CN208218548U - Muddy mine water Dynamic Membrane cleaning equipment - Google Patents
Muddy mine water Dynamic Membrane cleaning equipment Download PDFInfo
- Publication number
- CN208218548U CN208218548U CN201820105499.6U CN201820105499U CN208218548U CN 208218548 U CN208218548 U CN 208218548U CN 201820105499 U CN201820105499 U CN 201820105499U CN 208218548 U CN208218548 U CN 208218548U
- Authority
- CN
- China
- Prior art keywords
- purifier
- mine water
- water
- cleaning equipment
- dynamic membrane
- 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.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本实用新型涉及矿井净化的技术领域,尤其涉及一种浑浊矿井水动态膜净化设备,该设备适用于悬浮物SS浓度≥100mg/L的浑浊矿井水资源化预处理。The utility model relates to the technical field of mine purification, in particular to a dynamic membrane purification device for turbid mine water, which is suitable for resource pretreatment of turbid mine water with suspended matter SS concentration ≥ 100mg/L.
背景技术Background technique
煤炭开采时会破坏地下水资源,同时激化了该地区的供水紧张问题。目前矿井水一般工艺流程多为独立的调节池、沉淀池、絮凝池以及过滤池组成,由于矿井水的流量和水质不稳定会给这些传统工艺系统带来困难,使其无法稳定高效运行。因此,目前对于新型设备工艺的探索尤为重要,膜技术在水处理领域有广阔的前景,其中超滤技术在矿井水中多放置在混凝沉淀多孔过滤后端提高出水水质,前置超滤膜将会面临严重膜污染问题。在污水处理领域,为缓解膜污染问题,同时提高膜渗透通量,有关学者提出动态膜技术以期解决这一难题, 动态膜技术核心思想是有效利用动态膜污染,缓解膜污染和出水水质不能兼得的矛盾。另外,浑浊矿井水现有的一体净化装置出水水质也不稳定,处理效果有待提高。Coal mining destroys groundwater resources and exacerbates water shortages in the region. At present, the general process of mine water is mostly composed of independent regulating tanks, sedimentation tanks, flocculation tanks and filter tanks. Due to the unstable flow and quality of mine water, these traditional process systems will bring difficulties, making them unable to operate stably and efficiently. Therefore, the exploration of new equipment and technology is particularly important at present. Membrane technology has broad prospects in the field of water treatment. Among them, ultrafiltration technology is often placed at the back end of coagulation sedimentation porous filtration in mine water to improve the quality of effluent water. The pre-ultrafiltration membrane will There will be serious membrane fouling problems. In the field of sewage treatment, in order to alleviate the problem of membrane fouling and increase the permeation flux of the membrane, some scholars proposed dynamic membrane technology to solve this problem. got the contradiction. In addition, the effluent quality of the existing integrated purification device for turbid mine water is also unstable, and the treatment effect needs to be improved.
为此,本实用新型的设计者有鉴于上述缺陷,通过潜心研究和设计,综合长期多年从事相关产业的经验和成果,研究设计出一种浑浊矿井水动态膜净化设备,以克服上述缺陷。For this reason, in view of the above-mentioned defects, the designer of the utility model researches and designs a kind of turbid mine water dynamic membrane purification equipment to overcome the above-mentioned defects by concentrating on research and design, and integrating experience and achievements in related industries for many years.
实用新型内容Utility model content
本实用新型的目的在于提供一种浑浊矿井水动态膜净化设备,其结构简单,操作方便,克服了膜污染问题,同时将膜分离浓缩优点集中到一体化处理工艺中,使得混凝、沉淀、膜分离出水三种功能同步实现,解决了传统的矿井水处理工艺需要大量絮凝剂、出水水质不稳定以及占地面积大等缺点。The purpose of this utility model is to provide a dynamic membrane purification equipment for turbid mine water, which has a simple structure and is easy to operate, overcomes the problem of membrane pollution, and at the same time integrates the advantages of membrane separation and concentration into an integrated treatment process, so that coagulation, precipitation, The three functions of membrane separation and effluent are realized simultaneously, which solves the shortcomings of the traditional mine water treatment process that requires a large amount of flocculants, unstable effluent quality, and large floor space.
为解决上述问题,本实用新型公开了一种浑浊矿井水动态膜净化设备,包含混合反应池和净水装置,其特征在于:In order to solve the above problems, the utility model discloses a dynamic membrane purification equipment for turbid mine water, which includes a mixing reaction tank and a water purification device, and is characterized in that:
所述净水装置为上开口的中空筒体,其下端为锥形底且底端设有排泥口,所述混合反应池内为中空状以供高浓度絮凝剂容置和浑浊矿井水进入,所述混合反应池连通至所述净水装置内的下部以将混合反应后的流体通入净水装置,所述净水装置内的上部设有聚酯纤维编织管组件,所述净水装置内的中部设有横置的曝气管,所述曝气管连接至净水装置外部的空气压缩机从而通过空气压缩机利用曝气管不断曝气清扫聚酯纤维编织管组件的表面。The water purification device is a hollow cylinder with an upper opening, the lower end of which is a conical bottom and a mud discharge port is provided at the bottom, and the inside of the mixing reaction tank is hollow for the accommodation of high-concentration flocculants and the entry of turbid mine water. The mixing reaction tank is connected to the lower part of the water purification device to pass the fluid after the mixed reaction into the water purification device. The upper part of the water purification device is provided with a polyester fiber braided pipe assembly, and the water purification device A horizontal aeration tube is provided in the middle of the interior, and the aeration tube is connected to an air compressor outside the water purification device so that the air compressor uses the aeration tube to continuously aerate and clean the surface of the polyester fiber braided tube assembly.
其中:还设有第一抽水泵和第二抽水泵,所述第一抽水泵连通至混合反应池以将浑浊矿井水加入混合反应池,所述第二抽水泵连通至聚酯纤维编织管组件从而将通过聚酯纤维编织管组件后的液体抽出。Wherein: a first water pump and a second water pump are also provided, the first water pump is connected to the mixing reaction tank to add turbid mine water to the mixing reaction tank, and the second water pump is connected to the polyester fiber braided pipe assembly Thereby the liquid after passing through the polyester fiber braided tube assembly is drawn out.
其中:所述净水装置内的下部设有挡板。Wherein: the lower part of the water purification device is provided with a baffle.
其中:所述挡板为与净水装置底部相反的弯折状以对进入的液体进行减速和导向。Wherein: the baffle is in a bent shape opposite to the bottom of the water purification device to decelerate and guide the incoming liquid.
其中:所述混合反应池的顶端设有加药口,上部外缘设有进水口,下部外缘设有出水口,所述出水口连通至净水装置内。Wherein: the top of the mixing reaction tank is provided with a dosing port, the outer edge of the upper part is provided with a water inlet, and the outer edge of the lower part is provided with a water outlet, and the water outlet is connected to the water purification device.
其中:所述混合反应池还设有搅拌机。Wherein: the mixing reaction tank is also provided with a stirrer.
其中:所述搅拌机包含搅拌电机和搅拌轴,所述搅拌轴伸入混合反应池内且周缘间隔设有多个搅拌叶片。Wherein: the stirrer comprises a stirring motor and a stirring shaft, the stirring shaft protrudes into the mixing reaction tank and a plurality of stirring blades are arranged at intervals around the periphery.
其中:所述聚酯纤维编织管组件包含积水管道、多根中空聚酯纤维管以及密封端,所述多根中空聚酯纤维管竖向间隔设置于积水管道及密封端之间从而液体通过多根中空聚酯纤维管后才能进入积水管道。Wherein: the polyester fiber braided pipe assembly includes a water accumulation pipe, a plurality of hollow polyester fiber pipes and a sealing end, and the plurality of hollow polyester fiber pipes are vertically spaced between the water accumulation pipe and the sealing end so that the liquid After passing through multiple hollow polyester fiber pipes, it can enter the water accumulation pipe.
其中:所述中空聚酯纤维管内径1-1.2mm,外径1.8-2mm。Wherein: the inner diameter of the hollow polyester fiber tube is 1-1.2mm, and the outer diameter is 1.8-2mm.
其中:所述净水装置内还设有液面计,所述液面计设置于聚酯纤维编织管组件的上方。Wherein: the water purification device is also provided with a liquid level gauge, and the liquid level gauge is arranged above the polyester fiber braided pipe assembly.
通过上述结构可知,本实用新型的浑浊矿井水动态膜净化设备具有如下效果:It can be seen from the above structure that the turbid mine water dynamic membrane purification equipment of the present utility model has the following effects:
1、结构简单,操作方便,净化效果好,能解决出水水质和膜污染之间的平衡问题;1. The structure is simple, the operation is convenient, the purification effect is good, and it can solve the balance problem between the effluent water quality and the membrane pollution;
2、使得浑浊矿井水出水水质稳定,减少絮凝剂投加量,减少占地面积,提高使用范围。2. Make the turbid mine water effluent quality stable, reduce the amount of flocculant dosage, reduce the occupied area, and increase the scope of use.
3、克服了膜污染问题,同时将膜分离浓缩优点集中到一体化处理工艺中,使得混凝、沉淀、膜分离出水三种功能同步实现,解决了传统的矿井水处理工艺需要大量絮凝剂、出水水质不稳定以及占地面积大等缺点。3. Overcome the problem of membrane fouling, and at the same time integrate the advantages of membrane separation and concentration into the integrated treatment process, so that the three functions of coagulation, sedimentation and membrane separation can be realized simultaneously, which solves the need for a large amount of flocculant, Disadvantages such as unstable effluent quality and large floor space.
本实用新型的详细内容可通过后述的说明及所附图而得到。The details of the present invention can be obtained from the following description and the accompanying drawings.
附图说明Description of drawings
图1显示了本实用新型的浑浊矿井水动态膜净化设备的结构示意图。Fig. 1 has shown the structure schematic diagram of the turbid mine water dynamic membrane purification equipment of the present invention.
图2显示了本实用新型中混合反应池的结构示意图。Fig. 2 has shown the structure diagram of mixing reaction pool in the utility model.
图3显示了本实用新型中聚酯纤维编织管组件的结构示意图。Fig. 3 shows a schematic structural view of the polyester fiber braided tube assembly in the present invention.
附图标记:Reference signs:
1、第一抽水泵;2、混合反应池;201、加药口;202、进水口; 203、搅拌机;204、出水口;3、挡板;4、空气压缩机;5、曝气管; 6、组件支架;7、聚酯纤维编织管组件;701、积水管道;702、中空聚酯纤维管;703、密封端;8、液面计;9、压力表;10、第二抽水泵;11、第一阀门;12、第二阀门;13、排泥口。1. The first water pump; 2. Mixing reaction tank; 201. Dosing port; 202. Water inlet; 203. Mixer; 204. Water outlet; 3. Baffle; 4. Air compressor; 5. Aeration pipe; 6. Component support; 7. Polyester fiber braided pipe assembly; 701. Water accumulation pipe; 702. Hollow polyester fiber pipe; 703. Sealed end; 8. Liquid level gauge; 9. Pressure gauge; 10. Second water pump ; 11, the first valve; 12, the second valve; 13, the mud outlet.
具体实施方式Detailed ways
参见图1,显示了本实用新型的浑浊矿井水动态膜净化设备。Referring to Fig. 1, it shows the turbid mine water dynamic membrane purification equipment of the present invention.
该浑浊矿井水动态膜净化设备包含混合反应池2和净水装置,所述净水装置为上开口的中空筒体,其下端为锥形底且底端设有排泥口 13,所述混合反应池2内为中空状,以供高浓度絮凝剂容置和浑浊矿井水进入,所述混合反应池2连通至所述净水装置内的下部,以将混合反应后的流体通入净水装置,所述净水装置内的上部设有聚酯纤维编织管组件7,所述净水装置内的中部设有横置的曝气管5,所述曝气管5连接至净水装置外部的空气压缩机4,从而通过开启空气压缩机4利用曝气管5不断曝气清扫聚酯纤维编织管组件7的表面,其中,还设有第一抽水泵1和第二抽水泵10,所述第一抽水泵1连通至混合反应池2以将浑浊矿井水加入混合反应池2,所述第二抽水泵10 连通至聚酯纤维编织管组件7,从而将通过聚酯纤维编织管组件7后的液体抽出。This turbid mine water dynamic membrane purification equipment comprises a mixing reaction tank 2 and a water purification device. The water purification device is a hollow cylinder with an upper opening. The inside of the reaction tank 2 is hollow for the accommodation of high-concentration flocculants and the entry of turbid mine water. The mixing reaction tank 2 is connected to the lower part of the water purification device to pass the mixed reaction fluid into the purified water device, the upper part of the water purification device is provided with a polyester fiber braided pipe assembly 7, and the middle part of the water purification device is provided with a horizontal aeration pipe 5, and the aeration pipe 5 is connected to the outside of the water purification device The air compressor 4, thereby by opening the air compressor 4 and utilizing the aeration pipe 5 to constantly aerate and clean the surface of the polyester fiber braided pipe assembly 7, wherein a first water pump 1 and a second water pump 10 are also provided, so The first water pump 1 is connected to the mixing reaction tank 2 to add turbid mine water to the mixing reaction tank 2, and the second water pump 10 is connected to the polyester fiber braided pipe assembly 7, so that the water passing through the polyester fiber braided pipe assembly 7 After the liquid is drawn out.
其中,所述净水装置内的下部设有挡板3,如图1所示,所述挡板3可为与净水装置底部相反的弯折状,以对进入的液体进行减速和导向。Wherein, the lower part of the water purification device is provided with a baffle 3, as shown in Figure 1, the baffle 3 can be bent opposite to the bottom of the water purification device to decelerate and guide the incoming liquid.
其中,参见图2,所述混合反应池2的顶端设有加药口201,上部外缘设有进水口202,下部外缘设有出水口204,所述加药口201 供高浓度絮凝剂进行放入,所述进水口202连通至第一抽水泵1,所述出水口204连通至净水装置内。Wherein, referring to Fig. 2, the top of the mixing reaction tank 2 is provided with a dosing port 201, the upper outer edge is provided with a water inlet 202, and the lower outer edge is provided with a water outlet 204, and the described dosing port 201 is provided with a high-concentration flocculant. Putting in, the water inlet 202 is connected to the first water pump 1, and the water outlet 204 is connected to the water purification device.
其中,所述混合反应池还设有搅拌机203,所述搅拌机203可包含搅拌电机和搅拌轴,所述搅拌轴伸入混合反应池2内且周缘间隔设有多个搅拌叶片。Wherein, the mixing reaction tank is further provided with a stirrer 203, and the stirrer 203 may include a stirring motor and a stirring shaft, and the stirring shaft extends into the mixing reaction tank 2 and a plurality of stirring blades are arranged at intervals around the periphery.
其中,参见图1,所述聚酯纤维编织管组件7通过组件支架6安装于净水装置的内缘,参见图3,所述聚酯纤维编织管组件7包含积水管道701、多根中空聚酯纤维管702以及密封端703,所述多根中空聚酯纤维管702竖向间隔设置于积水管道701及密封端703之间,液体通过多根中空聚酯纤维管702后才能进入积水管道701,所述积水管道701连通至第二水泵10以进行净化后的抽取。Wherein, referring to Fig. 1, the polyester fiber braided pipe assembly 7 is installed on the inner edge of the water purification device through the assembly bracket 6, referring to Fig. 3, the polyester fiber braided pipe assembly 7 includes a water accumulation pipe 701, a plurality of hollow Polyester fiber tube 702 and sealing end 703, the plurality of hollow polyester fiber tubes 702 are vertically spaced between the accumulation water pipe 701 and the sealing end 703, the liquid can only enter the accumulation area after passing through the plurality of hollow polyester fiber tubes 702 The water pipe 701 is connected to the second water pump 10 for extraction after purification.
其中,所述净水装置内还设有液面计8,所述液面计8设置于聚酯纤维编织管组件7的上方。Wherein, a liquid level gauge 8 is also provided in the water purification device, and the liquid level gauge 8 is arranged above the polyester fiber braided pipe assembly 7 .
所述聚酯纤维编织管组件7和第二抽水泵10之间设有压力表9,所述第二抽水泵10的出口并联有第一阀门11和第二阀门12,所述第二阀门12的出口连通至所述净水装置内的下部。A pressure gauge 9 is provided between the polyester fiber braided pipe assembly 7 and the second water pump 10, and the outlet of the second water pump 10 is connected in parallel with a first valve 11 and a second valve 12, and the second valve 12 The outlet of the outlet is connected to the lower part of the water purification device.
其中,还设有控制装置,所述控制装置包含一PLC,所述PLC连接至第一抽水泵1、第二抽水泵10、空气压缩机4、液面计8和压力表9,以实现整个自动控制过程。Wherein, a control device is also provided, and the control device includes a PLC, and the PLC is connected to the first water pump 1, the second water pump 10, the air compressor 4, the liquid level gauge 8 and the pressure gauge 9, to realize the whole Automatically control the process.
进一步,所述中空聚酯纤维管702为聚酯PET纤维或PET/PBT混织所得,其内径1-1.2mm,外径1.8-2mm。Further, the hollow polyester fiber tube 702 is obtained by weaving polyester PET fiber or PET/PBT, with an inner diameter of 1-1.2 mm and an outer diameter of 1.8-2 mm.
进一步,所述曝气管5固定在聚酯纤维编织管组件7正下方,气水比为5:1-50:1,一方面为了清洗组件,另一方面控制气水比,较少对颗粒絮凝物的破坏,使得絮凝剂充分混合。Further, the aeration pipe 5 is fixed directly below the polyester fiber braided pipe assembly 7, and the air-water ratio is 5:1-50:1. On the one hand, in order to clean the assembly, on the other hand, the air-water ratio is controlled to reduce the impact on particles. The destruction of flocs makes the flocculants fully mixed.
进一步,所述的抽水泵10间歇运行特征在于:间歇出水的抽停时间为Amin/Bmin,A:10-30,B:1-5,水力停留时间设定为0.5-5h。Further, the intermittent operation of the suction pump 10 is characterized in that: the pumping stop time of the intermittent water outlet is Amin/Bmin, A: 10-30, B: 1-5, and the hydraulic retention time is set to 0.5-5h.
本实用新型的工作原理和工作过程如下,1)动态膜涂覆阶段打开抽水泵1,浑浊矿井水经过混合反应池2投加高浓度絮凝剂,从挡板3正下方进入净水设备,当水面超过聚酯纤维编织管组件10-15cm 时停止进水,然后打开抽水泵10和阀门12,从出水管排水并经过回流管回流到设备内,随着设备的不断运行,聚酯纤维编织管组件7内表面不断聚集煤泥,回流运行5-10min,由于聚酯纤维编织管组件7 内表面煤泥的阻塞和拦截作用,出水水质不断改善,压力表9显示的跨膜压差(TMP)不断增加。2)净水阶段打开抽水泵10和阀门11,同时减少浑浊矿井水中絮凝剂投加量,通过液面计8控制抽水泵1的启停,使得液面水位恒定,间隙运行抽水泵10,当TMP跨膜压差(TMP) 达到10-12KPa时,开启空气压缩机4不断曝气清扫聚酯纤维编织管组件7表面,使得跨膜压差(TMP)逐渐下降,当跨膜压差(TMP) 下降到3-6KPa时停止曝气,曝气停止后,跨膜压差(TMP)又会不断上升,如此不断间歇曝气保证跨膜压差(TMP)处于设定上下限之间,曝气清洗过程由自动控制系统(PLC)控制,出水过程中定期从排泥口13排出煤泥。The working principle and working process of the present utility model are as follows, 1) the dynamic film coating stage opens the water pump 1, and the turbid mine water is added with a high-concentration flocculant through the mixing reaction tank 2, and enters the water purification equipment from directly below the baffle plate 3, when Stop water intake when the water surface exceeds the polyester fiber braided pipe assembly by 10-15cm, then turn on the water pump 10 and valve 12, drain water from the outlet pipe and return it to the equipment through the return pipe. With the continuous operation of the equipment, the polyester fiber braided pipe Coal slime is continuously accumulated on the inner surface of component 7, and the backflow operation is 5-10 minutes. Due to the blocking and interception of the coal slime on the inner surface of polyester fiber braided tube component 7, the water quality of the effluent is continuously improved, and the transmembrane pressure difference (TMP) Increasing. 2) In the water purification stage, the water pump 10 and the valve 11 are turned on, and at the same time, the dosage of flocculant in the turbid mine water is reduced, and the start and stop of the water pump 1 is controlled by the liquid level gauge 8, so that the water level of the liquid surface is constant, and the water pump 10 is operated in intervals. When the TMP transmembrane pressure difference (TMP) reaches 10-12KPa, open the air compressor 4 to continuously aerate and clean the surface of the polyester fiber braided pipe assembly 7, so that the transmembrane pressure difference (TMP) gradually decreases, and when the transmembrane pressure difference (TMP ) stop aeration when it drops to 3-6KPa, after the aeration stops, the transmembrane pressure difference (TMP) will continue to rise, so continuous intermittent aeration ensures that the transmembrane pressure difference (TMP) is between the set upper and lower limits, and the aeration The gas cleaning process is controlled by an automatic control system (PLC), and the coal slime is regularly discharged from the mud discharge port 13 during the water discharge process.
进一步,所述浑浊矿井水的悬浮物SS≥100mg/L,絮凝剂为PAC (聚合氯化铝)、三氯化铁(FC)、聚合硫酸铁(PFS)和PAM(聚丙烯胺)中的一种或几种混合物,动态膜涂覆阶段,絮凝剂浓度为 50mg/L-1000mg/L,进水阶段,絮凝剂浓度为0mg/L-20mg/L。Further, the suspended matter SS of the turbid mine water is more than or equal to 100mg/L, and the flocculant is PAC (polyaluminum chloride), ferric chloride (FC), polyferric sulfate (PFS) and PAM (polypropylene amine). One or several mixtures, the flocculant concentration is 50mg/L-1000mg/L in the dynamic membrane coating stage, and the flocculant concentration is 0mg/L-20mg/L in the water inlet stage.
所述浑浊矿井水动态膜净化设备的具体过程包括The specific process of the turbid mine water dynamic membrane purification equipment includes
1)动态膜涂覆阶段,浑浊矿井水经过混合反应池投加高浓度絮凝剂,然后从挡板下方进入净水装置,通过不断循环回流矿井水使得聚酯纤维编织管组件内表面不断聚集煤泥,回流5-10min后,由于组件内表面煤泥的阻塞和拦截作用,出水水质不断改善,跨膜压差(TMP)不断增加。2)随后进入净水阶段,减少浑浊矿井水中絮凝剂投加量,间歇运行出水,当TMP跨膜压差(TMP)达到10-12KPa 时,开启曝气装置使得跨膜压差(TMP)逐渐下降,当跨膜压差(TMP) 下降到3-6KPa时停止曝气,曝气启停由自动控制系统(PLC)控制,使得跨膜压差(TMP)始终处于设定上下限之间,出水过程中定期排出煤泥。1) In the dynamic membrane coating stage, the turbid mine water is added with high-concentration flocculant through the mixing reaction tank, and then enters the water purification device from the bottom of the baffle, and the coal is continuously accumulated on the inner surface of the polyester fiber braided pipe assembly through continuous circulation of mine water. After reflux for 5-10 minutes, due to the blockage and interception of the slime on the inner surface of the module, the quality of the effluent water continues to improve, and the transmembrane pressure difference (TMP) continues to increase. 2) Then enter the water purification stage, reduce the dosage of flocculant in turbid mine water, run intermittently, and when the TMP transmembrane pressure (TMP) reaches 10-12KPa, turn on the aeration device to make the transmembrane pressure (TMP) gradually When the transmembrane pressure difference (TMP) drops to 3-6KPa, the aeration is stopped, and the start and stop of the aeration is controlled by the automatic control system (PLC), so that the transmembrane pressure difference (TMP) is always between the set upper and lower limits. The slime is regularly discharged during the water discharge process.
通过上述结构可知,本实用新型的浑浊矿井水动态膜净化设备具有如下优点:It can be seen from the above structure that the turbid mine water dynamic membrane purification equipment of the present invention has the following advantages:
1、结构简单,操作方便,净化效果好,能解决出水水质和膜污染之间的平衡问题;1. The structure is simple, the operation is convenient, the purification effect is good, and it can solve the balance problem between the effluent water quality and the membrane pollution;
2、使得浑浊矿井水出水水质稳定,减少絮凝剂投加量,减少占地面积,提高使用范围。2. Make the turbid mine water effluent quality stable, reduce the amount of flocculant dosage, reduce the occupied area, and increase the scope of use.
3、克服了膜污染问题,同时将膜分离浓缩优点集中到一体化处理工艺中,使得混凝、沉淀、膜分离出水三种功能同步实现,解决了传统的矿井水处理工艺需要大量絮凝剂、出水水质不稳定以及占地面积大等缺点。3. Overcome the problem of membrane fouling, and at the same time integrate the advantages of membrane separation and concentration into the integrated treatment process, so that the three functions of coagulation, sedimentation and membrane separation can be realized simultaneously, which solves the need for a large amount of flocculant, Disadvantages such as unstable effluent quality and large floor space.
显而易见的是,以上的描述和记载仅仅是举例而不是为了限制本实用新型的公开内容、应用或使用。虽然已经在实施例中描述过并且在附图中描述了实施例,但本实用新型不限制由附图示例和在实施例中描述的作为目前认为的最佳模式以实施本实用新型的教导的特定例子,本实用新型的范围将包括落入前面的说明书和所附的权利要求的任何实施例。Apparently, the above descriptions and records are only examples and not intended to limit the disclosure, application or use of the present utility model. Although the embodiment has been described in the embodiment and described in the accompanying drawings, the utility model is not limited by the examples of the accompanying drawings and described in the embodiment as the best mode currently considered to implement the teaching of the utility model Certain examples, the scope of the present invention shall include any embodiment falling within the foregoing description and appended claims.
Claims (10)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820105499.6U CN208218548U (en) | 2018-01-23 | 2018-01-23 | Muddy mine water Dynamic Membrane cleaning equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820105499.6U CN208218548U (en) | 2018-01-23 | 2018-01-23 | Muddy mine water Dynamic Membrane cleaning equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208218548U true CN208218548U (en) | 2018-12-11 |
Family
ID=64533676
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820105499.6U Active CN208218548U (en) | 2018-01-23 | 2018-01-23 | Muddy mine water Dynamic Membrane cleaning equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208218548U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117247186A (en) * | 2023-10-25 | 2023-12-19 | 陕西陕煤韩城矿业有限公司 | A zero-discharge treatment device and method for high-salinity mine water |
-
2018
- 2018-01-23 CN CN201820105499.6U patent/CN208218548U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117247186A (en) * | 2023-10-25 | 2023-12-19 | 陕西陕煤韩城矿业有限公司 | A zero-discharge treatment device and method for high-salinity mine water |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106745749B (en) | Aerobic-anoxic integrated AO membrane bioreactor | |
| CN104876360B (en) | Rainwater purification apparatus based on ceramic membrane | |
| CN111056632A (en) | Anaerobic external tubular ultrafiltration membrane bioreactor | |
| CN107459213A (en) | A kind of drum type brake integrated sewage treating apparatus | |
| CN202643421U (en) | External jet membrane bioreactor | |
| CN109293079B (en) | Low-energy-consumption aeration circulation clarification tank | |
| CN208218548U (en) | Muddy mine water Dynamic Membrane cleaning equipment | |
| CN203794724U (en) | Outer circulating type pressurized dissolved air flotation-film separation water treatment device | |
| CN201505512U (en) | A gas-water mixing cleaning device for submerged hollow fiber membrane modules | |
| CN100537448C (en) | Comb-like membrane-bioreactor having free end | |
| CN208802923U (en) | An urban domestic sewage treatment device | |
| CN102874965B (en) | System for recycling waste water containing oil and washing water | |
| CN206188491U (en) | Membrane bioreactor that sewage sludge integration was handled | |
| CN216106204U (en) | Side-arranged cross-flow aeration membrane bioreactor | |
| CN213771671U (en) | Vertical ultrafiltration purifier | |
| RU110368U1 (en) | WATER TREATMENT PLANT USING PRESSURE FLOTATION | |
| CN202139109U (en) | Membrane bioreactor | |
| CN209853875U (en) | Integrated water purifying device | |
| CN208485718U (en) | A kind of double purification sewage disposal devices | |
| CN223936381U (en) | Integrated device for wastewater treatment | |
| CN206384881U (en) | A kind of sludge condensation type air-floating apparatus | |
| CN206927727U (en) | A kind of sewage-treatment plant | |
| CN206289123U (en) | A kind of processing system for metro depot car-washing sewage | |
| CN220376470U (en) | Curtain type hollow fiber MBR membrane group device | |
| CN106430859B (en) | It takes up little area and aeration biological filter device and its technique that shock resistance is strong |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |