JPH0422480A - Apparatus for evaporative concentration treatment of waste photographic processing solution - Google Patents
Apparatus for evaporative concentration treatment of waste photographic processing solutionInfo
- Publication number
- JPH0422480A JPH0422480A JP12606590A JP12606590A JPH0422480A JP H0422480 A JPH0422480 A JP H0422480A JP 12606590 A JP12606590 A JP 12606590A JP 12606590 A JP12606590 A JP 12606590A JP H0422480 A JPH0422480 A JP H0422480A
- Authority
- JP
- Japan
- Prior art keywords
- waste liquid
- photographic processing
- column
- processing waste
- optical sensor
- 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
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 65
- 238000012545 processing Methods 0.000 title claims abstract description 58
- 239000007788 liquid Substances 0.000 claims abstract description 85
- 230000003287 optical effect Effects 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 238000001704 evaporation Methods 0.000 claims description 26
- 230000008020 evaporation Effects 0.000 claims description 18
- 239000012780 transparent material Substances 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 21
- 238000001816 cooling Methods 0.000 description 13
- 239000000243 solution Substances 0.000 description 12
- 238000001514 detection method Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 239000003507 refrigerant Substances 0.000 description 7
- 239000010802 sludge Substances 0.000 description 7
- 238000005406 washing Methods 0.000 description 5
- 229910052709 silver Inorganic materials 0.000 description 4
- 239000004332 silver Substances 0.000 description 4
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- XYXNTHIYBIDHGM-UHFFFAOYSA-N ammonium thiosulfate Chemical group [NH4+].[NH4+].[O-]S([O-])(=O)=S XYXNTHIYBIDHGM-UHFFFAOYSA-N 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000010808 liquid waste Substances 0.000 description 1
- 230000005226 mechanical processes and functions Effects 0.000 description 1
- 238000012946 outsourcing Methods 0.000 description 1
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- -1 silver halide Chemical class 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-L sulfite Chemical class [O-]S([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-L 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
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.
一般に、ハロゲン化銀感光材料の写真処理は、発色現像
、漂白定着(又は漂白、定着)、水洗又は安定化処理の
順に行なわれている。Generally, photographic processing of silver halide light-sensitive materials is carried out in the order of color development, bleach-fixing (or bleaching and fixing), and water washing or stabilization processing.
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一方、処理によ
って処理液中に溶出或は蒸発によって濃化する成分(例
えば現像液における具化物イオン、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が処理液に補充され、写真処理に
おける濃厚化成分の除去のために処理液の一部が廃棄さ
れている。In photographic processing in which a large amount of light-sensitive material is processed, the components consumed during the processing are replenished, while the components that are dissolved into the processing solution or concentrated by evaporation (for example, embodied ions in the developer, fixing A method is used to maintain the performance of the processing solution at a constant level by removing substances (such as silver complex salts in the solution) and keeping the processing components constant. A portion of the processing liquid is discarded to remove thickening 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
像機の冷却水等で希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 processing machines, 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
冷却水の下水道や河川への廃棄は可能であるが、これら
以外の写真処理液[例えば、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。しかしながら、廃液処理業者に委託する方法は、
廃液を貯留しておくのにかなりのスペースが必要となる
し、またコスト的にも極めて高価であり、さらに公害処
理設備は初期投資(イニシャルコスト)が極めて大きく
、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。However, due to stricter pollution regulations in recent years, it is possible to dispose of washing water and cooling water into sewers or rivers, but other photographic processing solutions [e.g. developer, fixer, color developer, bleach-fixer] (or bleaching solution, fixing solution), stabilizing solution, etc.] 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 is
A considerable amount of space is required to store the waste liquid, and it is also extremely expensive.Furthermore, the initial investment (initial cost) for pollution treatment equipment is extremely large, and it requires a fairly large space to set up. It has disadvantages such as requiring
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ばかりでなく、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、廃液が店に充満する等の問題を生
じている。Therefore, waste liquid is generally collected by a waste liquid collection company and rendered harmless through secondary and tertiary processing.However, not only is the price of waste liquid collection increasing year by year due to rising collection costs, but 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。ところで、発明者等の研究では写真処理
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。これは写真処理液の定着液や漂白定着液としてよく
用いられるチオ硫酸アンモニウムや亜硫酸塩(アンモニ
ウム塩、ナトリウム塩又はカリウム塩)が高温のため分
解することによって発生することがわかった。更に蒸発
処理時には写真処理廃液中の水分等が蒸気となって気体
化することにより体積が膨張し、蒸発釜中の圧力が増大
する。このためこの圧力によって蒸発処理装置から前記
有害ないし悪臭性のガスが装置外部へもれ出してしまい
、作業環境上極めて好ましくないことが起る。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. It is shown in JP-A No. 60-70841 and the like. By the way, the inventors' research has shown that when photographic processing waste liquid is evaporated, harmful or extremely malodorous gases such as sulfur dioxide gas, hydrogen sulfide, and ammonia gas are generated. It has been found that this is caused by the decomposition of ammonium thiosulfate and sulfites (ammonium salt, sodium salt, or potassium salt), which are commonly used as fixing solutions and bleach-fixing solutions in photographic processing solutions, due to high temperatures. Further, during the evaporation process, moisture and the like in the photographic processing waste liquid becomes vapor and gasifies, thereby expanding the volume and increasing the pressure in the evaporation pot. Therefore, due to this pressure, the harmful or malodorous gas leaks out of the evaporation treatment apparatus to the outside of the apparatus, resulting in an extremely unfavorable working environment.
そこで、これらを解決するために実開昭60−7084
1号には蒸発処理装置の排気管部に活性炭等の排ガス処
理部を設ける方法が開示されている。しかし、この方法
は写真処理廃液中の多量の水分による水蒸気により、排
ガス処理部で結露又は凝結し、ガス吸収処理剤を水分が
覆い、ガス吸収能力を瞬時に失わせてしまう重大な欠点
を有しており、未だ実用には供し得ないものであった。Therefore, in order to solve these problems,
No. 1 discloses a method of providing an exhaust gas treatment section such as activated carbon in the exhaust pipe section of an evaporation treatment device. However, this method has the serious drawback that water vapor from a large amount of water in the photographic processing waste liquid condenses or condenses in the exhaust gas treatment section, covering the gas absorption processing agent and causing it to instantly lose its gas absorption ability. However, it has not yet been put to practical use.
これらの問題点を解決するために、この発明者等は写真
処理廃液を蒸発処理するに際し、蒸発によって生じる蒸
気を凝縮させ、さらに凝縮によって生じる凝縮液を処理
するとともに非凝縮成分についても処理して外部へ放出
する写真処理廃液の濃縮処理装置について先に提案した
。In order to solve these problems, the present inventors condensed the vapor produced by evaporation when processing waste photographic processing liquid by evaporation, and further treated the condensate produced by condensation and also treated non-condensed components. We have previously proposed a device for concentrating photographic processing waste liquid that is discharged to the outside.
しかしなから、この提案によれば、次のような問:吊点
かあることを見いだした。すなわち、蒸発la Jカラ
ム内に規定液面位まで写真廃液を供給する1′二あたり
、正確な液面検出手段を必要とし、さら(ここの液面検
出手段は、カラム内にあると、蒸発濃縮行程に於て、蒸
発を阻害し又は、スラッジのハネ等によってすぐに機械
的な機能が害されるので、カラム内には検出手段の設置
が困liなことが a か ・っ /こ 。However, according to this proposal, we found that there is a hanging point. In other words, an accurate liquid level detection means is required to supply photographic waste liquid up to the specified liquid level in the evaporation column. During the concentration process, it is difficult to install a detection means inside the column because it will inhibit evaporation or the mechanical function will be quickly damaged by sludge splashes, etc.
そこで、カラム外から正しくカラム内の液面位を検出す
る手段を提供することを目的とするものである。Therefore, it is an object of the present invention to provide a means for accurately detecting the liquid level inside a column from outside the column.
その目的は、次の(a)、(b)、(c)、(d)の手
段のいずれか1項によって達成される。The object is achieved by any one of the following means (a), (b), (c), and (d).
(a)加熱部と蒸気凝縮部を連通した蒸発濃縮カラムの
、少なくとも1部を透明部材で構成し、該透明部材で構
成した部分に発光装置と受光装置からなる光センサーを
設け、上記カラム内の写真処理廃液か上記発光装置の光
をさえぎる構造とじた写真処理廃液の蒸発濃縮処理装置
。(a) At least a part of the evaporation concentration column that communicates the heating part and the vapor condensing part is made of a transparent member, and a light sensor consisting of a light emitting device and a light receiving device is provided in the part made of the transparent material, and a light sensor consisting of a light emitting device and a light receiving device is provided inside the column. An apparatus for evaporating and concentrating photographic processing waste liquid, which has a structure that blocks the light of the light emitting device.
(b)該光センサー設置部の写真処理廃液の温度を70
℃以下としたa項記載の写真処理廃液の蒸発濃縮処理装
置。(b) The temperature of the photographic processing waste liquid in the optical sensor installation part is set to 70°C.
An evaporative concentration treatment apparatus for photographic processing waste liquid as described in item a above, wherein the temperature is below ℃.
(c)該光センサー設置したカラム透明部材内側を供給
写真廃液廃液で洗浄する構造としたa%記載の写真処理
廃液の蒸発濃縮処理装置。(c) An apparatus for evaporating and concentrating photographic processing waste liquid as described in a%, having a structure in which the inside of the column transparent member in which the optical sensor is installed is washed with the supplied photographic waste liquid waste liquid.
(d)該光センサーによる信号を、写真処理廃液供給を
停止するための信号として使用するa項記載の写真処理
廃液の蒸発濃縮処理装置。(d) The apparatus for evaporating and concentrating photographic processing waste liquid according to item a, wherein the signal from the optical sensor is used as a signal for stopping the supply of photographic processing waste liquid.
この発明において、蒸発濃縮カラム9とは第1図に示す
如く、上下にそれぞれ室をもち、その2室が連通してい
る容器体であって、下室に加熱手段を設け、ここに写真
処理廃液を供給し、上記加熱手段で加熱することによっ
て、その水分を蒸発せしめる加熱部を形成し、王室に冷
却手段を設け、下室から発生した蒸気を上記連通部を通
して導き、冷却凝縮する蒸気凝縮部を形成している。In the present invention, the evaporative concentration column 9 is a container body having upper and lower chambers and communicating with each other, as shown in FIG. A heating section is formed in which the waste liquid is supplied and heated by the heating means to evaporate its moisture, a cooling means is provided in the royal chamber, and the steam generated from the lower chamber is guided through the communication section to cool and condense it.Steam condensation It forms a part.
二の発明における透明部材で構成する部分は上記下室の
加熱部を形成している部分である。この加熱部の上端で
ない所定の高さまで写真処理廃液を供給し、前記光セン
サーで検出して供給を停止する。この検出用の窓を透明
部材で構成するものである。The portion made of the transparent member in the second invention is a portion forming the heating section of the lower chamber. The photographic processing waste liquid is supplied to a predetermined height that is not the upper end of this heating section, and the supply is stopped when detected by the optical sensor. This detection window is made of a transparent member.
写真処理廃液は70℃をこすと汚れとして器物に付着し
易くなることを本出願人は発見し、上記透明部材で構成
した窓が汚れないように、この窓の中の写真処理廃液の
温度を70℃以下にする構成とし を二 。The applicant has discovered that photographic processing waste liquid tends to adhere to utensils as dirt when heated to 70°C, and the temperature of the photographic processing waste liquid inside the window has been adjusted to prevent the window made of the above-mentioned transparent member from becoming dirty. The temperature should be kept below 70℃.
更に上記窓の汚れをカラム内に供給する写真処理廃液を
もって洗浄する如く、上記供給口を上記窓の内面に向け
て、供給写真廃液を吹き付け、又はふりかける如く構成
するとよい。Furthermore, it is preferable to direct the supply port toward the inner surface of the window and spray or sprinkle the supplied photographic processing waste solution so that dirt on the window can be cleaned with the photographic processing waste solution supplied into the column.
光センサーによる検出は、液面の描れによるハンチング
やハネ等による誤検出を防止するために、検出時間を1
0秒ぐらいにするとよい。Detection using an optical sensor requires a detection time of 1 in order to prevent false detection due to hunting or splashes caused by the liquid level.
It is best to set it to about 0 seconds.
次にこの発明の実施例を図をもって説明する。 Next, embodiments of the present invention will be described with reference to the drawings.
第1図は、実施例の全体構成を説明する断面図である。FIG. 1 is a sectional view illustrating the overall configuration of the embodiment.
水循環ポンプ14を始動すると、容器16からくみ上げ
られた水は、エジェクター15から、勢いよく下方へ吹
き出される。このときエジェクター15でT字状に連結
された気路23は負圧となるから、バルブ】8を開くと
、蒸気凝縮部8及びこれに連通ずる蒸発濃縮カラム(以
下単にカラムということがある)9の気室から、空気が
吸い出され、これら、蒸気凝縮部8及び該カラム9は減
圧される。When the water circulation pump 14 is started, the water pumped up from the container 16 is vigorously blown downward from the ejector 15. At this time, the air passage 23 connected in a T-shape by the ejector 15 becomes under negative pressure, so when the valve 8 is opened, the vapor condensing section 8 and the evaporation concentration column (hereinafter simply referred to as column) connected thereto are opened. Air is sucked out from the air chamber 9, and these, the vapor condensing section 8 and the column 9 are depressurized.
次にバルブ20を開くと上記減圧によって、廃液は容器
19から吸い上げられて、カラム9内の上部に設けられ
たノズル21からカラム9内に散布する。Next, when the valve 20 is opened, the waste liquid is sucked up from the container 19 by the reduced pressure and sprayed into the column 9 through a nozzle 21 provided at the upper part of the column 9.
そしてカラム9内に廃液がたまり液面Aに至ると光セン
サ−22が検知して、バルブ20を閉じさせ注液が止ま
る。バルブ20は電磁弁を用いてもよい。When the waste liquid accumulates in the column 9 and reaches the liquid level A, the optical sensor 22 detects this, closes the valve 20, and stops the liquid injection. The valve 20 may be a solenoid valve.
カラム9の側壁の1部26a及び26b1を透明部材で
構成しこの窓を通して光センサ−22の発光部22aと
、受光部22bを向い合わせに配置し、そしてこの光路
をさえぎらないよう加熱部6の形状を逃がしである。One part 26a and 26b1 of the side wall of the column 9 is made of a transparent material, and the light emitting part 22a and the light receiving part 22b of the optical sensor 22 are arranged facing each other through these windows, and the heating part 6 is arranged so as not to block this optical path. The shape is an escape.
そしてカラム9の側壁の1部26a及び26bの内壁に
向けてノズル21の開口部を設けたから、この部分1−
二供給写真廃液か散布されるので洗浄が行なわれ上記光
センサ−22の光をスランジなどの汚れでさえぎること
がない。廃液の汲上げ手段としてバルブ20のかわりに
ポンプ2OAを用いたものを第2図に示す。Since the opening of the nozzle 21 was provided toward the inner wall of the first part 26a and 26b of the side wall of the column 9, this part 1-
Since the photographic waste liquid is sprayed, cleaning is performed and the light from the optical sensor 22 is not blocked by dirt such as sludge. FIG. 2 shows a system in which a pump 2OA is used instead of the valve 20 as a means for pumping up waste liquid.
第3図に液面位検出部の別の実施例を示した。FIG. 3 shows another embodiment of the liquid level detection section.
即ら、カラム9の側方に規定液面位である液面A以下の
ところで連通ずる管を設けその上部は液面へ以上のとこ
ろにし、更にこの上部に供給写真廃液のノズル21を設
けた。そして液面Aに位置する部分を透明部材で構成し
、図示の如く光センサ−22の発光部22aと受光部2
2bを対向させて設けた。That is, on the side of the column 9, a connecting pipe was provided below the liquid level A, which is the specified liquid level, and the upper part of the pipe was above the liquid level, and a nozzle 21 for supplying photographic waste liquid was installed above this pipe. . The part located at the liquid level A is made of a transparent member, and as shown in the figure, the light emitting part 22a and the light receiving part 2 of the optical sensor 22 are made of a transparent material.
2b were provided facing each other.
この光センサーで検出する液面位は液面Aと等しくしで
あるから、この光センサ−22の液面検出をもって写真
廃液の供給を停止する。Since the liquid level detected by this optical sensor is equal to the liquid level A, the supply of photographic waste liquid is stopped when the optical sensor 22 detects the liquid level.
そしてノズル21から、透明部材26a、 26bに向
けて、供給写真廃液を散布するからこの透明部材の内壁
は洗浄されて、光センサ−22の検出を汚れが妨げるこ
とがない。尚この第2の実施例も、カラム9の側方に突
出した管は特許請求項に言う蒸発製線カラム9の1部を
構成している。Then, since the supplied photographic waste liquid is sprayed from the nozzle 21 toward the transparent members 26a and 26b, the inner walls of the transparent members are cleaned, and the detection by the optical sensor 22 is not hindered by dirt. In this second embodiment as well, the tube projecting to the side of the column 9 constitutes a part of the evaporation wire forming column 9 mentioned in the claims.
次に、ヒートポンプ1を詳しく説明する。ヒートポンプ
1は、コンプレッサー2き、空冷凝m器3と、ファンモ
ーター5により駆動されるプロペラファン4と、加熱部
6と、冷却コイル13と、冷却部7とこれらを連結する
バイブと、この系内に注入した冷媒とよりなる。Next, the heat pump 1 will be explained in detail. The heat pump 1 includes a compressor 2, an air-cooled condenser 3, a propeller fan 4 driven by a fan motor 5, a heating section 6, a cooling coil 13, a cooling section 7, a vibrator connecting these, and this system. It consists of a refrigerant injected into the tank.
コンプレッサー2により圧縮された冷媒は高温となって
空冷凝縮器3に向けて吹き出される。ここで、ファンモ
ーター5で駆動されたプロペラファン4で強制空冷を行
なう。これはヒートポンプの暴走を防止し、かつ、加熱
部6の温度を制御し、高温によるガス発生を防止するた
めに行なわれる。The refrigerant compressed by the compressor 2 reaches a high temperature and is blown out toward the air-cooled condenser 3. Here, forced air cooling is performed using a propeller fan 4 driven by a fan motor 5. This is done in order to prevent the heat pump from running out of control, control the temperature of the heating section 6, and prevent gas generation due to high temperatures.
次に上記強制空冷によって適温になった冷媒は加熱部6
に入る。加熱部6はカラム9に注入した廃液の液面A以
下の部分に連続して液面上にも配設し、それぞれ液面A
以下の部分では廃液を加熱し、液面上の部分では、発生
した蒸気を加熱する。Next, the refrigerant that has reached an appropriate temperature due to the forced air cooling is heated to a heating section 6.
to go into. The heating unit 6 is also disposed continuously above the liquid level of the waste liquid injected into the column 9 below the liquid level A.
The part below heats the waste liquid, and the part above the liquid surface heats the generated steam.
そして加熱部6を通過した冷媒はドライヤー111キヤ
ピラリーチユーブlOを通って冷却コイル13に入って
、容器16に注入された水を冷却したのち、冷却部7に
入る。ここで、カラム9から蒸発してきた蒸気を冷却し
てのち、上記冷媒はコンプレッサー2に戻りlサイクル
を完了し、このサイクルを繰り返し行なう。The refrigerant that has passed through the heating section 6 passes through the dryer 111 and the capillary reach tube 10, enters the cooling coil 13, cools the water injected into the container 16, and then enters the cooling section 7. After cooling the vapor evaporated from the column 9, the refrigerant returns to the compressor 2 to complete one cycle, and this cycle is repeated.
この構成の特徴は、減圧手段として水循環ポンプによる
水の吹き出し力を活用し、その水を、ヒートポンプの冷
媒で冷却して使用していること、及び廃液の加熱蒸発を
行なう熱源にヒートポンプの加熱部(凝縮器)を使用し
、かつ、液面下だけでなく、液面上での蒸気加熱をも行
なうことにより、蒸発蒸気の上方への移動を早めて、蒸
発効率を大幅に向上したことである。The features of this configuration are that the water blowing force of the water circulation pump is used as a pressure reduction means, and the water is cooled with the heat pump's refrigerant. By using a condenser (condenser) and heating the steam not only below the liquid level but also above the liquid level, the upward movement of evaporated steam is accelerated and evaporation efficiency is greatly improved. be.
さらに効率設計として、カラム9を上記減圧したことで
、バルブ2oを開けば、廃液を送液ポンプなしでくみ上
げてカラム9内に入れこむ構成としたから効率化及びコ
ンパクト化に効果的である。Furthermore, as an efficiency design, by reducing the pressure in the column 9 as described above, by opening the valve 2o, the waste liquid is pumped up and put into the column 9 without a liquid pump, which is effective for efficiency and compactness.
上記の構成で減圧下で加熱蒸発が行なわれると、カラム
9の廃液面からは、廃液が上方へ、勢いよくはね上がる
現象が起るので、これが冷却部7に入りこむのを防止す
るため、ハネ防止板24を設けlこ 。When heating evaporation is carried out under reduced pressure with the above configuration, a phenomenon occurs in which the waste liquid violently splashes upward from the waste liquid surface of the column 9. To prevent this from entering the cooling section 7, a splash prevention is performed. A plate 24 is provided.
発生した水蒸気は、冷却部7で冷却凝縮され水滴として
、蒸気凝縮部8の底部8Cにたまるが、減圧手段により
バルブI8を通って、容器I6に排出される。そして、
容器16にはオーバーフロー口を設け、上記凝縮水であ
ふれた水はパイプ36によって凝縮水タンク35へと流
入し回収される。The generated water vapor is cooled and condensed in the cooling section 7 and accumulated as water droplets at the bottom 8C of the steam condensing section 8, but is discharged into the container I6 through the valve I8 by the pressure reducing means. and,
The container 16 is provided with an overflow port, and the water overflowing with the condensed water flows into the condensed water tank 35 through a pipe 36 and is collected.
このように蒸発濃縮が進み、廃液がスラッジ化すると、
上記のような冷熱サイクルのバランスが急にくずれると
ころがあって、それは、コンプレッサー2の圧縮後の出
口に於ける冷媒温度が100℃から120℃に急変する
ことで検出される。そこで、この温度変化を温度センサ
ーをもって検出することによって、廃液のスラッジ化検
出として、コンプレッサー2を止め、水循環ポンプ14
を止める。As evaporation concentration progresses and the waste liquid becomes sludge,
There is a point where the balance of the cooling/heating cycle as described above suddenly collapses, and this is detected when the refrigerant temperature at the outlet of the compressor 2 after compression suddenly changes from 100°C to 120°C. Therefore, by detecting this temperature change with a temperature sensor, the compressor 2 is stopped and the water circulation pump 14 is stopped to detect that the waste liquid has turned into sludge.
stop.
このとき、容器16が大気圧に開口しているため、容器
16内の水が蒸気凝縮部8の減圧状態により、気路23
を通って吸いこまれてしまうから、これを防止するため
に、バルブ18を三方弁として、上記停止時には気路2
3側を閉じて、大気に通じる開口を開く如くしている。At this time, since the container 16 is open to atmospheric pressure, the water in the container 16 is reduced to the air passage 23 due to the reduced pressure state of the steam condensing section 8.
In order to prevent this, the valve 18 is designed as a three-way valve so that the air passage 2 is inhaled when the valve is stopped.
The third side is closed, leaving an opening to the atmosphere.
但し三方弁でなくても、気路23に大気に通じる開口を
開閉する電磁弁等を設けて、これを開口し、上記停止と
同時に大気圧でバランスさせてもよい。However, instead of a three-way valve, an electromagnetic valve or the like for opening and closing an opening communicating with the atmosphere may be provided in the air passage 23, and this may be opened and balanced at atmospheric pressure at the same time as the above-mentioned stop.
しかるのち、カラム9の下部のバルブ25を開いて、ス
ラッジを排出する。ここで回収されたスラッジは銀を高
濃度で含むから、有価資源として密封容器にいれ、別途
銀回収をおこなった上で適当な所へ廃棄する。Thereafter, the valve 25 at the bottom of the column 9 is opened to discharge the sludge. The sludge collected here contains a high concentration of silver, so it is stored in a sealed container as a valuable resource, and the silver is collected separately before being disposed of in an appropriate location.
なお、この装置による濃縮度は、総合廃液で18〜20
倍まで濃縮でき、スラッジ化率は外見上98%である。In addition, the concentration level with this device is 18 to 20 in total waste liquid.
It can be concentrated up to twice as much, and the sludge conversion rate is apparently 98%.
このように構成したから、写真処理廃液の蒸発濃縮処理
装置に写真処理廃液を規定の液面位まで供給し、つねに
正確に規定液面位で供給を停止することができる。With this structure, it is possible to supply photographic processing waste liquid to the evaporation concentration processing apparatus for photographic processing waste liquid up to a specified liquid level, and to always stop the supply accurately at the specified liquid level.
第1図は実施例の断面図。
第2図、tiJ3図は別の実施例の部分断面図。
1・・・ヒートポンプ 2・・・コンプレッサー3・
・・空冷凝縮器 4・・・プロペラファン5・・・
ファンヒーター 6・・・加熱部(凝縮器)7・・・冷
却部(蒸発器) 8・・・蒸気凝縮部9・・・蒸発濃縮
カラム(カラム)
10・・・キャピラリーチューブ
11・・・ドライヤー 13・・・冷却コイル14
・・・水循環ポンプ I5・・・エジェクター16・
・・容器 17・・・減圧手段18・・・バ
ルブ 19・・・容器20・・・バルブ
21・・・ノズル22・・・光センサ−22a・・
・発光部22b・・・受光部 23・・・気路2
4・・・ハネ防止板 25・・・バルブ26a、2
6b・・・透明部材FIG. 1 is a sectional view of the embodiment. FIG. 2 and tiJ3 are partial cross-sectional views of another embodiment. 1...Heat pump 2...Compressor 3.
...Air-cooled condenser 4...Propeller fan 5...
Fan heater 6... Heating section (condenser) 7... Cooling section (evaporator) 8... Vapor condensing section 9... Evaporation concentration column (column) 10... Capillary tube 11... Dryer 13...Cooling coil 14
...Water circulation pump I5...Ejector 16.
... Container 17 ... Pressure reducing means 18 ... Valve 19 ... Container 20 ... Valve
21... Nozzle 22... Optical sensor-22a...
- Light emitting part 22b... Light receiving part 23... Airway 2
4...Splash prevention plate 25...Valve 26a, 2
6b...Transparent member
Claims (4)
、少なくとも1部を透明部材で構成し、該透明部材で構
成した部分に発光装置と受光装置からなる光センサーを
設け、上記カラム内の写真処理廃液が上記発光装置の光
をさえぎる構造とした写真処理廃液の蒸発濃縮処理装置
。(1) At least a part of the evaporation concentration column that communicates the heating part and the vapor condensing part is made of a transparent member, and a light sensor consisting of a light emitting device and a light receiving device is provided in the part made of the transparent material, An apparatus for evaporating and concentrating photographic processing waste liquid, having a structure in which the photographic processing waste liquid blocks light from the light emitting device.
℃以下とした請求項1記載の写真処理廃液の蒸発濃縮処
理装置。(2) Set the temperature of the photographic processing waste liquid in the optical sensor installation part to 70.
2. The apparatus for evaporating and concentrating photographic processing waste liquid according to claim 1, wherein the temperature is below .degree.
給写真処理廃液で洗浄する構造とした請求項1記載の写
真処理廃液の蒸発濃縮処理装置。(3) The apparatus for evaporating and concentrating photographic processing waste liquid according to claim 1, wherein the inside of the column transparent member in which the optical sensor is installed is constructed to be washed with the supplied photographic processing waste liquid.
停止するための信号として使用する請求項1記載の写真
処理廃液の蒸発濃縮処理装置。(4) The apparatus for evaporating and concentrating photographic processing waste liquid according to claim 1, wherein the signal from the optical sensor is used as a signal for stopping the supply of photographic processing waste liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12606590A JPH0422480A (en) | 1990-05-16 | 1990-05-16 | Apparatus for evaporative concentration treatment of waste photographic processing solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12606590A JPH0422480A (en) | 1990-05-16 | 1990-05-16 | Apparatus for evaporative concentration treatment of waste photographic processing solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0422480A true JPH0422480A (en) | 1992-01-27 |
Family
ID=14925757
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12606590A Pending JPH0422480A (en) | 1990-05-16 | 1990-05-16 | Apparatus for evaporative concentration treatment of waste photographic processing solution |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0422480A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2020054959A (en) * | 2018-10-02 | 2020-04-09 | 前田 和幸 | Separator of mixture in liquid |
-
1990
- 1990-05-16 JP JP12606590A patent/JPH0422480A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2020054959A (en) * | 2018-10-02 | 2020-04-09 | 前田 和幸 | Separator of mixture in liquid |
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