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    • 1. 发明申请
    • PROCESS AND DEVICE FOR REGENERATING AND RECOVERING METALS FROM CHLORIDE-CONTAINING SOLUTIONS
    • 用于从含氯化物溶液中再生和回收金属的工艺和装置
    • WO1992006227A1
    • 1992-04-16
    • PCT/EP1991001903
    • 1991-10-07
    • HANS HÖLLMÜLLER MASCHINENBAU GMBH & CO.MATSCHINER, HermannHARTMANN, BerndREICHELT, KlausLIEBER, Hans-Wilhelm
    • HANS HÖLLMÜLLER MASCHINENBAU GMBH & CO.
    • C23F01/46
    • C23G1/36C22B15/0093C23F1/46Y02P10/236
    • A process and device are disclosed for regenerating and recovering metals from chloride-containing solutions, such as those resulting from etching, corroding and rinsing during surface treatments, in particular galvanoplastic treatments and printed circuit board production, and that contain copper and other metal ions. The metals are separated from the acid, chloride-containing solutions with dissolved hydrogen. For that purpose, the acid chloride-containing solution is treated with hydrogen under a pressure from 0.0 to 0.5 MPa, available in the dissolved state in the water at a concentration from 0.6 to 1,8 kg/m h at a temperature between 10 and 60 DEG C, preferably between 15 and 50 DEG C, so that the metals are precipitated in the form of metal particles. A loop-type bubble column is used to carry out the process, said column comprising a reaction vessel (1), a circulating pump for stably delivering the gas-liquid mixture, a gas dispersing machine (3) for sucking-in and dispersing the gaseous hydrogen, a solid matter separating equipment (4) integrated in the circulating stream and possibly a dosing pump (5) for continuously feeding the solutions to be regenerated.
    • 公开了用于从含氯化物溶液再生和回收金属的方法和装置,例如在表面处理期间由腐蚀,腐蚀和漂洗产生的金属,特别是电镀锌处理和印刷电路板生产,并且含有铜和其它金属离子。 金属与含有溶解氢的含氯化物溶液分离。 为此,将含酰基氯的溶液在0.0〜0.5MPa的压力下用氢气处理,溶解状态在水中以0.6〜1.8kg / m 3的浓度在温度 10至60℃,优选15至50℃,以使金属以金属颗粒的形式沉淀。 使用环式鼓泡塔进行该方法,所述柱包括反应容器(1),用于稳定输送气液混合物的循环泵,用于吸入和分散的气体分散机(3) 气态氢,集成在循环流中的固体物质分离设备(4)和可能的计量泵(5),用于连续地供给要再生的溶液。
    • 4. 发明申请
    • METHOD OF RECYCLING WASTE ETCHING SOLUTION
    • 回收废弃溶剂的方法
    • WO1996035827A1
    • 1996-11-14
    • PCT/JP1995001673
    • 1995-08-23
    • AIN CO., LTD.AITECH CORPORATIONHOSODA, ShyujiONO, KaoruKASUYA, YutakaNAGAO, Minoru
    • AIN CO., LTD.AITECH CORPORATION
    • C23F01/46
    • C23F1/46
    • A method of recycling a waste etching solution formed in the etching of a copper article with an ammonia-alkaline cupric chloride etchant, which comprises continuously treating the waste solution with an extractant capable of selectively extracting copper while preventing the etching velocity from being lowered as a result of the contamination of the regenerated etching solution with a large amount of the extractant. The method comprises the steps of mixing the waste solution with the extractant under agitation to effect extraction, separating the regenerated etching solution having a lowered copper concentration for recycling, subjecting the copper-containing extractant to back extraction to cause the copper contained in the extractant to migrate into an aqueous sulfuric acid-copper sulfate solution, and cleaning the extractant after the back extraction with a cleaning fluid such as water, warm water or dilute hydrochloric acid to remove sulfuric acid from the extractant.
    • 一种利用氨 - 碱性氯化铜蚀刻剂回收在铜制品的蚀刻中形成的废蚀刻溶液的方法,其包括用能够选择性提取铜的萃取剂连续处理废溶液,同时防止蚀刻速度降低为 再生的蚀刻溶液用大量的萃取剂污染的结果。 该方法包括以下步骤:在搅拌下将废溶液与萃取剂混合以进行萃取,分离具有降低的铜浓度的再生蚀刻溶液进行再循环,使含铜萃取剂反萃取,使萃取剂中所含的铜 迁移到硫酸 - 硫酸铜水溶液中,并用清洗液如水,温水或稀盐酸清洗后提取物,以从萃取剂中除去硫酸。
    • 5. 发明申请
    • ELECTROLYSIS PROCESS FOR REGENERATING A FERRIC CHLORIDE OR SULPHATE SOLUTION, IN PARTICULAR FOR SPRAY ETCHING STEEL
    • 电解法再生铁III氯化物或铁III氯化物溶液的,尤其是用于钢的喷雾蚀刻
    • WO1995024518A1
    • 1995-09-14
    • PCT/DE1995000294
    • 1995-03-06
    • MIB METALLURGIE UND OBERFLÄCHENTECHNIK UND INNOVATION IN BERLIN GMBH & CO.LANDAU, UweHERRMANN, Sigrid
    • MIB METALLURGIE UND OBERFLÄCHENTECHNIK UND INNOVATION IN BERLIN GMBH & CO.
    • C23F01/46
    • C23G1/36C23F1/46
    • An electrolysis process for regenerating a ferric chloride or sulphate solution (etchant), in particular for spray etching steel, is disclosed. The etchant to be regenerated continuously flows through the anode chamber (17) of an electrolytic cell (10) whose cathode chamber (14) is filled with a diluted conductive acid. Anode and cathode chambers (12 and 14) are separated by a cation exchange membrane (16) through which Fe(II) ions, excess Fe(III) and dissolved non-ferrous metals, in particular nickel and chromium ions, reach the cathode chamber (14), while Fe(II) ions are oxidised into FE(III) ions at the anode. The metals accumulated in the catholyte preferably precipitate as a powder in the cathode chamber (14) or are electrolytically precipitated in a subsequent electrolytic cell whose cathode and anode chambers are separated by an anion exchange membrane. This process allows the etchant to be continuously regenerated in a closed circuit, ensures the depletion of non-ferrous metals and excess iron, as well as the electrolytic precipitation of the depleted metal ions.
    • 这是用于再生氯化铁或硫酸铁溶液(泡菜),找到特别是用于钢的使用喷雾蚀刻中描述的电解过程。 媒染剂,以通过阳极室(17)连续地再生通过电解池(10),其阴极空间(14)填充有稀释,高导电性酸。 阳极室和阴极室(12和14)是由一个阳离子交换膜(16)分开的,通过它的Fe-II-离子,铁III-过量和溶解的非铁金属,在阴极室特别是镍和铬离子(14) 被转移,而在阳极的Fe-II离子的Fe-III离子被氧化。 中阴极电解液的金属富集优选沉积在阴极室(14),为粉末或在下游电解槽的阴极和阳极室由阴离子交换膜隔开,电解沉积。 该方法允许在闭合回路中的污渍的连续再生,保证有色金属和铁过剩和耗尽的金属离子的电解沉积的耗尽。
    • 7. 发明申请
    • INSTALLATION FOR ETCHING OBJECTS
    • 搪瓷对象安装
    • WO1990005797A1
    • 1990-05-31
    • PCT/EP1989001345
    • 1989-11-10
    • HANS HÖLLMÜLLER MASCHINENBAU GMBH & CO.HAAS, Rainer
    • HANS HÖLLMÜLLER MASCHINENBAU GMBH & CO.
    • C23F01/46
    • C23F1/46C23F1/08
    • An installation for etching objects comprises at least one etching machine (1) in which metal is etched from the treated objects (7) and the etching reagent is enriched with metal. The etching reagent is regenerated in several electrolytic cells (5A, 5B, 5C) by removal of metal. For adaptation to different instantaneous etching capacities (loads) of the machine, the electrolytic cells (5A, 5B, 5C) are connected in succession by a device which integrates the quantity of enriched etching reagent removed from the etching machine (1) over a given time. A given limit value for this integral is assigned to each electrolytic cell (5A, 5B, 5C); when this limit value is exceeded, the corresponding electrolytic cell (5A, 5B, 5C) is activated. In this way, the total output of the electrolytic cells in service at any given time is adapted to the instantaneous load of the etching machine.
    • 用于蚀刻对象的装置包括至少一个蚀刻机(1),其中从被处理物体(7)蚀刻金属,并且蚀刻剂富含金属。 蚀刻剂通过去除金属在几个电解槽(5A,5B,5C)中再生。 为了适应机器的不同的瞬时蚀刻能力(负载),电解槽(5A,5B,5C)依次通过将从蚀刻机(1)去除的富集腐蚀试剂的量积聚在给定的 时间。 该积分的给定极限值被分配给每个电解槽(5A,5B,5C); 当超过该极限值时,相应的电解槽(5A,5B,5C)被激活。 以这种方式,在任何给定时间使用的电解池的总输出适应于蚀刻机的瞬时负载。
    • 8. 发明申请
    • INSTALLATION FOR ETCHING OBJECTS
    • 搪瓷对象安装
    • WO1990005796A1
    • 1990-05-31
    • PCT/EP1989001344
    • 1989-11-10
    • HANS HÖLLMÜLLER MASCHINENBAU GMBH & CO.HAAS, Rainer
    • HANS HÖLLMÜLLER MASCHINENBAU GMBH & CO.
    • C23F01/46
    • C23F1/08C23F1/46
    • An installation for etching objects comprises at least one etching machine in which metal is etched from the treated objects and the etching reagent is enriched with metal. The etching reagent is regenerated in at least one electrolytic cell (5) by removal of metal. Two buffer tanks (3, 4) are located in the lines (28, 35) which connect the etching machine (1) to the electrolytic cell. A first control circuit (15, 16, 17, 19, 23, 26) maintains the density of the etching reagent in the etching machine essentially constant. To this end, the depleted etching reagent is conveyed from the first buffer tank (3) to the etching machine (1) and the enriched etching agent is conveyed from the etching machine (1) to the second buffer tank (4). A second control circuit (40, 43, 44) maintains an essentially constant density in the electrolytic cell (5); to this end, enriched etching reagent is conveyed from the second buffer tank (4) to the electrolytic cell and an equivalent quantity of depleted etching reagent is conveyed from the electrolytic cell (5) to the first buffer tank (3). The two control circuits operate independently of each other.
    • 用于蚀刻对象的装置包括至少一个蚀刻机,其中从被处理物体蚀刻金属并且蚀刻剂富含金属。 蚀刻剂通过去除金属在至少一个电解池(5)中再生。 两个缓冲罐(3,4)位于将蚀刻机(1)连接到电解槽的管线(28,35)中。 第一控制电路(15,16,17,19,23,26)保持蚀刻机中蚀刻剂的密度基本恒定。 为此,耗尽的蚀刻试剂从第一缓冲罐(3)输送到蚀刻机(1),富集的蚀刻剂从蚀刻机(1)输送到第二缓冲罐(4)。 第二控制电路(40,43,44)在电解池(5)中保持基本恒定的密度; 为此,富集的蚀刻剂从第二缓冲罐(4)输送到电解槽,并且等量的耗尽的蚀刻剂从电解槽(5)输送到第一缓冲罐(3)。 两个控制电路彼此独立地工作。