...
首页> 外文期刊>Energy & fuels >Prediction of Sulfur Content, API Gravity, and Viscosity Using a Continuous Mixture Kinetic Model for Maya Crude Oil Hydrocracking in a Slurry-Phase Reactor
【24h】

Prediction of Sulfur Content, API Gravity, and Viscosity Using a Continuous Mixture Kinetic Model for Maya Crude Oil Hydrocracking in a Slurry-Phase Reactor

机译:浆态反应器中Maya原油加氢裂化的连续混合动力学模型预测硫含量,API重力和粘度

获取原文
获取原文并翻译 | 示例
           

摘要

ABSTRACT: A continuous mixture kinetic model was applied to describe the hydrocracking reactions of Maya crude oil in a slurry-phase reactor. Besides the prediction of simulated distillation curves, complementary models were developed to predict American Petroleum Institute (API) gravity, viscosity, and total sulfur content as the reaction proceeds. Experiments were carried out in a batch-type reactor under 800 psig of hydrogen and 400 °C at several reaction times. Powder ammonium heptamotybdate (1000 ppm Mo) was added and activated in situ. Vacuum residue (VR) conversion reached 88 and 96% after 7.5 and 24 h of reaction, respectively. The formation of liquid products (bp < 538 °C) was maximum and fairly constant (65-66 wt %) for VR conversions from 37 to 88%. Feed and liquid reaction products were characterized by thermogravimetric analysis (TGA). Total sulfur, viscosity, and API gravity were also measured. The mathematical model accurately describes TGA distillation curves for VR conversions up to 88%, and the developed models for the calculation of sulfur content, viscosity, and API gravity predict with good accuracy the values of these properties.
机译:摘要:应用连续混合物动力学模型描述了玛雅原油在淤浆相反应器中的加氢裂化反应。除了预测模拟蒸馏曲线外,还开发了互补模型来预测美国石油协会(API)的重力,粘度和反应进行中的总硫含量。实验是在间歇式反应器中在800 psig的氢气和400°C的温度下进行几个反应时间进行的。加入粉末状七钼酸铵(1000 ppm Mo)并原位活化。反应7.5和24小时后,真空残留物(VR)的转化率分别达到88%和96%。液体产物的形成(bp <538°C)最大,VR转化率从37%到88%相当稳定(65-66 wt%)。进料和液体反应产物通过热重分析(TGA)进行表征。还测量了总硫,粘度和API重力。该数学模型准确地描述了高达88%的VR转化的TGA蒸馏曲线,并且用于计算硫含量,粘度和API重力的已开发模型可以很好地预测这些特性的值。

著录项

  • 来源
    《Energy & fuels》 |2011年第julaaaug期|p.3605-3614|共10页
  • 作者单位

    Unidad de Investigation en Catalisis (UN1CAT), Facultad de Quimica, Universidad Nacional Autonoma de Mexico,Mexico Distrito Federal 04510, Mexico;

    Unidad de Energfa Renovable, Centro de Investigation Cientifica de Yucatan, Calle 43 No. 130, Colonia Chuburna de Hidalgo, Merida,Yucatan, CP 97200, Mexico;

    Unidad de Investigation en Catalisis (UN1CAT), Facultad de Quimica, Universidad Nacional Autonoma de Mexico,Mexico Distrito Federal 04510, Mexico;

    Unidad de Investigation en Catalisis (UN1CAT), Facultad de Quimica, Universidad Nacional Autonoma de Mexico,Mexico Distrito Federal 04510, Mexico;

    Unidad de Investigation en Catalisis (UN1CAT), Facultad de Quimica, Universidad Nacional Autonoma de Mexico,Mexico Distrito Federal 04510, Mexico;

  • 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