CN104860398B - Intensive device and its method of construction for processing domestic sewage in rural areas - Google Patents
Intensive device and its method of construction for processing domestic sewage in rural areas Download PDFInfo
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Abstract
本发明公开了一种用于处理农村生活污水的集约型装置及其建造方法,涉及污水处理领域,包括若干污水汇集管道;顺次连接的厌氧消化系统好氧消化池和生态净化系统;若干污水汇集管道均为一端与居民用水排水口连接,另一端与厌氧消化系统连接;厌氧消化系统包括顺次连接的一级厌氧消化池、二级厌氧消化池和三级厌氧消化池;一级厌氧消化池、二级厌氧消化池、三级厌氧消化池和好氧消化池的容积计算公式均为:V=aNqt/(24*1000),N为服务的人口数量;a为污水的产生系数0.7~0.9;q为人均用水量80~120L/d,t为水在对应消化池中停留的时间。本发明不仅占地面积较小,而且成本较低。
The invention discloses an intensive device for treating domestic sewage in rural areas and a construction method thereof, relating to the field of sewage treatment, comprising a plurality of sewage collection pipes; an aerobic digestion tank of an anaerobic digestion system connected in sequence and an ecological purification system; several One end of the sewage collection pipeline is connected to the residential water outlet, and the other end is connected to the anaerobic digestion system; the anaerobic digestion system includes the first-level anaerobic digestion tank, the second-level anaerobic digestion tank and the third-level anaerobic digestion system connected in sequence pool; the calculation formulas for the volume of the primary anaerobic digester, the secondary anaerobic digester, the tertiary anaerobic digester and the aerobic digester are: V=aNqt/(24*1000), N is the number of people served ; a is the sewage production coefficient of 0.7-0.9; q is the per capita water consumption of 80-120L/d, and t is the time that water stays in the corresponding digester. The invention not only occupies a small area, but also has a low cost.
Description
技术领域technical field
本发明涉及污水处理领域,具体涉及一种用于处理农村生活污水的集约型装置及其建造方法。The invention relates to the field of sewage treatment, in particular to an intensive device for treating rural domestic sewage and a construction method thereof.
背景技术Background technique
随着农村经济的发展和城镇化的不断推进,农村耕种的农药和肥料残留、养殖污水排放量急剧增加,对自然水体和土壤造成的严重的污染,同时农村分散式生活产生的大量污水也直接排入河流和湖泊中,造成严重的水体、土壤污染,水体和土壤被污染后,有害化合物、重金属等污染物通过食物链进入人体,导致农村癌症人口急剧增加,严重损害了农村人口的健康。With the development of the rural economy and the continuous advancement of urbanization, the discharge of pesticide and fertilizer residues in rural farming and aquaculture sewage has increased sharply, causing serious pollution to natural water bodies and soil. It is discharged into rivers and lakes, causing serious water and soil pollution. After the water and soil are polluted, harmful compounds, heavy metals and other pollutants enter the human body through the food chain, leading to a sharp increase in the number of cancer patients in rural areas and seriously damaging the health of the rural population.
美国、日本等发达国家处理农村生活污水积累了丰富的经验,主要是将污染物就地无害化处理和资源化处理。就地处理的方法为:将污染物排入土地或湿地等自然系统,进行自然分解;资源化处理的方法为:将污染物排入砂滤池、一体化好氧处理系统、净化槽等人工处理系统,不仅能够将污染物进行净化,而且能够得到生物肥料。The United States, Japan and other developed countries have accumulated rich experience in the treatment of rural domestic sewage, mainly in the in-situ harmless treatment and resource treatment of pollutants. The method of on-site treatment is: discharge pollutants into natural systems such as land or wetlands for natural decomposition; the method of resource treatment is: discharge pollutants into sand filters, integrated aerobic treatment systems, purification tanks and other artificial The treatment system can not only purify pollutants, but also obtain biological fertilizers.
采用就地无害化处理和资源化处理的能量消耗较少、成本较低、运行简单、管理方便,符合我国农村发展落后、技术含量低、人才紧缺、自动化程度低、经济滞后的现状。The use of in-situ harmless treatment and resource treatment has less energy consumption, lower cost, simple operation, and convenient management, which is in line with the current situation of backward rural development in my country, low technical content, shortage of talents, low degree of automation, and economic lag.
申请号为201010139475.0的发明专利公开了一种生活污水处理装置,该装置包括顺次连接的沉砂池、厌氧消化池和生态净化滤池,采用该方法处理后的污水能够达到国家污水综合排放标准GB8978-1996的一级要求。但该装置的占地面积较大,制作成本较高,结构复杂、管理维护难度大,不适应农村地区使用。The invention patent with the application number 201010139475.0 discloses a domestic sewage treatment device, which includes a grit chamber, anaerobic digestion tank and an ecological purification filter connected in sequence. The sewage treated by this method can reach the national sewage comprehensive discharge The first level requirement of standard GB8978-1996. However, the device occupies a large area, is expensive to manufacture, has a complex structure, is difficult to manage and maintain, and is not suitable for use in rural areas.
发明内容Contents of the invention
针对现有技术中存在的缺陷,本发明的目的在于提供一种用于处理农村生活污水的集约型装置及其建造方法,不仅占地面积较小,而且运行管理方便、建造和维护成本较低。In view of the defects existing in the prior art, the purpose of the present invention is to provide an intensive device for treating rural domestic sewage and its construction method, which not only occupies a small area, but also is convenient for operation and management, and has low construction and maintenance costs .
为达到以上目的,本发明采取的技术方案是:一种用于处理农村生活污水的集约型装置,包括:若干污水汇集管道;In order to achieve the above purpose, the technical solution adopted by the present invention is: an intensive device for treating domestic sewage in rural areas, including: several sewage collection pipes;
顺次连接的厌氧消化系统、好氧消化池和生态净化系统;所述若干污水汇集管道均为一端与居民用水排水口连接,另一端与厌氧消化系统连接;所述厌氧消化系统包括顺次连接的一级厌氧消化池、二级厌氧消化池和三级厌氧消化池;An anaerobic digestion system, an aerobic digestion tank and an ecological purification system connected in sequence; one end of the sewage collection pipes is connected to the residential water outlet, and the other end is connected to the anaerobic digestion system; the anaerobic digestion system includes The first-stage anaerobic digester, the second-stage anaerobic digester and the third-stage anaerobic digester connected in sequence;
所述一级厌氧消化池、二级厌氧消化池、三级厌氧消化池和好氧消化池的容积计算公式均为:V=aNqt/(24*1000),所述N为服务的人口数量;所述a为污水的产生系数0.7~0.9;所述q为人均用水量80~120L/d,所述t为水在对应消化池中停留的时间,水在一级厌氧消化池中停留的时间为4~7天、水在二级厌氧消化池中停留的时间为2~4天、水在三级厌氧消化池中停留的时间为2~4天、水在好氧消化池中停留的时间为2~4天。The volume calculation formulas of the first-stage anaerobic digester, the second-stage anaerobic digester, the third-stage anaerobic digester and the aerobic digester are all: V=aNqt/(24*1000), and the N is the service population; said a is the sewage production coefficient of 0.7-0.9; said q is the per capita water consumption of 80-120L/d, and said t is the time that water stays in the corresponding digester, and the water in the first-level anaerobic digester The residence time of water is 4-7 days, the residence time of water in the secondary anaerobic digester is 2-4 days, the residence time of water in the third-stage anaerobic digester is 2-4 days, and the residence time of water in the aerobic digester is 2-4 days. The time to stay in the digester is 2 to 4 days.
在上述技术方案的基础上,述一级厌氧消化池的内部设置有厌氧微生物填料层,所述厌氧微生物填料层与一级厌氧消化池顶部平行,所述厌氧微生物填料层的顶部与一级厌氧消化池顶部之间的距离为80~100cm。On the basis of the above technical scheme, an anaerobic microbial filler layer is arranged inside the first-stage anaerobic digester, and the anaerobic microbial filler layer is parallel to the top of the first-stage anaerobic digester, and the anaerobic microbial filler layer is The distance between the top and the top of the primary anaerobic digester is 80-100cm.
在上述技术方案的基础上,所述一级厌氧消化池和二级厌氧消化池通过第一连通管连接,所述第一连通管包括进水端和出水端,所述进水端高于出水端,所述进水端位于一级厌氧消化池的内部,所述出水端位于二级厌氧消化池的内部,所述进水端与一级厌氧消化池内顶之间的距离为15~30cm,出水端与二级厌氧消化池内底之间的距离为30~50cm。On the basis of the above technical solution, the first-stage anaerobic digester and the second-stage anaerobic digester are connected through a first connecting pipe, and the first connecting pipe includes a water inlet end and a water outlet end, and the water inlet end is as high as At the water outlet, the water inlet is located inside the primary anaerobic digester, the water outlet is located inside the secondary anaerobic digester, the distance between the water inlet and the inner top of the primary anaerobic digester The distance between the water outlet and the inner bottom of the secondary anaerobic digester is 30-50cm.
在上述技术方案的基础上,所述二级厌氧消化池和三级厌氧消化池通过第二连通管连接,所述第二连通管包括进水端和出水端,所述进水端高于出水端,所述进水端位于二级厌氧消化池的内部,所述出水端位于三级厌氧消化池的内部,所述进水端与二级厌氧消化池内顶之间的距离为15~30cm,所述出水端与三级厌氧消化池内底之间的距离为30~50cm。On the basis of the above technical solution, the secondary anaerobic digester and the tertiary anaerobic digester are connected through a second connecting pipe, the second connecting pipe includes a water inlet end and a water outlet end, and the water inlet end is as high as At the water outlet, the water inlet is located inside the secondary anaerobic digester, the water outlet is located inside the third-stage anaerobic digester, the distance between the water inlet and the inner top of the second-stage anaerobic digester The distance between the water outlet and the inner bottom of the tertiary anaerobic digester is 30-50 cm.
在上述技术方案的基础上,所述好氧消化池通过第三连通管与厌氧消化系统的三级厌氧消化池连接,所述第三连通管包括进水端和出水端,所述进水端高于出水端,所述进水端与三级厌氧消化池内顶之间的距离为15~30cm,所述出水端与好氧消化池内底之间的距离为15~30cm。On the basis of the above technical solution, the aerobic digestion tank is connected to the three-stage anaerobic digestion tank of the anaerobic digestion system through a third connecting pipe, the third connecting pipe includes a water inlet end and a water outlet end, and the inlet The water end is higher than the water outlet end, the distance between the water inlet end and the inner top of the three-stage anaerobic digester is 15-30cm, and the distance between the water outlet end and the inner bottom of the aerobic digester is 15-30cm.
在上述技术方案的基础上,所述好氧消化池的内部设置有曝气装置和好氧净化装置,所述曝气装置位于好氧净化装置的上方,所述好氧净化装置包括自上而下依次设置与好氧微生物填料层、秸秆碳层、砾石层和滤网,好氧微生物填料层与好养消化池内底之间的距离为30~50cm,其横截面呈方形,其表面积与好样消化池底面积相等。On the basis of the above technical solution, the inside of the aerobic digestion tank is provided with an aeration device and an aerobic purification device, the aeration device is located above the aerobic purification device, and the aerobic purification device includes a top-down The aerobic microbial filler layer, straw carbon layer, gravel layer and filter screen are arranged in sequence. The distance between the aerobic microbial filler layer and the inner bottom of the aerobic digester is 30-50cm, and its cross section is square, and its surface area is the same as that of the aerobic microbial filler layer. The sample digesters have the same bottom area.
在上述技术方案的基础上,所述生态净化系统包括若干引流单元和若干种植管,每个引流单元上均设置有若干引流管,所述每个引流管均与一个种植管对应,所述每个引流管均为一端与好氧消化池连接,另一端通过对应的种植管与清水收集池连接。On the basis of the above technical solution, the ecological purification system includes several drainage units and several planting pipes, each drainage unit is provided with several drainage pipes, each of the drainage pipes corresponds to a planting pipe, each of the One end of each drainage tube is connected to the aerobic digestion tank, and the other end is connected to the clear water collection tank through the corresponding planting tube.
在上述技术方案的基础上,所述一级厌氧消化池与二级厌氧消化池、三级厌氧消化池、好氧消化池的体积比为3~5:1:1:1~2。On the basis of the above technical scheme, the volume ratio of the first-stage anaerobic digester to the second-stage anaerobic digester, the third-stage anaerobic digester, and the aerobic digester is 3-5:1:1:1-2 .
在上述技术方案的基础上,所述每根污水汇集管道均伸入一级厌氧消化池的内部,污水汇集管道包括进水端和出水端,所述进水端高于出水端,进水端与居民排污口连接,出水端位于一级厌氧消化池内,出水端与一级厌氧消化池的内底之间的距离为60~100cm。On the basis of the above technical scheme, each of the sewage collection pipes extends into the interior of the primary anaerobic digester, the sewage collection pipe includes a water inlet end and a water outlet end, the water inlet end is higher than the water outlet end, and the water inlet The end is connected to the sewage outlet of the residents, the water outlet is located in the first-level anaerobic digestion tank, and the distance between the water outlet and the inner bottom of the first-level anaerobic digestion tank is 60-100cm.
一种集约型装置的建造方法,其特征在于,包括以下步骤:A method for building an intensive device, characterized in that it comprises the following steps:
S1:确定建造地的人口数量N、污水的产生系数a和人均用水量q,根据容积计算公式V=aNqt/(24*1000),计算一级厌氧消化池、二级厌氧消化池、三级厌氧消化池和好氧消化池的容积,所述t为水在对应消化池中停留的时间,水在一级厌氧消化池中停留的时间为4~7天、水在二级厌氧消化池中停留的时间为2~4天、水在三级厌氧消化池中停留的时间为2~4天、水在好氧消化池中停留的时间为2~4天,转入步骤S2;S1: Determine the population N of the construction site, the sewage production coefficient a, and the per capita water consumption q, and calculate the primary anaerobic digester, secondary anaerobic digester, and The volume of the three-stage anaerobic digester and the aerobic digester, the t is the time that the water stays in the corresponding digester, the time that the water stays in the first-stage anaerobic digester is 4 to 7 days, and the water stays in the second-stage anaerobic digester The time of staying in the anaerobic digester is 2 to 4 days, the time of water staying in the three-stage anaerobic digester is 2 to 4 days, and the time of water staying in the aerobic digester is 2 to 4 days. Step S2;
S2:选择平地作为建设地点,在建设地点上挖建顺次排列的一级厌氧消化池、二级厌氧消化池、三级厌氧消化池和好氧消化池,转入步骤S3:S2: Choose flat land as the construction site, dig and build the first-level anaerobic digestion tank, the second-level anaerobic digestion tank, the third-level anaerobic digestion tank and the aerobic digestion tank arranged in sequence on the construction site, and turn to step S3:
S3:安装隔栅井和若干污水汇集管道,将若干污水汇集管道的一端与居民用水排水口连接,另一端与一级厌氧消化池连接,在一级厌氧消化池和二级厌氧消化池之间安装第一连通管连接,在二级厌氧消化池和三级厌氧消化池之间安装第二连通管,在三级厌氧消化池和好氧消化池之间安装第三连通管,转入步骤S4;S3: Install grid wells and several sewage collection pipes, connect one end of several sewage collection pipes to the residential water outlet, and connect the other end to the first-level anaerobic digestion tank. The first connecting pipe is installed between the tanks, the second connecting pipe is installed between the secondary anaerobic digester and the third-stage anaerobic digester, the third connecting pipe is installed between the third-stage anaerobic digester and the aerobic digester, and the transfer Enter step S4;
S4:在一级厌氧消化池的内顶安装反冲洗装置,在一级厌氧消化池的内部安装托网和厌氧微生物填料层;在好氧消化池的内部安装曝气装置和好氧净化装置,转入步骤S5;S4: Install a backwashing device on the top of the primary anaerobic digester, install a tray and anaerobic microbial packing layer inside the primary anaerobic digester; install an aeration device and aerobic filter inside the aerobic digester Cleaning device, go to step S5;
S5:将好氧消化池的外部安装若干引流单元和若干种植管,在种植管上播种具有净化作用的植物,调试所述集约型装置至正常运行。S5: Install several drainage units and several planting pipes outside the aerobic digester, sow plants with purification effect on the planting pipes, and adjust the intensive device to normal operation.
与现有技术相比,本发明的优点在于:Compared with the prior art, the present invention has the advantages of:
(1)本发明中用于处理农村生活污水的集约型装置,包括相互连接的厌氧消化系统和好氧消化池,厌氧消化系统包括顺次连接的一级厌氧消化池、二级厌氧消化池和三级厌氧消化池;其中,一级厌氧消化池、二级厌氧消化池、三级厌氧消化池和好氧消化池的容积计算公式均为:V=aNqt/(24*1000),所述N为服务的人口数量;所述a为污水的产生系数0.7~0.9;所述q为人均用水量80~120L/d,所述t为水在对应消化池中停留的时间,本与现有技术中根据经验确定消化池尺寸,容易造成占地面积较大,成本较高相比,发明根据污水消化的时间确定消化池的尺寸,占地面积比较合理,制作成本较低。(1) The intensive device for processing rural domestic sewage in the present invention includes an anaerobic digestion system and an aerobic digestion tank connected to each other, and the anaerobic digestion system includes a first-level anaerobic digestion tank and a second-level anaerobic digestion tank connected in sequence. Aerobic digester and three-stage anaerobic digester; among them, the volume calculation formulas of the first-stage anaerobic digester, the second-stage anaerobic digester, the third-stage anaerobic digester and the aerobic digester are: V=aNqt/( 24*1000), the N is the number of people served; the a is the sewage production coefficient of 0.7-0.9; the q is the per capita water consumption of 80-120L/d, and the t is the water staying in the corresponding digester Compared with the size of the digestion tank determined based on experience in the prior art, which easily leads to a larger footprint and higher cost, the invention determines the size of the digestion tank according to the time of sewage digestion, and the floor area is more reasonable and the production cost is lower. lower.
(2)本发明中用于处理农村生活污水的集约型装置,包括第一连通管、第二连通管和第三连通管,第一连通管、第二连通管和第三连通管均包括进水端和出水端,每个进水端均高于对应的出水端,所有进水端与对应消化池内顶之间的距离均为15~30cm,进入进水端的水均为消化池内的上层清水;所有出水端与对应消化池内底之间的距离均为30~50cm,出水端的水进入下一消化池后,均位于消化池的底部,水由底部向上运动的过程中,其内部的杂质会发生自然沉降而净化。(2) The intensive device for processing rural domestic sewage in the present invention comprises a first connecting pipe, a second connecting pipe and a third connecting pipe, and the first connecting pipe, the second connecting pipe and the third connecting pipe all include Water end and water outlet end, each water inlet end is higher than the corresponding water outlet end, the distance between all water inlet ends and the inner top of the corresponding digestion tank is 15-30cm, and the water entering the water inlet end is the upper clear water in the digestion tank ;The distance between all water outlets and the inner bottom of the corresponding digester is 30-50cm. After the water at the outlet enters the next digester, it is located at the bottom of the digester. When the water moves upward from the bottom, the impurities inside will be Occurrence of natural sedimentation and purification.
(3)本发明中用于处理农村生活污水的集约型装置,第一连通管、第二连通管和第三连通管的高度依次降低,污水流动为溢满自流方式,无抽水动力系统,建造和维护费用低,能够节约能源。(3) In the intensive device used for processing rural domestic sewage in the present invention, the heights of the first connecting pipe, the second connecting pipe and the third connecting pipe are successively reduced, and the sewage flows in an overflowing self-flowing manner without a pumping power system. And maintenance costs are low, can save energy.
(4)本发明中用于处理农村生活污水的集约型装置,包括生态净化系统,生态净化系统包括种植管,种植管为迂回弯折的管道,管道上种植有植物,植物能够吸附水中的重金属,N、P化合物,深层净化水质、美化环境,增加经济效益。(4) The intensive device for processing rural domestic sewage in the present invention includes an ecological purification system, the ecological purification system includes a planting pipe, the planting pipe is a circuitous and bent pipeline, plants are planted on the pipeline, and the plants can absorb heavy metals in the water , N, P compounds, deep water purification, beautify the environment, increase economic benefits.
附图说明Description of drawings
图1为本发明实施例中用于处理农村生活污水的集约型装置的结构示意图;Fig. 1 is the structural representation of the intensive device for processing rural domestic sewage in the embodiment of the present invention;
图2为厌氧消化系统的结构示意图。Fig. 2 is a schematic structural diagram of an anaerobic digestion system.
图中:1-污水汇集管道,2-隔栅井,3-厌氧消化系统,4-好氧消化池,5-好氧微生物填料层,6-太阳能发电装置,7-曝气装置,8-引流单元,9-种植管,10-清水收集池,11-第三连通管,12-第二滤网,13-砾石层,14-反冲洗装置,15-厌氧微生物填料层,16-一级厌氧消化池,17-第一连通管,18-第二连通管,19-托网,20-二级厌氧消化池,21-三级厌氧消化池。In the figure: 1-sewage collection pipeline, 2-grid well, 3-anaerobic digestion system, 4-aerobic digestion tank, 5-aerobic microbial packing layer, 6-solar power generation device, 7-aeration device, 8 -drainage unit, 9-planting pipe, 10-clear water collection tank, 11-third connecting pipe, 12-second filter screen, 13-gravel layer, 14-backwashing device, 15-anaerobic microbial packing layer, 16- First-level anaerobic digester, 17-first connecting pipe, 18-second connecting pipe, 19-tray net, 20-secondary anaerobic digester, 21-tertiary anaerobic digester.
具体实施方式detailed description
以下结合附图及实施例对本发明作进一步详细说明。The present invention will be described in further detail below in conjunction with the accompanying drawings and embodiments.
参见图1所示,本发明实施例提供一种用于处理农村生活污水的集约型装置及其建造方法,包括若干污水汇集管道1,污水汇集管道1与水平方向的夹角为5°~10°,污水汇集管道1的直径为10~15cm,污水汇集管道1采用PVC制成,或者采用砖和水泥砌成。Referring to Fig. 1, an embodiment of the present invention provides an intensive device for treating domestic sewage in rural areas and a construction method thereof, including a plurality of sewage collection pipes 1, and the included angle between the sewage collection pipes 1 and the horizontal direction is 5° to 10° °, the diameter of the sewage collection pipe 1 is 10-15cm, and the sewage collection pipe 1 is made of PVC, or is made of brick and cement.
包括顺次连接的厌氧消化系统3、好氧消化池4、生态净化系统和清水收集池10。It includes an anaerobic digestion system 3 , an aerobic digestion tank 4 , an ecological purification system and a clear water collection tank 10 connected in sequence.
若干污水汇集管道1均为较高的一端与居民用水排水口连接,较低的一端与厌氧消化系统3连接,每根污水汇集管道1临近厌氧消化系统3之处均设置有隔栅井2,隔栅井2的内部设置有第一滤网,隔栅井2上设置有可开启井盖。A number of sewage collection pipes 1 are connected to the residential water outlet at the higher end, and connected to the anaerobic digestion system 3 at the lower end, and each sewage collection pipe 1 is provided with a grid well near the anaerobic digestion system 3 2. The inside of the grid well 2 is provided with a first filter screen, and the grid well 2 is provided with an openable well cover.
每根污水汇集管道1与厌氧消化系统3之间均设置有单向阀联通,使得污水只能从管道流向厌氧消化系统3,而不会从厌氧消化系统3溢至管道,厌氧消化系统3内产生的臭气也不会顺管道进入室内或是飘到户外空气中,保证了环境不受污染。A one-way valve is provided between each sewage collecting pipeline 1 and the anaerobic digestion system 3, so that the sewage can only flow from the pipeline to the anaerobic digestion system 3, and will not overflow from the anaerobic digestion system 3 to the pipeline. The odor produced in the digestive system 3 will not enter the room along the pipeline or float into the outdoor air, thus ensuring that the environment is not polluted.
参见图2所示,厌氧消化系统3包括顺次连接的一级厌氧消化池16、二级厌氧消化池20和三级厌氧消化池21,每根污水汇集管道1在厌氧消化池外部汇集,之后均伸入一级厌氧消化池16的内部,污水汇集管道1包括进水端和出水端,进水端高于出水端,进水端与居民排污口连接,出水端位于一级厌氧消化池16内,出水端与一级厌氧消化池16的内底之间的距离为80~100cm。Referring to Fig. 2, the anaerobic digestion system 3 includes a first-stage anaerobic digester 16, a second-stage anaerobic digester 20, and a third-stage anaerobic digester 21 connected in sequence, and each sewage collection pipe 1 undergoes anaerobic digestion The outside of the pool is collected, and then all extend into the inside of the primary anaerobic digester 16. The sewage collection pipeline 1 includes a water inlet and an outlet. The inlet is higher than the outlet. The inlet is connected to the sewage outlet of the residents. In the primary anaerobic digester 16, the distance between the water outlet and the inner bottom of the primary anaerobic digester 16 is 80-100 cm.
一级厌氧消化池16和二级厌氧消化池20通过第一连通管17连接,第一连通管17包括进水端和出水端,进水端高于出水端,进水端位于一级厌氧消化池16的内部,与一级厌氧消化池16内顶之间的距离为15~30cm;出水端位于二级厌氧消化池20的内部,与二级厌氧消化池20内底之间的距离为30~50cm。The primary anaerobic digester 16 and the secondary anaerobic digester 20 are connected by a first connecting pipe 17, the first connecting pipe 17 includes a water inlet and an outlet, the inlet is higher than the outlet, and the inlet is located at the first level The inside of the anaerobic digester 16 is 15 to 30 cm away from the top of the primary anaerobic digester 16; The distance between them is 30-50cm.
二级厌氧消化池20和三级厌氧消化池21通过第二连通管18连接,第二连通管18包括进水端和出水端,进水端高于出水端,进水端位于二级厌氧消化池20的内部,与二级厌氧消化池20内顶之间的距离为15~30cm;出水端位于三级厌氧消化池21的内部,与三级厌氧消化池21内底间的距离为30~50cm。The secondary anaerobic digester 20 and the tertiary anaerobic digester 21 are connected by a second connecting pipe 18, the second connecting pipe 18 includes a water inlet and an outlet, the inlet is higher than the outlet, and the inlet is located at the second The inside of the anaerobic digester 20 is 15 to 30 cm away from the top of the secondary anaerobic digester 20; The distance between them is 30-50cm.
一级厌氧消化池16的底部倾斜布置,与水平面呈30°~45°的夹角,一级厌氧消化池16的内部设置有厌氧微生物填料层15,厌氧微生物填料层15与水平面之间的夹角为0°~15°,厌氧微生物填料层15的横截面面积与一级厌氧消化池16的横截面积相等,厌氧微生物填料层15的底部设置有托网19。厌氧微生物填料层15的顶部与一级厌氧消化池16顶部之间的距离为80~100cm,一级厌氧消化池16的内顶设置有反冲洗装置14,一级厌氧消化池16的顶部设置有沼气导出管和沼气发电装置,导出管导入沼气发电装置的内部。The bottom of the primary anaerobic digester 16 is arranged obliquely, forming an angle of 30° to 45° with the horizontal plane. The interior of the primary anaerobic digester 16 is provided with an anaerobic microbial packing layer 15, and the anaerobic microbial packing layer 15 is in contact with the horizontal plane. The angle between them is 0°~15°, the cross-sectional area of the anaerobic microbial packing layer 15 is equal to the cross-sectional area of the primary anaerobic digester 16, and the bottom of the anaerobic microbial packing layer 15 is provided with a support net 19. The distance between the top of the anaerobic microbial packing layer 15 and the top of the primary anaerobic digester 16 is 80-100 cm, and the inner top of the primary anaerobic digester 16 is provided with a backwashing device 14, and the primary anaerobic digester 16 The top of the tank is provided with a biogas outlet pipe and a biogas power generation device, and the outlet pipe leads into the interior of the biogas power generation device.
污水沿污水汇集管道1进入一级厌氧消化池16的下方后,污水中密度较大的杂质直接沉淀在一级厌氧消化池16的底部、形成淤泥,水和密度较小的杂质在一级厌氧消化池16中向上浮动。After the sewage enters the bottom of the first-stage anaerobic digester 16 along the sewage collection pipe 1, the impurities with higher density in the sewage directly settle at the bottom of the first-stage anaerobic digester 16 to form silt, and the water and the less dense impurities are mixed together. Floating upward in the first-stage anaerobic digester 16.
淤泥通过排泥沟排出,一级厌氧消化池16底部沉降的污泥经过长期厌氧消化作用后,污泥富含有机质主要是氮、磷、钾等元素、腐殖酸、微量营养元素、多种氨基酸、酶类和有益微生物,质地疏松、保墒性能好、酸碱度适中,不仅能够改良土壤,还能满足作物生长的需要,也非常适合泥鳅、蚯蚓、鳝鱼的生长。因此,清出的污泥直接作为基质养泥鳅、蚯蚓、鳝鱼或作为肥料用于农作物种植。不仅可以改善生态环境,发展农业生产,还能提高经济效益。The sludge is discharged through the sludge discharge ditch, and the sludge settled at the bottom of the primary anaerobic digester 16 undergoes long-term anaerobic digestion, and the sludge is rich in organic matter, mainly nitrogen, phosphorus, potassium and other elements, humic acid, trace nutrients, A variety of amino acids, enzymes and beneficial microorganisms, loose texture, good moisture retention performance, moderate pH, can not only improve the soil, but also meet the needs of crop growth, and is also very suitable for the growth of loaches, earthworms and eels. Therefore, the cleared sludge is directly used as a substrate to raise loach, earthworms, eels or as a fertilizer for crop planting. It can not only improve the ecological environment, develop agricultural production, but also improve economic benefits.
由于厌氧微生物填料层15与一级厌氧消化池16底部之间的距离较大,水和密度较小的杂质向上浮动的过程中,部分杂质会发生聚集、进而沉降至一级厌氧消化池16的底部,其余杂质再通过托网19过滤,将体积较大的杂质滤除,得到水、微生物和与水混溶的物质后,通过厌氧微生物填料层15,厌氧微生物填料层15能够分解水中的有机物,降低水中有机物含量,得到初步净化水和甲烷气体,甲烷能够沿导出管导出,被净化后用作燃料。Due to the large distance between the anaerobic microbial packing layer 15 and the bottom of the first-stage anaerobic digestion tank 16, some impurities will gather and then settle down to the first-stage anaerobic digestion tank during the upward floating process of water and less dense impurities. At the bottom of the pool 16, the remaining impurities are filtered through the support net 19, and the larger impurities are filtered out, and after water, microorganisms and water-miscible substances are obtained, they pass through the anaerobic microbial packing layer 15, and the anaerobic microbial packing layer 15 It can decompose organic matter in water, reduce the content of organic matter in water, and obtain preliminary purified water and methane gas. Methane can be exported along the outlet pipe and used as fuel after being purified.
一级厌氧消化池16与二级厌氧消化池20、三级厌氧消化池21、好氧消化池4的体积比为3~5:1:1:1~2,且地势依次降低。污水汇集管道1、第一连通管17、第二连通管18和第三连通管11的进水端依次降低。The volume ratio of the first-stage anaerobic digester 16 to the second-stage anaerobic digester 20 , the third-stage anaerobic digester 21 , and the aerobic digester 4 is 3-5:1:1:1-2, and the topography decreases successively. The water inlet ends of the sewage collection pipe 1 , the first communication pipe 17 , the second communication pipe 18 and the third communication pipe 11 are lowered sequentially.
污水经过一级厌氧消化池16净化4~6天后,沿第一连通管17进入二级厌氧消化池20,在二级厌氧消化池20内消化2~4天后沿第二连通管18进入三级厌氧消化池21,在三级厌氧消化池21内消化2~4天后自动进入好氧消化池4,污水在好氧消化池4中停留时间为2~4天。After the sewage is purified by the primary anaerobic digester 16 for 4 to 6 days, it enters the secondary anaerobic digester 20 along the first connecting pipe 17, and is digested in the secondary anaerobic digester 20 for 2 to 4 days, then passes through the second connecting pipe 18 Enter the three-stage anaerobic digester 21, and automatically enter the aerobic digester 4 after being digested in the three-stage anaerobic digester 21 for 2 to 4 days. The residence time of the sewage in the aerobic digester 4 is 2 to 4 days.
由于一级厌氧消化池16、二级厌氧消化池20和三级厌氧消化池21均处于密闭状态,氧气含量较低,使得污水中的有害菌群难以生存,进而降低污水中的有害菌的含量。Since the primary anaerobic digester 16, the secondary anaerobic digester 20 and the tertiary anaerobic digester 21 are all in an airtight state, the oxygen content is low, making it difficult for the harmful bacteria in the sewage to survive, thereby reducing the harmful bacteria in the sewage. bacteria content.
三级厌氧消化池21通过第三连通管11与好氧消化池4连接,第三连通管11包括进水端和出水端,进水端高于出水端,进水端与三级厌氧消化池21的内顶之间的距离为15~30cm,出水端与好氧消化池4的内底之间的距离为30~50cm。The three-stage anaerobic digester 21 is connected to the aerobic digester 4 through the third connecting pipe 11, the third connecting pipe 11 includes a water inlet and an outlet, the water inlet is higher than the outlet, and the water inlet is connected to the third-stage anaerobic digester. The distance between the inner tops of the digester 21 is 15-30 cm, and the distance between the water outlet and the inner bottom of the aerobic digester 4 is 30-50 cm.
好氧消化池4的外部设置有太阳能发电装置6,好氧消化池4的内部设置有曝气装置7和好氧净化装置,曝气装置7位于好氧净化装置的上方,曝气装置7与太阳能发电装置6电连接,曝气装置7与沼气发电装置电连接,好氧净化装置包括自上而下依次设置与好氧微生物填料层5、秸秆碳层、砾石层13和第二滤网12,好氧微生物填料层5的表面积与好氧消化池4的横截面面积相等。The outside of the aerobic digester 4 is provided with a solar power generation device 6, and the inside of the aerobic digester 4 is provided with an aeration device 7 and an aerobic purification device. The aeration device 7 is located above the aerobic purification device. The solar power generation device 6 is electrically connected, the aeration device 7 is electrically connected to the biogas power generation device, and the aerobic purification device includes an aerobic microbial filler layer 5, a straw carbon layer, a gravel layer 13 and a second filter screen 12 arranged in sequence from top to bottom. , the surface area of the aerobic microbial filler layer 5 is equal to the cross-sectional area of the aerobic digester 4 .
秸秆碳层、砾石层13和第二滤网12能够将污染成分进一步分解和转化,水质得到进一步净化,水体透明度得到提升。The straw carbon layer, the gravel layer 13 and the second filter screen 12 can further decompose and transform the pollution components, further purify the water quality, and improve the transparency of the water body.
一级厌氧消化池16、二级厌氧消化池20、三级厌氧消化池21和好氧消化池4的容积均根据以下公式进行计算:The volumes of the primary anaerobic digester 16, the secondary anaerobic digester 20, the tertiary anaerobic digester 21 and the aerobic digester 4 are calculated according to the following formula:
V=aNqt/24*1000V=aNqt/24*1000
该公式中:V——容积,单位为m3;In this formula: V——volume, the unit is m 3 ;
N——服务的人口数量;N - the number of people served;
a——污水的产生系数;a——The production coefficient of sewage;
q——人均用水量,升/天(L/d);q——per capita water consumption, liter/day (L/d);
t——水在该消化池中停留的时间,天(d);t—the time that water stays in the digester, in days (d);
24*1000——转换系数。24*1000——conversion factor.
我国现有条件下,q为80~120L/d,a为0.7~0.9。Under the existing conditions in our country, q is 80-120L/d, and a is 0.7-0.9.
水在一级厌氧消化池16中停留的时间为4~7天、水在二级厌氧消化池20中停留的时间为2~4天、水在三级厌氧消化池21中停留的时间为2~4天、水在好氧消化池4中停留的时间为2~4天。The time that water stays in the primary anaerobic digester 16 is 4 to 7 days, the time that water stays in the secondary anaerobic digester 20 is 2 to 4 days, and the time that water stays in the third-stage anaerobic digester 21 The time is 2 to 4 days, and the time for the water to stay in the aerobic digester 4 is 2 to 4 days.
集约型装置中消化池容积的计算方法,消化池括相互连接的厌氧消化系统3和好氧消化池4,厌氧消化系统3包括顺次连接的一级厌氧消化池16、二级厌氧消化池20和三级厌氧消化池21。The calculation method for the volume of the digester in the intensive device, the digester includes the interconnected anaerobic digestion system 3 and the aerobic digester 4, the anaerobic digestion system 3 includes the first-stage anaerobic digester 16, the second-stage anaerobic digester Oxygen digester 20 and tertiary anaerobic digester 21.
一级厌氧消化池16中污水停留的时间t为4~7天、二级厌氧消化池20中污水停留的时间t为2~4天、三级厌氧消化池21中污水停留的时间t为2~4天、好氧消化池4中污水停留的时间t为2~4天。The residence time t of sewage in the primary anaerobic digester 16 is 4 to 7 days, the residence time t of sewage in the secondary anaerobic digester 20 is 2 to 4 days, and the residence time of sewage in the third stage anaerobic digester 21 t is 2-4 days, and the residence time t of the sewage in the aerobic digester 4 is 2-4 days.
生态净化系统包括若干引流单元8和若干种植管9,每个引流单元8上均设置有若干引流管,每个引流管均与一个种植管9对应,每个引流管均为一端与好氧消化池4连接,另一端通过对应的种植管9与清水收集池连接,种植管9为迂回弯折的管道,种植管9上开有若干种植孔,种植孔内种植有水培植物。The ecological purification system includes several drainage units 8 and several planting tubes 9, each drainage unit 8 is provided with several drainage tubes, each drainage tube corresponds to a planting tube 9, and each drainage tube has one end connected to the aerobic digestion tube. The pool 4 is connected, and the other end is connected with the clear water collection pool through the corresponding planting tube 9. The planting tube 9 is a circuitous and bent pipeline. There are several planting holes on the planting tube 9, and hydroponic plants are planted in the planting holes.
每个种植管9临近引流管10m内的种植孔内的水培植物为吊兰、紫茉莉、紫花玉簪和鸭跖草中的至少一种,每个种植管9与引流管距离大于10m的种植孔内的水培植物为水芹、生菜、油菜、小白菜、菊苣、油麦菜、番茄和黄瓜中的至少一种。The hydroponic plant in the planting hole within 10m of each planting tube 9 is adjacent to the drainage tube is at least one of Chlorophytum, Mirabilis, Violet Hosta and Commelina, and each planting tube 9 is more than 10m away from the planting hole of the drainage tube. The hydroponic plants in it are at least one of cress, lettuce, rape, Chinese cabbage, endive, lettuce, tomato and cucumber.
吊兰、紫茉莉、紫花玉簪和鸭跖草的细胞膜上含有大量金属离子转运蛋白:CDF家族蛋白、NRAMP家族蛋白和ZIP家族蛋白,在金属离子转运蛋白的作用下,植株对金属离子有较强的吸收、运输能力,植株吸收的金属离子主要富集在液泡、细胞壁和叶片表皮细胞的表皮毛上,部分以螯合体形式存在,金属离子不会进入植物细胞的内部,不会损坏植物。The cell membranes of spider plant, mirabilis, hosta and commelina contain a large number of metal ion transport proteins: CDF family proteins, NRAMP family proteins and ZIP family proteins. Under the action of metal ion transport proteins, the plants have a strong resistance to metal ions. Absorption and transportation capacity, the metal ions absorbed by plants are mainly concentrated in the vacuoles, cell walls and epidermis of leaf epidermis cells, and some of them exist in the form of chelates. Metal ions will not enter the interior of plant cells and will not damage plants.
吊兰、紫茉莉、紫花玉簪和鸭跖草不仅能够美化环境,而且能够增加经济效益。Chlorophytum, mirabilis, hosta and commelina can not only beautify the environment, but also increase economic benefits.
水芹、生菜、油菜、小白菜、菊苣、油麦菜、番茄和黄瓜的生长周期较短,生物量大,产量高,显著提高了空间利用率,增加了农业产出,促进了农业发展。Cress, lettuce, rape, Chinese cabbage, chicory, lettuce, tomato and cucumber have a short growth cycle, large biomass, and high yield, which significantly improves space utilization, increases agricultural output, and promotes agricultural development.
一种集约型装置的建造方法,包括以下步骤:A method for constructing an intensive device, comprising the steps of:
A、确定建造地的人口数量N、污水的产生系数a和人均用水量q,根据容积计算公式V=aNqt/(24*1000),计算一级厌氧消化池16、二级厌氧消化池20、三级厌氧消化池21和好氧消化池4的容积,所述t为水在对应消化池中停留的时间,水在一级厌氧消化池16中停留的时间为4~7天、水在二级厌氧消化池20中停留的时间为2~4天、水在三级厌氧消化池21中停留的时间为2~4天、水在好氧消化池4中停留的时间为2~4天,转入步骤B。A. Determine the population N of the construction site, the sewage production coefficient a and the per capita water consumption q, and calculate the primary anaerobic digester 16 and the secondary anaerobic digester according to the volume calculation formula V=aNqt/(24*1000) 20. The volume of the third-stage anaerobic digester 21 and the aerobic digester 4, the t is the time that the water stays in the corresponding digester, and the time that the water stays in the first-stage anaerobic digester 16 is 4 to 7 days 1. The time for water to stay in the secondary anaerobic digester 20 is 2 to 4 days, the time for water to stay in the third-stage anaerobic digester 21 is 2 to 4 days, and the time for water to stay in the aerobic digester 4 For 2 to 4 days, turn to step B.
B:选择平地作为建设地点,在建设地点上挖建顺次排列的一级厌氧消化池16、二级厌氧消化池20、三级厌氧消化池21和好氧消化池4,在一级厌氧消化池16、二级厌氧消化池20、三级厌氧消化池21和好氧消化池4的内壁涂覆防水材料并干燥后,注入清水,放置3天,判定无渗水发生,转入步骤C。B: Choose flat land as the construction site, dig and build the first-level anaerobic digester 16, the second-level anaerobic digester 20, the third-level anaerobic digester 21 and the aerobic digester 4 arranged in sequence on the construction site. After the inner walls of the first-level anaerobic digestion tank 16, the second-level anaerobic digestion tank 20, the third-level anaerobic digestion tank 21, and the aerobic digestion tank 4 are coated with waterproof materials and dried, they are injected with clean water and left for 3 days. It is determined that no water seepage occurs. Go to step C.
C:安装隔栅井2和若干污水汇集管道1,将若干污水汇集管道1的一端与居民用水排水口连接,另一端与一级厌氧消化池16连接,在一级厌氧消化池16和二级厌氧消化池20之间安装第一连通管17连接,在二级厌氧消化池20和三级厌氧消化池21之间安装第二连通管18,在三级厌氧消化池21和好氧消化池4之间安装第三连通管11,转入步骤D。C: Install grid wells 2 and several sewage collection pipes 1, connect one end of several sewage collection pipes 1 to the residential water outlet, and connect the other end to the primary anaerobic digester 16, and connect the primary anaerobic digester 16 and The first connecting pipe 17 is installed between the secondary anaerobic digesters 20 to connect, the second connecting pipe 18 is installed between the secondary anaerobic digesters 20 and the three-stage anaerobic digesters 21, and the third-stage anaerobic digesters 21 Install the third communication pipe 11 between the aerobic digester 4 and turn to step D.
D:在一级厌氧消化池16的外部安装沼气发电装置,在一级厌氧消化池16的内顶安装反冲洗装置14,在一级厌氧消化池16的内部安装托网19和厌氧微生物填料层15;在好氧消化池4的的顶部安装太阳能发电装置6,在好氧消化池4的内部安装曝气装置7和好氧净化装置,将太阳能发电装置6与曝气装置7电连接,将曝气装置7与沼气发电装置电连接,转入步骤E;D: Install a biogas power generation device outside the primary anaerobic digester 16, install a backwash device 14 on the top of the primary anaerobic digester 16, and install a support net 19 and an anaerobic digester 16 inside the primary anaerobic digester 16. Aerobic microbial filler layer 15; Solar power generation device 6 is installed on the top of aerobic digester 4, aeration device 7 and aerobic purification device are installed in the inside of aerobic digestion tank 4, solar power generation device 6 and aeration device 7 Electric connection, the aeration device 7 is electrically connected with the biogas power generation device, and proceeds to step E;
E:将好氧消化池4的外部安装若干引流单元8和若干种植管9,在种植管9上播种具有净化作用的植物,调试所述集约型装置至正常运行并投入使用。E: Install several drainage units 8 and several planting pipes 9 outside the aerobic digester 4, sow plants with purification effect on the planting pipes 9, adjust the intensive device to normal operation and put it into use.
采用本发明中用于处理农村生活污水的集约型装置处理后的污水,能够达到《污水综合排放标准》GB 8978-2006的一级级标准。The sewage treated by the intensive device for treating rural domestic sewage in the present invention can reach the first-level standard of the "Comprehensive Wastewater Discharge Standard" GB 8978-2006.
下面,通过1个实施例对本发明进行详细说明Below, the present invention is described in detail by an embodiment
实施例1Example 1
以湖北某小型村庄作为试验点,该村庄常驻人口为100人,一级厌氧消化池16的尺寸为400cm*350cm*400cm,二级厌氧消化池20的尺寸为250cm*250cm*260cm、三级厌氧消化池21的尺寸为300cm*300cm*180cm,好氧消化池4的尺寸为400cm*300cm*100cm。Taking a small village in Hubei as a test site, the village has a permanent population of 100 people, the size of the primary anaerobic digester 16 is 400cm*350cm*400cm, the size of the secondary anaerobic digester 20 is 250cm*250cm*260cm, The size of the three-stage anaerobic digester 21 is 300cm*300cm*180cm, and the size of the aerobic digester 4 is 400cm*300cm*100cm.
污水汇集管道1采用直径为15cm的PVC管,污水汇集管道1直接接通各住户生活污水排水口,隔栅井2呈矩形,其尺寸为50cm*80cm*30cm,隔栅井2的内部设置有过滤网12,第一滤网采用孔径为1.5cm*1.5cm的不锈钢丝网;一级厌氧消化池16、二级厌氧消化池20、三级厌氧消化池21和好氧消化池4均采用砖块和水泥砌成,其中,第一连通管17道、第二连通管18道和第三连通管11道均选用直径15cm的PVC管道。The sewage collection pipe 1 adopts a PVC pipe with a diameter of 15cm. The sewage collection pipe 1 is directly connected to the domestic sewage outlet of each household. The grid well 2 is rectangular and its size is 50cm*80cm*30cm. Filter screen 12, the first filter screen adopts stainless steel wire mesh with a pore size of 1.5cm*1.5cm; primary anaerobic digester 16, secondary anaerobic digester 20, tertiary anaerobic digester 21 and aerobic digester 4 They are all made of bricks and cement, and the first 17 connecting pipes, the second 18 connecting pipes and the third connecting pipe 11 are all made of PVC pipes with a diameter of 15cm.
本实施例中的引流单元8数量为10个,种植管9的数量为80个,每个引流单元8上设置有8个引流管,水培植物选用水仙花、生菜和大蒜,自水培系统流出的清水直接用作养鱼和农田灌溉。The number of drainage units 8 in the present embodiment is 10, the number of planting tubes 9 is 80, and each drainage unit 8 is provided with 8 drainage tubes. The hydroponic plants are selected from daffodils, lettuce and garlic, from the hydroponic system. The clear water flowing out is directly used for fish farming and farmland irrigation.
该污水处理系统建造工艺简单,净化效果好,COD(Chemical Oxygen Demand,化学需氧量)、TN(total nitrogen,总氮)、TP(total phosphorus),总磷的去除率均达到80%以上,运行一个月后检测出水水质检测结果见表1。The construction process of the sewage treatment system is simple, and the purification effect is good. The removal rates of COD (Chemical Oxygen Demand, chemical oxygen demand), TN (total nitrogen, total nitrogen), TP (total phosphorus), and total phosphorus are all above 80%. See Table 1 for the results of water quality testing after one month of operation.
由此可知,本发明中用于处理农村生活污水的集约型装置,能够较好的净化农村生活污水。It can be seen from this that the intensive device for treating rural domestic sewage in the present invention can better purify rural domestic sewage.
表1 集约化生活污水处理工程检测数据Table 1 Test data of intensive domestic sewage treatment project
本发明不局限于上述实施方式,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰也视为本发明的保护范围之内。本说明书中未作详细描述的内容属于本领域专业技术人员公知的现有技术。The present invention is not limited to the above-mentioned embodiments. For those of ordinary skill in the art, without departing from the principle of the present invention, some improvements and modifications can also be made, and these improvements and modifications are also considered protection of the present invention. within range. The content not described in detail in this specification belongs to the prior art known to those skilled in the art.
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