JPS62280375A - Device for water-washing chemical-conversion treated article - Google Patents
Device for water-washing chemical-conversion treated articleInfo
- Publication number
- JPS62280375A JPS62280375A JP12656086A JP12656086A JPS62280375A JP S62280375 A JPS62280375 A JP S62280375A JP 12656086 A JP12656086 A JP 12656086A JP 12656086 A JP12656086 A JP 12656086A JP S62280375 A JPS62280375 A JP S62280375A
- Authority
- JP
- Japan
- Prior art keywords
- water
- washing
- conductivity
- ion exchange
- washing water
- 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
- 238000005406 washing Methods 0.000 title claims abstract description 61
- 238000006243 chemical reaction Methods 0.000 title claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- 238000005349 anion exchange Methods 0.000 claims abstract description 10
- 238000005341 cation exchange Methods 0.000 claims abstract description 8
- 238000005342 ion exchange Methods 0.000 claims description 22
- 239000000126 substance Substances 0.000 claims description 7
- 230000005484 gravity Effects 0.000 claims description 4
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 238000007747 plating Methods 0.000 abstract description 5
- 238000011084 recovery Methods 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 238000002242 deionisation method Methods 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 150000002500 ions Chemical class 0.000 description 4
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
- Chemical Treatment Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
3、発明の詳細な説明
!豆肢血
本発明は化成処理した物品の水洗装置、さらに詳しくは
使用済洗浄水を浄化して再使用するクローズド方式を取
るそのような水洗装置に関する。[Detailed description of the invention] 3. Detailed description of the invention! BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a washing apparatus for chemically treated articles, and more particularly to such a washing apparatus that employs a closed system in which used washing water is purified and reused.
物品の化成処理、例えばメッキ処理においては付着した
薬品を洗い流すための水洗が必要である。In chemical conversion treatment of articles, such as plating treatment, washing with water is required to wash away adhering chemicals.
この水洗に使用した水は希薄とはいえクロム、シアン等
の有害物質を含んでいるのでそのまま環境へ放出するこ
とはできない。しかも洗浄水は希薄なため多量となるの
で排水処理設備に大きなF9を資を必要とし、その操業
コストも比較的高く濃縮処理が求められている。Although the water used for this washing is diluted, it contains harmful substances such as chromium and cyanide, so it cannot be released directly into the environment. Moreover, since the washing water is dilute, it is produced in a large amount, requiring a large amount of F9 in wastewater treatment equipment, and the operating cost thereof is also relatively high, requiring concentration treatment.
そこで洗浄水そのものを浄化して再使用し、廃水を外部
へ放出しないクローズド方式が理想的である。従来使用
済洗浄水を順次フィルター、カチオン交換塔、アニオン
交換塔を通過させ、水に不溶の不純物、夾雑イオンを除
去した後水洗槽へ返還する装置は知られているが、高度
に浄化しようとすると高価な混床式のイオン交換塔の併
用が必要となる。再生コストの安価な複床式のみの脱イ
オンで処理し返還される水の純度は導電率にしてlOμ
S / cm程度が限度であった。Therefore, a closed system that purifies and reuses the washing water itself and does not release wastewater to the outside is ideal. Conventionally, devices are known in which used washing water is sequentially passed through a filter, a cation exchange tower, and an anion exchange tower to remove water-insoluble impurities and contaminant ions before being returned to the washing tank. This requires the combined use of an expensive mixed bed type ion exchange tower. The purity of the water that is returned after being treated with deionization using only a multi-bed system with low recycling costs is 10μ in terms of conductivity.
The limit was about S/cm.
本発明はそのため、洗浄水の処理水準をさらに高純度に
、例えば導電率にして0.5μS / cm程度まで浄
化し、水洗槽へ返還することができる、比較的簡便な装
置を提供することを課題とする。Therefore, the present invention aims to provide a relatively simple device that can purify washing water to a higher level of purity, for example, to a conductivity of about 0.5 μS/cm, and return it to the washing tank. Take it as a challenge.
木光匪旦撮要
本発明は、化成処理した物品を水洗槽内において水洗し
、使用済洗浄水を浄化した後再び水洗槽へ返還するクロ
ーズド方式の水洗装置において、少なくとも1組の直列
に連結したカチオン交換塔とアニオン交換塔を設け、水
洗槽からの使用済洗浄水を前記イオン交換塔の組を通し
て浄化した後水洗槽へ循環させるようにし、さらに該イ
オン交換塔の組の下流と該イオン交換塔の上流とを結ぶ
ループ回路を設け、前記イオン交換塔の組を通過した後
の洗浄水の導電率があらかじめ定めた値以上のときは導
電率があらかじめ定めた値以下になるまで洗浄水を該ル
ープ回路内を循環させ、前記イオン交換塔の組を通過し
た後の洗浄水の導電率があらかじめ定めた値以下のとき
は該ループ回路を閉じ、前記イオン交換塔を通過した洗
浄水を水洗槽へ返還するように洗浄水の流れを制御する
手段を備えていることを特徴とする化成処理物品の水洗
装置に関する。The present invention is a closed-type washing device in which chemically treated articles are washed in a washing tank, and the used washing water is purified and then returned to the washing tank. A cation exchange tower and an anion exchange tower are provided, and the used washing water from the washing tank is purified through the set of ion exchange towers and then circulated to the washing tank, and further downstream of the set of ion exchange towers and the ion exchange tower. A loop circuit is provided to connect the upstream of the tower, and when the conductivity of the wash water after passing through the set of ion exchange towers is above a predetermined value, the wash water is continued until the conductivity falls below the predetermined value. The loop circuit is circulated, and when the conductivity of the washing water after passing through the set of ion exchange towers is less than a predetermined value, the loop circuit is closed and the washing water that has passed through the ion exchange towers is washed with water. The present invention relates to a water washing device for chemical conversion treated articles, characterized in that it is equipped with means for controlling the flow of washing water so as to return it to a tank.
好ましくは、使用済洗浄水は前記イオン交換塔へ導入す
る前に、重力式繊維フィルターで濾過される。Preferably, the used wash water is filtered through a gravity fiber filter before being introduced into the ion exchange column.
しい且 1の口 図面は本発明装置の一具体例の概略図である。The first mouth The drawing is a schematic diagram of a specific example of the device of the present invention.
化成処理としてクロムメッキを例にとると、物品はメッ
キ槽1においてメッキされ、矢印方向へ順次送られて付
着メソ+液を回収槽2において回収され、第1の水洗槽
3.第2の水洗jW4において水洗される。第2の水洗
槽4へは新鮮な洗浄水がタンク6から補給され、オーバ
ーフローして第1の水洗槽3へ送られるようになってい
る。従ってこれら水洗槽において物品は新鮮な洗浄水で
向流方向に洗浄されるようになっている。Taking chrome plating as an example of a chemical conversion treatment, articles are plated in a plating tank 1, are sequentially sent in the direction of the arrow, and the adhering meso+ liquid is collected in a recovery tank 2, and then transferred to a first washing tank 3. It is washed with water in the second water washing jW4. The second washing tank 4 is replenished with fresh washing water from a tank 6, which overflows and is sent to the first washing tank 3. In these washing tanks, the articles are therefore washed countercurrently with fresh washing water.
第1の水洗槽3からの使用済洗浄水は、この具体例では
直接または一旦タンクを通ってフィルターFにおいて水
不溶物が除去された後、総体を10で示したループ回路
へ導入されるようになっている。In this example, the used washing water from the first washing tank 3 is introduced into a loop circuit generally indicated by 10, after water insoluble matter is removed in a filter F, either directly or once through the tank. It has become.
フィルターFは、好ましくは重力流下式の繊維フィルタ
ー、特に球状の繊維塊を濾材として使用するフィルター
である。この種のフィルターでは水不溶の懸濁物が繊維
表面に沈着し、細かい粒子がよく捕捉されるので好都合
である。またこのフィルターを逆洗することによって沈
着粒子は容易に脱落し、濃厚液となって排出されるので
、保守も容易である。Filter F is preferably a gravity flow type fiber filter, particularly a filter using spherical fiber aggregates as a filter medium. This type of filter is advantageous because water-insoluble suspensions are deposited on the fiber surface and fine particles are better captured. Furthermore, by backwashing this filter, deposited particles easily fall off and are discharged as a concentrated liquid, making maintenance easy.
フィルターFを通過した洗浄水はバルブ■1を通ってル
ープ回路へ導入される。通常バルブ■1は開位置にあり
、バルブ■3は開位置にあり、バルブ■2は閉位置にあ
る。カチオン交換塔K、アニオン交換塔Aを通過した水
の導電率はイオン交換塔の下流に設置したメーターMに
よって常時監視されている。この導電率の値があらかじ
め定めた値、例えば0.5μS / 0m以下であれば
、装置はこの状態で運転される。しかしながらイオン交
換塔内部で短絡回路が発生した等のため十分に脱イオン
されず、メーターMが所定値例えば0.5μs/ cm
以上の高い導電率を感知した時は、制御器へその信号が
送られ、制御器はバルブ■1および■3を閉じ、■2を
開いて洗浄水をループ回路10内を循環させる。これに
よってイオン交換塔内部に生じた短絡回路は修復され、
所定値以下の導電率の水が得られるようになる。そこで
メーターMによって感知した所定値以下の低い導電率に
応答して、制御器はバルブ■1および■3を開き、バル
ブ■2を閉しる信号を発生し、イオン交換塔を通過した
洗浄水を水洗槽3.4の上流にあるタンク6へ送り、同
時に洗浄水がループ回路10内をi盾環している間にタ
ンク5に貯った使用済洗浄水をフィルターFを通ってイ
オン交換塔の対への導入が再開される。The cleaning water that has passed through the filter F is introduced into the loop circuit through the valve 1. Normally, valve (1) is in the open position, valve (3) is in the open position, and valve (2) is in the closed position. The conductivity of the water that has passed through the cation exchange tower K and the anion exchange tower A is constantly monitored by a meter M installed downstream of the ion exchange tower. If the value of this conductivity is less than a predetermined value, for example 0.5 μS/0 m, the device is operated in this state. However, due to a short circuit occurring inside the ion exchange tower, sufficient deionization was not achieved, and the meter M did not reach the predetermined value, for example, 0.5 μs/cm.
When a higher conductivity is detected, a signal is sent to the controller, and the controller closes valves (1) and (3) and opens (2) to circulate cleaning water within the loop circuit 10. This will repair the short circuit that occurred inside the ion exchange tower.
Water with conductivity below a predetermined value can be obtained. Therefore, in response to the low conductivity below a predetermined value sensed by the meter M, the controller generates a signal to open valves ■1 and ■3 and close valve ■2, allowing the cleaning water that has passed through the ion exchange tower to is sent to the tank 6 upstream of the washing tank 3.4, and at the same time, while the washing water is circulating in the loop circuit 10, the used washing water stored in the tank 5 passes through the filter F and undergoes ion exchange. Introduction to the pair of towers is resumed.
一般にイオン交換処理で通液速度が大きすぎるとカラム
内に短絡回路が発生し、処理が不完全になるので、安全
のため通液速度は低めに設定されるのが通常である。そ
のため未だ活性なイオン交換体を残したまま更新せざる
を得なかったが、本発明の装置では短絡回路が生じても
上記のように短時間で修復されるので、従来は採用し得
なかった高速度で通水しても良好に脱イオンできるよう
になった。Generally, in ion exchange treatment, if the liquid passing rate is too high, a short circuit will occur within the column and the treatment will be incomplete, so for safety reasons, the liquid passing rate is usually set to a low value. Therefore, it was necessary to update the device with the ion exchanger still active, but even if a short circuit occurs in the device of the present invention, it can be repaired in a short time as described above, so this could not be used in the past. Good deionization is now possible even when water is passed through at high speed.
本発明の範囲内において、図示した具体例に種々の修飾
、変更を加えることが可能である。Various modifications and changes can be made to the illustrated examples without departing from the scope of the present invention.
例えばループ回路10は1対の直列に連結したカチオン
交換塔とアニオン交換塔を備えているが、洗浄水槽3に
持ち込まれるイオン種と量に応じてこの段数を増すこと
ができ、その場合はカチオン交換塔とアニオン交換塔の
組は、図示した組と直列にも、並列にも連結することが
できる。この方式により、タンク6へ返還する処理した
水の導電率を0.5μS / cm程度に設定しても採
水の停止する循環時間は全体の20%以下にでき、洗浄
水槽3の水質の変動に影響はなかった。For example, the loop circuit 10 includes a pair of cation exchange towers and an anion exchange tower connected in series, but the number of stages can be increased depending on the type and amount of ions brought into the washing water tank 3. The exchange column and anion exchange column pair can be connected in series or in parallel with the illustrated pair. With this method, even if the conductivity of the treated water returned to tank 6 is set to about 0.5 μS/cm, the circulation time during which water sampling is stopped can be kept to less than 20% of the total, and fluctuations in water quality in washing tank 3 can be avoided. There was no effect on
イオン交換塔におよび/またはAの交換容量が残ってい
る間は(ここで図示しないが)その前後の導電率に変化
があられれるのでこれを検知し、この差が所定値以下に
低下した時、別に用意した再生済の交換塔と取り替え、
撤去した交換塔は別途常法により再生する。こうした交
換に備えてあらかじめ複数個のカラムを備えてお(と便
利である。While the exchange capacity of the ion exchange tower and/or A remains (not shown here), there will be a change in the conductivity before and after that, and this will be detected, and when this difference falls below a predetermined value, , Replaced with a separately prepared recycled exchange tower,
The removed exchange tower will be regenerated separately using standard methods. It is convenient to prepare multiple columns in advance for such exchanges.
図面には示していないが、フィルターFが重力式濾過で
あればこれが目詰まりした場合は、タンク6から新鮮な
洗浄水をフィルター下流側から導入し、逆洗することに
より付着した水不溶物を洗い流し、再生できるのでこの
組み合わせが好ましい。Although not shown in the drawing, if filter F is gravity filtration, if it becomes clogged, fresh cleaning water is introduced from tank 6 downstream of the filter and backwashed to remove the water-insoluble matter that has adhered to it. This combination is preferred because it can be washed away and regenerated.
本発明の装置は、カチオン交換塔およびアニオン交換塔
を循環するループ回路を備えることにより、生じた短絡
回路を修復できるため、従来の装置に比べ、洗浄水を高
品質な洗浄水として回収することができる。さらに、イ
オン交換体がアニオンとカチオンに分離しているので、
洗浄水の水質に応じて過不足なく更新できる特徴をもつ
。この結果、従来法に比ベイオン交換樹脂の使用量を半
減することができた。高度の脱イオンに必須の混床カラ
ム設置のコストに比べると著しいコスト低減を果たし得
た。The device of the present invention is equipped with a loop circuit that circulates through the cation exchange tower and the anion exchange tower, so that short circuits that occur can be repaired, so cleaning water can be recovered as high-quality cleaning water compared to conventional devices. Can be done. Furthermore, since the ion exchanger is separated into anions and cations,
It has the feature that it can be updated just in time depending on the quality of the washing water. As a result, the amount of bayone exchange resin used could be reduced by half compared to the conventional method. The cost was significantly reduced compared to the cost of installing a mixed bed column, which is essential for high-level deionization.
このように本発明は汚染物質を含む廃水を外部へ放出し
ないクローズド方式を低コストで可能とするものである
。In this manner, the present invention enables a closed system that does not discharge wastewater containing pollutants to the outside at low cost.
図面は、本発明装置の一具体例の概略図である。
1は化成処理槽、2は液きり回収槽、3.4は水洗槽、
5は使用済洗浄水タンク、6は処理済洗浄水貯蔵タンク
、10はループ回路、Fはフィルター、Kはカチオン交
換塔、Aはアニオン交換塔である。The drawing is a schematic diagram of a specific example of the device of the present invention. 1 is a chemical conversion treatment tank, 2 is a liquid recovery tank, 3.4 is a washing tank,
5 is a used washing water tank, 6 is a treated washing water storage tank, 10 is a loop circuit, F is a filter, K is a cation exchange tower, and A is an anion exchange tower.
Claims (2)
用済洗浄水を浄化した後再び水洗槽へ返還するクローズ
ド方式の水洗装置において、少なくとも1組の直列に連
結したカチオン交換塔とアニオン交換塔を設け、水洗槽
からの使用済洗浄水を前記イオン交換塔の組を通して浄
化した後水洗槽へ循環させるようにし、さらに該イオン
交換塔の組の下流と該イオン交換塔の上流とを結ぶルー
プ回路を設け、前記イオン交換塔の組を通過した後の洗
浄水の導電率があらかじめ定めた値以上のときは導電率
があらかじめ定めた値以下になるまで洗浄水を該ループ
回路内を循環させ、前記イオン交換塔の組を通過した後
の洗浄水の導電率があらかじめ定めた値以下のときは該
ループ回路を閉じ、前記イオン交換塔を通過した洗浄水
を水洗槽へ返還するように洗浄水の流れを制御する手段
を備えていることを特徴とする化成処理物品の水洗装置
。(1) In a closed-type washing system in which chemically treated articles are washed in a washing tank and the used washing water is purified and then returned to the washing tank, anion exchange is performed with at least one set of cation exchange towers connected in series. A column is provided so that the used washing water from the washing tank is purified through the set of ion exchange towers and then circulated to the washing tank, and further connects the downstream of the set of ion exchange towers and the upstream of the ion exchange tower. A loop circuit is provided, and when the conductivity of the wash water after passing through the set of ion exchange towers is above a predetermined value, the wash water is circulated within the loop circuit until the conductivity becomes below the predetermined value. and when the conductivity of the washing water after passing through the set of ion exchange towers is less than a predetermined value, the loop circuit is closed and the washing water that has passed through the ion exchange towers is returned to the washing tank. A water washing device for chemical conversion treated articles, characterized by comprising means for controlling the flow of washing water.
前に、重力式フィルターによって濾過するようにした第
1項の装置。(2) The apparatus of item 1, wherein the used wash water is filtered by a gravity filter before being introduced into the set of ion exchange towers.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12656086A JPS62280375A (en) | 1986-05-30 | 1986-05-30 | Device for water-washing chemical-conversion treated article |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12656086A JPS62280375A (en) | 1986-05-30 | 1986-05-30 | Device for water-washing chemical-conversion treated article |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62280375A true JPS62280375A (en) | 1987-12-05 |
Family
ID=14938187
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12656086A Pending JPS62280375A (en) | 1986-05-30 | 1986-05-30 | Device for water-washing chemical-conversion treated article |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62280375A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0453493U (en) * | 1990-09-14 | 1992-05-07 | ||
JP2002172391A (en) * | 2000-12-06 | 2002-06-18 | Japan Organo Co Ltd | Ion exchange system |
-
1986
- 1986-05-30 JP JP12656086A patent/JPS62280375A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0453493U (en) * | 1990-09-14 | 1992-05-07 | ||
JP2002172391A (en) * | 2000-12-06 | 2002-06-18 | Japan Organo Co Ltd | Ion exchange system |
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