CN206089401U - Processing system is handled to river lake silt - Google Patents
Processing system is handled to river lake silt Download PDFInfo
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- CN206089401U CN206089401U CN201620433401.0U CN201620433401U CN206089401U CN 206089401 U CN206089401 U CN 206089401U CN 201620433401 U CN201620433401 U CN 201620433401U CN 206089401 U CN206089401 U CN 206089401U
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- 238000012545 processing Methods 0.000 title abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 83
- 230000018044 dehydration Effects 0.000 claims abstract description 25
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 25
- 238000012216 screening Methods 0.000 claims abstract description 22
- 238000005245 sintering Methods 0.000 claims abstract description 21
- 239000010802 sludge Substances 0.000 claims description 110
- 238000011065 in-situ storage Methods 0.000 claims description 21
- 239000000463 material Substances 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 12
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- 208000005156 Dehydration Diseases 0.000 description 22
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- 239000012535 impurity Substances 0.000 description 21
- 238000004062 sedimentation Methods 0.000 description 20
- 230000008719 thickening Effects 0.000 description 19
- 238000003756 stirring Methods 0.000 description 9
- 238000010276 construction Methods 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 239000012024 dehydrating agents Substances 0.000 description 7
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- Treatment Of Sludge (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及一种河湖淤泥处理处置系统,属于环境岩土工程技术领域。The utility model relates to a treatment and disposal system for river and lake silt, which belongs to the technical field of environmental geotechnical engineering.
背景技术Background technique
随着中国城镇化的迅速发展,大量黑臭河湖急需治理。黑臭河湖治理的根本在于淤泥治理。河湖淤泥具有高亲水、高含水、高有机质含量、低渗透、体量大、含有不同程度污染物和垃圾杂物等特点,导致在工程中处理处置难度大,且容易发生二次污染。因此,如何规范系统处理处置是目前面临的关键难题。With the rapid development of urbanization in China, a large number of black and smelly rivers and lakes urgently need to be treated. The root of black and smelly river and lake governance lies in silt control. River and lake silt has the characteristics of high hydrophilicity, high water content, high organic matter content, low permeability, large volume, and contains different levels of pollutants and garbage, which makes it difficult to deal with in the project and is prone to secondary pollution. Therefore, how to standardize system processing and disposal is the key problem currently facing.
目前,主要的处理处置方法涉及:1)铰吸上岸脱水处理。目前,该方法对于杂物去除、加药快速浓缩泥浆、污染物稳化稳固化处理等环节欠缺统一考虑;同时铰吸淤泥含固率低(约3%-5%),且受脱水设备产能限制;该方法对于大体量的河湖淤泥处理,其工期较长、成本较高。2)抓泥上岸或铰吸上岸,自然沉淀后进行原位改性固化处理。目前采取单纯抓泥上岸或单纯铰吸上岸,二者缺乏配合。单纯抓泥上岸,由于工作原理的限制,难以彻底清除河湖淤泥,且对于有机质含量高的浮泥难以清除;同时该方法欠缺杂物去除环节,大量的杂物(垃圾、大粒径石头等)导致后续利用困难。单纯铰吸上岸沉淀,杂物去除和加药加速淤泥沉淀考虑不全,依靠自然沉淀速度慢,且沉淀后淤泥含水率高,后续改性固化处理药剂和施工成本高。At present, the main treatment and disposal methods involve: 1) reamer suction and dehydration treatment on shore. At present, this method lacks a unified consideration for the removal of sundries, the rapid concentration of mud by dosing, the stabilization and solidification of pollutants, and other links; at the same time, the solid content of the reaming sludge is low (about 3%-5%), and it is limited by the capacity of the dehydration equipment. Restrictions; this method has a long construction period and high cost for the treatment of a large amount of river and lake sludge. 2) Grab the mud ashore or suck it ashore, and carry out in-situ modification and solidification treatment after natural sedimentation. At present, either simply grasping mud to land or simply suctioning to land is adopted, and the two lack cooperation. Due to the limitations of the working principle, it is difficult to completely remove the river and lake silt, and it is difficult to remove the floating mud with high organic matter content; at the same time, this method lacks the removal of debris, and a large amount of debris (garbage, large-sized stones, etc.) ) makes subsequent use difficult. Simple reaming suction ashore sedimentation, debris removal and dosing to accelerate sludge sedimentation are not fully considered, relying on natural sedimentation speed is slow, and the moisture content of sludge after sedimentation is high, subsequent modification and solidification treatment agents and construction costs are high.
上述已有的这些技术一定程度上改善了淤泥处置难的困境,但淤泥处置是涉及清淤、除杂、脱水、改性固化和资源化利用的综合处理处置技术;同时需要满足河湖淤泥清除彻底、无二次污染、环保经济高效等要求。因此,在现有技术基础上,集成已有技术,开发新的淤泥处理处置技术是亟待解决的问题。The above-mentioned existing technologies have improved the difficulty of sludge disposal to a certain extent, but sludge disposal is a comprehensive treatment and disposal technology involving dredging, impurity removal, dehydration, modification and solidification, and resource utilization; Thorough, no secondary pollution, environmental protection, economic efficiency and other requirements. Therefore, it is an urgent problem to be solved on the basis of the existing technology, integrating the existing technology, and developing a new sludge treatment and disposal technology.
发明内容Contents of the invention
针对上述存在的问题,本实用新型的目的在于提供一种综合考虑清淤、除杂、脱水、改性固化和资源化利用环节,且环保、经济和高效的河湖淤泥处理处置系统。In view of the above existing problems, the purpose of this utility model is to provide an environmentally friendly, economical and efficient river and lake sludge treatment and disposal system that comprehensively considers dredging, impurity removal, dehydration, modification and solidification, and resource utilization.
为了实现上述目的,其技术解决方案为:In order to achieve the above purpose, its technical solution is:
一种河湖淤泥处理处置系统,所述的处理处置系统由控源分离改性固化系统、原位改性固化系统、成型烧结系统、改性淤泥运输装置和皮带运输装置组成,控源分离改性固化系统由铰吸设备、第一泥浆泵、筛分除杂装置、第一泥浆测量器、水剂自动加入装置、第一管道搅拌器、泥浆浓缩装置、第二泥浆测量器、第二泥浆泵、粉剂自动加入装置、第二管道搅拌器、泥浆罐、第一水处理装置、第三泥浆泵、尾水收集装置和深度脱水装置构成,铰吸设备通过管道连接筛分除杂装置的进料口,连接铰吸设备和筛分除杂装置的管道上设置有第一泥浆泵,筛分除杂装置的泥浆出口通过管道与泥浆浓缩装置的泥浆进口连接,连接筛分除杂装置和泥浆浓缩装置的管道上依次设置有第一泥浆测量器和第一管道搅拌器,第一泥浆测量器位于筛分除杂装置的一侧,第一管道搅拌器上设置有水剂自动加入装置,泥浆浓缩装置底部的泥浆出口通过管道与泥浆罐的泥浆进口连接,连接泥浆浓缩装置和泥浆罐的管道上依次设置有第二泥浆测量器、第二泥浆泵和第二管道搅拌器,第二泥浆测量器位于泥浆浓缩装置的一侧,第二管道搅拌器位于泥浆罐的一侧,第二管道搅拌器上设置有粉剂自动加入装置,泥浆浓缩装置上部的出水口通过管道连接第一水处理装置的进水口,泥浆罐底部的泥浆出口通过管道与深度脱水装置的泥浆进口连接,连接泥浆罐和深度脱水装置的管道上设置有第三泥浆泵,深度脱水装置的出水口下方设置有尾水收集装置,尾水收集装置的出水口通过管道与第一水处理装置的进水口连接,原位改性固化系统由抓泥设备、淤泥运输装置、淤泥沉淀池、粉剂加入装置、原位改性装置、振动除杂装置和第二水处理装置构成,淤泥运输装置位于抓泥设备与振动除杂装置之间,振动除杂装置的泥浆出口与淤泥沉淀池连接,淤泥沉淀池中设置有粉剂加入装置和原位改性装置,淤泥沉淀池的出水口与第二水处理装置的进水口连接,成型烧结系统由改性淤泥料仓、改性淤泥破碎装置、辅料添加装置、皮带运输搅拌装置、改性淤泥成型装置和烧结装置构成,改性淤泥料仓与深度脱水装置之间设置有皮带运输装置,深度脱水装置出料口位于皮带运输装置的上方,皮带运输装置的出料端位于改性淤泥料仓的上方,改性淤泥料仓底部出料口位于改性淤泥破碎装置的进料口上方,改性淤泥破碎装置的出口下方设置有皮带运输搅拌装置,皮带运输搅拌装置的上方还设置有辅料添加装置,皮带运输搅拌装置的出料端下方设置有改性淤泥成型装置,改性淤泥成型装置的出口通过运输托盘与烧结装置的进口连接,第一管道搅拌器和泥浆浓缩装置之间的管道上设置有通向淤泥沉淀池的支管,淤泥沉淀池和改性淤泥料仓之间设置有改性淤泥运输装置,铰吸设备、抓泥设备、第一泥浆泵、筛分除杂装置、第一泥浆测量器、水剂自动加入装置、第一管道搅拌器、泥浆浓缩装置、第二泥浆测量器、改性淤泥料仓、第二泥浆泵、粉剂自动加入装置、第二管道搅拌器、泥浆罐、第一水处理装置、第三泥浆泵、尾水收集装置、深度脱水装置、皮带运输装置、改性淤泥破碎装置、辅料添加装置、皮带运输搅拌装置、粉剂加入装置、改性淤泥成型装置、原位改性装置、烧结装置、振动除杂装置和第二水处理装置通过导线或无线与计算机控制系统连接。A river and lake sludge treatment and disposal system, the treatment and disposal system is composed of source control separation modified solidification system, in-situ modification solidification system, forming sintering system, modified sludge transport device and belt transport device, source control separation modified The permanent curing system consists of hinge suction equipment, the first mud pump, the screening and impurity removal device, the first mud measuring device, the water agent automatic adding device, the first pipeline agitator, the mud thickening device, the second mud measuring device, the second mud Pump, powder automatic adding device, second pipeline agitator, mud tank, first water treatment device, third mud pump, tail water collection device and deep dehydration device, the hinged suction device is connected to the inlet of the screening and impurity removal device through pipelines The first mud pump is installed on the pipeline connecting the hinge suction equipment and the screening and impurity removal device. The mud outlet of the screening and impurity removal device is connected to the mud inlet of the mud thickening device through the pipeline, and the screening and impurity removal device is connected with the mud The pipeline of the thickening device is provided with a first mud measuring device and a first pipeline agitator in sequence. The first mud measuring device is located on one side of the screening and impurity removal device. The first pipeline agitator is equipped with an automatic water agent adding device. The mud outlet at the bottom of the thickening device is connected to the mud inlet of the mud tank through a pipeline. The second mud measuring device, the second mud pump and the second pipeline agitator are arranged in sequence on the pipeline connecting the mud thickening device and the mud tank. The second mud measuring The mixer is located on one side of the mud thickening device, the second pipeline agitator is located on one side of the mud tank, the second pipeline agitator is equipped with an automatic powder adding device, and the water outlet on the upper part of the mud thickening device is connected to the first water treatment device through a pipeline. The water inlet and the mud outlet at the bottom of the mud tank are connected to the mud inlet of the deep dewatering device through pipes. The third mud pump is installed on the pipe connecting the mud tank and the deep dewatering device, and a tail water collection device is installed under the water outlet of the deep dewatering device. , the outlet of the tail water collection device is connected to the water inlet of the first water treatment device through a pipeline, and the in-situ modification and solidification system consists of a mud grabbing device, a sludge transport device, a sludge sedimentation tank, a powder adding device, an in-situ modification device, It consists of a vibration removal device and a second water treatment device. The sludge transport device is located between the mud grabbing equipment and the vibration removal device. The mud outlet of the vibration removal device is connected to the sludge sedimentation tank. The sludge sedimentation tank is equipped with a powder adding device and In-situ modification device, the water outlet of the sludge sedimentation tank is connected to the water inlet of the second water treatment device, and the forming and sintering system consists of a modified sludge silo, a modified sludge crushing device, an auxiliary material adding device, a belt transport stirring device, a modified The sludge forming device and the sintering device are composed of a belt conveyor device between the modified sludge silo and the deep dehydration device. The discharge port of the deep dehydration device is located above the belt conveyor device, and the discharge end of the belt conveyor device is located Above the silo, the outlet at the bottom of the modified sludge silo is located above the feed inlet of the modified sludge crushing device, and a belt transport mixing device is installed below the outlet of the modified sludge crushing device, and auxiliary materials are also installed above the belt transport stirring device. Adding device, a modified sludge forming device is installed under the discharge end of the belt transport mixing device, and the outlet of the modified sludge forming device passes through the transport tray It is connected with the inlet of the sintering device, the pipeline between the first pipeline agitator and the mud thickening device is provided with a branch pipe leading to the sludge sedimentation tank, and a modified sludge transportation device is provided between the sludge sedimentation tank and the modified sludge silo, Hinge suction equipment, mud grabbing equipment, first mud pump, screening and impurity removal device, first mud measuring device, water agent automatic adding device, first pipeline agitator, mud thickening device, second mud measuring device, modified sludge Stock silo, second mud pump, powder automatic adding device, second pipeline agitator, mud tank, first water treatment device, third mud pump, tail water collection device, deep dehydration device, belt transport device, modified sludge crushing The device, auxiliary material adding device, belt transport stirring device, powder adding device, modified sludge forming device, in-situ modification device, sintering device, vibration removal device and second water treatment device are connected to the computer control system through wires or wirelessly.
所述的淤泥运输装置为运输车或运输船中的一种。The silt transport device is one of a transport vehicle or a transport ship.
所述的改性淤泥运输装置为运输车。The modified sludge transport device is a transport vehicle.
由于采用了以上技术方案,本实用新型的一种河湖淤泥处理处置系统采用的抓泥设备对河湖中能抓取的淤泥通过淤泥运输装置输送到淤泥沉淀池,并利用原位改性固化系统进行处理,大大降低控源分离改性固化系统的处理量,有效避免该系统铰吸淤泥浓度低(3%-5%的含固率)、运输和后续处理成本高和处理效率相对低的问题;对于难以通过抓泥设备直接抓取的淤泥,采用铰吸设备清除,能确保河湖淤泥清除彻底;铰吸设备和抓泥设备并行清淤,确保淤泥清除彻底,同时保证清淤效率、效果和经济性。对于泥性较好的淤泥(加入脱水药剂后能快速沉淀)通过铰吸设备直接进入淤泥沉淀池,自然沉降后利用原位改性固化系统进行处理,降低控源分离改性固化系统的处理量,提高淤泥处理效率;对于泥性较差(加入脱水药剂后不能快速沉淀)的淤泥,铰吸进入控源分离改性固化系统进行处理,能确保淤泥处理效果(通过控源分离改性固化系统处理后的淤泥泥饼含水率能<35%),有效避免泥性差的淤泥进入淤泥沉淀池(自然沉淀后含水率高,从而增加改性固化成本);原位改性固化系统和控源分离改性固化系统同时使用,能保证淤泥处理效率和节约处理成本。筛分除杂装置和振动除杂装置能有效去除淤泥中的垃圾、石块和大粒径砂石,便于淤泥后续处理处置和资源化利用,同时筛分出来的砂石可以直接作为建材利用。水剂自动加入装置,能根据设计的加入量向淤泥中加入脱水药剂,保证淤泥快速沉降,降低淤泥后续改性固化成本。粉剂自动加入装置和粉剂加入装置,能根据设计的加入量向淤泥中加入稳化固化药剂,稳化固化淤泥中污染物,使改性达标后的淤泥能资源化利用。系统参数在计算机上设置,数据计算机程序处理,大大提高了系统效率。Due to the adoption of the above technical scheme, the sludge grabbing equipment used in the river and lake sludge treatment and disposal system of the present invention transports the sludge that can be grasped in the river and lake to the sludge sedimentation tank through the sludge transport device, and uses in-situ modification to solidify System processing, greatly reducing the processing capacity of the source control separation modified solidification system, effectively avoiding the low concentration of reaming sludge (3%-5% solid content), high transportation and subsequent treatment costs, and relatively low treatment efficiency. Problem: For the silt that is difficult to grab directly by the mud grabbing equipment, the use of hinge suction equipment to remove it can ensure that the river and lake silt is completely removed; effect and economy. For sludge with good mud properties (it can settle quickly after adding dehydrating agent), it will directly enter the sludge sedimentation tank through the hinge suction equipment, and after natural settlement, it will be treated with the in-situ modified solidification system to reduce the processing capacity of the control source separation modified solidification system , improve the efficiency of sludge treatment; for sludge with poor mud properties (cannot settle quickly after adding dehydrating agent), hinge suction enters the control source separation modified solidification system for treatment, which can ensure the sludge treatment effect (through the control source separation modified solidification system The moisture content of the treated sludge cake can be <35%), which can effectively prevent the sludge with poor mud properties from entering the sludge sedimentation tank (the moisture content is high after natural precipitation, thereby increasing the cost of modification and curing); the in-situ modification and curing system is separated from the source control The modified solidification system is used at the same time, which can ensure the efficiency of sludge treatment and save treatment costs. The screening impurity removal device and the vibration impurity removal device can effectively remove garbage, stones and large-sized sandstones in the sludge, which is convenient for subsequent treatment and resource utilization of the sludge. At the same time, the sandstones screened out can be directly used as building materials. The automatic water agent adding device can add dehydrating agent to the sludge according to the designed addition amount to ensure the rapid sedimentation of the sludge and reduce the cost of subsequent modification and solidification of the sludge. The automatic powder adding device and the powder adding device can add stabilizing and curing agents to the sludge according to the designed dosage to stabilize and solidify the pollutants in the sludge, so that the modified sludge that meets the standard can be used as a resource. The system parameters are set on the computer, and the data is processed by the computer program, which greatly improves the system efficiency.
附图说明Description of drawings
图1为本实用新型的结构示意图。Fig. 1 is the structural representation of the utility model.
具体实施方式detailed description
下面结合附图对本实用新型进行进一步详细描述,见附图。Below in conjunction with accompanying drawing, the utility model is described in further detail, see accompanying drawing.
一种河湖淤泥处理处置系统,处理处置系统由控源分离改性固化系统、原位改性固化系统、成型烧结系统、改性淤泥运输装置11和皮带运输装置24组成,控源分离改性固化系统由铰吸设备2、第一泥浆泵4、筛分除杂装置6、第一泥浆测量器8、水剂自动加入装置9、第一管道搅拌器10、泥浆浓缩装置12、第二泥浆测量器13、第二泥浆泵15、粉剂自动加入装置16、第二管道搅拌器17、泥浆罐18、第一水处理装置19、第三泥浆泵20、尾水收集装置21和深度脱水装置22构成,铰吸设备2通过管道连接筛分除杂装置6的进料口,连接铰吸设备2和筛分除杂装置6的管道上设置有第一泥浆泵4,筛分除杂装置6筛分出的杂物通过杂物出口排出,筛分除杂装置6的泥浆出口通过管道与泥浆浓缩装置12的泥浆进口连接,连接筛分除杂装置6和泥浆浓缩装置12的管道上依次设置有第一泥浆测量器8和第一管道搅拌器10,第一泥浆测量器8位于筛分除杂装置6的一侧,第一管道搅拌器10上设置有水剂自动加入装置9,泥浆浓缩装置12底部的泥浆出口通过管道与泥浆罐18的泥浆进口连接,连接泥浆浓缩装置12和泥浆罐18的管道上依次设置有第二泥浆测量器13、第二泥浆泵15和第二管道搅拌器17,第二泥浆测量器13位于泥浆浓缩装置12的一侧,第二管道搅拌器17位于泥浆罐18的一侧,第二管道搅拌器17上设置有粉剂自动加入装置16,泥浆浓缩装置12上部的出水口通过管道连接第一水处理装置19的进水口,泥浆罐18底部的泥浆出口通过管道与深度脱水装置22的泥浆进口连接,深度脱水装置22为强力钢板压滤机、隔膜式板框压滤机或钢带带式压滤机中的一种,深度脱水装置22出来的满足烧结材料、建筑/绿化用土泥饼通过皮带运输装置24运输到改性淤泥料仓14中,深度脱水装置22出来的不满足烧结材料、建筑/绿化用土泥饼运输到垃圾填埋场23中规范填埋,连接泥浆罐18和深度脱水装置22的管道上设置有第三泥浆泵20,深度脱水装置22的出水口下方设置有尾水收集装置21,尾水收集装置21的出水口通过管道与第一水处理装置19的进水口连接,第一水处理装置19可根据水体性质向水体中加入净水药剂使得水体达到排放标准,原位改性固化系统由抓泥设备3、淤泥运输装置5、淤泥沉淀池7、粉剂加入装置29、原位改性装置31、振动除杂装置33和第二水处理装置35构成,淤泥运输装置5位于抓泥设备3与振动除杂装置33之间,淤泥运输装置5为运输车或运输船中的一种,振动除杂装置33的泥浆出口与淤泥沉淀池7连接,振动除杂装置33筛分出的杂物通过杂物出口排出,淤泥沉淀池7中设置有粉剂加入装置29和原位改性装置31,粉剂加入装置29为履带式粉剂罐车、固定式输料地泵或固定立式粉料罐中的一种,原位改性装置31为履带式移动搅拌设备、挖机或固定安装搅拌机中的一种,淤泥沉淀池7的出水口与第二水处理装置35的进水口连接,第二水处理装置35可根据水体性质向水体中加入净水药剂使得水体达到排放标准,成型烧结系统由改性淤泥料仓14、改性淤泥破碎装置25、辅料添加装置26、皮带运输搅拌装置27、改性淤泥成型装置30和烧结装置32构成,改性淤泥料仓14与深度脱水装置22之间设置有皮带运输装置24,深度脱水装置22出料口位于皮带运输装置24的上方,皮带运输装置24的出料端位于改性淤泥料仓14的上方,改性淤泥料仓14底部出料口位于改性淤泥破碎装置25的进料口上方,改性淤泥破碎装置25的出口下方设置有皮带运输搅拌装置27,皮带运输搅拌装置27的上方还设置有辅料添加装置26,辅料添加装置26可根据需求添加黄土、粉煤灰、石灰、木屑和稻壳等材料,皮带运输搅拌装置27的出料端下方设置有改性淤泥成型装置30,皮带运输搅拌装置27出料口出来的满足建筑/绿化用土的改性淤泥运输到建筑/绿化用土场28中进行资源化利用,皮带运输搅拌装置27出料口出来的满足烧结材料的改性淤泥进入改性淤泥成型装置30,改性淤泥成型装置30的出口通过运输托盘与烧结装置32的进口连接,第一管道搅拌器10和泥浆浓缩装置12之间的管道上设置有通向淤泥沉淀池7的支管,淤泥沉淀池7和改性淤泥料仓14之间设置有改性淤泥运输装置11,改性淤泥运输装置11为运输车,对于可以作为烧结材料、建筑/绿化用土的改性淤泥用改性淤泥运输装置11运输到改性淤泥料仓14,对于不能作为建筑/绿化用土的改性淤泥用改性淤泥运输装置11运输到垃圾填埋场23中规范填埋,铰吸设备2、抓泥设备3、第一泥浆泵4、筛分除杂装置6、第一泥浆测量器8、水剂自动加入装置9、第一管道搅拌器10、泥浆浓缩装置12、第二泥浆测量器13、改性淤泥料仓14、第二泥浆泵15、粉剂自动加入装置16、第二管道搅拌器17、泥浆罐18、第一水处理装置19、第三泥浆泵20、尾水收集装置21、深度脱水装置22、皮带运输装置24、改性淤泥破碎装置25、辅料添加装置26、皮带运输搅拌装置27、粉剂加入装置29、改性淤泥成型装置30、原位改性装置31、烧结装置32、振动除杂装置33和第二水处理装置35通过导线或无线与计算机控制系统连接。A treatment and disposal system for river and lake sludge. The treatment and disposal system is composed of a source-controlled separation modified solidification system, an in-situ modified solidification system, a molding and sintering system, a modified sludge transportation device 11 and a belt transportation device 24. The source control separation modification The solidification system consists of hinge suction equipment 2, first mud pump 4, screening and impurity removal device 6, first mud measuring device 8, water agent automatic adding device 9, first pipeline agitator 10, mud thickening device 12, second mud Measuring device 13, second mud pump 15, powder automatic adding device 16, second pipeline agitator 17, mud tank 18, first water treatment device 19, third mud pump 20, tail water collection device 21 and deep dehydration device 22 Composition, the hinge suction device 2 is connected to the feed port of the screening and impurity removal device 6 through a pipeline, the pipeline connecting the hinge suction device 2 and the screening and impurity removal device 6 is provided with a first mud pump 4, and the screening and impurity removal device 6 sieves The sundries separated are discharged through the sundries outlet, and the mud outlet of the screening and removing impurities device 6 is connected with the mud inlet of the mud thickening device 12 through a pipeline, and the pipelines connecting the screening and removing impurities device 6 and the mud thickening device 12 are successively provided with The first mud measuring device 8 and the first pipeline agitator 10, the first mud measuring device 8 is positioned at one side of the screening and impurity removal device 6, the first pipeline agitator 10 is provided with an automatic water agent adding device 9, a mud thickening device 12 The mud outlet at the bottom is connected to the mud inlet of the mud tank 18 through a pipeline, and the pipeline connecting the mud thickening device 12 and the mud tank 18 is provided with a second mud measuring device 13, a second mud pump 15 and a second pipeline agitator 17 in sequence , the second mud measuring device 13 is positioned at one side of the mud thickening device 12, and the second pipeline agitator 17 is positioned at one side of the mud tank 18, and the second pipeline agitator 17 is provided with a powder automatic adding device 16, and the mud thickening device 12 top is The water outlet is connected to the water inlet of the first water treatment device 19 through a pipeline, and the mud outlet at the bottom of the mud tank 18 is connected to the mud inlet of the deep dehydration device 22 through a pipeline. The deep dehydration device 22 is a strong steel plate filter press, a diaphragm plate frame One of the filter presses or steel belt filter presses, the deep dehydration device 22 meets the requirements of sintering materials, construction/greening soil cakes are transported to the modified sludge silo 14 through the belt transport device 24, and the deep dehydration device The mud cakes that do not meet the requirements of sintering materials and construction/greening from 22 are transported to the landfill 23 for landfill. The pipeline connecting the mud tank 18 and the deep dehydration device 22 is provided with a third mud pump 20, and the deep dehydration device 22 A tail water collection device 21 is arranged below the water outlet of the tail water collection device, and the water outlet of the tail water collection device 21 is connected to the water inlet of the first water treatment device 19 through a pipeline, and the first water treatment device 19 can add clean water to the water body according to the nature of the water body The medicament makes the water reach the discharge standard. The in-situ modification and solidification system consists of a mud grabbing device 3, a sludge transportation device 5, a sludge sedimentation tank 7, a powder adding device 29, an in-situ modification device 31, a vibration removal device 33 and a second water The processing device 35 is formed, and the sludge transport device 5 is located between the mud grabbing equipment 3 and the vibration removal device 33, and the sludge transport device 5 It is a kind of transport vehicle or a transport ship. The mud outlet of the vibration removal device 33 is connected with the sludge settling tank 7, and the sundries screened out by the vibration removal device 33 are discharged through the sundry outlet. The powder adding device 29 and the in-situ modification device 31, the powder adding device 29 is one of a crawler powder tanker, a fixed feeding ground pump or a fixed vertical powder tank, and the in-situ modification device 31 is a crawler-type mobile One of mixing equipment, excavator or fixed installation mixer, the water outlet of the sludge sedimentation tank 7 is connected to the water inlet of the second water treatment device 35, and the second water treatment device 35 can add water purification agents to the water body according to the nature of the water body To make the water body reach the discharge standard, the forming and sintering system is composed of a modified sludge silo 14, a modified sludge crushing device 25, an auxiliary material adding device 26, a belt transport stirring device 27, a modified sludge forming device 30 and a sintering device 32. The modified sludge A belt transport device 24 is arranged between the feed bin 14 and the deep dehydration device 22, the discharge port of the deep dehydration device 22 is located above the belt transport device 24, and the discharge end of the belt transport device 24 is located above the modified sludge silo 14, The outlet at the bottom of the modified sludge silo 14 is located above the feed inlet of the modified sludge crushing device 25, and a belt transport stirring device 27 is arranged below the outlet of the modified sludge crushing device 25, and a belt transport stirring device 27 is also provided above the belt transport stirring device 27 The auxiliary material adding device 26, the auxiliary material adding device 26 can add materials such as loess, fly ash, lime, sawdust and rice husk according to the demand, and a modified sludge forming device 30 is arranged under the discharge end of the belt transport mixing device 27, and the belt transport and mixing The modified sludge that meets the requirements of construction/greening soil from the outlet of the device 27 is transported to the construction/greening soil field 28 for resource utilization, and the modified sludge that meets the requirements of sintering materials from the outlet of the mixing device 27 enters the modification The sludge forming device 30, the outlet of the modified sludge forming device 30 is connected to the inlet of the sintering device 32 through the transport tray, the pipeline between the first pipeline agitator 10 and the mud thickening device 12 is provided with a branch pipe leading to the sludge sedimentation tank 7 , a modified sludge transport device 11 is arranged between the sludge settling tank 7 and the modified sludge silo 14, and the modified sludge transport device 11 is a transport vehicle. The silt transport device 11 is transported to the modified silt silo 14, and the modified silt transport device 11 is used to transport the modified silt transport device 11 to the landfill 23 for the modified silt that cannot be used as soil for construction/greening. Equipment 3, first mud pump 4, screening and impurity removal device 6, first mud measuring device 8, water agent automatic adding device 9, first pipeline agitator 10, mud thickening device 12, second mud measuring device 13, improved Reactive sludge silo 14, second mud pump 15, powder automatic adding device 16, second pipeline agitator 17, mud tank 18, first water treatment device 19, third mud pump 20, tail water collection device 21, deep dehydration Device 22, belt transport device 24, modified sludge crushing device 25, auxiliary material adding Adding device 26, belt transport stirring device 27, powder adding device 29, modified sludge forming device 30, in-situ modification device 31, sintering device 32, vibration removal device 33 and the second water treatment device 35 communicate with each other via wire or wireless Computer control system connection.
本实用新型试验装置的工作原理:The working principle of the utility model test device:
系统运行时,通过计算机控制系统设定好系统参数并确保处理处置系统处于关闭状态,向水剂自动加入装置9加入脱水药剂,向粉剂自动加入装置16和粉剂加入装置29中加入淤泥稳化固化药剂,向辅料添加装置26中加入辅料,向第一水处理装置19和第二水处理装置35中加入水处理药剂,将抓泥设备3置于河道/湖泊1中,按照设定的清淤方法利用抓泥设备3进行抓泥清淤,淤泥通过淤泥运输装置5输送到振动除杂装置33中,通过振动除杂装置33去除垃圾、大粒径碎石等杂物后,进入淤泥沉淀池7;利用抓泥设备3对河道/湖泊1进行第一次清淤后,启动控源分离改性固化系统,将铰吸设备2置于河道/湖泊1中,按照设定的清淤方法利用铰吸设备2清除河道/湖泊1中剩余的淤泥,淤泥由第一泥浆泵4输送到筛分除杂装置6中,利用筛分除杂装置6去除泥浆中的垃圾、大粒径的石头等杂物,泥浆流经第一泥浆测量器8和第一管道搅拌器10,第一泥浆测量器8计量泥浆流量和浓度,计算机控制系统根据第一泥浆测量器8计量泥浆流量和浓度自动计算并设定水剂自动加入装置9向第一管道搅拌器10中加入脱水药剂量,泥浆与药剂通过第一管道搅拌器10进行混合,和脱水药剂混合后的泥浆有如下两个去路:1)泥性较差的淤泥(通过试验,泥浆加入脱水药剂后不能快速沉淀)通过管道输送到泥浆浓缩装置12,泥浆浓缩后,上层浮水进入到第一水处理装置19,经第一水处理装置19处理达标后排放,下层浓缩泥浆通过第二泥浆泵15输送到泥浆罐18中,在这过程中浓缩泥浆还流经第二泥浆测量器13和第二管道搅拌器17,第二泥浆测量器13计量泥浆流量和浓度,计算机控制系统根据第二泥浆测量器13计量泥浆流量和浓度自动计算并设定粉剂自动加入装置16向第二管道搅拌器17中加入稳化固化药剂量,泥浆与药剂通过第二管道搅拌器17均匀混合,泥浆罐18中的泥浆通过第三泥浆泵20泵输送到深度脱水装置22中,泥浆经过深度脱水装置22的深度脱水处理,压滤水流入尾水收集装置21中,然后通过管道输送到第一水处理装置19中,经过第一水处理装置19处理达标后排放,深度脱水装置22的泥饼(含水率<35%)通过皮带运输装置24输送到改性淤泥料仓14中。2)泥性较好的淤泥(通过试验,泥浆加入脱水药剂后能快速沉淀)通过管道输送到淤泥沉淀池7;淤泥沉淀池7中的泥浆(包含抓泥设备3和铰吸设备2清除的泥浆)自然沉降后,上层浮水排入第二水处理装置35中,经第二水处理装置35处理达标后排放,同时对淤泥沉淀池7中淤泥的含水率、有机质及有毒有害物质含量进行取样检测,根据检测结果设定粉剂加入装置29向淤泥中添加稳化固化药剂量,然后启动原位改性固化系统,在原位改性装置31和粉剂加入装置29的协同工作下完成对淤泥沉淀池7中淤泥的改性固化处理,改性后的淤泥经过三天的养护,对于满足制备建筑材料的改性淤泥,通过改性淤泥运输装置11输送到改性淤泥料仓14备用,对于不能满足制备建筑材料的改性淤泥通过改性淤泥运输装置11输送到垃圾填埋场23中进行规范填埋。改性淤泥料仓14中的泥饼进入到改性淤泥破碎装置25进行粉碎,然后进入到皮带运输搅拌装置27中,辅料添加装置26根据设计比例向改性淤泥中加入辅料,皮带运输搅拌装置27对各材料进行混合搅拌,搅拌混合后的材料一部分作为建筑/绿化用土场28进行利用,一部分进入改性淤泥成型装置30中成型,成型后的样品进入烧结装置32中烧结,烧结成品通过烧结成品运输车34运输到需要的地方进行资源化利用。处理处置系统运行过程中定期检查处理处置系统各装置,及时更换不符合处理处置系统要求和已有安全隐患的设备,确保处理处置系统安全运行,系统停运后要及时清洗和保养,确保处理处置系统下一次顺利运行及使用寿命。When the system is running, set the system parameters through the computer control system and ensure that the treatment and disposal system is in the closed state, add dehydration agent to the automatic water addition device 9, and add sludge to the automatic powder addition device 16 and powder addition device 29 to stabilize and solidify Chemicals, add auxiliary materials to the auxiliary material adding device 26, add water treatment chemicals to the first water treatment device 19 and the second water treatment device 35, place the mud grabbing equipment 3 in the river/lake 1, and dredge according to the set The method uses the mud grabbing equipment 3 to carry out mud grabbing and dredging, and the sludge is transported to the vibration removal device 33 through the sludge transport device 5, and after the vibration removal device 33 removes debris such as rubbish and large-sized gravel, it enters the sludge sedimentation tank 7. After the first dredging of the river/lake 1 with the mud grabbing device 3, start the source control separation modified solidification system, place the hinge suction device 2 in the river/lake 1, and use it according to the set dredging method The hinge suction device 2 removes the remaining silt in the river/lake 1, and the silt is transported to the screening and impurity removal device 6 by the first mud pump 4, and the garbage and large-sized stones in the mud are removed by the screening and impurity removal device 6 Sundries, mud flow through the first mud measuring device 8 and the first pipeline agitator 10, the first mud measuring device 8 measures the mud flow and concentration, and the computer control system automatically calculates and measures the mud flow and concentration according to the first mud measuring device 8 The water agent automatic adding device 9 is set to add the amount of dehydrating agent in the first pipeline agitator 10, and the mud and the medicament are mixed by the first pipeline agitator 10, and the mud mixed with the dehydrating agent has the following two outlets: 1) mud The sludge with poor properties (through the test, the mud cannot be quickly precipitated after adding the dehydrating agent) is transported to the mud thickening device 12 through the pipeline. After the mud is concentrated, the floating water in the upper layer enters the first water treatment device 19 and is processed by the first water treatment device 19. After reaching the standard, the concentrated mud in the lower layer is transported to the mud tank 18 by the second mud pump 15. During this process, the concentrated mud also flows through the second mud measuring device 13 and the second pipeline agitator 17, and the second mud measuring device 13 measures The mud flow and concentration, the computer control system automatically calculates and sets the powder automatic adding device 16 according to the second mud measuring device 13 metering mud flow and concentration to add the amount of stabilizing and solidifying medicine to the second pipeline agitator 17, and the mud and medicine pass through the second pipeline mixer 17. The two-pipe agitator 17 mixes evenly, and the mud in the mud tank 18 is pumped to the deep dehydration device 22 by the third mud pump 20. The mud is subjected to the deep dehydration treatment of the deep dehydration device 22, and the press water flows into the tail water collection device 21. , and then transported to the first water treatment device 19 through pipelines, discharged after the first water treatment device 19 is treated up to the standard, and the mud cake (moisture content<35%) of the deep dehydration device 22 is transported to the modified sludge by the belt conveyor 24 In the silo 14. 2) Sludge with better mud properties (through the test, the slurry can quickly settle after adding the dehydrating agent) is transported to the sludge settling tank 7 through pipelines; mud) after natural settlement, the floating water in the upper layer is discharged into the second water treatment device 35, and is discharged after being treated by the second water treatment device 35 to reach the standard. Detection, according to the detection results, the powder adding device 29 is set to add the amount of stabilizing and curing medicine to the sludge, and then the in-situ modification and curing system is started, and the sedimentation of the sludge is completed under the cooperative work of the in-situ modification device 31 and the powder adding device 29 The modified solidification treatment of the sludge in the pool 7, the modified sludge has been cured for three days, and the modified sludge that meets the requirements for the preparation of building materials is transported to the modified sludge silo 14 through the modified sludge transport device 11 for standby. The modified sludge that meets the requirements for preparing building materials is transported to the waste landfill 23 through the modified sludge transport device 11 for standard landfill. The mud cake in the modified sludge silo 14 enters the modified sludge crushing device 25 for crushing, and then enters the belt transport mixing device 27, the auxiliary material adding device 26 adds auxiliary materials to the modified sludge according to the design ratio, and the belt transport mixing device 27. Mix and stir each material. A part of the mixed material is used as the construction/greening soil field 28, and a part enters the modified sludge forming device 30 for molding, and the formed sample enters the sintering device 32 for sintering. The finished product transport vehicle 34 is transported to the place where it is needed for resource utilization. During the operation of the treatment and disposal system, regularly check the various devices of the treatment and disposal system, and promptly replace the equipment that does not meet the requirements of the treatment and disposal system and has potential safety hazards to ensure the safe operation of the treatment and disposal system. The next smooth operation and service life of the system.
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CN105819664A (en) * | 2016-05-12 | 2016-08-03 | 中国科学院武汉岩土力学研究所 | River and lake sludge treatment and disposal system |
CN111104744A (en) * | 2019-12-19 | 2020-05-05 | 中国电建集团成都勘测设计研究院有限公司 | Auxiliary type selection method for sand and stone crushing equipment |
-
2016
- 2016-05-12 CN CN201620433401.0U patent/CN206089401U/en not_active Withdrawn - After Issue
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105819664A (en) * | 2016-05-12 | 2016-08-03 | 中国科学院武汉岩土力学研究所 | River and lake sludge treatment and disposal system |
CN105819664B (en) * | 2016-05-12 | 2018-07-24 | 中国科学院武汉岩土力学研究所 | A kind of river and lake silt processing disposal system |
CN111104744A (en) * | 2019-12-19 | 2020-05-05 | 中国电建集团成都勘测设计研究院有限公司 | Auxiliary type selection method for sand and stone crushing equipment |
CN111104744B (en) * | 2019-12-19 | 2023-03-17 | 中国电建集团成都勘测设计研究院有限公司 | Auxiliary type selection method for sand and stone crushing equipment |
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