CN204714625U - Constructing tunnel advanced sewage treatment system - Google Patents

Constructing tunnel advanced sewage treatment system Download PDF

Info

Publication number
CN204714625U
CN204714625U CN201520279001.4U CN201520279001U CN204714625U CN 204714625 U CN204714625 U CN 204714625U CN 201520279001 U CN201520279001 U CN 201520279001U CN 204714625 U CN204714625 U CN 204714625U
Authority
CN
China
Prior art keywords
tank
oil
inlet
outlet
filter tank
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Lifetime
Application number
CN201520279001.4U
Other languages
Chinese (zh)
Inventor
杨志安
刘继鹏
汤贵海
庞前凤
司瑞明
邢立军
郭世荣
张明睿
徐小燕
王宾
朱冠劲
孙晓峰
胡观富
罗军
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
First Engineering Co Ltd of China Railway 22nd Bureau Group Co Ltd
China Railway 22nd Bureau Group Co Ltd
Original Assignee
First Engineering Co Ltd of China Railway 22nd Bureau Group Co Ltd
China Railway 22nd Bureau Group Co Ltd
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 First Engineering Co Ltd of China Railway 22nd Bureau Group Co Ltd, China Railway 22nd Bureau Group Co Ltd filed Critical First Engineering Co Ltd of China Railway 22nd Bureau Group Co Ltd
Priority to CN201520279001.4U priority Critical patent/CN204714625U/en
Application granted granted Critical
Publication of CN204714625U publication Critical patent/CN204714625U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

本实用新型公开了一种隧道污水深度处理系统,其特征是:该系统的沉砂池(1)处设有隧道污水入口,沉砂池(1)出口经由加药池(2)与隔油沉淀池(3)入口连通;所述隔油沉淀池(3)的含油废水出口通过气浮过滤设备(4)连通砂滤罐(5)入口,所述隔油衬垫尺(3)的不含有废水出口直接连通砂滤罐(5)入口;所述砂滤罐(5)出口与活性炭过滤罐(6)入口连通;活性炭过滤罐(6)出口与回用水池(7)连通。整套系统设备的利用可以有效的对隧道排放废水中的多种污染物进行净化处理,避免施工过程中的污水排放对附近水源的污染。

The utility model discloses a tunnel sewage advanced treatment system, which is characterized in that: the grit chamber (1) of the system is provided with a tunnel sewage inlet, and the grit chamber (1) exits through the dosing tank (2) and the oil separation tank. The inlet of the sedimentation tank (3) is connected; the oily waste water outlet of the oil-separating sedimentation tank (3) is connected to the inlet of the sand filter tank (5) through the air flotation filter equipment (4), and the oil-separating liner ruler (3) is not The waste water outlet is directly connected to the inlet of the sand filter tank (5); the outlet of the sand filter tank (5) is connected to the inlet of the activated carbon filter tank (6); the outlet of the activated carbon filter tank (6) is connected to the reuse water pool (7). The use of the whole set of system equipment can effectively purify various pollutants in the wastewater discharged from the tunnel, and avoid the pollution of nearby water sources by the sewage discharge during the construction process.

Description

隧道施工污水深度处理系统Tunnel Construction Sewage Advanced Treatment System

技术领域 technical field

本实用新型涉及污水处理领域,特别是涉及一种隧道施工污水深度处理系统。 The utility model relates to the field of sewage treatment, in particular to an advanced treatment system for tunnel construction sewage.

背景技术 Background technique

隧道施工中,隧道排水处理是一项重要的工作。为了避免施工过程中的污水排放对附近水源的污染,隧道施工地附近需要增设污水处理站。污水处理站的处理能力主要考虑两方面:污水水量和污水的水质。 In tunnel construction, tunnel drainage treatment is an important task. In order to avoid pollution of nearby water sources by sewage discharge during construction, a sewage treatment station needs to be added near the tunnel construction site. The treatment capacity of the sewage treatment station mainly considers two aspects: the amount of sewage water and the water quality of sewage.

隧道的水质由于隧道内的涌水主要为地下水,成分较纯净,主要污染物为沿途混入的固体悬浮物。而隧道污水的水量相对来说比较复杂,主要有以下几方面:与施工洞身段所处的涌水量有关;施工进尺的长度有关;衬砌完成跟进的速度有关;满足施工工艺所需生产用水;洞口至处理站段雨期汇聚水量等。 The water quality of the tunnel is mainly ground water with relatively pure components, and the main pollutants are the solid suspended matter mixed along the way. The water volume of tunnel sewage is relatively complicated, mainly in the following aspects: it is related to the water inflow in the construction tunnel body; it is related to the length of construction footage; it is related to the speed of lining completion follow-up; it can meet the production water required by the construction process; The amount of accumulated water in the rainy season from the entrance of the cave to the treatment station, etc.

实用新型内容 Utility model content

本实用新型所要解决的技术问题是:提供一种隧道施工污水深度处理系统,综合采用了简单可行的沉砂、混凝沉淀工艺、隔油气浮处理工艺、砂滤、活性炭等深度处理工艺,实现对隧道废水的良性循环使用。 The technical problem to be solved by the utility model is: to provide an advanced treatment system for tunnel construction sewage, which comprehensively adopts simple and feasible advanced treatment processes such as sand settling, coagulation sedimentation process, oil separation and air flotation treatment process, sand filter, activated carbon, etc., to realize The virtuous recycling of tunnel wastewater.

本实用新型所要解决的技术问题是通过以下技术方案实现的: The technical problem to be solved by the utility model is achieved through the following technical solutions:

一种隧道污水深度处理系统,该系统的沉砂池处设有隧道污水入口,沉砂池出口经由加药池与隔油沉淀池入口连通;所述隔油沉淀池的含油废水出口通过气浮过滤设备连通砂滤罐入口,所述隔油衬垫尺的不含有废水出口直接连通砂滤罐入口;所述砂滤罐出口与活性炭过滤罐入口连通;活性炭过滤罐出口与回用水池连通。 A tunnel sewage advanced treatment system, the grit chamber of the system is provided with a tunnel sewage inlet, and the grit chamber outlet is connected to the oil separation sedimentation tank entrance through the chemical dosing tank; the oily waste water outlet of the oil separation sedimentation tank is passed through the air flotation The filter equipment is connected to the inlet of the sand filter tank, and the outlet of the oil-separating liner ruler that does not contain waste water is directly connected to the inlet of the sand filter tank; the outlet of the sand filter tank is connected to the inlet of the activated carbon filter tank; the outlet of the activated carbon filter tank is connected to the reuse water pool.

所述沉砂池采用平流式沉砂池,沉砂池分为两格。沉砂池是设在处理构筑物之前的泥水分离的设施,分离的沉淀物质多为颗粒较大的砂子,沉淀物质比重较大,无机成分高,含水量低。污水在迁移、流动和汇集过程中不可避免会混入泥砂,污水中的砂如果不预先沉降分离去除,则会影响后续处理设备的运行。最主要的是磨损机泵、堵塞管网,干扰甚至破坏生化处理工艺过程。平流沉砂池得座数或分格数不得少于两个,宜按并联系列设计,污水量较小时,一备一用;较大时,同时工作。分格的平流式沉砂池是常用的池型,污水在池内沿水 平方向流动,具有构造简单,截流无机颗粒效果较好的优点。 The grit chamber adopts an advection type grit chamber, and the grit chamber is divided into two grids. The grit chamber is a facility for the separation of mud and water before the treatment of structures. The separated sediments are mostly sand with large particles. The proportion of sediments is relatively large, the inorganic components are high, and the water content is low. Sewage will inevitably be mixed with mud and sand in the process of migration, flow and collection. If the sand in the sewage is not pre-sedimented and separated, it will affect the operation of subsequent treatment equipment. The most important thing is to wear the machine pump, block the pipe network, interfere or even destroy the biochemical treatment process. The number of seats or divisions of the advection grit chamber should not be less than two, and it should be designed as a parallel series. When the amount of sewage is small, one is reserved and the other is used; when it is large, it should work at the same time. The grid advection grit chamber is a commonly used type of pond, and the sewage flows in the horizontal direction in the pond, which has the advantages of simple structure and good effect of intercepting inorganic particles.

所述隔油沉淀池还设有油出口,油出口外接集油桶。 The oil separation sedimentation tank is also provided with an oil outlet, and the oil outlet is externally connected to an oil collecting barrel.

所述沉砂池、隔油沉淀池的出水口高度低于入水口高度;所述砂滤罐的出水口高度高于入水口。 The height of the water outlet of the grit chamber and the oil separation sedimentation tank is lower than that of the water inlet; the height of the water outlet of the sand filter tank is higher than the water inlet.

所述加药池和隔油沉淀池的含油废水入口分别外接有加药机。 The oily wastewater inlets of the dosing tank and the oil-separating sedimentation tank are respectively externally connected with a dosing machine.

本实用新型采用上述技术方案所具有的技术效果是: The technical effect that the utility model adopts above-mentioned technical scheme to have is:

(1)合理确定污水处理站的处理能力,适当的考虑突增涌水量,提高应对突发情况下污水站的处理能力; (1) Reasonably determine the processing capacity of the sewage treatment station, properly consider the sudden increase in water inflow, and improve the processing capacity of the sewage station in response to emergencies;

(2)根据实际隧道污水污染物种类和含量,采用了合理的处理工艺,如对要求一般的不含油类污染物的隧道污水处理,宜采用沉砂+混凝沉淀工艺,含油污水宜采用混凝沉淀+气浮除油工艺,对有要求的隧道污水处理,宜采用混凝沉淀+深度处理(砂滤、活性炭等)工艺; (2) According to the type and content of actual tunnel sewage pollutants, a reasonable treatment process is adopted. For example, for the treatment of tunnel sewage without oil pollutants in general requirements, sand settling + coagulation sedimentation process should be adopted, and oily sewage should be mixed Coagulation sedimentation + air flotation degreasing process, for tunnel sewage treatment with requirements, coagulation sedimentation + advanced treatment (sand filter, activated carbon, etc.) process should be adopted;

(3)合理利用了天然地形、地貌,对各构筑物标高进行合理设计,尽量减少污水处理中间的动力提升,使各构筑物在重力流的水力条件下运行。 (3) Reasonable use of natural topography and landforms, reasonable design of the elevation of each structure, minimizing the power lift in the middle of sewage treatment, so that each structure operates under the hydraulic conditions of gravity flow.

附图说明 Description of drawings

下面结合附图对本实用新型作进一步说明 Below in conjunction with accompanying drawing, the utility model will be further described

图1为本实用新型处理流程图 Fig. 1 is the utility model processing flowchart

其中,1-沉砂池,2-加药池,3-隔油沉淀池,4-气浮过滤设备,5-砂滤罐,6-活性炭过滤罐,7-回用水池,8-集油桶,9-加药机 Among them, 1-grit chamber, 2-dosing tank, 3-oil separation sedimentation tank, 4-air flotation filter equipment, 5-sand filter tank, 6-activated carbon filter tank, 7-reuse water tank, 8-oil collection barrel, 9-dosing machine

具体实施方式 Detailed ways

如图1所示的一种隧道污水深度处理系统,该系统的沉砂池1处设有隧道污水入口,沉砂池1出口经由加药池2与隔油沉淀池3入口连通;所述隔油沉淀池3的含油废水出口通过气浮过滤设备4连通砂滤罐5入口,所述隔油衬垫尺3的不含有废水出口直接连通砂滤罐5入口;所述砂滤罐5出口与活性炭过滤罐6入口连通;活性炭过滤罐6出口与回用水池7连通。整套系统设备的利用可以有效的对隧道排放的废水进行净化处理,避免施工过程中的污水排放对附近水源的污染。 A kind of tunnel sewage advanced treatment system as shown in Figure 1, the grit chamber 1 of this system is provided with the tunnel sewage inlet, and the grit chamber 1 outlet communicates with the oil separation sedimentation tank 3 inlets via the dosing tank 2; The oily wastewater outlet of the oil sedimentation tank 3 is connected to the sand filter tank 5 inlet through the air flotation filter equipment 4, and the waste water outlet of the oil-separating liner 3 is directly connected to the sand filter tank 5 inlet; the sand filter tank 5 outlet is connected to the sand filter tank 5 inlet. The inlet of the activated carbon filter tank 6 is communicated; the outlet of the activated carbon filter tank 6 is communicated with the reuse pool 7 . The use of the whole set of system equipment can effectively purify the wastewater discharged from the tunnel, and avoid the pollution of nearby water sources caused by the sewage discharge during the construction process.

隧道施工中所产生的污水污染物主要有以下几方面: Sewage pollutants generated during tunnel construction mainly include the following aspects:

固体悬浮颗粒物SS:部分隧道采用钻爆法开挖,隧道污水水质中主要为固体悬浮颗粒物SS含量过大。洞身段主要为褐红色、棕红色泥岩及呈青色灰色、红褐色砂岩、页岩和砾岩组成,在采用机具钻眼及爆破过程中产生微小颗粒物及粉尘,与隧道出水混合,且经过施工机械的碾压,形成高浓度悬浮物污水, 设计过程中污水悬浮物浓度按1600mg/L,实际施工中实测悬浮物浓度在2200~2800mg/L,因此设计中主要考虑采用混凝沉淀的方法来去除这部分污染物; Solid suspended particles SS: Some tunnels are excavated by drill and blast method, and the water quality of the tunnel sewage is mainly due to the excessive content of solid suspended particles SS. The body of the tunnel is mainly composed of maroon, brownish red mudstone and cyan gray, reddish brown sandstone, shale and conglomerate. During the drilling and blasting process of machinery and tools, tiny particles and dust are produced, which are mixed with the tunnel water and passed through the construction machinery. In the design process, the concentration of suspended solids in sewage is 1600mg/L, and the actual concentration of suspended solids in actual construction is 2200-2800mg/L. Therefore, the method of coagulation and sedimentation is mainly considered in the design to remove This part of the pollutant;

油污:另一项污水中含量较高的为油污,主要来源于施工机械以及突发的设备漏油等情况,实际油类污染物的浓度在5~10mg/L,因此设计中采用一体化气浮过滤设备去除少量的含油污水。 Oil pollution: Another item with a relatively high content in sewage is oil pollution, which mainly comes from construction machinery and sudden equipment oil leakage. The actual concentration of oil pollutants is 5-10mg/L, so integrated gas is used in the design Float filtration equipment removes small amounts of oily sewage.

Ph:由于隧道开挖采用钻爆法施工,乳化炸药的主要成分为硝酸铵,溶于水后会影响水质的酸碱性,另外混凝土施工也导致水质酸碱性的变化,通过水质检测报告检测到污水水质Ph值一般为9~10。因此在设计处理中还应考虑对污水水质的Ph值进行调节。 Ph: Since the tunnel excavation is constructed by drilling and blasting method, the main component of the emulsion explosive is ammonium nitrate, which will affect the acidity and alkalinity of the water quality after being dissolved in water. In addition, the concrete construction will also lead to changes in the acidity and alkalinity of the water quality, which can be detected by the water quality test report The Ph value of sewage water quality is generally 9-10. Therefore, the adjustment of the Ph value of the sewage water quality should also be considered in the design of the treatment.

本实用新型针对上述污染物才有多段分级的处理方式,利用不用的处理环节分别净化对应的污染物质。 The utility model has a multi-stage classification treatment method for the above-mentioned pollutants, and uses unused treatment links to purify corresponding pollutants respectively.

沉砂池1采用平流式沉砂池,沉砂池1分为两格,主要功能是去除较大无机颗粒物。 The grit chamber 1 adopts an advection type grit chamber, and the grit chamber 1 is divided into two compartments, and its main function is to remove larger inorganic particles.

隔油沉淀池3还设有油出口,油出口外接集油桶8。隔油沉淀池的主要功能是用于去除隧道施工污水中的泥沙沉积物、较大颗粒的机械钻爆产物等,在隔油集泥区进行油水分离等。 The oil separation sedimentation tank 3 is also provided with an oil outlet, and the oil outlet is externally connected to the oil collecting drum 8 . The main function of the oil-separating sedimentation tank is to remove the sediment and larger particles of mechanical drilling and blasting products in the tunnel construction sewage, and to separate oil and water in the oil-separating mud collection area.

气浮过滤设备4主要功能是设在混凝沉淀之后,主要去除污水中的小颗粒油污及细小悬浮物,结合污水中污染物质的主要性能指标,对隔油工艺和气浮工艺配以混凝剂投加,混凝剂选用聚合氯化铝(PAC),对污水处理效果有明显改善。 The main function of the air flotation filter equipment 4 is to remove small particles of oil and fine suspended matter in the sewage after the coagulation and sedimentation. Combined with the main performance indicators of the pollutants in the sewage, the oil separation process and the air flotation process are equipped with a coagulant Dosing, polyaluminum chloride (PAC) is selected as the coagulant, which can significantly improve the sewage treatment effect.

砂滤罐5和活性炭过滤罐6的主要功能是污水深度处理及净化,为了达到一定的回用水标准使污水作为水资源回用于生产或生活的进一步水处理过程。 The main functions of the sand filter tank 5 and the activated carbon filter tank 6 are the advanced treatment and purification of sewage, in order to achieve a certain reuse water standard so that the sewage can be reused as a water resource for further water treatment in production or life.

沉砂池1、隔油沉淀池3的出水口高度低于入水口高度;所述砂滤罐5的出水口高度高于入水口。本实用新型的整体系统采用一字型布置,利用天然地形,对各构筑物标高进行合理设计,尽量减少污水中间的动力提升,使各构筑物在重力流的水力条件下运行。 The height of the water outlet of the grit chamber 1 and the oil separation sedimentation tank 3 is lower than that of the water inlet; the height of the water outlet of the sand filter tank 5 is higher than that of the water inlet. The overall system of the utility model adopts a straight layout, utilizes the natural terrain, rationally designs the elevation of each structure, minimizes the power lift in the middle of the sewage, and makes each structure operate under the hydraulic condition of gravity flow.

加药池2和隔油沉淀池3的含油废水入口分别外接有加药机9。加药机9采用一体化自动加药装置,加药泵采用三用一备,交替使用,保证连续混凝剂制备投加,采用两个储药桶,药筒容积为2m3。混凝剂采用PAC,助凝剂采用PAM,加药量及浓度应根据处理水量和悬浮物浓度,现场试验确定。 The oily wastewater inlets of the dosing tank 2 and the oil-separating sedimentation tank 3 are respectively connected with a dosing machine 9 . The dosing machine 9 adopts an integrated automatic dosing device, and the dosing pump adopts three functions and one standby, which are used alternately to ensure continuous coagulant preparation and dosing. Two medicine storage barrels are used, and the volume of the medicine cartridge is 2m 3 . PAC is used as the coagulant, and PAM is used as the coagulant aid. The dosage and concentration should be determined according to the amount of treated water and the concentration of suspended solids, and field tests.

应当说明的是,本实用新型的上述具体实施方式仅用于示例性说明或解释本实用新型的原理,而不构成对本实用新型的限制。因此,在不偏离本实用新型的精神和范围的情况下所做的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。此外,本实用新型所附权利要求旨在涵盖落入所附 权利要求范围和边界或者这种范围和边界的等同形式内的全部变化和修改。 It should be noted that the above specific implementations of the present utility model are only used to illustrate or explain the principle of the present utility model, but not to limit the present utility model. Therefore, any modification, equivalent replacement, improvement, etc. made without departing from the spirit and scope of the present utility model shall be included in the protection scope of the present utility model. Furthermore, the appended claims are intended to cover all changes and modifications that come within the scope and boundaries of the appended claims, or equivalents of such scope and boundaries.

Claims (5)

1.一种隧道污水深度处理系统,其特征是:该系统的沉砂池(1)处设有隧道污水入口,沉砂池(1)出口经由加药池(2)与隔油沉淀池(3)入口连通;所述隔油沉淀池(3)的含油废水出口通过气浮过滤设备(4)连通砂滤罐(5)入口,所述隔油衬垫尺(3)的不含有废水出口直接连通砂滤罐(5)入口;所述砂滤罐(5)出口与活性炭过滤罐(6)入口连通;活性炭过滤罐(6)出口与回用水池(7)连通。1. A tunnel sewage advanced treatment system is characterized in that: the grit chamber (1) of the system is provided with a tunnel sewage inlet, and the grit chamber (1) outlet passes through the dosing tank (2) and the oil separation sedimentation tank ( 3) The inlet is connected; the oily wastewater outlet of the oil-separating sedimentation tank (3) is connected to the inlet of the sand filter tank (5) through the air flotation filter equipment (4), and the outlet of the oil-separating liner (3) does not contain wastewater The inlet of the sand filter tank (5) is directly connected; the outlet of the sand filter tank (5) is communicated with the inlet of the activated carbon filter tank (6); the outlet of the activated carbon filter tank (6) is communicated with the reuse water pool (7). 2.根据权利要求1所述的隧道污水深度处理系统,其特征是:所述沉砂池(1)采用平流式沉砂池,沉砂池(1)分为两格。2. The tunnel sewage advanced treatment system according to claim 1, characterized in that: the grit chamber (1) adopts an advection type grit chamber, and the grit chamber (1) is divided into two compartments. 3.根据权利要求1所述的隧道污水深度处理系统,其特征是:所述隔油沉淀池(3)还设有油出口,油出口外接集油桶(8)。3. The tunnel sewage advanced treatment system according to claim 1, characterized in that: the oil separation sedimentation tank (3) is also provided with an oil outlet, and the oil outlet is externally connected to an oil collecting barrel (8). 4.根据权利要求1所述的隧道污水深度处理系统,其特征是:所述沉砂池(1)、隔油沉淀池(3)的出水口高度低于入水口高度;所述砂滤罐(5)的出水口高度高于入水口。4. The tunnel sewage advanced treatment system according to claim 1, characterized in that: the water outlet height of the grit chamber (1) and the oil separation sedimentation tank (3) is lower than the water inlet height; the sand filter tank (5) The water outlet height is higher than the water inlet. 5.根据权利要求1所述的隧道污水深度处理系统,其特征是:所述加药池(2)和隔油沉淀池(3)的含油废水入口分别外接有加药机(9)。5. The tunnel sewage advanced treatment system according to claim 1, characterized in that: the entrances of the dosing tank (2) and the oily waste water of the oil-separating sedimentation tank (3) are respectively connected with dosing machines (9).
CN201520279001.4U 2015-04-30 2015-04-30 Constructing tunnel advanced sewage treatment system Expired - Lifetime CN204714625U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520279001.4U CN204714625U (en) 2015-04-30 2015-04-30 Constructing tunnel advanced sewage treatment system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520279001.4U CN204714625U (en) 2015-04-30 2015-04-30 Constructing tunnel advanced sewage treatment system

Publications (1)

Publication Number Publication Date
CN204714625U true CN204714625U (en) 2015-10-21

Family

ID=54313634

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520279001.4U Expired - Lifetime CN204714625U (en) 2015-04-30 2015-04-30 Constructing tunnel advanced sewage treatment system

Country Status (1)

Country Link
CN (1) CN204714625U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107686180A (en) * 2017-09-22 2018-02-13 江苏上塍环保科技有限公司 The sewerage integrated pre-processing device in tunnel and preprocess method
CN108218027A (en) * 2017-12-27 2018-06-29 北京泰豪智能工程有限公司 A kind of sampling of water quality cleaning equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107686180A (en) * 2017-09-22 2018-02-13 江苏上塍环保科技有限公司 The sewerage integrated pre-processing device in tunnel and preprocess method
CN108218027A (en) * 2017-12-27 2018-06-29 北京泰豪智能工程有限公司 A kind of sampling of water quality cleaning equipment

Similar Documents

Publication Publication Date Title
CN109761395B (en) A fully mechanized face mine water resource utilization system and using method
CN101363311B (en) Technological process for comprehensive treatment for waste drilling fluid following drill for oil-gas field
CN104163536A (en) Magnetic coagulation mine water underground purification technology
CN102491557B (en) Underground mine water treatment method
CN204097269U (en) Magnetic force coagulation and separating treatment pit water device
Gunson Quantifying, reducing and improving mine water use
CN205773768U (en) A kind of oil field wastewater treatment system
CN104724876A (en) Coal mine underground water processing method
CN105439363A (en) Magnetic coagulation and separation purification technology for mine water
CN104747107B (en) Well drilling waste mud integral treatment method
CN106219701A (en) A kind of dense medium speed is heavy and sludge filtration water treatment system and processing method
CN104276638B (en) A kind of constructing tunnel drainage processing method and treatment unit thereof
CN204714625U (en) Constructing tunnel advanced sewage treatment system
CN104609635B (en) A kind of movable type well-flushing Waste Water Treatment
CN104692555B (en) Method and device for recovery, treatment and reuse of fracturing flowback fluid
CN211311154U (en) Mine water advanced treatment device
Tyulenev et al. Coal producers waste water purification
CN202390268U (en) In-situ reuse treatment system for downhole directional drilling machine medium circulation water
CN205575826U (en) Anti - flowing back processing system of sled multi -functional fracturing of dress formula
CN204022596U (en) A kind of oil-gas field fracturing waste liquor effective, harmless treatment unit
CN105253970A (en) Enhanced separation method for treating wastewater with high-content suspended solids
CN205840846U (en) Drilling mud does not land processing means
CN104692550B (en) A kind of mine water underground processes technique and device
Horner et al. Mobile Clarification for Re-Use of Unconventional Oil and Gas Produced Water to Reduce Costs and Minimize Environmental Footprint
CN115636453A (en) Underground reservoir mine wastewater circulating self-treatment method suitable for lump coal washing

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20151021