CN204211537U - 一体化兼氧mbr膜生物反应器 - Google Patents
一体化兼氧mbr膜生物反应器 Download PDFInfo
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- CN204211537U CN204211537U CN201420629743.0U CN201420629743U CN204211537U CN 204211537 U CN204211537 U CN 204211537U CN 201420629743 U CN201420629743 U CN 201420629743U CN 204211537 U CN204211537 U CN 204211537U
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- anaerobic pond
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- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 45
- 239000001301 oxygen Substances 0.000 title claims abstract description 45
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Abstract
本实用新型公开了一种一体化兼氧MBR膜生物反应器。主体呈长方体形，由厌氧池和兼氧池构成。所述厌氧池由改进型上流式厌氧污泥床反应器构成。所述兼氧池内布置球形悬浮填料，采用浸没结合方式，将中空纤维膜组件置于兼氧池中，并对膜组件底部进行射流曝气。膜组件外部加格栅网罩，以防球形悬浮填料损伤中空纤维膜组件。整个兼氧池中，膜组件及膜组件上方为好氧区，其余部分为兼氧区，兼氧区大于好氧区。经厌氧池处理后的污水先经过兼氧区，然后经过好氧区，再由膜组件抽吸过滤，最后达标出水。
Description
技术领域
[0001] 本实用新型涉及一种膜生物反应器，属于环保设备领域中的污水处理设备。
背景技术
[0002] 膜生物反应器是目前在高浓度有机废水处理、生活污水处理、中水回用处理等领域最有前途的废水生物处理技术之一。在现有膜生物反应器中，多采用厌氧一好氧处理工艺，而厌氧出水中溶解氧很低，厌氧出水的氧化电位也很低，直接进入后续的好氧单元，其水质条件不能满足好氧微生物生长活动的需要，且厌氧出水中某些厌氧产物如硫化物、氨等，对好氧微生物的生长有一定的抑制作用。故目前采用厌氧-好氧处理工艺的膜生物反应器普遍存在着厌氧单元处理不彻底和好氧单元出水效果较差的现象，致使整体处理工艺难以达到满意的运行效果。
[0003] 若在在厌氧、好氧单元之间增设兼氧单元，为厌氧出水进入后续好氧处理前增加废水的溶解氧，去除废水中的厌氧产物，减轻其对后续好氧处理的抑制影响，则能有效提高膜生物反应器的处理能力。但采用厌氧-兼氧-好氧处理工艺的膜生物反应器，由于工艺流程长，对每个工艺单元的溶氧量等技术参数的要求不同，传统的办法必须单独制造各个工艺单元，造成设备集成度低、结构复杂、占地面积大、生产成本高、不易运输等缺陷。
发明内容
[0004] 为了克服现有的厌氧-兼氧-好氧膜生物反应器设备集成度低、结构复杂、占地面积大、生产成本高等不足，本实用新型提供一种一体化兼氧MBR膜生物反应器，该反应器将兼氧和好氧单元有机组合成一个单元，不仅解决了设备集成的问题，在污水处理效果上面也有很大的进步。
[0005] 本实用新型解决其技术问题所采用的技术方案是:一种一体化兼氧MBR膜生物反应器，主体由厌氧池和兼氧池构成，兼氧池具备兼氧和好氧的功能。所述厌氧池由改进型上流式厌氧污泥床反应器构成，结构简单，容积负荷率高，污水在厌氧池内的水力停留时间短，大大缩小反应器容积。
[0006] 所述兼氧池具备兼氧和好氧的功能，兼氧池内布置球形悬浮填料。采用浸没结合方式，将中空纤维膜组件置于兼氧池中，以减小膜生物反应器体积。并对膜组件底部进行射流曝气。射流曝气形成的气水混合液一方面可以加速中空纤维膜扰动，另一方面可以在膜表面形成剪切力，吹扫膜表面沉积的污泥颗粒，两方面协同作用可有效控制膜污染。膜组件外部加格栅网罩，以防球形悬浮填料损伤中空纤维膜组件。兼氧池进水方向与射流曝气方向为同一旋转方向，以在兼氧池内形成水力循环，搅动球形悬浮填料在好氧-兼氧环境下不断循环。整个兼氧池中，膜组件及膜组件上方为好氧区，其余部分为兼氧区，从厌氧池进入的污水先经过兼氧区，然后经过好氧区，再由膜组件抽吸过滤，最后达标出水。
[0007] 本实用新型的有益效果是，在达到厌氧-兼氧-好氧处理工艺出水水质的同时，设备整体集成度高，结构简单，占地面积小，生产成本低。
附图说明
[0008] 下面结合附图例对本实用新型一体化生物流化床与生物滤池复合反应器进一步说明。
[0009] 附图1为一体化生物流化床与生物滤池复合反应器
[0010] 其中厌氧池，1-1进水管，1-2斜板，1-3透气帽，1-4厌氧池出水管，2兼氧池，2-1兼氧池进水管，2-2球形悬浮填料，2-3中空纤维膜组件，2-4潜水泵，2_5射流器，2-6格栅网罩，2-7抽吸泵。
[0011] 污水首先进入厌氧池，通过厌氧处理后进入兼氧池，反应后的污水通过中空纤维膜的微滤作用后，达标排放或回用。
具体实施方式
[0012] 一体化兼氧MBR膜生物反应器工作时，污水由进水管(1-1)引入厌氧池(I)底部，水流经由斜板(1-2)导流后，较为均匀的分布在池底。颗粒污泥(污泥絮体)在上升的水流和气泡作用下处于悬浮状态，厌氧池下部是浓度较高的污泥，上部是浓度较低的悬浮污泥。有机物在上部转化为甲烷和二氧化碳气体，气体由透气帽(1-3)外排，液体由厌氧池出水管(1-4)排出。厌氧池出水管(1-4)入口口向上，且向上高度不低于100毫米，以防气体进入。
[0013] 经厌氧处理后的污水由兼氧池进水管(2-1)进入兼氧池(2)，兼氧池内设置球形悬浮填料(2-2)、中空纤维膜组件(2-3)、潜水泵(2-4)、射流器(2-5)、格栅网罩(2-6)，潜水泵(2-4)与射流器(2-5)组成的射流曝气系统对准中空纤维膜组件(2-3)底部，射流曝气系统喷出的气水混合液一方面可以加速中空纤维膜扰动，另一方面可以在膜表面形成剪切力，吹扫膜表面沉积的污泥颗粒，两方面协同控制膜污染。中空纤维膜组件(2-3)外部加格栅网罩(2-6)，以防球形悬浮填料(2-2)损伤中空纤维膜组件(2-3)。兼氧池进水方向与射流曝气方向为同一旋转方向，且中空纤维膜组件(2-3)及其外部的格栅网罩(2-3)位于兼氧池(2)中间，污水便在兼氧池(2)内形成水力循环，搅动球形悬浮填料(2-3)在好氧-兼氧环境下不断循环。整个兼氧池(2)中，中空纤维膜组件(2-3)及其上方为好氧区，其余部分为兼氧区，兼氧区大于好氧区，兼氧菌为主故称为兼氧池。兼氧区可以为厌氧出水进入后续好氧处理前增加废水的溶解氧，去除废水中的厌氧产物，减轻其对后续好氧处理的抑制影响。从厌氧池(I)进入的污水先经过兼氧区，然后经过好氧区，再在抽吸泵(2-7)的抽吸作用下，经由中空纤维膜组件(2-3)进行微滤。最后达标出水。
Claims (3)
1.种一体化兼氧MBR膜生物反应器，包括厌氧池(I)、厌氧池出水管(1-4)、兼氧池进水管(2-1)兼氧池(2)，其特征在于:中空纤维膜组件(2-3)外部加格栅网罩(2-6)，将中空纤维膜与防球形悬浮填料隔开。
2.根据权利要求1所述的一体化兼氧MBR膜生物反应器，其特征在于:厌氧池出水管(1-4)入口 口向上，且向上高度不低于100毫米。
3.根据权利要求1所述的一体化兼氧MBR膜生物反应器，其特征在于:兼氧池进水管(2-1)进水方向与射流曝气方向为同一旋转方向。
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082438A (zh) * | 2016-06-30 | 2016-11-09 | 上海立泉环境科技有限公司 | 一种水处理系统 |
| CN106957107A (zh) * | 2016-12-31 | 2017-07-18 | 嘉兴里仁环保科技有限公司 | 采用mbr膜组件的污水处理系统 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106082438A (zh) * | 2016-06-30 | 2016-11-09 | 上海立泉环境科技有限公司 | 一种水处理系统 |
| CN106082438B (zh) * | 2016-06-30 | 2020-02-14 | 上海立泉环境科技有限公司 | 一种水处理系统 |
| CN106957107A (zh) * | 2016-12-31 | 2017-07-18 | 嘉兴里仁环保科技有限公司 | 采用mbr膜组件的污水处理系统 |
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