CN101693575A - Ferrate pre-oxidation-bioactivity filter combined water treatment method - Google Patents
Ferrate pre-oxidation-bioactivity filter combined water treatment method Download PDFInfo
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Abstract
本发明提供的是一种高铁酸盐预氧化-生物活性滤池联用水处理方法。首先,投加高铁酸盐对微污染水体进行预氧化,高铁酸盐的投加量控制在0.3-1.5mg/L,预氧化时间为5-30min;经预氧化处理的水,从生物活性滤池顶端流入,底端流出,所述生物活性滤池的上层是活性炭层,活性炭层高度为60-80cm,下层为石英砂层,滤速为6-9m/h。本发明包含了化学氧化、吸附、生物氧化等多种过程,在给水处理中应用可不改变现有工艺流程,不增加大的设备,表现出良好的除有机污染物效能,是一项适合我国国情、可经济低耗地提高饮用水水质的强化常规除污染技术。
The invention provides a ferrate preoxidation-biologically active filter combined water treatment method. First, add ferrate to pre-oxidize the slightly polluted water body. The dosage of ferrate is controlled at 0.3-1.5mg/L, and the pre-oxidation time is 5-30min; The top of the pond flows in, and the bottom flows out. The upper layer of the biologically active filter is an activated carbon layer with a height of 60-80cm, and the lower layer is a quartz sand layer with a filtration rate of 6-9m/h. The invention includes various processes such as chemical oxidation, adsorption, biological oxidation, etc. It can be applied in water supply treatment without changing the existing process flow, without adding large equipment, and showing good efficiency in removing organic pollutants. It is a project suitable for my country's national conditions. , Enhanced conventional pollution removal technology that can improve drinking water quality economically and with low consumption.
Description
(一)技术领域(1) Technical field
本发明涉及的是一种处理方法,是一种适用于老水厂的改造的水处理方法。The invention relates to a treatment method, which is a water treatment method suitable for the transformation of old water plants.
(二)背景技术(2) Background technology
受工业废水和生活污水排放的影响,我国饮用水源水质逐渐恶化。水中的污染成分主要是含有天然有机与无机成分的有机物,其中,许多微量的有机污染物是最难去除的部分,对人体健康危害很大,此外,水中氨氮等污染物含量的增加也严重影响水处理工艺的除污染效能。Affected by the discharge of industrial wastewater and domestic sewage, the quality of drinking water sources in my country has gradually deteriorated. The pollution components in water are mainly organic matter containing natural organic and inorganic components. Among them, many trace organic pollutants are the most difficult to remove, which is very harmful to human health. In addition, the increase in the content of ammonia nitrogen and other pollutants in water also seriously affects Pollution removal efficiency of water treatment processes.
活性炭由于具有发达的孔隙结构,能够有效吸附有机物,目前已广泛应用于饮用水深度处理过程中。但是活性炭吸附容量有限,使用周期短,因此需要经常再生和更换。针对活性炭的弱点,研究人员采用预氧化的方法来改善活性炭的吸附性能。其中,将臭氧氧化与生物活性炭技术进行联用是目前国际上普遍采用的微污染水体的净化方法,即微污染水体先经过臭氧氧化,部分有机物得到初步降解,水中容易被微生物降解的有机物所占比例提高,可生物降解性得到改善,然后再用生物活性炭方法进一步净化。然而臭氧氧化工艺在实际应用中也存在一定的问题:(1)臭氧氧化工艺设备投资大,运行成本相对较高,维护与管理复杂;(2)较高浓度的臭氧对人体会产生危害,臭氧尾气需要严格处理;(3)当原水中含有溴化物时,在臭氧的氧化作用下会形成对人体有害的溴酸盐,溴酸盐被国际癌症研究机构定为2B级(较高致癌可能性)的潜在致癌物,这些不足之处限制了臭氧工艺的应用。Activated carbon has been widely used in the advanced treatment of drinking water due to its well-developed pore structure, which can effectively adsorb organic matter. However, activated carbon has limited adsorption capacity and short service life, so it needs to be regenerated and replaced frequently. Aiming at the weakness of activated carbon, researchers use pre-oxidation method to improve the adsorption performance of activated carbon. Among them, the combination of ozone oxidation and biological activated carbon technology is the purification method of micro-polluted water commonly used in the world at present, that is, the micro-polluted water is firstly oxidized by ozone, and some organic matter is initially degraded, and the organic matter in the water is easily degraded by microorganisms. The ratio is increased, the biodegradability is improved, and then further purified by the bioactivated carbon method. However, there are certain problems in the actual application of the ozone oxidation process: (1) the investment in the ozone oxidation process equipment is large, the operating cost is relatively high, and the maintenance and management are complicated; (2) the high concentration of ozone will cause harm to the human body, and the ozone Exhaust gas needs to be strictly treated; (3) When the raw water contains bromide, it will form bromate harmful to human body under the oxidation of ozone. Bromate is classified as 2B level by the International Agency for Research on Cancer (higher carcinogenic possibility ), these deficiencies limit the application of the ozone process.
高铁酸盐是20世纪70年代以来开发的一种新型水处理剂。与臭氧相比,高铁酸盐是六价铁盐,具有很强的氧化性,特别是在酸性条件下,它的标准氧化还原电位(+2.20V),高于臭氧(+2.07V),是目前用于水和废水处理中氧化性最强的氧化剂。此外,在氧化过程中,高铁酸盐自身被还原成新的物质Fe3+或(Fe(OH)3),产物可进一步水解,具有混凝功效,是一种良好的无机絮凝剂,能高效地去除水中的细小的悬浮物。不仅如此,高铁酸盐在整个水的消毒和净化过程中,不会产生三氯甲烷等任何对人体有害的物质,不会引入有害生物体的二次污染。因此,高铁酸盐作为一种具有强氧化性和混凝作用的双功效绿色新型水处理药剂,引起研究人员的广泛关注。Ferrate is a new type of water treatment agent developed since the 1970s. Compared with ozone, ferrate is a hexavalent iron salt, which has strong oxidizing properties, especially under acidic conditions. Its standard oxidation-reduction potential (+2.20V) is higher than that of ozone (+2.07V), which is The most oxidizing oxidizing agent currently used in water and wastewater treatment. In addition, during the oxidation process, ferrate itself is reduced to a new substance Fe 3+ or (Fe(OH) 3 ), and the product can be further hydrolyzed and has a coagulation effect. It is a good inorganic flocculant and can efficiently Remove fine suspended solids from water. Not only that, during the whole water disinfection and purification process, ferrate will not produce any harmful substances such as chloroform, and will not introduce secondary pollution of harmful organisms. Therefore, ferrate, as a dual-effect green new water treatment agent with strong oxidizing and coagulating effects, has attracted extensive attention of researchers.
与本发明相关的公开报道有:1、“臭氧生物活性炭工艺深度处理微污染原水”(《环境科学与技术》,2009,32(7):125-127);2、“化学预氧化/生物活性炭去除微污染原水中氨氮”(《水处理技术》,2005,31(10):37-39);3、申请号为03107814.1,名称为“高锰酸盐预氧化与生物活性炭联用除污染工艺”的专利文件等。Public reports related to the present invention are: 1, "ozone biological activated carbon process advanced treatment of slightly polluted raw water" ("Environmental Science and Technology", 2009, 32 (7): 125-127); 2, "chemical preoxidation/biological Activated carbon to remove ammonia nitrogen in slightly polluted raw water" ("Water Treatment Technology", 2005, 31(10): 37-39); 3. The application number is 03107814.1, and the name is "Permanganate pre-oxidation and biological activated carbon combined to remove pollution Process" patent documents, etc.
(三)发明内容(3) Contents of the invention
本发明的目的在于提供一种在保证出水安全性的同时,降低整个水处理工艺成本的高铁酸盐预氧化-生物活性滤池联用水处理方法。The purpose of the present invention is to provide a ferrate preoxidation-biologically active filter combined water treatment method that reduces the cost of the entire water treatment process while ensuring the safety of effluent.
本发明的目的是这样实现的:The purpose of the present invention is achieved like this:
首先,投加一定量的高铁酸盐对微污染水体进行预处理,高铁酸盐是在混凝工艺前端投加,可同时起到氧化有机污染物和强化混凝的双重作用,其投加方式可以湿法投加,也可干法直接投加,根据水质污染情况,高铁酸盐的投加量控制在0.3-1.5mg/L,预氧化时间为5-30min,预氧化后投加混凝剂,进行混凝沉淀;First, a certain amount of ferrate is added to pretreat slightly polluted water. Ferrate is added at the front end of the coagulation process, which can simultaneously play the dual role of oxidizing organic pollutants and strengthening coagulation. It can be added by wet method or directly by dry method. According to the water pollution, the dosage of ferrate is controlled at 0.3-1.5mg/L, the pre-oxidation time is 5-30min, and the coagulation is added after pre-oxidation agent for coagulation and sedimentation;
经预氧化处理的沉淀后水,从生物活性滤池顶端流入,底端流出,所述生物活性滤池是由石英砂滤池改造而成,用细颗粒活性炭代替上层的石英砂,活性炭层高度为60-80cm,下层石英砂层保留,其高度为10-40cm。改造后的生物活性滤池对过滤工艺起强化作用。The pre-oxidized precipitated water flows in from the top of the biologically active filter and flows out from the bottom. The biologically active filter is transformed from a quartz sand filter, and the upper layer of quartz sand is replaced by fine-grained activated carbon. The height of the activated carbon layer is It is 60-80cm, and the lower quartz sand layer is reserved, and its height is 10-40cm. The modified bioactive filter strengthens the filtration process.
本发明还可以包括:The present invention may also include:
1、所述活性炭层的活性炭为细颗粒活性炭,其粒度为5-80目。1. The activated carbon in the activated carbon layer is fine granular activated carbon with a particle size of 5-80 mesh.
2、所述活性炭层的活性炭为细颗粒活性炭,其粒度为5-60目。2. The activated carbon in the activated carbon layer is fine granular activated carbon with a particle size of 5-60 mesh.
本发明是以高铁酸盐代替臭氧氧化工艺,与生物活性滤池工艺联用,提供了一种高铁酸盐-生物活性滤池工艺处理微污染水体,在保证出水安全性的同时,降低整个水处理工艺的成本。The present invention replaces the ozone oxidation process with ferrate and combines it with the biologically active filter process to provide a ferrate-biologically active filter process for treating micro-polluted water bodies. The cost of the treatment process.
在本发明中,需要根据原水污染程度,决定是否在生物活性滤池前增加曝气装置,一般认为生物活性炭出水中溶解氧浓度低于2.0mg/L时会影响生物活性炭工艺的去除效果,因此,可以依据生物活性炭滤池出水的溶解氧浓度作为监测指标,来衡量是否需要进行曝气。In the present invention, it is necessary to determine whether to add an aeration device before the biologically active filter according to the pollution degree of the raw water. It is generally believed that the removal effect of the biologically activated carbon process will be affected when the dissolved oxygen concentration in the effluent of the biologically activated carbon is lower than 2.0mg/L, so , the dissolved oxygen concentration in the effluent of the biological activated carbon filter can be used as a monitoring index to measure whether aeration is required.
由于采用上述技术方案,本发明具有如下有益效果:Owing to adopting above-mentioned technical scheme, the present invention has following beneficial effect:
1、高铁酸盐具有强氧化性,可有效分解受污染水体中的污染物质,降低污染物含量。1. Ferrate has strong oxidizing properties, which can effectively decompose the pollutants in the polluted water body and reduce the pollutant content.
2、高铁酸盐在氧化过程中,被还原为Fe3+或(Fe(OH)3),产物进一步水解具有混凝的功效,且没有任何毒副作用,不会对水体产生任何二次污染。2. Ferrate is reduced to Fe 3+ or (Fe(OH) 3 ) during the oxidation process, and the product is further hydrolyzed to have the effect of coagulation, without any toxic side effects, and will not cause any secondary pollution to the water body.
3、高铁酸盐氧化工艺所需装置包括搅拌、投加和计量设备等,装置简单且易于自动化控制。生物活性滤池是在原有砂滤池基础上改造而成,可在保证滤池对浊度去除效果的同时,又可使滤池具有去除氨氮、亚硝酸盐氮和有机物的能力,具有空床接触时间短、占地面积小、处理效率高等优点。因此,高铁酸盐预氧化与生物活性滤池联用技术具有不需要增加大的设备,基建投资少、运行费用低、处理效能高的特点,适合于新水厂的建设和老水厂的改造等特点;3. The equipment required for the ferrate oxidation process includes stirring, dosing and metering equipment, etc. The equipment is simple and easy to automatically control. The bioactive filter is transformed on the basis of the original sand filter, which can not only ensure the effect of the filter on turbidity removal, but also enable the filter to have the ability to remove ammonia nitrogen, nitrite nitrogen and organic matter, and has an empty bed It has the advantages of short contact time, small footprint and high processing efficiency. Therefore, the combination technology of ferrate pre-oxidation and bioactive filter has the characteristics of no need to add large equipment, less capital investment, low operating cost, and high treatment efficiency, and is suitable for the construction of new water plants and the transformation of old water plants Features;
4、该技术适用于不同污染程度的水体处理,效果良好,应用范围广。4. This technology is suitable for the treatment of water bodies with different pollution degrees, with good effect and wide application range.
高铁酸盐预氧化与生物活性滤池联用工艺包含了化学氧化、吸附、生物氧化等多种过程,在给水处理中应用可不改变现有工艺流程,不增加大的设备,表现出良好的除有机污染物效能,是一项适合我国国情、可经济低耗地提高饮用水水质的强化常规除污染技术。The combined process of ferrate pre-oxidation and biological active filter includes chemical oxidation, adsorption, biological oxidation and other processes. It can be used in water treatment without changing the existing process flow and without adding large equipment, showing good removal efficiency. The efficiency of organic pollutants is an enhanced conventional pollution removal technology that is suitable for my country's national conditions and can improve the quality of drinking water economically and with low consumption.
(四)附图说明(4) Description of drawings
图1是本发明的工艺流程图;Fig. 1 is a process flow diagram of the present invention;
图2是生物活性滤池的结构示意图。Figure 2 is a schematic diagram of the structure of a biologically active filter.
(五)具体实施方式(5) Specific implementation methods
下面举例对本发明做更详细地描述:The following examples describe the present invention in more detail:
实施例:以某地表水为实验源水,该水体污染严重,其中典型污染物为氨氮0.8mg/L,CODMn7.5mg/L,嗅味为土腥味(V)。Embodiment: Taking a certain surface water as the source water of the experiment, the water body is seriously polluted, wherein the typical pollutants are ammonia nitrogen 0.8mg/L, COD Mn 7.5mg/L, and the smell is earthy (V).
采用高铁酸盐预氧化-生物活性滤池联用工艺处理该污染水体。The polluted water body was treated by the combination process of ferrate preoxidation and bioactive filter.
首先,在混凝工艺前投加高铁酸盐进行预氧化,其投量为1.0mg/L,干法投加,预氧化时间为30min,预氧化后投加硫酸铝进行混凝,混凝剂投量为25~30mg/L。具体混凝条件为快速搅拌1min,转速为200~300转/min;慢速搅拌10min,转速为60转/min;沉淀时间为30~45min。First, add ferrate for pre-oxidation before the coagulation process, the dosage is 1.0mg/L, dosing in dry method, pre-oxidation time is 30min, after pre-oxidation, add aluminum sulfate for coagulation, coagulant The dosage is 25~30mg/L. The specific coagulation conditions are as follows: fast stirring for 1 min, with a rotation speed of 200-300 rpm; slow stirring for 10 min, with a rotation speed of 60 rpm; and a precipitation time of 30-45 min.
经高铁酸盐氧化处理的沉淀后水,作为生物活性滤池的进水。生物活性滤池是由普通砂滤池改造而成,将上层石英砂用颗粒活性炭1代替,生物活性炭为细颗粒活性炭,其粒度为6-9目,高度为80cm,保留下层石英砂2,其高度为10cm,滤速为6m/h。在生物活性滤池顶部设有曝气装置,以满足生物工艺中微生物对溶解氧的需求量,生物活性滤池反冲洗采用单独水冲洗,滤层膨胀高度为30%。The precipitated water treated by ferrate oxidation is used as the influent of the biologically active filter. The biologically active filter is transformed from an ordinary sand filter. The upper layer of quartz sand is replaced by granular activated
收污染水体经高铁酸盐-生物活性滤池处理后,出水水质满足《生活饮用水卫生标准》要求,其中氨氮0.05mg/L、CODMn1.15mg/L,无嗅味。After the polluted water is treated by the ferrate-biologically active filter, the effluent quality meets the requirements of the "Drinking Water Sanitation Standard", including ammonia nitrogen 0.05mg/L, COD Mn 1.15mg/L, and no smell.
高铁酸盐预氧化和生物活性滤池工艺分别改善了混凝工艺和过滤工艺的除污染效能,同时高铁酸盐预氧化可显著改善后续生物活性滤池的除污染效能,从而提高整体工艺对污染物的去除,提高饮用水水质的安全性。具体表现为:The ferrate pre-oxidation and bioactive filter process improved the decontamination efficiency of the coagulation process and the filtration process respectively, and at the same time, the ferrate pre-oxidation can significantly improve the decontamination performance of the subsequent bioactive filter, thereby improving the pollution of the overall process. The removal of pollutants improves the safety of drinking water quality. The specific performance is:
(1)在高浊度情况下长期运行,会造成活性炭的使用周期缩短,这就要求必须对生物活性炭滤池进水进行一定的预处理。高铁酸盐复合药剂具有强化混凝的功能,能够有效地去除水中大颗粒物质和胶体颗粒,减轻颗粒物对后续生物活性炭工艺的影响。(1) Long-term operation under high turbidity conditions will shorten the service life of activated carbon, which requires certain pretreatment of the influent of the biological activated carbon filter. The ferrate composite agent has the function of strengthening coagulation, which can effectively remove large particles and colloidal particles in water, and reduce the impact of particles on the subsequent biological activated carbon process.
(2)高铁酸盐与生物活性滤池对不同分子量有机物的去除具有协同作用。采用高铁酸盐预氧化能够改善混凝效果,提高混凝工艺对大分子有机物的去除效能;而生物处理单元对小分子有机物有明显去除。从分子量角度而言,高铁酸盐预氧化与生物活性炭联用工艺对有机物的去除具有一定的互补性,这两种工艺的结合有助于不同分子量有机物的去除,提高整个工艺对有机物的去除效率。(2) The ferrate and bioactive filter had a synergistic effect on the removal of organic matter with different molecular weights. The use of ferrate pre-oxidation can improve the coagulation effect and the removal efficiency of the coagulation process for macromolecular organic matter; while the biological treatment unit can significantly remove small molecular organic matter. From the perspective of molecular weight, the combined process of ferrate preoxidation and biological activated carbon has certain complementarity to the removal of organic matter. The combination of these two processes is helpful for the removal of organic matter with different molecular weights and improves the removal efficiency of the whole process for organic matter. .
(3)高铁酸盐预氧化可将部分大分子有机物转化成小分子有机物,提高了原水的可生化性,促进了后续生物活性滤池工艺生物降解效能,有利于提高整体工艺的除污染效能。(3) Ferrate pre-oxidation can convert some macromolecular organic matter into small molecular organic matter, which improves the biodegradability of raw water, promotes the biodegradation efficiency of the subsequent bioactive filter process, and is conducive to improving the pollution removal efficiency of the overall process.
(4)高铁酸盐的氧化还原产物Fe3+是微生物生长所必须的微量元素,能够刺激后续生物活性滤池中微生物的生长,对硝化细菌的活性与数量提高尤为显著,从而强化了生物活性滤池的除氮功能。(4) The redox product of ferrate, Fe 3+ , is a trace element necessary for the growth of microorganisms, which can stimulate the growth of microorganisms in the subsequent bioactive filter, especially significantly increasing the activity and quantity of nitrifying bacteria, thus strengthening the biological activity The nitrogen removal function of the filter.
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Cited By (9)
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CN101898857A (en) * | 2010-08-19 | 2010-12-01 | 西安建筑科技大学 | A method for retaining and deactivating aquatic organisms in a biological activated carbon filter |
CN102583879A (en) * | 2012-01-16 | 2012-07-18 | 宁波工程学院 | High-concentration integrated chemical organic wastewater treatment process |
CN103501906A (en) * | 2010-12-15 | 2014-01-08 | 高铁酸盐处理技术有限责任公司 | Methods and devices for measuring the concentration of an additive |
CN106045001A (en) * | 2016-07-08 | 2016-10-26 | 常州大学 | Method for jointly treating rhodamine B wastewater through potassium ferrate and activated carbon |
CN108178457A (en) * | 2018-02-08 | 2018-06-19 | 深圳市深水宝安水务集团有限公司 | The middle-size and small-size water factory's short route depth-averaged model system and remodeling method of common process |
CN108383236A (en) * | 2018-03-30 | 2018-08-10 | 哈尔滨工业大学 | A method of microorganism flco is activated to improve cohesion and dephosphorization performance using ferrate |
CN110642459A (en) * | 2019-09-19 | 2020-01-03 | 济南大学 | Combined pollution-removing process of ferrate and A/O biological filter |
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2009
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
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CN101898857A (en) * | 2010-08-19 | 2010-12-01 | 西安建筑科技大学 | A method for retaining and deactivating aquatic organisms in a biological activated carbon filter |
CN103501906A (en) * | 2010-12-15 | 2014-01-08 | 高铁酸盐处理技术有限责任公司 | Methods and devices for measuring the concentration of an additive |
CN102583879A (en) * | 2012-01-16 | 2012-07-18 | 宁波工程学院 | High-concentration integrated chemical organic wastewater treatment process |
CN106045001A (en) * | 2016-07-08 | 2016-10-26 | 常州大学 | Method for jointly treating rhodamine B wastewater through potassium ferrate and activated carbon |
CN108178457A (en) * | 2018-02-08 | 2018-06-19 | 深圳市深水宝安水务集团有限公司 | The middle-size and small-size water factory's short route depth-averaged model system and remodeling method of common process |
CN108383236A (en) * | 2018-03-30 | 2018-08-10 | 哈尔滨工业大学 | A method of microorganism flco is activated to improve cohesion and dephosphorization performance using ferrate |
CN108383236B (en) * | 2018-03-30 | 2022-02-11 | 哈尔滨工业大学 | A method for using ferrate to activate microbial flocs to improve coagulation and dephosphorization performance |
CN110642459A (en) * | 2019-09-19 | 2020-01-03 | 济南大学 | Combined pollution-removing process of ferrate and A/O biological filter |
CN110642460A (en) * | 2019-09-19 | 2020-01-03 | 济南大学 | Method for removing nitrogen and phosphorus by ferrate enhanced denitrification phosphorus removal biological filter |
CN118420173A (en) * | 2024-05-20 | 2024-08-02 | 华南理工大学 | Potassium permanganate catalytic oxidation-biological activated carbon water supply deep treatment method and filter tank |
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