JP4272586B2 - Activated carbon for water treatment - Google Patents
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- JP4272586B2 JP4272586B2 JP2004150163A JP2004150163A JP4272586B2 JP 4272586 B2 JP4272586 B2 JP 4272586B2 JP 2004150163 A JP2004150163 A JP 2004150163A JP 2004150163 A JP2004150163 A JP 2004150163A JP 4272586 B2 JP4272586 B2 JP 4272586B2
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- water treatment
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims description 226
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 139
- 239000002253 acid Substances 0.000 claims description 48
- 238000001035 drying Methods 0.000 claims description 22
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 18
- 238000005406 washing Methods 0.000 claims description 18
- 230000000717 retained effect Effects 0.000 claims description 11
- 230000003472 neutralizing effect Effects 0.000 claims description 5
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims 2
- 239000003513 alkali Substances 0.000 description 9
- 238000004140 cleaning Methods 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 7
- 238000010979 pH adjustment Methods 0.000 description 7
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000002384 drinking water standard Substances 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 4
- 238000006386 neutralization reaction Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000001139 pH measurement Methods 0.000 description 3
- OKTJSMMVPCPJKN-NJFSPNSNSA-N Carbon-14 Chemical class [14C] OKTJSMMVPCPJKN-NJFSPNSNSA-N 0.000 description 2
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000003651 drinking water Substances 0.000 description 2
- 235000020188 drinking water Nutrition 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000001678 irradiating effect Effects 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 238000004506 ultrasonic cleaning Methods 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 229910000272 alkali metal oxide Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 1
- 235000017557 sodium bicarbonate Nutrition 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Water Treatment By Sorption (AREA)
Description
本発明は、水処理用活性炭に関する。さらに詳しくは、本発明は、特定の方法によりpHを調整した水処理用活性炭に関する。 The present invention relates to activated carbon for water treatment. More specifically, the present invention relates to activated carbon for water treatment whose pH is adjusted by a specific method.
活性炭は、炭化物を賦活して得られるが、製造直後の活性炭はアルカリ金属の酸化物が多く含まれており、これを例えばJIS K1474によりpHを測定すると、アルカリ性となる。このため、水処理工程においてこれらの活性炭を使用すると、処理水のpHはアルカリ性を示すようになり、飲料水としては適さなくなる。また、同様に工業用途で用いる場合や廃水処理に用いる場合にも、アルカリ性の処理水では、用途に適さなくなる場合も生じる。 Activated carbon is obtained by activating carbide, but activated carbon immediately after production contains a large amount of alkali metal oxides, and becomes alkaline when the pH is measured, for example, according to JIS K1474. For this reason, when these activated carbons are used in the water treatment step, the pH of the treated water becomes alkaline, which makes it unsuitable as drinking water. Similarly, when used for industrial purposes or for wastewater treatment, alkaline treated water may not be suitable for use.
このため、一般的には、製造された活性炭を酸で洗浄し、活性炭の持つアルカリ成分を中和して活性炭のpHを中性領域まで低くした後、それぞれの工程に用いている。ここで、酸により洗浄した後、通常は、水による洗浄を経て、pH調整活性炭として各種工程に用いられることとなる。 For this reason, generally, the activated carbon produced is washed with an acid, and the alkaline component of the activated carbon is neutralized to lower the pH of the activated carbon to a neutral region, and then used for each step. Here, after washing with acid, usually, washing with water is used as various pH adjustment activated carbons.
ここで、上水場の活性炭吸着池に用いるpH調整活性炭の納品規格は、pH5.8〜8.6(JIS K1474またはJWWA K113)の場合が多い。 Here, the delivery standard of the pH-adjusted activated carbon used in the activated carbon adsorption pond in the water supply field is often pH 5.8 to 8.6 (JIS K1474 or JWWA K113).
そして、pHの測定方法としては、例えばJIS K1747に規定されており、その概略を示すと以下のようになる(非特許文献1参照)。 And as a measuring method of pH, it is prescribed | regulated, for example to JISK1747, and it will become as follows when the outline is shown (refer nonpatent literature 1).
(a)試料を乾燥質量換算し、粉末試料では1.0g、粒状試料では3.0gを量り取り、三角フラスコ200mlに移し入れる。
(b)水100mlを加えて、静かに沸騰が続くように5分間加熱する。
(c)室温まで冷却後、水を加えて100mlとし、よくかき混ぜ、pH計を用いて懸濁液のpH値を測定する。
(A) Convert the sample to dry mass, weigh 1.0 g for the powder sample and 3.0 g for the granular sample, and transfer to a 200 ml Erlenmeyer flask.
(B) Add 100 ml of water and heat for 5 minutes so that boiling continues gently.
(C) After cooling to room temperature, add water to make 100 ml, stir well, and measure the pH value of the suspension using a pH meter.
ここで、乾燥質量換算値から未乾燥試料の採取量を求めるには、下記の操作により乾燥減量を求め、次の式によって、算出する。
S’=S×1/(100−W)×100
ここで、S’は未乾燥試料採取量(g)、Sは試料の質量(乾燥質量換算)(g)、Wは乾燥減量(%)を示す。
Here, in order to obtain the amount of the undried sample collected from the dry mass conversion value, the loss on drying is obtained by the following operation and calculated by the following equation.
S ′ = S × 1 / (100−W) × 100
Here, S ′ represents an undried sample collection amount (g), S represents the mass of the sample (in terms of dry mass) (g), and W represents the loss on drying (%).
そして、乾燥減量は、以下のようにして求められる。 And loss on drying is calculated | required as follows.
(a)試料約5gを質量既知の平形はかり瓶に取り、はかり瓶の底面になるべく均等な厚さに広げ、ふたをした後、10mgのけたまで量る。
(b)ふたを取り、はかり瓶及びふたを115±5℃に調節した恒温乾燥器中で3時間乾燥する。
(c)デシケーター(乾燥剤 シリカゲル)中で放冷した後、ふたをして質量を量り減量を求める。
(d)乾燥減量は、次の式によって算出する。
F=N/S×100
ここで、Fは乾燥減量(%)、Nは減量(g)、Sは試料の質量(g)を示す。
(A) About 5 g of a sample is placed in a flat weighing bottle with a known mass, spread to the same thickness as possible on the bottom of the weighing bottle, capped, and weighed to 10 mg.
(B) Remove the lid and dry the balance bottle and lid for 3 hours in a constant temperature drier adjusted to 115 ± 5 ° C.
(C) After allowing to cool in a desiccator (desiccant silica gel), cover and measure the weight to determine the weight loss.
(D) The loss on drying is calculated by the following formula.
F = N / S × 100
Here, F is the loss on drying (%), N is the loss (g), and S is the mass (g) of the sample.
そして、上記のJIS K1474に従い、pH調整活性炭の未乾燥試料を乾燥質量換算してpHを測定した場合と、pH調整活性炭の乾燥試料を用いてpHを測定した場合とを比較すると、両者のpH測定値に大きな違いが生じることが確認された。 Then, according to the above JIS K1474, when the pH is measured by converting the dry sample of the pH-adjusted activated carbon into a dry mass and the pH is measured using the dry sample of the pH-adjusted activated carbon, both pH values are compared. It was confirmed that there was a big difference in measured values.
表1に、pH調整活性炭を乾燥した後にpHを測定した場合と、乾燥質量換算でpHを測定した場合の例を示す。 Table 1 shows an example in which the pH is measured after drying the pH-adjusted activated carbon, and in the case where the pH is measured in terms of dry mass.
そして、pH調整活性炭を製造する工程において、酸洗浄の後、水による洗浄を行うことにより、活性炭粒子間に存在する酸成分は、洗浄除去されるものの、活性炭細孔内や表面上に収着している酸成分は、水洗浄のみでは除去されにくい。このため、酸洗浄の後に水洗浄を行ったのみのpH調整活性炭を、例えば飲料水処理工程に用いると、残留した酸成分が徐々に処理水にリークして、処理水のpHが飲料水基準を外れる場合があることがわかった。 Then, in the process of producing pH-adjusted activated carbon, the acid component present between the activated carbon particles is washed away with water after the acid cleaning, but is sorbed in the activated carbon pores or on the surface. The acid component is difficult to remove only by washing with water. For this reason, if pH-adjusted activated carbon that has only been washed with water after acid cleaning is used in, for example, a drinking water treatment process, the remaining acid component gradually leaks into the treated water, and the pH of the treated water is adjusted to the drinking water standard. It was found that there are cases where it is off.
表1に示した各pH調整活性炭をカラムに充填し、SV=5h-1で通水して、処理水のpHの経時変化を観察した結果を図1に示す。 Each pH adjusted activated carbon shown in Table 1 is packed in a column, and water is passed through at SV = 5 h −1 , and the results of observing changes in pH of treated water over time are shown in FIG.
比較例1の活性炭では、乾燥質量換算して測定したpH調整活性炭のpHは、3.9であり、これを用いて水処理を行った場合、通水の初期でpHが5.0以下に低下し、pHを7付近に回復させるには、80倍以上の通水が必要であった。 In the activated carbon of Comparative Example 1, the pH of the pH-adjusted activated carbon measured in terms of dry mass is 3.9. When water treatment is performed using this, the pH is 5.0 or less at the initial stage of water flow. In order to lower the pH and restore it to around 7, it was necessary to pass water 80 times or more.
また、比較例3および4の活性炭では、乾燥質量換算して測定したpHは、それぞれ7.5および8.2であり、これを用いて水処理を行った場合、通水初期では中性付近であるが、通水を続けると、処理水のpHが増大し、アルカリ側に飲料水基準を外れることとなった。 In addition, in the activated carbons of Comparative Examples 3 and 4, the pH measured in terms of dry mass was 7.5 and 8.2, respectively, and when water treatment was performed using this, near neutrality at the initial stage of water flow However, when the water flow was continued, the pH of the treated water increased and the drinking water standard was deviated to the alkali side.
このように、残留している酸が多い場合には、処理水のpHが低くなりすぎる一方、酸洗浄の酸濃度を低くして通水初期の処理水pHを中性付近にした場合、その後の処理水pHがアルカリ側に外れることがある。 Thus, when there is a lot of remaining acid, the pH of the treated water becomes too low, while the acid concentration in the acid washing is lowered to bring the treated water pH in the initial stage of water flow to near neutral, The treated water pH may deviate to the alkali side.
従って、活性炭の酸の保持量が変われば、活性炭処理水のpHはその時々に異なってしまうこととなるため、活性炭の納入規格または製品規格を、従来の方法で規定するのは難しいこととなる。 Therefore, if the amount of acid retained in the activated carbon changes, the pH of the activated carbon treated water will change from time to time, so it will be difficult to specify the delivery standard or product standard of activated carbon by conventional methods. .
このため、酸による中和と水による洗浄によって、pH調整活性炭を得た場合は、処理水のpHを飲料基準内に維持するための活性炭のpH範囲は非常に狭いこととなり、従来の浄水場のpH納入規格では対応しづらいことがわかった。また、pHが飲料水基準から外れた場合に、これを飲料水基準に戻すには、多量の通水が必要であり、時間と使用水量がかさむという問題があった。
従って、pHを特定の基準内に納めるのに適した水処理用の活性炭が望まれていた。
Therefore, an activated carbon for water treatment suitable for keeping the pH within a specific standard has been desired.
本発明の課題は、活性炭による処理水のpH調整を容易にする水処理用活性炭およびその製造方法を提供することにある。また、本発明の課題は、これらの水処理用活性炭を用いた、水処理装置および水処理方法を提供することにある。 The subject of this invention is providing the activated carbon for water treatment which makes easy pH adjustment of the treated water by activated carbon, and its manufacturing method. Moreover, the subject of this invention is providing the water treatment apparatus and the water treatment method using these activated carbons for water treatment.
本発明は、活性炭を酸により中和した後、活性炭に保持された酸を除去することにより得られる水処理用活性炭である。 The present invention is an activated carbon for water treatment obtained by neutralizing activated carbon with an acid and then removing the acid retained on the activated carbon.
また、本発明は、酸の除去が、水洗浄、アルカリ洗浄、超音波洗浄、加熱洗浄および乾燥からなる群より選択される少なくとも1種により行われることを特徴とする、上記の水処理用活性炭である。 Further, the present invention provides the activated carbon for water treatment as described above, wherein the acid is removed by at least one selected from the group consisting of water cleaning, alkali cleaning, ultrasonic cleaning, heat cleaning and drying. It is.
また、本発明は、酸が、揮発性の酸であることを特徴とする、上記の水処理用活性炭である。 Moreover, this invention is activated carbon for water treatment as described above, wherein the acid is a volatile acid.
また、本発明は、酸が、塩酸および/または炭酸であることを特徴とする、上記の水処理用活性炭である。 The present invention also provides the activated carbon for water treatment as described above, wherein the acid is hydrochloric acid and / or carbonic acid.
これらの発明により、pHの調整が容易となる水処理用活性炭を得ることができる。 By these inventions, it is possible to obtain activated carbon for water treatment that facilitates pH adjustment.
また、本発明は、JIS K1474により測定されるpHが4.0〜7.0であることを特徴とする、上記の水処理用活性炭である。 Further, the present invention is the above activated carbon for water treatment, characterized in that the pH measured by JIS K1474 is 4.0 to 7.0.
また、本発明は、115±5℃で3時間乾燥した後、JIS K1474に準じて測定されるpHが4.0〜7.0であることを特徴とする、上記の水処理用活性炭である。 Further, the present invention is the above activated carbon for water treatment, characterized in that the pH measured in accordance with JIS K1474 is 4.0 to 7.0 after drying at 115 ± 5 ° C. for 3 hours. .
これらの発明により、安定した製品規格の水処理用活性炭を提供することができることとなる。 By these inventions, the activated carbon for water treatment of the stable product specification can be provided.
また、本発明は、活性炭を酸により中和する工程、前記中和された活性炭に保持された酸を除去する工程、を含むことを特徴とする、水処理用活性炭の製造方法である。 Moreover, this invention is a manufacturing method of the activated carbon for water treatment characterized by including the process of neutralizing activated carbon with an acid, and the process of removing the acid hold | maintained at the said neutralized activated carbon.
また、本発明は、酸の除去が、水洗浄、アルカリ洗浄、超音波洗浄、加熱洗浄および乾燥からなる群より選択される少なくとも1種により行われることを特徴とする、上記の製造方法である。 Further, the present invention is the above production method, wherein the acid is removed by at least one selected from the group consisting of water cleaning, alkali cleaning, ultrasonic cleaning, heat cleaning and drying. .
また、本発明は、酸が、揮発性の酸であることを特徴とする、上記の製造方法である。 Moreover, this invention is said manufacturing method characterized by the acid being a volatile acid.
また、本発明は、酸が、塩酸および/または炭酸であることを特徴とする、上記の製造方法である。 The present invention is also the above production method, wherein the acid is hydrochloric acid and / or carbonic acid.
これらの発明により、pHの調整が容易となる水処理用活性炭を製造することができることとなる。 By these inventions, it becomes possible to produce activated carbon for water treatment that facilitates pH adjustment.
また、本発明は、上記の水処理用活性炭を充填したカラムと、前記カラムに被処理水を供給するポンプと、を備えたことを特徴とする、水処理装置である。 Moreover, this invention is a water treatment apparatus provided with the column filled with said activated carbon for water treatment, and the pump which supplies to-be-processed water to the said column.
また、本発明は、上記の水処理用活性炭を用いることを特徴とする、水処理方法である。 Moreover, this invention is a water treatment method characterized by using said activated carbon for water treatment.
これらの発明により、pHの調整が容易となる水処理装置および水処理方法を提供することができることとなる。 These inventions can provide a water treatment apparatus and a water treatment method that facilitate the pH adjustment.
本発明により、活性炭による処理水のpH調整を容易にする水処理用活性炭およびその製造方法を提供することができる。また、本発明により、これらの水処理用活性炭を用いた、水処理装置および水処理方法を提供することができる。 ADVANTAGE OF THE INVENTION By this invention, the activated carbon for water treatment which makes easy pH adjustment of the treated water by activated carbon, and its manufacturing method can be provided. Moreover, according to the present invention, a water treatment apparatus and a water treatment method using these activated carbons for water treatment can be provided.
本発明に用いられる活性炭としては、特に制限はなく、水処理に通常用いられるものを利用することができる。また、活性炭の形状としては、特に制限はなく、粒状ものもの粉末状のものなど、いずれの形状のものも用いることができる。 There is no restriction | limiting in particular as activated carbon used for this invention, The thing normally used for a water treatment can be utilized. Moreover, there is no restriction | limiting in particular as a shape of activated carbon, The thing of any shape, such as a granular thing and a powder form, can be used.
本発明に用いられる酸としては、活性炭のアルカリ成分を中和できるものであれば特に制限はないが、例えば、塩酸、炭酸、硫酸、硝酸等の無機酸、蟻酸、酢酸、クエン酸等の有機酸を挙げることができ、これらの中でも、揮発性の酸であることが好ましく、塩酸または炭酸をより好ましい例として挙げることができる。 The acid used in the present invention is not particularly limited as long as it can neutralize the alkaline component of activated carbon. For example, inorganic acids such as hydrochloric acid, carbonic acid, sulfuric acid, and nitric acid, and organic acids such as formic acid, acetic acid, and citric acid. An acid can be mentioned, Among these, it is preferable that it is a volatile acid, and hydrochloric acid or carbonic acid can be mentioned as a more preferable example.
本発明において、活性炭を酸で中和する方法としては、特に制限はないが、酸の水溶液中に活性炭を浸漬すること等を挙げることができる。 In the present invention, the method for neutralizing activated carbon with an acid is not particularly limited, and examples include immersing activated carbon in an acid aqueous solution.
この際に用いる酸の濃度としては、中和する活性炭に含まれるアルカリ成分の量や強さにより適宜決定されるものであるが、一般に0.01〜0.3Nのものを挙げることができる。 The concentration of the acid used at this time is appropriately determined depending on the amount and strength of the alkali component contained in the activated carbon to be neutralized, and generally includes 0.01 to 0.3 N.
この中和操作により、活性炭に含まれるアルカリ成分が中和されることとなるが、通常活性炭には過剰の酸が保持されることとなる。 By this neutralization operation, the alkali component contained in the activated carbon is neutralized, but usually excess acid is retained in the activated carbon.
次に、活性炭に保持された酸を除去することにより本発明の水処理用活性炭を得ることができる。本発明に用いられる酸の除去方法としては、特に制限はないが、例えば、水洗浄、アルカリ洗浄、超音波洗浄、加熱洗浄および乾燥等を挙げることができる。 Next, the activated carbon for water treatment of the present invention can be obtained by removing the acid retained on the activated carbon. The acid removal method used in the present invention is not particularly limited, and examples thereof include water washing, alkali washing, ultrasonic washing, heat washing and drying.
即ち、酸による中和の後、活性炭を濾別し、これを水またはアルカリ水を用いて洗浄することにより、活性炭に保持された酸を除去することができる。ここで用いられる水の量としては、活性炭に保持された酸を除去できるものであれば特に制限はないが、例えば、活性炭の体積に対し、1〜10000倍、好ましくは10〜1000倍、より好ましくは50〜500倍の水量を挙げることができる。また、ここで用いられるアルカリ水としては、活性炭に保持された酸を除去できるものであれば特に制限はないが、例えば、pH8〜10程度のアルカリ水を挙げることができる。さらに、この場合に用いられるアルカリ成分としては、特に制限はないが、例えば、水酸化ナトリウム、水酸化カリウム、炭酸水素ナトリウム等を挙げることができる。例えば、水酸化ナトリウムを用いる場合は、0.0001〜10N、好ましくは0.001〜1N、より好ましくは0.01〜0.1Nのものを挙げることができる。 That is, after neutralization with an acid, the activated carbon is filtered off and washed with water or alkaline water to remove the acid retained on the activated carbon. The amount of water used here is not particularly limited as long as the acid retained on the activated carbon can be removed, but, for example, 1 to 10000 times, preferably 10 to 1000 times, more than the volume of the activated carbon. Preferably, the amount of water can be 50 to 500 times. In addition, the alkaline water used here is not particularly limited as long as it can remove the acid retained on the activated carbon, and examples thereof include alkaline water having a pH of about 8 to 10. Further, the alkali component used in this case is not particularly limited, and examples thereof include sodium hydroxide, potassium hydroxide, sodium hydrogen carbonate and the like. For example, when using sodium hydroxide, 0.0001-10N, preferably 0.001-1N, more preferably 0.01-0.1N can be mentioned.
超音波を照射して洗浄する場合には、例えば活性炭を水またはアルカリ水に分散させ、これに超音波を照射する方法を挙げることができる。この際に照射される超音波のエネルギー量としては、活性炭に保持された酸を除去できるものであれば特に制限はない。 In the case of cleaning by irradiating with ultrasonic waves, for example, a method of dispersing activated carbon in water or alkaline water and irradiating with ultrasonic waves can be mentioned. The energy amount of the ultrasonic wave irradiated at this time is not particularly limited as long as the acid retained on the activated carbon can be removed.
また、加熱洗浄する場合には、例えば、活性炭を水またはアルカリ水に分散させ、これを加熱する方法を挙げることができる。この際に加熱される温度としては、活性炭に保持された酸を除去できるものであれば特に制限はないが、例えば、40〜110℃、好ましくは50〜100℃、より好ましくは70〜90℃を挙げることができる。 Moreover, when heat-washing, the method of disperse | distributing activated carbon to water or alkaline water, and heating this can be mentioned, for example. The temperature heated at this time is not particularly limited as long as the acid retained on the activated carbon can be removed. For example, the temperature is 40 to 110 ° C, preferably 50 to 100 ° C, more preferably 70 to 90 ° C. Can be mentioned.
また、乾燥により酸を除去する場合には、例えば、活性炭を乾燥雰囲気中に保持する方法を挙げることができる。この場合の乾燥の程度としては、特に制限はないが、例えば、含水率として10%以下、好ましくは5%以下、より好ましくは3%以下とすることが挙げられる。具体的には、気流乾燥機、加熱型乾燥機、流動乾燥機等を用い、200℃程度の雰囲気に、湿潤状態の洗浄後の活性炭を投入して、数十分から数時間乾燥を行うことにより、含水率3%以下の乾燥した活性炭を得ることができる。 Moreover, when removing an acid by drying, the method of hold | maintaining activated carbon in a dry atmosphere can be mentioned, for example. The degree of drying in this case is not particularly limited. For example, the moisture content is 10% or less, preferably 5% or less, more preferably 3% or less. Specifically, using activated air dryer, heating type dryer, fluid dryer, etc., the activated carbon after washing in a wet state is put in an atmosphere of about 200 ° C. and dried for several tens of minutes to several hours. Thus, dried activated carbon having a water content of 3% or less can be obtained.
本発明の水処理用活性炭は、JIS K1474によりpHを測定した場合、4.0〜7.0となるものが好ましく、4.5〜6.5となるものがさらに好ましい。 When the pH of the activated carbon for water treatment of the present invention is measured according to JIS K1474, it is preferably 4.0 to 7.0, more preferably 4.5 to 6.5.
さらに、本発明の水処理用活性炭は、115±5℃で3時間乾燥した後、JIS K1474に準じてpHを測定した場合、4.0〜7.0となるものが好ましく、4.5〜6.5となるものがさらに好ましい。 Furthermore, the activated carbon for water treatment according to the present invention is preferably 4.0 to 7.0 when pH is measured according to JIS K1474 after drying at 115 ± 5 ° C. for 3 hours. What becomes 6.5 is more preferable.
本発明の水処理用活性炭を用いて水処理を行う方法としては、特に制限はなく、通常の水処理用の活性炭と同様にして水処理を行うことができる。例えば、本発明の水処理用活性炭をカラムに充填し、これに被処理水を通水することにより、水処理を行うことができる。また、被処理水に本発明の水処理用活性炭を投入し、撹拌後、活性炭をろ過することにより、水処理を行うこともできる。 There is no restriction | limiting in particular as a method of performing water treatment using the activated carbon for water treatment of this invention, Water treatment can be performed like the activated carbon for normal water treatment. For example, the water treatment can be performed by filling the activated carbon for water treatment of the present invention into a column and passing water to be treated through the column. Moreover, the activated carbon for water treatment of this invention is thrown into to-be-processed water, and water treatment can also be performed by filtering activated carbon after stirring.
次に、本発明の水処理装置について説明する。
本発明の水処理装置の1例を図2に示す。図2において、本発明の水処理装置10は、ポンプ2、ポンプ2に配管4を介して接続されたカラム6、カラム6に配管8を介して接続されたpH計12を備えており、カラム6には、水処理用活性炭14が充填されている。
Next, the water treatment apparatus of the present invention will be described.
An example of the water treatment apparatus of the present invention is shown in FIG. In FIG. 2, a water treatment apparatus 10 of the present invention includes a pump 2, a column 6 connected to the pump 2 via a pipe 4, and a pH meter 12 connected to the column 6 via a pipe 8. 6 is filled with activated carbon 14 for water treatment.
そして、ポンプ2により供給された被処理水は、配管4を通ってカラム6に投入される。カラム6に投入された被処理水は、水処理用活性炭14により処理され、処理水は、配管8を通って、pH計12によりpHが測定された後、処理水が排出される。これにより、一連の水処理工程が終了することとなる。 Then, the water to be treated supplied by the pump 2 is introduced into the column 6 through the pipe 4. The treated water put into the column 6 is treated with the activated carbon 14 for water treatment, and the treated water is discharged through the pipe 8 and the pH is measured by the pH meter 12. Thereby, a series of water treatment processes will be completed.
<参考例1〜4>
活性炭(「エバダイヤLG−20」:荏原製作所社製(酸による洗浄を行っていない活性炭))1kgを0.15N塩酸4Lで中和した後、水4Lにより洗浄した。活性炭をろ過後、その一部をJIS K1474によりpH測定したところ、pH=5.5であった。次に、ろ過した活性炭に、80℃の熱水4Lを加えて約20分間洗浄し、さらに活性炭をろ過することにより、本発明の水処理用活性炭を得た。
<Reference Examples 1-4>
1 kg of activated carbon (“Evadia LG-20”: manufactured by Ebara Manufacturing Co., Ltd. (activated carbon not washed with acid)) was neutralized with 4 L of 0.15 N hydrochloric acid, and then washed with 4 L of water. After filtering the activated carbon, a part of it was measured for pH according to JIS K1474. The result was pH = 5.5. Next, activated carbon for water treatment of the present invention was obtained by adding 4 L of hot water at 80 ° C. to the filtered activated carbon, washing for about 20 minutes, and further filtering the activated carbon.
得られた水処理用活性炭について、JIS K1474に従い、乾燥質量換算によりpHを測定したところ、pH=6.8であった。さらに、115℃で3時間乾燥した後、JIS K1474に準じてpHを測定したところ、pH=6.6であった(実施例1)。 About the obtained activated carbon for water treatment, it was pH = 6.8 when pH was measured by dry mass conversion according to JISK1474. Furthermore, after drying at 115 degreeC for 3 hours, when pH was measured according to JISK1474, it was pH = 6.6 (Example 1).
塩酸濃度を高くして、同様の操作を行うことにより、pHの異なる水処理用活性炭を3種類得た(参考例2〜4)。
pHの測定結果を表2に併せて示す。
By performing the same operation while increasing the hydrochloric acid concentration, three types of activated carbon for water treatment with different pH were obtained (Reference Examples 2 to 4).
The measurement results of pH are also shown in Table 2.
これより、本発明の水処理用活性炭を用いて水処理を行った場合、飲料水基準内に収まることがわかる。 From this, it is understood that when the water treatment is performed using the activated carbon for water treatment of the present invention, it falls within the drinking water standard.
<参考例5〜7、実施例1>
参考例1と同様の操作により、活性炭を酸による中和および水による洗浄を行った。次に、水洗浄、アルカリ洗浄、加熱洗浄、乾燥の操作をそれぞれ行って、本発明の水処理用活性炭を得た(参考例5〜7、実施例1)。
<Reference Examples 5-7, Example 1>
By the same operation as in Reference Example 1, the activated carbon was neutralized with acid and washed with water. Next, water washing, alkali washing, heat washing, and drying were performed to obtain activated carbon for water treatment of the present invention (Reference Examples 5 to 7, Example 1).
酸中和、水洗浄後の乾燥質量換算によるpH測定結果、各操作後の乾燥後のpH測定結果、各操作後の乾燥質量換算によるpH測定結果を、表3に示す。 Table 3 shows the pH measurement results in terms of dry weight after acid neutralization and water washing, the pH measurement results after drying after each operation, and the pH measurement results in terms of dry mass after each operation.
これより、酸の除去操作を行うことにより、pH調整が容易となる水処理用活性炭が得られることがわかる。 From this, it can be seen that activated carbon for water treatment that facilitates pH adjustment can be obtained by performing an acid removal operation.
以上より、本発明により、JIS K1474により測定されるpHが4.0〜7.0であり、かつ、115±5℃で3時間乾燥した後、JIS K1474に準じて測定されるpHが4.0〜7.0である水処理用活性炭が得られ、これを用いて水処理を行った場合、飲料水基準内におさまることがわかる。 As described above, according to the present invention, the pH measured according to JIS K1474 is 4.0 to 7.0, and after drying at 115 ± 5 ° C. for 3 hours, the pH measured according to JIS K1474 is 4. It turns out that the activated carbon for water treatment which is 0-7.0 is obtained, and when water treatment is performed using this, it falls within the drinking water standard.
Claims (6)
前記活性炭を水またはアルカリ水により洗浄する工程、
前記活性炭を乾燥させて、活性炭に保持された酸を除去する工程、
により得られる水処理用活性炭であって、前記活性炭の含水率が3%以下であることを特徴とする水処理用活性炭。 Neutralizing activated carbon with 0.01 to 0.15 N aqueous hydrochloric acid and / or aqueous carbonate,
Washing the activated carbon with water or alkaline water;
Drying the activated carbon to remove the acid retained on the activated carbon;
The activated carbon for water treatment obtained by the above, wherein the activated carbon has a water content of 3% or less.
前記活性炭を水またはアルカリ水により洗浄する工程、
前記活性炭を乾燥させて、活性炭に保持された酸を除去する工程、
前記活性炭の含水率が3%以下になるようにさらに乾燥する工程、
を含む水処理用活性炭の製造方法。 Neutralizing activated carbon with 0.01 to 0.15 N aqueous hydrochloric acid and / or aqueous carbonate,
Washing the activated carbon with water or alkaline water;
Drying the activated carbon to remove the acid retained on the activated carbon;
A step of further drying such that the moisture content of the activated carbon is 3% or less;
For producing activated carbon for water treatment.
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JP2015515443A (en) * | 2012-04-25 | 2015-05-28 | カルゴン カーボン コーポレーション | Reduction of arsenic and antimony leaching from activated carbon |
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