CN100344556C - Bioreactor for sewage treatment - Google Patents
Bioreactor for sewage treatment Download PDFInfo
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- CN100344556C CN100344556C CNB2005100491127A CN200510049112A CN100344556C CN 100344556 C CN100344556 C CN 100344556C CN B2005100491127 A CNB2005100491127 A CN B2005100491127A CN 200510049112 A CN200510049112 A CN 200510049112A CN 100344556 C CN100344556 C CN 100344556C
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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
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
一种污水处理生物反应器,包括反应器主体,反应器主体上部设有出水口和尾气出口,反应器主体下部设有进水口和压缩空气入口,所述的反应器主体内部设有固液分离装置,固液分离装置包括逆流管、回流管,逆流管上部与反应器内腔连通,回流管上部连接出水管,出水管连通反应器出水口;逆流管下方设有沉积腔,沉积腔连通所述的回流管,沉积腔下方设有挡泥板,沉积腔与挡泥板之间留有间隙;反应器主体底部设有排泥口。本发明所述污水处理生物反应器减少了常规的加压生化法的后需处理设备,采用内置式的固液分离装置自动进行液固分离,省去了后续沉淀处理,减化了工艺流程设备,降低了运行成本。
A bioreactor for sewage treatment, comprising a reactor main body, the upper part of the reactor main body is provided with a water outlet and a tail gas outlet, the lower part of the reactor main body is provided with a water inlet and a compressed air inlet, and the inside of the reactor main body is provided with a solid-liquid separation device, the solid-liquid separation device includes a counterflow pipe and a return pipe, the upper part of the counterflow pipe is connected with the inner cavity of the reactor, the upper part of the backflow pipe is connected with the water outlet pipe, and the water outlet pipe is connected with the water outlet of the reactor; For the return pipe mentioned above, a fender is provided under the deposition chamber, and a gap is left between the deposition chamber and the fender; a mud discharge port is provided at the bottom of the reactor main body. The sewage treatment bioreactor of the present invention reduces the post-processing equipment required in the conventional pressurized biochemical method, adopts a built-in solid-liquid separation device to automatically perform liquid-solid separation, saves subsequent sedimentation treatment, and reduces process flow equipment , reducing operating costs.
Description
(一)技术领域(1) Technical field
本发明涉及一种污水处理生物反应器。The invention relates to a biological reactor for sewage treatment.
(二)背景技术(2) Background technology
传统的好氧生物处理法由于其供氧能力受到限制,使微生物浓度和处理效率受到限制,并且只适用于中低浓度的有机废水。其主要原因是供氧速率不能满足微生物对氧的要求,致使停留时间长、去除效率低、容积负荷低。常规的加压生化法,在进行生化反应后,出水需进入后续沉淀池进行沉淀处理,使液固分离,这样增加了其反应器的后续处理设备。The traditional aerobic biological treatment method is limited by its oxygen supply capacity, which limits the concentration of microorganisms and treatment efficiency, and is only suitable for low-to-medium concentration organic wastewater. The main reason is that the oxygen supply rate cannot meet the requirements of microorganisms for oxygen, resulting in long residence time, low removal efficiency and low volume load. In the conventional pressurized biochemical method, after the biochemical reaction, the effluent needs to enter the follow-up sedimentation tank for sedimentation treatment to separate the liquid and solid, which increases the follow-up treatment equipment of the reactor.
(三)发明内容(3) Contents of the invention
本发明目的在于提供一种内置固液分离装置的污水处理生物反应器。The purpose of the present invention is to provide a sewage treatment bioreactor with a built-in solid-liquid separation device.
本发明所述的污水处理生物反应器,包括反应器主体,反应器主体上部设有出水口和尾气出口,反应器主体下部设有进水口和压缩空气入口,所述的反应器主体内部设有固液分离装置,所述的固液分离装置包括逆流管、回流管,逆流管上部与反应器内腔连通,回流管上部连接出水管,出水管连通反应器出水口;The sewage treatment bioreactor of the present invention comprises a reactor main body, the upper part of the reactor main body is provided with a water outlet and the tail gas outlet, the lower part of the reactor main body is provided with a water inlet and a compressed air inlet, and the inside of the reactor main body is provided with A solid-liquid separation device, the solid-liquid separation device includes a counterflow pipe and a return pipe, the upper part of the counterflow pipe is connected to the inner cavity of the reactor, the upper part of the backflow pipe is connected to the water outlet pipe, and the water outlet pipe is connected to the water outlet of the reactor;
所述的逆流管下方设有沉积腔,所述的沉积腔连通所述的回流管,所述的沉积腔下方设有挡泥板,沉积腔与挡泥板之间留有间隙;A deposition chamber is provided below the counterflow pipe, the deposition chamber communicates with the return pipe, a fender is provided below the deposition chamber, and a gap is left between the deposition chamber and the fender;
所述的反应器主体底部设有排泥口。The bottom of the main body of the reactor is provided with a sludge outlet.
本发明所述的固液分离装置可以设计成U形或其它形状,但最优选的是将回流管套接于逆流管外部,所述的逆流管下方的回流管内部构成所述的沉积腔。The solid-liquid separation device of the present invention can be designed in a U-shape or other shapes, but it is most preferable that the return pipe is sleeved on the outside of the reverse flow pipe, and the inside of the return pipe below the reverse flow pipe constitutes the deposition chamber.
所述的挡泥板还可同时用作导流装置,当废水和空气从反应器底部进入时,阻挡废水和空气进入固液分离装置中,从而确保固液分离装置里面的泥水完全分离,分离后的污泥及时回用,确保废水在反应器主体里停留一定的时间,以达到去除有机物的目的。所述的挡泥板优选为锥形折流板。The fender can also be used as a diversion device at the same time, when the waste water and air enter from the bottom of the reactor, it can prevent the waste water and air from entering the solid-liquid separation device, thereby ensuring that the muddy water in the solid-liquid separation device is completely separated, separated The final sludge is reused in time to ensure that the wastewater stays in the main body of the reactor for a certain period of time to achieve the purpose of removing organic matter. The fender is preferably a conical baffle.
为了使反应器内气体分布均匀,反应器内腔下部最好设有布气装置,布气装置连接压缩空气入口。In order to make the gas distribution in the reactor even, the lower part of the inner cavity of the reactor is preferably equipped with a gas distribution device, and the gas distribution device is connected to the compressed air inlet.
进一步,所述的反应器主体中部设有一个或多个取样口。Further, one or more sampling ports are provided in the middle part of the reactor main body.
再进一步,所述的反应器主体上部设有压力表。Still further, the upper part of the reactor main body is provided with a pressure gauge.
所述的污水处理生物反应器按如下方式工作:Described sewage treatment bioreactor works as follows:
1、污泥驯化:将活性污泥放入所述反应器的内腔,闷曝一定时间后,加入一定的污水和一定比例的营养物质进行驯化培养,待污泥具备一定的活性后,进行连续性生物氧化处理。1. Sludge domestication: put the activated sludge into the inner cavity of the reactor, and after a certain period of time, add a certain amount of sewage and a certain proportion of nutrients for domestication and cultivation. After the sludge has a certain activity, carry out Continuous biological oxidation treatment.
2、压力生物反应:污水由泵按一定的流量打入反应器内腔,曝气反应一定时间后,溢流到所述反应器主体内部的固液分离装置,完全分离后,污泥自固液分离装置底部自流到外部的反应器内腔,进行循环反应,上清液从设置在反应器上部的出水口流出。同时定期从排泥口排除反应器内的剩余污泥。2. Pressure biological reaction: The sewage is pumped into the inner cavity of the reactor according to a certain flow rate, and after a certain period of aeration reaction, it overflows to the solid-liquid separation device inside the main body of the reactor. After complete separation, the sludge is self-solidified. The bottom of the liquid separation device flows from the bottom of the reactor to the inner cavity of the external reactor, and the circulation reaction is carried out, and the supernatant liquid flows out from the water outlet arranged on the upper part of the reactor. At the same time, the remaining sludge in the reactor is regularly removed from the sludge outlet.
本发明所述污水处理生物反应器减少了常规的加压生化法的后需处理设备,采用内置式的固液分离装置自动进行液固分离,省去了后续沉淀处理,减化了工艺流程设备,降低了运行成本。The sewage treatment bioreactor of the present invention reduces the post-processing equipment required in the conventional pressurized biochemical method, adopts a built-in solid-liquid separation device to automatically perform liquid-solid separation, saves subsequent sedimentation treatment, and reduces process flow equipment , reducing operating costs.
(四)附图说明(4) Description of drawings
图1是实施例1所述污水处理生物反应器的结构示意图。FIG. 1 is a schematic structural view of the sewage treatment bioreactor described in Example 1.
图2是实施例1所述固液分离装置的工作示意图。Fig. 2 is a working schematic diagram of the solid-liquid separation device described in Example 1.
(五)具体实施方式(5) Specific implementation methods
下面结合实施例对本发明作进一步说明,但本发明的保护范围并不限于此。The present invention will be further described below in conjunction with the examples, but the protection scope of the present invention is not limited thereto.
实施例1Example 1
参照图1、图2,一种污水处理生物反应器,包括反应器主体1,反应器主体上部设有出水口2和尾气出口3,反应器主体1下部设有进水口4和压缩空气入口5,反应器主体1内部设有固液分离装置,固液分离装置包括逆流管6、回流管7,逆流管6上部与反应器内腔连通,回流管7上部连接出水管8,出水管8连通反应器出水口2;回流管7套接于逆流管6外部,逆流管6下方的回流管7内部构成沉积腔9,沉积腔9连通回流管7;沉积腔9下方设有挡泥板10,沉积腔9与挡泥板10之间留有间隙;反应器主体1底部设有排泥口11;反应器内腔下部设有布气装置12,布气装置12连接压缩空气入口5;反应器主体1中部设有取样口13;反应器主体1上部设有压力表14。Referring to Fig. 1 and Fig. 2, a bioreactor for sewage treatment includes a reactor main body 1, a water outlet 2 and an exhaust gas outlet 3 are provided on the upper part of the reactor main body, and a water inlet 4 and a compressed air inlet 5 are provided on the lower part of the reactor main body 1 , the reactor main body 1 is provided with a solid-liquid separation device inside, the solid-liquid separation device includes a
按下述方法进行污水的处理:Sewage is treated as follows:
1、污泥驯化阶段:取一定量的活性污泥放入反应器内腔,闷曝一定时间后,加入一定量的污水,维持反应器内COD在一定浓度(300~1000mg/L),污泥浓度在3~4g/L,并按C∶N∶P=100∶5∶1的比例投加营养物质进行驯化培养,待反应器内COD的去除率大于85%,逐步提高反应器内的COD浓度,驯化一段时间后,镜检菌胶团致密、色泽透明、微生物活动很活跃,此时可正常运行。1. Sludge domestication stage: Take a certain amount of activated sludge and put it into the inner cavity of the reactor. After a certain period of time, add a certain amount of sewage to maintain the COD in the reactor at a certain concentration (300-1000mg/L). The mud concentration is 3-4g/L, and nutrients are added according to the ratio of C:N:P=100:5:1 for acclimatization and cultivation. When the removal rate of COD in the reactor is greater than 85%, gradually increase the COD in the reactor. COD concentration, after acclimatization for a period of time, microscopic examination shows that the bacteria micelles are dense, transparent in color, and the microbial activities are very active, and they can operate normally at this time.
2、压力生物反应阶段:污水由进水口4按一定的流速打入反应器内腔,按一定的空气流量从压缩空气入口5鼓入空气,气水比控制在16∶1~20∶1,压力控制在0.05~0.8MPa,最好控制在0.1~0.2Mpa,并使其稳定。在反应器内腔曝气反应一定时间,使空气与污水充分接触反应后,溢流到反应器内部的固液分离装置,自动进行液固分离,待完全分离后,污泥自沉积腔9自流到外部的反应器内腔,进行循环反应,上清液从设置在反应器主体1上部的出水口2流出。定期从排泥口11排除反应器内的剩余污泥。2. Pressure bioreaction stage: Sewage is poured into the inner cavity of the reactor at a certain flow rate from the water inlet 4, and air is blown in from the compressed air inlet 5 at a certain air flow rate, and the air-water ratio is controlled at 16:1 to 20:1. The pressure is controlled at 0.05-0.8MPa, preferably 0.1-0.2Mpa, and made stable. Aeration reaction in the inner chamber of the reactor for a certain period of time, after the air and sewage are fully contacted and reacted, overflow to the solid-liquid separation device inside the reactor, and the liquid-solid separation is carried out automatically. After complete separation, the sludge flows from the
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EP2404879A1 (en) * | 2010-07-08 | 2012-01-11 | Paques IP. B.V. | Purifier comprising a solids separation device, and method for wastewater purification |
CN108866881B (en) * | 2018-06-22 | 2020-06-30 | 浙江新三印印染有限公司 | Rope-shaped washing machine |
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JPH11300381A (en) * | 1998-04-21 | 1999-11-02 | Toshikazu Shimodaira | Activated sludge concentration-regulated aerating and settling tank |
CN2530947Y (en) * | 2002-01-25 | 2003-01-15 | 浙江大学 | Internal recycling particle sludge bed nitrofication reactor |
CN1412130A (en) * | 2001-10-16 | 2003-04-23 | 金海洙 | Waste water treatment device using waste tyre carrier biological method |
CN2609918Y (en) * | 2003-04-14 | 2004-04-07 | 李声寿 | Self-circulation waste water biological treatment reactor |
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2005
- 2005-02-18 CN CNB2005100491127A patent/CN100344556C/en not_active Expired - Fee Related
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
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CH655083A5 (en) * | 1981-06-29 | 1986-03-27 | Sulzer Ag | Reaction vessel for biological waste-water purification plants |
CN2062728U (en) * | 1990-03-16 | 1990-09-26 | 谢绍舜 | Integrated biochemistry processor for sewage |
DE4130492A1 (en) * | 1990-09-22 | 1992-04-09 | Damann Franz Josef Dipl Ing | Bio-reactor esp. for waste water treatment - has separate compressed gas and reaction gas inlets |
US5190646A (en) * | 1991-03-11 | 1993-03-02 | Nikki Hanbai Co., Ltd. | Wastewater treating biological film tank |
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JPH11300381A (en) * | 1998-04-21 | 1999-11-02 | Toshikazu Shimodaira | Activated sludge concentration-regulated aerating and settling tank |
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CN2609918Y (en) * | 2003-04-14 | 2004-04-07 | 李声寿 | Self-circulation waste water biological treatment reactor |
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Assignee: Sobel France S. A. S. Assignor: Zhejiang University of Technology Contract record no.: 2010330001109 Denomination of invention: Bioreactor for sewage treatment Granted publication date: 20071024 License type: Exclusive License Open date: 20050921 Record date: 20100611 |
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