CN104150698B - A kind of apparatus and method of M type artificial swamp advanced treatment domestic sewage in rural areas - Google Patents
A kind of apparatus and method of M type artificial swamp advanced treatment domestic sewage in rural areas Download PDFInfo
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Abstract
一种M型人工湿地深度处理农村生活污水的装置,主要包括:一级格栅机连接二级格栅机;二级格栅机连接至M型人工湿地;M型人工湿地的出水口通过增压泵连接至表层湍流筛滤装置;表层湍流筛滤装置的出水口连接至出水池。本发明还公开了一种M型人工湿地深度处理农村生活污水的方法。针对重金属含量高以及水质污染负荷波动大的污水处理效果尤为明显。
A device for advanced treatment of rural domestic sewage in M-type constructed wetlands, mainly comprising: a first-level grille machine connected to a second-level grille machine; a second-level grille machine connected to an M-type constructed wetland; The pressure pump is connected to the surface turbulence screening device; the water outlet of the surface turbulence screening device is connected to the water outlet tank. The invention also discloses a method for the advanced treatment of rural domestic sewage by the M-shaped artificial wetland. The treatment effect is particularly obvious for sewage with high content of heavy metals and large fluctuations in water pollution load.
Description
技术领域technical field
本发明涉及一种M型人工湿地深度处理农村生活污水的装置。The invention relates to a device for advanced treatment of rural domestic sewage in an M-shaped artificial wetland.
本发明还涉及利用上述装置进行污水三级出水深度处理的方法。The invention also relates to a method for advanced treatment of tertiary effluent of sewage by using the above-mentioned device.
背景技术Background technique
人工湿地(CW·ConstructedWetland)污水处理技术是70年代末发展起来的一种污水处理新技术。它具有处理效果好、氮磷去除能力强,运转维护管理方便、工程基建和运转费用低以及对负荷变化适应能力强等特点,比较适合于技术管理水平不很高,规模较小的城镇或乡村的污水处理。人工湿地的净化机理:人工湿地对废水的处理综合了物理、化学和生物的三种作用。湿地系统成熟后,填料表面和植物根系将由于大量微生物的生长而形成生物膜。废水流经生物膜时,大量的SS被填料和植物根系阻挡截留,有机污染物则通过生物膜的吸收、同化及异化作用而被除去。湿地系统中因植物根系对氧的传递释放,使其周围的环境中依次出现好氧、缺氧、厌氧状态,保证了废水中的氮磷不仅能通过植物和微生物作为营养吸收,而且还可以通过硝化、反硝化作用将其除去,最后湿地系统更换填料或收割栽种植物将污染物最终除去。Constructed wetland (CW · Constructed Wetland) sewage treatment technology is a new sewage treatment technology developed in the late 1970s. It has the characteristics of good treatment effect, strong nitrogen and phosphorus removal ability, convenient operation and maintenance management, low engineering infrastructure and operation costs, and strong adaptability to load changes. It is more suitable for small towns or villages with low technical management level and small scale. sewage treatment. Purification mechanism of constructed wetlands: The treatment of wastewater by constructed wetlands integrates the three functions of physics, chemistry and biology. After the wetland system matures, the surface of the filler and the root system of the plant will form a biofilm due to the growth of a large number of microorganisms. When the wastewater flows through the biofilm, a large amount of SS is blocked and intercepted by the filler and plant roots, and the organic pollutants are removed through the absorption, assimilation and dissimilation of the biofilm. In the wetland system, due to the transfer and release of oxygen by plant roots, the surrounding environment appears aerobic, anoxic, and anaerobic in sequence, ensuring that nitrogen and phosphorus in wastewater can not only be absorbed by plants and microorganisms as nutrients, but also can be absorbed by plants and microorganisms. It is removed through nitrification and denitrification, and finally the wetland system replaces the filler or harvests the planted plants to remove the pollutants.
农村生活污水的主要问题在于其分散型,污染负荷低以及具有少量杂物的特点,本发明采用人工湿地结合表层湍流筛滤装置处理农村生活污水,为生态法处理农村生活污水提供了较好的后续净化步骤。The main problem of rural domestic sewage lies in its dispersed type, low pollution load and the characteristics of a small amount of sundries. This invention uses artificial wetland combined with surface turbulent flow screening device to treat rural domestic sewage, which provides a better solution for the ecological treatment of rural domestic sewage. Subsequent purification steps.
发明内容Contents of the invention
本发明的目的在于提供一种M型人工湿地深度处理农村生活污水的装置。The purpose of the present invention is to provide an M-type constructed wetland device for advanced treatment of rural domestic sewage.
本发明的又一目的在于提供一种M型人工湿地深度处理农村生活污水的方法。Another object of the present invention is to provide a method for advanced treatment of rural domestic sewage in an M-shaped constructed wetland.
为实现上述目的,本发明提供的M型人工湿地深度处理农村生活污水的装置,主要包括:In order to achieve the above purpose, the M-type constructed wetland device provided by the present invention for advanced treatment of rural domestic sewage mainly includes:
一级格栅机连接二级格栅机;The first-level grid machine is connected to the second-level grid machine;
二级格栅机连接至M型人工湿地;The secondary grid machine is connected to the M-type constructed wetland;
M型人工湿地的出水口通过增压泵连接至表层湍流筛滤装置;The water outlet of the M-type constructed wetland is connected to the surface turbulence screening device through a booster pump;
表层湍流筛滤装置的出水口连接至出水池;The water outlet of the surface turbulence screening device is connected to the water outlet tank;
其中:in:
M型人工湿地为混凝土墙体,做防渗处理,被隔墙分为两个部分,进水一侧整体高于出水一侧;The M-type artificial wetland is a concrete wall with anti-seepage treatment. It is divided into two parts by the partition wall. The water inlet side is higher than the water outlet side as a whole;
M型人工湿地中的每个部分又分为两个区域,靠近隔墙的两侧分别填充有A混合填料和B混合填料,靠近混凝土墙体的两侧填充有鹅卵石,对污水中杂质进行隔离;Each part of the M-shaped constructed wetland is divided into two areas. The two sides close to the partition wall are filled with A mixed filler and B mixed filler respectively, and the two sides close to the concrete wall are filled with pebbles to isolate impurities in the sewage. ;
隔墙下方与M型人工湿地底部之间设有空隙,该空隙的两侧与M型人工湿地的底部处平行地分别各设有一根钻孔PVC管,两根PVC管内均填充有沸石填料;在两根PVC管与隔墙以及M型人工湿地之间形成的空间内填充有沸石填料用于过水;There is a gap between the bottom of the partition wall and the bottom of the M-shaped artificial wetland, and a drilled PVC pipe is respectively provided on both sides of the gap parallel to the bottom of the M-shaped artificial wetland, and both PVC pipes are filled with zeolite fillers; The space formed between the two PVC pipes, the partition wall and the M-shaped artificial wetland is filled with zeolite filler for passing water;
M型人工湿地的出水通过增压泵进入表层湍流筛滤装置;The effluent of the M-type constructed wetland enters the surface turbulence screening device through the booster pump;
表层湍流筛滤装置由多孔板分为上、下两个部分,多孔板上方铺设有筛滤填料,筛滤填料的底部设有纳米曝气头,筛滤填料的表层充填有分子筛填料,在分子筛填料中安装有缩口进水管;表层湍流筛滤装置位于缩口进水管的另一侧下方,在筛滤填料中设有缩口反洗管,通过增压泵连接出水池;表层湍流筛滤装置位于缩口反洗管的上方设置有回流槽,筛滤填料上方位于回流槽一侧设置有曝气管,曝气管上设有多个垂直向上的曝气孔;在筛滤填料上方安装有超声波发生仪;多孔板下方为储水箱,储水箱内壁均匀负载一层非金属掺杂光催化剂,储水箱底部安装有紫外灭菌灯,在紫外灭菌灯的空隙间设置纳米曝气头,表层湍流筛滤装置内部剩余空间填充有半导体负载填料。The surface turbulence screening device is divided into upper and lower parts by a porous plate. A sieve packing is laid on the top of the porous plate. A nano aeration head is provided at the bottom of the sieve packing. The surface of the sieve packing is filled with a molecular sieve packing. A shrinkage inlet pipe is installed in the packing; the surface turbulence screening device is located under the other side of the shrinkage inlet pipe, and a shrinkage backwash pipe is set in the screening packing, which is connected to the outlet pool through a booster pump; the surface turbulence screening The device is located above the necking backwash pipe, and a reflux tank is installed. An aeration tube is installed on the side of the reflux tank above the filter packing. The aeration tube is provided with multiple vertically upward aeration holes; There is an ultrasonic generator; below the porous plate is a water storage tank, and the inner wall of the water storage tank is evenly loaded with a layer of non-metallic doped photocatalyst. The bottom of the water storage tank is equipped with an ultraviolet sterilizing lamp, and a nano aeration head is installed in the gap of the ultraviolet sterilizing lamp. The remaining space inside the surface turbulence screening device is filled with semiconductor-loaded fillers.
所述M型人工湿地深度处理农村生活污水的装置中,一级格栅和二级格栅的过滤精度分别为21mm及8mm。In the M-type constructed wetland device for advanced treatment of rural domestic sewage, the filtration accuracy of the primary grid and the secondary grid are 21 mm and 8 mm, respectively.
所述M型人工湿地深度处理农村生活污水的装置中,M型人工湿地中的进水一侧的混合填料是由粉煤灰制备的缓释分子筛和活性炭按体积比1:2-5混合而成,出水一侧的混合填料是由弗罗里硅藻土和赤泥分子筛按体积比为1:2-5混合而成。In the M-type constructed wetland device for advanced treatment of rural domestic sewage, the mixed filler on the water inlet side of the M-type constructed wetland is prepared by mixing slow-release molecular sieves prepared from fly ash and activated carbon at a volume ratio of 1:2-5. The mixed filler on the water outlet side is made of flori diatomaceous earth and red mud molecular sieve in a volume ratio of 1:2-5.
所述M型人工湿地深度处理农村生活污水的装置中,M型人工湿地近二级格栅机一侧的区域栽种用于浅水的菖蒲,靠近表层湍流筛滤装置一侧的区域栽种挺水植物芦苇。In the device for the advanced treatment of rural domestic sewage in the M-type constructed wetland, calamus for shallow water is planted in the area of the M-type constructed wetland near the second-level grid machine, and emergent plants are planted in the area near the surface turbulence screening device. reed.
所述M型人工湿地深度处理农村生活污水的装置中,表层湍流筛滤装置中的分子筛填料是用粉煤灰制备的颗粒型分子筛。In the M-type constructed wetland device for advanced treatment of rural domestic sewage, the molecular sieve filler in the surface turbulence screening device is a granular molecular sieve prepared from fly ash.
所述M型人工湿地深度处理农村生活污水的装置中,表层湍流筛滤装置中的筛滤填料是由石英砂、改性锰砂与天然沸石分子筛混合而成。In the M-type artificial wetland device for advanced treatment of rural domestic sewage, the sieve filler in the surface turbulence sieve device is made of quartz sand, modified manganese sand and natural zeolite molecular sieve.
所述M型人工湿地深度处理农村生活污水的装置中,表层湍流筛滤装置中的非金属掺杂光催化剂为纳米TiO2粉体,半导体负载填料为纳米TiO2粉体负载在立体网状聚丙烯填料。In the M-type artificial wetland advanced treatment device for rural domestic sewage, the non-metallic doped photocatalyst in the surface turbulence screening device is nano- TiO2 powder, and the semiconductor-loaded filler is nano- TiO2 powder loaded on a three-dimensional network polymer. Acrylic filler.
本发明提供的M型人工湿地深度处理农村生活污水的方法,其过程为:The method for the M-type artificial wetland advanced treatment of rural domestic sewage provided by the present invention, its process is:
两级格栅机分两个过滤精度对污水中的不同粒径大小的固体进行有效拦截,初步实现固液分离,阻隔污水中的大型固体,减少污水中的含固量,防止悬浮物对污水的后续处理造成影响;The two-stage grille machine can effectively intercept solids of different particle sizes in the sewage with two filtration precisions, and initially realize solid-liquid separation, block large solids in sewage, reduce solid content in sewage, and prevent suspended solids from affecting sewage. impact on subsequent processing;
M型人工湿地由隔墙分为两个部分,每个部分分为两个区域,每个区域为上流式和下流式,B区内填充的填料用于大量吸附污染负荷并逐渐缓释,用于降低污染负荷和毒性,同时C区利用偏碱性的赤泥分子筛作为填料,迅速吸附中和厌氧部分酸化产生的小分子酸,调节污水酸碱度,使装置内环境更适宜植物、微生物生存;同时营造偏碱性环境固定污水中的重金属,防止其浸出,利用小分子有机物供给植物养分,在植物生长过程中吸附、吸收重金属进行重金属生物稳定化。所有的混合填料表面形成生物膜,由上至下形成好氧、缺氧、厌氧状态,在植物根系与微生物的协同作用下去除污水中的污染物质;The M-type constructed wetland is divided into two parts by a partition wall, each part is divided into two areas, each area is an upflow type and a downflow type, and the filler filled in the B area is used to absorb a large amount of pollution load and gradually release it slowly. In order to reduce the pollution load and toxicity, at the same time, the C area uses the alkaline red mud molecular sieve as the filler to quickly absorb and neutralize the small molecule acid produced by the anaerobic partial acidification, adjust the pH of the sewage, and make the internal environment of the device more suitable for the survival of plants and microorganisms; At the same time, create an alkaline environment to fix the heavy metals in the sewage to prevent their leaching, use small molecular organic matter to supply plant nutrients, and absorb and absorb heavy metals in the process of plant growth for heavy metal biostabilization. Biofilms are formed on the surface of all mixed fillers, and aerobic, anoxic, and anaerobic states are formed from top to bottom, and pollutants in sewage are removed under the synergy of plant roots and microorganisms;
表层湍流筛滤装置在筛滤时导入M型人工湿地的出水,进水过程中利用进水错流的冲击力扰动筛滤填料和分子筛填料的表层,形成湍流,防止污染物质在表层堆积对水流的顺利通过形成阻力;气泡将浮起的污染物推至水面侧溢流至回流槽,与进水混合调节进水水质;The surface turbulence screening device introduces the effluent of the M-type constructed wetland during screening. During the water intake process, the impact force of the cross-flow of the incoming water is used to disturb the surface layer of the sieve packing and molecular sieve packing to form a turbulent flow and prevent pollutants from accumulating on the surface against the water flow. The smooth passage of the water forms resistance; the air bubbles push the floating pollutants to the water surface and overflow to the return tank, where they mix with the incoming water to adjust the incoming water quality;
表层湍流筛滤装置中筛滤填料的纳米曝气头进气为O2,用于清洁筛滤填料;储水箱内的纳米曝气头的进气为O3,通过纳米曝气获得羟基自由基,与紫外灭菌灯和半导体负载填料共同提高高级氧化效果,同时其中富含羟自由基的出水在装置进行反洗时,冲刷筛滤填料,使筛滤填料能够清洁与再生;The air intake of the nano-aeration head of the filter packing in the surface turbulence screening device is O 2 , which is used to clean the filter packing; the intake air of the nano-aeration head in the water storage tank is O 3 , and hydroxyl radicals are obtained through nano-aeration , together with the ultraviolet sterilizing lamp and the semiconductor-loaded filler, it improves the advanced oxidation effect, and at the same time, the effluent rich in hydroxyl radicals flushes the sieve packing when the device is backwashed, so that the sieve packing can be cleaned and regenerated;
表层湍流筛滤装置中使用纳米曝气的方式提高·OH产生率,使微气泡具有庞大的数量、比表面积、缓慢的上升速度,增加气液接触面积、接触时间,以利于臭氧溶于水中,克服臭氧难溶于水的缺点;微气泡内部具有的压力且纳米气泡破裂时界面消失,周围环境剧烈改变产生的化学能促使产生更多的羟基自由基,增强臭氧氧化分解有机物的能力;The nano-aeration method is used in the surface turbulent sieving device to increase the OH production rate, so that the microbubbles have a large number, specific surface area, and slow rising speed, and increase the gas-liquid contact area and contact time to facilitate the dissolution of ozone in water. Overcome the shortcomings of ozone insoluble in water; the pressure inside the microbubbles and the interface disappears when the nanobubbles are broken, and the chemical energy generated by the drastic changes in the surrounding environment promotes the generation of more hydroxyl radicals, enhancing the ability of ozone to oxidize and decompose organic matter;
臭氧在紫外光的照射作用下产生·OH,臭氧带走二氧化钛光致电子空穴对中的电子,从而产生了更多的羟基自由基,加速了有机物的降解,通过·OH的强氧化作用对有机污染物进行处理。Ozone produces OH under the irradiation of ultraviolet light, and ozone takes away the electrons in the photoinduced electron-hole pairs of titanium dioxide, thereby generating more hydroxyl radicals and accelerating the degradation of organic matter. Organic pollutants are treated.
表层湍流筛滤装置的出水回流至M型人工湿地进水,调节水质并刺激植物生长过程分泌次生物质。The effluent from the surface turbulence screening device flows back to the M-type constructed wetland to regulate water quality and stimulate the secretion of secondary substances during plant growth.
所述M型人工湿地深度处理农村生活污水的方法中,紫外灭菌灯平均照射剂量在300J/m2以上。In the method for the advanced treatment of rural domestic sewage in the M-type constructed wetland, the average irradiation dose of the ultraviolet sterilizing lamp is above 300J/m 2 .
本发明的工艺操作简单、效果明显,使用改良M型人工湿地、表层湍流筛滤装置两种装置机械法与生态法深度处理农村生活污水,处理速度快,处理周期短,操作简便,使用M型人工湿地改良处理技术,在有限空间内延长污水停留时间,提高污水处理效率,建造更加复杂优良有效的处理环境,同时打破传统工艺理念,其中表层湍流筛滤装置中纳米二氧化钛晶体作为光触媒在紫外灯照射下激发极具氧化力的自由负离子,同时在纳米曝气过程中以及超声波发生过程激发的能量亦可发生并加强自由负离子的产生,达成光催化效果;而自由负离子以及其摆脱共价键的束缚后留下空位,与纳米气泡表面带有的电荷同时产生微电解效果,可灭杀大肠杆菌、金黄色葡萄球菌、病毒等,分解残留难降解有机化合物及有毒物质,持久安全的对污水进行消毒降解。针对环境类激素(如激素类农药、抗生素、二恶英、雌激素以及人工合成激素等微量有害化学物质)的处理方面具有很大的优势,能够使绝大部分有机物完全矿化或分解,对污水进行筛滤处理的同时对其出水净化、消毒,出水较好的达到国家要求标准。The process of the present invention is simple in operation and obvious in effect. The improved M-type constructed wetland and the surface turbulence screening device are used for advanced treatment of rural domestic sewage by mechanical method and ecological method. The improved treatment technology of artificial wetland prolongs the residence time of sewage in a limited space, improves the efficiency of sewage treatment, and builds a more complex and effective treatment environment. At the same time, it breaks the traditional process concept. Under the irradiation, free negative ions with great oxidative power are excited, and at the same time, the energy excited during the nano-aeration process and the ultrasonic generation process can also occur and strengthen the generation of free negative ions to achieve the photocatalytic effect; while free negative ions and their ability to get rid of covalent bonds After being bound, vacancies are left, and the micro-electrolysis effect is produced at the same time as the charge on the surface of the nanobubbles, which can kill Escherichia coli, Staphylococcus aureus, viruses, etc., decompose residual refractory organic compounds and toxic substances, and carry out long-term and safe treatment of sewage Disinfection degradation. It has great advantages in the treatment of environmental hormones (such as hormone pesticides, antibiotics, dioxins, estrogens, and artificial synthetic hormones and other trace harmful chemicals), which can completely mineralize or decompose most of the organic matter. While the sewage is screened and treated, the effluent is purified and disinfected, and the effluent better meets the national requirements.
附图说明Description of drawings
图1是本发明的M型人工湿地深度处理农村生活污水的装置示意图。附图中主要组件符号说明:Fig. 1 is a schematic diagram of an M-type constructed wetland device for advanced treatment of rural domestic sewage according to the present invention. Explanation of main component symbols in the attached drawings:
1一级格栅机;2二级格栅机;3混凝土墙体;4菖蒲;5鹅卵石;6隔板;7a、7b混合填料;8M型人工湿地;8a隔墙;9芦苇;10进水阀门;11缩口进水管;12分子筛填料;13表层湍流筛滤装置;14筛滤填料;15缩口反洗管;16反洗阀门;17出水池;18液压泵;19增压泵;20出水阀门;21紫外灭菌灯;22多孔板;23纳米曝气头;24半导体负载填料;25储水箱;26纳米曝气机;27钻孔PVC管;28沸石填料;29超声波发生仪;30曝气管;31回流槽。1 first-level grid machine; 2 second-level grid machine; 3 concrete wall; 4 calamus; 5 cobblestone; 6 partition; Valve; 11 Shrink inlet pipe; 12 Molecular sieve filler; 13 Surface turbulence screening device; 14 Screen filler; 15 Shrink backwash pipe; 16 Backwash valve; 17 Outlet pool; 18 Hydraulic pump; Water outlet valve; 21 UV sterilizing lamp; 22 porous plate; 23 nanometer aeration head; 24 semiconductor loaded filler; 25 water storage tank; 26 nanometer aerator; 27 drilled PVC pipe; 28 zeolite filler; Aeration pipe; 31 reflux tanks.
具体实施方式detailed description
以下结合附图作详细说明。需要说明的是,在以下叙述中提到的左、右、上、下等均是以附图所示的方向为准。Describe in detail below in conjunction with accompanying drawing. It should be noted that the left, right, up, down, etc. mentioned in the following descriptions are all based on the directions shown in the drawings.
请参阅图1。本发明提供的M型人工湿地深度处理农村生活污水的装置,其主要结构包括:See Figure 1. The M-type artificial wetland advanced treatment device for rural domestic sewage provided by the present invention, its main structure includes:
一级格栅机1连接二级格栅机2,二级格栅机2连接至M型人工湿地8,分两个过滤精度(两级格栅机过滤精度分别为21mm及8mm)对污水中的不同粒径大小的固体进行有效拦截,初步实现固液分离,阻隔污水中的大型固体,减少污水中的含固量,防止悬浮物对污水的后续处理造成影响。The first-level grid machine 1 is connected to the second-level grid machine 2, and the second-level grid machine 2 is connected to the M-shaped artificial wetland 8, and two filtering precisions (two-level grid machine filtration precision are 21mm and 8mm respectively) are used for sewage Effectively intercept solids of different particle sizes, initially realize solid-liquid separation, block large solids in sewage, reduce solid content in sewage, and prevent suspended solids from affecting the subsequent treatment of sewage.
M型人工湿地8的出水口通过增压泵9连接至表层湍流筛滤装置13,表层湍流筛滤装置13的出水口连接至出水池。The water outlet of the M-type constructed wetland 8 is connected to the surface turbulent filtering device 13 through the booster pump 9, and the water outlet of the surface turbulent filtering device 13 is connected to the water outlet pool.
M型人工湿地8为混凝土墙体,做防渗处理,湿地被隔墙8a分为两个部分,进水一侧(即靠近二级格栅机2一侧)整体高于出水一侧(靠近表层湍流筛滤装置13一侧),其中每个部分又分为两个区域,A区和B区为一个区域,C区和D区为一个区域。A区为上流式,内部填充有鹅卵石5,对污水中杂质进行隔离,B区为下流式,内部填充有混合填料7a,是由粉煤灰制备的缓释分子筛和活性炭按体积比1:2-5混合而成,混合填料7表面形成生物膜,由上至下形成好氧、缺氧、厌氧状态,在植物根系4与微生物的协同作用下去除污水中的污染物质(左半部分栽种用于浅水的菖蒲,右半部分栽种挺水植物芦苇)。C区为上流式,内部填充有混合填料7b,是由弗罗里硅藻土和赤泥分子筛按体积比为1:2-5混合而成;D区为下流式,内部填充有鹅卵石5,鹅卵石5具有的大空隙便于出水的导出,导出的出水在增压泵19的作用下喷入表层湍流筛滤装置13。The M-type artificial wetland 8 is a concrete wall, which is treated with anti-seepage. The wetland is divided into two parts by the partition wall 8a. Surface turbulence screening device 13 side), wherein each part is divided into two areas again, A area and B area are an area, C area and D area are an area. Area A is an upflow type filled with pebbles 5 to isolate impurities in the sewage. Area B is a downflow type filled with a mixed filler 7a, which is a slow-release molecular sieve and activated carbon prepared by fly ash in a volume ratio of 1:2 -5 mixed, the surface of the mixed filler 7 forms a biofilm, and forms aerobic, anoxic, and anaerobic states from top to bottom, and removes pollutants in the sewage under the synergistic action of the plant root system 4 and microorganisms (the left half of the planted Calamus for shallow water, and the right half is planted with emergent plants reed). Zone C is an upflow type, filled with mixed filler 7b, which is made of flori diatomaceous earth and red mud molecular sieve at a volume ratio of 1:2-5; zone D is a downflow type, filled with pebbles 5, The large gaps of the pebbles 5 facilitate the export of the effluent, and the exported effluent is sprayed into the surface turbulence screening device 13 under the action of the booster pump 19 .
隔墙8a下方与M型人工湿地8底部之间设有空隙,该空隙的两侧分别各设有一根钻孔PVC管27,两根PVC管27内均填充有沸石填料。在两根PVC管27与隔墙8a以及M型人工湿地8之间形成的空间内填充有沸石填料用于过水。There is a gap between the bottom of the partition wall 8a and the bottom of the M-shaped constructed wetland 8, and a drilled PVC pipe 27 is respectively arranged on both sides of the gap, and both PVC pipes 27 are filled with zeolite filler. The space formed between the two PVC pipes 27, the partition wall 8a and the M-type constructed wetland 8 is filled with zeolite filler for passing water.
表层湍流筛滤装置13由多孔板22分为上、下两个部分。多孔板22的孔洞为倾斜状(本实施例为向右倾斜),多孔板22上方铺设有筛滤填料14,筛滤填料14是由石英砂、改性锰砂与天然沸石分子筛的混合物,是集过滤、吸附、离子交换、混凝及去除重金属为一体的多功能混合填料。筛滤填料14的底部设有纳米曝气头23,筛滤填料14的表层充填有用粉煤灰制备的分子筛填料12,在分子筛填料12中安装有缩口进水管11。该缩口进水管11通过增压泵19与M型人工湿地8的出水口相连接。表层湍流筛滤装置13位于缩口进水管11的另一侧下方,在筛滤填料14中设有缩口反洗管15,通过增压泵19连接出水池17。表层湍流筛滤装置13位于缩口反洗管15的上方设置有回流槽31。筛滤填料14上方位于回流槽31一侧设置有曝气管30,曝气管30设有多个细孔曝气孔,细孔曝气孔垂直向上;在筛滤填料14上方安装有超声波发生仪29。多孔板22下方为储水箱25,储水箱25内壁均匀负载一层非金属掺杂光催化剂,储水箱25底部安装有紫外灭菌灯21,在紫外灭菌灯21的空隙间设置纳米曝气头23,表层湍流筛滤装置13内部剩余空间填充有半导体负载填料24(如纳米TiO2粉体负载在立体网状聚丙烯填料),本发明将半导体负载填料24固定在载体上,解决了常规光催化剂需要分散剂协同使用的弊端,减少了催化剂的流失现象,避免了反应结束后催化剂的分离步骤。The surface turbulence filtering device 13 is divided into upper and lower parts by a perforated plate 22 . The holes of the perforated plate 22 are inclined (the present embodiment is inclined to the right), and a sieve packing 14 is laid on the top of the perforated plate 22. The sieve packing 14 is a mixture of quartz sand, modified manganese sand and natural zeolite molecular sieve. It is a multi-functional mixed packing integrating filtration, adsorption, ion exchange, coagulation and removal of heavy metals. The bottom of the sieve packing 14 is provided with a nano-aeration head 23, and the surface layer of the sieve packing 14 is filled with a molecular sieve packing 12 prepared from fly ash, and a shrinkage inlet pipe 11 is installed in the molecular sieve packing 12. The narrowed water inlet pipe 11 is connected with the water outlet of the M-type constructed wetland 8 through a booster pump 19 . The surface turbulence screening device 13 is located under the other side of the constricted water inlet pipe 11 , and a constricted backwash pipe 15 is provided in the screening packing 14 , and is connected to the water outlet pool 17 through a booster pump 19 . The surface turbulence screening device 13 is located above the shrinkage backwash pipe 15 and is provided with a backflow tank 31 . An aeration tube 30 is arranged above the sieve packing 14 on one side of the reflux tank 31, and the aeration tube 30 is provided with a plurality of fine-pore aeration holes, and the fine-pore aeration holes are vertically upward; an ultrasonic generator is installed above the sieve packing 14 Instrument 29. Below the porous plate 22 is a water storage tank 25, and the inner wall of the water storage tank 25 is evenly loaded with a layer of non-metallic doped photocatalyst. The bottom of the water storage tank 25 is equipped with an ultraviolet sterilizing lamp 21, and a nano aeration head is installed in the gap between the ultraviolet sterilizing lamp 21 23. The remaining space inside the surface turbulence screening device 13 is filled with semiconductor-loaded fillers 24 (such as nano- TiO2 powder loaded on three-dimensional network polypropylene fillers). The present invention fixes the semiconductor-loaded fillers 24 on the carrier to solve the problem of conventional light Catalysts need the disadvantages of dispersants to be used together, which reduces the loss of catalysts and avoids the separation step of catalysts after the reaction.
表层湍流筛滤装置13进行筛滤时,储水箱25内纳米曝气间歇曝气,曝气时储水箱内气压增大,空气被多孔板切割成为气泡鼓起,冲击筛滤填料和分子筛填料,打散筛滤填料和分子筛填料表面的污染物质层并使其浮起,使得污水能顺利经过筛滤填料过滤;筛滤填料上方右端设置有曝气管,曝气管设有多个细孔曝气孔,曝气孔垂直向上,气泡将浮起的污染物推至水面,于右侧溢流至回流槽,与进水混合调节进水水质,同时延长筛滤装置使用寿命及反洗周期,对于进水浊度较低的情况,甚至可以无需反冲洗,不断运行净化污水。When the surface turbulence screening device 13 performs screening, the nano-aeration in the water storage tank 25 is aerated intermittently. Break up the pollutant layer on the surface of the sieve packing and molecular sieve packing and make it float, so that the sewage can pass through the sieve packing smoothly; there is an aeration tube at the right end above the sieve packing, and the aeration tube is equipped with multiple fine holes The air hole and the aeration hole are vertically upward, and the air bubbles push the floating pollutants to the water surface, overflow to the return tank on the right side, mix with the influent water to adjust the influent water quality, and prolong the service life of the screening device and the backwash cycle. For the case of low influent turbidity, it can even run continuously to purify sewage without backwashing.
筛滤填料底部纳米曝气头进气为O2,用于清洁填料;储水箱内纳米曝气头的进气为O3,通过纳米曝气大量获得羟基自由基,与紫外灭菌灯、半导体负载填料共同提高高级氧化效果,同时其中富含羟自由基的出水在装置进行反洗时,冲刷筛滤填料,较好的做到填料清洁与再生。The air intake of the nano-aeration head at the bottom of the filter packing is O 2 for cleaning the packing; the air intake of the nano-aeration head in the water storage tank is O 3 , and a large amount of hydroxyl radicals are obtained through nano-aeration, which is compatible with ultraviolet sterilization lamps and semiconductors. Loaded fillers work together to improve the advanced oxidation effect, and at the same time, the effluent rich in hydroxyl radicals flushes the sieve fillers when the device is backwashed, so that the fillers are cleaned and regenerated better.
使用纳米曝气的方式提高·OH产生率,由于微气泡具有庞大的数量、比表面积、缓慢的上升速度,大大增加了气液接触面积、接触时间,有利于臭氧溶于水中,克服了臭氧难溶于水的缺点。微气泡内部具有较大的压力且纳米气泡破裂时界面消失,周围环境剧烈改变产生的化学能促使产生更多的羟基自由基,增强臭氧氧化分解有机物的能力。Use nano-aeration to increase the OH production rate. Because the microbubbles have a large number, specific surface area, and slow rising speed, the gas-liquid contact area and contact time are greatly increased, which is conducive to the dissolution of ozone in water and overcomes the difficulty of ozone. The disadvantage of being soluble in water. The inside of the microbubbles has a large pressure and the interface disappears when the nanobubbles are broken. The chemical energy generated by the drastic changes in the surrounding environment promotes the generation of more hydroxyl radicals, which enhances the ability of ozone to oxidize and decompose organic matter.
臭氧在紫外光的照射作用下产生·OH,紫外灭菌灯平均照射剂量在300J/m2以上。臭氧能带走二氧化钛光致电子空穴对中的电子,从而产生了更多的羟基自由基,加速了有机物的降解,通过·OH的强氧化作用对有机污染物进行处理。Ozone produces OH under the irradiation of ultraviolet light, and the average irradiation dose of ultraviolet germicidal lamp is above 300J/ m2 . Ozone can take away the electrons in the photo-induced electron-hole pairs of titanium dioxide, thereby generating more hydroxyl radicals, accelerating the degradation of organic matter, and treating organic pollutants through the strong oxidation of OH.
在表层湍流筛滤装置工作时导入M型人工湿地的出水,进水管埋在分子筛填料的表层,进水过程中利用进水错流的冲击力扰动分子筛填料表层,形成湍流,防止污染物质在表层堆积对水流的顺利通过形成阻力;在进行反冲洗时,纳米曝气头开始曝气,在高温纳米曝气的情况下对砂粒进行纳米曝气处理,在高温、纳米微小泡的剪切力以及曝气过程中产生的冲击力的作用下,清洗填料截流的杂质、胶体以及表面生长的生物膜。同时通过反洗管导入出水池内上清液进行反冲洗,缩口反洗管对筛滤填料施加一个向内的方向力,而储水箱在充水过程中,液面上的空气被强力挤压,通过多孔板上升至筛滤填料层,使筛滤填料呈现沸腾流动状态,储水箱内空气排空后,水流继续通过多孔板的孔洞倾斜向上高速流动,同时整个反冲洗过程中缩口反洗管内水流向内冲洗,整个表层湍流筛滤装置的填料(筛滤填料和分子筛填料)在水流的冲击力下形成快速运转的湍流,各种填料在不同方向力作用下形成的逆时针小旋涡中相互摩擦,附着的有机污染物得以去除,有利于取得较为纯净的填料。表层湍流筛滤装置储水箱出水口通过一液压泵与出水池相连。When the surface turbulence screening device is working, the outlet water of the M-type constructed wetland is introduced, and the water inlet pipe is buried in the surface layer of the molecular sieve packing. During the water intake process, the impact force of the cross-flow of the incoming water is used to disturb the surface layer of the molecular sieve packing to form a turbulent flow and prevent pollutants from being deposited on the surface. Accumulation forms resistance to the smooth passage of water flow; during backwashing, the nano-aeration head starts to aerate, and in the case of high-temperature nano-aeration, the sand particles are subjected to nano-aeration treatment. Under the action of the impact force generated during the aeration process, the impurities, colloids and biofilms grown on the surface are cleaned. At the same time, the supernatant liquid in the outlet pool is introduced through the backwash pipe for backwashing. The shrinking backwash pipe exerts an inward force on the filter packing, and the air on the liquid surface is strongly squeezed during the filling process of the water storage tank. , rise to the filter packing layer through the porous plate, so that the filter packing presents a state of boiling flow. After the air in the water storage tank is emptied, the water flow continues to flow upward at a high speed through the holes of the porous plate, and at the same time, the shrinkage backwashes during the entire backwashing process. The water in the pipe is flushed inward, and the fillers (filter fillers and molecular sieve fillers) of the entire surface turbulence screening device form a fast-moving turbulent flow under the impact of the water flow. By rubbing against each other, the attached organic pollutants can be removed, which is beneficial to obtain relatively pure fillers. The water outlet of the water storage tank of the surface turbulence screening device is connected with the water outlet pool through a hydraulic pump.
本发明的装置操作简单、效果明显,使用M型人工湿地、表层湍流筛滤装置两种装置机械法与生态法深度处理农村生活污水,处理速度快,处理周期短,操作简便,使用M型人工湿地改良处理技术,在有限空间内延长污水停留时间,提高污水处理效率,建造更加复杂优良有效的处理环境,同时打破传统工艺理念,并灭杀大肠杆菌、金黄色葡萄球菌、病毒等,分解残留难降解有机化合物及有毒物质,持久安全的对污水进行消毒降解。针对环境类激素(如激素类农药、抗生素、二恶英、雌激素以及人工合成激素等微量有害化学物质)的处理方面具有很大的优势,能够使绝大部分有机物完全矿化或分解,对污水进行筛滤处理的同时对其出水净化、消毒,出水较好的达到国家要求标准。The device of the present invention is simple in operation and obvious in effect. It uses M-type artificial wetland and surface turbulence screening device to treat rural domestic sewage in depth. It has fast processing speed, short processing cycle and easy operation. Wetland improvement treatment technology prolongs the residence time of sewage in a limited space, improves sewage treatment efficiency, and builds a more complex and effective treatment environment. At the same time, it breaks the traditional process concept and kills E. coli, Staphylococcus aureus, viruses, etc., and decomposes residues Refractory organic compounds and toxic substances can disinfect and degrade sewage in a durable and safe manner. It has great advantages in the treatment of environmental hormones (such as hormone pesticides, antibiotics, dioxins, estrogens, and artificial synthetic hormones and other trace harmful chemicals), which can completely mineralize or decompose most of the organic matter. While the sewage is screened and treated, the effluent is purified and disinfected, and the effluent better meets the national requirements.
根据本发明的一个实施例,重金属去除率高达100%,痕量有机物含量降低95%以上,类蛋白类物质特征荧光峰降低90%以上。According to an embodiment of the present invention, the removal rate of heavy metals is as high as 100%, the content of trace organic matter is reduced by more than 95%, and the characteristic fluorescence peak of proteinoid substances is reduced by more than 90%.
本发明采用先后三级反冲洗技术进行反冲洗:The present invention adopts successive three-stage backwashing technology for backwashing:
一级反冲洗为曝气循环反冲洗,由于污染物质在填料表面的堆积,污水难以透过填料之间的空隙渗透下去,在筛滤过程中进行反冲洗,开启曝气管30并间歇开启多孔板上方纳米曝气机26,储水箱内的纳米曝气头不连续工作,空气自多孔板向上鼓起,分割成小气泡,间歇冲散筛滤填料上的致密污物层,污染物质层破碎成片状浮起,在曝气管的气泡浮力以及缩口管进水时向右推力的协同作用下产生波轮效果,大力清洗填料表层片状致密污染物,溢流至回流槽,使填料截留的污染物集中排除装置外,与进水混合重新处理,污水也可继续自分子筛空隙渗透下去;一级反冲洗可延长筛滤装置使用寿命及反洗周期,对于进水浊度较低的情况,甚至可以无需反冲洗,使装置不断运行净化污水。The first level of backwash is an aeration cycle backwash. Due to the accumulation of pollutants on the surface of the filler, it is difficult for the sewage to penetrate through the gaps between the fillers. Backwash is carried out during the screening process, and the aeration pipe 30 is opened and the porous is intermittently opened. The nano-aerator 26 above the plate, the nano-aerator head in the water storage tank does not work continuously, the air bulges upward from the porous plate, and is divided into small bubbles, which intermittently wash away the dense dirt layer on the sieve packing, and the pollutant layer is broken Floating in flakes, under the synergistic effect of the buoyancy of the air bubbles in the aeration tube and the rightward thrust of the shrinking tube when it enters the water, a pulsator effect is produced, vigorously cleaning the flaky and dense pollutants on the surface of the packing, and overflowing to the return tank, so that the packing The intercepted pollutants are concentrated and removed from the device, mixed with the influent for retreatment, and the sewage can continue to permeate through the molecular sieve gap; the first-stage backwash can prolong the service life of the screening device and the backwash cycle. In some cases, there is even no need for backwashing, so that the device can continue to operate to purify sewage.
二级反冲洗为空气脉冲反冲洗,由于污水浊度过高,导致污染物质在填料表面的大量堆积,仅仅靠一级反冲洗步骤仍不能达到继续筛滤的效果。此时关闭进水阀门10、出水阀门20,开启反洗阀门16,启动增压泵19、曝气管30及两个纳米曝气机26,将出水池内的出水导入储水箱中。在回水压力的作用下,储水箱中的全部空气受到快速挤压,沿细孔上升,全部筛滤填料层在上升空气、旋转扰动的波轮作用及筛滤填料下部的纳米曝气头的冲击力作用下,填料间隙的污染物质破碎浮起,又在曝气管的浮力以及进水冲击挡流板向右推力的协同作用下,溢流至回流槽与初始进水混合,待水面快速下降。过滤速率重新稳定后,关闭增压泵19、多孔板下方纳米曝气机26、反洗阀门16,开启进水阀门10、出水阀门2,继续进行筛滤处理。The second-stage backwash is an air pulse backwash. Due to the high turbidity of the sewage, a large amount of pollutants accumulate on the surface of the filler. The effect of continuous screening cannot be achieved only by the first-stage backwash step. Now close the water inlet valve 10, the water outlet valve 20, open the backwash valve 16, start the booster pump 19, the aeration pipe 30 and two nano aerators 26, and the water outlet in the outlet pool is imported in the water storage tank. Under the action of the return water pressure, all the air in the water storage tank is quickly squeezed and rises along the pores, and the entire sieve packing layer is affected by the rising air, the action of the wave wheel of the rotating disturbance and the action of the nano-aeration head under the sieve packing. Under the action of the impact force, the pollutants in the filler gap are broken and floated, and under the synergistic effect of the buoyancy of the aeration tube and the rightward thrust of the incoming water impact baffle, they overflow to the return tank and mix with the initial incoming water. decline. After the filtration rate is stabilized again, close the booster pump 19, the nano aerator 26 under the perforated plate, the backwash valve 16, open the water inlet valve 10 and the water outlet valve 2, and continue the screening process.
三级反冲洗为曝气湍流反冲洗,此时一、二级反冲洗已经不足以解决污染物质对填料的覆盖、阻塞问题,污水大量积聚不得过滤。此时关闭进水阀门10,开启反洗阀门16、出水阀门20,启动增压泵19、曝气管30及两个纳米曝气机26、超声波发生仪29,反向启动液压泵18,将出水池内出水大量导入集水池中。(1)集水池内部空气沿多孔板细孔上升搅拌,填料底部纳米曝气头开始曝气,填料上方涡轮不断转动;(2)利用纳米曝气技术冲击、氧化、气浮及高温作用协同清洗,上方填料呈现湍流状态,进行无规则高速运动状态,填料在水流旋涡的冲击力和气泡的剪切力作用下相互摩擦,填料上附着的有机污染物能够去除,得到较为纯净的填料;(3)利用超声波发生仪在液体介质中产生超声波,在筛滤填料表面产生空化效应,空化汽泡在闭合过程中破裂时形成的冲击波,会在其周围产生上千个气压的冲击压力,作用在填料表面上破坏污物之间粘性,并使它们迅速分散在反洗液中,从而达到填料表面洁净的效果。(4)空气排净后,出水池的出水继续导入,纳米曝气与超声波可促使羟基自由基的产生,富含羟自由基的出水冲洗湍流状态的的填料颗粒表面及微孔,剥离污染物质,填料得到再生。(5)而污染物质在水流冲击力及右侧曝气管气浮作用下不断向上浮至水面,自左端进水堰及右端回流槽流出与初始进水混合。经过三级反冲洗,内部污染物被清洗排空殆尽。The third-stage backwashing is aeration turbulent backwashing. At this time, the first and second-stage backwashing are not enough to solve the problem of covering and blocking the filler by pollutants, and a large amount of sewage cannot be filtered. Now close the water inlet valve 10, open the backwash valve 16, the water outlet valve 20, start the booster pump 19, the aeration pipe 30 and two nano aerators 26, the ultrasonic generator 29, start the hydraulic pump 18 in reverse, and A large amount of effluent in the effluent pool is introduced into the sump. (1) The air in the sump rises and stirs along the pores of the porous plate, the nano-aeration head at the bottom of the filler starts to aerate, and the turbine above the filler rotates continuously; (2) Using nano-aeration technology for shock, oxidation, air flotation and high-temperature cleaning , the upper packing presents a state of turbulent flow and is in a state of irregular high-speed motion. The packing rubs against each other under the impact force of the vortex of the water flow and the shear force of the air bubbles, and the organic pollutants attached to the packing can be removed to obtain a relatively pure packing; (3 )Using an ultrasonic generator to generate ultrasonic waves in the liquid medium, the cavitation effect is generated on the surface of the filter packing, and the shock wave formed when the cavitation bubble breaks during the closing process will generate thousands of air pressure shock pressure around it. Break the stickiness between the dirt on the surface of the filler, and make them quickly disperse in the backwash solution, so as to achieve the effect of cleaning the surface of the filler. (4) After the air is exhausted, the effluent from the effluent tank continues to be introduced. Nano-aeration and ultrasonic waves can promote the generation of hydroxyl radicals. The effluent rich in hydroxyl radicals washes the surface and micropores of filler particles in a turbulent state, and strips pollutants. , the filler is regenerated. (5) The pollutants continuously float up to the water surface under the impact of the water flow and the air flotation of the right aeration tube, and flow out from the water inlet weir at the left end and the reflux tank at the right end to mix with the initial water inlet. After three-stage backwashing, the internal pollutants are cleaned and emptied.
常规砂滤是在过滤过程中不扰动砂层,使水流从砂子细小缝隙之间流过。通常采用不扰动砂层,压实填料、增加水压、砂上附加网格等手段改进砂滤过程,让水流从砂子细小缝隙之间流过,而污染物质停留在砂层的表层上。本发明则是利用缩口管高压进水扰动填料表层,防止污染物质堆积对水流的顺利通过形成阻力,同时利用高级氧化、超声波、纳米曝气、气泡的冲击力和剪切力等手段改进装置,利用分子筛、锰砂等填料进行优化设计,最后使用三级反冲洗等改进处理过程。本装置对胶体、纤维、藻类等悬浮物的截留效果好,对于浊度较低水质甚至无需反冲洗,即可完成处理过程,同时具有去除臭味,灭杀细菌、病原菌等微生物,分解难降解的少量残留表面活化剂、多氯联苯等难降解有机化合物的功效。Conventional sand filtration does not disturb the sand layer during the filtration process, allowing water to flow through the small gaps in the sand. Usually, the sand filtration process is improved by means of not disturbing the sand layer, compacting the filler, increasing the water pressure, and adding grids on the sand, so that the water flows through the small gaps in the sand, while the pollutants stay on the surface of the sand layer. The present invention utilizes the high-pressure water inlet of the constricted tube to disturb the surface layer of the filler, prevents the accumulation of pollutants from forming resistance to the smooth passage of the water flow, and uses advanced oxidation, ultrasonic waves, nano-aeration, impact force and shear force of air bubbles to improve the device. , use molecular sieve, manganese sand and other fillers to optimize the design, and finally use three-stage backwashing to improve the treatment process. The device has a good interception effect on suspended solids such as colloids, fibers, algae, etc. For water with low turbidity, the treatment process can be completed even without backwashing. At the same time, it can remove odors, kill bacteria, pathogenic bacteria, etc. The efficacy of a small amount of residual surfactants, polychlorinated biphenyls and other refractory organic compounds.
本发明的半导体负载填料-碳掺杂的纳米TiO2粉体的制备:Nano TiO of the present invention's semiconductor loaded filler-carbon doping Preparation of powder:
采用均匀沉淀法和水热法两步过程制备碳掺杂的纳米TiO2。以硫酸钛和尿素为前驱,葡萄糖为碳源,具体制备过程如下:取硫酸钛和尿素溶于去离子水中,再加入适量的葡萄糖搅拌均匀,硫酸钛:尿素:葡萄糖的摩尔比=1:2:0.023,在90℃的条件下反应2h。待反应结束后取出反应物干燥、反复水洗至中性,再次干燥,用球磨机研磨得到碳掺杂的纳米TiO2粉体。Carbon-doped nano-TiO 2 was prepared by a two-step process of uniform precipitation and hydrothermal method. With titanium sulfate and urea as the precursor, glucose as the carbon source, the specific preparation process is as follows: dissolve titanium sulfate and urea in deionized water, then add an appropriate amount of glucose and stir evenly, the molar ratio of titanium sulfate: urea: glucose = 1:2 : 0.023, reacted at 90°C for 2h. After the reaction is finished, the reactant is taken out and dried, repeatedly washed with water until neutral, dried again, and ground with a ball mill to obtain carbon-doped nano TiO 2 powder.
纳米TiO2粉体负载在填料上的方法:The method of loading nano TiO 2 powder on the filler:
采用聚丙烯材质的立体网状结构填料,将纳米TiO2粉体与去离子水(粉体与水的质量比为1:20)混合,用超声波超声成乳浊液,将洁净的立体网状结构填料浸入与乙醇体积比1:1混合的钛酸酯偶联剂,缓慢搅拌一段时间,然后将填料取出放入TiO2乳浊液中继续搅拌一段时间,取出后放入烘箱中干燥(85℃以下)2h,即制得负载纳米TiO2的聚丙烯悬浮填料,其外观呈淡黄色,膜层较均匀。The three-dimensional network structure filler made of polypropylene is used to mix nano-TiO 2 powder with deionized water (the mass ratio of powder to water is 1:20), and the emulsion is formed by ultrasonic wave, and the clean three-dimensional network The structural filler is immersed in a titanate coupling agent mixed with ethanol at a volume ratio of 1:1, stirred slowly for a period of time, then the filler is taken out and placed in the TiO 2 emulsion to continue stirring for a period of time, and then placed in an oven to dry (85 ℃) 2h, that is, the polypropylene suspension filler loaded with nano TiO 2 is prepared, its appearance is light yellow, and the film layer is relatively uniform.
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CN104496110B (en) * | 2014-12-04 | 2016-09-07 | 北京建筑大学 | Soil filtration device |
CN105502839A (en) * | 2016-01-18 | 2016-04-20 | 湖南博惢巳环境科技有限公司 | Wastewater treatment system for livestock and poultry breeding |
CN105731731B (en) * | 2016-03-25 | 2018-06-05 | 浙江科技学院 | River point-source pollution intercepts cleaning system |
CN107162338B (en) * | 2017-06-26 | 2020-07-21 | 华北电力大学 | Multi-medium treatment system and method for removing antibiotics in wastewater through micro-power |
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CN111943389A (en) * | 2019-05-17 | 2020-11-17 | 安徽伊尔思环境科技有限公司 | Domestic wastewater treatment device and method |
CN111320325A (en) * | 2020-03-12 | 2020-06-23 | 高自通 | Activated carbon sewage treatment device with monitoring device and method |
CN113511727A (en) * | 2021-05-27 | 2021-10-19 | 长沙理工大学 | Constructed wetland coupled photocatalytic treatment system for organic pesticide wastewater |
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CN1872738A (en) * | 2006-06-30 | 2006-12-06 | 南京大学 | Method and installation for treating domestic sewage by using artificial wetland |
CN101186382A (en) * | 2007-11-28 | 2008-05-28 | 浙江师范大学 | A three-dimensional artificial wetland system for sewage treatment |
KR100880535B1 (en) * | 2008-08-01 | 2009-01-28 | 윤성윤 | Filtration tank using wetland tank |
CN201284274Y (en) * | 2008-10-14 | 2009-08-05 | 中国科学院水生生物研究所 | Biological and ecological combined apparatus for purifying and recycling sewage |
CN201660528U (en) * | 2010-03-10 | 2010-12-01 | 贵州明威环保技术有限公司 | Sewage treatment unit of hybrid subsurface constructed wetland |
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