CN201292263Y - Vertical flow type aerobic gas float filter chamber - Google Patents
Vertical flow type aerobic gas float filter chamber Download PDFInfo
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- CN201292263Y CN201292263Y CNU2008201242578U CN200820124257U CN201292263Y CN 201292263 Y CN201292263 Y CN 201292263Y CN U2008201242578 U CNU2008201242578 U CN U2008201242578U CN 200820124257 U CN200820124257 U CN 200820124257U CN 201292263 Y CN201292263 Y CN 201292263Y
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Abstract
竖流式好气浮滤池属于一种水处理装置。本实用新型特征在于:进水管、溶气回流水管固定在该滤池底部,在溶气回流水管的末端安装溶气释放器,该滤池顶部设置浮渣槽,在气浮分离区下部设置反洗废水槽,在滤料层底部埋设穿孔布气管和集水管,其中穿孔布气管与曝气、反洗气管连接,集水管与出水管及反洗进水管连接。该装置将物理处理(气浮)和生物处理(好气滤池)结合在一起,组成一体化装置。气浮可将密度接近于水的污泥碎片、胶体颗粒、藻类等物质进一步去除,同时气浮出水中高溶解氧为好气滤池提供生物需氧,好气滤池对污染物质起到物理截留、吸附和生物降解的功能,从而更进一步的净化水质。
The vertical flow air flotation filter belongs to a water treatment device. The utility model is characterized in that: the water inlet pipe and the dissolved air return pipe are fixed at the bottom of the filter, a dissolved air releaser is installed at the end of the dissolved air return pipe, a scum tank is arranged on the top of the filter, and a reverse filter is arranged at the lower part of the air flotation separation area. In the waste water tank, perforated air distribution pipes and water collection pipes are buried at the bottom of the filter material layer. The perforated air distribution pipes are connected with aeration and backwash air pipes, and the water collection pipes are connected with outlet pipes and backwash water inlet pipes. The device combines physical treatment (air flotation) and biological treatment (good air filter) to form an integrated device. Air flotation can further remove sludge fragments, colloidal particles, algae and other substances with a density close to water. At the same time, high dissolved oxygen in the water produced by air flotation provides biological oxygen demand for the aerobic filter. The aerobic filter physically intercepts pollutants, The function of adsorption and biodegradation, so as to further purify the water quality.
Description
技术领域 technical field
本实用新型属于一种水处理装置,涉及水源水处理和污水深度处理领域。The utility model belongs to a water treatment device and relates to the fields of water source water treatment and sewage advanced treatment.
背景技术 Background technique
目前,污水深度处理和水源水的处理一般采用混凝+沉淀+过滤常规工艺,该工艺虽然可以有效去除水中的悬浮物、BOD、COD等污染物质,但出水中的氮等营养物和藻类等指标不能满足相应水质标准,而且工艺占地面积大,管理复杂。At present, the advanced treatment of sewage and water source water generally adopt the conventional process of coagulation + sedimentation + filtration. Although this process can effectively remove suspended solids, BOD, COD and other pollutants in the water, nutrients such as nitrogen and algae in the effluent The indicators cannot meet the corresponding water quality standards, and the process occupies a large area and the management is complicated.
实用新型内容 Utility model content
本实用新型的目的在于克服常规工艺的缺点,提供一种新型的水处理装置。该装置将物理处理(气浮)和生物处理(好气滤池)结合在一起,组成一体化装置。气浮可将密度接近于水的污泥碎片、胶体颗粒、藻类等物质进一步去除,同时气浮出水中高溶解氧为好气滤池提供生物需氧,好气滤池对污染物质起到物理截留、吸附和生物降解的功能,从而更进一步的净化水质。The purpose of the utility model is to overcome the shortcomings of the conventional technology and provide a new type of water treatment device. The device combines physical treatment (air flotation) and biological treatment (good air filter) to form an integrated device. Air flotation can further remove sludge fragments, colloidal particles, algae and other substances with a density close to water. At the same time, high dissolved oxygen in the water produced by air flotation provides biological oxygen demand for the aerobic filter. The aerobic filter physically intercepts pollutants, The function of adsorption and biodegradation, so as to further purify the water quality.
本实用新型的技术方案如下:The technical scheme of the utility model is as follows:
竖流式好气浮滤池,它涉及一种浮滤池结构的改进,是在传统的平流式浮滤池的基础上改进成竖流式的同时增加曝气装置,提高生物处理功能。The vertical flow type air flotation filter relates to an improvement of the structure of the floating filter, which is based on the traditional flat flow floating filter and is improved into a vertical flow type while adding an aeration device to improve the biological treatment function.
本实用新型竖流式好气浮滤池,其特征在于:进水管1、溶气回流水管2固定在滤池底部,在溶气回流水管2的末端安装溶气释放器8,滤池顶部设置浮渣槽6,在气浮分离区12下部设置反洗废水槽7,在滤料层13底部埋设穿孔布气管9和集水管10,其中穿孔布气管9和曝气、反洗气管5连接,集水管10和出水管3及反洗进水管4连接。The vertical flow type air flotation filter of the utility model is characterized in that: the
本装置与现有水处理装置相比有以下优点:Compared with the existing water treatment device, this device has the following advantages:
1、本装置采用的气浮池与沉淀池相比,易于去除二级出水中的悬浮污泥碎片、胶体颗粒以及较难混凝沉淀的藻类物质,同时还向出水中溶气充氧,利于后续好气滤池中的生化反应。1. Compared with the sedimentation tank, the air flotation tank used in this device is easy to remove suspended sludge fragments, colloidal particles and algae substances that are difficult to coagulate and settle in the secondary effluent, and at the same time, dissolve air and oxygenate the effluent, which is beneficial to the follow-up Biochemical reactions in an aerobic filter.
2、本装置采用好气滤池类似于曝气生物滤池,但好气滤池更强调过滤作用,同时在保持普通快滤池原有过滤除浊功能的前提下,增加曝气装置,强化其生物作用,增强滤池对有机物和氨氮等指标的去除效果。2. This device adopts an aerated filter similar to the aerated biological filter, but the aerated filter emphasizes the filtering effect. At the same time, on the premise of maintaining the original filtration and turbidity removal function of the ordinary fast filter, an aeration device is added to strengthen its biological Function, enhance the removal effect of the filter on organic matter and ammonia nitrogen and other indicators.
3、本装置采用竖流式与平流式相比,表面负荷高,占地面积小,刮渣设备对分离区影响小,出水质量高。3. Compared with the vertical flow type, this device adopts vertical flow type, which has high surface load and small floor space. The slag scraping equipment has little influence on the separation area, and the effluent quality is high.
4、气浮池和好气滤池结合为一体,设计合理,结构紧凑,方便管理和使用。4. The air flotation tank and the good air filter are combined into one, with reasonable design, compact structure, and convenient management and use.
附图说明 Description of drawings
图1为本实用新型结构图。Fig. 1 is a structural diagram of the utility model.
具体实施方式 Detailed ways
具体操作如下:The specific operation is as follows:
1、气浮过滤过程:进水管1来自絮凝反应的出水,溶气回流水管2来自浮滤池的出水通过气液混合泵溶气后的溶气水(溶气压力392kPa,回流比40%),二者一同从池底进入气浮接触区11,上升流速为11mm/S。絮凝后的絮体和溶气水通过释放器8释出的气泡碰撞接触形成气泡-絮粒结合体,二者上升至气浮分离区12进行分离,分离区下降流速为1.4mm/S,浮渣溢入浮渣槽6排出,气浮出水通过滤池的滤料层13,滤速为4m/h,在滤料层有物理截留、吸附作用,同时气浮出水中的高溶解氧为生物降解提供有氧环境,硝化反应不足的氧气由曝气管5补充,经穿孔布气管9均匀分布在滤层中,曝气量控制在100L/h,最后出水由集水管10收集经出水管3流出。1. Air flotation filtration process:
2、气浮滤池的反洗过程:当滤池最大水头损失超过1m,滤池过滤周期结束,需要进行反洗来保证装置的正常出水。反洗过程采用气水联合反洗:反洗气管5来自曝气系统,反洗水管4来自滤后水加压输送或由高位水箱提供,反洗废水经废水槽7排出。反冲洗参数为:单独气冲强度11.1L/m2·s,冲洗3min;联合气冲强度11.1L/m2·s,水冲强度4.5L/m2·s,冲洗6min;水漂洗强度8.9L/m2·s,漂洗时间5min。2. The backwashing process of the air flotation filter: When the maximum water head loss of the filter exceeds 1m, the filtration cycle of the filter is over, and backwashing is required to ensure the normal water discharge of the device. The backwashing process adopts air-water combined backwashing: the
从表1中看出,通过竖流式好气浮滤池一体化装置,二级出水水质得到大幅提高,除细菌指标需要增加消毒处理外,其它各项指标达到了再生水水质指标。It can be seen from Table 1 that through the integrated device of the vertical flow air flotation filter, the water quality of the secondary effluent has been greatly improved. Except for the bacteria index that needs to be disinfected, other indicators have reached the water quality index of the reclaimed water.
污水厂二级出水及经过竖流式好气浮滤池处理后出水水质与去除率情况如下表1:The water quality and removal rate of the secondary effluent of the sewage plant and the effluent treated by the vertical flow air flotation filter are shown in Table 1:
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201242578U CN201292263Y (en) | 2008-12-05 | 2008-12-05 | Vertical flow type aerobic gas float filter chamber |
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| CNU2008201242578U CN201292263Y (en) | 2008-12-05 | 2008-12-05 | Vertical flow type aerobic gas float filter chamber |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101928082A (en) * | 2010-09-16 | 2010-12-29 | 江苏新龙鼎环保成套工程有限公司 | Vertical-flow air flotation device with secondary filtering |
| CN101948196A (en) * | 2010-09-16 | 2011-01-19 | 江苏新龙鼎环保成套工程有限公司 | Cross flow air floating device with secondary filtration |
| CN101948156A (en) * | 2010-09-16 | 2011-01-19 | 江苏新龙鼎环保成套工程有限公司 | Electrocoagulation vertical air flotation device based on electrolytic reaction principle |
| CN103011509A (en) * | 2012-12-15 | 2013-04-03 | 华北水利水电学院 | Floatation/filtration-integrated polluted water advanced treatment device and method |
| CN103539318A (en) * | 2013-10-31 | 2014-01-29 | 福州城建设计研究院有限公司 | Air flotation biological filter tank integrated equipment and control method thereof |
| CN106745601A (en) * | 2016-12-19 | 2017-05-31 | 芜湖万向新元环保科技有限公司 | One kind flocculation aeration tank |
| CN107759035A (en) * | 2017-12-06 | 2018-03-06 | 广州鹏凯环境科技股份有限公司 | A kind of air supporting combination BAF integration apparatus and sewage treatment process |
| CN108218098A (en) * | 2016-12-13 | 2018-06-29 | 黑龙江吉纳森生物工程股份有限公司 | A kind of biological reinforced processing unit of oily wastewater |
| CN111777271A (en) * | 2020-07-08 | 2020-10-16 | 武汉凯迪电力环保有限公司 | A water purification device |
-
2008
- 2008-12-05 CN CNU2008201242578U patent/CN201292263Y/en not_active Expired - Fee Related
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101928082A (en) * | 2010-09-16 | 2010-12-29 | 江苏新龙鼎环保成套工程有限公司 | Vertical-flow air flotation device with secondary filtering |
| CN101948196A (en) * | 2010-09-16 | 2011-01-19 | 江苏新龙鼎环保成套工程有限公司 | Cross flow air floating device with secondary filtration |
| CN101948156A (en) * | 2010-09-16 | 2011-01-19 | 江苏新龙鼎环保成套工程有限公司 | Electrocoagulation vertical air flotation device based on electrolytic reaction principle |
| CN101948196B (en) * | 2010-09-16 | 2013-04-10 | 江苏新龙鼎环保成套工程有限公司 | Cross flow air floating device with secondary filtration |
| CN103011509A (en) * | 2012-12-15 | 2013-04-03 | 华北水利水电学院 | Floatation/filtration-integrated polluted water advanced treatment device and method |
| CN103539318A (en) * | 2013-10-31 | 2014-01-29 | 福州城建设计研究院有限公司 | Air flotation biological filter tank integrated equipment and control method thereof |
| CN108218098A (en) * | 2016-12-13 | 2018-06-29 | 黑龙江吉纳森生物工程股份有限公司 | A kind of biological reinforced processing unit of oily wastewater |
| CN106745601A (en) * | 2016-12-19 | 2017-05-31 | 芜湖万向新元环保科技有限公司 | One kind flocculation aeration tank |
| CN107759035A (en) * | 2017-12-06 | 2018-03-06 | 广州鹏凯环境科技股份有限公司 | A kind of air supporting combination BAF integration apparatus and sewage treatment process |
| CN111777271A (en) * | 2020-07-08 | 2020-10-16 | 武汉凯迪电力环保有限公司 | A water purification device |
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Granted publication date: 20090819 Termination date: 20121205 |