WO2018032805A1 - Multi-stage purification treatment system for residual water from treatment of contaminated bottom sludge from river or lake - Google Patents

Multi-stage purification treatment system for residual water from treatment of contaminated bottom sludge from river or lake Download PDF

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Publication number
WO2018032805A1
WO2018032805A1 PCT/CN2017/083570 CN2017083570W WO2018032805A1 WO 2018032805 A1 WO2018032805 A1 WO 2018032805A1 CN 2017083570 W CN2017083570 W CN 2017083570W WO 2018032805 A1 WO2018032805 A1 WO 2018032805A1
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Prior art keywords
residual water
water
river
treatment
stage
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PCT/CN2017/083570
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French (fr)
Chinese (zh)
Inventor
陶明
翟德勤
禹芝文
陈士强
田卫红
赵明江
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中电建水环境治理技术有限公司
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Publication of WO2018032805A1 publication Critical patent/WO2018032805A1/en

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/48Treatment of water, waste water, or sewage with magnetic or electric fields
    • C02F1/488Treatment of water, waste water, or sewage with magnetic or electric fields for separation of magnetic materials, e.g. magnetic flocculation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/54Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
    • C02F1/56Macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F2001/007Processes including a sedimentation step
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/007Contaminated open waterways, rivers, lakes or ponds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00Controlling or monitoring parameters in water treatment
    • C02F2209/11Turbidity

Definitions

  • the invention belongs to the technical field of sewage treatment, and particularly relates to a multi-stage purification treatment system for residual water treatment of river and lake pollution.
  • the river channel is a kind of open water area with narrow water surface and long process. In many places, the river channel has become a gathering place for various polluted water bodies. Due to years of sedimentation, polluted sediments are formed. Contaminated sediment is an intrinsic source of pollution that affects the quality of the water environment.
  • Environmental dredging is an important means of controlling heavy polluted water bodies. By dredging contaminated sediments, endogenous pollutants in polluted water bodies can be removed.
  • the traditional dredging project can achieve high-efficiency mud-water separation by using natural sedimentation method because its dredged mud is mainly inorganic particles and has a high density.
  • the content of organic clay in the fine clay in the dredged mud is continuously increased, which makes it difficult to achieve settlement under natural conditions.
  • the sludge sediment is broken, and the release of pollutants is enhanced, so that the residual water contains a large amount of pollutants rich in the sediment. Most of these substances adhere to the fine particles and are suspended in the residual water. It is difficult to settle.
  • the currently widely used residual water treatment technology utilizes chemical flocculation to treat residual water.
  • the chemical flocculant has the functions of compressing the electric double layer and adsorbing the bridge, so that the residual water can be gathered together to form flocculation and de-stabilization, and the purpose of purifying the residual water is achieved.
  • the usual treatment method is that the residual water is initially set by the sedimentation tank, and the supernatant liquid is taken out and introduced into the remaining pool. Dredged bottom mud is a complex and stable dispersion system.
  • the use of flocculant has a certain treatment effect, due to the prior art in the treatment of residual water, only the single equipment or components of the sedimentation tank are the main design body. Due to the limitation of the structure and function of the pool body, the amount of residual water treatment is small, and the rapid purification of residual water cannot be achieved, and the residual water purification effect is poor.
  • the products after the dredged sediment treatment mainly include residual water, residual sand, residual soil, etc., wherein the residual water treatment reaches the standard and returns to the river.
  • the discharge standard for residual water treatment stipulates that the treated residual water needs to meet the secondary emission standard stipulated in the Integrated Wastewater Discharge Standard (GB8978-1996).
  • the main object of the present invention is to provide a multi-stage purification treatment system for treating residual water in rivers and lakes, which aims to solve the problem that the conventional residual water treatment technology cannot achieve rapid purification of residual water and poor purification of residual water. problem.
  • the present invention is realized in this way, a multi-stage purification treatment system for treating residual water in rivers and lakes, including:
  • a primary sedimentation tank for removing natural particles from the residual water in series according to a residual water treatment path, a secondary sedimentation tank for intercepting particulate matter removed from the residual water, and a suspension for adsorbing and removing residual water
  • Three-stage magnetic filter purification device for removing natural particles from the residual water in series according to a residual water treatment path, a secondary sedimentation tank for intercepting particulate matter removed from the residual water, and a suspension for adsorbing and removing residual water
  • the primary sedimentation tank comprises a first pool body provided with a feed port, a slurry outlet and a water outlet;
  • the secondary sedimentation tank comprises a second pool body and is disposed in the second pool body
  • the auxiliary sinking device divides the second pool body into an upper clear water overflow area and a lower mud settling area, and the second pool body is provided with a water inlet connected to the water outlet, a fresh water outlet for discharging fresh water overflowing from the upper fresh water overflow region and a sludge discharge port for discharging sludge settled in the lower mud sedimentation zone;
  • the three-stage magnetic filter purification device including a dosing connected to the water clearing port a coagulation device and a magnetic filter device coupled to the dosing coagulation device.
  • the first cell body is provided with a decanter for flowing the supernatant liquid in the first cell body from the water outlet port to the second cell body.
  • the auxiliary sink device is configured as a subsidence sloping plate and/or a sloping inclined tube.
  • an end of the auxiliary sink device is provided with an overflow raft.
  • the auxiliary sinking device is disposed in plurality, and the plurality of the assisting and sinking devices are sequentially arranged according to the residual water treatment path, and each of the two auxiliary lifting devices is separated by a partition wall; The upper part of the partition wall is provided with a clear water overflow port.
  • the medicinal coagulation device includes a coagulation reactor and a dosing device connected to the coagulation reactor.
  • the dosing device includes a PAM dosing device and a P respectively connected to the coagulation reactor AC dosing device.
  • the first cell body is connected to the PAM dosing device; the second cell body is connected to the PAC dosing device.
  • the sludge settled in the lower mud settling zone is discharged into the conditioning system through the mud pump.
  • an online turbidimeter is disposed in the first cell body.
  • the present invention adopts a primary sedimentation tank, a secondary sedimentation tank and a three-stage magnetic filter purification device which are sequentially arranged in series, so that the residual water first passes through the natural settlement of the first pool body, and the coarse particulate matter is initially settled and discharged from the water outlet.
  • the supernatant liquid enters the second pool body, further intercepts the fine particles in the residual water by the auxiliary sinking device, and the auxiliary sinking device divides the second pool body into the upper clear water overflow area and the lower mud sedimentation area, and the fine particles are trapped and then fall into In the lower mud sedimentation zone, the overflow water in the clear water overflow zone enters the three-stage magnetic filter purification device, and the fine suspension of the residual water is adsorbed and removed by the drug coagulation and the release and recovery of the magnetic powder in the magnetic filter device.
  • the residual water treated by the first-stage sedimentation tank, the second-stage sedimentation tank and the three-stage magnetic filter purification device is directly discharged into the “returning river” after passing the test.
  • the multi-stage purification of the residual water in the river and lake sediments of the present invention is purified.
  • the treatment system after passing through the first-stage sedimentation tank and the second-stage sedimentation tank, enters the three-stage magnetic filter device, and filters the residual water by stepwise and systematically, without
  • the treatment reduces the concentration of pollutants in the river water body, and because the residual water circulates in the system consisting of the series first-stage sedimentation tank, the second-stage sedimentation tank and the three-stage magnetic filter purification device, the residual water stays in the system for a short time.
  • the sewage with higher turbidity can be treated, the amount of residual water treatment is large, and the residual water treatment efficiency is high, so that the same purification of residual water is achieved, so that the residual water purification effect is good, and the system covers an area. small.
  • FIG. 1 is a schematic structural view of a multi-stage purification treatment system for treating residual water in rivers and lakes;
  • FIG. 2 is a schematic structural view of a first-stage sedimentation tank of a multi-stage purification treatment system for treating residual water in rivers and lakes;
  • FIG. 3 is a second embodiment of a multi-stage purification treatment system for residual water treatment of river and lake sediments provided by an embodiment of the present invention. Schematic diagram of the stage sedimentation tank;
  • FIG. 4 is a schematic structural view of a three-stage magnetic filter purification device for a multi-stage purification treatment system for a river water rushing sediment sludge treatment residual water supply according to an embodiment of the present invention.
  • the present invention provides a multi-stage purification treatment system for treating residual water in rivers and lakes, which is used for systemic and step-by-step impurity removal and harmless treatment of residual water to reduce pollutants in river water bodies.
  • the concentration makes the treated residual water reach the discharge standard.
  • it can treat sewage with higher turbidity, large residual water treatment, high residual water treatment efficiency, quick purification of residual water, good residual water purification effect, and The area is small.
  • the multi-stage purification treatment system for the residual water treatment of the river and lake sediments includes: a first-stage sedimentation tank for removing natural particles from the residual water in series according to the residual water treatment path.
  • a secondary sedimentation tank 2 for trapping particulate matter in the residual water and a three-stage magnetic filter purification device 3 for adsorbing and removing the suspended matter in the residual water;
  • the primary sedimentation tank 1 includes a slurry inlet 111
  • the secondary sedimentation tank 2 includes a second pool body 21 and a subsidence device 22 disposed in the second pool body 21, and the auxiliary sink device 22 will be the second pool
  • the body 21 is divided into an upper fresh water overflow area 214 and a lower mud settling area 215, and the second pool body 21 is provided with a water inlet 211 communicating with the water outlet 113 for discharging the upper clear water overflow.
  • the tertiary magnetic filter purification device 3 includes a dosing and coagulation device 31 communicating with the fresh water outlet 213 and The magnetic filter device 32 to which the dosing and coagulation device 31 is connected.
  • the first-stage sedimentation tank 1, the second-stage sedimentation tank 2, and the three-stage magnetic filter purification device 3 are sequentially arranged in series, so that the residual water first passes through the natural settlement of the first pool body 11, and the coarse particulate matter is initially settled.
  • the supernatant discharged from the water outlet 113 is further introduced into the second cell body 21, and the fine particles in the residual water are further intercepted by the assisting device 22, and the auxiliary sinking device 22 divides the second cell body 21 into the upper fresh water overflow region 214.
  • the release and recovery of the magnetic powder to adsorb and remove the fine suspension in the residual water, and the residual water treated by the first-stage sedimentation tank 1 and the secondary sedimentation tank by the 2nd and 3rd-stage magnetic filter purification device 3 is directly tested.
  • the multi-stage purification treatment system for the treatment of residual water in rivers and lakes of the present invention, after the first-stage sedimentation tank 1, the second-stage sedimentation tank 2, and then enter the three-stage magnetic filter device 3, step by step Systematicly filtering and resolving impurities in the residual water, reducing the concentration of pollutants in the river water, and the system can treat sewage with higher turbidity, and because the residual water stays in the system is short,
  • the utility model has the advantages of large residual water treatment and high residual water treatment efficiency, thereby achieving the purpose of rapid purification of the residual water, and the same, the residual water purification effect is good, and the floor space is small.
  • the first pool body 11 is provided with a decanter for draining the supernatant liquid in the first pool body 11 from the water outlet 113 into the second pool body 21. 12.
  • the supernatant in the first cell body 11 is more conveniently drained into the second cell body 21 by the decanter 12 provided.
  • the value indicates that the decanter 12 can employ the conventional techniques of the prior art.
  • the decanter 12 is disposed at the water outlet 113.
  • an in-line turbidimeter 13 is disposed in the first cell body 11, and specifically, the in-line turbidimeter 13 is located on the first cell body 11 on one side of the slurry inlet port 111. The turbidity of the residual water in the first cell body 11 can be measured by setting the online turbidimeter 13.
  • the auxiliary sink device 22 is configured as a subsidence sloping plate and/or a sinker tube.
  • An overflow raft 25 is provided at the end of the assisting device 22.
  • the overflow weir plate 25 helps to maintain an even overflow of the overflow water of the upper fresh water overflow area 214.
  • the auxiliary lifting device 22 may be disposed in plurality, and the plurality of auxiliary lifting devices 22 are sequentially arranged according to the residual water treatment path, and each of the two auxiliary lifting devices 22 is separated by the partition wall 24; A clear water overflow port 241 is provided at the upper portion.
  • a diversion tank is disposed at the fresh water overflow port 241 of the partition wall 24, and the diverting trough is located between the overflow weir plate 25 and the partition wall 24, so as to facilitate the overflow and sinking of the clean water step by step. Drop.
  • the overflow water of the upper fresh water overflow zone 214 can be pumped into the coagulation reactor 311 by a clean water pump.
  • the assisting and sinking device 22 includes a first auxiliary sloping plate 221, a second auxiliary slanting tube 222, and a third auxiliary slanting tube 223 which are sequentially spaced according to the residual water treatment path.
  • the supernatant entering the second cell body 21 further intercepts the fine particles in the residual water through the auxiliary sinking device. Specifically, the supernatant liquid passes through the first auxiliary sloping plate 21, and the first auxiliary sloping plate 221 will be compared. After the coarse particles are trapped, the fine particles are again trapped by the interception of the second auxiliary inclined tube 222 and the third auxiliary inclined tube 223, passing through the first auxiliary inclined plate 221 in the second pool body 21, The second auxiliary inclined tube 222 and the third auxiliary inclined inclined tube 223 are stepped and overflowed to further remove fine particles in the residual water.
  • the sludge settled in the lower mud settling zone 215 is discharged into the conditioning system through the mud pump 23. It is worth noting that the slurry that has been initially concentrated in the prior art is also transported to the conditioning system by a small cutter suction boat. The purpose of the prior art conditioning system is to condition the mud slurry for conditioning treatment. Therefore, in the present invention, the sludge settled in the lower mud settling area 215 is discharged into the conditioning system, and the mud of the second pool body 21 is prevented from being separately treated, discharged into the conditioning system, and then directly subjected to subsequent treatment, thereby further improving the fouling. Mud treatment efficiency.
  • the slurry settled in the lower mud settling zone 215 can also be discharged into the first cell body 11 through the slurry pump 23.
  • the slurry pump 23 By directly pumping the slurry in the second cell body 21 into the first cell body 11, and then passing through the slurry outlet 112 of the first cell body 11 and discharging it, it is also possible to avoid the separate treatment of the slurry of the second cell body 21. At the same time, the efficiency of sludge removal is improved.
  • the dosing and coagulation device 31 includes a coagulation reactor 311 and a dosing device connected to the coagulation reactor 311.
  • the dosing device includes a PAM dosing device 312 and a PAC dosing device 313 which are respectively connected to the coagulation reactor 311.
  • the PAM dosing device 312 can add PAM to the coagulation reactor 311 by providing a metering pump.
  • PAM polyacrylamide
  • the PAC dosing device 313 can add PAC to the coagulation reactor 311 by providing a metering pump, which is also commonly referred to as a water purifying agent or a coagulant, which is a water-soluble inorganic high molecular polymer.
  • the added PAM and PAC are mixed in the coagulation reactor 311.
  • the coagulation reactor 311 is provided with a stirring device, and the added PAM and PAC are mixed with the overflow water by a stirring device.
  • the first cell body 11 is connected to the PA M dosing device 312; 21 is connected to the PAC dosing device 313.
  • the first cell body 11 and the second cell body 21 may also be connected to the PAC dosing device 313.
  • the treated residual water can meet the secondary emission standards specified in the Integrated Wastewater Discharge Standard (GB8978-1996).
  • the suspended matter content value (ie, the SS value) of the recirculating residual water obtained by the residual water multi-stage purification device is less than 15 mg/l, and the COD, BOD, strontium, and barium contents are higher than that of the original river and lake.
  • the concentration of pollutant-containing indicators is reduced by more than 60%, and the recirculated residual water can be discharged back into rivers and lakes, which can effectively dilute and reduce the concentration of polluted water bodies in the original rivers and lakes.

Abstract

Provided is a multi-stage purification treatment system for residual water from the treatment of contaminated bottom sludge from a river or lake, the system comprising a primary sedimentation tank (1) for naturally settling and removing particulate matters in the residual water, a secondary sedimentation tank (2) for retaining and removing the particulate matters in the residual water, and a tertiary magnetic filter purification device (3) for adsorbing and removing suspended matters in the residual water, these being sequentially connected in series with one another according to a residual water treatment path, wherein the primary sedimentation tank (1) comprises a first tank body(11); the secondary sedimentation tank (2) comprises a second tank body (21) and a device aiding sedimentation (22); and the tertiary magnetic filter purification device (3) comprises a chemical feeding coagulation device (31) and a magnetic filter device (32) connected with the chemical feeding coagulation device (31). Impurities in the residual water are filtered out and detoxified systematically and step by step, so that the concentration of pollutants in water in river channels can be decreased; and waste water with a higher turbidity can be treated by the system. In addition, the system has a high residual water treatment capacity and a high residual water treatment efficiency, and occupies a small area.

Description

发明名称:河湖泊涌污染底泥处理余水多级净化处理系统 技术领域  Name of the invention: Multi-stage purification treatment system for residual water treatment of river and lake sediments
[0001] 本发明属于污水处理技术领域, 特别涉及一种河湖泊涌污染底泥处理余水多级 净化处理系统。  [0001] The invention belongs to the technical field of sewage treatment, and particularly relates to a multi-stage purification treatment system for residual water treatment of river and lake pollution.
背景技术  Background technique
[0002] 河道是一种幵放式水域, 水面窄、 流程长, 在很多地方, 河道成了各种污染水 体的汇集场所, 由于多年沉积, 形成污染底泥。 污染底泥是影响水环境质量的 内在污染源。  [0002] The river channel is a kind of open water area with narrow water surface and long process. In many places, the river channel has become a gathering place for various polluted water bodies. Due to years of sedimentation, polluted sediments are formed. Contaminated sediment is an intrinsic source of pollution that affects the quality of the water environment.
[0003] 环保疏浚是治理重污染水体的重要手段, 通过对污染底泥的疏浚, 可清除污染 水体的内源污染物。 传统的疏浚工程由于其疏浚泥浆主要是无机颗粒, 且密度 较大, 选用自然沉降方法就可以实现高效的泥水分离。 但近年来随着大量有机 物的污染物质被排放进入水体, 使疏浚泥浆中细粘粒的有机质土含量不断增高 , 这就很难实现在自然条件下的沉降。 并且在疏浚过程中污泥底泥被打碎, 强 化了污染物的释放, 使余水中含有大量的富含于底泥中的污染物质, 这些物质 大部分附着在细颗粒上、 悬浮在余水中, 很难沉降。  [0003] Environmental dredging is an important means of controlling heavy polluted water bodies. By dredging contaminated sediments, endogenous pollutants in polluted water bodies can be removed. The traditional dredging project can achieve high-efficiency mud-water separation by using natural sedimentation method because its dredged mud is mainly inorganic particles and has a high density. However, in recent years, as a large amount of organic pollutants are discharged into the water body, the content of organic clay in the fine clay in the dredged mud is continuously increased, which makes it difficult to achieve settlement under natural conditions. In the process of dredging, the sludge sediment is broken, and the release of pollutants is enhanced, so that the residual water contains a large amount of pollutants rich in the sediment. Most of these substances adhere to the fine particles and are suspended in the residual water. It is difficult to settle.
[0004] 为了解决上述技术问题, 目前应用比较广泛的余水处理技术是利用化学絮凝来 处理余水。 化学絮凝剂, 具有压缩双电层和吸附架桥的功能, 可以使余水中可 以聚集在一起形成絮凝脱, 进行脱稳, 实现余水净化目的。 通常处理方法是, 余水经沉淀池初凝、 上清液淅出后导入余水池。 疏浚底泥余水是一种复杂、 稳 定的分散体系, 絮凝剂的使用虽然具有一定的处理效果, 但由于现有技术在处 理余水吋, 仅以沉淀池的单一的设备或部件为设计主体, 且受池体结构和功能 的限制, 余水处理量小、 无法实现快速净化余水, 且余水净化效果差。  [0004] In order to solve the above technical problems, the currently widely used residual water treatment technology utilizes chemical flocculation to treat residual water. The chemical flocculant has the functions of compressing the electric double layer and adsorbing the bridge, so that the residual water can be gathered together to form flocculation and de-stabilization, and the purpose of purifying the residual water is achieved. The usual treatment method is that the residual water is initially set by the sedimentation tank, and the supernatant liquid is taken out and introduced into the remaining pool. Dredged bottom mud is a complex and stable dispersion system. Although the use of flocculant has a certain treatment effect, due to the prior art in the treatment of residual water, only the single equipment or components of the sedimentation tank are the main design body. Due to the limitation of the structure and function of the pool body, the amount of residual water treatment is small, and the rapid purification of residual water cannot be achieved, and the residual water purification effect is poor.
[0005] 此外, 需说明的是, 疏浚底泥处理后的产物主要有余水、 余砂、 余土等, 其中 , 余水处理达标后还河。 行业内对余水处理排放标准规定, 处理后的余水需达 到 《污水综合排放标准》 (GB8978-1996) 中规定的二级排放标准。  [0005] In addition, it should be noted that the products after the dredged sediment treatment mainly include residual water, residual sand, residual soil, etc., wherein the residual water treatment reaches the standard and returns to the river. In the industry, the discharge standard for residual water treatment stipulates that the treated residual water needs to meet the secondary emission standard stipulated in the Integrated Wastewater Discharge Standard (GB8978-1996).
技术问题 [0006] 本发明的主要目的在于提供一种河湖泊涌污染底泥处理余水多级净化处理系统 , 旨在解决传统余水处理技术存在的无法实现快速净化余水、 余水净化效果差 的问题。 technical problem [0006] The main object of the present invention is to provide a multi-stage purification treatment system for treating residual water in rivers and lakes, which aims to solve the problem that the conventional residual water treatment technology cannot achieve rapid purification of residual water and poor purification of residual water. problem.
问题的解决方案  Problem solution
技术解决方案  Technical solution
[0007] 本发明是这样实现的, 一种河湖泊涌污染底泥处理余水多级净化处理系统, 包 括:  [0007] The present invention is realized in this way, a multi-stage purification treatment system for treating residual water in rivers and lakes, including:
[0008] 按照余水处理路径依次串联的用于自然沉降去除余水中的颗粒物的一级沉淀池 、 用于截留去除余水中的颗粒物的二级沉淀池以及用于吸附去除余水中的悬浊 物的三级磁滤净化装置;  [0008] a primary sedimentation tank for removing natural particles from the residual water in series according to a residual water treatment path, a secondary sedimentation tank for intercepting particulate matter removed from the residual water, and a suspension for adsorbing and removing residual water Three-stage magnetic filter purification device;
[0009] 其中, 所述一级沉淀池包括设有进浆口、 出浆口和出水口的第一池体; 所述二 级沉淀池包括第二池体以及置于所述第二池体内的助沉装置, 所述助沉装置将 所述第二池体分隔成上部清水溢流区和下部泥浆沉降区, 所述第二池体设有与 所述出水口连通的进水口、 用于排出所述上部清水溢流区溢流的清水的清水口 以及用于排出所述下部泥浆沉降区沉降的污泥的排泥口; 所述三级磁滤净化装 置包括与所述清水口连通的加药混凝装置以及与所述加药混凝装置连接的磁滤 装置。  [0009] wherein the primary sedimentation tank comprises a first pool body provided with a feed port, a slurry outlet and a water outlet; the secondary sedimentation tank comprises a second pool body and is disposed in the second pool body The auxiliary sinking device divides the second pool body into an upper clear water overflow area and a lower mud settling area, and the second pool body is provided with a water inlet connected to the water outlet, a fresh water outlet for discharging fresh water overflowing from the upper fresh water overflow region and a sludge discharge port for discharging sludge settled in the lower mud sedimentation zone; the three-stage magnetic filter purification device including a dosing connected to the water clearing port a coagulation device and a magnetic filter device coupled to the dosing coagulation device.
[0010] 作为本发明的优选技术方案:  [0010] As a preferred technical solution of the present invention:
[0011] 进一步地, 所述第一池体内设有用于将所述第一池体内的上清液从所述出水口 弓 I流至所述第二池体内的滗水器。  [0011] Further, the first cell body is provided with a decanter for flowing the supernatant liquid in the first cell body from the water outlet port to the second cell body.
[0012] 进一步地, 所述助沉装置设为助沉斜板和 /或助沉斜管。  [0012] Further, the auxiliary sink device is configured as a subsidence sloping plate and/or a sloping inclined tube.
[0013] 进一步地, 所述助沉装置的端部设有溢流堰板。 [0013] Further, an end of the auxiliary sink device is provided with an overflow raft.
[0014] 进一步地, 所述助沉装置设置为多个, 多个的所述助沉装置按照余水处理路径 依次间隔布置, 每两个的所述助沉装置之间通过隔离墙隔幵; 所述隔离墙的上 部设有清水溢流口。  [0014] Further, the auxiliary sinking device is disposed in plurality, and the plurality of the assisting and sinking devices are sequentially arranged according to the residual water treatment path, and each of the two auxiliary lifting devices is separated by a partition wall; The upper part of the partition wall is provided with a clear water overflow port.
[0015] 进一步地, 所述加药混凝装置包括混凝反应器以及与所述混凝反应器连接的加 药装置。  Further, the medicinal coagulation device includes a coagulation reactor and a dosing device connected to the coagulation reactor.
[0016] 进一步地, 所述加药装置包括分别与所述混凝反应器连接的 PAM加药装置和 P AC加药装置。 [0016] Further, the dosing device includes a PAM dosing device and a P respectively connected to the coagulation reactor AC dosing device.
[0017] 进一步地, 所述第一池体与所述 PAM加药装置相连; 所述第二池体与所述 PAC 加药装置相连。  [0017] Further, the first cell body is connected to the PAM dosing device; the second cell body is connected to the PAC dosing device.
[0018] 进一步地, 所述下部泥浆沉降区沉降的污泥通过泥浆泵排入调理系统内。  [0018] Further, the sludge settled in the lower mud settling zone is discharged into the conditioning system through the mud pump.
[0019] 进一步地, 所述第一池体内设有在线浊度仪。 [0019] Further, an online turbidimeter is disposed in the first cell body.
发明的有益效果  Advantageous effects of the invention
有益效果  Beneficial effect
[0020] 本发明通过依次串联设置的一级沉淀池、 二级沉淀池以及三级磁滤净化装置, 使得余水先经过第一池体的自然沉降, 粗颗粒物初步沉降下来, 从出水口排出 的上清液再进入第二池体内, 通过助沉装置进一步截留余水中的细颗粒物, 助 沉装置将第二池体分隔成上部清水溢流区和下部泥浆沉降区, 细颗粒物被截留 后落入下部泥浆沉降区, 清水溢流区的溢流水再进入三级磁滤净化装置, 通过 加药混凝并利用磁滤装置中的磁粉的释放和回收来吸附去除余水中的细微悬浊 物, 经一级沉淀池、 二级沉淀池以及三级磁滤净化装置处理后的余水经检测合 格后直接"还河"排放, 综上, 本发明的河湖泊涌污染底泥处理余水多级净化处理 系统, 经过一级沉淀池、 二级沉淀池后, 再进入三级磁滤装置, 通过逐级地、 系统性地对余水进行杂质滤除、 无害化处理, 降低了河道水体污染物浓度, 且 由于余水在串联的一级沉淀池、 二级沉淀池以及三级磁滤净化装置构成的系统 内流通, 余水在系统内的停留吋间短, 相对于现有技术, 可以处理浊度更高的 污水、 余水处理量大、 余水处理效率高, 从而实现快速净化余水的同吋使得余 水净化效果好, 且该系统占地面积小。  [0020] The present invention adopts a primary sedimentation tank, a secondary sedimentation tank and a three-stage magnetic filter purification device which are sequentially arranged in series, so that the residual water first passes through the natural settlement of the first pool body, and the coarse particulate matter is initially settled and discharged from the water outlet. The supernatant liquid enters the second pool body, further intercepts the fine particles in the residual water by the auxiliary sinking device, and the auxiliary sinking device divides the second pool body into the upper clear water overflow area and the lower mud sedimentation area, and the fine particles are trapped and then fall into In the lower mud sedimentation zone, the overflow water in the clear water overflow zone enters the three-stage magnetic filter purification device, and the fine suspension of the residual water is adsorbed and removed by the drug coagulation and the release and recovery of the magnetic powder in the magnetic filter device. The residual water treated by the first-stage sedimentation tank, the second-stage sedimentation tank and the three-stage magnetic filter purification device is directly discharged into the “returning river” after passing the test. In summary, the multi-stage purification of the residual water in the river and lake sediments of the present invention is purified. The treatment system, after passing through the first-stage sedimentation tank and the second-stage sedimentation tank, enters the three-stage magnetic filter device, and filters the residual water by stepwise and systematically, without The treatment reduces the concentration of pollutants in the river water body, and because the residual water circulates in the system consisting of the series first-stage sedimentation tank, the second-stage sedimentation tank and the three-stage magnetic filter purification device, the residual water stays in the system for a short time. Compared with the prior art, the sewage with higher turbidity can be treated, the amount of residual water treatment is large, and the residual water treatment efficiency is high, so that the same purification of residual water is achieved, so that the residual water purification effect is good, and the system covers an area. small.
对附图的简要说明  Brief description of the drawing
附图说明  DRAWINGS
[0021] 图 1是本发明实施例提供的河湖泊涌污染底泥处理余水多级净化处理系统的结 构示意图;  1 is a schematic structural view of a multi-stage purification treatment system for treating residual water in rivers and lakes;
[0022] 图 2是本发明实施例提供的河湖泊涌污染底泥处理余水多级净化处理系统的一 级沉淀池的结构示意图;  [0022] FIG. 2 is a schematic structural view of a first-stage sedimentation tank of a multi-stage purification treatment system for treating residual water in rivers and lakes;
[0023] 图 3是本发明实施例提供的河湖泊涌污染底泥处理余水多级净化处理系统的二 级沉淀池的结构示意图; [0023] FIG. 3 is a second embodiment of a multi-stage purification treatment system for residual water treatment of river and lake sediments provided by an embodiment of the present invention. Schematic diagram of the stage sedimentation tank;
[0024] 图 4是本发明实施例提供的河湖泊涌污染底泥处理余水多级净化处理系统的三 级磁滤净化装置的结构示意图。 4 is a schematic structural view of a three-stage magnetic filter purification device for a multi-stage purification treatment system for a river water rushing sediment sludge treatment residual water supply according to an embodiment of the present invention.
[0025] 图中: 1-一级沉淀池, 11-第一池体, 111-进浆口, 112-出浆口, 113-出水口, 1 2-滗水器, 13-在线浊度仪, 2-二级沉淀池, 21-第二池体, 211-进水口, 212-排 泥口, 213-清水口, 214-上部清水溢流区, 215-下部泥浆沉降区, 22-助沉装置, 221-第一助沉斜板, 222-第二助沉斜管, 223-第三助沉斜管, 23-泥浆泵, 24-隔 离墙, 241-溢流口, 25-溢流堰板, 3-三级磁滤净化装置, 31-加药混凝装置, 311 -混凝反应器, 312-PAM加药装置, 313-PAC加药装置, 32-磁滤装置。 [0025] In the figure: 1-prime sedimentation tank, 11-first cell body, 111-slurry port, 112-slurry port, 113-outlet, 1 2-drinker, 13-line turbidimeter , 2-Secondary sedimentation tank, 21-Second tank body, 211-inlet, 212-drain, 213-clear, 214- upper clear water overflow, 215-low mud subsidence area, 22-assisted sink , 221 - first auxiliary inclined sloping plate, 222 - second auxiliary inclined inclined pipe, 223 - third auxiliary inclined inclined pipe, 23 - mud pump, 24-wall, 241 - overflow port, 25 - overflow weir , 3-level magnetic filter purification device, 31-dosing coagulation device, 311-coagulation reactor, 312-PAM dosing device, 313-PAC dosing device, 32-magnetic filter device.
本发明的实施方式 Embodiments of the invention
[0026] 为了使本发明的目的、 技术方案及优点更加清楚明白, 以下结合附图及实施例 , 对本发明进行进一步详细说明。 应当理解, 此处所描述的具体实施例仅仅用 以解释本发明, 并不用于限定本发明。  The present invention will be further described in detail below with reference to the accompanying drawings and embodiments. It is understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
[0027] 需要说明的是, 当元件被称为 "固定于"或"设置于"另一个元件, 它可以直接在 另一个元件上或者间接在该另一个元件上。 当一个元件被称为"连接于 "另一个元 件, 它可以是直接连接到另一个元件或间接连接至该另一个元件。  [0027] It is to be noted that when an element is referred to as being "fixed" or "in" another element, it can be directly on the other element or indirectly. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or indirectly connected to the other element.
[0028] 本发明提供一种河湖泊涌污染底泥处理余水多级净化处理系统, 用于系统性、 逐级地对余水进行杂质滤除、 无害化处理, 以降低河道水体污染物浓度, 使得 处理后的余水达到排放标准, 同吋, 可以处理浊度更高的污水、 余水处理量大 、 余水处理效率高、 实现快速净化余水, 余水净化效果好, 且占地面积小。  [0028] The present invention provides a multi-stage purification treatment system for treating residual water in rivers and lakes, which is used for systemic and step-by-step impurity removal and harmless treatment of residual water to reduce pollutants in river water bodies. The concentration makes the treated residual water reach the discharge standard. At the same time, it can treat sewage with higher turbidity, large residual water treatment, high residual water treatment efficiency, quick purification of residual water, good residual water purification effect, and The area is small.
[0029] 请参阅附图 1~4, 该河湖泊涌污染底泥处理余水多级净化处理系统包括: 按照 余水处理路径依次串联的用于自然沉降去除余水中的颗粒物的一级沉淀池 1、 用 于截留去除余水中的颗粒物的二级沉淀池 2以及用于吸附去除余水中的悬浊物的 三级磁滤净化装置 3; 其中, 一级沉淀池 1包括设有进浆口 111、 出浆口 112和出 水口 113的第一池体 11; 二级沉淀池 2包括第二池体 21以及置于第二池体 21内的 助沉装置 22, 助沉装置 22将第二池体 21分隔成上部清水溢流区 214和下部泥浆沉 降区 215, 第二池体 21设有与出水口 113连通的进水口 211、 用于排出上部清水溢 流区 214溢流的清水的清水口 213以及用于排出下部泥浆沉降区 215沉降的污泥的 排泥口 212; 三级磁滤净化装置 3包括与清水口 213连通的加药混凝装置 31以及与 加药混凝装置 31连接的磁滤装置 32。 [0029] Referring to FIG. 1 to FIG. 4, the multi-stage purification treatment system for the residual water treatment of the river and lake sediments includes: a first-stage sedimentation tank for removing natural particles from the residual water in series according to the residual water treatment path. A secondary sedimentation tank 2 for trapping particulate matter in the residual water and a three-stage magnetic filter purification device 3 for adsorbing and removing the suspended matter in the residual water; wherein the primary sedimentation tank 1 includes a slurry inlet 111 The first pool body 11 of the slurry outlet 112 and the water outlet 113; the secondary sedimentation tank 2 includes a second pool body 21 and a subsidence device 22 disposed in the second pool body 21, and the auxiliary sink device 22 will be the second pool The body 21 is divided into an upper fresh water overflow area 214 and a lower mud settling area 215, and the second pool body 21 is provided with a water inlet 211 communicating with the water outlet 113 for discharging the upper clear water overflow. a fresh water outlet 213 overflowing the flow area 214 and a sludge discharge port 212 for discharging sludge settled in the lower mud settling area 215; the tertiary magnetic filter purification device 3 includes a dosing and coagulation device 31 communicating with the fresh water outlet 213 and The magnetic filter device 32 to which the dosing and coagulation device 31 is connected.
[0030] 本发明实施例通过依次串联设置的一级沉淀池 1、 二级沉淀池 2以及三级磁滤净 化装置 3, 使得余水先经过第一池体 11的自然沉降, 粗颗粒物初步沉降下来, 从 出水口 113排出的上清液再进入第二池体 21内, 通过助沉装置 22进一步截留余水 中的细颗粒物, 助沉装置 22将第二池体 21分隔成上部清水溢流区 214和下部泥浆 沉降区 215, 细颗粒物被截留后落入下部泥浆沉降区 215, 清水溢流区 214的溢流 水再进入三级磁滤净化装置 3, 通过加药混凝并利用磁滤装置 32中的磁粉的释放 和回收来吸附去除余水中的细微悬浊物, 经一级沉淀池 1、 二级沉淀池以 2及三 级磁滤净化装置 3处理后的余水经检测合格后直接"还河"排放, 本发明的河湖泊 涌污染底泥处理余水多级净化处理系统, 经过一级沉淀池 1、 二级沉淀池 2后, 再进入三级磁滤装置 3, 逐级地、 系统性地对余水进行杂质滤除、 无害化处理, 降低了河道水体污染物浓度, 且该系统可以处理浊度更高的污水, 且由于余水 在系统内的停留吋间短, 使得余水处理量大、 余水处理效率高, 从而实现了对 余水的快速净化的目的, 同吋, 余水净化效果好, 占地面积小。  [0030] In the embodiment of the present invention, the first-stage sedimentation tank 1, the second-stage sedimentation tank 2, and the three-stage magnetic filter purification device 3 are sequentially arranged in series, so that the residual water first passes through the natural settlement of the first pool body 11, and the coarse particulate matter is initially settled. The supernatant discharged from the water outlet 113 is further introduced into the second cell body 21, and the fine particles in the residual water are further intercepted by the assisting device 22, and the auxiliary sinking device 22 divides the second cell body 21 into the upper fresh water overflow region 214. And the lower mud settling zone 215, the fine particles are intercepted and then fall into the lower mud settling zone 215, and the overflow water of the clean water overflow zone 214 enters the third-stage magnetic filter purifying device 3, through the dosing and coagulation and utilizing the magnetic filter device 32 The release and recovery of the magnetic powder to adsorb and remove the fine suspension in the residual water, and the residual water treated by the first-stage sedimentation tank 1 and the secondary sedimentation tank by the 2nd and 3rd-stage magnetic filter purification device 3 is directly tested. River "discharge, the multi-stage purification treatment system for the treatment of residual water in rivers and lakes of the present invention, after the first-stage sedimentation tank 1, the second-stage sedimentation tank 2, and then enter the three-stage magnetic filter device 3, step by step Systematicly filtering and resolving impurities in the residual water, reducing the concentration of pollutants in the river water, and the system can treat sewage with higher turbidity, and because the residual water stays in the system is short, The utility model has the advantages of large residual water treatment and high residual water treatment efficiency, thereby achieving the purpose of rapid purification of the residual water, and the same, the residual water purification effect is good, and the floor space is small.
[0031] 具体地, 请参阅图 1和图 2, 第一池体 11内设有用于将第一池体 11内的上清液从 出水口 113引流至第二池体 21内的滗水器 12。 通过设置的滗水器 12更方便地将第 一池体 11内的上清液引流至第二池体 21内。 值的说明的是, 滗水器 12可以采用 现有技术常规的技术手段。 滗水器 12设置在出水口 113处。 进一步地, 第一池体 11内设有在线浊度仪 13, 具体地, 在线浊度仪 13位于进浆口 111的一侧的第一池 体 11上。 通过设置在线浊度仪 13可以测量第一池体 11内余水的浊度。  Specifically, referring to FIG. 1 and FIG. 2, the first pool body 11 is provided with a decanter for draining the supernatant liquid in the first pool body 11 from the water outlet 113 into the second pool body 21. 12. The supernatant in the first cell body 11 is more conveniently drained into the second cell body 21 by the decanter 12 provided. The value indicates that the decanter 12 can employ the conventional techniques of the prior art. The decanter 12 is disposed at the water outlet 113. Further, an in-line turbidimeter 13 is disposed in the first cell body 11, and specifically, the in-line turbidimeter 13 is located on the first cell body 11 on one side of the slurry inlet port 111. The turbidity of the residual water in the first cell body 11 can be measured by setting the online turbidimeter 13.
[0032] 进一步地, 请参阅图 1和图 3, 助沉装置 22设为助沉斜板和 /或助沉斜管。 助沉 装置 22的端部设有溢流堰板 25。 溢流堰板 25有助于维持上部清水溢流区 214的溢 流水均匀溢出。 具体地, 助沉装置 22可设置为多个, 多个的助沉装置 22按照余 水处理路径依次间隔布置, 每两个的助沉装置 22之间通过隔离墙 24隔幵; 隔离 墙 24的上部设有清水溢流口 241。 具体地, 在隔离墙 24的清水溢流口 241处设有 分流槽, 分流槽位于溢流堰板 25与隔离墙 24间, 便于清水逐级地进行溢流和沉 降。 另外, 上部清水溢流区 214的溢流水可通过清水泵泵入混凝反应器 311中。 优选地, 助沉装置 22包括按照余水处理路径依次间隔布置的第一助沉斜板 221、 第二助沉斜管 222和第三助沉斜管 223。 进入第二池体 21内的上清液进一步通过 助沉装置进一步截留余水中的细颗粒物, 具体地, 上清液先经过第一助沉斜板 2 21, 第一助沉斜板 221将较粗的颗粒物截留后, 再通过第二助沉斜管 222和第三 助沉斜管 223的截留, 较细的颗粒物再次被截留, 经过第二池体 21内的第一助沉 斜板 221、 第二助沉斜管 222和第三助沉斜管 223, 逐级溢流沉降, 进一步去除余 水中的较细颗粒。 [0032] Further, referring to FIG. 1 and FIG. 3, the auxiliary sink device 22 is configured as a subsidence sloping plate and/or a sinker tube. An overflow raft 25 is provided at the end of the assisting device 22. The overflow weir plate 25 helps to maintain an even overflow of the overflow water of the upper fresh water overflow area 214. Specifically, the auxiliary lifting device 22 may be disposed in plurality, and the plurality of auxiliary lifting devices 22 are sequentially arranged according to the residual water treatment path, and each of the two auxiliary lifting devices 22 is separated by the partition wall 24; A clear water overflow port 241 is provided at the upper portion. Specifically, a diversion tank is disposed at the fresh water overflow port 241 of the partition wall 24, and the diverting trough is located between the overflow weir plate 25 and the partition wall 24, so as to facilitate the overflow and sinking of the clean water step by step. Drop. In addition, the overflow water of the upper fresh water overflow zone 214 can be pumped into the coagulation reactor 311 by a clean water pump. Preferably, the assisting and sinking device 22 includes a first auxiliary sloping plate 221, a second auxiliary slanting tube 222, and a third auxiliary slanting tube 223 which are sequentially spaced according to the residual water treatment path. The supernatant entering the second cell body 21 further intercepts the fine particles in the residual water through the auxiliary sinking device. Specifically, the supernatant liquid passes through the first auxiliary sloping plate 21, and the first auxiliary sloping plate 221 will be compared. After the coarse particles are trapped, the fine particles are again trapped by the interception of the second auxiliary inclined tube 222 and the third auxiliary inclined tube 223, passing through the first auxiliary inclined plate 221 in the second pool body 21, The second auxiliary inclined tube 222 and the third auxiliary inclined inclined tube 223 are stepped and overflowed to further remove fine particles in the residual water.
[0033] 优选地, 下部泥浆沉降区 215沉降的污泥通过泥浆泵 23排入调理系统内。 值得 说明的是, 现有技术中经初步浓缩后的泥浆还会由小型绞吸船输送至调理系统 , 现有技术设置调理系统的目的在于对泥浆进行调理改性处理。 因此, 本发明 中通过将下部泥浆沉降区 215沉降的污泥排入调理系统内, 避免单独对第二池体 21的泥浆进行处理, 排入调理系统后再直接进行后续处理, 进一步提高了污泥 的处理效率。 此外, 本实施例中也可以将下部泥浆沉降区 215沉降的泥浆通过泥 浆泵 23排入第一池体 11内。 通过将第二池体 21内的泥浆快速泵入第一池体 11中 , 再通过第一池体 11的出浆口 112—并排出, 也可避免单独对第二池体 21的泥浆 进行处理, 同吋提高了排泥效率。  [0033] Preferably, the sludge settled in the lower mud settling zone 215 is discharged into the conditioning system through the mud pump 23. It is worth noting that the slurry that has been initially concentrated in the prior art is also transported to the conditioning system by a small cutter suction boat. The purpose of the prior art conditioning system is to condition the mud slurry for conditioning treatment. Therefore, in the present invention, the sludge settled in the lower mud settling area 215 is discharged into the conditioning system, and the mud of the second pool body 21 is prevented from being separately treated, discharged into the conditioning system, and then directly subjected to subsequent treatment, thereby further improving the fouling. Mud treatment efficiency. Further, in the present embodiment, the slurry settled in the lower mud settling zone 215 can also be discharged into the first cell body 11 through the slurry pump 23. By directly pumping the slurry in the second cell body 21 into the first cell body 11, and then passing through the slurry outlet 112 of the first cell body 11 and discharging it, it is also possible to avoid the separate treatment of the slurry of the second cell body 21. At the same time, the efficiency of sludge removal is improved.
[0034] 进一步地, 请参阅图 1和图 4, 加药混凝装置 31包括混凝反应器 311以及与混凝 反应器 311连接的加药装置。 加药装置包括分别与混凝反应器 311连接的 PAM加 药装置 312和 PAC加药装置 313。 值得说明的是, 混凝反应器 311、 PAM加药装置 312以及 PAC加药装置 313可采用现有常规技术。 PAM加药装置 312可通过设置计 量泵向混凝反应器 311中加入 PAM, PAM (聚丙烯酰胺) 是一种有机高分子助沉 齐 1J, 其具有在颗粒间形成更大的絮体由此产生巨大的表面吸附作用, 它是有机 高分子在水处理方面应用最为广泛的絮凝剂, 此外, PAM在水处理中, 利用其 吸附和架桥的作用, 对浊度、 色度都有很好的去除能力。 PAC加药装置 313可通 过设置计量泵向混凝反应器 311中加入 PAC, PAC (聚合氯化铝) 通常也称作净 水剂或混凝剂, 它是一种水溶性无机高分子聚合物, 其主要通过压缩双电层、 吸附电中和、 吸附架桥、 沉淀物网捕等机理作用, 使水中细微悬浮粒子和胶体 粒子脱稳, 聚集、 絮凝、 混凝、 沉淀, 从而达到净化处理的效果。 加入的 PAM 和 PAC通过在混凝反应器 311中混合, 具体地, 混凝反应器 311设置有搅拌装置, 通过搅拌装置将加入的 PAM和 PAC与溢流水混匀。 进一步地, 考虑到逐级对第 一池体 11、 第二池体 21内的余水也有很好的絮凝和净化作用, 第一池体 11与 PA M加药装置 312相连; 第二池体 21与 PAC加药装置 313相连。 此外, 第一池体 11、 第二池体 21也可以均与 PAC加药装置 313相连。 [0034] Further, referring to FIG. 1 and FIG. 4, the dosing and coagulation device 31 includes a coagulation reactor 311 and a dosing device connected to the coagulation reactor 311. The dosing device includes a PAM dosing device 312 and a PAC dosing device 313 which are respectively connected to the coagulation reactor 311. It is worth noting that the coagulation reactor 311, the PAM dosing device 312, and the PAC dosing device 313 can employ conventional conventional techniques. The PAM dosing device 312 can add PAM to the coagulation reactor 311 by providing a metering pump. PAM (polyacrylamide) is an organic polymer assisting solution 1J which has a larger floc formed between the particles. It produces a huge surface adsorption effect. It is the most widely used flocculant for organic polymers in water treatment. In addition, PAM has good turbidity and chromaticity in its water treatment by its adsorption and bridging functions. Removal capacity. The PAC dosing device 313 can add PAC to the coagulation reactor 311 by providing a metering pump, which is also commonly referred to as a water purifying agent or a coagulant, which is a water-soluble inorganic high molecular polymer. , mainly through the action of compressing electric double layer, adsorption electric neutralization, adsorption bridging, sediment net trapping, etc., to make fine suspended particles and colloids in water The particles are destabilized, aggregated, flocculated, coagulated, and precipitated to achieve the effect of purification treatment. The added PAM and PAC are mixed in the coagulation reactor 311. Specifically, the coagulation reactor 311 is provided with a stirring device, and the added PAM and PAC are mixed with the overflow water by a stirring device. Further, considering that the residual water in the first cell body 11 and the second cell body 21 is also well flocculated and purified step by step, the first cell body 11 is connected to the PA M dosing device 312; 21 is connected to the PAC dosing device 313. In addition, the first cell body 11 and the second cell body 21 may also be connected to the PAC dosing device 313.
[0035] 值得说明的是, 处理后的余水可达到 《污水综合排放标准》 (GB8978-1996) 中规定的二级排放标准。 具体地, 经余水多级净化装置处理后得到的可回排余 水的悬浮物含量值 (即 SS值) 小于 15mg/l, COD、 BOD、 ΤΡ、 ΤΝ含量较原河湖 泊涌污染水体所含污染物指标浓度降低 60%以上, 将可回排余水回排至河湖泊涌 中, 可以有效稀释、 降低原河湖泊涌污染水体指标浓度。  [0035] It is worth noting that the treated residual water can meet the secondary emission standards specified in the Integrated Wastewater Discharge Standard (GB8978-1996). Specifically, the suspended matter content value (ie, the SS value) of the recirculating residual water obtained by the residual water multi-stage purification device is less than 15 mg/l, and the COD, BOD, strontium, and barium contents are higher than that of the original river and lake. The concentration of pollutant-containing indicators is reduced by more than 60%, and the recirculated residual water can be discharged back into rivers and lakes, which can effectively dilute and reduce the concentration of polluted water bodies in the original rivers and lakes.
[0036] 以上仅为本发明的较佳实施例而已, 并不用以限制本发明, 凡在本发明的精 神和原则之内所作的任何修改、 等同替换或改进等, 均应包含在本发明的保护 范围之内。  The above are only the preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent substitutions or improvements made within the spirit and principles of the present invention are included in the present invention. Within the scope of protection.

Claims

权利要求书 Claim
一种河湖泊涌污染底泥处理余水多级净化处理系统, 其特征在于, 包 括: The utility model relates to a multi-stage purification treatment system for treating residual water in rivers and lakes, which is characterized in that it comprises:
按照余水处理路径依次串联的用于自然沉降去除余水中的颗粒物的一 级沉淀池、 用于截留去除余水中的颗粒物的二级沉淀池以及用于吸附 去除余水中的悬浊物的三级磁滤净化装置; a primary sedimentation tank for removing natural particles from the residual water in series according to the residual water treatment path, a secondary sedimentation tank for intercepting particulate matter removed from the residual water, and a third stage for adsorbing and removing the suspended matter in the residual water Magnetic filter purification device;
其中, 所述一级沉淀池包括设有进浆口、 出浆口和出水口的第一池体 ; 所述二级沉淀池包括第二池体以及置于所述第二池体内的助沉装置 , 所述助沉装置将所述第二池体分隔成上部清水溢流区和下部泥浆沉 降区, 所述第二池体设有与所述出水口连通的进水口、 用于排出所述 上部清水溢流区溢流的清水的清水口以及用于排出所述下部泥浆沉降 区沉降的污泥的排泥口; 所述三级磁滤净化装置包括与所述清水口连 通的加药混凝装置以及与所述加药混凝装置连接的磁滤装置。 Wherein, the primary sedimentation tank comprises a first pool body provided with a slurry inlet, a slurry outlet and a water outlet; the secondary sedimentation tank comprises a second pool body and a subsidence sink placed in the second pool body The auxiliary sinking device divides the second pool body into an upper clear water overflow area and a lower mud settling area, and the second pool body is provided with a water inlet connected to the water outlet for discharging the a fresh water outlet overflowing the upper fresh water overflow area and a sludge discharge port for discharging sludge settled in the lower mud settling zone; the three-stage magnetic filter purification device includes a medicine mixing and coagulation device connected to the water clearing port And a magnetic filter device coupled to the dosing coagulation device.
如权利要求 1所述的河湖泊涌污染底泥处理余水多级净化处理系统, 其特征在于, 所述第一池体内设有用于将所述第一池体内的上清液从 所述出水口引流至所述第二池体内的滗水器。 The multi-stage purification treatment system for river water rushing sediment sludge treatment residual water according to claim 1, wherein the first pool body is provided with the supernatant liquid from the first pool body The nozzle is drained to a decanter in the second cell.
如权利要求 1所述的河湖泊涌污染底泥处理余水多级净化处理系统, 其特征在于, 所述助沉装置设为助沉斜板和 /或助沉斜管。 The multi-stage purification treatment system for river water rushing sediment treatment residual water according to claim 1, wherein the auxiliary subsidence device is provided as a sloping plate and/or a sloping tube.
如权利要求 3所述的河湖泊涌污染底泥处理余水多级净化处理系统, 其特征在于, 所述助沉装置的端部设有溢流堰板。 The multi-stage purification treatment system for river water rushing sediment sludge treatment residual water according to claim 3, wherein the auxiliary subsidence device is provided with an overflow raft at the end.
如权利要求 1所述的河湖泊涌污染底泥处理余水多级净化处理系统, 其特征在于, 所述助沉装置设置为多个, 多个的所述助沉装置按照余 水处理路径依次间隔布置, 每两个的所述助沉装置之间通过隔离墙隔 幵; 所述隔离墙的上部设有溢流口。 The multi-stage purification treatment system for a river and lake flu-contaminated sludge treatment residual water according to claim 1, wherein the auxiliary subsidence device is provided in plurality, and the plurality of the auxiliary-sinking devices are sequentially arranged according to a residual water treatment path. Arranged at intervals, each of the two auxiliary sinking devices is separated by a partition wall; an upper portion of the partition wall is provided with an overflow port.
如权利要求 1~5任一项所述的河湖泊涌污染底泥处理余水多级净化处 理系统, 其特征在于, 所述加药混凝装置包括混凝反应器以及与所述 混凝反应器连接的加药装置。 The multi-stage purification treatment system for river water rushing sediment sludge treatment residual water according to any one of claims 1 to 5, wherein the medicinal coagulating device comprises a coagulation reactor and the coagulation reaction The dosing device connected to the device.
如权利要求 6所述的河湖泊涌污染底泥处理余水多级净化处理系统, 其特征在于, 所述加药装置包括分别与所述混凝反应器连接的 PAM 加药装置和 PAC加药装置。 a multi-stage purification treatment system for residual water treatment of river and lake sediments according to claim 6, The dosing device includes a PAM dosing device and a PAC dosing device respectively connected to the coagulation reactor.
[权利要求 8] 如权利要求 7所述的河湖泊涌污染底泥处理余水多级净化处理系统, 其特征在于, 所述第一池体与所述 PAM加药装置相连; 所述第二池 体与所述 PAC加药装置相连。 [Claim 8] The multi-stage purification treatment system for river and river flu pollution sludge treatment residual water according to claim 7, wherein the first pool body is connected to the PAM dosing device; The cell body is connected to the PAC dosing device.
[权利要求 9] 如权利要求 1~5任一项所述的河湖泊涌污染底泥处理余水多级净化处 理系统, 其特征在于, 所述下部泥浆沉降区沉降的污泥通过泥浆泵排 入调理系统内。 [Claim 9] The multi-stage purification treatment system for river water rushing sediment sludge treatment residual water according to any one of claims 1 to 5, wherein the sludge settled in the lower mud sedimentation zone is discharged through the mud pump Into the conditioning system.
[权利要求 10] 如权利要求 1~5任一项所述的河湖泊涌污染底泥处理余水多级净化处 理系统, 其特征在于, 所述第一池体内设有在线浊度仪。  [Claim 10] The multi-stage purification processing system for river water rushing sediment treatment residual water according to any one of claims 1 to 5, wherein an online turbidimeter is provided in the first cell.
PCT/CN2017/083570 2016-08-16 2017-05-09 Multi-stage purification treatment system for residual water from treatment of contaminated bottom sludge from river or lake WO2018032805A1 (en)

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