CN204385022U - 集中型污水处理系统 - Google Patents
集中型污水处理系统 Download PDFInfo
- Publication number
- CN204385022U CN204385022U CN201420778210.9U CN201420778210U CN204385022U CN 204385022 U CN204385022 U CN 204385022U CN 201420778210 U CN201420778210 U CN 201420778210U CN 204385022 U CN204385022 U CN 204385022U
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- raceway groove
- reaction tank
- diatomite
- treatment systems
- sewage treatment
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- 239000010865 sewage Substances 0.000 title claims abstract description 84
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound 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O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 63
- 238000006243 chemical reaction Methods 0.000 claims abstract description 47
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- 239000002562 thickening agent Substances 0.000 claims description 13
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- 230000000694 effects Effects 0.000 abstract description 8
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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- 239000004576 sand Substances 0.000 description 2
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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Abstract
本实用新型适用于生活污水处理领域，提供了一种集中型污水处理系统，包括中心岛、好氧沟道、缺氧沟道和厌氧沟道，中心岛上设有旋流沉砂池、硅藻精土反应池、投料室、消毒装置以及用于排出硅藻精土反应池中消毒后的清水的排水装置；投料室中安装有用于向硅藻精土反应池中投加硅藻精土的投料机，旋流沉砂池与厌氧沟道相连通，厌氧沟道与缺氧沟道相连通，缺氧沟道与好氧沟道相连通。通过在中心岛上设置旋流沉砂池，并环绕中心岛由内向外依次环绕好氧沟道、缺氧沟道和厌氧沟道，保证对污水进行生化处理的效果，提高氮、磷、COD等的去除效率；在中心岛上设置硅藻精土反应池、消毒装置和投料机，保证出水水质好、无臭味；减小占地面积。
Description
技术领域
[0001] 本实用新型属于生活污水处理领域，尤其涉及一种集中型污水处理系统。
背景技术
[0002] 随着农村经济的快速发展，农村综合废水排放量逐渐增大，使农村地区环境状况日益恶化，环境质量明显下降，据统计造成湖泊富营养化的氮、磷约84% -90%来源于农村生活污水和农田生产废水，农村污水的任意排放对生态环境造成了较为严重的影响，直接威胁着广大农民群众的生存环境与身体健康，制约了农村经济的健康发展。
[0003] 据调查目前国内采用的处理农村污水的方法多为人工湿地、稳定塘、生态沟等生态治理方法，优点是投资小、节约能源、无二次污染，但这类生态污水治理方法普遍存在占地面积大，随着气温变化，出水水质不稳定的缺点。
实用新型内容
[0004] 本实用新型的目的在于提供一种集中型污水处理系统，旨在解决现有农村污水处理系统占地面积大，随着气温变化，出水水质不稳定的问题。
[0005] 本实用新型是这样实现的，一种集中型污水处理系统，包括中心岛、环绕所述中心岛的好氧沟道、环绕所述好氧沟道的缺氧沟道和环绕所述缺氧沟道的厌氧沟道，所述中心岛上设有用于收集并初步处理外界污水的旋流沉砂池、与所述好氧沟道相连通的硅藻精土反应池、投料室、用于对所述硅藻精土反应池中清水进行消毒的消毒装置以及用于排出所述硅藻精土反应池中消毒后的清水的排水装置；所述投料室中安装有用于朝向所述硅藻精土反应池中投料入硅藻精土的投料机，所述旋流沉砂池与所述厌氧沟道相连通，所述厌氧沟道与所述缺氧沟道相连通，所述缺氧沟道与所述好氧沟道相连通。
[0006] 进一步地，所述中心岛上还设置有污泥浓缩池，所述污泥浓缩池与所述硅藻精土反应池相连通。
[0007] 进一步地，所述中心岛上还设置有脱水机房，所述脱水机房中安装有用于对所述污泥浓缩池中浓缩的污泥进行脱水的脱水机。
[0008] 进一步地，所述中心岛上还设置有控制室，所述控制室中安装有用于控制该集中型污水处理系统工作的控制器。
[0009] 进一步地，还包括连接所述娃藻精土反应池与所述厌氧沟道以使所述娃藻精土反应池中部分硅藻精土能够进入所述厌氧沟道中的污泥回流管道。
[0010] 进一步地，所述中心岛上还设置有鼓风机室，所述鼓风机室中安装有用于向所述好氧沟道中通风供氧的鼓风机。
[0011] 进一步地，还包括与外界污水管道相连通的集水池和用于将所述集水池中污水抽送至所述旋流沉砂池的提升泵。
[0012] 进一步地，还包括用于对所述外界污水管道进行粗过滤的粗格栅过滤器，所述粗格栅过滤器设于所述集水池的入口处。
[0013] 进一步地，还包括用于对进入所述提升泵的污水进行过滤的细格栅过滤器，所述细格栅过滤器安装于所述提升泵的入口处。
[0014] 进一步地，所述投料室中还安装有用于将所述好氧沟道中污水抽送至所述硅藻精土反应池中的加压泵，所述投料机与所述加压泵的入口相连通。
[0015] 本实用新型通过设置中心岛，在中心岛上设置旋流沉砂池，并环绕中心岛由内向外依次环绕好氧沟道、缺氧沟道和厌氧沟道，从而使好氧沟道、缺氧沟道和厌氧沟道有足够的长度，保证对污水进行生化处理的效果，提高除磷效率；设置硅藻精土反应池、消毒装置和投料机，对生化处理后的水进行硅藻精土再处理，保证出水水质好、无臭味；提高了整个集中型污水处理系统的氮、磷、COD等物质的去除效率；而将硅藻精土反应池、消毒装置和投料机设置在中心岛上，提高集成度，充分利用空间面积，减小该集中型污水处理系统的占地面积。
附图说明
[0016]图1是本实用新型实施例提供的集中型污水处理系统的结构示意图。
具体实施方式
[0017] 为了使本实用新型的目的、技术方案及优点更加清楚明白，以下结合附图及实施例，对本实用新型进行进一步详细说明。应当理解，此处所描述的具体实施例仅仅用以解释本实用新型，并不用于限定本实用新型。
[0018] 请参阅图1，本实用新型实施例提供的一种集中型污水处理系统，包括中心岛10、好氧沟道23、缺氧沟道22和厌氧沟道21 ;中心岛10上设有旋流沉砂池11、娃藻精土反应池14、投料室13、消毒装置16以及排水装置15，投料室13中安装有用于朝向硅藻精土反应池14中投料入硅藻精土的投料机(图中未示出)。旋流沉砂池11与厌氧沟道21相连通，厌氧沟道21与缺氧沟道22相连通，缺氧沟道22与好氧沟道23相连通。旋流沉砂池11用于收集并初步处理外界污水，以去除污水中的悬浮物，防止杂物在污水处理过程中堵塞管道，并同时以便向厌氧沟道21中供污水。好氧沟道23环绕中心岛10，缺氧沟道22环绕好氧沟道23，厌氧沟道21环绕缺氧沟道22，从而保证好氧沟道23、缺氧沟道22和厌氧沟道21有足够的长度，保证形成的氧化沟生化处理的效果。硅藻精土反应池14与好氧沟道23相连通，以便好氧沟道23中生化处理后的水进入硅藻精土反应池14中进行硅藻精土处理。消毒装置16用于对硅藻精土反应池14中清水进行消毒，经消毒后的清水经排水装置15排出。
[0019] 通过设置中心岛10，在中心岛10上设置旋流沉砂池11，并环绕中心岛10由内向外依次环绕好氧沟道23、缺氧沟道22和厌氧沟道21，从而使好氧沟道23、缺氧沟道22和厌氧沟道21有足够的长度，保证对污水进行生化处理的效果，提高除磷效率，简化了生化处理流程。设置硅藻精土反应池14、消毒装置16和投料机，对生化处理后的水进行硅藻精土再处理，保证出水水质好、无臭味。通过氧化沟生化处理和硅藻精土处理，提高了整个集中型污水处理系统的氮、磷等物质的去除效率；而将硅藻精土反应池14、消毒装置16和投料机设置在中心岛10上，提高集成度，充分利用空间面积，减小该集中型污水处理系统的占地面积。旋流沉砂池11可以通过管道与厌氧沟道21相连通。
[0020] 进一步地，中心岛10上还设置有污泥浓缩池17，污泥浓缩池17与硅藻精土反应池14相连通。设置污泥浓缩池17，以便对硅藻精土反应池14处理排出的污泥进行浓缩，方便运出。更进一步地，中心岛10上还设置有脱水机房18，脱水机房18中安装有用于对污泥浓缩池17中浓缩的污泥进行脱水的脱水机(图中未示出)。将污泥浓缩池17中浓缩的污泥进行脱水，以减小污泥的体积，并且可以对脱出的水回流到硅藻精土反应池14中进行再处理，减少污泥排放量，方便将浓缩的污泥运出处理。
[0021] 进一步地，旋流沉砂池11和投料室13位于硅藻精土反应池14的一侧，污泥浓缩池17与脱水机房18位于娃操精土反应池14的另一侧。以进一步提尚集成度，减小该集中型污水处理系统占地面积。
[0022] 进一步地，该集中型污水处理系统还包括连接硅藻精土反应池14与厌氧沟道21的污泥回流管道(图中未示出)。通过污泥回流管道来连通硅藻精土反应池14与厌氧沟道21，当硅藻精土加入硅藻精土反应池中后，部分硅藻精土可以经污泥回流管道进入厌氧沟道21中，利用硅藻精土的强吸附性和大比表面积对臭味进行吸附及为微生物提供附着场所，确保污水处理过程中不产生臭味的同时也加大生化池中微生物的含量。
[0023] 进一步地，中心岛10上还设置有鼓风机室12，鼓风机室12中安装有用于向好氧沟道23中通风供氧的鼓风机(图中未示出)。设置鼓风机向好氧沟道23中通风，实现对好氧沟道23的曝气，以便好氧沟道23中溶解有足够的氧，形成好氧环境；而将鼓风机室12设置在中心岛10上，提高集成度，可以减小该集中型污水处理系统占地面积。
[0024] 进一步地，该集中型污水处理系统还包括与外界污水管道相连通的集水池(图中未示出)和用于将集水池中污水抽送至旋流沉砂池11的提升泵(图中未示出)。设置集水池，以方便聚集外界生活污水，使污水在集水池中混合，均衡污水；并且可以初步对污水中的泥沙进行沉淀处理。设置提升泵，以便向旋流沉砂池11中供给污水，同时也可以提高供给污水的压力和流速，以便更好的去除污水中的悬浮物。
[0025] 进一步地，该集中型污水处理系统还包括用于对外界污水管道进行粗过滤的粗格栅过滤器(图中未示出)，粗格栅过滤器设于集水池的入口处。使用粗格栅对进入集水池中的污水进行过滤，可以去除较大的沙粒，也可以防止后期处理时堵塞管道。
[0026] 该集中型污水处理系统还包括用于对进入提升泵的污水进行过滤的细格栅过滤器(图中未示出)，细格栅过滤器安装于提升泵的入口处。设置细格栅过滤器既可以进一步过滤污水，又可以保护提升泵，减少污水中沙粒对提升泵的损害。
[0027] 进一步地，投料室13中还安装有用于将好氧沟道23中污水抽送至硅藻精土反应池14中的加压泵(图中未示出)，投料机与加压泵的入口相连通。通过加压泵来抽取好氧沟道23中污水，可以提高污水进入硅藻精土反应池14压力，对硅藻精土反应池14进行加压，提高硅藻精土反应池14的处理效果与处理效率。
[0028] 本实施例中优选地，排水装置15为连通硅藻精土反应池14与外界的叠水台。使用叠水台，可以使该集中型污水处理系统与周围环境更为协调，保持良好的生态环境。进一步地，中心岛10上还设置有控制室19，控制室19中安装有用于控制该集中型污水处理系统工作的控制器。通过控制器可以实现各部件，如提升泵、投料机、加压泵、鼓风机、硅藻精土反应池14、脱水机等设备的自动化工作。
[0029] 本实施例的集中型污水处理系统的处理过程如下:
[0030] 外界管道收集农村生活污水和生产废水经过粗格栅过滤器进入集水池中混合，均衡污水；然后通过细格栅过滤器过滤，进入提升泵；在提升泵的作用下进入旋流沉砂池11，进一步去除废水中的悬浮物，同时也防止杂物在污水处理过程中堵塞进水管；污水从旋流沉沙池通过自流进入厌氧沟道21中旋转流动，在厌氧沟道21中由于污水混合液对氧的吸收率高于供氧速率，供给的溶解氧立即被消耗掉，溶解氧一般为0-0.5mg/L，形成厌氧生化处理；污水混合液在厌氧沟道21中旋转流动的同时会有部分处理过的污水混合液进入缺氧沟道22，继续进行生化处理，缺氧沟道22的溶解氧呈波动状态，平均约0.5-1.5mg/L,形成缺氧生化处理；缺氧沟道22中流动的污水混合液有一部分会自流进入好氧沟道23，好氧沟道23中溶解氧为1.5-2.5mg/L，污水混合液在该好氧沟道23中形成好氧生化处理。好氧沟道23处理的污水，流经投料机处，投料机向污水中投加硅藻精土，每吨污水的投加量约为0.03-0.05kg，再通过加压泵加压，进入娃藻精土反应池14 ;娃藻精土反应池14中，在硅藻精土的作用下进一步去除废水中的氮、磷、SS等，然后进行泥水分离，清水通过硅藻精土反应池14上设置的消毒装置16消毒后通过叠水台排出，出水符合GB18918-2002 —级A标:pH7-8, COD < 50mg/L，BOD < 15mg/L，氨氮< 5mg/L，总磷< 0.5mg/L，SS < 20mg/L。而硅藻精土反应池14处理后排出的污泥，在污泥浓缩池17集中浓缩，再经脱水机脱水。
[0031] 本实施例中，粗格栅过滤器的一般选取40-60mm的粗格栅过滤，优选地选取50mm的粗格栅过滤，以便去除较大颗粒杂质。细格栅过滤器的一般选取3-5mm的细格栅过滤，优选地选取3mm的细格栅过滤，以进行进一步过滤，并保证提升泵的进水量。
[0032] 该集中型污水处理系统将氧化生化处理和硅藻精土处理进行高度集成，自动化程度高，占地面积小；相比现有技术剩余污泥量能减少60%以上。处理后的出水水质好、无臭味，且氮、磷等物质的去除效率高，效果好。还可以通过植物与叠水台的合理配置，实现与周围环境合理搭配，保持良好生态、美化环境的作用。
[0033] 以上所述仅为本实用新型的较佳实施例而已，并不用以限制本实用新型，凡在本实用新型的精神和原则之内所作的任何修改、等同替换和改进等，均应包含在本实用新型的保护范围之内。
Claims (10)
1.一种集中型污水处理系统，其特征在于，包括中心岛、环绕所述中心岛的好氧沟道、环绕所述好氧沟道的缺氧沟道和环绕所述缺氧沟道的厌氧沟道，所述中心岛上设有用于收集并初步处理外界污水的旋流沉砂池、与所述好氧沟道相连通的硅藻精土反应池、投料室、用于对所述硅藻精土反应池中清水进行消毒的消毒装置以及用于排出所述硅藻精土反应池中消毒后的清水的排水装置；所述投料室中安装有用于向所述硅藻精土反应池中投加硅藻精土的投料机，所述旋流沉砂池与所述厌氧沟道相连通，所述厌氧沟道与所述缺氧沟道相连通，所述缺氧沟道与所述好氧沟道相连通。
2.如权利要求1所述的集中型污水处理系统，其特征在于，所述中心岛上还设置有污泥浓缩池，所述污泥浓缩池与所述硅藻精土反应池相连通。
3.如权利要求2所述的集中型污水处理系统，其特征在于，所述中心岛上还设置有脱水机房，所述脱水机房中安装有用于对所述污泥浓缩池中浓缩的污泥进行脱水的脱水机。
4.如权利要求3所述的集中型污水处理系统，其特征在于，所述中心岛上还设置有控制室，所述控制室中安装有用于控制该集中型污水处理系统工作的控制器。
5.如权利要求1-4任一项所述的集中型污水处理系统，其特征在于，还包括连接所述硅藻精土反应池与所述厌氧沟道以使所述硅藻精土反应池中部分硅藻精土能够进入所述厌氧沟道中的污泥回流管道。
6.如权利要求1-4任一项所述的集中型污水处理系统，其特征在于，所述中心岛上还设置有鼓风机室，所述鼓风机室中安装有用于向所述好氧沟道中通风供氧的鼓风机。
7.如权利要求1-4任一项所述的集中型污水处理系统，其特征在于，还包括与外界污水管道相连通的集水池和用于将所述集水池中污水抽送至所述旋流沉砂池的提升泵。
8.如权利要求7所述的集中型污水处理系统，其特征在于，还包括用于对所述外界污水管道进行粗过滤的粗格栅过滤器，所述粗格栅过滤器设于所述集水池的入口处。
9.如权利要求8所述的集中型污水处理系统，其特征在于，还包括用于对进入所述提升泵的污水进行过滤的细格栅过滤器，所述细格栅过滤器安装于所述提升泵的入口处。
10.如权利要求1-4任一项所述的集中型污水处理系统，其特征在于，所述投料室中还安装有用于将所述好氧沟道中污水抽送至所述硅藻精土反应池中的加压泵，所述投料机与所述加压泵的入口相连通。
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