首页> 外文期刊>Energy & fuels >Improving the Efficiency of the THAI-CAPRI Process by Nanocatalysts Originated from Rock Minerals
【24h】

Improving the Efficiency of the THAI-CAPRI Process by Nanocatalysts Originated from Rock Minerals

机译:源自岩石矿物的纳米催化剂提高THAI-CAPRI工艺的效率

获取原文
获取原文并翻译 | 示例
           

摘要

Toe-to-heel air injection method is a modified pattern in situ combustion which is applicable for the recovery of heavy oil reservoirs. A fixed bed of catalyst around the production well can improve performance and quality of the produced oil; however, pilot tests revealed rapid deactivation of the catalyst bed. Dispersion of fine catalyst particles (ideally nanoparticles) around the production well by carrier fluids may reduce the deactivation problem. In the first step of this study, three nanoparticles, namely calcite, montmorillonite (MMT), and Cloisite 20A, were dispersed in a heavy oil as candidate catalysts and subjected to simultaneous thermal analysis. Kinetic parameters of different reaction zones were obtained by the Coats and Redfern model, and it was observed that 0.5 wt % of the MMT more effectively catalyzed the combustion reactions. In the second step, selected sample was subjected to multiple heating rate experiments to study detailed kinetic effects. Results were analyzed by Vyazovkin isoconversional kinetic modeling, and mechanism of different steps was determined. Results showed that all reaction regions follow nucleation growth models. It was found that low-temperature oxidation (LTO) reactions follow a power law model (n = 1/3) which means an acceleratory nucleation process. Nanoclay did not change the reactions mechanism of both fuel deposition (FD) and high-temperature oxidation (HTO) regions (both followed A(0) but E-0 and Ao in the FD step were increased from 187.3 +/- 19.0 kJ/mol and 51.2 +/- 3.4 min(-1) to 235.0 +/- 21.8 kJ/mol and 59.7 +/- 3.3 min(-1), respectively. In contrast to FD, Nanoclay decreased E-0 and A(0) of HTO from 100.1 +/- 17.2 kJ/mol and 34.6 +/- 2.1 min(-1) to 81.3.0 +/- 18.5 kJ/mol and 31.0 +/- 2.3 min(-1) respectively. In other words, MMT intensified LTO and catalyzed FD step and consequently altered the residual coke. It also decreased energy barriers and changed mass loss pattern of HTO which could be caused by change of reactant (coke) and resistance of MMT nucleation sites to heat in contrast to ingested nucleation sites of residual coke. Altogether, MMT improved LTO and prevented formation of excessive fuel; at the same time, MMT catalyzed HTO step and caused more uniform temperature profile which could sustain combustion.
机译:脚趾到脚跟的空气喷射方法是一种改进的原位燃烧模式,适用于重油储层的回收。在生产井周围固定催化剂床可以提高产出油的性能和质量;但是,中试测试表明催化剂床层迅速失活。载体流体将精细的催化剂颗粒(理想的是纳米颗粒)分散在生产井周围,可以减少失活问题。在这项研究的第一步中,将方解石,蒙脱石(MMT)和Cloisite 20A这三种纳米颗粒分散在重油中作为候选催化剂,并进行了同时热分析。通过Coats和Redfern模型获得了不同反应区的动力学参数,并且观察到0.5重量%的MMT更有效地催化了燃烧反应。第二步,对选定的样品进行多次加热速率实验,以研究详细的动力学影响。通过Vyazovkin等转化动力学模型分析结果,并确定了不同步骤的机理。结果表明,所有反应区域均遵循成核生长模型。发现低温氧化(LTO)反应遵循幂律模型(n = 1/3),这意味着加速成核过程。纳米粘土没有改变燃料沉积(FD)和高温氧化(HTO)区域的反应机理(都遵循A(0),但FD步骤中的E-0和Ao从187.3 +/- 19.0 kJ / mol和51.2 +/- 3.4 min(-1)分别达到235.0 +/- 21.8 kJ / mol和59.7 +/- 3.3 min(-1)。与FD相比,Nanoclay降低了E-0和A(0) HTO的值分别从100.1 +/- 17.2 kJ / mol和34.6 +/- 2.1 min(-1)增至81.3.0 +/- 18.5 kJ / mol和31.0 +/- 2.3 min(-1)。 MMT增强了LTO并催化了FD步骤,从而改变了残留焦炭,还减少了能量壁垒并改变了HTO的质量损失模式,这可能是由于反应物(焦炭)的变化和MMT成核部位对热量的抵抗性(与摄入成核相比)引起的总而言之,MMT改善了LTO并防止了过量燃料的形成;同时,MMT催化了HTO步骤并产生了更均匀的温度曲线,可以维持燃烧。

著录项

  • 来源
    《Energy & fuels》 |2018年第11期|11772-11784|共13页
  • 作者单位

    Shahid Bahonar Univ Kerman, Dept Petr Engn, Fac Engn, Jomhouri Blvd, Kerman, Iran|Razi Univ, Petr & Chem Engn Fac, Room 139,Univ Blvd, Kermanshah 6714414971, Iran;

    Shahid Bahonar Univ Kerman, Dept Petr Engn, Fac Engn, Jomhouri Blvd, Kerman, Iran;

    Yazd Univ, Fac Engn, Dept Chem & Polymer Engn, Univ Blvd, Safayieh, Yazd, Iran;

  • 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

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号