Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3360608B2 - Cleaning method for water treatment equipment - Google Patents
[go: Go Back, main page]

JP3360608B2 - Cleaning method for water treatment equipment - Google Patents

Cleaning method for water treatment equipment

Info

Publication number
JP3360608B2
JP3360608B2 JP13160698A JP13160698A JP3360608B2 JP 3360608 B2 JP3360608 B2 JP 3360608B2 JP 13160698 A JP13160698 A JP 13160698A JP 13160698 A JP13160698 A JP 13160698A JP 3360608 B2 JP3360608 B2 JP 3360608B2
Authority
JP
Japan
Prior art keywords
water
iron metal
metal particles
cleaning
air
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.)
Expired - Fee Related
Application number
JP13160698A
Other languages
Japanese (ja)
Other versions
JPH11319856A (en
Inventor
洋 黒部
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP13160698A priority Critical patent/JP3360608B2/en
Publication of JPH11319856A publication Critical patent/JPH11319856A/en
Application granted granted Critical
Publication of JP3360608B2 publication Critical patent/JP3360608B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、水処理装置の洗浄
方法に関する。さらに詳しくは、本発明は、鉄金属粒子
の充填層に通水して水中の不純物を還元処理する水処理
装置において、充填した鉄金属粒子がブロック状の塊を
形成することを効果的に防止することができる水処理装
置の洗浄方法に関する。
[0001] The present invention relates to a method for cleaning a water treatment apparatus. More specifically, the present invention provides a water treatment apparatus for reducing impurities in water by passing water through a packed bed of iron metal particles, and effectively prevents the filled iron metal particles from forming block-like lumps. The present invention relates to a method of cleaning a water treatment apparatus that can perform the treatment.

【0002】[0002]

【従来の技術】石炭又は石油を燃焼した際に発生する排
ガスの脱硫装置などから排出される排水は、重金属類、
非金属類などの種々の有害物質を含有するので、排水よ
りこれらの有害物質を除去する必要がある。排水にペル
オキソ硫酸、ヨウ素酸、セレン酸、硝酸などが含まれて
いる場合は、これらの有害物質を含む排水のpHを5以下
に調整して鉄金属と接触させたのち、凝集処理及び固液
分離を行うことにより、排水中のペルオキソ硫酸、ヨウ
素酸、セレン酸、硝酸などが溶出した2価の鉄イオンに
よって還元され、さらに、凝集処理により水中に溶解し
ている鉄イオンを水不溶性の水酸化鉄として沈殿させる
とき、重金属、フッ素などの有害物質も同時に効率的に
除去される。排水を鉄金属と接触させる方法としては、
反応槽において排水に鉄金属微粒子を添加して撹拌する
撹拌接触法と、排水を鉄金属粒子の充填層に通水する通
水接触法が知られている。撹拌接触法は、充填層の洗浄
操作は不要であるが、還元反応が十分でなく、排水中の
有害物質の除去が通水接触法にくらべて劣る上に、鉄金
属微粒子の添加量や、鉄金属微粒子を均一に分散させる
ための撹拌強度を管理したり、分散した鉄金属微粒子の
流出を防止するなど、運転管理上の問題が多い。これに
対して、鉄金属粒子の充填層に通水する通水接触法は、
運転管理が比較的容易であり、通水初期には排水中の有
害物質が効率的に除去されるが、長時間通水を続けると
鉄金属粒子の表面に汚染物質が付着したり、目詰まりを
生じたりして、排水処理効率が低下するという問題があ
る。本発明者らは、先に特開平9−323090号公報
において、鉄金属粒子表面に付着した汚染物質を容易に
剥離除去することができ、安定して排水中の有害物質を
除去することができる水処理装置の洗浄方法として、充
填層に洗浄水を通水して洗浄したのち、さらに洗浄水及
び空気の混合流を上向流で供給し、鉄金属粒子の充填層
の汚染物質を除去する水処理装置の洗浄方法を提案し
た。この方法により、排水処理を安定して行うことが可
能となったが、排水中に硝酸体窒素が高濃度に含まれる
場合など、排水の水質によっては、処理時に充填層の鉄
金属粒子がブロック状の塊を形成するという現象を生じ
た。鉄金属粒子がブロック状の塊を形成すると排水との
接触が不十分となって排水処理のために有効に使用され
ず、さらに、充填層内に鉄の塊として残留するという問
題が生ずる。鉄金属粒子のブロック状の塊は、通常の洗
浄方法によっては、ほぐすことができないので、鉄金属
粒子が充填層内でブロック状の塊を形成することのな
い、運転管理が容易な水処理装置の洗浄方法が求められ
ていた。
2. Description of the Related Art Wastewater discharged from a desulfurization device for exhaust gas generated when coal or oil is burned includes heavy metals,
Since it contains various harmful substances such as nonmetals, it is necessary to remove these harmful substances from wastewater. If the wastewater contains peroxosulfuric acid, iodic acid, selenic acid, nitric acid, etc., adjust the pH of the wastewater containing these harmful substances to 5 or less and bring it into contact with iron metal, then coagulate and solid-liquid By performing the separation, peroxosulfuric acid, iodic acid, selenic acid, nitric acid and the like in the wastewater are reduced by the divalent iron ions eluted, and the iron ions dissolved in the water due to the coagulation treatment are removed from the water-insoluble water. When precipitated as iron oxide, harmful substances such as heavy metals and fluorine are also efficiently removed at the same time. As a method of bringing wastewater into contact with ferrous metal,
There are known a stirring contact method in which iron metal fine particles are added to wastewater in a reaction tank and stirring, and a water contact method in which wastewater is passed through a packed bed of iron metal particles. The stirring contact method does not require a washing operation of the packed bed, but the reduction reaction is not sufficient, the removal of harmful substances in the wastewater is inferior to the water contact method, and the addition amount of iron metal fine particles, There are many problems in operation management such as controlling the stirring intensity for uniformly dispersing the iron metal fine particles and preventing the dispersed iron metal fine particles from flowing out. On the other hand, the water contact method of passing water through the packed bed of iron metal particles is as follows:
Operation management is relatively easy, and harmful substances in wastewater are efficiently removed at the beginning of water passage.However, if water continues to flow for a long time, pollutants may adhere to the surface of iron metal particles or clogging may occur. And the efficiency of wastewater treatment is reduced. The present inventors have previously disclosed in Japanese Patent Application Laid-Open No. 9-323090 that contaminants attached to the surface of iron metal particles can be easily peeled and removed, and harmful substances in wastewater can be stably removed. As a washing method of the water treatment apparatus, after washing water is passed through the packed bed and washed, a mixed flow of washing water and air is further supplied in an upward flow to remove contaminants in the packed bed of iron metal particles. A cleaning method for water treatment equipment was proposed. By this method, the wastewater treatment can be performed stably, but depending on the quality of the wastewater, such as when the wastewater contains a high concentration of nitrate nitrogen, the iron metal particles in the packed bed are blocked during the treatment. A phenomenon of forming a lumpy mass occurred. When the iron metal particles form a block-like mass, the contact with the wastewater becomes insufficient, so that the wastewater is not effectively used for wastewater treatment, and further, there is a problem that the iron metal particle remains in the packed bed as an iron mass. Since the block-like lump of iron metal particles cannot be loosened by a normal washing method, the water treatment device which does not form the block-like lump in the packed bed and is easy to operate and manage. There has been a demand for a cleaning method.

【0003】[0003]

【発明が解決しようとする課題】本発明は、鉄金属粒子
の充填層に通水して排水中の不純物を還元処理する水処
理装置において、排水を鉄金属粒子と接触しても、鉄金
属粒子がブロック状の塊を形成することなく、運転管理
が容易な水処理装置の洗浄方法を提供することを目的と
してなされたものである。
SUMMARY OF THE INVENTION The present invention relates to a water treatment apparatus for reducing impurities in wastewater by passing water through a packed bed of iron metal particles. An object of the present invention is to provide a method for cleaning a water treatment apparatus, in which particles do not form block-like lumps and operation management is easy.

【0004】[0004]

【課題を解決するための手段】本発明者は、上記の課題
を解決すべく鋭意研究を重ねた結果、鉄金属粒子の充填
層に空気を通じて充填層をほぐしたのち、洗浄水と空気
の混合気体を上向流で供給するという操作を1日に2回
以上行うことにより、鉄金属粒子がブロック状の塊を形
成する前にほぐされ、鉄金属粒子のブロック状の塊が形
成されなくなることを見いだし、この知見に基づいて本
発明を完成するに至った。すなわち、本発明は、 (1)鉄金属粒子の充填層に通水して排水中の不純物を
還元処理する水処理装置において、充填層に通気速度
が、LV=50〜200m/hで、5秒〜1分間空気を
通じて鉄金属粒子の充填層をほぐしたのち、さらに洗浄
水及び空気の混合流を上向流で供給し、鉄金属粒子の充
填層の汚染物質を除去する洗浄を、1日に2回以上の頻
度で行うことを特徴とする水処理装置の洗浄方法、 (2)洗浄水及び空気の混合流による洗浄を行ったの
ち、さらに洗浄水のみによる洗浄を行うことを特徴とす
る第1項記載の水処理装置の洗浄方法、及び、 (3)排水を酸性に調整して鉄金属粒子の充填層に通水
することを特徴とする第1項又は第2項記載の水処理装
置の洗浄方法、を提供するものである。さらに、本発明
の好ましい態様として、 (4)排水のpHを5以下に調整する第1項記載の水処理
装置の洗浄方法、 (5)洗浄水及び空気の混合流の供給において、洗浄水
の供給速度が、LV=30〜150m/hである第1項
記載の水処理装置の洗浄方法、 (6)洗浄水及び空気の混合流の供給において、空気の
供給速度が、LV=50〜200m/hである第1項記
載の水処理装置の洗浄方法、及び、 (7)洗浄水及び空気の混合流の供給を、30秒〜5分
間行う第1項記載の水処理装置の洗浄方法、を挙げるこ
とができる。
Means for Solving the Problems As a result of intensive studies to solve the above-mentioned problems, the present inventor dissolves the packed bed of iron metal particles by passing air through the packed bed, and then mixes washing water with air. By performing the operation of supplying the gas in an upward flow twice or more a day, the iron metal particles are loosened before forming the block-like mass, and the block-like mass of the iron metal particle is not formed. And completed the present invention on the basis of this finding. That is, the present invention provides: (1) a water treatment apparatus for reducing impurities in wastewater by passing water through a packed bed of iron metal particles; After loosening the packed bed of iron metal particles through air for 1 second to 1 minute, washing is performed for 1 day to remove contaminants from the packed bed of iron metal particles by supplying a mixed flow of washing water and air in an upward flow. (2) a method of cleaning a water treatment apparatus, wherein the cleaning is performed twice or more times; (2) cleaning is performed using a mixed flow of cleaning water and air, and then cleaning is performed using only cleaning water. 3. The method for cleaning a water treatment device according to item 1, and (3) the water treatment according to item 1 or 2, wherein the wastewater is adjusted to be acidic and water is passed through a packed bed of iron metal particles. A method of cleaning the apparatus. Further, as a preferred embodiment of the present invention, (4) the method for cleaning a water treatment apparatus according to item 1, wherein the pH of the wastewater is adjusted to 5 or less; (5) in the supply of a mixed flow of the cleaning water and the air, 2. The method for cleaning a water treatment apparatus according to claim 1, wherein the supply speed is LV = 30 to 150 m / h. (6) In the supply of a mixed flow of cleaning water and air, the supply speed of air is LV = 50 to 200 m. / H, the method for cleaning a water treatment apparatus according to item 1, wherein the supply of a mixed flow of cleaning water and air is performed for 30 seconds to 5 minutes. Can be mentioned.

【0005】[0005]

【発明の実施の形態】本発明方法は、排水を鉄金属粒子
の充填層に通水して、排水中の不純物を還元処理する水
処理装置の洗浄に使用することができる。排水を酸性、
好ましくはpHを5以下に調整し、鉄金属と接触させる
と、鉄金属より次式にしたがって2価の鉄イオンが水中
に溶出する。 Fe+2H+ → Fe2++H2 排水中に含まれるペルオキソ硫酸、ヨウ素酸、セレン酸
及び硝酸は、それぞれ以下に示す式にしたがって2価の
鉄イオンと反応し、還元処理される。 S28 2-+2Fe2+ → 2SO4 2-+2Fe3+ 2IO3 -+10Fe2++12H+ → I2+10Fe3+
6H2O SeO4 2-+6Fe2++8H+ → Se0+6Fe3++4
2O NO3 -+4Fe2++6H+ → NH4 ++4Fe3++O2
2O さらに、酸化還元電位が−400〜−100mVの場合
は、次式にしたがって鉄金属とセレン酸の反応が起こ
る。 SeO4 2-+3Fe+8H+ → Se0+3Fe2++4H2
O このようにして排水中に含まれる不純物を鉄金属と接触
して還元処理したのち、還元処理水にアルカリ剤を添加
してpHを7以上とすると、水中の鉄イオンは、例えば、
下記の式のように水不溶性の水酸化鉄となってフロック
を形成する。 Fe2++2NaOH → Fe(OH)2+2Na+ Fe3++3NaOH → Fe(OH)3+3Na+ このとき、還元されたセレンのほか、排水中に含まれる
重金属類、懸濁物質、フッ素、COD成分なども同時に
凝集、沈降して分離することができる。
BEST MODE FOR CARRYING OUT THE INVENTION The method of the present invention can be used for washing a water treatment apparatus for passing wastewater through a packed bed of iron metal particles to reduce impurities in the wastewater. Acid wastewater,
When the pH is preferably adjusted to 5 or less and brought into contact with iron metal, divalent iron ions elute from the iron metal into water according to the following formula. Fe + 2H + → Fe 2+ + H 2 Peroxosulfuric acid, iodic acid, selenic acid and nitric acid contained in the waste water react with divalent iron ions according to the following formulas, respectively, and are reduced. S 2 O 8 2- + 2Fe 2+ → 2SO 4 2- + 2Fe 3+ 2IO 3 + 10Fe 2+ + 12H + → I 2 + 10Fe 3+ +
6H 2 O SeO 4 2- + 6Fe 2+ + 8H + → Se 0 + 6Fe 3+ +4
H 2 O NO 3 + 4Fe 2+ + 6H + → NH 4 + + 4Fe 3+ + O 2 +
H 2 O In addition, if the redox potential of -400 to-100 mV, the reaction of ferrous metals and selenium acids takes place according to the following equation. SeO 4 2- + 3Fe + 8H + → Se 0 + 3Fe 2+ + 4H 2
O After the impurities contained in the wastewater are brought into contact with the iron metal and reduced as described above, if an alkaline agent is added to the reduced water and the pH is adjusted to 7 or more, iron ions in the water are, for example,
It becomes water-insoluble iron hydroxide to form flocs as shown in the following formula. Fe 2+ + 2NaOH → Fe (OH) 2 + 2Na + Fe 3+ + 3NaOH → Fe (OH) 3 + 3Na + At this time, in addition to reduced selenium, heavy metals, suspended solids, fluorine and COD components contained in wastewater Etc. can be simultaneously separated by aggregation and sedimentation.

【0006】本発明方法において、排水を接触させる鉄
金属粒子としては、純鉄、粗鋼、合金鋼、その他の鉄合
金などの粒子を挙げることができる。鉄金属が鉄合金で
あるときは、鉄の含有率が85重量%以上であることが
好ましい。排水を鉄金属粒子を充填したカラムなど、鉄
金属粒子の充填層に通水することにより、排水と鉄金属
粒子の接触を効率的に行うことができる。しかし、鉄金
属粒子の充填層に排水の通水を続けると、汚染物質の鉄
金属粒子の表面への付着や、鉄金属粒子の充填層の目詰
まりなどが生じ、排水中の不純物の除去効率が次第に低
下してくる。このような汚染物質には、鉄金属又は鉄イ
オンの反応により生成する酸化鉄、炭化鉄、硫化鉄や、
排水中の懸濁物質などがある。本発明方法においては、
鉄金属粒子の充填層に排水を通水し、不純物の還元処理
を続けたのち、排水の通水を停止し、鉄金属粒子の充填
層に空気を通じて鉄金属粒子の充填層をほぐし、さらに
洗浄水及び空気の混合流を上向流で供給し、鉄金属粒子
の表面に付着した汚染物質を剥離、除去し、あるいは、
鉄金属粒子の充填層に目詰まりを起こしている汚染物質
を除去する。本発明方法において、排水の通水を停止
し、鉄金属粒子の充填層に空気を通じることにより、鉄
金属粒子がブロック状の塊を形成する前に鉄金属粒子の
充填層がほぐされ、ブロック状の塊の形成を防止するこ
とができる。排水中に硝酸体窒素が含まれる場合は、鉄
金属粒子は特にブロック状の塊を形成しやすいが、鉄金
属粒子の充填層に空気を通じることにより、数百mg/リ
ットル程度の硝酸体窒素を含む排水を処理しても鉄金属
粒子のブロック状の塊の形成を防止することができる。
In the method of the present invention, examples of the iron metal particles to be brought into contact with drainage include particles of pure iron, crude steel, alloy steel, and other iron alloys. When the iron metal is an iron alloy, the iron content is preferably 85% by weight or more. By passing the wastewater through a packed bed of iron metal particles, such as a column filled with iron metal particles, it is possible to efficiently contact the wastewater with the iron metal particles. However, if the water continues to flow through the packed bed of iron metal particles, contaminants will adhere to the surface of the iron metal particles and clogging of the packed bed of iron metal particles will occur. Gradually decrease. Such contaminants include iron oxides, iron carbides, iron sulfides produced by the reaction of iron metal or iron ions,
There are suspended substances in wastewater. In the method of the present invention,
After passing the wastewater through the bed of iron metal particles and continuing the reduction treatment of impurities, stop the flow of wastewater, loosen the bed of iron metal particles by passing air through the bed of iron metal particles, and further wash A mixed flow of water and air is supplied in an upward flow to separate and remove contaminants adhering to the surface of iron metal particles, or
Remove contaminants that are clogging the packed bed of iron metal particles. In the method of the present invention, by stopping the flow of the wastewater and passing air through the packed layer of the iron metal particles, the packed layer of the iron metal particles is loosened before the iron metal particles form a block-like mass, and the block is formed. It is possible to prevent the formation of a lumpy mass. When nitrate nitrogen is contained in the wastewater, the iron metal particles are particularly likely to form block-like lumps. However, by passing air through the packed bed of iron metal particles, nitrate nitrogen of about several hundred mg / liter can be obtained. The formation of block-like lumps of iron metal particles can be prevented even when treating wastewater containing.

【0007】本発明方法において、鉄金属粒子の充填層
に空気を通じるときの流れ方向には特に制限はなく、上
向流又は下向流のいずれともすることができる。しか
し、通気方向を上向流とすることにより、鉄金属粒子の
充填層を効果的にほぐすことができ、また、酸性に調整
した排水の通水は、水素ガスが発生するため通常は上向
流で行い、さらに、洗浄水及び空気の混合流の供給も上
向流で行うので、設備設計及び運転管理上からも、鉄金
属粒子の充填層への通気は上向流とすることが好まし
い。本発明方法において、鉄金属粒子の充填層をほぐす
ための通気速度は、LV=50〜200m/hとするこ
とが好ましい。通気速度が50m/h未満であると、鉄
金属粒子の充填層が十分にほぐされず、ブロック状の塊
が発生するおそれがある。通気速度が200m/hを超
えると、消費する動力が多くなる上に、微小化された鉄
金属粒子が飛散するおそれがある。通気時間は、5秒〜
1分間とすることが好ましい。通気が5秒間未満である
と、鉄金属粒子の充填層が十分にほぐされず、ブロック
状の塊が発生するおそれがある。通気は、通常は1分間
以内で十分であり、通常は1分間の通気により鉄金属粒
子の充填層は、ブロック状の塊を形成しない程度にほぐ
される。本発明方法においては、鉄金属粒子の充填層に
空気を通じて鉄金属粒子の充填層をほぐしたのち、洗浄
水及び空気の混合流を上向流で供給する。洗浄水のみに
よる洗浄では、鉄金属粒子の充填層が展開しても、汚染
物質の剥離効果が小さく、多量の洗浄水を消費しても洗
浄効果は上がらないが、洗浄水及び空気の混合流を上向
流として供給することにより、鉄金属粒子の充填層は展
開、流動化するとともに、空気の気泡を含む混合流によ
り激しく撹拌され、鉄金属粒子表面から付着した汚染物
質が剥離され、目詰まりを起こしている汚染物質ととも
に水流に伴われて排出される。
In the method of the present invention, there is no particular limitation on the flow direction when air is passed through the packed bed of iron metal particles, and it can be either an upward flow or a downward flow. However, by setting the ventilation direction to upward flow, the packed bed of iron metal particles can be effectively loosened, and the flow of acidic adjusted wastewater is usually upward due to the generation of hydrogen gas. Since the supply of the mixed flow of the washing water and the air is also performed in the upward flow, the ventilation of the iron metal particles into the packed bed is preferably performed in the upward flow from the viewpoint of equipment design and operation management. . In the method of the present invention, it is preferable that the ventilation speed for loosening the packed layer of iron metal particles is LV = 50 to 200 m / h. When the ventilation speed is less than 50 m / h, the packed layer of iron metal particles is not sufficiently loosened, and a block-like lump may be generated. If the ventilation speed exceeds 200 m / h, the consumed power is increased, and the fine metal particles may be scattered. Aeration time is 5 seconds ~
Preferably, it is one minute. If the ventilation is less than 5 seconds, the packed layer of iron metal particles may not be sufficiently loosened, and a block-like lump may be generated. Ventilation within 1 minute is usually sufficient, and usually the ventilation layer for 1 minute loosens the packed layer of iron metal particles so as not to form a block-like mass. In the method of the present invention, after the packed bed of iron metal particles is loosened by passing air through the packed bed of iron metal particles, a mixed flow of washing water and air is supplied in an upward flow. In the case of washing only with washing water, even if the packed layer of iron metal particles is developed, the effect of removing contaminants is small and the washing effect is not improved even if a large amount of washing water is consumed. Is supplied as an upward flow, the packed bed of iron metal particles expands and fluidizes, and is vigorously stirred by a mixed flow containing air bubbles, and contaminants adhering from the surface of the iron metal particles are peeled off. Discharged along with the clogging pollutants in the water stream.

【0008】本発明方法において、洗浄水及び空気の混
合流を形成するための洗浄水の供給速度は、LV=30
〜150m/hであることが好ましい。洗浄水の通水速
度は、鉄金属粒子の大きさなどに応じて選択することが
できるが、洗浄水及び空気の混合流を供給したとき、鉄
金属粒子の充填層が10〜50%展開する程度とするこ
とが好ましい。洗浄水の通水速度が30m/h未満であ
ると、鉄金属粒子の充填層の展開が少なく、鉄金属粒子
の表面に付着した汚染物質が十分に剥離されないおそれ
がある。洗浄水の通水速度が150m/hを超えると、
消費する洗浄水の量が多くなる上に、鉄金属粒子が流出
するおそれがある。本発明方法において、洗浄水及び空
気の混合流を形成するための空気の供給速度は、LV=
50〜200m/hであることが好ましい。空気の供給
速度が、LV=50m/h未満であると、撹拌力が弱く
洗浄効果が十分に向上しないおそれがある。空気の供給
速度は、通常はLV=200m/hで十分であり、それ
以上の空気を供給しても、空気の供給量の増加に見合っ
て洗浄効果は向上しない。本発明方法においては、洗浄
水及び空気の混合流の供給を30秒〜5分間行うことが
好ましい。混合流の供給が30秒間未満であると、鉄金
属粒子の充填層の洗浄が不十分となるおそれがある。混
合流の供給は、通常は5分間以内で十分であり、それ以
上混合流を供給しても洗浄効果は向上しない。
In the method of the present invention, the supply rate of the washing water for forming the mixed stream of the washing water and the air is LV = 30.
It is preferably from 150 to 150 m / h. The flow rate of the washing water can be selected according to the size of the iron metal particles and the like, but when a mixed flow of the washing water and the air is supplied, the packed layer of the iron metal particles develops by 10 to 50%. It is preferable to set the degree. When the flow rate of the washing water is less than 30 m / h, the packed layer of the iron metal particles is less developed, and contaminants attached to the surface of the iron metal particles may not be sufficiently removed. When the flow rate of the washing water exceeds 150 m / h,
In addition to consuming a large amount of washing water, iron metal particles may flow out. In the method of the present invention, the supply rate of air for forming a mixed flow of washing water and air is LV =
It is preferably 50 to 200 m / h. If the air supply speed is less than LV = 50 m / h, the agitation power may be weak and the cleaning effect may not be sufficiently improved. Normally, the supply speed of air is sufficient to be LV = 200 m / h, and even if more air is supplied, the cleaning effect is not improved in proportion to the increase in the supply amount of air. In the method of the present invention, it is preferable to supply the mixed flow of the washing water and the air for 30 seconds to 5 minutes. If the supply of the mixed flow is less than 30 seconds, the cleaning of the packed bed of iron metal particles may be insufficient. The supply of the mixed flow within 5 minutes is usually sufficient, and the supply of the mixed flow longer than this does not improve the cleaning effect.

【0009】本発明方法においては、洗浄水及び空気の
混合流を供給して洗浄を行ったのち、洗浄水のみによる
洗浄を行うことが好ましい。洗浄水のみによる洗浄によ
り、洗浄水及び空気の混合流によって剥離した汚染物質
を完全に洗い流すとともに、鉄金属粒子の充填層から気
泡を追い出すことができ、さらに、鉄金属粒子の充填層
を均一に形成することができる。本発明方法において、
洗浄水及び空気の混合流の供給後の洗浄水のみによる洗
浄の通水速度は、LV=30〜150m/hであること
が好ましい。洗浄水の通水速度が30m/h未満である
と、鉄金属粒子の充填層の展開が少なく、剥離した汚染
物質の洗い流し及び気泡の追い出しが不十分となるおそ
れがある。洗浄水の通水速度が150m/hを超える
と、消費する洗浄水の量が多くなる上に、鉄金属粒子が
流出するおそれがある。本発明方法においては、洗浄水
及び空気の混合流の供給後の洗浄水のみによる洗浄は、
10秒〜3分間行うことが好ましい。洗浄水のみによる
洗浄時間が10秒間未満であると、剥離した汚染物質の
洗い流し及び気泡の追い出しが不十分となるおそれがあ
る。洗浄水のみによる洗浄は、通常は3分間以内で十分
であり、それ以上洗浄水のみによる洗浄を継続しても洗
浄効果は向上しない。洗浄水のみによる洗浄を終了した
のち、洗浄水の供給を停止して沈静化することにより、
鉄金属粒子の充填層をふたたび形成する。本発明方法に
おいては、充填層に空気を通じて鉄金属粒子の充填層を
ほぐしたのち、さらに洗浄水及び空気の混合流を上向流
で供給し、鉄金属粒子の充填層の汚染物質を除去する洗
浄を、1日に2回以上の頻度で行う。この洗浄の頻度が
1日に1回であると、充填した鉄金属粒子がブロック状
の塊を形成するおそれがある。充填層に空気を通じて鉄
金属粒子の充填層をほぐしたのち、さらに洗浄水及び空
気の混合流を上向流で供給し、鉄金属粒子の充填層の汚
染物質を除去する洗浄を、1日に2回以上の頻度で行う
ことにより、充填した鉄金属粒子がブロック状の塊を形
成することを防止し、充填した鉄金属粒子を有効に水処
理に利用することができる。
In the method of the present invention, it is preferable that after the cleaning is performed by supplying a mixed flow of the cleaning water and the air, the cleaning is performed using only the cleaning water. By washing only with the washing water, the contaminants separated by the mixed flow of the washing water and the air can be completely washed away, and bubbles can be expelled from the packed layer of the iron metal particles. Can be formed. In the method of the present invention,
It is preferable that the flow rate of the washing with only the washing water after the supply of the mixed flow of the washing water and the air is LV = 30 to 150 m / h. When the flow rate of the washing water is less than 30 m / h, the packed bed of the iron metal particles is less developed, and there is a possibility that the flushing of the separated contaminants and the expelling of bubbles are insufficient. When the flow rate of the cleaning water exceeds 150 m / h, the amount of the cleaning water to be consumed increases and the iron metal particles may flow out. In the method of the present invention, the washing with only the washing water after the supply of the mixed stream of the washing water and the air is performed by:
It is preferably performed for 10 seconds to 3 minutes. If the cleaning time using only the cleaning water is less than 10 seconds, there is a possibility that the removal of the separated contaminants and the removal of bubbles may be insufficient. Washing with only the washing water is usually sufficient for less than 3 minutes. Even if washing with only the washing water is continued longer than that, the washing effect is not improved. After the cleaning with only the cleaning water is completed, the supply of the cleaning water is stopped and settled,
A packed layer of iron metal particles is formed again. In the method of the present invention, after the packed bed of iron metal particles is loosened through air through the packed bed, a mixed flow of washing water and air is further supplied in an upward flow to remove contaminants in the packed bed of iron metal particles. Washing is performed at least twice a day. If the frequency of this washing is once a day, the filled iron metal particles may form a block-like mass. After loosening the packed bed of iron metal particles through the packed bed with air, a cleaning flow for removing contaminants in the packed bed of iron metal particles by supplying a mixed flow of washing water and air in an upward flow, and removing the contaminants from the packed bed of iron metal particles in one day. By performing the treatment twice or more times, the filled iron metal particles are prevented from forming a block-like lump, and the filled iron metal particles can be effectively used for water treatment.

【0010】図1は、本発明の水処理装置の洗浄方法の
説明図である。本図に示す水処理装置は、円筒状の反応
槽1の底部に水導入口2及び空気導入口3が設けられ、
頭部に還元処理水、洗浄水及び空気の排出口4が設けら
れている。反応槽の下部にはストレーナー5を備えた鉄
金属粒子支持板6が取り付けられ、さらにその上に鉄金
属粒子を充填して鉄金属粒子の充填層7が形成される。
反応槽の上部には多孔板8が取り付けられ、鉄金属粒子
供給口9が設けられる。排水の還元処理においては、酸
の添加によりpHを5以下、好ましくはpHを2〜3に調整
した排水を水導入口より供給し、鉄金属粒子の充填層に
おいて、排水中に含まれるペルオキソ硫酸、ヨウ素酸、
セレン酸、硝酸などの不純物を還元処理する。排水は上
向流として導入されるので、還元処理に際して発生する
水素ガスは、水流とともに上方へ移動し、反応槽頭部の
排出口より排出される。排出口より流出する還元処理水
は、さらに凝集沈澱設備に導き、アルカリ剤を添加して
pH7以上に調整し、必要に応じてさらに高分子凝集剤な
どを添加して凝集沈澱処理を行って処理水を得る。本発
明方法においては、1日に2回以上の頻度で水処理装置
の洗浄を行う。水処理装置の洗浄を行うためには、排水
の供給を停止し、空気導入口から空気を通じることによ
り、鉄金属粒子の充填層をほぐす。次いで、鉄金属粒子
の充填層に洗浄水及び空気の混合流を上向流で供給する
ことにより、鉄金属粒子の充填層を展開、流動化する。
鉄金属粒子の充填層の展開、流動化により、鉄金属粒子
の表面に付着した汚染物質は剥離され、目詰まりを起こ
していた汚染物質とともに、混合流に伴われて排出口よ
り排出される。洗浄水及び空気の混合流を所定時間供給
したのち、必要に応じて空気の供給を停止し、洗浄水の
みによる洗浄を行うことができる。洗浄水のみによる洗
浄を行うことにより、剥離した汚染物質を完全に洗い流
すとともに、鉄金属粒子の充填層から気泡を追い出す。
洗浄水のみによる洗浄を行ったのち、洗浄水の供給を停
止し、鉄金属粒子を沈静化して充填層を形成する。その
後、排水を水導入口より供給し、還元処理を再開する。
本発明方法によれば、充填した鉄金属粒子がブロック状
の塊を形成することを防止し、充填した鉄金属粒子を有
効に水処理に利用し、長期間にわたって安定して排水中
の不純物の還元処理を行うことができる。
FIG. 1 is an explanatory view of a method for cleaning a water treatment apparatus according to the present invention. The water treatment apparatus shown in this figure is provided with a water inlet 2 and an air inlet 3 at the bottom of a cylindrical reaction vessel 1,
A discharge port 4 for reducing water, washing water and air is provided on the head. A ferrous metal particle support plate 6 having a strainer 5 is attached to the lower part of the reaction tank, and a ferrous metal particle filling layer 7 is formed thereon by further filling the ferrous metal particle support plate.
A perforated plate 8 is attached to the upper part of the reaction tank, and an iron metal particle supply port 9 is provided. In the reduction treatment of the wastewater, wastewater whose pH is adjusted to 5 or less, preferably pH 2 to 3 by the addition of an acid is supplied from the water inlet, and the peroxosulfuric acid contained in the wastewater is filled in the packed bed of iron metal particles. , Iodic acid,
Reduction treatment of impurities such as selenic acid and nitric acid. Since the wastewater is introduced as an upward flow, the hydrogen gas generated during the reduction treatment moves upward together with the water flow, and is discharged from the outlet at the head of the reaction tank. The reduced water discharged from the discharge port is further led to the coagulation and sedimentation facility, where an alkaline agent is added.
The pH is adjusted to 7 or more, and if necessary, a polymer coagulant or the like is further added to perform coagulation precipitation treatment to obtain treated water. In the method of the present invention, the water treatment apparatus is washed at least twice a day. In order to wash the water treatment apparatus, the supply of the wastewater is stopped, and the packed bed of the iron metal particles is loosened by passing air from the air inlet. Next, a mixed flow of washing water and air is supplied to the packed bed of iron metal particles in an upward flow, whereby the packed bed of iron metal particles is developed and fluidized.
Due to the development and fluidization of the packed bed of iron metal particles, the contaminants adhering to the surface of the iron metal particles are peeled off, and are discharged from the outlet together with the pollutants that have caused clogging along with the mixed flow. After supplying the mixed flow of the cleaning water and the air for a predetermined time, the supply of the air may be stopped as necessary, and the cleaning using only the cleaning water may be performed. By performing the cleaning using only the cleaning water, the separated contaminants are completely washed away, and bubbles are expelled from the packed layer of the iron metal particles.
After washing with only the washing water, the supply of the washing water is stopped, and the iron metal particles are calmed down to form a packed layer. After that, the wastewater is supplied from the water inlet and the reduction process is restarted.
According to the method of the present invention, the filled iron metal particles are prevented from forming block-like lumps, the filled iron metal particles are effectively used for water treatment, and impurities in wastewater are stably removed over a long period of time. A reduction treatment can be performed.

【0011】[0011]

【実施例】以下に、実施例を挙げて本発明をさらに詳細
に説明するが、本発明はこれらの実施例によりなんら限
定されるものではない。 実施例1 内径200mm、高さ1,000mmのアクリル樹脂製カラ
ム下部に、水導入口と空気導入口を取り付け、その直上
にストレーナーを備えた鉄金属粒子支持板を設けた。ま
た、カラム上部には、鉄金属粒子供給口、多孔板及び還
元処理水排出口を設けた。鉄金属粒子支持板上に、粒径
0.6mmの均一な球状の鉄金属粒子10リットルを充填
して、図1に示す形状の鉄金属粒子の充填層を有するカ
ラムを作製した。pH6.7で、硝酸体窒素100mg/リ
ットルを含有する排煙脱硫排水に、塩酸をHCl濃度が
200mg/リットルになるように注入し、上記の鉄金属
粒子を充填したカラムに、300リットル/hすなわち
SV=30/hの速度で上向流で通水した。12時間ご
とに排煙脱硫排水の通水を止め、空気をLV=135m
/hで上向流で20秒間通じて鉄金属粒子の充填層をほ
ぐし、次いで水をLV=100m/h、空気をLV=1
35m/hで、水と空気の混合流として上向流で1分4
0秒間供給し、最後に水のみをLV=100m/hで上
向流で1分間供給して洗浄操作を終了した。洗浄操作終
了後、ふたたび排煙脱硫排水の処理を開始した。鉄金属
粒子は、カラム内の充填量が10リットルになるよう
に、鉄金属粒子供給口より補給した。12時間ごと、す
なわち1日に2回の頻度で洗浄を行いつつ、排煙脱硫排
水の処理を1カ月間継続したが、鉄金属粒子にはブロッ
ク状の塊は形成されなかった。 比較例1 実施例1と同じ鉄金属粒子の充填層を有するカラムを作
製し、洗浄を24時間ごと、すなわち1日に1回の頻度
で行った以外は、実施例1と同じ処理を、実施例1と並
行して行った。処理開始後2日目に、カラム内に直径5
〜10cmの塊が発生した。1カ月間同じ条件で通水処理
を続けたが、カラム内には常に鉄金属粒子のブロック状
の塊が存在していた。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the present invention. Example 1 A water inlet and an air inlet were attached to a lower part of an acrylic resin column having an inner diameter of 200 mm and a height of 1,000 mm, and a ferrous metal particle support plate provided with a strainer was provided immediately above the water inlet and the air inlet. In addition, an iron metal particle supply port, a perforated plate, and a reduction treatment water discharge port were provided at the top of the column. 10 liters of uniform spherical iron metal particles having a particle diameter of 0.6 mm were packed on the iron metal particle support plate to prepare a column having a packed layer of iron metal particles having the shape shown in FIG. Hydrochloric acid was injected into flue gas desulfurization wastewater containing 100 mg / liter of nitrate nitrogen at a pH of 6.7 so that the HCl concentration became 200 mg / liter. That is, water was passed in an upward flow at a speed of SV = 30 / h. Stop the flow of flue gas desulfurization wastewater every 12 hours, and allow air to reach LV = 135m
/ H in an upward flow for 20 seconds to loosen the packed bed of iron metal particles, then water = 100 m / h and air = 1
35m / h, 4 minutes per minute in the upward flow as a mixed flow of water and air
Water was supplied for 0 second, and finally, only water was supplied in an upward flow at LV = 100 m / h for 1 minute to complete the washing operation. After the completion of the washing operation, the treatment of the flue gas desulfurization wastewater was started again. The iron metal particles were supplied from the iron metal particle supply port such that the filling amount in the column became 10 liters. The treatment of the flue gas desulfurization effluent was continued for one month while washing every 12 hours, that is, twice a day, but no block-like mass was formed on the iron metal particles. Comparative Example 1 A column having the same packed layer of iron metal particles as in Example 1 was prepared, and the same process as in Example 1 was performed except that washing was performed every 24 hours, that is, once a day. Performed in parallel with Example 1. On the second day after the start of treatment, 5
A lump of 〜1010 cm formed. The water treatment was continued under the same conditions for one month, but a block-like mass of iron metal particles was always present in the column.

【0012】[0012]

【発明の効果】本発明の水処理装置の洗浄方法によれ
ば、鉄金属粒子の充填層に通水して排水中の不純物を還
元処理する水処理装置において、充填した鉄金属粒子が
ブロック状の塊を形成することを防止し、充填した鉄金
属粒子を有効に水処理に利用し、長期間にわたって安定
して排水中の不純物の還元処理を行うことができる。
According to the method for cleaning a water treatment apparatus of the present invention, in a water treatment apparatus for reducing impurities in wastewater by passing water through a packed bed of iron metal particles, the filled iron metal particles are formed in a block shape. Lumps are prevented from being formed, the filled iron metal particles are effectively used for water treatment, and the reduction treatment of impurities in wastewater can be stably performed over a long period of time.

【図面の簡単な説明】[Brief description of the drawings]

【図1】図1は、本発明の水処理装置の洗浄方法の説明
図である。
FIG. 1 is an explanatory diagram of a method for cleaning a water treatment apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 反応槽 2 水導入口 3 空気導入口 4 排出口 5 ストレーナー 6 鉄金属粒子支持板 7 鉄金属粒子の充填層 8 多孔板 9 鉄金属粒子供給口 DESCRIPTION OF SYMBOLS 1 Reaction tank 2 Water inlet 3 Air inlet 4 Outlet 5 Strainer 6 Iron metal particle support plate 7 Packing layer of iron metal particles 8 Perforated plate 9 Iron metal particle supply port

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】鉄金属粒子の充填層に通水して排水中の不
純物を還元処理する水処理装置において、充填層に通気
速度が、LV=50〜200m/hで、5秒〜1分間
気を通じて鉄金属粒子の充填層をほぐしたのち、さらに
洗浄水及び空気の混合流を上向流で供給し、鉄金属粒子
の充填層の汚染物質を除去する洗浄を、1日に2回以上
の頻度で行うことを特徴とする水処理装置の洗浄方法。
1. A water treatment apparatus for reduction treatment of impurities in the waste water was passed through the packed bed of iron metal particles, vent the filling layer
At a speed of LV = 50-200 m / h, the packed bed of iron metal particles is loosened through air for 5 seconds to 1 minute , and then a mixed flow of washing water and air is supplied in an upward flow. And a cleaning method for removing contaminants from the packed bed of iron metal particles at least twice a day.
【請求項2】洗浄水及び空気の混合流による洗浄を行っ
たのち、さらに洗浄水のみによる洗浄を行うことを特徴
とする請求項1記載の水処理装置の洗浄方法。
2. A cleaning process using a mixed flow of cleaning water and air.
After that, it is further characterized by washing with only washing water
The method for cleaning a water treatment apparatus according to claim 1, wherein
【請求項3】排水を酸性に調整して鉄金属粒子の充填層
に通水することを特徴とする請求項1又は2記載の水処
理装置の洗浄方法。
3. A packed bed of iron metal particles by adjusting waste water to be acidic.
The water treatment according to claim 1, wherein water is passed through the water treatment.
Method for cleaning equipment.
JP13160698A 1998-05-14 1998-05-14 Cleaning method for water treatment equipment Expired - Fee Related JP3360608B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13160698A JP3360608B2 (en) 1998-05-14 1998-05-14 Cleaning method for water treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13160698A JP3360608B2 (en) 1998-05-14 1998-05-14 Cleaning method for water treatment equipment

Publications (2)

Publication Number Publication Date
JPH11319856A JPH11319856A (en) 1999-11-24
JP3360608B2 true JP3360608B2 (en) 2002-12-24

Family

ID=15062004

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13160698A Expired - Fee Related JP3360608B2 (en) 1998-05-14 1998-05-14 Cleaning method for water treatment equipment

Country Status (1)

Country Link
JP (1) JP3360608B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4538706B2 (en) * 2001-01-18 2010-09-08 栗田工業株式会社 Cleaning method for water treatment equipment
JP6242227B2 (en) * 2014-02-04 2017-12-06 オルガノ株式会社 Iron / manganese-containing water treatment apparatus and treatment method

Also Published As

Publication number Publication date
JPH11319856A (en) 1999-11-24

Similar Documents

Publication Publication Date Title
KR101653129B1 (en) Method of treating coal gasification wastewater
EP1330414B9 (en) Method for treatment of water and wastewater
JP3739480B2 (en) Treatment method of flue gas desulfurization waste water
AU2002220093A1 (en) Method and apparatus for treatment of water and wastewater
JP3360608B2 (en) Cleaning method for water treatment equipment
JPH0712477B2 (en) How to remove phosphorus in water
JP4001472B2 (en) Method and apparatus for treating metal-containing water
JPH11277076A (en) Method and apparatus for treating manganese-containing water
JP4538706B2 (en) Cleaning method for water treatment equipment
JP3237524B2 (en) Cleaning method for water treatment equipment
JP5650164B2 (en) Crystallization reactor and crystallization reaction method
JP3729365B2 (en) Method and apparatus for treating manganese-containing water
JP4014679B2 (en) Wastewater treatment method
JP3880190B2 (en) Method and apparatus for treating manganese-containing water
JP3870405B2 (en) Treatment of selenium-containing wastewater
KR100325981B1 (en) Method for regenerating a waste solution of iron chloride-based etching solution
JP4214326B2 (en) Water treatment equipment
JP3564416B2 (en) Removal method of residual ozone in raw water treatment
CN107892411A (en) A kind of waste liquid electric flocculation hardness removing device and method
JPH09323089A (en) Water treatment equipment cleaning method
JP4177985B2 (en) Method and apparatus for treating fluorine-containing water
JP3062036B2 (en) Apparatus and method for producing slaked lime solution for tap water reforming
JP7377907B2 (en) Upflow treatment device and treatment method using upflow treatment device
JP2006272161A (en) Method and apparatus for treating nitrate nitrogen-containing wastewater
JPH09155368A (en) Treatment of flue gas desulfurization wastewater

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071018

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20081018

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091018

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091018

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101018

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101018

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111018

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111018

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121018

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121018

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131018

Year of fee payment: 11

LAPS Cancellation because of no payment of annual fees