CN204714595U - 用于改良ao的一体化污水处理池 - Google Patents
用于改良ao的一体化污水处理池 Download PDFInfo
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- CN204714595U CN204714595U CN201520292680.9U CN201520292680U CN204714595U CN 204714595 U CN204714595 U CN 204714595U CN 201520292680 U CN201520292680 U CN 201520292680U CN 204714595 U CN204714595 U CN 204714595U
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- 239000010865 sewage Substances 0.000 title claims abstract description 32
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 57
- 239000001301 oxygen Substances 0.000 claims abstract description 57
- 238000005273 aeration Methods 0.000 claims abstract description 45
- 238000005192 partition Methods 0.000 claims abstract description 4
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 15
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 23
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- 238000005265 energy consumption Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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- 229910052698 phosphorus Inorganic materials 0.000 description 3
- 239000011574 phosphorus Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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Abstract
本实用新型公开了一种用于改良AO的一体化污水处理池，所述的一体化污水处理池包括依次相邻并且一体设置且通过隔墙隔开的沉淀区、厌氧除磷区、空气推流区及低氧曝气区，所述低氧曝气区与沉淀区也相邻设置；所述沉淀区与厌氧除磷区相邻端设置进水区，另一端设置有缓冲区。本实用新型的用于改良AO的一体化污水处理池，在同一污水处理池内实现了厌氧处理、好氧处理、污泥回流、泥水分离不同的功能，省去了二沉池及污泥回流泵房，使得占地面积大大减小，同时也降低了建设成本，从而降低了污水处理成本。
Description
技术领域
[0001] 本实用新型设及污水处理装置，尤其设及一种一体化改良A0污水处理池。
背景技术
[0002] 随着社会的发展，水资源紧缺的问题日益严重，水将成为制约社会发展的一项重 要因素。人们也越来越重视水处理技术的开发和改进。
[0003]污水生物处理工艺是污水处理工艺中比较特殊的一种，又称为活性污泥法。活性 污泥法可W分为好氧法和厌氧法等。在好氧生物污水处理系统中，微生物利用水中的溶解 氧，氧化降解水中的有机污染物，然后进行微生物和水的分离操作，达到净化污水的目的。
[0004] A0工艺法也叫厌氧好氧工艺法，A (Anaerobic)是厌氧段，用与脱氮除磯；O(Oxic) 是好氧段，用于去除水中的有机物。
[0005] A0法脱氮工艺的特点：
[0006]1、流程简单，勿需外加碳源与后曝气池，W原污水为碳源，建设和运行费用较低；
[0007]2、反硝化在前，硝化在后，设内循环，W原污水中的有机底物作为碳源，效果好，反 硝化反应充分；
[000引 3、曝气池在后，使反硝化残留物得W进一步去除，提高了处理水水质；
[0009]4、A段揽拌，只起使污泥悬浮，而避免DO(溶解氧）的增加。0段的前段采用强曝 气，后段减少气量，使内循环液的DO含量降低，W保证A段的缺氧状态。
[0010] 传统A0法存在的问题；
[0011] 1、污泥循环比小，脱氮效率低；
[0012] 2、要将污水处理到符合标准，污水的停留时间长，处理效率低。 实用新型内容
[0013]本实用新型的第一个目的是提供一种占地面积小，能够降低污水处理成本的用于 改良A0的一体化污水处理池。
[0014]本实用新型的用于改良A0的一体化污水处理池，包括依次相邻并且一体设置且 通过隔墙隔开的沉淀区、厌氧除磯区、空气推流区及低氧曝气区，所述低氧曝气区与沉淀区 也相邻设置；所述沉淀区与厌氧除磯区相邻端设置进水区，另一端设置有缓冲区，厌氧除磯 区与空气推流区之间、空气推流区与低氧曝气区之间，低氧曝气区与沉淀区之间分别设置 有物料通道，所述低氧曝气区与沉淀区之间的隔板与池底分离设置，W使低氧曝气区与沉 淀区在底部连通。
[0015]可选的，所述低氧曝气区中设置有在线溶氧仪，所述在线溶氧仪连接有控制系统，W对低氧曝气区中的溶氧进行在线监测及控制。
[0016]可选的，所述低氧曝气区中设置有具有自清洗功能的曝气装置。
[0017]可选的，所述空气推流区中设置有空气提升装置，W便对混合液进行提升，从而输 送至低氧曝气区中。
[0018] 本实用新型还提供了一种用于改良AO的一体化污水处理池的污水处理方法，其 特征在于，包括W下步骤：
[0019] S10、将废水输送到进水区内与从沉淀区回流的回流液混合；
[0020] S20、步骤S10中混合后的混合液进入厌氧除磯区进行反硝化和厌氧释磯反应；
[0021] S30、步骤S20中处理后的混合液进入空气推流区，在空气推流区内经过空气提 升后进入到低氧曝气区在DO(溶解氧）<0. 8mg/L条件下利用微生物对COD(化学需氧量， 下同）、氨氮、TN(总氮，下同）及TP(总磯）进行吸收及降解；低氧曝气区溶解氧控制 00<0. 8mg/l，能够同时进行硝化和反硝化作用，从而有效去除部分难降解的有机物，提高有 机物的去除效率，简化了系统脱氮的运行流程，节约了能耗，提高了脱氮效率。
[0022] S40、低氧曝气区处理后的混合液进入到沉淀区中将泥水分离，部分污泥回流至进 水区底部与进水混合，剩余污泥排出污水处理池外，上清液经沉淀区顶部排出。
[002引可选的，回流液的量与废水进水量之比在20W上，W进行大比率的循环稀释，使 得处理池进水端至出水端的有机物浓度梯度大幅度缩小，一方面，可W降低污泥的冲击负 荷，提高了系统的稳定性；另一方面，给微生物创造了相对稳定的生长环境。
[0024] 可选的，所述厌氧除磯区、低氧曝气区中污泥浓度为4~8g/l，在此污泥浓度下， 微生物的吸收、降解能力增强，污泥负荷相对较低，容积负荷相对较高，可W节省±建投资， 同时增加了的系统抗冲击能力。
[0025] 本实用新型的用于改良A0的一体化污水处理池，由于将沉淀区、厌氧除磯区、空 气推流区及低氧曝气区一体设置，因此，在同一污水处理池内实现了厌氧处理、好氧处理、 污泥回流、泥水分离不同的功能，省去了二沉池及污泥回流累房，使得占地面积大大减小， 同时也降低了建设成本，从而降低了污水处理成本。
[0026] 本实用新型的采用上述的用于改良A0的一体化污水处理池的污水处理方法， 由于采用所述的一体化污水处理池，因此污水处理成本低，另外，由于低氧曝气区在 D0<0.8mg/L的条件下进行曝气处理，能够同时进行硝化和反硝化作用，从而有效去除部分 难降解的有机物，提高有机物的去除效率，简化了系统脱氮的运行流程，节约了能耗，提高 了脱氮效率，同时也避免了由于硝态氮积累带来的不利影响，减少了各反应器之间的机械 设备，既实现的良好的脱氮效果，又降低了鼓风能耗，实现了节能降耗和良好处理效果的双 重效果。
附图说明
[0027] 图1为本实用新型用于改良A0的一体化污水处理池的结构示意图。
[002引图中标记示意为；1-沉淀区；2 -厌氧除磯区；3 -空气推流区；4 -低氧曝气区； 101 -进水区；102 -缓冲区；5 -在线溶氧仪。
具体实施方式
[0029] 下面结合实施例及附图对本实用新型的技术方案作进一步阐述。
[0030] 实施例1
[003U参见图1，本实施例提供了一种用于改良AO的一体化污水处理池，包括依次相邻 并且一体设置且通过隔墙隔开的沉淀区1、厌氧除磯区2、空气推流区3及低氧曝气区4,所 述低氧曝气区4与沉淀区1也相邻设置；所述沉淀区1与厌氧除磯区2相邻端设置进水区101，另一端设置有缓冲区102,厌氧除磯区2与空气推流区3之间、空气推流区3与低氧曝 气区4之间，低氧曝气区4与沉淀区1之间分别设置有物料通道，所述低氧曝气区4与沉淀 区1之间的隔板与池底分离设置，W使低氧曝气区4与沉淀区1在底部连通。
[003引上述的用于改良AO的一体化污水处理池，由于将沉淀区1、厌氧除磯区2、空气推 流区3及低氧曝气区4 一体设置，因此，在同一污水处理池内实现了厌氧处理、好氧处理、污 泥回流、泥水分离不同的功能，省去了二沉池及污泥回流累房，使得占地面积大大减小，同 时也降低了建设成本，从而降低了污水处理成本。
[0033] 本实施例中，优选的，所述低氧曝气区4中设置有在线溶氧仪5,所述在线溶氧仪5 连接有控制系统，W对低氧曝气区4中的溶氧进行在线监测及控制。
[0034] 本实施例中，优选的，所述低氧曝气区4中设置有具有自清洗功能的曝气装置（图 中未示出）。
[0035] 本实施例中，优选的，所述空气推流区3中设置有空气提升装置（图中未示出），W 便对混合液进行提升，从而输送至低氧曝气区4中。
[0036] 本实施例中，所述具有自清洗功能的曝气装置，空气提升装置均为现有技术中的 常用设备，在此对其结构不再寶述。
[0037] 实施例2
[003引参见图1，本实施例提供了一种用于改良AO的一体化污水处理池的污水处理方 法，包括W下步骤：
[0039] S10、将废水输送到进水区101内与从沉淀区1回流的回流液混合；
[0040] S20、步骤S10中混合后的混合液进入厌氧除磯区2进行反硝化和厌氧释磯反应；
[0041]S30、步骤S20中处理后的混合液进入空气推流区3,在空气推流区内经过空气提 升后进入到低氧曝气区4在D0<0. 8mg/L条件下利用微生物对COD、氨氮、TN及TP进行吸收 及降解；低氧曝气区溶解氧控制D0<0. 8mg/l，能够同时进行硝化和反硝化作用，从而有效 去除部分难降解的有机物，提高有机物的去除效率，简化了系统脱氮的运行流程，节约了能 耗，提高了脱氮效率。
[0042]S40、低氧曝气区4处理后的混合液进入到沉淀区1中将泥水分离，部分污泥回流 至进水区101底部与进水混合，剩余污泥排出污水处理池外，上清液经沉淀区1顶部排出。
[0043] 本实施例中，优选的，回流液的量与废水进水量之比在20W上，进行大比率的循 环稀释，使得处理池进水端至出水端的有机物浓度梯度大幅度缩小，一方面，可W降低污泥 的冲击负荷，提高了系统的稳定性；另一方面，给微生物创造了相对稳定的生长环境。
[0044] 本实施例中，优选的，所述厌氧除磯区、低氧曝气区中污泥浓度为4~8g/L在此污 泥浓度下，微生物的吸收、降解能力增强，污泥负荷相对较低，容积负荷相对较高，可W节省 ±建投资，同时增加了的系统抗冲击能力。
[0045] 经验证，本实施例与传统A0工艺比较，排水COD指标可降低20%W上，节约电耗约 30%~40%，脱氮效率提高20%~40%。
[0046] 经验证，通过表1可W看出，本实施例与传统A0工艺比较，排水COD指标可降低 20%W上，节约电耗约30%~40%，脱氮效率提高20%~40%。
[0047] 表1改良A0工艺与传统A0工艺对比表
[0048]
[0049] 最后应说明的是；W上实施例仅用W说明本实用新型的技术方案，而非对其限制； 尽管参照前述实施例对本实用新型进行了详细的说明，本领域的普通技术人员应当理解： 其依然可W对前述各实施例所记载的技术方案进行修改，或者对其中部分技术特征进行等 同替换；而该些修改或者替换，并不使相应技术方案的本质脱离本实用新型各实施例技术 方案的精神和范围。
Claims (4)
1. 一种用于改良AO的一体化污水处理池，其特征在于，包括依次相邻并且一体设置且 通过隔墙隔开的沉淀区、厌氧除磷区、空气推流区及低氧曝气区，所述低氧曝气区与沉淀区 也相邻设置；所述沉淀区与厌氧除磷区相邻端设置进水区，另一端设置有缓冲区，厌氧除磷 区与空气推流区之间、空气推流区与低氧曝气区之间，低氧曝气区与沉淀区之间分别设置 有物料通道，所述低氧曝气区与沉淀区之间的隔板与池底分离设置，以使低氧曝气区与沉 淀区在底部连通。
2. 根据权利要求1所述的用于改良AO的一体化污水处理池，其特征在于，所述低氧曝 气区中设置有在线溶氧仪，所述在线溶氧仪连接有控制系统。
3. 根据权利要求1所述的用于改良AO的一体化污水处理池，其特征在于，所述低氧曝 气区中设置有具有自清洗功能的曝气装置。
4. 根据权利要求1所述的用于改良AO的一体化污水处理池，其特征在于，所述空气推 流区中设置有空气提升装置。
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| CN106186313A (zh) * | 2015-05-07 | 2016-12-07 | 易百皓源（北京）环保科技有限公司 | 用于改良ao的一体化污水处理池及污水处理方法 |
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| CN106007270A (zh) * | 2016-08-04 | 2016-10-12 | 迈邦（北京）环保工程有限公司 | 印染污水处理方法及印染污水处理系统 |
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