JP2000246262A - Method of reducing sludge generated when removing heavy metals from waste liquid - Google Patents
Method of reducing sludge generated when removing heavy metals from waste liquidInfo
- Publication number
- JP2000246262A JP2000246262A JP11055138A JP5513899A JP2000246262A JP 2000246262 A JP2000246262 A JP 2000246262A JP 11055138 A JP11055138 A JP 11055138A JP 5513899 A JP5513899 A JP 5513899A JP 2000246262 A JP2000246262 A JP 2000246262A
- Authority
- JP
- Japan
- Prior art keywords
- waste liquid
- sludge
- heavy metals
- iron hydroxide
- filtered
- 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
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
(57)【要約】
【課題】廃液から重金属を化学的に除去するにあたり、
発生したスラッジを大幅に低減し、スラッジの濾過乾燥
等の処理作業上の負担を軽減すると共に、放射性スラッ
ジの場合の減容効果を高め、保管費用、保管面積の効率
化をはかる。
【解決手段】重金属を含む廃液に塩化鉄(FeCl3)
を添加し、中和させて水酸化鉄(Fe(OH)3)を発
生させ、この水酸化鉄をフロック状態として前記含有各
種重金属を吸着沈澱させると共に、沈澱した水酸化鉄フ
ロックを濾過して廃液から重金属を除去する方法におい
て、前記濾過された水酸化鉄スラッジを更にHCl溶液
に溶解し、pHを調整して次ロットの廃液に添加再使用
する。この操作を所要複数回繰り返して発生スラッジ量
を低減させる。
(57) [Summary] [PROBLEMS] To chemically remove heavy metals from waste liquid,
The generated sludge is greatly reduced, the burden on processing operations such as filtration and drying of the sludge is reduced, the volume reduction effect in the case of radioactive sludge is increased, and storage costs and storage area are made more efficient. The waste liquid containing heavy metal is iron chloride (FeCl 3 ).
And neutralized to generate iron hydroxide (Fe (OH) 3 ). The iron hydroxide is brought into a floc state to adsorb and precipitate the various heavy metals contained therein, and the precipitated iron hydroxide floc is filtered. In the method of removing heavy metals from the waste liquid, the filtered iron hydroxide sludge is further dissolved in an HCl solution, the pH is adjusted, and added to the waste liquid of the next lot for reuse. This operation is repeated a required number of times to reduce the amount of generated sludge.
Description
【0001】[0001]
【発明の属する技術分野】本発明は廃液から重金属を化
学的に除去する際に発生するスラッジを可及的低減する
ための方法に係り、特に発生するスラッジが放射性廃棄
物の場合の廃棄物減容に効果的な上記方法に関するもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for reducing sludge generated when a heavy metal is chemically removed from a waste liquid as much as possible, particularly when the generated sludge is radioactive waste. It is concerned with the above method which is effective.
【0002】[0002]
【従来の技術】廃液から重金属を化学的に除去する方法
は各種あるが、その代表的なものは中和による方法であ
る。しかしこの方法は微量の不純物を除去することが難
しいため、一般的には廃液にFeCl3を添加し、中和
して水酸化鉄Fe(OH)3を発生させ、このフロック
(綿状浮遊物)に各種金属を吸着、沈殿させる方法が採
られている。この方法は他の方法に比べ適応範囲が広
く、古くから実施されている有効な手段である。2. Description of the Related Art There are various methods for chemically removing heavy metals from waste liquors, and a typical one is neutralization. However, since it is difficult to remove a trace amount of impurities by this method, generally, FeCl 3 is added to the waste liquid and neutralized to generate iron hydroxide Fe (OH) 3 . ) Is a method of adsorbing and precipitating various metals. This method has a wider range of application than other methods and is an effective means that has been practiced for a long time.
【0003】[0003]
【発明が解決しようとする課題】ところが、この手段は
除去重金属に比較して多量の沈澱物、即ち、スラッジの
発生を伴い、この処分が問題となる一面を有している。
これは、廃液が一般廃液の場合には多少のスラッジの発
生を伴うにしても、埋め立て等でさして問題になること
はなかったが、特に除去対象物がウラン(U)等の放射
性スラッジの場合では発生スラッジは管理区域外に搬出
できず、永久に保管されることとなる。However, this method involves the generation of a large amount of precipitates, that is, sludge, as compared with the heavy metals to be removed, and there is one aspect in which this disposal is problematic.
This is not a problem even if the waste liquid is a general waste liquid, even if a little sludge is generated. However, especially when the object to be removed is radioactive sludge such as uranium (U). In this case, the generated sludge cannot be carried out of the controlled area and will be stored permanently.
【0004】そのため現在では廃水各ロット毎に新しい
FeCl3を添加し、発生したスラッジはそのまま濾過
乾燥して保管されている現状である。従って、そのよう
な放射性スラッジでは、その発生前の抑制を図ることが
重要な課題となっている。Therefore, at present, fresh FeCl 3 is added to each lot of wastewater, and the generated sludge is filtered, dried and stored as it is. Therefore, in such a radioactive sludge, it is an important subject to suppress the generation before the generation.
【0005】本発明は上述のような実状に対処し、特に
上記化学法による沈澱処理したスラッジの再使用を試み
ることにより、発生スラッジを従来に比し大幅に低減
し、スラッジの濾過乾燥等の処理作業上の負担を軽減す
ると共に放射性スラッジの減容効果を高め、保管費用、
保管面積の効率化をはかることを目的とするものであ
る。The present invention addresses the above-mentioned situation, and in particular, attempts to reuse sludge that has been subjected to precipitation treatment by the above-mentioned chemical method, thereby significantly reducing the amount of generated sludge as compared with the prior art, and for filtering and drying sludge. Reduces the burden on processing work and enhances the effect of reducing the volume of radioactive sludge.
The purpose is to increase the efficiency of the storage area.
【0006】[0006]
【課題を解決するための手段】即ち、上記目的を達成す
るための本発明の特徴は、重金属を含む廃液に塩化鉄
(FeCl3)を添加し、中和させて水酸化鉄(Fe
(OH)3)を発生させ、この水酸化鉄をフロック状態
として前記含有各種重金属を吸着沈澱させると共に、沈
澱した水酸化鉄フロックを濾過して廃液から重金属を除
去するにあたり、前記濾過された水酸化鉄スラッジをH
Cl溶液に溶解し、pHを調整して次ロットの廃液に添
加再使用し、以後、上記次ロットへの添加を所要複数回
繰り返して発生スラッジ量を低減させることにある。特
に請求項2に係る発明は、本発明の実施に最も効果的な
ものとして廃液に含まれる重金属が放射性物質である場
合である。That is, a feature of the present invention to achieve the above object is that iron chloride (FeCl 3 ) is added to a waste liquid containing heavy metals and neutralized by adding iron chloride (FeCl 3 ).
(OH) 3 ), and the iron hydroxide is brought into a floc state to adsorb and precipitate the various heavy metals contained therein. In addition, the precipitated iron hydroxide floc is filtered to remove heavy metals from the waste liquid, and the filtered water is used to remove heavy metals. H to iron oxide sludge
It is to dissolve in a Cl solution, adjust the pH, add to the waste liquid of the next lot and reuse it, and thereafter repeat the addition to the next lot a required number of times to reduce the amount of generated sludge. In particular, the invention according to claim 2 is the most effective one for implementing the present invention when the heavy metal contained in the waste liquid is a radioactive substance.
【0007】[0007]
【発明の実施の形態】以下、上記本発明方法の具体的態
様について詳述する。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, specific embodiments of the method of the present invention will be described in detail.
【0008】先ず本発明方法は従来、行われている廃液
にFeCl3を添加し、その後、中和して水酸化鉄を発
生させ、この水酸化鉄のフロック(綿状浮遊物)に各種
重金属を吸着沈澱させ、その後、濾過させる方法を基本
とするものである。First, according to the method of the present invention, FeCl 3 is added to a conventional waste liquid, and then neutralized to generate iron hydroxide. Various heavy metals are added to a floc of the iron hydroxide (a flocculent floating substance). Is adsorbed and precipitated, followed by filtration.
【0009】この方法は図1に示すように廃液を廃液槽
1に導入してHCl含有のFeCl 3を添加し、次いで
中和槽2においてNaOHにより中和して水酸化鉄Fe
(OH)3を発生させる。そして、この水酸化鉄を次の
シックナーと呼ばれる沈降槽3に送り、重金属を吸着し
た水酸化鉄のフロックを下部に沈澱させると共に、上部
の処理水を分離し、分離した上澄み液は管理値を確認
し、それ以下であれぱ排水する。In this method, as shown in FIG.
FeCl containing HCl 3And then
Neutralized with NaOH in neutralization tank 2
(OH)3Generate. And this iron hydroxide
It is sent to a settling tank 3 called a thickener to adsorb heavy metals
The floc of iron hydroxide precipitated at the bottom and
Separate the treated water and confirm the control value of the separated supernatant
And drain below that.
【0010】一方、沈降した重金属吸着の水酸化鉄フロ
ックは引き続きフィルタープレス等の濾過機4で濾過
し、水酸化鉄スラッジはそのまま保管し、絞り液は廃液
槽1に返される。On the other hand, the precipitated iron hydroxide flocs adsorbed on heavy metals are subsequently filtered by a filter 4 such as a filter press, and the iron hydroxide sludge is stored as it is, and the squeeze liquid is returned to the waste liquid tank 1.
【0011】ところで、この方法はスラッジの保管に問
題があることは前述の通りである。そこで、本発明方法
は上記の方法において、更に濾過後の工程を付加してい
る。即ち、以下の化学反応式で示す通り、一旦、発生し
た水酸化鉄スラッジをそのまま保管することなくHCl
で再度溶解し、これを繰り返し使用するものである。As described above, this method has a problem in storage of sludge. Therefore, the method of the present invention further includes a step after filtration in the above method. That is, as shown by the following chemical reaction formula, once the generated iron hydroxide sludge is
Is used again, and this is used repeatedly.
【0012】この本発明方法における原理的な化学反応
式を示すと、 FeCl3+NaOH→Fe(OH)3(重金属吸着除
去) Fe(OH)3+HCl→FeCl3 FeCl3+NaOH→Fe(OH)3(重金属吸着除
去) Fe(OH)3+HCl→FeCl3 の繰り返しである。The principle chemical reaction formula in the method of the present invention is as follows: FeCl 3 + NaOH → Fe (OH) 3 (adsorption removal of heavy metal) Fe (OH) 3 + HCl → FeCl 3 FeCl 3 + NaOH → Fe (OH) 3 (Heavy metal adsorption removal) This is a repetition of Fe (OH) 3 + HCl → FeCl 3 .
【0013】そのため、本発明方法においては、図1に
おいてフィルタープレス等の濾過機4に続いてpH調整
槽5が設けられ、濾過機4で濾過した重金属含有の水酸
化鉄スラッジをpH調整槽5に導入し、HClを添加す
ることによって、FeCl3を重金属吸着のまま、次ロ
ットの廃液を入れた当初の廃液槽1に還流することにあ
る。Therefore, in the method of the present invention, a pH adjusting tank 5 is provided following the filter 4 such as a filter press in FIG. 1, and the heavy metal-containing iron hydroxide sludge filtered by the filter 4 is supplied to the pH adjusting tank 5. And adding HCl to reflux the FeCl 3 to the initial waste liquid tank 1 containing the waste liquid of the next lot while keeping the heavy metal adsorbed.
【0014】そして、本発明方法は上記の如き使用した
FeCl3を基本的に所要複数回、例えば10回程度ま
で繰り返し使用することであり、これにより10回程度
繰り返すとすると、FeCl3の投入は初めの1回のみ
で排水10ロット分処理することが出来ることになり、
発生スラッジも従来の方法の1/10となる。このよう
にスラッジ発生量を例えば1/10に低減させることは
単にスラッジの低減のみでなく、スラッジの濾過、乾燥
等の処理作業上の負担も軽減させることになる。[0014] Then, the method of the present invention is essentially required several times a FeCl 3 was used such as described above, it is repeatedly used that for example up to about 10 times, when Thereby repeated about 10 times, introduction of FeCl 3 is Only the first one can process 10 lots of wastewater,
The generated sludge is 1/10 of the conventional method. Reducing the amount of sludge generation to, for example, 1/10 in this manner not only reduces sludge, but also reduces the burden on processing operations such as filtration and drying of sludge.
【0015】[0015]
【実施例】以下、ウラン廃液について本発明方法の実施
例を示す。先ず、ウラン廃液(ウラン放射能測定 6
6.8mBq/cc)にFeCl3の状態を保持させる
ため、HClを含有させたFeCl3液をpH2.2ま
で添加する。その後pH8までNaOHで中和させ、凝
集沈澱させた後、濾過し、次いで濾過したスラッジをH
Clで完全に溶解し、次ロットの廃液に添加し、中和後
濾過し、濾液の放射能測定を行った。そして、上記操作
を6回繰り返し実施した。その実施結果を図2に示す。EXAMPLES Examples of the method of the present invention for uranium waste liquid will be described below. First, uranium waste liquid (uranium radioactivity measurement 6
In order to maintain the state of FeCl 3 at 6.8 mBq / cc), an FeCl 3 solution containing HCl is added to pH 2.2. Thereafter, the mixture was neutralized with NaOH to pH 8 to cause coagulation and precipitation, followed by filtration.
It was completely dissolved with Cl, added to the waste liquid of the next lot, neutralized and filtered, and the filtrate was measured for radioactivity. Then, the above operation was repeated six times. FIG. 2 shows the results of the implementation.
【0016】同図2に見られるように6回実施したがウ
ランの除去率は殆ど変化していない。また、当然にスラ
ッジ吸着中の吸着ウラン等の重金属もHClに溶解し、
2回目以降は倍々にウラン初期濃度が上昇されると予想
されるが、ウラン初期濃度が上昇しても、ウラン除去率
に格別、影響を与えていないことが分かる。As shown in FIG. 2, the operation was performed six times, but the uranium removal rate hardly changed. Also, naturally, heavy metals such as uranium adsorbed during sludge adsorption also dissolve in HCl,
It is expected that the initial uranium concentration will increase twice after the second time, but it can be seen that the increase in the initial uranium concentration does not significantly affect the uranium removal rate.
【0017】以上の結果から、複数回、繰り返しスラッ
ジをHCl溶解再使用しても初めのロットと殆ど同じ結
果であることが分かる。なお、上記実施例は6回までの
繰り返しとなっているが、これは6回まで繰り返して効
果が同じであるため、その後、中止したためであり、充
分、10回又はそれ以上の繰り返しも可能であると思わ
れる。From the above results, it can be seen that even when the sludge is repeatedly reused by dissolving in HCl a plurality of times, the results are almost the same as those of the first lot. The above example is repeated up to six times, but this is because the same effect is obtained by repeating up to six times, and thereafter, the operation is stopped. Thus, ten or more repetitions are possible. It appears to be.
【0018】また、上記実施例はウランについて実施し
た場合であるが、ウランに限らず、他の放射性排水及び
一般重金属除去についても適応可能であることは容易に
推測できるところである。Further, although the above-described embodiment is a case where uranium is used, it is easy to guess that the present invention is not limited to uranium and can be applied to other radioactive wastewater and general heavy metal removal.
【0019】[0019]
【発明の効果】本発明は以上のように廃液から重金属を
化学的に除去するに際し発生した水酸化鉄スラッジを濾
過後、HClに溶解し、再度、処理に使用し、これを繰
り返して発生スラッジを低減させる方法であり、FeC
l3投入は初めの1回のみで再使用して排水を複数ロッ
ト処理することによりスラッジ発生量を従来に比し、大
幅に低減することがでると共に、スラッジ発生量の抑制
の結果、スラッジ処理操作も大幅に軽減される顕著な効
果を有する。According to the present invention, as described above, iron hydroxide sludge generated during the chemical removal of heavy metals from wastewater is filtered, dissolved in HCl, and used again for treatment. Is a method of reducing FeC
l 3 is turned relative to sludge formation amount conventionally by treating multiple batches wastewater reused only once at the beginning, significantly with it out to reduce, as a result of the sludge load suppression, sludge treatment The operation also has a noticeable effect that is greatly reduced.
【0020】しかも本発明方法によるスラッジが放射性
廃棄物の場合には従来に比し保管費用及び保管面積を大
幅に低減させる格段の有利さを有している。Furthermore, when the sludge produced by the method of the present invention is radioactive waste, there is a remarkable advantage that the storage cost and storage area are greatly reduced as compared with the prior art.
【図1】本発明方法の実施工程を示す概要説明図であ
る。FIG. 1 is a schematic explanatory view showing the steps of carrying out the method of the present invention.
【図2】繰り返し回数と処理後、濾液の放射能濃度の関
係を示す図表である。FIG. 2 is a chart showing the relationship between the number of repetitions and the radioactivity concentration of a filtrate after treatment.
1 廃液槽 3 沈降槽 4 濾過機 5 pH調整槽 Reference Signs List 1 waste liquid tank 3 sedimentation tank 4 filter 5 pH adjustment tank
Claims (2)
l3)を添加し、中和させて水酸化鉄(Fe(O
H)3)を発生させ、この水酸化鉄をフロック状態とし
て前記含有各種重金属を吸着沈澱させると共に、沈澱し
た水酸化鉄フロックを濾過して廃液から重金属を除去す
る方法において、前記濾過された水酸化鉄スラッジをH
Cl溶液に溶解し、pHを調整して次ロットの廃液に添
加再使用し、以後、上記次ロットの廃液への添加を所要
複数回繰り返して、発生スラッジ量を低減させることを
特徴とする廃液からの重金属除去時、発生するスラッジ
の低減方法。1. A waste liquid containing a heavy metal contains iron chloride (FeC).
l 3 ) and neutralized with iron hydroxide (Fe (O
H) 3 ), the iron hydroxide is brought into a floc state to adsorb and precipitate the various heavy metals contained therein, and the precipitated iron hydroxide floc is filtered to remove heavy metals from the waste liquid. H to iron oxide sludge
A waste liquid characterized by reducing the amount of generated sludge by dissolving in a Cl solution, adjusting the pH, adding to the waste liquid of the next lot and reusing it, and thereafter repeating addition to the waste liquid of the next lot a required number of times. Of sludge generated when removing heavy metals from wastewater.
る請求項1記載の廃液からの重金属除去時、発生するス
ラッジの低減方法。2. The method according to claim 1, wherein the heavy metals contained in the waste liquid are radioactive substances.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11055138A JP2000246262A (en) | 1999-03-03 | 1999-03-03 | Method of reducing sludge generated when removing heavy metals from waste liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11055138A JP2000246262A (en) | 1999-03-03 | 1999-03-03 | Method of reducing sludge generated when removing heavy metals from waste liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000246262A true JP2000246262A (en) | 2000-09-12 |
Family
ID=12990430
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11055138A Pending JP2000246262A (en) | 1999-03-03 | 1999-03-03 | Method of reducing sludge generated when removing heavy metals from waste liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000246262A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002172395A (en) * | 2000-12-05 | 2002-06-18 | Nec Environment Eng Ltd | Method for iron hydroxide flocculation and sedimentation treatment of thick inorganic component- containing wastewater |
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| JP2011512531A (en) * | 2008-02-18 | 2011-04-21 | コミッサリア ア ロンネルジー アトミック エ オ ゾンネルジー ザルテルナティーフ | The process of decontaminating radioactive liquid effluent to one or more radioactive chemical elements by solid-liquid extraction using a recycling loop |
| JP2012507000A (en) * | 2008-10-27 | 2012-03-22 | コミッサリア ア ロンネルジー アトミック エ オ ゾンネルジー ザルテルナティーフ | Method for decontamination of liquid effluent containing one or more radioactive chemical elements by treatment in a fluidized bed |
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| JP2013178222A (en) * | 2011-07-30 | 2013-09-09 | Fumihisa Terayama | Decontamination device and decontamination method of wood contaminated with radioactive material |
| JP2015200505A (en) * | 2014-04-04 | 2015-11-12 | 住友大阪セメント株式会社 | Method for treating waste liquid containing radioactive strontium |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002172395A (en) * | 2000-12-05 | 2002-06-18 | Nec Environment Eng Ltd | Method for iron hydroxide flocculation and sedimentation treatment of thick inorganic component- containing wastewater |
| JP2009103396A (en) * | 2007-10-25 | 2009-05-14 | Dakkusu:Kk | Duct pipe manufacturing method, duct pipe, duct pipe connection structure |
| JP2011512531A (en) * | 2008-02-18 | 2011-04-21 | コミッサリア ア ロンネルジー アトミック エ オ ゾンネルジー ザルテルナティーフ | The process of decontaminating radioactive liquid effluent to one or more radioactive chemical elements by solid-liquid extraction using a recycling loop |
| JP2012507000A (en) * | 2008-10-27 | 2012-03-22 | コミッサリア ア ロンネルジー アトミック エ オ ゾンネルジー ザルテルナティーフ | Method for decontamination of liquid effluent containing one or more radioactive chemical elements by treatment in a fluidized bed |
| KR101278014B1 (en) | 2011-06-28 | 2013-06-27 | 현대제철 주식회사 | Apparatus and method for treating wastewater |
| JP2013178222A (en) * | 2011-07-30 | 2013-09-09 | Fumihisa Terayama | Decontamination device and decontamination method of wood contaminated with radioactive material |
| JP2013178221A (en) * | 2011-07-30 | 2013-09-09 | Fumihisa Terayama | Decontamination device and decontamination method of solid matter contaminated with radioactive material |
| JP2013178223A (en) * | 2011-07-30 | 2013-09-09 | Fumihisa Terayama | Decontamination apparatus and decontamination method of contaminated water contaminated by radioactive substance |
| JP2015200505A (en) * | 2014-04-04 | 2015-11-12 | 住友大阪セメント株式会社 | Method for treating waste liquid containing radioactive strontium |
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