Process for processing photographic baths from color processes
    92.
    发明授权
    Process for processing photographic baths from color processes 失效
    从彩色工艺处理照相浴的工艺

    公开(公告)号:US5783374A

    公开(公告)日:1998-07-21

    申请号:US857676

    申请日:1997-05-16

    申请人: Roger Noero

    发明人: Roger Noero

    摘要: A process for the processing of spent photographic baths from color processes, namely bleaching or fixing baths with a preponderant content of amonium-Fe-EDTA (ethylene diamine tetraacetic acid) as the sequestering agent, fixing baths with a preponderant content of thiosulphates, particularly ammonium thiosulphate and optionally sodium thiosulphate, and developing baths with a preponderant content of sulfate, particularly sodium sulfite is proposed, which is characterized in that, following the deposition of the silver contained in the baths, the multipart starting solution is adjusted to a pH of approximately 13.5 to 14 using NaOH and the Fe(OH).sub.3 obtained after Fe complex decomposition is separated, the remaining, first intermediate solution is adjusted to a pH of 10 by adding acid and the resulting ammonia is separated, the remaining, second intermediate solution is brought to a pH of approximately 0.5 with concentrated HCl, the thiosulphates being decomposed into elementary sulphur and sulphurous acid and the sulphur is separated, the remaining, third intermediate solution is raised to a pH of approximately 1.5 with inorganic liquor and the crystallizing out EDTA is drawn off, the residual solution mixed with developing baths is raised to pH-3 and the sulfate contained therein is transformed into SO.sub.2, which is separated.

    摘要翻译: 用于处理来自彩色工艺的废照相浴的方法,即漂白或固定浴,其中主要含量为钚-Fe-EDTA(乙二胺四乙酸)作为螯合剂,固定具有优势含量的硫代硫酸盐,特别是铵 提出了硫代硫酸盐和任选的硫代硫酸钠,并且提出了具有优势含量的硫酸盐,特别是亚硫酸钠的显影浴,其特征在于,在浴中包含的银沉积之后,将多部分起始溶液调节至大约的pH 使用NaOH进行13.5〜14℃,分离Fe络合物分解后得到的Fe(OH)3,通过加入酸将剩余的第一中间溶液调节至pH为10,分离得到的氨,剩余的第二中间溶液为 用浓HCl使pH达到约0.5,硫代硫酸盐分解成元素硫 和亚硫酸,硫分离,剩余的第三中间溶液用无机液体升至约1.5的pH,并将EDTA结晶除去,将与显影浴混合的残余溶液升至pH-3, 其中所含的硫酸盐转化为SO2,分离。

    Methods for removing silver from spent photoprocessing solution
    93.
    发明授权
    Methods for removing silver from spent photoprocessing solution 失效
    从废光处理溶液中除银的方法

    公开(公告)号:US5695645A

    公开(公告)日:1997-12-09

    申请号:US649415

    申请日:1996-05-16

    摘要: Spent solutions from photographic processors are fed into a conduit (18) to which subsequently are added precipitating agents from a first source (22) and flocculating agents from a second source (28); so that, well grown or ripened clumps of flocculated solids are formed along the conduit before being emptied into a gravity collecting vessel and shipping container (38) from which clarified liquids are displaced by a mass (50) of accumulated flocculated solids, typically through a filter (58, 142, 150, 158, 162, 166, 220)for removal of any unsettled fines. Many of the clumps of flocculated solids become enlarged enough to individually extend across and substantially fill a cross-sectional area of the conduit. As a result, the enlarged clumps substantially block passage of and strain from the solution remaining fine particles which then adhere to the clumps.

    摘要翻译: 来自摄影处理器的废液被加入导管(18)中,随后从第一源(22)和第二源(28)中加入沉淀剂; 使得在被排空到重力收集容器和运输容器(38)中之前,沿着导管形成良好生长的或成熟的絮凝固体的团块,由此,澄清的液体被积聚的絮凝固体的质量(50)代替,通常通过 过滤器(58,142,150,158,162,166,220),用于去除任何不稳定的细粉。 絮凝固体的许多团块变得足够扩大,以分别延伸穿过并基本上填充导管的横截面。 结果,扩大的团块基本上阻挡了溶液的通过和应变,然后粘附到团块上。

    Process for treating photographic waste water
    95.
    发明授权
    Process for treating photographic waste water 失效
    处理照相废水的方法

    公开(公告)号:US5605633A

    公开(公告)日:1997-02-25

    申请号:US348806

    申请日:1994-11-29

    摘要: A process for treating a photographic waste liquid containing a used processing liquid resulting from a processing step having a bleaching ability or a fixing ability in the processing of a silver halide photographic material which process comprises adding a polymer-complex-forming agent to the waste liquid in an amount in the range of from 0.5 to 4 equivalents to a metal contained in the waste liquid to thereby form a polymer-metal complex and then filtering off the polymer-metal complex with a mono-membrane filter having a pore size of 0.05 to 10 .mu.m to thereby remove the metal. A device for use in practicing the process is also disclosed.

    摘要翻译: 一种处理含有使用的处理液的照相废液的方法,所述处理液由在加工卤化银照相材料中具有漂白能力或定影能力的处理步骤产生,该方法包括向废液中加入聚合物复合物形成剂 相对于废液中含有的金属为0.5〜4当量,从而形成聚合物 - 金属络合物,然后用孔径为0.05的单膜滤器过滤掉聚合物 - 金属络合物,至 10微米,从而去除金属。 还公开了用于实施该方法的装置。

    Electrochemical deionization
    96.
    发明授权
    Electrochemical deionization 失效
    电化学去离子

    公开(公告)号:US5584981A

    公开(公告)日:1996-12-17

    申请号:US426978

    申请日:1995-04-24

    摘要: An electrochemical cell (50) for deionizsation utilizes electrochemical ion-exchange to remove ions from a feed solution. Under the influence of an electric field, ions are adsorbed into, are scored within and pass through a permeable layer (54, 64) of particulate ion-absorbing material and binder, the sheet being several millimeters thick. Water from the feed solution also permeates through the layer (54, 64), so a concentrated solution of the ions emerges from the rear (58) of the layer. The cell does not require separate sources of feed and eluant solutions and can be operated substantially continuously. In a modified cell (70) the flow path for the feed solution passes through a highly porous ion exchanger structure (77), which may be located between two such microporous layers (54, 64). Absorption in such a cell may be effective in the absence of an electric field, elution requiring the periodic application of the electric field.

    摘要翻译: 用于去离子的电化学电池(50)利用电化学离子交换来从进料溶液中除去离子。 在电场的影响下,离子吸附进入,并通过颗粒状离子吸收材料和粘结剂的渗透层(54,64)进行刻痕,该片材的厚度为几毫米。 来自进料溶液的水也渗透通过层(54,64),因此离子的浓缩溶液从层的后部(58)出现。 电池不需要单独的进料和洗脱液来源,并且可以基本连续地操作。 在改性细胞(70)中,进料溶液的流动路径通过高度多孔的离子交换结构(77),其可位于两个这样的微孔层(54,64)之间。 这种电池中的吸收在不存在电场的情况下可能是有效的,需要定期施加电场的洗脱。

    Treatment of photographic effluent
    98.
    发明授权
    Treatment of photographic effluent 失效
    照相废液处理

    公开(公告)号:US5503751A

    公开(公告)日:1996-04-02

    申请号:US190006

    申请日:1994-01-21

    摘要: It is known to treat the effluent resulting from photographic processing apparatus. Such treatment takes the form of either neutralization where the effluent is mixed with a neutralizing solution prior to disposal, or evaporation where the effluent is heated to form a precipitate and a concentrated liquid portion prior to disposal. However, both these techniques have disadvantages they do not account for toxic particles which may be suspended in the solutions. Described herein is apparatus in which photographic effluent can be treated to provide harmless end products which can be disposed of directly. The apparatus comprises a mixing unit (10) in which the effluent (S1) is mixed with treatment chemicals (S2, S3, S4, P1, P2, P3) and is then passed to a separation unit (20) in which the treated effluent is separated into non-toxic liquid and solid phases. A computer (100) is used to control all stages of the treatment of the effluent.

    摘要翻译: PCT No.PCT / EP92 / 01583第 371日期1994年1月21日 102(e)日期1994年1月21日PCT提交1992年7月13日PCT公布。 公开号WO94 / 00241 日期1994年1月6日。已知用于处理由照相处理装置产生的流出物。 这种处理采取中和的形式,其中在处理之前将流出物与中和溶液混合,或蒸发,其中流出物被加热以形成沉淀物,并且在处置之前是浓缩液体部分。 然而,这两种技术都有缺点,它们不能解释悬浮在溶液中的有毒颗粒。 这里描述的是其中可以处理照相流出物以提供可直接处置的无害终产物的装置。 该设备包括混合单元(10),其中流出物(S1)与处理化学品(S2,S3,S4,P1,P2,P3)混合,然后被传送到分离单元(20),其中经处理的流出物 被分离成无毒的液相和固相。 计算机(100)用于控制废水处理的所有阶段。

    Method for regenerating tetraalkylammonium hydroxide
    99.
    发明授权
    Method for regenerating tetraalkylammonium hydroxide 失效
    再生四烷基氢氧化铵的方法

    公开(公告)号:US5405508A

    公开(公告)日:1995-04-11

    申请号:US282903

    申请日:1994-07-29

    摘要: The present invention relates to a method for regenerating tetraalkylammonium hydroxide used as developer solution for positive type resist from waste developer solution. Waste solution from developer solution for positive type resist, which contains tetraalkylammonium hydroxide as principal component, is neutralized, and after depositing and removing alkali-soluble organic substances dissolved in it, it is electrolyzed in an anode chamber of an electrolytic cell partitioned by cation exchange membranes, and it is anodized in the anode chamber. Aqueous solution of tetraalkylammonium hydroxide obtained from the cathode chamber is further introduced to an anode chamber of the other electrolytic cell to perform multi-stage electrolysis or it is introduced into an anode chamber of an electrolytic cell partitioned into 3 chambers or more by two or more cation exchange membranes to perform multi-chamber electrolysis. The electrolytic solution of the intermediate chamber is circulated to an electrolytic cell for decomposing organic substances and electrolyzed, and tetraalkylammonium hydroxide, which can be re-used as developer solution, is obtained from the cathode chamber of the final stage electrolytic cell or from the cathode chamber of the multi-chamber electrolytic cell.

    摘要翻译: 本发明涉及用作废显影剂溶液中用作正型抗蚀剂的显影剂溶液的四烷基氢氧化铵再生方法。 来自含有四烷基氢氧化铵作为主要成分的正型抗蚀剂的显影剂溶液的废液被中和,并且在沉积和除去溶解在其中的碱溶性有机物质后,在由阳离子交换分隔的电解槽的阳极室中电解 膜,并且在阳极室中进行阳极氧化。 从阴极室获得的四烷基氢氧化铵的水溶液被进一步引入到另一个电解池的阳极室中,以进行多级电解,或者将其引入分隔成3个室以上的电解槽的阳极室中2个以上 阳离子交换膜进行多室电解。 将中间室的电解液循环到用于分解有机物质的电解池中并进行电解,从最终级电解池的阴极室或阴极中获得可再次用作显影剂溶液的四烷基氢氧化铵 多室电解池的室。

    Effluent treatment
    100.
    发明授权
    Effluent treatment 失效
    流出物处理

    公开(公告)号:US5350522A

    公开(公告)日:1994-09-27

    申请号:US984415

    申请日:1993-03-04

    申请人: John R. Fyson

    发明人: John R. Fyson

    摘要: A method for treating photographic effluent to remove harmful pollutants and which reduces silver and iron ion concentrations in the effluent to no more than about 2 ppm is disclosed. The method includes an oxidation step to convert reducing sulfur compounds to oxidized products; a heavy metal ion precipitation step; a step of adding a developing agent absorbent and a sequestering agent absorbent; and a step of separating a produced solid phase from a liquid phase. The separated Liquid phase is environmentally acceptable.

    摘要翻译: PCT No.PCT / EP91 / 01680 Sec。 371日期:1993年3月4日 102(e)1993年3月4日PCT PCT 1991年9月5日PCT公布。 出版物WO92 / 04660 1992年3月19日。一种用于处理照相流出物以除去有害污染物并且将流出物中的银和铁离子浓度降低至不超过约2ppm的方法。 该方法包括将还原性硫化合物转化为氧化产物的氧化步骤; 重金属离子沉淀步骤; 添加显影剂吸收剂和螯合剂吸收剂的步骤; 以及从液相中分离生成的固相的步骤。 分离的液相是环境可接受的。