JP2002129398A - Recycling system of waste water from surface treatment process such as plating - Google Patents

Recycling system of waste water from surface treatment process such as plating

Info

Publication number
JP2002129398A
JP2002129398A JP2000322855A JP2000322855A JP2002129398A JP 2002129398 A JP2002129398 A JP 2002129398A JP 2000322855 A JP2000322855 A JP 2000322855A JP 2000322855 A JP2000322855 A JP 2000322855A JP 2002129398 A JP2002129398 A JP 2002129398A
Authority
JP
Japan
Prior art keywords
water
adjusted
tank
washing
surface treatment
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
Application number
JP2000322855A
Other languages
Japanese (ja)
Inventor
Masatake Kano
昌武 加納
Katsuyuki Sakakima
捷之 榊間
Satoshi Kaneko
聡 金子
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.)
KS RIKA KK
SUIREI KK
Original Assignee
KS RIKA KK
SUIREI KK
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 KS RIKA KK, SUIREI KK filed Critical KS RIKA KK
Priority to JP2000322855A priority Critical patent/JP2002129398A/en
Publication of JP2002129398A publication Critical patent/JP2002129398A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Abstract

PROBLEM TO BE SOLVED: To establish a system for surely supplying a necessary quantity of water having predetermined pH which is variously adjusted by using clarified water as a base, and for surely rinsing plated products effectively, by improving an already proposed method of reusing waste water generated in a surface treatment process as various rinsing water in each tank, after obtaining a clarified water by process such as solid-liquid separation and pH adjustment, as a recycling and/or a cost reducing technology. SOLUTION: A recycling system of the waste water for supplying suitably pH adjusted water for each tank, using the clarified water as a base, which is separated in sedimentation equipment from waste water generated in the surface treatment process, comprises supplying pH adjusted water in about 8.5-10.5 for rinsing after alkaline degreasing, and pH adjusted water in about 4-7 for rinsing after acid treatment.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、一般メッキ処理・表面加
工、粉末塗装処理・表面加工、メッキ加工表面加工等の表
面処理用廃水の再利用管理システムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a reuse management system for surface treatment wastewater such as general plating / surface treatment, powder coating / surface treatment, and plating surface treatment.

【0002】[0002]

【従来の技術】従来、表面処理用廃水(以下、廃水とす
る)の再利用及び/又は処理コスト低減を達成する手段の
一つとして、当該廃水の固液等分離処理、PH調整を利用
し、上水を略同等の清澄水を生成し、この清澄水を各種
槽の水洗用水(水洗水)として再利用する方法が提案さ
れている。本出願人もその一環として特許第3096292号
のメッキ処理における水の利用方法を提案している。その
他、前記方法と関連する他の文献としては、特開昭48-2
9267号の化学銅メッキ廃液の処理方法、又は特開昭50-1294
90号のクロム酸含有廃水の処理方法、特開平10-277565号の
廃液の処理方法が挙げられる。
2. Description of the Related Art Conventionally, as one of means for achieving reuse and / or reduction of treatment cost of surface treatment wastewater (hereinafter referred to as wastewater), solid-liquid separation treatment of the wastewater and PH adjustment have been used. In addition, a method has been proposed in which clean water is produced by substantially equalizing clean water, and this clear water is reused as washing water (wash water) for various tanks. As a part of this, the present applicant has also proposed a method of using water in the plating treatment of Japanese Patent No. 3096292. Other documents related to the above method include JP-A-48-2
No. 9267 chemical copper plating waste liquid treatment method, or JP-A-50-1294
No. 90, a method for treating chromic acid-containing wastewater, and JP-A-10-277565, a method for treating wastewater.

【0003】[0003]

【発明が解決しようとする課題】前記各文献は、廃水の
再利用及び/又は処理コスト低減には有効と思われるが、
この処理コスト低減の一層の向上を図るシステム、又は清澄水
を、多種にPH調整し、この所定数値としたPH調整の清澄
水(PH調整水)を、各槽に確実かつ必要量を供給するシス
テムは確立されていないこと、又は各層で処理したメッキ製
品の確実な洗浄と、効率的な洗浄とを図るには、必ずし
も十分とは云えないこと、等の改良点が考えられる。
The above documents are considered to be effective in reusing wastewater and / or reducing treatment costs.
A system for further improving the treatment cost reduction, or the pH of the clarified water is adjusted to various types, and the predetermined amount of the clarified water (PH adjusted water) of the pH adjustment is supplied to each tank in a reliable and necessary amount. Improvements such as the fact that the system has not been established, or that it is not necessarily sufficient to ensure reliable and efficient cleaning of the plated product treated with each layer, are considered.

【0004】[0004]

【課題を解決するための手段】請求項1の発明は、均一
な品質のPH調整水を、各槽の水洗水として利用する技術
の確立と、また所定数値としたPH調整の清澄水(PH調整
水)を、各槽に確実かつ必要量を供給するシステムの確立
と、又は各層で処理したメッキ製品の確実な洗浄と、効率
的な洗浄とを図ることを意図する。
Means for Solving the Problems The invention of claim 1 is to establish a technology for using uniform-quality PH-adjusted water as washing water for each tank, and to provide a pH-adjusted clarified water (PH) having a predetermined value. The purpose of the present invention is to establish a system for supplying the required amount of conditioned water to each tank reliably and reliably, or to surely and efficiently wash the plated product treated in each layer.

【0005】請求項1は、表面処理で発生した廃水を、
沈降装置により分離処理して、生成した清澄水をPH調整
し、このPH調整水を各槽に対応する数値に変換して供給
する廃水の再利用管理システムであって、前記PH調整水を、
アルカリ脱脂槽後の水洗用としてPH8.5〜10.5程度で供給
し、また酸処理槽後の水洗用としてPH4〜7程度で供給す
ることを特徴とするメッキ処理等表面処理用廃水の再利用
管理システムである。
[0005] Claim 1 is to use the wastewater generated by the surface treatment,
Separation treatment by a sedimentation device, the pH of the generated clarified water is adjusted, a wastewater reuse management system that converts the PH adjusted water to a numerical value corresponding to each tank and supplies the wastewater, wherein the PH adjusted water is
Recycling management of wastewater for surface treatment such as plating, which is supplied at about PH 8.5 to 10.5 for washing after alkali degreasing tank and about 4 to 7 for washing after acid treatment tank System.

【0006】請求項2の発明は、均一な品質のPH調整水
を、各槽の水洗水として利用する技術の確立と、またPH
調整水を、各槽に確実かつ必要量を供給するシステムの確立
と、又は各層で処理したメッキ製品の確実な洗浄と、効率
的な洗浄とを図ることを意図する。
[0006] The invention of claim 2 is to establish a technology for using the pH adjusted water of uniform quality as the washing water for each tank,
It is intended to establish a system for supplying the required amount of conditioned water to each tank with certainty, or to surely and efficiently wash plated products treated in each layer.

【0007】請求項2は、表面処理で発生した廃水を、
沈降装置により分離処理して、生成した清澄水をPH調整
し、このPH調整水を生成し、このPH調整水を略17℃〜26
℃程度に昇温し、このPH調整昇温水を各槽に対応する数
値に変換して供給する廃水の再利用管理システムであって、
前記PH調整水を、アルカリ脱脂槽後の水洗用としてPH8.5〜1
0.5程度で供給し、また酸処理槽後の水洗用としてPH4〜
7程度で供給することを特徴とするメッキ処理等表面処理用
廃水の再利用管理システムである。
[0007] Claim 2 is to use the wastewater generated by the surface treatment,
Separation treatment is performed by a sedimentation device, and the generated clarified water is adjusted to a PH. This PH adjusted water is generated.
This is a wastewater reuse management system that raises the temperature to about ℃ and converts this PH-adjusted temperature-raised water into a value corresponding to each tank and supplies it.
The pH-adjusted water, PH 8.5 ~ 1 for washing after the alkaline degreasing tank
Supplied at about 0.5, and PH4 ~ for water washing after acid treatment tank
This is a reuse management system for wastewater for surface treatment such as plating, which is supplied at about 7.

【0008】請求項3の発明は、均一な品質のPH調整水
を、各槽の水洗水として利用する技術の確立と、またPH
調整水を、各槽に確実かつ必要量を供給するシステムの確立
と、又は各層で処理したメッキ製品の確実な洗浄と、効率
的な洗浄とを図ることを意図する。
[0008] The invention of claim 3 is to establish a technology to use the pH adjusted water of uniform quality as the washing water for each tank,
It is intended to establish a system for supplying the required amount of conditioned water to each tank with certainty, or to surely and efficiently wash plated products treated in each layer.

【0009】請求項3は、表面処理で発生した廃水を、
沈降装置により分離処理して、生成した清澄水をPH調整
し、このPH調整水を生成し、このPH調整水を触媒手段で
活性化処理し、このPH調整活性水を各槽に対応する数値
に変換して供給する廃水の再利用管理システムであって、前
記PH調整活性水を、アルカリ脱脂槽後の水洗用としてPH8.5
〜10.5程度で供給し、また酸処理槽後の水洗用としてPH
4〜7程度で供給することを特徴とするメッキ処理等表面処
理用廃水の再利用管理システムである。請求項4の発明は、
均一な品質のPH調整水を、各槽の水洗水として利用する
工程の確立と、またPH調整水を、各槽に確実かつ必要量
を供給する工程の確立と、又は各層で処理したメッキ製品
の確実な洗浄と、効率的な洗浄とを図ることを意図す
る。
[0009] Claim 3 is to use the wastewater generated by the surface treatment,
Separation treatment is performed by a sedimentation device, and the generated clarified water is adjusted for PH, this PH adjusted water is generated, and the PH adjusted water is activated by a catalyst means. A wastewater reuse management system that converts and supplies the PH-adjusted activated water to PH8.5 for washing after an alkaline degreasing tank.
~ 10.5 and PH for washing after acid treatment tank
This is a recycling management system for wastewater for surface treatment such as plating, which is supplied at about 4 to 7. The invention of claim 4 is
Establishment of a process to use uniform quality PH adjustment water as washing water for each tank, establishment of a process to supply the required amount of PH adjustment water to each tank reliably, or plating products treated in each layer It is intended to ensure reliable cleaning and efficient cleaning.

【0010】請求項4は、表面処理で発生した廃水を、
沈降装置により分離処理して、清澄水を生成する工程
と、この清澄水をPH調整し、各数値のPH調整水を生成
し、この各数値のPH調整水を、個々の水槽に貯留する工
程と、この各水槽の各数値のPH調整水を、表面処理後の
水洗に利用するに際し、当該各数値のPH調整水を各水洗
に対応して個別に制御する工程と、前記制御をコンヒ゜ュータ
管理し、このコンヒ゜ュータのテ゛ータを、ホストコンヒ゜ュータに通信手段
を介して伝達する工程と、で構成されるメッキ処理等表面
処理用廃水の再利用管理システムである。請求項5の発明
は、均一な品質のPH調整水を、各槽の水洗水として利用
する工程の確立と、またPH調整水を、各槽に確実かつ必
要量を供給する工程の確立と、又は各層で処理したメッキ
製品の確実な洗浄と、効率的な洗浄とを図ることを意図
する。
[0010] Claim 4 is to use the wastewater generated by the surface treatment,
Separation process by a sedimentation device to produce clarified water, and PH adjustment of the clarified water to generate PH adjusted water of each numerical value, and storing the PH adjusted water of each numerical value in an individual water tank And, when using the PH adjusted water of each numerical value of each water tank for washing after surface treatment, individually controlling the PH adjusted water of each numerical value corresponding to each washing, and controlling the control by computer management. And a step of transmitting the data of the computer to the host computer via a communication means. This is a reuse management system for surface treatment wastewater such as plating. The invention of claim 5 establishes a step of using uniform-quality PH adjusted water as washing water in each tank, and establishes a step of supplying PH adjusted water to each tank reliably and in a required amount. Alternatively, it is intended to ensure reliable cleaning of the plated product treated with each layer and efficient cleaning.

【0011】請求項5は、表面処理で発生した廃水を、
沈降装置により分離処理して、清澄水を生成する工程
と、この清澄水をPH調整し、各数値のPH調整水を生成
し、この各数値のPH調整水を、略17℃〜26℃程度に昇温
し、PH調整昇温水を生成する工程と、このPH調整昇温水
を、個々の水槽に貯留する工程と、この各水槽の各数値
のPH調整水を、表面処理後の水洗に利用するに際し、当
該各数値のPH調整水を各水洗に対応して個別に制御する
工程と、前記制御をコンヒ゜ュータ管理し、このコンヒ゜ュータのテ゛ータ
を、ホストコンヒ゜ュータに通信手段を介して伝達する工程と、で
構成されるメッキ処理等表面処理用廃水の再利用管理システム
である。請求項6の発明は、均一な品質のPH調整水を、
各槽の水洗水として利用する工程の確立と、またPH調整
水を、各槽に確実かつ必要量を供給する工程の確立と、
又は各層で処理したメッキ製品の確実な洗浄と、効率的な
洗浄とを図ることを意図する。
[0011] Claim 5 relates to wastewater generated in the surface treatment,
Separation treatment by a sedimentation device to produce clarified water, and the pH of the clarified water is adjusted to generate PH adjusted water of each numerical value, and the PH adjusted water of each numerical value is approximately 17 ° C. to 26 ° C. The process of raising the temperature to pH and raising the temperature of the pH-adjusted heated water, the process of storing the temperature-adjusted PH-adjusted water in individual water tanks, and the use of the pH-adjusted water of each numerical value in each water tank for washing after surface treatment In doing so, a step of individually controlling the PH adjustment water of each numerical value corresponding to each washing, a step of managing the control by a computer, and a step of transmitting data of the computer to a host computer via a communication means, This is a reuse management system for wastewater for surface treatment such as plating, which is composed of: The invention of claim 6 provides a uniform quality PH adjustment water,
Establishment of a process to use as washing water for each tank, and establishment of a process to supply the required amount of PH adjusted water to each tank reliably and
Alternatively, it is intended to ensure reliable cleaning of the plated product treated with each layer and efficient cleaning.

【0012】請求項6は、表面処理で発生した廃水を、
沈降装置により分離処理して、清澄水を生成する工程
と、この清澄水をPH調整し、各数値のPH調整水を生成
し、この各数値のPH調整水を、触媒手段で活性化処理
し、PH調整活性水を生成する工程と、このPH調整活性水
を、個々の水槽に貯留する工程と、この各水槽の各数値
のPH調整水を、表面処理後の水洗に利用するに際し、当
該各数値のPH調整水を各水洗に対応して個別に制御する
工程と、前記制御をコンヒ゜ュータ管理し、このコンヒ゜ュータのテ゛ータ
を、ホストコンヒ゜ュータに通信手段を介して伝達する工程と、で
構成されるメッキ処理等表面処理用廃水の再利用管理システム
である。
[0012] Claim 6 is to treat the wastewater generated by the surface treatment,
Separating by a sedimentation device to produce clarified water, and adjusting the pH of the clarified water to generate each value of PH adjusted water, and activating the pH adjusted water of each value by catalytic means. A step of generating PH-adjusted active water, a step of storing the PH-adjusted active water in individual water tanks, and a step of using the PH-adjusted water of each numerical value of each water tank for washing after surface treatment. A step of individually controlling the PH adjustment water of each numerical value in accordance with each washing, and a step of managing the control by a computer, and transmitting data of the computer to the host computer via communication means. It is a reuse management system for wastewater for surface treatment such as plating.

【0013】[0013]

【発明の実施の形態】メッキ処理の廃水は、例えば、貯留
槽から分離槽、PH調整槽(反応槽)及び凝集槽等の各槽
(一例である。)において処理された後、沈澱装置を介
して固液分離処理される。この沈澱装置で清澄化された
処理水は、その後、一基又は数基の処理槽及び/又はPH
調整槽等に導かれてPH調整されることで、PH調整した清
澄水を得ることができる。尚、この触媒手段を備えた活
性処理装置を付設する構成では、PH調整した清澄水が活
性処理されることで、一層よどみ、悪臭等がなく、優れ
たPH調整した清澄水を得ることができる。
BEST MODE FOR CARRYING OUT THE INVENTION Wastewater from a plating treatment is treated in, for example, a storage tank, a separation tank, a PH adjustment tank (reaction tank), a flocculation tank, and other tanks (one example). Through a solid-liquid separation process. The treated water clarified by this settling device is then treated with one or several treatment tanks and / or PH
The pH is adjusted by being guided to an adjustment tank or the like, so that clear water whose pH has been adjusted can be obtained. In addition, in the configuration in which the activation treatment device provided with this catalyst means is attached, the clarified water whose pH has been adjusted is subjected to the activation treatment, so that there is no stagnation, odor, etc., and excellent clarified water with the adjusted PH can be obtained. .

【0014】この処理槽に続いてPH調整槽が設けられて
おり、このPH調整槽において、例えば、PH8.5〜10.5調整
水、又はPH4〜7調整水、またPH6〜8調整水に、それぞれ
変換される。この変換された各数値のPH調整水は、対応
する各処理槽に充填される。このPH8.5〜10.5調整水
は、アルカリ脱脂槽等のメッキ浴で処理したメッキ製品の水洗いに
利用される。またPH4〜7調整水は、酸処理槽で処理した
メッキ製品の水洗いに利用される。またPH6〜8の調整水
は、電解洗浄槽で処理したメッキ製品の水洗いに利用され
る。即ち、各段階のメッキ製品の処理に対応したPH調整水
で洗浄し、メッキ製品の負担をかけずに、順次薬品を洗い
流す構造である。尚、図示しないが、青化ソータ゛浴、シアン
浴、シ゛ンケート浴、酸性塩化アンモン浴等のそれぞれのメッキ浴に対
応したPH調整水を利用する。前記PH8.5〜10.5調整水、又
はPH4〜7調整水、またPH6〜8調整水に、それぞれ変換さ
れた後、活性処理装置おいて、活性処理されることもあ
る。このようにして生成されたPH8.5〜10.5調整活性
水、又はPH4〜7調整活性水、またPH6〜8調整活性水に、
それぞれ変換されて、それぞれメッキ浴に応じたアルカリ脱脂
槽、酸処理、電解洗浄槽等のメッキ浴の処理水として利用
される。
Following the treatment tank, a PH adjustment tank is provided. In the PH adjustment tank, for example, PH 8.5 to 10.5 adjusted water, PH 4 to 7 adjusted water, and PH 6 to 8 adjusted water, respectively. Is converted. The converted PH adjustment water of each numerical value is filled in each corresponding treatment tank. The pH 8.5 to 10.5 adjusted water is used for washing a plated product treated with a plating bath such as an alkaline degreasing tank. The PH4-7 adjusted water is used for washing the plated product treated in the acid treatment tank. The conditioned water of pH 6 to 8 is used for washing the plating product treated in the electrolytic cleaning tank. That is, the structure is such that washing is performed with PH adjustment water corresponding to the treatment of the plated product in each stage, and the chemicals are sequentially washed away without imposing a burden on the plated product. Although not shown, pH adjusting water corresponding to each plating bath such as a bluish sorter bath, a cyan bath, a sink bath, and an acidic ammonium chloride bath is used. After being converted into the PH 8.5-10.5 adjusted water, the PH 4-7 adjusted water, and the PH 6-8 adjusted water, respectively, they may be subjected to activation treatment in an activation treatment device. PH8.5-10.5 adjusted active water, or PH4-7 adjusted active water, PH6-8 adjusted active water thus generated,
Each is converted and used as a treatment water for a plating bath such as an alkali degreasing tank, an acid treatment, and an electrolytic cleaning tank according to the plating bath.

【0015】このように、メッキ処理に使用した廃水を、
例えば、PH8.5〜10.5調整水、又はPH4〜7調整水、またPH
6〜8調整水等に、それぞれ変換して利用することによっ
て、上水等の使用を極力押えることができる。また公害
の発生防止に役立つ特徴がある。
Thus, the wastewater used for the plating process is
For example, PH 8.5-10.5 adjusted water, or PH 4-7 adjusted water, PH
The use of clean water and the like can be suppressed as much as possible by converting it to 6-8 adjusted water and using it. It also has features that help prevent pollution.

【0016】尚、前記PH4〜7調整水を昇温して、例え
ば、PH8.5〜10.5調整昇温水、又はPH4〜7調整昇温水、ま
たPH6〜8調整昇温水として、かつ年中略17℃〜26℃程度
に温度管理することで、例えば、洗浄効果の向上、PH8.
5〜10.5調整昇温水、PH4〜7調整昇温水等の使用時間の
拡充、メッキ製品の品質の向上等に役立つことが考えられ
る。尚、理想の温度は15℃〜20℃である。殊に、脱脂処
理後の洗浄水の温度を略20℃〜25℃程度で利用する。
The PH4 to 7 adjusted water is heated to, for example, PH8.5 to 10.5 adjusted heated water, PH4 to 7 adjusted heated water, or PH6 to 8 adjusted heated water, and at approximately 17 ° C. throughout the year. By controlling the temperature to about 26 ° C, for example, improving the cleaning effect, PH8.
It is thought that it will be useful for expanding the use time of 5-10.5 adjusted warming water, PH4-7 adjusted warming water, etc., and improving the quality of plated products. Note that the ideal temperature is 15 ° C to 20 ° C. In particular, the temperature of the washing water after the degreasing treatment is used at about 20 ° C to 25 ° C.

【0017】またPH調整水の塩濃度の処理行うことで、
洗浄効果の向上、PH8.5〜10.5調整昇温水、PH4〜7調整
昇温水等の使用回数・時間の拡充、メッキ製品の品質の向
上等に役立つことが考えられる。尚、理想の数値は、1
0,000〜15,000μs(μs:マイクロシ゛ーメンス値)の範囲内を維
持する。
Further, by performing the treatment of the salt concentration of the pH adjustment water,
It is thought to be useful for improving the cleaning effect, increasing the number of times and time of using PH8.5-10.5 adjusted heated water, PH4-7 adjusted heated water, etc., and improving the quality of plated products. The ideal value is 1
Maintain within the range of 000 to 15,000 μs (μs: microsiemens value).

【0018】尚、本発明では、図例の如く、メッキ処理の
廃水の処理方法及び工程、又はメッキ処理方法・メッキ種類・
メッキ浴の種類及び工程、製品に基づくメッキ処理方法及び工
程等は、一例であり、各例の説明、図面、使用態様には
限定されないことと、従来の各種の表面処理用の廃水に
同様に利用できることと、その効果も同様に考えられ
る。
According to the present invention, as shown in the figure, a method and a process for treating wastewater for plating, or a plating method, a plating type,
The type and process of the plating bath, the plating method and process based on the product are merely examples, and the description, drawings, and usage modes of each example are not limited to the same, and similarly to the conventional wastewater for various surface treatments. What is available and its effect are equally conceivable.

【0019】前記PH調整、PH調整水・PH調整活性水・PH
調整昇温水の生成と、このPH調整水・PH調整活性水等の
給排・停止又は量等の制御をコンヒ゜ュータ管理し、このコンヒ゜ュ
ータのテ゛ータを、ホストコンヒ゜ュータに通信手段を介して伝達し、工
程管理、指導・運転・警報管理、金銭管理等に利用す
る。
PH adjustment, PH adjustment water / PH adjustment activated water / PH
A computer manages the generation of the adjusted temperature-raised water and the control of supply / discharge, stop, and amount of the PH-adjusted water / PH-adjusted activated water, etc., and transmits the data of the computer to the host computer via communication means. Used for management, guidance / driving / alarm management, money management, etc.

【0020】[0020]

【実施例】以下、本発明の一実施例を説明する。An embodiment of the present invention will be described below.

【0021】メッキ処理の廃水Aは、貯留槽1から分離槽2、
PH調整槽3及び凝集槽4等の各槽(一例である。)におい
て処理された後、沈澱装置5を介して固液分離処理され
る。この沈澱装置5で清澄化された処理水Bは、図1の模
式図の如く、一基又は数基の処理槽6a、6b、6c〜6nに導
かれPH調整され、例えば、PH8.5〜10.5調整水6a-1、又
はPH4〜7調整水6b-1、またPH6〜8調整水6c-1に、それぞ
れ変換される。そして、このPH8.5〜10.5調整水6a-1
は、アルカリ脱脂槽7で処理したメッキ製品の水洗いに利用され
る。またPH4〜7調整水6b-1は、酸処理槽9で処理したメッキ
製品の水洗いに利用される。またPH6〜8の調整水6c-1
は、電解洗浄槽11等のメッキ浴で処理したメッキ製品の水洗い
に利用される。尚、PH8.5〜10.5調整水6a-1、又はPH4〜
7調整水6b-1、またPH6〜8調整水6c-1を、冷却器20を介
してセラミックホ゛ール200、炭素棒等の触媒手段21に送り、この
触媒手段21を利用して活性化を図り、一層よどみ、悪臭
等をなくす処理を行うことで、例えば、PH8.5〜10.5調
整活性水、又はPH4〜7調整活性水、又はPH6〜8調整活性
水を生成し(後述する)、このPH8.5〜10.5調整活性水
等を水洗水として利用する。
The wastewater A of the plating treatment is transferred from the storage tank 1 to the separation tank 2,
After the treatment in each of the tanks (one example) such as the PH adjustment tank 3 and the coagulation tank 4, the solid-liquid separation treatment is performed via the precipitation device 5. The treated water B clarified by the settling device 5 is guided to one or several treatment tanks 6a, 6b, 6c to 6n as shown in the schematic diagram of FIG. It is converted into 10.5 adjusted water 6a-1, PH4-7 adjusted water 6b-1, and PH6-8 adjusted water 6c-1, respectively. And this PH8.5 ~ 10.5 adjusted water 6a-1
Is used for washing the plated product treated in the alkaline degreasing tank 7 with water. The PH4 to PH7 adjusted water 6b-1 is used for washing the plated product treated in the acid treatment tank 9. Adjustment water 6c-1 for PH6 ~ 8
Is used for washing the plated product treated with a plating bath such as the electrolytic cleaning tank 11 with water. In addition, PH8.5 ~ 10.5 adjusted water 6a-1, or PH4 ~
(7) Adjusted water 6b-1 and PH6-8 adjusted water 6c-1 are sent through a cooler 20 to a catalyst means 21 such as a ceramic wheel 200 or a carbon rod, and the catalyst means 21 is used for activation. By performing a treatment for eliminating further stagnation and offensive odor, for example, PH8.5 to 10.5 adjusted active water, PH4 to 7 adjusted active water, or PH6 to 8 adjusted active water is generated (described later). .5 to 10.5 Use adjusted active water as washing water.

【0022】図中水洗8、8a、8b、8c〜8nとある場合に
は、このPH8.5〜10.5調整水6a-1(PH9〜10調整水が理想
である)を水洗8cから水洗8にリターンする構成である。水洗
8cに上水Cを利用することもある。尚、図示しないが、
このPH6〜8調整水6c-1の利用は、水洗10、10a、10b、10
c〜10nを循環移行する例、順次移行する例等もある(他
の水洗も可能である)。そして、前記中水洗8、8a、8
b、8c〜8nへのPH8.5〜10.5調整水6a-1等の供給量、給停
は、コンヒ゜ュータ管理と、電磁弁等の制御手段(図示せず)でコ
ントロールされる(他の例も同じ)。
In the figure, when there are washings 8, 8a, 8b, 8c to 8n, the PH 8.5 to 10.5 adjusted water 6a-1 (PH 9 to 10 adjusted water is ideal) is changed from the washing 8c to the washing 8 It is a configuration that returns. Washing
8c may use tap water C. Although not shown,
The use of this PH 6-8 adjusted water 6c-1 is for water washing 10, 10a, 10b, 10
There is an example in which c to 10n are cyclically transferred, and an example in which the transfer is performed sequentially (other washing is also possible). And said middle water washing 8, 8a, 8
b, the supply amount and stoppage of PH 8.5 to 10.5 adjusted water 6a-1 to 8c to 8n are controlled by computer management and control means (not shown) such as a solenoid valve (other examples are also provided). the same).

【0023】図中水洗10とある場合には、このPH4〜7調
整水6b-1(PH5〜6調整水が理想である)を水洗に使用する
構成である。水洗10に上水を利用することもある。尚、
図示しないが、このPH6〜8調整水6b-1の利用は、前記水
洗10a〜10nを循環移行する例、順次移行する例等もある
(他の水洗も可能である)。
In the figure, when there is a washing 10 in the figure, the PH4-7 adjusted water 6b-1 (PH5-6 adjusted water is ideal) is used for washing. Water may be used for washing 10. still,
Although not shown, the use of the PH 6-8 conditioning water 6b-1 includes an example in which the washings 10a to 10n are circulated, and an example in which the washings are sequentially shifted (other washing is also possible).

【0024】また図中水洗12〜12nとある場合には、こ
のPH6〜8調整水6c-1(PH7〜9調整水が理想である)を水洗
に使用する構成である。このPH6〜8調整水6c-1を水洗12
から水洗12aにリターンする構成である。
In the figure, when there is a washing 12-12n, the PH 6-8 adjusted water 6c-1 (PH 7-9 adjusted water is ideal) is used for washing. Wash this PH 6 ~ 8 adjusted water 6c-1 with water 12
This is a configuration to return to the water washing 12a from.

【0025】尚、前記PH8.5〜10.5調整水6a-1、又はPH4
〜7調整水6b-1、またPH6〜8調整水6c-1を、温度処理し
て略17℃〜26℃程度まで昇温して、PH8.5〜10.5調整昇
温水6a-10、又はPH4〜7調整昇温水6b-10、またPH6〜8調
整昇温水6c-10は、原則として前述の例に準ずる。尚、
このPH8.5〜10.5調整昇温水6a-10、又はPH4〜7調整昇温
水6b-10の塩濃度を、10,000〜15,000μsの範囲内に維持
した状態で、亜鉛メッキ13の処理後の洗浄水に利用する。
例えば、水洗14、14a、14b〜14nとある場合には、このP
H8.5〜10.5調整昇温水6a-10等を水洗14に導入した後、リ
ターンして水洗14nに導く構成とする。また水洗14に上水C
を使用することもある。そして、説明しない他の特徴
は、それぞれ前述の例に準ずる。
The pH 8.5 to 10.5 adjusted water 6a-1 or PH4
77 conditioned water 6b-1 and PH6-8 conditioned water 6c-1 are temperature-treated and heated to approximately 17 ° C to 26 ° C, and PH8.5 to 10.5 adjusted heated water 6a-10 or PH4 The temperature-controlling water 6b-10 for adjusting the temperature to 7 and the temperature-controlling water 6c-10 for adjusting the pH 6 to 8 follow the above-described example in principle. still,
Washing water after the treatment of the zinc plating 13 while maintaining the salt concentration of the PH 8.5-10.5 adjusted warmed water 6a-10 or the PH 4-7 adjusted warmed water 6b-10 within the range of 10,000-15,000 μs. Use for
For example, if there are washings 14, 14a, 14b to 14n, this P
After the H8.5 to 10.5 adjusted heated water 6a-10 and the like are introduced into the rinsing water 14, the water is returned and guided to the rinsing water 14n. Also wash water 14 to clean water C
Sometimes used. Other features that are not described follow the above-described examples.

【0026】また触媒手段21を利用して生成されたPH8.
5〜10.5調整活性水6a-100、PH4〜7調整活性水6b-100、又
はPH6〜8調整活性水6c-100、原則として前述の例に準ず
る。またこの触媒手段21は、前記PH8.5〜10.5調整昇温
水6a-10、PH4〜7調整昇温水6b-10、又はPH6〜8調整昇温
水6c-10の処理にも利用できる。尚、触媒手段21は、図
示しないが、処理槽6a〜6n等に設けて、PH調整前でも可
能である。
Further, PH8.
5 to 10.5 adjusted active water 6a-100, PH4 to 7 adjusted active water 6b-100, or PH6 to 8 adjusted active water 6c-100, in principle, according to the above example. The catalyst means 21 can also be used for the treatment of the PH 8.5-10.5 adjusted warmed water 6a-10, PH4-7 adjusted warmed water 6b-10, or PH6-8 adjusted warmed water 6c-10. Although not shown, the catalyst means 21 may be provided in the processing tanks 6a to 6n and the like, and may be provided before the PH adjustment.

【0027】前記水洗8、8a、8b、8c〜8nへのPH8.5〜1
0.5調整水6a-1、水洗10、10a、10b、10c〜8nへのPH4〜7
調整水6b-1、更には水洗12、12a、12b、12c〜12nへのPH
6〜8調整水6c-1、等の供給量、給停は、コンヒ゜ュータ管理
と、電磁弁等の制御手段でコントロールされる。このコンヒ゜ュータ
のテ゛ータを、ホストコンヒ゜ュータに通信手段を介して伝達し、工程
管理、指導・運転・警報管理、金銭管理等に利用する。
同様にPH8.5〜10.5調整活性水6a-100、PH4〜7調整活性水
6b-100、或いはPH8.5〜10.5調整昇温水6a-10、PH4〜7調
整昇温水6b-10等の供給量、給停は、コンヒ゜ュータ管理と、電
磁弁等の制御手段でコントロールされる等前の例に準ずる。従
って、前述の如く、メッキ工程管理、メッキ・水・工場等の指
導・運転・警報管理、管理ミスの減少化、コストの低廉化、
又は上水利用、公害の減少化、品質・金銭管理等に利用
できる。
PH 8.5-1 to the above-mentioned water washing 8, 8a, 8b, 8c-8n
0.5 adjusted water 6a-1, water washing 10, 10a, 10b, 10c ~ 8n to PH 8 ~ 7
Conditioning water 6b-1, and PH to washing 12, 12a, 12b, 12c-12n
The supply amount and supply / discharge of the 6-8 conditioned water 6c-1, etc. are controlled by computer management and control means such as a solenoid valve. The data of this computer is transmitted to the host computer via communication means, and is used for process management, guidance / operation / alarm management, money management, and the like.
Similarly, PH 8.5-10.5 adjusted active water 6a-100, PH 4-7 adjusted active water
The supply amount and supply / discharge of 6b-100, or PH8.5 to 10.5 adjusted heating water 6a-10, PH4 to 7 adjusted heating water 6b-10, etc., are controlled by computer management and control means such as solenoid valves, etc. Follow the previous example. Therefore, as mentioned above, plating process management, guidance, operation and alarm management of plating, water, factory, etc., reduction of management mistakes, cost reduction,
Or it can be used for tap water use, reduction of pollution, quality and money management, etc.

【0028】[0028]

【発明の効果】請求項1の発明は、表面処理で発生した
廃水を、沈降装置により分離処理して、生成した清澄水
をPH調整し、PH調整水を各槽に対応する数値に変換して
供給する廃水の再利用管理システムであって、PH調整水を、
アルカリ脱脂槽後の水洗用としてPH8.5〜10.5程度で供給
し、酸処理槽後の水洗用としてPH4〜7程度で供給するメッ
キ処理等表面処理用廃水の再利用管理システムである。従っ
て、均一な品質のPH調整水を、各槽の水洗水として利用
する技術の確立と、また所定数値としたPH調整水を、各
槽に確実かつ必要量を供給するシステムの確立と、又は各層
で処理したメッキ製品の確実な洗浄と、効率的な洗浄とが
図れること、等の特徴がある。
According to the first aspect of the present invention, wastewater generated by surface treatment is separated by a sedimentation device, and the generated clarified water is adjusted for PH, and the PH adjusted water is converted into a numerical value corresponding to each tank. Wastewater reuse management system that supplies PH-adjusted water,
This is a reuse management system for surface treatment wastewater, such as plating, which is supplied at about PH 8.5 to 10.5 for washing after an alkali degreasing tank and supplied at about PH 4 to 7 for washing after an acid treatment tank. Therefore, the establishment of technology to use uniform-quality PH adjusted water as the washing water for each tank, and the establishment of a system that reliably and reliably supplies the required amount of PH adjusted water with a predetermined value to each tank, or There are features such as reliable and efficient cleaning of the plated product treated in each layer.

【0029】請求項2の発明は、表面処理で発生した廃
水を、沈降装置により分離処理して、生成した清澄水を
PH調整して、PH調整水を生成し、このPH調整水を略17℃
〜26℃程度に昇温し、PH調整昇温水を各槽に対応する数
値に変換して供給する廃水の再利用管理システムであって、
PH調整水を、アルカリ脱脂槽後の水洗用としてPH8.5〜10.5
程度で供給し、酸処理槽後の水洗用としてPH4〜7程度で
供給するメッキ処理等表面処理用廃水の再利用管理システムで
ある。従って、均一な品質のPH調整水を、各槽の水洗水
として利用する技術の確立と、またPH調整水を、各槽に
確実かつ必要量を供給するシステムの確立と、又は各層で処
理したメッキ製品の確実な洗浄と、効率的な洗浄とが図れ
ること、等の特徴がある。
According to a second aspect of the present invention, the waste water generated by the surface treatment is separated by a settling device, and the generated clear water is separated.
PH adjustment to produce PH adjustment water, this PH adjustment water at about 17 ℃
It is a wastewater reuse management system that raises the temperature to about 26 ° C, converts the pH-adjusted temperature-raised water into numerical values corresponding to each tank, and supplies it.
PH adjusted water, PH 8.5 to 10.5 for washing after alkaline degreasing tank
It is a reuse management system for surface treatment wastewater, such as plating, which is supplied at about PH4 and supplied at about PH4-7 for washing after the acid treatment tank. Therefore, the establishment of technology to use uniform-quality PH adjusted water as washing water for each tank, and the establishment of a system to supply the required amount of PH adjusted water to each tank reliably and at each layer, or Features include reliable and efficient cleaning of plated products.

【0030】請求項3の発明は、表面処理で発生した廃
水を、沈降装置により分離処理して、生成した清澄水を
PH調整して、PH調整水を生成し、PH調整水を触媒手段で
活性化処理し、PH調整活性水を各槽に対応する数値に変
換して供給する廃水の再利用管理システムであって、PH調整
活性水を、アルカリ脱脂槽後の水洗用としてPH8.5〜10.5程
度で供給し、酸処理槽後の水洗用としてPH4〜7程度で供
給するメッキ処理等表面処理用廃水の再利用管理システムであ
る。従って、均一な品質のPH調整水を、各槽の水洗水と
して利用する技術の確立と、またPH調整水を、各槽に確
実かつ必要量を供給するシステムの確立と、又は各層で処理
したメッキ製品の確実な洗浄と、効率的な洗浄とが図れる
こと、等の特徴がある。
According to a third aspect of the present invention, waste water generated by the surface treatment is separated by a sedimentation device, and the generated clear water is separated.
This is a wastewater reuse management system that adjusts PH, generates PH-adjusted water, activates the PH-adjusted water with catalytic means, converts the PH-adjusted active water into numerical values corresponding to each tank, and supplies it. Re-use of pH-adjusted activated water at pH 8.5-10.5 for washing after alkaline degreasing tank and PH4-7 for washing after acid treatment tank It is a management system. Therefore, the establishment of technology to use uniform-quality PH adjusted water as washing water for each tank, and the establishment of a system to supply the required amount of PH adjusted water to each tank reliably and at each layer, or Features include reliable and efficient cleaning of plated products.

【0031】請求項4の発明は、表面処理で発生した廃
水を、沈降装置により分離処理して、清澄水を生成する
工程と、清澄水をPH調整し、各数値のPH調整水を生成
し、この各数値のPH調整水を、個々の水槽に貯留する工
程と、各水槽の各数値のPH調整水を、表面処理後の水洗
に利用するに際し、当該各数値のPH調整水を各水洗に対
応して個別に制御する工程と、制御をコンヒ゜ュータ管理し、コ
ンヒ゜ュータのテ゛ータを、ホストコンヒ゜ュータに通信手段を介して伝達す
る工程と、で構成されるメッキ処理等表面処理用廃水の再
利用管理システムである。従って、均一な品質のPH調整水
を、各槽の水洗水として利用する工程の確立と、またPH
調整水を、各槽に確実かつ必要量を供給する工程の確立
と、又は各層で処理したメッキ製品の確実な洗浄と、効率
的な洗浄とが図れること、またメッキ工程管理、メッキ・水・
工場等の指導・運転・警報管理、又は上水利用、公害の
減少化、品質・金銭管理等に利用できること、等の特徴
がある。
The invention according to claim 4 is a step of separating waste water generated by the surface treatment by a settling device to produce clarified water, and adjusting the pH of the clarified water to produce PH adjusted water of each numerical value. In the process of storing the pH-adjusted water of each numerical value in an individual water tank and using the PH-adjusted water of each numerical value of each water tank for washing after surface treatment, the PH-adjusted water of each numerical value is washed with each water. The process of individually controlling the computer in accordance with the requirements and the process of transmitting the computer data to the host computer via a communication means by controlling the computer with the control, and the reuse management of the wastewater for surface treatment such as plating. System. Therefore, establish a process to use uniform quality PH adjusted water as washing water for each tank, and
Establish a process to supply the required amount of conditioned water to each tank reliably, and ensure that plating products treated in each layer can be reliably and efficiently cleaned.Plating process management, plating / water /
It can be used for guidance / operation / warning management of factories, etc., or for use of water supply, reduction of pollution, quality / money management, etc.

【0032】請求項5の発明は、表面処理で発生した廃
水を、沈降装置により分離処理して、清澄水を生成する
工程と、清澄水をPH調整し、各数値のPH調整水を生成
し、この各数値のPH調整水を、略17℃〜26℃程度に昇温
し、PH調整昇温水を生成する工程と、PH調整昇温水を、
個々の水槽に貯留する工程と、各水槽の各数値のPH調整
水を、表面処理後の水洗に利用するに際し、各数値のPH
調整水を各水洗に対応して個別に制御する工程と、制御
をコンヒ゜ュータ管理し、コンヒ゜ュータのテ゛ータを、ホストコンヒ゜ュータに通信
手段を介して伝達する工程と、で構成されるメッキ処理等
表面処理用廃水の再利用管理システムである。従って、均一
な品質のPH調整水を、各槽の水洗水として利用する工程
の確立と、またPH調整水を、各槽に確実かつ必要量を供
給する工程の確立と、各層で処理したメッキ製品の確実な
洗浄と、効率的な洗浄とが図れること、又はメッキ工程管
理、メッキ・水・工場等の指導・運転・警報管理等に利用
できること、等の特徴がある。
The invention of claim 5 is a step of separating waste water generated by the surface treatment by a sedimentation device to produce clarified water, and adjusting the pH of the clarified water to produce PH adjusted water of each numerical value. A step of raising the PH adjusted water of each numerical value to about 17 ° C. to 26 ° C. to generate the PH adjusted heated water,
In the process of storing in individual water tanks and using the pH adjusted water of each numerical value in each water tank for washing after surface treatment,
A step of individually controlling the conditioned water for each washing, and a step of computer-controlling the control and transmitting the computer data to the host computer via communication means, for plating and other surface treatments. It is a wastewater reuse management system. Therefore, establish a process to use uniform quality PH adjustment water as washing water in each tank, establish a process to supply the required amount of PH adjustment water to each tank with certainty, and perform plating in each layer. Features include reliable washing of products and efficient washing, and use for plating process management, guidance, operation, and alarm management for plating, water, and factories.

【0033】請求項6の発明は、表面処理で発生した廃
水を、沈降装置により分離処理して、清澄水を生成する
工程と、清澄水をPH調整し、各数値のPH調整水を生成
し、各数値のPH調整水を、触媒手段で活性化処理し、PH
調整活性水を生成する工程と、PH調整活性水を、個々の
水槽に貯留する工程と、各水槽の各数値のPH調整水を、
表面処理後の水洗に利用するに際し、各数値のPH調整水
を各水洗に対応して個別に制御する工程と、制御をコンヒ゜
ュータ管理し、コンヒ゜ュータのテ゛ータを、ホストコンヒ゜ュータに通信手段を
介して伝達する工程と、で構成されるメッキ処理等表面処
理用廃水の再利用管理システムである。従って、均一な品質
のPH調整水を、各槽の水洗水として利用する工程の確立
と、またPH調整水を、各槽に確実かつ必要量を供給する
工程の確立と、各層で処理したメッキ製品の確実な洗浄
と、効率的な洗浄とが図れること、又はメッキ工程管理、メ
ッキ・水・工場等の指導・運転・警報管理等に利用できる
こと、等の特徴がある。更には、前記テ゛ータ管理を介して
使用する水、薬品等の使用量、処理時間、再利用回数等
を、従来の方法による使用する水、薬品等の使用量、処
理時間等と対比することで、金銭・資産・コスト等の対比
を顧客に提示することが可能となり、効率的な管理、販
路の拡充等が図れる実益がある。
[0033] The invention of claim 6 is a step of separating wastewater generated in the surface treatment by a sedimentation device to produce clarified water, and adjusting the pH of the clarified water to produce PH adjusted water of each numerical value. Activate the pH-adjusted water of each numerical value by catalytic means,
A step of generating adjusted active water, a step of storing PH adjusted active water in individual water tanks,
When using for water washing after surface treatment, the process of individually controlling the PH adjustment water of each numerical value corresponding to each washing, and computer control of the control, and transmitting the data of the computer to the host computer via communication means And a reuse management system for surface treatment wastewater such as plating. Therefore, establish a process to use uniform quality PH adjustment water as washing water in each tank, establish a process to supply the required amount of PH adjustment water to each tank with certainty, and perform plating in each layer. Features include reliable washing of products and efficient washing, and use for plating process management, guidance, operation, and alarm management for plating, water, and factories. Furthermore, the amount of water and chemicals used through the data management, the processing time, the number of reuses, and the like are compared with the amounts of water and chemicals used in the conventional method, the processing time, and the like. In addition, it is possible to present a comparison of money, assets, costs, and the like to a customer, and there is a real profit that efficient management and expansion of a sales channel can be achieved.

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

【図1】廃水を濾過する工程の一例を示す模式図であ
る。
FIG. 1 is a schematic diagram illustrating an example of a process of filtering wastewater.

【図2】メッキ工程の一例を示す要部の模式図である。FIG. 2 is a schematic diagram of a main part showing an example of a plating step.

【図3】メッキ工程の一例を示す模式図である。FIG. 3 is a schematic view illustrating an example of a plating step.

【図4】メッキ工程の他の一例を示す模式図である。FIG. 4 is a schematic view showing another example of the plating step.

【符号の説明】[Explanation of symbols]

1 貯留槽 2 分離槽 3 PH調整槽 4 凝集槽 5 沈澱装置 6a〜6n 処理槽 6a-1 PH8.5〜10.5調整水 6b-1 PH4〜7調整水 6c-1 PH6〜8調整水 6a-10 PH8.5〜10.5調整昇温水 6b-10 PH4〜7調整昇温水 6c-10 PH6〜8調整昇温水 6a-100 PH8.5〜10.5調整活性水 6b-100 PH4〜7調整活性水 6c-100 PH6〜8調整活性水 7 アルカリ脱脂槽 8〜8n 水洗 9 酸処理槽 10〜10n 水洗 11 電解洗浄槽 12〜12n 水洗 13 亜鉛メッキ 14〜14n 水洗 20 冷却器 21 触媒手段 200 セラミックホ゛ール A 廃水 B 処理水 C 上水 1 Storage tank 2 Separation tank 3 PH adjustment tank 4 Coagulation tank 5 Precipitation device 6a-6n Treatment tank 6a-1 PH8.5-10.5 conditioned water 6b-1 PH4-7 conditioned water 6c-1 PH6-8 conditioned water 6a-10 PH8.5 ~ 10.5 Adjusted heating water 6b-10 PH4 ~ 7 Adjusted heating water 6c-10 PH6 ~ 8 Adjusted heating water 6a-100 PH8.5 ~ 10.5 adjusted activated water 6b-100 PH4 ~ 7 Adjusted activated water 6c-100 PH6 -8 Adjusted activated water 7 Alkaline degreasing tank 8-8n water washing 9 Acid treatment tank 10-10n water washing 11 Electrolytic washing tank 12-12n water washing 13 Galvanized 14-14n water washing 20 Cooler 21 Catalyst means 200 Ceramic hole A Wastewater B Treated water C tap water

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/66 530 C02F 1/66 530L C23G 3/00 C23G 3/00 C25D 21/18 C25D 21/18 E (72)発明者 加納 昌武 名古屋市港区入場1丁目206−2 株式会 社スイレイ内 (72)発明者 榊間 捷之 名古屋市港区正保町4−15 株式会社ケイ エス理化内 (72)発明者 金子 聡 三重県津市南が丘2−25−16 Fターム(参考) 4D015 BA19 BB02 CA20 EA32 FA28 4D062 BA19 BB02 CA20 EA32 FA28 4K053 TA09 TA12 YA01 YA06 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/66 530 C02F 1/66 530L C23G 3/00 C23G 3/00 C25D 21/18 C25D 21/18 E (72) Inventor Masatake Kano 1-206-2, Minato-ku, Nagoya-shi, Japan Suirei Co., Ltd. (72) Inventor Katsuyuki Sakaki 4-15 Shobocho, Minato-ku, Nagoya-shi KS Rika Co., Ltd. (72) Invention Person Satoshi Kaneko 2-25-16 Minamigaoka, Tsu-shi, Mie F-term (reference) 4D015 BA19 BB02 CA20 EA32 FA28 4D062 BA19 BB02 CA20 EA32 FA28 4K053 TA09 TA12 YA01 YA06

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 表面処理で発生した廃水を、沈降装置に
より分離処理して、生成した清澄水をPH調整し、このPH
調整の清澄水(PH調整水)を各槽に対応する数値に変換
して供給する廃水の再利用管理システムであって、 前記PH調整水を、アルカリ脱脂槽後の水洗用としてPH8.5〜1
0.5程度で供給し、また酸処理槽後の水洗用としてPH4〜
7程度で供給することを特徴とするメッキ処理等表面処理用
廃水の再利用管理システム。
1. A wastewater generated in a surface treatment is separated by a sedimentation device, and a clarified water generated is adjusted in pH.
A wastewater reuse management system that converts adjusted clarified water (PH adjusted water) to a value corresponding to each tank and supplies the adjusted pH, wherein the PH adjusted water is used for washing after an alkaline degreasing tank with a pH of 8.5 to 8.5. 1
Supplied at about 0.5, and PH4 ~ for water washing after acid treatment tank
A recycling management system for wastewater for surface treatment, such as plating, which is supplied at about 7.
【請求項2】 表面処理で発生した廃水を、沈降装置に
より分離処理して、生成した清澄水をPH調整し、このPH
調整の清澄水(PH調整水)を生成し、このPH調整水を略
17℃〜26℃程度に昇温し、このPH調整昇温水を各槽に対
応する数値に変換して供給する廃水の再利用管理システムで
あって、 前記PH調整水を、アルカリ脱脂槽後の水洗用としてPH8.5〜1
0.5程度で供給し、また酸処理槽後の水洗用としてPH4〜
7程度で供給することを特徴とするメッキ処理等表面処理用
廃水の再利用管理システム。
2. The wastewater generated by the surface treatment is separated by a settling device, and the generated clear water is adjusted to a pH.
Generates clear water for adjustment (PH adjustment water) and abbreviates this PH adjustment water.
It is a wastewater reuse management system which raises the temperature to about 17 ° C. to 26 ° C., converts the PH-adjusted temperature-raised water into a value corresponding to each tank, and supplies the wastewater. PH8.5-1 for washing
Supplied at about 0.5, and PH4 ~ for water washing after acid treatment tank
A recycling management system for wastewater for surface treatment, such as plating, which is supplied at about 7.
【請求項3】 表面処理で発生した廃水を、沈降装置に
より分離処理して、生成した清澄水をPH調整し、このPH
調整の清澄水(PH調整水)を生成し、このPH調整水を触
媒手段で活性化処理し、このPH調整活性水を各槽に対応
する数値に変換して供給する廃水の再利用管理システムであ
って、 前記PH調整活性水を、アルカリ脱脂槽後の水洗用としてPH8.
5〜10.5程度で供給し、また酸処理槽後の水洗用としてP
H4〜7程度で供給することを特徴とするメッキ処理等表面処
理用廃水の再利用管理システム。
3. The wastewater generated in the surface treatment is separated by a sedimentation device, and the generated clear water is adjusted in pH.
Refined clear water (PH adjustment water) is generated, this PH adjustment water is activated by catalytic means, and this PH adjustment activated water is converted into numerical values corresponding to each tank and supplied to a wastewater reuse management system. The PH-adjusted activated water, PH8.
Supplied at about 5 to 10.5, and P for water washing after acid treatment tank
A recycling management system for wastewater for surface treatment such as plating, which is supplied at about H4 ~ 7.
【請求項4】 表面処理で発生した廃水を、沈降装置に
より分離処理して、清澄水を生成する工程と、 この清澄水をPH調整し、各数値のPH調整の清澄水(PH調
整水)を生成し、この各数値のPH調整水を、個々の水槽
に貯留する工程と、 この各水槽の各数値のPH調整水を、表面処理後の水洗に
利用するに際し、当該各数値のPH調整水を各水洗に対応
して個別に制御する工程と、 前記制御をコンヒ゜ュータ管理し、このコンヒ゜ュータのテ゛ータを、ホストコ
ンヒ゜ュータに通信手段を介して伝達する工程と、 で構成されるメッキ処理等表面処理用廃水の再利用管理システ
ム。
4. A step of separating wastewater generated by the surface treatment by a sedimentation device to produce clarified water, and adjusting the pH of the clarified water to obtain a clarified water (PH-adjusted water) of each value. And the step of storing the pH-adjusted water of each numerical value in an individual water tank, and the step of using the PH-adjusted water of each numerical value of each water tank for washing after surface treatment. A step of individually controlling water in response to each washing; and a step of computer-controlling the control and a step of transmitting data of the computer to a host computer via communication means. Wastewater reuse management system.
【請求項5】 表面処理で発生した廃水を、沈降装置に
より分離処理して、清澄水を生成する工程と、 この清澄水をPH調整し、各数値のPH調整の清澄水(PH調
整水)を生成し、この各数値のPH調整水を、略17℃〜26
℃程度に昇温し、PH調整昇温水を生成する工程と、 このPH調整昇温水を、個々の水槽に貯留する工程と、 この各水槽の各数値のPH調整水を、表面処理後の水洗に
利用するに際し、当該各数値のPH調整水を各水洗に対応
して個別に制御する工程と、 前記制御をコンヒ゜ュータ管理し、このコンヒ゜ュータのテ゛ータを、ホストコ
ンヒ゜ュータに通信手段を介して伝達する工程と、 で構成されるメッキ処理等表面処理用廃水の再利用管理システ
ム。
5. A process for separating waste water generated in the surface treatment by a sedimentation device to produce clarified water, adjusting the pH of the clarified water, and adjusting the clarified water (PH adjusted water) for each numerical value. Generate PH adjusted water of each numerical value, approximately 17 ℃ ~ 26
The process of raising the temperature to about ℃ and generating the pH-adjusted temperature-raised water; the process of storing the PH-adjusted temperature-raised water in individual water tanks; A step of individually controlling the PH-adjusted water of each numerical value corresponding to each washing, and a step of managing the control by a computer, and transmitting data of the computer to a host computer via a communication means. And a reuse management system for wastewater for surface treatment such as plating.
【請求項6】 表面処理で発生した廃水を、沈降装置に
より分離処理して、清澄水を生成する工程と、 この清澄水をPH調整し、各数値のPH調整の清澄水(PH調
整水)を生成し、この各数値のPH調整水を、触媒手段で
活性化処理し、PH調整活性水を生成する工程と、 このPH調整活性水を、個々の水槽に貯留する工程と、 この各水槽の各数値のPH調整水を、表面処理後の水洗に
利用するに際し、当該各数値のPH調整水を各水洗に対応
して個別に制御する工程と、 前記制御をコンヒ゜ュータ管理し、このコンヒ゜ュータのテ゛ータを、ホストコ
ンヒ゜ュータに通信手段を介して伝達する工程と、 で構成されるメッキ処理等表面処理用廃水の再利用管理システ
ム。
6. A step of separating wastewater generated in the surface treatment by a sedimentation device to generate clarified water, and adjusting the pH of the clarified water to adjust clarified water (PH adjusted water) for each numerical value. A step of activating the pH-adjusted water of each numerical value by a catalyst means to generate PH-adjusted active water; and a step of storing the PH-adjusted active water in individual water tanks. When the pH adjusted water of each numerical value of the above is used for washing after surface treatment, a step of individually controlling the PH adjusted water of each numerical value corresponding to each washing, and computer controlling the control, and controlling the computer. Transmitting the data to the host computer via a communication means; and a wastewater treatment system for surface treatment such as plating.
JP2000322855A 2000-10-23 2000-10-23 Recycling system of waste water from surface treatment process such as plating Pending JP2002129398A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000322855A JP2002129398A (en) 2000-10-23 2000-10-23 Recycling system of waste water from surface treatment process such as plating

Publications (1)

Publication Number Publication Date
JP2002129398A true JP2002129398A (en) 2002-05-09

Family

ID=18800654

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002129398A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010274244A (en) * 2009-06-01 2010-12-09 Nippon Steel Corp Method for clarifying treatment of steel production waste water
JP2011106004A (en) * 2009-11-19 2011-06-02 Suirei:Kk Waste water treatment apparatus reusing two treated water, ro permeated water or treated pure water generated in three systems formed by dividing plating treatment into three systems

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4879133A (en) * 1972-01-25 1973-10-24
JPS50153455A (en) * 1974-05-30 1975-12-10
JPH03202189A (en) * 1989-12-28 1991-09-03 Mitsubishi Electric Corp Apparatus for highly efficient treatment of waste water
JPH10277564A (en) * 1997-04-04 1998-10-20 Tetsugen:Kk Method for treating waste liquid

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4879133A (en) * 1972-01-25 1973-10-24
JPS50153455A (en) * 1974-05-30 1975-12-10
JPH03202189A (en) * 1989-12-28 1991-09-03 Mitsubishi Electric Corp Apparatus for highly efficient treatment of waste water
JPH10277564A (en) * 1997-04-04 1998-10-20 Tetsugen:Kk Method for treating waste liquid

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010274244A (en) * 2009-06-01 2010-12-09 Nippon Steel Corp Method for clarifying treatment of steel production waste water
JP2011106004A (en) * 2009-11-19 2011-06-02 Suirei:Kk Waste water treatment apparatus reusing two treated water, ro permeated water or treated pure water generated in three systems formed by dividing plating treatment into three systems

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