CN203754501U - 内置缺氧曝气滤池 - Google Patents
内置缺氧曝气滤池 Download PDFInfo
- Publication number
- CN203754501U CN203754501U CN201420124600.4U CN201420124600U CN203754501U CN 203754501 U CN203754501 U CN 203754501U CN 201420124600 U CN201420124600 U CN 201420124600U CN 203754501 U CN203754501 U CN 203754501U
- Authority
- CN
- China
- Prior art keywords
- aeration
- aeration tank
- anoxic
- flushing
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000005273 aeration Methods 0.000 claims abstract description 83
- 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 claims abstract description 50
- 238000011010 flushing procedure Methods 0.000 claims abstract description 44
- 238000009826 distribution Methods 0.000 claims abstract description 42
- 239000010865 sewage Substances 0.000 claims abstract description 40
- 239000007787 solid Substances 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims description 24
- 238000000034 method Methods 0.000 claims description 24
- 239000002245 particle Substances 0.000 claims description 6
- 230000002906 microbiologic Effects 0.000 claims description 4
- 230000011218 segmentation Effects 0.000 claims description 2
- 239000007789 gas Substances 0.000 abstract description 27
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 9
- 239000010802 sludge Substances 0.000 abstract description 9
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 6
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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- 244000005700 microbiome Species 0.000 description 7
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- 238000006396 nitration reaction Methods 0.000 description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group 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[N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 2
- ABLZXFCXXLZCGV-UHFFFAOYSA-N phosphorous acid Chemical compound 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Abstract
本实用新型公开一种内置缺氧曝气滤池包括曝气池、提升泵和吸水井，曝气池底部与吸水井底部通过提升泵连接，出水口设置在曝气池顶部堰口处；曝气池顶部堰口下方设置反冲水出水管道，反冲水出水管道上设有支管连接吸水井；曝气池内设有固体颗粒填充物和曝气、水系统，曝气曝水系统设置在固体颗粒填充物内，污水自下进入生物曝气滤池，经过缺氧段，充分进行反硝化反应，使污水中氮、磷含量降低。经缺氧段处理后污水再流至曝气布气系统之上后即进入好氧段，使污水中的有机物充分得到处理，因此能有效提高单位面积的处理能力，减少土地使用面积。减少了污泥产量，延长了污水处理周期，减少了反冲洗所需用水量，使得投资运行费用大幅降低。
Description
内置缺氧曝气滤池
技术领域
[0001] 本实用新型涉及一种废水处理装置，特别涉及一种内置缺氧曝气滤池。
背景技术
[0002] 活性污泥法和曝气生物滤池处理技术被广泛应用于各种工业污水、市政生活污水的处理和江河湖泊环境污水的治理，尤其是对传统方法无法处理的高浓度有机污水和高氨氮污水有着独特的处理效果，目前已在石油、化工、皮革、日化、造纸及城市生活污水等诸多类型的污水处理中成熟应用。活性污泥法+曝气生物滤池处理技术可广泛适用于各种工业污水、市政生活污水的处理和江河湖泊环境污水的治理，尤其是对传统方法无法处理的高浓度有机污水和高氨氮污水有独特的处理效果，填补了国内外用生化法处理高浓度有机污水和高氨氮污水的空白。目前已在石油、石化、化工、皮革、焦化(煤气化)、食品、酿造、日化、印染、生物制药、造纸及城市生活污水等诸多类型的污水处理中成功应用。活性污泥法+曝气生物滤池处理技术是当前污水处理技术的发展方向。通过一定的技术手段，让固定的微生物附着在载体上，使微生物固着生长，同时加入活性污泥，有利于提高微生物的数量，提高系统处理能力和适应性，缩短处理时间，降低处理成本。
[0003] 活性污泥法和曝气生物滤池法都存在一个污水处理周期，在这个周期末会因为污泥或者生物膜脱落累积等原因导致过滤水头损失加大、出水水质逐渐变差等现象，这时需要对曝气池进行反冲洗，反冲洗后滤料中截留的悬浮物及老化的生物膜随反冲洗水带出曝气池，使曝气池恢复到正常生产处理状态，如果不能及时进行反冲洗，极有可能导致处理设备堵塞、设备无法正常运行出水水质严重不达标等问题。
[0004] 因此曝气池的反冲洗是曝气池运行环节中必不可少的环节，曝气池反冲洗通过配备的反冲洗气系统和反冲洗水系统完成。通过空气单独擦洗，然后气水联合冲洗，最后进行水单独冲洗三个步骤，在现行反冲洗过程中为保证反冲洗效果，需水量很大。
[0005] 在现阶段使用的微生物包括好氧性和厌氧性两种，其根据处理污水特性不同所需处理环境也不一样，一般都是分开使用，但都存在同一个问题，为保证处理量，占地面积都很大。
实用新型内容
[0006] 本实用新型的目的在于提供一种内置缺氧曝气滤池减少反冲洗用水量、将好氧性和厌氧性微生物同时使用，并且能大幅减少土地使用和工程投资。
[0007] 为了达到上述目的，本实用新型提供了一种内置缺氧曝气滤池包括曝气池、提升泵和吸水井，曝气池底部与吸水井底部通过提升泵连接，出水口设置在曝气池顶部堰口处，待处理污水由吸水井流向曝气池；曝气池顶部堰口下方设置反冲水出水管道，反冲水出水管道上设有支管连接吸水井，部分反冲水由曝气池流向吸水井；所述曝气池内设有固体颗粒填充物和曝气、水系统，曝气曝水系统设置在固体颗粒填充物内，所述固体颗粒填充物包括设置于曝气池底部的承托层和设置于曝气池中部的滤料层，曝气、水系统包括反冲洗布水系统、反冲洗布气系统和工艺曝气布气系统，所述反冲洗布水系统、反冲洗布气系统和工艺曝气布气系统自下而上依次设置。
[0008] 优选的，所述曝气池自下向上分为缺氧段和好氧段，缺氧段与好氧段由工艺曝气管分段，工作时缺氧段内分布厌氧微生物，好氧段内分布好氧微生物。
[0009] 优选的，所述承托层占曝气池总高的12%~19%，所述滤料层占曝气池总高的45%~55%，余下部分不设填充物。
[0010] 优选的，所述反冲洗布水系统、反冲洗布气系统设置于承托层内，工艺曝气布气系统设置于滤料层内。
[0011] 优选的，所述承托层为装填级鹅卵石，所述滤料粒径3~32_，粒径从小到大自下而上排布。
[0012] 优选的，所述曝气池顶部设有堰口，堰口与水平成45°角。
[0013] 本实用新型的有益效果:
[0014] 本实用新型将曝气布气系统设置于承托层之上的滤料层中，并在曝气布气系统下面到承托层间留有一段缺氧段，缺氧段的高度根据污水中含氮、磷的量，污水中的碳氮比，以及设计要求的污水净化程度确定。
[0015] 污水自下进入生物曝气滤池，经过缺氧段，在厌氧微生物的作用下充分进行反硝化反应，使污水中氮、磷含量降低。经缺氧段处理后污水再流至曝气布气系统之上后即进入好氧段，同时在微 生物的作用下可以使污水中的有机物充分得到处理，因此能有效提高单位面积的处理能力，减少土地使用面积。
[0016] 曝气池由于同时使用好氧性和厌氧性两种微生物，在相同的环境条件下本实用新型C0D、B0D5、SS的平均去除率分别达到62.4%,62.9%,85.8%，与传统工艺的C0D、B0D5、SS的平均去除率51.7%、56.7%、78.1 %相比，效果明显提升，且减少了污泥产量，延长了污水处理周期，减少了反冲洗所需用水量，使得投资运行费用大幅降低。
附图说明
[0017] 图1为本实用新型的结构示意图；
[0018] 其中:1、工艺曝气管，2、好氧段，3、出水口，4、堰口，5、缺氧段，6、承托层，7、提升栗，8、支管,9、反冲洗布气系统,10、吸水井，11、滤料层，12、反冲洗布水系统。
具体实施方式
[0019] 如图1所示,一种内置缺氧曝气滤池包括曝气池、提升泵7和吸水井10，曝气池底部与吸水井10底部通过提升泵7连接，出水口 3设置在曝气池顶部堰口 4处，待处理污水由吸水井流向曝气池；曝气池顶部堰口 4下方设置反冲水出水管道，反冲水出水管道上设有支管8连接吸水井，部分反冲水由曝气池流向吸水井；所述曝气池内设有固体颗粒填充物和曝气、水系统，曝气曝水系统设置在固体颗粒填充物内，所述固体颗粒填充物包括设置于曝气池底部的承托层6和设置于曝气池中部的滤料层11，曝气、水系统包括反冲洗布水系统12、反冲洗布气系统9和工艺曝气布气系统I,所述反冲洗布水系统12、反冲洗布气系统9和工艺曝气布气系统I自下而上依次设置，曝气池自下向上由工艺曝气管分为缺氧段5和好氧段2，工作时缺氧段5内分布厌氧微生物，好氧段2内分布好氧微生物。[0020] 为了使厌氧微生物与好氧微生物有更好的处理效果，在设计时限定承托层6占曝气池总高的12%~19%，所述滤料层11占曝气池总高的45%~55%，余下部分不设填充物，承托层6出于成本和为了缩短反冲洗时间和减少反冲洗所需水量选择为装填级鹅卵石，滤料粒径3~32mm，粒径从小到大自下而上排布。
[0021] 为了取得更好的反冲洗效果，和反冲洗时带出部分厌氧和好氧菌反冲洗布水系统、反冲洗布气系统设置于承托层内，工艺曝气布气系统设置于滤料层内，出水口 3设置在堰口 4处，为了防止水经常性溢出堰口 4设计堰口 4与水平成45°角。
[0022] 以某化工厂实际投入日处理污水3000m3/天的两条生产线平均生产数据为例:
[0023]
[0024] 可以看出，本实用新型与传统技术相比，工程投资节省27.2%，运行费用节省58%，占地面积减少47.6%，管理简单，人员编制减少2/3。产生的污泥量极少，且卫生和景观条件好。
[0025] 在此需要进一步说明的是，该传统工艺为好氧曝气滤池工艺，其反冲洗过程为:(a)气反冲-气反冲强度:1.2m3/m2.min ,历时:4min ；
[0026] (b)气水联合反冲-气反冲强度:1.2m3/m2.ηήη、水反冲强度:0.4m3/m2.ηήη,历
时:5min ；
[0027] (c)水反冲-7jC反冲强度:0.4m3/m2.min,历时:3min。
[0028] 而本实用新型的反冲洗过程为:
[0029] (a)气反冲-反冲强度:1.2m3/m2.min,历时:4min ；
[0030] (b)气水联合反冲-气反冲强度:1.2m3/m2.min、水反冲强度:0.3m3/m2.min,历
时:5min ；
[0031] (c)水反冲-7jC反冲强度:0.3m3/m2.min ,历时:3min。
[0032] 由反冲洗试验的结果可知，内置缺氧曝气滤池和传统工艺相比，达到同样的反冲洗效果，内置缺氧曝气滤池可采用较低的反冲强度，反冲洗的总用水量可比传统工艺的节省约I / 4。
[0033] 本实用新型将曝气布气系统设置于承托层之上的滤料层中，并在曝气布气系统下面到承托层间留有一段缺氧段，缺氧段的高度根据污水中含氮、磷的量，污水中的碳氮比，以及设计要求的污水净化程度确定。
[0034] 污水自下进入生物曝气滤池，经过缺氧段，在厌氧微生物的作用下充分进行反硝化反应，使污水中氮、磷含量降低。经缺氧段处理后污水再流至曝气布气系统之上后即进入好氧段，同时在微生物的作用下可以使污水中的有机物充分得到处理，因此能有效提高单位面积的处理能力，减少土地使用面积。
[0035] 曝气池由于同时使用好氧性和厌氧性两种微生物，在相同的环境条件下本实用新型C0D、B0D5、SS的平均去除率分别达到62.4%,62.9%,85.8%，与传统工艺的C0D、B0D5、SS的平均去除率51.7%、56.7%、78.1 %相比，效果明显提升，且减少了污泥产量，延长了污水处理周期，减少了反冲洗所需用水量，使得投资运行费用大幅降低。
[0036] 以上所述的仅是本实用新型的优选实例。应当指出对于本领域的普通技术人员来说，在本实用新型所提供的技术启示下，作为本领域的公知常识，还可以做出其它等同变型和改进，也应视为本实用新型的保护范围。
Claims (6)
1.一种内置缺氧曝气滤池包括曝气池、提升泵和吸水井，其特征在于:所述曝气池底部与吸水井底部通过提升泵连接，出水口设置在曝气池顶部堰口处，待处理污水由吸水井流向曝气池；曝气池顶部堰口下方设置反冲水出水管道，反冲水出水管道上设有支管连接吸水井，部分反冲水由曝气池流向吸水井；所述曝气池内设有固体颗粒填充物和曝气、水系统，曝气曝水系统设置在固体颗粒填充物内，所述固体颗粒填充物包括设置于曝气池底部的承托层和设置于曝气池中部的滤料层，曝气、水系统包括反冲洗布水系统、反冲洗布气系统和工艺曝气布气系统，所述反冲洗布水系统、反冲洗布气系统和工艺曝气布气系统自下而上依次设置。
2.根据权利要求1所述一种内置缺氧曝气滤池，其特征在于:所述曝气池自下向上分为缺氧段和好氧段，缺氧段与好氧段由工艺曝气管分段，工作时缺氧段内分布厌氧微生物，好氧段内分布好氧微生物。
3.根据权利要求1所述一种内置缺氧曝气滤池，其特征在于:所述承托层占曝气池总高的12%〜19%，所述滤料层占曝气池总高的45%〜55%，余下部分不设填充物。
4.根据权利要求1所述一种内置缺氧曝气滤池，其特征在于:所述反冲洗布水系统、反冲洗布气系统设置于承托层内，工艺曝气布气系统设置于滤料层内。
5.根据权利要求1所述一种内置缺氧曝气滤池，其特征在于:所述承托层为装填级鹅卵石，所述滤料粒径3〜32mm,粒径从小到大自下而上排布。
6.根据权利要求1所述一种内置缺氧曝气滤池，其特征在于:所述曝气池顶部设有堰口，堰口与水平成45°角。
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| CN104118965A (zh) * | 2014-07-03 | 2014-10-29 | 济南大学 | 一种厌氧好氧三维电催化耦合净水系统及净水方法 |
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| CN104118965A (zh) * | 2014-07-03 | 2014-10-29 | 济南大学 | 一种厌氧好氧三维电催化耦合净水系统及净水方法 |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140806 Termination date: 20200319 |