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褐藻在热解过程中的转化及速率行为:操作参数的详细影响

Conversion and rate behavior of brown macroalgae in pyrolysis: Detailed effects of operating parameters.

作者信息

Amrullah Apip, Farobie Obie

机构信息

Department of Mechanical Engineering, Lambung Mangkurat University, Banjarmasin, South Kalimantan, Indonesia.

Division for Biomass and Energy, Wetland-Based Material (WBM) Research Center, Lambung Mangkurat University, Banjarmasin, South Kalimantan, Indonesia.

出版信息

Heliyon. 2023 Jul 17;9(7):e18350. doi: 10.1016/j.heliyon.2023.e18350. eCollection 2023 Jul.

DOI:10.1016/j.heliyon.2023.e18350
PMID:37519704
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC10372732/
Abstract

Non-catalytic pyrolysis of brown macroalgae (Padina sp.) was studied in a batch reactor at temperature ranges of 400-600 °C and 10-90 min reaction times on the product distribution and conversion rate behavior. The highest pyro-oil and pyro-gas yields were obtained at 600 °C, which reached 67 wt% and 27 wt%, respectively, when the reaction times were prolonged (30-90 min). In addition, the high reaction temperature resulted in more generations of heavy tar and a considerable enhancement in aromatization degree. N-aromatic groups and phenol were observed from pyro-oil at 500 °C and 600 °C, respectively. Tar yield increased with reaction temperature, reflecting an order of reaction greater than one for tar production. The rate constant of tar formation was found to be 0.0013/s at 400 °C; 0.0023/s at 500 °C; and 0.0033/s at 600 °C, respectively, with the reaction order being higher than one (1.25). These findings highlighted that the proposed model could be used to accurately predict the pyrolysis process's behavior.

摘要

在间歇式反应器中,研究了棕色大型海藻(Padina sp.)在400 - 600°C温度范围和10 - 90分钟反应时间下的非催化热解过程,考察了其对产物分布和转化率行为的影响。在600°C时获得了最高的热解油和热解气产率,当反应时间延长(30 - 90分钟)时,热解油产率达到67 wt%,热解气产率达到27 wt%。此外,较高的反应温度导致更多重质焦油生成,且芳构化程度显著提高。分别在500°C和600°C的热解油中观察到了N - 芳基基团和苯酚。焦油产率随反应温度升高而增加,这表明焦油生成反应的反应级数大于1。发现焦油生成的速率常数在400°C时为0.0013/s;在500°C时为0.0023/s;在600°C时为0.0033/s,反应级数高于1(1.25)。这些发现突出表明所提出的模型可用于准确预测热解过程的行为。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/69b8060655e7/gr7.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/cd0f7c425f23/gr1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/9799fcbe3dba/gr2.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/265c758e0396/gr3.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/512ca0d8c808/gr4.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/59f3923e27e6/gr5.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/9955d8884651/gr6.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/69b8060655e7/gr7.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/cd0f7c425f23/gr1.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/9799fcbe3dba/gr2.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/265c758e0396/gr3.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/512ca0d8c808/gr4.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/59f3923e27e6/gr5.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/9955d8884651/gr6.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/92a4/10372732/69b8060655e7/gr7.jpg

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Char and tar formation during hydrothermal gasification of dewatered sewage sludge in subcritical and supercritical water: Influence of reaction parameters and lumped reaction kinetics.在亚临界和超临界水中对脱水污水污泥进行水热气化过程中碳和焦油的形成:反应参数和集总反应动力学的影响。
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