CN104773824B - 一体化高效能污水处理器 - Google Patents
一体化高效能污水处理器 Download PDFInfo
- Publication number
- CN104773824B CN104773824B CN201510140032.6A CN201510140032A CN104773824B CN 104773824 B CN104773824 B CN 104773824B CN 201510140032 A CN201510140032 A CN 201510140032A CN 104773824 B CN104773824 B CN 104773824B
- Authority
- CN
- China
- Prior art keywords
- aerobic
- tank
- core
- simplification
- anaerobism
- 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.)
- Active
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 30
- 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 29
- 229920003048 styrene butadiene rubber Polymers 0.000 claims abstract description 23
- 238000000034 method Methods 0.000 claims abstract description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000002156 mixing Methods 0.000 claims description 12
- 238000005276 aerator Methods 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 230000001276 controlling effect Effects 0.000 claims description 3
- 238000005192 partition Methods 0.000 claims description 3
- 239000010802 sludge Substances 0.000 abstract description 17
- 230000000694 effects Effects 0.000 description 12
- 239000007789 gas Substances 0.000 description 4
- 238000011068 load Methods 0.000 description 4
- 238000005842 biochemical reaction Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 230000000284 resting Effects 0.000 description 3
- 238000005273 aeration Methods 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 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 description 2
- 238000000746 purification Methods 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 230000004308 accommodation Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 230000004059 degradation Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances 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 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 238000009428 plumbing Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Abstract
本发明提供了一种一体化高效能污水处理设备，包括一桶状罐体，所述桶状罐体内设有内筒，所述内筒内是一安装有IC厌氧强化处理系统的厌氧区，所述内筒与桶状罐体之间是一设有好氧简化SBR处理系统的好氧区，所述内筒的上方安装有与内筒连通收集沼气的沼气罐，所述IC厌氧强化处理系统的进水管与厂区集水池泵入罐的污水出口连接，所述IC厌氧强化处理系统的出水管与好氧简化SBR处理系统的管道连接，所述好氧简化SBR处理系统包括排水管和排污管，所述排污管与污水池连通。本发明减小了设备面积，全程自动化处理，易于操作。IC厌氧强化处理系统耐浓度变化和水量变化的冲击，好氧简化SBR处理系统，不易出现污泥膨胀现象。
Description
技术领域
[0001 ] 本发明属于污水处理设备领域，涉及一种一体化高效能污水处理器。
背景技术
[0002] 传统的污水处理工艺占地面积大，成本高，处理效率低，污泥产量大，对于高浓度污水处理，负荷不定、水质不稳易发生污泥膨胀，不易运营管理。
[0003] 现有污水处理技术存在以下问题:
[0004] 1、工业废水处理技术水平有限。目前我们对工业废水处理往往是设计院凭设计规范来确定容积负荷，在利用给排水和生活污水处理中的经验来进行工艺确定、设备选型。
[0005] 2、前期方案设计，取样小试，水质波动大，样品往往不具有代表性。
[0006] 3、污水处理建筑物复杂，水泥池占地面积大，成本大。
[0007] 4、进水水量、浓度变化大，冲击负荷大，普通的好氧污泥易发生污泥膨胀，污泥处理效率下降等问题，不易运营。
[0008] 5、污泥产量大，污泥处置费用高。
[0009] 6、对运营人员素质要求高，非专业人员很难运营好污水处理厂(站)。
发明内容
[0010]本发明提供了一种简单易操作，处理效率高，运行稳定的一体化高效能污水处理设备。
[0011 ]本发明采用的技术方案是:
[0012] —体化高效能污水处理设备，其特征在于:包括一桶状罐体，所述桶状罐体内设有内筒，所述内筒内是一安装有IC厌氧强化处理系统的厌氧区，所述内筒与桶状罐体之间是一设有好氧简化SBR处理系统的好氧区，所述内筒的上方安装有与内筒连通收集沼气的沼气罐，所述IC厌氧强化处理系统的进水管与厂区集水池栗入罐的污水出口连接，所述IC厌氧强化处理系统的出水管与好氧简化SBR处理系统的管道连接，所述好氧简化SBR处理系统包括排水管和排污管，所述排污管与污水池连通。本发明将所有设备设置在一个桶状罐体内，减小了设备面积，而且全程自动化处理，易于操作，对运营人员要求低。IC厌氧强化处理系统耐浓度变化和水量变化的冲击，好氧区采用好氧简化SBR处理系统，不易出现污泥膨胀现象。运行效果稳定，污水在理想的静止状态下沉淀，需要时间短、效率高，出水水质好。理想的推流过程使生化反应推动力增大，效率提高，池内厌氧、好氧处于交替状态，净化效果好。
[0013]进一步，所述污水池与IC厌氧强化处理系统的进水管连通。将污水池内的部分污泥回流到厌氧区补充污泥浓度，外排的污泥需要干化处理。
[0014] 进一步，所述IC厌氧强化处理系统包括HDIC布水器，所述HDIC布水器设有两层三相分离器，上层设有挂膜处理层，增强厌氧处理效果。
[0015]进一步，所述内筒与桶状罐体之间通过隔仓板隔成两个半圆的好氧区，每个好氧区内均设有好氧简化SBR处理系统。
[0016]进一步，所述好氧简化SBR处理系统的管道上设有控制进水的电动阀门。电动阀门使用PLC或时控，两个好氧区轮流周期进水。
[0017]进一步，所述好氧简化SBR处理系统包括一设置在桶状罐体底部的射流曝气器，所述射流曝气器外接有好氧混合栗，所述好氧混合栗与排污管连接。射流曝气器的射流水使用好氧混合栗连接，好氧混合栗兼有排泥作用，切换管道阀门可排泥至污泥池。
[0018]进一步，所述排水管设置在桶状罐体的上方。
[0019]本发明的有益效果:
[0020] 1.本设备受厂地面积限制小。
[0021 ] 2.对运营人员要求低，自动控制、易于操作。
[0022] 3.污泥产量低，降低污泥处理成本。
[0023] 4.理想的推流过程使生化反应推动力增大，效率提高，池内厌氧、好氧处于交替状态，净化效果好。
[0024] 5.运行效果稳定，污水在理想的静止状态下沉淀，需要时间短、效率高，出水水质好。
[0025] 6.耐冲击负荷，池内有滞留的处理水，对污水有稀释、缓冲作用，有效抵抗水量和有机污物的冲击。
[0026] 7.工艺过程中的各工序可根据水质、水量进行调整，运行灵活。
[0027] 8.处理设备少，构造简单，便于操作和维护管理。
[0028] 9.反应池内存在D0、B0D5浓度梯度，有效控制活性污泥膨胀。
[0029] 10.脱氮除磷，适当控制运行方式，实现好氧、缺氧、厌氧状态交替，具有良好的脱氣除憐效果。
[0030] 11.工艺流程简单、造价低。主体设备只有一个一体化高效能污水处理器，布置紧凑、占地面积省。
附图说明
[0031 ]图1是本发明的一种实施例的内部结构俯视示意图。
[0032]图2是本发明的一种实施例的内部结构主视示意图。
[0033]图3是本发明的俯视结构图。
[0034]图4是本发明的第二种实施例的内部结构俯视示意图。
[0035]图5是本发明的第二种实施例的内部结构主视示意图。
具体实施方式
[0036]下面结合具体实施例来对本发明进行进一步说明，但并不将本发明局限于这些具体实施方式。本领域技术人员应该认识到，本发明涵盖了权利要求书范围内所可能包括的所有备选方案、改进方案和等效方案。
[0037] 实施例一
[0038]参照图1-3，一体化高效能污水处理设备，包括一桶状罐体I，所述桶状罐体I内设有内筒2，所述内筒2内是一安装有IC厌氧强化处理系统的厌氧区3，所述内筒2与桶状罐体I之间是一设有好氧简化SBR处理系统的好氧区4，所述内筒2的上方安装有与内筒2连通收集沼气的沼气罐5，所述IC厌氧强化处理系统的进水管6与厂区集水池栗入罐的污水出口连接，所述IC厌氧强化处理系统的出水管7与好氧简化SBR处理系统的管道8连接，所述好氧简化SBR处理系统包括排水管9和排污管10，所述排污管10与污水池11连通。本发明将所有设备设置在一个桶状罐体I内，减小了设备面积，而且全程自动化处理，易于操作，对运营人员要求低。厌氧区3的IC厌氧强化处理系统耐浓度变化和水量变化的冲击，好氧区4采用好氧简化SBR处理系统，不易出现污泥膨胀现象。运行效果稳定，污水在理想的静止状态下沉淀，需要时间短、效率高，出水水质好。理想的推流过程使生化反应推动力增大，效率提高，池内厌氧、好氧处于交替状态，净化效果好。
[0039] 本实施例所述IC厌氧强化处理系统包括HDIC布水器，所述HDIC布水器设有两层三相分离器，上层设有挂膜处理层，增强厌氧处理效果。上层三相分离器与下层三相分离器之间是一深度净化反应室，下层三相分离器与内筒底部是一流化床反应室。
[0040]本实施例所述内筒2与桶状罐体I之间通过隔仓板12隔成两个半圆的好氧区4，每个好氧区4内均设有好氧简化SBR处理系统。
[0041 ]本实施例所述好氧简化SBR处理系统的管道8上设有控制进水的电动阀门13。电动阀门13使用PLC或时控，两个好氧区轮流周期进水。
[0042]本实施例所述好氧简化SBR处理系统包括一设置在桶状罐体I底部的射流曝气器14，所述射流曝气器14外接有好氧混合栗15，所述好氧混合栗15与排污管10连接。射流曝气器14的射流水使用好氧混合栗15连接，好氧混合栗15兼有排泥作用，切换管道阀门可排泥至污泥池11。
[0043]本实施例所述排水管10设置在桶状罐体I的上方。
[0044]本发明使用时，污水从厂区集水池栗进入内筒2内，通过HDIC布水器均匀布水，IC厌氧强化处理系统对高浓度污泥中进行厌氧降解，通过三相分离器后，气体进入沼气罐5，收集的沼气可再利用。液体通过出水管进入外层的好氧区4，好氧区4有两个，进入好氧区4的管道也有两个，两个一一对应，每个管道上设一个电动阀门13，阀门使用PLC或时控，两个好氧区轮流周期进水。好氧区4使用射流曝气，射流水使用好氧混合栗15连接，好氧混合栗15兼有排泥作用，切换管道阀门可排泥至污泥池11。污泥池11的污泥可以排出压干处理，部分回流至厌氧区3保证高浓度污泥。厌氧出水到好氧采用穿孔布水，均匀布水在好氧区4。好氧处理后的污水通过顶端出水堰的排水管10排出。
[0045] 实施例二
[0046]参照图4、图5，本实施例与实施例一的不同之处在于所述污水池11与IC厌氧强化处理系统的进水管6连通。将污水池11内的部分污泥回流到厌氧区3补充污泥浓度，外排的污泥需要干化处理。其余结构与功能均与实施例一相同。
Claims (6)
1.一体化高效能污水处理设备，其特征在于:包括一桶状罐体，所述桶状罐体内设有内筒，所述内筒内是一安装有IC厌氧强化处理系统的厌氧区，所述内筒与桶状罐体之间是一设有好氧简化SBR处理系统的好氧区，所述内筒的上方安装有与内筒连通收集沼气的沼气罐，所述IC厌氧强化处理系统的进水管与厂区集水池栗入罐的污水出口连接，所述IC厌氧强化处理系统的出水管与好氧简化SBR处理系统的管道连接，所述好氧简化SBR处理系统包括排水管和排污管，所述排污管与污水池连通，所述IC厌氧强化处理系统包括HDIC布水器，所述HDIC布水器设有两层三相分离器，上层设有挂膜处理层，上层三相分离器与下层三相分离器之间是一深度净化反应室，下层三相分离器与内筒底部是一流化床反应室。
2.如权利要求1所述的一体化高效能污水处理设备，其特征在于:所述污水池与IC厌氧强化处理系统的进水管连通。
3.如权利要求1所述的一体化高效能污水处理设备，其特征在于:所述内筒与桶状罐体之间通过隔仓板隔成两个半圆的好氧区，每个好氧区内均设有好氧简化SBR处理系统。
4.如权利要求3所述的一体化高效能污水处理设备，其特征在于:所述好氧简化SBR处理系统的管道上设有控制进水的电动阀门。
5.如权利要求3所述的一体化高效能污水处理设备，其特征在于:所述好氧简化SBR处理系统包括一设置在桶状罐体底部的射流曝气器，所述射流曝气器外接有好氧混合栗，所述好氧混合栗与排污管连接。
6.如权利要求1〜5之一所述的一体化高效能污水处理设备，其特征在于:所述排水管设置在桶状罐体的上方。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510140032.6A CN104773824B (zh) | 2015-03-27 | 2015-03-27 | 一体化高效能污水处理器 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510140032.6A CN104773824B (zh) | 2015-03-27 | 2015-03-27 | 一体化高效能污水处理器 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104773824A CN104773824A (zh) | 2015-07-15 |
| CN104773824B true CN104773824B (zh) | 2017-03-01 |
Family
ID=53615641
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510140032.6A Active CN104773824B (zh) | 2015-03-27 | 2015-03-27 | 一体化高效能污水处理器 |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104773824B (zh) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203346172U (zh) * | 2013-07-04 | 2013-12-18 | 上海兴怡化工有限公司 | 一种多区式生物反应器 |
| CN204727663U (zh) * | 2015-03-27 | 2015-10-28 | 杭州银江环保科技有限公司 | 一体化高效能污水处理器 |
-
2015
- 2015-03-27 CN CN201510140032.6A patent/CN104773824B/zh active Active
Also Published As
| Publication number | Publication date |
|---|---|
| CN104773824A (zh) | 2015-07-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104710078B (zh) | 地埋式一体化生活污水处理装置及方法 | |
| CN106746351A (zh) | 一种针对农村生活污水的处理系统 | |
| CN202881049U (zh) | 地埋式污水处理设备 | |
| CN104773824B (zh) | 一体化高效能污水处理器 | |
| CN204727663U (zh) | 一体化高效能污水处理器 | |
| CN202011812U (zh) | 一种处理高浓度有机废水一体化设备 | |
| CN203021403U (zh) | 地埋式一体化生活污水处理设备 | |
| CN103880185A (zh) | 一体化a/o/mbbr反应器 | |
| CN204588915U (zh) | 地埋式无动力五格净化槽污水处理设备 | |
| CN103420483B (zh) | 一种批序式污水处理装置 | |
| CN106430814A (zh) | 污水前处理一体化装置 | |
| CN203904069U (zh) | 一体化a/o/mbbr反应器 | |
| CN201240978Y (zh) | 组合式污水就地处理系统 | |
| CN206751597U (zh) | 一种生产橡胶废水处理装置 | |
| CN206417977U (zh) | 一种针对农村生活污水的处理系统 | |
| CN206219303U (zh) | 化粪池污水sbr一体处理装置 | |
| CN101792212B (zh) | 一体化空气提升sbr反应器 | |
| CN205933556U (zh) | 一种高效、集约化城镇污水处理装置 | |
| CN202022825U (zh) | 一种污水处理设施 | |
| CN201458903U (zh) | 一体化生活污水处理设备 | |
| CN202849198U (zh) | 一种地埋式平板膜mbr污水处理装置 | |
| CN205953661U (zh) | 一体化柱式高浓度有机废水处理器 | |
| CN206828314U (zh) | 农村污水一体化处理循环利用设备 | |
| CN101289253A (zh) | 升逆流厌氧滤池 | |
| CN202936251U (zh) | 立体式推流曝气一体化设备 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| C06 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| EXSB | Decision made by sipo to initiate substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Integrated high efficiency sewage treatment unit Effective date of registration: 20201229 Granted publication date: 20170301 Pledgee: Hangzhou High-tech Financing Guarantee Co.,Ltd. Pledgor: HANGZHOU ENJOY SCIENTECH Co.,Ltd. Registration number: Y2020330001329 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20220111 Granted publication date: 20170301 Pledgee: Hangzhou High-tech Financing Guarantee Co.,Ltd. Pledgor: HANGZHOU ENJOY SCIENTECH Co.,Ltd. Registration number: Y2020330001329 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of invention: Integrated high efficiency sewage processor Effective date of registration: 20220112 Granted publication date: 20170301 Pledgee: Hangzhou High-tech Financing Guarantee Co.,Ltd. Pledgor: HANGZHOU ENJOY SCIENTECH Co.,Ltd. Registration number: Y2022330000066 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |