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Energy Consumption Trends in BNR Mixing Technologies

机译:BNR混合技术的能耗趋势

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Secondary treatment is typically the largest energy consumer at municipal wastewater treatment plants (WWTPs), with aeration representing most of this demand. The energy used in the activated sludge process generally increases with enhanced levels of treatment. As WWTPs face more stringent nitrogen and phosphorus effluent limits, energy requirements for pumping and mixing will continue to increase relative to aeration. Although much of the energy reduction efforts in activated sludge treatment have been focused on reducing aeration energy and demand, comparatively, limited attention has been focused on reducing the energy associated with recycle pumping and mixing. Biological nutrient removal (BNR) processes generally include multiple unaerated anoxic and/or anaerobic zones to remove nitrogen and phosphorus, respectively. Greater unaerated tankage requirements are associated with increased levels of treatment; for example five-stage BNR processes require anaerobic, pre-anoxic and post-anoxic zones. These unaerated zones need to be mixed in order to maintain solids in suspension and provide efficient treatment. Unaerated tankage may account for more than 50% of the total activated sludge volume in a five-stage BNR process, and mixing requirements for these zones can exceed aeration requirements, particularly in underloaded systems. For example, Figure 1 illustrates a case in which the energy consumed by the mixing process was significant in comparison to the aeration process. The Figure illustrates the breakdown of energy consumption in the biological treatment system at a 20 million gallon per day (mgd) 5-stage BNR plant located in North Carolina. At this facility, the jet aeration mixing system consumed 32 % of the total energy consumption. Submersible mixers, vertical turbine mixers and jet mixing systems have provided decades of reliable mixing of unaerated zones at municipal WWTPs. These technologies have typically been applied at a range of mixing energy densit
机译:二次治疗通常是市政废水处理厂(WWTPS)最大的能源消费者,曝气代表了大部分需求。活性污泥过程中使用的能量通常随着治疗水平的增强而增加。由于WWTPS面向更严格的氮和磷流出限值,泵送和混合的能量要求相对于通气将继续增加。虽然活性污泥处理中的大部分能量减少努力都集中在减少曝气能源和需求上,但相对轻地,有限的注意力集中在减少与回收泵送和混合相关的能量。生物养分除去(BNR)工艺通常包括多个未出现的缺氧和/或厌氧区以分别除去氮和磷。更大的未经淘汰的奶油需求与增加的治疗水平有关;例如,五阶段BNR过程需要厌氧,缺氧和缺氧区。需要混合这些不合适的区域以保持悬浮液中的固体并提供有效的处理。未经盎司的牛奶库可能占5阶段BNR过程中总活性污泥体积的50%以上,这些区域的混合要求可能超过曝水要求,特别是在欠载系统中。例如,图1示出了与曝气过程相比,混合过程所消耗的能量的情况。该图说明了生物治疗系统中的能量消耗崩溃,每天2000万加仑(MGD)5阶段BNR植物位于北卡罗来纳州。在该设施,喷射曝气混合系统消耗了总能耗的32%。潜水搅拌机,垂直涡轮机混合器和喷射混合系统已经提供了几十年代在城市WWTPS在城市WWTPS的不合作区混合。这些技术通常应用于一系列混合能量密度

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