CN201746430U - Sequencing suspended carriers biomembrane sewage treatment device - Google Patents
Sequencing suspended carriers biomembrane sewage treatment device Download PDFInfo
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- CN201746430U CN201746430U CN2010202830235U CN201020283023U CN201746430U CN 201746430 U CN201746430 U CN 201746430U CN 2010202830235 U CN2010202830235 U CN 2010202830235U CN 201020283023 U CN201020283023 U CN 201020283023U CN 201746430 U CN201746430 U CN 201746430U
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- 239000010865 sewage Substances 0.000 title claims abstract description 28
- 238000012163 sequencing technique Methods 0.000 title description 3
- 239000000969 carrier Substances 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 50
- 239000000945 filler Substances 0.000 claims abstract description 23
- 238000005273 aeration Methods 0.000 claims abstract description 15
- 238000005276 aerator Methods 0.000 claims abstract description 12
- 238000012856 packing Methods 0.000 claims abstract description 10
- 239000004033 plastic Substances 0.000 claims abstract description 5
- 229920003023 plastic Polymers 0.000 claims abstract description 5
- 229920002635 polyurethane Polymers 0.000 claims abstract description 4
- 239000004814 polyurethane Substances 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 abstract description 29
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 20
- 239000010802 sludge Substances 0.000 abstract description 14
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 10
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 abstract description 8
- 230000000694 effects Effects 0.000 abstract description 8
- 239000002351 wastewater Substances 0.000 abstract description 7
- 238000003756 stirring Methods 0.000 abstract description 6
- 238000004062 sedimentation Methods 0.000 abstract description 2
- 238000006243 chemical reaction Methods 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- 230000001546 nitrifying effect Effects 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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Abstract
本实用新型涉及一种序批式悬浮填料生物膜污水处理装置。该装置包括水箱,该水箱经由管路、水泵、配水头后与反应器相连;反应器内装有螺旋搅拌器、与曝气机相连的曝气头和与水泵相连的配水头;水泵、曝气机、螺旋搅拌器以及阀门与时间控制器相连,其特征是上述反应器内还装有悬浮填料,该悬浮填料是塑料多面空心球或者聚氨酯网状海绵块;且配水头还与阀门相连通而又起到排水作用。本实用新型的装置采用改进的序批式运行方法,同时具有生物膜法和活性污泥法的优点,可自动控制进水时间、曝气时间、沉淀时间、排水和搅拌时间,保证COD、氨氮和总氮的去除效果,是一种适用于各种污/废水和河水的序批式悬浮填料污水处理装置。
The utility model relates to a sequence batch type suspended filler biofilm sewage treatment device. The device includes a water tank, which is connected to the reactor through a pipeline, a water pump, and a water distribution head; the reactor is equipped with a spiral agitator, an aeration head connected to the aerator, and a water distribution head connected to the water pump; the water pump, aeration The machine, the screw agitator and the valve are connected with the time controller, and the characteristic is that the above-mentioned reactor is also equipped with a suspended filler, which is a plastic multi-faceted hollow ball or a polyurethane mesh sponge block; and the water distribution head is also connected with the valve. It also plays a drainage role. The device of the utility model adopts the improved sequence batch operation method, which has the advantages of the biofilm method and the activated sludge method at the same time, and can automatically control the water inlet time, aeration time, sedimentation time, drainage and stirring time, and ensure COD, ammonia nitrogen And the removal effect of total nitrogen, it is a kind of sequential batch type suspended packing sewage treatment device suitable for various sewage/waste water and river water.
Description
技术领域technical field
本实用新型属于水处理设备领域,特别涉及一种序批式悬浮填料生物膜污水处理装置。The utility model belongs to the field of water treatment equipment, in particular to a sequential batch type suspended filler biofilm sewage treatment device.
背景技术Background technique
生物膜法污水处理是使微生物例如硝化菌和反硝化菌固着在填料表面,呈膜状生长,来实现污水处理的技术。一般可分为生物滤池、生物转盘、生物接触氧化法等,虽然它们的结构差别很大,但其基本原理相同,即通过废水与生物膜的接触,进行固液两相的传质,通过生物膜进行有机物的生物降解,使废水得以净化。生物膜法具有较高的处理效率,对于受有机物及氨氮轻度污染水体有明显的效果。但生物膜法的微生物挂膜技术还存在许多没有解决的问题。Biofilm sewage treatment is a technology that makes microorganisms such as nitrifying bacteria and denitrifying bacteria fix on the surface of the filler and grow in the form of a film to achieve sewage treatment. Generally, it can be divided into biological filter, biological turntable, biological contact oxidation method, etc. Although their structures are very different, their basic principles are the same, that is, through the contact between wastewater and biofilm, the mass transfer of solid-liquid two-phase is carried out. Biofilm biodegrades organic matter, enabling wastewater to be purified. The biofilm method has a high treatment efficiency and has obvious effects on water bodies slightly polluted by organic matter and ammonia nitrogen. However, there are still many unresolved problems in the microbial film-hanging technology of the biofilm method.
如今,污水生物处理技术不断完善,但从目前国内外的应用情况看,现有污水生物处理工艺还存在工艺流程较为复杂,需较大的占地面积和较高的基建投资,且运行的维护和管理难度较大等缺点。利用活性污泥和生物膜的复合工艺在解决传统工艺存在的问题时有其独到的特性和优点。活性污泥法具有处理能力大、处理效率高和出水水质好的优点,其各种变形工艺具有较好的脱氮除磷性能,在城市污水处理中得到了广泛的应用;其缺点是运行不够稳定,易产生污泥膨胀和污泥产量大,对低浓度污水的处理效果较差。生物膜法具有运行稳定、剩余污泥少、管理简单、对氨氮和难降解污染物去除能力强、能够适应较大水质范围变化等优点;其中固定填料生物膜污水处理装置的缺点有:填料和其支撑结构需要较高的初期投资,尘物膜脱落产生的细小颗粒不易沉降造成出水浊度较高,填料容易堵塞,总氮和总磷的去除能力较弱。Nowadays, sewage biological treatment technology is constantly improving, but judging from the current application situation at home and abroad, the existing sewage biological treatment process still has a relatively complicated process, which requires a large area and high infrastructure investment, and the operation and maintenance and management difficulties. The composite process using activated sludge and biofilm has its unique characteristics and advantages when solving the problems existing in traditional processes. The activated sludge method has the advantages of large processing capacity, high processing efficiency and good effluent quality. Its various deformation processes have good nitrogen and phosphorus removal performance, and have been widely used in urban sewage treatment; its disadvantage is that it is not enough Stable, easy to produce sludge bulking and large sludge output, poor treatment effect on low-concentration sewage. The biofilm method has the advantages of stable operation, less residual sludge, simple management, strong ability to remove ammonia nitrogen and refractory pollutants, and can adapt to a wide range of water quality changes; the disadvantages of the fixed-fill biofilm sewage treatment device are: packing and Its supporting structure requires a high initial investment, and the fine particles produced by the shedding of the dust film are not easy to settle, resulting in high turbidity of the effluent, easy plugging of the filler, and weak removal capacity of total nitrogen and total phosphorus.
目前已有生物膜法的相关专利报道,申请号200910069639.4的中国专利申请,以连续曝气-间歇曝气工艺为基础,反应器内投加活性污泥,以浮动曝气链为曝气装置,但浮动链上悬挂填料上的生物膜只起辅助作用。专利《生物接触氧化池中填料的挂膜方法》(专利号ZL200710061583.9),不能完全满足生物膜上硝化菌和反硝化菌的生长,达到去除总氮的目的。专利《污水好氧生物膜处理装置》(专利号ZL 02157780.3),采用固定填料上附生物膜,但脱落的生物膜容易堵塞填料,显然影响污水处理效果。At present, there are related patent reports on the biofilm method. The Chinese patent application with the application number 200910069639.4 is based on the continuous aeration-intermittent aeration process. Activated sludge is added to the reactor, and the floating aeration chain is used as the aeration device. But the biofilm on the filler suspended on the floating chain only played an auxiliary role. The patent "Film Hanging Method of Filler in Biological Contact Oxidation Pool" (Patent No. ZL200710061583.9) cannot fully satisfy the growth of nitrifying bacteria and denitrifying bacteria on the biofilm and achieve the purpose of removing total nitrogen. The patent "Sewage Aerobic Biofilm Treatment Device" (Patent No. ZL 02157780.3) adopts fixed packing to attach biofilm, but the falling biofilm is easy to block the packing, which obviously affects the sewage treatment effect.
发明内容Contents of the invention
本发明的目的是提供一种序批式悬浮填料生物膜污水处理装置,即结合活性污泥法和生物膜法装置的优点,提供一种能适应低浓度污/废水和河水,能有效去除COD、氨氮和总氮,使出水COD、氨氮和总氮均能达到城市污水处理一级排放标准的悬浮填料床污水处理装置,以弥补现有技术的不足。The purpose of the present invention is to provide a sequence batch type suspension filler biofilm sewage treatment device, which combines the advantages of the activated sludge method and the biofilm method device to provide a device that can adapt to low-concentration sewage/waste water and river water, and can effectively remove COD , ammonia nitrogen and total nitrogen, so that the effluent COD, ammonia nitrogen and total nitrogen can all meet the first-level discharge standard of urban sewage treatment, so as to make up for the shortcomings of the existing technology.
本实用新型的装置包括水箱,该水箱经由管路、水泵、配水头后与反应器相连;反应器内装有螺旋搅拌器、与曝气机相连的曝气头和与水泵相连的配水头;水泵、曝气机、螺旋搅拌器以及阀门与时间控制器相连,其特征是上述反应器内还装有悬浮填料,且配水头还与阀门相连通而又起到排水作用。The device of the utility model includes a water tank, which is connected to the reactor through pipelines, water pumps and water distribution heads; the reactor is equipped with a spiral agitator, an aeration head connected with the aerator and a water distribution head connected with the water pump; the water pump , an aerator, a spiral agitator and a valve are connected to a time controller, and it is characterized in that the above-mentioned reactor is also equipped with suspended packing, and the water distribution head is also connected with the valve and plays a role in drainage.
本实用新型改进的序批式悬浮填料生物膜污水处理反应器的创立原理是基于活性污泥法和生物膜法的结合,既同时具有生物膜法和活性污泥法的优点,又具有序批式SBR运行方式带来的好处。通过投加悬浮填料作为微生物附着生长的填料,增加反应器中的污泥浓度,提高硝化细菌和反硝化细菌的固着量、增强抵御外界环境变化的能力和抗冲击负荷的能力,从而也强化了系统对COD、氨氮和总氮的去除能力。特别是当活性污泥法和生物膜法的处理效果达到极限时,序批式悬浮填料床污水处理工艺将会显现出其独特优势。The creation principle of the utility model improved sequencing batch suspended packing biofilm sewage treatment reactor is based on the combination of activated sludge method and biofilm method, which not only has the advantages of biofilm method and activated sludge method, but also has the advantages of sequence batch The benefits brought by the traditional SBR operation mode. By adding suspended filler as filler for microbial attachment and growth, increasing the sludge concentration in the reactor, increasing the amount of fixation of nitrifying bacteria and denitrifying bacteria, enhancing the ability to resist changes in the external environment and the ability to resist impact loads, thereby also strengthening the The system's ability to remove COD, ammonia nitrogen and total nitrogen. Especially when the treatment effect of activated sludge method and biofilm method reaches the limit, the sequencing batch suspended packed bed sewage treatment process will show its unique advantages.
与现有技术相比,本实用新型的优点在于:Compared with the prior art, the utility model has the advantages of:
1.本实用新型采用的填料为悬浮填料,使用该类型填料使反应器兼有活性污泥法和生物膜法的优点,水力停留时间短,出水水质好;1. The filler used in this utility model is a suspension filler. Using this type of filler makes the reactor have the advantages of both the activated sludge method and the biofilm method, and the hydraulic retention time is short and the effluent water quality is good;
2.本实用新型在反应器内设螺旋搅拌器,保证填料与基质充分接触而获得充足的营养,发挥所有悬浮填料生物膜的作用,提高污水处理效率;2. The utility model has a spiral agitator in the reactor to ensure that the filler and the matrix are fully contacted to obtain sufficient nutrition, play the role of all suspended filler biofilms, and improve the efficiency of sewage treatment;
3.本实用新型采用序批式的运行方式,可以自动控制进水时间、曝气时间、沉淀时间、排水时间和搅拌时间,保证COD、氨氮和总氮的去除效果。3. The utility model adopts the sequence batch operation mode, which can automatically control the water intake time, aeration time, sedimentation time, drainage time and stirring time, so as to ensure the removal effect of COD, ammonia nitrogen and total nitrogen.
本实用新型设备简单,操作简便,易于控制,投资小,耗能少。并且污泥产生量小,污水处理效果好,是一种适用于各种污/废水和河水的序批式悬浮填料污水处理装置。The utility model has the advantages of simple equipment, convenient operation, easy control, small investment and low energy consumption. Moreover, the amount of sludge generated is small and the sewage treatment effect is good. It is a sequential batch type suspended filler sewage treatment device suitable for various sewage/waste water and river water.
附图说明Description of drawings
图1:本实用新型的装置结构示意图。Figure 1: Schematic diagram of the device structure of the present utility model.
其中:1水箱、2水泵、3时间控制器、4阀门、5曝气机、6配水头、7曝气头、8悬浮填料、9反应器、10螺旋搅拌器、11管路。Among them: 1 water tank, 2 water pump, 3 time controller, 4 valve, 5 aerator, 6 distribution head, 7 aeration head, 8 suspension packing, 9 reactor, 10 spiral agitator, 11 pipeline.
具体实施方式Detailed ways
以下将结合附图对本实用新型做进一步详细说明。The utility model will be described in further detail below in conjunction with the accompanying drawings.
如图1所示,本实用新型的装置包括水箱1,该水箱1经由管路11、水泵2、配水头6后与反应器9相连;反应器9内装有螺旋搅拌器10、与曝气机5相连的曝气头7和与水泵2相连的配水头6;水泵2、曝气机5、螺旋搅拌器10以及阀门4与时间控制器3相连,其特征是上述反应器9内还装有悬浮填料8,且配水头6还与阀门9相连通而又起到排水作用。As shown in Figure 1, the device of the present utility model includes a
上述悬浮填料8是塑料多面空心球或者聚氨酯网状海绵块;上述塑料多面空心球是半径20mm,密度0.13g/cm3的球体。The
本实用新型的装置采用改进的序批式方法运行,包括如下步骤:在进水阶段:开启水泵2,同时关闭阀门4、曝气机5和螺旋搅拌器10;好氧曝气阶段:关闭水泵2和阀门4,开启曝气机5和螺旋搅拌器10;缺氧反应阶段:关闭水泵2、阀门4和曝气机5,开启螺旋搅拌器10;沉淀阶段:关闭水泵2、阀门4、曝气机5和螺旋搅拌器10;排水阶段:关闭水泵2、曝气机5和螺旋搅拌器10,打开阀门4。反应器运行过程中,在好氧曝气阶段和缺氧反应阶段开启螺旋搅拌器10,保证废水与悬浮填料8的充分接触,提高污/废水和河水处理效率。The device of the present invention adopts the improved sequence batch method to operate, including the following steps: in the water intake stage: open the
实施例1Example 1
上述反应器9的容积为10L,内加悬浮填料8是塑料多面空心球填料(半径20mm、密度0.13g/cm3),启动挂膜成功后,开始进水,进水的污水水质为:CODCr120~140mg/L,NH4 +-N25~30mg/L,TN 30~35mg/L,pH 7~7.2。采用的运行条件为:瞬时进水,缺氧搅拌反应2h,好氧曝气反应6h,缺氧搅拌反应3h,沉淀1h,瞬时排水。处理效果:COD去除率为85.6%、氨氮去除率为100%、总氮去除率为67.3%,出水水质达到城市污水一级排放标准。The volume of the above-mentioned
实施例2Example 2
上述反应器9的容积为10L,内加的悬浮填料8是聚氨酯网状海绵块,启动挂膜成功后,开始进水,进水的污水水质为:CODCr120~140mg/L,NH4 +-N 25~30mg/L,TN 30~35mg/L,pH 7~7.2。采用的运行条件为:瞬时进水,缺氧搅拌反应2h,好氧曝气反应6h,缺氧搅拌反应3h,沉淀1h,瞬时排水。本实用新型的COD的去除率为81.2%、NH4 +去除率为100%、总氮去除率为62.8%。The volume of the above-mentioned
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101913732A (en) * | 2010-08-04 | 2010-12-15 | 中国海洋大学 | Sequencing batch suspended packing biofilm sewage treatment device |
CN105906030A (en) * | 2016-05-09 | 2016-08-31 | 宁波淳源环保科技有限公司 | Reactor for sewage using neuston |
CN106145325A (en) * | 2015-04-27 | 2016-11-23 | 中国科学院生态环境研究中心 | A kind of batch-type is moved through filter bed sewage water treatment method and device thereof |
CN109607766A (en) * | 2018-12-06 | 2019-04-12 | 同济大学 | A kind of start-up method for variable mud age in IFAS process |
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2010
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101913732A (en) * | 2010-08-04 | 2010-12-15 | 中国海洋大学 | Sequencing batch suspended packing biofilm sewage treatment device |
CN101913732B (en) * | 2010-08-04 | 2012-03-21 | 中国海洋大学 | Sequencing batch type suspended filler biofilm sewage treatment device |
CN106145325A (en) * | 2015-04-27 | 2016-11-23 | 中国科学院生态环境研究中心 | A kind of batch-type is moved through filter bed sewage water treatment method and device thereof |
CN105906030A (en) * | 2016-05-09 | 2016-08-31 | 宁波淳源环保科技有限公司 | Reactor for sewage using neuston |
CN109607766A (en) * | 2018-12-06 | 2019-04-12 | 同济大学 | A kind of start-up method for variable mud age in IFAS process |
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