Fixed-Growth Nitrification of Secondary Effluent

J. Gasser, R. Miele, Ching‐lin Chen
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Abstract

A downflow submerged-bed, fixed-growth nitrification process has been successfully applied to the effluents of an activated sludge process and an independent physical-chemical treatment process. The empty-bed detention time, gas/water ratio, backwashing frequency, water temperature, supporting medium, and the ammonia limit in the nitrified effluent are identified as the major parameters for efficient process control. The relationship between the empty-bed detention time and the water temperature has been fully illustrated. Both air and industrially pure oxygen are shown to be equally effective in providing the necessary oxygen source for the biological oxidation of ammonia. The gravel is demonstrated to be superior over the sand, stone, and activated carbon as the supporting medium for the fixed-growth nitrification process. The air or oxygen is bubbled through the sparging system at the bottom of the supporting medium. The cost estimate for nitrifying 10,000,000-gal/day (37,850-m³/day) activated sludge plant effluent is shown.
二次出水的固定生长硝化
下流式沉床固定生长硝化工艺已成功应用于活性污泥工艺和独立物理化学处理工艺的出水。确定了空床停留时间、气水比、反冲洗次数、水温、支撑介质、硝化出水氨限是有效控制过程的主要参数。充分说明了空床滞留时间与水温的关系。空气和工业纯氧在为氨的生物氧化提供必要的氧气来源方面同样有效。砾石被证明优于沙子、石头和活性炭作为固定生长硝化过程的支持介质。空气或氧气通过支撑介质底部的喷射系统产生气泡。对1000000加仑/天(37850立方米/天)活性污泥厂废水进行硝化处理的成本估算如下所示。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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