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Catalytic Pyrolysis/Gasification of Refuse Derived Fuel for Hydrogen Production and Tar Reduction: Influence of Nickel to Citric Acid Ratio Using Ni/SiO_2 Catalysts

机译:垃圾衍生燃料的催化热解/气化制氢和减少焦油:Ni / SiO_2催化剂对镍柠檬酸比的影响

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Gasification technology is an attractive alternative for the thermal treatment of solid wastes, producing a high energy value hydrogen rich syngas. The presence of tar in the produced gas diminishes its quality and potential use in further processes; for this reason the reduction of tar in waste gasification is a major challenge. In this work the pyrolysis/gasification of refuse derived fuel (RDF) from municipal solid wastes, was investigated using a two-stage reaction system with Ni/SiO_2 catalysts prepared by a sol-gel method varying the citric acid concentration (CA). The fresh and reacted catalysts were characterised for surface area and pore size distribution, temperature programmed oxidation, and high resolution scanning electron microscopy. The effect of the nickel to citric acid ratio (Ni:CA) was evaluated in terms of the characteristics and performance of the Ni/SiO_2 catalysts. The results showed that the prepared Ni/SiO_2 catalysts exhibited a relatively high surface area and an increase in pore size distribution as the Ni:CA ratio was increased. The efficiency of the prepared catalysts on tar reduction and hydrogen production was examined during the pyrolysis/gasification of RDF; the results were compared with a blank experiment using a bed of sand. The tar fraction was quantified using gas chro-matography/mass spectrometry. A low tar concentration of ~0.2 mg_(tar)/g_(RDF) was attained using the catalysts with Ni:CA ratios of 1:1 and 1:3; additionally a high hydrogen concentration (58 vol%), and low CH_4 (2.2 vol%) and C_2-C_4 concentrations (0.8 vol%), were attained using the catalyst with a Ni:CA ratio of 1:3. A higher tar concentration of ~ 1.7 mg_(tar)/g_(RDF) was attained using the bed of sand, while the hydrogen production was remarkably decreased. The major tar compounds identified in the tar samples using the Ni/SiO_2 catalysts were phenol, cresols, naphthalene, fluorene, and phenanthrene.
机译:气化技术是用于固体废物热处理的有吸引力的替代方法,可产生高能量值的富氢合成气。产气中焦油的存在降低了焦油的质量和在后续工艺中的潜在用途;因此,减少废气气化中的焦油是一个重大挑战。在这项工作中,使用两阶段反应系统和通过改变柠檬酸浓度(CA)的溶胶-凝胶法制备的Ni / SiO_2催化剂,研究了来自城市固体废物的垃圾衍生燃料(RDF)的热解/气化。表征新鲜的和反应的催化剂的表面积和孔径分布,程序升温氧化和高分辨率扫描电子显微镜。根据Ni / SiO_2催化剂的特性和性能评估了镍与柠檬酸之比(Ni:CA)的影响。结果表明,制备的Ni / SiO_2催化剂具有较高的表面积,并且随着Ni:CA比的增加,孔径分布增加。在RDF的热解/气化过程中检查了制备的催化剂对焦油还原和产氢的效率。将结果与使用沙床的空白实验进行比较。使用气相色谱/质谱法对焦油馏分进行定量。 Ni:CA比为1:1和1:3的催化剂的焦油浓度低至约0.2 mg_(tar)/ g_(RDF)。另外,使用Ni∶CA比为1∶3的催化剂,可获得高氢浓度(58体积%),低CH_4(2.2体积%)和C_2-C_4浓度(0.8体积%)。使用砂床可获得更高的焦油浓度〜1.7 mg_(tar)/ g_(RDF),而氢气的产生显着减少。使用Ni / SiO_2催化剂在焦油样品中鉴定出的主要焦油化合物为苯酚,甲酚,萘,芴和菲。

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