JPH0221990A - Treating device for waste photographic processing liquid - Google Patents

Treating device for waste photographic processing liquid

Info

Publication number
JPH0221990A
JPH0221990A JP17067488A JP17067488A JPH0221990A JP H0221990 A JPH0221990 A JP H0221990A JP 17067488 A JP17067488 A JP 17067488A JP 17067488 A JP17067488 A JP 17067488A JP H0221990 A JPH0221990 A JP H0221990A
Authority
JP
Japan
Prior art keywords
waste liquid
photographic processing
processing waste
concentrate
heating means
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
JP17067488A
Other languages
Japanese (ja)
Inventor
Masayuki Kurematsu
雅行 榑松
Shigeharu Koboshi
重治 小星
Nobutaka Goshima
伸隆 五嶋
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.)
Konica Minolta Inc
Original Assignee
Konica Minolta Inc
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 Konica Minolta Inc filed Critical Konica Minolta Inc
Priority to JP17067488A priority Critical patent/JPH0221990A/en
Publication of JPH0221990A publication Critical patent/JPH0221990A/en
Pending legal-status Critical Current

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  • Photographic Processing Devices Using Wet Methods (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)

Abstract

PURPOSE:To prevent the decomposition of a concentrate by overheating and to remarkably inhibit the generation of offensive odor by independently providing heating means and a separating means to separate steam from a waste photographic processing liquid in the waste soln. circulating system. CONSTITUTION:A waste photographic processing liquid is circulated in a circulating system 1 and heated by heating means 2. Vapor contg. gas generated by the heating is separated from the remaining waste photographic processing liquid by a separating means 3 and the waste liquid is evaporated and concentrated. The resulting concentrate is not heated by the heating means 2, the decomposition of the concentrate by overheating can be prevented and the generation of offensive odor due to gaseous ammonia, hydrogen sulfide, etc., can be remarkably inhibited.

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は、写真用自動現像機による写真感光材料の現
像処理に伴い発生する廃液(以下、写真処理廃液ないし
廃液と略称)を蒸発処理する処理装置に係り、特に、自
動現像機内若しくは自動現像機の近傍に配置して処理す
るのに適した写真処理廃液の処理装置に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is a method for evaporating waste liquid (hereinafter referred to as photographic processing waste liquid or waste liquid) generated during the processing of photographic light-sensitive materials using an automatic photographic processor. The present invention relates to a processing device, and particularly to a processing device for photographic processing waste liquid suitable for processing by being disposed in or near an automatic processor.

[従来の技術] 般に、へロケン化銀写真感光材料の写真処理は、厚白感
光材料の場合には現像、定着、水洗等、カラー感光材料
の場合には発色現像、漂白定着(又は漂白、定着)、水
洗、安定化等の機能の1つ又は2つ以上を有する処理液
を用いた工程を組合せて行なわれている。
[Prior Art] In general, photographic processing of silver helochloride photographic materials includes development, fixing, washing, etc. in the case of thick white materials, and color development, bleach-fixing (or bleaching, etc.) in the case of color photographic materials. (fixing), washing with water, stabilization, etc., using a processing liquid that has one or more of the following functions.

そして、多量の感光材料を処理する写真処理においては
、処理によって消費された成分を補充し方、処理によっ
て処理液中に溶出或いは蒸発によって濃化する成分(例
えは現像液における臭化物イオン、定着液における銀錯
塩のような)を除去して処理液成分を一定に保つことに
よって処理液の性能を一定に維持する手段が採られてお
り、補充のために補充液か処理液に補充され、写真処理
における濃厚化成分の除去のために処理液の部か廃棄さ
れている。
In photographic processing in which a large amount of light-sensitive material is processed, it is important to consider how to replenish components consumed during processing, and components that are eluted into the processing solution or concentrated by evaporation during processing (for example, bromide ions in the developer, bromide ions in the fixer, etc.). A method is used to maintain the performance of the processing solution at a constant level by removing substances (such as silver complex salts) and keeping the processing solution components constant. A portion of the processing solution is discarded to remove concentrated components during processing.

近年、補充液は水洗の補充液である水洗水を含めて公害
上や経済的理由から補充の量を大幅に減少させたシステ
ムに変わりつつあるが、写真処理廃液は自動現像機の処
理槽から廃液管によって導かれ、水洗水の廃液や自動現
像機の冷却水等で稀釈されて下水道等に廃棄されている
In recent years, systems have been changing to systems in which the amount of replenishment fluid, including washing water, which is used as a replenishment fluid for washing, has been significantly reduced due to pollution and economic reasons, but photographic processing waste fluid is removed from the processing tank of automatic processors. It is led through a waste liquid pipe, diluted with waste liquid from washing water, cooling water from automatic processors, etc., and then disposed of in a sewer or the like.

しかしながら、近年の公害規制の強化により、水洗水や
冷却水の下水道やY河川への廃棄は可能であるか、これ
ら以外の写真処理液[例えは、現像液、定着液、発色現
像液、漂白定着液(又は漂白液、定着液)、安定液等]
の廃棄は、実質的に不可能となっている。このため、各
写真処理業者は廃液を専門の廃液処理業者に回収料金を
払って回収してもらったり、公害処理設備を設置したり
している。しかしなから、廃液処理業者に委託する方法
は、廃液を貯溜しておくのにかなりのスペスが必要とな
るし、またコスト的にも極めて高価である。さらに、公
害fi埋設備は初期投資(イニシャルコスト)か極めて
大きく、整備するのにかなり広大な場所を必要とする等
の欠点を有している。従って、一般には廃液回収業者に
よって回収され、二次及び三次処理され無害化されてい
るが、回収費の高騰により廃液引き取り価格は年々高く
なるはかりでなく、ミニラボ等では回収効率は悪いため
、なかなか回収に来てもらうことができず、廃液か店に
充満する等の問題を生じている。
However, due to the tightening of pollution regulations in recent years, it is now possible to dispose of washing water and cooling water into sewers and rivers. Fixing solution (or bleaching solution, fixing solution), stabilizer, etc.]
It has become virtually impossible to dispose of. For this reason, each photo processing company pays a collection fee to a specialized waste liquid processing company to collect the waste liquid, or installs pollution treatment equipment. However, the method of outsourcing to a waste liquid treatment company requires a considerable amount of space to store the waste liquid and is also extremely expensive. Furthermore, the pollution-filtering equipment has drawbacks such as the initial investment (initial cost) being extremely large and the need for a fairly large area for maintenance. Therefore, waste liquid is generally collected by a waste liquid collection company and rendered harmless through secondary and tertiary processing, but due to rising collection costs, the price of waste liquid collection is increasing year by year, and collection efficiency is low in minilabs, etc., so it is difficult to do so. No one can come to collect the liquid, causing problems such as waste liquid filling the store.

これらの問題を解決するために写真処理廃液の処理をミ
ニラボ等でも容易に行なえることを目的として、写真処
理廃液を加熱して水分を蒸発乾固ないし固化することが
研究されており、例えば、実開昭60−70841号等
に示されている。
In order to solve these problems, research has been conducted to heat the photographic processing waste liquid to evaporate the water to dryness or solidify it, with the aim of making it easier to process the photographic processing waste liquid even in minilabs. This is shown in Utility Model Application Publication No. 60-70841.

[発明が解決しようとする課題] ところで、このように写真処理廃液を蒸発処理した場合
、亜硫酸ガス、硫化水素、アンモニアガス等の有害ない
し極めて悪臭性のガスが発生する。これは写真処理廃液
に含有される定着液や漂白定着液としてよく用いられる
特有のイオウ系化合物、例えはヂオ硫酸塩や亜硫酸塩の
分解によるものである。
[Problems to be Solved by the Invention] By the way, when photographic processing waste liquid is evaporated in this manner, harmful or extremely malodorous gases such as sulfur dioxide gas, hydrogen sulfide, and ammonia gas are generated. This is due to the decomposition of specific sulfur-based compounds, such as diosulfate and sulfite, which are often used as fixers and bleach-fixers contained in photographic processing waste solutions.

このため、臭気成分を除去すべく種々の研究、実験を行
なったところ、加熱手段の加熱で写真処理廃液が蒸発濃
縮されるが、これにより生しる濃縮物が蒸発手段内で、
加熱手段の近傍に長く留まって加熱され続けると、濃縮
物が過熱分解して、硫化水素、アンモニアガス等が発生
する。
For this reason, various studies and experiments have been conducted to remove odor components, and it has been found that the photographic processing waste liquid is evaporated and concentrated by the heating of the heating means, but the resulting concentrate is inside the evaporation means.
If the concentrate remains near the heating means for a long time and continues to be heated, the concentrate will be overheated and decomposed, generating hydrogen sulfide, ammonia gas, etc.

また、蒸発手段に貯留した蒸発手段を加熱して写真処理
廃液を蒸発濃縮するため、蒸発面積が大きく装置が大型
で、しかも蒸発手段を耐熱性の部材で形成する必要があ
り経費が嵩む。
Further, since the evaporation means stored in the evaporation means is heated to evaporate and concentrate the photographic processing waste liquid, the evaporation area is large and the apparatus is large in size.Moreover, the evaporation means must be made of a heat-resistant member, which increases costs.

従って、写真処理廃液を循環させて加熱するようにする
と、蒸発濃縮によって生じる濃縮物を加熱することがな
くなり、濃縮された濃縮物の過熱分解を防止でき、硫化
水素、アンモニアガス等の臭気の発生を大幅に抑制する
ことができると共に、蒸発効率がよく装置が小型になり
、しかも耐熱部分を少なくでき経費も低減することを見
い出した。
Therefore, if the photographic processing waste liquid is circulated and heated, the concentrate produced by evaporation concentration will not be heated, and overheating decomposition of the concentrated concentrate can be prevented, resulting in the generation of odors such as hydrogen sulfide and ammonia gas. It has been found that the evaporation efficiency can be significantly suppressed, the device can be made smaller, and the number of heat-resistant parts can be reduced, reducing costs.

この発明は従来の問題点に鑑みてなされたものであり、
写真処理廃液の蒸発濃縮によって生じる濃縮物の加熱分
解を防止し、悪臭の発生を軽減すると共に、装置の小型
化及び耐久性がある写真処理廃液の処理装置を提供する
ことを目的としている。
This invention was made in view of the conventional problems,
It is an object of the present invention to provide a processing device for photographic processing waste liquid that prevents thermal decomposition of a concentrate produced by evaporative concentration of photographic processing waste liquid, reduces the generation of bad odor, and is compact and durable.

[課題を解決するための手段] 前記課題を解決するために、この発明は写真処理廃液を
、加熱手段で加熱して蒸発濃縮せしめる写真処理廃液の
処理装置において、前記写真処理廃液を循環系で循環せ
しめ、この循環系に前記加熱手段と、加熱によって生じ
るガスを含む蒸気と写真処理廃液とを分離する分離手段
とを独立に備えることを特徴としている。
[Means for Solving the Problems] In order to solve the above-mentioned problems, the present invention provides a processing apparatus for photographic processing waste liquid that heats the photographic processing waste liquid with a heating means to evaporate and concentrate the photographic processing waste liquid, in which the photographic processing waste liquid is circulated through a circulation system. It is characterized in that the circulation system is independently equipped with the heating means and a separation means for separating the photographic processing waste liquid from the steam containing the gas generated by heating.

従って、写真処理廃液が循環系で循環し、これを加熱手
段で加熱して、この加熱によって生しるガスを含む蒸気
と写真処理廃液とを分離手段で分離させて蒸発濃縮する
ため、濃縮された濃縮物を加熱手段て加熱することがな
くなり、濃縮物の過熱分解を防止でき、硫化水素、アン
モニアガス等の臭気の発生を大幅に抑制することかでき
る。
Therefore, the photographic processing waste liquid is circulated in the circulation system, heated by the heating means, and the vapor containing gas produced by this heating is separated from the photographic processing waste liquid by the separation means and evaporated and concentrated. This eliminates the need to heat the concentrated concentrate using a heating means, thereby preventing the concentrate from being overheated and decomposing it, and greatly suppressing the generation of odors such as hydrogen sulfide and ammonia gas.

また、循S系に加熱手段と分離手段とを独立に備えるた
め、写真処理廃液の蒸発効率が向上し装置を小型にてき
、しかも耐熱部分は循環系の加熱手段が備えられる部分
でよく、耐熱部分を軽減でき安価な装置となる。
In addition, since the circulating S system is equipped with a heating means and a separating means independently, the evaporation efficiency of photographic processing waste liquid is improved and the apparatus can be made more compact. The number of parts can be reduced, resulting in an inexpensive device.

また、この発明の写真処理廃液の処理装置において、循
環系に空気を混入させることができ、この空気量は加熱
量に対して0.1〜100fL/kcanが好ましい。
Further, in the photographic processing waste liquid processing apparatus of the present invention, air can be mixed into the circulation system, and the amount of air is preferably 0.1 to 100 fL/kcan relative to the amount of heating.

この空気の混入によって、写真処理廃液の突沸状態をな
くし蒸発温度を低下させて、硫化水素、アンモニアガス
等の臭気の発生を抑制する。
By mixing this air, the bumping state of the photographic processing waste liquid is eliminated and the evaporation temperature is lowered, thereby suppressing the generation of odors such as hydrogen sulfide and ammonia gas.

また、分離手段に濃縮物を取り出す取出手段を備えると
、濃縮物を排出することができ、濃縮物の過熱を軽減て
ぎて臭気の発生を抑えることができる。この取出手段は
分離手段に配置されたスラッジフィルタで構成でき、例
えば、円筒フィルタ、フィルタバッグ等のフィルタの穴
のサイズが1〜200μmのものを使用し、また分離手
段の下部に配置されたバルブを開閉してバッグ等に取り
出すようにすることができる。
Further, if the separation means is provided with a take-out means for taking out the concentrate, the concentrate can be discharged, overheating of the concentrate can be reduced, and odor generation can be suppressed. This extraction means can be composed of a sludge filter arranged in the separation means, for example, a cylindrical filter, a filter bag, etc. with a filter hole size of 1 to 200 μm, and a valve arranged at the bottom of the separation means. It can be opened and closed and taken out into a bag or the like.

この発明の循環系の少なくとも一部がパイプであり、こ
のパイプに加熱手段を備えることができ、この加熱手段
はバイブの外部から写真処理廃液を加熱するようにして
もよいし、内部から加熱するようにしてもよい。
At least a part of the circulation system of the present invention is a pipe, and this pipe can be equipped with a heating means, and this heating means may heat the photographic processing waste liquid from the outside of the vibrator, or it may heat the photographic processing waste liquid from the inside. You can do it like this.

この加熱手段はニクロム線てあっても良いし、カートリ
ッジヒータ、石英ヒータ、テフロンヒタ、棒ヒータやパ
ネルヒータのように加工成型されたヒータまたはマイク
ロウェーブによる加熱であっても良い。また、写真処理
廃液に導電材料を直接接触させ、この導電材料によって
写真処理廃液中に電流を流すと共に、加熱するようにし
てもよい。
This heating means may be a nichrome wire, a heated heater such as a cartridge heater, a quartz heater, a Teflon heater, a bar heater, a panel heater, or a microwave. Alternatively, a conductive material may be brought into direct contact with the photographic processing waste liquid, and the conductive material may cause an electric current to flow through the photographic processing waste liquid and heat the photographic processing waste liquid.

循環系の加熱部の材質は、耐熱性ガラス、チタン、ステ
ンレス、カーボンスチール、耐熱プラスデック等の耐熱
性の材質であれはいかなる素材てあってもよいか、安全
性や耐腐食性の点からステンレス(好ましくは5US3
04や5US316、特に好ましくは5US316)や
チタンか好ましい。また、加熱手段の設置位置は、蒸発
手段の廃液を加熱できる位置てあれば、いずれの位置で
あっても良い。
The heating part of the circulation system can be made of any heat-resistant material, such as heat-resistant glass, titanium, stainless steel, carbon steel, heat-resistant plus deck, etc., from the standpoint of safety and corrosion resistance. Stainless steel (preferably 5US3
04 or 5US316, particularly preferably 5US316) or titanium. Further, the heating means may be installed at any position as long as it can heat the waste liquid of the evaporation means.

この発明による処理を行なうことができる写真処理廃液
の代表例については、この出願人が先に出願した特願昭
62−194615号明細書等に記載されるものが用い
られ、特に、この発明の処理装置においては、チオ硫酸
塩、亜硫酸塩、アンモニウム塩を多量に含有する写真処
理廃液の場合に有効であり、特に有機酸第2鉄錯塩及び
チオ硫酸塩を含有する場合極めて有効である。
Typical examples of photographic processing waste liquids that can be processed according to the present invention include those described in Japanese Patent Application No. 1986-194615 previously filed by this applicant. In processing equipment, it is effective for photographic processing waste liquids containing large amounts of thiosulfates, sulfites, and ammonium salts, and is particularly effective when containing organic acid ferric complex salts and thiosulfates.

この発明の好ましい適用例としては、自動現像機による
写真感光材料の現像処理に伴ない発生する写真処理廃液
を自動現像機内もしくはその近傍にて処理を行なうのに
適している。
A preferred application of the present invention is to treat photographic processing waste liquid generated during the development of photographic light-sensitive materials using an automatic processor in or near the automatic processor.

[実施例コ 第1図はこの発明の写真処理廃液の処理装置を示す概略
構成図である。
[Example 1] FIG. 1 is a schematic diagram showing a processing apparatus for photographic processing waste liquid according to the present invention.

図において符号1は写真処理廃液の循環系で、この循環
系1に写真処理廃液を加熱する加熱手段2と、この加熱
によって生じるガスを含む蒸気と写真処理廃液とを分離
する分離手段3とが独立に備えられ、加熱手段2は分離
手段3より低い位置に配置されている。
In the figure, reference numeral 1 denotes a circulation system for photographic processing waste liquid, and this circulation system 1 includes a heating means 2 for heating the photographic processing waste liquid, and a separation means 3 for separating the photographic processing waste liquid from steam containing gas generated by this heating. The heating means 2 is provided independently, and the heating means 2 is arranged at a lower position than the separating means 3.

加熱手段2は循環系のバイブ4の外周に設けて、パイプ
4の外部から写真処理廃液を加熱するようになっており
、この加熱で写真処理廃液が自動的に循環系1を循環し
て加熱される。この加熱手段2は第2図に示すように、
バイブ4の内部に配置して写真処理廃液を直接加熱する
ようにしてもよい。
The heating means 2 is provided around the outer periphery of the vibrator 4 of the circulation system, and is designed to heat the photographic processing waste liquid from the outside of the pipe 4, and by this heating, the photographic processing waste liquid automatically circulates through the circulation system 1 and is heated. be done. This heating means 2, as shown in FIG.
It may be placed inside the vibrator 4 to directly heat the photographic processing waste liquid.

なお、この加熱手段2を分離手段3より高い位置に配置
することもでき、この場合には循環系1に循環ポンプを
配置して強制的に循環させる。
Note that this heating means 2 can also be arranged at a higher position than the separating means 3, and in this case, a circulation pump is arranged in the circulation system 1 to force the circulation.

循環系1は加熱手段2が設けられる部分を耐熱性の部材
で形成すればよく、装置が安価になる。
The portion of the circulation system 1 where the heating means 2 is provided may be formed of a heat-resistant member, and the device becomes inexpensive.

また、加熱手段2を循環系1に設けることにより、写真
処理廃液の蒸発面積を小さくすることができ、しかも濃
縮物を過熱することがなくなるため、濃縮物の過熱分解
による臭気ガスを大幅に低下させることかでき、濃縮か
進行しても硫化水素、イオウ系の臭気の発生が軽減する
In addition, by providing the heating means 2 in the circulation system 1, the evaporation area of the photographic processing waste liquid can be reduced, and the concentrate is not overheated, so the odor gas caused by overheated decomposition of the concentrate is significantly reduced. Even if the concentration progresses, the generation of hydrogen sulfide and sulfur odors will be reduced.

前記分離手段3は所定容量の容器から構成され、この容
器はプラスチックやチタン等で形成され、容器本体3a
と蓋体3bとからなっている。
The separating means 3 is composed of a container having a predetermined capacity, and this container is made of plastic, titanium, etc., and has a container body 3a.
and a lid body 3b.

この分離手段3はガスを含む蒸気と写真処理廃液とを分
離する機能を有するため、この機能を有する程度まて容
量を小さくすることができ、また材質も高度の耐熱性を
有しないもので形成することができ製作コストの低減が
可能になっている。
Since this separation means 3 has the function of separating gas-containing steam and photographic processing waste liquid, the capacity can be reduced to the extent that it has this function, and it is also made of a material that does not have a high degree of heat resistance. This makes it possible to reduce manufacturing costs.

この分離手段3の内部には取出手段5が配置され、この
取出手段5はスラッジフィルタ5aで構成され、容器本
体3aに取付部材5bを介して着脱可能に支持されてい
る。循環系1のバイブ4から排出される加熱された写真
処理廃液は分離手段3に供給されることによって、ガス
を含む蒸気と濃縮された写真処理廃液に分離され、この
写真処理廃液はスラッジフィルタ5aに供給される。こ
のスラッジフィルタ5aで、ろ過されて水分が除去され
た濃縮物を取り出すことができる。
A take-out means 5 is disposed inside the separating means 3, and the take-out means 5 is comprised of a sludge filter 5a, and is detachably supported by the container body 3a via a mounting member 5b. The heated photographic processing waste liquid discharged from the vibrator 4 of the circulation system 1 is supplied to the separation means 3, where it is separated into gas-containing vapor and concentrated photographic processing waste liquid, and this photographic processing waste liquid is passed through the sludge filter 5a. is supplied to With this sludge filter 5a, it is possible to take out the filtered concentrate from which water has been removed.

分離手段3には液面検出センサ6が設けられており、こ
の液面検出センサ6て分離手段3内の写真処理廃液の液
量を監視している。循環系1のバイブ4はバイブ7を介
して廃液供給タンク8と接糸売されており、バイブ7に
設けられたベローズポンプ9を駆動して写真処理廃液が
供給される。このベローズポンプ9は液面検出センサ6
からの液面情報によって制御され、循環系1の写真処理
廃液を常に一定量にしている。廃液供給タンク8には液
面検出センサ10が設けられ、写真処理廃液の残量を監
視しており、所定量になると例えは自動的に廃液を供給
したり、或いは運転を停止する。前記分離手段3の上部
には排出バイブ11が接続され、この排出バイブ11か
ら分離されたガスを含む蒸気が排出され、冷却部12を
介して空気室13に導かれる。排出バイブ11の開口部
近傍には邪魔板11aが配置され、循環系1のバイブ4
から供給される液体が飛散して、直接排出されることを
防止している。
The separation means 3 is provided with a liquid level detection sensor 6, and this liquid level detection sensor 6 monitors the amount of photographic processing waste liquid within the separation means 3. The vibrator 4 of the circulation system 1 is connected to a waste liquid supply tank 8 via a vibrator 7, and a bellows pump 9 provided on the vibrator 7 is driven to supply photographic processing waste liquid. This bellows pump 9 has a liquid level detection sensor 6
The photographic processing waste liquid in the circulation system 1 is always kept at a constant amount. A liquid level detection sensor 10 is provided in the waste liquid supply tank 8 to monitor the remaining amount of photographic processing waste liquid, and when a predetermined amount is reached, the waste liquid is automatically supplied or the operation is stopped. A discharge vibrator 11 is connected to the upper part of the separating means 3, and steam containing the separated gas is discharged from the discharge vibrator 11 and guided to an air chamber 13 via a cooling section 12. A baffle plate 11a is arranged near the opening of the discharge vibrator 11, and a baffle plate 11a is arranged near the opening of the discharge vibrator 11, and
This prevents the liquid supplied from scattering and being directly discharged.

冷却部12で冷却されたガスは空気室13でその一部か
凝縮されて凝縮液となり、活性炭14を介して臭気成分
を除去して溜液タンク15内に貯溜される。この溜液タ
ンク15は消臭剤16を介して大気と連通している。
A portion of the gas cooled in the cooling unit 12 is condensed in the air chamber 13 to become a condensate, which removes odor components via activated carbon 14 and is stored in a reservoir tank 15. This reservoir tank 15 communicates with the atmosphere via a deodorizer 16.

空気室13で凝縮液と分離された残りの気体と空気は空
気バイブ17を介してバイブ7と接続されており、この
空気バイブ17に設けられた空気ポンプ18の作動で空
気を循環系1に混入するようになっている。この混入す
る空気量は加熱量に対して0.1〜100IL/kCa
Ilが好ましい。
The remaining gas and air separated from the condensate in the air chamber 13 are connected to the vibe 7 via an air vibe 17, and the air is pumped into the circulation system 1 by the operation of the air pump 18 provided in the air vibe 17. It is designed to be mixed in. The amount of air mixed in is 0.1 to 100 IL/kCa relative to the amount of heating.
Il is preferred.

この空気の混入によって、写真処理廃液の蒸発温度を低
下させて、硫化水素、アンモニアガス等の臭気の発生を
抑制する。
The mixture of air lowers the evaporation temperature of the photographic processing waste liquid and suppresses the generation of odors such as hydrogen sulfide and ammonia gas.

第3図は循環系1の分離手段3に所定量の写真処理廃液
を貯留して、循環系1のバイブ4をこの写真処理廃液の
貯留部の上方に接続しており、加熱手段2はこの貯留部
より下方の位置に配置されている。分離手段3の下方に
は取出手段であるバルブ20が設けられ、分離手段3内
に溜る濃縮物を取り出すことができるようになっている
In FIG. 3, a predetermined amount of photographic processing waste liquid is stored in the separation means 3 of the circulation system 1, and the vibrator 4 of the circulation system 1 is connected above the storage part of this photographic processing waste liquid. It is located below the storage section. A valve 20 serving as a take-out means is provided below the separating means 3, so that the concentrate accumulated in the separating means 3 can be taken out.

排出バイブ11に水流ポンプ21か接続され、循環系1
を減圧にして写真処理廃液の沸騰温度を低下させて臭気
の発生を抑えると共に、排出バイブ11から排出される
ガスに、水槽22からポンプ23によって供給される水
を混合させて、脱臭させている。この水槽22には水道
24から常に水が供給され、オーバーフローバイブ25
から排出される。
A water pump 21 is connected to the discharge vibrator 11, and the circulation system 1
The pressure is reduced to lower the boiling temperature of the photographic processing waste liquid to suppress the generation of odors, and the gas discharged from the discharge vibrator 11 is mixed with water supplied from the water tank 22 by the pump 23 to deodorize it. . Water is constantly supplied to this water tank 22 from a water supply 24, and an overflow vibe 25
is discharged from.

第4図は第3図に示す循環系を廃止して、第1図に示す
循環系を用いたものであり、他の構成は第3図に示すも
のと同一である。
In FIG. 4, the circulation system shown in FIG. 3 is abolished and the circulation system shown in FIG. 1 is used, and the other configuration is the same as that shown in FIG. 3.

[発明の効果] 前記のように、この発明の写真処理廃液の処理装置は、
写真処理廃液を循環系で循環せしめ、この循環系に加熱
手段と、蒸発濃縮によって生じるガスを含む蒸気と写真
処理廃液とを分離する分離手段とを独立に備えるから、
濃縮物を加熱手段で過加熱することがなくなり、濃縮物
の過熱分解を防止でき、硫化水素、アンモニアガス等の
臭気の発生を大幅に抑制することができる。
[Effects of the Invention] As mentioned above, the photographic processing waste liquid processing apparatus of the present invention has the following features:
The photographic processing waste liquid is circulated in a circulation system, and this circulation system is independently equipped with a heating means and a separation means for separating the photographic processing waste liquid from vapor containing gas generated by evaporation concentration.
The concentrate is not overheated by the heating means, the overheated decomposition of the concentrate can be prevented, and the generation of odors such as hydrogen sulfide and ammonia gas can be significantly suppressed.

また、循環系に加熱手段と分離手段とを独立に備えるた
め、それぞれを小型にすることができその分装置が小型
になり、しかも耐熱部分は循環系の加熱手段が備えられ
る部分でよく、耐熱部分を@減でき安価な装置となる。
In addition, since the circulation system is equipped with a heating means and a separation means independently, each can be made smaller, and the equipment can be made smaller accordingly.Moreover, the heat-resistant part can be the part equipped with the heating means of the circulation system, and the heat-resistant The number of parts can be reduced, resulting in an inexpensive device.

また、分離手段に濃縮物を取り出す取出手段を備えると
、濃縮物を排出することができ、濃縮物の過加熱を防止
でき、臭気の発生を抑えることができる。
Furthermore, if the separating means is provided with a take-out means for taking out the concentrate, the concentrate can be discharged, overheating of the concentrate can be prevented, and odor generation can be suppressed.

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

第1図はこの発明の写真処理廃液の処理装置を示す概略
構成図、第2図は加熱手段の他の取付状態を示す図、第
3図及び第4図はこの発明の写真処理廃液の処理装置の
他の実施例を示す概略構成図である。 図面中符号1は循環系、2は加熱手段、3は分離手段、
4はバイブ、5は取出手段である。 第 ↑ 医 つ 溜
FIG. 1 is a schematic configuration diagram showing a processing apparatus for photographic processing waste liquid according to the present invention, FIG. 2 is a diagram showing another installation state of the heating means, and FIGS. 3 and 4 are diagrams showing the processing apparatus for photographic processing waste liquid according to the present invention. FIG. 3 is a schematic configuration diagram showing another embodiment of the device. In the drawings, 1 is a circulation system, 2 is a heating means, 3 is a separation means,
4 is a vibrator, and 5 is a take-out means. No. ↑ Medicine collection

Claims (1)

【特許請求の範囲】 1、写真処理廃液を、加熱手段で加熱して蒸発濃縮せし
める写真処理廃液の処理装置において、前記写真処理廃
液を循環系で循環せしめ、この循環系に前記加熱手段と
、加熱によって生じるガスを含む蒸気と写真処理廃液と
を分離する分離手段とを独立に備えることを特徴とする
写真処理廃液の処理装置。 2、前記分離手段に、写真処理廃液の蒸発濃縮によって
生じる濃縮物を取り出す取出手段を備えることを特徴と
する請求項1記載の写真処理廃液の処理装置。
[Scope of Claims] 1. A processing apparatus for photographic processing waste liquid that heats the photographic processing waste liquid with a heating means to evaporate and concentrate the photographic processing waste liquid, in which the photographic processing waste liquid is circulated in a circulation system, and the heating means is included in the circulation system; A processing apparatus for photographic processing waste liquid, characterized in that it is independently equipped with a separating means for separating the photographic processing waste liquid from steam containing gas generated by heating. 2. The apparatus for processing a photographic processing waste liquid according to claim 1, wherein the separating means includes a taking-out means for taking out a concentrate produced by evaporation and concentration of the photographic processing waste liquid.
JP17067488A 1988-07-08 1988-07-08 Treating device for waste photographic processing liquid Pending JPH0221990A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17067488A JPH0221990A (en) 1988-07-08 1988-07-08 Treating device for waste photographic processing liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17067488A JPH0221990A (en) 1988-07-08 1988-07-08 Treating device for waste photographic processing liquid

Publications (1)

Publication Number Publication Date
JPH0221990A true JPH0221990A (en) 1990-01-24

Family

ID=15909282

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17067488A Pending JPH0221990A (en) 1988-07-08 1988-07-08 Treating device for waste photographic processing liquid

Country Status (1)

Country Link
JP (1) JPH0221990A (en)

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