JPH05154488A - Treatment of processing waste liquid of nonsilver salt photosensitive material - Google Patents
Treatment of processing waste liquid of nonsilver salt photosensitive materialInfo
- Publication number
- JPH05154488A JPH05154488A JP32476591A JP32476591A JPH05154488A JP H05154488 A JPH05154488 A JP H05154488A JP 32476591 A JP32476591 A JP 32476591A JP 32476591 A JP32476591 A JP 32476591A JP H05154488 A JPH05154488 A JP H05154488A
- Authority
- JP
- Japan
- Prior art keywords
- waste liquid
- liquid
- added
- processing waste
- acid
- 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.)
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Links
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- Treatment Of Water By Oxidation Or Reduction (AREA)
- Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
- Photosensitive Polymer And Photoresist Processing (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、非銀塩物質を感光性物
質とする感光材料の現像処理で生じる廃液を処理して固
形分と液体とに分離する技術に関し、更に詳しくは、酸
による中和処理で異臭を有したり衛生上有害な物質を生
じる還元剤を含有する廃液の処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a technique for treating a waste liquid generated in the development of a light-sensitive material containing a non-silver salt substance as a light-sensitive substance to separate it into a solid content and a liquid. The present invention relates to a method for treating a waste liquid containing a reducing agent that has an offensive odor or a substance that is harmful to hygiene during neutralization.
【0002】[0002]
【従来の技術】非銀塩感光材料、例えば感光性平版印刷
版の現像処理は、通常、自動現像機を用い、画像露光さ
れた感光性平版印刷版を搬送しながら、その感光層の表
面に現像液を供給し画像様に感光層を溶出させて平版印
刷版とする現像工程、及び該現像工程の後に、必要によ
り、水洗工程、リンス液による処理や不感脂化処理の工
程等を付加する処理が行われている。2. Description of the Related Art Development of a non-silver salt light-sensitive material such as a light-sensitive lithographic printing plate is usually carried out by using an automatic developing machine while the image-wise exposed light-sensitive lithographic printing plate is conveyed to the surface of the light-sensitive layer thereof. A developing step of supplying a developing solution to elute the photosensitive layer imagewise to form a lithographic printing plate, and after the developing step, a washing step, a treatment with a rinsing solution, a desensitizing step, etc. are added if necessary. Processing is taking place.
【0003】このような現像処理で排出される廃液の処
理方法として、廃液を中和剤で中和し、凝集剤を添加し
て溶解成分やコロイド状物質を凝集させ濾過して固形分
と液体とに分離し、更に該液体を加熱して蒸発させ固形
分と液体成分とに分離する処理廃液の処理方法が知られ
ている(特開平3-90239号等)。As a method for treating the waste liquid discharged in such a developing process, the waste liquid is neutralized with a neutralizing agent, and a coagulant is added to agglomerate dissolved components and colloidal substances for filtration to obtain a solid content and a liquid. There is known a method for treating a treatment waste liquid, in which the liquid is separated into a solid content and a liquid component by further evaporating the liquid by heating (Japanese Patent Laid-Open No. 3-90239, etc.).
【0004】[0004]
【発明が解決しようとする問題点】しかしながら、この
ような処理廃液が亜硫酸塩のような還元性物質を含有す
る場合、中和処理で酸を添加すると亜硫酸ガス等の異臭
を有したり衛生上有害な気体が生成し、室内環境が悪化
する問題が認められる。However, when such a treatment waste liquid contains a reducing substance such as a sulfite salt, addition of an acid in the neutralization treatment causes an offensive odor such as sulfurous acid gas or causes a hygienic problem. There is a problem that harmful gas is generated and the indoor environment deteriorates.
【0005】従って、本発明の目的は、非銀塩感光材料
の処理廃液(疲労液を包含する)の処理方法において、
還元剤を含有する処理廃液の中和処理によって異臭を有
したり衛生上有害な物質が生成するのを防止し、処理廃
液の処理装置周辺の作業環境が改善される処理廃液の処
理方法を提供することである。Therefore, an object of the present invention is to provide a method for treating a processing waste liquid (including a fatigue liquid) of a non-silver salt light-sensitive material,
Providing a processing waste liquid treatment method that prevents the generation of odorous or hygienic substances by neutralizing the processing waste liquid containing a reducing agent, and improves the working environment around the processing waste liquid processing equipment. It is to be.
【0006】[0006]
【問題点を解決するための手段】上記本発明の目的を達
成する本発明の処理方法は、還元性物質を含む非銀塩感
光材料の処理廃液に酸化剤を添加すると同時又は添加し
た後、酸で中和し、濾過により該処理廃液を固形分と液
体とに分離することを特徴とする。The processing method of the present invention which achieves the above-mentioned object of the present invention is, at the same time as or after the addition of an oxidizing agent to a processing waste liquid of a non-silver salt light-sensitive material containing a reducing substance, It is characterized in that it is neutralized with an acid and the treated waste liquid is separated into a solid content and a liquid by filtration.
【0007】以下、本発明について詳述する。The present invention will be described in detail below.
【0008】本発明方法が適用される処理廃液は、酸に
よる中和によって異臭を有したり衛生上有害な気体を生
成する亜硫酸塩(例えば亜硫酸カリウム、亜硫酸ナトリ
ウム等)のような還元性物質を含有する液である。The treatment waste liquid to which the method of the present invention is applied contains a reducing substance such as a sulfite salt (for example, potassium sulfite, sodium sulfite, etc.) which has an offensive odor and produces a gas harmful to hygiene by neutralization with an acid. It is the contained liquid.
【0009】このような還元性物質を含有する処理廃液
に添加する酸化剤としては、例えば、過酸化水素、酸化
銀、酸素酸(亜硝酸、硝酸、過マンガン酸、クロム酸、
塩素酸、次塩素酸等)及びその塩類、空気、酸素、オゾ
ンの他、酸素を放ちやすい化合物等が挙げられる。酸化
剤の添加量は、処理廃液が含有する還元剤の量に対して
化学当量以上であればよく、通常0.1〜10重量%の範囲
である。Examples of the oxidizing agent added to the processing waste liquid containing such a reducing substance include hydrogen peroxide, silver oxide, oxyacids (nitrous acid, nitric acid, permanganic acid, chromic acid,
(Chloric acid, hypochlorous acid, etc.) and salts thereof, air, oxygen, ozone, and compounds that easily release oxygen. The oxidizing agent may be added in a chemical equivalent amount or more with respect to the amount of the reducing agent contained in the treatment waste liquid, and is usually in the range of 0.1 to 10% by weight.
【0010】酸化剤の処理廃液への添加時期は、中和の
ための酸の添加と同時ないしそれより前である。酸化剤
の処理廃液への添加位置は、自動現像機の循環再使用す
る水洗水を入れた水洗槽若しくは該水洗槽中の水洗水を
水洗用シャワーノズルへ送る配管、又は処理廃液の処理
装置の凝集槽が好ましく、より好ましくは凝集槽であ
る。上記配管中の水洗水へ酸化剤を添加するには、該配
管と酸化剤を入れるタンクとを結ぶ管路にポンプの外に
逆止弁を設けて酸化剤を入れるタンクへの水洗水の逆流
を防止する。The oxidizing agent is added to the treatment waste liquid at the same time as or before the addition of the acid for neutralization. The position of addition of the oxidant to the processing waste liquid is determined by the rinsing tank containing the rinsing water to be recycled and reused in the automatic developing machine or the pipe for sending the rinsing water in the rinsing tank to the shower nozzle for rinsing, or the processing waste liquid treatment device. A coagulation tank is preferable, and a coagulation tank is more preferable. In order to add an oxidizer to the washing water in the pipe, a check valve is provided outside the pump in the pipe line connecting the pipe and the tank for storing the oxidizer, and the reverse flow of the washing water to the tank for storing the oxidizer is performed. Prevent.
【0011】本発明において、処理廃液の中和剤として
用いる酸は、硫酸、塩酸等の液状のものが好ましい。中
和後の処理廃液のpHは、6以下が好ましく、より好まし
くは2〜5の範囲である。pHの検知にはガラス電極を使
用することが好ましい。In the present invention, the acid used as a neutralizing agent for the treatment waste liquid is preferably a liquid acid such as sulfuric acid or hydrochloric acid. The pH of the treated waste liquid after neutralization is preferably 6 or less, more preferably 2 to 5. It is preferable to use a glass electrode for pH detection.
【0012】本発明において、処理廃液に濾過助剤を添
加することができる。濾過助剤としては、ケイソウ土、
セルロース系助剤、その他の鉱物系助剤(例えば、パー
ライト)等が好ましい。市販の濾過助剤としては、ケイ
ソウ土濾過助剤として、ラジオライト#100,#70
0,#800(昭和化学工業(株))、セルロース系濾
過助剤として、フィイブウセルSW−10,BH−40
(日本珪藻土(株))、ケイソウ土以外の他の鉱物系濾
過助剤として、セライトハイフロスーパーセル(日本珪
藻土(株))、トプコパーライト#36,#37
(同)、炭素(活性炭)、石綿等を使用することができ
る。濾過助剤は2種類以上を併用することができ、好ま
しい組み合わせはセルロース系濾過助剤と活性炭との併
用である。濾過助剤の添加量は、処理対象液に対して0.
1〜3重量%の範囲が好ましく、より好ましくは処理対
象液の残査量同等か残査量の1/2の量である。濾過助
剤の添加時期は、中和剤の添加と同時か中和剤の添加よ
り前であることが好ましい。In the present invention, a filter aid may be added to the processing waste liquid. As a filter aid, diatomaceous earth,
Cellulose-based auxiliaries and other mineral-based auxiliaries (for example, pearlite) and the like are preferable. Commercially available filter aids include Radiolite # 100 and # 70 as diatomaceous earth filter aids.
No. 0, # 800 (Showa Chemical Industry Co., Ltd.), as a cellulose-based filter aid, Fiibousel SW-10, BH-40
(Nippon diatomaceous earth Co., Ltd.), as a mineral-based filter aid other than diatomaceous earth, Celite Hyflo Supercell (Nippon diatomaceous earth Co., Ltd.), Topcoperlite # 36, # 37
(The same), carbon (activated carbon), asbestos, etc. can be used. Two or more kinds of filter aids can be used in combination, and a preferred combination is a combination of a cellulosic filter aid and activated carbon. The amount of filter aid added is 0.
The amount is preferably in the range of 1 to 3% by weight, and more preferably equal to or half the residual amount of the liquid to be treated. The filter aid is preferably added at the same time as the addition of the neutralizing agent or before the addition of the neutralizing agent.
【0013】本発明において、処理廃液に凝集剤を添加
することができる。好ましい態様として、第1の凝集剤
を添加した後、酸を添加して中和し、第2の凝集剤を添
加する態様が挙げられる。第1の凝集剤としては無機凝
集剤が好ましく、無機凝集剤としては、例えば次のよう
な化合物が挙げられる。In the present invention, a coagulant may be added to the processing waste liquid. As a preferred embodiment, there is an embodiment in which after adding the first coagulant, an acid is added to neutralize and the second coagulant is added. The first aggregating agent is preferably an inorganic aggregating agent, and examples of the inorganic aggregating agent include the following compounds.
【0014】低分子系として、硫酸アルミニウム、塩化
アルミニウム、硫酸鉄(II)、硫酸鉄(III)、塩化鉄
(III)、塩化鉄−硫酸鉄混合物、塩化亜鉛、硫酸亜
鉛、酸化マグネシウム、炭酸マグネシウム等;高分子系
として、ポリ塩化アルミニウム([Al2(OH)nCl6-n]m)、
ポリ硫酸アルミニウム([Al2(OH)n(SO4)3-n/2]m)、ポ
リ塩化鉄(III)([Fe2(OH)nCl6-n]m)、ポリ硫酸鉄(I
II) ([Fe(OH)n(SO4)3-n/2]m等;金属電解生成物として、
電解水酸化アルミニウム(Al(OH)3)、電解水酸化鉄(F
e(OH)3)等。第1の凝集剤の添加量は通常、0.1〜10重
量%が適当である。As a low molecular weight system, aluminum sulfate, aluminum chloride, iron (II) sulfate, iron (III) sulfate, iron (III) chloride, iron chloride-iron sulfate mixture, zinc chloride, zinc sulfate, magnesium oxide, magnesium carbonate Etc .; as a polymer system, polyaluminum chloride ([Al 2 (OH) n Cl 6-n ] m ),
Polyaluminum sulphate ([Al 2 (OH) n (SO 4 ) 3-n / 2 ] m ), polyiron chloride (III) ([Fe 2 (OH) n Cl 6-n ] m ), polyiron sulphate ( I
II) ([Fe (OH) n (SO 4 ) 3-n / 2 ] m etc .; as a metal electrolysis product,
Electrolytic aluminum hydroxide (Al (OH) 3 ), electrolytic iron hydroxide (F
e (OH) 3 ) etc. The appropriate amount of the first coagulant added is usually 0.1 to 10% by weight.
【0015】第2の凝集剤としては、有機凝集剤、特に
カチオン性高分子凝集剤が好ましい。カチオン性高分子
凝集剤として、ポリエチレンイミン(PEI)、>NOCR
(Rは、炭素数3〜21の直鎖アルキル基又は直鎖アリル
基を表す。)で示されるアシル化された水溶性ポリエチ
レンイミン系化合物、かにの甲殻から採取したキサント
ン等が挙げられる。>NOCRで示される部分アシル化水溶
性ポリエチレンイミンとして、通常平均分子量800〜657
00のポリエチレンイミンをアシル化し、アシル基を5〜
15%結合したものが用いられる。>NOCRで示される部分
アシル化水溶性ポリエチレンイミンの代表的なものとし
ては直鎖アルキル基を有するものが挙げられる。例え
ば、ROC−がCH3(CH2)2CO−、CH3(CH2)6CO−、CH3(CH2)
10CO−、CH3(CH2)16CO−、CH3(CH2)7CH=CH(CH2)7CO−
等で表される化合物である。表1〜表3に有機凝集剤の
具体例を示すが、その他にグアーガムも用いることがで
きる。表1〜表3の構造式中、R及びR′は各々アルキ
ル基を表し、X-はアニオンを表す。第2の凝集剤の添
加量は通常0.25重量%水溶液の場合0.1〜5重量%が適
当である。The second coagulant is preferably an organic coagulant, particularly a cationic polymer coagulant. As a cationic polymer flocculant, polyethyleneimine (PEI),> NOCR
(R represents a linear alkyl group or a linear allyl group having 3 to 21 carbon atoms), which is an acylated water-soluble polyethyleneimine compound, xanthone collected from crab shells, and the like. > NOCR as partially acylated water-soluble polyethyleneimine, usually with an average molecular weight of 800-657
Polyethylenimine of 00 is acylated and the acyl group becomes 5
15% bound is used. Typical examples of the partially acylated water-soluble polyethyleneimine represented by> NOCR include those having a linear alkyl group. For example, ROC-is CH 3 (CH 2) 2 CO- , CH 3 (CH 2) 6 CO-, CH 3 (CH 2)
10 CO−, CH 3 (CH 2 ) 16 CO−, CH 3 (CH 2 ) 7 CH = CH (CH 2 ) 7 CO−
And the like. Tables 1 to 3 show specific examples of the organic flocculant, but guar gum can also be used. Tables 1 3 in the structural formula, R and R 'each represent a alkyl group, X - represents an anion. The amount of the second coagulant added is usually 0.1 to 5% by weight in the case of a 0.25% by weight aqueous solution.
【0016】[0016]
【表1】 [Table 1]
【0017】[0017]
【表2】 [Table 2]
【0018】[0018]
【表3】 [Table 3]
【0019】本発明の処理方法において、酸で中和し、
必要により濾過助剤及び/又は凝集剤を添加して凝集物
を生じた処理廃液は濾過によって固形分と液体とに分離
する。濾過方法としてはは遠心濾過、吸引濾過、ベルト
プレス、フィルタプレス等公知の手段を用いることがで
きるが、遠心濾過が好ましい。濾過方法については特願
昭62-193051号明細書、同63-217403号明細書等の記載を
参照することができる。In the treatment method of the present invention, neutralization with an acid,
If necessary, a filter aid and / or a flocculant is added to form a coagulated product, and the treated waste liquid is separated into a solid content and a liquid by filtration. As a filtration method, known means such as centrifugal filtration, suction filtration, belt press and filter press can be used, but centrifugal filtration is preferred. For the filtration method, the descriptions in Japanese Patent Application Nos. Sho 62-193051 and Sho 63-217403 can be referred to.
【0020】次に、本発明の処理方法を実施する装置に
ついて図面を参照して説明する。Next, an apparatus for carrying out the processing method of the present invention will be described with reference to the drawings.
【0021】図1は本発明の方法を実施する装置の概略
構成を示す図である。1は非銀塩感光材料を処理する自
動現像機で、その内部構造は図示を省略してあるが、非
銀塩感光材料を搬送しながら、現像液をその感光層へ供
給しブラシローラで感光層面をこすって画像様に感光層
を除去する溶出現像を施した後、絞りローラで付着物を
除去して水洗部へ送る。水洗部では水洗水タンク内の水
洗水をポンプでシャワーノズルへ圧送し、そこから該感
光材料の表面に噴射させて水洗し、水洗に使用した水は
水洗水タンクに戻して循環再使用するようになってい
る。水洗した感光材料は絞りローラで表面の付着物を除
去して次工程(リンス処理又は不感脂化処理)へ送ら
れ、リンス処理又は不感脂化処理がされるように構成さ
れている。FIG. 1 is a view showing the schematic arrangement of an apparatus for carrying out the method of the present invention. Reference numeral 1 denotes an automatic developing machine for processing a non-silver salt photosensitive material, the internal structure of which is not shown in the drawing, while the non-silver salt photosensitive material is being conveyed, a developing solution is supplied to the photosensitive layer and is exposed by a brush roller. After the layer surface is rubbed to perform elution development for imagewise removal of the photosensitive layer, the squeeze roller is used to remove the deposits and send it to the washing section. In the rinsing section, the rinsing water in the rinsing water tank is pumped to the shower nozzle by a pump, from which it is sprayed onto the surface of the photosensitive material for rinsing, and the water used for rinsing is returned to the rinsing water tank for circulation and reuse It has become. The light-washed photosensitive material is configured to remove adhered substances on the surface with a squeeze roller and then sent to the next step (rinse treatment or desensitization treatment) to be rinsed or desensitized.
【0022】自動現像機1で循環再使用され疲労した水
洗疲労液はポンプ2を作動させて凝集槽3へ送り、図示
しない液面センサと制御機構により、所定の液面高さま
で液が送られるとポンプ2の作動が停止するように構成
されている。凝集槽3では、酸化剤タンク5に入れられ
た酸化剤がポンプ6で送られて添加され、次いで、中和
剤タンク7に入れられた酸がポンプ8で送られて水洗疲
労液へ添加される。The wash-fatigue liquid, which has been circulated and reused in the automatic processor 1 and is exhausted, is sent to the coagulation tank 3 by operating the pump 2, and the liquid is sent to a predetermined liquid level by a liquid level sensor and control mechanism (not shown). And the operation of the pump 2 is stopped. In the flocculation tank 3, the oxidant contained in the oxidant tank 5 is sent by the pump 6 and added, and then the acid contained in the neutralizer tank 7 is sent by the pump 8 to be added to the washing fatigue liquid. It
【0023】酸の添加は、処理廃液のpHが所定の範囲に
調整されるようにポンプ8の作動を図示しない制御機構
で制御するようになっている。10はpH計のガラス電極で
ある。一方、酸の添加と同時に、濾過助剤容器13aに入
れられた濾過助剤(粉体)がロータリフィーダ14aによ
り、もう一つの濾過助剤容器13bに入れられた別種の濾
過助剤(粉体)がロータリフィーダ14bにより凝集槽3
内の水洗疲労液へそれぞれ所定量添加される。17は撹拌
機である。The acid addition is such that the operation of the pump 8 is controlled by a control mechanism (not shown) so that the pH of the treatment waste liquid is adjusted within a predetermined range. 10 is the glass electrode of the pH meter. On the other hand, at the same time as the addition of the acid, the filter aid (powder) contained in the filter aid container 13a is moved by the rotary feeder 14a into another filter aid (powder) contained in the other filter aid container 13b. ) Is the flocculation tank 3 by the rotary feeder 14b.
A predetermined amount is added to each of the water-washed fatigue liquid. 17 is a stirrer.
【0024】このようにして、酸化剤、中和剤及び濾過
助剤が添加され、含有する溶解成分やコロイド状成分が
凝集した水洗疲労液はポンプ19によって遠心濾過器20へ
送られる。遠心濾過器20では回転する内槽21及びその内
部に装着した濾布22によって濾液と残査とに遠心濾過さ
れ、濾液はポンプ24にて自動現像機1へ送られ水洗水と
して再使用される。23は内槽21を回転させるモータであ
る。上記濾布の材質としては、綿、ポリエチレン、布織
布、ポリ塩化ビニル等が、上記内槽の回転数は500〜180
0rpmが好ましい。In this way, the oxidative agent, the neutralizing agent, and the filter aid are added, and the water-washed fatigue liquid in which the contained dissolved components and colloidal components are aggregated is sent to the centrifugal filter 20 by the pump 19. In the centrifugal filter 20, the filtrate and the residue are centrifugally filtered by a rotating inner tank 21 and a filter cloth 22 mounted therein, and the filtrate is sent to the automatic processor 1 by a pump 24 and reused as washing water. . 23 is a motor for rotating the inner tank 21. As the material of the filter cloth, cotton, polyethylene, woven cloth, polyvinyl chloride, etc., the rotation speed of the inner tank is 500 ~ 180
0 rpm is preferred.
【0025】本発明の処理方法が適用される処理廃液
は、亜硫酸塩のように酸と反応して亜硫酸ガスのような
異臭かつ衛生上有害な物質を生ずる還元剤を含有する処
理廃液である。このような処理廃液には、例えば感光性
物質としてジアゾ樹脂、o-キンノンジアジド化合物、フ
ォトポリマー等を用いたネガ型やポジ型の感光性平版印
刷版及びその現像液の廃液や現像処理後の水洗工程の水
洗水の廃液、例えば特開昭63-205658号公報に記載され
たような感光材料とその現像液がある。The treatment waste liquid to which the treatment method of the present invention is applied is a treatment waste liquid containing a reducing agent such as sulfite which reacts with an acid to produce an offensive odor and a sanitary harmful substance such as sulfurous acid gas. Such a processing waste liquid includes, for example, a negative or positive photosensitive lithographic printing plate using a diazo resin, an o-quinone diazide compound, a photopolymer or the like as a photosensitive substance, and a waste liquid of the developing solution or washing after development. There is a waste liquid of washing water in the process, for example, a light-sensitive material and a developer thereof as described in JP-A-63-205658.
【0026】[0026]
【実施例】以下、本発明を実施例でより具体的に説明す
る。EXAMPLES The present invention will be described in more detail below with reference to examples.
【0027】実施例 非銀塩感光材料としてポジ型感光性平版印刷版SMP−
N(コニカ(株)製)の1003mm×800mmサイズを自動現
像機で処理した。この自動現像機による処理は、現像液
SD−32(コニカ(株)製)で現像し、次いで水洗を
行った。水洗は、水洗水タンクに水を18l入れ、この水
をシャワーノズルから版面に供給して水洗を行い、水洗
に使用した水は上記水洗水タンクに戻し循環再使用し
た。循環再使用された水洗水(水洗疲労液)が含有する
還元剤はK2SO3であった。前記条件で、上記感光性平版印
刷版の処理を8時間行い、2時間おきに水洗タンク内の
水洗疲労液を5lずつ図1に示す装置の凝集槽3(液容
量は5l)へ送った。この送液が完了すると撹拌機17を
回転させ、酸化剤として過酸化水素(H2O2)を5重量%
添加した後、中和剤としてH2SO4の9%水溶液をpH3に
なるまで添加し、同時に濾過助剤容器13aからセルロー
ス系濾剤(日本珪藻土(株))を0.1重量%、濾過助剤
容器13bから活性炭を0.1重量%(いずれも凝集槽内液
量に対して)添加し、添加終了の後10分間撹拌した。次
いで、上記処理を施した水洗疲労液を撹拌しながら遠心
濾過器20へ送り、1400rpmで回転させて残査と濾液とに
分離し、濾液(再生水洗水)を自動現像機の水洗水タン
クへ戻して再使用した。濾布22には綿布を使用したこの
ような処理を行ったところ、水洗疲労液の処理において
異臭(SO2臭)の発生がなく、また、自動現像機の水洗
水タンク及び水洗水が循環する配管内に水垢の発生が見
られなかった。Example Positive photosensitive lithographic printing plate SMP-as a non-silver salt photosensitive material
N (manufactured by Konica Corporation) 1003 mm × 800 mm size was processed by an automatic processor. In the processing by this automatic developing machine, development was carried out with a developing solution SD-32 (manufactured by Konica Corporation), followed by washing with water. For washing, 18 l of water was put in a washing water tank, this water was supplied to the plate surface from a shower nozzle to wash the water, and the water used for washing was returned to the above washing water tank and reused by circulation. The reducing agent contained in the rinsing water (rinsing fatigue solution) that was circulated and reused was K 2 SO 3 . Under the above conditions, the photosensitive lithographic printing plate was treated for 8 hours, and every 2 hours, 5 liters of the rinsing fatigue solution in the rinsing tank was sent to the flocculating tank 3 (the liquid volume was 5 liters) of the apparatus shown in FIG. When this liquid transfer is completed, the stirrer 17 is rotated to add 5% by weight of hydrogen peroxide (H 2 O 2 ) as an oxidant.
After the addition, a 9% aqueous solution of H 2 SO 4 was added as a neutralizing agent until the pH reached 3, and at the same time, 0.1% by weight of a cellulosic filter (Nippon Diatomaceous Co., Ltd.) was added from the filter aid container 13a and a filter aid. 0.1% by weight of activated carbon (both with respect to the amount of liquid in the coagulation tank) was added from the container 13b, and the mixture was stirred for 10 minutes after the addition was completed. Then, the washed fatigue liquid treated above is sent to the centrifugal filter 20 while being stirred, rotated at 1400 rpm to separate the residue and the filtrate, and the filtrate (regenerated washing water) is transferred to the washing water tank of the automatic processor. It was returned and reused. When the filter cloth 22 is subjected to such a treatment using a cotton cloth, no strange odor (SO 2 odor) is generated in the treatment of the washing fatigue liquid, and the washing water tank and the washing water of the automatic processor are circulated. No generation of scale was found in the pipe.
【0028】比較例 酸化剤の添加を行わない外は上記実施例と同様の実験を
おこなったところ、水洗疲労液の処理中に異臭(SO
2臭)の発生が見られる問題が生じた。Comparative Example The same experiment as in the above example was carried out except that no oxidizing agent was added. As a result, an offensive odor (SO
(2 odor) occurred.
【0029】[0029]
【発明の効果】本発明によれば、非銀塩感光材料の処理
廃液の処理において、亜硫酸塩のような還元性物質を含
む処理廃液を酸で中和する際に、異臭を有したり衛生上
有害な物質が生成することが防止され、それにより処理
廃液の処理装置周辺の環境が改善される。According to the present invention, when a processing waste solution of a non-silver salt light-sensitive material is treated with an acid, the processing waste solution containing a reducing substance such as a sulfite salt has an offensive odor and is hygienic. The generation of harmful substances is prevented, thereby improving the environment of the processing waste liquid around the processing equipment.
【図1】本発明の方法を実施する装置の概略構成図であ
る。FIG. 1 is a schematic configuration diagram of an apparatus for carrying out the method of the present invention.
1 自動現像機 3 凝集槽 5 酸化剤タンク 7 中和剤タンク 13a,13b 濾過助剤容器 20 遠心濾過器 1 Automatic processor 3 Coagulation tank 5 Oxidizer tank 7 Neutralizer tank 13a, 13b Filter aid container 20 Centrifugal filter
───────────────────────────────────────────────────── フロントページの続き (72)発明者 志村 和弘 東京都日野市さくら町1番地コニカ株式会 社内 (72)発明者 渡辺 真也 東京都日野市さくら町1番地コニカ株式会 社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Kazuhiro Shimura 1 Konica Stock Company, Sakura Town, Hino City, Tokyo In-house (72) Shinya Watanabe 1 Konica Stock Company, Sakura Town, Hino City, Tokyo In-house
Claims (1)
廃液に酸化剤を添加すると同時又は添加した後、酸で中
和し、濾過により該処理廃液を固形分と液体とに分離す
ることを特徴とする非銀塩感光材料の処理廃液の処理方
法。1. A processing waste liquid of a non-silver salt light-sensitive material containing a reducing substance is added at the same time as or after the addition of an oxidizing agent, and then neutralized with an acid, and the processing waste liquid is separated into a solid content and a liquid by filtration. A method for treating a processing waste liquid of a non-silver salt light-sensitive material, comprising:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32476591A JPH05154488A (en) | 1991-12-09 | 1991-12-09 | Treatment of processing waste liquid of nonsilver salt photosensitive material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP32476591A JPH05154488A (en) | 1991-12-09 | 1991-12-09 | Treatment of processing waste liquid of nonsilver salt photosensitive material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH05154488A true JPH05154488A (en) | 1993-06-22 |
Family
ID=18169428
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP32476591A Pending JPH05154488A (en) | 1991-12-09 | 1991-12-09 | Treatment of processing waste liquid of nonsilver salt photosensitive material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH05154488A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002512123A (en) * | 1998-04-20 | 2002-04-23 | カルゴン コーポレイション | Inorganic composition, production method and method of use |
JP2012173660A (en) * | 2011-02-24 | 2012-09-10 | Mitsubishi Paper Mills Ltd | Thinning treatment method of dry film resist |
JP2012189750A (en) * | 2011-03-10 | 2012-10-04 | Mitsubishi Paper Mills Ltd | Process method for thinning dry film resist |
-
1991
- 1991-12-09 JP JP32476591A patent/JPH05154488A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002512123A (en) * | 1998-04-20 | 2002-04-23 | カルゴン コーポレイション | Inorganic composition, production method and method of use |
JP2012173660A (en) * | 2011-02-24 | 2012-09-10 | Mitsubishi Paper Mills Ltd | Thinning treatment method of dry film resist |
JP2012189750A (en) * | 2011-03-10 | 2012-10-04 | Mitsubishi Paper Mills Ltd | Process method for thinning dry film resist |
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