CN107162334B - Method for removing organic matters in micro-polluted source water based on biological purification filter column - Google Patents
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 223
- 238000000746 purification Methods 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract description 23
- 239000005416 organic matter Substances 0.000 claims abstract description 38
- 241000894006 Bacteria Species 0.000 claims abstract description 18
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910052748 manganese Inorganic materials 0.000 claims abstract description 15
- 239000011572 manganese Substances 0.000 claims abstract description 15
- 230000001590 oxidative effect Effects 0.000 claims abstract description 12
- 238000010276 construction Methods 0.000 claims abstract description 6
- 229940099596 manganese sulfate Drugs 0.000 claims description 19
- 235000007079 manganese sulphate Nutrition 0.000 claims description 19
- 239000011702 manganese sulphate Substances 0.000 claims description 19
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 claims description 19
- 238000001914 filtration Methods 0.000 claims description 16
- 239000011259 mixed solution Substances 0.000 claims description 15
- 239000008399 tap water Substances 0.000 claims description 15
- 235000020679 tap water Nutrition 0.000 claims description 15
- 229910001437 manganese ion Inorganic materials 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 11
- 239000000243 solution Substances 0.000 claims description 11
- 239000006004 Quartz sand Substances 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 5
- 238000005070 sampling Methods 0.000 claims description 5
- 239000004575 stone Substances 0.000 claims description 5
- 230000003647 oxidation Effects 0.000 abstract description 7
- 238000007254 oxidation reaction Methods 0.000 abstract description 7
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 239000002384 drinking water standard Substances 0.000 abstract description 2
- 244000005700 microbiome Species 0.000 abstract description 2
- 238000012258 culturing Methods 0.000 abstract 1
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 11
- 230000000694 effects Effects 0.000 description 10
- PPNAOCWZXJOHFK-UHFFFAOYSA-N manganese(2+);oxygen(2-) Chemical class [O-2].[Mn+2] PPNAOCWZXJOHFK-UHFFFAOYSA-N 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 235000020188 drinking water Nutrition 0.000 description 3
- 239000003651 drinking water Substances 0.000 description 3
- 238000010170 biological method Methods 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 239000000575 pesticide Substances 0.000 description 2
- 238000012271 agricultural production Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000000598 endocrine disruptor Substances 0.000 description 1
- 231100000049 endocrine disruptor Toxicity 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
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- 230000004083 survival effect Effects 0.000 description 1
- 230000002110 toxicologic effect Effects 0.000 description 1
- 231100000027 toxicology Toxicity 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/206—Manganese or manganese compounds
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- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological 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。
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.
Description
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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
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.
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