CN202223979U - Integrated inclined tube sedimentation tank - Google Patents
Integrated inclined tube sedimentation tank Download PDFInfo
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- CN202223979U CN202223979U CN201120325452.9U CN201120325452U CN202223979U CN 202223979 U CN202223979 U CN 202223979U CN 201120325452 U CN201120325452 U CN 201120325452U CN 202223979 U CN202223979 U CN 202223979U
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- inclined tube
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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
本实用新型涉及一种一体化斜管沉淀池。本实用新型的目的是提供一种集配水、混凝、沉淀和过滤等功能为一体的一体化斜管沉淀池,可增强其抗负荷冲击能力,提高污水处理效率,保证出水的悬浮物浓度能达到设计要求。本实用新型的技术方案是:一体化斜管沉淀池,包括池体,以及分别装在池体相对两个侧壁上部的水平向的进水管和排水管其特征在于:池体内沿水流方向设置两块挡板,将池体依次分为反应区、分离区和过滤区,所述挡板底端伸至池底且高于池底。本实用新型适用于去除污水中的杂质和悬浮物。
The utility model relates to an integrated inclined tube sedimentation tank. The purpose of this utility model is to provide an integrated inclined tube sedimentation tank integrating functions such as water distribution, coagulation, sedimentation and filtration, which can enhance its load impact resistance, improve sewage treatment efficiency, and ensure that the concentration of suspended solids in the effluent can Meet the design requirements. The technical scheme of the utility model is: an integrated inclined tube sedimentation tank, including a tank body, and horizontal water inlet pipes and drain pipes respectively installed on the upper parts of the two side walls of the tank body. Two baffles divide the pool body into a reaction zone, a separation zone and a filtration zone in turn, and the bottom of the baffles extends to the bottom of the pool and is higher than the bottom of the pool. The utility model is suitable for removing impurities and suspended matter in sewage.
Description
技术领域 technical field
本实用新型涉及一种沉淀池,尤其是一种一体化斜管沉淀池。适用于去除污水中的杂质和悬浮物。 The utility model relates to a sedimentation tank, in particular to an integrated inclined tube sedimentation tank. It is suitable for removing impurities and suspended solids in sewage. the
背景技术 Background technique
在采矿选矿、锅炉除尘、砂石骨料人工制取等过程中,常常会产生含有大量悬浮颗粒物的高浊度污水。采用普通斜管沉淀池处理该类污水时,为提高处理效率,往往需采用专设投药池或管道投药的方式投加絮凝剂,且为进一步去除污水中的细小颗粒物,还需在斜管沉淀池后增加过滤池。采用这种独立设置的方式不仅占地面积大,增加工程投资,而且斜管沉淀池对水量水质变化的适应能力较差,在实际工程中难以保证其出水悬浮物浓度能达到设计的要求。 In the process of mining ore dressing, boiler dedusting, and artificial production of sand and gravel aggregates, high-turbidity sewage containing a large amount of suspended particles is often produced. When using ordinary inclined tube sedimentation tanks to treat this type of sewage, in order to improve the treatment efficiency, it is often necessary to add flocculants in the form of special dosing tanks or pipelines, and in order to further remove fine particles in the sewage, sedimentation in inclined tubes is also required. Add a filter pool after the pool. Adopting this independent setting method not only occupies a large area and increases project investment, but also the inclined tube sedimentation tank has poor adaptability to changes in water quantity and water quality, and it is difficult to ensure that the concentration of suspended solids in the effluent can meet the design requirements in actual engineering.
发明内容 Contents of the invention
本实用新型要解决的技术问题是:针对上述存在的问题,提供一种集配水、混凝、沉淀和过滤等功能为一体的一体化斜管沉淀池,可增强其抗负荷冲击能力,提高污水处理效率,保证出水的悬浮物浓度能达到设计要求。 The technical problem to be solved by the utility model is to provide an integrated inclined tube sedimentation tank integrating the functions of water distribution, coagulation, sedimentation and filtration, which can enhance its load impact resistance and improve the quality of sewage. The treatment efficiency ensures that the concentration of suspended solids in the effluent can meet the design requirements. the
本实用新型所采用的技术方案是:一体化斜管沉淀池,包括池体,以及分别装在池体相对两个侧壁上部的水平向的进水管和排水管其特征在于:池体内沿水流方向设置两块挡板,将池体依次分为反应区、分离区和过滤区,所述挡板底端伸至池底且高于池底。 The technical solution adopted by the utility model is: an integrated inclined tube sedimentation tank, including a tank body, and horizontal water inlet pipes and drain pipes respectively installed on the upper parts of the two side walls of the tank body. Two baffles are arranged in the direction, and the pool body is divided into a reaction area, a separation area and a filtration area in turn, and the bottom of the baffles extends to the bottom of the pool and is higher than the bottom of the pool.
所述反应区顶部垂直安装有投药管和搅拌机。 A dosing pipe and a stirrer are installed vertically on the top of the reaction zone.
所述分离区内设有连接池底的开孔挡板,该开孔挡板上均匀布置若干圆孔。 A perforated baffle plate connected to the bottom of the pool is provided in the separation area, and several round holes are evenly arranged on the perforated baffle plate.
所述过滤区中下部为沉淀区,沉淀区上方设有斜管填料,斜管填料上面为纤维球滤层,纤维球滤层上面为清水区,清水区上方是位于过滤区上部的堰槽,堰槽与排水管连通,过滤区的底部为污泥区。 The middle and lower part of the filtration zone is a sedimentation zone, and above the sedimentation zone, there is an inclined tube packing, above which is a fiber ball filter layer, and above the fiber ball filter layer is a clean water zone, and above the clean water zone is a weir groove located at the upper part of the filter zone. The weir groove is connected with the drainage pipe, and the bottom of the filter area is the sludge area.
所述纤维球滤层由纤维丝扎结而成,滤层的厚度约200~500mm。 The fiber ball filter layer is formed by binding fiber filaments, and the thickness of the filter layer is about 200-500mm.
所述斜管填料下方设有冲洗气管,该冲洗气管一端连接池体外的高压气泵,所述冲洗气管直径为50~80mm。 A flushing air pipe is provided below the inclined tube filler, and one end of the flushing air pipe is connected to a high-pressure air pump outside the body of the pool. The diameter of the flushing air pipe is 50-80mm.
所述池体底部边缘到中心的倾角为50°~60°。 The inclination angle from the bottom edge of the pool body to the center is 50°-60°.
所述沉淀区内、沿池底布设污泥管,该污泥管一端伸至池底中心,另一端伸出池体。 In the sedimentation area, a sludge pipe is arranged along the bottom of the pool. One end of the sludge pipe extends to the center of the bottom of the pool, and the other end extends out of the pool body.
本实用新型的有益效果是:所述池体在进水口处投加絮凝剂并设置搅拌机进行搅拌,使废水和药剂充分接触、混合,提高了沉淀效果,并利用挡板降低污水的过流速度,消去部分动能;同时,在斜管填料上设置纤维球过滤层,使经沉淀处理后的废水中含有的残余细小悬浮颗粒物得以进一步去除。 The beneficial effects of the utility model are: the pool body is added flocculant at the water inlet and agitator is set for stirring, so that the wastewater and the medicament are fully contacted and mixed, the sedimentation effect is improved, and the flow rate of the sewage is reduced by using the baffle , to eliminate part of the kinetic energy; at the same time, a fiber ball filter layer is set on the inclined tube filler to further remove the residual fine suspended particles contained in the wastewater after sedimentation treatment.
因此,本实用新型能集配水、混凝、沉淀和过滤等功能为一体,一池起到多池的作用和效果,占地面积小,降低了工程投资,并提高了污水处理效率和沉淀池对水量水质变化的适应能力。 Therefore, the utility model can integrate functions such as water distribution, coagulation, sedimentation and filtration, and one pool plays the role and effect of multiple pools, occupies a small area, reduces engineering investment, and improves sewage treatment efficiency and sedimentation tank Adaptability to changes in water quantity and quality.
附图说明 Description of drawings
图1为本实用新型的结构布置图。 Figure 1 is a structural layout diagram of the utility model.
具体实施方式 Detailed ways
如图1所示,本实施例包括池体1,在池体1相对两个侧壁上部水平向布置进水管2和排水管3。池体1池底呈漏斗形,池体底部边缘到中心的倾角为50°~60°。所述池体1内沿水流方向设置两块挡板4,将池体1依次分为反应区5、分离区6和过滤区。挡板4伸至池体1池底且不与池底接触,污水可从挡板4下方流通。 As shown in FIG. 1 , this embodiment includes a pool body 1 , and a water inlet pipe 2 and a drain pipe 3 are arranged horizontally on the upper part of the opposite two side walls of the pool body 1 . The bottom of the pool body 1 is funnel-shaped, and the inclination angle from the bottom edge of the pool body to the center is 50°~60°. Two baffles 4 are arranged in the pool body 1 along the water flow direction, and the pool body 1 is divided into a reaction zone 5, a separation zone 6 and a filtration zone in turn. The baffle plate 4 extends to the bottom of the pool body 1 without contacting with the bottom of the pool, and the sewage can flow from below the baffle plate 4 .
所述反应区5顶部垂直安装有投药管9和搅拌机10。 A dosing tube 9 and a mixer 10 are installed vertically on the top of the reaction zone 5 .
所述分离区6内置有开孔挡板11,该开孔挡板连接池底,其上均匀开有若干圆孔11-1。污水可从开孔挡板11的上方和圆孔11-1中流通,开孔挡板起阻挡和消能作用。 The separation area 6 is built with a perforated baffle 11, which is connected to the bottom of the pool and has a number of round holes 11-1 evenly opened thereon. Sewage can flow through the top of the perforated baffle 11 and the circular hole 11-1, and the perforated baffle acts as a barrier and dissipates energy.
所述过滤区占池体1的一半左右,该过滤区的中下部为沉淀区7,所述沉淀区7上方依次设有斜管填料12、纤维球滤层14、清水区15和堰槽16,所述排水管3与堰槽16连接。在斜管填料12的下方设有冲洗气管17,冲洗气管17一端连接池体1外的高压气泵,该冲洗气管17可定期对斜管填料12和纤维球滤层14进行冲洗,避免出现堵塞。过滤区的底部为污泥区8。
The filter area accounts for about half of the pool body 1, and the middle and lower part of the filter area is the
过滤区底部设置污泥管13,该污泥管13一端通入污泥区8(即池底中心),另一端伸出池体1。 A sludge pipe 13 is arranged at the bottom of the filter area. One end of the sludge pipe 13 leads into the sludge area 8 (that is, the center of the pool bottom), and the other end extends out of the pool body 1 .
本实用新型的处理方式是:污水从进水管2进入反应区5内,在搅拌机10的作用下污水与絮凝剂充分接触、混合。从反应区5底部流出的污水进入分离区6,在开孔挡板11阻挡作用下过流速度有所降低,消去部分动能,部分悬浮颗粒得以去除。沉淀区7上方设置有斜管填料12,利用水和颗粒速度差的不同,悬浮颗粒开始从污水中分离,进入污泥区8,并通过污泥管13排出池体外。纤维球滤层14设置于斜管填料12的上方,通过拦截、吸附、筛滤等作用将废水中残余的细小颗粒进一步去除。当清水区15中的水达到一定高度,通过堰槽16由排水管3排出。
The treatment method of the utility model is: the sewage enters the reaction zone 5 from the water inlet pipe 2, and under the action of the mixer 10, the sewage and the flocculant fully contact and mix. The sewage flowing out from the bottom of the reaction zone 5 enters the separation zone 6, and under the blocking effect of the perforated baffle plate 11, the flow velocity is reduced, part of the kinetic energy is eliminated, and part of the suspended particles are removed. An inclined tube filler 12 is arranged above the
Claims (8)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120325452.9U CN202223979U (en) | 2011-09-01 | 2011-09-01 | Integrated inclined tube sedimentation tank |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201120325452.9U CN202223979U (en) | 2011-09-01 | 2011-09-01 | Integrated inclined tube sedimentation tank |
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| CN202223979U true CN202223979U (en) | 2012-05-23 |
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| CN201120325452.9U Expired - Lifetime CN202223979U (en) | 2011-09-01 | 2011-09-01 | Integrated inclined tube sedimentation tank |
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Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103285661A (en) * | 2013-06-18 | 2013-09-11 | 浙江大学 | Solid-liquid separation device for waste water suspended matters |
| CN103432819A (en) * | 2013-09-04 | 2013-12-11 | 大连力达环境工程有限公司 | Upward-flow-direction filtering tank connected with common water treatment device |
| CN104355478A (en) * | 2014-10-14 | 2015-02-18 | 浙江钱江纺织印染有限公司 | Printing and dyeing sewage treatment system |
| CN104628229A (en) * | 2015-02-05 | 2015-05-20 | 四川立新瑞德水处理有限责任公司 | Deep chemical wastewater treatment system and process |
| CN104857769A (en) * | 2014-02-26 | 2015-08-26 | 上海清浥环保科技有限公司 | Light filter material combined suspension tank |
| CN105233566A (en) * | 2015-10-22 | 2016-01-13 | 安尼康(福建)环保设备有限公司 | Flocculation concentration device with grille structure bodies and filtrate recycling tank with grille structure bodies |
| CN105461180A (en) * | 2016-01-12 | 2016-04-06 | 浙江大学 | Water quality purification integrated device and method for eutrophic water |
| CN105771337A (en) * | 2015-12-28 | 2016-07-20 | 张春辉 | An efficient solid-liquid separation device and its application |
| CN105999842A (en) * | 2016-07-21 | 2016-10-12 | 江苏展宏环保科技有限公司 | Coal wastewater purifier |
| CN106242170A (en) * | 2016-08-23 | 2016-12-21 | 徐州工程学院 | A kind of integrated flocculation sediment equipment being applicable to micro-pollution algae removal |
| CN107050953A (en) * | 2016-12-12 | 2017-08-18 | 东莞市鸿捷环保科技有限公司 | Intellectuality backwash filter tank and its back-flushing method |
| CN107129077A (en) * | 2017-07-11 | 2017-09-05 | 佛山市银禾企业管理咨询有限公司 | A kind of process for treating industrial waste water |
| CN107754446A (en) * | 2017-11-01 | 2018-03-06 | 安徽舜禹水务股份有限公司 | A kind of sedimentation basin and filtering ponds compound sewage processing unit |
| CN109179813A (en) * | 2018-11-13 | 2019-01-11 | 安徽理工大学 | A kind of filtering settling pond |
| CN109467174A (en) * | 2018-12-25 | 2019-03-15 | 欧基(上海)环保科技有限公司 | A kind of gas return-air washes inclined plate inclined tube-type settler |
| CN113443741A (en) * | 2021-07-01 | 2021-09-28 | 重庆市梁平排水有限公司 | Follow-on high-density pond |
| CN113622994A (en) * | 2021-08-17 | 2021-11-09 | 安徽理工大学 | Drainage device for mining industry |
| CN113695077A (en) * | 2020-05-22 | 2021-11-26 | 中国科学院青海盐湖研究所 | Filtering tank for removing magnetic impurities from fluid and filtering method thereof |
| CN113979605A (en) * | 2021-11-30 | 2022-01-28 | 产学研(广州)环境服务有限公司 | A high-efficiency pretreatment device for pharmaceutical wastewater |
| CN116282415A (en) * | 2023-01-09 | 2023-06-23 | 江西省三余环保节能科技股份有限公司 | Magnetic coagulation sedimentation system |
| CN121005448A (en) * | 2025-07-07 | 2025-11-25 | 广东鑫都环保实业有限公司 | A multifunctional integrated rapid sedimentation and flotation filtration device for sewage |
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2011
- 2011-09-01 CN CN201120325452.9U patent/CN202223979U/en not_active Expired - Lifetime
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| CN103285661B (en) * | 2013-06-18 | 2015-12-09 | 浙江大学 | The equipment for separating liquid from solid of waste water suspension |
| CN103285661A (en) * | 2013-06-18 | 2013-09-11 | 浙江大学 | Solid-liquid separation device for waste water suspended matters |
| CN103432819A (en) * | 2013-09-04 | 2013-12-11 | 大连力达环境工程有限公司 | Upward-flow-direction filtering tank connected with common water treatment device |
| CN104857769A (en) * | 2014-02-26 | 2015-08-26 | 上海清浥环保科技有限公司 | Light filter material combined suspension tank |
| CN104355478B (en) * | 2014-10-14 | 2016-07-13 | 浙江钱江纺织印染有限公司 | A kind of dyeing and printing sewage processes system |
| CN104355478A (en) * | 2014-10-14 | 2015-02-18 | 浙江钱江纺织印染有限公司 | Printing and dyeing sewage treatment system |
| CN104628229A (en) * | 2015-02-05 | 2015-05-20 | 四川立新瑞德水处理有限责任公司 | Deep chemical wastewater treatment system and process |
| CN105233566A (en) * | 2015-10-22 | 2016-01-13 | 安尼康(福建)环保设备有限公司 | Flocculation concentration device with grille structure bodies and filtrate recycling tank with grille structure bodies |
| CN105771337A (en) * | 2015-12-28 | 2016-07-20 | 张春辉 | An efficient solid-liquid separation device and its application |
| CN105771337B (en) * | 2015-12-28 | 2018-01-30 | 张春辉 | Efficient solid-liquid separation device and application thereof |
| CN105461180A (en) * | 2016-01-12 | 2016-04-06 | 浙江大学 | Water quality purification integrated device and method for eutrophic water |
| CN105999842A (en) * | 2016-07-21 | 2016-10-12 | 江苏展宏环保科技有限公司 | Coal wastewater purifier |
| CN106242170A (en) * | 2016-08-23 | 2016-12-21 | 徐州工程学院 | A kind of integrated flocculation sediment equipment being applicable to micro-pollution algae removal |
| CN107050953A (en) * | 2016-12-12 | 2017-08-18 | 东莞市鸿捷环保科技有限公司 | Intellectuality backwash filter tank and its back-flushing method |
| CN107129077A (en) * | 2017-07-11 | 2017-09-05 | 佛山市银禾企业管理咨询有限公司 | A kind of process for treating industrial waste water |
| CN107754446A (en) * | 2017-11-01 | 2018-03-06 | 安徽舜禹水务股份有限公司 | A kind of sedimentation basin and filtering ponds compound sewage processing unit |
| CN109179813A (en) * | 2018-11-13 | 2019-01-11 | 安徽理工大学 | A kind of filtering settling pond |
| CN109467174A (en) * | 2018-12-25 | 2019-03-15 | 欧基(上海)环保科技有限公司 | A kind of gas return-air washes inclined plate inclined tube-type settler |
| CN113695077A (en) * | 2020-05-22 | 2021-11-26 | 中国科学院青海盐湖研究所 | Filtering tank for removing magnetic impurities from fluid and filtering method thereof |
| CN113443741A (en) * | 2021-07-01 | 2021-09-28 | 重庆市梁平排水有限公司 | Follow-on high-density pond |
| CN113443741B (en) * | 2021-07-01 | 2023-09-12 | 重庆市梁平排水有限公司 | Improved high-density pool |
| CN113622994A (en) * | 2021-08-17 | 2021-11-09 | 安徽理工大学 | Drainage device for mining industry |
| CN113979605A (en) * | 2021-11-30 | 2022-01-28 | 产学研(广州)环境服务有限公司 | A high-efficiency pretreatment device for pharmaceutical wastewater |
| CN116282415A (en) * | 2023-01-09 | 2023-06-23 | 江西省三余环保节能科技股份有限公司 | Magnetic coagulation sedimentation system |
| CN121005448A (en) * | 2025-07-07 | 2025-11-25 | 广东鑫都环保实业有限公司 | A multifunctional integrated rapid sedimentation and flotation filtration device for sewage |
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Granted publication date: 20120523 |
