JP4774617B2 - Cleaning method of activated carbon - Google Patents

Cleaning method of activated carbon Download PDF

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Publication number
JP4774617B2
JP4774617B2 JP2001107431A JP2001107431A JP4774617B2 JP 4774617 B2 JP4774617 B2 JP 4774617B2 JP 2001107431 A JP2001107431 A JP 2001107431A JP 2001107431 A JP2001107431 A JP 2001107431A JP 4774617 B2 JP4774617 B2 JP 4774617B2
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Prior art keywords
water
activated carbon
specific resistance
cleaning
carbonic acid
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JP2001107431A
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JP2002301366A (en
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明和 山本
満 野末
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Kurita Water Industries Ltd
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Kurita Water Industries Ltd
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Description

【0001】
【発明の属する技術分野】
本発明は活性炭の洗浄方法に係り、特に、検査用水等として用いられる比抵抗調整水の回収再利用プロセスにおいて、TOC成分除去手段としての活性炭の調整に好適な活性炭の洗浄方法に関する。
【0002】
【従来の技術】
半導体製造プロセス、シリコンウエハー製造プロセス、液晶製造プロセス、検査用水プロセスにおいては、高度純水や炭酸を溶解させることにより特定の抵抗率に調整された純水が大量に使用されており、従って、これらのプロセスからは使用済み純水が大量に排出される。従来、これらのプロセスから排出される使用済み純水は、回収して脱塩処理することによりその純度を高め、再使用することが行われているが、系内でTOC成分が不純物として混入する場合には、多くの場合、再利用することなくそのまま廃棄されている。
【0003】
しかし、近年、環境負荷の低減や水処理コストの低減が要望され、TOC成分が混入した使用済み純水についてもこれを回収して再利用することが行われるようになってきている。
【0004】
従来、水中のTOC成分を除去するプロセスとしては、逆浸透膜分離装置、紫外線分解装置、電気分解装置、オゾン酸化装置等を組み合わせたものがあるが、いずれもイニシャルコスト、ランニングコストが高くつくことから、回収した使用済み純水中のTOC成分の除去には、仕組みが簡単な活性炭或いは活性炭と他の装置とを組み合わせたものを採用するケースが増えている。
【0005】
このような回収再利用プロセスでTOC成分の除去手段としての活性炭カートリッジに充填される活性炭は、その製造過程において最終的に純水による仕上げ洗浄が行われ、洗浄排水の比抵抗値が1MΩ・cm以上になるまで十分に洗浄して製品とされる。
【0006】
【発明が解決しようとする課題】
しかしながら、このように純水による洗浄のみを行った活性炭が充填された活性炭カートリッジを、炭酸を用いて比抵抗を調整する比抵抗調整水の回収再利用プロセスでTOC成分除去手段として用いた場合、使用開始初期において、得られる処理水の抵抗率が変化し、抵抗率の設定範囲を超えてしまうという問題があった。
【0007】
このため、従来、活性炭カートリッジを新品の活性炭カートリッジに交換した際は、立ち上げ運転を行って、通水初期の活性炭カートリッジの流出水を採水せず、抵抗率が設定範囲内となる水が得られるようになった後、活性炭カートリッジの流出水を採水し、次工程へ送給することが行われている。また、この採水停止期間において、プロセスが停止しないように、活性炭カートリッジを複数系列並列に配置して、通水を切り換えることにより、連続処理を可能とすることが行われている。
【0008】
しかしながら、このように、使用開始時の採水を行えない活性炭カートリッジでは、処理効率が悪く、大量の水を処理する回収再利用プロセスには不適当である。
【0009】
本発明は上記従来の問題点を解決し、使用開始初期の処理水の抵抗率の変動の問題がなく、目標水質の処理水を直ちに採水することが可能な活性炭を調整することができる活性炭の洗浄方法を提供することを目的とする。
【0010】
【課題を解決するための手段】
本発明の活性炭の洗浄方法は、活性炭を純水で洗浄し、次いで炭酸水と接触させることを特徴とする。
【0011】
比抵抗調整水の回収再利用プロセスにおいて活性炭カートリッジを交換した際、通水初期の処理水の抵抗率が高くなるのは、次のような理由による。
【0012】
即ち、活性炭は、純水で洗浄されることにより吸着している炭酸が洗浄除去される。このような活性炭を、炭酸により抵抗率が調整された比抵抗調整水の回収再利用プロセスにおいてTOC除去に使用すると、通水される比抵抗調整水中の炭酸を吸着し、このため流出水の抵抗率が変化する。活性炭は、通水を継続することにより炭酸の吸着量が飽和して平衡状態となるまで比抵抗調整水中の炭酸を吸着するため、この間は流出水の抵抗率が高いものとなる。そして、活性炭の炭酸吸着量が飽和に達すると、もはや活性炭は炭酸を吸着しなくなるため、流出水の抵抗率の変動の問題はなくなり、所定の抵抗率の処理水を得ることができるようになる。
【0013】
本発明では、活性炭を純水で洗浄した後、純水に炭酸を溶解させた炭酸水に接触させて、予め活性炭に炭酸を吸着させておく。このため、通水開始初期においても活性炭が被処理水中の炭酸を吸着することがなく、抵抗率の変動の問題は解消される。従って、使用開始初期から直ちに採水を行うことが可能となる。
【0014】
本発明では、洗浄排水の比抵抗値が所定の値Aになるまで純水で洗浄し、その後、洗浄排水の比抵抗値が所定の値Bになるまで炭酸水で洗浄することが好ましく、これにより活性炭に炭酸を十分に吸着させて平衡状態とし、通水開始初期の炭酸の吸着による抵抗率の変動を完全に排除することが可能となる。
【0015】
なお、炭酸水洗浄で活性炭に吸着された炭酸は、使用済み活性炭を再生する際の障害となることはない。
【0016】
【発明の実施の形態】
以下に本発明の活性炭の洗浄方法の実施の形態を詳細に説明する。
【0017】
本発明においては、活性炭の調整工程の最終の仕上げ処理として、純水による洗浄と炭酸水による洗浄を行う。なお、活性炭の調整工程は、新品の活性炭の調整工程であっても良く、各種のプロセスから回収された活性炭の再生工程であっても良い。
【0018】
活性炭の純水洗浄工程は、カートリッジ等に充填された活性炭に純水を通水し、洗浄排水の比抵抗値Aが0.1MΩ・cm以上、特に1.0〜10.0MΩ・cm程度となるように行うのが好ましい。
【0019】
上記範囲よりも比抵抗値Aが低いと活性炭の純度が不十分であり、各種回収再利用プロセス等で用いた場合、被処理水にイオン汚染等の問題が生じ好ましくない。この比抵抗値Aは高い程活性炭の純度が高まり好ましいが、比抵抗値Aが過度に高くなるように洗浄することは、洗浄に大量の純水と時間を要し、活性炭が高コストとなり好ましくない。
【0020】
なお、洗浄に用いる純水としては、比抵抗値が15MΩ・cm以下、特に18MΩ・cm程度の高純度水であることが好ましい。
【0021】
上記純水洗浄後は、次いで炭酸水による洗浄を行う。この炭酸水としては、比抵抗値が1.0MΩ・cm以上、特に15〜18MΩ・cm程度の純水に炭酸を5〜30ppm程度溶解させることにより比抵抗値が0.15〜0.3MΩ・cm程度とされたものが好ましい。この炭酸水の炭酸濃度が過度に低いと活性炭の調整に用いる炭酸水量及び洗浄時間が長くなり好ましくなく、逆に過度に高いと調整が困難である。
【0022】
活性炭の炭酸水洗浄工程は、カートリッジ等に充填された純水洗浄後の活性炭に炭酸水を通水し、洗浄排水の比抵抗値Bが比抵抗調整水プロセスにおける目標値例えば、0.05〜1.0MΩ・cm、特に0.1〜0.5MΩ・cm程度となるように、また、洗浄排水中の遊離炭酸濃度が0.1〜30ppm、特に0.5〜20ppm程度となるように行うのが好ましい。
【0023】
上記範囲よりも比抵抗値Bが高く炭酸濃度が低いと、活性炭の炭酸吸着量が十分でなく、通水開始初期の炭酸吸着の問題があり、逆に比抵抗値Bが上記範囲よりも低く、炭酸濃度が高いと回収水として不適当である。
【0024】
ただし、各洗浄工程の洗浄排水の比抵抗値A,Bは、活性炭の使用目的に応じて適宜決定され、何ら上記範囲に限定されるものではない。
【0025】
なお、活性炭の洗浄方法は、カートリッジへの純水又は炭酸水の通水洗浄に限定されず、容器内に純水又は炭酸水と活性炭とを入れて攪拌洗浄し、洗浄水を交換するバッチ洗浄であっても良い。
【0026】
このような本発明の活性炭の洗浄方法で調整された活性炭は、特に、炭酸で抵抗率が調整された比抵抗調整水の回収再利用プロセスに好適に使用されるが、その他、各種の高純度水の回収再利用プロセス又は水処理プロセスに有効に使用することができる。特に、炭酸水で洗浄することにより、活性炭に吸着された金属イオンが除去され易くなるため、金属イオンを嫌う水処理プロセスに好適である。
【0027】
【実施例】
以下に実施例及び比較例を挙げて本発明をより具体的に説明する。
【0028】
実施例1
図1に示す活性炭カートリッジ内の活性炭を本発明の方法に従って洗浄した。
【0029】
図1の活性炭カートリッジ1は、容器2の上部開口3に設けられた蓋4部分から、被処理水の撒水管5と処理水の集水管6が挿入されており、容器2内部に活性炭7が充填されている。撒水管5の撒水部5Aは、活性炭7の充填層の上方に位置し、集水管6の集水部6Aは、活性炭7の充填層の下層にまで達している。被処理水は撒水管5の給水入口5Bから活性炭カートリッジ1内に導入され、撒水部5Aから活性炭7上に撒水される。被処理水は、活性炭7の層を流下して、下層に達し、この間に活性炭と接触することにより含有されるTOC成分が活性炭に吸着除去される。そして処理水は、集水管6の集水部6Aで集水され、処理水出口6Bから排出される。
【0030】
洗浄に当たっては、まず、撒水管5から純水(比抵抗値10MΩ・cm)を流入させて、洗浄排水を集水管6から取り出す純水洗浄を、洗浄排水の比抵抗値Aが1.0MΩ・cmになるまで行った。
【0031】
次に、純水(比抵抗値10MΩ・cm)に炭酸を10ppm溶解させて比抵抗値0.25MΩ・cmとした炭酸水を用いて、同様に洗浄排水の比抵抗値Bが0.25MΩ・cmで遊離炭酸濃度が10ppmになるまで炭酸水洗浄を行った。
【0032】
このようにして活性炭の洗浄を行った活性炭カートリッジに、炭酸で抵抗率を調整した表1に示す水質の比抵抗調整水をSV=40hr−1の流量で通水し、通水開始初期10分の処理水の平均水質を調べ結果を表1に示した。
【0033】
なお、本実施例では、処理水は通水開始直後に比抵抗値0.25MΩ・cmに達した。
【0034】
比較例1
炭酸水洗浄を行わなかったこと以外は実施例1と同様にして活性炭の洗浄を行い、同様に通水試験を行い、結果を表1に示した。
【0035】
なお、本比較例では、処理水の比抵抗値が0.25MΩ・cmに到達するまでに2.5時間を要し、それまでの通水量は100B.V.(100倍量)を要した。
【0036】
【表1】

Figure 0004774617
【0037】
表1より明らかなように、本発明によれば通水開始初期の比抵抗調整水の抵抗率の変動の問題が解消される。
【0038】
【発明の効果】
以上詳述した通り、本発明の活性炭の洗浄方法によれば、使用開始初期の処理水の抵抗率の変動の問題がなく、目標水質の処理水を直ちに採水することが可能な活性炭を調整することができる。
【図面の簡単な説明】
【図1】実施例1で洗浄を行った活性炭カートリッジを示す模式的な断面図である。
【符号の説明】
1 活性炭カートリッジ
2 容器
5 撒水管
6 集水管
7 活性炭[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an activated carbon cleaning method, and more particularly to an activated carbon cleaning method suitable for adjusting activated carbon as a TOC component removing means in a process for recovering and reusing specific resistance adjustment water used as inspection water or the like.
[0002]
[Prior art]
In semiconductor manufacturing processes, silicon wafer manufacturing processes, liquid crystal manufacturing processes, and inspection water processes, highly pure water or pure water adjusted to a specific resistivity by dissolving carbonic acid is used in large quantities. A large amount of used pure water is discharged from this process. Conventionally, spent pure water discharged from these processes has been recovered and desalted to increase its purity and reused, but TOC components are mixed as impurities in the system. In many cases, it is discarded without being reused.
[0003]
However, in recent years, reduction of environmental load and reduction of water treatment costs have been demanded, and used pure water mixed with TOC components has also been collected and reused.
[0004]
Conventionally, processes for removing TOC components in water include a combination of a reverse osmosis membrane separator, an ultraviolet decomposition device, an electrolysis device, an ozone oxidation device, etc., all of which have high initial costs and running costs. Therefore, in order to remove the TOC component in the collected used pure water, there are an increasing number of cases employing activated carbon with a simple mechanism or a combination of activated carbon and other devices.
[0005]
The activated carbon filled in the activated carbon cartridge as a means for removing the TOC component in such a recovery and reuse process is finally cleaned with pure water in the manufacturing process, and the specific resistance value of the cleaning waste water is 1 MΩ · cm. The product is thoroughly washed until it is above.
[0006]
[Problems to be solved by the invention]
However, when the activated carbon cartridge filled with activated carbon that has been washed only with pure water in this way is used as a TOC component removal means in the recovery and reuse process of specific resistance adjustment water that adjusts the specific resistance using carbonic acid, At the beginning of use, there was a problem that the resistivity of the treated water obtained changed and exceeded the set range of resistivity.
[0007]
For this reason, conventionally, when the activated carbon cartridge is replaced with a new activated carbon cartridge, the start-up operation is performed, and the effluent water of the activated carbon cartridge at the initial stage of water flow is not collected, and the water whose resistivity falls within the set range is not obtained. After being obtained, the effluent water from the activated carbon cartridge is collected and fed to the next step. In addition, in this water sampling stop period, continuous processing is made possible by arranging activated carbon cartridges in parallel and switching water flow so that the process does not stop.
[0008]
However, the activated carbon cartridge that cannot collect water at the start of use as described above has poor processing efficiency and is inappropriate for a recovery and reuse process for processing a large amount of water.
[0009]
The present invention solves the above-described conventional problems, and there is no problem of variation in the resistivity of treated water at the beginning of use, and activated carbon capable of adjusting the activated carbon that can immediately collect treated water of the target water quality can be prepared. An object of the present invention is to provide a cleaning method.
[0010]
[Means for Solving the Problems]
The activated carbon cleaning method of the present invention is characterized in that the activated carbon is cleaned with pure water and then brought into contact with carbonated water.
[0011]
When the activated carbon cartridge is replaced in the process of collecting and reusing specific resistance adjustment water, the resistivity of the treated water at the initial stage of water flow increases for the following reason.
[0012]
That is, the activated carbon is washed with pure water to remove the adsorbed carbonic acid. When such activated carbon is used for removing TOC in the process of recovering and reusing specific resistance adjusted water whose resistivity is adjusted by carbonic acid, the carbon dioxide in the specific resistance adjusted water to be passed is adsorbed, and thus the resistance of the effluent water. The rate changes. The activated carbon adsorbs the carbonic acid in the specific resistance adjustment water until the amount of carbonic acid adsorption is saturated and reaches an equilibrium state by continuing the water flow, and therefore the resistivity of the effluent water is high during this period. When the carbon dioxide adsorption amount of the activated carbon reaches saturation, the activated carbon no longer adsorbs carbonic acid, so there is no problem of fluctuation in the resistivity of the outflow water, and treated water having a predetermined resistivity can be obtained. .
[0013]
In the present invention, after the activated carbon is washed with pure water, it is brought into contact with carbonated water obtained by dissolving carbonic acid in pure water, so that carbon is adsorbed on the activated carbon in advance. For this reason, activated carbon does not adsorb carbonic acid in the water to be treated even at the beginning of water flow, and the problem of variation in resistivity is solved. Therefore, water can be collected immediately from the beginning of use.
[0014]
In the present invention, it is preferable to wash with pure water until the specific resistance value of the cleaning wastewater reaches a predetermined value A, and then wash with carbonated water until the specific resistance value of the cleaning wastewater reaches a predetermined value B. As a result, carbon dioxide is sufficiently adsorbed on the activated carbon to achieve an equilibrium state, and it becomes possible to completely eliminate the fluctuation of resistivity due to the adsorption of carbonic acid at the beginning of water flow.
[0015]
Carbonic acid adsorbed on the activated carbon by the carbonated water washing does not become an obstacle when the used activated carbon is regenerated.
[0016]
DETAILED DESCRIPTION OF THE INVENTION
The embodiment of the activated carbon cleaning method of the present invention will be described in detail below.
[0017]
In the present invention, cleaning with pure water and cleaning with carbonated water are performed as the final finishing process in the adjustment process of the activated carbon. In addition, the adjustment process of activated carbon may be an adjustment process of new activated carbon, and may be a regeneration process of activated carbon recovered from various processes.
[0018]
In the pure water cleaning process of activated carbon, pure water is passed through activated carbon filled in a cartridge or the like, and the specific resistance value A of the cleaning waste water is 0.1 MΩ · cm or more, particularly about 1.0 to 10.0 MΩ · cm. It is preferable to carry out as follows.
[0019]
When the specific resistance value A is lower than the above range, the purity of the activated carbon is insufficient, and when used in various recovery and reuse processes, problems such as ion contamination occur in the water to be treated, which is not preferable. The higher the specific resistance value A, the higher the purity of the activated carbon, which is preferable. However, cleaning so that the specific resistance value A is excessively high requires a large amount of pure water and time for the cleaning, and the activated carbon is expensive and preferable. Absent.
[0020]
The pure water used for cleaning is preferably high-purity water having a specific resistance of 15 MΩ · cm or less, particularly about 18 MΩ · cm.
[0021]
After the pure water cleaning, cleaning with carbonated water is then performed. The carbonated water has a resistivity value of 0.15 to 0.3 MΩ · cm by dissolving about 5 to 30 ppm of carbonate in pure water having a resistivity value of 1.0 MΩ · cm or more, particularly about 15 to 18 MΩ · cm. What was made into about cm is preferable. If the carbonate concentration of the carbonated water is too low, the amount of carbonated water used for the adjustment of the activated carbon and the washing time are undesirably increased, and conversely if too high, the adjustment is difficult.
[0022]
In the carbonated water washing step of activated carbon, carbonated water is passed through activated carbon after pure water washing filled in a cartridge or the like, and the specific resistance value B of the washing wastewater is a target value in the specific resistance adjustment water process, for example, 0.05 to 1.0 MΩ · cm, particularly 0.1 to 0.5 MΩ · cm, and the concentration of free carbonic acid in the washing waste water is 0.1 to 30 ppm, particularly about 0.5 to 20 ppm. Is preferred.
[0023]
If the specific resistance value B is higher than the above range and the carbonic acid concentration is low, the carbon dioxide adsorption amount of the activated carbon is not sufficient, and there is a problem of carbonic acid adsorption at the beginning of water flow. Conversely, the specific resistance value B is lower than the above range. If the carbonic acid concentration is high, it is not suitable as recovered water.
[0024]
However, the specific resistance values A and B of the cleaning waste water in each cleaning step are appropriately determined according to the purpose of use of the activated carbon, and are not limited to the above range.
[0025]
The cleaning method for activated carbon is not limited to passing pure water or carbonated water through the cartridge, but batch cleaning in which pure water or carbonated water and activated carbon are placed in a container and stirred and washed to replace the cleaning water. It may be.
[0026]
The activated carbon prepared by the activated carbon cleaning method of the present invention is particularly suitable for use in the process of collecting and reusing specific resistance adjusted water whose resistivity is adjusted with carbonic acid. It can be effectively used for water recovery and reuse processes or water treatment processes. In particular, washing with carbonated water facilitates removal of metal ions adsorbed on the activated carbon, which is suitable for a water treatment process that dislikes metal ions.
[0027]
【Example】
Hereinafter, the present invention will be described more specifically with reference to Examples and Comparative Examples.
[0028]
Example 1
The activated carbon in the activated carbon cartridge shown in FIG. 1 was washed according to the method of the present invention.
[0029]
The activated carbon cartridge 1 shown in FIG. 1 has a treated water submerged pipe 5 and a treated water collecting pipe 6 inserted through a lid 4 provided in the upper opening 3 of the container 2. Filled. The submerged portion 5A of the submerged pipe 5 is located above the packed bed of activated carbon 7, and the water collecting section 6 A of the water collecting pipe 6 reaches the lower layer of the packed bed of activated carbon 7. The water to be treated is introduced into the activated carbon cartridge 1 from the feed water inlet 5B of the brine pipe 5 and is poured onto the activated carbon 7 from the flooded portion 5A. The water to be treated flows down the layer of activated carbon 7 and reaches the lower layer. During this time, the TOC component contained by contacting the activated carbon is adsorbed and removed by the activated carbon. And treated water is collected by the water collection part 6A of the water collection pipe 6, and discharged from the treated water outlet 6B.
[0030]
In cleaning, pure water (specific resistance value 10 MΩ · cm) is first introduced from the submerged pipe 5 and the cleaning waste water is taken out from the collecting pipe 6. The cleaning waste water has a specific resistance value A of 1.0 MΩ · It went until it became cm.
[0031]
Next, using carbonated water in which 10 ppm of carbonic acid was dissolved in pure water (specific resistance value 10 MΩ · cm) to a specific resistance value of 0.25 MΩ · cm, the specific resistance value B of the washing waste water was similarly 0.25 MΩ · cm. Washing with carbonated water was performed until the free carbonic acid concentration became 10 ppm in cm.
[0032]
The water quality specific resistance adjustment water shown in Table 1 whose resistivity was adjusted with carbonic acid was passed through the activated carbon cartridge thus washed with activated carbon at a flow rate of SV = 40 hr −1. The average water quality of the treated water was examined and the results are shown in Table 1.
[0033]
In this example, the treated water reached a specific resistance value of 0.25 MΩ · cm immediately after the start of water flow.
[0034]
Comparative Example 1
The activated carbon was washed in the same manner as in Example 1 except that the carbonated water was not washed, and a water flow test was conducted in the same manner. The results are shown in Table 1.
[0035]
In this comparative example, it takes 2.5 hours for the specific resistance value of the treated water to reach 0.25 MΩ · cm, and the water flow up to that time is 100B. V. (100 times the amount) was required.
[0036]
[Table 1]
Figure 0004774617
[0037]
As apparent from Table 1, according to the present invention, the problem of fluctuation in resistivity of the specific resistance adjustment water at the beginning of water flow is solved.
[0038]
【The invention's effect】
As described above in detail, according to the activated carbon cleaning method of the present invention, there is no problem of variation in the resistivity of the treated water at the beginning of use, and the activated carbon that can immediately collect the treated water of the target water quality is prepared. can do.
[Brief description of the drawings]
FIG. 1 is a schematic cross-sectional view showing an activated carbon cartridge that has been cleaned in Example 1. FIG.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Activated carbon cartridge 2 Container 5 Flood water pipe 6 Catchment pipe 7 Activated carbon

Claims (2)

活性炭を純水で洗浄し、次いで炭酸水と接触させることを特徴とする活性炭の洗浄方法。A method for cleaning activated carbon, characterized in that the activated carbon is washed with pure water and then brought into contact with carbonated water. 請求項1において、洗浄排水が所定の比抵抗値Aになるまで活性炭を純水で洗浄し、次いで洗浄排水が所定の比抵抗値Bになるまで活性炭を炭酸水で洗浄することを特徴とする活性炭の洗浄方法。2. The method according to claim 1, wherein the activated carbon is washed with pure water until the washing wastewater has a predetermined specific resistance value A, and then the activated carbon is washed with carbonated water until the washing wastewater has a predetermined specific resistance value B. Cleaning method for activated carbon.
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CN102500571A (en) * 2011-11-08 2012-06-20 江苏竹溪活性炭有限公司 Active carbon pickling device

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JP5380870B2 (en) * 2008-03-14 2014-01-08 栗田工業株式会社 Method and apparatus for producing gas-dissolved water

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JP3699502B2 (en) * 1995-04-13 2005-09-28 新日本製鐵株式会社 Semiconductor cleaning wastewater collection method
JPH1147589A (en) * 1997-08-07 1999-02-23 Ebara Corp Regeneration pretreatment of activated carbon

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102500571A (en) * 2011-11-08 2012-06-20 江苏竹溪活性炭有限公司 Active carbon pickling device

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