JPS6031884A - Recovery of contained substance from washing water - Google Patents

Recovery of contained substance from washing water

Info

Publication number
JPS6031884A
JPS6031884A JP58141657A JP14165783A JPS6031884A JP S6031884 A JPS6031884 A JP S6031884A JP 58141657 A JP58141657 A JP 58141657A JP 14165783 A JP14165783 A JP 14165783A JP S6031884 A JPS6031884 A JP S6031884A
Authority
JP
Japan
Prior art keywords
washing water
concentrate
water
reverse osmosis
osmosis membrane
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
JP58141657A
Other languages
Japanese (ja)
Inventor
Hajime Nakato
肇 中藤
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP58141657A priority Critical patent/JPS6031884A/en
Publication of JPS6031884A publication Critical patent/JPS6031884A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

PURPOSE:To efficiently recover the low concn. substance in washing water, by treating washing water by a medium pressure reverse osmosis membrane apparatus while treating the concentrate therefrom with a high pressure reverse osmosis membrane apparatus and applying electrolytic treatment to the concentrate to recover the contained substance. CONSTITUTION:Washing water A used in photographic treatment passes a pretreating part while the treated water is sent to a medium pressure reverse osmosis membrane apparatus 1 where receives primary separation treatment to be separated into permeated water B and a concentrate A1. The permeated water B is re-utilized as washing water or discharged while the concentrate A1 is supplied to a high pressure reverse osmosis membrane apparatus 2 where subjected to secondary separation treatment to be separated into permeated water B1 and a concentrate A2. The permeated water B1 is re-utilized as washing water or discharged while the concentrate A2 is subsequently treated with an electrolytic apparatus to recover silver. In this case, 10g/l of high purity silver is recovered from the concentrate A2. Waste water B2 from the electrolytic apparatus 3 after silver recovery is discharged after subjected to ozone treatment.

Description

【発明の詳細な説明】 この発明は、水洗水に含まれている低濃度の含有物質を
回収する方法、例えば写真処理水洗水に含まれている銀
を回収するのに適した回収方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for recovering low-concentration substances contained in washing water, for example, a recovery method suitable for recovering silver contained in photographic processing washing water. It is.

写真の処理工程において銀が使用されるため、写真処理
水洗水に銀が低濃度で含まれており、これをそのまま廃
棄することは、資源の無駄となって写真処理コストを高
騰させると共に公害問題を引き起すことになる。
Because silver is used in the photo processing process, the photo processing washing water contains a low concentration of silver, and disposing of this as is would be a waste of resources, raising photo processing costs and causing pollution problems. This will cause

写真処理水洗水の場合、低濃度で含まれる銀を回収する
には、イオン交換法や鉄ウール置換法等を用いることが
考えられているが、コスト的に、また二次公害発生等の
理由により実用化されていないのが現状であり、低濃度
で含まれる銀の効率よい回収方法の提案がまたれている
のが現状である。
In the case of photographic processing washing water, it has been considered to use ion exchange methods or iron wool replacement methods to recover silver contained in low concentrations, but these methods are expensive and cause secondary pollution. Currently, this method has not been put into practical use, and there are currently several proposals for efficient recovery methods for silver contained in low concentrations.

この発明は、上記のような点にかんがみてなされたもの
であり、水洗水に含まれている低濃度の物質を低コスト
で効率よく、しかも公害を発生させることなく回収でき
る回収方法を提供するのが目的である。
This invention has been made in view of the above points, and provides a recovery method that can efficiently recover low-concentration substances contained in washing water at low cost and without causing pollution. The purpose is to

この発明の構成は、中圧タイプと高圧タイプの逆浸透膜
装置で水洗水を順次濃縮成理して含有物質の濃度を高め
、この濃縮処理水から電解装置で濃度の高い物質を回収
するようにしたものである。
The structure of this invention is to sequentially concentrate washing water using medium-pressure type and high-pressure type reverse osmosis membrane devices to increase the concentration of contained substances, and to recover high-concentration substances from this concentrated treated water using an electrolytic device. This is what I did.

以下、この発明を添付図面の実施例に基づいて説明する
Hereinafter, the present invention will be explained based on embodiments shown in the accompanying drawings.

図面はこの発明に係る回収方法の処理工程を示しており
、写真処理水洗水Aは、前処理部分を通過した後、中圧
タイプの逆浸透膜装置1に送られ、透過水Bと濃縮液A
Iに一次分離処理される。
The drawing shows the processing steps of the recovery method according to the present invention, in which photographic processing washing water A passes through a pre-treatment section and is then sent to a medium-pressure type reverse osmosis membrane device 1, where it is separated into permeated water B and concentrated liquid. A
I undergo primary separation processing.

前処理部は、例えば夾雑物を除去するフィルター等で構
成され、逆浸透膜装置1に対して目詰まりを生じさせず
、分離処理に全く支障を与えないようにしている。
The pretreatment section is composed of, for example, a filter for removing impurities, and is designed not to clog the reverse osmosis membrane device 1 and to not interfere with the separation process at all.

逆浸透膜装置1は、セルローズアセテートを主体とする
ものやポリアミド型高分子化合物等任意のタイプのもの
が使用できる。
The reverse osmosis membrane device 1 can be of any type, such as one mainly made of cellulose acetate or a polyamide type polymer compound.

透過水Bは水洗水として再利用するかまたは排水とし、
濃縮液A+は高圧タイプの逆浸透膜装置2に供給され、
透過水B1と濃縮液A2に二次分離処理される。
Permeated water B is reused as washing water or drained,
The concentrated liquid A+ is supplied to a high-pressure type reverse osmosis membrane device 2,
It is subjected to secondary separation treatment into permeated water B1 and concentrated liquid A2.

この高圧タイプの逆浸透膜装置2は前記中圧用タイプと
同様の構造であるが、処理圧力が高く濃度の高い透過水
でも分離処理ができるようになっており、例えば銀含有
量が5PPMの水洗水Aは、中圧タイプの逆浸透膜装置
1を通過する間に59PPMの濃縮液A1になり、更に
高圧タイプの逆浸透膜装置2により、10,000 P
PMの濃縮液A2に濃度が高められている。
This high-pressure type reverse osmosis membrane device 2 has the same structure as the above-mentioned medium-pressure type, but it has a high processing pressure and can perform separation treatment even with highly concentrated permeate water. Water A becomes a concentrated liquid A1 of 59 PPM while passing through a medium pressure type reverse osmosis membrane device 1, and further becomes a 59 PPM concentrated liquid A1 by a high pressure type reverse osmosis membrane device 2.
The concentration of PM is increased in concentrated solution A2.

透過水Blは水洗水として再利用するか排水し、濃縮液
A2は次に電解装置3で処理して銀を回収することによ
り、純度の高い銀を濃縮液A2に対して10 f/、 
の量を回収できる。
The permeated water Bl is reused as washing water or drained, and the concentrated liquid A2 is then treated with the electrolyzer 3 to recover silver, so that highly pure silver is produced at a ratio of 10 f/, to the concentrated liquid A2.
can be recovered.

銀回収後の電解装置3からの排水B2はオゾン処理等を
施せば公害の発生がなくそのまま排出することができる
If the waste water B2 from the electrolyzer 3 after silver recovery is subjected to ozone treatment, etc., it can be discharged as it is without causing any pollution.

なお、実施例は、写真処理水洗水の処理について説明し
たが、処理対欧洗浄水はこのようなものに限定されるも
のではなく、金属等を含有する排水の処理に広く利用で
きる。
Although the embodiments have described the treatment of photographic processing washing water, the processing and washing water is not limited to this, and can be widely used for the treatment of wastewater containing metals and the like.

以上のように、この発明によると、水洗水を中圧タイプ
と高圧タイプの逆浸透膜装置で順番に処理し、濃縮液を
電解処理するようにしたので、両逆浸透膜装置によって
水洗水を高濃度に処理して含有物の濃度を高めることが
でき、水洗水に低濃度で含まれている金属等の含有物質
を効率よく回収することができ、透過水は水洗水として
再使用できる。
As described above, according to the present invention, the washing water is sequentially treated with the medium-pressure type and high-pressure type reverse osmosis membrane devices, and the concentrated solution is electrolytically treated, so that the washing water is treated with both reverse osmosis membrane devices. It is possible to increase the concentration of contained substances by processing to a high concentration, and it is possible to efficiently recover contained substances such as metals contained in low concentrations in washing water, and the permeated water can be reused as washing water.

また、写真処理水洗水の処理を行なえば高価な銀の回収
が純度の高い状態で行なえ、写真処理材料のコストダウ
ンが可能になる。
Furthermore, by treating the photographic processing water, expensive silver can be recovered in a highly pure state, making it possible to reduce the cost of photographic processing materials.

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

図面はこの発明に係る処理方法の工程図である。 1は中圧タイプの逆浸透膜装置、2は高圧タイプの逆浸
透膜装置、3は電解装置、Aは水洗水、A+ 、A2は
濃縮液、B、11は透過水。 特許出願人 中 藤 筆 同 代理人 鎌 1) 文 二
The drawings are process diagrams of the treatment method according to the present invention. 1 is a medium pressure type reverse osmosis membrane device, 2 is a high pressure type reverse osmosis membrane device, 3 is an electrolysis device, A is washing water, A+, A2 is concentrated liquid, B, 11 is permeated water. Patent applicant: Fumi Nakafuji Agent: Kama 1) Bun 2

Claims (1)

【特許請求の範囲】[Claims] 水洗水を先ず中圧タイプの逆浸透膜装置で処理し、次に
その濃縮液を高圧タイプの逆浸透膜装置で処理し、その
濃縮液を電解処理して含有物質を回収することを特徴と
する水洗水からの含有物質回収方法。
The washing water is first treated with a medium-pressure reverse osmosis membrane device, then the concentrated liquid is treated with a high-pressure reverse osmosis membrane device, and the concentrated liquid is electrolytically treated to recover the contained substances. A method for recovering contained substances from washing water.
JP58141657A 1983-08-01 1983-08-01 Recovery of contained substance from washing water Pending JPS6031884A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58141657A JPS6031884A (en) 1983-08-01 1983-08-01 Recovery of contained substance from washing water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58141657A JPS6031884A (en) 1983-08-01 1983-08-01 Recovery of contained substance from washing water

Publications (1)

Publication Number Publication Date
JPS6031884A true JPS6031884A (en) 1985-02-18

Family

ID=15297137

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58141657A Pending JPS6031884A (en) 1983-08-01 1983-08-01 Recovery of contained substance from washing water

Country Status (1)

Country Link
JP (1) JPS6031884A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4880511A (en) * 1986-05-16 1989-11-14 Electroplating Engineers Of Japan, Limited Process and apparatus for recovery of precious metal compound
JPH07224312A (en) * 1994-02-11 1995-08-22 Leybold Durferrit Gmbh Method and equipment for melting and processing metal and metal alloy
US5552055A (en) * 1994-09-15 1996-09-03 London Drugs Limited Photofinishing effluent purifying process and apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4880511A (en) * 1986-05-16 1989-11-14 Electroplating Engineers Of Japan, Limited Process and apparatus for recovery of precious metal compound
JPH07224312A (en) * 1994-02-11 1995-08-22 Leybold Durferrit Gmbh Method and equipment for melting and processing metal and metal alloy
US5552055A (en) * 1994-09-15 1996-09-03 London Drugs Limited Photofinishing effluent purifying process and apparatus

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