CN207933226U - A kind of industrial wastewater treatment system - Google Patents
A kind of industrial wastewater treatment system Download PDFInfo
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- CN207933226U CN207933226U CN201721881879.0U CN201721881879U CN207933226U CN 207933226 U CN207933226 U CN 207933226U CN 201721881879 U CN201721881879 U CN 201721881879U CN 207933226 U CN207933226 U CN 207933226U
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- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
一种工业废水处理系统,具有RO浓水预处理系统,除臭系统,事故池、调节池、水解酸化池、缺氧池、好氧池、MBBR池、沉淀池、溶气气浮池、臭氧接触池、曝气生物滤池、过滤池、消毒监测池、污泥浓缩池、脱水机、废水收集池各单元由管道连通。沉淀池的剩余污泥由泵将污泥回流到缺氧池和水解酸化池。该方法特别对石油化工工业废水处理效果好,运行稳定,出水水质达到国家一级A排放标准。
An industrial wastewater treatment system with RO concentrated water pretreatment system, deodorization system, accident pool, regulation pool, hydrolysis acidification pool, anoxic pool, aerobic pool, MBBR pool, sedimentation pool, dissolved air flotation pool, ozone contact Each unit of pool, biological aerated filter, filter pool, disinfection monitoring pool, sludge thickening pool, dehydrator, and waste water collection pool is connected by pipelines. The remaining sludge in the sedimentation tank is returned to the anoxic tank and the hydrolytic acidification tank by the pump. The method is particularly effective in treating petrochemical industrial wastewater, and the operation is stable, and the quality of the effluent reaches the national first-class A discharge standard.
Description
技术领域technical field
本实用新型涉及一种水处理技术,特别是一种工业废水处理系统。The utility model relates to a water treatment technology, in particular to an industrial waste water treatment system.
背景技术Background technique
随着现代工业迅速的发展,各类企业在生产过程中产生的工业废水种类也不同。由于消费需求的增加,企业生产量就不断增加,因此产生的工业废水量也不断的增加。如果不对这些工业废水做进一步的处理,不仅会对环境造成严重的污染,而且还威胁着人类的健康和安全。由于工业废水中主要为碳氢化合物,氮磷营养不足,生化性较差,部分金属离子和部分难降解物质都对微生物有较强的毒害和抑制作用。还有各种有机及无机化工污染物和含有少量的污油、盐分高、悬浮物高、COD和氨氮较高,这些基本上属于难生化降解的废水,因此工业废水处理工艺流程比较复杂。With the rapid development of modern industry, the types of industrial wastewater produced by various enterprises in the production process are also different. Due to the increase in consumer demand, the production volume of enterprises has continued to increase, so the amount of industrial wastewater produced has also continued to increase. If the industrial wastewater is not further treated, it will not only cause serious pollution to the environment, but also threaten human health and safety. Since industrial wastewater is mainly composed of hydrocarbons, nitrogen and phosphorus nutrients are insufficient, and the biochemical properties are poor, some metal ions and some refractory substances have strong poisonous and inhibitory effects on microorganisms. There are also various organic and inorganic chemical pollutants and a small amount of dirty oil, high salinity, high suspended solids, high COD and ammonia nitrogen, which are basically wastewater that is difficult to biodegrade, so the industrial wastewater treatment process is relatively complicated.
发明内容Contents of the invention
本实用新型要解决的技术问题是针对现有技术的不足,提出了一种效果好,运行稳定的工业废水处理系统。The technical problem to be solved by the utility model is to propose an industrial wastewater treatment system with good effect and stable operation in view of the deficiencies of the prior art.
本实用新型要解决的技术问题是通过以下技术方案来实现的,一种工业废水处理系统,其特点是:The technical problem to be solved by the utility model is achieved through the following technical solutions, an industrial wastewater treatment system, which is characterized in that:
设有经管道流入正常工业废水的调节池和非正常工业废水临时储存的事故池,在调节池和事故池之间通过管道连接有溶气气浮池;There is a regulating pool for normal industrial wastewater flowing through pipelines and an emergency pool for temporary storage of abnormal industrial wastewater, and a dissolved air flotation pool is connected through pipelines between the regulating pool and the emergency pool;
设有水解酸化池,调节池内的工业废水由循环泵输送到水解酸化池,水解酸化池内设有PE材质组合填料,水解酸化池的底部设有升流式连续进水的穿空管,并在水解酸化池的池底设有排泥管;There is a hydrolytic acidification tank, and the industrial wastewater in the regulating tank is transported to the hydrolytic acidification tank by a circulating pump. The hydrolytic acidification tank is equipped with PE material composite packing, and the bottom of the hydrolysis acidification tank is provided with an upflow continuous water inlet pipe, and in the There is a mud discharge pipe at the bottom of the hydrolytic acidification tank;
设有缺氧池和好氧池,水解酸化池出水经管道流入到缺氧池,工业废水在缺氧的环境下进行反硝化;缺氧池出水流入好氧池,在好氧池底安装有微孔曝气器。通过鼓风曝气实现好氧生物氧化和硝化;There is an anoxic pool and an aerobic pool, and the effluent from the hydrolytic acidification pool flows into the anoxic pool through the pipeline, and the industrial wastewater is denitrified in an anoxic environment; the effluent from the anoxic pool flows into the aerobic pool, and a Microporous aerator. Aerobic biological oxidation and nitrification are achieved by blast aeration;
设有流化床生物膜反应器,好氧池出水流入到流化床生物膜反应器,在流化床生物膜反应器的池底安装有微孔曝气器,在流化床生物膜反应器的池内添加有生物流化填料,在流化床生物膜反应器的出水端设有泥水混合液回流泵,并在回流管道上安装流量计;回流泵通过分支管路将一部分泥水混合液回流至缺氧池内;There is a fluidized bed biofilm reactor, the effluent from the aerobic tank flows into the fluidized bed biofilm reactor, and a microporous aerator is installed at the bottom of the fluidized bed biofilm reactor, and the fluidized bed biofilm reacts Biological fluidization filler is added in the tank of the fluidized bed biofilm reactor, and a mud-water mixture reflux pump is installed at the outlet of the fluidized bed biofilm reactor, and a flow meter is installed on the return pipe; the reflux pump returns a part of the mud-water mixture through the branch pipeline. into the anoxic pool;
设有沉淀池,流化床生物膜反应器的出水经管道流入沉淀池,工业废水泥水混合液在沉淀池进行固液分离,沉淀池内安装有刮泥机;There is a sedimentation tank, the effluent of the fluidized bed biofilm reactor flows into the sedimentation tank through the pipeline, and the industrial waste cement-water mixture is separated from the solid and liquid in the sedimentation tank, and a mud scraper is installed in the sedimentation tank;
设有深度溶气气浮池,沉淀池出水经管道流入深度溶气气浮池,There is a deep dissolved air flotation tank, and the water from the sedimentation tank flows into the deep dissolved air flotation tank through the pipeline.
设有臭氧接触池,深度溶气气浮池出水经管道流入臭氧接触池,臭氧接触池设有臭氧发生器、换热器和尾气破坏系统,由臭氧发生器产生的臭氧加入到臭氧接触池中与工业废水充分接触,对工业废水中残留的有机物进行氧化;There is an ozone contact tank, and the water from the deep dissolved air flotation tank flows into the ozone contact tank through pipelines. The ozone contact tank is equipped with an ozone generator, a heat exchanger, and an exhaust gas destruction system. The ozone generated by the ozone generator is added to the ozone contact tank. Full contact with industrial wastewater to oxidize residual organic matter in industrial wastewater;
设有曝气生物滤池,臭氧接触池出水经管道流入曝气生物滤池,曝气生物滤池内装填有高比表面积的陶粒颗粒的填料层,以提供微生物膜生长的载体,在填料层下部设有鼓风曝气系统;There is a biological aerated filter, and the effluent from the ozone contact tank flows into the biological aerated filter through the pipeline. The biological aerated filter is filled with a packing layer of ceramsite particles with a high specific surface area to provide a carrier for the growth of microbial film. The lower part of the floor is equipped with a blast aeration system;
设有过滤池,曝气生物滤池出水经管道流入过滤池;There is a filter tank, and the effluent of the biological aerated filter flows into the filter tank through the pipeline;
设有消毒监测池,过滤池出水经管道流入消毒监测池,达标水通过泵排放到接纳体中。There is a disinfection monitoring pool, the water from the filter pool flows into the disinfection monitoring pool through the pipeline, and the standard water is discharged into the receiving body through the pump.
本实用新型要解决的技术问题还可以通过以下技术方案来进一步实现,在调节池和事故池之间设有超越溶气气浮池的直排管路。The technical problem to be solved by the utility model can be further realized through the following technical scheme, a straight-line pipeline beyond the dissolved air flotation pool is provided between the adjustment pool and the emergency pool.
本实用新型要解决的技术问题还可以通过以下技术方案来进一步实现,沉淀池设有回流井,将底部的剩余污泥经泵一部分回流到缺氧池,一部分回流到调节池,对调节池内的混合工业废水进行预处理酸化处理,分别在回流到调节池和缺氧池管道上安装流量计。The technical problem to be solved by the utility model can also be further realized through the following technical solutions. The settling tank is provided with a return well, and part of the remaining sludge at the bottom is returned to the anoxic tank through the pump, and part of it is returned to the regulating tank. The mixed industrial wastewater is pretreated and acidified, and flow meters are installed on the pipelines returning to the regulating tank and the anoxic tank respectively.
本实用新型要解决的技术问题还可以通过以下技术方案来进一步实现,水解酸化池内安装有污泥浓度计,排泥管上安装有流量计。The technical problem to be solved by the utility model can be further realized through the following technical solutions. A sludge concentration meter is installed in the hydrolysis acidification tank, and a flow meter is installed on the sludge discharge pipe.
本实用新型要解决的技术问题还可以通过以下技术方案来进一步实现,深度溶气气浮池设有一级絮凝搅拌机、二级絮凝搅拌机、三级絮凝搅拌机和溶气释放器。The technical problems to be solved by the utility model can be further realized through the following technical solutions. The deep dissolved air flotation tank is equipped with a first-level flocculation mixer, a second-level flocculation mixer, a third-level flocculation mixer and a dissolved air releaser.
本实用新型要解决的技术问题还可以通过以下技术方案来进一步实现,设有RO浓水预处理系统,RO浓水预处理系统包括Fenton氧化池和混凝沉淀池,Fenton氧化池出水加入氢氧化钠溶液调节pH至中性后进入混凝沉淀池,在混凝沉淀池分离后的出水经泵输送与调节池相连接;设有污泥浓缩池,经混凝沉淀池沉淀的污泥排放至污泥浓缩池。The technical problem to be solved by the utility model can also be further realized through the following technical schemes. An RO concentrated water pretreatment system is provided. The RO concentrated water pretreatment system includes a Fenton oxidation pond and a coagulation sedimentation pond, and the effluent of the Fenton oxidation pond is added with hydrogen oxidation The sodium solution adjusts the pH to neutral and then enters the coagulation sedimentation tank. The effluent separated in the coagulation sedimentation tank is pumped and connected to the adjustment tank; there is a sludge concentration tank, and the sludge settled in the coagulation sedimentation tank is discharged to Sludge thickening tank.
本实用新型要解决的技术问题还可以通过以下技术方案来进一步实现,在Fenton氧化池前端连接有pH调节池。The technical problem to be solved by the utility model can also be further realized through the following technical solutions, a pH adjustment pool is connected to the front end of the Fenton oxidation pool.
本实用新型要解决的技术问题还可以通过以下技术方案来进一步实现,设有除臭系统,除臭系统包括臭气密封收集系统、气体输送系统、生物除臭装置以及及控制系统。The technical problem to be solved by the utility model can be further realized by the following technical solutions. A deodorization system is provided. The deodorization system includes an odor sealing collection system, a gas delivery system, a biological deodorization device and a control system.
本实用新型与现有技术相比,具有RO浓水预处理系统,除臭系统,事故池、调节池、水解酸化池、缺氧池、好氧池、MBBR池、沉淀池、溶气气浮池、臭氧接触池、曝气生物滤池、过滤池、消毒监测池、污泥浓缩池、脱水机、废水收集池各单元由管道连通。沉淀池的剩余污泥由泵将污泥回流到缺氧池和水解酸化池。该方法特别对石油化工工业废水处理效果好,运行稳定,出水水质达到国家一级A排放标准。Compared with the prior art, the utility model has RO concentrated water pretreatment system, deodorization system, accident pool, regulation pool, hydrolytic acidification pool, anoxic pool, aerobic pool, MBBR pool, sedimentation pool, dissolved air flotation pool , ozone contact tank, biological aerated filter tank, filter tank, disinfection monitoring tank, sludge thickening tank, dehydrator, and waste water collection tank are connected by pipelines. The remaining sludge in the sedimentation tank is pumped back to the anoxic tank and the hydrolytic acidification tank. The method is particularly effective in treating petrochemical industrial wastewater, and the operation is stable, and the quality of the effluent reaches the national first-class A discharge standard.
附图说明Description of drawings
图1为本实用新型的结构简图。Fig. 1 is a structural diagram of the utility model.
具体实施方式Detailed ways
以下进一步描述本发明的具体技术方案,以便于本领域的技术人员进一步地理解本发明,而不构成对其权利的限制。The specific technical solutions of the present invention are further described below, so that those skilled in the art can further understand the present invention, without limiting their rights.
一种工业废水处理系统,具有RO浓水预处理系统,除臭系统,事故池2、调节池1、水解酸化池4、缺氧池5、好氧池6、MBBR池7、沉淀池8、溶气气浮池9、臭氧接触池10、曝气生物滤池11、过滤池12、消毒监测池13、污泥浓缩池、脱水机、废水收集池各单元由管道连通。沉淀池的剩余污泥由泵将污泥回流到缺氧池和水解酸化池。An industrial wastewater treatment system with RO concentrated water pretreatment system, deodorization system, accident pool 2, regulation pool 1, hydrolytic acidification pool 4, anoxic pool 5, aerobic pool 6, MBBR pool 7, sedimentation pool 8, Dissolved air flotation tank 9, ozone contact tank 10, biological aerated filter tank 11, filter tank 12, disinfection monitoring tank 13, sludge concentration tank, dehydrator, and waste water collection tank are connected by pipelines. The remaining sludge in the sedimentation tank is pumped back to the anoxic tank and the hydrolytic acidification tank.
RO浓水进水流入到Fenton氧化池前端的pH调节池,与加入硫酸溶液搅拌混合,将pH调节至酸性后进入Fenton反应池,RO浓水与投加的双氧水、硫酸亚铁溶液搅拌混合,经催化氧化去除部分COD,同时提高浓水的可生化性能,然后Fenton氧化池出水加入氢氧化钠溶液调节pH至中性后,进入混凝沉淀池,在混凝沉淀池投加絮凝剂PAC和PAM混合进行沉淀固液分离,分离后的出水经泵提升至调节池。沉淀的污泥排放至污泥浓缩池。The RO concentrated water inflow flows into the pH adjustment tank at the front end of the Fenton oxidation tank, and is stirred and mixed with the added sulfuric acid solution. After adjusting the pH to acidity, it enters the Fenton reaction tank. The RO concentrated water is stirred and mixed with the added hydrogen peroxide and ferrous sulfate solution. Part of the COD is removed by catalytic oxidation, and the biochemical properties of the concentrated water are improved at the same time. Then the effluent of the Fenton oxidation tank is added with sodium hydroxide solution to adjust the pH to neutral, and then enters the coagulation sedimentation tank, where the flocculant PAC and PAM is mixed for solid-liquid separation of precipitation, and the separated effluent is lifted to the regulating tank by the pump. The settled sludge is discharged to the sludge thickening tank.
正常的工业废水经管道流入调节池,由循环泵进行水量的调节和水质的均和。非正常工业废水有阀门控制进入事故池临时储存。若事故池内含油浓度较高,则先经溶气气浮池处理后在流入调节池,若含油浓度不高,直接直接通过泵超越溶气气浮池3小流量送入调节池。事故池储水后,在工艺生产许可的情况下,尽快将事故池中的废水处理后输送到调节池内,进行处理,以便尽快腾出空间随时备用。Normal industrial wastewater flows into the regulating tank through the pipeline, and the water volume is regulated and the water quality is equalized by the circulating pump. Abnormal industrial wastewater is controlled by a valve and enters the accident pool for temporary storage. If the oil concentration in the accident pool is high, it will be treated by the dissolved air flotation tank first and then flow into the adjustment tank. If the oil concentration is not high, it will be directly sent to the adjustment pool by the pump beyond the dissolved air flotation tank with a small flow rate of 3. After storing water in the accident pool, the wastewater in the accident pool should be treated and transported to the regulating pool as soon as possible under the condition of process production permit, so as to free up space as soon as possible for standby at any time.
调节池内的工业废水由循环泵输送到水解酸化池,水解酸化池内设有PE材质组合填料,底部穿空管升流式连续进水,底部设有排泥管,根据工艺要求可间断排泥。上部水平堰式连续出水,水力停留时间6小时,上升流速为0.5~1米/时,污泥龄在30天以上。通过悬浮污泥和PE材质组合填料生物膜中的厌氧微生物的新陈代谢作用将工艺废水中难降解的有机物水解酸化为易于生化降解的简单有机物,提高工业废水的可生化性,同时消解部分剩余污泥,以减少污泥量。水解酸化池内安装有污泥浓度计,排泥管道上安装有流量计。通过排放剩余污泥来控制污泥浓度和污泥龄,使处理效果达到最佳状态。剩余污泥排放至污泥浓缩池。The industrial wastewater in the regulating tank is transported to the hydrolysis and acidification tank by the circulating pump. The hydrolysis and acidification tank is equipped with PE material composite filler, the bottom is pierced through the hollow pipe to ascend the flow continuously, and the bottom is equipped with a mud discharge pipe, which can discharge mud intermittently according to the process requirements. The upper horizontal weir discharges water continuously, the hydraulic retention time is 6 hours, the rising flow rate is 0.5-1 m/h, and the sludge age is more than 30 days. Through the metabolism of anaerobic microorganisms in the biofilm combined with suspended sludge and PE material, the refractory organic matter in the process wastewater is hydrolyzed and acidified into simple organic matter that is easy to biodegrade, improving the biodegradability of industrial wastewater and degrading part of the remaining sewage. mud to reduce sludge volume. A sludge concentration meter is installed in the hydrolytic acidification tank, and a flow meter is installed on the sludge discharge pipe. Control the sludge concentration and sludge age by discharging excess sludge, so that the treatment effect can reach the best state. The remaining sludge is discharged to the sludge thickening tank.
水解酸化池出水经管道流入到缺氧池。缺氧池水力停留时间为5小时,污泥龄为20~30天。工业废水在缺氧的环境下进行反硝化,将硝酸盐氮还原成氮气逸出到空气中。水解酸化池内设有推进器,防止污泥沉积,影响处理效果。The effluent from the hydrolytic acidification tank flows into the anoxic tank through the pipeline. The hydraulic retention time of the anoxic pool is 5 hours, and the sludge age is 20-30 days. Industrial wastewater undergoes denitrification in an oxygen-deficient environment, reducing nitrate nitrogen to nitrogen and escaping into the air. A propeller is installed in the hydrolytic acidification tank to prevent sludge deposition and affect the treatment effect.
缺氧池出水流入好氧池。好氧池水力停留时间10小时,污泥龄为20~30天。在池底安装有微孔曝气器。通过鼓风曝气实现好氧生物氧化和硝化,降解去除有机污染物,并将氨氮转化成硝酸盐氮。The effluent from the anoxic pool flows into the aerobic pool. The hydraulic retention time of the aerobic pool is 10 hours, and the sludge age is 20-30 days. A microporous aerator is installed at the bottom of the pool. Aerobic biological oxidation and nitrification are achieved through blast aeration, organic pollutants are degraded and removed, and ammonia nitrogen is converted into nitrate nitrogen.
好氧池出水流入到流化床生物膜反应器(即MBBR池),工业废水在MBBR池水力停留时间为6小时,污泥龄为20~30天。在池底安装有微孔曝气器,池内添加有生物流化填料,提高好氧生化处理效率及氨氮处理效果。在MBBR出水端设有泥水混合液回流泵,并在回流管道上安装流量计。由回流泵将一部分泥水混合液回流到缺氧池内。通过控制泥水混合液的回流量大小,以保证MBBR出水硝酸盐氮指标平稳可控。The effluent from the aerobic tank flows into the fluidized bed biofilm reactor (ie MBBR tank), the hydraulic retention time of industrial wastewater in the MBBR tank is 6 hours, and the sludge age is 20-30 days. A microporous aerator is installed at the bottom of the pool, and biological fluidized filler is added in the pool to improve the efficiency of aerobic biochemical treatment and the effect of ammonia nitrogen treatment. There is a mud-water mixture return pump at the MBBR outlet, and a flow meter is installed on the return pipe. A part of the mud-water mixture is returned to the anoxic pool by the return pump. By controlling the return flow of mud-water mixture, the nitrate nitrogen index of MBBR effluent is stable and controllable.
MBBR池出水经管道流入沉淀池,水力停留时间3小时,泥位0.5~2米。安装有刮泥机。工业废水泥水混合液在沉淀池进行固液分离。沉淀池并设有回流井,将底部的剩余污泥经泵一部分回流到缺氧池,一部分回流到调节池,对调节池内的混合工业废水进行预处理酸化处理。分别在回流到调节池和缺氧池管道上安装流量计,通过控制各回流量大小,使处理效果达到最佳状态。The effluent from the MBBR tank flows into the sedimentation tank through the pipeline, the hydraulic retention time is 3 hours, and the mud level is 0.5-2 meters. A mud scraper is installed. The solid-liquid separation of industrial waste cement-water mixture is carried out in the sedimentation tank. The settling tank is also equipped with a return well, and part of the remaining sludge at the bottom is returned to the anoxic tank through the pump, and part of it is returned to the regulating tank, and the mixed industrial wastewater in the regulating tank is pretreated and acidified. Flowmeters are installed on the pipelines of the backflow to the adjustment pool and the anoxic pool respectively, and the treatment effect can reach the best state by controlling the size of each backflow.
深度溶气气浮池由搅拌机,一级絮凝搅拌机、二级絮凝搅拌机、三级絮凝搅拌机、溶气释放器,刮渣机、空压机、压力溶气罐、溶气水泵、浮渣泵组成。沉淀池出水经管道流入深度溶气气浮池混合池,在一级絮凝池内加入PAC由一级絮凝搅拌机与工业废水混合搅拌后,在到二级絮凝池,在二级絮凝池加入PAM,由二级絮凝搅拌机搅拌混合后,在到三级絮凝池,在三级絮凝池内用三级絮凝搅拌机充分搅拌混合后在到气浮池。由溶气水泵向溶气释放器输送空气,在由溶气释放器释放出来的空气与工业废水充分混合,在溶气水微小气泡的浮力作用下,絮体粘附气泡上浮,后经由刮渣机刮到浮渣池中,在由浮渣泵排至污泥浓缩池。The deep dissolved air flotation tank is composed of a mixer, a first-stage flocculation mixer, a second-stage flocculation mixer, a third-stage flocculation mixer, a dissolved air releaser, a slag scraper, an air compressor, a pressure dissolved air tank, a dissolved air water pump, and a scum pump. The effluent from the sedimentation tank flows into the mixing tank of the deep dissolved air flotation tank through the pipeline, and PAC is added to the first-level flocculation tank, and the first-level flocculation mixer is mixed with industrial wastewater. After stirring and mixing with the three-stage flocculation mixer, it goes to the third-stage flocculation tank, and then fully stirs and mixes with the three-stage flocculation mixer in the three-stage flocculation tank before going to the air flotation tank. The air is delivered from the dissolved air pump to the dissolved air releaser, and the air released from the dissolved air releaser is fully mixed with the industrial wastewater. Under the action of the buoyancy of the tiny air bubbles in the dissolved air water, the flocs adhere to the air bubbles and float up, and then pass through the scraping slag. The machine is scraped into the scum tank, and then discharged to the sludge thickening tank by the scum pump.
深度溶气气浮池出水经管道流入臭氧接触池,有臭氧发生器、换热器、尾气破坏系统等设备,由臭氧发生器产生的臭氧加入到臭氧接触池中与工业废水充分接触,对工业废水中残留的有机物进行氧化,提高其可生化性。如果有过量的臭氧,由尾气破坏系统把过量的臭氧转变成氧气排放到空气中。The effluent from the deep dissolved air flotation tank flows into the ozone contact tank through pipelines, equipped with equipment such as an ozone generator, heat exchanger, and tail gas destruction system. The ozone generated by the ozone generator is added to the ozone contact tank to fully contact with industrial wastewater, and the industrial wastewater Oxidizes the organic matter remaining in the water to improve its biodegradability. If there is excess ozone, the exhaust gas destruction system converts excess ozone into oxygen and discharges it into the air.
臭氧接触池出水经管道流入曝气生物滤池。曝气生物滤池内装填有高比表面积的陶粒颗粒的填料层,以提供微生物膜生长的载体。工业废水自下向上流过填料层,在填料层下部设有鼓风曝气系统,让空气与工业废水充分接触,使工业废水中的有机污染物与填料表面生物膜通过生化反应得到降解,填料同时也起到物理过滤作用。如果填料层堵塞过滤性不好,可通过反冲洗系统进行反冲洗,反冲洗水与初滤水流入到废水收集池内。The effluent from the ozone contact tank flows into the biological aerated filter through the pipeline. The biological aerated filter is filled with a filler layer of ceramsite particles with a high specific surface area to provide a carrier for microbial film growth. Industrial wastewater flows through the packing layer from bottom to top, and a blower aeration system is installed at the bottom of the packing layer to allow the air to fully contact the industrial wastewater, so that the organic pollutants in the industrial wastewater and the biofilm on the surface of the filler can be degraded through biochemical reactions. It also acts as a physical filter. If the packing layer is clogged and the filterability is not good, it can be backwashed through the backwashing system, and the backwashing water and primary filtration water will flow into the waste water collection tank.
曝气生物滤池出水经管道流入过滤池,过滤池种类多,如活性砂滤池、纤维转盘滤池、D型滤池、V型滤池、虹吸滤池,本实用新型采用的是D型过滤池。工业废水经过纤维滤料过滤去除水中的悬浮物,以确保出水中悬浮物达标排放。如果纤维滤料堵塞过滤性不好,可通过反冲洗系统进行反冲洗。过滤池反冲洗水、初滤水流入到废水收集池内。The effluent of the biological aerated filter flows into the filter tank through the pipeline. There are many types of filter tanks, such as active sand filter, fiber turntable filter, D-type filter, V-type filter, and siphon filter. The utility model adopts D-type filter pool. Industrial wastewater is filtered through fiber filter material to remove suspended solids in the water to ensure that the suspended solids in the effluent are discharged up to the standard. If the fiber filter material is clogged and the filterability is not good, it can be backwashed through the backwashing system. The backwash water of the filter tank and the primary filter water flow into the waste water collection tank.
过滤池出水经管道流入消毒监测池。工业废水先进消毒池对即将排放的水进行消毒,消毒方式有臭氧消毒、二氧化氯消毒、紫外线消毒等。本实用新型采用的是二氧化氯消毒。消毒后的水进入在线监测池对出水水质指标进行在线监测,各项指标达标后,通过泵排放到接纳体中。当出水水质不达标时通过泵将监测池内的废水输送到事故池,再次进行全流程处理。The effluent from the filter tank flows into the disinfection monitoring tank through the pipeline. The advanced disinfection pool for industrial wastewater disinfects the water to be discharged. The disinfection methods include ozone disinfection, chlorine dioxide disinfection, ultraviolet disinfection, etc. What the utility model adopted was chlorine dioxide disinfection. The disinfected water enters the online monitoring pool to monitor the effluent water quality indicators online. After all indicators meet the standards, it is discharged into the receiving body through the pump. When the effluent water quality does not meet the standard, the wastewater in the monitoring pool is transported to the accident pool through the pump, and the whole process is processed again.
废水收集池主要用于厂区的初期雨水,管道溢流放空、杂排水以及曝气生物滤池、过滤池的反冲洗水和初滤水的收集。收集后的水由泵输送到事故池内。然后进入处理系统进行全流程处理。The waste water collection tank is mainly used for the initial rainwater in the factory area, the overflow and emptying of pipelines, miscellaneous drainage, and the collection of backwash water and primary filtration water of biological aerated filter and filter tank. The collected water is pumped into the emergency pool. Then enter the processing system for the whole process processing.
污泥浓缩池收集调节池、水解酸化池的排泥,收集溶气气浮浮渣。它们在污泥浓缩池内充分混合,在重力脱水与污泥消化的作用下,使污泥含水率有99%以上降低至97%~98%,污泥体积减少2~3倍,为后续的污泥脱水创造条件。The sludge thickening tank collects the sludge from the regulating tank and the hydrolysis acidification tank, and collects the dissolved air flotation scum. They are fully mixed in the sludge thickening tank, and under the action of gravity dehydration and sludge digestion, the moisture content of the sludge is reduced from more than 99% to 97% to 98%, and the volume of the sludge is reduced by 2 to 3 times. Mud dehydration creates conditions.
污泥浓缩池中的污泥由污泥泵输送到污泥脱水机中,由污泥脱水机脱去污泥中的水分,使污泥含水率小于80%。生产的污泥外运到其他地方处置。The sludge in the sludge thickening tank is transported by the sludge pump to the sludge dehydrator, and the sludge dehydrator removes the moisture in the sludge, so that the moisture content of the sludge is less than 80%. The produced sludge is transported to other places for disposal.
除臭系统,本实用新型采用的是生物滤池法,由臭气密封收集系统、气体输送系统、生物除臭装置及控制系统四部分组成。污水处理过程中对产生恶臭气体的单元经臭气密封收集系统收集,收集后由气体输送系统将恶臭气体输送至生物除臭装置中。恶臭气体在生物除臭装置中经过湿润、多孔和充满活性微生物的滤层,利用微生物的细胞个体小、表面积大、吸附性强、代谢种类多等特点,将恶臭气体物质吸附、降解后,分解成二氧化碳和水以及其它无、低害物质。对经过处理过的气体达标进入排气筒排放。The deodorization system, the utility model adopts the biological filter method, which is composed of four parts: the odor sealing collection system, the gas delivery system, the biological deodorization device and the control system. During the sewage treatment process, the unit that produces malodorous gas is collected by the odor sealing collection system, and the malodorous gas is transported to the biological deodorization device by the gas delivery system after collection. The malodorous gas passes through the wet, porous and active microorganism filter layer in the biological deodorization device, and utilizes the characteristics of microorganisms such as small cell size, large surface area, strong adsorption, and various metabolic types to absorb and degrade the malodorous gas substances, and then decomposes them. into carbon dioxide and water and other non-toxic and low-harm substances. The treated gas reaches the standard and enters the exhaust pipe for discharge.
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Assignee: JIANGSU FANGYANG ENERGY TECHNOLOGY Co.,Ltd. Assignor: JIANGSU FANGYANG WATER Co.,Ltd. Contract record no.: X2024980036675 Denomination of utility model: An industrial wastewater treatment system Granted publication date: 20181002 License type: Common License Record date: 20241216 |