首页> 外文期刊>Environmental progress & sustainable energy >The Effect of Biomass Feedstock Type and Process Parameters on Achieving the Total Carbon Conversion in the Large Scale Fluidized Bed Gasification of Biomass
【24h】

The Effect of Biomass Feedstock Type and Process Parameters on Achieving the Total Carbon Conversion in the Large Scale Fluidized Bed Gasification of Biomass

机译:生物质原料类型和工艺参数对生物质大规模流化床气化中总碳转化率的影响

获取原文
获取原文并翻译 | 示例
           

摘要

One option for the production of liquid biofuel in Finland is based on fluidized bed gasification of biomass and Fischer-Tropsch synthesis process. The total carbon conversion achieved in the gasifier, operating at temperatures below 1000℃, depends mainly on the reactivity of solid char residue. The reactivity of the char residue is affected by temperature, partial pressures of the reactants H_2O and CO_2 and product gas components (H_2 and CO), which are inhibiting the reactivity. In this reactivity, catalytic active substances, alkaline and earth-alkaline metal compounds play a significant role. Other elements like silicon can react with the metals, leading to losses in the catalytic activity. These elements are naturally occurring in the biomass, and their behavior is individually dependent on the biomass type. The carbon conversion can be improved by increasing temperature, but it should not be too high to avoid ash sintering. By increasing the pressure, the reactivity increases normally, but for biomass it sometimes has no effect or it is even reduced. It was also observed that during the process of debarking and storage ofrnbiomass, it remains in contact with water, which can reduce the amount of some alkaline and earth alkaline metals because of leaching that can further affect reactivity and ash sintering. We studied the effects of the above-mentioned factors on various barks, like spruce, pine, birch, aspen, which are the most potential biomass feedstock to be used in the large-scale gasification in Finland. The measurements were carried out in the pressurized thermobalance in the conditions relevant for the pressurized oxygen gasification. Thus, the total pressure range was up to 20 bar, and the partial pressures of the reactants and the product gas components varied respectively. The parameters measured will be used for the development of the gasifier model.
机译:芬兰生产液态生物燃料的一种选择是基于生物质的流化床气化和费托合成工艺。在低于1000℃的温度下运行的气化炉中实现的总碳转化率主要取决于固体残炭的反应性。炭残留物的反应性受温度,反应物H_2O和CO_2的分压以及抑制反应性的产物气体成分(H_2和CO)的影响。在这种反应中,催化活性物质,碱金属和碱土金属化合物起着重要作用。硅等其他元素也会与金属发生反应,从而导致催化活性下降。这些元素自然存在于生物质中,其行为分别取决于生物质的类型。碳转化率可以通过提高温度来提高,但不应过高以避免灰烬烧结。通过增加压力,反应性通常会增加,但对生物质而言,有时没有作用,甚至会降低。还观察到,在生物质的剥皮和存储过程中,它与水保持接触,这可以减少一些碱金属和碱土金属的含量,这是因为浸出会进一步影响反应性和灰分烧结。我们研究了上述因素对各种树皮的影响,例如云杉,松树,桦树,白杨树,它们是芬兰大规模气化中最有潜力的生物质原料。在加压热天平中在与加压氧气气化有关的条件下进行测量。因此,总压力范围高达20巴,并且反应物和产物气体组分的分压分别变化。测得的参数将用于气化炉模型的开发。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号