固体磷酸催化调控生物质热解产物分析

    Analysis of catalytic biomass pyrolysis by a novel solid phosphoric acid

    • 摘要: 为探究固体磷酸在生物质热解中的催化作用,该研究利用等体积浸渍法制备了一种石英砂基固体磷酸催化剂(quartz sand-based solid phosphoric acid catalyst,PS)并开展了杨木催化热解试验,研究了PS及其添加比例对热解产物产率及组成的影响。结果发现PS使得热解气体产率相比原样热解降低了32.2%~41.2%,焦炭产率增加了18.8%~28.2%。催化热解气体中CO占比相比原样热解增加了27.1%~32.4%,但CH4、CO2和C2-C3占比均有不同程度降低,使得气体热值降低5.6%~16.2%。此外,PS显著提升了生物油中呋喃类化合物的选择性,在PS与杨木掺混比为1:1时,呋喃类产物相对丰度最高可达88.6%。催化热解焦炭碳保留率相比原样增加了40.6%~72.3%,分析表明PS中活性物质与生物大分子通过交联反应在焦炭表面生成了C-O-P、C-PO3和C2-PO2等化学键,抑制了焦炭侧链结构的断裂。研究结果可为固体磷酸催化剂开发及木质纤维素类生物质高值化利用提供参考。

       

      Abstract: Pyrolysis can convert the biomass into pyrolysis gas, coke, and bio-oil. With the aid of pyrolysis, the biofuels can be utilized to produce the high-value value-added chemicals. Recently, the phosphorous catalysts have been introduced into biomass pyrolysis to produce the chemicals, such as levoglucosan, furans, and high-surface-area activated carbon. However, most research has focused mostly on the directed preparation of bio-oil. It is still lacking on the effects of the solid phosphoric acid on the biomass catalytic pyrolysis. This study aims to explore the catalytic performance of solid phosphoric acid in biomass pyrolysis. A quartz sand-based solid phosphoric acid catalyst (PS) was also prepared using impregnation. A series of experiments were conducted on the catalytic pyrolysis using poplar wood. A diatomaceous earth-based solid phosphoric acid catalyst (PD) was also prepared for comparison. Firstly, the catalysts were characterized using BET, SEM, and XRD techniques. A comparison was then made on the composition and morphology of the catalysts before and after the reaction. The catalytic mechanisms were then determined during pyrolysis. Finally, the pyrolysis experiments were performed to investigate the effect of the PS catalyst and its addition ratio on the yield and composition of pyrolysis products. The results showed that the PS was reduced the yield of pyrolysis gas by 32.2% to 41.2%, compared with non-catalytic pyrolysis, while the yield of coke increased by 18.8% to 28.2%. This trend was attributed to the cross-linking reactions between the phosphoric acid and the macromolecular organic structures in the poplar wood. In terms of pyrolytic gas, the proportion of CO increased by 27.1% to 32.4%, whereas the proportions of CH4, CO2, and C2-C3 decreased, leading to a reduction of 5.6% to 16.2% in the heating value of the gas. Furthermore, the PS was has significantly enhanced the selectivity of furan compounds in the bio-oil. The relative abundance of furan compounds reached 88.6%, when the PS-to-poplar wood ratio was 1:1. Although the PD was also enhanced the selectivity of furan compounds in the bio-oil, its effect was significantly lower than that of PS. In terms of the char, the carbon retention rate increased by 40.6% to 72.3% in the catalytic pyrolysis, compared with the non-catalytic pyrolysis. The active species in the PS were formed C-O-P, C-PO3, and C2-PO2 chemical bonds on the char surface after the cross-linking reactions with the oxygen-containing functional groups of the biomass, indicating the inhibited cracking of side-chain structures. In contrast, the PD was improved only the carbon retention rate by 6.8%, indicating the a much lower retention of solid carbon, compared with the PS. The products were obtained from the solid phosphoric acid-catalyzed pyrolysis of poplar wood. It was found that the PS exhibited the a strong selectivity for the furan compounds in bio-oil, indicating the great potential to for the production of furans from biomass pyrolysis. Additionally, the PS significantly was improved the carbon retention rate in char after cross-linking reactions with oxygen-containing functional groups. Therefore, the PS shared the significant potential in the preparation of furan chemicals for the high carbon retention rate during biomass pyrolysis. These findings can provide valuable insights into the new solid phosphoric acid catalysts and the high-value utilization of lignocellulosic biomass.

       

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