JPS58177193A - Removal of hydrazine from waste liquid - Google Patents
Removal of hydrazine from waste liquidInfo
- Publication number
- JPS58177193A JPS58177193A JP5910582A JP5910582A JPS58177193A JP S58177193 A JPS58177193 A JP S58177193A JP 5910582 A JP5910582 A JP 5910582A JP 5910582 A JP5910582 A JP 5910582A JP S58177193 A JPS58177193 A JP S58177193A
- Authority
- JP
- Japan
- Prior art keywords
- waste liquid
- line
- hydrazine
- liquid
- tank
- 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
- Water Treatment By Sorption (AREA)
Abstract
Description
【発明の詳細な説明】 活性炭で吸着除去する方法に関する。[Detailed description of the invention] This article relates to a method of adsorption removal using activated carbon.
火力発電プラ/トにおいては.クリー/アノプ時の水洗
液や休止中の満水保存液には,腐食防食対策のために定
常運転時よりも非常に高濃度のヒドラジン含有水を使用
している。このヒドランン含有水は,プラントの定常運
転に入る前に廃液として排出される。このような廃液中
のヒドラジノはCOD負荷成分であるため,排出に際し
, に01)を規制値内゛まで下げるだめの廃液処理
が必要である。In thermal power generation platforms. Water containing hydrazine at a much higher concentration than during normal operation is used for the rinsing solution during Cree/Anop operation and for the full-water storage solution during rest periods to prevent corrosion. This hydrane-containing water is discharged as waste liquid before the plant enters steady operation. Since hydrazino in such waste liquid is a COD loading component, it is necessary to treat the waste liquid to reduce the 01) to within the regulated value when discharging it.
従来.このような廃液中のヒドラジンの処理方法として
は,次亜塩素酸ノーダ法により行なわれている。すなわ
ち、ヒドラジ/廃液に次亜塩素酸ソーダ溶液をヒドラジ
/に対し当量添加し,エアレー/ヨ/をしつつCODの
低減を見極めてから塩酸でPHを調整して放流する方法
である。しかし、この方法では,次亜塩素酸ソーダ溶液
をヒドラジ/に対して当量添加後, CODの規制値
まで低減するのにかなりの時間を必要としている。Conventional. As a method for treating hydrazine in such waste liquid, the hypochlorous acid nodal method is used. That is, this is a method in which a sodium hypochlorite solution is added to the hydrazine/waste solution in an amount equivalent to the hydrazine/hydrazine, and the COD reduction is determined while air-raying/y/o/, and the pH is adjusted with hydrochloric acid before being discharged. However, with this method, it takes a considerable amount of time to reduce COD to the regulation value after adding an equivalent amount of sodium hypochlorite solution to hydrazine.
本発明の目的は,上記のような欠点を解消し。The object of the present invention is to eliminate the above-mentioned drawbacks.
ジ/を含む廃液中からヒドラジ/を除去する方法におい
て,前記廃液を活性炭に接着させ,廃液中のヒドラジ7
を活性炭に吸着ぎせて除去することを特徴とする廃液中
のヒドラジ/の除去方法を提供する。In a method for removing hydrazi/ from a waste liquid containing hydrazi, the waste liquid is adhered to activated carbon, and the
Provided is a method for removing hydrazide from a waste liquid, which is characterized in that hydrazide is removed by adsorption on activated carbon.
本発明者等は、活性炭により水中の溶存酸素を吸着させ
除去する研究実験を実施してきた。The present inventors have conducted research experiments in which dissolved oxygen in water is adsorbed and removed using activated carbon.
この溶存酸素は、ヒドラジ/と活性炭との組み合せによ
り分解除去できる事を見い出したが。It has been found that this dissolved oxygen can be decomposed and removed by a combination of hydrazi and activated carbon.
この研究実験段階で、ヒドラジ/のみでも活性炭に短時
間で吸着するという結果を得た。そごで2本発明者等は
、この結果に着目し9本発明に至ったものである。At this research and experimental stage, we obtained the result that even hydrazide/alone was adsorbed onto activated carbon in a short period of time. The inventors of the present invention have focused on this result and have arrived at the present invention.
次に本発明方法の一実施例を図面に基いて説明する。Next, an embodiment of the method of the present invention will be explained based on the drawings.
第1図に示すフローシートに従って説明する。This will be explained according to the flow sheet shown in FIG.
第1図において、1は、水洗液や満水保存液を受ける廃
液貯槽で、ライ/2より集められる。In FIG. 1, 1 is a waste liquid storage tank that receives washing liquid and full-water storage liquid, and is collected from Lie/2.
通常この廃液は、ポンプ3により、ライン4゜パルプ6
を通して廃液処理槽6へ送液され、この廃液処理槽6で
薬品投入後、規制値以下に処・:・1
理てれた後、ライ/7よ□り放流される。Normally, this waste liquid is pumped to line 4゜pulp 6 by pump 3.
The liquid is sent to the waste liquid treatment tank 6 through the waste liquid treatment tank 6, where it is treated to below the regulation value after being charged with chemicals.
本発明では、廃液の送液ライ/4より、バルブ8.ライ
/9全通して、活性炭の充填塔10を経た後、ライフ】
1を通して廃液処理槽6へ導くライ/を設置し、廃液中
のヒドラジ7を活性炭の充填塔10で吸着させ除去する
ものである。In the present invention, valve 8. Life]
1 is installed to lead the waste liquid to a waste liquid treatment tank 6, and the hydrazide 7 in the waste liquid is adsorbed and removed by an activated carbon packed column 10.
第2図は9本発明方法によりカラム連続通水法によるヒ
ドラジンの除去試験を行なったl実験例を示す。以下、
第2図に従って説明する。FIG. 2 shows an experimental example in which a hydrazine removal test was carried out using the column continuous water flow method according to the method of the present invention. below,
This will be explained according to FIG.
こ\で第1表に実験に使用した活性炭の充填密度及び粒
度の関係を示す。Table 1 shows the relationship between the packing density and particle size of the activated carbon used in the experiment.
第2図において、被処理水タンク20に、ヒドラジノを
含む被処理水21を用意し、ライン221φ
を通しポンプ2′3でカラム24に連続通水する。In FIG. 2, treated water 21 containing hydrazino is prepared in a treated water tank 20, and is continuously passed through a line 221φ to a column 24 by a pump 2'3.
カラム24には第1表で示した活性炭25が500m1
充填してあり、扱処理水21中のヒドンシフをカラム2
4中で活性炭25と接触させた後、ライン26より出て
きた処理水をサノプリノグし、よう素滴定法により残存
するヒドラジン濃度を分。Column 24 contains 500 ml of activated carbon 25 shown in Table 1.
Hidden Schiff in treated water 21 is removed from column 2.
After contacting with activated carbon 25 in 4, the treated water coming out from line 26 was subjected to Sanoprinog, and the remaining hydrazine concentration was determined by iodine titration.
析した。analyzed.
上記カラム連続通水試験での除去試験結果を第3図に示
す。第3図において7曲線Aは、frしい活性炭を使用
し、′被処理水中のヒドラジ/濃度を200ppmに調
整し、 5V=20の条件で除去試験を行なった結果で
ある。また1曲線Bは。The results of the removal test in the above column continuous water flow test are shown in FIG. In FIG. 3, curve 7 A is the result of a removal test conducted under the condition of 5V=20 using fresh activated carbon and adjusting the hydrazine concentration in the water to be treated to 200 ppm. Also, curve 1 is B.
曲線Aの条件で試験を行なった後の活性炭を。Activated carbon after testing under the conditions of curve A.
一般的に公知な方法である熱水、水蒸気27等を再生用
配管28を介してカラム24に供給し活性炭25を再生
した後、上記条件で除去試験を行なった結果である。These are the results of a removal test conducted under the above conditions after the activated carbon 25 was regenerated by supplying hot water, steam 27, etc. to the column 24 via the regeneration piping 28 using a generally known method.
第3図の結果から、活性炭500−に対して10tの廃
液を処理できることを示している。これは9例えば、活
性炭1トンでヒドラジンを含む廃液(ヒドラジ/濃度2
00ppm)を42゛ト/処理することか可能であるこ
とを示す。1だ再生後の活性炭は吸着能力は5〜7%程
度悪くなるが、新しい活性炭と同程度の吸着能力を持つ
ところまで回復することがわかる。The results shown in FIG. 3 show that 10 tons of waste liquid can be treated for 500 tons of activated carbon. 9 For example, if 1 ton of activated carbon is used, waste liquid containing hydrazine (hydrazine/concentration 2
00 ppm) at a rate of 42 tons/process. It can be seen that the adsorption capacity of the activated carbon after one-day regeneration deteriorates by about 5 to 7%, but it recovers to the point where it has the same adsorption capacity as new activated carbon.
以上のように1本発明によれば、 200ppm程度
のヒドラジノを含むような廃液は、活性炭1トノ当りで
4.2トン処理可能であり、また、再生後の吸着能力は
新しト活性炭に比べ5〜7チ減少する程度であるため繰
返し使用が可能である。As described above, according to the present invention, it is possible to treat 4.2 tons of waste liquid containing about 200 ppm of hydrazino per ton of activated carbon, and the adsorption capacity after regeneration is higher than that of fresh activated carbon. Since the amount decreases by only 5 to 7 inches, it can be used repeatedly.
これらのことにより、廃液中のヒドラジンを除去する方
法として活性炭の利用は有効な方法であることがわかる
。These results show that the use of activated carbon is an effective method for removing hydrazine from waste liquid.
なお本発明は9例えば火J発電プラ/トのクリ−772
1時の水洗液や、休止中の満水保存液、あるいはディー
ゼル機関冷却水、軸冷却水などの腐食防食対策として使
用する高濃度のヒドラジ/含有廃液からヒドラジノを除
去する場合等に適用できる。Note that the present invention applies to 9, for example, the Cree-772 of the Tue J power generation platform.
It can be applied to the case of removing hydrazino from the 1-hour washing liquid, the full-water storage liquid during rest, or the highly concentrated hydrazi-containing waste liquid used as a corrosion protection measure for diesel engine cooling water, shaft cooling water, etc.
第1図は2本発明の一実施例を示すフローンート。第2
図は1本発明を実施するだめの実験装置を示すフローン
ート、第3図は、第2図の実験装置を用いて試験を行な
った実験データを示す線図である。
l・・廃液貯槽、2・・・廃液注入ライ/、6・・・廃
液処理槽、7・・・処理液放流ライン、10・・・活性
炭充填塔、 20・・・被処理水タンク、21・・被
処理水。
24・・・カラム、25・・・活性炭、27・・・再生
用熱水。
水蒸気、28・・・再生用配管。
才1図
7
2
牙27
手続補正書(自9:)
昭和67 412 月 72EI
特許庁 若杉和夫殿
事例の表示
昭和57年 特 許 願第 59105
号発明の名称
廃液中のヒドラジノの除去方法
補正をする者
串4Llとの関係 特許出願人
住 所 東京都T代111[ズ丸の内=J]1
5番113名 称(620)三菱重工業株式会社
代 理 人
住 所 同 上
(1) 明細書第3ペー/第14行の「ライン2より
集められる。」を[廃液はライン2.1m ’J 災め
られる。」と訂正する。
(2) 同上第5ページ第19行の「42」を[、l
12.Jと訂正する。
(3) 同上第6ページ第7行の142」を「42」
と訂正する。FIG. 1 is a flow route showing an embodiment of the present invention. Second
1 is a flow route showing an experimental apparatus for carrying out the present invention, and FIG. 3 is a diagram showing experimental data obtained by conducting a test using the experimental apparatus shown in FIG. 2. l... Waste liquid storage tank, 2... Waste liquid injection line/, 6... Waste liquid treatment tank, 7... Treated liquid discharge line, 10... Activated carbon packed tower, 20... Water tank to be treated, 21 ...Water to be treated. 24... Column, 25... Activated carbon, 27... Hot water for regeneration. Steam, 28... Piping for regeneration. 1 Figure 7 2 Fang 27 Procedural amendment (J9:) December 1987 72EI Patent Office Case presentation by Mr. Kazuo Wakasugi 1981 Patent Application No. 59105
Title of invention Name of method for removing hydrazino in waste liquid Relationship with Kushi 4Ll Patent applicant address Tokyo, T-dai 111 [Zu Marunouchi = J] 1
No. 5 113 Name (620) Representative of Mitsubishi Heavy Industries, Ltd. Address Same as above (1) Change "Waste liquid will be collected from line 2" on page 3/line 14 of the specification [waste liquid will be collected from line 2.1 m'J It will be a disaster. ” he corrected. (2) Replace “42” in the 19th line of page 5 with [, l
12. Correct it with J. (3) ``142'' in the 7th line of the 6th page of the same page as ``42''
I am corrected.
Claims (1)
において、前記廃液を活性炭に接着させ、廃液中のヒド
ラジンを活性炭に吸着させて除去することを特徴とする
廃液中のヒドラジンの除去方法。A method for removing hydrazine from a waste liquid containing hydrazine, the method comprising adhering the waste liquid to activated carbon, and removing hydrazine in the waste liquid by adsorbing it to the activated carbon.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5910582A JPS58177193A (en) | 1982-04-09 | 1982-04-09 | Removal of hydrazine from waste liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5910582A JPS58177193A (en) | 1982-04-09 | 1982-04-09 | Removal of hydrazine from waste liquid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58177193A true JPS58177193A (en) | 1983-10-17 |
Family
ID=13103700
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5910582A Pending JPS58177193A (en) | 1982-04-09 | 1982-04-09 | Removal of hydrazine from waste liquid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58177193A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007106682A (en) * | 2005-10-11 | 2007-04-26 | Asahi Kasei Chemicals Corp | Hydrazine derivative composition |
WO2009051958A1 (en) * | 2007-10-19 | 2009-04-23 | E. I. Du Pont De Nemours And Company | Method for removing hydrazine compounds |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5423071A (en) * | 1977-07-21 | 1979-02-21 | Ebara Infilco Co Ltd | Treating method for waste liquid contained hydrazine |
-
1982
- 1982-04-09 JP JP5910582A patent/JPS58177193A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5423071A (en) * | 1977-07-21 | 1979-02-21 | Ebara Infilco Co Ltd | Treating method for waste liquid contained hydrazine |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007106682A (en) * | 2005-10-11 | 2007-04-26 | Asahi Kasei Chemicals Corp | Hydrazine derivative composition |
WO2009051958A1 (en) * | 2007-10-19 | 2009-04-23 | E. I. Du Pont De Nemours And Company | Method for removing hydrazine compounds |
US7758757B2 (en) | 2007-10-19 | 2010-07-20 | E. I. Du Pont De Nemours And Company | Method for removing hydrazine compounds |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4556492A (en) | Deoxygenation process | |
US3401101A (en) | Separation of hydrogen sulfide and mercaptans from fluid streams | |
JP5431208B2 (en) | Ballast water treatment equipment | |
JPS58177193A (en) | Removal of hydrazine from waste liquid | |
US4818411A (en) | Deoxygenation process | |
CN108439540A (en) | A kind of reverse osmosis concentrated saline water treatment device of cold rolling wastewater and method | |
US3956115A (en) | Process for the regeneration of ion-exchange resins and applications thereof | |
JPH11169848A (en) | Nitric acid containing waste water treating device and treating method | |
JP4511881B2 (en) | Wastewater treatment method | |
JPS5851904A (en) | Method for washing membrane surface of membrane separation apparatus | |
JPH1147589A (en) | Regeneration pretreatment of activated carbon | |
JP2601879B2 (en) | Anaerobic treatment equipment for organic wastewater | |
JP2019098248A (en) | Modifier of platinum group catalyst for water treatment, catalyst modification device, modification method of platinum group catalyst for water treatment, water treatment system, and water treatment method | |
JP2000294266A (en) | Method and device for recovering energy | |
JP7274379B2 (en) | water treatment method | |
JPS60102945A (en) | Catalyst regenerating method | |
JPS58223483A (en) | Removing method of hydrazine in waste liquid | |
JPH11216372A (en) | Treatment method for preventing oxidative deterioration of cation exchange resin by oxidizing agent | |
JPS59162946A (en) | Regeneration of activated carbon having hydrazine adsorbed therein | |
JP6543363B2 (en) | Nuclear power spent fuel pool water purification method and device and spent fuel pool water treatment method and device | |
JP3366204B2 (en) | Ammonia-containing waste liquid treatment method | |
JPS6057369B2 (en) | How to regenerate activated carbon | |
JPS5827039A (en) | Hydraulic pressure tester | |
JPS5943233B2 (en) | Wastewater treatment equipment containing residual chlorine | |
JPH0124607Y2 (en) |