CN205241438U - Contain coal waste water electron flocculation facility - Google Patents
Contain coal waste water electron flocculation facility Download PDFInfo
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- CN205241438U CN205241438U CN201521007333.3U CN201521007333U CN205241438U CN 205241438 U CN205241438 U CN 205241438U CN 201521007333 U CN201521007333 U CN 201521007333U CN 205241438 U CN205241438 U CN 205241438U
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Abstract
本实用新型公开了一种含煤废水电子絮凝设施,包括按工序步骤布置的煤水沉淀池、电子絮凝器、沉降反应罐、中间清水池、多介质过滤器和回用水池,所述工序步骤为将煤水沉淀池中的含煤废水泵入电子絮凝器;含煤废水在电子絮凝器中经絮凝处理后泵入沉降反应罐,颗粒物通过回流管回排煤水沉淀池;含煤废水在沉降反应池中沉降,沉降物通过排污管回排至煤水沉淀池,清水通过溢流管导入中间清水池;清水自中间清水池泵入多介质过滤器进行过滤;多介质过滤器中的沉渣随反冲洗水回流至煤水沉淀池,过滤水通过管路导入回用水池供厂区内用水。本实用新型作为一项新兴节能环保技术,可产生可观的经济效益,具有较大的应用价值。
The utility model discloses an electronic flocculation facility for coal-containing wastewater, which comprises a coal-water sedimentation tank, an electronic flocculator, a sedimentation reaction tank, an intermediate clear water tank, a multi-media filter and a reuse water pool arranged according to the process steps. In order to pump the coal-containing wastewater in the coal-water sedimentation tank into the electronic flocculator; the coal-containing wastewater is flocculated in the electronic flocculator and then pumped into the sedimentation reaction tank, and the particulate matter is returned to the coal-water sedimentation tank through the return pipe; the coal-containing wastewater is in the Settling in the sedimentation reaction tank, the sediment is discharged back to the coal-water sedimentation tank through the sewage pipe, and the clean water is introduced into the intermediate clear water tank through the overflow pipe; the clear water is pumped from the intermediate clear water tank into the multi-media filter for filtration; the sediment in the multi-media filter With the backwash water, it returns to the coal water sedimentation tank, and the filtered water is led into the reuse water tank through the pipeline for water use in the factory area. As an emerging energy-saving and environment-friendly technology, the utility model can generate considerable economic benefits and has great application value.
Description
技术领域technical field
本实用新型涉及废水处理工艺及设备,具体为一种含煤废水电子絮凝工艺及设施。The utility model relates to a wastewater treatment process and equipment, in particular to an electronic flocculation process and facility for coal-containing wastewater.
背景技术Background technique
含煤废水主要来自煤场喷洒废水、输煤栈桥冲洗废水以及煤场初期雨水。The coal-containing wastewater mainly comes from the spraying wastewater of the coal yard, the washing wastewater of the coal trestle and the initial rainwater of the coal yard.
对含煤废水的传统加药凝絮+膜过滤处理系统的问题所在:The problems of the traditional dosing flocculation + membrane filtration treatment system for coal-containing wastewater:
1、含煤废水中含有大量的煤粉颗粒,颗粒粒径分布不均,存在大量细小粒径的颗粒,密度较小,造成悬浮物不能有效自然沉淀。1. Coal-containing wastewater contains a large amount of coal powder particles, and the particle size distribution is uneven. There are a large number of fine particle size particles with a low density, which causes the suspended solids to fail to settle naturally.
2、加药絮凝要达到较好的絮凝效果必须要准确的计算加药量,加药量过少或过多都会降低絮凝效果。2. Dosing flocculation must be accurately calculated to achieve a better flocculation effect. Too little or too much dosing will reduce the flocculation effect.
3、输煤系统冲洗水不是连续的,含煤废水中的水质指标(TSS、PH、水量、水温等)不断变化,根据水质的变化要不断重新计算加药量,这是难以实现的,最终造成絮凝效果差,处理后出水越来越差。3. The flushing water of the coal conveying system is not continuous, and the water quality indicators (TSS, PH, water volume, water temperature, etc.) The flocculation effect is poor, and the effluent after treatment is getting worse.
4、目前药剂市场各厂家配方比例不同,若采购的厂家不同,对投放量又会有新的计算。4. At present, the formula ratio of each manufacturer in the pharmaceutical market is different. If the purchased manufacturer is different, there will be a new calculation for the dosage.
5、加药絮凝对水质要求高,投加药剂过多过少都会造成出水不合格,进而影响整个系统的稳定运行。5. Dosing flocculation has high requirements on water quality, too much or too little dosing will result in unqualified effluent, which will affect the stable operation of the entire system.
实用新型内容Utility model content
针对现有技术的不足,本实用新型所要解决的技术问题是提出了一种节能环保的含煤废水电子絮凝设施。Aiming at the deficiencies of the prior art, the technical problem to be solved by the utility model is to propose an energy-saving and environment-friendly electronic flocculation facility for coal-containing wastewater.
能够解决上述技术问题的含煤废水电子絮凝设施,其技术方案包括根据上述含煤废水电子絮凝工艺布置的煤水沉淀池、电子絮凝器、沉降反应罐、中间清水池、多介质过滤器和回用水池,所述煤水沉淀池通过泵管连通电子絮凝器,所述电子絮凝器通过泵管连通沉降反应罐,电子絮凝器还通过回流管连通煤水沉淀池,所述沉降反应罐通过溢流管连通中间清水池,沉降反应罐还通过排污管连通煤水沉淀池,所述中间清水池通过泵管连通多介质过滤器,所述多介质过滤器通过管路连通回用水池,多介质过滤器内设置有反冲洗装置并通过反冲洗管连通煤水沉淀池,所述回用水池连通用水泵管。The coal-containing wastewater electronic flocculation facility that can solve the above-mentioned technical problems, its technical solution includes a coal-water sedimentation tank, an electronic flocculator, a settling reaction tank, an intermediate clear water tank, a multi-media filter and a return Using a pool, the coal-water sedimentation tank is connected to the electronic flocculator through the pump tube, the electronic flocculator is connected to the sedimentation tank through the pump tube, and the electronic flocculator is also connected to the coal-water sedimentation tank through the return pipe, and the sedimentation tank is connected through the overflow The flow pipe is connected to the intermediate clean water tank, and the settling reaction tank is also connected to the coal-water sedimentation tank through the sewage pipe. A backwashing device is arranged in the filter and is connected to a coal-water sedimentation tank through a backwashing pipe, and the reused water pool is connected to a water pump pipe.
本实用新型的有益效果:The beneficial effects of the utility model:
1、本实用新型含煤废水电子絮凝设施采用的处理方法是一种先进的物理处理法,整个过程无任何药剂加入,无二次污染,为完全的环保产品。1. The treatment method adopted by the coal-containing wastewater electronic flocculation facility of this utility model is an advanced physical treatment method. There is no chemical agent added in the whole process, no secondary pollution, and it is a completely environmentally friendly product.
2、本实用新型全自动运行,无需人工维护,设备运行稳定,基本不需设备维护。2. The utility model operates fully automatically without manual maintenance, the equipment runs stably, and basically does not require equipment maintenance.
3、本实用新型可作为一项新兴节能环保技术加以应用,项目实施后,每年可节约运行和维护费用约100万元,对企业发展产生可观的经济效益,具有较大的应用价值。3. The utility model can be applied as a new energy-saving and environmental protection technology. After the project is implemented, the operation and maintenance costs can be saved by about 1 million yuan per year, which will generate considerable economic benefits for the development of enterprises and have great application value.
附图说明Description of drawings
图1为本实用新型一种实施方式的结构示意图。Fig. 1 is a schematic structural view of an embodiment of the present invention.
图2为图1实施方式的平面布置图。Fig. 2 is a plan view of the embodiment of Fig. 1 .
图号标识:1、煤水沉淀池;2、电子絮凝器;3、沉降反应罐;4、中间清水池;5、多介质过滤器;6、回用水池;7、泵管;8、回流管;9、管路;10、排污管;11、反冲洗管;12、用水泵管;13、溢流管;14、含煤废水排放管。Drawing number identification: 1. Coal water sedimentation tank; 2. Electronic flocculator; 3. Settling reaction tank; 4. Intermediate clean water tank; 5. Multimedia filter; 6. Reuse water tank; 7. Pump pipe; 8. Return 9. Pipeline; 10. Sewage pipe; 11. Backwash pipe; 12. Water pump pipe; 13. Overflow pipe; 14. Coal-containing wastewater discharge pipe.
具体实施方式detailed description
下面结合附图所示实施方式对本实用新型的技术方案作进一步说明。The technical solutions of the present utility model will be further described below in conjunction with the embodiments shown in the accompanying drawings.
本实用新型含煤废水电子絮凝设施,其技术方案包括煤水沉淀池1、电子絮凝器2、沉降反应罐3、中间清水池4、多介质过滤器5和回用水池6。The technical scheme of the utility model electronic flocculation facility for coal-containing wastewater includes a coal-water sedimentation tank 1, an electronic flocculator 2, a sedimentation reaction tank 3, an intermediate clear water tank 4, a multi-media filter 5 and a reuse water tank 6.
所述煤水沉淀池1、中间清水池4和回用水池6采用地坑形式,所述电子絮凝器2和沉降反应罐3建立在煤水沉淀池1和中间清水池4之间的地面上,所述多介质过滤器5建立在中间清水池4和回用水池6之间的地面上,如图1、图2所示。The coal-water sedimentation tank 1, the middle clear water tank 4 and the reuse water tank 6 adopt the pit form, and the electronic flocculator 2 and the sedimentation reaction tank 3 are built on the ground between the coal-water sedimentation tank 1 and the middle clear water tank 4 , the multimedia filter 5 is built on the ground between the intermediate clean water pool 4 and the reuse water pool 6, as shown in Fig. 1 and Fig. 2 .
所述煤水沉淀池1的进水口连通含煤废水排放管14,煤水沉淀池1的出水口通过泵管7连通电子絮凝器2的进水口,电子絮凝器2的排渣口通过回流管8连通煤水沉淀池1,电子絮凝器2的出水口通过泵管7连通沉降反应罐3的进水口,所述沉降反应罐3的出水口通过溢流管13连通中间清水池4的进水口,沉降反应3的排污口通过排污管10连通煤水沉淀池1,所述中间清水池4的出水口通过泵管7连通多介质过滤器5的进水口,所述多介质过滤器5的出水口通过管路9连通回用水池6的进水口,多介质过滤器5内设有反冲洗装置,多介质过滤器5的排渣口通过反冲洗管11连通煤水沉淀池1,所述回用水池6的出水口连通用水泵管12,如图1、图2所示。The water inlet of the coal-water sedimentation tank 1 is connected to the coal-containing wastewater discharge pipe 14, the water outlet of the coal-water sedimentation tank 1 is connected to the water inlet of the electronic flocculator 2 through the pump pipe 7, and the slag discharge port of the electronic flocculator 2 is passed through the return pipe 8 is connected to the coal-water sedimentation tank 1, and the water outlet of the electronic flocculator 2 is connected to the water inlet of the sedimentation reaction tank 3 through the pump tube 7, and the water outlet of the sedimentation reaction tank 3 is connected to the water inlet of the middle clear water tank 4 through the overflow pipe 13 The sewage outlet of the sedimentation reaction 3 is connected to the coal-water sedimentation tank 1 through the sewage pipe 10, and the water outlet of the intermediate clear water tank 4 is connected to the water inlet of the multimedia filter 5 through the pump pipe 7, and the outlet of the multimedia filter 5 The water inlet is connected to the water inlet of the recycling pool 6 through the pipeline 9, and a backwashing device is arranged in the multimedia filter 5, and the slag outlet of the multimedia filter 5 is connected to the coal water sedimentation tank 1 through the backwashing pipe 11. The water outlet of the water pool 6 is connected with the water pump pipe 12, as shown in Fig. 1 and Fig. 2 .
所述电子絮凝器2常规采用并联的两台,对应的所述沉降反应罐3设置为并联的两个,与其处理量相匹配,所述多介质过滤器5设置为并联的12个,如图2所示。The electronic flocculator 2 conventionally adopts two in parallel, and the corresponding settling reaction tank 3 is set as two in parallel to match its processing capacity, and the multimedia filter 5 is set as 12 in parallel, as shown in the figure 2 shown.
根据含煤废水电子絮凝各设施的布置,本实用新型含煤废水电子絮凝工艺的工序步骤为:According to the layout of various facilities for electronic flocculation of coal-containing wastewater, the process steps of the utility model electronic flocculation process for coal-containing wastewater are:
1、含煤废水通过含煤废水排放管14排放至煤水沉淀池1,较大物料直接沉底。1. The coal-containing wastewater is discharged to the coal-water sedimentation tank 1 through the coal-containing wastewater discharge pipe 14, and the larger materials directly sink to the bottom.
2、含煤废水经泵管7抽送入电子絮凝器2,电极板通电后产生电场,细小带电颗粒、胶体、大分子的蛋白质,病毒粒子,细胞等在电场的作用下进行定向运动,碰撞,压缩双电子层脱稳,导致双电层压缩脱稳、絮凝,形成的絮体可以吸附细小的胶体等物质形成大颗粒加速沉淀。2. The coal-containing wastewater is pumped into the electronic flocculator 2 through the pump tube 7. After the electrode plate is energized, an electric field is generated, and the fine charged particles, colloids, macromolecular proteins, virus particles, cells, etc. move directionally and collide under the action of the electric field. The destabilization of the compressed double electron layer leads to the destabilization and flocculation of the double electric layer. The flocs formed can absorb fine colloids and other substances to form large particles to accelerate precipitation.
3、经过絮凝处理后的含煤废水经泵管7抽送入沉降反应罐3,沉淀的颗粒物通过回流管8回排至煤水沉淀池1。3. The coal-containing wastewater after flocculation treatment is pumped into the sedimentation reaction tank 3 through the pump pipe 7, and the precipitated particles are discharged back to the coal-water sedimentation tank 1 through the return pipe 8.
4、含煤废水中的杂质在沉降反应罐3中继续沉降,沉降物经排污口通过排污管10回排至煤水沉淀池1,清水则通过溢流管13(连通在沉降反应罐3的溢流口)导入中间清水池4。4. The impurities in the coal-containing wastewater continue to settle in the settling reaction tank 3, and the sediment is discharged to the coal-water sedimentation tank 1 through the sewage outlet through the blowdown pipe 10, and the clear water passes through the overflow pipe 13 (connected to the bottom of the settling reaction tank 3). overflow port) into the middle clear water tank 4.
5、清水自中间清水池4经泵管7抽送入多介质过滤器5继续进行过滤,多介质过滤器5的过滤介质不受油脂的影响,而且介质中有一定数量的无烟煤可以吸附去除大部分的油类,降低出水含油量。5. Clean water is pumped from the middle clean water tank 4 through the pump tube 7 into the multimedia filter 5 for further filtration. The filter medium of the multimedia filter 5 is not affected by grease, and there is a certain amount of anthracite in the medium that can absorb and remove most of it. Oil, reduce the oil content of water.
6、经多介质过滤器5过滤处理后的干净水通过管路9导入回用水池6,多介质过滤器5中的残渣经内设的反冲洗装置的冲洗后,从排渣口通过反冲洗管11回排至煤水沉淀池1。6. The clean water filtered by the multi-media filter 5 is introduced into the reuse pool 6 through the pipeline 9. After the residue in the multi-media filter 5 is washed by the built-in backwash device, it is backwashed from the slag outlet. The pipe 11 is discharged back to the coal water sedimentation tank 1.
7、通过用水泵管12将回用水池6中的干净水抽送至煤场所需用水单位。7. Use the water pump pipe 12 to pump the clean water in the reuse water pool 6 to the water unit required by the coal yard.
本实用新型设施在中央智能控制器PLC控制下,从含煤废水进入到回收利用干净水,整个工艺过程连续自动运行,不需添加化学药剂和采取铺膜措施。Under the control of the central intelligent controller PLC, the facility of the utility model runs continuously and automatically from the coal-containing waste water entering to the recycling of clean water, without adding chemical agents and taking film-laying measures.
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| CN201521007333.3U CN205241438U (en) | 2015-12-08 | 2015-12-08 | Contain coal waste water electron flocculation facility |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106115993A (en) * | 2016-08-31 | 2016-11-16 | 霍普科技(天津)股份有限公司 | A kind of electricity flocculation sewage-treatment plant |
| CN108218056A (en) * | 2018-01-16 | 2018-06-29 | 广州发展集团股份有限公司 | A kind of seashore coal yard wastewater collection processing system |
-
2015
- 2015-12-08 CN CN201521007333.3U patent/CN205241438U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106115993A (en) * | 2016-08-31 | 2016-11-16 | 霍普科技(天津)股份有限公司 | A kind of electricity flocculation sewage-treatment plant |
| CN108218056A (en) * | 2018-01-16 | 2018-06-29 | 广州发展集团股份有限公司 | A kind of seashore coal yard wastewater collection processing system |
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