首页> 外文会议>International Conference on Greenhouse Gas Control Technologies; 20040905-09; Vancouver(CA) >CO_2 CAPTURE FOR PC-BOILERS USING OXY-FUELS - A TRANSITION STRATEGY
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CO_2 CAPTURE FOR PC-BOILERS USING OXY-FUELS - A TRANSITION STRATEGY

机译:使用氧燃料的PC锅炉的CO_2捕集-过渡策略

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Retrofitting pulverized coal (PC) boilers with flue gas recirculation to recover CO_2 was conceived and tested in the mid-1980's by Argonne National Laboratory as a low-cost CO_2 source for enhanced oil recovery (EOR). The fundamental concept involves replacing combustion air with oxygen diluted by recirculated CO_2 from the flue gas. This eliminates N_2-CO_2 separation, permitting more economical CO_2 recovery than competing amine systems. A CO_2/O_2 molar ratio of ~3 is necessary to preserve the heat-transfer performance and gas-path temperatures. In a site-specific study retrofitting a low-sulfur coal-fed (0.2% S) boiler, CO_2 recycle shows competitive, operating, and environmental release advantages when compared to amine scrubbing systems. Anticipated breakthroughs in O_2 production will further improve the advantages. Oxy-fuel costs at $42/tonne CO_2 compare favorably to $50/tonne CO_2 with monoethanolamine (MEA) scrubbing. Higher sulfur contents degrades solvents faster, and this puts amines at an additional disadvantage since the oxy-fuels require no solvents or solvent disposal. At present, power station derating is similar in both approaches. Both have the same internal power demand of 94 MW_(internal) for 300 MW_(gross) station. For oxy-fuels high-sulfur operation using flue gas desulfurization (FGD) should be practical, and in a related experimental study, we found that high CO_2 partial pressures from oxy-fuels have a negligible impact on SO_2-reagent use although FGD solids handling will require redesign. One of the special opportunities afforded by CO_2/O_2 recycle is that it should prove very attractive at sites considering repowering and converting to an integrated-gasification-combined-cycle (IGCC) to produce H_2 and electricity. Early efforts to construct a CO_2 pipeline and build an oxygen plant would permit companies to approach CO_2 sequestration in a phased manner, particularly if construction schedules for CO_2 pipelines need long lead-times.
机译:Argonne国家实验室在1980年代中期构思并通过烟气再循环改造粉煤锅炉以回收CO_2,并以此作为低成本CO_2来源来提高石油采收率(EOR)。基本概念涉及用烟气中再循环的CO_2稀释的氧气代替燃烧空气。这消除了N_2-CO_2的分离,与竞争的胺系统相比,可以更经济地回收CO_2。为了保持传热性能和气体路径温度,必须使CO_2 / O_2摩尔比约为3。在特定地点的研究中,对低硫煤粉(0.2%S)锅炉进行了改造,与胺洗涤系统相比,CO_2再循环显示出竞争,运行和环境释放方面的优势。 O_2生产的预期突破将进一步提高优势。含氧燃料成本为$ 42 / t二氧化碳,而单乙醇胺(MEA)洗涤的含氧燃料成本为$ 50 / t CO_2。较高的硫含量会使溶剂更快地降解,这使胺成为另一个缺点,因为含氧燃料不需要溶剂或无需溶剂处理。目前,两种方法中的电站降额都很相似。两者对于300 MW_(总)电站的内部功率需求相同,为94 MW_(内部)。对于含氧燃料,使用烟道气脱硫(FGD)的高硫操作应该是可行的,并且在相关的实验研究中,我们发现含氧燃料中的高CO_2分压对SO_2试剂的使用影响可忽略不计将需要重新设计。 CO_2 / O_2循环所提供的特殊机会之一是,在考虑重新供电并转换为整体气化联合循环(IGCC)以生产H_2和电力的场所,它应该证明非常具有吸引力。早期建设CO_2管道和建设制氧厂的努力将使公司能够分阶段进行CO_2封存,特别是在CO_2管道的建设计划需要较长交付时间的情况下。

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