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Design of Auto Mix Single Stage Anaerobic Digester and Aspen Plus Simulation for Biogas Production

机译:自动混合单级厌氧消化池的设计和沼气生产的Aspen Plus模拟

摘要

Bio fuels have been considered to be the viable alternatives and the supportive sources for the depleting fossil fuels under the objective of satisfying the energy demand. The work explored the possibility of biogas production in various operational scales. The present work can be categorized into two parts. In the first part, the work has surveyed various digester designs under operation and focused on the mixing and intermittent aeration that are not under light in the regular practice. The digester gas collector configuration that could promote the mixing and intermittent aeration was designed. The setup was run on 20 L scale with an objective of observing the gas production phenomenon. The recommended operational solutions were modified and implemented in the form of a 50 L digester setup to observe the performance improvements in attaining self-buffering capacity and sensitivity to the acidic feed stocks. Further suggested modifications lead to the final design that could promote intermittent aeration and mix the digester constituents without the use of impeller and with minimal or no power consumption depending on the amount of gas produced. An advanced design called compartmental digester design was next presented for the medium to large scale applications which was run on 200 L scale in a semi continuous mode using cow dung as substrate and was tested for the feasibility. The second part of our work focused on simulation of a two stage anaerobic digester configuration for studying the kinetics of hydrolysis, acidogenesis and acetogenesis and methanogenesis in three different reactors. In this study, kitchen waste stream were analysed for biogas production which was compared with the results of NISARGRUNA biogas plant (BARC) for the validation of the model and the model with same kinetics was then used to analyse the gas production from poultry manure
机译:在满足能源需求的目标下,生物燃料被认为是枯竭化石燃料的可行替代品和支持性资源。这项工作探索了各种规模的沼气生产可能性。目前的工作可以分为两部分。在第一部分中,这项工作对运行中的各种蒸煮器设计进行了调查,并着重于常规实践中未进行的混合和间歇曝气。设计了可以促进混合和间歇通气的沼气收集器配置。该装置以20 L规模运行,目的是观察产气现象。修改并以50 L蒸煮器设置的形式实施了推荐的操作解决方案,以观察在实现自我缓冲能力和对酸性原料的敏感性方面的性能改进。进一步建议的修改导致最终设计,该设计可促进间歇通气并在不使用叶轮的情况下混合蒸煮器的组成部分,并且根据产生的气体量而消耗的功率最少或没有。接下来介绍了一种适用于中型到大型应用的,称为隔室蒸煮器设计的高级设计,该设计以牛粪为底物,以半连续模式在200 L规模下运行,并进行了可行性测试。我们工作的第二部分集中于模拟两阶段厌氧消化池配置,以研究三个不同反应器中水解,产酸,产乙酸和产甲烷的动力学。在这项研究中,分析了厨房废物流中的沼气产生量,并与NISARGRUNA沼气厂(BARC)的结果进行了比较,以验证该模型,然后使用具有相同动力学的模型来分析家禽粪便产生的沼气。

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    Tenneti Srinivas;

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  • 年度 2015
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