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A NEW KIND OF MULTIFUNCTIONAL ENERGY SYSTEM (MES) BASED ON MODERATE CONVERSION OF CHEMICAL ENERGY OF FOSSIL FUELS

机译:基于化石燃料化学能适度转化的新型多功能能源系统(MES)

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This paper proposes a new kind of multifunctional energy system (MES) using natural gas and coal to more efficiently and more economically produce methanol and power. Traditional chemical processes pursue high conversion ratios of chemical energy of fuels. The new MES focuses on the moderate conversion of the chemical energy of fuels. To do this, about 50% of the coal is partially gasified with pure oxygen and steam as oxidant, and then the unconverted residuals (char) and natural gas are utilized synthetically by char-fired reforming to generate syngas. The combustion of char drives the methane/steam reforming reaction. Here, the reforming reaction is also moderately converted, and the reforming temperature is decreased 100°C-150°C compared with that of the conventional method. The carbon-rich syngas from the partial gasifier of coal and hydrogen-rich syngas from char-fired reformer are mixed together and converted into methanol at a proper conversion ratio (lower than that of conventional chemical process). Finally, the unconverted syngas is used in a combined cycle as fuel for power generation. As a result, the total exergy efficiency of the new system is 55-60%. Comparing to individual systems, including IGCC and natural gas-based methanol plants (MSN), this new system can generate 10-20% more electricity with the same quantity of fossil fuels input and methanol output. In addition, the possibility of reducing the size of gasifier, reformer, and methanol synthesis reactor may reduce investment costs accordingly. These results may provide a new way to use coal and natural gas more efficiently and economically.
机译:本文提出了一种新型的利用天然气和煤炭的多功能能源系统(MES),以更高效,更经济地生产甲醇和电力。传统的化学过程追求燃料化学能的高转化率。新的MES专注于燃料化学能的适度转化。为此,约50%的煤被纯氧和蒸汽作为氧化剂部分气化,然后未转化的残渣(焦炭)和天然气通过焦炭重整法合成利用,以生成合成气。焦炭的燃烧驱动甲烷/蒸汽重整反应。在此,重整反应也被适度地转化,并且与常规方法相比,重整温度降低了100℃至150℃。将煤的部分气化炉中的富碳合成气与焦炭重整器中的富氢合成气混合在一起,并以适当的转化率转化为甲醇(低于常规化学工艺的转化率)。最后,未转化的合成气在联合循环中用作发电的燃料。结果,新系统的总火用效率为55-60%。与包括IGCC和基于天然气的甲醇工厂(MSN)在内的单个系统相比,该新系统在输入相同数量的化石燃料和甲醇的情况下,可以产生10-20%的电力。另外,减小气化器,重整器和甲醇合成反应器的尺寸的可能性可以相应地降低投资成本。这些结果可能提供一种更有效,更经济地使用煤炭和天然气的新方法。

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