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首页> 外文期刊>Energy & fuels >Stone Dust Looping for Ventilation Air Methane Abatement: A 1 m~3/s Pilot-Scale Study
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Stone Dust Looping for Ventilation Air Methane Abatement: A 1 m~3/s Pilot-Scale Study

机译:石屑循环用于通风甲烷减排:1 m〜3 / s中试研究

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摘要

Ventilation air methane (VAM) emissions are a significant contributor to fugitive greenhouse gas emissions at underground coal mines. The stone dust looping (SDL) process is a novel technology developed at The University of Newcastle, Australia, for VAM abatement. The SDL process is a cyclic process in which calcium oxide (CaO) is first obtained from the calcination of limestone (CaCO3). CaO is then used to simultaneously oxidize VAM (methane concentrations of 0.1-1 vol % in air) and capture carbon dioxide (CO2) produced to form CaCO3. The two cycles can be performed in a single reactor, or the process can be performed continuously in dual interconnected reactors. Preliminary experiments on the SDL process have previously been performed at laboratory scale. In this study, further laboratory-scale studies were conducted in conjunction with pilot-scale SDL investigations in a single 1 m(3)/s fluidized bed reactor. The effect of inventory size (1-2 tonnes of CaCO3), operating temperature (565-700 degrees C), and flow rate (1-1.7 m(3)/s) on methane conversion was investigated. At temperatures of 600 degrees C and above, >99.5% methane conversion was achieved for all inventory sizes and flow rates examined. At temperatures of 565 and 575 degrees C, 41 and 70% methane conversions were achieved, respectively. VAM fluctuation experiments were performed, and it was shown that a fluid bed can act as a thermal mass to reduce fluctuations in the bed temperature as the VAM concentration changes.
机译:通风甲烷(VAM)排放是造成地下煤矿逃逸性温室气体排放的重要因素。石粉循环(SDL)工艺是澳大利亚纽卡斯尔大学为减少VAM而开发的一项新技术。 SDL工艺是一种循环工艺,其中首先从石灰石(CaCO3)的煅烧中获得氧化钙(CaO)。然后,将CaO用于同时氧化VAM(空气中甲烷浓度为0.1-1%(体积))并捕获生成CaCO3的二氧化碳(CO2)。这两个循环可以在单个反应器中进行,或者该过程可以在双互连反应器中连续进行。先前已经在实验室规模上进行了SDL过程的初步实验。在这项研究中,在单个1 m(3)/ s流化床反应器中,结合中试规模SDL研究进行了进一步的实验室规模研究。研究了库存量(1-2吨碳酸钙),工作温度(565-700摄氏度)和流速(1-1.7 m(3)/ s)对甲烷转化率的影响。在600摄氏度或更高的温度下,对于所有库存量和所检查的流量,甲烷转化率均> 99.5%。在565和575摄氏度的温度下,分别实现了41%和70%的甲烷转化率。进行了VAM波动实验,结果表明,随着VAM浓度的变化,流化床可以充当热质以减少床层温度的波动。

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  • 来源
    《Energy & fuels》 |2019年第12期|12568-12577|共10页
  • 作者单位

    Univ Newcastle Prior Res Ctr Frontier Energy Technol & Utilisat Univ Dr Callaghan NSW 2308 Australia;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
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