JPH0749574A - Processing method of waste liquid from planographic printing plate treatment - Google Patents

Processing method of waste liquid from planographic printing plate treatment

Info

Publication number
JPH0749574A
JPH0749574A JP19372593A JP19372593A JPH0749574A JP H0749574 A JPH0749574 A JP H0749574A JP 19372593 A JP19372593 A JP 19372593A JP 19372593 A JP19372593 A JP 19372593A JP H0749574 A JPH0749574 A JP H0749574A
Authority
JP
Japan
Prior art keywords
liquid
plate
waste liquid
printing plate
processing
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
JP19372593A
Other languages
Japanese (ja)
Inventor
Yasuhiro Aizawa
泰洋 相澤
Yuji Takagami
裕二 高上
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.)
Mitsubishi Paper Mills Ltd
Original Assignee
Mitsubishi Paper Mills Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Paper Mills Ltd filed Critical Mitsubishi Paper Mills Ltd
Priority to JP19372593A priority Critical patent/JPH0749574A/en
Publication of JPH0749574A publication Critical patent/JPH0749574A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To provide a processing method for waste liquid as a byproduct of planographic printing process by which waste liquid can be easily processed and the burden concerning to processing of waste liquid is decreased without using such a method that an acid material is newly added to waste liquid to decrease pH of the liquid when the liquid is to be discharged. CONSTITUTION:After an alkali treating liquid is supplied to the image forming surface of a planographic printing plate to dissolve a nonpicture part, the alkali treating liquid on the plate and the dissolved nonpicture part are removed and discharged. In the processing method of the waste liquid in the planographic printing process, a gas containing at least carbon dioxide is blown into the waste liquid comprising the alkali treating liquid and the nonpicture part.

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、平版印刷版の画像形成
面にアルカリ性処理液を供給して非画像部を溶解した
後、非画像部成分を印刷版上より除去して印刷版を作製
する際に副製する処理疲労アルカリ性処理液と非画像部
成分とからなる処理廃液の処理方法に関し、高アルカリ
性の処理廃液の廃棄時に改めて液pHを低下させること
なく簡便かつ安全に処理廃液が処理出来、処理廃液処理
負担を大幅に軽減させる平版印刷版処理廃液処理方法に
関する。
FIELD OF THE INVENTION The present invention provides a printing plate by supplying an alkaline processing liquid to the image forming surface of a lithographic printing plate to dissolve the non-image part and then removing the non-image part components from the printing plate. Regarding processing method of processing waste solution consisting of processing fatigue alkaline processing solution and non-image part component which is by-produced when processing, processing waste solution is processed easily and safely without lowering the pH of the solution again when discarding highly alkaline processing waste solution The present invention relates to a lithographic printing plate processing waste liquid processing method capable of significantly reducing the processing waste liquid processing load.

【0002】[0002]

【従来の技術】非画像部アルカリ溶解除去型平版印刷版
には、親水性支持体上に少なくとも活性線による化学構
造変化を伴う活性線誘起処理液可溶化物質或は活性線硬
化性物質を含有する感光層を設けてなる感光性平版印刷
版(所謂PS版)が知られており、高耐刷性が要求され
る重印刷に広く利用されている。これらは、予め画像記
録された銀塩写真フィルム原版を印刷版画像形成面に密
着させて露光し、これにより最終印刷物に於ける画像部
に対応する硬化部分或は非画像部に対応する処理液可溶
化部分を形成させ、非画像部はアルカリ性処理液によっ
て溶解除去する。
2. Description of the Related Art A non-image area alkali dissolution removing type lithographic printing plate contains an actinic ray-inducing treatment liquid solubilizing substance or an actinic ray curable substance accompanied by a chemical structure change by actinic rays on a hydrophilic support. A photosensitive lithographic printing plate (so-called PS plate) provided with a photosensitive layer is known and is widely used for heavy printing that requires high printing durability. These are exposed to a silver salt photographic film original plate on which an image has been recorded in advance, in close contact with the printing plate image forming surface, whereby a treatment liquid corresponding to a cured portion or a non-image portion corresponding to the image portion in the final printed matter. A solubilized portion is formed, and a non-image portion is dissolved and removed by an alkaline processing liquid.

【0003】また、電子写真技術を利用して画像形成す
る電子写真平版印刷版も知られており、走査露光対応の
印刷版も製造されている。電子写真技術を利用した非画
像部アルカリ除去型平版印刷版は、親水性支持体上に一
般に有機光導電性物質を樹脂中に分散させたインク受理
性の光導電層を設けてなり、電子写真法により光導電層
上にトナー画像を形成した後、トナーをレジストとして
アルカリ剤からなる溶出液で非画像部を溶出処理して印
刷版として使用される。
Further, an electrophotographic lithographic printing plate which forms an image by utilizing an electrophotographic technique is also known, and a printing plate compatible with scanning exposure is also manufactured. The non-image area alkali-removing lithographic printing plate utilizing electrophotographic technology comprises an ink-receptive photoconductive layer in which an organic photoconductive substance is generally dispersed in a resin on a hydrophilic support. After forming a toner image on the photoconductive layer by the method, the toner is used as a resist and the non-image portion is subjected to an elution treatment with an eluate containing an alkaline agent to be used as a printing plate.

【0004】これら非画像部アルカリ溶出型平版印刷版
の製版処理は、一般的に印刷版を自動的に搬送しながら
処理液を供給して処理する自動機を用いて製版される。
その自動機に採用されている処理方式としては、液循環
再利用方式、新液使捨て処理方式、及び処理過程計量残
存液廃棄方式等が知られている。
The plate-making process of these non-image area alkali-eluting type lithographic printing plates is generally carried out by using an automatic machine for automatically supplying the processing liquid while carrying the printing plate.
As a processing method adopted in the automatic machine, a liquid circulation reuse method, a new liquid disposal processing method, a processing step measurement residual liquid disposal method and the like are known.

【0005】液循環再利用方式は、印刷版に過剰量の処
理液を接触させた後、処理済み液を版上から全て除去し
て循環再利用する方式で、処理液は水平搬送しながらス
プレー或はシャワー等から供給する他、印刷版を処理液
槽中に湾曲浸漬(ディップ方式)させる方法等がある。
新液使捨て処理方式は、液供給スリットのギャップやワ
イヤバーのワイヤ径等の調整によって、版面に処理液を
供給する前に必要最低量を前計量して一版毎に新液を供
給し、場合に応じて処理促進手段を処理過程で施した
後、処理済みの疲労処理液は可溶化した非画像部と共に
全て除去廃棄する方式である。処理過程計量残存液廃棄
方式は、版面に一旦過剰量の処理液を供給した後、処理
途中で処理液を一定量に計量して余剰液は循環再使用
し、計量後の版上の処理液は処理完了後に可溶化した非
画像部と共に廃棄する方式である。
The liquid circulation / reuse system is a system in which an excessive amount of the processing liquid is brought into contact with the printing plate, all the processed liquid is removed from the plate, and then the liquid is circulated and reused. Alternatively, in addition to supplying from a shower or the like, there is a method of immersing the printing plate in a treatment liquid tank in a curved manner (dip method).
The new liquid waste disposal method supplies the new liquid for each plate by adjusting the gap of the liquid supply slit and the wire diameter of the wire bar to pre-measure the required minimum amount before supplying the processing liquid to the plate surface. This is a method in which after the treatment promoting means is applied in the treatment process as the case may be, the treated fatigue treatment liquid is removed and discarded together with the solubilized non-image portion. In the process process metering residual liquid disposal method, after supplying an excessive amount of processing liquid to the plate once, the processing liquid is metered to a certain amount during processing and the excess liquid is circulated and reused, and the processing liquid on the plate after weighing is measured. Is a method of discarding together with the solubilized non-image portion after the processing is completed.

【0006】これら処理方式全てに共通した課題は、製
版処理の安定化及び処理廃液発生の抑制・液交換周期の
長期化等の処理液及び装置の保守管理の軽減にある。特
に使用者の立場からは、装置に起因する製版処理の安定
化は大前提であり、処理液及び装置の保守管理の軽減が
処理装置に於ける実使用上の性能を決定付けている。則
ち、製版処理の安定化は端的には処理液活性度の安定化
であり、使捨て方式以外一般的には処理によって消費さ
れた成分を補充する一方、処理中に高濃度化する成分を
除去して処理液成分を一定に維持する手段が採られてお
り、補充液が補充され、高濃度化成分の除去のために処
理液の一部が廃棄されるし、処理液の処理性能が許容限
度外となった場合及び使捨てでは、使用済み処理液全部
が廃棄されるからである。
The problems common to all of these processing methods are stabilization of plate-making processing, suppression of generation of processing waste liquid, reduction of maintenance management of processing liquid and equipment such as prolongation of liquid exchange cycle. Particularly from the user's point of view, stabilization of the plate-making process caused by the apparatus is a major premise, and reduction in maintenance of the processing liquid and the apparatus determines the performance in actual use in the processing apparatus. In other words, stabilization of the plate-making process is basically stabilization of the activity of the processing solution.In general, components other than the throw-away method are replenished with the components consumed by the process, while the components that increase in concentration during the process are removed. A means for removing and maintaining the components of the treatment liquid constant is adopted, the replenisher is replenished, a part of the treatment liquid is discarded to remove the high-concentration component, and the treatment performance of the treatment liquid is improved. This is because all used processing liquids are discarded when they are out of the allowable limit or when they are discarded.

【0007】ところで、液交換や処理液槽の清掃は、通
常定期的に人為的に行なわれる作業工程であるから、処
理装置的にはより簡便かつ短時間に完了する構造や方式
であることが要求される。特に液交換等に付帯する処理
廃液の廃棄は、作業性ばかりでなく処理液交換期間の延
長をも図るために、製版処理により発生する疲労処理液
の少なくとも一部を製版に伴って廃棄して、装置に付帯
する廃液容器に直接貯留する方式が採られている。特に
上記非画像部の溶解除去に用いられるアルカリ性処理液
はかなり高pHであり、これに付随して処理廃液に於て
も相当の液pHとなるから、廃棄物処理法との兼合いで
例えこの処理廃液を廃液処理業者に処理依頼するにせ
よ、必ず液pHを特定範囲内に調整しなければならな
い。
By the way, since the liquid exchange and the cleaning of the processing liquid tank are usually work steps which are manually performed on a regular basis, the processing apparatus may have a structure and system which can be completed more simply and in a shorter time. Required. In particular, when disposing of the processing waste liquid that accompanies liquid exchange, etc., in order to not only improve workability but also extend the processing liquid exchange period, at least a portion of the fatigue processing liquid generated by the plate making process should be discarded along with the plate making. A method of directly storing in a waste liquid container attached to the device is adopted. In particular, the alkaline treatment liquid used for dissolving and removing the non-image area has a considerably high pH, and accompanying this, the treatment waste liquid also has a considerable liquid pH, so that it can be compared with the waste treatment method. Even if a waste liquid processing company is requested to process this waste liquid, the liquid pH must be adjusted within a specific range.

【0008】[0008]

【発明が解決しようとする課題】本発明は、平版印刷版
画像形成面にアルカリ性処理液を供給して非画像部を溶
解した後、印刷版上のアルカリ性処理液と溶解した非画
像部とを除去して廃棄する平版印刷版の製版処理に付帯
して発生する処理廃液の処理方法に関し、製版処理に於
て廃棄する処理廃液の管理が軽減される平版印刷版処理
廃液処理方法を提供することにある。更に詳しくは、高
アルカリ性の処理廃液を廃液する際に、改めて液pHを
低下させることなしに簡単かつ安全に処理廃液が処理出
来、処理廃液の処理負担を大幅に軽減させる平版印刷版
処理廃液処理方法を提供することにある。
DISCLOSURE OF THE INVENTION According to the present invention, an alkaline processing liquid is supplied to the image forming surface of a lithographic printing plate to dissolve the non-image area, and then the alkaline processing liquid on the printing plate and the dissolved non-image area are separated. Provided is a method for treating a processing liquid waste that accompanies plate-making processing of a planographic printing plate to be removed and discarded, and a method for treating a processing liquid waste of a planographic printing plate that reduces management of the processing liquid waste to be discarded in the plate-making processing. It is in. More specifically, when draining a highly alkaline processing waste liquid, it is possible to easily and safely process the processing waste liquid without lowering the liquid pH anew, and to significantly reduce the processing load of the processing waste liquid. To provide a method.

【0009】[0009]

【課題を解決するための手段】上記問題を解決するため
に検討を重ねた結果、平版印刷版画像形成面にアルカリ
性処理液を供給して非画像部を溶解した後、印刷版上の
アルカリ性処理液と溶解した非画像部とを除去して廃棄
する平版印刷版の製版処理に於ける処理廃液処理方法で
あって、廃棄されたアルカリ性処理液と非画像部成分と
からなる処理廃液中に少なくとも二酸化炭素を含有する
気体を吹込むことを特徴とする平版印刷版処理廃液処理
方法により達成された。
As a result of repeated studies to solve the above problems, an alkaline treatment liquid was supplied to the image forming surface of the lithographic printing plate to dissolve the non-image area, and then the alkaline treatment on the printing plate was performed. A treatment waste liquid treatment method in the plate making process of a lithographic printing plate which removes and discards the liquid and the dissolved non-image portion, wherein at least the waste treatment liquid consisting of the discarded alkaline treatment liquid and non-image portion components It was achieved by a lithographic printing plate processing waste liquid processing method characterized by blowing a gas containing carbon dioxide.

【0010】非画像部アルカリ溶解除去型平版印刷版の
非画像部溶解除去に用いられるアルカリ性処理液は一般
的にpH13前後であり、この処理疲労液を含む廃液に
於ても当然相当高pHとなる。廃棄物処理法の改正によ
り、この様な高アルカリ性廃液は、排出するにせよ廃棄
物処理業者に処理依頼するにせよ、必ず液pHを基準値
以下に調整しなければならない。
The alkaline processing liquid used for dissolving and removing the non-image area alkaline dissolution type lithographic printing plate generally has a pH of about 13, and the waste liquid containing this processing fatigue solution naturally has a considerably high pH. Become. Due to the revision of the Waste Treatment Law, it is necessary to adjust the pH of the highly alkaline waste liquid below the standard value regardless of whether it is discharged or a waste disposal company is requested to dispose of it.

【0011】そこで、廃液のpHを低下させるため、廃
液に溶解する無機及び/または有機の酸を添加する方法
を採れば、中和は一般的に急激な発熱を伴うため、廃液
容器がポリエチレン製等であれば、熱変形する可能性が
ある。また、中和作業中にアルカリ廃液または酸が飛散
すれば、衛生面ばかりでなく安全上からも好ましくな
い。特に、アルカリ剤として一般式SiO2/M2Oで表現
される珪酸アルカリ金属塩が含有されていると、急激な
pH低下によって廃液全体が凝集する可能性が高く、液
全体のpHを基準値以下に低下させる前に廃液中の酸注
入部分付近だけが凝集してしまうため、攪拌等の操作を
加えなければならない。
Therefore, if a method of adding an inorganic and / or organic acid that dissolves in the waste liquid is used in order to lower the pH of the waste liquid, neutralization generally involves a rapid heat generation, and therefore the waste liquid container is made of polyethylene. If they are equal, there is a possibility of thermal deformation. Further, if the alkaline waste liquid or the acid is scattered during the neutralization work, it is not preferable not only from the viewpoint of hygiene but also from the viewpoint of safety. In particular, when an alkali metal silicate represented by the general formula SiO 2 / M 2 O is contained as an alkaline agent, there is a high possibility that the entire waste liquid will agglomerate due to a sudden decrease in pH, and the pH of the entire liquid will be the standard value. Before lowering to below, only the vicinity of the acid injection portion in the waste liquid will be aggregated, so it is necessary to add an operation such as stirring.

【0012】その点、廃棄されたアルカリ性処理液と溶
解非画像部成分とからなる処理廃液中に、少なくとも二
酸化炭素を含有する気体を吹込む様にしておけば、二酸
化炭素が水性液、特にアルカリ溶液に溶解し易く、廃液
廃棄時に改めて酸を添加しなくても処理廃液のpHは充
分に基準値以下に達する。また、炭酸塩は弱アルカリ域
に緩衝作用を有するから、アルカリ性処理液成分として
珪酸アルカリ金属塩が含有されていたとしても、凝集を
起こす可能性は明らかに低下する。従って、二酸化炭素
吹込み中の処理廃液の飛散を防止する手段さえ講じてお
けば、廃液廃棄時に何等手を加えることなく処理(依
頼)することが出来る。
In that respect, if a gas containing at least carbon dioxide is blown into the processing waste liquid consisting of the discarded alkaline processing liquid and the dissolved non-image part components, carbon dioxide will be an aqueous liquid, especially an alkali. It is easily dissolved in the solution, and the pH of the treated waste liquid can sufficiently reach the standard value or lower without adding acid again when the waste liquid is discarded. Further, since carbonate has a buffering action in the weak alkaline region, even if the alkali metal silicate is contained as the alkaline treatment liquid component, the possibility of causing aggregation is obviously reduced. Therefore, the treatment (request) can be performed without any action at the time of discarding the waste liquid, if only means for preventing the dispersion of the treatment liquid during the blowing of carbon dioxide is taken.

【0013】以下に、本発明の処理方法に係わる少なく
とも二酸化炭素を含む気体及び処理廃液への供給方法に
ついて説明する。本発明に係わる少なくとも二酸化炭素
を含む気体は、画像形成された平版印刷版にアルカリ性
処理液を供給して非画像部を溶解した後、印刷版上のア
ルカリ性処理液と溶解した非画像部とを除去して廃棄し
た処理廃液中に供給する。廃液中に吹込む気体は、少な
くとも二酸化炭素を含んでいれば良いから、ドライアイ
スや二酸化炭素高圧ボンベ等の二酸化炭素源から高濃度
の二酸化炭素を供給しても良いが、通常の空気中に含ま
れる二酸化炭素濃度に於ても充分に処理廃液のpHを基
準値以下に低下出来るから、二酸化炭素含有気体として
空気を利用しても良い。
A method of supplying a gas containing at least carbon dioxide and a processing waste liquid according to the processing method of the present invention will be described below. The gas containing at least carbon dioxide according to the present invention supplies the alkaline processing liquid to the image-formed lithographic printing plate to dissolve the non-image portion, and then the alkaline processing liquid on the printing plate and the dissolved non-image portion are separated. It is supplied to the processing waste liquid that has been removed and discarded. The gas blown into the waste liquid may contain at least carbon dioxide, so high concentration carbon dioxide may be supplied from a carbon dioxide source such as dry ice or a carbon dioxide high pressure cylinder, but in normal air Air can be used as the carbon dioxide-containing gas because the pH of the treatment waste liquid can be sufficiently lowered below the reference value even with the concentration of carbon dioxide contained.

【0014】本発明の処理方法に係わる少なくとも二酸
化炭素を含む気体の供給は、空気を包含する二酸化炭素
含有気体を処理廃液に吹込むことで行なう。二酸化炭素
源が空気であれば、コンプレッサやエアポンプ等を用い
て吹込む。また、ドライアイスであれば廃液中に直接投
入しても良いが、一度に多量の二酸化炭素気体が発生し
てしまい、その殆どが廃液中に吸収されないため、雰囲
気を低温に保持して徐々に気化させるか、一旦耐圧容器
内で気化させながら漸次廃液中に供給する。何れの二酸
化炭素源に於ても処理廃液のpH低下効率を向上させる
ため、吹込む気体は廃液中でより細かな気泡にして供給
し、単位気体量の液との界面の面積を大きくすることが
肝要である。廃液の粘性により、気泡が細かくなればな
る程液中の上昇速度は緩慢になり、吸収効率は向上す
る。このため、散気用エアーストーンを気体吹込み口先
に利用しても良い。
The supply of the gas containing at least carbon dioxide in the processing method of the present invention is performed by blowing a carbon dioxide-containing gas containing air into the processing waste liquid. If the carbon dioxide source is air, blow it using a compressor, air pump, or the like. Also, if it is dry ice, it may be put directly into the waste liquid, but since a large amount of carbon dioxide gas is generated at one time and most of it is not absorbed in the waste liquid, keep the atmosphere at a low temperature and gradually It is vaporized or gradually vaporized in a pressure vessel and gradually supplied into the waste liquid. In order to improve the pH lowering efficiency of the treatment waste liquid in any carbon dioxide source, the gas to be blown should be supplied as fine bubbles in the waste liquid to increase the area of the interface with the liquid of unit gas amount. Is essential. Due to the viscosity of the waste liquid, the finer the bubbles, the slower the rising speed in the liquid and the higher the absorption efficiency. Therefore, air diffuser stones may be used at the tip of the gas blowing port.

【0015】本発明に係わる気体の供給口は、製版処理
に先立って処理廃液を貯液する容器中に配置しておけば
良いが、廃液処理(依頼)時点で廃棄物処理法の定める
基準pH値を下回っていれば良いから、本発明に係わる
二酸化炭素含有気体の供給は製版開始直後からでなくと
も良く、処理廃液がある程度貯液されてからで充分であ
る。貯液された廃液量が多い程、供給気体の処理廃液と
の接触時間は長くなって、効率的に液pHを低下出来
る。そのため、貯液槽中の廃液量により供給を開始した
り、時間当たりの供給量を変更しても良い。二酸化炭素
はアルカリ性溶液に吸収されて酸として作用するが、二
酸化炭素と作用した処理廃液中の成分がそのことで有害
物質となる可能性は極めて低く、pH低下後の後処理が
他の酸を添加した場合に比して煩雑になることはない。
The gas supply port according to the present invention may be arranged in a container for storing the processing waste liquid prior to the plate-making process, but at the time of the waste liquid processing (request), the standard pH determined by the waste treatment method is set. As long as it is below the value, the supply of the carbon dioxide-containing gas according to the present invention does not have to start immediately after the start of plate making, and it is sufficient after the processing waste liquid has been stored to some extent. The larger the amount of the stored waste liquid, the longer the contact time of the supply gas with the processing waste liquid, and the more efficiently the liquid pH can be lowered. Therefore, the supply may be started or the supply amount per hour may be changed depending on the amount of waste liquid in the liquid storage tank. Carbon dioxide is absorbed by an alkaline solution and acts as an acid, but it is extremely unlikely that the components in the treatment waste liquid that have acted with carbon dioxide will be harmful substances, and post-treatment after pH reduction will reduce other acids. It does not become complicated compared to the case where it is added.

【0016】次に、本発明の処理方法を製版処理工程に
順じて詳細に説明する。本発明の処理方法に於ける製版
処理工程は、少なくともアルカリ性処理液供給工程及び
非画像部除去廃棄工程からなり、更に廃棄された廃液中
に少なくとも二酸化炭素を含む気体を吹込む二酸化炭素
含有気体供給処理手段を付帯する。
Next, the processing method of the present invention will be described in detail in the order of plate-making processing steps. The plate-making processing step in the processing method of the present invention comprises at least an alkaline processing solution supplying step and a non-image part removing and discarding step, and a carbon dioxide-containing gas supply for blowing a gas containing at least carbon dioxide into the discarded waste solution. A processing means is attached.

【0017】アルカリ性処理液供給工程では、平版印刷
版の画像形成面にアルカリ性処理液を過剰に供給する。
アルカリ性処理液供給方式は従来公知の機構、例えばシ
ャワー、スライドホッパ、カーテンコータ、ディップ方
式等が使用出来る。特にシャワーを用いる場合には、管
から吐出した液を別の部材、例えば整流板や版搬送上ロ
ール等を介して一旦整流した後に画像形成面に供給する
方式が好適である。また全ての方式に於て、より処理時
間を短縮し液供給不良を防止するために、流動促進機構
を設けて版上に供給されたアルカリ性処理液の置換を図
ることや、アルカリ性処理液を複数回に亙って供給する
ことが望ましい。
In the alkaline treatment liquid supplying step, the alkaline treatment liquid is excessively supplied to the image forming surface of the lithographic printing plate.
A conventionally known mechanism such as a shower, a slide hopper, a curtain coater, or a dip system can be used as the alkaline processing liquid supply system. Particularly when a shower is used, it is preferable that the liquid discharged from the tube is once rectified through another member, for example, a rectifying plate or a plate conveying roll, and then supplied to the image forming surface. In addition, in all methods, in order to further shorten the processing time and prevent defective liquid supply, a flow promoting mechanism is provided to replace the alkaline processing liquid supplied on the plate, and multiple alkaline processing liquids are used. It is desirable to supply over time.

【0018】アルカリ性処理液の最低供給量は、搬送中
に版端部からアルカリ性処理液が流下する量であること
が肝要である。則ち、一部は非画像部を溶解させ、余剰
分は版上を流動して被アルカリ性処理部に於て既にある
アルカリ性処理液と一部置換しながら版端部より流下す
る。これにより、版端部では液置換が頻繁に起こり、画
像形成層界面近傍のアルカリ性処理液流動速度が上昇す
ることによって、溶解度の版内変動が抑制される。
It is important that the minimum supply amount of the alkaline processing liquid is such that the alkaline processing liquid flows down from the edge of the plate during transportation. That is, a part of the non-image part is dissolved, and the surplus part flows over the plate and flows down from the plate end part while partially replacing the existing alkaline processing liquid in the alkali-treated part. As a result, liquid replacement frequently occurs at the plate edge, and the flow rate of the alkaline processing liquid in the vicinity of the interface of the image forming layer increases, so that intra-plate variation in solubility is suppressed.

【0019】印刷版上に過剰に供給されたアルカリ性処
理液は、非画像部除去廃棄工程に搬送されるが、版上の
アルカリ性処理液はその全てが非画像部の溶解過程で消
費されず、しかも非画像部除去廃棄工程では版上の液状
物を全て除去して廃棄するため、非画像部画像形成層の
溶解が終了し非画像部除去廃棄工程に到る間に、処理液
供給工程を設けて液計量手段によって少なくとも版上に
あるアルカリ性処理液を一定量残して計量除去すること
が好ましい。
The alkaline processing liquid excessively supplied onto the printing plate is conveyed to the non-image area removing and discarding step, but all of the alkaline processing liquid on the plate is not consumed in the dissolution process of the non-image area, Moreover, in the non-image area removal / disposal step, all the liquid material on the plate is removed and discarded.Therefore, during the non-image area removal / disposal step after the dissolution of the non-image area image forming layer, the processing liquid supply step is performed. It is preferable to provide and measure and remove at least a certain amount of the alkaline processing liquid on the plate by the liquid measuring means.

【0020】液計量を実施する場合は、液計量時に溶解
した非画像部の混入を抑制防止しながら、実質的に画像
形成層の溶解に関与しなかったアルカリ性処理液を最大
限印刷版上から除去することが重要である。従って、液
計量後の版上に残すアルカリ性処理液量(液計量残液
量)は、多いと必然的にアルカリ性処理液の消費量が増
加して単位アルカリ性処理液量当たりのアルカリ性処理
効率が低下するし、液計量後非画像部除去廃棄工程に到
る迄に更に溶解が進行して画線細りを招く恐れがあるた
め、アルカリ性処理液計量残液量は少ない方が望まし
い。
When the liquid measurement is carried out, the alkaline processing liquid which is substantially not involved in the dissolution of the image forming layer is prevented from being mixed on the printing plate at the maximum while preventing the mixing of the non-image portion dissolved during the liquid measurement. It is important to remove. Therefore, if the amount of the alkaline treatment liquid left on the plate after the liquid measurement (liquid measurement residual liquid amount) is large, the consumption of the alkaline treatment liquid inevitably increases and the alkaline treatment efficiency per unit amount of the alkaline treatment liquid decreases. However, it is desirable that the residual amount of the alkaline treatment liquid measured be small, because further dissolution may occur after the liquid measurement until the non-image area removal / disposal step, leading to fine image lines.

【0021】しかしながら、アルカリ性処理液計量残液
量が少なすぎると、結果として除去液の粘性が著しく上
昇し、応々にして連続製版では非画像部除去廃棄部(部
材)に除去液が蓄積して除去効果が低減するし、液計量
部で溶解した画像形成層が剥離する可能性が高くなって
好ましくない。まして、液循環方式の様にアルカリ処理
工程で版上の液状物を全て除去すると、疲労アルカリ性
処理液及び画像形成層成分まで混入して好ましくない。
液計量後のアルカリ性処理液計量残液量は、如何なる液
計量手段を用いるかにもよるが、30〜120g/m2
良く、更に好ましくは40〜100g/m2が良い。
However, when the residual amount of the alkaline processing liquid is too small, the viscosity of the removal liquid increases remarkably, and in the continuous plate making, the removal liquid accumulates in the non-image part removal discard part (member). The removal effect is reduced, and the image-forming layer dissolved in the liquid metering section is likely to peel off, which is not preferable. Furthermore, if all of the liquid material on the plate is removed in the alkaline treatment step as in the liquid circulation system, the fatigue alkaline treatment liquid and the components of the image forming layer are also mixed, which is not preferable.
The alkaline processing liquid metering residual liquid amount after the liquid metering, depending on whether using any liquid metering means, often 30 to 120 g / m 2, further preferably from 40 to 100 g / m 2.

【0022】液計量工程で使用する液計量具としては、
版搬送方向に対し何等かの駆動伝達により回転可能であ
って、少なくとも版表面に対し回転方向全てに計量幅方
向に対し均一に接触し、液計量時は可溶化した画像形成
層の剥離を抑制防止する形状を有することが肝要であ
る。液計量具としては、軸回りに一定直径の細いワイヤ
を螺旋状に巻付けたワイヤバー、溝付きロール、プレー
ンバー、軽量のゴムロール等が挙げられる。液計量具の
回転は、回転軸をある周速で順方向或は逆方向に強制的
に回転させても、また少なくとも版通過時にのみ回転す
る様にしておいても良い。押付け重量は液計量具のみの
重量で充分にその範囲をカバー出来るが、所望により加
圧ロール等で液計量具全体を加圧しても、或はその両端
にニップ圧をかけて実質的な押付け重量を増加させても
良い。
As a liquid measuring tool used in the liquid measuring step,
It can be rotated by some kind of drive transmission in the plate conveying direction, and evenly contacts the plate surface in all the rotating directions uniformly in the measuring width direction, and suppresses peeling of the solubilized image forming layer during liquid measurement. It is essential to have a shape that prevents. Examples of the liquid measuring tool include a wire bar in which a thin wire having a constant diameter is spirally wound around an axis, a grooved roll, a plain bar, and a lightweight rubber roll. The liquid measuring device may be rotated by forcibly rotating the rotating shaft in a forward direction or a reverse direction at a certain peripheral speed, or at least only when the plate passes. The pressing weight can cover the range sufficiently with the weight of only the liquid measuring tool, but if desired, the entire liquid measuring tool can be pressed with a pressure roll or the like, or the nip pressure is applied to both ends of the liquid measuring tool for substantial pressing. The weight may be increased.

【0023】非画像部が溶解された印刷版は、非画像部
除去廃棄工程に入り除去手段により非画像部に残る溶解
した画像形成層成分を除去し、更に次工程へ搬送され
る。非画像部除去廃棄工程で除去された除去物は、その
殆どが溶解した画像形成層成分及び疲労アルカリ性処理
液なので、廃棄処分とする。また、少なくとも廃液に含
まれるアルカリ性処理液量相当分は循環液中に新液を補
充して、循環液量の確保とアルカリ性処理活性度の保持
に努めることが必要である。
The printing plate in which the non-image area has been dissolved is subjected to a non-image area removing and discarding step to remove the dissolved image forming layer component remaining in the non-image area by the removing means, and further conveyed to the next step. Most of the removed substances removed in the non-image part removing and discarding step are the dissolved image forming layer components and the fatigue alkaline processing liquid, and are therefore discarded. In addition, it is necessary to replenish the circulating liquid with a new liquid at least as much as the amount of the alkaline processing liquid contained in the waste liquid so as to secure the amount of the circulating liquid and maintain the alkaline processing activity.

【0024】本発明に係わる非画像部除去工程に於ける
除去手段としては、エアナイフ、ゴムブレード、弾性ロ
ール、回転及び非回転(固定或は摺動等)ブラシ、及び
モルトンロール等を用いた方法等が挙げられる。弾性ロ
ールは、ロール対の間に印刷版を通してそのニップ圧に
よって版面のアルカリ性処理液を除去出来、ゴムブレー
ドは少なくとも版との接触面が滑らかな弾性材を印刷版
の搬送路に沿わせた状態で配置し、版面と摺接させるこ
とにより版面のアルカリ性処理液を取除くことが可能で
ある。これらに用いられる弾性材としては、シリコーン
ゴム、ネオプレンゴム、ブチルゴム、エチレンプロピレ
ンゴム、ニトリルブタジエンゴム、及びテフロンコート
ゴム等が挙げられる。
As a removing means in the non-image portion removing step according to the present invention, a method using an air knife, a rubber blade, an elastic roll, a rotating and non-rotating (fixed or sliding) brush, a Molton roll, etc. Etc. The elastic roll can remove the alkaline treatment liquid on the plate surface by the nip pressure through the printing plate between the roll pair, and the rubber blade has an elastic material with at least a smooth contact surface with the plate along the conveyance path of the printing plate. It is possible to remove the alkaline treatment liquid on the plate surface by arranging the plate and making a sliding contact with the plate surface. Examples of elastic materials used in these include silicone rubber, neoprene rubber, butyl rubber, ethylene propylene rubber, nitrile butadiene rubber, and Teflon-coated rubber.

【0025】ゴムブレードの設置に当たっては、ゴムブ
レード下に搬送速度以上の周速で回転するガイドロール
を設けたり、版先頭部がゴムブレード通過した直後に加
圧する様、搬送不良の誘発を防止するための何等かの機
構を設けることが望ましい。また、モルトンロール及び
ブラシによる除去では、溶解した画像形成層成分の剥離
除去を促進するため、少なくとも除去時に少量の除去用
処理液を供給しても良い。本発明に於ては、機構上の保
守管理負担の軽減、廃液量の低下、除去効率、及びアル
カリ性処理品質の低下防止等の総合的理由から、ゴムブ
レードが好適に用いられる。加圧を向上させるために、
ゴムブレードの版接触面と反対側に金属板等の加圧補助
部材及び手段を併用しても良い。
In installing the rubber blade, a guide roll rotating at a peripheral speed higher than the conveying speed is provided under the rubber blade, or pressurization is performed immediately after the leading edge of the plate passes through the rubber blade to prevent the conveyance failure from being induced. It is desirable to provide some mechanism for In addition, in the removal with a molton roll and a brush, a small amount of a treatment liquid for removal may be supplied at least at the time of removal in order to accelerate the peeling and removal of the dissolved image forming layer component. In the present invention, the rubber blade is preferably used for the comprehensive reasons such as reduction of maintenance load on the mechanism, reduction of waste liquid amount, removal efficiency, and prevention of deterioration of alkaline treatment quality. To improve pressure,
A pressure assisting member and means such as a metal plate may be used on the side opposite to the plate contact surface of the rubber blade.

【0026】非画像部除去廃棄工程から搬出された印刷
版は、リンス処理工程に於てリンス液を供給して僅かな
がら残存する除去物を完全に版上から除去する。リンス
処理工程に於けるリンス液供給法は、アルカリ性処理液
のそれと同様に従来公知の液供給機構、例えばシャワ
ー、高圧スプレー、ディップ方式等が使用出来るが、ア
ルカリ処理液に於ける処理と異なり、リンス処理はリン
ス液で速やかに版上に残存する液上物を完全に除去し得
なければならない。従って、液供給は液の飛散が抑制出
来る機構であれば、特開平3−109575号公報記載
の方法により版面に直接供給しても良いし、特開平4−
261543号公報記載の方法により圧搾空気と共に供
給しても良い。リンス処理で用いる処理方式は、使捨て
方式でも循環再使用方式でも良く、或は所望によりその
他の方式も利用出来る。リンス処理が終了した印刷版
は、保護ガム液を塗布して処理した後、保護ガム液を必
要に応じ熱風等で乾燥させて印刷に供する。
The printing plate carried out from the non-image area removing and discarding step is supplied with a rinse liquid in the rinse processing step to completely remove a slight residual substance removed from the plate. The rinse liquid supply method in the rinse treatment step can use a conventionally known liquid supply mechanism like that of the alkaline treatment liquid, for example, a shower, a high pressure spray, a dip method, etc., but unlike the treatment in the alkaline treatment liquid, The rinsing process must be able to quickly and completely remove the residual substance on the plate with the rinse liquid. Therefore, the liquid may be directly supplied to the printing plate by the method described in JP-A-3-109575, as long as it has a mechanism capable of suppressing the scattering of the liquid.
It may be supplied together with compressed air by the method described in Japanese Patent No. 261543. The treatment method used in the rinse treatment may be a disposal method or a circulation reuse method, or another method can be used if desired. The printing plate after the rinsing treatment is coated with a protective gum solution, treated, and then dried with hot air or the like as necessary for printing.

【0027】本発明に於て処理する非画像部アルカリ溶
解除去型平版印刷版は、支持体上に画像形成層として感
光層を有する感光性平版印刷版や、同様に光導電層を有
する電子写真平版印刷版である。これらの印刷版に用い
られる支持体としては、アルミニウム、亜鉛、銅−アル
ミニウム、銅−ステンレス、クロム−銅、クロム−銅−
アルミニウム、及びクロム−銅−ステンレス等の金属板
等を基体とし、少なくとも画像形成層を設ける面は親水
化処理が施された導電性支持体が挙げられる。また、そ
れらの厚みは0.07〜2.0mm、より好ましくは0.
1〜0.5mmが良い。これらの基体中でもアルミニウ
ム板が好適に使用される。このアルミニウム板は、アル
ミニウムを主成分とし微量の異元素を含有しても良く、
従来公知・公用の素材を適宜使用することが出来る。
The non-image area alkali dissolution removal type lithographic printing plate to be treated in the present invention is a photosensitive lithographic printing plate having a photosensitive layer as an image forming layer on a support, or an electrophotographic layer having a photoconductive layer. It is a lithographic printing plate. As the support used for these printing plates, aluminum, zinc, copper-aluminum, copper-stainless steel, chromium-copper, chromium-copper-
Examples of the conductive support include aluminum and a metal plate such as chrome-copper-stainless steel as a base, and at least the surface on which the image forming layer is provided is subjected to a hydrophilic treatment. Further, their thickness is 0.07 to 2.0 mm, more preferably 0.07 mm.
1 to 0.5 mm is good. Among these substrates, the aluminum plate is preferably used. The aluminum plate may contain aluminum as a main component and a slight amount of a foreign element,
Conventionally known / publicly used materials can be appropriately used.

【0028】所望の表面性状を画像形成層を設ける支持
体面に持たせるため、公知の方法で砂目立て、陽極酸化
することが好ましい。砂目立て処理に先立って、界面活
性剤またはアルカリ水溶液による脱脂処理しても良い。
砂目立て処理方法には、機械的粗面化法、電気化学的粗
面化法、化学的表面選択溶解法等がある。粗面化された
基体は、必要に応じてアルカリエッチング処理及び中和
処理して用いる。処理された基体は、その表面に酸化皮
膜を形成させるために陽極酸化処理する。陽極酸化皮膜
量は0.1〜10g/m2が良く、更には1〜6g/m2
好適である。
In order to impart desired surface texture to the surface of the support on which the image forming layer is provided, it is preferable to grain and anodize by a known method. Prior to the graining treatment, degreasing treatment with a surfactant or an alkaline aqueous solution may be performed.
The graining treatment method includes a mechanical surface roughening method, an electrochemical surface roughening method, and a chemical surface selective dissolution method. The roughened substrate is used after being subjected to alkali etching treatment and neutralization treatment, if necessary. The treated substrate is anodized to form an oxide film on its surface. Anodized film weight may have 0.1 to 10 g / m 2, and more is preferably 1 to 6 g / m 2.

【0029】この様にして得られた支持体上に所望の画
像形成層を設けて、感光性平版印刷版(PS版)や電子
写真平版印刷版が得られる。本発明の処理方法に関係す
るPS版としては、英国特許第1,350,521号明細
書等に記載の様なジアゾ樹脂(p-ジアゾフェニルアミン
とパラホルムアルデヒドとの縮合物の塩)とシェラック
との混合物からなる感光層、また英国特許第1,460,
978号及び同第1,505,739号明細書等に記載の
ジアゾ樹脂とヒドロキシエチルメタクリレート単位また
はヒドロキシエチルアクリレート単位を主なる繰返し単
位として有するポリマとの混合物からなる感光層を有す
るネガ型PS版、及び特開昭50−125806号公報
等に記載の様なo-キノンジアジド感光性物質とノボラッ
ク型フェノール樹脂との混合物からなる感光層を有する
ポジ型PS版が挙げられる。
A desired image forming layer is provided on the support thus obtained to obtain a photosensitive lithographic printing plate (PS plate) or an electrophotographic lithographic printing plate. Examples of PS plates relating to the treatment method of the present invention include diazo resins (salts of a condensate of p-diazophenylamine and paraformaldehyde) as described in British Patent 1,350,521 and shellac. A photosensitive layer consisting of a mixture with
Negative PS plate having a photosensitive layer composed of a mixture of a diazo resin described in JP-A No. 978 and No. 1,505,739 and a polymer having a hydroxyethyl methacrylate unit or a hydroxyethyl acrylate unit as a main repeating unit. And a positive PS plate having a photosensitive layer composed of a mixture of an o-quinonediazide photosensitive substance and a novolac type phenolic resin as described in JP-A-50-125806.

【0030】更に、米国特許第3,860,426号明細
書等に記載の様な光架橋性フォトポリマからなる感光層
を有するPS版や、米国特許第4,072,527号及び
同第4,072,528号明細書等に記載の様な光重合型
フォトポリマからなる感光層を有するPS版、英国特許
第1,235,281号及び同第1,495,861号明細
書等に記載の様なアジドと水溶性ポリマとの混合物から
なる感光層を有するPS版も知られており、これらにも
使用出来る。
Further, a PS plate having a photosensitive layer made of a photocrosslinkable photopolymer as described in US Pat. No. 3,860,426, US Pat. Nos. 4,072,527 and 4 are used. PS plates having a photosensitive layer composed of a photopolymerizable photopolymer as described in JP-B No. 1,072,528, described in British Patent Nos. 1,235,281 and 1,495,861. PS plates having a photosensitive layer made of a mixture of such an azide and a water-soluble polymer are also known and can be used for these.

【0031】また、電子写真平版印刷版としては、特公
昭37−17162号公報記載の有機光導体及びアルカ
リ可溶性基(酸または酸無水物基)含有高分子物質から
なる光導電層を有する印刷版、特公昭38−6961号
公報記載の低分子アルカリ可溶性有機光伝導体を含有す
る光導電層を有する印刷版、特公昭41−2426号公
報記載の酢酸ビニルとアルカリ可溶基含有ビニル化合物
との共重合体を含有する光導電層を有する印刷版、特公
昭41−39405号公報記載の光重合性光導伝性化合
物を含有する光導電層を有する印刷版、特公昭47−3
6778号公報記載のキナクリドン顔料とフェノール樹
脂等の有機樹脂結着剤とを含有する光導電層を有する印
刷版、特開昭54−89801号公報記載のフタロシア
ニン顔料と親水性樹脂とを含有する光導電層を有する印
刷版、特公平2−43181号公報記載のビニル基含有
カルボン酸とメタクリル酸及び/またはアクリル酸のエ
ステルとの特定比共重合体を含有する光導電層を有する
印刷版、特公平2−44065号公報記載のスチレン/
マレイン酸モノエステル共重合体を含有する光導電層を
有する印刷版が挙げられる。
As an electrophotographic lithographic printing plate, a printing plate having a photoconductive layer composed of an organic photoconductor described in JP-B-37-17162 and a polymer substance containing an alkali-soluble group (acid or acid anhydride group) is disclosed. A printing plate having a photoconductive layer containing a low-molecular-weight alkali-soluble organic photoconductor described in JP-B-38-6961, and a vinyl acetate described in JP-B-41-2426 and a vinyl compound containing an alkali-soluble group. A printing plate having a photoconductive layer containing a copolymer, a printing plate having a photoconductive layer containing a photopolymerizable photoconductive compound described in JP-B-41-39405, JP-B-47-3.
A printing plate having a photoconductive layer containing a quinacridone pigment described in 6778 and an organic resin binder such as a phenol resin, and a light containing a phthalocyanine pigment described in JP-A-54-89801 and a hydrophilic resin. Printing plate having a conductive layer, a printing plate having a photoconductive layer containing a specific ratio copolymer of a vinyl group-containing carboxylic acid and an ester of methacrylic acid and / or acrylic acid described in JP-B-2-43181, Styrene described in JP-B-2-44065 /
A printing plate having a photoconductive layer containing a maleic acid monoester copolymer may be mentioned.

【0032】これらの感光性平版印刷版及び電子写真平
版印刷版は、公知の操作によって画像形成させることが
出来る。本発明に於て、画像とは最終的に印刷版上でイ
ンク受理部となる下記アルカリ性処理液にレジストを有
する部分を指し、画像の形成は前者は露光し、後者は帯
電及び露光後、トナー現像して行なう。露光方法として
は、キセノンランプ、タングステンランプ、蛍光灯等を
光源として反射画像露光、透明陽画フィルムを通した密
着露光や、特に高感度型の感光層や光導電層を有する平
版印刷版の場合は、レーザ光、発光ダイオード等による
走査露光が挙げられる。走査露光を行なう場合は、He
−Neレーザ、He−Cdレーザ、アルゴンイオンレー
ザ、クリプトンイオンレーザ、ルビーレーザ、YAGレ
ーザ、窒素レーザ、色素レーザ、エキサイマーレーザ、
GaAs/GaAlAs、InGaAsPの様な半導体
レーザ、アレキサンドライトレーザ、銅蒸気レーザ等の
レーザ光源による走査露光、或は発光ダイオード、液晶
シャッタを利用した走査露光(発光ダイオードアレイ、
液晶シャッタアレイ等を用いたラインプリンタ型の光源
も含む)によって露光することが出来る。
Images can be formed on these photosensitive lithographic printing plates and electrophotographic lithographic printing plates by known operations. In the present invention, the image refers to a portion having a resist in the following alkaline processing liquid which finally becomes an ink receiving portion on a printing plate, the former is exposed to light, the latter is charged and exposed to toner after exposure. Develop and perform. As an exposure method, a reflection image exposure using a xenon lamp, a tungsten lamp, a fluorescent lamp or the like as a light source, a contact exposure through a transparent positive film, or a lithographic printing plate having a highly sensitive photosensitive layer or photoconductive layer Scanning exposure with a laser beam, a light emitting diode, or the like. He is used for scanning exposure.
-Ne laser, He-Cd laser, argon ion laser, krypton ion laser, ruby laser, YAG laser, nitrogen laser, dye laser, excimer laser,
Scanning exposure using a laser light source such as a semiconductor laser such as GaAs / GaAlAs or InGaAsP, an alexandrite laser, or a copper vapor laser, or scanning exposure using a light emitting diode or a liquid crystal shutter (light emitting diode array,
It can be exposed by a line printer type light source using a liquid crystal shutter array or the like).

【0033】電子写真平版印刷版の場合は、露光後トナ
ー現像する。トナー現像方法には、乾式現像法(カスケ
ード現像、磁気ブラシ現像、パウダクラウド現像)及び
液体現像法が知られており、何れも使用出来る。殊に液
体現像法は微細なトナー画像を形成出来、再現性良い印
刷版を作製するのに好適である。更に、正現像によるポ
ジ/ポジ現像や、適当なバイアス電圧の印加の下反転現
像によるネガ/ポジ現像も可能である。形成されたトナ
ー画像は公知の定着法、例えば加熱定着、圧力定着、溶
剤定着等により定着出来る。トナー成分は、下記のアル
カリ性処理液にレジスト性を有する公知の組成物が利用
出来る。
In the case of an electrophotographic planographic printing plate, toner development is performed after exposure. As a toner developing method, a dry developing method (cascade developing, magnetic brush developing, powder cloud developing) and liquid developing method are known, and any of them can be used. In particular, the liquid development method can form a fine toner image and is suitable for producing a printing plate with good reproducibility. Further, positive / positive development by positive development and negative / positive development by reversal development under application of an appropriate bias voltage are also possible. The formed toner image can be fixed by a known fixing method such as heat fixing, pressure fixing, solvent fixing and the like. As the toner component, a known composition having a resist property in the following alkaline processing liquid can be used.

【0034】画像形成された印刷版は、アルカリ性処理
液で処理して非画像部を溶解して除去する。非画像部除
去に用いられるアルカリ性処理液としては、アルカリ剤
を含有し高アルカリ域に緩衝能を有するものが望まし
い。従来、感光性平版印刷版現像液及び電子写真平版印
刷版溶出液に用いられているアルカリ剤としては、一般
式SiO2/M2O(M=Li、Na、K)で表現される珪
酸塩、アルカリ金属水酸化物、リン酸及び炭酸のアルカ
リ金属及びアンモニウム塩等の無機アルカリ剤、エタノ
ールアミン類、ジエチルアミン、エチレンジアミン、ト
リエチレンテトラミン、モルホリン等の有機アルカリ
剤、及びこれらの混合物が挙げられる。
The image-formed printing plate is treated with an alkaline treatment liquid to dissolve and remove the non-image area. As the alkaline processing liquid used for removing the non-image area, it is desirable to use an alkaline processing liquid containing an alkaline agent and having a buffering capacity in a high alkaline region. Conventionally, as an alkaline agent used in a photosensitive lithographic printing plate developer and an electrophotographic lithographic printing plate eluate, a silicate represented by the general formula: SiO 2 / M 2 O (M = Li, Na, K) Inorganic alkali agents such as alkali metal hydroxides, alkali metal and ammonium salts of phosphoric acid and carbonic acid, organic amine agents such as ethanolamines, diethylamine, ethylenediamine, triethylenetetramine, morpholine, and mixtures thereof.

【0035】また、非画像部へのアルカリ剤の浸透を促
進させ、アルカリ処理時間を短縮するために、特に電子
写真平版印刷版に於てはアルカリ処理中にトナー剥離が
誘発しない範囲で、エタノール、2-プロパノール、及
び1-ブタノール等の脂肪族アルコール、ベンジルアル
コール、フェネチルアルコール、及びフェニルプロパノ
ール類等の芳香族アルコール、2-エトキシエタノー
ル、1-メトキシ-2-プロパノール、及び1,2-ジメト
キシエタン等の脂肪族エーテル類等の水溶性有機溶剤
や、亜硫酸塩等の無機塩を併用しても良い。
Further, in order to accelerate the penetration of the alkaline agent into the non-image area and shorten the alkaline treatment time, especially in electrophotographic lithographic printing plates, ethanol is used in the range where toner peeling is not induced during the alkaline treatment. Aliphatic alcohols such as 2-propanol and 1-butanol, benzyl alcohol, phenethyl alcohol, and aromatic alcohols such as phenylpropanols, 2-ethoxyethanol, 1-methoxy-2-propanol, and 1,2-dimethoxy Water-soluble organic solvents such as aliphatic ethers such as ethane, and inorganic salts such as sulfite may be used in combination.

【0036】アルカリ性処理液には更に、特開昭55−
25100号公報記載のイオン性化合物、特開昭55−
95946号公報記載の水溶性カチオニックポリマ、特
開昭56−142528号公報記載の水溶性両性高分子
電解質、特開昭58−75152号公報記載の中性塩、
特開昭58−190952号公報記載のキレート剤、特
開平1−177541号公報記載の液粘度調整剤、特開
昭63−226657号公報記載の防腐剤や殺菌剤、及
び各種界面活性剤、天然及び合成水溶性ポリマ等の公知
の成分を必要に応じ含有させることが出来る。
The alkaline processing liquid is further described in JP-A-55-55.
Ionic compounds described in Japanese Patent No. 25100, JP-A-55-
Water-soluble cationic polymers described in JP-A-95946, water-soluble amphoteric polymer electrolytes described in JP-A-56-142528, neutral salts described in JP-A-58-75152,
Chelating agents described in JP-A-58-190952, liquid viscosity modifiers described in JP-A-1-177541, preservatives and bactericides described in JP-A-63-226657, and various surfactants and natural agents. Also, known components such as a synthetic water-soluble polymer can be contained if necessary.

【0037】[0037]

【実施例】本発明を実施例により更に具体的に説明する
が、本発明はその主旨を越えない限り、下記の実施例に
限定されるものではない。
EXAMPLES The present invention will be described in more detail by way of examples, but the present invention is not limited to the following examples as long as the gist thereof is not exceeded.

【0038】実施例1 JIS1050アルミニウムシートをパミス/水懸濁液
を研磨剤として回転ナイロンブラシで表面を砂目立てし
た。水洗後、60℃、10%水酸化ナトリウム水溶液に
浸漬し、アルミニウム溶解量が6g/m2になる様にエッ
チングした。水洗後、30%硝酸水溶液に1分間浸漬し
て中和し、充分水洗した。続いて3%塩酸水溶液中で電
解粗面化を行ない、50℃、20%硫酸水溶液中に浸漬
して表面を洗浄した後、水洗した。更に、20%硫酸水
溶液中で陽極酸化処理を施して、表面にアルミニウム酸
化物皮膜を形成させ、水洗後乾燥して支持体とした。こ
の支持体表面処理面に、ダイノミルにて1時間分散させ
た表1記載の光導電層形成用塗液を固形分塗布量が4.
4g/m2となる様塗布後、90℃で30秒間乾燥させ
て電子写真平版印刷版(印刷版A)とした。
Example 1 The surface of a JIS 1050 aluminum sheet was grained with a rotating nylon brush using a pumice / water suspension as an abrasive. After washing with water, it was immersed in a 10% sodium hydroxide aqueous solution at 60 ° C. and etched so that the amount of aluminum dissolved was 6 g / m 2 . After washing with water, it was immersed in a 30% aqueous nitric acid solution for 1 minute for neutralization, and then thoroughly washed with water. Subsequently, electrolytic surface roughening was performed in a 3% hydrochloric acid aqueous solution, and the surface was washed by immersing in a 20% sulfuric acid aqueous solution at 50 ° C. and then washed with water. Furthermore, anodizing treatment was performed in a 20% aqueous solution of sulfuric acid to form an aluminum oxide film on the surface, washed with water and dried to obtain a support. On the surface-treated surface of the support, the coating liquid for forming a photoconductive layer shown in Table 1 dispersed for 1 hour with Dynomill was applied at a solid content of 4.
After being coated at 4 g / m 2 , it was dried at 90 ° C. for 30 seconds to obtain an electrophotographic lithographic printing plate (printing plate A).

【0039】[0039]

【表1】 [Table 1]

【0040】この印刷版AをA2サイズに裁断し、遮光
して50℃で2時間加温した後に室温で放置した。次に
暗所にて光導電層の表面電位が約+280Vになる様帯
電させた後に半導体レーザ(780nm)を用いて走査
画像露光し、直ちに正電荷トナー(三菱製紙(株)製、L
OM-ED III)を用いて反転現像(バイアス電圧:+1
20V)を行ない、冷風乾燥してトナー分散媒を除去
後、更に熱定着して光導電層上にトナー画像を形成させ
た。得られたトナー現像済みの印刷版について、下記に
示す様な平版印刷版処理装置を用いて製版した。
The printing plate A was cut into A2 size, shielded from light and heated at 50 ° C. for 2 hours, and then left at room temperature. Next, the surface of the photoconductive layer was charged in a dark place so that the surface potential was about +280 V, and then scanning image exposure was performed using a semiconductor laser (780 nm), and immediately a positively charged toner (L paper manufactured by Mitsubishi Paper Mills Ltd., L
Inverse development (bias voltage: +1) using OM-ED III
20 V), and dried with cold air to remove the toner dispersion medium, and then heat-fixed to form a toner image on the photoconductive layer. The obtained toner-developed printing plate was subjected to plate making using a planographic printing plate processing apparatus as shown below.

【0041】図1に本実施例で用いた除去廃液への二酸
化炭素含有気体供給手段を付帯する平版印刷版処理装置
を示す。本処理装置の基本構成は、アルカリ性処理液供
給工程及び二酸化炭素含有気体供給手段を含む非画像部
除去廃棄工程からなり、更に図示しないリンス処理工程
及び保護ガム液塗布乾燥工程が付帯する。平版印刷版は
矢印の方向に印刷版搬送ライン1上を自動的に搬送さ
れ、処理液が供給される様になっている。
FIG. 1 shows a planographic printing plate treating apparatus equipped with a carbon dioxide-containing gas supply means for the removal waste liquid used in this embodiment. The basic constitution of this processing apparatus comprises an alkaline processing liquid supply step and a non-image part removing and discarding step including a carbon dioxide containing gas supply means, and a rinse processing step and a protective gum solution coating / drying step which are not shown are additionally provided. The planographic printing plate is automatically conveyed on the printing plate conveying line 1 in the direction of the arrow, and the processing liquid is supplied.

【0042】アルカリ性処理液供給工程は、処理液供給
管27、整流板28、及び給液ロール11aからなるア
ルカリ性処理液供給部と、液計量具47及びガイドロー
ル13からなる液計量部とで構成される。アルカリ性処
理液16は液供給管27及び整流板28を経て給液ロー
ル11aを介して版面に供給される様になっており、余
剰分はバックアップロール11b及び下部ガイド板76
を経てアルカリ性処理液貯液槽3に回収される様になっ
ている。また、液計量部で計量されたアルカリ性処理液
も、液誘導板75上を流動して液落下孔78より再びア
ルカリ性処理液貯液槽3に回収される様になっている。
The alkaline processing liquid supply step is composed of an alkaline processing liquid supply section composed of the processing solution supply pipe 27, the flow rectifying plate 28 and the liquid supply roll 11a, and a liquid measuring section composed of the liquid measuring tool 47 and the guide roll 13. To be done. The alkaline processing liquid 16 is adapted to be supplied to the plate surface via the liquid supply pipe 27 and the straightening plate 28 and the liquid supply roll 11a, and the surplus portion is backed up by the backup roll 11b and the lower guide plate 76.
After that, it is collected in the alkaline treatment liquid storage tank 3. Further, the alkaline processing liquid measured by the liquid measuring unit also flows on the liquid guide plate 75 and is collected again in the alkaline processing liquid storage tank 3 through the liquid drop hole 78.

【0043】アルカリ性処理液貯液槽3内側には、外周
が図示しない液面静止手段に隔絶された貯液量検知手段
であるセンサ21が配置されており、補充液はアルカリ
性処理液16が設定量減量した後に補充手段が作動する
様にも、また印刷版通過検知手段14により設定処理枚
数毎に補充手段が作動して、設定量若しくはセンサ上限
まで補充する様に補充様式が選定出来る様になってい
る。また、補充液の補充は、図示しない補充液補充制御
機構により、印刷版が印刷版通過検知手段14を通過直
後から任意の時間に補充が開始される様になっている。
Inside the alkaline processing liquid storage tank 3, there is arranged a sensor 21 which is a stored liquid amount detecting means whose outer periphery is separated by a liquid surface stationary means (not shown), and the alkaline processing liquid 16 is set as the replenishing liquid. Even if the replenishing means is operated after the quantity is reduced, and the replenishing means is operated by the printing plate passage detecting means 14 for each set number of sheets to be processed so that the replenishing mode can be selected so that the set amount or the sensor upper limit is replenished. Has become. Further, the replenishment of the replenishing liquid is started by the replenishing liquid replenishing control mechanism (not shown) at an arbitrary time immediately after the printing plate passes the printing plate passage detecting means 14.

【0044】アルカリ性処理液貯液槽3への給液は、三
系統の経路で行なえる様になっている。補充液貯液槽1
9に貯液された溶出補充液7は、補充ポンプ94及び電
磁バルブ100を経てアルカリ性処理液貯液槽3に直接
補充され、補充液貯液槽89に貯液された溶出補充液8
4は、補充ポンプ99、電磁バルブ101、及び補充液
供給管54を経て、液計量具47を介してアルカリ性処
理液貯液槽3に補充される様になっている。これら二系
統の補充路の他に、本実施例に係わる処理装置に付帯し
ない液貯留源から、配管128、電磁バルブ125、及
び補充液供給管54を経て、液計量具47を介してアル
カリ性処理液貯液槽3に補充される様にもなっている。
Liquid supply to the alkaline processing liquid storage tank 3 can be carried out through three routes. Replenisher tank 1
The eluate replenisher 7 stored in 9 is directly replenished to the alkaline processing liquid reservoir 3 via the replenishment pump 94 and the electromagnetic valve 100, and the eluate replenisher 8 stored in the replenisher reservoir 89.
4 is configured to be replenished to the alkaline processing liquid storage tank 3 via the replenishing pump 99, the electromagnetic valve 101, and the replenishing liquid supply pipe 54 and the liquid measuring tool 47. In addition to these two systems of replenishment paths, an alkaline treatment is performed from a liquid storage source not attached to the treatment apparatus according to the present embodiment, via the pipe 128, the electromagnetic valve 125, and the replenishment liquid supply pipe 54, and via the liquid measuring tool 47. The liquid storage tank 3 is also replenished.

【0045】非画像部除去廃棄工程は、溶解した非画像
部の除去手段であるゴムブレード22及びバックアップ
ロール20からなる溶解非画像部除去部、及び除去廃液
一次貯留槽4で構成される。ゴムブレード22の加圧
は、図示しないゴムブレード加圧機構により、溶解した
非画像部画像形成層の除去が最適に実施される範囲でバ
ックアップロール20との接触幅が最低になる様に調整
してある。ゴムブレード22によって除去された液状物
は、除去廃液一次貯留槽4に一時貯留されて、最終的に
除去廃液二次貯留槽9に廃棄される様になっている。
The non-image area removing / disposing step is composed of a dissolved non-image area removing section comprising a rubber blade 22 and a backup roll 20 which are means for removing the dissolved non-image area, and a removal waste liquid primary storage tank 4. The pressure of the rubber blade 22 is adjusted by a rubber blade pressing mechanism (not shown) so that the contact width with the backup roll 20 is minimized within a range where the dissolved non-image area image forming layer is optimally removed. There is. The liquid material removed by the rubber blade 22 is temporarily stored in the removal waste liquid primary storage tank 4 and finally disposed in the removal waste liquid secondary storage tank 9.

【0046】除去廃液二次貯留槽9内には給気管152
が配管されおり、二酸化炭素含有気体供給手段により除
去廃液二次貯留槽9底部に少なくとも二酸化炭素を含む
気体を吹込める様になっている。二酸化炭素含有気体供
給手段としては、エアポンプ157からバルブ145を
経て空気を供給する給気経路と、図示しない二酸化炭素
含有気体貯蔵源から管路148及びバルブ143を経て
主に二酸化炭素を供給する給気経路の二系統があり、何
れも給気管152に接続されている。また、給気管15
2の吹込み口先には散気用エアーストーン165が接続
されている。
An air supply pipe 152 is provided in the removal waste liquid secondary storage tank 9.
Is provided so that a gas containing at least carbon dioxide can be blown into the bottom portion of the second removal waste liquid storage tank 9 by the carbon dioxide-containing gas supply means. As the carbon dioxide-containing gas supply means, a supply path for supplying air from the air pump 157 through the valve 145 and a supply path for mainly supplying carbon dioxide from a carbon dioxide-containing gas storage source (not shown) through the conduit 148 and the valve 143. There are two systems of air paths, both of which are connected to the air supply pipe 152. In addition, the air supply pipe 15
An air diffuser air stone 165 is connected to the inlet of No. 2.

【0047】非画像部除去廃棄工程にて非画像部が除去
された印刷版は、図示しないリンス処理工程にてリンス
液と共に版上に残存する溶解非画像部画像形成層とアル
カリ性処理液とがリンスされて除去され、更に保護ガム
液塗布乾燥工程にて保護ガム液が塗布され、乾燥される
様になっている。
The printing plate from which the non-image area has been removed in the non-image area removing and discarding step has the dissolved non-image area image forming layer and the alkaline processing solution remaining on the plate together with the rinse liquid in the rinse processing step (not shown). After being rinsed and removed, the protective gum solution is applied and dried in the protective gum solution applying and drying step.

【0048】製版処理には表2及び表3に記載の溶出液
及び補充液を用いた。補充液は補充液補充槽89から補
充液供給管54を経て液計量具47を介して供給し、ま
た使用減量に応じて適宜補充液貯液槽89に補充した。
また、除去廃液二次貯留槽9への二酸化炭素含有気体の
供給は、バルブ143を閉栓しバルブ145を開栓して
エアポンプ157から空気を供給出来る様にしておき、
エアポンプ157を作動させずに製版を開始した。
For the plate-making process, the eluents and replenishers shown in Tables 2 and 3 were used. The replenisher was supplied from the replenisher replenisher tank 89 through the replenisher solution supply pipe 54 and the liquid measuring device 47, and was replenished to the replenisher solution storage tank 89 as appropriate according to the amount of use reduction.
Further, the supply of the carbon dioxide-containing gas to the removal waste liquid secondary storage tank 9 is performed by closing the valve 143 and opening the valve 145 so that the air can be supplied from the air pump 157.
Plate making was started without operating the air pump 157.

【0049】[0049]

【表2】 [Table 2]

【0050】[0050]

【表3】 [Table 3]

【0051】500版製版した時点で除去廃液二次貯留
槽9中の除去廃液のpHを測定したところ12.72で
あった。そこで、再び製版を開始すると同時にエアポン
プ157を作動させ、平版印刷版処理装置を起動させて
いる間は除去廃液二次貯留槽9中に空気を吹込みながら
更に1000版製版したところ、除去廃液は空気中の二
酸化炭素の吸収によって降下したため、改めてpH降下
性物質を添加することなくpHは11.97になった。
この二酸化炭素含有気体を吹込んだ除去廃液は、二酸化
炭素吹込み前に比して特に発熱や凝集物の発生は観られ
ず、スムーズに廃液タンクに注液出来た。
The pH of the removal waste liquid in the removal waste liquid secondary storage tank 9 was measured at the time of making the 500th plate, and it was 12.72. Therefore, when the plate making is started again and at the same time, the air pump 157 is operated and air is blown into the removal waste liquid secondary storage tank 9 while the planographic printing plate processing apparatus is being activated, further 1000 plates are produced. Since it was lowered by the absorption of carbon dioxide in the air, the pH became 11.97 without adding a pH-lowering substance again.
The removed waste liquid in which the carbon dioxide-containing gas was blown in did not generate heat or generated agglomerates as compared with before the injection of carbon dioxide, and could be smoothly injected into the waste liquid tank.

【0052】比較例1 製版期間中二酸化炭素含有気体を除去廃液に吹込まなか
った他は、実施例1と全く同様に製版処理を行なったと
ころ、除去廃液二次貯留槽9中の除去廃液量は18.8
dm3になり、pHは12.70であった。この除去廃液
には凝集物の発生は観られなかったが、液pHを12.
5以下にするため改めて濃硝酸を添加した。濃硝酸を添
加すると除去廃液は直ちに発熱すると共に除去廃液二次
貯留槽9底部に多量の軟らかい凝集物が発生し、結果と
して濃硝酸分の廃液が増加するばかりか凝集物を崩しな
がら注液しなければならないため廃液タンクへの移し換
えがスムーズに行なえなかった。
Comparative Example 1 When the plate making process was performed in exactly the same manner as in Example 1 except that the carbon dioxide-containing gas was not blown into the removal waste liquid during the plate making period, the amount of the removal waste liquid in the removal waste liquid secondary storage tank 9 was found. Is 18.8
It became dm 3 and the pH was 12.70. No agglomerates were found in the removed waste liquid, but the liquid pH was 12.
Concentrated nitric acid was added again to make it 5 or less. When concentrated nitric acid is added, the removed waste liquid immediately generates heat and a large amount of soft agglomerates are generated at the bottom of the removed waste liquid secondary storage tank 9. As a result, not only the amount of the concentrated nitric acid waste liquid increases but also the agglomerates are destroyed while pouring. Since it had to be done, the transfer to the waste liquid tank could not be performed smoothly.

【0053】実施例2 実施例1で用いた平版印刷版処理装置に於て管路148
に二酸化炭素高圧ボンベを連通し、バルブ145を閉栓
しバルブ143を開栓して、製版処理中二酸化炭素を供
給した他は実施例1と全く同様に製版処理を行なったと
ころ、実施例1と同様に改めてpH降下性物質を添加す
ることなくpHは12.17になった。この二酸化炭素
を吹込んだ除去廃液は、実施例1と同様に特に凝集物の
発生は観られず、スムーズに廃液タンクに注液出来た。
Example 2 In the planographic printing plate processing apparatus used in Example 1, a pipe line 148 was used.
A carbon dioxide high-pressure cylinder was communicated with the valve, the valve 145 was closed and the valve 143 was opened, and carbon dioxide was supplied during the plate-making process. Similarly, the pH became 12.17 without adding a pH-lowering substance. The removed waste liquid in which carbon dioxide was blown into the waste liquid tank could be smoothly injected into the waste liquid tank, as in Example 1, no particular agglomerates were observed.

【0054】実施例3 JIS1050のアルミニウムシートをパミス/水懸濁
液を研磨剤として回転ナイロンブラシで表面を砂目立て
した。水洗後、60℃の10重量%水酸化ナトリウム水
溶液に浸漬し、アルミニウム溶解量が6g/m2になる様
にエッチングした。水洗後、30重量%硝酸水溶液に1
分間浸漬して中和し、充分水洗した。続いて2重量%硝
酸水溶液中で電解粗面化を行ない、50℃の20重量%
硫酸水溶液中に浸漬して表面を洗浄した後、水洗した。
更に、20重量%硫酸水溶液中で陽極酸化処理を施し
て、表面にアルミニウム酸化物皮膜を形成させ、水洗後
乾燥して支持体とした。この支持体表面処理面に、表4
記載の感光層形成用塗液を固形分塗布量が2.1g/m2
となる様塗布後、90℃で乾燥させて感光性平版印刷版
(印刷版B)を得た。
Example 3 The surface of a JIS 1050 aluminum sheet was grained with a rotating nylon brush using a pumice / water suspension as an abrasive. After washing with water, it was immersed in a 10% by weight aqueous sodium hydroxide solution at 60 ° C. and etched so that the amount of aluminum dissolved was 6 g / m 2 . After washing with water, add 30% by weight nitric acid solution to 1
It was soaked for a minute for neutralization and then thoroughly washed with water. Subsequently, electrolytic surface roughening was performed in a 2 wt% nitric acid aqueous solution, and 20 wt% at 50 ° C.
The surface was washed by immersing it in an aqueous solution of sulfuric acid and then washing with water.
Further, anodization treatment was performed in a 20 wt% sulfuric acid aqueous solution to form an aluminum oxide film on the surface, washed with water and dried to obtain a support. Table 4 shows the surface of this support.
The photosensitive layer forming coating solution described above has a solid content of 2.1 g / m 2
And then dried at 90 ° C. to obtain a photosensitive lithographic printing plate (printing plate B).

【0055】[0055]

【表4】 [Table 4]

【0056】この印刷版BをA2サイズに裁断し、これ
に陽画原稿を通して80cmの距離から2KWのメタル
ハライドランプを用いて露光し、続いて実施例1で用い
た平版印刷版処理装置、及び表5及び表6に記載の処理
液を用いて製版した。尚、製版処理の適性から、実施例
1で用いた平版印刷版処理装置に於てガイドロール13
上に配置した液計量具47を搬送ロール17上に移動さ
せ、アルカリ処理時間は非画像部除去廃棄工程搬入直前
に非画像部感光層が完全に溶解する様版搬送速度を調整
して製版した。
This printing plate B was cut into A2 size, and a positive image original was passed through the plate to expose it from a distance of 80 cm using a 2 KW metal halide lamp, and then the planographic printing plate processing apparatus used in Example 1 and Table 5 were used. And plate making was carried out using the treatment liquid described in Table 6. From the suitability of the plate making process, the guide roll 13 was used in the planographic printing plate processing apparatus used in Example 1.
The liquid measuring tool 47 arranged above was moved onto the transport roll 17, and the plate was prepared by adjusting the plate transport speed so that the alkali processing time was such that the photosensitive layer of the non-image part was completely dissolved immediately before the non-image part removal and disposal process was carried in. .

【0057】[0057]

【表5】 [Table 5]

【0058】[0058]

【表6】 [Table 6]

【0059】版搬送速度を変更し、200版製版した時
点(除去廃液のpHは12.67であった)から空気を
除去廃液中に吹込んだ他は、実施例1と同様に計150
0版製版した。その結果、除去廃液は空気中の二酸化炭
素の吸収によって降下したため、改めてpH降下性物質
を添加することなくpHは11.85となった。この二
酸化炭素含有気体を吹込んだ除去廃液は、二酸化炭素吹
込み前に比して特に発熱や凝集物の発生は観られず、ス
ムーズに廃液タンクに注液出来た。
The same as in Example 1, except that the plate conveying speed was changed and air was blown into the removal waste liquid at the time of making the 200th plate (the pH of the removal waste liquid was 12.67).
0 plate was made. As a result, the removed waste liquid dropped due to the absorption of carbon dioxide in the air, so that the pH became 11.85 without adding a pH-lowering substance again. The removed waste liquid in which the carbon dioxide-containing gas was blown in did not generate heat or generated agglomerates as compared with before the injection of carbon dioxide, and could be smoothly injected into the waste liquid tank.

【0060】比較例2 実施例3で用いた平版印刷版処理装置に於てバルブ14
5エアポンプ157間に高アルカリ系の二酸化炭素脱気
機構を連通し、製版期間中二酸化炭素を含有しない空気
を除去廃液に吹込んだ他は、実施例3と全く同様に製版
処理を行なったところ、除去廃液二次貯留槽9中のpH
は気体を吹込まなかった時と殆ど降下せず12.62で
あった。この除去廃液には凝集物の発生は観られなかっ
たが、液pHを12.5以下にするため改めて酸を添加
しなければならなかった。
Comparative Example 2 The valve 14 was used in the planographic printing plate processing apparatus used in Example 3.
5 A plate-making process was performed in exactly the same manner as in Example 3 except that a highly alkaline carbon dioxide degassing mechanism was connected between the five air pumps 157, and carbon dioxide-free air was blown into the removed waste liquid during the plate-making period. , PH in the removal waste liquid secondary storage tank 9
Was 12.62 with almost no drop when no gas was blown. No agglomerates were observed in the removed waste liquid, but an acid had to be added again in order to adjust the liquid pH to 12.5 or less.

【0061】[0061]

【発明の効果】以上説明した如く、本発明の平版印刷版
処理廃液処理方法によって製版処理で副製する高アルカ
リ性の処理廃液を処理すれば、処理廃液廃棄時に改めて
酸性物質を添加することによって液pHを低下させるこ
となく、簡便かつ安全に処理廃液が処理出来、処理廃液
処理負担を大幅に軽減させる秀逸なる効果をもたらす。
As described above, by treating the highly alkaline processing waste liquid produced by the plate making process by the planographic printing plate processing waste liquid processing method of the present invention, the liquid is added by adding an acidic substance again when the processing waste liquid is discarded. The treatment waste liquid can be treated easily and safely without lowering the pH, and the excellent effect of significantly reducing the treatment waste liquid treatment load is brought about.

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

【図1】本発明の平版印刷版処理廃液処理方法に係わる
製版処理を実施するために用いた平版印刷版処理装置の
縦断面構成図。
FIG. 1 is a vertical cross-sectional configuration diagram of a planographic printing plate processing apparatus used for carrying out a plate making process according to a planographic printing plate processing waste liquid processing method of the present invention.

【符号の説明】[Explanation of symbols]

1 印刷版搬送ライン 3 アルカリ性処理液貯液槽 9 除去廃液二次貯留槽 157 エアポンプ 165 散気用エアーストーン 1 Printing plate conveyance line 3 Alkaline treatment liquid storage tank 9 Removal waste liquid secondary storage tank 157 Air pump 165 Air diffuser air stone

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 平版印刷版画像形成面にアルカリ性処理
液を供給して非画像部を溶解した後、印刷版上のアルカ
リ性処理液と溶解した非画像部とを除去して廃棄する平
版印刷版の製版処理に於ける処理廃液処理方法であっ
て、廃棄されたアルカリ性処理液と非画像部成分とから
なる処理廃液中に少なくとも二酸化炭素を含有する気体
を吹込むことを特徴とする平版印刷版処理廃液処理方
法。
1. A lithographic printing plate that is supplied with an alkaline processing liquid on the image forming surface of the lithographic printing plate to dissolve the non-image area, and then the alkaline processing liquid and the dissolved non-image area on the printing plate are removed and discarded. A method for treating waste liquid in the plate making process, wherein a gas containing at least carbon dioxide is blown into the waste treatment liquid consisting of the discarded alkaline processing liquid and non-image part components. Treatment waste liquid treatment method.
JP19372593A 1993-08-04 1993-08-04 Processing method of waste liquid from planographic printing plate treatment Pending JPH0749574A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19372593A JPH0749574A (en) 1993-08-04 1993-08-04 Processing method of waste liquid from planographic printing plate treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19372593A JPH0749574A (en) 1993-08-04 1993-08-04 Processing method of waste liquid from planographic printing plate treatment

Publications (1)

Publication Number Publication Date
JPH0749574A true JPH0749574A (en) 1995-02-21

Family

ID=16312767

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19372593A Pending JPH0749574A (en) 1993-08-04 1993-08-04 Processing method of waste liquid from planographic printing plate treatment

Country Status (1)

Country Link
JP (1) JPH0749574A (en)

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