JPH03229688A - Method for evaporative concentration of waste photographic processing solution and defoaming agent added to same waste solution - Google Patents
Method for evaporative concentration of waste photographic processing solution and defoaming agent added to same waste solutionInfo
- Publication number
- JPH03229688A JPH03229688A JP2273390A JP2273390A JPH03229688A JP H03229688 A JPH03229688 A JP H03229688A JP 2273390 A JP2273390 A JP 2273390A JP 2273390 A JP2273390 A JP 2273390A JP H03229688 A JPH03229688 A JP H03229688A
- Authority
- JP
- Japan
- Prior art keywords
- photographic processing
- waste
- solution
- waste liquid
- processing waste
- 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 52
- 238000000034 method Methods 0.000 title claims abstract description 22
- 239000002518 antifoaming agent Substances 0.000 title claims abstract description 16
- 239000007788 liquid Substances 0.000 claims abstract description 49
- 238000010438 heat treatment Methods 0.000 claims abstract description 14
- 229920001296 polysiloxane Polymers 0.000 claims abstract description 4
- 238000001704 evaporation Methods 0.000 claims description 15
- 239000000243 solution Substances 0.000 abstract description 10
- 238000002347 injection Methods 0.000 abstract description 3
- 239000007924 injection Substances 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 239000007789 gas Substances 0.000 description 11
- 230000008020 evaporation Effects 0.000 description 8
- 239000000463 material Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 3
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- GGCZERPQGJTIQP-UHFFFAOYSA-N sodium;9,10-dioxoanthracene-2-sulfonic acid Chemical compound [Na+].C1=CC=C2C(=O)C3=CC(S(=O)(=O)O)=CC=C3C(=O)C2=C1 GGCZERPQGJTIQP-UHFFFAOYSA-N 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
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- XYXNTHIYBIDHGM-UHFFFAOYSA-N ammonium thiosulfate Chemical compound [NH4+].[NH4+].[O-]S([O-])(=O)=S XYXNTHIYBIDHGM-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、写真処理廃液を蒸発濃縮によって、水分を効
率よく取り除き、廃棄に関わる分量の減少と、不快なガ
スを発生させないための処理技術に関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a processing technology for efficiently removing moisture from photographic processing waste liquid by evaporation concentration, reducing the amount of waste involved in disposal, and preventing the generation of unpleasant gases. Regarding.
写真処理廃液は、銀塩感光材料を現像処理するために使
用した写真処理液の老廃物であり、これには、もとより
調合した化学成分に加え、銀塩感光材料より溶出した成
分や、化学反応生成物が含まれるため、写真処理に悪影
響するから写真処理を良好に持続するためには、処理し
た感光材料の量に応じて新液補充によって、その性能を
補い、不要の汚染成分が含まれ老化した液を廃棄する。Photographic processing waste liquid is a waste product of the photographic processing liquid used to develop silver salt photosensitive materials.In addition to the chemical components prepared from the beginning, it also contains components eluted from the silver salt photosensitive materials and chemical reactions. Because it contains products, it has a negative effect on photographic processing.In order to maintain good photographic processing, it is necessary to replenish the new solution according to the amount of processed light-sensitive material to compensate for its performance and eliminate unnecessary contaminating components. Discard aged liquid.
これが写真処理廃液である。そしてその廃棄量は、写真
処理の種類によって異なるけれども、例を挙げるならば
0.03CC/am2のものもある。This is photographic processing waste liquid. The amount of waste varies depending on the type of photographic processing, but for example, it can be as much as 0.03 CC/am2.
ここでは、処理する感光材料の面積に対する液量で示し
た。従って、業として写真処理を多量に、継続的に行な
う場合に、発生する写真処理廃液は多量で、これを回収
業者に依頼して無害化してもらう迄の保管場所にも困る
ような状況であった。Here, the amount of liquid is expressed in terms of the area of the photosensitive material to be processed. Therefore, when a large amount of photographic processing is carried out continuously as a business, a large amount of photographic processing waste is generated, and it is difficult to find a place to store it until a collection company is asked to detoxify it. Ta.
回収業者は電解法等の手段で写真処理廃液に含まれる銀
を回収したり、無公害化処理を施しているが、これら回
収にはコストが多大にかかるため、何とか、写真処理廃
液を減らそうという工夫や無公害化の工夫かなされてき
た。活性汚泥法、蒸発法電解酸化法逆浸透法、化学処理
法等か知られているか、これらは未だ効率か良くなく、
コスト高で、広く需要に応えるものではなかった。Collection companies use methods such as electrolysis to recover the silver contained in photographic processing waste liquid, or treat it to make it non-polluting, but these recovery methods are very costly, so we are trying to somehow reduce the amount of photographic processing waste liquid. Efforts have been made to make the area pollution-free. Are there any known methods such as activated sludge method, evaporation method, electrolytic oxidation method, reverse osmosis method, chemical treatment method, etc., but these methods are still not efficient;
It was expensive and did not meet widespread demand.
写真処理廃液から水分を分離し、無害な水を投棄してし
まえは、残る固形成分は少ないから、その上、回収処理
の点で有利であるから、近年、蒸発濃縮方法で、水分を
除去する工夫か数多くなされている。しかし、問題は、
写真処理廃液を加熱蒸発したときに水分の蒸発だけでな
く、不快なガスか発生するから、安易に既存の蒸留手段
で、水分を除去することは出来ないことである。そのた
め、カス対策等を施した大かがすな装置が必要となるか
ら、コ、スト及び管理面からして、大規模な処理業者に
設置することか考えられ、求められていた、簡便化、省
スペース省コストのねらいからは外れてしまうものであ
る。If the water is separated from the photographic processing waste and the harmless water is dumped, there will be less solid components remaining, and it is also advantageous in terms of recovery processing, so in recent years, water has been removed using the evaporation concentration method. Many improvements have been made. But the problem is,
When photographic processing waste liquid is heated and evaporated, not only water evaporates, but also unpleasant gases are generated, so water cannot be easily removed using existing distillation means. Therefore, large-scale equipment with waste countermeasures is required, so from the cost, cost, and management standpoint, it is considered that large-scale processing companies should install it, and the simplification that was required. This deviates from the aim of saving space and cost.
写真処理廃液は自然界に投棄するには公害負荷か高くて
許されない。しかし、写真処理廃液の発生量は多く比較
的小規模の写真処理業者でも一日にIOリットル程度は
発生し、その保管場所の確保と廃液処理業者への支払い
も多額になっている。It is not permissible to dump photographic processing waste into nature due to its high pollution burden. However, the amount of photographic processing waste liquid generated is large, and even a relatively small-scale photographic processing company generates about IO liters per day, and the cost of securing storage space and paying the waste liquid processing company is large.
そこで写真処理廃液が発生するすぐその近くで容易に減
量が出来る方法か切望されていた。写真処理廃液を減量
する手段として、含有水分を分離し、除去する手段があ
り、その具体的方法として、蒸発濃縮方法がある。一般
に写真処理液は1リットル当り70g程度の塩類が含ま
れるだけで残りは水分であって、写真処理廃液であって
も大きな相違まないから、この水分を除去できれば、上
記のごとき保管場所の問題はなくなる。但し写真処理廃
液から、完全に水分を取り除くまで蒸発濃縮するには、
多大のエネルギーを必要とし、むしろ経済的でないこと
はいうまでもない。一方、−船釣に蒸発処理を適用する
には写真処理廃液の場合は不快なカス発生または有害ガ
スの発生かあり、かなりの工夫を巳なけれは実用化して
はならない。即ち、亜硫酸ガス、硫化水素、アンモニア
ガス等の有害ないしは悪臭性のカスが発生する。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、
ナトリウム塩またはカリウム塩)か高温で分解すること
によって発生するのであって、これをヒントにして対策
を構ずれはよい。Therefore, there was a strong need for a method that could easily reduce the amount of photographic processing waste immediately close to where it is generated. As a means of reducing the amount of photographic processing waste liquid, there is a means of separating and removing the water content, and a specific method thereof is evaporation concentration method. Generally, photographic processing solutions only contain about 70g of salts per liter, and the rest is water, and there is no big difference even if it is photographic processing waste, so if this water can be removed, there will be no problem with the storage location mentioned above. will disappear. However, in order to evaporate and concentrate until the water is completely removed from photographic processing waste liquid,
Needless to say, this requires a large amount of energy and is rather uneconomical. On the other hand, when applying evaporation treatment to boat fishing, in the case of photographic processing waste liquid, unpleasant scum or harmful gases are generated, so that it cannot be put to practical use without considerable ingenuity. That is, harmful or malodorous residues such as sulfur dioxide gas, hydrogen sulfide, and ammonia gas are generated. Ammonium thiosulfate and sulfite (ammonium salt,
It is caused by the decomposition of salts (sodium salts or potassium salts) at high temperatures, so it is a good idea to take countermeasures based on this.
本発明は、上記のような従来技術に鑑み、写真処理廃液
を蒸発濃縮するに際し、ガス発生を抑止した、蒸発濃縮
方法を提供することを目的とするものである。SUMMARY OF THE INVENTION In view of the above-mentioned prior art, it is an object of the present invention to provide an evaporative concentration method that suppresses gas generation when evaporating and concentrating photographic processing waste liquid.
この目的は、減圧手段を接続して、写真処理廃液を減圧
状態で加熱蒸発して濃縮するに当たり、該写真処理廃液
に消泡剤を添加する事により不快なカス発生をなくシ、
たことを特徴とする写真処理廃液の蒸発濃縮方法又は減
圧手段を接続して写真処理廃液を減圧状態で加熱蒸発し
て濃縮するに当たり、不快なカス発生をなくすために該
写真処理廃液中に添加するシリコン系消泡剤によって達
成される。The purpose of this is to eliminate the generation of unpleasant scum by adding an antifoaming agent to the photographic processing waste liquid when the photographic processing waste liquid is heated and evaporated and concentrated under reduced pressure by connecting a pressure reduction means.
A method for evaporating and concentrating photographic processing waste liquid characterized by the following: or when the photographic processing waste liquid is concentrated by heating and evaporating under reduced pressure by connecting a depressurizing means, the method is added to the photographic processing waste liquid in order to eliminate the generation of unpleasant scum. This is achieved by using a silicone antifoaming agent.
この発明に於て、減圧手段とは例えは真空ポンプで、有
限の空間から気体を吸い出し続ける能力を持ち、該有限
の空間内の気体圧力を、外の大気圧より低くするもので
ある。この発明に於いては該有限の空間として、写真処
理廃液の蒸発濃縮のためのハウジングを当て、そして減
圧する気体圧力値は、写真処理廃液の加熱蒸発に際して
、水分の蒸発を許し、不快又は有害のカス気泡の発生を
抑える範囲に設定するものてあり、この実施例では30
〜60mmHgで良好な結果を得ている。In this invention, the pressure reducing means is, for example, a vacuum pump, which has the ability to continuously suck out gas from a finite space, and makes the gas pressure within the finite space lower than the outside atmospheric pressure. In this invention, a housing for evaporative concentration of photographic processing waste liquid is applied as the limited space, and the gas pressure value to be reduced allows moisture to evaporate during heating and evaporation of photographic processing waste liquid, causing unpleasant or harmful This is set to a range that suppresses the generation of dust bubbles, and in this example, the range is set to 30.
Good results have been obtained at ~60 mmHg.
さらに、発生する水蒸気は、体積膨張か大きいため、上
記減圧状態をすぐ崩してしまうから、上記減圧手段の能
力を大きく取り、水蒸気により発生する圧力増分をすぐ
に吸収して、該ハウジング内の気体圧力を規定値に保つ
ように、圧力計を設けてチエ7りし、減圧手段の運転を
制御する如くした。次ぎに減圧状態で加熱蒸発させる理
由は、減圧状態では液体の沸点が下がることが知られて
おり、特に低い温度での水分の蒸発を早めるために効果
か大きいことに加え、この低温か前記の不快または有害
カスの発生しない温度域であることか大きい理由である
。しかしながら減圧状態で写真処理廃液を加熱手段に触
れさせて熱伝達し、蒸発濃縮を行なう構成に於いては加
熱手段表面に触れた写真処理廃液中にカス気泡か発生す
ることがあり、これを防ぐこともガス対策として必要と
なった。そこでこの発明では、消泡剤を添加して減圧状
態で写真処理廃液を蒸発濃縮する如くした。Furthermore, the generated water vapor has a large volumetric expansion and will quickly break the reduced pressure state. Therefore, the capacity of the pressure reducing means is increased to immediately absorb the pressure increase generated by the water vapor, and the gas inside the housing is In order to maintain the pressure at a specified value, a pressure gauge was provided to control the operation of the pressure reducing means. Next, the reason for heating and evaporating in a reduced pressure state is that it is known that the boiling point of a liquid is lowered in a reduced pressure state, and it is particularly effective in accelerating the evaporation of water at low temperatures. The main reason for this is that the temperature range does not generate unpleasant or harmful residue. However, in a configuration in which the photographic processing waste liquid is brought into contact with a heating means under reduced pressure to transfer heat and perform evaporative concentration, dregs bubbles may be generated in the photographic processing waste liquid that touches the surface of the heating means, and this should be prevented. This also became necessary as a gas countermeasure. Therefore, in this invention, an antifoaming agent is added and the photographic processing waste liquid is evaporated and concentrated under reduced pressure.
蒸発濃縮の進行にともなって、気泡の発生状況か変化す
るから、その変化に合わせて、該消泡剤の添加量または
添加するタイミングを制御してもよい。この消泡剤とし
て、実施例では下記の化学式で示すようなノリコン系消
泡剤を使用した。As the evaporation concentration progresses, the state of bubble generation changes, so the amount or timing of addition of the antifoaming agent may be controlled in accordance with the change. As this antifoaming agent, a Noricon type antifoaming agent as shown by the following chemical formula was used in the examples.
その添加量は好ましくは0.001g#2〜lOg/(
2,更に好ましくは0.O1g/ff −1gIQであ
る。この消泡剤の入手は、ダウコーニング社、信越シリ
コーン社、(・−レンリコーン社、日本ユニカー社より
できる。The amount added is preferably 0.001g#2~lOg/(
2, more preferably 0. O1g/ff -1gIQ. This antifoaming agent can be obtained from Dow Corning Co., Shin-Etsu Silicone Co., Ltd., Renricorn Co., Ltd., and Nippon Unicar Co., Ltd.
消泡剤は上記に限定するものではなく各処理液に適合し
、上記理由でガス気泡発生を抑止するものであれはよい
。The antifoaming agent is not limited to those mentioned above, but any antifoaming agent may be used as long as it is compatible with each treatment liquid and suppresses the generation of gas bubbles for the above reasons.
第1図に、この発明の方法を用いたl実施例の写真処理
廃液の蒸発濃縮装置の模式図を示す。FIG. 1 shows a schematic diagram of an evaporative concentration apparatus for photographic processing waste liquid according to an embodiment using the method of the present invention.
第1図においてハウジング1内には、加熱手段2か立体
的に配置され、注入口Pから供給された写真処理廃液の
液面位Aをまたいで、液溜部4の液中と液外に存在する
。そして給送手段3によって汲み上げられた液は吐出口
Rから加熱手段2に向かって噴出する。また、ハウジン
グlの上部分には、冷却手段8を配設した水分を凝縮す
る部分5が形成され、またこのハウジングlには吸引ポ
ンプ6を設けた減圧装置7が接続され、ハウジング)内
な減圧し、30〜59mmHgに保つ。In FIG. 1, a heating means 2 is arranged three-dimensionally in the housing 1, and extends over the liquid level A of the photographic processing waste liquid supplied from the inlet P, into and out of the liquid reservoir 4. exist. The liquid pumped up by the feeding means 3 is ejected from the discharge port R toward the heating means 2. In addition, a portion 5 for condensing moisture provided with a cooling means 8 is formed in the upper portion of the housing l, and a pressure reducing device 7 provided with a suction pump 6 is connected to the housing l. Apply vacuum and maintain at 30-59 mmHg.
この状態で、加熱手段2で温められた、写真処理廃液か
らは活発な水蒸気が発生し、蒸発濃縮が進められるか、
同時に液中から気泡が発生し易くなる。気泡か発生する
と、上記加熱手段の表面に該写真処理液か触れない部分
か出来て、当該部分の冷却かなされないから、部分的に
表面温度か、規定値を越すから次に触れた写真処理廃液
を加熱分解してカス発生させることになる。この現象を
防止するために消泡剤を注入口Qから該写真処理廃液に
供給する如くした。In this state, active water vapor is generated from the photographic processing waste liquid heated by the heating means 2, and evaporation and concentration proceed.
At the same time, bubbles are likely to be generated from the liquid. When bubbles are generated, there is a part on the surface of the heating means that does not touch the photographic processing liquid, and this part is not cooled, so the surface temperature of the part exceeds the specified value, so the photographic processing waste liquid that comes into contact with it next. will be thermally decomposed and generate scum. In order to prevent this phenomenon, an antifoaming agent was supplied from the injection port Q to the photographic processing waste liquid.
このように構成したから、写真処理廃液の蒸発濃縮に際
し、カス発生を抑止した蒸発濃縮方法及び該廃液中に添
加する消泡剤を提供できるものである。従って、写真処
理廃液か発生する装置のすく近くで容易に濃縮減量が出
来るコンパクトな装置を実用化できる。With this structure, it is possible to provide an evaporative concentration method that suppresses the generation of scum during evaporative concentration of photographic processing waste liquid, and an antifoaming agent to be added to the waste liquid. Therefore, it is possible to put into practical use a compact device that can easily concentrate and reduce the amount of photographic processing waste close to the device that generates it.
第1図は本発明の方法を用いた装置の模式図である。
■・・ハウジング 2・・・加熱手段3・・液給送
手段 4・・・液溜部5・・・水分を凝縮する部分
・吸弓
ボ
フ
7・・・減圧装置FIG. 1 is a schematic diagram of an apparatus using the method of the present invention. ■...Housing 2...Heating means 3...Liquid feeding means 4...Liquid reservoir 5...Part that condenses moisture/Suction bow 7...Pressure reduction device
Claims (2)
加熱蒸発して濃縮するに当たり、該写真処理廃液に消泡
剤を添加する事により不快なガス発生をなくしたことを
特徴とする写真処理廃液の蒸発濃縮方法。(1) A defoaming agent is added to the photographic processing waste liquid when the photographic processing waste liquid is heated to evaporate and concentrated under reduced pressure by connecting a pressure reduction means, thereby eliminating unpleasant gas generation. Method for evaporating and concentrating photographic processing waste liquid.
熱蒸発して濃縮するに当たり、不快なガス発生をなくす
ために該写真処理廃液中に添加するシリコン系消泡剤。(2) A silicone antifoaming agent that is added to the photographic processing waste liquid in order to eliminate the generation of unpleasant gas when the photographic processing waste liquid is concentrated by heating and evaporating under reduced pressure by connecting a pressure reducing means.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2273390A JPH03229688A (en) | 1990-01-31 | 1990-01-31 | Method for evaporative concentration of waste photographic processing solution and defoaming agent added to same waste solution |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2273390A JPH03229688A (en) | 1990-01-31 | 1990-01-31 | Method for evaporative concentration of waste photographic processing solution and defoaming agent added to same waste solution |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03229688A true JPH03229688A (en) | 1991-10-11 |
Family
ID=12090938
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2273390A Pending JPH03229688A (en) | 1990-01-31 | 1990-01-31 | Method for evaporative concentration of waste photographic processing solution and defoaming agent added to same waste solution |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03229688A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0573927A1 (en) * | 1992-06-12 | 1993-12-15 | Konica Corporation | Recycling method for photographic processing waste liquid |
JPH06134444A (en) * | 1992-10-27 | 1994-05-17 | Toshiba Corp | Method and apparatus for regenerating cleaning drainage and method and apparatus for cleaning |
EP0610505A1 (en) * | 1991-10-28 | 1994-08-17 | Kabushiki Kaisha Toshiba | Wash waste liquid regenerating method, wash waste liquid regenerating apparatus, washing method and washing apparatus |
-
1990
- 1990-01-31 JP JP2273390A patent/JPH03229688A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0610505A1 (en) * | 1991-10-28 | 1994-08-17 | Kabushiki Kaisha Toshiba | Wash waste liquid regenerating method, wash waste liquid regenerating apparatus, washing method and washing apparatus |
EP0610505A4 (en) * | 1991-10-28 | 1994-11-09 | Toshiba Kk | Wash waste liquid regenerating method, wash waste liquid regenerating apparatus, washing method and washing apparatus. |
EP0573927A1 (en) * | 1992-06-12 | 1993-12-15 | Konica Corporation | Recycling method for photographic processing waste liquid |
JPH06134444A (en) * | 1992-10-27 | 1994-05-17 | Toshiba Corp | Method and apparatus for regenerating cleaning drainage and method and apparatus for cleaning |
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