WO2022088327A1 - 一种陷阱式淤泥原位处理装置与方法 - Google Patents

一种陷阱式淤泥原位处理装置与方法 Download PDF

Info

Publication number
WO2022088327A1
WO2022088327A1 PCT/CN2020/131050 CN2020131050W WO2022088327A1 WO 2022088327 A1 WO2022088327 A1 WO 2022088327A1 CN 2020131050 W CN2020131050 W CN 2020131050W WO 2022088327 A1 WO2022088327 A1 WO 2022088327A1
Authority
WO
WIPO (PCT)
Prior art keywords
trap
pipe
heat
sludge
conducting
Prior art date
Application number
PCT/CN2020/131050
Other languages
English (en)
French (fr)
Inventor
胡明明
朱霖毅
潘正国
Original Assignee
无锡德林海环保科技股份有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 无锡德林海环保科技股份有限公司 filed Critical 无锡德林海环保科技股份有限公司
Publication of WO2022088327A1 publication Critical patent/WO2022088327A1/zh

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/13Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/02Biological treatment
    • C02F11/04Anaerobic treatment; Production of methane by such processes

Definitions

  • the invention relates to the technical field of environmental protection equipment, in particular to a trap-type sludge in-situ processing device and method.
  • the pollutants in the silt are mainly distributed in the floating mud and the flowing mud in the shallow 0-20 cm area of the bottom mud. It is black or grayish black, the geological deposition is relatively new, and the organic matter deposition rate is fast. It is the product of the impact of human activities (eutrophication or enclosure culture) on the water environment in recent decades.
  • This part of the silt has bedding characteristics, and is easily lifted up by comprehensive dynamic factors such as wind waves and wind blowing currents, and gathers in the downwind direction under the action of wind boosting.
  • the silt pollution layer can be resuspended in the water body when it is slightly stirred, and it is the main reservoir and release source of the source pollutants in the water body. The cleaning of bedding sludge can intuitively bring nutrients and heavy metals out of the polluted water body.
  • the existing sediment dredging technologies mainly include water conservancy scouring + pump suction, dredging + filling/shipping, stirring suction and other technologies.
  • water conservancy scouring + pump suction mainly include water conservancy scouring + pump suction, dredging + filling/shipping, stirring suction and other technologies.
  • the nutrients in the sludge are accelerated to the water body.
  • the cleared sludge needs to be dehydrated, stacked and landfilled, and it also occupies land resources, which is easy to cause secondary pollution.
  • the first object of the present invention is to provide a trap-type sludge in-situ treatment device, which can dry and dehydrate the sludge in-situ, thereby reducing the secondary pollution of the cleared sludge to the environment.
  • this scheme can use natural factors such as lake current to concentrate the silt in the trap tube for water isolation treatment, which has little disturbance to the benthic habitat, small impact range, and little damage to the underwater ecology.
  • the second object of the present invention is to provide a trap-type sludge in-situ treatment method, which adopts the above-mentioned in-situ treatment device.
  • a trap type sludge in-situ treatment device is characterized in that: it comprises a trap pipe, a water retaining pipe and a heating device;
  • the trap tube is used to be placed in a lake bed or a river bed, and the inside of the trap tube constitutes a trap cavity for storing silt;
  • the upper end of the water retaining pipe is higher than the water surface, and the lower end is butted with the upper end of the trap pipe to prevent river (lake) water from entering the trap cavity;
  • the heating device heats and dries the sludge in the trap cavity of the trap tube.
  • the present invention adopts the above technical solution, and the technical solution relates to a trap-type sludge in-situ treatment device
  • the sludge in-situ treatment device includes a trap pipe, a water retaining pipe and a heating device.
  • the trap tube is used to be placed in the lake bed or the river bed, and the silt can flow into the trap cavity through the action of artificial or water flow; in this way, the trap tube separates the silt in the trap cavity from the silt outside the tube.
  • the water retaining pipe can prevent the river water from entering the trap cavity, that is, the river water in the pipe is separated from the river water outside the pipe; in this way, the river water inside the retaining pipe can be drained.
  • the heating device heats and dries the sludge in the trap cavity of the trap tube, and the water vapor of the sludge is continuously evaporated and gradually dried.
  • this scheme Compared with the existing sludge cleaning, this scheme performs drying and dehydration treatment on the sludge in situ, which reduces the secondary pollution of the cleared sludge to the environment; and the scheme can use natural factors such as lake flow to concentrate the sludge in the environment.
  • the internal water isolation treatment of the trap pipe has little disturbance to the benthic habitat, small impact range, and little damage to the underwater ecology.
  • the heating device includes a heat conduction pipe capable of drilling into the ground to obtain geothermal energy, and a heat conduction component located inside the trap cavity of the trap tube and generating heat conduction between the heat conduction pipe and the heat conduction pipe.
  • the technical solution further defines the specific structure of the heating device. The heating device drills into the ground through a heat-conducting pipe to obtain geothermal energy and conducts the geothermal energy, that is, uses the geothermal energy to dry the stored sludge without consuming energy.
  • this solution also reduces pollution and potential safety hazards, and is not limited by conditions.
  • the heat-conducting component is disposed on the inner sidewall of the trap tube or formed inside the trap tube, and the heat-conducting tube and the heat-conducting component communicate with each other to achieve heat conduction.
  • this solution further defines that the heat-conducting component is arranged around the inner side wall of the trap tube or formed inside the trap tube, and the heat-conducting tube transfers heat to the heat-conducting component.
  • the heat-conducting component can heat and dry the sludge from the outside to the inside by enclosing the internal mud.
  • the surrounding mud is closer to the heat-conducting component and is easier to be heated and dried; the internal mud is subjected to heat conduction in multiple directions around the circumference. Therefore, it is also relatively easy to dry, so as to ensure that the sludge in each area is heated evenly.
  • a heat-conducting cavity is provided in the heat-conducting component, or a heat-conducting cavity is formed between the heat-conducting component and the trap tube; and a heat-conducting fluid medium that communicates with each other is provided in the heat-conducting tube and the heat-conducting cavity in the heat-conducting component.
  • the trap tube includes a bottom plate and a side wall arranged around the edge of the bottom plate; a trap cavity is formed between the side wall and the bottom plate, and the heat pipe passes through the bottom plate of the trap tube.
  • the trap tube separates the sludge in the trap cavity from the sludge outside the tube, so the trap tube is required to be enclosed by a side wall, but not a bottom plate.
  • the trap tube may not be provided with a bottom plate; however, in this solution, a bottom plate is provided at the bottom of the trap tube, which can improve drying efficiency and reduce drying time.
  • the heat-conducting component is an inner tube body disposed inside the trap tube; a heat-conducting cavity is formed between the inner tube body and the trap tube; the heat-conducting tube at least includes a lower tube section below the trap tube, and a tube above the trap tube.
  • the upper pipe section; the upper end of the lower pipe section is connected with the bottom plate of the trap tube, the upper end of the upper pipe section is higher than the water surface, and the lower end communicates with the inner pipe body or the trap pipe; the upper pipe section, the lower pipe section and the heat conduction cavity are connected with each other .
  • the solution further defines the connection structure of the heat conduction component, the trap tube and the heat conduction tube.
  • the heat-conducting component in this solution is an inner tube body, the inner tube body and the trap tube form an inner and outer tube, and a heat-conducting cavity is formed inside, similar to a heat-conducting sandwich; and the heat-conducting cavity is provided with two openings, One opening communicates with the lower pipe section, and the other opening communicates with the upper pipe section, so that the heat transfer cavity, the lower pipe section and the upper pipe section are all connected, and the heat transfer fluid medium can circulate between the heat transfer cavity, the lower pipe section and the upper pipe section.
  • the specific gravity of the bottom medium is lighter than that of the upper medium after heating, and the up-and-down convection is formed. Sludge heating.
  • the sludge far from the trap type sludge in-situ treatment device flows into the mud guide groove under the action of the lake flow, and then enters the trap pipe from the mud guide groove to realize the sludge removal. Natural collection.
  • the lower end of the water blocking pipe is sleeved on the outer end of the trap pipe.
  • the solution that the water retaining pipe is directly placed on the upper end of the trap pipe needs to be sealed at the joint, but the water retaining pipe in this solution is slightly larger than the trap pipe. The sealing effect can be achieved if the water retaining pipe is placed outside the trap pipe and directly inserted into the lake bed. Also sealed.
  • a trap type sludge in-situ treatment method is characterized in that: comprises the following steps:
  • S3 The silt in the trap tube is heated by a heating device. At the same time, the silt naturally undergoes anaerobic digestion and generates heat. Under the superposition of natural subsidence, geothermal and biochemical heat, the silt water vapor continuously evaporates, gradually dries and continues to settle and reduce volume , until the moisture content is lower than the preset standard;
  • the step S1 includes arranging a mud guide groove or digging a mud guide groove along the radial direction of the trap pipe; due to the fluidity of the mud, the mud close to the trap mouth of the trap type mud in-situ treatment device directly under the action of the lake flow.
  • the sludge that flows into the trap pipe and is far away from the trap-type sludge in-situ treatment device flows into the mud guide tank under the action of the lake flow, and then enters the trap pipe from the mud guide groove to realize the natural collection of sludge.
  • the heating device includes a heat transfer pipe that can be drilled into the ground to obtain geothermal energy, and a heat transfer component that is located inside the trap cavity of the trap tube and generates heat conduction with the heat transfer pipe.
  • the heat transfer pipe and the heat transfer cavity in the heat transfer component are provided with The heat-conducting fluid medium that conducts with each other;
  • Step S3 is specifically: injecting the heat-conducting fluid medium into the heat-conducting pipe, the heat-conducting fluid medium inside the heat-conducting pipe absorbs the underground heat, and flows to the upper part of the heat-conducting pipe and the heat-conducting components, and the sludge in the trap pipe is cleaned. heating.
  • the stored sludge is dried by using geothermal energy without consuming additional energy.
  • the sludge is dried by using geothermal heat, without adding flocculation and other chemicals, and avoiding the unusable sludge after chemical chemicals are used.
  • the trap-type sludge in-situ treatment device and method shown in this application realizes the continuous treatment of the flow dynamic sludge with the most serious bottom pollution, which is beneficial to the endogenous treatment of eutrophic water bodies.
  • FIG. 1 is a cross-sectional view of the trap-type sludge in-situ treatment device shown in Example 1.
  • FIG. 1 is a cross-sectional view of the trap-type sludge in-situ treatment device shown in Example 1.
  • FIG. 2 is a plan view of the trap-type sludge in-situ treatment device in Example 1.
  • FIG. 2 is a plan view of the trap-type sludge in-situ treatment device in Example 1.
  • FIG. 3 is a process flow diagram of the trap-type sludge in-situ treatment method in Example 2.
  • first and second are only used for descriptive purposes, and should not be construed as indicating or implying relative importance or implying the number of indicated technical features. Thus, a feature defined as “first” or “second” may expressly or implicitly include one or more of that feature.
  • plural means two or more, unless otherwise expressly defined.
  • the terms “installed”, “connected”, “connected”, “fixed” and other terms should be understood in a broad sense, for example, it may be a fixed connection or a detachable connection , or integrally connected; it can be a mechanical connection or an electrical connection; it can be a direct connection, or an indirect connection through an intermediate medium, or the internal communication between the two components.
  • installed e.g., it may be a fixed connection or a detachable connection , or integrally connected; it can be a mechanical connection or an electrical connection; it can be a direct connection, or an indirect connection through an intermediate medium, or the internal communication between the two components.
  • a first feature "on” or “under” a second feature may include the first and second features in direct contact, or may include the first and second features Not directly but through additional features between them.
  • the first feature being “above”, “over” and “above” the second feature includes the first feature being directly above and obliquely above the second feature, or simply means that the first feature is level higher than the second feature.
  • the first feature is “below”, “below” and “below” the second feature includes the first feature being directly below and diagonally below the second feature, or simply means that the first feature has a lower level than the second feature.
  • this embodiment relates to a trap-type sludge in-situ treatment device, including a trap pipe 2, a water retaining pipe 1 and a heating device.
  • the specific structures of the trap pipe 2, the water blocking pipe 1 and the heating device are as follows:
  • the trap tube 2 is used to be placed in the lake bed 7 or the river bed, and the trap tube 2 forms a trap cavity for storing sludge inside.
  • the trap tube 2 includes a bottom plate and a side wall arranged around the edge of the bottom plate, and a trap cavity is formed between the side wall and the bottom plate.
  • the trap tube 2 in this scheme is used to be placed in the lake bed 7 or the river bed, and the sludge 5 can flow into the trap cavity through the action of artificial or water flow.
  • the trap tube 2 needs to separate the sludge in the trap cavity from the sludge outside the tube.
  • the enclosed side wall is necessary, but the bottom plate is not necessary.
  • the trap tube 2 may not be provided with a bottom plate.
  • a bottom plate is provided at the bottom of the trap tube 2, which can improve the drying efficiency and reduce the drying time.
  • the diameter of the trap tube is greater than 10cm, the upper end is flush with the lake bed, and the depth of the lower end is not more than 100 meters.
  • the upper end of the water retaining pipe 1 is higher than the water surface 8, and the lower end is butted with the upper end of the trap pipe 2 to prevent the river water from entering the trap cavity; even if the river water in the pipe is separated from the river water outside the pipe.
  • the lower end of the water blocking pipe 1 is sleeved on the outer end of the trap pipe 2 .
  • the solution in which the water blocking pipe 1 is directly placed on the upper end of the trap pipe 2 is to seal the connection, and the water blocking pipe 1 in this scheme is slightly larger than the trap pipe 2. It can be inserted outside the trap pipe 2 and directly inserted into the lake bed 7 To achieve the sealing effect, no additional sealing is required.
  • the heating device heats and dries the sludge in the trap cavity of the trap tube 2 .
  • the heating device is used to heat the sludge in the trap cavity of the trap pipe 2, so that the sludge water vapor 10 is continuously evaporated and gradually dried.
  • the above-mentioned heating device can be any device that can be inserted into the trap cavity of the trap tube 2 to heat the sludge; for example, it can be an electric heating tube, which extends into the trap cavity of the trap tube 2 from the top of the water retaining tube 1 .
  • the heating device includes a heat transfer pipe 3 that can be drilled into the ground to obtain geothermal energy, and a heat transfer pipe 3 that is located inside the trap cavity of the trap pipe 2 and generates heat conduction with the heat transfer pipe 3 Part 11, the heat transfer pipe 3 passes through the bottom plate of the trap pipe 2, the upper end of the heat transfer pipe 3 is higher than the lake bed, and the depth of the lower end exceeds 100 meters.
  • the technical solution further defines the specific structure of the heating device. The heating device drills into the ground through the heat pipe 3 to obtain geothermal energy and conducts the geothermal energy, that is, the stored sludge is dried by using the geothermal energy without consuming additional energy. .
  • this solution also reduces pollution and potential safety hazards, and is not limited by conditions.
  • the heat-conducting component 11 is disposed on the inner side wall of the trap tube 2 or formed inside the trap tube 2 , and the heat-conducting tube 3 communicates with the heat-conducting component 11 to achieve heat conduction.
  • the heat-conducting member 11 is arranged around the inner wall of the trap tube 2 or is formed inside the trap tube 2, and the heat-transfer tube 3 dissipates heat 9
  • the heat-conducting component 11 can heat and dry the sludge from the outside to the inside by enclosing the internal mud.
  • the internal sludge is thermally conducted in multiple directions in the circumferential direction, so it is relatively easy to dry, so as to ensure that the sludge in each area is heated evenly.
  • the thermally conductive component 11 is provided with a thermally conductive cavity or a thermally conductive cavity 12 is formed between the thermally conductive component 11 and the trap tube 2 .
  • the heat-conducting fluid medium 4 in the heat-conducting pipe 3 and the heat-conducting cavity 12 in the heat-conducting component 11 is provided with the heat-conducting fluid medium 4, and the heat-conducting fluid medium 4 here is generally water.
  • the heat transfer pipe 3 obtains the geothermal heat
  • the heat 9 is transferred to the heat transfer cavity 12 in the heat transfer component 11 through the heat transfer fluid medium 4, and the heat conduction efficiency is higher.
  • the connection structure of the heat conduction component 11 , the trap tube 2 and the heat conduction tube 3 is as follows: the heat conduction component 11 is an inner tube body disposed inside the trap tube 2 , and a heat conduction cavity 12 is formed between the inner tube body and the trap tube 2 .
  • the heat transfer pipe 3 at least includes a lower pipe section 31 located below the trap pipe 2 and an upper pipe section 32 located above the trap pipe 2 .
  • the upper end of the lower pipe section 31 is connected to the bottom plate of the trap tube 2. Since the lower pipe section 31 needs to obtain geothermal energy and may need to be drilled into the ground several hundred meters, the lower pipe section 31 can be formed by splicing multiple pipe bodies.
  • the upper end of the upper pipe section 32 is higher than the water surface 8 , and the lower end communicates with the inner pipe body or trap pipe 2 .
  • the upper pipe section 32 , the lower pipe section 31 and the heat conduction cavity 12 are connected to each other.
  • the heat transfer pipe 3 transfers the heat 9 to the heat transfer member 11 through the heat transfer fluid medium 4
  • the heat transfer member 11 in this scheme is an inner tube body, and the inner tube body and the trap tube 2 form an inner and outer tube.
  • a heat conducting cavity 12 it is similar to a heat conducting interlayer.
  • the heat-conducting cavity 12 is provided with two openings, one opening communicates with the lower pipe section 31 and the other opening communicates with the upper pipe section 32, so that the heat-conducting cavity 12, the lower pipe section 31 and the upper pipe section 32 are all communicated, and the heat-conducting fluid medium 4 can be
  • the heat transfer cavity 12 , the lower pipe section 31 and the upper pipe section 32 communicate with each other.
  • the specific gravity is lighter than that of the upper medium to form up and down convection, and the heat-conducting fluid medium 4 flows into the heat-conducting cavity 12 through the heat-conducting pipe 3. , the sludge in the trap tube 2 is heated by the heat conducting member 11 .
  • the above-mentioned trap-type sludge in-situ treatment device further includes a plurality of mud guiding grooves 6 radially arranged relative to the trap pipe 2 .
  • a mud guiding groove 6 is also provided.
  • the mud guiding tank 6 in this scheme is used as a trap-type sludge in-situ treatment device, which is a kind of groove member and is an integral part of the device.
  • the mud guiding groove 6 can also be a trench temporarily excavated on the river bed. At this time, the mud guiding groove 6 is not a component of the trap-type sludge in-situ treatment device.
  • the stored sludge is dried by using geothermal energy without consuming energy.
  • the sludge is dried by using geothermal heat, without adding flocculation and other chemicals, and avoiding the unusable sludge after chemical chemicals are used.
  • the trap-type sludge in-situ treatment device and method shown in this application realizes the continuous treatment of the flow dynamic sludge with the most serious bottom pollution, which is beneficial to the endogenous treatment of eutrophic water bodies.
  • Embodiment 2 For the specific sludge treatment method of the trap-type sludge in-situ treatment device described in the above embodiment, refer to Embodiment 2.
  • this embodiment describes a trap-type sludge in-situ treatment method, which adopts the trap-type sludge in-situ treatment device in the above-mentioned embodiment 1, and specifically includes the following steps:
  • the sludge flows directly into the trap pipe 2, and the sludge far from the trap type sludge in-situ treatment device flows into the mud guide tank 6 under the action of the lake flow, and then enters the trap pipe 2 from the mud guide tank 6 to realize the natural collection of sludge.
  • S2 Cover the trap tube 2 with the water blocking tube 1, and drain the water on the trap tube 2.
  • S3 Use a heating device to heat the sludge in the trap pipe 2, specifically injecting water into the heat transfer pipe 3, the water inside the heat transfer pipe 3 absorbs the underground heat 9 and flows to the upper part of the heat transfer pipe 3 and the heat transfer component 11.
  • the sludge in the trap tube 2 is heated.
  • the silt naturally undergoes anaerobic digestion and generates heat 9.
  • the silt water vapor 10 continuously evaporates, gradually dries and continues to settle and reduce volume until the water content is lower than the preset standard.
  • S5 Repeat steps S1-S4 until the trap is filled with sludge with a moisture content lower than the preset standard, and then execute S6.
  • the collection represents the natural or artificial flow of silt into the trap pipe 2, that is, step S1;
  • Water blocking means that the water blocking pipe 1 covers the trap pipe 2 to prevent the river water from entering the trap cavity; that is, step S2;
  • Drying means that the heating device heats and dries the sludge in the trap tube 2, which is recorded in S3;
  • Digestion represents the organic matter in the anaerobic digestion sludge of the sludge entering the trap tube 2 under natural conditions, recorded in S3;
  • Sealing means covering the sludge in the trap tube 2 with a water-proof material, that is, S4;
  • a small cycle refers to repeating steps S1-S4; a large cycle refers to repeating steps S1-S6.
  • the temperature in the trap tube 2 can reach more than 30°C at a depth of 700 meters; when the lower end of the heat transfer tube 3 is inserted into the ground at a depth of 700 meters, the temperature in the trap tube 2 can also increase by about 6°C.
  • the silt in the trap pipe 2 is dried until the water content can be lower than 75%.
  • the 500-meter solution has higher drying efficiency and shorter time consumption.
  • the energy obtained by the heat transfer pipe 3 is related to the drying degree of the sludge in the trap pipe 2; under the condition that the drying time is sufficient, the above-mentioned device and method can make the sludge dry. can be lower than 60%.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Treatment Of Sludge (AREA)

Abstract

本发明涉及环保设备技术领域,尤其涉及一种陷阱式淤泥原位处理装置与方法。一种陷阱式淤泥原位处理装置,其特征在于:包括陷阱管、挡水管和加热装置;所述陷阱管用于置入湖床或河床内,陷阱管内部构成用于存放淤泥的陷阱腔;所述挡水管的上端高于水面,且下端与陷阱管上端对接,用以阻挡河水进入陷阱腔;所述加热装置对于陷阱管陷阱腔内的淤泥进行加热干化。本发明采用上述方案,该方案在原位上对于淤泥进行干化、脱水处理,降低了清出的淤泥对于环境的二次污染;并且该方案可利用湖流等自然因素将淤泥集中在陷阱管内部隔水处理,对底栖生境扰动小,影响范围小,对水底生态破坏小。

Description

一种陷阱式淤泥原位处理装置与方法 技术领域
本发明涉及环保设备技术领域,尤其涉及一种陷阱式淤泥原位处理装置与方法。
背景技术
随着生活水平的不断提高和人们环保意识的逐渐增强,人们对周边生活环境和生存空间质量都非常关注。面对日益恶化的各种环境,改善和治理的呼声越来越高。其中水体环境的保护和治污尤显突出。城市及其周围地区各种水体环境(包括水库、湖泊、河道、沟渠等)由于治理难度大,多年未治理使得大量淤泥沉积于水底,严重影响水体环境,使得水质变黑发臭,扰民问题时有发生。水体清淤是将河道、湖泊等的淤泥从水底切削、收集、抽取、输送至特定的地区集中进行环保处理的全过程。城市淤泥中生活垃圾、建筑垃圾堆积成山,湖底蕴藏大量的沼气、毒气、臭气甚至带有重金属等有害污染物质。如何进行环保清淤、清出的淤泥如何处理是当今国际社会都在探讨的问题。如果某个环节处理不好,清淤工程将带来严重的、大面积的二次污染,后果不堪设想。
淤泥中的污染物主要分布在底泥浅层0~20厘米的区域的浮泥以及流泥中,上部呈浆状(浮泥),下部呈流塑状(流泥),有臭味,一般呈黑色或灰黑色,地质沉积年代较新,有机质沉积速度快,为近几十年人类活动(富营养化或围隔养殖)对水环境影响的产物。此部分淤泥呈现推移质特征,极易在风浪、风吹流等综合动力因素作用下被掀起,并在风力助推作用下,向下风向聚集。淤泥的污染层在水体中稍微被搅动就能再悬浮,是水体内源污染物的主要蓄积库和释放源。推移质淤泥的清理,能够很直观的把污染水体的营养盐和重金属带出水体。
现有的底泥清淤技术主要有水利冲刷+泵吸、挖泥+吹填/船运、搅吸等技术,上述技术在实施过程中不但存在搅动底泥,加速淤泥中的营养盐向水体中释放的危害,清出的淤泥需要脱水、堆放和填埋还占用土地资源,易造成二次污染,甚至在乏科学认知和深入调研的情况下,把底泥挖出来清理掉,打破原有湖床河道水生态系统。针对上述弊端,有提出采用在需要底泥清淤出开挖一定数量及深度的淤泥捕获沟渠,通过自然水动力带动的浮泥、流泥经过沟渠时跌落到沟渠底部,此法虽然减少了清淤过程中底泥扰动的程度,但淤泥填满清出时仍面临脱水、堆放和填埋等问题,鉴于上述技术的各种缺陷,有必要对现有清淤技术中使用的装备进行改进,以实现原位的处理,降低淤泥处置过程中产生的次生危害。
发明内容
为了解决上述问题,本发明的第一目的在于提供一种陷阱式淤泥原位处理装置,该方案在原位上对于淤泥进行干化、脱水处理,降低了清出的淤泥对于环境的二次污染;并且该方案可利用湖流等自然因素将淤泥集中在陷阱管内部隔水处理,对底栖生境扰动小,影响范围小,对水底生态破坏小。
本发明的第二目的在于提供一种陷阱式淤泥原位处理方法,该陷阱式淤泥原位处理方法采用上述原位处理装置。
为了实现上述的目的,本发明采用了以下的技术方案:
一种陷阱式淤泥原位处理装置,其特征在于:包括陷阱管、挡水管和加热装置;
所述陷阱管用于置入湖床或河床内,陷阱管内部构成用于存放淤泥的陷阱腔;
所述挡水管的上端高于水面,且下端与陷阱管上端对接,用以阻挡河(湖)水进入陷阱腔;
所述加热装置对于陷阱管陷阱腔内的淤泥进行加热干化。
本发明采用上述技术方案,该技术方案涉及一种陷阱式淤泥原位处理装置,该淤泥原位处理装置包括陷阱管、挡水管和加热装置。其中,陷阱管用于置入湖床或河床内,通过人工或水体流动的作用使淤泥能够流入陷阱腔;如此,陷阱管将陷阱腔内的淤泥与管外的淤泥分隔开。挡水管则是能够阻挡河水进入陷阱腔,即采用管内的河水与管外的河水隔开;如此才能将挡水管内部河水抽干。加热装置对于陷阱管陷阱腔内的淤泥进行加热干化,淤泥水汽不断蒸发,逐渐干化。
与现有淤泥清理相比,该方案在原位上对于淤泥进行干化、脱水处理,降低了清出的淤泥对于环境的二次污染;并且该方案可利用湖流等自然因素将淤泥集中在陷阱管内部隔水处理,对底栖生境扰动小,影响范围小,对水底生态破坏小。
作为优选,所述加热装置包括能够钻入地底获取地热能的导热管,以及处于陷阱管陷阱腔内部并与所述导热管之间产生热传导的导热部件。该技术方案中进一步限定了加热装置的具体结构,该加热装置通过导热管钻入地底获取地热能并将地热能传导出来,即利用地热能对收纳的淤泥进行烘干,无需消耗能源。并且,该方案相比于其他加热方式,也减少污染和使用安全隐患,且不受条件的限制。
作为优选,所述导热部件设置在陷阱管的内侧壁或形成在陷阱管内部,导热管与导热部件相导通实现热传导。在上述技术方案记载利用地热能对收纳的淤泥进行烘干的原理上,本方案进一步限定了导热部件的围绕在陷阱管的内侧壁设置或形成在陷阱管内部,导热管将热量传递到导热部件上时,导热部件能以围合内部淤泥的方式从外至内对于淤泥加热干化,外围的淤泥与导热部件更近,更易于受热干化;内部的淤泥则受到周向多个方位的导热,故也 相对易于干化,如此保证各区域的淤泥加热均匀。
作为优选,所述导热部件内设有导热腔或者是导热部件与陷阱管之间构成导热腔;所述导热管和导热部件内的导热腔中设有相互导通的导热流体介质。在该技术方案中,导热管获取地热后是通过导热流体介质将热量传递至导热部件内的导热腔中,热传导效率更高。
作为优选,所述陷阱管包括底板以及围绕底板边缘设置的侧壁;所述侧壁和底板之间构成陷阱腔,导热管穿过所述陷阱管的底板。如上述技术方案所述,陷阱管将陷阱腔内的淤泥与管外的淤泥分隔开,故对于陷阱管来说其围合设置的侧壁是必须的,底板并非必须。在另一实施方案中,陷阱管可以不设置底板;但相比之下,该方案在陷阱管的底部设置底板,能够提升干化效率,减少干化所耗时间。
作为优选,所述导热部件为设置在陷阱管内侧的内管体;内管体与陷阱管之间构成导热腔;所述导热管至少包括处于陷阱管下方的下部管段,以及处于陷阱管上方的上部管段;所述下部管段的上端与陷阱管的底板相连接,上部管段的上端高于水面,下端与所述内管体或陷阱管相通;所述上部管段、下部管段和导热腔相导通。在上述方案记载导热管通过导热流体介质将热量传递至导热部件的方案基础上,该方案进一步限定了导热部件、陷阱管和导热管的连接结构。具体来说,该方案中的导热部件为内管体,内管体与陷阱管之间构成了内外管的形式且内部构成导热腔,类似导热夹层;而该导热腔上设有两个开口,一开口与下部管段相通,另一开口与上部管段相通,如此导热腔、下部管段和上部管段全部相通,导热流体介质能够在导热腔、下部管段和上部管段之间流通。当插入地底端在地热的作用下将导热管内的导热流体介质加热,底部介质升温后比重较上部介质比重轻而形成上下对流,导热流体介质经导热管流入导热腔内,通过导热部件对陷阱管内的淤泥加热。
作为优选,还包括相对所述陷阱管径向布置的若干条导泥槽,导泥槽的近端深度大于远端深度且近端指向陷阱腔。该技术方案还设置导泥槽,通过导泥槽的设置,使远离陷阱式淤泥原位处理装置的淤泥在湖流的作用下流进导泥槽,再从导泥槽进入陷阱管内,实现淤泥的自然收集。
作为优选,所述挡水管的下端套接于陷阱管的外端部上。挡水管直接置于陷阱管上端的方案是需要对连接处进行密封,而本方案中的挡水管比陷阱管略大,套在陷阱管外直接插在湖床中则可达到密封效果,不需要另外密封。
一种陷阱式淤泥原位处理方法,其特征在于:包括如下步骤:
S1:将陷阱管置入湖床或河床内,淤泥自然或人为流入陷阱管中,直至装满不再沉降为止;
S2:将挡水管罩住陷阱管,抽干陷阱管上覆水;
S3:采用加热装置对陷阱管内的淤泥进行加热,同时,淤泥自然发生厌氧消化作用并产生热 量,在自然沉降、地热和生化热叠加作用下淤泥水汽不断蒸发,逐渐干化并持续沉降减容,直至含水率低于预设标准;
S4:用隔水材料盖住陷阱管内的淤泥上,拔出挡水管;
S5:重复S1-S4步骤,直至陷阱内装满含水率低于预设标准的淤泥时,执行S6;
S6:先从位于陷阱管底部淤泥含水率最低的部分开始,用泵或适当方式清除陷阱管内淤泥,拔出挡水管。
作为优选,所述步骤S1包括布置导泥槽或挖取沿陷阱管径向布置导泥槽;由于淤泥存在流动性,靠近陷阱式淤泥原位处理装置陷阱口的淤泥在湖流的作用下直接流入到陷阱管内,远离陷阱式淤泥原位处理装置的淤泥在湖流的作用下流进导泥槽,再从导泥槽进入陷阱管内,实现淤泥的自然收集。
作为优选,加热装置包括能够钻入地底获取地热能的导热管,以及处于陷阱管陷阱腔内部并与所述导热管之间产生热传导的导热部件,导热管和导热部件内的导热腔中设有相互导通的导热流体介质;步骤S3具体是:在导热管中注入导热流体介质,导热管内部的导热流体介质吸收地下热量,并流动至导热管上部及导热部件中,对陷阱管内的淤泥进行加热。
综上所述,本发明与现有技术相比的有益效果是:
通过本发明所示出的陷阱式淤泥原位处理装置及方法,可利用湖流等自然因素收集淤泥与现有淤泥清理相比,不需要消耗能源,且在淤泥收集过程中对底栖生境扰动小,影响范围小,对水底生态破坏小。
通过本发明所示出的陷阱式淤泥原位处理装置及方法,利用地热能对收纳的淤泥进行烘干,无需消耗额外的能源。
通过本发明所示出的陷阱式淤泥原位处理装置及方法,利用地热对污泥进行干化,无需添加絮凝等药剂,避免了使用化学药剂后淤泥无法利用的。
最后,本申请所示出的陷阱式淤泥原位处理装置及方法,实现了对水底污染最为严重的流动态淤泥实现了连续性的处理,有利于富营养化水体的内源治理。
附图说明
图1为实施例1中所示的陷阱式淤泥原位处理装置剖视图。
图2为实施例1中的陷阱式淤泥原位处理装置俯视图。
图3为实施例2中的陷阱式淤泥原位处理方法工艺流程图。
图中,1、挡水管;2、陷阱管;3、导热管;4、导热流体介质;5.淤泥;6、导泥槽;7、湖床;8、水面;9、热量;10、水汽;11、导热部件;12、导热腔;31、下部管段;32、上部管段。
具体实施方式
下面详细描述本发明的实施例,所述实施例的示例在附图中示出,其中自始至终相同或类似的标号表示相同或类似的元件或具有相同或类似功能的元件。下面通过参考附图描述的实施例是示例性的,旨在用于解释本发明,而不能理解为对本发明的限制。
在本发明的描述中,需要理解的是,术语“中心”、“纵向”、“横向”、“长度”、“宽度”、“厚度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”“内”、“顺时针”、“逆时针”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本发明的限制。
此外,术语“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此,限定有“第一”、“第二”的特征可以明示或者隐含地包括一个或者更多个该特征。在本发明的描述中,除非另有说明,“多个”的含义是两个或两个以上,除非另有明确的限定。
在本发明中,除非另有明确的规定和限定,术语“安装”、“相连”、“连接”、“固定”等术语应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以根据具体情况理解上述术语在本发明中的具体含义。
在本发明中,除非另有明确的规定和限定,第一特征在第二特征之“上”或之“下”可以包括第一和第二特征直接接触,也可以包括第一和第二特征不是直接接触而是通过它们之间的另外的特征接触。而且,第一特征在第二特征“之上”、“上方”和“上面”包括第一特征在第二特征正上方和斜上方,或仅仅表示第一特征水平高度高于第二特征。第一特征在第二特征“之下”、“下方”和“下面”包括第一特征在第二特征正下方和斜下方,或仅仅表示第一特征水平高度小于第二特征。
实施例1:
如图1和2所示,本实施例涉及一种陷阱式淤泥原位处理装置,包括陷阱管2、挡水管1 和加热装置。陷阱管2、挡水管1和加热装置的具体结构如下:
所述陷阱管2用于置入湖床7或河床内,陷阱管2内部构成用于存放淤泥的陷阱腔。具体来说,所述陷阱管2包括底板以及围绕底板边缘设置的侧壁,所述侧壁和底板之间构成陷阱腔。此方案中的陷阱管2用于置入湖床7或河床内,通过人工或水体流动的作用使淤泥5能够流入陷阱腔。陷阱管2需将陷阱腔内的淤泥与管外的淤泥分隔开,对于陷阱管2来说其围合设置的侧壁是必须的,底板并非必须。在另一实施方案中,陷阱管2可以不设置底板。但相比之下,该方案在陷阱管2的底部设置底板,能够提升干化效率,减少干化所耗时间。在实际使用时,陷阱管直径大于10cm,上端与湖床齐平,下端深度不超过100米。
所述挡水管1的上端高于水面8,且下端与陷阱管2上端对接,用以阻挡河水进入陷阱腔;即使管内的河水与管外的河水隔开。在进一步的实施方案中,所述挡水管1的下端套接于陷阱管2的外端部上。挡水管1直接置于陷阱管2上端的方案是需要对连接处进行密封,而本方案中的挡水管1比陷阱管2略大,套在陷阱管2外直接插在湖床7中则可达到密封效果,不需要另外密封。
所述加热装置对于陷阱管2的陷阱腔内的淤泥进行加热干化。使用时一般在抽干挡水管1内部河水后,才使用加热装置对于陷阱管2的陷阱腔内的淤泥进行加热,使淤泥水汽10不断蒸发,逐渐干化。上述的加热装置可以是任意一种能够伸入陷阱管2的陷阱腔内,以对于淤泥进行加热的装置;如可以是电加热管,由挡水管1的顶部伸入陷阱管2的陷阱腔内。
在本实施例记载的更优选的方案中,所述加热装置包括能够钻入地底获取地热能的导热管3,以及处于陷阱管2陷阱腔内部并与所述导热管3之间产生热传导的导热部件11,导热管3穿过所述陷阱管2的底板,所述的导热管3上端高于湖床,下端深度超过100米。该技术方案中进一步限定了加热装置的具体结构,该加热装置通过导热管3钻入地底获取地热能并将地热能传导出来,即利用地热能对收纳的淤泥进行烘干,无需消耗额外的能源。并且,该方案相比于其他加热方式,也减少污染和使用安全隐患,并不受条件的限制。在进一步的实施方案中,所述导热部件11设置在陷阱管2的内侧壁或形成在陷阱管2内部,导热管3与导热部件11相导通实现热传导。上述技术方案记载利用地热能对收纳的淤泥进行烘干的原理上,本方案进一步限定了导热部件11的围绕在陷阱管2的内侧壁设置或形成在陷阱管2内部,导热管3将热量9传递到导热部件11上时,导热部件11能以围合内部淤泥的方式从外至内对于淤泥加热干化,外围的淤泥与导热部件11更近,更易于受热干化。内部的淤泥则受到周向多个方位的导热,故也相对易于干化,如此保证各区域的淤泥加热均匀。
基于上述方案,本方案中的导热部件11内设有导热腔或者是导热部件11与陷阱管2之间构成导热腔12。所述导热管3和导热部件11内的导热腔12中设有相互导通的导热流体介 质4,此处的导热流体介质4一般选用水。导热管3获取地热后是通过导热流体介质4将热量9传递至导热部件11内的导热腔12中,热传导效率更高。导热部件11、陷阱管2和导热管3的连接结构如下:所述导热部件11为设置在陷阱管2内侧的内管体,内管体与陷阱管2之间构成导热腔12。所述导热管3至少包括处于陷阱管2下方的下部管段31,以及处于陷阱管2上方的上部管段32。所述下部管段31的上端与陷阱管2的底板相连接,由于下部管段31需要获得地热能,可能需要钻入几百米的地底,故下部管段31可采用是多根管体拼接构成。上部管段32的上端高于水面8,下端与所述内管体或陷阱管2相通。所述上部管段32、下部管段31和导热腔12相导通。在上述方案记载导热管3通过导热流体介质4将热量9传递至导热部件11的方案基础上,该方案中的导热部件11为内管体,内管体与陷阱管2之间构成了内外管的形式且内部构成导热腔12,类似导热夹层。而该导热腔12上设有两个开口,一开口与下部管段31相通,另一开口与上部管段32相通,如此导热腔12、下部管段31和上部管段32全部相通,导热流体介质4能够在导热腔12、下部管段31和上部管段32之间流通。当插入地底端在地热的作用下将导热管3内的导热流体介质4加热,当底部介质升温后比重较上部介质比重轻而形成上下对流,导热流体介质4经导热管3流入导热腔12内,通过导热部件11对陷阱管2内的淤泥加热。
最后,上述陷阱式淤泥原位处理装置还包括相对所述陷阱管2径向布置的若干条导泥槽6,导泥槽6的近端深度大于远端深度且近端指向陷阱腔。该技术方案还设置导泥槽6,通过导泥槽6的设置,使远离陷阱式淤泥原位处理装置的淤泥在湖流的作用下流进导泥槽6,再从导泥槽6进入陷阱管2内,实现淤泥的自然收集。此方案中的导泥槽6作为陷阱式淤泥原位处理装置,是一种沟槽构件,为装置的一组成部分。当然导泥槽6也可以是临时在河床上开挖的沟渠,此时导泥槽6就不作为陷阱式淤泥原位处理装置的组成部分。
综上所述,本发明与现有技术相比的有益效果是:
通过本发明所示出的陷阱式淤泥原位处理装置及方法,可利用湖流等自然因素收集淤泥与现有淤泥清理相比,不需要消耗能源,且在淤泥收集过程中对底栖生境扰动小,影响范围小,对水底生态破坏小。
通过本发明所示出的陷阱式淤泥原位处理装置及方法,利用地热能对收纳的淤泥进行烘干,无需消耗能源。
通过本发明所示出的陷阱式淤泥原位处理装置及方法,利用地热对污泥进行干化,无需添加絮凝等药剂,避免了使用化学药剂后淤泥无法利用的。
最后,本申请所示出的陷阱式淤泥原位处理装置及方法,实现了对水底污染最为严重的流动态淤泥实现了连续性的处理,有利于富营养化水体的内源治理。
上述实施例记载的陷阱式淤泥原位处理装置的具体淤泥处理方法,则参考实施例2。
实施例2:
如图3所示,本实施例记载一种陷阱式淤泥原位处理方法,该处理方法采用上述实施例1中的陷阱式淤泥原位处理装置,具体包括如下步骤:
S1:将陷阱管2置入湖床7或河床内,淤泥自然或人为流入陷阱管2中,直至装满不再沉降为止。具体来说,该步骤还布置导泥槽6或挖取沿陷阱管2径向布置导泥槽6;由于淤泥存在流动性,靠近陷阱式淤泥原位处理装置陷阱口的淤泥在湖流的作用下直接流入到陷阱管2内,远离陷阱式淤泥原位处理装置的淤泥在湖流的作用下流进导泥槽6,再从导泥槽6进入陷阱管2内,实现淤泥的自然收集。
S2:将挡水管1罩住陷阱管2,抽干陷阱管2上覆水。
S3:采用加热装置对陷阱管2内的淤泥进行加热,具体是在导热管3中注入水,导热管3内部的水吸收地下热量9,并流动至导热管3上部及导热部件11中,对陷阱管2内的淤泥进行加热。同时,淤泥自然发生厌氧消化作用并产生热量9,在自然沉降、地热和生化热叠加作用下淤泥水汽10不断蒸发,逐渐干化并持续沉降减容,直至含水率低于预设标准。
S4:用隔水材料盖住陷阱管2内的淤泥上,拔出挡水管1。
S5:重复S1-S4步骤,直至陷阱内装满含水率低于预设标准的淤泥时,执行S6。
S6:先从位于陷阱管底部淤泥含水率最低的部分开始,用泵或适当方式清除陷阱管2内整管淤泥,拔出挡水管1。
以下是对于附图3中框图含义进行说明,其中
收集代表将淤泥自然或人为流入陷阱管2中,即指步骤S1;
挡水代表将挡水管1罩住陷阱管2,阻挡河水进入陷阱腔;即指步骤S2;
干化代表加热装置对陷阱管2内的淤泥进行加热干化,记载在S3中;
消化代表进入陷阱管2中的淤泥在自然条件下的厌氧消化淤泥中的有机质,记载在S3中;
封存代表用隔水材料盖住陷阱管2内的淤泥上,即指S4;
清除代表将陷阱管2内整管淤泥清掉,即指步骤S6;
小循环是指重复步骤S1-S4;大循环是指重复步骤S1-S6。
实验记录:
申请人采用实施例1中记载的陷阱式淤泥原位处理装置和实施例2中记载的一种陷阱式淤泥原位处理方法,通过多次实验得到以下数据;当导热管3下端端插入地底500米深度, 陷阱管2内的温度能够达到30℃以上;当导热管3下端端插入地底700米深度,陷阱管2内的温度还能提升6℃左右。虽然两组数据中,导热管插入地底的深度不同,但陷阱管2内的淤泥被干化至含水率都能能低于75%,不过导热管3插入地底700米的方案相比于插入地底500米的方案,干化效率更高,所花费时间更短。从其实验可以看出导热管3所能获得的能量与陷阱管2内的淤泥被干化程度有关;在干化时间足够的情况下,上述装置和方法可使淤泥被干化的含水率是可以低于60%。
在本说明书的描述中,参考术语“一个实施例”、“一些实施例”、“示例”、“具体示例”、或“一些示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本发明的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不一定指的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任何的一个或多个实施例或示例中以合适的方式结合。
尽管上面已经示出和描述了本发明的实施例,可以理解的是,上述实施例是示例性的,不能理解为对本发明的限制,本领域的普通技术人员在不脱离本发明的原理和宗旨的情况下在本发明的范围内可以对上述实施例进行变化、修改、替换和变型。

Claims (10)

  1. 一种陷阱式淤泥原位处理装置,其特征在于:包括陷阱管(2)、挡水管(1)和加热装置;
    所述陷阱管(2)用于置入湖床(7)或河床内,陷阱管(2)内部构成用于存放淤泥(5)的陷阱腔;
    所述挡水管(1)的上端高于水面(8),且下端与陷阱管(2)上端对接,用以阻挡河(湖)水进入陷阱腔;
    所述加热装置用于对陷阱管(2)陷阱腔内的淤泥进行加热干化。
  2. 根据权利要求1所述的一种陷阱式淤泥原位处理装置,其特征在于:所述加热装置包括能够钻入地底获取地热能的导热管(3),以及处于陷阱管(2)陷阱腔内部并与所述导热管(3)之间产生热传导的导热部件(11)。
  3. 根据权利要求2所述的一种陷阱式淤泥原位处理装置,其特征在于:所述导热部件(11)设置在陷阱管(2)的内侧壁或形成在陷阱管(2)内部,导热管(3)与导热部件(11)相导通实现热传导。
  4. 根据权利要求3所述的一种陷阱式淤泥原位处理装置,其特征在于:所述导热部件(11)内设有导热腔(12)或者是导热部件(11)与陷阱管(2)之间构成导热腔(12);所述导热管(3)和导热部件(11)内的导热腔(12)中设有相互导通的导热流体介质(4)。
  5. 根据权利要求1~4中任一项所述的一种陷阱式淤泥原位处理装置,其特征在于:所述陷阱管(2)包括底板以及围绕底板边缘设置的侧壁;所述侧壁和底板之间构成陷阱腔,导热管(3)穿过所述陷阱管(2)的底板。
  6. 根据权利要求5所述的一种陷阱式淤泥原位处理装置,其特征在于:所述导热部件(11)为设置在陷阱管(2)内侧的内管体;内管体与陷阱管(2)之间构成导热腔(12);所述导热管(3)至少包括处于陷阱管(2)下方的下部管段(31),以及处于陷阱管(2)上方的上部管段(32);所述下部管段(31)的上端与陷阱管(2)的底板相连接,上部管段(32)的上端高于水面(8),下端与所述内管体或陷阱管(2)相通;所述上部管段(32)、下部管段(31)和导热腔(12)相导通。
  7. 根据权利要求1所述的一种陷阱式淤泥原位处理装置,其特征在于:还包括相对所述陷阱管(2)径向布置的若干条导泥槽(6),导泥槽(6)的近端深度大于远端深度且近端指向陷阱腔。
  8. 一种陷阱式淤泥原位处理方法,其特征在于:包括如下步骤:
    S1:将陷阱管(2)置入湖床(7)或河床内,淤泥(5)自然或人为流入陷阱管(2)中,直至装满不再沉降为止;
    S2:将挡水管(1)罩住陷阱管(2),抽干陷阱管(2)上覆水;
    S3:采用加热装置对陷阱管(2)内的淤泥进行加热,同时,淤泥自然发生厌氧消化作用并产生热量(9),在自然沉降、加热和生化热叠加作用下淤泥水汽(10)不断蒸发,逐渐干化并持续沉降减容,直至含水率低于预设标准;
    S4:用隔水材料盖住陷阱管(2)内的淤泥上,拔出挡水管(1);
    S5:重复S1-S4步骤;直至陷阱内装满含水率低于预设标准的淤泥时,执行S6;
    S6:清除陷阱管(2)内整管淤泥,拔出挡水管(1)。
  9. 根据权利要求8所述的一种陷阱式淤泥原位处理方法,其特征在于:所述步骤S1包括布置导泥槽(6)或挖取沿陷阱管(2)径向布置导泥槽(6);靠近陷阱式淤泥原位处理装置陷阱口的淤泥在湖流的作用下直接流入到陷阱管(2)内,远离陷阱式淤泥原位处理装置的淤泥在湖流的作用下流进导泥槽(6),再从导泥槽(6)进入陷阱管(2)内,实现淤泥的自然收集。
  10. 根据权利要求8所述的一种陷阱式淤泥原位处理方法,其特征在于:步骤S3中的加热装置对陷阱管(2)内的淤泥进行加热,具体是指在导热管(3)中注入导热流体介质(4),导热管(3)内部的导热流体介质(4)吸收地下热量(9),并流动至导热管(3)上部及导热部件(11)中,对陷阱管(2)内的淤泥进行加热。
PCT/CN2020/131050 2020-10-26 2020-11-24 一种陷阱式淤泥原位处理装置与方法 WO2022088327A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202011157842.XA CN113045173A (zh) 2020-10-26 2020-10-26 一种陷阱式淤泥原位处理装置及方法
CN202011157842.X 2020-10-26

Publications (1)

Publication Number Publication Date
WO2022088327A1 true WO2022088327A1 (zh) 2022-05-05

Family

ID=76507815

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2020/131050 WO2022088327A1 (zh) 2020-10-26 2020-11-24 一种陷阱式淤泥原位处理装置与方法

Country Status (2)

Country Link
CN (1) CN113045173A (zh)
WO (1) WO2022088327A1 (zh)

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5330291A (en) * 1991-11-13 1994-07-19 Battelle Memorial Institute Heating of solid earthen material, measuring moisture and resistivity
US20070154267A1 (en) * 2005-11-28 2007-07-05 Bratton Wesley L In situ immobilzation of subsurface contamination
CN107746163A (zh) * 2017-11-22 2018-03-02 长江水利委员会长江科学院 一种基于孔隙水导排的河湖污染底泥原位减量除污装置
CN108341569A (zh) * 2018-04-11 2018-07-31 长江水利委员会长江科学院 一种重金属污染河湖底泥原位修复系统及方法
CN108358419A (zh) * 2018-01-23 2018-08-03 中环沃野环保有限公司 原位式无动力模块化泥水分离装置及泥水分离的方法
CN109174948A (zh) * 2018-10-11 2019-01-11 江苏大地益源环境修复有限公司 一种用于原位或异位热脱附土壤修复的传热装置
CN110842019A (zh) * 2019-11-30 2020-02-28 上海康恒环境修复有限公司 一种加热井结构
CN210208077U (zh) * 2019-05-20 2020-03-31 湖南恒凯环保科技投资有限公司 一种用于原位热脱附土壤修复的传热装置
CN210497636U (zh) * 2019-08-21 2020-05-12 森特士兴集团股份有限公司 一种原位土壤热脱附用加热井系统

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5647691A (en) * 1994-11-14 1997-07-15 Wirth; John C.J. Method and apparatus for transferring mud and silt
JP4132210B2 (ja) * 1998-04-30 2008-08-13 株式会社Adeka 河川、湖沼、海洋の浄化方法
CN104180695A (zh) * 2013-05-25 2014-12-03 滕州市通达电子有限公司 导管式地热交换器
CN105859096A (zh) * 2016-05-24 2016-08-17 宁夏环境科学研究院(有限责任公司) 一种浅表层地热能干化污泥系统及干化方法
CN106946339B (zh) * 2017-02-08 2020-02-21 中国科学院南京地理与湖泊研究所 一种河道原位净化及生态修复方法
CN206502728U (zh) * 2017-02-14 2017-09-19 安徽师范大学 一种黑臭水体底泥的原位处理装置
CN107916689A (zh) * 2017-10-06 2018-04-17 中国水利水电科学研究院 一种环保清淤装置及其应用方法
CN109336258A (zh) * 2018-11-26 2019-02-15 珠江水利委员会珠江水利科学研究院 一种富营养化水体的生态修复方法
CN111719617B (zh) * 2020-06-24 2023-05-12 天津大学 一种水底底泥封闭清淤装置及方法

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5330291A (en) * 1991-11-13 1994-07-19 Battelle Memorial Institute Heating of solid earthen material, measuring moisture and resistivity
US20070154267A1 (en) * 2005-11-28 2007-07-05 Bratton Wesley L In situ immobilzation of subsurface contamination
CN107746163A (zh) * 2017-11-22 2018-03-02 长江水利委员会长江科学院 一种基于孔隙水导排的河湖污染底泥原位减量除污装置
CN108358419A (zh) * 2018-01-23 2018-08-03 中环沃野环保有限公司 原位式无动力模块化泥水分离装置及泥水分离的方法
CN108341569A (zh) * 2018-04-11 2018-07-31 长江水利委员会长江科学院 一种重金属污染河湖底泥原位修复系统及方法
CN109174948A (zh) * 2018-10-11 2019-01-11 江苏大地益源环境修复有限公司 一种用于原位或异位热脱附土壤修复的传热装置
CN210208077U (zh) * 2019-05-20 2020-03-31 湖南恒凯环保科技投资有限公司 一种用于原位热脱附土壤修复的传热装置
CN210497636U (zh) * 2019-08-21 2020-05-12 森特士兴集团股份有限公司 一种原位土壤热脱附用加热井系统
CN110842019A (zh) * 2019-11-30 2020-02-28 上海康恒环境修复有限公司 一种加热井结构

Also Published As

Publication number Publication date
CN113045173A (zh) 2021-06-29

Similar Documents

Publication Publication Date Title
WO2022088328A1 (zh) 一种沉降式淤泥原位处理装置及方法
CN102587352B (zh) 一种软土地基的热排水固结处理装置及其处理方法
CN101831903B (zh) 一种软地基处理方法
CN101705680B (zh) 能够加快疏浚底泥脱水干化过程的堆场构建方法
US9039326B1 (en) Tidal power system and methods
CN104829071B (zh) 一种工程泥浆快速处理装置及使用方法
CN206089292U (zh) 一种油田采油污水处理装置
WO2022088327A1 (zh) 一种陷阱式淤泥原位处理装置与方法
CN214167724U (zh) 一种沉降式淤泥原位处理装置
CN213950945U (zh) 一种陷阱式淤泥原位处理装置
CN207878610U (zh) 一种基于土工管袋污泥脱水技术的配套排水装置
CN105399290A (zh) 一种农村河道清淤施工方法
CN202117047U (zh) 淤泥堆场快速排水装置
CN214218387U (zh) 一种用于低渗透性区域有机污染地下水修复系统
CN208379740U (zh) 一种生态型雨水井
CN207314415U (zh) 一种水利工程清淤设备
CN207002509U (zh) 一种人工湿地系统
CN204491572U (zh) 多功能集成管井排水振冲一体化装置
CN105271511A (zh) 一种分散式污水处理装置及其安装方法
CN218572988U (zh) 一种清淤底泥快速固液分离机
CN217459179U (zh) 一种污染底泥清除装置
CN219261074U (zh) 一种基坑槽底埋泵降水结构
CN217053432U (zh) 一种节能基坑降排水装置
CN220034307U (zh) 一种用于江河湖库疏浚底泥转驳的泥驳船
US10458087B2 (en) System and method for dewatering sediment ponds

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20959486

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20959486

Country of ref document: EP

Kind code of ref document: A1