固定床反应器中木质颗粒在惰性和氧化条件下热分解行为的详细实验研究

Q3 Chemical Engineering Chemical engineering transactions Pub Date : 2021-06-15 DOI:10.3303/CET2186012
Ø. Skreiberg, M. Bugge, J. Sandquist, Fredrik Buvarp, N. Haugen
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引用次数: 1

摘要

在这项工作中,云杉木颗粒在电加热固定床反应器中进行热解。实验考察了最终热解温度(600 ~ 800℃)、升温速率(5 ~ 20 K/min)和吹扫气体组成(无、100% N2和90/10% N2/O2)的影响。反应器的仪器包括整个热分解过程中反应器内(垂直方向上3个位置)和球团床内(径向上3个位置)的瞬态温度测量。对永久气体(使用气相色谱)进行气体测量,可冷凝物被冷凝并收集,剩余的固体也被收集。因此,可以建立质量平衡。详细的实验结果对热分解建模方法的验证很有帮助。实验结果表明纤维素存在吸热分解反应和放热成炭过程。在高加热速率和吹扫气体中使用氧气时,这两个过程重叠发生。通过降低加热速率至5 K/min,可以直观地将这两个过程分开。气体分析证实了温度曲线上的分离现象。CO和CH4的产率在高温区呈明显的肩带。在温度读数上可见的吸热平台可以通过增加加热速率来减小。吹扫气体中的氧气将进一步降低高原的能见度。实验过程中形成的二氧化碳量与吹扫气体中的氧气有关,但与加热速率无关。综合的实验结果为进一步的建模工作提供了有用的知识和验证基础。
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A Detailed Experimental Study on the Thermal Decomposition Behaviour of Wood Pellets Under Inert and Oxidative Conditions in a Fixed Bed Reactor
In this work, spruce wood pellets are pyrolysed in an electrically heated fixed bed reactor. Experimental campaigns have been conducted to investigate the influence of final pyrolysis temperature (600-800°C), heating rate (5-20 K/min) and purge gas composition (none, 100% N2 and 90/10% N2/O2). The instrumentation of the reactor includes transient temperature measurements in the reactor (3 locations in the vertical direction) and inside the pellets bed (3 locations in the radial direction) throughout the thermal decomposition process. Gas measurements are carried out for permanent gases (using a GC), condensables are condensed and collected and the remaining solids are also collected. Hence, the mass balance can be established. The detailed experimental results make them useful for validation of thermal decomposition modelling approaches. The experimental results show evidence of endothermal cellulose decomposition reactions as well as the exothermal char formation process. The occurrence of these two processes overlap at high heating rates and when oxygen is used in the purge gas. The two processes can be separated visually by decreasing the heating rate to 5 K/min. The separation shown in the temperature curves is confirmed by the gas analysis. The yields of CO and CH4 show a visible shoulder in the higher temperature region. The endothermic plateau visible on the temperature readings can be reduced by increasing the heating rate. Oxygen present in the purge gas will further reduce the visibility of the plateau. The amount of CO2 formed during experiments shows dependency on the oxygen in the purge gas but appears independent of the applied heating rate. The comprehensive experimental results provide both useful knowledge and a validation basis for further modelling work.
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来源期刊
Chemical engineering transactions
Chemical engineering transactions Chemical Engineering-Chemical Engineering (all)
CiteScore
1.40
自引率
0.00%
发文量
0
审稿时长
6 weeks
期刊介绍: Chemical Engineering Transactions (CET) aims to be a leading international journal for publication of original research and review articles in chemical, process, and environmental engineering. CET begin in 2002 as a vehicle for publication of high-quality papers in chemical engineering, connected with leading international conferences. In 2014, CET opened a new era as an internationally-recognised journal. Articles containing original research results, covering any aspect from molecular phenomena through to industrial case studies and design, with a strong influence of chemical engineering methodologies and ethos are particularly welcome. We encourage state-of-the-art contributions relating to the future of industrial processing, sustainable design, as well as transdisciplinary research that goes beyond the conventional bounds of chemical engineering. Short reviews on hot topics, emerging technologies, and other areas of high interest should highlight unsolved challenges and provide clear directions for future research. The journal publishes periodically with approximately 6 volumes per year. Core topic areas: -Batch processing- Biotechnology- Circular economy and integration- Environmental engineering- Fluid flow and fluid mechanics- Green materials and processing- Heat and mass transfer- Innovation engineering- Life cycle analysis and optimisation- Modelling and simulation- Operations and supply chain management- Particle technology- Process dynamics, flexibility, and control- Process integration and design- Process intensification and optimisation- Process safety- Product development- Reaction engineering- Renewable energy- Separation processes- Smart industry, city, and agriculture- Sustainability- Systems engineering- Thermodynamic- Waste minimisation, processing and management- Water and wastewater engineering
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