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METHOD AND REACTOR FOR BIOLOGICAL REMOVAL OF NITROGEN BY AUTOTROPHIC AMMONIUM OXIDATION AND SUBSEQUENT DENITRIFICATION

机译:自养铵氧化和后续脱氮生物脱氮的方法和反应器

摘要

FIELD: ecology; water treatment.;SUBSTANCE: group of inventions can be used in water treatment. Method of biological removal of nitrogen from unrefined water involves autotrophic nitrification and subsequent denitrification. Unrefined water is passed through at least one common reactor with at least two, in particular, three successive reaction zones. At least a gaseous and/or liquid oxidiser is fed into the reactor and a first microbiological nitrification reaction zone is formed, followed by a microbiological denitrification reaction zone and, if necessary, at least one intermediate reaction zone of microbiological nitrification and microbiological denitrification. In the first reaction zone concentration of dissolved oxygen is created at least 2.5 mg/l, in an intermediate reaction zone – from 0.5 to 2.5 mg/l, and in the following reaction zone – at most 0.5 mg/l. Denitrification is carried out autotrophically. Reactor (2) for biological removal of nitrogen from unrefined water contains at least one reaction frame (8) for dispersing microorganisms, as well as means for feeding into reactor at least gaseous and/or liquid oxidizer. Reaction frame (8) is configured to rotate around its own axis and form reaction zones (3, 4, 5) for autotrophic nitrification and autotrophic denitrification during reactor operation. At least one radial internal reaction zone (3) is configured to dominate microbiological autotrophic nitrification. At least one radial external reaction zone (5) is configured to dominate microbiological autotrophic denitrification.;EFFECT: group of inventions makes it possible to accelerate removal of nitrogen with reduced volume of the reactor.;15 cl, 9 dwg
机译:领域:生态学;物质:一组发明可以用于水处理。从未精制水中生物去除氮的方法包括自养硝化和随后的反硝化。使未精制的水通过至少一个具有至少两个,特别是三个连续反应区的普通反应器。至少将气态和/或液态氧化剂进料到反应器中,并形成第一微生物硝化反应区,随后是微生物反硝化反应区,以及如果需要的话,至少一个中间反应区为微生物硝化和微生物反硝化。在第一个反应区中,溶解氧的浓度至少为2.5 mg / l,在中间反应区中为0.5至2.5 mg / l,在随后的反应区中最高为0.5 mg / l。反硝化自养地进行。用于从未精制水中生物去除氮的反应器(2)包含至少一个用于分散微生物的反应框架(8),以及至少将气态和/或液态氧化剂供入反应器的装置。反应框架(8)构造成围绕其自身的轴旋转并形成反应区(3、4、5),以在反应器运行期间进行自养硝化和自养反硝化。至少一个径向内部反应区(3)被配置为控制微生物自养硝化作用。至少一个径向外部反应区(5)配置为控制微生物自养反硝化作用;效果:一组发明可以在减少反应器体积的情况下加速脱氮; 15 cl,9 dwg

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