CN204727663U - 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
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- CN204727663U CN204727663U CN201520179637.1U CN201520179637U CN204727663U CN 204727663 U CN204727663 U CN 204727663U CN 201520179637 U CN201520179637 U CN 201520179637U CN 204727663 U CN204727663 U CN 204727663U
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- 239000010865 sewage Substances 0.000 title claims abstract description 46
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- 229910052698 phosphorus Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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Abstract
本实用新型提供了一种一体化高效能污水处理器，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。本实用新型减小了设备面积，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] 本实用新型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] 本实用新型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] 本实用新型采用的技术方案是:
[0012] 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。本实用新型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] 本实用新型的有益效果:
[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DO、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是本实用新型的一种实施例的内部结构俯视示意图。
[0032] 图2是本实用新型的一种实施例的内部结构主视示意图。
[0033] 图3是本实用新型的俯视结构图。
[0034] 图4是本实用新型的第二种实施例的内部结构俯视示意图。
[0035] 图5是本实用新型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实用新型进行进一步说明，但并不将本实用新型局限于这些具体实施方式。本领域技术人员应该认识到，本实用新型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1，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。本实用新型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。
[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] 本实用新型使用时，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，夕卜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 (7)
1.一体化高效能污水处理器，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。
2.如权利要求1所述的一体化高效能污水处理器，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器，其特征在于: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。
4.如权利要求1所述的一体化高效能污水处理器，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。
5.如权利要求4所述的一体化高效能污水处理器，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。
6.如权利要求4所述的一体化高效能污水处理器，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。
7.如权利要求1~6之一所述的一体化高效能污水处理器，其特征在于:所述排水管设置在桶状罐体的上方。
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