CN201334406Y - 一种用于地表水和污水处理的一体化水处理设备 - Google Patents
一种用于地表水和污水处理的一体化水处理设备 Download PDFInfo
- Publication number
- CN201334406Y CN201334406Y CNU2009201052741U CN200920105274U CN201334406Y CN 201334406 Y CN201334406 Y CN 201334406Y CN U2009201052741 U CNU2009201052741 U CN U2009201052741U CN 200920105274 U CN200920105274 U CN 200920105274U CN 201334406 Y CN201334406 Y CN 201334406Y
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- China
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- water
- dissolving
- integrated
- sewage disposal
- pond
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- 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 - Lifetime
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- 239000000706 filtrate Substances 0.000 description 5
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- 238000005516 engineering process Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound 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- 230000005587 bubbling Effects 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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Abstract
本实用新型的一种用于地表水和污水处理的一体化水处理设备，包括池主体，池主体左端设进水渠，进水渠右侧设快混池，快混池上面设第一搅拌机，快混池在其底部通过隔墙与两个并排的絮凝池连接，每个絮凝池上面均设一个第二搅拌机，每个絮凝池右侧通过导流筒与溶气释放区连接，溶气释放区通过堰墙与两个并排的气浮滤池连接，每个气浮滤池上面均设一台刮渣机，气浮滤池上部为气浮区、下部为过滤区。本实用新型将混凝过程的快混池、絮凝池及气浮滤池集成为一套整体设备，使得结构紧凑、占用空间小，对污水处理效果好。
Description
一种用于地表水和污水处理的一体化水处理设备
技术领域
本实用新型涉及一种水处理设备，尤其涉及一种用于地表水和污水处理的一体化水处理 设备。属于水处理领域。
背景技术
对地表水及污水，如包括生活污水和工业污水的处理工艺和设备有很多种，气浮和滤池 是常见的水处理工艺。气浮法是通过某种方法产生大量的微气泡，使其与废水中密度接近于 水的固体或液体污染物微粒粘附，形成密度小于水的气浮体，在浮力的作用下，上浮至水面 形成浮渣，进行固液或液液分离。过滤一般是指石英砂等粒状滤料层截留水中悬浮杂质，从 而使水获得澄清的工艺过程。但传统的气浮池和滤池有以下几点不足：（l)传统气浮池产生气 泡的大小不均匀、大气泡容易产生搅动，因而出水浊度高。（2)如果滤池的前一工序处理不当， 进入滤池时的悬浮物高，将大大增加滤池的过滤负担，就必然会缩短反冲洗的周期，而频繁 的反冲洗会出现跑砂现象，同时平整、补砂的周期也会频繁，增加了工作负担。（3)气浮池和 滤池的单独建造，两者之间需要进行水力提升，并且占地面积较大、建造成本大大提高。
实用新型内容
本实用新型的目的是克服现有技术的不足，提供一种将混凝过程的快混池、絮凝池及气 浮池、滤池组合为一体化的、用于地表水和污水处理的设备。 本实用新型是通过以下技术方案实现的：
一种用于地表水和污水处理的一体化水处理设备，包括池主体，所述池主体左端设进水 渠，所述进水渠里的污水通过进水管进入快混池，絮凝药液通过药液注入管流入到快混池， 所述进水渠右侧设快混池，所述快混池上面设第一搅拌机，所述快混池在底部连通地通过隔 墙与两个并排的絮凝池连接，所述两个并排的絮凝池之间的壁上设溶气罐，或者将溶气罐设 置在其它地方，如快混池、絮凝池等的上部，每个絮凝池上面均设第二搅拌机，所述每个絮 凝池右侧通过导流筒与溶气释放区连接，所述溶气释放区通过堰墙与两个并排的气浮滤池连 接，所述每个气浮滤池上面均设一台刮渣机。
所述溶气罐上端设溶气罐进气管道、侧下面设溶气罐进水管道。
所述气浮滤池底部右侧设出水管及反冲洗进气管，所述气浮滤池下部(即过滤区内)设有 长柄滤头及气管，反冲洗进气管连接外部的鼓风机，并通过气管为气浮滤池冲气。
3所述气浮滤池上部为气浮区、下部为过滤区。
所述溶气罐通过溶气释放管道与设置在所述溶气释放区内的减压阀连接，减压阀分为两 组，每组10个。
所述出水管与所述溶气罐上的溶气罐进水管道相连接。
所述地表水和污水处理的一体化处理设备可以制做成一体化的成套设备，也可以制做成 土工结构。
本实用新型的一种用于地表水和污水处理的一体化水处理设备相对于现有技术具有如下 有益效果：
1、 本实用新型利用轻质易浮特点进行较好的泥水分离，气浮池工艺能将水中分离出来污 泥的含固率提高到2%以上，现有技术中的固含率一般为1〜1.5%之间；
2、 本实用新型减少排泥水量的消耗量，降低处理厂工艺的自耗水量，节约用水，气浮工 艺分离能将水中悬浮物降至10mg/1以下，出水水质好，特别在冬季低温状态下的泥水分离更 能显示出水水质高的特点；
3、 本实用新型结构紧凑，占地面积小，将气浮池和滤池集成为一体，建设成本低，处理 效率高。应用于给水及污水深度处理，尤其适合面积较小的处理作业场。
附图说明
图l为本实用新型的一种用于地表水和污水处理的一体化水处理设备俯视图； 图2为本实用新型的一种用于地表水和污水处理的一体化水处理设备A-A剖面图。 图3为本实用新型的一种用于地表水和污水处理的一体化水处理设备B-B剖面图。 其中：1-池主体，2-进水渠，3-进水管，4-第一搅拌机，5-溶气罐，6-溶气释放管道，7-快混 池，8-絮凝池，9-第二搅拌机，10-溶气释放区，11-堰墙，12-释放阀，13-长柄滤头，14-气浮 区，15-过滤区，16-穿孔管，17-出水管，18-刮渣机，19-溶气罐进气管道，20-溶气罐进水管 道，21-反冲洗进气管，22-隔墙，23-药液注入管，24-导流筒，25-气浮滤池，26-反冲洗出水 管，27-反冲洗排水槽。
具体实施方式
为了使本领域的一般技术人员能够清楚理解本实用新型的技术方案，现结合附图作进一
步详尽地说明：
本实用新型的一种用于地表水和污水处理的一体化水处理设备，如图1、图2及图3所 示，包括池主体l,池主体1左端设进水渠2，进水渠2与进水管3连接，进水渠2右侧设快混池7，快混池7上面设第一搅拌机4，快混池7在其底部连通地通过隔墙22与两个并排的 絮凝池8连接，两个并排的絮凝池8之间的壁上面设溶气罐5，每个絮凝池8上面均设一个 第二搅拌机9，每个絮凝池8右侧通过导流筒24与溶气释放区10连接，溶气释放区10通过 堰墙11与两个并排的气浮滤池25连接，每个气浮滤池25上面均设一台刮渣机18。 进一步地，溶气罐5上端设溶气罐进气管道19、侧面设溶气罐进水管道20。 进一步地，气浮滤池25底部右侧设出水管17及反冲洗进气管21，气浮滤池25内设有 长柄滤头13及穿孔管16。
进一步地，溶气罐5通过溶气释放管道6与释放阀12连接，释放阀12设置在溶气释放 区10内。
进一步地，气浮滤池25上部为气浮区14、下部为过滤区15。 进一步地，出水管17与溶气罐5上的溶气罐进水管道20相连接。 工作原理：
如图1、图2及图3所示，将现有技术的气浮池（DAF)和滤池（F)叠加在一起，形成 一个气浮滤池的整体，尺寸为（9X5X5)m，每个气浮滤池25为矩形结构，按其作用功能分为 两部分，上部为气浮区14，深度为0.8〜1.0m，下部为用于放置多层滤料的过滤区15，深度 为1.2〜1. 5m。
采用部分回流压力溶气气浮法，将经过滤区15过滤后的净水（产水量的10〜27%)用分 散泵（图中未示)泵入到容积为4m3的溶气罐5，加压0.6〜0.70MPa的压力，同时空压机（图中 未示)通过溶气罐进气管道向溶气罐5内注入压缩空气，溶气罐5内经过加压的溶气水与加压 后的空气在溶气罐5内充分混合溶气，在工作压力下，溶气罐5的水形成过饱和空气水，再 由连接于溶气罐5右侧下面的溶气释放管6道进入气浮滤池25左侧的溶气释放区10，通过 释放阀12减压释放，形成微气泡的混合液越过堰墙11进入气浮滤池25。
当污水自进水渠2经过进水管3与药液注入管23下来的药剂混合后，在快混池7经过 第一搅拌机4的快速搅拌均匀，从隔墙22下部连通处进入絮凝池8，并由第二搅拌机9慢速 搅拌，使絮凝药液与原水混合均匀，形成细小絮花，这些带有小絮花的混合液体通过导流筒 24再进入溶气释放区10，再经过堰墙11进入气浮滤池25，气浮滤池25的上部为气浮区14、 下部为过滤区15，由溶气释放系统释放的微细气泡与絮凝产生的絮体物质合一些细小的颗粒 结合在一起，比重小于1的浮到气浮区14表面，比重大于1的依靠重力下沉到滤料层。气泡 颗粒形成很轻的絮体浮至水面，形成漂浮污泥，在气浮区14表面形成一层污泥层，通过刮泥 机18将污泥去除。处理后的水经过排水管17排放。而一小部份水通过溶气罐进水管道20回 流溶气罐5。根据处理水质水量情况，定期对滤料采用气水反冲洗方式。反冲洗时，先将排水管17 关闭。通过反冲洗进气管21通入空气，进行气洗。气洗完毕，将排水管17打开，进行气水 同时反洗。最后将进气管21关闭，将排水管17打开进行水洗。反冲洗水收集到排水槽27经 反冲洗排水管26排放。
本实用新型的气浮滤池25设置为两个并排的区域，每个区域安装10个DN32专用的高效 释放阀12，两个区域共装20个释放阀12。为防止水流冲击，保证微气泡与颗粒的粘附条件， 释放阀12前的进水流速小于lm/s，释放阀12的出口流速为0. 4〜0. 5ra/s，每个释放阀12的 服务半径O. 3〜1. lm。
本实用新型的将混凝过程的快混池7、絮凝池8和气浮滤池25作为一套整体设备；高压 的溶气罐5的出水通过稳压系统经释放阀12释放后，气泡直径可达到10〜15 u m，大小均匀， 分散性好。而一般的释放阀12释放出的气泡直径在20〜40um左右；放置在过滤区底部的滤 料为石英砂、无烟煤细滤料、砾石骨料，滤料经久耐用，可以连续运行10年，不需要填补滤 料，减少维护。
本实用新型可集成为成套设备，也可以做成土工结构。
Claims (7)
1、一种用于地表水和污水处理的一体化水处理设备，包括池主体(1)，其特征在于，所述池主体(1)左端设进水渠(2)，所述进水渠(2)与进水管(3)连接，所述进水渠(2)右侧设快混池(7)，所述快混池(7)上面设第一搅拌机(4)，所述快混池(7)在其底部连通地通过隔墙(22)与两个并排的絮凝池(8)连接，所述两个并排的絮凝池(8)之间的壁上面设溶气罐(5)，所述每个絮凝池(8)上面均设一个第二搅拌机(9)，所述每个絮凝池(8)右侧通过导流筒(24)与溶气释放区(10)连接，所述溶气释放区(10)通过堰墙(11)与两个并排的气浮滤池(25)连接，所述每个气浮滤池(25)上面均设一台刮渣机(18)。
2、 根据权利要求1所述的一种用于地表水和污水处理的一体化水处理设备，其特征在于， 所述溶气罐(5)顶端设溶气罐进气管道(19)、侧下面设溶气罐进水管道(20)。
3、 根据权利要求1所述的一种用于地表水和污水处理的一体化水处理设备，其特征在于， 所述气浮滤池(25)底部右侧设出水管(17)及反冲洗进气管(21)，所述气浮滤池(25)下部设有长 柄滤头(13)及气管(16)。
4、 根据权利要求1所述的一种用于地表水和污水处理的一体化水处理设备，其特征在于， 所述溶气罐(5)通过溶气释放管道(6)与减压阀(12)连接，所述释放阀(12)设置在溶气释放区(10) 内。
5、 根据权利要求l所述的一种用于地表水和污水处理的一体化处理设备，其特征在于， 所述气浮滤池(25)上部为气浮区(14)、下部为过滤区(15)。
6、 根据权利要求3所述的一种用于地表水和污水处理的一体化处理设备，其特征在于， 所述出水管(17)与所述溶气罐(5)上的溶气罐进水管道(20)相连接。
7、 根据权利要求l所述的一种用于地表水和污水处理的一体化处理设备，其特征在于， 所述地表水和污水处理的一体化处理设备为一体化成套设备或土工结构之一。
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102774922A (zh) * | 2012-08-20 | 2012-11-14 | 宜兴市富陶环境保护设备有限公司 | 气浮装置 |
| CN103951099A (zh) * | 2014-03-28 | 2014-07-30 | 宁波埃克钛能源科技有限公司 | 废水一体化处理装置 |
| CN106039785A (zh) * | 2016-06-29 | 2016-10-26 | 浙江东瓯过滤机制造有限公司 | 一种母液连续过滤自动卸刮渣压干洗涤机 |
| CN106830243A (zh) * | 2017-02-17 | 2017-06-13 | 郭晓辉 | 多功能硅藻精土混凝气浮一体化设备 |
| CN108654154A (zh) * | 2018-06-04 | 2018-10-16 | 广东科学技术职业学院 | 侧向流滤池 |
| CN109621539A (zh) * | 2018-12-29 | 2019-04-16 | 林豪杰 | 阻隔过滤式可吸附悬浮物的v型滤池过滤水头保护装置 |
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| CN102774922A (zh) * | 2012-08-20 | 2012-11-14 | 宜兴市富陶环境保护设备有限公司 | 气浮装置 |
| CN103951099A (zh) * | 2014-03-28 | 2014-07-30 | 宁波埃克钛能源科技有限公司 | 废水一体化处理装置 |
| CN103951099B (zh) * | 2014-03-28 | 2016-01-13 | 宁波埃克钛能源科技有限公司 | 废水一体化处理装置 |
| CN106039785A (zh) * | 2016-06-29 | 2016-10-26 | 浙江东瓯过滤机制造有限公司 | 一种母液连续过滤自动卸刮渣压干洗涤机 |
| CN106039785B (zh) * | 2016-06-29 | 2018-01-05 | 浙江东瓯过滤机制造有限公司 | 一种母液连续过滤自动卸刮渣压干洗涤机 |
| CN106830243A (zh) * | 2017-02-17 | 2017-06-13 | 郭晓辉 | 多功能硅藻精土混凝气浮一体化设备 |
| CN108654154A (zh) * | 2018-06-04 | 2018-10-16 | 广东科学技术职业学院 | 侧向流滤池 |
| CN109621539A (zh) * | 2018-12-29 | 2019-04-16 | 林豪杰 | 阻隔过滤式可吸附悬浮物的v型滤池过滤水头保护装置 |
| CN109621539B (zh) * | 2018-12-29 | 2021-04-06 | 郭素青 | 阻隔过滤式可吸附悬浮物的v型滤池过滤水头保护装置 |
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