Effects of mild acid pre-treatment on the co-pyrolysis behaviour of biosolids and wheat straw

生物固体 生物炭 稻草 热解 烧焦 废物管理 木质素 化学 制浆造纸工业 核化学 产量(工程) 材料科学 有机化学 工程类 无机化学 冶金
作者
Ibrahim Gbolahan Hakeem,Nimesha Rathnayake,Aravind Surapaneni,Kalpit Shah
出处
期刊:Chemical Engineering Research & Design [Elsevier]
卷期号:185: 375-391 被引量:4
标识
DOI:10.1016/j.psep.2024.03.022
摘要

Co-pyrolysis of biosolids (BS) and wheat straw (WS), as well as their treated variants, was performed in a fluidised bed reactor at 500 ℃. Under mild acid pre-treatment conditions (3% H2SO4 and 25 ℃), demineralisation was the dominating effect of pre-treatment on BS, while it was hemicellulose hydrolysis for WS. Consequently, the co-pyrolysis of raw biosolids (RBS) or treated biosolids (TBS) with raw wheat straw (RWS) or treated wheat straw (TWS) had varying effects on product distribution and product compositions. The co-pyrolysis of RBS+RWS gave the lowest bio-oil yield (36.3 wt%) and highest gas yield (23.1 wt%). In contrast, the highest bio-oil yield (45.8 wt%) and lowest gas yield (14.4 wt%) occurred during the co-pyrolysis of TBS+TWS. The degree of synergy in product distribution was strongest in TBS+RWS followed by RBS+RWS and was weakest in TBS+TWS, demonstrating the catalytic effect of inherent minerals on organic matter devolatilisation and char cracking reactions during co-pyrolysis. Biosolids pre-treatment alone performed competitively with BS co-pyrolysis alone with respect to enhancement in biochar properties producing biochar having 15-18 MJ/kg calorific value, 43-51 wt% carbon content, 0.7-1.0 fuel ratio, ⁓30% organic matter retention, and 27-41 wt% ash content. However, combining BS co-pyrolysis and pre-treatment gave the lowest reduction in biochar heavy metal concentration. Furthermore, bio-oil compositions were influenced by pre-treatment and/or co-pyrolysis, increasing the yield (area%) of phenols to 25.4%, furans to 24.8%, anhydrosugars to 7.8%, and aromatic hydrocarbons to 20.6%. Lastly, pre-treatment alone weakened gas production while co-pyrolysis combined with pre-treatment impacted the pyrolysis gas profile, switching between light hydrocarbons and carbon oxides (CO and CO2). Overall, co-pyrolysis and pre-treatment can each be a standalone strategy for enhancing BS pyrolysis; however, their combination produced greater synergy for generating high value products.
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