WO2017128729A1 - 一种污水处理技术系统及其使用方法 - Google Patents

一种污水处理技术系统及其使用方法 Download PDF

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WO2017128729A1
WO2017128729A1 PCT/CN2016/098592 CN2016098592W WO2017128729A1 WO 2017128729 A1 WO2017128729 A1 WO 2017128729A1 CN 2016098592 W CN2016098592 W CN 2016098592W WO 2017128729 A1 WO2017128729 A1 WO 2017128729A1
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treatment tank
treatment
sewage treatment
sewage
water
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PCT/CN2016/098592
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English (en)
French (fr)
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严润峰
闭历平
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严润峰
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    • C—CHEMISTRY; METALLURGY
    • 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
    • C02F3/30—Aerobic and anaerobic processes
    • C—CHEMISTRY; METALLURGY
    • 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
    • C02F3/348—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the way or the form in which the microorganisms are added or dosed
    • C—CHEMISTRY; METALLURGY
    • 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
    • C02F3/30—Aerobic and anaerobic processes
    • C02F3/301—Aerobic and anaerobic treatment in the same reactor
    • C—CHEMISTRY; METALLURGY
    • 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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  • the invention belongs to the field of sewage treatment, and particularly relates to a sewage treatment technical system and a using method thereof.
  • biological sewage treatment technology can only produce single strain biological treatment in the same period of the treatment tank, that is, anaerobic bacteria or aerobic bacteria treatment. And my technology will break through this dilemma.
  • the prior art CN1562824A living community sewage treatment recycling system belongs to the field of environmental protection, and is characterized in that the integrated sewage treatment tank integrating the activated sludge method and the biofilm method is divided into a collecting pool and a pump pool. Floating biological bed, sedimentation tank, biological filtration layer, reuse pool, and a sludge well; filling 30-40% of the floating biological carrier in the biological bed; the sewage is biodegraded and precipitated into water The precipitated excess sludge is returned to the floating biological bed for sludge aerobic treatment when the amount of sewage is small (such as at night).
  • the prior art CN104556390A is a water pollution control system, which is characterized in that it comprises a pump and a filter, and the pump is connected with the water body to provide water for the filter; the filter is connected with the water body, and the filter can be filtered.
  • the water is discharged into the water body; the water body is provided with a diversion wall, the diversion wall makes the water in the water body flow in a curved shape; the biofilm network is arranged on both sides of the diversion wall;
  • Filtration of the water body through the filter tank can remove most of the suspended matter, algae and other organic and inorganic substances in the water, and the filtered water re-flows into the water body, and forms a water body circulation with the diversion wall provided in the water body.
  • the present invention will break through the biological treatment mode in which only a single strain can be present in the same treatment tank at the same time, and can simultaneously contain aerobic bacteria, anaerobic bacteria and anoxic bacteria in the same treatment tank at the same time.
  • Concurrent bacteria combines the treatment of organic matter in sewage and adjusts their respective proportions. Use sewage to enter the treatment tank evenly from the bottom at a certain speed, using the depth of sewage, oxygen content or local oxygenation, so that the strains attached to the net or strip-like body and the strains at the bottom of the sink are different. Aerobic bacteria, anaerobic bacteria and anoxic bacteria (facultative bacteria) for biological treatment to achieve comprehensive treatment and reach No sludge discharge, eliminating the shortcomings of conventional sewage treatment tanks.
  • a sewage treatment technical system comprising: a treatment tank, a water inlet (1) is arranged on one side of the top or side of the treatment tank, and a drainage port (2) is arranged on the other side, and the bacteria-attached component (4) is disposed on In the treatment tank, the water inlet is connected by a pipe, and one end of the pipe is provided with more than one water outlet (3), wherein the water outlet is located at the bottom of the treatment tank and below the contaminated parts of the strain.
  • the strain-attaching member be in the form of a mesh or a strip.
  • the water outlet is downward.
  • the above-mentioned setting ensures that the water rising rate of the treatment tank is 0.1 to 10 m/hr.
  • the treatment tank is a regular or irregular shape such as a square or a circle.
  • the bacterial adhering member is fixed above the treatment tank by suspension, anchoring or the like.
  • the treatment tank be used in a single or repeated series design.
  • an oxygenator or an aeration head is disposed in the water inlet and outlet pipes of the treatment tank.
  • Another object of the present invention is to provide a sewage treatment technology system treatment method, comprising: using the foregoing sewage treatment technology system, the water body in the treatment tank is lifted at a speed of 0.1 to 10 meters per hour, passed through an oxygenator or exposed The gas head controls the dissolved oxygen content in the treatment tank.
  • Figure 2 is a strip cross-sectional view of the sewage treatment technology system of the present invention
  • Figure 3 is a mesh and strip top view of the sewage treatment technology system of the present invention
  • a sewage treatment technical system includes a treatment tank.
  • the top side of the treatment tank is provided with a water inlet (1), and the other side is provided with a water outlet (2), and the strain is attached.
  • the component (4) is disposed in the processing tank, and the water inlet is connected by a pipe.
  • the pipe end is provided with more than one water outlet (3), wherein the water outlet is located at the bottom of the treatment tank and is located below the strained component.
  • the bacteria-attached parts are in the form of a mesh.
  • the water outlet is downward.
  • the above-mentioned setting ensures that the water rising speed of the treatment tank is 1 m/hr.
  • the processing pool is a square regular shape.
  • strain-adhering parts are fixed to the top of the treatment tank by suspension.
  • a sewage treatment technical system includes a treatment tank.
  • the top side of the treatment tank is provided with a water inlet (1), and the other side is provided with a water outlet (2), and the strain is attached.
  • the component (4) is disposed in the processing tank, and the water inlet is connected by a pipe.
  • the pipe end is provided with more than one water outlet (3), wherein the water outlet is located at the bottom of the treatment tank and is located below the strained component.
  • the bacteria-attached parts are in the form of a mesh.
  • the water outlet is downward.
  • the above-mentioned setting ensures that the water rising speed of the treatment tank is 5 m/hr.
  • the processing pool is in the shape of a circular rule.
  • strain-adhering parts are anchored to the top of the treatment tank.
  • a sewage treatment technical system includes a treatment tank and a top of the treatment tank One side is provided with a water inlet (1), the other side is provided with a water outlet (2), the bacteria attachment component (4) is arranged in the treatment tank, the water inlet is connected by a pipe, and one end of the pipe is provided with more than one water outlet ( 3), wherein the water outlet is located at the bottom of the treatment tank and is located below the strained component.
  • the bacteria-attached parts are strip-shaped.
  • the water outlet is downward.
  • the above-mentioned setting ensures that the water rising speed of the treatment tank is 10 m/hr.
  • the processing pool is in the shape of a circular rule.
  • strain-adhering parts are anchored to the top of the treatment tank.
  • a sewage treatment technology system in which any one of the embodiments 1-3 is repeatedly designed in series using a treatment tank, and the number of series is two or more.
  • Example 5 sewage treatment technology system use method
  • the sewage treatment technology system of any of the embodiments 1-4 is used for sewage treatment, and the use method is as follows:
  • the sewage enters the floating and sinking tank it is discharged through the drainage port at the middle of the floating and sinking tank, that is, the water inlet of the treatment tank, and the pipeline connected through the water inlet and the water outlet.
  • the treatment tank is used in a complex series design.
  • the drain of the previous treatment tank is the inlet of the next treatment tank, and so on, from the flow.
  • the size of the treatment tank and the number of series are determined by the amount of sewage and discharge standards, and the number of inlets, outlets and outlets of the treatment tank is determined by the size of the treatment tank.
  • the preferred solution is as follows: A; floating and sinking pool (can be determined according to whether the sewage contains floating objects); the upper third of the surface of the floating sinking tank is set as the sewage with the floating object staying area, and the lower third of the floating sinking pool is set. For the sedimentation area with sediments in the sewage, when the floating objects and sediments reach a certain amount, they are removed. After the sewage enters the floating and sinking pool, it is discharged from the drainage outlet in the middle of the floating and sinking tank.
  • oxygenation in the pipeline an oxygenator (aeration head) is placed in the inlet and outlet pipes of the treatment tank, and the oxygen is supplied to the oxygenator (aeration head) through an oxygenation pipeline by an external oxygenation machine.
  • the sewage is oxygenated, and the amount of dissolved oxygen is required to be increased or decreased according to the treatment tank to ensure the adjustment of the layer distribution of the mesh or strip adhesion bacteria in the treatment tank.
  • anoxic dissolved oxygen content between 0.7mg / L to 0.1mg / L
  • anaerobic dissolved oxygen content is basically not
  • the microbial population in which the mesh or strip adhered to the surface of the water surface is about 0.5 m deep is aerobic, and the surface layer below about 0.5 m is hypoxic (oxygen) and anaerobic.
  • hypoxic oxygen
  • anaerobic hypoxic
  • the sewage enters the bottom of the treatment tank from the water outlet, the sewage enters when the proper amount of dissolved oxygen is contained, the microbial bacteria deposited at the bottom of the treatment tank and the microbial population adhered to the net or strip at the bottom of the treatment tank, and the dissolved oxygen content in the contactable sewage When it is above 1mg/L, it is aerobic bacteria, and the sewage is biotransformed. When the microbial bacteria are biotransformed, a certain amount of dissolved oxygen is consumed.
  • the dissolved oxygen content of the water body is more and more The lower, until there is no dissolved oxygen, this will form the bottom of the treatment tank to push up to aerobic, anoxic (oxygen), anaerobic layer, such as the surface layer of the water can contact oxygen, it will form the bottom layer of the treatment pool or strip
  • the microbial population adhering to the substance pushes up to aerobic, anoxic (oxygen), anaerobic layer, anoxic (oxygen), aerobic (recommended, COD, total nitrogen removal can reach surface water ).
  • the water depth of the treatment tank is more than 3 meters.
  • the increase in the number of microorganisms promotes the production of activated sludge, and the growth process of activated sludge can be divided into four stages: adaptation stage, logarithmic growth stage, deceleration growth stage and endogenous metabolic stage, as long as the activated sludge is not sufficient.
  • the nutrients will enter the self-oxidation stage, the activated sludge will be reduced, and the activated sludge residue will be deposited on the bottom of the treatment tank, as long as there is sufficient residence time (the residence time is not known, but In the case of treating sewage, there is indeed no discharge of sludge in 10 years, and the activated sludge deposited on the bottom of the treatment tank is not increased or decreased. It will be biotransformed by other active microorganisms for virtuous circulation. Therefore, the activated sludge does not need to be discharged in the treatment tank.

Abstract

一种污水处理技术系统及其使用方法，包括，处理池，处理池的顶部或侧部设置有进水口(1)，另外一侧设置有排水口(2)，菌种沾附部件(4)设置于处理池内，进水口(1)通过管道连接，管道末端设置有一个以上出水口(3)，其中，出水口(3)位于处理池的底部，且位于菌种沾附部件(4)的下方。该污水处理技术系统实现生物污水处理技术在处理池内同一时期多种菌种生物处理，即厌氧菌和好氧菌同时处理；比常规工艺快速有效，节能，并可达到无污泥排放。

Description

一种污水处理技术系统及其使用方法 技术领域
本发明属于污水处理领域，具体涉及一种污水处理技术系统及其使用方法。
背景技术
目前，生物污水处理技术在处理池内同一时期只能出现单一菌种生物处理，即厌氧菌或是好氧菌处理。而本人的技术将突破这一困境。
例如现有技术CN1562824A生活小区污水处理回用系统，属于环保领域，其特征是在把活性污泥法和生物膜法融为一体的一体化的综合污水处理池中，分隔为集水池、泵池、浮动生物床、沉淀池、生物过滤层、回用水池，还有一个污泥井；在生物床中填加占池容30－40％的浮动生物载体；污水经生物降解、沉淀处理成回用水，沉淀下来的剩余污泥在污水量少时(如夜间)，再回到浮动生物床进行污泥好氧处理。
现有技术CN104556390A一种水体污染治理系统，其特征在于，包括抽水泵和滤池，所述抽水泵与水体连通，可为滤池提供水；所述滤池与水体连通，可将过滤后的水排入水体中；所述水体中设有导流墙，导流墙使水体中的水呈弯曲状流动；所述导流墙的两侧设有生物膜网；在所述的水体内设有生态浮岛，在水的流动路径上安设推流曝气机。通过滤池先对水体进行过滤，可去除水中大部分的悬浮物、藻类等有机物和无机物，过滤后的水重新流入水体，与水体中设置的导流墙构成水体循环。
上述现有技术的处理系统均难以实现多种菌种的同时处理。
发明内容
鉴于现有技术存在的技术问题，本发明将突破在同一处理池内同一时期只能出现单一菌种的生物处理方式，可在同一时间同一处理池内同时容纳好氧菌、厌氧菌和缺氧菌(兼氧菌)联合处理污水中的有机物，并可调节其各自比例。利用污水从底部均匀按一定的速度进入处理池，利用污水深度、含氧量或局部加氧，从而使沾附在网状或条状物体的菌种和沉殿于底部的菌种，产生不同的好氧菌、厌氧菌和缺氧菌(兼氧菌)，从而进行生物处理，达到综合处理的效果，并可达 到无污泥排放，免去了常规污水处理池的短处。
本发明通过以下技术方案来实现：
一种污水处理技术系统，包括，处理池，处理池的顶部或侧部一侧设置有进水口(1)，另外一侧设置有排水口(2)，菌种沾附部件(4)设置于处理池内，进水口通过管道连接，管道末端设置有一个以上出水口(3)，其中，出水口位于处理池的底部，且位于菌种沾附部件的下方。
其中，优选菌种沾附部件为网状或条状。
其中，优选出水口为多个时，每个出水口量均匀分布。
其中，优选出水口向下。
其中，通过上述设置保证处理池水体上升速度为0.1～10米/小时。
优选处理池为方形或者圆形等规则或者不规则形状。
优选菌种沾附部件通过悬挂、锚定等方式固定于处理池上方。
进一步优选处理池为单个或重复串联设计使用。
进一步优化方案，可根据污水含有浮沉物体决定设立与否浮沉池。
其中，处理池进水口与出水口管道内安置充氧器或曝气头。
本发明的另一目的在于：提供一种污水处理技术系统处理方法，包括，使用前述一种污水处理技术系统，处理池中的水体以0.1～10米/小时速度抬升，通过充氧器或曝气头控制处理池内溶解氧含量。
本发明相对于现有技术的有益效果包括：
1、实现生物污水处理技术在处理池内同一时期多种菌种生物处理，即厌氧菌和好氧菌同时处理；
2、比常规工艺快速有效，节能，并可达到无污泥排放。
附图说明
图1，本发明的污水处理技术系统的网状截面图
图2，本发明的污水处理技术系统的条状截面图
图3，本发明的污水处理技术系统的网状和条状俯视图
其中，1—进水口，2—排水口，3—出水口，4—菌种沾附部件。
具体实施方式
下面结合实施例和附图对本发明作进一步详细的描述，但发明的实施方式不限于此。
实施例1：
参照图1和图3所示，一种污水处理技术系统，包括，处理池，处理池的顶部一侧设置有进水口(1)，另外一侧设置有排水口(2)，菌种沾附部件(4)设置于处理池内，进水口通过管道连接，管道末端设置有一个以上出水口(3)，其中，出水口位于处理池的底部，且位于菌种沾附部件的下方。
其中，菌种沾附部件为网状。
其中，出水口向下。
其中，通过上述设置保证处理池水体上升速度为1米/小时。
处理池为方形规则形状。
菌种沾附部件通过悬挂方式固定于处理池上方。
实施例2：
参照图1和图3所示，一种污水处理技术系统，包括，处理池，处理池的顶部一侧设置有进水口(1)，另外一侧设置有排水口(2)，菌种沾附部件(4)设置于处理池内，进水口通过管道连接，管道末端设置有一个以上出水口(3)，其中，出水口位于处理池的底部，且位于菌种沾附部件的下方。
其中，菌种沾附部件为网状。
其中，出水口为11个，每个出水口量均匀分布。
其中，出水口向下。
其中，通过上述设置保证处理池水体上升速度为5米/小时。
处理池为圆形规则形状。
菌种沾附部件通过锚定方式固定于处理池上方。
实施例3：
参照图2和图3所示，一种污水处理技术系统，包括，处理池，处理池的顶 部一侧设置有进水口(1)，另外一侧设置有排水口(2)，菌种沾附部件(4)设置于处理池内，进水口通过管道连接，管道末端设置有一个以上出水口(3)，其中，出水口位于处理池的底部，且位于菌种沾附部件的下方。
其中，菌种沾附部件为条状。
其中，出水口为8个，每个出水口量均匀分布。
其中，出水口向下。
其中，通过上述设置保证处理池水体上升速度为10米/小时。
处理池为圆形规则形状。
菌种沾附部件通过锚定方式固定于处理池上方。
实施例4：
一种污水处理技术系统，实施例1-3任一方案采用处理池重复串联设计使用，串联个数为2个以上。
实施例5污水处理技术系统使用方法
采用实施例1-4任一方案的污水处理技术系统进行污水处理，使用方法如下：
污水流动线路，污水在进入处理池前面，设置一个浮沉池，当污水进入浮沉池后，经浮沉池中部位置的排水口排出，即处理池的进水口，并经过进水口与出水口联接的管道内充氧器，污水由出水口进入处理池底部,使整个处理池底部均匀受水，并每个出水口的出水量均匀，使处理池整体水体从底部以0.1～10米/小时速度往上抬升，在水体抬升的过程中，与粘附在网状或条状物体的微生物菌体接触，发生分解污水中的有机物，进行生物转化过程，水体直至处理池顶部或侧面管道排水口排出.如处理池采用复式串联设计使用，上一个的处理池的排水口便是下一个处理池的进水口，如此类推，自流进入。
处理池大小、串联数量由污水量及排放标准决定，而处理池进水口、出水口及排水口数量又由处理池大小决定。
具有优选方案如下：A；浮沉池(可根据污水含有浮沉物体决定设立与否)；浮沉池上部三分之一水面设置为污水带有上浮物停留区，浮沉池下部三分之一水底部分设置为污水带有沉积物的沉积区，当上浮物及沉积物达到一定量时，清除掉，污水进入浮沉池后，由浮沉池中部的排水口排出。
B；管道内充氧；处理池进水口与出水口管道内安置充氧器(曝气头)，由外置的充氧机器通过充氧管道对充氧器(曝气头)输送氧气，对污水进行充氧，根据处理池须求溶解氧量进行增减，确保处理池内网状或条状物粘附菌种层次分布的调节。
C；处理池；污水由出水口进入处理池底部时，当污水没有含有溶解氧时进入，只有水面表层约0.5米深的以上水层溶解氧含量在1mg/L以上，而0.5米深以下部分都在1mg/L以下，直至没有溶解氧。假设处理池水体深度为3米时，水面表层约1.5米以下部分基本没有溶解氧含量，根据微生物对氧需求程度的不同而划分的生物处理方法分为好氧(溶解氧含量在1mg/L以上)、缺氧(溶解氧含量在0.7mg/L至0.1mg/L之间)、厌氧(溶解氧含量基本没有)等三大类。即是说水面表层约0.5米深的网状或条状物粘附的微生物群体为好氧，水面表层约0.5米以下的为缺氧(兼氧)和厌氧。当处理池的水表层不提供氧份时，整个处理池成厌氧状态。
如污水由出水口进入处理池底部时，污水含有适量溶解氧时进入，处理池底部沉积的微生物菌及处理池底部网状或条状物粘附的微生物群体、可接触污水中的溶解氧含量在1mg/L以上时为好氧菌，并对污水进行生物转化处理,因微生物菌进行生物转化处理时，要消耗一定的溶解氧，当离处理池底部越远时，水体溶解氧含量越来越低，直至没有溶解氧，这样会形成处理池底层往上推为好氧、缺氧(兼氧)、厌氧层，如水面表层可接触氧份，就会形成处理池底层网状或条状物粘附的微生物群体往上推为好氧、缺氧(兼氧)、厌氧层、缺氧(兼氧)、好氧(推荐该方式，COD、总氮去除可达地表水二类)。处理池水深3米以上较为明显。当污水由出水口含有充足溶解氧进入处理池底部时，使整个处理池的水体溶解氧在1mg/L以上时，整个处理池为好氧状态。
根据水体流动原理，处理池底部时均匀出水，水体会以层次地从底部往上推移，当以0.1～10米/小时速度抬升时，接触处理池内的网状或条状物粘附的微生物对污水处理效果优越。
微生物数量的变化增多促使活性污泥产生，而活性污泥的增长过程可分为适应阶段、对数增长阶段、减速增长阶段和内源代谢阶段等四个阶段，只要活性污泥得不到充足的营养物质，就会进入自身氧化阶段，活性污泥就会减少，活性污泥残留物沉积在处理池底层，只要有充足停留时间(停留时间确实不知长短，但 在处理污水实例中，确实有十年没有过排放过污泥，并沉积于处理池底层的活性污泥没有增减)，会被其它活性微生物重新进行生物转化，进行良性循环。故活性污泥在本处理池中不须排放。
以上内容是结合具体的优选实施方式对本发明所做的进一步详细的说明，但是不表示本发明的具体实施是局限于这些说明。对于本发明所属拘束领的普通技术人员来说，在不脱离本发明构思的前提下，还可以做出若干简单推演或是替换，都应视为属于本发明的保护范围。

Claims (10)

  1. 一种污水处理技术系统，其特征在于，包括，处理池，处理池的顶部或侧部一侧设置有进水口(1)，另外一侧设置有排水口(2)，菌种沾附部件(4)设置于处理池内，进水口通过管道连接，管道末端设置有一个以上出水口(3)，其中，出水口位于处理池的底部，且位于菌种沾附部件的下方。
  2. 根据权利要求1所述的一种污水处理技术系统，其特征在于，优选菌种沾附部件为网状或条状。
  3. 根据权利要求1所述的一种污水处理技术系统，其特征在于，优选出水口为多个时，每个出水口量均匀分布。
  4. 根据权利要求1所述的一种污水处理技术系统，其特征在于，优选出水口向下。
  5. 根据权利要求1所述的一种污水处理技术系统，其特征在于，通过上述设置保证处理池水体上升速度为0.1～10米/小时。
  6. 根据权利要求1所述的一种污水处理技术系统，其特征在于，优选处理池为方形或者圆形等规则或者不规则形状。
  7. 根据权利要求1所述的一种污水处理技术系统，其特征在于，优选菌种沾附部件通过悬挂、锚定等方式固定于处理池上方。
  8. 根据权利要求1所述的一种污水处理技术系统，其特征在于，优选处理池为单个或重复串联设计使用。
  9. 根据权利要求1所述的一种污水处理技术系统，其特征在于，可根据污水含有浮沉物体决定设立与否浮沉池，处理池进水口与出水口管道内安置充氧器或曝气头。
  10. 一种污水处理技术系统处理方法，包括，使用前述权利要求1—9任一权利要求所述一种污水处理技术系统，处理池中的水体以0.1～10米/小时速度抬升，通过充氧器或曝气头控制处理池内溶解氧含量。
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116177744A (zh) * 2023-03-29 2023-05-30 北京华夏启新环境科技有限公司 改良aoa工艺耦合mbr高效脱氮除磷的污水处理系统及方法

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105540872B (zh) * 2016-01-26 2019-12-24 严润峰 一种污水处理技术系统及其使用方法

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09155372A (ja) * 1995-12-04 1997-06-17 Tokyu Constr Co Ltd 散水濾床装置及びその洗浄方法
CN201330197Y (zh) * 2009-01-23 2009-10-21 北京基亚特环保工程有限公司 一种高效厌氧反应器
CN204224386U (zh) * 2014-10-20 2015-03-25 北京沃尔德斯水务科技有限公司 一种污水处理一体化设备
CN104591349A (zh) * 2015-01-26 2015-05-06 北京金科复合材料有限责任公司 一种帘式填料铁碳微电解反应器
CN204607678U (zh) * 2015-03-03 2015-09-02 长沙攀力科技开发有限公司 一种多功能生化处理设备
CN105540872A (zh) * 2016-01-26 2016-05-04 严润峰 一种污水处理技术系统及其使用方法

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201458895U (zh) * 2009-08-03 2010-05-12 王玉华 宾馆和居民小区污水的集成式处理装置
CN202465367U (zh) * 2011-11-22 2012-10-03 桑德集团有限公司 污水处理生化反应池
CN104058499B (zh) * 2014-07-15 2016-01-20 许建民 一种曝气生物滤池及工艺
CN204022556U (zh) * 2014-09-03 2014-12-17 福建省臻苑环保科技有限公司 基波传质厌氧污废水处理装置
CN205575780U (zh) * 2016-01-26 2016-09-14 严润峰 一种污水处理系统

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09155372A (ja) * 1995-12-04 1997-06-17 Tokyu Constr Co Ltd 散水濾床装置及びその洗浄方法
CN201330197Y (zh) * 2009-01-23 2009-10-21 北京基亚特环保工程有限公司 一种高效厌氧反应器
CN204224386U (zh) * 2014-10-20 2015-03-25 北京沃尔德斯水务科技有限公司 一种污水处理一体化设备
CN104591349A (zh) * 2015-01-26 2015-05-06 北京金科复合材料有限责任公司 一种帘式填料铁碳微电解反应器
CN204607678U (zh) * 2015-03-03 2015-09-02 长沙攀力科技开发有限公司 一种多功能生化处理设备
CN105540872A (zh) * 2016-01-26 2016-05-04 严润峰 一种污水处理技术系统及其使用方法

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116177744A (zh) * 2023-03-29 2023-05-30 北京华夏启新环境科技有限公司 改良aoa工艺耦合mbr高效脱氮除磷的污水处理系统及方法

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