CN1295163C - Anaerobic ammonia oxidation reactor - Google Patents
Anaerobic ammonia oxidation reactor Download PDFInfo
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- CN1295163C CN1295163C CNB2005100616940A CN200510061694A CN1295163C CN 1295163 C CN1295163 C CN 1295163C CN B2005100616940 A CNB2005100616940 A CN B2005100616940A CN 200510061694 A CN200510061694 A CN 200510061694A CN 1295163 C CN1295163 C CN 1295163C
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- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 18
- 230000003647 oxidation Effects 0.000 title claims abstract description 15
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title abstract description 30
- 229910021529 ammonia Inorganic materials 0.000 title abstract description 15
- 239000010802 sludge Substances 0.000 claims abstract description 52
- 238000006243 chemical reaction Methods 0.000 claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000007789 sealing Methods 0.000 claims abstract description 15
- 239000002245 particle Substances 0.000 claims abstract description 4
- 238000004062 sedimentation Methods 0.000 claims description 12
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 7
- 241000894006 Bacteria Species 0.000 claims description 6
- 238000004220 aggregation Methods 0.000 claims description 2
- 230000002776 aggregation Effects 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 4
- 238000012546 transfer Methods 0.000 abstract description 4
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 abstract description 3
- 230000000694 effects Effects 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 3
- 238000005243 fluidization Methods 0.000 abstract description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 7
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 241000251468 Actinopterygii Species 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- QDHHCQZDFGDHMP-UHFFFAOYSA-N Chloramine Chemical compound ClN QDHHCQZDFGDHMP-UHFFFAOYSA-N 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000012271 agricultural production Methods 0.000 description 1
- 238000010170 biological method Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000007954 hypoxia Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000011081 inoculation Methods 0.000 description 1
- 231100000518 lethal Toxicity 0.000 description 1
- 230000001665 lethal effect Effects 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- -1 physical Substances 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 239000011150 reinforced concrete Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- 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氨氧化反应器。The invention relates to an anaerobic ammonia oxidation reactor.
背景技术Background technique
随着工农业生产的发展和人民生活水平的提高,含氮有机物的排放量急剧增加。二级生物处理的陆续上马,虽然对有机物污染起到了很好的遏制作用,但是出水的含氮量较高,依然是一个严重的环境污染源。氮素污染的危害极大,氨进入水体,不但能诱发“富营养化”,造成水生生态系统的紊乱,而且还能消耗溶解氧,造成水体缺氧,影响鱼锶的氧传递,使鱼类致死;与氯气作用生成氯胺,影响氯化消毒处理。因此经济有效地控制氮素污染已势在必行。With the development of industrial and agricultural production and the improvement of people's living standards, the discharge of nitrogenous organic matter has increased dramatically. Secondary biological treatment has been launched one after another. Although it has played a good role in curbing organic pollution, the high nitrogen content in the effluent is still a serious source of environmental pollution. Nitrogen pollution is extremely harmful. Ammonia entering the water body can not only induce "eutrophication" and cause the disorder of the aquatic ecosystem, but also consume dissolved oxygen, resulting in hypoxia in the water body, affecting the oxygen transfer of strontium in fish, making fish Lethal; react with chlorine gas to form chloramine, which affects chlorination disinfection treatment. Therefore, it is imperative to control nitrogen pollution economically and effectively.
废水脱氮的方法较多,有物理法、化学法和生物法等。由于种种原因,物理、化学法的应用受到很大限制,目前国内外主要采用生物脱氮技术。厌氧氨氧化反应可将氨和亚硝酸盐转化为氮气,消除氨对环境的影响。因此,研究和开发厌氧氨氧化反应器具有重要的现实意义。There are many methods for denitrification of wastewater, including physical, chemical and biological methods. Due to various reasons, the application of physical and chemical methods is greatly restricted. At present, biological denitrification technology is mainly used at home and abroad. Anammox reaction can convert ammonia and nitrite into nitrogen gas, eliminating the impact of ammonia on the environment. Therefore, the research and development of anammox reactor has important practical significance.
现有的厌氧氨氧化反应器主要由厌氧池演变而来。为了保证装置中有一定数量的微生物(活性污泥)进行厌氧氨氧化作用,一般在厌氧池后建造二次沉淀池,用以分离活性污泥,一方面满足厌氧池所需的活性污泥,另一方面满足出水水质要求。以二沉池分离活性污泥,并通过回流泵送回厌氧池,不仅增加设备,消耗动力,而且会破坏活性污泥结构,不利于形成沉淀性能优良的颗粒污泥和泥水分离。The existing anammox reactors are mainly evolved from anaerobic tanks. In order to ensure that there is a certain amount of microorganisms (activated sludge) in the device for anaerobic ammonia oxidation, a secondary sedimentation tank is generally built after the anaerobic tank to separate the activated sludge. On the one hand, it can meet the activity required by the anaerobic tank. Sludge, on the other hand, meets the requirements of effluent water quality. Separating the activated sludge with the secondary settling tank and sending it back to the anaerobic tank through the reflux pump not only increases the equipment and consumes power, but also destroys the structure of the activated sludge, which is not conducive to the formation of granular sludge with excellent sedimentation performance and the separation of mud and water.
发明内容Contents of the invention
本发明的目的是提供一种厌氧氨氧化反应器。The purpose of the present invention is to provide a kind of anaerobic ammonium oxidation reactor.
厌氧氨氧化反应器具有圆柱形反应器本体,在反应器本体下端设有进水管,反应器本体上端设有污泥沉淀区、溢流堰、密封盖,在污泥沉淀区下端设有污泥回流缝,反应器内部设有搅拌器,在密封盖上设有搅拌轴套筒和出气口,反应器内厌氧氨氧化菌以颗粒污泥的形态存在。The anaerobic ammonium oxidation reactor has a cylindrical reactor body, with a water inlet pipe at the lower end of the reactor body, a sludge settling area, an overflow weir, and a sealing cover at the upper end of the reactor body, and a sludge settling area at the lower end of the sludge settling area. There is a stirrer inside the reactor, and a stirring shaft sleeve and an air outlet on the sealing cover. The anammox bacteria in the reactor exist in the form of granular sludge.
本发明的优点:1)进行厌氧氨氧化反应的微生物以颗粒污泥的形态存在,厌氧氨氧化反应潜力大,泥水分离效果好;2)沉淀室设置在反应器本体上部外环,结构紧凑,省去了二次沉淀池和污泥回流设施,避免了回流泵对颗粒污泥的破坏;3)搅拌器以一定速度运行,使得反应器内污水与颗粒污泥充分接触,强化了传质过程;4)反应器内无死区,污泥的流化性能好,运行性能稳定;5)该反应器具有很好的厌氧氨氧化性能,能承受高进水氨浓度,具有高容积转化效率。Advantages of the present invention: 1) The microorganisms performing the anammox reaction exist in the form of granular sludge, the anaerobic ammonium oxidation reaction potential is large, and the mud-water separation effect is good; 2) the settling chamber is arranged on the upper outer ring of the reactor body, and the It is compact, eliminating the need for secondary sedimentation tanks and sludge return facilities, and avoiding the damage of the return pump to the granular sludge; 3) The agitator runs at a certain speed, so that the sewage in the reactor is fully in contact with the granular sludge, and strengthens the transmission process. 4) There is no dead zone in the reactor, the fluidization performance of the sludge is good, and the operation performance is stable; 5) The reactor has good anaerobic ammonium oxidation performance, can withstand high influent ammonia concentration, and has high volumetric conversion efficiency .
附图说明Description of drawings
图1是厌氧氨氧化反应器结构示意图;Fig. 1 is a structural representation of anaerobic ammonium oxidation reactor;
图2是厌氧氨氧化反应器结构俯视图;Fig. 2 is a structural top view of anaerobic ammonium oxidation reactor;
图中:圆柱形反应器本体1、进水管2、污泥沉淀区3、溢流堰4、密封盖5、污泥回流缝6、搅拌器7、搅拌轴套筒8、出气口9。In the figure:
具体实施方式Detailed ways
如图所示,厌氧氨氧化反应器具有圆柱形反应器本体1,在反应器本体下端设有进水管2,反应器本体上端设有污泥沉淀区3、溢流堰4、密封盖5,在污泥沉淀区下端设有污泥回流缝6,反应器内部设有搅拌器7,在密封盖上设有搅拌轴套筒8和出气口9,反应器内厌氧氨氧化菌以颗粒污泥的形态存在。As shown in the figure, the anammox reactor has a
所述的圆柱形反应器本体1高径比H/D为1.5~2.5,下部斜面的水平倾角α为50°~55°。污泥沉淀区3的高度占反应器本体高度的1/5~1/6,污泥沉淀区的体积占总体积的1/6~1/7,污泥回流缝(6)的底板与水平面之间的夹角β为50°~55°。进水管2设置于反应器底部以上15~20mm处。搅拌器设置于反应器本体中心离反应器底部50~150mm处,搅拌轴通过浸没于反应液中的套筒连结。密封盖为活动型,呈圆柱形,倒扣在反应器本体外侧,密封盖筒体下端浸没在反应液的30~50mm处。厌氧氨氧化颗粒污泥是一种由厌氧氨氧化细菌聚集而成的生物颗粒。The height-to-diameter ratio H/D of the
本发明的密封盖为活动型,呈圆柱形,倒扣在反应器本体外侧,需要时可与反应器本体分离;密封盖筒体下端浸在反应液中,可防止外部空气进入反应区;密封盖上设有出气口,可排出反应器内产生的气体。污泥沉淀区下端设有污泥回流缝,可让沉淀区的污泥返回反应区。反应器内部设有搅拌器,可强化基质和生物的接触,搅拌轴通过浸没在反应液中的套筒与搅拌器连结,可防止外部空气进入反应区。反应器内厌氧氨氧化菌以颗粒污泥的形态存在,沉淀性能优良,易于泥水分离。The sealing cover of the present invention is a movable type, cylindrical in shape, upside down on the outside of the reactor body, and can be separated from the reactor body when necessary; the lower end of the sealing cover cylinder body is immersed in the reaction solution, which can prevent external air from entering the reaction zone; There is a gas outlet on the cover to discharge the gas generated in the reactor. There is a sludge return slot at the lower end of the sludge settling area, allowing the sludge in the settling area to return to the reaction area. There is a stirrer inside the reactor, which can strengthen the contact between the substrate and the organism, and the stirring shaft is connected with the stirrer through a sleeve immersed in the reaction solution, which can prevent external air from entering the reaction zone. The anammox bacteria in the reactor exist in the form of granular sludge, which has excellent sedimentation performance and is easy to separate mud and water.
厌氧氨氧化反应器可用钢材或钢筋混凝土构建,反应室和污泥沉淀室合建于同一圆型池中。接种污泥投加至反应区。污水通过进水管导入反应区底部。反应区通过搅拌机搅拌使固液充分接触,有效提高传质效率。污泥沉淀区环绕反应器本体。沉淀区液流上升速度较慢,被带至沉淀区的污泥得到有效分离,并依靠污泥重力返回反应区。出水由沉淀区溢流堰排出。The anaerobic ammonium oxidation reactor can be constructed with steel or reinforced concrete, and the reaction chamber and the sludge sedimentation chamber are built together in the same circular pool. Inoculation sludge was added to the reaction zone. Sewage is introduced into the bottom of the reaction zone through the water inlet pipe. The reaction zone is stirred by a stirrer to fully contact the solid and liquid, effectively improving the mass transfer efficiency. The sludge settling zone surrounds the reactor body. The rising speed of the liquid flow in the sedimentation area is relatively slow, and the sludge brought to the sedimentation area is effectively separated and returned to the reaction area by the gravity of the sludge. The effluent is discharged from the overflow weir in the sedimentation area.
本发明通过污泥颗粒化来改善活性污泥沉降性能,通过在装置上部合建沉淀池来回收颗粒污泥、提高污泥浓度,通过搅拌来提高传质效率。试验证明,据此开发的新型厌氧氨氧化反应器具有很好的厌氧氨氧化性能。在pH7.5~8.5,反应温度25~35℃的条件下,能承受高进水氨和亚硝酸盐浓度,具有高容积转化效率,运行性能稳定。The invention improves the settling performance of the activated sludge by granulating the sludge, recovers the granular sludge by building a settling tank on the upper part of the device, increases the sludge concentration, and improves the mass transfer efficiency by stirring. The test proves that the new anammox reactor developed accordingly has good anammox performance. Under the conditions of pH 7.5-8.5 and reaction temperature 25-35°C, it can withstand high concentrations of ammonia and nitrite in the feed water, has high volumetric conversion efficiency, and has stable operating performance.
Claims (7)
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CN102493622B (en) * | 2011-12-21 | 2014-03-05 | 湖北格林森新型建材科技有限公司 | Wallboard installing component |
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JP5582388B2 (en) * | 2010-03-12 | 2014-09-03 | 三菱レイヨン株式会社 | Biological treatment system and biological treatment method |
CN101913704B (en) * | 2010-08-10 | 2012-01-25 | 浙江大学 | Anchi Reactor |
CN102249407A (en) * | 2011-05-13 | 2011-11-23 | 杭州师范大学 | High-efficiency anaerobic ammonia oxidation reactor |
CN102730829A (en) * | 2012-06-13 | 2012-10-17 | 杭州师范大学 | Ordered internally-circulated anaerobic ammoxidation reactor |
CN102775027B (en) * | 2012-08-15 | 2013-07-24 | 北京城市排水集团有限责任公司 | Granular sludge integrated autotrophic nitrogen removal device and operating method thereof |
CN114477441A (en) * | 2022-03-11 | 2022-05-13 | 西安建筑科技大学 | Dynamic membrane anaerobic ammonia oxidation reactor |
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CN2717941Y (en) * | 2004-08-02 | 2005-08-17 | 西安建筑科技大学 | Liquid floating cover sequential batch intermittent anaerobic reactor |
CN1689986A (en) * | 2004-04-23 | 2005-11-02 | 中国科学院生态环境研究中心 | Aerobic start-up method of anammox reactor |
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CN2717941Y (en) * | 2004-08-02 | 2005-08-17 | 西安建筑科技大学 | Liquid floating cover sequential batch intermittent anaerobic reactor |
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