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The operation of a micro-scale cogeneration system prototype - A comprehensive experimental and numerical analysis

机译:微级热电联产系统原型的操作 - 全面的实验和数值分析

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This paper shows the results of experimental and numerical investigations related to the energy use of straw from the point of view of its preparation (drying), combustion, energy production and emissions. Experimental works on straw drying were conducted on a specially developed installation based on dedicated batch straw dryers, which use flue gas, coming from a 500 kWth boiler, as a drying medium. The further part of the work was conducted on a prototype of a micro-scale cogeneration system that operates according to a low temperature Rankine cycle and it is powered by a 100 kWth biomass-fired batch boiler. Conducted so far research allowed to analyse selected operation aspects of the developed system. An analysis of straw drying, proximate, ultimate, and heating value analysis, heat generation process in the boiler, steam generation process in the evaporator and superheater, steam engine operation as well as dust emissions during straw combustion related to the boiler return temperature were presented. Energy transferred from flue gases to straw with a high value of moisture content was 5.75 kW, which allowed to evaporate about 18.6 kg of water from 192 kg wheat straw bale. The moisture content was reduced from 36.9 to 27.2%. The power generated in the system was lower than the one expected, since only 1.15 kWel was achieved which was about 1% of the boiler?s heat capacity. Such result was caused by construction restrictions of the installation. Experimental results were supported by dynamic simulations performed in TRNSYS software. The simulations were performed for both the current configuration of the system and suggested modifications. Simulation results showed, that the expected power generation in the final version of the system should be at a level of 10 kWel. Results obtained during the analysis of multi-cyclone operation showed, that the concentration of dust was reduced in a range from 55% to even 85% depending on the temperature of the boiler return and flue gas flowrate in multi-cyclone.
机译:本文显示了与其制备(干燥),燃烧,能源生产和排放的秸秆的能量使用有关的实验性和数值研究的结果。在基于专用批量秸秆干燥器的专用安装装置上进行了对秸秆干燥的实验工作,该批量秸秆干燥器使用烟气,来自500 kWth锅炉,作为干燥介质。该工作的另一部分是在微级热电联产系统的原型上进行的,该系统根据低温朗肯循环操作,它由100夸克生物染色批次锅炉供电。迄今为止进行了迄今为止,允许分析开发系统的所选操作方面。呈分析秸秆干燥,近,终极和加热值分析,蒸发器和过热器中的蒸汽发电过程,蒸汽发动机操作以及秸秆燃烧中的蒸汽发动机,蒸汽发动机的蒸汽发动过程,蒸汽发动机与锅炉返回温度相关的灰尘排放。从烟道气转移到具有高水分含量的秸秆的能量为5.75千瓦,从192 kg小麦秸秆捆包中蒸发约18.6kg水。水分含量从36.9减少到27.2%。系统中产生的功率低于预期的功率,因为​​只有1.15 kWel的热容量约为1%。这些结果是由安装的施工限制引起的。在Trnsys软件中执行的动态模拟支持实验结果。对系统的当前配置进行了模拟和建议的修改。模拟结果显示,系统最终版本的预期发电应为10 kWel的水平。在分析多旋风操作期间获得的结果,取决于锅炉返回和多旋风中烟气流量的温度,粉尘浓度降低了55%至甚至85%。

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