Hydrogen-rich gas generation from enhanced catalytic cracking of biomass tar and related model compounds on Ni-Fe/ASA@HZSM-5 catalyst: Pathways and mechanisms

IF 5.6 1区 农林科学 Q1 AGRICULTURAL ENGINEERING
Xueqin Li , Zhiwei Wang , Peng Liu , Dongjin Wan , Shiyong Wu , Youqing Wu , Tingzhou Lei
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Abstract

This study focused on the design of complex tar model compounds (CTMC) and synthesized a highly efficient aluminum dross (ASA) combined with HZSM-5 molecular sieve co-loaded bimetallic Ni-Fe catalyst (Ni-Fe/ASA@HZSM-5), comprehensively evaluated the catalytic cracking of real tar and its model compound by adjusting the injection amount and injection state of tar, and catalyst types to obtain hydrogen-rich gas with high H2 and low CO2 content. The results showed under the conditions of the injection amount of 0.6 mL/min, pyrolysis temperature of 600 °C, reforming temperature of 800 °C in the liquid phase, Ni-Fe/ASA@HZSM-5 displays excellent catalytic cracking performance with CTMC conversion efficiency of 87.80 % (79.46 % of gas yield and 34.20 vol% of H2 yield). The possible cracking paths between different components of CTMC in the Ni-Fe catalytic system were summarized by the experimental data and product distribution, the catalytic mechanism of Ni–Fe based catalysts can be attributed to the formation of a Ni-Fe alloy and the synergistic effect of ASA and HZSM-5 co-carrier. Further, the catalytic cracking pathway of CTMC was enhanced in the gas phase, the higher CTMC conversion efficiency of 93.68 %, gas yield (a mass fraction of 82.51 %) and H2 (a volume fraction of 33.59 %) were obtained from catalytic cracking of CTMC, the liquid yield decreased by 12.39 %, significantly improved the cracking degree and gas production capacity of CTMC. The real tar showed the same catalytic pyrolysis path and product distribution. Under the same cracking conditions, the yields of gas, liquid and char were 84.85 %, 12.00 % and 3.15 % respectively, and obtained the hydrogen yield of 55.29 mL/g. The CTMC simplifies the cracking process and reduces polymerization, provides insights into the cracking mechanisms of heavy components in biomass tar. Furthermore, the synergy of Ni and Fe contributed to greater activity for CTMC and real tar cracking, ASA combined with HZSM-5 molecular sieve co-loaded bimetallic Ni-Fe catalysts have a promising application potential as highly efficient catalysts for tar removal and reutilization.
在 Ni-Fe/ASA@HZSM-5 催化剂上强化催化裂化生物质焦油和相关模型化合物产生富氢气体:途径和机制
本研究以复杂焦油模型化合物(CTMC)的设计为重点,合成了高效铝渣(ASA)与HZSM-5分子筛共负载双金属Ni-Fe催化剂(Ni-Fe/ASA@HZSM-5),通过调整焦油的喷射量、喷射状态和催化剂类型,综合评价了实际焦油及其模型化合物的催化裂解效果,以获得高H2、低CO2含量的富氢气体。结果表明,在注入量为 0.6 mL/min、热解温度为 600 ℃、液相重整温度为 800 ℃的条件下,Ni-Fe/ASA@HZSM-5 表现出优异的催化裂解性能,CTMC 转化效率为 87.80 %(气体产率为 79.46 %,H2 产率为 34.20 vol%)。通过实验数据和产物分布总结了 CTMC 不同组分在 Ni-Fe 催化体系中的可能裂解途径,Ni-Fe 基催化剂的催化机理可归结为 Ni-Fe 合金的形成以及 ASA 和 HZSM-5 共载体的协同效应。此外,CTMC 在气相中的催化裂解途径得到了增强,CTMC 的催化裂解获得了较高的 CTMC 转化效率(93.68%)、气体产率(质量分数为 82.51%)和 H2(体积分数为 33.59%),液体产率降低了 12.39%,显著提高了 CTMC 的裂解度和产气能力。实际焦油的催化热解路径和产物分布相同。在相同的裂解条件下,气体、液体和焦炭的产率分别为 84.85 %、12.00 % 和 3.15 %,氢气产率为 55.29 mL/g。CTMC 简化了裂解过程,减少了聚合,为生物质焦油中重组分的裂解机理提供了启示。此外,镍和铁的协同作用提高了 CTMC 和实际焦油裂解的活性,ASA 与 HZSM-5 分子筛共负载的双金属镍铁催化剂作为焦油脱除和再利用的高效催化剂具有广阔的应用前景。
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来源期刊
Industrial Crops and Products
Industrial Crops and Products 农林科学-农业工程
CiteScore
9.50
自引率
8.50%
发文量
1518
审稿时长
43 days
期刊介绍: Industrial Crops and Products is an International Journal publishing academic and industrial research on industrial (defined as non-food/non-feed) crops and products. Papers concern both crop-oriented and bio-based materials from crops-oriented research, and should be of interest to an international audience, hypothesis driven, and where comparisons are made statistics performed.
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