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Pyrolysis of an Indonesian oil sand in a thermogravimetric analyser and a fixed-bed reactor

机译:热重分析仪和固定床反应器中印度尼西亚油砂的热解

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摘要

Pyrolysis experiments of Buton oil sand were first carried out in a thermogravimetric analyser (TGA) at different heating rates from 5 K min(-1) to 80 K min-1 to study the thermal decomposition characteristics and then in a fixed bed reactor (FBR) operating at temperatures varied from 673 to 873 K, to study the effect of temperature on the yields, compositions and properties of pyrolysis liquid, gas and coke. The TGA results suggest that the pyrolysis process of Buton oil sand could be divided into two distinct stages, namely, pyrolysis of bitumen at temperatures below 873 K and decomposition of the residual sand above 873 K. The residual sand was mainly composed of CaCO3 and acted as inert during the bitumen pyrolysis stage. The FBR results show that as temperature increased, the pyrolysis gas yield increased and the coke yield decreased while the pyrolysis liquid yield increased initially and then decreased slightly at above 773 K. More than 60% of bitumen contained in the oil sand was converted into pyrolysis liquid at the temperatures tested, reaching a maximum value of 76.4 wt% at 773 K. The pyrolysis liquid obtained was mainly consisted of maltenes, with the asphaltenes content being less than 3.4 wt%. As the temperature increased from 673 to 873 K, the pyrolysis liquids became lighter with average molecular weight decreasing from 500 Da to 434 Da and the amounts of light oil fractions (with boiling points lower than 811 K) increasing from 70 wt% to 75 wt%. The pyrolysis gas mainly consisted of H-2, CH4, C2H6, C3H8 and C2H4, with H-2 accounting for ca. 50 vol% in the gas when the pyrolysis temperatures were above 773 K. (C) 2015 Elsevier B.V. All rights reserved.
机译:首先在热重分析仪(TGA)中以从5 K min(-1)到80 K min-1的不同加热速率进行Buton油砂的热解实验,以研究其热分解特性,然后在固定床反应器(FBR)中进行)在673至873 K的温度范围内运行,以研究温度对热解液,气和焦炭的收率,组成和性能的影响。 TGA结果表明,Buton油砂的热解过程可分为两个不同的阶段,即在873 K以下的温度下沥青的热解和873 K以上的残余砂的分解。残余砂主要由CaCO3组成并起作用。在沥青热解阶段为惰性。 FBR结果表明,随着温度的升高,在773 K以上,热解气产率增加,焦炭产率降低,而热解液产率先升高,然后略有降低。油砂中60%以上的沥青转化为热解。液体在测试温度下达到最大值,在773 K时达到76.4 wt%。所获得的热解液体主要由麦芽汁组成,其中沥青质含量小于3.4 wt%。随着温度从673 K升高到873 K,热解液体变得更轻,平均分子量从500 Da降低到434 Da,轻油馏分(沸点低于811 K)的量从70 wt%增加到75 wt %。热解气体主要由H-2,CH4,C2H6,C3H8和C2H4组成,其中H-2占大约2%。当热解温度高于773 K时,气体中的气体含量为50 vol%。(C)2015 Elsevier B.V.保留所有权利。

著录项

  • 来源
    《Journal of Analytical & Applied Pyrolysis》 |2016年第1期|191-198|共8页
  • 作者单位

    Univ Western Australia, Ctr Energy M473, 35 Stirling Highway, Crawley, WA 6009, Australia;

    Univ Western Australia, Ctr Energy M473, 35 Stirling Highway, Crawley, WA 6009, Australia;

    Univ Western Australia, Ctr Energy M473, 35 Stirling Highway, Crawley, WA 6009, Australia;

    Univ Western Australia, Ctr Energy M473, 35 Stirling Highway, Crawley, WA 6009, Australia;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Bitumen; Fixed-bed reactor; Oil sand; Pyrolysis; TGA;

    机译:沥青;固定床反应器;油砂;热解;TGA;
  • 入库时间 2022-08-18 03:01:48

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