CN201932988U - 厌氧/好氧接触氧化膜生物反应器 - Google Patents
厌氧/好氧接触氧化膜生物反应器 Download PDFInfo
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- CN201932988U CN201932988U CN2011200227445U CN201120022744U CN201932988U CN 201932988 U CN201932988 U CN 201932988U CN 2011200227445 U CN2011200227445 U CN 2011200227445U CN 201120022744 U CN201120022744 U CN 201120022744U CN 201932988 U CN201932988 U CN 201932988U
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- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate Chemical compound 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- 238000006396 nitration reaction Methods 0.000 description 2
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- 241000589651 Zoogloea Species 0.000 description 1
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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[N].N CVTZKFWZDBJAHE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
厌氧/好氧接触氧化膜生物反应器，污水调节池与厌氧/好氧接触氧化反应池连通，厌氧/好氧接触氧化反应池由隔板分成厌氧反应池和好氧接触氧化反应池两部分。厌氧反应池进水管端设有挡板，并设有搅拌器；好氧接触氧化反应池中挂有软性填料，底部设有微孔曝气头，末端设有出水/膜滤槽。出水/膜滤槽的输出管道与膜处理系统连通，膜处理系统输出管道与净水池连通。既可处理低浓度有机废水、又可处理高浓度有机废水。既可除有机物，又可脱氮，应用范围广。工艺设备集中、处理效率高、污泥排放少、无二次污染，占地面积少、工作安全稳定、运行可靠，处理后出水可直接回用，具有较大的环境效益、社会效益和经济效益。
Description
厌氧/好氧接触氧化膜生物反应器
技术领域
[0001] 本实用新型涉及膜生物反应器结构的改进，具体说是一种厌氧/好氧接触氧化膜生物反应器，属污水处理设备。
背景技术
[0002] 水质污染的加剧和用水量的增加，使有限的水资源日趋紧张，污水再生回用和资源化成为解决水资源短缺的重要途径之一。目前，污水处理的设备和技术比较多，有各种大型的污水处理设备和一些小型的污水处理器等等。但是，传统的回用工艺，流程复杂、占地面积大、出水水质稳定性差；采用厌氧/好氧（A/0)工艺的大型污水处理厂，只适用于工矿企业的高浓度有机废水的处理，结构复杂、占地面积大；接触氧化工艺、一体式或分置式的小型膜生物反应器，主要处理低浓度的污水，虽然结构简单，但是不能脱氮除磷，处理的水质一般达不到回用水的要求，难以处理高浓度废水。
实用新型内容
[0003] 本实用新型的目的是针对上述不足，提供一种结构简单，占地面积小，节约能源、 节省设备及运行费用，既可处理低浓度有机废水、又可处理高浓度有机废水，处理效率高， 出水可直接回用的厌氧/好氧接触氧化膜生物反应器。
[0004] 实现本实用新型目的的技术方案是：
[0005] 这种厌氧/好氧接触氧化膜生物反应器，包括污水调节池、膜处理系统、鼓风机、 净水池，特点是污水调节池的污水输出管道经污水进水泵与厌氧/好氧接触氧化反应池连通，厌氧/好氧接触氧化反应池由隔板分成厌氧反应池和好氧接触氧化反应池两部分，厌氧反应池的污水进水管端设有进水挡板，在厌氧反应池中设有搅拌器；在好氧接触氧化反应池中挂有软性填料，好氧接触氧化反应池的底部设有与鼓风机连通的至少4个微孔曝气头，好氧接触氧化反应池的末端设有出水/膜滤槽，出水/膜滤槽的输出管道与膜处理系统连通，膜处理系统的输出管道经抽吸泵与净水池连通。
[0006] 为了脱氮除磷反硝化的顺利进行，在膜处理系统浓液出口端和厌氧反应池之间， 设有由回流泵连通的回流管道，回流管道的进口端设在膜处理系统浓液出口端，回流管道的出口端设在厌氧反应池的前端。
[0007] 根据水质、处理目的以及处理效果的不同，所述的膜处理系统，可采用抗污染膜组件、微滤膜组件或纳滤膜组件等不同膜组件。
[0008] 为了随时了解和掌握污水的处理状况，还可以根据需要在好氧接触氧化反应池和膜处理系统中，设有由电导率监测仪、PH监测仪、COD监测仪等监测仪器组成的在线监测系统，在线监测处理污水的技术参数。
[0009] 这种厌氧/好氧接触氧化膜生物反应器，由污水调节池，调节污水的水质、水量， 保证生化部分水质的稳定；污水首先进入厌氧反应池，厌氧反应池首段设有挡板，控制水力冲击，厌氧反应池不供氧，可以利用原废水中的有机物直接作为有机碳源，将从膜系统浓液回流回来的含有硝酸盐的混合液中的硝酸盐反硝化成为氮气；而且，在厌氧反应池中由于反硝化反应而产生的碱度可以随出水进入好氧接触氧化反应池，补偿硝化反应过程中所需消耗碱度；厌氧混合液溢流至好氧接触氧化反应池，好氧接触氧化反应池由鼓风机供氧，池中挂有软性填料，以增大污水与活性污泥的接触面积，提高处理效率，好氧接触氧化反应池内既有活性污泥菌胶团，又有软性填料上生长的生物膜，能够维持污泥的高活性，污泥保留时间长，减少污泥浪费，提高处理效率，从而缩小处理设备的规模。同时硝化与反硝化作用， 完全保留处理设备中缓慢生长的硝化细菌，达到脱氮除磷的目的，好氧接触氧化反应池设置在流程的后端，也可以使反硝化过程中常常残留的有机物得以进一步去除；在好氧接触氧化反应池的末端设有出水/膜滤槽，既是出水槽又兼做膜滤池，克服了分置式膜生物反应器单设膜滤池，能耗高和长循环管带来的安装难度较大、造价较高和长循环管易积泥等问题。膜处理系统，可以通过更换膜组件的方式，实现微滤、超滤和纳滤之间的转换，处理后的净水，进入净水池回用。
[0010] 本实用新型结构简单，可选用现有的各种过滤材料和通用的管路部件等，并采用常规的技术制作，容易实施。
[0011] 与现有技术相比，本实用新型的有益效果在于：
[0012] 既可处理低浓度有机废水、又可处理高浓度有机废水，应用范围十分广泛；
[0013] 处理效率高，同时硝化与反硝化，污泥保留时间长，同时具有除有机物脱氮的功能。反应器内的微生物浓度高，耐冲击负荷。物质迁移转化效率高，大约为1〜2Kg干有机物/m3曝气池· d。有利于增殖缓慢的硝化细菌的截流、生长和繁殖，系统硝化效率得以提
尚ο
[0014] 泥龄长。厌氧污泥、好氧污泥及生物膜联合作用，大大提高了难降解有机物的降解效率。反应池在高容积负荷、低污泥负荷、长泥龄下运行，污泥排放少。
[0015] 具有结构简单、成本低、工作安全稳定、运行可靠、操作简单、占地面积少、工艺设备集中、无二次污染等优点，具有较大的环境效益、社会效益和经济效益。
附图说明
[0016] 图1是本实用新型一种实施例的结构示意图。
[0017] 图中：1污水调节池，2污水进水泵，3厌氧/好氧接触氧化反应池、3-1厌氧反应池、3-2好氧接触氧化反应池，4隔板，5进水挡板，6搅拌器，7软性填料，8微孔曝气头，9鼓风机，10出水/膜滤槽，11膜处理系统，12抽吸泵，13净水池，14回流泵，15回流管道。
具体实施方式
[0018] 下面结合附图和给出的实施例对本实用新型作进一步描述。
[0019] 参照附图，这种厌氧/好氧接触氧化膜生物反应器的结构如下：
[0020] 污水调节池1的污水输出管道经污水进水泵2与厌氧/好氧接触氧化反应池3连通，厌氧/好氧接触氧化反应池3由隔板4分成厌氧反应池3-1和好氧接触氧化反应池3-2 两部分。厌氧反应池的污水进水管端设有进水挡板5，在厌氧反应池中设有搅拌器6。在好氧接触氧化反应池中挂有软性填料7，好氧接触氧化反应池的底部设有与鼓风机9连通的8 个微孔曝气头8，好氧接触氧化反应池的末端设有出水/膜滤槽10。出水/膜滤槽的输出管道与纳滤膜处理系统11连通，纳滤膜处理系统的输出管道经抽吸泵12与净水池13连通。 在膜处理系统和厌氧反应池之间，设有由回流泵14连通的回流管道15，回流管道的进口端设在纳滤膜浓液出口端，回流管道的出口端设在厌氧反应池的前端。
[0021] 本实用新型申请人按实施例，实施一种厌氧/好氧接触氧化膜生物反应器，厌氧/ 好氧接触氧化反应池的有效容积1200毫米X 800毫米X 800毫米，其中厌氧反应池的有效容积占厌氧/好氧接触氧化反应池有效容积的五分之一；好氧接触氧化反应池的有效容积占厌氧/好氧接触氧化反应池有效容积的五分之四，软性填料网格排列，挂有180个球形填料。主要参数：温度为 10-28°C、pH>6. 5、HRT 8h、SRT 130h、MLSS 10. 2g/L。膜处理系统选用50纳米纳滤膜组件。膜面流速5. 0-7. Om/s，膜操作压力为0. 20MPa条件下处理生活污水，膜通量为：130-170L/h.m2。
[0022] 经内部试用显示，利用这种厌氧/好氧接触氧化膜生物反应器，处理城市污水，系统出水SS去除率达到100%，COD去除率达94.5%，BOD5的去除率达到95%，氨氮去除率达到98. 3%，出水水质优于城市杂用水水质标准（GB/T18920-2002)。系统运行稳定，有较强的抗冲击负荷能力。处理后的水可以作为喷灌、浇洒道路、洗车和人工湖补充水使用。使用十分方便，清洁生产，无二次污染，不用添加药剂，处理的污水可直接回用，实现了污水资源化，受到试用单位的好评。
Claims (4)
1. 一种厌氧/好氧接触氧化膜生物反应器，包括污水调节池、膜处理系统、鼓风机、净水池，其特征在于污水调节池的污水输出管道经污水进水泵与厌氧/好氧接触氧化反应池连通，厌氧/好氧接触氧化反应池由隔板分成厌氧反应池和好氧接触氧化反应池两部分， 厌氧反应池的污水进水管端设有进水挡板，在厌氧反应池中设有搅拌器；在好氧接触氧化反应池中挂有软性填料，好氧接触氧化反应池的底部设有与鼓风机连通的至少4个微孔曝气头，好氧接触氧化反应池的末端设有出水膜滤槽，出水/膜滤槽的输出管道与膜处理系统连通，膜处理系统的输出管道经抽吸泵与净水池连通。
2.根据权利要求1所述的厌氧/好氧接触氧化膜生物反应器，其特征在于在膜处理系统浓液出口端和厌氧反应池之间，设有由回流泵连通的回流管道，回流管道的进口端设在膜处理系统浓液出口端，回流管道的出口端设在厌氧反应池的前端。
3.根据权利要求1所述的厌氧/好氧接触氧化膜生物反应器，其特征在于膜处理系统采用抗污染膜组件、微滤膜组件或纳滤膜组件。
4.根据权利要求1所述的厌氧/好氧接触氧化膜生物反应器，其特征在于在好氧接触氧化反应池和膜处理系统中，设有由电导率监测仪、PH监测仪或COD监测仪组成的在线监测系统。
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN103183450A (zh) * | 2011-12-31 | 2013-07-03 | 上海轻工业研究所有限公司 | 日化废水的处理方法和设备 |
| CN103232109A (zh) * | 2013-05-14 | 2013-08-07 | 大连东利伟业环保节能科技有限公司 | 多功能生物反应器 |
| CN105152329A (zh) * | 2015-07-24 | 2015-12-16 | 中电环保股份有限公司 | 一种移动床生物反应器 |
| CN105731734A (zh) * | 2016-03-31 | 2016-07-06 | 浙江大学 | 一种节能mbr污水处理系统 |
| CN106145525A (zh) * | 2016-07-28 | 2016-11-23 | 中冶焦耐(大连)工程技术有限公司 | 一种焦化废水硝酸盐氮脱除装置 |
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| CN103183450A (zh) * | 2011-12-31 | 2013-07-03 | 上海轻工业研究所有限公司 | 日化废水的处理方法和设备 |
| CN103183450B (zh) * | 2011-12-31 | 2014-11-12 | 上海轻工业研究所有限公司 | 日化废水的处理方法和设备 |
| CN103232109A (zh) * | 2013-05-14 | 2013-08-07 | 大连东利伟业环保节能科技有限公司 | 多功能生物反应器 |
| CN105152329A (zh) * | 2015-07-24 | 2015-12-16 | 中电环保股份有限公司 | 一种移动床生物反应器 |
| CN105731734A (zh) * | 2016-03-31 | 2016-07-06 | 浙江大学 | 一种节能mbr污水处理系统 |
| CN106145525A (zh) * | 2016-07-28 | 2016-11-23 | 中冶焦耐(大连)工程技术有限公司 | 一种焦化废水硝酸盐氮脱除装置 |
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