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开发同时进行部分硝化、厌氧氨氧化和反硝化(SNAD)的中试规模工艺,以去除肥料工业废水中的氨。

Development of a simultaneous partial nitrification, anaerobic ammonia oxidation and denitrification (SNAD) bench scale process for removal of ammonia from effluent of a fertilizer industry.

机构信息

Department of Microbiology and Biotechnology Centre, Faculty of Science, The Maharaja Sayajirao University of Baroda, Vadodara 390 002, Gujarat, India.

出版信息

Bioresour Technol. 2013 Feb;130:390-7. doi: 10.1016/j.biortech.2012.12.066. Epub 2012 Dec 20.

Abstract

A simultaneous partial nitrification, anammox and denitrification (SNAD) process was developed for the treatment of ammonia laden effluent of a fertilizer industry. Autotrophic aerobic and anaerobic ammonia oxidizing biomass was enriched and their ammonia removal ability was confirmed in synthetic effluent system. Seed consortium developed from these was applied in the treatment of effluent in an oxygen limited bench scale SNAD type (1L) reactor run at ambient temperature (∼30°C). Around 98.9% ammonia removal was achieved with ammonia loading rate 0.35kgNH(4)(+)-N/m(3)day in the presence of 46.6mg/L COD at 2.31days hydraulic retention time. Qualitative and quantitative analysis of the biomass from upper and lower zone of the reactor revealed presence of autotrophic ammonia oxidizing bacteria (AOB), Planctomycetes and denitrifiers as the dominant bacteria carrying out anoxic oxidation of ammonia in the reactor. Physiological and molecular studies strongly indicate presence of anammox bacteria in the anoxic zone of the SNAD reactor.

摘要

针对化肥厂含氨废水,开发了同步部分硝化、厌氧氨氧化和反硝化(SNAD)工艺。在合成废水系统中,富集了自养好氧和厌氧氨氧化生物量,并证实了其去除氨的能力。从这些生物量中开发的种子混合物被应用于在氧气有限的实验室规模 SNAD 型(1L)反应器中处理废水,该反应器在环境温度(约 30°C)下运行。在水力停留时间为 2.31 天、COD 为 46.6mg/L 的条件下,氨负荷为 0.35kgNH(4)(+)-N/m(3)day 时,氨去除率达到 98.9%。对反应器上下区的生物量进行定性和定量分析表明,存在自养氨氧化细菌(AOB)、浮霉菌和反硝化菌,它们是在反应器中进行缺氧氨氧化的主要细菌。生理和分子研究强烈表明,SNAD 反应器的缺氧区存在厌氧氨氧化菌。

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