CN203212433U - 农村污水处理系统 - Google Patents
农村污水处理系统 Download PDFInfo
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- CN203212433U CN203212433U CN 201320161192 CN201320161192U CN203212433U CN 203212433 U CN203212433 U CN 203212433U CN 201320161192 CN201320161192 CN 201320161192 CN 201320161192 U CN201320161192 U CN 201320161192U CN 203212433 U CN203212433 U CN 203212433U
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- sewage treatment
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- 239000010865 sewage Substances 0.000 title claims abstract description 53
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
本实用新型提供一种农村污水处理系统，其特征在于：包括通过管道顺序连接的集水池、沉淀池、A/O池、二沉池和人工湿地；集水池上设置栅网，污水通过污水管网流经栅网过滤后进入集水池池；集水池的出水自流到沉淀池；沉淀池的出水用提升泵泵入A/O池；A/O池由顺序连接的缺氧段和好氧段组成；好氧段的出水自流到二沉池，二沉池的出水自流入人工湿地中，二沉池的剩余污泥回流到A/O池的缺氧段。本实用新型具有成本低、投资省、动力消耗少、耐冲击负荷力强、操作简单、管理方便、处理效果好的优点，并具有绿色生态效益，增加周边空气含氧量和湿地，截留空气中的微型颗粒物，适合中国的新农村水污染控制项目。
Description
农村污水处理系统
技术领域
[0001] 本实用新型涉及水资源与环境技术领域，特别是涉及一种农村污水处理系统。
背景技术
[0002] A/0工艺是七十年代发展起来的水处理工艺，具有较长的历史，在污水处理方面应用较为广泛。A/0工艺通过鼓风机进行充氧曝气，在A/0池内，利用填料上附着的微生物膜吸收分解污水中的有机污染物质，达到降解COD和BOD等的目的。A/0池出水自流进入沉淀池，脱落的生物膜等在其中进行沉淀，澄清水经过加药系统投加絮凝剂后进入中间水箱，经消毒后即可排放。如需回用，另需加后续深度过滤处理。该工艺具有以下特点:(1)由于填料比表面积大，池内充氧条件良好，池内单位容积的生物固体量较高，因此，A/0池具有较高的容积负荷；(2)不存在污泥膨胀问题；(3) —次性投资少。该工艺的缺点是(I)出水水质不稳定，抗冲击负荷较差；(2)流程复杂，自动化程度较低，依赖于管理人员的经验，管理不方便；(3)布水、曝气不易均匀，容易出现死区；(4)占地面积大。
[0003] 针对于农村地区经济技术条件相对落后，农村污水处理系统可以建于不同的地方，以充分发挥自己的优势。而生态处理系统，如“人工湿地”技术，能在污染源头直接应用该技术对污水进行处理，污水在水生植物、介质、微生物的综合作用下得到了净化。生态处理系统有其固有的优势，如低费用、低能耗、运行管理维护简单，经济有效、易操作运行，因此，考虑将A/0工艺与生态处理系统有效地结合起来的农村污水处理系统，即组合型生物综合处理法可以实现技术、经济、环境效益的统一。
发明内容
[0004] 本实用新型的目的是针对农村污水的进水特点，将A/0工艺与生态处理系统有效地结合起来，通过将栅网集水池与预处理、A/0缺氧好氧池、生态高效型潜流湿地处理系统相结合，提供一种能够截留大粒径生产生活杂物、处理效率高、出水效果好、水质稳定、实际操作简便、运行成本低、维护简单、能耗低的农村污水处理系统，从而获得技术、经济、环境
效益三丰收。
[0005] 本实用新型的技术方案是:
[0006] 农村污水处理系统，其特征在于:包括通过管道顺序连接的集水池、沉淀池、A/0池、二沉池和人工湿地；所述集水池上设置栅网，所述污水通过污水管网流经所述栅网过滤后进入集水池池；所述集水池的出水自流到所述沉淀池；所述沉淀池的出水用提升泵泵入A/0池；A/0池由顺序连接的缺氧段和好氧段组成；所述好氧段的出水自流到二沉池，所述二沉池的出水自流入所述人工湿地中，所述二沉池的剩余污泥回流到所述A/0池的缺氧段。
[0007] 进一步地，
[0008] 所述栅网采用间隙为5mm的不锈钢材质焊制。
[0009] 所述集水池的池顶设置可滑动的盖。[0010] 所述集水池与所述沉淀池共用一面墙。
[0011] 所述A/0池与所述二沉池共用一面墙，所述二沉池与所述人工湿地有高度差。
[0012] 所述人工湿地是潜流型人工湿地；所述人工湿地的挡墙底部及四壁均设有防渗层；所述人工湿地自上而下由水生植物层、布水层、介质层和集水层组成；布水管均匀布设在所述介质层中；所述二沉池的出水管通过管道与所述布水管连通；所述布水管上均匀分布通孔，污水通过布水管上的所述通孔进入所述介质层。
[0013] 所述布水管为UPVC管。
[0014] 所述防渗层为复合土工膜防渗层。
[0015] 本实用新型的农村污水处理系统的优点在于:
[0016] (I)综合建设成本低、动力消耗少、运行费用低、投资省；
[0017] (2)工艺耐冲击负荷力强，系统安全、运行稳定，操作简单，管理方便，且使用寿命长;
[0018] (3)运行中无需添加化学药剂，运行稳定，处理效果好，并具有绿色生态效益、能够美化周边环境、调节周边区域气候、改善局部空气质量环境的优点，具有广阔的市场前景。
附图说明
[0019] 图1为本实用新型的农村污水处理系统的结构示意图。
[0020] 图2为本实用新型的农村污水处理系统的平面布置示意图。
[0021] 附图标记说明
[0022] I栅网，2集水池，3沉淀池，4A/0池，5污泥池，6 二沉池，7进水阀门井，8人工湿地，9出水调节井。
具体实施方式
[0023] 下面结合附图对本实用新型作进一步详细说明。
[0024] 如图1-2所示的本实用新型的农村污水处理系统，包括通过管道顺序连接的集水池2、沉淀池3、A/0池4、二沉池6和人工湿地8 ;集水池上设置栅网1，污水通过污水管网流经栅网过滤后进入集水池；集水池的出水自流到沉淀池；沉淀池的出水用提升泵(图中未显示)泵入A/0池；A/0池由顺序连接的缺氧段和好氧段组成；好氧段的出水自流到二沉池，二沉池的出水自流入人工湿地处理系统中，二沉池的剩余污泥回流到A/0池的缺氧段。
[0025] 本例中，二沉池通过管道与进水阀门井7相连通，并进一步连通人工湿地，人工湿地通过管道与出水调节井9相连通。
[0026] 本例中，栅网采用间隙为5mm的不锈钢材质焊制。
[0027] 本例中，集水池的池顶设置可滑动的盖。
[0028] 本例中，A/0池的好氧段通过沉水曝气机(图中未显示)实现供氧。
[0029] 本例中，集水池与沉淀池共用一面墙。
[0030] 本例中，A/0池与二沉池共用一面墙，二沉池与人工湿地有高度差，因此能够实现二沉池的出水自流入人工湿地中
[0031] 本例中，栅网I与集水池2是一体的，污水通过进水口进入，经细栅网拦截污水中粒径大于5_的较大的污染物质后再通过出水口流出，通过管道进入集水池2。[0032] 本例中，污水在集水池2内通过一定的停留时间，均化水质水量，该集水池的主要功能相当于一个化粪池，针对农村污水的特点，农村污水中携带大量的垃圾和杂质以及污泥，经过集水池进行预沉淀，预沉污水中的泥沙、大粒径的悬浮物，这个集水池，同时具有水解酸化功能，能够将污水中的固体、大分子和不易生物降解的有机物降解为易于生物降解的小分子有机物，提高污水的生化性。污水在集水池内停留8到12个小时左右，上清液自流进入沉淀池3，沉淀池进一步分离污水中的固体、大分子的污染物，去除污水中大部分悬浮物和部分有机物，将高峰期和低峰期的水质水量进行初步沉淀。沉淀池3中的污水通过提升泵经管道被泵入A/0池4。
[0033] A/0池由顺序连接的缺氧段和好氧段组成；缺氧段主要利用水解和产酸微生物，将污水中的固体、大分子和不易生物降解的有机物降解为易于生物降解的小分子有机物，使得污水在后续的好氧单元以较少的能耗和较短的停留时间下得到处理。好氧段中具有较大的表面积的生物膜，能够大量吸附废水中的有机物，而且具有很强的氧化能力，将有机污染物分解为C02、H2O等无害物质，使污水得到净化。在有机物被分解的同时，微生物的机体则在不断增长和繁殖，也就是增加了生物膜的数量。由于生物膜上微生物的老化死亡，生物膜将会从滤料表面脱落下来，然后随着废水流出池外。由于生物膜的吸附作用，在它的表面往往附着一层薄薄的水层，水中的有机物被生物膜所氧化，其浓度要比滤池进水中有机物的浓度低得多，因此当废水在滤料表面流动时，有机物就会从运动着的废水中转移到附着在生物膜表面的水中去，并进一步被生物膜所吸附。同时，空气中的氧也将经过废水而进入生物膜。生物膜上的微生物在氧的参与、作用下对有机物进行分解和机体新陈代谢，产生了包括二氧化碳等无机物，它们又沿着相反的方向，即从生物膜经过附着水排到流动着的废水及空气中去；在这些过程的综合作用下，废水中有机物的含量大大减少，因此得到了净化。
[0034] 好氧段的出水自流到二沉池，二沉池主要为满足好氧段随水流出的脱落微生物(膜)、游离菌胶团、有机杂质等的泥水沉降分离，二沉池的出水自流入人工湿地，二沉池的剩余污泥回流到A/0池的缺氧段。
[0035] 本例中，A/0池内的水力停留时间:硝化不小于5〜6h ;反硝化不大于2h ;缺氧段:好氧段=1:3 ;污泥回流比:50〜100% ;混合液回流比:300〜400% ;反硝化段碳/氮比:B0D5/TNM，理论BOD消耗量为1.72gB0D/gN0x—N ;硝化段的TKN/MLSS负荷率(单位活性污泥浓度单位时间内所能硝化的凯氏氮):<0.05KgTKN/KgMLSS • d，缺氧段D0〈0.2〜0.5mg/L,好氧段D0>2〜4mg/L。
[0036] 本例中，A/0池与与人工湿地8有高度差，有利于水的自流，节省能源。
[0037] 人工湿地利用水生植物根脉净化系统、生物滤料以及栖息在介质中的微生物，通过物理、化学、生物和植物的相互协同作用来去除污水中的污染物的，最后出水达到排放标准排入附近水体或回用与绿化灌溉等。
[0038] 本例中，人工湿地是潜流型人工湿地；该潜流型人工湿地的挡墙底部及四壁均设有防渗层(图中未显示)；人工湿地自上而下由水生植物层、布水层、介质层和集水层组成；布水管均匀布设在介质层中；二沉池的出水管通过管道与布水管连通；布水管上均匀分布通孔，污水通过布水管上的通孔进入介质层。布水管可以为UPVC管。
[0039] 本实用新型的介质层内的介质由火山岩生物陶粒滤料、钙石和水洗砂按一定比例组成。本例中，陶粒滤料、钙石和水洗砂的重量配比比例为2:6:2。
[0040] 本例中，陶粒滤料的粒径范围为16〜25mm，钙石的粒径范围20〜37mm，水洗砂的粒径范围2〜4mm。
[0041] 本例中，防渗层为复合土工膜防渗层。
[0042] 本例中，污水通过布水管进入介质层，在介质层停留一定的时间，通过介质层的过滤，下渗至集水层的集水石笼收集，水生植物吸收污水中的N、P作为自身的营养物质从而达到去除污染物的目的，并且通过根茎向介质层中输送氧气。
[0043] 本例中，出水调节井9通过管道与人工湿地相连接，人工湿地的水位高差的调节通过设置与该出水调节井内的调节装置(图中未显示)来实现。
[0044] 上述仅对本实用新型中的几种具体实施例加以说明，但并不能作为本实用新型的保护范围，凡是依据本实用新型中的设计精神所作出的等效变化或修饰，均应认为落入本实用新型的保护范围。
Claims (6)
1.农村污水处理系统，其特征在于:包括通过管道顺序连接的集水池、沉淀池、A/0池、二沉池和人工湿地；所述集水池上设置栅网，所述污水通过污水管网流经所述栅网过滤后进入集水池池；所述集水池的出水自流到所述沉淀池；所述沉淀池的出水用提升泵泵入A/O池；A/0池由顺序连接的缺氧段和好氧段组成；所述好氧段的出水自流到二沉池，所述二沉池的出水自流入所述人工湿地中，所述二沉池的剩余污泥回流到所述A/0池的缺氧段。
2.根据权利要求1所述的农村污水处理系统，其特征在于:所述栅网采用间隙为5_的不锈钢材质焊制。
3.根据权利要求2所述的农村污水处理系统，其特征在于:所述集水池的池顶设置可滑动的盖。
4.根据权利要求1所述的农村污水处理系统，其特征在于:所述人工湿地是潜流型人工湿地；所述人工湿地的挡墙底部及四壁均设有防渗层；所述人工湿地自上而下由水生植物层、布水层、介质层和集水层组成；布水管均匀布设在所述介质层中；所述二沉池的出水管通过管道与所述布水管连通；所述布水管上均匀分布通孔，污水通过布水管上的所述通孔进入所述介质层。
5.根据权利要求4所述的农村污水处理系统，其特征在于:所述布水管为UPVC管。
6.根据权利要求4所述的农村污水处理系统，其特征在于:所述防渗层为复合土工膜防渗层。
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103613240A (zh) * | 2013-11-18 | 2014-03-05 | 广西鸿生源环保科技有限公司 | 多级生态净化治理污水的装置及方法 |
| CN104445831A (zh) * | 2014-12-18 | 2015-03-25 | 重庆大学 | 一种户用式农村生活污水处理、回用一体化系统 |
| CN105254137A (zh) * | 2015-11-18 | 2016-01-20 | 北京清水生态环境工程股份有限公司 | 一种加强型复合生物净化床污水处理系统 |
| CN110498576A (zh) * | 2019-09-23 | 2019-11-26 | 苏州首创嘉净环保科技股份有限公司 | 一种高效低耗村镇生活污水处理工艺 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103613240A (zh) * | 2013-11-18 | 2014-03-05 | 广西鸿生源环保科技有限公司 | 多级生态净化治理污水的装置及方法 |
| CN103613240B (zh) * | 2013-11-18 | 2015-12-02 | 广西鸿生源环保科技有限公司 | 多级生态净化治理污水的装置及方法 |
| CN104445831A (zh) * | 2014-12-18 | 2015-03-25 | 重庆大学 | 一种户用式农村生活污水处理、回用一体化系统 |
| CN104445831B (zh) * | 2014-12-18 | 2016-08-24 | 重庆大学 | 一种户用式农村生活污水处理、回用一体化系统 |
| CN105254137A (zh) * | 2015-11-18 | 2016-01-20 | 北京清水生态环境工程股份有限公司 | 一种加强型复合生物净化床污水处理系统 |
| CN110498576A (zh) * | 2019-09-23 | 2019-11-26 | 苏州首创嘉净环保科技股份有限公司 | 一种高效低耗村镇生活污水处理工艺 |
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