CN201115796Y - Percolation clarifier - Google Patents
Percolation clarifier Download PDFInfo
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- CN201115796Y CN201115796Y CNU2007201787132U CN200720178713U CN201115796Y CN 201115796 Y CN201115796 Y CN 201115796Y CN U2007201787132 U CNU2007201787132 U CN U2007201787132U CN 200720178713 U CN200720178713 U CN 200720178713U CN 201115796 Y CN201115796 Y CN 201115796Y
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- 238000005325 percolation Methods 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 172
- 239000010802 sludge Substances 0.000 claims abstract description 33
- 239000000725 suspension Substances 0.000 claims abstract description 29
- 238000005352 clarification Methods 0.000 claims abstract description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 18
- 239000000701 coagulant Substances 0.000 claims description 10
- 239000000835 fiber Substances 0.000 claims description 4
- 239000000945 filler Substances 0.000 claims description 4
- 230000032258 transport Effects 0.000 claims description 2
- 238000011026 diafiltration Methods 0.000 claims 1
- 238000007790 scraping Methods 0.000 abstract description 3
- 230000000630 rising effect Effects 0.000 description 7
- 230000009286 beneficial effect Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000004071 biological effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012765 fibrous filler Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000001174 ascending effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000007726 management method Methods 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
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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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- Water Treatment By Sorption (AREA)
Abstract
一种渗滤澄清池,它包括有一个矩形平底的池体,在池体内中部设有通到池体内底部的进水竖井,在进水竖井底部两侧连通有配水渠,在配水渠的两侧壁连通有设置在池体内底部的多个配水管,在配水管上部形成的配水区内并排设置有人字板,在配水区的上部形成有悬浮区,在该悬浮区的上部形成有清水区,在清水区内设置有过水斜管,在清水区的上端设置排列有集水管,在集水管的中部设有V形集水总渠,该V形集水总渠的侧壁与集水管的内端相通,在进水竖井的两侧设有泥渣浓缩室,在泥渣浓缩室的底部设置有排泥螺旋输送机。本渗滤澄清池池型简单、占地小、停留时间短、容积利用率高、具有一定的生物特性、不设大型刮泥装置,是一种适应性较强的高效澄清池。
A percolation clarification tank, which includes a rectangular flat-bottomed tank body, a water inlet shaft leading to the bottom of the tank body is provided in the middle of the tank body, and a water distribution channel is connected to both sides of the bottom of the water inlet shaft. The side wall is connected with a plurality of water distribution pipes arranged at the bottom of the pool body, herringbone boards are arranged side by side in the water distribution area formed on the upper part of the water distribution pipes, a suspension area is formed on the upper part of the water distribution area, and a clear water area is formed on the upper part of the suspension area , in the clean water area, there is an inclined water pipe, and a water collection pipe is arranged at the upper end of the clean water area, and a V-shaped water collection canal is arranged in the middle of the water collection pipe. The side wall of the V-shaped water collection canal and the water collection pipe The inner ends of the tanks are connected, and a sludge concentration chamber is provided on both sides of the water inlet shaft, and a sludge discharge screw conveyor is installed at the bottom of the sludge concentration chamber. This percolation clarifier has simple pool type, small footprint, short residence time, high volume utilization rate, certain biological characteristics, and no large mud scraping device. It is a high-efficiency clarifier with strong adaptability.
Description
技术领域 technical field
本实用新型涉及水处理澄清设备技术领域,是一种高效的水处理装置,特别涉及到一种渗滤澄清的新概念。不仅用于给水处理方面,而且用于污水回用的处理。The utility model relates to the technical field of water treatment and clarification equipment, which is an efficient water treatment device, in particular to a new concept of percolation and clarification. Not only for water supply treatment, but also for the treatment of sewage reuse.
背景技术 Background technique
澄清池根据泥渣的工作状态可分为泥渣悬浮型澄清池和泥渣循环型澄清池两大类。前者通过池中保持一层泥渣层起到接触絮凝作用。后者通过絮凝区絮体的循环增强接触絮凝作用。泥渣悬浮型澄清池包括悬浮澄清池(锥底)和脉冲澄清池(配有脉冲发生器)。它们存在的不足是清水区上升流速较低(0.7~1.0mm/s),停留时间较长(约60min以上),不能承受变化较大的冲击负荷。According to the working state of the sludge, the clarifier can be divided into two categories: the sludge suspension type clarifier and the sludge circulation type clarifier. The former plays the role of contact flocculation by maintaining a layer of mud layer in the tank. The latter enhances contact flocculation through the circulation of flocs in the flocculation zone. Sludge suspension clarifiers include suspension clarifiers (cone bottom) and pulse clarifiers (with pulse generators). Their disadvantages are that the rising velocity in the clear water area is low (0.7-1.0mm/s), the residence time is long (about 60min or more), and they cannot bear the impact load with large changes.
脉冲澄清池悬浮层工作的稳定性主要靠脉冲作用,因此需设脉冲发生装置,从而在脉动的水流作用下,使悬浮泥渣层出现周期性的膨胀和压缩状态,达到净水目的。脉冲澄清池清水区上升流速一般在1.0mm/s左右。若上升流速过高,悬浮泥渣层将被破坏,净水效果降低。The stability of the suspension layer in the pulse clarifier mainly depends on the pulse action, so a pulse generating device is required to make the suspended sludge layer periodically expand and compress under the action of the pulsating water flow to achieve the purpose of water purification. The rising flow rate in the clear water area of the pulse clarifier is generally around 1.0mm/s. If the rising velocity is too high, the suspended mud layer will be destroyed and the water purification effect will be reduced.
实用新型内容Utility model content
本实用新型的目的是提供一种在保证澄清池出水水质的前提下,综合其它类型澄清池优点的渗滤澄清池,它充分利用池体的容积,强化泥渣浓度,提高悬浮区的上升流速,缩短停留时间,增大澄清池的净化能力,简化构造不设脉冲发生装置,降低基建费用。The purpose of this utility model is to provide a percolation clarifier that integrates the advantages of other types of clarifiers under the premise of ensuring the water quality of the clarifier. It makes full use of the volume of the tank body, strengthens the concentration of sludge, and increases the rising velocity of the suspension area. , shorten the residence time, increase the purification capacity of the clarifier, simplify the structure without a pulse generating device, and reduce the cost of infrastructure.
为实现上述目的,本实用新型采取以下技术方案:To achieve the above object, the utility model takes the following technical solutions:
一种渗滤澄清池,其特征在于:它包括有一个矩形平底的池体,在池体内中部设有通到池体内底部的进水竖井,在进水竖井底部两侧连通有配水渠,在配水渠的两侧壁连通有设置在池体内底部的多个配水管,在配水管上部形成的配水区内并排设置有人字板,在配水区的上部形成有悬浮区,在该悬浮区的上部形成有清水区,在清水区内设置有斜管,在清水区的上端设置排列有集水管,在集水管的中部设有V形集水总渠,该V形集水总渠的侧壁与集水管的内端相通,在V形集水总渠的一端设有出水管,在进水竖井的侧壁连接有伸出池体侧壁的原水进水管,在进水竖井的两侧设有泥渣浓缩室,在泥渣浓缩室的底部设置有排泥螺旋输送机。A percolation clarifier, characterized in that it includes a rectangular flat-bottomed tank body, a water inlet shaft leading to the bottom of the tank body is provided in the middle of the tank body, and a water distribution channel is connected to both sides of the bottom of the water inlet shaft. The two side walls of the water distribution channel are connected with a plurality of water distribution pipes arranged at the bottom of the pool body. Herringbone boards are arranged side by side in the water distribution area formed on the upper part of the water distribution pipes. A suspension area is formed on the upper part of the water distribution area. A clear water area is formed, and inclined pipes are arranged in the clear water area, and water collecting pipes are arranged at the upper end of the clear water area, and a V-shaped water collecting canal is arranged in the middle of the water collecting pipes. The side wall of the V-shaped water collecting canal and the The inner ends of the water collection pipes are connected, and an outlet pipe is provided at one end of the V-shaped water collection channel, and a raw water inlet pipe protruding from the side wall of the pool is connected to the side wall of the water inlet shaft. The sludge concentration chamber is provided with a sludge discharge screw conveyor at the bottom of the sludge concentration chamber.
在配水管的侧壁设有多个出水孔,在集水管的侧壁设有多个进水孔,在V形集水总渠上设置有向进水竖井内输清水的立式清水回流泵。There are multiple water outlet holes on the side wall of the water distribution pipe, multiple water inlet holes on the side wall of the water collection pipe, and a vertical clean water backflow pump to deliver clean water to the water inlet shaft on the V-shaped water collection main channel .
设置采用自动调节流量的立式清水回流泵用来平衡悬浮区的上升流速,使之保持相对的衡定,从而有效地防止进水负荷的突变带来对悬浮区及出水水质的冲击。A vertical clear water return pump with automatic flow adjustment is set to balance the rising flow rate of the suspension zone to keep it relatively stable, thereby effectively preventing the impact of sudden changes in the influent load on the suspension zone and the quality of the effluent.
在悬浮区内纵向设置有纤维填料。Fibrous fillers are longitudinally arranged in the suspension area.
适当增加悬浮区高度,使高密实度的泥渣延长了在悬浮区内的停留时间,有利于其生物性能的提高,对去除部分微量污染物有一定作用。Appropriately increasing the height of the suspension zone prolongs the residence time of the high-density sludge in the suspension zone, which is beneficial to the improvement of its biological performance and has a certain effect on the removal of some trace pollutants.
在悬浮区设置纤维填料,可保持高浓度悬浮活性泥渣层的稳定和生物性能,增强抗冲击负荷的能力。The fiber filler in the suspension area can maintain the stability and biological properties of the high-concentration suspended active sludge layer and enhance the ability to resist impact loads.
在池体的上部设有助凝剂投加装置,该助凝剂投加装置的输出管插入进水竖井内。当原水中微量污染物较多时,可在池体上部设置粉末活性炭投加装置,该粉末活性炭投加装置的输送管与原水进水管连接相通。The upper part of the pool body is provided with a coagulant aid dosing device, and the output pipe of the coagulant aid dosing device is inserted into the water inlet shaft. When there are many trace pollutants in the raw water, a powdered activated carbon dosing device can be installed on the upper part of the pool body, and the delivery pipe of the powdered activated carbon dosing device is connected to the raw water inlet pipe.
V形集水总渠的斜渠壁与水平方向呈60°角度,斜管和清水区的侧壁与水平方向呈60°角度。由于清水区上部两侧池壁与水平呈60°,因而有利于斜管的安装,同时增大了斜管区水流断面。The inclined channel wall of the V-shaped catchment main channel forms an angle of 60° with the horizontal direction, and the side walls of the inclined pipe and the clear water area form an angle of 60° with the horizontal direction. Since the pool walls on both sides of the upper part of the clear water area are 60° to the horizontal, it is beneficial to the installation of the inclined pipe, and at the same time, the water flow section in the inclined pipe area is increased.
本实用新型的有益效果是:The beneficial effects of the utility model are:
1、池型为平底,容积利用率高,出水水质理想,节约投资和运行成本。1. The pool type is flat bottom, the volume utilization rate is high, the effluent water quality is ideal, and the investment and operation costs are saved.
2、达到较高的清水区上升流速,水力负荷可达10m3/m2·h以上,沉淀效率高。2. Reach a higher rising flow rate in the clear water area, the hydraulic load can reach more than 10m 3 /m 2 ·h, and the sedimentation efficiency is high.
3、悬浮层泥渣浓度高,具有吸附、接触、渗滤和一定的生物处理(包括活性炭的吸附和生物特性)功能。3. The suspension layer has a high concentration of sludge and has the functions of adsorption, contact, percolation and certain biological treatment (including the adsorption and biological characteristics of activated carbon).
4、自动调节流量的立式清水回流泵可以有效地防止进水负荷的突变带来对悬浮区及出水水质的冲击。4. The vertical clear water return pump with automatic flow adjustment can effectively prevent the sudden change of the inflow load from impacting the suspension area and the effluent water quality.
5、高浓度泥渣产生的污泥含水率低,有利于脱水干化。5. The sludge produced by high-concentration sludge has a low moisture content, which is conducive to dehydration and drying.
6、池型简单,无需大型刮泥设备,节约建设和日常管理费用。6. The pool type is simple, without large-scale mud scraping equipment, saving construction and daily management costs.
附图说明 Description of drawings
图1是本实用新型渗滤澄清池的平面图。Fig. 1 is the plane view of the utility model percolation clarifier.
图2是本实用新型渗滤澄清池A-A剖面图。Fig. 2 is the A-A sectional view of the percolation clarifier of the utility model.
图3是本实用新型渗滤澄清池B-B剖面图。Fig. 3 is the sectional view of B-B of the percolation clarifier of the utility model.
图4是本实用新型渗滤澄清池C-C剖面图。Fig. 4 is the C-C sectional view of the percolation clarifier of the utility model.
图5是本实用新型渗滤澄清池D-D剖面图。Fig. 5 is a D-D sectional view of the percolation clarification tank of the present invention.
图6是图5的A部放大示意图。FIG. 6 is an enlarged schematic view of part A of FIG. 5 .
附图标:1.池体,2.原水进水管,3.进水竖井,4.助凝剂投加装置,5.配水渠,6.配水管、7.人字板,8.悬浮区,9.纤维填料,10.斜管,11.集水管,12.V形集水总渠,13.立式清水回流泵,14.泥渣浓缩室,15.排泥螺旋输送机,16.出水管,17.配水区,18.清水区,19.出水孔,20.进水孔,21.输出管,22.清水区侧壁,23.粉末活性炭投加装置,24.输送管。Attached icons: 1. Tank body, 2. Raw water inlet pipe, 3. Water inlet shaft, 4. Coagulant aid dosing device, 5. Water distribution channel, 6. Water distribution pipe, 7. Herringbone plate, 8. Suspension area, 9. Fiber filler, 10. Inclined pipe, 11. Water collection pipe, 12. V-shaped water collection channel, 13. Vertical clear water return pump, 14. Sludge concentration chamber, 15. Mud discharge screw conveyor, 16. Outlet Water pipe, 17. Water distribution area, 18. Clean water area, 19. Water outlet hole, 20. Water inlet hole, 21. Output pipe, 22. Side wall of clean water area, 23. Powdered activated carbon dosing device, 24. Delivery pipe.
具体实施方式 Detailed ways
参见图1~图6所示:一种渗滤澄清池,它包括有一个矩形平底的池体1,在池体内中部设有通到池体内底部的进水竖井3,在进水竖井3底部两侧连通有配水渠5,在配水渠5的两侧壁连通有设置在池体内底部的多个配水管6,在配水管6上部形成的配水区17内并排设置有人字板7,在配水区17的上部形成有悬浮区8,在该悬浮区8的上部形成有清水区18,在清水区18内设置有斜管10,在清水区18的上端设置排列有集水管11,在集水管11的中部设有V形集水总渠12,该V形集水总渠12的侧壁与集水管11的内端相通,在V形集水总渠12的一端设有出水管16,在进水竖井3的侧壁连接有伸出池体侧壁的原水进水管2,在进水竖井3的两侧设有泥渣浓缩室14,在泥渣浓缩室14的底部设置有排泥螺旋输送机15。See Figures 1 to 6: a percolation clarifier, which includes a rectangular flat-bottomed
在配水管6的侧壁设有多个出水孔,在集水管11的侧壁设有多个进水孔20,在V形集水总渠12上设置有向进水竖井3内输清水的立式清水回流泵13。The side wall of the
在悬浮区8内设有纤维填料9。纤维填料9呈圆柱形毛刷状,由纤维材料制成,可保持悬浮区8内高浓度悬浮活性泥渣层的稳定和生物性能,增强抗冲击负荷的能力。A
在池体1的上部设有助凝剂投加装置4,该助凝剂投加装置4的输出管21插入进水竖井3内。A coagulant aid dosing device 4 is provided on the upper part of the
当原水中微量污染物较多时,可在池体上部设置粉末活性炭投加装置23,该粉末活性炭投加装置23的输送管24与原水进水管2连接相通。When there are many trace pollutants in the raw water, a powdered activated
V形集水总渠12的斜渠壁与水平方向呈60°角度,斜管10和清水区的侧壁22与水平方向呈60°角度。The inclined channel wall of the V-shaped catchment
本实用新型的工作过程是:在原水中投加混凝剂(处理微污染水时需在原水管道内投加粉末活性炭)后经过气水分离后,通过原水进水管2、进水竖井3、配水渠5进入配水管6内,原水在进入配水渠5前通过助凝剂投加装置4的输出管21向进水竖井3内投加有机高分子助凝剂(聚丙烯酰胺),原水从配水管6的孔眼19流出,得到充分混合,经过人字板7稳流,上升到悬浮区8,使悬浮区8内形成的高浓度活性泥渣处于动态平衡状态,原水中的微絮粒与活性泥渣进行充分接触、絮凝、吸附等,增大了絮体颗粒密实度,提高了泥渣的浓度,对颗粒物进行渗滤,所形成的泥渣颗粒更大、更重、沉降速度更快,使之适应悬浮区内的高上升流速,处理效率更高。水流经过悬浮区8后,继续向上,经过过水斜管10进一步得到净化,过水斜管10的出水孔19的出水流入集水管11,再由集水管11汇入V形集水总渠12内,其侧壁与水平呈60°;过水斜管10和清水区两侧的侧壁22与水平方向呈60°角度,因而有利于过水斜管10的安装,同时增大了清水区水流断面;进入V形集水总渠12内的清水通过出水管16排出;The working process of the utility model is: adding a coagulant to the raw water (powdered activated carbon should be added to the raw water pipeline when dealing with slightly polluted water), and after gas-water separation, the raw water is passed through the raw
立式清水回流泵13用来平衡悬浮区的上升流速,通过立式清水回流泵13向进水竖井内输清水,使悬浮区保持相对的衡定,从而有效地防止进水负荷的突变带来对悬浮区及出水水质的冲击。The vertical clear
悬浮区8多余老化的泥渣溢流进入污泥浓缩室14,污泥浓缩室内静置的泥渣含水率低,通过排泥螺旋输送机15排出,可直接用于脱水干化。The excess aged sludge in the
本渗滤澄清池池型简单、占地小、停留时间短、容积利用率高、具有一定的生物特性、不设大型刮泥装置,是一种适应性较强的高效澄清池。This percolation clarifier has simple pool type, small footprint, short residence time, high volume utilization rate, certain biological characteristics, and no large mud scraping device. It is a high-efficiency clarifier with strong adaptability.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105130095A (en) * | 2015-07-15 | 2015-12-09 | 上海市政工程设计研究总院(集团)有限公司 | Raw water biological pre-treatment system and raw water biological pre-treatment method |
| CN106075995A (en) * | 2016-07-29 | 2016-11-09 | 江苏省冶金设计院有限公司 | Metallurgical industry plant area early-stage rainwater processes buried integrated apparatus |
| CN107445269A (en) * | 2017-09-08 | 2017-12-08 | 王娜 | A kind of water quality ensuring equipment based on Mechanical Driven pulse clarifying equipment |
| CN107445267A (en) * | 2017-09-04 | 2017-12-08 | 王娜 | A kind of low energy consumption depositing reservoir pulse generating unit for sewage disposal |
-
2007
- 2007-09-25 CN CNU2007201787132U patent/CN201115796Y/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105130095A (en) * | 2015-07-15 | 2015-12-09 | 上海市政工程设计研究总院(集团)有限公司 | Raw water biological pre-treatment system and raw water biological pre-treatment method |
| CN106075995A (en) * | 2016-07-29 | 2016-11-09 | 江苏省冶金设计院有限公司 | Metallurgical industry plant area early-stage rainwater processes buried integrated apparatus |
| CN107445267A (en) * | 2017-09-04 | 2017-12-08 | 王娜 | A kind of low energy consumption depositing reservoir pulse generating unit for sewage disposal |
| CN107445269A (en) * | 2017-09-08 | 2017-12-08 | 王娜 | A kind of water quality ensuring equipment based on Mechanical Driven pulse clarifying equipment |
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Owner name: BEIJING GOLDEN STATE ENGINEERING CO., LTD. Effective date: 20121030 |
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| TR01 | Transfer of patent right |
Effective date of registration: 20121030 Address after: Cayman Islands Grand Cayman George town church street agrand Mansion Patentee after: Golden State Environment Group Corporation Patentee after: Beijing Jinzhou Environment Protection Development Co., Ltd. Address before: Cayman Islands Grand Cayman George town church street agrand Mansion Patentee before: Golden State Environment Group Corporation |
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