CN209259888U - A domestic gray water treatment system - Google Patents
A domestic gray water treatment system Download PDFInfo
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技术领域technical field
本实用新型属于灰水处理领域,更具体地说,涉及一种生活灰水处理系统,对城镇及农村生活灰水进行处理。The utility model belongs to the field of gray water treatment, and more specifically relates to a domestic gray water treatment system for treating urban and rural domestic gray water.
背景技术Background technique
目前,我国人口增加快速,淡水资源的质量和数量下降快速,水资源分布与人口和经济布局极不匹配,居民用水的供应压力日益增大。污水回用既能减少污染排放,减轻水体污染,也是解决我国居民生活和工业用水短缺的重要手段。而根据最新统计数据显示,我国污水的回收循环利用率极低,仅占其总量的7.2%。因此,加强污水净化再利用的研究就显得尤为重要。At present, my country's population is increasing rapidly, and the quality and quantity of fresh water resources are declining rapidly. The distribution of water resources does not match the population and economic layout, and the pressure on the supply of water for residents is increasing. Sewage reuse can not only reduce pollution discharge and water pollution, but also an important means to solve the shortage of domestic and industrial water in our country. According to the latest statistical data, the recycling rate of sewage in my country is extremely low, accounting for only 7.2% of the total. Therefore, it is particularly important to strengthen the research on sewage purification and reuse.
在各类污水中,生活污水排放率占污水总量的55%左右,按照污水污染程度的轻重以及来源的不同,可将生活污水划分为四个类别:黑水、黄水、褐水和灰水。生活灰水主要是指生活中排放的厨房废水、洗涤废水以及洗浴废水,在生活污水中所占的比例高达50%~80%。与生活黑水、黄水以及褐水的水质相比,灰水的污染程度相对较轻,仅含有少量的致病细菌、病原体以及碳、氮、磷等污染物,具有回用处理价值高,公众易接受等特点,是最具发展潜力的回用水源之一,因此对灰水的处理研究受到了国内外研究人员的广泛关注。Among all kinds of sewage, the discharge rate of domestic sewage accounts for about 55% of the total sewage. According to the degree of sewage pollution and the different sources, domestic sewage can be divided into four categories: black water, yellow water, brown water and gray water. water. Domestic gray water mainly refers to kitchen waste water, washing waste water and bath waste water discharged in daily life, accounting for as high as 50% to 80% of domestic sewage. Compared with domestic black water, yellow water and brown water, the pollution degree of gray water is relatively light, containing only a small amount of pathogenic bacteria, pathogens and pollutants such as carbon, nitrogen and phosphorus, and has high value for reuse and treatment. It is easily accepted by the public, and it is one of the most potential water reuse sources. Therefore, the research on the treatment of gray water has attracted extensive attention from researchers at home and abroad.
目前,灰水处理技术主要包括物理法、化学法以及生物法。物理法主要包括粗砂、土壤过滤和膜过滤,后续进行消毒处理。但是,单独的物理处理技术处理过后的水,其内有机物浓度和悬浮物浓度均不满足回用的标准。比如,March等人(Experiences ongreywater reuse for toilet flushing in a hote[J],Desalination,2004,164(3):241-247)利用尼龙材料的过滤装置与沉淀和消毒工艺联用,对洗澡灰水进行了处理,洗澡灰水中的化学需氧量(COD)、浊度、固体悬浮物浓度(SS)和总氮(TN)从171mg/L、20NTU、44mg/L和11.4mg/L分别降至78mg/L、 16.5NTU、18.6mg/L和7.1mg/L,其相应的去除率仅为54%、17.5%、57.8%和36.8%,去除率极低。灰水的化学处理方法包括混凝、光催化氧化、离子交换和颗粒活性炭处理,化学处理方法具有系统可控、更加智能化等优势,与其他技术联用更是进一步提升了净化水体的水质,但化学试剂的引入往往会带来二次污染。如中国专利,申请号:201711058783.9,申请日:2017.11.01,的发明专利公布了一种生活污水处理剂,由河沙、黏土、硅藻土、三氯化铁、活性炭、二氧化硅、岩砂晶以及草木灰组成,用以处理浓度较高的生活污水,能够起到抑制藻类生长的效果,但是容易引进其他污染源,造成水质的二次污染。处理生活灰水的生物法包括:生物转盘法,序批式反应器,升流式厌氧污泥床,构建湿地处理以及膜生物反应器。如中国专利,申请号:CN201320372762.5,申请日:2013.06.26,的实用新型专利公开了一种纤毛生物转盘、污水处理装置和污水处理系统,该纤毛生物转盘盘片内层为支撑材料,外层固定纤毛材料,该污水处理装置分为多级,每级包括多个生物转盘组,转盘组的每个盘片之间呈间隔相互连接,配有相应的上游、下游设备,该实用新型所用的纤毛生物转盘比表面积大,挂膜性能高,对生活灰水处理效率较高,其不足之处在于:由于生活灰水污染物浓度较低,有机物含量较少,缺乏营养元素和微量元素,挂膜性能较差,需要外加营养物质,容易造成水体的二次污染。Currently, gray water treatment technologies mainly include physical, chemical and biological methods. Physical methods mainly include coarse sand, soil filtration and membrane filtration, followed by disinfection treatment. However, the concentration of organic matter and suspended solids in the water treated by a separate physical treatment technology does not meet the standards for reuse. For example, March et al. (Experiences ongreywater reuse for toilet flushing in a hote [J], Desalination, 2004, 164 (3): 241-247) utilized a filter device of nylon material in combination with a sedimentation and disinfection process to treat gray water from a bath. After treatment, the chemical oxygen demand (COD), turbidity, suspended solids concentration (SS) and total nitrogen (TN) in the bath gray water were reduced from 171mg/L, 20NTU, 44mg/L and 11.4mg/L to 78mg/L, 16.5NTU, 18.6mg/L and 7.1mg/L, the corresponding removal rates are only 54%, 17.5%, 57.8% and 36.8%, the removal rates are extremely low. The chemical treatment methods of gray water include coagulation, photocatalytic oxidation, ion exchange and granular activated carbon treatment. The chemical treatment method has the advantages of system controllability and more intelligentization. It is combined with other technologies to further improve the water quality of purified water. However, the introduction of chemical reagents often brings secondary pollution. Such as the Chinese patent, application number: 201711058783.9, application date: 2017.11.01, the invention patent announced a domestic sewage treatment agent, which is composed of river sand, clay, diatomaceous earth, ferric chloride, activated carbon, silicon dioxide, rock Composed of sand crystals and plant ash, it is used to treat domestic sewage with high concentration, which can inhibit the growth of algae, but it is easy to introduce other pollution sources, causing secondary pollution of water quality. Biological methods for treating domestic gray water include: biological rotating disk method, sequencing batch reactor, upflow anaerobic sludge bed, constructed wetland treatment and membrane bioreactor. Such as the Chinese patent, application number: CN201320372762.5, application date: 2013.06.26, the utility model patent discloses a ciliated biological turntable, a sewage treatment device and a sewage treatment system. The inner layer of the ciliated biological turntable is a supporting material. The outer layer is fixed with ciliated material. The sewage treatment device is divided into multiple stages, and each stage includes multiple biological turntable groups. The ciliated biological turntable used has a large specific surface area, high film-hanging performance, and high treatment efficiency for domestic gray water. The disadvantages are: due to the low concentration of domestic gray water pollutants, low organic matter content, and lack of nutrients and trace elements , The film-hanging performance is poor, and nutrients need to be added, which is likely to cause secondary pollution of the water body.
湿地处理系统运行成本低、便于维护,同时兼具工艺效能高以及观赏性,被认为是一种友好经济的灰水处理工艺,但由于其占地面积大,实际应用受到了一定的限制。如中国专利,申请号:CN200910250342.8,申请日:20091204,的发明专利公开了一种集成的灰水处理方法及系统,该集成的灰水处理方法包括收集调节步骤、生物氧化处理、固液分离步骤、连续流砂过滤深度处理步骤以及消毒步骤,从固液分离区经过初步过滤的水通过连续流动砂滤器底部的进水布水管均匀配水,并沿着砂滤层向上流动,在砂水接触过程中细小的悬浮物等被拦截,清水穿过砂滤层后在滤器上部汇集并通过清水管自流进入回用水单元;深度处理单元的出水通过投加消毒剂来杀灭其中的微生物。该发明将收集、处理和回用融合在同一个处理系统,处理的难度低,投资费用少,污染物去除效果大幅度提高。其不足之处在于装置易堵塞,建造规模较大,管理步骤较多,较复杂,不适合企业、小型居民区以及分散的农村家庭住户。The wetland treatment system has low operating cost, easy maintenance, high process efficiency and ornamental value. It is considered as a friendly and economical gray water treatment process, but its practical application is limited due to its large area. Such as the Chinese patent, application number: CN200910250342.8, application date: 20091204, the invention patent discloses an integrated gray water treatment method and system, the integrated gray water treatment method includes collection adjustment steps, biological oxidation treatment, solid-liquid Separation step, continuous flow sand filtration advanced treatment step and disinfection step, the pre-filtered water from the solid-liquid separation area is evenly distributed through the water inlet distribution pipe at the bottom of the continuous flow sand filter, and flows upward along the sand filter layer. During the process, the fine suspended solids are intercepted, and the clear water passes through the sand filter layer and then collects on the upper part of the filter and flows into the reuse water unit through the clear water pipe; the effluent of the advanced treatment unit kills the microorganisms in it by adding disinfectant. The invention integrates collection, treatment and reuse into one treatment system, which has low treatment difficulty, low investment cost and greatly improved pollutant removal effect. Its shortcomings are that the device is easy to block, the construction scale is relatively large, and the management steps are more and more complicated. It is not suitable for enterprises, small residential areas and scattered rural family households.
发明内容Contents of the invention
1、要解决的问题1. Problems to be solved
针对现有灰水处理装置易堵塞,净化处理效果差,易产生二次污染,占地面积大,不适于在密集的城镇地区和分散的农村地区应用以及在处理过程中因过度饱和的厌氧状态致使出水水体发黑发臭等问题,本实用新型提供一种集集水、净化处理、消毒为一体的生活灰水处理系统,在底部设置多孔水平板,并利用植物以及大-中-小滤料的分布组合,确保了对灰水的净化效果,避免下层过度饱和的厌氧状态,提高周围复氧环境,具有低成本,低维护,占地面积小、应用灵活以及净化效果好的优势。In view of the fact that the existing gray water treatment device is easy to block, the purification effect is poor, and it is easy to produce secondary pollution. It occupies a large area and is not suitable for application in dense urban areas and scattered rural areas. The state causes the effluent water to become black and smelly. The utility model provides a domestic gray water treatment system integrating water collection, purification treatment and disinfection. A porous horizontal plate is arranged at the bottom, and plants and large-medium-small The distribution and combination of filter materials ensures the purification effect of gray water, avoids the oversaturated anaerobic state of the lower layer, and improves the surrounding reoxygenation environment. It has the advantages of low cost, low maintenance, small footprint, flexible application and good purification effect .
2、技术方案2. Technical solution
为解决上述问题,本实用新型采用如下的技术方案:In order to solve the above problems, the utility model adopts the following technical solutions:
一种生活灰水处理系统,包括集水井、消毒池和生活墙装置;集水井通过管道与生活墙装置底部的进水口连接;消毒池通过管道与生活墙装置底部的出水口连接;集水井与生活墙装置的连接管道上安装有蠕动泵;消毒池与生活墙装置的连接管道上设有出水开关;生活墙装置设置在建筑物一侧,其内从上到下包括植物、布水区、滤料区以及饱和区;滤料区上层为水洗砂层,中层为粗砂层,下层为砾石层;饱和区内填充有多孔水平板,多孔水平板上部侧壁与生活墙装置内侧壁契合,下部侧壁与生活墙装置内侧壁留有空隙;所述生活墙装置底部的进水口以及出水口分别位于饱和区相对的两侧。A domestic gray water treatment system includes a water collection well, a disinfection tank and a living wall device; the water collection well is connected to the water inlet at the bottom of the living wall device through a pipeline; the disinfection tank is connected to the water outlet at the bottom of the living wall device through a pipeline; the water collection well and the living wall device are connected through a pipeline. A peristaltic pump is installed on the connecting pipe of the living wall device; a water outlet switch is installed on the connecting pipe between the disinfection tank and the living wall device; the living wall device is set on one side of the building, which includes plants, water distribution area, Filter material area and saturated area; the upper layer of the filter material area is a washed sand layer, the middle layer is a coarse sand layer, and the lower layer is a gravel layer; the saturated area is filled with a porous horizontal plate, and the upper side wall of the porous horizontal plate fits with the inner wall of the living wall device. There is a gap between the lower side wall and the inner wall of the living wall device; the water inlet and the water outlet at the bottom of the living wall device are respectively located on opposite sides of the saturation zone.
优选地,所述植物包括观赏性花草或藤蔓植物,种植密度为5~20株/m2;所述观赏性花草包括金银花、百合、芦苇、鹤望兰以及莎草等;所述藤蔓植物包括葡萄藤、爬山虎、常春藤以及吊藤莓等。Preferably, the plants include ornamental flowers or vines, with a planting density of 5-20 plants/m 2 ; the ornamental flowers include honeysuckle, lily, reed, strelitzia, and sedge, etc.; the vines include Grape vines, creepers, ivy, hanging vines, etc.
优选地,所述水洗砂层厚度为43~62cm,水洗砂粒径为2~4mm;粗砂层厚度为5~12cm,粗砂粒径为3~7mm;砾石层厚度为5~12cm,砾石粒径为6~12mm。滤料也可以换成其他的滤料,如陶粒、珍珠岩或多种混合物等。同时在系统运行初期时,上部8~14cm的水洗砂与土壤混合以支持植物生长。Preferably, the thickness of the washed sand layer is 43-62 cm, and the particle size of the washed sand is 2-4 mm; the thickness of the coarse sand layer is 5-12 cm, and the particle size of the coarse sand is 3-7 mm; the thickness of the gravel layer is 5-12 cm, and the gravel layer is The particle size is 6-12mm. The filter material can also be replaced with other filter materials, such as ceramsite, perlite or various mixtures. At the same time, in the early stage of system operation, the upper 8-14cm of washed sand is mixed with soil to support plant growth.
优选地,所述多孔水平板底面与生活墙装置底面紧密接触,高度为12~20cm,孔隙度>95%,出水一侧设置有过滤网,以防较大颗粒物流出,避免混合污染。。Preferably, the bottom surface of the porous horizontal plate is in close contact with the bottom surface of the living wall device, the height is 12-20cm, the porosity is >95%, and a filter is provided on the water outlet side to prevent larger particles from flowing out and mixed pollution. .
优选地,所述多孔水平板内部孔径为纵向垂直分布。Preferably, the internal pore diameters of the porous horizontal plate are longitudinally and vertically distributed.
优选地,所述多孔水平板内部孔径为倾斜分布。Preferably, the internal pore diameters of the porous horizontal plate are distributed obliquely.
优选地,所述多孔水平板内部通孔具有一定的弧度。Preferably, the internal through holes of the porous horizontal plate have a certain curvature.
优选地,所述生活墙装置上部还留有2~4cm的超高以及7~15cm的布水区。Preferably, the upper part of the living wall device has a super height of 2-4 cm and a water distribution area of 7-15 cm.
优选地,所述集水井与生活墙装置的连接管道上还设有定时器,所述定时器规格为德力西KG316TS型。Preferably, a timer is provided on the connecting pipe between the water collection well and the living wall device, and the specification of the timer is Delixi KG316TS type.
优选地,所述消毒池与生活墙装置的连接管道上设有出水开关。Preferably, a water outlet switch is provided on the connecting pipe between the disinfection pool and the living wall device.
3、有益效果3. Beneficial effects
相比于现有技术,本实用新型的有益效果为:Compared with the prior art, the beneficial effects of the utility model are:
(1)本实用新型所提供的生活墙灰水处理系统,设有集水井,方便灰水的收集待用;生活墙装置内设有植物以及大-中-小的滤料层(水洗砂层、粗砂层、砾石层),植物本身对污染物进行吸收净化的同时,其根部会聚集大量微生物,根际微生物会促进植物的营养循环、生长代谢、根部环境的维持以及有害污染物的降解,极大的提高水体净化能力,同时,大-中- 小的滤料层及其内附着微生物的截留过滤、生物降解等作用进一步提高了水体污染物的去除效果,通过植物以及滤料层的协同作用可以极大的提高系统对污水的净化效果;(1) The living wall gray water treatment system provided by the utility model is provided with a water collection well to facilitate the collection of gray water for use; the living wall device is provided with plants and large-medium-small filter material layers (washed sand layer) , coarse sand layer, gravel layer), while the plant itself absorbs and purifies pollutants, a large number of microorganisms will gather in its roots, and rhizosphere microorganisms will promote plant nutrient cycle, growth metabolism, maintenance of root environment and degradation of harmful pollutants , which greatly improves the water purification ability. At the same time, the large-medium-small filter layer and the interception and filtration and biodegradation of microorganisms attached to it further improve the removal effect of water pollutants. Through the plant and filter layer Synergy can greatly improve the purification effect of the system on sewage;
生活墙装置底部饱和区内填充有多孔水平板,利于水体的流动以及多孔水平板上部侧壁与生活墙装置内侧壁契合,下部侧壁与生活墙装置内侧壁留有空隙;即有利于水体的流动与气体的排放流动,避免下层过度饱和的厌氧状态,提高周围复氧环境,又可以提高装置空间利用率,多孔板底部与生活墙装底部无需预留空间,减小了装置体积;多孔水平板内部孔径为倾斜分布,且具有一定弧度,可以有效的将悬浮物(TSS)拦截在装置之外,防止装置堵塞;最后,通过消毒池的后续处理,更是进一步提升了净化水体的出水水质;The saturated area at the bottom of the living wall device is filled with a porous horizontal plate, which is beneficial to the flow of the water body and the upper side wall of the porous horizontal plate fits with the inner wall of the living wall device, and there is a gap between the lower side wall and the inner wall of the living wall device; that is, it is beneficial to the flow of the water body The flow and gas discharge flow can avoid the oversaturated anaerobic state of the lower layer, improve the surrounding reoxygenation environment, and improve the space utilization rate of the device. There is no need to reserve space at the bottom of the porous plate and the bottom of the living wall, which reduces the volume of the device; porous The internal aperture of the horizontal plate is obliquely distributed and has a certain radian, which can effectively intercept suspended solids (TSS) outside the device and prevent the device from clogging; finally, through the subsequent treatment of the disinfection tank, the effluent of the purified water body is further improved. water quality;
(2)本实用新型所提供的生活墙灰水处理系统,采用单级处理,并种植有观赏性花草或藤蔓;将生活墙装置设置在建筑物一侧,可以充分考虑周边环境实际特点,减少占地面积,最大程度上减少灰水处理的管理成本和建设成本;利用本实用新型系统进行生活灰水处理的方法,运行操作简单,处理效果好,对生活灰水中总悬浮物(TSS)、生化需氧量(BOD)、总有机碳(TOC)、总氮(TN)以及总磷(TP)的去除率分别达到了94~96%、98~99%、 80~83%、85~88%以及53~56%;从可持续发展的角度来看,将生活污水中的灰水单独处理回用,是一种较前沿的污水处理概念,也是实现水资源循环利用、提高水资源利用率的重要途径;(2) The living wall gray water treatment system provided by the utility model adopts single-stage treatment, and is planted with ornamental flowers and plants or vines; the living wall device is arranged on one side of the building, which can fully consider the actual characteristics of the surrounding environment and reduce the Covering an area, the management cost and construction cost of gray water treatment can be reduced to the greatest extent; the method for domestic gray water treatment using the system of the utility model has simple operation and good treatment effect, and can reduce total suspended solids (TSS), The removal rates of biochemical oxygen demand (BOD), total organic carbon (TOC), total nitrogen (TN) and total phosphorus (TP) reached 94-96%, 98-99%, 80-83%, 85-88% respectively % and 53-56%; From the perspective of sustainable development, the separate treatment and reuse of gray water in domestic sewage is a relatively advanced concept of sewage treatment, and it is also a way to realize the recycling of water resources and improve the utilization rate of water resources. important way of
(3)本实用新型所提供的生活灰水处理系统,结构简单,设计合理,易于制造,易于操作,所选材料成本低廉,净化效果显著,尤其适合密集的城镇地区和分散的农村地区,具有较大的市场前景和推广应用价值。(3) The domestic gray water treatment system provided by the utility model is simple in structure, reasonable in design, easy to manufacture and easy to operate, the cost of the selected materials is low, and the purification effect is remarkable, especially suitable for dense urban areas and scattered rural areas. Larger market prospects and promotion and application value.
附图说明Description of drawings
图1为本实用新型中生活灰水处理系统的结构示意图;Fig. 1 is the structural representation of domestic gray water treatment system in the utility model;
图2为本实用新型中多孔水平板结构示意图;Fig. 2 is the structure schematic diagram of porous horizontal plate in the utility model;
图3为本实用新型中多孔水平板结构示意图;Fig. 3 is the schematic diagram of the structure of the porous horizontal plate in the utility model;
图4为本实用新型中多孔水平板结构示意图;Fig. 4 is a structural schematic diagram of a porous horizontal plate in the utility model;
图中:1、集水井;2、生活墙装置;3、消毒池;4、出水开关;5、植物;6、滤料区;7、水洗砂层;8、粗砂层;9、砾石层;10、多孔水平板;11、蠕动泵;12、定时器;13、建筑物;14、过滤网。In the figure: 1. Water collection well; 2. Living wall device; 3. Disinfection tank; 4. Outlet switch; 5. Plant; 6. Filter area; 7. Washed sand layer; 8. Coarse sand layer; 9. Gravel layer ; 10, porous horizontal plate; 11, peristaltic pump; 12, timer; 13, building; 14, filter.
具体实施方式Detailed ways
下面结合附图以及具体实施例对本实用新型进行详细描述。The utility model will be described in detail below in conjunction with the accompanying drawings and specific embodiments.
实施例1Example 1
如图1所示,一种生活灰水处理系统,包括集水井1、消毒池3、生活墙装置2;生活墙装置2设置在建筑物13一侧,其内从上到下包括植物5、滤料区6以及饱和区,生活墙装置 2底部还设有进水口以及出水口,分别位于饱和区相对的两侧壁;集水井1通过管道与生活墙装置2的进水口连接,消毒池3通过管道与生活墙装置2的出水口连接;集水井1与生活墙装置2的连接管道上安装有蠕动泵11以及定时器12(可以采用德力西KG316TS型定时器。);消毒池3与生活墙装置2的连接管道上设有出水开关4。As shown in Figure 1, a kind of domestic gray water treatment system comprises a water collection well 1, a disinfection pond 3, and a living wall device 2; the living wall device 2 is arranged on one side of a building 13, and includes plants 5, The filter area 6 and the saturated area, the bottom of the living wall device 2 are also provided with a water inlet and a water outlet, which are respectively located on the opposite side walls of the saturated area; Connect with the water outlet of the living wall device 2 through the pipeline; Peristaltic pump 11 and timer 12 (Delixi KG316TS type timer can be used.) are installed on the connecting pipeline between the sump well 1 and the living wall device 2; Disinfecting pool 3 and The connecting pipe of the living wall device 2 is provided with a water outlet switch 4 .
生活墙装置2上层种植的植物5为金银花,种植密度为5株/m2;The plant 5 planted on the upper layer of the living wall device 2 is honeysuckle, and the planting density is 5 plants/m 2 ;
滤料区6内上层为水洗砂层7厚度为43cm,水洗砂粒径为2~4mm;粗砂层厚度为5cm,粗砂粒径为3~7mm;砾石层厚度为5cm,砾石粒径为6~12mm。滤料也可以换成其他的滤料,如陶粒、珍珠岩或多种混合物等。同时在系统运行初期时,上部的水洗砂与土壤混合以支持植物生长。The upper layer in the filter area 6 is a washed sand layer 7 with a thickness of 43cm and a washed sand particle size of 2 to 4 mm; a coarse sand layer with a thickness of 5 cm and a coarse sand particle size of 3 to 7 mm; a gravel layer with a thickness of 5 cm and a gravel particle size of 6 ~ 12mm. The filter material can also be replaced with other filter materials, such as ceramsite, perlite or various mixtures. At the same time, in the early stage of system operation, the upper washed sand is mixed with soil to support plant growth.
饱和区内填充有多孔水平板10,多孔水平板10侧壁与生活墙装置2内侧壁契合,底部呈现为倒梯台状,出水一侧设置有过滤网14,以防较大颗粒物流出,避免混合污染,内部孔径为纵向垂直分布,高度为12cm,孔隙度>95%,避免下层过度饱和的厌氧状态,提高周围复氧环境。The saturated area is filled with porous horizontal plates 10, the side walls of the porous horizontal plates 10 fit with the inner walls of the living wall device 2, the bottom is in the shape of an inverted terrace, and a filter screen 14 is provided on the water outlet side to prevent larger particles from flowing out and avoid Mixed pollution, the internal pore diameter is vertically distributed, the height is 12cm, and the porosity is >95%, so as to avoid the oversaturated anaerobic state of the lower layer and improve the surrounding reoxygenation environment.
本实施例中灰水处理系统的工作原理为:集水井1用于收集需要处理的生活灰水,蠕动泵11开启,调节它的转速来控制进水速率,(预先对定时器12进行开关时间设定,使其进入定时模式),集水井1中的生活灰水在蠕动泵11的驱动作用下进入生活墙装置2中,进入生活墙装置2的待净化灰水依次经过多孔水平板10、砾石层9、粗砂层8以及水洗砂层7后进入布水区,当达到设定时间后,定时器12自动控制蠕动泵11关闭,停止进水,生活墙装置 2内的灰水在植物5以及滤料区6的协同作用下进行循环净化。净化完成后,打开出水开关4,生活墙装置2内的水体通过进入消毒池3,进行进一步消毒净化。The working principle of the gray water treatment system in this embodiment is: the water collection well 1 is used to collect the domestic gray water that needs to be treated, the peristaltic pump 11 is turned on, and its rotating speed is adjusted to control the water intake rate, (the timer 12 is switched on and off in advance set to make it enter the timing mode), the domestic gray water in the sump 1 enters the living wall device 2 under the driving action of the peristaltic pump 11, and the gray water to be purified entering the living wall device 2 passes through the porous horizontal plate 10, After the gravel layer 9, the coarse sand layer 8 and the washed sand layer 7 enter the water distribution area, when the set time is reached, the timer 12 automatically controls the peristaltic pump 11 to shut down and stop the water intake. 5 and the synergistic effect of the filter material area 6 for circular purification. After the purification is completed, the water outlet switch 4 is turned on, and the water body in the living wall device 2 enters the disinfection pool 3 for further disinfection and purification.
本实施例中,在系统正式运行前,将植物5转移到生活墙装置2中,用自来水浇灌,并定期补充营养液,持续10天。进水水力负荷范围为55~110mm/d,pH范围为6.5~9.3,总悬浮物(TSS)浓度范围为50~400mg/L,生化需氧量(BOD)浓度范围为50~800mg/L,总有机碳(TOC)浓度范围为30~100mg/L,总氮(TN)浓度范围为5~100mg/L,总磷(TP) 浓度范围为1~150mg/L。系统每周进水5天,休息2天。In this embodiment, before the official operation of the system, the plants 5 are transferred to the living wall device 2, watered with tap water, and supplemented with nutrient solution regularly for 10 days. Influent hydraulic load range is 55-110mm/d, pH range is 6.5-9.3, total suspended solids (TSS) concentration range is 50-400mg/L, biochemical oxygen demand (BOD) concentration range is 50-800mg/L, The total organic carbon (TOC) concentration ranges from 30 to 100 mg/L, the total nitrogen (TN) concentration ranges from 5 to 100 mg/L, and the total phosphorus (TP) concentration ranges from 1 to 150 mg/L. The system was flooded 5 days a week and rested 2 days a week.
此系统连续运行3个月对洗浴灰水进行了净化,每隔3天对出水水质进行监测,最终的处理效果如表1所示,对灰水中的TSS、BOD、TOC以及TN均有较高的去除效果,对TP 也保持了较高的去除率。The system has been running continuously for 3 months to purify bathing gray water, and monitor the quality of effluent water every 3 days. The final treatment effect is shown in Table 1, and the TSS, BOD, TOC and TN in gray water are all higher. The removal effect of TP also maintained a high removal rate.
表1实施例1中某洗浴灰水的进水与出水水质测试指标情况The influent and effluent water quality test index situation of certain bath gray water in the embodiment 1 of table 1
实施例2Example 2
本实施例在实施例1的基础上对灰水处理系统进行了进一步优化,其中不同之处在于,所处理灰水种类为洗衣灰水,种植植物5为观赏性葡萄藤,种植密度为20株/m2,利用建筑物13墙体使根系生长和攀缘。In this example, the gray water treatment system is further optimized on the basis of Example 1. The difference is that the type of gray water to be treated is laundry gray water, and planting plants 5 are ornamental grape vines, and the planting density is 20 plants. /m 2 , using the walls of the building 13 to make the roots grow and climb.
滤料区6内上层为水洗砂层7厚度为62cm,水洗砂粒径为2.5~3mm;粗砂层厚度为12cm,粗砂粒径为4~5mm;砾石层厚度为12cm,砾石粒径为8~10mm。The upper layer in the filter area 6 is a washed sand layer 7 with a thickness of 62cm and a washed sand particle size of 2.5 to 3 mm; a coarse sand layer with a thickness of 12 cm and a coarse sand particle size of 4 to 5 mm; a gravel layer with a thickness of 12 cm and a gravel particle size of 8 ~ 10mm.
多孔水平板10高度为20cm,内部孔径倾斜分布;其他部分同实施例1。The height of the porous horizontal plate 10 is 20 cm, and the internal apertures are distributed obliquely; other parts are the same as in Embodiment 1.
本实施例中进水水力负荷为70mm/d,pH范围为8.3~9.3,总悬浮物(TSS)浓度范围为 180~310mg/L,生化需氧量(BOD)浓度范围为80~450mg/L,总有机碳(TOC)浓度范围为20~60mg/L,总氮(TN)浓度范围为5~15mg/L,总磷(TP)浓度范围为10~100mg/L。In this embodiment, the influent hydraulic load is 70 mm/d, the pH range is 8.3 to 9.3, the total suspended solids (TSS) concentration range is 180 to 310 mg/L, and the biochemical oxygen demand (BOD) concentration range is 80 to 450 mg/L , the total organic carbon (TOC) concentration ranges from 20 to 60 mg/L, the total nitrogen (TN) concentration ranges from 5 to 15 mg/L, and the total phosphorus (TP) concentration ranges from 10 to 100 mg/L.
此系统连续运行2个月对洗衣灰水进行了净化,每隔5天对出水水质进行监测,最终的处理效果如表2所示,对灰水中的TSS、BOD、TOC以及TN均有较高的去除效果,对TP 也保持了较高的去除率。The system has been running continuously for 2 months to purify the laundry gray water, and monitor the quality of the effluent water every 5 days. The final treatment effect is shown in Table 2, and the TSS, BOD, TOC and TN in the gray water are all higher. The removal effect of TP also maintained a high removal rate.
表2实施例2中某洗衣灰水的进水与出水水质测试指标情况The influent and effluent water quality test index situation of certain laundry gray water in the embodiment 2 of table 2
实施例3Example 3
本实施例在实施例2的基础上对灰水处理系统进行了进一步优化,其中不同之处在于,所处理灰水种类为厨房灰水,种植的植物5为百合,种植密度为9株/m2;This example further optimizes the gray water treatment system on the basis of Example 2, where the difference is that the type of gray water to be treated is kitchen gray water, the plant 5 is lily, and the planting density is 9 plants/m 2 ;
滤料区6内上层为水洗砂层7厚度为53cm,水洗砂粒径为3~3.5mm;粗砂层厚度为8cm,粗砂粒径为3.8~6mm;砾石层厚度为7cm,砾石粒径为9~11mm。The upper layer in the filter area 6 is a washed sand layer 7 with a thickness of 53cm and a washed sand particle size of 3-3.5mm; a coarse sand layer with a thickness of 8cm and a coarse sand particle size of 3.8-6mm; a gravel layer with a thickness of 7cm and a gravel particle size of It is 9-11mm.
多孔水平板10内部通孔具有一定的弧度,高度为16cm;其他部分同实施例1。The internal through holes of the porous horizontal plate 10 have a certain radian, and the height is 16 cm; other parts are the same as in the first embodiment.
本实施例中进水水力负荷为85mm/d,pH范围为6.5~8.3,总悬浮物(TSS)浓度范围为 150~400mg/L,生化需氧量(BOD)浓度范围为450~800mg/L,总有机碳(TOC)浓度范围为40~100mg/L,总氮(TN)浓度范围为50~100mg/L,总磷(TP)浓度范围为20~150mg/L。In this embodiment, the influent hydraulic load is 85 mm/d, the pH range is 6.5 to 8.3, the total suspended solids (TSS) concentration range is 150 to 400 mg/L, and the biochemical oxygen demand (BOD) concentration range is 450 to 800 mg/L , the total organic carbon (TOC) concentration ranges from 40 to 100 mg/L, the total nitrogen (TN) concentration ranges from 50 to 100 mg/L, and the total phosphorus (TP) concentration ranges from 20 to 150 mg/L.
此系统连续运行3个月对厨房灰水进行了净化,每隔5天对出水水质进行监测,处理效果如表3所示,对灰水中的TSS、BOD、TOC以及TN均有较高的去除效果,对TP也保持了较高的去除率。The system has been running continuously for 3 months to purify the gray water in the kitchen, and the quality of the effluent water is monitored every 5 days. The treatment effect is shown in Table 3, and the TSS, BOD, TOC and TN in the gray water are all highly removed. As a result, it also maintained a high removal rate for TP.
表3实施例3中某厨房灰水的进水与出水水质测试指标情况The influent and effluent water quality test index situation of certain kitchen gray water in the embodiment 3 of table 3
实施例4Example 4
本实施例在实施例1的基础上对灰水处理系统进行了进一步优化,其中不同之处在于,所处理灰水种类为人工灰水,种植的植物5为鹤望兰,种植密度为12株/m2,其他部分同实施例1。This example further optimizes the gray water treatment system on the basis of Example 1, where the difference is that the type of gray water treated is artificial gray water, and the plant 5 is Strelitzia chinensis, and the planting density is 12 plants /m 2 , other parts are the same as in Example 1.
本实施例中进水灰水水力负荷为100mm/d,pH范围为7.2~7.8,总悬浮物(TSS)浓度范围为70~120mg/L,生化需氧量(BOD)浓度范围为104~270mg/L,总有机碳(TOC)浓度范围为30~60mg/L,总氮(TN)浓度范围为5~12mg/L,总磷(TP)浓度范围为2~4mg/L。In this embodiment, the hydraulic load of the influent gray water is 100 mm/d, the pH range is 7.2 to 7.8, the total suspended solids (TSS) concentration range is 70 to 120 mg/L, and the biochemical oxygen demand (BOD) concentration range is 104 to 270 mg /L, the concentration of total organic carbon (TOC) ranges from 30 to 60 mg/L, the range of total nitrogen (TN) concentration ranges from 5 to 12 mg/L, and the range of total phosphorus (TP) concentration ranges from 2 to 4 mg/L.
此系统连续运行2个月对人工灰水进行了净化,每隔5天对出水水质进行监测,处理效果如表4所示。The system has been continuously operated for 2 months to purify the artificial gray water, and the quality of the effluent water is monitored every 5 days. The treatment effect is shown in Table 4.
表4实施例4中某人工灰水的进水与出水水质测试指标情况The influent and effluent water quality test index situation of a certain artificial gray water in the embodiment 4 of table 4
对灰水中的TSS、BOD、TOC以及TN均有较高的去除效果,对TP也保持了较高的去除率。It has a high removal effect on TSS, BOD, TOC and TN in gray water, and maintains a high removal rate on TP.
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