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CN103449670B - System for treating acidic industrial wastewater - Google Patents

System for treating acidic industrial wastewater Download PDF

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CN103449670B
CN103449670B CN201310401393.2A CN201310401393A CN103449670B CN 103449670 B CN103449670 B CN 103449670B CN 201310401393 A CN201310401393 A CN 201310401393A CN 103449670 B CN103449670 B CN 103449670B
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reaction tank
treatment
concrete reaction
acidic industrial
artificial swamp
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CN103449670A (en
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徐大勇
徐建平
裘秀群
李文
蔡昌凤
张冬冬
江文
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Anhui Polytechnic University
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    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
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Abstract

本发明公开了一种用于处理酸性工业废水的系统,包括沉淀调节池、多孔混凝土反应池、人工湿地、出水井,所述沉淀调节池上部与多孔混凝土反应池下部之间通过第一连通管相连通,所述多孔混凝土反应池上部与人工湿地上部之间通过第二连通管相连通,所述人工湿地下部与出水井下部之间通过第三连通管相连通。所述沉淀调节池、多孔混凝土反应池、人工湿地、出水井布置的高度依次降低。该系统对酸性工业废水处理效率高、生态效益好、维护和运行成本低。

The invention discloses a system for treating acidic industrial wastewater, which comprises a sedimentation adjustment tank, a porous concrete reaction tank, an artificial wetland, and a water outlet well. The upper part of the sedimentation adjustment tank and the lower part of the porous concrete reaction tank are connected by a first connecting pipe The upper part of the porous concrete reaction tank is connected with the upper part of the constructed wetland through a second communication pipe, and the lower part of the artificial wetland is connected with the lower part of the outlet well through a third communication pipe. The arrangement heights of the sedimentation regulating tank, the porous concrete reaction tank, the artificial wetland and the outlet wells are successively reduced. The system has high treatment efficiency for acidic industrial wastewater, good ecological benefits, and low maintenance and operation costs.

Description

一种用于处理酸性工业废水的系统A system for treating acidic industrial wastewater

技术领域technical field

本发明涉及污水处理技术领域,尤其是涉及一种用于处理酸性工业废水的系统。The invention relates to the technical field of sewage treatment, in particular to a system for treating acidic industrial wastewater.

背景技术Background technique

酸性废水是工业废水的常见形式,主要来自矿山、冶金、电镀、制革以及医药等行业。极端酸性、高量的有毒金属和丰富的SO4 2-含量是此类废水的重要特征。酸性废水会腐蚀排水管道和构筑物,如果不加以治理直接排入环境,会使水体水质逐渐酸化,重金属超标,危害农作物和水生生物,因此必须在外排前进行无害化处理。Acidic wastewater is a common form of industrial wastewater, mainly from mining, metallurgy, electroplating, tanning and pharmaceutical industries. Extreme acidity, high amounts of toxic metals and rich SO 4 2- content are important characteristics of this type of wastewater. Acidic wastewater will corrode drainage pipes and structures. If it is discharged directly into the environment without treatment, the water quality will gradually acidify, heavy metals will exceed the standard, and endanger crops and aquatic organisms. Therefore, harmless treatment must be carried out before discharge.

目前处理酸性工业废水的方法众多,具体包括化学中和法、吸附法、微生物法等。其中,投药中和法是传统的处理酸性废水的方法,中和剂一般用石灰或石灰石。其次是吸附法,它利用多孔性的固体物质,使水中的一种或多种物质被吸附在固体表面从而使其去除。目前,常用的吸附剂主要有活性炭、粉煤灰、赤泥、天然炉渣、人造沸石、膨润土和海泡石等,不同吸附剂的吸附机理不尽相同,效果也有差异。At present, there are many methods for treating acidic industrial wastewater, including chemical neutralization, adsorption, and microbial methods. Among them, the chemical neutralization method is a traditional method for treating acidic wastewater, and the neutralizer generally uses lime or limestone. The second is the adsorption method, which uses porous solid substances to make one or more substances in the water be adsorbed on the solid surface to remove them. At present, the commonly used adsorbents mainly include activated carbon, fly ash, red mud, natural slag, artificial zeolite, bentonite and sepiolite, etc. Different adsorbents have different adsorption mechanisms and effects.

国内外比较受关注的酸性水处理方法还有硫酸盐还原菌(SRB)法。他最早由美国的M.凯特(1997)提出,应用自然界的硫循环反应原理,利用SRB将硫酸盐转化为硫化物或单质硫并最终去除,同时其对酸性水也具有很好的中和作用。The acidic water treatment method that has attracted more attention at home and abroad is the sulfate reducing bacteria (SRB) method. It was first proposed by M. Kate (1997) in the United States, applying the principle of sulfur cycle reaction in nature, using SRB to convert sulfate into sulfide or elemental sulfur and finally remove it, and it also has a good neutralization effect on acidic water .

除中和沉淀、吸附和SRB等方法外,电解、电渗析、树脂交换法、离子交换法以及溶剂萃取等也常用于酸性废水的治理当中。但上述方法均有不足之处,中和法中和剂的投加量不容易掌握,使排水pH值不稳定且成本高,其后续的分离时间长,占地面积大。吸附法最常用的吸附剂活性碳价格十分昂贵,且对有机物的处理效率不高。SRB法常受到高浓度金属污染的限制,也降低了其使用效率。而电解、电渗析、离子交换以及溶剂萃取等方法,普遍存在工艺条件严格、处理成本高以及重金属去除不完全等缺陷。In addition to methods such as neutralization and precipitation, adsorption and SRB, electrolysis, electrodialysis, resin exchange, ion exchange and solvent extraction are also commonly used in the treatment of acidic wastewater. However, the above-mentioned methods have shortcomings. The dosage of the neutralizing agent in the neutralization method is not easy to control, which makes the pH value of the drainage unstable and the cost is high. The subsequent separation takes a long time and occupies a large area. Activated carbon, the most commonly used adsorbent in the adsorption method, is very expensive, and the treatment efficiency of organic matter is not high. The SRB method is often limited by high concentrations of metal pollution, which also reduces its efficiency. However, methods such as electrolysis, electrodialysis, ion exchange, and solvent extraction generally have defects such as strict process conditions, high processing costs, and incomplete removal of heavy metals.

因此,寻找一种经济有效、技术可靠且易于推广应用的方法,是酸性工业废水治理过程中急需解决的问题。Therefore, it is an urgent problem to be solved in the treatment of acidic industrial wastewater to find a method that is economical, effective, reliable and easy to popularize and apply.

发明内容Contents of the invention

针对现有技术不足,本发明所要解决的技术问题是提供一种用于处理酸性工业废水的系统,以达到污水处理效率高、生态效益好、运行成本低的目的。Aiming at the deficiencies of the prior art, the technical problem to be solved by the present invention is to provide a system for treating acidic industrial wastewater, so as to achieve the purpose of high sewage treatment efficiency, good ecological benefit and low operating cost.

为了解决上述技术问题,本发明所采用的技术方案为:一种用于处理酸性工业废水的系统,包括沉淀调节池、多孔混凝土反应池、人工湿地、出水井,所述沉淀调节池上部与多孔混凝土反应池下部之间通过第一连通管相连通,所述多孔混凝土反应池上部与人工湿地上部之间通过第二连通管相连通,所述人工湿地下部与出水井下部之间通过第三连通管相连通。In order to solve the above-mentioned technical problems, the technical solution adopted in the present invention is: a system for treating acidic industrial wastewater, including a sedimentation adjustment tank, a porous concrete reaction tank, an artificial wetland, and a water outlet well. The lower part of the concrete reaction tank is connected through the first connecting pipe, the upper part of the porous concrete reaction tank is connected with the upper part of the artificial wetland through the second connecting pipe, and the lower part of the artificial wetland is connected with the lower part of the outlet well through the third connecting pipe. The pipes are connected.

进一步的,所述沉淀调节池、多孔混凝土反应池、人工湿地、出水井布置的高度依次降低。Further, the arrangement heights of the sedimentation regulating tank, porous concrete reaction tank, artificial wetland and outlet wells are successively reduced.

所述沉淀调节池内设有出水堰,第一连通管一端连到出水堰中。A water outlet weir is arranged in the sedimentation adjustment tank, and one end of the first connecting pipe is connected to the water outlet weir.

所述多孔混凝土反应池中的多孔混凝土的孔隙率为15-30%、抗压强度为2.12-4.58Mpa。The porosity of the porous concrete in the porous concrete reaction tank is 15-30%, and the compressive strength is 2.12-4.58Mpa.

所述人工湿地为垂直流人工湿地,垂直流人工湿地的基质从顶部往下依次为:砂层、砾石层、鹅卵石层,在砂层中设有与第二连通管相连通的布水管。The constructed wetland is a vertical flow constructed wetland, and the matrix of the vertical flow constructed wetland is: sand layer, gravel layer, and pebble layer in order from top to bottom, and a water distribution pipe connected with the second connecting pipe is arranged in the sand layer.

所述人工湿地上栽植有湿地植物,所述湿地植物为芦苇、蒌蒿、菖蒲、水葱其中的一种,或几种植物的组合。Wetland plants are planted on the artificial wetland, and the wetland plants are one of reed, Artemisia betel, calamus and water onion, or a combination of several plants.

所述人工湿地的基质厚度为0.8-1.0m。The matrix thickness of the constructed wetland is 0.8-1.0m.

所述砾石层分为上下两层,上层砾石的粒径小于下层砾石的粒径。The gravel layer is divided into upper and lower layers, and the particle size of the gravel in the upper layer is smaller than that of the gravel in the lower layer.

所述第一连通管、第二连通管、第三连通管以及布水管均为PVC管。The first communicating pipe, the second communicating pipe, the third communicating pipe and the water distribution pipe are all PVC pipes.

所述多孔混凝土反应池和人工湿地的四周挡墙及底部均设有防渗层。The surrounding retaining walls and the bottom of the porous concrete reaction tank and the artificial wetland are all provided with an anti-seepage layer.

本发明与现有技术相比,具有以下优点:Compared with the prior art, the present invention has the following advantages:

1、通过多孔混凝土和人工湿地结合对酸性工业废水进行处理,运用物理、化学、生物方法达到对酸性污水高效处理的目的;1. Treat acidic industrial wastewater through the combination of porous concrete and constructed wetland, and use physical, chemical and biological methods to achieve the purpose of efficient treatment of acidic wastewater;

2、无需添加药剂、靠重力维持运行,动力能耗少,维护和运行费用低;2. No need to add chemicals, rely on gravity to maintain operation, less power consumption, low maintenance and operation costs;

3、污水在湿地中通过湿地植物吸收和分解,湿地植物并能起到绿化美观、净化环境的作用;3. The sewage is absorbed and decomposed by wetland plants in the wetland, and the wetland plants can also play a role in greening and beautiful, and purifying the environment;

4、该酸性工业废水的处理系统属于生态处理范畴,生态效益好。4. The acid industrial wastewater treatment system belongs to the category of ecological treatment, and has good ecological benefits.

附图说明Description of drawings

下面对本说明书各幅附图所表达的内容及图中的标记作简要说明:The following is a brief description of the content expressed in the drawings of this manual and the marks in the drawings:

图1为本发明处理酸性工业废水的系统平面布置示意图。Fig. 1 is a schematic layout diagram of the system for treating acidic industrial wastewater according to the present invention.

图2为本发明处理酸性工业废水的系统结构示意图。Fig. 2 is a schematic structural diagram of the system for treating acidic industrial wastewater according to the present invention.

图中:1.沉淀调节池、11.出水堰、2.多孔混凝土反应池、21.多孔混凝土、3.人工湿地、31.布水管、32.湿地植物、33.砂层、34.砾石层、35.鹅卵石层、4.出水井。In the figure: 1. Sedimentation adjustment tank, 11. Outlet weir, 2. Porous concrete reaction tank, 21. Porous concrete, 3. Constructed wetland, 31. Water distribution pipe, 32. Wetland plants, 33. Sand layer, 34. Gravel layer , 35. Cobblestone layer, 4. Outlet well.

具体实施方式Detailed ways

下面对照附图,通过对实施例的描述,对本发明的具体实施方式作进一步详细的说明。The specific implementation manner of the present invention will be described in further detail below by describing the embodiments with reference to the accompanying drawings.

如图1和图2所示,用于处理酸性工业废水的生态系统,无需添加药剂,该系统包括通过连通管依次相连通的沉淀调节池1、多孔混凝土反应池2、人工湿地3、出水井4;具体为,沉淀调节池1上部与多孔混凝土反应池2下部之间通过第一连通管相连通,多孔混凝土反应池2上部与人工湿地3上部之间通过第二连通管相连通,人工湿地3下部与出水井4下部之间通过第三连通管相连通。As shown in Figure 1 and Figure 2, the ecological system used to treat acidic industrial wastewater does not need to add chemicals. The system includes a sedimentation adjustment tank 1, a porous concrete reaction tank 2, a constructed wetland 3, and a water outlet well connected in sequence through connecting pipes. 4; Specifically, the upper part of the sedimentation adjustment tank 1 is connected to the lower part of the porous concrete reaction tank 2 through the first connecting pipe, and the upper part of the porous concrete reaction tank 2 is connected to the upper part of the constructed wetland 3 through the second connecting pipe. The lower part of 3 communicates with the lower part of outlet well 4 through a third communication pipe.

沉淀调节池1、多孔混凝土反应池2、人工湿地3、出水井4布置的高度依次降低。酸性工业废水依次通过沉淀调节池、多孔混凝土反应池、人工湿地,靠重力流通,动力能耗少,维护和运行费用低。The heights of the sedimentation regulating tank 1, the porous concrete reaction tank 2, the constructed wetland 3, and the outlet well 4 are successively lowered. Acidic industrial wastewater passes through the sedimentation adjustment tank, porous concrete reaction tank, and artificial wetland in sequence, and circulates by gravity, with less power consumption and low maintenance and operation costs.

沉淀调节池1内设有出水堰11,第一连通管一端连到出水堰11中。酸性工业废水经沉淀调节池沉淀停留一定时间,去除较大悬浮物、部分有机物和漂浮物,沉淀时间为2.0-3.0小时,完成初步沉淀;沉淀后清水从出水堰11中流出,经第一连通管流入多孔混凝土反应池2中。A water outlet weir 11 is arranged in the sedimentation adjustment tank 1 , and one end of the first communication pipe is connected to the water outlet weir 11 . The acidic industrial wastewater settles and stays in the sedimentation adjustment tank for a certain period of time to remove larger suspended matter, some organic matter and floating matter. The sedimentation time is 2.0-3.0 hours to complete the initial sedimentation; The pipe flows into the porous concrete reaction tank 2.

多孔混凝土反应池2的四周挡墙及底部均设有防渗层,并在多孔混凝土反应池内设有方形或圆形的多孔混凝土21,多孔混凝土21的孔隙率为15-30%、抗压强度为2.12-4.58Mpa,多孔混凝土反应池一侧的进水口在底部上方10cm处,多孔混凝土反应池另一侧出水口在多孔混凝土上方30cm处。进水为从沉淀调节池内出水堰11中流出的清水,进水在多孔混凝土反应池中停留8-12h,完成酸碱中和、部分重金属吸附及有机物吸附降解作用后经出水口排出,经第二连通管流入人工湿地。The surrounding retaining walls and the bottom of the porous concrete reaction tank 2 are all provided with an anti-seepage layer, and square or circular porous concrete 21 is arranged in the porous concrete reaction tank. The porosity of the porous concrete 21 is 15-30%. 2.12-4.58Mpa, the water inlet on one side of the porous concrete reaction tank is 10cm above the bottom, and the water outlet on the other side of the porous concrete reaction tank is 30cm above the porous concrete. The influent water is clear water flowing out from the outlet weir 11 in the sedimentation adjustment tank, and the influent water stays in the porous concrete reaction tank for 8-12 hours, and is discharged through the outlet after completing acid-base neutralization, adsorption of some heavy metals, and adsorption and degradation of organic matter. The two connecting pipes flow into the constructed wetland.

人工湿地3四周挡墙及底部均设有防渗层。人工湿地为垂直流人工湿地,人工湿地的基质厚度为0.8-1.0m,垂直流人工湿地的基质从顶部往下依次为:砂层33、砾石层34、鹅卵石层35,与第二连通管相连通的布水管31置于5cm深沙层中。其中,砾石层34分为上下两层,上层砾石的粒径小于下层砾石的粒径。砂层厚度为15cm,粒径5-10mm;上层砾石厚度为25cm,粒径10-20mm;下层砾石厚度为25cm,粒径30-50mm;鹅卵石层厚度为15cm,粒径50-100mm。并在人工湿地上栽植有湿地植物32,所述湿地植物32为芦苇、蒌蒿、菖蒲、水葱其中的一种,或几种植物的组合。The retaining walls and the bottom of the artificial wetland 3 are provided with anti-seepage layers. The constructed wetland is a vertical flow constructed wetland, and the thickness of the matrix of the constructed wetland is 0.8-1.0m. The matrix of the vertical flow constructed wetland from the top to the bottom is: sand layer 33, gravel layer 34, pebble layer 35, connected to the second connecting pipe The common water distribution pipe 31 is placed in the deep sand layer of 5 cm. Wherein, the gravel layer 34 is divided into upper and lower layers, and the particle size of the gravel in the upper layer is smaller than that of the gravel in the lower layer. The thickness of the sand layer is 15cm, with a particle size of 5-10mm; the thickness of the upper layer of gravel is 25cm, with a particle size of 10-20mm; the thickness of the lower layer of gravel is 25cm, with a particle size of 30-50mm; And wetland plants 32 are planted on the constructed wetland, and the wetland plants 32 are one of reed, Artemisia betel, calamus, water onion, or a combination of several plants.

人工湿地进水为所述多孔混凝土反应池的出水,经具有均匀通孔分布的布水管布水;人工湿地通过物理、化学、生物和植物的综合反应过程将水中可沉降固体、胶体物质、BOD、N、P、重金属、难降解有机物、细菌和病毒等去除,具有强大的多功能净化能力,最后,出水由鹅卵石层收集,并流入与人工湿地底部相通的人工湿地外的出水井,清水从出水井流出后达标排放。The water inflow to the constructed wetland is the effluent from the porous concrete reaction tank, and the water is distributed through the water distribution pipes with uniform through-hole distribution; the constructed wetland passes through the comprehensive reaction process of physics, chemistry, biology and plants to dispose of settleable solids, colloidal substances, and BOD in the water. , N, P, heavy metals, refractory organic matter, bacteria and viruses, etc., with powerful multifunctional purification capabilities. Finally, the effluent is collected by the pebble layer and flows into the effluent well outside the constructed wetland connected to the bottom of the constructed wetland. The clean water comes from After the effluent well flows out, it is discharged up to the standard.

第一连通管、第二连通管、第三连通管以及布水管31均为PVC管,降低系统成本。The first communication pipe, the second communication pipe, the third communication pipe and the water distribution pipe 31 are all PVC pipes, which reduces the system cost.

上面结合附图对本发明进行了示例性描述,显然本发明具体实现并不受上述方式的限制,只要采用了本发明的构思和技术方案进行的各种非实质性的改进,或未经改进将本发明的构思和技术方案直接应用于其它场合的,均在本发明的保护范围之内。The present invention has been exemplarily described above in conjunction with the accompanying drawings. Obviously, the specific implementation of the present invention is not limited by the above methods, as long as various insubstantial improvements are made using the concept and technical solutions of the present invention, or the present invention will be If the concept and technical solutions of the present invention are directly applied to other occasions, they all fall within the protection scope of the present invention.

Claims (8)

1. the system for the treatment of acidic industrial effluent, it is characterized in that: comprise sedimentary adjustive pool (1), cellular concrete reaction tank (2), artificial swamp (3), wet well (4), be connected by the first communicating pipe between described sedimentary adjustive pool (1) top with cellular concrete reaction tank (2) bottom, described cellular concrete reaction tank (2) top is connected by the second communicating pipe with between artificial swamp (3) top, be connected by third connecting pipe between described artificial swamp (3) bottom with wet well (4) bottom, the height that described sedimentary adjustive pool (1), cellular concrete reaction tank (2), artificial swamp (3), wet well (4) are arranged reduces successively, be provided with effluent weir (11) in described sedimentary adjustive pool (1), first communicating pipe one end link in effluent weir (11).
2. as claimed in claim 1 for the treatment of the system of acidic industrial effluent, it is characterized in that: the porosity of the cellular concrete (21) in described cellular concrete reaction tank (2) is 15-30%, ultimate compression strength is 2.12-4.58Mpa.
3. as claimed in claim 1 for the treatment of the system of acidic industrial effluent, it is characterized in that: described artificial swamp (3) is vertical current constructed wetland, the matrix of vertical current constructed wetland is down followed successively by from top: layer of sand (33), gravel bed (34), pebbles layer (35), is provided with the water distributor (31) be connected with the second communicating pipe in layer of sand (33).
4. as claimed in claim 3 for the treatment of the system of acidic industrial effluent, it is characterized in that: wetland plant (32) that described artificial swamp (3) has been planted, described wetland plant (32) is reed, beach wormwood wormwood artemisia, calamus, Scirpus tabernaemontani one wherein, or the combination of several plant.
5. as claimed in claim 3 for the treatment of the system of acidic industrial effluent, it is characterized in that: the stromal thickness of described artificial swamp (3) is 0.8-1.0m.
6. as claimed in claim 3 for the treatment of the system of acidic industrial effluent, it is characterized in that: described gravel bed (34) is divided into two-layer up and down, the particle diameter of upper strata gravel is less than the particle diameter of lower floor's gravel.
7. as described in any one of claim 3 to 6 for the treatment of the system of acidic industrial effluent, it is characterized in that: described first communicating pipe, the second communicating pipe, third connecting pipe and water distributor (31) are pvc pipe.
8. as described in any one of claim 1 to 6 for the treatment of the system of acidic industrial effluent, it is characterized in that: surrounding barricade and the bottom of described cellular concrete reaction tank (2) and artificial swamp (3) are equipped with impervious barrier.
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