CN105859085A - Cone-shaped anaerobic reactor - Google Patents
Cone-shaped anaerobic reactor Download PDFInfo
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- CN105859085A CN105859085A CN201610411782.7A CN201610411782A CN105859085A CN 105859085 A CN105859085 A CN 105859085A CN 201610411782 A CN201610411782 A CN 201610411782A CN 105859085 A CN105859085 A CN 105859085A
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- reactor
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- anaerobic reactor
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- 239000007788 liquid Substances 0.000 claims abstract description 19
- 239000012528 membrane Substances 0.000 claims abstract description 3
- 238000010992 reflux Methods 0.000 claims description 8
- 239000010802 sludge Substances 0.000 description 12
- 230000029087 digestion Effects 0.000 description 6
- 238000000034 method Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
Classifications
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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
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
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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
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Molecular Biology (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种厌氧反应器,尤其涉及一种用于剩余污泥厌氧消化的反应器。The invention relates to an anaerobic reactor, in particular to a reactor for anaerobic digestion of excess sludge.
背景技术Background technique
剩余污泥厌氧消化可以得到沼气,可以使污泥稳定,也可以使污泥固形物得到削减,是污水处理厂的一个重要的工艺单元。剩余污泥厌氧消化常用的反应器有柱形池和卵形池,其所需土建费用很高,从而使得很多污水处理厂不得不放弃了污泥消化这一处理单元。从节约土建费用的考虑,本专利提出了锥形池的设想。Anaerobic digestion of excess sludge can obtain biogas, stabilize sludge, and reduce solids in sludge. It is an important process unit in sewage treatment plants. Commonly used reactors for anaerobic digestion of excess sludge include cylindrical tanks and oval tanks, which require high civil engineering costs, which makes many sewage treatment plants have to give up the treatment unit of sludge digestion. From the consideration of saving civil engineering costs, this patent proposes the idea of a conical pool.
发明内容Contents of the invention
本发明所要解决的技术问题是提供一种锥形厌氧反应器,由进料系统、反应器、回流系统和一体式双膜气柜组成,其特征在于,所述反应器主体为锥形;所述回流系统由浮桶、集液器、导流框、回流泵组成,所述浮桶漂浮于液面,所述集液器挂于浮桶并位于液面以下适当位置,所述导流框为固定于集液器四周的闭合框体,所述回流泵出口位于反应器下部;The technical problem to be solved by the present invention is to provide a conical anaerobic reactor, which is composed of a feed system, a reactor, a reflux system and an integrated double-membrane gas tank. It is characterized in that the main body of the reactor is conical; The return system is composed of a floating bucket, a liquid collector, a diversion frame, and a return pump. The floating barrel floats on the liquid surface. The frame is a closed frame fixed around the liquid collector, and the outlet of the reflux pump is located at the lower part of the reactor;
作为优选,一种锥形厌氧反应器,其特征在于,所述反应器主体为锥台。Preferably, a conical anaerobic reactor is characterized in that the main body of the reactor is a truncated cone.
作为优选,一种锥形厌氧反应器,其特征在于,所述反应器主体为锥形且和柱体形成组合。Preferably, a conical anaerobic reactor is characterized in that the main body of the reactor is conical and combined with a column.
作为优选,一种锥形厌氧反应器,其特征在于,所述反应器主体为锥台且和柱体形成组合。Preferably, a conical anaerobic reactor is characterized in that the main body of the reactor is a frustum of a cone and is combined with a column.
作为优选,一种锥形厌氧反应器,其特征在于,所述反应器主体侧壁为外倾斜壁。Preferably, a conical anaerobic reactor is characterized in that the side wall of the main body of the reactor is an outer inclined wall.
作为优选,一种锥形厌氧反应器,其特征在于,所述反应器主体侧壁为外倾斜壁,斜壁上部有直壁。Preferably, a conical anaerobic reactor is characterized in that the side wall of the main body of the reactor is an outer inclined wall, and the upper part of the inclined wall has a straight wall.
与现有技术相比,本发明的一种锥形厌氧反应器的有益效果是:可在土地上挖一个锥形池,做好防渗,替代钢砼结构,节约土建费用。Compared with the prior art, the beneficial effect of the conical anaerobic reactor of the present invention is that a conical pool can be dug on the ground to prevent seepage, replace the steel-concrete structure, and save civil engineering costs.
附图说明Description of drawings
图1是本发明实施例一的一种锥形厌氧反应器的结构示意图。Fig. 1 is a schematic structural view of a conical anaerobic reactor in Example 1 of the present invention.
图2是本发明实施例二的一种锥形厌氧反应器的结构示意图。Fig. 2 is a schematic structural view of a conical anaerobic reactor in Example 2 of the present invention.
具体实施方式detailed description
下面结合附图详细说明本发明的实施例。Embodiments of the present invention will be described in detail below in conjunction with the accompanying drawings.
实施例一:Embodiment one:
如图1所示的一种锥形厌氧反应器,包括:进料系统1、反应器2、回流系统3和一体式双膜气柜4,反应器2为锥形;回流系统3由浮桶3-1、集液器3-2、导流框3-3、回流泵3-4组成,浮桶3-1漂浮于液面,集液器3-2挂于浮桶3-1并位于液面以下适当位置,导流框3-3固定于集液器四周的并形成闭合框体,回流泵3-4出口位于反应器下部。A kind of conical anaerobic reactor as shown in Figure 1, comprises: feeding system 1, reactor 2, reflux system 3 and integrated double film gas cabinet 4, and reactor 2 is conical; Composed of barrel 3-1, liquid collector 3-2, diversion frame 3-3, and return pump 3-4, the floating barrel 3-1 floats on the liquid surface, and the liquid collector 3-2 is hung on the floating barrel 3-1 and Located at an appropriate position below the liquid surface, the guide frame 3-3 is fixed around the liquid collector and forms a closed frame body, and the outlet of the reflux pump 3-4 is located at the lower part of the reactor.
下面对实施例一的工作过程简要介绍如下:Below the working process of embodiment one is briefly introduced as follows:
剩余污泥由进料系统1进入反应器2底部,向上流动并进行厌氧消化,为使反应器2内污泥有良好的混合,开启回流系统3。The remaining sludge enters the bottom of the reactor 2 from the feed system 1, flows upward and undergoes anaerobic digestion. In order to make the sludge in the reactor 2 well mixed, the reflux system 3 is opened.
本专利虽从节约土建费用的思路进行的设计,但锥形结构本身,还为污泥消化带来了两大优点:一是,从下向上,污泥上流速度递减,污泥颗粒易沉于反应器下部,从而使得水力停留时间和固体停留时间分离,可使污泥颗粒得到更好的消化;二是,集液器3-2不断地将上层液体抽至下层,有效地防止了浮渣结壳。Although this patent is designed from the idea of saving civil engineering costs, the conical structure itself has brought two advantages to sludge digestion: first, from the bottom to the top, the upward flow velocity of the sludge decreases, and the sludge particles are easy to sink in The lower part of the reactor, so that the hydraulic retention time and the solid retention time are separated, so that the sludge particles can be better digested; the second is that the liquid collector 3-2 continuously pumps the upper liquid to the lower layer, effectively preventing the scum Crust.
实施例二:实施例二为实施例一的一种变形,除反应器2为锥形和柱形组合外,其总体结构和工作原理与实施例一完全一样。Embodiment 2: Embodiment 2 is a modification of Embodiment 1, except that the reactor 2 is a combination of cone and column, its overall structure and working principle are exactly the same as Embodiment 1.
以上实施例仅为本发明的示例性实施例,不用于限制本发明,本发明的保护范围由权利要求书限定。本领域技术人员可以在本发明的实质和保护范围内,对本发明做出各种修改或等同替换,这种修改或等同替换也应视为落在本发明的保护范围内。The above embodiments are only exemplary embodiments of the present invention, and are not intended to limit the present invention, and the protection scope of the present invention is defined by the claims. Those skilled in the art can make various modifications or equivalent replacements to the present invention within the spirit and protection scope of the present invention, and such modifications or equivalent replacements should also be deemed to fall within the protection scope of the present invention.
Claims (6)
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CN201610411782.7A CN105859085A (en) | 2016-06-14 | 2016-06-14 | Cone-shaped anaerobic reactor |
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CN201610411782.7A CN105859085A (en) | 2016-06-14 | 2016-06-14 | Cone-shaped anaerobic reactor |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107583763A (en) * | 2017-10-11 | 2018-01-16 | 于清 | Speed change fluid bed can digested sludge knockout tower |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101585601A (en) * | 2009-06-15 | 2009-11-25 | 中国市政工程中南设计研究院 | Monomer ultra-large volume steel post cone high-temperature anaerobic fermentation system |
CN102351382A (en) * | 2011-09-06 | 2012-02-15 | 北京昊业怡生科技有限公司 | Combined treatment method of leachate and excrement wastewater |
-
2016
- 2016-06-14 CN CN201610411782.7A patent/CN105859085A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101585601A (en) * | 2009-06-15 | 2009-11-25 | 中国市政工程中南设计研究院 | Monomer ultra-large volume steel post cone high-temperature anaerobic fermentation system |
CN102351382A (en) * | 2011-09-06 | 2012-02-15 | 北京昊业怡生科技有限公司 | Combined treatment method of leachate and excrement wastewater |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107583763A (en) * | 2017-10-11 | 2018-01-16 | 于清 | Speed change fluid bed can digested sludge knockout tower |
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