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CN115124171A - Treatment method and treatment system for gold-containing waste liquid - Google Patents

Treatment method and treatment system for gold-containing waste liquid Download PDF

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Publication number
CN115124171A
CN115124171A CN202210738350.2A CN202210738350A CN115124171A CN 115124171 A CN115124171 A CN 115124171A CN 202210738350 A CN202210738350 A CN 202210738350A CN 115124171 A CN115124171 A CN 115124171A
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gold
waste liquid
containing waste
treatment
liquid
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张亚
谌京
向铖
王雷
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Peking University Founder Group Co Ltd
Zhuhai Founder Technology Multilayer PCB Co Ltd
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Peking University Founder Group Co Ltd
Zhuhai Founder Technology Multilayer PCB Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/285Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/16Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/14Maintenance of water treatment installations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/22Eliminating or preventing deposits, scale removal, scale prevention

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention provides a treatment method and a treatment system of gold-containing waste liquid, wherein the treatment method comprises the following steps: carrying out electrolysis treatment on the first gold-containing waste liquid to obtain metallic gold and electrolysis raffinate; performing adsorption treatment on the electrolysis residual liquid and the second gold-containing waste liquid by using resin to obtain gold-loaded resin and adsorption residual liquid; the gold content in the first gold-containing waste liquid is greater than the gold content in the second gold-containing waste liquid. The treatment method can realize the high-efficiency recovery of gold, does not generate secondary wastewater, and is beneficial to industrial production and application.

Description

含金废液的处理方法和处理系统Treatment method and treatment system for gold-containing waste liquid

技术领域technical field

本发明涉及废水处理技术领域,具体涉及一种含金废液的处理方法和处理系统。The invention relates to the technical field of wastewater treatment, in particular to a treatment method and treatment system for gold-containing waste liquid.

背景技术Background technique

随着市场金价的上涨,镀金成本成为关注的重点。在线路板的镀金工艺中,先对待镀金的线路板进行镀金处理,然后对镀金后的线路板进行水洗,镀金残余液中含有大量未反应的金盐,水洗残余液中含有少量金盐,若将镀金残余液和水洗残余液直接排放到环境中,不仅会造成环境的污染,还增加了制造成本。With the rising gold price in the market, the cost of gold plating has become the focus of attention. In the gold plating process of the circuit board, the circuit board to be gold-plated is first plated with gold, and then the gold-plated circuit board is washed with water. The gold plating residue contains a large amount of unreacted gold salt, and the washing residue contains a small amount of gold salt. Directly discharging the gold-plating residual liquid and the water-washing residual liquid into the environment will not only cause environmental pollution, but also increase the manufacturing cost.

因此,如何对线路板镀金工艺中产生的含金废液进行有效处理和金回收,是本领域亟待解决的技术问题。Therefore, how to effectively treat and recover the gold-containing waste liquid produced in the gold plating process of the circuit board is a technical problem to be solved urgently in the art.

发明内容SUMMARY OF THE INVENTION

本发明提供一种含金废液的处理方法和处理系统,该处理方法能够对含金废液进行有效处理和回收。The invention provides a processing method and a processing system for the gold-containing waste liquid, which can effectively treat and recover the gold-containing waste liquid.

本发明的一方面,提供一种含金废液的处理方法,包括以下步骤:对第一含金废液进行电解处理,得到金属金和电解残余液;采用树脂对电解残余液和第二含金废液分别进行吸附处理,得到载金树脂和吸附残余液;第一含金废液中的金含量大于第二含金废液中的金含量。In one aspect of the present invention, a method for treating gold-containing waste liquid is provided, comprising the following steps: electrolyzing the first gold-containing waste liquid to obtain metallic gold and electrolytic residual liquid; The gold waste liquids are respectively subjected to adsorption treatment to obtain a gold-loaded resin and an adsorption residual liquid; the gold content in the first gold-containing waste liquid is greater than that in the second gold-containing waste liquid.

根据本发明的一实施方式,电解处理的条件为:电压为2.5-5V,电流为2.5-5V,温度为50-80℃。According to an embodiment of the present invention, the conditions of the electrolysis treatment are as follows: the voltage is 2.5-5V, the current is 2.5-5V, and the temperature is 50-80°C.

根据本发明的一实施方式,树脂包括环氧树脂。According to an embodiment of the present invention, the resin includes epoxy resin.

根据本发明的一实施方式,对第一含金废液进行电解处理之前,还包括,对第一含金废液进行过滤;在采用树脂对第二含金废液进行吸附处理之前,还包括:对第二含金废液进行过滤。According to an embodiment of the present invention, before the electrolytic treatment of the first gold-containing waste liquid, the method further includes: filtering the first gold-containing waste liquid; : Filter the second gold-containing waste liquid.

根据本发明的一实施方式,第一含金废液为对待镀金的线路板进行镀金处理后得到的镀金废液;第二含金废液经过对镀金处理后的线路板进行水洗处理得到。According to an embodiment of the present invention, the first gold-containing waste liquid is a gold-plating waste liquid obtained after gold-plating the circuit board to be gold-plated; the second gold-containing waste liquid is obtained by washing the gold-plated circuit board with water.

根据本发明的一实施方式,水洗处理包括以下步骤:对镀金处理后的线路板进行一级水洗处理,得到第二含金废液和一级水洗后线路板,采用清洗液对一级水洗后线路板进行二级水洗处理,得到二级排水和二级水洗后线路板;采用二级排水对镀金处理后的线路板进行一级水洗处理。According to an embodiment of the present invention, the water washing treatment includes the following steps: performing primary water washing treatment on the gold-plated circuit board to obtain the second gold-containing waste liquid and the circuit board after primary water washing, and using the cleaning solution to wash the circuit board after primary water washing The circuit board is subjected to secondary water washing treatment to obtain secondary drainage and a circuit board after secondary water washing; the secondary drainage is used to perform primary water washing treatment on the gold-plated circuit board.

本发明的另一方面,提供一种含金废液的处理系统,用于实施上述的含金废液的处理方法,包括:电解装置和树脂吸附装置,电解装置的液相出口与树脂吸附装置的入口连通。Another aspect of the present invention provides a treatment system for gold-containing waste liquid for implementing the above-mentioned treatment method for gold-containing waste liquid, comprising: an electrolysis device and a resin adsorption device, a liquid phase outlet of the electrolysis device and a resin adsorption device The entrance is connected.

根据本发明的一实施方式,还包括水洗装置,水洗装置包括一级水洗槽和二级水洗槽,在二级水洗槽上设置有二级排水口,在重力方向上,二级排水口高于一级水洗槽的一级进水口;在一级水洗槽上设置有一级排水口,一级排水口连通于树脂吸收装置。According to an embodiment of the present invention, it further includes a water washing device, the water washing device includes a primary water washing tank and a secondary water washing tank, the secondary water washing tank is provided with a secondary water outlet, and in the direction of gravity, the secondary water outlet is higher than The primary water inlet of the primary water washing tank; the primary water washing tank is provided with a primary water outlet, and the primary water outlet is communicated with the resin absorption device.

根据本发明的一实施方式,还包括储液装置,储液装置用于容置第二含金废液;储液装置的入口连通于一级排水口的出口,储液装置的出口连通于树脂吸收装置。According to an embodiment of the present invention, a liquid storage device is further included, and the liquid storage device is used for accommodating the second gold-containing waste liquid; the inlet of the liquid storage device is connected to the outlet of the primary water outlet, and the outlet of the liquid storage device is connected to the resin Absorber.

根据本发明的一实施方式,还包括第一过滤装置和第二过滤装置;第一过滤装置的液体出口连通于电解装置的入口;第二过滤装置的入口连通于储液罐的出口,第二过滤装置的液体出口与树脂吸附罐的入口连通。According to an embodiment of the present invention, it further includes a first filter device and a second filter device; the liquid outlet of the first filter device is connected to the inlet of the electrolysis device; the inlet of the second filter device is connected to the outlet of the liquid storage tank, and the second filter device The liquid outlet of the filtering device communicates with the inlet of the resin adsorption tank.

本发明的实施,至少具有如下有益效果:The implementation of the present invention has at least the following beneficial effects:

本发明提供的含金废液的处理方法,根据金含量对待处理含金废液进行区分,并采用更为合适的方法进行处理,从而能够将含金废液中的金进行高效回收。具体地,第一含金废液的金含量大于第二含金废液的金含量,先对第一含金废液进行电解处理,降低第一含金废液中的金含量,然后采用树脂对电解残余液和第二含金废液分别进行吸附处理,进一步回收金属金,降低电解残余液和第二含金废液中的金含量。该处理方法能够实现对第一含金废液和第二含金废液中金的高效回收,且不会产生二次废水,大幅度降低处理成本;此外,该处理方法还具有处理过程简单、易操作等优点,利于工业化生产和应用。The method for treating the gold-containing waste liquid provided by the present invention distinguishes the gold-containing waste liquid to be treated according to the gold content, and adopts a more appropriate method for treatment, so that the gold in the gold-containing waste liquid can be efficiently recovered. Specifically, if the gold content of the first gold-containing waste liquid is greater than the gold content of the second gold-containing waste liquid, the first gold-containing waste liquid is electrolytically treated to reduce the gold content in the first gold-containing waste liquid, and then a resin The electrolysis residual liquid and the second gold-containing waste liquid are respectively subjected to adsorption treatment to further recover metallic gold and reduce the gold content in the electrolysis residual liquid and the second gold-containing waste liquid. The treatment method can realize the efficient recovery of gold in the first gold-containing waste liquid and the second gold-containing waste liquid, without generating secondary waste water and greatly reducing the treatment cost; in addition, the treatment method also has the advantages of simple treatment process, It has the advantages of easy operation, etc., which is beneficial to industrial production and application.

本发明提供的含金废液的处理系统,将电解装置和树脂吸附装置联合使用,可以用于处理镀金工艺中产生的第一含金废液和水洗产生的第二含金废液,该处理系统结构简单、实用性强。The gold-containing waste liquid treatment system provided by the present invention, which uses an electrolysis device and a resin adsorption device in combination, can be used to treat the first gold-containing waste liquid generated in the gold-plating process and the second gold-containing waste liquid generated by water washing. The system has simple structure and strong practicability.

附图说明Description of drawings

图1是本发明一实施方式中含金废液的处理方法的流程图;Fig. 1 is the flow chart of the processing method of gold-containing waste liquid in one embodiment of the present invention;

图2是本发明一实施方式中含金废液的处理方法的流程图;Fig. 2 is the flow chart of the treatment method of gold-containing waste liquid in one embodiment of the present invention;

图3是本发明一实施方式中含金废液的处理系统的示意图。3 is a schematic diagram of a treatment system for gold-containing waste liquid in an embodiment of the present invention.

具体实施方式Detailed ways

为使本发明的目的、技术方案和优点更加清楚,下面将结合本发明的实施例,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Obviously, the described embodiments are part of the implementation of the present invention. examples, but not all examples. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

需要说明的是,“第一”、“第二”等术语仅用于描述目的,例如区分不同废液,以更清楚说明/解释技术方案,而不能理解为指示或暗示所指示的技术特征的数量或具有实质性意义的顺序等含义。此外,在本发明的描述中,除非另有明确的规定和限定,术语“设置”、“连通”、“相连”、“连通于”等应做广义理解,例如,连通可以是直接连通,也可以是通过中间媒介间接连通。对于本领域的普通技术人员而言,可以具体情况理解上述属于在本发明中的具体含义。It should be noted that terms such as "first" and "second" are only used for descriptive purposes, such as distinguishing different waste liquids, so as to describe/explain the technical solution more clearly, and should not be understood as indicating or implying the indicated technical features Quantity or substantive order, etc. In addition, in the description of the present invention, unless otherwise expressly specified and limited, the terms "arranged", "connected", "connected", "connected with" and the like should be understood in a broad sense, for example, the communication may be direct communication, or It can be indirectly connected through an intermediary. For those of ordinary skill in the art, the above-mentioned specific meanings in the present invention can be understood in specific situations.

如图1所示,本发明提供一种含金废液的处理方法,包括以下步骤:对第一含金废液进行电解处理,得到金属金和电解残余液;采用树脂对电解残余液和第二含金废液分别进行吸附处理,得到载金树脂和吸附残余液;第一含金废液中的金含量大于第二含金废液中的金含量。As shown in Figure 1, the present invention provides a kind of treatment method of gold-containing waste liquid, comprising the following steps: carry out electrolytic treatment to the first gold-containing waste liquid, obtain metallic gold and electrolysis residual liquid; The two gold-containing waste liquids are respectively subjected to adsorption treatment to obtain a gold-loaded resin and an adsorption residual liquid; the gold content in the first gold-containing waste liquid is greater than that in the second gold-containing waste liquid.

本发明提供的含金废液的处理方法,不仅能够降低含金废液中的金含量,而且能够实现对含金废液中金的回收。The method for treating gold-containing waste liquid provided by the invention can not only reduce the gold content in the gold-containing waste liquid, but also realize the recovery of gold in the gold-containing waste liquid.

本发明中,含金废液包括第一含金废液和第二含金废液,第一含金废液中金的含量较高,可以采用电解处理回收金属金,经电解操作后的第一含金废水中金的含量大大降低,可以采用树脂对电解残余液进行吸附处理。第二含金废液中的金的含量较低,适合采用树脂吸附回收金。In the present invention, the gold-containing waste liquid includes the first gold-containing waste liquid and the second gold-containing waste liquid. The gold content in the first gold-containing waste liquid is relatively high, and the metal gold can be recovered by electrolytic treatment. The content of gold in the gold-containing wastewater is greatly reduced, and resin can be used to adsorb the residual liquid of electrolysis. The content of gold in the second gold-containing waste liquid is relatively low, and it is suitable to adopt resin adsorption to recover gold.

在一些实施例中,第一含金废液为对待镀金的线路板进行镀金处理后得到的镀金废液,其中金的含量范围为0.4g/L-1.2g/L。In some embodiments, the first gold-containing waste liquid is a gold-plating waste liquid obtained after the circuit board to be gold-plated is subjected to gold-plating treatment, wherein the gold content ranges from 0.4 g/L to 1.2 g/L.

进一步地,第一含金废液还可以是线路板表面沉金、化金处理中产生的含金废液。Further, the first gold-containing waste liquid may also be the gold-containing waste liquid generated in the process of gold immersion and chemical gold treatment on the surface of the circuit board.

在一些实施例中,第二含金废液经过对镀金处理后的线路板进行水洗处理得到,即第二含金废液来自于水洗产生的废液,其中金的含量范围为2ppm-5ppm。In some embodiments, the second gold-containing waste liquid is obtained by washing the gold-plated circuit board with water, that is, the second gold-containing waste liquid comes from the waste liquid generated by water washing, and the gold content ranges from 2ppm to 5ppm.

如图2所示,在一些实施例中,对第一含金废液进行电解处理之前,还包括,对第一含金废液进行过滤,以去除第一含金废液中的固体杂质、泥沙等,防止其影响电解处理的效果。As shown in FIG. 2 , in some embodiments, before the electrolytic treatment of the first gold-containing waste liquid, the method further includes filtering the first gold-containing waste liquid to remove solid impurities, Sediment, etc., to prevent it from affecting the effect of electrolytic treatment.

通常情况下,上述电解处理在电解装置中进行,电解装置至少包括电解槽、阴极板、阳极板,阴极板和阳极板均设于电解槽内,阳极板和阴极板相互平行设置。Usually, the above-mentioned electrolysis treatment is carried out in an electrolysis device, and the electrolysis device at least includes an electrolytic cell, a cathode plate, and an anode plate.

在上述电解处理中,将第一含金废液导入电解槽中通电进行电解处理,并控制电解处理的电压和电流,在电解过程中,第一含金废液中的金离子被还原,在阴极板表面以沉积物的形式析出,然后刮取沉积在阴极板的沉积物,对沉积物进行提纯、清洗、干燥后得到金属金。经电解处理后,电解槽内剩余的溶液是电解残余液。In the above-mentioned electrolytic treatment, the first gold-containing waste liquid is introduced into an electrolytic cell and energized for electrolytic treatment, and the voltage and current of the electrolytic treatment are controlled. During the electrolysis process, the gold ions in the first gold-containing waste liquid are reduced. The surface of the cathode plate is precipitated in the form of deposits, and then the deposits deposited on the cathode plate are scraped off, and the deposits are purified, cleaned and dried to obtain metallic gold. After the electrolysis treatment, the remaining solution in the electrolysis tank is the electrolysis residual solution.

在上述实施例中,通常采用稳定电压对第一含金废液进行电解处理,避免电压的波动,减小电流的变化幅度。电解处理的电压为2.5V-5V,例如2.5V、3V、3.5V、4V、4.5V、5V或其中的任意两者组成的范围。若电解处理的电压较低,电解的速率较慢,金难以在阴极表面沉积;若电压较高,则电解速率较快,金的析出速率较快,在极板上沉积的厚度不均,容易从阴极板表面脱落,影响电解处理的效果。In the above embodiment, a stable voltage is usually used to electrolyze the first gold-containing waste liquid, so as to avoid voltage fluctuation and reduce the current fluctuation range. The voltage of the electrolytic treatment is 2.5V-5V, for example, a range composed of 2.5V, 3V, 3.5V, 4V, 4.5V, 5V or any two thereof. If the voltage of the electrolysis treatment is low, the rate of electrolysis is slow, and it is difficult for gold to deposit on the surface of the cathode; It falls off from the surface of the cathode plate, which affects the effect of electrolytic treatment.

在一些实施例中,电解处理的电流为2.5A-5A,例如2.5A、3A、3.5A、4A、4.5A、5A或其中的任意两者组成的范围。若电解处理的电流较小,电子流量较小,发生电子转移的概率降低,不利于金的析出;若电流较大,极板容易发热,影响电解装置的正常运行。In some embodiments, the current of the electrolytic treatment is 2.5A-5A, such as a range of 2.5A, 3A, 3.5A, 4A, 4.5A, 5A, or any two thereof. If the current of the electrolysis treatment is small, the electron flow is small, and the probability of electron transfer is reduced, which is not conducive to the precipitation of gold; if the current is large, the electrode plate is easy to heat up, which affects the normal operation of the electrolysis device.

为使电解处理过程正常进行,需要维持通入电解槽内的第一含金废液的温度不变。在一些实施例中,电解处理的温度为50℃-80℃,例如50℃、55℃、60℃、65℃、70℃、75℃、80℃或其中的任意两者组成的范围。若温度较低,会导致电解速率较慢,增加能耗,影响电解效率;若温度较高,会导致第一含金废液中的溶液蒸发增大、沉积物结晶较粗等。In order to carry out the electrolytic treatment process normally, it is necessary to maintain the temperature of the first gold-containing waste liquid passed into the electrolytic cell unchanged. In some embodiments, the temperature of the electrolytic treatment is 50°C-80°C, eg, a range of 50°C, 55°C, 60°C, 65°C, 70°C, 75°C, 80°C, or any two thereof. If the temperature is low, the electrolysis rate will be slow, the energy consumption will be increased, and the electrolysis efficiency will be affected; if the temperature is high, the evaporation of the solution in the first gold-containing waste liquid will be increased, and the crystallization of the deposit will be coarser.

具体实施时,首先对电解槽进行预加热,设置电解槽的温度等参数;对第一含金废液的进行预加热,将预加热后的第一含金废水通入电解槽内,使阳极板与阴极板之间的第一含金废液流动起来;当电解槽内的阳极板与阴极板之间充满第一含金废液时,使阳极板与阴极板通电,设置阳极板与阴极板两端的电压,对第一含金废液进行电解处理。In the specific implementation, firstly preheat the electrolytic cell, and set parameters such as the temperature of the electrolytic cell; preheat the first gold-containing waste liquid, and pass the preheated first gold-containing waste water into the electrolytic cell to make the anode The first gold-containing waste liquid between the plate and the cathode plate flows; when the first gold-containing waste liquid is filled between the anode plate and the cathode plate in the electrolytic cell, the anode plate and the cathode plate are energized, and the anode plate and the cathode plate are set. The voltage across the plate is used to electrolyze the first gold-containing waste liquid.

在上述具体实施过程中,在电解槽内的阳极板与阴极板之间充满第一含金废液时进行电解,有利于第一含金废液在极板间的均匀电解,有利于提高金的回收率,并且有利于对第一含金废液进行大规模处理。In the above-mentioned specific implementation process, electrolysis is carried out when the first gold-containing waste liquid is filled between the anode plate and the cathode plate in the electrolytic cell, which is beneficial to the uniform electrolysis of the first gold-containing waste liquid between the electrode plates, and is conducive to improving gold The recovery rate is high, and it is beneficial to the large-scale treatment of the first gold-containing waste liquid.

在上述具体实施过程中,当阴极板上的阴极材料表面充满沉积物时,将该阴极板从电解槽内取出,更换新的阴极材料,再将其插置在电解槽内;当阳极板上的阳极材料消耗完时,直接将阳极板从电解槽内取出,将阳极材料拆除,更换新的阳极材料,再将其插入在电解槽内。In the above specific implementation process, when the surface of the cathode material on the cathode plate is full of deposits, the cathode plate is taken out from the electrolytic cell, replaced with a new cathode material, and then inserted into the electrolytic cell; when the anode plate is When the anode material is consumed, the anode plate is directly taken out from the electrolytic cell, the anode material is removed, the new anode material is replaced, and then inserted into the electrolytic cell.

在一些实施例中,采用树脂对电解残余液和第二含金废液分别进行吸附处理,进一步降低电解残余液和第二含金废液中的金含量。在吸附处理中,电解残余液和第二含金废液中残余金被吸附在树脂上,得到载金树脂和吸附残余液。吸附残余液中金含量大大降低,可以直接排入环境中,不会对环境造成二次污染。In some embodiments, resin is used to perform adsorption treatment on the electrolysis residual liquid and the second gold-containing waste liquid, so as to further reduce the gold content in the electrolytic residual liquid and the second gold-containing waste liquid. In the adsorption treatment, the residual gold in the electrolysis residual liquid and the second gold-containing waste liquid is adsorbed on the resin to obtain a gold-loaded resin and an adsorption residual liquid. The gold content in the adsorption residual liquid is greatly reduced, and it can be directly discharged into the environment without causing secondary pollution to the environment.

如图2所示,在上述实施例中,在采用树脂对第二含金废液进行吸附处理之前,还包括:对第二含金废液进行过滤处理,以去除固体杂质、泥沙等,防止堵塞树脂影响树脂选择性吸附金的性能。As shown in Figure 2, in the above-mentioned embodiment, before adopting resin to carry out adsorption treatment to the second gold-containing waste liquid, it also includes: filtering the second gold-containing waste liquid to remove solid impurities, sediment, etc., Preventing clogging of the resin affects the performance of the resin to selectively adsorb gold.

在上述实施例中,电解残余液、第二含金废液与树脂充分接触,使得残余金被吸附在树脂上,该吸附处理在常温条件下进行。In the above embodiment, the electrolysis residual liquid and the second gold-containing waste liquid are fully contacted with the resin, so that the residual gold is adsorbed on the resin, and the adsorption treatment is carried out under normal temperature conditions.

在本发明的具体实施过程中,使电解残余液、第二含金废液流经树脂,以使液体与树脂充分接触,通常将树脂填充于吸附柱中,使电解残余液、第二含金废液分别流至吸附柱中进行吸附处理,其中液体的流速为1000L/h-1500L/h。In the specific implementation process of the present invention, the electrolysis residual liquid and the second gold-containing waste liquid are made to flow through the resin, so that the liquid and the resin are fully contacted. The waste liquid is respectively flowed to the adsorption column for adsorption treatment, wherein the flow rate of the liquid is 1000L/h-1500L/h.

在上述实施例中,当树脂吸附金饱和后,可以将载金树脂从吸附柱中拆除,更换新的树脂进行吸附。In the above embodiment, when the resin is saturated with gold adsorption, the gold-loaded resin can be removed from the adsorption column and replaced with a new resin for adsorption.

本发明中,选用的树脂对金具有高选择性,能够排除铜、镍等其他金属对树脂选择性的干扰,提高金的吸附率。在一些实施例中,树脂包括环氧树脂,本发明的树脂可以是商购,也可以是采用常规方法获得,树脂的饱和吸附量在此不作限定。In the present invention, the selected resin has high selectivity to gold, can eliminate the interference of other metals such as copper and nickel on the resin selectivity, and improve the adsorption rate of gold. In some embodiments, the resin includes epoxy resin. The resin of the present invention may be commercially available or obtained by conventional methods. The saturated adsorption capacity of the resin is not limited herein.

在上述实施例中,在吸附处理完成后,还包括载金树脂的解吸和再生,采用焚烧法、酸洗法等本领域常规方法对载金树脂进行解吸和再生,进一步对载金树脂上的金进行提取。示例性地,使载金树脂与解吸液充分接触,使得吸附在树脂上的金以离子的形式溶于解吸液中,解吸完成后,采用清洁的水对解吸后的载金树脂进行清洗,得到再生的树脂。In the above embodiment, after the adsorption treatment is completed, the desorption and regeneration of the gold-loaded resin are also included, and the gold-loaded resin is desorbed and regenerated by conventional methods in the field such as incineration, pickling, etc. Gold is withdrawn. Exemplarily, the gold-loaded resin is fully contacted with the desorption liquid, so that the gold adsorbed on the resin is dissolved in the desorption liquid in the form of ions, and after the desorption is completed, the desorbed gold-loaded resin is washed with clean water to obtain recycled resin.

本发明中,第二含金废液来自于对线路板水洗后产生的废液,水洗处理包括以下步骤:对镀金处理后的线路板进行一级水洗处理,得到第二含金废液和一级水洗后线路板,采用清洗液对一级水洗后线路板进行二级水洗处理,得到二级排水和二级水洗后线路板;采用二级排水对镀金处理后的线路板进行一级水洗处理。In the present invention, the second gold-containing waste liquid comes from the waste liquid generated after washing the circuit board, and the water washing treatment includes the following steps: performing a primary water washing treatment on the gold-plated circuit board to obtain the second gold-containing waste liquid and a The circuit board after the first-level water washing is used to perform the second-level water washing treatment on the circuit board after the first-level water washing, so as to obtain the second-level drainage and the circuit board after the second-level water washing; the second-level drainage is used to perform the first-level water washing treatment on the gold-plated circuit board. .

本发明中,将二级水洗处理产生的二级排水用于一级水洗处理中,循环利用二级排水,采用该种水洗方式,不仅将线路板表面的残余金冲洗下来,还能通过少量用水达到清洗效果,以达到节水的目的。In the present invention, the secondary drainage produced by the secondary water washing treatment is used in the primary water washing treatment, and the secondary drainage is recycled. By adopting this water washing method, not only the residual gold on the surface of the circuit board is washed off, but also a small amount of water can be used for washing. To achieve the cleaning effect, in order to achieve the purpose of saving water.

在上述实施例中,清洗液可以是本领域常规的线路板清洗液。In the above embodiment, the cleaning solution may be a conventional circuit board cleaning solution in the art.

本发明中,将上述线路板的水洗处理与含金废水的处理方法联合应用,有利于提高金的回收率,并且有利于对第一含金废液和第二含金废液进行大规模处理。In the present invention, the combined application of the above-mentioned water washing treatment of circuit boards and the treatment method of gold-containing wastewater is beneficial to improve the recovery rate of gold, and is conducive to large-scale treatment of the first gold-containing waste liquid and the second gold-containing waste liquid .

本发明提供一种含金废液的处理系统,用于实施上述含金废液的处理方法,该装置包括:电解装置和树脂吸附装置,电解装置的液相出口与树脂吸附装置的入口连通。The invention provides a treatment system for gold-containing waste liquid, which is used for implementing the above-mentioned treatment method for gold-containing waste liquid. The device includes an electrolysis device and a resin adsorption device.

其中,电解装置的入口可以直接与镀金工艺的废液槽连通,也可以与第一含金废液的收集槽连通。Wherein, the inlet of the electrolysis device may be directly communicated with the waste liquid tank of the gold plating process, or may be communicated with the collection tank of the first gold-containing waste liquid.

本发明中,电解装置包括电源、电解槽、阴极板、阳极板,阴极板和阳极板均设于电解槽内,阳极板与电源的正极相连,阴极板与电源的负极相连。In the present invention, the electrolysis device includes a power source, an electrolytic cell, a cathode plate, and an anode plate. The cathode plate and the anode plate are both arranged in the electrolytic cell, the anode plate is connected to the positive electrode of the power source, and the cathode plate is connected to the negative electrode of the power source.

本发明中,树脂吸附装置包括吸附罐、以及填充在吸附罐内的树脂,其中树脂可拆卸填充于吸附罐内,吸附罐具体可以是吸附柱。In the present invention, the resin adsorption device includes an adsorption tank and a resin filled in the adsorption tank, wherein the resin is detachably filled in the adsorption tank, and the adsorption tank may be an adsorption column.

在一些实施例中,还包括金回收水洗装置和金缸,其中金回收水洗装置用于清洗经电解处理后产生的沉积物金,金缸用于收集回收的金,金回收水洗装置的入口连通于电解装置的固体出口,金缸连通于金回收水洗装置。In some embodiments, a gold recovery water washing device and a gold tank are also included, wherein the gold recovery water washing device is used for cleaning the deposited gold produced after electrolytic treatment, the gold tank is used for collecting the recovered gold, and the inlet of the gold recovery water washing device is communicated with At the solid outlet of the electrolysis device, the gold tank is communicated with the gold recovery water washing device.

在上述实施例中,第一含金废液的收集槽用于收集第一含金废液。第一含金废液的收集槽连通于电解装置的入口,收集槽内的第一含金废液可以经由电解装置的入口通入电解装置的电解槽内。In the above embodiment, the collecting tank of the first gold-containing waste liquid is used to collect the first gold-containing waste liquid. The collection tank of the first gold-containing waste liquid is communicated with the inlet of the electrolysis device, and the first gold-containing waste liquid in the collection tank can be passed into the electrolysis tank of the electrolysis device through the inlet of the electrolysis device.

在一些实施例中,树脂吸附装置用于对电解残余液进行吸附处理,树脂吸附装置的入口与电解装置的液体出口连通。In some embodiments, the resin adsorption device is used for adsorption treatment of the electrolysis residual liquid, and the inlet of the resin adsorption device is communicated with the liquid outlet of the electrolysis device.

在本发明的具体实施过程中,电解残余液从电解装置的液体出口排出,从而使得电解残余液经由液体出口,流至树脂吸附装置内进行吸附处理。In the specific implementation process of the present invention, the electrolysis residual liquid is discharged from the liquid outlet of the electrolysis device, so that the electrolytic residual liquid flows through the liquid outlet to the resin adsorption device for adsorption treatment.

在上述实施例中,本发明的连通可以管道连通。In the above-described embodiments, the communication of the present invention may be ducted.

在上述实施例中,还包括第一过滤装置,第一过滤装置设置电解装置之前,用于过滤掉第一含金废液中的固体颗粒等杂质。在一些实施例中,第一过滤装置的入口连通于第一含金废液的收集槽,第一过滤装置的液体出口连通于电解装置的入口。In the above-mentioned embodiment, a first filter device is also included, and before the first filter device is installed in the electrolysis device, it is used to filter out impurities such as solid particles in the first gold-containing waste liquid. In some embodiments, the inlet of the first filtering device is communicated with the collection tank of the first gold-containing waste liquid, and the liquid outlet of the first filtering device is communicated with the inlet of the electrolysis device.

在一些实施例中,还包括水洗装置,水洗装置包括一级水洗槽和二级水洗槽,一级水洗槽和二级水洗槽依次排列设置。In some embodiments, a water washing device is also included, and the water washing device includes a primary water washing tank and a secondary water washing tank, and the primary water washing tank and the secondary water washing tank are arranged in sequence.

在上述实施例中,水洗装置用于对镀金处理后的线路板进行水洗,得到水洗后的线路板和第二含金废液。In the above embodiment, the water washing device is used to wash the gold-plated circuit board with water to obtain the washed circuit board and the second gold-containing waste liquid.

在一些实施例中,一级水洗槽的侧壁上设置有一级进水口和一级排水口,二级水洗槽的侧壁上设置有二级进水口和二级排水口;一级水洗槽的一级排水口连通于树脂吸收装置。In some embodiments, a primary water inlet and a primary water outlet are provided on the side wall of the primary water washing tank, and a secondary water inlet and a secondary water outlet are provided on the side wall of the secondary water washing tank; The primary water outlet is communicated with the resin absorption device.

在上述实施例中,二级排水口的高度不高于二级进水口的高度,一级排水口的高度不高于一级进水口的高度。In the above embodiment, the height of the secondary water outlet is not higher than the height of the secondary water inlet, and the height of the primary water outlet is not higher than the height of the primary water inlet.

在上述实施例中,二级排水口所在的高度高于一级进水口的高度,二级排水口与一级进水口通过管道连通。In the above embodiment, the height of the secondary water outlet is higher than the height of the primary water inlet, and the secondary water outlet and the primary water inlet are communicated with each other through pipes.

本发明中,水洗装置的入口是二级水洗槽的二级进水口,水洗装置的出口是一级水洗槽的一级排水口。In the present invention, the inlet of the water washing device is the secondary water inlet of the secondary water washing tank, and the outlet of the water washing device is the primary water outlet of the primary water washing tank.

在一些实施例中,清洗液的流向为:从二级水洗槽的二级进水口进入,依次流经二级水洗槽、一级水洗槽,最后从一级水洗槽的一级排水口排出。In some embodiments, the flow direction of the cleaning liquid is as follows: entering from the secondary water inlet of the secondary washing tank, flowing through the secondary washing tank and the primary washing tank in sequence, and finally discharging from the primary drainage port of the primary washing tank.

在本发明的具体实施过程中,清洗液先从二级进水口流入二级水洗槽,当二级水洗槽内的水高度超过二级排水口的高度后,清洗液从二级水洗槽溢流至一级水洗槽,当一级水洗槽内的水高度超过一级排水口的高度后,从一级水洗槽排出。In the specific implementation process of the present invention, the cleaning liquid first flows into the secondary washing tank from the secondary water inlet, and when the water level in the secondary washing tank exceeds the height of the secondary water outlet, the cleaning liquid overflows from the secondary washing tank To the first-level washing tank, when the water level in the first-level washing tank exceeds the height of the first-level drain outlet, it will be discharged from the first-level washing tank.

本发明中,清洗线路板时,镀金处理后的线路板的进入顺序与清洗液的流向相反。镀金处理后的线路板依次流经一级水洗槽、二级水洗槽,即线路板首先在一级水洗槽内进行水洗(清洗),清洗后,再移动至二级水洗槽内进行清洗。In the present invention, when cleaning the circuit board, the entering sequence of the circuit board after gold plating is opposite to the flow direction of the cleaning solution. The gold-plated circuit board flows through the first-level washing tank and the second-level washing tank in sequence, that is, the circuit board is first washed (cleaned) in the first-level washing tank, and then moved to the second-level washing tank for cleaning after cleaning.

在上述实施例中,线路板从一级水洗槽的一级排出口进入,依次经过一级水洗槽、二级水洗槽,最后从二级水洗槽的二级进水口排出。In the above embodiment, the circuit board enters from the primary discharge port of the primary washing tank, passes through the primary washing tank and the secondary washing tank in sequence, and finally discharges from the secondary water inlet of the secondary washing tank.

上述实施例中,采用该水洗装置对线路板进行水洗时,可以先使清洗液依次流经二级水洗槽、一级水洗槽后,再将线路板进入水洗装置中进行清洗,清洗完毕后,从一级排水口排出的液体为第二含金废液。In the above embodiment, when using the water washing device to wash the circuit board, the cleaning solution can be made to flow through the secondary water washing tank and the primary water washing tank in sequence, and then the circuit board enters the water washing device for cleaning. After cleaning, The liquid discharged from the primary water outlet is the second gold-containing waste liquid.

在上述实施例中,清洗液从二级水洗槽流入到一级水洗槽的过程中,清洗液逐渐浑浊,因此,当线路板进入的顺序与清洗液的流向相反时,线路板由一级水洗槽进入时,可以使用较浊的清洗液先清洗较脏的线路板,随着线路板进入二级水洗槽中清洗,线路板越来越洁净,清洗液也越来越清洁,对线路板的清洗效果也更好,并且可以节约清洗液。In the above embodiment, in the process of the cleaning liquid flowing from the secondary washing tank to the primary washing tank, the cleaning liquid is gradually turbid. Therefore, when the circuit board enters in the opposite direction to the cleaning liquid, the circuit board is washed by the primary water. When the tank enters, you can use the turbid cleaning solution to clean the dirty circuit board first. As the circuit board enters the secondary washing tank for cleaning, the circuit board becomes cleaner and the cleaning solution is cleaner The cleaning effect is also better and the cleaning fluid can be saved.

本发明中,通过设置两个水洗槽对线路板进行清洗,采用溢流水洗这种清洗方式,不仅清洗效果好,而且节省了大量的清洗液,降低了生产成本,利于节能减排。In the present invention, the circuit board is cleaned by setting two water washing tanks, and the overflow water washing is used to clean the circuit board, which not only has a good cleaning effect, but also saves a large amount of cleaning liquid, reduces the production cost, and is conducive to energy saving and emission reduction.

在一些实施例中,还包括储液装置,储液装置用于临时容置第二含金废液,当储液装置中第二含金废液的量满足一定体积时,使第二含金废液流至树脂吸附装置。In some embodiments, a liquid storage device is further included, the liquid storage device is used to temporarily accommodate the second gold-containing waste liquid, and when the amount of the second gold-containing waste liquid in the liquid storage device meets a certain volume, the second gold-containing waste liquid is The waste liquid flows to the resin adsorption device.

在上述实施例中,储液装置的入口连通于水洗装置的出口,储液装置的出口连通于树脂吸收装置。In the above embodiment, the inlet of the liquid storage device is communicated with the outlet of the water washing device, and the outlet of the liquid storage device is communicated with the resin absorption device.

在本发明的具体实施过程中,使水洗装置中产生的第二含金废液流入储液装置中,再将第二含金废液从储液装置的出口输送到树脂吸收装置中进行吸附处理。In the specific implementation process of the present invention, the second gold-containing waste liquid generated in the water washing device flows into the liquid storage device, and then the second gold-containing waste liquid is transported from the outlet of the liquid storage device to the resin absorption device for adsorption treatment. .

在一些实施例中,树脂吸附装置用于对第二含金废液进行吸附处理,树脂吸附装置内设有吸附树脂,树脂吸附装置的入口与储液装置的出口连通。In some embodiments, the resin adsorption device is used for adsorption treatment of the second gold-containing waste liquid, the resin adsorption device is provided with an adsorption resin, and the inlet of the resin adsorption device is communicated with the outlet of the liquid storage device.

在本发明的具体实施过程中,第二含金废液从储液装置的出口排出,流至树脂吸附装置内进行吸附处理。第二含金废液中的金被吸附在树脂上,形成载金树脂,吸附残余液可以直接从树脂吸附装置的出口排出。In the specific implementation process of the present invention, the second gold-containing waste liquid is discharged from the outlet of the liquid storage device and flows into the resin adsorption device for adsorption treatment. The gold in the second gold-containing waste liquid is adsorbed on the resin to form a gold-loaded resin, and the adsorption residual liquid can be directly discharged from the outlet of the resin adsorption device.

在上述实施例中,当载金树脂的吸附量达到树脂的饱和吸附量时,需要将树脂吸附装置内的载金树脂拆卸下来,更换新的树脂,然后对拆卸下来的载金树脂进行解吸和再生。In the above embodiment, when the adsorption capacity of the gold-loaded resin reaches the saturated adsorption capacity of the resin, the gold-loaded resin in the resin adsorption device needs to be disassembled, replaced with a new resin, and then desorbed and removed from the gold-loaded resin. regeneration.

在一些实施例中,上述处理系统还包括第二过滤装置,用于对第二含金废液进行过滤处理,以去除第二含金废液中的固体杂质、泥沙等,防止进入树脂吸附装置中对树脂造成堵塞,影响树脂吸附金的性能。In some embodiments, the above-mentioned treatment system further includes a second filtering device for filtering the second gold-containing waste liquid, so as to remove solid impurities, sediment, etc. in the second gold-containing waste liquid, and prevent them from entering into resin adsorption The resin is blocked in the device, which affects the performance of the resin to adsorb gold.

在上述实施例中,第二过滤装置的入口连通于储液罐的出口,第二过滤装置的液体出口与树脂吸附罐的入口连通。In the above embodiment, the inlet of the second filter device is communicated with the outlet of the liquid storage tank, and the liquid outlet of the second filter device is communicated with the inlet of the resin adsorption tank.

本发明中,第一含金废液的收集槽不间断地向电解装置中通入第一含金废液,电解装置不间断地对第一含金废液进行电解处理,水洗装置不间断地对线路板进行水洗处理,可以将上述不间断运行的处理系统与线路板的制造生产线联合使用,实现大规模推广应用。In the present invention, the collection tank of the first gold-containing waste liquid continuously feeds the first gold-containing waste liquid into the electrolysis device, the electrolysis device continuously electrolyzes the first gold-containing waste liquid, and the water washing device continuously The circuit board is washed with water, and the above-mentioned uninterrupted operation processing system can be combined with the circuit board manufacturing production line to realize large-scale popularization and application.

本发明提供的含金废液的处理系统结构简单,使用方便快捷,能够用于处理含金废液,回收含金废液中的金,同时进一步降低含金废液中的金含量,该处理系统能够与线路板的表面镀金、沉金、化金处理生产线联合使用。The gold-containing waste liquid treatment system provided by the invention has a simple structure, is convenient and quick to use, and can be used to treat the gold-containing waste liquid, recover the gold in the gold-containing waste liquid, and at the same time further reduce the gold content in the gold-containing waste liquid. The system can be used in conjunction with the surface gold plating, immersion gold and chemical gold processing production lines of circuit boards.

为使本发明的目的、技术方案和优点更加清楚,下面将结合本发明的实施例,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below in conjunction with the embodiments of the present invention. Obviously, the described embodiments are part of the implementation of the present invention. examples, but not all examples. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

实施例1Example 1

本实施例的含金废液的处理系统如图3所示,包括:The treatment system of the gold-containing waste liquid of the present embodiment is shown in Figure 3, including:

第一含金废液收集槽1,用于收集第一含金废水;The first gold-containing waste liquid collection tank 1 is used to collect the first gold-containing waste water;

水洗装置2,包括依次排列的一级水洗槽3、二级水洗槽4;用于对线路板进行水洗处理;The water washing device 2 includes a first-level washing tank 3 and a second-level washing tank 4 arranged in sequence; it is used for washing the circuit board;

储液装置5,用于容置水洗处理后产生的第二含金废液;储液装置5的入口连通于水洗装置2的出口;The liquid storage device 5 is used for accommodating the second gold-containing waste liquid generated after the water washing treatment; the inlet of the liquid storage device 5 is connected to the outlet of the water washing device 2;

第一过滤装置6,用于去除第一含金废液中的固体杂质、泥沙等;第一过滤装置6的入口连通于第一含金废液收集槽1;The first filter device 6 is used to remove solid impurities, sediment, etc. in the first gold-containing waste liquid; the inlet of the first filter device 6 is connected to the first gold-containing waste liquid collection tank 1;

第二过滤装置7,用于去除第二含金废液中的固体杂质、泥沙等;第二过滤装置7的入口连通于储液装置5的出口;The second filter device 7 is used to remove solid impurities, sediment, etc. in the second gold-containing waste liquid; the inlet of the second filter device 7 is connected to the outlet of the liquid storage device 5;

电解装置8,用于对经过滤后的第一含金废液进行电解处理;电解装置8的入口连通于第一过滤装置6的液体出口;The electrolysis device 8 is used for electrolyzing the filtered first gold-containing waste liquid; the inlet of the electrolysis device 8 is communicated with the liquid outlet of the first filter device 6;

树脂吸附装置9,用于对电解残余液和过滤后的第二含金废液进行吸附处理;树脂吸附装置9的入口分别连通于电解装置8的液体出口、第二过滤装置7的液体出口;The resin adsorption device 9 is used to carry out adsorption treatment to the electrolysis residual liquid and the filtered second gold-containing waste liquid; the inlet of the resin adsorption device 9 is respectively connected to the liquid outlet of the electrolysis device 8 and the liquid outlet of the second filter device 7;

金回收水洗装置10,用于对电解处理沉积在阴极的沉积物金进行清洗;The gold recovery water washing device 10 is used to clean the deposited gold deposited on the cathode by electrolytic treatment;

金缸11,用于收集经清洗后的金。The gold vat 11 is used to collect the cleaned gold.

本实施例的含金废液的处理方法在上述处理系统中进行,包括:The processing method of the gold-containing waste liquid of the present embodiment is carried out in the above-mentioned processing system, including:

将第一含金废液收集槽内第一含金废液(金浓度为0.4g/L-1.2g/L,控制中值为0.8g/L),通入第一过滤装置中,经过滤后,流至电解装置中进行电解处理,控制电解处理中温度为50℃,电压为2-3V,电流为3-5A;经电解处理后,测得电解残余液中平均金浓度为0.0166g/L;The first gold-containing waste liquid in the first gold-containing waste liquid collection tank (the gold concentration is 0.4g/L-1.2g/L, and the control median value is 0.8g/L) is passed into the first filter device, and filtered. Then, flow to the electrolysis device for electrolysis treatment, and control the temperature in the electrolysis treatment to be 50° C., the voltage to be 2-3V, and the current to be 3-5A; after the electrolysis treatment, the average gold concentration in the electrolysis residual liquid was measured to be 0.0166g/ L;

然后将电解残余液经电解装置的液体出口排出,流至树脂吸收装置中进行吸附处理;控制吸附处理的流体的流速为1000L/h-1500L/h,Then the electrolytic residual liquid is discharged through the liquid outlet of the electrolysis device, and flows to the resin absorption device for adsorption treatment; the flow rate of the fluid for the adsorption treatment is controlled to be 1000L/h-1500L/h,

使清洁液自二级进水口进入,依次流经二级水洗槽、一级水洗槽;将线路板输送至水洗装置中进行水洗,依次流经一级水洗槽、二级水洗槽,水洗产生的二含金废液自一级排水口排出,流至储液装置、第二过滤装置,经过滤后,流至树脂吸收装置中进行吸附处理;控制吸附处理的流体的流速为1000L/h-1500L/h,经测量,储液装置中的第二含金废液的平均含金浓度为0.004368g/L;The cleaning liquid enters from the secondary water inlet and flows through the secondary washing tank and the primary washing tank in turn; the circuit board is transported to the washing device for washing, and flows through the primary washing tank and the secondary washing tank in turn. The second gold-containing waste liquid is discharged from the first-level drainage port, and flows to the liquid storage device and the second filtering device. After filtering, it flows to the resin absorption device for adsorption treatment; the flow rate of the fluid for adsorption treatment is controlled to be 1000L/h-1500L /h, after measurement, the average gold-containing concentration of the second gold-containing waste liquid in the liquid storage device is 0.004368g/L;

在树脂吸附装置的出口测得吸附残余液中的金浓度为0.00001g/L,可以直接排放入环境中。The gold concentration in the adsorption residual liquid measured at the outlet of the resin adsorption device is 0.00001g/L, which can be directly discharged into the environment.

本发明提供的含金废液的处理方法和处理系统,能够对第一含金废液和第二含金废液中残留金离子进行彻底回收,同时进一步降低含金废液中的金含量,处理后的液体排入环境中不会造成二次污染。The gold-containing waste liquid treatment method and treatment system provided by the invention can thoroughly recover the residual gold ions in the first gold-containing waste liquid and the second gold-containing waste liquid, and at the same time further reduce the gold content in the gold-containing waste liquid, The treated liquid is discharged into the environment without causing secondary pollution.

以上详细描述了本发明的较佳具体实施例以及试验验证。应当理解,本领域的普通技术无需创造性劳动就可以根据本发明的构思作出诸多修改和变化。因此,凡本技术领域中技术人员依本发明的构思在现有技术的基础上通过逻辑分析、推理或者有限的实验可以得到的技术方案,皆应在由权利要求书所确定的保护范围内。The preferred embodiments of the present invention and the experimental verification are described in detail above. It should be understood that many modifications and changes can be made according to the concept of the present invention by those skilled in the art without creative efforts. Therefore, all technical solutions that can be obtained by those skilled in the art through logical analysis, reasoning or limited experiments on the basis of the prior art according to the concept of the present invention shall fall within the protection scope determined by the claims.

Claims (10)

1.一种含金废液的处理方法,其特征在于,包括以下步骤:对第一含金废液进行电解处理,得到金属金和电解残余液;1. a processing method of gold-containing waste liquid, is characterized in that, comprises the following steps: the first gold-containing waste liquid is carried out electrolytic treatment, obtains metallic gold and electrolysis residual liquid; 采用树脂对所述电解残余液和第二含金废液分别进行吸附处理,得到载金树脂和吸附残余液;The electrolysis residual liquid and the second gold-containing waste liquid are respectively subjected to adsorption treatment with resin to obtain gold-loaded resin and adsorption residual liquid; 所述第一含金废液中的金含量大于所述第二含金废液中的金含量。The gold content in the first gold-containing waste liquid is greater than the gold content in the second gold-containing waste liquid. 2.根据权利要求1所述的处理方法,其特征在于,所述电解处理的条件为:电压为2.5-5V,电流为2.5-5V,温度为50-80℃。2 . The treatment method according to claim 1 , wherein the electrolytic treatment conditions are as follows: the voltage is 2.5-5V, the current is 2.5-5V, and the temperature is 50-80° C. 3 . 3.根据权利要求1所述的处理方法,其特征在于,所述树脂包括环氧树脂。3. The processing method of claim 1, wherein the resin comprises an epoxy resin. 4.根据权利要求1所述的处理方法,其特征在于,对所述第一含金废液进行电解处理之前,还包括,对所述第一含金废液进行过滤;4. The processing method according to claim 1, characterized in that, before the first gold-containing waste liquid is electrolyzed, further comprising, filtering the first gold-containing waste liquid; 在采用树脂对所述第二含金废液进行吸附处理之前,还包括:对所述第二含金废液进行过滤。Before performing adsorption treatment on the second gold-containing waste liquid with resin, the method further includes: filtering the second gold-containing waste liquid. 5.根据权利要求1所述的处理方法,其特征在于,所述第一含金废液为对待镀金的线路板进行镀金处理后得到的镀金废液;5. The processing method according to claim 1, wherein the first gold-containing waste liquid is the gold-plated waste liquid obtained after the circuit board to be plated with gold is subjected to gold-plating treatment; 所述第二含金废液经过对镀金处理后的线路板进行水洗处理得到。The second gold-containing waste liquid is obtained by washing the gold-plated circuit board with water. 6.根据权利要求5所述的处理方法,其特征在于,所述水洗处理包括以下步骤:6. processing method according to claim 5, is characterized in that, described washing treatment comprises the following steps: 对镀金处理后的线路板进行一级水洗处理,得到所述第二含金废液和一级水洗后线路板,采用清洗液对一级水洗后线路板进行二级水洗处理,得到二级排水和二级水洗后线路板;The circuit board after the gold-plating treatment is subjected to a primary water washing treatment to obtain the second gold-containing waste liquid and a circuit board after the primary water washing, and the circuit board after the primary water washing is subjected to a secondary water washing treatment with a cleaning solution to obtain a secondary drainage and circuit boards after secondary washing; 采用所述二级排水对所述镀金处理后的线路板进行所述一级水洗处理。The first-level water washing treatment is performed on the gold-plated circuit board by using the second-level drainage. 7.一种含金废液的处理系统,其特征在于,用于实施权利要求1-6任一项所述的含金废液的处理方法,包括:7. A processing system for gold-containing waste liquid, characterized in that, for implementing the processing method of the gold-containing waste liquid according to any one of claims 1-6, comprising: 电解装置和树脂吸附装置,所述电解装置的液相出口与所述树脂吸附装置的入口连通。An electrolysis device and a resin adsorption device, wherein the liquid phase outlet of the electrolysis device is communicated with the inlet of the resin adsorption device. 8.根据权利要求7所述的处理系统,其特征在于,还包括水洗装置,所述水洗装置包括一级水洗槽和二级水洗槽,在二级水洗槽上设置有二级排水口,在重力方向上,所述二级排水口高于所述一级水洗槽的一级进水口;8 . The treatment system according to claim 7 , further comprising a water washing device, wherein the water washing device comprises a primary water washing tank and a secondary water washing tank, and the secondary water washing tank is provided with a secondary water outlet, and the In the direction of gravity, the secondary water outlet is higher than the primary water inlet of the primary washing tank; 在一级水洗槽上设置有一级排水口,所述一级排水口连通于所述树脂吸收装置。The primary water washing tank is provided with a primary water outlet, and the primary water outlet is communicated with the resin absorption device. 9.根据权利要求8所述的处理系统,其特征在于,还包括储液装置,所述储液装置用于容置第二含金废液;9 . The processing system according to claim 8 , further comprising a liquid storage device, wherein the liquid storage device is used for accommodating the second gold-containing waste liquid; 9 . 所述储液装置的入口连通于所述一级排水口的出口,所述储液装置的出口连通于所述树脂吸收装置。The inlet of the liquid storage device is communicated with the outlet of the primary water outlet, and the outlet of the liquid storage device is communicated with the resin absorption device. 10.根据权利要求9所述的处理系统,其特征在于,还包括第一过滤装置和第二过滤装置;10. The processing system of claim 9, further comprising a first filtering device and a second filtering device; 所述第一过滤装置的液体出口连通于所述电解装置的入口;The liquid outlet of the first filtering device is communicated with the inlet of the electrolysis device; 所述第二过滤装置的入口连通于所述储液罐的出口,所述第二过滤装置的液体出口与所述树脂吸附罐的入口连通。The inlet of the second filter device is communicated with the outlet of the liquid storage tank, and the liquid outlet of the second filter device is communicated with the inlet of the resin adsorption tank.
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Publication number Priority date Publication date Assignee Title
CN116926563A (en) * 2023-06-15 2023-10-24 肇庆宏旺金属实业有限公司 Strip pickling waste mixed acid treatment system and method for removing metal ions from waste mixed acid

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Application publication date: 20220930