CN110448940B - Mud water treatment system and mud water treatment method for water purification plant - Google Patents
Mud water treatment system and mud water treatment method for water purification plant Download PDFInfo
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 372
- 238000000746 purification Methods 0.000 title claims abstract description 97
- 238000000034 method Methods 0.000 title claims abstract description 16
- 239000010802 sludge Substances 0.000 claims abstract description 113
- 238000004062 sedimentation Methods 0.000 claims abstract description 43
- 230000018044 dehydration Effects 0.000 claims abstract description 31
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 31
- 230000001105 regulatory effect Effects 0.000 claims abstract description 28
- 238000003860 storage Methods 0.000 claims abstract description 20
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 17
- 239000010959 steel Substances 0.000 claims abstract description 17
- 238000004140 cleaning Methods 0.000 claims abstract description 4
- 230000007246 mechanism Effects 0.000 claims description 47
- 239000006228 supernatant Substances 0.000 claims description 45
- 239000007788 liquid Substances 0.000 claims description 37
- 238000003756 stirring Methods 0.000 claims description 30
- 239000010865 sewage Substances 0.000 claims description 26
- 238000001514 detection method Methods 0.000 claims description 24
- 239000013049 sediment Substances 0.000 claims description 18
- 238000003809 water extraction Methods 0.000 claims description 15
- 238000000605 extraction Methods 0.000 claims description 13
- 230000033001 locomotion Effects 0.000 claims description 7
- 238000000926 separation method Methods 0.000 claims description 7
- 230000009471 action Effects 0.000 claims description 4
- 230000001276 controlling effect Effects 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 claims description 3
- 238000009418 renovation Methods 0.000 abstract description 3
- 238000010586 diagram Methods 0.000 description 11
- 238000002156 mixing Methods 0.000 description 10
- 238000010276 construction Methods 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 238000007790 scraping Methods 0.000 description 4
- 230000032258 transport Effects 0.000 description 4
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000011001 backwashing Methods 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000003712 anti-aging effect Effects 0.000 description 1
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- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000003657 drainage water Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
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- 229910052573 porcelain Inorganic materials 0.000 description 1
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- 238000012545 processing Methods 0.000 description 1
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- 238000006467 substitution reaction Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
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- 239000002699 waste material Substances 0.000 description 1
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0003—Making of sedimentation devices, structural details thereof, e.g. prefabricated parts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/02—Settling tanks with single outlets for the separated liquid
- B01D21/04—Settling tanks with single outlets for the separated liquid with moving scrapers
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2405—Feed mechanisms for settling tanks
- B01D21/2416—Liquid distributors with a plurality of feed points
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2444—Discharge mechanisms for the classified liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
- B01D21/32—Density control of clear liquid or sediment, e.g. optical control ; Control of physical properties
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- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
Abstract
本发明公开了一种净水厂排泥水处理系统及处理方法,净水厂排泥水处理系统包括分别与净水厂沉淀池、净水厂滤池相连接的若干集水井、组合式调节池、浓缩池、污泥平衡池、脱水系统以及用于储存污泥的污泥储存系统,集水井、浓缩池、污泥平衡池、脱水系统和污泥储存系统为钢制池体,其优点在于,本发明的排泥水处理系统中的大部分处理设备为钢制,可根据净水厂的实际空地面积进行定制,而后运送至现场进行组装,大大缩短了改造工期,减少占地,避免了对净水厂的大规模改建,保证在净水厂正常运行的同时,完成排泥水处理系统的建立。
The invention discloses a water purification plant sludge water treatment system and a treatment method. The water purification plant sludge water treatment system includes a number of water collection wells, a combined regulating tank, and a water purification plant sedimentation tank and a water purification plant filter tank respectively connected. The concentration tank, sludge balance tank, dehydration system and sludge storage system for storing sludge. The water collection well, concentration tank, sludge balance tank, dehydration system and sludge storage system are made of steel tanks. The advantages are that, Most of the treatment equipment in the sludge water treatment system of the present invention is made of steel and can be customized according to the actual open space area of the water purification plant and then transported to the site for assembly, which greatly shortens the renovation period, reduces the land occupation, and avoids the need for cleaning. The large-scale reconstruction of the water plant ensures that the sludge water treatment system is completed while the water purification plant is operating normally.
Description
技术领域Technical field
本发明涉及水处理技术领域,尤其涉及一种净水厂排泥水处理系统及处理方法。The present invention relates to the technical field of water treatment, and in particular to a treatment system and treatment method for muddy water from a water purification plant.
背景技术Background technique
城市用水一直是城市生活的重要组成部分,来源为城市净水厂。净水厂将原水处理成符合标准的自来水一般需经过混合、絮凝、沉淀、过滤、消毒而后进行配水,在沉淀和过滤过程中会产生大量的排泥水,排泥水的主要成分是原水中的杂质加入混凝剂后形成的絮凝颗粒,而排泥水的去处一般有两种,直排水体和直排管网,排泥水直排水体会导致河道、湖泊淤积、可能会使河床或湖底太高和造成水体污染,而排泥水直排管网会增大污水处理厂的符合,也可能堵塞下水道。排泥水占整个系统净水厂日产水量的3%-5%,直接排掉会造成了水资源的极大浪费。Urban water has always been an important part of urban life, and the source is urban water purification plants. To treat raw water into tap water that meets standards, a water purification plant generally needs to go through mixing, flocculation, sedimentation, filtration, disinfection and then water distribution. During the sedimentation and filtration process, a large amount of muddy water will be produced. The main component of the muddy water is impurities in the raw water. Flocculated particles formed after adding coagulants, and there are generally two places for muddy water to go, direct drainage and direct drainage pipe networks. Direct drainage of muddy water will cause siltation of rivers and lakes, and may cause the river bed or lake bottom to be too high and cause Water pollution, and the direct discharge of muddy water into the pipe network will increase the compliance of the sewage treatment plant and may also block the sewer. The muddy water accounts for 3%-5% of the daily water production of the entire system's water purification plant. Direct drainage will cause a huge waste of water resources.
现有的很多净水厂由于设备老旧、场地有限,不具备排泥水的处理能力,且厂区空地面积有限,施工场地受限,不利于大型排泥水处理设备建设,且很多净水厂厂区经过多期建设,地下管线复杂,部分管线情况未明,无法对空地地面进行挖掘式改造,而且一般净水厂都有严格的进出场规定,每日施工时间有限,同时,由于实际使用需要,工期较紧。如何快速地在老旧净水厂改造增加排泥水处理系统,使净水厂的水资源得到合理利用,污水排放量达标,是个比较严峻的问题。Many existing water purification plants do not have the ability to treat sludge water due to old equipment and limited space. The open space in the factory area is limited and the construction site is restricted, which is not conducive to the construction of large-scale sludge water treatment equipment. Moreover, many water purification plants pass through Multi-phase construction, underground pipelines are complicated, and the condition of some pipelines is unknown. It is impossible to carry out excavation-type reconstruction of the open space. Moreover, general water purification plants have strict entry and exit regulations, and the daily construction time is limited. At the same time, due to actual use needs, the construction period is relatively long. tight. How to quickly renovate and add a sludge treatment system to the old water purification plant so that the water resources in the water purification plant can be rationally utilized and the sewage discharge reaches the standard is a serious problem.
发明内容Contents of the invention
为了克服现有技术的不足,本发明的目的之一在于提供一种净水厂排泥水处理系统。In order to overcome the shortcomings of the prior art, one of the objects of the present invention is to provide a sludge water treatment system for water purification plants.
本发明的目的之二在于一种净水厂排泥水处理方法,用于老旧净水厂的排泥水处理系统改造。The second object of the present invention is to provide a method for treating muddy water from a water purification plant, which can be used to transform the muddy water treatment system of an old water purification plant.
本发明的目的之一采用如下技术方案实现:One of the purposes of the present invention is achieved by adopting the following technical solutions:
一种净水厂排泥水处理系统,包括分别与净水厂沉淀池、净水厂滤池相连接的若干集水井、组合式调节池、浓缩池、污泥平衡池、脱水系统以及用于储存污泥的污泥储存系统,所述集水井、所述浓缩池、所述污泥平衡池、所述脱水系统和所述污泥储存系统为钢制池体,A water purification plant sludge water treatment system, including a number of water collection wells, a combined regulating tank, a concentration tank, a sludge balance tank, a dehydration system and a storage unit respectively connected to the water purification plant sedimentation tank and the water purification plant filter tank. A sludge storage system for sludge. The water collection well, the concentration tank, the sludge balancing tank, the dehydration system and the sludge storage system are steel tanks,
所述组合式调节池包括排水池和排泥池,与净水厂滤池相连接的集水井与所述排水池相连接,与净水厂沉淀池相连接的集水井与所述排泥池相连接,所述排水池与所述排泥池之间设有连接有底泥输送装置,所述排泥池的出泥口上设有泥水抽取装置,所述排水池的出水口上设有上清液抽取装置,所述泥水抽取装置中设有第一加药机构,与所述浓缩池相连接,The combined regulating tank includes a drainage tank and a mud drainage tank. A water collection well connected to the filter tank of the water purification plant is connected to the drainage tank. A water collection well connected to the sedimentation tank of the water purification plant is connected to the mud drainage tank. Connected to each other, a sediment conveying device is provided between the drainage pool and the mud drainage pool, a mud water extraction device is provided on the mud outlet of the mud drainage pool, and a supernatant is provided on the water outlet of the drainage pool. Liquid extraction device, the mud water extraction device is provided with a first dosing mechanism and is connected to the concentration tank,
所述浓缩池中设有用于均匀进泥水的均匀进泥水结构和上清液出液管,所述浓缩池与所述污泥平衡池相连接,The concentration tank is provided with a uniform mud water feeding structure and a supernatant liquid outlet pipe for uniform mud water feeding, and the concentration tank is connected to the sludge balancing tank.
所述污泥平衡池中设有用于对泥水进行调制平衡的摆式搅拌装置,所述污泥平衡池与所述脱水系统相连接,所述脱水系统中设有第二加药机构,所述脱水系统与所述污泥储存系统相连接。The sludge balance tank is provided with a pendulum stirring device for modulating and balancing muddy water. The sludge balance tank is connected to the dehydration system. The dehydration system is provided with a second dosing mechanism. The dewatering system is connected to the sludge storage system.
进一步地,所述排水池内设有水位检测机构,所述水位检测机构与上清液抽取装置相连接,所述排泥池内设有液位检测机构,所述液位检测机构与所述泥水抽取装置相连接。Further, a water level detection mechanism is provided in the drainage tank, and the water level detection mechanism is connected to the supernatant liquid extraction device. A liquid level detection mechanism is provided in the mud drainage tank, and the liquid level detection mechanism is connected to the mud water extraction device. device is connected.
进一步地,所述底泥输送装置包括桁架式泵吸排泥机和设置在排水池的池壁顶端的导轨,所述桁架式泵吸排泥机沿所述导轨移动,所述桁架式泵吸排泥机的吸泥口位于所述排水池底部,排泥口设置在所述排泥池上方。Further, the sediment conveying device includes a truss-type pump suction mud discharger and a guide rail provided at the top of the wall of the drainage pool. The truss type pump suction mud discharge machine moves along the guide rail. The truss type pump suction mud discharge machine moves along the guide rail. The mud suction port is located at the bottom of the drainage pool, and the mud discharge port is located above the mud drainage pool.
进一步地,所述排泥池和所述排水池通过分离装置分别与集水井相连接,所述分离装置包括污水管、与污水管相连接的净水厂沉淀池排泥管、与污水管相连接的净水厂滤池排水管、用于截留净水厂滤池的反冲洗水的第一控制阀、用于截留净水厂沉淀池的泥水的第二控制阀、用于连接所述污水管和调节池的排水池的进水管和用于连接所述污水管和调节池的排泥池的进泥管,所述进水管设置在所述第一控制阀和所述净水厂滤池排水管之间;所述进泥管设置在所述第二控制阀和所述净水厂沉淀池排泥管之间,所述净水厂沉淀池位于所述进泥管和第一控制阀之间;所述进泥管与所述污水管的连接处设有用于控制泥水进入所述排泥池的第三控制阀。Further, the sludge drainage tank and the drainage pool are respectively connected to the water collection well through a separation device. The separation device includes a sewage pipe, a sedimentation tank sludge drainage pipe of the water purification plant connected to the sewage pipe, and a sludge drainage pipe connected to the sewage pipe. The connected water purification plant filter drain pipe, the first control valve for intercepting the backwash water of the water purification plant filter, the second control valve for intercepting the muddy water of the water purification plant sedimentation tank, and the connected sewage pipe. pipe and the water inlet pipe of the drainage pool of the regulating pool and the mud inlet pipe used to connect the sewage pipe and the mud drainage pool of the regulating pool. The water inlet pipe is arranged between the first control valve and the filter tank of the water purification plant. between the drainage pipes; the mud inlet pipe is arranged between the second control valve and the mud discharge pipe of the sedimentation tank of the water purification plant, and the sedimentation tank of the water purification plant is located between the mud inlet pipe and the first control valve. between; the connection between the mud inlet pipe and the sewage pipe is provided with a third control valve for controlling mud water to enter the mud discharge tank.
进一步地,所述均匀进泥水结构包括包括设置在所述浓缩池中部的进泥水主管、与进泥水主管连通的若干进泥水支管和位于在进泥水支管上的朝上设置的出流孔,所述出流孔上方罩有用于拦截从所述出流孔中射出的泥水的整流滑泥板,相邻的所述整流滑泥板之间存在间隙。Further, the uniform mud water inlet structure includes a mud water main pipe arranged in the middle of the concentration tank, several mud water branch pipes connected with the mud water main pipe, and upwardly located outflow holes located on the mud water branch pipes, so A rectifying mud plate is covered above the outflow hole for intercepting the muddy water ejected from the outflow hole, and there is a gap between adjacent rectifying mud plates.
进一步地,所述整流滑泥板朝向所述出流孔的一侧上设有凹槽,所述凹槽与所述出流孔的位置相对应,从出流孔射出的泥水撞击在所述凹槽中。Further, a groove is provided on one side of the rectifying mud plate facing the outflow hole, and the groove corresponds to the position of the outflow hole. The muddy water ejected from the outflow hole hits the in the groove.
进一步地,所述摆式搅拌装置包括至少一个叶轮,所述叶轮设置在摆杆组件上,所述摆杆组件内设有带动所述叶轮转动的转动电机,所述摆杆组件上设有带动所述摆杆相对池壁摆动的驱动组件。Further, the swing-type stirring device includes at least one impeller. The impeller is arranged on a swing rod assembly. A rotating motor is provided in the swing rod assembly to drive the impeller. The swing rod assembly is provided with a driving mechanism. The swing rod is a driving assembly that swings relative to the pool wall.
进一步地,所述驱动组件包括带动所述摆杆组件左右移动的第一电机、带动所述摆杆组件上下移动的第二电机和控制第一电机和第二电机的控制器,所述控制器的第一端和第二端分别与第一电机和第二电机相连接,其中所述第一端输出第一控制信号,所述第二端输出第二控制信号,所述第一控制信号的导通时间与所述第二控制信号的导通时间不同,所述池壁上设有与所述摆杆组件相连接的安装座,所述安装座上设有用于带动所述摆杆组件上下移动的升降机构。Further, the driving assembly includes a first motor that drives the swing bar assembly to move left and right, a second motor that drives the swing bar assembly to move up and down, and a controller that controls the first motor and the second motor. The controller The first end and the second end are connected to the first motor and the second motor respectively, wherein the first end outputs a first control signal, the second end outputs a second control signal, and the first control signal The conduction time is different from the conduction time of the second control signal. The pool wall is provided with a mounting base connected to the swing bar assembly. The mounting base is provided with a mounting base for driving the swing bar assembly up and down. Mobile lifting mechanism.
进一步地,所述驱动组件包括在竖直平面做周向运动的转动件以及连接所述转动件和所述摆杆组件的连接件,所述摆杆组件在所述连接件的带动下相对所述池壁摆动,所述连接件为软质绳索,所述转动件与所述连接件的连接处设有用于收发所述连接件的收放机构,所述摆杆组件在所述收发机构的作用下上下移动。Further, the driving assembly includes a rotating member that performs circumferential motion in a vertical plane and a connecting member that connects the rotating member and the swing lever assembly. The swing lever assembly is driven by the connecting member relative to the The pool wall swings, the connecting piece is a soft rope, the connection between the rotating piece and the connecting piece is provided with a retracting and retracting mechanism for sending and receiving the connecting piece, and the swing rod assembly is at the end of the sending and receiving mechanism. Move up and down under the action.
本发明的目的之二采用如下技术方案实现:The second object of the present invention is achieved by adopting the following technical solutions:
一种净水厂的排泥水处理方法,包括如下步骤:A method for treating muddy water from a water purification plant, including the following steps:
设备准备步骤,调研净水厂空地情况,制作相应尺寸的钢制池体,运送至各个空地,而后通过管路进行组装,The equipment preparation step involves investigating the open space conditions of the water purification plant, making steel pool bodies of corresponding sizes, transporting them to various open spaces, and then assembling them through pipelines.
钢制池体包括分别与净水厂沉淀池、净水厂滤池相连接的若干集水井,用于浓缩泥水的浓缩池,用于使泥水均匀的污泥平衡池,脱水系统以及污泥储存系统;The steel tank body includes several water collection wells connected to the sedimentation tank and filter tank of the water purification plant respectively, a concentration tank for concentrating mud water, a sludge balancing tank for making mud water uniform, a dehydration system and sludge storage. system;
调节步骤,将净水厂原有废水池改建成组合式调节池,分隔成排水池和排泥池,与净水厂滤池相连接的集水井将滤池反冲洗水排入排水池,与净水厂沉淀池相连接的集水井将排泥水排入排泥池,排水池底部的底泥被吸至排泥池,上部的上清液回收利用,排泥池中的泥水排入浓缩池,期间向泥水中投加絮凝剂;In the adjustment step, the original wastewater pool of the water purification plant is transformed into a combined regulating pool, which is divided into a drainage pool and a mud drainage pool. The water collection well connected to the filter tank of the water purification plant discharges the filter backwash water into the drainage pool, and is connected to the drainage pool. The water collection well connected to the sedimentation tank of the water purification plant discharges the sludge water into the sludge drainage tank. The sediment at the bottom of the drainage tank is sucked into the sludge drainage tank. The upper supernatant is recycled and used. The mud water in the sludge drainage tank is discharged into the concentration tank. , during which flocculant is added to the muddy water;
浓缩步骤,泥水进入钢制池体的浓缩池,通过均匀进泥水结构,在浓缩池中均匀进水、沉泥、分离泥水,而后将浓缩池上部的上清液回收利用,下部的泥浆排入污泥平衡池;In the concentration step, the muddy water enters the concentration tank with a steel tank body. Through the uniform mudwater feeding structure, water is evenly fed, sedimented, and muddy water is separated in the concentration tank. Then the supernatant liquid in the upper part of the concentration tank is recycled, and the mud in the lower part is discharged into the concentration tank. sludge balancing tank;
污泥平衡及脱水步骤,进入污泥平衡池中的泥浆经摆式搅拌装置搅拌均匀,而后将调制平衡的泥浆输送至脱水系统中进行机械脱水,泥块储存在污泥储存系统中,定期外运。In the sludge balance and dehydration step, the mud entering the sludge balance tank is stirred evenly by the pendulum stirring device, and then the balanced mud is transported to the dehydration system for mechanical dehydration. The mud blocks are stored in the sludge storage system and are periodically removed. transport.
相比现有技术,本发明的有益效果在于:Compared with the existing technology, the beneficial effects of the present invention are:
(1)本发明的排泥水处理系统中的大部分处理设备为钢制,可根据净水厂的实际空地面积进行定制,而后运送至现场进行组装,大大缩短了改造工期,减少占地,避免了对净水厂的大规模改建,保证在净水厂正常运行的同时,完成排泥水处理系统的建立;(1) Most of the treatment equipment in the sludge treatment system of the present invention is made of steel and can be customized according to the actual open space area of the water purification plant and then transported to the site for assembly, which greatly shortens the renovation period, reduces the occupation of land, and avoids A large-scale reconstruction of the water purification plant was carried out to ensure the normal operation of the water purification plant while completing the establishment of the sludge treatment system;
(2)在组合式调节池和浓缩池部分实现了对上清液的回收利用,提高了水利用率;(2) The supernatant is recycled and utilized in the combined regulating tank and concentration tank, improving water utilization;
(3)利用浓缩池的均匀进泥水结构,实现全断面进水,克服了进水短流的问题,保证了进水的均匀性,提高了浓缩效率,实现泥水分区;(3) Utilize the uniform mud water inflow structure of the concentration tank to achieve full-section water inflow, overcome the problem of short water inflow, ensure the uniformity of water inlet, improve the concentration efficiency, and realize mud water zoning;
(4)利用摆式搅拌装置,加快污泥平衡池的泥水调制平衡速度,保证污泥平衡池中的污泥浓度一致,相对于传统的定点定向的搅拌装置,通过更少的搅拌装置,达到更好的搅拌效果,有效降低整个排泥水处理系统的成本。(4) The pendulum stirring device is used to speed up the mud-water modulation and balancing speed of the sludge balance tank to ensure that the sludge concentration in the sludge balance tank is consistent. Compared with the traditional fixed-point directional stirring device, fewer stirring devices are used to achieve the desired results. Better mixing effect effectively reduces the cost of the entire sludge water treatment system.
附图说明Description of the drawings
图1为本发明实施例的处理系统的框架示意图;Figure 1 is a schematic framework diagram of a processing system according to an embodiment of the present invention;
图2为本发明实施例的组合式调节池的结构示意图;Figure 2 is a schematic structural diagram of a combined regulating pool according to an embodiment of the present invention;
图3为图2中的A-A的剖面结构示意图;Figure 3 is a schematic cross-sectional structural diagram of A-A in Figure 2;
图4为本发明实施例的底泥输送装置的结构示意图;Figure 4 is a schematic structural diagram of a sediment conveying device according to an embodiment of the present invention;
图5为本发明实施例的浓缩池的内部结构示意图;Figure 5 is a schematic diagram of the internal structure of the concentration tank according to the embodiment of the present invention;
图6为本发明实施例的浓缩池的俯视结构示意图;Figure 6 is a schematic top view of the concentration tank according to the embodiment of the present invention;
图7为图6中B-B的剖面结构示意图;Figure 7 is a schematic cross-sectional structural diagram of B-B in Figure 6;
图8为本发明实施例的均匀进泥水结构的结构示意图;Figure 8 is a schematic structural diagram of a uniform mud water inlet structure according to an embodiment of the present invention;
图9为图8中C-C的剖面结构示意图;Figure 9 is a schematic cross-sectional structural diagram of C-C in Figure 8;
图10为本发明实施例的污泥平衡池的结构示意图;Figure 10 is a schematic structural diagram of the sludge balancing tank according to the embodiment of the present invention;
图11为图10中的D-D的剖面结构示意图;Figure 11 is a schematic cross-sectional structural diagram of D-D in Figure 10;
图12为本发明实施例的摆式搅拌装置的结构示意图Figure 12 is a schematic structural diagram of a swing stirring device according to an embodiment of the present invention.
图中:In the picture:
10、净水厂沉淀池;11、净水厂滤池;12、净水厂进水口;10. Sedimentation tank of water purification plant; 11. Filter tank of water purification plant; 12. Water inlet of water purification plant;
20、集水井;20. Water collection well;
30、组合式调节池;31、排泥池;311、上清液抽取装置;312、水位检测机构;313、上清液流量控制装置;32、排水池;321、泥水抽取装置;322、液位检测机构;323、排泥管;324、第一加药机构;325、搅拌装置;33、底泥输送装置;331、桁架式泵吸刮泥机;332、导轨;333、吸泥口;334、排泥口;335、刮泥板;336、刮泥组件;337、工作桥;338、吸泥管;34、进水装置;341、污水管;342、净水厂沉淀池排泥管;343、净水厂滤池排水管;344、第一控制阀;345、第二控制阀;346、进水管;347、进泥管;348、第三控制阀;349、转换井;35、控制中心;30. Combined regulating tank; 31. Mud drainage tank; 311. Supernatant extraction device; 312. Water level detection mechanism; 313. Supernatant flow control device; 32. Drainage tank; 321. Mud water extraction device; 322. Liquid 323. Mud discharge pipe; 324. First dosing mechanism; 325. Stirring device; 33. Sediment conveying device; 331. Truss type pump suction mud scraper; 332. Guide rail; 333. Mud suction port; 334. Mud discharge port; 335. Mud scraper; 336. Mud scraping assembly; 337. Working bridge; 338. Mud suction pipe; 34. Water inlet device; 341. Sewage pipe; 342. Mud discharge pipe of sedimentation tank of water purification plant ; 343. Water purification plant filter drain pipe; 344. First control valve; 345. Second control valve; 346. Water inlet pipe; 347. Mud inlet pipe; 348. Third control valve; 349. Conversion well; 35. control center;
40、浓缩池;411、上部;412、中部;413、下部;414、池体;415、斜管;42、集水槽;421、上清液回流管;422、溢出管;423、支槽;424、锯齿状堰板;43、均匀进泥水结构;431、进泥水主管;432、进泥水支管;433、出流孔;434、整流滑泥板;435、间隙;436、凹槽;44、泥水进管;45、中心传动浓缩机;46、搅拌浓缩栅条;40. Concentration tank; 411. Upper part; 412. Middle part; 413. Lower part; 414. Tank body; 415. Inclined pipe; 42. Collection tank; 421. Supernatant return pipe; 422. Overflow pipe; 423. Branch tank; 424. Zigzag weir plate; 43. Uniform mud water inlet structure; 431. Mud water inlet main pipe; 432. Mud water inlet branch pipe; 433. Outflow hole; 434. Rectifying mud plate; 435. Gap; 436. Groove; 44. Mud water inlet pipe; 45. Center drive concentrator; 46. Stirring and concentrating grid;
50、污泥平衡池;51、叶轮;511、转动电机;52、摆杆组件;521、水压检测装置;53、驱动组件;531、转动件;532、连接件;533、收放机构;54、安装座;541、万向连接头;542、升降机构;543、轨道;50. Sludge balancing tank; 51. Impeller; 511. Rotating motor; 52. Pendulum assembly; 521. Water pressure detection device; 53. Driving assembly; 531. Rotating parts; 532. Connectors; 533. Retraction mechanism; 54. Mounting base; 541. Universal connector; 542. Lifting mechanism; 543. Track;
60、脱水系统;61、第二加药机构;60. Dehydration system; 61. Second dosing mechanism;
70、污泥储存系统。70. Sludge storage system.
具体实施方式Detailed ways
下面,结合附图以及具体实施方式,对本发明做进一步描述,需要说明的是,在不相冲突的前提下,以下描述的各实施例之间或各技术特征之间可以任意组合形成新的实施例。Below, the present invention will be further described with reference to the accompanying drawings and specific embodiments. It should be noted that, on the premise that there is no conflict, the various embodiments or technical features described below can be arbitrarily combined to form new embodiments. .
在本发明的描述中,需要说明的是,对于方位词,如有术语“中心”, “横向”、“纵向”、“长度”、“宽度”、“厚度”、“上”、“下”、 “前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”、“顺时针”、“逆时针”等指示方位和位置关系为基于附图所示的方位或位置关系,仅是为了便于叙述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定方位构造和操作,不能理解为限制本发明的具体保护范围。In the description of the present invention, it should be noted that for directional words, there are terms such as "center", "lateral", "longitudinal", "length", "width", "thickness", "upper", "lower" , "Front", "Back", "Left", "Right", "Vertical", "Horizontal", "Top", "Bottom", "Inside", "Outside", "Clockwise", "Counterclockwise" ", etc. indicate the orientation and positional relationship based on the orientation or positional relationship shown in the drawings. They are only for the convenience of describing the present invention and simplifying the description. They do not indicate or imply that the device or element referred to must have a specific orientation or be in a specific orientation. The construction and operation should not be construed as limiting the specific protection scope of the present invention.
此外,如有术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或隐含指明技术特征的数量。由此,限定有“第一”、“第二”特征可以明示或者隐含包括一个或者多个该特征,在本发明描述 中,“数个”的含义是两个或两个以上,除非另有明确具体的限定。In addition, the terms "first" and "second" if used are for descriptive purposes only and cannot be understood as indicating or implying relative importance or implicitly indicating the quantity of technical features. Therefore, features defined as "first" and "second" may explicitly or implicitly include one or more of these features. In the description of the present invention, "several" means two or more, unless otherwise stated. There are clear and specific limitations.
在本发明中,除另有明确规定和限定,如有术语“组装”、“相连”、“连接”术语应作广义去理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;也可以是机械连接;可以是直接相连,也可以是通过中间媒介相连,可以是两个元件内部相连通。对于本领域普通技术人员而言,可以根据具体情况理解上述的术语在本发明中的具体含义。In the present invention, unless otherwise expressly stated and limited, the terms "assembly", "connection" and "connection" should be understood in a broad sense. For example, it can be a fixed connection, a detachable connection, or an integrated connection. Ground connection; it can also be a mechanical connection; it can be directly connected, it can be connected through an intermediate medium, and it can be internally connected between two components. For those of ordinary skill in the art, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.
如附图1所示,一种净水厂排泥水处理系统,包括分别与净水厂沉淀池10、净水厂滤池11相连接的若干集水井20、组合式调节池30、浓缩池40、污泥平衡池50、脱水系统60以及用于储存污泥的污泥储存系统70,集水井20、浓缩池40、污泥平衡池50、脱水系统60和污泥储存系统70为钢制池体,本实施例的排泥水处理系统中的大部分处理设备为钢制,可根据净水厂的实际空地面积进行定制,而后运送至现场进行组装,大大缩短了改造工期,减少占地,避免了对净水厂的大规模改建,保证在净水厂正常运行的同时,完成排泥水处理系统的建立。As shown in Figure 1, a water purification plant sludge water treatment system includes a plurality of water collection wells 20, a combined regulating tank 30, and a concentration tank 40 that are respectively connected to the water purification plant sedimentation tank 10 and the water purification plant filter tank 11. , sludge balancing tank 50, dehydration system 60 and sludge storage system 70 for storing sludge. The water collection well 20, concentration tank 40, sludge balancing tank 50, dehydration system 60 and sludge storage system 70 are steel tanks. Specifically, most of the treatment equipment in the sludge water treatment system of this embodiment is made of steel and can be customized according to the actual open space area of the water purification plant and then transported to the site for assembly, which greatly shortens the renovation period, reduces the occupation of land, and avoids A large-scale reconstruction of the water purification plant was carried out to ensure the normal operation of the water purification plant while completing the establishment of a sludge treatment system.
组合式调节池30包括排泥池31和排水池32,与净水厂滤池11相连接的集水井20与排泥池31相连接,与净水厂沉淀池10相连接的集水井20与排水池32相连接,排泥池31与排水池32之间设有连接有底泥输送装置33,排水池32的出泥口上设有泥水抽取装置321,排泥池31的出水口上设有上清液抽取装置311,泥水抽取装置321中设有第一加药机构324,与浓缩池40相连接,The combined regulating tank 30 includes a mud drainage tank 31 and a drainage tank 32. The water collection well 20 connected to the filter tank 11 of the water purification plant is connected to the mud drainage tank 31. The water collection well 20 is connected to the sedimentation tank 10 of the water purification plant. The drainage pool 32 is connected to each other. A sediment conveying device 33 is provided between the mud drainage pool 31 and the drainage pool 32. A mud water extraction device 321 is provided on the mud outlet of the drainage pool 32, and a mud water extraction device 321 is provided on the outlet of the mud drainage pool 31. The supernatant extraction device 311 and the muddy water extraction device 321 are provided with a first dosing mechanism 324, which is connected to the concentration tank 40.
浓缩池40中设有用于均匀进泥水的均匀进泥水结构43和上清液回流管421,浓缩池40与污泥平衡池50相连接,利用浓缩池40的均匀进泥水结构43,实现全断面进水,克服了进水短流的问题,保证了进水的均匀性,提高了浓缩效率,实现泥水分区。The concentration tank 40 is provided with a uniform mud water inlet structure 43 and a supernatant return pipe 421 for uniform mud water inflow. The concentration tank 40 is connected to the sludge balancing tank 50. The uniform mud water inlet structure 43 of the concentration tank 40 is used to achieve a full-section Water inflow overcomes the problem of short flow of incoming water, ensures the uniformity of incoming water, improves concentration efficiency, and realizes muddy water partitioning.
同时,在组合式调节池30和浓缩池40部分实现了对上清液的回收利用,提高了水利用率。At the same time, the supernatant liquid is recycled in the combined regulating tank 30 and the concentration tank 40, thereby improving the water utilization rate.
污泥平衡池50中设有用于对泥水进行调制平衡的摆式搅拌装置325,污泥平衡池50与脱水系统60相连接,脱水系统60中设有第二加药机构61,脱水系统60与污泥储存系统70相连接。利用摆式搅拌装置325,加快污泥平衡池50的泥水调制平衡速度,保证污泥平衡池50中的污泥浓度一致,相对于传统的定点定向的搅拌装置325,通过更少的搅拌装置325,达到更好的搅拌效果,有效降低整个排泥水处理系统的成本。The sludge balance tank 50 is provided with a pendulum stirring device 325 for modulating and balancing muddy water. The sludge balance tank 50 is connected to the dehydration system 60. The dehydration system 60 is provided with a second dosing mechanism 61, and the dehydration system 60 is connected to the dehydration system 60. The sludge storage system 70 is connected. The pendulum stirring device 325 is used to speed up the mud water modulation and balancing speed of the sludge balance tank 50 and ensure that the sludge concentration in the sludge balance tank 50 is consistent. Compared with the traditional fixed-point directional stirring device 325, fewer stirring devices 325 are used. , achieve better mixing effect and effectively reduce the cost of the entire muddy water treatment system.
现结合附图,针对每一部分进行详细描述。Each part is now described in detail with reference to the accompanying drawings.
如图2-4所示,本发明的组合式调节池30包括调节池本体和进水装置34,调节池本体包括用于接收净水厂滤池11的反冲洗水的排泥池31和用于接收净水厂沉淀池10的排泥水的排水池32,排泥池31与排水池32之间连接有底泥输送装置33,相对于现有的调节池,本实施例的调节池具有自动控制功能,具体提现在,排泥池31和排水池32并排设置,排水池32的出泥口上设有泥水抽取装置321,排泥池31的出水口上设有上清液抽取装置311,排泥池31内设有水位检测机构312,水位检测机构312与上清液抽取装置311相连接,排水池32内设有液位检测机构322,液位检测机构322与泥水抽取装置321相连接,由于净水厂滤池11反冲洗水的排放时间不定,因此流量也不是匀速的,因此,当排泥池31中的底泥被抽取到排水池32中,留下较清澈的上清液,水位检测机构312检测到上清液达到设定水位,则启动上清液抽取装置311,将上清液回收利用,一般情况下为送至净水厂的进水口,重新进入净水系统;而当液位检测机构322检测到排水池32中的液位达到设定值时,泥水抽取装置321开始工作,将泥水转移至浓缩池40中,防止液位过高,泥水溢出排水池32中,设备自动化运行,根据调节池水位情况进行自动控制,无需人员进行现场操作,无需额外增加原有工作人员的工作量。另外,排水池32中可设置搅拌装置325,用于保持池中泥水平衡,防止底部沉积淤泥,导致排水池32容量降低。上清液抽取装置311上连接有上清液流量控制装置313。As shown in Figures 2-4, the combined regulating tank 30 of the present invention includes a regulating tank body and a water inlet device 34. The regulating tank body includes a sludge drainage tank 31 for receiving backwash water from the water purification plant filter tank 11 and a water inlet device 34. A sediment conveying device 33 is connected between the drainage pool 31 and the drainage pool 32 for receiving the muddy water from the sedimentation tank 10 of the water purification plant. Compared with the existing regulating pool, the regulating pool of this embodiment has an automatic The control function is specifically mentioned in that the mud drainage pool 31 and the drainage pool 32 are arranged side by side. The mud outlet of the drainage pool 32 is provided with a mud water extraction device 321. The outlet of the mud drainage pool 31 is provided with a supernatant liquid extraction device 311. A water level detection mechanism 312 is provided in the mud pool 31, and the water level detection mechanism 312 is connected to the supernatant liquid extraction device 311. A liquid level detection mechanism 322 is provided in the drainage pool 32, and the liquid level detection mechanism 322 is connected to the mud water extraction device 321. Since the discharge time of the backwash water from the filter tank 11 of the water purification plant is uncertain, the flow rate is not uniform. Therefore, when the sediment in the mud drainage tank 31 is extracted into the drainage tank 32, a clearer supernatant liquid is left behind. When the water level detection mechanism 312 detects that the supernatant reaches the set water level, it starts the supernatant extraction device 311 to recycle the supernatant. Generally, it is sent to the water inlet of the water purification plant and re-enters the water purification system; When the liquid level detection mechanism 322 detects that the liquid level in the drainage pool 32 reaches the set value, the muddy water extraction device 321 starts to work and transfers the muddy water to the concentration pool 40 to prevent the liquid level from being too high and the muddy water from overflowing into the drainage pool 32. The equipment operates automatically and is automatically controlled according to the water level of the regulating pool. There is no need for personnel to perform on-site operations, and there is no need to increase the workload of the original staff. In addition, a stirring device 325 may be provided in the drainage pool 32 to maintain a balance of mud and water in the pool and prevent silt from depositing at the bottom, resulting in a reduction in the capacity of the drainage pool 32 . The supernatant liquid extraction device 311 is connected to a supernatant liquid flow control device 313.
另外,由于将调节池分隔成排泥池31和排水池32,对于进水装置34还需特别设置,具体地说,排水装置包括污水管341,与污水管341相连接的净水厂沉淀池排泥管342以及与污水管341相连接的净水厂滤池排水管343,包括用于截留净水厂滤池11的反冲洗水的第一控制阀344、用于截留净水厂沉淀池10的泥水的第一控制阀344、用于连接污水管341和调节池的排泥池31的进水管346和用于连接污水管341和调节池的排水池32的进泥管347,进水管346设置在第一控制阀344和净水厂滤池排水管343之间;进泥管347设置在第二控制阀345和净水厂沉淀池排泥管342之间,净水厂沉淀池10位于进泥管347和第一控制阀344之间;进泥管347与污水管341的连接处设有用于控制泥水进入排水池32的第三控制阀348。利用多个控制阀对进入排水池32和排泥池31的泥水进行控制,可实现排泥水和反冲洗水分离,还可实现排水池32和排泥池31的放空检修,也可在不影响滤池反冲洗水回收使用和水厂正常运行的情况下,实现部分排泥水应急排放。In addition, since the regulating tank is divided into a mud drainage tank 31 and a drainage tank 32, the water inlet device 34 needs to be specially set up. Specifically, the drainage device includes a sewage pipe 341 and a sedimentation tank of a water purification plant connected to the sewage pipe 341. The sludge discharge pipe 342 and the water purification plant filter drain pipe 343 connected to the sewage pipe 341 include a first control valve 344 for intercepting the backwash water of the water purification plant filter 11, and a first control valve 344 for intercepting the sedimentation tank of the water purification plant. The first control valve 344 of the muddy water of 10, the water inlet pipe 346 for connecting the sewage pipe 341 and the mud drainage pool 31 of the regulating pool, and the mud inlet pipe 347 for connecting the sewage pipe 341 and the drainage pool 32 of the regulating pool. The water inlet pipe 346 is set between the first control valve 344 and the water purification plant filter drain pipe 343; the mud inlet pipe 347 is set between the second control valve 345 and the water purification plant sedimentation tank mud drain pipe 342, the water purification plant sedimentation tank 10 It is located between the mud inlet pipe 347 and the first control valve 344; the connection between the mud inlet pipe 347 and the sewage pipe 341 is provided with a third control valve 348 for controlling mud water to enter the drainage pool 32. Multiple control valves are used to control the mud water entering the drainage pool 32 and the mud drainage pool 31, so that the mud drainage water and the backwash water can be separated, and the drainage pool 32 and the mud drainage pool 31 can also be vented and inspected without affecting the operation. When the filter backwash water is recycled and the water plant is operating normally, some of the sludge water can be discharged in an emergency manner.
更具体地说,通过关闭第一控制阀344实现对于反冲洗水的截留,反冲洗水从净水厂滤池排水管343进入污水管341,而后进入排泥池31;另外,通过关闭第一控制阀344和第二控制阀345,打开第三控制阀348,实现对于排泥水的截留,排泥水从净水厂沉淀池排泥管342排出,进入污水管341,而后进入排水池32,实现两者分而治之的目的;另外,如需对调节池进行检修,则可关闭第三控制阀348,打开第一控制阀344和第二控制阀345,排泥池31和排水池32不再接纳滤池反冲洗水和沉淀池排泥水,且不影响水厂正常运转。由于净水厂沉淀池10的清洗时间和滤池反冲洗时间不一致,且水量不同,净水厂沉淀池10在清洗和大排泥时,排泥水量会远远超出排水池32的可利用容积,因此排泥池31在进行回收的同时,排泥水需应急排放,具体操作为,打开第二控制阀345,关闭第一控制阀344和第三控制阀348,清洗水和大排泥水通过污水管进入市政管网。排泥池31中的泥水沉淀后,排水池32中的部分泥水也进入了浓缩池40,因此可用底泥输送装置33将排泥池31中的底泥送至排水池32中,此时排泥池31中的水位检测机构312通过监测水位变化来反馈信号控制上清液抽取装置311,实现上清液和底泥的分离。More specifically, by closing the first control valve 344, the backwash water is intercepted, and the backwash water enters the sewage pipe 341 from the filter drain pipe 343 of the water purification plant, and then enters the mud drainage tank 31; in addition, by closing the first control valve 344, The control valve 344 and the second control valve 345 open the third control valve 348 to intercept the muddy water. The muddy water is discharged from the muddy discharge pipe 342 of the sedimentation tank of the water purification plant, enters the sewage pipe 341, and then enters the drainage pool 32. The purpose of dividing and conquering the two; in addition, if the adjustment tank needs to be inspected, the third control valve 348 can be closed, the first control valve 344 and the second control valve 345 can be opened, and the mud drainage tank 31 and the drainage tank 32 will no longer accept the filter. The tank backwash water and sedimentation tank discharge mud water will not affect the normal operation of the water plant. Since the cleaning time of the sedimentation tank 10 of the water purification plant is inconsistent with the backwashing time of the filter, and the water volume is different, when the sedimentation tank 10 of the water purification plant is being cleaned and a large amount of mud is discharged, the volume of mud discharged will far exceed the available volume of the drainage tank 32 , therefore while the sludge tank 31 is recovering, the sludge water needs to be discharged urgently. The specific operation is to open the second control valve 345, close the first control valve 344 and the third control valve 348, and let the cleaning water and large sludge water pass through the sewage. The pipe enters the municipal pipe network. After the mud water in the drainage tank 31 settles, part of the mud water in the drainage tank 32 also enters the concentration tank 40. Therefore, the sediment transport device 33 can be used to send the sediment in the drainage tank 31 to the drainage tank 32. At this time, The water level detection mechanism 312 in the mud pool 31 monitors water level changes to provide feedback signals to control the supernatant extraction device 311 to achieve separation of the supernatant and bottom mud.
考虑到水厂原有构筑物设施和场地情况,因此进泥管347与污水管341的连接处设有转换井349,第三控制阀348位于转换井349中,打开第三控制阀348,通过转换井349转换功能使排泥水进入排水池32。更具体地说,第三控制阀348为蝶阀,便于调节泥水流量。Taking into account the original structural facilities and site conditions of the water plant, a conversion well 349 is provided at the connection between the mud inlet pipe 347 and the sewage pipe 341. The third control valve 348 is located in the conversion well 349. Open the third control valve 348, and through the conversion The well 349 conversion function allows muddy water to enter the drainage pool 32. More specifically, the third control valve 348 is a butterfly valve to facilitate adjustment of mud water flow.
对于第一控制阀344的位置设置,本实施例中的第一控制阀344设置在进水管346与污水管341的连接处,可设置成截止阀,防止排泥水反冲至排水池中,也可将第一控制阀344设为闸板阀,闸板阀开启,保证了反冲洗水可排入排水池32中,防止排泥池31发生溢流现象,不干扰净水厂和滤池的正常工作。Regarding the position setting of the first control valve 344, the first control valve 344 in this embodiment is set at the connection between the water inlet pipe 346 and the sewage pipe 341, and can be set as a stop valve to prevent the muddy water from backwashing into the drainage pool, and also The first control valve 344 can be set as a gate valve, and the gate valve is opened to ensure that the backwash water can be discharged into the drainage pool 32, preventing overflow of the mud drainage pool 31, and not interfering with the water purification plant and the filter tank. normal work.
排泥池31中的水位检测机构312和排水池32中的液位检测机构322为超声波液位计,实际应用中,包括控制中心35,控制中心35为PLC控制柜,水位检测机构312和液位检测机构322与控制中心35相连接,泥水抽取装置321为潜水泵,超声波液位计监控排泥池31和排水池32内的水位,达到一定水位时会把信号反馈到PLC控制柜,然后启动潜水泵开关进行抽水,下降到设定水位时会把信号反馈回PLC控制柜,然后关闭潜水泵,潜水泵与浓缩池40相连接。上清液抽取装置311的原理同上,上清液抽取装置311为回收水泵,与净水厂进水口12相连接。The water level detection mechanism 312 in the mud drainage pool 31 and the liquid level detection mechanism 322 in the drainage pool 32 are ultrasonic liquid level meters. In practical applications, they include a control center 35. The control center 35 is a PLC control cabinet. The water level detection mechanism 312 and liquid The level detection mechanism 322 is connected to the control center 35. The mud water extraction device 321 is a submersible pump. The ultrasonic liquid level meter monitors the water levels in the mud drainage pool 31 and the drainage pool 32. When the water level reaches a certain level, the signal will be fed back to the PLC control cabinet, and then Start the submersible pump switch to pump water. When the water level drops to the set water level, the signal will be fed back to the PLC control cabinet, and then the submersible pump will be closed. The submersible pump is connected to the concentration tank 40. The principle of the supernatant extraction device 311 is the same as above. The supernatant extraction device 311 is a recovery water pump and is connected to the water inlet 12 of the water purification plant.
本实施例中采用的底泥输送装置33包括桁架式泵吸刮泥机331和设置在排泥池31的池壁顶端的导轨332,桁架式泵吸刮泥机331沿导轨332移动,桁架式泵吸刮泥机331的吸泥口333位于排泥池31底部,排泥口334设置在排水池32上方。桁架式泵吸刮泥机331沿导轨332来回移动,将排泥池31底部的底泥吸收,通过排泥口334排入排水池32中,实现了上清液和底泥的分离。The sediment conveying device 33 used in this embodiment includes a truss-type pumping mud scraper 331 and a guide rail 332 provided at the top of the tank wall of the mud discharge tank 31. The truss-type pumping mud scraper 331 moves along the guide rail 332. The mud suction port 333 of the pump suction scraper 331 is located at the bottom of the mud discharge pool 31 , and the mud discharge port 334 is provided above the drainage pool 32 . The truss-type pump suction scraper 331 moves back and forth along the guide rail 332, absorbs the sediment at the bottom of the drainage pool 31, and discharges it into the drainage pool 32 through the drainage port 334, thereby realizing the separation of the supernatant liquid and the sediment.
更具体地说,桁架式泵吸刮泥机331底部设有若干刮泥板335,相邻的刮泥板335朝向位于中间的吸泥口333倾斜设置,桁架式泵吸刮泥机331包括用于安装刮泥板335的安装架。桁架式泵吸刮泥机331在移动时,刮泥板335将底泥集中至吸泥口333处,方便吸泥口333吸取,减少了吸泥口333的数量,提高吸泥效率。More specifically, the truss type pump suction scraper 331 is provided with a number of scrapers 335 at the bottom, and the adjacent scrapers 335 are inclined toward the middle suction port 333. The truss type pump suction scraper 331 includes a The mounting bracket for installing the scraper 335. When the truss type pump suction mud scraper 331 is moving, the mud scraper 335 concentrates the bottom mud to the mud suction port 333, which facilitates the mud suction port 333 to absorb, reduces the number of mud suction ports 333, and improves the mud suction efficiency.
另一种刮泥结构为,桁架式泵吸刮泥机331底部设有菱形的刮泥组件336,吸泥口333位于两个刮泥组件336之间,桁架式泵吸刮泥机331包括用于安装刮泥组件336的安装架,方便桁架式泵吸刮泥机331在来回运动时均可刮泥,提高刮泥效率,刮泥效果更好。Another type of mud scraping structure is that the bottom of the truss type pump suction mud scraper 331 is provided with a diamond-shaped mud scraper assembly 336, and the mud suction port 333 is located between the two mud scraper assemblies 336. The truss type pump suction mud scraper 331 includes a The mounting bracket for installing the mud scraper assembly 336 facilitates the truss type pump suction scraper 331 to scrape mud during its back and forth movement, thereby improving the mud scraping efficiency and achieving a better mud scraping effect.
由于调节池面积较大,为了方便检修,可利用横跨排泥池31的桁架式泵吸刮泥机331,在桁架式泵吸排泥机顶端设有工作桥337。Since the area of the regulating tank is large, in order to facilitate maintenance, a truss-type pump suction scraper 331 across the mud discharge tank 31 can be used, and a working bridge 337 is provided at the top of the truss type pump suction mud scraper.
另外,排泥池31中的底泥量可能不多,不方便在桁架式泵吸刮泥机331的吸泥管338中移动,因此,本实施例中的两个相邻的吸泥口333与同一根吸泥管338相连接,吸泥管338与排泥口334相连接,节省了桁架式泵吸刮泥机331的材料,预先将底泥汇总,方便输送至排泥口334,进入排水池32中。In addition, the amount of sediment in the mud discharge tank 31 may not be large, and it is inconvenient to move it in the mud suction pipe 338 of the truss type pump suction scraper 331. Therefore, the two adjacent mud suction ports 333 in this embodiment are The same mud suction pipe 338 is connected, and the mud suction pipe 338 is connected to the mud discharge port 334, which saves the material of the truss type pump suction mud scraper 331, collects the bottom mud in advance, and conveniently transports it to the mud discharge port 334 and enters the drainage. Pool 32.
由于排水池32与浓缩池40相连接,为了加快处理流程,提高污泥沉淀率,泥水抽取装置321包括与浓缩池40相连接的排泥管323,排泥管323中设有第一加药机构324,第一加药机构324包括管道混合器,在管道混合器中进行絮凝剂与泥水的混合。Since the drainage pool 32 is connected to the concentration tank 40, in order to speed up the treatment process and improve the sludge sedimentation rate, the mud water extraction device 321 includes a sludge drainage pipe 323 connected to the concentration tank 40, and a first dosing agent is provided in the sludge drainage pipe 323. Mechanism 324, the first dosing mechanism 324 includes a pipe mixer, in which the flocculant and muddy water are mixed.
如图5-9所示,本发明的均匀进泥水结构43,将浓缩池40分为上部411和下部413,泥水进入浓缩池40后,依次通过自然沉淀区,斜管415沉淀区及上清液集水区,浓缩池40下部413设置中心传动浓缩机45和搅拌浓缩栅条46,以浓缩底部污泥。As shown in Figures 5-9, the uniform mud water inlet structure 43 of the present invention divides the concentration tank 40 into an upper part 411 and a lower part 413. After the mud water enters the concentration tank 40, it passes through the natural sedimentation area, the inclined tube 415 sedimentation area and the supernatant in sequence. In the liquid water collection area, the lower part 413 of the concentration tank 40 is provided with a central drive concentrator 45 and a stirring concentration grid 46 to concentrate the bottom sludge.
为了保证进泥水的均匀性,克服以前进水短流的问题,本发明的均匀进泥水结构43,其分别与泥水进管44以及浓缩池40连通,包括设置在浓缩池40中部412的进泥水主管431、与进泥水主管431连通的若干进泥水支管432和位于在进泥水支管432上的朝上设置的出流孔433,出流孔433上方罩有用于拦截从出流孔433中射出的泥水的整流滑泥板434,相邻的整流滑泥板434之间存在间隙435。In order to ensure the uniformity of the incoming mud water and overcome the problem of short flow of incoming water in the past, the uniform mud water inlet structure 43 of the present invention is connected to the mud water inlet pipe 44 and the concentration tank 40 respectively, including the incoming mud water provided in the middle part 412 of the concentration tank 40 The main pipe 431, several muddy water branch pipes 432 connected with the muddy water main pipe 431, and upwardly located outflow holes 433 located on the muddy water branch pipes 432. The upper part of the outflow hole 433 is covered with a cover for intercepting the water emitted from the outflow hole 433. Mud water rectifying mud plates 434, and gaps 435 exist between adjacent rectifying mud plates 434.
利用设置在浓缩池40中部412的进泥水主管431和与进泥水主管431连通的若干进泥水支管432进水,而后,泥水从位于在进泥水支管432上的朝上设置的出流孔433的射出,撞击在设置出流孔433上方的整流滑泥板434上,泥水被打散,下落,而后在后续射出的泥水的推动下,转向上流动,泥水多次改变方向,每次改变方向均分散一侧,而后泥水均匀分布在整个平面上,同时也使泥水的运行流程变长,速度梯度也一直在变化,与浓缩池40中的更高浓度的泥水接触时间更长,增加颗粒碰撞的机会,提高了絮凝效果和沉淀浓缩的效率。而经过沉淀的水从整流滑泥板434之间的间隙435上升至斜管415沉淀区,再次进行沉淀,形成上清液进入上清液集水区,进入集水槽42而后被回收利用。在此过程中,出流速度有所要求,速度的实现可以依靠设置水泵和限制出流孔433的孔径,出流孔433的孔径范围为9mm ~16mm。The mud water main pipe 431 arranged in the middle part 412 of the concentration tank 40 and several mud water branch pipes 432 connected with the mud water main pipe 431 are used to enter the water. Then, the mud water flows from the outlet hole 433 located upward on the mud water branch pipe 432. It is ejected and hits the rectifying mud plate 434 provided above the outlet hole 433. The muddy water is scattered and falls, and then driven by the subsequently injected muddy water, it turns to flow upward. The muddy water changes direction multiple times, and each time the direction changes, the muddy water changes direction. Disperse one side, and then the muddy water is evenly distributed on the entire plane. At the same time, the running process of the muddy water is lengthened, and the velocity gradient is also constantly changing. The contact time with the higher concentration of muddy water in the concentration tank 40 is longer, which increases the probability of particle collision. opportunity to improve the flocculation effect and the efficiency of sedimentation and concentration. The precipitated water rises from the gap 435 between the rectifying mud plates 434 to the sedimentation area of the inclined tube 415, and is precipitated again to form a supernatant liquid that enters the supernatant water collection area, enters the water collection tank 42, and is recycled. During this process, the outflow speed is required, and the speed can be achieved by setting up a water pump and limiting the aperture of the outflow hole 433. The aperture range of the outflow hole 433 is 9mm ~ 16mm.
更具体地说,整流滑泥板434朝向出流孔433的一侧上设有凹槽436,凹槽436与出流孔433的位置相对应,从出流孔433射出的泥水撞击在凹槽436中,由于凹槽436的设置,使泥水的撞击角度不同,撞击后的分散角度和速度也不同,与池内更高浓度的泥水接触时间增长,增加颗粒碰撞的机会,提高了絮凝效果和沉淀浓缩的效率,凹槽436的形状有多种形式,斜槽、弧形槽等,优选的,凹槽436为倒“V”型槽,角度一般大于45°。More specifically, a groove 436 is provided on the side of the rectifying mud plate 434 facing the outflow hole 433. The groove 436 corresponds to the position of the outflow hole 433, and the muddy water ejected from the outflow hole 433 hits the groove. In 436, due to the setting of the groove 436, the impact angle of the muddy water is different, and the dispersion angle and speed after the impact are also different. The contact time with the higher concentration of muddy water in the pool increases, increasing the chance of particle collision, and improving the flocculation effect and sedimentation. In order to improve the efficiency of concentration, the shape of the groove 436 can be in various forms, such as inclined grooves, arc-shaped grooves, etc. Preferably, the groove 436 is an inverted "V"-shaped groove, and the angle is generally greater than 45°.
另外,为了防止从出流孔433中射出的泥水没有接触到整流滑泥板434,整流滑泥板434为倒“V”型长条板,罩设在每根进泥水支管432的上方,保证每股水流至少经过一次撞击和变向。In addition, in order to prevent the muddy water ejected from the outflow hole 433 from contacting the rectifying mud plate 434, the rectifying mud plate 434 is an inverted "V" shaped strip, and the cover is located above each muddy water inlet branch pipe 432 to ensure that Each stream of water undergoes at least one collision and change of direction.
同时,为了实现全断面的均匀进水,若干进泥水支管432平行设置在进泥水主管431两侧,呈天线状分布,涉及到浓缩池40中部412水平面的每个部位,每一根进泥水支管432上均罩有整流滑泥板434,保证进入的泥水在整个断面上均匀分布。At the same time, in order to achieve uniform water inflow across the entire section, a number of mud water branch pipes 432 are arranged in parallel on both sides of the mud water main pipe 431, distributed in an antenna shape, involving every part of the horizontal plane 412 in the middle part of the concentration tank 40, and each mud water branch pipe 432 are covered with rectifying mud plates 434 to ensure that the incoming mud water is evenly distributed on the entire section.
为了缩短浓缩池40的建设时间,本实施例的浓缩池40的池体414为一体化钢制结构,制作完成后,运送至所需场所,而后组装内部结构和设备,大大缩短了净水厂排泥水处理系统的建设工期。由于工作环境的限制,浓缩池40的池体414表面经过防腐处理,具有抗老化瓷性,使用寿命长,便于维护。In order to shorten the construction time of the concentration tank 40, the tank body 414 of the concentration tank 40 in this embodiment is an integrated steel structure. After the production is completed, it is transported to the required place, and then the internal structure and equipment are assembled, which greatly shortens the time of the water purification plant. The construction period of the sludge water treatment system. Due to the limitations of the working environment, the surface of the tank body 414 of the concentration tank 40 has undergone anti-corrosion treatment, has anti-aging porcelain properties, has a long service life, and is easy to maintain.
排泥水从均匀进泥水结构43中进入后,逐步沉淀、分层,高效浓缩池40的上部411设有斜管415,整流滑泥板434位于斜管415下方,进入斜管415的泥水进一步进行沉淀,该区域为斜管415沉淀区。After the muddy water enters from the uniform muddy water inlet structure 43, it gradually settles and stratifies. The upper part 411 of the high-efficiency concentration tank 40 is provided with an inclined tube 415. The rectifying mud plate 434 is located below the inclined tube 415. The muddy water entering the inclined tube 415 is further processed. Precipitation, this area is the sedimentation area of the inclined tube 415.
泥水经过斜管415的进一步沉淀后,悬浮物等杂质含量大大降低,达到回收标准,因此斜管415沉淀区上方设有上清液集水区,上清液集水区内设有集水槽42,集水槽42位于斜管415上方,集水槽42中设有上清液回流管421和溢出管422。上清液进入集水槽42中,而后进入上清液回流管421回收利用,当上清液过多,为了避免溢出,多余的上清液可从溢出管422排出。After further sedimentation of the muddy water through the inclined pipe 415, the content of impurities such as suspended solids is greatly reduced and reaches the recovery standard. Therefore, a supernatant water collection area is provided above the sedimentation area of the inclined pipe 415, and a water collection tank 42 is provided in the supernatant water collection area. , the water collection tank 42 is located above the inclined pipe 415, and the water collection tank 42 is provided with a supernatant return pipe 421 and an overflow pipe 422. The supernatant liquid enters the water collection tank 42 and then enters the supernatant liquid return pipe 421 for recycling. When there is too much supernatant liquid, in order to avoid overflow, the excess supernatant liquid can be discharged from the overflow pipe 422.
为了增加上清液的收集面,集水槽42两侧连通有若干支槽423,支槽423包括设置在两侧的锯齿状堰板424,上清液低于堰板的锯齿时不过水,此时堰板只起挡水作用;若水位持续上升,高于锯齿时,上清液就进入支槽423,再汇入集水槽,保证了均匀集水。In order to increase the collection surface of the supernatant, several branch grooves 423 are connected on both sides of the water collection tank 42. The branch grooves 423 include serrated weir plates 424 arranged on both sides. When the supernatant liquid is lower than the saw teeth of the weir plate, no water will flow. The weir plate only serves to retain water; if the water level continues to rise and is higher than the saw teeth, the supernatant liquid will enter the branch groove 423 and then flow into the water collection tank, ensuring uniform water collection.
如图10-12所示,本发明的摆式搅拌装置325,除了包括常规搅拌装置325的搅拌用的叶轮51外,还包括带动叶轮51摆动的摆杆组件52,本实施例中的叶轮51可在转动电机511的带动下正常转动,同时在摆杆组件52的带动下摆动任意角度,增大了搅拌面积,减少死角,提高搅拌效率。为了方便摆杆组件52的安装,池壁上设有与摆杆组件52相连接的安装座54,另外,为了保证摆杆组件52的灵活性和摆动角度的任意性,摆杆组件52与安装座54通过万向连接头541相连接。As shown in Figures 10-12, the swing stirring device 325 of the present invention, in addition to the stirring impeller 51 of the conventional stirring device 325, also includes a swing rod assembly 52 that drives the impeller 51 to swing. The impeller 51 in this embodiment It can rotate normally under the driving of the rotating motor 511, and at the same time, it can swing at any angle under the driving of the swing rod assembly 52, which increases the mixing area, reduces dead spots, and improves the mixing efficiency. In order to facilitate the installation of the swing bar assembly 52, a mounting seat 54 connected to the swing bar assembly 52 is provided on the pool wall. In addition, in order to ensure the flexibility of the swing bar assembly 52 and the arbitrary swing angle, the swing bar assembly 52 is installed with the swing bar assembly 52. The seats 54 are connected through universal connectors 541 .
而摆杆组件52的摆动方式有多种,总体分为定点的前后左右摆动以及整体的上下移动。There are many ways of swinging the swing bar assembly 52, which are generally divided into fixed-point swinging back and forth, left and right, and overall up and down movement.
对于定点的前后左右摆动的实现,一实施例中,驱动机构包括带动摆杆组件52左右移动的第一电机、带动摆杆组件52上下移动的第二电机和控制第一电机和第二电机的控制器,控制器的第一端和第二端分别与第一电机和第二电机相连接,其中第一端输出第一控制信号,第二端输出第二控制信号,第一控制信号的导通时间与第二控制信号的导通时间不同。通过输出导通时间不同的第一控制信号与第二控制信号,从而能够使上下摆动和左右摆动具有不同的运行时间,使摆杆组件52的摆动运行轨迹不断变化,实现大范围搅拌,并且搅拌区域无“死区”,提升了搅拌效率。更具体地说,第一控制信号和第二控制信号中的一个持续导通,第一控制信号和所第二控制信号中的另一个在导通过程中按照预设周期截止预设时间,第一电机和第二电机独立运行,上下摆动和左右摆动具有不同的运行时间,摆动轨迹不断变化,实现大范围搅拌。For realizing the forward, backward, left and right swing of the fixed point, in one embodiment, the driving mechanism includes a first motor that drives the swing bar assembly 52 to move left and right, a second motor that drives the swing bar assembly 52 to move up and down, and a motor that controls the first motor and the second motor. Controller, the first end and the second end of the controller are connected to the first motor and the second motor respectively, wherein the first end outputs the first control signal, the second end outputs the second control signal, and the conductor of the first control signal The conduction time is different from the conduction time of the second control signal. By outputting the first control signal and the second control signal with different conduction times, the up and down swing and the left and right swing can have different operating times, so that the swing operating trajectory of the swing rod assembly 52 is continuously changed, realizing large-scale stirring, and stirring There is no "dead zone" in the area, which improves the mixing efficiency. More specifically, one of the first control signal and the second control signal continues to be turned on, and the other of the first control signal and the second control signal is cut off for a preset time according to a preset cycle during the conduction process. The first motor and the second motor operate independently, and the up and down swings and left and right swings have different running times. The swing trajectories are constantly changing to achieve large-scale stirring.
该种实施方式下,整体的上下移动可通过安装座54上升降机构542实现,更具体地说,池壁上设有升降轨道543,安装座54上设有升降电机,安装座54与升降轨道543滑移配合,升降电机带动摆杆组件52沿升降轨道543移动,更进一步地,可将升降轨道543设计成三角函数式的谷峰波形,环绕池壁设置。In this embodiment, the overall upward and downward movement can be realized by the lifting mechanism 542 of the mounting base 54. More specifically, a lifting rail 543 is provided on the pool wall, and a lifting motor is provided on the mounting base 54. The mounting base 54 and the lifting rail 543 slip fit, the lifting motor drives the swing rod assembly 52 to move along the lifting track 543. Furthermore, the lifting track 543 can be designed into a trigonometric valley-peak waveform and set around the pool wall.
另一实施例中,可采用机械结构带动摆杆组件52摆动,具体实现方式为:驱动组件53包括在竖直平面做周向运动的转动件531以及连接转动件531和摆杆组件52的连接件532,摆杆组件52在连接件532的带动下相对池壁摆动。如图2所示,为了方便转动件531转动,转动件531设置在池壁上方,持续转动,通过连接件532与摆动组件相连接,转动件531转动过程中带动摆动组件摆动,从而实现大面积地搅拌,此时,摆杆组件52可不与池壁相连接,摆动组件在转动中的叶轮51和转动件531的作用下实现任意角度的摆动,从而加大搅拌面积,也可与池壁上的安装座54相连接,实现定点的变向搅拌。In another embodiment, a mechanical structure can be used to drive the swing bar assembly 52 to swing. The specific implementation method is: the driving assembly 53 includes a rotating member 531 that performs circumferential motion in a vertical plane and a connection connecting the rotating member 531 and the swing bar assembly 52 Part 532, the swing rod assembly 52 is driven by the connecting part 532 to swing relative to the pool wall. As shown in Figure 2, in order to facilitate the rotation of the rotating member 531, the rotating member 531 is set above the pool wall, continues to rotate, and is connected to the swing component through the connecting member 532. During the rotation of the rotating member 531, the swing component is driven to swing, thereby realizing a large area. At this time, the swing rod assembly 52 does not need to be connected to the pool wall. The swing assembly can swing at any angle under the action of the rotating impeller 51 and the rotating member 531, thereby increasing the mixing area. It can also be connected to the pool wall. The mounting base 54 is connected to realize the direction-changing mixing at a fixed point.
在该种方式下,整体的上下移动主要依靠收放机构533,更具体地说,连接件532为软质绳索,转动件531与连接件532的连接处设有用于收发连接件532的收放机构533,摆杆组件52在收发机构的作用下上下移动。通过连接件532的收放,整个摆杆组件52和叶轮51的整体升降,浓缩池40内设有轨道543,摆杆组件52与轨道543滑动连接,沿轨道543上下移动。In this way, the overall upward and downward movement mainly relies on the retractable and retractable mechanism 533. More specifically, the connecting member 532 is a soft rope. Mechanism 533, the swing rod assembly 52 moves up and down under the action of the sending and receiving mechanism. Through the retracting and unfolding of the connecting piece 532, the entire swing bar assembly 52 and the impeller 51 move up and down as a whole. A track 543 is provided in the concentration tank 40. The swing bar assembly 52 is slidingly connected to the track 543 and moves up and down along the track 543.
同时,为了确定摆杆组件52的摆动距离和升降距离,摆杆组件52上设有水压检测装置521,水压检测装置521与驱动机构相连接,当水压检测装置521检测到水压较低时,则驱动机构停止上升,降低高度,同时持续摆动,防止摆杆组件52空转。At the same time, in order to determine the swing distance and lifting distance of the pendulum assembly 52, a water pressure detection device 521 is provided on the pendulum assembly 52. The water pressure detection device 521 is connected to the driving mechanism. When the water pressure detection device 521 detects that the water pressure is relatively high, When it is low, the driving mechanism stops rising and lowers the height while continuing to swing to prevent the swing rod assembly 52 from idling.
一种污泥平衡池50,包括若干上述的摆式搅拌装置325,摆式搅拌装置325分散设置在污泥平衡池50的内壁上,对污泥平衡池50中的泥水实现全角度全方位的搅拌,实现泥水调匀均质,保证全池污泥浓度一致,不沉淀。相对于传统的定点定向搅拌装置325,可以减少搅拌装置325的数量,经实际测验可知,每池内安装数量相当于传统工艺的1/3。A sludge balancing tank 50 includes a plurality of the above-mentioned swing stirring devices 325. The swing stirring devices 325 are dispersedly arranged on the inner wall of the sludge balancing tank 50 to achieve full-angle and all-round mixing of the muddy water in the sludge balancing tank 50. Stir to achieve even mixing and homogeneity of mud and water, ensuring that the sludge concentration in the entire tank is consistent and does not settle. Compared with the traditional fixed-point directional stirring device 325, the number of stirring devices 325 can be reduced. Actual testing shows that the number installed in each pool is equivalent to 1/3 of the traditional process.
脱水系统60包括第二加压机构和2台离心脱水机,一用一备,单机能力12-15m3/h,电机功率N=22/7.5kW,变频调速。转鼓转速为max4000r/min,分离因数3200。脱水机房配套设备包含污泥进料螺杆泵、污泥切割机、自动投药溶药装置、加药螺杆泵、冲洗泵及螺旋输送机等。出泥含固率达到20-25%。The dehydration system 60 includes a second pressurizing mechanism and two centrifugal dehydrators, one for use and one for standby, with a single machine capacity of 12-15m3/h, motor power N=22/7.5kW, and variable frequency speed regulation. The drum speed is max4000r/min, and the separation factor is 3200. The supporting equipment of the dewatering machine room includes sludge feeding screw pumps, sludge cutting machines, automatic dosing and dissolving devices, dosing screw pumps, flushing pumps and screw conveyors. The solid content of the mud reaches 20-25%.
污泥储存系统70包括一座污泥料仓,用于脱水后的污泥储存,可储存5-7天泥量;料仓采用方形平底结构,储存的污泥仅靠重力自动下落,料仓规格为4000×3000×3600mm,有效容积为30m3;配套设施有:液压驱动滑架破拱装置、卸料螺旋、液压闸板阀、液压动力站、电控系统等。The sludge storage system 70 includes a sludge silo, which is used to store dehydrated sludge and can store sludge for 5-7 days; the silo adopts a square flat-bottom structure, and the stored sludge will automatically fall by gravity alone. Specifications of the silo It is 4000×3000×3600mm, with an effective volume of 30m3; supporting facilities include: hydraulic drive slide arch breaking device, discharge screw, hydraulic gate valve, hydraulic power station, electronic control system, etc.
基于上述系统,设计一种净水厂的排泥水处理方法,包括如下步骤:Based on the above system, design a muddy water treatment method for water purification plants, including the following steps:
设备准备步骤,调研净水厂空地情况,制作相应尺寸的钢制池体,运送至各个空地,而后通过管路进行组装,The equipment preparation step involves investigating the open space conditions of the water purification plant, making steel pool bodies of corresponding sizes, transporting them to various open spaces, and then assembling them through pipelines.
钢制池体包括分别与净水厂沉淀池、净水厂滤池相连接的若干集水井,用于浓缩泥水的浓缩池,用于使泥水均匀的污泥平衡池,脱水系统以及污泥储存系统;The steel tank body includes several water collection wells connected to the sedimentation tank and filter tank of the water purification plant respectively, a concentration tank for concentrating mud water, a sludge balancing tank for making mud water uniform, a dehydration system and sludge storage. system;
调节步骤,将净水厂原有废水池改建成组合式调节池,分隔成排水池和排泥池,与净水厂滤池相连接的集水井将滤池反冲洗水排入排水池,与净水厂沉淀池相连接的集水井将排泥水排入排泥池,排水池底部的底泥被吸至排泥池,上部的上清液回收利用,排泥池中的泥水排入浓缩池,期间向泥水中投加絮凝剂;In the adjustment step, the original wastewater pool of the water purification plant is transformed into a combined regulating pool, which is divided into a drainage pool and a mud drainage pool. The water collection well connected to the filter tank of the water purification plant discharges the filter backwash water into the drainage pool, and is connected to the drainage pool. The water collection well connected to the sedimentation tank of the water purification plant discharges the sludge water into the sludge drainage tank. The sediment at the bottom of the drainage tank is sucked into the sludge drainage tank. The upper supernatant is recycled and used. The mud water in the sludge drainage tank is discharged into the concentration tank. , during which flocculant is added to the muddy water;
浓缩步骤,泥水进入钢制池体的浓缩池,通过均匀进泥水结构,在浓缩池中均匀进水、沉泥、分离泥水,而后将浓缩池上部的上清液回收利用,下部的泥浆排入污泥平衡池;In the concentration step, the muddy water enters the concentration tank with a steel tank body. Through the uniform mudwater feeding structure, water is evenly fed, sedimented, and muddy water is separated in the concentration tank. Then the supernatant liquid in the upper part of the concentration tank is recycled, and the mud in the lower part is discharged into the concentration tank. sludge balancing tank;
污泥平衡及脱水步骤,进入污泥平衡池中的泥浆经摆式搅拌装置搅拌均匀,而后将调制平衡的泥浆输送至脱水系统中进行机械脱水,泥块储存在污泥储存系统中,定期外运。In the sludge balance and dehydration step, the mud entering the sludge balance tank is stirred evenly by the pendulum stirring device, and then the balanced mud is transported to the dehydration system for mechanical dehydration. The mud blocks are stored in the sludge storage system and are periodically removed. transport.
上述实施方式仅为本发明的优选实施方式,不能以此来限定本发明保护的范围,本领域的技术人员在本发明的基础上所做的任何非实质性的变化及替换均属于本发明所要求保护的范围。The above-mentioned embodiments are only preferred embodiments of the present invention and cannot be used to limit the scope of protection of the present invention. Any non-substantive changes and substitutions made by those skilled in the art on the basis of the present invention fall within the scope of the present invention. Scope of protection claimed.
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