phosphate ions or sulfate ions to the anion exchange groups is considerably stronger than chloride ions, even if raw water is filtered with activated carbon after the above treatment, chloride ions in the raw water are almost ion-exchanged. Never
Therefore, the amount of chloride ions in the filtered water is almost the same as that of the raw water.

なお新品の活性炭をリン酸あるいは硫酸水溶液で処理
する場合、当該水溶液の濃度としては1〜2%程度のも
のを用い、活性炭容量に対して、2倍量程度の液量を用
いれば充分である。
When a new activated carbon is treated with an aqueous solution of phosphoric acid or sulfuric acid, a concentration of the aqueous solution of about 1 to 2% is used, and it is sufficient to use about twice the amount of the activated carbon volume. .

また当該酸水溶液を活性炭に接触させる場合、当該酸
水溶液に活性炭を浸漬してもよいし、活性炭充填層に当
該酸水溶液を通液してもよい。なお上記浸漬あるいは通
液した後、活性炭を脱塩水等の清澄水で充分に洗浄す
る。
When the acid aqueous solution is brought into contact with activated carbon, the activated carbon may be immersed in the acid aqueous solution, or the acid aqueous solution may be passed through the activated carbon packed bed. After the immersion or the passage, the activated carbon is sufficiently washed with clear water such as demineralized water.

他の一つは新品活性炭のpH上昇を防ぐための酸洗浄と
しては従来のように塩酸水溶液を用いるが、次いで以下
の処理を行うものである。
The other is to use an aqueous hydrochloric acid solution as in the prior art for acid washing for preventing the pH of new activated carbon from rising, and then performing the following treatment.

すなわち塩酸水溶液で活性炭を処理すると、前述した
ごとく陰イオン交換基が塩化物イオン形となるが、次い
で当該塩酸処理後の活性炭をリン酸水溶液、硫酸水溶
液、リン酸と硫酸の混合水溶液あるいは、リン酸塩水溶
液、硫酸塩水溶液、リン酸塩と硫酸塩の水溶液で処理す
るものである。
That is, when activated carbon is treated with an aqueous solution of hydrochloric acid, the anion exchange group is converted into a chloride ion form as described above. Treatment with an aqueous solution of an acid salt, an aqueous solution of a sulfate, or an aqueous solution of a phosphate and a sulfate.

なおリン酸塩、硫酸塩としては、ナトリウム塩、カリ
ウム塩等の水に対する溶解度の大きい塩を用いる。
As the phosphate and sulfate, salts having high solubility in water, such as sodium salt and potassium salt, are used.

このように塩酸処理後に、リン酸またはその塩あるい
は硫酸またはその塩で処理することにより、活性炭中の
塩化物イオン形の交換基をリン酸形およびまたは硫酸形
に置換することができるので、前述したと同様な効果を
達成する。
By treating with a phosphoric acid or a salt thereof or a sulfuric acid or a salt thereof after the hydrochloric acid treatment as described above, the exchange group of the chloride ion form in the activated carbon can be replaced with a phosphoric acid form and / or a sulfuric acid form. Achieve the same effect as you did.

なお本処理におけるリン酸またはその塩あるいは硫酸
またはその塩の濃度および使用量、活性炭との接触の手
法は前述したのと同様に行うとよい。
In this treatment, the concentration and amount of phosphoric acid or its salt or sulfuric acid or its salt, and the method of contacting with activated carbon may be performed in the same manner as described above.

<効果> 以上説明したごとく、本発明によれば活性炭の有する
陰イオン交換基が塩化物イオン形とならず、リン酸形お
よびまたは硫酸形となるので、通水初期に活性炭濾過水
に塩化物イオンが多量に増加するということを確実に回
避できる。またリン酸形およびまたは硫酸形の交換基は
比較的安定であり、当該イオン形となっている活性炭に
原水を通水しても原水中の塩化物イオンが交換されるこ
とがほとんどなく、したがって濾過水中の塩化物イオン
の量は、通水の初期からほとんど原水のそれと同じ値と
なる。
<Effects> As described above, according to the present invention, the anion exchange group of the activated carbon is not in the chloride ion form, but in the phosphoric acid form or the sulfuric acid form. A large increase in ions can be reliably avoided. In addition, the phosphate group and / or sulfate group exchange group is relatively stable, and even if the raw water is passed through the activated carbon in the ionic form, the chloride ion in the raw water is hardly exchanged. The amount of chloride ions in the filtered water has almost the same value as that of the raw water from the beginning of passing water.

よって本発明の処理を施した活性炭を用いた濾過器の
濾過水を、原水の塩化物イオン量に対応して通電時間や
電流をあらかじめ決定してある電解式塩素発生器に供給
しても、遊離塩素濃度が異常に増加したり、あるいは異
常に低下した電解処理水となることはない。
Therefore, even if the filtered water of the filter using the activated carbon subjected to the treatment of the present invention is supplied to an electrolytic chlorine generator having a predetermined energizing time and current corresponding to the amount of chloride ions in the raw water, The concentration of free chlorine does not increase abnormally or the electrolytically treated water does not decrease abnormally.

なお上述したごとく本発明の処理を施した活性炭を用
いた場合、その濾過水の塩化物イオン量は原水のそれと
ほぼ同じ値となるので、電解式塩素発生器の通電時間や
電流の調整は、原水の塩化物イオン量に応じて調整すれ
ばよく、当該発生器に特別な操作が加わることがなく、
たとえば自動販売機の場合は、その機内の構造を全く変
更する必要がない。
In addition, as described above, when using the activated carbon that has been subjected to the treatment of the present invention, the amount of chloride ions in the filtered water is substantially the same as that of the raw water. It may be adjusted according to the amount of chloride ions in the raw water, and no special operation is added to the generator.
For example, in the case of a vending machine, there is no need to change the structure inside the machine at all.

また本発明の処理を施した活性炭の濾過水のpHは、ア
ルカリ性とならないことは言うまでもない。
Needless to say, the pH of the filtered water of the activated carbon subjected to the treatment of the present invention does not become alkaline.

以下に本発明の効果を明確とするために実施例を説明
する。
Examples will be described below to clarify the effects of the present invention.

実施例 市販の粒状活性炭(新品)0.8を1%のリン酸水溶
液1.6中に浸漬し、約60分間時々撹拌しながら放置し
た。次いで上澄液を捨て、処理活性炭を3.2の50℃の
脱塩水に約30分間浸漬し、その上澄水を捨て、再び同様
にして温脱塩水で洗浄する操作を5回程度繰り返して、
活性炭を充分に洗浄した。
Example 0.8 Commercially available granular activated carbon (new) 0.8 was immersed in a 1% aqueous phosphoric acid solution 1.6 and left for about 60 minutes with occasional stirring. Next, the supernatant was discarded, and the treated activated carbon was immersed in demineralized water at 50 ° C. of 3.2 for about 30 minutes, the supernatant was discarded, and the operation of washing again with warm demineralized water was repeated about 5 times.
The activated carbon was thoroughly washed.

上述の処理をした活性炭を濾過器に充填し、pH7.3、
電気伝導率約290μs/cm、炭酸水素イオン34ppm(CaC
O3)、硝酸イオン6ppm(CaCO3)、硫酸イオン49ppm(Ca
CO3)、塩化物イオン41ppm(CaCO3)、全カチオン130pp
m(CaCO3)の上水を通水した結果、活性炭濾過水の塩化
物イオンは通水直後から40ppm(CaCO3)前後であり、入
口水の塩化物イオン量とほぼ同じであった。また濾過水
のpHも通水直後から7.0前後であり、濾過水のpHがアル
カリ性を示すことがなかった。
Fill the filter with the activated carbon treated above, pH 7.3,
Electric conductivity about 290μs / cm, hydrogen carbonate ion 34ppm (CaC
O 3 ), nitrate ion 6 ppm (CaCO 3 ), sulfate ion 49 ppm (Ca
CO 3 ), chloride ion 41ppm (CaCO 3 ), total cation 130pp
As a result of passing the m (CaCO 3 ) clean water, the chloride ion in the activated carbon filtered water was about 40 ppm (CaCO 3 ) immediately after the passage, which was almost the same as the chloride ion amount in the inlet water. Further, the pH of the filtered water was around 7.0 immediately after the passage, and the pH of the filtered water did not show alkalinity.

なお、1%のリン酸水溶液に代えて、1%の硫酸水溶
液あるいは全酸濃度が1%のリン酸と硫酸の混合水溶液
を用いて、他は同じ操作で洗浄した場合も、ほぼ同様な
結果となった。
In addition, almost the same result is obtained when the 1% sulfuric acid aqueous solution or a mixed aqueous solution of phosphoric acid and sulfuric acid having a total acid concentration of 1% is used instead of the 1% phosphoric acid aqueous solution, and the other steps are performed by the same operation. It became.

また同じ粒状活性炭0.8を1%の塩酸水溶液1.6中
に浸漬し、約60分間時々撹拌しながら放置し、塩酸を充
分に洗浄した後、同様にして1%のリン酸水溶液、リン
酸ナトリウム水溶液、硫酸水溶液、硫酸ナトリウム水溶
液、それぞれ1.6中に浸漬し、約60分間時々撹拌しな
がら放置し、以後は前述と同じ条件で温脱塩水で洗浄し
た活性炭を用いた場合も、活性炭濾過水の塩化物イオン
はそれぞれ通水直後から40ppm(CaCO3)前後であり、入
口水の塩化物イオン量とほぼ同じであり、pHも7.0前後
であった。
Further, the same granular activated carbon 0.8 is immersed in a 1% hydrochloric acid aqueous solution 1.6, and left for about 60 minutes with occasional stirring to sufficiently wash the hydrochloric acid. Similarly, a 1% phosphoric acid aqueous solution, a sodium phosphate aqueous solution, Sulfuric acid aqueous solution, sodium sulfate aqueous solution, immersed in 1.6 each, and left with occasional stirring for about 60 minutes, after that, using activated carbon washed with warm demineralized water under the same conditions as above The ions were around 40 ppm (CaCO 3 ) immediately after passing water, respectively, almost the same as the chloride ion amount in the inlet water, and the pH was around 7.0.

一方比較のために、従来方法として同じ粒状活性炭0.
8を1%の塩酸水溶液1.6中に浸漬し、約60分間時々
撹拌しながら放置し、次いで上澄液を捨て、処理活性炭
を3.2の50℃の脱塩水に約30分間浸漬し、その上澄水
を捨て、再び同様にして温脱塩水で洗浄する操作を5回
程度繰り返して処理した活性炭を濾過器に充填し、同じ
市水を通水したところ、活性炭濾過水の塩化物イオンは
通水直後で100ppm(CaCO3)となり、以後通水時間に応
じて塩化物イオン量が徐々に低下する現象が見られた。
On the other hand, for comparison, the same granular activated carbon as the conventional method was used.
8 was immersed in 1% hydrochloric acid aqueous solution 1.6 and left for about 60 minutes with occasional stirring. Then, the supernatant was discarded, and the treated activated carbon was immersed in 3.2% demineralized water at 50 ° C. for about 30 minutes. The activated carbon treated by repeating the operation of washing with warm demineralized water about 5 times in the same manner was filled in the filter and the same city water was passed through. At 100 ppm (CaCO 3 ), and thereafter, a phenomenon was observed in which the amount of chloride ions gradually decreased with the passage of water.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】地下水あるいは上水を活性炭濾過器で濾過
し、その濾過水を電解式塩素発生器で処理することによ
り、遊離塩素を含む水を製造する処理装置において、前
記活性炭濾過器に用いる活性炭をあらかじめリン酸およ
び硫酸から選ばれる一種以上の酸の水溶液で処理するこ
とを特徴とする活性炭の処理方法。
1. A treatment apparatus for producing water containing free chlorine by filtering ground water or tap water with an activated carbon filter and treating the filtered water with an electrolytic chlorine generator. A method for treating activated carbon, wherein the activated carbon is previously treated with an aqueous solution of one or more acids selected from phosphoric acid and sulfuric acid.
【請求項2】地下水あるいは上水を活性炭濾過器で濾過
し、その濾過水を電解式塩素発生器で処理することによ
り、遊離塩素を含む水を製造する処理装置において、前
記活性炭濾過器に用いる活性炭をあらかじめ塩酸の水溶
液で処理した後、次いでリン酸および硫酸から選ばれる
一種以上の酸あるいは塩の水溶液で処理することを特徴
とする活性炭の処理方法。
2. A treatment apparatus for producing water containing free chlorine by filtering ground water or tap water with an activated carbon filter and treating the filtered water with an electrolytic chlorine generator. A method for treating activated carbon, wherein the activated carbon is treated in advance with an aqueous solution of hydrochloric acid, and then treated with an aqueous solution of one or more acids or salts selected from phosphoric acid and sulfuric acid.
JP28258588A 1988-11-10 1988-11-10 Activated carbon treatment method Expired - Fee Related JP2705813B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28258588A JP2705813B2 (en) 1988-11-10 1988-11-10 Activated carbon treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28258588A JP2705813B2 (en) 1988-11-10 1988-11-10 Activated carbon treatment method

Publications (2)

Publication Number Publication Date
JPH02131183A JPH02131183A (en) 1990-05-18
JP2705813B2 true JP2705813B2 (en) 1998-01-28

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Country Link
JP (1) JP2705813B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0458560B1 (en) * 1990-05-21 1994-10-26 Ishikawajima-Harima Jukogyo Kabushiki Kaisha Heat protection element
JP2002113313A (en) * 2000-10-10 2002-04-16 Sanyo Electric Co Ltd Filter
JP2002113312A (en) * 2000-10-10 2002-04-16 Sanyo Electric Co Ltd Water purification filter media
JP4541042B2 (en) * 2004-06-15 2010-09-08 日本エンバイロケミカルズ株式会社 Powdered activated carbon for water treatment and method for producing the same
JP4585436B2 (en) * 2005-12-02 2010-11-24 カーボンテック株式会社 Method for adjusting pH of activated carbon
TW200732253A (en) * 2006-02-10 2007-09-01 Japan Enviro Chemicals Ltd Absorbent for liquid phase treatment and process for producing the same
JP2007237169A (en) * 2006-02-10 2007-09-20 Japan Enviro Chemicals Ltd Adsorbent for treating liquid phase and its manufacturing method

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