首页> 外文会议>International Technical Conference on Coal Utilization amp; Fuel Systems vol.2; 20060521-26; Clearwater,FL(US) >CO_2-capture from coal combustion using chemical-looping combustion — Reactivity investigation of Fe, Ni and Mn based oxygen carriers using syngas
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CO_2-capture from coal combustion using chemical-looping combustion — Reactivity investigation of Fe, Ni and Mn based oxygen carriers using syngas

机译:化学循环燃烧从煤燃烧中捕获CO_2 —使用合成气对Fe,Ni和Mn基氧载体进行反应性研究

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Chemical-looping combustion (CLC) is a combustion technology where an oxygen carrier is used to transfer oxygen from the combustion air to the fuel, thus avoiding direct contact between air and fuel. The system is composed of two reactors, a fuel and an air reactor, where the flue gas from the fuel reactor contains CO_2 and H_2O and the flue gas from the air reactor contains only N_2 and some unreacted O_2. Thus, CO_2 and H_2O are inherently separated from the rest of the flue gases, and no major energy is expended for this separation. This paper investigates the use of three promising oxygen carriers based on the metals Mn, Fe and Ni together with syngas from coal gasification. Reactivity investigations in a laboratory fluidized bed reactor under alternating oxidizing and reducing conditions, using 50% H_2 and 50% CO for the reducing period, and 5% O_2 for the oxidation period, found that the reactivity of all three was high at 950℃. For the Mn and Ni based oxygen carriers, there was full conversion of the fuel gas using bed masses of 46 and 173 kg oxygen carrier per MW of syngas. The Fe based carrier had a somewhat lower reactivity, but the gas yield to CO_2 was still high. The effect of temperature was investigated, and manganese oxide showed high reactivity and conversion interval in the temperature range 650-950℃. For Ni and Fe based carriers the degree of conversion decreased as a function of temperature, although the initial reactivity was high. At lower temperatures there was formation of both carbon and methane for some of the oxygen carriers. This was associated with low degrees of gas yields, and is not expected in a real system. For comparison methane was also used as fuel. The nickel based carrier showed a much higher reactivity in comparison to manganese- and iron oxide at 950℃. Thus one implication of the results in this paper are that when using syngas as fuel, the cheaper and more environmentally sound Mn or Fe-based particles may be better candidates compared to Ni. On the other hand, when using natural gas, which has a high content of methane, Ni based particles would be the preferred oxygen carrier.
机译:化学循环燃烧(CLC)是一种燃烧技术,其中氧气载体用于将氧气从燃烧空气转移到燃料,从而避免空气与燃料直接接触。该系统由两个反应堆组成,一个燃料和一个空气反应堆,其中燃料反应堆的烟道气包含CO_2和H_2O,空气反应堆的烟道气仅包含N_2和一些未反应的O_2。因此,CO_2和H_2O固有地与其余烟气分离,并且这种分离不会消耗大量能量。本文研究了基于金属Mn,Fe和Ni的三种有前途的氧气载体与煤气化合成气的使用。在实验室流化床反应器中,在交替的氧化和还原条件下进行反应性研究,在还原阶段使用50%H_2和50%CO,在氧化阶段使用5%O_2,发现这三个反应器在950℃时都具有很高的反应性。对于基于Mn和Ni的氧气载体,使用每兆瓦合成气46和173 kg氧气载体的床质量可完全转化燃料气体。铁基载体的反应性略低,但对CO_2的产气量仍然很高。研究了温度的影响,氧化锰在650-950℃的温度范围内表现出较高的反应活性和转化间隔。对于镍和铁基载流子,尽管初始反应性很高,但其转化率却随温度而降低。在较低的温度下,一些氧气载体会同时形成碳和甲烷。这与气体产率低有关,在实际系统中是无法预期的。为了比较,甲烷也用作燃料。与950℃下的锰和铁氧化物相比,镍基载体显示出更高的反应性。因此,本文结果的一个暗示是,当使用合成气作为燃料时,与Ni相比,便宜或对环境无害的Mn或Fe基颗粒可能是更好的选择。另一方面,当使用甲烷含量高的天然气时,Ni基颗粒将是优选的氧载体。

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