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CN107162334B - Method for removing organic matters in micro-polluted source water based on biological purification filter column - Google Patents

Method for removing organic matters in micro-polluted source water based on biological purification filter column Download PDF

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CN107162334B
CN107162334B CN201710473896.9A CN201710473896A CN107162334B CN 107162334 B CN107162334 B CN 107162334B CN 201710473896 A CN201710473896 A CN 201710473896A CN 107162334 B CN107162334 B CN 107162334B
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CN107162334A (en
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程庆锋
黄杨
能子礼超
唐晓茹
李�瑞
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Chengdu University of Information Technology
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/001Processes for the treatment of water whereby the filtration technique is of importance
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • C02F2101/206Manganese or manganese compounds
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F2101/30Organic compounds
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2201/00Apparatus for treatment of water, waste water or sewage
    • C02F2201/002Construction details of the apparatus
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2301/00General aspects of water treatment
    • C02F2301/08Multistage treatments, e.g. repetition of the same process step under different conditions
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    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/34Biological treatment of water, waste water, or sewage characterised by the microorganisms used

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Abstract

一种基于生物净化滤柱的去除微污染水源水中有机物的方法,去除微污染水源水中有机物的方法,本发明是要解决现有的采用生物法去除微污染水源水中的有机物的方法的去除率低的技术问题。本方法:一:生物净化滤柱系统的搭建;二、在生物净化滤柱中培养降解有机物的异养微生物以及催化氧化锰的锰氧化菌;三、生物净化滤柱系统的运行。本发明去除微污染水源水中有机物时的去除效率高,实现了水源水中有机物的高效稳定去除,出水中的有机物明显低于国家饮用水标准,有利于实际工程应用。

Figure 201710473896

A method for removing organic matter in micro-polluted water source water based on a biological purification filter column, and a method for removing organic matter in micro-polluted water source water. technical issues. The method includes: 1. construction of a biological purification filter column system; 2. culturing heterotrophic microorganisms that degrade organic matter and manganese oxidizing bacteria that catalyze manganese oxidation in the biological purification filter column; 3. operation of the biological purification filter column system. The invention has high removal efficiency when removing organic matter in slightly polluted water source water, realizes efficient and stable removal of organic matter in water source water, and the organic matter in effluent is obviously lower than the national drinking water standard, which is beneficial to practical engineering application.

Figure 201710473896

Description

一种基于生物净化滤柱的去除微污染水源水中有机物的方法A method for removing organic matter in slightly polluted water source water based on biological purification filter column

技术领域technical field

本发明涉及去除微污染水源水中有机物的方法,属于饮用水处理领域。The invention relates to a method for removing organic matter in slightly polluted water source water, and belongs to the field of drinking water treatment.

背景技术Background technique

水是人类生存和生产活动中不可缺少的资源。随着人口的迅速增长,经济的快速发展以及人们生活水平的不断提高,人类对水资源的需求量逐渐增多。然而随着工农业生产过程中,大量农药、化肥的使用,以及生活污水、工业“三废”等没有经过严格处理后排放,水源水中检测到的有机污染物日益增多,包括农药、化工原料、药物、个人护理品和内分泌干扰物等。其中,许多污染物的浓度虽然较低,但是难以生物降解,并且危害极大。卫生部2006年颁布的《生活饮用水卫生标准》中关于有机污染的毒理指标已经增加到了53项。如何高效去除微污染水源水中的微量有机污染物成为当前饮用水处理中的热点问题。Water is an indispensable resource for human survival and production activities. With the rapid growth of the population, the rapid development of the economy and the continuous improvement of people's living standards, the demand for water resources is gradually increasing. However, with the use of a large number of pesticides and fertilizers in the process of industrial and agricultural production, and the discharge of domestic sewage and industrial "three wastes" without strict treatment, the organic pollutants detected in the water source water are increasing day by day, including pesticides, chemical raw materials, drugs, etc. Personal care products and endocrine disruptors, etc. Among them, although the concentration of many pollutants is low, they are difficult to biodegrade and are extremely harmful. The number of toxicological indicators on organic pollution in the "Sanitation Standards for Drinking Water" promulgated by the Ministry of Health in 2006 has increased to 53 items. How to efficiently remove trace organic pollutants in slightly polluted water source water has become a hot issue in drinking water treatment.

现有的采用生物法去除微污染水源水中的有机物的方法工艺流程简单、运行稳定、投资费用少、占地面积小,但是去除效果不够理想。The existing biological method for removing organic matter in slightly polluted water source water has the advantages of simple process flow, stable operation, low investment cost and small footprint, but the removal effect is not ideal.

发明内容SUMMARY OF THE INVENTION

本发明是要解决现有的采用生物法去除微污染水源水中的有机物的方法的去除率低的技术问题,而提供一种基于生物净化滤柱的去除微污染水源水中有机物的方法。The present invention aims to solve the technical problem of low removal rate of the existing biological method for removing organic matter in micro-polluted water source water, and provides a method for removing organic matter in micro-polluted water source water based on a biological purification filter column.

本发明的基于生物净化滤柱的去除微污染水源水中有机物的方法,按以下步骤进行:The method for removing organic matter in the micro-polluted water source water based on the biological purification filter column of the present invention is carried out according to the following steps:

一、生物净化滤柱系统的搭建:生物净化滤柱系统由滤柱、第一水箱、第二水箱、第三水箱、第一水泵、第二水泵、第三水泵和混合器组成,滤柱内的下部为承托层,在承托层之上为滤料层,在滤柱1的上端设置溢流口,在滤柱的底部设置出水口,在滤柱的侧壁设置取样口;第一水箱与混合器之间的管路上设置第一水泵,第二水箱与混合器之间的管路上设置第二水泵,第三水箱与混合器之间的管路上设置第三水泵,混合器设置在滤柱顶部;1. Construction of the biological purification filter column system: The biological purification filter column system consists of a filter column, a first water tank, a second water tank, a third water tank, a first water pump, a second water pump, a third water pump and a mixer. The lower part of the filter column is a supporting layer, above the supporting layer is a filter material layer, an overflow port is set at the upper end of the filter column 1, a water outlet is set at the bottom of the filter column, and a sampling port is set on the side wall of the filter column; A first water pump is arranged on the pipeline between the water tank and the mixer, a second water pump is arranged on the pipeline between the second water tank and the mixer, and a third water pump is arranged on the pipeline between the third water tank and the mixer, and the mixer is arranged in the the top of the filter column;

二、生物净化滤柱系统的启动:Second, the start of the biological purification filter column system:

a、将第一水箱内注入自来水、第二水箱注入接种异养菌的河水;通过第一水泵和第二水泵将自来水、接种异养菌的河水按体积比为(5~6):1注入混合器中混合,混合后流入滤柱中,控制滤速为4~5m/h,最后从滤柱1底部的出水口排出;当出水中COD的去除率大于40%后,完成第一阶段的启动;a. Inject tap water into the first water tank, and inject the river water inoculated with heterotrophic bacteria into the second water tank; inject the tap water and the river water inoculated with heterotrophic bacteria in a volume ratio of (5 to 6): 1 through the first water pump and the second water pump Mix in the mixer, flow into the filter column after mixing, control the filtration rate to be 4-5m/h, and finally discharge from the water outlet at the bottom of the filter column 1; when the removal rate of COD in the effluent is greater than 40%, the first stage is completed. start up;

b、将第一水箱内注入自来水、第二水箱注入接种锰氧化菌的河水,第三水箱注入硫酸锰溶液,通过第一水泵、第二水泵和第三水泵将自来水、接种锰氧化菌的河水和硫酸锰溶液注入混合器中混合,其中混合液中硫酸锰溶液的浓度为0.5~0.6mg/L,混合液流入滤柱中,控制滤速为4~5m/h,最后从滤柱底部的出水口排出;当锰离子的去除率大于90%后,将混合液中硫酸锰溶液的浓度提高至1.0~1.1mg/L,再运行至锰离子的去除率大于90%后,再将混合液中硫酸锰溶液的浓度提高至1.8~2mg/L,再运行至锰离子的去除率大于90%,完成第二阶段的启动;b. The first water tank is filled with tap water, the second water tank is injected with the river water inoculated with manganese oxidizing bacteria, the third water tank is injected with manganese sulfate solution, and the tap water and the river water inoculated with manganese oxidizing bacteria are injected into the first water pump, the second water pump and the third water pump by the first water pump, the second water pump and the third water pump It is mixed with manganese sulfate solution into the mixer, wherein the concentration of manganese sulfate solution in the mixed solution is 0.5~0.6mg/L, the mixed solution flows into the filter column, and the filtration rate is controlled to be 4~5m/h. Discharge from the water outlet; when the removal rate of manganese ions is greater than 90%, increase the concentration of manganese sulfate solution in the mixed solution to 1.0-1.1 mg/L, and then run until the removal rate of manganese ions is greater than 90%, and then add The concentration of the medium manganese sulfate solution is increased to 1.8-2 mg/L, and then the operation is carried out until the removal rate of manganese ions is greater than 90%, and the start-up of the second stage is completed;

三、生物净化滤柱系统的运行:3. Operation of the biological purification filter column system:

通过第一水泵将第一水箱内的待处理的微污染水源水通入混合器,第二水泵和第三水泵停止工作,水流入到滤柱中,控制滤速为4~5m/h,最后从滤柱底部的出水口排出,完成微污染水源水的处理。The micro-polluted water source water to be treated in the first water tank is passed into the mixer through the first water pump, the second water pump and the third water pump stop working, the water flows into the filter column, and the filtration speed is controlled to be 4-5m/h, and finally It is discharged from the water outlet at the bottom of the filter column to complete the treatment of the slightly polluted water source water.

本发明的方法在生物净化滤柱中实现了生物锰氧化物对有机物的催化氧化,以及异养菌对有机物的生物氧化,从而提高了有机物的去除效果。采用生物净化滤柱去除水体中的锰时,水中的二价锰被滤料上的生物锰氧化物吸附、氧化成高价的生物锰氧化物。而该生物锰氧化物的颗粒粒径在纳米级别,具有较大的比表面积,是氧化能力很强的一种氧化性成分,它对微量有机物的迁移转化起到重要的作用。生物锰氧化物催化氧化有机物后其自身被还原成锰离子,产生的锰离子仍可以被锰氧化菌氧化至锰氧化物,从而可以对有机物进行持续有效的降解,而有机物的氧化产物也可以被微生物利用进行进一步的代谢降解。因此采用生物净化滤柱同步去除有机物、锰时,其滤料上会生成大量的生物锰氧化物,充分利用这些生物锰氧化物的催化氧化能力,并结合生物净化滤柱中微生物对有机物的生物氧化,将大幅提高微污染水源水中有机物的去除效果。The method of the invention realizes the catalytic oxidation of the organic matter by the biological manganese oxide and the biological oxidation of the organic matter by the heterotrophic bacteria in the biological purification filter column, thereby improving the removal effect of the organic matter. When the biological purification filter column is used to remove manganese in the water body, the divalent manganese in the water is adsorbed by the biological manganese oxides on the filter material and oxidized into high-priced biological manganese oxides. The particle size of the biological manganese oxide is at the nanometer level and has a large specific surface area. It is an oxidizing component with strong oxidizing ability, and it plays an important role in the migration and transformation of trace organic matter. After the biological manganese oxide catalyzes the oxidation of organic matter, it is itself reduced to manganese ions, and the generated manganese ions can still be oxidized to manganese oxides by manganese oxidizing bacteria, so that organic matter can be degraded continuously and effectively, and the oxidation products of organic matter can also be oxidized. Microorganisms utilize for further metabolic degradation. Therefore, when the biological purification filter column is used to remove organic matter and manganese synchronously, a large amount of biological manganese oxides will be generated on the filter material, and the catalytic oxidation ability of these biological manganese oxides will be fully utilized. Oxidation will greatly improve the removal effect of organic matter in slightly polluted water source water.

本发明去除微污染水源水中有机物时的去除效率高,实现了水源水中有机物的高效稳定去除,出水中的有机物明显低于国家饮用水标准,有利于实际工程应用。The invention has high removal efficiency when removing organic matter in slightly polluted water source water, realizes efficient and stable removal of organic matter in water source water, and the organic matter in effluent is obviously lower than the national drinking water standard, which is beneficial to practical engineering applications.

附图说明Description of drawings

图1是本发明的生物净化滤柱系统的示意图;生物净化滤柱系统的搭建:生物净化滤柱系统由1为滤柱、2为第一水箱、3为第二水箱、4为第三水箱、5为第一水泵、6为第二水泵、7为第三水泵,8为混合器,9为流量计;1-1为承托层1-1,滤1-2为料层,1-3为溢流口,1-4为出水口,1-5为取样口;Fig. 1 is the schematic diagram of the biological purification filter column system of the present invention; the construction of the biological purification filter column system: the biological purification filter column system is composed of 1 as the filter column, 2 as the first water tank, 3 as the second water tank, and 4 as the third water tank , 5 is the first water pump, 6 is the second water pump, 7 is the third water pump, 8 is the mixer, 9 is the flow meter; 1-1 is the supporting layer 1-1, the filter 1-2 is the material layer, 1- 3 is the overflow port, 1-4 is the water outlet, and 1-5 is the sampling port;

图2是试验1中第一启动阶段的有机物的去除效果图;Fig. 2 is the removal effect diagram of organic matter in the first start-up stage in test 1;

图3是试验1中第二启动阶段的有机物的去除效果图Figure 3 is a diagram of the removal effect of organic matter in the second start-up stage in Experiment 1

图4是试验1中第二启动阶段的锰的去除效果图。FIG. 4 is a graph showing the removal effect of manganese in the second start-up stage in Experiment 1. FIG.

具体实施方式Detailed ways

具体实施方式一:本实施方式的基于生物净化滤柱的去除微污染水源水中有机物的方法,按以下步骤进行:Embodiment 1: The method for removing organic matter in micro-polluted water source water based on a biological purification filter column of the present embodiment is carried out according to the following steps:

一、生物净化滤柱系统的搭建:生物净化滤柱系统由滤柱1、第一水箱2、第二水箱3、第三水箱4、第一水泵5、第二水泵6、第三水泵7和混合器8组成,滤柱1内的下部为承托层1-1,在承托层之上为滤料层1-2,在滤柱1的上端设置溢流口1-3,在滤柱1的底部设置出水口1-4,在滤柱1的侧壁设置取样口1-5;第一水箱2与混合器8之间的管路上设置第一水泵5,第二水箱3与混合器8之间的管路上设置第二水泵6,第三水箱4与混合器8之间的管路上设置第三水泵7,混合器8设置在滤柱1顶部;1. Construction of biological purification filter column system: The biological purification filter column system consists of filter column 1, first water tank 2, second water tank 3, third water tank 4, first water pump 5, second water pump 6, third water pump 7 and The mixer 8 is composed, the lower part in the filter column 1 is the supporting layer 1-1, the above the supporting layer is the filter material layer 1-2, the upper end of the filter column 1 is provided with an overflow port 1-3, The bottom of 1 is provided with water outlet 1-4, and the side wall of filter column 1 is provided with sampling port 1-5; the pipeline between the first water tank 2 and the mixer 8 is provided with the first water pump 5, the second water tank 3 and the mixer A second water pump 6 is arranged on the pipeline between 8, and a third water pump 7 is arranged on the pipeline between the third water tank 4 and the mixer 8, and the mixer 8 is arranged on the top of the filter column 1;

二、生物净化滤柱系统的启动:Second, the start of the biological purification filter column system:

a、将第一水箱2内注入自来水、第二水箱3注入接种异养菌的河水;通过第一水泵5和第二水泵6将自来水、接种异养菌的河水按体积比为(5~6):1注入混合器8中混合,混合后流入滤柱1中,控制滤速为4~5m/h,最后从滤柱1底部的出水口1-4排出;当出水中COD的去除率大于40%后,完成第一阶段的启动;A, the first water tank 2 is injected with tap water, the second water tank 3 is injected into the river water inoculated with heterotrophic bacteria; by the first water pump 5 and the second water pump 6, tap water, the river water inoculated with heterotrophic bacteria are (5~6 ): 1 is injected into the mixer 8 and mixed, and after mixing, it flows into the filter column 1, and the filtration rate is controlled to be 4-5m/h, and finally discharged from the water outlet 1-4 at the bottom of the filter column 1; when the removal rate of COD in the effluent is greater than After 40%, complete the first phase of startup;

b、将第一水箱2内注入自来水、第二水箱3注入接种锰氧化菌的河水,第三水箱4注入硫酸锰溶液,通过第一水泵5、第二水泵6和第三水泵7将自来水、接种锰氧化菌的河水和硫酸锰溶液注入混合器8中混合,得到的混合液中硫酸锰的浓度为0.5~0.6mg/L,混合液流入滤柱1中,控制滤速为4~5m/h,最后从滤柱1底部的出水口1-4排出;当锰离子的去除率大于90%后,将混合液中硫酸锰的浓度提高至1.0~1.1mg/L,再运行至锰离子的去除率大于90%后,再将混合液中硫酸锰的浓度提高至1.8~2mg/L,再运行至锰离子的去除率大于90%,完成第二阶段的启动;b, the first water tank 2 is injected with tap water, the second water tank 3 is injected into the river water inoculated with manganese oxidizing bacteria, the third water tank 4 is injected with manganese sulfate solution, and the tap water, The river water inoculated with manganese oxidizing bacteria and manganese sulfate solution are injected into mixer 8 and mixed, the concentration of manganese sulfate in the obtained mixed solution is 0.5~0.6mg/L, and the mixed solution flows into filter column 1, and the control filtration rate is 4~5m/L. h, and finally discharged from the water outlet 1-4 at the bottom of the filter column 1; when the removal rate of manganese ions is greater than 90%, increase the concentration of manganese sulfate in the mixed solution to 1.0-1.1 mg/L, and then run to the level of manganese ions. After the removal rate is greater than 90%, the concentration of manganese sulfate in the mixed solution is increased to 1.8-2 mg/L, and then the operation is carried out until the removal rate of manganese ions is greater than 90%, and the start-up of the second stage is completed;

三、生物净化滤柱系统的运行:3. Operation of the biological purification filter column system:

将待处理的微污染水源水注入第一水箱2内通,通过第一水泵5将第一水箱2内的待处理的微污染水源水通入混合器,第二水泵6和第三水泵7停止工作,水流入到滤柱1中,控制滤速为4~5m/h,最后从滤柱1底部的出水口1-4排出,完成微污染水源水的处理。The micro-polluted water source water to be treated is injected into the first water tank 2, and the micro-polluted water source water to be treated in the first water tank 2 is passed into the mixer through the first water pump 5, and the second water pump 6 and the third water pump 7 are stopped. Work, the water flows into the filter column 1, the filtration rate is controlled to be 4-5m/h, and finally discharged from the water outlet 1-4 at the bottom of the filter column 1 to complete the treatment of the slightly polluted water source water.

具体实施方式二:本实施方式与具体实施方式一不同的是步骤一中承托层1-1由石粒辅成,石粒粒径为30~50mm;其它与具体实施方式一相同。Embodiment 2: The difference between this embodiment and Embodiment 1 is that in Step 1, the supporting layer 1-1 is supplemented by stone particles, and the particle size of the stone particles is 30-50 mm; the others are the same as Embodiment 1.

具体实施方式三:本实施方式与具体实施方式一或二不同的是步骤一中滤料层1-2为石英砂,石英砂粒径为10~20mm;其它与具体实施方式一或二相同。Embodiment 3: The difference between this embodiment and Embodiment 1 or 2 is that in step 1, the filter material layer 1-2 is quartz sand, and the particle size of the quartz sand is 10-20 mm; others are the same as Embodiment 1 or 2.

具体实施方式四:本实施方式与具体实施方式一至三之一不同的是步骤一中滤料层1-2厚度为1.5~2m;其它与具体实施方式一至三之一相同。Embodiment 4: The difference between this embodiment and one of Embodiments 1 to 3 is that the thickness of the filter material layer 1-2 in step 1 is 1.5-2 m; the other is the same as that of Embodiment 1 to 3.

具体实施方式五:本实施方式与具体实施方式一至四之一不同的是步骤二中滤速为4.5m/h;其它与具体实施方式一至四之一相同。Embodiment 5: The difference between this embodiment and one of Embodiments 1 to 4 is that the filtration rate in step 2 is 4.5 m/h; the others are the same as those of Embodiment 1 to 4.

具体实施方式六:本实施方式与具体实施方式一至五之一不同的是步骤三中滤速为4.5m/h;其它与具体实施方式一至五之一相同。Embodiment 6: The difference between this embodiment and one of Embodiments 1 to 5 is that the filtration rate in step 3 is 4.5 m/h; the others are the same as those of Embodiment 1 to 5.

用以下试验验证本发明的有益效果:Verify the beneficial effects of the present invention with the following tests:

试验1:本试验的基于生物净化滤柱的去除微污染水源水中有机物的方法,按以下步骤进行:Test 1: The method of removing organic matter in slightly polluted water source water based on biological purification filter column in this test is carried out according to the following steps:

一、生物净化滤柱系统的搭建:生物净化滤柱系统由滤柱1、第一水箱2、第二水箱3、第三水箱4、第一水泵5、第二水泵6、第三水泵7和混合器8组成,滤柱1内的下部为承托层1-1,承托层1-1由粒径为30~50mm的石粒辅成,在承托层之上为滤料层1-2,滤料层1-2为粒径为10~20mm的石英砂,其厚度为1.5m;在滤柱1的上端设置溢流口1-3,在滤柱1的底部设置出水口1-4,在滤柱1的侧壁设置取样口1-5;第一水箱2与混合器8之间的管路上设置第一水泵5,第二水箱3与混合器8之间的管路上设置第二水泵6,第三水箱4与混合器8之间的管路上设置第三水泵7,混合器8设置在滤柱1顶部;1. Construction of biological purification filter column system: The biological purification filter column system consists of filter column 1, first water tank 2, second water tank 3, third water tank 4, first water pump 5, second water pump 6, third water pump 7 and The mixer 8 is composed, the lower part of the filter column 1 is a supporting layer 1-1, the supporting layer 1-1 is supplemented by stone particles with a particle size of 30-50 mm, and above the supporting layer is a filter material layer 1-1 2. The filter material layer 1-2 is quartz sand with a particle size of 10-20mm, and its thickness is 1.5m; an overflow port 1-3 is set at the upper end of the filter column 1, and a water outlet 1-3 is set at the bottom of the filter column 1. 4. Sampling ports 1-5 are set on the side wall of the filter column 1; the first water pump 5 is set on the pipeline between the first water tank 2 and the mixer 8, and the second water tank 3 and the mixer 8 on the pipeline Two water pumps 6, a third water pump 7 is arranged on the pipeline between the third water tank 4 and the mixer 8, and the mixer 8 is arranged on the top of the filter column 1;

二、生物净化滤柱系统的启动:Second, the start of the biological purification filter column system:

a、将第一水箱2内注入自来水、第二水箱3注入接种异养菌的河水;通过第一水泵5和第二水泵6将自来水、接种异养菌的河水按体积比为5:1注入混合器8中混合,混合后流入滤柱1中,控制滤速为4m/h,最后从滤柱1底部的出水口1-4排出;当出水中COD的去除率大于40%后,完成第一阶段的启动;在此过程中有机物的去除效果如图2所示;a, the first water tank 2 is injected with tap water, the second water tank 3 is injected into the river water inoculated with heterotrophic bacteria; the tap water and the inoculated river water with heterotrophic bacteria are injected by the first water pump 5 and the second water pump 6 in a volume ratio of 5:1 Mix in mixer 8, flow into filter column 1 after mixing, control the filtration rate to 4m/h, and finally discharge from water outlet 1-4 at the bottom of filter column 1; when the removal rate of COD in the effluent is greater than 40%, complete the first step. One-stage startup; the removal effect of organic matter during this process is shown in Figure 2;

b、将第一水箱2内注入自来水、第二水箱3注入接种锰氧化菌的河水,第三水箱4注入硫酸锰溶液,通过第一水泵5、第二水泵6和第三水泵7将自来水、接种锰氧化菌的河水和硫酸锰溶液注入混合器8中混合,得到的混合液中硫酸锰的浓度为0.5mg/L,混合液流入滤柱1中,控制滤速为4m/h,最后从滤柱1底部的出水口1-4排出;当锰离子的去除率大于90%后,将混合液中硫酸锰的浓度提高至1.0mg/L,再运行至锰离子的去除率大于90%后,再将混合液中硫酸锰的浓度提高至2mg/L,再运行至锰离子的去除率大于90%,完成第二阶段的启动;在此过程中有机物的去除效果如图3所示,锰的去除效果如图4所示。b, the first water tank 2 is injected with tap water, the second water tank 3 is injected into the river water inoculated with manganese oxidizing bacteria, the third water tank 4 is injected with manganese sulfate solution, and the tap water, The river water inoculated with manganese oxidizing bacteria and manganese sulfate solution are injected into mixer 8 and mixed, the concentration of manganese sulfate in the obtained mixed solution is 0.5mg/L, and the mixed solution flows into filter column 1, and the control filtration rate is 4m/h, and finally from The water outlet 1-4 at the bottom of the filter column 1 is discharged; when the removal rate of manganese ions is greater than 90%, the concentration of manganese sulfate in the mixed solution is increased to 1.0mg/L, and then run until the removal rate of manganese ions is greater than 90%. , and then increase the concentration of manganese sulfate in the mixed solution to 2 mg/L, and then run until the removal rate of manganese ions is greater than 90% to complete the start-up of the second stage; in this process, the removal effect of organic matter is shown in Figure 3. The removal effect is shown in Figure 4.

三、生物净化滤柱系统的运行:3. Operation of the biological purification filter column system:

将待处理的微污染水源水注入第一水箱2内,再通过第一水泵5将第一水箱2内的待处理的微污染水源水通入混合器,其中微污染水源水的COD的浓度为5~8mg/L,第二水泵6和第三水泵7停止工作,水流入到滤柱1中,控制滤速为4m/h,最后从滤柱1底部的出水口1-4排出,出水中有机物的浓度逐步降到2.8mg/L~2.6mg/L,完成微污染水源水的处理。The micro-polluted water source water to be treated is injected into the first water tank 2, and then the micro-polluted water source water to be treated in the first water tank 2 is passed into the mixer through the first water pump 5, wherein the COD concentration of the micro-polluted water source water is 5 ~ 8mg/L, the second water pump 6 and the third water pump 7 stop working, the water flows into the filter column 1, and the filtration rate is controlled to be 4m/h, and finally it is discharged from the water outlet 1-4 at the bottom of the filter column 1, and the water is discharged. The concentration of organic matter is gradually reduced to 2.8mg/L ~ 2.6mg/L, and the treatment of slightly polluted water source water is completed.

对于微污染水源水,本试验的生物净化滤柱系统对于其中有机物的去除率为44%~67%。本试验的方法,实现了微污染水源水中的有机物的高效稳定去除。For the slightly polluted water source water, the biological purification filter column system in this experiment has a removal rate of 44% to 67% for the organic matter in it. The method of this experiment realizes the efficient and stable removal of organic matter in slightly polluted water source water.

Claims (6)

1.一种基于生物净化滤柱的去除微污染水源水中有机物的方法,其特征在于该方法按以下步骤进行:1. a method for removing organic matter in slightly polluted water source water based on biological purification filter column, is characterized in that this method is carried out according to the following steps: 一、生物净化滤柱系统的搭建:生物净化滤柱系统由滤柱(1)、第一水箱(2)、第二水箱(3)、第三水箱(4)、第一水泵(5)、第二水泵(6)、第三水泵(7)和混合器(8)组成,滤柱(1)内的下部为承托层(1-1),在承托层之上为滤料层(1-2),在滤柱(1)的上端设置溢流口(1-3),在滤柱(1)的底部设置出水口(1-4),在滤柱(1)的侧壁设置取样口(1-5);第一水箱(2)与混合器(8)之间的管路上设置第一水泵(5),第二水箱(3)与混合器(8)之间的管路上设置第二水泵(6),第三水箱(4)与混合器(8)之间的管路上设置第三水泵(7),混合器(8)设置在滤柱(1)顶部;1. Construction of the biological purification filter column system: The biological purification filter column system consists of a filter column (1), a first water tank (2), a second water tank (3), a third water tank (4), a first water pump (5), The second water pump (6), the third water pump (7) and the mixer (8) are composed, the lower part of the filter column (1) is a supporting layer (1-1), and above the supporting layer is a filter material layer (1-1). 1-2), an overflow port (1-3) is set at the upper end of the filter column (1), a water outlet (1-4) is set at the bottom of the filter column (1), and a side wall of the filter column (1) is set Sampling ports (1-5); a first water pump (5) is arranged on the pipeline between the first water tank (2) and the mixer (8), and a first water pump (5) is arranged on the pipeline between the second water tank (3) and the mixer (8) A second water pump (6) is arranged, a third water pump (7) is arranged on the pipeline between the third water tank (4) and the mixer (8), and the mixer (8) is arranged on the top of the filter column (1); 二、生物净化滤柱系统的启动:Second, the start of the biological purification filter column system: a、将第一水箱(2)内注入自来水、第二水箱(3)注入接种异养菌的河水;通过第一水泵(5)和第二水泵(6)将自来水、接种异养菌的河水按体积比为(5~6):1注入混合器(8)中混合,混合后流入滤柱(1)中,控制滤速为4~5m/h,最后从滤柱(1)底部的出水口(1-4)排出;当出水中COD的去除率大于40%后,完成第一阶段的启动;a. Inject tap water into the first water tank (2) and the river water inoculated with heterotrophic bacteria in the second water tank (3); According to the volume ratio of (5-6): 1, it is injected into the mixer (8) and mixed, and after mixing, it flows into the filter column (1), and the filtration rate is controlled to be 4-5m/h, and finally the outlet from the bottom of the filter column (1) The water outlet (1-4) is discharged; when the removal rate of COD in the effluent is greater than 40%, the start-up of the first stage is completed; b、将第一水箱(2)内注入自来水、第二水箱(3)注入接种锰氧化菌的河水,第三水箱(4)注入硫酸锰溶液,通过第一水泵(5)、第二水泵(6)和第三水泵(7)将自来水、接种锰氧化菌的河水和硫酸锰溶液注入混合器(8)中混合,得到的混合液中硫酸锰的浓度为0.5~0.6mg/L,混合液流入滤柱(1)中,控制滤速为4~5m/h,最后从滤柱(1)底部的出水口(1-4)排出;当锰离子的去除率大于90%后,将混合液中硫酸锰的浓度提高至1.0~1.1mg/L,再运行至锰离子的去除率大于90%后,再将混合液中硫酸锰的浓度提高至1.8~2mg/L,再运行至锰离子的去除率大于90%,完成第二阶段的启动;b. Inject tap water into the first water tank (2), river water inoculated with manganese oxidizing bacteria in the second water tank (3), and manganese sulfate solution in the third water tank (4), through the first water pump (5), the second water pump ( 6) with the third water pump (7), tap water, the river water inoculated with manganese oxidizing bacteria and the manganese sulfate solution are injected into the mixer (8) and mixed, and the concentration of manganese sulfate in the obtained mixed solution is 0.5~0.6mg/L, and the mixed solution Flow into the filter column (1), control the filtration rate to be 4-5m/h, and finally discharge from the water outlet (1-4) at the bottom of the filter column (1); when the removal rate of manganese ions is greater than 90%, the mixed solution The concentration of manganese sulfate in the mixed solution is increased to 1.0-1.1mg/L, and then the operation is carried out until the removal rate of manganese ions is greater than 90%. The removal rate is greater than 90%, and the start-up of the second stage is completed; 三、生物净化滤柱系统的运行:3. Operation of the biological purification filter column system: 将待处理的微污染水源水注入第一水箱(2)内,通过第一水泵(5)将第一水箱(2)内的待处理的微污染水源水通入混合器,第二水泵(6)和第三水泵(7)停止工作,水流入到滤柱(1)中,控制滤速为4~5m/h,最后从滤柱(1)底部的出水口(1-4)排出,完成微污染水源水的处理。The micro-polluted water source water to be treated is injected into the first water tank (2), the micro-polluted water source water to be treated in the first water tank (2) is fed into the mixer through the first water pump (5), and the second water pump (6) ) and the third water pump (7) stop working, the water flows into the filter column (1), the filtration speed is controlled to be 4-5m/h, and finally it is discharged from the water outlet (1-4) at the bottom of the filter column (1), and the completion is completed. Treatment of slightly polluted water source water. 2.根据权利要求1所述的一种基于生物净化滤柱的去除微污染水源水中有机物的方法,其特征在于步骤一中承托层(1-1)由石粒辅成,石粒粒径为30~50mm。2. a kind of method for removing organic matter in micro-polluted water source water based on biological purification filter column according to claim 1, is characterized in that in step 1, the supporting layer (1-1) is assisted by stone particles, and the stone particle diameter 30 to 50mm. 3.根据权利要求1或2所述的一种基于生物净化滤柱的去除微污染水源水中有机物的方法,其特征在于步骤一中滤料层(1-2)为石英砂,石英砂粒径为10~20mm。3. a kind of method for removing organic matter in micro-polluted water source water based on biological purification filter column according to claim 1 and 2, is characterized in that in step 1, filter material layer (1-2) is quartz sand, and quartz sand particle size 10 to 20 mm. 4.根据权利要求1或2所述的一种基于生物净化滤柱的去除微污染水源水中有机物的方法,其特征在于步骤一中滤料层(1-2)厚度为1.5~2m。4. A method for removing organic matter in micro-polluted water source water based on a biological purification filter column according to claim 1 or 2, characterized in that in step 1, the thickness of the filter material layer (1-2) is 1.5-2 m. 5.根据权利要求1或2所述的一种基于生物净化滤柱的去除微污染水源水中有机物的方法,其特征在于步骤二中滤速为4.5m/h。5. a kind of method for removing organic matter in micro-polluted water source water based on biological purification filter column according to claim 1 and 2, is characterized in that in step 2, the filtration rate is 4.5m/h. 6.根据权利要求1或2所述的一种基于生物净化滤柱的去除微污染水源水中有机物的方法,其特征在于步骤三中滤速为4.5m/h。6. A method for removing organic matter in micro-polluted water source water based on a biological purification filter column according to claim 1 or 2, wherein the filtration rate in step 3 is 4.5m/h.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003070647A1 (en) * 2002-02-22 2003-08-28 Bwt Wassertechnik Gmbh Method for treating water
CN103204579A (en) * 2013-03-23 2013-07-17 北京工业大学 Quick recovery method of biological deironing and manganese-removing filter technique
CN103420491A (en) * 2013-08-20 2013-12-04 哈尔滨工业大学 Simultaneous iron, manganese, ammonia nitrogen and turbidity removing method based on biological iron and manganese removing process
CN104529096A (en) * 2015-01-19 2015-04-22 哈尔滨工业大学 Water treatment device and method for removing ferromanganese, ammonia nitrogen and organic matters from underground water in synergy manner

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003070647A1 (en) * 2002-02-22 2003-08-28 Bwt Wassertechnik Gmbh Method for treating water
CN103204579A (en) * 2013-03-23 2013-07-17 北京工业大学 Quick recovery method of biological deironing and manganese-removing filter technique
CN103420491A (en) * 2013-08-20 2013-12-04 哈尔滨工业大学 Simultaneous iron, manganese, ammonia nitrogen and turbidity removing method based on biological iron and manganese removing process
CN104529096A (en) * 2015-01-19 2015-04-22 哈尔滨工业大学 Water treatment device and method for removing ferromanganese, ammonia nitrogen and organic matters from underground water in synergy manner

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
纳米水合二氧化锰氧化水中典型有机污染物的效能研究;杨晶晶;《中国优秀硕士学位论文全文数据库 工程科技I辑》;20140215(第2期);第3页 *

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