CN209652000U - A kind of processing system of nickel-containing waste water - Google Patents

A kind of processing system of nickel-containing waste water Download PDF

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Publication number
CN209652000U
CN209652000U CN201821986774.6U CN201821986774U CN209652000U CN 209652000 U CN209652000 U CN 209652000U CN 201821986774 U CN201821986774 U CN 201821986774U CN 209652000 U CN209652000 U CN 209652000U
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storage tank
treatment device
treatment
nickel
water storage
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宁武珍
蒋茂胜
彭胜峰
郑凡
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ZHUHAI SMART TECHNOLOGY Co Ltd
GCI Science and Technology Co Ltd
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ZHUHAI SMART TECHNOLOGY Co Ltd
GCI Science and Technology Co Ltd
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Abstract

本实用新型公开了一种含镍废水的处理系统,包括储存装置、过滤装置、处理装置和管道系统,所述储存装置包括原水储罐、产水储罐和浓水储罐,所述原水储罐、过滤装置和处理装置顺序连接,所述处理装置的产水出口与所述产水储罐连接,所述处理装置的浓水出口与所述浓水储罐连接,所述过滤装置过滤精度为5‑10μ,所述处理装置为反渗透处理装置,所述管道系统用于提供含镍废水处理过程中液体流通的管道。本实用新型采用反渗透的原理,将废水进行浓缩和分离,出水水质稳定且不受废水处理水量的限制,并易于维护;占地面积小,既适用于新建也适用于在原有场地升级改造建设;废水处理过程中无需添加化学药品,对环境污染小,同时本实用新型易于实现自动化。

The utility model discloses a treatment system for nickel-containing waste water, which comprises a storage device, a filter device, a treatment device and a pipeline system. The storage device includes a raw water storage tank, a produced water storage tank and a concentrated water storage tank. The raw water storage tank The tank, filter device and treatment device are connected in sequence, the water product outlet of the treatment device is connected to the product water storage tank, the concentrated water outlet of the treatment device is connected to the concentrated water storage tank, and the filtration accuracy of the filter device is 5-10μ, the treatment device is a reverse osmosis treatment device, and the pipeline system is used to provide pipelines for liquid circulation during the treatment of nickel-containing wastewater. The utility model adopts the principle of reverse osmosis to concentrate and separate the waste water, the water quality of the effluent is stable and not limited by the amount of waste water treatment, and it is easy to maintain; it occupies a small area and is suitable for both new construction and upgrading and reconstruction of the original site There is no need to add chemicals in the waste water treatment process, and the environmental pollution is small, and at the same time, the utility model is easy to realize automation.

Description

一种含镍废水的处理系统A treatment system for nickel-containing wastewater

【技术领域】【Technical field】

本实用新型涉及含镍废水处理相关的技术领域,具体涉及一种含镍废水的处理系统。The utility model relates to the technical field related to the treatment of nickel-containing wastewater, in particular to a treatment system for nickel-containing wastewater.

【背景技术】【Background technique】

现有含镍废水通常是采用化学沉淀的方法进行处理,也有采用树脂吸附的方法处理含镍废水的。化学沉淀是通过调整并控制含镍废水的pH值,同时添加混凝和絮凝物质等,将含镍废水中的镍沉淀下来,再压滤成含镍污泥后,转交给有资质的单位处理。此方法占用场地面积较大,需额外加入大量的化学药品,处理后的废水,出水水质不稳定,很难控制在0.1mg/l以下。树脂吸附是利用树脂对一定化合价态的金属离子的吸附(一般情况下是金属离子与树脂中的氢离子交换吸附)作用,降低含镍废水中的镍离子,树脂吸附饱和后,将含镍树脂委托给有资质的处理单位进行处理。树脂吸附方法处理后的废水受原含镍废水中的镍含量影响比较大,当原含镍废水中的镍含量比较高时,既会影响到树脂吸附的处理效率,严重时,也会导致处理效果变差,即处理后的废水镍含量大于0.1mg/l,且树脂吸附成本较高,一般用于含镍废水产生量比较小的单位。由此可见,无论是采用化学沉淀法,还是树脂吸附法,含镍废水的出水质稳定性比较差。化学沉淀法占用场地面积大,树脂吸附常用于含镍废水量比较小的单位。Existing nickel-containing wastewater is usually treated by chemical precipitation, and some nickel-containing wastewater is treated by resin adsorption. Chemical precipitation is to adjust and control the pH value of nickel-containing wastewater, and at the same time add coagulation and flocculation substances, etc., to precipitate nickel in nickel-containing wastewater, and then filter it into nickel-containing sludge, and then transfer it to a qualified unit for treatment . This method occupies a large area of the site and needs to add a large amount of additional chemicals. The quality of the treated wastewater is unstable and it is difficult to control it below 0.1mg/l. Resin adsorption is the use of resin to adsorb metal ions in a certain valence state (generally, metal ions and hydrogen ion exchange adsorption in the resin) to reduce nickel ions in nickel-containing wastewater. After the resin is saturated, the nickel-containing resin Entrust it to a qualified processing unit for processing. The wastewater treated by the resin adsorption method is greatly affected by the nickel content in the original nickel-containing wastewater. When the nickel content in the original nickel-containing wastewater is relatively high, it will not only affect the treatment efficiency of the resin adsorption, but also lead to serious problems. The effect becomes worse, that is, the nickel content of the treated wastewater is greater than 0.1mg/l, and the resin adsorption cost is relatively high. It is generally used in units with a relatively small amount of nickel-containing wastewater. It can be seen that whether chemical precipitation method or resin adsorption method is used, the effluent quality stability of nickel-containing wastewater is relatively poor. The chemical precipitation method occupies a large area of the site, and resin adsorption is often used in units with a relatively small amount of nickel-containing wastewater.

【实用新型内容】【Content of utility model】

本实用新型提供了一种含镍废水的处理系统及处理方法,采用反渗透的原理对含镍废水进行处理,可有效避免上述两个处理方法在实际运行过程中存在的水质不稳定的问题,且不受含镍废水处理水量的限制,并且场地占用面积小。The utility model provides a treatment system and treatment method for nickel-containing wastewater. The principle of reverse osmosis is used to treat nickel-containing wastewater, which can effectively avoid the problem of unstable water quality in the actual operation of the above two treatment methods. And it is not limited by the amount of nickel-containing wastewater treatment, and the site occupies a small area.

为了解决现有技术中的上述问题,本实用新型的目的在于提供一种含镍废水的处理系统,主要的技术方案如下:In order to solve the above problems in the prior art, the purpose of this utility model is to provide a treatment system for nickel-containing waste water, the main technical solutions are as follows:

一种含镍废水的处理系统,包括储存装置、过滤装置、处理装置和管道系统,所述储存装置包括原水储罐、产水储罐和浓水储罐,所述原水储罐、过滤装置和处理装置顺序连接,所述处理装置的产水出口与所述产水储罐连接,所述处理装置的浓水出口与所述浓水储罐连接,所述处理装置为反渗透处理装置,所述管道系统用于提供含镍废水处理过程中液体流通的管道。A treatment system for nickel-containing wastewater, comprising a storage device, a filter device, a treatment device and a piping system, the storage device includes a raw water storage tank, a produced water storage tank and a concentrated water storage tank, the raw water storage tank, the filtering device and The processing devices are connected sequentially, the water product outlet of the processing device is connected to the water product storage tank, the concentrated water outlet of the processing device is connected to the concentrated water storage tank, the processing device is a reverse osmosis processing device, and the The pipeline system described above is used to provide pipelines for liquid circulation during the treatment of nickel-containing wastewater.

进一步地,所述含镍废水的处理系统还包括增压装置,所述增压装置设于过滤装置和处理装置之间,用于给所述反渗透处理装置增压。Further, the treatment system for nickel-containing wastewater also includes a booster device, which is arranged between the filter device and the treatment device, and is used to pressurize the reverse osmosis treatment device.

进一步地,所述处理装置包括一级处理装置、二级处理装置和三级处理装置,所述一级处理装置的产水出口和浓水出口分别与所述三级处理装置和所述二级处理装置的入口连接,所述三级处理装置的产水出口和浓水出口分别与所述产水储罐和所述原水储罐连接;所述二级处理装置的产水出口和浓水出口分别与所述原水储罐和浓水储罐连接。Further, the treatment device includes a primary treatment device, a secondary treatment device and a tertiary treatment device, and the product water outlet and the concentrated water outlet of the primary treatment device are connected to the tertiary treatment device and the secondary treatment device respectively. The inlet of the treatment device is connected, and the product water outlet and concentrated water outlet of the tertiary treatment device are respectively connected with the product water storage tank and the raw water storage tank; the product water outlet and concentrated water outlet of the secondary treatment device They are respectively connected with the raw water storage tank and the concentrated water storage tank.

进一步地,所述含镍废水的处理系统还包括中间储罐,所述处理装置包括一级处理装置、二级处理装置和三级处理装置,所述中间储罐用于储存含镍废水经所述一级处理装置后的产水,所述中间储罐中的产水再进入三级处理装置进行处理。Further, the treatment system of the nickel-containing wastewater also includes an intermediate storage tank, and the treatment device includes a primary treatment device, a secondary treatment device and a tertiary treatment device, and the intermediate storage tank is used to store the nickel-containing wastewater through the The produced water after the primary treatment device, and the produced water in the intermediate storage tank enters the tertiary treatment device for treatment.

进一步地,所述一级处理装置、二级处理装置和三级处理装置分别设有一级RO膜、二级RO膜和三级RO膜,其中,所述一级RO膜为抗污染膜,二级RO膜为海水淡化膜,所述三级RO膜为常规RO膜。Further, the primary processing device, secondary processing device and tertiary processing device are respectively provided with a primary RO membrane, a secondary RO membrane and a tertiary RO membrane, wherein the primary RO membrane is an anti-pollution membrane, and the secondary RO membrane is an anti-pollution membrane. The first-stage RO membrane is a seawater desalination membrane, and the third-stage RO membrane is a conventional RO membrane.

进一步地,所述过滤装置为过滤泵,所述过滤装置过滤精度为5-10μ。Further, the filtering device is a filtering pump, and the filtering precision of the filtering device is 5-10 μ.

进一步地,所述含镍废水的处理系统还包括PLCS控制系统。Further, the nickel-containing wastewater treatment system also includes a PLCS control system.

进一步地,所述含镍废水的处理系统还包括清洗装置,所述清洗装置包括药水储罐,所述药水储罐与处理装置连接。Further, the treatment system for nickel-containing wastewater also includes a cleaning device, the cleaning device includes a liquid medicine storage tank, and the liquid medicine storage tank is connected to the treatment device.

本实用新型还提供了一种含镍废水的处理方法,该处理方法使用上述所述的含镍废水的处理系统进行处理。The utility model also provides a treatment method for nickel-containing wastewater, which uses the above-mentioned nickel-containing wastewater treatment system for treatment.

进一步地,所述含镍废水的处理方法包括以下步骤:Further, the treatment method of described nickel-containing wastewater comprises the following steps:

①废水收集:将含镍废水集中收集到原水储罐中;①Wastewater collection: Collect nickel-containing wastewater into raw water storage tanks;

②废水处理:将原水储罐中的含镍废水经过滤装置初步过滤后进入处理装置,经处理装置进行反渗透处理后,产水进入产水储罐中,浓水进入浓水储罐中。②Wastewater treatment: The nickel-containing wastewater in the raw water storage tank is initially filtered by the filter device and then enters the treatment device. After reverse osmosis treatment by the treatment device, the produced water enters the produced water storage tank, and the concentrated water enters the concentrated water storage tank.

相较于现有技术,本实用新型的有益效果在于:Compared with the prior art, the utility model has the beneficial effects of:

①使用反渗透的原理,将含镍废水进行浓缩和分离,出水水质稳定且不受含镍废水处理水量的限制,并且易于维护;① Using the principle of reverse osmosis to concentrate and separate nickel-containing wastewater, the effluent quality is stable and not limited by the amount of nickel-containing wastewater treated, and it is easy to maintain;

②本处理装置占地面积小,既适用于新项目建设,也适用于在原有的场地升级改造建设;② The treatment device occupies a small area, which is suitable for both new project construction and upgrading and reconstruction of the original site;

③本实用新型所提供的含镍废水的处理系统运行过程中无需添加化学药品,对环境污染小;③ The nickel-containing wastewater treatment system provided by the utility model does not need to add chemicals during operation, and has little environmental pollution;

④本实用新型所提供的含镍废水的处理系统易于实现自动化。④ The treatment system of nickel-containing wastewater provided by the utility model is easy to realize automation.

【附图说明】【Description of drawings】

图1为本实用新型的结构示意图;Fig. 1 is the structural representation of the utility model;

图2为实施例1的具体结构示意图;Fig. 2 is the specific structural representation of embodiment 1;

图3为实施例2的具体结构示意图Fig. 3 is the specific structural representation of embodiment 2

其中,1、储存装置;11、原水储罐;12、产水储罐;13、浓水储罐;14、中间储罐;2、处理装置;21/210、一级处理装置;22/220、二级处理装置;23/230、三级处理装置;3、过滤装置;31、第一过滤装置;32、第二过滤装置;33、第三过滤装置;4、增压装置;41/410、第一增压装置;42/420、第二增压装置;43/430、第三增压装置。Among them, 1. storage device; 11. raw water storage tank; 12. produced water storage tank; 13. concentrated water storage tank; 14. intermediate storage tank; 2. processing device; 21/210, primary processing device; 22/220 , secondary processing device; 23/230, tertiary processing device; 3, filtering device; 31, first filtering device; 32, second filtering device; 33, third filtering device; 4, booster device; 41/410 , the first supercharging device; 42/420, the second supercharging device; 43/430, the third supercharging device.

【具体实施方式】【Detailed ways】

为了使本实用新型的目的、技术方案及优点更加清楚明白,以下结合附图及实施例,对本实用新型进行进一步详细说明。应当理解,此处所描述的具体实施例仅用以解释本实用新型,并不用于限定本实用新型。In order to make the purpose, technical solution and advantages of the utility model clearer, the utility model will be further described in detail below in conjunction with the accompanying drawings and embodiments. It should be understood that the specific embodiments described here are only used to explain the utility model, and are not intended to limit the utility model.

实施例1Example 1

如图1所示,一种含镍废水的处理系统,包括储存装置1、过滤装置3、处理装置2和管道系统(图中未标识),所述储存装置1包括原水储罐11、产水储罐12和浓水储罐13,所述原水储罐11、过滤装置3和处理装置2顺序连接,所述处理装置2的产水出口与所述产水储罐12连接,所述处理装置2的浓水出口与所述浓水储罐13连接,所述处理装置2为反渗透处理装置,所述管道系统用于提供含镍废水处理过程中液体流通的管道。As shown in Figure 1, a kind of treatment system of nickel-containing wastewater comprises a storage device 1, a filter device 3, a treatment device 2 and a pipeline system (not marked in the figure), and the storage device 1 includes a raw water storage tank 11, a produced water The storage tank 12 and the concentrated water storage tank 13, the raw water storage tank 11, the filtering device 3 and the processing device 2 are connected in sequence, the water production outlet of the processing device 2 is connected with the water production storage tank 12, and the processing device The concentrated water outlet of 2 is connected to the concentrated water storage tank 13, the treatment device 2 is a reverse osmosis treatment device, and the pipeline system is used to provide pipelines for liquid circulation during the treatment of nickel-containing wastewater.

具体结构可以为:储罐装置1还包括中间储罐14和增压装置,处理装置2包括一级处理装置21、二级处理装置22和三级处理装置23,一级处理装置21、二级处理装置22和三级处理装置23分别设有一级RO膜、二级RO膜和三级RO膜,其中,一级RO膜为抗污染膜,脱盐率可达99%;二级RO膜为海水淡化膜,脱盐率可达99.5%;三级RO膜为常规反渗透膜,如低压高脱盐反渗透膜、ESPA系列超低压大通量反渗透膜、陶氏工业用苦咸水渗透膜等,脱盐率可达99%;过滤装置3包括第一过滤装置31、第二过滤装置32和第三过滤装置33,过滤装置3为过滤泵,过滤装置3的过滤精度为5-10μ;增压装置包括第一增压装置41、第二增压装置42和第三增压装置43,增压装置为立式长轴增压泵。The specific structure can be as follows: the storage tank device 1 also includes an intermediate storage tank 14 and a pressurization device, the processing device 2 includes a primary processing device 21, a secondary processing device 22 and a tertiary processing device 23, the primary processing device 21, the secondary processing device The processing device 22 and the tertiary processing device 23 are respectively equipped with a primary RO membrane, a secondary RO membrane and a tertiary RO membrane. Among them, the primary RO membrane is an anti-pollution membrane, and the desalination rate can reach 99%; the secondary RO membrane is seawater The desalination membrane has a desalination rate of up to 99.5%; the third-stage RO membrane is a conventional reverse osmosis membrane, such as a low-pressure high-desalination reverse osmosis membrane, ESPA series ultra-low pressure and high-flux reverse osmosis membrane, Dow industrial brackish water permeable membrane, etc. The desalination rate can reach 99%; the filter device 3 includes a first filter device 31, a second filter device 32 and a third filter device 33, the filter device 3 is a filter pump, and the filtration accuracy of the filter device 3 is 5-10μ; the booster device It includes a first booster 41 , a second booster 42 and a third booster 43 , and the booster is a vertical long-axis booster pump.

进一步地,具体的连接结构为:如图2所示,原水储罐11、第一过滤装置31、第一增压装置41和一级处理装置21通过管道依次连接,一级处理系统21的浓水出口和产水出口分别与浓水储罐13和中间储罐14连接,即原水储罐11中的含镍废水经第一过滤装置31初步过滤后,进入一级处理装置21进行处理,经一级处理装置21处理后的产水进入中间储罐14,浓水进入浓水储罐13;中间储罐14、三级过滤装置33、三级增压装置43和三级处理装置23通过管道依次连接,三级处理装置23的浓水出口和产水出口分别与原水储罐11和产水储罐12连接,即经一级处理装置21处理后进入中间储罐14的产水再经三级过滤装置33后进入三级处理装置23进行处理,三级处理装置23处理后,产水进入产水储罐12,浓水回到原水储罐11;而经一级处理装置21处理后进入浓水储罐13的浓水,再经二级过滤装置32后进入二级处理装置22进行处理,产水进入原水储罐11,浓水回到浓水储罐13。整个含镍废水处理的过程中,过滤装置3即第一过滤装置31、第二过滤装置32和第三过滤装置33的主要作用在于对进入一级处理装置21、二级处理装置22和三级处理装置23的液体进行初步过滤,过滤掉大颗粒物质的同时不影响废液流动的正常速率,保证废液按原有的速度进入处理装置,增压装置4即第一增压装置41、第二增压装置42和第三增压装置43主要用于给处理装置2增压,使处理装置2的反渗透处理更顺畅。Further, the specific connection structure is as follows: as shown in Figure 2, the raw water storage tank 11, the first filtering device 31, the first pressurizing device 41 and the primary treatment device 21 are connected sequentially through pipelines, and the concentration of the primary treatment system 21 is The water outlet and the produced water outlet are respectively connected to the concentrated water storage tank 13 and the intermediate storage tank 14, that is, the nickel-containing wastewater in the raw water storage tank 11 is initially filtered by the first filter device 31, and then enters the primary treatment device 21 for treatment. The product water treated by the primary treatment device 21 enters the intermediate storage tank 14, and the concentrated water enters the concentrated water storage tank 13; the intermediate storage tank 14, the tertiary filtering device 33, the tertiary booster device 43 and the tertiary processing device 23 pass through the pipeline connected in sequence, the concentrated water outlet and the product water outlet of the third-stage treatment device 23 are respectively connected to the raw water storage tank 11 and the product water storage tank 12, that is, the product water that enters the intermediate storage tank 14 after being treated by the primary treatment device 21 is then passed through the third stage. After the three-stage filter device 33, it enters the three-stage treatment device 23 for processing. After the three-stage treatment device 23 is processed, the produced water enters the product water storage tank 12, and the concentrated water returns to the raw water storage tank 11; The concentrated water in the concentrated water storage tank 13 enters the secondary treatment device 22 for treatment after passing through the secondary filter device 32 , the produced water enters the raw water storage tank 11 , and the concentrated water returns to the concentrated water storage tank 13 . In the process of the whole nickel-containing wastewater treatment, the main function of the filter device 3, that is, the first filter device 31, the second filter device 32 and the third filter device 33, is to treat the primary treatment device 21, the secondary treatment device 22 and the tertiary treatment device. The liquid in the processing device 23 is initially filtered to filter out large particles while not affecting the normal flow rate of the waste liquid, ensuring that the waste liquid enters the processing device at the original speed. The booster 4 is the first booster 41, the second booster The second pressurization device 42 and the third pressurization device 43 are mainly used to pressurize the processing device 2 to make the reverse osmosis treatment of the processing device 2 smoother.

一种含镍废水的处理方法,该处理方法使用上述的处理装置进行含镍废水的处理。就本实施例的具体结构而言,处理步骤如下:①原水储罐11中的含镍废水经第一过滤装置31初步过滤后进入一级处理装置11,经一级处理装置11处理后产水进入中间储罐14、浓水进入浓水储罐13。A treatment method for nickel-containing wastewater, which uses the above-mentioned treatment device to treat nickel-containing wastewater. As far as the specific structure of this embodiment is concerned, the treatment steps are as follows: ① The nickel-containing wastewater in the raw water storage tank 11 is initially filtered by the first filter device 31 and then enters the primary treatment device 11, and after being treated by the primary treatment device 11, water is produced Enter the intermediate storage tank 14, concentrated water enters the concentrated water storage tank 13.

②中间储罐14中的产水经第三过滤装置33后进入三级处理装置23,经三级处理装置33处理后产水进入产水储罐12、浓水进入浓水储罐;步骤①中进入浓水储罐13的浓水经第二过滤装置32初步过滤后进入二级处理装置22,经二级处理装置22处理后产水进入原水储罐11、浓水进入浓水储罐12。②The produced water in the intermediate storage tank 14 enters the tertiary treatment device 23 after passing through the third filtering device 33, and after being treated by the tertiary treatment device 33, the produced water enters the produced water storage tank 12, and concentrated water enters the concentrated water storage tank; step ① The concentrated water entering the concentrated water storage tank 13 is preliminarily filtered by the second filter device 32 and then enters the secondary treatment device 22. After being treated by the secondary treatment device 22, the produced water enters the raw water storage tank 11, and the concentrated water enters the concentrated water storage tank 12. .

含镍废水经上述处理系统和处理方法进行处理后,进入产水储罐12的产水经检测(检测方法依照《GB 11912-1989水质镍的测定火焰原子吸收分光光度法》或《水质32种元素的测定电感耦合等离子体发射光谱法HJ776-2015》的标准进行检测),镍含量小于0.1㎎/L,根据《电镀污染物排放标准》(GB21900-2008)的规定,符合排放标准,可直接排放;进入浓水储罐13的浓水经不断检测,当电导率超过22000μs/cm时,浓水中镍含量可达450-550㎎/L,此时可将浓水转移委外给有资质的单位收集处理。After the nickel-containing wastewater is treated by the above-mentioned treatment system and treatment method, the product water entering the product water storage tank 12 is detected (the detection method is in accordance with "GB 11912-1989 Determination of Nickel in Water Quality by Flame Atomic Absorption Spectrophotometry" or "32 Types of Water Quality Determination of elements by Inductively Coupled Plasma Emission Spectrometry HJ776-2015 "Standard detection), the nickel content is less than 0.1㎎/L, according to the provisions of the "Electroplating Pollutant Discharge Standard" (GB21900-2008), in line with the emission standards, can be directly Discharge; the concentrated water entering the concentrated water storage tank 13 is continuously tested. When the conductivity exceeds 22000μs/cm, the nickel content in the concentrated water can reach 450-550㎎/L. At this time, the concentrated water can be transferred to qualified personnel Unit collection processing.

作为优选的实施方式之一,分别在原水储罐11、产水储罐12、浓水储罐13和中间储罐14中安装电导率探测头,通过通信线路将各个储罐中的检测数据传输至电导率仪,可实时监控各个储罐中的电导率。电导率仪主要用于监控处理系统是否正常运行,当产水储罐12中的电导率超过200us/cm时,可说明处理系统出现问题,需要分析查找原因并解决。As one of the preferred embodiments, the conductivity probes are respectively installed in the raw water storage tank 11, the produced water storage tank 12, the concentrated water storage tank 13 and the intermediate storage tank 14, and the detection data in each storage tank are transmitted through the communication line. To the conductivity meter, the conductivity in each storage tank can be monitored in real time. The conductivity meter is mainly used to monitor whether the treatment system is running normally. When the conductivity in the product water storage tank 12 exceeds 200us/cm, it can indicate that there is a problem in the treatment system, which needs to be analyzed to find out the cause and solve it.

进一步地,上述的处理系统还可包括PLCS控制系统,用于实现处理系统的自动化。Further, the above-mentioned processing system may also include a PLCS control system for realizing automation of the processing system.

进一步地,还可以包括清洗装置,清洗装置包括药水储罐,药水储罐用于配置清洗药水,药水储罐、过滤装置3和处理装置2依次连接,将处理装置进行清洗后,浓水和产水均回到药水储罐中,循环使用。就本实施例的具体结构,第一过滤装置31、第一增压装置41和一级处理装置21、第二过滤装置32、第二增压装置42和二级处理装置22以及第三过滤装置33、第三增压装置43和三级处理装置23分别串联后,再连接药水储罐,一级处理装置21、二级处理装置22和三级处理装置23的浓水和产水出口均与药水储罐连接,即药水储罐中的药水分别经第一过滤装置31、第二过滤装置32和第三过滤装置33后进入一级处理装置21、二级处理装置22和三级处理23装置对处理装置进行药洗或清洗,清洗后的液体回到药水储罐中。Further, a cleaning device may also be included. The cleaning device includes a liquid medicine storage tank, which is used to configure cleaning liquid. The liquid medicine storage tank, the filtering device 3 and the processing device 2 are connected in sequence. After the processing device is cleaned, concentrated water and product The water all returns to the liquid medicine storage tank for recycling. With regard to the specific structure of the present embodiment, the first filtering device 31, the first boosting device 41 and the primary processing device 21, the second filtering device 32, the second boosting device 42 and the secondary processing device 22 and the third filtering device 33. After the third pressurization device 43 and the third-stage treatment device 23 are respectively connected in series, they are connected to the liquid medicine storage tank. The medicine storage tank is connected, that is, the medicine in the medicine storage tank passes through the first filter device 31, the second filter device 32 and the third filter device 33 respectively, and then enters the primary treatment device 21, the secondary treatment device 22 and the tertiary treatment device 23 The treatment device is washed or cleaned with medicine, and the cleaned liquid is returned to the liquid medicine storage tank.

实施例2Example 2

如图3所示,本实施例与上述实施例的区别在于,原水储罐110、过滤装置3、第一增压装置410和一级处理装置210依次连接,一级处理装置210的产水出口和浓水出口分别与三级处理装置230和二级处理装置220连接,三级处理装置230的产水出口和浓水出口分别与产水储罐120和原水储罐110连接,二级处理装置220的产水出口和浓水出口分别与原水储罐110和浓水储罐130连接。本实施例的污水处理过程为:原水储罐110中的含镍废水经过滤装置3初步过滤后进入一级处理装置210,经一级处理装置210处理后的产水进入三级处理装置230、浓水进入二级处理装置220;进入三级处理装置230的产水经处理后,产水进入产水储罐120,浓水回到原水储罐110;进入二级处理装置220的浓水经处理后,产水回到原水储罐110,浓水进入浓水储罐130。As shown in Figure 3, the difference between this embodiment and the above-mentioned embodiments is that the raw water storage tank 110, the filter device 3, the first booster device 410 and the primary treatment device 210 are connected in sequence, and the water produced outlet of the primary treatment device 210 and the concentrated water outlet are respectively connected with the tertiary treatment device 230 and the secondary treatment device 220, the produced water outlet and the concentrated water outlet of the tertiary treatment device 230 are respectively connected with the produced water storage tank 120 and the raw water storage tank 110, and the secondary treatment device The product water outlet and the concentrated water outlet of 220 are respectively connected with the raw water storage tank 110 and the concentrated water storage tank 130 . The sewage treatment process in this embodiment is as follows: the nickel-containing wastewater in the raw water storage tank 110 enters the primary treatment device 210 after being initially filtered by the filter device 3, and the produced water treated by the primary treatment device 210 enters the tertiary treatment device 230, Concentrated water enters the secondary treatment device 220; after the product water entering the tertiary treatment device 230 is treated, the product water enters the product water storage tank 120, and the concentrated water returns to the raw water storage tank 110; the concentrated water entering the secondary treatment device 220 passes through After treatment, the produced water returns to the raw water storage tank 110 , and the concentrated water enters the concentrated water storage tank 130 .

经本实施例的系统循环处理后,产水储罐120中的产水经检测,镍含量小于0.1㎎/L,可直接排放;浓水储罐130中的浓水浓度越来越高,当达到一定标准(如浓水中镍含量达450-550㎎/L,电导率超过22000μs/cm)时,移交至有资质的单位进行处理。After the system circulation treatment of this embodiment, the product water in the product water storage tank 120 is tested, and the nickel content is less than 0.1㎎/L, and can be discharged directly; the concentrated water concentration in the concentrated water storage tank 130 is getting higher and higher, when When a certain standard is reached (for example, the nickel content in the concentrated water reaches 450-550㎎/L, and the conductivity exceeds 22000μs/cm), it will be handed over to a qualified unit for processing.

同样的,本实施例可以增加PLCS控制系统进行控制,以实现自动化管理;Similarly, this embodiment can increase the PLCS control system for control to realize automatic management;

同样的,本实施例也可以安装清洗装置对处理装置进行清洗。Similarly, in this embodiment, a cleaning device can also be installed to clean the processing device.

以上内容是结合具体的优选技术方案对本实用新型所作的进一步详细说明,不能认定本实用新型的具体实施只局限于这些说明。对于本实用新型所属技术领域的专业技术人员来说,在不脱离本实用新型构思的前提下,还可以做出若干简单推演或替换,都应当视为属于本实用新型的保护范围。The above content is a further detailed description of the utility model in combination with specific preferred technical solutions, and it cannot be determined that the specific implementation of the utility model is only limited to these descriptions. For those skilled in the technical field to which the utility model belongs, without departing from the concept of the utility model, some simple deduction or substitutions can be made, which should be regarded as belonging to the protection scope of the utility model.

Claims (7)

1.一种含镍废水的处理系统,包括储存装置、过滤装置、处理装置和管道系统,其特征在于,所述储存装置包括原水储罐、产水储罐和浓水储罐,所述原水储罐、过滤装置和处理装置连接,所述处理装置的产水出口与所述产水储罐连接,所述处理装置的浓水出口与所述浓水储罐连接,所述处理装置为反渗透处理装置,所述管道系统用于提供含镍废水处理过程中液体流通的管道;所述含镍废水处理系统还包括清洗装置,所述清洗装置包括药水储罐,所述药水储罐、所述过滤装置和所述处理装置依次连接。1. A treatment system for nickel-containing waste water, comprising a storage device, a filtering device, a treatment device and a piping system, characterized in that, the storage device includes a raw water storage tank, a produced water storage tank and a concentrated water storage tank, and the raw water The storage tank, the filtering device and the processing device are connected, the water product outlet of the processing device is connected with the water product storage tank, the concentrated water outlet of the processing device is connected with the concentrated water storage tank, and the processing device is a reverse The osmotic treatment device, the pipeline system is used to provide the pipeline for liquid circulation in the nickel-containing wastewater treatment process; the nickel-containing wastewater treatment system also includes a cleaning device, and the cleaning device includes a medicinal solution storage tank, the medicinal solution storage tank, the The filtering device and the processing device are connected in sequence. 2.根据权利要求1所述的含镍废水的处理系统,其特征在于,所述含镍废水的处理系统还包括增压装置,所述增压装置设于过滤装置和处理装置之间,用于给所述反渗透处理装置增压。2. the treatment system of nickel-containing waste water according to claim 1, is characterized in that, the treatment system of described nickel-containing waste water also comprises supercharging device, and described supercharging device is located between filtering device and treatment device, uses To pressurize the reverse osmosis treatment device. 3.根据权利要求1所述的含镍废水的处理系统,其特征在于,所述处理装置包括一级处理装置、二级处理装置和三级处理装置,所述一级处理装置的产水出口和浓水出口分别与所述三级处理装置和所述二级处理装置的入口连接,所述三级处理装置的产水出口和浓水出口分别与所述产水储罐和所述原水储罐连接;所述二级处理装置的产水出口和浓水出口分别与所述原水储罐和浓水储罐连接。3. the treatment system of nickel-containing waste water according to claim 1, is characterized in that, described treatment device comprises primary treatment device, secondary treatment device and tertiary treatment device, and the produced water outlet of described primary treatment device and the concentrated water outlet are respectively connected with the inlets of the tertiary treatment device and the secondary treatment device, and the produced water outlet and the concentrated water outlet of the tertiary treatment device are connected with the produced water storage tank and the raw water storage tank respectively. tank connection; the produced water outlet and the concentrated water outlet of the secondary treatment device are respectively connected with the raw water storage tank and the concentrated water storage tank. 4.根据权利要求1所述的含镍废水的处理系统,其特征在于,所述含镍废水的处理系统还包括中间储罐,所述处理装置包括一级处理装置、二级处理装置和三级处理装置,所述中间储罐的入口和出口分别与所述一级处理装置的产水出口和三级处理装置的入口连接,所述三级处理装置的产水出口和浓水出口分别与所述产水储罐和浓水储罐的入口连接;所述浓水储罐的出口与所述二级处理装置的入口连接,所述二级处理装置的产水出口和浓水出口分别与所述原水储罐和所述浓水储罐的入口连接。4. the treatment system of nickel-containing waste water according to claim 1, is characterized in that, the treatment system of described nickel-containing waste water also comprises intermediate storage tank, and described treatment device comprises primary treatment device, secondary treatment device and three stage treatment device, the inlet and outlet of the intermediate storage tank are respectively connected to the water production outlet of the first stage treatment device and the inlet of the third stage treatment device, and the product water outlet and concentrated water outlet of the third stage treatment device are respectively connected to The inlet of the produced water storage tank is connected to the concentrated water storage tank; the outlet of the concentrated water storage tank is connected to the inlet of the secondary treatment device, and the produced water outlet and concentrated water outlet of the secondary treatment device are respectively connected to The raw water storage tank is connected to the inlet of the concentrated water storage tank. 5.根据权利要求3或4所述的含镍废水的处理系统,其特征在于,所述一级处理装置、二级处理装置和三级处理装置分别设有一级RO膜、二级RO膜和三级RO膜,其中,所述一级RO膜为抗污染膜,二级RO膜为海水淡化膜,所述三级RO膜为常规RO膜。5. according to the treatment system of claim 3 or 4 described nickel-containing waste water, it is characterized in that, described primary treatment device, secondary treatment device and tertiary treatment device are respectively provided with primary RO membrane, secondary RO membrane and A three-stage RO membrane, wherein the first-stage RO membrane is an anti-pollution membrane, the second-stage RO membrane is a seawater desalination membrane, and the third-stage RO membrane is a conventional RO membrane. 6.根据权利要求1所述的含镍废水的处理系统,其特征在于,所述过滤装置为过滤泵,所述过滤装置过滤精度为5-10μ。6 . The treatment system for nickel-containing wastewater according to claim 1 , wherein the filter device is a filter pump, and the filtration accuracy of the filter device is 5-10 μ. 7.根据权利要求1所述的含镍废水的处理系统,其特征在于,所述含镍废水的处理系统还包括PLCS控制系统。7. The treatment system of nickel-containing wastewater according to claim 1, characterized in that, the treatment system of said nickel-containing wastewater also comprises a PLCS control system.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109293034A (en) * 2018-11-29 2019-02-01 珠海杰赛科技有限公司 A kind of processing system and processing method of nickel-containing waste water

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109293034A (en) * 2018-11-29 2019-02-01 珠海杰赛科技有限公司 A kind of processing system and processing method of nickel-containing waste water

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Granted publication date: 20191119