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Combined ammonia recovery and solid oxide fuel cell use at wastewater treatment plants for energy and greenhouse gas emission improvements

机译:氨恢复和固体氧化物燃料电池用于能量和温室气体排放改进的废水处理厂

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Current standard practice at wastewater treatment plants (WWTPs) involves the recycling of digestate liquor, produced from the anaerobic digestion of sludge, back into the treatment process. However, a significant amount of energy is required to enable biological breakdown of ammonia present in the liquor. This biological processing also results in the emission of damaging quantities of greenhouse gases, making diversion of liquor and recovery of ammonia a noteworthy option for improving the sustainability of wastewater treatment. This study presents a novel process which combines ammonia recovery from diverted digestate liquor for use (alongside biomethane) in a solid oxide fuel cell (SOFC) system for implementation at WWTPs. Aspen Plus V.8.8 and numerical steady state models have been developed, using data from a WWTP in West Yorkshire (UK) as a reference facility (750,000p.e.). Aspen Plus simulations demonstrate an ability to recover 82% of ammoniacal nitrogen present in digestate liquor produced at the WWTP. The recovery process uses a series of stripping, absorption and flash separation units where water is recovered alongside ammonia. This facilitates effective internal steam methane reforming in the fuel cell with a molar steam:CH4 ratio of 2.5. The installation of the process at the WWTP used as a case of study has the potential to make significant impacts energetically and environmentally; findings suggest the treatment facility could transform from a net consumer of electricity to a net producer. The SOFC has been demonstrated to run at an electrical efficiency of 48%, with NH3 contributing 4.6% of its power output It has also been demonstrated that 3.5 kg CO(2)e per person served by the WWTP could be mitigated a year due to a combination of emissions savings by diversion of ammonia from biological processing and lifecyde emissions associated with the lack of reliance on grid electricity.
机译:废水处理厂(WWTPS)的目前的标准实践涉及从污泥的厌氧消化生产的消化液中的回收,回到处理过程中。然而,需要大量的能量来实现氨中存在的氨的生物分解。这种生物处理还会导致损坏损坏的温室气体量,使液体的转移和氨的回收,以改善废水处理的可持续性。该研究呈现了一种新的方法,将氨恢复与转移的消化液中的氨恢复相结合用于在WWTPS的固体氧化物燃料电池(SOFC)系统中使用(沿着生物甲烷)以实施。已经开发了Aspen Plus V.8.8和数值稳态模型,使用来自West Yorkshire(英国)的WWTP中作为参考设施(750,000P.E)的数据。 Aspen Plus模拟证明了在WWTP中产生的消化液中恢复82%的氨基氮。恢复过程使用一系列剥离,吸收和闪光分离单元,其中水沿氨回收。这有助于具有摩尔蒸汽的燃料电池中的有效内部蒸汽甲烷重整:Ch 4比为2.5。在WWTP中使用作为研究的案例的过程的安装有可能在大力和环境中产生重大影响;调查结果表明治疗设施可以从净消费者转换为净生产商。已证明SOFC以48%的电效率运行,NH3有助于4.6%的电力输出,也已经证明了由WWTP服务的3.5千克CO(2)e可能会减轻一年从生物加工和生物加工和Lifecyde排放的转移节省的排放量的组合与缺乏依赖网格电网。

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