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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:使用合成气的化学环燃烧 - Fe,Ni和Mn氧携带者的化学循环燃烧 - 反应性研究Co_2捕获。使用合成气

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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°C. 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°C. 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°C. 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:化学环燃烧(CLC)是一种燃烧技术,其中氧载体用于将氧气从燃烧空气转移到燃料,从而避免在空气和燃料之间直接接触。该系统由两个反应器,燃料和空气反应器组成,其中来自燃料反应器的烟气含有CO_2和H_2O,并且来自空气反应器的烟道气仅含有N_2和一些未反应的O_2。因此,CO_2和H_2O固有地与烟道气的其余部分分离,并且不会为该分离消耗主要能量。本文研究了三种有前途的氧气载体,基于金属Mn,Fe和Ni与合成气来自煤气化。实验室流化床反应器中的反应性研究在交替氧化和还原条件下,使用50%H_2和50%CO用于还原期,5%O_2用于氧化期,发现所有三种的反应性高950°C 。对于基于Mn和Ni的氧载体,每兆瓦的合成气均为46和173千克氧载体的燃料气体全转化。 Fe基载体的反应性略有较低,但煤气产量仍然高。研究了温度的效果,氧化锰显示出高反应性和温度范围内的高反应性和转化间隔在650-950℃。对于Ni和Fe基载体的转换程度随温度的函数而降低,尽管初始反应性高。在较低的温度下,形成一些氧载体的碳和甲烷。这与低气体产量有关,并且在真实系统中预计不会预期。对于比较甲烷也用作燃料。与950℃下的锰和氧化铁相比,基于镍的载体显示出更高的反应性。因此,在本文中的一种含义中的一种含义,当使用合成气作为燃料时,与Ni相比,当使用合成气时,更便宜和更环境声音Mn或Fe基颗粒可以更好地候选。另一方面,当使用具有高含量的甲烷的天然气时,基于Ni的颗粒是优选的氧载体。

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